CN112409684A - Processing method of high-strength toy plastic - Google Patents
Processing method of high-strength toy plastic Download PDFInfo
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- CN112409684A CN112409684A CN202011207820.XA CN202011207820A CN112409684A CN 112409684 A CN112409684 A CN 112409684A CN 202011207820 A CN202011207820 A CN 202011207820A CN 112409684 A CN112409684 A CN 112409684A
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/30—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof by mixing gases into liquid compositions or plastisols, e.g. frothing with air
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
- C08J2323/10—Homopolymers or copolymers of propene
- C08J2323/12—Polypropene
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2491/00—Characterised by the use of oils, fats or waxes; Derivatives thereof
- C08J2491/06—Waxes
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K13/00—Use of mixtures of ingredients not covered by one single of the preceding main groups, each of these compounds being essential
- C08K13/02—Organic and inorganic ingredients
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/30—Sulfur-, selenium- or tellurium-containing compounds
- C08K2003/3045—Sulfates
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/32—Phosphorus-containing compounds
- C08K2003/321—Phosphates
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/34—Silicon-containing compounds
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/36—Sulfur-, selenium-, or tellurium-containing compounds
- C08K5/41—Compounds containing sulfur bound to oxygen
- C08K5/42—Sulfonic acids; Derivatives thereof
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- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Injection Moulding Of Plastics Or The Like (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
The invention discloses a processing method of high-strength toy plastic, which comprises the following steps: firstly, adding polypropylene, sodium alkyl benzene sulfonate and water into a stirrer, uniformly mixing and stirring to obtain an A-phase mixture, then adding paraffin oil into the A-phase mixture, and then adding a C-phase auxiliary material, wherein the C-phase auxiliary material comprises an anionic surfactant, a nonionic surfactant, high-efficiency whitening and stain removing ions, a buffering agent and spice; then adding phosphate, silicate, anhydrous sodium sulphate and enzyme to obtain an E-phase mixture; and finally, putting the mixture into an injection molding machine for high-temperature high-pressure melting extrusion molding to obtain the high-performance plastic. Through adding C looks auxiliary material in the processing material, can promote plastics material's foaming effect and sclerosis effect simultaneously, not only can reduce plastics product's density, reduce the weight of product, can promote plastics product's hardness moreover, promote the intensity of product, be favorable to prolonging the life of product.
Description
Technical Field
The invention belongs to the technical field of high-performance plastic preparation, and particularly relates to a processing method of high-strength toy plastic.
Background
In the processing process of the plastic product, the hardness of the plastic product with good foaming effect is generally lower, and the foaming effect of the plastic product with high strength and high hardness is generally poorer in the foaming process, so that the density of the product is higher, the foaming effect and the hardness can not be taken into consideration, and the plastic product can not meet the material requirement of the existing high-performance toy.
Disclosure of Invention
The present invention has been made to solve the above problems, and an object of the present invention is to provide a method for processing a high-strength toy plastic, which can be used by a high-performance plastic processor to process high-performance plastic products having a low density and a high hardness, and can be widely applied to the fields of high-end toy manufacturing, consumer goods processing, and the like.
The processing technology of the high-performance plastic comprises the following steps:
s1, polypropylene, sodium alkyl benzene sulfonate and water in a mass ratio of 250: (0.8-1.2): (0.8-1.2) adding the mixture into a stirrer, and uniformly mixing and stirring to obtain an A-phase mixture;
s2, adding paraffin oil into the phase A mixture, and uniformly stirring to obtain a phase B mixture, wherein the mass of the paraffin oil is 0.01-0.02 times of that of the polypropylene;
s3, adding a C-phase auxiliary material into the B-phase mixture to obtain a D-phase mixture, wherein the mass of the C-phase auxiliary material is 0.02-0.04 times that of the polypropylene, and the C-phase auxiliary material comprises an anionic surfactant, a nonionic surfactant, high-efficiency whitening and stain removing ions, a buffering agent and a spice;
s4, adding phosphate, silicate, anhydrous sodium sulphate and enzyme into the D-phase mixture to obtain an E-phase mixture;
s5, putting the E-phase mixture into an injection molding machine, and performing high-temperature high-pressure melt extrusion molding to obtain the high-performance plastic, wherein the working temperature of the injection molding machine is 185-250 ℃, and the pressure is 12-14 MPa.
According to some specific embodiments of the present invention, in the step S1, the polypropylene, the sodium alkyl benzene sulfonate and the water are mixed in a mass ratio of 250: 1: 1.
according to some embodiments of the invention, in the step S2, the paraffin oil has a mass of 0.015 times that of the polypropylene.
According to some embodiments of the present invention, in step S3, the mass of the phase C auxiliary material is 0.03 times of the mass of the polypropylene.
According to some embodiments of the present invention, in step S5, the injection molding machine is operated at 220 ℃ and 13 MPa.
According to the processing technology of the high-performance plastic disclosed by the embodiment of the invention, the anionic surfactant, the nonionic surfactant, the high-efficiency whitening and stain removing ions, the buffering agent and the spice are added into the processing material, so that the foaming effect and the hardening effect of the plastic material can be simultaneously improved, the density of the plastic product can be reduced, the weight of the product can be reduced, the hardness of the plastic product can be improved, the strength of the product is improved, and the service life of the product can be prolonged.
Drawings
FIG. 1 is a flow chart of a process for processing high performance plastics according to an embodiment of the present invention.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
The processing of high performance plastics according to an embodiment of the invention is described below with reference to fig. 1, comprising the following steps:
s1, polypropylene, sodium alkyl benzene sulfonate and water in a mass ratio of 250: (0.8-1.2): (0.8-1.2) adding the mixture into a stirrer, and uniformly mixing and stirring to obtain an A-phase mixture;
s2, adding paraffin oil into the phase A mixture, and uniformly stirring to obtain a phase B mixture, wherein the mass of the paraffin oil is 0.01-0.02 times of that of the polypropylene;
s3, adding a C-phase auxiliary material into the B-phase mixture to obtain a D-phase mixture, wherein the mass of the C-phase auxiliary material is 0.02-0.04 times that of the polypropylene, and the C-phase auxiliary material comprises an anionic surfactant, a nonionic surfactant, high-efficiency whitening and stain removing ions, a buffering agent and a spice;
s4, adding phosphate, silicate, anhydrous sodium sulphate and enzyme into the D-phase mixture to obtain an E-phase mixture;
s5, putting the E-phase mixture into an injection molding machine, and performing high-temperature high-pressure melt extrusion molding to obtain the high-performance plastic, wherein the working temperature of the injection molding machine is 185-250 ℃, and the pressure is 12-14 MPa.
According to the processing technology of the high-performance plastic disclosed by the embodiment of the invention, the anionic surfactant, the nonionic surfactant, the high-efficiency whitening and stain removing ions, the buffering agent and the spice are added into the processing material, so that the foaming effect and the hardening effect of the plastic material can be simultaneously improved, the density of the plastic product can be reduced, the weight of the product can be reduced, the hardness of the plastic product can be improved, the strength of the product can be improved, the service life of the product can be prolonged, and the processing technology can be widely applied to the fields of high-end toy manufacturing, living goods processing and the like.
According to some specific embodiments of the present invention, in the step S1, the polypropylene, the sodium alkyl benzene sulfonate and the water are mixed in a mass ratio of 250: 1: 1, the proportion is convenient for material preparation, and the produced plastic product has better quality.
According to some embodiments of the present invention, in the step S2, the mass of the paraffin oil is 0.015 times of the mass of the polypropylene, and the addition of the paraffin oil 0.015 times of the mass of the polypropylene can ensure that various active agents and ions in the phase C auxiliary material are bonded to the foamed main material, thereby improving the foaming effect and the hardening effect of the plastic.
According to some embodiments of the present invention, in step S3, the mass of the phase C auxiliary material is 0.03 times that of the polypropylene, and the addition of the phase C auxiliary material in an amount 0.03 times that of the polypropylene can improve the performance of the melted material to the greatest extent, so as to improve the quality of the product after extrusion molding.
According to some embodiments of the present invention, in step S5, the operating temperature of the injection molding machine is 220 ℃, the pressure is 13MPa, the operating temperature of the injection molding machine is controlled to be about 220 ℃, and the pressure is controlled to be about 13MPa, so that the plastic ball product obtained by processing has the best performance, and the weight reduction and hardness of the plastic ball are optimized to the greatest extent.
It will be evident to those skilled in the art that the invention is not limited to the details of the foregoing illustrative embodiments, and that the present invention may be embodied in other specific forms without departing from the spirit or essential attributes thereof. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Furthermore, it should be understood that although the present description refers to embodiments, not every embodiment may contain only a single embodiment, and such description is for clarity only, and those skilled in the art should integrate the description, and the embodiments may be combined as appropriate to form other embodiments understood by those skilled in the art.
Claims (5)
1. A processing method of high-strength toy plastic is characterized by comprising the following steps:
s1, polypropylene, sodium alkyl benzene sulfonate and water in a mass ratio of 250: (0.8-1.2): (0.8-1.2) adding the mixture into a stirrer, and uniformly mixing and stirring to obtain an A-phase mixture;
s2, adding paraffin oil into the phase A mixture, and uniformly stirring to obtain a phase B mixture, wherein the mass of the paraffin oil is 0.01-0.02 times of that of the polypropylene;
s3, adding a C-phase auxiliary material into the B-phase mixture to obtain a D-phase mixture, wherein the mass of the C-phase auxiliary material is 0.02-0.04 times that of the polypropylene, and the C-phase auxiliary material comprises an anionic surfactant, a nonionic surfactant, high-efficiency whitening and stain removing ions, a buffering agent and a spice;
s4, adding phosphate, silicate, anhydrous sodium sulphate and enzyme into the D-phase mixture to obtain an E-phase mixture;
s5, putting the E-phase mixture into an injection molding machine, and performing high-temperature high-pressure melt extrusion molding to obtain the high-performance plastic, wherein the working temperature of the injection molding machine is 185-250 ℃, and the pressure is 12-14 MPa.
2. The method for processing high-strength toy plastic according to claim 1, wherein the method comprises the following steps: in the step S1, the polypropylene, the sodium alkyl benzene sulfonate and the water are mixed according to a mass ratio of 250: 1: 1.
3. the processing method of high-strength toy plastic according to claim 2, wherein the processing method comprises the following steps: in the step S2, the paraffin oil has a mass of 0.015 times the mass of the polypropylene.
4. A method for processing a high strength toy plastic according to claim 3, wherein: in step S3, the mass of the phase C auxiliary material is 0.03 times the mass of the polypropylene.
5. The processing method of high-strength toy plastic according to claim 4, wherein the processing method comprises the following steps: in the step S5, the operating temperature of the injection molding machine is 220 ℃ and the pressure is 13 MPa.
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| CN202011207820.XA CN112409684A (en) | 2020-11-03 | 2020-11-03 | Processing method of high-strength toy plastic |
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| CN202011207820.XA CN112409684A (en) | 2020-11-03 | 2020-11-03 | Processing method of high-strength toy plastic |
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