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31. 发明授权

US07988754B1 Process for producing clean liquid fuels from coal waste 失效
标题翻译：从废煤中生产清洁液体燃料的工艺
公开(公告)号：US07988754B1
公开(公告)日：2011-08-02
申请号：US11969336
申请日：2008-01-04
申请人： John W. Rich, Jr.
发明人： John W. Rich, Jr.
IPC分类号： C10K3/06 , C10J3/16 , C10J3/46
CPC分类号： C10G2/32 , C10J3/466 , C10J3/506 , C10J3/86 , C10J2300/0903 , C10J2300/093 , C10J2300/0943 , C10J2300/0959 , C10J2300/0973 , C10J2300/0993 , C10J2300/1634 , C10J2300/1659 , C10J2300/1678 , C10K1/004 , C10K1/026
摘要： The present invention is directed to a process for producing ultra clean liquid fuel from abandoned mine waste. A feedstock is prepared from water and coal mine waste having relatively high ash (non-carbonaceous matter) content. Foundry slag is added to the feedstock as a fluxant to adjust the melting behavior of the ash in the feedstock. Preferably, the fluxant is blast furnace slag provided in a particle size of less than about 150 μm and is provided in an amount sufficient to lower the melting point of the ash in the feedstock by at least about 200° F. The feedstock is admitted with a flow of oxygen into a pressurized chamber of an entrained flow gasifier in which the feedstock and oxygen are heated to produce a synthetic gas from a coal component of the feedstock and molten slag from the ash and fluxant components of the feedstock. The molten slag is of a viscosity to freely flow out of the gasifier through an exit port in the bottom of the gasifier. The synthetic gas can be used to produce paraffin from which ultra clean liquid fuel can be produced.
摘要翻译：本发明涉及从废弃矿山废料生产超清洁液体燃料的方法。从具有相对高的灰分（非碳质物质）含量的水和煤矿废料制备原料。将铸造渣作为助剂添加到原料中，以调节原料中灰分的熔融行为。优选地，助熔剂是提供的粒度小于约150μm的高炉矿渣，其用量足以将原料中灰分的熔点降至至少约200°F。原料被允许用氧气流入夹带流气化器的加压室中，其中原料和氧被加热以从原料的煤组分和来自原料的灰分和助熔剂组分的熔融渣中产生合成气。熔渣具有通过气化器底部的出口自由流出气化器的粘度。合成气可用于生产可以生产超清洁液体燃料的石蜡。

32. 发明申请

US20110142721A1 FUEL GASIFICATION EQUIPMENT 审中-公开
标题翻译：燃油气化设备
公开(公告)号：US20110142721A1
公开(公告)日：2011-06-16
申请号：US13059007
申请日：2008-08-20
申请人： Takahiro Murakami , Satoko Aoki , Toshiyuki Suda , Hidehisa Tani
发明人： Takahiro Murakami , Satoko Aoki , Toshiyuki Suda , Hidehisa Tani
IPC分类号： B01J8/18
CPC分类号： F23C10/22 , C10G2/30 , C10J3/463 , C10J2300/0976 , C10J2300/0993 , C10J2300/1637 , C10J2300/1659 , C10J2300/1668 , C10J2300/1678 , C10J2300/1807 , C10J2300/1815 , C10K1/005 , C10K1/026 , C10K3/005 , F23C10/10 , Y02E50/32
摘要： Provided is a fuel gasification equipment capable of effectively utilizing a CO2 gas finally separated from a product or combustible gas such as H2 and CO for supply of a solid fuel to a gasification furnace, enabling stable supply of the solid fuel to the gasification furnace. The equipment has CO2 gas separation/circulation means for separating CO2 gas from the gasification gas produced in the gasification furnace 2 and introducing the separated CO2 gas to a supply system supplying the solid fuel to the gasification furnace 2.
摘要翻译：提供一种燃料气化设备，其能够有效地利用最终从产物或诸如H2和CO的可燃气体分离的CO 2气体，以向固化燃料炉供应固体燃料，从而能够将固体燃料稳定地供应到气化炉。该设备具有用于从气化炉2中产生的气化气体中分离CO 2气体并将分离出的CO 2气体引入到向气化炉2供应固体燃料的供给系统的CO 2气体分离/循环装置。

33. 发明申请

US20110135556A1 METHOD AND DEVICE FOR PRODUCING ENERGY, DME (DIMETHYL ETHER) AND BIO-SILICA USING CO2-NEUTRAL BIOGENIC REACTIVE AND INERT INGREDIENTS 审中-公开
标题翻译：用于生产能量的方法和装置，使用二氧化碳中和生物反应和成分的二甲醚（二甲醚）和二氧化硅
公开(公告)号：US20110135556A1
公开(公告)日：2011-06-09
申请号：US13057282
申请日：2009-08-03
申请人： Oliver Neumann , Peter Mehrling
发明人： Oliver Neumann , Peter Mehrling
IPC分类号： C01B33/20 , C07C41/01 , C10J3/46 , B01J8/18 , C01B33/12
CPC分类号： C10J3/721 , C07C29/1518 , C07C41/09 , C10G2300/1011 , C10J3/482 , C10J3/523 , C10J3/56 , C10J3/66 , C10J2300/0916 , C10J2300/094 , C10J2300/0959 , C10J2300/0973 , C10J2300/1261 , C10J2300/16 , C10J2300/165 , C10J2300/1665 , C10J2300/1671 , C10J2300/1838 , C10J2300/1853 , C10K1/024 , C10K1/026 , C10K1/16 , Y02E50/18 , Y02E50/32 , Y02P30/20 , C07C43/043 , C07C31/04
摘要： Processes and facilities for the production of biological synthesis gases and/or a synthetic propellant, in particular DME (dimethyl ether), and/or biological silica using biogenic input materials and comprising the following steps: Allothermal gasification of the biogenic input material by means of impulse burners for the integrated generation of process heat in a fluidized bed gasifier Gasification of inert pyrolytic coke from the first gasification step in a second gasification step preferably operated in parallel according to the principle of the expanded or circulating fluidized bed using oxygen/steam as gasification agents Combination of at least part of the gasification products from the two gasifiers for common processing
摘要翻译：用于生产生物合成气体和/或合成推进剂，特别是DME（二甲醚）的生物二氧化硅和/或使用生物来源输入材料的生物二氧化硅的方法和设备，包括以下步骤：通过以下步骤将生物来源的物质进行热热气化用于在流化床气化器中综合生成工艺热的脉冲燃烧器在第二气化步骤中从第一气化步骤气化惰性热解焦炭优选根据膨胀或循环流化床原理使用氧气/蒸汽作为气化进行平行操作代理商组合来自两个气化器的气化产物的至少一部分用于共同加工

34. 发明申请

US20110120139A1 MODIFIED GAS AND STEAM TURBINE PROCESS WITH INTEGRATED COAL GASIFICATION UNDER PRESSURE 有权
标题翻译：压力下整体煤气化改造气体和蒸汽涡轮机
公开(公告)号：US20110120139A1
公开(公告)日：2011-05-26
申请号：US12737032
申请日：2009-05-15
申请人： Ralf Abraham , Domenico Pavone
发明人： Ralf Abraham , Domenico Pavone
IPC分类号： F02C6/04 , H02K7/18 , F01K23/08 , F02C7/22
CPC分类号： C10J3/52 , C01B3/32 , C01B2203/0244 , C01B2203/025 , C01B2203/04 , C01B2203/042 , C01B2203/0465 , C01B2203/147 , C01B2203/84 , C10J2300/1606 , C10J2300/165 , C10J2300/1653 , C10J2300/1675 , C10K1/026 , C10K1/32 , F02C3/28 , F02C6/18 , Y02E20/16 , Y02E20/18 , Y02E50/11
摘要： A process for the production, treatment and combustion of synthesis gas for the purpose of generating electric power is disclosed. The synthesis gas is produced from a solid, carbon-containing fuel with the aid of an oxygen-containing gas and treated by a slag-separating device and a device separating alkalis. Subsequently, the synthesis gas produced is fed to an expansion turbine where the pressure energy is used for generating power. On account of the treatment and separation of alkalis the expansion turbine is protected from corrosion and mechanical impact. The expanded synthesis gas is then burnt under pressure and the combustion is used in a combined-cycle process using a gas turbine, steam generator and steam turbine for generating power. The process thus has an increased efficiency. Apparatus for use of the process is also described.
摘要翻译：公开了用于产生电力的合成气的生产，处理和燃烧的方法。合成气借助于含氧气体由固体含碳燃料产生，并通过炉渣分离装置和分离碱的装置进行处理。随后，将产生的合成气供给到膨胀涡轮机，其中压力能用于发电。由于碱的处理和分离，膨胀涡轮机被保护免受腐蚀和机械冲击。膨胀的合成气然后在压力下燃烧，并且燃烧在使用燃气轮机，蒸汽发生器和用于发电的蒸汽轮机的联合循环过程中使用。因此，该方法具有提高的效率。还描述了使用该方法的装置。

35. 发明申请

US20110088320A1 METHOD AND APPARATUS TO PRODUCE SYNTHESIS GAS VIA FLASH PYROLYSIS AND GASIFICATION IN A MOLTEN LIQUID 有权
标题翻译：生产合成气的方法和装置通过液体中的闪蒸和气化
公开(公告)号：US20110088320A1
公开(公告)日：2011-04-21
申请号：US12964036
申请日：2010-12-09
申请人： Mark A. Dietenberger , Mark H. Anderson
发明人： Mark A. Dietenberger , Mark H. Anderson
IPC分类号： C10J3/48 , C10J3/46
CPC分类号： C10J3/57 , C10J3/463 , C10J3/66 , C10J2300/0909 , C10J2300/0916 , C10J2300/092 , C10J2300/0946 , C10J2300/0973 , C10J2300/0989 , C10J2300/1659 , C10J2300/1823 , C10K1/026 , Y02E20/18 , Y02E50/32 , Y02P20/145
摘要： Disclosed are a method and a corresponding apparatus for converting a biomass reactant into synthesis gas. The method includes the steps of (1) heating biomass in a first molten liquid bath at a first temperature, wherein the first temperature is at least about 100° C., but less than the decomposition temperature of the biomass, wherein gas comprising water is evaporated and air is pressed from the biomass, thereby yielding dried biomass with minimal air content. (2) Recapturing the moisture evaporated from the biomass in step 1 for use in the process gas. (3) Heating the dried biomass in a second molten liquid bath at a second temperature, wherein the second temperature is sufficiently high to cause flash pyrolysis of the dried biomass, thereby yielding product gases, tar, and char. (4) Inserting recaptured steam into the process gas, which may optionally include external natural gas or hydrogen gas or recycled syngas for mixing and reforming with tar and non-condensable gases. (5) Further reacting the product gases, tar, and char with the process gas within a third molten liquid bath at a third temperature which is equal to or greater than the second temperature within the second molten liquid bath, thereby yielding high quality and relatively clean synthesis gas after a relatively long residence time needed for char gasification. A portion of the synthesis gas so formed is combusted to heat the first, second, and third molten liquid baths, unless external natural or hydrogen gas is available for this use.
摘要翻译：公开了一种用于将生物质反应物转化成合成气的方法和相应的装置。该方法包括以下步骤：（1）在第一温度下在第一熔融液浴中加热生物质，其中第一温度为至少约100℃，但小于生物质的分解温度，其中包含水的气体为蒸发并从生物质中压制空气，从而产生具有最小空气含量的干燥生物质。（2）在步骤1中回收从生物质蒸发的水分，用于工艺气体。（3）在第二温度下在第二熔融液体浴中加热干燥的生物质，其中第二温度足够高以引起干燥的生物质的快速热解，从而产生产物气体，焦油和焦炭。（4）将再吸收的蒸汽插入工艺气体中，其可任选地包括外部天然气或氢气或再循环的合成气，用于与焦油和不可冷凝气体混合和重整。（5）使产物气体，焦油和焦炭与第三熔融液槽内的处理气体在第二熔融液浴中的第三温度等于或大于第二温度的第三温度下反应，从而产生高品质和相对的洁净的合成气在焦化气化所需的较长停留时间后。如此形成的合成气的一部分被燃烧以加热第一，第二和第三熔融液体浴，除非可用于该用途的外部天然或氢气。

36. 发明申请

US20110036013A1 REMOVAL OF LIQUID ASH AND ALKALIS FROM SYNTHESIS GAS 审中-公开
标题翻译：从合成气中去除液体ASH和碱
公开(公告)号：US20110036013A1
公开(公告)日：2011-02-17
申请号：US12735205
申请日：2008-12-22
申请人： Domenico Pavone , Michael Rieger , Ralf Abraham
发明人： Domenico Pavone , Michael Rieger , Ralf Abraham
IPC分类号： C10J3/72 , C07C1/02 , B01J19/00 , F02C3/20 , H02K7/18
CPC分类号： C10J3/46 , C01B3/36 , C01B3/382 , C01B3/56 , C01B2203/0244 , C01B2203/025 , C01B2203/042 , C01B2203/0465 , C01B2203/84 , C10J2300/0983 , C10J2300/0993 , C10K1/026 , C10K1/20
摘要： A process for the production of synthesis gas by gasification with the aid of air or oxygen or oxygen-saturated air as well as water vapor, a solid or liquid carbon-bearing fuel material being fed to a reactor, is shown. The fuel material is converted with the aid of air or oxygen or oxygen-saturated air and water vapor at an elevated temperature into a synthesis gas essentially consisting of hydrogen, carbon dioxide and carbon monoxide; the reaction also yields mineral slag droplets which are removed from the reactor separately from the synthesis gas obtained, and the synthesis gas being discharged from the reactor in any random direction desired; the vaporous alkalis contained in the synthesis gas come into contact with a getter ceramic material so that they separate from the synthesis gas and hence, the synthesis gas can be sent to a slag separation device without previous cooling step and the slag droplets being withdrawn from the said device as liquid slag.
摘要翻译：借助于空气或氧气或氧饱和空气以及水蒸汽，固体或液体含碳燃料材料供给到反应器来生产合成气的方法。借助空气或氧气或氧气饱和的空气和水蒸汽在升高的温度下将燃料转化为基本上由氢气，二氧化碳和一氧化碳组成的合成气; 该反应还产生与所获得的合成气体分离地从反应器中除去的矿渣液滴，并且合成气以任何所需的随机方向从反应器排出; 包含在合成气中的气态碱与吸气剂陶瓷材料接触，使得它们与合成气体分离，因此，可以将合成气送到渣分离装置，而无需先前的冷却步骤，并且渣液从所述装置为液体渣。

37. 发明申请

US20100224835A1 Production of synthesis gas through controlled oxidation of biomass 有权
标题翻译：通过生物质的受控氧化生产合成气
公开(公告)号：US20100224835A1
公开(公告)日：2010-09-09
申请号：US12653564
申请日：2009-12-16
申请人： Esteban Chornet , Boris Valsecchi , Sébastien Rheault , Martin Gagnon
发明人： Esteban Chornet , Boris Valsecchi , Sébastien Rheault , Martin Gagnon
IPC分类号： C01B3/02
CPC分类号： C10J3/463 , C10J3/16 , C10J3/66 , C10J2300/0916 , C10J2300/092 , C10J2300/0923 , C10J2300/0946 , C10J2300/0956 , C10J2300/0959 , C10J2300/0976 , C10J2300/0996 , C10J2300/1603 , C10J2300/1615 , C10J2300/169 , C10J2300/1838 , C10J2300/1884 , C10J2300/1892 , C10K1/003 , C10K1/004 , C10K1/026 , C10K1/101 , C10K1/12 , C10K3/005 , C10K3/006 , Y02E50/32 , Y02P20/145
摘要： A process for producing synthesis gas from biomass in which biomass is contacted with oxygen and steam, wherein the oxygen is present in an amount effective to oxidize the biomass partially and to heat the biomass to a temperature of at least 500° C. and no greater than 750° C. At least a portion of the partially oxidized biomass then is treated with oxygen and steam to heat the biomass to a temperature of at least 800° C., thereby producing a synthesis gas, which then is recovered.
摘要翻译：一种从生物质生产与氧气和蒸汽接触的生物质生产合成气的方法，其中氧气以有效氧化生物质部分的方式存在，并将生物质加热到至少500℃和不大于然后用氧气和蒸汽处理至少一部分部分氧化的生物质，以将生物质加热到至少800℃的温度，从而产生合成气，然后将其回收。

38. 发明授权

US07740672B2 Method and apparatus for a coal gasifier 有权
标题翻译：煤气化炉的方法和装置
公开(公告)号：US07740672B2
公开(公告)日：2010-06-22
申请号：US12140430
申请日：2008-06-17
申请人： Kenneth M. Sprouse
发明人： Kenneth M. Sprouse
IPC分类号： C10J3/68
CPC分类号： C10J3/721 , C10J3/54 , C10J3/78 , C10J2200/09 , C10J2200/15 , C10J2300/093 , C10J2300/0943 , C10J2300/0956 , C10J2300/0959 , C10J2300/0969 , C10J2300/0973 , C10J2300/1634 , C10J2300/1687 , C10J2300/1807 , C10J2300/1838 , C10J2300/1846 , C10J2300/1884 , C10J2300/1892 , C10K1/026 , C10K1/101
摘要： A method and apparatus for efficiently forming a gaseous material from a solid starting material. The produced gaseous material includes a CGE HHV having a high percentage of an original HHV of the starting material. The gaseous product may be used to form a plurality of materials for various purposes.
摘要翻译：一种用于从固体起始材料有效地形成气态材料的方法和装置。产生的气态材料包括具有起始材料的原始HHV的高百分比的CGE HHV。气态产物可以用于形成用于各种目的的多种材料。

39. 发明申请

US20090064581A1 PLASMA-ASSISTED WASTE GASIFICATION SYSTEM 有权
标题翻译：等离子体辅助废气加气系统
公开(公告)号：US20090064581A1
公开(公告)日：2009-03-12
申请号：US12209011
申请日：2008-09-11
申请人： Matthew Christian Nielsen , Richard Anthony DePuy , Aditya Kumar , James Patrick Francis Lyons , Vitali Lissianski , Ruijie Shi , Surinder Prabhjot Singh , Kenneth Brakeley Welles , Vladimir Zamansky
发明人： Matthew Christian Nielsen , Richard Anthony DePuy , Aditya Kumar , James Patrick Francis Lyons , Vitali Lissianski , Ruijie Shi , Surinder Prabhjot Singh , Kenneth Brakeley Welles , Vladimir Zamansky
IPC分类号： C10J3/18 , C10J3/56
CPC分类号： C10J3/86 , C10J3/18 , C10J3/20 , C10J3/84 , C10J2200/158 , C10J2300/0903 , C10J2300/0946 , C10J2300/0956 , C10J2300/0959 , C10J2300/0969 , C10J2300/0973 , C10J2300/1238 , C10J2300/1671 , C10J2300/169 , C10J2300/1884 , C10K1/026 , C10K1/04 , C10K1/101 , Y02E20/16
摘要： A plasma-assisted waste gasification system and process for converting waste stream reaction residues into a clean synthesis gas (syngas) is disclosed. The feedstock is fed into a reactor roughly one-third from the bottom through the use of a feed mechanism. The reactor has three zones; a bottom zone where melting occurs, a middle zone where gasification takes place, and a top zone with integrated plasma torches to control the temperature and polish the syngas. The residence times in the three zones are selected to optimize the syngas composition and melted products. The syngas leaves the reactor and is partially quenched with relatively cooler synthesis gas. The partially quenched syngas is further cooled to recover heat for steam generation and/or preheating the waste stream to the reactor. The cold syngas is then processed to remove pollutants. The clean synthesis gas is combusted in power generation equipment to generate electricity, or converted to other fuels by chemical processes.
摘要翻译：公开了一种等离子体辅助废气处理系统和将废物流反应残余物转化为清洁合成气（合成气）的方法。原料通过使用进料机构从底部进料到反应器的大约三分之一。反应堆有三个区域; 发生熔化的底部区域，发生气化的中间区域以及具有集成等离子体炬的顶部区域以控制温度和抛光合成气。选择三个区域中的停留时间以优化合成气组合物和熔融产物。合成气离开反应器，并用较冷的合成气进行部分淬火。将部分淬灭的合成气进一步冷却以回收热量用于产生蒸汽和/或将废物流预热到反应器。然后处理冷合成气以除去污染物。清洁的合成气在发电设备中燃烧以发电，或通过化学过程转化为其他燃料。

40. 发明申请

US20080307703A1 METHOD AND APPARATUS TO PROTECT SYNTHESIS GAS VIA FLASH PYROLYSIS AND GASIFICATION IN A MOLTEN LIQUID 有权
标题翻译：生产合成气的方法和装置通过液体中的闪蒸和气化
公开(公告)号：US20080307703A1
公开(公告)日：2008-12-18
申请号：US12108747
申请日：2008-04-24
申请人： Mark A. Dietenberger , Mark H. Anderson
发明人： Mark A. Dietenberger , Mark H. Anderson
IPC分类号： C10J3/68 , C10J3/00
CPC分类号： C10J3/57 , C10J3/463 , C10J3/66 , C10J2300/0909 , C10J2300/0916 , C10J2300/092 , C10J2300/0946 , C10J2300/0973 , C10J2300/0989 , C10J2300/1659 , C10J2300/1823 , C10K1/026 , Y02E20/18 , Y02E50/32 , Y02P20/145
摘要： Disclosed are a method and a corresponding apparatus for converting a biomass reactant into synthesis gas. The method includes the steps of (1) heating biomass in a first molten liquid bath at a first temperature, wherein the first temperature is at least about 100° C., but less than the decomposition temperature of the biomass, wherein gas comprising water is evaporated and air is pressed from the biomass, thereby yielding dried biomass with minimal air content. (2) Recapturing the moisture evaporated from the biomass in step 1 for use in the process gas. (3) Heating the dried biomass in a second molten liquid bath at a second temperature, wherein the second temperature is sufficiently high to cause flash pyrolysis of the dried biomass, thereby yielding product gases, tar, and char. (4) Inserting recaptured steam into the process gas, which may optionally include external natural gas or hydrogen gas or recycled syngas for mixing and reforming with tar and non-condensable gases. (5) Further reacting the product gases, tar, and char with the process gas within a third molten liquid bath at a third temperature which is equal to or greater than the second temperature within the second molten liquid bath, thereby yielding high quality and relatively clean synthesis gas after a relatively long residence time needed for char gasification. A portion of the synthesis gas so formed is combusted to heat the first, second, and third molten liquid baths, unless external natural or hydrogen gas is available for this use.
摘要翻译：公开了一种用于将生物质反应物转化成合成气的方法和相应的装置。该方法包括以下步骤：（1）在第一温度下在第一熔融液浴中加热生物质，其中第一温度为至少约100℃，但小于生物质的分解温度，其中包含水的气体为蒸发并从生物质中压制空气，从而产生具有最小空气含量的干燥生物质。（2）在步骤1中回收从生物质蒸发的水分，用于工艺气体。（3）在第二温度下在第二熔融液体浴中加热干燥的生物质，其中第二温度足够高以引起干燥的生物质的快速热解，从而产生产物气体，焦油和焦炭。（4）将再吸收的蒸汽插入工艺气体中，其可任选地包括外部天然气或氢气或再循环的合成气，用于与焦油和不可冷凝气体混合和重整。（5）使产物气体，焦油和焦炭与第三熔融液槽内的处理气体在第二熔融液浴中的第三温度等于或大于第二温度的第三温度下反应，从而产生高品质和相对的洁净的合成气在焦化气化所需的较长停留时间后。如此形成的合成气的一部分被燃烧以加热第一，第二和第三熔融液体浴，除非可用于该用途的外部天然或氢气。

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