Reactor Design 3

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Muhammad Zafar Iqbal

Education

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Some important & Practical Consideration in Designing a Batch Reactor ,[object Object],[object Object],[object Object],[object Object]

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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.

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ABSTRACT : The evaluation of oil is fundamental to understand the physical chemical behavior of the fractions and the valorization of the oils. Among the methods used for it, the yield information in certain temperature ranges is obtained from the true boiling point (TBP), performed on bench scale according to ASTM D 2892. In this article, the experimental data from the TBP of Light oils are compared to the curve estimated from empirical correlations and to commercial simulator. The correlation used has the temperature range and density related constants as input variables, and presented a greater deviation compared to the experimental TBP curve. The data of the experimental TBP curve, and oil properties such as viscosity at different temperatures and density were inputs for the HYSYS simulation, with the result showed a smaller deviation from the experimental one. The comparison of the experimental and alternative methodologies show the importance of the development of faster and less deviation techniques to determine the TPB curve and for the evaluation of the oils.

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