Valores de variables Fortran accedidas | Ejercicios de Termodinámica Química

sensibilidad_K.txt

SENSITIVITYBLOCK:K

‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐

SAMPLEDVARIABLES:

K:SENTENCE=RXN‐RESVARIABLE=K‐CALCID1=1INUOSBLOCKREACTOR

H2:H2MOLEFLOWINSTREAM4SUBSTREAMMIXED

N2:N2MOLEFLOWINSTREAM4SUBSTREAMMIXED

NH3:NH3MOLEFLOWINSTREAM4SUBSTREAMMIXED

CO2:CO2MOLEFLOWINSTREAM4SUBSTREAMMIXED

QHEAT1:SENTENCE=PARAMVARIABLE=QCALCINUOSBLOCKHEATER1

QHEAT2:SENTENCE=PARAMVARIABLE=QCALCINUOSBLOCKHEATER2

QREAC:SENTENCE=PARAMVARIABLE=QCALCINUOSBLOCKREACTOR

QFLASH:SENTENCE=PARAMVARIABLE=QCALCINUOSBLOCKFLASH

VARIEDVARIABLES:

VARY1:SENTENCE=PARAMVARIABLE=PRESINUOSBLOCKREACTOR

LOWERLIMIT=3600.0000PSI

UPPERLIMIT=4100.0000PSI

INCREMENT=50.0000

VARY2:SENTENCE=PARAMVARIABLE=TEMPINUOSBLOCKREACTOR

LOWERLIMIT=500.0000F

UPPERLIMIT=1100.0000F

INCREMENT=50.0000

TABULATEDVARIABLES:

COLUMN3:K

COLUMN4:H2

COLUMN5:N2

COLUMN6:NH3

COLUMN7:CO2

COLUMN8:QHEAT1

COLUMN9:QHEAT2

COLUMN10:QREAC

COLUMN11:QFLASH

‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐‐

!VARY1!VARY2!K!H2!N2!NH3!

!REACTOR!REACTOR!!!!!

!PARAM!PARAM!!!!!

!PRES!TEMP!!!!!

!!!!!!!

!PSI!F!!LBMOL/HR!LBMOL/HR!LBMOL/HR!

!!!!!!!

!============!============!============!============!============!============!

!3600.0000!500.0000!2.2820‐02!101.7855!2.4905!197.8340!

!3600.0000!550.0000!7.3691‐03!152.4946!3.1447!197.9960!

!3600.0000!600.0000!2.6255‐03!224.0136!4.0532!198.2514!

!3600.0000!650.0000!1.0192‐03!323.3890!5.3240!198.6052!

!3600.0000!700.0000!4.2664‐04!458.0674!7.1291!199.0623!

!‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐!

!3600.0000!750.0000!1.9089‐04!641.1701!9.5797!199.7059!

!3600.0000!800.0000!9.0611‐05!886.4238!12.8797!200.5794!

!3600.0000!850.0000!4.5343‐05!1204.9353!17.3614!201.6977!

!3600.0000!900.0000!2.3791‐05!1620.4350!23.2166!203.1905!

!3600.0000!950.0000!1.3027‐05!2140.6952!31.0055!205.0298!

!‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐!

!3600.0000!1000.0000!7.4129‐06!2789.9634!41.1246!207.3308!

!3600.0000!1050.0000!4.3685‐06!3563.4277!54.5508!210.0357!

!3600.0000!1100.0000!2.6577‐06!4597.3176!70.3337!213.7785!

!3650.0000!500.0000!2.2820‐02!100.7314!2.4814!197.8179!

!3650.0000!550.0000!7.3691‐03!150.9299!3.1268!197.9891!

!‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐!

!3650.0000!600.0000!2.6255‐03!221.6938!4.0229!198.2435!

!3650.0000!650.0000!1.0192‐03!319.0621!5.3020!198.5745!

!3650.0000!700.0000!4.2664‐04!452.4920!7.0709!199.0371!

!3650.0000!750.0000!1.9089‐04!633.8495!9.4753!199.6817!

!3650.0000!800.0000!9.0611‐05!873.8803!12.7691!200.5227!

!‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐!

!3650.0000!850.0000!4.5343‐05!1190.4175!17.1445!201.6482!

!3650.0000!900.0000!2.3791‐05!1600.5708!22.9101!203.1219!

!3650.0000!950.0000!1.3027‐05!2113.9632!30.5790!204.9368!

!3650.0000!1000.0000!7.4129‐06!2752.8727!40.5633!207.1975!

!3650.0000!1050.0000!4.3685‐06!3521.0797!53.6923!209.8920!

!‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐+‐‐‐‐‐‐‐‐‐‐‐‐!

!3650.0000!1100.0000!2.6577‐06!4532.8598!69.3203!213.5447!

!3700.0000!500.0000!2.2820‐02!99.7770!2.4688!197.8148!

!3700.0000!550.0000!7.3691‐03!149.2781!3.1147!197.9748!

!3700.0000!600.0000!2.6255‐03!218.6164!4.0215!198.2077!

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Valores de variables Fortran accedidas, Ejercicios de Termodinámica Química

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SENSITIVITY BLOCK: K

SAMPLED VARIABLES:

K : SENTENCE=RXN‐RES VARIABLE=K‐CALC ID1=1 IN UOS BLOCK REACTOR

H2 : H2 MOLEFLOW IN STREAM 4 SUBSTREAM MIXED

N2 : N2 MOLEFLOW IN STREAM 4 SUBSTREAM MIXED

NH3 : NH3 MOLEFLOW IN STREAM 4 SUBSTREAM MIXED

CO2 : CO2 MOLEFLOW IN STREAM 4 SUBSTREAM MIXED

QHEAT1 : SENTENCE=PARAM VARIABLE=QCALC IN UOS BLOCK HEATER

QHEAT2 : SENTENCE=PARAM VARIABLE=QCALC IN UOS BLOCK HEATER

QREAC : SENTENCE=PARAM VARIABLE=QCALC IN UOS BLOCK REACTOR

QFLASH : SENTENCE=PARAM VARIABLE=QCALC IN UOS BLOCK FLASH

VARIED VARIABLES:

VARY 1: SENTENCE=PARAM VARIABLE=PRES IN UOS BLOCK REACTOR

LOWER LIMIT = 3600.0000 PSI

UPPER LIMIT = 4100.0000 PSI

INCREMENT = 50.

VARY 2: SENTENCE=PARAM VARIABLE=TEMP IN UOS BLOCK REACTOR

LOWER LIMIT = 500.0000 F

UPPER LIMIT = 1100.0000 F

INCREMENT = 50.

TABULATED VARIABLES:

COLUMN 3: K

COLUMN 4: H

COLUMN 5: N

COLUMN 6: NH

COLUMN 7: CO

COLUMN 8: QHEAT

COLUMN 9: QHEAT

COLUMN 10: QREAC

COLUMN 11: QFLASH

! VARY 1! VARY 2! K! H2! N2! NH3!

! REACTOR! REACTOR!!!!!

! PARAM! PARAM!!!!!

! PRES! TEMP!!!!!

! PSI! F!! LBMOL/HR! LBMOL/HR! LBMOL/HR!

VALUES OF ACCESSED FORTRAN VARIABLES ON MOST RECENT SIMULATION PASS:

VARIABLE VALUE UNITS

K 0.237909E‐ 04

H2 1532.16 LBMOL/HR

N2 20.3808 LBMOL/HR

NH3 203.051 LBMOL/HR

CO2 1.35626 LBMOL/HR

QHEAT1 0.100798E+08 BTU/HR

QHEAT2 ‐0.118303E+08 BTU/HR

QREAC ‐0.451510E+07 BTU/HR

QFLASH ‐0.210305E+07 BTU/HR