CN112265249B - Extrusion-stretching-based high polymer plasticizing transportation method, module, device and equipment - Google Patents

Extrusion-stretching-based high polymer plasticizing transportation method, module, device and equipment Download PDF

Info

Publication number
CN112265249B
CN112265249B CN202011058228.8A CN202011058228A CN112265249B CN 112265249 B CN112265249 B CN 112265249B CN 202011058228 A CN202011058228 A CN 202011058228A CN 112265249 B CN112265249 B CN 112265249B
Authority
CN
China
Prior art keywords
plasticizing
polymer
transportation
rotor
stator
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.)
Active
Application number
CN202011058228.8A
Other languages
Chinese (zh)
Other versions
CN112265249A (en
Inventor
李伟
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Foshan University
Original Assignee
Foshan University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Foshan University filed Critical Foshan University
Priority to CN202011058228.8A priority Critical patent/CN112265249B/en
Publication of CN112265249A publication Critical patent/CN112265249A/en
Application granted granted Critical
Publication of CN112265249B publication Critical patent/CN112265249B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/395Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
    • B29C48/397Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using a single screw
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/68Barrels or cylinders
    • B29C48/681Barrels or cylinders for single screws
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/76Venting, drying means; Degassing means
    • B29C48/763Vent constructions, e.g. venting means avoiding melt escape
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/50Details of extruders
    • B29C48/76Venting, drying means; Degassing means
    • B29C48/765Venting, drying means; Degassing means in the extruder apparatus
    • B29C48/766Venting, drying means; Degassing means in the extruder apparatus in screw extruders
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/78Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling
    • B29C48/80Thermal treatment of the extrusion moulding material or of preformed parts or layers, e.g. by heating or cooling at the plasticising zone, e.g. by heating cylinders
    • B29C48/83Heating or cooling the cylinders
    • B29C48/832Heating

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Abstract

本发明提供了一种基于挤压拉伸的高分子塑化输运方法、模块、装置及设备;其中,方法是指:用于输运高分子物料的输运空间容积实现依次由小到大再由大到小的周期变化;在输运空间容积由小到大变化过程中,高分子物料被强制纳入至输运空间中;在输运空间容积由大到小变化过程中,高分子物料受正应力作用被压实、塑化,之后强制排出,从而依靠输运空间容积变化实现高分子物料正位移输送和塑化输运。本发明可缩短塑化输运过程的热机械历程,降低塑化输运能耗,提高输送效率,缩小设备体积和占用空间。

Figure 202011058228

The invention provides a polymer plasticizing and transporting method, module, device and equipment based on extrusion and stretching; wherein, the method refers to: the volume of transport space used for transporting polymer materials is realized in order from small to large Then the cycle changes from large to small; in the process of changing the volume of the transportation space from small to large, the polymer materials are forced to be incorporated into the transportation space; in the process of changing the volume of the transportation space from large to small, the polymer materials are Under the action of normal stress, it is compacted and plasticized, and then forced to discharge, so as to realize the positive displacement transportation and plasticized transportation of polymer materials depending on the volume change of the transportation space. The invention can shorten the thermo-mechanical history of the plasticizing transportation process, reduce the energy consumption of the plasticizing transportation, improve the transportation efficiency, and reduce the equipment volume and occupied space.

Figure 202011058228

Description

基于挤压拉伸的高分子塑化输运方法、模块、装置及设备Polymer plasticization and transportation method, module, device and equipment based on extrusion and stretching

技术领域technical field

本发明涉及高分子材料塑化输运技术领域,更具体地说,涉及一种基于挤压拉伸的高分子塑化输运方法、模块、装置及设备。The present invention relates to the technical field of polymer material plasticization and transportation, and more particularly, to a method, module, device and equipment for polymer plasticization and transportation based on extrusion stretching.

背景技术Background technique

高分子材料成型加工过程作业能耗较高,从上世纪30年代开始,螺杆机械就已经广泛使用,如螺杆挤出机、螺杆注射机等,但无论是挤出制品加工,还是注射、压延、吹塑等制品加工,塑料原料都必须经过固体输送、熔融塑化这一基本和共性的过程,这一过程所用能量占高分子材料加工能耗的绝大部分。High energy consumption in the process of polymer material molding and processing. Since the 1930s, screw machinery has been widely used, such as screw extruder, screw injection machine, etc., but whether it is extrusion product processing, or injection, calendering, In the processing of products such as blow molding, plastic raw materials must go through the basic and common process of solid conveying, melting and plasticizing, and the energy used in this process accounts for most of the energy consumption of polymer materials processing.

在螺杆机械中物料固体输运主要是靠螺杆旋转时,螺杆对物料的摩擦拖拽作用,熔体输送靠的是粘性拖曳,物料的速度梯度与其流动和变形方向垂直,这种流动与变形主要受剪切应力支配,流动变形与剪切应力的方向一致,螺杆旋转无法推动物料的时候,螺杆可以打滑空转,不属于强制挤压输送范畴;因此可以认为目前普遍采用的螺杆机械是基于剪切流变的高分子材料螺杆塑化输运设备。这样就存在塑化输运能力强烈依赖于物料与金属料筒表面之间的摩擦力和物料内摩擦力的问题。这两类问题又与物料自身物性与金属材料、工艺过程有关联。在螺杆机械中通常采取对料筒的固体输送段开槽以增加与物料的摩擦力、增大螺杆长径比、优化螺杆结构等措施可以在一定程度上解决上述问题。但这些措施又势必造成物料塑化输运所经历的热机械历程加长、能耗增加、设备结构体积大等缺陷。In the screw machine, the solid transport of the material is mainly based on the friction and drag of the screw on the material when the screw rotates. The melt transport relies on the viscous drag. The velocity gradient of the material is perpendicular to its flow and deformation direction. This flow and deformation are mainly Subject to the shear stress, the flow deformation is consistent with the direction of the shear stress. When the screw rotation cannot push the material, the screw can slip and idle, which does not belong to the category of forced extrusion transportation; therefore, it can be considered that the commonly used screw machinery is based on shearing. Rheological polymer material screw plasticizing transport equipment. In this way, there is a problem that the plasticizing transportation capacity is strongly dependent on the friction between the material and the surface of the metal barrel and the friction within the material. These two types of problems are related to the physical properties of the material itself, metal materials and technological processes. In screw machinery, measures such as slotting the solid conveying section of the barrel to increase the friction with the material, increasing the length-diameter ratio of the screw, and optimizing the screw structure can solve the above problems to a certain extent. However, these measures are bound to cause defects such as prolonged thermomechanical history, increased energy consumption, and large equipment structure during the plasticization and transportation of materials.

后续进行的新型螺杆设计及改造,都改变不了其剪切流变的本质。为了改变这种情况,迫切需要在高分子材料加工方式上进行创新。The subsequent design and modification of the new screw will not change the nature of its shear rheology. In order to change this situation, innovation in the way of processing polymer materials is urgently needed.

发明内容SUMMARY OF THE INVENTION

为克服现有技术中的缺点与不足,本发明的目的在于提供一种基于挤压拉伸的高分子塑化输运方法、模块、装置及设备;本发明可缩短塑化输运过程的热机械历程,降低塑化输运能耗,提高输送效率,缩小设备体积和占用空间。In order to overcome the shortcomings and deficiencies in the prior art, the purpose of the present invention is to provide a polymer plasticizing and transporting method, module, device and equipment based on extrusion stretching; The mechanical process reduces the energy consumption of plasticizing transportation, improves the transportation efficiency, and reduces the size and space of the equipment.

为了达到上述目的,本发明通过下述技术方案予以实现:一种基于挤压拉伸的高分子塑化输运方法,其特征在于:用于输运高分子物料的输运空间容积实现依次由小到大再由大到小的周期变化;在输运空间容积由小到大变化过程中,高分子物料被强制纳入至输运空间中;在输运空间容积由大到小变化过程中,高分子物料受正应力作用被压实、塑化,之后强制排出,从而依靠输运空间容积变化实现高分子物料正位移输送和塑化输运。In order to achieve the above-mentioned purpose, the present invention is achieved through the following technical solutions: a method for plasticizing and transporting polymers based on extrusion and stretching, characterized in that: the volume of the transport space used for transporting the polymer material is realized in turn by Periodically change from small to large and then from large to small; in the process of changing the volume of the transportation space from small to large, the polymer materials are forced to be incorporated into the transportation space; in the process of changing the volume of the transportation space from large to small, The polymer material is compacted and plasticized by normal stress, and then forced to discharge, so as to realize the positive displacement transportation and plasticized transportation of the polymer material depending on the volume change of the transportation space.

优选地,采用多段输运空间按相位依次串联来输运高分子物料,以实现高分子物料多级增压和增速地进行塑化输运。Preferably, multi-stage transport spaces are used to transport the polymer materials in series in sequence, so as to realize the plasticized transport of the polymer materials with multi-stage pressurization and acceleration.

一种高分子塑化输运模块,其特征在于:包括至少一组输运单元;每组输运单元均包括带有定子内腔的定子、外转子和带有外齿的内转子,以及分别设置在定子两侧的挡料盘一和挡料盘二;定子内腔与外转子外侧面相匹配,以实现外转子与定子之间可转动布设;所述外转子设有带有内齿的外转子内腔;所述内转子位于外转子内腔中,且外转子与内转子之间偏心设置;外转子内腔的内齿与内转子的外齿啮合,以实现内转子带动外转子转动;内转子与外转子内腔壁之间留有空间以形成容积呈由小到大再由大到小周期变化的输运空间;所述挡料盘一或定子设有与输运空间首端连通的进料口;挡料盘二或定子设有与输运空间末端连通的出料口。A polymer plasticizing transport module is characterized in that: it includes at least one group of transport units; each group of transport units includes a stator with a stator inner cavity, an outer rotor and an inner rotor with outer teeth, and The first and second baffle plates are arranged on both sides of the stator; the inner cavity of the stator is matched with the outer surface of the outer rotor, so as to realize the rotatable arrangement between the outer rotor and the stator; the outer rotor is provided with an outer rotor with inner teeth a rotor inner cavity; the inner rotor is located in the outer rotor inner cavity, and the outer rotor and the inner rotor are eccentrically arranged; the inner teeth of the outer rotor inner cavity mesh with the outer teeth of the inner rotor, so that the inner rotor drives the outer rotor to rotate; A space is left between the inner rotor and the inner cavity wall of the outer rotor to form a transportation space whose volume changes periodically from small to large and then from large to small; the baffle plate or the stator is provided with a head end communicating with the transportation space. The feeding port is provided; the second material blocking plate or the stator is provided with a discharging port which is communicated with the end of the transport space.

本发明高分子塑化输运模块中,内转子与外转子的偏心量(e)不可调,两者具有确定的啮合关系;外转子内腔壁、内转子外表面、挡料盘一和挡料盘二围成具有确定几何形状的空间。在内转子旋转时,与内转子偏心啮合的外转子在定子内腔内圆周旋转,由于偏心距的存在致使外转子内腔壁、内转子外表面、挡料盘一和挡料盘二围成的输运空间容积由小到大再由大到小周期性变化;输运空间容积由小变大时高分子物料被逐渐纳入,输运空间容积由大变小时高分子物料在正应力起主要作用下被研磨、压实、排气。In the polymer plasticizing and transporting module of the present invention, the eccentricity (e) of the inner rotor and the outer rotor is not adjustable, and the two have a definite meshing relationship; The material tray is surrounded by a space with a certain geometric shape. When the inner rotor rotates, the outer rotor that meshes with the inner rotor eccentrically rotates on the inner circumference of the inner cavity of the stator. Due to the existence of the eccentricity, the inner cavity wall of the outer rotor, the outer surface of the inner rotor, the baffle plate 1 and the baffle plate 2 are enclosed. The volume of the transport space changes periodically from small to large and then from large to small; when the volume of the transport space changes from small to large, the polymer material is gradually incorporated, and the polymer material plays a major role in the normal stress when the volume of the transport space changes from large to small. It is ground, compacted and exhausted under the action.

输运空间容积由小到大再由大到小周期性变化时,高分子物料在流动和变形过程中通过的截面积也由小到大再由大到小周期性变化,因此高分子物料的速度梯度与其流动和变形方向一致,这种流动与变形主要受正应力支配,实现了强制挤压拉伸塑化输运过程。When the volume of the transport space changes periodically from small to large and then from large to small, the cross-sectional area of the polymer material passing through in the process of flow and deformation also changes periodically from small to large and then from large to small. The velocity gradient is consistent with the direction of its flow and deformation, which are mainly dominated by normal stress, which realizes the forced extrusion-stretch-plasticization transport process.

本发明利用正应力强制输送高分子物料,塑化输运过程中塑化能力不再依赖高分子物料与金属料筒表面之间的摩擦力和物料内摩擦力;缩短了塑化输运过程的热机械历程,致使塑化输运能耗降低,有效设备体积和占用空间;塑化输运能力对高分子物料的物理特性依赖低,高分子物料适应性高;实现逐级增压,使高分子物料塑化均匀,同时能对高分子物料产生更大的压力,加快塑化速度和提高塑化质量。The present invention utilizes normal stress to forcibly transport the polymer material, and the plasticizing ability no longer depends on the friction force between the polymer material and the surface of the metal barrel and the internal friction force of the material during the plasticization and transportation process; The thermo-mechanical process reduces the energy consumption of plasticization and transportation, and reduces the effective equipment volume and occupied space; the plasticization and transportation capacity is less dependent on the physical properties of polymer materials, and the adaptability of polymer materials is high; The molecular material is uniformly plasticized, and at the same time, it can generate more pressure on the polymer material, speed up the plasticization speed and improve the plasticization quality.

优选地,所述输运单元为两个以上;各个输运单元依次并排贴合布设;相邻输运单元之间存在相位差;前一输运单元的出料口与后一输运单元的进料口位置相对,以实现各个输运单元的输运空间依次连通;各个内转子同轴设置,并分别与驱动轴连接。本发明采用多段输运空间按相位依次串联来输运高分子物料,以实现高分子物料多级增压和增速地进行塑化输运;使高分子物料塑化更加均匀,进一步提高塑化质量。Preferably, there are more than two transport units; each transport unit is laid side by side in sequence; there is a phase difference between adjacent transport units; the discharge port of the previous transport unit is The positions of the feeding ports are opposite, so that the transport spaces of each transport unit are communicated in sequence; each inner rotor is coaxially arranged and connected to the drive shaft respectively. The invention adopts multi-stage transport spaces to transport polymer materials in series according to the phases, so as to realize the multi-stage pressurization and speed-up plasticization transportation of polymer materials; make the plasticization of the polymer materials more uniform, and further improve the plasticization. quality.

优选地,所述外转子与定子内腔壁之间设有轴承。Preferably, a bearing is provided between the outer rotor and the inner cavity wall of the stator.

一种高分子塑化挤出装置,其特征在于:包括至少一组上述高分子塑化输运模块;还包括用于放置待输运高分子物料的入料器件、定子外衬和用于与驱动装置连接的驱动轴;所述高分子材料塑化输运模块设置在定子外衬中;所述入料器件与高分子材料塑化输运模块的输运空间连通;驱动轴与内转子连接,以带动内转子转动。A polymer plasticizing extrusion device is characterized in that: it includes at least one set of the above-mentioned polymer plasticizing and transporting modules; it also includes a feeding device for placing the polymer material to be transported, a stator outer lining and a the drive shaft connected to the drive device; the polymer material plasticizing and transporting module is arranged in the outer lining of the stator; the feeding device is communicated with the transport space of the polymer material plasticizing and transporting module; the driving shaft is connected with the inner rotor , to drive the inner rotor to rotate.

优选地,还包括加热器;加热器设置在定子外衬上。加热器可产生热量,热量传递至输运空间中;高分子物料在外加热辅助作用下熔融塑化并被排出,在外加热和强制挤压热双重作用下,高分子物料在较短时间内完成塑化输运过程。Preferably, a heater is also included; the heater is arranged on the outer lining of the stator. The heater can generate heat, and the heat is transferred to the transport space; the polymer material is melted and plasticized and discharged under the auxiliary action of external heating. the transport process.

优选地,在高分子材料塑化输运模块的后侧设有螺杆挤压单元;螺杆挤压单元包括筒体和螺杆;所述筒体与高分子材料塑化输运模块连接;所述螺杆活动设置在筒体的筒腔中,并与所述驱动轴连接,以实现驱动轴带动螺杆旋转。Preferably, a screw extrusion unit is provided on the rear side of the polymer material plasticizing and transporting module; the screw extrusion unit includes a barrel and a screw; the barrel is connected to the polymer material plasticizing and transporting module; the screw The movable device is arranged in the barrel cavity of the barrel and is connected with the drive shaft, so that the drive shaft drives the screw to rotate.

一种高分子塑化加工设备,其特征在于:包括上述高分子塑化挤出装置。A polymer plasticizing processing equipment is characterized in that it comprises the above-mentioned polymer plasticizing and extruding device.

优选地,所述高分子塑化加工设备为高分子塑化注射设备;还包括柱塞注射单元、模具和集料器;所述高分子材料塑化挤出装置通过集料器与柱塞注射单元连接;柱塞注射单元与模具连接。Preferably, the polymer plasticizing processing equipment is a polymer plasticizing injection equipment; it also includes a plunger injection unit, a mold and a collector; the polymer material plasticizing extrusion device is injected through the collector and the plunger The unit is connected; the plunger injection unit is connected to the mold.

本发明采用基于强制挤压拉伸,利用正应力强制输送高分子物料,高分子物料塑化输运过程中塑化能力不再依赖物料与金属料筒表面之间的摩擦力和物料内摩擦力;与现有技术相比,本发明具有如下优点与有益效果:The present invention adopts the forced extrusion and stretching based on the use of positive stress to force the transport of polymer materials, and the plasticization capacity of the polymer materials in the process of plasticization and transportation no longer depends on the friction between the material and the surface of the metal barrel and the internal friction of the material. ; Compared with the prior art, the present invention has the following advantages and beneficial effects:

1、本发明输送过程存在正应力,缩短了塑化输运过程的热机械历程,致使塑化输运能耗降低;1. The present invention has positive stress in the conveying process, which shortens the thermomechanical history of the plasticizing and conveying process, resulting in a reduction in the energy consumption of plasticizing and conveying;

2、本发明塑化输运靠特定形状的封闭空间容积变化完成,过程连续,具有完全正位移特性,输送效率提高;2. The plasticizing transportation of the present invention is completed by the volume change of the enclosed space with a specific shape, the process is continuous, and it has a completely positive displacement characteristic, and the transportation efficiency is improved;

3、本发明塑化输运过程在很短的热机械历程内完成,塑化输运设备体积和占地小;3. The plasticizing and transporting process of the present invention is completed within a very short thermomechanical process, and the plasticizing and transporting equipment is small in volume and footprint;

4、本发明塑化输运能力对高分子物料的物理特性依赖低,高分子物料适应性高;4. The plasticizing and transporting capacity of the present invention has low dependence on the physical properties of the polymer material, and the polymer material has high adaptability;

5、本发明实现逐级增压,使熔料塑化均匀,同时能对熔料产生更大的压力,加快塑化速度和塑化质量。5. The present invention realizes step-by-step pressurization, so that the melt is plasticized evenly, and at the same time, it can generate greater pressure on the melt, so as to speed up the plasticizing speed and plasticizing quality.

附图说明Description of drawings

图1是实施例一高分子塑化输运模块的结构示意图;1 is a schematic structural diagram of a polymer plasticizing and transporting module in Example 1;

图2是实施例一高分子塑化输运模块的剖面图;2 is a cross-sectional view of a polymer plasticizing and transporting module in Example 1;

图3是实施例一高分子塑化输运模块的原理示意图;3 is a schematic diagram of the principle of a polymer plasticizing and transporting module in Example 1;

图4是实施例二高分子塑化输运模块的结构示意图;Fig. 4 is the structural representation of the polymer plasticizing and transporting module of the second embodiment;

图5是实施例三高分子塑化输运模块的结构示意图;5 is a schematic structural diagram of a polymer plasticizing and transporting module in Example 3;

图6是实施例四高分子塑化挤出装置的结构示意图;Fig. 6 is the structural representation of embodiment four polymer plasticizing extrusion device;

图7是实施例五高分子塑化挤出装置的结构示意图;Fig. 7 is the structural representation of the polymer plasticizing extrusion device of the fifth embodiment;

图8是实施例六高分子塑化注射设备的结构示意图;Fig. 8 is the structural schematic diagram of the polymer plasticizing injection equipment of Example 6;

其中,1为输运单元、11为定子、12为外转子、13为内转子、14为挡料盘一、15为挡料盘二、16为进料口、17为出料口、18为输运空间、2为入料器件、3为定子外衬、4为连接件、5为驱动轴、6为螺杆挤压单元、61为筒体、62为螺杆、7为柱塞注射单元、71为注射油缸、72为注射活塞、73为注射料筒、74为喷嘴、8为模具、9为集料器、10为加热器。Among them, 1 is the transport unit, 11 is the stator, 12 is the outer rotor, 13 is the inner rotor, 14 is the baffle plate one, 15 is the baffle plate two, 16 is the feeding port, 17 is the discharging port, and 18 is the feeding port. Transport space, 2 is the feeding device, 3 is the stator outer lining, 4 is the connecting piece, 5 is the drive shaft, 6 is the screw extrusion unit, 61 is the barrel, 62 is the screw, 7 is the plunger injection unit, 71 72 is an injection piston, 73 is an injection barrel, 74 is a nozzle, 8 is a mold, 9 is a collector, and 10 is a heater.

具体实施方式Detailed ways

下面结合附图与具体实施方式对本发明作进一步详细的描述。The present invention will be described in further detail below with reference to the accompanying drawings and specific embodiments.

实施例一Example 1

本实施例一种基于挤压拉伸的高分子塑化输运方法,用于输运高分子物料的输运空间容积实现依次由小到大再由大到小的周期变化;在输运空间容积由小到大变化过程中,高分子物料被强制纳入至输运空间中;在输运空间容积由大到小变化过程中,高分子物料受正应力作用被压实、塑化,之后强制排出,从而依靠输运空间容积变化实现高分子物料正位移输送和塑化输运。In this embodiment, a method for plasticizing and transporting polymers based on extrusion and stretching, the volume of the transport space used for transporting polymer materials is cyclically changed from small to large and then from large to small; In the process of changing the volume from small to large, the polymer material is forced into the transportation space; in the process of changing the volume of the transportation space from large to small, the polymer material is compacted and plasticized by normal stress, and then forced to Discharge, so as to realize the positive displacement transportation and plasticization transportation of polymer materials depending on the volume change of the transportation space.

为实现基于挤压拉伸的高分子塑化输运方法,本实施例提供一种高分子塑化输运模块,如图1至图3所示,包括一组输运单元1;输运单元1包括带有定子内腔的定子11、外转子12和带有外齿的内转子13,以及分别设置在定子11两侧的挡料盘一14和挡料盘二15。In order to realize the polymer plasticization and transportation method based on extrusion and stretching, this embodiment provides a polymer plasticization and transportation module, as shown in Fig. 1 to Fig. 3 , including a group of transportation units 1; the transportation unit 1 includes a stator 11 with a stator cavity, an outer rotor 12 and an inner rotor 13 with outer teeth, as well as a blocking plate 14 and a blocking plate 2 15 arranged on both sides of the stator 11 respectively.

定子内腔与外转子12外侧面相匹配,以实现外转子12与定子11之间可转动布设;外转子12与定子内腔壁之间优选设有轴承,保证外转子灵活转动。外转子12设有带有内齿的外转子内腔;内转子13位于外转子内腔中,且外转子12与内转子13之间偏心设置;外转子内腔的内齿与内转子13的外齿啮合,以实现内转子13带动外转子12转动;内转子13与外转子内腔壁之间留有空间以形成容积呈由小到大再由大到小周期变化的输运空间18;挡料盘一14设有与输运空间18首端连通的进料口16;挡料盘二15设有与输运空间18末端连通的出料口17。The inner cavity of the stator is matched with the outer surface of the outer rotor 12 to realize the rotatable arrangement between the outer rotor 12 and the stator 11; a bearing is preferably provided between the outer rotor 12 and the inner cavity wall of the stator to ensure the flexible rotation of the outer rotor. The outer rotor 12 is provided with an outer rotor inner cavity with inner teeth; the inner rotor 13 is located in the outer rotor inner cavity, and the outer rotor 12 and the inner rotor 13 are eccentrically arranged; The outer teeth are meshed, so that the inner rotor 13 drives the outer rotor 12 to rotate; a space is left between the inner rotor 13 and the inner cavity wall of the outer rotor to form a transport space 18 whose volume changes periodically from small to large and then from large to small; The first stopper plate 14 is provided with a feed port 16 which communicates with the head end of the transport space 18 ; the second stopper plate 15 is provided with a discharge port 17 which communicates with the end of the transport space 18 .

本发明高分子塑化输运模块中,内转子13与外转子12的偏心量(e)不可调,两者具有确定的啮合关系;外转子内腔壁、内转子13外表面、挡料盘一14和挡料盘二15围成具有确定几何形状的空间。在内转子13旋转时,与内转子13偏心啮合的外转子12在定子内腔内圆周旋转,由于偏心距的存在致使外转子内腔壁、内转子13外表面、挡料盘一14和挡料盘二15围成的输运空间18容积由小到大再由大到小周期性变化;输运空间18容积由小变大时高分子物料被逐渐纳入,输运空间18容积由大变小时高分子物料在正应力起主要作用下被研磨、压实、排气。如图3中,内转子和外转子逆时针转动过程中依次经过A、B、C、D区;其中A为进入腔,B为负压区、C为受挤区、D为挤出腔。In the polymer plasticization and transportation module of the present invention, the eccentricity (e) of the inner rotor 13 and the outer rotor 12 is not adjustable, and the two have a definite meshing relationship; the inner cavity wall of the outer rotor, the outer surface of the inner rotor 13, the baffle plate The first 14 and the second baffle plate 15 enclose a space with a certain geometric shape. When the inner rotor 13 rotates, the outer rotor 12 meshing with the inner rotor 13 eccentrically rotates on the inner circumference of the inner cavity of the stator. The volume of the transportation space 18 enclosed by the second tray 15 changes periodically from small to large and then from large to small; when the volume of the transportation space 18 changes from small to large, the polymer materials are gradually incorporated, and the volume of the transportation space 18 changes from large to large. The polymer material is ground, compacted and exhausted under the main effect of normal stress. As shown in Figure 3, the inner rotor and the outer rotor pass through areas A, B, C, and D in turn during counterclockwise rotation; A is the entry cavity, B is the negative pressure area, C is the squeezed area, and D is the extrusion cavity.

在内转子13与外转子12啮合后,内转子13和外转子12的啮合线相互分离时,输运空间容积由小变大,进入腔处会形成负压进而不断使熔体被吸进,被吸进的熔体在B区处的区域里处于负压状态;在内转子13逐渐移入外转子12的B区内,当内转子13和外转子12的啮合线相互嵌入时,内外齿逐渐接合,输运空间容积由大变小,流到C区处密闭空间的熔体处于挤压状态,该密闭空间的压力会不断增大,进而使塑化的熔体以高压、高速的状态从挤出腔挤出。当输运空间容积由小变大时可以通过挡料盘14上的进料口16纳入高分子物料,输运空间容积由大变小时,高分子物料在正应力的主要作用下被研磨、压实、排气、塑化,并由挡料盘15上的出料口17排出。After the inner rotor 13 meshes with the outer rotor 12, when the meshing lines of the inner rotor 13 and the outer rotor 12 are separated from each other, the volume of the transport space changes from small to large, and negative pressure will be formed at the entrance to the cavity to continuously suck the melt in. The sucked melt is in a negative pressure state in the area at the B area; the inner rotor 13 gradually moves into the B area of the outer rotor 12. When the meshing lines of the inner rotor 13 and the outer rotor 12 are embedded in each other, the inner and outer teeth gradually move. Joining, the volume of the transport space changes from large to small, and the melt flowing into the closed space at the C area is in an extruded state, and the pressure of the closed space will continue to increase, so that the plasticized melt will be Extrusion cavity extrusion. When the volume of the transportation space changes from small to large, the polymer material can be incorporated through the feed port 16 on the baffle plate 14. When the volume of the transportation space changes from large to small, the polymer material is ground and pressed under the main action of normal stress. Solid, exhaust, plasticized, and discharged from the discharge port 17 on the baffle plate 15.

输运空间18容积由小到大再由大到小周期性变化时,高分子物料在流动和变形过程中通过的截面积也由小到大再由大到小周期性变化,因此高分子物料的速度梯度与其流动和变形方向一致,这种流动与变形主要受正应力支配,实现了强制挤压拉伸塑化输运过程。When the volume of the transport space 18 changes periodically from small to large and then from large to small, the cross-sectional area of the polymer material passing through during the flow and deformation process also changes periodically from small to large and then from large to small. The velocity gradient is consistent with its flow and deformation direction. This flow and deformation are mainly dominated by normal stress, which realizes the forced extrusion, stretch, plasticization and transportation process.

本发明利用正应力强制输送高分子物料,塑化输运过程中塑化能力不再依赖高分子物料与金属料筒表面之间的摩擦力和物料内摩擦力;缩短了塑化输运过程的热机械历程,致使塑化输运能耗降低,有效设备体积和占用空间;塑化输运能力对高分子物料的物理特性依赖低,高分子物料适应性高;实现逐级增压,使高分子物料塑化均匀,同时能对高分子物料产生更大的压力,加快塑化速度和提高塑化质量。The present invention utilizes normal stress to forcibly transport the polymer material, and the plasticizing ability no longer depends on the friction force between the polymer material and the surface of the metal barrel and the internal friction force of the material during the plasticization and transportation process; The thermo-mechanical process reduces the energy consumption of plasticization and transportation, and reduces the effective equipment volume and occupied space; the plasticization and transportation capacity is less dependent on the physical properties of polymer materials, and the adaptability of polymer materials is high; The molecular material is uniformly plasticized, and at the same time, it can generate more pressure on the polymer material, speed up the plasticization speed and improve the plasticization quality.

实施例二Embodiment 2

本实施例一种高分子塑化输运模块,与实施例一的区别在于:本实施例中,进料口16不是设置在挡料盘一上,而是设置在定子11中,进料口16与输运空间18首端连通,如图4所示。实际应用中,出料口也可以不设置在挡料盘二上,而是设置在定子上,出料口与输运空间末端连通。本实施例的其余结构与实施例一相同。This embodiment is a polymer plasticizing and transporting module. The difference from the first embodiment is that: in this embodiment, the feeding port 16 is not provided on the material baffle plate 1, but is provided in the stator 11. 16 communicates with the head end of the transport space 18, as shown in FIG. 4 . In practical applications, the discharge port may not be provided on the second stopper plate, but on the stator, and the discharge port is communicated with the end of the transport space. The rest of the structure of this embodiment is the same as that of the first embodiment.

实施例三Embodiment 3

本实施例一种基于挤压拉伸的高分子塑化输运方法,与实施例一的区别在于:本实施例中,采用多段输运空间按相位依次串联来输运高分子物料;每段输运空间容积实现依次由小到大再由大到小的周期变化;在输运空间容积由小到大变化过程中,高分子物料被强制纳入至输运空间中;在输运空间容积由大到小变化过程中,高分子物料受正应力作用被压实、塑化,之后强制排出,以实现高分子物料多级增压和增速地进行塑化输运。This embodiment is a method for plasticizing and transporting polymers based on extrusion and stretching. The difference from Embodiment 1 is that: in this embodiment, multiple transport spaces are used in series to transport polymer materials in series in sequence; The volume of the transportation space can be changed periodically from small to large and then from large to small; in the process of changing the volume of the transportation space from small to large, the polymer materials are forced to be incorporated into the transportation space; the volume of the transportation space is changed from In the process of changing from large to small, the polymer material is compacted and plasticized by normal stress, and then forced to discharge, so as to realize the multi-stage pressurization and speed-up of plasticized transportation of the polymer material.

为实现所述基于挤压拉伸的高分子塑化输运方法,在实施例一所述的一种高分子塑化输运模块基础上作进一步优化。In order to realize the polymer plasticization and transportation method based on extrusion and stretching, further optimization is made on the basis of the polymer plasticization and transportation module described in the first embodiment.

如图5所示,输运单元1为两个以上;例如本实施例中采用五个输运单元,实际应用中也可以是两个、三个、四个、六个、七个,甚至更多;输运单元数量越多,塑化效果越好。各个输运单元1依次并排贴合布设;各个输运单元1之间的定子11分别安装,通过定子11上的沟槽用楔子统一固定连接。相邻输运单元1之间存在相位差,以使前一输运单元1的出料口17与后一输运单元1的进料口16位置相对,以实现各个输运单元1的输运空间18依次连通。本实施例中,相邻输运单元的内转子13相对于外转子14的偏心方向相反。各个内转子13同轴设置并与驱动轴连接。As shown in FIG. 5 , there are more than two transport units 1; for example, five transport units are used in this embodiment, but in practical applications, there may be two, three, four, six, seven, or even more The more the number of transport units, the better the plasticizing effect. The respective transport units 1 are arranged side by side in a close fit; the stators 11 between the respective transport units 1 are installed separately, and the grooves on the stator 11 are uniformly fixed and connected with wedges. There is a phase difference between adjacent transport units 1, so that the discharge port 17 of the previous transport unit 1 is opposite to the feed port 16 of the latter transport unit 1, so as to realize the transportation of each transport unit 1 The spaces 18 are sequentially connected. In this embodiment, the eccentric directions of the inner rotors 13 of adjacent transport units relative to the outer rotors 14 are opposite. Each of the inner rotors 13 is coaxially arranged and connected to the drive shaft.

本发明采用多段输运空间18按相位依次串联来输运高分子物料;上一级被挤压出去的熔体塑料又因负压作用被吸进下一级转子泵塑化单元的进入腔区,进而实现塑化后的熔融塑料在转子泵塑化单元的逐级增压、增速功能;高分子物料塑化更加均匀,进一步提高塑化质量。The present invention adopts the multi-segment transport space 18 to transport polymer materials in series in sequence; the melt plastic extruded from the previous stage is sucked into the entry cavity area of the plasticizing unit of the rotor pump of the next stage due to the action of negative pressure , and then realize the step-by-step pressurization and speed-up function of the plasticized molten plastic in the plasticizing unit of the rotor pump; the plasticization of the polymer material is more uniform, and the plasticization quality is further improved.

从最后一级转子泵塑化单元挤出来的高压、高速熔体通过一定形状的口模后,以口模形状相仿的形状快速的被挤出来,经冷却作用后成型,就得到所需要强度、几何形状的塑料制品。After the high-pressure and high-speed melt extruded from the plasticizing unit of the last stage rotor pump passes through a die of a certain shape, it is quickly extruded in a shape similar to the die shape, and is formed after cooling to obtain the required strength, Plastic products with geometric shapes.

实施例四Embodiment 4

本实施例一种高分子塑化挤出装置,如图6所示,包括实施例一至三中任一组高分子塑化输运模块;还包括用于放置待输运高分子物料的入料器件2、定子外衬3和用于与驱动装置连接的驱动轴5;高分子材料塑化输运模块设置在定子外衬3中;入料器件2与高分子材料塑化输运模块的输运空间连通;驱动轴5与内转子连接,以带动内转子转动。入料器件2可采用料斗;工作时高分子物料进入料斗中,料斗的末端设置有视窗口,便于观察高分子物料情况,在视窗口的下部,设置有插板,控制料斗的下料速度。A polymer plasticizing extrusion device in this embodiment, as shown in FIG. 6 , includes any one group of polymer plasticizing and transporting modules in Embodiments 1 to 3; and also includes an input material for placing polymer materials to be transported The device 2, the stator outer lining 3 and the drive shaft 5 for connecting with the driving device; the polymer material plasticizing and transporting module is arranged in the stator outer lining 3; the feeding device 2 and the polymer material plasticizing and transporting module are transported The transport space is connected; the drive shaft 5 is connected with the inner rotor to drive the inner rotor to rotate. The feeding device 2 can use a hopper; when the polymer material enters the hopper, the end of the hopper is provided with a viewing window, which is convenient for observing the condition of the polymer material. In the lower part of the viewing window, a plug-in plate is set to control the feeding speed of the hopper.

实施例五Embodiment 5

本实施例一种高分子塑化挤出装置,与实施例四的区别在于:如图7所示,本实施例中,在高分子材料塑化输运模块的后侧设有螺杆挤压单元6;螺杆挤压单元6包括筒体61和螺杆62;筒体61与高分子材料塑化输运模块连接;螺杆62活动设置在筒体的筒腔中,并与驱动轴5连接,以实现驱动轴5带动螺杆62旋转。This embodiment is a polymer plasticizing and extruding device, which is different from the fourth embodiment in that: as shown in FIG. 7 , in this embodiment, a screw extrusion unit is provided on the rear side of the polymer material plasticizing and transporting module 6; The screw extrusion unit 6 includes a barrel 61 and a screw 62; the barrel 61 is connected with the polymer material plasticizing and transporting module; the screw 62 is movably arranged in the barrel cavity of the barrel and is connected with the drive shaft 5 to achieve The drive shaft 5 drives the screw 62 to rotate.

驱动轴5带动输运单元1的内转子和螺杆挤压单元6的螺杆62旋转,料斗中的高分子物料被纳入输运单元1,经塑化后进入螺杆挤压单元6中进一步塑化和均化,再经连接在螺杆挤压单元6的筒体61上的模具挤出、冷却、定型得到制品。The drive shaft 5 drives the inner rotor of the conveying unit 1 and the screw 62 of the screw extruding unit 6 to rotate, and the polymer material in the hopper is brought into the conveying unit 1, and then enters the screw extruding unit 6 after being plasticized for further plasticization and processing. Homogenized, and then extruded, cooled and shaped through a die connected to the barrel 61 of the screw extrusion unit 6 to obtain a product.

本实施例中,还包括加热器10;加热器10设置在定子外衬和筒体61上,以实现定子外衬和筒体61加热,热量传递至输运空间18中,高分子物料在外加热辅助作用下熔融塑化并被排出,在外加热和强制挤压热双重作用下,高分子物料在较短时间内完成塑化输运过程。In this embodiment, a heater 10 is also included; the heater 10 is arranged on the stator outer lining and the cylinder body 61 to realize the heating of the stator outer lining and the cylinder body 61, the heat is transferred to the transport space 18, and the polymer material is heated externally Under the auxiliary action, it is melted and plasticized and discharged. Under the dual action of external heating and forced extrusion heat, the polymer material can complete the plasticization and transportation process in a relatively short time.

实施例六Embodiment 6

本实施例以高分子塑化挤出装置应用于高分子塑化注射设备为例进行说明。如图8所示,高分子塑化注射设备包括实施例四至六中任一项高分子塑化挤出装置;还包括柱塞注射单元7、模具8和集料器9;高分子材料塑化挤出装置通过集料器9与柱塞注射单元连接;柱塞注射单元与模具8连接。In this embodiment, the application of the polymer plasticizing extrusion device to the polymer plasticizing injection equipment is taken as an example for description. As shown in FIG. 8 , the polymer plasticizing injection equipment includes the polymer plasticizing extrusion device in any one of Embodiments 4 to 6; it also includes a plunger injection unit 7, a mold 8 and a collector 9; the polymer material plasticizing The extrusion device is connected with the plunger injection unit through the accumulator 9 ; the plunger injection unit is connected with the mold 8 .

柱塞注射单元7由注射油缸71、注射活塞72、注射料筒73、喷嘴74等零件组成。集料器9的进料端面与高分子塑化挤出装置上的出料端面固定连接,集料器9的出料端面与柱塞注射单元7的注射料筒73的进料端面固定连接。由高分子塑化挤出装置塑化好的熔体经过集料器9进入注射料筒73中,在熔体的压力下注射活塞72后退,当注射料筒73中储料量达到注射制品要求的计量值时高分子塑化挤出装置停止塑化,塑化计量工序结束。待完成充模、保压工序后,在制品冷却阶段高分子塑化挤出装置开始塑化,设备开始制品成型的新一个周期。The plunger injection unit 7 is composed of injection cylinder 71 , injection piston 72 , injection barrel 73 , nozzle 74 and other parts. The feed end face of the accumulator 9 is fixedly connected with the discharge end face of the polymer plasticizing extrusion device, and the discharge end face of the accumulator 9 is fixedly connected with the feed end face of the injection barrel 73 of the plunger injection unit 7 . The melt plasticized by the polymer plasticizing extrusion device enters the injection barrel 73 through the accumulator 9, and the injection piston 72 retreats under the pressure of the melt. When the storage volume in the injection barrel 73 reaches the requirements of the injection product When the metering value is reached, the polymer plasticizing extrusion device stops plasticizing, and the plasticizing metering process ends. After the filling and pressure keeping processes are completed, the polymer plasticizing extrusion device starts plasticizing in the cooling stage of the product, and the equipment starts a new cycle of product molding.

实际应用中,高分子塑化挤出装置也可应用于其它高分子塑化加工设备上。In practical applications, the polymer plasticizing extrusion device can also be applied to other polymer plasticizing processing equipment.

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-mentioned embodiments are preferred embodiments of the present invention, but the embodiments of the present invention are not limited by the above-mentioned embodiments, and any other changes, modifications, substitutions, combinations, The simplification should be equivalent replacement manners, which are all included in the protection scope of the present invention.

Claims (8)

1.一种高分子塑化输运模块,其特征在于:包括至少一组输运单元;每组输运单元均包括带有定子内腔的定子、外转子和带有外齿的内转子,以及分别设置在定子两侧的挡料盘一和挡料盘二;定子内腔与外转子外侧面相匹配,以实现外转子与定子之间可转动布设;所述外转子设有带有内齿的外转子内腔;所述内转子位于外转子内腔中,且外转子与内转子之间偏心设置;外转子内腔的内齿与内转子的外齿啮合,以实现内转子带动外转子转动;内转子与外转子内腔壁之间留有空间以形成容积呈由小到大再由大到小周期变化的输运空间;所述挡料盘一或定子设有与输运空间首端连通的进料口;挡料盘二或定子设有与输运空间末端连通的出料口。1. a polymer plasticizing transport module, it is characterized in that: comprise at least one group of transport units; each group of transport units all include stator with stator inner cavity, outer rotor and inner rotor with outer teeth, The first and second stopper plates are respectively arranged on both sides of the stator; the inner cavity of the stator is matched with the outer surface of the outer rotor, so as to realize the rotatable arrangement between the outer rotor and the stator; the outer rotor is provided with inner teeth The inner rotor is located in the inner cavity of the outer rotor, and the outer rotor and the inner rotor are eccentrically arranged; the inner teeth of the inner cavity of the outer rotor mesh with the outer teeth of the inner rotor, so that the inner rotor drives the outer rotor Rotation; space is left between the inner rotor and the inner cavity wall of the outer rotor to form a transportation space whose volume changes periodically from small to large and then from large to small; The feeding port is connected to the end; the second material blocking plate or the stator is provided with a discharging port that is communicated with the end of the transport space. 2.根据权利要求1所述的高分子塑化输运模块,其特征在于:所述输运单元为两个以上;各个输运单元依次并排贴合布设;相邻输运单元之间存在相位差;前一输运单元的出料口与后一输运单元的进料口位置相对,以实现各个输运单元的输运空间依次连通;各个内转子同轴设置,并分别与驱动轴连接。2 . The polymer plasticization and transportation module according to claim 1 , wherein the number of the transportation units is two or more; the transportation units are arranged side by side in sequence; there is a phase between adjacent transportation units. 3 . Poor; the discharge port of the previous transport unit is opposite to the feed port of the latter transport unit, so that the transport spaces of each transport unit are connected in sequence; each inner rotor is coaxially arranged and connected to the drive shaft respectively . 3.根据权利要求1所述的高分子塑化输运模块,其特征在于:所述外转子与定子内腔壁之间设有轴承。3 . The polymer plasticizing and transporting module according to claim 1 , wherein a bearing is provided between the outer rotor and the inner cavity wall of the stator. 4 . 4.一种高分子塑化挤出装置,其特征在于:包括至少一组权利要求1至3中任一项所述的高分子塑化输运模块;还包括用于放置待输运高分子物料的入料器件、定子外衬和用于与驱动装置连接的驱动轴;所述高分子材料塑化输运模块设置在定子外衬中;所述入料器件与高分子材料塑化输运模块的输运空间连通;驱动轴与内转子连接,以带动内转子转动。4. A polymer plasticizing extrusion device, characterized in that: it comprises at least one set of polymer plasticizing and transporting modules according to any one of claims 1 to 3; The material feeding device, the stator outer lining and the drive shaft for connecting with the driving device; the polymer material plasticizing and transporting module is arranged in the stator outer lining; the feeding device and the polymer material plasticizing and transporting The transport space of the module is communicated; the drive shaft is connected with the inner rotor to drive the inner rotor to rotate. 5.根据权利要求4所述的高分子塑化挤出装置,其特征在于:还包括加热器;加热器设置在定子外衬上。5 . The polymer plasticizing extrusion device according to claim 4 , further comprising a heater; the heater is arranged on the outer lining of the stator. 6 . 6.根据权利要求4所述的高分子塑化挤出装置,其特征在于:在高分子材料塑化输运模块的后侧设有螺杆挤压单元;螺杆挤压单元包括筒体和螺杆;所述筒体与高分子材料塑化输运模块连接;所述螺杆活动设置在筒体的筒腔中,并与所述驱动轴连接,以实现驱动轴带动螺杆旋转。6. The polymer plasticizing extrusion device according to claim 4, characterized in that: a screw extruding unit is provided on the rear side of the polymer material plasticizing and transporting module; the screw extruding unit comprises a barrel and a screw; The barrel is connected with the polymer material plasticizing and transporting module; the screw is movably arranged in the barrel cavity of the barrel, and is connected with the drive shaft, so that the drive shaft drives the screw to rotate. 7.一种高分子塑化加工设备,其特征在于:包括权利要求4所述的高分子塑化挤出装置。7. A polymer plasticizing processing equipment, characterized in that: comprising the polymer plasticizing extrusion device according to claim 4. 8.根据权利要求7所述的高分子塑化加工设备,其特征在于:所述高分子塑化加工设备为高分子塑化注射设备;还包括柱塞注射单元、模具和集料器;所述高分子材料塑化挤出装置通过集料器与柱塞注射单元连接;柱塞注射单元与模具连接。8 . The polymer plasticizing processing equipment according to claim 7 , wherein the polymer plasticizing processing equipment is a polymer plasticizing injection equipment; it also comprises a plunger injection unit, a mold and a collector; The polymer material plasticizing and extruding device is connected with the plunger injection unit through the accumulator; the plunger injection unit is connected with the mold.
CN202011058228.8A 2020-09-30 2020-09-30 Extrusion-stretching-based high polymer plasticizing transportation method, module, device and equipment Active CN112265249B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202011058228.8A CN112265249B (en) 2020-09-30 2020-09-30 Extrusion-stretching-based high polymer plasticizing transportation method, module, device and equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202011058228.8A CN112265249B (en) 2020-09-30 2020-09-30 Extrusion-stretching-based high polymer plasticizing transportation method, module, device and equipment

Publications (2)

Publication Number Publication Date
CN112265249A CN112265249A (en) 2021-01-26
CN112265249B true CN112265249B (en) 2022-09-13

Family

ID=74337720

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202011058228.8A Active CN112265249B (en) 2020-09-30 2020-09-30 Extrusion-stretching-based high polymer plasticizing transportation method, module, device and equipment

Country Status (1)

Country Link
CN (1) CN112265249B (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6588925B1 (en) * 1998-10-20 2003-07-08 Kaltor Limited Rotor-stator mixing apparatus especially for single screw extruder
CN101518943A (en) * 2009-03-19 2009-09-02 广东轻工职业技术学院 Method and equipment for extruding macromolecular material by differential plasticizing of double rotors
EP2505335A2 (en) * 2011-03-31 2012-10-03 Frank Reineke Extrusion device for producing a strip-shaped profile or tube made of plastic or rubber mass
CN203110301U (en) * 2012-12-20 2013-08-07 华南理工大学 Volume-stretching rheological plasticized transport equipment for macromolecular-material slant-face rollers

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6254266B1 (en) * 1998-05-22 2001-07-03 Robert A. Barr Floating ring mixer for extruder
CN100496927C (en) * 2008-01-25 2009-06-10 华南理工大学 Polymer material plasticizing and transporting method and apparatus based on draft flowing deformation
US9347266B2 (en) * 2009-11-13 2016-05-24 Schlumberger Technology Corporation Stator inserts, methods of fabricating the same, and downhole motors incorporating the same

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6588925B1 (en) * 1998-10-20 2003-07-08 Kaltor Limited Rotor-stator mixing apparatus especially for single screw extruder
CN101518943A (en) * 2009-03-19 2009-09-02 广东轻工职业技术学院 Method and equipment for extruding macromolecular material by differential plasticizing of double rotors
EP2505335A2 (en) * 2011-03-31 2012-10-03 Frank Reineke Extrusion device for producing a strip-shaped profile or tube made of plastic or rubber mass
CN203110301U (en) * 2012-12-20 2013-08-07 华南理工大学 Volume-stretching rheological plasticized transport equipment for macromolecular-material slant-face rollers

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
单螺杆泵定子和螺杆的有限元分析;杨秀萍 等;《机床与液压》;20070328;第35卷(第03期);第17、43-45页 *
聚合物叶片塑化挤出机正位移输送特性研究;杨智韬 等;《中国塑料》;20131226;第27卷(第12期);第68-72页 *

Also Published As

Publication number Publication date
CN112265249A (en) 2021-01-26

Similar Documents

Publication Publication Date Title
CN100496927C (en) Polymer material plasticizing and transporting method and apparatus based on draft flowing deformation
JP6657372B2 (en) Volume pulsation deformation plasticizing method and apparatus for biaxial or triaxial eccentric rotor
CN104002447B (en) A kind of eccentric rotor volume fluctuation deformation plasticizing transportation method and device
CN203110301U (en) Volume-stretching rheological plasticized transport equipment for macromolecular-material slant-face rollers
CN112265249B (en) Extrusion-stretching-based high polymer plasticizing transportation method, module, device and equipment
CN103182775B (en) The volume displaced tensile deformation plasticizing processing method of a kind of twin-screw and equipment
CN103057087B (en) Macromolecular material inclined-plane roller volume draft flowing deformation plasticizing transportation method and equipment
CN107627568B (en) Synchronous plasticizing metering injection molding method and equipment based on eccentric rotor
CN207207019U (en) Synchronous plasticizing metered shot former based on eccentric rotor
CN203863962U (en) Eccentric rotor volume impulse deformation plasticization transportation device
CN102126262A (en) Blade type processing equipment and processing method of plastic and plantfiber composite materials
CN202088322U (en) Blade type device for processing plastics and vegetable fiber composite materials
CN205614958U (en) Biax, triaxial eccentric rotor volume pulsation deformation plastify processingequipment
CN203141814U (en) Double-screw volume-replacing tensile-deformation plasticization processing equipment
HK1250691B (en) Biaxial or tri-axial eccentric rotor volume pulsed deformation plasticizing method and device
HK1134062B (en) A method and a device for plasticizing and transporting polymer material based on elongation rheology

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
CP03 Change of name, title or address

Address after: No.33, Guangyun Road, Nanhai District, Foshan City, Guangdong Province, 528200

Patentee after: Foshan University

Country or region after: China

Address before: No.33, Guangyun Road, Nanhai District, Foshan City, Guangdong Province, 528200

Patentee before: FOSHAN University

Country or region before: China

CP03 Change of name, title or address