aspen共沸精馏塔(3)

2019-03-16 22:30

= 11128.

<-80> <3> / SSID1 = MIXED CID = NBA FLOW = 280. <-80> <3> / SSID1 = MIXED

CID = HAC FLOW = 11. <-80> <3> / SSID1 = MIXED CID = MA FLOW = 128. <-80>

<3> \\ ? STREAM MATERIAL 129 ? ; \MIXED

TEMP = 30. <22> <4> PRES = 1. <20> <3> BASIS = \TOTAL = 4.01 <-80>

<0> JUNK = 2 \\ \\ MOLE-FLOW SSID1 = MIXED CID = NBA FLOW = 4. <-80> <3> /

SSID1 = MIXED CID = PX FLOW = 0.01 <-80> <3> \\ ? STREAM MATERIAL \

; \= 1.2

<20> <3> BASIS = \MOLE-FLOW

SSID1 = MIXED CID = H2O FLOW = 838. <-80> <3> / SSID1 = MIXED CID = NBA FLOW

= 28776. <-80> <3> / SSID1 = MIXED CID = MA FLOW = 393. <-80> <3> / SSID1

= MIXED CID = PX FLOW = 1856. <-80> <3> \\ ? BLOCK FSPLIT M1 ? ; \; ; DOT ; \\ PARAM SID = 45A FRAC = 0.5 <0> <0> / SID = 45B \\ \\ STREAM-ORDER ORDER-STREAM = 45A / ORDER-STREAM = 45B \\ ? BLOCK FSPLIT M2 ? ; \; ; DOT ; \\ PARAM SID = 142 FRAC = 0.9 <0> <0> / SID = 143 \\ \\ STREAM-ORDER ORDER-STREAM = 142 / ORDER-STREAM = 143 \\ ? BLOCK FSPLIT M3 ? ; \

; ; DOT ; \\ PARAM SID = 126 / SID = 139 FRAC = 0.048 <0> <0> \\ \\ STREAM-ORDER ORDER-STREAM = 126 / ORDER-STREAM = 139 \\ ? BLOCK HEATER \

? ; \; ; HEATER ; \\ PARAM TEMP = 40. <22> <4> PRES = 1.02 <20>

<5> \\ ? BLOCK HEATER \TEMP =

65. <22> <4> PRES = 0.029 <20> <23> \\ ? BLOCK DECANTER \\<20> <3>

KLL-CORR = PROPOPTSET LL-METH = \PROPERTIES

OPSETNAME = NRTL \\ \\ \BLKOPFREWAT = NO \\ ? BLOCK RADFRAC \? ; \; ; STRIP1 ; \\ PARAM NSTAGE = 60 ALGORITHM = NONIDEAL

EFF = MURPHREE INIT-OPTION = AZEOTROPIC MAXOL = 200 GAMMA-MODEL = COMBINED NO-PHASE = 2 DAMPING = NONE OPT-PRES = \CONV-METH

= OTHERS \\ \\ \\\ \\ FEEDS

FEED-SID = 45A FEED-STAGE = 30 / FEED-SID = 45B FEED-STAGE = 37 / FEED-SID

= 142 FEED-STAGE = 1 / FEED-SID = 143 FEED-STAGE = 22 / FEED-SID = 139

FEED-STAGE = 1 \\ \\ PRODUCTS PROD-STREAM = 120 PROD-STAGE = 1 PROD-PHASE = V

P-S = N / PROD-STREAM = 121 PROD-STAGE = 60 PROD-PHASE = L P-S = N \\ \\

P-SPEC PRES-STAGE = 1 STAGE-PRES = 1.02 <20> <5> / PRES-STAGE = 60 STAGE-PRES = 1.25 <20> <5> \\ \\ \\

DP-COL = 0.23 <75> <5> BASIS-RDV = 1.0 <0> <0> B-BASIS = MASS BASIS-B = 9192.

<-80> <3> \\ \\ \DB-STREAMS = ( 45A 45B ) DB-COMPS = ( HAC ) \\ \\

THERMOSYPHON TH-TEMP = 120. <22> <4> TH-BASIS = MASS OPT-TH-REB = OUTLET \\ \\

STAGE-EFF SEFF-STAGE = 1 STAGE-EFF = 0.6 <0> <0> / SEFF-STAGE = 60 STAGE-EFF

= 0.6 <0> <0> \\ \\ T-EST TEMP-STAGE = 1 TEMP-EST = 90. <22> <4> / TEMP-STAGE = 60 TEMP-EST = 118. <22> <4> \\ \\ SPEC SPEC-NO = 1 SPEC-TYPE = \VALUE = 11. <0> <0> SPEC-COMPS = ( HAC ) SPEC-STREAMS = ( 120 ) SPEC-HIDE =

HIDDEN \\ \\ VARY VARY-NO = 1 VARTYPE = D LB = 30000. <0> <0> UB = 50000. <0>

<0> VARY-HIDE = HIDDEN \\ \\ \= NO \\ \\

\\\ \\ \\\ ? BLOCK RADFRAC \? ; \

; FRACT1 ; \\ PARAM NSTAGE = 25 ALGORITHM = NONIDEAL EFF = MURPHREE INIT-OPTION = STANDARD MAXOL = 100 GAMMA-MODEL = COMBINED NO-PHASE = 2

DAMPING = NONE OPT-PRES = \VIEW-PRES = PROFILE CONV-METH = OTHERS \\ \\

\CONDENSER = TOTAL REBOILER = THERMOSYPHON \\ \\ FEEDS FEED-SID =

140 FEED-STAGE = 13 \\ \\ PRODUCTS PROD-STREAM = 145 PROD-STAGE = 25

PROD-PHASE = L P-S = N / PROD-STREAM = 130 PROD-STAGE = 7 PROD-PHASE = L FLOW-BASIS =

MASS PROD-FLOW = 510. <-80> <3> / PROD-STREAM = 131 PROD-STAGE = 1 PROD-PHASE = L P-S = N \\ \\ P-SPEC PRES-STAGE = 1 STAGE-PRES = 1.01 <20> <5>

/ PRES-STAGE = 25 STAGE-PRES = 1.22 <20> <5> \\ \\ \1.01 <20> <5> \\ \\ \DP-COL = 0.21 <75> <5> BASIS-RDV = 0.0 <0> <0> D-BASIS =

MASS BASIS-D = 97. <-80> <3> RR-BASIS = MASS BASIS-RR = 30. <0> <0> \\ \\

\SC-TEMP

= 40. <22> <4> \\ \\ THERMOSYPHON TH-TEMP = 106. <22> <4> OPT-TH-REB = OUTLET

\\ \\ STAGE-EFF SEFF-STAGE = 1 STAGE-EFF = 0.9 <0> <0> / SEFF-STAGE = 2

STAGE-EFF = 0.6 <0> <0> / SEFF-STAGE = 25 STAGE-EFF = 0.6 <0> <0> \\ \\ T-EST

TEMP-STAGE = 7 TEMP-EST = 92. <22> <4> / TEMP-STAGE = 25 TEMP-EST = 105.3

<22> <4> \\ \\ \\\ \\ \BLKOPFREWAT = NO \\ \\ \

\\ \DMO-PARAMS MODE = SIMULATION \\ \\ DMO-PARAMS MODE = \

DMO-PARAMS MODE = RECONCILIATION \\ \\ DMO-PARAMS MODE = OPTIMIZATION \\ \\

LSSQP-PARAMS MODE-L = DEFAULT \\ \\ LSSQP-PARAMS MODE-L = SIMULATION \\ \\

LSSQP-PARAMS MODE-L = \MODE-L =

RECONCILIATION \\ \\ LSSQP-PARAMS MODE-L = OPTIMIZATION \\ ? \

WEGSTEIN WEG-MAXIT = 30 \\ ? CONVERGENCE BROYDEN \\

/ SID = \\\\ SEQUENCE BLOCK-TYPE = BLOCK BLOCK-ID = M1 / RETURN = BEGIN BLOCK-TYPE =

CONVERGENCE BLOCK-ID = \BLOCK-TYPE = BLOCK BLOCK-ID = M3 / BLOCK-TYPE = BLOCK BLOCK-ID = \

BLOCK-TYPE = BLOCK BLOCK-ID = \/ BLOCK-TYPE = BLOCK BLOCK-ID =

\/ BLOCK-TYPE = BLOCK BLOCK-ID = \/ BLOCK-TYPE = BLOCK BLOCK-ID = \BLOCK-ID =

\\\ ? REPORT REPORT ? ? REPORT \? ? REPORT \

\\ OPTIONS MOLEFLOW = MOLEFLOW MASSFLOW = MASSFLOW MOLEFRAC = MOLEFRAC MASSFRAC = MASSFRAC \\ ? REPORT \? ? REPORT \? \\

OPTIONS PCES = PCES PROP-DATA = \DFMS = NODFMS \\ ? REPORT \

GRAPHICS_BACKUP PFS V 5.00 $CONFIG

paramdata ENRTL-RK paramdata VLE-IG paramdata VLE-RK paramdata VLE-HOC paramdata LLE-LIT paramdata LLE-ASPEN paramdata VLE-LIT paramdata BINARY paramdata EOS-LIT paramdata HENRY purebank PURE11 purebank AQUEOUS purebank SOLIDS purebank INORGANIC regdbank 1 ftn_check 1 autoblockid 0 autostreamid 0 showblockid 1 showstreamid 1 autoplacement 1 grid 2

gridresolution 0.100000 scale 0

streamprefix blockprefix B

labelscale 1.000000 qwformat %.3f

tempformat %.1f presformat %.1f flowformat %.1f strmqwformat %.0f vflowformat %.0f mflowformat %.1f vfracformat %.2f pseudobatch 0 partial 0 animation 1 runanyway 0

tooldrawvisible 0 browserheight 6465 browserwidth 10770 browsertreewidth 3810 polyplusenabled 1 dynaplusenabled 1 bfracenabled 1 rtfenabled 1 pinchenabled 0 linklimit 500 material_color 0

material_style 983041 material_width 1 material_termid heat_color 0

heat_style 983042 heat_width 1 heat_termid Q work_color 0

work_style 983043 work_width 1 work_termid W

connections_color 9

connections_style 983044 connections_width 1 measurements_color 4

measurements_style 983044 measurements_width 1 displayeoconn 0 displayeomeas 1

displayeomeastype 2 showeoviews 0 eoautosave 1


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