CN202186917U - Special-shaped deep-cone concentrator - Google Patents
Special-shaped deep-cone concentrator Download PDFInfo
- Publication number
- CN202186917U CN202186917U CN 201120302066 CN201120302066U CN202186917U CN 202186917 U CN202186917 U CN 202186917U CN 201120302066 CN201120302066 CN 201120302066 CN 201120302066 U CN201120302066 U CN 201120302066U CN 202186917 U CN202186917 U CN 202186917U
- Authority
- CN
- China
- Prior art keywords
- pool body
- cylinder
- pool
- stirring shaft
- bridge frame
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000009826 distribution Methods 0.000 claims abstract description 22
- 238000003756 stirring Methods 0.000 claims abstract description 20
- 238000004088 simulation Methods 0.000 claims abstract description 11
- 230000000423 heterosexual effect Effects 0.000 claims abstract description 10
- 238000005516 engineering process Methods 0.000 claims abstract description 9
- 238000005189 flocculation Methods 0.000 claims abstract description 8
- 230000016615 flocculation Effects 0.000 claims abstract description 8
- 239000004744 fabric Substances 0.000 claims abstract description 6
- 238000003466 welding Methods 0.000 claims abstract 2
- 239000002562 thickening agent Substances 0.000 claims description 6
- 230000007246 mechanism Effects 0.000 claims description 5
- 230000008878 coupling Effects 0.000 claims description 2
- 238000010168 coupling process Methods 0.000 claims description 2
- 238000005859 coupling reaction Methods 0.000 claims description 2
- 239000000463 material Substances 0.000 abstract description 9
- 239000002351 wastewater Substances 0.000 abstract description 8
- 229910000831 Steel Inorganic materials 0.000 abstract description 3
- 239000010802 sludge Substances 0.000 abstract description 3
- 239000010959 steel Substances 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 230000000694 effects Effects 0.000 abstract description 2
- 230000009467 reduction Effects 0.000 abstract description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 230000015271 coagulation Effects 0.000 description 3
- 238000005345 coagulation Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000001687 destabilization Effects 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000007596 consolidation process Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
Images
Landscapes
- Treatment Of Sludge (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
本实用新型公开了异性深锥浓缩机,包括有絮凝剂管、桥架和池体,池体由三段不同锥度锥面构成,且自上而下锥度依次增大,其锥度由CFD技术对絮凝沉降数值模拟确定;桥架中间设有横梁,桥架下部固定有环形桶,环形桶下部连接有布料筒,所述布料筒为母线是样条曲线的圆桶状,上、下部截面大,中间小,其形状由CFD技术对混合流场数值模拟确定;环形桶内壁上设有挡圈,布料筒上盖置于挡圈上;布料筒上部沿切线方向连通有入料管,絮凝剂管在池外连到入料管上;所述布料筒中间设有圆柱筒,其顶部固定在横梁的下表面上,其底部安装有喇叭形的导流板,导流板与布料筒之间通过圆钢均布焊接;横梁上安装有电机,电机的输出轴外连接有搅拌轴,搅拌轴穿过圆柱筒并伸到池体的下部。本实用新型的布料筒及池体几何结构适应废水矿浆的絮凝沉降、浓缩规律,并利于污泥沉降、排卸,结构简单、浓缩效果好、效率高、节能降耗。
The utility model discloses a heterosexual deep cone concentrator, which includes a flocculant tube, a bridge frame and a pool body. The pool body is composed of three sections of different taper surfaces, and the taper increases sequentially from top to bottom. The taper is controlled by CFD technology. Settlement numerical simulation is determined; there is a beam in the middle of the bridge frame, an annular barrel is fixed at the lower part of the bridge frame, and a distribution tube is connected to the lower part of the ring barrel. The distribution tube is a barrel-shaped busbar with a spline curve. Its shape is determined by the numerical simulation of the mixed flow field by CFD technology; there is a retaining ring on the inner wall of the annular barrel, and the upper cover of the distributing cylinder is placed on the retaining ring; It is connected to the feed pipe; a cylinder is arranged in the middle of the cloth tube, the top of which is fixed on the lower surface of the beam, and a trumpet-shaped deflector is installed at the bottom, and the round steel is passed between the deflector and the distribution tube. Cloth welding; the motor is installed on the beam, the output shaft of the motor is connected with the stirring shaft, the stirring shaft passes through the cylinder and extends to the lower part of the pool body. The geometric structure of the material distributing cylinder and the pool body of the utility model is adapted to the flocculation, settlement and concentration rules of waste water ore pulp, and is beneficial to sludge settlement and discharge. The utility model has the advantages of simple structure, good concentration effect, high efficiency, energy saving and consumption reduction.
Description
技术领域 technical field
本实用新型属于环保机械,涉及一种选矿生产用的尾矿水处理设备,具体是一种添加絮凝剂的异形深锥浓缩机。 The utility model belongs to environmental protection machinery and relates to tailings water treatment equipment for ore dressing production, in particular to a special-shaped deep-cone concentrator with flocculant added.
背景技术 Background technique
选矿生产中的尾矿废水一般都使用深锥浓缩机处理,该机池体呈立式圆柱加倒锥结构,一般设有入料管、布料筒、溢流槽、搅拌装置、排料装置。废水由入料管进入浓缩机,在搅拌装置作用下,与絮凝剂混凝脱稳,并凝聚造粒下降沉淀,沉淀浓缩的矿浆经下部排料装置排出,上部澄清后的溢流水可循环再使用。 The tailings wastewater in mineral processing production is generally treated by a deep cone thickener. The tank body of this machine is a vertical cylinder and an inverted cone structure. It is generally equipped with a feeding pipe, a material distribution cylinder, an overflow tank, a stirring device, and a discharging device. The waste water enters the concentrator from the feed pipe, and under the action of the stirring device, it coagulates with the flocculant and destabilizes, and coagulates and granulates to descend and settle. The precipitated and concentrated pulp is discharged through the lower discharge device, and the overflow water after upper clarification can be recycled. use.
普通深锥浓缩机的入料方式是废水从池中心直接给入,布料筒的作用是仅把物料送往指定深度,并无混凝脱稳功能;或在筒中或在其出口处设置搅拌装置以实现该功能,但结构复杂且有能耗。普通布料筒出口大多竖直向下,无缓冲装置,高速入料的悬浮液难以充分沉淀,导致溢流浓度偏高;已经沉淀的尾矿层也会受其冲刷而遭到破坏,导致底流浓度偏低。普通深锥浓缩机的池体为整体圆柱加倒锥结构,锥面锥度固定,不能适应矿浆的絮凝沉降、浓缩汇聚、污泥排泄的要求。普通深锥浓缩机在锥底所设的刮泥耙一般为平板结构,常翻起高浓度的悬浮液,影响底流浓度,且运行阻力及消耗功率大。 The feeding method of the ordinary deep cone thickener is that the waste water is fed directly from the center of the pool, and the function of the distributing cylinder is only to send the material to the specified depth, without the function of coagulation and destabilization; or a stirring device is installed in the cylinder or at its outlet To realize this function, but the structure is complicated and energy consumption is arranged. Most of the outlets of ordinary material distribution tubes are vertically downward without buffer devices. The high-speed feeding suspension is difficult to fully settle, resulting in high overflow concentration; Low. The tank body of the ordinary deep cone thickener is a whole cylinder plus an inverted cone structure, and the taper of the cone surface is fixed, which cannot meet the requirements of flocculation and settlement, concentration and aggregation of ore pulp, and sludge discharge. The mud scraper installed at the bottom of the cone of ordinary deep cone thickeners is generally a flat structure, which often turns up high-concentration suspensions, affecting the concentration of the bottom flow, and has high running resistance and power consumption. the
实用新型内容 Utility model content
本实用新型的目的在于弥补已有技术的不足,提供一种异形深锥浓缩机,用于浓缩分离选矿生产中尾矿水的矿浆。 The purpose of the utility model is to make up for the deficiencies of the prior art, and to provide a special-shaped deep cone concentrator, which is used for concentrating and separating the slurry of tailings water in mineral processing production. the
异性深锥浓缩机,包括有絮凝剂管、桥架和池体,其特征在于:池体为锥度由CFD技术对絮凝沉降数值模拟确定的锥面构成,所述锥面包括三段不同的锥度且自上而下锥度依次增大;所述桥架中间设有横梁,桥架下部固定有环形桶,所述环形桶下部通过法兰连接有位于池体内的布料筒,布料筒的形状由CFD技术对混合流场数值模拟确定为母线是样条曲线的圆桶状,其上、下部截面尺寸大于其中部截面尺寸;所述环形桶内壁上设有挡圈,布料筒上盖置于挡圈上;布料筒上部沿切线方向连通有入料管,絮凝剂管在池外连到入料管上;所述布料筒中间设有圆柱筒,其顶部穿过布料筒上盖上的中心孔后固定在横梁的下表面上,其底部安装有导流板,导流板的形状为由CFD技术对混合流场数值模拟确定的喇叭形;所述导流板与布料筒之间通过圆钢均布焊接;所述横梁上安装有电机,电机的输出轴通过联轴器连接有搅拌轴,所述搅拌轴穿过圆柱筒并伸到池体的下部,搅拌轴底部固定套装有疏松机构,疏松机构包括有套装在搅拌轴上的中心毂,中心毂上均布若干梳状耙。 The heterosexual deep cone thickener includes a flocculant tube, a bridge frame and a pool body. It is characterized in that: the pool body is tapered and is composed of a cone surface determined by CFD technology for flocculation and settlement numerical simulation. The cone surface includes three sections of different tapers and The taper increases sequentially from top to bottom; there is a beam in the middle of the bridge frame, and an annular barrel is fixed on the lower part of the bridge frame. The lower part of the annular barrel is connected with a distribution tube located in the pool through a flange. The numerical simulation of the flow field determines that the generatrix is a barrel-shaped spline curve, and its upper and lower cross-sectional dimensions are larger than the middle cross-sectional dimension; the inner wall of the annular barrel is provided with a retaining ring, and the upper cover of the distribution tube is placed on the retaining ring; The upper part of the cylinder is connected with the feed pipe along the tangential direction, and the flocculant pipe is connected to the feed pipe outside the tank; a cylindrical cylinder is arranged in the middle of the distribution cylinder, and its top passes through the center hole on the upper cover of the distribution cylinder and is fixed on the beam On the lower surface of the lower surface, a deflector is installed at the bottom, and the shape of the deflector is trumpet-shaped determined by the numerical simulation of the mixed flow field by CFD technology; the deflector and the distribution cylinder are evenly welded by round steel; A motor is installed on the beam, and the output shaft of the motor is connected to the stirring shaft through a coupling. The stirring shaft passes through the cylinder and extends to the lower part of the pool body. The bottom of the stirring shaft is fixed with a loosening mechanism, and the loosening mechanism includes: The central hub is set on the stirring shaft, and several comb rakes are evenly distributed on the central hub.
异性深锥浓缩机,其特征在于:包括有位于池体内的轴承座,轴承座内安装有轴承,所述轴承套装在搅拌轴的下部,所述轴承座与池体内壁之间固定连接有支撑杆。 The heterosexual deep cone concentrator is characterized in that it includes a bearing seat located in the tank body, a bearing is installed in the bearing seat, the bearing is set on the lower part of the stirring shaft, and a support is fixedly connected between the bearing seat and the inner wall of the pool pole.
异性深锥浓缩机,其特征在于:所述池体的池底设有排泥口。 The heterosexual deep cone concentrator is characterized in that: the bottom of the pool body is provided with a mud discharge port.
异性深锥浓缩机,其特征在于:所述布料筒上盖上分布有透气孔。 The heterosexual deep cone concentrator is characterized in that: the upper cover of the cloth cylinder is distributed with air holes.
异性深锥浓缩机,其特征在于:池体通过支柱支撑固定。 The heterosexual deep cone concentrator is characterized in that the pool body is supported and fixed by pillars.
其工作过程为,絮凝剂在池外加入所述入料管,流动中与废水初步混合;并沿切线进入布料筒上段,沿布料筒内壁旋转下降,并产生涡流,使絮凝剂与废水进一步混合;在布料筒中段,随着截面减小,物料流速增加,絮凝剂与废水得以充分混合,完成混凝脱稳阶段;在布料筒下段,物料在喇叭形布料筒与导流板共同作用下,沿水平布料,对下部沉降物不冲击扰动,随着下锥段断面不断加大、流速降低,形成絮凝所需条件,开始絮凝。由于物料已在布料筒中充分混合,此处无需搅拌装置。物料上升过程中,随着池体截面的增大,流速进一步降低,不断析出颗粒形成絮团,沉降到池体上,完成凝聚造粒阶段;水流继续上升,最后形成清水从溢流槽流出。所述池体上段锥面锥度较小,沉降面积大;池体中段锥面锥度增大,实现快速沉降并利于絮团下滑;池体锥面下段锥度较大,便于池底絮团排泄。梳状刮泥耙可有效减少絮团挂壁并避免固结,阻力及消耗功率小,不易压耙;底泥由排泥口排出。 The working process is that the flocculant is added to the feeding pipe outside the pool, and is initially mixed with the wastewater during the flow; and enters the upper section of the distribution cylinder along the tangent, rotates and descends along the inner wall of the distribution cylinder, and generates a vortex to further mix the flocculant with the wastewater ;In the middle section of the distribution tube, as the cross section decreases, the flow rate of the material increases, the flocculant and the wastewater are fully mixed, and the coagulation and destabilization stage is completed; The material is distributed along the horizontal, without impact and disturbance on the lower sediment. As the section of the lower cone section continues to increase and the flow velocity decreases, the conditions required for flocculation are formed and flocculation begins. Since the materials have been fully mixed in the distribution drum, no stirring device is needed here. During the rising process of the material, as the cross section of the tank body increases, the flow rate further decreases, and the particles are continuously precipitated to form flocs, which settle on the tank body and complete the coagulation and granulation stage; the water flow continues to rise, and finally forms clear water to flow out from the overflow tank. The taper of the upper section of the pool body is small and the settlement area is large; the taper of the cone surface of the middle section of the pool body is increased to achieve rapid settlement and facilitate the sliding of flocs; the taper of the lower section of the pool body is larger to facilitate the discharge of flocs at the bottom of the pool. The comb-shaped mud scraping rake can effectively reduce the floc hanging on the wall and avoid consolidation, the resistance and power consumption are small, and it is not easy to press the rake; the bottom mud is discharged from the mud discharge port.
本实用新型的优点是: The utility model has the advantages of:
本实用新型中的布料筒及池体几何结构适应废水矿浆的絮凝沉降、浓缩规律,并利于污泥沉降、排卸;结构简单、浓缩效果好、效率高、节能降耗。 The geometric structure of the material distributing cylinder and the pool body in the utility model is adapted to the flocculation, settlement and concentration rules of wastewater ore pulp, and is beneficial to sludge settlement and discharge; the utility model has the advantages of simple structure, good concentration effect, high efficiency, energy saving and consumption reduction.
附图说明 Description of drawings
图1为本实用新型的结构示意图。 Fig. 1 is the structural representation of the utility model.
图2为布料筒与桥架连接部分放大图。 Figure 2 is an enlarged view of the connection part between the distribution tube and the bridge frame.
具体实施方式 Detailed ways
参见附图1和2,一种异形深锥浓缩机,包括布料筒1、池体、疏松机构、桥架5、入料管18等。所述池体上沿设有环形溢流槽19,并设有过池体中心的所述桥架5,桥架5上设有扶手6,供人员通行。絮凝剂管17在池外连到所述入料管18,所述入料管18沿切线进入所述布料筒1上段。所述布料筒1为母线是样条曲线的圆桶状,上、下部截面大,中间小,其形状由CFD技术对混合流场数值模拟确定,所述布料筒1通过法兰2用螺栓21联接到环形桶4上,所述环形桶4与所述桥架5焊接固定,所述环形桶4内壁焊有挡圈3,布料筒上盖20置于其上,所述布料筒上盖20均布若干φ10透气孔。所述布料筒1中间设有细长圆柱筒23,其上部通过螺栓15连接到法兰盘14,所述法兰盘14与横梁16焊接,所述横梁16与所述桥架5焊接固定。所述圆柱筒23底部装有喇叭形导流板26,其形状由CFD技术对混合流场数值模拟确定。所述布料筒1及导流板26用圆钢25均布焊接,连为一体。所述池体为三段不同锥度锥面24、29、35联接构成,锥度依次增大,其锥度由CFD技术对絮凝沉降数值模拟确定,所述池底设有排泥口36。所述疏松机构布置在中段池体29的下部,其搅动轴27通过联接法兰9与电机7用螺栓10连接,用键8带动旋转。所述搅动轴27及装配于其上的梳状刮泥耙的重量通过推力球轴承11作用在轴承座12上,所述轴承座12用螺钉13连接到法兰14上。所述搅动轴27下部以滑动轴承30支撑,所述滑动轴承30安装在轴承座32上,所述轴承座32用三个支撑杆31与池体29均布焊接固定。所述梳状刮泥耙安装在搅动轴27下端,其中心毂33与搅拌轴27以键传动,所述中心毂33上均布若干梳状耙34。所述倒锥池体24、29、35用若干支柱28支撑固定。
Referring to accompanying
Claims (5)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201120302066 CN202186917U (en) | 2011-08-18 | 2011-08-18 | Special-shaped deep-cone concentrator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201120302066 CN202186917U (en) | 2011-08-18 | 2011-08-18 | Special-shaped deep-cone concentrator |
Publications (1)
Publication Number | Publication Date |
---|---|
CN202186917U true CN202186917U (en) | 2012-04-11 |
Family
ID=45918380
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 201120302066 Expired - Fee Related CN202186917U (en) | 2011-08-18 | 2011-08-18 | Special-shaped deep-cone concentrator |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN202186917U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112169383A (en) * | 2020-10-16 | 2021-01-05 | 淮北市协力重型机器有限责任公司 | Recovery device with slurry intervention interference structure |
CN112221207A (en) * | 2019-12-13 | 2021-01-15 | 安徽理工大学 | Efficient multistage sedimentation rake-free concentration device |
-
2011
- 2011-08-18 CN CN 201120302066 patent/CN202186917U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112221207A (en) * | 2019-12-13 | 2021-01-15 | 安徽理工大学 | Efficient multistage sedimentation rake-free concentration device |
CN112169383A (en) * | 2020-10-16 | 2021-01-05 | 淮北市协力重型机器有限责任公司 | Recovery device with slurry intervention interference structure |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102001769A (en) | Integrated water purifying and processing equipment | |
CN110025988B (en) | A coal slime water concentration treatment system with three-stage underflow discharge | |
CN102078708A (en) | Water treatment solid-liquid separator by hydrocyclone granulation | |
CN101569808B (en) | Uninterrupted anti-disturbance flocculent deposit reverse separation system | |
CN209537204U (en) | Magnetic loads water treatment facilities | |
CN205886307U (en) | There is not concentrated machine of harrow with formula of circling round annular channel | |
CN105641980B (en) | Washed-out sand waste water solid separator | |
CN104803523B (en) | The continuous harvesting apparatus of microalgae and method thereof associated with a kind of electricity flocculation-flotation | |
CN201815155U (en) | Novel slow-flow high-efficiency thickening machine | |
CN110342621B (en) | Two-stage concentration sedimentation high-concentration beneficiation wastewater treatment equipment | |
CN202186917U (en) | Special-shaped deep-cone concentrator | |
CN207581572U (en) | High-efficient sedimentation tank | |
CN205672618U (en) | A kind of high-efficiency concentrator with self-cleaning pressure-preventing rake function | |
CN110025989B (en) | Rake-free thickener with three-section discharge outlets | |
CN204503355U (en) | A kind of defoaming device for floatation ore dressing | |
CN105381887B (en) | A slurry mixing tank for fine mineral flotation | |
CN106984070A (en) | A kind of flocculation stirring device dense for mine tailing | |
CN204550164U (en) | For the contact flocculation reaction unit of water treatment coagulation process | |
CN208454682U (en) | A kind of environment-friendly sewage processing unit | |
CN205055507U (en) | 50 heavy high -efficient concentrated machine of indisputable tailing of rice | |
CN205413365U (en) | A stirred tank of sizing mixing that is used for flotation of fine grain mineral | |
CN202654759U (en) | Deep-cone thickener | |
CN212954460U (en) | High-efficient device that subsides of mine water | |
CN107522270A (en) | A kind of dense device of combined type magnetic flocculation | |
CN202725305U (en) | Desliming equipment for beneficiation |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120411 Termination date: 20120818 |