Mineral oils: processes and products – Chemical conversion of hydrocarbons – Cracking
Patent
1996-12-20
1999-02-09
Griffin, Walter D.
Mineral oils: processes and products
Chemical conversion of hydrocarbons
Cracking
208120, 208150, 208DIG1, 585905, 585906, 502 55, C10G 1118
Patent
active
058689222
ABSTRACT:
A FCC process in which spent catalyst is stripped of hydrocarbon in a stripping zone prior to entering the regenerator. In order to maximize the amount of strippable hydrocarbon removed in the stripping zone with minimal use of stripping gas, a sample of spent catalyst is removed prior to entering the regenerator. The spent catalyst is analyzed for strippable hydrocarbon by conducting the sample to a heated catalyst collection vessel, evacuating the catalyst, collecting the gases from the collection vessel and analyzing the gases for amount of strippable hydrocarbon on the spent catalyst.
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P. Rivault, D. Nevicato, I. Pitault, M. Forissier, S. Collet, J.R. Bernard; "Coking and Chemical Stripping of FCC Catalyst in a MAT Reactor"; Symposium on Advances in FCC Conversion Cataysts, 211th National Meeting, American Chemial Society, New Orleans, LA; Mar. 24-29, 1996.
P.B. Venuto; "Fluid Catalytic Cracking with Zeolite Catalysts"; 1979 Marcel Dekker, Inc., New York; pp. 13-15. No Month.
A. Mohammed, B.J. McGhee, J.M. Andresen, C.E. Snape, R. Hughes; "Effect of Stripper Conditions on the Yield and Structure of Coke Deried from n-Hexadecane"; Symposium on Advances in FCC Conversion Catalysts, 211th National Meeting, Americal Chemical Society, New Orleans, LA; Mar., 24-29, 1996.
Gary D. Christian, "Analytical Chemistry", pp. 362 and 369, 1986, No Month.
Glass, Jr. James P.
Swan George A.
Exxon Research and Engineering Company
Griffin Walter D.
Preisch Nadine
Takemoto James H.
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