Enhanced heat transfer reformer and method

Claim 1

A method for reforming hydrocarbons in a plural stage reformation wherein a first reformation of a first reactant stream occurs in a first reforming zone heated by combustion furnace gases and a second reformation of a second reactant stream occurs in a second reforming zone which second reformation comprises the steps of: (a) introducing said second reactant stream of hydrocarbons and steam at elevated temperature and pressure into said second reforming zone; (b) passing said second reactant stream through a plurality of reaction tubes while contacting said second reactant stream with reforming catalyst packed in said tubes; (c) introducing a reformed reaction product at elevated temperature and pressure into said second reforming zone but outside said tubes at a temperature substantially above the temperature of said second reactant stream at the latter's introduction into said second reforming zone; (d) mixing the reformed reaction product with similar product produced from said second reactant stream passing through said reaction tubes; (e) heating said second reactant stream to reaction temperature and reforming it in said reaction tubes by heat exchange of said mixed reaction product with said second reactant stream, and (f) removing a mixed reaction product of reformed fluid from said second reforming zone.

Claim 2

A method for reforming hydrocarbons in a plural stage reformation wherein a first reformation of a first reactant stream occurs in a first reforming zone heated by combustion furnace gases and a second reformation of a second reactant stream occurs in a second reforming zone which second reformation comprises the steps of: (a) introducing said second reactant stream of hydrocarbons and steam at elevated temperature and pressure into said second reforming zone; (b) passing said second reactant stream through a plurality of reaction tubes while contacting said second reactant stream with reforming catalyst packed in said tubes; (c) introducing a reformed reaction product at elevated temperature and pressure into said second reforming zone but outside said tubes at a temperature substantially above the temperature of said second reactant stream at the latter's introduction into said second reforming zone; (d) mixing the reformed reaction product with similar product produced from said second reactant stream passing through said reaction tubes; (e) heating said second reactant stream to reaction temperature and reforming it in said reaction tubes by heat exchange of said mixed reaction product with said second reactant stream, and (f) removing a mixed reaction product of reformed fluid from said second reforming zone.

Claim 4

A method for reforming hydrocarbons comprising the steps of: (a) heating and desulfurizing a hydrocarbon feed stream; (b) blending the hydrocarbon feed stream with steam to produce a saturated hydrocarbon feed stream; (c) splitting the saturated hydrocarbon feed stream into a main feed stream and a bypass feed stream; (d) reforming said main feed stream in a first catalytic reformation zone using the heat of a combustion furnace; (e) reforming the bypass feed stream in a second catalytic reformation zone using the heat of the reaction product of the first reformation zone; (f) combining the reformation reaction products and introducing them into a shift reactor to shift any carbon monoxide to carbon dioxide and hydrogen, and (g) cooling the reaction product and separating the hydrogen content of the reaction product from the remaining reaction components.

Claim 5

A method for reforming hydrocarbons comprising the steps of: (a) heating and desulfurizing a hydrocarbon feed stream; (b) blending the hydrocarbon feed stream with steam to produce a saturated hydrocarbon feed stream; (c) splitting the saturated hydrocarbon feed stream into a main feed stream and a bypass feed stream; (d) reforming said main feed stream in a first catalytic reformation zone using the heat of a combustion furnace; (e) reforming the bypass feed stream in a second catalytic reformation zone using the heat of the reaction product of the first reformation zone; (f) combining the reformation reaction products and introducing them into a shift reactor to shift any carbon monoxide to carbon dioxide and hydrogen, and (g) cooling the reaction product and separating the hydrogen content of the reaction product from the remaining reaction components.