CN112029149B - Polyester water-soluble polymer modifier for calcium carbonate surface modification and preparation method thereof - Google Patents

Polyester water-soluble polymer modifier for calcium carbonate surface modification and preparation method thereof Download PDF

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CN112029149B
CN112029149B CN202010974710.XA CN202010974710A CN112029149B CN 112029149 B CN112029149 B CN 112029149B CN 202010974710 A CN202010974710 A CN 202010974710A CN 112029149 B CN112029149 B CN 112029149B
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soluble polymer
polyester
calcium carbonate
polymer modifier
surface modification
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CN112029149A (en
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陈珍明
何凤春
韦师
刘健华
何星存
张新星
李鹏
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Hezhou Bureau Of Industry And Information Technology
Hezhou University
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Hezhou University
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K9/00Use of pretreated ingredients
    • C08K9/08Ingredients agglomerated by treatment with a binding agent
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/68Polyesters containing atoms other than carbon, hydrogen and oxygen
    • C08G63/688Polyesters containing atoms other than carbon, hydrogen and oxygen containing sulfur
    • C08G63/6884Polyesters containing atoms other than carbon, hydrogen and oxygen containing sulfur derived from polycarboxylic acids and polyhydroxy compounds
    • C08G63/6886Dicarboxylic acids and dihydroxy compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/78Preparation processes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/78Preparation processes
    • C08G63/82Preparation processes characterised by the catalyst used
    • C08G63/83Alkali metals, alkaline earth metals, beryllium, magnesium, copper, silver, gold, zinc, cadmium, mercury, manganese, or compounds thereof
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/78Preparation processes
    • C08G63/82Preparation processes characterised by the catalyst used
    • C08G63/85Germanium, tin, lead, arsenic, antimony, bismuth, titanium, zirconium, hafnium, vanadium, niobium, tantalum, or compounds thereof
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/24Acids; Salts thereof
    • C08K3/26Carbonates; Bicarbonates
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/24Acids; Salts thereof
    • C08K3/26Carbonates; Bicarbonates
    • C08K2003/265Calcium, strontium or barium carbonate

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Polyesters Or Polycarbonates (AREA)

Abstract

The invention belongs to the field of inorganic powder processing and modifying synthetic additives, and particularly relates to a polyester water-soluble polymer modifier for calcium carbonate surface modification and a preparation method thereof. The modifier is prepared from the following raw materials in parts by mole: 1mol portion of dimethyl ester, 2.1mol portions of diol, 0.0001-0.001 mol portion of ester exchange catalyst and 0.0001-0.001 mol portion of polymerization catalyst; the modification has water solubility, the agent can reduce the oil absorption value of the heavy calcium powder, so that the high-value utilization of the heavy calcium powder is realized, and the preparation method has simple steps and low cost, and is suitable for industrial production.

Description

Polyester water-soluble polymer modifier for calcium carbonate surface modification and preparation method thereof
[ technical field ] A method for producing a semiconductor device
The invention belongs to the field of inorganic powder processing and modifying synthetic additives, and relates to a polyester water-soluble polymer modifier for calcium carbonate surface modification and a preparation method thereof.
[ background of the invention ]
Polyesters are a generic name for polymers obtained by polycondensation of polyhydric alcohols and polybasic acids, and are a very important class of high molecular materials. They can be classified into thermoplastic polyesters and thermosetting polyesters according to their behavior after heating, and into aromatic polyesters, aliphatic polyesters, alicyclic polyesters, etc. according to their molecular structures. Polyesters are widely used in various aspects of daily life, such as mineral water bottles (polyethylene terephthalate), clothing (dacron, polyethylene terephthalate), and the like. Particularly since the 21 st century, the sustainability of human production activities and the reduction of carbon dioxide gas emissions have attracted considerable attention, so that biodegradable polyesters have been developed vigorously, and some biodegradable polyesters excellent in overall performance, such as Polycaprolactone (PCL), polylactic acid (PLA), polybutylene succinate (PBS), polybutylene adipate terephthalate (PBAT), have successively appeared and occupied a large share of the market, but they have a great disadvantage in price compared with polyolefins of comparable performance, and have restricted to some extent their faster and wider applications.
Calcium carbonate is an extremely important non-metallic mineral material, is widely applied to the fields of papermaking, plastics, rubber, coatings, papermaking, adhesives, foods, feeds and the like, and is expected to be low-carbon and economical in the face of the problems of excessive consumption of fossil resources, gradual severe environmental pollution and the like, and is upgraded to be a low-carbon material with high quality and low price.
However, the large differences in density and surface properties make calcium carbonate less than ideal for use in plastic, rubber, and the like articles. For this reason, a great deal of research and development efforts have focused on modifying the surface of calcium carbonate, mainly by chemical coating and assisted by mechanochemistry. The surface modifier used at present comprises stearic acid (salt), titanate coupling agent, aluminate coupling agent, atactic polypropylene, polyethylene wax and the like, the main purposes and effects of modification are mostly concentrated on reducing the oil absorption value and the like, the effect is single, the refinement is insufficient, and the modified powder is mainly applied to the field of polyolefin.
In order to expand the wider application of the biodegradable polymer, the cost is greatly reduced by high filling of calcium carbonate, which is a more effective way, however, how to ensure the better comprehensive performance of the composite material under the condition of high filling of calcium carbonate is a key problem in the industry commonality. Therefore, the research and development of the calcium carbonate surface macromolecular modifier special for the polyester is not slow, and no relevant research work is reported at present.
[ summary of the invention ]
The invention aims to provide a polyester water-soluble polymer modifier for calcium carbonate surface modification and a preparation method thereof, wherein the modifier has water solubility and can reduce the oil absorption value of heavy calcium powder so as to realize high-value utilization of the heavy calcium powder, the preparation method fully utilizes the characteristic of melt polycondensation, and sulfonic acid groups are introduced on a polyester macromolecular chain by virtue of dimethyl isophthalate-5-sodium sulfonate to regulate and control the water solubility of the product; in addition, the diol system can realize refined surface modification of calcium carbonate aiming at different polyester raw materials by introducing flexible chain segments such as polyethylene glycol, and the method has the advantages of simple steps and low cost, and is suitable for industrial production.
In order to achieve the purpose, the technical scheme adopted by the invention is as follows:
a polyester water-soluble polymer modifier for calcium carbonate surface modification is prepared from the following raw materials in parts by mole: 1mol portion of dimethyl ester, 2.1mol portions of diol, 0.0001-0.001 mol portion of ester exchange catalyst and 0.0001-0.001 mol portion of polymerization catalyst.
Further, the dimethyl ester is a mixture of dimethyl terephthalate and dimethyl isophthalate-5-sodium sulfonate, and the mole ratio of the dimethyl terephthalate to the dimethyl isophthalate-5-sodium sulfonate is 0.97:0.03-0.5: 0.5.
Further, the diol is selected from one or more of ethylene glycol, propylene glycol, butanediol and polyethylene glycol.
Further, the transesterification catalyst is selected from antimony trioxide, tetra-n-butyl titanate or K2TiF6One kind of (1).
Further, the polymerization catalyst is selected from one of copper acetate, magnesium acetate or zinc acetate.
The preparation method of the polyester water-soluble polymer modifier for calcium carbonate surface modification comprises the following steps:
(1) ester exchange: mixing dimethyl ester, glycol and an ester exchange catalyst, placing the obtained mixture in a reactor with stirring, starting stirring, controlling the reaction temperature to be 140-205 ℃, and carrying out ester exchange reaction;
(2) polymerization: and (2) when the amount of the methanol evaporated in the step (1) is more than 1.6 times of that of the dimethyl ester, adding a polymerization catalyst, raising the temperature to 240-280 ℃, adjusting the vacuum degree to be below 40Pa, carrying out polycondensation reaction for 4-6 h, controlling the temperature to be 60-80 ℃ after the polycondensation is finished, and carrying out vacuum drying for 24-48 h to obtain the high-molecular modifier.
Further, the reactor is a three-neck flask or a stainless steel reaction kettle.
In summary, due to the adoption of the technical scheme, the invention has the beneficial effects that:
compared with the prior art, the modifier prepared by the invention has water solubility, can reduce the oil absorption value of the heavy calcium powder, thereby realizing high-value utilization of the heavy calcium powder, and the preparation method fully utilizes the characteristics of melt polycondensation, introduces sulfonic acid groups on a polyester macromolecular chain by virtue of dimethyl isophthalate-5-sodium sulfonate, and can regulate and control the water solubility of the product; in addition, the diol system can realize refined surface modification of calcium carbonate aiming at different polyester raw materials by introducing flexible chain segments such as polyethylene glycol, and the method has the advantages of simple steps and low cost, and is suitable for industrial production.
[ detailed description ] embodiments
The invention will now be further illustrated by reference to the following examples.
Example 1
(1) Adding 0.97mol of dimethyl terephthalate, 0.03mol of dimethyl isophthalate-5-sodium sulfonate, 2.1mol of ethylene glycol and 0.0001mol of n-tetrabutyl titanate into a 500ml three-neck flask with mechanical stirring, and controlling the reaction temperature to be 140 ℃ for ester exchange;
(2) adding 0.0001mol of zinc acetate after the amount of methanol evaporated by ester exchange reaches 65.5ml, controlling the temperature to 240 ℃, carrying out polycondensation reaction for 4h under the pressure of less than 40Pa, and carrying out vacuum drying for 24h at 80 ℃ after polycondensation reaction to obtain the product. The molecular weight, water solubility and oil absorption value of the 1500-mesh heavy calcium powder modified by 1% aqueous solution of the product are measured.
Example 2
(1) Adding 0.90mol of dimethyl terephthalate, 0.10mol of dimethyl isophthalate-5-sodium sulfonate, 2.1mol of propylene glycol and 0.0005mol of antimony trioxide into a 500ml three-neck flask with mechanical stirring, and controlling the reaction temperature to be 160 ℃ for ester exchange;
(2) and (3) after the methanol amount evaporated by ester exchange reaches 65.5ml, adding 0.0005mol of copper acetate, controlling the temperature to be 240 ℃, carrying out polycondensation reaction for 4h under the pressure of less than 40Pa, and carrying out vacuum drying for 24h at 80 ℃ after polycondensation reaction to obtain the product. The molecular weight, water solubility and oil absorption value of the 1500-mesh heavy calcium powder modified by 1% aqueous solution of the product are measured.
Example 3
(1) Adding 0.80mol of dimethyl terephthalate, 0.20mol of dimethyl isophthalate-5-sodium sulfonate, 2.1mol of butanediol and 0.0007mol of K2TiF6 into a 500ml three-neck flask with mechanical stirring, and controlling the reaction temperature to be 180 ℃ for ester exchange;
(2) after the methanol amount distilled out by ester exchange reaches 65.5ml, 0.0007mol of magnesium acetate is added, the temperature is controlled to be 240 ℃, the polycondensation reaction is carried out for 4h under the pressure of less than 40Pa, and the product is obtained after the polycondensation reaction is carried out for 24h under the vacuum drying at the temperature of 80 ℃. The molecular weight, water solubility and oil absorption value of the 1500-mesh heavy calcium powder modified by 1% aqueous solution of the product are measured.
Example 4
(1) Adding 0.50mol of dimethyl terephthalate, 0.50mol of dimethyl isophthalate-5-sodium sulfonate, 2.1mol of butanediol and 0.001mol of tetra-n-butyl titanate into a 500ml three-neck flask with mechanical stirring, and controlling the reaction temperature to be 205 ℃ for ester exchange;
(2) adding 0.001mol of zinc acetate after the amount of methanol evaporated by ester exchange reaches 65.5ml, controlling the temperature at 280 ℃, carrying out polycondensation reaction for 4h under the pressure of less than 40Pa, and carrying out vacuum drying for 24h at 80 ℃ after polycondensation reaction to obtain the product. The molecular weight, water solubility and oil absorption value of the 1500-mesh heavy calcium powder modified by 1% aqueous solution of the product are measured.
Example 5:
(1) adding 0.70mol of dimethyl terephthalate, 0.30mol of dimethyl isophthalate-5-sodium sulfonate, 2.0mol of butanediol, 0.1mol of polyethylene glycol (with a weight average molecular weight of 2000g/mol) and 0.001mol of tetra-n-butyl titanate into a stainless steel reaction kettle which is provided with a mechanical stirrer and has a volume of 1L, and controlling the reaction temperature to be 160 ℃ for ester exchange;
(2) adding 0.001mol of zinc acetate after the amount of methanol evaporated by ester exchange reaches 65.5ml, controlling the temperature to be 260 ℃, carrying out polycondensation reaction for 4h under the pressure of less than 40Pa, and carrying out vacuum drying for 24h at 80 ℃ after polycondensation reaction to obtain the product. The molecular weight, water solubility and oil absorption value of the 1500-mesh heavy calcium powder modified by 1% aqueous solution of the product are measured. The values are given in Table 1.
TABLE 1
Figure BDA0002685368170000041
The test methods used by the performance indexes are respectively as follows:
molecular weight test used was Gel Permeation Chromatography (GPC): the instrument used was ALC-GPC (high temperature high pressure gel permeation chromatograph at 150 ℃ C.) from Waters corporation, USA; a mixed solvent of phenol and tetrachloroethane (the weight ratio is 1:1) is used as a solvent; chloroform and 1% absolute ethyl alcohol are used as eluent; time: 25 minutes; flow rate: 1.0 mL/min; sample introduction amount: 150 ul; column Chamber temperature: 30 ℃; sample chamber temperature: 30 ℃; pump chamber temperature: at 30 ℃.
The method for measuring the solubility comprises the following steps: the equilibrium method comprises accurately weighing 10g of water-soluble polymer modifier, adding into 100g of deionized water, stirring at constant temperature of 25 deg.C for 5min, standing, and analyzing the composition of the upper layer solution to obtain the solubility at the temperature.
The method for measuring the oil absorption value comprises the following steps: accurately weighing 5g of activated calcium carbonate product, placing the calcium carbonate product on a glass plate, dripping DOP (dioctyl phthalate) (DOP) into a dropping bottle with known weight, continuously turning and grinding by using a knife, dispersing a sample initially, gradually agglomerating until the sample is completely infiltrated by the DOP, and forming an integral agglomerate as a terminal point, and accurately weighing the mass of the dropping bottle. The oil absorption value is expressed as the mass fraction of DOP absorbed per 100g of calcium carbonate.
The foregoing description of the embodiments is provided to facilitate an understanding and appreciation of the invention by those skilled in the art. It will be readily apparent to those skilled in the art that various modifications to these embodiments may be made, and the generic principles described herein may be applied to other embodiments without the use of the inventive faculty. Therefore, the present invention is not limited to the embodiments described herein, and those skilled in the art should make improvements and modifications within the scope of the present invention based on the disclosure of the present invention.

Claims (5)

1. The application of polyester water-soluble polymer modifier in calcium carbonate surface modification is characterized by that,
the polyester water-soluble polymer modifier is prepared from the following raw materials in parts by mole: 1mol portion of dimethyl ester, 2.1mol portions of diol, 0.0001-0.001 mol portion of ester exchange catalyst and 0.0001-0.001 mol portion of polymerization catalyst; the dimethyl ester is a mixture of dimethyl terephthalate and dimethyl isophthalate-5-sodium sulfonate, and the mole ratio of the dimethyl ester to the sodium isophthalate is 0.97:0.03-0.5: 0.5;
the preparation method of the polyester water-soluble polymer modifier comprises the following steps:
(1) ester exchange: mixing dimethyl ester, glycol and an ester exchange catalyst, placing the obtained mixture in a reactor with stirring, starting stirring, controlling the reaction temperature to be 140-205 ℃, and carrying out ester exchange reaction;
(2) polymerization: and (2) when the amount of the methanol evaporated in the step (1) is more than 1.6 times of that of the dimethyl ester, adding a polymerization catalyst, raising the temperature to 240-280 ℃, adjusting the vacuum degree to be below 40Pa, carrying out polycondensation reaction for 4-6 h, controlling the temperature to be 60-80 ℃ after the polycondensation is finished, and carrying out vacuum drying for 24-48 h to obtain the high-molecular modifier.
2. The use of the polyester-based water-soluble polymer modifier for surface modification of calcium carbonate according to claim 1, wherein the glycol is one or more selected from ethylene glycol, propylene glycol, butylene glycol and polyethylene glycol.
3. The use of the polyester-based water-soluble polymer modifier according to claim 1 for surface modification of calcium carbonateCharacterized in that the transesterification catalyst is selected from antimony trioxide, tetra-n-butyl titanate or K2TiF6One kind of (1).
4. The use of the polyester-based water-soluble polymer modifier for surface modification of calcium carbonate according to claim 1, wherein the polymerization catalyst is one selected from copper acetate, magnesium acetate and zinc acetate.
5. The use of the polyester-based water-soluble polymer modifier according to claim 1 for surface modification of calcium carbonate, wherein the reactor is a three-necked flask or a stainless steel reaction vessel.
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KR100616188B1 (en) * 2000-07-26 2006-08-25 주식회사 휴비스 Polyester copolymer and preparation thereof
JP4225107B2 (en) * 2003-05-08 2009-02-18 東レ株式会社 Water-soluble polyester composition
CN1329425C (en) * 2004-06-16 2007-08-01 浙江工程学院 Modified polyester and preparing method thereof
CN100415795C (en) * 2006-06-23 2008-09-03 江苏江南高纤股份有限公司 Alkali soluble polyester and its preparation method
CN101402722B (en) * 2008-11-26 2012-05-30 吉林大学 Method for preparing nano calcium carbonate/polyester composite material
CN101492530B (en) * 2009-03-05 2011-06-08 绍兴文理学院 Ion type copolyester and method for preparing the same
CN103183817B (en) * 2011-12-31 2015-12-16 金发科技股份有限公司 A kind of modified PTT copolyesters and its preparation method and application
CN103626980A (en) * 2012-08-23 2014-03-12 东丽纤维研究所(中国)有限公司 Alkali-soluble copolyester, preparation method and applications thereof
CN103232594B (en) * 2013-04-10 2015-06-17 中国纺织科学研究院 Cationic dyeable propylene glycol polyterephthalate continuous polymerization preparation method
CN105199089B (en) * 2015-11-04 2018-03-23 绍兴文理学院 A kind of preparation method of aliphatic aromatic water-soluble copolyester slurry
CN110964184A (en) * 2018-09-30 2020-04-07 东丽纤维研究所(中国)有限公司 Oligomer containing sulfonate group and preparation method and application thereof
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