Exxon Catalytic Coal Gasification Process Development Program Quarterly Technical Progress Report January 1 March 31 1979

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Exxon Catalytic Coal Gasification Process Development Program. Quarterly Technical Progress Report, January 1-March 31, 1979

Exxon Catalytic Coal Gasification Process Development Program. Quarterly Technical Progress Report, January 1-March 31, 1979
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ISBN-10 : OCLC:1065926704
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Book Synopsis Exxon Catalytic Coal Gasification Process Development Program. Quarterly Technical Progress Report, January 1-March 31, 1979 by :

Download or read book Exxon Catalytic Coal Gasification Process Development Program. Quarterly Technical Progress Report, January 1-March 31, 1979 written by and published by . This book was released on 1979 with total page pages. Available in PDF, EPUB and Kindle. Book excerpt: This report covers the activites for the Exxon Catalytic Coal Gasification Development Program during the quarter January 1-March 31, 1979. Construction of a bench apparatus to study reactions of product and recycle gas in furnace and heat exchanger tubes was completed and checkout of the apparatus was begun. A Startup and Initial Operation Schedule, a Checkout Test Plan, and an Initial Startup Plan were developed for the Process Develoment Unit (PDU). The PDU will be started up in a sequential manner, with the gasification system being started up on a once-through basis first. The gas separation system will be started up next, followed by the catalyst recovery system. The programmable controller, which handles valve sequencing, alarming, and other miscellaneous functions on the PDU, was programmed and checkout was completed on the coal feed, gas feed, and filter systems. Work continued on defining the cause of the breakdown of char and lime during digestion in the prototype catalyst recovery unit. It was concluded that both the lime and char particles are fragile and will break down to fines if handled roughly. Removal of the potassium from the char by water washing does not cause the char particles to disintegrate. The perferred processing sequence for catalyst recovery in the PDU has been identified. Bench scale tests confirmed that the change in catalyst from K2CO3 to KOH was not responsible for the differences in fluidized bed densities between the present and the predevelopment operations of the FBG. Work was completed on a revised offsites facilities definition and cost estimate to update the CCG Commercial Plant Study Design prepared during the predevelopment program.


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