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 |
|---|---|---|---|---|---|---|
| 101 | 타공판을 구비한 부상분리 장치 | KR1020097024429 | 2008-04-02 | KR1020100017304A | 2010-02-16 | 트로우보니스조지; 멘케루카스 |
| A flotation apparatus (10) for the separation of solid particles from a suspension with formation of a fraction lacking in solid particles and a fraction rich in solid particles comprises a tank with an inlet (14) for the suspension, with an outlet (16) for the fraction lacking in solid particles, with an outlet (18) for the fraction rich in solid particles, and with at least one block of slats (20) composed of multiple overlapping slats (22), wherein the at least one block of slats (20) has a rear side oriented toward the tank wall and a front side arranged on the opposite side of the block of slats (20). On the rear side of the at least one block of slats, a plate (26) is arranged which extends over at least a part of the rear side of the block of slats, wherein the plate has a plurality of openings which facilitate the penetration of liquid through the plate. The sum of the areas of the individual openings (38) in the upper region, relative to the vertical axis, of the plate, per square centimeter of the plate, is greater than the sum of the areas of the individual openings in the lower region of the plate, per square centimeter of the plate. | ||||||
| 102 | 토양 속의 식물유체 및 유물을 분리하는 장치 | KR1020050071548 | 2005-08-05 | KR1020070016680A | 2007-02-08 | 유기정 |
| 본 발명은 고고학 및 고민족식물학(Paleoethnobotany) 등의 조사과정에서 식물유체나 유물이 포함된 토양을 부유통으로 주입하여 신속하고 손상없이 자동으로 분리ㆍ선별ㆍ채집하기 위하여 토양 속의 식물유체 및 유물을 분리하는 장치에 관한 것이다. 보다 구체적으로 본 발명은 물과 토양이 혼합된 부유물을 회전시키고, 부유물 내부에 공기를 분출시켜 식물유체의 부유를 촉진시키는 부유통과, 부유통의 상측에 형성된 토출 공을 통해서 토출된 식물유체를 막힘없이 신속하고 효율적으로 거르기 위하여 체에 진동을 가하여 크기별로 다단계로 거를 수 있는 다단계 거름체를 구비하고, 거름체를 통과한 물을 저수하고 재순환시키는 저수조와, 부유통 아래에 침전된 토양 슬러지를 흡입하여 슬러지에 혼합되어 있는 유물과 비중이 큰 목탄을 분리시키고 물은 재활용할 수 있도록 제작된 진공유물 분리탱크를 구비하며, 물의 재활용을 위하여 물을 피드백시키기 위한 수중펌프와 상기 거름체를 진동시키는 바이브레이터 등을 구비한 토양 속의 식물유체 및 유물을 분리하는 장치를 구현함으로써 문화재 조사지역의 토양에 포함된 식물유체 및 소형유물 등을 고도의 선별도를 유지하면서 자동으로 신속하고 효율적으로 분리ㆍ채취할 수 있으므로 이중작업이 필요하지 않으면서 작업시간 및 인건비를 크게 절감하는데 그 특징이 있다. 고고학, 문화재, 식물유체, 유물, 플로테이션, 부유, 분리, 토양 | ||||||
| 103 | 액체에 가스를 공급하는 방법 및 장치 | KR1020020056583 | 2002-09-17 | KR1020030024631A | 2003-03-26 | 쉐르징거베른하르트; 가블헬무트 |
| PURPOSE: A process and device for aerating a liquid with gas is provided to saturate a liquid with a gas with much improved mass transfer, while drawing closer more effectively to the maximum degree of saturation obtainable. CONSTITUTION: The process comprises the steps of injecting the liquid through a nozzle(11) into a volume of the gas; generating a vacuum with the injected liquid; sucking a portion of the volume of gas into the liquid with the vacuum; and carrying away the gas portion and the liquid while mixing the gas portion intimately with the liquid. | ||||||
| 104 | 부유 선별에 의하여 현탁액으로부터 불순물을 분리하는방법 및 장치 | KR1020020056581 | 2002-09-17 | KR1020030024630A | 2003-03-26 | 쉐르징거베른하르트; 가블헬무트 |
| PURPOSE: A process and device for separating impurities from a suspension by flotation are provided to offer improved conditions for setting the optimum size and quantity of bubbles in the suspension and thus, make the process more effective. CONSTITUTION: The process comprises the steps of aerating a liquid with a gas until the liquid is saturated with the gas; expanding the liquid saturated with gas to form gas bubbles; and adding the liquid containing gas bubbles to the suspension(5); wherein the liquid saturated with gas is expanded separately before the liquid containing the gas bubbles is added to the suspension. | ||||||
| 105 | 双向充气射流浮选柱 | CN00243228.5 | 2000-07-07 | CN2431047Y | 2001-05-23 | 张荣曾; 曾鸣; 皇甫京华; 谢华; 徐志强; 孙宗岳 |
| 一种在液体介质中进行微细颗粒物料分选的双向充气射流浮选柱,主要由柱体(1)、泡沫收集槽(2)、锥形漏斗(3)、入料管(4)、中矿循环泵(6)和气泡发生器(5)和(7)、尾矿漏斗(13)、筛板(14)等组成。柱体(1)上部外表面安装有泡沫收集槽(2),在柱体(1)中心设置入料管(4)及一组气泡发生器(5),柱体(1)内下部安装有锥形漏斗(3),并与中矿循环泵(6)相连,其间装有一组气泡发生器(7),在柱体(1)下部壁上设有若干个孔与环形套(12)相通,它的排料管与中矿循环泵入口相连,在柱体(1)上部装有若干层筛板(14),其底部装有尾矿漏斗(13)及排料管(11)。本实用新型采用了入料从上部和循环从下部进行双向充气矿化的结构,一方面使易浮的精矿得到优先浮选,另一方面加强了中矿的复选,从而提高了浮选的质量和回收率。本实用新型结构简单易于安装,维护与维修非常方便。 | ||||||
| 106 | 湿式排煙脱硫方法と装置 | JP2017510964 | 2016-04-01 | JPWO2016163318A1 | 2018-04-26 | 下平 和佳子; 吉川 博文; 片川 篤 |
| 脱硫吸収塔13内に噴霧する吸収液中に活性炭を添加して排ガスの脱硫と同時に排ガス中の水銀成分を除去し、前記脱硫処理後の吸収液を浮選装置32に送り、泡沫気泡層36を形成させ、該気泡層36の物性値が所定の範囲となるように、吸収液中の塩素イオン濃度が所定値を上回らない範囲で排水量を減少させ、同時にCaイオン及び/又はMgイオン、さらには起泡剤を吸収液に添加することで、浮選装置32における活性炭の分離回収率を高め、脱硫吸収塔13での水銀再放出と回収石膏への水銀移行を安定的に抑制する。 | ||||||
| 107 | 界面エマルジョン、水及び固体を処理する装置 | JP2014533542 | 2012-09-04 | JP6068481B2 | 2017-01-25 | ゲイリー ダブリュ.サムズ; ロナルド ディー.ハイプス |
| 108 | 界面エマルジョン、水及び固体を処理する装置 | JP2014533542 | 2012-09-04 | JP2014533194A | 2014-12-11 | ダブリュ．サムズ ゲイリー; ディー．ハイプス ロナルド |
| 分離装置容器内に含まれる界面エマルジョン、水及び固体を処理する方法であって、容器からそれらの成分を連続的に取り出すステップと、次にそれらをガス浮選セルに通すステップを含む。セルは、好ましくは縦型誘導ガス浮選セルであり、界面エマルジョンに含まれるオイルと水を分離し、回収されたオイルをセルの上方部分から排出し、処理された水をセルの底部から排出する。回収されたオイルと処理された水は更に処理されて容器に再循環されるか、又は他のところに送られてよい。処理された水はセルに再循環されるか、又は処理下水管に送られてもよい。セルの上方部分に滞留する燃料ガスは冷却されてスプリッタに通されてよい。この方法の全てのステップは大気への放出物のない閉じた装置を含む。 | ||||||
| 109 | Floating separation apparatus and method as well as the production method of its use product | JP2009168346 | 2009-07-17 | JP4802305B2 | 2011-10-26 | 泰典 松藤; 清隆 達見; 幸二 高巣 |
| By storing a liquid to be treated in a treatment tank main body 10 having a bottom portion 10g that narrows downward, with particles of materials to be treated dispersed therein, taking out the liquid to be treated from a position lower than the liquid level of the treatment tank main body 10, and returning the liquid to the bottom portion 10g of the treatment tank main body 10, thereby circulating the liquid to be treated while forming a vortex flow within the treatment tank main body 10, and at the same time supplying air bubbles from the lower part of the treatment main unit 10, a first component contained in froths is separated from a second component, which is less susceptible to floatation, contained in the liquid to be treated. | ||||||
| 110 | Water purification and biosolids collection system and related methods | JP2010520193 | 2008-07-31 | JP2010535104A | 2010-11-18 | カイル・アール．・ジェンセン; ダニエル・ケイズ; ロナルド・ピー．・アレン |
| A system and method for remediating a body of water and collecting suspended and dissolved solids therefrom are provided. The system includes a water-impervious lining positionable in a depression in or adjacent a body of water. The lining and depression define a treatment vessel, which includes a treatment portion, an outlet portion for containing treated water, and an outflow weir between the treatment portion and the outlet portion. Water to be treated is transported from the water body to the treatment portion. An entrapment element is delivered and mixed into the transported water, the entrapment element for capturing suspended and dissolved solids in the transported water and effecting a separation between the captured solids and water cleansed therefrom. The captured solids can be removed from the treatment basin, and the cleansed water can move through a channel in the outflow weir into the outlet portion. | ||||||
| 111 | Bubble treatment device and water treatment apparatus | JP2007039257 | 2007-02-20 | JP2008200604A | 2008-09-04 | HASEGAWA KOJI |
| PROBLEM TO BE SOLVED: To provide an effective technology which enables continuous use of a bubble treatment device atomizing bubbles and supplying them to water to be treated with a simple structure. SOLUTION: In a water treatment apparatus 100, a bubble treatment device 200 introduces bubble-containing water to be treated into a flow pipe 220. While the water to be treated flows downward through the flow pipe 220, bubbles contained in the water to be treated are separated into floating bubbles which floats upward by buoyancy resisting downward water flow to be discharged from an exhaust port 222 and fine bubbles which are finer than the floating bubbles and flows downward with the downward water flow to flow out together with the water to be treated from the outlet port 220a. COPYRIGHT: (C)2008,JPO&INPIT | ||||||
| 112 | Method and apparatus for separating the heavy fraction of the aqueous slurry from the light fraction by centrifugal action | JP53851197 | 1997-04-17 | JP4047386B2 | 2008-02-13 | アイヒラー，ディートリッヒ |
| The invention relates to a process and apparatus for the separation of heavier from lighter fractions in aqueous slurries by means of centrifugal force. The slurry is made to spin in the separation chamber under the influence of the differential pressure generated between the inlet and outlet of a cyclone separation chamber (4). The differential pressure, which can amount to several bar, is generated by means of a pressure increasing stage in the form of a transport rotor device (20) which acts in conjunction with a stator arrangement (22); essentially this takes place immediately in front of the inlet of the slurry into the separation chamber (4). The rotor blades of the cyclone rotor device (10) as the rotor blades of the transport rotor device (20) can be mounted on the same rotary shaft (5) in order to induce additional rotary force into the slurry. The separation of floatable fractions in aqueous slurries is effected by the presence of micro gas bubbles introduced into the separation chamber (4). The separated floatable fractions can be removed from the gas bubbles to which they adhere by means of an anti-foaming device driven by the rotary shaft (5) of the transport rotor device (20). | ||||||
| 113 | Suspended water separation processing system | JP2002323204 | 2002-11-06 | JP4009180B2 | 2007-11-14 | 昌紀 江内 |
| 114 | Pulp and paper deinking method and apparatus | JP7817795 | 1995-03-09 | JP3819948B2 | 2006-09-13 | セレス アラン |
| To separate and remove ink from a paper pulp, an air bubble recirculation flow is directed at the pulp against its direction of travel in a circuit, to increase the probability that the air bubbles will collide with ink particles. Also claimed is an appts. with a vertical chamber (1) with one or more outlet channels (M) for the foam at the top. At least one pulp inlet (E) is at the upper zone. At least one recirculation circuit has an outlet opening (S), a circulation pump (P) and one or more injectors. At the lower section of the chamber, an opening gives return of a pulp/air bubble mixture above the outlet for the deinked pulp. | ||||||
| 115 | Precipitation and floatation separation structure for suspension, suspension separation system, and precipitate collection block for suspension separation system | JP2002323204 | 2002-11-06 | JP2004154690A | 2004-06-03 | ENAI MASANORI |
| <P>PROBLEM TO BE SOLVED: To provide a suspension separation system in which the water flow state inside a liquid cyclone is controlled corresponding to the use conditions, a supplied suspension is efficiently separated and classified by setting the classification particle size, no heavy load is applied to a supply pump, and even gel-like precipitates accumulated in the bottom part can easily be removed, and which is excellent in maintenance easiness and economical properties. <P>SOLUTION: The suspension separation system is constituted of a plurality of groups of precipitate separation parts 2-4 which are assembled together and each independently provided with a downward flow path where a suspension or treatment water supplied from an upper side flows downward, a precipitation part 7 formed by setting its opening in a lower part of the downward flow path for turning the downward current to upward current, an upward flow path formed by setting its opening in an upper part of the precipitation part 7 for passing the upward current through. The system further is provided with flotation parts 8a installed so as to join the downward flow paths and the upward flow paths of the neighboring precipitate separation parts 2-4 in the upper sides. <P>COPYRIGHT: (C)2004,JPO | ||||||
| 116 | Waste water treatment method and plant | JP51638296 | 1995-11-17 | JP3358066B2 | 2002-12-16 | 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. | ||||||
| 117 | A method and apparatus for separating the insoluble particles from the liquid | JP52793396 | 1996-03-20 | JP3331219B2 | 2002-10-07 | デュフュール、ルノー |
| Disclosed is a clarifier for use in treating a liquid containing non-soluble particles in suspension in order to separate these particles from the liquid. It comprises a tank, a liquid supply duct opening into the bottom portion of the tank and an injector for injecting a gas under pressure into at least part of liquid supplied to the supply duct in order to saturate this liquid with said gas and thus to generate gas bubbles as the saturated liquid is subject to depressurization within the tank. The gas bubbles that are so-generated adhere to the particles in suspension in the liquid and lift them up to form a floating layer of sludge in the top portion of the tank. A scraper is provided in the top portion of the tank for skimming off the layer of sludge while it is formed. A plurality of plates extend at an angle within the tank above the supply duct. These plates define a set of upwardly inclined channels each having an upper end that is opened and through which the liquid fed into the tank may enter the channel. A liquid outlet mounted within the lower end of each channel to collect and remove from the tank the liquid that has been treated within the same. Thanks to its shape and structure, this clarifier occupies a surface area on the ground that is 50% or less smaller than any known clarifier of the same capacity. Its structure also permits to maintain much more microbubbles of requested size for a same amount of injected air in order to increase the probability of contact between the particles and the air bubbles. | ||||||
| 118 | Floating separation method and system for the extraction of components from dehydration and micro-algae of microalgae suspension | JP52882898 | 1997-12-10 | JP2001509011A | 2001-07-10 | スコット カネル，ジェフリー; アーサー ゲルシェール，スコット |
| A process and system are disclosed for recovering mixed carotenoids from the alga Dunaliella salina. The harvested cells are ruptured, typically by circulating the algal suspension at high pressure through a pump loop. The cells can then be dewatered by absorptive bubble separation techniques, including a froth floatation circuit that has a roughing zone and a concentrating zone. If further concentration is desired, the algal concentrate can be mechanically filtered in a cross flow microfiltration unit in the absence of flocculating agents with substantially no loss of carotenoids in the permeate. Various methods for extracting mixed carotenoids and other components from the algae are disclosed, including dense gas extraction, and extractions with natural and synthetic flavorants, and edible oils. | ||||||
| 119 | Flotation apparatus and method | JP52121197 | 1996-12-06 | JP2000501645A | 2000-02-15 | ダールクヴイスト，ヤン; ヘードベルイ，トウーシユテン |
| Flotation apparatus (1) for the purification of polluted water, comprising a flotation vessel (3) having an inlet means (23) for supplying polluted water to said vessel, an assembly (41) of spaced elements (43, 65) defining passages for the flow of water through said elements, and outlet means for surface sludge (15, 17) and outlet means (39, 45; 57, 61) for treated water, further comprising flow directing means for forcing the incoming polluted water to reach a level above said assembly (41) and to flow downwardly through said assembly and towards said treated water outlet means (39, 45; 57, 61); and a process for the purification of polluted water by flotation performed in such apparatus. | ||||||
| 120 | Deinking of paper pulp and apparatus therefor | JP35509098 | 1998-12-14 | JPH11269787A | 1999-10-05 | SERRES ALAIN |
| PROBLEM TO BE SOLVED: To effectively deink paper pulp, by passing an air foam through an old paper pulp flow to carry an ink component and removing particles except the ink component by a water counterflow. SOLUTION: A paper pulp comprising various kinds of old papers is introduced from an inlet E 1 to a column 1, filled to a level N positioned below a foam discharging pipe M, sent to a baffle plate D 1 by a top grip C, discharged from an outlet S 1 while being filled in the interior of the baffle plate, passed through a pipe 2 and recycled through a regenerating pump P 1 from an inlet E 2 to the column 1. Hereafter the paper pulp is similarly recycled from the inlet E 2 → an outlet S 2 → a pipe 3→ a regenerating pump P 2 → an inlet E 3 and the pump P 3 is worked in cooperation with an injector 13 for air supplied from an air duct 6 to raise an air foam, which is passed through a pulp flow to carry ink. Particles except an ink component carried on the air foam is removed by a water counterflow to deink the paper pulp. COPYRIGHT: (C)1999,JPO | ||||||
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