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初學(xué)PIPEPHASE,用組分模型計(jì)算一條管道到的壓降,參數(shù)都輸入進(jìn)去了,檢查沒有錯(cuò)誤,但是點(diǎn)擊RUN,不進(jìn)行計(jì)算,報(bào)如下錯(cuò)誤:
***THERMO PREPROCESSOR ERRORS DETECTED 1
圖如下。
做了兩個(gè)不同的例子,都是這種情況。是哪里沒選好嗎?
請(qǐng)有經(jīng)驗(yàn)的同學(xué)不吝賜教。
輸入文件如下:
$ SIMSCI PIPEPHASE Version 9.1 keyword file...
$
$ General Data Section
$
TITLE DATE=05/16/13
$
$
DIMENSION Metric, LENGTH=M,IN
$
CALCULATION NETWORK, Compositional, PRANDTL
$
DEFAULT IDPIPE=4.026, IDTUBING=4.026, IDRISER=4.026, *
IDANNULUS=6.065, HAUSEN
$
PRINT INPUT=FULL, DEVICE=FULL, PLOT=FULL, *
PROPERTY=FULL, MAP=TAITEL, DATABASE=FULL, *
SIMULATOR=PART, SLUG=BRILL
$
SEGMENT AUTO=OFF, DLHORIZ(M)=609.59967, *
DLVERT(M)=152.39992
$
$ Component Data Section
$
COMPONENT DATA
$
LIBID 1, H2S / *
2, C1 / *
3, C2 / *
4, C3 / *
5, IC4 / *
6, NC4 / *
7, IC5 / *
8, NC5 / *
9, NC6
$
PHASE VL=1,9
$
$ Network Data Section
$
NETWORK DATA
$
SOLUTION PBALANCE, FLOWAL=2, STEP=1
$
TOLERANCE PRESSURE=0.138
$
$ Thermodynamic Data Section
$
THERMODYNAMIC DATA
$
METHOD SET=SET01, SYSTEM=SRK
$
WATER PROPERTY=Super
$
KVALUE BANK=SimSci
$
$ PVT Data Section
$
PVT PROPERTY DATA
$
SET SETNO=1, SET=SET01
$
$ Structure Data Section
$
STRUCTURE DATA
$
SOURCE NAME=S001, IDNAME=S001, PRIORITY=0, *
PRES=74, TEMP=74, RATE(ESTI,W)=5.0000e+005, *
XCORD=-105, YCORD=135, *
COMP(M)=1, 5.4 / 2, 2 / 3, 14.3 / *
4, 16.3 / 5, 2.9 / 6, 8.6 / *
7, 3.1 / 8, 2.9 / 9, 44.5
$
SINK NAME=D001, IDNAME=D001, SET=SET01 , *
PRES=10, RATE(ESTI)=5.000e+005, XCORD=1153, *
YCORD=132
$
$
$
LINK NAME=L001, FROM=S001, TO=D001, *
IDNAME=L001, IDFROM=S001, IDTO=D001, *
XCOR=606,460,309, YCOR=182,185,182
PIPE NAME=P001, LENGTH(KM)=200, ECHG=400, *
NOMD=24, SCHED= 40, U=1, *
TAMB=20
$
$ End of keyword file...
$
END
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