Hydrocarbon conversion catalyst system and method

Claim 2

A process for reforming a hydrocarbon stream comprising contacting the hydrocarbon stream in a reforming zone under reforming conditions and in the presence of hydrogen and a hydrocarbon conversion catalyst system comprising a physical particle-form mixture of first and second catalysts, the first catalyst comprising at least one noble metal component and a combined halogen deposed on a high surface area, porous refractory inorganic oxide and being free of a crystalline aluminosilicate component, and the second catalyst being free of a noble metal component and comprising at least one metal component deposed on a solid support comprising a crystalline aluminosilicate material having an alkali metal content of less than about 1 percent of its weight, and being dispersed in a high surface area, porous refractory inorganic oxide; each noble metal component in the first catalyst comprising a noble metal, a compound thereof or a mixture thereof; each metal component in the second catalyst consisting essentially of a member selected from the group consisting of chromium, gallium, germanium, indium, lead, manganese, rhenium, technetium, thallium, tin, tungsten, a compound thereof and a mixture thereof; the weight percent of each noble metal component in the first catalyst, calculated as the noble metal element therein and based on the weight of the first catalyst, being in the range of from about 0.1 to about 1; the weight percent of each combined halogen in the first catalyst, calculated as the halogen element therein and based on the weight of the first catalyst, being in the range of from about 0.1 to about 1; the weight percent of each metal component in the second catalyst, calculated as the metal element therein and based on the weight of the second catalyst, being in the range of from about 0.1 to about 5; the weight percent of crystalline aluminosilicate material in the second catalyst, based on the weight of the second catalyst, being in the range of from about 1 to about 80; and the weight ratio of the first catalyst to the second catalyst being in the range of from about 1:1 to about 10:1.

Claim 3

A process for reforming a hydrocarbon stream comprising contacting the hydrocarbon stream in a first reforming zone under reforming conditions and in the presence of hydrogen with a catalyst comprising at least one noble metal-containing component deposed on a high surface area, porous refractory inorganic oxide to produce a reformate and subsequently contacting the reformate in a second reforming zone under reforming conditions and in the presence of hyrogen and a hydrocarbon conversion catalyst system comprising a physical particle-form mixture of first and second catalysts, the first catalyst comprising at least one noble metal component and a combined halogen deposed on a high surface area, porous refractory inorganic oxide and being free of a crystalline aluminosilicate component, and the second catalyst being free of a noble metal component and comprising at least one metal component deposed on a solid support comprising a crystalline aluminosilicate material having an alkali metal content of less than about 1 percent of its weight, and being dispersed in a high surface area, porous refractory inorganic oxide; each noble metal component in the first catalyst comprising a noble metal, a compound thereof or a mixture thereof; each metal component in the second catalyst consisting essentially of a member selected from the group consisting of chromium, gallium, germanium, indium, lead, manganese, rhenium, technetium, thallium, tin, tungsten, a compound thereof and a mixture thereof; the weight percent of each noble metal component in the first catalyst, calculated as the noble metal element therein and based on the weight of the first catalyst, being in the range of from about 0.1 to about 1; the weight percent of each combined halogen in the first catalyst, calculated as the halogen element therein and based on the weight of the first catalyst, being in the range of from about 0.1 to about 1; the weight percent of each metal component in the second catalyst, calculated as the metal element therein and based on the weight of the second catalyst, being in the range of from about 0.1 to about 5; the weight percent of crystalline aluminosilicate material in the second catalyst, based on the weight of the second catalyst, being in the range of from about 1 to about 80; and the weight ratio of the first catalyst to the second catalyst being in the range of from about 1:1 to about 10:1.

Claim 4

A process for reforming a hydrocarbon stream comprising contacting the hydrocarbon stream in a first reforming zone under reforming conditions and in the presence of hydrogen with a catalyst comprising at least one noble metal-containing component deposed on a high surface area, porous refractory inorganic oxide to produce a reformate and subsequently contacting the reformate in a second reforming zone under reforming conditions and in the presence of hyrogen and a hydrocarbon conversion catalyst system comprising a physical particle-form mixture of first and second catalysts, the first catalyst comprising at least one noble metal component and a combined halogen deposed on a high surface area, porous refractory inorganic oxide and being free of a crystalline aluminosilicate component, and the second catalyst being free of a noble metal component and comprising at least one metal component deposed on a solid support comprising a crystalline aluminosilicate material having an alkali metal content of less than about 1 percent of its weight, and being dispersed in a high surface area, porous refractory inorganic oxide; each noble metal component in the first catalyst comprising a noble metal, a compound thereof or a mixture thereof; each metal component in the second catalyst consisting essentially of a member selected from the group consisting of chromium, gallium, germanium, indium, lead, manganese, rhenium, technetium, thallium, tin, tungsten, a compound thereof and a mixture thereof; the weight percent of each noble metal component in the first catalyst, calculated as the noble metal element therein and based on the weight of the first catalyst, being in the range of from about 0.1 to about 1; the weight percent of each combined halogen in the first catalyst, calculated as the halogen element therein and based on the weight of the first catalyst, being in the range of from about 0.1 to about 1; the weight percent of each metal component in the second catalyst, calculated as the metal element therein and based on the weight of the second catalyst, being in the range of from about 0.1 to about 5; the weight percent of crystalline aluminosilicate material in the second catalyst, based on the weight of the second catalyst, being in the range of from about 1 to about 80; and the weight ratio of the first catalyst to the second catalyst being in the range of from about 1:1 to about 10:1.

Claim 5

The process of claim 1 or 2 wherein the reforming conditions comprise an average catalyst temperature of from about 750° F. (399° C.) to about 1,050° F. (566° C.), a pressure of from about 65 psia (4.42 atmospheres) to about 1,000 psia (68 atmospheres), a WHSV of from about 0.5 to about 10 weight units of hydrocarbon per hour per weight unit of catalyst, and a hydrogen addition rate of from about 1,500 SCFB (252.8 liters of hydrogen per liter of feed) to about 15,000 SCFB (2528 liters of hydrogen per liter of feed).

Claim 6

The process of claim 1 wherein the hydrocarbon stream is virgin naphtha, a cracked naphtha, a partially-reformed naphtha, a hydrocarbon boiling in the gasoline boiling range, or a mixture thereof.

Claim 7

The process of claim 1 wherein the hydrocarbon stream is derived from petroleum.

Claim 8

The process of claim 2 wherein the first reforming zone comprises at least two reactors and the second reforming zone comprises at least one reactor.

Claim 9

A process for reforming a hydrocarbon stream comprising contacting the hydrocarbon stream in a first reforming zone under reforming conditions and in the presence of hydrogen with a catalyst comprising at least one noble metal-containing component deposed on a high surface area, porous refractory inorganic oxide to produce a reformate and subsequently contacting the reformate in a second reforming zone under reforming conditions and in the presence of hydrogen and a hydrocarbon conversion catalyst system comprising a physical particle-form mixture of first and second catalysts, the first catalyst comprising a component and a chloride-containing component deposed on a high surface area and being free of a crystalline aluminosilicate component, and the second catalyst being free of a noble metal component and comprising at least one metal component deposed on a solid support comprising cation-exchanged mordenite having an alkali metal content of less than about 1 percent of its weight, and being dispersed in a high surface area alumina; the platinum-containing component in the first catalyst comprising platinum, a compound thereof or a mixture thereof; each metal component in the second catalyst consisting essentially of a member selected from the group consisting of gallium, rhenium, tungsten, a compound thereof and a mixture thereof; the weight percent of the platinum-containing component in the first catalyst, calculated as platinum and based on the weight of the first catalyst, being in the range of from about 0.1 to about 1; the weight percent of chloride in the first catalyst, calculated as the chloride therein and based on the weight of the first catalyst, being in the range of from about 0.1 to about 1; the weight percent of each metal component in the second catalyst, calculated as the metal element therein and based on the weight of the second catalyst, being in the range of from about 0.1 to about 5; the weight percent of cation-exchanged mordenite in the second catalyst, based on the weight of the second catalyst, being in the range of from about 1 to about 80; and the weight ratio of the first catalyst to the second catalyst being in the range of from about 1:1 to about 10:1; wherein the catalyst system comprises a physical mixture of (1) first particles comprising the first catalyst and free of the second catalyst and (2) second particles comprising the second catalyst and free of the first catalyst; and wherein the sizes of the first and second particles are the same or different and are each in the range of from about 0.031 inch (0.079 cm.) to about 0.188 inch (0.48 cm.) in their largest dimension.

Claim 10

A process for reforming a hydrocarbon stream comprising contacting the hydrocarbon stream in a first reforming zone under reforming conditions and in the presence of hydrogen with a catalyst comprising at least one noble metal-containing component deposed on a high surface area, porous refractory inorganic oxide to produce a reformate and subsequently contacting the reformate in a second reforming zone under reforming conditions and in the presence of hydrogen and a hydrocarbon conversion catalyst system comprising a physical particle-form mixture of first and second catalysts, the first catalyst comprising a component and a chloride-containing component deposed on a high surface area and being free of a crystalline aluminosilicate component, and the second catalyst being free of a noble metal component and comprising at least one metal component deposed on a solid support comprising cation-exchanged mordenite having an alkali metal content of less than about 1 percent of its weight, and being dispersed in a high surface area alumina; the platinum-containing component in the first catalyst comprising platinum, a compound thereof or a mixture thereof; each metal component in the second catalyst consisting essentially of a member selected from the group consisting of gallium, rhenium, tungsten, a compound thereof and a mixture thereof; the weight percent of the platinum-containing component in the first catalyst, calculated as platinum and based on the weight of the first catalyst, being in the range of from about 0.1 to about 1; the weight percent of chloride in the first catalyst, calculated as the chloride therein and based on the weight of the first catalyst, being in the range of from about 0.1 to about 1; the weight percent of each metal component in the second catalyst, calculated as the metal element therein and based on the weight of the second catalyst, being in the range of from about 0.1 to about 5; the weight percent of cation-exchanged mordenite in the second catalyst, based on the weight of the second catalyst, being in the range of from about 1 to about 80; and the weight ratio of the first catalyst to the second catalyst being in the range of from about 1:1 to about 10:1; wherein the catalyst system comprises a physical mixture of (1) first particles comprising the first catalyst and free of the second catalyst and (2) second particles comprising the second catalyst and free of the first catalyst; and wherein the sizes of the first and second particles are the same or different and are each in the range of from about 0.031 inch (0.079 cm.) to about 0.188 inch (0.48 cm.) in their largest dimension.