Status of Flue Gas Desulphurisation (FGD) systems from coal-fired power plants: Overview of the physic-chemical control processes of wet limestone FGDs

被引:413
作者
Cordoba, Patricia [1 ,2 ]
机构
[1] Heriot Watt Univ, CICCS, IMPEE, Edinburgh EH14 4AS, Midlothian, Scotland
[2] Spanish Natl Res Council IDAEA CSIC, Inst Environm Assessment & Water Res, Barcelona 28080, Spain
关键词
Flue Gas Desulphurisation (FGD); Trace elements; Outgoing FGD (OUT-FGD) gas; FGD-gypsum; Pulverised Coal Combustion (PCC); COMBUSTION BY-PRODUCTS; TRACE-ELEMENT BEHAVIOR; BUFFER ADDITIVES; SULFUR-DIOXIDE; MASS-TRANSFER; MERCURY; GYPSUM; EMISSIONS; ABSORPTION; MODEL;
D O I
10.1016/j.fuel.2014.12.065
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
080707 [能源环境工程]; 082001 [油气井工程];
摘要
This paper presents a general review of the Flue Gas Desulphurisation (FGD) technologies used to abate sulphur emissions from coal-fired power plants, and exposes the major physic-chemical processes occurring during wet limestone FGD. The abatement capacity of major, minor, and trace elements and the fate of trace pollutants during wet limestone FGD, as well as the features of wet limestone FGD by-products are discussed. It can be stated that wet limestone FGD system is the FGD process most widely used because of its high desulphurisation performance and low operating cost. Among control parameters evaluated in this review, pH range > limestone reactivity and SO2 concentration > efficiency of particulate control devices > water re-circulation to the scrubber > entrainment of particles by the OUT-FGD gas, are the key factors of wet limestone FGDs. It is noted that, the enrichment of inorganic trace pollutants in FGD waters because of the re-circulation of water to the scrubber from gypsum slurry filtration, and the entrainment of accumulated fly ash particles in gypsum sludge, those of unreacted limestone, and the particles and droplets from gypsum slurry by the outgoing FGD (OUT-FGD) gas reduce considerably the desulphurisation efficiency and the abatement capacity of trace pollutants by wet limestone FGDs. The paper concludes with a number of issues to be investigated in depth in view of the worldwide FGD market growth and the forthcoming implementation of one of the most promising technologies to reduce CO2 emissions, oxy-fuel combustion, in Pulverised Coal Combustion (PCC)-FGD processes at an industrial scale. (c) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:274 / 286
页数:13
相关论文
共 114 条
[1]
ABETRAP European project, RFCRCT200600006
[2]
Study of the use of coal fly ash as an additive to minimise fluoride leaching from FGD gypsum for its disposal [J].
Alvarez-Ayuso, E. ;
Querol, X. .
CHEMOSPHERE, 2008, 71 (01) :140-146
[3]
Stabilization of FGD gypsum for its disposal in landfills using amorphous aluminium oxide as a fluoride retention additive [J].
Alvarez-Ayuso, E. ;
Querol, X. .
CHEMOSPHERE, 2007, 69 (02) :295-302
[4]
Environmental impact of a coal combustion-desulphurisation plant:: Abatement capacity of desulphurisation process and environmental characterisation of combustion by-products [J].
Alvarez-Ayuso, E. ;
Querol, X. ;
Tomas, A. .
CHEMOSPHERE, 2006, 65 (11) :2009-2017
[5]
[Anonymous], 2006, REFERENCE DOCUMENT B
[6]
[Anonymous], EN124574
[7]
Argarwal RS, 1993, EPA600R95015, V3, P78
[8]
A study of trace element behaviour in two modern coal-fired power plants - II. Trace element balances in two plants equipped with semi-dry flue gas desulphurisation facilities [J].
Aunela-Tapola, L ;
Hatanpaa, E ;
Hoffren, H ;
Laitinen, T ;
Larjava, K ;
Rasila, P ;
Tolvanen, M .
FUEL PROCESSING TECHNOLOGY, 1998, 55 (01) :13-34
[9]
Babcock & Wilcox Power Generation Group (B&W), 1991, STEAM ITS GENERATION, P980
[10]
Babu M, 1986, P 3 ANN PITTSB COAL