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    • 2. 发明专利
    • Denitrification method and apparatus
    • 脱色方法和装置
    • JP2003047989A
    • 2003-02-18
    • JP2001237517
    • 2001-08-06
    • Kurita Water Ind LtdNisshin Steel Co Ltd日新製鋼株式会社栗田工業株式会社
    • NISHIMURA SOSUKEFUJII HIROYUKITOKUHARA MINORU
    • C02F3/34
    • Y02W10/15
    • PROBLEM TO BE SOLVED: To provide a denitrification method and apparatus wherein the volume of an active sludge can be reduced and the holding time of the sludge can be extended without increasing the volume of a denitrification vessel, and thereby the treated water of a high quality can be steadily obtained at a low cost without generation of a separation trouble of the sludge. SOLUTION: Raw water is separately charged into respective denitrification vessels 1a, 1b, etc., from a raw water separately charging passage 5 to be mixed with an active sludge, and to be denitrified by making the mixed solution 12 pass through successively from the former stage-side denitrification vessel 1a to the latter stage-side denitrification vessel 1d. The mixed solution 12 in the final stage-denitrification vessel 1d is introduced into an aeration vessel 2 and remaining organic materials are decomposed followed by solid-liquid separation in a solid-liquid separation device 3. The separated liquid is taken out as a treated water 21, one part of the separated sludge is returned to the first-stage denitrification vessel 1a as a returning sludge from a sludge returning passage 22, and another one part is taken out from a taking out passage 23 to a reforming device 4 to be reformed to be readily biodegradable, and the reformed sludge is fed to the first-stage denitrification vessel 1a to be utilized as electron-donors required for nitrate respiration of denitrification bacteria.
    • 要解决的问题:提供一种反硝化方法和装置,其中可以减少活性污泥的体积并且可以延长污泥的保持时间,而不增加反硝化容器的体积,从而提高高质量的处理水 可以以低成本稳定地获得,而不会产生污泥的分离问题。 解决方案:将原水分别从原水中分别装入各自的反硝化容器1a,1b等中以与活性污泥混合,并使混合溶液12从前者连续通过,使其脱氮 阶段侧脱氮容器1a到后段侧脱氮容器1d。 将最终阶段 - 脱氮容器1d中的混合溶液12引入通气容器2中,并在固液分离装置3中将剩余的有机材料分解,然后进行固液分离。将分离的液体作为处理水取出 如图21所示,一部分分离后的污泥作为来自污泥返回通道22的返回污泥返回到第一级脱氮容器1a,另一部分从取出通道23取出至重整装置4,以进行重整 易于生物降解,并且将重整后的污泥送入第一级脱氮装置1a,作为硝化菌对硝化细菌的硝酸盐呼吸所需的电子给体。
    • 3. 发明专利
    • Trimmed chip guide device
    • TRIMMED芯片指南设备
    • JP2013075343A
    • 2013-04-25
    • JP2011216968
    • 2011-09-30
    • Nisshin Steel Co Ltd日新製鋼株式会社
    • TANAKA NARIAKITOKUHARA MINORU
    • B23D33/00B23D19/06
    • PROBLEM TO BE SOLVED: To solve a problem that the load of an operator is great because careful operation is needed because the operator needs to convey the end part of the trimmed chip to a scrap baller in the case the trimmed chip is not wound by the scrap baller up to now.SOLUTION: A gripper 10 for gripping the trimmed chip 4 is arranged, a wire 11 is connected to the gripper 10, and sheaves 12a, 12b are arranged such that the vicinity of the shaft 1a of the scrap baller 1 is contained in a moving passage of the gripper 10. Further, the trimmed chip 4 is gripped by the gripper 10, thereafter the wire 11 is wound by a winder 13, thereby the trimmed chip 4 is guided to the scrap baller 1.
    • 要解决的问题:为了解决操作员的负载大的问题,因为需要仔细操作,因为在修整的芯片不是的情况下,操作者需要将修剪的芯片的端部传送到废钢球 由废钢球员伤痕到现在为止。

      解决方案:用于夹紧修剪的芯片4的夹持器10布置成,线11连接到夹持器10,并且滑轮12a,12b布置成使得废料滚珠1的轴1a附近被包含在 夹持器10的移动通道。此外,修整的芯片4被夹持器10夹持,之后,线11被卷绕机13卷绕,由此修剪的芯片4被引导到废料滚珠1上。版权所有: (C)2013,JPO&INPIT

    • 4. 发明专利
    • BIOLOGICAL DENITRIFICATION TREATMENT METHOD
    • JP2000325989A
    • 2000-11-28
    • JP14157099
    • 1999-05-21
    • NISSHIN STEEL CO LTDKURITA WATER IND LTD
    • TOKUHARA MINORUFUJIYASU HIDEKAZUKITAGAWA MIKIOOKANO HITOSHI
    • C02F3/34C02F3/28
    • PROBLEM TO BE SOLVED: To stable and efficiently obtain treated water of good quality by a minimum necessary addition of a hydrogen donor by increasing and decreasing the addition ratio of the hydrogen donor to nitrogen load amt., that is, a hydrogen donor amt./nitrogen load amt. ratio corresponding to the nitrogen load amt. of a denitrification reaction tank. SOLUTION: A ratio of hydrogen donor (methanol) amt./nitrogen load amt. is increased and decreased corresponding to the nitrogen load amt. of a denitrification reaction tank. In treatment equipment, the nitrogen concn. of nitrogen-containing waste water being raw water and the amt. of water are continuously measured and the addition control of methanol is performed on the basis of the amt. of methanol operated by a coefficient of methanol optimum at every preset nitrogen load amt. The coefficient of methanol is set by preliminarily performing a preparatory test by using nitrogen-containing waste water being raw water. The coefficient of methanol corresponding to the nitrogen load amt. is used and the nitrogen load amt. is multiplied by the coefficient of methanol to set the optimum addition amt. of methanol corresponding to the fluctuations of the nitrogen load amt.
    • 6. 发明专利
    • METHOD FOR TREATING NITROGEN-CONTAINING WASTEWATER
    • JP2002192189A
    • 2002-07-10
    • JP2000394079
    • 2000-12-26
    • NISSHIN STEEL CO LTDKURITA WATER IND LTD
    • TOKUHARA MINORUNISHIMURA SOSUKEFUJII HIROYUKI
    • C02F3/12C02F3/34C02F11/06
    • PROBLEM TO BE SOLVED: To provide a method for treating nitrogen-containing wastewater capable of reducing the addition amount of organic matter, capable of efficiently reducing the formation amount of excess sludge and capable of stably obtaining treated water of high water quality. SOLUTION: Raw water, return sludge 11 and the ozone treated sludge 12 from an ozone treatment tank 6 are introduced into a first denitrification tank 1 to be subjected to denitrification treatment. The amount of introduced ozone treated sludge is regulated in the first denitrification tank to control the concentration of NOx-N of the liquid sent to a second denitrification tank 2 to 5 mg-N/l or more. The liquid in the first denitrification tank 1 is introduced into the second denitrification tank 2 and methanol 16 is injected to almost perfectly denitrify residual NOx-N. The denitrified liquid of the second denitrification tank is aerated and subsequently introduced into a sedimentation tank 4 to be subjected to solid-liquid separation treatment and a part of separated sludge is returned to the first denitrification tank as return sludge and the separated liquid is discharged as treated water. The separated sludge of which the pH is adjusted in a pH adjusting tank 5 is introduced into an ozone treatment tank 6 to be treated with ozone before introduced into the first denitrification tank.
    • 7. 发明专利
    • BIOLOGICAL DENITRIFICATION TREATMENT METHOD
    • JP2000325990A
    • 2000-11-28
    • JP14157199
    • 1999-05-21
    • NISSHIN STEEL CO LTDKURITA WATER IND LTD
    • TOKUHARA MINORUFUJIYASU HIDEKAZUKITAGAWA MIKIOOKANO HITOSHI
    • C02F3/34C02F3/28C02F5/00C02F5/08
    • PROBLEM TO BE SOLVED: To cetainly prevent the generation of calcium carbonate scale by a minium necessary addition of an acid in a method performing biological denitrification treatment in a denitrification reaction tank by adding an aid to calcium nitrate-containing waste water. SOLUTION: In performing biological denitrification treatment in a denitrification reaction tank by adding an aid to calcium nitrate-containing waste water, the amount amt. of addition of the acid (hydrochloric acid) is controlled corresponding to the nitrogen load amt. of a denitrification reaction tank. In actual treatment equipment, the concn. of nitrogen of calcium nirate- containing waste water being raw water and the amt. of water are continuously measured and the inflow nitrogen load amt. to the denitrification reaction tank is calculated and the addition amt. of hydrochloric acid is operated by multiplying the nitrogen load amt. by the coefficient of hydrochloric acid to nitrogen calculated by a preparatory experiment preliminarily performed by using raw water and the addition control of hydrochloric acid is performed on the basis of this result. By this constitution, since the control of the proper charging amt. of hydrochloric acid can be performed on the basis of the nitorgen load amt., the generation of calcium carbonate scale can be certainly prevented.
    • 9. 发明专利
    • SLUDGE-BLANKET-TYPE SOLID-LIQUID SEPARATION VESSEL
    • JP2000325706A
    • 2000-11-28
    • JP14157399
    • 1999-05-21
    • NISSHIN STEEL CO LTDKURITA WATER IND LTD
    • TOKUHARA MINORUKITAGAWA MIKIOOKANO HITOSHI
    • B01D21/24
    • PROBLEM TO BE SOLVED: To prevent the rise of the upper boundary of sludge blanket(SB) and the flow-out of the sludge blanket into treated water by making adjustable the height of the heed port of treated water which is arranged in a way that the treated water passes through the sludge blanket formed in the vessel. SOLUTION: This solid-liquid separation vessel 1 is provided with a multi- stage inner cylinder-type feed well 4, and a movable wall 4B, which slides in contact with the fixed wall 4A of the feed well 4, is moved up and down through a hanger 6 by a hoist 5 corresponding to the height of an SB interface. The position of an opening 4S of the feed well 4 is moved up and down to change the height of the feed port from which sludge mixture liquid is injected into the separation vessel 1. At this time, the height of the SB boundary is measured by a sludge boundary detector 7, and the movable wall 4B is moved up and down by the operation of the motor 5M of the hoist based on such a measured result. By this method, solid-liquid separation can be achieved efficiently with a high water-surface area load even in the case of active sludge and flocculated sludge of slow settling velocity.
    • 10. 发明专利
    • BEARING BOX AND FOOT ROLL SEGMENT
    • JPH10274247A
    • 1998-10-13
    • JP9131497
    • 1997-03-27
    • NISSHIN STEEL CO LTD
    • TOKUHARA MINORU
    • F16C35/00B22D11/128F16C37/00
    • PROBLEM TO BE SOLVED: To provide a simply structured and light bearing box having a suffi cient cooling effect by providing a plurality of grooves in the partial outer peripheral high heat load side of a bearing housing, a cooling water flow-in hole corresponding to the groove and a cap covering the groove. SOLUTION: A SUS 304 is used for a bearing housing 1, a SUS 310 is used for a cap 3 and two grooves 2 are provided and these grooves are machined in positions above a bearing groove. For a flow-in hole 4, for forming round holes from the inside of each groove 2 and the outside of the groove 2 and communicating these holes from a direction vertical to the holes, round holes are formed from a lower side to an upper side and two cooling water passages are provided by burying the lower side hole. Also, for the flow-in hole 4, a tap is cut to provide a female screw, a cooling water supply pipe side is used as a male screw, two flow-out holes 5 are provided in the cap 3, machined in a shape matching the outer periphery of the bearing housing 1 and then the full periphery of the cap 3 is full-welded to the bearing housing 1 to be used as a bearing box. Thus, good bearing cooling capacity is provided in the bearing, a structure is simplified and a weight is reduced.