Abstract

Nowadays, polyvinyl chloride (PVC) is the most usual plastic. Therefore, to make PVC, its monomer called vinyl chloride (VCM) must be produced first. It is a severely endothermic reaction that is done in an ethylene dichloride thermal cracking reactor within a temperature range of 680 to 758°K and pressure range of 2500000 Pascal. Thus, this cracking reaction changes into hydrochloric acid and VCM. In production unit, monomeric chloride has the main and principal role as the core of the process of thermal cracking that occurs in the furnace. Increased wall temperature causes boil gas mixture and pyrolysis reactions. Regarding simulation, the results showed that the number of pyrolysis produced composition with maximum concentration in the length of the reactor. This illustrated that these compositions participated in secondary reactions. Furthermore, by increasing the amount of coil outlet temperatures, the amount of formed coke will increase. If carbon tetrachloride is considered as the chlorine radicals, it has an important role as the motivator in the cracking procedures, radicals causing an enhancement in VCM production. Key words: Carbon tetrachloride, conversion factor, coke, coil outlet temperatures, thermal cracking.

Highlights

  • Afshin DavarpanahTo make polyvinyl chloride (PVC), its monomer called vinyl chloride (VCM) must be produced first

  • Designing and simulation of thermal cracking reactor of the chemical reactions in the processes and heat transfer in the furnace are very complex

  • Computational Fluid Dynamics (CFD) tools help us to investigate the development of detailed models of these reactors, and by understanding the basic principles, the optimized design of reactor, saving of cost and time performance of this equipment in a virtual laboratory can be done

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Summary

Afshin Davarpanah

To make PVC, its monomer called vinyl chloride (VCM) must be produced first. It is a severely endothermic reaction that is done in an ethylene dichloride thermal cracking reactor within a temperature range of 680 to 758°K and pressure range of 2500000 Pascal. This cracking reaction changes into hydrochloric acid and VCM. The results showed that the number of pyrolysis produced composition with maximum concentration in the length of the reactor. This illustrated that these compositions participated in secondary reactions.

INTRODUCTION
Molecular cracking
Geometry of thermal cracking reactor
Wall of furnace
Output flow
INVESTIGATING ADDING CARBON TETRACHLORIDE AS PROPULSION
Conclusion
Full Text
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