期刊文献+
共找到3篇文章
< 1 >
每页显示 20 50 100
Design and Control of Self-Heat Recuperative Distillation Process for Separation of Close-Boiling Mixtures: n-Butanol and iso-Butanol 被引量:3
1
作者 Li Lumin Liu Yuliang +2 位作者 Zhai Jian Sun Lanyi Tian Yuanyu 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2015年第4期111-120,共10页
In order to explore the advantages of self-heat recuperative distillation(SHRD) process, the design and control of the SHRD process was studied for the separation of n-butanol and iso-butanol mixtures. The economic su... In order to explore the advantages of self-heat recuperative distillation(SHRD) process, the design and control of the SHRD process was studied for the separation of n-butanol and iso-butanol mixtures. The economic superiority of SHRD process is presented when a comparison on the total annual cost(TAC) of the conventional distillation process, the vapor recompression distillation process and the SHRD process was made. For the SHRD process, 37.74% and 11.35% savings of TAC can be achieved as compared to the conventional distillation process and vapor recompression distillation process, respectively. The dynamic characteristics of this promising SHRD sequence had been studied, and the dynamic responses demonstrated that 10% changes in both feed flow rate and feed composition can be well handled by the control strategy with dual-temperature control. It is proven that the SHRD system not only can provide economical savings but also can operate normally with good controllability. 展开更多
关键词 n-butanol iso-butanol self-heat recuperative distillation total annual cost control
在线阅读 下载PDF
Maximum useful energy rate and efficiency of a recuperative Brayton cogeneration plant
2
作者 郝小礼 张国强 《Journal of Central South University》 SCIE EI CAS 2013年第1期156-163,共8页
A thermodynamic model was developed to analyze the performance of cogeneration plant based on irreversible recuperative Brayton cycle. A parameter, dimensionless total useful energy rate (DTUER), was used as the crite... A thermodynamic model was developed to analyze the performance of cogeneration plant based on irreversible recuperative Brayton cycle. A parameter, dimensionless total useful energy rate (DTUER), was used as the criterion for performance optimization of cogeneration plant. The effects of cycle parameters, internal irreversibilities, and recuperator efficiency on maximum DTUER and on the efficiency at maximum DTUER were numerically investigated. The relation between DTUER and cogeneration efficiency was also analyzed. The results show that there exists an optimal compressor pressure ratio which maximizes the DTUER. It is also found that there exists an optimal power-to-heat ratio which results in a dual-maximum DTUER. 展开更多
关键词 recuperative Brayton cycle COGENERATION OPTIMIZATION THERMODYNAMICS
在线阅读 下载PDF
间壁式液-液热交换实验及其信息化过程研究——1.工程实验、类似率分析与信息化过程(下)
3
作者 段毅文 张友谊 +1 位作者 王云飞 都丽娜 《内蒙古石油化工》 CAS 2014年第22期4-7,共4页
由图34、图35、图36和图37的数据分析,可知:从冷流体进口端到热流体进口端之间,在热流体雷诺数增大(1905.044-23101.71)过程中,l=0.9时:热流体温度增加10.8℃(温32.3-43.1℃),l=0.7时:热流体温度增加10.1℃(温33.8-43.9℃),l=... 由图34、图35、图36和图37的数据分析,可知:从冷流体进口端到热流体进口端之间,在热流体雷诺数增大(1905.044-23101.71)过程中,l=0.9时:热流体温度增加10.8℃(温32.3-43.1℃),l=0.7时:热流体温度增加10.1℃(温33.8-43.9℃),l=0.5时:热流体温度增加9.2℃(温35.4-44.6℃),l=0.1时:热流体温度仅增加7.2℃(温38.8-46.0℃);l=0.9时:壁面温度增加12.4℃(温15.7-28.1℃),l=0.7时:壁面温度增加13.6℃(温17.5—31.1℃),l=0.5时:壁面温度增加14.9℃(温19.3—34.2℃),l=0.1时:壁面温度增加17.3℃(温22.9—40.2℃);1=0.9时:冷流体温度增加-0.1℃(温11.4—11.3℃),l=0.7时:冷流体温度增加1.2℃(温11.8—13.0℃),l=0.5时:冷流体温度增加2.5℃(温12.2—14.7℃),l=0.1时: 展开更多
关键词 recuperative LIQUID-LIQUID Heat EXCHANGE COMPUTER Aided Simulation Experimental Re-search Informization Process LORENTZ Force
在线阅读 下载PDF
上一页 1 下一页 到第
使用帮助 返回顶部