[Visual Basic] Public Enum EpErrorCode [C#] public enum EpErrorCode [C++] public __value enum EpErrorCode [JScript] public enum EpErrorCode
| Member Name | Description |
|---|---|
| epErrorCode_0__OK | |
| epErrorCode_1__General_error | |
| epErrorCode_2__Net_calorific_value_calculated_value_different_from_specified | |
| epErrorCode_3__P3_LT_P1 | |
| epErrorCode_4__Surface_tension_can_be_calculated_for_water_steam_streams_only | |
| epErrorCode_5__Requested_FTYP_not_available_for_this_stream | |
| epErrorCode_6__Fuel_inlet_10_cannot_be_used_in_old_mode_Calculation_is_performed_with_FCALC_new_mode | |
| epErrorCode_7__Economiser_pressure_loss_too_high | |
| epErrorCode_8__Extraction_steam_flow_is_too_high | |
| epErrorCode_9__P2_GT_P1 | |
| epErrorCode_10__Starting_value_for_temperature_required | |
| epErrorCode_11__Starting_value_for_pressure_required | |
| epErrorCode_12__Energy_balance_defect | |
| epErrorCode_13__Isentropic_efficiency_out_of_characteristic_range | |
| epErrorCode_14__P2_LT_P1 | |
| epErrorCode_15__Inlet_status_of_compressor_is_steam | |
| epErrorCode_16__Condensate_inlet_contains_steam | |
| epErrorCode_17__Exhaust_gas_loss_GT_5 | |
| epErrorCode_18__T3_LE_T1 | |
| epErrorCode_19__T2_LE_T1_or_Q12_LT_0 | |
| epErrorCode_20__T4_LE_T1 | |
| epErrorCode_21__T4_LE_T2 | |
| epErrorCode_22__Pinch_point_violation | |
| epErrorCode_23__Heat_transfer_coefficient_k_A_out_of_characteristic_range | |
| epErrorCode_24__Heat_exchanger_iteration_not_completed | |
| epErrorCode_25__Heating_steam_flow_is_0 | |
| epErrorCode_26__Pinch_point_problem_LT_10_K | |
| epErrorCode_27__Parameter_for_characteristics_xs_out_of_range | |
| epErrorCode_28__Efficiency_GT_1 | |
| epErrorCode_29__Exergy_cannot_be_calculated_because_reference_temperature_is_below_property_table_limit | |
| epErrorCode_30__Unreasonable_value_for_FDAMP_FDAMP_0_used | |
| epErrorCode_31__Unreasonable_value_for_FL3 | |
| epErrorCode_32__Duplicate_start_value_specification_internal_value_xs_used | |
| epErrorCode_33__Outlet_enthalpy_in_we_tsteam_area_DQ_H1_H2S | |
| epErrorCode_34__Inlet_enthalpy_in_wet_steam_area_DQ_0 | |
| epErrorCode_35__Loss_of_heat_flow_is_too_high_H2_is_LT_0 | |
| epErrorCode_36__Loss_of_temperature_is_too_high_H2_is_LT_0 | |
| epErrorCode_37__GCV_could_not_be_calculated | |
| epErrorCode_38__Outlet_flow_too_high_Main_stream_set_to_xs_kg_s | |
| epErrorCode_39__Water_extraction_not_active_No_wet_steam | |
| epErrorCode_40__Mass_flow_starting_value_required | |
| epErrorCode_41__Heating_too_small_Heating_steam_flow_is_0 | |
| epErrorCode_42__Heating_steam_enthalpy_LT_enthalpy_of_circulating_condensate | |
| epErrorCode_43__Condensate_inlet_is_steam | |
| epErrorCode_44__Energy_balance_defect_GT_5 | |
| epErrorCode_45__For_this_fluid_type_reference_temperature_for_NCV_is_always_0C_and_GCV_is_set_to_NCV | |
| epErrorCode_46__Heating_value_0_no_temperature_increase | |
| epErrorCode_47__Outlet_temperature_too_high_or_NCV_too_small | |
| epErrorCode_48__Compressor_power_consumption_too_high_for_GT | |
| epErrorCode_49__Unreasonable_value_for_FTYPHX | |
| epErrorCode_50__Small_evaporation_xs_in_economiser | |
| epErrorCode_51__Evaporation_xs_in_economiser | |
| epErrorCode_52__100_steam_in_vaporisor | |
| epErrorCode_53__No_evaporation_in_vaporisor | |
| epErrorCode_54__Wet_steam_at_superheater_outlet | |
| epErrorCode_55__Condensate_at_superheater_outlet | |
| epErrorCode_56__Wet_steam_at_superheater_inlet | |
| epErrorCode_57__Condensate_at_superheater_inlet | |
| epErrorCode_58__Evaporation_at_outlet_X2_GT_0 | |
| epErrorCode_59__Steam_at_inlet_X3_GT_0 | |
| epErrorCode_60__Evaporation_at_outlet_X4_GT_0 | |
| epErrorCode_61__P3_LT_P1 | |
| epErrorCode_62__P4_LT_P1 | |
| epErrorCode_63__P5_LT_P1 | |
| epErrorCode_64__P6_LT_P1 | |
| epErrorCode_65__Electrical_efficiency_out_of_characteristic_range | |
| epErrorCode_66__Mechanical_efficiency_out_of_characteristic_range | |
| epErrorCode_67__Unreasonable_value_for_FTYP | |
| epErrorCode_68__P4_cooling_water_LT_P3_condensate | |
| epErrorCode_69__Negative_subcooling | |
| epErrorCode_70__Cooling_water_H4_GT_H3_of_condensate_M4_0 | |
| epErrorCode_71__Condensate_H3TS_DT_GT_H1_of_steam_M4_0 | |
| epErrorCode_72__Condensate_H3_GT_H1_of_steam_M4_set_to_0 | |
| epErrorCode_73__Temperature_of_condensate_outlet_LE0 | |
| epErrorCode_74__Temperature_of_condensate_outlet_GT_T1 | |
| epErrorCode_75__Outlet_condensate_too_hot_Q_LT_0 | |
| epErrorCode_76__Water_at_steam_inlet | |
| epErrorCode_77__Water_at_steam_outlet | |
| epErrorCode_78__Steam_at_water_inlet | |
| epErrorCode_79__Steam_at_water_outlet | |
| epErrorCode_80__REF1_too_small_or_empty_calculated_with_REF1_xs | |
| epErrorCode_81__REF2_too_small_or_empty_calculated_with_REF2_xs | |
| epErrorCode_82__Only_xs_of_the_original_outlet_composition_is_covered_by_equations_composition_has_been_modified_to_fit | |
| epErrorCode_83__Mass_balance_defect | |
| epErrorCode_84__Unreasonable_value_for_FL1SCV | |
| epErrorCode_85__Unreasonable_value_for_FL2 | |
| epErrorCode_86__Value_of_FL1SCV_valid_for_water_steam_lines_only | |
| epErrorCode_87__Value_of_FL1SCV_valid_for_lines_with_composition_only | |
| epErrorCode_88__Missing_start_value | |
| epErrorCode_89__Mass_fractions_of_exhaust_gas_missing | |
| epErrorCode_90__Check_mass_fractions_of_fuel | |
| epErrorCode_91__Load_LT_25_of_QN | |
| epErrorCode_92__GCV_setting_not_possible_for_this_stream_type_NCV_calculated_from_composition | |
| epErrorCode_93__NCV_setting_not_possible_for_this_stream_type_specified_value_ignored | |
| epErrorCode_94__Empty_value_for_DP12N_deprecated_use_FDP12_1_for_external_pressure_specification | |
| epErrorCode_95__Empty_value_for_DP34N_deprecated_use_FDP34_1_for_external_pressure_specification | |
| epErrorCode_96__Generator_power_out_of_characteristic_range | |
| epErrorCode_97__Energy_balance_defect_between_25_and_5 | |
| epErrorCode_98__Air_to_fuel_ratio_of_combustion_LT_12 | |
| epErrorCode_99__Primary_air_to_fuel_ratio_between_12_and_18 | |
| epErrorCode_100__Check_for_pinch_point_violation | |
| epErrorCode_101__Cold_side_evaporation_at_deheater_outlet | |
| epErrorCode_102__Wet_steam_instead_of_steam_at_deheater_inlet | |
| epErrorCode_103__Condensate_instead_of_steam_at_deheater_inlet | |
| epErrorCode_104__Wet_steam_at_hot_side_on_deheater_outlet | |
| epErrorCode_105__Condensate_at_hot_side_on_deheater_outlet | |
| epErrorCode_106__Intermediate_pressure_is_GT_than_pressure_of_outlet | |
| epErrorCode_107__Intermediate_pressure_is_LT_than_pressure_of_inlet | |
| epErrorCode_108__FTYP_not_possible_for_this_stream_type | |
| epErrorCode_109__Value_of_FTYP_valid_for_air_fluegas_lines_only | |
| epErrorCode_110__Cold_water_temperature_T4N_too_low | |
| epErrorCode_111__T4_LT_0 | |
| epErrorCode_112__Moisture_calculation_not_possible | |
| epErrorCode_113__Cooling_tower_iteration_not_completed | |
| epErrorCode_114__Temperature_limit_for_inlet_air_not_possible | |
| epErrorCode_115__DPDPNMAX_too_small_DPNMAX_1_used | |
| epErrorCode_116__Inlet_1_out_of_characteristic_range | |
| epErrorCode_117__Inlet_2_out_of_characteristic_range | |
| epErrorCode_118__Unreasonable_value_for_FTS | |
| epErrorCode_119__Carbon_gasification_out_of_characteristic_range | |
| epErrorCode_120__Methane_production_out_of_characteristic_range | |
| epErrorCode_121__H2S_production_out_of_characteristic_range | |
| epErrorCode_122__Carbon_gasification_is_GT_100 | |
| epErrorCode_123__Carbon_gasification_is_LT_0 | |
| epErrorCode_124__CH4_production_C_in_CH4_to_C_total_is_GT_100 | |
| epErrorCode_125__CH4_production_C_in_CH4_to_C_total_is_LT_0 | |
| epErrorCode_126__H2S_production_S_in_H2S_to_S_total_is_GT_100 | |
| epErrorCode_127__H2S_production_S_in_H2S_to_S_total_is_LT_0 | |
| epErrorCode_128__Portion_of_flying_ash_total_ash_is_GT_100 | |
| epErrorCode_129__Portion_of_flying_ash_total_ash_is_LT_0 | |
| epErrorCode_130__C_flying_ashes_C_flying_ashes_C_slag_GT_100 | |
| epErrorCode_131__C_flying_ashes_C_flying_ashes_C_slag_LT_0 | |
| epErrorCode_132__Internal_iteration_for_saturation_mass_flow_not_completed | |
| epErrorCode_133__Stream_1_is_already_saturated | |
| epErrorCode_134__Volume_at_outlet_too_high_cross_section_blocking | |
| epErrorCode_135__Check_mass_fractions_in_exhaust_gas_of_turbine | |
| epErrorCode_136__Parameter_out_of_range | |
| epErrorCode_137__Characteristic_field_out_of_range | |
| epErrorCode_138__Surface_tension_can_be_calculated_in_the_wet_steam_region_only | |
| epErrorCode_139__Inlet_pressure_from_characteristic_too_small_Stodola_pressure_used | |
| epErrorCode_140__Nozzlegroup_out_of_characteristic_range | |
| epErrorCode_141__Unreasonable_value_for_FSPEC12_or_FSPEC56 | |
| epErrorCode_142__Evaporation_in_ECO_12_Maybe_wrong_T_settings | |
| epErrorCode_143__Evaporation_in_ECO_56_Maybe_wrong_T_settings | |
| epErrorCode_144__Heating_water_pressure_P3_LT_P1 | |
| epErrorCode_145__Support_steam_pressure_P6_LT_P1 | |
| epErrorCode_146__Unreasonable_value_for_FL4L5 | |
| epErrorCode_147__Steam_at_condensate_inlet_negative_approach | |
| epErrorCode_148__General_error_in_P_MAP_calculation | |
| epErrorCode_149__Dimension_error_in_P_MAP_calculation | |
| epErrorCode_150__P_MAP_DLL_not_found | |
| epErrorCode_151__Connection_to_P_MAP_DLL_failed | |
| epErrorCode_152__Number_of_lines_exceeds_program_limit | |
| epErrorCode_153__P_P0_FTIT_out_of_characteristic_range | |
| epErrorCode_154__E_E0_FTIT_out_of_characteristic_range | |
| epErrorCode_155__L_L0_FTIT_out_of_characteristic_range | |
| epErrorCode_156__TA_TA0_FTIT_out_of_characteristic_range | |
| epErrorCode_157__Moisture_smaller_than_PHI_min | |
| epErrorCode_158__Moisture_greater_than_PHI_max | |
| epErrorCode_159__Load_factor_smaller_than_minimum | |
| epErrorCode_160__Load_factor_greater_than_maximum | |
| epErrorCode_161__Less_water_in_air_outlet_than_in_air_inlet | |
| epErrorCode_162__Error_162 | |
| epErrorCode_163__FDN_9_available_on_electric_streams_only | |
| epErrorCode_164__Surface_tension_could_not_be_calculated_2_phase_pressure_drop_may_be_underestimated | |
| epErrorCode_165__Too_few_O_for_requested_NOx_or_CO_concentration | |
| epErrorCode_166__Illegal_value_for_REFIN_10_used | |
| epErrorCode_167__Illegal_value_for_REFOUT_10_used | |
| epErrorCode_168__Speed_transformation_not_possible_Check_whether_either_inlet_or_outlet_speed_is_specified | |
| epErrorCode_169__T3_above_characteristic_value_CT3_CR_6_Due_to_FSPECL_value_of_CT3_CR_6_used_for_internal_calculation | |
| epErrorCode_170__T3_below_characteristic_value_CT3_CR_1_Due_to_FSPECL_value_of_CT3_CR_1_used_for_internal_calculation | |
| epErrorCode_171__T3_above_characteristic_value_CT3_CR_6 | |
| epErrorCode_172__T3_below_characeristic_CT3_CR_1 | |
| epErrorCode_173__Rel_fan_power_smaller_than_minimum | |
| epErrorCode_174__Rel_fan_power_greater_than_maximum | |
| epErrorCode_175__Wrong_fluid_at_hot_side | |
| epErrorCode_176__Construction_type_1_co_current_flow_not_possible | |
| epErrorCode_177__T4_GT_T3 | |
| epErrorCode_178__T3_LT_T2 | |
| epErrorCode_179__Affinity_laws_cannot_be_applied_characteristics_were_used_without_scaling | |
| epErrorCode_180__Speed_calculation_failed_characteristics_were_used_without_scaling | |
| epErrorCode_181__Number_of_components_exceeds_program_limit_xs | |
| epErrorCode_182__Actual_parameter_for_characteristics_xs_LT_lowest_parameter | |
| epErrorCode_183__Actual_parameter_for_characteristics_xs_GT_greatest_parameter | |
| epErrorCode_184__Actual_point_LT_first_point_of_characteristic_xs | |
| epErrorCode_185__Actual_point_GT_last_point_of_characteristic_xs | |
| epErrorCode_186__k_A_too_large_or_M1_too_small_Q12_Q34_k_A_DTM | |
| epErrorCode_187__Internal_error_no_category_for_stream_xs | |
| epErrorCode_188__Alpha12_out_of_characteristic_range | |
| epErrorCode_189__Alpha34_out_of_characteristic_range | |
| epErrorCode_190__Rad_34_out_of_characteristic_range | |
| epErrorCode_191__Lambda_out_of_characteristic_range | |
| epErrorCode_192__Cold_and_hot_side_twisted | |
| epErrorCode_193__Internal_dimension_error_for_relaxation_xs | |
| epErrorCode_194__Unknown_fluid_type_xs_for_combustion_calculation | |
| epErrorCode_195__Gasification_not_possible_lack_of_C | |
| epErrorCode_196__Gasification_not_possible_lack_of_H | |
| epErrorCode_197__Gasification_not_possible_lack_of_O | |
| epErrorCode_198__Gasification_not_possible_lack_of_O2_C_remaining | |
| epErrorCode_199__Gasification_not_possible_O2_too_high_combustion | |
| epErrorCode_250__Saturation_factor_used_instead_of_relative_humidity_because_MEASM_GT_1 | |
| epErrorCode_251__No_solution_of_the_shift_equation | |
| epErrorCode_252__Calculation_not_completed_successfully | |
| epErrorCode_253__Number_of_coefficients_exceeds_program_limit_xs | |
| epErrorCode_254__Number_of_equations_exceeds_program_limit_xs | |
| epErrorCode_255__Error_xs_in_matrix_solution | |
| epErrorCode_256__Validation_error_illegal_flag_VALID_xs | |
| epErrorCode_257__Temperature_level_wrong_Q12_0 | |
| epErrorCode_258__H2_LT_H1 | |
| epErrorCode_259__Terminal_temperature_difference_set_too_small | |
| epErrorCode_260__H3_LT_H4 | |
| epErrorCode_261__Massflow_too_high | |
| epErrorCode_262__Unreasonable_value_for_xs | |
| epErrorCode_263__Illegal_material_type_xs | |
| epErrorCode_264__Too_many_components_of_type_xs | |
| epErrorCode_265__Composition_error | |
| epErrorCode_266__Illegal_stream_type | |
| epErrorCode_267__Return_code_from_user_routine_is_xs | |
| epErrorCode_268__Characteristic_xs_missing | |
| epErrorCode_269__Illegal_component_type_xs | |
| epErrorCode_270__General_error_xs_in_adaptation_polynomial | |
| epErrorCode_271__Number_of_streams_exceeds_license_limit_xs | |
| epErrorCode_272__Table_transition_executed_at_maximum_temperature_of_injection_fluid_table | |
| epErrorCode_273__Component_requires_continuation_of_iteration | |
| epErrorCode_274__Topology_error_xs_connections | |
| epErrorCode_275__Composition_error_on_stream_2 | |
| epErrorCode_276__Composition_error_on_stream_3 | |
| epErrorCode_277__Illegal_material_for_composition_controling | |
| epErrorCode_278__Mismatch_between_source_and_target_type | |
| epErrorCode_279__Duplicate_definition_of_ambient_pressure | |
| epErrorCode_280__Air_ratio_ALAM_LT_1 | |
| epErrorCode_281__Steam_mass_flow_to_low_or_efficiency_to_high | |
| epErrorCode_282__Too_many_specification_values_xs | |
| epErrorCode_283__Fluid_on_pin_xs_must_be_water_or_steam | |
| epErrorCode_284__Fluid_on_pin_xs_must_not_be_water_or_steam | |
| epErrorCode_285__Unreasonable_composition_for_fluid_on_pin_xs | |
| epErrorCode_286__Energy_balance_error_in_ETAI_or_characteristics | |
| epErrorCode_287__Oxygen_concentration_in_1_too_low_for_electrolysis | |
| epErrorCode_288__Liquid_water_in_cathode_fluegas_Energy_balance_violated | |
| epErrorCode_289__Liquid_water_in_anode_fluegas_Energy_balance_violated | |
| epErrorCode_290__Component_not_available | |
| epErrorCode_291__Error_xs_in_adaptation_polynomial | |
| epErrorCode_292___Mode_of_calculation_not_licensed_usable_with_an_additional_module_only | |
| epErrorCode_293__Number_of_components_exceeds_license_limit_xs | |
| epErrorCode_294__Illegal_or_duplicate_index_FIND | |
| epErrorCode_295__Cycle_too_large_for_validation | |
| epErrorCode_296__H5_GT_H4 | |
| epErrorCode_297__T6_too_low_M6_was_restricted | |
| epErrorCode_298__Discrepancy_between_FIDENT_and_FADAPT | |
| epErrorCode_299__Error_in_energy_balance_please_correct_mass_flow_or_terminal_temperature_difference | |
| epErrorCode_300__Wrong_phase_at_pin_3_nothing_to_condensate | |
| epErrorCode_301__Steam_instead_of_water_at_pin_1 | |
| epErrorCode_302__Terminal_temperature_difference_LT_0_xs_K | |
| epErrorCode_303__Energy_balance_violated_xs | |
| epErrorCode_304__Component_does_not_support_different_compositions_or_different_tables_at_pin_3_and_5 | |
| epErrorCode_305__Concentration_cannot_be_set | |
| epErrorCode_306__P1_LT_P3 | |
| epErrorCode_307__P2_GT_P3 | |
| epErrorCode_308__Switched_off_due_to_large_deviation | |
| epErrorCode_309__Lambda_out_of_characteristic_range | |
| epErrorCode_310__Affinity_laws_cannot_be_applied_RRPM_or_VM1_too_small_characteristics_were_used_without_scaling | |
| epErrorCode_311__T4_LT_T1_PINPMIN | |
| epErrorCode_312__T2_GT_T3_PINPMIN | |
| epErrorCode_313__T2_GT_T4_PINPMIN | |
| epErrorCode_314__Last_point_in_characteristics_too_high | |
| epErrorCode_315__NH3_GT_NH3MAX | |
| epErrorCode_316__Internal_iteration_not_converged | |
| epErrorCode_317__Double_definition_in_concentration | |
| epErrorCode_318__Ambient_pressure_missing_1013_bar_assumed | |
| epErrorCode_319__Conflict_between_FSPECH_and_fluid_type | |
| epErrorCode_320__Volume_of_solid_and_liquid_part_xs_of_mass_fraction_is_neglected | |
| epErrorCode_321__No_NOx_reduction_because_NOx_at_inlet_is_already_smaller_than_required | |
| epErrorCode_322__NH3_content_on_stream_2_too_low | |
| epErrorCode_323__DH1LN_GT_DH2LN | |
| epErrorCode_324__DH1LN_too_large | |
| epErrorCode_325__Too_few_N_for_requested_NOx_concentration | |
| epErrorCode_326__Too_few_O_for_requested_NOx_concentration | |
| epErrorCode_327__T2_GE_T3 | |
| epErrorCode_328__T3_LE_T1 | |
| epErrorCode_329__T2_GE_T4 | |
| epErrorCode_330__T4_LE_T5 | |
| epErrorCode_331__T6_GE_T3 | |
| epErrorCode_332__T3_LE_T5 | |
| epErrorCode_333__T6_GE_T4 | |
| epErrorCode_334__Efficiency_negative | |
| epErrorCode_335__Efficiency_too_large | |
| epErrorCode_336__Component_under_construction_usage_not_yet_possible | |
| epErrorCode_337__Relative_weight_ignored | |
| epErrorCode_338__Weight_of_10_6_assumed | |
| epErrorCode_339__Pseudo_measurement_not_available_specification_value_used | |
| epErrorCode_340__Not_more_than_xs_specification_values_allowed_for_validation | |
| epErrorCode_341__Double_definition_of_index_xs_for_pseudo_measurement_point | |
| epErrorCode_342__Duplicate_definition_of_ambient_temperature | |
| epErrorCode_343__T6_GT_T5 | |
| epErrorCode_344__Longitudinal_transversal_pitch_incorrect | |
| epErrorCode_345__Depth_of_fluegas_zone_or_outer_tube_diameter_incorrect | |
| epErrorCode_346__Depth_or_height_of_fluegas_zone_incorrect | |
| epErrorCode_347__Type_of_heating_surface_incorrect | |
| epErrorCode_348__Transversal_pitch_incorrect | |
| epErrorCode_349__Geometry_of_fluegas_zone_incorrect_Probably_not_connected_to_port_3_of_component_88_90 | |
| epErrorCode_350__Type_of_outlet_orientation_incorrect | |
| epErrorCode_351__Type_of_heating_surface_incorrect | |
| epErrorCode_352__Type_of_phase_medium_incorrect | |
| epErrorCode_353__Fluegas_cross_section_incorrect | |
| epErrorCode_354__Longitudinal_transversal_pitch_or_outer_tube_diameter_incorrect | |
| epErrorCode_355__Type_of_tube_arrangement_incorrect | |
| epErrorCode_356__Fin_pitch_should_be_greater_than_fin_thickness | |
| epErrorCode_357__Outer_tube_diameter_incorrect | |
| epErrorCode_358__Fin_thickness_incorrect | |
| epErrorCode_359__Fin_pitch_too_small | |
| epErrorCode_360__Inner_tube_diameter_incorrect | |
| epErrorCode_361__Type_of_alpha_inside_calculation_incorrect | |
| epErrorCode_362__Fin_width_should_be_greater_than_DIAM_2_THWALL | |
| epErrorCode_363__Fin_type_incorrect | |
| epErrorCode_364__Outer_tube_diameter_should_be_greater_than_2_wall_thickness | |
| epErrorCode_365__Type_of_heating_surface_incorrect | |
| epErrorCode_366__Mechanical_losses_too_high | |
| epErrorCode_367__Wrong_call_to_fluid_property_table | |
| epErrorCode_368__Possibly_component_before_and_behind_confused | |
| epErrorCode_369__Component_89_without_component_88_90 | |
| epErrorCode_370__Group_identification_without_T2_prescription | |
| epErrorCode_371__Group_identification_with_more_than_one_T2_prescription | |
| epErrorCode_372__Mismatch_of_medium_types | |
| epErrorCode_373__Salt_concentration_at_outlet_too_high | |
| epErrorCode_374__There_is_no_valid_license_for_the_calculation_of_the_boiler_components_xs_in_total_included_in_the_model | |
| epErrorCode_375__Liquid_water_at_compressor_inlet | |
| epErrorCode_376__There_is_no_valid_license_for_the_calculation_of_the_desalination_components_xs_in_total_included_in_the_model | |
| epErrorCode_377__In_design_KAN_is_calculated_and_cannot_be_specified_by_pseudomeasurement_point | |
| epErrorCode_378__Terminal_temperature_difference_set_too_large | |
| epErrorCode_379__Switched_off_due_to_mass_flow_LT_xs | |
| epErrorCode_380__Switched_off_due_to_wet_steam_region | |
| epErrorCode_381__Specified_stage_pressure_too_high_no_evaporation_possible | |
| epErrorCode_382__Possibly_too_low_stage_pressure_specified | |
| epErrorCode_383__Relative_deviation_between_the_last_two_validation_steps_xs | |
| epErrorCode_384__Drain_larger_than_water_inlet_flow | |
| epErrorCode_385__Requested_outlet_composition_not_possible | |
| epErrorCode_386__Adaptation_polynomial_ignored_due_to_M3_specification | |
| epErrorCode_387__No_flap_position_in_characteristic_array_for_this_pressure_increase | |
| epErrorCode_388__Flap_position_exceeds_range_of_characteristic_array | |
| epErrorCode_389__CO2_concentration_in_1_too_low_conversion_rate_ECONCO_reduced_to_xs | |
| epErrorCode_390__Stream_3_must_be_fuel_stream_for_the_specified_type_of_fuel_cell | |
| epErrorCode_391__Sum_of_efficiences_is_not_1_normalization_performed | |
| epErrorCode_392__T2_too_high | |
| epErrorCode_393__Pressure_loss_not_possible_for_this_type_of_stream | |
| epErrorCode_394__Temperature_loss_not_possible_for_this_type_of_stream | |
| epErrorCode_395__Phase_transition_in_heat_exchanger | |
| epErrorCode_396__Pressure_increase_out_of_characteristic_range | |
| epErrorCode_397__Actual_point_GT_first_point_of_characteristic | |
| epErrorCode_398__Actual_point_LT_last_point_of_characteristic | |
| epErrorCode_399__General_error_in_characteristic_field | |
| epErrorCode_400__Duplicate_usage_of_pseudomeasurement_index_xs | |
| epErrorCode_401__Handling_of_solid_C_not_possible | |
| epErrorCode_402__Steam_supply_not_required_for_this_type_of_fuel_cell | |
| epErrorCode_403__Duplicate_definition_of_target_value | |
| epErrorCode_404__P1_GT_critical_pressure_evaporation_not_possible | |
| epErrorCode_405__HEI_method_may_be_used_only_for_water_as_cooling_fluid | |
| epErrorCode_406__Material_specification_not_used_in_validation | |
| epErrorCode_407__Unreasonable_value_for_air_humidity | |
| epErrorCode_408__Path_to_specified_Dll_xs_not_found | |
| epErrorCode_409__Too_many_xs_coefficients_for_material_equation | |
| epErrorCode_410__Heat_loss_too_large_reduced_to_50 | |
| epErrorCode_411__Requested_CH4_concentration_not_possible | |
| epErrorCode_412__Requested_ethane_concentration_not_possible | |
| epErrorCode_413__Requested_methanol_concentration_not_possible | |
| epErrorCode_414__Requested_C_concentration_not_possible | |
| epErrorCode_415__Requested_acetylene_concentration_not_possible | |
| epErrorCode_416__Requested_CO_concentration_not_possible | |
| epErrorCode_417__Error_in_inlet_concentration | |
| epErrorCode_418__Error_in_outlet_concentration | |
| epErrorCode_419__Requested_CO2_concentration_not_possible | |
| epErrorCode_420__Requested_H2_concentration_not_possible | |
| epErrorCode_421__Requested_H2O_concentration_not_possible | |
| epErrorCode_422__For_validation_of_KA_it_is_recommended_to_use_FSPECM1_given | |
| epErrorCode_423__Mass_balance_violated_xs | |
| epErrorCode_424__Energy_balance_violated_xs | |
| epErrorCode_425__No_unburnt_possible_for_this_fuel_type_ETAB_set_to_1 | |
| epErrorCode_426__Combustion_balance_violated_xs | |
| epErrorCode_427__Validation_of_concentration_not_possible_in_this_calculation_mode | |
| epErrorCode_428__Error_in_calculation_of_pressure_drop | |
| epErrorCode_429__Distribution_economizer_evaporator_superheater_not_calculated_in_this_calculation_mode | |
| epErrorCode_430__Oxygen_supplyxs_too_low_on_inlet_1 | |
| epErrorCode_431__Parameter_error_in_sorption_isothermals | |
| epErrorCode_432__Coal_humidity_value_from_sorption_isotherms_invalid_xs_value_from_CXH2OB_used | |
| epErrorCode_433__Sorption_isothermal_out_of_characteristic_range | |
| epErrorCode_434__DT23_out_of_characteristic_range | |
| epErrorCode_435__DT5S5_out_of_characteristic_range | |
| epErrorCode_436__Parameter_error_in_binding_enthalpy_characteristics | |
| epErrorCode_437__Outlet_humidity_too_high | |
| epErrorCode_438__Heat_loss_set_to_0 | |
| epErrorCode_439__Feature_not_yet_implemented_xs | |
| epErrorCode_440__NH3_production_out_of_characteristic_range | |
| epErrorCode_441__Benzene_production_out_of_characteristic_range | |
| epErrorCode_442__CH4_production_too_high | |
| epErrorCode_443__CH4_production_LT_0 | |
| epErrorCode_444__H2S_production_too_high | |
| epErrorCode_445__H2S_production_LT_0 | |
| epErrorCode_446__NH3_production_too_high | |
| epErrorCode_447__NH3_production_LT_0 | |
| epErrorCode_448__Benzene_production_too_high | |
| epErrorCode_449__Benzene_production_LT_0 | |
| epErrorCode_450__S_flying_ashes_S_flying_ashes_S_slag_GT_100 | |
| epErrorCode_451__S_flying_ashes_S_flying_ashes_S_slag_LT_0 | |
| epErrorCode_452__H2S_setting_inconsistent_with_mass_balance | |
| epErrorCode_453__NH3_setting_inconsistent_with_mass_balance | |
| epErrorCode_454__Concentration_XOUT_inconsistent_with_mass_balance | |
| epErrorCode_455__Unreasonable_value_xs | |
| epErrorCode_456__Water_extraction_is_too_high | |
| epErrorCode_457__DTN_too_low | |
| epErrorCode_458__T2_GT_Flue_gas_inlet_temperature | |
| epErrorCode_459__T1_GT_Flue_gas_outlet_temperature | |
| epErrorCode_460__T1_GT_Flue_gas_inlet_temperature | |
| epErrorCode_461__T2_GT_Flue_gas_outlet_temperature | |
| epErrorCode_462__Function_xs_missing_in_User2PhaseDLL | |
| epErrorCode_463__Elementary_balance_violated_for_C_xs | |
| epErrorCode_464__Elementary_balance_violated_for_H_xs | |
| epErrorCode_465__Elementary_balance_violated_for_O_xs | |
| epErrorCode_466__Elementary_balance_violated_for_N_xs | |
| epErrorCode_467__Elementary_balance_violated_for_S_xs | |
| epErrorCode_468__Elementary_balance_violated_for_Cl_xs | |
| epErrorCode_469__Elementary_balance_violated_for_Ar_xs | |
| epErrorCode_470__Elementary_balance_violated_for_Ash_xs | |
| epErrorCode_471__Elementary_balance_violated_for_Ca_xs | |
| epErrorCode_472__Elementary_balance_violated_for_Mg_xs | |
| epErrorCode_473__Elementary_balance_violated_for_He_xs | |
| epErrorCode_474__Elementary_balance_violated_for_Ne_xs | |
| epErrorCode_475__Elementary_balance_violated_for_Kr_xs | |
| epErrorCode_476__Elementary_balance_violated_for_Xe_xs | |
| epErrorCode_477__Elementary_balance_violated_for_unknown_element_xs | |
| epErrorCode_478__Elementary_balance_violated_for_2_phase_fluid_xs | |
| epErrorCode_479__Elementary_balance_violated_for_ELEM_3_xs | |
| epErrorCode_480__Temperature_transmission_near_phase_boundary | |
| epErrorCode_481__Unreasonable_value_for_UBSL | |
| epErrorCode_482__Unreasonable_value_for_UBFL | |
| epErrorCode_483__Unreasonable_value_for_FUBSL_or_FUBFL | |
| epErrorCode_484__Illegal_combination_of_UBFL_and_UBSL | |
| epErrorCode_485__Unreasonable_value_for_UBASH | |
| epErrorCode_486__CO2L_inconsistent_to_calculation_mode_ideal_gas_considered_as_gaseous | |
| epErrorCode_487__NH3L_inconsistent_to_calculation_mode_ideal_gas_considered_as_gaseous | |
| epErrorCode_488__P4_GT_P3 | |
| epErrorCode_489__Controller_deviates_by_xs_from_target_value | |
| epErrorCode_490__M3M2_inconsistent_with_FSPECM_FSPECM_ignored | |
| epErrorCode_491__Usage_of_T_0_for_H_specification_antiquated | |
| epErrorCode_492__Specification_of_relative_humidity_is_overwritten | |
| epErrorCode_493__Efficiency_too_small_changed_to_00001 | |
| epErrorCode_494__Efficiency_too_high_changed_to_100 | |
| epErrorCode_495__Duplicate_definition_of_composition | |
| epErrorCode_496__Fluid_not_defined | |
| epErrorCode_497__Missing_concentration | |
| epErrorCode_498__Steam_mass_flow_too_small | |
| epErrorCode_499__Requested_substance_for_controlling_not_available | |
| epErrorCode_500__Requested_value_is_equal_to_concentration_in_mixing_stream | |
| epErrorCode_501__Requested_concentration_value_outside_of_possible_range | |
| epErrorCode_502__Lower_heating_value_too_low | |
| epErrorCode_503__Temperature_at_outlet_xs_higher_than_maximum | |
| epErrorCode_504__Temperature_at_outlet_xs_higher_than_saturation | |
| epErrorCode_505__Fluegas_temperature_lower_than_minimum | |
| epErrorCode_506__Fluegas_temperature_higher_then_maximum | |
| epErrorCode_507__HEI_value_for_KA_not_used_if_FADAPT_2 | |
| epErrorCode_508__Too_few_C_or_O_for_requested_CO_concentration | |
| epErrorCode_509__ETABN_too_high_according_to_COCON_NCV_of_fluegas_was_reduced | |
| epErrorCode_510__Wrong_fluid_type_at_pin_xs | |
| epErrorCode_511__Wrong_value_for_EFF | |
| epErrorCode_512__Pure_steam_outlet_possible_for_LiBr_only | |
| epErrorCode_513__Lower_limit_reached | |
| epErrorCode_514__Upper_limit_reached | |
| epErrorCode_515__Unreasonable_value_for_FACT_set_to_10 | |
| epErrorCode_516__Component_does_not_support_table_change | |
| epErrorCode_517__Water_outlet_temperature_limited_by_wet_bulb_temperature_of_the_air | |
| epErrorCode_518__Dew_point_temperature_could_not_be_calculated | |
| epErrorCode_519__Temperature_setting_failed_T_xs_C_used_instead | |
| epErrorCode_520__Identification_mode_not_possible_because_of_FFU_eq_off | |
| epErrorCode_521__Unable_to_load_VTU_Gasturbine_Library | |
| epErrorCode_524__Material_composition_of_outlet_fluid_could_not_be_created_correctly | |
| epErrorCode_525__Outlet_fluid_contains_substances_that_are_missing_the_library_specification | |
| epErrorCode_526__Requested_outlet_composition_not_reachable | |
| epErrorCode_527__QLOSSM_too_high_restricted_to_5 | |
| epErrorCode_528__There_is_no_valid_license_for_the_calculation_of_the_gas_turbine_OEM_GT_components_xs_in_total_included_in_the_model | |
| epErrorCode_529__Fan_power_is_0 | |
| epErrorCode_530__Error_in_calculation_of_humidity | |
| epErrorCode_531__Model_contains_streams_of_type_universal_fluid_binary_mixture_thermoliquid_saltwater_or_humid_air_Calculation_mode_integration_of_material_equations_not_possible | |
| epErrorCode_532__Fan_power_is_not_specified | |
| epErrorCode_533__Pressure_drop_too_low_considering_the_geodesic_height | |
| epErrorCode_534__Overdetermination_in_material_concentration_largest_portion_is_determined_by_normalization | |
| epErrorCode_535__Condenser_pressure_was_limited_by_P3MIN | |
| epErrorCode_536__Air_ratio_would_be_LT_1_for_complete_combustion | |
| epErrorCode_537__Calculation_of_H2S_not_unique | |
| epErrorCode_538__HEI_method_may_be_used_for_water_steam_only | |
| epErrorCode_539__Usage_of_FTYP_pressure_from_saturation_temperature_may_be_not_suitable_here | |
| epErrorCode_540__P6_LT_P2 | |
| epErrorCode_541__P7_LT_P4 | |
| epErrorCode_542__Index_for_solar_data_not_found_xs_assumed | |
| epErrorCode_543__LEVMAX_LT_LEVMIN_storage_switched_off | |
| epErrorCode_544__Illegal_value_for_RHO_calculated_value_used_instead | |
| epErrorCode_545__Calculation_of_density_failed_10_kg_m3_used_instead | |
| epErrorCode_546__Calculation_of_density_failed_specification_value_RHO_used_instead | |
| epErrorCode_547__Negative_value_for_LEVMIN_not_possible_set_to_0 | |
| epErrorCode_548__P2_total_GT_P1_total | |
| epErrorCode_549__NBRANCH_too_large_set_to_499 | |
| epErrorCode_550__M3M1_too_large_set_to_099 | |
| epErrorCode_551__M3M2_too_large_set_to_099 | |
| epErrorCode_552__Upper_storage_limit_exceeded_by_xs | |
| epErrorCode_553__Storage_falls_below_its_lower_limit_by_xs | |
| epErrorCode_554__Calculation_of_new_storage_temperature_did_not_converge | |
| epErrorCode_555__Unknown_Error | |
| epErrorCode_556__Unknown_Warning | |
| epErrorCode_557__Could_not_determine_necessary_Heatexchanger_Size_in_Hybrid_Mode | |
| epErrorCode_558__Plume_Margin_set_cannot_be_achieved_Hybrid_mode_will_be_deactivated | |
| epErrorCode_559__The_number_of_fans_half_speed_and_the_number_of_fans_switched_off_exceed_the_total_number_of_fans | |
| epErrorCode_560__The_number_of_fans_switched_off_exceed_the_total_number_of_fans | |
| epErrorCode_561__Fluegas_pressure_port_7_is_smaller_than_the_ambient_pressure | |
| epErrorCode_562__Wet_Bulb_Temperature_calculations_failed_in_WDT_Using_estimated_value | |
| epErrorCode_563__Dew_Point_calculations_failed_in_WDT_Using_estimated_value | |
| epErrorCode_564__Could_not_determine_stream_temperature_Wet_Bulb_Temperature_calculations_failed_in_WDT | |
| epErrorCode_565__Could_not_determine_stream_temperature_Dew_Point_calculations_failed_in_WDT | |
| epErrorCode_566__Heat_exchanger_effectiveness_is_limited | |
| epErrorCode_567__The_wet_zone_temperature_specification_is_limited_by_the_ambient_air_wet_bulb_temperature | |
| epErrorCode_568__The_wet_zone_temperature_specification_is_limited_by_the_triple_point_of_pure_water | |
| epErrorCode_569__The_approach_temperature_cannot_be_smaller_than_06_C | |
| epErrorCode_570__Gas_side_pressure_drop_will_be_limited_to_50_mbar | |
| epErrorCode_571__Gas_side_pressure_drop_is_very_small | |
| epErrorCode_572__Gas_side_pressure_drop_is_very_high | |
| epErrorCode_573__Stack_height_is_very_high | |
| epErrorCode_574__Stack_height_is_at_the_lower_limit | |
| epErrorCode_575__Desired_water_outlet_temperature_GT_water_inlet_temperature | |
| epErrorCode_576__Desired_water_outlet_temperature_is_limited | |
| epErrorCode_577__Desired_Merkel_number_cannot_be_LT_0_Bypassing_wet_zone | |
| epErrorCode_578__Calculated_Merkel_number_is_LT_0_Bypassing_wet_zone | |
| epErrorCode_579__Could_not_determine_minimum_water_outlet_temperature | |
| epErrorCode_580__Could_not_determine_maximum_water_to_gas_ratio | |
| epErrorCode_581__Could_not_determine_wet_zone_water_outlet_temperature | |
| epErrorCode_582__The_ODE_integrator_failed | |
| epErrorCode_583__The_ODE_integrator_failed | |
| epErrorCode_584__The_Merkel_number_is_under_the_current_conditions_on_its_upper_limit | |
| epErrorCode_585__The_air_to_water_ratio_is_on_its_lower_limit | |
| epErrorCode_586__A_call_to_wdtdll_failed | |
| epErrorCode_587__The_Water_Inlet_Temperature_Is_Below_The_Minimum_Approach_Temperature_Bypassing_the_wet_zone | |
| epErrorCode_588__Parameter_out_of_range_PWETZONE | |
| epErrorCode_589__Parameter_out_of_range_PWETZONEMe | |
| epErrorCode_590__Parameter_out_of_range_PWETZONENTU | |
| epErrorCode_591__Parameter_out_of_range_DT34N | |
| epErrorCode_592__Parameter_out_of_range_AWR | |
| epErrorCode_593__Parameter_out_of_range_PACKFACT | |
| epErrorCode_594__Parameter_out_of_range_PACKEXP | |
| epErrorCode_595__Parameter_out_of_range_PHI2 | |
| epErrorCode_596__Parameter_out_of_range_DRIFT | |
| epErrorCode_597__Parameter_out_of_range_COC | |
| epErrorCode_598__Parameter_out_of_range_NBAYS | |
| epErrorCode_599__Parameter_out_of_range_DTBAND | |
| epErrorCode_600__Parameter_out_of_range_NBAYSH | |
| epErrorCode_601__Parameter_out_of_range_NBAYSOFF | |
| epErrorCode_602__Parameter_out_of_range_DP12 | |
| epErrorCode_603__Parameter_out_of_range_MGNPLUME | |
| epErrorCode_604__Parameter_out_of_range_WATRAT | |
| epErrorCode_605__Parameter_out_of_range_AIRRAT | |
| epErrorCode_606__Parameter_out_of_range_KAIR | |
| epErrorCode_607__Parameter_out_of_range_KWAT | |
| epErrorCode_608__Parameter_out_of_range_FOUL | |
| epErrorCode_609__Parameter_out_of_range_HXFRAC | |
| epErrorCode_610__Parameter_out_of_range_PSTACK | |
| epErrorCode_611__Parameter_out_of_range_FRVMH | |
| epErrorCode_612__Parameter_out_of_range_EFFFANN | |
| epErrorCode_613__Parameter_out_of_range_EFFFANH | |
| epErrorCode_614__Parameter_out_of_range_LGEARN | |
| epErrorCode_615__Parameter_out_of_range_LGEARH | |
| epErrorCode_616__Parameter_out_of_range_EFFMOT | |
| epErrorCode_617__The_ambient_pressure_is_limited_to_06_bar_minimum | |
| epErrorCode_618__Water_inlet_pressure_LT_inlet_air_pressure | |
| epErrorCode_619__Makeup_inlet_pressure_LT_inlet_air_pressure | |
| epErrorCode_620__Makeup_Salinity_GT_100_g_kg | |
| epErrorCode_621__Cooling_water_outlet_Salinity_GT_100_g_kg_The_COC_should_be_reduced | |
| epErrorCode_622__Cooling_water_inlet_Salinity_GT_100_g_kg | |
| epErrorCode_623__Parameter_out_of_range_PACKPERF_LT_0 | |
| epErrorCode_624__Cannot_size_heat_exchanger_in_plume_formation_automode_The_inlet_temperature_distance_to_the_dew_point_is_smaller_than_the_desired_margin | |
| epErrorCode_625__Plume_Margin_without_heat_exchanger_GT_desired_Margin_Hybrid_mode_will_be_deactivated | |
| epErrorCode_626__The_wet_zone_water_outlet_temperature_would_be_LT_01_C | |
| epErrorCode_627__The_cooling_water_input_stream_is_out_of_range_P3_GE_P1_01C_LE_T3_LE_80C_M3_GT_00001_kg_s_Bypassing_calculations | |
| epErrorCode_628__The_hybrid_mode_heat_exchanger_cannot_be_calculated_due_to_missing_water_or_gas_flow | |
| epErrorCode_629__The_air_outlet_port_has_considerable_amounts_of_liquid_water_Please_review_the_drift_loss_settings_DRIFT | |
| epErrorCode_630__Cannot_evaluate_characteristic | |
| epErrorCode_631__Characteristic_etrapolated | |
| epErrorCode_632__Cannot_evaluate_kernel_expression | |
| epErrorCode_633__Settings_require_logic_port_8_to_be_connected | |
| epErrorCode_634__Parameter_out_of_range_CFWIND | |
| epErrorCode_635__Parameter_out_of_range_CWTDT | |
| epErrorCode_636__Parameter_out_of_range_FHUM | |
| epErrorCode_637__Parameter_out_of_range_circulationModeFlag | |
| epErrorCode_638__Parameter_out_of_range_fMerkel | |
| epErrorCode_639__Parameter_out_of_range_FIDENT | |
| epErrorCode_640__Parameter_out_of_range_fPackPerf | |
| epErrorCode_641__Parameter_out_of_range_fCfWind | |
| epErrorCode_642__Cannot_evaluate_characteristic_CWINDAIRFLOW_reference_lookup_is_zero | |
| epErrorCode_643__FIDENT_requires_off_design_mode_and_all_bays_set_manually_to_the_same_speed | |
| epErrorCode_644__Could_not_determine_off_design_air_flow | |
| epErrorCode_645__Temperature_LT_maximum_acid_dew_point_ACDEWMAX | |
| epErrorCode_646__FSPECFAN_2_requires_Logic_port_9_to_be_connected_and_H_set_as_T4MIN | |
| epErrorCode_647__The_fuel_pressure_is_LT_minimum_fuel_pressure_of_the_active_curveset | |
| epErrorCode_648__Parsing_Error_of_CEAIN | |
| epErrorCode_649__Initial_internal_iteration_not_converged_check_time_step | |
| epErrorCode_650__Problem_with_calculation_of_transferred_heat_probably_inconsistent_specifications | |
| epErrorCode_651__Error_in_calculation_of_incident_angle | |
| epErrorCode_652__Mixing_fluids_with_different_coefficients | |
| epErrorCode_653__Isentropic_efficiency_too_high | |
| epErrorCode_654__IBRANCH_too_small_set_to_1 | |
| epErrorCode_655__IBRANCH_too_large_set_to_NBRANCH | |
| epErrorCode_656__Cold_side_pressure_drop_was_restricted_according_to_pdropmaximum_in_the_model_options | |
| epErrorCode_657__Hot_side_pressure_drop_was_restricted_according_to_pdropmaximum_in_the_model_options | |
| epErrorCode_658__xs | |
| epErrorCode_659__No_evaporation_at_outlet_expected_for_FPROC_1 | |
| epErrorCode_660__General_error_in_calculation_of_sun_position | |
| epErrorCode_661__Error_Date_Time_out_of_range_before_111950_or_after_31122050_in_calculation_of_sun_position | |
| epErrorCode_662__Error_latitude_LT_900_or_GT_900_in_calculation_of_sun_position | |
| epErrorCode_663__Error_longitude_LT_1800_or_GT_1800_in_calculation_of_sun_position | |
| epErrorCode_664__Error_azimuth_LT_00_or_GT_3600_in_calculation_of_sun_position | |
| epErrorCode_665__Error_tilt_LT_00_or_GT_900_in_calculation_of_sun_position | |
| epErrorCode_666__Pump_power_calculated_via_density_instead_of_entropy | |
| epErrorCode_667__Unreasonable_value_xs_for_cp_correction_factor_set_to_00001 | |
| epErrorCode_668__There_is_no_valid_license_for_the_calculation_of_the_EbsSolar_Library_components_xs_in_total_included_in_the_model | |
| epErrorCode_669__Difference_in_mass_flow_exceeds_error_limit | |
| epErrorCode_670__Difference_in_pressure_exceeds_error_limit | |
| epErrorCode_671__Difference_in_enthalpy_exceeds_error_limit | |
| epErrorCode_672__Difference_in_mass_flow_exceeds_warning_limit | |
| epErrorCode_673__Difference_in_pressure_exceeds_warning_limit | |
| epErrorCode_674__Difference_in_enthalpy_exceeds_warning_limit | |
| epErrorCode_675__Calculated_sun_height_of_xs_set_to_2 | |
| epErrorCode_676__FACT_too_small_set_to_0001 | |
| epErrorCode_677__Limitation_of_mass_flow_by_M2MAX_not_possible_for_FSPEC_mass_flow_given | |
| epErrorCode_678__Limitation_of_temperature_by_T2MAX_not_possible_for_FPROC_preheating_and_evaporation | |
| epErrorCode_679__Limitation_of_steam_quality_by_X2MAX_possible_only_for_FPROC_preheating_and_evaporation | |
| epErrorCode_680__IDP_too_small_set_to_2 | |
| epErrorCode_681__Cross_flow_not_available_countercurrent_flow_assumed | |
| epErrorCode_682__Unreasonable_value_for_FFLOW_countercurrent_flow_assumed | |
| epErrorCode_683__Pinch_point_xs_K_LT_PINPMIN | |
| epErrorCode_684__FELOSS_2_or_3_only_possible_in_combination_with_FSPHI_1_since_calculation_requires_the_sun_azimuth_angle_which_cannot_be_specified_in_collector_component | |
| epErrorCode_685__Data_from_collecting_header_not_found_check_logical_connection | |
| epErrorCode_686__xs_values_LT_PMIN_during_interpolation_of_pressure_drops_changed_to_PMIN | |
| epErrorCode_687__xs_values_LT_PMAX_during_interpolation_of_pressure_drops_changed_to_PMAX | |
| epErrorCode_688__NBRANCH_too_small_set_to_1 | |
| epErrorCode_689__IDP_too_large_set_to_NBRANCH_1 | |
| epErrorCode_690__DPSHN_GT_DP12N_set_to_DP12N | |
| epErrorCode_691__Steam_at_outlet_in_contradiction_to_FPROC_0 | |
| epErrorCode_692__Outlet_is_not_superheated_in_contradiction_to_FPROC_2 | |
| epErrorCode_693__RFOCUS_LT_0 | |
| epErrorCode_694__FSPEC_1_not_possible_for_FLIMIT_GE_3 | |
| epErrorCode_695__Wet_steam_at_inlet_not_possible_for_FPROC_GT_0 | |
| epErrorCode_696__Outlet_steam_is_superheated_in_contradiction_to_FPROC_1 | |
| epErrorCode_697__Drift_loss_fraction_too_high_reduced_to_xs | |
| epErrorCode_698__1_Phase_calculation_required_in_2_phase_flow | |
| epErrorCode_699__FDPN_FDPPL_mismatch | |
| epErrorCode_700__Concentration_cannot_be_scaled_to_reference_O2_concentration | |
| epErrorCode_701__Cross_flow_still_under_construction_Handle_with_care | |
| epErrorCode_702__Error_in_logical_connection_to_distributing_header | |
| epErrorCode_703__Heat_loss_limited_due_to_small_mass_flow | |
| epErrorCode_704__P1_too_small | |
| epErrorCode_705__P2_too_high | |
| epErrorCode_706__P3_too_small | |
| epErrorCode_707__Duplicate_solar_index_ISUN_xs | |
| epErrorCode_708__Double_definition_of_heating_value | |
| epErrorCode_709__Double_definition_of_fluid_coefficients | |
| epErrorCode_710__Illegal_value_for_MCONF | |
| epErrorCode_711__Illegal_value_for_MCONF_set_to_xs | |
| epErrorCode_712__Mismatch_of_binary_mixture_types | |
| epErrorCode_713__Mismatch_of_coal_types_coal_type_from_main_input_used | |
| epErrorCode_714__Wet_bulb_temperature_could_not_be_calculated | |
| epErrorCode_715__T4_would_be_smaller_than_T1 | |
| epErrorCode_716__T2_would_be_larger_than_T3 | |
| epErrorCode_717__Relative_zero_head_flow_too_small_set_to_xs | |
| epErrorCode_718__Zero_head_flow_too_small_set_to_xs | |
| epErrorCode_719__Value_at_RZHF_xs_in_delivery_head_characteristic_too_small_set_to_001 | |
| epErrorCode_720__Value_at_RZHF_xs_in_efficiency_characteristic_too_small_set_to_001 | |
| epErrorCode_721__Requested_outlet_pressure_too_high | |
| epErrorCode_722__Requested_flow_too_high | |
| epErrorCode_723__Flow_GT_ZHF_no_pressure_increase | |
| epErrorCode_724__Pressure_increase_too_high_flow_becomes_smaller_than_minimum | |
| epErrorCode_725__Specified_flow_smaller_than_minimum_flow | |
| epErrorCode_726__Internal_recirculation_required_for_minimum_flow_is_too_high | |
| epErrorCode_727__Check_value_for_xsfor_liquid_water_a_value_of_4000_is_recommended | |
| epErrorCode_728__Illegal_value_xs_for_PHITRAN_90_assumed | |
| epErrorCode_729__FFLOW_Cross_flow_not_implemented_for_this_calculation_mode | |
| epErrorCode_730__Infinite_coefficient_in_equation_xs | |
| epErrorCode_731__Infinite_right_hand_side_in_equation_xs | |
| epErrorCode_732__Polytropical_efficiency_not_converged_isentropic_used_instead | |
| epErrorCode_733__Value_too_small | |
| epErrorCode_734__P_too_small | |
| epErrorCode_735__M_too_small | |
| epErrorCode_736__Composition_error_in_combustion_calculation | |
| epErrorCode_737__Fluegas_temperature_out_of_characteristic_range | |
| epErrorCode_738__Error_in_pressure_calculation | |
| epErrorCode_739__Error_in_evaluation_of_Kernel_expression_xs | |
| epErrorCode_740__Negative_cooling_range | |
| epErrorCode_741__Required_air_mass_flow_too_low_restricted_to_xs_of_water_mass_flow | |
| epErrorCode_742__Required_air_mass_flow_too_high_restricted_to_xs_water_mass_flow | |
| epErrorCode_743__Heat_loss_GT_heat_input_M1_set_to_0 | |
| epErrorCode_744__Heat_loss_GT_heat_input | |
| epErrorCode_745__Total_number_of_connection_points_exceeded | |
| epErrorCode_746__Total_number_of_lines_exceeded | |
| epErrorCode_747__External_setting_of_T4_missing_H4_set_to_0 | |
| epErrorCode_748__Characteristic_field_xs_could_not_be_interpolated | |
| epErrorCode_749__Outlet_temperature_exceeds_the_limit_specified_in_the_field | |
| epErrorCode_750__weight_cannot_be_negative | |
| epErrorCode_751__Unknown_warning | |
| epErrorCode_752__Specification_value_FMODE_is_out_of_range | |
| epErrorCode_753__Specification_value_FSPEC_is_out_of_range | |
| epErrorCode_754__Specification_value_FLAB_is_out_of_range | |
| epErrorCode_755__Specification_value_NTEETH_is_out_of_range | |
| epErrorCode_756__Specification_value_CFLOW_is_out_of_range | |
| epErrorCode_757__Specification_value_DIAM_is_out_of_range | |
| epErrorCode_758__Specification_value_CLEARANCE_is_out_of_range | |
| epErrorCode_759__Specification_value_PF_is_out_of_range | |
| epErrorCode_760__Desired_flow_M1N_LT_0 | |
| epErrorCode_761__Nominal_value_CAN_LT_0 | |
| epErrorCode_762__Calculated_specific_volume_LT_0 | |
| epErrorCode_763__Division_by_0_in_GetCAN | |
| epErrorCode_764__Inlet_pressure_LT_outlet_pressure | |
| epErrorCode_765__Inlet_pressure_LT_0 | |
| epErrorCode_766__Cannot_calculate_specific_volume | |
| epErrorCode_767__Cannot_calculate_kappa | |
| epErrorCode_768__Kappa_out_of_range | |
| epErrorCode_769__Initial_internal_iteration_converged_with_deviation_see_result_value_PREC_check_time_step | |
| epErrorCode_770__Initial_internal_iteration_oscillates_check_time_step_FTSTEPS_TISTEP_and_ISUBMAX_IERRMAX | |
| epErrorCode_771__No_weight_GT_0_Sulfuric_acid_dewpoint_will_not_be_calculated | |
| epErrorCode_772__NMODSER_must_be_GE_1 | |
| epErrorCode_773__NMODPAR_must_be_GE_1 | |
| epErrorCode_774__Index_for_wind_data_not_found_xs_assumed | |
| epErrorCode_775__Fin_length_should_be_greater_than_fin_width | |
| epErrorCode_776__Fin_width_too_small | |
| epErrorCode_777__Mixing_temperature_specified_exceeds_the_highest_inlet_gas_temperature | |
| epErrorCode_778__Gearbox_loss_could_not_be_calculated_set_to_0 | |
| epErrorCode_779__For_FOP_1_calculation_is_always_performed_with_FALAM_1 | |
| epErrorCode_780__Wet_bulb_temperature_setting_not_possible_for_this_composition | |
| epErrorCode_781__Wet_bulb_temperature_setting_failed | |
| epErrorCode_782__Dynamic_viscosity_not_available_pressure_loss_set_to_0 | |
| epErrorCode_783__Unknown_index_for_xs | |
| epErrorCode_784__Design_values_outside_valid_range_of_matrix_double_lookup_not_possible | |
| epErrorCode_785__First_argument_too_low_in_characteristic_field_xs | |
| epErrorCode_786__First_argument_too_high_in_characteristic_field_xs | |
| epErrorCode_787__Second_argument_too_low_in_characteristic_field_xs | |
| epErrorCode_788__Second_argument_too_high_in_characteristic_field_xs | |
| epErrorCode_789__Both_arguments_too_low_in_characteristic_field_xs | |
| epErrorCode_790__Both_arguments_too_high_in_characteristic_field_xs | |
| epErrorCode_791__First_argument_too_low_and_second_too_high_in_characteristic_field_xs | |
| epErrorCode_792__First_argument_too_high_and_second_too_low_in_characteristic_field_xs | |
| epErrorCode_793__Cannot_evaluate_charline_CEFF_Lookup_at_nominal_conditions_gave_zero | |
| epErrorCode_794__The_input_variable_EFF_is_out_of_range_0_LE_eff_LE_1 | |
| epErrorCode_795__The_current_settings_for_ffu_require_the_logic_port_to_be_connected | |
| epErrorCode_796__Desired_draft_DP_exceeds_100_mbar | |
| epErrorCode_797__Desired_draft_DP_exceeds_50_mbar | |
| epErrorCode_798__Calculated_stack_height_exceeds_500_meters | |
| epErrorCode_799__Desired_stack_height_exceeds_500_meters | |
| epErrorCode_800__General_fluid_property_error | |
| epErrorCode_801__ALGEX2_Exponent_LE_175_save_value_used | |
| epErrorCode_802__PST_T_GT_TC_value_TC_used | |
| epErrorCode_803__PST_T_LT_TMIN_value_TMIN_used | |
| epErrorCode_804__S1_FPT_Argument_in_LOG_LE0 | |
| epErrorCode_805__TSP_P_GT_PC_value_PC_used | |
| epErrorCode_806__TSP_P_GT_PMIN_value_PMIN_used | |
| epErrorCode_807__Volume_iteration_not_completed | |
| epErrorCode_808__P_FS_not_converged_last_value_used | |
| epErrorCode_809__H_FPT_P_GT_1000_bar_P_1000_bar_used | |
| epErrorCode_810__H_FPT_P_LT_001_bar_P_001_bar_used | |
| epErrorCode_811__H_FPT_T_GT_800_C_T_800C_used | |
| epErrorCode_812__H_FPT_T_LT_0_C_T_0C_used | |
| epErrorCode_813__S_FPT_P_GT_1000_bar_P_1000_bar_used | |
| epErrorCode_814__S_FPT_P_LT_001_bar_P_001_bar_used | |
| epErrorCode_815__S_FPT_T_GT_800_C_T_800C_used | |
| epErrorCode_816__S_FPT_T_LT_0C_T_0C_used | |
| epErrorCode_817__T_FPH_P_GT_1000_bar_P_1000_bar_used | |
| epErrorCode_818__T_FPH_P_LT_001_bar_P_001_bar_used | |
| epErrorCode_819__T_FPH_H_GT_HMAX_H_HMAX_used | |
| epErrorCode_820__T_FPH_H_LT_HMIN_H_HMIN_used | |
| epErrorCode_821__Temperature_iteration_not_completed | |
| epErrorCode_822__T_FPS_P_GT_1000_bar_P_1000_bar_used | |
| epErrorCode_823__T_FPS_001_bar_P_001_bar_used | |
| epErrorCode_824__T_FPS_S_GT_SMAX_S_SMAX_used | |
| epErrorCode_825__T_FPS_S_LT_SMIN_S_SMIN_used | |
| epErrorCode_826__P_FH_not_converged_last_value_used | |
| epErrorCode_827__Unsupported_function_call_in_fluid_property_table | |
| epErrorCode_828__Internal_fluid_property_table_error | |
| epErrorCode_829__Iteration_for_T_FPS_not_completed | |
| epErrorCode_830__Iteration_for_T_FPH_not_completed | |
| epErrorCode_831__Sum_of_substances_not_equal_1 | |
| epErrorCode_832__T_LT_Tmin_in_water_steam_table | |
| epErrorCode_833__P_LT_Pmin_in_water_steam_table | |
| epErrorCode_834__Default_material_table_used | |
| epErrorCode_835__P_LT_Pmin_in_fluid_property_table_used | |
| epErrorCode_836__T_LT_Tmin_in_fluid_property_table_used | |
| epErrorCode_837__P_GT_Pmax_in_fluid_property_table_used | |
| epErrorCode_838__T_GT_Tmax_in_fluid_property_table_used | |
| epErrorCode_839__H_would_be_LT_Hmin_in_fluid_property_table_used | |
| epErrorCode_840__H_would_be_GT_Hmax_in_fluid_property_table_used | |
| epErrorCode_841__S_would_be_LT_Smin_in_fluid_property_table_used | |
| epErrorCode_842__S_would_be_GT_Smax_in_fluid_property_table_used | |
| epErrorCode_843__Function_xs_not_available_in_fluid_property_library | |
| epErrorCode_844__Error_in_real_gas_calculation_FDBR_used_instead | |
| epErrorCode_845__Error_in_2_phase_calculation_for_CO2_real_gas_used_instead | |
| epErrorCode_846__Iteration_for_table_function_not_completed | |
| epErrorCode_847__Function_available_in_wet_steam_region_only | |
| epErrorCode_848__Error_in_VDI_4670_calculation_FDBR_used_instead | |
| epErrorCode_849__Problem_in_fluid_property_table_XI_099999_assumed | |
| epErrorCode_850__General_fluid_property_table_error | |
| epErrorCode_851__Fluid_property_table_error_in_T_calculation | |
| epErrorCode_852__Fluid_property_table_error_in_X_calculation | |
| epErrorCode_853__Fluid_property_table_error_in_V_calculation | |
| epErrorCode_854__Fluid_property_table_error_in_S_calculation | |
| epErrorCode_855__Crystallization_because_XI_too_low_for_temperature | |
| epErrorCode_856__Pressure_above_critical_pressure | |
| epErrorCode_857__Specific_heat_cp_not_available_in_the_2_phase_region_interpolated_value_used_for_convergence_reasons | |
| epErrorCode_858__Function_requires_composition_equal_to_air | |
| epErrorCode_859__Function_not_available_in_this_library | |
| epErrorCode_860__Function_not_implemented | |
| epErrorCode_861__Water_content_too_high_set_to_099 | |
| epErrorCode_862__Refprop_initialization_error | |
| epErrorCode_863__Range_or_composition_error | |
| epErrorCode_864__Gas_not_in_gaseous_state | |
| epErrorCode_865__Mixture_not_possible | |
| epErrorCode_866__Fluid_property_table_error_T_GT_TC | |
| epErrorCode_867__Phase_transition_is_sublimation | |
| epErrorCode_868__H_T_relation_not_unique_probably_2_phase_state_not_supported_by_this_fluid_type_or_range_overflow | |
| epErrorCode_869__XI_LT_XImin_in_fluid_property_table_used | |
| epErrorCode_870__XI_GT_XImax_in_fluid_property_table_used | |
| epErrorCode_871__Error_xs_from_property_table_library | |
| epErrorCode_872__Missing_material_composition | |
| epErrorCode_873__Binary_interaction_parameters_not_available_for_this_mixture_ideal_solution_behavior_assumed | |
| epErrorCode_874__Error_in_setup_Refprop | |
| epErrorCode_875__Error_in_setting_references_Refprop | |
| epErrorCode_876__Iteration_for_S_SPH_not_completed | |
| epErrorCode_877__Density_is_0_kinematic_viscosity_set_to_0 | |
| epErrorCode_878__Fluid_property_table_error_in_P_calculation | |
| epErrorCode_879__Function_not_available_for_specified_composition | |
| epErrorCode_880__Density_is_0_specific_volume_cannot_be_calculated_set_to_0 | |
| epErrorCode_881__Phase_equilibrium_cannot_be_calculated | |
| epErrorCode_882__Wet_bulb_temperature_cannot_be_calculated | |
| epErrorCode_883__CP_calculated_numerically | |
| epErrorCode_884__Composition_or_heating_value_outside_validity_range_of_selected_method | |
| epErrorCode_885__Fluid_contains_substances_that_are_not_considered_in_the_NCV_calculation | |
| epErrorCode_886__NCV_is_calculated_by_FDBR_because_of_negative_reference_temperature | |
| epErrorCode_887__NCV_is_calculated_by_FDBR_because_of_error_in_transformation_to_molar_composition | |
| epErrorCode_888__NCV_calculation_method_unknown_FDBR_used_instead | |
| epErrorCode_889__ASTM_3588_is_defined_for_a_reference_temperature_of_60F_ISO_6976_used_for_temperature_correction_of_NCV_to_0C | |
| epErrorCode_890__Real_gas_correction_could_not_be_applied | |
| epErrorCode_891__Temperature_below_melting_temperature_not_supported_by_property_library | |
| epErrorCode_892__Specified_medium_not_available_in_property_library | |
| epErrorCode_893__Specified_function_not_available_in_property_library | |
| epErrorCode_894__For_given_concentration_requested_temperature_is_below_freezing_temperature_xs | |
| epErrorCode_895__ASTM_3588_calculation_of_NCV_not_possible_for_the_specified_substances | |
| epErrorCode_896__Mixture_phase_state_determination_is_only_approximate | |
| epErrorCode_897__Function_available_only_for_para_hydrogen | |
| epErrorCode_898__Water_content_too_high_for_real_gas_calculation_change_model_settings | |
| epErrorCode_899__Wet_bulb_temperature_cannot_be_calculated_because_of_composition | |
| epErrorCode_900__S_lower_than_possible_value_in_property_table | |
| epErrorCode_901__S_higher_than_possible_value_in_property_table | |
| epErrorCode_902__P_lower_than_saturation_pressure_water_is_in_gaseous_phase_for_any_concentration | |
| epErrorCode_903__H_lower_than_possible_value_in_property_table | |
| epErrorCode_904__H_higher_than_possible_value_in_property_table | |
| epErrorCode_905__Wet_bulb_temperature_cannot_be_calculated_because_there_is_already_condensed_water | |
| epErrorCode_906__Error_xs_from_REFPROP_library | |
| epErrorCode_907__Liquid_density_calculation_did_not_converge | |
| epErrorCode_908__Error_in_calculation_of_relative_humidity | |
| epErrorCode_909__One_or_more_inputs_are_out_of_range_temperature_less_than_triple_point | |
| epErrorCode_910__One_or_more_inputs_are_out_of_range_inputs_are_within_the_solid_phase | |
| epErrorCode_911__Crystallization_because_XI_too_low_for_pressure | |
| epErrorCode_912__Crystallization_because_liquid_phase_fraction_too_small | |
| epErrorCode_913__Wet_bulb_temperature_below_valid_range_of_property_function | |
| epErrorCode_914__Wet_bulb_temperature_may_not_be_higher_than_ambient_temperature | |
| epErrorCode_915__H_could_be_calculated_only_approximately_at_this_state_point | |
| epErrorCode_916__Error_xs_from_CoolProp_library | |
| epErrorCode_917__Enthalpy_in_crystallization_region | |
| epErrorCode_918__Uncertainty_in_calculation_of_relative_humidity | |
| epErrorCode_919__Required_humidity_too_high_XH2O_restricted_to_0999 | |
| epErrorCode_920__Error_in_calculation_of_water_fraction_from_humidity | |
| epErrorCode_921__Ice_fraction_was_not_considered_in_calculation_of_X | |
| epErrorCode_922__Relative_humidity_undefined_due_to_lack_of_gaseous_substances | |
| epErrorCode_923__Dew_point_temperature_undefined_due_to_lack_of_water | |
| epErrorCode_924__Adiabatic_exponent_kappa_cannot_be_calculated_in_the_wet_steam_region_value_for_vapor_used | |
| epErrorCode_925__Water_content_too_high_for_LibHuGas_FDBR_used_for_water_fraction | |
| epErrorCode_926__Dynamic_viscosity_eta_not_available_in_the_2_phase_region_interpolated_value_used_for_convergence_reasons | |
| epErrorCode_927__Entropy_in_crystallization_region | |
| epErrorCode_928__Pressure_below_triple_point_liquid_phase_no_longer_existing | |
| epErrorCode_929__Kinematic_viscosity_nue_not_available_in_the_2_phase_region_interpolated_value_used_for_convergence_reasons | |
| epErrorCode_930__Heat_conductivity_lambda_not_available_in_the_2_phase_region_interpolated_value_used_for_convergence_reasons | |
| epErrorCode_931__Specific_heat_cv_not_available_in_the_2_phase_region_interpolated_value_used_for_convergence_reasons | |
| epErrorCode_932__On_this_stream_type_GCV_can_be_calculated_for_Tref_0C_only | |
| epErrorCode_933__Viscosity_calculation_not_possible_in_solid_state_and_for_gases_not_included_in_LibIdGasMix | |
| epErrorCode_934__Viscosity_calculation_failed | |
| epErrorCode_935__Viscosity_calculation_not_possible_for_T_LT_200_K | |
| epErrorCode_936__Heat_conductivity_calculation_not_possible_for_T_LT_200_K | |
| epErrorCode_937__Heat_conductivity_failed | |
| epErrorCode_938__Heat_conductivity_not_possible_in_solid_state_fraction_and_for_gases_not_included_in_LibIdGasMix | |
| epErrorCode_939__Solid_state_fractions_and_gases_not_included_in_LibIdGasMix_neglected_in_viscosity_calculation | |
| epErrorCode_940__Solid_state_fractions_and_gases_not_included_in_LibIdGasMix_neglected_in_heat_conductivity_calculation | |
| epErrorCode_941__Viscosity_cannot_be_calculated_in_the_2_phase_region | |
| epErrorCode_942__Dew_point_beyond_validity_range_of_property_table | |
| epErrorCode_943__No_sublimation_above_triple_point | |
| epErrorCode_944__Calculation_of_HPX_failed | |
| epErrorCode_945__X_outside_of_valid_range | |
| epErrorCode_946__NCV_calculation_not_possible_for_this_fluid | |
| epErrorCode_947__LibCO2_used_for_entropy_calculation_of_liquid_CO2 | |
| epErrorCode_948__Molar_mass_cannot_be_calculated | |
| epErrorCode_949__Error_xs_from_TREND_library | |
| epErrorCode_950__Property_call_failed_because_T_cannot_be_calculated | |
| epErrorCode_951__HPT_call_failed_H_calculated_iteratively | |
| epErrorCode_952__TPH_call_failed_T_calculated_iteratively | |
| epErrorCode_953__For_boiling_dewing_state_of_universal_fluid_the_largest_fraction_only_is_considered | |
| epErrorCode_954__Temperature_above_critical_temperature | |
| epErrorCode_955__HPS_call_failed_H_calculated_iteratively | |
| epErrorCode_956__Water_content_too_high_for_this_library | |
| epErrorCode_957__For_given_concentration_requested_temperature_is_above_boiling_temperature_xs | |
| epErrorCode_958__Dew_point_in_crystallization_region | |
| epErrorCode_959__T_could_be_calculated_only_approximately_at_this_state_point | |
| epErrorCode_960__S_could_be_calculated_only_approximately_at_this_state_point | |
| epErrorCode_961__V_could_be_calculated_only_approximately_at_this_state_point | |
| epErrorCode_962__X_could_be_calculated_only_approximately_at_this_state_point | |
| epErrorCode_963__Unknown_type_of_polynomial_based_fluid | |
| epErrorCode_964__Salt_concentration_too_high | |
| epErrorCode_965__Kernel_expression_for_heat_transfer_coefficients_implemented_for_falg_1_only | |
| epErrorCode_966__Unreasonable_value_for_calcoptions_sim_transientmode_1_assumed | |
| epErrorCode_967__Problem_in_LibHuGas_with_H2O__H2O_calculated_using_FDBR | |
| epErrorCode_968__Problem_with_LibSeaWa2013_LibSeaWa2009_used | |
| epErrorCode_969__Problem_with_LibSeaWa2009_LibSeaWa2013_used | |
| epErrorCode_970__Pmel_gt_Pmax | |
| epErrorCode_971__Pmel_lt_Pmin | |
| epErrorCode_972__Viscosity_not_available_in_the_2_phase_region | |
| epErrorCode_973__Heat_conductivity_lambda_not_available_in_the_2_phase_region | |
| epErrorCode_974__Adiabatic_exponent_kappa_not_available_in_the_2_phase_region | |
| epErrorCode_975__Prandtl_number_Pr_not_available_in_the_2_phase_region | |
| epErrorCode_977__Speed_of_sound_w_not_available_in_the_2_phase_region | |
| epErrorCode_978__Thermal_diffusivity_a_not_available_in_the_2_phase_region | |
| epErrorCode_979__Dew_point_beyond_validity_range_of_property_table | |
| epErrorCode_980__Prandtl_number_calculation_not_possible_in_solid_state_and_for_gases_not_included_in_LibIdGasMix | |
| epErrorCode_981__Prandtl_number_calculation_failed | |
| epErrorCode_982__Prandtl_number_calculation_not_possible_for_T_LT_200_K | |
| epErrorCode_983__Solid_state_fractions_and_gases_not_included_in_LibIdGasMix_neglected_in_Prandtl_number_calculation | |
| epErrorCode_984__CV_cannot_be_calculated_due_to_solid_state_fractions | |
| epErrorCode_985__Solid_state_fractions_are_neglected_in_the_calculation_of_CV | |
| epErrorCode_986__Pressure_below_triple_point__sublimation_temperature_used | |
| epErrorCode_987__Temperature_above_triple_point__solid_phase_not_existing | |
| epErrorCode_988__Temperature_below_triple_point__sublimation_pressure_used | |
| epErrorCode_989__Below_triple_point__valid_range_is_100_le_X_le_101 | |
| epErrorCode_990__Above_triple_point__valid_range_is_10_le_X_le_11_or_0_le_X_le_1 | |
| epErrorCode_991__Effective_property_function_not_available__ordinary_function_used | |
| epErrorCode_992__Effective_enthalpy_calculation_failed | |
| epErrorCode_993__Effective_specific_heat_capacity_calculation_failed | |
| epErrorCode_994__Effective_density_calculation_failed | |
| epErrorCode_995__Effective_heat_conductivity_calculation_failed | |
| epErrorCode_996__Effective_enthalpy_difference_could_not_be_determined | |
| epErrorCode_997__Effective_temperature_calculation_failed | |
| epErrorCode_998__Prandtl_number_not_available_in_the_2_phase_region_interpolated_value_used_for_convergence_reasons | |
| epErrorCode_999__Melting_point_used_instead_of_freezing_point | |
| epErrorCode_1000__Unknown_Error | |
| epErrorCode_1001__Unknown_Warning | |
| epErrorCode_1002__The_spec_variable_FMODE_is_out_of_range | |
| epErrorCode_1003__The_spec_variable_FP1N_is_out_of_range | |
| epErrorCode_1004__The_spec_variable_P1NSET_is_too_small | |
| epErrorCode_1005__The_spec_variable_FSPEC_is_out_of_range | |
| epErrorCode_1006__The_spec_variable_FETA_is_out_of_range | |
| epErrorCode_1007__The_spec_variable_SCCTF_is_out_of_range | |
| epErrorCode_1008__The_spec_variable_FSETA_is_out_of_range | |
| epErrorCode_1009__The_spec_variable_FETAOD_is_out_of_range | |
| epErrorCode_1010__The_spec_variable_ETAN_is_out_of_range | |
| epErrorCode_1011__The_spec_variable_FMOISL_is_out_of_range | |
| epErrorCode_1012__The_spec_variable_BFMOISL_is_out_of_range | |
| epErrorCode_1013__The_spec_variable_FSECT_is_out_of_range | |
| epErrorCode_1014__The_spec_variable_NFENDS_is_too_small | |
| epErrorCode_1015__The_spec_variable_FAEXH_is_out_of_range | |
| epErrorCode_1016__The_spec_variable_AEXH_is_too_small | |
| epErrorCode_1017__The_spec_variable_VEXH_is_too_small | |
| epErrorCode_1018__The_spec_variable_FDHEXHA_is_out_of_range | |
| epErrorCode_1019__The_spec_variable_DHEXHA_is_too_small | |
| epErrorCode_1020__The_spec_variable_FDHEXTR_is_out_of_range | |
| epErrorCode_1021__The_spec_variable_DHEXTR_is_too_small | |
| epErrorCode_1022__The_spec_variable_FEFFMOISR_is_out_of_range | |
| epErrorCode_1023__The_spec_variable_EFFMOISR_is_out_of_range | |
| epErrorCode_1024__The_spec_variable_FM34_is_out_of_range | |
| epErrorCode_1025__The_spec_variable_X34_is_too_small | |
| epErrorCode_1026__The_spec_variable_T1MAX_is_out_of_range | |
| epErrorCode_1027__The_spec_variable_X2MIN_is_out_of_range | |
| epErrorCode_1028__The_spec_variable_PFFLOW_is_out_of_range | |
| epErrorCode_1029__The_spec_variable_PFETA_is_out_of_range | |
| epErrorCode_1030__The_nominal_value_H1N_is_too_small | |
| epErrorCode_1031__The_nominal_value_V1N_is_too_small | |
| epErrorCode_1032__The_nominal_value_M1N_is_too_small | |
| epErrorCode_1033__The_nominal_value_P1N_is_too_small | |
| epErrorCode_1034__The_nominal_value_P2N_is_too_small | |
| epErrorCode_1035__The_nominal_value_ETAIN_is_out_of_range | |
| epErrorCode_1036__The_nominal_value_ETAPN_is_out_of_range | |
| epErrorCode_1037__The_nominal_value_NAEXH_is_out_of_range | |
| epErrorCode_1038__The_nominal_value_P2N_must_be_less_than_P1N | |
| epErrorCode_1039__Choked_Flow_in_Exhaust_Section_Expansionline_end_pressure_is_GT_P2 | |
| epErrorCode_1040__Off_design_efficiency_GT_1 | |
| epErrorCode_1041__Off_design_efficiency_LT_0001 | |
| epErrorCode_1042__Exhaust_Loss_iterations_did_not_converge | |
| epErrorCode_1043__Moisture_removal_only_possible_in_steam_turbine | |
| epErrorCode_1044__Expansion_line_steam_flow_LT_0 | |
| epErrorCode_1045__Main_outlet_flow_LT_0 | |
| epErrorCode_1046__Cannot_mix_streams_MainIn_and_HPLeakageIn | |
| epErrorCode_1047__Cannot_mix_streams_ELEP_and_LPLeakageIn | |
| epErrorCode_1048__Cannot_evaluate_characteristic_xs | |
| epErrorCode_1049__Cannot_find_a_characteristic_xs | |
| epErrorCode_1050__Extraction_vapor_fraction_must_be_LE_expansionline_endpoint_vapor_fraction | |
| epErrorCode_1051__Extraction_vapor_fraction_must_be_GE_0005 | |
| epErrorCode_1052__Extraction_vapor_fraction_must_be_LE_used_energy_endpoint_vapor_fraction | |
| epErrorCode_1053__Insufficient_extraction_flow_for_the_calculated_moisure_removal_efficiency | |
| epErrorCode_1054__All_water_is_removed_by_moisture_removal | |
| epErrorCode_1055__All_steam_is_removed_by_moisture_removal_No_Steam_at_MainOut | |
| epErrorCode_1056__Could_not_evaluate_kernel_expression_EP1 | |
| epErrorCode_1057__Could_not_evaluate_kernel_expression_EETA | |
| epErrorCode_1058__Could_not_evaluate_kernel_expression_EDHEXHA | |
| epErrorCode_1059__Could_not_evaluate_kernel_expression_EEFFMOISR | |
| epErrorCode_1060__Could_not_evaluate_kernel_expression_EMOISL | |
| epErrorCode_1061__The_kernel_expression_EP1_gives_a_negative_value_for_P1 | |
| epErrorCode_1062__The_kernel_expression_EETA_gives_an_invalid_value_for_ETA | |
| epErrorCode_1063__The_kernel_expression_EDHEXHA_gives_a_negative_value_for_DHEXHA | |
| epErrorCode_1064__The_kernel_expression_EEFFMOISR_gives_a_negative_value_for_EFFMOISR | |
| epErrorCode_1065__The_kernel_expression_EEMOISL_gives_a_negative_value_for_EMOISL | |
| epErrorCode_1066__Characteristic_lookup_CETAM_resulted_in_an_off_design_efficiency_out_of_range | |
| epErrorCode_1067__Characteristic_lookup_CETAV_resulted_in_an_off_design_efficiency_out_of_range | |
| epErrorCode_1068__Characteristic_lookup_CETAP_resulted_in_an_off_design_efficiency_out_of_range | |
| epErrorCode_1069__Characteristic_lookup_CETATFR_resulted_in_an_off_design_efficiency_out_of_range | |
| epErrorCode_1070__The_characteristic_lookup_CDHEXH_resulted_in_a_negative_value_for_DHEXHA | |
| epErrorCode_1071__The_characteristic_lookup_CEFFMOISR_resulted_in_an_invalid_value_for_EFFMOISR | |
| epErrorCode_1072__The_characteristic_lookup_CMOISL_resulted_in_an_invalid_value_for_EMOISL | |
| epErrorCode_1073__The_spec_variable_GSPR_is_out_of_range | |
| epErrorCode_1074__The_spec_variable_GSPD_is_out_of_range | |
| epErrorCode_1075__The_spec_variable_DPMSV_is_out_of_range | |
| epErrorCode_1076__The_HP_Leakage_can_only_be_in_one_direction_active | |
| epErrorCode_1077__The_LP_Leakage_can_only_be_in_one_direction_active | |
| epErrorCode_1078__Polytropic_expansion_line_calculations_failed | |
| epErrorCode_1079__Steam_turbine_inlet_pressure_P1_is_too_low_for_the_required_mass_flow | |
| epErrorCode_1080__Governing_stage_pressure_calculations_of_throttled_section_failed | |
| epErrorCode_1081__Governing_stage_pressure_calculations_of_valves_wide_open_section_failed | |
| epErrorCode_1082__SCC_type_cannot_be_determined | |
| epErrorCode_1083__The_characteristic_CVSCAP_governing_stage_has_an_entry_LT_0 | |
| epErrorCode_1084__The_characteristic_CVSCAP_governing_stage_has_an_entry_GT_1 | |
| epErrorCode_1085__Stodola_pressure_calculations_failed | |
| epErrorCode_1086__Cannot_use_identification_mode_in_design_mode | |
| epErrorCode_1087__The_spec_variable_FIDENT_is_out_of_range | |
| epErrorCode_1088__The_spec_variable_FGS_is_out_of_range | |
| epErrorCode_1089__The_spec_variable_DPCVVWO_is_out_of_range_10e_6_LE_DPCVVWO_LE_095 | |
| epErrorCode_1090__The_spec_variable_GSPR_is_out_of_range_005_LE_GSPR_LE_10 | |
| epErrorCode_1091__The_spec_variable_DPMSV_is_out_of_range_0_LT_DPMSV_LE_095 | |
| epErrorCode_1092__The_spec_variable_NVALVES_is_out_of_range | |
| epErrorCode_1093__The_spec_variable_FPFFLOW_is_out_of_range | |
| epErrorCode_1094__The_spec_variable_FPFETA_is_out_of_range | |
| epErrorCode_1095__Main_inlet_temperature_GT_T1MAX | |
| epErrorCode_1096__Outlet_vapor_fraction_LT_X2MIN | |
| epErrorCode_1097__The_characteristic_lookup_CPFFLOW_resulted_in_a_negative_value_for_PFFLOW | |
| epErrorCode_1098__The_characteristic_lookup_CPFETA_resulted_in_a_negative_value_for_PFETA | |
| epErrorCode_1099__Calculated_Bowl_Pressure_LT_P2 | |
| epErrorCode_1100__SCC_efficiency_calculations_are_only_valid_for_steam_as_fluid | |
| epErrorCode_1101__The_spec_variable_ETAMN_is_out_of_range | |
| epErrorCode_1102__The_spec_variable_QLOSSM_is_LT_0 | |
| epErrorCode_1103__The_main_outlet_port_port_2_must_be_connected_for_FSECT_GT_0 | |
| epErrorCode_1104__A_steam_outlet_port_must_be_connected | |
| epErrorCode_1105__The_extraction_enthalpy_cannot_be_greater_than_the_inlet_enthalpy_You_need_to_check_the_respective_settings | |
| epErrorCode_1106__In_moisture_removal_mode_FSECT_4_and_extraction_flow_mode_FM34_0_at_least_one_extraction_port_3_and_4_has_to_be_connected | |
| epErrorCode_1107__Extraction_flow_too_big_for_moisture_removal_It_cannot_exceed_EFFMOISR_ELEP_flow_for_having_an_effect | |
| epErrorCode_1108__The_Settings_of_FPFFLOW_require_Logic_Port_11_to_be_connected_and_the_value_of_PFFLOW_to_be_written_to_M_of_this_stream | |
| epErrorCode_1109__The_Settings_of_FPFETA_require_Logic_Port_11_to_be_connected_and_the_value_of_PFETA_to_be_written_to_H_of_this_stream | |
| epErrorCode_1110__The_Settings_of_FIDENT_require_Logic_Port_11_to_be_connected_and_the_bowl_pressure_to_be_written_to_P_of_this_stream | |
| epErrorCode_1111__The_Settings_of_FETAN_require_Logic_Port_11_to_be_connected_and_the_value_of_PFETA_to_be_written_to_H_of_this_stream | |
| epErrorCode_1112__FETAN_and_FPFETA_require_input_from_Logic_Port_11_H_Please_change_one_of_these_to_a_different_mode | |
| epErrorCode_1113__FETAN_and_FIDENT_have_conflicting_settings_for_enthalpy | |
| epErrorCode_1114__Calculated_Efficiency_GT_1 | |
| epErrorCode_1115__Temperature_setting_failed_H_0_used_instead | |
| epErrorCode_1116__Flow_too_far_above_design_point_pressure_drop_would_be_xs_times_too_high | |
| epErrorCode_1117__Molar_mass_cannot_be_calculated_due_to_ash_fraction | |
| epErrorCode_1118__Efficiency_too_small | |
| epErrorCode_1119__Pressure_rather_high_for_ideal_gas_calculation | |
| epErrorCode_1120__Call_to_NASA_ideal_gas_library_for_temperature_setting_failed_because_of_non_gaseous_fraction | |
| epErrorCode_1121__Call_to_NASA_ideal_gas_library_for_temperature_setting_failed_usage_of_FDBR_recommended | |
| epErrorCode_1122__FTYPHX_Economizer_not_suitable_because_inlet_is_not_in_liquid_state | |
| epErrorCode_1123__For_this_fluid_type_of_cold_stream_FTYPHX_must_be_general_heat_exchanger | |
| epErrorCode_1124__For_this_fluid_type_of_stream_12_FTYPHX12_must_be_general_heat_exchanger | |
| epErrorCode_1125__For_this_fluid_type_of_stream_56_FTYPHX56_must_be_general_heat_exchanger | |
| epErrorCode_1126__For_this_FSPECD_the_distribution_on_streams_1_2_and_5_6_is_not_unique_50_split_of_hot_stream_assumed | |
| epErrorCode_1127__Composition_transmission_not_possible_between_incompatible_fluid_types | |
| epErrorCode_1128__Material_equation_not_possible_for_this_stream_type_To_use_this_measurement_point_deactivate_extension_of_system_of_equations | |
| epErrorCode_1129__Validation_of_power_factor_not_possible | |
| epErrorCode_1130__Drain_mass_flow_of_xs_kg_s_specified_although_steam_is_superheated | |
| epErrorCode_1131__Double_definition_of_phase_power_factor | |
| epErrorCode_1132__Resistance_too_high_Voltage_would_be_LT_0 | |
| epErrorCode_1133__Fuel_contains_newer_substances_that_cannot_be_used_in_old_mode_Please_use_FCALC_2 | |
| epErrorCode_1134__Mean_logarithmic_temperature_difference_for_desuperheating_zone_too_small_10_5_K_assumed | |
| epErrorCode_1135__Mean_logarithmic_temperature_difference_for_condensing_zone_too_small_10_5_K_assumed | |
| epErrorCode_1136__Ratio_desuperheating_to_condensing_heat_above_validity_range_of_Rabek_formula_result_may_be_imprecise | |
| epErrorCode_1137__Validity_range_of_Rabek_formula_exceeded_result_may_be_imprecise | |
| epErrorCode_1138__M3_M3N_in_Rabek_formula_restricted_to_upper_limit_of_3 | |
| epErrorCode_1139__M3_M3N_in_Rabek_formula_restricted_to_lower_limit_of_001 | |
| epErrorCode_1140__M1_M1N_in_Rabek_formula_restricted_to_upper_limit_of_3 | |
| epErrorCode_1141__M1_M1N_in_Rabek_formula_restricted_to_lower_limit_of_001 | |
| epErrorCode_1142__No_composition_to_transfer_found_input_line_is_not_connected_to_a_line_with_a_valid_composition | |
| epErrorCode_1143__Specified_DTN_was_matched_quite_early_during_the_iteration_could_be_a_hint_for_an_ambigious_definition | |
| epErrorCode_1144__Default_value_1_min_used_for_rotary_speed_Probably_specification_is_missing_on_the_logical_inlet | |
| epErrorCode_1145__Shaft_default_value_1_min_used_for_rotary_speed_Probably_specification_is_missing_on_the_shaft | |
| epErrorCode_1146__Missing_specification_for_substance_xs | |
| epErrorCode_1147__EFF_has_to_be_decreased_to_avoid_evaporation_in_eco_at_outlet_2 | |
| epErrorCode_1148__Missing_composition_specification_at_pin_3 | |
| epErrorCode_1149__Lower_pressure_limit_reached | |
| epErrorCode_1150__Outlet_enthalpy_exceeds_the_limit_specified_in_the_field | |
| epErrorCode_1151__Outlet_steam_content_exceeds_the_limit_specified_in_the_field | |
| epErrorCode_1152__Outlet_mass_flow_exceeds_the_limit_specified_in_the_field | |
| epErrorCode_1153__Calculation_of_RFOCUS_not_converged | |
| epErrorCode_1154__Cooling_water_mass_flow_too_small | |
| epErrorCode_1155__Error_1155 | |
| epErrorCode_1156__Inlet_for_heat_transfer_not_connected | |
| epErrorCode_1157__No_connection_to_main_heating_surface_component_89 | |
| epErrorCode_1158__Steam_content_cannot_be_set_due_to_supercritical_state_TKRIT_used_for_H_calculation | |
| epErrorCode_1159__Group_index_too_big | |
| epErrorCode_1160__Duplicate_library_specification | |
| epErrorCode_1161__Insufficient_oxygen_for_combustion | |
| epErrorCode_1162__Negative_value_xs_of_adapation_polynomial_set_to_0 | |
| epErrorCode_1163__Field_switched_off_due_to_high_wind_velocity | |
| epErrorCode_1164__Specified_FOCUS_xs_GT_1_Set_to_1 | |
| epErrorCode_1165__Fouling_too_small_xs_set_to_0 | |
| epErrorCode_1166__Eco_outlet_was_restricted_to_saturation_line | |
| epErrorCode_1167__NCV_of_NH3_inlet_not_plausible_may_yield_to_wrong_NCV_of_exhaust_gas | |
| epErrorCode_1168__Instable_time_step_width_too_large_or_boundary_condition_wrong_TSTORAGE_LT_TMIN | |
| epErrorCode_1169__NFLOW_too_large_max_value_used | |
| epErrorCode_1170__NRAD_too_large_max_value_used | |
| epErrorCode_1171__Mismatch_between_DTUBEIN_DWALL_and_DTUBEOU | |
| epErrorCode_1172__Setting_of_values_not_possible_for_this_FTYP_setting_ignored | |
| epErrorCode_1173__Instable_time_interval_too_large_or_zero | |
| epErrorCode_1174__Specification_of_composition_not_possible_here | |
| epErrorCode_1175__Double_definition_of_scaling_method | |
| epErrorCode_1176__P_LT_Psat_xs_bar_consider_evaporation | |
| epErrorCode_1177__FMODE_1_will_become_local_design_use_FDP12RN_1_for_P2_given | |
| epErrorCode_1178__VTU_Gasturbine_Library_Version_too_old_for_the_given_curve_set | |
| epErrorCode_1179__Wrong_component_type_connected_to_pin_xs | |
| epErrorCode_1180__Missing_connection_at_pin_xs | |
| epErrorCode_1181__Implementation_of_this_component_not_yet_completed_use_with_caution | |
| epErrorCode_1182__FSPEC_19_not_recommended_use_component_61_and_controller_instead | |
| epErrorCode_1183__Characteristic_CQLOSS_GT_1 | |
| epErrorCode_1184__Controller_still_inactive_would_be_started_in_iteration_step_xs_global_setting | |
| epErrorCode_1185__Controller_still_inactive_would_be_started_in_iteration_step_xs_FACT | |
| epErrorCode_1186__Heat_exchanger_is_not_an_economizer_check_FTYPHX | |
| epErrorCode_1187__Heat_exchanger_is_not_an_evaporator_check_FTYPHX | |
| epErrorCode_1188__Heat_exchanger_is_not_a_superheater_check_FTYPHX | |
| epErrorCode_1189__In_design_case_mixing_of_ranges_eco_eva_superheater_is_not_allowed | |
| epErrorCode_1190__Additional_specification_of_composition_ignored_composition_is_set_by_component_at_stream_inlet | |
| epErrorCode_1191__FSPECM_4_only_possible_for_a_well_stirred_reactor_NX_set_to_1 | |
| epErrorCode_1192__FSPECM_4_only_possible_for_fluids_with_pressure_dependent_specific_volume | |
| epErrorCode_1193__FSPECM_4_not_possible_if_MFLUID_0 | |
| epErrorCode_1194__Result_of_MXFIELDEFF_deviates_from_product_of_single_efficiencies_by_xs | |
| epErrorCode_1195__Heat_transfer_restricted_by_minimum_value_of_pinchpoint | |
| epErrorCode_1196__Internal_iteration_of_distribution_between_both_paths_not_completed_temperature_difference_xs_K | |
| epErrorCode_1197__Pin_xs_not_connected_to_a_stream_with_material_data_Q_is_used_without_conversion_to_TR_and_consideration_of_NCV | |
| epErrorCode_1198__Unreasonable_value_xs_for_COSPHI_set_to_10 | |
| epErrorCode_1199__Unreasonable_effectivity_xs_set_to_50_Increase_heating_surface_area_A | |
| epErrorCode_1200__FSPEC_7_not_possible_without_KAN_validation_FSPEC_6_used | |
| epErrorCode_1201__FSPEC_7_only_possible_for_wet_steam_FSPEC_6_used | |
| epErrorCode_1202__Validation_for_NCV_not_possible_in_mode_INTMAT_off | |
| epErrorCode_1203__FTYP_mass_fraction_recommended_for_INTMAT_GT_0_because_of_side_effects_on_other_concentration | |
| epErrorCode_1204__Switched_off_due_to_contradiction_with_NCV_0_in_simulation | |
| epErrorCode_1205__Switched_off_due_to_contradiction_with_PHI_0_in_simulation | |
| epErrorCode_1206__Validation_for_PHI_not_possible_in_mode_INTMAT_off | |
| epErrorCode_1207__Double_definition_of_moisture | |
| epErrorCode_1208__Deprecated_values_FCHR_and_FSPEC_are_used_it_is_recommended_to_use_FSPECP_and_FSPECH | |
| epErrorCode_1209__Deprecated_values_FCHR_and_FSPEC_are_ignored_change_to_unused | |
| epErrorCode_1210__Error_1210 | |
| epErrorCode_1211__FCALC_GT_0_ignored_because_of_FSPECP_1 | |
| epErrorCode_1212__Deprecated_value_FCHR_is_used_it_is_recommended_to_use_FSPECH | |
| epErrorCode_1213__Deprecated_value_xs_is_ignored_change_to_unused | |
| epErrorCode_1214__Deprecated_value_FDP_is_used_it_is_recommended_to_use_FSPECP | |
| epErrorCode_1215__Deprecated_value_FSPEC_is_used_it_is_recommended_to_use_FSPECH | |
| epErrorCode_1216__Deprecated_value_FDP_was_set_to_FSPECP | |
| epErrorCode_1217__Deprecated_value_FSPEC_was_set_to_FSPECH | |
| epErrorCode_1218__FVALETA_GT_0_only_possible_for_isentropic_efficiency_FETA_0_FVALETA_0_is_used | |
| epErrorCode_1219__Deprecated_values_FCHR_and_FSPEC_were_set_to_FSPECP_and_FSPECH | |
| epErrorCode_1220__Deprecated_value_FCHR_was_set_to_FSPECH | |
| epErrorCode_1221__Minimum_pressure_reached_pressure_drop_limited | |
| epErrorCode_1222__Too_much_xs_in_slag | |
| epErrorCode_1223__Supercritical_state_blowdown_temperature_set_to_inlet_temperature | |
| epErrorCode_1224__Result_values_RE_PR_and_NU_may_be_inaccurate_because_of_problems_with_property_calculation_for_average_quantities | |
| epErrorCode_1225__Relative_deviation_of_xs_restricted_to_2_ICONF | |
| epErrorCode_1226__Deviation_set_to_0_to_avoid_fluctuations_on_stream_with_M_LT_xs | |
| epErrorCode_1227__Validation_did_not_converge_for_xs_measurement_points | |
| epErrorCode_1228__Unreasonable_value_for_KAN_set_to_10_9 | |
| epErrorCode_1229__FSPEC_11_not_possible_for_FRABEK_1_FSPEC_0_used | |
| epErrorCode_1230__Characteristic_xs_LT_tmin | |
| epErrorCode_1231__Characteristic_xs_GT_tmax | |
| epErrorCode_1232__X_value_in_characteristic_xs_LT_first_point | |
| epErrorCode_1233__X_value_in_characteristic_xs_GT_last_point | |
| epErrorCode_1234__No_CPOS_characteristic_found_for_flap_position_xs | |
| epErrorCode_1235__Y_value_LT_first_point_of_characteristic_xs | |
| epErrorCode_1236__Y_value_GT_last_point_of_characteristic_xs | |
| epErrorCode_1237__Y_value_GT_first_point_of_characteristic_xs | |
| epErrorCode_1238__Y_value_LT_last_point_of_characteristic_xs | |
| epErrorCode_1239__Default_stream_start_value_xs_used | |
| epErrorCode_1240__VM1N_too_small_efficiency_characteristic_not_used | |
| epErrorCode_1241__M1N_too_small_efficiency_characteristic_not_used | |
| epErrorCode_1242__Calculated_P1_too_small_P1_set_to_P2 | |
| epErrorCode_1243__Upper_terminal_temperature_difference_too_small_set_to_10_15 | |
| epErrorCode_1244__Lower_terminal_temperature_difference_too_small_set_to_10_15 | |
| epErrorCode_1245__Mean_logarithmic_temperature_difference_too_small_set_to_10_15 | |
| epErrorCode_1246__Unreasonable_value_xs_Hz_for_frequency_to_specify_power_factor_use_FTYP_9 | |
| epErrorCode_1247__KA_reduced_to_avoid_DTLO_LT_xs_K | |
| epErrorCode_1248__Error_in_adaptation_polynomial_variable_name_xs_unknown | |
| epErrorCode_1249__Error_in_adaptation_polynomial_division_by_zero | |
| epErrorCode_1250__Error_in_adaptation_polynomial_power_by_negative_non_integral | |
| epErrorCode_1251__Error_in_adaptation_polynomial_result_is_not_a_number_NaN | |
| epErrorCode_1252__Error_in_adaptation_polynomial_FIND_index_xs_not_specified | |
| epErrorCode_1253__Error_in_adaptation_polynomial_arcus_co_sinus_argument_LT_1_or_GT_1 | |
| epErrorCode_1254__Error_in_adaptation_polynomial_log_log10_of_non_positive_number | |
| epErrorCode_1255__Error_in_adaptation_polynomial_sqrt_of_negative_number | |
| epErrorCode_1256__Invalid_scaling_method_for_material_equation_mode | |
| epErrorCode_1257__Variables_are_missing_or_new_variables_showed_up_in_equation_x2_in_iteration_step_x1 | |
| epErrorCode_1258__Validation_of_KAN_not_reasonable_for_this_component | |
| epErrorCode_1259__setting_reading_of_liquid_phase_not_possible_setting_reading_whole_fraction | |
| epErrorCode_1260__Non_zero_mass_flow_M1_specified_is_ignored_due_to_charge_mode | |
| epErrorCode_1261__Non_zero_mass_flow_M3_specified_is_ignored_due_to_discharge_mode | |
| epErrorCode_1262__setting_of_liquid_phase_is_deprecated_setting_whole_fraction | |
| epErrorCode_1263__In_off_design_FSPECP_1_not_possible_for_FCALC_1_FCALC_0_assumed | |
| epErrorCode_1264__Ambient_temperature_missing_0C_assumed | |
| epErrorCode_1265__Characteristic_xs_out_of_range | |
| epErrorCode_1266__Negative_FACT_values_deprecated_usage_of_FFU_recommended | |
| epErrorCode_1267__PMIN_GT_P1NSET_PMIN_set_to_P1NSET | |
| epErrorCode_1268__Specification_requires_connected_logical_stream_with_measurement | |
| epErrorCode_1269__Deviation_to_the_specified_raw_coal_XH2OB_GT_TOLMF | |
| epErrorCode_1270__Flag_combination_FCM_1_or_FCM_3_and_FCMEB_1_is_not_allowed | |
| epErrorCode_1271__FTMIX_1_expected_for_the_FCM_and_FCMEB_values_specified | |
| epErrorCode_1272__FTMIX_0_expected_for_the_FCM_and_FCMEB_values_specified | |
| epErrorCode_1273__Unplausible_value_of_M4N_specified | |
| epErrorCode_1274__Unplausible_value_of_TCLASSN_specified | |
| epErrorCode_1275__Unplausible_value_of_RXH2OB_expected | |
| epErrorCode_1276__Zero_drying_gas_mass_flow | |
| epErrorCode_1277__CWCB4_expected_due_to_RXH2OB_specification_exceeds_XH2OB_in_raw_coal | |
| epErrorCode_1278__Deviation_to_the_specified_raw_coal_water_content_GT_TOLMF | |
| epErrorCode_1279__Delivery_head_characteristic_ignored_because_value_is_0 | |
| epErrorCode_1280__Exergy_not_calculated_because_Tref_LT_Tmin_xs_C | |
| epErrorCode_1281__T_too_high_or_P_too_low_relative_humidity_undefined | |
| epErrorCode_1282__P3_GT_critical_pressure_condensation_not_possible | |
| epErrorCode_1283__Calculated_enthalpy_loss_too_high_reduced_to_reasonable_value | |
| epErrorCode_1284__Calculated_mass_flow_too_high_reduced_to_reasonable_value | |
| epErrorCode_1285__Calculated_enthalpy_gain_too_high_reduced_to_reasonable_value | |
| epErrorCode_1286__Heat_loss_reduced_because_of_small_mass_flow | |
| epErrorCode_1287__Iteration_of_heat_loss_calculation_not_completely_converged_deviation_xs_kW | |
| epErrorCode_1288__Upper_pressure_limit_reached | |
| epErrorCode_1289__Upper_enthalpy_limit_reached | |
| epErrorCode_1290__Upper_mass_flow_limit_reached | |
| epErrorCode_1291__Unreasonable_value_xs_for_dummy_mass_flow | |
| epErrorCode_1292__Lower_enthalpy_limit_reached | |
| epErrorCode_1293__Specification_value_TASHE_LT_T1_T5_set_to_T1 | |
| epErrorCode_1294__Parameters_for_characteristic_field_xs_not_in_ascending_order | |
| epErrorCode_1295__Oxygen_supplyxs_too_low_on_inlet_1_cooling_air_is_not_used_for_combustion | |
| epErrorCode_1296__Nominal_value_for_characteristic_xs_too_small | |
| epErrorCode_1297__Design_parameter_for_characteristics_xs_out_of_range | |
| epErrorCode_1298__Desulphuration_rate_reduced_to_xs_CaO_concentration_too_low | |
| epErrorCode_1299__xs_out_of_range_calculated_with_0 | |
| epErrorCode_1300__Unknown_Error | |
| epErrorCode_1301__Unknown_Warning | |
| epErrorCode_1302__Parameter_out_of_range_FTYPE | |
| epErrorCode_1303__Parameter_out_of_range_FCOOLING | |
| epErrorCode_1304__Parameter_out_of_range_FPMIN | |
| epErrorCode_1305__Parameter_out_of_range_PMIN_LT_1_mbar | |
| epErrorCode_1306__Parameter_out_of_range_FAIRMODE | |
| epErrorCode_1307__Parameter_out_of_range_DT24_LT_01 | |
| epErrorCode_1308__Parameter_out_of_range_DT14_LT_01 | |
| epErrorCode_1309__Parameter_out_of_range_Q34_LT_0 | |
| epErrorCode_1310__Parameter_out_of_range_EFF_01 | |
| epErrorCode_1311__Parameter_out_of_range_FDPMODE | |
| epErrorCode_1312__Parameter_out_of_range_DP12_LT_0 | |
| epErrorCode_1313__Parameter_out_of_range_FANPOWER_LT_0 | |
| epErrorCode_1314__Parameter_out_of_range_DP34_LT_0 | |
| epErrorCode_1315__Parameter_out_of_range_FSIZEKA | |
| epErrorCode_1316__Parameter_out_of_range_AREA_LE_0 | |
| epErrorCode_1317__Parameter_out_of_range_OHTC_LE_0 | |
| epErrorCode_1318__Parameter_out_of_range_HTC12_LE_0 | |
| epErrorCode_1319__Parameter_out_of_range_HTC34_LE_0 | |
| epErrorCode_1320__Parameter_out_of_range_S_WALL_LT_0 | |
| epErrorCode_1321__Parameter_out_of_range_L_WALL_LT_0 | |
| epErrorCode_1322__Parameter_out_of_range_DI_LE_0 | |
| epErrorCode_1323__Parameter_out_of_range_CFINS_LT_1 | |
| epErrorCode_1324__Parameter_out_of_range_NBAYS_LT_1 | |
| epErrorCode_1325__Parameter_out_of_range_DP62EXP | |
| epErrorCode_1326__Parameter_out_of_range_DP34EXP | |
| epErrorCode_1327__Parameter_out_of_range_EXP12 | |
| epErrorCode_1328__Parameter_out_of_range_EXP34 | |
| epErrorCode_1329__Parameter_out_of_range_FFANSPEED | |
| epErrorCode_1330__Parameter_out_of_range_FANSPEED_015 | |
| epErrorCode_1331__Parameter_out_of_range_FAIRFLOW | |
| epErrorCode_1332__Parameter_out_of_range_FFANEFF | |
| epErrorCode_1333__Parameter_out_of_range_FPFKA12 | |
| epErrorCode_1334__Parameter_out_of_range_FPFKA34 | |
| epErrorCode_1335__Parameter_out_of_range_PFKA12_001100 | |
| epErrorCode_1336__Parameter_out_of_range_PFKA34_001100 | |
| epErrorCode_1337__Parameter_out_of_range_FBAYMODE | |
| epErrorCode_1338__Parameter_out_of_range_FPRESSURE | |
| epErrorCode_1339__Parameter_out_of_range_target_pressure_LT_PMIN | |
| epErrorCode_1340__Parameter_out_of_range_FANSPEED_LO_LT_1_percent | |
| epErrorCode_1341__Parameter_out_of_range_FANSPEED_HI_FANSPEED_LO_099 | |
| epErrorCode_1342__Parameter_out_of_range_NBAYS_0_NBAYSN | |
| epErrorCode_1343__Parameter_out_of_range_FANEFF | |
| epErrorCode_1344__Parameter_out_of_range_FMOTOREFF | |
| epErrorCode_1345__Parameter_out_of_range_FanMotorEff | |
| epErrorCode_1346__Parameter_out_of_range_FMODE | |
| epErrorCode_1347__logic_stream_input_for_fan_speed_out_of_range_015 | |
| epErrorCode_1348__FFANSPEED_settings_require_input_on_logic_stream | |
| epErrorCode_1349__logic_stream_input_for_target_pressure_LT_PMIN | |
| epErrorCode_1350__FPRESSURE_settings_require_input_on_logic_stream | |
| epErrorCode_1351__logic_stream_input_for_PFKA_out_of_range_001100 | |
| epErrorCode_1352__FPFKA_settings_require_input_on_logic_stream | |
| epErrorCode_1353__Cannot_determine_T1 | |
| epErrorCode_1354__Cannot_determine_T2 | |
| epErrorCode_1355__Cannot_determine_T3 | |
| epErrorCode_1356__Cannot_determine_T4 | |
| epErrorCode_1357__Cannot_determine_H4sat | |
| epErrorCode_1358__Cannot_determine_T4sat | |
| epErrorCode_1359__Cannot_determine_H4 | |
| epErrorCode_1360__Cannot_determine_RHO1 | |
| epErrorCode_1361__Cannot_determine_S1 | |
| epErrorCode_1362__Cannot_determine_RHO1_from_PH | |
| epErrorCode_1363__Cannot_determine_h2max | |
| epErrorCode_1364__Cannot_determine_h4min | |
| epErrorCode_1365__T3_LT_T2 | |
| epErrorCode_1366__P4_LT_PMIN | |
| epErrorCode_1367__cannot_determine_H2isen | |
| epErrorCode_1368__FAIRFLOW_settings_require_Characteristic_Input_CFANFLOW | |
| epErrorCode_1369__Cannot_determine_H2 | |
| epErrorCode_1370__Cannot_determine_saturation_pressure | |
| epErrorCode_1371__Condensate_Pressure_Calculations_did_not_Converge | |
| epErrorCode_1372__Pinch_Point_reached | |
| epErrorCode_1373__CannotDeliverRequestedDutyMaximumPossibleCrossflowEffectivenessExceeded | |
| epErrorCode_1374__Cannot_Meet_Air_Temperature_Specification | |
| epErrorCode_1375__FFPFKA12_settings_require_Characteristic_CPFM1M1N | |
| epErrorCode_1376__FFPFKA34_settings_require_Characteristic_CPFM3M3N | |
| epErrorCode_1377__Cannot_determine_RHO3_from_PH | |
| epErrorCode_1378__Cannot_determine_RHO3N_from_PH | |
| epErrorCode_1379__Solver_for_Airflow_failed | |
| epErrorCode_1380__cannot_determine_P1_from_SH | |
| epErrorCode_1381__Zero_lookup_Value_detected_in_Characteristic_CFANEFF | |
| epErrorCode_1382__FFANEFF_settings_require_Characteristic_CFANEFF | |
| epErrorCode_1383__FANEFF_LE_0 | |
| epErrorCode_1384__FANMOTOREFF_LE_0 | |
| epErrorCode_1385__Cannot_evaluate_characteristic_CFANCURVE | |
| epErrorCode_1386__Cannot_evaluate_characteristic_CFANEFF | |
| epErrorCode_1387__Cannot_evaluate_characteristic_CMOTOREFF | |
| epErrorCode_1388__Cannot_evaluate_characteristic_CFANFLOW | |
| epErrorCode_1389__Cannot_evaluate_characteristic_CPFM1M1N | |
| epErrorCode_1390__Cannot_evaluate_characteristic_CPFM3M3N | |
| epErrorCode_1391__FAIRFLOW_settings_require_Characteristic_Input_CFANCURVE | |
| epErrorCode_1392__Cannot_evaluate_Kernel_Expression_EPMIN | |
| epErrorCode_1393__Cannot_evaluate_Kernel_Expression_ERELVOLFLOW | |
| epErrorCode_1394__Cannot_evaluate_Kernel_Expression_EFANEFF | |
| epErrorCode_1395__Cannot_evaluate_Kernel_Expression_EMOTOREFF | |
| epErrorCode_1396__Cannot_evaluate_Kernel_Expression_EPFKA12 | |
| epErrorCode_1397__Cannot_evaluate_Kernel_Expression_EPFKA34 | |
| epErrorCode_1398__Expression_ERELVOLFLOW_returned_value_out_of_range_000110 | |
| epErrorCode_1399__Expression_EFANEFF_returned_value_out_of_range_0011000 | |
| epErrorCode_1400__Expression_EMOTOREFF_returned_value_out_of_range_0011000 | |
| epErrorCode_1401__ShaftPowerN_LE_0 | |
| epErrorCode_1402__M1N_LE_0 | |
| epErrorCode_1403__Kernel_Expression_EPFKA12_returned_value_out_of_range_0011000 | |
| epErrorCode_1404__Zero_lookup_value_detected_in_Characteristic_CMOTOREFF | |
| epErrorCode_1405__FMOTOREFF_settings_require_Characteristic_CMOTOREFF | |
| epErrorCode_1406__Kernel_Expression_EPFKA34_returned_value_out_of_range_0011000 | |
| epErrorCode_1407__M3N_LE_0 | |
| epErrorCode_1408__Maximum_Effectiveness_Exceeded | |
| epErrorCode_1409__T2_spec_FAIRMODE_results_in_too_high_temperature_T2_for_effectiveness_method_FCOOLING | |
| epErrorCode_1410__T2_spec_FAIRMODE_results_in_too_low_temperature_T2_for_effectiveness_method_FCOOLING | |
| epErrorCode_1411__Cannot_determine_H4lim | |
| epErrorCode_1412__Effectiveness_is_limited_in_the_selected_design_mode | |
| epErrorCode_1413__Cannot_determine_HTC12_required_OHTC_is_too_big | |
| epErrorCode_1414__TargetTemperature_LT_1_C | |
| epErrorCode_1415__H3_LT_desired_H4_no_cooling_possible | |
| epErrorCode_1416__Could_not_find_a_solution_for_fan_speed_in_cooler_mode | |
| epErrorCode_1417__Could_not_find_a_solution_for_fan_speed | |
| epErrorCode_1418__Could_not_find_a_solution_for_pressure_P3_P4 | |
| epErrorCode_1419__Could_not_find_a_solution_for_NBays_in_cooler_mode | |
| epErrorCode_1420__Could_not_find_a_solution_for_NBays | |
| epErrorCode_1421__Cannot_Determine_inlet_steam_content_on_port_3 | |
| epErrorCode_1422__Steam_detected_on_port_3_inlet_Cooler_mode_FMODE_1_is_not_designed_to_handle_condensation_on_the_hot_side | |
| epErrorCode_1423__No_steam_detected_on_port_3_inlet_Condenser_mode_FMODE_0_can_only_handle_condensation_on_the_hot_side | |
| epErrorCode_1424__Flow_smaller_than_specified_minimum_flow_not_acceptable_in_design_case | |
| epErrorCode_1425__Inlet_flow_too_small_but_cannot_be_increased | |
| epErrorCode_1426__Minimum_pressure_reached_pressure_drop_first_reheat_limited | |
| epErrorCode_1427__Minimum_pressure_reached_pressure_drop_second_reheat_limited | |
| epErrorCode_1428__P11_LT_P10 | |
| epErrorCode_1429__Switched_off_because_specific_volume_cannot_be_calculated | |
| epErrorCode_1430__Steam_content_cannot_be_set_due_to_supercritical_state | |
| epErrorCode_1431__Switched_off_because_enthalpy_is_higher_than_enthalpy_of_saturated_liquid | |
| epErrorCode_1432__Switched_off_because_enthalpy_is_lower_than_enthalpy_of_saturated_vapour | |
| epErrorCode_1433__No_valid_substance_selected | |
| epErrorCode_1434__Switched_off_due_to_large_deviation_in_temperature | |
| epErrorCode_1435__Switched_off_because_calculated_value_is_too_small | |
| epErrorCode_1436__Heat_loss_too_large_reduced_to_10_of_delivered_heat | |
| epErrorCode_1437__xs_too_large | |
| epErrorCode_1438__xs_too_small | |
| epErrorCode_1439__Voltage_drop_restricted_because_of_H2MIN | |
| epErrorCode_1440__Thermal_loss_restricted_because_of_H2MIN | |
| epErrorCode_1441__Lower_mass_flow_limit_reached | |
| epErrorCode_1442__Empty_value_for_M3M1_deprecated_appropriate_setting_of_FSPECM_recommended | |
| epErrorCode_1443__Empty_value_for_DP12_deprecated_appropriate_setting_of_FSPECP_recommended | |
| epErrorCode_1444__Negative_value_for_steam_content_not_possible_X_0_used_for_calculation | |
| epErrorCode_1445__Steam_content_GT_1_not_possible_X_1_used_for_calculation | |
| epErrorCode_1446__Calculation_of_dry_gas_molecularweight_failed | |
| epErrorCode_1447__FTEMPERATURE_settings_require_input_on_logic_stream | |
| epErrorCode_1448__Parameter_out_of_range_FTEMPERATURE | |
| epErrorCode_1449__Lookup_Value_for_xs_Outside_of_Charline_Points | |
| epErrorCode_1450__xs_out_of_range_calculated_with_1 | |
| epErrorCode_1451__Dumped_heat_QDUMP_smaller_than_specified_minimum_QLOSSMIN | |
| epErrorCode_1452__Unreasonable_value_of_FTUBGEOM | |
| epErrorCode_1453__Flag_combination_FCM_5_and_FCMEB_0_is_not_allowed | |
| epErrorCode_1454__The_greatest_value_of_BWG_25_is_taken_instead_of_the_specified_value | |
| epErrorCode_1455__The_smallest_value_of_BWG_12_is_taken_instead_of_the_specified_value | |
| epErrorCode_1456__Unreasonable_value_of_VM12N | |
| epErrorCode_1457__The_smallest_value_of_NPASS_1_is_taken_instead_of_the_specified_value | |
| epErrorCode_1458__The_greatest_value_of_NPASS_4_is_taken_instead_of_the_specified_value | |
| epErrorCode_1459__Unreasonable_value_of_the_tube_inner_diameter_expected | |
| epErrorCode_1460__Flag_combination_FTMIX_0_FCMEB_1_and_1_LT_FCM_LT_4_is_not_allowed | |
| epErrorCode_1461__Mass_flow_setting_on_this_stream_not_possible | |
| epErrorCode_1462__Pressure_setting_on_this_stream_not_possible | |
| epErrorCode_1463__Set_FSPECLOG_to_determine_quantity_to_be_multiplied | |
| epErrorCode_1464__Setting_of_H_and_Q_not_possible | |
| epErrorCode_1465__No_gaseous_or_liquid_substances_are_allowed_at_inlet_4 | |
| epErrorCode_1466__No_XH2OB_fraction_is_allowed_at_inlet_xs | |
| epErrorCode_1467__Requested_setting_of_relative_humidity_not_possible | |
| epErrorCode_1468__Humidity_setting_requires_pressure_and_temperature_in_the_same_component | |
| epErrorCode_1469__Inlet_enthalpy_too_low_for_desuperheater_KA_set_to_0 | |
| epErrorCode_1470__Method_for_off_design_pressure_drop_calculation_FVOL_inconsistent_with_design_FDP | |
| epErrorCode_1471__FDP12RN_1_deprecated_FDP_1_used | |
| epErrorCode_1472__Calculated_velocity_W_exceeds_specified_maximum_WMAX | |
| epErrorCode_1473__Pressure_drop_was_restricted_according_to_pdropmaximum_in_the_model_options | |
| epErrorCode_1474__Maximum_number_of_coefficients_must_be_increased_to_xs | |
| epErrorCode_1475__Target_value_SCV_missing | |
| epErrorCode_1476__Start_value_outside_of_specified_min_max_range | |
| epErrorCode_1477__L3OFF_outside_of_specified_min_max_range | |
| epErrorCode_1478__Calculated_xs_kg_s_is_set_to_0 | |
| epErrorCode_1479__Recommendation_air_humidity_can_be_defined_in_this_component_now | |
| epErrorCode_1480__H1_was_limited_to_saturated_water | |
| epErrorCode_1481__Error_in_setting_of_relative_humidity | |
| epErrorCode_1482__Setting_of_relative_humidity_not_possible_because_composition_is_not_air | |
| epErrorCode_1483__Component_does_not_support_material_equations_use_INTMAT_off | |
| epErrorCode_1484__For_FVALDP_GT_0_pressure_drop_must_be_absolute | |
| epErrorCode_1485__Unknown_variable_in_equation_xs | |
| epErrorCode_1486__BRUM_deprecated_ETABN_used | |
| epErrorCode_1487__Desulphuration_not_implemented_for_FCALC_old_mode | |
| epErrorCode_1488__Insufficient_combustion_not_possible_for_this_fluid_type_ETABN_1_used | |
| epErrorCode_1489__Violation_of_energy_balance_coolant_outlet_temperature_greater_than_anode_exhaust | |
| epErrorCode_1490__Violation_of_energy_balance_coolant_outlet_temperature_greater_than_cathode_exhaust | |
| epErrorCode_1491__Component_not_available_for_fluids_without_phase_transition_FBIN_LT_0 | |
| epErrorCode_1492__Elementary_analysis_for_non_water_part_not_possible_assumed_to_be_ash | |
| epErrorCode_1493__Instable_time_step_width_too_large_or_boundary_condition_wrong_TSTORAGE_GT_TMAX | |
| epErrorCode_1494__Duplicate_definition_of_component_xs | |
| epErrorCode_1495__Inconsistent_specification_of_composition | |
| epErrorCode_1496__Sum_of_specified_components_is_xs_instead_of_10_and_no_explicit_scaling_method_set | |
| epErrorCode_1497__In_design_KAN_is_calculated_and_cannot_be_specified_by_logical_input_port | |
| epErrorCode_1498__For_usage_of_pseudomeasurement_point_IPS_must_be_GT_0 | |
| epErrorCode_1499__Gaseous_fraction_at_pump_inlet_GT_5 | |
| epErrorCode_1500__Parsing_failed_for_equation_xs | |
| epErrorCode_1501__Function_xs_not_found_in_Programmable_Dll | |
| epErrorCode_1502__General_error_xs_in_Programmable_Dll | |
| epErrorCode_1503__Invalid_interface_type_specified | |
| epErrorCode_1504__Invalid_options_specified | |
| epErrorCode_1505__DTN_has_to_be_increased_to_avoid_evaporation_in_eco_at_outlet_2 | |
| epErrorCode_1506__T4_has_to_be_increased_to_avoid_evaporation_in_eco_at_outlet_2 | |
| epErrorCode_1507__FADAPT_4_not_compatible_with_FDP12RN_DP12_ADAPT_DP12RN_P1_used | |
| epErrorCode_1508__Characteristic_FTRANS_2_cannot_be_used_for_composition_transmission | |
| epErrorCode_1509__Factor_MUL_cannot_be_used_for_composition_transmission | |
| epErrorCode_1510__OFFSET_cannot_be_used_for_composition_transmission | |
| epErrorCode_1511__FOUT_not_possible_for_specified_FIN | |
| epErrorCode_1512__User_break_Calculation_stopped | |
| epErrorCode_1513__Kernel_expression_xs_LT_1_was_set_to_1 | |
| epErrorCode_1514__Kernel_expression_xs_GT_1_was_set_to_1 | |
| epErrorCode_1515__DINNER_too_small | |
| epErrorCode_1516__PINPMIN_should_be_GT_001 | |
| epErrorCode_1517__This_FSPECD_is_only_possible_for_FTYPHX_1 | |
| epErrorCode_1518__This_FSPECD_is_only_possible_for_FTYPHX_2 | |
| epErrorCode_1519__Unable_to_reach_TCLASS_value_specified | |
| epErrorCode_1520__See_the_Detailed_Log_Output_of_the_Gas_Turbine | |
| epErrorCode_1521__Unknown_Setting | |
| epErrorCode_1522__Only_one_Value_Curve_per_Correction_is_allowed | |
| epErrorCode_1523__Unknown_Correction_Type | |
| epErrorCode_1524__Lookup_for_inconsistent_settings | |
| epErrorCode_1525__Unknown_Extrapolation_Method | |
| epErrorCode_1526__Curve_already_exists | |
| epErrorCode_1527__Could_not_look_up_reference_value | |
| epErrorCode_1528__Calculations_set_M4_flow_GT_0_but_no_Stream_is_connected | |
| epErrorCode_1529__failure_in_wdt_call_mt_calc_MT_PHI_OF_PT_for_Air_Inlet_Stream | |
| epErrorCode_1530__Massfractions_do_not_sum_up_to_1 | |
| epErrorCode_1531__Calculation_End | |
| epErrorCode_1532__Calculation_Start | |
| epErrorCode_1533__Created_Gasturbine_Object | |
| epErrorCode_1534__Initializing | |
| epErrorCode_1535__Do_Curve_Based_Calculations | |
| epErrorCode_1536__Calculate_Curve_Based_Output | |
| epErrorCode_1537__Get_Current_Conditions | |
| epErrorCode_1538__Read_Input | |
| epErrorCode_1539__Calculate_Output | |
| epErrorCode_1540__Calculate_Baseload_Corrections | |
| epErrorCode_1541__Calculate_Load_Corrections | |
| epErrorCode_1542__Error_in_CalcExhaustEnthalpy_when_calling_mt_calc_with_MT_H_OF_PT | |
| epErrorCode_1543__Error_in_GetStreamEnthalpy_when_calling_mt_calc_with_MT_H_OF_PT | |
| epErrorCode_1544__Error_in_wdt_call_mt_calc_MT_T_OF_PH_for_exhaust_stream | |
| epErrorCode_1545__Error_in_wdt_call_mt_calc_MT_T_OF_PH_for_injection_stream | |
| epErrorCode_1546__Error_in_wdt_call_mt_set_analyse_MT_AP_H2OG_for_MT_AT_FLUEGAS | |
| epErrorCode_1547__Error_in_wdt_call_mt_calc_MT_H_OF_PT_for_MT_AT_FLUEGAS | |
| epErrorCode_1548__Error_in_wdt_call_mt_calc_MT_X_OF_PH_for_injection_stream | |
| epErrorCode_1549__Error_in_wdt_call_mt_calc_MT_H_OF_PT_for_Air_Inlet_Stream | |
| epErrorCode_1550__Error_in_wdt_call_mt_calc_MT_CP_OF_PT_for_Air_Inlet_Stream | |
| epErrorCode_1551__Error_in_wdt_call_mt_inq_analyse_MT_AP_H2OG_for_Air_Inlet_Stream | |
| epErrorCode_1552__Error_in_wdt_call_mt_calc_MT_XG_OF_PT_for_Air_Inlet_Stream | |
| epErrorCode_1553__Error_in_wdt_mt_set_analyse_MT_AP_N2 | |
| epErrorCode_1554__Error_in_wdt_mt_set_analyse_MT_AP_O2 | |
| epErrorCode_1555__Error_in_wdt_mt_set_analyse_MT_AP_AR | |
| epErrorCode_1556__Error_in_wdt_mt_set_analyse_MT_AP_H2OG | |
| epErrorCode_1557__Error_in_wdt_mt_set_analyse_MT_AP_CO2 | |
| epErrorCode_1558__Error_in_wdt_mt_set_analyse_MT_AP_SO2 | |
| epErrorCode_1559__Error_in_wdt_mt_set_analyse_MT_AP_HCL | |
| epErrorCode_1560__Error_in_wdt_mt_set_analyse_MT_AP_CO | |
| epErrorCode_1561__Error_in_wdt_mt_set_analyse_MT_AP_NO | |
| epErrorCode_1562__Error_in_wdt_mt_set_analyse_MT_AP_NO2 | |
| epErrorCode_1563__Error_in_wdt_mt_set_analyse_MT_AP_CH4 | |
| epErrorCode_1564__Calculation_Finished_in_x0_iterations | |
| epErrorCode_1565__Correction_Type_x0_already_present | |
| epErrorCode_1566__Calculate_Correction_for_x0_x1 | |
| epErrorCode_1567__The_current_Load_Fraction_will_be_limited_to_the_Configured_Minimum | |
| epErrorCode_1568__The_current_Load_Fraction_will_be_limited_to_the_Configured_Maximum | |
| epErrorCode_1569__The_current_Load_will_be_limited_to_the_Configured_Minimum | |
| epErrorCode_1570__The_current_Load_will_be_limited_to_the_Configured_Maximum | |
| epErrorCode_1571__The_current_Loadfraction_exceeds_11_the_current_Baseload_You_Should_consider_to_configure_an_upper_Limit | |
| epErrorCode_1572__The_current_Loadfraction_is_below_01_the_current_Baseload_You_Should_consider_to_configure_a_lower_Limit | |
| epErrorCode_1573__Curve_Is_Limited_in_X_due_to_Extrapolation_Mode_Settings | |
| epErrorCode_1574__Curve_Is_Extrapolated_in_X | |
| epErrorCode_1575__Ambient_pressure_too_low_LT_600_mbar_or_Port_6_is_not_connected | |
| epErrorCode_1576__Ambient_pressure_exceeds_1200_mbar_Please_review_the_Pressure_settings_on_Port_6 | |
| epErrorCode_1577__Inlet_Pressuredrop_negative_LT_0_Please_review_the_Pressure_settings_on_Port_6_and_Port_1 | |
| epErrorCode_1578__Inlet_Pressuredrop_will_be_limited_to_70_mbar | |
| epErrorCode_1579__Inlet_Pressuredrop_exceeds_50_mbar | |
| epErrorCode_1580__Exhaust_Pressuredrop_negative_LT_0_Please_review_the_Pressure_settings_on_Port_6_and_Port_2 | |
| epErrorCode_1581__Exhaust_Pressuredrop_will_be_limited_to_100_mbar | |
| epErrorCode_1582__Exhaust_Pressuredrop_exceeds_70_mbar | |
| epErrorCode_1583__The_x1_Reference_Value_for_the_Correction_x0_x1_is_Outside_the_given_Data_Range | |
| epErrorCode_1584__The_Y_Reference_Value_for_the_Correction_x0_x1_is_Outside_the_given_Data_Range | |
| epErrorCode_1585__Correction_Type_already_present_Details_are_in_the_OEM_GT_Calculation_Log | |
| epErrorCode_1586__The_X_Reference_Value_for_a_Correction_is_Outside_the_given_Data_Range_Details_are_in_the_OEM_GT_Calculation_Log | |
| epErrorCode_1587__The_Y_Reference_Value_for_a_Correction_is_Outside_the_given_Data_Range_Details_are_in_the_OEM_GT_Calculation_Log | |
| epErrorCode_1588__The_Energy_Balance_Difference_Mode_FEBD_is_Not_Compatible_With_The_Load_Mode_FLOAD | |
| epErrorCode_1589__The_Exhaust_Temperature_is_Limited_by_the_Maximum_Exhaust_Temperature_of_the_CurveSet | |
| epErrorCode_1590__The_Generator_Output_is_Limited_by_the_GeneratorCap_of_the_CurveSet | |
| epErrorCode_1591__The_Partload_Fraction_is_Below_the_Minimum_Partload_Fraction_of_the_CurveSet | |
| epErrorCode_1592__The_Desired_Power_Output_Cannot_be_Met | |
| epErrorCode_1593__Exhaust_Temperature_Correction_cannot_be_Multiplicative_Skipping_Correction | |
| epErrorCode_1594__No_license_to_use_the_VTU_OEM_Gasturbine_Library_This_curve_set_requires_a_higher_version_of_the_VTU_Gas_Turbine_Library | |
| epErrorCode_1595__The_calculated_energy_balance_difference_is_LT_0_Please_check_your_input_data | |
| epErrorCode_1596__Error_in_WDT_call_mt_calc_MT_H_OF_PT_for_fuel_port | |
| epErrorCode_1597__The_OEMGT_curve_data_require_a_newer_version_of_the_software_The_current_version_cannot_handle_the_data_in_the_model | |
| epErrorCode_1598__Cannot_determine_the_exhaust_temperature | |
| epErrorCode_1599__The_cooling_port_port_8_must_be_connected_when_having_a_cooling_duty | |
| epErrorCode_1600__The_current_Curve_is_Empty | |
| epErrorCode_1601__Curve_Is_Limited_in_Y_due_to_Extrapolation_Mode_Settings | |
| epErrorCode_1602__Curve_Is_Extrapolated_in_Y | |
| epErrorCode_1603__Fuel_LHV_LT_75_percent_of_the_reference_LHV_of_the_curveset | |
| epErrorCode_1604__Fuel_LHV_LT_5000_kJ_kg | |
| epErrorCode_1605__For_phase_separation_FSPECH_2_is_used | |
| epErrorCode_1606__Fluid_not_suitable_for_phase_separation | |
| epErrorCode_1607__Pinchpoint_violation_xs_K_due_to_curvature_in_cp | |
| epErrorCode_1608__Controller_deactivated_due_to_supercritical_state | |
| epErrorCode_1609__FSPEC_GT_0_only_possible_for_isentropic_efficiency_FETA_0_FSPEC_0_is_used | |
| epErrorCode_1610__Pressure_on_inlet_xs_LT_tank_pressure_PN | |
| epErrorCode_1611__Pressure_on_outlet_xs_GT_tank_pressure_PN | |
| epErrorCode_1612__Calculation_of_result_array_for_total_fractions_failed | |
| epErrorCode_1613__A_fraction_xs_of_the_fluid_cannot_be_displayed_in_the_result_arrays | |
| epErrorCode_1614__Error_1614 | |
| epErrorCode_1615__Negative_values_for_xs_not_implemented_yet_Absolute_value_used_instead | |
| epErrorCode_1616__In_design_case_evaporation_in_economizer_should_be_avoided_for_this_component_because_of_impreciseness_in_off_design | |
| epErrorCode_1617__In_design_case_subcooling_at_inlet_of_evaporator_should_be_avoided_for_this_component_because_of_impreciseness_in_off_design | |
| epErrorCode_1618__In_design_case_superheating_at_outlet_of_evaporator_should_be_avoided_for_this_component_because_of_impreciseness_in_off_design | |
| epErrorCode_1619__Usage_of_ksSetPipeValue_without_automatic_generated_default_equations_see_spec_value_FDEFEQN | |
| epErrorCode_1620__Duplicate_variable_in_equation_xs_source_and_target_stream_and_variable_type_are_identical_or_identified_by_internal_factorization | |
| epErrorCode_1621__Number_of_equations_LT_number_of_variables | |
| epErrorCode_1622__No_coefficients_in_validation | |
| epErrorCode_1623__Too_many_coefficients_in_validation | |
| epErrorCode_1624__No_variables_in_validation | |
| epErrorCode_1625__Energy_balance_not_considered_due_to_large_temperature_deviations | |
| epErrorCode_1626__Error_evaluating_kernel_expression_xs | |
| epErrorCode_1627__Pressure_drop_restricted | |
| epErrorCode_1628__Outlet_enthalpy_restricted_to_reasonable_value | |
| epErrorCode_1629__Efficiency_restricted_to_reasonable_value | |
| epErrorCode_1630__Component_design_not_reasonable_with_a_mass_flow_of_xs | |
| epErrorCode_1631__NCV_999_is_deprecated_may_be_an_error_in_future_releases_please_use_appropiate_setting_for_FFLSET | |
| epErrorCode_1632__KV_value_computed_exceeds_the_max_value_of_char_line_The_valve_is_possibly_underdesigned | |
| epErrorCode_1633__2_phase_state_at_component_inlet_outlet | |
| epErrorCode_1634__Phase_transition_in_component_is_not_allowed | |
| epErrorCode_1635__Transition_to_cavitating_flow_occurs_XF_GE_XFZ | |
| epErrorCode_1636__DP12_GE_DPMAX_Choked_flow_limitation_reached | |
| epErrorCode_1637__Computed_M1_set_to_M1MAX | |
| epErrorCode_1638__Height_beyond_range_of_formula_pressure_of_001_bar_assumed | |
| epErrorCode_1639__Fluid_at_pin_3_available_in_liquid_state_only_condenser_cannot_be_used | |
| epErrorCode_1640__Medium_phase_state_can_not_be_determined_precisely | |
| epErrorCode_1641__Calculation_of_thermal_loss_from_geometry_not_possible_for_this_type_of_stream | |
| epErrorCode_1642__Component_for_solar_data_not_found_TAMB_from_specification_value_used | |
| epErrorCode_1643__No_heat_loss_because_T_LT_Tamb | |
| epErrorCode_1644__Unreasonable_value_for_NROW_NROW_1_used | |
| epErrorCode_1645__NROW_too_large_NROW_3_used | |
| epErrorCode_1646__Unreasonable_value_for_NRO2_NRO2_1_used | |
| epErrorCode_1647__NRO2_too_large_NRO2_3_used | |
| epErrorCode_1648__Not_enough_heat_available_for_requested_steam_production | |
| epErrorCode_1649__T4_would_be_smaller_than_T2_not_possible_in_concurrent_flow_DT44SN_xs_K_assumed | |
| epErrorCode_1650__T4_would_be_smaller_than_T1_DT44SN_xs_K_assumed | |
| epErrorCode_1651__Negative_or_0_values_for_xs_are_unreasonable_Absolute_or_minimum_value_used_instead | |
| epErrorCode_1652__Fluid_type_mismatch_at_injection_Table_difference_could_not_be_calculated | |
| epErrorCode_1653__Material_table_problem_during_calculation_of_table_difference_xs_assumed | |
| epErrorCode_1654__Incompatible_fluid_type_on_pin_xs | |
| epErrorCode_1655__Medium_with_FMED_xs_cannot_be_injected | |
| epErrorCode_1656__RCORR_is_not_transferred_to_L2START_because_L2START_was_set_to_empty | |
| epErrorCode_1657__RCORR_is_not_transferred_to_L3START_because_L3START_was_set_to_empty | |
| epErrorCode_1658__Invalid_Injection_Correction_Settings | |
| epErrorCode_1659__Invalid_Humidity_Correction_Settings | |
| epErrorCode_1660__Unknown_Corrected_Parameter_in_Curveset | |
| epErrorCode_1661__Double_lookup_for_efficiency_characteristic_not_possible | |
| epErrorCode_1662__Reference_for_double_lookup_not_available_for_characteristic_xs | |
| epErrorCode_1663__Value_of_0_not_possible_for_xs | |
| epErrorCode_1664__Missing_fluid_coefficients | |
| epErrorCode_1665__Mass_flow_rather_small_for_design_Consider_setting_component_to_FMODE_Local_Off_design | |
| epErrorCode_1666__Switched_off_because_MCONF_is_too_large | |
| epErrorCode_1667__Mass_flow_of_xs_kg_s_out_of_empty_storage | |
| epErrorCode_1668__Mass_flow_of_xs_kg_s_into_full_storage | |
| epErrorCode_1669__Mismatch_of_types_of_real_gas_correction_type_of_main_inlet_used_at_outlet | |
| epErrorCode_1670__Flag_combination_FTMIX_1_and_FCMEB_0_and_1_LT_FCM_LT_4_is_not_allowed | |
| epErrorCode_1671__Flag_combination_FCM_5_and_FCMEB_1_and_FTMIX_1_is_not_allowed | |
| epErrorCode_1672__Minimum_temperature_of_property_table_reached | |
| epErrorCode_1673__Maximum_temperature_of_property_table_reached | |
| epErrorCode_1674__Specified_DTN_too_small_T2_would_be_higher_than_maximum_temperature_of_property_table | |
| epErrorCode_1675__Specified_DTN_too_large_T2_would_be_lower_than_T1 | |
| epErrorCode_1676__Cannot_determine_exhaust_temperature | |
| epErrorCode_1677__The_desired_calculation_mode_requires_a_connected_logic_inlet_port | |
| epErrorCode_1678__Cannot_determine_exhaust_temperature_from_previous_iteration | |
| epErrorCode_1679__Equilibrium_calculations_returned_with_error_number_01_REACTANT_xs_TEMPERATURE_MORE_THAN_10K_FROM_TEMPERATURE_IN_thermpinp_REACT | |
| epErrorCode_1680__Equilibrium_calculations_returned_with_error_number_02_WARNING_REACTANT_xs_TEMPERATURE_NOT_EQUAL_TO_BUT_LESS_THAN_10K_FROM_THE_TEMPERATURE_IN_THE_THERMODYNAMIC_DATA_REACT | |
| epErrorCode_1681__Equilibrium_calculations_returned_with_error_number_03_REACTANT_xs_IS_EITHER_NOT_IN_THE_THERMODYNAMIC_DATA_OR_THE_TEMPERATURE_IS_OUT_OF_RANGE_FOR_THIS_SPECIES_REACT | |
| epErrorCode_1682__Equilibrium_calculations_returned_with_error_number_04_TEMPERATURE_MISSING_FOR_REACTANT_xs_REACT | |
| epErrorCode_1683__Equilibrium_calculations_returned_with_error_number_05_ELEMENT_SYMBOL_NOT_FOUND_IN_BLOCKDATA_REACT | |
| epErrorCode_1684__Equilibrium_calculations_returned_with_error_number_06_AMOUNT_MISSING_FOR_REACTANT_xs_PROGRAM_SET_WEIGHT_PERCENT_TO_100_REACT | |
| epErrorCode_1685__Equilibrium_calculations_returned_with_error_number_07_AMOUNT_MISSING_FOR_REACTANT_xs_REACT | |
| epErrorCode_1686__Equilibrium_calculations_returned_with_error_number_08_PRODUCT_SPECIES_CONTAINING_AN_ELEMENT_MISSING_SEARCH | |
| epErrorCode_1687__Equilibrium_calculations_returned_with_error_number_09_INSUFFICIENT_STORAGE_FOR_PRODUCTS_SEE_RP_1311_PART_2_PAGE_39_SEARCH | |
| epErrorCode_1688__Equilibrium_calculations_returned_with_error_number_10_LOW_TEMPERATURE_IMPLIES_CONVERGENCE_REQUIRES_A_CONDENSED_PRODUCT_EQLBRM | |
| epErrorCode_1689__Equilibrium_calculations_returned_with_error_number_11_SINGULAR_MATRIX_FIX_MAY_BE_ATTEMPTED_EQLBRM | |
| epErrorCode_1690__Equilibrium_calculations_returned_with_error_number_12_REDUCED_SET_OF_COMPONENTS_ATTEMPTED_EQLBRM | |
| epErrorCode_1691__Equilibrium_calculations_returned_with_error_number_13_DID_NOT_CONVERGE_ON_ELECTRON_BALANCE_EQLBRM | |
| epErrorCode_1692__Equilibrium_calculations_returned_with_error_number_14_CONVERGENCE_WAS_NOT_OBTAINED_EQLBRM | |
| epErrorCode_1693__Equilibrium_calculations_returned_with_error_number_15_NEW_COMPONENTS_EQLBRM | |
| epErrorCode_1694__Equilibrium_calculations_returned_with_error_number_16_RESULTS_MAY_BE_WRONG_DUE_TO_LOW_MOLE_FRACTION_OF_GASES_EQLBRM | |
| epErrorCode_1695__Equilibrium_calculations_returned_with_error_number_17_TEMPERATURE_IS_OUT_OF_RANGE_OF_THERMODYNAMIC_DATA_IN_LIBRARY_EQLBRM | |
| epErrorCode_1696__Equilibrium_calculations_returned_with_error_number_18_DERIVATIVE_MATRIX_SINGULAR_EQLBRM | |
| epErrorCode_1697__Equilibrium_calculations_returned_with_error_number_19_DID_NOT_CONVERGE_EQLBRM | |
| epErrorCode_1698__Equilibrium_calculations_returned_with_error_number_20_FROZEN_DID_NOT_CONVERGE_IN_11_ITERATIONS_FROZEN | |
| epErrorCode_1699__Equilibrium_calculations_returned_with_error_number_21_COEFFICIENTS_NOT_FOUND_FOR_REACTANT_REACT | |
| epErrorCode_1700__Equilibrium_calculations_returned_with_error_number_22_TEMPERATURE_IS_OUTSIDE_TEMPERATURE_RANGE_OF_THERMO_DATA_FOR_CONDENSED_SPECIES_FROZEN | |
| epErrorCode_1701__Equilibrium_calculations_returned_with_error_number_23_THE_NUMBER_OF_GASEOUS_SPECIES_USED_IN_THE_TRANSPORT_PROPERTIES_CALCULATIONS_WAS_CUT_OFF | |
| epErrorCode_1702__Equilibrium_calculations_returned_with_error_number_24_NUMBER_OF_FROZEN_REACTANTS_EXCEEDS_20 | |
| epErrorCode_1703__Equilibrium_calculations_returned_with_error | |
| epErrorCode_1704__Cannot_determine_exhaust_enthalpy | |
| epErrorCode_1705__Component_for_solar_data_not_found | |
| epErrorCode_1706__Five_parameter_model_solver_failed_Please_check_you_input_carefully | |
| epErrorCode_1707__Cannot_determine_maximum_power_point_MPP | |
| epErrorCode_1708__FCURVESET_is_out_of_range_There_are_less_curves_stored_than_indicated_by_FCURVESET | |
| epErrorCode_1709__The_internally_stored_curveset_cannot_be_read_please_check_your_data | |
| epErrorCode_1710__The_operating_modes_FLOAD_012_require_valid_curve_data_Bypassing_calculations | |
| epErrorCode_1711__Specified_DTN_too_small_T4_would_be_lower_than_minimum_temperature_of_property_table | |
| epErrorCode_1712__Specified_DTN_too_small_T4_would_be_lower_than_T1_PINPMIN | |
| epErrorCode_1713__Specified_DTN_too_small_T4_would_be_higher_than_T3 | |
| epErrorCode_1714__Design_of_heat_exchanger_not_possible_because_T1_GE_T3 | |
| epErrorCode_1715__DTN_must_be_GE_PINPMIN | |
| epErrorCode_1716__H4_decreased_because_H4_would_be_GT_H3 | |
| epErrorCode_1717__Pressure_drop_on_cold_side_too_large | |
| epErrorCode_1718__Pressure_drop_on_hot_side_too_large | |
| epErrorCode_1719__Specified_DTN_too_small_T3_would_be_lower_than_minimum_temperature_of_property_table | |
| epErrorCode_1720__H2_increased_because_H2_would_be_LT_H1 | |
| epErrorCode_1721__DTN_too_small_due_to_cross_flow | |
| epErrorCode_1722__DTN_too_high_due_to_cross_flow | |
| epErrorCode_1723__Heat_transfer_restricted_by_lower_limit_of_property_table | |
| epErrorCode_1724__Heat_transfer_restricted_by_upper_limit_of_property_table | |
| epErrorCode_1725__Specified_DTN_too_small_T2_would_be_lower_than_T2S | |
| epErrorCode_1726__Specified_DTN_too_large_T3_would_be_higher_than_maximum_temperature_of_property_table | |
| epErrorCode_1727__Specified_DTN_too_small_or_evaporator_wrong_type_T4_would_be_higher_than_T3 | |
| epErrorCode_1728__Specified_DTN_too_large_T2_would_be_higher_than_T4_PINPMIN | |
| epErrorCode_1729__Specified_DTN_too_small_T2_would_be_higher_than_T3_PINPMIN | |
| epErrorCode_1730__Controller_unable_to_change_the_controlled_variable_because_it_is_already_set_by_another_component | |
| epErrorCode_1731__Condenser_mode_can_only_handle_pure_two_phase_fluid_lines | |
| epErrorCode_1732__Loss_of_accuracy_due_to_very_high_ratio_of_kA_heat_transfer_coefficient_times_area_to_m_cp_fluid_mass_flow_times_heat_capacity | |
| epErrorCode_1733__Internal_iteration_for_the_calculation_of_ETAP_failed | |
| epErrorCode_1734__Computed_M1_set_to_zero_since_P2_GE_P1 | |
| epErrorCode_1735__Internal_iteration_for_mixing_enthalpy_not_converged_remaining_uncertainty_xs_kJ_kg | |
| epErrorCode_1736__Off_design_calculation_for_this_fluid_combination_not_yet_implemented | |
| epErrorCode_1737__Error_in_adaptation_polynomial_named_indicator_xs_not_found_please_ensure_FIND_is_set_to_0 | |
| epErrorCode_1738__No_transient_calculation_please_see_Model_Options_Simulation_Transient_Time_handling_no_heat_transfer_and_mass_changes_will_be_calculated | |
| epErrorCode_1739__FALAM_11_can_be_used_with_FCALC_2_only_Calculation_is_performed_with_FALAM_1 | |
| epErrorCode_1740__Unburnt_C_increased_due_to_lack_of_oxygen | |
| epErrorCode_1741__FSPEC_2_can_be_used_with_FOP_0_and_FCALC_2_only_Calculation_is_performed_with_FOP_0_and_FCALC_2 | |
| epErrorCode_1742__INTMAT_GT_0_not_available_for_FOP_1_Equations_are_set_up_only_for_substances_that_are_defined_elsewhere_in_the_model | |
| epErrorCode_1743__FTYPUB_GT_0_can_be_used_with_FCALC_LE_2_only_Calculation_is_performed_with_FTYPUB_0 | |
| epErrorCode_1744__Unburnt_C_and_S_increased_due_to_lack_of_oxygen | |
| epErrorCode_1745__Unburnt_C_H_S_increased_due_to_lack_of_oxygen | |
| epErrorCode_1746__Unburnt_Cl_increased_due_to_lack_of_hydrogen | |
| epErrorCode_1747__Insufficient_hydrogen_for_reduction_of_Cl | |
| epErrorCode_1748__FOP_chemical_equilibrium_can_be_used_with_FCALC_3_only_Calculation_is_performed_with_FCALC_3 | |
| epErrorCode_1749__Fluid_type_humid_air_can_be_used_with_FCALC_3_only_Calculation_is_performed_with_FCALC_3 | |
| epErrorCode_1750__Secondary_fuel_inlet_can_be_used_with_FCALC_3_only_Calculation_is_performed_with_FCALC_3 | |
| epErrorCode_1751__Specification_of_air_ratio_FALAM_1_not_possible_for_chemical_equilibrium_calculation_FOP_1 | |
| epErrorCode_1752__INTMAT_GT_0_can_be_used_with_FOP_0_only_Calculation_was_performed_with_FOP_0 | |
| epErrorCode_1753__FTYPUB_GT_0_can_be_used_with_FOP_0_only_Calculation_was_performed_with_FTYPUB_0 | |
| epErrorCode_1754__FCALC_LT_2_can_be_used_with_FOP_0_only_Calculation_was_performed_with_FCALC_2 | |
| epErrorCode_1755__FCOAL_0_recommended_for_ash_inlet_pin_4_to_avoid_enthalpy_difference_with_outlet_pin_5 | |
| epErrorCode_1756__Oil_fraction_defined_by_elementary_composition_in_oil_stream_is_only_xs_Another_stream_type_may_be_more_suitable | |
| epErrorCode_1757__Negative_DT3S2N_not_possible_in_case_of_wet_steam_at_port_3 | |
| epErrorCode_1758__Group_index_GT_0_with_FIDENT_5_not_possible | |
| epErrorCode_1759__Small_inaccuracy_in_calculation_of_transferred_heat | |
| epErrorCode_1760__Temperature_loss_too_high_restricted_according_to_TMIN_from_property_table | |
| epErrorCode_1761__Mixing_different_voltage_levels | |
| epErrorCode_1762__Idle_current_too_high | |
| epErrorCode_1763__Superconductivity_cannot_be_considered_Current_set_to_0_because_voltage_is_0 | |
| epErrorCode_1764__Mixing_different_frequencies | |
| epErrorCode_1765__Component_is_running_in_compatibility_mode_using_deprecated_setting_FSPEC | |
| epErrorCode_1766__If_FSPECD12_3_FSPECD56_also_must_be_3 | |
| epErrorCode_1767__If_FSPECD56_3_FSPECD12_also_must_be_3 | |
| epErrorCode_1768__For_FSPECD12_FSPECD56_3_DTAN_and_DTAB_must_have_the_same_value | |
| epErrorCode_1769__Inconsistent_design_values_xs | |
| epErrorCode_1770__Too_many_equations_reduce_overdeterminations | |
| epErrorCode_1771__T2MAX_LT_TMIN_from_property_table_TMIN_used | |
| epErrorCode_1772__Equation_x2_is_missing_in_iteration_step_x1 | |
| epErrorCode_1773__Equation_x2_was_added_in_iteration_step_x1 | |
| epErrorCode_1774__Calculation_of_phase_changes_are_not_implemented_yet | |
| epErrorCode_1775__Value_of_power_factor_not_reasonable_because_of_frequency_0 | |
| epErrorCode_1776__Value_of_phase_not_reasonable_because_of_frequency_0 | |
| epErrorCode_1777__Storage_capacity_is_0_storage_switched_off | |
| epErrorCode_1778__Reheat_is_cooled_down_T4_LT_T3 | |
| epErrorCode_1779__Torque_defined_on_mechanical_shafts_only | |
| epErrorCode_1780__Specified_upper_terminal_temperature_difference_DT3S2N_too_large_See_result_value_DT3S2_for_the_maximum_possible_value | |
| epErrorCode_1781__For_FSPEC_3_bearing_FSPECQ_4_or_5_recommended | |
| epErrorCode_1782__Cannot_evaluate_charline_CPLCOP_Lookup_at_nominal_conditions_gave_zero | |
| epErrorCode_1783__Cannot_evaluate_charline_CT4MIN | |
| epErrorCode_1784__Cannot_evaluate_charline_CT4MAX | |
| epErrorCode_1785__Cannot_evaluate_matrix_MXQC_The_settings_of_FDESHEAT_require_this_matrix | |
| epErrorCode_1786__Cannot_evaluate_matrix_MXQH_The_settings_of_FDESHEAT_require_this_matrix | |
| epErrorCode_1787__FFU_Settings_require_Port_7_to_be_connected | |
| epErrorCode_1788__extremely_small_unplausible_value_for_Monin_Obukhov_length_while_hub_height_wind_velocity_calculation | |
| epErrorCode_1789__unplausible_value_for_roughness_length_while_hub_height_wind_velocity_calculation | |
| epErrorCode_1790__unplausible_value_for_the_reference_wind_velocity_height_while_hub_height_wind_velocity_calculation | |
| epErrorCode_1791__unplausible_value_for_the_hub_height_while_hub_height_wind_velocity_calculation | |
| epErrorCode_1792__unplausible_value_for_the_reference_temperature_while_IEC_normalized_wind_velocity_calculation | |
| epErrorCode_1793__CLF_out_of_range_0_1 | |
| epErrorCode_1794__CLFN_out_of_range_0_1 | |
| epErrorCode_1795__Could_not_find_a_solution_for_cleanliness_in_design_run | |
| epErrorCode_1796__Non_monotonic_x_values_in_characteristic_xs | |
| epErrorCode_1797__The_range_of_validity_violation_for_the_Reynolds_number_LT_2300 | |
| epErrorCode_1798__The_range_of_validity_violation_for_the_Reynolds_number_GT_20E6 | |
| epErrorCode_1799__Elementary_balance_violated_for_refrigerant | |
| epErrorCode_1800__Refrigerant_fraction_too_small_at_inlet_3 | |
| epErrorCode_1801__Calculation_of_refrigerant_fraction_not_possible_at_inlet_1_presumely_unsuitable_composition | |
| epErrorCode_1802__Calculation_of_refrigerant_fraction_not_possible_at_inlet_3_presumely_unsuitable_composition | |
| epErrorCode_1803__Transient_calculation_cannot_be_carried_out_without_initialisation | |
| epErrorCode_1804__Changing_the_algorithm_without_a_new_initialisation_step_leads_to_wrong_calculation_results | |
| epErrorCode_1805__Results_of_initialisation_step_are_not_going_to_be_stored_Use_time_series_dialogue_instead_and_calculate_at_least_two_steps_First_run_and_Continuation_run | |
| epErrorCode_1806__Not_enough_inlet_mass_flow_to_satisfy_the_mass_balance_please_consider_model_set_up | |
| epErrorCode_1807__Residual_water_content_of_fine_coal_set_to_10e_6 | |
| epErrorCode_1808__Residual_water_content_of_fine_coal_set_to_raw_coal_water_content | |
| epErrorCode_1809__Generator_outlet_temperature_higher_than_boiling_temperature_reduced_to_xs_C | |
| epErrorCode_1810__No_transient_calculation_please_see_Model_Options_Simulation_Transient_Time_handling_only_heat_transfer_will_be_calculated_at_steady_state_conditions | |
| epErrorCode_1811__Inaccuracy_of_xs_K_in_temperature_setting | |
| epErrorCode_1812__Value_of_FL1F2_valid_for_water_steam_lines_only | |
| epErrorCode_1813__Value_of_FL1F2_valid_for_lines_with_composition_only | |
| epErrorCode_1814__SCC_method_is_used_out_of_range_Pressure_ratio_is_too_low_for_Fig_13 | |
| epErrorCode_1815__SCC_method_is_used_out_of_range_Flow_is_too_small_for_Fig_13 | |
| epErrorCode_1816__SCC_method_is_used_out_of_range_Inlet_pressure_Fig_2 | |
| epErrorCode_1817__SCC_method_is_used_out_of_range_Flow_is_too_small_for_Fig_2 | |
| epErrorCode_1818__SCC_method_is_used_out_of_range_Initial_pressure_not_in_range_for_Fig_14 | |
| epErrorCode_1819__SCC_method_is_used_out_of_range_Initial_temperature_not_in_range_for_Fig_14_500F_1400F | |
| epErrorCode_1820__KA_would_be_negative_calculation_was_performed_with_KA_0 | |
| epErrorCode_1821__SCC_Groups_must_be_configured_identically_Deviating_values_will_be_overridden_by_the_first_in_a_group | |
| epErrorCode_1822__This_SCC_Type_cannot_be_split_into_a_group | |
| epErrorCode_1823__Supercritical_pressure_critical_temperature_used_instead_of_boiling_temperature | |
| epErrorCode_1824__With_this_set_of_parameters_thermocline_cannot_be_specified | |
| epErrorCode_1825__Cannot_evaluate_matrix_MXQEL_The_settings_of_FDESEFF_require_this_matrix | |
| epErrorCode_1826__Cannot_evaluate_matrix_MXCOP_The_settings_of_FDESEFF_require_this_matrix | |
| epErrorCode_1827__T2_below_freezing_point_LOAD_will_be_reduced | |
| epErrorCode_1828__LOAD_will_be_increased_due_to_LOADMIN | |
| epErrorCode_1829__LOAD_is_below_LOADMIN | |
| epErrorCode_1830__Cannot_evaluate_charline_CPLCOP | |
| epErrorCode_1831__T4_LT_T4min_CT4MINT1 | |
| epErrorCode_1832__T4_GT_T4max_CT4MAXT1 | |
| epErrorCode_1833__Improper_negative_mass_flow_at_PIN_xs | |
| epErrorCode_1834__The_current_calculation_settings_FCALC_1_require_the_Reciprocating_Engine_Library_license_Please_contact_license_provider | |
| epErrorCode_1835__The_current_dataset_requires_a_more_actual_Reciprocating_Engine_Library_license_Please_contact_license_provider | |
| epErrorCode_1836__Cannot_read_dataset_The_library_mode_FCALC_1_requires_a_valid_dataset | |
| epErrorCode_1837__FDATASET_is_not_set_to_a_valid_dataset | |
| epErrorCode_1838__Gradient_of_density_may_cause_instable_stratification_please_check_storage_set_up | |
| epErrorCode_1839__Low_number_of_nodes_probably_imprecise_calculation_of_RPOSTC | |
| epErrorCode_1840__TemperatureControlMode_FTMODEx_4_requires_the_assignment_of_a_unique_ordinal_15_for_every_heatsource_of_that_respective_group | |
| epErrorCode_1841__TemperatureControlMode_FTMODEx_4_The_Specified_Heat_Source_Is_Not_Part_Of_The_Heat_Rejection_Group | |
| epErrorCode_1842__TemperatureControlMode_FTMODEx_4_at_least_one_group_member_is_required | |
| epErrorCode_1843__FLOADFRAC_1_requires_logic_port_11_to_be_connected | |
| epErrorCode_1844__FPOWER_1_requires_logic_port_11_to_be_connected | |
| epErrorCode_1845__FPOWER_2_requires_power_out_port_4_to_be_connected | |
| epErrorCode_1846__Air_Inlet_flow_LT_0 | |
| epErrorCode_1847__FVMODEA_and_FTMODEA_have_incompatible_settings_System_not_determined | |
| epErrorCode_1848__FVMODEB_and_FTMODEB_have_incompatible_settings_System_not_determined | |
| epErrorCode_1849__FVMODEC_and_FTMODEC_have_incompatible_settings_System_not_determined | |
| epErrorCode_1850__The_flow_settings_for_group_A_require_a_temperature_change_GT_0 | |
| epErrorCode_1851__The_flow_settings_for_group_B_require_a_temperature_change_GT_0 | |
| epErrorCode_1852__The_flow_settings_for_group_C_require_a_temperature_change_GT_0 | |
| epErrorCode_1853__The_temperature_settings_for_group_A_require_a_flow_GT_0 | |
| epErrorCode_1854__The_temperature_settings_for_group_B_require_a_flow_GT_0 | |
| epErrorCode_1855__The_temperature_settings_for_group_C_require_a_flow_GT_0 | |
| epErrorCode_1856__FUELTYPE_0_requires_a_connected_gas_fuel_port_3 | |
| epErrorCode_1857__FUELTYPE_1_requires_a_connected_oil_fuel_port_13 | |
| epErrorCode_1858__FUELTYPE_2_requires_a_connected_gas_fuel_port_3_and_a_connected_oil_fuel_port_13 | |
| epErrorCode_1859__FUELTYPE_out_of_range_012 | |
| epErrorCode_1860__PFOFHRATIO_out_of_range_01 | |
| epErrorCode_1861__Energy_Balance_Error_The_Engine_provides_more_heat_and_power_than_the_amount_of_fuel_can_deliver | |
| epErrorCode_1862__xs | |
| epErrorCode_1863__X_value_in_matrix_xs_LT_first_point | |
| epErrorCode_1864__X_value_in_matrix_xs_GT_last_point | |
| epErrorCode_1865__Y_value_in_matrix_xs_LT_first_point | |
| epErrorCode_1866__Y_value_in_matrix_xs_GT_last_point | |
| epErrorCode_1867__Site_eleveation_is_above_the_configured_upper_limit_Please_contact_the_engine_vendor_for_derating_details | |
| epErrorCode_1868__Inlet_temperature_is_above_the_configured_upper_limit_Please_contact_the_engine_vendor_for_derating_details | |
| epErrorCode_1869__Inlet_temperature_is_below_the_configured_lower_limit_Please_contact_the_engine_vendor_for_derating_details | |
| epErrorCode_1870__Inlet_specific_humidity_is_above_the_configured_upper_limit_Please_contact_the_engine_vendor_for_derating_details | |
| epErrorCode_1871__Inconsistency_between_the_heat_exchanger_type_and_port_indices_specification_for_object_xs | |
| epErrorCode_1872__Usage_of_LP_Leakage_ports_910_REQUIRES_Port_2_as_main_outlet_port_You_cannot_use_Port_34_as_main_outlet_port | |
| epErrorCode_1873__The_spec_variable_CFAEXH_is_out_of_range | |
| epErrorCode_1875__FDESEFF_0_is_not_compatible_with_FDESHEAT_2_FDESEFF_must_be_1_or_2 | |
| epErrorCode_1876__FDESHEAT_is_out_of_bounds | |
| epErrorCode_1877__FDESEFF_is_out_of_bounds | |
| epErrorCode_1878__FFU_is_out_of_bounds | |
| epErrorCode_1879__Partial_differential_equations_solver_failed | |
| epErrorCode_1880__Solver_failed_due_to_dry_area_in_cross_flow_section_You_need_to_increase_the_water_flow | |
| epErrorCode_1881__Not_enough_units_for_the_desired_load | |
| epErrorCode_1882__Load_GT_1 | |
| epErrorCode_1883__Partial_differential_equations_solver_failed_Water_air_ratio_is_probably_too_low | |
| epErrorCode_1884__FDES_is_out_of_bounds | |
| epErrorCode_1885__The_calculation_of_the_outlet_enthalpy_for_group_A_failed | |
| epErrorCode_1886__The_calculation_of_the_outlet_enthalpy_for_group_B_failed | |
| epErrorCode_1887__The_calculation_of_the_outlet_enthalpy_for_group_C_failed | |
| epErrorCode_1888__Could_not_determine_ambient_temperature_from_logic_port_12 | |
| epErrorCode_1889__The_calculation_of_the_inlet_enthalpy_for_group_A_failed | |
| epErrorCode_1890__The_calculation_of_the_inlet_enthalpy_for_group_B_failed | |
| epErrorCode_1891__The_calculation_of_the_inlet_enthalpy_for_group_C_failed | |
| epErrorCode_1892__TemperatureControlMode_FTMODEx_5_requires_logic_port_12_to_be_connected_to_an_ambient_air_line | |
| epErrorCode_1893__DP12_too_high_value_will_be_limited | |
| epErrorCode_1894__COC_must_be_GT_1 | |
| epErrorCode_1895__Desired_Outlet_Temperature_must_be_greater_than_the_Wet_Bulb_Temperature_and_less_or_equal_the_inlet_Temperature | |
| epErrorCode_1896__T2TARGET_is_empty | |
| epErrorCode_1897__Spec_variable_xs_has_no_Input | |
| epErrorCode_1898__Port_xs_not_connected | |
| epErrorCode_1899__Port_xs_is_out_of_specified_Min_Max_Range | |
| epErrorCode_1900__Due_to_PMIN_xs_bar_in_the_model_options_P_setting_not_possible_P_was_set_to_PMIN | |
| epErrorCode_1901__Due_to_PMIN_xs_bar_in_the_property_table_P_setting_not_possible_P_was_set_to_PMIN | |
| epErrorCode_1902__Due_to_PMAX_xs_bar_in_the_property_table_P_setting_not_possible_P_was_set_to_PMAX | |
| epErrorCode_1903__Due_to_TMIN_xs_C_in_the_property_table_T_setting_not_possible_T_was_set_to_TMIN | |
| epErrorCode_1904__Due_to_TMAX_xs_C_in_the_property_table_T_setting_not_possible_T_was_set_to_TMAX | |
| epErrorCode_1905__Governing_Stage_DPCVVWO_must_be_greater_than_Zero | |
| epErrorCode_1906__Dew_point_temperature_is_valid_for_pure_water_only_as_LiBr_cannot_be_in_the_vapor_phase | |
| epErrorCode_1907__Composition_error_negative_fraction_of_xs | |
| epErrorCode_1908__Composition_error_fraction_of_xs_GT_1 | |
| epErrorCode_1909__Heat_Rejection_Group_xs_Cannot_reach_target_temperature_due_to_flow_limitation | |
| epErrorCode_1910__Due_to_PMAX_xs_bar_in_the_model_options_P_setting_not_possible_P_was_set_to_PMAX | |
| epErrorCode_1911__Due_to_HMIN_xs_kJ_kg_in_the_model_options_H_setting_not_possible_H_was_set_to_HMIN | |
| epErrorCode_1912__Due_to_HMAX_xs_kJ_kg_in_the_model_options_H_setting_not_possible_H_was_set_to_HMAX | |
| epErrorCode_1913__Due_to_MMIN_xs_kg_s_in_the_model_options_M_setting_not_possible_M_was_set_to_MMIN | |
| epErrorCode_1914__Due_to_MMAX_xs_kg_s_in_the_model_options_M_setting_not_possible_M_was_set_to_MMAX | |
| epErrorCode_1915__Unreasonable_value_for_xs_0_used | |
| epErrorCode_1916__Unreasonable_value_for_emissisivity_06_used | |
| epErrorCode_1917__Problem_in_calculation_of_result_value_ETAP | |
| epErrorCode_1918__Compatibility_mode_when_using_FCHR_LT_0_FIDENT_is_ignored | |
| epErrorCode_1919__The_design_method_FDESIGN_1_requires_all_nominal_values_except_NBAYSN_and_CLFN_to_be_populated | |
| epErrorCode_1920__Off_design_requires_all_nominal_values_to_be_populated | |
| epErrorCode_1921__There_are_duplicate_X_or_Y_values_in_one_of_the_Curves | |
| epErrorCode_1922__For_FSTART_2_at_initialization_step_M1M2_GT_0_and_M1_M2_expected | |
| epErrorCode_1923__Heating_value_on_NH3_inlet_differs_from_expected_value_xs | |
| epErrorCode_1924__FVMODED_and_FTMODED_have_incompatible_settings_System_not_determined | |
| epErrorCode_1925__The_flow_settings_for_group_D_require_a_temperature_change_GT_0 | |
| epErrorCode_1926__The_temperature_settings_for_group_D_require_a_flow_GT_0 | |
| epErrorCode_1927__The_calculation_of_the_outlet_enthalpy_for_group_D_failed | |
| epErrorCode_1928__The_calculation_of_the_inlet_enthalpy_for_group_D_failed | |
| epErrorCode_1929__Difference_in_voltage_exceeds_error_limit | |
| epErrorCode_1930__Difference_in_power_exceeds_error_limit | |
| epErrorCode_1931__Difference_in_frequency_exceeds_warning_limit | |
| epErrorCode_1932__Difference_in_voltage_exceeds_warning_limit | |
| epErrorCode_1933__Difference_in_power_exceeds_warning_limit | |
| epErrorCode_1934__Difference_in_frequency_exceeds_error_limit | |
| epErrorCode_1935__There_are_duplicate_X_values_in_the_following_curves_xs | |
| epErrorCode_1936__There_are_duplicate_Y_values_in_the_following_curves_xs | |
| epErrorCode_1937__Mixing_of_1_phase_and_3_phase_alternating_current_not_possible_NPHAS_from_inlet_1_used | |
| epErrorCode_1938__Unknown_material_type_in_xs_ST35_8_used | |
| epErrorCode_1939__Calculated_lambda_for_material_selected_in_xs_too_small_Lambda_40_used | |
| epErrorCode_1940__The_power_outlet_port_5_must_be_connected_when_frequency_correction_is_active_and_FGENF_1 | |
| epErrorCode_1941__Electrical_phase_at_inlet_xs_is_overwritten | |
| epErrorCode_1942__Electrical_phase_at_inlet_cannot_be_calculated | |
| epErrorCode_1943__Component_requires_continuation_of_iteration_because_of_phase_setting | |
| epErrorCode_1944__Internal_iteration_for_cross_flow_DTM_not_converged | |
| epErrorCode_1945__Mixing_of_different_circuit_types_NPHAS | |
| epErrorCode_1946__Capacity_ignored_because_of_DC | |
| epErrorCode_1947__Electrical_phase_calculation_failed_best_possible_value_used | |
| epErrorCode_1948__Unreasonable_value_for_NPHAS_calculation_performed_with_NPHAS_1 | |
| epErrorCode_1949__Electrical_phase_calculation_failed_phase_shift_ignored | |
| epErrorCode_1950__Voltage_too_small_calculation_performed_with_00001_V | |
| epErrorCode_1951__Temperature_setting_could_not_be_checked | |
| epErrorCode_1952__T_calculation_Refprop_returns_xs | |
| epErrorCode_1953__Drain_cannot_be_used_for_predefined_Refprop_mixture_because_composition_change_is_not_possible | |
| epErrorCode_1954__Requested_accuracy_too_high_maximum_deviation_is_xs | |
| epErrorCode_1955__Lower_frequency_limit_reached | |
| epErrorCode_1956__Upper_frequency_limit_reached | |
| epErrorCode_1957__Lower_voltage_limit_reached | |
| epErrorCode_1958__Upper_voltage_limit_reached | |
| epErrorCode_1959__Lower_power_limit_reached | |
| epErrorCode_1960__Upper_power_limit_reached | |
| epErrorCode_1961__No_accurate_solution_found_for_P1_FTARGETOD_0 | |
| epErrorCode_1962__FSPEC_1_for_Off_Design_only_Nominal_values_are_not_updated | |
| epErrorCode_1963__Uncertainty_in_calculation_of_electric_current | |
| epErrorCode_1964__Voltage_or_power_factor_is_0_current_cannot_be_calculated | |
| epErrorCode_1965__Mixing_different_voltage_phases_correct_phase_calculation_not_possible | |
| epErrorCode_1966__Negative_power | |
| epErrorCode_1967__DT3S2N_too_large_Note_that_in_in_the_2_phase_region_it_is_related_to_the_fluid_temperature_xs_C | |
| epErrorCode_1968__DT3S2N_too_large_Note_that_for_superheated_vapor_it_is_related_to_the_dew_point_temperature_xs_C | |
| epErrorCode_1969__KAN_was_calculated_with_DTUP_10_15_Use_a_desuperheater_for_more_reasonable_KAN_values | |
| epErrorCode_1970__Result_values_XIL2_and_XILV2_could_not_be_calculated | |
| epErrorCode_1971__Internal_iteration_for_radiation_not_converged | |
| epErrorCode_1972__X_setting_not_possible_for_this_fluid | |
| epErrorCode_1973__Component_cannot_be_designed_when_switched_off_FMODE_local_off_design_used | |
| epErrorCode_1974__Component_cannot_be_switched_off_when_bypass_outlet_7_is_not_connected | |
| epErrorCode_1975__FSPEC_1_not_possible_when_switched_off_FSPEC_0_used | |
| epErrorCode_1976__No_accurate_solution_found_for_P3_and_M3_FTARGETOD_2 | |
| epErrorCode_1977__P3_is_out_of_Range_P3_GT_P2_3_LE_P3_P1_LE_10000 | |
| epErrorCode_1978__Component_overwrites_material_data_at_pin_xs | |
| epErrorCode_1979__No_wind_data_component_with_index_xs_found | |
| epErrorCode_1980__Only_one_of_F_or_M_can_be_specified | |
| epErrorCode_1981__Only_one_of_P_or_U_can_be_specified | |
| epErrorCode_1982__Only_one_of_I_Q_or_H_can_be_specified | |
| epErrorCode_1983__Only_one_of_COSP_or_PHEL_can_be_specified | |
| epErrorCode_1984__Setting_of_I_also_requires_specification_of_COSP_or_PHEL | |
| epErrorCode_1985__Setting_of_I_also_requires_specification_of_type_of_current_NPHAS | |
| epErrorCode_1986__Setting_of_I_also_requires_specification_of_voltage_U | |
| epErrorCode_1987__Standard_dataset_is_suitable_for_large_motors_ETAEN_may_be_too_high | |
| epErrorCode_1988__Power_factor_must_be_between_1_and_1 | |
| epErrorCode_1989__Unreasonable_value_for_PP_PP_1_used | |
| epErrorCode_1990__Empty_value_for_xs_set_to_0 | |
| epErrorCode_1991__Deprecated_setting_M_1_ignored_To_avoid_this_warning_leave_either_empty_or_use_another_frequency_setting | |
| epErrorCode_1992__FLOAD_7_requires_port_9_to_be_connected | |
| epErrorCode_1993__FLOAD_7_could_not_find_a_solution_for_the_desired_heat_consumption_within_the_load_range | |
| epErrorCode_1994__No_data_for_temperature_setting_available_for_this_fluid_in_the_NASA_library | |
| epErrorCode_1995__T4_too_high | |
| epErrorCode_1996__Property_function_issue_in_H2S_calculation | |
| epErrorCode_1997__Problem_in_H2S_calculation_REFPROP_returns_xs | |
| epErrorCode_1998__Hub_height_HH_LT_recommended_minimum_HHMIN_for_this_wind_turbine_type | |
| epErrorCode_1999__H2S_calculation_was_executed_without_real_gas_correction | |
| epErrorCode_2000__Direct_current_phase_undefined | |
| epErrorCode_2001__FCPOS_field_is_suitable_for_design_up_to_a_flap_position_of_xs | |
| epErrorCode_2002__FCPOS_field_is_suitable_for_design_for_a_flap_position_of_at_least_xs | |
| epErrorCode_2003__xs_is_empty_Please_repeat_design_and_take_over_reference_values | |
| epErrorCode_2004__Pure_solid_normalized_volume_cannot_be_calculated | |
| epErrorCode_2005__H2S_calculation_was_executed_with_FDBR | |
| epErrorCode_2006__Issue_in_heating_value_calculation_at_pin_xs | |
| epErrorCode_2007__Critical_point_cannot_be_calculated | |
| epErrorCode_2008__Calculation_of_current_requires_specification_of_NPHAS_in_the_same_component | |
| epErrorCode_2009__Calculation_of_current_requires_specification_of_U_in_the_same_component | |
| epErrorCode_2010__Calculation_of_current_requires_specification_of_PHEL_in_the_same_component | |
| epErrorCode_2011__Direct_current_frequency_undefined | |
| epErrorCode_2012__Inlet_DC_Power_GT_Q1N_PDCO_in_Sandia_Performance_Model | |
| epErrorCode_2013__Inlet_DC_Voltage_GT_VDCMAX | |
| epErrorCode_2014__Inlet_DC_Current_GT_IDCMAX | |
| epErrorCode_2015__Choked_flow_condition_in_governing_stage_design_GSPR_too_small | |
| epErrorCode_2016__SOLPOS_algorithm_does_not_support_solar_time_conversion_in_cases_of_date_changes_use_other_algorithm_or_specify_local_time | |
| epErrorCode_2017__Choked_flow_condition_in_governing_stage_design_Outlet_pressure_P2_too_small | |
| epErrorCode_2018__Liquid_level_limit_violated | |
| epErrorCode_2019__At_FSPEC_EQ_1_only_FSPIN_EQ_0_is_compatible_with_transient_simulation | |
| epErrorCode_2020__H_calculation_Refprop_returns_xs | |
| epErrorCode_2021__Efficiency_becomes_infinite_because_power_is_0 | |
| epErrorCode_2022__Convergence_not_reached_because_of_high_fluctuations_in_partial_derivatives | |
| epErrorCode_2023__Convergence_delayed_because_of_controller_fluctuations_higher_than_TOL | |
| epErrorCode_2024__T2_too_high_for_design_of_an_evaporator | |
| epErrorCode_2025__No_transient_simulation_in_Design_mode_Component_set_to_Off_Design | |
| epErrorCode_2026__Supercritical_temperature_critical_pressure_used_instead_of_boiling_pressure | |
| epErrorCode_2027__For_phase_separation_same_library_on_all_streams_required_Library_selection_in_component_105_ignored | |
| epErrorCode_2028__HPT_call_failed_Table_difference_calculated_iteratively_with_an_uncertainty_of_xs | |
| epErrorCode_2029__HPT_call_failed_H_calculated_iteratively_with_an_uncertainty_of_xs | |
| epErrorCode_2030__Cannot_determine_inlet_temperature_of_mixture_of_all_inlet_flows | |
| epErrorCode_2031__Only_components_of_type_1_33_46_148_150_are_allowed_within_a_header | |
| epErrorCode_2032__FM_1_is_expected_in_exactly_one_component_of_type_149_within_a_header | |
| epErrorCode_2033__At_least_one_component_of_type_148_is_expected_within_a_header | |
| epErrorCode_2034__At_least_one_component_of_type_149_is_expected_within_a_header | |
| epErrorCode_2035__Mixing_different_speeds | |
| epErrorCode_2036__Correction_in_NCV2_too_large_NCV3_adapted_as_well | |
| epErrorCode_2037__Battery_cannot_operate_with_AC | |
| epErrorCode_2038__Superheated_steam_at_PIN_3_eventually_unreliable_results_at_FHEI_EQ_20_or_transient_simulations | |
| epErrorCode_2039__No_operation_because_of_value_of_xs | |
| epErrorCode_2040__For_this_FTYP_only_single_elements_can_be_used_for_FSUBST | |
| epErrorCode_2041__Charging_current_higher_then_ICSCELL | |
| epErrorCode_2042__DC_should_not_have_an_imaginary_part_of_current | |
| epErrorCode_2043__Second_fuel_port_cannot_be_used_with_INTMAT_gt_0_or_FVALNCV_gt_0 | |
| epErrorCode_2044__Requested_discharge_current_would_decrease_voltage_below_UCOCELL | |
| epErrorCode_2045__Charge_voltage_below_UCELLN_battery_not_charged | |
| epErrorCode_2046__Distance_to_plume_formation_is_below_the_configured_threshold_DTWARN | |
| epErrorCode_2047__SOC_LT_SOCMIN_battery_switched_off | |
| epErrorCode_2048__SOCNEW_LT_SOCMIN_battery_should_be_switched_off | |
| epErrorCode_2049__SOC_GT_SOCMAX_battery_should_be_discharged | |
| epErrorCode_2050__SOCNEW_GT_SOCMAX_charging_should_be_stopped | |
| epErrorCode_2051__SOH_setting_on_pin_4_outside_of_valid_range_0_LT_SOH_LE_1_SOH_EQ_1_assumed | |
| epErrorCode_2052__SOC_GT_SOCMAX_battery_is_not_charged | |
| epErrorCode_2053__Specified_DTN_too_large_T4_would_be_higher_than_T3 | |
| epErrorCode_2054__Only_one_of_VEL_SET_D_SET_or_A_SET_can_be_specified_VEL_SET_is_used | |
| epErrorCode_2055__For_VEL_EQ_0_either_P_or_PSTAT_SET_can_be_specified_PSTAT_SET_ignored | |
| epErrorCode_2056__TSTAT_SET_ignored_because_H_is_already_specified_by_H_T_or_Q | |
| epErrorCode_2057__A_SET_D_SET_are_ignored_because_M_is_specified | |
| epErrorCode_2058__PSTAT_SET_is_ignored_because_P_is_specified_without_specification_of_TSTAT_SET | |
| epErrorCode_2059__PSTAT_SET_GT_P_not_possible | |
| epErrorCode_2060__Only_one_of_VEL_SET_D_SET_or_A_SET_can_be_specified_A_SET_is_used | |
| epErrorCode_2061__Either_T_or_TSTAT_SET_can_be_specified_T_ignored | |
| epErrorCode_2062__Error_in_calculation_of_PSTAT | |
| epErrorCode_2063__The_current_operating_point_is_out_of_the_mapped_range | |
| epErrorCode_2064__Need_a_valid_D_IN_for_FX_EQ_1 | |
| epErrorCode_2065__Need_a_valid_D_IMP_for_FY_EQ_1 | |
| epErrorCode_2066__Need_a_valid_D_OUT_for_total_static_calculations | |
| epErrorCode_2067__Choked_flow_condition_in_compressor_inlet_D_IN_is_too_small_for_required_mass_flow | |
| epErrorCode_2068__FQ_setting_deprecated_additional_shaft_port_available_for_reverse_flow_direction | |
| epErrorCode_2069__xs_out_of_range_calculated_with_1 | |
| epErrorCode_2070__Invalid_FPREFF_selected | |
| epErrorCode_2071__On_stream_type_humid_air_humidity_has_to_be_specified_in_component_1_or_33 | |
| epErrorCode_2072__Controller_switched_due_to_problems_with_temperature_calculation | |
| epErrorCode_2073__Superheating_cannot_be_calculated_FTSCV_EQ_0_used | |
| epErrorCode_2074__Subcooling_cannot_be_calculated_FTSCV_EQ_0_used | |
| epErrorCode_2075__No_gas_phase_available_to_extract_at_current_conditions | |
| epErrorCode_2076__No_liquid_phase_available_to_extract_at_current_conditions | |
| epErrorCode_2077__Outlet_specific_volume_xs_times_higher_than_inlet_Taking_the_average_for_calculation_of_geodesic_pressure_drop_may_be_inaccurate | |
| epErrorCode_2078__ULIM_LE_LLIM | |
| epErrorCode_2079__Non_zero_mass_flows_at_outlets_inconsistent_to_FOMOD_specification | |
| epErrorCode_2080__Non_zero_mass_flows_at_inlet_inconsistent_to_FOMOD_specification | |
| epErrorCode_2081__Non_zero_mass_flows_at_inlet_outlets_inconsistent_to_FOMOD_specification | |
| epErrorCode_2082__Boiling_state_calculation_failed | |
| epErrorCode_2083__Dewing_state_calculation_failed | |
| epErrorCode_2084__Phase_separation_not_possible_due_to_fluid_property_errors | |
| epErrorCode_2085__Reaction_rate_for_CaO_H2O_GT_CaOH2_reduced_to_xs_H2O_concentration_too_low | |
| epErrorCode_2086__Reaction_rate_for_CaO_CO2_GT_CaCO3_reduced_to_xs_CO2_concentration_too_low | |
| epErrorCode_2087__Reaction_rate_for_CaO_CO2_GT_CaCO3_reduced_to_xs_CaO_already_converted_to_CaOH2 | |
| epErrorCode_2088__Reaction_rate_for_MgO_CO2_GT_MgCO3_reduced_to_xs_CO2_concentration_too_low | |
| epErrorCode_2089__Power_restricted_by_CRATE | |
| epErrorCode_2090__Fluid_type_not_suitable_for_modification_of_power_enthalpy_used_instead | |
| epErrorCode_2091__Oxygen_concentration_in_1_too_low_conversion_rate_ECONH2_reduced_to_xs | |
| epErrorCode_2092__CO_concentration_in_4_too_low_conversion_rate_reduced | |
| epErrorCode_2093__Power_restricted_by_internal_resistance | |
| epErrorCode_2094__Battery_not_charged_because_requested_power_LT_STHR | |
| epErrorCode_2095__Resistance_too_low_voltage_would_become_LT_0 | |
| epErrorCode_2096__Diffusion_number_GT_08_consider_decreasing_the_time_step_increasing_the_spatial_step_to_ensure_stable_solution | |
| epErrorCode_2097__Current_determined_by_next_battery_FOP_EQ_min_1_used | |
| epErrorCode_2098__Pin_1_is_used_for_series_connection_of_batteries_only_For_current_input_use_negative_current_at_pin_2 | |
| epErrorCode_2099__Humidity_correction_deactivated_below_freezing_point | |
| epErrorCode_2100__Desired_pressure_condenser_mode_temperature_cooler_mode_could_not_be_met_size_too_small | |
| epErrorCode_2101__Compressor_power_calculated_via_density_instead_of_entropy | |
| epErrorCode_2102__Min_pressure_limit_violated | |
| epErrorCode_2103__Max_pressure_limit_violated | |
| epErrorCode_2104__Fluid_pressure_in_storage_higher_than_the_inlet_pressure | |
| epErrorCode_2105__No_other_component_is_setting_NCV_at_outlet_NCV_0_used | |
| epErrorCode_2106__No_other_component_is_setting_NCV_NCV_0_used | |
| epErrorCode_2107__VEL_calculated_from_p_and_pstat_VEL_SET_ignored | |
| epErrorCode_2108__The_characteristic_lookup_CDHEXHVOL_resulted_in_a_negative_value_for_DHEXHA | |
| epErrorCode_2109__Setting_in_this_component_is_deprecated_and_overwrites_setting_of_air_humidity_in_component_1_or_33 | |
| epErrorCode_2110__error_solving_validation_matrix | |
| epErrorCode_2111__Error_xs_from_mixture_library | |
| epErrorCode_2112__Pseudo_pure_fluid_or_predefined_mixture_in_2_phase_state__different_composition_of_both_phases_is_neglected | |
| epErrorCode_2113__Flag_FPREFF_is_out_of_range | |
| epErrorCode_2114__Flag_FX_is_out_of_range | |
| epErrorCode_2115__Flag_FY_is_out_of_range | |
| epErrorCode_2116__Flag_FZ_is_out_of_range | |
| epErrorCode_2117__Impeller_diameter_DIMP_invalid | |
| epErrorCode_2118__Inlet_Port_not_connected | |
| epErrorCode_2119__Discharge_Port_not_connected | |
| epErrorCode_2120__Shaft_inlet_not_connected | |
| epErrorCode_2121__The_current_flow_is_out_of_range_of_the_given_surge_line_x | |
| epErrorCode_2122__The_current_operating_point_is_beyond_the_surge_limit | |
| epErrorCode_2123__PREF_must_be_GT_0 | |
| epErrorCode_2124__Calulations_gave_infinite_results | |
| epErrorCode_2125__For_MWF13_LSTO12_RHOBW_values_specified_the_value_of_AWF13_must_be_gt_x1 | |
| epErrorCode_2126__Condensation_not_possible_because_T1_GT_T3S_EQ_xs | |
| epErrorCode_2127__Mixing_of_flue_gas_and_cooling_air_failed__FCOOLAIR_EQ_0_used | |
| epErrorCode_2128__FOUT_0_not_possible_for_this_fluid | |
| epErrorCode_2129__FXH2OBN_1_requires_connection_at_pin_7 | |
| epErrorCode_2130__FXH2OBN_1_requires_a_value_between_0_and_1_for_XH2OBN_as_enthalpy_on_pin_7 | |
| epErrorCode_2131__For_FSPECT_2__outlet_humidity_is_calculated_by_sorption_characteristics__Pin_7_useless | |
| epErrorCode_2132__FM_1_requires_connection_at_pin_5 | |
| epErrorCode_2133__Outlet_flow_reduced_to_avoid_falling_below_LEVMIN | |
| epErrorCode_2134__Outlet_flow_reduced_to_avoid_exceeding_LEVMAX | |
| epErrorCode_2135__Exhaust_mass_flow_too_small | |
| epErrorCode_2136__FTYP_available_on_electric_streams_only | |
| epErrorCode_2137__Component_for_solar_data_not_found_VWIND_from_specification_value_used | |
| epErrorCode_2138__Component_for_wind_data_not_found_VWIND_from_specification_value_used | |
| epErrorCode_2139__Numeric_heat_exchange_calculation_algorithm_is_available_for_FALGINST_eq_4_only | |
| epErrorCode_2140__P5_LT_P4 | |
| epErrorCode_2141__P4_LT_P2 | |
| epErrorCode_2142__Error_in_calculation_of_saturation_point | |
| epErrorCode_2143__M5S_out_of_range_0__1 | |
| epErrorCode_2144__Blowdown_flow_must_be_at_least_xs_to_drain_all_salt | |
| epErrorCode_2145__Transient_calculation_not_available_for_saltwater | |
| epErrorCode_2146__No_resistance_at_outlet | |
| epErrorCode_2147__Unrealistic_characteristic_field_FUTERM__specification_value_RINTCELL_used | |
| epErrorCode_2148__Current_transmission_available_on_electrical_pipes_only | |
| epErrorCode_2149__Inaccuracy_of_xs_m_s_in_iteration_for_flow_velocity__consider_manual_setting | |
| epErrorCode_2150__Flow_velocity_could_not_be_determined__please_specify_VEL_SET_manually | |
| epErrorCode_2151__Need_a_valid_N_REF_for_FY_EQ_2 | |
| epErrorCode_2152__Characteristic_fields_yields_xs_at_design_point__Really_use_single_lookup | |
| epErrorCode_2153__The_used_property_set_issued_a_warning_while_determining_exhaust_enthalpy | |
| epErrorCode_2154__Entropy_calculated_from_temperature_instead_of_enthalpy__may_be_wrong_in_two_phase_region | |
| epErrorCode_2155__Volume_calculated_from_temperature_instead_of_enthalpy__may_be_wrong_in_two_phase_region | |
| epErrorCode_2156__Not_enough_oxygen_to_close_balance_for_CO_and_CO2 | |
| epErrorCode_2157__Substance_balance_requires_elementary_C_at_outlet | |
| epErrorCode_2158__Substance_balance_requires_free_O2_at_outlet | |
| epErrorCode_2159__T_would_be_gt_Tmax_of_property_table__P_must_be_lt_xs_bar | |
| epErrorCode_2160__H_calculation_failed__Consider_to_set_H_directly | |
| epErrorCode_2161__Selected_FSUBST_not_available_for_this_FTYP | |
| epErrorCode_2162__Inlet_specific_volume_xs_times_higher_than_outlet_Taking_the_average_for_calculation_of_geodesic_pressure_drop_may_be_inaccurate | |
| epErrorCode_2163__P3_P4_might_be_off_0_1__1_mbar | |
| epErrorCode_2164__Setting_of_Q_requires_setting_of_M_in_the_same_component | |
| epErrorCode_2165__For_M_eq_0_H_cannot_be_determined_from_Q | |
| epErrorCode_2166__Flow_velocity_undefined__vel_eq_0_assumed | |
| epErrorCode_2167__Insufficient_Compressormap_Data_Bypassing | |
| epErrorCode_2168__FY_eq_3_Requires_Port3_connected | |
| epErrorCode_2169__Specifications_cannot_be_met_without_pinchpoint_violation_results_of_numerical_algorithm_are_meaningless | |
| epErrorCode_2170__FPFX_and_FPFZ_are_mutually_exclusive_You_can_only_activate_one_of_them | |
| epErrorCode_2171__Cannot_evaluate_Kernel_Expression_EPFEFF | |
| epErrorCode_2172__Cannot_evaluate_Kernel_Expression_EPFX | |
| epErrorCode_2173__Cannot_evaluate_Kernel_Expression_EPFZ | |
| epErrorCode_2174__The_current_operating_point_is_out_of_the_mapped_performance_curve_range | |
| epErrorCode_2175__Performance_curve_lookup_failed | |
| epErrorCode_2176__Refprop_not_available_in_viewer | |
| epErrorCode_2177__Metallic_Mg_or_Ca_is_specified_as_part_of_the_fuel_and_will_be_oxidized_in_the_combustion__Probably_it_should_be_part_of_the_ash | |
| epErrorCode_2178__Deviation_of_AL12N_from_fluid_specific_database_value_higher_xs_than_WARNLEVAL | |
| epErrorCode_2179__Deviation_of_AL34N_from_fluid_specific_database_value_higher_xs_than_WARNLEVAL | |
| epErrorCode_2180__Data_for_AL12N_AL34N_available_for_each_single_fluid_but_not_for_the_combination__average_values_used | |
| epErrorCode_2181__Data_for_xs_not_available_for_this_fluid__manually_specified_value_used | |
| epErrorCode_2182__AN_too_small_must_be_gt_xs_m2 | |
| epErrorCode_2183__For_FSPECD_EQ_9__FAA_must_be_0_or_1__otherwise_the_specification_is_not_unique | |
| epErrorCode_2184__x1_not_reasonable_for_FTYPHX_eq_x2_W_m2K_used_instead | |
| epErrorCode_2185__Thermal_diffusivity_a_cannot_be_calculated_in_the_wet_steam_region_value_for_vapor_used | |
| epErrorCode_2186__Calling_h_of_pt_on_saturation_line_result_h_fluid | |
| epErrorCode_2187__Calling_h_of_pt_on_saturation_line_result_h_gas | |
| epErrorCode_2188__Convergence_target_not_reached_Maximum_deviation_is_x1_in_x2_on_this_line | |
| epErrorCode_2189__Enthalpy_definition_not_unique_by_xs_because_of_phase_boundary | |
| epErrorCode_2190__CDS_solution_instable_numeric_scheme_set_to_Upwind | |
| epErrorCode_2191__Temperature_below_minimum_temperature_of_property_table | |
| epErrorCode_2192__Maximum_temperature_of_property_table_exceeded | |
| epErrorCode_2193__Requested_NOX_flow_too_high__NOX_set_to_0 | |
| epErrorCode_2194__The_recursion_leaves_an_inaccuracy_of_the_NOX_fraction_of_xs_ppm | |
| epErrorCode_2195__Different_zero_points_for_NCV__FSPECNCV_eq_3_recommended | |
| epErrorCode_2196__For_universalfluid_FTYP_42_can_be_used_only_with_FNORMW_eq_FNORMO2_eq_0 | |
| epErrorCode_2197__Specified_NCV_not_used_because_of_FSPECNCV_eq_0 | |
| epErrorCode_2198__NCV_calculation_not_possible__specification_value_NCV_used | |
| epErrorCode_2199__Fluid_conversion_ambiguous | |
| epErrorCode_2200__General | |
| epErrorCode_2201__PTH_Definition | |
| epErrorCode_2202__MissingMassFlow | |
| epErrorCode_2203__MissingPressure | |
| epErrorCode_2204__MissingEnthalpy | |
| epErrorCode_2205__OverdeterminationInMassFlow | |
| epErrorCode_2206__OverdeterminationInPressure | |
| epErrorCode_2207__OverdeterminationInEnthalpy | |
| epErrorCode_2208__OpenPipes | |
| epErrorCode_2209__NegativeMassFlow | |
| epErrorCode_2210__NegativePressure | |
| epErrorCode_2211__NegativeEnthalpy | |
| epErrorCode_2212__Component | |
| epErrorCode_2213__LowerPrecisionInMassFlow | |
| epErrorCode_2214__LowerPrecisionInPressure | |
| epErrorCode_2215__LowerPrecisionInEnthalpy | |
| epErrorCode_2216__ExpressionCouldNotBeEvaluated | |
| epErrorCode_2217__NoLicenseForGasTurbineMacrosAvailable | |
| epErrorCode_2218__ValidationForMassFlow | |
| epErrorCode_2219__ValidationForPressure | |
| epErrorCode_2220__ValidationForEnthalpy | |
| epErrorCode_2221__GeneralPipe | |
| epErrorCode_2222__MissingNCV | |
| epErrorCode_2223__OverdeterminationInNCV | |
| epErrorCode_2224__ValidationForNCV | |
| epErrorCode_2225__MissingMaterialComposition | |
| epErrorCode_2226__OverdeterminationInMaterialComposition | |
| epErrorCode_2227__ValidationForMaterialComposition | |
| epErrorCode_2228__MaximalCalculationTimeExceeded | |
| epErrorCode_2229__SingularMatrixInValidation | |
| epErrorCode_2230__NearlySingularMatrixInValidation | |
| epErrorCode_2231__TopologyLogicPipeCycle | |
| epErrorCode_2232__TopologyLogicPipeAmbiguity | |
| epErrorCode_2233__PipeSetToNotCalculate | |
| epErrorCode_2234__OverdeterminationInFrequency | |
| epErrorCode_2235__OverdeterminationInVoltage | |
| epErrorCode_2236__OverdeterminationInPower | |
| epErrorCode_2237__OverdeterminationInPhase | |
| epErrorCode_2238__MissingFrequency | |
| epErrorCode_2239__MissingVoltage | |
| epErrorCode_2240__MissingPower | |
| epErrorCode_2241__MissingPhase | |
| epErrorCode_2242__user_message_from_ebsscript | |
| epErrorCode_2243__user_message_from_xui_dll | |
| epErrorCode_2244__ebsscript_exit_code_greater_zero | |
| epErrorCode_2245__error_running_ebsscript | |
| epErrorCode_2246__error_compiling_ebsscript | |
| epErrorCode_2247__massflow_at_unconnected_pin_1 | |
| epErrorCode_2248__Error_calculating_NCV__FSPECNCV_eq_3_not_usable | |
| epErrorCode_2249__NCV2_was_calculated_from_composition_because_FSPECNCV_eq_2_leads_to_NCV2_eq_0__If_you_really_want_to_set_NCV2_eq_0__use_FSPECNCV_eq_1 | |
| epErrorCode_2250__Phase_equilibrium_not_correct__At_least_one_component_below_TMIN_for_the_corresponding_phase | |
| epErrorCode_2251__Phase_equilibrium_not_correct__At_least_one_component_above_TMAX_for_the_corresponding_phase | |
| epErrorCode_2252__The_current_operating_point_is_near_the_surge_limit | |
| epErrorCode_2253__The_corrected_speed_is_outside_the_compressor_map | |
| epErrorCode_2254__The_selected_input_is_outside_the_compressor_map | |
| epErrorCode_2255__Speed_of_sound_could_not_be_calculated | |
| epErrorCode_2256__NCV_at_inlet_does_not_match_to_composition_and_is_ignored | |
| epErrorCode_2257__Fuel_inlet_is_not_connected | |
| epErrorCode_2258__Iteration_for_P_FSH_not_completed | |
| epErrorCode_2259__Iteration_for_T_FSH_not_completed | |
| epErrorCode_2260__Iteration_for_H_FTS_not_completed | |
| epErrorCode_2261__If_pin_4_is_not_connected_FSPEC_eq_xs_cannot_be_used | |
| epErrorCode_2262__Calculated_specification_design_data_not_taken_over | |
| epErrorCode_2263__Design_of_heat_exchanger_not_possible_because_T4_LE_T1 | |
| epErrorCode_2264__Design_of_heat_exchanger_not_possible_because_T2_GE_T3 | |
| epErrorCode_2265__Internal_iteration_for_DTM_reached_x1_K_in_x2_steps | |
| epErrorCode_2266__If_pin_4_is_not_connected_FT4_eq_1_cannot_be_used | |
| epErrorCode_2267__If_pin_10_is_not_connected_FT10_eq_1_cannot_be_used | |
| epErrorCode_2268__REFIN_could_not_be_used | |
| epErrorCode_2269__Maximum_heat_transfer_limited_by_property_table_boundaries__effectiveness_method_not_suitable | |
| epErrorCode_2270__Frequency_setting_not_possible_on_this_stream_type | |
| epErrorCode_2271__Voltage_setting_not_possible_on_this_stream_type | |
| epErrorCode_2272__Electric_current_setting_not_possible_on_this_stream_type | |
| epErrorCode_2273__Stream_contains_non_gaseous_fractions__Their_influence_on_the_pressure_drop_is_neglected | |
| epErrorCode_2274__Mass_balance_violated_xs | |
| epErrorCode_2275__Mismatch_of_gas_formulations__type_of_main_inlet_used_at_outlet | |
| epErrorCode_2276__Mismatch_of_water_steam_formulations__default_value_iapws_if97_used_at_outlet | |
| epErrorCode_2277__Shaft_outlet_not_connected | |
| epErrorCode_2278__Freezing_pressure_gt_PMAX_eq_x1_bar_reached_at_x2_GrdC | |
| epErrorCode_2279__Cannot_perform_Design_Run_with_Zero_Flow | |
| epErrorCode_2280__Upper_enthalpy_limit_from_model_options_reached | |
| epErrorCode_2281__Lower_enthalpy_limit_from_model_options_reached | |
| epErrorCode_2282__P_setting_restricted_to_x1_bar | |
| epErrorCode_2283__H_setting_restricted_to_x1_kJ_kg | |
| epErrorCode_2284__Upper_pressure_limit_from_model_options_reached | |
| epErrorCode_2285__Lower_pressure_limit_from_model_options_reached | |
| epErrorCode_2286__Due_to_TMIN_xs_C_in_the_property_table_H_setting_not_possible_H_was_set_to_HMIN | |
| epErrorCode_2287__Due_to_TMAX_xs_C_in_the_property_table_H_setting_not_possible_H_was_set_to_HMAX | |
| epErrorCode_2288__HEI_6_method_is_valid_only_for_5CltT1lt40C | |
| epErrorCode_2289__Component_contains_a_hidden_voltage_specification | |
| epErrorCode_2290__Component_contains_a_hidden_frequency_specification_which_may_interfere_with_a_mass_flow_setting | |
| epErrorCode_2291__Component_contains_a_hidden_voltage_specification_which_may_interfere_with_a_pressure_setting | |
| epErrorCode_2292__Component_contains_a_hidden_electric_current_specification_which_may_interfere_with_an_enthalpy_setting | |
| epErrorCode_2293__Contradicting_specifications_for_the_enthalpy | |
| epErrorCode_2294__Desired_pressure_condenser_mode_temperature_cooler_mode_could_not_be_met_size_too_big | |
| epErrorCode_2295__Desired_pressure_condenser_mode_temperature_cooler_mode_could_not_be_met_clf_not_found | |
| epErrorCode_2296__Desired_pressure_condenser_mode_temperature_cooler_mode_could_not_be_met_fanspeed_not_found | |
| epErrorCode_2297__Salinity_in_the_liquid_phase_x1_exceeds_XIMAX_eq_x2 | |
| epErrorCode_2298__Complete_evaporation_of_salt_water_leaves_solid_salt_behind__which_is_neglected_in_the_calculation | |
| epErrorCode_2299__Too_many_components_in_material_composition | |
| epErrorCode_2300__Unable_to_reach_the_desired_value_of_RXH2OB | |
| epErrorCode_2301__Elemental_analysis_not_available_for_this_stream | |
| epErrorCode_2302__Phase_fraction_cannot_be_determined | |
| epErrorCode_2303__Specification_value_REV_different_from_shaft_speed__For_the_transformation_of_the_reduced_mass_flow__the_shaft_speed_is_used_now | |
| epErrorCode_2304__Component_calculation_unsuccessful | |
| epErrorCode_2305__Error_ocurred_calculating_components | |
| epErrorCode_2306__Ash_extraction_at_port_5_must_be_connected_or_RFLAS_set_to_1 | |
| epErrorCode_2307__Speed_is_supersonic | |
| epErrorCode_2308__Configurations_square_channel_inside_tube_outside_are_not_implemented | |
| epErrorCode_2309__Fluid_contains_substances_with_non_fdbr_elements | |
| epErrorCode_2310__Fluid_contains_substances_with_unknown_composition | |
| epErrorCode_2311__Setting_of_2phase_index_0_ignored | |
| epErrorCode_2312__Setting_of_invalid_binary_mixture_type_ignored | |
| epErrorCode_2313__pcm_parse_error_pcm_general_error | |
| epErrorCode_2314__pcm_parse_error_wrong_variable_type_for_property_assignment | |
| epErrorCode_2315__pcm_parse_error_unsupported_variable_type | |
| epErrorCode_2316__pcm_parse_error_too_many_values_for_array | |
| epErrorCode_2317__pcm_parse_error_unsupported_region_for_region_polynomial | |
| epErrorCode_2318__pcm_parse_error_unsupported_pcm_function_type | |
| epErrorCode_2319__pcm_parse_error_substance_property_not_available | |
| epErrorCode_2320__pcm_parse_error_property_not_defined_as_json_object | |
| epErrorCode_2321__pcm_parse_error_property_not_defined_as_array | |
| epErrorCode_2322__pcm_parse_error_property_not_defined_as_primitive_variable_type | |
| epErrorCode_2323__pcm_parse_error_wrong_parenthesis | |
| epErrorCode_2324__pcm_parse_error_one_level_of_array_missing | |
| epErrorCode_2325__pcm_parse_error_json_syntax_error | |
| epErrorCode_2326__pcm_parse_error_missing_properties | |
| epErrorCode_2327__pcm_parse_error_property_already_defined | |
| epErrorCode_2328__pcm_parse_error_piecewise_polynomial_not_in_ascending_order | |
| epErrorCode_2329__pcm_parse_error_t_max_le_than_t_min | |
| epErrorCode_2330__pcm_parse_error_piecewise_polynomials_dont_cover_temp_range | |
| epErrorCode_2331__pcm_parse_error_t_trans_upper_less_than_t_trans_lower | |
| epErrorCode_2332__pcm_parse_error_expression_parsing_failed | |
| epErrorCode_2333__FDEGRADATION_settings_require_Characteristic_CDEGRADATION | |
| epErrorCode_2334__Cannot_evaluate_Kernel_Expression_EDEGRADATION | |
| epErrorCode_2335__FCURRENT_EQ_1_requires_port_8_connected | |
| epErrorCode_2336__FLOSSES_is_out_of_range | |
| epErrorCode_2337__PEM_electrolysis_expects_liquid_water_at_operating_conditions | |
| epErrorCode_2338__Current_is_limited_by_air_flow | |
| epErrorCode_2339__Current_is_limited_by_fuel_flow | |
| epErrorCode_2340__Current_is_limited_by_water_flow | |
| epErrorCode_2341__FLOSSES_EQ_0_seleted_CUI_curve_should_be_falling_for_fuel_cell | |
| epErrorCode_2342__FLOSSES_EQ_0_seleted_CUI_curve_should_be_rising_for_electrolysis_cell | |
| epErrorCode_2343__The_Settings_of_FGSOD_require_Logic_Port_11_to_be_connected_and_the_value_of_ODVPNT_to_be_written_to_P_of_this_stream | |
| epErrorCode_2344__The_valve_point_from_the_logic_line_P11_is_out_of_range | |
| epErrorCode_2345__The_Logic_Line_lookup_at_M11_resulted_in_a_negative_value_for_PFFLOW | |
| epErrorCode_2346__The_Logic_Line_lookup_at_H11_resulted_in_a_negative_value_for_PFETA | |
| epErrorCode_2347__Duplicate_wind_data_index_IWDATA_xs | |
| epErrorCode_2348__pcm_parse_error_region_polynomial_not_supported | |
| epErrorCode_2349__pcm_parse_error_calculation_of_tanh_coeffs_failed | |
| epErrorCode_2350__The_cooling_port_port_13_must_be_connected_when_having_a_cooling_duty_2 | |
| epErrorCode_2351__the_specified_phi_value_leads_to_a_number_of_pcm_balls_less_than_one | |
| epErrorCode_2352__the_specified_nballs_value_leads_to_a_value_of_phi_less_than_theor_limit | |
| epErrorCode_2353__for_pcm_in_balls_nflow_is_always_set_to_one | |
| epErrorCode_2354__Condenser_unable_to_set_condenser_pressure_because_it_is_set_by_another_component | |
| epErrorCode_2355__NASA_and_non_NASA_lines_cannot_be_used_simultaneously_at_the_reactor_inputs | |
| epErrorCode_2356__Calculated_specification_design_data_1_not_taken_over_due_to_expression_for_2 | |
| epErrorCode_2357__Calculated_gas_outlet_temperatureis_too_low__Check_your_temperature_and_heat_loss_settings | |
| epErrorCode_2358__Cannot_evaluate_Kernel_Expression_xs | |
| epErrorCode_2359__FGASN_2_REQUIRES_LOGIC_PORT_9_INPUT_H | |
| epErrorCode_2360__Cannot_evaluate_characteristic_xs_reference_lookup_is_zero | |
| epErrorCode_2361__Missing_C_or_H_in_tar_xs | |
| epErrorCode_2362__Calculation_of_static_quantities_not_available_for_this_stream_type | |
| epErrorCode_2363__Internal_iteration_for_PSTAT_not_converged | |
| epErrorCode_2364__collector_bar_component_requires_connection_on_port_x1 | |
| epErrorCode_2365__Missing_internal_start_value_required_for_line_x1 | |
| epErrorCode_2366__PSTAT_SET_was_used_for_PTOT_instead_of_PSTAT | |
| epErrorCode_2367__THE_GIVEN_CHO_RATIOS_INDICATE_SOOT_FORMATION_FOR_THE_GIVEN_P_TREACT | |
| epErrorCode_2368__THE_GIVEN_CHO_RATIOS_INDICATE_TOO_MUCH_OXYGEN_COMBUSTION_TAKES_PLACE | |
| epErrorCode_2369__Setting_of_normalized_volume_flow_failed | |
| epErrorCode_2370__Setting_FNORMW_eq_1_ignored | |
| epErrorCode_2371__Cannot_evaluate_Matrix_xs | |
| epErrorCode_2372__Ideal_gas_approximation_might_be_inaccurate__real_gas_factor_is_x1 | |
| epErrorCode_2373__Viscosity_only_available_in_liquid_phase_region | |
| epErrorCode_2374__Valid_range_is_10_le_X_le_11 | |
| epErrorCode_2375__Calculation_of_HTX_failed | |
| epErrorCode_2376__Calculation_of_SPX_failed | |
| epErrorCode_2377__Calculation_of_STX_failed | |
| epErrorCode_2378__AEN_Pressure_calculations_failed | |
| epErrorCode_2379__Negative_entropy_production_second_low_violation | |
| epErrorCode_2380__Unable_to_reach_the_desired_outlet_temperature_due_to_performance_factor_limit_value_violation_of_x_ | |
| epErrorCode_2381__for_pcm_in_balls_only_fconf_eq_one_is_possible | |
| epErrorCode_2382__PHS_call_failed_P_calculated_iteratively | |
| epErrorCode_2383__Internal_iteration_for_PSH_did_not_converge | |
| epErrorCode_2384__When_using_M3MAX__M4_is_used_as_a_constant_instead_of_a_variable__i_e__the_splitting_ratio_is_not_validated | |
| epErrorCode_2385__When_solids_are_present_FSOLID_eq_0_should_be_used_for_display_only_FFU_eq_0_Usage_of_FTYP_eq_22_recommended | |
| epErrorCode_2386__HCl_in_fluegas_quite_high__Be_aware_that_only_chemical_active_Cl_may_be_specified_as_elementary_Cl__Inactive_Cl_ions_must_be_included_in_the_ash | |
| epErrorCode_2387__Requested_enthalpy_lt_hmin_of_property_table | |
| epErrorCode_2388__ASET_too_small__speed_of_sound_reached_at_xs_m2 | |
| epErrorCode_2389__DSET_too_small__speed_of_sound_reached_at_xs_m | |
| epErrorCode_2390__pcm_parse_error_t_freeze_less_than_t_melt | |
| epErrorCode_2391__volume_reduced_by_liquid_water_at_norm_conditions | |
| epErrorCode_2392__xs_out_of_range_value_limited | |
| epErrorCode_2393__Result_values_RE_PR_and_NU_are_undefined_in_the_2phase_region | |
| epErrorCode_2394__Specific_heat_capacity_not_defined_in_the_2_phase_region | |
| epErrorCode_2395__Duplicate_X_Entries_Y_xs_Z_YX_Fails | |
| epErrorCode_2396__Z_NotMonotonic_for_Y_xs_X_YZ_Fails | |
| epErrorCode_2397__MalformedMapData_MultipleExtremaDetected_ForY_xs_ | |
| epErrorCode_2398__Map_contains_duplicate_rows_xs_Please_clean_up_data | |
| epErrorCode_2399__Heat_exchanger_EFF_gt_0999999_may_lead_to_numeric_problems | |
| epErrorCode_2400__xs_kW_leaving_through_unconnected_pin_3 | |
| epErrorCode_2401__Z_cannot_be_calculated_due_to_solid_state_fractions | |
| epErrorCode_2402__Solid_state_fractions_are_neglected_in_the_calculation_of_Z | |
| epErrorCode_2403__FALG_1_available_only_for_geometry_based_approach_FHEI_20_FALG_internally_set_to_0 | |
| epErrorCode_2404__XIL_LT_XIMIN_for_TCRYST | |
| epErrorCode_2405__XIL_LT_XIMIN_for_PCRYST | |
| epErrorCode_2406__Air_Port_1_not_connected | |
| epErrorCode_2407__Outlet_Port_2_not_connected | |
| epErrorCode_2408__At_Least_One_Fuel_Port_must_be_connected_with_flow | |
| epErrorCode_2409__Temperature_below_triple_point__liquid_phase_not_existing | |
| epErrorCode_2410__Required_pressure_gt_pmax_of_property_table | |
| epErrorCode_2411__Desired_Flow_direction_does_not_match_imposed_differential_pressure | |
| epErrorCode_2412__FXOH2_settings_require_Characteristic_CXOH2 | |
| epErrorCode_2413__Cannot_evaluate_Kernel_Expression_EXOH2 | |
| epErrorCode_2414__FXOO2_settings_require_Characteristic_CXOO2 | |
| epErrorCode_2415__Cannot_evaluate_Kernel_Expression_EXOO2 | |
| epErrorCode_2416__Connection_to_component_xs_missing_at_inlet | |
| epErrorCode_2417__No_result_data_available_maybe_component_is_not_switched_to_calculate_results_in_each_iteration_step | |
| epErrorCode_2418__Mass_balance_violation_caused_by_mass_flow_specified_at_PIN_xs | |
| epErrorCode_2419__Internal_pinch_point_of_xs_due_to_numeric_instabilities_Upwind_scheme_FNUMSC_eq_0_recommended | |
| epErrorCode_2420__Saturation_temperature_cannot_be_determined_for_that_fluid_FT_eq_3_used | |
| epErrorCode_2421__TheCurrentOperatingPointBringsYoutOfTheMappedRange | |
| epErrorCode_2422__TheISOlinesOfTheMapAreNotMovingMonotonicallyWithyY | |
| epErrorCode_2423__TheCurrentOperatingPointHasMultipleSolutionsInY | |
| epErrorCode_2424__NoSolutionFoundForTheCurrentOperatingPointAndFMODEYXZ | |
| epErrorCode_2425__pcm_parse_error_pcm_schema_validation_error | |
| epErrorCode_2426__pcm_parse_error_t_not_monotonically_increasing | |
| epErrorCode_2427__No_CP_data_in_dataset_Temperature_dependent_HPSetc_cannot_be_calculated | |
| epErrorCode_2428__At_least_one_component_has_TMAX_xs_which_is_LT__actual_T_xs_in_the_property_table | |
| epErrorCode_2429__At_least_one_component_has_TMIN_xs_which_is_GT__actual_T_xs_in_the_property_table | |
| epErrorCode_2430__No_composition_given | |
| epErrorCode_2431__Inconsistency_of_xs_kJ_kg_between_H_PT_and_T_PH__Temperature_is_probably_inaccurate | |
| epErrorCode_2432__ExpressionRecursevilyDependent | |
| epErrorCode_2433__Geodesic_height_not_defined__Use_FFILL_0_and_FLEV_0_or_FLEV_1_instead | |
| epErrorCode_2434__Uncertainty_in_Joule_Thomson_effect_due_to_high_non_linearity | |
| epErrorCode_2435__Controller_switched_off_due_to_problems_with_temperature_calculation | |
| epErrorCode_2436__Heat_loss_area_not_defined__Use_FFILL_0_and_FLEV_0_or_FLEV_1_instead | |
| epErrorCode_2437__Compression_factor_z_not_available_in_the_2_phase_region | |
| epErrorCode_2438__H_gt_H_Tmax_T_cannot_be_calculated | |
| epErrorCode_2439__H_lt_H_Tmin_T_cannot_be_calculated | |
| epErrorCode_2440__H1_gt_H_Tmax_As_Tmax_is_used_for_the_outlets_xs_kW_are_lost | |
| epErrorCode_2441__H1_lt_H_Tmin_As_Tmin_is_used_for_the_outlets_xs_kW_are_missing |
Namespace: EbsOpen
Assembly: EbsOpen (in ebs2000.exe)