Pure oxygen fixed-bed gasification of wood under high temperature (>1000 °C) freeboard conditions

被引:30
作者
Wiinikka, Henrik [1 ]
Wennebro, Jonas [1 ]
Gullberg, Marcus [1 ]
Pettersson, Esbjorn [1 ]
Weiland, Fredrik [1 ]
机构
[1] SP Energy Technol Ctr AB, Box 726, S-94128 Pitea, Sweden
关键词
Gasification; Oxygen blown; Biomass; Fixed bed; Entrained flow; ENTRAINED-FLOW GASIFICATION; BIOMASS GASIFICATION; TORREFIED WOOD; PERFORMANCE; PYROLYSIS; BEHAVIOR; WASTE; STEAM; COAL; AIR;
D O I
10.1016/j.apenergy.2017.01.054
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In this paper, the performance (syngas composition, syngas production and gasification efficiency) of an 18 kW atmospheric fixed bed oxygen blown gasifier (FOXBG) with a high temperature (>1000 degrees C) freeboard section was compared to that of a pressurized (2-7 bar) oxygen blown entrained flow biomass gasifier (PEBG). Stem wood in the form of pellets (FOXBG) or powder (PEBG) was used as fuel. The experimentally obtained syngas compositions, syngas production rates and gasification efficiencies for both gasification technologies were similar. Efficient generation of high quality syngas (in terms of high concentration and yield of CO and H-2 and low concentration and yield of CH4, heavier hydrocarbons and soot) is therefore not specific to the PEBG. Instead, efficient gasification seems to be linked to high reactor process temperatures that can also be obtained in a FOXBG. The high quality of the syngas produced in the FOXBG from fuel pellets is promising, as it suggests that in the future, much of the cost associated with milling the fuel to a fine powder will be avoidable. Furthermore, it is also implied that feedstocks that are nearly impossible to pulverize can be used as un-pretreated fuels in the FOXBG. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:153 / 162
页数:10
相关论文
共 31 条
[1]   A review on biomass gasification syngas cleanup [J].
Abdoulmoumine, Nourredine ;
Adhikari, Sushil ;
Kulkarni, Avanti ;
Chattanathan, Shyamsundar .
APPLIED ENERGY, 2015, 155 :294-307
[2]   Gasification behavior of coal and woody biomass: Validation and parametrical study [J].
Adeyemi, Idowu ;
Janajreh, Isam ;
Arink, Thomas ;
Ghenai, Chaouki .
APPLIED ENERGY, 2017, 185 :1007-1018
[3]   Techno-economic analysis of ammonia production via integrated biomass gasification [J].
Andersson, Jim ;
Lundgren, Joakim .
APPLIED ENERGY, 2014, 130 :484-490
[4]   Influence of H2O, CO2 and O2 addition on biomass gasification in entrained flow reactor conditions: Experiments and modelling [J].
Billaud, Joseph ;
Valin, Sylvie ;
Peyrot, Marine ;
Salvador, Sylvain .
FUEL, 2016, 166 :166-178
[5]   Gasification of Wood and Torrefied Wood with Air, Oxygen, and Steam in a Fixed-Bed Pilot Plant [J].
Cerone, N. ;
Zimbardi, F. ;
Villone, A. ;
Strjiugas, N. ;
Kiyikci, E. G. .
ENERGY & FUELS, 2016, 30 (05) :4034-4043
[6]   Mechanisms and Kinetics of Methane Thermal Conversion in a Syngas [J].
Dufour, Anthony ;
Valin, Sylvie ;
Castelli, Pierre ;
Thiery, Sebastien ;
Boissonnet, Guillaume ;
Zoulalian, Andre ;
Glaude, Pierre-Alexandre .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (14) :6564-6572
[7]   Performance of an effectively integrated biomass multi-stage gasification system and a steel industry heat treatment furnace [J].
Gunarathne, Duleeka Sandamali ;
Mellin, Pelle ;
Yang, Weihong ;
Pettersson, Magnus ;
Ljunggren, Rolf .
APPLIED ENERGY, 2016, 170 :353-361
[8]  
Higman C, 2008, BURLINGTON
[9]   Performance of a Pilot-Scale Entrained-Flow Black Liquor Gasifier [J].
Jafri, Yawer ;
Furusjo, Erik ;
Kirtania, Kawnish ;
Gebart, Rikard .
ENERGY & FUELS, 2016, 30 (04) :3175-3185
[10]   Using Ilmenite To Reduce the Tar Yield in a Dual Fluidized Bed Gasification System [J].
Larsson, Anton ;
Israelsson, Mikael ;
Lind, Fredrik ;
Seemann, Martin ;
Thunman, Henrik .
ENERGY & FUELS, 2014, 28 (04) :2632-2644