Packed Bed Reactor for Catalytic Cracking of Plasma Pyrolyzed Gas |
Author(s): |
Dr. Nema S.K , FCIPT division, Institute for plasma research, Gandhinagar; Murugan P.V, FCIPT division, Institute for plasma research, Gandhinagar; Rana P.H, Vishwakarma Government Engineering College, Chandkheda; Nayak M. G., Vishwakarma Government Engineering College, Chandkheda |
Keywords: |
Vacuum residue, X ray analysis SEM of catalyst, contact time, pressure drop, coking. |
Abstract |
Packed bed reactors play vital role in chemical industries for obtaining valuable product, like steam reforming of natural gas, ammonia synthesis, sulphuric acid production, methanol synthesis, methanol oxidation, butadiene production, styrene production. It is not only used for production but also used in separation process like adsorption, distillation and stripping section. Packed bed reactors are work horse of the chemical and petroleum industries. Its low cost, and simplicity makes it first choice to any chemical processes. In our experimental work vacuum residue is used as a feed which is pyrolyzed in the primary chamber with the help of plasma into hydrogen and hydrocarbon gases which is feed stream to the Ni catalyst containing packed bed reactor called catalytic cracker. Ni loading in the catalyst about 70 % is used to crack or decompose lower molecular hydrocarbon in to hydrogen to maximize the energy content per mass flow of gas steam and also to minimize the carbon dioxide equivalent gases at outlet of the reactor. Since cracking is surface phenomena so the catalyst play important role in designing of reactor shape. Parallel Catalytic packed bed with regeneration and deactivation can be used for commercial production of clean fuel. |
Other Details |
Paper ID: IJSRDV1I4010 Published in: Volume : 1, Issue : 4 Publication Date: 01/07/2013 Page(s): 845-849 |
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