序号 专利名 申请号 申请日 公开(公告)号 公开(公告)日 发明人
161 Apparatus and method for treating particle in fluid and method for forming spiral separation device JP2011288614 2011-12-28 JP2012071309A 2012-04-12 LEAN MENG H; SEO JEONGGI; KOLE ASHUTOSH; CHANG NORINE; LIMB SCOTT J
PROBLEM TO BE SOLVED: To provide an apparatus that can continuously separate particles from a fluid with volume in a range from a micro scale to a large scale by using a spiral form of a channel and velocity of the fluid.SOLUTION: The device (20) comprises: an inlet operable to receive the fluid containing the particles; the channel (22) in a spiral configuration, operable to allow a flow of the fluid; means (24, 26) for separating the particles within the fluid; and at least one outlet for the fluid. The channel has a width, a height and a radius of curvature. The particles are separated based on at least one of the width, the height, the radius of curvature, the velocity of the fluid and viscosity of the fluid.
162 In the process of obtaining cellulose acetate, the use of surfactants in the impurity removal process from a solution containing acetic acid derivatives using nano filtration by the membrane JP2001521932 2000-04-18 JP4897168B2 2012-03-14 イアコヴォン,エアリス; ナサー,ジュニア,ロベルト
163 Membrane element and membrane filtration apparatus JP2009197169 2009-08-27 JP2011045842A 2011-03-10 KONISHI TAKAHISA; IKEYAMA NORIO; NAGASHIMA TOSHIO
PROBLEM TO BE SOLVED: To provide a membrane element for successfully supplying power to the sensor or the like and to provide a membrane filtration apparatus. SOLUTION: A first electroconductive wire 102 is arranged in a shape along the outer peripheral surface of the membrane element 10 and connected to sensors 104, 105, 106 for detecting the characteristic of at least one of an object to be filtered and a filtered material. When power supply and/or data communication are performed from the outside through the first electroconductive wire 102, a distance between an external unit and the first electroconductive wire 102 can be made as short as possible. As a result, power can be supplied successfully to the sensors 104, 105, 106 or the like from the outside through the first electroconductive wire 102 and signals outputted from the sensors 104, 105, 106 can be sent successfully to the outside through the first electroconductive wire 102. COPYRIGHT: (C)2011,JPO&INPIT
164 Membrane filtration apparatus JP2009197156 2009-08-27 JP2011045841A 2011-03-10 KONISHI TAKAHISA; IKEYAMA NORIO; NAGASHIMA TOSHIO
PROBLEM TO BE SOLVED: To provide a membrane filtration apparatus, wherein a radio antenna is arranged more suitably to successfully perform radio communication. SOLUTION: An internal member 100 is arranged at different positions in a pressure-resistant vessel 40 between a filtration membrane and the inner wall of the pressure-resistant vessel 40 so that at least a part of the outer wall of the internal member comes close to the inner wall of the pressure-resistant vessel 40. The radio antenna 103A is arranged on the internal member 100. Since at least a part of the outer wall of the internal member 100 comes close to the inner wall of the pressure-resistant vessel 40, the thickness of a stock liquid existing between the outer wall of the internal member and the inner wall of the pressure-resistant vessel 40 becomes thinner and a radio wave is restrained from being attenuated owing to the stock liquid to successfully perform wireless communication. When compared with the case that the radio antenna 103A is arranged in the pressure-resistant vessel 40 between the filtration membrane and the inner wall of the pressure-resistant vessel 40, a restriction as to the position of the wireless antenna 103A to be arranged can be lightened and the radio antenna 103A can be arranged suitably. COPYRIGHT: (C)2011,JPO&INPIT
165 免疫グロブリン1量体の分離方法 JP2009520521 2008-06-18 JPWO2008156124A1 2010-08-26 文彦 山口; 均 溝元; 真也 浜崎; 多計奈 望月
【課題】限外濾過膜を用いて、少なくとも免疫グロブリンの1量体とその凝集体を含む免疫グロブリン溶液をクロスフロー濾過することにより、免疫グロブリン1量体を高精度で分離する方法およびその限外濾過膜モジュール、クロスフロー濾過装置を提供すること。【解決手段】分画分子量が10万以上50万未満である限外濾過膜を用いて、少なくとも免疫グロブリンの1量体とその凝集体を含む免疫グロブリン溶液であって、免疫グロブリン濃度が1〜150g/Lである溶液を、クロスフロー濾過することにより、免疫グロブリン1量体を80%以上の透過率で透過させ、かつ、限外濾過膜を透過する免疫グロブリン1量体と2量体の透過率比が0.20以下となる分画性能で免疫グロブリン1量体を分離できる。【選択図】選択図なし
166 Membrane separation method JP2008302635 2008-11-27 JP2010131469A 2010-06-17 OI YASUHIRO; TANAKA TAMOTSU; TADA KEIJIRO
PROBLEM TO BE SOLVED: To stably and efficiently perform membrane separation treatment for a long period of time by improving water quality of membrane feed water before performing the membrane separation treatment of separated water obtained by adding an alkaline solution of a phenol-based polymer to raw water, then adding an inorganic coagulant to perform coagulation treatment, and subjecting coagulation-treated water to solid-liquid separation. SOLUTION: The alkaline solution of the phenol-based polymer, which has phenolic hydroxyl groups, is alkali-soluble, and becomes insoluble in a neutral region and/or in the presence of high salts, is diluted to a predetermined concentration and then added to the raw water. COPYRIGHT: (C)2010,JPO&INPIT
167 超純の高純度化方法及び装置 JP2008542095 2007-10-29 JPWO2008053826A1 2010-02-25 小林 秀樹; 秀樹 小林; 邦洋 早川; 大澤 公伸; 公伸 大澤
超純中の不純物を小スペース内で長期にわたって安定的かつ高度に除去することが可能な超純水の高純度化方法及びその装置。超純水の高純度化装置10に導入した超純水は、下室1a内のイオン交換樹脂層5を通過する。このとき、超純水中における金属イオン等が、イオン交換樹脂によって除去される。その後、純水は目皿4を通過して上室1b内に流入し、イオン交換フィルタ6を透過する。このとき、このイオン交換樹脂層5によって、除去し切れなかった金属イオン等が除去される。このように、イオン交換樹脂によってある程度の金属イオンが除去されるため、その下流側のイオン交換フィルタでは極少量の金属イオンを除去するだけでよく、その結果、イオン交換フィルタが短期間で破過に至ることが防止され、長期間にわたって超純水の高純度化を行うことができる。
168 Method of using module for purifying fluid containing cleaning agent JP2009153733 2009-06-29 JP2009214107A 2009-09-24 GAIGNET YVES; KANO ICHIRO
PROBLEM TO BE SOLVED: To provide a method of using a module for purifying a fluid containing a cleaning agent. SOLUTION: The method for cleaning at least a part of a fluid purification system includes the steps of (a) connecting a disposable pre-treatment module to the fluid purification system and (b) thereafter, starting cleaning of the fluid purification system by cleaning involving tangential filtration. COPYRIGHT: (C)2009,JPO&INPIT
169 Device for measuring the penetration flow rate and permeate conductivity of the individual of the reverse osmosis membrane element JP2009500407 2007-03-12 JP2009530082A 2009-08-27 ウィルフ、マーク; バーテルズ、クレイグ; フランクス、リッチ; 紀男 池山
本開示は、個々の膜エレメント(163)の浸透物流量および浸透物電導度を、それらがROユニットで運転中に測定するための一体化センサ(169、170)を含むシステムに関する。 流量および電導度測定の一体化センサ(169、170)は小さなサイズであり、それらはROユニットの運転中に接続された膜エレメント(163)の浸透管(172)中に挿入することが可能である。 測定された流量および電導度情報は電気的配線または無線伝送を介して記録デバイス(174)に伝送される。
【選択図】図14
170 Waste liquid filtration system vehicle JP2005500724 2003-06-10 JP4289352B2 2009-07-01 晃一 井上; 雅仁 井上
An object of the present invention is to provide a vehicle which is capable of recycling contaminated liquid in a factory or the like swiftly and efficiently without performing incineration. In order to achieve this object, a contaminated liquid filtration system vehicle is characterized in comprising: vehicle driving unit comprising a driving engine and a driving mechanism; suction unit for aspirating the contaminated liquid within a contaminated liquid collection unit as liquid to be treated; a filtration system constituted by a charged filter device and a charged coalescer type oil water separator for filtration treating the aspirated liquid to be treated; electric power supply unit for supplying a driving power source to the filtration system; delivery unit for returning treated liquid which has been treated in the filtration system to the same or a different collection unit in the factory or the like; and control unit for controlling operations of the filtration system, wherein the charged filter device is caused to advance the filtration of impurity particles by applying a voltage between electrodes within the charged filter device using the driving power source supplied from the electric power supply unit, and the charged coalescer type oil water separator is caused to advance oil water separation by applying a voltage between electrodes within the oil water separator using the driving power source supplied from the electric power supply unit.
171 Method of producing hydrogen-containing drinking water JP2007303053 2007-11-22 JP2009125654A 2009-06-11 KATO AKIRA; YOSHIZAWA MICHIO; KONNO KOSUKE; YUZAKI YOSHINORI
<P>PROBLEM TO BE SOLVED: To provide a method of producing hydrogen-containing drinking water, which is appropriate for production on a large scale, small in a fluctuation of hydrogen dissolved amounts, and high in a hydrogen concentration. <P>SOLUTION: The method comprises dissolving hydrogen into raw water by feeding the raw water to a raw water streaming part of a hydrogen gas dissolving module which is partitioned into the raw water streaming part and a hydrogen gas streaming part with a gas-permeable membrane composed of a hydrophobic material while feeding pressurized hydrogen gas to the hydrogen gas streaming part of the hydrogen gas dissolving module, thereafter filling the raw water dissolved with hydrogen gas ejected from the raw water streaming part of the hydrogen gas dissolving module into a container, sealing it, and sterilizing it. <P>COPYRIGHT: (C)2009,JPO&INPIT
172 Processing backwashing amount is reduced JP2008543616 2006-12-11 JP2009518165A 2009-05-07 ワレン・トーマス・ジョンソン
膜濾過モジュールを逆洗する方法であり、ここで上記モジュールは、フィード含有容器の中に設置される膜を1つまたは複数含む。 上記膜は、濾過操作にかけられる透過壁を有するものであり、汚染物質を含有するフィード液が膜壁の一方の側面に加えられ、濾過液が膜壁の他方の側面から回収される。 この方法は、濾過操作を一時停止する段階と、付着物質を膜表面から取り除くために気泡で膜表面を通気する段階と、所定期間の間、フィード含有容器へのフィード液の流動を一時停止しながら、濾過操作を再開する段階と、再び濾過操作を一時停止する段階と、付着物質を膜壁から取り除くために膜壁を液体で逆洗する段階と、取り除かれた汚染物質を含有する液体の少なくとも一部をフィード含有容器から除去する段階と、次いで濾過操作を再開する段階とを含む。
173 Reverse osmosis filtration device having a flow meter and conductivity meter is powered by Rfid tags JP2008530205 2006-09-07 JP2009508665A 2009-03-05 マーク・ウィルフ; 紀男 池山
本発明は、逆浸透濾過装置に関し、より具体的には、RFIDタグによって電を供給される流量計及び液体導電度計を有する膜濾過装置(10、11、12)に関する。 本発明の実施形態は、逆浸透フィルタと、流量計及び導電度計を含む測定装置を備える濾過システムとを備えている。 本発明の測定器は、好ましくは濾過装置及びシステムの透過性コアチューブ(16)の上若しくは中に配置されている。
174 Dewatering system and dewatering method JP2007066287 2007-03-15 JP2008221176A 2008-09-25 SEIKI YOSHIO; YUKIMOTO ATSUHIRO; OZORA HIROYUKI; HIRAYAMA HARUAKI
<P>PROBLEM TO BE SOLVED: To provide a dewatering system with an improved film property. <P>SOLUTION: The dewatering system comprises a dewatering apparatus 1 having a water separation membrane part 10 having a liquid inlet in a lower part of a water separation membrane having one or more flow channels extended up and down for passing a liquid 50 and a liquid outlet in an upper part in a dewatering apparatus 1 main body and a shell part 11 defined by the outside face of the water separation membrane and the inner wall of the apparatus main body, a pressure reduction means 13 for reducing pressure of the shell part 11, a pressurizing means for pressurizing the liquid to be supplied to the water separation membrane part, and a heating means for heating the pressurized liquid; wherein the dewatering apparatus 1 dewaters a liquid by passing water through the water separation membrane while the liquid ascends the channels and releasing the water to the shell part. <P>COPYRIGHT: (C)2008,JPO&INPIT
175 Shear protection agent in the collection microfiltration JP2007552756 2006-01-24 JP2008528273A 2008-07-31 エンダ・モラン; ジェイムズ・ピアース
透析ろ過中の収集流への緩衝液添加は、濁度の上昇を引き起こし、産物回収を制限することを含む他の望ましくない効果を有しうる。 非イオン界面活性剤の使用に関する方法および組成物は、透析ろ過を改善するために提供される。
176 Physico-chemically emulsified hydrocarbon / water separator JP2003016245 2003-01-24 JP3955534B2 2007-08-08 カミロ・バスケス・ペレス; ホセ・サアベドゥラ・ペレイラ
The separator is intended to separate hydrocarbons emulsified in water, both physically and chemically, being based on a combination of two technologies, one of them corresponding to gravimetric separation of the hydrocarbon from the water and the other corresponding to ultrafiltration in membranes. The gravimetric separation unit (1) includes a pack of facet mpack coalescent plates, while the ultrafiltration unit (5) includes a series of membranes (6) via which passes the mixture of water exempt from free hydrocarbon which has been separated in the gravimetric unit (1). The separator finds special application in ship bilges and, as well as carrying out separation of free hydrocarbon in a current of water, also performs the separation of the emulsified hydrocarbon, having automatic functioning.
177 Module for purifying a fluid containing a cleaning agent, and methods of making and using that kind of module JP2006537485 2004-10-28 JP2007509741A 2007-04-19 ガイネ イヴ; イチロー カノー
本発明は、流体浄化システムの一部を形成するように構成された、特にである、流体を浄化するための使い捨て式のモジュール(31)であって、流体浄化手段(25,28)、前記流体浄化手段を収容する筐体(35)、及び浄化システムと浄化モジュール(31)の間の流体伝達を確立するために前記浄化モジュール(31)を前記浄化システムに取り外し可能に接続するための手段を備え、前記筐体(35)が最初に、浄化システムの少なくとも一部を洗浄するために前記筐体内を循環させられる流体と接触するように配置された洗浄剤を収容することを特徴とするモジュールを提供する。 本発明はまた、浄化システム、並びに、浄化システムの製造方法及び洗浄方法を提供する。
178 Wastewater treatment which combines a solid / liquid separation and pulse field JP2004518863 2003-07-02 JP2006511321A 2006-04-06 アラン・グラスミック; フィリップ・ヌヴル; リュク・シュリヴ
本発明は、廃の処理に関するものであり、廃水の流れに対して、物理化学的性質と生物学的性質とを変更するという効果を有したパルス型電界を印加し、このような性質変更を、固体/液体分離操作時に行う。 固体/液体分離操作(13,14,15)とパルス型電界印加操作(12)とは、廃水流れの互いに異なる場所において行われる。 パルス型電界は、パルス型電界の電圧値と電流値とパルス繰返し周波数と電圧立上り特性とが、固体/液体分離操作とパルス型電界印加操作とが行われる場所の関数として所望の廃水処理が得られるように、選択される。
179 Filter to remove the solids from the liquid JP2000543224 1999-04-15 JP2003526492A 2003-09-09 ウィリアム グラハム、
(57)【要約】 フィルタ(10)は、浄化されるの入口(42)を有するケーシング(18)を含むものとして開示されている。 第1段階フィルタ(12、16、58)があり、水から固体を除去する。 水は第1段階フィルタから第2段階フィルタ(66)へ流れ、これは限外濾過もしくは精密濾過および/または逆浸透を受けさせるためである。
180 Piping structure and filter device using the same JP2000146032 2000-05-18 JP2001321642A 2001-11-20 MONGAKI TATSUO
PROBLEM TO BE SOLVED: To provide a piping structure in which a support construction for individually fixing various pipings as used in a conventional piping is made unnecessary by allowing a portion of the piping to serve also as a support member for the piping and in which a change of a lay-out and an increase, or the like, of devices are made easier by making the support reconstruction unnecessary and to provide a filter device using this piping structure. SOLUTION: A horizontal part 30a and an erection part 30b of a raw liquid return pipe line 30 being a portion of a pipe line of a filter membrane unit 5 are formed to an L shape via an elbow 30c, and a lower end part of the erection part 30b is fixed to a pedestal 51, thus the membrane filter unit 5 is constituted such that it independently stands one's own legs by itself. COPYRIGHT: (C)2001,JPO
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