| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 181 | Hydrocyclone and device for separating liquid slurry component | JP17123591 | 1991-07-11 | JPH04240288A | 1992-08-27 | RUISU OO TOREGUROTSUSA |
| PURPOSE: To improve the diversity and efficiency of a gas-sparged hydrocyclone. CONSTITUTION: This hydrocyclone has a means for establishing a vortex action in a volume between the bottom (second end) 21 of the porous surface of a hollow main body and the second withdrawal means or outlet 23, to effect separation of some or substantially all of the remaining gases in the fluent material when it reaches the bottom 21 of the porous surface of revolution 18. The revolution means comprises a shroud means 25 disposed above a conical bottom (second end) section 24 (e.g. sharply tapered), a means 28 for forming the shroud means and the central axially extending passage 27 of the conical interior passage 30 of the shroud means 25. A gas separated in the conical bottom section 24 by the other revolution means is joined to a gas separated by a revolution flow 15 in the hollow main body and then discharged from a gas withdrawal conduit 14 at the top. High density and larger particles move toward the wall where they are extracted through a generally tangential outlet nozzle 35. The accepted slurry flows downwardly toward the outlet 23. COPYRIGHT: (C)1992,JPO | ||||||
| 182 | Froth flotation apparatus and method | JP40141290 | 1990-12-11 | JPH0411086A | 1992-01-16 | RONARUDO DEII KURUA; MAIKERU EFU KINEE; JIYON JIEI PINREI; KURISUTOFUAA EMU BUITORI; AIRIIN JIEI FUIRITSUPII; POORU JII MAASHIYU |
| PURPOSE: To increase the capacity of a froth flotation apparatus by leading an aerated stock to a flotation chamber through a specific means. CONSTITUTION: A drum-shaped rotor 240 whose axis 242 extends transversely of an inlet conduit 220 is attached to the conduit leading the flow of an aerated stock suspension to a flotation chamber. Multiple protuberances are disposed on the outer surface of the rotor 240, and an air supply conduit 252 is disposed on the upstream side of the rotor. A discharge nozzle 255 is positioned in close relation with the surface of the rotor, and the rotor is continuously driven at a rate of rotation sufficiently high to cause the protuberances on the outer surface thereof to mix air discharged from the nozzle 255 with the stock flowing past the rotor into the cell. COPYRIGHT: (C)1992,JPO | ||||||
| 183 | Floatation device for removing ink | JP26621089 | 1989-10-16 | JPH03130483A | 1991-06-04 | IWASHIGE NAOYUKI; EGUCHI MASAKAZU |
| PURPOSE: To homogeneously mix air bubbles with the raw materials of paper is a reduced stirring power by disposing a trough for floated substances, an inlet for the raw materials, an outlet for the raw materials and an air bubble- generating device in specific states in a cylindrical cell disposed sideways. CONSTITUTION: A trough 4 for receiving substances floated on the free solution surface of a raw material solution is disposed at the upper portion of a cylindri cal cell 5 disposed sideways and having a free solution surface formed at the upper portion. An inlet 1 for the raw materials and an outlet 2 for the raw materials are disposed at one end of the lower portion of the cell 5 and at the other end thereof, respectively, and an air-bubble-generating device 3 is sideways hung at the lower portion of the cell. The raw material solution is charged from the raw material inlet to the cell and flowed toward the raw material outlet to form a spiral flow having a sideway rotation aixs and mix the raw material solution with air bubbles generated from the air bubble- generating device 3, thereby permitting to remove inks, etc., along the spiral flow. COPYRIGHT: (C)1991,JPO&Japio | ||||||
| 184 | Liquid skimming device and liquid surface layer skimming method | JP6989890 | 1990-03-22 | JPH02280889A | 1990-11-16 | SAREAMU ESOTSUPU |
| PURPOSE: To scoop up an oils and fats layer or the like on the water body by arranging a hollow body provided with an inlet capable of being connected with a liquid moving device and two outlets separated from each other at one end and at the other end respectively, and a baffle plate. CONSTITUTION: By a support structural body such as a buoy or a vessel, a boat, a flat-bottomed boat or a Hovercraft, a device 1 is made to descent in the liquid body. The level of a body 12 in liquid is adjusted so that a part thereof may sink and a baffle plate 18 may be just under the surface layer of the liquid body. In this state, the liquid surface layer is deflected in a first path 20 and the remainder of liquid is deflected to a second path 22. A suction pump is connected with outlets 24, 26, and by the suction pump, the liquid surface layer enters the path 20 and is separated through the outlet 24. The remainder of liquid enters the second path 22 and is returned to the liquid body. COPYRIGHT: (C)1990,JPO | ||||||
| 185 | JPH0148075B2 - | JP14937182 | 1982-08-30 | JPH0148075B2 | 1989-10-17 | MIROSU KUROFUTA |
| Apparatus and a method for removing suspended particles from water in a circular tank having a distribution and flocculation chamber immersed in the tank of water and carried circularly around the tank by a carriage. Flocculating material and inlet water are introduced into the body of water from the moving flocculating chamber at the same rate as clarified water is discharged through a filter substantially covering the bottom of the tank. A majority of particles in the water is collected by flocs in the water and floated to the water surface by air bubble action. The floating sludge is removed by a spiral scoop carried by the carriage. The water is then passed through the bottom filter which removes the remaining flocs completing the clarification of the water for discharge. Apparatus is provided for selectively back washing sections of the filter while the remainder of the filter is in operation. | ||||||
| 186 | Ventilation/floating type reactor | JP32161887 | 1987-12-21 | JPS63166498A | 1988-07-09 | OVERATH HORST |
| An aeration/flotation reactor, of particular usefulness in the treatment of biomass-containing liquids, comprises a foam tube which terminates at the top in a collecting vessel and overlaps, or is inverted over, an inner rising tube which is preferably coaxial. The latter tube delimits an inlet chamber positioned, at the bottom of the foam tube, to receive liquid and finely divided gas bubbles. The lower end of the foam tube is enlarged, preferably into a funnel-shape, and runs into the lower region of an outer tube, the upper end of which is connected, via a return tube, to the inlet chamber below the axial rising tube. The outer tube, which is open at the top, is provided with a T-shaped liquid outlet having a dip connector, which extends below the liquid level, and with an outlet level immediately above the junction of the return tube, The upper end of the foam tube can be extended telescopically, thus permitting adaptation of the device to liquid/gas systems characterized by different foam properties. | ||||||
| 187 | Froth floating method and device | JP30884887 | 1987-12-08 | JPS63158143A | 1988-07-01 | JIEFURII ROOERU CHIENBAARIN; MIKAERU ANTONII MATSUKUURU |
| A method and several embodiments of apparatus are disclosed for use in foam flotation separation. The method discloses performing the separation in a module (12) operated at nonatmospheric pressure, and the apparatus disclosed are suitable for use as the module (12) of the method. Both the method and the apparatus contemplate positive and negative pressure operation. | ||||||
| 188 | Apparatus and method for foam flotation | JP27688986 | 1986-11-21 | JPS62129162A | 1987-06-11 | ARETSUKUSU ZENTORAZEROI; FURANSHISU JIEI MAKUDONERU; JIEEMUSU BUI DATSUTERA |
| Apparatus for froth flotation comprising a flotation tank having a series of cells separated by partitions but having a communicating common bottom sloped towards the feed end of the tank under all the cells. A method for froth flotation employing the novel apparatus is also disclosed. | ||||||
| 189 | JPS6143120B2 - | JP8243076 | 1976-07-10 | JPS6143120B2 | 1986-09-25 | FURANKU KOONERYUUSU ROESURAA |
| A solids-liquid mixture, such as waste water, containing biologically degradable material is treated in a circulatory system having alternating upward and downward flow kept in motion by injection of gas such as air. Mixture is diverted from the system into a separating chamber in which solids-enriched mixture is separated by flotation and/or sedimentation. A solids-rich mixture, preferably recycled from the separation chamber, is fed into the system hydrostatically and thereby the concentration of such solids in the system is maintained and/or such solids are transferred from one location to another without mechanical pumping. | ||||||
| 190 | Froth floatation apparatus and method | JP5774783 | 1983-04-01 | JPS58220886A | 1983-12-22 | RONARUDO DEII KURIYUUA; RARII DEII MAAKAMU; DERARUDO AARU HATSUTOSON; GUREGORII DEII KIIRU |
| A froth flotation apparatus for elimination of solid particle impurities contained within a liquid includes a vessel defining a flotation cell which includes an upstanding foam discharge conduit, an inlet conduit communicating with the vessel such that fluid flowing through the inlet conduit and into the vessel moves in a vortical fashion within the vessel, a skimmer, and a sparger. The skimmer consists of a generally cylindrical roller which is rotatably mounted between the discharge conduit and a side wall of the vessel and is buoyant so that it floats on the surface of the fluid within the vessel such that it is rotated by the vortical movement of the fluid within the vessel to prevent buildup of foam and maintain the motion of the fluid within the vessel. The sparger includes a substantially cylindrical porous element mounted on a tubular shaft which is rotatably mounted within the inlet conduit and driven by a motor. Compressed air is forced through the porous element to aerate the fluid entering the vessel. Two or more flotation cells may be arranged in a tower to provide series operation in which the liquid effluent of one cell flows downwardly by gravity into a subsequent cell, thereby eliminating the need for additional mechanical pumps. | ||||||
| 191 | Apparatus for selective floatation of substance | JP516583 | 1983-01-14 | JPS58180250A | 1983-10-21 | RICHIYAADO BAKUSUTAA UEBAA; ROBAATO HENRII FUOOSAISU |
| A flotation machine consists of a flotation chamber and a rotating gas diffuser. The flotation chamber has a lower mixing chamber and an upper quiescent zone for maximizing float accumulation. The rotating diffuser produces ultra fine bubbles as small as 50 microns in diameter. The size of the bubble diameter can be controlled and produced in any size from less than 50 microns to greater than 10 mm to enable flotation of various materials and/or various sized fractions of materials. The ultra fine bubbles are produced by the diffuser in the same size range as bubbles produced by dissolved air flotation, but without the necessity of pressurizing gas in a first tank followed by depressurizing in a second tank. Since the diffuser is located within the flotation chamber and can vary bubble size, it also provides the advantage of sparged air flotation. This rotating diffuser configuration is a low drag thin disc and, when combined with a specially designed flotation chamber, embodies a flotation machine which produces higher product yields over a wider range of feed size fractions utilizing significantly less energy. | ||||||
| 192 | Solid-liquid separation apparatus | JP15973882 | 1982-09-16 | JPS5884093A | 1983-05-20 | DEEBITSUDO ARUBAATO HAINZU; FURANKU KOONERIYUUSU ROESURAA; RICHIYAADO TOREBOO JIYOONZU |
| Solids-liquid separation, wherein a solids-liquid mixture containing dissolved oxygen-containing gas is circulated around a circulatory system comprising a downcomer and a riser, part of the mixture in the riser being introduced into a flotation chamber in which the hydrostatic pressure gradually decreases as the mixture flows upwards, with consequent release from solution of gas bubbles which carry solid particles to the top of the mixture. | ||||||
| 193 | Method and apparatus for purifying water by floatation and filtering | JP14937182 | 1982-08-30 | JPS5845785A | 1983-03-17 | MIROSU KUROFUTA |
| Apparatus and a method for removing suspended particles from water in a circular tank having a distribution and flocculation chamber immersed in the tank of water and carried circularly around the tank by a carriage. Flocculating material and inlet water are introduced into the body of water from the moving flocculating chamber at the same rate as clarified water is discharged through a filter substantially covering the bottom of the tank. A majority of particles in the water is collected by flocs in the water and floated to the water surface by air bubble action. The floating sludge is removed by a spiral scoop carried by the carriage. The water is then passed through the bottom filter which removes the remaining flocs completing the clarification of the water for discharge. Apparatus is provided for selectively back washing sections of the filter while the remainder of the filter is in operation. | ||||||
| 194 | Floatation separator for using used paper | JP12044682 | 1982-07-10 | JPS5817854A | 1983-02-02 | ROTAARU FUARUTSUAA; CHIEKOFUSUKII BERUNARU; MITSUTAAKU YURUGEN |
| In a flotation device for processing waste-paper, the flotation tank (1) is substantially in the form of an upright cylinder and the waste- paper suspension, mixed with air, is supplied to the flotation tank substantially tangentially and with a horizontal in-flow direction through a single supply line (6, 6') connected in the vicinity of the floor of the flotation tank (1) and having a diffuser widening portion (6) therein. The extraction line (3) for the cleaned suspension is provided near to the connection opening (2) of the supply line in the flotation tank (1), also in the region of the floor thereof. <IMAGE> | ||||||
| 195 | JPS5743679B2 - | JP1508179 | 1979-02-14 | JPS5743679B2 | 1982-09-16 | |
| Apparatus for de-inking waste paper pulp using a foam flotation process in which the deinked slurry is to be recycled for the production of paper. The old paper is pulped (slushed), mixed with water and flotation- and other chemicals, to produce a slurry which is introduced into the flotation tank. Movement of the slurry through the flotation tank is achieved by the positioning of one or more water injector nozzles with air inlets which causes a swirling rotation from the injector towards a central outlet. Froth or foam bubbles float to the surface of the slurry carrying ink particles. A baffle plate leads the floated froth or foam and ink particles to a vacuum actuated outlet. | ||||||
| 196 | JPS5717586B2 - | JP2404679 | 1979-03-03 | JPS5717586B2 | 1982-04-12 | |
| A flotator for use in benefication, coal dressing, wet refining and so forth, incorporating a surface flotation technic. The flotator has a funnel-shaped liquid cell having a bottom of an area smaller than that of the top opening. A bubbling device is constituted by an upper sleeve partly immersed in the liquid contained by the cell, a lower sleeve disposed coaxially with the upper sleeve and fully immersed in the liquid. The upper end of the lower sleeve is spaced by a predetermined distance from the lower end of the upper sleeve to form therebetween a spaced region located at a small depth from the liquid surface. The bubbling device further has a rotary blade unit constituted by upper and lower blades separated by a flat partition plate. The rotary blade unit is adapted to rotate around the common axis of the upper and lower sleeves, and has a thickness or axial height substantially equal to the aforementioned predetermined distance in the spaced region, and is located such that the flat partition plate is located at the heightwise mid point of the spaced region. The flotator further has a liquid surface stabilizer constituted by a frusto-conical member disposed around the bubbling device and adapted to deflect the liquid downwardly. Further, provided are a feeding passage having a feed gate opening in the bottom area of the cell and a discharging passage having a discharge gate spaced from both of the feed gate and the lower edge of the liquid surface stabilizer so as to avoid the "short-circuiting" of the liquid. | ||||||
| 197 | Separator | JP12482381 | 1981-08-11 | JPS5759652A | 1982-04-10 | 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. | ||||||
| 198 | Flotation method and its device | JP2999281 | 1981-03-04 | JPS56150444A | 1981-11-20 | MARUKO TSUROKARUNIKU |
| The present invention relates to an apparatus for flotation, wherein the mixture to be subjected to flotation is mixed with gas, preferably air, inside a flotation cell, in funnel-shaped nozzles in which a conical deflector is arranged in line with the axis of the propulsion jet. | ||||||
| 199 | JPS5622992B2 - | JP8781978 | 1978-07-20 | JPS5622992B2 | 1981-05-28 | |
| Apparatus for removing impurities entrapped in a suspension of fibrous material includes a fluidized bed chamber having opposite ends, a top wall, and a perforated bottom wall. An inlet feeds the suspension to be purified to a diffusing chamber which imparts laminar flow thereto and, in turn, feeds the suspension to the fluidized bed chamber through one end thereof for flow across the bottom wall toward the other end. A pressure chamber is positioned below the fluidized bed chamber and communicates with the bottom wall thereof, the pressure chamber having a plurality of walls thereacross dividing the same into a plurality of sections. A manifold has branches communicating with each section of the pressure chamber for introducing a fluidizing agent under pressure thereto for upward flow through the perforations in the bottom wall and through the suspension therein thereby to separate impurities from the suspension by flotation. A separation chamber has a forward end communicating the other end of the fluidized bed chamber for receiving the suspension therefrom and has top and bottom walls and a rear wall. A light impurities withdrawal conduit extends upwardly from the top wall of the separation chamber in the forward region thereof for removing separated impurities from the suspension which have relatively low specific gravity and float to the top thereof. A fibrous suspension withdrawal conduit extends from the rear upper region of the separation chamber for removing the purified fibrous suspension therefrom, and a heavy impurity withdrawal conduit extends from the lower region of the separation chamber for removing separated impurities from the suspension which have relatively high specific gravity and settle to the bottom wall of the separation chamber. | ||||||
| 200 | Flotation machine | JP2404679 | 1979-03-03 | JPS55116454A | 1980-09-08 | TAKAKUWA TAKESHI |
| PURPOSE: To enhance flotation capacity by using both-face blade rotary body to cause effective foaming and liquid surface stabilizer to stabilize liquid surface. CONSTITUTION: A rotary body 3 having blades 3b at lower and upper sides of partition plate 3c is concemtrically mounted in the upper and lower cylinders 2a, 2b. Multiple dispersers 5 are mounted on the periphery facing the rotary member 3. The outer periphery is installed with a liquid stabilizer 7. Air and liquid are mixed by rotation of the rotary body 3, are subjected to centrifugal force and divided into fine particles by the dispersers 5, are downwardly deflected by thr stabilizer 7, and jetted out without disturbing liquid surface. Liquid sucked from the lower cylinder 2b contains only a little bubbles, so that useless power due to bubbles is not used. Because liquid is supplied from the supply route 9, the liquid is not flowed from outlet route 10 without passing bubble section 6. COPYRIGHT: (C)1980,JPO&Japio | ||||||
QQ群二维码
意见反馈
意见反馈