| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 41 | Tangential solid separation device | JP2000594576 | 1999-08-25 | JP4514958B2 | 2010-07-28 | トラバウニズ ゲオルゲ; ニームツェジック ベルンハルト; メンケ ルカス; ヘインッ ロベルト |
| The invention relates to a device and a method for chemically and physically separating solid materials from a suspension using flotation. A rotationally symmetrical flocculation/flow reactor is provided with outlets in the lower part thereof and is arranged in a separating tank. At least one suspension inlet extends eccentrically into said reactor. The supplied suspension is guided into said reactor. The supplied suspension is guided into the upper area of the flocculation reactor via the suspension inlet. A circular flow is thus created which drains off from the flocculation reactor downwards in a tangential and radial manner over the outer circumference into circularly arranged distribution cells which reinforce the tangential component of the suspension flow when said flow is delivered into the separating tank. In prior art, the flow of the mixture consisting of the suspension and air-sacs extends radially outwards. One advantage of the invention is that said flow of the mixture has to travel a longer way to the outlets in the area of the wall of the tank due to the tangential flow component. The solid matter can be separated more effectively by virtue of the longer travel path or the longer presence in the separating tank. | ||||||
| 42 | 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. | ||||||
| 43 | 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. | ||||||
| 44 | 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 | ||||||
| 45 | Apparatus and method for supplying the coolant in the cutting machine and grinding machine | JP52918697 | 1997-02-12 | JP3354156B2 | 2002-12-09 | 義和 中井 |
| A method and apparatus for feeding coolant liquid to a lathe with a nozzle (53) having a discharge port (58) of substantially rectangular cross section and a constricted curved surface portion (62) on its inner wall to produce a turbulent flow and a loosely mounted tongue piece (59) crossing the section of the discharge port and projecting outside the port. The coolant is thus discharged as a collection of particulate turbulent flows containing air bubbles drawn into the coolant liquid as it passes by the tongue piece. The coolant is caused to impinge on the rotating peripheral surface (56) which is continuous with the region of the workpiece in contact with the cutter (57). <IMAGE> | ||||||
| 46 | Centrifugation dexterity control device | JP2000513675 | 1998-09-14 | JP2001518384A | 2001-10-16 | ニーベルイ、スヴェン−ウーロフ |
| In a centrifugal rotor (1) for separation of a substance from a liquid mixture supplied to the centrifugal rotor there is delimited a separation chamber (7) having peripheral outlets (30). The centrifugal rotor includes an outlet device (20-28) for intermittent opening and closing of the outlets (30) during rotation of the centrifugal rotor. An actuation device (31-40) may cause the outlet device (20-28) to keep the outlets (30) open to a varying extent and/or during a varying time, and a control device (43) is adapted to control the actuation device (31-40) in response to a sensed value of the amount of mixture supplied to the rotor, such that a predetermined amount of separated substance (29) having collected in the separation chamber (7) is discharged through the outlets (30) each time these are opened and closed. | ||||||
| 47 | Method and apparatus for separating the heavy fraction of the aqueous slurry from the light fraction by centrifugal action | JP53851197 | 1997-04-17 | JP2000508968A | 2000-07-18 | 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). | ||||||
| 48 | 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. | ||||||
| 49 | Paper pulp for cleaning equipment | JP6984086 | 1986-03-29 | JPH0718110B2 | 1995-03-01 | JANNPIEERU RAMOORU |
| 1. An appratus for decontaminating and, more particularly, for deinking paper pulp of the type in which a mixture of air with the pulp to be deinked is injected under pressure inot a volume and the foam of ink-laden air bubbles is separed out, characterized in that it is formed of a least one volume (1) having a shape of revolution, divided into at least two parts (2, 3...) by at least one internal ring (4) perpendicular to the axis, extending from the wall (31) of the volume towards the axis, while the said parts (2, 3) communicate together through the central aperture (23, 24) of the ring (4), the injection of the pressurized mixture of pulp and air running into the upper part (2) of said volume, in the form of a high-velocity flat tangential sheet (7) of liquid, the outlet (8, 9) for the purified pulp being located tangentially on the side wall (31) of the lower part (3), and the release of foam taking place in the central zone of the volume. | ||||||
| 50 | JPH07500881A - | JP50545093 | 1992-09-04 | JPH07500881A | 1995-01-26 | |
| 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. | ||||||
| 51 | How to flotation of the dispersion and equipment | JP50105885 | 1985-02-26 | JPH0639754B2 | 1994-05-25 | バルンシヤイト，ヴオルフガング |
| In deinking, the flotation of fiber suspensions is performed in a cylindrical tank 2 to which the fiber suspension is fed through a coupling means 36 as primary stream. The fiber suspension is already aerated and is withdrawn through a suction connection 33 below the coupling means 36 and fed after another aeration through a secondary connection 35 above the coupling means. The volume of the circulated secondary stream is greater than the volume of the primary stream. It is thereby assured that the fiber suspension is aerated at least twice and thus better cleaned. | ||||||
| 52 | JPH04507213A - | JP50523190 | 1990-03-06 | JPH04507213A | 1992-12-17 | |
| 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. | ||||||
| 53 | JPS61501272A - | JP50105885 | 1985-02-26 | JPS61501272A | 1986-06-26 | |
| In deinking, the flotation of fiber suspensions is performed in a cylindrical tank 2 to which the fiber suspension is fed through a coupling means 36 as primary stream. The fiber suspension is already aerated and is withdrawn through a suction connection 33 below the coupling means 36 and fed after another aeration through a secondary connection 35 above the coupling means. The volume of the circulated secondary stream is greater than the volume of the primary stream. It is thereby assured that the fiber suspension is aerated at least twice and thus better cleaned. | ||||||
| 54 | Deinking method and apparatus of pulp | JP24756083 | 1983-12-23 | JPS60134090A | 1985-07-17 | MORISANE MITSUO |
| 55 | JPS607945B2 - | JP12482381 | 1981-08-11 | JPS607945B2 | 1985-02-28 | BAANAADO SUMISON |
| A separator and a method for separating putrescent solids from water in sewage. A vortex chamber (2) has an inlet (for the sewage), a first (solids) outlet (6) and a second (water) outlet (8). Near the outlet (6) there is a flow modifying member (14) which induces a secondary flow in the vortex chamber (2). A portion of this secondary flow passes radially inwardly beneath the member (14) and upwardly through a passage (18). The member (14), if suitably shaped and dimensioned, improves the efficiency of the separator. | ||||||
| 56 | Flotation appartus of floated fiber extracted from waste paper | JP2842884 | 1984-02-17 | JPS59157392A | 1984-09-06 | HERUBERUTO HORITSUKU |
| The flotation apparatus has a vessel or container into which vortex or turbulence channels lead. These vortex channels supply the fiber suspension or stock to the vessel and are provided with at least one stepped enlargement. An air conduit supplying flotation air opens into the vortex channel. The vessel is substantially cylindrical about a vertical axis and is provided in its upper region with a central conduit or pipe for extracting the flotation foam. In the lower region of the vessel a conduit for extracting the recovered good stock is disposed tangentially. | ||||||
| 57 | Device for removing impurity contained in liquid in form of solid grain by flotation | JP16901480 | 1980-11-29 | JPS56161849A | 1981-12-12 | ENAARU BUARENTEIN HERUBERUGU |
| A floatation tower for paper recovery has a set of cells one above the other, holding the fibrous paper paste, and into which water and compressed air are injected so that the impurities mix. with the bubbles to form a foam which can be removed separately. Water is admitted as a thin layer at the same time as the air to mix. with the liquid paste as it is circulated in a thin layer in a mixing chamber, passing it through and along the flow, controlling the thickness of the layer. Air is then admitted to skin off the foam and drive it into a collector vessel below, for recycling. By a similar process for each cell, ink, kaolin and fibres can be removed separately. The mixing chamber is conical, with a tangential lop entry. | ||||||
| 58 | JPS5623659B2 - | JP4099577 | 1977-04-12 | JPS5623659B2 | 1981-06-01 | |
| A floatation tower for paper recovery has a set of cells one above the other, holding the fibrous paper paste, and into which water and compressed air are injected so that the impurities mix. with the bubbles to form a foam which can be removed separately. Water is admitted as a thin layer at the same time as the air to mix. with the liquid paste as it is circulated in a thin layer in a mixing chamber, passing it through and along the flow, controlling the thickness of the layer. Air is then admitted to skin off the foam and drive it into a collector vessel below, for recycling. By a similar process for each cell, ink, kaolin and fibres can be removed separately. The mixing chamber is conical, with a tangential lop entry. | ||||||
| 59 | JPS4910023B1 - | JP5499468 | 1968-08-05 | JPS4910023B1 | 1974-03-07 | |
| 1,241,051. Flotation apparatus. BERGWERKSVERBAND G.m.b.H. 2 Aug., 1968 [5 Aug., 1967], No. 37079/68. Heading B2H. Apparatus for effecting the classification of particles by flotation comprises a cell a containing a series of zig-zag guide walls 21 to form a number of zig-zag ducts, diffusers 17 arranged below the cell a to conduct a suspension of solid concentrated particles in a finely dispersed mixture of air bubbles to the ducts and to reduce the entry speed of the suspension into the ducts and irregularly arcuate guide wall portions 45 arranged to produce eddy zones at the bends in the zig-zag ducts. As shown in Fig. 1b an aqueous suspension of a material passes from a rod mill to a stirring mixer where reagents are added and then to a pre-mixing chamber 4 which is provided with internal fittings 5 which distribute air into the suspension, a supply duct 6 opening into the chamber 4 and serving for the introduction of air and a mist of a foaming reagent formed by an atomising device 7. The suspension passes to a stirring device which includes an annular space 10 from which the suspension passes through a number of outlet openings 11. Coarse particles coming against the wall of the space 10 are passed by centrifugal force through ducts 12 for repeated treatment. The suspension passes through flexible ducts 16 to the diffusers 17, oversize particles being separated and fed back through hoses 18 into a dock 19 for further treatment. Each of the diffusers opens into the zig-zag ducts the zigzag walls 21 ending in the upper part of cell a at different levels so that the suspension is directed at right angles and moves over a sedimentation device 22 the tapering outlet ducts of which are connected by means of flexible pipes to an overflow 25 the height of which can be adjusted by a handwheel 21. Above the foam bed runs an endless band provided with blades 30 which remove the foam to a gutter 29. | ||||||
| 60 | 분쇄 및 포말 부유 선광을 동시에 수행하기 위한 장치 | KR1020177017896 | 2015-11-24 | KR1020170088983A | 2017-08-02 | 슈타인벤더미카엘; 쇠테만외르크 |
| 본발명은 1 이상의미정제광물및/또는안료의분쇄및 포말부유선광(froth flotation)을동시에수행하기위한장치, 1 이상의분쇄광물및/또는안료의제조장치에서수행되는방법, 상기방법으로수득가능한분쇄광물및/또는안료함유상의, 제지응용분야에서뿐만아니라종이, 플라스틱, 페인트, 코팅, 접착제, 밀봉제, 식품, 사료, 의약품, 콘크리트, 시멘트, 화장품, 수처리(water treatment) 및/또는농업응용분야에서의용도, 바람직하게는제지기의습식엔드공정(wet end process), 궐련지, 보드및/또는코팅응용분야에서의용도, 또는로토그라비어(rotogravure) 및/또는오프셋및/또는잉크젯프린팅및/또는연속잉크젯프린팅및/또는플렉소그래피(flexography) 및/또는전자사진술및/또는장식표면(decoration surface)을위한지지체로서의용도, 및상기방법으로수득가능한분쇄광물및/또는안료함유상 또는분쇄광물및/또는안료에관한것이다. | ||||||
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