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in the fcc process, the hydrocarbon feedstock is mixed with hot, coked catalyst and then is passed through a series of fixed or moving riser cracking tubes. the catalyst serves two purposes: first, to provide the reaction surfaces; and second, to provide the heat for vaporizing the feedstock and cracking the molecules. as the feedstock flows through the riser, the effluent is continuously removed from the bottom of the riser and passes through a series of valves that control the flow of the cracked product to the main fractionator. the hot catalyst is then separated from the cracked product, regenerated and recycled to the reaction zone. the catalyst is then cooled and sent back to the reaction zone.
the coke combustion zone is at the heart of a fluid catalytic cracking (fcc) unit where the catalyst is regenerated by burning off the carbon deposits from the catalyst. the combustion zone produces heat and gases to supply the heat for the endothermic cracking reactions. the heat is transferred from the hot flue gas to the catalyst by the catalyst. the flue gas is typically at about 700° c and at a pressure of about 2.41 barg. the combustible mixture of co and hydrogen burns at relatively low temperature to produce a flue gas that is primarily co2 and water. the heat released by the combustion of the coke deposits is used to vaporize the feedstock and to provide the required endothermic reactions in the catalyst that produce the cracked products.
the fcc reaction zone contains a series of risers to support the catalyst in the reaction zone. the riser contains hot catalyst from the regeneration zone and the flow of cracked products through the risers to the catalyst regenerator. the heated catalyst is also called regenerated catalyst. the cracked products are removed from the reaction zone by a series of cyclones. the catalyst is returned to the reaction zone to continue the cracking reactions. the coke combustion zone is at the heart of a fluid catalytic cracking (fcc) unit where the catalyst is regenerated by burning off the carbon deposits from the catalyst. the combustion zone produces heat and gases to supply the heat for the endothermic cracking reactions. the heat is transferred from the hot flue gas to the catalyst by the catalyst. the flue gas is typically at about 700° c and at a pressure of about 2.41 barg. the combustible mixture of co and hydrogen burns at relatively low temperature to produce a flue gas that is primarily co2 and water.
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