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A catalyst regeneration process and apparatus for the oxidative removal of coke from a coke-contaminated fluid catalyst. The process comprises of high temperature coke combustion zone, a lower temperature heat removal zone and an upper disengagement zone. Coke-contaminated catalyst, oxygen-containin

A catalyst regeneration process and apparatus for the oxidative removal of coke from a coke-contaminated fluid catalyst. The process comprises of high temperature coke combustion zone, a lower temperature heat removal zone and an upper disengagement zone. Coke-contaminated catalyst, oxygen-containing gas and cooled regenerated catalyst from the heat removal zone are contacted in the high temperature combustion zone, the temperature of which is controlled by adjusting the rate at which catalyst is recycled to the heat removal zone. The heat removal zone contains a relatively dense-phase fluid catalyst bed in which is immersed heat removal means such as cooling coils. The level of this fluid catalyst bed, and thus the extent of immersion of the heat removal means in the bed, is maintained by controlling the quantity of regeneration gas passed into the transfer line that carries catalyst upward from the heat removal zone to the combustion zone.

대표청구항 ▼

A process for regenerating a coke-contaminated fluid catalyst, said process including the steps of: (a) introducing oxygen-containing regeneration gas, coke-contaminated fluid catalyst into a lower locus of a combustion zone maintained at a temperature sufficient for coke-oxidation and therein oxidi

A process for regenerating a coke-contaminated fluid catalyst, said process including the steps of: (a) introducing oxygen-containing regeneration gas, coke-contaminated fluid catalyst into a lower locus of a combustion zone maintained at a temperature sufficient for coke-oxidation and therein oxidizing coke to produce hot regenerated catalyst and hot flue gas; (b) transporting said hot flue gas and a portion of said hot regenerated catalyst into a regenerated catalyst disengaging zone, wherein said hot regenerated catalyst is separated from said flue gas; (c) passing a portion of hot regenerated catalyst from said disengaging zone to a heat removal zone and therein maintaining said catalyst at dense-phase fluid bed conditions, said combustion and heat removal zones being substantially vertically oriented with respect to each other with said heat removal zone below said combustion zone; (d) removing heat in said heat removal zone by providing heat removal means at least partially immersed in said dense-phase fluid catalyst bed of said heat removal zone; (e) passing relatively cool catalyst from said heat removal zone to said combustion zone through a substantially vertical transfer line having an inlet in a lower locus of said dense-phase fluid bed in said heat removal zone and an outlet in a lower locus of said combustion zone, said passing of relatively cool catalyst effected by passing at least a portion of said regeneration gas into said transfer line at a locus below the level of said dense-phase fluid bed; and (f) controllably maintaining the extent of immersion of said heat removal means in said dense-phase fluid catalyst bed by maintaining the level of said dense-phase fluid catalyst bed in said heat removal zone by controlling the quantity of said regeneration gas passed into said transfer line in response to said level. Process of claim 1 further characterized in that the temperature at an upper locus of said combustion zone is controllably maintained by controlling the quantity of said hot regenerated catalyst passed from said disengaging zone to said heat removal zone in response to said temperature at said upper locus. Process of claim 1 further characterized in that fluidization of said dense-phase fluid catalyst bed in said heat removal zone is effected by introducing at least a portion of said regeneration gas into a lower locus of said bed and venting said portion from said removal zone to a lower locus of said combustion zone.