利索-全球专利检索

  1. 登录
  2. 注册

搜索结果

22 条记录 (耗时 0.03 秒)

    WASTEWATER TREATMENT DEVICE
    2.
    发明申请
    WASTEWATER TREATMENT DEVICE 有权
    废水处理装置

    公开(公告)号：US20140311959A1

    公开(公告)日：2014-10-23

    申请号：US14358054

    申请日：2012-04-03

    申请人： Kazuhide Kamimura ,  Makoto Ishino ,  Shigeru Yoshioka ,  Hozumi Otozai ,  Seiichi Terakura ,  Hideo Suzuki ,  Gaku Kondo

    发明人： Kazuhide Kamimura ,  Makoto Ishino ,  Shigeru Yoshioka ,  Hozumi Otozai ,  Seiichi Terakura ,  Hideo Suzuki ,  Gaku Kondo

    IPC分类号： C02F9/00 ,  C02F1/70 ,  C02F3/00 ,  C02F1/52

    CPC分类号： C02F1/52 ,  C02F1/441 ,  C02F1/4695 ,  C02F1/5245 ,  C02F3/12 ,  C02F3/121 ,  C02F3/1273 ,  C02F9/00 ,  C02F2001/5218 ,  C02F2101/14 ,  C02F2101/20 ,  C02F2101/32 ,  C02F2303/24 ,  Y02W10/15

    摘要： Provided is a wastewater treatment device that can reduce the fluoride ion concentration in industrial wastewater to improve the recovery rate of purified water. A wastewater treatment device (1) includes a biological treatment unit (3) that decomposes and eliminates organic matter in wastewater by means of microorganisms, and a desalinization unit (4) that is provided downstream of the biological treatment unit (3) and eliminates salt-forming ionic components from within the wastewater. A pretreatment unit (2), which removes components, such as heavy metals or oil contained in the wastewater, which inhibit the function of the biological treatment unit (3) or the desalinization unit (4), is provided upstream of the biological treatment unit (3), and the pretreatment unit (2) is provided with a fluoride concentration reduction unit that reduces the concentration of fluoride ions in the wastewater by eliminating the fluoride ions from within the wastewater.

    摘要翻译： 提供了可以降低工业废水中的氟离子浓度以提高净化水的回收率的废水处理装置。 废水处理装置（1）包括通过微生物分解和消除废水中的有机物的生物处理装置（3），以及设置在生物处理装置（3）下游并消除盐的脱盐装置（4） 在废水中形成离子成分。 在生物处理单元的上游设置有去除抑制生物处理单元（3）或脱盐单元（4）的功能的废水中含有的重金属或者重油等成分的预处理单元（2） （3），并且预处理单元（2）设置有氟化物浓度降低单元，其通过从废水中排除氟离子来降低废水中的氟离子的浓度。

    WASTEWATER TREATMENT DEVICE
    4.
    发明申请
    WASTEWATER TREATMENT DEVICE 有权
    废水处理装置

    公开(公告)号：US20140319031A1

    公开(公告)日：2014-10-30

    申请号：US14358169

    申请日：2012-04-10

    申请人： Kazuhide Kamimura ,  Takuhiro Maeda ,  Morikata Nishida ,  Kosuke Shigiishi ,  Seiichi Terakura ,  Hideo Suzuki ,  Gaku Kondo

    发明人： Kazuhide Kamimura ,  Takuhiro Maeda ,  Morikata Nishida ,  Kosuke Shigiishi ,  Seiichi Terakura ,  Hideo Suzuki ,  Gaku Kondo

    IPC分类号： C02F3/00 ,  C02F3/04 ,  C02F3/12

    CPC分类号： C02F3/006 ,  C02F1/32 ,  C02F1/4604 ,  C02F1/4608 ,  C02F1/66 ,  C02F3/04 ,  C02F3/06 ,  C02F3/1226 ,  C02F3/1268 ,  C02F3/1273 ,  C02F2103/34 ,  C02F2209/001 ,  C02F2209/08 ,  C02F2209/20 ,  C02F2209/40 ,  Y02W10/15

    摘要： A wastewater treatment device includes a first biological treatment device (10) that treats wastewater through a membrane-separated activated sludge method; a second biological treatment device (20) that treats wastewater through a biofilm method; measurement units (31, 32) that measure load concentration and flow rate in the wastewater flowing upstream of the first biological treatment device (10) and the second biological treatment device (20); and a control unit (30) that calculates a load quantity from the load concentration and the flow rate, determines, according to the load quantity, a distribution ratio between a flow rate of the wastewater supplied to the first biological treatment device (10) and a flow rate of the wastewater supplied to the second biological treatment device (20), and adjusts the flow rate of the wastewater supplied to the first biological treatment device (10) and the second biological treatment device (20), based on the distribution ratio.

    摘要翻译： 废水处理装置包括通过膜分离的活性污泥法处理废水的第一生物处理装置（10）; 通过生物膜方法处理废水的第二种生物处理装置（20）; 测量单元（31,32），其测量在所述第一生物处理装置（10）和所述第二生物处理装置（20）上游流动的废水中的负荷浓度和流量; 以及根据负荷浓度和流量计算负荷量的控制单元（30），根据负荷量，确定供给到第一生物处理装置（10）的废水的流量与 供给到第二生物处理装置（20）的废水的流量，基于分配比例调节供给到第一生物处理装置（10）和第二生物处理装置（20）的废水的流量 。

    SACCHARIDE-SOLUTION PRODUCING APPARATUS, FERMENTATION SYSTEM, SACCHARIDE-SOLUTION PRODUCING METHOD, AND FERMENTATION METHOD
    6.
    发明申请
    SACCHARIDE-SOLUTION PRODUCING APPARATUS, FERMENTATION SYSTEM, SACCHARIDE-SOLUTION PRODUCING METHOD, AND FERMENTATION METHOD 有权
    生产装置，发酵系统，生产方法和发酵方法的方法

    公开(公告)号：US20120315677A1

    公开(公告)日：2012-12-13

    申请号：US13578116

    申请日：2011-01-13

    申请人： Minoru Genta ,  Seiichi Terakura ,  Hideo Suzuki ,  Gaku Kondo ,  Michio Nishiyama

    发明人： Minoru Genta ,  Seiichi Terakura ,  Hideo Suzuki ,  Gaku Kondo ,  Michio Nishiyama

    IPC分类号： C12P19/02 ,  C12P7/14 ,  B01J8/00 ,  C12M1/00

    CPC分类号： C12P19/14 ,  C12M21/12 ,  C12M43/02 ,  C12M45/02 ,  C12M45/09 ,  C12M45/20 ,  C12P7/10 ,  C12P19/02 ,  C12P2201/00 ,  C12P2203/00 ,  C13K1/02 ,  Y02E50/16 ,  Y02T50/678

    摘要： A saccharide-solution producing apparatus 11A according to the present invention is a saccharide-solution producing apparatus for producing a saccharide solution 22 derived from a carbohydrate-based material 21, and includes a saccharide-solution controlling unit 15A that controls the saccharide solution derived from the carbohydrate-based material 21, a cellulosic biomass saccharifying unit 16 that saccharifies hydrothermally treated biomass obtained by hydrothermally decomposing a cellulosic biomass material 35 that contains a lignin component and a hemicellulose component, and produces a diluted saccharide solution 37, and a diluted-saccharide-solution supply pipe L11 that mixes the diluted saccharide solution 37 produced by the cellulosic biomass saccharifying unit 16 into the saccharide-solution controlling unit 15A. With this configuration, it is possible to improve production efficiency of the saccharide solution 22 and to realize cost reduction.

    摘要翻译： 本发明的糖溶液生成装置11A是由碳水化合物系材料21制造的糖溶液22的糖溶液制造装置，其具有控制来源于糖类的物质的糖溶液的糖溶液控制部15A， 基于碳水化合物的材料21，将通过水热分解包含木质素成分和半纤维素成分的纤维素生物质材料35得到的水热处理生物质进行糖化并生成稀释的糖溶液37的纤维素生物质糖化单元16和稀释的糖类 将由纤维素生物质糖化单元16生成的稀释的糖溶液37与糖溶液控制单元15A混合的溶液供给管L11。 通过这种结构，可以提高糖溶液22的生产效率，实现成本降低。

    BIOMASS HYDROTHERMAL DECOMPOSITION APPARATUS, METHOD THEREOF, AND ORGANIC MATERIAL PRODUCTION SYSTEM USING BIOMASS MATERIAL
    7.
    发明申请
    BIOMASS HYDROTHERMAL DECOMPOSITION APPARATUS, METHOD THEREOF, AND ORGANIC MATERIAL PRODUCTION SYSTEM USING BIOMASS MATERIAL 有权
    生物质水热分解装置及其方法，以及使用生物质材料的有机材料生产系统

    公开(公告)号：US20100184176A1

    公开(公告)日：2010-07-22

    申请号：US12443515

    申请日：2008-09-19

    申请人： Isao Ishida ,  Seiichi Terakura ,  Hideo Suzuki ,  Seiji Kobayashi

    发明人： Isao Ishida ,  Seiichi Terakura ,  Hideo Suzuki ,  Seiji Kobayashi

    IPC分类号： C12P7/10 ,  C12M1/00 ,  C12M1/02

    CPC分类号： B01D11/0226 ,  B09B3/00 ,  B09B3/0083 ,  C08B37/0057 ,  C08H6/00 ,  C10L5/44 ,  C10L9/086 ,  C12M21/12 ,  C12M45/02 ,  C12M45/20 ,  C12P7/10 ,  C12P2201/00 ,  Y02E50/10 ,  Y02E50/16 ,  Y02E50/17 ,  Y02E50/30

    摘要： A biomass hydrothermal decomposition apparatus includes, a biomass feeder (31) that feeds biomass material (11) under normal pressure to under increased pressure, a hydrothermal decomposition device (42A) that allows the fed biomass material (11) to be gradually moved inside a device main body (42A) from either end thereof in a consolidated condition, and also allows hot compressed water (15) to be fed from an other end of a feed section for the biomass material into the main body (42A), so as to cause the biomass material (11) and the hot compressed water (15) to countercurrently contact with each other and undergo hydrothermal decomposition, and that elutes a lignin component and a hemicellulose component into the hot compressed water, so as to separate the lignin component and the hemicellulose component from the biomass material (11); and a biomass discharger (51) that discharges, from the side where the hot compressed water is fed into the device main body, a biomass solid residue (17) under increased pressure to under normal pressure.

    摘要翻译： 生物质热液分解装置包括在常压下在增压下进料生物质材料（11）的生物质进料器（31），使得所供给的生物质材料（11）能够逐渐移动到内部的水热分解装置（42A） 装置主体（42A），并且还允许将热压缩水（15）从用于生物质材料的进料部分的另一端进料到主体（42A）中，以便 使得生物质材料（11）和热压缩水（15）彼此逆流接触并进行水热分解，并将木质素组分和半纤维素组分洗脱到热压缩水中，以将木质素组分和 来自生物质材料（11）的半纤维素组分; 以及将生物质固体残渣（17）在加压下排出到正常压力下的从生物质固体残渣（17）排出的生物质排出器（51）。

    Biomass hydrothermal decomposition apparatus, temperature control method thereof, and organic raw material production system using biomass material
    8.
    发明授权
    Biomass hydrothermal decomposition apparatus, temperature control method thereof, and organic raw material production system using biomass material 有权
    生物质水热分解装置及其温度控制方法以及使用生物质材料的有机原料生产系统

    公开(公告)号：US09102956B2

    公开(公告)日：2015-08-11

    申请号：US13132040

    申请日：2010-03-10

    申请人： Minoru Genta ,  Ryosuke Uehara ,  Hideo Suzuki ,  Seiichi Terakura

    发明人： Minoru Genta ,  Ryosuke Uehara ,  Hideo Suzuki ,  Seiichi Terakura

    IPC分类号： C12M1/40 ,  B01J19/00 ,  C08B15/00 ,  C12P7/10 ,  C10L1/02

    CPC分类号： C12P7/10 ,  C10G2300/1014 ,  C10G2300/805 ,  C10L1/02 ,  Y02E50/16 ,  Y02P30/20

    摘要： A biomass hydrothermal decomposition apparatus that feeds a solid biomass material 11 from one side of an apparatus body 42, feeds hot water 15 from the other side, to hydrothermally decompose the biomass material 11 while bringing the biomass material 11 into counter contact with the hot water 15, dissolves hot-water soluble fractions in hot water, discharges the hot water to outside from the one side of the apparatus body 42 as a hot-water effluent 16, and discharges a biomass solid (a hot water insoluble) 17 to outside from the other side. The biomass hydrothermal decomposition apparatus includes an effective reaction region A formed from the other side to the one side of the apparatus body 42, in which a feeding temperature of the hot water 15 (for example, 200° C.) is maintained for a predetermined period of time to cause hydrothermal decomposition, and a temperature drop region B in which a temperature is rapidly dropped to a temperature (for example, 140° C.) at which the hot-water soluble fractions are not excessively decomposed (for example, from 200° C. to 140° C.), immediately after it is out of the effective reaction region A.

    摘要翻译： 从装置本体42的一侧供给固体生物质材料11的生物质热液分解装置从另一侧供给热水15，使生物质材料11热水分解，同时使生物质材料11与热水反接触 15，将热水溶性部分溶解在热水中，将热水从装置主体42的一侧作为热水流出物16排出到外部，将生物质固体（不溶于热水）17排出到外部 另一边。 生物质热液分解装置包括从设备主体42的另一侧形成的有效反应区域A，其中将热水15的供给温度（例如200℃）保持在预定的温度 引起水热分解的时间段，以及温度迅速下降到热水可溶级分未过分分解的温度（例如140℃）的温度下降区域B（例如， 200℃至140℃），刚刚离开有效反应区域A.