The energyβefficient and safe conversion of ethane into ethylene is possible by simultaneous exothermic oxidative dehydrogenation and endothermic cracking of ethane in the presence of steam and limited amounts of O~2~, by using the thermally and hydrothermally stable supported catalyst SrO/La~2~O~3~
Coupling of thermal cracking with noncatalytic oxidative conversion of Ethane to Ethylene
β Scribed by Vasant R. Choudhary; Shafeek A. R. Mulla
- Publisher
- American Institute of Chemical Engineers
- Year
- 1997
- Tongue
- English
- Weight
- 522 KB
- Volume
- 43
- Category
- Article
- ISSN
- 0001-1541
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β¦ Synopsis
Homogeneous thermal cracking of ethane, which is an endothermic and hence energy-intensive process, was carried out in the presence of limited 0, under different process conditions (at 60O"-85O0C; O,/ethane ratio of 0 -0.2; H,O/ethane ratio of 0-3.3; and space velocity of 2,000-11,000 h-'). The influence of a sulfitr additive in the feed and reactor material on the process pegormance was also investigated. Noncatalytic oxycracking of ethane in the presence of limited O,, greatly enhances not only the total conversion of ethane but also the conversion of ethane by purely thermal cracking. This process also occurs at a much lower contact time than that required to achieve the same conversion for the thermal cracking process. Also, both the exothermic oxidative conversion and the endothermic thermal cracking of ethane occur simultaneousl), which makes this process very energy-efficient, with a drastic reduction in external energy requirement and coke formation. By manipulating the process conditions, particularly the temperature and O,/C, H6 ratio, the overall process can be made almost thermoneutral, mildly exothermic, or mildly endothermic.
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