Hydrocracking process including upgrading of bottoms fraction of the product

Claim 2

In a hydrocracking process wherein a hydrocrackable hydrocarbon feedstock is contacted with a hydrocracking catalyst under hydrocracking conditions and bottoms are separated from the resulting hydrocrackate product mixture, said bottoms containing at least one undesirable component selected from the group consisting of residual polycyclic hydrocarbons and nitrogen-containing hydrocarbon impurities, the improvement comprising: removing at least a portion of said undesirable components from said bottoms by contacting said bottoms under liquid-liquid extracting conditions with a solution of ferric chloride, said solution containing (a) at least a major portion of furfural and (b) an amount of said chloride, based by weight upon said solution, in the range of from about 0.001 to 10%, said extracting conditions including (i) a temperature in the range of from about 0° C. to 50° C., (ii) a solvent-to-feedstock volume ratio in the range of from about 0.1 to 10, and (iii) a resulting bottoms raffinate oil having, relative to said bottoms, a reduced content of said undesirable component.

Claim 3

A process as in claim 1 wherein (1) said feedstock contains an amount of said nitrogen-containing impurities, calculated by weight as nitrogen, in the range of from about 1 to 200 ppmw, (2) said solvent-to-feedstock volume ratio is in the range of 0.1 to 5, and (3) said amount of ferric chloride is in the range of 0.01 to 5.

Claim 4

A proces as in claim 2 wherein said solvent contains at least 80 volume percent of furfural.

Claim 5

A process as in claim 1 wherein said solvent consists essentially of furfural.

Claim 6

A process as in claim 2 wherein (1) said content of nitrogen-containing impurities is in the range 1 to 100 ppmw, and (2) said solvent-to-feedstock volume ratio is in the range 0.1 to 3.

Claim 7

A process as in claim 2 wherein (1) said solvent-to-feedstock volume ratio is in the range 0.4-1.5, and (2) said extracting temperature is in the range 10-30° C.

Claim 8

A process as in claim 1 wherein said process is carried out in a continuous countercurrent extracting.

Claim 9

In a hydrocracking process wherein a mixture of a hydrocrackable hydrocarbon feedstock and recycled bottoms is admixed and contacted with a hydrocracking catalyst under hydrocracking conditions, said bottoms having been separated from a hydrocrackate product mixture and containing at least one undesirable component selected from the group consisting of residual polycyclic hydrocarbons and nitrogen-containing hydrocarbon impurities, the improvement comprising: (1) removing at least a portion of said undesirable component from said bottoms by contacting said bottoms under liquid-liquid extracting conditions with a solution of ferric chloride, said solution containing (a) at least a major portion of furfural solvent and (b) an amount of said chloride, based by weight upon said solution, in the range of from about 0.001 to 10%, said extracting conditions including (i) a temperature in the range of from about 0° C. to 50° C., (ii) a solvent-to-mixture volume ratio in the range of from about 0.1 to 10, and (iii) a resulting bottoms raffinate oil having, relative to said bottoms, a reduced content of said undesirable component; and (2) recycling said resulting bottoms raffinate oil to form said mixture in the hydrocracking step.

Claim 10

In a hydrocracking process wherein a mixture of a hydrocrackable hydrocarbon feedstock and recycled bottoms is admixed and contacted with a hydrocracking catalyst under hydrocracking conditions, said bottoms having been separated from a hydrocrackate product mixture and containing at least one undesirable component selected from the group consisting of residual polycyclic hydrocarbons and nitrogen-containing hydrocarbon impurities, the improvement comprising: (1) removing at least a portion of said undesirable component from said bottoms by contacting said bottoms under liquid-liquid extracting conditions with a solution of ferric chloride, said solution containing (a) at least a major portion of furfural solvent and (b) an amount of said chloride, based by weight upon said solution, in the range of from about 0.001 to 10%, said extracting conditions including (i) a temperature in the range of from about 0° C. to 50° C., (ii) a solvent-to-mixture volume ratio in the range of from about 0.1 to 10, and (iii) a resulting bottoms raffinate oil having, relative to said bottoms, a reduced content of said undesirable component; and (2) recycling said resulting bottoms raffinate oil to form said mixture in the hydrocracking step.

Claim 11

A process as in claim 8 wherein (1) said feedstock contains an amount of said nitrogen-containing impurities, calculated by weight as nitrogen, in the range of from about 1 to 200 ppmw, (2) said solvent-to-feedstock volume ratio is in the range of 0.1 to 5, and (3) said amount of ferric chloride is in the range of 0.01 to 5.

Claim 12

A process as in claim 8 wherein said solvent contains at least 80 volume percent of furfural.

Claim 13

A process as in claim 8 wherein said solvent consists essentially of furfural.

Claim 14

A process as in claim 8 wherein (1) said content of nitrogen-containing impurities is in the range 1 to 100 ppmw, and (2) said solvent-to-feedstock volume ratio is in the range 0.1 to 3.

Claim 15

A process as in claim 8 wherein (1) said solvent-to-feedstock volume ratio is in the range 0.4-1.5, and (2) said extracting temperature is in the range 10°-30° C.

Claim 16

A process as in claim 8 wherein said process is carried out in said continuous countercurrent extracting.