US 12,281,064 B2
Methods for dehydrogenation of perhydro-benzyltoluene
Christopher Declan Lane, San Ramon, CA (US); Steven Xuqi Song, San Ramon, CA (US); Bi-Zeng Zhan, San Ramon, CA (US); Trenton J. Otto, San Ramon, CA (US); Michael J. Girgis, San Ramon, CA (US); and Yaofan Yi, San Ramon, CA (US)
Assigned to CHEVRON U.S.A. INC., San Ramon, CA (US)
Filed by CHEVRON U.S.A. INC., San Ramon, CA (US)
Filed on Aug. 23, 2023, as Appl. No. 18/237,157.
Prior Publication US 2025/0066271 A1, Feb. 27, 2025
Int. Cl. C07C 5/367 (2006.01); C07C 7/04 (2006.01)
CPC C07C 5/367 (2013.01) [C07C 7/04 (2013.01)] 11 Claims
OG exemplary drawing
 
1. A method for dehydrogenation comprising:
pre-heating perhydro benzyl-toluene (12H-BT);
co-feeding the pre-heated perhydro benzyl-toluene (12H-BT) with a gas comprising hydrogen into a fixed-bed reactor in a first-stage reactor wherein under conditions sufficient to produce at least a partially converted product mixture comprising 12H-BT, 6H-BT, 0H-BT, and hydrogen, wherein the amount of co-fed hydrogen is sufficient to reduce coke formation;
introducing at least a portion of the partially converted product mixture from the first-stage reactor into a second stage reactor comprising a gas-phase reactor and a distillation column at a temperature below the boiling point of 12H-BT and under gas-phase reactor conditions sufficient to produce a gas-liquid mixture comprising (1) a gas comprising hydrogen and (2) a liquid mixture comprising 12H-BT, 6H-BT, and 0H-BT;
removing a product comprising hydrogen product from second stage reactor and cooling the hydrogen product for compression; and
distilling the liquid in the distillation column to substantially separate 12H-BT, 6H-BT, and 0H-BT.