CN103045136B - Environment-friendly high-speed cigarette holder glue for cigarettes and preparation method thereof - Google Patents
Environment-friendly high-speed cigarette holder glue for cigarettes and preparation method thereof Download PDFInfo
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- 235000019504 cigarettes Nutrition 0.000 title claims abstract description 33
- 239000003292 glue Substances 0.000 title claims abstract description 33
- 238000002360 preparation method Methods 0.000 title claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 28
- 239000004014 plasticizer Substances 0.000 claims abstract description 20
- 239000000839 emulsion Substances 0.000 claims abstract description 19
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 claims abstract description 13
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims abstract description 12
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims abstract description 12
- 229920003180 amino resin Polymers 0.000 claims abstract description 11
- 239000007787 solid Substances 0.000 claims abstract description 7
- 238000003756 stirring Methods 0.000 claims description 45
- 239000003999 initiator Substances 0.000 claims description 24
- 239000008367 deionised water Substances 0.000 claims description 20
- 229910021641 deionized water Inorganic materials 0.000 claims description 20
- 239000013530 defoamer Substances 0.000 claims description 11
- 239000003995 emulsifying agent Substances 0.000 claims description 11
- 238000010438 heat treatment Methods 0.000 claims description 9
- 238000000034 method Methods 0.000 claims description 8
- ZFOZVQLOBQUTQQ-UHFFFAOYSA-N Tributyl citrate Chemical group CCCCOC(=O)CC(O)(C(=O)OCCCC)CC(=O)OCCCC ZFOZVQLOBQUTQQ-UHFFFAOYSA-N 0.000 claims description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical group CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 4
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 claims description 4
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium persulfate Chemical group [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 claims description 4
- 150000002148 esters Chemical class 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 229910001870 ammonium persulfate Inorganic materials 0.000 claims description 2
- 238000001816 cooling Methods 0.000 claims description 2
- WPUMTJGUQUYPIV-JIZZDEOASA-L disodium (S)-malate Chemical compound [Na+].[Na+].[O-]C(=O)[C@@H](O)CC([O-])=O WPUMTJGUQUYPIV-JIZZDEOASA-L 0.000 claims description 2
- 238000002156 mixing Methods 0.000 claims description 2
- 229910000403 monosodium phosphate Inorganic materials 0.000 claims description 2
- 235000019799 monosodium phosphate Nutrition 0.000 claims description 2
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 claims description 2
- 239000002994 raw material Substances 0.000 claims description 2
- 235000019265 sodium DL-malate Nutrition 0.000 claims description 2
- 229910000030 sodium bicarbonate Inorganic materials 0.000 claims description 2
- 235000017557 sodium bicarbonate Nutrition 0.000 claims description 2
- AJPJDKMHJJGVTQ-UHFFFAOYSA-M sodium dihydrogen phosphate Chemical compound [Na+].OP(O)([O-])=O AJPJDKMHJJGVTQ-UHFFFAOYSA-M 0.000 claims description 2
- 239000001394 sodium malate Substances 0.000 claims description 2
- 235000012424 soybean oil Nutrition 0.000 claims description 2
- 239000003549 soybean oil Substances 0.000 claims description 2
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 abstract description 14
- 125000005498 phthalate group Chemical class 0.000 abstract description 5
- 125000002887 hydroxy group Chemical group [H]O* 0.000 abstract description 4
- 150000001299 aldehydes Chemical class 0.000 abstract 1
- 239000005038 ethylene vinyl acetate Substances 0.000 description 13
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 13
- DQXBYHZEEUGOBF-UHFFFAOYSA-N but-3-enoic acid;ethene Chemical group C=C.OC(=O)CC=C DQXBYHZEEUGOBF-UHFFFAOYSA-N 0.000 description 12
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 9
- 239000000853 adhesive Substances 0.000 description 9
- 230000001070 adhesive effect Effects 0.000 description 9
- 239000000463 material Substances 0.000 description 7
- 229920001577 copolymer Polymers 0.000 description 4
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 description 4
- 239000004816 latex Substances 0.000 description 3
- 229920000126 latex Polymers 0.000 description 3
- 238000007334 copolymerization reaction Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 2
- 229920002689 polyvinyl acetate Polymers 0.000 description 2
- 239000011118 polyvinyl acetate Substances 0.000 description 2
- 229920006027 ternary co-polymer Polymers 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 235000005979 Citrus limon Nutrition 0.000 description 1
- 244000131522 Citrus pyriformis Species 0.000 description 1
- 244000061176 Nicotiana tabacum Species 0.000 description 1
- 235000002637 Nicotiana tabacum Nutrition 0.000 description 1
- -1 PVA acetal Chemical class 0.000 description 1
- DHKHKXVYLBGOIT-UHFFFAOYSA-N acetaldehyde Diethyl Acetal Natural products CCOC(C)OCC DHKHKXVYLBGOIT-UHFFFAOYSA-N 0.000 description 1
- 150000001252 acrylic acid derivatives Chemical class 0.000 description 1
- 229920006243 acrylic copolymer Polymers 0.000 description 1
- 238000012644 addition polymerization Methods 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 230000009477 glass transition Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- XNGIFLGASWRNHJ-UHFFFAOYSA-L phthalate(2-) Chemical compound [O-]C(=O)C1=CC=CC=C1C([O-])=O XNGIFLGASWRNHJ-UHFFFAOYSA-L 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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Abstract
本发明公开一种卷烟用环保型高速接嘴胶及其制备方法。该环保型高速接嘴胶以VAE乳液为基料,并添加醋酸乙烯、丙烯酸、丙烯酸丁酯进行聚合改性,且增塑剂采用环保增塑剂,PVA的羟基使用氨基树脂封端,所得高速接嘴胶基本不含对人体有害的醛类物质和邻苯二甲酸酯类物质,醋酸乙烯酯单体残余量低,固含量为47.4-52.0%,粘度为2800-3300mPa·s,具有良好的初粘性、粘接强度和耐水性适用于车速12000-15000支/分钟的高速卷烟机。The invention discloses an environment-friendly high-speed joint glue for cigarettes and a preparation method thereof. The environmentally friendly high-speed joint glue is based on VAE emulsion, and is polymerized and modified by adding vinyl acetate, acrylic acid, and butyl acrylate. The plasticizer is an environmentally friendly plasticizer, and the hydroxyl group of PVA is blocked with amino resin. The mouthpiece glue basically does not contain aldehydes and phthalates that are harmful to the human body. The residual amount of vinyl acetate monomer is low, the solid content is 47.4-52.0%, and the viscosity is 2800-3300mPa·s. The initial tack, bonding strength and water resistance are suitable for high-speed cigarette making machines with a speed of 12000-15000 cigarettes per minute.
Description
技术领域technical field
本发明涉及一种环保型高速接嘴胶及其制备方法,具体涉及一种卷烟用环保型高速接嘴胶的制备方法,属于卷烟用胶粘剂领域。The invention relates to an environment-friendly high-speed mouth glue and a preparation method thereof, in particular to a preparation method of an environment-friendly high-speed mouth glue for cigarettes, and belongs to the field of cigarette adhesives.
背景技术Background technique
卷烟用胶粘剂主要分为接嘴胶、搭口胶、包装胶及嘴棒成型胶四种,我国约有170余家卷烟厂,年产3600万箱左右,卷烟产量居世界首位,卷烟过程中需要消耗的烟用胶每年可达3万吨。其中,接嘴胶所占份额最大,约2万吨。近年来,为了提高生产效率,卷烟机的车速已从之前的4000-5000支/分钟提高到了8000-15000支/分钟,相应地,卷烟粘合剂就必须能够满足高速卷烟的要求,如具有一定的初粘性,干燥速度快,粘结力强等。Adhesives for cigarettes are mainly divided into four types: mouthpiece glue, mouthpiece glue, packaging glue and mouth rod forming glue. There are more than 170 cigarette factories in my country, with an annual output of about 36 million boxes, and the cigarette output ranks first in the world. The consumption of tobacco rubber can reach 30,000 tons per year. Among them, mouthpiece glue accounts for the largest share, about 20,000 tons. In recent years, in order to improve production efficiency, the speed of the cigarette machine has been increased from the previous 4000-5000 cigarettes/minute to 8000-15000 cigarettes/minute. Correspondingly, the cigarette adhesive must be able to meet the requirements of high-speed cigarettes. Excellent initial tack, fast drying, strong adhesion, etc.
接嘴胶的粘度为2800-3300mPa·s,目前,用于高速卷烟机的接嘴胶主要有两类:一类是VAE(乙烯-醋酸乙烯)胶乳或聚醋酸乙烯酯(PVAc)胶乳;另一类是醋酸乙烯和丙烯酸酯类共聚乳液接嘴胶,通过两者的共聚,达到降低共聚物玻璃化温度的目的,即获得内增塑的效果,这是改善醋酸乙烯乳液初粘性能的一种办法。The viscosity of the mouthpiece glue is 2800-3300mPa s. At present, there are two main types of mouthpiece glue used for high-speed cigarette machines: one is VAE (ethylene-vinyl acetate) latex or polyvinyl acetate (PVAc) latex; the other is One is vinyl acetate and acrylic copolymer emulsion joint glue, through the copolymerization of the two, the purpose of reducing the glass transition temperature of the copolymer is achieved, that is, the effect of internal plasticization is obtained, which is a way to improve the initial viscosity of vinyl acetate emulsion way.
如专利申请CN200510031185提到的高粘度乳胶是基于醋酸乙烯酯的胶粘剂,用于高速卷烟机接嘴卷烟车速大于8000支/分钟,具有初粘性好、粘接强度高、粘接平滑、贮存稳定好的特点。通过醋酸乙烯和丙烯酸酯类共聚的方法可获得流动性、初粘性好、抗寒性良好的高速卷烟接嘴胶。如陈元武在《FHX-2高速卷烟胶粘剂》中提到的醋-丙共聚高速卷烟接嘴胶粘剂是醋酸乙烯与丙烯酸丁酯、不饱和羧酸的三元共聚乳液,该乳液采用通常的种子连续滴加聚合方法,加入了少量分子量调节剂,使得共聚物分子量小,共聚乳液具有良好的粘度稳定性和流动性,且具有初粘力大、干燥速度快、粘接强度高的特点,可以满足接嘴车速7000~8000支/min的要求。专利申请CN201110068785提到的水基型超高速烟用接嘴胶,是以乙酸乙烯酯、丙烯酸丁酯、丙烯酸三元单体,在过硫酸铵-亚硫酸氢钠复合引发剂的作用下,聚合成三元共聚乳液,然后通过抽真空工艺和添加柠檬三正丁酯增塑剂,降低乙酸乙烯酯含量,并用水调节胶粘剂的粘度、固体含量技术指标,制得的接嘴胶粘接能力强,机速可达到12000-17000支/min,乙酸乙烯酯含量低于1000mg/kg,邻苯二甲酸总酯类低于500mg/kg,甲醛含量低于50mg/kg。As mentioned in the patent application CN200510031185, the high-viscosity latex is an adhesive based on vinyl acetate. It is used for high-speed cigarette machine joints with a speed of more than 8000 cigarettes per minute. It has good initial viscosity, high bonding strength, smooth bonding, and good storage stability. specialty. A high-speed cigarette mouthpiece glue with good fluidity, good initial tack and good cold resistance can be obtained through the copolymerization of vinyl acetate and acrylates. For example, the vinegar-propylene copolymer high-speed cigarette joint adhesive mentioned by Chen Yuanwu in "FHX-2 High-speed Cigarette Adhesive" is a ternary copolymer emulsion of vinyl acetate, butyl acrylate, and unsaturated carboxylic acid. Addition polymerization method, adding a small amount of molecular weight regulator, makes the molecular weight of the copolymer small, and the copolymer emulsion has good viscosity stability and fluidity, and has the characteristics of high initial tack, fast drying speed, and high bonding strength, which can meet the requirements of splicing. Nozzle speed 7000 ~ 8000 / min requirements. Patent application CN201110068785 mentions water-based ultra-high-speed mouthpiece glue for cigarettes, which is based on vinyl acetate, butyl acrylate, and acrylic acid ternary monomers, and is polymerized under the action of ammonium persulfate-sodium bisulfite composite initiator. into a ternary copolymer emulsion, and then reduce the content of vinyl acetate through vacuuming process and adding lemon tri-n-butyl plasticizer, and adjust the viscosity and solid content technical indicators of the adhesive with water, so that the prepared joint adhesive has strong bonding ability , the machine speed can reach 12000-17000 pieces/min, the content of vinyl acetate is less than 1000mg/kg, the total esters of phthalic acid is less than 500mg/kg, and the content of formaldehyde is less than 50mg/kg.
以上接嘴胶的制法中均用到保护胶体PVA和增塑剂,PVA中的羟基基团易吸水,为增加接嘴胶的耐水性,必须封闭羟基,最常见的方法是采用PVA缩醛类来实现,如侯琼在《EVA乳液改性生产高速卷烟胶》采用PVA缩甲醛作为改性增粘剂,这可能使得接嘴胶中有一定量的醛类物质;同时增塑剂采用的邻苯二甲酸酯类也是对人体有害物质,尽管专利申请CN201110068785已采用柠檬三正丁酯对增塑剂做了改进,但所得接嘴胶中乙酸乙烯酯、邻苯二甲酸酯类、甲醛含量仍较高,且接嘴胶的初粘性、粘结强度、耐水性需要改进。The protective colloid PVA and plasticizer are used in the preparation of the above joint glue. The hydroxyl group in PVA is easy to absorb water. In order to increase the water resistance of the joint glue, the hydroxyl group must be blocked. The most common method is to use PVA acetal For example, Hou Qiong used PVA formal as a modified tackifier in "EVA Emulsion Modification to Produce High-Speed Cigarette Adhesive", which may cause a certain amount of aldehydes in the mouthpiece; at the same time, the adjacent plasticizer used Phthalates are also harmful substances to the human body. Although the patent application CN201110068785 has adopted tri-n-butyl citrate to improve the plasticizer, vinyl acetate, phthalates, and formaldehyde content are still Higher, and the initial tack, bond strength, and water resistance of the mouthpiece glue need to be improved.
发明内容Contents of the invention
本发明以VAE乳液为基料,并添加醋酸乙烯、丙烯酸、丙烯酸丁酯进行聚合改性,提高初粘性和粘接强度,且增塑剂采用环保增塑剂;PVA封闭羟基的方法改变,在降低甲醛含量的同时提高耐水性,所得接嘴胶基本不含对人体有害的醛类物质和邻苯二甲酸酯类物质、醋酸乙烯单体残留量低,环保。The present invention uses VAE emulsion as base material, and adds vinyl acetate, acrylic acid, butyl acrylate to carry out polymerization modification, improves initial viscosity and bonding strength, and plasticizer adopts environment-friendly plasticizer; The water resistance is improved while the formaldehyde content is reduced, and the obtained mouthpiece glue basically does not contain aldehydes and phthalates which are harmful to the human body, and the residual amount of vinyl acetate monomer is low, which is environmentally friendly.
为了实现上述目的,本发明采用以下技术方案:In order to achieve the above object, the present invention adopts the following technical solutions:
环保型高速接嘴胶,由含有下述重量含量的原料配比制成:Environmentally friendly high-speed joint glue is made of raw materials with the following weight content:
所述的VAE乳液为市售型号为BJ-707,固含量为55%。The VAE emulsion is a commercially available model BJ-707 with a solid content of 55%.
所述的环保增塑剂为柠檬酸三丁酯或环氧大豆油;Described environment-friendly plasticizer is tributyl citrate or epoxidized soybean oil;
所述的PVA为由1788与1799按照2:1比例混合溶解自制而成,固含量为15%;The PVA is self-made by mixing and dissolving 1788 and 1799 at a ratio of 2:1, with a solid content of 15%;
所述引发剂为过硫酸铵或过硫酸钾;Described initiator is ammonium persulfate or potassium persulfate;
所述的乳化剂为OP-10或TX-10中任意一种或以任意比例混合;The emulsifier is any one of OP-10 or TX-10 or mixed in any proportion;
所述pH调节剂为苹果酸钠、碳酸氢钠或磷酸二氢钠中任意一种以任意比例混合;The pH regulator is any one of sodium malate, sodium bicarbonate or sodium dihydrogen phosphate mixed in any proportion;
所述的消泡剂为乙醇,乙醇不仅没有其他醇类的特殊气味,同时又具有优良的消泡效果;The defoamer is ethanol, which not only has no special smell of other alcohols, but also has excellent defoaming effect;
本发明进一步提供一种环保型高速接嘴胶的制备方法,按照如下步骤:The present invention further provides a method for preparing an environment-friendly high-speed joint glue, which comprises the following steps:
1)取42-50%的VAE乳液加入到密封容器中,打开搅拌机,设定搅拌速度为100-150转/分钟,向容器内依次添加15-18%的VAc,3-6%的丙烯酸丁酯,0.6-1.2%的丙烯酸及部分去离子水(约占去离子水总量的一半)后持续搅拌混合均匀;1) Take 42-50% of VAE emulsion and put it into a sealed container, turn on the mixer, set the stirring speed to 100-150 rpm, and add 15-18% of VAc and 3-6% of butyl acrylate to the container in sequence Esters, 0.6-1.2% acrylic acid and some deionized water (accounting for about half of the total amount of deionized water), and then continue to stir and mix evenly;
2)打开加热装置,加热升温至70-75℃,加入一定量的引发剂(约占总引发剂量的三分之一),调整搅拌速度为200-250转/分钟,并继续升温至85-90℃,在1个小时内将剩余的引发剂添加完。再次升温至95℃,添加PVA为6-10%,氨基树脂0.5-1.2%,保温搅拌1-1.2个小时。降温至45-55℃,按顺序添加环保增塑剂1-2.2%,乳化剂0.1-0.8%,pH调节剂0.02-0.05%,消泡剂0.1-0.5%及剩余的去离子水,继续搅拌约0.8-1.5小时,静置冷却,过滤出料。2) Turn on the heating device, heat up to 70-75°C, add a certain amount of initiator (about one-third of the total initiator dose), adjust the stirring speed to 200-250 rpm, and continue to heat up to 85- At 90°C, the remainder of the initiator was added over 1 hour. Heat up to 95°C again, add 6-10% of PVA, 0.5-1.2% of amino resin, and keep stirring for 1-1.2 hours. Cool down to 45-55°C, add 1-2.2% environmentally friendly plasticizer, 0.1-0.8% emulsifier, 0.02-0.05% pH regulator, 0.1-0.5% defoamer and the remaining deionized water in order, and continue stirring About 0.8-1.5 hours, let stand to cool, filter and discharge.
由以上方案制得的环保型高速接嘴胶成本低、用氨基树脂对PVA的羟基进行封端的方法避免了引入醛类物质,环保增塑剂为非邻苯二甲酸酯类物质,因此所得接嘴胶基本不含对人体有害的醛类物质和邻苯二甲酸酯类物质,且醋酸乙烯酯单体残余量低,固含量为45.2-52%,粘度为2800-3300mPa·s,具有良好的初粘性、粘接强度和耐水性,适用于车速12000-15000支/分钟的高速卷烟机。The environmentally friendly high-speed joint glue prepared by the above scheme has low cost, and the method of capping the hydroxyl groups of PVA with amino resin avoids the introduction of aldehydes, and the environmentally friendly plasticizer is non-phthalate. Mouth glue basically does not contain aldehydes and phthalates that are harmful to the human body, and the residual amount of vinyl acetate monomer is low, with a solid content of 45.2-52% and a viscosity of 2800-3300mPa·s. Initial tack, bonding strength and water resistance, suitable for high-speed cigarette making machines with a speed of 12000-15000 cigarettes per minute.
本发明的环保型高速接嘴胶经检测后,各性能指标如下所示:After the environmental-friendly high-speed joint glue of the present invention is tested, each performance index is as follows:
具体实施方式Detailed ways
实施例1Example 1
取42千克的VAE乳液加入到密封容器中,打开搅拌机,设定搅拌速度为100转/分钟,向容器内依次添加18千克的VAc,3千克的丙烯酸丁酯,1.2千克的丙烯酸及12千克的去离子水,持续搅拌混合均匀。打开加热装置,加热升温至70℃,加入0.2千克的引发剂,调整搅拌速度为200转/分钟,并继续升温至85℃,在1个小时内将剩余的引发剂添加完。再次升温至95℃,添加PVA6千克,氨基树脂1.2千克,保温搅拌1个小时。降温至48℃,按顺序添加环保增塑剂2.2千克,乳化剂0.7千克,pH调节剂0.05千克,消泡剂0.35千克及剩余的去离子水,继续搅拌约0.8-1.5小时,静置冷却,过滤出料。Get 42 kg of VAE emulsion into a sealed container, turn on the mixer, set the stirring speed to 100 rpm, add 18 kg of VAc, 3 kg of butyl acrylate, 1.2 kg of acrylic acid and 12 kg of deionized water, stirring continuously to mix well. Turn on the heating device, heat up to 70°C, add 0.2 kg of initiator, adjust the stirring speed to 200 rpm, and continue to heat up to 85°C, and add the remaining initiator within 1 hour. Heat up to 95°C again, add 6 kg of PVA and 1.2 kg of amino resin, and keep stirring for 1 hour. Cool down to 48°C, add 2.2 kg of environmentally friendly plasticizer, 0.7 kg of emulsifier, 0.05 kg of pH regulator, 0.35 kg of defoamer and the remaining deionized water in order, continue to stir for about 0.8-1.5 hours, and let it stand for cooling. Filter the discharge.
实施例2Example 2
取50千克的VAE乳液加入到密封容器中,打开搅拌机,设定搅拌速度为120转/分钟,向容器内依次添加15千克的VAc,6千克的丙烯酸丁酯,0.8千克的丙烯酸及6千克的去离子水,持续搅拌混合均匀。打开加热装置,加热升温至75℃,加入0.12千克的引发剂(约占总引发剂量的三分之一),调整搅拌速度为250转/分钟,并继续升温至90℃,在1个小时内将剩余的引发剂添加完。再次升温至95℃,添加PVA6千克,氨基树脂0.6千克,保温搅拌1.2个小时。降温至55℃,按顺序添加环保增塑剂1千克,乳化剂0.8千克,pH调节剂0.02千克,消泡剂0.41千克及剩余的去离子水,继续搅拌约1.5小时,静置冷却,过滤出料。Take 50 kg of VAE emulsion and add it to a sealed container, turn on the mixer, set the stirring speed to 120 rpm, add 15 kg of VAc, 6 kg of butyl acrylate, 0.8 kg of acrylic acid and 6 kg of deionized water, stirring continuously to mix well. Turn on the heating device, heat up to 75°C, add 0.12 kg of initiator (accounting for about one-third of the total initiator dose), adjust the stirring speed to 250 rpm, and continue to heat up to 90°C, within 1 hour The remaining initiator was added to completion. Heat up to 95°C again, add 6 kg of PVA and 0.6 kg of amino resin, and keep stirring for 1.2 hours. Cool down to 55°C, add 1 kg of environmentally friendly plasticizer, 0.8 kg of emulsifier, 0.02 kg of pH regulator, 0.41 kg of defoamer and the remaining deionized water in order, continue to stir for about 1.5 hours, let stand to cool, and filter out material.
实施例3Example 3
取46千克的VAE乳液加入到密封容器中,打开搅拌机,设定搅拌速度为110转/分钟,向容器内依次添加18千克的VAc,4千克的丙烯酸丁酯,0.6千克的丙烯酸及10千克去离子水后持续搅拌混合均匀。打开加热装置,加热升温至73℃,加入0.1千克的引发剂,调整搅拌速度为240转/分钟,并继续升温至89℃,在1个小时内将剩余的引发剂添加完。再次升温至95℃,添加PVA7千克,氨基树脂0.5千克,保温搅拌1个小时。降温至50℃,按顺序添加环保增塑剂2千克,乳化剂0.3千克,pH调节剂0.03千克,消泡剂0.5千克及剩余的去离子水,继续搅拌约1小时,静置冷却,过滤出料。Take 46 kg of VAE emulsion and add it to a sealed container, turn on the mixer, set the stirring speed to 110 rpm, add 18 kg of VAc, 4 kg of butyl acrylate, 0.6 kg of acrylic acid and 10 kg of After deionized water, keep stirring to mix well. Turn on the heating device, heat up to 73°C, add 0.1 kg of initiator, adjust the stirring speed to 240 rpm, and continue to heat up to 89°C, and add the remaining initiator within 1 hour. Heat up to 95°C again, add 7 kg of PVA and 0.5 kg of amino resin, and keep stirring for 1 hour. Cool down to 50°C, add 2 kg of environmentally friendly plasticizer, 0.3 kg of emulsifier, 0.03 kg of pH regulator, 0.5 kg of defoamer and the remaining deionized water in order, continue to stir for about 1 hour, let stand to cool, and filter out material.
实施例4Example 4
取44千克的VAE乳液加入到密封容器中,打开搅拌机,设定搅拌速度为120转/分钟,向容器内依次添加17千克的VAc,6千克的丙烯酸丁酯,1千克的丙烯酸及9千克去离子水后持续搅拌混合均匀。打开加热装置,加热升温至70℃,加入0.2千克的引发剂,调整搅拌速度为200转/分钟,并继续升温至87℃,在1个小时内将剩余的引发剂添加完。再次升温至95℃,添加PVA9千克,氨基树脂1.2千克,保温搅拌1.2个小时。降温至48℃,按顺序添加环保增塑剂1.9千克,乳化剂0.6千克,pH调节剂0.04千克,消泡剂0.1千克及剩余的去离子水,继续搅拌约1.4小时,静置冷却,过滤出料。Take 44 kg of VAE emulsion and add it to a sealed container, turn on the mixer, set the stirring speed to 120 rpm, add 17 kg of VAc, 6 kg of butyl acrylate, 1 kg of acrylic acid and 9 kg of After deionized water, keep stirring to mix well. Turn on the heating device, heat up to 70°C, add 0.2 kg of initiator, adjust the stirring speed to 200 rpm, and continue to heat up to 87°C, and add the remaining initiator within 1 hour. Heat up to 95°C again, add 9 kg of PVA and 1.2 kg of amino resin, and keep stirring for 1.2 hours. Cool down to 48°C, add 1.9 kg of environmentally friendly plasticizer, 0.6 kg of emulsifier, 0.04 kg of pH regulator, 0.1 kg of defoamer and the remaining deionized water in order, continue to stir for about 1.4 hours, let stand to cool, and filter out material.
实施例5Example 5
取45千克的VAE乳液加入到密封容器中,打开搅拌机,设定搅拌速度为100-150转/分钟,向容器内依次添加16千克的VAc,5千克的丙烯酸丁酯,0.7千克的丙烯酸及11千克去离子水后持续搅拌混合均匀。打开加热装置,加热升温至75℃,加入0.2千克的引发剂,调整搅拌速度为220转/分钟,并继续升温至88℃,在1个小时内将剩余的引发剂添加完。再次升温至95℃,添加PVA8千克,氨基树脂0.8千克,保温搅拌1.1个小时。降温至52℃,按顺序添加环保增塑剂1.7千克,乳化剂0.5千克,pH调节剂0.05千克,消泡剂0.2千克及剩余的去离子水,继续搅拌约1.2小时,静置冷却,过滤出料。Take 45 kg of VAE emulsion and add it to a sealed container, turn on the mixer, set the stirring speed to 100-150 rpm, add 16 kg of VAc, 5 kg of butyl acrylate, 0.7 kg of acrylic acid and 11 After adding one kilogram of deionized water, keep stirring to mix well. Turn on the heating device, heat up to 75°C, add 0.2 kg of initiator, adjust the stirring speed to 220 rpm, and continue to heat up to 88°C, and add the remaining initiator within 1 hour. Heat up to 95°C again, add 8 kg of PVA and 0.8 kg of amino resin, and keep stirring for 1.1 hours. Cool down to 52°C, add 1.7 kg of environmentally friendly plasticizer, 0.5 kg of emulsifier, 0.05 kg of pH regulator, 0.2 kg of defoamer and the remaining deionized water in order, continue to stir for about 1.2 hours, let stand to cool, and filter out material.
实施例6Example 6
取48千克的VAE乳液加入到密封容器中,打开搅拌机,设定搅拌速度为130转/分钟,向容器内依次添加17.5千克的VAc,4.8千克的丙烯酸丁酯,0.9千克的丙烯酸及8千克去离子水后持续搅拌混合均匀。打开加热装置,加热升温至72℃,加入0.2千克引发剂,调整搅拌速度为210转/分钟,并继续升温至86℃,在1个小时内将剩余的引发剂添加完。再次升温至95℃,添加PVA10千克,氨基树脂0.7千克,保温搅拌1.2个小时。降温至55℃,按顺序添加环保增塑剂1.5千克,乳化剂0.4千克,pH调节剂0.02千克,消泡剂0.3千克及剩余的去离子水,继续搅拌约1.5小时,静置冷却,过滤出料。Get 48 kg of VAE emulsion into a sealed container, turn on the mixer, set the stirring speed to 130 rpm, add 17.5 kg of VAc, 4.8 kg of butyl acrylate, 0.9 kg of acrylic acid and 8 kg of After deionized water, keep stirring to mix well. Turn on the heating device, heat up to 72°C, add 0.2 kg of initiator, adjust the stirring speed to 210 rpm, and continue to heat up to 86°C, and add the remaining initiator within 1 hour. Heat up to 95°C again, add 10 kg of PVA and 0.7 kg of amino resin, and keep stirring for 1.2 hours. Cool down to 55°C, add 1.5 kg of environmentally friendly plasticizer, 0.4 kg of emulsifier, 0.02 kg of pH regulator, 0.3 kg of defoamer and the remaining deionized water in order, continue to stir for about 1.5 hours, let stand to cool, and filter out material.
实施例7Example 7
取49千克的VAE乳液加入到密封容器中,打开搅拌机,设定搅拌速度为150转/分钟,向容器内依次添加16.5千克的VAc,5.4千克的丙烯酸丁酯,1.1千克的丙烯酸及9千克去离子水后持续搅拌混合均匀。打开加热装置,加热升温至75℃,加入0.1千克引发剂,调整搅拌速度为200转/分钟,并继续升温至90℃,在1个小时内将剩余的引发剂添加完。再次升温至95℃,添加PVA7.5千克,氨基树脂0.9千克,保温搅拌1个小时。降温至45℃,按顺序添加环保增塑剂1.2千克,乳化剂0.1千克,pH调节剂0.05千克,消泡剂0.4千克及剩余的去离子水,继续搅拌约0.8小时,静置冷却,过滤出料。Get 49 kg of VAE emulsion into a sealed container, turn on the mixer, set the stirring speed to 150 rpm, add 16.5 kg of VAc, 5.4 kg of butyl acrylate, 1.1 kg of acrylic acid and 9 kg of After deionized water, keep stirring to mix well. Turn on the heating device, heat up to 75°C, add 0.1 kg of initiator, adjust the stirring speed to 200 rpm, and continue to heat up to 90°C, and add the remaining initiator within 1 hour. The temperature was raised to 95°C again, 7.5 kg of PVA and 0.9 kg of amino resin were added, and kept stirring for 1 hour. Cool down to 45°C, add 1.2 kg of environmentally friendly plasticizer, 0.1 kg of emulsifier, 0.05 kg of pH regulator, 0.4 kg of defoamer and the remaining deionized water in order, continue to stir for about 0.8 hours, let stand to cool, and filter out material.
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