CN111037774B - Mixing control method for preplasticizing plastic powder - Google Patents

Mixing control method for preplasticizing plastic powder Download PDF

Info

Publication number
CN111037774B
CN111037774B CN201911243114.8A CN201911243114A CN111037774B CN 111037774 B CN111037774 B CN 111037774B CN 201911243114 A CN201911243114 A CN 201911243114A CN 111037774 B CN111037774 B CN 111037774B
Authority
CN
China
Prior art keywords
preplasticizing
temperature rise
plastic powder
rise slope
mixed plastic
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
CN201911243114.8A
Other languages
Chinese (zh)
Other versions
CN111037774A (en
Inventor
冼伟发
何冠峰
黄云志
孙秀慧
李弟
邵世雄
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.)
LIANSU TECHNOLOGY DEVELOPMENT (WUHAN) CO LTD
Original Assignee
LIANSU TECHNOLOGY DEVELOPMENT (WUHAN) CO LTD
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 LIANSU TECHNOLOGY DEVELOPMENT (WUHAN) CO LTD filed Critical LIANSU TECHNOLOGY DEVELOPMENT (WUHAN) CO LTD
Priority to CN201911243114.8A priority Critical patent/CN111037774B/en
Publication of CN111037774A publication Critical patent/CN111037774A/en
Application granted granted Critical
Publication of CN111037774B publication Critical patent/CN111037774B/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
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/80Component parts, details or accessories; Auxiliary operations
    • B29B7/82Heating or cooling
    • B29B7/823Temperature control

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Abstract

The invention provides a mixing control method for preplasticizing plastic powder. A mixing control method for preplasticizing plastic powder comprises the following steps: s1, heating mixed plastic powder by a high-speed mixer; s2, monitoring the actual temperature rise slope d of the mixed plastic powder before entering a preplasticizing temperature rangexThe difference value with the temperature rise slope threshold value d' is obtained, and when the difference value meets the preset value, the step S3 is carried out; s3, continuously heating the mixed plastic powder to a preplasticizing temperature interval by the high-speed mixer, setting the duration of the preplasticizing temperature interval, and monitoring the actual preplasticizing temperature rise slope d of the mixed plastic powderiRegulating and controlling the operation frequency f' of the shearing tool bit of the high-speed mixer to ensure that the actual plasticizing temperature rise slope d in the preplasticizing temperature intervaliThe temperature rise slope allowable value d is the same as the temperature rise slope allowable value d; and S4, sending the mixed plastic powder subjected to preplasticizing into a cold mixing cylinder for rapid cooling. The invention fully ensures the heat exchange in the mixed plastic powder, thereby fully preplasticizing the mixed plastic powder and improving the performance of plastic products.

Description

Mixing control method for preplasticizing plastic powder
Technical Field
The invention relates to the technical field of powder preplasticizing, in particular to a mixing control method for preplasticizing plastic powder.
Background
The existing plastic powder mixing equipment does not pay much attention to the pre-plasticizing process of mixed plastic powder, the mixed plastic powder is qualified as long as the mixing time is enough, if the material and the equipment are unstable, the temperature of the mixed plastic powder is too low or the pre-plasticizing time is insufficient, so that the pre-plasticizing of the mixed plastic powder cannot be well completed, and in the process of conveying the material to an extrusion or injection molding process, the components generated by the uniformly mixed material are layered and the like, so that the performance of a plastic product is seriously influenced. If the temperature rise of the mixed materials is too fast, the extrusion or injection molding quality of the product can be seriously influenced due to excessive consumption or denaturation of the stabilizer and the like.
Disclosure of Invention
The invention aims to overcome the defect that the performance of a plastic product is influenced because the temperature rise control is not carried out in the prior plastic powder preplasticizing process, and provides a mixing control method for preplasticizing plastic powder. The invention controls the operation frequency of the shearing cutter head of the high-speed mixer through the temperature rise condition of the plastic powder, and fully ensures the heat exchange in the mixed plastic powder, thereby fully preplasticizing the mixed plastic powder and improving the performance of plastic products.
In order to solve the technical problems, the invention adopts the technical scheme that: a mixing control method for preplasticizing plastic powder comprises the following steps:
s1, heating mixed plastic powder by a high-speed mixer;
s2, monitoring the actual temperature rise slope d of the mixed plastic powder before entering a preplasticizing temperature rangexIf the difference value is larger than or equal to the preset value, stopping the preplasticizing process, and if the difference value is smaller than the preset value, entering step S3;
s3, continuously heating the mixed plastic powder to a preplasticizing temperature interval by the high-speed mixer, setting the duration of the preplasticizing temperature interval, and monitoring the actual preplasticizing temperature rise slope d of the mixed plastic powderiRegulating and controlling the operation frequency f' of the shearing tool bit of the high-speed mixer to ensure that the actual plasticizing temperature rise slope d in the preplasticizing temperature intervaliThe temperature rise slope allowable value d is the same as the temperature rise slope allowable value d;
and S4, sending the mixed plastic powder subjected to preplasticizing into a cold mixing cylinder for rapid cooling.
Further, in step S2, the actual temperature rise slope dxThe difference with the temperature rise slope threshold value d 'is less than 0.1d', and the step S3 is executed, namely: | dx-d'|<0.1d'。
Further, in step S3, the preplasticizing temperature range is [ T1,T2]Keeping the duration of the preplasticizing temperature interval as t, the temperature rise slope allowable value as d, and calculating the formula of d: d ═ T2-T1|÷t。
Further, in step S3, the period time of the mixed plastic powder is monitored as t1The mixed plastic powder is monitored for i monitoring periods t1Has a temperature change interval of [ Ti,Ti+1]Actual preplasticizing temperature rise slope diThe calculation formula of (2): di=|Ti-Ti+1|÷t1
Further, in step S3, when the actual plasticizing temperature rise slope diWhen the temperature rise slope allowable value d is larger than the temperature rise slope allowable value d, the operation frequency f' of the shearing tool bit is reduced; when the actual plasticizing temperature rises to a slope diAnd when the temperature rise slope allowable value d is smaller than the temperature rise slope allowable value d, increasing the operation frequency f' of the shearing tool head.
Further, in step S3, after the operation frequency f' of the cutting head is adjusted each time, the monitoring period t is waited for1Then comparing the actual plasticizing temperature rise slope diAnd the allowed value d of the temperature rise slope1And (4) until the mixed plastic powder is subjected to preplasticizing.
Compared with the prior art, the invention has the beneficial effects that:
the method can calculate the temperature rise slope of the mixed plastic powder during the pre-plasticizing period, and control the temperature rise process of the mixed plastic powder during the pre-plasticizing period; according to the actual plasticizing temperature rise slope diCompared with the temperature rise slope allowable value d, the operation frequency f' of the shearing tool bit is changed, so that the heat exchange in the mixed plastic powder can be ensured, the mixed plastic powder is fully pre-plasticized, and the performance of a plastic product is improved.
Drawings
FIG. 1 is a flow chart of a mixing control method for preplasticizing plastic powder according to the present invention.
FIG. 2 shows the detailed steps of step 3 in FIG. 1.
Detailed Description
The present invention will be further described with reference to the following embodiments. Wherein the showings are for the purpose of illustration only and are shown by way of illustration only and not in actual form, and are not to be construed as limiting the present patent; to better illustrate the embodiments of the present invention, some parts of the drawings may be omitted, enlarged or reduced, and do not represent the size of an actual product; it will be understood by those skilled in the art that certain well-known structures in the drawings and descriptions thereof may be omitted.
Example 1
Fig. 1 to 2 show an embodiment of a mixing control method for preplasticizing plastic powder according to the present invention. A mixing control method for preplasticizing plastic powder comprises the following steps:
s1, heating mixed plastic powder by a high-speed mixer;
s2, monitoring the actual temperature rise slope d of the mixed plastic powder before entering a preplasticizing temperature rangexIf the difference value is larger than or equal to the preset value, stopping the preplasticizing process, and if the difference value is smaller than the preset value, entering step S3;
s3, continuously heating the mixed plastic powder to a preplasticizing temperature interval by the high-speed mixer, setting the duration of the preplasticizing temperature interval, and monitoring the actual preplasticizing temperature rise slope d of the mixed plastic powderiRegulating and controlling the operation frequency f' of the shearing tool bit of the high-speed mixer to ensure that the actual plasticizing temperature rise slope d in the preplasticizing temperature intervaliThe temperature rise slope allowable value d is the same as the temperature rise slope allowable value d;
and S4, sending the mixed plastic powder subjected to preplasticizing into a cold mixing cylinder for rapid cooling.
In step S2, the actual temperature rise ramp dxThe difference with the temperature rise slope threshold value d 'is less than 0.1d', and the step S3 is executed, namely: | dx-d'|<0.1d'。
In step S3, the preplasticizing temperature range is [ T1,T2]Keeping the duration of the preplasticizing temperature interval as t, the temperature rise slope allowable value as d, and calculating the formula of d: d ═ T2-T1|÷t。
In step S3, the mixed plastic powder is monitored for a period of time t1The mixed plastic powder is monitored for i monitoring periods t1Has a temperature change interval of [ Ti,Ti+1]Actual preplasticizing temperature rise slope diThe calculation formula of (2): di=|Ti-Ti+1|÷t1
In step S3, when the actual plasticizing temperature rise slope diWhen the temperature rise slope allowable value d is larger than the temperature rise slope allowable value d, the operation frequency f' of the shearing tool bit is reduced; when the actual plasticizing temperature rises to a slope diAnd when the temperature rise slope allowable value d is smaller than the temperature rise slope allowable value d, increasing the operation frequency f' of the shearing tool head.
In step S3, each time the operation frequency f' of the cutter head is adjusted, the period time t of the monitoring period is waited for1Then comparing the actual plasticizing temperature rise slope diAnd the temperature rise slope allowable value d until the mixed plastic powder is completely pre-plasticized.
The working principle of the embodiment is as follows: in the present embodiment, the actual plasticizing temperature rise slope d is comparediObtaining the temperature rise condition of the mixed plastic powder according to the temperature rise slope allowable value d, and if the temperature rise slope d is actually plasticizediIf the temperature rise slope allowable value d is larger than the temperature rise slope allowable value d, the temperature rise of the mixed plastic powder is too fast, and the operation frequency f' of the shearing cutter head needs to be reduced, so that the temperature rise of the mixed plastic powder is slowed down; if the actual plasticizing temperature rise slope diThe temperature rise slope allowable value d is smaller than, the operation frequency f' of the shearing tool bit needs to be increased, so that the temperature rise of the mixed plastic powder is accelerated; therefore, the operation frequency f' of the shearing cutter head is controlled to ensure that the temperature rise process of the mixed plastic powder conforms to the expected process and the heat exchange inside the mixed plastic powder is fully ensured, so that the mixed plastic powder is fully pre-plasticized, and the performance of a plastic product is improved.
It should be understood that the above-described embodiments of the present invention are merely examples for clearly illustrating the present invention, and are not intended to limit the embodiments of the present invention. Other variations and modifications will be apparent to persons skilled in the art in light of the above description. And are neither required nor exhaustive of all embodiments. Any modification, equivalent replacement, and improvement made within the spirit and principle of the present invention should be included in the protection scope of the claims of the present invention.

Claims (6)

1. A mixing control method for preplasticizing plastic powder is characterized in that: the method comprises the following steps:
s1, heating mixed plastic powder by a high-speed mixer;
s2, monitoring the actual temperature rise slope d of the mixed plastic powder before entering a preplasticizing temperature rangexIf the difference value is larger than or equal to the preset value, stopping the preplasticizing process, and if the difference value is smaller than the preset value, entering step S3;
s3, continuously heating the mixed plastic powder to a preplasticizing temperature interval by the high-speed mixer, setting the duration of the preplasticizing temperature interval, and monitoring the actual preplasticizing temperature rise slope d of the mixed plastic powderiRegulating and controlling the operation frequency f' of the shearing tool bit of the high-speed mixer to ensure that the actual plasticizing temperature rise slope d in the preplasticizing temperature intervaliAnd the allowed value d of the temperature rise slope1The same;
and S4, sending the mixed plastic powder subjected to preplasticizing into a cold mixing cylinder for rapid cooling.
2. The mixing control method for preplasticizing plastic powders according to claim 1, characterized in that: in step S2, the actual temperature rise ramp dxThe difference with the temperature rise slope threshold value d 'is less than 0.1d', and the step S3 is executed, namely: | dx-d'|<0.1d'。
3. The mixing control method for preplasticizing plastic powders according to claim 1, characterized in that: in step S3, the preplasticizing temperature range is [ T1,T2]Keeping the duration of the preplasticizing temperature interval as t, the temperature rise slope allowable value as d, and calculating the formula of d: d ═ T2-T1|÷t。
4. The mixing control method for preplasticizing plastic powders according to claim 1, characterized in that: in step S3, the mixed plastic powder is monitored for a period of time t1The mixed plastic powder is monitored for i monitoring periods t1Has a temperature change interval of [ Ti,Ti+1]Actual preplasticizing temperature rise slope diThe calculation formula of (2): di=|Ti-Ti+1|÷t1
5. The mixing control method for preplasticizing plastic powders according to claim 4, characterized in that: in step S3, when the actual plasticizing temperature rise slope diWhen the temperature rise slope allowable value d is larger than the temperature rise slope allowable value d, the operation frequency f' of the shearing tool bit is reduced; when the actual plasticizing temperature rises to a slope diAnd when the temperature rise slope allowable value d is smaller than the temperature rise slope allowable value d, increasing the operation frequency f' of the shearing tool head.
6. The mixing control method for preplasticizing plastic powders according to claim 5, characterized in that: in step S3, each time the operation frequency f' of the cutter head is adjusted, the period time t of the monitoring period is waited for1Then comparing the actual plasticizing temperature rise slope diAnd the temperature rise slope allowable value d until the mixed plastic powder is completely pre-plasticized.
CN201911243114.8A 2019-12-06 2019-12-06 Mixing control method for preplasticizing plastic powder Active CN111037774B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201911243114.8A CN111037774B (en) 2019-12-06 2019-12-06 Mixing control method for preplasticizing plastic powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201911243114.8A CN111037774B (en) 2019-12-06 2019-12-06 Mixing control method for preplasticizing plastic powder

Publications (2)

Publication Number Publication Date
CN111037774A CN111037774A (en) 2020-04-21
CN111037774B true CN111037774B (en) 2021-10-29

Family

ID=70234865

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201911243114.8A Active CN111037774B (en) 2019-12-06 2019-12-06 Mixing control method for preplasticizing plastic powder

Country Status (1)

Country Link
CN (1) CN111037774B (en)

Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08224733A (en) * 1995-02-23 1996-09-03 Matsushita Electric Works Ltd Mixer
US6224796B1 (en) * 1998-08-19 2001-05-01 CENTRE DE RECHERCHE INDUSTRIELLE DU QUéBEC Process for producing batches of rubber-based composition
JP2005298553A (en) * 2004-04-06 2005-10-27 Nissei Plastics Ind Co Method for mixing resin material with carbon nano material and device for mixing them
CN104035461A (en) * 2014-07-02 2014-09-10 深圳市捷佳伟创新能源装备股份有限公司 Temperature control system and method
CN105183041A (en) * 2015-10-08 2015-12-23 厦门艾美森新材料科技股份有限公司 Method for controlling heating temperature of heating wires of buffer air cushion machine
CN105643824A (en) * 2016-03-24 2016-06-08 镇江康源新材料科技有限公司 Mixing system for medical PVC materials
CN205704794U (en) * 2016-06-30 2016-11-23 上海韬溢实业有限公司 Rubber high speed mixer
JP2017188397A (en) * 2016-04-08 2017-10-12 エリーパワー株式会社 Kneading method for preparing battery electrode slurry
JP2018030056A (en) * 2016-08-22 2018-03-01 ホソカワミクロン株式会社 Treatment apparatus and powder treatment method
CN108567311A (en) * 2017-03-16 2018-09-25 佛山市顺德区美的电热电器制造有限公司 A kind of cooking apparatus anti-dry method, apparatus and cooking system
CN108628361A (en) * 2018-05-29 2018-10-09 广东联塑科技实业有限公司 A kind of " temperature-current " intelligent control method
CN109382926A (en) * 2017-08-10 2019-02-26 安丘市云科机械有限公司 One kind exempting from heating temperature control type blending bunker
CN109730526A (en) * 2018-11-27 2019-05-10 华帝股份有限公司 Constant temperature control method of electric steam box

Family Cites Families (32)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4037020A1 (en) * 1990-11-20 1992-05-21 Koch Heinrich Plastmasch Control of welding extruder temp. using control appts. - which measures actual temp. of plasticised welding wire at screw end and compares it with set value prior to varying temp., etc.
DE4127493C2 (en) * 1991-08-20 2002-02-07 Norbert Krumm Thermo controller
JP3039727B2 (en) * 1992-07-20 2000-05-08 東陶機器株式会社 Dry battery driven electronically controlled hot and cold water mixing equipment
US5456870A (en) * 1994-05-20 1995-10-10 Van Dorn Demag Corporation Barrel temperature state controller for injection molding machine
US20040096385A1 (en) * 2000-09-12 2004-05-20 Antonio Proni Thermally regulated closed mixer
JP2002233741A (en) * 2001-02-13 2002-08-20 Kanegafuchi Chem Ind Co Ltd Continuous mixing device, manufacturing method for the same, continuous mixing method, and method and device for distinguishing performance of continuous mixing device
JP3950648B2 (en) * 2001-05-29 2007-08-01 有限会社ケイシーケイ応用技術研究所 Method and apparatus for kneading ultrafine powder and resin
JP3942411B2 (en) * 2001-11-28 2007-07-11 日東電工株式会社 Stirrer
US7178353B2 (en) * 2004-02-19 2007-02-20 Advanced Thermal Sciences Corp. Thermal control system and method
JP2006321821A (en) * 2005-04-22 2006-11-30 Toyo Ink Mfg Co Ltd Method for producing pigment
JP4374354B2 (en) * 2006-06-02 2009-12-02 株式会社コーハン Plastic waste material recycling mixing equipment
US8498523B2 (en) * 2009-02-03 2013-07-30 Intellihot, Inc. Apparatus and control method for a hybrid tankless water heater
CN102307712B (en) * 2009-02-05 2014-01-29 株式会社新泻机械科技 High-shear device and method of high shearing
JP5651317B2 (en) * 2009-03-31 2015-01-07 東京エレクトロン株式会社 Semiconductor manufacturing apparatus and temperature control method
EP2322333A1 (en) * 2009-11-16 2011-05-18 Bami Intelligence S.A. Mixed plastic waste processing apparatus, method of producing a hybrid plastic material, and hybrid plastic material obtained by blending.
CN201677423U (en) * 2010-01-11 2010-12-22 姜维 Material mixing device for devulcanizing and plasticizing waster rubber powder
DE102010060423A1 (en) * 2010-11-08 2012-05-10 Dr. Herfeld Gmbh & Co. Kg Method for mixing a mixture consisting of solid particles and mixer arrangement
CN203471987U (en) * 2013-09-10 2014-03-12 新疆联塑节水设备有限公司 Mixing, stirring and preplasticizing integrated automatic control system
CN104877295A (en) * 2014-02-27 2015-09-02 周绪洪 An energy-saving flame-retardant raw material and a preparing method thereof
KR101541268B1 (en) * 2015-05-20 2015-08-03 (주)한도기공 Tandem mixer for rubber mixing having heating and cooling function
CN105085987B (en) * 2015-09-18 2016-08-31 佟子豪 The preparation method of covering property granule
FR3051703A1 (en) * 2016-05-27 2017-12-01 Michelin & Cie MANUFACTURE OF RUBBER MIXTURES
CN105884169B (en) * 2016-06-12 2018-05-15 蚌埠玻璃工业设计研究院 A kind of glass batch temprature control method and its device
US10466727B2 (en) * 2016-11-22 2019-11-05 Haier US Appliance Solution, Inc. Water supply system and a method for operating the same
CN106553285A (en) * 2016-11-29 2017-04-05 陕西环珂生物科技有限公司 A kind of preparation method of starch EVA composite foam materials
CN207549185U (en) * 2017-12-06 2018-06-29 惠州市晋裕塑料科技有限公司 A kind of high mixer
CN108034171A (en) * 2017-12-28 2018-05-15 广西南宁桂尔创环保科技有限公司 A kind of PVC wood plastic composite material and preparation method thereof
CN108644827A (en) * 2018-05-21 2018-10-12 广东美的厨房电器制造有限公司 Microwave oven defrosting control method, micro-wave oven, terminal and computer storage media
CN208359159U (en) * 2018-05-28 2019-01-11 河南强宏镁业科技股份有限公司 The hoisting mechanism of kneading machine feed
CN209416525U (en) * 2019-01-08 2019-09-20 广东联塑科技实业有限公司 The measuring device of temperature of charge in a kind of high speed mixing
CN110124594A (en) * 2019-06-03 2019-08-16 常州瑞曦生物科技有限公司 Fine chemistry industry temperature of reaction kettle control method
CN110303615A (en) * 2019-07-24 2019-10-08 南通中联工业发展有限公司 A kind of preparation method of highly elastic polyvinyl chloride product

Patent Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08224733A (en) * 1995-02-23 1996-09-03 Matsushita Electric Works Ltd Mixer
US6224796B1 (en) * 1998-08-19 2001-05-01 CENTRE DE RECHERCHE INDUSTRIELLE DU QUéBEC Process for producing batches of rubber-based composition
JP2005298553A (en) * 2004-04-06 2005-10-27 Nissei Plastics Ind Co Method for mixing resin material with carbon nano material and device for mixing them
CN104035461A (en) * 2014-07-02 2014-09-10 深圳市捷佳伟创新能源装备股份有限公司 Temperature control system and method
CN105183041A (en) * 2015-10-08 2015-12-23 厦门艾美森新材料科技股份有限公司 Method for controlling heating temperature of heating wires of buffer air cushion machine
CN105643824A (en) * 2016-03-24 2016-06-08 镇江康源新材料科技有限公司 Mixing system for medical PVC materials
JP2017188397A (en) * 2016-04-08 2017-10-12 エリーパワー株式会社 Kneading method for preparing battery electrode slurry
CN205704794U (en) * 2016-06-30 2016-11-23 上海韬溢实业有限公司 Rubber high speed mixer
JP2018030056A (en) * 2016-08-22 2018-03-01 ホソカワミクロン株式会社 Treatment apparatus and powder treatment method
CN108567311A (en) * 2017-03-16 2018-09-25 佛山市顺德区美的电热电器制造有限公司 A kind of cooking apparatus anti-dry method, apparatus and cooking system
CN109382926A (en) * 2017-08-10 2019-02-26 安丘市云科机械有限公司 One kind exempting from heating temperature control type blending bunker
CN108628361A (en) * 2018-05-29 2018-10-09 广东联塑科技实业有限公司 A kind of " temperature-current " intelligent control method
CN109730526A (en) * 2018-11-27 2019-05-10 华帝股份有限公司 Constant temperature control method of electric steam box

Also Published As

Publication number Publication date
CN111037774A (en) 2020-04-21

Similar Documents

Publication Publication Date Title
CN105538641A (en) Material plasticizing production system
US10464246B2 (en) Injection molding method
US20090057938A1 (en) Closed Loop Control for an Injection Unit
JPH06240153A (en) Process of formation of elastic composition
CN105437493A (en) Intelligent single line production system for material plasticizing
CN102604206A (en) Superfine talcum powder-polypropylene filled master batch, preparation method and equipment thereof
CN111037774B (en) Mixing control method for preplasticizing plastic powder
EP0566276A1 (en) Die plate for plastics extruder
CN104175412A (en) Chloroprene rubber mixing process
CN203198215U (en) Extrusion forming device based on hard PVC (Polyvinyl Chloride) door-window profiled bar
JP4100326B2 (en) Plasticizer for injection molding machine
CN105385012B (en) A kind of SEBS/EVA intermingling materials closed-cell foam process
CN205097492U (en) Promote extruder of PVC section bar rerum natura
CN205553117U (en) Quick shaping material plastifying single line production system of intelligent 3D
CN210651427U (en) Electromagnetic heating type plastic granulator convenient for mixing materials
CN205800089U (en) A kind of light guide plate die injection moulding
JP2012045865A (en) Method for producing fiberglass-reinforced thermoplastic resin composition pellet
US3023460A (en) Process of vulcanizing rubber including a delayed addition of ultra-accelerator
JPH08103926A (en) Screw structure for molding machine of liquid crystal resin composite material
CN109971092A (en) A kind of microballon composite door closure material and preparation method
CN215729458U (en) Control system of high-pressure forming machine
CN105835340A (en) Intelligent control system for door seal extrusion process
JP4773645B2 (en) Injection molding method for heat-resistant thin-walled molded products
JP2002144405A (en) Foam molding method and foamed resin extrusion machine used for this method
JP4842046B2 (en) Plasticizing apparatus and plasticizing method for injection molding machine

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