哪位好人共享一下proII8.3呀！

nokiae50

哪位好人共享一下proII8.3呀！

gjj0503

强烈赞成，急需8.3的版本，望拥有者迅速上传

mahoupao.com

没有破解的话，有了也只有40days啊，8.2都没。。。

逍遥居士

已经有人上传，自己在论坛搜索一下就可以啦！

Horse

没有破解的话，有了也只有40days啊，8.2都没。。。
mahoupao.com 发表于 2009-10-10 21:12

                               
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8.2版本在ftp里面有一个，不过似乎是没有破解的，，，我没有安装测试过

gjj0503

4# 逍遥居士 你说的是8.2 版本吧

imeagor

支持8.3上传，个人觉得8.3可以用8.2的许可文件的，所以这个不用担心

gjj0503

8.2的破解，可以直接采用8.3的啊

TOMMORROW

都蹦到8.3版本了，呵呵，真快啊
我现在还在用的是8.0版本的

Horse

没看到8.3的版本，，ftp里面有8.2版本。。。

lg888

*  Product Upgrades for v8.3.1 (patch 1)  *
*******************************************

1. RATEFRAC now supports electrolyte thermodynamics for equilibrium and non
   equilibrium systems.  To use RATEFRAC with electrolytes, v7.0 OLI chemistry
   models must be used.  RATEFRAC/Electrolytes support both the OLI aqueous
   model and also the newer MSE model.  Within PRO/II, supplied models created
   in OLI v7.0 end with the characters 70.  Built in model SW0170 is created
   using OLI v7.0 and SW0166 is created using OLI v6.6.  Only models created
   in 7.0 can be used in RATEFRAC. Users creating their own models should
   use Chem Wizard 2 or Chem Wizard 3 to create compatible v7.0 models.


   The OLI aqueous model requires that the water mole fraction be greater than
   0.6 on every stage or packed column segment.  The newer MSE model  
   allows the water mole fraction to vary from 0 to 1.  However, OLI is still
   regressing data for the newer MSE model, and some components are not yet
   available.  In particular, amines are not yet available using the MSE model.

   Note that RATEFRAC supports both equilibrium and non-equilibrium stages.  
   Therefore RATEFRAC provides an alternative algorithm to Eldist for solving
   electrolytic distillation models.

   RATEFRAC/Electrolytes for non equilibrium systems requires transport
   properties. At the current time, OLI provides rigorous liquid viscosity
   for electrolyte   systems, but not surface tension or liquid thermal
   conductivity.  OLI does provide diffusion coefficients for electrolyte
   systems.


   RATEFRAC/Electrolytes does not support solid precipitates forming within
   the column.  Chemistry models including solids may be used, but the solid
   reactions and components will be ignored by RATEFRAC.

   Following are the rules for transport property usage within PRO/II:
   a) Diffusion Coefficients
      The OLI supplied diffusion coefficients are always used. No other option
      is available.

   b) Liquid Viscosity
      By default, the OLI viscosity is used.  Alternatively, the user can
      select a PRO/II method such as library.  In this case, the apparent mole
      fractions will be used with the apparent mole fractions to calculate the
      viscosity.  Note that the OLI method takes into account the true species
      composition (ions and neutral aqueous species) and is the preferred
      method.

   c) Vapor Viscosity
      By default, water properties are used for the vapor viscosity.  The user
      can select a PRO/II method.  However, OLI adds additional components to
      the model beyond what the user specifies in the OLI Chemistry Wizard,
      and these additional components also require viscosity correlations.

   d) Surface Tension
      Currently OLI does not provide a rigorous surface tension method for
      electrolyte systems.  OLI estimates availability the end of first
      quarter 2010. Currently, RATEFRAC will use water properties for
      surface tension.  The user can also supply the surface tension via
      library correlations based on apparent compositions. Surface tension
      can also be supplied on a tray by tray basis for the tower being
      simulated.

   e) Liquid Thermal Conductivity
      Same rules as surface tension.

   f) Vapor Thermal Conductivity
      Same rules as vapor viscosity

2.  OLI's Chemistry Wizard version 3.0 is included in the PRO/II 8.3.1
    release. This Chemistry Wizard allows users to generate custom
    electrolyte models with three new types of components: Assay, Pseudo and
    Inert Solids. By default the Assay and Pseudo components invoke the
    "Second Liquid" phase calculations. This option works well for modeling
    desalters with flash drums, but for column modeling we suggest turning
    off the "Second Liquid" phase calculations.
     
    The Assay curve input requires a minimum of 5 percent / boiling point
    temperature data pairs that must be in ascending temperature order. The
    Assay curve calculations generate a list of assay cut components named by
    boiling point temperature and a component with the assay name. The
    component with the assay name can be given a flow rate using the
    normal PRO/II Stream Data Entry Window and the OLI calculation engine
    will distribute that flow rate over the list of assay cuts.

    The Inert Solids are in the Chemistry Wizard "Available Components" Data
    Entry Window. The four new components are "Ash", "Carbon", "Coal" and
    "Coke". OLI provides default density and heat capacity for these
    components and allows user overrides.

Horse

ftp服务器暂时只有8.2版本

banch

吸引大家的眼睛啊

printer

请有proii8。3版本软件迅速上传

abcd

呵呵，也盼望着能传上来啊

hmzhu

感觉现在proII 还不如chemcad

ktjs06

现在一般都是用HYSYS中的参数。
PROII中感觉参数做的一点少！

abcd

13# lg888


楼上的能否不发这样的信息啊，发个软件或者补丁，不好吗？

alexpodsh

*  Product Upgrades for v8.3.2 (patch 2)  *
*******************************************

   ***************************************************************************               
   *  The aqueous flowrates of the iconic species were previously available  *
   *  only in the output report.  The other forms of output reports (SIM4ME  *
   *  Reports, spread sheet tools, SIM4ME Portal) were added to Patch 1 but  *
   *  were overlooked in to patch 1 readme file.                             *      *                                                                         *
   ***************************************************************************

1.  New Adjusted Standard Conditions, Volumes, and Volume Rates
    PRO/II uses different standard conditions for different systems of
    dimensional units. These differences cause a simulation to reach different
    solutions when re-run using a different system of units of measure.  
    Also, support for user-defined standard conditions, volumes, and volume
    rates was limited. These have caused chronic problems for users.
    Version 8.3.2 introduces extensive enhancements to address them.

    • Enhanced user-defined standard conditions separate from and in addition
      to default standard conditions. User-supplied values now constitute new
      "adjusted standard conditions" that apply to liquid as well as vapor.

    • Adjusted standard vapor volumes are computed using vapor density methods
      in thermodynamic METHOD sets. Standard vapor volume still is computed
      using the ideal gas law.

    • Adjusted standard liquid volumes are computed using liquid density
      methods in thermodynamic METHOD sets.
  
    • Standard liquid volumes still are computed at default standard
      conditions, not from user-supplied values.

    • Stream total rates may be specified using the new adjusted standard
      volume rates. Composition, assay, and referencing streams support
      these new options.

    • Unit operations that allow product rate specifications using the new
      adjusted standard volumes include: flash drum, splitter, column,
      controller, MVC, optimizer, and calculator.

    • Calculators also provide new functions to retrieve adjusted standard
      volume rates from streams.
      
      Utility subroutine SRXSTR supports new argument options that change
      total stream rate using the new adjusted standard volume rates.
      DEFINE statements that define calculator parameters can retrieve the
      stream rates using the new adjusted standard volume rates.

    • Upstream unit operations now report Gas/Oil Ratio (GOR) using the new
      adjusted standard rates.

    • Interface subroutines UDENS and DUDENS allow user-added subroutines
      and PDTS applications to calculate density at vapor or liquid adjusted
      standard conditions.

    • New options in stream reports and the Stream Report Writer support the new
      adjusted standard vapor and liquid volume rates. New footnotes
      automatically appear on pages that display these properties.
   
    For a comprehensive introduction to these enhancements, refer to the new
    technical bulletin "Adjusted Standard Conditions & Adjusted Standard Volume
    Rates". It is available in the "Manual" directory where PRO/II installs all
    the other documents.

alexpodsh

*  Product Upgrades for v8.3.2 (patch 2)  *
*******************************************

   ***************************************************************************               
   *  The aqueous flowrates of the iconic species were previously available  *
   *  only in the output report.  The other forms of output reports (SIM4ME  *
   *  Reports, spread sheet tools, SIM4ME Portal) were added to Patch 1 but  *
   *  were overlooked in to patch 1 readme file.                             *      *                                                                         *
   ***************************************************************************

1.  New Adjusted Standard Conditions, Volumes, and Volume Rates
    PRO/II uses different standard conditions for different systems of
    dimensional units. These differences cause a simulation to reach different
    solutions when re-run using a different system of units of measure.  
    Also, support for user-defined standard conditions, volumes, and volume
    rates was limited. These have caused chronic problems for users.
    Version 8.3.2 introduces extensive enhancements to address them.

    • Enhanced user-defined standard conditions separate from and in addition
      to default standard conditions. User-supplied values now constitute new
      "adjusted standard conditions" that apply to liquid as well as vapor.

    • Adjusted standard vapor volumes are computed using vapor density methods
      in thermodynamic METHOD sets. Standard vapor volume still is computed
      using the ideal gas law.

    • Adjusted standard liquid volumes are computed using liquid density
      methods in thermodynamic METHOD sets.
  
    • Standard liquid volumes still are computed at default standard
      conditions, not from user-supplied values.

    • Stream total rates may be specified using the new adjusted standard
      volume rates. Composition, assay, and referencing streams support
      these new options.

    • Unit operations that allow product rate specifications using the new
      adjusted standard volumes include: flash drum, splitter, column,
      controller, MVC, optimizer, and calculator.

    • Calculators also provide new functions to retrieve adjusted standard
      volume rates from streams.
      
      Utility subroutine SRXSTR supports new argument options that change
      total stream rate using the new adjusted standard volume rates.
      DEFINE statements that define calculator parameters can retrieve the
      stream rates using the new adjusted standard volume rates.

    • Upstream unit operations now report Gas/Oil Ratio (GOR) using the new
      adjusted standard rates.

    • Interface subroutines UDENS and DUDENS allow user-added subroutines
      and PDTS applications to calculate density at vapor or liquid adjusted
      standard conditions.

    • New options in stream reports and the Stream Report Writer support the new
      adjusted standard vapor and liquid volume rates. New footnotes
      automatically appear on pages that display these properties.
   
    For a comprehensive introduction to these enhancements, refer to the new
    technical bulletin "Adjusted Standard Conditions & Adjusted Standard Volume
    Rates". It is available in the "Manual" directory where PRO/II installs all
    the other documents.