Severe corrosion has been experienced in a Thermofor catalytic cracking gas plant over several years. Representative inspection findings are outlined. A complete chemical survey of gas plant streams for amount and type of corrosives, together with water present, is given. Ammonia and hydrogen sulfide are indicated the principal corrosives present. These have caused corrosion of overhead condensing equipment. Some ammonia acid salts are present which have dissociated at reboiler temperatures to give acid conditions which have caused rapid attack of reboiler tubes. Measures are suggested to remove water, which will also remove the principal corrosive constituents at appropriate points in the system. Possible places for chemical injection are suggested to neutralize any traces of remaining corrosives.
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1 March 1951
Research Article|
March 01 1951
Thermofor Catalytic Cracking Gas Plant Corrosion Survey⋆ Available to Purchase
Christopher A. Murray
Christopher A. Murray
CHRISTOPHER A. MURRAY — Presently with Pure Oil Company, Smith's Bluff Refinery, Nederland, Texas, he holds a BS degree in chemistry from the University of Wisconsin. He has been engaged in refinery corrosion work for five years and formerly was chemist for two years in the butadiene laboratory of the Neches Butane Products Co., Port Neches, Texas and for three years with the Research and Development Laboratories of The Pure Oil Company at Chicago, III.
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Online ISSN: 1938-159X
Print ISSN: 0010-9312
Copyright 1951 by the National Association of Corrosion Engineers
1951
CORROSION (1951) 7 (3): 98–108.
Citation
Christopher A. Murray; Thermofor Catalytic Cracking Gas Plant Corrosion Survey⋆. CORROSION 1 March 1951; 7 (3): 98–108. https://doi.org/10.5006/0010-9312-7.3.98
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