CN108480057B - flotation pulp preprocessing device - Google Patents
flotation pulp preprocessing device Download PDFInfo
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- CN108480057B CN108480057B CN201810413618.9A CN201810413618A CN108480057B CN 108480057 B CN108480057 B CN 108480057B CN 201810413618 A CN201810413618 A CN 201810413618A CN 108480057 B CN108480057 B CN 108480057B
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- 238000005188 flotation Methods 0.000 title claims abstract description 25
- 238000007781 pre-processing Methods 0.000 title claims 2
- 230000000694 effects Effects 0.000 claims abstract description 9
- 230000001804 emulsifying effect Effects 0.000 claims abstract description 3
- 238000003756 stirring Methods 0.000 claims description 52
- 239000002002 slurry Substances 0.000 claims description 21
- 239000000126 substance Substances 0.000 claims description 13
- 239000012530 fluid Substances 0.000 claims description 3
- 239000000725 suspension Substances 0.000 claims description 3
- 230000000149 penetrating effect Effects 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 abstract description 17
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract description 11
- 239000011707 mineral Substances 0.000 abstract description 11
- 239000003814 drug Substances 0.000 abstract description 10
- 239000002245 particle Substances 0.000 abstract description 10
- 150000002500 ions Chemical class 0.000 abstract description 3
- 239000003153 chemical reaction reagent Substances 0.000 description 6
- 238000012423 maintenance Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 3
- 229940079593 drug Drugs 0.000 description 3
- 238000004945 emulsification Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000013043 chemical agent Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 239000004088 foaming agent Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000008396 flotation agent Substances 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011268 mixed slurry Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000004537 pulping Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION 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
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Biotechnology (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
Description
技术领域technical field
本发明属于矿物浮选机械设备技术领域,具体说是涉及一种浮选矿浆预处理装置。The invention belongs to the technical field of mineral flotation mechanical equipment, and in particular relates to a flotation pulp pretreatment device.
背景技术Background technique
浮选是矿物分选的最主要方法之一,而调浆过程是实现矿物高效浮选的前提。传统的矿浆准备过程是通过在拌桶装置中进行调浆搅拌,以实现矿物颗粒充分分散,便于矿浆输送;实现药剂分子分散并在矿物颗粒表面吸附;调节浮选浓度等作用。通过调浆作用可以通过不同吸附作用捕收剂和抑制剂在固体颗粒表面吸附,其余调整剂和起泡剂充分与矿浆液体混合。然而,大部分浮选药剂是大分子有机物,溶解度和分散性较差。生产实践中,简单的调浆搅拌经常造成药剂分子不能充分的在矿物颗粒表面吸附,而造成的药剂大量浪费,使难免离子增多,浮选溶液化学恶化,使浮选效率降低。因此,调浆加药的好坏对浮选分离起着至关重要的作用,高效的矿浆预处理装置是提高浮选分离效果,降低药剂消耗最有效的手段之一。Flotation is one of the most important methods of mineral separation, and the pulping process is the premise of realizing efficient mineral flotation. The traditional slurry preparation process is to carry out slurry mixing in the mixing tank device to achieve sufficient dispersion of mineral particles and facilitate slurry transportation; to achieve drug molecular dispersion and adsorption on the surface of mineral particles; to adjust flotation concentration and other functions. Collectors and inhibitors can be adsorbed on the surface of solid particles through different adsorption effects through slurry adjustment, and the remaining regulators and foaming agents are fully mixed with the pulp liquid. However, most flotation reagents are macromolecular organics with poor solubility and dispersibility. In production practice, simple slurry mixing often results in insufficient adsorption of reagent molecules on the surface of mineral particles, resulting in a large waste of reagents, which inevitably increases ions, chemically deteriorates the flotation solution, and reduces flotation efficiency. Therefore, the quality of pulp mixing and dosing plays a vital role in flotation separation. Efficient pulp pretreatment device is one of the most effective means to improve flotation separation effect and reduce chemical consumption.
发明内容Contents of the invention
本发明的目的正是针对上述现有技术中存在的因调浆搅拌不充分,而导致的浮选药剂消耗大、浮选效率低、分选工艺复杂、成本较高、环境保护压力大等不足之处而提供一种基于梯级强化吸附作用的一种高效浮选矿浆预处理装置。本发明通过射流、低速混合、“W型流”的梯级强化吸附作用,改善药剂分子与矿物颗粒吸附效果,提高浮选效率,设备体积小,结构简单,便于维护。The purpose of the present invention is to solve the shortcomings in the above-mentioned prior art, such as large consumption of flotation reagents, low flotation efficiency, complicated sorting process, high cost, and high environmental protection pressure due to insufficient slurry mixing and stirring. Therefore, a high-efficiency flotation pulp pretreatment device based on step-enhanced adsorption is provided. The invention improves the adsorption effect of drug molecules and mineral particles and improves the flotation efficiency through jet flow, low-speed mixing, and "W-shaped flow" step-enhanced adsorption. The equipment is small in size, simple in structure, and easy to maintain.
本发明的目的可以通过以下技术方案来实现:The purpose of the present invention can be achieved through the following technical solutions:
本发明的浮选矿浆预处理装置包括底部设置有矿浆底流口的矿浆桶,由下至上以与矿浆桶共轴线的方式安装在矿浆桶内的搅拌叶片、搅拌轴套筒,在搅拌轴套筒上设置有延伸至矿浆桶外的用于向搅拌轴套筒内添加药剂的搅拌加药管,在矿浆桶的侧上部设置有矿浆溢流槽以及矿浆出料口,环绕矿浆桶外壁安装有带有矿浆给料口、乳化加药口以及若干个分流管的环形管,与分流管出口相连接的喷嘴分别以切向伸入矿浆桶内。The flotation pulp pretreatment device of the present invention comprises a pulp bucket with a pulp bottom outlet at the bottom, a stirring blade and a stirring shaft sleeve installed in the pulp bucket in a coaxial manner with the pulp bucket from bottom to top, and the stirring shaft sleeve There is a stirring and dosing pipe extending to the outside of the pulp barrel for adding chemicals to the stirring shaft sleeve. A pulp overflow tank and a pulp outlet are arranged on the upper side of the pulp barrel, and a belt is installed around the outer wall of the pulp barrel. There is a slurry feeding port, an emulsifying chemical feeding port and a ring pipe of several shunting pipes, and the nozzles connected with the outlets of the shunting pipes respectively extend into the pulp barrel tangentially.
本发明中所述搅拌轴套筒悬吊在矿浆桶的上盖体下方,且在搅拌轴套筒上均匀分布若干个圆形通孔;所述搅拌叶片通过穿装在搅拌轴套筒内、且竖直向上延伸的搅拌轴与设置在矿浆桶顶部的电机驱动系统相结合,并以悬吊方式设置搅拌轴套筒下方。In the present invention, the stirring shaft sleeve is suspended under the upper cover of the pulp barrel, and several circular through holes are evenly distributed on the stirring shaft sleeve; the stirring blades are installed in the stirring shaft sleeve, And the stirring shaft extending vertically upwards is combined with the motor drive system arranged on the top of the slurry tank, and is set under the stirring shaft sleeve in a suspended manner.
本发明中所述环形管的横截面呈正方形结构,环绕所述环形管以均布的方式设置有六个分流管;所述矿浆桶底部为45度椎体,并安装有检修底流控制阀门,桶体通过连接件固定安装在机架上。The cross-section of the annular pipe in the present invention is a square structure, and six shunt pipes are evenly distributed around the annular pipe; the bottom of the slurry tank is a 45-degree cone, and an underflow control valve is installed for maintenance. The bucket body is fixedly installed on the frame through the connecting piece.
本发明中与分流管出口相连接的喷嘴的切向进入方向与搅拌叶片转动方向相反,喷嘴产生的高速射流,搅拌叶片与套筒产生负压吸入作用,相反的方向使两股流体形成“W型流”,增加了矿浆的二次混合。In the present invention, the tangential entry direction of the nozzle connected to the outlet of the shunt pipe is opposite to the rotation direction of the stirring blade. The high-speed jet flow produced by the nozzle, the stirring blade and the sleeve produce negative pressure suction, and the opposite direction makes the two fluids form a "W" type flow", increasing the secondary mixing of pulp.
本发明中所述入料口、环形管呈水平方向固定于预处理装置矿浆桶下方600mm处,环形管距离桶体50mm,以保证分流管的喷嘴可沿切向进出桶体,并可实现检修和更换。In the present invention, the feed inlet and the annular pipe are fixed horizontally at the place 600 mm below the slurry tank of the pretreatment device, and the annular pipe is 50 mm away from the barrel body, so as to ensure that the nozzle of the shunt pipe can enter and exit the barrel body tangentially, and maintenance can be realized and replace.
本发明的工作原理及有益效果如下:Working principle of the present invention and beneficial effect are as follows:
原矿浆通过矿浆给料口进入环形管,第一类浮选药剂(诸如调整剂、捕收剂,或者难溶性、难分散药剂等)通过乳化加药口也进入环形管中,第一类药剂与矿浆在环形管内进行初步混合。初步混合后的矿浆从6个分流管的喷嘴处,以高速射流切向进入矿浆桶中,在此过程中,第一类药剂分散成乳化状态,并在高紊流作用下药剂分子在矿物表面吸附(通过药剂和矿浆的高速射流作用实现难溶性药剂乳化并在矿物颗粒表面高效附着)。与此同时通过搅拌加药管向搅拌轴套筒内添加第二类药剂(诸如起泡剂,易溶解分散药剂等),电机驱动系统驱动搅拌轴以300r/min转速实现第二类药剂与矿浆混合吸附,并使矿浆呈悬浮状态,充分解离后,粒度和浓度符合浮选要求的原矿浆。预处理后的矿浆通过溢流槽从矿浆出料口流出。矿浆桶底部设置的矿浆底流口,以备排料、停机检修。The raw ore pulp enters the annular pipe through the pulp feeding port, and the first type of flotation agents (such as regulators, collectors, or insoluble and difficult to disperse agents, etc.) also enters the annular pipe through the emulsification feeding port. Preliminary mixing with the slurry in the annular tube. The preliminarily mixed slurry enters the slurry tank tangentially with high-speed jets from the nozzles of the six distribution pipes. During this process, the first type of chemical is dispersed into an emulsified state, and the chemical molecules are on the surface of the mineral under the action of high turbulence. Adsorption (through the high-speed jet action of the agent and the pulp to emulsify the insoluble agent and attach it efficiently to the surface of the mineral particles). At the same time, add the second type of chemical (such as foaming agent, easy-to-dissolve and disperse chemical, etc.) Mixed adsorption, and make the ore pulp in a suspended state, after fully dissociated, the particle size and concentration meet the flotation requirements of raw ore pulp. The pretreated pulp flows out from the pulp outlet through the overflow tank. The bottom outlet of the slurry tank is set at the bottom of the slurry tank for discharge, shutdown and maintenance.
在上述的高效浮选矿浆预处理装置中,经高速射流乳化后吸附与颗粒表面的矿浆通过搅拌轴套筒、电机驱动搅拌叶片实现矿浆的悬浮,并在桶体内形成“W”型流,易溶解分散的第二类药剂通过搅拌加药管加入搅拌轴套筒内75cm高度处,在低紊流作用下实现第二类药剂的混合、吸附和悬浮。In the above-mentioned high-efficiency flotation pulp pretreatment device, after high-speed jet emulsification, the pulp adsorbed on the surface of the particles is suspended through the stirring shaft sleeve and the motor-driven stirring blades, and a "W"-shaped flow is formed in the barrel, which is easy The dissolved and dispersed second-type medicament is fed into the stirring shaft sleeve at a height of 75 cm through the stirring dosing pipe, and the mixing, adsorption and suspension of the second-type medicament are realized under the action of low turbulence.
综上所述,本发明优点在于:降低药剂消耗量,改善药剂分子与矿物颗粒吸附效果,减少浮选中难免离子;设备体积小,结构简单,便于维护。To sum up, the advantages of the present invention are: reducing the consumption of chemicals, improving the adsorption effect of drug molecules and mineral particles, reducing unavoidable ions in flotation; the equipment is small in size, simple in structure and easy to maintain.
附图说明Description of drawings
图1 是本发明的整体结构示意图。Figure 1 is a schematic diagram of the overall structure of the present invention.
图2 是图1的横截面示意图。FIG. 2 is a schematic cross-sectional view of FIG. 1 .
图3 是分流管结构示意图。Figure 3 is a schematic diagram of the shunt tube structure.
具体实施方式Detailed ways
本发明以下将结合实施例(附图)作进一步描述:The present invention will be further described below in conjunction with embodiment (accompanying drawing):
如图1、2所示,本发明的浮选矿浆预处理装置包括底部设置有矿浆底流口12的矿浆桶,由下至上以与矿浆桶共轴线的方式安装在矿浆桶内的搅拌叶片8、搅拌轴套筒5,在搅拌轴套筒5上设置有延伸至矿浆桶外的用于向搅拌轴套筒内添加药剂的搅拌加药管9,所述搅拌轴套筒5悬吊在矿浆桶的上盖体下方,且在搅拌轴套筒5上均匀分布若干个圆形通孔;所述搅拌叶片8通过穿装在搅拌轴套筒5内、且竖直向上延伸的搅拌轴7与设置在矿浆桶顶部的电机驱动系统6相结合,并以悬吊方式设置搅拌轴套筒5下方;在矿浆桶的侧上部设置有矿浆溢流槽10以及矿浆出料口11,环绕矿浆桶外壁安装有带有矿浆给料口1、乳化加药口3以及六个分流管4的环形管2,与分流管4出口相连接的喷嘴分别以切向伸入矿浆桶内;所述环形管2的横截面呈正方形结构,六个分流管4环绕所述环形管2以均布的方式设置;所述矿浆桶底部为45度椎体,并安装有检修底流控制阀门,桶体通过连接件固定安装在机架上。As shown in Figures 1 and 2, the flotation pulp pretreatment device of the present invention includes a pulp bucket with a bottom flow port 12 at the bottom, and a stirring blade 8 installed in the pulp bucket in a coaxial manner with the pulp bucket from bottom to top. The stirring shaft sleeve 5 is provided with a stirring dosing tube 9 extending outside the pulp barrel for adding medicine to the stirring shaft sleeve, and the stirring shaft sleeve 5 is suspended on the pulp barrel Below the upper cover, and several circular through-holes are evenly distributed on the stirring shaft sleeve 5; the stirring blade 8 passes through the stirring shaft 7 and the setting The motor drive system 6 on the top of the pulp bucket is combined, and the bottom of the stirring shaft sleeve 5 is set in a suspended manner; a pulp overflow tank 10 and a pulp outlet 11 are arranged on the upper side of the pulp bucket, which are installed around the outer wall of the pulp bucket There is an annular pipe 2 with a pulp feeding port 1, an emulsification dosing port 3 and six shunt pipes 4, and the nozzles connected to the outlets of the shunt pipes 4 respectively extend into the pulp barrel tangentially; the ring pipe 2 The cross-section is a square structure, and six shunt pipes 4 are arranged in a uniform manner around the annular pipe 2; the bottom of the slurry tank is a 45-degree cone, and is installed with an underflow control valve for maintenance, and the tank body is fixed and installed by connecting pieces on the rack.
所述分流管4的结构参见图3所示。The structure of the shunt pipe 4 is shown in FIG. 3 .
本发明中与分流管4出口相连接的喷嘴的切向进入方向与搅拌叶片8转动方向相反,喷嘴产生的高速射流,搅拌叶片8与套筒5产生负压吸入作用,相反的方向使两股流体形成“W型流”,增加了矿浆的二次混合。In the present invention, the tangential entry direction of the nozzle connected to the outlet of the shunt pipe 4 is opposite to the rotation direction of the stirring blade 8. The high-speed jet flow produced by the nozzle causes the negative pressure suction effect of the stirring blade 8 and the sleeve 5, and the opposite direction makes the two streams The fluid forms a "W-shaped flow", which increases the secondary mixing of the pulp.
本发明中所述入料口1、环形管2呈水平方向固定于预处理装置矿浆桶下方600mm处,环形管距离桶体50mm,以保证分流管的喷嘴可沿切向进出桶体,并可实现检修和更换。In the present invention, the inlet 1 and the annular pipe 2 are fixed horizontally at the place 600 mm below the slurry tank of the pretreatment device, and the annular pipe is 50 mm away from the barrel to ensure that the nozzle of the shunt pipe can enter and exit the barrel tangentially, and can Realize maintenance and replacement.
本发明中所述的电机驱动系统6驱动搅拌轴7以300r/min转速实现第二类药剂与矿浆混合吸附,并使矿浆呈悬浮状态。给料口1通过公称通径DN80法兰连接输料管路,所述环形管横截面边长均为80mm的正方形。分流管的公称通径DN25,喷嘴口内径为15mm,分流管4的喷嘴分别以切向伸入矿浆桶内20mm。The motor drive system 6 described in the present invention drives the stirring shaft 7 at a speed of 300 r/min to realize the mixing and adsorption of the second type of medicament and the pulp, and make the pulp in a suspended state. The feeding port 1 is connected to the feeding pipeline through a flange with a nominal diameter of DN80, and the cross-section of the annular pipe is a square with a side length of 80 mm. The nominal diameter of the shunt pipe is DN25, the inner diameter of the nozzle opening is 15 mm, and the nozzles of the shunt pipe 4 respectively extend 20 mm into the pulp bucket tangentially.
本发明的矿浆预处理装置筒体参考直径1000mm,高1280mm,矿浆桶内通过悬臂固定有直径为450mm的搅拌轴套筒5,套筒上均匀分布100mm圆形开孔,开孔率38%,沿套筒固定700mm长,25mm直径搅拌加药管9。The cylinder of the pulp pretreatment device of the present invention has a reference diameter of 1000 mm and a height of 1280 mm. A stirring shaft sleeve 5 with a diameter of 450 mm is fixed in the pulp tank through a cantilever. 100 mm circular openings are evenly distributed on the sleeve, and the opening rate is 38%. Fix 700mm long along sleeve, 25mm diameter stirs and feeds pipe 9.
本发明采用3kw电机通过皮带轮减速驱动1000mm长的搅拌轴7带动三叶片叶轮转动,转速300r/min。这一转速使得第二类药剂易分散,以及后序作用药剂与矿浆实现低速混合吸附。The present invention uses a 3kw motor to drive the 1000mm long stirring shaft 7 to drive the three-blade impeller to rotate through the belt pulley deceleration at a speed of 300r/min. This rotation speed makes the second type of chemical agent easy to disperse, and realizes low-speed mixing and adsorption of subsequent acting chemical agent and ore pulp.
本发明中分流管4的喷嘴产生的射流,搅拌轴套筒5、搅拌轴7、搅拌叶片8产生的低速搅拌系统,“W型流”形成的二次混合作用,分别对溶解度从难到易和顺序为从前到后的药剂形成“梯级强化吸附作用”。In the present invention, the jet flow produced by the nozzle of the shunt pipe 4, the low-speed stirring system produced by the stirring shaft sleeve 5, the stirring shaft 7, and the stirring blade 8, and the secondary mixing effect formed by "W-shaped flow" affect the solubility from difficult to easy respectively. And the order is from the front to the back of the reagents to form a "step-enhanced adsorption effect".
本发明的主要特点在于:Main features of the present invention are:
(1)经初步混合后的难溶、难分散药剂与矿浆通过高速射流乳化,实现高效吸附。(1) After preliminary mixing, the insoluble and difficult-to-disperse chemicals and pulp are emulsified by high-speed jet to achieve high-efficiency adsorption.
(2)易溶性、分散药剂实现低紊流混合吸附,并通过底部“W”型流实现矿浆悬浮。(2) Easily soluble and dispersible chemicals realize low turbulence mixing and adsorption, and realize slurry suspension through the bottom "W" flow.
(3)吸附难易程度不同的药剂通过梯级强化方式实现高效浮选矿浆预处理。(3) Reagents with different degrees of difficulty in adsorption can achieve high-efficiency flotation pulp pretreatment through cascade strengthening.
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CN105363380A (en) * | 2015-10-27 | 2016-03-02 | 中国矿业大学 | Device and method for pretreating external circulation type pulp based on jet flow mixing |
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