公开(公告)号：US20180131022A1

公开(公告)日：2018-05-10

申请号：US15626337

申请日：2017-06-19

Applicant: Proton Power, Inc.

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

IPC: H01M8/06 ,  C10J3/72 ,  C10J3/10

CPC classification number: H01M8/06 ,  C10J3/10 ,  C10J3/723 ,  C10J2300/0906 ,  C10J2300/092 ,  C10J2300/0973 ,  C10J2300/1646

Abstract: Methods are disclosed for extracting hydrogen from a biomass compound comprising carbon, oxygen, and hydrogen. The biomass may include cellulose, lignin, and/or hemicellulose. 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.

公开(公告)号：US20180057760A1

公开(公告)日：2018-03-01

申请号：US15251494

申请日：2016-08-30

Applicant: ThermoChem Recovery International, Inc.

Inventor： Ravi CHANDRAN ,  Daniel A. BURCIAGA ,  Daniel Michael LEO ,  Shawn Robert FREITAS ,  Dave G. NEWPORT ,  Justin Kevin MILLER ,  Kaitlin Emily HARRINGTON ,  Brian Christopher ATTWOOD ,  Emily Jane SCHULTHEIS ,  Kelly Ann KISHTON

IPC: C10J3/12 ,  C01B3/02 ,  C10J3/10 ,  C10J3/24 ,  C10J3/32 ,  C10J3/72 ,  C10J3/84 ,  C10G5/06 ,  C10G1/04 ,  C10L1/04 ,  F02B43/08

CPC classification number: C10J3/12 ,  C01B2203/0405 ,  C01B2203/0475 ,  C01B2203/061 ,  C01B2203/062 ,  C01B2203/146 ,  C10G1/045 ,  C10G2/32 ,  C10G5/06 ,  C10G2300/1003 ,  C10G2300/205 ,  C10G2400/04 ,  C10G2400/08 ,  C10J3/10 ,  C10J3/24 ,  C10J3/32 ,  C10J3/721 ,  C10J3/723 ,  C10J3/845 ,  C10J2200/09 ,  C10J2200/15 ,  C10J2200/154 ,  C10J2200/36 ,  C10J2300/0903 ,  C10J2300/094 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0969 ,  C10J2300/0993 ,  C10J2300/1246 ,  C10J2300/1606 ,  C10J2300/1637 ,  C10J2300/165 ,  C10J2300/1656 ,  C10J2300/1659 ,  C10J2300/1846 ,  C10J2300/1853 ,  C10L1/04 ,  C10L5/46 ,  C10L2270/026 ,  C10L2270/04 ,  C10L2290/02 ,  C10L2290/04 ,  C10L2290/06 ,  C10L2290/08 ,  C10L2290/145 ,  C10L2290/148 ,  C10L2290/24 ,  C10L2290/42 ,  C10L2290/54 ,  C10L2290/58 ,  F02B43/08 ,  Y02E20/16 ,  Y02E50/10 ,  Y02E50/30 ,  Y02E50/32 ,  Y02T10/32

Abstract: A feedstock delivery system transfers a carbonaceous material, such as municipal solid waste, into a product gas generation system. The feedstock delivery system includes a splitter for splitting bulk carbonaceous material into a plurality of carbonaceous material streams. Each stream is processed using a weighing system for gauging the quantity of carbonaceous material, a densification system for forming plugs of carbonaceous material, a de-densification system for breaking up the plugs of carbonaceous material, and a gas and carbonaceous material mixing system for forming a carbonaceous material and gas mixture. A pressure of the mixing gas is reduced prior to mixing with the carbonaceous material, and the carbonaceous material to gas weight ratio is monitored. A transport assembly conveys the carbonaceous material and gas mixture to a first reactor where at least the carbonaceous material within the mixture is subject to thermochemical reactions to form the product gas.

公开(公告)号：US6048374A

公开(公告)日：2000-04-11

申请号：US912485

申请日：1997-08-18

Applicant: Alex E. S. Green

Inventor： Alex E. S. Green

IPC: C10B7/10 ,  C10B53/00 ,  C10B53/02 ,  C10B53/07 ,  C10J3/10 ,  C10J3/00

CPC classification number: C10B53/00 ,  C10B53/02 ,  C10B53/07 ,  C10B7/10 ,  C10J3/10 ,  C10J2200/158 ,  C10J2300/0916 ,  C10J2300/1246 ,  C10J2300/1675 ,  C10J2300/1869 ,  Y02E50/14 ,  Y02P20/129 ,  Y02P20/133 ,  Y02P20/143

Abstract: The subject invention pertains to unique and advantageous systems for gasifying and/or liquefying biomass. The systems of the subject invention utilize a unique design whereby heat from a combustion chamber is used to directly gasify or liquefy biomass. In a preferred embodiment, the biomass is moved through a reactor tube in which all the gasification and/or liquefaction takes place. Preferably, char exits the biomass reactor tube and enters the combustion chamber where the char serves as fuel for combustion. The combustion chamber partially surrounds the reactor tube and is in direct thermal contact with the reactor tube such that heat from the combustion chamber passes through the reactor wall and directly heats the biomass within the reactor tube.

Abstract translation: 本发明涉及用于气化和/或液化生物质的独特且有利的系统。 本发明的系统利用独特的设计，从而使用来自燃烧室的热直接气化或液化生物质。 在优选的实施方案中，将生物质移动通过其中发生所有气化和/或液化的反应器管。 优选地，炭离开生物质反应器管并进入燃烧室，其中焦炭用作燃烧燃料。 燃烧室部分地围绕反应器管并且与反应器管直接热接触，使得来自燃烧室的热量通过反应器壁并直接加热反应器管内的生物质。

公开(公告)号：US4881947A

公开(公告)日：1989-11-21

申请号：US212519

申请日：1988-06-28

Applicant: Thomas H. Parker ,  Virgil J. Flanigan

Inventor： Thomas H. Parker ,  Virgil J. Flanigan

IPC: C10B1/10 ,  C10J3/06 ,  C10J3/10

CPC classification number: C10B1/10 ,  C10J3/005 ,  C10J3/06 ,  C10J3/10 ,  C10K1/024 ,  C10K3/04 ,  C10J2200/158 ,  C10J2300/1246 ,  C10J2300/1621 ,  C10J2300/1807 ,  C10J2300/1823

Abstract: A high efficiency gasifier employs a rotary kiln having an indirect fired gasifier and a recycle system. The rotary kiln provides an essentially oxygen-free gasifying chamber into which raw feed material is introduced. Radiant tubes within the chamber transfer heat to the incoming raw feed material to pyrolyze it and convert it to char and product gas as the material advances toward the outlet end. The recycle system within the chamber returns both product gas and hot char to a receiving end of the kiln to aid in heat transfer to the raw feed material. The feed is thus heated more rapidly, and less heat input is required. Efficiency is further aided by providing additional residence time and gasification of the char.

Abstract translation: 高效气化器采用具有间接燃烧气化器和循环系统的回转窑。 回转窑提供基本上无氧的气化室，其中引入原料。 室内的辐射管将热量转移到输入的原料进料中以将其热解并随着材料向出口端前进而将其转化成炭和产物气体。 室内的再循环系统将产品气和热炭都送回到窑的接收端，以帮助热量传递到原料。 因此，进料被更快地加热，并且需要较少的热量输入。 通过提供额外的焦炭停留时间和气化来进一步提高效率。

公开(公告)号：US3647379A

公开(公告)日：1972-03-07

申请号：US3647379D

申请日：1969-08-22

Applicant: RHEINISCHE BRAUNKOHLEWERKE AG

Inventor： WENZEL WERNER ,  SCHENCK HERMANN

IPC: C10J3/08 ,  C10J3/10 ,  C10J3/00 ,  C10J3/46

CPC classification number: C10J3/10 ,  C10J3/08 ,  C10J3/57 ,  C10J3/76 ,  C10J2200/154 ,  C10J2300/0909 ,  C10J2300/0946 ,  C10J2300/0973

Abstract: For gasifying coal, a coal-water mixture is pumped in the form of a viscous mass into a treating chamber where the mixture is heated, causing, in immediately successive steps and in said chamber, first, dehydration of the mixture by vaporizing its water content, second, gasification thereof and, third, endothermic reaction of the products precedingly obtained by the heat treatment.

Abstract translation: 对于气化煤，将煤 - 水混合物以粘性物质的形式泵送到加热混合物的处理室中，在立即连续的步骤中并在所述室中首先通过蒸发其含水量使混合物脱水 ，第二，其气化，以及第三，通过热处理获得的产物的吸热反应。

公开(公告)号：US2619415A

公开(公告)日：1952-11-25

申请号：US69081846

申请日：1946-08-15

Applicant: STANDARD OIL DEV CO

Inventor： HEMMINGER CHARLES E

IPC: B01J8/18 ,  C10B49/22 ,  C10J3/10

CPC classification number: C10J3/10 ,  B01J8/1836 ,  B01J2208/00088 ,  B01J2208/00132 ,  B01J2208/00141 ,  B01J2208/00495 ,  B01J2208/0053 ,  C10B49/22 ,  C10J3/482 ,  C10J2300/1246 ,  C10J2300/1807 ,  C10K1/026 ,  Y10S48/04

公开(公告)号：US09698439B2

公开(公告)日：2017-07-04

申请号：US12758355

申请日：2010-04-12

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

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

IPC: H01M8/06 ,  C10J3/10 ,  C10J3/72

CPC classification number: H01M8/06 ,  C10J3/10 ,  C10J3/723 ,  C10J2300/0906 ,  C10J2300/092 ,  C10J2300/0973 ,  C10J2300/1646

Abstract: Methods are disclosed for extracting hydrogen from a biomass compound comprising carbon, oxygen, and hydrogen. The biomass may include cellulose, lignin, and/or hemicellulose. 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.

公开(公告)号：US09458397B2

公开(公告)日：2016-10-04

申请号：US12996792

申请日：2009-06-11

Applicant: Rolf Ljunggren

Inventor： Rolf Ljunggren

IPC: C10J3/20 ,  C10J3/10 ,  C10J3/58

CPC classification number: C10J3/20 ,  C10J3/10 ,  C10J3/58 ,  C10J2300/0916 ,  C10J2300/093 ,  C10J2300/094 ,  C10J2300/0946 ,  C10J2300/0973 ,  C10J2300/1223 ,  C10J2300/1246 ,  C10J2300/1261 ,  C10J2300/1269 ,  C10J2300/1861 ,  C10J2300/1884 ,  Y02E50/30 ,  Y02P20/145

Abstract: A method and equipment for producing synthesis gas (S) from solid carbon particles (C), the carbon particles (C) being obtained by pyrolysis, gasification of the carbon particles (C) occurs by indirect heating of the carbon particles (C) in the presence of a process gas (P) in the same space where the carbon particles (C) are present, and the synthesis gas (S) generated during the gasification is discharged from the space. The method is characterised in that the carbon particles (C) and the process gas (P) are located in a reactor (1), and the indirect heating occurs by way of radiant heat from burners (Br1-Brn) located in the reactor (1).

Abstract translation: 用于从固体碳颗粒（C）生产合成气（S）的方法和设备，通过热解获得的碳颗粒（C），碳颗粒（C）的气化通过间接加热碳颗粒（C）在 在存在碳颗粒（C）的相同空间中存在处理气体（P）和在气化过程中产生的合成气体（S）从该空间排出。 该方法的特征在于，碳颗粒（C）和工艺气体（P）位于反应器（1）中，间接加热通过位于反应器中的来自燃烧器（Br1-Brn）的辐射热 1）。

公开(公告)号：US09388348B2

公开(公告)日：2016-07-12

申请号：US14431872

申请日：2013-10-09

Applicant: MITSUBISHI HEAVY INDUSTRIES, LTD.

Inventor： Katsuhiko Yokohama ,  Osamu Shinada ,  Masashi Kitada

IPC: C10L3/10 ,  C10J3/76 ,  F01K23/10 ,  C10J3/84 ,  C10J3/10 ,  C10J3/48 ,  C10J3/50 ,  F01K23/06

CPC classification number: C10J3/10 ,  C10J3/485 ,  C10J3/506 ,  C10J3/76 ,  C10J3/84 ,  C10J2200/152 ,  C10J2200/156 ,  C10J2300/0906 ,  C10J2300/093 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0976 ,  C10J2300/1653 ,  C10J2300/1678 ,  C10J2300/1876 ,  C10L3/10 ,  F01K23/067 ,  F01K23/10 ,  Y02E20/16 ,  Y02E20/18

Abstract: A gasification apparatus that is capable of appropriately controlling a differential pressure variation between the interior of a pressure vessel and the interior of a gasification furnace, and of simplifying a structure, by providing: a pressure vessel which forms a hollow shape; a gasification furnace which forms a hollow shape, and which is positioned inside the pressure vessel with a space section therebetween; a heat exchanger positioned at the upper section of the gasification furnace; a gas nozzle which supplies seal gas to the lower section of the space section; a char-receiving section provided above the heat exchanger in the space section; a pressure equalizer of which one end communicates with the interior of the gasification furnace, and the other end opens into the char-receiving section; and a gas flow channel which passes vertically through a side section of the char-receiving section.

Abstract translation: 一种气化装置，其能够适当地控制压力容器的内部与气化炉的内部之间的压力差异，并且简化了结构，其特征在于，提供：形成中空形状的压力容器; 气化炉，其形成中空形状，并且位于压力容器内部，其间具有空间部分; 位于气化炉上段的热交换器; 气体喷嘴，其向所述空间部的下部供给密封气体; 设置在所述空间部中的所述热交换器的上方的炭吸收部; 一个压力平衡器，其一端与气化炉的内部连通，另一端通向焦炭接收部分; 以及气体流路，其垂直地穿过所述炭吸收部分的侧部。

公开(公告)号：US08969647B2

公开(公告)日：2015-03-03

申请号：US13384436

申请日：2010-07-07

Applicant: Giacomo Fernando Rispoli ,  Felicia Massetti ,  Michelangelo D'Abbieri ,  Medardo Pinti ,  Maria Ilaria Pistelli

Inventor： Giacomo Fernando Rispoli ,  Felicia Massetti ,  Michelangelo D'Abbieri ,  Medardo Pinti ,  Maria Ilaria Pistelli

IPC: A62D3/20 ,  C01B3/36 ,  B01J7/00 ,  C10J3/10 ,  C10J3/00 ,  C10J3/14 ,  C10J3/20 ,  C10J3/80

CPC classification number: C10J3/10 ,  C10J3/005 ,  C10J3/14 ,  C10J3/20 ,  C10J3/80 ,  C10J2300/0909 ,  C10J2300/0926 ,  C10J2300/0989 ,  C10J2300/1606 ,  Y02P20/145

Abstract: A continuous process for the thermal treatment of a refinery sludge, comprising the following operations: a. drying of the refinery sludge, possibly mixed with pet-coke, at a temperature ranging from 110 to 120° C.; b. gasification of the dried sludge, at a temperature ranging from 750 to 950° C., for a time of 30 to 60 minutes, in the presence of a gas containing oxygen and water vapour, with the associated production of synthesis gas (CO+H2) and a solid residue; c. combustion of the synthesis gas at a temperature ranging from 850 to 1,200° C. and recycling of the combustion products for the drying and gasification phases; and d. inertization of the solid residue, at a temperature ranging from 1,300 to 1,500° C., by vitrification with plasma torches.

Abstract translation: 炼油厂污泥热处理的连续工艺，包括以下操作：a。 在110至120℃的温度范围内干燥可能与宠物焦炭混合的炼油厂污泥; b。 在含有氧气和水蒸汽的气体存在下，在750〜950℃的温度范围内，将干燥的污泥气化30〜60分钟，伴随生产合成气（CO + H2 ）和固体残渣; C。 在850〜1200℃的温度下对合成气进行燃烧，再循环用于干燥和气化阶段的燃烧产物; 和d。 通过用等离子炬玻璃化，在1300至1500℃的温度下使固体残余物惰性化。