High-pressure co-gasification of coal with biomass and petroleum coke

被引：165

作者：

Fermoso, J. ^{[1
]}

Arias, B. ^{[1
]}

Plaza, M. G. ^{[1
]}

Pevida, C. ^{[1
]}

Rubiera, F. ^{[1
]}

Pis, J. J. ^{[1
]}

Garcia-Pena, F. ^{[2
]}

Casero, P. ^{[2
]}

机构：

[1] CSIC, Inst Nacl Carbon, E-33080 Oviedo, Spain

[2] Elcogas SA CT GICC Puertollano, Ciudad Real, Spain

来源：

FUEL PROCESSING TECHNOLOGY | 2009年 / 90卷 / 7-8期

关键词：

Hydrogen; Co-gasification; High pressure; Coal; Biomass; SPOUT-FLUID BED; HYDROGEN-PRODUCTION SYSTEMS; STEAM GASIFICATION; PART; ELECTRICITY; CONVERSION; CAPTURE; REACTOR; STORAGE; WASTES;

D O I：

10.1016/j.fuproc.2009.02.006

中图分类号：

O69 [应用化学];

学科分类号：

070301 [无机化学];

摘要：

The effects of the main operation variables (temperature, pressure and gasifying agent composition) on gas production and other process parameters, such as carbon conversion, cold gas efficiency and high heating value, during the steam-oxygen gasification of a bituminous coal were studied. It was observed that temperature and oxygen concentration were the most influential variables during the gasification process. In addition, co-gasification tests of binary blends of a bituminous coal with different types of biomass (up to 10%) and petroleum coke (up to 60%), as well as ternary blends of coal-petcoke-biomass (45-45-10%) were conducted in order to study the effect of blending on gas production and carbon conversion. (C) 2009 Elsevier B.V. All rights reserved.

引用

页码：926 / 932

页数：7

共 27 条

[1]

Fluidised bed co-gasification of coal and olive oil industry wastes [J].