Claims Analysis
Total Claims: 34
Claim 1
Independent Claim
104 words
Composition of matter suitable as a catalyst (base) in hydroprocessing comprising a crystalline aluminosilicate zeolite and a binder wherein the crystalline aluminosilicate comprises a modified Y zeolite having a unit cell size below 24.35 Å, a degree of crystallinity which is at least retained at increasing SiO₂/Al₂O₃ molar ratios, a water adsorption capacity (at 25 °C and a p/p o value of 0.2) of at least 8% by weight of modified zeolite and a pore volume of at least 0.25 ml/g wherein between 10% and 60% of the total pore volume is made up of pores having a diameter of at least 8 nm.
Claim 2
Dependent Claim
104 words
Composition of matter suitable as a catalyst (base) in hydroprocessing comprising a crystalline aluminosilicate zeolite and a binder wherein the crystalline aluminosilicate comprises a modified Y zeolite having a unit cell size below 24.35 Å, a degree of crystallinity which is at least retained at increasing SiO₂/Al₂O₃ molar ratios, a water adsorption capacity (at 25 °C and a p/p o value of 0.2) of at least 8% by weight of modified zeolite and a pore volume of at least 0.25 ml/g wherein between 10% and 60% of the total pore volume is made up of pores having a diameter of at least 8 nm.
Claim 3
Dependent Claim
32 words
Composition according to claim 1, wherein between 10% and 40% of the total pore volume of the modified zeolite is made up of pores having a diameter of at least 8 nm.
Claim 4
Dependent Claim
26 words
Composition according to claim 1 or 2, wherein the modified zeolite Y has a water adsorption capacity of at least 10% by weight of modified zeolite.
Claim 5
Dependent Claim
23 words
Composition according to claim 3, wherein the modified zeolite has a water adsorption capacity between 10% and 15% by weight of modified zeolite.
Claim 6
Dependent Claim
25 words
Composition according to any one of claims 1-4, wherein the composition comprises 5-90% by weight of modified Y zeolite and 10-95% by weight of binder.
Claim 7
Dependent Claim
22 words
Composition according to claim 5, wherein the composition comprises 50-85% by weight of modified zeolite Y and 15-50% by weight of binder.
Claim 8
Dependent Claim
20 words
Composition according to any one of claims 1-6, wherein the binder comprises an inorganic oxide or mixture of inorganic oxides.
Claim 9
Dependent Claim
15 words
Composition according to claim 7, wherein the binder comprises silica, alumina, silica-alumina, silica-zirconia or silica-boria.
Claim 10
Dependent Claim
23 words
Composition according to any one of claims 1-8, wherein the modified Y zeolite has a SiO₂/Al₂O₃ molar ratio of from 4 to 25.
Claim 11
Dependent Claim
20 words
Composition according to claim 9, wherein the modified Y zeolite has a SiO₂/Al₂O₃ molar ratio of from 8 to 15.
Claim 12
Dependent Claim
38 words
Catalyst composition comprising a binder, a modified Y zeolite according to any one of claims 1-10 and at least one hydrogenation component of a Group VI metal and/or at least one hydrogenation component of a Group VIII metal.
Claim 13
Dependent Claim
37 words
Catalyst composition according to claim 11, wherein the hydrogenation component comprises one or more components of nickel and/or cobalt and one or more components of molybdenum and/or tungsten or one or more components of platinum and/or palladium.
Claim 14
Dependent Claim
38 words
Catalyst composition according to claim 12, wherein the hydrogenation component comprises between 0.5 and 10% by weight of nickel and between 2 and 40% by weight of tungsten, calculated as metals per 100 parts by weight of binder.
Claim 15
Dependent Claim
19 words
Catalyst composition according to any one of claims 11-13, wherein the hydrogenation component(s) is (are) present in sulphided form.
Claim 16
Dependent Claim
141 words
A process for converting hydrocarbon oils into products of lower average molecular weight and lower average boiling point comprising contacting a hydrocarbon oil at elevated temperature and pressure in the presence of hydrogen with catalyst comprising a modified Y zeolite having a unit cell size below 24.35 Å, a degree of crystallinity which is at least retained at increasing SiO₂/Al₂O₃ molar ratios, a water adsorption capacity (at 25 °C and a p/p o value of 0.2) of at least 8% by weight of modified zeolite and a pore volume of at least 0.25 ml/g wherein between 10% and 60% of the total pore volume is made up of pores having a diameter of at least 8 nm, a binder and at least one hydrogenation component of a Group VI metal and/or at least one hydrogenation component of a Group VIII metal.
Claim 17
Dependent Claim
141 words
A process for converting hydrocarbon oils into products of lower average molecular weight and lower average boiling point comprising contacting a hydrocarbon oil at elevated temperature and pressure in the presence of hydrogen with catalyst comprising a modified Y zeolite having a unit cell size below 24.35 Å, a degree of crystallinity which is at least retained at increasing SiO₂/Al₂O₃ molar ratios, a water adsorption capacity (at 25 °C and a p/p o value of 0.2) of at least 8% by weight of modified zeolite and a pore volume of at least 0.25 ml/g wherein between 10% and 60% of the total pore volume is made up of pores having a diameter of at least 8 nm, a binder and at least one hydrogenation component of a Group VI metal and/or at least one hydrogenation component of a Group VIII metal.
Claim 18
Dependent Claim
41 words
A process according to claim 15, wherein use is made of a catalyst comprising a modified Y zeolite wherein between 10% and 40% of the total pore volume is made up of pores having a diameter of at least 8 nm.
Claim 19
Dependent Claim
31 words
A process according to claim 15 or 16, wherein use is made of a modified Y zeolite having a water adsorption capacity of at least 10% by weight of modified zeolite.
Claim 20
Dependent Claim
28 words
A process according to claim 17, wherein use is made of a modified zeolite having a water adsorption capacity between 10% and 15% by weight of modified zeolite.
Claim 21
Dependent Claim
27 words
A process according to any one of claims 15-18, wherein the catalyst used comprises 5-90% by weight of modified Y zeolite and 10-95% by weight of binder.
Claim 22
Dependent Claim
27 words
A process according to claim 19, wherein use is made of a catalyst comprising 50-85% by weight of modified Y zeolite and 15-50% by weight of binder.
Claim 23
Dependent Claim
26 words
A process according to any one of claims 15-20, wherein use is made of a binder comprising an inorganic oxidic or a mixture of inorganic oxides.
Claim 24
Dependent Claim
20 words
A process according to claim 21, wherein use is made of silica, alumina, silica-alumina, clay, silica-zirconia or silica-boria as binder.
Claim 25
Dependent Claim
28 words
A process according to any one of claims 15-22, wherein use is made of a modified Y zeolite having a SiO₂/Al₂O₃ molar ratio of from 4 to 25.
Claim 26
Dependent Claim
25 words
A process according to claim 23, wherein use is made of a modified Y zeolite having a SiO₂/Al₂O₃ molar ratio of from 8 to 15.
Claim 27
Dependent Claim
43 words
A process according to any one of claims 15-24, wherein use is made of a catalyst comprising one or more components of nickel and/or cobalt and one or more components of molybdenum and/or tungsten or one or more components of platinum and/or palladium.
Claim 28
Dependent Claim
43 words
A process according to claim 25, wherein use is made of a hydrogenation component comprising between 0.05 and 10% by weight of nickel and between 2 and 40% by weight of tungsten, calculated as metals per 100 parts by weight of total catalyst.
Claim 29
Dependent Claim
22 words
A process according to any one of claims 15-26, wherein use is made of hydrogenation component(s) of Group VI in sulphided form.
Claim 30
Dependent Claim
48 words
A process according to any one of claims 15-27 which is carried out at a temperature in the range of from 250 °C to 500 °C, a pressure up to 300 bar and a space velocity between 0.1 and 10 kg feed per litre of catalyst per hour.
Claim 31
Dependent Claim
41 words
A process according to claim 28 which is carried out at a temperature between 300 °C and 450 °C, a pressure between 25 and 200 bar and a space velocity between 0.2 and 5 kg feed per litre catalyst per hour.
Claim 32
Dependent Claim
17 words
Composition according to any one of claims 1-10, substantially as hereinbefore described with reference to the Examples.
Claim 33
Dependent Claim
18 words
Catalyst composition according to any one of claims 11-14, substantially as hereinbefore described with reference to the Examples.
Claim 34
Dependent Claim
34 words
A process for converting hydrocarbon oils into products of lower average molecular weight and lower average boiling point according to any one of claims 15-29, substantially as hereinbefore described with reference to the Examples.