CN221678002U - An extrusion processing device and its melt index control system - Google Patents
An extrusion processing device and its melt index control system Download PDFInfo
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- 238000001125 extrusion Methods 0.000 title claims abstract description 24
- 238000012545 processing Methods 0.000 title claims abstract description 24
- 239000000155 melt Substances 0.000 claims abstract description 46
- 238000001514 detection method Methods 0.000 claims abstract description 42
- 239000012768 molten material Substances 0.000 claims abstract description 34
- 239000000463 material Substances 0.000 claims description 16
- 238000010438 heat treatment Methods 0.000 claims description 12
- 238000011084 recovery Methods 0.000 claims description 5
- 238000005057 refrigeration Methods 0.000 claims description 5
- 238000002844 melting Methods 0.000 claims description 4
- 230000008018 melting Effects 0.000 claims description 4
- 238000000034 method Methods 0.000 abstract description 8
- 239000004033 plastic Substances 0.000 abstract description 7
- 229920003023 plastic Polymers 0.000 abstract description 7
- 238000001816 cooling Methods 0.000 description 9
- 238000012986 modification Methods 0.000 description 5
- 230000004048 modification Effects 0.000 description 5
- 238000012544 monitoring process Methods 0.000 description 5
- 238000005485 electric heating Methods 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 101001121408 Homo sapiens L-amino-acid oxidase Proteins 0.000 description 2
- 102100026388 L-amino-acid oxidase Human genes 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- AFCARXCZXQIEQB-UHFFFAOYSA-N N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CCNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 AFCARXCZXQIEQB-UHFFFAOYSA-N 0.000 description 1
- 101100012902 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) FIG2 gene Proteins 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
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- 238000012360 testing method Methods 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
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- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
Description
技术领域Technical Field
本实用新型涉及改性塑料在挤出加工技术领域,特别涉及一种挤出加工过程中在线控制熔融指数的系统。The utility model relates to the technical field of extrusion processing of modified plastics, in particular to a system for online controlling the melting index during the extrusion processing.
背景技术Background Art
采用失重秤和双螺杆挤出机进行共混改性是塑料行业最常用的加工手段之一。但是在共混改性过程中进行熔融指数的测试往往需要30min到45min的时间,一旦熔融指数不合格再进行调整又需要20min到30min的时间。熔融指数不合格时,需要调整喂料比例来调整熔融指数,又在很大程度上仍然依赖于相关人员的经验。中间产生的不合格品一般需要重新熔融造粒或者分批掺混,耗能高,用时久,浪费多。Using a loss-in-weight scale and a twin-screw extruder for blending and modification is one of the most commonly used processing methods in the plastics industry. However, it often takes 30 to 45 minutes to test the melt index during the blending and modification process. Once the melt index is unqualified, it takes another 20 to 30 minutes to adjust it. When the melt index is unqualified, it is necessary to adjust the feed ratio to adjust the melt index, which still depends to a large extent on the experience of relevant personnel. The unqualified products produced in the middle generally need to be re-melted and granulated or blended in batches, which consumes a lot of energy, takes a long time, and is wasteful.
目前,在线控制或者预测熔融指数的方法多集中在聚合领域,在挤出加工领域鲜有报道。因此,提供一种在挤出加工的过程中对改性塑料的熔融指数进行在线调整的控制系统。At present, the methods for online control or prediction of melt index are mostly concentrated in the field of polymerization, and are rarely reported in the field of extrusion processing. Therefore, a control system for online adjustment of the melt index of modified plastics during extrusion processing is provided.
实用新型内容Utility Model Content
本实用新型要解决的技术问题是现有塑料挤出加工过程中熔融指数调整耗费时间长的问题。The technical problem to be solved by the utility model is that it takes a long time to adjust the melting index in the existing plastic extrusion process.
针对上述技术问题,本实用新型提供如下技术方案:In view of the above technical problems, the utility model provides the following technical solutions:
一种挤出加工装置的熔融指数控制系统,包括:引流装置、输送装置、检测装置以及控制装置;所述引流装置连接于挤出机本体的引流孔上,用于接收沿挤出机引流孔流出的熔融物料;所述输送装置连接于引流装置的出口侧并将熔融物料输送至检测装置侧,所述检测装置用于检测所述熔融物料的熔融指数;所述控制装置与所述检测装置连接并根据检测装置的熔融指数控制所述挤出机的给料量。A melt index control system for an extrusion processing device comprises: a drainage device, a conveying device, a detection device and a control device; the drainage device is connected to the drainage hole of the extruder body and is used to receive the molten material flowing out along the drainage hole of the extruder; the conveying device is connected to the outlet side of the drainage device and conveys the molten material to the detection device side, and the detection device is used to detect the melt index of the molten material; the control device is connected to the detection device and controls the feed amount of the extruder according to the melt index of the detection device.
本实用新型的部分实施方式中,所述输送装置包括机壳以及位于机壳内的螺旋输送杆。In some implementation modes of the present invention, the conveying device includes a casing and a spiral conveying rod located in the casing.
本实用新型的部分实施方式中,还包括控温单元,所述控温单元包括加热模块与制冷模块,所述加热模块用于对机壳内的熔融物料进行加热,所述制冷模块用于对机壳内的熔融物料进行冷却。Some embodiments of the present invention further include a temperature control unit, which includes a heating module and a cooling module. The heating module is used to heat the molten material in the casing, and the cooling module is used to cool the molten material in the casing.
本实用新型的部分实施方式中,还包括加压装置,所述加压装置用于对机壳内的物料沿其输送方向加压。Some embodiments of the present invention further include a pressurizing device, which is used to pressurize the material in the casing along its conveying direction.
本实用新型的部分实施方式中,所述控温单元与所述加压装置位于所述输送装置后侧。In some implementation modes of the present invention, the temperature control unit and the pressurizing device are located at the rear side of the conveying device.
本实用新型的部分实施方式中,所述引流装置包括可拆卸连接于引流孔上的引流管,所述引流管上设有控制其通断的控制阀。In some embodiments of the utility model, the drainage device includes a drainage tube detachably connected to the drainage hole, and the drainage tube is provided with a control valve for controlling the on-off of the drainage tube.
本实用新型的部分实施方式中,所述控制装置还用于根据所述检测装置的熔融指数控制所述引流管上的控制阀。In some implementation modes of the utility model, the control device is also used to control the control valve on the drainage tube according to the melting index of the detection device.
本实用新型的部分实施方式中,还包括物料回收装置,所述物料回收装置位于所述机壳的下侧并所述检测装置后端,用于接收经过检测后的熔融物料。Some implementations of the present invention further include a material recovery device, which is located at the lower side of the housing and at the rear end of the detection device and is used to receive the molten material after detection.
本实用新型同时提供一种挤出加工装置,包括挤出机本体以及所述的熔融指数控制系统。The utility model also provides an extrusion processing device, comprising an extruder body and the melt index control system.
本实用新型的部分实施方式中,所述挤出机本体在接近其出料机头的侧壁上设置至少一个所述引流孔。In some implementation modes of the present invention, at least one drainage hole is provided on the side wall of the extruder body close to its discharge head.
本实用新型的技术方案相对现有技术具有如下技术效果:The technical solution of the utility model has the following technical effects compared with the prior art:
本实用新型提供的挤出加工装置的熔融指数控制系统中,通过将熔融物料从挤出机本体引出的方式,以对熔融物料实现在线监测,控制装置根据检测装置检测的熔融指数控制挤出机的给料量。该控制系统能够实现挤出机内熔融物料的熔融指数的实时监控,且同时能够实现挤出机给料量的控制,整个控制系统反应迅速,检测效率较高。In the melt index control system of the extrusion processing device provided by the utility model, the melted material is led out from the extruder body to realize online monitoring of the melted material, and the control device controls the feeding amount of the extruder according to the melt index detected by the detection device. The control system can realize real-time monitoring of the melt index of the molten material in the extruder, and at the same time can realize the control of the feeding amount of the extruder, and the whole control system responds quickly and has high detection efficiency.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
下面将通过附图详细描述本实用新型中优选实施例,将有助于理解本实用新型的目的和优点,其中:The preferred embodiments of the present invention will be described in detail below with reference to the accompanying drawings, which will help to understand the purpose and advantages of the present invention, wherein:
图1为本实用新型提供的挤出加工装置的一种具体实施方式的结构示意图;FIG1 is a schematic structural diagram of a specific embodiment of an extrusion processing device provided by the utility model;
图2为本实用新型提供的挤出加工装置中输送装置的一种具体实施方式的结构示意图。FIG. 2 is a schematic structural diagram of a specific implementation of a conveying device in an extrusion processing device provided by the utility model.
具体实施方式DETAILED DESCRIPTION
下面将结合附图对本实用新型的技术方案进行清楚、完整地描述,显然,所描述的实施例是本实用新型一部分实施例,而不是全部的实施例。基于本实用新型中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本实用新型保护的范围。The technical solution of the utility model will be described clearly and completely below in conjunction with the accompanying drawings. Obviously, the described embodiments are part of the embodiments of the utility model, not all of them. Based on the embodiments of the utility model, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the utility model.
在本实用新型的描述中,需要说明的是,术语“中心”、“上”、“下”、“左”、“右”、“竖直”、“水平”、“内”、“外”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本实用新型和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本实用新型的限制。此外,术语“第一”、“第二”、“第三”仅用于描述目的,而不能理解为指示或暗示相对重要性。In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc., indicating the orientation or positional relationship, are based on the orientation or positional relationship shown in the drawings, and are only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and therefore cannot be understood as a limitation on the present invention. In addition, the terms "first", "second", and "third" are used for descriptive purposes only, and cannot be understood as indicating or implying relative importance.
在本实用新型的描述中,需要说明的是,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或一体地连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通。对于本领域的普通技术人员而言,可以具体情况理解上述术语在本实用新型中的具体含义。In the description of the present invention, it should be noted that, unless otherwise clearly specified and limited, the terms "installed", "connected", and "connected" should be understood in a broad sense, for example, it can be a fixed connection, a detachable connection, or an integral connection; it can be a direct connection, or an indirect connection through an intermediate medium, or it can be the internal communication of two components. For ordinary technicians in this field, the specific meanings of the above terms in the present invention can be understood according to specific circumstances.
此外,下面所描述的本实用新型不同实施方式中所涉及的技术特征只要彼此之间未构成冲突就可以相互结合。In addition, the technical features involved in the different embodiments of the present invention described below can be combined with each other as long as they do not conflict with each other.
如图1所示为本实用新型提供的挤出加工装置的具体实施方式,该装置包括用户共混改性的挤出机本体10以及对挤出机本体10内熔融体进行熔融指数监测的熔融指数控制系统,所述熔融指数控制系统用于根据熔融体的熔融指数控制所述挤出机的给料量。As shown in Figure 1, a specific embodiment of the extrusion processing device provided by the utility model is shown. The device includes an extruder body 10 for user blending and modification and a melt index control system for monitoring the melt index of the melt in the extruder body 10. The melt index control system is used to control the feed amount of the extruder according to the melt index of the melt.
如图1同时示出了上述熔融指数控制系统的具体实施方式,包括:引流装置100、输送装置200、检测装置300以及控制装置400;所述引流装置100连接于挤出机本体10的引流孔上,用于接收沿挤出机引流孔流出的熔融物料;所述输送装置200连接于引流装置100的出口侧并将熔融物料输送至检测装置300侧,所述检测装置300用于检测所述熔融物料的熔融指数;所述控制装置400与所述检测装置300连接并根据检测装置300的熔融指数控制所述挤出机的给料量。As shown in FIG1 , a specific implementation of the above-mentioned melt index control system is shown, which includes: a drainage device 100, a conveying device 200, a detection device 300 and a control device 400; the drainage device 100 is connected to the drainage hole of the extruder body 10, and is used to receive the molten material flowing out along the drainage hole of the extruder; the conveying device 200 is connected to the outlet side of the drainage device 100 and conveys the molten material to the detection device 300 side, and the detection device 300 is used to detect the melt index of the molten material; the control device 400 is connected to the detection device 300 and controls the feed rate of the extruder according to the melt index of the detection device 300.
上述熔融指数控制系统通过将熔融物料从挤出机本体10引出的方式,以对熔融物料实现在线监测,其中,输送装置200用于接受挤出机本体10引出的熔融物料并输送至检测装置300侧,控制装置400根据检测装置300检测的熔融指数控制挤出机的给料量,当检测到的熔融指数超出设置阈值后,将控制信号反馈到物料原料供给装置所在的失重秤控制器中,调整失重秤的喂料量,实现挤出机给料量的控制,直至熔融指数达到设定的范围为止。该控制系统能够实现挤出机内熔融物料的熔融指数的实时监控,且同时能够实现挤出机给料量的控制,整个控制系统反应迅速,检测效率较高。The above-mentioned melt index control system realizes online monitoring of the molten material by leading the molten material from the extruder body 10, wherein the conveying device 200 is used to receive the molten material led out of the extruder body 10 and convey it to the detection device 300 side, and the control device 400 controls the feed amount of the extruder according to the melt index detected by the detection device 300. When the detected melt index exceeds the set threshold, the control signal is fed back to the loss-in-weight scale controller where the material raw material supply device is located, and the feed amount of the loss-in-weight scale is adjusted to realize the control of the feed amount of the extruder until the melt index reaches the set range. The control system can realize real-time monitoring of the melt index of the molten material in the extruder, and at the same time can realize the control of the feed amount of the extruder. The whole control system responds quickly and has high detection efficiency.
具体地,一种可选的实施方式中,如图2所示,所述输送装置200包括机壳201以及位于机壳201内的螺旋输送杆202,螺旋输送杆202具有螺旋槽,适于继续将粘度较高的熔融物料输送至后续检测装置300侧。螺旋输送杆202可采用单螺杆输送、双螺杆输送、多螺杆输送等螺杆输送方式。Specifically, in an optional embodiment, as shown in FIG2 , the conveying device 200 includes a housing 201 and a screw conveying rod 202 located in the housing 201, and the screw conveying rod 202 has a spiral groove, which is suitable for continuing to convey the molten material with higher viscosity to the subsequent detection device 300. The screw conveying rod 202 can adopt a screw conveying mode such as single screw conveying, double screw conveying, and multi-screw conveying.
具体地,为了使从挤出机本体10引出的熔融物料的状态与在挤出机本体10内的状态保持一致;所述熔融指数控制系统还包括控温单元,所述控温单元包括加热模块500与制冷模块600,所述加热模块500用于对机壳201内的熔融物料进行加热,所述加热模块500的加热方式包括但不限于电加热、油加热,例如在机壳201上缠绕电加热丝以实现电加热,或通过围绕于机壳201外侧并充满液体加热介质(例如油液等)的加热容腔实现油加热;所述制冷模块600用于对机壳201内的熔融物料进行冷却,所述制冷模块600的冷却方式包括但不限于水冷、风冷,例如通过围绕于机壳201外侧并充满冷却介质的冷却容腔实现水冷冷却;或通过连通于机壳201上的风冷管实现风冷冷却。通过将机壳201内熔融物料的温度调节为与挤出机本体10内的熔融物料基本一致,以使检测装置300的检测准确性更高。Specifically, in order to make the state of the molten material drawn out from the extruder body 10 consistent with the state in the extruder body 10; the melt index control system also includes a temperature control unit, the temperature control unit includes a heating module 500 and a refrigeration module 600, the heating module 500 is used to heat the molten material in the housing 201, and the heating method of the heating module 500 includes but is not limited to electric heating and oil heating, for example, winding an electric heating wire on the housing 201 to achieve electric heating, or through a heating chamber surrounding the outside of the housing 201 and filled with a liquid heating medium (such as oil, etc.) to achieve oil heating; the refrigeration module 600 is used to cool the molten material in the housing 201, and the cooling method of the refrigeration module 600 includes but is not limited to water cooling and air cooling, for example, through a cooling chamber surrounding the outside of the housing 201 and filled with a cooling medium to achieve water cooling; or through an air cooling pipe connected to the housing 201 to achieve air cooling. By adjusting the temperature of the molten material in the housing 201 to be substantially consistent with the molten material in the extruder body 10, the detection accuracy of the detection device 300 is higher.
具体地,一种可选的实施方式中,所述熔融指数控制系统还包括加压装置700,所述加压装置700用于对机壳201内的物料沿其输送方向加压,以实现熔融物料以一定流速进行流动。其可以使机壳201内的熔融物料的流动状态与挤出机本体10内的流体流动状态一致,以提高检测装置300的检测准确性。具体地,所述加压装置700可采用气动加压、电动加压等加压方式。Specifically, in an optional embodiment, the melt index control system further includes a pressurizing device 700, which is used to pressurize the material in the housing 201 along its conveying direction to achieve the flow of the molten material at a certain flow rate. It can make the flow state of the molten material in the housing 201 consistent with the flow state of the fluid in the extruder body 10, so as to improve the detection accuracy of the detection device 300. Specifically, the pressurizing device 700 can adopt a pressurizing method such as pneumatic pressurization and electric pressurization.
具体地,一种可选的实施方式中,所述控温单元与所述加压装置700位于所述输送装置200后侧,熔融物料被输送装置200向后输送至机壳201后侧经过控温单元与加压装置700可使进入检测装置300前侧的熔融物料与挤出机本体10内的物料状态一致,使检测装置300的检测准确性得到保证。Specifically, in an optional embodiment, the temperature control unit and the pressurizing device 700 are located on the rear side of the conveying device 200. The molten material is conveyed backward by the conveying device 200 to the rear side of the casing 201 and passes through the temperature control unit and the pressurizing device 700. The molten material entering the front side of the detection device 300 can be consistent with the material state in the extruder body 10, so that the detection accuracy of the detection device 300 is guaranteed.
具体地,一种可选的实施方式中,所述引流装置100包括可拆卸连接于引流孔上的引流管101,所述引流管101上设有控制其通断的控制阀102,通过控制阀102的开闭可控制该熔融指数控制系统的启动或停止。Specifically, in an optional embodiment, the drainage device 100 includes a drainage tube 101 detachably connected to the drainage hole, and the drainage tube 101 is provided with a control valve 102 for controlling its on and off. The start or stop of the melt index control system can be controlled by opening and closing the control valve 102.
具体地,所述控制装置400还用于根据所述检测装置300的熔融指数控制所述引流管101上的控制阀102,当检测装置300检测到物料的熔融指数在设定时间内的变化量小于预设值,此时,挤出机内物料处于平稳状态,控制所述控制阀102关闭即可;间隔设定时间后,例如1-2小时,将控制阀102打开,再次检测物料的熔融指数。Specifically, the control device 400 is also used to control the control valve 102 on the drainage tube 101 according to the melt index of the detection device 300. When the detection device 300 detects that the change in the melt index of the material within the set time is less than the preset value, at this time, the material in the extruder is in a stable state, and the control valve 102 can be controlled to be closed; after a set interval, for example 1-2 hours, the control valve 102 is opened to detect the melt index of the material again.
具体地,一种可选的实施方式中,所述控制系统还包括物料回收装置800,所述物料回收装置800连接于所述检测装置300后端,用于接收检测后的熔融物料以便后续使用。物料回收装置800包括位于机壳201的排料口下端的回收箱。Specifically, in an optional embodiment, the control system further includes a material recovery device 800, which is connected to the rear end of the detection device 300 and is used to receive the detected molten material for subsequent use. The material recovery device 800 includes a recovery box located at the lower end of the discharge port of the housing 201.
具体地,一种可选的实施方式中,所述挤出机本体10在接近其出料机头11的侧壁上设置至少一个所述引流孔,通过将引流孔设置于接近出料机头11侧,可使检测的物料与挤出机的出料侧的物料状态一致,能够显著降低塑料生产期间熔融指数的极差和方差。Specifically, in an optional embodiment, at least one drainage hole is provided on the side wall of the extruder body 10 close to its discharge head 11. By providing the drainage hole close to the discharge head 11, the state of the detected material can be consistent with the material state on the discharge side of the extruder, which can significantly reduce the range and variance of the melt index during plastic production.
显然,上述实施例仅仅是为清楚地说明所作的举例,而并非对实施方式的限定。对于所属领域的普通技术人员来说,在上述说明的基础上还可以做出其它不同形式的变化或变动。这里无需也无法对所有的实施方式予以穷举。而由此所引伸出的显而易见的变化或变动仍处于本实用新型的保护范围之中。Obviously, the above embodiments are merely examples for the purpose of clear explanation, and are not intended to limit the implementation methods. For those skilled in the art, other different forms of changes or modifications can be made based on the above description. It is not necessary and impossible to list all the implementation methods here. The obvious changes or modifications derived therefrom are still within the scope of protection of the present utility model.
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