EXERGOECONOMIC ANALYSIS AND OPTIMIZATION OF MULTI-STAGE GAS COMPRESSION PROCESSES

Petroleum Processing and Petrochemicals ›› 2019, Vol. 50 ›› Issue (9): 70-74.

EXERGOECONOMIC ANALYSIS AND OPTIMIZATION OF MULTI-STAGE GAS COMPRESSION PROCESSES

Received:2018-12-03 Revised:2019-02-27 Online:2019-09-12 Published:2019-09-25
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Abstract

Abstract: Exergoeconomic analysis was conducted on an actual cracking gas multi-stage compression process based on simulation data from Aspen Plus. The impacts of number of compressing stages on the total economic performance at different prices of input exergy were studied to reveal the relationship between optimal stage number and price of input exergy. The results obtained showed that the higher the price of input exergy, the more the impact of the stage number on the total cost. The optimal stage number increased as the price of the input exergy increased. Among them,the optimal number of compressor stage was 3 When the price of input exergy was 0.31-0.0.58 Yuan/(kW.h),When price of input exergy was 0.59-0.94 Yuan/(kW.h), the optimal number of stage was 4, and as input exergy exceeded 0.94 Yuan/(kW.h), the optimal number of stages was 5 at least.

Key words: cracking gas, exergoeconomic analysis, optimization of energy utilization, multi-stage compression

CLC Number:

References

[1] 华贲.工艺过程用能分析及综合[M].北京:烃加工出版社,1989,29-33.
[2] 陈清林,尹清华,华贲.过程系统?经济学优化策略[J].石油学报(石油加工),2000,16(3):70-77.
[3] TSATSARONIS G. Thermoeconomic analysis and optimization of energy systems[J].Progress of Energy Combust Science, 1993,19(3):227-257.
[4] TSATSARONIS G , MOROSUK T. Advanced exergetic analysis of a novel system for generating electricity and vaporizing liquefied natural gas[J].Energy,2010,35(2): 820-829.
[5] KELLY S , TSATSARONIS G , MOROSUK T. Advanced exergetic analysis : Approaches for splitting the exergy destruction into endogenous and exogenous parts[J]. Energy ,2009, 34(3):384-391
[6] HUA B , CHEN Q L , WANG P. A new exergoeconomic approach for analysis and optimization of energy systems[J].Energy, 1997, 22(11): 1071-1078.
[7] CHEN Q L, YIN Q H, HUA B. An exergoeconomic approach for retrofit of fractionating systems[J].Energy,2002,27(1):65-75.
[8] 郭伟新,陆航宇,万向成,等.基于Aspen Plus模拟的气体多级压缩过程?分析[J].石油炼制与化工,2018.
[9] 陈清林,尹清华,王松平,等.过程系统能量流结构模型及其应用[J].化工进展,2003,22(3):239-243.
[10] 华贲.炼油过程用能技术经济分析[J].炼油设计,1982,7(5):54-66.
[11] 华贲.过程系统的能量综合和优化[J].化工进展,1994,13(3):6-15.
[12] 王松平,尹清华,陈清林,等.?传递规律——基础理论研究[J].华南理工大学学报(自然科学版),1998,26(6):30-36.
[13] R. Smith. Chemical Process Design and Integration[M]. John Wiley And Sons, Ltd, 2005,17-33.
[14] H. Silla. Analysis , Synthesis , and Design of Chemical Processes [M]. Pearson Education Inc, 2012,162-168.
[15] 谭天恩等.化工原理(上册)[M].北京:化学工业出版社,2006,142-146.
[16] 魏志强,张冰剑,吴升元,等.?经济分解协调优化中的量化评价及工程应用[J].石油学报(石油加工),2012,28(2):281-288.