Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
248 words
A process of producing high quality gasoline and higher boiling products which comprises hydrotreating a wide boiling range aliphatic hydrocarbon fraction comprising oxygenates boiling in the range of about 350° to 850° F; separating the hydrotreated product to produce a 650° F plus fraction and a 650° F minus fraction, separating said 650° F minus fraction to produce a gasoline boiling fraction and higher boiling light oil fraction, separating said high boiling light oil fraction to produce a kerosine boiling fraction and a higher boiling distillate fraction having a low pour point. separately converting said kerosine boiling fraction and said 650° F plus fraction with a catalyst comprising a special zeolite component having a silica to alumina ratio of at least 12 and a constraint index of 1 to 12, at a temperature in the range of about 500° to 800° F, and at a space velocity of about 0.5 to 5 WHSV, to produce a conversion product of said zeolite catalyst, separating product obtained by converting said 650° F plus distillate fraction with said special zeolite catalyst to produce a C 4 minus gaseous product, a naphtha boiling range product, and a higher boiling distillate product suitable for producing jet fuel boiling range material and diesel fuel; and separating product obtained by converting said kerosine boiling fraction with said special zeolite catalyst to produce a C 4 minus gaseous product, a naphtha boiling range product and a kerosine boiling range product suitable for use as jet fuel.
Claim 2
Dependent Claim
248 words
A process of producing high quality gasoline and higher boiling products which comprises hydrotreating a wide boiling range aliphatic hydrocarbon fraction comprising oxygenates boiling in the range of about 350° to 850° F; separating the hydrotreated product to produce a 650° F plus fraction and a 650° F minus fraction, separating said 650° F minus fraction to produce a gasoline boiling fraction and higher boiling light oil fraction, separating said high boiling light oil fraction to produce a kerosine boiling fraction and a higher boiling distillate fraction having a low pour point. separately converting said kerosine boiling fraction and said 650° F plus fraction with a catalyst comprising a special zeolite component having a silica to alumina ratio of at least 12 and a constraint index of 1 to 12, at a temperature in the range of about 500° to 800° F, and at a space velocity of about 0.5 to 5 WHSV, to produce a conversion product of said zeolite catalyst, separating product obtained by converting said 650° F plus distillate fraction with said special zeolite catalyst to produce a C 4 minus gaseous product, a naphtha boiling range product, and a higher boiling distillate product suitable for producing jet fuel boiling range material and diesel fuel; and separating product obtained by converting said kerosine boiling fraction with said special zeolite catalyst to produce a C 4 minus gaseous product, a naphtha boiling range product and a kerosine boiling range product suitable for use as jet fuel.
Claim 3
Dependent Claim
11 words
The process claimed in claim 1 wherein said zeolite is ZSM-5.
Claim 4
Dependent Claim
31 words
The process of claim 1 wherein said gasoline boiling fraction separated from said 650° F minus fraction has an end boiling point within the range of 350° to about 400° F.
Claim 5
Dependent Claim
23 words
The process of claim 1 wherein said kerosine boiling fraction separated from said 650° F minus fraction boils up to about 550° F.
Claim 6
Dependent Claim
31 words
The process of claim 1 wherein a naphtha boiling product is recovered from said zeolite catalyst conversion operation having an end boiling point within the range of 350° to 400° F.
Claim 7
Dependent Claim
31 words
The process of claim 1 wherein a kerosine product of desired low freeze point boiling within the range of 350° to 450° F is recovered from said zeolite catalyst conversion operation.
Claim 8
Dependent Claim
21 words
The process of claim 1 wherein a diesel fuel is recovered from said zeolite catalyst conversion operation boiling above 400° F.
Claim 9
Dependent Claim
25 words
The process of claim 1 wherein said zeolite conversion catalyst is in admixture with from 0.5 to 5 weight percent of a metal hydrogenation/dehydrogenation component.
Claim 10
Dependent Claim
24 words
The process of claim 8 wherein a hydrogen pressure within the range of 100 to 800 psig is employed in said zeolite conversion operation.