Hydrocracking process with feed pretreatment

Claim 2

A hydrocracking process which comprises the steps: (a) passing a feedstock comprising an admixture of hydrocarbons having boiling points above 204 degrees C. through a first treating zone maintained at conditions of superatmospheric pressure and a temperature of from about 260 to about 375 degrees C., with the feedstock contacting a bed of porous metal oxide particles under said conditions which cause the formation of polycyclic aromatic compounds but result in essentially no cracking reactions and producing a first effluent stream substantially similar to the feedstock and having a higher concentration of polycyclic aromatic compounds than the feed stream; (b) contacting the first effluent stream with a bed of treating particles comprising charcoal in a second treating zone maintained at conditions which promote the retention of the polycyclic aromatic compounds on said treating particles and producing a second effluent stream substantially similar to the feedstock but having a lower concentration of the polycyclic aromatic compounds than said first effluent stream; (c) passing the second effluent stream into a hydrocracking reaction zone maintained at hydrocracking conditions which include a temperature of from about 375 to about 510 degrees C., a pressure above 3500 kPa g, a hydrogen to hydrocarbon mole ratio above 1.0:1.0 and the presence of a hydrocracking catalyst and producing a hydrocracking reaction zone effluent stream; and, (d) recovering a hydrocracking process product stream from said reaction zone effluent stream.

Claim 3

The process of claim 1 further limited in that hydrogen is admixed into said second effluent stream prior to passage of the second effluent stream into the hydrocracking reaction zone.

Claim 4

The process of claim 2 further limited in that the porous metal oxide particles present in the first treating zone are substantially free of any catalytically active metal component which promotes hydrocracking wherein said metal component does not form an integral part of the support component of said particles.

Claim 5

The process of claim 3 further limited in that the porous metal oxide particles present in the first treating zone comprise alumina.

Claim 6

The process of claim 3 further limited in that the porous metal oxide particles present in the first treating zone comprise a material used as a support material for the hydrocracking catalyst present in the hydrocracking reaction zone.

Claim 7

The process of claim 2 further limited in that the feedstock and the first effluent stream contain substantially no uncombined hydrogen.

Claim 8

The process of claim 1 further limited in that the first and the second treating zone are operated at substantially the same conditions of temperature and pressure, and in that the pressure in the first and second treating zones is less than 2800 kPa g.

Claim 9

The process of claim 7 further limited in that the first effluent stream contains substantially no uncombined hydrogen and in that the porous metal oxide particles present in the first treating zone consist essentially of alumina.

Claim 10

A hydrocracking process which comprises the steps: (a) passing a feedstock comprising an admixture of hydrocarbons having boiling points above 204 degrees C. and which is substantially free of uncombined hydrogen through a first treating zone maintained at conditions of superatmospheric pressure and a temperature of from about 260 to about 375 degrees C., with the feedstock contacting a bed of porous metal oxide particles comprising alumina under said conditions which cause the formation of polycyclic aromatic compounds but result in essentially no cracking reactions and producing a first effluent stream substantially similar to the feedstock and having a higher concentration of polycyclic aromatic compounds than the feed stream; (b) contacting the first effluent stream with a bed of treating particles comprising charcoal in a second treating zone maintained at conditions which promote the retention of the polycyclic aromatic compounds on said treating particles and producing a second effluent stream which is substantially free of uncombined hydrogen and is substantially similar to the feedstock but having a lower concentration of the polycyclic aromatic compounds than said first effluent stream; (c) passing the second effluent stream and hydrogen into a hydrocracking reaction zone maintained at hydrocracking conditions which include a temperature of from about 375 to about 510 degrees C., a pressure above 3500 kPa g, a hydrogen to hydrocarbon mole ratio above 1.0:1.0 and the presence of a hydrocracking catalyst and producing a hydrocracking reaction zone effluent stream; and, (d) recovering a hydrocracking process product stream from said reaction zone effluent stream.

Claim 11

A hydrocracking process which comprises the steps: (a) passing a feedstock comprising an admixture of hydrocarbons having boiling points above 204 degrees C. and which is substantially free of uncombined hydrogen through a first treating zone maintained at conditions of superatmospheric pressure and a temperature of from about 260 to about 375 degrees C., with the feedstock contacting a bed of porous metal oxide particles comprising alumina under said conditions which cause the formation of polycyclic aromatic compounds but result in essentially no cracking reactions and producing a first effluent stream substantially similar to the feedstock and having a higher concentration of polycyclic aromatic compounds than the feed stream; (b) contacting the first effluent stream with a bed of treating particles comprising charcoal in a second treating zone maintained at conditions which promote the retention of the polycyclic aromatic compounds on said treating particles and producing a second effluent stream which is substantially free of uncombined hydrogen and is substantially similar to the feedstock but having a lower concentration of the polycyclic aromatic compounds than said first effluent stream; (c) passing the second effluent stream and hydrogen into a hydrocracking reaction zone maintained at hydrocracking conditions which include a temperature of from about 375 to about 510 degrees C., a pressure above 3500 kPa g, a hydrogen to hydrocarbon mole ratio above 1.0:1.0 and the presence of a hydrocracking catalyst and producing a hydrocracking reaction zone effluent stream; and, (d) recovering a hydrocracking process product stream from said reaction zone effluent stream.

Claim 12

The process of claim 1 further limited in that the first and the second treating zone are operated at substantially the same conditions of temperature and pressure, and in that the pressure in the first and second treating zones is less than 2800 kPa g.

Claim 13

The process of claim 10 further limited in that the porous metal oxide particles present in the first treating zone are substantially free of any catalytically active metal component which promotes hydrocracking wherein said component does not form an integral part of the support component of said particles.

Claim 14

The process of claim 11 further limited in that the porous metal oxide particles present in the first treating zone comprise a material used as a support material for the hydrocracking catalyst present in the hydrocracking reaction zone.