The effect of carbon dioxide partial pressure on the gasification rate and pore development of Highveld coal chars at elevated pressures

被引:14
作者
Gouws, Saartjie M. [1 ]
Neomagus, Hein W. J. P. [1 ]
Roberts, Daniel G. [2 ]
Bunt, John R. [1 ]
Everson, Ray C. [1 ]
机构
[1] North West Univ, Coal Res Grp, Unit Energy & Technol Syst, Sch Chem & Minerals Engn, ZA-2520 Potchefstroom, South Africa
[2] CSIRO Energy, POB 883, Kenmore, Qld 4069, Australia
基金
新加坡国家研究基金会;
关键词
Carbon dioxide gasification; Elevated pressure; Highveld coal char; Pore development; INERTINITE-RICH COAL; CO2; GASIFICATION; REACTION-KINETICS; GAS-ADSORPTION; BROWN-COAL; POROSITY; STEAM; H2O;
D O I
10.1016/j.fuproc.2018.05.027
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Char structural changes occurring during gasification are normally only related to conversion and few data is published on the effect of carbon dioxide partial pressure on the extent of pore development. In this study, the char-CO2 reactivity and consequential pore development of different Highveld coal chars were investigated over a wide pressure range. Reactivity experiments were performed in a fixed bed reactor under reaction controlled conditions. The initial reaction rate was found to be solely a function of temperature and CO2 partial pressure and was well described by the Langmuir Hinshelwood rate equation. Surface analyses were performed on fresh and partially converted chars to quantify the effect of CO2 partial pressure on pore development. It was found that pores development more rapidly with conversion if the CO2 partial pressure is increased. This outcome has fundamental implications for the interpretations of gasification reaction kinetics. The term describing the total amount of active sites in the Langmuir Hinshelwood equation might not be constant at all partial pressures, and the possible impact of that is shown in this work. More work is required to further understand these effects and incorporate them appropriately into high pressure rate equations.
引用
收藏
页码:1 / 9
页数:9
相关论文
共 28 条
[1]  
BHATIA SK, 1980, AICHE J, V26, P379, DOI 10.1002/aic.690260308
[2]   On a theory of the van der Waals adsorption of gases [J].
Brunauer, S ;
Deming, LS ;
Deming, WE ;
Teller, E .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1940, 62 :1723-1732
[3]   Identification of the reaction zones occurring in a commercial-scale Sasol-Lurgi FBDB gasifier [J].
Bunt, J. R. ;
Waanders, F. B. .
FUEL, 2008, 87 (10-11) :1814-1823
[4]   Characterization of tight gas reservoir pore structure using USANS/SANS and gas adsorption analysis [J].
Clarkson, C. R. ;
Freeman, M. ;
He, L. ;
Agamalian, M. ;
Melnichenko, Y. B. ;
Mastalerz, M. ;
Bustin, R. M. ;
Radlinski, A. P. ;
Blach, T. P. .
FUEL, 2012, 95 (01) :371-385
[5]   Pore development during gasification of South African inertinite-rich chars evaluated using small angle X-ray scattering [J].
Coetzee, G. Hennie ;
Sakurovs, Richard ;
Neomagus, Hein W. J. P. ;
Morpeth, Leigh ;
Everson, Raymond C. ;
Mathews, Jonathan P. ;
Bunt, John R. .
CARBON, 2015, 95 :250-260
[6]  
du Toit G.J.D., 2013, INFLUENCE CO2 STEAM
[7]   Properties of high ash coal-char particles derived from inertinite-rich coal: II. Gasification kinetics with carbon dioxide [J].
Everson, Raymond C. ;
Neomagus, Hein W. J. P. ;
Kaitano, Rufaro ;
Falcon, Rosemary ;
du Cann, Vivien M. .
FUEL, 2008, 87 (15-16) :3403-3408
[8]   Reaction kinetics of pulverized coal-chars derived from inertinite-rich coal discards: Gasification with carbon dioxide and steam [J].
Everson, RC ;
Neomagus, HWJP ;
Kasaini, H ;
Njapha, D .
FUEL, 2006, 85 (7-8) :1076-1082
[9]  
Gadsby J., 1948, P ROYAL SOC LONDON, VA193, P357
[10]   THE REACTIVITY OF COAL CHARS GASIFIED IN A CARBON-DIOXIDE ENVIRONMENT [J].
HAMPARTSOUMIAN, E ;
MURDOCH, PL ;
POURKASHANIAN, M ;
TRANGMAR, DT ;
WILLIAMS, A .
COMBUSTION SCIENCE AND TECHNOLOGY, 1993, 92 (1-3) :105-121