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Coal conversion to liquid and gaseous hydrocarbons in a cross flow moving bed reactor. [Coal particles move horizontally while H/sub 2/ moves vertically]

Conference ·
OSTI ID:7297119
A study of coal hydrogenation has been performed in a cross flow moving bed reactor. Coal particles move horizontally in packed form in the reactor while hydrogen moves vertically. Temperature distributions of both gas and solid are obtained by solving the energy equations for packed bed. Weight fractions of carbon, and its gas and liquid products, can be obtained using a three-step coal hydrogenation model as a first approximation. The problem is solved numerically for some practical operating conditions of a reactor using a CDC 7600 computer. The effect of several operating parameters on the temperature distribution of the reactor is examined. Increasing the gas residence time will decrease the temperature of both solid and gas phases. Increasing the solid phase residence time will increase the temperature of both phases. Hydrogen partial pressure does not have any effect on the temperature field. An example of the application of the model to a specific set of conditions is presented. High coal conversion yield such as 60 percent or higher can be obtained in the assumed reactor for the following conditions: hydrogen partial pressure of 100 to 400 atm, solid velocity of 30 to 100 cm/sec, particle size of 50 to 60 ..mu..m, hydrogen velocity of 25 to 30 cm/sec. (auth)
Research Organization:
Brookhaven National Lab., Upton, N.Y. (USA)
OSTI ID:
7297119
Report Number(s):
BNL-20754; CONF-760402-2
Country of Publication:
United States
Language:
English