Process for manufacturing lube base stocks

Claim 2

In a process for manufacturing low pour point lubricant base stocks from vacuum distillation fractions of a reduced paraffin base crude or of a reduced mixed base crude, said fractions comprising a distillate fraction and a deasphalted vacuum residuum, which process comprises dewaxing said fractions thereby reducing the pour point thereof, the improvement, whereby more efficiently producing said base stocks, which comprises dewaxing said deasphalted vacuum residuum to a predetermined pour point by contact under dewaxing conditions with a dewaxing catalyst, said catalyst and conditions being effective to produce a yield of dewaxed residuum not less than is produced by solvent dewaxing said residuum to the same pour point, and solvent dewaxing said distillate fraction.

Claim 3

The process described in claim 1 wherein said catalytic dewaxing is conducted by contacting said deasphalted vacuum residuum fraction and hydrogen with a dewaxing catalyst comprising a crystalline zeolite having a silica to alumina ratio of at least about 12 and a constraint index of 1.0 to to 12.0.

Claim 4

The process described in claim 2 wherein said dewaxing catalyst comprises ZSM-5.

Claim 5

The process described in claim 2 or in claim 3 wherein said improvement comprises catalytically dewaxing only said deasphalted vacuum residuum.

Claim 6

The process described in claim 2 or in claim 3 wherein said improvement comprises catalytically dewaxing said deasphalted vacuum residuum and one or more of the higher boiling distillate fractions.

Claim 7

A process for manufacturing a slate of lubricant base stocks from an atmospheric residuum of a paraffin base crude or of a mixed base crude, which comprises: vacuum distilling said crude and recovering a plurality of fractions of increasing boiling range, said fractions including at least one distillate fraction and a deasphalted vacuum residuum; solvent extracting separately each of said fractions and recovering the corresponding waxy raffinates, including a neutral raffinate and a bright stock raffinate; solvent dewaxing at least the lowest boiling waxy raffinate and recovering a dewaxed neutral stock; and catalytically dewaxing at least the waxy bright stock raffinate by contacting said raffinate and hydrogen, at a hydrogen partial pressure of 150 psia to 1500 psia, at a temperature of 400° to 850° F. and at a L.H.S.V. of about 0.1 to about 5.0, with a dewaxing catalyst comprising a crystalline zeolite having a constraint index of about 1 to about 12 and a silica to alumina ratio of at least about 12.

Claim 8

A process for manufacturing a slate of lubricant base stocks from an atmospheric residuum of a paraffin base crude or of a mixed base crude, which comprises: vacuum distilling said crude and recovering a plurality of fractions of increasing boiling range, said fractions including at least one distillate fraction and a deasphalted vacuum residuum; solvent extracting separately each of said fractions and recovering the corresponding waxy raffinates, including a neutral raffinate and a bright stock raffinate; solvent dewaxing at least the lowest boiling waxy raffinate and recovering a dewaxed neutral stock; and catalytically dewaxing at least the waxy bright stock raffinate by contacting said raffinate and hydrogen, at a hydrogen partial pressure of 150 psia to 1500 psia, at a temperature of 400° to 850° F. and at a L.H.S.V. of about 0.1 to about 5.0, with a dewaxing catalyst comprising a crystalline zeolite having a constraint index of about 1 to about 12 and a silica to alumina ratio of at least about 12.

Claim 9

The process described in claim 6 wherein said crystalline zeolite is selected from the group consisting of ZSM-5, ZSM-11, ZSM-12, ZSM-23, ZSM-35 and ZSM-38.

Claim 10

The process described in claim 7 wherein said crystalline zeolite is associated with a hydrogen component.

Claim 11

The process described in claim 6 wherein only said bright stock raffinate is catalytically dewaxed.

Claim 12

The process described in claim 7 wherein only said bright stock raffinate is catalytically dewaxed.

Claim 13

The process described in claim 8 wherein only said bright stock raffinate is catalytically dewaxed.

Claim 14

The process described in claim 7 or claim 8 or claim 9 wherein said crystalline zeolite is ZSM-5.