CN104941246B - A kind of percussion flow hypergravity liquid-liquid extraction device - Google Patents

A kind of percussion flow hypergravity liquid-liquid extraction device Download PDF

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Publication number
CN104941246B
CN104941246B CN201510189596.9A CN201510189596A CN104941246B CN 104941246 B CN104941246 B CN 104941246B CN 201510189596 A CN201510189596 A CN 201510189596A CN 104941246 B CN104941246 B CN 104941246B
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China
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liquid
rotating shaft
porous plate
spiral
extraction
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CN201510189596.9A
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Chinese (zh)
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CN104941246A (en
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杜奕
常军
彭金辉
张利波
丁家满
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昆明理工大学
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Abstract

The present invention relates to a kind of percussion flow hypergravity liquid-liquid extraction device, belong to chemical industry and technical field of metallurgical equipment.This percussion flow hypergravity liquid-liquid extraction device, including power transmission structure, liquid header mechanism, pivot structure, liquid mass transfer structure and fixing element structure, power transmission structure is the Poewr transmission mechanism that upper and lower two sets are symmetrical, extraction liquids is sprayed into liquid header mechanism, extraction liquids is in pivot structure and liquid mass transfer structure is detained and in disorderly head-on collision state, flows out after completing extraction from this extractor.This extractor uses Dual-motors Driving, adds the mass transport process of the adjustable parameter of hypergravity extraction reactor, the negative pressure of eddy current baffle plate generation and the common prolonged action of cone cylinder porous plate mixing liquid, increases mass transfer area.

Description

A kind of percussion flow hypergravity liquid-liquid extraction device

Technical field

The present invention relates to a kind of percussion flow hypergravity liquid-liquid extraction device, belong to chemical industry and technical field of metallurgical equipment.

Background technology

Hypergravity slewing is a kind of novel device risen the beginning of the eighties in last century.Compared with traditional equipment, having mass-transfer efficiency high, equipment volume is little, and floor space is little, and liquid utilization rate is high, the advantages such as energy consumption is low.General super gravity field slewing is made up of casing, rotor, material inlet, material outlet, rotating shaft and motor, but the most common rotor is all the filler rotor of concentric groove, and the wire packing area needed is big, easily causes the waste of material, overhauls and safeguard inconvenience.

nullChinese patent database has some patent applications belonging to super gravity field reaction method or consersion unit,Such as No. 91109255.2 " rotating bed super gravity field strengthening transmission and reaction unit "、No. 91229204.0 " rotating bed super gravity field transmission and reaction unit "、Number 99105437.7 " eddy-current ultragravitational field reactor and application thereof "、99200696.1 number " super gravity field mass transfer、Reaction unit "、Number 99208429.6 " pneumatic eddy-current ultragravitational field reactor "、No. 01143459.7 " super gravity field mesohigh revolving bed gas-liquid mass transfer and consersion unit "、Number 200310103434.6 " a kind of hypergravity field swinging bed mass transfer and consersion unit "、No. 200410073624.2 " a kind of method carrying out catalytic reaction in super gravity field "、No. 02224172.8 " rotating bed super gravity heterophase reactor " etc..But the hypergravity equipment development currently for liquid-liquid extraction is less.

Summary of the invention

The problem existed for above-mentioned prior art and deficiency, the present invention provides a kind of percussion flow hypergravity liquid-liquid extraction device.This extractor uses Dual-motors Driving, add the adjustable parameter of hypergravity extraction reactor, negative pressure that eddy current baffle plate produces and the mass transport process of the common prolonged action mixing liquid of cone cylinder porous plate, increase mass transfer area, and the present invention is achieved through the following technical solutions.

nullA kind of percussion flow hypergravity liquid-liquid extraction device,Including power transmission structure、Liquid header mechanism、Pivot structure、Liquid mass transfer structure and fixing element structure,Power transmission structure is the Poewr transmission mechanism that upper and lower two sets are symmetrical,Liquid header mechanism includes water nozzle 2、Liquid header end cap 3、Liquid header 4 and lip-type packing 5,Liquid header mechanism is upper and lower two set symmetrical structures,Pivot structure includes bearing 6、Bearing block 7 and rotating shaft,Pivot structure is upper and lower two set symmetrical structures,Rotating shaft is divided into laterally zygomorphic upper rotating shaft 13 and lower rotary shaft 19 according to position,Liquid mass transfer structure includes rotating shaft spiral porous plate 14、Cone cylinder porous plate 15、Eddy current baffle plate 16、Shower 17、Lower rotary shaft spiral porous plate 18、Spiral stream guidance groove 20 and liquid outlet 22,Fixing element structure includes frame 8 and housing 21;

Fixing housing 21 in described fixing element structure in frame 8, external motor 1 imparts power to rotating shaft by the synchronous pulley 9 of power transmission structure;

Described pivot structure shaft is fixed in frame 8 by bearing 6 and bearing block 7, bearing block 7 is fixed in frame 8 by screw attachment, and bearing 6 inner ring coordinates with rotating shaft, and outer ring coordinates with bearing block 7, it is internal that rotating shaft is inserted perpendicularly into housing 21 from centre position, and rotating shaft is hollow axle;

In described liquid header mechanism, water nozzle 2 is fixed on liquid header end cap 3 top by inner and outer pipes threaded engagement, catcher end cap 3 and liquid header 4 matched in clearance, catcher end cap 3 is fixed on liquid header 4 by screw attachment, liquid header 4 is connected with rotating shaft by lip-type packing 5, lip-type packing 5 inner ring coordinates with rotating shaft, and outer ring coordinates with the inner chamber of liquid header 4;

In described liquid mass transfer structure, upper rotating shaft spiral porous plate 14 is fixed on upper rotating shaft 13 bottom by screw attachment, cone cylinder porous plate 15 is fixed on rotating shaft spiral porous plate 14 lower surface, cone cylinder porous plate 15 surface uniform welding eddy current baffle plate 16, the hollow mouth of rotating shaft is connected with shower 17 entrance, shower 17 is fixed in rotating shaft by internal and external threads cooperation, lower rotary shaft spiral porous plate 18 is fixed by screw attachment in lower rotary shaft 19 upper end, spiral stream guidance groove 20 is fixed on housing 21 interior bottom portion by screw attachment, and housing 21 bottom is provided with liquid outlet 22.

Described rotating shaft is the multidiameter of flanged dish, and the uniform through hole for thread connection on ring flange, bottom rotating shaft, bore design is the female thread matched with shower 17.

The tapering of described cone cylinder porous plate 15 is 2o~5o, cone cylinder porous plate 15 is the corrosion resistant plate of thickness 1 ~ 2mm, and cone cylinder porous plate 15 surface is uniformly distributed the micropore of a diameter of 1 ~ 2mm.

Described eddy current baffle plate 16 is 3 ~ 6 pieces, is shaped as right-angled trapezium.

Described upper rotating shaft spiral porous plate 14, lower rotary shaft spiral porous plate 18 are the corrosion resistant plate of thickness 2 ~ 4mm, being evenly distributed with the micropore of a diameter of 1 ~ 2mm on stainless steel, upper rotating shaft spiral porous plate 14, the inner side and outer side of lower rotary shaft spiral porous plate 18 are all welded with spiral type rustless steel rib.

Described spiral stream guidance groove 20 is made up of the dividing plate raised the most successively, and the distribution of dividing plate uses spiral of Archimedes to be evenly distributed.

The motor 1 of this percussion flow hypergravity liquid-liquid extraction device upper part described stops operating, and only regulates the motor 1 of lower part, and this percussion flow hypergravity liquid-liquid extraction device is converted into sound disc type baffling supergravity reactor.

When apparatus of the present invention use, open upper and lower two motor 1 power supplys simultaneously, upper rotating shaft 13 and the rotating speed of lower rotary shaft 19 and direction of rotation can be regulated respectively by the mode of connection of frequency modulator and power supply.Regulated pressure and the flow velocity of biphase liquid by magnetic drive pump and glass rotameter after, by biphase liquid respectively by upper and lower water nozzle 2, enter in the cavity of liquid header 4, although upper rotating shaft 13 is in rotation status, but the liquid constantly sprayed into liquid header 4 will pour in the hollow channel of upper rotating shaft 13, and is outwards sprayed by shower 17.After biphase liquid achieves adverse current head-on collision respectively after upper and lower two showers ejection, to outwards spray, run into the cone cylinder porous plate 15 and eddy current baffle plate 16 rotated together with along with upper rotating shaft 13, under the barrier effect of eddy current baffle plate 16, mixing liquid is detained being in cone cylinder porous plate 15 and in disorderly head-on collision state, and the tapering of cone cylinder is conducive to the delay of liquid longer time.After mixing liquid passes the aperture of cone cylinder porous plate 15, spray to lower rotary shaft spiral porous plate 18 under the influence of centrifugal force, under the different rotating speeds of lower rotary shaft spiral porous plate 18 and the common effect of spiral rib that is distributed in internal and external walls, mixing liquid will be between cone cylinder porous plate 15 and lower rotary shaft spiral porous plate 18 and be detained and disorderly head-on collision state.After mixing liquid passes the aperture of lower rotary shaft spiral porous plate 18, spray to rotating shaft spiral porous plate 14 under the influence of centrifugal force, under the different rotating speeds of upper rotating shaft spiral porous plate 14 and the common effect of spiral rib that is distributed in internal and external walls, mixing liquid will be between upper rotating shaft spiral porous plate 14 and lower rotary shaft spiral porous plate 18 and be detained and disorderly head-on collision state.After mixing liquid passes the aperture of upper rotating shaft spiral porous plate 14, spray is fixed on housing 21 on actionless spiral stream guidance groove 20 under the influence of centrifugal force, after the baffling passage of spiral stream guidance groove 20, to be deposited on bottom the inwall of housing 21, by liquid outlet 22, flow out to the outside of housing 21.

In reactor, the material of each parts is corrosion resistant rustless steel.In all porous plates, the spacing between the size of hole diameter and aperture need to determine with character according to concrete liquid viscosity.

The invention has the beneficial effects as follows: 1, Dual-motors Driving, add the adjustable parameter of hypergravity extraction reactor;2, biphase liquid achieves adverse current head-on collision effect through shower ejection, improves and mixes mass-transfer efficiency for the first time;3, eddy current baffle plate produces negative pressure and the mass transport process of the common prolonged action mixing liquid of cone cylinder porous plate, increase mass transfer area;4, the upper microcellular structure of lower rotary shaft spiral porous plate and the internal and external screw rib of band spiral change the movement locus of mixing liquid, increase mass transfer area, extend the response time, improve mass transfer effect;5, the spiral of Archimedes structure of spiral stream guidance groove extends the mixing liquid holdup time at reactor.6, the employing of porous plate avoids the clogging that conventional filler is likely to occur.

Accompanying drawing explanation

Fig. 1 is percussion flow hypergravity liquid-liquid extraction device structural representation of the present invention;

Fig. 2 is the motor of percussion flow hypergravity liquid-liquid extraction device of the present invention, housing and supporting structure schematic diagram;

Fig. 3 is the liquid header mechanism structure schematic diagram of percussion flow hypergravity liquid-liquid extraction device of the present invention;

Fig. 4 is the upper pivot structure schematic diagram of percussion flow hypergravity liquid-liquid extraction device of the present invention;

Fig. 5 is the upper rotating shaft schematic top plan view of percussion flow hypergravity liquid-liquid extraction device of the present invention;

Fig. 6 is cone cylinder porous plate and the eddy current baffle plate schematic diagram that jet flow of the present invention clashes into hypergravity liquid-liquid extraction device;

Fig. 7 is cone cylinder porous plate and the eddy current baffle plate schematic top plan view that jet flow of the present invention clashes into hypergravity liquid-liquid extraction device;

Fig. 8 is the lower rotary shaft spiral porous plate schematic diagram that jet flow of the present invention clashes into hypergravity liquid-liquid extraction device;

Fig. 9 is the upper rotating shaft spiral porous plate schematic diagram that jet flow of the present invention clashes into hypergravity liquid-liquid extraction device;

Figure 10 is the Archimedian screw guiding gutter schematic diagram A that jet flow of the present invention clashes into hypergravity liquid-liquid extraction device;

Figure 11 is the Archimedian screw guiding gutter schematic diagram B that jet flow of the present invention clashes into hypergravity liquid-liquid extraction device;

In figure: 1-motor, 2-water nozzle, 3-liquid header end cap, 4-liquid header, 5-lip-type packing, 6-bearing, 7-bearing block, 8-frame, 9-synchronous pulley, 10-housing end plug, 11-self-aligning bearing, 12-housing cover, the upper rotating shaft of 13-, 14-upper rotating shaft spiral porous plate, 15-cone cylinder porous plate, 16-eddy current baffle plate, 17-shower, 18-lower rotary shaft spiral porous plate, 19-lower rotary shaft, 20-spiral stream guidance groove, 21-housing, 22-liquid outlet.

Detailed description of the invention

Below in conjunction with the accompanying drawings and detailed description of the invention, the invention will be further described.

Embodiment 1

nullIf Fig. 1 is to shown in 11,This percussion flow hypergravity liquid-liquid extraction device,Including power transmission structure、Liquid header mechanism、Pivot structure、Liquid mass transfer structure and fixing element structure,Power transmission structure is the Poewr transmission mechanism that upper and lower two sets are symmetrical,Liquid header mechanism includes water nozzle 2、Liquid header end cap 3、Liquid header 4 and lip-type packing 5,Liquid header mechanism is upper and lower two set symmetrical structures,Pivot structure includes bearing 6、Bearing block 7 and rotating shaft,Pivot structure is upper and lower two set symmetrical structures,Rotating shaft is divided into laterally zygomorphic upper rotating shaft 13 and lower rotary shaft 19 according to position,Liquid mass transfer structure includes rotating shaft spiral porous plate 14、Cone cylinder porous plate 15、Eddy current baffle plate 16、Shower 17、Lower rotary shaft spiral porous plate 18、Spiral stream guidance groove 20 and liquid outlet 22,Fixing element structure includes frame 8 and housing 21;

Fixing housing 21 in described fixing element structure in frame 8, external motor 1 imparts power to rotating shaft by the synchronous pulley 9 of power transmission structure;

Described pivot structure shaft is fixed in frame 8 by bearing 6 and bearing block 7, bearing block 7 is fixed in frame 8 by screw attachment, and bearing 6 inner ring coordinates with rotating shaft, and outer ring coordinates with bearing block 7, it is internal that rotating shaft is inserted perpendicularly into housing 21 from centre position, and rotating shaft is hollow axle;

In described liquid header mechanism, water nozzle 2 is fixed on liquid header end cap 3 top by inner and outer pipes threaded engagement, catcher end cap 3 and liquid header 4 matched in clearance, catcher end cap 3 is fixed on liquid header 4 by screw attachment, liquid header 4 is connected with rotating shaft by lip-type packing 5, lip-type packing 5 inner ring coordinates with rotating shaft, and outer ring coordinates with the inner chamber of liquid header 4;

In described liquid mass transfer structure, upper rotating shaft spiral porous plate 14 is fixed on upper rotating shaft 13 bottom by screw attachment, fixing upper rotating shaft spiral porous plate 14 lower surface of cone cylinder porous plate 15, cone cylinder porous plate 15 surface uniform welding eddy current baffle plate 16, the hollow mouth of rotating shaft is connected with shower 17 entrance, shower 17 is fixed in rotating shaft by internal and external threads cooperation, lower rotary shaft spiral porous plate 18 is fixed by screw attachment in lower rotary shaft 19 upper end, spiral stream guidance groove 20 is fixed on housing 21 interior bottom portion by screw attachment, and housing 21 bottom is provided with liquid outlet 22.

Its shaft is the multidiameter of flanged dish, and the uniform through hole for thread connection on ring flange, bottom rotating shaft, bore design is the female thread matched with shower 17;The tapering of cone cylinder porous plate 15 is 2o, cone cylinder porous plate 15 is the corrosion resistant plate of thickness 1mm, and cone cylinder porous plate 15 surface is uniformly distributed the micropore of a diameter of 1mm;Described eddy current baffle plate 16 is 3 ~ 6 pieces, is shaped as right-angled trapezium;Described upper rotating shaft spiral porous plate 14, lower rotary shaft spiral porous plate 18 are the corrosion resistant plate of thickness 2mm, being evenly distributed with the micropore of a diameter of 1mm on stainless steel, upper rotating shaft spiral porous plate 14, the inner side and outer side of lower rotary shaft spiral porous plate 18 are all welded with spiral type rustless steel rib;Spiral stream guidance groove 20 is made up of the dividing plate raised the most successively, and the distribution of dividing plate uses spiral of Archimedes to be evenly distributed.

Embodiment 2

nullIf Fig. 1 is to shown in 11,This percussion flow hypergravity liquid-liquid extraction device,Including power transmission structure、Liquid header mechanism、Pivot structure、Liquid mass transfer structure and fixing element structure,Power transmission structure is the Poewr transmission mechanism that upper and lower two sets are symmetrical,Liquid header mechanism includes water nozzle 2、Liquid header end cap 3、Liquid header 4 and lip-type packing 5,Liquid header mechanism is upper and lower two set symmetrical structures,Pivot structure includes bearing 6、Bearing block 7 and rotating shaft,Pivot structure is upper and lower two set symmetrical structures,Rotating shaft is divided into laterally zygomorphic upper rotating shaft 13 and lower rotary shaft 19 according to position,Liquid mass transfer structure includes rotating shaft spiral porous plate 14、Cone cylinder porous plate 15、Eddy current baffle plate 16、Shower 17、Lower rotary shaft spiral porous plate 18、Spiral stream guidance groove 20 and liquid outlet 22,Fixing element structure includes frame 8 and housing 21;

Fixing housing 21 in described fixing element structure in frame 8, external motor 1 imparts power to rotating shaft by the synchronous pulley 9 of power transmission structure;

Described pivot structure shaft is fixed in frame 8 by bearing 6 and bearing block 7, bearing block 7 is fixed in frame 8 by screw attachment, and bearing 6 inner ring coordinates with rotating shaft, and outer ring coordinates with bearing block 7, it is internal that rotating shaft is inserted perpendicularly into housing 21 from centre position, and rotating shaft is hollow axle;

In described liquid header mechanism, water nozzle 2 is fixed on liquid header end cap 3 top by inner and outer pipes threaded engagement, catcher end cap 3 and liquid header 4 matched in clearance, catcher end cap 3 is fixed on liquid header 4 by screw attachment, liquid header 4 is connected with rotating shaft by lip-type packing 5, lip-type packing 5 inner ring coordinates with rotating shaft, and outer ring coordinates with the inner chamber of liquid header 4;

In described liquid mass transfer structure, upper rotating shaft spiral porous plate 14 is fixed on upper rotating shaft 13 bottom by screw attachment, fixing upper rotating shaft spiral porous plate 14 lower surface of cone cylinder porous plate 15, cone cylinder porous plate 15 surface uniform welding eddy current baffle plate 16, the hollow mouth of rotating shaft is connected with shower 17 entrance, shower 17 is fixed in rotating shaft by internal and external threads cooperation, lower rotary shaft spiral porous plate 18 is fixed by screw attachment in lower rotary shaft 19 upper end, spiral stream guidance groove 20 is fixed on housing 21 interior bottom portion by screw attachment, and housing 21 bottom is provided with liquid outlet 22.

Its shaft is the multidiameter of flanged dish, and the uniform through hole for thread connection on ring flange, bottom rotating shaft, bore design is the female thread matched with shower 17;The tapering of cone cylinder porous plate 15 is 5o, cone cylinder porous plate 15 is the corrosion resistant plate of thickness 2mm, and cone cylinder porous plate 15 surface is uniformly distributed the micropore of a diameter of 2mm;Described eddy current baffle plate 16 is 6 ~ 8 pieces, is shaped as right-angled trapezium;Described upper rotating shaft spiral porous plate 14, lower rotary shaft spiral porous plate 18 are the corrosion resistant plate of thickness 3mm, being evenly distributed with the micropore of a diameter of 2mm on stainless steel, upper rotating shaft spiral porous plate 14, the inner side and outer side of lower rotary shaft spiral porous plate 18 are all welded with spiral type rustless steel rib;Spiral stream guidance groove 20 is made up of the dividing plate raised the most successively, and the distribution of dividing plate uses spiral of Archimedes to be evenly distributed.

Embodiment 3

nullIf Fig. 1 is to shown in 11,This percussion flow hypergravity liquid-liquid extraction device,Including power transmission structure、Liquid header mechanism、Pivot structure、Liquid mass transfer structure and fixing element structure,Power transmission structure is the Poewr transmission mechanism that upper and lower two sets are symmetrical,Liquid header mechanism includes water nozzle 2、Liquid header end cap 3、Liquid header 4 and lip-type packing 5,Liquid header mechanism is upper and lower two set symmetrical structures,Pivot structure includes bearing 6、Bearing block 7 and rotating shaft,Pivot structure is upper and lower two set symmetrical structures,Rotating shaft is divided into laterally zygomorphic upper rotating shaft 13 and lower rotary shaft 19 according to position,Liquid mass transfer structure includes rotating shaft spiral porous plate 14、Cone cylinder porous plate 15、Eddy current baffle plate 16、Shower 17、Lower rotary shaft spiral porous plate 18、Spiral stream guidance groove 20 and liquid outlet 22,Fixing element structure includes frame 8 and housing 21;

Fixing housing 21 in described fixing element structure in frame 8, external motor 1 imparts power to rotating shaft by the synchronous pulley 9 of power transmission structure;

Described pivot structure shaft is fixed in frame 8 by bearing 6 and bearing block 7, bearing block 7 is fixed in frame 8 by screw attachment, and bearing 6 inner ring coordinates with rotating shaft, and outer ring coordinates with bearing block 7, it is internal that rotating shaft is inserted perpendicularly into housing 21 from centre position, and rotating shaft is hollow axle;

In described liquid header mechanism, water nozzle 2 is fixed on liquid header end cap 3 top by inner and outer pipes threaded engagement, catcher end cap 3 and liquid header 4 matched in clearance, catcher end cap 3 is fixed on liquid header 4 by screw attachment, liquid header 4 is connected with rotating shaft by lip-type packing 5, lip-type packing 5 inner ring coordinates with rotating shaft, and outer ring coordinates with the inner chamber of liquid header 4;

In described liquid mass transfer structure, upper rotating shaft spiral porous plate 14 is fixed on upper rotating shaft 13 bottom by screw attachment, fixing upper rotating shaft spiral porous plate 14 lower surface of cone cylinder porous plate 15, cone cylinder porous plate 15 surface uniform welding eddy current baffle plate 16, the hollow mouth of rotating shaft is connected with shower 17 entrance, shower 17 is fixed in rotating shaft by internal and external threads cooperation, lower rotary shaft spiral porous plate 18 is fixed by screw attachment in lower rotary shaft 19 upper end, spiral stream guidance groove 20 is fixed on housing 21 interior bottom portion by screw attachment, and housing 21 bottom is provided with liquid outlet 22.

Its shaft is the multidiameter of flanged dish, and the uniform through hole for thread connection on ring flange, bottom rotating shaft, bore design is the female thread matched with shower 17;The tapering of cone cylinder porous plate 15 is 4o, cone cylinder porous plate 15 is the corrosion resistant plate of thickness 2mm, and cone cylinder porous plate 15 surface is uniformly distributed the micropore of a diameter of 2mm;Described eddy current baffle plate 16 is 3 ~ 6 pieces, is shaped as right-angled trapezium;Described upper rotating shaft spiral porous plate 14, lower rotary shaft spiral porous plate 18 are the corrosion resistant plate of thickness 3mm, being evenly distributed with the micropore of a diameter of 2mm on stainless steel, upper rotating shaft spiral porous plate 14, the inner side and outer side of lower rotary shaft spiral porous plate 18 are all welded with spiral type rustless steel rib;Spiral stream guidance groove 20 is made up of the dividing plate raised the most successively, and the distribution of dividing plate uses spiral of Archimedes to be evenly distributed.

The motor 1 of this percussion flow hypergravity liquid-liquid extraction device upper part described stops operating, and only regulates the motor 1 of lower part, and this percussion flow hypergravity liquid-liquid extraction device is converted into sound disc type baffling supergravity reactor.

Above in association with accompanying drawing, the detailed description of the invention of the present invention is explained in detail, but the present invention is not limited to above-mentioned embodiment, in the ken that those of ordinary skill in the art are possessed, it is also possible to make a variety of changes on the premise of without departing from present inventive concept.

Claims (7)

  1. null1. a percussion flow hypergravity liquid-liquid extraction device,It is characterized in that: include power transmission structure、Liquid header mechanism、Pivot structure、Liquid mass transfer structure and fixing element structure,Power transmission structure is the Poewr transmission mechanism that upper and lower two sets are symmetrical,Liquid header mechanism includes water nozzle (2)、Liquid header end cap (3)、Liquid header (4) and lip-type packing (5),Liquid header mechanism is upper and lower two set symmetrical structures,Pivot structure includes bearing (6)、Bearing block (7) and rotating shaft,Pivot structure is upper and lower two set symmetrical structures,Rotating shaft is divided into laterally zygomorphic upper rotating shaft (13) and lower rotary shaft (19) according to position,Liquid mass transfer structure includes rotating shaft spiral porous plate (14)、Cone cylinder porous plate (15)、Eddy current baffle plate (16)、Shower (17)、Lower rotary shaft spiral porous plate (18)、Spiral stream guidance groove (20) and liquid outlet (22),Fixing element structure includes frame (8) and housing (21);
    Fixing housing (21) in described fixing element structure in frame (8), external motor (1) imparts power to rotating shaft by the synchronous pulley (9) of power transmission structure;
    Described pivot structure shaft is fixed in frame (8) by bearing (6) and bearing block (7), is inserted perpendicularly into housing (21) from centre position internal, and rotating shaft is hollow axle;
    In described liquid header mechanism, water nozzle (2) is fixed on liquid header end cap (3) top, and catcher end cap (3) coordinates with liquid header (4), and liquid header (4) is connected with rotating shaft by lip-type packing (5);
    In described liquid mass transfer structure, upper rotating shaft spiral porous plate (14) is fixed on rotating shaft (13) bottom, cone cylinder porous plate (15) is fixed on rotating shaft spiral porous plate (14) lower surface, cone cylinder porous plate (15) surface uniform welding eddy current baffle plate (16), the hollow mouth of rotating shaft is connected with shower (17) entrance, lower rotary shaft spiral porous plate (18) is fixed in lower rotary shaft (19) upper end, spiral stream guidance groove (20) is fixed on housing (21) interior bottom portion, and housing (21) bottom is provided with liquid outlet (22).
  2. Percussion flow hypergravity liquid-liquid extraction device the most according to claim 1, it is characterised in that: described rotating shaft is the multidiameter of flanged dish, the uniform through hole for thread connection on ring flange.
  3. Percussion flow hypergravity liquid-liquid extraction device the most according to claim 1, it is characterised in that: the tapering of described cone cylinder porous plate (15) is 2o~5o, cone cylinder porous plate (15) is the corrosion resistant plate of thickness 1 ~ 2mm, and cone cylinder porous plate (15) surface is uniformly distributed the micropore of a diameter of 1 ~ 2mm.
  4. Percussion flow hypergravity liquid-liquid extraction device the most according to claim 1, it is characterised in that: described eddy current baffle plate (16) is 3 ~ 6 pieces, is shaped as right-angled trapezium.
  5. Percussion flow hypergravity liquid-liquid extraction device the most according to claim 1, it is characterized in that: described upper rotating shaft spiral porous plate (14), lower rotary shaft spiral porous plate (18) are the corrosion resistant plate of thickness 2 ~ 4mm, being evenly distributed with the micropore of a diameter of 1 ~ 2mm on stainless steel, upper rotating shaft spiral porous plate (14), the inner side and outer side of lower rotary shaft spiral porous plate (18) are all welded with spiral type rustless steel rib.
  6. Percussion flow hypergravity liquid-liquid extraction device the most according to claim 1, it is characterised in that: described spiral stream guidance groove (20) is made up of the dividing plate raised the most successively, and the distribution of dividing plate uses spiral of Archimedes to be evenly distributed.
  7. Percussion flow hypergravity liquid-liquid extraction device the most according to claim 1, it is characterized in that: the motor (1) of described percussion flow hypergravity liquid-liquid extraction device upper part stops operating, only regulating the motor (1) of lower part, this percussion flow hypergravity liquid-liquid extraction device is converted into sound disc type baffling supergravity reactor.
CN201510189596.9A 2015-04-21 2015-04-21 A kind of percussion flow hypergravity liquid-liquid extraction device CN104941246B (en)

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Publication number Priority date Publication date Assignee Title
CN106075950B (en) * 2016-06-24 2018-03-06 昆明理工大学 A kind of dual drive cross_flow rotating packed bed
CN107158745B (en) * 2016-10-18 2019-11-12 四川大学 A kind of micro-extraction component and super gravity field micro-extraction device and extracting process
CN106865674B (en) * 2017-03-01 2020-06-05 煤炭科学技术研究院有限公司 Method for extracting and dephenolizing phenol-containing wastewater by multistage mixing and enhanced separation

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CN102441323A (en) * 2011-11-03 2012-05-09 袁长胜 Swirl double hypergravity machine
CN102583250A (en) * 2012-03-19 2012-07-18 瓮福(集团)有限责任公司 Device for extracting iodine from wet process phosphate acid liquor
CN103372328A (en) * 2012-04-17 2013-10-30 青岛科技大学 Rotating packed bed for dual-phase extraction
CN204671936U (en) * 2015-04-21 2015-09-30 昆明理工大学 A kind of percussion flow hypergravity liquid-liquid extraction device

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TWI384021B (en) * 2009-04-23 2013-02-01 Ind Tech Res Inst Method for transferring inorganic oxide nanoparticles from aqueous phase to organic phase

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Publication number Priority date Publication date Assignee Title
CN102441323A (en) * 2011-11-03 2012-05-09 袁长胜 Swirl double hypergravity machine
CN102583250A (en) * 2012-03-19 2012-07-18 瓮福(集团)有限责任公司 Device for extracting iodine from wet process phosphate acid liquor
CN103372328A (en) * 2012-04-17 2013-10-30 青岛科技大学 Rotating packed bed for dual-phase extraction
CN204671936U (en) * 2015-04-21 2015-09-30 昆明理工大学 A kind of percussion flow hypergravity liquid-liquid extraction device

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