Gas leakage measurements in a cold model of an interconnected fluidized bed for chemical-looping combustion

被引:128
作者
Johansson, E [1 ]
Lyngfelt, A [1 ]
Mattisson, T [1 ]
Johnsson, F [1 ]
机构
[1] Chalmers Univ Technol, Dept Energy Convers, S-41296 Gothenburg, Sweden
关键词
chemical-looping combustion; CO2; separation; interconnected fluidized beds; gas leakage;
D O I
10.1016/S0032-5910(03)00125-6
中图分类号
TQ [化学工业];
学科分类号
0817 [化学工程与技术];
摘要
In chemical-looping combustion (CLC) a gaseous fuel is burnt with inherent separation of the greenhouse gas carbon dioxide. The oxygen is transported from the combustion air to the fuel by means of metal oxide particles acting as oxygen carriers. A CLC system can be designed similar to a circulating fluidized bed, but with the addition of a bubbling fluidized bed on the return side. Thus, the system consists of a riser (fast fluidized bed) acting as the air reactor. This is connected to a cyclone, where the particles and the gas from the air reactor are separated. The particles fall down into a second fluidized bed, the fuel reactor, and are via a fluidized pot-seal transported back into the riser. The gas leaving the air reactor consists of nitrogen and unreacted oxygen, while the reaction products, carbon dioxide and water, come out from the fuel reactor. The water can easily be condensed and removed, and the remaining carbon dioxide can be liquefied for subsequent sequestration. The gas leakage between the reactors must be minimized to prevent the carbon dioxide from being diluted with nitrogen, or to prevent carbon dioxide from leaking to the air reactor decreasing the efficiency of carbon dioxide capture. In this system, the possible gas leakages are: (i) from the fuel reactor to the cyclone and to the pot-seal, (ii) from the cyclone down to the fuel reactor, (iii) from the pot-seal to the fuel reactor. These gas leakages were investigated in a scaled cold model. A typical leakage from the fuel reactor was 2%, i.e. a CO2 capture efficiency of 98%. No leakage was detected from the cyclone to the fuel reactor. Thus, all product gas from the air reactor leaves the system from the cyclone. A typical leakage from the pot-seal into the fuel reactor was 6%, which corresponds to 0.3% of the total air added to the system, and would give a dilution of the CO2 produced by approximately 6% air. However, this gas leakage can be avoided by using steam, instead of air, to fluidize the whole, or part of, the pot-seal. The disadvantages of diluting the CO2 are likely to motivate the use of steam. (C) 2003 Elsevier B.V. All rights reserved.
引用
收藏
页码:210 / 217
页数:8
相关论文
共 24 条
[1]
A single radiotracer particle method for the determination of solids circulation rate in interconnected fluidized beds [J].
Abellon, RD ;
Kolar, ZI ;
denHollander, W ;
deGoeij, JJM ;
Schouten, JC ;
vandenBleek, CM .
POWDER TECHNOLOGY, 1997, 92 (01) :53-60
[2]
Avidan A.A, 1997, CIRC FLUID BEDS, P466
[3]
SOLIDS EXCHANGE BETWEEN ADJACENT FLUID BEDS WITHOUT GAS MIXING [J].
CHONG, YO ;
NICKLIN, DJ ;
TAIT, PJ .
POWDER TECHNOLOGY, 1986, 47 (02) :151-156
[4]
COPELAND RJ, 2002, 27 INT TECHN C COAL
[5]
CONTROL MECHANISMS OF FLUIDIZED SOLIDS CIRCULATION BETWEEN ADJACENT VESSELS [J].
FOX, D ;
MOLODTSOF, Y ;
LARGE, JF .
AICHE JOURNAL, 1989, 35 (12) :1933-1941
[6]
SIMPLIFIED SCALING RELATIONSHIPS FOR FLUIDIZED-BEDS [J].
GLICKSMAN, LR ;
HYRE, M ;
WOLOSHUN, K .
POWDER TECHNOLOGY, 1993, 77 (02) :177-199
[7]
GOTTLICHER G, 1998, P 4 INT C GREENH GAS, P83
[8]
Experimental results of chemical-looping combustion with NiO/NiAl2O4 particle circulation at 1200 °C [J].
Ishida, M ;
Yamamoto, M ;
Ohba, T .
ENERGY CONVERSION AND MANAGEMENT, 2002, 43 (9-12) :1469-1478
[9]
A NOVEL COMBUSTOR BASED ON CHEMICAL-LOOPING REACTIONS AND ITS REACTION-KINETICS [J].
ISHIDA, M ;
JIN, HG .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1994, 27 (03) :296-301
[10]
A novel interconnected fluidised bed for the combined flash pyrolysis of biomass and combustion of char [J].
Janse, AMC ;
Biesheuvel, PM ;
Prins, W ;
van Swaaij, WPM .
CHEMICAL ENGINEERING JOURNAL, 1999, 75 (02) :121-130