CIESC Journal ›› 2019, Vol. 70 ›› Issue (12): 4689-4697.DOI: 10.11949/0438-1157.20190888
• Process system engineering • Previous Articles Next Articles
Rui YANG1(),Yu ZHUANG1,2,Nanxi DI1,Jian DU1(
)
Received:
2019-08-06
Revised:
2019-08-16
Online:
2019-12-05
Published:
2019-12-05
Contact:
Jian DU
通讯作者:
都健
作者简介:
杨蕊(1994—),女,硕士研究生,基金资助:
CLC Number:
Rui YANG, Yu ZHUANG, Nanxi DI, Jian DU. Synthesis of heat integrated with indirect power exchange networks based on superstructure model[J]. CIESC Journal, 2019, 70(12): 4689-4697.
杨蕊, 庄钰, 邸楠茜, 都健. 基于超结构法的热集成间接式功交换网络综合[J]. 化工学报, 2019, 70(12): 4689-4697.
流股 | 流量F/(kg·s-1) | 入口温度T in/K | 出口温度T out/K | 入口压力P in /kPa | 出口压力P out /kPa | 热容Cp /(kJ·(kg·K)-1) | 最高温度/K | 最低温度/K |
---|---|---|---|---|---|---|---|---|
HP1 | 12 | 410 | 600 | 900 | 100 | 2.454 | 700 | 273 |
HP2 | 18 | 355 | 500 | 850 | 150 | 0.982 | 700 | 273 |
LP1 | 15 | 600 | 350 | 100 | 700 | 1.432 | 700 | 273 |
LP2 | 18 | 600 | 360 | 100 | 900 | 2.454 | 700 | 273 |
Table 1 Streams properties for the case
流股 | 流量F/(kg·s-1) | 入口温度T in/K | 出口温度T out/K | 入口压力P in /kPa | 出口压力P out /kPa | 热容Cp /(kJ·(kg·K)-1) | 最高温度/K | 最低温度/K |
---|---|---|---|---|---|---|---|---|
HP1 | 12 | 410 | 600 | 900 | 100 | 2.454 | 700 | 273 |
HP2 | 18 | 355 | 500 | 850 | 150 | 0.982 | 700 | 273 |
LP1 | 15 | 600 | 350 | 100 | 700 | 1.432 | 700 | 273 |
LP2 | 18 | 600 | 360 | 100 | 900 | 2.454 | 700 | 273 |
设备单元 | 固定设备投资×10-3/ (USD·a-1) | 可变设备投资×10-3/(USD·a-1) | 操作费用/(USD·(kW·h)-1) |
---|---|---|---|
膨胀阀 | 2 | 1 | — |
公用工程涡轮机 | 200 | 1 | 0.10 |
公用工程压缩机 | 250 | 1 | 0.12 |
SSTC涡轮机 | 40 | 1 | — |
SSTC压缩机 | 50 | 1 | — |
Table 2 Cost parameters for the case
设备单元 | 固定设备投资×10-3/ (USD·a-1) | 可变设备投资×10-3/(USD·a-1) | 操作费用/(USD·(kW·h)-1) |
---|---|---|---|
膨胀阀 | 2 | 1 | — |
公用工程涡轮机 | 200 | 1 | 0.10 |
公用工程压缩机 | 250 | 1 | 0.12 |
SSTC涡轮机 | 40 | 1 | — |
SSTC压缩机 | 50 | 1 | — |
来源 | W SSTC/kW | WE /kW | WC /kW | TAC×10-3/(USD·a-1) |
---|---|---|---|---|
本文 | 3052.4 | 7907.3 | 17884.2 | 13652.8 |
文献[ | 7770 | 13832 | 2987 | 14405 |
Table 3 Solution comparison of two different configurations
来源 | W SSTC/kW | WE /kW | WC /kW | TAC×10-3/(USD·a-1) |
---|---|---|---|---|
本文 | 3052.4 | 7907.3 | 17884.2 | 13652.8 |
文献[ | 7770 | 13832 | 2987 | 14405 |
1 | Linnhoff B , Flower J R . Synthesis of heat exchanger networks(Ⅰ): Systematic generation of energy optimal networks[J]. AIChE Journal, 1978, 24(4): 633-642. |
2 | 都健, 李春妮, 陈理 .基于虚拟温度法的间歇过程换热网络结构优化[J]. 化工学报, 2010, 61(12): 3162-3166. |
Du J , Li C N , Chen L . Structure optimization of heat exchanger network for batch processes based on pseudo-temperature[J]. CIESC Journal, 2010, 61(12): 3162-3166. | |
3 | Papoulias S A , Grossmann I E . A structural optimization approach in process synthesis(Ⅱ): Heat recovery networks[J]. Computers & Chemical Engineering, 1983, 7(6): 707-721. |
4 | Yee T F , Grossmann I E . Simultaneous optimization models for heat integration(Ⅱ): Heat exchanger network synthesis[J]. Computers & Chemical Engineering, 1990, 14(10): 1165-1184. |
5 | Huang Y L , Fan L T . Analysis of a work exchanger network[J]. Industrial & Engineering Chemistry Research, 1996, 35(10): 3528-3538. |
6 | Liu G , Hua Z , Shen R , et al . A graphical method for integrating work exchange network[J]. Applied Energy, 2014, 114(2): 588-599. |
7 | Zhuang Y , Liu L L , Zhang L , et al . Upgraded graphical method for the synthesis of direct work exchanger networks[J]. Industrial & Engineering Chemistry Research, 2017, 56: 14304-14315. |
8 | 庄钰, 刘琳琳, 李继龙, 等 . 基于转运模型的功交换网络综合[J]. 化工进展, 2015, 34(4): 952-956 |
Zhuang Y , Liu L L , Li J L , et al . Synthesis of work exchange network based on transshipment model[J]. Chemical Industry & Engineering Progress, 2015, 34(4): 952-956. | |
9 | Zhuang Y , Liu L L , Zhang L , et al . Direct work exchanger network synthesis of isothermal process based on improved transshipment model[J]. Journal of the Taiwan Institute of Chemical Engineers, 2017, 81: 295-304. |
10 | Zhuang Y , Liu L L , Liu Q L , et al . Step-wise synthesis of work exchange networks involving heat integration based on the transshipment model[J]. Chinese Journal of Chemical Engineering, 2017, 25(8): 1052-1060. . |
11 | Zhuang Y , Liu L , Zhang L , et al . An extended superstructure modeling method for simultaneous synthesis of direct work exchanger networks[J]. Chemical Engineering Research & Design, 2019, 144(1): 258-271. |
12 | Razib M S , Hasan M M F , Karimi I A . Pressure management using optimal compressor networks[C]// 8th World Congress of Chemical Engineering: Incorporating the 59th Canadian Chemical Engineering Conference and the 24th Interamerican Congress of Chemical Engineering. 2009. |
13 | Razib M S , Hasan M M F , Karimi I A . Preliminary synthesis of work exchange networks[J]. Computers & Chemical Engineering, 2012, 37: 262-277. |
14 | 周华, 刘桂莲, 冯霄 . 考虑效率的功交换网络问题表格法[J]. 化工学报, 2011, 62(6): 1600-1605. |
Zhou H , Liu G L , Feng X . Problem table method for work exchange network with efficiency considered[J]. CIESC Journal, 2011, 62(6): 1600-1605. | |
15 | 陈慧, 冯霄 . 考虑经济性的功量交换网络的最优匹配[J]. 清华大学学报(自然科学版), 2012, 52(3): 298-302. |
Chen H , Feng X . Optimized work exchange networks with economic consideration[J]. J. Tsinghua Univ. (Sci. & Tech.), 2012, 52(3: 298-302. | |
16 | Zhuang Y , Liu L L , Zhang L , et al . Synthesis of indirect work exchange networks considering both isothermal and adiabatic process together with exergy analysis[J]. Chinese Journal of Chemical Engineering, 2018, 26(8): 1644-1652. |
17 | Aspelund A , Berstad D O , Gundersen T . An extended pinch analysis and design procedure utilizing pressure based exergy for subambient cooling[J]. Applied Thermal Engineering, 2007, 27(16): 2633-2649. |
18 | Gundersen T , Berstad D O , Aspelund A . Extending pinch analysis and process integration into pressure and fluid phase considerations[J]. Chemical Engineering Transactions, 2009, 18: 33-38. |
19 | Fu C , Gundersen T . Sub-ambient heat exchanger network design including expanders[J]. Chemical Engineering Science, 2015, 138: 712-729. |
20 | Fu C , Gundersen T . Integrating expanders into heat exchanger networks above ambient temperature[J]. AIChE Journal, 2015, 61(10): 3404-3422. |
21 | Fu C , Gundersen T . Sub-ambient heat exchanger network design including compressors[J]. Chemical Engineering Science, 2015, 137: 631-645. |
22 | Fu C , Gundersen T . Integrating compressors into heat exchanger networks above ambient temperature[J]. AIChE Journal, 2015, 61(11): 3770-3785. |
23 | Wechsung A , Aspelund A , Gundersen T , et al . Synthesis of heat exchanger networks at subambient conditions with compression and expansion of process streams[J]. AIChE Journal, 2011, 57(8): 2090-2108. |
24 | Onishi V C , Ravagnani M A S S , Caballero J A . Simultaneous synthesis of work exchange networks with heat integration[J]. Chemical Engineering Science, 2014, 112: 87-107. |
25 | Onishi V C , Ravagnani M A S S , Caballero J A . Simultaneous synthesis of heat exchanger networks with pressure recovery: optimal integration between heat and work[J]. AIChE Journal, 2014, 60(3): 893-908. |
26 | Onishi V C , Ravagnani M A S S , Jiménez L , et al . Multi-objective synthesis of work and heat exchange networks: optimal balance between economic and environmental performance[J]. Energy Conversion Management, 2017, 140: 192-202. |
27 | Huang K F , Karimi I A . Work-heat exchanger network synthesis(WHENS)[J]. Energy, 2016, 113: 1006-1017. |
28 | Nair S K , Rao H N , Karimi I A . Framework for work-heat exchange network synthesis [J]. AIChE Journal, 2018, 64(7): 2472-2485. |
29 | Onishi V C , Quirante N , Ravagnani M A S S , et al . Optimal synthesis of work and heat exchangers networks considering unclassified process streams at sub and above-ambient conditions[J]. Applied Energy, 2018, 224: 567-581. |
30 | Yu H S , Fu C , Vikse M , et al . Identifying optimal thermodynamic paths in work and heat exchange network synthesis[J]. AIChE Journal, 2019, 65(2): 549-561. |
31 | Zhuang Y , Zhang L , Liu L L , et al . Simultaneous synthesis of WHEN based on superstructure modelling considering thermodynamic and economic factors[J]. Computers Aided Chemical Engineering, 2018, 44: 1033-1038. |
Viewed | ||||||||||||||||||||||||||||||||||||||||||||||||||
Full text 93
|
|
|||||||||||||||||||||||||||||||||||||||||||||||||
Abstract 366
|
|
|||||||||||||||||||||||||||||||||||||||||||||||||