CN114350105A - Processing technology of antioxidant plastic product - Google Patents
Processing technology of antioxidant plastic product Download PDFInfo
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- CN114350105A CN114350105A CN202210052506.1A CN202210052506A CN114350105A CN 114350105 A CN114350105 A CN 114350105A CN 202210052506 A CN202210052506 A CN 202210052506A CN 114350105 A CN114350105 A CN 114350105A
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Abstract
The invention discloses an antioxidant plastic product processing technology, which relates to the field of plastic product processing and comprises the following operation steps: s1: raw material preparation, comprising the following portions of materials: 20-24% of acrylonitrile-butadiene-styrene copolymer particles, 20-24% of polyethylene terephthalate particles, 15-20% of nitrile rubber, 15-20% of nylon fiber strips, 5-10% of sodium polyacrylate, 5-10% of antioxidant, 1-5% of colorant and 1-5% of flame retardant. According to the processing technology of the antioxidant plastic product, the acrylonitrile-butadiene-styrene copolymer particles, the polyethylene terephthalate particles and the nitrile rubber are polymerized to form plastic, the nylon fiber strips are used as supporting frameworks, and the polymerized plastic is modified by the sodium polyacrylate, the antioxidant, the colorant and the flame retardant, so that the prepared finished product has excellent tensile resistance, bending resistance and impact resistance.
Description
Technical Field
The invention relates to the field of plastic product processing, in particular to an antioxidant plastic product processing technology.
Background
Articles which are made of plastics serving as main raw materials and processed are collectively called as plastic products, the existing plastic products have the problem of poor antioxidant effect in some special environments, and the plastic products are easily oxidized and degraded after being used for a certain time, so that the service life of the plastic products is short indirectly.
Disclosure of Invention
The invention mainly aims to provide a processing technology of an antioxidant plastic product, which can effectively solve the problems in the background technology.
In order to achieve the purpose, the invention adopts the technical scheme that:
an antioxidant plastic product processing technology comprises the following operation steps:
s1: raw material preparation, comprising the following portions of materials: 20-24% of acrylonitrile-butadiene-styrene copolymer particles, 20-24% of polyethylene terephthalate particles, 15-20% of nitrile rubber, 15-20% of nylon fiber strips, 5-10% of sodium polyacrylate, 5-10% of antioxidant, 1-5% of colorant and 1-5% of flame retardant;
s2: weighing acrylonitrile-butadiene-styrene copolymer particles, polyethylene glycol terephthalate particles and nitrile rubber according to the weight, putting the acrylonitrile-butadiene-styrene copolymer particles, the polyethylene glycol terephthalate particles and the nitrile rubber into a crusher to be crushed into fine powder, taking out the fine powder to be heated at the temperature of 200 ℃ and 300 ℃, synchronously stirring in the hot melting process for 1-2 hours, and stirring at the constant temperature of 50 ℃ after heating is finished;
s3: weighing sodium polyacrylate, antioxidant, colorant and flame retardant according to weight, adding sodium polyacrylate, antioxidant, colorant and flame retardant into the stirred colloid, and continuously stirring for 3-5 hours to make the colloid fully contact with sodium polyacrylate, antioxidant, colorant and flame retardant;
s4: weighing nylon fiber strips according to the weight, adding the nylon fiber strips into the stirred colloid, and stirring at a low speed for 30 minutes to uniformly mix the colloid and the nylon fiber strips;
s5: and adding the stirred colloid into a quantitative extruder, controlling the quantitative extruder to quantitatively extrude the colloid into a lower die, immediately controlling a hot press to hot press an upper die to the lower die, obtaining a plastic product after the hot pressing is finished, trimming the plastic product, cutting off leftover materials, collecting the leftover materials, and obtaining a plastic finished product.
Preferably, the proportion of the acrylonitrile-butadiene-styrene copolymer particles is 20%, the proportion of the polyethylene terephthalate particles is 20%, the proportion of the nitrile rubber is 15%, the proportion of the nylon fiber strips is 15%, the proportion of the sodium polyacrylate is 10%, the proportion of the antioxidant is 10%, the proportion of the colorant is 5%, and the proportion of the flame retardant is 5%.
Preferably, the proportion of the acrylonitrile-butadiene-styrene copolymer particles is 21%, the proportion of the polyethylene terephthalate particles is 21%, the proportion of the nitrile rubber is 16%, the proportion of the nylon fiber strips is 17%, the proportion of the sodium polyacrylate is 8%, the proportion of the antioxidant is 9%, the proportion of the colorant is 4%, and the proportion of the flame retardant is 4%.
Preferably, the acrylonitrile-butadiene-styrene copolymer particles account for 22%, the polyethylene terephthalate particles account for 22%, the nitrile rubber accounts for 18%, the nylon fiber strips account for 18%, the sodium polyacrylate accounts for 7%, the antioxidant accounts for 7%, the colorant accounts for 3%, and the flame retardant accounts for 3%.
Preferably, the proportion of the acrylonitrile-butadiene-styrene copolymer particles is 23%, the proportion of the polyethylene terephthalate particles is 23%, the proportion of the nitrile rubber is 19%, the proportion of the nylon fiber strips is 19%, the proportion of the sodium polyacrylate is 6%, the proportion of the antioxidant is 6%, the proportion of the colorant is 2%, and the proportion of the flame retardant is 2%.
Preferably, the proportion of the acrylonitrile-butadiene-styrene copolymer particles is 24%, the proportion of the polyethylene terephthalate particles is 24%, the proportion of the nitrile rubber is 20%, the proportion of the nylon fiber strips is 20%, the proportion of the sodium polyacrylate is 5%, the proportion of the antioxidant is 5%, the proportion of the colorant is 1%, and the proportion of the flame retardant is 1%.
Compared with the prior art, the invention has the following beneficial effects:
in the invention, acrylonitrile-butadiene-styrene copolymer particles, polyethylene terephthalate particles and nitrile rubber are polymerized to form plastic, nylon fiber strips are used as a supporting framework, and the polymerized plastic is modified by sodium polyacrylate, an antioxidant, a coloring agent and a flame retardant, so that the prepared finished product has excellent tensile, bending and impact resistance, and the service life of the plastic product is prolonged.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to 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 first embodiment is as follows:
an antioxidant plastic product processing technology comprises the following operation steps:
s1: raw material preparation, comprising the following portions of materials: 20-24% of acrylonitrile-butadiene-styrene copolymer particles, 20-24% of polyethylene terephthalate particles, 15-20% of nitrile rubber, 15-20% of nylon fiber strips, 5-10% of sodium polyacrylate, 5-10% of antioxidant, 1-5% of colorant and 1-5% of flame retardant;
s2: weighing acrylonitrile-butadiene-styrene copolymer particles, polyethylene glycol terephthalate particles and nitrile rubber according to the weight, putting the acrylonitrile-butadiene-styrene copolymer particles, the polyethylene glycol terephthalate particles and the nitrile rubber into a crusher to be crushed into fine powder, taking out the fine powder to be heated at the temperature of 200 ℃ and 300 ℃, synchronously stirring in the hot melting process for 1-2 hours, and stirring at the constant temperature of 50 ℃ after heating is finished;
s3: weighing sodium polyacrylate, antioxidant, colorant and flame retardant according to weight, adding sodium polyacrylate, antioxidant, colorant and flame retardant into the stirred colloid, and continuously stirring for 3-5 hours to make the colloid fully contact with sodium polyacrylate, antioxidant, colorant and flame retardant;
s4: weighing nylon fiber strips according to the weight, adding the nylon fiber strips into the stirred colloid, and stirring at a low speed for 30 minutes to uniformly mix the colloid and the nylon fiber strips;
s5: and adding the stirred colloid into a quantitative extruder, controlling the quantitative extruder to quantitatively extrude the colloid into a lower die, immediately controlling a hot press to hot press an upper die to the lower die, obtaining a plastic product after the hot pressing is finished, trimming the plastic product, cutting off leftover materials, collecting the leftover materials, and obtaining a plastic finished product.
Example two:
an antioxidant plastic product processing technology comprises the following operation steps:
s1: raw material preparation, comprising the following portions of materials: 20% of acrylonitrile-butadiene-styrene copolymer particles, 20% of polyethylene terephthalate particles, 15% of nitrile rubber, 15% of nylon fiber strips, 10% of sodium polyacrylate, 10% of antioxidant, 5% of colorant and 5% of flame retardant;
s2: weighing acrylonitrile-butadiene-styrene copolymer particles, polyethylene glycol terephthalate particles and nitrile rubber according to the weight, putting the acrylonitrile-butadiene-styrene copolymer particles, the polyethylene glycol terephthalate particles and the nitrile rubber into a crusher to be crushed into fine powder, taking out the fine powder to be heated at the temperature of 200 ℃ and 300 ℃, synchronously stirring in the hot melting process for 1-2 hours, and stirring at the constant temperature of 50 ℃ after heating is finished;
s3: weighing sodium polyacrylate, antioxidant, colorant and flame retardant according to weight, adding sodium polyacrylate, antioxidant, colorant and flame retardant into the stirred colloid, and continuously stirring for 3-5 hours to make the colloid fully contact with sodium polyacrylate, antioxidant, colorant and flame retardant;
s4: weighing nylon fiber strips according to the weight, adding the nylon fiber strips into the stirred colloid, and stirring at a low speed for 30 minutes to uniformly mix the colloid and the nylon fiber strips;
s5: and adding the stirred colloid into a quantitative extruder, controlling the quantitative extruder to quantitatively extrude the colloid into a lower die, immediately controlling a hot press to hot press an upper die to the lower die, obtaining a plastic product after the hot pressing is finished, trimming the plastic product, cutting off leftover materials, collecting the leftover materials, and obtaining a plastic finished product.
Example three:
an antioxidant plastic product processing technology comprises the following operation steps:
s1: raw material preparation, comprising the following portions of materials: 21% of acrylonitrile-butadiene-styrene copolymer particles, 21% of polyethylene terephthalate particles, 16% of nitrile rubber, 17% of nylon fiber strips, 8% of sodium polyacrylate, 9% of antioxidant, 4% of colorant and 4% of flame retardant;
s2: weighing acrylonitrile-butadiene-styrene copolymer particles, polyethylene glycol terephthalate particles and nitrile rubber according to the weight, putting the acrylonitrile-butadiene-styrene copolymer particles, the polyethylene glycol terephthalate particles and the nitrile rubber into a crusher to be crushed into fine powder, taking out the fine powder to be heated at the temperature of 200 ℃ and 300 ℃, synchronously stirring in the hot melting process for 1-2 hours, and stirring at the constant temperature of 50 ℃ after heating is finished;
s3: weighing sodium polyacrylate, antioxidant, colorant and flame retardant according to weight, adding sodium polyacrylate, antioxidant, colorant and flame retardant into the stirred colloid, and continuously stirring for 3-5 hours to make the colloid fully contact with sodium polyacrylate, antioxidant, colorant and flame retardant;
s4: weighing nylon fiber strips according to the weight, adding the nylon fiber strips into the stirred colloid, and stirring at a low speed for 30 minutes to uniformly mix the colloid and the nylon fiber strips;
s5: and adding the stirred colloid into a quantitative extruder, controlling the quantitative extruder to quantitatively extrude the colloid into a lower die, immediately controlling a hot press to hot press an upper die to the lower die, obtaining a plastic product after the hot pressing is finished, trimming the plastic product, cutting off leftover materials, collecting the leftover materials, and obtaining a plastic finished product.
Example four:
an antioxidant plastic product processing technology comprises the following operation steps:
s1: raw material preparation, comprising the following portions of materials: 22% of acrylonitrile-butadiene-styrene copolymer particles, 22% of polyethylene terephthalate particles, 18% of nitrile rubber, 18% of nylon fiber strips, 7% of sodium polyacrylate, 7% of antioxidant, 3% of colorant and 3% of flame retardant;
s2: weighing acrylonitrile-butadiene-styrene copolymer particles, polyethylene glycol terephthalate particles and nitrile rubber according to the weight, putting the acrylonitrile-butadiene-styrene copolymer particles, the polyethylene glycol terephthalate particles and the nitrile rubber into a crusher to be crushed into fine powder, taking out the fine powder to be heated at the temperature of 200 ℃ and 300 ℃, synchronously stirring in the hot melting process for 1-2 hours, and stirring at the constant temperature of 50 ℃ after heating is finished;
s3: weighing sodium polyacrylate, antioxidant, colorant and flame retardant according to weight, adding sodium polyacrylate, antioxidant, colorant and flame retardant into the stirred colloid, and continuously stirring for 3-5 hours to make the colloid fully contact with sodium polyacrylate, antioxidant, colorant and flame retardant;
s4: weighing nylon fiber strips according to the weight, adding the nylon fiber strips into the stirred colloid, and stirring at a low speed for 30 minutes to uniformly mix the colloid and the nylon fiber strips;
s5: and adding the stirred colloid into a quantitative extruder, controlling the quantitative extruder to quantitatively extrude the colloid into a lower die, immediately controlling a hot press to hot press an upper die to the lower die, obtaining a plastic product after the hot pressing is finished, trimming the plastic product, cutting off leftover materials, collecting the leftover materials, and obtaining a plastic finished product.
Example five:
an antioxidant plastic product processing technology comprises the following operation steps:
s1: raw material preparation, comprising the following portions of materials: 23% of acrylonitrile-butadiene-styrene copolymer particles, 23% of polyethylene terephthalate particles, 19% of nitrile rubber, 19% of nylon fiber strips, 6% of sodium polyacrylate, 6% of antioxidant, 2% of colorant and 2% of flame retardant;
s2: weighing acrylonitrile-butadiene-styrene copolymer particles, polyethylene glycol terephthalate particles and nitrile rubber according to the weight, putting the acrylonitrile-butadiene-styrene copolymer particles, the polyethylene glycol terephthalate particles and the nitrile rubber into a crusher to be crushed into fine powder, taking out the fine powder to be heated at the temperature of 200 ℃ and 300 ℃, synchronously stirring in the hot melting process for 1-2 hours, and stirring at the constant temperature of 50 ℃ after heating is finished;
s3: weighing sodium polyacrylate, antioxidant, colorant and flame retardant according to weight, adding sodium polyacrylate, antioxidant, colorant and flame retardant into the stirred colloid, and continuously stirring for 3-5 hours to make the colloid fully contact with sodium polyacrylate, antioxidant, colorant and flame retardant;
s4: weighing nylon fiber strips according to the weight, adding the nylon fiber strips into the stirred colloid, and stirring at a low speed for 30 minutes to uniformly mix the colloid and the nylon fiber strips;
s5: and adding the stirred colloid into a quantitative extruder, controlling the quantitative extruder to quantitatively extrude the colloid into a lower die, immediately controlling a hot press to hot press an upper die to the lower die, obtaining a plastic product after the hot pressing is finished, trimming the plastic product, cutting off leftover materials, collecting the leftover materials, and obtaining a plastic finished product.
Example six:
an antioxidant plastic product processing technology comprises the following operation steps:
s1: raw material preparation, comprising the following portions of materials: 24% of acrylonitrile-butadiene-styrene copolymer particles, 24% of polyethylene terephthalate particles, 20% of nitrile rubber, 20% of nylon fiber strips, 5% of sodium polyacrylate, 5% of antioxidant, 1% of colorant and 1% of flame retardant;
s2: weighing acrylonitrile-butadiene-styrene copolymer particles, polyethylene glycol terephthalate particles and nitrile rubber according to the weight, putting the acrylonitrile-butadiene-styrene copolymer particles, the polyethylene glycol terephthalate particles and the nitrile rubber into a crusher to be crushed into fine powder, taking out the fine powder to be heated at the temperature of 200 ℃ and 300 ℃, synchronously stirring in the hot melting process for 1-2 hours, and stirring at the constant temperature of 50 ℃ after heating is finished;
s3: weighing sodium polyacrylate, antioxidant, colorant and flame retardant according to weight, adding sodium polyacrylate, antioxidant, colorant and flame retardant into the stirred colloid, and continuously stirring for 3-5 hours to make the colloid fully contact with sodium polyacrylate, antioxidant, colorant and flame retardant;
s4: weighing nylon fiber strips according to the weight, adding the nylon fiber strips into the stirred colloid, and stirring at a low speed for 30 minutes to uniformly mix the colloid and the nylon fiber strips;
s5: and adding the stirred colloid into a quantitative extruder, controlling the quantitative extruder to quantitatively extrude the colloid into a lower die, immediately controlling a hot press to hot press an upper die to the lower die, obtaining a plastic product after the hot pressing is finished, trimming the plastic product, cutting off leftover materials, collecting the leftover materials, and obtaining a plastic finished product.
The invention polymerizes acrylonitrile-butadiene-styrene copolymer particles, polyethylene glycol terephthalate particles and nitrile rubber to form plastic, takes nylon fiber strips as a supporting framework, and modifies the polymerized plastic by sodium polyacrylate, antioxidant, colorant and flame retardant, so that the prepared finished product has excellent tensile, bending and impact resistance properties, and the service life of the plastic product is prolonged.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (6)
1. An antioxidant plastic product processing technology is characterized in that: the method comprises the following operation steps:
s1: raw material preparation, comprising the following portions of materials: 20-24% of acrylonitrile-butadiene-styrene copolymer particles, 20-24% of polyethylene terephthalate particles, 15-20% of nitrile rubber, 15-20% of nylon fiber strips, 5-10% of sodium polyacrylate, 5-10% of antioxidant, 1-5% of colorant and 1-5% of flame retardant;
s2: weighing acrylonitrile-butadiene-styrene copolymer particles, polyethylene glycol terephthalate particles and nitrile rubber according to the weight, putting the acrylonitrile-butadiene-styrene copolymer particles, the polyethylene glycol terephthalate particles and the nitrile rubber into a crusher to be crushed into fine powder, taking out the fine powder to be heated at the temperature of 200 ℃ and 300 ℃, synchronously stirring in the hot melting process for 1-2 hours, and stirring at the constant temperature of 50 ℃ after heating is finished;
s3: weighing sodium polyacrylate, antioxidant, colorant and flame retardant according to weight, adding sodium polyacrylate, antioxidant, colorant and flame retardant into the stirred colloid, and continuously stirring for 3-5 hours to make the colloid fully contact with sodium polyacrylate, antioxidant, colorant and flame retardant;
s4: weighing nylon fiber strips according to the weight, adding the nylon fiber strips into the stirred colloid, and stirring at a low speed for 30 minutes to uniformly mix the colloid and the nylon fiber strips;
s5: and adding the stirred colloid into a quantitative extruder, controlling the quantitative extruder to quantitatively extrude the colloid into a lower die, immediately controlling a hot press to hot press an upper die to the lower die, obtaining a plastic product after the hot pressing is finished, trimming the plastic product, cutting off leftover materials, collecting the leftover materials, and obtaining a plastic finished product.
2. The processing technology of the antioxidant plastic product as claimed in claim 1, wherein the processing technology comprises the following steps: the proportion of the acrylonitrile-butadiene-styrene copolymer particles is 20%, the proportion of the polyethylene terephthalate particles is 20%, the proportion of the nitrile rubber is 15%, the proportion of the nylon fiber strips is 15%, the proportion of the sodium polyacrylate is 10%, the proportion of the antioxidant is 10%, the proportion of the colorant is 5%, and the proportion of the flame retardant is 5%.
3. The processing technology of the antioxidant plastic product as claimed in claim 1, wherein the processing technology comprises the following steps: the proportion of the acrylonitrile-butadiene-styrene copolymer particles is 21%, the proportion of the polyethylene terephthalate particles is 21%, the proportion of the nitrile rubber is 16%, the proportion of the nylon fiber strips is 17%, the proportion of the sodium polyacrylate is 8%, the proportion of the antioxidant is 9%, the proportion of the colorant is 4%, and the proportion of the flame retardant is 4%.
4. The processing technology of the antioxidant plastic product as claimed in claim 1, wherein the processing technology comprises the following steps: the proportion of the acrylonitrile-butadiene-styrene copolymer particles is 22%, the proportion of the polyethylene terephthalate particles is 22%, the proportion of the nitrile rubber is 18%, the proportion of the nylon fiber strips is 18%, the proportion of the sodium polyacrylate is 7%, the proportion of the antioxidant is 7%, the proportion of the colorant is 3%, and the proportion of the flame retardant is 3%.
5. The processing technology of the antioxidant plastic product as claimed in claim 1, wherein the processing technology comprises the following steps: the proportion of the acrylonitrile-butadiene-styrene copolymer particles is 23%, the proportion of the polyethylene terephthalate particles is 23%, the proportion of the nitrile rubber is 19%, the proportion of the nylon fiber strips is 19%, the proportion of the sodium polyacrylate is 6%, the proportion of the antioxidant is 6%, the proportion of the colorant is 2%, and the proportion of the flame retardant is 2%.
6. The processing technology of the antioxidant plastic product as claimed in claim 1, wherein the processing technology comprises the following steps: the proportion of the acrylonitrile-butadiene-styrene copolymer particles is 24%, the proportion of the polyethylene terephthalate particles is 24%, the proportion of the nitrile rubber is 20%, the proportion of the nylon fiber strips is 20%, the proportion of the sodium polyacrylate is 5%, the proportion of the antioxidant is 5%, the proportion of the colorant is 1%, and the proportion of the flame retardant is 1%.
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20080290330A1 (en) * | 2007-05-25 | 2008-11-27 | Mitac Precision Technology (Shunde) Ltd. | Composition of high impact glass firber reinforced flame-retardant engineering plastic and preparation method thereof |
| CN102807742A (en) * | 2011-05-31 | 2012-12-05 | 上海杰事杰新材料(集团)股份有限公司 | Semi-aromatic polyamide short fiber reinforced composite material and preparation method thereof |
| KR101230581B1 (en) * | 2012-07-10 | 2013-02-06 | (주)케이피텍 | Preparation method of functional foam composition using polyethyleneterephthalate |
| CN104725789A (en) * | 2013-12-23 | 2015-06-24 | 青岛万力科技有限公司 | High-performance low-cost flame-retardant PET/ABS composite material |
| CN105694341A (en) * | 2016-03-17 | 2016-06-22 | 合肥晨煦信息科技有限公司 | Glass bead filled and modified ABS composite |
| CN107151400A (en) * | 2017-07-12 | 2017-09-12 | 合肥思博特软件开发有限公司 | It is a kind of for composite of notebook computer shell and preparation method thereof |
-
2022
- 2022-01-18 CN CN202210052506.1A patent/CN114350105A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20080290330A1 (en) * | 2007-05-25 | 2008-11-27 | Mitac Precision Technology (Shunde) Ltd. | Composition of high impact glass firber reinforced flame-retardant engineering plastic and preparation method thereof |
| CN102807742A (en) * | 2011-05-31 | 2012-12-05 | 上海杰事杰新材料(集团)股份有限公司 | Semi-aromatic polyamide short fiber reinforced composite material and preparation method thereof |
| KR101230581B1 (en) * | 2012-07-10 | 2013-02-06 | (주)케이피텍 | Preparation method of functional foam composition using polyethyleneterephthalate |
| CN104725789A (en) * | 2013-12-23 | 2015-06-24 | 青岛万力科技有限公司 | High-performance low-cost flame-retardant PET/ABS composite material |
| CN105694341A (en) * | 2016-03-17 | 2016-06-22 | 合肥晨煦信息科技有限公司 | Glass bead filled and modified ABS composite |
| CN107151400A (en) * | 2017-07-12 | 2017-09-12 | 合肥思博特软件开发有限公司 | It is a kind of for composite of notebook computer shell and preparation method thereof |
Non-Patent Citations (2)
| Title |
|---|
| 胡俊梅;: "ABS/PET复合材料的制备及界面相容性", 高分子材料科学与工程, no. 06, pages 155 - 158 * |
| 贾剑楠;何小芳;许明路;秦刚;: "ABS/PET合金改性应用研究进展", 化工新型材料, no. 04, pages 1 - 3 * |
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