- 积分
- 15
- 注册时间
- 2017-10-3
- 积分
- 15
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aspen求助
aspen版本: |
aspen one V8.4 |
老师发过来的,应该是在他那边运行好了的,但是到我这里就不行了
STRUCTURE FOR COMPONENT H2O HAS NOT BEEN DEFINED.
PCES CANNOT USE GROUP-CONTRIBUTION METHODS TO ESTIMATE MISSING PROPERTIES
USE THE STRUCTURES PARAGRAPH TO DEFINE STRUCTURES OF THIS COMPONENT.
STRUCTURE FOR COMPONENT OLEIC-01 HAS NOT BEEN DEFINED.
PCES CANNOT USE GROUP-CONTRIBUTION METHODS TO ESTIMATE MISSING PROPERTIES
USE THE STRUCTURES PARAGRAPH TO DEFINE STRUCTURES OF THIS COMPONENT.
STRUCTURE FOR COMPONENT METHY-01 HAS NOT BEEN DEFINED.
PCES CANNOT USE GROUP-CONTRIBUTION METHODS TO ESTIMATE MISSING PROPERTIES
USE THE STRUCTURES PARAGRAPH TO DEFINE STRUCTURES OF THIS COMPONENT.
STRUCTURE FOR COMPONENT TRIOL-01 HAS NOT BEEN DEFINED.
PCES CANNOT USE GROUP-CONTRIBUTION METHODS TO ESTIMATE MISSING PROPERTIES
USE THE STRUCTURES PARAGRAPH TO DEFINE STRUCTURES OF THIS COMPONENT.
* WARNING IN PHYSICAL PROPERTY SYSTEM
PARAMETER DHVLWT/ELEMENT 4 (DATA SET 1)
UPPER BOUND VIOLATED FOR COMPONENT TRIOL-01
VALUE = 2.2450 , UPPER BOUND = 2.0000
* WARNING IN PHYSICAL PROPERTY SYSTEM
PARAMETER DGFORM/ELEMENT 1 (DATA SET 1)
UPPER BOUND VIOLATED FOR COMPONENT TRIOL-01
VALUE = 0.17230E+11, UPPER BOUND = 0.50000E+10
Flowsheet Analysis :
Block $OLVER01 (Method: WEGSTEIN) has been defined to converge
streams: FV-OUT FL-OUT
COMPUTATION ORDER FOR THE FLOWSHEET:
PUMP-1 PUMP-3 PUMP-2 HEATER-3 HEATER-1 HEATER-2 SHUI-JIE
DECANTER
$OLVER01 ZHI-HUA PRE
(RETURN $OLVER01)
COOLER B1 COOLER3 FLASH-2 COOLER2 B2 MEOH-SEP FLASH-1
COOLER1 GLY-SEP COOLER4 COOLER5 MIXER
->Calculations begin ...
IDEAL GAS MODEL HAS MISSING PARAMETERS:
CPIG/1ST ELEMENT (DATA SET 1) MISSING FOR COMPONENT TRIOL-01
****PROPERTY PARAMETER ERROR
ERRORS ENCOUNTERED IN CALCULATION OF IDEAL GAS PROPS FOR
HIG
PLEASE FIX THE ERRORS, RE-INITIALIZE, AND RUN AGAIN.
! Calculations stopped because of missing property parameters
会不会是aspen版本的问题,还是要我自己设置这些参数
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