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U.S. Department of Energy
Office of Scientific and Technical Information

Diagrams and tables on various patterns of heat exchange in coal hydrogenation (in German)

Technical Report ·
OSTI ID:5750954
The various alternatives illustrated included heat exchange of gases only, heat exchange for coal paste as well, and heat exchange of part of the paste in one stream and the rest in another stream. There were several different types of diagrams, including schematic flow sheets with temperatures indicated at various spots in the apparatus, heat-balance and heat-flow diagrams, temperature-change diagrams, etc. There were graphs of heat-transfer efficiency and pressure drops within the apparatus. There were tables giving throughputs, flow rates, temperature changes, heat transfer coefficients, etc. for preheaters and heat exchangers. The diagrams were scaled for a process in which 50.2 (metric) tons/hr of coal paste and residues and 48,000 m/sup 3//hr of hydrogen gas were reacted to give 24.5 t/hr of liquid product, 20.6 t/hr sludge residue out of the process (with another 5.8 t/hr of residues recycled into the process) and 83,000 m/sup 3//hr of circulating gases. In each case, there were 26,000,000 cal accounted for in a heat balance into and out of the reaction ovens. In each case, the heat of reaction was 9,100,000 cal. The remainder of the heat into the ovens came from heating the reactants up to 100/sup 0/, from heat exchange involving part or all of the reactants, and from preheating part of all of them. The heat out of the oven was lost in the product coolers, carried away in the sludge residue, lost to radiation, or used in heat exchange. 4 figures, 4 tables.
OSTI ID:
5750954
Report Number(s):
TOM-77-00884-00895
Country of Publication:
United States
Language:
German