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1. 发明公开

EP3533904A1 HYDROGEN PRODUCTION MICROELECTRODE OPTICAL FIBER, OPTICAL CABLE, AND HYDROGEN PRODUCTION DEVICE FOR LIGHT SUPPLEMENTARY ELECTROLYSIS OF WATER 审中-公开
公开(公告)号：EP3533904A1
公开(公告)日：2019-09-04
申请号：EP17864147.8
申请日：2017-08-07
申请人： Zhongying Changjiang International New Energy Investment Co., Ltd.
发明人： CHEN, Yilong , ZHANG, Yanfeng , TAO, Leiming , DU, Fuying , ZHOU, Huanhuan , ZHENG, Xingcai
IPC分类号： C25B1/04 , C25B9/00
摘要： A hydrogen production microelectrode optical fiber (1), optical cable (11), and hydrogen production device for light supplementary electrolysis of water. The microelectrode optical fiber (1) comprises a light guide core (2). The light guide core (2) has at least a first light guide section (A) and a second light guide section (B); in the first light guide section (A), the light guide core (2) is sequentially provided with a light absorption layer (3), an inner electrode layer (4), an insulating layer (5), a void layer (6), a proton exchange membrane (8) and an outer electrode layer (9) from inside to outside; and in the second light guide section (B), the light guide core (2) is provided with a conductive layer (10) that is connected with the inner electrode layer (4). The hydrogen production optical cable (11) comprises a protective casing (12) and microelectrode optical fibers (1) that are encapsulated and bundled therein. The hydrogen production device comprises an electrolyte bath (13), a hydrogen production optical cable (11), an inner electrode bus, an outer electrode bus, and an optical fiber distributing device. Each microelectrode optical fiber (1) in the hydrogen production optical cable (11) is distributed in the electrolyte (14); and the outer electrode layer (9) and the conductive layer (10) in each microelectrode optical fiber (1) are respectively connected with the inner electrode bus and the outer electrode bus. The hydrogen production device uses solar energy as a supplement to electric energy, effectively reducing electric energy consumption, increasing the space-time yield of hydrogen.

2. 发明公开

EP3088360A1 METHOD FOR PRODUCING NANO SILICON DIOXIDE AND NANO CALCIUM CARBONATE BY USING RICE HULL ASH AND FLUE GAS OF BIOMASS POWER PLANT 审中-公开
标题翻译：用于生产纳米氧化硅和纳米钙BY饭碗ASH和烟雾生物质电厂
公开(公告)号：EP3088360A1
公开(公告)日：2016-11-02
申请号：EP14874949.2
申请日：2014-11-12
申请人： Zhongying Changjiang International New Energy Investment Co. Ltd.
发明人： CHEN, Yilong , ZHANG, Yanfeng , ZHUO, Zhijiu , ZHENG, Xingcai , FANG, Zhangjian , TAO, Leiming , CHENG, Yuting
IPC分类号： C01B33/12 , C01F11/18 , B82Y30/00
CPC分类号： C01B33/18 , B82Y30/00 , B82Y40/00 , C01B33/12 , C01F11/18 , C01F11/181 , C01F11/183 , C01P2004/64 , C01P2006/80
摘要： Provided is a method for producing nano silicon dioxide and nano calcium carbonate by using rice hull ash and flue gas of a biomass power plant. The method comprises: adding the rice hull ash into a sodium hydroxide solution, fully reacting at the temperature of 95-100 °C for 3-4 hours, and performing filtration; adding water into a filtrate to dilute the filtrate, controlling sodium silicate in a system to be 8-15 wt% in silicon dioxide, heating to 60-80 °C, adding a dispersing agent, continuously feeding the flue gas of the biomass power plant under a normal pressure condition, stirring to react for 2-4 hours to obtain the nano silicon dioxide; mixing the filtrate and a washing liquid, adding a calcium hydroxide solution at the temperature of 50-70 °C, and stirring to react for 0.5-2 hours to obtain the nano calcium carbonate. The particle sizes of the silicon dioxide product and the calcium carbonate product which are obtained by the method are extremely small and can both reach the nano level.
摘要翻译：提供了一种用于通过使用稻壳灰和生物质电厂的烟道气产生纳米二氧化硅和纳米碳酸钙的方法。该方法包括：将所述稻壳灰到氢氧化钠溶液中，在充分的95-100℃下进行3-4小时的温度下反应，并进行过滤; 将水加入滤液稀释滤液，控制硅酸钠中的系统是在二氧化硅8-15重量％，加热至60-80℃，加入分散剂，连续进料生物质电厂的烟道气在常压条件下，搅拌2-4小时，以获得所述纳米二氧化硅反应; 混合滤液和洗涤液，添加在50-70℃的温度下氢氧化钙溶液中，并在搅拌下反应0.5-2小时，得到纳米碳酸钙。其是由所述方法得到的二氧化硅产品和碳酸钙产物的颗粒大小是非常小的，并且可以达到这两种纳米级。

4. 发明公开

EP3093271A1 APPARATUS AND METHOD FOR INCREASING BIOMASS PYROLYSIS AND GAS PRODUCTION SPEED AND OBTAINING NANO-SCALE SILICA MATERIAL 审中-公开
标题翻译：设备和方法增加天然气生产和BIOMASSEPYROLYSE速度和纳米级二氧化硅的提取
公开(公告)号：EP3093271A1
公开(公告)日：2016-11-16
申请号：EP15733305.5
申请日：2015-01-23
申请人： Zhongying Changjiang International New Energy Investment Co., Ltd
发明人： CHEN, Yilong , ZHANG, Yanfeng , HAN, Xu , LI, Hong , TAO, Leiming
IPC分类号： C01B33/12 , C10B53/02 , C10B57/10
CPC分类号： C01B33/18 , C01B33/181 , C10B47/22 , C10B53/02 , C10B57/005 , C10B57/10 , C10L3/00 , C10L2290/02 , C10L2290/06 , F22G1/02 , Y02E50/14 , Y02P20/129 , Y02P20/136 , Y02P20/145
摘要： The present invention provides an apparatus and a method for increasing a biomass pyrolysis and gas production speed and obtaining a nano-scale silica material. The apparatus comprises a spiral feeding apparatus, a pretreatment stirrer, a pyrolysis apparatus, a combustion apparatus, a steam generator and a calcination apparatus. A biomass raw material is sent to the pretreatment stirrer through the spiral feeding apparatus. The biomass raw material after stirring is mixed with superheated steam generated by the steam generator and enters the pyrolysis apparatus. Combustible gas separated out from the pyrolysis apparatus enters the combustion apparatus for combustion. Hot flue gas generated by combustion in the combustion apparatus heats the steam generator to generate the superheated steam. Ash discharged from an ash outlet in a lower part of the pyrolysis apparatus enters the calcination apparatus for calcination. The present invention uses the superheated steam to heat and dry the biomass raw material, and is faster than a dry speed of a method where the biomass raw material is dried by hot air in a same temperature, thus greatly increasing a pyrolysis gas separating-out speed of a system compared with a pyrolysis gas separating-out speed of a conventional system and a heat value of produced gas.
摘要翻译：本发明提供的装置和用于增加生物质热解和气体生产速度和获得纳米级二氧化硅材料的方法。该装置包括一个螺旋进给装置，一个预处理搅拌器，热解设备，燃烧装置，蒸汽发生器和焙烧装置。生物质原料通过螺旋馈电装置发送至预处理搅拌器。搅拌后，生物质原料是混合由蒸汽发生器产生的过热蒸汽，并进入热解设备。从热解装置中分离出来的可燃气体进入燃烧用燃烧装置。在燃烧装置的燃烧所产生的热烟道气加热所述蒸汽发生器以产生所述过热蒸汽。从灰中排出的热解设备的下部到出口灰进入煅烧煅烧装置。本发明使用的过热蒸汽以加热和干燥所述的生物质原料，并且比的方法的干燥速度，其中所述生物质原料通过热空气在相同的温度下干燥，因而大大增加热解气体中分离出较快的系统的速度与常规系统的热分解气体分离出速度和所产生的气体的热值相比。

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