公开(公告)号：US20150307784A1

公开(公告)日：2015-10-29

申请号：US14638959

申请日：2015-03-04

Applicant: Proton Power, Inc.

Inventor： Samuel C. Weaver ,  Daniel L. Hensley ,  Samuel P. Weaver ,  Daniel C. Weaver

IPC: C10B53/02 ,  C11B1/12 ,  C10B57/00 ,  C10L1/02

CPC classification number: C10B53/02 ,  C10B47/00 ,  C10B49/02 ,  C10B57/005 ,  C10B57/02 ,  C10G49/007 ,  C10G2300/1011 ,  C10G2300/4037 ,  C10G2300/42 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10K3/06 ,  C10L1/02 ,  C10L1/04 ,  C10L2200/0469 ,  C10L2270/023 ,  C10L2270/026 ,  C10L2270/04 ,  C10L2290/02 ,  C10L2290/08 ,  C11B1/12 ,  Y02E50/14 ,  Y02E50/32 ,  Y02P30/20 ,  Y02T50/678

Abstract: Methods, systems, and devices for continuous fuel production are provided. Some embodiments may utilize two pyrolysis platforms, which may utilize biomass as a feedstock. One platform may generally utilize a high temperature pyrolysis process that may generate at least hydrogen and carbon monoxide. This high temperature gas stream may be fed into a lower temperature fast pyrolysis stream as a cover gas. The hot cover gas may react with the fast pyrolysis vapors hydrotreating while the vapors may still be hot and the molecules may still be small. The reacted product may then be distilled on the cool down. This may provide a rapid continuous process for the production of liquid fuels from biomass or other compounds that include carbon-oxygen-hydrogen (C—O—H) compounds.

Abstract translation: 提供了连续燃料生产的方法，系统和设备。 一些实施方案可以利用可利用生物质作为原料的两个热解平台。 一个平台通常可以利用可产生至少氢和一氧化碳的高温热解过程。 这种高温气流可以作为覆盖气体进料到较低温度的快速热解流中。 热覆盖气体可以与快速热解蒸气加氢处理反应，同时蒸气仍然是热的，并且分子可能仍然很小。 然后将反应的产物在冷却下蒸馏。 这可以提供用于从生物质或包括碳 - 氧 - 氢（C-O-H）化合物的其它化合物生产液体燃料的快速连续方法。

公开(公告)号：US20150252275A1

公开(公告)日：2015-09-10

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: C10L1/04 ,  C10B7/10 ,  C10B1/02

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.

公开(公告)号：US20150252268A1

公开(公告)日：2015-09-10

申请号：US14593411

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 ,  C10G1/06 ,  B01D53/14 ,  C10L1/04

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.

公开(公告)号：US20140059921A1

公开(公告)日：2014-03-06

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

IPC: C10G1/00

CPC classification number: C10G1/002 ,  C10G3/50 ,  C10G2300/1014 ,  C10L1/08 ,  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.

Abstract translation: 提供了从生物质连续生产液体燃料的方法，系统和装置。 一些实施方案利用热化学方法与热化学方法平行地生产生物油以产生富氢合成气。 两种产物流可以进料到第三反应室中，其可以例如在连续生产过程中用氢气富集生物油。 一个产品流可以包括诸如柴油的液体燃料。 一些实施例还可以产生其他产品流，包括但不限于发电和/或生物炭。