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Aspen模拟常减压出现干板？塔内不能出现干板，常压炉进塔上一块板要有内回流，相当于过气化油，为原料的1~3%。造成干板的原因是侧线抽出量太大的或者回流取热量太小了。查看更多 5个回答 . 2人已关注

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公用工程冷却剂？ 各位大侠，我想请教一下-65摄氏度左右的冷却剂有哪些？？？急用！！！查看更多 1个回答 . 2人已关注

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煤气取样间的管理制度？ 急求煤气取样间的管理制度及安全措施查看更多 2个回答 . 3人已关注

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循环过程求助？加循环时会迭代时会有些错误但不影响流程收敛，请问有影响吗？ << Run reinitialized 20:35:20 Sat May 28, 2016>> ->Processing input specifications ... Flowsheet Analysis : Block $OLVER01 (Method: BROYDEN ) has been defined to converge streams: 1108 1208 302 408 415 R1 R2 COMPUTATION ORDER FOR THE FLOWSHEET: H101 V101 F101 $OLVER01 M2101 E1201 H1201 V1201 R1201 E1202 C1201 M1101 | E1101 M101 E102 E103 E104 C201 F301 F302 M301 E401 T401 | T402 V401 E402 FS401 P401 C401 F401 P403 FS402 E403 V402 | FS403 H1101 V1101 R1101 E1102 C1101 (RETURN $OLVER01) P402 S301 M302 ->Calculations begin ... Block: H101 Model: HEATER Block: V101 Model: VALVE Block: F101 Model: FSPLIT > Beginning Convergence Loop $OLVER01 Method: BROYDEN Converging tear streams: 1108 1208 302 408 415 R1 R2 Block: M2101 Model: MIXER Block: E1201 Model: HEATX * WARNING AT LEAST ONE FEED HAS ZERO FLOW BLOCK BYPASSED Block: H1201 Model: HEATER Block: V1201 Model: VALVE Block: R1201 Model: RPLUG Block: E1202 Model: HEATER Block: C1201 Model: COMPR Block: M1101 Model: MIXER Block: E1101 Model: HEATX * WARNING AT LEAST ONE FEED HAS ZERO FLOW BLOCK BYPASSED Block: M101 Model: MIXER * WARNING ZERO FEED TO BLOCK. Block: E102 Model: HEATER * WARNING ZERO FEED TO THE BLOCK. BLOCK BYPASSED Block: E103 Model: HEATER * WARNING ZERO FEED TO THE BLOCK. BLOCK BYPASSED Block: E104 Model: HEATX * WARNING AT LEAST ONE FEED HAS ZERO FLOW BLOCK BYPASSED Block: C201 Model: MCOMPR * WARNING ZERO FEED TO THE BLOCK. BLOCK IS BYPASSED Block: F301 Model: FLASH2 * WARNING ZERO FEED TO THE BLOCK. BLOCK BYPASSED Block: F302 Model: FLASH2 * WARNING ZERO FEED TO THE BLOCK. BLOCK BYPASSED Block: M301 Model: MIXER * WARNING ZERO FEED TO BLOCK. Block: E401 Model: HEATER * WARNING ZERO FEED TO THE BLOCK. BLOCK BYPASSED Block: T401 Model: RADFRAC * WARNING ZERO FEED - BLOCK BYPASSED. Block: T402 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 1 2 6.1816 2 6 14 5.0400 3 4 8 5.4179 4 2 4 0.49010 ** ERROR DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED VARIABLE IS AT ITS BOUND. Block: V401 Model: VALVE Block: E402 Model: HEATX Block: FS401 Model: FSPLIT Block: P401 Model: PUMP Block: C401 Model: COMPR Block: F401 Model: FLASH2 Block: P403 Model: PUMP Block: FS402 Model: FSPLIT Block: E403 Model: HEATER Block: V402 Model: VALVE Block: FS403 Model: FSPLIT Block: H1101 Model: HEATER Block: V1101 Model: VALVE Block: R1101 Model: RPLUG Block: E1102 Model: HEATER Block: C1101 Model: COMPR > Loop $OLVER01 Method: BROYDEN Iteration 1 Converging tear streams: 1108 1208 302 408 415 R1 R2 30 vars not converged, Max Err/Tol 0.10000E+07 Block: M2101 Model: MIXER Block: E1201 Model: HEATX Block: H1201 Model: HEATER Block: V1201 Model: VALVE Block: R1201 Model: RPLUG Block: E1202 Model: HEATER Block: C1201 Model: COMPR Block: M1101 Model: MIXER Block: E1101 Model: HEATX Block: M101 Model: MIXER Block: E102 Model: HEATER Block: E103 Model: HEATER Block: E104 Model: HEATX * WARNING AT LEAST ONE FEED HAS ZERO FLOW BLOCK BYPASSED Block: C201 Model: MCOMPR Block: F301 Model: FLASH2 Block: F302 Model: FLASH2 Block: M301 Model: MIXER Block: E401 Model: HEATER Block: T401 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 1 2 35.162 2 1 3 0.81445 Block: T402 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 4 12 44.090 2 2 4 0.39444 ** ERROR DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED VARIABLE IS AT ITS BOUND. Block: V401 Model: VALVE Block: E402 Model: HEATX Block: FS401 Model: FSPLIT Block: P401 Model: PUMP Block: C401 Model: COMPR Block: F401 Model: FLASH2 Block: P403 Model: PUMP Block: FS402 Model: FSPLIT Block: E403 Model: HEATER Block: V402 Model: VALVE Block: FS403 Model: FSPLIT Block: H1101 Model: HEATER Block: V1101 Model: VALVE Block: R1101 Model: RPLUG Block: E1102 Model: HEATER Block: C1101 Model: COMPR > Loop $OLVER01 Method: BROYDEN Iteration 2 Converging tear streams: 1108 1208 302 408 415 R1 R2 36 vars not converged, Max Err/Tol 0.10000E+07 Block: M2101 Model: MIXER Block: E1201 Model: HEATX Block: H1201 Model: HEATER Block: V1201 Model: VALVE Block: R1201 Model: RPLUG Block: E1202 Model: HEATER Block: C1201 Model: COMPR Block: M1101 Model: MIXER Block: E1101 Model: HEATX Block: M101 Model: MIXER Block: E102 Model: HEATER Block: E103 Model: HEATER Block: E104 Model: HEATX Block: C201 Model: MCOMPR Block: F301 Model: FLASH2 Block: F302 Model: FLASH2 Block: M301 Model: MIXER Block: E401 Model: HEATER Block: T401 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 1 3 1.6687 2 1 3 0.19834 Block: T402 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 3 10 1.5213 2 2 3 0.32102E-01 ** ERROR DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED VARIABLE IS AT ITS BOUND. Block: V401 Model: VALVE Block: E402 Model: HEATX Block: FS401 Model: FSPLIT Block: P401 Model: PUMP Block: C401 Model: COMPR Block: F401 Model: FLASH2 Block: P403 Model: PUMP Block: FS402 Model: FSPLIT Block: E403 Model: HEATER Block: V402 Model: VALVE Block: FS403 Model: FSPLIT Block: H1101 Model: HEATER Block: V1101 Model: VALVE Block: R1101 Model: RPLUG Block: E1102 Model: HEATER Block: C1101 Model: COMPR > Loop $OLVER01 Method: BROYDEN Iteration 3 Converging tear streams: 1108 1208 302 408 415 R1 R2 37 vars not converged, Max Err/Tol 0.85876E+04 Block: M2101 Model: MIXER Block: E1201 Model: HEATX Block: H1201 Model: HEATER Block: V1201 Model: VALVE Block: R1201 Model: RPLUG Block: E1202 Model: HEATER Block: C1201 Model: COMPR Block: M1101 Model: MIXER Block: E1101 Model: HEATX Block: M101 Model: MIXER Block: E102 Model: HEATER Block: E103 Model: HEATER Block: E104 Model: HEATX Block: C201 Model: MCOMPR Block: F301 Model: FLASH2 Block: F302 Model: FLASH2 Block: M301 Model: MIXER Block: E401 Model: HEATER Block: T401 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 1 2 0.79368 Block: T402 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 3 10 2.1467 2 2 4 0.44682E-01 ** ERROR DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED VARIABLE IS AT ITS BOUND. Block: V401 Model: VALVE Block: E402 Model: HEATX Block: FS401 Model: FSPLIT Block: P401 Model: PUMP Block: C401 Model: COMPR Block: F401 Model: FLASH2 Block: P403 Model: PUMP Block: FS402 Model: FSPLIT Block: E403 Model: HEATER Block: V402 Model: VALVE Block: FS403 Model: FSPLIT Block: H1101 Model: HEATER Block: V1101 Model: VALVE Block: R1101 Model: RPLUG Block: E1102 Model: HEATER Block: C1101 Model: COMPR > Loop $OLVER01 Method: BROYDEN Iteration 4 Converging tear streams: 1108 1208 302 408 415 R1 R2 37 vars not converged, Max Err/Tol 0.41984E+04 Block: M2101 Model: MIXER Block: E1201 Model: HEATX Block: H1201 Model: HEATER Block: V1201 Model: VALVE Block: R1201 Model: RPLUG Block: E1202 Model: HEATER Block: C1201 Model: COMPR Block: M1101 Model: MIXER Block: E1101 Model: HEATX Block: M101 Model: MIXER Block: E102 Model: HEATER Block: E103 Model: HEATER Block: E104 Model: HEATX Block: C201 Model: MCOMPR Block: F301 Model: FLASH2 Block: F302 Model: FLASH2 Block: M301 Model: MIXER Block: E401 Model: HEATER Block: T401 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 1 3 1.2157 2 1 3 0.47745E-01 Block: T402 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 3 10 3.3115 2 2 4 0.64661E-01 ** ERROR DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED VARIABLE IS AT ITS BOUND. Block: V401 Model: VALVE Block: E402 Model: HEATX Block: FS401 Model: FSPLIT Block: P401 Model: PUMP Block: C401 Model: COMPR * WARNING FEED STREAM IS BELOW DEW POINT Block: F401 Model: FLASH2 Block: P403 Model: PUMP Block: FS402 Model: FSPLIT Block: E403 Model: HEATER Block: V402 Model: VALVE Block: FS403 Model: FSPLIT Block: H1101 Model: HEATER Block: V1101 Model: VALVE Block: R1101 Model: RPLUG Block: E1102 Model: HEATER Block: C1101 Model: COMPR > Loop $OLVER01 Method: BROYDEN Iteration 5 Converging tear streams: 1108 1208 302 408 415 R1 R2 37 vars not converged, Max Err/Tol 0.20829E+04 Block: M2101 Model: MIXER Block: E1201 Model: HEATX Block: H1201 Model: HEATER Block: V1201 Model: VALVE Block: R1201 Model: RPLUG Block: E1202 Model: HEATER Block: C1201 Model: COMPR Block: M1101 Model: MIXER Block: E1101 Model: HEATX Block: M101 Model: MIXER Block: E102 Model: HEATER Block: E103 Model: HEATER Block: E104 Model: HEATX Block: C201 Model: MCOMPR Block: F301 Model: FLASH2 Block: F302 Model: FLASH2 Block: M301 Model: MIXER Block: E401 Model: HEATER Block: T401 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 1 3 1.9794 2 1 3 0.73360E-01 Block: T402 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 4 14 6.3515 2 5 15 6.7556 3 5 21 23.766 4 2 5 11.818 5 2 5 1.3146 6 2 4 0.45447 ** ERROR DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED VARIABLE IS AT ITS BOUND. Block: V401 Model: VALVE Block: E402 Model: HEATX Block: FS401 Model: FSPLIT Block: P401 Model: PUMP Block: C401 Model: COMPR * WARNING FEED STREAM IS BELOW DEW POINT Block: F401 Model: FLASH2 Block: P403 Model: PUMP Block: FS402 Model: FSPLIT Block: E403 Model: HEATER Block: V402 Model: VALVE Block: FS403 Model: FSPLIT Block: H1101 Model: HEATER Block: V1101 Model: VALVE Block: R1101 Model: RPLUG Block: E1102 Model: HEATER Block: C1101 Model: COMPR > Loop $OLVER01 Method: BROYDEN Iteration 6 Converging tear streams: 1108 1208 302 408 415 R1 R2 37 vars not converged, Max Err/Tol 0.29930E+04 Block: M2101 Model: MIXER Block: E1201 Model: HEATX Block: H1201 Model: HEATER Block: V1201 Model: VALVE Block: R1201 Model: RPLUG Block: E1202 Model: HEATER Block: C1201 Model: COMPR Block: M1101 Model: MIXER Block: E1101 Model: HEATX Block: M101 Model: MIXER Block: E102 Model: HEATER Block: E103 Model: HEATER Block: E104 Model: HEATX Block: C201 Model: MCOMPR Block: F301 Model: FLASH2 Block: F302 Model: FLASH2 Block: M301 Model: MIXER Block: E401 Model: HEATER Block: T401 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 1 2 0.67834 Block: T402 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 7 33 32.966 2 3 12 19.847 3 5 17 5.8414 4 2 5 2.9435 5 2 4 0.17356 ** ERROR DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED VARIABLE IS AT ITS BOUND. Block: V401 Model: VALVE Block: E402 Model: HEATX Block: FS401 Model: FSPLIT Block: P401 Model: PUMP Block: C401 Model: COMPR * WARNING FEED STREAM IS BELOW DEW POINT Block: F401 Model: FLASH2 Block: P403 Model: PUMP Block: FS402 Model: FSPLIT Block: E403 Model: HEATER Block: V402 Model: VALVE Block: FS403 Model: FSPLIT Block: H1101 Model: HEATER Block: V1101 Model: VALVE Block: R1101 Model: RPLUG Block: E1102 Model: HEATER Block: C1101 Model: COMPR > Loop $OLVER01 Method: BROYDEN Iteration 7 Converging tear streams: 1108 1208 302 408 415 R1 R2 35 vars not converged, Max Err/Tol 0.15142E+04 Block: M2101 Model: MIXER Block: E1201 Model: HEATX Block: H1201 Model: HEATER Block: V1201 Model: VALVE Block: R1201 Model: RPLUG Block: E1202 Model: HEATER Block: C1201 Model: COMPR Block: M1101 Model: MIXER Block: E1101 Model: HEATX Block: M101 Model: MIXER Block: E102 Model: HEATER Block: E103 Model: HEATER Block: E104 Model: HEATX Block: C201 Model: MCOMPR Block: F301 Model: FLASH2 Block: F302 Model: FLASH2 Block: M301 Model: MIXER Block: E401 Model: HEATER Block: T401 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 1 2 0.37997 Block: T402 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 4 12 0.95289 ** ERROR DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED VARIABLE IS AT ITS BOUND. Block: V401 Model: VALVE Block: E402 Model: HEATX Block: FS401 Model: FSPLIT Block: P401 Model: PUMP Block: C401 Model: COMPR * WARNING FEED STREAM IS BELOW DEW POINT Block: F401 Model: FLASH2 Block: P403 Model: PUMP Block: FS402 Model: FSPLIT Block: E403 Model: HEATER Block: V402 Model: VALVE Block: FS403 Model: FSPLIT Block: H1101 Model: HEATER Block: V1101 Model: VALVE Block: R1101 Model: RPLUG Block: E1102 Model: HEATER Block: C1101 Model: COMPR > Loop $OLVER01 Method: BROYDEN Iteration 8 Converging tear streams: 1108 1208 302 408 415 R1 R2 35 vars not converged, Max Err/Tol -0.13075E+04 Block: M2101 Model: MIXER Block: E1201 Model: HEATX Block: H1201 Model: HEATER Block: V1201 Model: VALVE Block: R1201 Model: RPLUG Block: E1202 Model: HEATER Block: C1201 Model: COMPR Block: M1101 Model: MIXER Block: E1101 Model: HEATX Block: M101 Model: MIXER Block: E102 Model: HEATER Block: E103 Model: HEATER Block: E104 Model: HEATX Block: C201 Model: MCOMPR Block: F301 Model: FLASH2 Block: F302 Model: FLASH2 Block: M301 Model: MIXER Block: E401 Model: HEATER Block: T401 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 1 2 0.77745 Block: T402 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 4 13 3.7182 2 5 15 6.4073 3 5 20 21.001 4 2 5 9.8185 5 2 5 1.7264 6 2 4 0.52931 ** ERROR DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED VARIABLE IS AT ITS BOUND. Block: V401 Model: VALVE Block: E402 Model: HEATX Block: FS401 Model: FSPLIT Block: P401 Model: PUMP Block: C401 Model: COMPR * WARNING FEED STREAM IS BELOW DEW POINT Block: F401 Model: FLASH2 Block: P403 Model: PUMP Block: FS402 Model: FSPLIT Block: E403 Model: HEATER Block: V402 Model: VALVE Block: FS403 Model: FSPLIT Block: H1101 Model: HEATER Block: V1101 Model: VALVE Block: R1101 Model: RPLUG Block: E1102 Model: HEATER Block: C1101 Model: COMPR > Loop $OLVER01 Method: BROYDEN Iteration 9 Converging tear streams: 1108 1208 302 408 415 R1 R2 35 vars not converged, Max Err/Tol 0.20323E+04 Block: M2101 Model: MIXER Block: E1201 Model: HEATX Block: H1201 Model: HEATER Block: V1201 Model: VALVE Block: R1201 Model: RPLUG Block: E1202 Model: HEATER Block: C1201 Model: COMPR Block: M1101 Model: MIXER Block: E1101 Model: HEATX Block: M101 Model: MIXER Block: E102 Model: HEATER Block: E103 Model: HEATER Block: E104 Model: HEATX Block: C201 Model: MCOMPR Block: F301 Model: FLASH2 Block: F302 Model: FLASH2 Block: M301 Model: MIXER Block: E401 Model: HEATER Block: T401 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 1 2 0.48395 Block: T402 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 5 19 3.6521 2 3 6 0.16667 Block: V401 Model: VALVE Block: E402 Model: HEATX Block: FS401 Model: FSPLIT Block: P401 Model: PUMP Block: C401 Model: COMPR * WARNING FEED STREAM IS BELOW DEW POINT Block: F401 Model: FLASH2 Block: P403 Model: PUMP Block: FS402 Model: FSPLIT Block: E403 Model: HEATER Block: V402 Model: VALVE Block: FS403 Model: FSPLIT Block: H1101 Model: HEATER Block: V1101 Model: VALVE Block: R1101 Model: RPLUG Block: E1102 Model: HEATER Block: C1101 Model: COMPR > Loop $OLVER01 Method: BROYDEN Iteration 10 Converging tear streams: 1108 1208 302 408 415 R1 R2 30 vars not converged, Max Err/Tol 0.15375E+04 Block: M2101 Model: MIXER Block: E1201 Model: HEATX Block: H1201 Model: HEATER Block: V1201 Model: VALVE Block: R1201 Model: RPLUG Block: E1202 Model: HEATER Block: C1201 Model: COMPR Block: M1101 Model: MIXER Block: E1101 Model: HEATX Block: M101 Model: MIXER Block: E102 Model: HEATER Block: E103 Model: HEATER Block: E104 Model: HEATX Block: C201 Model: MCOMPR Block: F301 Model: FLASH2 Block: F302 Model: FLASH2 Block: M301 Model: MIXER Block: E401 Model: HEATER Block: T401 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 1 2 0.75005 Block: T402 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 7 35 31.007 2 3 12 18.910 3 5 16 5.7956 4 2 5 2.8236 5 2 4 0.16583 ** ERROR DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED VARIABLE IS AT ITS BOUND. Block: V401 Model: VALVE Block: E402 Model: HEATX Block: FS401 Model: FSPLIT Block: P401 Model: PUMP Block: C401 Model: COMPR * WARNING FEED STREAM IS BELOW DEW POINT Block: F401 Model: FLASH2 Block: P403 Model: PUMP Block: FS402 Model: FSPLIT Block: E403 Model: HEATER Block: V402 Model: VALVE Block: FS403 Model: FSPLIT Block: H1101 Model: HEATER Block: V1101 Model: VALVE Block: R1101 Model: RPLUG Block: E1102 Model: HEATER Block: C1101 Model: COMPR > Loop $OLVER01 Method: BROYDEN Iteration 11 Converging tear streams: 1108 1208 302 408 415 R1 R2 35 vars not converged, Max Err/Tol 0.15276E+04 Block: M2101 Model: MIXER Block: E1201 Model: HEATX Block: H1201 Model: HEATER Block: V1201 Model: VALVE Block: R1201 Model: RPLUG Block: E1202 Model: HEATER Block: C1201 Model: COMPR Block: M1101 Model: MIXER Block: E1101 Model: HEATX Block: M101 Model: MIXER Block: E102 Model: HEATER Block: E103 Model: HEATER Block: E104 Model: HEATX Block: C201 Model: MCOMPR Block: F301 Model: FLASH2 Block: F302 Model: FLASH2 Block: M301 Model: MIXER Block: E401 Model: HEATER Block: T401 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 1 2 0.34356 Block: T402 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 4 12 0.84783 ** ERROR DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED VARIABLE IS AT ITS BOUND. Block: V401 Model: VALVE Block: E402 Model: HEATX Block: FS401 Model: FSPLIT Block: P401 Model: PUMP Block: C401 Model: COMPR * WARNING FEED STREAM IS BELOW DEW POINT Block: F401 Model: FLASH2 Block: P403 Model: PUMP Block: FS402 Model: FSPLIT Block: E403 Model: HEATER Block: V402 Model: VALVE Block: FS403 Model: FSPLIT Block: H1101 Model: HEATER Block: V1101 Model: VALVE Block: R1101 Model: RPLUG Block: E1102 Model: HEATER Block: C1101 Model: COMPR > Loop $OLVER01 Method: BROYDEN Iteration 12 Converging tear streams: 1108 1208 302 408 415 R1 R2 30 vars not converged, Max Err/Tol 0.13257E+04 Block: M2101 Model: MIXER Block: E1201 Model: HEATX Block: H1201 Model: HEATER Block: V1201 Model: VALVE Block: R1201 Model: RPLUG Block: E1202 Model: HEATER Block: C1201 Model: COMPR Block: M1101 Model: MIXER Block: E1101 Model: HEATX Block: M101 Model: MIXER Block: E102 Model: HEATER Block: E103 Model: HEATER Block: E104 Model: HEATX Block: C201 Model: MCOMPR Block: F301 Model: FLASH2 Block: F302 Model: FLASH2 Block: M301 Model: MIXER Block: E401 Model: HEATER Block: T401 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 1 2 0.67562 Block: T402 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 4 14 3.5931 2 5 15 6.6133 3 5 21 22.465 4 2 5 10.852 5 2 5 1.6078 6 2 4 0.54973 ** ERROR DESIGN SPEC IS NOT SATISFIED BECAUSE ONE OR MORE MANIPULATED VARIABLE IS AT ITS BOUND. Block: V401 Model: VALVE Block: E402 Model: HEATX Block: FS401 Model: FSPLIT Block: P401 Model: PUMP Block: C401 Model: COMPR * WARNING FEED STREAM IS BELOW DEW POINT Block: F401 Model: FLASH2 Block: P403 Model: PUMP Block: FS402 Model: FSPLIT Block: E403 Model: HEATER Block: V402 Model: VALVE Block: FS403 Model: FSPLIT Block: H1101 Model: HEATER Block: V1101 Model: VALVE Block: R1101 Model: RPLUG Block: E1102 Model: HEATER Block: C1101 Model: COMPR > Loop $OLVER01 Method: BROYDEN Iteration 13 Converging tear streams: 1108 1208 302 408 415 R1 R2 36 vars not converged, Max Err/Tol 0.23002E+04 Block: M2101 Model: MIXER Block: E1201 Model: HEATX Block: H1201 Model: HEATER Block: V1201 Model: VALVE Block: R1201 Model: RPLUG Block: E1202 Model: HEATER Block: C1201 Model: COMPR Block: M1101 Model: MIXER Block: E1101 Model: HEATX Block: M101 Model: MIXER Block: E102 Model: HEATER Block: E103 Model: HEATER Block: E104 Model: HEATX Block: C201 Model: MCOMPR Block: F301 Model: FLASH2 Block: F302 Model: FLASH2 Block: M301 Model: MIXER Block: E401 Model: HEATER Block: T401 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 1 2 0.36627 Block: T402 Model: RADFRAC Convergence iterations: OL ML IL Err/Tol 1 5 19 5.7208 2 3 9 0.88011 Block: V401 Model: VALVE Block: E402 Model: HEATX Block: FS401 Model: FSPLIT Block: P401 Model: PUMP Block: C401 Model: COMPR * WARNING FEED STREAM IS BELOW DEW POINT *** Summary of Simulation Errors *** Physical Property System Simulation Terminal Errors 0 0 0 Severe Errors 0 0 0 Errors 0 0 13 Warnings 0 0 27 希望大神给看看查看更多 1个回答 . 2人已关注

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求化工厂电气最常用手册？ 求比较针对化工厂的常用电气手册，谢谢查看更多 0个回答 . 5人已关注

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如何测未知物？我现在有一种白色粉末，只知道是氯化钙与一种斥水性油脂混合反应，在裹覆氢氧化钠。现在我想知道这个白色粉末都有什么物质，含量是多少，大家能不能给个测试方案，因为要送出去测试，都让自己定方案。请高手们帮帮忙，万分感谢查看更多 7个回答 . 5人已关注

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求问哪本合成塔设计书籍比较好？ 要做一个非标的合成塔设计，各位前辈能否推荐一下那本书比较好？查看更多 0个回答 . 3人已关注

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什么是脱水塔，水份可以作到多少？ 什么是脱水塔，水份可以作到多少查看更多 2个回答 . 1人已关注

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2011年注册化工案例还是有难度的，哪位大虾帮忙解答下下 ...？ 3、将含苯0.4（质量分数）和甲苯0.6（质量分数）的混合液在精馏塔中进行分离，混合液进料量15000kg/h，饱和液体进料。分离要求塔顶产品含苯0.97（质量分数），塔釜产品含苯0.02（质量分数）。操作采用的回流比为3.5。再沸器用2.0MPa（A）的蒸汽加热，加热蒸汽凝结水在饱和温度下排出。若不计整个系统的热损失，再沸器每小时消耗的加热蒸汽量（kg）是下列哪个数值？操作条件下各物流的焓值（kJ/kg）物料名称饱和液体进料离开塔顶的馏出物蒸汽塔底液体产物回流液体用于再沸器的加热蒸汽加热蒸汽凝结水焓值 163 577 410 100 2798 903 （A）1376 （B）5262 （C）5943 （C）7770 4、在一填料吸收塔中，用一乙醇胺（MEA）溶剂吸收烟道气中的CO2，烟道气中含18%的CO2，其余可视为N2。吸收塔入塔混合气流量3000kg/(m2•h)；入塔液体CO2的含量为0.02kmol/kmolMEA，流量为2500 kg/(m2•h)。已知MEA的分子量为61，MEA溶液浓度为122kg/m3，操作条件下其密度为992 kg/m3，若要求吸收塔排出气体CO2的含量≤1%，则出塔液体中CO2的最小量（kmol/kmolMEA）是下列哪个数值？（A）3.01 （B）3.33 （C）5.04 （C）5.06 查看更多 7个回答 . 1人已关注

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对复合衬里的评价如何？ 为应对轻质\致密的要求,最近使用比较热闹的浇注料+纤维喷涂复合衬里,各位对其评价如何? 在石化行业质量\信誉比较好的供应商有哪些公司查看更多 4个回答 . 4人已关注

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今年注册化工考试可能延迟或者不考？ 大家顶住外界压力，按部就班地复习就是，相信会很快出考试通知的。。。。。。。查看更多 13个回答 . 1人已关注

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苯甲酸结晶？ 苯甲酸结晶aspen能做吗？怎么模拟呢查看更多 5个回答 . 5人已关注

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柴油调和基础知识？ 柴油调和基础知识查看更多 1个回答 . 1人已关注

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谁能提供粉煤气化激冷流程排放污水指标? 谁能提供粉煤气化（航天，科林）装置排放污水指标？及排放污水处理工艺？查看更多 0个回答 . 2人已关注

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关于35kv变电站设计间距问题？ 各位好，哪位师傅知道35kv变电站和更衣间的间距有没有什么要求呢？变电站里面有35kv 2台 10kv变 5台，我看了设计规范上面没有，谢谢查看更多 0个回答 . 1人已关注

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油库设计学习资料？现在正在做油库设计,请推荐基本油库设计的书. 另外, 谁能提供油库设计手册这本书的[wiki]电子[/wiki]版你在论坛里边搜一下，有《油库设计与管理》，资料区有《油品储运设计手册》，这次先不加分，留着分下次鼓励你。--qwer123 [ ]查看更多 31个回答 . 2人已关注

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氧化铜矿搅拌浸出的粒度控制？ 氧化铜矿搅拌浸出的粒度控制一般是多大？如果增大会有什么问题？查看更多 0个回答 . 3人已关注

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安监总局:上半年全国事故死亡数同比降12.8%？国家安监总局局长杨栋梁在17日召开的全国安全生产工作视频会议上说，今年上半年，全国事故起数和死亡人数同比分别下降3.7%和12.8%；重特大事故起数和死亡人数同比分别下降34.5%和52.2%。　　同时，煤矿连续15个月没有发生特别重大事故；大部分地区、行业领域安全生产状况比较稳定。但是，全国安全生产形势依然严峻复杂。个别地区重特大事故上升，非法违法导致的较大以上事故占比较高，中央企业较大以上事故时有发生。　　杨栋梁指出，下半年全国安全生产工作要建立健全“党政同责、一岗双责、齐抓共管”的安全生产责任体系；扎实推进煤矿安全生产治本攻坚；深入开展道路交通，危化品和烟花爆竹，油气输送管道、城市燃气和消防，尾矿库，应急救援和汛期安全防范等五项重点整治。查看更多 0个回答 . 3人已关注

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钢制薄壁外压圆筒的可靠性稳定系数.PDF？ 钢制薄壁外压圆筒的可靠性稳定系数.PDF查看更多 0个回答 . 1人已关注

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简介

职业：常州吉恩药业有限公司 - 项目文控

学校：洛阳理工学院 - 电气工程与自动化系

地区：黑龙江省

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