个人信息Personal Information
副教授
硕士生导师
性别:男
毕业院校:南开大学
学位:博士
所在单位:化工海洋与生命学院
学科:化学工程. 工业催化
电子邮箱:xiaopengzhang@dlut.edu.cn
Performance enhancement of two-stage condensation combined cycle for LNG cold energy recovery using zeotropic mixtures
点击次数:
论文类型:期刊论文
发表时间:2018-08-15
发表刊物:ENERGY
收录刊物:SCIE
卷号:157
页面范围:588-598
ISSN号:0360-5442
关键字:Two-stage condensation combined cycle; LNG cold energy; Zeotropic mixtures
摘要:The isothermal phase transition process of pure working fluids cannot effectively match the liquefied natural gas (LNG) gasification process, resulting in low efficiency of LNG cold energy power generation systems. In order to improve the temperature matching characteristics, mixed working fluids with a temperature glide during the phase change process can be adopted. In our previous study, the two-stage condensing process also effectively improved the temperature matching characteristics; thus, this paper presents a two-stage condensation combined cycle using zeotropic mixtures, and the effects of the type and number of components for mixed refrigerants on the two-stage condensing combined cycle system performance are studied. With the net power output as the objective function, the evaporation temperature, condensing temperatures, LNG expander inlet temperature, and working fluid mole fractions are optimised by the genetic algorithm. The results demonstrate that the net power output of n-05H(12) is the largest among the studied pure fluids. The net power output of the binary mixed working fluid at the optimum mole fractions is obviously superior to that of pure working fluids. The system performance is improved when the hydrocarbon mixture is selected as a working fluid, and the optimum number of components is three. (C) 2018 Elsevier Ltd. All rights reserved.
上一条:Understanding of imidazolium group hydration and polymer structure for hydroxide anion conduction in hydrated imidazolium-g-PPO membrane by molecular dynamics simulations
下一条:The effect of the arrangements for compression process and expansion process on the performance of the two-stage condensation Rankine cycle