Cobalt metal foam catalyst, method of making same, thermal-medium-circulating heat-exchange reactor using same, and method of producing a liquid fuel by means of a Fischer-Tropsch synthesis reaction using thermal-medium-circulating heat-exchange reactor

US10160917B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10160917-B2
Application numberUS-201615075743-A
CountryUS
Kind codeB2
Filing dateMar 21, 2016
Priority dateFeb 16, 2010
Publication dateDec 25, 2018
Grant dateDec 25, 2018

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Abstract

Official abstract text for this publication.

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.

First claim

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The invention claimed is: 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, and the metal-foam was pre-treated by atomic layer deposition to form an Al 2 O 3 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, and wherein the metal-foam comprises a copper-nickel alloy that was pre-treated by atomic layer deposition to form and Al 2 O 3 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 Al 2 O 3 thin film on the surface of the metal-foam.

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What does patent US10160917B2 cover?
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 …
Who is the assignee on this patent?
Korea Inst Energy Res
What technology area does this patent fall under?
Primary CPC classification C10G2/34. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Dec 25 2018 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).