专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明申请

US20120061618A1 Plasma gasification reactors with modified carbon beds and reduced coke requirements 审中-公开
标题翻译：具有改性碳床的等离子体气化反应器和焦炭需求降低
公开(公告)号：US20120061618A1
公开(公告)日：2012-03-15
申请号：US13199814
申请日：2011-09-09
申请人： James Santoianni , Pieter VanNierop , Michael Erskine Heier , Aleksandr Gorodetsky , Stephanie Reese , Kent Olis Hicks
发明人： James Santoianni , Pieter VanNierop , Michael Erskine Heier , Aleksandr Gorodetsky , Stephanie Reese , Kent Olis Hicks
IPC分类号： C01B3/24 , C22B5/00 , C22B1/00 , B01J19/08 , B28B1/14
CPC分类号： C04B14/022 , C04B7/02 , C04B12/04 , C04B28/04 , C04B35/62204 , C04B2111/00474 , C10B53/08 , C10J3/02 , C10J3/18 , C10J3/20 , C10J3/34 , C10J3/72 , C10J3/82 , C10J2200/06 , C10J2200/15 , C10J2300/092 , C10J2300/094 , C10J2300/0946 , C10J2300/0956 , C10J2300/0959 , C10J2300/0983 , C10J2300/0993 , C10J2300/0996 , C10J2300/1238 , Y02W30/92 , C04B14/06 , C04B14/104 , C04B14/28 , C04B14/303 , C04B14/34 , C04B18/08
摘要： A carbonaceous bed in a reactor includes carbon bearing material that is not coke and rather includes natural wood blocks or bricks formed of non-coke carbonaceous material in a binder along with, as options, other constituents such as catalysts and fluxing agents. The bed reduces the amount of coke required in processes such as for syngas production. Such non-coke units are applicable to an original carbonaceous bed in a reactor and also to replenishment of reacted carbon in the original bed. The bed may include ungasified carbon particulate matter separated from gaseous reaction products of a gasification reactor, either in non-coke bricks or otherwise applied, as may other carbonaceous material often regarded as waste such as spent potliner material from aluminum making and soot residue from a gasification reactor. Certain reactor structural modifications can also result in reduced consumption of carbon in a bed.
摘要翻译：反应器中的含碳床包括不是焦炭的碳承载材料，而是包括粘合剂中由非焦炭碳质材料形成的天然木块或砖，以及其它成分如催化剂和助熔剂。该床减少了合成气生产过程中所需的焦炭量。这样的非焦炭单元适用于反应器中的原始碳质床，并且还可以补充原始床中反应的碳。床可以包括与气化反应器的气态反应产物分离的非气化碳颗粒物质，无论是在非焦炭砖中，还是以其他方式施加，其他碳质材料通常被认为是废物，例如来自铝制造的废弃废料，以及来自气化反应器。某些反应器结构改性也可导致床中碳的消耗降低。

2. 发明申请

US20100199560A1 Plasma gasification reactor 有权
公开(公告)号：US20100199560A1
公开(公告)日：2010-08-12
申请号：US12378184
申请日：2009-02-11
申请人： Shyam V. Dighe , Mark F. Darr , Ivan A. Martorell , Pieter van Nierop , Aleksandr Gorodetsky , Richard Dale Bower
发明人： Shyam V. Dighe , Mark F. Darr , Ivan A. Martorell , Pieter van Nierop , Aleksandr Gorodetsky , Richard Dale Bower
IPC分类号： C10J3/30
CPC分类号： C10J3/18 , C10J2200/152 , C10J2300/0916 , C10J2300/093 , C10J2300/0946 , C10J2300/1238
摘要： A plasma gasification reactor vessel having a top section with a conical wall extending up from a bottom section, containing a carbonaceous bed into which plasma is injected by plasma torches, to a roof of the vessel is arranged in ways that can contribute to characteristics of gas flow and solids residence time that are favorable for thoroughness of reactions and yield of useful reactions products. In some cases, such a conical wall is combined in arrangements with other features such as one or more feed ports arranged to give more uniform distribution including examples with a feed port that has a distributive feed mechanism. The roof of the vessel, in some examples, has vertical outlet ports that include intrusions into the interior volume of the reactor proximate the conical wall of the top section. The configurations of outlet ports with intrusions and the configurations of feed ports for more uniform distribution of feed material are also applicable to reactor vessels with other geometries.

3. 发明申请

US20100199557A1 Plasma gasification reactor 审中-公开
公开(公告)号：US20100199557A1
公开(公告)日：2010-08-12
申请号：US12378167
申请日：2009-02-11
申请人： Shyam V. Dighe , Mark F. Darr , Ivan A. Martorell , Pieter van Nierop , Aleksandr Gorodetsky , Richard Dale Bower
发明人： Shyam V. Dighe , Mark F. Darr , Ivan A. Martorell , Pieter van Nierop , Aleksandr Gorodetsky , Richard Dale Bower
IPC分类号： C10J3/18
CPC分类号： C10J3/18 , C10J2200/09 , C10J2200/152 , C10J2300/0916 , C10J2300/093 , C10J2300/0946 , C10J2300/1238
摘要： A plasma gasification reactor vessel having a top section with a conical wall extending up from a bottom section, containing a carbonaceous bed into which plasma is injected by plasma torches, to a roof of the vessel is arranged in ways that can contribute to characteristics of gas flow and solids residence time that are favorable for thoroughness of reactions and yield of useful reactions products. In some cases, such a conical wall is combined in arrangements with other features such as one or more feed ports arranged to give more uniform distribution including examples with a feed port that has a distributive feed mechanism. The roof of the vessel, in some examples, has vertical outlet ports that include intrusions into the interior volume of the reactor proximate the conical wall of the top section. The configurations of outlet ports with intrusions and the configurations of feed ports for more uniform distribution of feed material are also applicable to reactor vessels with other geometries.

4. 发明授权

US07632394B2 System and process for upgrading heavy hydrocarbons 有权
标题翻译：升级重质烃的系统和工艺
公开(公告)号：US07632394B2
公开(公告)日：2009-12-15
申请号：US11807436
申请日：2007-05-29
申请人： Shyam V. Dighe , Mark Anthony Montemurro , Richard Dale Bower , Aleksandr Gorodetsky , Mark F. Darr , Ivan A. Martorell
发明人： Shyam V. Dighe , Mark Anthony Montemurro , Richard Dale Bower , Aleksandr Gorodetsky , Mark F. Darr , Ivan A. Martorell
IPC分类号： C10G51/02
CPC分类号： C10G15/12 , C10G2/40 , C10G45/26 , C10G47/22 , F23G7/05 , F23G2201/40 , F23G2204/201 , F23G2900/7013 , Y02E50/32
摘要： A system and process for upgrading hydrocarbons such as heavy oils includes high temperature plasma reactor apparatus, in one or more vessels, into which the oils are introduced along with water, such as steam, to produce lighter hydrocarbon fractions, along with carbon monoxide and hydrogen, that flows to an additional stage where more hydrocarbons and water are introduced for further fractionating reactions facilitated by reaction of carbon monoxide and water to produce carbon dioxide and nascent, or prompt, free radicals of hydrogen. Heavy hydrocarbons upgraded can include heavy oils in the form of tar sands, oil shale, and oil residuals. The vessel or vessels can each contain a carbonaceous bed facilitating the described reactions and example embodiments include one vessel with the reactions performed in a single bed and, also, two vessels with the reactions performed in a carbonaceous bed portion in each vessel.
摘要翻译：用于升级烃类如重油的系统和方法包括在一个或多个容器中的高温等离子体反应器装置，油与水一起引入其中，例如蒸汽，以产生较轻的烃馏分以及一氧化碳和氢气，其流入另外的阶段，其中引入更多的碳氢化合物和水以进一步分馏反应，由一氧化碳和水的反应促进，从而产生二氧化碳和新生的氢或快速的氢自由基。重质烃升级可包括焦油砂，油页岩和油残留物形式的重油。容器或容器可各自含有促进所述反应的碳质床，并且示例性实施方案包括在单床中进行反应的一个容器，以及在每个容器中在碳质床部分中进行反应的两个容器。

5. 发明授权

US09314655B2 Process and apparatus for treatment of incinerator bottom ash and fly ash 有权
标题翻译：用于处理焚烧炉底灰和飞灰的工艺和设备
公开(公告)号：US09314655B2
公开(公告)日：2016-04-19
申请号：US13445255
申请日：2012-04-12
申请人： Kent Olis Hicks , Surendra Chavda , James Santoianni , Aleksandr Gorodetsky , Pieter Van Nierop
发明人： Kent Olis Hicks , Surendra Chavda , James Santoianni , Aleksandr Gorodetsky , Pieter Van Nierop
IPC分类号： B09B3/00 , A62D3/40 , C03B5/00 , F23J1/00 , F23G5/027 , A62D101/08
CPC分类号： A62D3/40 , A62D2101/08 , B09B3/00 , B09B3/005 , B09B3/0083 , C03B5/00 , F23G5/0276 , F23J1/00 , Y02W30/20
摘要： A method for treatment of ash from incineration plants includes: collecting ash from an incinerator; feeding the collected ash and additional feed material to a gasification/vitrification reactor; vitrifying the ash and additional feed material in the gasification/vitrification reactor, to form a slag of molten material; allowing the slag to flow from the gasification/vitrification reactor and solidify outside the gasification/vitrification reactor; gasifying volatile components in the ash and the additional feed material; and using syngas generated in the gasification/vitrification reactor to augment the thermal environments of the incinerator.
摘要翻译：从焚烧厂处理灰分的方法包括：从焚化炉收集灰分; 将收集的灰分和额外的进料送入气化/玻璃化反应器; 在气化/玻璃化反应器中玻璃化灰分和额外的进料，形成熔融材料的炉渣; 允许炉渣从气化/玻璃化反应器流出并固化在气化/玻璃化反应器外部; 在灰分和附加进料中气化挥发性成分; 并使用在气化/玻璃化反应器中产生的合成气来增加焚烧炉的热环境。

6. 发明授权

US09005320B2 Enhanced plasma gasifiers for producing syngas 有权
标题翻译：用于生产合成气的增强等离子气化器
公开(公告)号：US09005320B2
公开(公告)日：2015-04-14
申请号：US13199813
申请日：2011-09-09
申请人： Aleksandr Gorodetsky , James Santoianni , Surendra Chavda , Sureshkumar Kukadiya
发明人： Aleksandr Gorodetsky , James Santoianni , Surendra Chavda , Sureshkumar Kukadiya
IPC分类号： B01J7/00 , C10J3/84 , C10J3/18
CPC分类号： C10L3/10 , C10J3/18 , C10J3/84 , C10J2300/1238
摘要： A plasma gasification reactor, and process for its operation, with one or both of, first, a quench zone within an upper part of a top section of the reactor and, second, feed ports through a lateral wall of a middle section of the reactor for supplying feed material to a feed bed within the middle section and the feed ports located proximate the feed bed. The quench zone is provided with nozzles for introducing a fluid to reduce the temperature of molten solid bits sufficiently to minimize their sticking within external ductwork. The middle section feed port arrangement assists in more thorough reaction of light particles in the feed material that may otherwise exit with gaseous products.
摘要翻译：等离子体气化反应器及其操作方法，其中在反应器的顶部的上部中的一个或两个第一骤冷区，以及第二，通过反应器的中间部分的侧壁的进料口用于将进料材料供应到中间部分内的进料床和位于进料床附近的进料口。淬火区域设置有用于引入流体的喷嘴，以充分降低熔融固体钻头的温度，以使其在外部管道系统内的粘附最小化。中间部分进料口布置有助于进料中轻质颗粒的更彻底的反应，否则可能会用气体产物排出。

7. 发明申请

US20080299019A1 System and process for upgrading heavy hydrocarbons 有权
标题翻译：升级重质烃的系统和工艺
公开(公告)号：US20080299019A1
公开(公告)日：2008-12-04
申请号：US11807436
申请日：2007-05-29
申请人： Shyam V. Dighe , Mark Anthony Montemurro , Richard Dale Bower , Aleksandr Gorodetsky , Mark F. Darr , Ivan A. Martorell
发明人： Shyam V. Dighe , Mark Anthony Montemurro , Richard Dale Bower , Aleksandr Gorodetsky , Mark F. Darr , Ivan A. Martorell
IPC分类号： B01J8/04
CPC分类号： C10G15/12 , C10G2/40 , C10G45/26 , C10G47/22 , F23G7/05 , F23G2201/40 , F23G2204/201 , F23G2900/7013 , Y02E50/32
摘要： A system and process for upgrading hydrocarbons such as heavy oils includes high temperature plasma reactor apparatus, in one or more vessels, into which the oils are introduced along with water, such as steam, to produce lighter hydrocarbon fractions, along with carbon monoxide and hydrogen, that flows to an additional stage where more hydrocarbons and water are introduced for further fractionating reactions facilitated by reaction of carbon monoxide and water to produce carbon dioxide and nascent, or prompt, free radicals of hydrogen. Heavy hydrocarbons upgraded can include heavy oils in the form of tar sands, oil shale, and oil residuals. The vessel or vessels can each contain a carbonaceous bed facilitating the described reactions and example embodiments include one vessel with the reactions performed in a single bed and, also, two vessels with the reactions performed in a carbonaceous bed portion in each vessel.
摘要翻译：用于升级烃类如重油的系统和方法包括在一个或多个容器中的高温等离子体反应器装置，油与水一起引入其中，例如蒸汽，以产生较轻的烃馏分以及一氧化碳和氢气，其流入另外的阶段，其中引入更多的碳氢化合物和水以进一步分馏反应，由一氧化碳和水的反应促进，从而产生二氧化碳和新生的氢或快速的氢自由基。重质烃升级可包括焦油砂，油页岩和油残留物形式的重油。容器或容器可各自含有促进所述反应的碳质床，并且示例性实施方案包括在单床中进行反应的一个容器，以及在每个容器中在碳质床部分中进行反应的两个容器。

8. 发明申请

US20120286210A1 SYNGAS PRODUCED BY PLASMA GASIFICATION 审中-公开
标题翻译：由等离子体气化生产的SYNGAS
公开(公告)号：US20120286210A1
公开(公告)日：2012-11-15
申请号：US13293330
申请日：2011-11-10
申请人： Gowri Krishnamurthy , Christine Peck Kretz , Charles Roland Higdon, III , Aleksandr Gorodetsky , James Santoianni
发明人： Gowri Krishnamurthy , Christine Peck Kretz , Charles Roland Higdon, III , Aleksandr Gorodetsky , James Santoianni
IPC分类号： C01B3/00 , C01B3/02
CPC分类号： C10J3/72 , C10J3/18 , C10J2300/0906 , C10J2300/0943 , C10J2300/0946 , C10J2300/0959 , C10J2300/1238 , C10J2300/1643 , C10J2300/1671 , C10K1/06 , Y02E60/324
摘要： A syngas stream composition comprising on a dry basis up to about 50,000 mg/Nm3 particulates; 5-39 vol % H2; 5-39 vol % CO; 15-50 vol % CO2; 8-30 vol % N2; 0-2 vol % Argon; and 15-50 vol % moisture on a wet basis. The stream includes a H2/CO ratio that is about 0.3-2 and at least 15 wt % of particulates have an aerodynamic particle diameter of less than or equal to 1 micron. A gasified waste stream and a method for forming a gasified waste stream are also disclosed.
摘要翻译：一种合成气流组合物，其包含基于约50,000mg / Nm3颗粒的干基; 5-39体积％H2; 5-39体积％CO; 15-50体积％二氧化碳; 8-30体积％N2; 0-2体积％氩气; 湿度为15-50％（体积）。该流包括约0.3-2的H 2 / CO比，并且至少15重量％的颗粒具有小于或等于1微米的空气动力学粒径。还公开了气化废物流和形成气化废物流的方法。

9. 发明授权

US08052946B2 System and process for upgrading heavy hydrocarbons 有权
标题翻译：升级重质烃的系统和工艺
公开(公告)号：US08052946B2
公开(公告)日：2011-11-08
申请号：US12589657
申请日：2009-10-27
申请人： Shyam V. Dighe , Mark Anthony Montemurro , Richard Dale Bower , Aleksandr Gorodetsky , Mark F. Darr , Ivan A. Martorell
发明人： Shyam V. Dighe , Mark Anthony Montemurro , Richard Dale Bower , Aleksandr Gorodetsky , Mark F. Darr , Ivan A. Martorell
IPC分类号： B01J8/04
CPC分类号： C10G15/12 , C10G2/40 , C10G45/26 , C10G47/22 , F23G7/05 , F23G2201/40 , F23G2204/201 , F23G2900/7013 , Y02E50/32
摘要： A system and process for upgrading hydrocarbons such as heavy oils includes a high temperature plasma reactor apparatus, in one or more vessels, into which the oils are introduced along with water, such as steam, to produce lighter hydrocarbon fractions, along with carbon monoxide and hydrogen, that flows to an additional stage where more hydrocarbons and water are introduced for further fractionating reactions facilitated by reaction of carbon monoxide and water to produce carbon dioxide and nascent, or prompt, free radicals of hydrogen. Heavy hydrocarbons upgraded can include heavy oils in the form of tar sands, oil shale, and oil residuals. The vessel or vessels can each contain a carbonaceous bed facilitating the described reactions and example embodiments include one vessel with the reactions performed in a single bed and, also, two vessels with the reactions performed in a carbonaceous bed portion in each vessel.
摘要翻译：用于升级烃类如重油的系统和方法包括在一个或多个容器中的高温等离子体反应器装置，油与水一起引入其中，例如蒸汽，以产生较轻的烃馏分以及一氧化碳，以及氢，其流入另外的阶段，其中引入更多的烃和水用于通过一氧化碳和水的反应促进的进一步分馏反应以产生二氧化碳和新生的氢或快速的氢的自由基。重质烃升级可包括焦油砂，油页岩和油残留物形式的重油。容器或容器可各自含有促进所述反应的碳质床，并且示例性实施方案包括在单床中进行反应的一个容器，以及在每个容器中在碳质床部分中进行反应的两个容器。

10. 发明申请

US20100199556A1 Plasma gasification reactor 审中-公开
标题翻译：等离子气化反应器
公开(公告)号：US20100199556A1
公开(公告)日：2010-08-12
申请号：US12378166
申请日：2009-02-11
申请人： Shyam V. Dighe , Mark F. Darr , Ivan A. Martorell , Pieter van Nierop , Aleksandr Gorodetsky , Richard Dale Bower
发明人： Shyam V. Dighe , Mark F. Darr , Ivan A. Martorell , Pieter van Nierop , Aleksandr Gorodetsky , Richard Dale Bower
IPC分类号： C10J3/18
CPC分类号： C10J3/18 , C10J3/30 , C10J2200/152 , C10J2300/0916 , C10J2300/093 , C10J2300/0946 , C10J2300/1238
摘要： A plasma gasification reactor vessel having a top section with a conical wall extending up from a bottom section, containing a carbonaceous bed into which plasma is injected by plasma torches, to a roof of the vessel is arranged in ways that can contribute to characteristics of gas flow and solids residence time that are favorable for thoroughness of reactions and yield of useful reactions products. In some cases, such a conical wall is combined in arrangements with other features such as one or more feed ports arranged to give more uniform distribution including examples with a feed port that has a distributive feed mechanism. The roof of the vessel, in some examples, has vertical outlet ports that include intrusions into the interior volume of the reactor proximate the conical wall of the top section. The configurations of outlet ports with intrusions and the configurations of feed ports for more uniform distribution of feed material are also applicable to reactor vessels with other geometries.
摘要翻译：等离子体气化反应器容器具有顶部，该顶部具有从底部向上延伸的锥形壁，该底部包含通过等离子体喷枪将等离子体注入到其中的碳质床到容器的顶部，其方式可以有助于气体的特性流动和固体停留时间，有利于反应的完全性和有用的反应产物的产率。在一些情况下，这样的锥形壁与其它特征（例如一个或多个进料口）组合，其布置成给出更均匀的分布，包括具有具有分配进料机构的进料口的实例。在一些示例中，容器的顶部具有垂直的出口端口，其包括在顶部的锥形壁附近侵入反应器的内部容积。具有入侵的出口端口的结构和用于进料均匀分布的进料口的结构也适用于具有其它几何形状的反应器容器。

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式