Alie, C.; Backham, L.; Croiset, E.; Douglas, P.L., E-mail: pdouglas@uwaterloo.ca2005
AbstractAbstract
[en] Technically, the capture of CO2 from the flue gas of natural gas/coal fired power plants, using a monoethanolamine (MEA) absorption process is a viable short to medium term strategy for mitigation of the atmospheric CO2 emissions from large point sources. The costs, however, of such systems are currently perceived to be too high to be economically feasible. A practical research objective is the analysis of the CO2 capture process with a view towards minimizing the cost of implementation. Because large scale CO2 capture operations are expensive, process simulation and modelling have an important role to play in evaluation of the process alternatives. In the case of amine scrubbing, the convergence of the process flow sheet is a nontrivial exercise due to the highly nonlinear nature of the process and the large recycle stream involved. This paper presents a method of decomposing the flow sheet that assists in converging the process flow sheet and in optimizing key process operating variables, in particular the amine loadings and temperature of MEA entering the stripper. This method was applied to three different CO2 concentrations (molar fraction, wet basis): 3% (to simulate flue gas from a gas turbine), 14% (flue gas from a coal plant) and 25% (flue gas from a cement plant). The decomposition method proved useful for investigation of the process parameters in both the absorber and the stripper. The results from the decoupled flow sheet provided good initial estimates for the convergence of the integrated flow sheet. The results from the decoupled and integrated flow sheets were similar. A minimum reboiler duty was found at a lean MEA loading of 0.25 for all CO2 concentrations studied
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Source
S0196890404000822; Copyright (c) 2004 Elsevier Science B.V., Amsterdam, The Netherlands, All rights reserved.; Country of input: International Atomic Energy Agency (IAEA)
Record Type
Journal Article
Journal
Country of publication
AIR POLLUTION CONTROL, AMINES, CARBON COMPOUNDS, CARBON OXIDES, CHALCOGENIDES, CONTROL, DRUGS, EQUIPMENT, GASEOUS WASTES, INDUSTRY, MACHINERY, ORGANIC COMPOUNDS, ORGANIC SULFUR COMPOUNDS, OXIDES, OXYGEN COMPOUNDS, POLLUTION CONTROL, POWER PLANTS, RADIOPROTECTIVE SUBSTANCES, RESPONSE MODIFYING FACTORS, SEPARATION PROCESSES, THERMAL POWER PLANTS, THIOLS, TURBINES, TURBOMACHINERY, WASTES
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Nguyen, T.T.; Backham, L., E-mail: leslie.backham@areva.ca
Uranium 2010: The Future is U. Proceedings Volume 1 and 22010
Uranium 2010: The Future is U. Proceedings Volume 1 and 22010
AbstractAbstract
[en] Midwest is a unique uranium deposit with exceptionally high arsenic content. The ore body is located 17 km west of the McClean Lake operation. The McClean Lake mill will be modified to process Midwest ore and handle solid wastes from the Midwest water treatment plant. This paper describes the modifications required of the McClean Lake mill, process challenges associated with treatment of the arsenic, and the possibility of recovering nickel and cobalt as a by-product. It also reviews the complexity in the design of the Midwest water treatment facility which incorporates reverse osmosis technology with conventional physical-chemical water treatment. (author)
Primary Subject
Source
Lam, E.K. (Cameco, Port Hope, Ontario (Canada)); Rowson, J.W. (AREVA Resources, Saskatoon, Saskatchewan (Canada)); Ozberk, E. (Cameco, Saskatoon, Saskatchewan (Canada)) (eds.); The Canadian Inst. of Mining, Metallurgy and Petroleum, Westmount, Quebec (Canada); 2 v; ISBN 1-894475-97-6; ; 2010; (v.1) p. 439-450; Uranium 2010 The Future is U: 3. International Conference on Uranium; Saskatoon, Saskatchewan (Canada); 15-18 Aug 2010; 40. Annual Hydrometallurgy Meeting; Saskatoon, Saskatchewan (Canada); 15-18 Aug 2010; Available from The Canadian Inst. of Mining, Metallurgy and Petroleum, Westmount, Quebec (Canada); 12 refs., 3 tabs., 2 figs.
Record Type
Miscellaneous
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Conference
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