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公开(公告)号：EP4271734A1
公开(公告)日：2023-11-08
申请号：EP22734832.3
申请日：2022-01-04
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公开(公告)号：EP4001379A1
公开(公告)日：2022-05-25
申请号：EP20208567.6
申请日：2020-11-19
申请人： iGas energy GmbH
发明人： Lentz, Karl-Heinz
摘要： Gegenstand der Erfindung ist ein Hybridkraftwerk zur autarken Energieversorgung von Gebäuden, insbesondere Wohngebäuden 15 und Industrieanlagen. Das Hybridkraftwerk ist zur lokalen Energieversorgung vorzugsweise in der Nähe der zu versorgenden Gebäude und Industrieanlagen angeordnet. Das Hybridkraftwerk umfasst mindestens eine Anlage zur Erzeugung von Strom aus erneuerbarer Energiequelle und eine Power-to-X Vorrichtung zur thermochemische Umwandlung von Biomasse in andere Energieträger 3. Zur Überbrückung von Licht- und Dunkelflauten umfasst das Hybridkraftwerk ein oder mehrere Energiespeicher. Die Energieversorgung der Gebäude bzw. Industrieanlagen durch das Hybridkraftwerk ist klima- und CO 2 -neutral.
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公开(公告)号：EP3710126A1
公开(公告)日：2020-09-23
申请号：EP18877730.4
申请日：2018-11-16
申请人： Rasirc, Inc.
发明人： BLETHEN, Richard D. , SPIEGELMAN, Jeffrey J. , HOLMES, Russell J. , ALVAREZ, Daniel, Jr. , YANG, Jian , SPEED, Ericca, Lynne
IPC分类号： B01D5/00 , B01F3/02 , C10J1/08 , C23C16/442 , H01L21/306 , H01L21/54 , H01L23/20
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公开(公告)号：EP2118458B1
公开(公告)日：2018-01-17
申请号：EP08714647.8
申请日：2008-02-19
申请人： Westport Power Inc.
IPC分类号： F01N3/08 , C01B3/02 , C10J1/20 , C10K3/00 , F01N3/00 , F02M25/12 , F01N3/20 , F02D41/02 , F02N3/02
CPC分类号： F02M25/12 , C01B3/36 , C01B2203/0211 , C01B2203/0255 , F01N3/0253 , F01N3/0842 , F01N3/0871 , F01N3/206 , F01N3/2073 , F01N2240/30 , F02B1/12 , F02B3/06 , F02D41/0235 , F02D41/027
摘要： A method of operating a syngas generator within a desired temperature range, despite a need for intermittent syngas output, involves switching between operating the syngas generator in a rich mode and a lean mode. Operation of the syngas generator in both the rich mode and the lean mode sustains the operating temperature of the syngas generator within that desired temperature range, particularly for non-catalytic reactors. The method of switching from the lean mode to the rich mode of operation can include decreasing the oxygen-to-carbon ratio of reactants supplied to the syngas generator. The flow rate of one or more of the reactant streams supplied to the syngas generator can be actively controlled in order to switch operation of the syngas generator between the rich and lean modes.
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公开(公告)号：EP2389444A4
公开(公告)日：2016-09-21
申请号：EP10733750
申请日：2010-01-08
申请人： XYLECO INC
发明人： MEDOFF MARSHALL , MASTERMAN THOMAS
CPC分类号： C12P7/10 , C10J2300/1612 , C10J2300/1665 , C10J2300/1681 , C12P7/04 , C12P7/065 , C12P7/14 , C12P7/40 , C12P7/46 , C12P7/54 , C12P7/56 , C12P7/62 , C13K1/02 , C13K1/06 , Y02E50/17 , Y02T50/678
摘要： Carbon-containing materials, such as biomass (e.g., plant biomass, animal biomass, and municipal waste biomass) or coal are processed to produce useful products, such as fuels, carboxylic acids and equivalents thereof (e.g., esters and salts). For example, systems are described that can use feedstock materials, such as cellulosic and/or lignocellulosic materials and/or starchy materials, to produce ethanol, butanol or organic acids (e.g., acetic or lactic acid), salts of organic acids or mixtures thereof. If desired, organic acids can be converted into alcohols, such as by first converting the acid, salt or mixtures of the acid and its salt to an ester, and then hydrogenating the formed ester. Acetogens or homoacetogens which are capable of utilizing a syngas from a thermochemical conversion of coal or biomass can be utilized to produce the desired product.
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6.发明公开HYBRID FIXED-KINETIC BED GASIFIER FOR FUEL FLEXIBLE GASIFICATION 审中-公开FIXED混合KINETIKBETT碳水化合物FOR灵活燃料气化
公开(公告)号：EP2970772A1
公开(公告)日：2016-01-20
申请号：EP14765373.7
申请日：2014-03-17
申请人： All Power Labs, Inc.
发明人： MASON, James
CPC分类号： C10J3/485 , C01B3/02 , C10J3/466 , C10J3/48 , C10J3/66 , C10J2200/152 , C10J2300/0906 , C10J2300/0909 , C10J2300/0916 , C10J2300/1861 , C10J2300/1884 , Y02P20/129 , Y02P20/145
摘要： A gasification system including: a casing defining: a solid material inlet; a fixed bed drying zone proximal the solid material inlet; a fixed bed pyrolysis zone arranged below the drying zone along a gravity vector, distal the solid material inlet across the pyrolysis zone; a kinetic bed combustion zone surrounded by the pyrolysis zone; and a kinetic channel extending through the drying zone and pyrolysis zone and fluidly connected to the combustion zone, the kinetic channel defining a kinetic bed reduction zone fluidly isolated from and thermally connected to the pyrolysis zone and the drying zone by the kinetic channel.
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7.发明公开
公开(公告)号：EP2619288A4
公开(公告)日：2014-07-16
申请号：EP11827082
申请日：2011-09-19
IPC分类号： C10J1/26 , B01D53/10 , C10J3/18 , C10J3/84 , C10J3/86 , F02C3/20 , F23G5/00 , F23G5/46 , F23J15/00
CPC分类号： F02C3/20 , B01D53/10 , B01D2257/2045 , B01D2257/302 , B01D2257/404 , B01D2257/602 , B01D2258/0283 , C10J3/18 , C10J3/84 , C10J2200/12 , C10J2300/0946 , C10J2300/0996 , C10J2300/1238 , C10J2300/1606 , C10J2300/1653 , C10J2300/1869 , C10J2300/1876 , F02C6/18 , F02C9/20 , F05D2220/32 , F05D2220/72 , F22B1/18 , F22B37/008 , F23G5/006 , F23G5/46 , F23G2201/303 , F23G2201/40 , F23G2201/701 , F23G2201/80 , F23G2202/106 , F23G2204/201 , F23G2206/202 , F23G2206/203 , F23J15/006 , F23J15/025 , F23J2215/10 , F23J2215/20 , F23J2217/104 , F23J2219/60 , Y02E20/12 , Y02E20/16 , Y02E20/18 , Y02P20/129 , Y02P20/133
摘要： A method and system for cost effectively converting a feedstock using thermal plasma, or other styles of gassifiers, into to a feedwater energy transfer system. The feedstock can be any organic material, or fossil fuel. The energy transferred in the feedwater is converted into steam which is then injected into the low turbine of a combined cycle power plant. Heat is extracted from gas product issued by a gassifier and delivered to a power plant via its feedwater system. The gassifier is a plasma gassifier and the gas product is syngas. In a further embodiment, prior to performing the step of extracting heat energy, there is provided the further step of combusting the syngas in an afterburner. An air flow, and/or EGR flow is provided to the afterburner at a rate that is varied in response to an operating characteristic of the afterburner. The air flow to the afterburner is heated.
摘要翻译： 一种用于使用热等离子体或其他类型的放气器将原料成本有效地转化为给水能量转移系统的方法和系统。 原料可以是任何有机材料或化石燃料。 在给水中转移的能量被转化为蒸汽，然后将其注入到联合循环发电厂的低涡轮机中。 热气从放气器发出的气体产品中提取，并通过其给水系统输送到发电厂。 放气器是等离子体放气器，气体产物是合成气。 在另一个实施方案中，在进行提取热能的步骤之前，提供了在加力燃烧器中燃烧合成气的另外的步骤。 以加速器的操作特性变化的速率将空气流和/或EGR流提供给后燃器。 加热到加力燃烧器的空气流。
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公开(公告)号：EP1861478B1
公开(公告)日：2012-02-22
申请号：EP06738735.7
申请日：2006-03-16
申请人： Fuelcor LLC
CPC分类号： C10G2/32 , C10G2/30 , C10G2300/1022 , C10J3/18 , C10J2300/093 , C10J2300/1238 , C10J2300/1659 , C25B1/04 , C25B15/08 , Y02E60/364 , Y02E60/366 , Y02E70/10 , Y02P20/128 , Y02P20/129 , Y02P20/133
摘要： A process and system for producing hydrocarbon compounds or fuels that recycle products of hydrocarbon compound combustion-carbon dioxide or carbon monoxide, or both, and water. The energy for recycling is electricity derived from preferably not fossil based fuels, like from nuclear fuels or from renewable energy. The process comprises electrolyzing water, and then using hydrogen to reduce externally supplied carbon dioxide to carbon monoxide, then using so produced carbon monoxide together with any externally supplied carbon monoxide and hydrogen in Fischer-Tropsch reactors, with upstream upgrading to desired specification fuels-for example, gasoline, jet fuel, kerosene, diesel fuel, and others. Energy released in some of these processes is used by other processes. Using adiabatic temperature changes and isothermal pressure changes for gas processing and separation, large amounts of required energy are internally recycled using electric and heat distribution lines. Phase conversion of working fluid is used in heat distribution lines for increased energy efficiency. The resulting use of electric energy is less than 1.4 times the amount of the high heating value of combustion of so produced hydrocarbon compounds when carbon dioxide is converted to carbon monoxide in the invention, and less than 0.84 when carbon monoxide is the source.
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公开(公告)号：EP2417226A2
公开(公告)日：2012-02-15
申请号：EP10762299.5
申请日：2010-04-06
申请人： Rentech, Inc.
发明人： CARRYER, Benjamin, H. , ELROD, Eric, R. , IBSEN, Mark, D. , WRIGHT, Harold, A. , JOHNSON, Brian, K.
CPC分类号： C01B3/36 , B01J23/745 , C01B13/0259 , C01B2203/0261 , C01B2203/062 , C01B2203/0894 , C01B2203/1241 , C01B2203/1247 , C10G2/332 , C10G2300/1011 , C10J2300/0909 , C10J2300/0916 , C10J2300/0959 , C10J2300/1618 , C10J2300/1659 , C10J2300/1884 , Y02P20/145 , Y02P20/52 , Y02P30/20
摘要： A thermal conversion process comprising: pyrolizing or gasifying a carbonaceous feedstock to produce a first synthesis gas having a first H2:CO ratio of less than a minimum value or greater than a maximum value; providing enriched oxygen; and subjecting the first synthesis gas to partial oxidation in the presence of at least a portion of the enriched oxygen to produce a conditioned synthesis gas having a desired ratio of H2:CO in the range of from the minimum value to the maximum value. A method of producing FT product liquids by providing a conditioned synthesis gas according to the process and producing FT product liquids by subjecting the conditioned synthesis gas to FT reaction under FT operating conditions. A system for carrying out the methods is also provided.
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公开(公告)号：EP1789168A4
公开(公告)日：2011-04-13
申请号：EP05794209
申请日：2005-09-02
CPC分类号： E04C3/28 , E04B2001/2418 , E04B2001/2451 , E04B2001/2454 , E04C2003/043 , E04C2003/0439 , E04C2003/0452 , E04C2003/0465 , E04H5/12 , F28F25/00 , Y02P20/129 , Y10S261/11
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