CN111057295A - Foaming master batch and preparation method thereof - Google Patents
Foaming master batch and preparation method thereof Download PDFInfo
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- CN111057295A CN111057295A CN201911169561.3A CN201911169561A CN111057295A CN 111057295 A CN111057295 A CN 111057295A CN 201911169561 A CN201911169561 A CN 201911169561A CN 111057295 A CN111057295 A CN 111057295A
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- polyisobutylene
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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
- C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
- C08J9/06—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
- C08J9/08—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing carbon dioxide
-
- 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
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/20—Compounding polymers with additives, e.g. colouring
- C08J3/22—Compounding polymers with additives, e.g. colouring using masterbatch techniques
- C08J3/226—Compounding polymers with additives, e.g. colouring using masterbatch techniques using a polymer as a carrier
-
- 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
- C08J9/0014—Use of organic additives
- C08J9/0023—Use of organic additives containing oxygen
-
- 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
- C08J9/0014—Use of organic additives
- C08J9/0033—Use of organic additives containing sulfur
-
- 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
- C08J9/0014—Use of organic additives
- C08J9/0042—Use of organic additives containing silicon
-
- 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
- C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
- C08J9/06—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent
- C08J9/10—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a chemical blowing agent developing nitrogen, the blowing agent being a compound containing a nitrogen-to-nitrogen bond
- C08J9/102—Azo-compounds
-
- 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
- C08J2203/00—Foams characterized by the expanding agent
- C08J2203/02—CO2-releasing, e.g. NaHCO3 and citric acid
-
- 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
- C08J2203/00—Foams characterized by the expanding agent
- C08J2203/04—N2 releasing, ex azodicarbonamide or nitroso compound
-
- 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
- C08J2203/00—Foams characterized by the expanding agent
- C08J2203/18—Binary blends of expanding agents
-
- 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
- C08J2423/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2423/02—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
- C08J2423/04—Homopolymers or copolymers of ethene
- C08J2423/08—Copolymers of ethene
-
- 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
- C08J2423/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
- C08J2423/02—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
- C08J2423/18—Homopolymers or copolymers of hydrocarbons having four or more carbon atoms
- C08J2423/20—Homopolymers or copolymers of hydrocarbons having four or more carbon atoms having four to nine carbon atoms
-
- 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
- C08K5/04—Oxygen-containing compounds
- C08K5/09—Carboxylic acids; Metal salts thereof; Anhydrides thereof
-
- 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
- C08K5/45—Heterocyclic compounds having sulfur in the ring
- C08K5/46—Heterocyclic compounds having sulfur in the ring with oxygen or nitrogen in the ring
-
- 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
- C08K5/54—Silicon-containing compounds
Abstract
The invention discloses a foaming master batch and a preparation method thereof, comprising the following steps: cutting polyisobutylene into small pieces of polyisobutylene; stirring and uniformly mixing 4.5-10.5% of polyisobutylene, 15-35% of inorganic foaming agent, 12-24% of organic foaming agent, 0.1-2.5% of antioxidant, 1-3% of coupling agent, 2-5% of stearic acid and POE 20-40% at the temperature of below 90 ℃ to obtain a mixture; and step three, adding the mixture into a double-screw extruder, extruding, cooling and granulating to obtain the foaming master batch. The total specific gravity of the organic foaming agent and the inorganic foaming agent in the master batch can be increased to more than 50 percent, the variety of the used raw materials is very small, the production flow is short, the operation is simple, and the small molecular precipitate is not generated, so that the master batch can be used for enhancing and modifying the resins such as polyolefin and the like with low VOC and low volatility.
Description
Technical Field
The invention relates to the field of chemical industry, and particularly relates to a foaming master batch and a preparation method thereof.
Background
The foaming process produces dust flying during direct use, which pollutes the environment and damages health. Meanwhile, the foaming is directly mixed in the resin matrix, and the reinforcing effect of the foaming on the resin cannot be fully exerted due to factors such as uneven dispersion, poor interface bonding and the like. These all affect the use of foaming.
Therefore, the foaming is usually carried out by banburying and granulating in advance. In order to further improve the proportion of the foaming components in the master batch, reduce the use of other additives and improve the cost performance of the foaming master batch, the patent provides the foaming master batch taking polyisobutylene as a carrier.
Disclosure of Invention
The invention aims to overcome the defects of the prior art, and the master batch of the invention has the advantages that the total specific gravity of the organic foaming agent and the inorganic foaming agent can be increased to more than 50 percent, the variety of the used raw materials is very small, the production flow is short, the operation is simple, no micromolecule precipitate exists, and the master batch can be used for enhancing and modifying the resins such as polyolefin with low VOC and low volatility.
In order to achieve the purpose, the technical scheme adopted by the invention is as follows:
a foaming master batch comprises 4.5-10.5% of polyisobutylene, 15-35% of an inorganic foaming agent, 12-24% of an organic foaming agent, 0.1-2.5% of an antioxidant, 1-3% of a coupling agent, 2-5% of stearic acid and 2-40% of POE 20.
In a further improvement, the molecular weight of the polyisobutylene is 20000-65000.
In a further improvement, the inorganic foaming agent is sodium bicarbonate.
In a further improvement, the organic blowing agent is 2, 2' -azobisisobutyronitrile.
In a further improvement, the antioxidant is alkyl phenothiazine, and the coupling agent is a silane coupling agent.
A method for preparing foaming master batches comprises the following steps:
cutting polyisobutylene into small pieces of polyisobutylene;
stirring and uniformly mixing 4.5-10.5% of polyisobutylene, 15-35% of inorganic foaming agent, 12-24% of organic foaming agent, 0.1-2.5% of antioxidant, 1-3% of coupling agent, 2-5% of stearic acid and POE 20-40% at the temperature of below 90 ℃ to obtain a mixture;
and step three, adding the mixture into a double-screw extruder, extruding, cooling and granulating to obtain the foaming master batch.
The further improvement is that in the third step, the extrusion temperature is controlled to be 90-100 ℃; and cooling the extruded material strips by air at room temperature, and granulating after shaping.
In the step one, polyisobutylene in an indefinite form is put into a tablet machine, and is extruded into tablets and then cut into small polyisobutylene pieces with the thickness of 1mm and the area of less than or equal to 1cm 2.
Detailed Description
The manufacturing process of the invention is as follows:
1. placing polyisobutylene in indefinite form into a tablet machine, extruding into pieces, and cutting into small pieces with thickness of 1mm and area of 1cm 2; or heating to about 80 deg.C to molten state, and adding into internal mixer or high-speed mixer;
2. mixing the polyisobutylene flakes with auxiliary agents such as foaming agent, adding into a high-speed stirrer, heating to 70 ℃, and keeping stirring for 15 min;
3. putting the stirred and mixed raw materials into a double-screw extruder, and controlling the extrusion temperature to be about 90-100 ℃; and cooling the extruded material strips by air at room temperature, and granulating after shaping.
Example 1
A method for preparing foaming master batches comprises the following steps:
firstly, cutting the polyisobutylene with an indefinite form into small polyisobutylene blocks after passing through a tablet press;
step two, stirring and uniformly mixing 10.5% of polyisobutylene, 35% of inorganic foaming agent, 24% of organic foaming agent, 2.5% of antioxidant, 3% of coupling agent, 5% of stearic acid and POE 20% at the temperature of below 90 ℃ to obtain a mixture;
and step three, adding the mixture into a double-screw extruder, extruding, cooling and granulating to obtain the foaming master batch.
Example 2
A method for preparing foaming master batches comprises the following steps:
firstly, cutting the polyisobutylene with an indefinite form into small polyisobutylene blocks after passing through a tablet press;
step two, stirring and uniformly mixing 10.5% of polyisobutylene, 15% of inorganic foaming agent, 24% of organic foaming agent, 2.5% of antioxidant, 3% of coupling agent, 5% of stearic acid and POE 40% by weight at the temperature of below 90 ℃ to obtain a mixture;
and step three, adding the mixture into a double-screw extruder, extruding, cooling and granulating to obtain the foaming master batch.
Example 3
A method for preparing foaming master batches comprises the following steps:
firstly, cutting the polyisobutylene with an indefinite form into small polyisobutylene blocks after passing through a tablet press;
stirring and uniformly mixing 8% of polyisobutylene, 28% of inorganic foaming agent, 22% of organic foaming agent, 0.1% of antioxidant, 1% of coupling agent, 2% of stearic acid and 38.9% of POE at the temperature of below 90 ℃ to obtain a mixture;
and step three, adding the mixture into a double-screw extruder, extruding, cooling and granulating to obtain the foaming master batch.
Example 4
A method for preparing foaming master batches comprises the following steps:
firstly, cutting the polyisobutylene with an indefinite form into small polyisobutylene blocks after passing through a tablet press;
stirring and uniformly mixing 8% of polyisobutylene, 31% of inorganic foaming agent, 21% of organic foaming agent, 0.5% of antioxidant, 2% of coupling agent, 3% of stearic acid and 34.5% of POE at the temperature of below 90 ℃ to obtain a mixture;
and step three, adding the mixture into a double-screw extruder, extruding, cooling and granulating to obtain the foaming master batch.
The properties of the four products described above are as follows:
thus, example 4 is the preferred example, and the blowing agent loading is greatly increased while product performance is maintained.
The above examples are merely preferred examples and are not intended to limit the embodiments of the present invention.
Claims (8)
1. The foaming master batch is characterized by comprising 4.5-10.5% of polyisobutylene, 15-35% of an inorganic foaming agent, 12-24% of an organic foaming agent, 0.1-2.5% of an antioxidant, 1-3% of a coupling agent, 2-5% of stearic acid and 2-40% of POE 20.
2. The foaming concentrate of claim 1, wherein the polyisobutylene has a molecular weight of 20000-.
3. The foaming concentrate of claim 1, wherein the inorganic foaming agent is sodium bicarbonate.
4. The foaming concentrate of claim 1, wherein the organic blowing agent is 2, 2' -azobisisobutyronitrile.
5. The foamed masterbatch of claim 1 wherein said antioxidant is an alkyl phenothiazine and said coupling agent is a silane coupling agent.
6. The preparation method of the foaming master batch is characterized by comprising the following steps:
cutting polyisobutylene into small pieces of polyisobutylene;
stirring and uniformly mixing 4.5-10.5% of polyisobutylene, 15-35% of inorganic foaming agent, 12-24% of organic foaming agent, 0.1-2.5% of antioxidant, 1-3% of coupling agent, 2-5% of stearic acid and POE 20-40% at the temperature of below 90 ℃ to obtain a mixture;
and step three, adding the mixture into a double-screw extruder, extruding, cooling and granulating to obtain the foaming master batch.
7. The method for preparing the foaming masterbatch of claim 6, wherein in the third step, the extrusion temperature is controlled to be 90-100 ℃; and cooling the extruded material strips by air at room temperature, and granulating after shaping.
8. The method for preparing the foaming concentrate as set forth in claim 6, wherein in the first step, the irregularly shaped polyisobutylene is put into a tablet machine, and is extruded into a sheet and then cut into small pieces of polyisobutylene having a thickness of 1mm and an area of 1cm or less 2.
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CN201911169561.3A CN111057295A (en) | 2019-11-25 | 2019-11-25 | Foaming master batch and preparation method thereof |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114262451A (en) * | 2021-11-30 | 2022-04-01 | 上海金发科技发展有限公司 | Foaming agent master batch material and preparation method and application thereof |
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US5965628A (en) * | 1998-12-23 | 1999-10-12 | Dow Corning Corporation | Low density hydrocarbon polymer foam |
CN101245159A (en) * | 2008-03-28 | 2008-08-20 | 天津市润达塑料包装有限公司 | Process for manufacturing polyolefin foaming particle material |
CN104341688A (en) * | 2013-07-25 | 2015-02-11 | 上海英科实业有限公司 | Foam master batch for microcellular polystyrene foam material, and its preparation method |
CN106883490A (en) * | 2017-03-21 | 2017-06-23 | 合肥华凌股份有限公司 | Fretting map master batch and preparation method thereof and refrigerator foaming plate |
CN106977760A (en) * | 2017-04-20 | 2017-07-25 | 苏州固德新材科技有限公司 | Super soft high resilience resin foamed material and preparation method thereof |
CN107337840A (en) * | 2017-08-23 | 2017-11-10 | 山东昊智新型材料科技有限公司 | A kind of foaming concentrate for expandable polypropylene resin and preparation method thereof |
CN109370039A (en) * | 2018-10-15 | 2019-02-22 | 佛山市南海区承欣塑料助剂有限公司 | A kind of thickening master batch and preparation method thereof |
-
2019
- 2019-11-25 CN CN201911169561.3A patent/CN111057295A/en active Pending
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CN106883490A (en) * | 2017-03-21 | 2017-06-23 | 合肥华凌股份有限公司 | Fretting map master batch and preparation method thereof and refrigerator foaming plate |
CN106977760A (en) * | 2017-04-20 | 2017-07-25 | 苏州固德新材科技有限公司 | Super soft high resilience resin foamed material and preparation method thereof |
CN107337840A (en) * | 2017-08-23 | 2017-11-10 | 山东昊智新型材料科技有限公司 | A kind of foaming concentrate for expandable polypropylene resin and preparation method thereof |
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Non-Patent Citations (1)
Title |
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吴其晔 等: "《高分子材料流变学导论》", 30 June 1994, 冶金工业出版社, pages: 255 - 259 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114262451A (en) * | 2021-11-30 | 2022-04-01 | 上海金发科技发展有限公司 | Foaming agent master batch material and preparation method and application thereof |
CN114262451B (en) * | 2021-11-30 | 2024-03-15 | 上海金发科技发展有限公司 | Foaming agent master batch material and preparation method and application thereof |
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