US 5,626,741 AGranted

Catalytic cracking with quenching

AssigneeAmoco Corporation

InventorsJames F. Mosby, F. William Hauschildt, George P. Quinn, Douglas N. Rundell, John G. Schwartz, Mark S. Camp, John M. Forgac

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Abstract

A catalytic cracking process is disclosed in which cracking is performed in a riser reactor, catalytically cracked product is substantially separated from the catalyst in a gross-cut separator downstream of the riser reactor, and the cracked product is quenched with an anhydrous quench liquid at a location immediately downstream of the oil outlet of the gross-cut separator.

Claims23

Dependent claims

A catalytic cracking process, comprising the steps of:

catalytically cracking feed oil in a reactor of a catalytic cracking unit in the presence of a cracking catalyst to produce a catalytically cracked effluent product stream of upgraded oil containing particulates of spent coked cracking catalyst in a catalytic cracking reactor selected from the group consisting of a riser reactor and a fluidized bed reactor;
substantially separating said catalytically cracked effluent product stream in a gross-cut separator spaced downstream of said catalytic cracking reactor into a catalyst lean stream of vaporized upgraded oil and a catalyst-laden oil-lean stream of spent cracking catalyst, passing said catalyst lean stream of vaporized upgraded oil through an oil outlet of the gross-cut separator, discharging said catalyst-laden oil-lean stream of spent cracking catalyst substantially downwardly through a catalyst outlet of an elongated dipleg of said gross-cut separator substantially below said oil outlet of said gross-cut separator into a dense catalyst bed in a lower portion of a disengaging vessel, said dense catalyst bed being at an elevation substantially below said oil outlet of said gross-cut separator;
and
quenching said catalyst lean stream of upgraded oil by spraying said upgraded oil with an anhydrous quench, said anhydrous quench being sprayed adjacent to said oil outlet of said gross-cut separator in an open area located externally and downstream of said reactor, said anhydrous quench being introduced and sprayed at a location substantially spaced above said dipleg of said gross-cut separator, said spraying comprising injecting said quench generally downwardly towards said oil outlet of said gross-cut separator at an elevation substantially above said dense catalyst bed of said disengaging vessel, said quench comprising at least one member selected from the group consisting of light catalytic cycle oil, heavy catalytic cycle oil, kerosene, coker distillate, hydrotreated distillate, and virgin gas oil to decrease the temperature of said catalyst lean stream of upgraded oil by a temperature of from about 30.degree. F. to about 200.degree. F. and substantially minimize thermal cracking of said product stream to less valuable hydrocarbon products and light hydrocarbon gases.

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A catalytic cracking process, comprising the steps of:

catalytically cracking feed oil in the presence of a cracking catalyst in a catalytic cracking unit comprising a catalytic cracking reactor, a disengager, and a gross-cut separator downstream of the cracking reactor and either upstream of or within said disengager, said separator having an oil outlet and a separate catalyst outlet, and said disengager having an upper portion and a lower dense phase portion;
and
cooling said catalytically cracked feed oil after said catalytic cracking is substantially completed by decreasing the temperature of said catalytically cracked feed oil by a temperature of from about 30.degree. F. to about 200.degree. F. to substantially minimize thermal cracking of said catalytically cracked oil to fuel gas by contacting said catalytically cracked oil with a hydrocarbon liquid quench in a quench zone positioned externally and downstream of said catalytic cracking reactor and of the oil outlet of gross-cut separator, said quench zone being further positioned at a location selected from the group consisting of
(a) upstream of said disengager, when the gross-cut separator is upstream of said disengager, or
(b) inside said disengager, when the gross-cut separator is within said disengager, in an area above the oil outlet of the gross-cut separator in said upper portion of said disengager substantially above said lower dense phase portion;
said hydrocarbon liquid quench having a boiling point greater than water, a molecular weight over 90, and a volumetric expansion less than about 3% of the volume of said catalytically cracked oil;
and
said hydrocarbon liquid quench being injected into said catalytically cracked oil at a downward angle of inclination ranging from about 15 degrees to less than about 90 degrees relative to a vertical to increase production of gasoline.

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A catalytic cracking process, comprising the steps of:

catalytically cracking feed oil in a catalytic cracking unit comprising a regenerator and at least one catalytic cracking reactor selected from the group consisting of a riser reactor and a fluidized bed reactor, in the presence of a cracking catalyst to produce catalytically cracked upgraded oil and coked catalyst;
making a gross-cut separation of said coked catalyst from said upgraded oil downstream of said catalytic cracking reactor in a gross-cut separator having a vapor exit providing a product outlet and substantially immediately thereafter;
reducing the temperature of said upgraded oil by about 30.degree. F. to about 200.degree. F. by substantially quenching said upgraded oil at a location adjacent to said product outlet of said gross-cut separator with a quench selected from the group consisting of light catalytic cycle oil, heavy catalytic cycle oil, coker distillate, and mixtures thereof, by injecting said quench generally downwardly towards said product outlet of said gross-cut separator to substantially decrease thermal cracking of said upgraded oil to less valuable hydrocarbon products and light hydrocarbon gases;
regenerating said coked catalyst in a regenerator;
and
recycling said regenerated catalyst to said catalytic cracking reactor.

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Dependencies are inferred from the claim text.

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Abstract

A catalytic cracking process, comprising the steps of:

catalytically cracking feed oil in a reactor of a catalytic cracking unit in the presence of a cracking catalyst to produce a catalytically cracked effluent product stream of upgraded oil containing particulates of spent coked cracking catalyst in a catalytic cracking reactor selected from the group consisting of a riser reactor and a fluidized bed reactor;
substantially separating said catalytically cracked effluent product stream in a gross-cut separator spaced downstream of said catalytic cracking reactor into a catalyst lean stream of vaporized upgraded oil and a catalyst-laden oil-lean stream of spent cracking catalyst, passing said catalyst lean stream of vaporized upgraded oil through an oil outlet of the gross-cut separator, discharging said catalyst-laden oil-lean stream of spent cracking catalyst substantially downwardly through a catalyst outlet of an elongated dipleg of said gross-cut separator substantially below said oil outlet of said gross-cut separator into a dense catalyst bed in a lower portion of a disengaging vessel, said dense catalyst bed being at an elevation substantially below said oil outlet of said gross-cut separator;
and
quenching said catalyst lean stream of upgraded oil by spraying said upgraded oil with an anhydrous quench, said anhydrous quench being sprayed adjacent to said oil outlet of said gross-cut separator in an open area located externally and downstream of said reactor, said anhydrous quench being introduced and sprayed at a location substantially spaced above said dipleg of said gross-cut separator, said spraying comprising injecting said quench generally downwardly towards said oil outlet of said gross-cut separator at an elevation substantially above said dense catalyst bed of said disengaging vessel, said quench comprising at least one member selected from the group consisting of light catalytic cycle oil, heavy catalytic cycle oil, kerosene, coker distillate, hydrotreated distillate, and virgin gas oil to decrease the temperature of said catalyst lean stream of upgraded oil by a temperature of from about 30.degree. F. to about 200.degree. F. and substantially minimize thermal cracking of said product stream to less valuable hydrocarbon products and light hydrocarbon gases.

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