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This present work aimed to investigate the influence of CO2 on HCl removal using calcined Ca–Mg–Al layered double hydroxides (CaMgAl-LDHs) at medium–high temperature (400–800 C) in a fixed

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A process and a system for increasing para-xylene production from a C 8 aromatic feedstream by coupling at least one xylene isomerization reactor with at least one pressure swing adsorption unit or temperature swing absorption unit to produce a product having a

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Petroleum coke (pet coke) is a byproduct of the oil refining coking process. • Tons means metric tons. One metric ton equals 1.102 short tons. 2 Table of Contents SUMMARY This summary highlights

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