公开(公告)号：US20130000569A1

公开(公告)日：2013-01-03

申请号：US13583689

申请日：2010-03-11

Applicant: Arno Schneider ,  Ergun Cehreli

Inventor： Arno Schneider ,  Ergun Cehreli

IPC: F02B43/12 ,  F02B43/10

CPC classification number: C10K1/14 ,  C10B47/30 ,  C10J3/482 ,  C10J3/503 ,  C10J3/62 ,  C10J2200/158 ,  C10J2300/0906 ,  C10J2300/0916 ,  C10J2300/0956 ,  C10J2300/1621 ,  C10J2300/165 ,  C10J2300/1675 ,  C10J2300/1693 ,  C10J2300/1823 ,  C10J2300/1838 ,  C10J2300/1869 ,  C10J2300/1884 ,  C10J2300/1892 ,  C10K1/026 ,  C10K1/028 ,  F02B43/08 ,  Y02P20/145 ,  Y02T10/32

Abstract: The invention relates to a method and a device for producing synthesis gas and for operating an internal combustion engine therewith. The engine fuel gases can be produced from changing heterogeneous organic fuels, wherein highly tar-laden product gas and pyrolysis gas are formed. By combining and purifying these gases, the gas mixtures or the syntheses gas formed and by special operation of the gas engine, tars and pyrolysis oil produced in a high proportion are usable as an addition to the ignition oil. The synthesis gas is generated from the pyrolysis gas that is generated in a pyrolysis reactor (2) and from the product gas that results from autothermal gasification of the pyrolysis coke formed and/or of the pyrolysis oil in an atmospheric steady-state fluidisedbed gasifier (8). Then purifying the synthesis gas in a gas scrubber (16) and in an tar electrostatic filter (21), passing the synthesis gas via a compressor (22) into a separate injector (24) of a two-stroke dual-fuel engine (30), bypassing turbocharger and intercooler.

Abstract translation: 本发明涉及一种用于生产合成气并用于操作内燃机的方法和装置。 发动机燃料气体可以由改变的异质有机燃料生产，其中形成高焦油的产物气体和热解气体。 通过组合和净化这些气体，气体混合物或合成气体以及高比例生产的燃气发动机，焦油和热解油的特殊操作可用作点火油的添加剂。 合成气由在热解反应器（2）中产生的热分解气体和由大气稳态流化床气化器中形成的热解焦炭和/或热解油的自热气化产生的产物气体产生， 8）。 然后在气体洗涤器（16）和焦油静电过滤器（21）中纯化合成气，使合成气通过压缩机（22）进入二冲程双燃料发动机（30）的单独注射器（24） ），旁通涡轮增压器和中间冷却器。

公开(公告)号：US20120273175A1

公开(公告)日：2012-11-01

申请号：US13098230

申请日：2011-04-29

Applicant: Ryan Blanchard ,  Gregory Michael Laskowski

Inventor： Ryan Blanchard ,  Gregory Michael Laskowski

IPC: F28D7/00

CPC classification number: C10J3/526 ,  C10J3/485 ,  C10J3/86 ,  C10J2300/0959 ,  C10J2300/1653 ,  C10J2300/1678 ,  C10J2300/169 ,  C10J2300/1884 ,  C10K1/04 ,  F28D7/16 ,  F28D2021/0059 ,  F28F9/0263 ,  Y02E20/16 ,  Y02E20/18

Abstract: Gasification cooling systems provided herein may include a housing having a fluid passage extending in a flow direction lengthwise along the housing and an annular wall disposed about the fluid passage and having one or more annular steps. Such systems may also include a plurality of heat exchanger tubes downstream of the one or more annular steps and adapted to cool a syngas in the gas passage as the syngas flows in the flow direction.

Abstract translation: 本文提供的气化冷却系统可以包括具有沿着壳体沿纵向延伸的流体通道的壳体和围绕流体通道设置并具有一个或多个环形台阶的环形壁。 这样的系统还可以包括在一个或多个环形台阶下游的多个热交换器管，并且适于在合成气沿流动方向流动时冷却气体通道中的合成气。

公开(公告)号：US20120227442A1

公开(公告)日：2012-09-13

申请号：US13046513

申请日：2011-03-11

Applicant: Fredric Samuel Russ ,  George Frederick Frey ,  Charles Martin Mitchell ,  Paul William Plummer

Inventor： Fredric Samuel Russ ,  George Frederick Frey ,  Charles Martin Mitchell ,  Paul William Plummer

IPC: F25J3/00

CPC classification number: B01D53/1425 ,  B01D53/1456 ,  C10J3/00 ,  C10J2300/093 ,  C10J2300/1678 ,  C10J2300/1861 ,  C10J2300/1884 ,  C10K1/004 ,  C10K1/005 ,  F25J3/04084 ,  F25J3/0409 ,  F25J3/04545 ,  F25J3/04612 ,  F25J3/04769 ,  F25J2205/50 ,  F25J2215/40 ,  F25J2250/40 ,  F25J2250/42 ,  F25J2250/50 ,  Y02E20/16 ,  Y02E20/18

Abstract: The present embodiments are directed towards the cooling of a solvent of a gas treatment system using a fluid flow from an air separation unit. In one embodiment, a system is provided that includes an air separation unit. The air separation unit has an air inlet configured to receive an air flow, an oxygen outlet configured to output an oxygen flow, a nitrogen outlet configured to output a nitrogen flow and a cooling system configured to cool the air flow to enable separation of the air flow into the oxygen flow and the nitrogen flow, wherein the cooling system is configured to cool a first solvent of a first gas treatment system.

Abstract translation: 本实施例涉及使用来自空气分离单元的流体流冷却气体处理系统的溶剂。 在一个实施例中，提供了一种包括空气分离单元的系统。 空气分离单元具有被配置为接收空气流的空气入口，被配置为输出氧气流的氧气出口，被配置为输出氮气流的氮气出口和构造成冷却空气流以使空气分离的冷却系统 流入氧气流和氮气流中，其中冷却系统构造成冷却第一气体处理系统的第一溶剂。

公开(公告)号：US20120126176A1

公开(公告)日：2012-05-24

申请号：US13111832

申请日：2011-05-19

Applicant: Randy Blevins ,  Joshua B. Pearson ,  Harold A. Wright

Inventor： Randy Blevins ,  Joshua B. Pearson ,  Harold A. Wright

IPC: C01B3/02

CPC classification number: C10J3/86 ,  C10J3/50 ,  C10J2300/0906 ,  C10J2300/0909 ,  C10J2300/0916 ,  C10J2300/0976 ,  C10J2300/0986 ,  C10J2300/0989 ,  C10J2300/1246 ,  C10J2300/1659 ,  C10J2300/1687 ,  C10J2300/1693 ,  C10J2300/1853 ,  C10J2300/1884 ,  C10J2300/1892 ,  Y02P20/145 ,  Y02P30/30

Abstract: A method of producing synthesis gas by mixing a carbonaceous feed comprising at least one carbonaceous material with superheated steam to produce a reformer feedstock and reforming the reformer feedstock to produce a first synthesis gas comprising hydrogen and carbon monoxide by introducing the reformer feedstock into a plurality of coiled tubes within a reformer at a reformer temperature and a reformer pressure at which at least a portion of the reformer feedstock is converted to synthesis gas.

Abstract translation: 通过将包含至少一种含碳材料的含碳原料与过热蒸汽混合来生产合成气的方法，以产生重整器原料，并通过将重整器原料引入到多个原料中来重整重整器原料以产生包含氢气和一氧化碳的第一合成气 在转化器温度和重整器压力下，在重整器内的盘管，其中至少一部分重整器原料转化为合成气。

公开(公告)号：US20120111009A1

公开(公告)日：2012-05-10

申请号：US12939937

申请日：2010-11-04

Applicant: Judeth Brannon Corry ,  Leroy Omar Tomlinson ,  James Michael Storey ,  Paul Stephen Dimascio ,  Mark Joseph Steffen ,  Wei Chen ,  Benjamin Campbell Steinhaus ,  Richard Anthony De Puy

Inventor： Judeth Brannon Corry ,  Leroy Omar Tomlinson ,  James Michael Storey ,  Paul Stephen Dimascio ,  Mark Joseph Steffen ,  Wei Chen ,  Benjamin Campbell Steinhaus ,  Richard Anthony De Puy

IPC: F01K13/00 ,  F01K23/00 ,  F01K7/38

CPC classification number: C10J3/86 ,  C10J3/845 ,  C10J2300/1884 ,  C10J2300/1892 ,  F01K23/067 ,  F22B1/1846 ,  F28D7/0075 ,  F28D7/04 ,  F28D2021/0022 ,  F28D2021/0059 ,  F28D2021/0075 ,  Y02E20/16 ,  Y02E20/18 ,  Y02P20/13

Abstract: A system includes a syngas cooler configured to cool a syngas. The syngas cooler includes a first syngas cooler section configured to cool the syngas and a second syngas cooler section configured to cool the syngas and generate a first superheated steam with an enthalpy of less than approximately 3800 kJ/kg.

Abstract translation: 一种系统包括被配置为冷却合成气的合成气冷却器。 合成气冷却器包括构造成冷却合成气的第一合成气冷却器部分和被配置为冷却合成气并产生焓小于约3800kJ / kg的第一过热蒸汽的第二合成气冷却器部分。

公开(公告)号：US20120102834A1

公开(公告)日：2012-05-03

申请号：US12916219

申请日：2010-10-29

Applicant: Surinder Prabhjot Singh ,  Vitali V. Lissianski ,  Aaron John Avagliano ,  Wolfgang Madl

Inventor： Surinder Prabhjot Singh ,  Vitali V. Lissianski ,  Aaron John Avagliano ,  Wolfgang Madl

IPC: B01J7/00 ,  C10J3/00

CPC classification number: C10J3/20 ,  C10J3/64 ,  C10J3/66 ,  C10J2300/0909 ,  C10J2300/0916 ,  C10J2300/0959 ,  C10J2300/1823 ,  C10J2300/1846 ,  C10J2300/1869 ,  C10J2300/1884 ,  Y02P20/145

Abstract: A gasifier system which includes a reactor; a feedstock inlet; an oxidant inlet; a raw product gas outlet; and a recycle conduit, is provided. The reactor usually includes an upper section, a central section, and a lower section. The feedstock inlet is disposed in the upper section of the reactor to receive a carbonaceous feedstock. The oxidant inlet is disposed in the lower section of the reactor to receive an oxidant. The raw product gas outlet is disposed in the upper section of the reactor. The recycle conduit is configured to couple the raw product gas outlet to the lower section of the reactor, and to recycle a raw product gas from the upper section of the reactor to the lower section of the reactor. A method for converting a carbonaceous stream into a product gas in a gasifier system is also provided.

Abstract translation: 一种气化器系统，包括一个反应器; 原料入口; 氧化剂入口 原料气出口; 并提供循环管道。 反应器通常包括上部，中心部和下部。 原料入口设置在反应器的上部以容纳碳质原料。 氧化剂入口设置在反应器的下部以接收氧化剂。 原料气体出口设置在反应器的上部。 循环管道被配置成将原始产物气体出口连接到反应器的下部，并将来自反应器的上部的原始产物气体再循环到反应器的下部。 还提供了一种在气化器系统中将碳质物流转化为产物气体的方法。

公开(公告)号：US20120067060A1

公开(公告)日：2012-03-22

申请号：US13322144

申请日：2010-05-20

Applicant: Isabella Lodewina Greeff

Inventor： Isabella Lodewina Greeff

IPC: F02C6/18

CPC classification number: C01B3/36 ,  B01D53/229 ,  B01D2256/12 ,  B01D2257/102 ,  C01B13/0251 ,  C01B2203/0211 ,  C01B2203/0227 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/025 ,  C01B2203/061 ,  C01B2203/062 ,  C01B2203/0838 ,  C01B2203/1241 ,  C01B2203/84 ,  C01B2210/0046 ,  C10G2/32 ,  C10J3/00 ,  C10J2300/093 ,  C10J2300/0959 ,  C10J2300/0976 ,  C10J2300/1659 ,  C10J2300/1678 ,  C10J2300/1884 ,  F01K23/068 ,  F02C1/04 ,  F02C3/28 ,  G21D9/00 ,  Y02E20/18 ,  Y02P20/129

Abstract: A process for co-producing synthesis gas and power includes producing a synthesis gas comprising at least CO and H2 by reacting a hydrocarbonaceous feedstock with oxygen, the synthesis gas being at a first temperature, separating air from a compressed air stream by means of at least one ion transport membrane unit thereby producing a permeate stream consisting predominantly of oxygen and a reject stream of oxygen-depleted air at a second temperature which is lower than the first temperature, indirectly heating the reject stream of oxygen-depleted air with the synthesis gas and at least partially expanding, the heated reject stream of oxygen-depleted air through at least one turbine to generate power, producing an at least partially expanded reject stream of oxygen-depleted air, and feeding at least a portion of the permeate stream consisting predominantly of oxygen to the synthesis gas generation stage to provide oxygen for production of synthesis gas.

Abstract translation: 共同生产合成气和动力的方法包括通过使烃原料与氧气反应来生产至少包含CO和H 2的合成气，所述合成气处于第一温度，至少通过至少从压缩空气流中分离空气 一个离子传递膜单元，从而在低于第一温度的第二温度下产生主要由氧气和贫氧空气的排出流组成的渗透物流，间接地用合成气加热贫氧空气的废气流，以及 至少部分地膨胀经过至少一个涡轮的加热的贫氧气流，以产生动力，产生至少部分膨胀的贫氧空气的废气流，以及将至少一部分主要由 氧气到合成气生成阶段提供氧气生产合成气。

公开(公告)号：US20120020846A1

公开(公告)日：2012-01-26

申请号：US13246451

申请日：2011-09-27

Applicant: Randy BLEVINS ,  Joshua B. PEARSON ,  Harold A. WRIGHT

Inventor： Randy BLEVINS ,  Joshua B. PEARSON ,  Harold A. WRIGHT

IPC: B01J19/00

CPC classification number: C10G2/342 ,  C01B3/34 ,  C01B2203/0216 ,  C01B2203/04 ,  C01B2203/043 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/0485 ,  C01B2203/049 ,  C01B2203/062 ,  C01B2203/0811 ,  C01B2203/1276 ,  C01B2203/1294 ,  C01B2203/86 ,  C10G2/32 ,  C10G2300/1011 ,  C10G2300/701 ,  C10G2300/807 ,  C10J3/32 ,  C10J3/466 ,  C10J3/487 ,  C10J3/506 ,  C10J3/80 ,  C10J2200/06 ,  C10J2300/0906 ,  C10J2300/0909 ,  C10J2300/0916 ,  C10J2300/092 ,  C10J2300/093 ,  C10J2300/0946 ,  C10J2300/0976 ,  C10J2300/1223 ,  C10J2300/1659 ,  C10J2300/1687 ,  C10J2300/1807 ,  C10J2300/1853 ,  C10J2300/1876 ,  C10J2300/1884 ,  C10J2300/1892 ,  C10K1/003 ,  C10K1/005 ,  Y02E50/32 ,  Y02P20/129 ,  Y02P20/136 ,  Y02P20/145 ,  Y02P30/20 ,  Y02P30/30

Abstract: A system for the production of conversion products from synthesis gas, the system including a mixing apparatus configured for mixing steam with at least one carbonaceous material to produce a reformer feedstock; a reformer configured to produce, from the reformer feedstock, a reformer product comprising synthesis gas comprising hydrogen and carbon monoxide from the reformer feedstock; a synthesis gas conversion apparatus configured to catalytically convert at least a portion of the synthesis gas in the reformer product into synthesis gas conversion product and to separate from the synthesis gas conversion product a tailgas comprising at least one gas selected from the group consisting of carbon monoxide, carbon dioxide, hydrogen and methane; and one or more recycle lines fluidly connecting the synthesis gas conversion apparatus with the mixing apparatus, the reformer, or both.

Abstract translation: 一种用于从合成气生产转化产物的系统，该系统包括配置用于将蒸汽与至少一种碳质材料混合以产生重整器原料的混合装置; 配置成从重整器原料生产包含来自重整器原料的包含氢气和一氧化碳的合成气的重整产物的重整器; 合成气转化装置，其被配置为将重整产物中的至少一部分合成气催化转化为合成气转化产物，并与合成气转化产物分离出包含至少一种选自一氧化碳 ，二氧化碳，氢气和甲烷; 以及一个或多个将合成气转化装置与混合装置，重整器或两者流体连接的循环管线。

公开(公告)号：US08070863B2

公开(公告)日：2011-12-06

申请号：US12785219

申请日：2010-05-21

Applicant: Andreas Tsangaris ,  Margaret Swain

Inventor： Andreas Tsangaris ,  Margaret Swain

IPC: B01D53/02

CPC classification number: C10J3/84 ,  C10J3/00 ,  C10J3/20 ,  C10J3/463 ,  C10J3/482 ,  C10J3/723 ,  C10J3/82 ,  C10J2200/09 ,  C10J2300/0946 ,  C10J2300/0983 ,  C10J2300/1223 ,  C10J2300/1238 ,  C10J2300/1618 ,  C10J2300/1634 ,  C10J2300/165 ,  C10J2300/1671 ,  C10J2300/1681 ,  C10J2300/1693 ,  C10J2300/1884 ,  C10K1/00 ,  C10K1/002 ,  C10K1/003 ,  C10K1/004 ,  C10K1/007 ,  C10K1/02 ,  C10K1/024 ,  C10K1/101 ,  C10K1/102 ,  C10K1/12 ,  C10K1/122 ,  C10K1/14 ,  C10K1/143 ,  C10K1/16 ,  C10K1/20 ,  C10K1/26 ,  C10K1/32 ,  C10K3/008 ,  F23G5/027 ,  F23G5/085 ,  F23G2204/201 ,  F23G2209/262 ,  F23J7/00 ,  F23J2219/70 ,  Y02E20/12 ,  Y02E20/18 ,  Y02E50/32 ,  Y02P20/13

Abstract: The present invention provides a gas conditioning system for processing an input gas from a low temperature gasification system to an output gas of desired characteristics. The system comprises a two-stage process, the first stage separating heavy metals and particulate matter in a dry phase, and the second stage including further processing steps of removing acid gases, and/or other contaminants. Optional processes include adjusting the humidity and temperature of the input gas as it passes through the gas conditioning system. The presence and sequence of processing steps is determined by the composition of the input gas, the desired composition of output gas for downstream applications, and by efficiency and waste minimization.

Abstract translation: 本发明提供了一种用于处理从低温气化系统到具有所需特性的输出气体的输入气体的气体调节系统。 该系统包括两阶段工艺，第一阶段在干燥阶段分离重金属和颗粒物质，第二阶段包括除去酸性气体和/或其它污染物的进一步处理步骤。 可选的工艺包括调节输入气体通过气体调节系统时的湿度和温度。 处理步骤的存在和顺序由输入气体的组成，下游应用的输出气体的期望组成以及效率和废物最小化来确定。

公开(公告)号：US08038745B2

公开(公告)日：2011-10-18

申请号：US12102685

申请日：2008-04-14

Applicant: Stanley R. Pearson

Inventor： Stanley R. Pearson

IPC: B01J7/00 ,  B01J8/00 ,  B01J23/75

CPC classification number: B01J23/864 ,  B01J21/18 ,  B01J23/80 ,  B01J23/8892 ,  B01J37/0009 ,  B01J37/04 ,  B01J37/18 ,  C01B3/34 ,  C01B3/52 ,  C01B2203/0216 ,  C01B2203/0415 ,  C01B2203/043 ,  C01B2203/0465 ,  C01B2203/047 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/0485 ,  C01B2203/049 ,  C01B2203/061 ,  C01B2203/062 ,  C01B2203/84 ,  C07C29/1518 ,  C07C29/32 ,  C10G2/331 ,  C10G2/34 ,  C10G2/50 ,  C10J3/00 ,  C10J3/466 ,  C10J2200/156 ,  C10J2300/0906 ,  C10J2300/0909 ,  C10J2300/092 ,  C10J2300/0946 ,  C10J2300/0973 ,  C10J2300/1621 ,  C10J2300/1659 ,  C10J2300/1665 ,  C10J2300/1884 ,  C10J2300/1892 ,  C10K1/005 ,  C10K1/101 ,  C10K1/16 ,  C10K1/32 ,  Y02E50/18 ,  Y02E50/32 ,  Y02P20/145 ,  Y02P20/52 ,  C07C31/04 ,  C07C31/08

Abstract: A carbonaceous feedstock to alcohol conversion process in which carbon dioxide and a portion of the hydrogen produced are removed from the syngas stream issuing from a feedstock reformer, to yield a reduced hydrogen, carbon monoxide and methane syngas stream. The hydrogen and the carbon dioxide are passed through a Fischer Tropsch reactor which is catalyzed to favor the production of methanol. The methanol produced in the Fischer-Tropsch reactor is passed with the reduced hydrogen syngas through a second Fischer-Tropsch reactor which is catalyzed to favor the production of ethanol. Also disclosed, without limitation, are a unique catalyst, a method for controlling the content of the syngas formed in the feedstock reformer, and a feedstock handling system.

Abstract translation: 将碳酸原料转化为醇转化方法，其中从原料重整器发出的合成气流中除去产生的二氧化碳和一部分氢，得到还原的氢，一氧化碳和甲烷合成气流。 氢气和二氧化碳通过费托反应器，该反应器被催化以有利于生产甲醇。 在费 - 托反应器中生产的甲醇通过还原的氢合成气通过第二个费 - 托反应器，其被催化以有利于生产乙醇。 还公开了但不限于独特的催化剂，用于控制在原料重整器中形成的合成气的含量的方法和原料处理系统。