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. 发明授权

US09623399B2 Method of surface modification of alumina 有权
公开(公告)号：US09623399B2
公开(公告)日：2017-04-18
申请号：US14476762
申请日：2014-09-04
申请人： Sunshine Kaidi New Energy Group Co., Ltd.
发明人： Shenke Zheng , Dechen Song , Xiaodong Zhan
IPC分类号： B01D53/86 , H01B1/12 , B01J21/04 , B01J35/02 , B01J35/10 , C01F7/02
CPC分类号： B01J21/04 , B01J35/023 , B01J35/1014 , B01J35/1038 , B01J35/1042 , B01J35/1061 , C01F7/021 , C01P2004/61 , C01P2006/12 , C01P2006/14 , C01P2006/16 , C01P2006/90
摘要： A method of surface modification of an alumina carrier. The method includes: 1) dissolving a soluble kazoe in deionized water to yield a kazoe aqueous solution; 2) submerging an alumina carrier in the kazoe aqueous solution and drying the alumina carrier in a vacuum environment; 3) placing the dried alumina carrier in a reactor, adding silicon tetrachloride and Grignard reagent dropwise to the reactor, sealing the reactor and heating it to a constant temperature, and maintaining the constant temperature for between 3 and 18 hours, where a volume ratio of the added silicon tetrachloride and the alumina carrier is between 0.5:1 and 5:1, the constant temperature is controlled to be between 160 and 350° C.; and 4) cooling the reactor, filtering, washing, and drying the alumina carrier in the vacuum environment.

2. 发明授权

US09005555B2 Method for preparing solid ruthenium nitrosyl nitrate 有权
标题翻译：固体硝基硝酸硝基钌的制备方法
公开(公告)号：US09005555B2
公开(公告)日：2015-04-14
申请号：US14475547
申请日：2014-09-02
申请人： Sunshine Kaidi New Energy Group Co., Ltd.
发明人： Li Xu , Bo Lai , Dechen Song , Qianqian Liu , Yiming Han
IPC分类号： C01G55/00 , C22B3/00
CPC分类号： C22B11/048 , C01G55/00 , C01P2006/80 , C22B1/005 , C22B7/009 , Y02P10/214 , Y02P10/234
摘要： A method for preparing solid ruthenium nitrosyl nitrate, including: 1) drying a ruthenium-containing spent catalyst, and calcining the spent catalyst, and cooling to room temperature, whereby yielding a ruthenium-containing solid; 2) grinding the ruthenium-containing solid to yield a powder, introducing the powder to a fluidized bed reactor, aerating the fluidized bed reactor with nitrogen or an inert gas, charging hydrogen, whereby yielding ruthenium metal; 3) contacting a mixed gas of ozone and air with the ruthenium metal, whereby yielding gaseous ruthenium tetroxide; 4) introducing the gaseous ruthenium tetroxide into a three-stage absorption plant, whereby yielding an acid solution including ruthenium nitrate; 5) adding a solid of sodium nitrite to the acid solution, stirring, and heating a resulting solution, whereby yielding a solution of ruthenium nitrosyl nitrate; and 6) extracting the solution of ruthenium nitrosyl nitrate with anhydrous ether.
摘要翻译：一种制备固体硝酸亚硝基硝酸盐的方法，包括：1）干燥含钌废废催化剂，煅烧废催化剂，冷却至室温，由此得到含钌固体; 2）研磨含钌固体产生粉末，将粉末引入流化床反应器，用氮气或惰性气体充气流化床反应器，加入氢气，从而产生钌金属; 3）将臭氧和空气的混合气体与钌金属接触，从而产生四氧化四钌; 4）将气态四氧化钌引入三级吸收装置，从而产生包含硝酸钌的酸溶液; 5）向酸溶液中加入亚硝酸钠固体，搅拌并加热所得溶液，由此得到硝酸亚硝基硝酸钌溶液; 和6）用无水乙醚萃取硝酸亚硝基硝酸钌溶液。

3. 发明申请

US20140250931A1 SEASONAL THERMAL ENERGY STORAGE SYSTEM 有权
标题翻译：季节热能储存系统
公开(公告)号：US20140250931A1
公开(公告)日：2014-09-11
申请号：US14285666
申请日：2014-05-23
申请人： SUNSHINE KAIDI NEW ENERGY GROUP CO., LTD
发明人： Yilong CHEN , Shuchuan HU
IPC分类号： F25B27/00 , F24J2/34
CPC分类号： F25B27/007 , F24D11/003 , F24F5/0017 , F24F2005/0025 , F24S60/30 , F25B15/06 , F25B30/04 , Y02A30/272 , Y02A30/277 , Y02B10/20 , Y02B10/24 , Y02B30/62 , Y02E60/147 , Y02E70/30
摘要： A seasonal thermal energy storage system for heat supply and removal, including an energy-storage device, a solar collector, a refrigerating unit, and a water supply device in closed-loop connection to a user terminal. The energy-storage device includes at least a heat source storage pond and a cold source storage pond. The heat source storage pond and the cold source storage pond are connected to water source via first water pumps. The water supply device includes a hot water supply pool connected to the heat source storage pond and a cold water supply pool connected to the cold source storage pond. The solar collector is connected to the heat source storage pond and the hot water supply pool via second water pumps. The refrigerating unit is connected to the hot water supply pool and the cold water supply pool via third water pumps.
摘要翻译：一种用于供热和排除的季节性热能储存系统，包括能量存储装置，太阳能收集器，制冷单元和与用户终端闭环连接的供水装置。储能装置至少包括热源储存池和冷源储存池。热源蓄水池和冷源蓄水池通过第一台水泵连接到水源。供水装置包括连接到热源储存池的热水供应池和连接到冷源储存池的冷水供应池。太阳能集热器通过第二台水泵连接到热源蓄水池和热水供水池。制冷机组通过第三台水泵连接到热水供应池和冷水供水池。

4. 发明授权

US08986632B2 Process for recovery of cobalt, ruthenium, and aluminum from spent catalyst 有权
标题翻译：从废催化剂中回收钴，钌和铝的方法
公开(公告)号：US08986632B2
公开(公告)日：2015-03-24
申请号：US14477935
申请日：2014-09-05
申请人： Sunshine Kaidi New Energy Group Co., Ltd.
发明人： Qianqian Liu , Yiming Han , Dechen Song , Li Xu , Bo Lai
IPC分类号： C22B11/00 , C22B3/00 , C22B11/06 , C22B21/02
CPC分类号： C22B23/0446 , C01F7/142 , C01G51/00 , C01G51/04 , C01G55/004 , C01G55/005 , C01P2006/80 , C22B7/00 , C22B7/009 , C22B11/026 , C22B11/04 , C22B11/048 , C22B11/06 , C22B21/003 , C22B21/02 , C22B23/00 , C22B23/026 , Y02P10/214 , Y02P10/218 , Y02P10/224 , Y02P10/234 , Y02P20/129 , Y02P20/142
摘要： A method for recovering cobalt, ruthenium, and aluminum from spent Co—Ru/Al2O3 catalyst. First, Co—Ru/Al2O3 spent catalyst is subjected to hydrocarbon removal, reaction with hydrogen, and alkali fusion to obtain a slag. The slag is subjected to acid leaching, precipitation of cobalt with oxalic acid or ammonium oxalate, reduction of cobalt oxalate, and dissolution of cobalt metal with nitric acid to obtain Co(NO3)2.6 H2O. The effluent of acid leaching is subjected to reaction with ethanol, filtration to obtain a filtrate and residue, dissolution of the residue with concentrated hydrochloric acid, and vacuum distillation to obtain β-RuCl3.x H2O. Aluminum hydroxide is prepared from the filtrate through carbonation and calcination. The cobalt yield is ≧97%; the ruthenium yield is ≧95%, and the aluminum yield is ≧92%.
摘要翻译：从废Co-Ru / Al2O3催化剂中回收钴，钌和铝的方法。首先，将Co-Ru / Al2O3废催化剂进行烃去除，与氢反应和碱熔融，得到渣。炉渣进行酸浸，用草酸或草酸铵沉淀钴，还原草酸钴，用硝酸溶解钴金属，得到Co（NO 3）2·6H 2 O。将酸浸出液与乙醇反应，过滤，得到滤液和残留物，用浓盐酸溶解残余物，减压蒸馏，得到-RClCl 3·H 2 O。通过碳酸化和煅烧从滤液制备氢氧化铝。钴产率≥97％。钌产率≥95％，铝产率≥92％。

5. 发明申请

US20130125465A1 METHOD AND APPARATUS FOR PYROLYSIS AND GASIFICATION OF BIOMASS 有权
标题翻译：生物量热解和气化的方法和装置
公开(公告)号：US20130125465A1
公开(公告)日：2013-05-23
申请号：US13745861
申请日：2013-01-20
申请人： SUNSHINE KAIDI NEW ENERGY GROUP CO., LTD.
发明人： Hongming TANG , Yanfeng ZHANG , Yilong CHEN
IPC分类号： C10J3/46
CPC分类号： C10J3/46 , C10J3/12 , C10J3/20 , C10J3/48 , C10J3/66 , C10J3/72 , C10J3/721 , C10J3/84 , C10J2300/0916 , C10J2300/093 , C10J2300/094 , C10J2300/0993 , Y02P20/145
摘要： A method for pyrolysis and gasification of biomass by: a) providing a gasifier and a pyrolysis furnace; heating and introducing a solid particle, or a plurality thereof, into the gasifier and the pyrolysis furnace; b) grinding and feeding the biomass into the pyrolysis furnace while spraying saturated water vapor into the pyrolysis furnace, contacting the biomass with the saturated water vapor at 500-800° C. to yield crude synthetic gas and ash including coke; c) separating the ash, heating the solid particle, and transporting the solid particle into the gasifier; d) cooling the ash, and separating the coke; and e) introducing the crude synthetic gas into the gasifier, transporting the coke into the gasifier while spraying saturated water vapor into the gasifier, contacting the coke and the crude synthetic gas with the saturated water vapor at 1200-1600° C.
摘要翻译：一种通过以下方式热解和气化生物质：a）提供气化炉和热解炉; 将固体颗粒或其多个加热并引入气化器和热解炉中; b）将生物质研磨并进料到热解炉中，同时将饱和水蒸气喷入热解炉中，使生物质与饱和水蒸气在500-800℃接触，得到粗合成气和灰分，包括焦炭; c）分离灰分，加热固体颗粒，并将固体颗粒输送到气化器中; d）冷却灰分，分离焦炭; 和e）将粗合成气体引入气化器中，将焦炭输送到气化器中，同时将饱和水蒸汽喷射到气化器中，使焦炭和粗合成气体与饱和水蒸汽在1200-1600℃接触。

6. 发明授权

US09631846B2 Seasonal thermal energy storage system 有权
公开(公告)号：US09631846B2
公开(公告)日：2017-04-25
申请号：US14285666
申请日：2014-05-23
申请人： SUNSHINE KAIDI NEW ENERGY GROUP CO., LTD
发明人： Yilong Chen , Shuchuan Hu
IPC分类号： F25B27/00 , F24D11/00 , F24J2/34 , F24F5/00 , F25B15/06 , F25B30/04
CPC分类号： F25B27/007 , F24D11/003 , F24F5/0017 , F24F2005/0025 , F24S60/30 , F25B15/06 , F25B30/04 , Y02A30/272 , Y02A30/277 , Y02B10/20 , Y02B10/24 , Y02B30/62 , Y02E60/147 , Y02E70/30
摘要： A seasonal thermal energy storage system for heat supply and removal, including an energy-storage device, a solar collector, a refrigerating unit, and a water supply device in closed-loop connection to a user terminal. The energy-storage device includes at least a heat source storage pond and a cold source storage pond. The heat source storage pond and the cold source storage pond are connected to water source via first water pumps. The water supply device includes a hot water supply pool connected to the heat source storage pond and a cold water supply pool connected to the cold source storage pond. The solar collector is connected to the heat source storage pond and the hot water supply pool via second water pumps. The refrigerating unit is connected to the hot water supply pool and the cold water supply pool via third water pumps.

7. 发明授权

US09279169B2 Method for recycling noble metals from Fischer-Tropsch products 有权
标题翻译：从费 - 托产品回收贵金属的方法
公开(公告)号：US09279169B2
公开(公告)日：2016-03-08
申请号：US14578539
申请日：2014-12-22
申请人： SUNSHINE KAIDI NEW ENERGY GROUP CO., LTD.
发明人： Yilong Chen , Jiaqi Jin , Yanfeng Zhang , Kan Song , Xiaodong Zhan , Manyi Jiang
IPC分类号： C07C1/04 , C22B61/00 , C22B11/02 , B01J23/75 , C10G31/09 , C21B15/00 , C22B3/00 , C22B7/00
CPC分类号： C22B61/00 , B01J8/006 , B01J8/007 , B01J8/22 , B01J23/75 , C10G31/09 , C10G2300/1022 , C10G2300/205 , C10G2300/208 , C10G2300/706 , C21B15/00 , C21B2200/00 , C22B7/009 , C22B11/026 , C22B23/04 , Y02P10/214 , Y02W30/54
摘要： A method for recycling a noble metal from Fischer-Tropsch synthesis products. The method includes: 1) filtering a reaction product in a Fischer-Tropsch synthesis reactor by an inner filter; discharging a filtered reaction product to a first filtration buffer tank; separating a gas phase product or a part of a liquid phase product from the reaction product; introducing the liquid-solid two-phase product to a refining filter for product refining; 2) introducing a liquid phase product containing a catalyst slurry to a dynamic filter, collecting the filtered liquid phase product including a waste catalyst and noble metal ions; introducing the liquid phase product to a second filtration buffer tank; and introducing the filtered liquid phase product to the refining filter; and 3) forming a clay filter cake on a filter disk; and refining the products introduced into the refining filter in 1) and 2).
摘要翻译：一种从费 - 托合成产品中回收贵金属的方法。该方法包括：1）通过内部过滤器过滤费 - 托合成反应器中的反应产物; 将过滤的反应产物排放到第一过滤缓冲罐; 从反应产物中分离气相产物或一部分液相产物; 将液固两相产品引入用于产品精炼的精制过滤器; 2）将含有催化剂浆液的液相产物引入动态过滤器，收集包含废催化剂和贵金属离子的过滤液相产物; 将液相产物引入第二过滤缓冲罐; 并将经过滤的液相产物引入精炼过滤器; 和3）在过滤盘上形成粘土滤饼; 并在1）和2）中精炼引入精制过滤器的产品。

8. 发明授权

US08999022B2 Method and system for producing synthetic gas from biomass 有权
标题翻译：从生物质生产合成气的方法和系统
公开(公告)号：US08999022B2
公开(公告)日：2015-04-07
申请号：US13745859
申请日：2013-01-20
申请人： Sunshine Kaidi New Energy Group Co., Ltd.
发明人： Yilong Chen , Hongming Tang , Yanfeng Zhang
IPC分类号： C10J3/46 , C10J3/66 , C10J3/72
CPC分类号： C10J3/46 , C10J3/66 , C10J3/721 , C10J2300/0906 , C10J2300/0916 , C10J2300/094 , C10J2300/0976 , C10J2300/1238 , C10J2300/1884 , C10J2300/1892 , Y02P20/145
摘要： A method for producing synthetic gas from biomass by: a) grinding the biomass, feeding the biomass into a pyrolysis furnace while spraying a first superheated water vapor into the pyrolysis furnace, controlling the temperature of the pyrolysis furnace at 500-800° C., contacting the biomass with the first superheated water vapor for a pyrolysis reaction to yield crude synthetic gas and ash including coke; b) cooling the ash, and separating the coke from the ash; c) transporting the crude synthetic gas and the coke into a gasifier, spraying a second superheated water vapor into the gasifier, controlling the gasifier at an operating temperature of 1200-1600° C., contacting the biomass with the second superheated water vapor for a gasification reaction to yield primary synthetic gas; and d) cooling, removing dust, deacidifying, and desiccating the primary synthetic gas to obtain clean synthetic gas.
摘要翻译：一种从生物质生产合成气的方法，包括：a）研磨生物质，将生物质送入热解炉，同时将第一过热水蒸气喷入热解炉中，将热解炉的温度控制在500-800℃，使生物质与第一过热水蒸汽接触进行热解反应，以产生粗合成气和灰分，包括焦炭; b）冷却灰分，并将焦炭与灰分离; c）将粗合成气和焦炭输送到气化器中，将第二过热水蒸汽喷射到气化器中，在1200-1600℃的操作温度下控制气化器，使生物质与第二过热水蒸气接触气化反应产生初级合成气; 和d）冷却，去除灰尘，脱酸和干燥初级合成气体以获得清洁的合成气体。

9. 发明申请

US20130125464A1 METHOD AND SYSTEM FOR PRODUCING SYNTHETIC GAS FROM BIOMASS 有权
标题翻译：从生物质生产合成气的方法和系统
公开(公告)号：US20130125464A1
公开(公告)日：2013-05-23
申请号：US13745859
申请日：2013-01-20
申请人： SUNSHINE KAIDI NEW ENERGY GROUP CO., LTD.
发明人： Yilong CHEN , Hongming TANG , Yanfeng ZHANG
IPC分类号： C10J3/46
CPC分类号： C10J3/46 , C10J3/66 , C10J3/721 , C10J2300/0906 , C10J2300/0916 , C10J2300/094 , C10J2300/0976 , C10J2300/1238 , C10J2300/1884 , C10J2300/1892 , Y02P20/145
摘要： A method for producing synthetic gas from biomass by: a) grinding the biomass, feeding the biomass into a pyrolysis furnace while spraying a first superheated water vapor into the pyrolysis furnace, controlling the temperature of the pyrolysis furnace at 500-800° C., contacting the biomass with the first superheated water vapor for a pyrolysis reaction to yield crude synthetic gas and ash including coke; b) cooling the ash, and separating the coke from the ash; c) transporting the crude synthetic gas and the coke into a gasifier, spraying a second superheated water vapor into the gasifier, controlling the gasifier at an operating temperature of 1200-1600° C., contacting the biomass with the second superheated water vapor for a gasification reaction to yield primary synthetic gas; and d) cooling, removing dust, deacidifying, and desiccating the primary synthetic gas to obtain clean synthetic gas.
摘要翻译：一种从生物质生产合成气的方法，包括：a）研磨生物质，将生物质送入热解炉，同时将第一过热水蒸气喷入热解炉中，将热解炉的温度控制在500-800℃，使生物质与第一过热水蒸汽接触进行热解反应，以产生粗合成气和灰分，包括焦炭; b）冷却灰分，并将焦炭与灰分离; c）将粗合成气和焦炭输送到气化器中，将第二过热水蒸汽喷射到气化器中，在1200-1600℃的操作温度下控制气化器，使生物质与第二过热水蒸气接触气化反应产生初级合成气; 和d）冷却，去除灰尘，脱酸和干燥初级合成气体以获得清洁的合成气体。

10. 发明申请

US20130125463A1 METHOD AND SYSTEM FOR GASIFICATION OF BIOMASS 有权
标题翻译：生物量气化方法与系统
公开(公告)号：US20130125463A1
公开(公告)日：2013-05-23
申请号：US13745858
申请日：2013-01-20
申请人： SUNSHINE KAIDI NEW ENERGY GROUP CO., LTD.
发明人： Yilong CHEN , Yanfeng ZHANG , Hongming TANG
IPC分类号： C10J3/46
CPC分类号： C10J3/84 , C10J3/20 , C10J3/46 , C10J2200/152 , C10J2300/0906 , C10J2300/0916 , C10J2300/0973 , C10J2300/0976 , C10J2300/1238 , C10J2300/1246 , C10J2300/1653 , C10J2300/1659 , C10J2300/1665 , C10J2300/1693 , C10J2300/1853 , C10J2300/1884 , C10J2300/1892 , C10K1/002 , C10K1/003 , C10K1/02 , C10K1/06 , Y02E20/18 , Y02E50/14 , Y02E50/18 , Y02P20/145
摘要： A method for gasifying biomass. The method includes: a) grinding the biomass, feeding the biomass into a gasifier while spraying superheated water vapor into the gasifier, controlling the gasifier at an operating temperature of 1200-1600° C., contacting the biomass with the superheated water vapor, desiccating, separating volatile matters, pyrolyzing, and gasifying the biomass to produce crude synthetic gas and ash; b) transporting the crude synthetic gas into a spray tower, quenching the crude synthetic gas by spraying water to cool down the crude synthetic gas to a temperature of 650-800° C., condensing a slag and a tar from the crude synthetic gas, dissolving and removing alkali metal oxides and part of acid gas to obtain primary synthetic gas; and c) cooling, dust removing, deacidifying, and desiccating the primary synthetic gas to transform the primary synthetic gas into clean synthetic gas.
摘要翻译：一种气化生物质的方法。该方法包括：a）研磨生物质，将生物质进料到气化器中，同时将过热水蒸汽喷射到气化炉中，在1200-1600℃的操作温度下控制气化器，使生物质与过热水蒸汽接触，干燥分离挥发性物质，热解和气化生物质以产生粗合成气和灰分; b）将粗合成气体输送到喷雾塔中，通过喷洒水将粗合成气体冷却至650-800℃的温度，将粗合成气体冷凝，从粗合成气中冷凝出渣和焦油，溶解和除去碱金属氧化物和一部分酸性气体，得到初级合成气; 和c）冷却，除尘，脱酸和干燥初级合成气体，以将主要合成气体转化成清洁的合成气体。

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