Change List PS
List of improvements included in this service pack
| Defect | Description |
| 20894 | CHP Fired process heater - consistency errors |
| 20478 | KPI Utility - Issue when deleting KPIs |
| 20442 | Nonsense "Mass Flow" variable gets added when meter is created |
| 20257 | Crash when deleting ammonia in Esso Tabular |
| 20237 | Case solves infinitely due to spreadsheet |
| 20234 | Crash in lab analysis when moving Petro-SIM to another monitor |
| 20225 | Spreadsheet crash loading Unisim XML |
| 20202 | Crash on save, after deleting a stream |
| 20199 | Crash building workbook |
| 20162 | Petro-SIM LPU export formula issue |
| 20161 | Faraday efficiency is not affecting the H2 production as it should |
| 20150 | Base delta op crash due to bad memory access when options are changed |
| 20114 | CNHTR-SIM crashed when feed's RON is empty |
| 20064 | Crash on LP Utility when generating data |
| 20024 | Petro-SIM crashes when validating distillation curves after historian read |
| 20005 | Petro-SIM Database Save Issue |
| 19967 | ISOM case crashes because of unhandled uninitialized index catalyst weight |
| 19825 | Air Cooler: Rating mode not calculating Air Heat Transfer Coefficient |
| 19801 | Applying initial conditions in large refinery cases causes issues |
| 19706 | FCC-SIM: Hysteresis during solving leads to unconverged cases |
| 19021 | Negative flue gas temperatures in the fired heater |
| 20441 | CopyCalcParamToInput unexpectedly fails when "Mass Flow" is specified in reactor meter |
| 20353 | XSimOp Exchanger returns the wrong tube count after resolve |
| 20284 | Fired Heater in Dynamic - drastic increase in Flue Gas Temp after cutting flow |
| 20261 | Synthesis templates do not work in the base delta unit operation |
| 20176 | Component fractions incorrectly passed to synthesis from base-delta op |
| 20168 | Heater cooler duties are not updated when temperature spec is used |
| 20160 | Reversible voltage discontinuity using Peng-Robinson |
| 20122 | Reporting Workbook: "load selected case" opens Base case but not pull any new data from Excel |
| 20117 | CNHTR-SIM mishandles the H2 balance when light ends in liquid feed get shifted to once-through gas feed |
| 20113 | Heat exchanger worksheet displays incorrect components |
| 20077 | Wrong XL WB behavior of "Load Selected Case" for a Primed Prediction |
| 20066 | Screen Resolution and Scaling - Detaching windows |
| 20036 | HXX: rn arrays (core properties) do not update if feed core properties characterized as 0.0 |
| 20003 | Distop calibration: Synthesize box unchecked when minus status removed from stream |
| 20002 | Distop calibration: Auto-setup incorrectly classifying feeds as minus streams |
| 19999 | Network solver does not solve with feed pressure not known |
| 19995 | The model is complaining about empty Co, Co2 and H2O flash factor but they don“t exist in the reactor inlet streams |
| 19983 | Base Variable disconnects |
| 19953 | GetObjectXML strips attachments when told provide them |
| 19941 | EBR-SIM generates bogus result of negative equilibrium PV and Expanded Bed PV when catalyst makeup rate is unrealistically low |
| 19940 | DHTR ULSD targeting bottoms S generates misleading error message because the case is operating on the other side of equilibrium |
| 19928 | Basis Environment: It does not allow to exit the environment if Basis-1 does not have property package defined |
| 19834 | Excel Scenarios: Copying a scenario does not copy the Mode properly |
| 19820 | Increasing the reactor temperature, a discontinuity in the aromatics is observed |
| 19721 | ULSD bottoms sulfur target fails even though iteratively running with temperature target can actually reach the solution |
| 18846 | Distop not able to find Calc. Duty property properly to report in LPU |
| 18584 | 2 liquid phases causing inconsistency |
| 18461 | DC-SIM: AntiFoam Effectiveness Factor not working as expected |
| 14621 | LP Utility Help improvements: Data Generation - LP tag: Feed Type |
| 20894 | New ULSD Catalyst Deactivation Mechanism" does not work with once-through gas mode |
| 20504 | Amines TP flash calculation fails |
| 21101 | BP Curve utility discrepancies |
| 21083 | Crash on a VDU column on Essar (UK) case |
| 21023 | Strip charts and icons stop painting and simulator becomes unresponsive |
| 20864 | DHTR Isomerization: Isoparaffins in feed not characterized by model |
| 20712 | Distillation column Range Specs: Connecting lower and upper limit to spreadsheet and using formula triggers infinite loop |
| 20586 | FCC-SIM Crash - RI override undo |
| 20526 | Spreadsheet: When opening a case from v7.2 the values in the spreadsheet are incorrect |
| 20197 | Paste Objects from file Crash when selecting pasted objects to use default fluid package |
| 21487 | Average Deactivation Rate needs to be tagged as tuning factors for PTP to populate the list |
| 21119 | The embedded BD op in the FCC ist handling the multi-base table |
| 21079 | Balance only throwing inconsistency error on resolve |
| 21078 | Propagation of property methods to correlations |
| 21070 | Database historian does not recognize DSN connections |
| 21067 | Explorer not showing sub-folders when parent folder contains a case |
| 21065 | Pump: The option Enable NPSH curves does not work in PS v7.4 SP ONE |
| 21048 | Workbook does not allow selection or copy when transposed |
| 21039 | installer - demo32.exe |
| 21001 | Component splitter calibration fails |
| 20988 | Importing XML with rotated object causes the selection area to be wrong |
| 20956 | HX: Geometry Screening and Optimization does not allow to select small OD |
| 20926 | CNHTR diolefin/deS (2RX) Cracking Override does not work for R2 |
| 20913 | Issues specifying case range for chart pages |
| 20911 | Unable to delete chart pages from chart manager |
| 20903 | Streams: If a value is being exported from a spreadsheet to a stream it does not appear listed in the attachment tab |
| 20887 | H&MB templates - issue with regional number formats |
| 20883 | Base delta op is not mapping the dViscosity property in the assay adjuster to the stream viscosity properly |
| 20882 | New Quench Setup Option unable to calculate R2 B1 HXQ when R2 TG rate is positive (calibration) |
| 20873 | Transfer function does not work correctly |
| 20841 | LP Utility: Calculated variables can be sent as Manipulated variables from Assay Adjuster worksheet page |
| 20838 | Spreadsheet regional formula problem |
| 20836 | Add RON and MON values for Methanol and Ethanol in the pure component database |
| 20775 | 3 phase separator doesn't solve |
| 20613 | CHP Fired Process Heater - Radiant losses not calculating |
| 20568 | Calibration Env > Data Tab > Active Data (view): Every time new data is added in synthesis meter, PS switch to Column subflowsheet meters |
| 20417 | Steam Ejector needs better zero flow handling |
| 20389 | Error in the effluent curve plot in a DHTR-SIM Renewables model |
| 20380 | Heat Exchanger: PFD Table mistaking Wall Temperatures at inlet and outlet |
| 20364 | Not possible to change from Simulation rating mode to Calculate Fouling on a HX |
| 20351 | Petro-SIM erases customized Property Table |
| 20322 | Pipe Profile page in the Help File should include more details |
| 20307 | Issues with the scalling of the icons |
| 20242 | Enter motion down |
| 20057 | Screen Resolution and Scaling - Detaching windows and change fonts |
| 19121 | Csb Factor Method not showing warning |
| 18089 | Coker Furnace: Increase the severity of Feed not defined from Warning to Error |
| 15821 | Component Splitter failed to calibrate because the Calib App is not smart enough |
| 12010 | Orpic Aromizer model |
| 11252 | Dynamic Depressurisation - Subcritical Flow |
| 21063 | Shell-and-Tube Exchanger Behavior |
| 20816 | Spreadsheet object changes the # of displayed decimals |