A thermodynamic approach to the stabilization of tubular reactors

2021 ◽  
Vol 108 ◽  
pp. 98-111
Author(s):  
Weijun Zhou ◽  
Boussad Hamroun ◽  
Yann Le Gorrec ◽  
Françoise Couenne
1996 ◽  
Vol 97 (1) ◽  
pp. 175-179 ◽  
Author(s):  
Avigad Vonshak ◽  
Giuseppe Torzillo ◽  
Paola Accolla ◽  
Luisa Tomaselli

1997 ◽  
Vol 94 ◽  
pp. 849-860 ◽  
Author(s):  
PY Chevalier ◽  
E Fischer ◽  
B Cheynet ◽  
A Rivet ◽  
G Cenerino

Author(s):  
Ivan Francisco Yupanqui Tello ◽  
Daniel Coutinho ◽  
Joseph Winkin ◽  
Alain Vande Wouver

2015 ◽  
Vol 14 (5) ◽  
pp. 1231-1240
Author(s):  
Mauri Sergio Alves Palma ◽  
Attilio Converti ◽  
Milena Nakagawa ◽  
Gisele Pigatto ◽  
Alessandra Lodi ◽  
...  

1982 ◽  
Vol 47 (7) ◽  
pp. 1838-1847 ◽  
Author(s):  
Martin Bajus ◽  
Jozef Baxa

Pyrolysis of tetraline, decaline, 1,1'-bicyclohexane, cyclohexylbenzene and gas oil was studied in stainless steel and quartz flow tubular reactors at 780 and 800 °C, residence time 0.08 to 0.5 s and at the mass ratio of steam to the raw material changing from 0.5 to 1.5. The effect of reaction temperature, the mass ratio of steam to the raw material, reactor material and of the added elemental sulphur on the yields of individual reaction products is reported. Of bicyclic hydrocarbons, condensed hydrocarbons are more stable than those with noncondensed rings, cyclanoaromates being more stable than bicyclanes. Pyrolysis of gas oil in the stainless steel reactor yields greater amounts of ethylene, propylene, butadiene and smaller amounts of methane and ethane, compared to the pyrolysis carried out under identical conditions in the quartz reactor. Elemental sulphur increases the conversion of gas oil into gaseous pyrolysis products.


Author(s):  
Jazael G. Moguel-Castañeda ◽  
Juan L. Hernandez-Ayala ◽  
Rafael Gomez-Rodriguez ◽  
Juan-Rodrigo Bastidas-Oyanedel ◽  
Eliseo Hernandez-Martinez

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