Process Configurations and Simulations for a Novel Single-Column Cryogenic Air Separation Process

被引:28
作者
Zhou, Hua [1 ]
Cai, Yunan [1 ]
Xiao, Yao [1 ]
Mkhalel, Zeinab A. [1 ]
You, Biao [2 ]
Shi, Jia [1 ]
Li, Jun [1 ]
Chen, Bing H. [1 ]
机构
[1] Xiamen Univ, Dept Chem & Biochem Engn, Natl Engn Lab Green Chem Prod Alcohols Ethers Est, Coll Chem & Chem Engn, Xiamen 361005, Peoples R China
[2] Corp Beijing Mingduhoude Technol, Beijing 100022, Peoples R China
关键词
Cryogenics - Distillation - Nitrogen - Computer software - Energy utilization;
D O I
10.1021/ie3022225
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In this article, a novel single-column atmospheric cryogenic,air separation, process is proposed to reduce energy consumption through the implementation of thermal pump. technique Different from the Conventional double column cryogenic process, the new single column distillation includes a nitrogen compressor acting as a thermal pump, which makes use of the latent thermal energy of the streams in the distillation column. To verify the validity of the proposed separation process, four typical configurations of the single-column processes are constructed and simulated on the ASPEN PLUS platform with the operation conditions: air flow rate at 50 000 N m(3), inlet temperature of the distillation column at 87 k, and various nitrogen compression temperatures. The conventional double column cryogenic air separation process is also simulated as the base to compare the energy consumptions between the conventional and the novel processes., On the basis of such a comparison, the novel single-column cryogenic air separation process can save energy up to 23% and produce the products purity in industrial standard.
引用
收藏
页码:15431 / 15439
页数:9
相关论文
共 18 条
[1]  
Agrawal R., 1991, Gas separation purification, V5, P139
[2]   Compartmental modeling of high purity air separation columns [J].
Bian, SJ ;
Khowinij, S ;
Henson, MA ;
Belanger, P ;
Megan, L .
COMPUTERS & CHEMICAL ENGINEERING, 2005, 29 (10) :2096-2109
[3]   Simulation of multistream plate-fin heat exchangers of an air separation unit [J].
Boehme, R ;
Parise, JAR ;
Marques, RP .
CRYOGENICS, 2003, 43 (06) :325-334
[4]   Exergy analysis of cryogenic air separation [J].
Cornelissen, RL ;
Hirs, GG .
ENERGY CONVERSION AND MANAGEMENT, 1998, 39 (16-18) :1821-1826
[5]   A novel cryogenic air separation process based on self-heat recuperation [J].
Kansha, Yasuki ;
Kishimoto, Akira ;
Nakagawa, Tsuguhiko ;
Tsutsumi, Atsushi .
SEPARATION AND PURIFICATION TECHNOLOGY, 2011, 77 (03) :389-396
[6]   Integrated Process Module for Distillation Processes Based on Self-Heat Recuperation Technology [J].
Kansha, Yasuki ;
Tsuru, Naoki ;
Fushimi, Chihiro ;
Tsutsumi, Atsushi .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2010, 43 (06) :502-507
[7]   An innovative modularity of heat circulation for fractional distillation [J].
Kansha, Yasuki ;
Tsuru, Naoki ;
Fushimi, Chihiro ;
Shimogawara, Kaoru ;
Tsutsumi, Atsushi .
CHEMICAL ENGINEERING SCIENCE, 2010, 65 (01) :330-334
[8]  
Li Huazhi, 2009, TECHNOLOGY OXYGEN PR
[9]  
Lu M., 1974, CRYOG TECHNOL, V4, P1
[10]   Improving agility of cryogenic air separation plants [J].
Miller, Jason ;
Luyben, William L. ;
Belanger, Paul ;
Blouin, Stephane ;
Megan, Larry .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (02) :394-404