novel expertmental set up for determmmg the kinetics of coke deposltlon m thermal cracking IS described and Its apphcation to the crackmg of propane IS dlustrated The reactor Itself IS of the completely muted type and provides kmetic mnformation on propane crackmg whch IS m agreement with that obtam
Coke deposition in the thermal cracking of ethane
β Scribed by K. M. Sundaram; P. S. Van Damme; G. F. Froment
- Publisher
- American Institute of Chemical Engineers
- Year
- 1981
- Tongue
- English
- Weight
- 522 KB
- Volume
- 27
- Category
- Article
- ISSN
- 0001-1541
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β¦ Synopsis
Abstract
A novel experimental setup allowed both the kinetics of the thermal cracking of ethane and of the coke formation to be studied over a temperature range extending from 750 to 870Β°C. The overall kinetics of ethane disappearance are in excellent agreement with previously reported pilot results. Coking rates are initially high but rapidly decrease to reach an asymptotic value. The initial product distribution also differs from the asymptotic product distribution. A kinetic model for the coking is derived from the experiments and used in conjunction with a set of conservation equations for the simulation of industrial ethane cracking. The predicted run length, thickness of the coke layer and evolution of the tubeskin temperatures are in agreement with industrial observations.
π SIMILAR VOLUMES
The coking and cracking behaviour of a heavy oil fraction derived from Stuart shale oil was investigated in a moving packed-bed reactor. Experiments were performed to evaluate the conversion of heavy oil into lower-boiling products, coke and gases when contacted with fully burnt shale ash and sand.