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公开(公告)号：US20180280906A1
公开(公告)日：2018-10-04
申请号：US15873052
申请日：2018-01-17
Applicant: Proton Power, Inc.
Inventor： Samuel C. Weaver
Abstract: Tools and techniques for biochar method, systems, devices, and products are provided in accordance with various embodiments. For example, methods are provided in accordance with various embodiments that may include rubbing one or more objects with biochar. Rubbing the one or more objects with biochar may include: polishing one or more objects utilizing biochar; cleaning one or more objects utilizing biochar; grinding one or more objects utilizing biochar; scratching one or more objects utilizing biochar; and/or abrading one or more objects utilizing biochar. In some embodiments, polishing the one or more objects utilizing the biochar includes: combining water, the biochar, and the one or more objects; and/or tumbling the combined water, biochar, and one or more objects. The one or more objects may include one or more stones. The tumbling may occur for 72 hours or less. The tumbling may occur as a single step.
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公开(公告)号：US20160362607A1
公开(公告)日：2016-12-15
申请号：US15062788
申请日：2016-03-07
Applicant: Proton Power, Inc.
Inventor： Samuel C. Weaver , Daniel L. Hensley , Jim Bierkamp , Neal Evans , Will Johnson , Bryan Biss , Davis McLemore , John Borden , Carson Bone , Priyanka Bhattacharya
IPC: C10B53/02 , C05F11/00 , C05G3/00 , C10B53/00 , A23K20/20 , A01K1/015 , A01K31/04 , C10B57/00 , C05F11/08 , C08L95/00
CPC classification number: C10B53/02 , A01K1/0154 , A01K31/04 , A23K20/20 , C01B32/184 , C01B32/20 , C05F11/00 , C05F11/02 , C05F11/08 , C05G3/0005 , C08L95/00 , C08L2555/50 , C10B53/00 , C10B57/005 , C10L5/44 , C10L9/086 , Y02E50/10 , Y02E50/14 , Y02E50/30
Abstract: Tools and techniques for biochar production and biochar products are provided in accordance with various embodiments. For example, some embodiments include a method of biochar production that may include introducing a compound that includes at least carbon, oxygen, and hydrogen into a reaction chamber. The compound may be heated to a temperature of at least 1,000 degrees Celsius in the reaction chamber such that the compound reacts through a pyrolysis reaction to produce biochar. The produced biochar may be collected and/or further processed in some cases. In some embodiments, the compound includes at least biomass or a waste product. In some embodiments, the temperature of the reaction chamber is at least 1,100 degrees Celsius. In some embodiments, the compound has a residence time in the reaction chamber between 10 seconds and 1,000 seconds to produce the biochar. Some embodiments include biochar that may include graphite or graphene.
Abstract translation: 根据各种实施方案提供用于生物炭生产和生物炭产品的工具和技术。 例如，一些实施方案包括生物碳生产的方法，其可以包括将至少包含碳，氧和氢的化合物引入反应室。 化合物可以在反应室中加热到至少1000摄氏度的温度，使得化合物通过热解反应进行反应以产生生物炭。 生产的生物炭可能在某些情况下被收集和/或进一步加工。 在一些实施方案中，化合物至少包括生物质或废物。 在一些实施方案中，反应室的温度至少为1100摄氏度。 在一些实施方案中，化合物在反应室中的停留时间在10秒至1,000秒之间以产生生物炭。 一些实施方案包括可以包括石墨或石墨烯的生物炭。
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13.发明授权Methods, systems, and devices for liquid hydrocarbon fuel production, hydrocarbon chemical production, and aerosol capture 有权用于液体碳氢化合物燃料生产，碳氢化合物生产和气溶胶捕获的方法，系统和装置公开(公告)号：US09254461B2
公开(公告)日：2016-02-09
申请号：US14593876
申请日：2015-01-09
Applicant: Proton Power, Inc.
Inventor： Samuel C. Weaver , Daniel L. Hensley , Samuel P. Weaver , Daniel C. Weaver , Lee S. Smith
IPC: C10G1/00 , B01D50/00 , C10B53/02 , C10B53/00 , C10L1/04 , C10B47/06 , C10G1/02 , B01D45/08 , B01D47/02 , B01D53/14 , C10G1/06 , C10B1/02 , C10B7/10
CPC classification number: C10G1/02 , B01D45/08 , B01D47/02 , B01D50/004 , B01D53/1412 , B01D53/1418 , B01D53/1425 , B01D53/1487 , B01D53/1493 , B01D2252/103 , C10B1/02 , C10B7/10 , C10B47/06 , C10B47/44 , C10B53/00 , C10B53/02 , C10G1/00 , C10G1/002 , C10G1/06 , C10G3/40 , C10G2300/1011 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10L1/04 , C10L1/06 , C10L1/08 , C10L2200/0469 , C10L2270/023 , C10L2270/026 , C10L2270/04 , C10L2290/02 , C10L2290/06 , C10L2290/08 , C10L2290/24 , C10L2290/543 , C10L2290/544 , C10L2290/547 , C10L2290/56 , Y02E50/14 , Y02P30/20 , Y02T50/678
Abstract: 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.
Abstract translation: 提供了液体烃燃料生产，碳氢化合物生产和气溶胶捕集的方法，系统和装置。 例如，可以将碳 - 氢 - 氢（C-O-H）化合物加热到至少800摄氏度的温度，使得C-O-H化合物通过非氧化反应反应以产生至少一种 烃化合物，其可以是至少液体烃燃料或烃化学物质的组分。 当液体烃燃料在20摄氏度的温度下可以是液体。 C-O-H化合物可包括生物质。 在一些情况下，通过非氧化反应产生的烃化合物至少包括烃生成或冷却的烃类气溶胶形式。 一些实施例包括气溶胶捕获方法，系统和装置，其可以包括使烃气溶胶形式通过液相中的材料以收集气溶胶材料。
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公开(公告)号：US20150275109A1
公开(公告)日：2015-10-01
申请号：US14679141
申请日：2015-04-06
Applicant: Proton Power, Inc.
Inventor： Samuel C. Weaver , Daniel L. Hensley , Samuel P. Weaver , Daniel C. Weaver
IPC: C10J3/82
CPC classification number: C10J3/82 , C01B3/50 , C01B32/50 , C01B2203/04 , C01B2203/1211 , C10G2300/1011 , C10J3/00 , C10J2200/15 , C10J2300/0909 , C10J2300/0916 , C10J2300/0973 , C10J2300/1246 , C10J2300/1253 , C10J2300/1807 , C10J2300/1861 , C10J2300/1884 , C10K1/002 , C10K1/024 , C10K1/20 , C10K1/32 , Y02P20/145 , Y02P30/20
Abstract: Methods, systems, and/or devices for synthesis gas recapture are provided, which may include methods, systems, and/or devices for filtering a synthesis gas stream. In some cases, tars, particulates, water, and/or heat may be removed from the synthesis gas stream through the filtering of the synthesis gas stream. The filtered synthesis gas stream may then be captured and/or utilized in a variety of different ways. Some embodiments utilizing a C—O—H compound to filter a synthesis gas stream. In some embodiments, the C—O—H compound utilized to filter the synthesis gas stream may be utilized to produce additional synthesis gas. The additional synthesis gas may be filtered by additional C—O—H compound.
Abstract translation: 提供了用于合成气回收的方法，系统和/或装置，其可以包括用于过滤合成气流的方法，系统和/或装置。 在某些情况下，焦油，颗粒，水和/或热可以通过合成气流的过滤从合成气流中除去。 然后可以以各种不同的方式捕获和/或利用经过滤的合成气流。 利用C-O-H化合物过滤合成气流的一些实施方案。 在一些实施方案中，用于过滤合成气流的C-O-H化合物可用于产生另外的合成气。 另外的合成气可以通过另外的C-O-H化合物过滤。
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15.发明申请METHODS, SYSTEMS, AND DEVICES FOR LIQUID HYDROCARBON FUEL PRODUCTION, HYDROCARBON CHEMICAL PRODUCTION, AND AEROSOL CAPTURE 有权液体烃燃料生产的方法，系统和装置，油气化学生产和气溶胶捕获公开(公告)号：US20150203760A1
公开(公告)日：2015-07-23
申请号：US14593876
申请日：2015-01-09
Applicant: Proton Power, Inc.
Inventor： Samuel C. Weaver , Daniel L. Hensley , Samuel P. Weaver , Daniel C. Weaver , Lee S. Smith
CPC classification number: C10G1/02 , B01D45/08 , B01D47/02 , B01D50/004 , B01D53/1412 , B01D53/1418 , B01D53/1425 , B01D53/1487 , B01D53/1493 , B01D2252/103 , C10B1/02 , C10B7/10 , C10B47/06 , C10B47/44 , C10B53/00 , C10B53/02 , C10G1/00 , C10G1/002 , C10G1/06 , C10G3/40 , C10G2300/1011 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10L1/04 , C10L1/06 , C10L1/08 , C10L2200/0469 , C10L2270/023 , C10L2270/026 , C10L2270/04 , C10L2290/02 , C10L2290/06 , C10L2290/08 , C10L2290/24 , C10L2290/543 , C10L2290/544 , C10L2290/547 , C10L2290/56 , Y02E50/14 , Y02P30/20 , Y02T50/678
Abstract: 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.
Abstract translation: 提供了液体烃燃料生产，碳氢化合物生产和气溶胶捕集的方法，系统和装置。 例如，可以将碳 - 氢 - 氢（C-O-H）化合物加热到至少800摄氏度的温度，使得C-O-H化合物通过非氧化反应反应以产生至少一种 烃化合物，其可以是至少液体烃燃料或烃化学物质的组分。 当液体烃燃料在20摄氏度的温度下可以是液体。 C-O-H化合物可包括生物质。 在一些情况下，通过非氧化反应产生的烃化合物至少包括烃生成或冷却的烃类气溶胶形式。 一些实施例包括气溶胶捕获方法，系统和装置，其可以包括使烃气溶胶形式通过液相中的材料以收集气溶胶材料。
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Patent Agency Ranking
16.发明申请公开(公告)号：US20140287333A1
公开(公告)日：2014-09-25
申请号：US14183625
申请日：2014-02-19
Applicant: Proton Power, Inc.
Inventor： Samuel C. Weaver , Samuel P. Weaver , Daniel C. Weaver , Daniel L. Hensley
CPC classification number: C01B3/02 , C01B3/0094 , C01B3/323 , C10J3/00 , C10J2300/0903 , F02C3/00 , F23K5/002 , H01M8/0612 , H01M8/0618 , Y02E60/50
Abstract: Methods are disclosed for generating electrical power from a compound comprising carbon, oxygen, and hydrogen. Water is combined with the compound to produce a wet form of the compound. The wet form of the compound is transferred into a reaction processing chamber. The wet form of the compound is heated within the reaction chamber such that elements of the compound dissociate and react, with one reaction product comprising hydrogen gas. The hydrogen gas is processed to generate electrical power.
Abstract translation: 公开了从包含碳，氧和氢的化合物产生电力的方法。 水与化合物结合以产生湿形式的化合物。 化合物的湿形式转移到反应处理室中。 化合物的湿形式在反应室内加热，使得化合物的元素离解并反应，一个反应产物包含氢气。 处理氢气以产生电力。
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公开(公告)号：US10144875B2
公开(公告)日：2018-12-04
申请号：US14593692
申请日：2015-01-09
Applicant: Proton Power, Inc.
Inventor： Samuel C. Weaver , Daniel L. Hensley , Samuel P. Weaver , Daniel C. Weaver , Lee S. Smith
IPC: C10G1/02 , C10G1/00 , B01D53/14 , C10B53/02 , C10B53/00 , C10L1/04 , C10B47/06 , B01D45/08 , B01D47/02 , B01D50/00 , C10G1/06 , C10B1/02 , C10B7/10 , C10L1/06 , C10L1/08 , C10B47/44 , C10G3/00
Abstract: 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.
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公开(公告)号：US10005961B2
公开(公告)日：2018-06-26
申请号：US13800228
申请日：2013-03-13
Applicant: Proton Power, Inc.
Inventor： Samuel C. Weaver , Daniel L. Hensley , Samuel P. Weaver , Daniel C. Weaver
CPC classification number: C10G1/002 , C10G3/50 , C10G2300/1014 , C10L1/08 , Y02E50/13 , Y02E50/32 , Y02P30/20
Abstract: Methods, systems, and devices for continuous production of liquid fuels from biomass are provided. Some embodiments utilize a thermochemical process to produce a bio-oil in parallel with a thermochemical process to produce a hydrogen-rich synthesis gas. Both product streams may be fed into a third reaction chamber that may enrich the bio-oil with the hydrogen gas, for example, in a continuous production process. One product stream may include a liquid fuel such as diesel. Some embodiments may also produce other product streams including, but not limited to, electrical power generation and/or biochar.
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公开(公告)号：US20170267931A1
公开(公告)日：2017-09-21
申请号：US15424835
申请日：2017-02-04
Applicant: Proton Power, Inc.
IPC: C10C5/00
Abstract: Tools and techniques for pyroligneous acid production are provided in accordance with various embodiments. For example, a method of pyroligneous acid production is provided. The method may include: introducing a compound that includes at least carbon, oxygen, and hydrogen into a reaction chamber; heating the compound to a temperature of at least 700 degrees Celsius in the reaction chamber such that the compound reacts through a pyrolysis reaction to produce a liquid, where the liquid may include pyroligneous acid; and/or collecting the produced liquid. In some cases, the residence time of the compound may be less than 1,000 seconds. Temperatures above 1,000 degrees Celsius may be utilized in some cases. The produced liquid may be separated into an oil component and a water component that includes the pyroligneous acid. A lighter fraction may be distilled from the water component, where the lighter component includes the pyroligneous acid.
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20.发明申请公开(公告)号：US20160222299A1
公开(公告)日：2016-08-04
申请号：US15017693
申请日：2016-02-08
Applicant: Proton Power, Inc.
Inventor： Samuel C. Weaver , Daniel L. Hensley , Samuel P. Weaver , Daniel C. Weaver , Lee S. Smith
CPC classification number: C10G1/02 , B01D45/08 , B01D47/02 , B01D50/004 , B01D53/1412 , B01D53/1418 , B01D53/1425 , B01D53/1487 , B01D53/1493 , B01D2252/103 , C10B1/02 , C10B7/10 , C10B47/06 , C10B47/44 , C10B53/00 , C10B53/02 , C10G1/00 , C10G1/002 , C10G1/06 , C10G3/40 , C10G2300/1011 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10L1/04 , C10L1/06 , C10L1/08 , C10L2200/0469 , C10L2270/023 , C10L2270/026 , C10L2270/04 , C10L2290/02 , C10L2290/06 , C10L2290/08 , C10L2290/24 , C10L2290/543 , C10L2290/544 , C10L2290/547 , C10L2290/56 , Y02E50/14 , Y02P30/20 , Y02T50/678
Abstract: 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.
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