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DOI	10.2172/6094135
报告编号	DOE/PC/89867-T2
来源ID	OSTI_ID: 6094135
	Slurry reactor design studies
	Fox, J.M.; Degen, B.D.; Cady, G.; Deslate, F.D.; Summers, R.L. (Bechtel Group, Inc., San Francisco, CA (USA)); Akgerman, A. (Texas A and M Univ., College Station, TX (USA)); Smith, J.M. (California Univ., Davis, CA (USA))
英文摘要	The objective of these studies was to perform a realistic evaluation of the relative costs of tublar-fixed-bed and slurry reactors for methanol, mixed alcohols and Fischer-Tropsch syntheses under conditions where they would realistically be expected to operate. The slurry Fischer-Tropsch reactor was, therefore, operated at low H{sub 2}/CO ratio on gas directly from a Shell gasifier. The fixed-bed reactor was operated on 2.0 H{sub 2}/CO ratio gas after adjustment by shift and CO{sub 2} removal. Every attempt was made to give each reactor the benefit of its optimum design condition and correlations were developed to extend the models beyond the range of the experimental pilot plant data. For the methanol design, comparisons were made for a recycle plant with high methanol yield, this being the standard design condition. It is recognized that this is not necessarily the optimum application for the slurry reactor, which is being proposed for a once-through operation, coproducing methanol and power. Consideration is also given to the applicability of the slurry reactor to mixed alcohols, based on conditions provided by Lurgi for an Octamix{trademark} plant using their standard tubular-fixed reactor technology. 7 figs., 26 tabs.
出版年	1990
报告类型	Technical Report
语种	英语
国家	美国
来源学科分类	01 COAL, LIGNITE, AND PEAT ; CHEMICAL REACTORS ; DESIGN ; COAL LIQUEFACTION ; CHEMICAL REACTION KINETICS ; FISCHER-TROPSCH SYNTHESIS ; CATALYSTS ; COMPILED DATA ; COST ; HEAT TRANSFER ; HYDRODYNAMICS ; IRON ; MASS TRANSFER ; METHANOL ; PACKED BED ; PROGRESS REPORT ; SYNTHESIS GAS ; ALCOHOLS ; CHEMICAL REACTIONS ; DATA ; DOCUMENT TYPES ; ELEMENTS ; ENERGY TRANSFER ; FLUID MECHANICS ; FLUIDS ; GASES ; HYDROXY COMPOUNDS ; INFORMATION ; KINETICS ; LIQUEFACTION ; MECHANICS ; METALS ; NUMERICAL DATA ; ORGANIC COMPOUNDS ; REACTION KINETICS ; THERMOCHEMICAL PROCESSES ; TRANSITION ELEMENTS 010408* -- Coal, Lignite, & Peat-- C1 Processes-- (1987-) ; 010405 -- Coal, Lignite, & Peat-- Hydrogenation & Liquefaction
URL	http://www.osti.gov/scitech/servlets/purl/6094135
资源类型	科技报告
条目标识符	http://119.78.100.177/qdio/handle/2XILL650/264255
推荐引用方式 GB/T 7714	Fox, J.M.,Degen, B.D.,Cady, G.,et al. Slurry reactor design studies,1990.