Carbon molecular sieve membranes for biogas upgrading: Techno-economic feasibility analysis

被引:52
作者
He, Xuezhong [1 ]
Chu, Yunhan [1 ]
Lindbrathen, Arne [1 ]
Hillestad, Magne [1 ]
Hagg, May-Britt [1 ]
机构
[1] Norwegian Univ Sci & Technol, Dept Chem Engn, NO-7491 Trondheim, Norway
关键词
Biogas upgrading; Carbon molecular sieve membrane; Process simulation; Cost estimation; Technology feasibility; SEPARATION; GAS; TECHNOLOGIES; PERMEATION; MODEL;
D O I
10.1016/j.jclepro.2018.05.172
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Biomethane, produced by biogas upgrading, has a great potential to replace part of the fossil fuel natural gas, and may be injected into a gas grid or used as compressed biomethane as vehicle fuel. The state-ofthe-art technologies for biogas upgrading in the European region are water scrubbing, pressure swing adsorption and chemical absorption, however, high performance carbon membranes may also have a great potential in this application. In this work, cellulose-derived hollow fiber carbon membranes were tested for CO2/CH4 separation at moderate pressures (5-20 bar), and a CO2/CH4 permeance selectivity >60 was obtained. The developed membranes were evaluated for biogas upgrading in a 1000 m(3)(STP)/h biogas plant based on HYSYS simulation and cost estimation. The results indicated that carbon membranes can be a promising candidate for biogas upgrading with a low processing cost of 0.078 $/m(3) at the feed pressure of 8.5 bar. Increased membrane performance can further reduce the cost. Moreover, a carbon membrane system can be very cost-effective for upgrading of biogas in small-scale plants of around 350 m(3)(STP)/h. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:584 / 593
页数:10
相关论文
共 23 条
[1]   COMMENTS ON IMPROVEMENTS ON A REPLACEMENT FOR THE LOGARITHMIC MEAN [J].
CHEN, JJJ .
CHEMICAL ENGINEERING SCIENCE, 1987, 42 (10) :2488-2489
[2]   A new numerical approach for a detailed multicomponent gas separation membrane model and AspenPlus simulation [J].
Chowdhury, MHM ;
Feng, XS ;
Douglas, P ;
Croiset, E .
CHEMICAL ENGINEERING & TECHNOLOGY, 2005, 28 (07) :773-782
[3]  
Davis RA, 2002, CHEM ENG TECHNOL, V25, P717, DOI 10.1002/1521-4125(20020709)25:7<717::AID-CEAT717>3.0.CO
[4]  
2-N
[5]   Separation of carbon dioxide for biogas upgrading to biomethane [J].
Ferella, Francesco ;
Puca, Alessandro ;
Taglieri, Giuliana ;
Rossi, Leucio ;
Gallucci, Katia .
JOURNAL OF CLEANER PRODUCTION, 2017, 164 :1205-1218
[6]  
Grainger D., 2007, DEV CARBON MEMBRANES
[7]   Vehicle fuel from biogas with carbon membranes; a comparison between simulation predictions and actual field demonstration [J].
Haider, Shamim ;
Lindbrathen, Arne ;
Lie, Jon Arvid ;
Carstensen, Petter Vattekar ;
Johannessen, Thorbjorn ;
Hagg, May-Britt .
GREEN ENERGY & ENVIRONMENT, 2018, 3 (03) :266-276
[8]   CO2 separation with carbon membranes in high pressure and elevated temperature applications [J].
Haider, Shamim ;
Lindbrathen, Arne ;
Lie, Jon Arvid ;
Andersen, Ingerid Caroline Tvenning ;
Hagg, May-Britt .
SEPARATION AND PURIFICATION TECHNOLOGY, 2018, 190 :177-189
[9]   Techno-economical evaluation of membrane based biogas upgrading system: A comparison between polymeric membrane and carbon membrane technology [J].
Haider, Shamim ;
Lindbrathen, Arne ;
Hagg, May-Britt .
GREEN ENERGY & ENVIRONMENT, 2016, 1 (03) :222-234
[10]   Techno-economic feasibility analysis on carbon membranes for hydrogen purification [J].
He, Xuezhong .
SEPARATION AND PURIFICATION TECHNOLOGY, 2017, 186 :117-124