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adiabatic methanol reaction.rep
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+ + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + +
ADIABATIC CONVERSION OF METHANOL VAPOR TO DME
RUN CONTROL SECTION
ADIABATIC CONVERSION OF METHANOL VAPOR TO DME
FLOWSHEET SECTION
FLOWSHEET CONNECTIVITY BY STREAMS
---------------------------------
STREAM SOURCE DEST STREAM SOURCE DEST
S1 ---- B1 S2 B1 ----
FLOWSHEET CONNECTIVITY BY BLOCKS
--------------------------------
BLOCK INLETS OUTLETS
B1 S1 S2
COMPUTATIONAL SEQUENCE
----------------------
SEQUENCE USED WAS:
B1
OVERALL FLOWSHEET BALANCE
-------------------------
*** MASS AND ENERGY BALANCE ***
IN OUT GENERATION RELATIVE DIFF.
CONVENTIONAL COMPONENTS
(KMOL/HR )
METHANOL 1.00000 0.137423 -0.862577 -0.832667E-16
DME 0.00000 0.431288 0.431288 0.00000
H2O 0.00000 0.431288 0.431288 0.00000
TOTAL BALANCE
MOLE(KMOL/HR ) 1.00000 1.00000 -0.115142E-13 0.00000
MASS(KG/HR ) 32.0422 32.0422 0.887010E-15
ENTHALPY(KCAL/HR ) -46541.6 -46541.6 0.213420E-07
ADIABATIC CONVERSION OF METHANOL VAPOR TO DME
PHYSICAL PROPERTIES SECTION
COMPONENTS
----------
ID TYPE ALIAS NAME
METHANOL C CH4O METHANOL
DME C C2H6O-1 DIMETHYL-ETHER
H2O C H2O WATER
ADIABATIC CONVERSION OF METHANOL VAPOR TO DME
U-O-S BLOCK SECTION
BLOCK: B1 MODEL: RGIBBS
------------------------------
INLET STREAM: S1
OUTLET STREAM: S2
PROPERTY OPTION SET: NRTL RENON (NRTL) / IDEAL GAS
*** MASS AND ENERGY BALANCE ***
IN OUT GENERATION RELATIVE DIFF.
TOTAL BALANCE
MOLE(KMOL/HR ) 1.00000 1.00000 -0.115142E-13 0.00000
MASS(KG/HR ) 32.0422 32.0422 0.887010E-15
ENTHALPY(KCAL/HR ) -46541.6 -46541.6 0.213420E-07
*** INPUT DATA ***
EQUILIBRIUM SPECIFICATIONS:
ONLY CHEMICAL EQUILIBRIUM IS CONSIDERED, THE FLUID PHASE IS VAPOR
CALCULATED TEMPERATURE C 303.81
TEMPERATURE FOR FREE ENERGY EVALUATION C 303.81
SYSTEM PRESSURE ATM 1.0000
SPECIFIED DUTY KCAL/HR 0.0000
FLUID PHASE SPECIES IN PRODUCT LIST:
METHANOL DME H2O
ATOM MATRIX:
ELEMENT H C O
METHANOL 4.00 1.00 1.00
DME 6.00 2.00 1.00
H2O 2.00 0.00 1.00
*** RESULTS ***
TEMPERATURE C 303.81
PRESSURE ATM 1.0000
VAPOR FRACTION 1.0000
NUMBER OF FLUID PHASES 1
ADIABATIC CONVERSION OF METHANOL VAPOR TO DME
U-O-S BLOCK SECTION
BLOCK: B1 MODEL: RGIBBS (CONTINUED)
FLUID PHASE MOLE FRACTIONS:
PHASE VAPOR
OF TYPE VAPOR
PHASE FRACTION 1.000000
PLACED IN STREAM S2
DME 0.4312884
H2O 0.4312884
METHANOL 0.1374231
KMOL/HR 1.000000
ADIABATIC CONVERSION OF METHANOL VAPOR TO DME
STREAM SECTION
S1 S2
-----
STREAM ID S1 S2
FROM : ---- B1
TO : B1 ----
SUBSTREAM: MIXED
PHASE: VAPOR VAPOR
COMPONENTS: KMOL/HR
METHANOL 1.0000 0.1374
DME 0.0 0.4313
H2O 0.0 0.4313
COMPONENTS: KG/HR
METHANOL 32.0422 4.4033
DME 0.0 19.8690
H2O 0.0 7.7698
TOTAL FLOW:
KMOL/HR 1.0000 1.0000
KG/HR 32.0422 32.0422
L/HR 3.4722+04 4.7343+04
STATE VARIABLES:
TEMP C 150.0000 303.8113
PRES ATM 1.0000 1.0000
VFRAC 1.0000 1.0000
LFRAC 0.0 0.0
SFRAC 0.0 0.0
ENTHALPY:
CAL/MOL -4.6542+04 -4.6542+04
CAL/GM -1452.5119 -1452.5120
KCAL/HR -4.6542+04 -4.6542+04
ENTROPY:
CAL/MOL-K -26.8945 -22.3563
CAL/GM-K -0.8393 -0.6977
DENSITY:
MOL/CC 2.8800-05 2.1122-05
GM/CC 9.2282-04 6.7681-04
AVG MW 32.0422 32.0422
PROBLEM STATUS SECTION
BLOCK STATUS
------------
****************************************************************************
* *
* Calculations were completed normally *
* *
* All Unit Operation blocks were completed normally *
* *
* All streams were flashed normally *
* *
****************************************************************************