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A method of producing liquid fuel by a Fischer-Tropsch synthesis reaction using a thermal medium-circulated heat exchanger type reactor is provided. The thermal medium-circulated heat exchanger type reactor uses the cobalt metal foam catalyst including a metal foam coated with cobalt catalyst powder

A method of producing liquid fuel by a Fischer-Tropsch synthesis reaction using a thermal medium-circulated heat exchanger type reactor is provided. The thermal medium-circulated heat exchanger type reactor uses the cobalt metal foam catalyst including a metal foam coated with cobalt catalyst powder is used. Exothermic reaction heat generated by the Fischer-Tropsch synthesis reaction occurring in the cobalt metal foam catalyst layer of the tube unit is controlled by thermal medium oil circulating in the shell unit at a reaction temperature of 190˜250° C. and a reaction pressure of 20˜25 atm, and simultaneously the reaction is conducted, thus producing liquid fuel.

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1. A method of producing liquid fuel by a Fischer-Tropsch synthesis reaction using a thermal medium-circulated heat exchanger type reactor, comprising: preparing a tube unit comprising an outer heat exchange surface having a circumference and a shell unit that fully surrounds the circumference of th

1. A method of producing liquid fuel by a Fischer-Tropsch synthesis reaction using a thermal medium-circulated heat exchanger type reactor, comprising: preparing a tube unit comprising an outer heat exchange surface having a circumference and a shell unit that fully surrounds the circumference of the outer heat exchange surface of the tube unit to form a space between the tube unit and the shell unit;disposing a cobalt metal-foam catalyst layer inside the tube unit;supplying a synthesis gas into an upper portion of the tube unit through a synthesis gas supply line;heating the cobalt metal-foam catalyst layer to bring about a Fischer-Tropsch synthesis reaction inside the tube unit, using an electric heater provided at the circumference of the shell unit, to thereby produce a liquid fuel product from the synthesis gas;supplying a thermal medium oil having a predetermined temperature into a lower portion of the space through a thermal medium oil supply line;recovering the thermal medium oil from an upper portion of the space through a thermal medium oil recovery line;heat-exchanging between the tube unit and the thermal medium oil using a heat exchange pin protruding from an outer surface of the tube unit, thereby controlling heat generated by the Fischer-Tropsch synthesis reaction;recovering the liquid fuel product through a lower portion of the tube unit,wherein the metal-foam of the cobalt metal-foam catalyst layer comprises any one of iron-chromium-aluminum alloy, nickel-chromium alloy, copper-nickel alloy, aluminum-copper alloy, zinc-copper alloy, or silver-copper alloy, andthe metal-foam was pre-treated by atomic layer deposition to form an Al2O3 thin film on the surface of the metal-foam. 2. The method of producing liquid fuel according to claim 1, further comprising: controlling the predetermined temperature using a heat exchanger provided on the thermal medium oil supply line. 3. The method of producing liquid fuel according to claim 2, wherein the predetermined temperature is adjusted to 190˜250° C. 4. The method of producing liquid fuel according to claim 1, wherein the cobalt metal-foam catalyst layer is heated to 300˜500° C. 5. A method of producing liquid fuel by a Fischer-Tropsch synthesis reaction using a thermal medium-circulated heat exchanger type reactor, comprising: preparing a tube unit comprising an outer heat exchange surface having a circumference and a shell unit that fully surrounds the circumference of the outer heat exchange surface of the tube unit to form a space between the tube unit and the shell unit;disposing a cobalt metal-foam catalyst layer inside the tube unit, wherein the cobalt metal-foam catalyst layer is heated to 300˜500° C.;supplying a synthesis gas into an upper portion of the tube unit through a synthesis gas supply line;heating the cobalt metal-foam catalyst layer to bring about a Fischer-Tropsch synthesis reaction inside the tube unit, using an electric heater provided at the circumference of the shell unit, to thereby produce a liquid fuel product from the synthesis gas;supplying a thermal medium oil having a predetermined temperature into a lower portion of the space through a thermal medium oil supply line;controlling the predetermined temperature using a heat exchanger provided on the thermal medium oil supply line, wherein the predetermined temperature is adjusted to 190˜250° C.;recovering the thermal medium oil from an upper portion of the space through a thermal medium oil recovery line;heat-exchanging between the tube unit and the thermal medium oil using a heat exchange pin protruding from an outer surface of the tube unit, thereby controlling heat generated by the Fischer-Tropsch synthesis reaction;recovering the liquid fuel product through a lower portion of the tube unit, andwherein the metal-foam comprises a copper-nickel alloy that was pre-treated by atomic layer deposition to form and Al2O3 thin film on the surface of the metal-foam. 6. The method of producing liquid fuel according to claim 1, wherein the metal-foam of the cobalt metal-foam catalyst layer comprises aluminum, iron, iron-chromium-aluminum alloy, nickel-chromium alloy, copper-nickel alloy, aluminum-copper alloy, zinc-copper alloy, or silver-copper alloy. 7. The method of producing liquid fuel according to claim 6, wherein the metal-foam comprises a copper-nickel alloy that was pre-treated by atomic layer deposition to form an Al2O3 thin film on the surface of the metal-foam.