CN116199602A - Preparation process and application of high-temperature environment-friendly foaming agent barium azodicarbonate - Google Patents

Preparation process and application of high-temperature environment-friendly foaming agent barium azodicarbonate Download PDF

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CN116199602A
CN116199602A CN202310216801.0A CN202310216801A CN116199602A CN 116199602 A CN116199602 A CN 116199602A CN 202310216801 A CN202310216801 A CN 202310216801A CN 116199602 A CN116199602 A CN 116199602A
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azodicarbonate
barium
foaming
composite composition
foamable
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谢南生
刘鑫
罗李华
王圣
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Zhejiang Jieshangjie New Material Co ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C281/00Derivatives of carbonic acid containing functional groups covered by groups C07C269/00 - C07C279/00 in which at least one nitrogen atom of these functional groups is further bound to another nitrogen atom not being part of a nitro or nitroso group
    • C07C281/20Derivatives of carbonic acid containing functional groups covered by groups C07C269/00 - C07C279/00 in which at least one nitrogen atom of these functional groups is further bound to another nitrogen atom not being part of a nitro or nitroso group the two nitrogen atoms of the functional groups being doubly-bound to each other, e.g. azoformamide
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/06Working-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
    • C08J9/10Working-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
    • C08J9/102Azo-compounds
    • C08J9/103Azodicarbonamide
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2203/00Foams characterized by the expanding agent
    • C08J2203/04N2 releasing, ex azodicarbonamide or nitroso compound
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2367/00Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • C08J2367/02Polyesters derived from dicarboxylic acids and dihydroxy compounds
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2377/00Characterised by the use of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2423/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2423/02Characterised 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
    • C08J2423/04Homopolymers or copolymers of ethene
    • C08J2423/06Polyethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2423/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2423/02Characterised 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
    • C08J2423/04Homopolymers or copolymers of ethene
    • C08J2423/08Copolymers of ethene

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  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
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  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

The invention belongs to the technical field of foaming agents, and particularly relates to a preparation process of a high-temperature environment-friendly (decomposition product is free of ammonia gas and formamide) foaming agent barium azodicarbonate and application of the foaming agent barium azodicarbonate in engineering plastics. The preparation process comprises the following steps: s1: taking azodicarbonamide and barium hydroxide as raw materials, taking water as a solvent, and catalyzing by inorganic strong alkali to hydrolyze the azodicarbonamide and then directly salify; s2: after the reaction in the step S1 is finished, the generated barium azodicarbonate is separated out and is deposited in an aqueous solution, and then the barium azodicarbonate is separated out by filtration; s3: and drying the separated barium azodicarbonate to obtain the target product. The process has the advantages of one-step synthesis, water as solvent, safety, environmental protection, high yield, simple operation and convenient and easily obtained raw materials. The barium azodicarbonate can be suitable for foaming nylon compounds (PA 6, PA66, PA610, PA612 and the like) and polyester compounds (PET, PBT and the like), and can be expanded into other high-performance plastic foaming materials processed at high temperature.

Description

Preparation process and application of high-temperature environment-friendly foaming agent barium azodicarbonate
Technical Field
The invention belongs to the technical field of foaming agents, and particularly relates to a preparation process of a high-temperature environment-friendly (decomposition product is free of ammonia gas and formamide) foaming agent barium azodicarbonate and application of the foaming agent barium azodicarbonate in engineering plastics.
Background
Blowing agents refer to a class of additives that are capable of forming a cellular structure in a plastic, i.e., to be added to make a foam. They can generate a large amount of gas under specific conditions, and the formed porous structure material containing continuous or discontinuous air holes (i.e. open holes or closed holes) and making the plastic form gas-solid phase combination can reduce the density and hardness of the plastic or enhance the sound insulation and heat insulation of the plastic.
The chemical foaming agents commonly used in the market at present are mainly divided into exothermic foaming agents and endothermic foaming agents.
Exothermic blowing agents are mainly of the three main classes azo, nitroso and sulfonyl hydrazides, however none of these blowing agents have a rise temperature of more than 250 ℃. Among them, azodicarbonamide (ADC) foaming agents, which are most widely used, have a starting temperature of 190-210 ℃ and have a large gas generation amount, but decomposition products have toxic substances such as ammonia, formamide, etc., so that the non-environmental protection is a fatal weakness.
For the foaming agent of heat-absorbing baking soda and citric acid, although the environment-friendly nontoxic harmful gas is generated, the gas generation amount is smaller, and the decomposition product is mainly carbon dioxide, but the initiation temperature is lower.
For foaming of engineering plastics with high melting point (melting point greater than 220 ℃) it is necessary to select a chemical foaming agent with a high foaming temperature (preferably a foaming temperature above 250 ℃) so that the foaming process can be matched with the melt processing process of the engineering plastics. Therefore, the two common exothermic and endothermic chemical foaming agents are not suitable for foaming high-melting-point high polymer materials such as engineering plastic foaming and the like, and the chemical foaming agents are limited to be applied to high ends such as automobile weight reduction, aerospace weight reduction, engineering plastic modification, special military industry and the like.
Disclosure of Invention
The invention aims to provide a preparation process and application of a high-temperature environment-friendly (decomposition product is ammonia-free and formamide-free) foaming agent barium azodicarbonate, so as to solve the problems in the prior art.
In order to achieve the above purpose, the present invention provides the following technical solutions:
in one aspect, a preparation process of a high-temperature environment-friendly foaming agent barium azodicarbonate is provided, which comprises the following steps:
s1: taking azodicarbonamide and barium hydroxide as raw materials, taking water as a solvent, and catalyzing by inorganic strong alkali to hydrolyze the azodicarbonamide and then directly salify;
s2: after the reaction in the step S1 is finished, the generated barium azodicarbonate is separated out and is deposited in an aqueous solution, and then the barium azodicarbonate is separated out by filtration;
s3: drying the separated barium azodicarbonate to obtain a target product;
the chemical reaction equation in step S1 is:
Figure BDA0004115262700000021
in the above embodiment, in step S1, after azodicarbonamide is left at 0.5% or less, the reaction is completed.
The reaction temperature in the step s1 is-10 ℃ to 20 ℃.
The drying temperature in the step S3 is 10-70 ℃.
The inorganic strong base in the step S1 is one or more of sodium hydroxide, potassium hydroxide and lithium hydroxide.
In a second aspect, a foamed nylon composite composition is provided, comprising the following components in percentage by weight:
Figure BDA0004115262700000022
Figure BDA0004115262700000031
in a third aspect, there is also provided a foamable thermoplastic polyester composite composition consisting of the following components in weight percent:
Figure BDA0004115262700000032
in a fourth aspect, there is provided a method for preparing the foamable composition described above, the foamable composition being foamed by injection molding, wherein secondary opening is required for foaming, and the secondary opening is at a distance of 1.0 to 2.0mm.
Additional aspects and advantages of the invention will be described in detail in connection with the examples to make the effects apparent.
Drawings
FIG. 1 is an infrared spectrum of barium azodicarbonate;
FIG. 2 is a thermogram of barium azodicarbonate;
Detailed Description
Technical solutions in the embodiments of the present application will be clearly described below with reference to the drawings in the embodiments of the present application, and it is apparent that the described embodiments are some of the embodiments of the present application, but not all of the embodiments. All other embodiments obtained by a person of ordinary skill in the art based on the embodiments in the present application are within the scope of the protection of the present application.
In the description of the present application, it is to be understood that the terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of example embodiments in accordance with the present application. For ease of description, the dimensions of the various features shown in the drawings are not drawn to actual scale. Techniques, methods, and apparatus known to one of ordinary skill in the relevant art may not be discussed in detail, but should be considered part of the specification where appropriate. In all examples shown and discussed herein, any specific values should be construed as merely illustrative, and not a limitation. Thus, other examples of the exemplary embodiments may have different values. It should be noted that: like reference numerals and letters denote like items in the following figures, and thus once an item is defined in one figure, no further discussion thereof is necessary in subsequent figures.
As shown in figures 1 and 2, regarding the high-temperature foaming agent barium azodicarbonate, the foaming temperature is high, the initiation temperature is 250 ℃, the termination gas generation temperature is 300 ℃, the gas generation amount is 60ml-90ml/g (the document reports that the gas generation amount is 170-175ml/g which is a theoretical calculated value and is not a truly measured value), compared with the general exothermic chemical foaming agent barium azodicarbonate (190-210 ℃), the high-temperature foaming agent barium azodicarbonate has the advantages of no toxic gas as a degradation product, environmental protection, mild and controllable gas generation process and high initiation temperature, thereby widening the application of the high-temperature foaming agent barium azodicarbonate in foaming engineering plastics with high melting points.
Example 1:
the embodiment provides a synthesis method of barium azodicarbonate, which is characterized by one-step synthesis, water as solvent, safety, environmental protection, high yield, simple operation and convenient and easily obtained raw materials. The method comprises the following steps:
s1: taking azodicarbonamide and barium hydroxide as raw materials, taking water as a solvent, and catalyzing by inorganic strong alkali to hydrolyze the azodicarbonamide and then directly salify;
s2: after the reaction in the step S1 is finished, the generated barium azodicarbonate is separated out and is deposited in an aqueous solution, and then the barium azodicarbonate is separated out by filtration;
s3: drying the separated barium azodicarbonate to obtain a target product;
the chemical reaction equation in step S1 is:
Figure BDA0004115262700000051
preferably, in step S1, after azodicarbonamide remains to 0.5% or less, the reaction is completed.
The reaction temperature in the step s1 is-10 ℃ to 20 ℃.
The drying temperature in the step S3 is 10-70 ℃.
The inorganic strong base in the step S1 is one or more of sodium hydroxide, potassium hydroxide and lithium hydroxide.
Example 2:
the applicant researches the feasibility of foaming the high-temperature environment-friendly chemical foaming agent barium azodicarbonate in a thermoplastic nylon compound, and particularly relates to a foaming nylon compound composition which comprises the following components in percentage by weight:
Figure BDA0004115262700000052
other processing aids are stearic acid, stearic acid complex esters, and the like.
The foaming nylon compound composition is foamed by injection molding, wherein secondary mold opening is needed during foaming, and the distance of the secondary mold opening is 1.0-2.0mm. The secondary mold opening refers to: after the whole cavity is filled with the compound melt through an extruder, the compound melt is opened slightly in the thickness direction or the variable cavity core is retracted, the primary mold opening is carried out, the quick release of pressure is realized, a large number of cells are induced to be generated simultaneously, then the secondary mold opening is carried out, and the molded resin matrix is taken out.
Regarding the production of the foamed nylon composite composition, the following test was conducted,
test one:
Figure BDA0004115262700000061
the above numbers 1-2 are control groups without adding barium azodicarbonate, the number 3 is a test group without secondary mold opening, after injection molding, the densities of the resin matrixes in the numbers 1 and 2 are similar, no obvious change occurs, the main reason is that no foaming agent is added, no foam cells are generated in the resin matrixes, the resin matrix in the test 3 starts to change, foam cells are generated in the resin matrixes, and compared with the numbers 1 and 2, the density is reduced, and the weight reduction of 7.0% is achieved under the same volume.
After several tests, it was found that the density of the injection molded resin matrix was not only related to the material being produced, but also related to the injection molding method, and for this purpose, tests No. 4-7 were carried out, and the test No. 4-7 was based on the raw material, and the demolding process of the injection molded product was adjusted, specifically, a secondary demolding, i.e., a secondary mold opening, was employed, and after controlling the distance of the mold opening, it was found that a foamed nylon resin matrix having a lighter weight and more uniform cells could be obtained by the secondary mold opening. However, it should be noted that the secondary mold opening distance cannot be too large, otherwise large bulge is caused, and under the control of the number 4-7, the secondary mold opening distance is controlled to be 1.3mm, so that the appearance is ensured, and the weight is reduced by 25.3%.
And (2) testing II:
Figure BDA0004115262700000071
the second test is a control test, the traditional azodicarbonamide is adopted for foaming, and the foaming behavior of the azodicarbonamide is not as good as that of the barium azodicarbonate after the control of the first test and the second test.
And (3) test III:
Figure BDA0004115262700000072
Figure BDA0004115262700000081
test three is a control test, adopting a heat-absorbing high-temperature foaming agent PS516KS (brand name of Jie New Material Co., ltd.) and a foaming behavior test of a heat-absorbing foaming agent ZnCO3 in a PA nylon compound,
the test results show that the whole foaming process is uncontrollable, the foam holes are larger and have broken holes, and the high-temperature heat-absorbing foaming agent is not suitable for the combination.
The applicant has also studied the feasibility of foaming the high-temperature environment-friendly chemical foaming agent barium azodicarbonate in a thermoplastic polyester composite, in particular to a foamable thermoplastic polyester composite composition which comprises the following components in percentage by weight:
Figure BDA0004115262700000082
the foaming thermoplastic polyester compound composition is foamed by injection molding, wherein secondary mold opening is needed during foaming, and the distance of the secondary mold opening is 1.0-2.0mm.
Regarding the production of the foamed thermoplastic polyester composite composition, the following test, test four, was performed:
Figure BDA0004115262700000091
the above-mentioned reference number 1 is a control group to which no barium azodicarbonate was added, and the reference numbers 2 to 3 are test groups, and it was found from the above-mentioned test that adding barium azodicarbonate can reduce weight by 15% while securing appearance after injection molding.
According to the experimental results of the above experiments 1-4, the high-temperature heat-release environment-friendly chemical foaming agent barium azodicarbonate can be uniformly foamed in specific engineering plastic composites (thermoplastic nylon PA, thermoplastic polyester PBT and the like), and the foaming effect in the specific engineering plastic composites is superior to that of the general heat-release chemical foaming agent azodicarbonamide AC, and is greatly superior to that of the general heat-absorption chemical foaming agent PS516KS and zinc carbonate. The foaming agent can be suitable for foaming nylon compounds (PA 6, PA66, PA610, PA612 and the like) and polyester compounds (PET, PBT and the like), and can be also expanded into other high-performance plastic foaming materials processed at high temperature.
The embodiments of the present application and the features of the embodiments may be combined without conflict, and the present application is not limited to the specific embodiments described above, which are merely illustrative, not restrictive, and many forms may be made by those of ordinary skill in the art, without departing from the spirit of the present application and the scope of the claims, which are also within the protection of the present application.

Claims (10)

1. The preparation process of the high-temperature foaming agent barium azodicarbonate is characterized by comprising the following steps of:
s1: taking azodicarbonamide and barium hydroxide as raw materials, taking water as a solvent, and catalyzing by inorganic strong alkali to hydrolyze the azodicarbonamide and then directly salify;
s2: after the reaction in the step S1 is finished, the generated barium azodicarbonate is separated out and is deposited in an aqueous solution, and then the barium azodicarbonate is separated out by filtration;
s3: drying the separated barium azodicarbonate to obtain a target product;
the chemical reaction equation in step S1 is:
Figure FDA0004115262690000011
2. the process for preparing barium azodicarbonate as claimed in claim 1, wherein in step S1, after the azodicarbonamide is left to be 0.5% or less, the reaction is completed; the reaction temperature in the step s1 is-10 ℃ to 20 ℃.
3. The process for preparing barium azodicarbonate as claimed in claim 1, wherein the drying temperature in step S3 is 10-70 ℃.
4. The process for preparing the high-temperature foaming agent barium azodicarbonate according to claim 1, wherein the inorganic strong base in the step S1 is one or more of sodium hydroxide, potassium hydroxide and lithium hydroxide.
5. A foamable nylon composite composition, which is characterized by comprising the following components in percentage by weight:
Figure FDA0004115262690000012
Figure FDA0004115262690000021
6. a foamable nylon composite composition according to claim 5, wherein the other processing aid is stearic acid, a stearic acid complex ester or the like.
7. A process for the preparation of a foamable nylon composite composition according to claim 5 or 6, wherein the foamable composite composition is foamed by injection molding, wherein secondary mold opening is required for foaming, and the secondary mold opening is at a distance of 1.0 to 2.0mm.
8. A foamable thermoplastic polyester composite composition, characterized by comprising the following components in weight percent:
Figure FDA0004115262690000022
9. a foamable thermoplastic polyester composite composition according to claim 8, wherein the other processing aid is stearic acid, a stearic acid complex ester or the like.
10. A process for the preparation of a foamable thermoplastic polyester composite composition according to claim 8 or 9, wherein the foamable composite composition is foamed by injection moulding, wherein secondary mould opening is required for foaming and the secondary mould opening is at a distance of 1.0-2.0mm.
CN202310216801.0A 2023-03-01 2023-03-01 Preparation process and application of high-temperature environment-friendly foaming agent barium azodicarbonate Pending CN116199602A (en)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU170067A1 (en) * Г. М. Стронгин , Я. Ю. Рекшинский
GB1007988A (en) * 1961-09-13 1965-10-22 Nat Distillers Chem Corp Molded plastic foams
CN103415558A (en) * 2011-03-09 2013-11-27 东丽株式会社 Crosslinked polyolefin resin foam
CN112469773A (en) * 2018-07-27 2021-03-09 株式会社大阪曹达 Composition for sound absorbing material
CN115286841A (en) * 2022-08-24 2022-11-04 宁波公牛电器有限公司 Metal powder compound and preparation method thereof, spraying-free PC (polycarbonate) composite material and preparation method thereof, and metal-texture injection molding part

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU170067A1 (en) * Г. М. Стронгин , Я. Ю. Рекшинский
GB1007988A (en) * 1961-09-13 1965-10-22 Nat Distillers Chem Corp Molded plastic foams
CN103415558A (en) * 2011-03-09 2013-11-27 东丽株式会社 Crosslinked polyolefin resin foam
CN112469773A (en) * 2018-07-27 2021-03-09 株式会社大阪曹达 Composition for sound absorbing material
CN115286841A (en) * 2022-08-24 2022-11-04 宁波公牛电器有限公司 Metal powder compound and preparation method thereof, spraying-free PC (polycarbonate) composite material and preparation method thereof, and metal-texture injection molding part

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Application publication date: 20230602