CN2095706U - Settle extractor - Google Patents

Settle extractor Download PDF

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Publication number
CN2095706U
CN2095706U CN 90221366 CN90221366U CN2095706U CN 2095706 U CN2095706 U CN 2095706U CN 90221366 CN90221366 CN 90221366 CN 90221366 U CN90221366 U CN 90221366U CN 2095706 U CN2095706 U CN 2095706U
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CN
China
Prior art keywords
heavy phase
extractor
mutually
mixing chamber
pallet
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Granted
Application number
CN 90221366
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Chinese (zh)
Inventor
钟盛华
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Individual
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Individual
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Publication date
Application filed by Individual filed Critical Individual
Priority to CN 90221366 priority Critical patent/CN2095706U/en
Publication of CN2095706U publication Critical patent/CN2095706U/en
Granted legal-status Critical Current

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Abstract

The utility model relates to a settle extractor which is a mixing clarifying device used for liquid-liquid extraction. The utility model is characterized in that a clarifying chamber is arranged on the upper part of the extractor; a mixing chamber is positioned at the bottom of the extractor, one side of the mixing chamber is a channel interface region, and the top of the mixing chamber is provided with a tray which can keep heavy phase; a stirrer is a trapezoidal blade; the light and the heavy phases enter the mixing chamber from the top and the bottom of a hollow tubular shaft; the height of an interface adjusting plate in the heavy phase channel is equal to that of the heavy phase in the interface channel region. For the same workshop, the processing ability of the extractor is four times as large as that of the existing extractor. The storage of the organic phase and the metal is small, the flux is enhanced by about 2.5 times, and the fluctuation of the phase interface is small, which is favorable to the steady quality of the separated production. The utility model has high efficiency and low power consumption and is easy to control automatically.

Description

Settle extractor
The utility model is that a kind of mixing chamber occupies the bottom, and the clarifying chamber places the liquid-liquid extraction mixer-settler extractor on top.
Mixer-settler extractor is to use liquid-liquid extraction equipment very widely, the horizontal tandem arrangement in the mixing chamber of general horizontal mixer-settler extractor and clarifying chamber.Make the mixer-settler extractor floor space big like this, can not be than the space of good utilisation factory building, flux is little, organic facies, the water hold-up is big, produces substantial contribution and overstocks.Enter light, the heavy phase of mixing chamber, the employing that has enters from the mixing chamber bottom simultaneously, and it needs bigger suction force, and consume additional power is many.Have gently from the top, heavy phase enters mixing chamber from the bottom, mixes from the mixing chamber middle part to flow out, it is short in the mixing chamber time of staying that this method easily produces the part particle, and cause stage efficiency low.The employing that has is from top (Shang Xiangkou) gently, and (Xia Xiangkou) enters mixing chamber to heavy phase from the bottom.Heavy phase through mixing is taken mixing chamber out of by mixing to flow out from last phase mouth, and gently returns mixing chamber from last phase mouth after the phase-splitting, mixed from mouthful flowing out mutually down through gently communicating of mixing and take mixing chamber out of, and the heavy phase after the phase-splitting is returned mixing chamber again.Because light, heavy phase that already hybrid reaction is crossed are returned mixing chamber again again, cause mixing chamber, clarifying chamber's load to increase about 1 times, processing flux will be little like this, and perhaps stage efficiency reduces.Moreover weight boundary fluctuation has considerable influence to the product quality of extract and separate stable in the mixer-settler extractor.Existing mixer-settler extractor does not have fine addressing this problem.
The purpose of this utility model is will provide a kind of can utilize the factory building space, and floor space is little, but not too high again when equipment is large-scale, flux is big, and the stage efficiency height is easy to make, stable, the liquid-liquid extraction mixer-settler extractor that consume additional power is low.
Mixing chamber of the present utility model occupy the bottom of extractor, and the top of extractor is last clarifying chamber, and mixing chamber one side is other to be the Entry Interface district.Improve the horizontal tandem arrangement of mixing chamber and clarifying chamber in the past like this, floor space reduces at double, can utilize the factory building space.The utility model is because the clarifying chamber mainly on extractor top, so can make settling section be the thin layer phase-splitting, can dwindle the volume of clarification so greatly.The pallet that can keep heavy phase is arranged at mixing chamber of the present utility model top, and having realized like this has heavy phase and light interface mutually on extractor top, is beneficial to the clarification that mixes phase.Arrive the Entry Interface district and enter in this district's heavy phase at the heavy phase that this pallet is clarified out the pallet overfall that overflow.Under occasions such as some extraction system or specified conditions, the Entry Interface district of mixing chamber one side also can be used as settling section, carries out clarification mutually to mixing.This moment on pallet also not the mixing of the phase-splitting pallet overfall that also overflow mutually arrive the Entry Interface district and further clarify.Pallet has and mixes the tube outlet of phase garden, or and (one or several) rectangle mix mutually and export.Threaded in mixing phase garden tube exports, make outer movable threaded energy height up and down, rectangle is mixed outlet mutually the big or small portable plate of the outlet can regulated.
Weight of the present utility model is to enter mixing chamber so mutually, and the shaft hypomere is hollow pipe (claiming hollow tubular axis), has several holes (promptly gently portal mutually and heavy phase portal) at the hollow tubular axis in paddle place.Hollow tubular axis has several and gently enters the hole mutually above stirring vane.There is a little socket broad in the middle in two hollow tubular axis outside in this position, as gently sucking mutually every the tube of diving.Rotate when stirring, the suction force of agitator passes to by hollow tubular axis gently enters the hole mutually, is to make the suction force of gently entering the hole mutually can aspirate the light phase that will advance mixing chamber every latent effect.The light suction mutually every the tube of diving is communicated with light passage mutually.The lower ending opening of hollow tubular axis, and place the heavy out pipe.Hollow tubular axis lower ending opening rotates when stirring, in can suck heavy phase and stir.Weight of the present utility model enters mixing chamber mutually like this, needs less suction force, can not reduce stage efficiency simultaneously or reduce flux.Stirring vane shape of the present utility model is trapezoidal greatly, can be by two, and three, four or multi-disc composition agitator.Because agitator is big trapezoid blade, and major diameter is arranged, large tracts of land is so agitator upper and lower suction is less than gently advancing hole, heavy phase import mutually.Can stir under the slow-speed of revolution like this, peptizaiton is evenly distributed, avoid the meticulous phenomenon of drop to produce, power consumption is low.The mass-transfer efficiency height.
The weight boundary of the utility model extractor is control like this, have in the heavy phase channels of settling section upper end and the adjacent level aperture of intercommunication (hole on the phase of the weighing passage) mutually, adjacent level gently is on good terms to flow in the heavy phase channels, because the light boundary height of adjacent level equates, thus in the heavy phase channels light phase liquid level gently liquid level is similar mutually with this level.The heavy phase height in heavy phase height and Entry Interface district is suitable in the heavy phase channels like this, and dividing plate and interface adjustable plate are arranged in the heavy phase channels.When heavy phase was higher than the interface adjustable plate in the Entry Interface district, the heavy phase in the heavy phase channels also was higher than the interface adjustable plate, and the heavy phase interface adjustable plate that can overflow flows to next stage like this.When the adjustable plate of the low interface of heavy phase in the Entry Interface district, heavy phase in the heavy phase channels also is lower than the interface adjustable plate, the heavy phase interface adjustable plate that can not overflow, because next stage has suction force to heavy phase channels, heavy phase height in the dividing plate will descend, light also decline mutually in the heavy phase channels like this, because hole on the heavy phase channels is arranged, adjacent levels gently adds in the heavy phase channels by this hole, make in the heavy phase channels light light highly quite mutually with this level all the time mutually, the heavy phase height in the heavy phase channels can not raise because heavy phase decline in the dividing plate like this.If next stage is too big to heavy phase suction force in the heavy phase channels dividing plate, to cause in the dividing plate heavy phase to suck and further aspirate light phase.Can pass through to change conditions such as stirring in this case, and/or regulate the heavy phase traffic controller and aligned.The utility model carries out like this, and the fluctuation of weight boundary is little, and the heavy phase of inter-stage is steadily flowed uniformly, and stage efficiency is steady, is beneficial to the products of separated steady quality.Reduced the suction force of next stage simultaneously to this grade heavy phase.In like manner also reduce the suction force to the upper level heavy phase at the corresponding levels, thereby reduced power consumption.
The utility model is to realize like this, when being used for the liquid-liquid extraction, after agitator rotates, the suction force of agitator passes to by hollow tubular axis gently enters the hole mutually, since every the existence of the tube of diving make easily light phase on the lenient side the phase passage through entering stirring every the tube of diving, hollow tubular axis, hybrid reaction in mixing chamber, heavy phase is under the suction force effect of agitator, from heavy phase channels, enter through heavy phase inlet tube, hollow tubular axis and to be stirred in hybrid reaction in the mixing chamber.Mix from mixing the tube outlet of phase garden, or/and mix outlet mutually from rectangle, flow in the pallet on the mixing chamber top and clarify, mix the portable plate of outlet mutually by regulating rectangle, and/or the garden tube mixes the movable tube high and low position of outlet mutually, can control the size of mixing the phase export volume.The heavy phase of clarifying on the pallet (the perhaps same not mixing phase of phase-splitting), the pallet overfall that overflow arrives Entry Interface district (or further clarification).Pallet heavy phase overfall has the overfall adjustable plate, regulates this plate and can control pallet weighed boundary height.Light phase after clarification phase passage on the lenient side flows in upper level (or next stage) mixing chamber, and the heavy phase after the clarification flows to the mixing chamber of next stage (or upper level) from the heavy phase channels interface adjustable plate that overflow.
The utility model is described in further detail below in conjunction with accompanying drawing:
Fig. 1, be this mixer-settler extractor level Four master TV structure schematic diagram
Fig. 2, be that this mixer-settler extractor level Four is overlooked the sectional structure schematic diagram
Fig. 3, be this mixer-settler extractor side-looking sectional structure schematic diagram
Fig. 4, be gently the sucking mutually of this mixer-settler extractor every the tube cutaway view of diving
Fig. 5, be that two dimension tilt to be placed porose corrugated plating stereogram above the pallet
Fig. 6, be two layers of pallet stereogram
Fig. 7, be threaded garden tube passage in the heavy phase channels, adjustable pipe, flow-control lid cutaway view.
Among the figure:
1, shaft; 2, heavy phase channels; 3, interface adjusting knob; 4, heavy phase flow-control knob; 5, hole on the heavy phase channels; 6, mix the tube outlet of phase garden; 7, hollow tubular axis; 8, the movable tube of band external screw thread; 9, pallet; 10, light phase passage; 11, pallet overfall adjustable plate; 12, pallet overfall; 13, heavy out joint; 14, gently suck mutually every the tube of diving; 15, gently enter the hole mutually; 16, heavy phase inlet tube; 17, hollow tubular axis lower ending opening (heavy phase import); 18, light, heavy phase is portalled; 19, trapezoid blade; 20, dividing plate; 21, interface adjustable plate; 22, heavy phase traffic controller; 23, rectangle is mixed outlet mutually; 24, heavy phase inlet union; 25, mixing exports portable plate mutually; 26, obstruct plate; 27, go up the clarifying chamber; 28, Entry Interface district; 29, every the tube movable part of diving; 30, heavy phase flow-control lid; 31, the heavy phase import of flow-control lid; 32, threaded interface adjustable pipe; 33, threaded garden tube passage; 34, obstruct plate on the movable tray; 35, second layer pallet; 36, ground floor pallet; 37, second layer pallet overfall; 38, mixing exports the garden tube mutually; 39, heavy phase flows down direction in the two-dimentional inclination corrugated plating trough groove; 40, perforate on the corrugated plating; 41, light phase upstream direction in the two-dimentional inclination corrugated plating crest groove; 42, mixing chamber.
Pallet 9 can be made the activity pattern, also can make fixing.Movable pallet 9 can be taken out, and puts into extractor, around this kind situation mixing chamber top frame is arranged, and prevents to mix the phase earial drainage and comes out.The mixing that can design pallet exports mutually and can allow agitator conveniently pass in and out mixing chamber, also can make agitator turnover mixing chamber by the activity of pallet 9.Divide phase system and other factor for difficulty, can be above the weight phase interface of pallet, two dimension tilts to place one or more layers corrugated plating, to help clarification and to prevent disturbance, there is a rows of openings at the middle part of every groove of this corrugated plating, to pass through to mix phase, the heavy phase of clarifying in the trough groove is gone to (39) below the low end of groove flows to, that clarifies in the crest groove gently goes above the higher end of groove flows to.Fig. 5.Divide phase system and other factor also can on pallet, put into one deck for difficulty, two layers, or the multilayer pallet, Fig. 2 is a stereogram of putting one deck on pallet again.Upper layer pallet overfall position and following surface layer pallet overfall position relative edge.Gently suck mutually every the tube of diving, the movable part 29 that can conveniently extract out is arranged, its activity can make hollow tubular axis enter in the tube of diving.Interface adjustable plate in the heavy phase channels, the heavy phase traffic controller can be regulated by interface adjusting knob 3 and heavy phase flow-control knob 4 respectively.Dividing plate in the heavy phase channels, interface adjustable plate and heavy phase traffic controller can adopt threaded garden tube passage 33, and threaded interface adjustable pipe 32 and threaded heavy phase flow-control lid 30 replace Fig. 7.Adjustable pipe 32 height in threaded interface are few with this grade extractor Entry Interface district heavy phase difference in height, and its transfer up and down can be regulated this grade Entry Interface district weight boundary height.The turn of threaded heavy phase flow-control lid 30 can be controlled the heavy phase flow.
The utility model can use separately, also can plural serial stage or other connecting mode use, also multistage mixer-settler extractor can be formed an integral body, constitute Box Mixer-settler, if progression reaches tens or hundreds of level, can form a box assembly to some grades, carry out the connection of many assemblys again with pipeline, it can be poly (methyl methacrylate) plate, plastic plate, various metallic plate or other material that the utility model is made material.
The utility model and existing mixer-settler extractor relatively can utilize the factory building space, and floor space is little, but again not too high when equipment is large-scale. The utility model floor space only need have about 20% of mixer-settler extractor now, organic phase and the metal amount of stockpiling are little, reduce great amount of investment, reducing substantial contribution overstocks, with the volume treating capacity than about 2.5 times of existing raisings, stage efficiency height (greater than 95%) power consumption is low, and weights at different levels flow steadily mutually, is conducive to the stable of products of separated quality, the stream that is suitable for is bigger than scope, be easy to automatically control, contain volatile materials for heavy phase, be difficult for exposing the outside with this extractor heavy phase, can greatly reduce volatile materials escapes, this extractor is used in the example hydrochloric acid back extraction, and hydrochloric acid escapes and greatly reduces.
The utility model can be used for non-ferrous metal, noble metal, heavy metal, the solvent extraction and separation in the fields such as antibiotic. Particularly be applicable to Rare Earth Separation industry. Especially take organic phase as continuous phase, the more extraction system of progression.

Claims (9)

1, a kind of clarification extractor of putting, by mixing chamber, the clarifying chamber, compositions such as agitator is characterized in that:
A, mixing chamber 42 occupy the extractor bottom, and its extractor top is last clarifying chamber 27, and mixing chamber one side is other to be Entry Interface district 28;
B, mixing chamber have the pallet 9 that can keep heavy phase to little one deck on 42 tops, and heavy phase and light interface are mutually arranged at extractor top like this, are beneficial to mixing and clarify mutually;
C, shaft hypomere are hollow tubular axis 7, and agitator is a trapezoid blade 19, are made up of two or three or multi-disc; The place opens several light phases, heavy phase and portals 18 (promptly gently portal mutually and heavy phase is portalled) in the blade of hollow tubular axis; Also open several at the hollow tubular axis in blade top and gently enter hole 15 mutually, this hole is located to have and is gently sucked mutually every the tube 14 of diving; Hollow pipe lower ending opening 17, and place among the heavy phase inlet tube 16;
D, heavy phase channels 2, upper end have hole 5 on the heavy phase channels with the light intercommunication mutually of adjacent level; Dividing plate 20 in the heavy phase channels, and the heavy phase interfacial level is suitable in the Entry Interface district of the height of interface adjustable plate 21 and this extractor; Have above the heavy phase in the heavy phase channels gently to exist mutually, in the heavy phase channels heavy phase traffic controller 22 can be arranged.
2, the clarification extractor of putting according to claim 1 is characterized in that by said mixing chamber one side, and under difficult phase-splitting extraction system or other situation, mixing chamber one side is other to be the other settling section of side.
3, the clarification extractor of putting according to claim 1 is characterized in that having on the said pallet 9 the garden tube to mix and exports 6 mutually, also can have one or several rectangles to mix simultaneously and export 23 mutually; Garden tube mixing exports the threaded outer threaded activity 8 energy height up and down that make in 6 mutually; Rectangle is mixed and to be exported 23 mutually and have and can regulate this mixings and export big or small portable plate 25 mutually; The overfall adjustable plate 11 that can regulate this pallet weighed boundary height is arranged on the pallet 9.
4, the clarification extractor of putting according to claim 1 is characterized in that said pallet 9, the activity of can making, can conveniently take out, put into extractor, around the mixing chamber top frame is arranged, prevent to mix the phase earial drainage to the clarifying chamber.
5, the clarification extractor of putting according to claim 1 is characterized in that said pallet 9, also can make fixing.
6, the clarification extractor of putting according to claim 1 is characterized in that keeping can also placing above the pallet 9 of heavy phase the pallet that one deck, two layers or multilayer can keep heavy phase, to help clarification; The superiors obstruct plate 34.
7, the clarification extractor of putting according to claim 1 is characterized in that keeping above the pallet of heavy phase, also can two dimension tilt to place one or more layers porose corrugated plating, to help clarification.With prevent disturbance.
8, the clarification extractor of putting according to claim 1 is characterized in that saidly gently inhaling the people mutually every the tube 14 of diving, and has and can activity take out out part 29, so that shaft can be put into every the tube of diving.
9, the clarification extractor of putting according to claim 1 is characterized in that the heavy phase channels inner boundary is regulated and flow-control can be adopted threaded garden tube passage 33, threaded interface adjustable pipe 32,30 replacements of threaded heavy phase flow-control lid.
CN 90221366 1990-09-25 1990-09-25 Settle extractor Granted CN2095706U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 90221366 CN2095706U (en) 1990-09-25 1990-09-25 Settle extractor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 90221366 CN2095706U (en) 1990-09-25 1990-09-25 Settle extractor

Publications (1)

Publication Number Publication Date
CN2095706U true CN2095706U (en) 1992-02-12

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ID=4899511

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 90221366 Granted CN2095706U (en) 1990-09-25 1990-09-25 Settle extractor

Country Status (1)

Country Link
CN (1) CN2095706U (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102277493A (en) * 2011-08-04 2011-12-14 陆文光 Method for extracting rare earth elements and rare earth extraction system
CN101708382B (en) * 2009-12-07 2012-10-03 昆明冶金研究院 Extraction and back-extraction device
CN102936664A (en) * 2011-08-04 2013-02-20 陆文光 Method for extracting rare earth elements and rare earth extraction system
CN103657143A (en) * 2013-12-18 2014-03-26 河北新启元能源技术开发股份有限公司 Novel extraction device
CN108031148A (en) * 2017-12-08 2018-05-15 中国科学院力学研究所 A kind of gas-liquid separation device and application

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101708382B (en) * 2009-12-07 2012-10-03 昆明冶金研究院 Extraction and back-extraction device
CN102277493A (en) * 2011-08-04 2011-12-14 陆文光 Method for extracting rare earth elements and rare earth extraction system
CN102277493B (en) * 2011-08-04 2013-01-23 陆文光 Method for extracting rare earth elements and rare earth extraction system
CN102936664A (en) * 2011-08-04 2013-02-20 陆文光 Method for extracting rare earth elements and rare earth extraction system
CN102936664B (en) * 2011-08-04 2014-02-19 陆文光 Method for extracting rare earth elements
CN103657143A (en) * 2013-12-18 2014-03-26 河北新启元能源技术开发股份有限公司 Novel extraction device
CN108031148A (en) * 2017-12-08 2018-05-15 中国科学院力学研究所 A kind of gas-liquid separation device and application

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