Thermo-economic process model for thermochemical production of Synthetic Natural Gas (SNG) from lignocellulosic biomass

被引:210
作者
Gassner, Martin [1 ]
Marechal, Francois [1 ]
机构
[1] Ecole Polytech Fed Lausanne, Ind Energy Syst Lab, CH-1015 Lausanne, Switzerland
关键词
Biofuels; Gasification; Methane synthesis; CO2-removal; Thermo-economic modelling; Process design; Process integration; FLUIDIZED-BED; PROCESS DESIGN; STEAM-GASIFICATION; PILOT-SCALE; OPTIMIZATION; INTEGRATION; REMOVAL; FUEL; PERFORMANCE; OPERATION;
D O I
10.1016/j.biombioe.2009.08.004
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
A detailed thermo-economic model considering different technological alternatives for thermochemical production of Synthetic Natural Gas (SNG) from lignocellulosic biomass is presented. First, candidate technology for processes based on biomass gasification and subsequent methanation is discussed and assembled in a general superstructure. Both energetic and economic models for biomass drying with air or steam, thermal pretreatment by torrefaction or pyrolysis, indirectly and directly heated gasification, methane synthesis and carbon dioxide removal physical absorption pressure swing adsorption and polymeric membranes are then developed. Performance computations for the different process steps and some exemplary technology scenarios of integrated plants are carried out, and overall energy and exergy efficiencies in the range of 69-76% and 63-69%, respectively, are assessed. For these scenarios, the production cost of SNG including the investment depreciation is estimated to 76-107 (sic) MWh(SNG)(-1) for a plant capacity of 20 MWth,biomass, whereas 59-97 (sic) MWh(SNG)(-1) might be reached at scales of 150 MWth,biomass and above. Based on this work, a future thermo-economic optimisation will allow for deter-mining the most promising options for the polygeneration of fuel, power and heat. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1587 / 1604
页数:18
相关论文
共 76 条
[1]   Developments in membrane research: from material via process design to industrial application [J].
Abetz, Volker ;
Brinkmann, Torsten ;
Dijkstra, Marga ;
Ebert, Katrin ;
Fritsch, Detlev ;
Ohlrogge, Klaus ;
Paul, Dieter ;
Peinemann, Klaus-Viktor ;
Nunes, Suzana Pereira ;
Scharnagl, Nico ;
Schossig, Michael .
ADVANCED ENGINEERING MATERIALS, 2006, 8 (05) :328-358
[2]  
[Anonymous], DEFC2600NT40904 US D
[3]  
[Anonymous], 1985, ACID SOUR GAS TREATI
[4]  
BACON D, 1982, MODELING FLUIDIZED B, P717
[5]  
BART HJ, 2009, ULLMANNS ENCY IND CH
[6]   Basic design criteria and corresponding results performance of a pilot-scale fluidized superheated atmospheric condition steam dryer [J].
Berghel, J ;
Renström, R .
BIOMASS & BIOENERGY, 2002, 23 (02) :103-112
[7]  
*BFE, 2004, AUFD STAND CO2 GES C
[8]   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
[9]  
BOLL W, 2009, GAS PRODUCTION GAS T, pCH5
[10]  
BOLLIGER R, 2005, P 18 INT C EFF COST