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公开(公告)号：US20130134098A1
公开(公告)日：2013-05-30
申请号：US13307656
申请日：2011-11-30
申请人： William Leonard Kostedt, IV , James Manio Silva , Hope Matis , Vicki Herzl Watkins , Harish Radhakrishna Acharya
发明人： William Leonard Kostedt, IV , James Manio Silva , Hope Matis , Vicki Herzl Watkins , Harish Radhakrishna Acharya
CPC分类号： C02F1/281 , B01J20/06 , B01J20/28009 , B01J20/3433 , B01J20/3475 , B01J2220/42 , B03C1/01 , B03C2201/18 , C02F1/041 , C02F1/08 , C02F1/288 , C02F1/488 , C02F1/5236 , C02F1/66 , C02F5/06 , C02F2001/5218 , C02F2101/006 , C02F2101/10 , C02F2101/20 , C02F2103/10 , C02F2303/16
摘要： Methods for treating water to remove radium include contacting the water with a magnetic adsorbent comprising manganese oxide(s), and applying a magnetic field to separate the magnetic adsorbent from the water, whereby radium is removed from the water. The methods may additionally include regenerating the magnetic adsorbent, and contacting the water with regenerated magnetic adsorbent. Alternately, calcium and/or strontium may be precipitated as carbonate salts from lime-treated water containing radium and barium without precipitating a significant fraction of the barium or radium; and removing radium from calcium- and strontium-free water by precipitating the barium and radium as carbonate salts. The barium- and radium carbonate precipitate may be redissolved in hydrochloric acid and disposed of by deep-well injection.
摘要翻译： 用于处理水以去除镭的方法包括使水与包含氧化锰的磁性吸附剂接触，并施加磁场以将磁性吸附剂与水分离，从而从水中除去镭。 所述方法还可包括再生磁吸附剂，并使水与再生磁吸附剂接触。 或者，钙和/或锶可以从含有镭和钡的石灰处理水中以碳酸盐形式沉淀而不沉淀出大部分的钡或镭; 并通过沉淀钡和镭作为碳酸盐，从钙和无锶水中去除镭。 碳酸钡和镭碳酸盐沉淀可以重新溶解在盐酸中，并通过深井注射进行处理。
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公开(公告)号：US20130098049A1
公开(公告)日：2013-04-25
申请号：US13279186
申请日：2011-10-21
CPC分类号： B01D53/56 , F01N3/0205 , F01N3/04 , F01N3/103 , F01N3/36 , F01N5/02 , F01N9/00 , F01N2240/02 , F01N2240/14 , F01N2560/026 , F01N2560/14 , F01N2570/04 , F01N2570/22 , F01N2610/03 , F01N2610/1453 , F01N2610/146 , F01N2900/0408 , F01N2900/1402 , F01N2900/1404 , F02M26/35 , Y02T10/16 , Y02T10/20 , Y02T10/47
摘要： A system includes a gas production source configured to produce a gas stream comprising nitrogen oxides (NOx) and a hydrocarbon injector disposed downstream of the gas production source and configured to inject a hydrocarbon into the gas stream. The hydrocarbon is configured to oxidize molecules of the NOx in the gas stream to produce a higher order compound of nitrogen and oxygen (NyOz). The system also includes a removal device disposed downstream of the hydrocarbon injector. The removal device is configured to remove the NyOz from the gas stream via absorption or reaction.
摘要翻译： 一种系统包括气体生成源，其被配置为产生包含氮氧化物（NOx）的气流和设置在气体生产源的下游的烃喷射器，并且构造成将烃注入到气流中。 烃被配置为氧化气流中的NO x的分子，以产生氮和氧的较高级化合物（NyOz）。 该系统还包括设置在烃喷射器下游的去除装置。 去除装置构造成通过吸收或反应从气流中除去NyOz。
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公开(公告)号：US07901646B2
公开(公告)日：2011-03-08
申请号：US12535740
申请日：2009-08-05
CPC分类号： B01D53/228 , B01D53/507 , B01D53/508 , B01D53/523 , B01D2251/402 , B01D2251/404 , B01D2251/408 , B01D2251/602 , B01D2252/2023 , B01D2252/204 , B01D2255/20723 , B01D2255/20738 , B01D2255/20753 , B01D2255/20761 , B01D2255/20776 , B01D2255/20784 , B01D2255/20792 , B01D2255/2094 , C01B17/021 , C01B17/04 , C01B17/76
摘要： Disclosed herein are various types of systems and methods for the efficient production of sulfur from a sulfur-laden gas. The system described herein includes a desulfurization unit, a regenerator receiving sulfurized mass from the desulfurization unit, a sulfur recovery unit, a sulfur track in fluid communication with the regenerator and the sulfur recovery unit, and a sulfur concentrator on a sulfur track. The sulfur stream coming out of the regenerator is concentrated using the sulfur concentrator and converted into a sulfur product at the sulfur recovery unit.
摘要翻译： 本文公开了用于从含硫载气有效生产硫的各种类型的系统和方法。 本文所述的系统包括脱硫单元，从脱硫单元接收硫化物质的再生器，硫回收单元，与再生器和硫回收单元流体连通的硫轨道，以及硫轨道上的硫浓缩器。 使用硫浓缩器浓缩从再生器出来的硫流，并在硫回收单元处转化成硫产物。
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公开(公告)号：US20110033370A1
公开(公告)日：2011-02-10
申请号：US12535740
申请日：2009-08-05
CPC分类号： B01D53/228 , B01D53/507 , B01D53/508 , B01D53/523 , B01D2251/402 , B01D2251/404 , B01D2251/408 , B01D2251/602 , B01D2252/2023 , B01D2252/204 , B01D2255/20723 , B01D2255/20738 , B01D2255/20753 , B01D2255/20761 , B01D2255/20776 , B01D2255/20784 , B01D2255/20792 , B01D2255/2094 , C01B17/021 , C01B17/04 , C01B17/76
摘要： Disclosed herein are various types of systems and methods for the efficient production of sulfur from a sulfur-laden gas. The system described herein includes a desulfurization unit, a regenerator receiving sulfurized mass from the desulfurization unit, a sulfur recovery unit, a sulfur track in fluid communication with the regenerator and the sulfur recovery unit, and a sulfur concentrator on a sulfur track. The sulfur stream coming out of the regenerator is concentrated using the sulfur concentrator and converted into a sulfur product at the sulfur recovery unit.
摘要翻译： 本文公开了用于从含硫载气有效生产硫的各种类型的系统和方法。 本文所述的系统包括脱硫单元，从脱硫单元接收硫化物质的再生器，硫回收单元，与再生器和硫回收单元流体连通的硫轨道，以及硫轨道上的硫浓缩器。 使用硫浓缩器浓缩从再生器出来的硫流，并在硫回收单元处转化成硫产物。
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公开(公告)号：US07879295B2
公开(公告)日：2011-02-01
申请号：US11172288
申请日：2005-06-30
申请人： Ke Liu , Arnaldo Frydman , Vladimir Zamansky , Teresa Grocela Rocha , Jonathan Lloyd Male , Harish Radhakrishna Acharya , Roy James Primus
发明人： Ke Liu , Arnaldo Frydman , Vladimir Zamansky , Teresa Grocela Rocha , Jonathan Lloyd Male , Harish Radhakrishna Acharya , Roy James Primus
CPC分类号： B01D53/9418 , B01D53/90 , B01D2251/208 , B01D2255/1021 , B01D2255/50 , C10G11/05 , C10G2300/104 , C10G2300/1051 , C10G2300/1055 , C10G2300/405 , C10G2300/708 , F01N3/2066 , F01N2240/30 , F01N2570/14 , F01N2610/03 , F01N2610/04 , F01N2610/1426 , F02M27/02 , Y02A50/2325 , Y02A50/2344 , Y02T10/24
摘要： Disclosed herein is a system for reducing NOx emissions comprising a fuel tank in fluid communication with a fuel converter, wherein the fuel converter is located down stream of the fuel tank and wherein the fuel converter comprises a catalyst composition that is operative to continuously convert heavy hydrocarbon molecules having 9 or more carbon atoms per molecule into light hydrocarbon molecules having 8 or less carbon atoms per molecule; a selective catalytic reduction catalyst reactor in fluid communication with the fuel converter and located downstream of the fuel converter; and an engine in fluid communication with the fuel tank and the selective catalytic reduction catalyst reactor, wherein the engine is located downstream of the fuel tank and upstream of the selective catalytic reduction catalyst reactor.
摘要翻译： 本文公开了一种用于减少NOx排放的系统，其包括与燃料转化器流体连通的燃料箱，其中燃料转化器位于燃料箱的下游，并且其中燃料转化器包括催化剂组合物，其用于连续转化重质烃 每分子具有9个或更多个碳原子的分子转化成每分子具有8个或更少碳原子的轻质烃分子; 选择性催化还原催化剂反应器，其与燃料转化器流体连通并位于燃料转化器的下游; 以及与所述燃料箱和所述选择性催化还原催化剂反应器流体连通的发动机，其中所述发动机位于所述燃料箱的下游以及所述选择性催化还原催化剂反应器的上游。
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公开(公告)号：US09056274B2
公开(公告)日：2015-06-16
申请号：US13279186
申请日：2011-10-21
IPC分类号： B01D53/56
CPC分类号： B01D53/56 , F01N3/0205 , F01N3/04 , F01N3/103 , F01N3/36 , F01N5/02 , F01N9/00 , F01N2240/02 , F01N2240/14 , F01N2560/026 , F01N2560/14 , F01N2570/04 , F01N2570/22 , F01N2610/03 , F01N2610/1453 , F01N2610/146 , F01N2900/0408 , F01N2900/1402 , F01N2900/1404 , F02M26/35 , Y02T10/16 , Y02T10/20 , Y02T10/47
摘要： A system includes a gas production source configured to produce a gas stream comprising nitrogen oxides (NOx) and a hydrocarbon injector disposed downstream of the gas production source and configured to inject a hydrocarbon into the gas stream. The hydrocarbon is configured to oxidize molecules of the NOx in the gas stream to produce a higher order compound of nitrogen and oxygen (NyOz). The system also includes a removal device disposed downstream of the hydrocarbon injector. The removal device is configured to remove the NyOz from the gas stream via absorption or reaction.
摘要翻译： 一种系统包括气体生成源，其被配置为产生包含氮氧化物（NOx）的气流和设置在气体生产源的下游的烃喷射器，并且构造成将烃注入到气流中。 烃被配置为氧化气流中的NO x的分子，以产生氮和氧的较高级化合物（NyOz）。 该系统还包括设置在烃喷射器下游的去除装置。 去除装置构造成通过吸收或反应从气流中除去NyOz。
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7.发明授权公开(公告)号：US08495882B2
公开(公告)日：2013-07-30
申请号：US12538327
申请日：2009-08-10
申请人： Anthony Yu-Chung Ku , Harish Radhakrishna Acharya , Parag Prakash Kulkarni , Scott Michael Miller , William Cook Livingood, III
发明人： Anthony Yu-Chung Ku , Harish Radhakrishna Acharya , Parag Prakash Kulkarni , Scott Michael Miller , William Cook Livingood, III
CPC分类号： C01B3/32 , C01B3/50 , C01B3/501 , C01B3/52 , C01B2203/0283 , C01B2203/0288 , C01B2203/0405 , C01B2203/044 , C01B2203/045 , C01B2203/0455 , C01B2203/047 , C01B2203/0475 , C01B2203/0485 , C01B2203/0495 , C01B2203/06 , C01B2203/145 , C01B2203/146 , C01B2203/84 , Y02E20/16 , Y02E20/18 , Y02P30/30
摘要： A syngas cleanup section includes a water-gas shift reactor, a first operation unit and a second operation unit. The first operation unit includes a high permeance membrane with H2/CO2 selectivity in flow communication with the water-gas shift reactor to provide a H2-rich permeate stream and an H2-poor retentate stream. The second operation unit recovers H2 and CO from the retentate stream to produce a single, CO2-rich product stream, the entire content of which has a minimum pressure of at least about 10.0 bar. In one embodiment, the second operation unit includes a membrane with Knudsen selectivity for permeating H2, CO and CO2. In this embodiment, the permeate streams are combined to produce a H2 and CO-rich fuel stream used by a combined cycle power generation unit to produce electricity, and the retentate stream is sent to a catalytic oxidation unit to produce the CO2-rich product stream. In another embodiment, the second operation unit is the catalytic oxidation unit.
摘要翻译： 合成气净化部分包括水煤气变换反应堆，第一操作单元和第二操作单元。 第一操作单元包括具有与水煤气变换反应器流动连通的H 2 / CO 2选择性的高渗透膜，以提供富H2的渗透物流和不良的滞留物流。 第二操作单元从滞留物流中回收H 2和CO以产生单一的富含CO 2的产物流，其全部内容物具有至少约10.0巴的最小压力。 在一个实施方案中，第二操作单元包括具有用于渗透H 2，CO和CO 2的Knudsen选择性的膜。 在该实施方案中，将渗透物流组合以产生由联合循环发电单元使用的H 2和CO富燃料流以产生电力，并将滞留物流送至催化氧化装置以产生富含CO 2的产物流 。 在另一个实施方案中，第二操作单元是催化氧化单元。
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公开(公告)号：US09985295B2
公开(公告)日：2018-05-29
申请号：US11235555
申请日：2005-09-26
申请人： Bastiaan Arie Korevaar , Yuk-Chiu Lau , Anteneh Kebbede , Harish Radhakrishna Acharya , Badri Narayan Ramamurthi , Gregory John Parker
发明人： Bastiaan Arie Korevaar , Yuk-Chiu Lau , Anteneh Kebbede , Harish Radhakrishna Acharya , Badri Narayan Ramamurthi , Gregory John Parker
IPC分类号： H01M8/12 , H01M8/24 , H01M4/86 , H01M4/90 , H01M4/88 , H01M8/1226 , H01M8/1246
CPC分类号： H01M4/9025 , H01M4/8621 , H01M4/8885 , H01M4/9016 , H01M4/9066 , H01M8/1226 , H01M8/1246 , Y02E60/525 , Y02P70/56
摘要： A solid oxide fuel cell is disclosed. The fuel cell includes a porous anode, formed of finely-dispersed nickel/stabilized-zirconia powder particles. The particles have an average diameter of less than about 300 nanometers. They are also characterized by a tri-phase length of greater than about 50 μm/μm3. A solid oxide fuel cell stack is also described, along with a method of forming an anode for a solid oxide fuel cell. The method includes the step of using a spray-agglomerated, nickel oxide/stabilized-zirconia powder to form the anode.
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9.发明申请公开(公告)号：US20110030384A1
公开(公告)日：2011-02-10
申请号：US12538327
申请日：2009-08-10
申请人： Anthony Yu-Chung Ku , Harish Radhakrishna Acharya , Parag Prakash Kulkarni , Scott Michael Miller , William Cook Livingood, III
发明人： Anthony Yu-Chung Ku , Harish Radhakrishna Acharya , Parag Prakash Kulkarni , Scott Michael Miller , William Cook Livingood, III
CPC分类号： C01B3/32 , C01B3/50 , C01B3/501 , C01B3/52 , C01B2203/0283 , C01B2203/0288 , C01B2203/0405 , C01B2203/044 , C01B2203/045 , C01B2203/0455 , C01B2203/047 , C01B2203/0475 , C01B2203/0485 , C01B2203/0495 , C01B2203/06 , C01B2203/145 , C01B2203/146 , C01B2203/84 , Y02E20/16 , Y02E20/18 , Y02P30/30
摘要： A syngas cleanup section includes a water-gas shift reactor, a first operation unit and a second operation unit. The first operation unit includes a high permeance membrane with H2/CO2 selectivity in flow communication with the water-gas shift reactor to provide a H2-rich permeate stream and an H2-poor retentate stream. The second operation unit recovers H2 and CO from the retentate stream to produce a single, CO2-rich product stream, the entire content of which has a minimum pressure of at least about 10.0 bar. In one embodiment, the second operation unit includes a membrane with Knudsen selectivity for permeating H2, CO and CO2. In this embodiment, the permeate streams are combined to produce a H2 and CO-rich fuel stream used by a combined cycle power generation unit to produce electricity, and the retentate stream is sent to a catalytic oxidation unit to produce the CO2-rich product stream. In another embodiment, the second operation unit is the catalytic oxidation unit.
摘要翻译： 合成气净化部分包括水煤气变换反应堆，第一操作单元和第二操作单元。 第一操作单元包括具有与水煤气变换反应器流动连通的H 2 / CO 2选择性的高渗透膜，以提供富H2的渗透物流和不良的滞留物流。 第二操作单元从滞留物流中回收H 2和CO以产生单一的富含CO 2的产物流，其全部内容物具有至少约10.0巴的最小压力。 在一个实施方案中，第二操作单元包括具有用于渗透H 2，CO和CO 2的Knudsen选择性的膜。 在该实施方案中，将渗透物流组合以产生由联合循环发电单元使用的H 2和CO富燃料流以产生电力，并将滞留物流送至催化氧化装置以产生富含CO 2的产物流 。 在另一个实施方案中，第二操作单元是催化氧化单元。
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公开(公告)号：US06339109B1
公开(公告)日：2002-01-15
申请号：US09371451
申请日：1999-08-10
IPC分类号： C08J900
CPC分类号： C08J9/26 , B29C44/3461 , C08J9/142 , C08J9/16 , C08J2201/0422 , C08J2369/00
摘要： A method of preparing cellular pellets from a prepolymer comprising a blowing agent, the method comprising the steps of: a) extruding the prepolymer through a die, the die maintained at conditions such that the blowing agent remains in the condensed phase in the prepolymer prior to emerging from the die, and b) upon emergence of the prepolymer through the die, substantially simultaneously cooling the prepolymer by contacting the prepolymer with a cooling agent and cutting the prepolymer; the conditions outside the die being maintained such that the blowing agent vaporizes in the prepolymer to form pores.
摘要翻译： 一种从包含发泡剂的预聚物制备细胞颗粒的方法，所述方法包括以下步骤：a）将预聚物挤出通过模具，模具保持在使发泡剂在预聚物之前保持在凝聚相中的状态， 在模具出现时，通过模头出现预聚物，通过使预聚物与冷却剂接触并切割预聚物，基本上同时冷却预聚物; 保持模具外部的条件使得发泡剂在预聚物中蒸发以形成孔。
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