EXPERIMENTS ON THE PYROLYSIS OF GASEOUS PARAFFINS, WITH SPECIAL REFERENCE TO THE PRODUCTION OF ETHYLENE

1932 ◽  
Vol 7 (6) ◽  
pp. 646-661 ◽  
Author(s):  
Adrien Cambron

On passing natural gas, containing 4.8% ethane, through an electrically heated tungsten spiral, the formation of liquid products was observed at 1050 °C.On passing the same gas over an electrically heated 4-mm. carbon rod enclosed in an uninsulated silica tube 2.0 cm. wide, 7.7% of the gas was converted to liquid and solid hydrocarbons at a rod temperature of 1050–1100 °C. No liquids or solids except carbon were formed when the silica tube was insulated.By replacing the 2.0-cm. silica tube by a water-cooled Pyrex tube, 3.2 cm. wide, no liquid or solid hydrocarbons were obtained, but 17% of the gas was converted to gaseous unsaturated hydrocarbons at 993 °C. On passing ethane through the 3.2-cm. water-cooled reaction tube at rod temperature of 989 °C., 50.5% of the entering gas was converted to ethylene, and 90.0% of the ethane decomposed did so according to the equation C2H6 → C2H4 + H2.The dehydrogenation of ethane was found to be greatly accelerated by the presence of reduced copper in the tube, the metal being used in the form of a cylindrical wire gauze and placed around the carbon rod. Copper bronze coated with molybdic oxide was also found to be active under the same conditions.

2007 ◽  
Vol 41 (5) ◽  
pp. 686-690
Author(s):  
L. N. Vosmerikova ◽  
L. L. Korobitsyna ◽  
A. V. Vosmerikov ◽  
G. V. Echevskii

2008 ◽  
Vol 42 (5) ◽  
pp. 622-626 ◽  
Author(s):  
L. N. Vosmerikova ◽  
A. V. Vosmerikov ◽  
G. V. Echevsky

1947 ◽  
Vol 25b (6) ◽  
pp. 494-501 ◽  
Author(s):  
E. H. Boomer ◽  
S. N. Naldrett

Mixtures of methane and oxygen with some nitrogen were passed over catalysts of copper, silver, zinc, nickel, and Monel metal and the yields of methanol and other liquid products determined. The conditions of temperature, pressure, and rate of flow that were known to be best for a copper catalyst were used. Nickel and Monel metal appear to offer most promise. A massive form of catalyst appears to be better than a catalyst in the form of fine wire gauze for the maximum yield of liquid products.


2016 ◽  
Vol 5 (4) ◽  
pp. 271 ◽  
Author(s):  
A.V. Vosmerikov ◽  
L.N. Vosmerikova ◽  
G.V. Echevsky ◽  
L.L. Korobitsyna ◽  
Ye.G. Kodenev ◽  
...  

<p>The main component of the natural gas is methane, whose molecules are characterized by a high chemical and thermal stability. It is impossible to perform the chemical transformation of natural gas into liquid organic compounds without applying highly active polyfunctional catalysts. Natural gas might be converted into liquid products in the presence of zeolite catalysts of pentasil family. Zeolite catalysts of ZSM-5 type were prepared to realize the process. They contained various amounts of Zn and Ga promoters introduced by ion exchange and impregnation. It has been shown that in the presence of small amounts of C<sub>2</sub>-C<sub>5</sub> alkanes in the feedstock the methane is converted into aromatic hydrocarbons much more readily and in softer conditions than pure methane. At optimum process conditions reached is a high conversion of the natural gas into a mixture of aromatic hydrocarbons. This mixture mainly consists of benzene and naphthalene and small amounts of their derivatives – toluene, C<sub>8</sub> and C<sub>9+</sub> alkylbenzenes, methyl- and dimethylnaphthalenes. An optimum composition of zeolite matrix and the amount of the modifier in the catalyst have been established.</p>


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