WO2014117587A1 - Rotational-flow sorting and cleaning apparatus and method for waste plastic pieces - Google Patents

Rotational-flow sorting and cleaning apparatus and method for waste plastic pieces Download PDF

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Publication number
WO2014117587A1
WO2014117587A1 PCT/CN2013/088124 CN2013088124W WO2014117587A1 WO 2014117587 A1 WO2014117587 A1 WO 2014117587A1 CN 2013088124 W CN2013088124 W CN 2013088124W WO 2014117587 A1 WO2014117587 A1 WO 2014117587A1
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WO
WIPO (PCT)
Prior art keywords
waste plastic
sediment
cleaning device
tapered
isolation net
Prior art date
Application number
PCT/CN2013/088124
Other languages
French (fr)
Chinese (zh)
Inventor
冯愚斌
Original Assignee
Feng Yubin
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Publication date
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Publication of WO2014117587A1 publication Critical patent/WO2014117587A1/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • 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
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B5/00Washing granular, powdered or lumpy materials; Wet separating
    • B03B5/28Washing granular, powdered or lumpy materials; Wet separating by sink-float separation
    • B03B5/30Washing granular, powdered or lumpy materials; Wet separating by sink-float separation using heavy liquids or suspensions
    • B03B5/32Washing granular, powdered or lumpy materials; Wet separating by sink-float separation using heavy liquids or suspensions using centrifugal force
    • B03B5/34Applications of hydrocyclones
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B04CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04CAPPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
    • B04C5/00Apparatus in which the axial direction of the vortex is reversed
    • B04C5/08Vortex chamber constructions
    • B04C5/103Bodies or members, e.g. bulkheads, guides, in the vortex chamber
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • B29B2017/0213Specific separating techniques
    • B29B2017/0217Mechanical separating techniques; devices therefor
    • B29B2017/0231Centrifugating, cyclones
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • B29B2017/0213Specific separating techniques
    • B29B2017/0286Cleaning means used for separation
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Definitions

  • the present invention relates to recycling and cleaning techniques for waste plastics and, in particular, to a cyclone sorting and cleaning apparatus and method for waste plastic chips. Background technique
  • waste plastics continue to increase. If these waste plastics are not handled properly, they will inevitably damage the environment, destroy the ecological balance, and ultimately threaten the survival of mankind.
  • the existing waste plastics are mainly treated as follows: After the waste plastics are recycled, they are first classified, broken into pieces, cleaned, and then the chips are melted to form new plastic raw material pellets and finished products for recycling.
  • the sorting plastics are all sorted by flotation, which is inefficient and costly.
  • the brine solution is usually used as a fluid medium for flotation cleaning.
  • the fluid medium used is difficult to handle and pollutes the environment after discharge.
  • the cleaning of the sediment and impurities of the waste plastic fragments is mainly carried out manually or mechanically.
  • one method is to use an aqueous solution of a halide to increase the density of the fluid medium to achieve flotation cleaning;
  • one method is to provide a stirring device at the bottom of the washing tank (water) Under cleaning, it is difficult to separate waste plastic debris, sand and impurities.
  • the object of the present invention is to provide a cyclone sorting and cleaning device and method for waste plastic fragments which are simple in structure, can be continuously produced, and efficiently realize sorting and cleaning of waste plastic chips. .
  • a cyclone sorting and cleaning device for waste plastic chips comprising: a conical tank, an inlet pipe, a sediment isolation net, a top feed port, a top discharge pipe and a side wall discharge pipe;
  • the inverted cone has a sand discharge port at the bottom; the sediment isolation net that allows only the sediment and impurities to pass through is located in the conical tank, the shape is wide and narrow, and the upper end is open; the inlet pipe is connected to the conical tank along the tangential direction.
  • the side wall extends into the sediment isolation net; the top feed port is located at the top of the conical tank; the top discharge pipe position At the top of the conical tank; the side wall discharge pipe is connected to the side wall of the conical tank along the tangential direction of the conical tank and extends into the sedimentation net.
  • the cyclone cleaning apparatus for waste plastic chips further includes a cylindrical outer casing; the conical can is located within the outer casing, and the top of the conical can is fixed to the rounded top of the outer casing.
  • the sediment isolation net is inverted conical; the inner wall of the conical tank is provided with a spiral groove, and the edge of the spiral groove abuts against the outer wall of the sedimentation net.
  • the spiral groove is close to the outer wall of the sediment isolation net, which slows the flow rate of the fluid medium outside the sediment isolation net, so that the sediment and impurities can be subjected to gravity along the spiral groove. It slides down to the bottom of the conical tank for easy collection and separation of sediment and impurities.
  • the tapered can includes a tapered conical portion at the lower end and a cylindrical portion at the upper end; the inlet pipe is located at the conical portion, and the side wall discharge pipe is located at the cylindrical portion.
  • the inverted cone facilitates swirling of the fluid medium and simultaneously pushing up until the waste plastic debris is pushed to the side wall of the cylindrical portion.
  • the discharge tube is discharged with the fluid medium.
  • inlet pipes There are several inlet pipes, which are arranged in parallel with each other. With this structure, the structure of the multiple inlet pipes can maximize the force of the fluid medium entering the conical tank compared with the structure of one inlet pipe, thereby enhancing the swirling effect and eliminating the "dead angle".
  • the top discharge pipe is disposed along the axial direction of the tapered can, and the lower end of the top discharge pipe extends into the cylindrical portion.
  • the inner wall of the sediment isolation net is undulating. After using this structure, the friction between the inner wall of the sediment isolation net and the waste plastic fragments is strengthened, and the sand and impurities adhering to the waste plastic fragments are cleaned up to improve the cleaning effect of the waste plastic fragments.
  • the space between the sand isolation net and the conical tank slides down along the inner wall of the conical tank by gravity, from the discharge port Discharge. ⁇
  • two kinds of waste plastic fragments of different sizes are separated by swirling; the sediment and impurities are separated by cyclone and isolation.
  • the sediment isolation net has a spiral groove between the inner wall of the conical tank and the sediment isolation net, which effectively slows the flow velocity of the fluid medium outside the sediment isolation net.
  • the inner wall of the sediment isolation net undulates and rubs against the waste plastic fragments to separate the sediment and impurities adhering to the surface of the waste plastic fragments. ⁇ After using this method, the friction between the inner wall of the sediment isolation net and the waste plastic fragments is strengthened, and the sand and impurities adhering to the waste plastic fragments are cleaned up to improve the cleaning effect of the waste plastic fragments.
  • the fluid medium After the fluid medium is discharged from the side wall discharge pipe, it enters the dewatering machine and separates from the waste plastic debris, and then enters the conical tank from the inlet pipe through the water circulation system to realize recycling. ⁇ Using this method, the amount of fluid medium is effectively saved.
  • the present invention has the following advantages: The structure is simple, the processing efficiency is effectively improved, the automation and continuity of the operation process are realized, and the sorting and cleaning of the waste plastic fragments can be simultaneously realized. DRAWINGS
  • Figure 1 is an elevational view of one embodiment of a cyclone sorting and cleaning apparatus for waste plastic chips of the present invention.
  • Figure 2 is a plan view of the cyclone sorting and cleaning device of the waste plastic chips shown in Figure 1.
  • Figure 3 is a half cross-sectional view of Figure 2.
  • 1 is a conical tank
  • 2 is an inlet pipe
  • 3 is a sediment isolation net
  • 4 is a side wall discharge pipe
  • 5 is a top discharge pipe
  • 6 is a top feed port
  • 7 is an outer casing
  • 11 is a cylinder
  • the shape portion, 12 is a tapered portion
  • 13 is a spiral groove
  • 14 is a sand discharge port.
  • the swirling sorting and cleaning device for waste plastic chips shown in Figs. 1 to 3 includes a conical tank 1, an inlet pipe 1, a sediment isolation net 3, a side wall discharge pipe 4, a top discharge pipe 5, and a top inlet Feed port 6 and outer casing 7.
  • the tapered can 1 includes a tapered tapered portion 12 located below and a cylindrical portion 11 located above.
  • the entire inner wall of 1 is provided with a spiral groove 13 for the sediment and impurities to be discharged along the bottom of the conical tank 1 to be discharged.
  • the bottom is provided with a sand discharge port 14 , which is connected to a screw hoist for continuous discharge of sediment and impurities, and ensures that the fluid medium does not flow out of the discharge port 14 .
  • the inlet pipe 2 is connected to the side wall of the tapered tank 1 and extends into the inside of the sediment separating net 3, specifically, the position corresponds to the side wall of the tapered portion 12.
  • Lifting cone The swirling effect of the fluid medium in the tank 1.
  • the sediment isolation net 3 has an inverted cone shape corresponding to the conical tank 1, and is installed in the conical tank 1 with a small gap between the inner wall of the conical tank 1.
  • the spiral groove 13 on the inner wall of the conical tank is tightly attached to the outer wall of the sediment isolation net 3, thereby slowing the flow velocity outside the sediment isolation net 3, facilitating the deposition of sediment and impurities.
  • the sediment isolation net 3 may be a warp braided net, a weft braided net, a mesh net or a net having a wavy surface. As long as the mesh size is suitable, it can block the throwing of waste plastic fragments and allow sediment and Impurities can pass.
  • the inner wall of the sediment isolation net is undulating, and the friction between the sediment isolation net and the waste plastic fragments is increased. This undulation may be formed by the texture of the sediment isolation net itself, or may be provided with a bump in the sediment isolation net. And / or embossed.
  • the warp weaving net refers to the silt segregation net surrounded by a plurality of weft-aligned net wires, and the remaining net wires are arranged in a warp (vertical) manner.
  • the weft-arranged net refers to a network of wires arranged by a plurality of warp-separated nets, and the remaining nets are arranged in a weft ( ⁇ -like) manner.
  • Grid network refers to the network formed by the intersection of network lines.
  • a net having a wavy surface means that the mesh is not flattened after being arranged, the warp is superposed on the weft or the weft is superposed on the warp, and the overlapping portion causes the surface of the net to undulate and form a wave.
  • the side wall discharge pipe 4 is connected to the side wall of the cylindrical portion 11 of the tapered tank 1, i.e., near the upper end of the tapered can 1.
  • the projection of the side wall discharge pipe 4 on the horizontal plane is located in the tangential direction of the tapered can 1 so as to be easily thrown along the tangential direction.
  • the side wall discharge pipe 4 is led out of the conical tank 1, and the outlet of the side wall discharge pipe is higher than the top of the conical tank to maintain the liquid level in the conical tank.
  • the fluid medium exits the side wall discharge tube 4, and the flowing fluid medium further promotes the discharge of waste plastic fragments having a density greater than that of the fluid medium.
  • the top discharge pipe 5 is mounted at the top of the tapered can 1 and inserted into the cylindrical portion 11 of the tapered can 1 from above.
  • the top discharge pipe 5 is disposed in the vertical direction and coincides with the axis of the tapered can 1, i.e., at the top center of the tapered can 1, facilitating the discharge of waste plastic fragments having a density smaller than that of the fluid medium.
  • the top feed port 6 is located at the top of the conical tank 1 and communicates with the interior of the sediment isolation net 3 for material input.
  • the outer casing is cylindrical, divided into a cylindrical side wall and a circular bottom plate, and the tapered can 1 is inserted into the outer casing 7 from above the outer casing 7.
  • the outer casing 7 is designed to enhance the overall appearance of the device, protect the internal structure, and facilitate the placement and installation of the device.
  • a cyclone separation cleaning method for waste plastic chips which is mixed with waste plastic fragments, sediments and impurities of different density.
  • the material is put into the conical tank from the top feeding port, and the fluid medium enters the sedimentation net from the inlet pipe along the tangential direction to form a high-speed swirling flow in the sediment isolation net; the material swirls with the fluid medium at high speed to generate centrifugal force.
  • the high-density waste plastic fragments form a large centrifugal force during the rotation process.
  • the high-density waste plastic fragments are thrown at high speed toward the inner wall of the conical tank and rise with the fluid medium, and finally
  • the side wall discharge pipe discharges the conical tank; the small-density waste plastic pieces form a centrifugal force smaller, and are gathered toward the center of the conical tank under the squeeze of the dense plastic waste pieces.
  • the sediment and impurities pass through the sedimentation net and enter the space between the sediment isolation net and the conical tank; since both sides of the spiral groove are close to the sedimentation net
  • the flow velocity outside the sedimentation net is slowed down, which facilitates the deposition of sediment and impurities.
  • the sediment and impurities slide down along the inner wall of the conical tank by gravity, and are discharged from the discharge port;
  • a fluid medium circulation system is installed between the pipe and the inlet pipe, so that the fluid medium is reused and the amount is saved.
  • the inner wall of the sediment isolation net undulates and rubs against the waste plastic fragments to separate the sediment and impurities adhering to the surface of the waste plastic fragments.
  • spiral grooves may be provided in two, three or even more.
  • the number of inlet pipes can also be set to other than four.
  • the manner of transformation here is within the scope of protection of the present invention.

Abstract

The present invention relates to a rotational-flow sorting and cleaning apparatus for waste plastic pieces. The apparatus comprises a tapered tank, a water inlet pipe, a silt separating net, a top feeding hole, a top discharging pipe, and a sidewall discharging pipe. The tapered tank is inverted taper-shaped on the whole, and a silt discharging hole is disposed on the bottom of the tapered tank. The slit separating net only used for silt and impurities to pass through is located in the tapered tank, and the silt separating net is wide on the upper part and narrow on the lower part. The water inlet pipe is connected to the sidewall of the tapered tank along a tangent direction and extends inside the silt separating net. The top feeding hole is located on the top of the tapered tank. The top discharging pipe is located on the top of the tapered tank. The sidewall discharging pipe is connected to the sidewall of the tapered tank along the tangent direction of the tapered tank and extends into the silt separating net. The present invention further relates to a rotational-flow sorting and cleaning method for waste plastic pieces. The present invention has the advantages: the structure is simple; the processing efficiency is effectively improved; the separation process is automatic and continuous; and the sorting and cleaning of the waste plastic pieces can be synchronously implemented. The apparatus and method relate to recycling and cleaning technologies of the waste plastics.

Description

废塑料碎片的旋流分选清洗装置和方法 技术领域  Swirl sorting cleaning device and method for waste plastic chips
本发明涉及废塑料的回收和清洗技术, 具体的说, 涉及一种废塑料碎片的旋流分选清 洗装置和方法。 背景技术  The present invention relates to recycling and cleaning techniques for waste plastics and, in particular, to a cyclone sorting and cleaning apparatus and method for waste plastic chips. Background technique
随着塑料制品消费量的不断增大, 废塑料也不断增多。 这些废塑料若处理不得当, 势 必会破坏环境, 破坏生态平衡, 最终威胁人类的生存。  As the consumption of plastic products continues to increase, waste plastics continue to increase. If these waste plastics are not handled properly, they will inevitably damage the environment, destroy the ecological balance, and ultimately threaten the survival of mankind.
现有的废塑料主要通过如下方式处理: 废塑料回收后, 先进行分类, 破碎成碎片, 清 洗干净, 再将碎片熔融, 制成新的塑料原料颗粒和成品, 实现再生利用。  The existing waste plastics are mainly treated as follows: After the waste plastics are recycled, they are first classified, broken into pieces, cleaned, and then the chips are melted to form new plastic raw material pellets and finished products for recycling.
现有设备中, 不存在塑料旋流分选清洗装置。  In the existing equipment, there is no plastic cyclone sorting cleaning device.
一般分选塑料都釆用浮选分选的方式, 这种方法效率低下, 成本高昂。 对密度大于水 的废塑料碎片目前通常使用卤盐溶液作为流体介质进行浮选清洗, 用毕的流体介质难以处 理, 排放后给环境带来污染。  Generally, the sorting plastics are all sorted by flotation, which is inefficient and costly. For waste plastic fragments with a density greater than water, the brine solution is usually used as a fluid medium for flotation cleaning. The fluid medium used is difficult to handle and pollutes the environment after discharge.
对废塑料碎片的泥沙和杂质的清洗处理主要通过人工或机械的方式进行。 对于密度大 于水的废塑料碎片的清洗, 一种方法是需要用卤化物的水溶液以增加流体介质的密度, 才 能实现浮选清洗; 一种方法是在洗涤槽(器)底部设置搅动装置在水下清洗, 难以分离废 塑料碎片、 泥沙和杂质。  The cleaning of the sediment and impurities of the waste plastic fragments is mainly carried out manually or mechanically. For the cleaning of waste plastic chips with a density greater than water, one method is to use an aqueous solution of a halide to increase the density of the fluid medium to achieve flotation cleaning; one method is to provide a stirring device at the bottom of the washing tank (water) Under cleaning, it is difficult to separate waste plastic debris, sand and impurities.
因此, 需要引入专门的分选清洗装置, 实现密度大于流体介质的废塑料碎片、 密度小 于流体介质的废塑料碎片、泥沙和杂质三类物质的自动分选, 同时对废塑料碎片进行清洗, 实现操作过程的自动化和连续化, 有效提高加工效率。 发明内容  Therefore, it is necessary to introduce a special sorting and cleaning device to realize automatic sorting of waste plastic fragments having a density greater than that of the fluid medium, waste plastic fragments having a lower density than the fluid medium, sediment and impurities, and at the same time, cleaning the waste plastic fragments. Automate and continuous operation process to effectively improve processing efficiency. Summary of the invention
针对现有技术中存在的技术问题, 本发明的目的是: 提供一种结构简单、 可连续化生 产、 高效实现废塑料碎片的分选和清洗的废塑料碎片的旋流分选清洗装置和方法。  In view of the technical problems existing in the prior art, the object of the present invention is to provide a cyclone sorting and cleaning device and method for waste plastic fragments which are simple in structure, can be continuously produced, and efficiently realize sorting and cleaning of waste plastic chips. .
为了达到上述目的, 本发明釆用如下技术方案:  In order to achieve the above object, the present invention uses the following technical solutions:
废塑料碎片的旋流分选清洗装置, 其特征在于: 包括: 锥形罐、 进水管、 泥沙隔离网、 顶部进料口、 顶部出料管和侧壁出料管; 锥形罐整体成倒锥形, 底部设有排沙口; 仅让泥 沙和杂质通过的泥沙隔离网位于锥形罐内, 形状上宽下窄、 上端开口; 进水管沿着切线方 向接入锥形罐的侧壁并伸入泥沙隔离网内; 顶部进料口位于锥形罐的顶部; 顶部出料管位 于锥形罐的顶部; 侧壁出料管沿着锥形罐的切线方向接锥形罐的侧壁且伸入泥沙隔离网 内。 釆用这种结构后, 实现密度大于流体介质的废塑料碎片、 密度小于流体介质的废塑料 碎片、 泥沙和杂质三类物质的自动分选, 同时对废塑料碎片进行清洗, 实现操作过程的自 动化和连续化, 有效提高加工效率。 泥沙隔离网的上端边缘与锥形罐的内壁之间留有小间 隙, 从上往下, 泥沙隔离网的外壁和锥形罐的内壁之间的间隙可逐渐增大。 A cyclone sorting and cleaning device for waste plastic chips, comprising: a conical tank, an inlet pipe, a sediment isolation net, a top feed port, a top discharge pipe and a side wall discharge pipe; The inverted cone has a sand discharge port at the bottom; the sediment isolation net that allows only the sediment and impurities to pass through is located in the conical tank, the shape is wide and narrow, and the upper end is open; the inlet pipe is connected to the conical tank along the tangential direction. The side wall extends into the sediment isolation net; the top feed port is located at the top of the conical tank; the top discharge pipe position At the top of the conical tank; the side wall discharge pipe is connected to the side wall of the conical tank along the tangential direction of the conical tank and extends into the sedimentation net. After using this structure, automatic sorting of waste plastic fragments with a density greater than that of the fluid medium, waste plastic fragments with a density lower than that of the fluid medium, sediment and impurities can be realized, and the waste plastic fragments can be cleaned to realize the operation process. Automated and continuous, effectively improving processing efficiency. A small gap is left between the upper end edge of the sediment isolation net and the inner wall of the conical tank, and the gap between the outer wall of the sediment isolation net and the inner wall of the conical tank can be gradually increased from the top to the bottom.
废塑料碎片的旋流分选清洗装置还包括圆柱形的外壳; 锥形罐位于外壳内, 锥形罐的 顶部固定于外壳的圆形的顶部。 釆用这种结构后, 外壳对锥形罐进行有效保护, 外形美观, 也便于旋流分选清洗装置的放置。  The cyclone cleaning apparatus for waste plastic chips further includes a cylindrical outer casing; the conical can is located within the outer casing, and the top of the conical can is fixed to the rounded top of the outer casing. After adopting this structure, the outer casing effectively protects the conical tank, and the appearance is beautiful, and the placement of the swirl sorting cleaning device is also facilitated.
泥沙隔离网是倒锥形的; 锥形罐的内壁设有螺旋形凹槽, 螺旋形凹槽的边缘紧贴泥沙 隔离网的外壁。 釆用这种结构后, 螺旋形凹槽紧贴泥沙隔离网的外壁, 减緩了流体介质在 泥沙隔离网外的流动速率, 以便泥沙和杂质可沿着螺旋形凹槽受重力作用下滑至锥形罐的 底部, 便于泥沙和杂质的收集和分离。  The sediment isolation net is inverted conical; the inner wall of the conical tank is provided with a spiral groove, and the edge of the spiral groove abuts against the outer wall of the sedimentation net. After using this structure, the spiral groove is close to the outer wall of the sediment isolation net, which slows the flow rate of the fluid medium outside the sediment isolation net, so that the sediment and impurities can be subjected to gravity along the spiral groove. It slides down to the bottom of the conical tank for easy collection and separation of sediment and impurities.
锥形罐包括位于下端的倒锥形的锥形部分和位于上端的圆筒形部分; 进水管位于锥形 部分, 侧壁出料管位于圆筒形部分。 釆用这种结构后, 倒锥形便于将流体介质旋流并同时 向上推挤, 直至废塑料碎片推挤至圆筒形部分的侧壁出料管随流体介质排出。  The tapered can includes a tapered conical portion at the lower end and a cylindrical portion at the upper end; the inlet pipe is located at the conical portion, and the side wall discharge pipe is located at the cylindrical portion. With this configuration, the inverted cone facilitates swirling of the fluid medium and simultaneously pushing up until the waste plastic debris is pushed to the side wall of the cylindrical portion. The discharge tube is discharged with the fluid medium.
进水管有多条, 相互平行设置。 釆用这种结构后, 釆用多条进水管的结构与一条进水 管的结构相比,可最大限度加强流体介质进入锥形罐的冲力,从而加强旋流效果,消除 "死 角"。  There are several inlet pipes, which are arranged in parallel with each other. With this structure, the structure of the multiple inlet pipes can maximize the force of the fluid medium entering the conical tank compared with the structure of one inlet pipe, thereby enhancing the swirling effect and eliminating the "dead angle".
顶部出料管沿着锥形罐的轴线方向设置, 顶部出料管的下端伸入至圆筒形部分。 釆用 这种结构后, 便于密度小于流体介质的废塑料碎片的排出。  The top discharge pipe is disposed along the axial direction of the tapered can, and the lower end of the top discharge pipe extends into the cylindrical portion. When this structure is used, the discharge of waste plastic fragments having a density smaller than that of the fluid medium is facilitated.
泥沙隔离网的内壁起伏不平。 釆用这种结构后, 加强泥沙隔离网的内壁和废塑料碎片 之间的摩擦,将紧贴在废塑料碎片上的泥沙和杂质清理出来,提升废塑料碎片的清洗效果。  The inner wall of the sediment isolation net is undulating. After using this structure, the friction between the inner wall of the sediment isolation net and the waste plastic fragments is strengthened, and the sand and impurities adhering to the waste plastic fragments are cleaned up to improve the cleaning effect of the waste plastic fragments.
使用废塑料碎片的旋流分选清洗装置的废塑料碎片的旋流分选清洗方法, 待处理的混 合有密度大小不一的废塑料碎片、 泥沙和杂质的物料从顶部进料口进入锥形罐和泥沙隔离 网内; 应用于清洗的流体介质从进水管沿着切线方向进入泥沙隔离网内, 在泥沙隔离网内 形成高速旋流; 物料随流体介质高速旋流, 产生离心力, 其中, 密度大的废塑料碎片在转 动过程中形成较大的离心力, 高速抛向泥沙隔离网的内壁且随流体介质沿锥形而上升, 从 侧壁出料管排出; 密度小的废塑料碎片形成的离心力较小, 在密度大的废塑料碎片的挤压 下向锥形罐的中心聚拢, 从而进入顶部出料管排出锥形罐; 泥沙和杂质穿过泥沙隔离网, 进入泥沙隔离网和锥形罐之间的空间, 沿着锥形罐的内壁受重力的作用而滑落, 从排沙口 排出。 釆用这种方法后, 通过旋流的方式分离大小密度的两种废塑料碎片; 通过旋流加隔 离的方式分离泥沙和杂质。 同时, 泥沙隔离网除了具有泥沙和杂质的隔离功能外, 锥形罐 的内壁与泥沙隔离网之间设有螺旋形凹槽, 有效减緩泥沙隔离网外流体介质的流动速度, 便于泥沙和杂质的沉积。 Swirl sorting and cleaning method for waste plastic chips of a cyclone sorting and cleaning device using waste plastic chips, materials to be treated mixed with waste plastic fragments, sediments and impurities of different density from the top feed inlet into the cone The shaped tank and the sediment are separated into the net; the fluid medium applied for cleaning enters the sediment isolation net from the inlet pipe along the tangential direction, forming a high-speed swirling flow in the sediment isolation net; the material swirls with the fluid medium at high speed, generating centrifugal force , wherein the dense plastic waste pieces form a large centrifugal force during the rotation process, and are thrown at high speed to the inner wall of the sediment isolation net and rise along the tapered shape of the fluid medium, and are discharged from the side wall discharge pipe; The centrifugal force generated by the debris is small, and it is gathered toward the center of the conical tank under the extrusion of the dense plastic waste pieces, so as to enter the top discharge pipe and discharge the conical tank; the sediment and impurities pass through the sedimentation net and enter the mud. The space between the sand isolation net and the conical tank slides down along the inner wall of the conical tank by gravity, from the discharge port Discharge.釆 After this method, two kinds of waste plastic fragments of different sizes are separated by swirling; the sediment and impurities are separated by cyclone and isolation. At the same time, in addition to the isolation function of sediment and impurities, the sediment isolation net has a spiral groove between the inner wall of the conical tank and the sediment isolation net, which effectively slows the flow velocity of the fluid medium outside the sediment isolation net. Facilitate the deposition of sediment and impurities.
泥沙隔离网的内壁起伏, 与废塑料碎片相互摩擦, 分离出粘附在废塑料碎片表面的泥 沙和杂质。 釆用这种方法后, 加强泥沙隔离网的内壁和废塑料碎片之间的摩擦, 将紧贴在 废塑料碎片上的泥沙和杂质清理出来, 提升废塑料碎片的清洗效果。  The inner wall of the sediment isolation net undulates and rubs against the waste plastic fragments to separate the sediment and impurities adhering to the surface of the waste plastic fragments.这种 After using this method, the friction between the inner wall of the sediment isolation net and the waste plastic fragments is strengthened, and the sand and impurities adhering to the waste plastic fragments are cleaned up to improve the cleaning effect of the waste plastic fragments.
流体介质从侧壁出料管排出后, 进入脱水机与废塑料碎片分离后, 经水循环系统从进 水管再次进入锥形罐, 实现循环利用。 釆用这种方法后, 有效节约流体介质用量。  After the fluid medium is discharged from the side wall discharge pipe, it enters the dewatering machine and separates from the waste plastic debris, and then enters the conical tank from the inlet pipe through the water circulation system to realize recycling.这种Using this method, the amount of fluid medium is effectively saved.
总的说来, 本发明具有如下优点: 结构简单, 有效提高加工效率, 实现操作过程的自 动化和连续化, 可同步实现废塑料碎片的分选和清洗。 附图说明  In general, the present invention has the following advantages: The structure is simple, the processing efficiency is effectively improved, the automation and continuity of the operation process are realized, and the sorting and cleaning of the waste plastic fragments can be simultaneously realized. DRAWINGS
图 1是本发明的废塑料碎片的旋流分选清洗装置一个实施例的立面图。  BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is an elevational view of one embodiment of a cyclone sorting and cleaning apparatus for waste plastic chips of the present invention.
图 2是图 1所示的废塑料碎片的旋流分选清洗装置的俯视图。  Figure 2 is a plan view of the cyclone sorting and cleaning device of the waste plastic chips shown in Figure 1.
图 3是图 2的半剖视图。  Figure 3 is a half cross-sectional view of Figure 2.
其中, 1为锥形罐、 2为进水管, 3为泥沙隔离网, 4为侧壁出料管, 5为顶部出料管, 6为顶部进料口, 7为外壳, 11为圆筒形部分, 12为锥形部分, 13为螺旋形凹槽, 14为 排沙口。 具体实施方式  Among them, 1 is a conical tank, 2 is an inlet pipe, 3 is a sediment isolation net, 4 is a side wall discharge pipe, 5 is a top discharge pipe, 6 is a top feed port, 7 is an outer casing, 11 is a cylinder The shape portion, 12 is a tapered portion, 13 is a spiral groove, and 14 is a sand discharge port. detailed description
下面将结合附图和具体实施方式来对本发明做进一步详细的说明。  The invention will be further described in detail below with reference to the drawings and specific embodiments.
图 1至图 3所示的废塑料碎片的旋流分选清洗装置, 包括锥形罐 1、 进水管 1、 泥沙 隔离网 3、 侧壁出料管 4、 顶部出料管 5、 顶部进料口 6和外壳 7。  The swirling sorting and cleaning device for waste plastic chips shown in Figs. 1 to 3 includes a conical tank 1, an inlet pipe 1, a sediment isolation net 3, a side wall discharge pipe 4, a top discharge pipe 5, and a top inlet Feed port 6 and outer casing 7.
锥形罐 1 包括位于下方的倒锥形的锥形部分 12和位于上方的圆筒形部分 11。 锥形罐 The tapered can 1 includes a tapered tapered portion 12 located below and a cylindrical portion 11 located above. Conical tank
1的整个内壁设有一条螺旋形凹槽 13 ,便于泥沙和杂质沿着其滑落到锥形罐 1的底部排出。 底部设有排沙口 14 , 接螺旋提升机, 进行泥沙和杂质的连续排放, 并保证流体介质不会从 排沙口 14流出。 The entire inner wall of 1 is provided with a spiral groove 13 for the sediment and impurities to be discharged along the bottom of the conical tank 1 to be discharged. The bottom is provided with a sand discharge port 14 , which is connected to a screw hoist for continuous discharge of sediment and impurities, and ensures that the fluid medium does not flow out of the discharge port 14 .
进水管 2接锥形罐 1的侧壁, 并伸入泥沙隔离网 3的内侧, 具体的说, 位置与锥形部 分 12的侧壁相应。 进水管 2有多条(本实施例为四条), 相互平行设置; 进水管 2位于锥 形罐的切线方向, 使流体介质从进水管 2进入锥形罐 1时, 可形成较大的冲力, 提升锥形 罐 1内流体介质旋流效果。 The inlet pipe 2 is connected to the side wall of the tapered tank 1 and extends into the inside of the sediment separating net 3, specifically, the position corresponds to the side wall of the tapered portion 12. There are a plurality of inlet pipes 2 (four in this embodiment) which are arranged in parallel with each other; the inlet pipe 2 is located in the tangential direction of the conical tank, so that when the fluid medium enters the conical tank 1 from the inlet pipe 2, a large impulse can be formed. Lifting cone The swirling effect of the fluid medium in the tank 1.
泥沙隔离网 3呈倒锥形, 形状与锥形罐 1相应, 安装于锥形罐 1中, 与锥形罐 1的内 壁之间留有小的间隙。 锥形罐内壁的螺旋形凹槽 13的两侧紧贴泥沙隔离网 3的外壁, 从 而减緩泥沙隔离网 3外的水流速度, 便于泥沙和杂质的沉积。 泥沙隔离网 3可以是经线编 排网、 纬线编排网、 网格网或具有波浪形表面的网, 只要满足网孔尺寸合适, 既能阻挡废 塑料碎片向外抛出, 也能允许泥沙和杂质通过即可。 泥沙隔离网的内壁起伏不平, 加大泥 沙隔离网和废塑料碎片之间的摩擦, 这种起伏不平, 可由泥沙隔离网自身的紋理形成, 也 可在泥沙隔离网内设置凸点和 /或凸紋所形成。 经线编排网, 指的是泥沙隔离网由若干条 纬线排列的网线围成框架, 其余网线均以经线 (竖向) 方式排列。 纬线编排网, 指的是泥 沙隔离网若干条经线排列的网线围成框架, 其余网线均以纬线(圏状)方式排列。 网格网, 指的是网线纵横交织形成的网。 具有波浪形表面的网, 指的是网线编排后未被压平, 经线 叠置在纬线之上或纬线叠置在经线之上, 叠置部位使得网的表面凹凸起伏, 形成波浪。  The sediment isolation net 3 has an inverted cone shape corresponding to the conical tank 1, and is installed in the conical tank 1 with a small gap between the inner wall of the conical tank 1. The spiral groove 13 on the inner wall of the conical tank is tightly attached to the outer wall of the sediment isolation net 3, thereby slowing the flow velocity outside the sediment isolation net 3, facilitating the deposition of sediment and impurities. The sediment isolation net 3 may be a warp braided net, a weft braided net, a mesh net or a net having a wavy surface. As long as the mesh size is suitable, it can block the throwing of waste plastic fragments and allow sediment and Impurities can pass. The inner wall of the sediment isolation net is undulating, and the friction between the sediment isolation net and the waste plastic fragments is increased. This undulation may be formed by the texture of the sediment isolation net itself, or may be provided with a bump in the sediment isolation net. And / or embossed. The warp weaving net refers to the silt segregation net surrounded by a plurality of weft-aligned net wires, and the remaining net wires are arranged in a warp (vertical) manner. The weft-arranged net refers to a network of wires arranged by a plurality of warp-separated nets, and the remaining nets are arranged in a weft (圏-like) manner. Grid network refers to the network formed by the intersection of network lines. A net having a wavy surface means that the mesh is not flattened after being arranged, the warp is superposed on the weft or the weft is superposed on the warp, and the overlapping portion causes the surface of the net to undulate and form a wave.
侧壁出料管 4接锥形罐 1 中圆筒形部分 11的侧壁, 即靠近锥形罐 1的上端。 侧壁出 料管 4在水平面上的投影位于锥形罐 1的切线方向, 便于其沿着切线方向抛出。 侧壁出料 管 4从锥形罐 1引出, 侧壁出料管的出口高于锥形罐的顶部, 以保持锥形罐体内的液面高 度。 流体介质从侧壁出料管 4流出, 流动的流体介质进一步推动密度大于流体介质的废塑 料碎片的排出。  The side wall discharge pipe 4 is connected to the side wall of the cylindrical portion 11 of the tapered tank 1, i.e., near the upper end of the tapered can 1. The projection of the side wall discharge pipe 4 on the horizontal plane is located in the tangential direction of the tapered can 1 so as to be easily thrown along the tangential direction. The side wall discharge pipe 4 is led out of the conical tank 1, and the outlet of the side wall discharge pipe is higher than the top of the conical tank to maintain the liquid level in the conical tank. The fluid medium exits the side wall discharge tube 4, and the flowing fluid medium further promotes the discharge of waste plastic fragments having a density greater than that of the fluid medium.
顶部出料管 5安装在锥形罐 1的顶部, 从上方插入至锥形罐 1的圆筒形部分 11。 顶部 出料管 5沿着竖直方向设置, 与锥形罐 1的轴线重合, 即位于锥形罐 1的顶部中心位置, 便于密度小于流体介质的废塑料碎片的排出。  The top discharge pipe 5 is mounted at the top of the tapered can 1 and inserted into the cylindrical portion 11 of the tapered can 1 from above. The top discharge pipe 5 is disposed in the vertical direction and coincides with the axis of the tapered can 1, i.e., at the top center of the tapered can 1, facilitating the discharge of waste plastic fragments having a density smaller than that of the fluid medium.
顶部进料口 6位于锥形罐 1的顶部,并与泥沙隔离网 3的内部相通,用于物料的投入。 外壳 Ί为圆筒形, 分为圆筒形的侧壁和圆形的底板, 锥形罐 1从外壳 7的上方装入外 壳 7中。 外壳 7的设置, 可美化设备整体的外观, 保护内部结构, 同时便于设备的放置和 安装。  The top feed port 6 is located at the top of the conical tank 1 and communicates with the interior of the sediment isolation net 3 for material input. The outer casing is cylindrical, divided into a cylindrical side wall and a circular bottom plate, and the tapered can 1 is inserted into the outer casing 7 from above the outer casing 7. The outer casing 7 is designed to enhance the overall appearance of the device, protect the internal structure, and facilitate the placement and installation of the device.
废塑料碎片的旋流分选清洗方法, 物料混合有密度大小不一的废塑料碎片、 泥沙和杂 质。物料从顶部进料口投入锥形罐内,流体介质从进水管沿着切线方向进入泥沙隔离网内, 在泥沙隔离网内形成高速旋流; 物料随流体介质高速旋流, 产生离心力, 密度大的废塑料 碎片在转动过程中形成较大的离心力, 由于有泥沙隔离网的阻挡, 密度大的废塑料碎片高 速抛向锥形罐的内壁且随流体介质循锥形而上升, 最终从侧壁出料管排出锥形罐; 密度小 的废塑料碎片形成的离心力较小, 在密度大的废塑料碎片的挤压下向锥形罐的中心聚拢, 从而进入顶部出料管排出锥形罐; 泥沙和杂质穿过泥沙隔离网, 进入泥沙隔离网和锥形罐 之间的空间; 由于螺旋形凹槽的两侧紧贴泥沙隔离网的内壁, 泥沙隔离网外的水流速度减 緩, 便于泥沙和杂质的沉积, 泥沙和杂质沿着锥形罐的内壁受重力的作用滑落, 从排沙口 排出; 在侧壁出料管和进水管之间安装流体介质循环系统, 使得流体介质重复利用, 节约 用量。 A cyclone separation cleaning method for waste plastic chips, which is mixed with waste plastic fragments, sediments and impurities of different density. The material is put into the conical tank from the top feeding port, and the fluid medium enters the sedimentation net from the inlet pipe along the tangential direction to form a high-speed swirling flow in the sediment isolation net; the material swirls with the fluid medium at high speed to generate centrifugal force. The high-density waste plastic fragments form a large centrifugal force during the rotation process. Due to the blockage of the sediment isolation net, the high-density waste plastic fragments are thrown at high speed toward the inner wall of the conical tank and rise with the fluid medium, and finally The side wall discharge pipe discharges the conical tank; the small-density waste plastic pieces form a centrifugal force smaller, and are gathered toward the center of the conical tank under the squeeze of the dense plastic waste pieces. Thereby entering the top discharge pipe to discharge the conical tank; the sediment and impurities pass through the sedimentation net and enter the space between the sediment isolation net and the conical tank; since both sides of the spiral groove are close to the sedimentation net On the inner wall, the flow velocity outside the sedimentation net is slowed down, which facilitates the deposition of sediment and impurities. The sediment and impurities slide down along the inner wall of the conical tank by gravity, and are discharged from the discharge port; A fluid medium circulation system is installed between the pipe and the inlet pipe, so that the fluid medium is reused and the amount is saved.
上述过程中, 泥沙隔离网的内壁起伏, 与废塑料碎片相互摩擦, 分离出粘附在废塑料 碎片表面的泥沙和杂质。  In the above process, the inner wall of the sediment isolation net undulates and rubs against the waste plastic fragments to separate the sediment and impurities adhering to the surface of the waste plastic fragments.
除了本实施例提及的方式外, 螺旋形凹槽可设置两条、 三条甚至更多。 进水管的数量 也可设置为四条以外的其他数量。 这边变换方式均在本发明的保护范围内。  In addition to the manners mentioned in this embodiment, the spiral grooves may be provided in two, three or even more. The number of inlet pipes can also be set to other than four. The manner of transformation here is within the scope of protection of the present invention.
上述实施例为本发明较佳的实施方式, 但本发明的实施方式并不受上述实施例的限 制, 其他的任何未背离本发明的精神实质与原理下所作的改变、 修饰、 替代、 组合、 简化, 均应为等效的置换方式, 都包含在本发明的保护范围之内。  The above embodiments are preferred embodiments of the present invention, but the embodiments of the present invention are not limited to the above embodiments, and any other changes, modifications, substitutions, combinations, and modifications may be made without departing from the spirit and scope of the invention. Simplifications, which are equivalent replacement means, are included in the scope of the present invention.

Claims

权利要求 Rights request
1. 废塑料碎片的旋流分选清洗装置, 其特征在于: 包括: 锥形罐、 进水管、 泥沙隔 离网、 顶部进料口、 顶部出料管和侧壁出料管; 所述锥形罐整体成倒锥形, 底部设有排沙 口; 仅让泥沙和杂质通过的所述泥沙隔离网位于所述锥形罐内, 形状上宽下窄、上端开口; 所述进水管沿着切线方向接入所述锥形罐的侧壁并伸入所述泥沙隔离网内; 所述顶部进料 口位于所述锥形罐的顶部; 所述顶部出料管位于所述锥形罐的顶部; 所述侧壁出料管沿着 所述锥形罐的切线方向接锥形罐的侧壁且伸入所述泥沙隔离网内。 1. A cyclone sorting and cleaning device for waste plastic chips, comprising: a conical tank, an inlet pipe, a sediment isolation net, a top feed port, a top discharge pipe and a side wall discharge pipe; The shaped can is integrally inverted, and the bottom is provided with a sand discharge port; the sediment isolation net for allowing only sediment and impurities to pass is located in the tapered can, which is wide and narrow in shape and has an open upper end; Accessing the side wall of the conical tank along a tangential direction and extending into the sediment barrier; the top feed port is located at the top of the conical tank; the top discharge tube is located at the cone a top of the shaped can; the side wall discharge pipe is connected to the side wall of the tapered can along the tangential direction of the tapered can and extends into the sediment barrier.
2. 按照权利要求 1 所述的废塑料碎片的旋流分选清洗装置, 其特征在于: 还包括圆 柱形的外壳; 所述锥形罐位于所述外壳内, 所述锥形罐的顶部固定于所述外壳的圆形的顶 部。  2. The cyclone sorting and cleaning device for waste plastic chips according to claim 1, further comprising: a cylindrical outer casing; said conical tank being located in said outer casing, said top of said conical tank being fixed On the top of the circle of the outer casing.
3. 按照权利要求 1 所述的废塑料碎片的旋流分选清洗装置, 其特征在于: 所述泥沙 隔离网是倒锥形的; 所述锥形罐的内壁设有螺旋形凹槽, 所述螺旋形凹槽的边缘紧贴所述 泥沙隔离网的外壁。  3. The cyclone separation cleaning device for waste plastic chips according to claim 1, wherein: the sediment isolation net is inverted conical; the inner wall of the conical can is provided with a spiral groove. The edge of the spiral groove abuts against the outer wall of the sediment barrier.
4. 按照权利要求 1 所述的废塑料碎片的旋流分选清洗装置, 其特征在于: 所述锥形 罐包括位于下端的倒锥形的锥形部分和位于上端的圆筒形部分; 所述进水管位于所述锥形 部分, 所述侧壁出料管位于所述圆筒形部分。  4. The cyclone sorting and cleaning device for waste plastic chips according to claim 1, wherein: said tapered can comprises a tapered portion at the lower end and a cylindrical portion at the upper end; The inlet pipe is located at the tapered portion, and the side wall discharge pipe is located at the cylindrical portion.
5. 按照权利要求 4 所述的废塑料碎片的旋流分选清洗装置, 其特征在于: 所述进水 管有多条, 相互平行设置。  The cyclone sorting and cleaning device for waste plastic chips according to claim 4, wherein: the plurality of water inlet pipes are disposed in parallel with each other.
6. 按照权利要求 4 所述的废塑料碎片的旋流分选清洗装置, 其特征在于: 所述顶部 出料管沿着所述锥形罐的轴线方向设置, 所述顶部出料管的下端伸入至所述圆筒形部分。  6. The cyclone sorting and cleaning device for waste plastic chips according to claim 4, wherein: said top discharge pipe is disposed along an axial direction of said tapered can, and said lower end of said top discharge pipe Extends into the cylindrical portion.
7. 按照权利要求 1 所述的废塑料碎片的旋流分选清洗装置, 其特征在于: 所述泥沙 隔离网的内壁起伏不平。  7. The cyclone sorting and cleaning device for waste plastic chips according to claim 1, wherein: the inner wall of the sediment isolation net is undulating.
8. 使用权利要求 1至 7 中任一项所述废塑料碎片的旋流分选清洗装置的废塑料碎片 的旋流分选清洗方法,其特征在于:待处理的物料混合有密度大于流体介质的废塑料碎片、 密度小于流体介质的废塑料碎片、 泥沙和杂质, 物料从所述旋流分选清洗装置的顶部进料 口进入锥形罐和泥沙隔离网内; 应用于清洗的流体介质从所述旋流分选清洗装置的进水管 沿着切线方向进入泥沙隔离网内, 在泥沙隔离网内形成高速旋流; 物料随流体介质高速旋 流, 产生离心力, 其中, 密度大于流体介质的废塑料碎片在转动过程中形成较大的离心力, 高速抛向泥沙隔离网的内壁且随流体介质沿锥形而上升, 从侧壁出料管排出; 密度小于流 体介质的废塑料碎片形成的离心力较小, 在密度大于流体介质的废塑料碎片的挤压下向锥 形罐的中心聚拢, 从而进入顶部出料管排出锥形罐; 泥沙和杂质穿过泥沙隔离网, 进入泥 沙隔离网和锥形罐之间的空间, 沿着锥形罐的内壁受重力的作用而滑落, 从排沙口排出。 8. A cyclone sorting and cleaning method for waste plastic chips using a spinning sorting and cleaning device for waste plastic chips according to any one of claims 1 to 7, characterized in that the material to be treated is mixed with a density greater than that of the fluid medium Waste plastic fragments, waste plastic fragments having a lower density than the fluid medium, sediment and impurities, the material entering the conical tank and the sediment isolation net from the top feed inlet of the cyclone sorting cleaning device; The medium enters the sediment isolation net from the inlet pipe of the cyclone sorting cleaning device along the tangential direction to form a high-speed swirling flow in the sediment isolation net; the material is swirled at a high speed with the fluid medium to generate centrifugal force, wherein the density is greater than The waste plastic fragments of the fluid medium form a large centrifugal force during the rotation process, and are thrown at high speed to the inner wall of the sediment isolation net and rise along the tapered shape of the fluid medium, and are discharged from the side wall discharge pipe; the density is less than the flow The waste plastic fragments of the bulk medium form less centrifugal force, and are gathered toward the center of the conical tank under the extrusion of the waste plastic fragments having a density greater than the fluid medium, thereby entering the top discharge pipe and discharging the conical tank; the sediment and impurities pass through The sediment isolation net enters the space between the sediment isolation net and the conical tank, and slides along the inner wall of the conical tank by the action of gravity, and is discharged from the discharge port.
9. 按照权利要求 8 所述的废塑料碎片的旋流分选清洗方法, 其特征在于: 所述旋流 分选清洗装置的所述泥沙隔离网的内壁起伏, 与废塑料碎片相互摩擦, 分离出粘附在废塑 料碎片表面的泥沙和杂质。  9. The method according to claim 8, wherein: the inner wall of the sediment isolation net of the cyclone separation cleaning device is undulated, and rubs against the waste plastic fragments. Sediment and impurities adhering to the surface of the waste plastic fragments are separated.
10.按照权利要求 8 所述的废塑料碎片的旋流分选清洗方法, 其特征在于: 所述流体 介质从所述旋流分选清洗装置的侧壁出料管排出后, 进入脱水机与废塑料碎片分离后, 经 水循环系统从所述旋流分选清洗装置的进水管再次进入锥形罐, 实现循环利用。  The method according to claim 8, wherein the fluid medium is discharged from the side wall discharge pipe of the cyclone sorting and cleaning device, and then enters the dewatering machine. After the waste plastic fragments are separated, they are again re-entered into the conical tank from the inlet pipe of the cyclone sorting and cleaning device through the water circulation system to realize recycling.
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