printer 发表于 2011-6-3 17:40:27

PROII/9.0 PATCH1出来了

**********************************************************
****PRO/IITM v9.0.1(Patch to v9.0)               *****
****SIMSCI-ESSCOR                  Date: May 2011*****
**********************************************************
The following README file contains installation instructions and a
list of changes (problems fixed or features added) that will be
implemented on PRO/II version 9.0 once this Patch is applied.
This patch can be installed over v9.0.
********************************
*How to install this Patch   *
********************************
To install Proii90Patch1.zip:
   1. Make sure you are not running PRO/II simulation.This may
      be verified through Task Manager in Windows 2003, Windows XP,
      VISTA?and Windows 7 operating systems.
   2. To receive this Service Pack, copy and unzip the
      PROII90Patch1.zip file on your system.On more recent OS's,
      the zip file may appear as a folder in which case you can
      proceed directly to step 4.
   3. When prompted, enter the path to the directory where you want
      the files to be unpacked (for example, C:\TEMP\PROII90).
      Important: when you unzip the files, make sure to select the
      "use folder names" option (or equivalent) so that the required
      subdirectory structure is created at the location where the
      file is unzipped.
   4. After the file has been unzipped, go to the directory where
      the files were extracted (for example, C:\TEMP\Proii90)
      then go into the subdirectory "PROII90Patch1".
      Double click on update.exe to begin installing the PRO/II patch.
      This setup will install the PRO/II patch.
      If you did not unzip the folder first, it will take a few
      moments for the computer to respond to your double click as the
      unzipping has to occur first.Do not double click again or you
      will launch a second instance of the install.
   5. Select the "Next" Button on the Welcome Screen and the install starts
      installing the updated modules.
   6. Select the "Finish" button.The Patch will be copied onto your
      hard drive and will automatically begin installing.
   7. When the installation of the PRO/II patch has been completed,
      the following files will be updated on your system:
   
\Proii90\Bin\CapeOpenExec.dll
\Proii90\Bin\LMAccess.dll
\Proii90\Bin\MFLib.dll
\Proii90\Bin\MTOCOCustom.tlb
\Proii90\Bin\MTCppGUI.dll
\Proii90\Bin\MTLib.dll
\Proii90\Bin\MTPointerLink.dll
\Proii90\Bin\MTWrapper.dll
\Proii90\Bin\P2Interface.dll
\Proii90\Bin\P2oledbs.exe
\Proii90\Bin\PESCalcMain.dll
\Proii90\Bin\PESGuiMain.dll
\Proii90\Bin\RATEFRAC.dll
\Proii90\Bin\proii.exe
\Proii90\Bin\ProII_KGTower.exe
\Proii90\Bin\RateFrac.dll
\Proii90\Bin\RGLib.dll
   
\Proii90\Resource\solidsremoval.bin
\Proii90\Resource\thermo.bin
   
\Proii90\System\p2.kgs
\Proii90\System\p2.xsf
\Proii90\System\p2.xvf
\Proii90\System\PROII.sp1
\Proii90\System\PROII.sx1
\Proii90\System\PROII.sx2
\Proii90\System\PROIIDB
\Proii90\System\uomdata_proii.txt
   
\Proii90\System\UnitXML\SOLRemoval.xml
            
\TDM\*.* /s(Some SIM4ME thermo files have been updated)
****************************************************
* Defects corrected in PRO/II v9.0.1 (patch 1)   *
****************************************************
Number   Feature         Description
HIPE#20314 Amsim   Converting a file with an Amsim unit operation from
   8.3 to 9.0, the new .prz works fine but the _v83.prz
    does not contain the required .apj file. The file
    won't run in v8.3 because it lacks the Amsim model.
LFPE#28095 AssayWith Cubic Spline and IF97, recalculating the
    assay breakdown may result in a Bad Pointer
    Starting Address error.
LFPE# 28165 AssayThere is a small error that can be introduced in the
    calculated TBP result when there are multiple
    components that cover exactly or nearly the same
    range.For exmaple, if there are two blends with
    the following:
      CUTPOINTS TBPCUTS=100,800,28/1200,8/1600,4, DEFAULT
      CUTPOINTS TBPCUTS=100,800,28/1200,8/1600,4, BLEND=A
    you may end up with a TBP value (any percent), that
    is not exactly on the line plotted by lv% vs T of any
    of the resulting streams.Most of the points will be
    correct.If the problem shows up, it may have one
    point that is off by 2 degrees or so.On one
    occasion we saw a result that was off by more.
HIPE#20352 Cape Open Cape Open COCO_COUS mixer convert from PROII83 to
    PROII90 gives a crash when there are more than 6 feeds.
HIPE#20372 Cape Open A CAPE-OPEN Property package name having
    embedded space is not supported through keywords.
HIPE#20382 Cape Open    Properties retrieved via Cape Open thermo
    have non-sensical values.These were OK in v8.3.
    Properties affected include density, surface tension,
    thermal conductivity and viscosity.
   
HIPE#20385 Cape OpenFile convert via .com (Say, from Excel) of a file
PRZ   containing Cape Open COCO units fail because the
    relevant .dat file is not containerized in the .prz.
LFPE#27981 Case Study Choose to run Base Case only in Case Study problem
    may result in an error message that the PARAMETER
    'PARAM1', changed during calculations in cycle 1.
    Since cycle 1 is not run, there should have been
    no error message.
LFPE#28076 ColumnThe <Liquid> tag information on the xml file for
    data transfer to FRI's DRP program or Koch-Glitsch
    KGTower reports the Liquid To rather than the Liquid
    From.
   
HIPE#20503 Column    The Ratefrac Electrolyte column crash may crash when
    hydraulics data are present using the built-in SCRU70
    thermo package.Other built in packages, like SOUR
    and MEA are fine.
HIPE#20319 Component User supplied VP data using correlation 20 will be
    incorrect if the parameters are supplied using
    deg R. deg K is OK.
LFPE#28143 ComponentThe critical Pressure for mercury is incorrect
Databank in the PROCESS databank.
LFPE#28096 Compressor The the user-supplied Polytropic Efficiency for a
    compressor does not persist after OKing back to the
    PFD level.
LFPE#28136 Compressor Compressors with primarily vapor, but some liquid
    feed, and VLLE thermo, results in a bad outlet
    condition calculation, even though there is only
    one liquid phase. VLE thermo works correctly.
LFPE#28152 FlashIn one case, the dew point calculation for an all
    water stream using IF97 results in incorrect enthalpy
    near the critical.
HIPE#20285 PFDThe stream icon on the build palette turns red
    (unsatisfied) after a Save As operation. Click
    around the PFD restores it to the correct black
    color.
LFCR#4298 Reaction揇efine?is being ignored in column reaction data
Datafor the Pre-Exponential Factor and resets it to a
   value of 1.0
LFPE#28115 Security Starting PRO/II 9.0 with TokenNet security may
    result in a security error message about the license
    expiration date, even though the license is good.
HIPE#20370 SolidsThe Solid removal unit does not material balance
    when the feed is a solids-only stream.
HIPE#20378 SolidsThe energy balance is not attained for solid removal
    unit operation.
HIPE#20473 SolidsThe Plant Material Balance Table could be in error
    if decant water is present.
LFPE#28105 SolidsSolids Removal adiabatic option does not result
    in the correct temperature in at least one case.
LFPE#27921 SpreadsheetAfter running a file, click on Tools/Spreadsheet
Tools/Stream Properties. At the conclusion of laying
    out the spreadsheet it may crash with a
    p2oledbs.exe application error.
    'The instruction at "0x7c9116f4" reference memory at
    "0x001a4era". The memory could not be "written".'
LFPE#28112 StreamThe Find Stream and Find Unit are not alpha
    sorted in v9.0.
LFPE#28106 Stream   When a Stream Property Table is present and rate
Property in liters/day is requested, the file is exported
Table    to keywords as LIT/DAY for the Stream Report Writer.
    LIT/DAY is not accepted in import. The workaround
    is to change the keyword to L/D.
HIPE#18602 ThermoThe Unifac group breakdown is incorrect for the
    following components:CITRONIC, DC9PHEN, DEAA,
    HYOXCAPR, MALIC, MALONIC, MERPRO, METOXYAC, HNEOC5,
    PYRUVIC.

HIPE#20447 ThermoThe parachor surface tension calculation is incorrect
    for single component flowsheets
LFCR#4208 ThermoThe Unifac group breakdown is incorrect for the
    following components: 1M2PRBZ, 1M3PRBZ, 1M4PRBZ,
    MMSTYR, OMSTRY, 4HSTYREN, IPCH, 2MNON, 4MNON, 5MNON."
LFPE#27975 ThermoUsing GPSA water saturation, if the stream is
    nearly pure in a vapor-liquid mix, adding
    more liquid water decreases the vapor water
    flowrate. This is because there is a cutoff
    concentration for pure-component handling
    (in this one scenario) that is not close enough
    to 1.0.
HIPE#20403 Update InitialUpdating controller the current variable values
Estimates to a stream estimate updates the field to the
    moles/hr value even when the UOM for that field
    is mass/hr.
   
HIPE#20488 User Added   A User Added Subroutines linked with Intel?VF 8
    may not work subroutines because of extraneous
    routines listed in the .sln file.

science_z 发表于 2011-6-3 18:02:15

it's strong!

pl283600780 发表于 2011-6-3 19:00:06

有下载没?{:1106_368:}

hydg17 发表于 2011-6-7 17:24:43

哪里下载嘛

tianfa19 发表于 2011-6-7 18:39:21

最新的吗,和以前有什么区别?

sunflower98 发表于 2011-6-12 20:29:45

在哪些地方有改进?

七月龙城 发表于 2011-6-14 22:29:57

看的都是帖子,有下载没?

ktjs06 发表于 2011-6-15 08:47:58

这些软件更新可真快啊!

chenhaijunsjy 发表于 2011-6-15 08:50:27

期待能下载,求救

无然歆羡 发表于 2011-6-15 08:50:54

求下载啊,求下载

science_z 发表于 2011-6-16 08:35:16

没有下载,发来何用。。。

meiguimi 发表于 2011-6-16 10:10:49

要是有下载就好了,{:soso_e100:}

zh74 发表于 2011-7-31 13:15:21

楼主挣钱呀。。。。。提供个链接吧

xinmu1978 发表于 2012-4-17 09:05:56

到哪下载啊,我现在做的感觉很多数据没有

chenhaijunsjy 发表于 2012-4-17 09:32:53

好心人给出下载附件!

zhdg_zhdg 发表于 2012-4-21 05:39:27

以前使用tdm数据库就没有成功,patch1是不是解决了?

elementzhou 发表于 2012-6-8 10:14:30

好心人在哪里啊


elementzhou于2012-6-8 10:14补充以下内容:
好心人在哪里啊

tianshanxue 发表于 2012-6-11 09:45:14

{:1106_362:}
有下载就更好了

北风与南风 发表于 2012-6-11 18:52:59

PROII 9.1去年就出了,PROII 9.1的patch1也出了。

gzhhzcz 发表于 2012-8-24 22:06:30

发个下载地址呗,谢谢分享了!发251390314@qq.com
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