Techno-economic evaluation of biogas upgrading process using CO2 facilitated transport membrane

被引:206
作者
Deng, Liyuan [1 ]
Hagg, May-Britt [1 ]
机构
[1] Norwegian Univ Sci & Technol NTNU, Dept Chem Engn, Fac Nat Sci & Technol, NO-7491 Trondheim, Norway
关键词
Biogas upgrading; CO2; separation; Membrane process; Process optimization; Biomethane; CO2-SELECTIVE POLYMER MEMBRANES; QUALITY NATURAL-GAS; PROCESS DESIGN; ACID GASES; CAPTURE; OPTIMIZATION; ECONOMICS; REMOVAL; PLANT;
D O I
10.1016/j.ijggc.2009.12.013
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The biogas upgrading by membrane separation process using a highly efficient CO2-selective polyvinylamine/polyvinylalcohol (PVAm/PVA) blend membrane was investigated by experimental study and simulation with respect to process design, operation optimization and economic evaluation. This blend membrane takes advantages of the unique CO2 facilitated transport from PVAm and the robust mechanical properties from PVA, exhibits both high CO2/CH4 separation efficiency and very good stability. CO2 transports through the water swollen membrane matrix in the form of bicarbonate. CO2/CH4 selectivity up to 40 and CO2 permeance up to 0.55 m(3)(STP)/m(2) h bar at 2 bar were documented in lab with synthesized biogas (35% CO2 and 65% CH4). Membrane performances at varying feed pressures were recorded and used as the simulation basis in this work. The process simulation of an on-farm scale biogas upgrading plant (1000 Nm(3)/h) was conducted. Processes with four different membrane module configurations with or without recycle were evaluated technically and economically, and the 2-stage in cascade with recycle configuration was proven optimal among the four processes. The sensitivity of the process to various operation parameters was analyzed and the operation conditions were optimized. (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:638 / 646
页数:9
相关论文
共 26 条
[1]  
[Anonymous], 2009, CHEM ENG
[2]   Future directions of membrane gas separation technology [J].
Baker, RW .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (06) :1393-1411
[3]   MEMBRANE PROCESSES FOR THE REMOVAL OF ACID GASES FROM NATURAL-GAS .2. EFFECTS OF OPERATING-CONDITIONS, ECONOMIC-PARAMETERS, AND MEMBRANE-PROPERTIES [J].
BHIDE, BD ;
STERN, SA .
JOURNAL OF MEMBRANE SCIENCE, 1993, 81 (03) :239-252
[4]   MEMBRANE PROCESSES FOR THE REMOVAL OF ACID GASES FROM NATURAL-GAS .1. PROCESS CONFIGURATIONS AND OPTIMIZATION OF OPERATING-CONDITIONS [J].
BHIDE, BD ;
STERN, SA .
JOURNAL OF MEMBRANE SCIENCE, 1993, 81 (03) :209-237
[5]   Facilitated transport of CO2 in novel PVAm/PVA blend membrane [J].
Deng, Liyuan ;
Kim, Taek-Joong ;
Haegg, May-Britt .
JOURNAL OF MEMBRANE SCIENCE, 2009, 340 (1-2) :154-163
[6]  
GRAINGER D, 2007, CARBON MEMBRANES HYD, P150
[7]   Techno-economic evaluation of a PVAmCO2-selective membrane in an IGCC power plant with CO2 capture [J].
Grainger, David ;
Haegg, May-Britt .
FUEL, 2008, 87 (01) :14-24
[8]   Polymeric facilitated transport membranes for hydrogen purification [J].
Hagg, May-Britt ;
Quinn, Robert .
MRS BULLETIN, 2006, 31 (10) :750-755
[9]   CO2 capture from natural gas fired power plants by using membrane technology [J].
Hägg, MB ;
Lindbråthen, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (20) :7668-7675
[10]   Upgrading low-quality natural gas with H2S- and CO2-selective polymer membranes -: Part II.: Process design, economics, and sensitivity study of membrane stages with recycle streams [J].
Hao, J. ;
Rice, P. A. ;
Stern, S. A. .
JOURNAL OF MEMBRANE SCIENCE, 2008, 320 (1-2) :108-122