CN101712197B - Visual polymer micro-extrusion mold - Google Patents
Visual polymer micro-extrusion mold Download PDFInfo
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- CN101712197B CN101712197B CN2009103092663A CN200910309266A CN101712197B CN 101712197 B CN101712197 B CN 101712197B CN 2009103092663 A CN2009103092663 A CN 2009103092663A CN 200910309266 A CN200910309266 A CN 200910309266A CN 101712197 B CN101712197 B CN 101712197B
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- 229920000642 polymer Polymers 0.000 title claims abstract description 41
- 238000001125 extrusion Methods 0.000 title claims abstract description 40
- 230000000007 visual effect Effects 0.000 title claims abstract description 25
- 238000010438 heat treatment Methods 0.000 claims abstract description 24
- 238000000034 method Methods 0.000 claims abstract description 19
- 238000009423 ventilation Methods 0.000 claims description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 2
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- 238000012800 visualization Methods 0.000 description 10
- 238000011160 research Methods 0.000 description 8
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- 239000004433 Thermoplastic polyurethane Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/92—Measuring, controlling or regulating
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92009—Measured parameter
- B29C2948/92019—Pressure
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92009—Measured parameter
- B29C2948/92209—Temperature
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92323—Location or phase of measurement
- B29C2948/92361—Extrusion unit
- B29C2948/92409—Die; Nozzle zone
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/92514—Pressure
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92504—Controlled parameter
- B29C2948/92704—Temperature
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2948/00—Indexing scheme relating to extrusion moulding
- B29C2948/92—Measuring, controlling or regulating
- B29C2948/92819—Location or phase of control
- B29C2948/92857—Extrusion unit
- B29C2948/92904—Die; Nozzle zone
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
Description
技术领域technical field
本发明属于聚合物微挤出模具技术领域,涉及到一种观测聚合物熔体在微小流道内的流场分布和壁面滑移速度的可视化微挤出模具。The invention belongs to the technical field of polymer micro-extrusion dies, and relates to a visualized micro-extrusion die for observing the flow field distribution and wall sliding velocity of polymer melt in a micro flow channel.
背景技术Background technique
聚合物熔体在挤出模具微小流道内的流动过程一直是模具设计和聚合物流变学研究的重点问题。传统的研究方法只能通过输入和输出参量,如温度、粘度、压力等推测聚合物熔体在微小流道内的流动过程,并不能直接描述聚合物在流道中真实的流动行为,对实际微挤出模具结构设计的指导作用有限。The flow process of polymer melt in the micro-channel of extrusion die has always been a key issue in the research of die design and polymer rheology. Traditional research methods can only infer the flow process of polymer melt in micro-channels through input and output parameters, such as temperature, viscosity, pressure, etc., and cannot directly describe the real flow behavior of polymers in the channel. The guiding role of the mold structure design is limited.
微挤出模具是塑料熔体整个微挤出成型过程的关键设备。目前微挤出模具设计时,由于微尺度效应下聚合物流变理论尚不完整,无法准确地描述聚合物熔体在微挤出模具流道内的流动行为,所以使得微挤出模具的设计很大程度上依赖于“试错法”。这种方法需要不断的进行试模、修模,耗时耗力,同时设计质量也不高。据统计,试模、修模的时间占微挤出模具整个设计制造周期的30%~40%,这样造成了模具成本大幅增加,影响到了微挤出模具的进一步发展。模具可视化技术是揭开模具内熔体流动状态这一黑匣子最有效的技术手段之一。目前,模具可视化技术已经成为国内外模具领域研究的热点,主要集中在注塑模具可视化技术方面,并且取得了显著的研究进展,而对于聚合物微挤出模具可视化技术方面的研究国内外未见报道。Micro-extrusion die is the key equipment in the whole micro-extrusion molding process of plastic melt. At present, when designing micro-extrusion dies, due to the incomplete rheological theory of polymers under the micro-scale effect, it is impossible to accurately describe the flow behavior of polymer melt in the flow channel of micro-extrusion dies, so the design of micro-extrusion dies is very complicated. Much depends on "trial and error". This method requires continuous mold testing and mold repair, which is time-consuming and labor-intensive, and the design quality is not high at the same time. According to statistics, the time for mold testing and mold repairing accounts for 30% to 40% of the entire design and manufacturing cycle of micro-extrusion molds, which causes a substantial increase in mold costs and affects the further development of micro-extrusion molds. Mold visualization technology is one of the most effective technical means to uncover the black box of the melt flow state in the mold. At present, mold visualization technology has become a research hotspot in the field of molds at home and abroad, mainly focusing on injection mold visualization technology, and has achieved significant research progress, but there is no report on the research on polymer micro-extrusion mold visualization technology at home and abroad. .
发明内容Contents of the invention
本发明要解决的技术问题是提供一种可视化聚合物微挤出模具,用于直接观测聚合物熔体微挤出过程中的流场分布和壁面滑移速度,观测的结果可以完善聚合物流变学理论,直接指导聚合物微挤出模具的设计。The technical problem to be solved by the present invention is to provide a visualized polymer micro-extrusion die, which is used to directly observe the flow field distribution and wall slip velocity in the process of polymer melt micro-extrusion. The observed results can improve the polymer rheology Theories directly guide the design of polymer micro-extrusion dies.
本发明的技术方案是:Technical scheme of the present invention is:
一种可视化聚合物微挤出模具,主要由连接管、加热圈、机头体、调整螺栓、定位销、挡板、紧固螺栓、可视化口模、压力/温度传感器、芯棒、垫圈、温度传感器、通气螺栓、支撑板、分流锥和法兰组成。机头体通过连接管和法兰与挤出机出口相连,分流锥和芯棒分别固定在支撑板两侧,调整螺栓和通气螺栓通过机头体上的螺栓孔与支撑板相接触,利用垫圈、挡板和紧固螺栓将可视化口模固定在机头体上,温度传感器与加热圈固定在连接管、机头体和可视化口模的外部,压力/温度传感器安装在口模平直段的小孔内。A visualized polymer micro-extrusion die, mainly composed of connecting pipe, heating ring, machine head body, adjusting bolt, positioning pin, baffle plate, fastening bolt, visualized die, pressure/temperature sensor, mandrel, gasket, temperature It consists of sensor, vent bolt, support plate, diverter cone and flange. The head body is connected to the outlet of the extruder through connecting pipes and flanges. The splitter cone and mandrel are respectively fixed on both sides of the support plate. The adjustment bolts and ventilation bolts are in contact with the support plate through the bolt holes on the head body. , baffle and fastening bolts fix the visualization die on the head body, the temperature sensor and heating ring are fixed on the connecting pipe, the head body and the outside of the visualization die, and the pressure/temperature sensor is installed on the straight section of the die Inside the small hole.
该模具可以根据研究的需要更换不同结构参数的分流锥、芯棒和口模。The mold can be replaced with splitter cones, mandrels and dies with different structural parameters according to the needs of research.
熔融的聚合物熔体在压力的作用下通过连接管进入模具流道,在分流锥的作用下进入流道内,经过压缩段的压缩,最后由平直段挤出。安装在模具上的加热圈和温度传感器控制聚合物熔体在挤出过程中保持恒定的温度;通过调节调整螺栓改变芯棒和口模之间的同轴度与间隙,使得聚合物熔体挤出过程的流场分布更为均匀;石英玻璃材质的可视化口模用来拍摄聚合物熔体在口模内部的流动过程;安装在平直段的压力传感器同时还具有测量温度的功能,是一个压力/温度集成型传感器,具有计算机通讯接口,用于测量聚合物熔体在挤出过程中的压力和温度。The molten polymer melt enters the flow channel of the mold through the connecting pipe under the action of pressure, enters the flow channel under the action of the splitter cone, is compressed by the compression section, and finally extruded from the straight section. The heating ring and temperature sensor installed on the mold control the polymer melt to maintain a constant temperature during the extrusion process; the coaxiality and gap between the mandrel and the die are changed by adjusting the adjusting bolt, so that the polymer melt is extruded The distribution of the flow field in the exit process is more uniform; the visualization die made of quartz glass is used to photograph the flow process of the polymer melt inside the die; the pressure sensor installed in the straight section also has the function of measuring temperature, which is a Integrated pressure/temperature sensor with computer communication interface for measuring pressure and temperature of polymer melt during extrusion.
本发明的效果和益处是:通过可视化模具获得聚合物熔体在微挤出模具微小流道内的真实流动状态,观测聚合物的流场分布和壁面滑移速度,从而完善聚合物流变学研究和微挤出模具设计理论;根据研究需要更换不同结构参数的分流锥、芯棒和口模,可以研究不同的模具型腔结构参数对聚合物流场分布和壁面滑移速度的影响;通过采用固定可视化口模、调整芯棒的方法,可以有效地避免直接调整可视化口模容易破碎的弊端。本发明可以直接指导聚合物微挤出模具的设计。The effect and benefit of the present invention are: obtain the real flow state of the polymer melt in the micro flow channel of the micro-extrusion die by visualizing the die, observe the flow field distribution and wall slip velocity of the polymer, thereby perfecting the polymer rheology research and Micro-extrusion die design theory; according to the research needs to replace the splitter cone, mandrel and die with different structural parameters, the influence of different mold cavity structural parameters on the polymer flow field distribution and wall slip velocity can be studied; through the use of fixed visualization The method of adjusting the die and adjusting the mandrel can effectively avoid the disadvantages of directly adjusting the visual die that is easy to break. The invention can directly guide the design of polymer micro-extrusion dies.
附图说明Description of drawings
附图是可视化聚合物微挤出模具的结构示意图。The accompanying drawing is a structural schematic diagram of a visualized polymer micro-extrusion die.
图中:1连接管;2A加热圈;3B加热圈;4机头体;5调整螺栓;In the figure: 1 connecting pipe; 2A heating ring; 3B heating ring; 4 head body; 5 adjusting bolts;
6定位销;7C加热圈;8D加热圈;9挡板;10紧固螺栓;11E加热圈;12可视化口模;13压力/温度传感器;14芯棒;15A温度传感器;16垫圈;17B温度传感器;18通气螺栓;19支撑板;20C温度传感器;21分流锥;6 positioning pin; 7C heating ring; 8D heating ring; 9 baffle; 10 fastening bolt; 11E heating ring; 12 visual die; 13 pressure/temperature sensor; ; 18 ventilation bolts; 19 support plate; 20C temperature sensor; 21 split cone;
22D温度传感器;23法兰。22D temperature sensor; 23 flange.
具体实施方式Detailed ways
以下结合技术方案和附图详细叙述本发明的具体实施例。Specific embodiments of the present invention will be described in detail below in conjunction with technical solutions and accompanying drawings.
使用A加热圈2、B加热圈3、C加热圈7、D加热圈8、E加热圈11对模具进行加热,使模具各区域温度达到设定值。通过安装在连接管1、机头体4和可视化口模12上的A温度传感器15、B温度传感器17、C温度传感器20、D温度传感器22控制挤出过程中温度保持恒定。在挤出机螺杆的作用下,聚合物熔体由连接管1流入机头体4,经分流锥21作用进入流道,然后在芯棒14和可视化口模12的共同作用下,熔体截面形状逐渐压缩达到设计要求,并从可视化口模12出口挤出。调节调整螺栓5,使挤出过程平稳、均匀。通过安装在可视化口模12平直段部分的压力/温度传感器13测量稳态挤出时的温度与压力;同时使用高速摄像机拍摄可视化口模12中熔体的流动状态。Use A heating ring 2, B heating ring 3,
观测热塑性聚氨酯(TPU)微型介入导管挤出模具内熔体流动过程。Observation of the melt flow process in the extrusion die of thermoplastic polyurethane (TPU) micro-intervention catheter.
操作步骤:Steps:
步骤1.使用烘干箱在一定温度下烘干TPU,去除水分;Step 1. Use a drying oven to dry the TPU at a certain temperature to remove moisture;
步骤2.启动挤出机,将挤出机各段和模具各区域分阶段加热到设定温度,并保温一段时间;Step 2. Start the extruder, heat each section of the extruder and each area of the mold to the set temperature in stages, and keep it warm for a period of time;
步骤3.将烘干的TPU塑料颗粒和示踪粒子搅拌均匀后倒入料筒,设置螺杆转速,进行挤出;Step 3. Stir the dried TPU plastic particles and tracer particles evenly, then pour them into the barrel, set the screw speed, and extrude;
步骤4.根据挤出制品截面形状和壁厚均匀情况,调节调整螺栓,改变芯棒和口模之间的同轴度与间隙,使挤出过程均匀、稳定;Step 4. According to the cross-sectional shape and uniform wall thickness of the extruded product, adjust the adjusting bolt to change the coaxiality and gap between the mandrel and the die, so that the extrusion process is uniform and stable;
步骤5.将显微镜头与高速摄像机相连,调节好拍摄视场光亮强度,拍摄聚合物熔体在微小流道内的流动状态,同时压力/温度传感器记录熔体的压力和温度情况;Step 5. Connect the microscope lens to the high-speed camera, adjust the light intensity of the shooting field, and shoot the flow state of the polymer melt in the tiny flow channel, and the pressure/temperature sensor records the pressure and temperature of the melt;
步骤6.通过数据处理和分析,获得微挤出模具内聚合物熔体流场分布、流变特性和壁面滑移速度;
步骤7.设置新的挤出工艺参数,或者更换不同结构参数的分流锥、芯棒和可视化口模,重复步骤2~步骤6,获得微挤出流道结构对熔体流动过程的影响规律,指导聚合物微挤出模具的设计。
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| US6814557B1 (en) * | 1999-12-14 | 2004-11-09 | Advanced Neuromodulation Systems, Inc. | Apparatus and method of producing ultra thin wall extrusions and coatings |
| CN1982033A (en) * | 2005-12-16 | 2007-06-20 | 张民良 | Screw extruder of visual and adjusting screw, steel-jacket gap and binding length |
| CN100411854C (en) * | 2005-03-04 | 2008-08-20 | 华南理工大学 | Visualized experiment equipment for the whole process of vibrating plasticizing extrusion process of polymer materials |
-
2009
- 2009-11-04 CN CN2009103092663A patent/CN101712197B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2231175Y (en) * | 1995-05-05 | 1996-07-17 | 北京化工大学 | Visible double screw extruder |
| US6814557B1 (en) * | 1999-12-14 | 2004-11-09 | Advanced Neuromodulation Systems, Inc. | Apparatus and method of producing ultra thin wall extrusions and coatings |
| CN100411854C (en) * | 2005-03-04 | 2008-08-20 | 华南理工大学 | Visualized experiment equipment for the whole process of vibrating plasticizing extrusion process of polymer materials |
| CN1982033A (en) * | 2005-12-16 | 2007-06-20 | 张民良 | Screw extruder of visual and adjusting screw, steel-jacket gap and binding length |
Non-Patent Citations (2)
| Title |
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| JP特开2004-230874A 2004.08.19 |
| JP特开平8-178854A 1996.07.12 |
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| CN101712197A (en) | 2010-05-26 |
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