Quenched catalytic cracking process

Claim 2

In a fluidized catalytic cracking process wherein a fluidizable catalyst cracking catalyst and a hydrocarbon feed are charged to a reactor riser at catalytic riser cracking conditions to form catalytically cracked vapor product and spent catalyst which are discharged into a reactor vessel having a volume via a riser reactor outlet equipped with a separation means to produce a catalyst lean phase comprising a majority of said cracked product, and a catalyst rich phase comprising a majority of said spent catalyst, said catalyst rich phase is discharged into a dense bed of catalyst maintained below said riser outlet and said catalyst lean phase is discharged into said vessel for a time, and at a temperature, which cause unselective thermal cracking of the cracked product in the reactor volume before product is withdrawn from said vessel via a vessel outlet, the improvement comprising addition, after riser cracking is completed, and after separation of cracked products from catalyst, of a quenching stream into said vessel above said dense bed of catalyst, via a quench stream addition point which allows the quench stream to contact at least a majority of the volume of the vessel above said dense bed.

Claim 3

Process of claim 1 wherein said quenching stream is selected from the group consisting of water, steam and hydrocarbons.

Claim 4

Process of claim 1 wherein said quenching stream is steam.

Claim 5

Process of claim 3 wherein the amount of steam quench added to said vessel, expressed as weight percent of said hydrocarbon feed, is 0.1 to 10 wt %.

Claim 6

Process of claim 4 wherein 0.5 to 5 wt % steam is added as quench.

Claim 7

Process of claim 3 wherein said separation means comprises at least one cyclone separator connected to the reactor riser outlet.

Claim 8

Process of claim 3 wherein said separation means comprises a downwardly discharging reactor riser outlet, positioned about 3 to 20 meters above said dense bed of catalyst.

Claim 9

Process of claim 7 wherein the amount and temperature of steam quench addition to said reactor are sufficient to reduce the thermal cracking in said reactor volume, as measured by equivalent reaction time at 800° F., by at least 4%.

Claim 10

Process of claim 1 wherein said separation means comprises a primary cyclone attached to said riser outlet, and wherein a secondary cyclone is provided at an elevation above said dense bed and connective with said vessel outlet, and said quench is added to said vessel at an elevation intermediate said dense bed and said secondary cyclone.

Claim 11

Process of claim 8 wherein thermal cracking is reduced by at least 50%.

Claim 12

A fluidized catalytic cracking process wherein a stream of hot regenerated catalyst contacts a hydrocarbon feed comprising gas oils, vacuum gas oils, topped crudes, tar sands, shale oil, or asphaltic fractions in a conventional reactor riser, and is cracked in said riser to form cracked hydrocarbon vapor products of reduced molecular weight and spent catalyst; said vapor products and spent catalyst are discharged into a vessel having a volume through a cyclone separator which produces a catalyst-rich phase which is discharged into a dense bed of spent catalyst maintained in a lower portion of said reactor vessel and a vapor phase which is separately discharged into said vessel above said dense bed, steam quench is added, after riser cracking is completed, and after separation of cracked products from catalyst, to said cracked product vapor phase via a quench steam addition point which allows quenching of at least a majority of the volume in the vessel and quenched vapor products are removed from said vessel as a product of the process.

Claim 13

A fluidized catalytic cracking process wherein a stream of hot regenerated catalyst contacts a hydrocarbon feed comprising gas oils, vacuum gas oils, topped crudes, tar sands, shale oil, or asphaltic fractions in a conventional reactor riser, and is cracked in said riser to form cracked hydrocarbon vapor products of reduced molecular weight and spent catalyst; said vapor products and spent catalyst are discharged into a vessel having a volume through a cyclone separator which produces a catalyst-rich phase which is discharged into a dense bed of spent catalyst maintained in a lower portion of said reactor vessel and a vapor phase which is separately discharged into said vessel above said dense bed, steam quench is added, after riser cracking is completed, and after separation of cracked products from catalyst, to said cracked product vapor phase via a quench steam addition point which allows quenching of at least a majority of the volume in the vessel and quenched vapor products are removed from said vessel as a product of the process.

Claim 14

Process of claim 11 wherein the amount of steam quench added to said vessel, expressed as weight percent of said hydrocarbon feed, is 0.1 to 10 wt %.

Claim 15

Process of claim 11 wherein 0.5 to 5 wt % steam is added as quench.

Claim 16

Process of claim 11 wherein quench steam is added in an amount equal to at least 1 wt % of the hydrocarbon feed.

Claim 17

Process of claim 11 wherein the amount and temperature of steam quench addition to said reactor are sufficient to reduce the thermal cracking, as measured by equivalent reaction time at 800° F., by at least 4%.

Claim 18

Process of claim 11 wherein thermal cracking is reduced by at least 50%.

Claim 19

A fluidized catalytic cracking process comprising a conventional reactor riser wherein hot regenerated catalyst contacts a hydrocarbon feed comprising gas oils, vacuum gas oils, topped crudes, tar sands, shale oil, or asphaltic fractions and is cracked in said riser to form catalytically cracked hydrocarbon products of reduced molecular weight and spent catalyst; said cracked products and spent catalyst are discharged into a vessel through a primary cyclone separator which produces a catalyst phase containing a minor amount of said cracked product which is discharged into a dense bed of catalyst maintained in a lower portion of said vessel and a cracked product vapor phase discharged via a primary cyclone vapor outlet and wherein a quench stream is added, after riser cracking is completed, and after separation of cracked products from catalyst, to said vessel 0.15 to 5 meters above said dense bed and wherein there is a volume in said vessel above said dense bed and the quench stream contacts at least a majority of the volume of the vessel above said dense bed and at least about 90% of said vapor phase passes from said primary cyclone vapor outlet into an inlet of a secondary cyclone within one second and said minor amount of cracked product passes from said dense bed through said vessel to said secondary cyclone inlet in a period of time in excess of one second and additional separation, of entrained spent catalyst from cracked product and said quench stream, occurs in said secondary cyclone to produce a cracked product and quenched stream vapor.

Claim 20

A fluidized catalytic cracking process comprising a conventional reactor riser wherein hot regenerated catalyst contacts a hydrocarbon feed comprising gas oils, vacuum gas oils, topped crudes, tar sands, shale oil, or asphaltic fractions and is cracked in said riser to form catalytically cracked hydrocarbon products of reduced molecular weight and spent catalyst; said cracked products and spent catalyst are discharged into a vessel through a primary cyclone separator which produces a catalyst phase containing a minor amount of said cracked product which is discharged into a dense bed of catalyst maintained in a lower portion of said vessel and a cracked product vapor phase discharged via a primary cyclone vapor outlet and wherein a quench stream is added, after riser cracking is completed, and after separation of cracked products from catalyst, to said vessel 0.15 to 5 meters above said dense bed and wherein there is a volume in said vessel above said dense bed and the quench stream contacts at least a majority of the volume of the vessel above said dense bed and at least about 90% of said vapor phase passes from said primary cyclone vapor outlet into an inlet of a secondary cyclone within one second and said minor amount of cracked product passes from said dense bed through said vessel to said secondary cyclone inlet in a period of time in excess of one second and additional separation, of entrained spent catalyst from cracked product and said quench stream, occurs in said secondary cyclone to produce a cracked product and quenched stream vapor.

Claim 21

Process of claim 17 wherein steam quench is added to said vessel in an amount, expressed as weight percent of said hydrocarbon feed, of 0.1 to 10 wt %.

Claim 22

Process of claim 17 wherein the amount and temperature of quench stream added are sufficient to reduce the thermal cracking in the reactor vessel, as measured by equivalent reaction time at 800° F., by at least 50%.

Claim 23

Process of claim 17 wherein said secondary cyclone inlet is substantially radially aligned with, and is over said primary cyclone vapor outlet, and wherein all of the quench stream and cracked product enter said secondary cyclone inlet with the vapor from said primary cyclone, and wherein said quenched hydrocarbon represents less than about 10% of the total amount of hydrocarbon entering said secondary cyclone.