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公开(公告)号：US20120186783A1
公开(公告)日：2012-07-26
申请号：US13203230
申请日：2010-02-24
IPC分类号： F28D15/00
CPC分类号： F22B1/165 , C10J3/86 , C10J2300/1238 , C10J2300/1884 , F23J15/06 , F28D21/0001 , Y02E20/363 , Y02P20/124
摘要： Heat is reclaimed from a high temperature gasifier exhaust gas of between 250° C. and 20000C. A first duct receives the exhaust gas, and outputs it at a reduced temperature. A second duct receives a heat transfer fluid and outputs it at an elevated temperature. A heat transfer arrangement conducts heat extracted from the product gas to the heat transfer fluid (steam), thereby elevating the temperature of the heat transfer fluid. A heat pipe formed of sodium, potassium, rubidium, or lithium, has a first end for communicating with the high temperature exhaust gas and a second end for communicating with the heat transfer fluid. The heat pipe has an envelope formed of a selectable combination of stainless steel, Inconel, nickel, molybdenum, tungsten, niobium, carbon, carbon composite, and Hastelloy X, and a safety valve that ensures safe operation. An adiabatic zone is interposed between the first and second ducts.
摘要翻译： 从250°C到200°C的高温气化炉排气回收热量。 第一管道接收废气，并在降低的温度下输出。 第二管道接收传热流体并在升高的温度下输出。 传热装置将从产物气体提取的热量传导到传热流体（蒸汽），从而提高传热流体的温度。 由钠，钾，铷或锂形成的热管具有与高温废气连通的第一端和用于与传热流体连通的第二端。 热管具有由不锈钢，铬镍铁合金，镍，钼，钨，铌，碳，碳复合材料和Hastelloy X的可选择组合形成的外壳，以及确保安全操作的安全阀。 在第一和第二管道之间插入绝热区域。
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2.发明申请Renewable Blended Natural Gas and Rock Wool Production from a Plasma-Based System 审中-公开基于等离子体系统的可再生混合天然气和岩棉生产公开(公告)号：US20130326952A1
公开(公告)日：2013-12-12
申请号：US13825122
申请日：2011-09-19
IPC分类号： C10K3/06
CPC分类号： C10K3/06 , B09B3/00 , B09B3/005 , C03B5/025 , C10J3/18 , C10J3/723 , C10J2200/12 , C10J2300/0906 , C10J2300/0946 , C10J2300/0976 , C10J2300/0996 , C10J2300/1238 , C10J2300/1618 , C10J2300/1621 , C10K1/06 , C10L3/003 , C10L3/10 , Y02P20/133 , Y02W30/20
摘要： A method and system for cost effectively converting a feedstock using thermal plasma or other styles of gassifiers, into an energy transfer medium using a blended gaseous fuel. The feedstock can be any organic material or inorganic combination to generate a syngas. The syngas is blended with any fuel of a higher thermal content (BTU) than the syngas. The resulting blended high thermal content fuel is used on site or reinjected into the fuel supply pipe line. Rock wool and accessory heat are produced to increase the efficiency of the plant.
摘要翻译： 一种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成使用混合气体燃料的能量转移介质的方法和系统。 原料可以是任何有机材料或无机组合以产生合成气。 合成气与任何比合成气高的热含量（BTU）的燃料混合。 所得到的混合高热量燃料现场使用或重新注入燃料供应管线。 产生岩棉和附加热量以提高工厂的效率。
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3.发明申请RENEWABLE BLENDED NATURAL GAS AND ROCK WOOL PRODUCTION FROM A PLASMA-BASED SYSTEM 审中-公开可重复混合的天然气和基于等离子体系统的岩棉生产公开(公告)号：US20130323132A1
公开(公告)日：2013-12-05
申请号：US13825123
申请日：2011-09-19
IPC分类号： H05H1/26
CPC分类号： H05H1/26 , C10J3/18 , C10J2200/12 , C10J2300/0906 , C10J2300/0946 , C10J2300/0989 , C10J2300/0993 , C10J2300/0996 , C10J2300/1238 , C10J2300/1823
摘要： A method and system for augmenting the heat energy of a plasma torch in a gassifier using chemical energy, including the steps of injecting a fuel in the proximity of a plasma torch inside the gassifier chamber; and injecting an oxidant in the proximity of a plasma torch inside the gassifier chamber. As apparatus, an enhanced plasma gassifier arrangement is of the type that has a gassifier chamber having an electrically operated plasma torch for issuing a plasma discharge into the gassifier chamber. A fuel injection arrangement is disposed to surround the electrically operated plasma torch for injecting a fuel and an oxidant into the gassifier chamber. A natural gas inlet delivers natural gas into the gassifier chamber, thereby enhancing the temperature within the gassifier chamber.
摘要翻译： 一种用于使用化学能增加放气器中的等离子体焰炬的热能的方法和系统，包括以下步骤：在所述放气室内的等离子体焰炬附近注入燃料; 以及在所述放气室内的等离子体焰炬附近注入氧化剂。 作为设备，增强的等离子体放气装置是具有放电室的类型，其具有用于将等离子体放电发射到放气室中的电操作的等离子体焰炬。 燃料喷射装置设置成围绕用于将燃料和氧化剂喷射到放气室中的电操作等离子体焰炬。 天然气入口将天然气输送到放气室中，从而提高放气室内的温度。
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公开(公告)号：US20120189500A1
公开(公告)日：2012-07-26
申请号：US13320404
申请日：2010-05-11
CPC分类号： B01D53/864 , B01D53/002 , B01D53/62 , B01D53/75 , B01D53/84 , B01D2255/20761 , B01D2255/2092 , B01D2256/16 , B01D2256/20 , B01D2256/22 , B01D2256/24 , B01D2257/70 , B01D2259/818 , C01B3/342 , C01B3/36 , C01B3/56 , C01B2203/043 , C01B2203/047 , C01B2203/86 , C07C29/1518 , Y02A50/2358 , Y02C10/04 , Y02P20/152 , Y02P30/30 , C07C31/04
摘要： A system for treating an exhaust stream issued by a power plant processes the exhaust stream in a methanol reactor. The exhaust stream contains CO and/or CO2, and can be a full stack or a partial stack exhaust stream. The methanol reactor is a pellet style of methanol reactor, and can be a foam or an alpha alumina oxide foam reactor. A plasma chamber generates H2 for reacting in the methanol reactor. A portion of the exhaust stream issued by the power plant is consumed in the plasma chamber. An algae reactor converts sequestered CO2 to O2. The algae is exposed to the exhaust stream to extract nutrients therefrom and thereby augment growth of the algae. The plasma chamber receives at a high temperature region thereof CO that is reduced to its elemental state. Cooling of the exhaust stream and precipitates the methanol to be re-burned as a fuel.
摘要翻译： 用于处理由发电厂发出的废气流的系统处理甲醇反应器中的废气流。 废气流包含CO和/或CO 2，并且可以是全堆垛或部分堆垛排气流。 甲醇反应器是甲醇反应器的颗粒形式，可以是泡沫或α氧化铝泡沫反应器。 等离子体室产生H2以在甲醇反应器中反应。 由发电厂发出的排气流的一部分在等离子体室中消耗。 藻类反应器将隔离的二氧化碳转化为氧气。 藻类暴露于废气流中以从中提取营养物质，从而增加藻类的生长。 等离子体室在其高温区域接收CO，其被还原成其基本状态。 冷却排气流并将甲醇沉淀成燃料再燃烧。
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公开(公告)号：US20120232173A1
公开(公告)日：2012-09-13
申请号：US13382155
申请日：2010-07-02
CPC分类号： C10L1/04 , C01B3/12 , C01B3/48 , C01B3/50 , C01B3/52 , C01B3/56 , C01B2203/0233 , C01B2203/0283 , C01B2203/04 , C01B2203/0415 , C01B2203/043 , C01B2203/047 , C01B2203/0475 , C01B2203/062 , C01B2203/0827 , C01B2203/1241 , C01B2203/1258 , C01B2203/146 , C01B2203/148 , C01B2203/86 , C10G2/30 , C10G2300/1003 , C10G2300/1014 , C10G2300/4043 , C10G2300/405 , C10G2300/807 , C10J3/18 , C10J2300/0916 , C10J2300/0946 , C10J2300/0969 , C10J2300/1238 , C10J2300/16 , C10J2300/1659 , C10J2300/1665 , C10J2300/1668 , C10J2300/1681 , C10J2300/1815 , C10K1/005 , C10K3/04 , Y02E50/18 , Y02E50/32 , Y02P20/145 , Y02P30/20 , Y02P30/30 , Y02P30/446
摘要： A system for producing a high hydrogen to carbon ratio fuel centered approximately around C9 treats an exhaust stream from a manufacturing plant processes. The exhaust stream is processed in a Fischer Tropsch reactor, and contains CO and/or CO2, which is sequestered, and can be a full stack exhaust stream. The Fischer Tropsch reactor is a pellet style reactor, a foam reactor, or an alpha alumina oxide foam reactor. A plasma chamber generates H2 for reacting in the Fischer Tropsch reactor. A portion of the exhaust stream is consumed in the plasma chamber. An algae reactor converts sequestered CO2 to O2. The algae is exposed to the exhaust stream to extract nutrients therefrom and augment its growth. The plasma chamber receives at a high temperature region thereof CO or CO2 that is reduced to its elemental state. The product stream and fuel are condensed and separated, and re-burned as fuel.
摘要翻译： 用于生产中心大约C9左右的高氢碳比燃料的系统处理来自制造工厂工艺的废气流。 废气流在费托反应器中进行处理，并且包含被隔离的CO和/或CO 2，并且可以是完整的堆排气流。 费 - 托反应器是颗粒式反应器，泡沫反应器或α氧化铝泡沫反应器。 等离子体室产生H2以在费托反应器中反应。 排气流的一部分在等离子体室中消耗。 藻类反应器将隔离的二氧化碳转化为氧气。 藻类暴露于废气流中以从中提取营养物质并增加其生长。 等离子体室在其高温区域接收CO或CO 2，其被还原成其元素状态。 产品流和燃料被冷凝和分离，并作为燃料再燃烧。
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公开(公告)号：US20120193925A1
公开(公告)日：2012-08-02
申请号：US13203227
申请日：2010-02-24
IPC分类号： H02K7/18
摘要： A system for generating electrical power employs a reactor for producing a product gas in response to the consumption of a feedstock. A heat reclamation arrangement employs a sodium heat pipe that communicates with the product gas the spent steam to extract heat from the product gas and thereby form heated steam. Heated steam is delivered to a turbine that has an input for receiving the heated steam, an outlet for exhausting spent steam, and a rotatory output. An electrical generator is coupled to the rotatory output of the turbine for producing the electrical energy. A recirculating system returns the spent steam to the heat reclamation arrangement. The fuel provided to the reactor may be any combination of coal, municipal solid waste, biomass, or a non-fossil fuel. Additives serve to neutralize the acid or base content of the product gas. A secondary power generation facility receives the product gas and produces additional electrical power.
摘要翻译： 用于产生电力的系统响应于原料的消耗而使用用于产生产物气体的反应器。 热回收装置采用钠热管，其与产品气体连通废蒸汽以从产物气体中提取热量，从而形成加热的蒸汽。 加热蒸汽被输送到具有用于接收加热的蒸汽的输入的涡轮机，用于排出废蒸汽的出口和旋转输出。 发电机耦合到涡轮的旋转输出以产生电能。 循环系统将废蒸汽返回到热回收装置。 提供给反应器的燃料可以是煤，城市固体废物，生物质或非化石燃料的任何组合。 添加剂用于中和产物气体的酸或碱含量。 二次发电设备接收产品气并产生额外的电力。
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