aspen共沸精馏塔

来源：用户分享时间：2019-03-16 本文由

一世逍遥分享下载这篇文档手机版

说明：文章内容仅供预览，部分内容可能不全，需要完整文档或者需要复制内容，请下载word后使用。下载word有问题请添加微信号:xxxxxx或QQ：xxxxxx 处理（尽可能给您提供完整文档），感谢您的支持与谅解。

MM \FLAVOR \VERSION \DATETIME \Nov 29 08:46:25 2005\MACHINE \startlibrary version1 NumLibs = 1 Built-In NumCats = 9

Mixers/Splitters active

Separators active

Heat Exchangers active Columns active Reactors active

Pressure Changers active

Manipulators active Solids active

User Models active

endlibrary ; 8

>VERSION 0 YT-501 RadFrac Built-In RADFRAC >VERSION 0 YD-501 Decanter Built-In DECANTER >VERSION 0 YT-511 RadFrac Built-In RADFRAC >VERSION 0

YE-500 Heater Built-In HEATER

>VERSION 0 YE-513 Heater Built-In HEATER

>VERSION 0 M1

FSplit Built-In FSPLIT

>VERSION 0 M2

FSplit Built-In FSPLIT

>VERSION 0 M3

FSplit Built-In FSPLIT

? SETUP MAIN ? \\ \RUN-CLASS = FLOWSHEET \\ \\ SIMULATE INTERACTIVE

= NO MOLEFLOW = MOLEFLOW MASSFLOW = MASSFLOW MOLEFRAC = MOLEFRAC MASSFRAC =

MASSFRAC TFFFILE = \VISITED = 1 \\ ? SETUP GLOBAL ? \\ \INSET

= METCBAR \\ \\ \SCLASS = CONVEN \\ ? SETUP DIAGNOSTICS ? ? SETUP

\DESCRIPTION DESCRIPTION = \CUM\

MMLOCAL \\ \\ UNITSET BASESET = MET ( 3 3 3 3 3 3 3 3 3 3 3 7 7 3 3 5 3 3 3 5 3

4 3 3 3 3 1 3 3 3 4 3 7 3 3 3 1 1 4 4 3 3 3 3 3 3 3 3 3 3 3 3 5 3 3 3 3 3 3 3

3 3 3 4 3 3 3 3 3 3 3 3 3 3 5 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3

3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 ) \\ ? SETUP \METCKGCM ? \\

DESCRIPTION DESCRIPTION = \

and CUM\

\\ \\ MMLOCAL \\ \\ UNITSET BASESET = MET ( 3 3 3 3 3 3 3 3 3 3 3 7 7 3 3 5 3 3 3

8 3 4 3 3 3 3 1 3 3 3 4 3 7 3 3 3 3 3 4 4 3 3 3 3 3 3 3 3 3 3 3 3 5 3 3 3 3 3

3 3 3 3 3 4 3 3 3 3 3 3 3 3 3 3 8 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 3 ) \\ ? SETUP \\? \\ DESCRIPTION DESCRIPTION = \and /HR\

\\ \\ MMLOCAL \\ \\ UNITSET BASESET = SI ( 1 1 1 1 1 1 1 1 1 3 3 7 1 1 1 1 1 1 1

5 1 4 1 1 1 1 1 1 1 1 4 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1

1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 4 5 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1

1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 ) \\ ? SETUP \SETUP

\? \\ ACCOUNT USER-NAME = \\\ ? SETUP \? ? SETUP DESCRIPTION ? \\ DESCRIP DESCRIP = ( \\bar, kg/hr, kmol/hr, MMKcal/hr, cum/hr.\\\\Method: None\\\basis for input: Mole\\\\report composition: Mole flow\) \\ ?

DATABANKS ? \\ DATABANKS \\ ? COMPONENTS MAIN ? \\ COMPONENTS CID = H2O ANAME =

H2O OUTNAME = H2O TYPE = CONV DBNAME1 = \= NBA ANAME = C6H12O2-1 OUTNAME = NBA TYPE = CONV DBNAME1 = \ANAME1 = \= CONV DBNAME1 = \ANAME1 = \/ CID = MA ANAME = C3H6O2-3 OUTNAME = MA TYPE = CONV DBNAME1 = \ANAME1 = \/

CID = PX ANAME = C8H10-3 OUTNAME = PX TYPE = CONV DBNAME1 = \ANAME1

= \\\ ? COMPONENTS \GLOBAL ? ? SOLVE ? ? FLOWSHEET GLOBAL

? \\ BLOCK BLKID = \142

M0-1 143 M0-1 139 M0-1 ) OUT = ( 120 M0-1 121 M2-3 ) \\ \\ BLOCK BLKID = \

BLKTYPE = HEATER IN = ( 126 M0-1 ) OUT = ( 140 M0-1 ) \\ \\ BLOCK BLKID

\BLKTYPE = HEATER IN = ( 120 M0-1 ) OUT = ( 138 M0-1 ) \\ \\ BLOCK BLKID = \130

M3-4 131 M1-2 ) \\ \\ BLOCK BLKID = \BLKTYPE = DECANTER IN = ( 138 M0-1

130 M0-1 129 M0-1 ) OUT = ( \BLKID

= M1 BLKTYPE = FSPLIT IN = ( 45 M0-1 ) OUT = ( 45A M0-1 45B M0-1 ) \\ \\ BLOCK

BLKID = M2 BLKTYPE = FSPLIT IN = ( \143 M0-1

) \\ \\ BLOCK BLKID = M3 BLKTYPE = FSPLIT IN = ( \= ( 126

M0-1 139 M0-1 ) \\ \\ \SCLASS = CONVEN \\ ? PROPERTIES MAIN ? \\

GPROPERTIES GBASEOPSET = \-2 \\ ?

PROPERTIES COMPARE ? ? PROPERTIES \= NRTL \\

? PROPERTIES \PROPERTIES

\\\\PARNAME =

\COMPI = \COMPJ = \VALUE = ( \\\

\\\\\\\\

\DIRECTOR

ALLONLY = NONE UNCHOICE = NO TCHOICE = NO GRPCHOICE = NO \\ ? PROPERTIES PARAMETERS BINARY SCALAR \PARAMNAME = HOCETA SETNO = 1 UNITROW = 0 BDBANK = ( \BPVAL

PARAMNAME2 = HOCETA CID1 = H2O CID2 = H2O VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = H2O CID2 = NBA VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = H2O CID2 = HAC VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = H2O CID2 = MA VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2

= HOCETA CID1 = NBA CID2 = H2O VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA

CID1 = NBA CID2 = NBA VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 =

NBA CID2 = HAC VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = NBA CID2

= MA VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = NBA CID2 = PX

VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = HAC CID2 = H2O VALUE =

EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = HAC CID2 = NBA VALUE = EOS-LIT \\

\\ BPVAL PARAMNAME2 = HOCETA CID1 = HAC CID2 = HAC VALUE = EOS-LIT \\ \\ BPVAL

PARAMNAME2 = HOCETA CID1 = HAC CID2 = MA VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2

= HOCETA CID1 = HAC CID2 = PX VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA

CID1 = MA CID2 = H2O VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = MA

CID2 = NBA VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = MA CID2 = HAC

VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = MA CID2 = MA VALUE =

EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = MA CID2 = PX VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = PX CID2 = NBA VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2 = HOCETA CID1 = PX CID2 = HAC VALUE = EOS-LIT \\ \\ BPVAL PARAMNAME2

= HOCETA CID1 = PX CID2 = MA VALUE = EOS-LIT \\ ? PROPERTIES PARAMETERS BINARY SCALAR \? ; \; \\ PROP-LIST PARAMNAME = RKTKIJ SETNO = 1 UNITROW = 0 \\ ? PROPERTIES PARAMETERS BINARY \\

? ; \0

TUNITROW = 22 TUNITLABEL = F NEL = 2 \\ ? PROPERTIES PARAMETERS BINARY \\? ; \; \\ PROP-LIST PARAMNAME = ANDMIJ SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL = F NEL = 2 \\ ? PROPERTIES PARAMETERS BINARY \\? ; \; \\ PROP-LIST

PARAMNAME = HENRY SETNO = 1 UNITROW = 20 UNITLABEL = bar TUNITROW = 22

TUNITLABEL = C BDBANK = ( BINARY HENRY ) NEL = 6 \\ ? PROPERTIES PARAMETERS BINARY \\? ; \; \\ PROP-LIST PARAMNAME = NRTL SETNO = 1 UNITROW = 0 TUNITROW = 22 TUNITLABEL = C BDBANK = ( \

搜索“diyifanwen.net”或“第一范文网”即可找到本站免费阅读全部范文。收藏本站方便下次阅读，第一范文网，提供最新综合文库aspen共沸精馏塔全文阅读和word下载服务。

aspen共沸精馏塔.doc 将本文的Word文档下载到电脑，方便复制、编辑、收藏和打印

下载这篇word文档

本文链接：https://www.diyifanwen.net/wenku/61013.html（转载请注明文章来源）

上一篇：2012-2013学年八年级上学期数学期中测评试卷及答案北票市桃园中
下一篇：工程力学复习资料