Shnaider, A. G. Models of Catalytic Cracking of Oil Fractions in Single-stage and Multistage Reactors with Fluidized Beds and Interpretation of Experimental Data of Catalytic Cracking
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چکیده
Lewis, W. K.; Gilliland, E. R. Glass Werner, Solid-catalyzed reaction in a fluidized bed. AIChE J . 1959,5 (4), 419. McFatter, W. E.; Resen, F. L. Technical data of cat cracker Model 11. Oil Gas J . 1954, 53 (21), 86. McWhriter, W. E.; Tusson, J. R.; Parker, H. A. Detrehan Model 1V Fluid Cat Cracker. Pet. Refin. 1956,35 (4), 201. May, W. G. Fluidized-bed reactor studies. Chem. Eng. Prog. 1959, 55, (12), 49. Mathis, J. F.; Watson, C. C. Effect of fluidization on catalytic cumene dealkylation. AIChE J . 1956, 2 (4), 518. Mireur, J . P.; Bischoff, K. B. Mixing and contacting models for fluidized beds. AIChE J . 1967, 13 (5), 839. Reidel, J . C. Cities Serivce puts first Orthoflow cat cracker in United States on stream a t Ponca City (Okla.). Oil Gas J . 1952 50 (461, 200. Resen, F. L. Model 1V cat cracker brings lower investment, plus more efficient operation to Pan-Am Southern a t Detrehan. Oil Gas J . 1954a, 52 (46), 214. Resen, F. L. Suntide’s new plant features vacuum unit, fluid cat cracker, HF alkylation and propylene tetramer unit, and unusual handling of segregated crudes. Oil Gas J . 1954b, 52 (461, 203. Resen, F. L. Operating report-nothing stands still at Suntide. Plant improvement started as first units went on stream. Oil Gas J . 1956, 54 (42), 115. Rowe, P. N. The effect of bubbles on gas-solids contacting in fluidized beds. Chem. Eng. Prog., Symp. Ser. 1962,58 (381, 42. Shen, C. Y.; Johnstone, H. F. Gas-solids contact in fluidized beds. AIChE J . 1955, 1 (31, 349. Shnaider, G. S. Evaluation of the rate of reaction in single-stage and multistage reactors with fluidized beds. Khim. Promst. (Moscow), 1966, 6 , 35. Shnaider, G. S. Some equations which describe catalytic cracking of oil fractions in fluidized beds of multistaged reactor. Neftepererab. Neftekhim. (Moscow) 1972a, 12, 9. Shnaider, G. S. Grapho-analytical method of determination cetane numbers of light catalytic gas oils. Khim. Tekhnol. Topl. Masel 1972b, 6, 40. Shnaider, G. S. Influence of catalyst-to-charge on the results of catalytic cracking of heavy distillates in multistaged reactor. Khim. Tekhnol. Topl. Masel 1973, 1, 12. Shnaider, G . S. Evaluation of the Hydrodynamic Conditions in Multistaged Fluidized Countercurrent Flow Reactors in Pilot and Semicommercial Catalytic Cracking Units. Chem. Eng. J . 1988, 38 (2), 97. Shnaider, G. S.; Shnaider, A. G. Models of Catalytic Cracking of Oil Fractions in Single-stage and Multistage Reactors with Fluidized Beds and Interpretation of Experimental Data of Catalytic Cracking Performed in these Reactors. Chem. Eng. J . 1990, in press. Sittig, M. Catalytic Cracking Techniques in Review. Pet. Refin. 1952, 31 (9), 263. Spencer, H. A. A mixture of residue fraction and gas oil as feed for cat cracker Model 111. Pet. Process. 1954, 9 (71, 1083. Toei, R.; Matsuno, R.; Kojima, H.; Nagai, Y.; Nakagawa, K.; Yu, S. Behavior of bubbles in the gas-solid fluidized bed. Chem. Eng. Jpn. 1965,29, 851. Wheeler, H. K. New design features in catalytic cracker. Pet. Eng. 1951, 23 (ll), C-5.
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