CN111844671A - Special process method for producing PBT plastic rod - Google Patents
Special process method for producing PBT plastic rod Download PDFInfo
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- CN111844671A CN111844671A CN202010634974.0A CN202010634974A CN111844671A CN 111844671 A CN111844671 A CN 111844671A CN 202010634974 A CN202010634974 A CN 202010634974A CN 111844671 A CN111844671 A CN 111844671A
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- 238000000034 method Methods 0.000 title claims abstract description 27
- 229920003023 plastic Polymers 0.000 title claims abstract description 13
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- 238000001125 extrusion Methods 0.000 claims abstract description 23
- 239000000155 melt Substances 0.000 claims abstract description 19
- 238000005520 cutting process Methods 0.000 claims abstract description 16
- 230000006835 compression Effects 0.000 claims abstract description 14
- 238000007906 compression Methods 0.000 claims abstract description 14
- 238000001035 drying Methods 0.000 claims abstract description 9
- 238000000265 homogenisation Methods 0.000 claims abstract description 8
- 238000010438 heat treatment Methods 0.000 claims description 41
- 229920000426 Microplastic Polymers 0.000 claims description 13
- 238000007493 shaping process Methods 0.000 claims description 12
- 239000000463 material Substances 0.000 claims description 5
- 238000000748 compression moulding Methods 0.000 claims description 4
- 238000000465 moulding Methods 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 238000004857 zone melting Methods 0.000 claims 1
- 238000005336 cracking Methods 0.000 abstract description 3
- 238000003466 welding Methods 0.000 abstract description 2
- 229920001707 polybutylene terephthalate Polymers 0.000 description 36
- 238000001816 cooling Methods 0.000 description 5
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 229910000831 Steel Inorganic materials 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 239000012768 molten material Substances 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 235000012438 extruded product Nutrition 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- -1 polybutylene phthalate Polymers 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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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
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
- B29C48/06—Rod-shaped
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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
- B29C48/001—Combinations of extrusion moulding with other shaping operations
- B29C48/0022—Combinations of extrusion moulding with other shaping operations combined with cutting
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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
- B29C48/022—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the choice of material
-
- 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
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/505—Screws
- B29C48/625—Screws characterised by the ratio of the threaded length of the screw to its outside diameter [L/D ratio]
-
- 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
-
- 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
- B29C2948/9258—Velocity
-
- 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
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2067/00—Use of polyesters or derivatives thereof, as moulding material
- B29K2067/006—PBT, i.e. polybutylene terephthalate
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
本发明提供一种专用于生产PBT塑料棒的工艺方法,所述工艺包括:烘干,去除水分:塑化挤出,采用特定温度分三区加热机筒,采用特定结构的PBT炮筒螺杆以及特定挤出速度;均化分流,主模分四区以使熔体进一步均化;成型/定型,直线流动的熔体通过主模出口被均匀流入导流板,通过导流板进行分流,分别进入多棒成型模的成型管,熔体在成型管内的压缩成型区成型;裁切。本发明克服了棒材内应力过大造成的收缩变形或开裂报废,棒材耐冲击力更好,表面光滑,几乎没有熔悍缝。The invention provides a process method specially used for producing PBT plastic rods. The process includes: drying, removing moisture, plasticizing and extruding, using a specific temperature to heat a barrel in three zones, using a PBT barrel screw with a specific structure, and Specific extrusion speed; homogenization and splitting, the main mold is divided into four zones to further homogenize the melt; forming/setting, the melt flowing in a straight line is uniformly flowed into the guide plate through the main mold outlet, and the flow is divided through the guide plate, respectively. Entering the forming tube of the multi-rod forming die, the melt is formed in the compression forming zone within the forming tube; cutting. The invention overcomes the shrinkage deformation or cracking and scrapping caused by excessive internal stress of the bar, and the bar has better impact resistance, smooth surface and almost no welding seam.
Description
技术领域technical field
本发明涉及一种专用于生产PBT塑料棒的工艺方法。The invention relates to a process method specially used for producing PBT plastic rods.
背景技术Background technique
PBT(polybutyleneterephthalate,聚苯二甲酸丁二醇酯)成型是把粒状物料由料斗加入到挤出机的机筒内,物料在螺杆旋转的挤压推动作用下,通过机筒内壁和螺杆表面的摩擦作用向前输送和压实,通过机筒外部的加热装置和摩擦预热,在高温、高压条件下熔融塑化。然后,连续转动的螺杆再把熔融物料推入机头模具,从机头模具挤出的熔融物料经冷却定型成为所需的PBT制品。PBT (polybutyleneterephthalate, polybutylene phthalate) molding is to add granular materials from a hopper into the barrel of the extruder. The function is forward conveying and compacting, and is melted and plasticized under high temperature and high pressure conditions through the heating device and frictional preheating outside the barrel. Then, the continuously rotating screw pushes the molten material into the die, and the molten material extruded from the die is cooled and shaped into the desired PBT product.
PBT棒成型工艺过程包括:投料-烘干-塑化挤出-成型定型-切割/堆放等。The PBT rod forming process includes: feeding - drying - plasticizing extrusion - forming and shaping - cutting/stacking, etc.
目前在制备PBT棒过程中,塑化挤出时分为三区对机筒加温:At present, in the process of preparing PBT rods, the barrel is heated in three zones during plasticization and extrusion:
一区加料段温度为260-270℃;The temperature of the feeding section in the first zone is 260-270 °C;
二区融熔压缩段温度为260-270℃;The temperature of the melting and compression section of the second zone is 260-270 °C;
三区均化段温度为270-280℃;The temperature of the three-zone homogenization section is 270-280℃;
接头温度为250-260℃;The temperature of the joint is 250-260℃;
螺杆长径比为30:1,压缩比为3,挤出速度为25-30r/min。The screw length-diameter ratio is 30:1, the compression ratio is 3, and the extrusion speed is 25-30r/min.
在成型定型过程中,通过螺杆旋转剪切作用下进入机头体(机头体温度250-260℃)后进入单棒模具中直接成型,成型后在冷却水的作用下,温度不断降低,最后凝固结晶、定型被挤出单棒模具。In the process of forming and setting, it enters the head body (the temperature of the head body is 250-260 ℃) under the action of screw rotation and shearing, and then enters the single-bar mold for direct molding. After molding, under the action of cooling water, the temperature continues to decrease. Solidification, crystallization, and shape are extruded from a single-rod die.
在后续热处理分为十一段:The subsequent heat treatment is divided into eleven sections:
第一段:加温温度45℃、升温时间100分钟;The first stage: heating temperature 45 ℃, heating time 100 minutes;
第二段:恒温温度50℃、恒温时间为厚度*3*70分钟;The second stage: the constant temperature is 50°C, and the constant temperature time is thickness * 3 * 70 minutes;
第三段:加温温度75℃、加温时间20分钟;The third stage: heating temperature 75 ℃, heating time 20 minutes;
第四段:恒温温度90℃、恒温时间200分钟;The fourth stage: constant temperature of 90°C and constant temperature of 200 minutes;
第五段:加温温度100℃、加温时间30分钟;The fifth stage: heating temperature 100 ℃, heating time 30 minutes;
第六段:恒温温度130℃、恒温时间150分钟;Section 6: constant temperature of 130°C and constant temperature of 150 minutes;
第七段:加温温度100℃、加温时间10分钟;The seventh stage: heating temperature 100 ℃,
第八段:恒温温度60℃、恒温时间180分钟;Section 8: constant temperature of 60°C and constant temperature of 180 minutes;
第九段:加温温度60℃、加温时间60分钟;The ninth paragraph: heating temperature 60 ℃, heating time 60 minutes;
第十段:恒温温度60℃、恒温时间180分钟;Section 10: constant temperature of 60°C and constant temperature of 180 minutes;
第十一段:降温温度60℃、降温时间20分钟。The eleventh stage: the cooling temperature is 60°C, and the cooling time is 20 minutes.
上述工艺存在的问题是:1、棒材耐冲击力低;2、表面不光、有熔悍缝;3、棒材内应力大;4、加工易开裂。The problems existing in the above process are: 1. The impact resistance of the bar is low; 2. The surface is not bright, but there are melted seams; 3. The internal stress of the bar is large; 4. It is easy to crack during processing.
发明内容SUMMARY OF THE INVENTION
鉴于此,有必要提供一种专用于生产PBT塑料棒的工艺方法,以解决以上技术问题。In view of this, it is necessary to provide a special process method for producing PBT plastic rods to solve the above technical problems.
本发明提供一种专用于生产PBT塑料棒的工艺方法,所述工艺包括以下步骤:The present invention provides a kind of process method specially used for producing PBT plastic rod, and described process comprises the following steps:
烘干:通过100℃的循环热风对PBT塑料粒进行干燥使得所述PBT塑料粒水分含量低于0.2%;Drying: drying the PBT plastic pellets by circulating hot air at 100°C so that the moisture content of the PBT plastic pellets is lower than 0.2%;
塑化挤出:通过机筒的温度与挤出螺杆的作用使所述PBT塑料粒转变为具有一定流动性的均匀连续熔体被挤出;其中,前后分为三区对所述机筒加温:Plasticizing extrusion: The PBT plastic pellets are transformed into a uniform continuous melt with a certain fluidity through the action of the temperature of the barrel and the extrusion screw and extruded; temperature:
一区加料段温度为240-250℃;The temperature of the feeding section in the first zone is 240-250 °C;
二区融熔压缩段温度为250-260℃;The temperature of the melting and compression section of the second zone is 250-260 °C;
三区均化段温度为250-270℃;The temperature of the three-zone homogenization section is 250-270℃;
接头温度为260-270℃;The temperature of the joint is 260-270℃;
所述挤出螺杆为专用等距渐变型的PBT炮筒螺杆,螺杆长径比为25:1,压缩比为3.3,挤出速度为30-35r/min;The extrusion screw is a special equidistant gradient type PBT barrel screw, the screw length-diameter ratio is 25:1, the compression ratio is 3.3, and the extrusion speed is 30-35r/min;
均化分流:在所述挤出螺杆的旋转挤压下,通过料嘴进入主模,熔体在所述主模内进一步均化,并且将熔体由螺旋运动转为直线运动;其中,所述主模分四区设定恒温:Homogenization and shunting: under the rotary extrusion of the extrusion screw, the melt enters the main mold through the material nozzle, and the melt is further homogenized in the main mold, and the melt is converted from a spiral motion to a linear motion; The main mold is divided into four zones to set the constant temperature:
前一区温度为260-270℃;The temperature of the previous zone is 260-270℃;
前二区温度为250-260℃;The temperature of the first two zones is 250-260℃;
后一区温度为250-260℃;The temperature of the latter zone is 250-260℃;
后二区温度为240-250℃;The temperature of the second zone is 240-250℃;
成型/定型:直线流动的熔体通过所述主模出口被均匀流入导流板,通过所述导流板进行分流,分别进入多棒成型模的成型管,熔体在所述成型管内的压缩成型区成型;其中Forming/Shaping: The melt flowing in a straight line is uniformly flowed into the deflector through the outlet of the main die, and is divided by the deflector, and then enters the forming tube of the multi-rod forming die respectively, and the melt is compressed in the forming tube. forming zone forming; wherein
所述导流板的均化温度为250-260℃;The homogenization temperature of the guide plate is 250-260°C;
所述成型管的定型区的定型温度为140-160℃;The shaping temperature of the shaping zone of the shaping tube is 140-160°C;
裁切:将成型后的棒材切成预定长度。Cutting: Cut the formed bar into a predetermined length.
进一步的,在裁切后还包括后期热处理步骤:Further, after cutting, it also includes a post-heat treatment step:
将叠放好的PBT棒材进行热处理,分为十一段:The stacked PBT bars are heat treated and divided into eleven sections:
第一段加温温度40℃升温时间:120分钟;The heating temperature of the first stage is 40°C and the heating time: 120 minutes;
第二段恒温温度70℃恒温时间:厚度*3*60分钟;The second section of constant temperature is 70°C constant temperature time: thickness * 3 * 60 minutes;
第三段加温温度70℃加温时间:20分钟;The third stage heating temperature 70 ℃ heating time: 20 minutes;
第四段恒温温度100℃恒温时间:180分钟;The fourth section of constant temperature 100 ℃ constant temperature time: 180 minutes;
第五段加温温度120℃加温时间:20分钟;The fifth stage heating temperature 120 ℃ heating time: 20 minutes;
第六段恒温温度100℃恒温时间:180分钟;The sixth section constant temperature 100 ℃ constant temperature time: 180 minutes;
第七段加温温度70℃加温时间:20分钟;The seventh stage heating temperature 70 ℃ heating time: 20 minutes;
第八段恒温温度40℃恒温时间:180分钟;The eighth section constant temperature 40 ℃ constant temperature time: 180 minutes;
第九段加温温度40℃加温时间:40分钟;The ninth stage heating temperature 40 ℃ heating time: 40 minutes;
第十段恒温温度40℃恒温时间:180分钟;The tenth section constant temperature 40 ℃ constant temperature time: 180 minutes;
第十一段降温温度40℃降温时间:150分钟。The eleventh section cooling temperature 40 ℃ cooling time: 150 minutes.
进一步的,在所述成型/定型之后,还包括:Further, after the forming/setting, it also includes:
牵引:通过牵引机构对定型后的棒材进行牵引,以使熔体在所述压缩成型区形成一定的压力,以提高棒材的结构紧密型。Traction: The shaped bar is pulled by the traction mechanism, so that the melt forms a certain pressure in the compression molding area, so as to improve the compact structure of the bar.
本发明通过以上工艺步骤的选择以及工艺参数的设定,克服了棒材内应力过大造成的收缩变形或开裂报废,棒材耐冲击力更好,表面光滑,几乎没有熔悍缝。Through the selection of the above process steps and the setting of process parameters, the invention overcomes the shrinkage deformation or cracking and scrapping caused by excessive internal stress of the bar, and the bar has better impact resistance, smooth surface and almost no welding seam.
附图说明Description of drawings
图1为本发明使用的一实施方式的生产设备的结构示意图。FIG. 1 is a schematic structural diagram of a production equipment according to an embodiment of the present invention.
具体实施方式Detailed ways
本发明所提供的一种专用于生产PBT塑料棒的工艺方法,通过图1所示的PBT专用生产设备来进行生产。如图1所示,所述设备包括电机1、减速箱2、料斗4、干燥机3、控制柜5、PBT专用炮筒螺杆6、法兰接头7、连接四方板8、进料口9、主模10、模具架12、导流板11、成型管13、牵引机14、切割机15、以及烤箱等。A process method specially used for producing PBT plastic rods provided by the present invention is produced by the special production equipment for PBT shown in FIG. 1 . As shown in Figure 1, the equipment includes a motor 1, a reduction box 2, a hopper 4, a dryer 3, a control cabinet 5, a special barrel screw 6 for PBT, a flange joint 7, a connecting square plate 8, a feeding port 9, The
所述电机1、所述减速箱2、所述料斗4、所述干燥机3、所述控制柜5、所述PBT专用炮筒螺杆6等可构成所述设备的主机部分,所述主模10、所述模具架12、所述导流板11、所述隔热圈14、所述成型管13、所述牵引机14、所述切割机15、以及所述烤箱等可以构成所述设备的辅机部分。The motor 1, the reduction box 2, the hopper 4, the dryer 3, the control cabinet 5, the PBT-specific barrel screw 6, etc. can constitute the main part of the equipment. 10. The mold frame 12, the deflector 11, the heat insulation ring 14, the forming tube 13, the tractor 14, the cutting machine 15, and the oven can constitute the equipment the auxiliary part.
其中,所述电机1和所述减速箱2构成了转动系统,所述电机1运转,通过皮带传动带动减速箱2,从而使PBT专用炮筒螺杆6保持一定的剪切速率。所述PBT专用炮筒螺杆6特别参数:长径比为25:1,压缩比为3.3。The motor 1 and the reduction box 2 constitute a rotating system. The motor 1 operates and drives the reduction box 2 through a belt drive, so that the PBT special barrel screw 6 maintains a certain shear rate. The special parameters of the PBT special barrel screw 6: the length-diameter ratio is 25:1, and the compression ratio is 3.3.
所述控制柜5内可设有控制系统,其具体可以包括电器仪表和执行机构其主要作用是控制主机,使其操作的转速和功率正常,并保证主机和辅机的温度、压力、流量和制品的质量,实现全机组的自动控制。The control cabinet 5 can be provided with a control system, which can specifically include electrical instruments and actuators. Its main function is to control the main engine, so that the speed and power of its operation are normal, and to ensure the temperature, pressure, flow and power of the main engine and auxiliary machines. The quality of the products is realized, and the automatic control of the whole unit is realized.
所述主模10设在模具架12上。熔体通过所述进料口9进入所述主模10。进流道分流挡块两边进行分流,经过分流的熔体在一定的压力下进入导流板11的八个喇叭口和成型管13,在一定的压力和油温恒温定型的状态下在所述成型管13内成型、定型。The
成型管13包括压缩成型区以及定型区。油温机安装在成型管13的定型区,通过热油不断循环,使定型区制品在恒定均衡的温度下定型并顺利挤出模具。The forming tube 13 includes a compression forming area and a setting area. The oil temperature machine is installed in the setting area of the forming tube 13, and through the continuous circulation of hot oil, the products in the setting area are shaped at a constant and balanced temperature and smoothly extruded from the mold.
牵引机14主要由传动装置、辊筒压紧装置和刹车制动装置组成,通过连杆将所述主模13与牵引机14固定在一起,气控制牵引机14上下连接四方板8,减速机拖动辊筒使制品在压缩区保持一定压力匀速前进。The tractor 14 is mainly composed of a transmission device, a roller pressing device and a braking device. The main mold 13 and the tractor 14 are fixed together by connecting rods. The pneumatic control tractor 14 is connected with the square plate 8 up and down, and the reducer Drag the roller to make the product keep a certain pressure in the compression zone and move forward at a constant speed.
切割机15为棒材切割设备,它安装在后面,挤出的制品穿过切割机15的切割支撑面,通过锯片的高速旋转切割棒材,切成所需要的长度制品。The cutting machine 15 is a bar cutting device, which is installed at the back. The extruded products pass through the cutting support surface of the cutting machine 15, and the bars are cut by the high-speed rotation of the saw blade to cut products of required lengths.
所述烤箱为密封型的箱体结构,通过温度控制器,设定不同温度,不同时间多段对制品进行热处理。The oven is a sealed box structure, and different temperatures are set through a temperature controller, and the products are heat-treated in multiple stages at different times.
本发明所提供的专用于生产PBT塑料棒的工艺方法,主要包括以下步骤:投料、烘干、塑化挤出、均化分流、成型/定型、牵引、裁切、堆料、热处理。The process method specially used for producing PBT plastic rods provided by the present invention mainly includes the following steps: feeding, drying, plasticizing and extruding, homogenizing and shunting, forming/setting, pulling, cutting, stacking, and heat treatment.
下面着重说明本发明的一具体实施方式的具体工艺步骤。The specific process steps of a specific embodiment of the present invention are emphatically described below.
1、投料:在投料时,应当及时投料,保证料斗4不空。不同的料不能混用,注意分清料的牌号及料的类型,防止杂物、杂料进入料斗4,造成下料口堵塞。1. Feeding: When feeding, it should be fed in time to ensure that the hopper 4 is not empty. Different materials can not be mixed, pay attention to distinguish the grades and types of materials, to prevent sundries and sundries from entering the hopper 4, causing the discharge port to be blocked.
2、烘干:由于PBT树脂吸温性较大,在挤出成型前必须经进干燥处理,排除水分,否则其水分含量超过一定限度,水分就会在挤出机筒内挥发成气体,使制品内部含有气孔,使得制品强度下降。2. Drying: Due to the high temperature absorption of PBT resin, it must be dried before extrusion to remove water, otherwise its water content exceeds a certain limit, and the water will volatilize into gas in the extruder barrel, causing The product contains pores, which reduces the strength of the product.
在本步骤中,针对PBT塑料粒的特性,采用100℃循环热风对PBT塑料粒进行干燥,干燥时间为2-4H,使产品内的水分含量低于0.2%,采用100℃的循环热风对PBT塑料粒干燥同时实现PBT塑料粒的预热效果。In this step, according to the characteristics of PBT plastic pellets, 100°C circulating hot air is used to dry the PBT plastic pellets, and the drying time is 2-4H, so that the moisture content in the product is less than 0.2%, and 100°C circulating hot air is used to dry the PBT plastic pellets. The plastic pellets are dried and the preheating effect of the PBT plastic pellets is achieved.
3、塑化挤出:通过机筒的温度与挤出螺杆的作用使所述PBT塑料粒转变为具有一定流动性的均匀连续熔体被挤出。3. Plasticizing extrusion: The PBT plastic pellets are transformed into a uniform continuous melt with a certain fluidity and extruded through the action of the temperature of the barrel and the extrusion screw.
所述挤出螺杆为专用等距渐变型的PBT炮筒螺杆,螺杆长径比为25:1,压缩比为3.3。The extrusion screw is a special equidistant gradient type PBT barrel screw, the screw length-diameter ratio is 25:1, and the compression ratio is 3.3.
其中,前后分为三区对所述机筒加温,一区加料段温度为240-250℃(例如241℃、242℃、243℃、244℃、245℃、246℃、247℃、248℃、249℃);二区融熔压缩段温度为250-260℃(例如251℃、252℃、253℃、254℃、255℃、256℃、257℃、258℃、259℃);三区均化段温度为250-270℃(例如251℃、252℃、253℃、254℃、255℃、256℃、257℃、258℃、259℃、260℃、261℃、262℃、263℃、264℃、265℃、266℃、267℃、268℃、269℃);接头温度为260-270℃(例如261℃、262℃、263℃、264℃、265℃、266℃、267℃、268℃、269℃);挤出速度为30-35r/min(例如31r/min、32r/min、33r/min、34r/min)。Wherein, the front and back are divided into three zones to heat the barrel, and the temperature of the feeding section in one zone is 240-250°C (for example, 241°C, 242°C, 243°C, 244°C, 245°C, 246°C, 247°C, 248°C) , 249°C); the temperature of the melting and compression section of the second zone is 250-260°C (for example, 251°C, 252°C, 253°C, 254°C, 255°C, 256°C, 257°C, 258°C, 259°C); The temperature of the melting section is 250-270°C (for example, 251°C, 252°C, 253°C, 254°C, 255°C, 256°C, 257°C, 258°C, 259°C, 260°C, 261°C, 262°C, 263°C, 264°C °C, 265 °C, 266 °C, 267 °C, 268 °C, 269 °C); joint temperature is 260-270 °C (eg 261 °C, 262 °C, 263 °C, 264 °C, 265 °C, 266 °C, 267 °C, 268 °C , 269°C); the extrusion speed is 30-35r/min (eg 31r/min, 32r/min, 33r/min, 34r/min).
通过选择特定的螺杆长径比、压缩比、三区加温温度、接头温度以及挤出速度,能够使PBT塑料粒更完全地塑化以及熔融以及挤出成型,每一参数的设置都影响着棒材制品的应力、气孔以及机械性能等。By selecting specific screw aspect ratio, compression ratio, three-zone heating temperature, joint temperature and extrusion speed, the PBT plastic pellets can be more completely plasticized, melted and extruded. The settings of each parameter affect the Stress, porosity and mechanical properties of bar products.
4、均化分流:在所述挤出螺杆的旋转挤压下,通过料嘴进入主模,熔体在所述主模内进一步均化,并且将熔体由螺旋运动转为直线运动。4. Homogenization and diversion: Under the rotary extrusion of the extrusion screw, the melt enters the main mold through the material nozzle, and the melt is further homogenized in the main mold, and the melt is converted from a spiral motion to a linear motion.
所述主模分四区设定恒温,前一区温度为260-270℃(例如261℃、262℃、263℃、264℃、265℃、266℃、267℃、268℃、269℃);前二区温度为250-260℃(例如251℃、252℃、253℃、254℃、255℃、256℃、257℃、258℃、259℃);后一区温度为250-260℃(例如251℃、252℃、253℃、254℃、255℃、256℃、257℃、258℃、259℃);后二区温度为240-250℃(例如241℃、242℃、243℃、244℃、245℃、246℃、247℃、248℃、249℃)。The main mold is divided into four zones to set a constant temperature, and the temperature of the previous zone is 260-270°C (for example, 261°C, 262°C, 263°C, 264°C, 265°C, 266°C, 267°C, 268°C, 269°C); The temperature of the first two zones is 250-260°C (eg 251°C, 252°C, 253°C, 254°C, 255°C, 256°C, 257°C, 258°C, 259°C); the temperature of the latter zone is 250-260°C (eg 251°C, 252°C, 253°C, 254°C, 255°C, 256°C, 257°C, 258°C, 259°C); , 245°C, 246°C, 247°C, 248°C, 249°C).
5、成型/定型:直线流动的熔体通过所述主模10出口被均匀流入导流板11,通过所述导流板11进行分流,分别进入多棒成型模的成型管,熔体在所述成型管内的压缩成型区成型。所述导流板的均化温度为250-260℃(例如251℃、252℃、253℃、254℃、255℃、256℃、257℃、258℃、259℃);所述成型管的定型区的定型温度为140-160℃(例如141℃、142℃、143℃、144℃、145℃、146℃、147℃、148℃、149℃、150℃、151℃、152℃、153℃、154℃、155℃、156℃、157℃、158℃、159℃)。5. Forming/Shaping: The melt flowing in a straight line is uniformly flowed into the deflector 11 through the outlet of the
结合步骤4,分四区对所述主模进行恒温、通过导流板进行分流并且采用特定的导流板温度以及成型管定型温度,得到熔体流动性、定型要求互配,保证棒材制品能够顺利被挤出,得到的棒材表面光洁度高。Combined with step 4, the main mold is kept at a constant temperature in four zones, the flow is divided through the baffle plate, and the specific baffle plate temperature and forming tube setting temperature are used to obtain the mutual matching of melt fluidity and shaping requirements, so as to ensure the bar product. It can be extruded smoothly, and the obtained bar has a high surface finish.
6、牵引:在保温装置主模10的出口位置装有刹车座,通过该刹车座调节刹车条的松紧而夹紧棒材制品,通过牵引机14构对定型的棒材牵引以使熔体在所述压缩成型区形成一定的压力,以提高棒材的结构紧密型以及调节棒材的厚度以偏心度。6. Traction: A brake seat is installed at the outlet of the
7、裁切:用卷尺测出1000MM长度,启动切割机,切出所需要的长度。7. Cutting: measure the length of 1000MM with a tape measure, start the cutting machine, and cut out the required length.
8、堆料:用吸盘吊葫芦将板吊起,整齐叠放在特定的堆料架上;在棒层与棒层之间放有不锈方钢,层与层之间的方钢上下看起来最好在一条直线上。8. Stacking: Use suction cup hoist to lift the board and stack it neatly on a specific stacker; place stainless square steel between the rod layer and the rod layer, and the square steel between the layers looks up and down It's best to be in a straight line.
9、后期热处理:通过烤箱对叠放堆好的PBT棒材进行热处理,分为十一段:9. Post-heat treatment: heat treatment of the stacked PBT bars through the oven, which is divided into eleven sections:
第一段 加温温度40℃ 升温时间:120分钟;The first section heating temperature 40 ℃ heating time: 120 minutes;
第二段 恒温温度70℃ 恒温时间:厚度*3*60分钟;The second section constant temperature temperature 70 ℃ constant temperature time: thickness * 3 * 60 minutes;
第三段 加温温度70℃ 加温时间:20分钟;The third stage heating temperature 70 ℃ heating time: 20 minutes;
第四段 恒温温度100℃ 恒温时间:180分钟;The fourth section constant temperature 100 ℃ constant temperature time: 180 minutes;
第五段 加温温度120℃ 加温时间:20分钟;The fifth section heating temperature 120 ℃ heating time: 20 minutes;
第六段 恒温温度100℃ 恒温时间:180分钟;Section 6 Constant temperature 100℃ Constant temperature time: 180 minutes;
第七段 加温温度70℃ 加温时间:20分钟;The seventh paragraph heating temperature 70 ℃ heating time: 20 minutes;
第八段 恒温温度40℃ 恒温时间:180分钟;The eighth section constant temperature 40 ℃ constant temperature time: 180 minutes;
第九段 加温温度40℃ 加温时间:40分钟;The ninth paragraph heating temperature 40 ℃ heating time: 40 minutes;
第十段 恒温温度40℃ 恒温时间:180分钟;
第十一段 降温温度40℃ 降温时间:150分钟。Section 11 Cooling temperature 40℃ Cooling time: 150 minutes.
通过以上具体的后期热处理步骤,采用特定时间、多段对PBT棒材制品进行特定温度热处理,能够有效消除PBT棒材制品残余内应力,保证PBT棒材质量以及稳定性。Through the above specific post-heat treatment steps, the PBT bar products are heat treated at a specific temperature for a specific time and multiple stages, which can effectively eliminate the residual internal stress of the PBT bar products and ensure the quality and stability of the PBT bar products.
将PBT棒材进行测试,测试项目和结果如下:The PBT bar is tested, and the test items and results are as follows:
以上各具体参数为本发明的发明人经过反复大量的具体实验、耗时数年才最终确定的适用于生产PBT塑料棒的参数,这些参数是相互依存的而并非孤立存在,参数的选择至关重要,这些参数配套在一起最终获得了期望的PBT塑料棒,通过以上具体的工艺方法步骤,制得的PBT塑料棒克服了因内应力过大造成的收缩变形或开裂报废的缺陷,避免了严重浪费的缺陷,制品内部几无气孔杂质,保证了产品的质量,合格品产量有很大的提高。The above specific parameters are the parameters suitable for the production of PBT plastic rods finally determined by the inventor of the present invention after repeated a large number of specific experiments and taking several years to produce. These parameters are interdependent rather than isolated, and the selection of parameters is crucial It is important that these parameters are matched together to finally obtain the desired PBT plastic rod. Through the above specific process steps, the obtained PBT plastic rod overcomes the defects of shrinkage deformation or cracking and scrapping caused by excessive internal stress, and avoids serious problems. Waste defects, there are almost no pores and impurities in the product, which ensures the quality of the product, and the yield of qualified products is greatly improved.
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