aspen共沸精馏塔(2)

\\\) NEL = 12 \\ \\ BPVAL PARAMNAME2 = NRTL CID1

= H2O CID2 = NBA UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = C VAL1 = VLE-IG

VAL2 = VLE-IG VAL3 = VLE-IG VAL4 = VLE-IG VAL5 = VLE-IG VAL6 = VLE-IG VAL7 =

VLE-IG VAL8 = VLE-IG VAL9 = VLE-IG VAL10 = VLE-IG VAL11 = VLE-IG VAL12 =

VLE-IG / PARAMNAME2 = NRTL CID1 = H2O CID2 = HAC UNITROW2 = 0 TUNITROW2 = 22

TUNITLABEL2 = C VAL1 = VLE-HOC VAL2 = VLE-HOC VAL3 = VLE-HOC VAL4 = VLE-HOC VAL5 = VLE-HOC VAL6 = VLE-HOC VAL7 = VLE-HOC VAL8 = VLE-HOC VAL9 = VLE-HOC VAL10 = VLE-HOC VAL11 = VLE-HOC VAL12 = VLE-HOC / PARAMNAME2 = NRTL CID1 = NBA CID2 = HAC UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = C VAL1 = VLE-HOC VAL2 = VLE-HOC VAL3 = VLE-HOC VAL4 = VLE-HOC VAL5 = VLE-HOC VAL6 = VLE-HOC VAL7 = VLE-HOC VAL8 = VLE-HOC VAL9 = VLE-HOC VAL10 = VLE-HOC VAL11 = VLE-HOC

VAL12 = VLE-HOC / PARAMNAME2 = NRTL CID1 = H2O CID2 = MA UNITROW2 = 0

TUNITROW2 = 22 TUNITLABEL2 = C VAL1 = VLE-IG VAL2 = VLE-IG VAL3 = VLE-IG VAL4

= VLE-IG VAL5 = VLE-IG VAL6 = VLE-IG VAL7 = VLE-IG VAL8 = VLE-IG VAL9 =

VLE-IG VAL10 = VLE-IG VAL11 = VLE-IG VAL12 = VLE-IG / PARAMNAME2 = NRTL CID1

= NBA CID2 = MA UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = C VAL1 = VLE-IG

VAL2 = VLE-IG VAL3 = VLE-IG VAL4 = VLE-IG VAL5 = VLE-IG VAL6 = VLE-IG VAL7 =

VLE-IG VAL8 = VLE-IG VAL9 = VLE-IG VAL10 = VLE-IG VAL11 = VLE-IG VAL12 =

VLE-IG / PARAMNAME2 = NRTL CID1 = HAC CID2 = MA UNITROW2 = 0 TUNITROW2 = 22

TUNITLABEL2 = C VAL1 = VLE-HOC VAL2 = VLE-HOC VAL3 = VLE-HOC VAL4 = VLE-HOC VAL5 = VLE-HOC VAL6 = VLE-HOC VAL7 = VLE-HOC VAL8 = VLE-HOC VAL9 = VLE-HOC VAL10 = VLE-HOC VAL11 = VLE-HOC VAL12 = VLE-HOC / PARAMNAME2 = NRTL CID1 = H2O CID2 = PX UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = C VAL1 = LLE-ASPEN VAL2 = LLE-ASPEN VAL3 = LLE-ASPEN VAL4 = LLE-ASPEN VAL5 = LLE-ASPEN VAL6 =

LLE-ASPEN VAL7 = LLE-ASPEN VAL8 = LLE-ASPEN VAL9 = LLE-ASPEN VAL10 =

LLE-ASPEN VAL11 = LLE-ASPEN VAL12 = LLE-ASPEN / PARAMNAME2 = NRTL CID1 = HAC

CID2 = PX UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = C VAL1 = VLE-HOC VAL2 =

VLE-HOC VAL3 = VLE-HOC VAL4 = VLE-HOC VAL5 = VLE-HOC VAL6 = VLE-HOC VAL7 =

VLE-HOC VAL8 = VLE-HOC VAL9 = VLE-HOC VAL10 = VLE-HOC VAL11 = VLE-HOC VAL12 =

VLE-HOC \\ ? PROPERTIES PARAMETERS BINARY \\TUNITROW

= 22 TUNITLABEL = C BDBANK = ( \= 12 \\ \\

BPVAL PARAMNAME2 = NRTL CID1 = H2O CID2 = NBA UNITROW2 = 0 TUNITROW2 = 22

TUNITLABEL2 = C VAL1 = VLE-IG VAL2 = VLE-IG VAL3 = VLE-IG VAL4 = VLE-IG VAL5

= VLE-IG VAL6 = VLE-IG VAL7 = VLE-IG VAL8 = VLE-IG VAL9 = VLE-IG VAL10 =

VLE-IG VAL11 = VLE-IG VAL12 = VLE-IG / PARAMNAME2 = NRTL CID1 = H2O CID2 =

MA UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = C VAL1 = VLE-IG VAL2 = VLE-IG

VAL3 = VLE-IG VAL4 = VLE-IG VAL5 = VLE-IG VAL6 = VLE-IG VAL7 = VLE-IG VAL8 =

VLE-IG VAL9 = VLE-IG VAL10 = VLE-IG VAL11 = VLE-IG VAL12 = VLE-IG / PARAMNAME2 = NRTL CID1 = H2O CID2 = PX UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = C VAL1 = LLE-ASPEN VAL2 = LLE-ASPEN VAL3 = LLE-ASPEN VAL4 =

LLE-ASPEN VAL5 = LLE-ASPEN VAL6 = LLE-ASPEN VAL7 = LLE-ASPEN VAL8 = LLE-ASPEN

VAL9 = LLE-ASPEN VAL10 = LLE-ASPEN VAL11 = LLE-ASPEN VAL12 = LLE-ASPEN /

PARAMNAME2 = NRTL CID1 = NBA CID2 = MA UNITROW2 = 0 TUNITROW2 = 22 TUNITLABEL2 = C VAL1 = VLE-IG VAL2 = VLE-IG VAL3 = VLE-IG VAL4 = VLE-IG VAL5

= VLE-IG VAL6 = VLE-IG VAL7 = VLE-IG VAL8 = VLE-IG VAL9 = VLE-IG VAL10 =

VLE-IG VAL11 = VLE-IG VAL12 = VLE-IG \\ ? PROPERTIES REGRESSION \? \\

DATA-GROUPS GROUPID = \= 8

PARAMNAME = NRTL CIDI = H2O CIDJ = HAC ELEMNO = 2 PINIT = -242.2730940 <0>

<0> SCALE = 1.0 <0> <0> / TYPE = \NRTL

CIDI = HAC CIDJ = H2O ELEMNO = 2 PINIT = 474.5232630 <0> <0> SCALE = 1.0 <0>

<0> / TYPE = \= HAC

ELEMNO = 3 PINIT = .3000000000 <0> <0> USAGE = FIX \\ \\ REPORT \\ ? PROPERTIES

DATA MIXTURE \? ; \; \\ \STATESPEC = TXY CIDS = ( H2O HAC ) PRES = 760. <20> <9> \\ \\ \PEQTYPE1 = VL VLECIDS1 =

( H2O HAC ) \\ \\ USING USE = \/ USE = DATA / USE = DATA / USE =

DATA / USE = DATA / USE = DATA / USE = DATA / USE = DATA / USE = DATA /

USE = DATA / USE = DATA / USE = DATA / USE = DATA / USE = DATA \\ \\ DATA 1

PROPLIST = \PROPLIST =

\PROPLABEL = H2O VALUE = \<0> <0> / 1 PROPLIST = \PROPLABEL = H2O VALUE = \PROPLABEL = C VALUE = 118.5 <0> <0> / 2 PROPLIST = \= H2O

VALUE = 0 <0> <0> / 2 PROPLIST = \<0> <0>

/ 3 PROPLIST = \/ 3

PROPLIST = \PROPLABEL = H2O VALUE = 0.208 <0> <0> / 3 PROPLIST =

\PROPLABEL = H2O VALUE = 0.331 <0> <0> / 4 PROPLIST = \

PROPLABEL = C VALUE = 107.2 <0> <0> / 4 PROPLIST = \= H2O

VALUE = 0.327 <0> <0> / 4 PROPLIST = \= 0.441

<0> <0> / 5 PROPLIST = \<0> <0>

/ 5 PROPLIST = \PROPLIST =

\PROPLABEL = H2O VALUE = 0.602 <0> <0> / 6 PROPLIST = \

PROPLABEL = C VALUE = 104.0 <0> <0> / 6 PROPLIST = \= H2O

VALUE = 0.592 <0> <0> / 6 PROPLIST = \= 0.713

<0> <0> / 7 PROPLIST = \<0> <0>

/ 7 PROPLIST = \PROPLIST =

\PROPLABEL = H2O VALUE = 0.787 <0> <0> / 8 PROPLIST = \

PROPLABEL = C VALUE = 101.7 <0> <0> / 8 PROPLIST = \= H2O

VALUE = 0.779 <0> <0> / 8 PROPLIST = \= 0.852

<0> <0> / 9 PROPLIST = \<0> <0>

/ 9 PROPLIST = \PROPLIST =

\PROPLABEL = H2O VALUE = 0.895 <0> <0> / 10 PROPLIST = \

PROPLABEL = C VALUE = 100.9 <0> <0> / 10 PROPLIST = \PROPLABEL = H2O

VALUE = 0.884 <0> <0> / 10 PROPLIST = \= 0.918

<0> <0> / 11 PROPLIST = \<0> <0>

/ 11 PROPLIST = \PROPLIST

= \\\PROPLABEL = H2O VALUE = 0.97 <0> <0> / 12 PROPLIST = \PROPLABEL = H2O

VALUE = 0.978 <0> <0> / 13 PROPLIST = \VALUE =

100.2 <0> <0> / 13 PROPLIST = \<0> <0>

/ 13 PROPLIST = \PROPLIST

= \\

PROPLABEL = H2O VALUE = 1 <0> <0> / 14 PROPLIST = \= H2O

VALUE = 1 <0> <0> \\ ? \ID =

MASSVFRA \\ \\ P1 ID = MASSFLMX UNITS = ( \) \\ \\ P1 ID = HMX UNITS

= (

\= (

\= (

\) \\ \\ P1 ID = KMX UNITS = ( \) \\ \\ P1 ID = SIGMAMX UNITS = ( \) \\ \\ P1 ID = MWMX \\ \\ P2 PHASE = ( T V L ) \\ \\ DESCRIPTION DESCRIPTION = \\

MAIN THERMAL ? ; \\\ \\ P1

ID = CPMX UNITS = ( \MIXED

PHASE = ( V L ) \\ \\ DESCRIPTION DESCRIPTION = \heat capacity, and themral conductivity\\\ ? \MAIN TXPORT ? ; \P1 ID =

MUMX \\ \\ P1 ID = SIGMAMX \\ \\ P2 SUBSTREAM = MIXED PHASE = ( V L ) \\ \\

DESCRIPTION DESCRIPTION = \\\ ?

\GAMMA \\

\\ P1 ID = PL \\ \\ P2 SUBSTREAM = MIXED PHASE = ( V L ) \\ \\ DESCRIPTION DESCRIPTION = \activity, and vapor pressure\\\ ? \MAIN

VLLE ? ; \= PL \\

\\ P2 SUBSTREAM = MIXED PHASE = ( V L1 L2 ) \\ \\ DESCRIPTION DESCRIPTION =

\activity, and vapor pressure\\\ ? \? ? STREAM MATERIAL 45 ? ; \<22> <4>

PRES = 4.6 <20> <5> BASIS = \= 3 \\ \\

MOLE-FLOW SSID1 = MIXED CID = H2O FLOW = 10918. <-80> <3> / SSID1 = MIXED

CID = HAC FLOW = 8647. <-80> <3> / SSID1 = MIXED CID = MA FLOW = 107. <-80> <3> \\ ? STREAM MATERIAL \? ; \; \\ SUBSTREAM SSID =

MIXED TEMP = 40. <22> <4> PRES = 1. <20> <3> BASIS = \TOTAL =

11547. <-80> <0> JUNK = 4 \\ \\ MOLE-FLOW SSID1 = MIXED CID = H2O FLOW

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