초록 ▼

A mixture of natural gas and air is converted to a C 5-C19 diesel fuel-grade liquid hydrocarbon. The natural gas and air mixture is supplied to the input of a catalytic partial oxidation reactor. The carbon-containing gas output of the catalytic partial oxidation reactor is connected as an input to

A mixture of natural gas and air is converted to a C 5-C19 diesel fuel-grade liquid hydrocarbon. The natural gas and air mixture is supplied to the input of a catalytic partial oxidation reactor. The carbon-containing gas output of the catalytic partial oxidation reactor is connected as an input to a first Fischer-Tropsch reactor, to thereby form a first diesel fuel grade C5-C19 liquid hydrocarbon output. A carbon-containing gas output of the first Fischer-Tropsch reactor is connected to the input of a second Fischer-Tropsch reactor, to thereby form a second diesel fuel grade C 5-C19 liquid hydrocarbon output. The catalytic partial oxidation reactor contains a platinum group catalyst, a promoted platinum group catalyst, a rhodium catalyst, or a platinum promoted rhodium catalyst. Each of the Fischer-Tropsch reactors contain a catalyst that is made up of from about 3 to about 60 parts-by-weight cobalt and from about 0.1 to about 100 parts-by-weight of at least one metal selected from a group consisting of cerium, lanthanum and ruthenium per 100 parts-by-weight of a support selected from a group consisting of silica, alumina and combinations of silica and alumina, and more preferably a catalyst that is made up of about 20 percent by weight cobalt, about 0.1 percent by weight ruthenium, about 0.1 percent by weight platinum, the remainder being an alumina support.

대표청구항 ▼

What is claimed is: 1. Apparatus for processing a low molecular weight gas-phase hydrocarbon in order to provide a high molecular weight, liquid-phase hydrocarbon, compression ignition fuel, comprising: a catalytic partial oxidation reactor having an input and an output; a platinum-group catalyst w

What is claimed is: 1. Apparatus for processing a low molecular weight gas-phase hydrocarbon in order to provide a high molecular weight, liquid-phase hydrocarbon, compression ignition fuel, comprising: a catalytic partial oxidation reactor having an input and an output; a platinum-group catalyst within said catalytic partial oxidation reactor; supply means for supplying a pressurized oxygen-containing gas such as air and a pressurized low molecular weight gas-phase hydrocarbon to said input of said catalytic partial oxidation reactor; a synthesis reactor having an input connected to said output of said catalytic partial oxidation reactor, and having an output; a second catalyst within said synthesis reactor; said second catalyst including from about 3 to about 60 parts-by-weight cobalt and from about 0.1 to about 100 parts-by-weight of at least one metal selected from a group consisting of cerium, lanthanum, platinum and ruthenium per 100 parts-by-weight of a support selected from a group consisting of silica, alumina and combinations of silica and alumina; and a first liquid separator having an input connected to said output of said synthesis reactor, and having an output providing said high molecular weight, liquid-phase hydrocarbon, compression-ignition fuel. 2. The apparatus of claim 1 wherein said catalytic partial oxidation reactor operates at a temperature of from about 700 to about 1000 degrees centigrade and at a pressure of about 2 to about 25 bar, and wherein said synthesis reactor operates at a temperature of from about 125 to about 350 degrees centigrade and at a pressure of from about 5 to about 100 bar. 3. The apparatus of claim 1 wherein said platinum-group catalyst is selected from a group consisting of a promoted platinum-group catalyst, a rhodium catalyst, and a rhodium catalyst having a platinum promoter. 4. The apparatus of claim 3 wherein said catalytic partial oxidation reactor operates at a temperature of from about 700 to about 1000 degrees centigrade and at a pressure of from about 2 to about 25 bar, and wherein said first synthesis reactor operates at a temperature of from about 125 to about 359 degrees centigrade and at a pressure of from about 5 to about 100 bar. 5. The apparatus of claim 1 wherein said second catalyst is prepared by impregnating said support with at least cobalt and said metal. 6. The apparatus of claim 5 wherein said platinum-group catalyst is selected from a group consisting of a promoted platinum-group catalyst, a rhodium catalyst, and a rhodium catalyst having a platinum promoter. 7. The apparatus of claim 1 wherein said low molecular weight gas-phase hydrocarbon is selected from a group consisting of methane, natural gas, and a mixture of methane and natural gas. 8. The apparatus of claim 1 wherein said second catalyst contains from about 15 to about 50 parts-by-weight cobalt. 9. The apparatus of claim 1 wherein said metal is cerium and said support is alumina. 10. The apparatus of claim 1 wherein said synthesis reactor is a first Fischer-Tropsch reactor. 11. The apparatus claim 10 including: a second Fischer Tropsch reactor having an input, an output, and having said second catalyst therein; a first liquid/gas separator connected intermediate said output of said first Fischer-Tropsch reactor and said input of said first liquid separator; said first liquid/gas separator having a liquid output connected to said input of said first liquid separator, and having a gas output connected to said input of said second Fischer-Tropsch reactor; and a second liquid separator having an input connected to said output of said second Fischer-Tropsch reactor, and having an output providing said high molecular weight, liquid-phase hydrocarbon, compression ignition fuel. 12. The apparatus of claim 1 wherein said synthesis reactor is a first Fischer-Tropsch reactor including: a first cooling heat exchanger having an output, and having an input connected to said output of said catalytic partial oxidation reactor; a first liquid/gas separator having an input connected to said output of said first cooling heat exchanger, and having a hydrocarbon-containing gas output connected to said input of said first Fischer-Tropsch reactor; a second cooling heat exchanger having an output and having an input connected to said output of said first Fischer-Tropsch reactor; a second liquid/gas separator having an input connected to said output of said second cooling heat exchanger, having a liquid output connected to said input of said first liquid separator, and having a hydrocarbon containing gas output; a heating heat exchanger having an input connected to said hydrocarbon-containing gas output of said second liquid/gas separator, and having an output; a second Fischer-Tropsch reactor having an input connected to said output of said heating heat exchanger having an output, and having said second catalyst therein; a third cooling heat exchanger having an input connected to said output of said second Fischer-Tropsch reactor, and having an output; and a second liquid separator having an input connected to said output of said third cooling heat exchanger, and an output providing said high molecular weight, liquid-phase hydrocarbon, compression-ignition fuel. 13. The apparatus claim 12 wherein said catalytic partial oxidation reactor is operated at a temperature of from about 700 to about 1000 degrees centigrade and at a pressure of from about 2 to about 25 bar, and wherein said first and second Fischer-Tropsch reactors are operated at a temperature of from about 125 to about 350 degrees centigrade and at a pressure of from about 5 to about 100 bar. 14. The apparatus of claim 13 wherein said high molecular weight, liquid-phase hydrocarbon, compression-ignition fuel is a C5+ hydrocarbon. 15. Apparatus for processing a low molecular weight gas-phase hydrocarbon to provide a high molecular weight, liquid-phase hydrocarbon compression-ignition fuel comprising: a first Fischer Tropsch reactor having an input connected to receive said low molecular weight gas-phase hydrocarbon, and having an output; a catalyst within said first Fischer-Tropsch reactor including about 20 percent by weight cobalt, about 0.1-percent by weight ruthenium, about 1.0-percent by weight platinum, the remainder being an alumina support; and a first liquid/water separator having an input connected to said output of said first Fischer-Tropsch reactor, and having a liquid output providing said high molecular weight, liquid-phase hydrocarbon compression ignition fuel. 16. The apparatus claim 15 including: a second Fischer-Tropsch reactor having an input, an output and having said catalyst therein; a liquid/gas separator connected intermediate said output of said first Fischer-Tropsch reactor and said input of said first liquid/water separator; said liquid/gas separator having a liquid output connected to said input of said first liquid/water separator, and having a gas output connected to said input of said second Fischer-Tropsch reactor; and a second liquid/water separator having an input connected to said output of said second Fischer-Tropsch reactor, and having a liquid output providing said high molecular weight, liquid-phase hydrocarbon compression ignition fuel. 17. The apparatus of claim 16 wherein said high molecular weight, liquid-phase hydrocarbon, compression-ignition fuel is a C5+ hydrocarbon. 18. Apparatus for processing a low molecular weight gas-phase hydrocarbon in order to provide a high molecular weight, liquid-phase hydrocarbon, compression ignition fuel comprising: a catalytic partial oxidation reactor having an input and an output; a platinum-group catalyst within said catalytic partial oxidation reactor; supply means for supplying a pressurized oxygen-containing gas such as air and a pressurized low molecular weight gas-phase hydrocarbon to said input of said catalytic partial oxidation reactor; a synthesis reactor having an input connected to said output of said catalytic partial oxidation reactor, and having an output; a second catalyst within said synthesis reactor; said second catalyst including about 20 percent by weight cobalt, about 0.1 percent by weight ruthenium, about 1.0 percent by weight platinum, the remainder being an alumina support; and a liquid separator having an input connected to said output of said synthesis reactor, and having an output providing said high molecular weight, liquid-phase hydrocarbon, compression-ignition fuel. 19. The apparatus of claim 1 wherein said at least one metal is ruthenium, and wherein said support is alumina.