Economic assessment of Temperature Swing Adsorption systems as Claus Tail Gas Clean Up Units

被引:20
作者
Al Wahedi, Yasser [1 ,2 ]
Torres, Ana I. [1 ]
Al Hashimi, Saleh [2 ]
Dowling, Norman I. [3 ]
Daoutidis, Prodromos [1 ]
Tsapatsis, Michael [1 ]
机构
[1] Univ Minnesota, Dept Chem Engn & Mat Sci, Minneapolis, MN 55455 USA
[2] Abu Dhabi Petr Inst, Dept Chem Engn, Abu Dhabi, U Arab Emirates
[3] Alberta Sulfur Res Ltd, Ctr Appl Catalysis & Ind Sulfur Chem, Calgary, AB T2L 2K8, Canada
关键词
Sulfur recovery; Process design; Adsorption; Optimization; MIXED-METAL OXIDES; MULTIOBJECTIVE OPTIMIZATION; CU-V; H2S; REMOVAL; HYDROGEN; SORBENTS; DESIGN;
D O I
10.1016/j.ces.2014.12.015
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Current regulations of SOx emissions require Sulfur Recovery Units (SRUs) to achieve recoveries in excess of 99.9%. Capital cost of existing commercial Claus Tail gas clean up technologies capable of achieving that benchmark can amount to 45% of the total capital cost of the SRU. Adsorption based processes hold significant potential for achieving the targeted recovery at lower costs considering their high selectivity towards removal of ppm level contaminants. This work assesses the economics of a Tail Gas Treatment Unit relying on a Temperature Swing Adsorption module for treating a typical industrial feed. An optimization problem is formulated and solved to determine the designs that minimize Net Present Worth (NPWC) of total capital investment,operating and bed replacement costs ensued during a 30 years project life. The total capital investment contribution of the optimized TGTU is around $20 M comprising similar to 65% of the NPWC value. Operating costs ranged between $3.0 and $3.6 per tonne of sulfur. Both figures compare favorably with commercial technologies. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:186 / 195
页数:10
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