Conversion of a lower alkane

Claim 1

A method for converting at least one feedstock alkane containing from one to three carbon atoms to a higher molecular weight hydrocarbon comprising: reacting said feedstock alkane with air to form a gaseous product mixture comprising carbon monoxide, hydrogen, and nitrogen and passing said gaseous product mixture through an elongated reactor packed with a bed of particles comprising a Fischer-Tropsch catalyst, maintained at a pressure in the range of from about 1 to about 50 pounds per square inch gauge and cooled to maintain the temperature therein in the range of from about 160° C. to about 240° C., to thereby form a gaseous product stream comprising aliphatic hydrocarbon products having higher molecular weights than the feedstock alkane, the Fischer-Tropsch catalyst in the bed of particles of said reactor having increasing average activity for the conversion of synthesis gas from the inlet to the outlet of said reactor, the activity gradient being effected by dilution of Fischer-Tropsch catalyst particles with substantially inert particles, with the degree of dilution decreasing from the inlet to the outlet of said reactor.

Claim 2

A method for converting at least one feedstock alkane containing from one to three carbon atoms to a higher molecular weight hydrocarbon comprising: reacting said feedstock alkane with air to form a gaseous product mixture comprising carbon monoxide, hydrogen, and nitrogen and passing said gaseous product mixture through an elongated reactor packed with a bed of particles comprising a Fischer-Tropsch catalyst, maintained at a pressure in the range of from about 1 to about 50 pounds per square inch gauge and cooled to maintain the temperature therein in the range of from about 160° C. to about 240° C., to thereby form a gaseous product stream comprising aliphatic hydrocarbon products having higher molecular weights than the feedstock alkane, the Fischer-Tropsch catalyst in the bed of particles of said reactor having increasing average activity for the conversion of synthesis gas from the inlet to the outlet of said reactor, the activity gradient being effected by dilution of Fischer-Tropsch catalyst particles with substantially inert particles, with the degree of dilution decreasing from the inlet to the outlet of said reactor.

Claim 3

A method for converting at least one feedstock alkane containing from one to three carbon atoms to a higher molecular weight hydrocarbon comprising: reacting said feedstock alkane with air to form a gaseous product mixture comprising carbon monoxide, hydrogen, and nitrogen and passing said gaseous product mixture through an elongated reactor packed with a bed of particles comprising a Fischer-Tropsch catalyst, maintained at a pressure in the range of from about 1 to about 50 pounds per square inch gauge and cooled to maintain the temperature therein in the range of from about 160° C. to about 240° C., to thereby form a gaseous product stream comprising aliphatic hydrocarbon products having higher molecular weights than the feedstock alkane, the Fischer-Tropsch catalyst in the bed of particles of said reactor having increasing average activity for the conversion of synthesis gas from the inlet to the outlet of said reactor, the activity gradient being effected by maintaining the temperature of the particles in the inlet portion of said reactor at a relatively lower level and the temperature of the particles in the outlet portion of said reactor at a relatively higher level, with the temperature of particles generally increasing from the inlet portion to the outlet portion of the bed of particles of said reactor.

Claim 4

A method for converting at least one feedstock alkane containing from one to three carbon atoms to a higher molecular weight hydrocarbon comprising: reacting said feedstock alkane with air to form a gaseous product mixture comprising carbon monoxide, hydrogen, and nitrogen and passing said gaseous product mixture through an elongated reactor packed with a bed of particles comprising a Fischer-Tropsch catalyst, maintained at a pressure in the range of from about 1 to about 50 pounds per square inch gauge and cooled to maintain the temperature therein in the range of from about 160° C. to about 240° C., to thereby form a gaseous product stream comprising aliphatic hydrocarbon products having higher molecular weights than the feedstock alkane, the Fischer-Tropsch catalyst in the bed of particles of said reactor having increasing average activity for the conversion of synthesis gas from the inlet to the outlet of said reactor, the activity gradient being effected by maintaining the temperature of the particles in the inlet portion of said reactor at a relatively lower level and the temperature of the particles in the outlet portion of said reactor at a relatively higher level, with the temperature of particles generally increasing from the inlet portion to the outlet portion of the bed of particles of said reactor.

Claim 5

A method for converting at least one feedstock alkane containing from one to three carbon atoms to a higher molecular weight hydrocarbon comprising: reacting said feedstock alkane with air to form a gaseous product mixture comprising carbon monoxide, hydrogen, and nitrogen and passing said gaseous product mixture through an elongated reactor packed with a bed of particles comprising a Fischer-Tropsch catalyst, maintained at a pressure in the range of from about 1 to about 50 pounds per square inch gauge and cooled to maintain the temperature therein in the range of from about 160° C. to about 240° C. to thereby form a gaseous product stream comprising aliphatic hydrocarbon products having higher molecular weights than the feedstock alkane, the Fischer-Tropsch catalyst in the bed of particles of said reactor having increasing average activity for the conversion of synthesis gas from the inlet to the outlet of said reactor, the activity gradient being effected by employing in the inlet portion of said reactor catalyst particles having a lower concentration of a component therein which is catalytically effective in synthesis gas conversion and in the outlet portion of said reactor catalyst particles having a relatively higher concentration of the aforesaid catalytically effective component, with the concentration of the aforesaid catalytically effective component increasing from the inlet portion to the outlet portion of the bed of particles of said reactor.

Claim 6

A method for converting at least one feedstock alkane containing from one to three carbon atoms to a higher molecular weight hydrocarbon comprising: reacting said feedstock alkane with air to form a gaseous product mixture comprising carbon monoxide, hydrogen, and nitrogen and passing said gaseous product mixture through an elongated reactor packed with a bed of particles comprising a Fischer-Tropsch catalyst, maintained at a pressure in the range of from about 1 to about 50 pounds per square inch gauge and cooled to maintain the temperature therein in the range of from about 160° C. to about 240° C. to thereby form a gaseous product stream comprising aliphatic hydrocarbon products having higher molecular weights than the feedstock alkane, the Fischer-Tropsch catalyst in the bed of particles of said reactor having increasing average activity for the conversion of synthesis gas from the inlet to the outlet of said reactor, the activity gradient being effected by employing in the inlet portion of said reactor catalyst particles having a lower concentration of a component therein which is catalytically effective in synthesis gas conversion and in the outlet portion of said reactor catalyst particles having a relatively higher concentration of the aforesaid catalytically effective component, with the concentration of the aforesaid catalytically effective component increasing from the inlet portion to the outlet portion of the bed of particles of said reactor.

Claim 7

A method for converting a gaseous mixture comprising carbon monoxide, hydrogen, and nitrogen to a hydrocarbon, said method comprising the step of passing said gaseous mixture through an elongated reactor packed with a bed of particles comprising a Fischer-Tropsch catalyst, maintained at a pressure in the range of from about 1 to about 50 pounds per square inch gauge and cooled to maintain the temperature therein in the range of from about 160° C. to about 240° C., to thereby form a gaseous product stream comprising aliphatic hydrocarbon products, the Fischer-Tropsch catalyst in the bed of particles of said reactor having increasing average activity for the conversion of synthesis gas from the inlet to the outlet of said reactor, the activity gradient being effected by dilution of Fischer-Tropsch catalyst particles with substantially inert particles, with the degree of dilution decreasing from the inlet to the outlet of said reactor.

Claim 8

A method for converting a gaseous mixture comprising carbon monoxide, hydrogen, and nitrogen to a hydrocarbon, said method comprising the step of passing said gaseous mixture through an elongated reactor packed with a bed of particles comprising a Fischer-Tropsch catalyst, maintained at a pressure in the range of from about 1 to about 50 pounds per square inch gauge and cooled to maintain the temperature therein in the range of from about 160° C. to about 240° C., to thereby form a gaseous product stream comprising aliphatic hydrocarbon products, the Fischer-Tropsch catalyst in the bed of particles of said reactor having increasing average activity for the conversion of synthesis gas from the inlet to the outlet of said reactor, the activity gradient being effected by dilution of Fischer-Tropsch catalyst particles with substantially inert particles, with the degree of dilution decreasing from the inlet to the outlet of said reactor.

Claim 9

A method for converting a gaseous mixture comprising carbon monoxide, hydrogen, and nitrogen to a hydrocarbon, said method comprising the step of passing said gaseous mixture through an elongated reactor packed with a bed of particles comprising a Fischer-Tropsch catalyst, maintained at a pressure in the range of from about 1 to about 50 pounds per square inch gauge and cooled to maintain the temperature therein in the range of from about 160° C. to about 240° C., to thereby form a gaseous product stream comprising aliphatic hydrocarbon products, the Fischer-Tropsch catalyst in the bed of particles of said reactor having increasing average activity for the conversion of synthesis gas from the inlet to the outlet of said reactor, the activity gradient being effected by maintaining the temperature of the particles in the inlet portion of said reactor at a relatively lower level and the temperature of the particles in the outlet portion of said reactor at a relatively higher level, with the temperature of the particles generally increasing from the inlet portion to the outlet portion of the bed of particles of said reactor.

Claim 10

A method for converting a gaseous mixture comprising carbon monoxide, hydrogen, and nitrogen to a hydrocarbon, said method comprising the step of passing said gaseous mixture through an elongated reactor packed with a bed of particles comprising a Fischer-Tropsch catalyst, maintained at a pressure in the range of from about 1 to about 50 pounds per square inch gauge and cooled to maintain the temperature therein in the range of from about 160° C. to about 240° C., to thereby form a gaseous product stream comprising aliphatic hydrocarbon products, the Fischer-Tropsch catalyst in the bed of particles of said reactor having increasing average activity for the conversion of synthesis gas from the inlet to the outlet of said reactor, the activity gradient being effected by maintaining the temperature of the particles in the inlet portion of said reactor at a relatively lower level and the temperature of the particles in the outlet portion of said reactor at a relatively higher level, with the temperature of the particles generally increasing from the inlet portion to the outlet portion of the bed of particles of said reactor.

Claim 11

A method for converting a gaseous mixture comprising carbon monoxide, hydrogen, and nitrogen to a hydrocarbon, said method comprising the step of passing said gaseous mixture through an elongated reactor packed with a bed of particles comprising a Fischer-Tropsch catalyst, maintained at a pressure in the range of from about 1 to about 50 pounds per square inch gauge and cooled to maintain the temperature therein in the range of from about 160° C. to about 240° C., to thereby form a gaseous product stream comprising aliphatic hydrocarbon products, the Fischer-Tropsch catalyst in the bed of particles of said reactor having increasing average activity for the conversion of synthesis gas from the inlet to the outlet of said reactor, the activity gradient being effected by employing in the inlet portion of said reactor catalyst particles having a lower concentration of a component therein which is catalytically effective in synthesis gas conversion and in the outlet portion of said reactor catalyst particles having a relatively higher concentration of the aforesaid catalytically effective component, with the concentration of the aforesaid catalytically effective component increasing from the inlet portion to the outlet portion of the bed of particles of said reactor.

Claim 12

A method for converting a gaseous mixture comprising carbon monoxide, hydrogen, and nitrogen to a hydrocarbon, said method comprising the step of passing said gaseous mixture through an elongated reactor packed with a bed of particles comprising a Fischer-Tropsch catalyst, maintained at a pressure in the range of from about 1 to about 50 pounds per square inch gauge and cooled to maintain the temperature therein in the range of from about 160° C. to about 240° C., to thereby form a gaseous product stream comprising aliphatic hydrocarbon products, the Fischer-Tropsch catalyst in the bed of particles of said reactor having increasing average activity for the conversion of synthesis gas from the inlet to the outlet of said reactor, the activity gradient being effected by employing in the inlet portion of said reactor catalyst particles having a lower concentration of a component therein which is catalytically effective in synthesis gas conversion and in the outlet portion of said reactor catalyst particles having a relatively higher concentration of the aforesaid catalytically effective component, with the concentration of the aforesaid catalytically effective component increasing from the inlet portion to the outlet portion of the bed of particles of said reactor.