Methods, systems, and devices for liquid hydrocarbon fuel production, hydrocarbon chemical production, and aerosol capture
원문보기
IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
C10G-001/00
B01D-050/00
C10B-053/02
C10B-053/00
C10L-001/04
C10B-047/06
C10G-001/02
B01D-045/08
B01D-047/02
B01D-053/14
C10G-001/06
C10B-001/02
C10B-007/10
출원번호
US-0593876
(2015-01-09)
등록번호
US-9254461
(2016-02-09)
발명자
/ 주소
Weaver, Samuel C.
Hensley, Daniel L.
Weaver, Samuel P.
Weaver, Daniel C.
Smith, Lee S.
출원인 / 주소
Proton Power, Inc.
대리인 / 주소
Wilson Patent Law, LLC
인용정보
피인용 횟수 :
5인용 특허 :
25
초록▼
Methods, systems, and devices for liquid hydrocarbon fuel production, hydrocarbon chemical production, and aerosol capture are provided. For example, a carbon-oxygen-hydrogen (C—O—H) compound may be heated to a temperature of at least 800 degrees Celsius such that the C—O—H compound reacts through a
Methods, systems, and devices for liquid hydrocarbon fuel production, hydrocarbon chemical production, and aerosol capture are provided. For example, a carbon-oxygen-hydrogen (C—O—H) compound may be heated to a temperature of at least 800 degrees Celsius such that the C—O—H compound reacts through a non-oxidation reaction to generate at least a hydrocarbon compound that may be at least a component of a liquid hydrocarbon fuel or a hydrocarbon chemical. The liquid hydrocarbon fuel may be a liquid when at a temperature of 20 degrees Celsius. The C—O—H compound may include biomass. In some cases, the hydrocarbon compound produced through the non-oxidation reaction includes a hydrocarbon aerosol form as the hydrocarbon compound at least as it is produced or cools. Some embodiments include aerosol capture methods, systems, and devices, which may include passing a hydrocarbon aerosol form through a material in a liquid phase in order to gather the aerosol material.
대표청구항▼
1. A method of direct liquid hydrocarbon fuel production comprising: heating a compound comprising carbon, oxygen, and hydrogen, wherein the compound is selected from a group consisting of biomass and waste product, to a temperature of at least 800 degrees Celsius such that the compound comprising c
1. A method of direct liquid hydrocarbon fuel production comprising: heating a compound comprising carbon, oxygen, and hydrogen, wherein the compound is selected from a group consisting of biomass and waste product, to a temperature of at least 800 degrees Celsius such that the compound comprising carbon, oxygen, and hydrogen has a residence time of at least 100 seconds and reacts through a pyrolysis reaction to generate at least a hydrocarbon aerosol that includes at least naphthalene or a component of a hydrocarbon fuel, wherein the hydrocarbon fuel includes at least gasoline, diesel, or aviation fuel; andbubbling the hydrocarbon aerosol through a liquid fuel to gather the hydrocarbon aerosol and produce the liquid hydrocarbon fuel, wherein the liquid fuel includes at least gasoline, diesel, or aviation fuel and the liquid hydrocarbon fuel includes at least gasoline, diesel, or aviation fuel. 2. The method of claim 1, wherein the liquid hydrocarbon fuel is liquid when at a temperature of 20 degrees Celsius. 3. The method of claim 1, wherein the pyrolysis reaction comprises a hydrous pyrolysis reaction. 4. The method of claim 1, further comprising directly distilling the liquid hydrocarbon fuel. 5. The method of claim 1, wherein bubbling the hydrocarbon aerosol through the liquid fuel includes bubbling the hydrocarbon aerosol through a mesh disposed within the liquid fuel. 6. The method of claim 1, further comprising mixing the liquid hydrocarbon fuel with at least another liquid fuel. 7. The method of claim 1, wherein the biomass comprises at least cellulose, lignin, or hemicelluloses and the waste product comprises at least paper waste, sawdust, cardboard, hay, straw, switchgrass, municipal solid waste, sanitized waste, simulated nuclear waste, demolition wood waste, or construction wood waste. 8. The method of claim 1, wherein the compound comprising carbon, oxygen, and hydrogen has a residence time of at least 300 second. 9. The method of claim 1, wherein the pyrolysis reaction is performed within a tube furnace. 10. The method of claim 9, wherein the tube furnace includes a material composition that includes at least a high-nickel metal alloy. 11. The method of claim 9, further comprising using an auger to effect continuous motion of the compound comprising carbon, oxygen, and hydrogen into and through the tube furnace and wherein the compound comprising carbon, oxygen, and hydrogen is in a solid phase. 12. The method of claim 1, wherein the temperature is at least 1100 degrees Celsius. 13. The method of claim 1, wherein the liquid hydrocarbon fuel has an energy content of at least 16,000 BTU/lb or 37,000 kJ/kg. 14. The method of claim 1, wherein the compound comprising carbon, oxygen, and hydrogen comprises a compound comprising carbon, oxygen, and hydrogen mixed with at least water. 15. The method of claim 14, wherein heating the compound comprising carbon, oxygen, and hydrogen comprises reacting the mixed water as well as any water in the compound comprising carbon, oxygen, and hydrogen with the compound comprising carbon, oxygen, and hydrogen to generate at least the hydrocarbon aerosol. 16. The method of claim 1, wherein the compound comprising carbon, oxygen, and hydrogen comprises a wet compound comprising carbon, oxygen, and hydrogen. 17. The method of claim 16, further comprising heating the wet compound comprising carbon, oxygen, and hydrogen through reacting water from the wet compound comprising carbon, oxygen, and hydrogen with the compound comprising carbon, oxygen, and hydrogen to generate at least the hydrocarbon aerosol. 18. The method of claim 17, further comprising transferring the wet compound comprising carbon, oxygen, and hydrogen to a reaction chamber before heating the wet compound comprising carbon, oxygen, and hydrogen. 19. The method of claim 11, wherein the auger comprises a composition that includes at least a high-nickel metal alloy. 20. The method of claim 11, wherein the auger includes at least a single pitch between a plurality of blades or multiple different pitches between the plurality of blades. 21. The method of claim of 1, further comprising distilling at least a portion of the generated hydrocarbon aerosol. 22. The method of claim 1, wherein bubbling the hydrocarbon aerosol through the liquid fuel includes bubbling the hydrocarbon aerosol with respect to a plurality of baffles disposed within the liquid fuel. 23. The method of claim 22, wherein bubbling the hydrocarbon aerosol through the liquid fuel includes bubbling the hydrocarbon aerosol through a mesh disposed around the plurality of baffles disposed within the liquid fuel.
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