WO2020220584A1 - Flow synergy-enhanced flotation separation apparatus and method - Google Patents

Flow synergy-enhanced flotation separation apparatus and method Download PDF

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WO2020220584A1
WO2020220584A1 PCT/CN2019/109882 CN2019109882W WO2020220584A1 WO 2020220584 A1 WO2020220584 A1 WO 2020220584A1 CN 2019109882 W CN2019109882 W CN 2019109882W WO 2020220584 A1 WO2020220584 A1 WO 2020220584A1
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mineralization
slurry
flotation separation
releaser
pipe
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PCT/CN2019/109882
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French (fr)
Chinese (zh)
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张海军
刘炯天
闫小康
王利军
刘清侠
王永田
李丹龙
李鑫
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中国矿业大学
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Priority to CA3100767A priority Critical patent/CA3100767C/en
Publication of WO2020220584A1 publication Critical patent/WO2020220584A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/02Froth-flotation processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/14Flotation machines
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B3/00Cleaning by methods involving the use or presence of liquid or steam
    • B08B3/04Cleaning involving contact with liquid
    • B08B3/10Cleaning involving contact with liquid with additional treatment of the liquid or of the object being cleaned, e.g. by heat, by electricity or by vibration
    • B08B3/12Cleaning involving contact with liquid with additional treatment of the liquid or of the object being cleaned, e.g. by heat, by electricity or by vibration by sonic or ultrasonic vibrations

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  • the invention relates to a fluid cooperative enhanced flotation separation device and method, and is particularly suitable for a fluid cooperative enhanced flotation separation device and method used for the flotation of fine mineral particles or coal particles.
  • Flotation is a method of sorting according to the difference of mineral particle surface physical and chemical properties and the difference of mineral floatability.
  • the mineralization process is the most critical, involving the three main processes of collision, adhesion and desorption.
  • collision is the basic premise of flotation mineralization, mainly controlled by fluid dynamics. For fine particles, in order to break through the streamlines and collide with bubbles efficiently, it is necessary to construct a reasonable fluid environment, such as increasing the collision probability of fine particles and bubbles with the help of highly turbulent impinging flow and cross flow, thereby enhancing the mineralization of fine particles effect.
  • the fluid synergistic enhanced flotation separation device of the present invention includes a circulating pump, a turbulent mineralization generator and a flotation separation releaser, and the turbulent mineralization generator is arranged above the flotation separation releaser.
  • Ring pumps respectively connect the outlet of the flotation separation releaser with the turbulent mineralization generator;
  • the turbulent mineralization generator includes a cylinder, a truncated cone with a funnel structure is arranged under the cylinder, a slurry distribution pipe is arranged side by side around the cylinder, and a plurality of impinging stream mineralization is arranged transversely between the slurry distribution pipe and the cylinder.
  • Tube and multiple cross-flow mineralization tubes, cross-flow mineralization tube and cylinder are connected in tangential direction, impinging flow mineralization tube and cylinder are connected in radial direction, cross-flow mineralization tube and impinging flow mineralization tube are both installed
  • There is a micro-bubble generator and there is a slurry injection pipe under the truncated cone;
  • the flotation separation releaser has a cylindrical structure, the bottom of the flotation separation releaser is narrowed to form an inverted terrace structure, the bottom center is provided with a tailings tube, one side of the tailings tube is provided with a medium ore tube, and the upper part of the cylindrical structure is provided There is a foam tank, the bottom of the foam tank is equipped with a concentrate tube, the cylindrical structure is provided with a vertical rectangular structure ultrasonic vibration plate under the foam tank, and a ring-shaped feed distributor is provided under the ultrasonic vibration plate.
  • the material distributor is provided with multiple nozzles, the cylindrical structure is provided with a sieve plate under the annular feeder distributor, and the inverted terrace structure at the bottom of the cylindrical structure is equipped with a conical deflector.
  • the conical deflector includes Counterattack plate, there is a gap between the bottom of the counterattack plate and the bottom of the inverted terrace structure.
  • the inverted terrace structure is provided with an inverted cone whose contour matches the inverted terrace structure, and there is a slurry flow channel between the inverted terrace structure.
  • the inverted cone is provided with a plurality of inverted trapezoidal structure guide vertical plates, and the slurry jet pipe extends from the foam tank on the top of the flotation separation releaser into the cylindrical structure, passes through the ultrasonic vibration plate, the feed distributor, Between the sieve plate and several vertical guide plates, the end of the slurry injection pipe is a horn structure;
  • the middle ore pipe is connected with the inlet of the circulating pump, and the outlet of the circulating pump is connected with the slurry distribution pipe.
  • Both the impinging stream mineralization tube and the cross-flow mineralization tube are in the form of venturi tube; the impinging stream mineralization tube and the cross-flow mineralization tube are alternately arranged at intervals; the adjacent cross-flow mineralization tubes are connected to the cylinder in opposite directions ;
  • the inner wall of the slurry jet pipe is provided with a prismatic turbulence strengthening generator.
  • a method for fluid synergistic enhanced flotation separation includes the following steps:
  • a. close the tailings pipe, and feed the initial slurry after mixing into the feed distributor from the inlet of the feed distributor, and spray it into the flotation separation releaser through the nozzle of the feed distributor.
  • the initial slurry is under gravity. After being diffused by the sieve plate, it is fed into the conical deflector, and flows into the middle ore pipe through the slurry flow channel between the conical deflector and the flotation separation releaser barrel wall, and is fed into the slurry distribution pipe through the circulating pump;
  • the slurry in the slurry distribution is fed into the cylinder through the impinging stream mineralization tube and the cross-flow mineralization tube, and a swirling flow of square and different directions is generated in the cylinder, and the compressed air is mixed into the slurry through the microbubble generator to be in the turbulent mine
  • the forced mixed mineralization of particles and microbubbles is realized in the chemical generator, and the forced mixed mineralized slurry is fed to the conical deflector in the flotation separation releaser through the slurry spray pipe at the bottom of the turbulent mineralization generator;
  • Part of the slurry carrying difficult-to-float particles enters the slurry flow channel between the cone-shaped deflector and the wall of the flotation separator release from the gap of the cone-shaped deflector, and finally enters the tailings separator of China Mines, opens the tailings pipe, and enters Part of the slurry of the tailings separator of Zhongkuang is used as tailings to be discharged from the tailings tube outlet of the tailings tube to the flotation separation releaser; the other part is used as the medium to be fed to the circulating pump through the medium ore tube to continue to circulate, so as to realize circulating separation. At the same time strengthen the suspension of coarse particles and increase the floatation bubble load;
  • the medium floatable particles in the slurry are rectified by the sieve plate in the flotation separation releaser to avoid the violent slurry disturbance in the flotation separation releaser causing the mineralized particles to fall off the bubbles, and then vibrate by the rectangular ultrasonic vibration plate After cleaning the entrained impurity mineral particles, it is discharged from the concentrate pipe on the foam tank above the flotation separation releaser.
  • the compressed air is sent into the impinging stream mineralization tube and the cross-flow mineralization tube through the microbubble generator, and the forced mixing and mineralization of particles and microbubbles are realized in the turbulent mineralization generator, which provides guarantee for subsequent flotation separation.
  • the fluid synergistic enhanced flotation separation device and method integrate high-speed impinging flow, cross-flow, counter-current and ultrasonic oscillating flow.
  • the impinging flow and cross-flow generated by the turbulent mineralization generator improve the mineralization effect of difficult-to-float particles ;
  • the countercurrent generated by the flotation separation releaser plays a synergistic effect of secondary separation, enhanced particle suspension and increased flotation bubble load;
  • the oscillating flow generated by the rectangular ultrasonic vibration plate set in the upper foam layer of the flotation separator further strengthens
  • the cleaning effect of the impurity mineral particles entrained in the foam improves the grade of the concentrate.
  • the present invention proposes a method for enhancing mineral flotation separation efficiency and improving concentrate grade by integrating high-speed impinging flow, cross-flow, counter-current and ultrasonic oscillation flow.
  • the impinging flow and cross-flow produced by a turbulent mineralization reactor are improved.
  • the collision probability of fine and difficult-to-float particles and bubbles strengthens the effect of mixing and mineralization of fine particles;
  • the countercurrent generated by the countercurrent flotation device strengthens the secondary separation of mineral particles, and at the same time strengthens the synergistic effect of the suspension of coarse particles and the increase of the flotation bubble load ;
  • the oscillating flow generated by the rectangular ultrasonic vibration plate in the upper foam layer of the flotation separator further strengthens the cleaning effect of the impurity mineral particles entrained in the foam and improves the concentrate grade.
  • Fig. 1 is a schematic diagram of the structure of a flotation separation device with enhanced fluid synergy of the present invention.
  • the fluid synergistic enhanced flotation separation device is characterized in that it includes a circulating pump 1, a turbulent mineralization generator 2 and a flotation separation releaser 5.
  • the turbulent mineralization generator 2 is set in the flotation separation release Above the device 5, the ring pump 1 respectively connects the outlet of the flotation separation release device 5 with the turbulent mineralization generator 2;
  • the turbulent mineralization generator 2 includes a cylinder, a truncated cone with a funnel structure is arranged below the cylinder, a slurry distribution pipe 11 is arranged side by side around the cylinder, and a plurality of collisions are arranged laterally between the slurry distribution pipe 11 and the cylinder.
  • the impinging stream mineralization tube 13 is equipped with a microbubble generator 12, and there is a slurry jet pipe 6 below the truncated cone; the impinging stream mineralization tube 13 and the cross-flow mineralization tube 14 are both in the form of a venturi tube;
  • the chemical tube 13 and the cross-flow mineralization tube 14 are arranged alternately at intervals; the adjacent cross-flow mineralization tubes 14 are connected to the cylinder in the opposite direction; the inner wall of the slurry injection tube 15 is provided with a prismatic turbulence intensifying generator 15;
  • the flotation separation releaser 5 has a cylindrical structure.
  • the bottom of the flotation separation releaser 5 is narrowed to form an inverted terrace structure.
  • the bottom center is provided with a tailing pipe 19, and one side of the tailing pipe 19 is provided with a medium ore pipe 10.
  • the upper part of the cylindrical structure is provided with a foam tank 3, and the bottom of the foam tank 3 is provided with a concentrate tube 16.
  • the cylindrical structure is provided with a rectangular ultrasonic vibration plate 7 placed vertically below the foam tank 3 and below the ultrasonic vibration plate 7.
  • a feed distributor 4 with a ring structure is provided.
  • the feed distributor 4 is provided with multiple nozzles.
  • a screen 8 is provided under the ring feed distributor 4 in the cylindrical structure.
  • An inverted ladder structure at the bottom of the cylindrical structure There is a cone-shaped deflector.
  • the cone-shaped deflector includes a counterattack plate 18. There is a gap between the bottom of the counterattack plate 18 and the bottom of the inverted terrace structure.
  • the inverted terrace structure has a contour that matches the inverted terrace structure.
  • the slurry injection pipe 6 is separated from the flotation releaser 5
  • the foam tank 3 on the top extends into the inside of the cylindrical structure, passes through the ultrasonic vibration plate 7, the feed distributor 4, the sieve plate 8 and reaches between the multiple guide vertical plates 9, and the end of the slurry injection pipe 6 is a horn structure;
  • the middle mine pipe 10 is connected with the inlet of the circulating pump 1, and the outlet of the circulating pump 1 is connected with the slurry distribution pipe 11.
  • a method for fluid synergistic enhanced flotation separation includes the following steps:
  • the slurry in the slurry distribution 11 is fed into the cylinder through the impinging stream mineralization tube 13 and the cross-flow mineralization tube 14 and generates a swirling flow in different directions in the cylinder, and the compressed air is mixed into the slurry through the microbubble generator 12 In this way, the forced mixed mineralization of particles and microbubbles is realized in the turbulent mineralization generator 2, and the forced mixed mineralized slurry is fed into the flotation separation releaser 5 through the slurry injection pipe 15 at the bottom of the turbulent mineralization generator 2.
  • Conical deflector compressed air is sent into the impinging stream mineralization tube 13 and the cross-flow mineralization tube 14 through the microbubble generator 12, and the forced mixing and mineralization of particles and microbubbles is realized in the turbulent mineralization generator 2. Provide guarantee for subsequent flotation separation;
  • Part of the slurry carrying difficult-to-float particles enters the slurry flow channel between the cone-shaped deflector and the flotation separation releaser 5 from the gap of the cone-shaped deflector, and finally enters the tailings separator of China Mine, and the tailings pipe is opened 19 , Part of the slurry that enters the tailings separator of Zhongkuang is used as tailings and is discharged from the tailings tube outlet B of the tailings pipe 19 to the flotation separation releaser 5; the other part is fed into the circulating pump 1 through the Zhongmine pipe 10 as the medium and continues to circulate , So as to realize cyclic separation, at the same time strengthen the suspension of coarse particles and increase the load of flotation bubbles;
  • the medium floatable particles in the slurry are rectified by the sieve plate 8 in the flotation separation releaser 5 to avoid the violent slurry disturbance in the flotation separation releaser 5 causing the mineralized particles to fall off the bubbles, and then pass the rectangular ultrasonic wave After the oscillating flow of the vibrating plate 7 washes away the entrained impurity mineral particles, it is discharged from the concentrate pipe 16 on the foam tank 3 above the flotation separation releaser 5.
  • the specific working process a. First, the initial slurry after mixing is fed into the flotation separation releaser 5 from the inlet A of the feed distributor 4, and the easily floating particles rise and float quickly, and the entrainment is cleaned by the rectangular ultrasonic vibration plate 7 oscillating flow After the impurity mineral particles are discharged from the outlet C of the concentrate pipe 16 on the foam tank 3 above the flotation separation releaser 5, they become a concentrate product;
  • the difficult-to-float particles separated by the flotation separation releaser 5 enter the middle mine tailings separator through the slurry flow channel between the cone deflector and the flotation separation releaser 5, and are divided into two parts One part is used as tailings and discharged from the flotation separation releaser 5 through tailings pipe 19 outlet B to become tailings products; the other part is used as a medium mine to be given to circulation pump 1 through medium mine pipe 10, and then to turbulent mine by circulation pump 1
  • the slurry distribution pipe 11 of the chemical generator 2 is efficiently mineralized by the turbulent mineralization generator 2 and then injected into the flotation separation releaser 5 to achieve cyclic separation, while strengthening the suspension of coarse particles and increasing the load of flotation bubbles;

Abstract

A flow synergy-enhanced flotation separation apparatus and a method, suitable for use in flotation of microscopic mineral particles or coal particles. The apparatus comprises a circulation pump (1), a mineralization turbulent flow generator (2), and a flotation separation releaser (5). A pulp is fed into the flotation separation releaser (5), and more-buoyant particles rapidly rise and are expelled by means of a concentrate pipe (16) on a froth trough (3) above the flotation separation releaser (5). Moderately-buoyant particles are separated by means of the flotation separation releaser (5), and then a portion float to the froth trough (3) above the flotation separation releaser (5) and are expelled via the concentrate pipe (16) on the froth trough (3). Less-buoyant particles that have been separated by the flotation separation releaser (5) enter a middling/tailing separator via a pulp flow channel between a conical flow director and a cylindrical wall of the flotation separation releaser (5), and are divided into two portions. One portion serves as tailings and is expelled from the flotation separation releaser (5), and a portion is fed into the mineralization turbulent flow generator (2) by means of the circulation pump (1), and after undergoing high-efficiency mineralization, is sprayed back into the flotation separation releaser (5), thus achieving circulating separation. The invention features a simple structure and an excellent flotation result.

Description

一种流体协同强化浮选分离装置及方法Fluid synergistic enhanced flotation separation device and method 技术领域Technical field
本发明涉及一种流体协同强化浮选分离装置及方法,尤其适用于微细矿物颗粒或煤粒的浮选使用的流体协同强化浮选分离装置及方法。The invention relates to a fluid cooperative enhanced flotation separation device and method, and is particularly suitable for a fluid cooperative enhanced flotation separation device and method used for the flotation of fine mineral particles or coal particles.
背景技术Background technique
浮选是根据矿物颗粒表面物理化学性质的不同,按矿物可浮性的差异进行分选的方法,其中矿化过程最为关键,涉及碰撞、粘附和脱附三个主要过程。其中,碰撞是浮选矿化的基本前提,主要受流体动力学控制。对于微细颗粒而言,要想突破流线与气泡发生高效碰撞,需要构建合理的流体环境,如借助高湍流的撞击流和错流提高微细颗粒与气泡的碰撞概率,从而强化微细颗粒的矿化效果。此外,对于微细粒矿物颗粒浮选而言,脉石矿物更容易因夹带进入浮选泡沫,从而影响精矿产品质量。虽然,泡沫清水水具有一定的清洗作用,但效果不甚理想,而且很难设计出合理的泡沫清洗水冲水结构,清洗过程也很难优化控制。Flotation is a method of sorting according to the difference of mineral particle surface physical and chemical properties and the difference of mineral floatability. Among them, the mineralization process is the most critical, involving the three main processes of collision, adhesion and desorption. Among them, collision is the basic premise of flotation mineralization, mainly controlled by fluid dynamics. For fine particles, in order to break through the streamlines and collide with bubbles efficiently, it is necessary to construct a reasonable fluid environment, such as increasing the collision probability of fine particles and bubbles with the help of highly turbulent impinging flow and cross flow, thereby enhancing the mineralization of fine particles effect. In addition, for the flotation of fine mineral particles, gangue minerals are more likely to enter the flotation foam due to entrainment, thereby affecting the quality of the concentrate product. Although the foam clean water has a certain cleaning effect, the effect is not ideal, and it is difficult to design a reasonable foam cleaning water flushing structure, and the cleaning process is also difficult to optimize and control.
发明内容Summary of the invention
技术问题:针对上述技术问题,提供一种结构简单,使用效果好,能够有效矿化微细粒矿物的流体协同强化浮选分离装置及方法。Technical problem: In view of the above technical problems, a fluid synergistic enhanced flotation separation device and method with simple structure, good use effect, and effective mineralization of fine-grained minerals are provided.
技术方案:为实现上述技术目的,本发明的流体协同强化浮选分离装置,包括循环泵、湍流矿化发生器和浮选分离释放器,湍流矿化发生器设置在浮选分离释放器上方,环泵分别将浮选分离释放器的出口与湍流矿化发生器相连接;Technical solution: In order to achieve the above technical objectives, the fluid synergistic enhanced flotation separation device of the present invention includes a circulating pump, a turbulent mineralization generator and a flotation separation releaser, and the turbulent mineralization generator is arranged above the flotation separation releaser. Ring pumps respectively connect the outlet of the flotation separation releaser with the turbulent mineralization generator;
所述的湍流矿化发生器包括圆筒,圆筒下方设有漏斗结构的圆锥台,圆筒周围并排设置有矿浆分配管,矿浆分配管与圆筒之间横向设有多个撞击流矿化管和多个错流矿化管,错流矿化管与圆筒沿切向连接,撞击流矿化管与圆筒沿径向连接,错流矿化管和撞击流矿化管上均设置有微泡发生器,圆锥台下方设有矿浆喷射管;The turbulent mineralization generator includes a cylinder, a truncated cone with a funnel structure is arranged under the cylinder, a slurry distribution pipe is arranged side by side around the cylinder, and a plurality of impinging stream mineralization is arranged transversely between the slurry distribution pipe and the cylinder. Tube and multiple cross-flow mineralization tubes, cross-flow mineralization tube and cylinder are connected in tangential direction, impinging flow mineralization tube and cylinder are connected in radial direction, cross-flow mineralization tube and impinging flow mineralization tube are both installed There is a micro-bubble generator, and there is a slurry injection pipe under the truncated cone;
所述浮选分离释放器为圆筒结构,浮选分离释放器下方收窄形成倒梯台结构,底部中央设有尾矿管,尾矿管一侧设有中矿管,圆筒结构上方设有泡沫槽,泡沫槽底部设有精矿管,圆筒结构在泡沫槽下方的内部设有竖直放置的矩形结构的超声波振板,超声波振板下方设有环形结构的给料分配器,给料分配器上设有多个喷头,圆筒结构内位于环形给料分配器下方设有筛板,圆筒结构底部的倒梯台结构处设有锥形导流器,锥形导流器包括反击板,反击板下方与倒梯台结构底部之间留有间隙,倒梯台结构上设有轮廓与倒梯台结构匹配一致,并与倒梯台结构之间留有矿浆流动通道的倒锥,倒锥内设有多块倒梯形结构的导流立板,所述矿浆喷射管从浮选分离释放器顶部的泡沫槽伸入圆筒结构内部,穿过超声波振板、给料分配器、筛板直至多块导流立板之间,矿浆喷射管的末端为喇叭结构;The flotation separation releaser has a cylindrical structure, the bottom of the flotation separation releaser is narrowed to form an inverted terrace structure, the bottom center is provided with a tailings tube, one side of the tailings tube is provided with a medium ore tube, and the upper part of the cylindrical structure is provided There is a foam tank, the bottom of the foam tank is equipped with a concentrate tube, the cylindrical structure is provided with a vertical rectangular structure ultrasonic vibration plate under the foam tank, and a ring-shaped feed distributor is provided under the ultrasonic vibration plate. The material distributor is provided with multiple nozzles, the cylindrical structure is provided with a sieve plate under the annular feeder distributor, and the inverted terrace structure at the bottom of the cylindrical structure is equipped with a conical deflector. The conical deflector includes Counterattack plate, there is a gap between the bottom of the counterattack plate and the bottom of the inverted terrace structure. The inverted terrace structure is provided with an inverted cone whose contour matches the inverted terrace structure, and there is a slurry flow channel between the inverted terrace structure. , The inverted cone is provided with a plurality of inverted trapezoidal structure guide vertical plates, and the slurry jet pipe extends from the foam tank on the top of the flotation separation releaser into the cylindrical structure, passes through the ultrasonic vibration plate, the feed distributor, Between the sieve plate and several vertical guide plates, the end of the slurry injection pipe is a horn structure;
所述中矿管与循环泵的入口相连接,循环泵的出口与矿浆分配管相连接。The middle ore pipe is connected with the inlet of the circulating pump, and the outlet of the circulating pump is connected with the slurry distribution pipe.
撞击流矿化管和错流矿化管均为文丘里管结构形式;撞击流矿化管和错流矿化管交替间隔设置;相邻错流矿化管切向接入圆筒的方向相反;矿浆喷射管内壁设置有棱形湍流强化发生器。Both the impinging stream mineralization tube and the cross-flow mineralization tube are in the form of venturi tube; the impinging stream mineralization tube and the cross-flow mineralization tube are alternately arranged at intervals; the adjacent cross-flow mineralization tubes are connected to the cylinder in opposite directions ; The inner wall of the slurry jet pipe is provided with a prismatic turbulence strengthening generator.
一种流体协同强化浮选分离方法,包括如下步骤:A method for fluid synergistic enhanced flotation separation includes the following steps:
a.首先关闭尾矿管,将调浆后的初始矿浆从给料分配器入口给入给料分配器,并通过给料分配器的喷头喷洒至浮选分离释放器内,初始矿浆在重力的作用下经筛板扩散后给入锥形导流器,并通过锥形导流器与浮选分离释放器筒壁间的矿浆流动通道流入中矿管,通过循环泵给入矿浆分配管;a. First, close the tailings pipe, and feed the initial slurry after mixing into the feed distributor from the inlet of the feed distributor, and spray it into the flotation separation releaser through the nozzle of the feed distributor. The initial slurry is under gravity. After being diffused by the sieve plate, it is fed into the conical deflector, and flows into the middle ore pipe through the slurry flow channel between the conical deflector and the flotation separation releaser barrel wall, and is fed into the slurry distribution pipe through the circulating pump;
b.矿浆分配中的矿浆通过撞击流矿化管和错流矿化管给入圆筒并在圆筒中产生正方不同方向的旋流,并通过微泡发生器将压缩空气混入矿浆从而在湍流矿化发生器内实现颗粒与微泡的强制混合矿化,强制混合矿化后的矿浆通过湍流矿化发生器底部的矿浆喷射管给入浮选分离释放器内的锥形导流器;b. The slurry in the slurry distribution is fed into the cylinder through the impinging stream mineralization tube and the cross-flow mineralization tube, and a swirling flow of square and different directions is generated in the cylinder, and the compressed air is mixed into the slurry through the microbubble generator to be in the turbulent mine The forced mixed mineralization of particles and microbubbles is realized in the chemical generator, and the forced mixed mineralized slurry is fed to the conical deflector in the flotation separation releaser through the slurry spray pipe at the bottom of the turbulent mineralization generator;
部分携带难浮颗粒的矿浆从锥形导流器的间隙进入锥形导流器与浮选分离释放器筒壁间的矿浆流动通道,最终进入中矿尾矿分离器,打开尾矿管,进入中矿尾矿分离器的部分矿浆作为尾矿经尾矿管的尾矿管出口排出浮选分离释放器;另一部分作为中矿经中矿管给入循环泵继续循环,从而实现循环分选,同时强化粗颗粒悬浮和提高浮选气泡载荷;Part of the slurry carrying difficult-to-float particles enters the slurry flow channel between the cone-shaped deflector and the wall of the flotation separator release from the gap of the cone-shaped deflector, and finally enters the tailings separator of China Mines, opens the tailings pipe, and enters Part of the slurry of the tailings separator of Zhongkuang is used as tailings to be discharged from the tailings tube outlet of the tailings tube to the flotation separation releaser; the other part is used as the medium to be fed to the circulating pump through the medium ore tube to continue to circulate, so as to realize circulating separation. At the same time strengthen the suspension of coarse particles and increase the floatation bubble load;
部分携带易浮颗粒的矿浆被气泡粘附后在锥形导流器中反击板和导流立板的作用下提高矿化气泡的升浮速度,易浮颗粒随气泡一起上浮,通过筛板时过滤掉,经矩形超声波振板振荡流清洗掉夹带的杂质矿物颗粒后,由浮选分离释放器上方泡沫槽上的精矿管的精矿管出口排出,其余颗粒与矿浆一起继续留在浮选分离释放器内;Part of the ore slurry carrying easy-floating particles is adhered to by the air bubbles, and then under the action of the counter-attack plate and the vertical guide plate in the conical deflector, the lifting speed of the mineralized bubbles is increased. The easy-floating particles float together with the air bubbles and pass through the sieve. After filtering out, the entrained impurity mineral particles are cleaned by the oscillating flow of the rectangular ultrasonic vibration plate, and then discharged from the concentrate tube outlet of the concentrate tube on the foam tank above the flotation separator releaser, and the remaining particles remain in the flotation together with the slurry Inside the release release;
c.矿浆中的易浮颗粒快速升浮,经矩形超声波振板振荡流清洗掉夹带的杂质矿物颗粒后,由浮选分离释放器上方泡沫槽上的精矿管的精矿管出口排出;c. The easy-floating particles in the slurry rise and float rapidly, and the entrained impurity mineral particles are cleaned by the oscillating flow of the rectangular ultrasonic vibration plate, and then discharged from the concentrate pipe outlet of the concentrate pipe on the foam tank above the flotation separation releaser;
d.矿浆中的中等可浮颗粒在浮选分离释放器内经筛板整流后避免在浮选分离释放器内剧烈的矿浆扰动造成矿化后的颗粒从气泡上脱落,再经矩形超声波振板振荡流清洗掉夹带的杂质矿物颗粒后,由浮选分离释放器上方泡沫槽上的精矿管排出。d. The medium floatable particles in the slurry are rectified by the sieve plate in the flotation separation releaser to avoid the violent slurry disturbance in the flotation separation releaser causing the mineralized particles to fall off the bubbles, and then vibrate by the rectangular ultrasonic vibration plate After cleaning the entrained impurity mineral particles, it is discharged from the concentrate pipe on the foam tank above the flotation separation releaser.
压缩空气经微泡发生器分别送入撞击流矿化管和错流矿化管,在湍流矿化发生器内实现颗粒与微泡的强制混合矿化,为后续浮选分离提供保障。The compressed air is sent into the impinging stream mineralization tube and the cross-flow mineralization tube through the microbubble generator, and the forced mixing and mineralization of particles and microbubbles are realized in the turbulent mineralization generator, which provides guarantee for subsequent flotation separation.
有益效果:该流体协同强化浮选分离装置及方法集高速撞击流、错流、逆流及超声振荡流于一体,湍流矿化发生器产生的撞击流和错流提高了难浮颗粒的矿化效果;浮选分离释放器产生的逆流起到了二次分选、强化颗粒悬浮和提高浮选气泡载荷的协同作用;浮选分离器上部泡沫层中设置的矩形超声波振板产生的振荡流进一步强化了对泡沫中所夹带的杂质矿物颗粒的清洗作用,提高了精矿品位。Beneficial effects: The fluid synergistic enhanced flotation separation device and method integrate high-speed impinging flow, cross-flow, counter-current and ultrasonic oscillating flow. The impinging flow and cross-flow generated by the turbulent mineralization generator improve the mineralization effect of difficult-to-float particles ; The countercurrent generated by the flotation separation releaser plays a synergistic effect of secondary separation, enhanced particle suspension and increased flotation bubble load; the oscillating flow generated by the rectangular ultrasonic vibration plate set in the upper foam layer of the flotation separator further strengthens The cleaning effect of the impurity mineral particles entrained in the foam improves the grade of the concentrate.
本发明针对上述问题,提出采用集高速撞击流、错流、逆流及超声振荡流来强化矿物浮选分离效率和提高精矿品位的方法,通过湍流矿化反应器产生的撞击流和错流提高微细难浮颗粒与气泡的碰撞概率,强化细粒混合矿化效果;通过逆流浮选器产生的逆流,强化矿物颗粒的二次分选,同时强化粗颗粒悬浮 和提高浮选气泡载荷的协同作用;通过浮选分离器上部泡沫层中矩形超声波振板产生的振荡流进一步强化对泡沫中所夹带的杂质矿物颗粒的清洗作用,提高精矿品位。通过上述装置和方法的实施,强化矿物浮选分离过程,提高目的矿物的回收率和产品质量。In view of the above-mentioned problems, the present invention proposes a method for enhancing mineral flotation separation efficiency and improving concentrate grade by integrating high-speed impinging flow, cross-flow, counter-current and ultrasonic oscillation flow. The impinging flow and cross-flow produced by a turbulent mineralization reactor are improved. The collision probability of fine and difficult-to-float particles and bubbles strengthens the effect of mixing and mineralization of fine particles; the countercurrent generated by the countercurrent flotation device strengthens the secondary separation of mineral particles, and at the same time strengthens the synergistic effect of the suspension of coarse particles and the increase of the flotation bubble load ; The oscillating flow generated by the rectangular ultrasonic vibration plate in the upper foam layer of the flotation separator further strengthens the cleaning effect of the impurity mineral particles entrained in the foam and improves the concentrate grade. Through the implementation of the above device and method, the mineral flotation separation process is strengthened, and the recovery rate of target minerals and the product quality are improved.
附图说明Description of the drawings
图1是本发明的一种流体协同强化浮选分离装置结构示意图。Fig. 1 is a schematic diagram of the structure of a flotation separation device with enhanced fluid synergy of the present invention.
图中:1-循环泵,2-湍流矿化发生器,3-泡沫槽,4-给料分配器,5-浮选分离释放器,6-矿浆喷射管,7-超声波振板,8-筛板,9-导流立板,10-中矿管,11-矿浆分配管,12-微泡发生器,13-撞击流矿化管,14-错流矿化管,15-湍流强化发生器,16-精矿管,17-倒锥,18-反击板,19-尾矿管,A-给料分配器入口,B-尾矿管出口,C-精矿管出口。In the picture: 1-circulating pump, 2-turbulent mineralization generator, 3-foam tank, 4-feed distributor, 5-flotation separation releaser, 6-slurry jet pipe, 7-ultrasonic vibration plate, 8- Sieve plate, 9- diversion vertical plate, 10-medium mine pipe, 11-slurry distribution pipe, 12-microbubble generator, 13-impinging stream mineralization pipe, 14-cross flow mineralization pipe, 15-turbulence intensification generation Device, 16-concentrate pipe, 17-inverted cone, 18-counterattack plate, 19-tailings pipe, A-feed distributor inlet, B-tailings pipe outlet, C-concentrate pipe outlet.
具体实施方式Detailed ways
下面结合附图对本发明的具体实施方式作进一步详细描述:The specific embodiments of the present invention will be described in further detail below in conjunction with the accompanying drawings:
如图1所示,流体协同强化浮选分离装置,其特征在于:它包括循环泵1、湍流矿化发生器2和浮选分离释放器5,湍流矿化发生器2设置在浮选分离释放器5上方,环泵1分别将浮选分离释放器5的出口与湍流矿化发生器2相连接;As shown in Figure 1, the fluid synergistic enhanced flotation separation device is characterized in that it includes a circulating pump 1, a turbulent mineralization generator 2 and a flotation separation releaser 5. The turbulent mineralization generator 2 is set in the flotation separation release Above the device 5, the ring pump 1 respectively connects the outlet of the flotation separation release device 5 with the turbulent mineralization generator 2;
所述的湍流矿化发生器2包括圆筒,圆筒下方设有漏斗结构的圆锥台,圆筒周围并排设置有矿浆分配管11,矿浆分配管11与圆筒之间横向设有多个撞击流矿化管13和多个错流矿化管14,错流矿化管14与圆筒沿切向连接,撞击流矿化管13与圆筒沿径向连接,错流矿化管14和撞击流矿化管13上均设置有微泡发生器12,圆锥台下方设有矿浆喷射管6;撞击流矿化管13和错流矿化管14均为文丘里管结构形式;撞击流矿化管13和错流矿化管14交替间隔设置;相邻错流矿化管14切向接入圆筒的方向相反;矿浆喷射管15内壁设置有棱形湍流强化发生器15;The turbulent mineralization generator 2 includes a cylinder, a truncated cone with a funnel structure is arranged below the cylinder, a slurry distribution pipe 11 is arranged side by side around the cylinder, and a plurality of collisions are arranged laterally between the slurry distribution pipe 11 and the cylinder. The flow mineralization tube 13 and a plurality of cross flow mineralization tubes 14, the cross flow mineralization tube 14 is connected with the cylinder along the tangential direction, the impinging flow mineralization tube 13 is connected with the cylinder along the radial direction, the cross flow mineralization tube 14 and The impinging stream mineralization tube 13 is equipped with a microbubble generator 12, and there is a slurry jet pipe 6 below the truncated cone; the impinging stream mineralization tube 13 and the cross-flow mineralization tube 14 are both in the form of a venturi tube; The chemical tube 13 and the cross-flow mineralization tube 14 are arranged alternately at intervals; the adjacent cross-flow mineralization tubes 14 are connected to the cylinder in the opposite direction; the inner wall of the slurry injection tube 15 is provided with a prismatic turbulence intensifying generator 15;
所述浮选分离释放器5为圆筒结构,浮选分离释放器5下方收窄形成倒梯台结构,底部中央设有尾矿管19,尾矿管19一侧设有中矿管10,圆筒结构上方设有泡沫槽3,泡沫槽3底部设有精矿管16,圆筒结构在泡沫槽3下方的内部设有竖直放置的矩形结构的超声波振板7,超声波振板7下方设有环形结构的给料分配器4,给料分配器4上设有多个喷头,圆筒结构内位于环形给料分配器4下方设有筛板8,圆筒结构底部的倒梯台结构处设有锥形导流器,锥形导流器包括反击板18,反击板18下方与倒梯台结构底部之间留有间隙,倒梯台结构上设有轮廓与倒梯台结构匹配一致,并与倒梯台结构之间留有矿浆流动通道的倒锥17,倒锥17内设有多块倒梯形结构的导流立板9,所述矿浆喷射管6从浮选分离释放器5顶部的泡沫槽3伸入圆筒结构内部,穿过超声波振板7、给料分配器4、筛板8直至多块导流立板9之间,矿浆喷射管6的末端为喇叭结构;The flotation separation releaser 5 has a cylindrical structure. The bottom of the flotation separation releaser 5 is narrowed to form an inverted terrace structure. The bottom center is provided with a tailing pipe 19, and one side of the tailing pipe 19 is provided with a medium ore pipe 10. The upper part of the cylindrical structure is provided with a foam tank 3, and the bottom of the foam tank 3 is provided with a concentrate tube 16. The cylindrical structure is provided with a rectangular ultrasonic vibration plate 7 placed vertically below the foam tank 3 and below the ultrasonic vibration plate 7. A feed distributor 4 with a ring structure is provided. The feed distributor 4 is provided with multiple nozzles. A screen 8 is provided under the ring feed distributor 4 in the cylindrical structure. An inverted ladder structure at the bottom of the cylindrical structure There is a cone-shaped deflector. The cone-shaped deflector includes a counterattack plate 18. There is a gap between the bottom of the counterattack plate 18 and the bottom of the inverted terrace structure. The inverted terrace structure has a contour that matches the inverted terrace structure. , And leave the inverted cone 17 of the slurry flow channel between the inverted terrace structure, and the inverted cone 17 is provided with a plurality of inverted trapezoidal structure guide vertical plates 9, the slurry injection pipe 6 is separated from the flotation releaser 5 The foam tank 3 on the top extends into the inside of the cylindrical structure, passes through the ultrasonic vibration plate 7, the feed distributor 4, the sieve plate 8 and reaches between the multiple guide vertical plates 9, and the end of the slurry injection pipe 6 is a horn structure;
所述中矿管10与循环泵1的入口相连接,循环泵1的出口与矿浆分配管11相连接。The middle mine pipe 10 is connected with the inlet of the circulating pump 1, and the outlet of the circulating pump 1 is connected with the slurry distribution pipe 11.
一种流体协同强化浮选分离方法,包括如下步骤:A method for fluid synergistic enhanced flotation separation includes the following steps:
a.首先关闭尾矿管19,将调浆后的初始矿浆从给料分配器入口A给入给料分配器4,并通过给料分配器4的喷头喷洒至浮选分离释放器5内,初始矿浆在重力的作用下经筛板8扩散后给入锥形导流器,并通过锥形导流器与浮选分离释放器5筒壁间的矿浆流动通道流入中矿管10,通过循环泵1给入矿浆分配管11;a. First, close the tailings pipe 19, and feed the initial slurry after mixing into the feed distributor 4 from the feed distributor inlet A, and spray it into the flotation release releaser 5 through the nozzle of the feed distributor 4, The initial slurry is diffused by the sieve plate 8 under the action of gravity, and then fed into the cone deflector, and flows into the middle ore pipe 10 through the slurry flow channel between the cone deflector and the flotation separation releaser 5 barrel wall, and passes through the circulation Pump 1 feeds into the slurry distribution pipe 11;
b.矿浆分配11中的矿浆通过撞击流矿化管13和错流矿化管14给入圆筒并在圆筒中产生正方不同方向的旋流,并通过微泡发生器12将压缩空气混入矿浆从而在湍流矿化发生器2内实现颗粒与微泡的强制混合矿化,强制混合矿化后的矿浆通过湍流矿化发生器2底部的矿浆喷射管15给入浮选分离释放器5内的锥形导流器;压缩空气经微泡发生器12分别送入撞击流矿化管13和错流矿化管14,在湍流矿化发生器2内实现颗粒与微泡的强制混合矿化,为后续浮选分离提供保障;b. The slurry in the slurry distribution 11 is fed into the cylinder through the impinging stream mineralization tube 13 and the cross-flow mineralization tube 14 and generates a swirling flow in different directions in the cylinder, and the compressed air is mixed into the slurry through the microbubble generator 12 In this way, the forced mixed mineralization of particles and microbubbles is realized in the turbulent mineralization generator 2, and the forced mixed mineralized slurry is fed into the flotation separation releaser 5 through the slurry injection pipe 15 at the bottom of the turbulent mineralization generator 2. Conical deflector; compressed air is sent into the impinging stream mineralization tube 13 and the cross-flow mineralization tube 14 through the microbubble generator 12, and the forced mixing and mineralization of particles and microbubbles is realized in the turbulent mineralization generator 2. Provide guarantee for subsequent flotation separation;
部分携带难浮颗粒的矿浆从锥形导流器的间隙进入锥形导流器与浮选分离释放器5筒壁间的矿浆流动通道,最终进入中矿尾矿分离器,打开尾矿管19,进入中矿尾矿分离器的部分矿浆作为尾矿经尾矿管19的尾矿管出口B排出浮选分离释放器5;另一部分作为中矿经中矿管10给入循环泵1继续循环,从而实现循环分选,同时强化粗颗粒悬浮和提高浮选气泡载荷;Part of the slurry carrying difficult-to-float particles enters the slurry flow channel between the cone-shaped deflector and the flotation separation releaser 5 from the gap of the cone-shaped deflector, and finally enters the tailings separator of China Mine, and the tailings pipe is opened 19 , Part of the slurry that enters the tailings separator of Zhongkuang is used as tailings and is discharged from the tailings tube outlet B of the tailings pipe 19 to the flotation separation releaser 5; the other part is fed into the circulating pump 1 through the Zhongmine pipe 10 as the medium and continues to circulate , So as to realize cyclic separation, at the same time strengthen the suspension of coarse particles and increase the load of flotation bubbles;
部分携带易浮颗粒的矿浆被气泡粘附后在锥形导流器中反击板18和导流立板9的作用下提高矿化气泡的升浮速度,易浮颗粒随气泡一起上浮,通过筛板8时过滤掉,经矩形超声波振板7振荡流清洗掉夹带的杂质矿物颗粒后,由浮选分离释放器5上方泡沫槽3上的精矿管16的精矿管出口C排出,其余颗粒与矿浆一起继续留在浮选分离释放器5内;Part of the ore slurry carrying easy-floating particles is adhered to by the air bubbles, and then under the action of the counter-attack plate 18 and the vertical guide plate 9 in the cone deflector, the lifting speed of the mineralized air bubbles is increased. The easy-floating particles float together with the air bubbles and pass through the screen. The plate 8 is filtered out, and the entrained impurity mineral particles are cleaned by the oscillating flow of the rectangular ultrasonic vibration plate 7, and then discharged from the concentrate pipe outlet C of the concentrate pipe 16 on the foam tank 3 above the flotation separation releaser 5, and the remaining particles Continue to stay in the flotation separation releaser 5 together with the pulp;
c.矿浆中的易浮颗粒快速升浮,经矩形超声波振板7振荡流清洗掉夹带的杂质矿物颗粒后,由浮选分离释放器5上方泡沫槽3上的精矿管16的精矿管出口C排出;c. The easy-floating particles in the slurry rise and float rapidly. After the entrained impurity mineral particles are cleaned by the oscillating flow of the rectangular ultrasonic vibration plate 7, the concentrate tube 16 on the foam tank 3 above the flotation separator 5 is separated. Exit C discharge;
d.矿浆中的中等可浮颗粒在浮选分离释放器5内经筛板8整流后避免在浮选分离释放器5内剧烈的矿浆扰动造成矿化后的颗粒从气泡上脱落,再经矩形超声波振板7振荡流清洗掉夹带的杂质矿物颗粒后,由浮选分离释放器5上方泡沫槽3上的精矿管16排出。d. The medium floatable particles in the slurry are rectified by the sieve plate 8 in the flotation separation releaser 5 to avoid the violent slurry disturbance in the flotation separation releaser 5 causing the mineralized particles to fall off the bubbles, and then pass the rectangular ultrasonic wave After the oscillating flow of the vibrating plate 7 washes away the entrained impurity mineral particles, it is discharged from the concentrate pipe 16 on the foam tank 3 above the flotation separation releaser 5.
具体工作过程:a.首先经调浆后的初始矿浆由给料分配器4入口A给入浮选分离释放器5内,易浮颗粒快速升浮,经矩形超声波振板7振荡流清洗掉夹带的杂质矿物颗粒后,由浮选分离释放器5上方泡沫槽3上的精矿管16出口C排出,成为精矿产品;The specific working process: a. First, the initial slurry after mixing is fed into the flotation separation releaser 5 from the inlet A of the feed distributor 4, and the easily floating particles rise and float quickly, and the entrainment is cleaned by the rectangular ultrasonic vibration plate 7 oscillating flow After the impurity mineral particles are discharged from the outlet C of the concentrate pipe 16 on the foam tank 3 above the flotation separation releaser 5, they become a concentrate product;
b.中等可浮颗粒经浮选分离释放器5分选后,一部分在浮选分离释放器5内经筛板8整流后上浮,再经矩形超声波振板7振荡流清洗掉夹带的杂质矿物颗粒后,由浮选分离释放器5上方泡沫槽3上的精矿管16排出;b. After the medium floatable particles are sorted by the flotation separation releaser 5, a part of the flotation separation releaser 5 is rectified by the sieve plate 8 and floated, and then the entrained impurity mineral particles are cleaned by the rectangular ultrasonic vibration plate 7 oscillating flow , Discharged from the concentrate pipe 16 on the foam tank 3 above the flotation separation releaser 5;
c.浮选分离释放器5分选后的难浮颗粒,经锥形导流器与浮选分离释放器5筒壁间的矿浆流动通道进入中矿尾矿分离器,并被分割成两部分,一部分作为尾矿经尾矿管19出口B排出浮选分离释放器5,成为尾矿产品;另一部分作为中矿经中矿管10给人循环泵1,再由循环泵1给入湍流矿化发生器2的矿 浆分配管11,经湍流矿化发生器2高效矿化后再次喷射给入浮选分离释放器5实现循环分选,同时强化粗颗粒悬浮和提高浮选气泡载荷;c. The difficult-to-float particles separated by the flotation separation releaser 5 enter the middle mine tailings separator through the slurry flow channel between the cone deflector and the flotation separation releaser 5, and are divided into two parts One part is used as tailings and discharged from the flotation separation releaser 5 through tailings pipe 19 outlet B to become tailings products; the other part is used as a medium mine to be given to circulation pump 1 through medium mine pipe 10, and then to turbulent mine by circulation pump 1 The slurry distribution pipe 11 of the chemical generator 2 is efficiently mineralized by the turbulent mineralization generator 2 and then injected into the flotation separation releaser 5 to achieve cyclic separation, while strengthening the suspension of coarse particles and increasing the load of flotation bubbles;
d.压缩空气经微泡发生器12分别送入撞击流矿化管13和错流矿化管14,在湍流矿化发生器2内实现颗粒与微泡的强制混合矿化,为后续浮选分离提供保障。d. Compressed air is sent into the impinging stream mineralization tube 13 and the cross-flow mineralization tube 14 respectively through the microbubble generator 12, and the forced mixing and mineralization of particles and microbubbles is realized in the turbulent mineralization generator 2, which is a subsequent flotation Separation provides protection.

Claims (4)

  1. 一种流体协同强化浮选分离装置,其特征在于:它包括循环泵(1)、湍流矿化发生器(2)和浮选分离释放器(5),湍流矿化发生器(2)设置在浮选分离释放器(5)上方,环泵(1)分别将浮选分离释放器(5)的出口与湍流矿化发生器(2)相连接;A fluid cooperative enhanced flotation separation device, which is characterized in that it includes a circulating pump (1), a turbulent mineralization generator (2), and a flotation separation releaser (5). The turbulent mineralization generator (2) is set in Above the flotation separation releaser (5), the ring pump (1) respectively connects the outlet of the flotation separation releaser (5) with the turbulent mineralization generator (2);
    所述的湍流矿化发生器(2)包括圆筒,圆筒下方设有漏斗结构的圆锥台,圆筒周围并排设置有矿浆分配管(11),矿浆分配管(11)与圆筒之间横向设有多个撞击流矿化管(13)和多个错流矿化管(14),错流矿化管(14)与圆筒沿切向连接,撞击流矿化管(13)与圆筒沿径向连接,错流矿化管(14)和撞击流矿化管(13)上均设置有微泡发生器(12),圆锥台下方设有矿浆喷射管(6);The turbulent mineralization generator (2) includes a cylinder, a truncated cone with a funnel structure is arranged under the cylinder, and a slurry distribution pipe (11) is arranged side by side around the cylinder. The slurry distribution pipe (11) and the cylinder are A plurality of impinging stream mineralization tubes (13) and a plurality of cross-flow mineralization tubes (14) are arranged transversely. The cross-flow mineralization tubes (14) and the cylinder are connected in a tangential direction, and the impinging stream mineralization tubes (13) are connected with The cylinders are connected in the radial direction, the cross-flow mineralization tube (14) and the impinging stream mineralization tube (13) are both provided with a microbubble generator (12), and a slurry injection tube (6) is provided under the truncated cone;
    所述浮选分离释放器(5)为圆筒结构,浮选分离释放器(5)下方收窄形成倒梯台结构,底部中央设有尾矿管(19),尾矿管(19)一侧设有中矿管(10),圆筒结构上方设有泡沫槽(3),泡沫槽(3)底部设有精矿管(16),圆筒结构在泡沫槽(3)下方的内部设有竖直放置的矩形结构的超声波振板(7),超声波振板(7)下方设有环形结构的给料分配器(4),给料分配器(4)上设有多个喷头,圆筒结构内位于环形给料分配器(4)下方设有筛板(8),圆筒结构底部的倒梯台结构处设有锥形导流器,锥形导流器包括反击板(18),反击板(18)下方与倒梯台结构底部之间留有间隙,倒梯台结构上设有轮廓与倒梯台结构匹配一致,并与倒梯台结构之间留有矿浆流动通道的倒锥(17),倒锥(17)内设有多块倒梯形结构的导流立板(9),所述矿浆喷射管(6)从浮选分离释放器(5)顶部的泡沫槽(3)伸入圆筒结构内部,穿过超声波振板(7)、给料分配器(4)、筛板(8)直至多块导流立板(9)之间,矿浆喷射管(6)的末端为喇叭结构;The flotation separation releaser (5) has a cylindrical structure, the bottom of the flotation separation releaser (5) is narrowed to form an inverted terrace structure, and the bottom center is provided with a tailing pipe (19) and a tailing pipe (19). There is a medium ore pipe (10) on the side, a foam tank (3) is provided on the upper part of the cylindrical structure, a concentrate pipe (16) is provided at the bottom of the foam tank (3), and the cylindrical structure is provided inside the lower part of the foam tank (3). There is an ultrasonic vibration plate (7) with a rectangular structure vertically placed. A feed distributor (4) with a ring structure is arranged under the ultrasonic vibration plate (7). The feed distributor (4) is provided with multiple nozzles. A sieve plate (8) is provided under the annular feed distributor (4) in the cylinder structure, and a conical deflector is provided at the inverted terrace structure at the bottom of the cylindrical structure. The conical deflector includes a counterattack plate (18) There is a gap between the bottom of the counterattack plate (18) and the bottom of the inverted terrace structure. The inverted terrace structure is provided with a contour that matches the inverted terrace structure, and there is a slurry flow channel between the inverted terrace structure. Cone (17), inverted cone (17) is provided with a plurality of inverted trapezoidal structure guide vertical plates (9), the slurry injection pipe (6) from the foam tank (3) on the top of the flotation separation release device (5) ) Extends into the inside of the cylindrical structure, passes through the ultrasonic vibration plate (7), feed distributor (4), sieve plate (8) and reaches between the multiple deflector vertical plates (9), and the slurry injection pipe (6) The end is a horn structure;
    所述中矿管(10)与循环泵(1)的入口相连接,循环泵(1)的出口与矿浆分配管(11)相连接。The middle mine pipe (10) is connected with the inlet of the circulating pump (1), and the outlet of the circulating pump (1) is connected with the slurry distribution pipe (11).
  2. 根据权利要求1所述的流体协同强化浮选分离装置,其特征在于:撞击流矿化管(13)和错流矿化管(14)均为文丘里管结构形式;撞击流矿化管(13)和错流矿化管(14)交替间隔设置;相邻错流矿化管(14)切向接入圆筒的方向相反;矿浆喷射管(15)内壁设置有棱形湍流强化发生器(15)。The fluid synergistic enhanced flotation separation device according to claim 1, characterized in that: the impinging stream mineralization tube (13) and the cross-flow mineralization tube (14) are both in the form of a venturi tube; the impinging stream mineralization tube ( 13) and the cross-flow mineralization tube (14) are arranged alternately; the adjacent cross-flow mineralization tubes (14) are connected to the cylinder in the opposite direction; the inner wall of the slurry injection tube (15) is provided with a prismatic turbulence intensifying generator (15).
  3. 一种使用权利要求1所述流体协同强化浮选分离装置的流体协同强化浮选分离方法,其特征在于包括如下步骤:A method for fluid cooperative enhanced flotation separation using the fluid cooperative enhanced flotation separation device according to claim 1, characterized in that it comprises the following steps:
    a.首先关闭尾矿管(19),将调浆后的初始矿浆从给料分配器入口(A)给入给料分配器(4),并通过给料分配器(4)的喷头喷洒至浮选分离释放器(5)内,初始矿浆在重力的作用下经筛板(8)扩散后给入锥形导流器,并通过锥形导流器与浮选分离释放器(5)筒壁间的矿浆流动通道流入中矿管(10),通过循环泵(1)给入矿浆分配管(11);a. First, close the tailings pipe (19), and feed the initial slurry after mixing into the feed distributor (4) from the feed distributor inlet (A), and spray it through the nozzle of the feed distributor (4). In the flotation separation releaser (5), the initial slurry is diffused by the sieve plate (8) under the action of gravity and then fed into the conical deflector, and then passes through the conical deflector and the flotation release releaser (5) barrel The slurry flow channel between the walls flows into the middle ore pipe (10), and is fed into the slurry distribution pipe (11) through the circulating pump (1);
    b.矿浆分配(11)中的矿浆通过撞击流矿化管(13)和错流矿化管(14)给入圆筒并在圆筒中产生正方不同方向的旋流,并通过微泡发生器(12)将压缩空气混入矿浆从而在湍流矿化发生器(2)内实现颗粒与微泡的强制混合矿化,强制混合矿化后的矿浆通过湍流矿化发生器(2)底部的矿浆喷射管(15)给入浮选分离释放器(5)内的锥形导流器;b. The slurry in the slurry distribution (11) is fed into the cylinder through the impinging stream mineralization tube (13) and the cross-flow mineralization tube (14) and generates a swirling flow in different directions in the cylinder, and passes through the microbubble generator (12) The compressed air is mixed into the slurry to realize the forced mixing and mineralization of particles and microbubbles in the turbulent mineralization generator (2), and the mixed and mineralized slurry is forced to pass through the slurry jet at the bottom of the turbulent mineralization generator (2) The tube (15) feeds into the conical deflector in the flotation separation releaser (5);
    部分携带难浮颗粒的矿浆从锥形导流器的间隙进入锥形导流器与浮选分离释放器(5)筒壁间的矿浆流动通道,最终进入中矿尾矿分离器,打开尾矿管(19),进入中矿尾矿分离器的部分矿浆作为尾矿经尾矿管(19)的尾矿管出口(B)排出浮选分离释放器(5);另一部分作为中矿经中矿管(10)给入循环泵(1)继续循环,从而实现循环分选,同时强化粗颗粒悬浮和提高浮选气泡载荷;Part of the slurry carrying difficult-to-float particles enters the slurry flow channel between the cone-shaped deflector and the flotation separator release (5) from the gap of the cone-shaped deflector, and finally enters the Zhongmine tailings separator to open the tailings. Pipe (19), part of the slurry that enters the tailings separator of Zhongkuang Mine is used as tailings and is discharged from the flotation separation releaser (5) through the tailings tube outlet (B) of the tailings pipe (19); The ore pipe (10) is fed into the circulating pump (1) to continue to circulate, so as to realize circulating separation, and at the same time strengthen the suspension of coarse particles and increase the load of flotation bubbles;
    部分携带易浮颗粒的矿浆被气泡粘附后在锥形导流器中反击板(18)和导流立板(9)的作用下提高矿化气泡的升浮速度,易浮颗粒随气泡一起上浮,通过筛板(8)时过滤掉,经矩形超声波振板(7)振荡流清洗掉夹带的杂质矿物颗粒后,由浮选分离释放器(5)上方泡沫槽(3)上的精矿管(16)的精矿管出口(C)排出,其余颗粒与矿浆一起继续留在浮选分离释放器(5)内;Part of the ore slurry carrying easy-floating particles is adhered to by the air bubbles, and then under the action of the counterattack plate (18) and the vertical guide plate (9) in the cone deflector, the lifting speed of the mineralized air bubbles is increased, and the easy-floating particles are accompanied by the air bubbles. Float and filter out when passing through the sieve plate (8). After the entrained impurity mineral particles are cleaned by the oscillating flow of the rectangular ultrasonic vibration plate (7), the concentrate on the foam tank (3) above the flotation separator (5) The concentrate pipe outlet (C) of the pipe (16) is discharged, and the remaining particles remain in the flotation separation releaser (5) together with the slurry;
    c.矿浆中的易浮颗粒快速升浮,经矩形超声波振板(7)振荡流清洗掉夹带的杂质矿物颗粒后,由浮选分离释放器(5)上方泡沫槽(3)上的精矿管(16)的精矿管出口(C)排出;c. The easy-floating particles in the slurry rise and float rapidly. After the entrained impurity mineral particles are cleaned by the rectangular ultrasonic vibration plate (7), the concentrate on the foam tank (3) above the flotation releaser (5) is separated Concentrate pipe outlet (C) of pipe (16) is discharged;
    d.矿浆中的中等可浮颗粒在浮选分离释放器(5)内经筛板(8)整流后避免在浮选分离释放器(5)内剧烈的矿浆扰动造成矿化后的颗粒从气泡上脱落,再经矩形超声波振板(7)振荡流清洗掉夹带的杂质矿物颗粒后,由浮选分离释放器(5)上方泡沫槽(3)上的精矿管(16)排出。d. The medium floatable particles in the slurry are rectified by the sieve plate (8) in the flotation separation releaser (5) to avoid the violent slurry disturbance in the flotation separation releaser (5) causing the mineralized particles to fall from the bubbles. After falling off, the entrained impurity mineral particles are cleaned by the oscillating flow of the rectangular ultrasonic vibration plate (7), and then discharged from the concentrate pipe (16) on the foam tank (3) above the flotation separation release device (5).
  4. 根据权利要求1所述的流体协同强化浮选分离方法,其特征在于:压缩空气经微泡发生器(12)分别送入撞击流矿化管(13)和错流矿化管(14),在湍流矿化发生器(2)内实现颗粒与微泡的强制混合矿化,为后续浮选分离提供保障。The fluid synergistic enhanced flotation separation method according to claim 1, wherein the compressed air is sent into the impinging stream mineralization tube (13) and the cross-flow mineralization tube (14) through the microbubble generator (12), The forced mixing and mineralization of particles and microbubbles is realized in the turbulent mineralization generator (2), which provides guarantee for subsequent flotation separation.
PCT/CN2019/109882 2019-04-29 2019-10-08 Flow synergy-enhanced flotation separation apparatus and method WO2020220584A1 (en)

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