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利用Aspen Plus模拟焦炉煤气甲烷化过程及其热集成网络优化
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作者 彭胜 《科技创新与应用》 2015年第20期59-60,共2页
焦炉煤气甲烷化制备天然气是一种清洁高效的焦炉煤气利用方式。根据焦炉煤气组成,选择BWRS物性方法及LHHW本征动力学方程,利用Aspen Plus软件模拟3段式固定床甲烷化反应器,结果与试验数据相近。利用夹点技术进行热集成分析,消减了热负... 焦炉煤气甲烷化制备天然气是一种清洁高效的焦炉煤气利用方式。根据焦炉煤气组成,选择BWRS物性方法及LHHW本征动力学方程,利用Aspen Plus软件模拟3段式固定床甲烷化反应器,结果与试验数据相近。利用夹点技术进行热集成分析,消减了热负荷的消耗,优化余热回收过程,余热利用率从45.85%提高到88.42%。 展开更多
关键词 焦炉煤气 甲烷化反应分析 集成网络优化
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State Space Approach to Mass Exchange Network Synthesis 被引量:1
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作者 马蔚钧 胡山鹰 +1 位作者 李有润 沈静珠 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2003年第3期312-317,共6页
State space approach is an effective method to mass-exchange network (MEN) synthesis. By decomposing the network into two interactive parts, a distribution network and a process operator, the synthesis problem can be ... State space approach is an effective method to mass-exchange network (MEN) synthesis. By decomposing the network into two interactive parts, a distribution network and a process operator, the synthesis problem can be formulated into a mixed integer nonlinear programming (MINLP) model. In this article, a generalized state space model based on typical MEN is established and verified in two cases. A new asymmetrical operator and cost index are also adopted to speed up the solution process. The results demonstrate the efficiency of the proposed approach. 展开更多
关键词 mass exchange network state space SYNTHESIS OPTIMIZATION
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Step-wise synthesis of work exchange networks involving heat integration based on the transshipment model 被引量:7
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作者 Yu Zhuang Linlin Liu +1 位作者 Qilei Liu Jian Du 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2017年第8期1052-1060,共9页
Due to the deterioration of serious energy dilemma,energy-conservation and emission–reduction have been the strategic target in the past decades,thus people have identified the vital importance of higher energy effic... Due to the deterioration of serious energy dilemma,energy-conservation and emission–reduction have been the strategic target in the past decades,thus people have identified the vital importance of higher energy efficiency and the influence of lower carbon development.Since work exchange network is a significant part of energy recovery system,its optima design will have dramatically significant effect on energy consumption reduction in chemical process system.With an extension of the developed transshipment model in isothermal process,a novel step-wise methodology for synthesis of direct work exchange network(WEN)in adiabatic process involving heat integration is first proposed in this paper,where a nonlinear programming(NLP)model is formulated by regarding the minimum utility consumption as objective function and optimizing the initial WEN in accordance with the presented matching rules to get the optimized WEN configuration at first.Furthermore,we focus on the work exchange network synthesis with heat integration to attain the minimal total annual cost(TAC)with the introduction of heat-exchange equipment that is achieved by the following strategies in sequence:introducing heat-exchange equipment directly,adjusting the work quantity of the adjacent utility compressors or expanders,and approximating upper/lower pressure limits consequently to obtain considerable cost savings of expanders or compressors and work utility.Finally,a case taken from the literature is studied to illustrate the feasibility and effectiveness of the proposed method. 展开更多
关键词 Work exchange network Transshipment model Adiabatic process Trade-off between work and heat Economic analysis
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