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1. 发明申请

US20070130831A1 System and method for co-production of hydrogen and electrical energy 审中-公开
标题翻译：用于共同生产氢气和电能的系统和方法
公开(公告)号：US20070130831A1
公开(公告)日：2007-06-14
申请号：US11297774
申请日：2005-12-08
申请人： Ravikumar Vipperla , Parag Kulkarni , Vladimir Zamansky
发明人： Ravikumar Vipperla , Parag Kulkarni , Vladimir Zamansky
IPC分类号： C10J3/46 , F02G3/00
CPC分类号： C01B3/382 , C01B3/48 , C01B2203/0233 , C01B2203/0244 , C01B2203/0261 , C01B2203/0283 , C01B2203/0288 , C01B2203/0405 , C01B2203/0415 , C01B2203/043 , C01B2203/0475 , C01B2203/06 , C01B2203/066 , C01B2203/0844 , C01B2203/1211 , C01B2203/1223 , C01B2203/1229 , C01B2203/1241 , C01B2203/1247 , C01B2203/1252 , C01B2203/84
摘要： A system for the co-production of hydrogen and electrical energy includes a reformer comprising at least one mixed reforming zone configured to receive a fuel stream and steam, at least one steam reforming zone and a plurality of oxidant inlets to introduce an oxidant into the reformer. The mixed reforming zone is followed by the steam reforming zone to produce a first reformate stream comprising hydrogen. The system further includes a shift reactor configured to receive the first reformate stream and generate a second reformate stream and a carbon dioxide separation unit configured to receive the second reformate stream and separate carbon dioxide from the second reformate stream to generate a carbon dioxide rich stream and a hydrogen rich stream. The system also includes a power generation device configured to receive the hydrogen rich stream to generate electrical energy.
摘要翻译：用于共同生产氢气和电能的系统包括重整器，该重整器包括至少一个混合重整区域，该混合重整区域构造成接收燃料流和蒸汽，至少一个蒸汽重整区和多个氧化剂入口，以将氧化剂引入重整器。混合的重整区之后是蒸汽重整区，以产生包含氢的第一重整产物流。系统还包括配置成接纳第一重整产物流并产生第二重整产物流的转化反应器，和二氧化碳分离单元，其被配置为接收第二重整产物流并将二氧化碳与第二重整产物流分离以产生富含二氧化碳的物流，富氢流。该系统还包括被配置为接收富氢流以产生电能的发电装置。

2. 发明申请

US20060137246A1 System and method for hydrogen production 有权
公开(公告)号：US20060137246A1
公开(公告)日：2006-06-29
申请号：US11022406
申请日：2004-12-27
申请人： Ravi Kumar , Vladimir Zamansky , Boris Eiteneer , Shawn Barge , Parag Kulkarni , Ke Liu
发明人： Ravi Kumar , Vladimir Zamansky , Boris Eiteneer , Shawn Barge , Parag Kulkarni , Ke Liu
IPC分类号： B01J7/00
CPC分类号： B01J8/0496 , B01J8/0257 , B01J8/0438 , B01J8/0442 , B01J8/0465 , B01J8/0469 , B01J8/048 , B01J8/067 , B01J2208/00132 , B01J2208/00194 , B01J2208/00203 , B01J2208/00212 , B01J2208/00309 , B01J2208/00362 , B01J2208/00504 , B01J2208/0053 , B01J2208/00849 , B01J2208/025 , C01B3/382 , C01B3/386 , C01B2203/0233 , C01B2203/0244 , C01B2203/0261 , C01B2203/0283 , C01B2203/0288 , C01B2203/04 , C01B2203/0405 , C01B2203/0415 , C01B2203/043 , C01B2203/046 , C01B2203/0475 , C01B2203/0827 , C01B2203/0838 , C01B2203/1223 , C01B2203/1229 , C01B2203/1235 , C01B2203/143 , C01B2203/82 , C01B2203/84
摘要： A system for production of hydrogen comprises at least one steam reforming zone configured to receive a first fuel and steam to produce a first reformate gas stream comprising hydrogen using a steam reforming process. The system further comprises a mixed reforming zone configured to receive an oxidant to produce a second reformate gas stream comprising hydrogen, wherein the first reformate gas stream is sent to the mixed reforming zone to complete the reforming process.

3. 发明申请

US20070130832A1 Methods and apparatus for converting a fuel source to hydrogen 审中-公开
标题翻译：将燃料源转化为氢的方法和装置
公开(公告)号：US20070130832A1
公开(公告)日：2007-06-14
申请号：US11301806
申请日：2005-12-13
申请人： Ke Liu , Jennifer Molaison , Parag Kulkarni , Vladimir Zamansky
发明人： Ke Liu , Jennifer Molaison , Parag Kulkarni , Vladimir Zamansky
IPC分类号： C01B3/32
CPC分类号： C01B3/48 , B01D2257/504 , B01J2219/00006 , C01B3/501 , C01B2203/02 , C01B2203/0288 , C01B2203/0294 , C01B2203/0405 , C01B2203/041 , C01B2203/0475 , C01B2203/0485 , C01B2203/0877 , C01B2203/0883 , C01B2203/0894 , C01B2203/1041 , C01B2203/1047 , C01B2203/1064 , C01B2203/107 , C01B2203/1076 , C01B2203/1235 , C01B2203/146 , C01B2203/84 , C01B2203/86 , C10J3/485 , C10J3/82 , C10J2300/093 , C10J2300/0959 , C10J2300/1687 , C10J2300/1884 , C10J2300/1892 , Y02E20/16 , Y02E20/18 , Y02E20/185 , Y02P20/52 , Y02P30/30
摘要： An apparatus for producing hydrogen gas, wherein the apparatus includes a gasification unit or a reforming unit configured to form a first syngas and a first clean-up section is coupled to the gasification unit for acidic gas removal. The first clean-up section is configured to form a second syngas and includes at least one of a high temperature shift catalyst and a low temperature shift catalyst. The apparatus also includes a second clean-up section coupled to the first clean-up section for acidic gas removal.
摘要翻译：一种用于生产氢气的装置，其中所述装置包括构造成形成第一合成气的气化单元或重整单元，并且第一清除部分耦合到用于酸性气体去除的气化单元。第一清理部分构造成形成第二合成气，并且包括高温变换催化剂和低温变换催化剂中的至少一种。该装置还包括联接到第一清理部分用于酸性气体去除的第二清理部分。

4. 发明申请

US20070122339A1 Methods and apparatus for hydrogen production 审中-公开
标题翻译：氢气生产的方法和装置
公开(公告)号：US20070122339A1
公开(公告)日：2007-05-31
申请号：US11287644
申请日：2005-11-28
申请人： Parag Kulkarni , Richard Bourgeois , Ke Liu , Ravi Sathya Vipperla , Vladimir Zamansky
发明人： Parag Kulkarni , Richard Bourgeois , Ke Liu , Ravi Sathya Vipperla , Vladimir Zamansky
IPC分类号： C01B3/26 , C25C1/02 , B01J8/04 , C25B9/00
CPC分类号： C25B1/04 , C01B3/386 , C01B3/48 , C01B2203/0261 , C01B2203/0288 , C01B2203/044 , C01B2203/047 , C01B2203/0475 , C01B2203/0495 , C01B2203/06 , C01B2203/147 , C01B2203/84 , Y02E60/366
摘要： An apparatus for producing hydrogen (H2) includes an electrolyzer configured to produce H2 gas from steam and a catalytic partial oxidation (CPO) reformer. The CPO reformer is coupled to the electrolyzer and configured to utilize byproducts of the electrolyzer as input to produce more H2. The electrolyzer is coupled to the CPO reformer to utilize steam and heat byproducts from the CPO reformer as input to the electrolyzer.
摘要翻译：一种生产氢气（H2）的装置包括一个电解槽，其被配置为从蒸汽和催化部分氧化（CPO）重整器中产生H2气。 CPO重整器耦合到电解器并且被配置为利用电解器的副产物作为输入以产生更多的H 2。电解槽连接到CPO重整器，以利用来自CPO重整器的蒸汽和热副产物作为电解槽的输入。

5. 发明授权

US08574329B2 Method of operating a gasifier 有权
标题翻译：操作气化炉的方法
公开(公告)号：US08574329B2
公开(公告)日：2013-11-05
申请号：US12337742
申请日：2008-12-18
申请人： Vladimir Zamansky , Vitali Lissianski , Boris Nikolaevich Eiteneer , Wei Wei , Ravichandra Srinivasa Jupudi , Ramanathan Subramanian
发明人： Vladimir Zamansky , Vitali Lissianski , Boris Nikolaevich Eiteneer , Wei Wei , Ravichandra Srinivasa Jupudi , Ramanathan Subramanian
IPC分类号： C01B3/36 , C01B6/24 , C10J3/00 , B01J7/00 , F23B10/00
CPC分类号： C10J3/466 , C10J3/506 , C10J3/721 , C10J2200/152 , C10J2300/0916 , C10J2300/093 , C10J2300/0956 , C10J2300/0959 , C10J2300/0969 , C10J2300/0976 , Y02E20/18
摘要： A method of operating a gasifier is provided that envisions dividing the gasifier into multiple zones. A high-calorific-value feedstock with an oxidant is injected in the first zone. The gasifier is operated to substantially consume the oxidant within the first gasification zone. The method of operating the gasifier further includes injecting a low-calorific-value, high-oxygen-content feedstock in a second gasification zone. The low-calorific-value, high-oxygen-content feedstock is devolatilized and gasified in second zone. A method of operation provides for a synergistic co-gasification of the high-calorific-value feedstock and the low-calorific-value, high oxidant content feedstock. The method provides for specific control actions that enable operation of multi-fuel, multizone gasifier.
摘要翻译：提供了一种操作气化器的方法，其设想将气化器分成多个区域。在第一区域注入具有氧化剂的高热值原料。操作气化器以在第一气化区内基本上消耗氧化剂。操作气化器的方法还包括在第二气化区中注入低热值，高含氧量的原料。低热值，高含氧量的原料在第二区域脱挥发和气化。操作方法提供高热值原料和低热值，高氧化剂含量原料的协同共气化。该方法提供了能够操作多燃料多区域气化器的具体控制动作。

6. 发明申请

US20100146858A1 METHOD OF RETROFITTING A COAL GASIFIER 有权
标题翻译：改进煤气化炉的方法
公开(公告)号：US20100146858A1
公开(公告)日：2010-06-17
申请号：US12337762
申请日：2008-12-18
申请人： Vladimir Zamansky , Vitali Lissianski , Boris Nikolaevich Eiteneer , Wei Wei , Ravichandra Srinivasa Jupudi , Ramanathan Subramanian
发明人： Vladimir Zamansky , Vitali Lissianski , Boris Nikolaevich Eiteneer , Wei Wei , Ravichandra Srinivasa Jupudi , Ramanathan Subramanian
IPC分类号： C10J3/00
CPC分类号： C10J3/721 , C10J3/466 , C10J2300/0956 , C10J2300/0959 , C10J2300/0976 , C10J2300/1223 , Y02E20/18 , Y02P20/145
摘要： A coal gasifier is retrofitted to achieve multiple advantages such as reduced oxygen consumption, reduced CO2 and NOx emissions, better H:C ratio, better carbon conversion etc. This is achieved by dividing the coal into at least two zones and modifying the gasifier and operating it as described. The coal is injected into a first zone, configured to devolatilize a substantial portion of the injected coal to produce coal char and volatiles. The operation is tuned to substantially consume the oxidant injected in the first zone. A low-calorific-value, high oxidant feedstock is injected in second zone of the gasifier. The devolatilization of the low-calorific-value, high oxidant content feedstock provides the oxygen containing compounds which gasify at least a portion of the coal char generated in the first zone.
摘要翻译：改造煤气化炉可实现多种优点，例如减少氧气消耗，减少二氧化碳和NOx排放，更好的H：C比，更好的碳转化等。这是通过将煤分为至少两个区域和修改气化器和运行如所述。煤被注入第一区域，其被配置为使大部分注入的煤脱挥发生以产生煤炭和挥发物。该操作被调整以基本上消耗在第一区域中注入的氧化剂。将低热值的高氧化剂原料注入气化器的第二区。低热值高氧化剂含量原料的脱挥发分提供了含氧化合物，其使在第一区域中产生的煤焦炭的至少一部分气化。

7. 发明授权

US07569085B2 System and method for hydrogen production 有权
标题翻译：氢气生产的系统和方法
公开(公告)号：US07569085B2
公开(公告)日：2009-08-04
申请号：US11022406
申请日：2004-12-27
申请人： Ravi Vipperia Kumar , Vladimir Zamansky , Boris Nikolaevich Eiteneer , Shawn David Barge , Parag Prakash Kulkarni , Ke Liu
发明人： Ravi Vipperia Kumar , Vladimir Zamansky , Boris Nikolaevich Eiteneer , Shawn David Barge , Parag Prakash Kulkarni , Ke Liu
IPC分类号： C01B3/36 , C01B3/00 , B01J7/00 , B01J8/04 , B01J10/00
CPC分类号： B01J8/0496 , B01J8/0257 , B01J8/0438 , B01J8/0442 , B01J8/0465 , B01J8/0469 , B01J8/048 , B01J8/067 , B01J2208/00132 , B01J2208/00194 , B01J2208/00203 , B01J2208/00212 , B01J2208/00309 , B01J2208/00362 , B01J2208/00504 , B01J2208/0053 , B01J2208/00849 , B01J2208/025 , C01B3/382 , C01B3/386 , C01B2203/0233 , C01B2203/0244 , C01B2203/0261 , C01B2203/0283 , C01B2203/0288 , C01B2203/04 , C01B2203/0405 , C01B2203/0415 , C01B2203/043 , C01B2203/046 , C01B2203/0475 , C01B2203/0827 , C01B2203/0838 , C01B2203/1223 , C01B2203/1229 , C01B2203/1235 , C01B2203/143 , C01B2203/82 , C01B2203/84
摘要： A system for production of hydrogen comprises at least one steam reforming zone configured to receive a first fuel and steam to produce a first reformate gas stream comprising hydrogen using a steam reforming process. The system further comprises a mixed reforming zone configured to receive an oxidant to produce a second reformate gas stream comprising hydrogen, wherein the first reformate gas stream is sent to the mixed reforming zone to complete the reforming process.
摘要翻译：用于生产氢气的系统包括至少一个蒸汽重整区，其配置成接收第一燃料和蒸汽，以使用蒸汽重整过程产生包含氢的第一重整产品气流。该系统还包括混合重整区，其配置为接收氧化剂以产生包含氢的第二重整产品气流，其中将第一重整产物气流送至混合重整区以完成重整过程。

8. 发明申请

US20060029534A1 Process for treating ammonia-containing exhaust gases 审中-公开
标题翻译：处理含氨废气的方法
公开(公告)号：US20060029534A1
公开(公告)日：2006-02-09
申请号：US10910637
申请日：2004-08-04
申请人： Boris Eiteneer , Vladimir Zamansky , William Seeker , Glenn England
发明人： Boris Eiteneer , Vladimir Zamansky , William Seeker , Glenn England
IPC分类号： B01D53/58
CPC分类号： B01D53/8634 , B01D2251/102 , B01D2255/102 , B01D2257/406
摘要： A method for reducing ammonia emissions in combustion exhaust gases and other waste streams using an oxidation catalyst, whereby unreacted ammonia (ammonia “slip”) is reduced downstream of a Selective Catalytic Reduction (“SCR”) system simultaneously with the reduction of other gaseous pollutants. The invention utilizes a noble metal-based catalyst, such as Pt, Pd or Ru, such that the ammonia is oxidized in the presence of oxygen to a species having a higher oxidation state of nitrogen, preferably elemental nitrogen N2. The efficiency of the process can be increased by optimizing the catalyst operating conditions and adjusting the temperature and space velocity, or the position of the metal-based catalyst relative to the SCR system.
摘要翻译：一种使用氧化催化剂减少燃烧废气和其他废物流中的氨排放的方法，由此在选择性催化还原（SCR））系统的下游减少未反应的氨（氨“滑”）同时减少其它气体污染物。本发明使用贵金属类催化剂，例如Pt，Pd或Ru，使得氨在氧气存在下被氧化成具有较高氧化态氮的物质，优选氮元素N 2， SUB>。可以通过优化催化剂操作条件并调节温度和空间速度或金属基催化剂相对于SCR系统的位置来提高该方法的效率。

9. 发明申请

US20060021554A1 Mercury reduction system and method in combustion flue gas using staging 有权
公开(公告)号：US20060021554A1
公开(公告)日：2006-02-02
申请号：US11237949
申请日：2005-09-29
申请人： Vitali Lissianski , Peter Maly , William Seeker , Roy Payne , Vladimir Zamansky , Loc Ho
发明人： Vitali Lissianski , Peter Maly , William Seeker , Roy Payne , Vladimir Zamansky , Loc Ho
IPC分类号： F23J15/00 , B01D53/02
CPC分类号： B01D53/64 , B01D53/02 , B01D53/10 , B01D2253/102 , B01D2257/602 , F23C6/045 , F23C2201/101 , F23C2201/30 , F23J15/006 , F23J15/022 , F23J2215/60 , F23J2219/40
摘要： A method to reduce mercury in gas emissions from the combustion of coal is disclosed. Mercury emissions can be reduced by staging combustion process and/or reducing boiler excess oxygen. Fly ash formed under combustion staging conditions is more reactive towards mercury than fly ash formed under typical combustion conditions. Reducing boiler excess oxygen can also improve ability of fly ash to adsorb mercury.

10. 发明申请

US20050129600A1 Product and process to reduce mercury emission 审中-公开
标题翻译：减少汞排放的产品和工艺
公开(公告)号：US20050129600A1
公开(公告)日：2005-06-16
申请号：US11045389
申请日：2005-01-31
申请人： William Lanier , Charles Booth , Vitali Lissianski , Vladimir Zamansky , Peter Maly , William Seeker
发明人： William Lanier , Charles Booth , Vitali Lissianski , Vladimir Zamansky , Peter Maly , William Seeker
IPC分类号： B01D53/64
CPC分类号： B01D53/64
摘要： In a method to decrease emission of mercury, a factor is selected to control a combustion process to generate a flue gas comprising fly ash with enhanced unburned carbon; the combustion process is controlled according to a factor selected from reburning fuel, flue gas temperature, OFA injection, coal particle size, LNB flow, LNB design, combustion zone air, stoichiometric ratio of fuel, fuel/air mixing in a primary combustion zone and fuel/air mixing in a secondary combustion zone to produce the flue gas comprising fly ash with enhanced unburned carbon and to vaporize mercury; and the flue gas is allowed to cool to collect fly ash with enhanced unburned carbon with absorbed mercury. A system to decrease emission of mercury; comprises a combustion zone that is controlled to generate a flue gas comprising fly ash with enhanced unburned carbon and that produces vaporized mercury; and a post combustion zone to cool the flue gas to collect fly ash with enhanced unburned carbon with absorbed mercury.
摘要翻译：在减少汞的排放的方法中，选择一个因素来控制燃烧过程以产生包含具有增强的未燃碳的飞灰的烟道气; 燃烧过程根据燃料重新燃烧，烟气温度，OFA注入，煤粒度，LNB流量，LNB设计，燃烧区空气，燃料的化学计量比，主燃烧区中的燃料/空气混合，以及在二次燃烧区域中的燃料/空气混合以产生包含具有增强的未燃烧碳的飞灰和蒸发汞的烟道气; 并且允许烟道气冷却以收集具有吸收的汞的增强的未燃碳的飞灰。减少汞排放的制度; 包括燃烧区，其被控制以产生包含具有增强的未燃烧碳的飞灰和产生汽化的汞的烟道气; 和一个后燃烧区域，用于冷却烟气以收集具有吸收的汞的增强的未燃烧碳的飞灰。

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