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- 2013-5-15
- 积分
- 45
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来大神帮我看看ba，谢谢咯
我把运行结果页翻译了一下，可还是不会修改block参数，帮我看看吧，通俗点~~~谢谢，急啊{:1106_361:}
<< Run reinitialized 18:23:34 Thu May 30, 2013>>
运行重新启动于2013年五月30日下午6：23
->Processing input specifications ...加载输入规范
** ERROR IN THE "BLOCK" PARAGRAPH WHICH BEGINS ON LINE 157
BLOCK NAME: B12 MODEL NAME: DSTWU SKW: PARAM TKW: TEMP-TOL
错误开始发生在157行模块群
模块名称：B12 模型名称：DSTWU SKW:PARAM TKW:TEMP-TOL
INVALID USE OF UNITS SPECIFICATION IN BRACES OR BRACKETS.
SENTENCE IGNORED.
在括号或者括弧中的单位规范应用无效。
句子的忽略。
** ERROR IN THE "BLOCK" PARAGRAPH WHICH BEGINS ON LINE 157
BLOCK NAME: B12 MODEL NAME: DSTWU SKW: PARAM TKW: FREE-WATER
错误开始发生在157行模块群
模块名称：B12 模型名称：DSTWU SKW:PARAM TKW:FREE-WATER
VALUE IS REQUIRED FOR TERTIARY KEYWORD: HEAVYKEY
BUT WAS NOT ENTERED. PARAGRAPH IGNORED.
值是第三关键字的所必需的：重关键组分
但是没有输入。 段落的忽略。
*** SEVERE ERROR
BLOCK: "B12" APPEARS IN THE FLOWSHEET, BUT
NO BLOCK PARAGRAPH HAS BEEN ENTERED FOR IT.
严重错误
模块：B12出现在流程中，但是却没有块段为其输入。
INFORMATION
STREAM: "16" HAS NO SOURCE OR DESTINATION.
IT WILL BE SAVED TEMPORARILY.
信息
流股：16没有源或者目的地。
它将暂时保存。
! Errors while processing input specifications
处理输入规格时发生错误
->Processing input specifications ...加载输入规范
Flowsheet Analysis :流程分析
Block $OLVER01 (Method: WEGSTEIN) has been defined to converge
streams: 13 3
块$OLVER01（方法：WEGSTEIN）已经被定义为收敛流股：13 3
COMPUTATION ORDER FOR THE FLOWSHEET:
$OLVER01 B12 B4 B20 B7 B8 B6 B11 REACTOR B5 DECANTER B21
(RETURN $OLVER01)
流程的计算秩序：
$OLVER01 B12 B4 B20 B7 B8 B6 B11 REACTOR B5 DECANTER B21
(RETURN $OLVER01)
->Calculations begin ...计算开始
> Beginning Convergence Loop $OLVER01 Method: WEGSTEIN开始收敛循环$OLVER01方法：WEGSTEIN
Block: B12 Model: DSTWU 模块：B12 模型：DSTWU
** ERROR
MINIMUM REFLUX RATIO CALCULATED FROM UNDERWOOD EQUATION
IS -1.3999. REFLUX RATIO RESET TO 0.1.
** 错误
由UNDERWOOD方程计算出的最小回流比
是-1.3999.回流比复位为0.1。
Block: B4 Model: FLASH2
Block: B20 Model: MIXER
Block: B7 Model: HEATER
Block: B8 Model: COMPR
* WARNING
IMPROPER OUTLET PRESSURE SPECIFIED FOR THE GIVEN UNIT
INPUT PRESSURE = (0.6000E+07) OUTPUT PRESSURE = (0.6000E+07)
* 警告
不当的出口压力为给定的单元指定
输入压力=(0.6000E+07) 出口压力=(0.6000E+07)
*** SEVERE ERROR
FORTRAN INVALID OPERATION ENCOUNTERED.
*** 严重错误
FORTRAN语言遇到无效的操作。
** ERROR
LIQUID PHASE EXISTS EITHER AT OUTLET CONDITIONS OR
AT SOME INTERMEDIATE CONDITIONS. SPECIFY "VALID PHASES"
WHICH ALLOWS TWO OR THREE PHASES CALCULATION.
** 错误
液相不仅在出口条件也在一些中间条件存在。指定的“有效相态”
允许2或3个相态参与计算。
Block: B6 Model: HEATER
Block: B11 Model: COMPR
* WARNING
IMPROPER OUTLET PRESSURE SPECIFIED FOR THE GIVEN UNIT
INPUT PRESSURE = (0.6000E+07) OUTPUT PRESSURE = (0.6000E+07)
* 警告
不当的出口压力为给定的单元指定
输入压力=(0.6000E+07) 出口压力=(0.6000E+07)
* WARNING
FEED STREAM IS BELOW DEW POINT AND "VALID PHASES" IS NOT SPECIFIED.
TWO PHASES FLASH IS USED TO DETERMINE FEED STREAM PROPERTIES.
* 警告
低于露点和有效相态的进料流未指定。
两个阶段的闪蒸是用来确定进料流性质的。
*** SEVERE ERROR
FORTRAN DIVIDE BY ZERO ENCOUNTERED.
*** 严重错误
FORTRAN语言遇到了除以0。
*** SEVERE ERROR
SINGLE PHASE TEMPERATURE CALCULATIONS FAILED IN 3 ITERATIONS. FINAL
TEMPERATURE IS 10.0000 FINAL ENTHALPY IS -2.5144D+08 SPECIFIED
ENTHALPY IS -2.5686D+08 CALCULATION OF OUTLET TEMPERATURE FOR
ISENTROPIC COMPRESSOR FAILED DUE TO ERROR IN FLASH. BLOCK IS BYPASSED.
*** 严重错误
单相温度计算失败3次。
最后的温度是10，最后的焓是-2.5144D+08，指定的焓是-2.5686D+08，对于
等熵压缩机的出口温度计算错误是由于闪蒸罐被忽略了。
SKIPPING REST OF THE BLOCK CALCULATIONS.
跳过其余块的计算。
Block: REACTOR Model: RYIELD
* WARNING
SPECIFIED YIELDS HAVE BEEN NORMALIZED BY A FACTOR OF (0.98000)
TO MAINTAIN AN OVERALL MATERIAL BALANCE.
* 警告
为了保持总的物料平衡，收益率由一个因子（0.9800）归一化。
Block: B5 Model: HEATER
Block: DECANTER Model: DECANTER
* WARNING
H2O WAS SPECIFIED AS AN L2-KEY COMPONENT BUT IS NOT
PRESENT IN THE INLET STREAM. SPECIFICATION IGNORED.
* 警告
水被指定为第二关键组分但是却并没有出现在进料流股。规范忽略。
Block: B21 Model: MIXER
> Loop $OLVER01 Method: WEGSTEIN Iteration 1
6 vars not converged, Max Err/Tol 0.11161E+05
> 循环$OLVER01方法：WEGSTEIN 迭代16次不收敛，最大错误比上公差= 0.11161E+05
Block: B12 Model: DSTWU
*** SEVERE ERROR
THE LIGHT KEY COMPONENT IS NOT PRESENT IN THE FEED. BLOCK BYPASSED.
*** 严重错误
轻关键组分没有出现在进料中。模块跳过。
Block: B4 Model: FLASH2
Block: B20 Model: MIXER
Block: B7 Model: HEATER
Block: B8 Model: COMPR
* WARNING
IMPROPER OUTLET PRESSURE SPECIFIED FOR THE GIVEN UNIT
INPUT PRESSURE = (0.6000E+07) OUTPUT PRESSURE = (0.6000E+07)
* 警告
不当的出口压力为给定的单元指定
输入压力=(0.6000E+07) 出口压力=(0.6000E+07)
*** SEVERE ERROR
FORTRAN INVALID OPERATION ENCOUNTERED.
*** 严重错误
FORTRAN语言遇到无效操作。
** ERROR
LIQUID PHASE EXISTS EITHER AT OUTLET CONDITIONS OR
AT SOME INTERMEDIATE CONDITIONS. SPECIFY "VALID PHASES"
WHICH ALLOWS TWO OR THREE PHASES CALCULATION.
** 错误
液相不仅在出口条件也在一些中间条件存在。指定的“有效相态”
允许2或3个相态参与计算。
Block: B6 Model: HEATER
Block: B11 Model: COMPR
* WARNING
IMPROPER OUTLET PRESSURE SPECIFIED FOR THE GIVEN UNIT
INPUT PRESSURE = (0.6000E+07) OUTPUT PRESSURE = (0.6000E+07)
* 警告
不当的出口压力为给定的单元指定
输入压力=(0.6000E+07) 出口压力=(0.6000E+07)
* WARNING
FEED STREAM IS BELOW DEW POINT AND "VALID PHASES" IS NOT SPECIFIED.
TWO PHASES FLASH IS USED TO DETERMINE FEED STREAM PROPERTIES.
* 警告
低于露点和有效相态的进料流未指定。
两个阶段的闪蒸是用来确定进料流性质的。
*** SEVERE ERROR
FORTRAN DIVIDE BY ZERO ENCOUNTERED.
*** 严重错误
FORTRAN语言遇到了除以0。
*** SEVERE ERROR
SINGLE PHASE TEMPERATURE CALCULATIONS FAILED IN 3 ITERATIONS. FINAL
TEMPERATURE IS 10.0000 FINAL ENTHALPY IS -2.5144D+08 SPECIFIED
ENTHALPY IS -2.5686D+08 CALCULATION OF OUTLET TEMPERATURE FOR
ISENTROPIC COMPRESSOR FAILED DUE TO ERROR IN FLASH. BLOCK IS BYPASSED.
*** 严重错误
单相温度计算失败3次。
最后的温度是10，最后的焓是-2.5144D+08，指定的焓是-2.5686D+08，对于
等熵压缩机的出口温度计算错误是由于闪蒸罐被忽略了。
SKIPPING REST OF THE BLOCK CALCULATIONS.
跳过其余模块的计算
Block: REACTOR Model: RYIELD
* WARNING
SPECIFIED YIELDS HAVE BEEN NORMALIZED BY A FACTOR OF (0.98000)
TO MAINTAIN AN OVERALL MATERIAL BALANCE.
* 警告
为了保持总的物料平衡，收益率由一个因子（0.9800）归一化。
Block: B5 Model: HEATER
Block: DECANTER Model: DECANTER
* WARNING
H2O WAS SPECIFIED AS AN L2-KEY COMPONENT BUT IS NOT
PRESENT IN THE INLET STREAM. SPECIFICATION IGNORED.
* 警告
水被指定为第二关键组分但是却并没有出现在进料流股。规范忽略。
Block: B21 Model: MIXER
> Loop $OLVER01 Method: WEGSTEIN Iteration 2
2 vars not converged, Max Err/Tol -0.26537E+03
> 循环 $OLVER01 方法：WEGSTEIN
迭代22次没有收敛，最大错误比上公差= -0.26537E+03
Block: B12 Model: DSTWU
*** SEVERE ERROR
THE LIGHT KEY COMPONENT IS NOT PRESENT IN THE FEED. BLOCK BYPASSED.
*** 严重错误
轻关键组分没有出现在进料中。模块跳过。
Block: B4 Model: FLASH2
Block: B20 Model: MIXER
Block: B7 Model: HEATER
Block: B8 Model: COMPR
* WARNING
IMPROPER OUTLET PRESSURE SPECIFIED FOR THE GIVEN UNIT
INPUT PRESSURE = (0.6000E+07) OUTPUT PRESSURE = (0.6000E+07)
* 警告
不当的出口压力为给定的单元指定
输入压力=(0.6000E+07) 出口压力=(0.6000E+07)
*** SEVERE ERROR
FORTRAN INVALID OPERATION ENCOUNTERED.
*** 严重错误
FORTRAN语言遇到无效的操作。
** ERROR
LIQUID PHASE EXISTS EITHER AT OUTLET CONDITIONS OR
AT SOME INTERMEDIATE CONDITIONS. SPECIFY "VALID PHASES"
WHICH ALLOWS TWO OR THREE PHASES CALCULATION.
** 错误
液相不仅在出口条件也在一些中间条件存在。指定的“有效相态”
允许2或3个相态参与计算。
Block: B6 Model: HEATER
Block: B11 Model: COMPR
* WARNING
IMPROPER OUTLET PRESSURE SPECIFIED FOR THE GIVEN UNIT
INPUT PRESSURE = (0.6000E+07) OUTPUT PRESSURE = (0.6000E+07)
* 警告
不当的出口压力为给定的单元指定
输入压力=(0.6000E+07) 出口压力=(0.6000E+07)
* WARNING
FEED STREAM IS BELOW DEW POINT AND "VALID PHASES" IS NOT SPECIFIED.
TWO PHASES FLASH IS USED TO DETERMINE FEED STREAM PROPERTIES.
* 警告
低于露点和有效相态的进料流未指定。
两个阶段的闪蒸是用来确定进料流性质的。
*** SEVERE ERROR
FORTRAN DIVIDE BY ZERO ENCOUNTERED.
*** 严重错误
FORTRAN语言遇到了除以0。
*** SEVERE ERROR
SINGLE PHASE TEMPERATURE CALCULATIONS FAILED IN 3 ITERATIONS. FINAL
TEMPERATURE IS 10.0000 FINAL ENTHALPY IS -2.5144D+08 SPECIFIED
ENTHALPY IS -2.5686D+08 CALCULATION OF OUTLET TEMPERATURE FOR
ISENTROPIC COMPRESSOR FAILED DUE TO ERROR IN FLASH. BLOCK IS BYPASSED.
*** 严重错误
单相温度计算失败3次。
最后的温度是10，最后的焓是-2.5144D+08，指定的焓是-2.5686D+08，对于
等熵压缩机的出口温度计算错误是由于闪蒸罐被忽略了。
SKIPPING REST OF THE BLOCK CALCULATIONS.
跳过其余模块的计算
Block: REACTOR Model: RYIELD
* WARNING
SPECIFIED YIELDS HAVE BEEN NORMALIZED BY A FACTOR OF (0.98000)
TO MAINTAIN AN OVERALL MATERIAL BALANCE.
* 警告
为了保持总的物料平衡，收益率由一个因子（0.9800）归一化。
Block: B5 Model: HEATER
Block: DECANTER Model: DECANTER
* WARNING
H2O WAS SPECIFIED AS AN L2-KEY COMPONENT BUT IS NOT
PRESENT IN THE INLET STREAM. SPECIFICATION IGNORED.
* 警告
水被指定为第二关键组分但是却并没有出现在进料流股。规范忽略。
Block: B21 Model: MIXER
> Loop $OLVER01 Method: WEGSTEIN Iteration 3
2 vars not converged, Max Err/Tol -0.13630E+03
> 循环 $OLVER01 方法：WEGSTEIN
迭代32次没有收敛，最大错误比上公差=-0.13630E+03
Block: B12 Model: DSTWU
*** SEVERE ERROR
THE LIGHT KEY COMPONENT IS NOT PRESENT IN THE FEED. BLOCK BYPASSED.
*** 严重错误
轻关键组分没有出现在进料流股中，模块忽略。
Block: B4 Model: FLASH2
Block: B20 Model: MIXER
Block: B7 Model: HEATER
Block: B8 Model: COMPR
* WARNING
IMPROPER OUTLET PRESSURE SPECIFIED FOR THE GIVEN UNIT
INPUT PRESSURE = (0.6000E+07) OUTPUT PRESSURE = (0.6000E+07)
* 警告
不当的出口压力为给定的单元指定
输入压力=(0.6000E+07) 出口压力=(0.6000E+07)
*** SEVERE ERROR
FORTRAN INVALID OPERATION ENCOUNTERED.
*** 严重错误
FORTRAN语言遇到无效的操作。
** ERROR
LIQUID PHASE EXISTS EITHER AT OUTLET CONDITIONS OR
AT SOME INTERMEDIATE CONDITIONS. SPECIFY "VALID PHASES"
WHICH ALLOWS TWO OR THREE PHASES CALCULATION.
** 错误
液相不仅在出口条件也在一些中间条件存在。指定的“有效相态”
允许2或3个相态参与计算。
Block: B6 Model: HEATER
Block: B11 Model: COMPR
* WARNING
IMPROPER OUTLET PRESSURE SPECIFIED FOR THE GIVEN UNIT
INPUT PRESSURE = (0.6000E+07) OUTPUT PRESSURE = (0.6000E+07)
* 警告
不当的出口压力为给定的单元指定
输入压力=(0.6000E+07) 出口压力=(0.6000E+07)
* WARNING
FEED STREAM IS BELOW DEW POINT AND "VALID PHASES" IS NOT SPECIFIED.
TWO PHASES FLASH IS USED TO DETERMINE FEED STREAM PROPERTIES.
* 警告
低于露点和有效相态的进料流未指定。
两个阶段的闪蒸是用来确定进料流性质的。
*** SEVERE ERROR
FORTRAN DIVIDE BY ZERO ENCOUNTERED.
*** 严重错误
FORTRAN语言遇到了除以0。
*** SEVERE ERROR
SINGLE PHASE TEMPERATURE CALCULATIONS FAILED IN 3 ITERATIONS. FINAL
TEMPERATURE IS 10.0000 FINAL ENTHALPY IS -2.5144D+08 SPECIFIED
ENTHALPY IS -2.5686D+08 CALCULATION OF OUTLET TEMPERATURE FOR
ISENTROPIC COMPRESSOR FAILED DUE TO ERROR IN FLASH. BLOCK IS BYPASSED.
*** 严重错误
单相温度计算失败3次。
最后的温度是10，最后的焓是-2.5144D+08，指定的焓是-2.5686D+08，对于
等熵压缩机的出口温度计算错误是由于闪蒸罐被忽略了。
SKIPPING REST OF THE BLOCK CALCULATIONS.
Block: REACTOR Model: RYIELD
* WARNING
SPECIFIED YIELDS HAVE BEEN NORMALIZED BY A FACTOR OF (0.98000)
TO MAINTAIN AN OVERALL MATERIAL BALANCE.
Block: B5 Model: HEATER
Block: DECANTER Model: DECANTER
* WARNING
H2O WAS SPECIFIED AS AN L2-KEY COMPONENT BUT IS NOT
PRESENT IN THE INLET STREAM. SPECIFICATION IGNORED.
Block: B21 Model: MIXER
> Loop $OLVER01 Method: WEGSTEIN Iteration 4
# Converged Max Err/Tol 0.00000E+00
->Simulation calculations completed ...
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发表于 2013-5-31 13:32:40
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