WO2014054829A1 - 고분자수지 연속압출장치 - Google Patents
고분자수지 연속압출장치 Download PDFInfo
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- WO2014054829A1 WO2014054829A1 PCT/KR2012/009295 KR2012009295W WO2014054829A1 WO 2014054829 A1 WO2014054829 A1 WO 2014054829A1 KR 2012009295 W KR2012009295 W KR 2012009295W WO 2014054829 A1 WO2014054829 A1 WO 2014054829A1
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- polymer resin
- extrusion
- oil
- continuous extrusion
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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
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
- B29C48/397—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using a single screw
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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
- B29C48/03—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
- B29C48/09—Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
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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
- B29C48/30—Extrusion nozzles or dies
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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
- B29C48/30—Extrusion nozzles or dies
- B29C48/304—Extrusion nozzles or dies specially adapted for bringing together components, e.g. melts within the die
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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
- B29C48/94—Lubricating
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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
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Definitions
- the present invention relates to a polymer resin continuous extrusion apparatus, and more particularly, in a continuous extrusion apparatus for continuously extruding the polymer resin melt in a direction parallel to the flow direction, the lubricant injected through the oil inlet formed in the extrusion die is the extrusion passage
- the present invention relates to a polymer resin continuous extrusion apparatus capable of a continuous process by flowing along an inner circumferential surface of the polymer resin.
- Extrusion processing for example, melts a soft metal such as aluminum or magnesium or various thermoplastic polymer resins (molding raw materials) in the barrel and pushes them to the extrusion opening, so that the molding raw materials have a cross-sectional shape of the extrusion openings. It is a processing method for manufacturing rods and pipes.
- extrusion apparatuses for the extrusion processing, for example, a cylindrical barrel extending in the longitudinal direction to pressurize the molding raw material, and an extrusion screw for conveying the molten polymer resin axially rotated in the barrel; It is common to have, at least one extrusion screw may be provided inside the extruder.
- thermoplastic resin In the extrusion process using resin as the molding material, only one thermoplastic resin can be used as the molding material, but in most cases, various kinds of thermoplastic resins are used together to maximize the physical and chemical characteristics of each resin. Seek improvement.
- thermoplastic resins to be added to the extrusion device is of course depending on the type or physical properties of the desired product.
- the resins can also chemically react with each other in a molten state in the extrusion apparatus or can only remain mixed.
- the conventional polymer continuous extrusion process was able to work only at a resin temperature higher than the melting temperature (Tm) of the resin in the case of the crystalline polymer or higher than the transition temperature (Tg) in the case of the amorphous polymer. This is because when the resin temperature is lowered, the resin solidifies and sticks to the inner surface of the die, and continuous operation is impossible.
- an object of the present invention is to allow the lubricant injected through the oil inlet formed on the upper side of the extrusion die flows along the inner peripheral surface of the extrusion passage to move together with the polymer resin melt It is to provide a polymer resin continuous extrusion apparatus capable of a continuous process by allowing the lubricant is evenly applied to the surface of the polymer resin melt.
- An object of the present invention is to inject a lubricant lubricating the surface of the polymer in order to facilitate the extrusion of the polymer to be coated, so that the polymer resin is easily extruded, the polymer can be easily removed after extrusion It is to provide a resin continuous extrusion apparatus.
- An object of the present invention is to enable the extrusion of the polymer resin melt with a very high viscosity, and to enable low-temperature extrusion, by introducing a lubricant that acts as a lubricating coating to the die to coat the surface of the extrudate, the polymer resin is
- the present invention provides a polymer resin continuous extrusion apparatus that can be easily extruded, and the injected organic and inorganic lubricant generates two-phase fluid flow without mixing in the extrudate.
- the polymer resin continuous extrusion device of the present invention is a continuous extrusion device (1) for continuously extruding the polymer resin melt in a direction parallel to the flow direction, the hopper 110 is provided on one side and the extrusion hole 141 on the other end
- An extruder (100) comprising a barrel (140) having and an extrusion screw (130) rotatably installed about a rotation axis in the barrel (140);
- An extrusion die (200) connected to the extruder (100), into which a polymer resin melt flows from the extruder (100), and passes through an extrusion passage (221) formed therein and discharged to the nozzle unit (300); It includes, characterized in that the lubricant injected through the oil inlet 211 formed on the upper side of the extrusion die 200 flows along the inner circumferential surface of the extrusion passage 221 is characterized in that it is moved with the polymer resin melt.
- the extrusion die 200 is the die body 210, the oil inlet 211 is formed on the upper side, including a through hole 212 penetrates in the flow direction of the polymer resin melt therein; Is formed in the shape of a cylindrical pipe is inserted and coupled to the through-hole 212 of the die body 210, the extrusion passage 221 is formed therein, the oil injection hole 211 is formed around the position
- An oil flow hole 222 is formed to be dug in the radial direction in the outer peripheral surface, the oil flow hole is formed so that both ends of the oil flow portion 222 is hollow so that the oil flows into the extrusion passage 221
- the polymer resin continuous extrusion device 1 is characterized in that the oil flow portion 222 is formed adjacent to one end of the body inserting portion 220 is located on the side connected to the neck portion 230. .
- the neck portion 230 is characterized in that the connecting portion 232 is formed in the region coupled to one end of the body insertion portion 220.
- the extrusion passage 221 is gradually reduced in diameter from the region in which the oil flow hole 223 is formed so as to correspond to the shape of the connecting portion 232, a predetermined diameter from the region where the end of the connecting portion 232 is located It is characterized in that it is formed to be maintained.
- the polymer resin continuous extrusion device (1) is characterized in that it is formed by including an oil pump 400 is inserted into the oil inlet 211 to supply the oil at a predetermined pressure.
- the oil pump 400 is characterized in that the gear pump or plunger pump.
- the lubricant is characterized in that the water, silicone oil, ethylene glycol, canola oil, oligomer or synthetic oil.
- the lubricant injected through the oil inlet formed on the upper side of the extrusion die flows along the inner circumferential surface of the extrusion passage so as to move together with the polymer resin melt so that the lubricant is evenly applied to the surface of the polymer resin melt.
- the polymer resin continuous extrusion apparatus of the present invention has the advantage that not only can be extruded at a temperature near or below the transition temperature of the polymer resin, it is also possible to extrude a polymer resin melt having a very high viscosity.
- the polymer resin continuous extrusion apparatus of the present invention can be continuously extruded from the extrusion die at a temperature near or below the melting temperature of the polymer resin, energy cost is reduced by reducing the extrusion pressure and torque, thereby The manufacturing cost can be lowered and carbon dioxide generation can be reduced.
- the polymer resin continuous extrusion apparatus of the present invention does not necessarily maintain the resin temperature in the extruder above the melting temperature to improve the physical properties of the final extrudate, and reduces the die swell which is a critical variable of the final extrudate form
- the advantage is that the die shape can be varied.
- the polymer resin continuous extrusion apparatus of the present invention facilitates continuous extrusion of the polymer resin melt, enables extrusion even if the viscosity of the melt is very high, and enables low-temperature extrusion to enable physical properties of the polymer due to deterioration.
- the polymer resin can be continuously extruded by preventing the fall and by dramatically lowering the pressure of the extruder.
- FIG. 1 is a schematic view showing a polymer resin continuous extrusion apparatus according to an embodiment of the present invention.
- Figure 2 is an exploded perspective view showing an extrusion die in a polymer resin continuous extrusion apparatus according to an embodiment of the present invention.
- Figure 3 is a perspective view of the extrusion die in the polymer resin continuous extrusion apparatus according to an embodiment of the present invention.
- Figure 4 is a side view showing the extrusion die in the polymer resin continuous extrusion apparatus according to an embodiment of the present invention.
- Figure 5 is a plan view showing an extrusion die in a polymer resin continuous extrusion apparatus according to an embodiment of the present invention.
- FIG. 6 is a schematic diagram schematically showing a path through which oil flows and a path through which a polymer resin melt flows in a polymer resin continuous extrusion apparatus according to an embodiment of the present invention.
- Figure 7 is a graph showing the speed distribution in the conventional extrusion method.
- Figure 9 is a graph showing the speed distribution in the polymer resin continuous extrusion apparatus according to an embodiment of the present invention.
- Figure 10 is a graph showing the shear rate distribution in the conventional extrusion method in the polymer resin continuous extrusion apparatus according to an embodiment of the present invention.
- the polymer resin continuous extrusion device 1 of the present invention continuously extrudes a polymer resin melt in a direction parallel to the flow direction, and is formed to include an extruder 100 and an extrusion die 200.
- the polymer resin continuous extrusion device 1 of the present invention may further include a cooling device or a calibrator at the rear end of the extrusion die 200.
- the present invention is generally applied to a configuration in which a crosslinking device is not provided at the rear end of the extrusion die 200, that is, an extrusion process not crosslinking.
- the polymer resin continuous extrusion device 1 of the present invention can be applied to the operation of the rubber compound that is not directly connected to the crosslinking device at the rear end.
- the extruder 100 includes a hopper 110 at one side, a barrel 140 having an extrusion hole 141 at the other end thereof, and a rotating shaft inside the barrel 140. It is formed including an extrusion screw 130 is rotatably installed to the center.
- the barrel 140 is provided with a heater 120 to melt the polymer resin inside the barrel 140.
- the extrusion die 200 is connected to the extruder 100 so that the polymer resin melt flows from the extruder 100 and passes through the extrusion passage 221 formed therein to be discharged to the nozzle unit 300.
- the polymer resin continuous extrusion device 1 of the present invention flows along the inner circumferential surface of the extrusion passage 221 is a lubricant injected through the oil inlet 211 formed on the extrusion die 200, the polymer resin melt Do not mix with, the surface of the polymer resin melt is characterized in that it is moved together.
- the lubricant is water, Various oligomers or synthetic oils such as silicone oil, ethylene glycol and canola oil may be used.
- the lubricant is preferably a material having a lower viscosity than the polymer resin during the extrusion process, in the case of polypropylene during extrusion, 100 s -One Since the viscosity is about 300 Pa ⁇ s at the shear rate, the organic material, the inorganic material or the oligomer which is less than that is not limited and can be changed as many as possible.
- the organic-inorganic coating agent may use a variety of oligomers or synthetic oils, such as silicone oil, ethylene glycol, canola oil, etc., in the case of using water is a process that is usually cooled by the cooling water in the post-process, it is more preferable because no post-treatment to wash .
- the viscosity of the organic / inorganic coating agent exceeds 500 Pa ⁇ s, the viscosity of the organic / inorganic coating agent is generally higher than the polymer melt viscosity, and thus the organic / inorganic coating agent does not flow between the polymer resin melt and the inner circumferential surface of the extrusion die 200 and tends to move to the center of the fluid. Since it exists, the range which is 500 Pa * s or less is preferable.
- the polymer resin continuous extrusion apparatus 1 of the present invention enables continuous extrusion of the polymer resin melt, and enables low-temperature extrusion, thereby preventing degradation of the physical properties of the polymer due to deterioration, and of the extruder 100 By dramatically lowering the pressure, the polymer resin can be continuously extruded.
- the extrusion die 200 may be formed to include a die body 210, a body inserting portion 220, and a neck portion 230.
- the oil was introduced in at least two directions.
- An oil inlet 211 which may be evenly coated on the surface of the polymer resin melt, the structure of which will be described later.
- the die body 210 has the oil inlet 211 is formed on the upper side, it is formed including a through hole 212 penetrates in the flow direction of the polymer resin melt therein.
- the body inserting portion 220 is formed in a cylindrical pipe shape and is inserted and coupled to the through hole 212 of the die body 210.
- the body insertion portion 220 is an oil flow portion formed in the extrusion passage 221 is formed in the longitudinal direction in the longitudinal direction, the radially dug along the outer peripheral surface around the position where the oil inlet 211 is formed.
- FIG. 6 schematically shows a path through which the lubricant injected from the outside flows along the oil flow part 222 and the oil flow hole 223 formed in the body insertion part 220.
- the lubricant flows into the extrusion passage 221 through the oil flow hole 223 along the oil flow part 222 and uniformly coats the surface of the polymer resin melt. It moves with the resin melt.
- the neck portion 230 includes a communication hole 231 formed therein so that the extruder 141 and the extrusion passage 221 of the extruder 100 communicate with each other, one side of the extruder 100 of the extruder 100. It is coupled to 141, the other side is coupled to one end of the body insertion unit 220.
- the polymer resin continuous extrusion device 1 of the present invention is adjacent to one end of the body inserting portion 220 is located on the side where the region in which the oil flow portion 222 is formed is connected to the neck portion 230
- the lubricant may be injected into at least one of the extrusion holes 141, the neck part 230, and the extrusion die 200, as shown in FIG. 1.
- the body insertion portion 220 may be formed with a plurality of the oil inlet 211.
- the oil flow portion 222 is formed is dug along the outer circumferential surface so as to pass through the position where the oil inlet 211 is formed, at least two oil flow holes 223 may be formed.
- the lubricant may further coat the outer circumferential surface of the polymer resin melt.
- the neck portion 230 may further include a connecting portion 232 having a diameter that is gradually narrowed in an area coupled to one end of the body inserting portion 220.
- the extrusion passage 221 is gradually reduced in diameter from the region in which the oil flow hole 223 is formed, so that the region coupled to the neck portion 230 corresponds to the shape of the connecting portion 232, the connection portion ( 232 may be formed in a shape in which a diameter is constantly maintained from a region where the end is located to the other end.
- Polymer resin continuous extrusion device 1 of the present invention by applying heat to the die body 210 so that the body inserting portion 220 coupled with the neck portion 230 is inserted into the die body 210; In the expanded state of the through-hole 212, the body insertion unit 220 may be inserted, and coupled to be fixed by cooling at room temperature or low temperature.
- the polymer resin continuous extrusion apparatus 1 of the present invention may be variously modified in a manner in which the body inserting portion 220, the die body 210, and the neck portion 230 are coupled to each other.
- the polymer resin continuous extrusion apparatus 1 of the present invention may be formed to include an oil pump 400 is inserted into the oil inlet 211 to supply the oil at a predetermined pressure.
- the oil pump 400 may be a gear type gear pump or a plunger type plunger pump.
- the pressure of the oil pump 400 should be greater than or equal to the resin pressure. do.
- the temperature difference between the resin temperature and the lubricant is preferably adjusted to 50 ° C. or less.
- the polymer resin continuous extrusion apparatus 1 of the present invention is filled with lubricant in the groove of the gear by the gear engagement and suction at the suction port of the oil pump 400 and forced.
- a plunger pump it is forcibly conveyed by the reciprocating motion of the plunger.
- the lubricant when the lubricant is filled in the space created by the gear casting and the plate, the lubricant moves along the inner circumference of the casing toward the discharge port, where the lubricant flows by gear meshing, and the stainless steel pipe connected to the discharge port is opened. Accordingly, the oil inlet 211 and the oil flow hole 223 may be flowed into the extrusion die 200.
- the velocity distribution Vz is shown in a flat flow form as shown in FIG. 9, and the diameter of the extrusion passage 221 inside the extrusion die 200 is 3.0.
- the oil absorbs all the frictional force with the wall of the extrusion passage 221 in the state in which a lubricant of about 0.5 mm is coated on the surface of the polymer resin melt, the polymer resin melt coated with the lubricant is extruded at a constant speed. You can see the work going on.
- the polymer resin continuous extrusion apparatus 1 of the present invention can be seen that the shear rate of the polymer resin melt is much smaller than the shear rate of the oil coated on the surface, the conventional extrusion apparatus shown in FIG. This distribution differs greatly from the shear rate distribution at.
- the polymer resin continuous extrusion apparatus (1) of the present invention can evenly spray the organic-inorganic coating material into the extrusion die 200 in the continuous extrusion method of the polymer resin disclosed in the applicant's Korean Patent Publication No. 2011-0110040.
- the invention can be more fully implemented.
- a polymer resin continuous extrusion method is a) a polymer resin or a resin composition containing an additive is added to the extruder 100 step; b) transferring the mixed resin composition melted in the barrel 140 to the extrusion die 200; And, c) the lubricant is injected into the extrusion passage 221 of the extrusion die 200, extruded from the extrusion die 200 extruded from the extrusion die 200 with the surface of the polymer resin melt coated by the lubricant Is prepared; It includes.
- the lubricant is removed after the shape of the extruded body is completed.
- the polymer resin may be a polymer resin alone, or a mixture of one or more polymer blends or polymer resins and additives different in kind. All polymers used in the extrusion process and in other continuous processes can be used.
- the polymer resin may be used as a crystalline polymer, an amorphous polymer or a mixture thereof.
- the crystalline polymers include polyethylene, polypropylene, polyvinyl acetate copolymers, polyester resins, nylon resins, and blends containing polymer resins containing copolymers or organic materials thereof, and amorphous polymer resins. May be polyvinyl chloride, polystyrene, acrylic resin, polycarbonate, ABS, PAN and copolymers or blends thereof.
- the resins referred to as rubber are natural rubber, SBR, BR, CR, IR, IIR, EPDM, thermoplastic rubber such as polyether, silicone rubber and copolymers or blends thereof.
- additives commonly used in the art may be added.
- the additive is usually added in the melt extrusion process, it means an additive used to improve the physical properties of the polymer resin, the type is not limited. Specifically, for example, a blowing agent, a pigment, an organic filler, an inorganic filler, a plasticizer, and the like may be used, but are not limited thereto.
- polypropylene may be used as the polymer resin, and melting temperature (Tm) is 130 to 170 ° C, MI is 0.1 to 50, and specific gravity is 0.8 to 1.0. It is excellent in processability and is suitable for injecting organic-inorganic substances or oligomers. A polymer other than that can also be mixed and workability can be improved.
- the resin composition is melt kneaded during continuous operation in the extruder 100, and in the process, the additive and the polypropylene-based resin are uniformly mixed, wherein the extruder 100 of the extruded screw 130
- the rotational speed is preferably 10 to 50 rpm and the extrusion amount is 0.1 to 0.5 Kg / h.
- the extrusion is continuously performed from a temperature lower than the melting temperature or the glass transition temperature of the polymer resin. It is characteristic in manufacturing. Specifically, the temperature of the die preferably satisfies Expression 1 and Expression 2 below.
- PT is the temperature of the polymer resin in the die
- Tm means the melting temperature of the crystalline polymer resin
- Tg means the glass transition temperature of the amorphous polymer resin.
- the organic-inorganic coating material may be formed at a relatively low temperature, that is, a condition at which the viscosity of the polymer in the die is increased, i.
- the polymer resin melt can be extruded continuously.
- the present invention is capable of continuous extrusion in the range of the temperature Tm-60 ° C. to Tm + 300 ° C. and the range of Tg-10 ° C. to Tg + 350 ° C. where the high viscosity of the polymer resin melt is expected.
- the present inventors have studied to solve the above problems, and as a result of injecting a low viscosity organic-inorganic coating material into the die, the viscosity of the polymer resin is very high, or the temperature is below or near the melting temperature of the polymer resin. Extrusion through a new method of coating the lubricant solves this problem and surprisingly finds that the polymer molded body can be extruded from a high viscosity melt at low temperatures to complete the present invention.
- the polymer resin continuous extrusion device 1 of the present invention is capable of extruding at a temperature near or below the transition temperature of the polymer resin, and also capable of extruding a polymer resin melt having a very high viscosity.
- the polymer resin continuous extrusion apparatus 1 of the present invention does not necessarily maintain the resin temperature in the extruder 100 above the melting temperature, so that the physical properties of the final extrudate can be improved, and the critical parameters of the final extrudate form
- the advantage is that the die shape can be varied by reducing the in die swell.
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Abstract
Description
Claims (8)
- 연속적으로 고분자수지 용융체를 흐름방향과 나란한 방향으로 압출하는 연속압출장치(1)에 있어서,일측에 호퍼(110)가 구비되며 타측 단부에 압출구(141)를 갖는 배럴(140)과, 상기 배럴(140)의 내부에 회전축을 중심으로 회전가능하게 설치되는 압출스크류(130)를 포함하는 압출기(100);상기 압출기(100)와 연결되어 상기 압출기(100)로부터 고분자수지 용융체가 유입되며, 내부에 관통 형성된 압출통로(221)를 통과하여 노즐부(300)로 배출되도록 하는 압출다이(200); 를 포함하며,상기 압출다이(200)에 형성된 오일주입구(211)를 통해 주입되는 윤활제가 상기 압출통로(221)의 내부에 유동되는 고분자수지 용융체의 표면을 코팅하며 이동되는 것을 특징으로 하는 고분자수지 연속압출장치.
- 제 1항에 있어서,상기 압출다이(200)는상기 오일주입구(211)가 일측에 형성되며, 내부에 고분자수지 용융체의 흐름방향으로 관통되는 관통홀(212)을 포함하여 형성되는 다이몸체(210);원통형의 파이프 형태로 형성되어 상기 다이몸체(210)의 상기 관통홀(212)에 삽입 결합되며, 내부에 상기 압출통로(221)가 형성되고, 상기 오일주입구(211)가 형성되는 위치를 중심으로 외주면 일정영역에 방사방향으로 파여져 형성되는 오일유동부(222)를 포함하며, 상기 오일유동부(222)의 양측 단부가 중공되어 상기 압출통로(221) 내부로 오일이 유동되도록 형성되는 오일유동홀(223)을 포함하는 몸체삽입부(220);상기 압출기(100)의 압출구(141) 및 압출통로(221)가 연통되도록 내부에 관통 형성되는 연통홀(231)을 포함하며, 일측이 상기 압출기(100)의 압출구(141)에 결합되고, 타측이 상기 몸체삽입부(220)의 일측 단부에 결합되는 넥부(230); 를 포함하여 형성되는 것을 특징으로 하는 고분자수지 연속압출장치.
- 제 2항에 있어서,상기 고분자수지 연속압출장치(1)는상기 오일유동부(222)가 상기 넥부(230)와 연결되는 측에 위치한 상기 몸체삽입부(220)의 일측 단부에 인접하여 형성되는 것을 특징으로 하는 고분자수지 연속압출장치.
- 제 2항에 있어서,상기 몸체삽입부(220)는상기 오일주입구(211)가 복수개 형성되는 것을 특징으로 하는 고분자수지 연속압출장치.
- 제 4항에 있어서,상기 고분자수지 연속압출장치(1)는상기 오일유동부(222)가 상기 오일주입구(211)가 형성되는 위치를 지나가도록 외주면을 따라 파여져 형성되며,상기 오일유동홀(223)이 적어도 2개 이상 형성되는 것을 특징으로 하는 고분자수지 연속압출장치.
- 제 2항에 있어서,상기 고분자수지 연속압출장치(1)는상기 오일주입구(211)에 삽입 결합되어 오일을 일정 압력으로 공급하는 오일펌프(400)를 포함하여 형성되는 것을 특징으로 하는 고분자수지 연속압출장치.
- 제 6항에 있어서,상기 오일펌프(400)는기어펌프 또는 플런저펌프인 것을 특징으로 하는 고분자수지 연속압출장치.
- 제 1항에 있어서,상기 윤활제는물, 실리콘오일, 에틸렌글리콜, 카놀라유, 올리고머 또는 합성오일인인 것을 특징으로 하는 고분자수지 연속압출장치.
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DE112012002898.8T DE112012002898T5 (de) | 2012-10-05 | 2012-11-07 | Vorrichtung zum kontinuierlichen Extrudieren eines Polymerharzes |
US14/001,921 US20140099393A1 (en) | 2012-10-05 | 2012-11-07 | Apparatus for continuously extruding polymer resin |
CN201280010954.XA CN104023939A (zh) | 2012-10-05 | 2012-11-07 | 高分子树脂连续挤出装置 |
JP2015535551A JP2015530297A (ja) | 2012-10-05 | 2012-11-07 | 高分子樹脂連続圧出装置 |
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Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR950002796B1 (ko) * | 1991-05-13 | 1995-03-27 | 젠코프 인코포레이티드 | 압출물의 코팅방법 및 코팅장치 |
US20020075756A1 (en) * | 2000-10-05 | 2002-06-20 | Horst Finder | Apparatus for premixing additives and feeding them into a polymer stream |
JP2009006362A (ja) * | 2007-06-28 | 2009-01-15 | Sumitomo Electric Ind Ltd | 粉末成形用金型 |
WO2011122870A2 (ko) * | 2010-03-31 | 2011-10-06 | 충남대학교산학협력단 | 고분자수지의 연속 압출방법 |
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KR100843609B1 (ko) | 2006-03-09 | 2008-07-03 | 주식회사 엘지화학 | 비상용성 고분자수지 압출장치 |
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2012
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- 2012-11-07 JP JP2015535551A patent/JP2015530297A/ja active Pending
- 2012-11-07 WO PCT/KR2012/009295 patent/WO2014054829A1/ko active Application Filing
- 2012-11-07 DE DE112012002898.8T patent/DE112012002898T5/de not_active Withdrawn
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Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
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KR950002796B1 (ko) * | 1991-05-13 | 1995-03-27 | 젠코프 인코포레이티드 | 압출물의 코팅방법 및 코팅장치 |
US20020075756A1 (en) * | 2000-10-05 | 2002-06-20 | Horst Finder | Apparatus for premixing additives and feeding them into a polymer stream |
JP2009006362A (ja) * | 2007-06-28 | 2009-01-15 | Sumitomo Electric Ind Ltd | 粉末成形用金型 |
WO2011122870A2 (ko) * | 2010-03-31 | 2011-10-06 | 충남대학교산학협력단 | 고분자수지의 연속 압출방법 |
Cited By (1)
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NO347874B1 (en) * | 2022-09-23 | 2024-04-22 | Norsk Hydro As | Apparatus and a method for continuous extrusion of materials with high viscosity |
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JP2015530297A (ja) | 2015-10-15 |
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DE112012002898T5 (de) | 2014-08-28 |
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