| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 61 | 에어레이션 및 다른 목적용 거품 생성 | KR1020097011171 | 2007-10-29 | KR101378672B1 | 2014-03-26 | 짐머만,윌리엄,바우어,제이; 테사르,바클라브 |
| 액체 내에 작은 기체 거품(90)을 생성하는 방법은, 압력을 받는 기체 소스(16); 액체로 개방되고 1 내지 100 헤르쯔 사이의 주파수에서 도관을 따라 통과하는 기체를 진동시키는 상기 도관(64a)을 포함한다. 상기 진동은 상기 공급을 각 출력(A, B)으로 나누는 전환기를 포함하는 유체 진동기(10)에 의해 수행되며, 각 출력은 제어 포트에 의해 제어되며, 상기 제어 포트들은 폐루프(22)에 의해 서로 연결된다. 적어도 두 개의 상기 도관들(62a, 64a)이 있을 수 있으며, 각 출력 포트는 상기 도관들의 하나 또는 다른 하나에 연결되며, 상기 진동하는 기체의 한 단계는 다른 단계의 진동에서의 거품 형성 이후에 상기 도관(64a)을 통해 액체를 유도하도록 채용된다. 상기 거품은 상기 유도된 액체의 힘에 의해 떨어진다. | ||||||
| 62 | 수평 탱크들을 가스 부상 분리기들로 전환시키기 위한 방법 및 장치 | KR1020107007034 | 2007-09-04 | KR101217363B1 | 2012-12-31 | 이더글라스더블유; 오웬스니콜라스 |
| 부유식원유생산저장하역설비선들(FPSO vessels))위의석유저장고용으로사용되는것들같은수평탱크에사용가능한가스부상분리기(gas flotation separator)는상기탱크를연속하여작용하는복수개의챔버들로나누는것을포함한다. 각각의챔버로들어가기전에상기오염된수성상(aqueous phase)은상기비혼화성상오염물의응집과부상을돕기위해가스버블들을포함하는흐름(stream)과혼합된다. 상기가스버블재순환흐름은상기탱크외부에서의공정에서조절된비율의압축가스를깨끗한생산수의흐름으로주입하거나, 상기탱크로의내부적기상의유입에의해생성될수 있다. 상기혼합물은첫번째챔버로흘러들어가서굽어진유입수위어에부딪힌다. 상기비혼화성상과상기기상의일부는상기챔버의상부로올라오고, 한편, 비혼화성혼합물의나머지는수성상으로상기챔버의바닥을향해아래로흘러간다. 상기수성상은상기각 연속된챔버를분할시키는배플의벽 안으로형성된복수개의평행한라이저도관으로들어감으로써 180°위쪽으로돌게된다. 상기비혼화성오염물의응집및 부상을더욱돕기위해두 번째가스버블흐름은각각의평행한덕트안으로주입된다. 상기수성상은그것이두 번째굽은위어에부딪히는두 번째챔버의상부에서재혼합된다. 이러한공정은각각의연속된챔버내에서마지막챔버에이르기까지반복되며, 마지막챔버에서는정수가액체펌프를거쳐상기챔버의밖으로나간다. 거기서의다양한물 제거비율은마지막챔버내의수위를조절한다. 상기응집되어부상한석유오염물은, 1) 상기챔버내에서수위를올림으로써범람(over-flow) 위어안쪽으로주기적으로걷어내는것 또는, 2) 부상하는석유층을상기물 표면으로부터들어올리거나, 멀리옮겨서수집장치(collector system)로그것을전달하는연속적으로회전하는패달혹은브러쉬같은것에의해제거될수 있다. | ||||||
| 63 | 플로테이터 | KR1020097017765 | 2008-09-02 | KR101190578B1 | 2012-10-15 | 이시다미노루; 가시보마사미; 소노다무네타카; 고야나기도모아키; 호사카다쓰미; 아이카와요시히코 |
| A flotation apparatus F includes a tank 1 for receiving a liquid raw material, and introduces air into the tank 1 to generate bubbles for adsorbing print ink in the liquid raw material to the bubbles, thereby floating and separating the print ink. The flotation apparatus F includes a circulating device for circulating the liquid raw material by raising and then lowering the liquid raw material in the tank 1, an air supply tube 4 for supplying air into the tank 1, and an agitating member 5 provided in the tank 1 for taking the air from the air supply tube 4 and agitating the air for forming the air into fine bubbles. The agitating member 5 has a rotary shaft 51 held horizontally and a plurality of members 52 horizontally separately provided around an outer periphery. On a cross section transverse to a longitudinal direction of the tank 1, an outer periphery of the agitating member 5 is arranged on a lower side of the tank 1 and in a position at a downstream side of the liquid raw material relative to a vertical line V passing through a center of the tank 1. | ||||||
| 64 | 고액 분리 장치 | KR1020080084265 | 2008-08-28 | KR100990913B1 | 2010-11-01 | 멘주다카시; 아시카가노부유키; 유카와아츠시; 츠쿠이히로미; 노구치히로후미; 오오노신지 |
| A solid-liquid separator that separates raw water containing suspended solids into suspended solids (solid) and treated water (liquid) in easy and a short time is provided. A solid-liquid separator includes a separation tub, an inflow pipe configured to rotate raw water which flowed from the outlet of the inflow pipe in the separation tub, a froth discharge pipe configured to discharge the suspended solids surfaced in the separation tub and a treated water discharge pipe configured to discharge treated water by which the suspended solids were removed from raw water from the separation tub. | ||||||
| 65 | 플로테이터 | KR1020097017765 | 2008-09-02 | KR1020100051038A | 2010-05-14 | 이시다미노루; 가시보마사미; 소노다무네타카; 고야나기도모아키; 호사카다쓰미; 아이카와요시히코 |
| A flotation apparatus (F) includes a reservoir (1) for receiving a stock material liquid for leading the air into the reservoir (1) to generate bubbles, adsorbing print ink in the liquid to the bubbles for floating and separating. The flotation apparatus (F) has a circulating means for circulating the stock material liquid in the reservoir (1) by raising the liquid and then lowering, an air supply tube (4) for supplying the air into the reservoir (1), and a stirring member (5) provided in the reservoir (1) for taking in the air from the air supply tube (4) and stirring the air for forming the air into the fine bubbles. The stirring member (5) has a plurality of members having a rotary shaft held horizontally and also horizontally separately provided around the outer periphery. The outer periphery of the stirring member (5) is provided on a lower part of the reservoir (1) and at a position closer to the downstream side of the stock material liquid than a vertical line (V) passing through the center of the reservoir (1) on a cross section transverse to the longitudinal direction of the reservoir (1). | ||||||
| 66 | 부양식 수처리 장치 및 방법 | KR1020097023995 | 2008-05-16 | KR1020100016650A | 2010-02-12 | 두모린,로랑스; 패스토렐리,델리아; 바다드,미쉘 |
| The invention relates to a flotation water treatment plant comprising at least: an inlet zone (31) for the water to be treated, which is coagulated and flocculated beforehand; a mixing zone (32), for mixing pressurized and then depressurized water with said water to be treated; a flotation zone (35) separated from said mixing zone by a wall; a clarified-water take-up zone (36) provided in the lower part of said flotation zone (35). According to the technique shown here, said mixing zone accommodates (32) at least one spray nozzle (40, 91, 92) for spraying said pressurized water, said spray nozzle (40, 91, 92) lying close to a panel (33), at least part of which has perforations (331), said panel separating said inlet zone (31) from said mixing zone (32). | ||||||
| 67 | 액체로부터 비용해 입자를 분리하기 위한 방법 및 장치 | KR1019970706033 | 1996-03-20 | KR100404716B1 | 2004-02-18 | 듀포르레뉴 |
| 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. | ||||||
| 68 | 浮选装置 | CN201220089792.0 | 2012-03-12 | CN202570415U | 2012-12-05 | 利拉·格罗斯曼; 沃尔夫冈·克里格尔施泰因; 斯文·门格尔 |
| 本实用新型涉及一种用于将固体颗粒与悬浮液分离的浮选装置，该浮选装置包括：一个带有用于容纳悬浮液的浮选腔室的壳体，以及至少一个用于向浮选腔室中输送气体的输送装置，其中，该至少一个输送装置包括至少一个气体分配元件，该气体分配元件由至少一种开孔结构构成，其中，气体分配元件的至少一个表面区域这样布置在浮选腔室的区域中，使得该表面区域能被悬浮液润湿。该开孔结构按照本实用新型由泡沫结构构成，该泡沫结构主要由金属或塑料构成。 | ||||||
| 69 | Water treatment by flotation equipment and water treatment process | JP2010507933 | 2008-05-16 | JP5259698B2 | 2013-08-07 | 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 |
| The invention relates to a flotation water treatment plant comprising at least: an inlet zone (31) for the water to be treated, which is coagulated and flocculated beforehand; a mixing zone (32), for mixing pressurized and then depressurized water with said water to be treated; a flotation zone (35) separated from said mixing zone by a wall; a clarified-water take-up zone (36) provided in the lower part of said flotation zone (35). According to the technique shown here, said mixing zone accommodates (32) at least one spray nozzle (40, 91, 92) for spraying said pressurized water, said spray nozzle (40, 91, 92) lying close to a panel (33), at least part of which has perforations (331), said panel separating said inlet zone (31) from said mixing zone (32). | ||||||
| 70 | Solid-liquid separation equipment | JP2007227581 | 2007-09-03 | JP4455631B2 | 2010-04-21 | 慎二 大野; 卓 毛受; 裕己 津久井; 敦司 湯川; 伸行 足利; 博史 野口 |
| A solid-liquid separator that separates raw water containing suspended solids into suspended solids (solid) and treated water (liquid) in easy and a short time is provided. A solid-liquid separator includes a separation tub, an inflow pipe configured to rotate raw water which flowed from the outlet of the inflow pipe in the separation tub, a froth discharge pipe configured to discharge the suspended solids surfaced in the separation tub and a treated water discharge pipe configured to discharge treated water by which the suspended solids were removed from raw water from the separation tub. | ||||||
| 71 | Foam generation for aeration and other objects | JP2009535112 | 2007-10-29 | JP2010508143A | 2010-03-18 | バウアー ジェイ ジマーマン ウィリアム; テーザー バツラフ |
| 気体の小さな泡(９０)を液体中に作り出す方法は、加圧気体の供給源(１６)と、液体中に開口する管路(６４ａ)であって、この管路内を伝わる気体を１と１００Ｈzとの間の周波数にて振動させる管路とを具えている。 この振動は、供給物を個々の出力(Ａ，Ｂ)に割り振る分流器を具えた流体発振器(１０)によってもたらされ、個々の出力は制御ポートによって制御され、制御ポートは閉ループ(２２)によって相互に接続されている。 少なくとも２つの前記管路(６２ａ，６４ａ)があってよく、個々の出力ポートが前記管路の一方または他方に接続され、振動する気体の一方の相が振動の他方の相での泡の形成後に液体を管路(６４ａ)中で駆動するために用いられ、それにより泡が前記駆動される液体の力によって分離される。 | ||||||
| 72 | Deinking method of paper pulp and flotation machine used for this method | JP2004144357 | 2004-05-14 | JP4339744B2 | 2009-10-07 | セール アラン; ラクール グザヴィエ; ポティエ ステファン |
| The de-inking procedure consists of circulating the pulp in a flotation cell comprising a chamber (2) with a vertical axis in which the pulp can move downwards from top to bottom, passing through a series of stages (E1...En), in each of which bubbles (13) introduced in the lower part of the chamber pass through it. The bubbles reach the top of the chamber in the form of a foam (5) carrying particles of non-soluble materials, the foam being removed at the top while the de-inked pulp is drawn off at the bottom. In each of the aforementioned stages the rising bubbles follow the under-surface of a spiral guide (12) to reach the passages taking them to the higher levels. In addition, the speed of the pulp is accelerated at the passage entrances by a progressive reduction in the passages' cross-section to draw the bubbles through and mix them with the pulp. | ||||||
| 73 | Equipment for water treatment due to the stray | JP2004571042 | 2003-04-16 | JP2006513854A | 2006-04-27 | ボール，クリスチャン; ボシシオ，マルコ; マルシャン，ジャン |
| The invention relates to an installation for treating water by flotation, said installation comprising flotation equipment consisting of a flotation cell ( 10 ) into which flocculated raw water mixed with micro-bubbles produced by a pressurization-depressurization system ( 11 ) is guided, said cell being provided with a perforated collection device ( 13 ) designed in such a way that the surface of the flotation cell is crossed by an identical and uniform flow of water to be treated. The inventive installation comprises capture modules ( 14 ) which are arranged in the flotation cell in such a way that the lower part thereof is located at a distance (h) from the perforated collection device ( 13 ), said distance being determined such that any disturbance of the uniform distribution established by the perforated collection device is avoided. | ||||||
| 74 | Process for de-inking paper pulp and flotation cell used for this process | JP2004144357 | 2004-05-14 | JP2004339684A | 2004-12-02 | SERRES ALAIN; LACOUR XAVIER; POTTIER STEPHAN |
| <P>PROBLEM TO BE SOLVED: To provide a process for de-inking paper pulp and flotation cell reducing energy consumption, controlling waste and enabling a larger modular property than the conventional flotation cell. <P>SOLUTION: The process comprises introduction of pulp from a main inlet (3) of the flotation cell having a vertical outlet conduit (16) in the vessel (2), de-inking of the introduced pulp in a transfer process of the introduced pulp from top to bottom by bubbles introduced from the bottom of the vessel, wherein bubbles can rise along a guiding means (12) to reach a bubble passage (13) for passing to upper level in each step (E1-En), and in the section of the bubble passage (13) acceleration of the pulp speed is induced and that causes suction of the bubbles coming out, promotes mixing of the pulp with bubbles, the acceleration of the pulp speed is obtained by step down of the passing cross-sectional area of the pulp on the guiding means (12) on the adjacent upper stream of the bubble path. <P>COPYRIGHT: (C)2005,JPO&NCIPI | ||||||
| 75 | Flotation machine | JP2002532358 | 2001-09-26 | JP3585231B2 | 2004-11-04 | トラバウニズ ゲオルゲ; メンケ ルカス |
| A flotation device for separating materials or mixtures of materials from suspensions includes a reaction and mixing space (18) with eccentric inlet (16) for the mixture of suspension particles with gas bubbles and for further transport into at least one centrally arranged vertical suspension distribution tube (26), wherein the suspension distribution tube (26) and the clarified fluid collecting tube (48) are arranged adjacently, the plates (30) surround the suspension distribution tube (26) and the clarified fluid collecting tube (48) in an annular manner; and every second annular plate space (31) between adjacent plates (30) is connected to the suspension distribution tube (26) and every other space (31) between plates is connected to the clarified fluid collecting tube (48), so that the flow takes place out of one space (31) between plates from the inside towards the outside to the separating space (32), and subsequently into an adjacent space (31) between plates from the outside towards the inside. The substantive advantages of the invention are in that by combination of the plate arrangement with the eccentrically loaded reaction and mixing space, improved flocculation and thus better processing values are obtained in the filtrate. Better separation values are obtained by separation using the double-plate principle. | ||||||
| 76 | ばっ気式水中スクリーンシステム | JP2002560743 | 2001-02-01 | JPWO2002060554A1 | 2004-09-09 | 近六 山下 |
| 本発明は、傾斜させて立設した微細目スクリーン2と、散気管6から発生する気泡によって、微細目スクリーン2に目詰まりを起こすこと無く、更に、旋回流によって汚物を微細に分解させる曝気式水中スクリーンシステムであり、固液分離槽1に設けた微細目スクリーン2で汚水流入側1aと濾過液廃水側1bとに仕切るように且つ上方を倒れ込むように取着するためのスクリーン取着手段3に取着された微細目スクリーン2と、散気管6と、汚水流入手段7と、濾過液排水手段8と、汚水流入側1aの下方には沈澱物を排出する沈澱物排出手段9とを備えたものである。 | ||||||
| 77 | Reactor for liquid purification | JP50023399 | 1998-05-27 | JP3340751B2 | 2002-11-05 | マガラッジィア，フラビオ |
| PCT No. PCT/EP98/03119 Sec. 371 Date Jan. 26, 1999 Sec. 102(e) Date Jan. 26, 1999 PCT Filed May 27, 1998 PCT Pub. No. WO98/54402 PCT Pub. Date Dec. 3, 1998The invention realises a reactor for liquids purification comprising: a tank containing the liquid to be purified; a plurality of upper injectors suitable for introducing in the tank said liquid to be purified with an aeriform substance dispersed in it in the form of bubbles; one or more blades arranged inside said tank and connected with a rotating shaft; one or more intermediate injectors cooperating with said first interception means suitable for sucking the liquid up and introducing it again in the tank in a lower position in comparison with said upper injectors. Said reactor comprises at least a low box, arranged at an intermediate height in said tank, suitable for receiving the descending liquid during a purification phase, which is supplied with interception means suitable for permitting the suction and the re-flowing of said liquid inside said tank. | ||||||
| 78 | Centrifugal flotation device and method | JP50523190 | 1990-03-06 | JP3042875B2 | 2000-05-22 | キャンベル，トーマス・ピー |
| The apparatus includes a powered bowl assembly having a tubular shaft journalled within a base of the apparatus. A pressurized air flow is discharged into slurry in the bowl assembly via a circular array of bubble generators. An impellor discharges the slurry outwardly against an upwardly inclined annular surface of the bowl assembly to cause the slurry to merge upwardly with the streams to promote flotation. Slurry within the bowl assembly forms a vortex with particle flotation forming a froth layer inwardly of a slurry vortex. The froth exits the bowl assembly upwardly past a barrier partially closing the bowl assembly. Heavier gangue particles exit via an outlet about the bowl assembly periphery. A collector shroud is partitioned to receive the froth and the heavier waste material. A modified form of the apparatus includes an independently powered bowl assembly and impellor. | ||||||
| 79 | Hydrodynamic mixing method and apparatus | JP20910187 | 1987-08-20 | JP2601283B2 | 1997-04-16 | ジェフリー・レル・チャンバーリン; ボージェ・フレドリックソン |
| A plurality of fluent substances are combined in a distributor (11) and caused to flow in a continuous, pressurized stream through a mixing zone (13) wherein the substances are intimately mixed by turbulent dispersion effected by a series of conically shaped surfaces (24,27) and alternate restrictions (25) and expansion chambers (28). While various fluent substances may be advantageously mixed, a typical utility is for effecting a thorough air binding of ink particles to attain efficient foaming in the deinking of reconstituted printed paper slurry. | ||||||
| 80 | Small purification system for wastewater treatment in the city | JP52125494 | 1994-03-18 | JPH08510952A | 1996-11-19 | クロフタ，ミロス |
| A compact water treatment plant has at least one vertical stack of dissolved air flotation (DAF) type clarifiers. Raw water is directed first to a single stage clarifier with a shallow tank. Its output is fed to an underlying two stage clarifier, preferably one with tall, mutually isolated cells, inclined baffles over a filtration medium in each cell, a cell-by-cell backwash capability, and an arrangement for isolating the first filtrate from the clarified water. Preferably, there are two such stacks in side-by-side array to provide a peak-load capacity, redundancy, and extreme compactness. Also preferably, clarified water from the single stage clarifier flows to the two stage clarifier via a bioreactor and an associated DAF clarifier. A source of aeration defines an upper, aerobic zone in the reactor where bacteria act on organic contaminants (COD's and BOD's). Strips of a deep pile, woven textile form a biocarrier. The strips oscillate in the tank. A portion of the bioliquor and sludge from the bioreactor-dedicated clarifier recirculate through a lower, anoxic zone of the bioreactor for denitrification. | ||||||
QQ群二维码
意见反馈
意见反馈