子分类：
| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 141 | 가스 부유 탱크 | KR1020167007546 | 2014-08-08 | KR101824064B1 | 2018-01-31 | 커크,토드윌리엄; 휘트니,다니엘클리포드; 이,더글라스워커 |
| 인접하는챔버들내에서회전흐름이일어나게하는그러한일련의인접하는챔버들을포함하는가스부유탱크가제공된다. 각각의챔버는스키밍위어에의해스킴오일통으로부터분리된다. 각각의챔버는하나걸러인접챔버들사이에유체소통장치를포함하며, 여기서유체소통장치는인접챔버들사이의분할벽에서소통포트의형태로인접챔버들간의유체소통이가능하게하고, 다공성판과결합된챔버유출부가포함되며, 유출부는마지막챔버와유체소통을행하도록위치하고있다. | ||||||
| 142 | 용존공기부상법을 이용한 응집조 포함형 또는 제외형 수처리 장치 | KR1020140041148 | 2014-04-07 | KR101628678B1 | 2016-06-22 | 박성원; 박병성 |
| 본발명은용존공기부상법을이용한응집조포함형또는제외형수처리장치에관한것으로, 보다상세하게는최종처리수가아닌최초유입수의일부를분리하고, 분리된유입수에공기를유입및 포화시켜미세기포생성에활용하는것으로, 장치의효율을향상시킬수 있는용존공기부상법을이용한응집조포함형또는제외형수처리장치에관한것이다. 본발명에따르면, 처리수가아닌유입수의일부를이용하여미세기포를형성하기때문에접촉조와분리조의크기를축소할수 있으며, 공기압축기를사용하지않고대기공기를사용할수 있고, 기존의포화장치에비해낮은압력에서운전이가능하며, 사용되는응집제의양을줄일수 있고, 필요에따라응집조를생략할수 있어전체설비의설비/장치비용(CAPEX) 및운전비용(OPEX)를모두절감할수 있는효과가있다. | ||||||
| 143 | 용존공기부상법을 이용한 응집조 포함형 또는 제외형 수처리 장치 | KR1020140041148 | 2014-04-07 | KR1020150116511A | 2015-10-16 | 박성원; 박병성 |
| 본발명은용존공기부상법을이용한응집조포함형또는제외형수처리장치에관한것으로, 보다상세하게는최종처리수가아닌최초유입수의일부를분리하고, 분리된유입수에공기를유입및 포화시켜미세기포생성에활용하는것으로, 장치의효율을향상시킬수 있는용존공기부상법을이용한응집조포함형또는제외형수처리장치에관한것이다. 본발명에따르면, 처리수가아닌유입수의일부를이용하여미세기포를형성하기때문에접촉조와분리조의크기를축소할수 있으며, 공기압축기를사용하지않고대기공기를사용할수 있고, 기존의포화장치에비해낮은압력에서운전이가능하며, 사용되는응집제의양을줄일수 있고, 필요에따라응집조를생략할수 있어전체설비의설비/장치비용(CAPEX) 및운전비용(OPEX)를모두절감할수 있는효과가있다. | ||||||
| 144 | 물 시스템으로부터 탄소 나노튜브들을 제거하는 방법 | KR1020147032115 | 2013-04-10 | KR1020140145626A | 2014-12-23 | 덴톤로버트디.; 코벌주니어러셀제이.; 노예스달라스비.; 링테리에이. |
| 수류로부터 탄소 나노튜브들을 제거하기 위한 방법들 및 시스템이 제공된다. 시스템은 정화 용기를 포함하고, 정화 용기는 수류 내의 탄소 나노튜브들로부터 탄소 산화물을 형성하도록 구성된다. 이 방법은 정화 용기 내로 수류를 유동시키는 단계와, 정화 용기 내에 화학 물질을 주입하는 단계를 포함한다. 탄소 나노튜브들은 정화 용기 내의 탄소 나노튜브들과 화학 물질의 상호작용을 통해 수류로부터 분리된다. | ||||||
| 145 | 실리콘 폐기물의 재생방법 및 그 방법으로 재생된 실리콘 | KR1020090094103 | 2009-10-01 | KR101138733B1 | 2012-04-24 | 김구성; 류근걸; 김재준 |
| 본 발명에 따른 실리콘 폐기물 재생방법은 용기 내에 실리콘 폐기물, 페하지수(pH)가 5 내지 6인 용매 및 계면활성제를 담고, 이를 혼합하는 단계 및 용기 내에 공기를 주입하여 부유물과 침전물로 분리하는 단계를 포함한다. 따라서, 본 발명의 실시예들에 의하면, 실리콘 폐기물로부터 실리콘을 용이하게 분리해 냄으로써, 재생되는 실리콘의 수율을 높일 수 있다. 재생된 실리콘은 재활용이 가능하므로, 전량 수입에 의존하고 있는 고순도 실리콘의 수입 대체 효과를 얻을 수 있다. 또한, 실리콘 폐기물이 매립 처분되는 양을 줄일 수 있어, 환경오염을 줄이는데 효과가 있다. 폐 실리콘, 슬러리, 알루미늄, 산화물, 재생 | ||||||
| 146 | 바닥재 처리방법 | KR1020090087168 | 2009-09-15 | KR1020100035589A | 2010-04-05 | 유광석; 안지환; 조희찬; 엄남일; 한기천; 이성주 |
| PURPOSE: A method for processing flooring materials is provided to improve a removal ratio of fixed carbon which is included in the flooring materials by selectively reacting the flooring materials after mixing the flooring materials having different content of the fixed carbon and to recycle bunt ashes. CONSTITUTION: A method for processing flooring materials comprises the following steps: a drying, mixing, and crushing a first fund flooring material and a second fund flooring material which have different content of fixed carbon of 10w/w.% or more; injecting water and air into the flooring materials passing through the previous step; and assorting the flooring materials by reacting the flooring materials in which oxygen is injected in a floating selector. | ||||||
| 147 | 부선기 | KR1020070035284 | 2007-04-10 | KR1020080092019A | 2008-10-15 | 양재열; 이지헌 |
| A flotation machine is provided to reduce the installation space and the cost by smoothly sorting out, floating, and removing harmful matter by forcibly supplying the air. A flotation machine is composed of: a flotation tank(10) receiving slurry and forming a separation layer to sort out necessary ores; a valuable substance discharging unit(20) obliquely installed along the outer peripheral surface of the upper end of the flotation tank to discharge the valuable substances flowing over by the air; an impurity discharging unit(30) installed on the other side at the lower part of the valuable substance discharging unit to discharge the sorted and separated impurities; a stand pipe(40) separated from the floor at the predetermined distance to be positioned in the center of the flotation tank, wherein the upper end of the stand pipe corresponds to the separating layer of the impurities and the middle portion is connected to a slurry transfer pipe(50) to supply slurry smoothly; a driving unit(60) installed at the upper end of the flotation tank to pass a driving shaft through the stand pipe and driven at low speed; an impeller(70) fixed at the lower end of the driving shaft and positioned at the lower part of the stand pipe to stir slurry and a reagent and disperse centrifugal force; a reagent supply unit(80) mounted on the upper part of the flotation tank and disposed at the lower part of the stand pipe to supply a reagent continuously while setting the quantity and ratio of slurry fed continuously; and a blower supply unit(90) positioned at the inner lower part of the flotation tank to feed the air for supplying slurry, forcibly. | ||||||
| 148 | 토양 속의 식물유체 및 유물을 수동으로 분리하는 장치 | KR1020050072539 | 2005-08-09 | KR1020070018154A | 2007-02-14 | 유기정 |
| 본 발명은 고고학 및 고민족식물학(Paleoethnobotany) 등의 조사과정에서 식물유체나 유물이 포함된 문화재 조사지역의 토양을 유물분리통으로 주입하여 수동으로 식물유체 및 유물을 분리ㆍ선별ㆍ채집하는 장치에 관한 것이다. 보다 구체적으로 본 발명은 식물유체와 유물이 포함된 토양에서 비교적 큰 부피와 무게를 가진 유물을 크기별로 거를 수 있도록 다단계 거름 크기를 가진 원통형거름망을 구비한 구조물이 설치되어 소정크기의 유물들을 분리할 수 있는 유물 분리탱크를 구비하며, 유물 분리탱크에는 식물유체 및 유물들이 물과 함께 존재하며 이들을 원통형거름망으로 이루어진 구조물을 잡고 흔들어서 용이하게 분리할 수 있으면서 용이한 운반을 위하여 손잡이가 부착 설치되고, 유물 분리탱크의 상단 일측에는 비교적 큰 부피와 무게를 가진 유물들을 분리한 후에 부유물속에 존재하는 비교적 작은 크기의 식물유체들을 분리하기 위하여 인접하여 설치된 다단계 소형 원형거름체로 이루진 구조물을 구비하며, 유물분리통 상단에는 부유물을 용이하게 따를 수 있도록 돌출되게 형성시킴과 동시에 회전이 가능하도록 설계 제작함으로써 적은 비용으로 효율적으로 식물유체 및 유물을 동시에 분리할 수 있도록 하는데 그 특징이 있다. 고고학, 문화재, 식물유체, 소형 유물 | ||||||
| 149 | 폐지펄프의 잉크제거장치와 방법 | KR1019940700725 | 1992-09-04 | KR100239630B1 | 2000-02-01 | 마일로스크로프타 |
| An apparatus and method for de-inking waste paper pulp using a foam flotation process to recycle printed waste paper for the manufacture of new paper. Pulped printed paper is fed as a slurry to an inlet of a shallow tank. Internal guide walls in the tank establish a flow path from the inlet to an outlet. The walls are sized and positioned to create a generally uniform cross-sectional flow area. A plurality of modules are disposed along the flow path. Each module includes at least one injector that aerates the flow and an extractor that removes floated ink foam. A portion of the flow from each module is recycled to an upstream module, preferably by a conduit and associated pump. In a preferred form, an injector (or injectors) alone located at the inlet is fed by the next downstream module and an extractor alone is located near the outlet. The invention also includes a main recycling loop from the downstream end of the flow path to the upstream end. This main recycling loop has a large flow rate compared to the recycled flow between the modules. | ||||||
| 150 | 水系からのカーボンナノチューブの除去 | JP2015507053 | 2013-04-10 | JP6303244B2 | 2018-04-04 | デントン ロバート ディー; コヴィール ジュニア ラッセル ジェイ; ノイエス ダラス ビー; リング テリー エイ |
| 151 | 海水淡水化装置及びその方法 | JP2015515809 | 2014-03-18 | JP6170552B2 | 2017-08-02 | 秦 良介; 島村 和彰; 千田 祐司 |
| 152 | 海水淡水化装置及びその方法 | JP2015515809 | 2014-03-18 | JPWO2014181583A1 | 2017-02-23 | 良介 秦; 和彰 島村; 祐司 千田 |
| 膜分離法による海水淡水化装置及び方法において、TEPを除去して、逆浸透膜の閉塞を防止し、長期にわたり、効率よく安定稼働が可能な海水淡水化装置及び方法を提供する。海水を取水する海水取水部10、取水した海水からTEP成分を除去する気泡発生及びTEP含有気泡除去部20、TEP成分を除去した海水から濁質分を除去する除濁部30、及び濁質分を除去した海水を脱塩処理して淡水化する逆浸透膜処理部40を具備する海水淡水化装置。 | ||||||
| 153 | 雑排水を浄化するための装置およびプロセス | JP2016521354 | 2014-09-30 | JP2016532541A | 2016-10-20 | ジャイディープ・チャタルジー; シャージャハン・アブドゥル・カリーム; サントーシュ・クマール・グプタ; シャイレンドラ・プラタップ; ラジーシュ・クマール・ラマチャンドラン |
| 本発明は雑排水を浄化するための装置およびプロセスに関するものである。特に、本発明は、再利用による節水のための、汚れた衣類の洗濯および/またはすすぎ液剤から発生する雑排水の家庭内浄化に関するものである。驚くべきことに、連続的な空気混和、破泡および分離によって、汚れた衣類の洗濯およびすすぎの水から界面活性剤を実質的になくすことができる装置およびプロセスを設計することが可能であることが判明した。次いで、この水は、多くの用途に再利用することができる淡水を回収するために、好ましくはフィルタにかけられる。 | ||||||
| 154 | Device and method for flotation separation and method for producing product using same | JP2009168346 | 2009-07-17 | JP2011020070A | 2011-02-03 | MATSUFUJI TAISUKE; TAKASU KOJI; TATSUMI KIYOTAKA |
| <P>PROBLEM TO BE SOLVED: To provide a device and a method for floatation separation for treating liquid having suspended treating objects containing impurities to be separated, floating-separating the liquid into floss and tail in a short time with high efficiency by using the difference in the surface wettabilities between the impurities and the treating objects, with an energy-saving simple structure, compact and low in cost. <P>SOLUTION: The treating liquid is contained in a treatment tank body 10, and a part of the treating liquid is taken out of a circulation liquid outlet 12 and returned through a circulation liquid inlet 13 by a circulation pump 20 and bubbles are injected to a lower part in the treatment tank body 10, to generate a vortex flow to the entire treating liquid in the treatment tank body 10, to disperse the bubbles into the treating liquid and to make the bubbles attach to the impurities, and to float the bubble-attached impurities and collect to the center of the vortex flow. When the floating deposit of floss, aggregate of the bubble-attached impurities, has proceeded, water is added to a part lower than the circulation liquid outlet 12 in the treatment tank body 10 to raise the liquid level, the floating deposit of floss is removed by overflowing, to recover the tail reduced in the impurities remaining in the treatment tank body 10. <P>COPYRIGHT: (C)2011,JPO&INPIT | ||||||
| 155 | Method and apparatus for aeration | JP2010520616 | 2008-07-18 | JP2010535627A | 2010-11-25 | レー・ミン・ソン |
| A method and apparatus for aerating a liquid wherein the liquid to be treated is drawn down a vertical pipe at a predetermined velocity to entrain air bubbles into the moving liquid forming an air liquid mixture, maintaining the air bubbles in liquid contact for a minimum period under increasing hydrostatic pressure to dissolve the air and returning the aerated liquid to the reactor, the air bubbles being generated close to the surface of the liquid above the inlet of the vertical pipe. | ||||||
| 156 | Water treatment by flotation equipment and water treatment process | JP2010507933 | 2008-05-16 | JP2010527286A | 2010-08-12 | デュムラン，ロランス; パストレリ，デリア; バダール，ミシェル |
| 本発明は、浮上分離水処理プラントに関するものである。 このプラントは、予め凝集され、かつフロック形成された被処理水の入口区域（３１）と、加圧された後で減圧された水を前記被処理水と混合するための混合区域（３２）と、壁によって前記混合区域から区分された浮上分離区域（３５）と、前記浮上分離区域（３５）の下部に設けられた浄化水取出し区域（３６）とを備えている。 ここに示されている技術によれば、前記混合区域（３２）は、前記加圧水を噴射するための少なくとも１つの噴射ノズル（４０，９１，９２）を収容している。 前記噴射ノズル（４０，９１，９２）は、少なくとも一部に穿孔（３３１）を有して前記入口区域（３１）を前記混合区域（３２）から区分しているパネル（３３）の近くに位置している。 | ||||||
| 157 | Flotation device comprising a perforated plate | JP2010504486 | 2008-04-02 | JP2010524671A | 2010-07-22 | トルブニス，ゲオルゲ; メンケ，ルーカス |
| 固体粒子高含有フラクションおよび固体粒子低含有フラクションを生成するように懸濁液から固体粒子を分離する浮選装置（１０）であって、この浮選装置（１０）は槽（１２）を備え、この槽（１２）は、懸濁液用の入口（１４）と、固体粒子低含有フラクション出口（１６）および固体粒子高含有フラクション出口（１８）と、重ねて配置された複数のスラット（２２）からなる少なくとも１つのスラット団（２０）と、を含み、少なくとも１つのスラット団（２０）が、槽（１２）の壁を向いた後方面と、該スラット団（２０）の反対側にある前方面と、を有する。 少なくとも１つのスラット団の後方面に、該スラット団（２０）の少なくとも一部を覆うように延びるプレート（２６）が配置され、このプレート（２６）に形成された複数の開口を介して液体が該プレート（２６）を通ることができる。 垂直方向について、プレートの上部領域における１ｃｍ 2当たりの個々の開口の面積の合計は、プレートの下部領域における１ｃｍ 2当たりの個々の開口の合計の面積よりも大きい。 | ||||||
| 158 | Process and device for aerating liquid with gas | JP2002267357 | 2002-09-12 | JP2003181260A | 2003-07-02 | SCHERZINGER BERNHARD; GABL HELMUTH |
| PROBLEM TO BE SOLVED: To provide a process and a device for aerating a liquid with a gas to realize dissolution of the gas. SOLUTION: The process to saturate the liquid with the gas is for a use in a process for separating impurities from a suspension 5 by means of floatation, covering the injection of a large quantity of gas to the liquid through a nozzle. In order to draw closer more effectively to maximum degree of saturation obtainable with improved mass transfer, a part of the gas is sucked in by the vacuum produced by the liquid injected, carried along together with the liquid and mixed uniformly with the liquid at the same time. The device for performing the process includes a pressure vessel 2 for the liquid and the gas present in the upper side which has a pressure connection in the upper section of the pressure vessel 2 to receive the gas and a nozzle for injecting the liquid to the pressure vessel 2. The nozzle is connected to a head of an injector provided in the pressure vessel 2, the injector is protruded into the lower part of the pressure vessel 2 holding the liquid and the head of the injector is connected to the upper part of the pressure vessel 2 containing the gas. COPYRIGHT: (C)2003,JPO | ||||||
| 159 | Waste water treatment method and plant | JP51638296 | 1995-11-17 | JPH10510203A | 1998-10-06 | バーネット、ケネス、エドワード |
| PCT No. PCT/AU95/00764 Sec. 371 Date May 13, 1997 Sec. 102(e) Date May 13, 1997 PCT Filed Nov. 17, 1995 PCT Pub. No. WO96/15991 PCT Pub. Date May 30, 1996A method of treating wastewater including: biologically treating wastewater under pressure; then reducing the pressure and substantially removing solids by dissolved gas flotation at the reduced pressure. | ||||||
| 160 | Separation method and apparatus according to the flotation | JP51743694 | 1994-01-20 | JPH08506050A | 1996-07-02 | チュダセク，マイケル・ウェンゼル; マーシャル，ステファン・ヘンリー; ワーマン，チャールズ・ハロルド |
| PCT No. PCT/AU94/00026 Sec. 371 Date Sep. 13, 1995 Sec. 102(e) Date Sep. 13, 1995 PCT Filed Jan. 20, 1994 PCT Pub. No. WO94/17920 PCT Pub. Date Aug. 18, 1994A suitably conditioned slurry feed is introduced to a trough from which it is distributed into a slurry layer-flow forming chamber provided with a discharge weir which discharges an evenly spread layer of slurry onto an inclined plate feeding into a mixing passage and then into a vessel. Recirculated slurry from the vessel is also fed into the mixing passage via a recycle gate which forms it into a layer of slurry. An array of clean liquid jets accelerates thin gas envelopes and impinges between layers of slurry and causes intensive mixing of all streams in the mixing passage. A high shear rate produces high intensity turbulence and shears gas into very small bubbles. A multiphase mixture flow is discharged from the mixing passage into the vessel, where it flows past one or more longitudinal stabilizing baffles. Gas bubbles loaded with hydrophobic particles disengage from the stream, rise toward the liquid surface and are diverted by bubble-diverting guides toward a froth discharge end of the vessel. A layer of froth travels toward a froth weir where it is discharged. Residual slurry leaves a discharge launder via a weir to a following flotation cell or process stage. | ||||||
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