CN108822241A - A kind of preparation method of environment-friendly type wet strength agent - Google Patents
A kind of preparation method of environment-friendly type wet strength agent Download PDFInfo
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- CN108822241A CN108822241A CN201810577854.4A CN201810577854A CN108822241A CN 108822241 A CN108822241 A CN 108822241A CN 201810577854 A CN201810577854 A CN 201810577854A CN 108822241 A CN108822241 A CN 108822241A
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- 238000002360 preparation method Methods 0.000 title claims abstract description 14
- 239000000178 monomer Substances 0.000 claims abstract description 65
- 238000003756 stirring Methods 0.000 claims abstract description 56
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 55
- 239000000839 emulsion Substances 0.000 claims abstract description 47
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 31
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims abstract description 18
- 239000003999 initiator Substances 0.000 claims abstract description 17
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 claims abstract description 17
- 239000008367 deionised water Substances 0.000 claims abstract description 16
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 16
- 239000000463 material Substances 0.000 claims abstract description 16
- 239000003995 emulsifying agent Substances 0.000 claims abstract description 10
- VOZRXNHHFUQHIL-UHFFFAOYSA-N glycidyl methacrylate Chemical compound CC(=C)C(=O)OCC1CO1 VOZRXNHHFUQHIL-UHFFFAOYSA-N 0.000 claims abstract description 10
- 238000010438 heat treatment Methods 0.000 claims abstract description 10
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 claims abstract description 9
- 238000004945 emulsification Methods 0.000 abstract 1
- 239000000123 paper Substances 0.000 description 66
- 239000000835 fiber Substances 0.000 description 22
- 229920001807 Urea-formaldehyde Polymers 0.000 description 8
- GZCGUPFRVQAUEE-SLPGGIOYSA-N aldehydo-D-glucose Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C=O GZCGUPFRVQAUEE-SLPGGIOYSA-N 0.000 description 8
- 238000004132 cross linking Methods 0.000 description 8
- 230000007246 mechanism Effects 0.000 description 6
- 229920002085 Dialdehyde starch Polymers 0.000 description 5
- 229920000877 Melamine resin Polymers 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 229920000642 polymer Polymers 0.000 description 5
- 229920005989 resin Polymers 0.000 description 5
- 239000011347 resin Substances 0.000 description 5
- LEJBBGNFPAFPKQ-UHFFFAOYSA-N 2-(2-prop-2-enoyloxyethoxy)ethyl prop-2-enoate Chemical compound C=CC(=O)OCCOCCOC(=O)C=C LEJBBGNFPAFPKQ-UHFFFAOYSA-N 0.000 description 4
- 229920002873 Polyethylenimine Polymers 0.000 description 4
- 108010039918 Polylysine Proteins 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 229920000656 polylysine Polymers 0.000 description 4
- 238000005728 strengthening Methods 0.000 description 4
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 description 3
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- 239000004952 Polyamide Substances 0.000 description 3
- 239000000654 additive Substances 0.000 description 3
- 239000002131 composite material Substances 0.000 description 3
- 229920002647 polyamide Polymers 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 230000008961 swelling Effects 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- RPNUMPOLZDHAAY-UHFFFAOYSA-N Diethylenetriamine Chemical compound NCCNCCN RPNUMPOLZDHAAY-UHFFFAOYSA-N 0.000 description 2
- 239000004593 Epoxy Substances 0.000 description 2
- 229920000663 Hydroxyethyl cellulose Polymers 0.000 description 2
- 239000004354 Hydroxyethyl cellulose Substances 0.000 description 2
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical compound [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- HRBZRZSCMANEHQ-UHFFFAOYSA-L calcium;hexadecanoate Chemical compound [Ca+2].CCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCC([O-])=O HRBZRZSCMANEHQ-UHFFFAOYSA-L 0.000 description 2
- 230000002708 enhancing effect Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 235000019447 hydroxyethyl cellulose Nutrition 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 229920002401 polyacrylamide Polymers 0.000 description 2
- 239000002952 polymeric resin Substances 0.000 description 2
- SCVFZCLFOSHCOH-UHFFFAOYSA-M potassium acetate Chemical compound [K+].CC([O-])=O SCVFZCLFOSHCOH-UHFFFAOYSA-M 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 description 2
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- FLPJVCMIKUWSDR-UHFFFAOYSA-N 2-(4-formylphenoxy)acetamide Chemical compound NC(=O)COC1=CC=C(C=O)C=C1 FLPJVCMIKUWSDR-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- DPXJVFZANSGRMM-UHFFFAOYSA-N acetic acid;2,3,4,5,6-pentahydroxyhexanal;sodium Chemical compound [Na].CC(O)=O.OCC(O)C(O)C(O)C(O)C=O DPXJVFZANSGRMM-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000005804 alkylation reaction Methods 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 229920003123 carboxymethyl cellulose sodium Polymers 0.000 description 1
- 229940063834 carboxymethylcellulose sodium Drugs 0.000 description 1
- 231100000357 carcinogen Toxicity 0.000 description 1
- 239000003183 carcinogenic agent Substances 0.000 description 1
- 239000011111 cardboard Substances 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 229940074979 cetyl palmitate Drugs 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 229940008099 dimethicone Drugs 0.000 description 1
- 239000004205 dimethyl polysiloxane Substances 0.000 description 1
- 235000013870 dimethyl polysiloxane Nutrition 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000010292 electrical insulation Methods 0.000 description 1
- 230000001815 facial effect Effects 0.000 description 1
- 230000009477 glass transition Effects 0.000 description 1
- PXDJXZJSCPSGGI-UHFFFAOYSA-N hexadecanoic acid hexadecyl ester Natural products CCCCCCCCCCCCCCCCOC(=O)CCCCCCCCCCCCCCC PXDJXZJSCPSGGI-UHFFFAOYSA-N 0.000 description 1
- 239000000017 hydrogel Substances 0.000 description 1
- XMBWDFGMSWQBCA-UHFFFAOYSA-N hydrogen iodide Chemical compound I XMBWDFGMSWQBCA-UHFFFAOYSA-N 0.000 description 1
- -1 hydrogen ions Chemical class 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 230000000269 nucleophilic effect Effects 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 150000002924 oxiranes Chemical class 0.000 description 1
- 238000010979 pH adjustment Methods 0.000 description 1
- 239000011087 paperboard Substances 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 description 1
- 229920000768 polyamine Polymers 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920005862 polyol Polymers 0.000 description 1
- 150000003077 polyols Chemical class 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 235000011056 potassium acetate Nutrition 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 229920001059 synthetic polymer Polymers 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- 238000011282 treatment Methods 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F212/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
- C08F212/02—Monomers containing only one unsaturated aliphatic radical
- C08F212/04—Monomers containing only one unsaturated aliphatic radical containing one ring
- C08F212/06—Hydrocarbons
- C08F212/08—Styrene
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/37—Polymers of unsaturated acids or derivatives thereof, e.g. polyacrylates
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
- D21H21/18—Reinforcing agents
- D21H21/20—Wet strength agents
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Paper (AREA)
Abstract
本发明公开了一种环保型湿强剂的制备方法,包括如下步骤:将苯乙烯、丙烯酸丁酯、甲基丙烯酸缩水甘油酯进行混合制备成混合单体;将混合单体与去离子水、入乳化剂和引发剂过硫酸钾一起进行预乳化,得到预乳化的混合单体乳液;往一带夹套搅拌釜中加入去离子水30重量份,预乳化的混合单体乳液15重量份,开启加热,当物料温度达到75℃~85℃时,恒温20分钟,然后开始缓慢加入上述剩下的预乳化的混合单体乳液,控制加入时间在2~4小时,预乳化的混合单体乳液加入完毕后开始升温,当物料温度达到90℃时恒温1小时,得到环保型湿强剂乳液。The invention discloses a preparation method of an environment-friendly wet strength agent, which comprises the following steps: mixing styrene, butyl acrylate and glycidyl methacrylate to prepare a mixed monomer; mixing the mixed monomer with deionized water, Add emulsifier and initiator potassium persulfate to carry out pre-emulsification together to obtain pre-emulsified mixed monomer emulsion; add 30 parts by weight of deionized water to a jacketed stirring tank, 15 parts by weight of pre-emulsified mixed monomer emulsion, and open Heating, when the temperature of the material reaches 75 ℃ ~ 85 ℃, keep the temperature constant for 20 minutes, then slowly add the remaining pre-emulsified mixed monomer emulsion, control the addition time in 2 to 4 hours, add the pre-emulsified mixed monomer emulsion After the completion, start to heat up, and when the temperature of the material reaches 90°C, keep the temperature for 1 hour to obtain an environment-friendly wet strength agent emulsion.
Description
技术领域technical field
本发明涉及一种环保型湿强剂的制备方法,具体地说是一种造纸用环保型湿强剂的制备方法。The invention relates to a preparation method of an environment-friendly wet strength agent, in particular to a preparation method of an environment-friendly wet strength agent for papermaking.
背景技术Background technique
湿强度是指,在一定时间中,将纸张放到水中润湿后得到的纸张强度。普通纸被润湿后,只能保持其原来干强度的2%-10%左右。由于纸浆纤维具有高度的亲水性,易吸水,当纸与水接触时,在水的作用下,自身的平衡结构被破坏,因而使其湿强度比干强度明显降低。对于某些纸或纸板,因对湿强度有较高的要求,普通纸张自身的强度无法满足需求,就需在纸浆中加入一些增强纸张湿强度的添加剂,所加入的物质为增湿强剂。Wet strength refers to the paper strength obtained after the paper is wetted in water within a certain period of time. After ordinary paper is wetted, it can only maintain about 2%-10% of its original dry strength. Because the pulp fiber is highly hydrophilic and easy to absorb water, when the paper is in contact with water, under the action of water, its own balance structure is destroyed, so its wet strength is significantly lower than the dry strength. For some paper or cardboard, due to the high requirements for wet strength, the strength of ordinary paper itself cannot meet the demand, so it is necessary to add some additives to the pulp to enhance the wet strength of paper, and the added substances are wet strength agents.
通常纸的湿强度以纸的湿强度(干纸再湿后的强度)对干强度的比率来表示,强度性质常用抗张强度来表示。通过添加湿强剂,生产出保留50%以上干抗张强度的湿强纸是可能的。但大多数种类的湿强纸,当用水浸透后只能保留20%-40%的干抗张强度。某些种类的纸,例如卫生纸,如果他们不含湿强剂就可能一点湿强度都没有,因此,如果这类纸被浸透后能够保留10%-20%的干抗张强度,也被认为是湿强纸。Usually the wet strength of the paper is expressed by the ratio of the wet strength of the paper (the strength of the dry paper after rewetting) to the dry strength, and the strength properties are usually expressed by the tensile strength. By adding wet strength agents, it is possible to produce wet strength papers that retain more than 50% of the dry tensile strength. However, most types of wet strength paper can only retain 20%-40% of the dry tensile strength when soaked in water. Some types of paper, such as toilet paper, may have no wet strength at all if they do not contain wet strength agents, so if such paper retains 10%-20% of its dry tensile strength after being saturated, it is also considered a wet strength paper.
湿强纸也可以根据它们的湿强特性来分类,某些湿强处理仅仅使强度损失的速度变慢,这类纸被称为具有临时湿强度。另外一些湿强剂能赋予纸张持久湿强度,在普通使用条件下,这类纸的湿强度在长时期内保持不变。由此湿强剂可分为永久性湿强剂和临时性湿强剂。永久性湿强剂包括脲醛树脂(UF)、三聚氰胺甲醛树脂(MF)、聚酸胺环氧氯丙烷树脂(PAE)等;临时性湿强剂包括聚乙烯亚胺(PEI)、双醛淀粉(DAS)等。Wet strength papers can also be classified according to their wet strength properties, certain wet strength treatments only slow the rate of strength loss, such papers are said to have temporary wet strength. In addition, some wet strength agents can give paper durable wet strength. Under normal use conditions, the wet strength of this kind of paper remains unchanged for a long time. Therefore, wet strength agents can be divided into permanent wet strength agents and temporary wet strength agents. Permanent wet strength agents include urea-formaldehyde resin (UF), melamine formaldehyde resin (MF), polyamide epichlorohydrin resin (PAE), etc.; temporary wet strength agents include polyethyleneimine (PEI), dialdehyde starch ( DAS), etc.
应当指出,并非各种纸的湿强度越高越持久就越好,因为大多数种类的纸需要能够再制浆,因此所需要的湿强度取决于纸的用途。湿强剂最重要的应用是用于生产卫生用纸,包括手巾纸、餐巾纸、清洁布和面巾纸。包装纸是湿强剂应用的另一个重要方面,包括纸袋、手携纸袋、牛奶纸盒、冷冻包装、肉类包装和水果盘。湿强剂也用于各种特种纸,例如招贴纸、标签纸、贴面薄页纸、壁纸、砂纸、地图纸、滤纸、电绝缘纸、印相纸、钞票纸以及其他潮湿时需要保持一定强度的纸种。It should be pointed out that it is not better for all kinds of papers to have higher and more durable wet strength, because most kinds of paper need to be able to be repulped, so the required wet strength depends on the use of the paper. The most important application for wet strength agents is in the production of hygiene tissue, including towels, napkins, cleaning cloths and facial tissues. Packaging paper is another important aspect of wet strength agent applications and includes paper bags, tote bags, milk cartons, freezer packs, meat wraps and fruit bowls. Wet strength agents are also used in various specialty papers, such as poster paper, label paper, overlay tissue paper, wallpaper, sandpaper, map paper, filter paper, electrical insulation paper, photographic paper, banknote paper, and other papers that need to maintain a certain level of stability when wet. Strong paper grade.
UF和MF典型应用于钞票纸和层压纸,双醛淀粉典型用于特种纸,聚酰胺类湿强剂主要应用于薄页纸、纸巾、液体包装纸版、层压纸、滤纸和高级纸,聚胺类湿强剂主要用于容器纸板、薄页纸和纸巾,环氧化物类则主要用于钞票纸和特种纸。UF and MF are typically used in banknote paper and laminated paper, dialdehyde starch is typically used in specialty paper, and polyamide wet strength agents are mainly used in tissue paper, tissue paper, liquid packaging paper, laminated paper, filter paper and high-grade paper , Polyamine wet strength agents are mainly used for container boards, tissue paper and paper towels, while epoxides are mainly used for banknote paper and special paper.
湿强度助剂都是热固性树脂,在干燥加热时形成不溶性防水网络体,从而对纸页起到增湿强作用。其作用发展机理如下:(1)一般情况下,将小分子而易在水中溶解的低聚合物添加到抄纸过程中,其能在短时间内迅速进入至纤维的内部结构,并在一定条件下,低聚物缩合成高聚合物,高聚物树脂分子的基团与纤维羟基基团反应生成共价键,从而增强纸张的强度;(2)一些合成的高聚合物无法进入到纤维内部,沉积于纤维之间,与纤维结合成互穿网状结构,不仅能够局限纤维间的活动,也能够限制纤维的膨胀,降低纸页伸缩变形的可能性等作用,因此保护纸张在水分子中也具有一定强度;(3)而其余合成的高分子树脂广泛存在于纤维表面,经过固化后,使纸纤维拥有难以溶于水且性能稳定的优势,从而纸张会拥有良好的湿强效果。Wet strength additives are all thermosetting resins, which form an insoluble waterproof network body when dried and heated, thus playing a role in humidifying and strengthening the paper. The development mechanism of its action is as follows: (1) In general, low polymers with small molecules and easy to dissolve in water are added to the papermaking process, which can quickly enter the internal structure of the fiber in a short time, and under certain conditions Under this condition, the oligomers condense into high polymers, and the groups of the polymer resin molecules react with the fiber hydroxyl groups to form covalent bonds, thereby enhancing the strength of the paper; (2) Some synthetic high polymers cannot enter the interior of the fibers , deposited between the fibers, and combined with the fibers to form an interpenetrating network structure, which can not only limit the movement between the fibers, but also limit the expansion of the fibers and reduce the possibility of stretching and deformation of the paper sheet, thus protecting the paper in the water molecules It also has a certain strength; (3) The remaining synthetic polymer resins are widely present on the surface of the fiber. After curing, the paper fiber has the advantages of being difficult to dissolve in water and has stable performance, so that the paper will have a good wet strength effect.
在纸张浸入水中的过程中,一般利用以下几种办法来保持本身一定的强度:一、通过增强表面交联,减少水分子浸入,加强和保护已形成的纤维共价键;二、通过添加助剂,从而结合成不溶于水的共价键;三、树脂与纤维交联得到网络结构。从而一般增湿强的反应机理包括以下两方面:第一方面为保护机理,也为限制或均交联;另一方面为增强机理,也称为新键或共交联。其中保护机理是指湿强剂分子之间进行化学反应生成共价键,会在纤维表面和空隙间,形成互穿网络结构,阻止水分子进入,则阻止纸页的强度降低;增强机理认为树脂与纤维间的羟基、羧基反应得到共价结合键,且加强了纤维间的氢键结合,从而增强湿强作用。During the process of immersing paper in water, the following methods are generally used to maintain a certain strength: 1. By strengthening the surface crosslinking, reducing the immersion of water molecules, strengthening and protecting the formed fiber covalent bonds; 2. By adding auxiliary agent, thus combining into a water-insoluble covalent bond; 3. Resin and fiber are cross-linked to obtain a network structure. Therefore, the reaction mechanism of general humidification includes the following two aspects: the first aspect is the protection mechanism, which is also restricted or homo-crosslinked; the other is the enhanced mechanism, also known as new bond or co-crosslinked. The protection mechanism refers to the chemical reaction between the wet strength agent molecules to form covalent bonds, which will form an interpenetrating network structure on the surface of the fiber and between the gaps, preventing water molecules from entering, and preventing the strength of the paper from decreasing; the strengthening mechanism believes that the resin It reacts with the hydroxyl and carboxyl groups between fibers to obtain covalent bonds, and strengthens the hydrogen bonding between fibers, thereby enhancing the wet strength.
常见的湿强剂有聚乙烯亚胺(PEI)、脲醛树脂(UF)、聚酸胺环氧氯丙烷树脂(PAE)等,均具有良好的湿强效果,同时也存在一些缺点,如脲醛树脂(UF)和三聚氰胺甲醛树脂(MF),虽使用时间最早,但由于其含有游离甲醛,污染环境,限制其应用,近年来被各国禁用;PAE 湿强效果好,各国对其需求量与日俱增,但其价格昂贵,损纸不易降解,含有致癌物质有机氯等缺点;双醛淀粉(DAS)使用时间较早,但有对环境造成很大污染的碘化物排放,使用量趋于降低。Common wet strength agents include polyethyleneimine (PEI), urea-formaldehyde resin (UF), polyamide epichlorohydrin resin (PAE), etc., all of which have good wet strength effects, but also have some disadvantages, such as urea-formaldehyde resin (UF) and melamine formaldehyde resin (MF), although they were used the first time, they have been banned by various countries in recent years because they contain free formaldehyde, pollute the environment, and restrict their application; PAE has a good wet strength effect, and the demand for it in various countries is increasing day by day, but It is expensive, broken paper is not easy to degrade, and contains carcinogens such as organochlorine; dialdehyde starch (DAS) has been used for a long time, but it has iodide emissions that cause great pollution to the environment, and its usage tends to decrease.
如今,传统湿强剂已不能满足人们的需要,为了更好地提高纸质,满足需求,各种新型湿强剂产品种类层出不穷。鉴于环保的要求,并考虑到湿部化学因素,如纸浆的接受性、pH值、固化温度、与其它助剂的相溶性、单程留着率、均匀分布性和抗干扰物的能力等,开发无污染高效湿强剂是今后势在必行的发展趋势。Nowadays, traditional wet strength agents can no longer meet people's needs. In order to better improve paper quality and meet the needs, various new types of wet strength agents have emerged in an endless stream. In view of the requirements of environmental protection, and considering the chemical factors of the wet end, such as the acceptance of pulp, pH value, curing temperature, compatibility with other additives, single-pass retention rate, uniform distribution and anti-interference ability, etc., the development Pollution-free and high-efficiency wet strength agent is an inevitable development trend in the future.
现有新型环保交联体系多为与纤维反应型的交联体系,利用这些交联体系的新型湿强剂仍未商品化,是因为他们还各有缺点,如成本高、固化温度太高、使纸发脆等、固含低等。因此,这些新型环保交联体系还需深入研究,如向天然原料移植降低成本,改进聚合工艺增加分子量,开发可实用的工艺,研究再制浆性能等。Most of the existing new environmentally friendly cross-linking systems are cross-linking systems that react with fibers. The new wet strength agents using these cross-linking systems have not yet been commercialized because they still have their own shortcomings, such as high cost, too high curing temperature, Make paper brittle and low solid content. Therefore, these new environmentally friendly cross-linking systems still need to be further studied, such as transplanting to natural raw materials to reduce costs, improving the polymerization process to increase molecular weight, developing practical processes, and studying repulping performance.
聚苯乙烯/甲基丙烯酸缩水甘油酯湿强剂可以替代现有的湿强剂,从而满足社会对环保的要求,乃至提高湿强剂的效能,减少湿强剂制备的成本。The polystyrene/glycidyl methacrylate wet strength agent can replace the existing wet strength agent, so as to meet the social requirements for environmental protection, even improve the performance of the wet strength agent, and reduce the cost of wet strength agent preparation.
中国专利CN201711303433.4公开了一种纸张湿强剂的制备方法。本发明以聚赖氨酸为原料,丙烯酸为接枝单体,通过交联剂制备了一种聚赖氨酸水凝胶,再与聚丙烯酰胺进行反应,提高吸附阴离子能力,且纸张纤维带负电荷,从而提高其留着率,同时利用过硫酸钾为质子源,在加热的情况下,过硫酸钾缓慢分解,为聚赖氨酸提供氢离子,降低聚赖氨酸的亲水性能,从而提高纸张的抗水性能,此外,还通过环氧氯丙烷进行烷基化反应,环氧交联基团的引入增加了分子链段的交联活性,进一步增强了聚合物和纤维间的亲和力,其分子链的交联网状结构,有效地限制了纤维和纤维间的活动,阻止了纤维的润胀和吸水,从而提高了纸张的湿强度。Chinese patent CN201711303433.4 discloses a preparation method of paper wet strength agent. In the present invention, polylysine is used as raw material, acrylic acid is used as grafting monomer, a polylysine hydrogel is prepared through a crosslinking agent, and then reacted with polyacrylamide to improve the ability to absorb anions, and the paper fiber tape Negative charge, thereby improving its retention rate, while using potassium persulfate as a proton source, under the condition of heating, potassium persulfate slowly decomposes, providing hydrogen ions for polylysine, reducing the hydrophilic property of polylysine, In order to improve the water resistance of paper, in addition, through the alkylation reaction of epichlorohydrin, the introduction of epoxy crosslinking groups increases the crosslinking activity of molecular segments, and further enhances the affinity between polymers and fibers , the cross-linked structure of its molecular chains effectively limits the activities between fibers and fibers, prevents swelling and water absorption of fibers, and thus improves the wet strength of paper.
中国专利CN201711102105.8公开了一种复合型造纸湿强剂及其制备方法,复合型湿强剂由以下成分按照重量比组成:脲醛树脂为5-9份、羧甲基纤维素钠为4-7份、醋酸钾为8-10份、对甲基苯磺酸为2-4份、聚乙二醇为4-6份、丙酮为5-8份、水为105-120份。本发明的复合型湿强剂具有较好的稳定性和干湿抗张强度,可以广泛应用于造纸行业中,提升产品的品质。Chinese patent CN201711102105.8 discloses a composite papermaking wet strength agent and its preparation method. The composite wet strength agent is composed of the following components according to the weight ratio: 5-9 parts of urea-formaldehyde resin, 4-9 parts of carboxymethyl cellulose sodium 7 parts, 8-10 parts of potassium acetate, 2-4 parts of p-toluenesulfonic acid, 4-6 parts of polyethylene glycol, 5-8 parts of acetone, and 105-120 parts of water. The composite wet strength agent of the invention has better stability and dry and wet tensile strength, and can be widely used in the papermaking industry to improve the quality of products.
中国专利CN201711088238.4公开了一种环保型造纸湿强剂及其制备方法,环保型造纸湿强剂包括以下重量份计的原料:二乙烯三胺10~20份、碳酸氢钠20~30份、羟乙基纤维素30~50份、二乙二醇二丙烯酸酯36~40份、十六烷酸钙45~50份、十六酸十六酯45~50份、二甲基硅油40~50份、阳离子聚丙烯酰胺60~70份、二元酸40~50份、多元醇20~35份。其制备方法是将二乙烯三胺、碳酸氢钠、羟乙基纤维素、二乙二醇二丙烯酸酯、十六烷酸钙搅拌反应,升温后加入剩余组分进行保温反应;滴加pH调节剂。本湿强剂在制备过程中不添加对人体有害的有机溶剂,无游离甲醛的释放,副产物不会污染环境,环保健康。本湿强剂能够提高纸张的湿抗涨强度和干抗涨强度,可以大大提高纸张表面的抗水性能。Chinese patent CN201711088238.4 discloses an environment-friendly papermaking wet strength agent and its preparation method. The environment-friendly papermaking wet strength agent includes the following raw materials in parts by weight: 10-20 parts of diethylenetriamine, 20-30 parts of sodium bicarbonate , 30-50 parts of hydroxyethyl cellulose, 36-40 parts of diethylene glycol diacrylate, 45-50 parts of calcium hexadecanoate, 45-50 parts of cetyl palmitate, 40-40 parts of dimethicone 50 parts, 60-70 parts of cationic polyacrylamide, 40-50 parts of dibasic acid, 20-35 parts of polyol. The preparation method is to stir and react diethylenetriamine, sodium bicarbonate, hydroxyethyl cellulose, diethylene glycol diacrylate and calcium hexadecanoate, add the remaining components after heating up and carry out heat preservation reaction; dropwise add pH adjustment agent. In the preparation process of the wet strength agent, no organic solvent harmful to human body is added, no free formaldehyde is released, and by-products do not pollute the environment, and are environmentally friendly and healthy. The wet strength agent can improve the wet swelling strength and dry swelling strength of paper, and can greatly improve the water resistance of the paper surface.
本发明的目标是制备高效的湿强剂,选用甲基丙烯酸缩水甘油酯作为环氧功能单体,赋予聚合物一定的反应性,使合成的湿强剂能与纤维中的亲核基团发生交联反应;选用苯乙烯作为硬单体,苯环能够提供优秀的憎水性,且能提高结构强度、膜层内聚力和耐磨性,选用玻璃化温度较低的丙烯酸丁酯作为软单体,赋予共聚物良好的柔韧性,使纸张不会脆化。The object of the present invention is to prepare a highly efficient wet strength agent. Glycidyl methacrylate is selected as the epoxy functional monomer to endow the polymer with a certain reactivity, so that the synthesized wet strength agent can react with the nucleophilic group in the fiber. Cross-linking reaction: Styrene is selected as the hard monomer, and the benzene ring can provide excellent hydrophobicity, and can improve structural strength, film cohesion and wear resistance, and butyl acrylate with a lower glass transition temperature is selected as the soft monomer. Give the copolymer good flexibility, so that the paper will not be brittle.
发明内容Contents of the invention
本发明的目的是提供一种环保型湿强剂的制备方法,以解决现有技术存在的上述问题。The purpose of the present invention is to provide a preparation method of an environment-friendly wet strength agent to solve the above-mentioned problems in the prior art.
本发明的一种环保型湿强剂的制备方法包括如下步骤:A kind of preparation method of environment-friendly type wet strength agent of the present invention comprises the steps:
一种环保型湿强剂的制备方法,包括如下步骤:将苯乙烯35~40重量份、丙烯酸丁酯25~30重量份、甲基丙烯酸缩水甘油酯15~20重量份进行混合制备成混合单体;A preparation method of an environment-friendly wet strength agent, comprising the steps of: mixing 35-40 parts by weight of styrene, 25-30 parts by weight of butyl acrylate, and 15-20 parts by weight of glycidyl methacrylate to prepare a mixed unit body;
将去离子水100~120重量份加入到搅拌槽中,开启搅拌,加入乳化剂CO436 0.8~1.2重量份,充分搅拌使乳化剂分散均匀;然后向搅拌槽中缓慢加入混合单体,充分搅拌使混合单体乳化形成乳液,混合单体加入完毕后再加入引发剂过硫酸钾0.5~1.0重量份,充分搅拌使引发剂过硫酸钾溶解,最后得到预乳化的混合单体乳液;Add 100-120 parts by weight of deionized water into the stirring tank, start stirring, add 0.8-1.2 parts by weight of emulsifier CO436, stir well to disperse the emulsifier evenly; then slowly add mixed monomers into the stirring tank, stir fully to make The mixed monomers are emulsified to form an emulsion, after the mixed monomers are added, 0.5 to 1.0 parts by weight of the initiator potassium persulfate is added, and the initiator potassium persulfate is fully stirred to dissolve the initiator, and finally a pre-emulsified mixed monomer emulsion is obtained;
往一带夹套搅拌釜中加入去离子水30重量份,开启搅拌,再加入上述预乳化的混合单体乳液15重量份,开启加热,当物料温度达到75℃~85℃时,恒温20分钟,然后开始缓慢加入上述剩下的预乳化的混合单体乳液,控制加入时间在2~4小时,预乳化的混合单体乳液加入完毕后开始升温,当物料温度达到90℃时恒温1小时,得到环保型湿强剂乳液。Add 30 parts by weight of deionized water into a jacketed stirring tank, start stirring, then add 15 parts by weight of the above-mentioned pre-emulsified mixed monomer emulsion, start heating, when the temperature of the material reaches 75°C-85°C, keep the temperature constant for 20 minutes, Then start to slowly add the above remaining pre-emulsified mixed monomer emulsion, control the addition time in 2 to 4 hours, start to heat up after the pre-emulsified mixed monomer emulsion has been added, and keep the temperature for 1 hour when the material temperature reaches 90°C. Environmentally friendly wet strength agent emulsion.
具体实施方式Detailed ways
实施例1Example 1
将苯乙烯35kg、丙烯酸丁酯30kg、甲基丙烯酸缩水甘油酯15kg进行混合制备成混合单体;将去离子水100kg加入到搅拌槽中,开启搅拌,加入乳化剂CO436 1.2kg,充分搅拌使乳化剂分散均匀;然后向搅拌槽中缓慢加入混合单体,充分搅拌使混合单体乳化形成乳液,混合单体加入完毕后再加入引发剂过硫酸钾1.0kg,充分搅拌使引发剂过硫酸钾溶解,最后得到预乳化的混合单体乳液;往一带夹套搅拌釜中加入去离子水30kg,开启搅拌,再加入上述预乳化的混合单体乳液15kg,开启加热,当物料温度达到85℃时,恒温20分钟,然后开始缓慢加入上述剩下的预乳化的混合单体乳液,控制加入时间在3小时,预乳化的混合单体乳液加入完毕后开始升温,当物料温度达到90℃时恒温1小时,得到环保型湿强剂乳液。Mix 35kg of styrene, 30kg of butyl acrylate, and 15kg of glycidyl methacrylate to prepare a mixed monomer; add 100kg of deionized water into the stirring tank, start stirring, add 1.2kg of emulsifier CO436, and stir fully to emulsify The agent is evenly dispersed; then slowly add the mixed monomer into the stirring tank, stir fully to emulsify the mixed monomer to form an emulsion, add 1.0 kg of initiator potassium persulfate after adding the mixed monomer, and fully stir to dissolve the initiator potassium persulfate , and finally obtain a pre-emulsified mixed monomer emulsion; add 30 kg of deionized water to a jacketed stirring tank, start stirring, then add 15 kg of the above-mentioned pre-emulsified mixed monomer emulsion, and start heating. When the temperature of the material reaches 85 ° C, Keep the temperature constant for 20 minutes, then slowly add the remaining pre-emulsified mixed monomer emulsion, control the addition time at 3 hours, start to heat up after the pre-emulsified mixed monomer emulsion is added, and keep the temperature for 1 hour when the material temperature reaches 90°C , to obtain an environment-friendly wet strength agent emulsion.
实施例2Example 2
将苯乙烯40kg、丙烯酸丁酯29kg、甲基丙烯酸缩水甘油酯20kg进行混合制备成混合单体;将去离子水115kg加入到搅拌槽中,开启搅拌,加入乳化剂CO436 1.1kg,充分搅拌使乳化剂分散均匀;然后向搅拌槽中缓慢加入混合单体,充分搅拌使混合单体乳化形成乳液,混合单体加入完毕后再加入引发剂过硫酸钾0.9kg,充分搅拌使引发剂过硫酸钾溶解,最后得到预乳化的混合单体乳液;往一带夹套搅拌釜中加入去离子水30kg,开启搅拌,再加入上述预乳化的混合单体乳液15kg,开启加热,当物料温度达到82℃时,恒温20分钟,然后开始缓慢加入上述剩下的预乳化的混合单体乳液,控制加入时间在2.5小时,预乳化的混合单体乳液加入完毕后开始升温,当物料温度达到90℃时恒温1小时,得到环保型湿强剂乳液。Mix 40kg of styrene, 29kg of butyl acrylate, and 20kg of glycidyl methacrylate to prepare a mixed monomer; add 115kg of deionized water into the stirring tank, start stirring, add 1.1kg of emulsifier CO436, and stir fully to emulsify The agent is evenly dispersed; then slowly add the mixed monomer into the stirring tank, fully stir to emulsify the mixed monomer to form an emulsion, add 0.9 kg of initiator potassium persulfate after adding the mixed monomer, and fully stir to dissolve the initiator potassium persulfate , and finally obtain a pre-emulsified mixed monomer emulsion; add 30 kg of deionized water to a jacketed stirring tank, start stirring, then add 15 kg of the above-mentioned pre-emulsified mixed monomer emulsion, and start heating. When the temperature of the material reaches 82 ° C, Keep the temperature constant for 20 minutes, then slowly add the remaining pre-emulsified mixed monomer emulsion, control the addition time at 2.5 hours, start to heat up after the pre-emulsified mixed monomer emulsion is added, and keep the temperature for 1 hour when the material temperature reaches 90°C , to obtain an environment-friendly wet strength agent emulsion.
实施例3Example 3
将苯乙烯35kg、丙烯酸丁酯25kg、甲基丙烯酸缩水甘油酯15kg进行混合制备成混合单体;将去离子水100kg加入到搅拌槽中,开启搅拌,加入乳化剂CO436 0.8kg,充分搅拌使乳化剂分散均匀;然后向搅拌槽中缓慢加入混合单体,充分搅拌使混合单体乳化形成乳液,混合单体加入完毕后再加入引发剂过硫酸钾0.5kg,充分搅拌使引发剂过硫酸钾溶解,最后得到预乳化的混合单体乳液;往一带夹套搅拌釜中加入去离子水30kg,开启搅拌,再加入上述预乳化的混合单体乳液15kg,开启加热,当物料温度达到75℃℃时,恒温20分钟,然后开始缓慢加入上述剩下的预乳化的混合单体乳液,控制加入时间在2小时,预乳化的混合单体乳液加入完毕后开始升温,当物料温度达到90℃时恒温1小时,得到环保型湿强剂乳液。Mix 35kg of styrene, 25kg of butyl acrylate, and 15kg of glycidyl methacrylate to prepare a mixed monomer; add 100kg of deionized water into the stirring tank, start stirring, add 0.8kg of emulsifier CO436, and stir fully to emulsify The agent is evenly dispersed; then slowly add the mixed monomer into the stirring tank, fully stir to emulsify the mixed monomer to form an emulsion, add 0.5 kg of initiator potassium persulfate after adding the mixed monomer, and fully stir to dissolve the initiator potassium persulfate , and finally obtain a pre-emulsified mixed monomer emulsion; add 30 kg of deionized water to a jacketed stirring tank, start stirring, then add 15 kg of the above-mentioned pre-emulsified mixed monomer emulsion, and start heating, when the material temperature reaches 75 °C , keep the temperature for 20 minutes, then start to slowly add the remaining pre-emulsified mixed monomer emulsion, control the addition time at 2 hours, start to heat up after the pre-emulsified mixed monomer emulsion is added, when the temperature of the material reaches 90 ° C, keep the temperature for 1 Hours, an environment-friendly wet strength agent emulsion was obtained.
实施例4Example 4
将苯乙烯40kg、丙烯酸丁酯30kg、甲基丙烯酸缩水甘油酯20kg进行混合制备成混合单体;将去离子水120kg加入到搅拌槽中,开启搅拌,加入乳化剂CO436 1.2kg,充分搅拌使乳化剂分散均匀;然后向搅拌槽中缓慢加入混合单体,充分搅拌使混合单体乳化形成乳液,混合单体加入完毕后再加入引发剂过硫酸钾1.0kg,充分搅拌使引发剂过硫酸钾溶解,最后得到预乳化的混合单体乳液;往一带夹套搅拌釜中加入去离子水30kg,开启搅拌,再加入上述预乳化的混合单体乳液15kg,开启加热,当物料温度达到85℃时,恒温20分钟,然后开始缓慢加入上述剩下的预乳化的混合单体乳液,控制加入时间在4小时,预乳化的混合单体乳液加入完毕后开始升温,当物料温度达到90℃时恒温1小时,得到环保型湿强剂乳液。Mix 40kg of styrene, 30kg of butyl acrylate, and 20kg of glycidyl methacrylate to prepare a mixed monomer; add 120kg of deionized water into the stirring tank, start stirring, add 1.2kg of emulsifier CO436, and stir fully to emulsify The agent is evenly dispersed; then slowly add the mixed monomer into the stirring tank, stir fully to emulsify the mixed monomer to form an emulsion, add 1.0 kg of initiator potassium persulfate after adding the mixed monomer, and fully stir to dissolve the initiator potassium persulfate , and finally obtain a pre-emulsified mixed monomer emulsion; add 30 kg of deionized water to a jacketed stirring tank, start stirring, then add 15 kg of the above-mentioned pre-emulsified mixed monomer emulsion, and start heating. When the temperature of the material reaches 85 ° C, Keep the temperature constant for 20 minutes, then start to slowly add the remaining pre-emulsified mixed monomer emulsion, control the addition time at 4 hours, start to heat up after the pre-emulsified mixed monomer emulsion is added, and keep the temperature for 1 hour when the material temperature reaches 90°C , to obtain an environment-friendly wet strength agent emulsion.
实施例5Example 5
将苯乙烯38kg、丙烯酸丁酯27kg、甲基丙烯酸缩水甘油酯18kg进行混合制备成混合单体;将去离子水110kg加入到搅拌槽中,开启搅拌,加入乳化剂CO436 1.0kg,充分搅拌使乳化剂分散均匀;然后向搅拌槽中缓慢加入混合单体,充分搅拌使混合单体乳化形成乳液,混合单体加入完毕后再加入引发剂过硫酸钾0.8kg,充分搅拌使引发剂过硫酸钾溶解,最后得到预乳化的混合单体乳液;往一带夹套搅拌釜中加入去离子水30kg,开启搅拌,再加入上述预乳化的混合单体乳液15kg,开启加热,当物料温度达到80℃时,恒温20分钟,然后开始缓慢加入上述剩下的预乳化的混合单体乳液,控制加入时间在3小时,预乳化的混合单体乳液加入完毕后开始升温,当物料温度达到90℃时恒温1小时,得到环保型湿强剂乳液。Mix 38kg of styrene, 27kg of butyl acrylate, and 18kg of glycidyl methacrylate to prepare a mixed monomer; add 110kg of deionized water into the stirring tank, start stirring, add 1.0kg of emulsifier CO436, and stir fully to emulsify The agent is evenly dispersed; then slowly add the mixed monomer into the stirring tank, fully stir to emulsify the mixed monomer to form an emulsion, add 0.8 kg of initiator potassium persulfate after adding the mixed monomer, and fully stir to dissolve the initiator potassium persulfate , and finally obtain a pre-emulsified mixed monomer emulsion; add 30 kg of deionized water to a jacketed stirring tank, start stirring, then add 15 kg of the above-mentioned pre-emulsified mixed monomer emulsion, and start heating. When the temperature of the material reaches 80 ° C, Keep the temperature constant for 20 minutes, then slowly add the remaining pre-emulsified mixed monomer emulsion, control the addition time at 3 hours, start to heat up after the pre-emulsified mixed monomer emulsion is added, and keep the temperature for 1 hour when the material temperature reaches 90°C , to obtain an environment-friendly wet strength agent emulsion.
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