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    • 2. 发明专利
    • Microbial carrier blended with nitrohumate
    • 微生物携带者与NITROHUMATE混合
    • JP2006272171A
    • 2006-10-12
    • JP2005095237
    • 2005-03-29
    • Denka Consult & Eng Co Ltdデンカエンジニアリング株式会社
    • YOSHII TATSUYAICHIHARA JOJIMIZUNO KANEO
    • C02F3/10C02F3/08C12N11/08
    • Y02W10/15
    • PROBLEM TO BE SOLVED: To provide a method for enhancing activity of an attached microbe higher using a rigid microbial carrier for drainage treatment having many communicating gas cavities in a fluid bed drainage treatment method. SOLUTION: The microbial carrier blended with a nitrohumate comprises high density polyethylene and/or polyproylene as a main component, and preferably a rigid thermoplastic foamed body having a communicating air bubble obtained by blending a resin composition blending polystyrene of 2 to 10 mass% with a magnesium salt, a calcium salt or a sodium salt of nitrohumic acid obtained by neutralizing after decomposing low rank coal such as lignite or brown coal with nitric acid of 1 to 15 mass% per the resin composition of 100 pts.mass to carry out expansion molding. COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:提供一种使用刚性微生物载体提高附着微生物的活性的方法,用于在流化床排水处理方法中具有许多连通气体腔的排水处理。 < P>解决方案:与硝酸根合物混合的微生物载体包括高密度聚乙烯和/或聚丙烯作为主要成分,优选具有通过将混合2至10质量份的聚苯乙烯的树脂组合物获得的连通气泡的刚性热塑性发泡体 %的镁盐,钙盐或硝基酸钠盐,其通过在分解低等级煤如褐煤或褐煤之后通过用100重量份的树脂组合物的1至15质量%的硝酸分解中和获得 膨胀成型。 版权所有(C)2007,JPO&INPIT
    • 4. 发明专利
    • Gas transportation apparatus for granular powder
    • 颗粒粉煤气运输装置
    • JPS61136815A
    • 1986-06-24
    • JP25736984
    • 1984-12-07
    • Denka Consult & Eng Co Ltd
    • FUJII SHUZOKOBAYASHI MINORU
    • B65G53/04B65G53/52
    • B65G53/525
    • PURPOSE:To certainly form a plug and avoid closure by installing an intermittently opening and closing apparatus at the terminal of a transportation pipe and transporting the plug by the expansion force of gas due to the intermittent opening and closing of the opening and closing apparatus, in the captioned apparatus for transporting powder in plug form. CONSTITUTION:Pressurized gas 2 is supplied into a pressurizing tank 1 filled with powder, and an intermittently opening and closing apparatus 4 is opened and closed at a time intervals set in a time-interval setting device 5. When the opening and closing apparatus 4 is in closed state, the inside of a transportation pipe 3 is field with gas. When the apparatus 4 is opened, the inside gas sharply expands and is blown-out with powder into a receiving container 7. By the next closing operation, the inside of the tnrasprtation pipe 3 is charged. Plugs are transported by the repetition of the above-described operations. With such constitution, plugs can be certainly formed, and closure can be avoided.
    • 目的:通过在输送管的端子处安装间歇地打开和关闭装置并且由于打开和关闭装置的间歇地打开和关闭而通过气体的膨胀力来运送塞子来肯定地形成塞子并避免闭合, 用于以塞子形式输送粉末的标题装置。 构成:将加压气体2供给到填充有粉末的加压槽1中,并且间歇开闭装置4以设定在时间间隔设定装置5中的时间间隔开闭。当开闭装置4为 在关闭状态下,输送管3的内部为气体。 当装置4打开时,内部气体急剧地膨胀并用粉末吹出到容纳容器7中。通过下一次关闭操作,对管道内部3进行充电。 通过重复上述操作来传送插头。 通过这样的结构,能够可靠地形成插头,能够避免闭合。
    • 5. 发明专利
    • “台湾”生物处理设备
    • JPS60197295A
    • 1985-10-05
    • JP5316584
    • 1984-03-19
    • Denka Consult & Eng Co Ltd
    • KONISHI KOUZOUMORIYAMA TAKASHI
    • C02F3/08C02F3/28
    • Y02W10/15
    • PURPOSE: To enhance purification efficiency, by packing a porous inorg. substance, of which the density is 0.4W1.0g/cm
      3 and the particle size is 3W15mm as a carrier so that the ratio of the static layer volume of the carrier to a "tater- bed" is adjusted to 20W80vol%.
      CONSTITUTION: An upper screen 2a and a lower screen 2b each having a mesh width smaller than the particle size of a carrier are provided in a treating tower or tank 1 in two upper and lower stages. Sewage is introduced from the pipe 5 below the lower screen 2b and air is blown into the sewage through a porous air diffusion disc 4. Oxygen required in sustaining existing microorganisms is supplied by the aeration from the air diffusion disc 4 and the up-and-down fluidization of the carrier is performed. Further, microorganism flocs released from the carrier by sludging due to rising air bubbles in the lower part of the upper screen 2a are added to said upper screen 2a to prevent the clogging thereof. Purified treated water is discharged along with flocs from a drain pipe 6 above the upper screen 2a.
      COPYRIGHT: (C)1985,JPO&Japio
    • 目的:提高净化效率,通过包装多孔inorg。 物质,其密度为0.4-1.0g / cm 3,粒径为3-15mm。 作为载体,使得载体的静态层体积与“加料床”的比率被调节为20-80vol%。 构成:在两个上下两级的处理塔或槽1中设置有具有比载体的粒径小的网格宽度的上筛网2a和下筛网2b。 从下部屏幕2b下方的管道5引入污水,并且空气通过多孔空气扩散盘4吹入污水中。维持现有微生物所需的氧气通过曝气从空气扩散盘4提供, 执行载体的向下流化。 此外,由于上部筛网2a的下部的气泡的上升而通过淤积而从载体释放的微生物絮凝物被添加到上部筛网2a中,以防止其堵塞。 净化后的处理水与来自上部筛网2a上方的排水管6的絮凝物排出。
    • 6. 发明专利
    • Removal of difficultly decomposable cod from waste water
    • 从废水中去除差异不大的COD
    • JPS59189996A
    • 1984-10-27
    • JP6374083
    • 1983-04-13
    • Denka Consult & Eng Co Ltd
    • KONISHI KOUZOUTANIGUCHI KEIJIMIZUNO KANEO
    • C02F1/78C02F9/00
    • PURPOSE: To efficiently remove COD existent in waste water, by biooxidizing waste water in the process of manufacturing thermosetting resin, introducing it into an ozone contact device of specified length, and adding the specified amount of ozone at a pH of 5.8W8.4 to oxidize COD.
      CONSTITUTION: Waste water in the process of manufacturing thermosetting resin is biooxidized and then introduced into an ozone contact device having effective contact length of 2W4m. Hereon, ozone in an amount of 0.6W2.0 by wt. ratio to the amount of COD to be removed existent in water to be treated residing in the ozone contact device is introduced, and ozone oxidation is performed in the neutral zone where the pH of water to be treated is 5.8W8.6. Hence, difficultly decomposable COD existent in the waste water is removed. Since suspended substance as the result of the biooxidation of BOD is mixedly existent in said biooxidized water, it is necessary to preremove the suspended substance by precipitation separation in advance of the ozone oxidation. In addition, it is preferable to adjust the suspended substance to below 10mg/l conjunctly using sand filtration.
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:为了有效去除废水中的COD,在制造热固性树脂的过程中通过生物氧化废水,将其引入特定长度的臭氧接触装置,并在5.8-8.4的pH下加入规定量的臭氧以氧化 COD。 构成:将热固性树脂制造过程中的废水进行生物氧化,然后引入具有2-4m有效接触长度的臭氧接触装置。 这里,臭氧量为0.6-2.0重量% 引入与在臭氧接触装置中存在的待处理水中存在的待除去COD量的比例,并且在要处理的水的pH为5.8-8.6的中性区域中进行臭氧氧化。 因此,废水中存在难分解的COD。 由于作为BOD的生物氧化的结果的悬浊物质混合存在于所述生物氧化水中,因此需要在臭氧氧化之前通过析出分离来除去悬浮物质。 此外,优选使用砂过滤将悬浮物质调节至10mg / l以下。
    • 7. 发明专利
    • Intermittent discharge quantity control method for granular powder
    • 颗粒粉末的间歇放电量控制方法
    • JPS5922819A
    • 1984-02-06
    • JP13113082
    • 1982-07-29
    • Denka Consult & Eng Co Ltd
    • FUJII SHIYUUZOUYANAGIHARA YASUOTAKASE ITARUTANIGUCHI KEIJIKOBAYASHI MINORU
    • B65G53/18B65G53/66
    • B65G53/66
    • PURPOSE:To control the intermittent discharge quantity of granular powder while holding the maximum solid-gas ratio, by supplying the primary gas and the secondary gas in the vicinity of an exhaust nozzle and a transport pipe, respectively and controlling the quantity of the primary gas in case of discharging granular powder from the exhaust nozzle connected to the transport pipe onto a fluid bed. CONSTITUTION:Granular powder is discharged onto a fluid bed 2 from a press-feeding container where an exhaust nozzle 3 connected to a transport pipe 6 is opened. In this case, a booster supply pipe 12 is divided into the secondary pipe 12a and the primary pipe 12b, the secondary pipe 12a being connected to a transport pipe 6, the primary pipe 12b being connected to an exhaust pipe 4 near the exhaust nozzle 3. A part Q3 of booster gas is supplied in order to lower the mixing ratio and pressure loss in the exhaust pipe 4 so that the discharge quantity of granular powder is increased, and Q3 is controlled to regulate the discharge quantity. A valve 15 for controlling the secondary booster quantity Q4 is operated in such a manner as to set up the optimum solid-gas ratio Mc determined in relation to the length of the transport pipe 6. The primary booster quantity Q3 is controlled within 5 to 50% to the total gas quantity Q2 of the booster by a control valve 14.
    • 目的:通过分别在排气喷嘴和输送管附近供给一次气体和二次气体来控制颗粒状粉末的间歇排放量,同时保持最大固体气体比例,并控制一次气体的量 在从与输送管连接的排气喷嘴将粒状粉末排出到流化床上的情况下。 构成:将粒状粉末从与输送管6连接的排气喷嘴3打开的加压容器排出到流化床2上。 在这种情况下,助力供给管12被分成二次管12a和主管12b,二次管12a与输送管6连接,主管12b与排气喷嘴3附近的排气管4连接 为了降低排气管4的混合比和压力损失,供给增压气体的第三部分Q3,使得粒状粉末的排出量增加,控制Q3来调节排出量。 用于控制二次助力量Q4的阀15以设定相对于输送管6的长度确定的最佳固气比Mc的方式操作。主增压量Q3被控制在5至50 %,通过控制阀14与增压器的总气体量Q2成比例。
    • 8. 发明专利
    • Treatment of filthy water and apparatus therefor
    • 净水器及其设备的处理
    • JPS58183988A
    • 1983-10-27
    • JP6649482
    • 1982-04-21
    • Denka Consult & Eng Co Ltd
    • KONISHI KOUZOUMIZUNO KANEOISHIDA SHIYOUJI
    • C02F3/06C02F3/12
    • Y02W10/15
    • PURPOSE: To efficiently remove BOD and COD components, by supplying precipitated activated sludge to a flocculating-precipitating tank by a withdrawing means, adding a cationic macromolecular flocculant to change said sludge into coarse particles, and continously returning it to an aerating tank.
      CONSTITUTION: The apparatus for the treatment of filthy water is constituted by a stationary-bed aerating tank A, a precipitating tank B, a flocculating-precipitating tank C and a means D for supplying a macromolecular flocculant. At first, filthy water is supplied from a tank for reserving filthy water through a distributor 1 for uniformly supplying filthy water and piping 2 to the aerating tank A. Into the precipitating tank B, the filthy water is introduced from an discharging opening 10 at the upper part of the aerating tank A through piping and a feed well 13 provided inside the main body 12 of the precipitating tank B. It is then supplied through piping 16 to the flocculating-precipitating tank C by the operation of a pump 14. In the flocculating-precipitating tank C, a cationic macromolecular flocculant is added at a ratio of 0.05W1wt% based on activated sludge from an upper part.
      COPYRIGHT: (C)1983,JPO&Japio
    • 目的:为了有效地去除BOD和COD成分,通过提取方法将沉淀的活性污泥提供给絮凝沉淀池,加入阳离子大分子絮凝剂将污泥变成粗颗粒,并连续返回到充气罐。 构成:用于处理污水的装置由固定床充气罐A,沉淀池B,絮凝沉淀​​罐C和用于供应大分子絮凝剂的装置D构成。 首先,从用于通过分配器1储存污水的罐中提供肮脏的水,以将污水和管道2均匀地供给到充气罐A.进入沉淀池B中,污水从排出口10引入 通风管A的上部和设置在沉淀池B的主体12的内部的进料井13,然后通过管道16通过泵14的运转而供给到絮凝析出罐C.在 絮凝沉淀槽C,以上述部分的活性污泥为0.05〜1wt%的比例添加阳离子大分子絮凝剂。
    • 9. 发明专利
    • Method of detecting abnormality of transportation pipeline, method of monitoring condition and safety of transport, and abnormality detector
    • 检测运输管道异常的方法,监测条件和运输安全的方法和异常检测器
    • JP2003065944A
    • 2003-03-05
    • JP2001256457
    • 2001-08-27
    • Denka Consult & Eng Co LtdSumitomo Metal Ind Ltdデンカエンジニアリング株式会社住友金属工業株式会社
    • KAWAMOTO MASASHIANDO HISANORIWATANABE HARUO
    • G01N19/08B65G53/52C21C5/46F16L55/00
    • PROBLEM TO BE SOLVED: To enable an article transportation facility, such as the pneumatic powder feeding facility, etc., of a converter to surely prevent the occurrence of a secondary accident or disaster caused by the leakage of a transported article or fluid by surely detecting in an early stage such a deficit as the perforation of a transport pipeline, such as a pneumatic pipeline, liquid feed pipeline, etc., caused by wear, corrosion, etc., by means of a relatively simple inexpensive device.
      SOLUTION: Double-pipe abnormality detectors 20 for transportation pipeline are installed to the transporting direction changing sections 5a, 5b, and 5c which are the specific wearing sections of the pneumatic pipeline 5 of the pneumatic powder feeding facility. The pressure P
      2 between the inner pipe 21 and outer pipe 22 of each detector 20 is preset to meet P
      3 >P
      2 >P
      1 (wherein, P
      3 is the internal pressure of the pipeline 5 during pneumatic feeding and P
      1 is the internal pressure of the pipeline 5 while the pneumatic feeding is stopped) and always monitored. When the measured P
      2 value rises (P
      2 becomes equal to P
      3 during pneumatic feeding or drops (P
      2 becomes equal to P
      1 while pneumatic feeding is stopped), it is discriminated that the pneumatic feeding pipeline is perforated by corrosion.
      COPYRIGHT: (C)2003,JPO
    • 要解决的问题:为了使转炉的气动粉末给料设备等的物品输送设备能够可靠地防止由运输物品或流体的泄漏引起的二次事故或灾难的发生, 在早期阶段,通过相对简单的廉价装置,由磨损,腐蚀等引起的诸如气动管道,液体供给管线等的运输管线的穿孔的缺陷。 解决方案:作为气动粉末供给设备的气动管路5的具体磨损部分的输送方向改变部分5a,5b和5c安装用于运输管线的双管异常检测器20。 每个检测器20的内管21和外管22之间的压力P2预设为满足P3> P2> P1(其中,P3是气动进给期间管道5的内部压力,P1是管道5的内部压力 而气动进给停止)并且始终被监视。 当测量的P2值上升时(气动送料或液滴下P2变为P3)(气动送料停止时P2变为P1),则鉴别出气动送料管道被腐蚀穿孔。
    • 10. 发明专利
    • Treatment of waste water
    • 废水处理
    • JPS6161694A
    • 1986-03-29
    • JP18278184
    • 1984-09-03
    • Denka Consult & Eng Co Ltd
    • KONISHI KOZOMIZUNO KANEO
    • C02F3/02C02F3/06C02F3/08
    • Y02W10/15
    • PURPOSE: To increase the efficiency of the titled process by regulating raw water to the pH that the treatment efficiency becomes maximum before introducing the raw water into a treatment apparatus and thereafter introducing it into a biological treatment apparatus.
      CONSTITUTION: The pH value that the treatment efficiency becomes maximum is obtained in every waste water by means of preliminary experiment and the pH of raw water is regulated to the obtained pH and thereafter it is treated. In case of providing two or more stages of treatment vessels, COD contained in treated water of each stage on and after the second stage is adopted as the indication and raw water is passed so that the pH in which COD is made minimum becomes optimum pH. In regulating pH of raw water, NaOH or NH
      4 OH is used as alkali and inorganic acid is used as acid.
      COPYRIGHT: (C)1986,JPO&Japio
    • 目的:通过将原水调节至处理效率达到最大值,然后将原水引入处理设备中,然后将其引入生物处理设备中,从而提高标准工艺的效率。 构成:通过初步实验,在各废水中获得处理效率最大的pH值,将原水的pH调节至所得pH值,然后进行处理。 在提供两级或更多级处理容器的情况下,采用第二阶段和第二阶段后处理水中所含的COD,作为指标,原水通过,使COD最低的pH达到最佳pH。 在调节原水的pH时,使用NaOH或NH 4 OH作为碱,使用无机酸作为酸。