Change List PS
List of improvements included in this service pack
Defect | Description |
20083 | 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 |