Thermal cracking of light gas oil at high severity to ethylene

Claim 2

A process for producing ethylene by thermally cracking a hydrocarbon feed at least 90 volume percent of which comprises a light gas oil fraction of a crude oil boiling between 400° and 650° F. comprising passing said hydrocarbon feed, a diluent gas, and entrained inert hot solids through a cracking zone at a temperature between 1,300° and 2,500° F. for a residence time of 0.05 to 2 seconds, the weight ratio of diluent gas to feed oil being at least 0.3, the cracking severity corresponding to a methane yield of at least 12 weight percent based on said feed oil, and quench cooling said product immediately upon leaving said cracking zone to a temperature below 1,300° F. so that the ethylene yield is greater than the methane yield on a weight basis.

Claim 3

The process of claim 1 wherein the diluent gas is steam.

Claim 4

The process of claim 1 wherein said methane yield is at least 14 weight percent.

Claim 5

The process of claim 1 wherein said weight ratio is at least 1.

Claim 6

The process of claim 1 wherein essentially all of said hydrocarbon feed comprises a light gas oil fraction of a crude oil boiling between 400° and 650° F.

Claim 7

The process of claim 1 wherein said light gas oil fraction of a crude oil has been hydrodesulfurized.

Claim 8

A process for thermally cracking first and second hydrocarbon feeds to produce first and second products including ethylene comprising passing said first hydrocarbon feed at least 90 volume percent of which comprises a petroleum light gas oil fraction of a crude oil boiling between 400° and 650° F., a diluent gas, and entrained inert hot solids through a first cracking zone at a temperature between 1,300° and 2,500° F. for a residence time of 0.05 to 2 seconds, the weight ratio of diluent gas to feed oil being at least 0.3, at a cracking severity corresponding to a methane yield of at least 12 weight percent based on said first feed oil, and quench cooling said first product immediately upon leaving said first cracking zone to a temperature below 1,300° F. so that the ethylene yield is greater than the methane yield on a weight basis; passing said second hydrocarbon feed comprising primarily a C 5 to 400° F. naphtha fraction, a diluent gas and a stream of entrained inert hot solids through a second cracking zone at a temperature between 1,300° and 2,500° F. for a residence time between 0.05 and 2 seconds and at a cracking severity corresponding to a methane yield below the methane yield in said first cracking zone, quench cooling said second cracked product immediately upon leaving said second cracking zone to a temperature below 1,300° F., and combining first and second cracked product.

Claim 9

A process for thermally cracking first and second hydrocarbon feeds to produce first and second products including ethylene comprising passing said first hydrocarbon feed at least 90 volume percent of which comprises a petroleum light gas oil fraction of a crude oil boiling between 400° and 650° F., a diluent gas, and entrained inert hot solids through a first cracking zone at a temperature between 1,300° and 2,500° F. for a residence time of 0.05 to 2 seconds, the weight ratio of diluent gas to feed oil being at least 0.3, at a cracking severity corresponding to a methane yield of at least 12 weight percent based on said first feed oil, and quench cooling said first product immediately upon leaving said first cracking zone to a temperature below 1,300° F. so that the ethylene yield is greater than the methane yield on a weight basis; passing said second hydrocarbon feed comprising primarily a C 5 to 400° F. naphtha fraction, a diluent gas and a stream of entrained inert hot solids through a second cracking zone at a temperature between 1,300° and 2,500° F. for a residence time between 0.05 and 2 seconds and at a cracking severity corresponding to a methane yield below the methane yield in said first cracking zone, quench cooling said second cracked product immediately upon leaving said second cracking zone to a temperature below 1,300° F., and combining first and second cracked product.

Claim 10

The process of claim 7 wherein said light gas oil fraction of a crude oil has been hydrodesulfurized.

Claim 11

The process of claim 7 wherein the methane yield in said second cracking zone is below 12 weight percent.

Claim 12

The process of claim 7 wherein said C 5 to 400° F. fraction comprises at least 75 volume percent of said second feed oil.

Claim 13

The process of claim 7 wherein said C 5 to 400° F. fraction comprises at least 90 volume percent of said second feed oil.

Claim 14

The process of claim 8 wherein essentially all of said first hydrocarbon feed comprises a petroleum light gas oil fraction of a crude oil boiling between 400° and 650° F.

Claim 15

The process of claim 7 wherein the diluent gas in said first and second cracking zones is steam.

Claim 16

The process of claim 7 wherein the percentage of ethylene based on feed in the product from the first cracking zone is greater than in the product from said second cracking zone.

Claim 17

The process of claim 7 wherein the products from said first and second cracking zones contain propylene, and the percentage of propylene based on feed in the product from said second cracking zone is greater than in the product from said first cracking zone.

Claim 18

The process of claim 7 wherein the products from said first and second cracking zones contain 1,3-butadiene and the percentage of 1,3-butadiene based on feed in the product from said second cracking zone is greater than in the product from said first cracking zone.

Claim 19

The process of claim 7 wherein the weight ratio of diluent gas to feed oil in said second cracking zone is lower than the ratio in said first cracking zone.

Claim 20

The process of claim 7 wherein the hot solids from said first and second cracking zones are passed to a common coke burner, the products from said first and second cracking zones include liquid oils, and passing the residue portion of the liquid oils from both said first and second cracking zones to said coke burner as fuel.

Claim 21

The process of claim 7 wherein said first and second feedstocks are obtained by distilling a wide boiling range oil.