Membrane air separation for intensification of coal gasification process

被引:18
作者
Belyaev, AA
Yampolskii, YP
Starannikova, LE
Polyakov, AM
Clarizia, G
Drioli, E
Marigliano, G
Barbieri, G
机构
[1] Russian Acad Sci, AV Topchiev Petrochem Synth Inst, Moscow 119991, Russia
[2] Fossil Fuels Inst, Moscow 119991, Russia
[3] Univ Calabria, Dept Chem & Mat Engn, CNR, IRMERC, I-87030 Arcavacata Di Rende, CS, Italy
关键词
air separation; intensification; coal gasification;
D O I
10.1016/S0378-3820(02)00241-2
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
High-ash and other low-quality coals are available in huge quantities in Russia and in other East European countries. Similar solid fuels can also be obtained as by-product of the enrichment process of coal. The aim of this work is the analysis of the possibility to use such low-quality coals as alternative energy sources in fluidised bed gasification process. In order to intensify gasification process in conditions where possible ash melting is avoided, it is proposed to use oxygen-enriched air (OEA) instead of air as a blow and gasification agent. The supply of OEA as fluidisation medium can be beneficial in other respects: it allows to burn at least a part of fly ash before they leave the furnace, thus improving energy efficiency and ecological impacts of the process. In this paper, the first successful example of combination of membrane air separation and coal gasification process is given. This paper summarises the performance of coal gasification in the presence of different oxygen/nitrogen mixtures as a blow for processing of low-quality (high moisture content) coal. The optimal content Of 02 in the blow is in the range 27-33% v/v. The heating value of synthesis gas obtained in optimal conditions was in the range 3.5-4.7 MJ/m(3) (STP). In second part of the paper, the performance of several membranes available for cheap and efficient air separation is analysed and, after comparing them, recommendations on appropriate selection of membrane type and module needed are given. (C) 2002 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:119 / 141
页数:23
相关论文
共 19 条
[1]   Circulating fluidized bed combustion in the turbulent regime:: modelling of carbon combustion efficiency and sulphur retention [J].
Adanez, J ;
Gayán, P ;
Grasa, G ;
de Diego, LF ;
Armesto, L ;
Cabanillas, A .
FUEL, 2001, 80 (10) :1405-1414
[2]  
ALTSHULLER VS, 1955, METHODS INTENSIFICAT
[3]  
Araki S., 1996, J JAPAN I ENERGY, V75, P839
[4]  
BELYAEV AA, 1997, THESIS MOSCOW I POWE
[5]  
BELYAEV AA, UNPUB TEPLOENERGETIC
[6]  
BELYAEV AA, 2000, INT SCH CHEM BORDE 2, P259
[7]   Use of numerical modeling in the design and scale-up of entrained flow coal gasifiers [J].
Chen, CX ;
Horio, M ;
Kojima, T .
FUEL, 2001, 80 (10) :1513-1523
[8]  
FULBE Y, 1980, CHEM COAL
[9]  
GOLLAN A, 1984, 6 IND EN CONS C HOUS
[10]  
HOGSETT JE, 1983, HYDROCARB PROCESS, V62, P52