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CN114606799B - High-performance base paper of paper-mixing adhesive tape, production method and paper-mixing adhesive tape using base paper - Google Patents

High-performance base paper of paper-mixing adhesive tape, production method and paper-mixing adhesive tape using base paper
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CN114606799B
CN114606799BCN202210266543.2ACN202210266543ACN114606799BCN 114606799 BCN114606799 BCN 114606799BCN 202210266543 ACN202210266543 ACN 202210266543ACN 114606799 BCN114606799 BCN 114606799B
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paper
fiber
base paper
surface sizing
pulp
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CN114606799A (en
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周振宇
华一鸣
林晓毅
毛香琴
颜鲁呜
郭婉
郑蓉
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Zhejiang Kaien New Material Co ltd
Zhejiang Yuanrun Electronic Materials Co ltd
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Zhejiang Kan Special Paper Co ltd
Zhejiang Kan Specialties Material Co ltd
Zhejiang Kaien New Material Co ltd
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Abstract

Translated fromChinese

本发明属于特种纸新材料技术领域,尤其涉及一种高性能和纸胶带原纸、生产方法和采用该原纸的和纸胶带。该原纸配方包括以下纤维类原料:5‑20份化学纤维,20‑50份漂白短纤维木浆和50‑80份漂白长纤维木浆;所述漂白短纤维木浆采用化学制浆法制得。通过该配方原料制备得到的原纸产品封闭性能好,手感更柔软、撕裂度更高、抗渗透及抗老化性能更好、印刷性能更优越、色泽更艳丽且色彩饱满,产品做成胶带后有一种通透润泽感,产品更受用户喜欢。The invention belongs to the technical field of new special paper materials, and in particular relates to a high-performance washi tape base paper, a production method and a washi tape using the base paper. The base paper formula includes the following fiber raw materials: 5-20 parts of chemical fibers, 20-50 parts of bleached short-fiber wood pulp and 50-80 parts of bleached long-fiber wood pulp; the bleached short-fiber wood pulp is prepared by a chemical pulping method. The base paper product prepared by this formula raw material has good sealing performance, softer hand feeling, higher tearing degree, better anti-permeation and anti-aging performance, superior printing performance, brighter and fuller color. A transparent and moist feeling, the product is more popular with users.

Description

Translated fromChinese
一种高性能和纸胶带原纸、生产方法和采用该原纸的和纸胶带A kind of base paper of high-performance washi adhesive tape, production method and washi using the base paperadhesive tape

技术领域technical field

本发明属于特种纸新材料技术领域,尤其涉及一种高性能和纸胶带原纸、生产方法和采用该原纸的和纸胶带。The invention belongs to the technical field of new special paper materials, and in particular relates to a high-performance washi tape base paper, a production method and a washi tape using the base paper.

背景技术Background technique

和纸胶带原纸用于制作和纸胶带的基础材料,和纸胶带原纸一面涂硅类的防粘层,另一面涂上丙烯酸类的胶水,制成和纸胶带。如果需要印刷的产品,先在和纸胶带原纸表面进行印刷,然后再涂硅和上胶两道工序。和纸胶带用途:工业系统中140℃以下遮护烤漆用,比如汽车喷漆;和纸胶带纸质柔软,适合运动器材、橡塑胶部件及建筑工地,室内外装潢、装修喷刷油漆时遮蔽用途;现还大量用于DIY制作、包装、文具礼品配套、制作微广告等。和纸胶带有:黄色,红色,黑色,白色,蓝色等各种颜色,色彩丰富,艳丽。白色的和纸胶带还可以印上各种图案,非常漂亮。使用特性:是一种理想薄型胶带,有良好的附着力粘性适中,要求有超好柔韧性,对大多数的平滑表面、弯曲或转角处有很好的贴附性及遮蔽性,作业性良好,易撕拉、易书写、易贴易揭,使用后快速撕除,不留残胶。Washi tape base paper is used as the basic material for making washi tape. One side of the washi tape base paper is coated with a silicon-based anti-adhesive layer, and the other side is coated with an acrylic glue to make a washi tape. If you need printed products, first print on the base paper surface of the washi tape, and then apply silicon and glue two processes. Use of washi tape: it is used to cover baking paint below 140°C in industrial systems, such as car spray paint; washi tape is soft in paper, suitable for sports equipment, rubber and plastic parts and construction sites, indoor and outdoor decoration, decoration and painting for covering purposes ; Now it is also widely used in DIY production, packaging, stationery gift matching, making micro-advertisements, etc. Washi tape is available in various colors such as yellow, red, black, white, blue, etc., with rich and bright colors. White washi tape can also be printed with various patterns, which is very beautiful. Features: It is an ideal thin adhesive tape with good adhesion and moderate viscosity, which requires super flexibility. It has good adhesion and shielding properties to most smooth surfaces, bends or corners, and has good workability. , easy to tear, easy to write, easy to stick and easy to peel off, quickly tear off after use, leaving no glue residue.

已有中国发明专利(公开号:CN105155329A)公开了和纸胶带原纸及其生产方法;该产品原料上选用长纤维木浆、短纤维化学机械木浆、湿强剂、涂布胶乳、黄栢萃取液,通过打浆处理、加入助剂、过冷处理、抄造处理、涂布处理、成纸这些步骤获得和纸胶带原纸。该专利中所选用的化学机械木浆简称化机浆,化机浆的性质和用途:化学机械法制浆的化学预处理比化学法制浆的蒸煮过程温和得多,对原料的脱木素作用较小,对纤维素的破坏也少,仅分子量较低的半纤维素溶出较多,因此,所制得的化机浆一般含有较高的木素和纤维素组分。这种纸浆的物理强度介于化学浆与机械浆之间,能使成纸具有十分良好的挺度,其漂白性、水化和滤水性能比较接近于机械浆,滤水性能好。经过适当漂白的化机浆则多用于生产纸板、新闻纸、中低档印刷纸或配用于涂布加工原纸等。There is a Chinese invention patent (publication number: CN105155329A) disclosing washi tape base paper and its production method; the raw materials of this product are long fiber wood pulp, short fiber chemical mechanical wood pulp, wet strength agent, coating latex, cork extract Liquid, through the steps of beating treatment, adding additives, supercooling treatment, papermaking treatment, coating treatment, and paper forming, the washi tape base paper is obtained. The chemi-mechanical wood pulp used in this patent is referred to as chemi-mechanical pulp. The properties and uses of chemi-mechanical pulp: the chemical pretreatment of chemi-mechanical pulping is much milder than the cooking process of chemical pulping. The effect is small, and the damage to cellulose is also small. Only the hemicellulose with lower molecular weight is more dissolved. Therefore, the prepared chemical-mechanical pulp generally contains higher lignin and cellulose components. The physical strength of this kind of pulp is between chemical pulp and mechanical pulp, which can make the paper have very good stiffness, and its bleaching property, hydration and water drainage performance are relatively close to mechanical pulp, and the water drainage performance is good. Properly bleached chemical-mechanical pulp is mostly used in the production of cardboard, newsprint, medium and low-grade printing paper or as base paper for coating processing.

漂白阔叶木化学机械浆中有大量的纤维束存在,浆料疏解2小时后还有少量成束的纤维,必须要打浆到30°SR以上才没有纤维束,才能抄造匀度好的纸张。There are a large number of fiber bundles in bleached hardwood chemical mechanical pulp, and there are still a small amount of bundled fibers after the pulp is decomposed for 2 hours. It must be beaten to 30°SR or above to have no fiber bundles, so that paper with good formation can be produced.

黄栢萃取液即黄柏提取物(phellodendronbarkextract)提取于芸香科植物黄皮树或黄檗的干燥树皮。前者习称“川黄柏”,后者习称“关黄柏”。剥取树皮后,除去粗皮,晒干。黄柏别称黄檗、元柏、檗木、檗皮Chemicalbook,主要成分为小檗碱。用作苦味剂。具有抗微生物及原虫,降压,抗肾上腺素样作用,松弛血管平滑肌,兴奋子宫、膀胱、支气管、胃肠道,利胆及兴奋大脑皮层的作用。经过对比试验黄栢萃取液对提升和纸胶带抗老化性能没有明显的提升,在生产高性能和纸胶带原纸时可以不用添加。Phellodendron barkextract is extracted from the dry bark of the Rutaceae plant Phellodendron bark or Phellodendron barkextract. The former is commonly called "Sichuan Phellodendron", and the latter is commonly called "Guan Phellodendron". After peeling off the bark, remove the rough bark and dry it in the sun. Cortex Phellodendron is also known as Cortex Phellodendron, Yuanbai, Berberis Wood, Berberis Bark, and its main component is berberine. Used as a bittering agent. It has anti-microbial and protozoa, antihypertensive, anti-adrenaline-like effects, relaxes vascular smooth muscle, excites the uterus, bladder, bronchus, gastrointestinal tract, choleretic and excites the cerebral cortex. After comparative tests, Phellodendron Phellodendron extract did not significantly improve the anti-aging performance of washi tape, so it does not need to be added when producing high-performance washi tape base paper.

上述工艺不足之处有:1)和纸胶带原纸必须有很好的匀度,因为定量低,涂布或施胶前的定量一般控制在26-30g/m2,中国发明专利(公开号:CN105155329A)公开了和纸胶带原纸及其生产方法中该产品纤维原料上选用针叶木浆和短纤维化学机械木浆,而为了达到很好的外观匀度,就必须对阔叶木化学机械浆打浆到30°SR以上才没有纤维束,才能抄造匀度好的纸张。这种原料配比抄成的原纸紧度指标高,透气度指标低,不利于后道工序涂布液的吸收,这种纸手感会偏硬;如果含有阔叶木化机浆的混合浆只打到15-20°SR,抄造出的纸张中会有较多的纤维束引起的白点,总体纤维分布也不均匀,影响纸的外观质量;2)化学机械木浆本身硬度高,浆中含有较多木素,使成纸具有十分良好的挺度,含有25%阔叶木化机浆的纸张,会使最终产品手感偏硬。木片中纤维之间含有大量的木素把木片中的纤维粘合在一起,采用化机浆的生产方式,木片先经过化学预处理,化学预处理较温和,木素溶出量很少,再使用盘磨的机械力来把纤维强制分离开,这样处理后浆里纤维之间还有较大量的木素存在,成品浆中还有很多纤维没有单独疏解开,有较大部分是几根纤维粘合在一起,同时很多纤维在木片经过盘磨的机械摩擦过程中受到较大损伤,使成浆中的纤维和纤维束大小、长短极不规则,其中含有很多细小纤维,同时有较大部分纤维或纤维束颗粒尺寸远大于单根纤维尺寸,用这种浆抄的纸张空隙偏大,纸透气度偏低,紧度偏高,不利于纸张的耐水、耐溶剂性能,容易渗水、渗溶剂;3)从表1中可看到漂白阔叶木化机浆亮度只有76.1%,比其他漂白化学浆亮度低约10%,这样抄造出的纸张亮度会低一些,影响白纸的外观质量,如果做彩色的和纸,因原纸亮度低,染成的纸张颜色会不够艳丽,影响纸的外观质量;4)化学机械木浆还有一明显缺点:漂白化机浆中还残留有较多木素,抄成纸后极易发生返黄现象,抗老化性能差,纤维同时变脆,易折断,强度下降明显;5)该技术只经过一道涂布,同时上胶量少,纸表面的封闭性不够,不利于纸张的耐水、耐溶剂性能;6)纸没有经过超级软压光,纸表面光泽性和封闭性也相对较差,纸的手感也会相对偏硬。The disadvantages of the above process are: 1) The base paper of the washi tape must have a good evenness, because the basis weight is low, and the basis weight before coating or sizing is generally controlled at 26-30g/m2 , the Chinese invention patent (publication number: CN105155329A) discloses Japanese paper tape base paper and production method thereof, selects coniferous wood pulp and short fiber chemical mechanical wood pulp on the fiber raw material of this product, and in order to reach good appearance uniformity, just must beat hardwood chemical mechanical pulp to Above 30°SR, there will be no fiber bundles, and paper with good evenness can be produced. The base paper made of this kind of raw material ratio has high tightness index and low air permeability index, which is not conducive to the absorption of coating liquid in the subsequent process. This kind of paper will feel hard; if the mixed pulp containing hardwood chemical pulp is only To 15-20°SR, there will be more white spots caused by fiber bundles in the paper produced, and the overall fiber distribution is not uniform, which will affect the appearance quality of the paper; 2) The chemical mechanical wood pulp itself has high hardness, and the pulp contains More lignin makes the paper have very good stiffness, and the paper containing 25% hardwood chemical pulp will make the final product feel harder. There is a large amount of lignin between the fibers in the wood chips to bind the fibers in the wood chips together. The production method of chemical mechanical pulp is adopted. The wood chips are chemically pretreated first. The chemical pretreatment is relatively mild, and the amount of lignin dissolved is very small, and then used The mechanical force of the disc mill is used to forcibly separate the fibers. In this way, there is still a large amount of lignin between the fibers in the pulp after treatment. There are still many fibers in the finished pulp that have not been loosened separately. Together, at the same time, many fibers are greatly damaged during the mechanical friction process of the wood chips through the disc grinding, so that the size and length of the fibers and fiber bundles in the pulp are extremely irregular, which contains many fine fibers and a large part of them Or the particle size of the fiber bundle is much larger than the size of a single fiber. The paper made with this kind of pulp has a large void, low air permeability and high tightness, which is not conducive to the water resistance and solvent resistance of the paper, and is easy to seep water and solvent; 3) It can be seen from Table 1 that the brightness of bleached hardwood chemical pulp is only 76.1%, which is about 10% lower than that of other bleached chemical pulps. In this way, the brightness of the paper produced will be lower, which will affect the appearance quality of white paper. For colored washi paper, due to the low brightness of the base paper, the color of the dyed paper will not be bright enough, which will affect the appearance quality of the paper; 4) There is another obvious disadvantage of chemical mechanical wood pulp: there is still a lot of lignin in the bleached mechanical pulp, which is difficult to copy. After the paper is finished, yellowing phenomenon is very easy to occur, the anti-aging performance is poor, the fiber becomes brittle at the same time, easy to break, and the strength drops significantly; It is not conducive to the water resistance and solvent resistance of the paper; 6) The paper has not been super soft calendered, the gloss and sealing of the paper surface are relatively poor, and the hand feeling of the paper will be relatively hard.

发明内容Contents of the invention

为了改善并解决上述现有产品技术存在的问题,本发明的目的是提供一种高性能和纸胶带原纸及其生产方法,采用了化学短纤维和漂白的天然木浆纤维混合作为纤维类原料,其中天然木浆短纤维由化学制浆法获得。通过该配方原料制备得到的原纸产品封闭性能好,手感更柔软、撕裂度更高、抗渗透及抗老化性能更好、印刷性能更优越、色泽更艳丽且色彩饱满,产品做成胶带后有一种通透润泽感,产品更受用户喜欢。In order to improve and solve the problems existing in the above-mentioned existing product technology, the object of the present invention is to provide a kind of high-performance washi tape base paper and its production method, which adopts the mixing of short chemical fibers and bleached natural wood pulp fibers as fiber raw materials, Among them, natural wood pulp short fibers are obtained by chemical pulping. The base paper product prepared by this formula raw material has good sealing performance, softer hand feeling, higher tearing degree, better anti-permeation and anti-aging performance, superior printing performance, brighter and fuller color. A transparent and moist feeling, the product is more popular with users.

为了实现上述的目的,本发明采用了以下的技术方案:In order to achieve the above object, the present invention adopts the following technical solutions:

一种高性能和纸胶带原纸,按质量份数计,该和纸胶带原纸的纤维浆料的配方由以下的纤维类原料组成:A high-performance washi tape base paper, in terms of parts by mass, the fiber slurry formula of the washi tape base paper consists of the following fiber raw materials:

化学纤维5-20份,5-20 parts of chemical fiber,

漂白短纤维木浆20-50份,20-50 parts of bleached short-fiber wood pulp,

漂白长纤维木浆50-80份;50-80 parts of bleached long fiber wood pulp;

其中漂白短纤维木浆+漂白长纤维木浆为100份;所述的化学纤维的规格为:0.4-3.0dtex,长度为2-10mm;所述漂白短纤维木浆采用化学制浆法制得,漂白短纤维木浆的纤维长度为0.65-1.0mm,纤维的宽度为18-23μm,漂白长纤维木浆的纤维长度为1.50-3.0mm,纤维的宽度为28-35μm。Wherein bleached short-fiber wood pulp + bleached long-fiber wood pulp is 100 parts; the specification of the chemical fiber is: 0.4-3.0dtex, and the length is 2-10mm; the bleached short-fiber wood pulp is made by chemical pulping method, The fiber length of the bleached short-fiber wood pulp is 0.65-1.0 mm, and the fiber width is 18-23 μm, and the fiber length of the bleached long-fiber wood pulp is 1.50-3.0 mm, and the fiber width is 28-35 μm.

在上述配比中选用了部分的漂白短纤维木浆,漂白短纤维木浆选用化学制浆法,每根纤维都单独游离存在,纤维的外形由于没有收到强力的机械损伤,尺寸保留比较完整均一,同时化学制浆法生产的浆中极少含有木素,用这种浆抄造的纸张和用化机浆抄造的纸张相比手感明显会较柔软,纤维分布均匀,纸张匀度好,亮度会更高,纸的孔径更小。Part of the bleached short-fiber wood pulp is selected in the above ratio. The bleached short-fiber wood pulp adopts the chemical pulping method, and each fiber exists independently. The shape of the fiber has not received strong mechanical damage, and the size is relatively complete. Homogeneous, at the same time, the pulp produced by chemical pulping method contains very little lignin. Compared with the paper made by chemical pulp, the paper made by this kind of pulp will have a softer hand feeling, even fiber distribution, good paper evenness, and brightness. It will be higher and the paper will have a smaller pore size.

在上述配比中选用了5-20%的涤纶纤维或粘胶纤维,是因为选用的涤纶纤维或粘胶纤维和漂白短纤维木浆、漂白长纤维木浆相比,纤维宽度更小,纤维外形尺寸更均一,成纸的外观匀度会更好,同时纤维宽度更小,成纸的孔径也会更小。选用部分的涤纶纤维或粘胶纤维抄造的原纸紧度更低,纤维之间更疏松,原纸的紧度低,透气度高,更利于施胶或涂布时施胶液或涂布液的吸收。5-20% polyester fiber or viscose fiber is selected for use in the above proportioning, because compared with bleached short-fiber wood pulp and bleached long-fiber wood pulp, the fiber width of the selected polyester fiber or viscose fiber is smaller. The more uniform the dimensions, the better the appearance of the finished paper, and the smaller the fiber width, the smaller the pore size of the finished paper. The base paper made of some polyester fibers or viscose fibers has lower tightness, looser fibers, lower tightness of base paper, and higher air permeability, which is more conducive to the absorption of sizing liquid or coating liquid during sizing or coating .

作为优选,所述化学纤维为涤纶纤维或粘胶纤维中的一种;优选,纤维的规格为:0.5-1.7dtex*4-5mm;优选,质量份数为8-12份。Preferably, the chemical fiber is one of polyester fiber or viscose fiber; preferably, the specification of the fiber is: 0.5-1.7dtex*4-5mm; preferably, the number of parts by mass is 8-12 parts.

作为优选,所述漂白短纤维木浆质量份数为20-40份;漂白长纤维木浆质量份数为60-80份;优选,漂白短纤维木浆的纤维长度为0.70-0.85mm,纤维的宽度为18-21μm,漂白长纤维木浆的纤维长度为1.80-2.5mm,纤维的宽度为30-33μm。As preferably, the mass fraction of the bleached short-fiber wood pulp is 20-40 parts; the mass fraction of the bleached long-fiber wood pulp is 60-80 parts; preferably, the fiber length of the bleached short-fiber wood pulp is 0.70-0.85 mm, and the fiber The width of the fiber is 18-21 μm, the fiber length of bleached long-fiber wood pulp is 1.80-2.5 mm, and the width of the fiber is 30-33 μm.

作为优选,所述原纸配方还包括湿强剂、表面施胶液和染料中的一种或多种。Preferably, the base paper formula also includes one or more of wet strength agent, surface sizing solution and dye.

作为优选,所述湿强剂采用PAE和PPE中的一种或两种;表面施胶液为丙烯酸乳。Preferably, one or both of PAE and PPE are used as the wet strength agent; the surface sizing solution is acrylic emulsion.

本发明选用表面施胶(机内涂布)+单面涂布。原纸定量通常定量只有28g/m2左右,原纸很亲水,同时结构疏松,紧度在0.43g/m3左右,原纸经过一道机内表面施胶(机内涂布),施胶液(涂布液)完全浸透原纸,上胶量达到10g/m2左右,再经过一道机外单面涂布,上胶量约2g/m2,原纸经过上胶约10g/m2的第一道浸渍式施胶,纸的透气度指标已大幅度下降,然后再通过单面机外涂布,纸的表面封闭性会大幅度提高,纸的紧度提高,透气度大幅下降,孔径明显下降,纸的耐水、耐溶剂性能会明显提高。The present invention selects surface sizing (in-machine coating)+single-side coating. The basis weight of the base paper is usually only about 28g/m2 , the base paper is very hydrophilic, and the structure is loose at the same time, the tightness is about 0.43g/m3 . Cloth liquid) completely soaks the base paper, the amount of gluing reaches about 10g/m2 , and then goes through a single-sided coating outside the machine, the amount of gluing is about 2g/m2 , and the base paper is impregnated in the first step of gluing about 10g/m2 The air permeability index of the paper has dropped significantly, and then through single-sided coating outside the machine, the surface sealing of the paper will be greatly improved, the tightness of the paper will be improved, the air permeability will be greatly reduced, and the pore diameter will be significantly reduced. The water resistance and solvent resistance will be significantly improved.

选用更多的上胶量可以使纸张更柔软,更好的柔韧性,纸的透明度会更高;因为丙烯酸胶乳在160℃以下性质稳定,不会熔融,在和纸胶带原纸中含有更多的丙烯酸胶乳,可以使纸张有更好的耐高温,抗老化性能。Choosing more sizing amount can make the paper softer, better flexibility, and the transparency of the paper will be higher; because the acrylic latex is stable below 160°C and will not melt, it contains more acrylic latex in the base paper of washi tape Acrylic latex can make the paper have better high temperature resistance and anti-aging performance.

作为优选,所述湿强剂的加入量为纤维总质量0.5-2.5%;表面施胶液的总上胶量为原纸总质量30-50%;染料按颜色需要确定添加量。As a preference, the added amount of the wet strength agent is 0.5-2.5% of the total fiber mass; the total sizing amount of the surface sizing solution is 30-50% of the total mass of the base paper; the added amount of the dye is determined according to the color requirement.

作为优选,所述湿强剂的加入量为纤维总质量的1.0-2.0%。Preferably, the added amount of the wet strength agent is 1.0-2.0% of the total fiber mass.

作为优选,所述表面施胶液的总上胶量为原纸总质量的35-45%。Preferably, the total sizing amount of the surface sizing solution is 35-45% of the total mass of the base paper.

进一步,本申请提供了所述和纸胶带原纸的生产方法,该方法包括以下的步骤:Further, the application provides the production method of the base paper of the washi tape, the method comprises the following steps:

1)木浆碎解:将漂白短纤维木浆、漂白长纤维木浆加入到碎浆机中进行碎解;1) Wood pulp disintegration: adding bleached short-fiber wood pulp and bleached long-fiber wood pulp into a pulper for disintegration;

2)疏解和打浆:各种木浆经碎浆机混合碎解后经浸泡后再进行疏解和打浆,磨浆浓度控制在4.0-6.0%;打浆度控制在:16-20°SR,湿重:≥7g;完成后放到成浆池;2) Thinning and beating: All kinds of wood pulp are mixed and crushed by a pulper, then soaked and then deflagged and beaten. The refining concentration is controlled at 4.0-6.0%; the beating degree is controlled at: 16-20°SR, wet weight : ≥7g; put it into the slurry tank after completion;

3)配浆:将磨好的木浆在配浆池中按一定比例配置,加入化学纤维混合,再加入湿强剂;湿强剂稀释到0.8-2.0%的浓度再添加;3) Pulp blending: the ground wood pulp is prepared in a certain proportion in the pulp blending tank, mixed with chemical fibers, and then added with wet strength agent; the wet strength agent is diluted to a concentration of 0.8-2.0% before adding;

4)抄造:将配好的浆料稀释至0.1-0.5%浓度,抽到抄前池经冲浆泵上斜网或圆网成形、压榨、干燥;4) Papermaking: Dilute the prepared slurry to a concentration of 0.1-0.5%, pump it to the forebay, and form it on the inclined screen or circular screen through the pulping pump, press, and dry;

5)表面施胶(机内涂布):经过前道烘干的纸页进入表面施胶装置进行表面施胶或机内涂布,表面施胶液或涂布液完全浸没纸页,经过表面施胶辊或涂布辊的均匀挤压,表面施胶液或涂布液均匀的吸附在纸页里面;表面施胶液或涂布液的浓度为2%-7%;所述的表面施胶的表面施胶液或涂布液为丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为5-10%,上胶量为原纸定量的30-50%;如果需要染色的产品,在施胶液或涂布液中另添加相应的颜料;5) Surface sizing (in-machine coating): The paper sheet that has been dried in the previous process enters the surface sizing device for surface sizing or in-machine coating. Uniform extrusion of the sizing roller or coating roller, the surface sizing liquid or coating liquid is evenly absorbed in the paper; the concentration of the surface sizing liquid or coating liquid is 2%-7%; the surface sizing liquid The surface sizing solution or coating solution of the glue is acrylic latex, the concentration of the acrylic latex solution is 5-10%, and the amount of sizing is 30-50% of the base paper quantitative; Or add corresponding pigments to the coating solution;

6)干燥、卷取;6) drying and coiling;

7)纸张再经过机外单面涂布,涂布液为:丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为20-25%,上胶量为原纸定量的4-6%;7) The paper is coated on one side outside the machine again, and the coating liquid is: acrylic latex, the concentration of the acrylic latex solution is 20-25%, and the amount of gluing is 4-6% of the base paper quantitative;

8)超级软压光:纸张经过单面涂布后,继续干燥,再经过超级软压光,压光压力控制在:30-60MPa;8) Super soft calendering: After the paper is coated on one side, continue to dry, and then go through super soft calendering, and the calendering pressure is controlled at: 30-60MPa;

9)卷取,分切,包装。9) Coiling, cutting and packaging.

本发明选用超级软压光可以提高纸的表面平整度,纸的柔软度也会提高,纸的透气性会进一步降低,孔径下降,提高纸的耐水、耐溶剂性能,涂布后纸经过超级软压光处理,会使和纸胶带原纸通透润泽感增强,更受用户喜欢。In the present invention, the super soft calendering can improve the surface smoothness of the paper, the softness of the paper will also be improved, the air permeability of the paper will be further reduced, the pore diameter will be reduced, and the water resistance and solvent resistance of the paper will be improved. Calendering treatment will enhance the transparency and moistness of the washi tape base paper, which is more popular with users.

进一步,本申请提供了一种和纸胶带,该和纸胶带的原纸采用所述的和纸胶带原纸。Further, the present application provides a washi tape, and the base paper of the washi tape adopts the above-mentioned base paper of the washi tape.

本发明的有益效果是:本发明的高性能和纸胶带原纸及其生产方法,生产出来的和纸胶带原纸和对比例的原发明生产的产品相比,质量更好,产品更受客户欢迎,具备以下优点:The beneficial effects of the present invention are: the high-performance washi tape base paper of the present invention and the production method thereof, the produced washi tape base paper is better in quality than the product produced by the original invention in the comparative example, and the product is more popular with customers. Has the following advantages:

一、具有更好的干、湿强度,更好的柔韧性和抗撕裂性能,产品不会分层;1. It has better dry and wet strength, better flexibility and tear resistance, and the product will not be delaminated;

二、具备更好的柔软性;2. Better flexibility;

三、具备更好的耐水、耐溶剂性能;3. Better water resistance and solvent resistance;

四、具备更好的耐高温、抗老化性能;4. It has better high temperature resistance and anti-aging performance;

五、具备更好的透明度,染色后的和纸胶带原纸色彩更加艳丽,用这种和纸胶带原纸生产的和纸胶带,有一种通透润泽感,产品更受用户喜欢。5. It has better transparency. The dyed washi tape base paper is more colorful. The washi tape produced from this washi tape base paper has a transparent and moist feeling, and the product is more popular with users.

具体实施方式Detailed ways

下面结合具体实例对本发明作进一步说明,但本发明的实施和保护范围不限于此。The present invention will be further described below in conjunction with specific examples, but the implementation and protection scope of the present invention are not limited thereto.

本申请的纤维浆料的原料性状如下:The raw material properties of the fiber slurry of the present application are as follows:

表1纤维浆料的原料性状The raw material character of table 1 fiber slurry

原料raw material纤维长度mmFiber length mm纤维宽度μmFiber width μm漂白阔叶木化学机械浆Bleached Hardwood Chemi-Mechanical Pulp0.60-0.700.60-0.7020-2320-23漂白阔叶木化学浆Bleached Hardwood Chemical Pulp0.70-0.800.70-0.8019-2019-20漂白针叶木化学浆Bleached Softwood Chemical Pulp1.80-2.101.80-2.1030-3530-35

一种高性能和纸胶带原纸生产工艺,包括以下步骤:木浆碎解、纤维分散、疏解和打浆、添加助剂、添加化纤、配浆、除渣、上网成形(抄造)、压榨、前道烘干、表面施胶(机内涂布)、后道烘干、卷取、分切包装、机外涂布、烘干、柔压光超压、卷取、检验、分切包装等工序。A high-performance washi tape base paper production process, including the following steps: wood pulp disintegration, fiber dispersion, deflaking and beating, adding additives, adding chemical fibers, pulping, slag removal, online forming (papermaking), pressing, pre-processing Drying, surface sizing (in-machine coating), post-drying, coiling, slitting and packaging, off-machine coating, drying, soft calendering and overpressure, coiling, inspection, slitting and packaging, etc.

本发明制备的和纸胶带原纸的关键指标:定量:35-65g/m2,其中最终定量控制在35-42g/m2的产品,其它指标符合如下要求:透气度:≤100CU,抗张强度(纵向):≥3.0kN/m,抗张强度(横向):≥1.2kN/m2,伸长率:≥4%(纵向),≥8%(横向);湿强度(纵向):≥1.6kN/m2,湿强度(横向):≥0.6kN/m,表面吸收性(Cob,120s):8±2g/m2(正面),10±2g/m2(反面),10ml水渗过纸表面时间:≥60s,纸柔软度:≤400mN(横向),≤1000mN(纵向),孔径:≤5μm,白色和纸胶带原纸透明度:≥55%,亮度≥82%。纸柔软度数值越低,纸越柔软。The key indicators of the washi tape base paper prepared by the present invention: Quantitative: 35-65g/m2 , of which the final quantitative control is 35-42g/m2 , other indicators meet the following requirements: air permeability: ≤100CU, tensile strength (longitudinal): ≥3.0kN/m, tensile strength (transverse): ≥1.2kN/m2 , elongation: ≥4% (longitudinal), ≥8% (transverse); wet strength (longitudinal): ≥1.6 kN/m2 , wet strength (transverse direction): ≥0.6kN/m, surface absorption (Cob, 120s): 8±2g/m2 (front), 10±2g/m2 (reverse), 10ml water seepage Paper surface time: ≥60s, paper softness: ≤400mN (horizontal), ≤1000mN (longitudinal), aperture: ≤5μm, transparency of white washi tape base paper: ≥55%, brightness ≥82%. The lower the paper softness number, the softer the paper.

实施例1Example 1

1)浆料配比:将质量份为80份漂白针叶木浆、20份漂白阔叶木浆加入到碎浆机中进行碎解;1) Pulp ratio: 80 parts by mass of bleached softwood pulp and 20 parts of bleached hardwood pulp are added to a pulper for disintegration;

2)疏解和打浆:各种浆板经碎浆机混合碎解后经浸泡后再进行疏解和打浆,磨浆浓度控制在5.5-6.0%;打浆度控制在:16-18°SR,湿重≥8.5g。疏解和打浆完成后放到成浆池;2) Thinning and beating: All kinds of pulp boards are mixed and crushed by a pulper, then soaked and then deflated and beaten. The refining concentration is controlled at 5.5-6.0%; the beating degree is controlled at: 16-18°SR, wet weight ≥8.5g. Put it into the slurry tank after deflaking and beating;

3)配浆:将磨好的木浆在配浆池中按一定比例配置,再加入15份0.5dtex*4mm涤纶短纤混合,再加入湿强剂,稀释到0.8-1.0%的浓度;湿强剂加入量:1.0%。3) Pulp preparation: prepare the ground wood pulp in a certain proportion in the pulp preparation tank, then add 15 parts of 0.5dtex*4mm polyester staple fiber to mix, then add wet strength agent, and dilute to a concentration of 0.8-1.0%; Amount of strong agent added: 1.0%.

4)抄造:将配好的浆料稀释至0.1-0.2%浓度,抽到抄前池经冲浆泵上斜网网成形、压榨、干燥;4) Paper making: Dilute the prepared slurry to a concentration of 0.1-0.2%, pump it into the forecourt pool, form it on the inclined screen on the pulp pump, squeeze it, and dry it;

5)表面施胶:经过前道烘干的纸页进入表面施胶装置进行表面施胶,施胶前纸定量控制在:27-29g/m2,紧度控制在:0.40-0.46g/m3,透气度:20000-40000CU,表面施胶液完全浸没纸页,经过表面施胶辊的均匀挤压,表面施胶液均匀的涂在纸页上;表面施胶液选用丙烯酸胶乳,表面施胶液的浓度为5%-6%。上胶量控制在原纸定量的35-40%,即上胶量控制在10g/m2左右。5) Surface sizing: The paper sheets that have been dried in the previous process enter the surface sizing device for surface sizing. Before sizing, the quantitative control of the paper is: 27-29g/m2 , and the tightness is controlled at: 0.40-0.46g/m3 , air permeability: 20000-40000CU, the surface sizing liquid is completely immersed in the paper, and the surface sizing liquid is evenly coated on the paper through the uniform extrusion of the surface sizing roller; the surface sizing liquid is made of acrylic latex, and the surface sizing liquid The concentration of the glue is 5%-6%. The amount of gluing is controlled at 35-40% of the base paper weight, that is, the amount of gluing is controlled at about 10g/m2 .

6)纸的定量控制在36-39g/m26) The basis weight of the paper is controlled at 36-39g/m2 .

7)干燥、卷取和分切包装。7) Drying, coiling and slitting and packaging.

8)纸张再经过机外单面涂布,涂布液为:丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为20-25%,上胶量为原纸定量的5-6%,即上胶量为2g/m2左右;8) The paper is coated on one side outside the machine again, and the coating liquid is: acrylic latex, the concentration of the described acrylic latex solution is 20-25%, and the amount of gluing is 5-6% of the base paper quantitative, that is, the amount of gluing About 2g/m2 ;

9)超级软压光:纸张经过单面涂布后,继续干燥,再经过超级软压光,压光压力控制在:50-60MPa。9) Super soft calendering: After the paper is coated on one side, continue to dry, and then go through super soft calendering, the calendering pressure is controlled at: 50-60MPa.

10)最终纸的定量控制在:38-42g/m210) The quantitative control of the final paper is: 38-42g/m2 .

11)卷取,分切,包装。11) Coiling, cutting and packaging.

实施例2Example 2

1)浆料配比:将质量份为80份漂白针叶木浆、20份漂白阔叶木浆加入到碎浆机中进行碎解;1) Pulp ratio: 80 parts by mass of bleached softwood pulp and 20 parts of bleached hardwood pulp are added to a pulper for disintegration;

2)疏解和打浆:各种浆板经碎浆机混合碎解后经浸泡后再进行疏解和打浆,磨浆浓度控制在5.5-6.0%;打浆度控制在:17-19°SR,湿重≥8.5g。疏解和打浆完成后放到成浆池;2) Deflagging and beating: all kinds of pulp boards are mixed and crushed by a pulper and then soaked before deflaking and beating. The refining concentration is controlled at 5.5-6.0%; the beating degree is controlled at: 17-19°SR, wet weight ≥8.5g. Put it into the slurry tank after deflaking and beating;

3)配浆:将磨好的木浆在配浆池中按一定比例配置,再加入20份1.1dtex*5mm粘胶纤维混合,再加入湿强剂,稀释到0.8-1.0%的浓度;湿强剂加入量:1.2%。3) Pulp preparation: Prepare the ground wood pulp in a certain proportion in the pulp preparation tank, then add 20 parts of 1.1dtex*5mm viscose fiber to mix, then add wet strength agent, and dilute to a concentration of 0.8-1.0%; Amount of strong agent added: 1.2%.

4)抄造:将配好的浆料稀释至0.1-0.2%浓度,抽到抄前池经冲浆泵上圆网成形、压榨、干燥;4) Paper making: Dilute the prepared slurry to a concentration of 0.1-0.2%, pump it into the forecourt pool, form it on the rotary screen on the pulp pump, squeeze it, and dry it;

5)表面施胶:经过前道烘干的纸页进入表面施胶装置进行表面施胶,施胶前纸定量控制在:27-29g/m2,紧度控制在:0.40-0.46g/m3,透气度:20000-40000CU,表面施胶液完全浸没纸页,经过表面施胶辊的均匀挤压,表面施胶液均匀的涂在纸页上;表面施胶液选用丙烯酸胶乳,再添加一种黄色颜料,表面施胶液的浓度为5%-6%。上胶量控制在原纸定量的35-40%,即上胶量控制在10g/m2左右。5) Surface sizing: The paper sheets that have been dried in the previous process enter the surface sizing device for surface sizing. Before sizing, the quantitative control of the paper is: 27-29g/m2 , and the tightness is controlled at: 0.40-0.46g/m3 , air permeability: 20000-40000CU, the surface sizing solution is completely immersed in the paper, and the surface sizing solution is evenly coated on the paper after being uniformly squeezed by the surface sizing roller; the surface sizing solution is made of acrylic latex, and then added A yellow pigment, the concentration of the surface sizing solution is 5%-6%. The amount of gluing is controlled at 35-40% of the base paper weight, that is, the amount of gluing is controlled at about 10g/m2 .

6)纸的定量控制在36-39g/m26) The basis weight of the paper is controlled at 36-39g/m2 .

7)干燥、卷取和分切包装。7) Drying, coiling and slitting and packaging.

8)纸张再经过机外单面涂布,涂布液为:丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为20-25%,上胶量为原纸定量的5-6%,即上胶量为2g/m2左右;8) The paper is coated on one side outside the machine again, and the coating liquid is: acrylic latex, the concentration of the described acrylic latex solution is 20-25%, and the amount of gluing is 5-6% of the base paper quantitative, that is, the amount of gluing About 2g/m2 ;

9)超级软压光:纸张经过单面涂布后,继续干燥,再经过超级软压光,压光压力控制在:50-60MPa。9) Super soft calendering: After the paper is coated on one side, continue to dry, and then go through super soft calendering, the calendering pressure is controlled at: 50-60MPa.

10)最终纸的定量控制在:38-42g/m210) The quantitative control of the final paper is: 38-42g/m2 .

11)卷取,分切,包装。11) Coiling, cutting and packaging.

实施例3Example 3

1)浆料配比:将质量份为70份漂白针叶木浆、30份漂白阔叶木浆加入到碎浆机中进行碎解;1) Pulp ratio: 70 parts by mass of bleached softwood pulp and 30 parts of bleached hardwood pulp are added to a pulper for disintegration;

2)疏解和打浆:各种浆板经碎浆机混合碎解后经浸泡后再进行疏解和打浆,磨浆浓度控制在5.5-6.0%;打浆度控制在:17-19°SR,湿重≥8.0g。疏解和打浆完成后放到成浆池;2) Deflagging and beating: all kinds of pulp boards are mixed and crushed by a pulper and then soaked before deflaking and beating. The refining concentration is controlled at 5.5-6.0%; the beating degree is controlled at: 17-19°SR, wet weight ≥8.0g. Put it into the slurry tank after deflaking and beating;

3)配浆:将磨好的木浆在配浆池中按一定比例配置,再加入10份1.5dtex*4mm涤纶短纤混合,再加入湿强剂,稀释到0.8-1.0%的浓度;湿强剂加入量:1.5%。3) Pulp mixing: mix the ground wood pulp in a certain proportion in the pulp mixing tank, then add 10 parts of 1.5dtex*4mm polyester staple fiber to mix, then add wet strength agent, and dilute to a concentration of 0.8-1.0%; Dosage of strong agent: 1.5%.

4)抄造:将配好的浆料稀释至0.1-0.2%浓度,抽到抄前池经冲浆泵上斜网成形、压榨、干燥;4) Papermaking: Dilute the prepared slurry to a concentration of 0.1-0.2%, pump it to the forebay pool, form it on the inclined screen through the pulp pump, squeeze it, and dry it;

5)表面施胶:经过前道烘干的纸页进入表面施胶装置进行表面施胶,施胶前定量控制在:27-29g/m2,紧度控制在:0.40-0.46g/m3,透气度:20000-40000CU,表面施胶液完全浸没纸页,经过表面施胶辊的均匀挤压,表面施胶液均匀的涂在纸页上;表面施胶液选用丙烯酸胶乳,再添加一种蓝色颜料,表面施胶液的浓度为5%-6%。上胶量控制在原纸定量的35-40%,即上胶量控制在10g/m2左右。5) Surface sizing: The paper sheets that have been dried in the previous process enter the surface sizing device for surface sizing. The quantitative control before sizing is: 27-29g/m2 , and the tightness is controlled at: 0.40-0.46g/m3 ,Permeability: 20000-40000CU, the surface sizing solution is completely immersed in the paper, after being evenly squeezed by the surface sizing roller, the surface sizing solution is evenly coated on the paper; the surface sizing solution is made of acrylic latex, and then add a A blue pigment, the concentration of the surface sizing solution is 5%-6%. The amount of gluing is controlled at 35-40% of the base paper weight, that is, the amount of gluing is controlled at about 10g/m2 .

6)纸的定量控制在36-39g/m26) The basis weight of the paper is controlled at 36-39g/m2 .

7)干燥、卷取和分切包装。7) Drying, coiling and slitting and packaging.

8)纸张再经过机外单面涂布,涂布液为:丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为20-25%,上胶量为原纸定量的5-6%,即上胶量为2g/m2左右;8) The paper is coated on one side outside the machine again, and the coating liquid is: acrylic latex, the concentration of the described acrylic latex solution is 20-25%, and the amount of gluing is 5-6% of the base paper quantitative, that is, the amount of gluing About 2g/m2 ;

9)超级软压光:纸张经过单面涂布后,继续干燥,再经过超级软压光,压光压力控制在:45-55MPa。9) Super soft calendering: After the paper is coated on one side, continue to dry, and then go through super soft calendering, the calendering pressure is controlled at: 45-55MPa.

10)最终纸的定量控制在:38-42g/m210) The quantitative control of the final paper is: 38-42g/m2 .

11)卷取,分切,包装。11) Coiling, cutting and packaging.

实施例4Example 4

1)浆料配比:将质量份为70份漂白针叶木浆、30份漂白阔叶木浆加入到碎浆机中进行碎解;1) Pulp ratio: 70 parts by mass of bleached softwood pulp and 30 parts of bleached hardwood pulp are added to a pulper for disintegration;

2)疏解和打浆:各种浆板经碎浆机混合碎解后经浸泡后再进行疏解和打浆,磨浆浓度控制在5.5-6.0%;打浆度控制在:17-19°SR,湿重≥8.0g。疏解和打浆完成后放到成浆池;2) Deflagging and beating: all kinds of pulp boards are mixed and crushed by a pulper and then soaked before deflaking and beating. The refining concentration is controlled at 5.5-6.0%; the beating degree is controlled at: 17-19°SR, wet weight ≥8.0g. Put it into the slurry tank after deflaking and beating;

3)配浆:将磨好的木浆在配浆池中按一定比例配置,再加入10份1.1dtex*5mm涤纶短纤混合,再加入湿强剂,稀释到0.8-1.0%的浓度;湿强剂加入量:1.8%。3) Pulp mixing: mix the ground wood pulp in a certain proportion in the pulp mixing tank, then add 10 parts of 1.1dtex*5mm polyester staple fiber to mix, then add wet strength agent, and dilute to a concentration of 0.8-1.0%; Amount of strong agent added: 1.8%.

4)抄造:将配好的浆料稀释至0.2-0.3%浓度,抽到抄前池经冲浆泵上斜网成形、压榨、干燥;4) Papermaking: Dilute the prepared slurry to a concentration of 0.2-0.3%, pump it to the forebay pool, form it on the inclined screen through the pulp pump, squeeze it, and dry it;

5)机内涂布:经过前道烘干的纸页进入机内涂布装置进行涂布,施胶前定量控制在:27-29g/m2,紧度控制在:0.40-0.46g/m3,透气度:20000-40000CU,涂布液完全浸没纸页,经过涂布辊的均匀挤压,涂布液均匀的涂在纸页上;涂布液选用丙烯酸胶乳,再添加一种红色颜料,涂布液的浓度为5%-6%。上胶量控制在原纸定量的35-40%,即上胶量控制在10g/m2左右。5) In-machine coating: The paper sheets that have been dried in the previous process enter the in-machine coating device for coating. The quantitative control before sizing is: 27-29g/m2 , and the tightness is controlled at: 0.40-0.46g/m3. Air permeability: 20000-40000CU, the coating liquid is completely immersed in the paper, and evenly squeezed by the coating roller, the coating liquid is evenly coated on the paper; the coating liquid is made of acrylic latex, and a red pigment is added , the concentration of the coating liquid is 5%-6%. The amount of gluing is controlled at 35-40% of the base paper weight, that is, the amount of gluing is controlled at about 10g/m2 .

6)纸的定量控制在36-39g/m26) The basis weight of the paper is controlled at 36-39g/m2 .

7)干燥、卷取和分切包装。7) Drying, coiling and slitting and packaging.

8)纸张再经过机外单面涂布,涂布液为:丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为20-25%,上胶量为原纸定量的4-5%,即上胶量为2g/m2左右;8) The paper is coated on one side outside the machine again, and the coating liquid is: acrylic latex, the concentration of the described acrylic latex solution is 20-25%, and the amount of gluing is 4-5% of the base paper quantitative, that is, the amount of gluing About 2g/m2 ;

9)超级软压光:纸张经过单面涂布后,继续干燥,再经过超级软压光,压光压力控制在:45-55MPa。9) Super soft calendering: After the paper is coated on one side, continue to dry, and then go through super soft calendering, the calendering pressure is controlled at: 45-55MPa.

10)最终纸的定量控制在:38-42g/m210) The quantitative control of the final paper is: 38-42g/m2 .

11)卷取,分切,包装。11) Coiling, cutting and packaging.

实施例5Example 5

1)浆料配比:将质量份为60份漂白针叶木浆、40份漂白阔叶木浆加入到碎浆机中进行碎解;1) Pulp ratio: 60 parts by mass of bleached softwood pulp and 40 parts of bleached hardwood pulp are added to a pulper for disintegration;

2)疏解和打浆:各种浆板经碎浆机混合碎解后经浸泡后再进行疏解和打浆,磨浆浓度控制在5.5-6.0%;打浆度控制在:17-19°SR,湿重≥7.0g。疏解和打浆完成后放到成浆池;2) Thinning and beating: All kinds of pulp boards are mixed and crushed by a pulper, then soaked and then deflagged and beaten. The refining concentration is controlled at 5.5-6.0%; the beating degree is controlled at: 17-19 ° SR, wet weight ≥7.0g. Put it into the slurry tank after deflaking and beating;

3)配浆:将磨好的木浆在配浆池中按一定比例配置,再加入10份1.1dtex*5mm涤纶短纤混合,再加入湿强剂,稀释到0.8-1.0%的浓度;湿强剂加入量:0.8%。3) Pulp mixing: mix the ground wood pulp in a certain proportion in the pulp mixing tank, then add 10 parts of 1.1dtex*5mm polyester staple fiber to mix, then add wet strength agent, and dilute to a concentration of 0.8-1.0%; Amount of strong agent added: 0.8%.

4)抄造:将配好的浆料稀释至0.2-0.3%浓度,抽到抄前池经冲浆泵上圆网成形、压榨、干燥;4) Papermaking: Dilute the prepared slurry to a concentration of 0.2-0.3%, pump it to the forebay pool, form it on a rotary screen on the pulping pump, squeeze it, and dry it;

5)机内涂布:经过前道烘干的纸页进入机内涂布装置进行涂布,施胶前定量控制在:37-39g/m2,紧度控制在:0.42-0.47g/m3,透气度:15000-30000CU,涂布液完全浸没纸页,经过涂布辊的均匀挤压,涂布液均匀的涂在纸页上;涂布液选用丙烯酸胶乳,涂布液的浓度为5%-6%。上胶量控制在原纸定量的35-40%,即上胶量控制在12g/m2左右。5) In-machine coating: The paper sheets that have been dried in the previous process enter the in-machine coating device for coating. The quantitative control before sizing is: 37-39g/m2 , and the tightness is controlled at: 0.42-0.47g/m3. Air permeability: 15000-30000CU, the coating liquid is completely immersed in the paper, and evenly squeezed by the coating roller, the coating liquid is evenly coated on the paper; the coating liquid is made of acrylic latex, and the concentration of the coating liquid is 5%-6%. The amount of gluing is controlled at 35-40% of the base paper weight, that is, the amount of gluing is controlled at about 12g/m2 .

6)纸的定量控制在45-49g/m26) The basis weight of the paper is controlled at 45-49g/m2 .

7)干燥、卷取和分切包装。7) Drying, coiling and slitting and packaging.

8)纸张再经过机外单面涂布,涂布液为:丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为20-25%,上胶量为原纸定量的3-4%,即上胶量为2g/m2左右;8) The paper is coated on one side outside the machine again, and the coating liquid is: acrylic latex, the concentration of the described acrylic latex solution is 20-25%, and the amount of gluing is 3-4% of the base paper quantitative, that is, the amount of gluing About 2g/m2 ;

9)超级软压光:纸张经过单面涂布后,继续干燥,再经过超级软压光,压光压力控制在:45-55MPa。9) Super soft calendering: After the paper is coated on one side, continue to dry, and then go through super soft calendering, the calendering pressure is controlled at: 45-55MPa.

10)最终纸的定量控制在:48-52g/m210) The quantitative control of the final paper is: 48-52g/m2 .

11)卷取,分切,包装。11) Coiling, cutting and packaging.

实施例6Example 6

1)浆料配比:将质量份为50份漂白针叶木浆、50份漂白阔叶木浆加入到碎浆机中进行碎解;1) Pulp ratio: 50 parts by mass of bleached softwood pulp and 50 parts of bleached hardwood pulp are added to a pulper for disintegration;

2)疏解和打浆:各种浆板经碎浆机混合碎解后经浸泡后再进行疏解和打浆,磨浆浓度控制在5.5-6.0%;打浆度控制在:17-19°SR,湿重≥8.0g。疏解和打浆完成后放到成浆池;2) Deflagging and beating: all kinds of pulp boards are mixed and crushed by a pulper and then soaked before deflaking and beating. The refining concentration is controlled at 5.5-6.0%; the beating degree is controlled at: 17-19°SR, wet weight ≥8.0g. Put it into the slurry tank after deflaking and beating;

3)配浆:将磨好的木浆在配浆池中按一定比例配置,再加入20份1.7dtex*4mm涤纶短纤混合,再加入湿强剂,稀释到0.8-1.0%的浓度;湿强剂加入量:0.5%。3) Pulp mixing: mix the ground wood pulp in a certain proportion in the pulp mixing tank, then add 20 parts of 1.7dtex*4mm polyester staple fiber to mix, then add wet strength agent, and dilute to a concentration of 0.8-1.0%; Dosage of strong agent: 0.5%.

4)抄造:将配好的浆料稀释至0.2-0.3%浓度,抽到抄前池经冲浆泵上斜网成形、压榨、干燥;4) Papermaking: Dilute the prepared slurry to a concentration of 0.2-0.3%, pump it to the forebay pool, form it on the inclined screen through the pulp pump, squeeze it, and dry it;

5)表面施胶:经过前道烘干的纸页进入表面施胶装置进行表面施胶,施胶前定量控制在:47-49g/m2,紧度控制在:0.43-0.48g/m3,透气度:10000-20000CU,表面施胶液完全浸没纸页,经过表面施胶辊的均匀挤压,表面施胶液均匀的涂在纸页上;表面施胶液选用丙烯酸胶乳,表面施胶液的浓度为5%-6%。上胶量控制在原纸定量的35-40%,即上胶量控制在14/m2左右。5) Surface sizing: The paper sheets that have been dried in the previous process enter the surface sizing device for surface sizing. The quantitative control before sizing is: 47-49g/m2 , and the tightness is controlled at: 0.43-0.48g/m3 ,Permeability: 10000-20000CU, the surface sizing solution is completely immersed in the paper, after being uniformly squeezed by the surface sizing roller, the surface sizing solution is evenly coated on the paper; the surface sizing solution is made of acrylic latex, and the surface sizing The concentration of liquid is 5%-6%. The amount of gluing is controlled at 35-40% of the base paper weight, that is, the amount of gluing is controlled at about 14/m2 .

6)纸的定量控制在55-59g/m26) The basis weight of the paper is controlled at 55-59g/m2 .

7)干燥、卷取和分切包装。7) Drying, coiling and slitting and packaging.

8)纸张再经过机外单面涂布,涂布液为:丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为20-25%,上胶量为原纸定量的2-3%,即上胶量为2g/m2左右;8) The paper is coated on one side outside the machine again, and the coating liquid is: acrylic latex, the concentration of the described acrylic latex solution is 20-25%, and the amount of gluing is 2-3% of the base paper quantitative, that is, the amount of gluing About 2g/m2 ;

9)超级软压光:纸张经过单面涂布后,继续干燥,再经过超级软压光,压光压力控制在:50-60MPa。9) Super soft calendering: After the paper is coated on one side, continue to dry, and then go through super soft calendering, the calendering pressure is controlled at: 50-60MPa.

10)最终纸的定量控制在:58-62g/m210) The quantitative control of the final paper is: 58-62g/m2 .

11)卷取,分切,包装。11) Coiling, cutting and packaging.

对比例1Comparative example 1

1)浆料配比:将质量份为100份漂白针叶木浆加入到碎浆机中进行碎解;1) Pulp ratio: 100 parts by mass of bleached softwood pulp is added to a pulper for disintegration;

2)疏解和打浆:各种浆板经碎浆机混合碎解后经浸泡后再进行疏解和打浆,磨浆浓度控制在5.5-6.0%;打浆度控制在:16-18°SR,湿重≥8.5g。疏解和打浆完成后放到成浆池;2) Thinning and beating: All kinds of pulp boards are mixed and crushed by a pulper, then soaked and then deflated and beaten. The refining concentration is controlled at 5.5-6.0%; the beating degree is controlled at: 16-18°SR, wet weight ≥8.5g. Put it into the slurry tank after deflaking and beating;

3)配浆:将磨好的木浆在配浆池中按一定比例配置,再加入15份0.5dtex*4mm涤纶短纤混合,再加入湿强剂,稀释到0.8-1.0%的浓度;湿强剂加入量:1.0%。3) Pulp preparation: prepare the ground wood pulp in a certain proportion in the pulp preparation tank, then add 15 parts of 0.5dtex*4mm polyester staple fiber to mix, then add wet strength agent, and dilute to a concentration of 0.8-1.0%; Amount of strong agent added: 1.0%.

4)抄造:将配好的浆料稀释至0.1-0.2%浓度,抽到抄前池经冲浆泵上斜网成形、压榨、干燥;4) Papermaking: Dilute the prepared slurry to a concentration of 0.1-0.2%, pump it to the forebay pool, form it on the inclined screen through the pulp pump, squeeze it, and dry it;

5)表面施胶:经过前道烘干的纸页进入表面施胶装置进行表面施胶,施胶前定量控制在:27-29g/m2,紧度控制在:0.40-0.46g/m3,透气度:20000-40000CU,表面施胶液完全浸没纸页,经过表面施胶辊的均匀挤压,表面施胶液均匀的涂在纸页上;表面施胶液选用丙烯酸胶乳,表面施胶液的浓度为5%-6%。上胶量控制在原纸定量的35-40%,即上胶量控制在10g/m2左右。5) Surface sizing: The paper sheets that have been dried in the previous process enter the surface sizing device for surface sizing. The quantitative control before sizing is: 27-29g/m2 , and the tightness is controlled at: 0.40-0.46g/m3 ,Permeability: 20000-40000CU, the surface sizing solution is completely immersed in the paper, after being uniformly squeezed by the surface sizing roller, the surface sizing solution is evenly coated on the paper; the surface sizing solution is made of acrylic latex, and the surface sizing The concentration of liquid is 5%-6%. The amount of gluing is controlled at 35-40% of the base paper weight, that is, the amount of gluing is controlled at about 10g/m2 .

6)纸的定量控制在39-39g/m26) The basis weight of the paper is controlled at 39-39g/m2 .

7)干燥、卷取和分切包装。7) Drying, coiling and slitting and packaging.

8)纸张再经过机外单面涂布,涂布液为:丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为20-25%,上胶量为原纸定量的5-6%,即上胶量为2g/m2左右;8) The paper is coated on one side outside the machine again, and the coating liquid is: acrylic latex, the concentration of the described acrylic latex solution is 20-25%, and the amount of gluing is 5-6% of the base paper quantitative, that is, the amount of gluing About 2g/m2 ;

9)超级软压光:纸张经过单面涂布后,继续干燥,再经过超级软压光,压光压力控制在:50-60MPa。9) Super soft calendering: After the paper is coated on one side, continue to dry, and then go through super soft calendering, the calendering pressure is controlled at: 50-60MPa.

10)最终纸的定量控制在:38-42g/m210) Quantitative control of the final paper: 38-42g/m2

11)卷取,分切,包装。11) Coiling, cutting and packaging.

对比例2Comparative example 2

1)浆料配比:将质量份为40份漂白针叶木浆、60份漂白阔叶木浆加入到碎浆机中进行碎解;1) Pulp ratio: 40 parts by mass of bleached softwood pulp and 60 parts of bleached hardwood pulp are added to a pulper for disintegration;

2)疏解和打浆:各种浆板经碎浆机混合碎解后经浸泡后再进行疏解和打浆,磨浆浓度控制在5.5-6.0%;打浆度控制在:16-18°SR,湿重≥5.0g。疏解和打浆完成后放到成浆池;2) Thinning and beating: All kinds of pulp boards are mixed and crushed by a pulper, then soaked and then deflagged and beaten. The refining concentration is controlled at 5.5-6.0%; the beating degree is controlled at: 16-18°SR, wet weight ≥5.0g. Put it into the slurry tank after deflaking and beating;

3)配浆:将磨好的木浆在配浆池中按一定比例配置,再加入15份0.5dtex*4mm涤纶短纤混合,再加入湿强剂,稀释到0.8-1.0%的浓度;湿强剂加入量:1.2%。3) Pulp preparation: prepare the ground wood pulp in a certain proportion in the pulp preparation tank, then add 15 parts of 0.5dtex*4mm polyester staple fiber to mix, then add wet strength agent, and dilute to a concentration of 0.8-1.0%; Amount of strong agent added: 1.2%.

4)抄造:将配好的浆料稀释至0.2-0.3%浓度,抽到抄前池经冲浆泵上圆网成形、压榨、干燥;4) Papermaking: Dilute the prepared slurry to a concentration of 0.2-0.3%, pump it to the forebay pool, form it on a rotary screen on the pulping pump, squeeze it, and dry it;

5)表面施胶:经过前道烘干的纸页进入表面施胶装置进行表面施胶,施胶前定量控制在:27-29g/m2,紧度控制在:0.40-0.46g/m3,透气度:20000-40000CU,表面施胶液完全浸没纸页,经过表面施胶辊的均匀挤压,表面施胶液均匀的涂在纸页上;表面施胶液选用丙烯酸胶乳,表面施胶液的浓度为5%-6%。上胶量控制在原纸定量的35-40%,即上胶量控制在10g/m2左右。5) Surface sizing: The paper sheets that have been dried in the previous process enter the surface sizing device for surface sizing. The quantitative control before sizing is: 27-29g/m2 , and the tightness is controlled at: 0.40-0.46g/m3 ,Permeability: 20000-40000CU, the surface sizing solution is completely immersed in the paper, after being uniformly squeezed by the surface sizing roller, the surface sizing solution is evenly coated on the paper; the surface sizing solution is made of acrylic latex, and the surface sizing The concentration of liquid is 5%-6%. The amount of gluing is controlled at 35-40% of the base paper weight, that is, the amount of gluing is controlled at about 10g/m2 .

6)纸的定量控制在36-39g/m26) The basis weight of the paper is controlled at 36-39g/m2 .

7)干燥、卷取和分切包装。7) Drying, coiling and slitting and packaging.

8)纸张再经过机外单面涂布,涂布液为:丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为20-25%,上胶量为原纸定量的5-6%,即上胶量为2g/m2左右;8) The paper is coated on one side outside the machine again, and the coating liquid is: acrylic latex, the concentration of the described acrylic latex solution is 20-25%, and the amount of gluing is 5-6% of the base paper quantitative, that is, the amount of gluing About 2g/m2 ;

9)超级软压光:纸张经过单面涂布后,继续干燥,再经过超级软压光,压光压力控制在:50-60MPa。9) Super soft calendering: After the paper is coated on one side, continue to dry, and then go through super soft calendering, the calendering pressure is controlled at: 50-60MPa.

10)最终纸的定量控制在:38-42g/m210) The quantitative control of the final paper is: 38-42g/m2 .

11)卷取,分切,包装。11) Coiling, cutting and packaging.

对比例3Comparative example 3

1)浆料配比:将质量份为80份漂白针叶木浆、20份漂白阔叶木浆加入到碎浆机中进行碎解;1) Pulp ratio: 80 parts by mass of bleached softwood pulp and 20 parts of bleached hardwood pulp are added to a pulper for disintegration;

2)疏解和打浆:各种浆板经碎浆机混合碎解后经浸泡后再进行疏解和打浆,磨浆浓度控制在5.5-6.0%;打浆度控制在:16-18°SR,湿重≥8.5g。疏解和打浆完成后放到成浆池;2) Thinning and beating: All kinds of pulp boards are mixed and crushed by a pulper, then soaked and then deflated and beaten. The refining concentration is controlled at 5.5-6.0%; the beating degree is controlled at: 16-18°SR, wet weight ≥8.5g. Put it into the slurry tank after deflaking and beating;

3)配浆:将磨好的木浆在配浆池中按一定比例配置,再加入30份0.5dtex*4mm涤纶短纤混合,再加入湿强剂,稀释到0.8-1.0%的浓度;湿强剂加入量:2.0%。3) Pulp mixing: mix the ground wood pulp in a certain proportion in the pulp mixing tank, then add 30 parts of 0.5dtex*4mm polyester staple fiber to mix, then add wet strength agent, and dilute to a concentration of 0.8-1.0%; Amount of strong agent added: 2.0%.

4)抄造:将配好的浆料稀释至0.1-0.2%浓度,抽到抄前池经冲浆泵上斜网成形、压榨、干燥;4) Papermaking: Dilute the prepared slurry to a concentration of 0.1-0.2%, pump it to the forebay pool, form it on the inclined screen through the pulp pump, squeeze it, and dry it;

5)表面施胶:经过前道烘干的纸页进入表面施胶装置进行表面施胶,施胶前定量控制在:27-29g/m2,紧度:0.35-0.38g/m3,透气度:45000-55000CU(本例中化纤含量太高,引起纸紧度下降,透气度升高),表面施胶液完全浸没纸页,经过表面施胶辊的均匀挤压,表面施胶液均匀的涂在纸页上;表面施胶液选用丙烯酸胶乳,再添加一种黄色颜料,表面施胶液的浓度为4%-5%。上胶量控制在原纸定量的35-40%,即上胶量控制在10g/m2左右。5) Surface sizing: The paper sheets that have been dried in the previous process enter the surface sizing device for surface sizing. The quantitative control before sizing is: 27-29g/m2 , the tightness: 0.35-0.38g/m3 , breathable Degree: 45000-55000CU (in this example, the chemical fiber content is too high, causing the paper tightness to decrease and the air permeability to increase), the surface sizing solution is completely immersed in the paper, and the surface sizing solution is evenly squeezed by the surface sizing roller The surface sizing liquid is made of acrylic latex, and a yellow pigment is added, and the concentration of the surface sizing liquid is 4%-5%. The amount of gluing is controlled at 35-40% of the base paper weight, that is, the amount of gluing is controlled at about 10g/m2 .

6)纸的定量控制在36-39g/m26) The basis weight of the paper is controlled at 36-39g/m2 .

7)干燥、卷取和分切包装。7) Drying, coiling and slitting and packaging.

8)纸张再经过机外单面涂布,涂布液为:丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为20-25%,上胶量为原纸定量的5-6%,即上胶量为2g/m2左右;8) The paper is coated on one side outside the machine again, and the coating liquid is: acrylic latex, the concentration of the described acrylic latex solution is 20-25%, and the amount of gluing is 5-6% of the base paper quantitative, that is, the amount of gluing About 2g/m2 ;

9)超级软压光:纸张经过单面涂布后,继续干燥,再经过超级软压光,压光压力控制在:50-60MPa。9) Super soft calendering: After the paper is coated on one side, continue to dry, and then go through super soft calendering, the calendering pressure is controlled at: 50-60MPa.

10)最终纸的定量控制在:38-42g/m210) The quantitative control of the final paper is: 38-42g/m2 .

11)卷取,分切,包装。11) Coiling, cutting and packaging.

对比例4Comparative example 4

1)浆料配比:将质量份为80份漂白针叶木浆、20份漂白阔叶木浆加入到碎浆机中进行碎解;1) Pulp ratio: 80 parts by mass of bleached softwood pulp and 20 parts of bleached hardwood pulp are added to a pulper for disintegration;

2)疏解和打浆:各种浆板经碎浆机混合碎解后经浸泡后再进行疏解和打浆,磨浆浓度控制在5.5-6.0%;打浆度控制在:16-18°SR,湿重≥8.5g。疏解和打浆完成后放到成浆池;2) Thinning and beating: All kinds of pulp boards are mixed and crushed by a pulper, then soaked and then deflated and beaten. The refining concentration is controlled at 5.5-6.0%; the beating degree is controlled at: 16-18°SR, wet weight ≥8.5g. Put it into the slurry tank after deflaking and beating;

3)配浆:将磨好的木浆在配浆池中按一定比例配置,再加入10份0.5dtex*4mm涤纶短纤混合,再加入湿强剂,稀释到0.8-1.0%的浓度;湿强剂加入量:1.2%。3) Pulp mixing: mix the ground wood pulp in a certain proportion in the pulp mixing tank, then add 10 parts of 0.5dtex*4mm polyester staple fiber to mix, then add wet strength agent, and dilute to a concentration of 0.8-1.0%; Amount of strong agent added: 1.2%.

4)抄造:将配好的浆料稀释至0.2-0.3%浓度,抽到抄前池经冲浆泵上斜网成形、压榨、干燥;4) Papermaking: Dilute the prepared slurry to a concentration of 0.2-0.3%, pump it to the forebay pool, form it on the inclined screen through the pulp pump, squeeze it, and dry it;

5)表面施胶:经过前道烘干的纸页进入表面施胶装置进行表面施胶,施胶前定量控制在:29-31g/m2,紧度控制在:0.40-0.46g/m3,透气度:20000-40000CU,表面施胶液完全浸没纸页,经过表面施胶辊的均匀挤压,表面施胶液均匀的涂在纸页上;表面施胶液选用丙烯酸胶乳,表面施胶液的浓度为5%-6%。上胶量控制在原纸定量的35-40%,即上胶量控制在12g/m2左右。5) Surface sizing: The paper sheets that have been dried in the previous process enter the surface sizing device for surface sizing. The quantitative control before sizing is: 29-31g/m2 , and the tightness is controlled at: 0.40-0.46g/m3 ,Permeability: 20000-40000CU, the surface sizing solution is completely immersed in the paper, after being uniformly squeezed by the surface sizing roller, the surface sizing solution is evenly coated on the paper; the surface sizing solution is made of acrylic latex, and the surface sizing The concentration of liquid is 5%-6%. The amount of gluing is controlled at 35-40% of the base paper weight, that is, the amount of gluing is controlled at about 12g/m2 .

6)纸的定量控制在40-42g/m26) The basis weight of the paper is controlled at 40-42g/m2 .

7)干燥、卷取和分切包装。7) Drying, coiling and slitting and packaging.

对比例5Comparative example 5

1)浆料配比:将质量份为80份漂白针叶木浆、20份漂白化机浆加入到碎浆机中进行碎解;1) Pulp ratio: 80 parts by mass of bleached softwood pulp and 20 parts of bleached mechanical pulp are added to a pulper for disintegration;

2)疏解和打浆:各种浆板经碎浆机混合碎解后经浸泡后再进行疏解和打浆,磨浆浓度控制在5.5-6.0%;打浆度控制在:18-20°SR,湿重≥8.5g。疏解和打浆完成后放到成浆池;2) Deflagging and beating: all kinds of pulp boards are mixed and crushed by a pulper, then soaked and then deflagrated and beaten. The refining concentration is controlled at 5.5-6.0%; the beating degree is controlled at: 18-20°SR, wet weight ≥8.5g. Put it into the slurry tank after deflaking and beating;

3)配浆:将磨好的木浆在配浆池中按一定比例配置,再加入15份0.5dtex*4mm涤纶短纤混合,再加入湿强剂,稀释到0.8-1.0%的浓度;湿强剂加入量:1.5%。3) Pulp preparation: prepare the ground wood pulp in a certain proportion in the pulp preparation tank, then add 15 parts of 0.5dtex*4mm polyester staple fiber to mix, then add wet strength agent, and dilute to a concentration of 0.8-1.0%; Dosage of strong agent: 1.5%.

4)抄造:将配好的浆料稀释至0.2-0.3%浓度,抽到抄前池经冲浆泵上斜网成形、压榨、干燥;4) Papermaking: Dilute the prepared slurry to a concentration of 0.2-0.3%, pump it to the forebay pool, form it on the inclined screen through the pulp pump, squeeze it, and dry it;

5)表面施胶:经过前道烘干的纸页进入表面施胶装置进行表面施胶,施胶前定量控制在:28-30g/m2,紧度控制在:0.45-0.47g/m3,透气度:15000-20000CU(使用化机浆后纸的紧度会提高,透气度会降低),表面施胶液完全浸没纸页,经过表面施胶辊的均匀挤压,表面施胶液均匀的涂在纸页上;表面施胶液选用丙烯酸胶乳,表面施胶液的浓度为5%-6%。上胶量控制在原纸定量的25-30%,即上胶量控制在9g/m2左右。5) Surface sizing: The paper sheets that have been dried in the previous process enter the surface sizing device for surface sizing. The quantitative control before sizing is: 28-30g/m2 , and the tightness is controlled at: 0.45-0.47g/m3 , Air permeability: 15000-20000CU (the tightness of the paper will increase after using chemical-mechanical pulp, and the air permeability will decrease), the surface sizing liquid is completely immersed in the paper, and the surface sizing liquid is evenly squeezed by the surface sizing roller The surface sizing solution is made of acrylic latex, and the concentration of the surface sizing solution is 5%-6%. The amount of gluing is controlled at 25-30% of the base paper weight, that is, the amount of gluing is controlled atabout 9g/m2.

6)纸的定量控制在36-39g/m26) The basis weight of the paper is controlled at 36-39g/m2 .

7)干燥、卷取和分切包装。7) Drying, coiling and slitting and packaging.

8)纸张再经过机外单面涂布,涂布液为:丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为20-25%,上胶量为原纸定量的5-6%,即上胶量为2g/m2左右;8) The paper is coated on one side outside the machine again, and the coating liquid is: acrylic latex, the concentration of the described acrylic latex solution is 20-25%, and the amount of gluing is 5-6% of the base paper quantitative, that is, the amount of gluing About 2g/m2 ;

9)超级软压光:纸张经过单面涂布后,继续干燥,再经过超级软压光,压光压力控制在:50-60MPa。9) Super soft calendering: After the paper is coated on one side, continue to dry, and then go through super soft calendering, the calendering pressure is controlled at: 50-60MPa.

10)最终纸的定量控制在:38-42g/m210) The quantitative control of the final paper is: 38-42g/m2 .

11)卷取,分切,包装。11) Coiling, cutting and packaging.

对比例6Comparative example 6

1)浆料配比:将质量份为80份漂白针叶木浆、20份漂白化机浆加入到碎浆机中进行碎解;1) Pulp ratio: 80 parts by mass of bleached softwood pulp and 20 parts of bleached mechanical pulp are added to a pulper for disintegration;

2)疏解和打浆:浆板经碎浆机混合碎解后经浸泡后再进行疏解和打浆,磨浆浓度控制在5.5-6.0%;打浆度控制在:27-29°SR,湿重≥8.5g。疏解和打浆完成后放到成浆池;2) Deflagging and beating: the pulp board is mixed and crushed by a pulper and then soaked before deflaking and beating. The refining concentration is controlled at 5.5-6.0%; the beating degree is controlled at: 27-29 ° SR, wet weight ≥ 8.5 g. Put it into the slurry tank after deflaking and beating;

3)配浆:将磨好的木浆在配浆池中按一定比例配置,再加入15份0.5dtex*4mm涤纶短纤混合,再加入湿强剂,稀释到0.8-1.0%的浓度;湿强剂加入量:0.8%。3) Pulp preparation: prepare the ground wood pulp in a certain proportion in the pulp preparation tank, then add 15 parts of 0.5dtex*4mm polyester staple fiber to mix, then add wet strength agent, and dilute to a concentration of 0.8-1.0%; Amount of strong agent added: 0.8%.

4)抄造:将配好的浆料稀释至0.1-0.3%浓度,抽到抄前池经冲浆泵上斜网成形、压榨、干燥;4) Papermaking: Dilute the prepared slurry to a concentration of 0.1-0.3%, pump it to the forebay pool, form it on the inclined screen through the pulp pump, squeeze it, and dry it;

5)表面施胶:经过前道烘干的纸页进入表面施胶装置进行表面施胶,施胶前定量控制在:30-33g/m2,紧度控制在:0.50-0.55g/m3,透气度:4000-6000CU(本例中浆料配比里有部分漂白化机浆,为提高纸的匀度,把打浆度提高至27-29°SR,纸的紧度会大幅提高,透气度会降低很多),表面施胶液完全浸没纸页,经过表面施胶辊的均匀挤压,表面施胶液均匀的涂在纸页上;表面施胶液选用丙烯酸胶乳,表面施胶液的浓度为5%-6%。上胶量控制在原纸定量的18-22%,即上胶量控制在6g/m2左右(施胶前原纸紧度提高较大,纸透气度下降很多,吸收性下降,上胶量减少)。5) Surface sizing: The paper sheets that have been dried in the previous process enter the surface sizing device for surface sizing. The quantitative control before sizing is: 30-33g/m2 , and the tightness is controlled at: 0.50-0.55g/m3 , Air permeability: 4000-6000CU (in this example, there is some bleached mechanical pulp in the pulp ratio, in order to improve the evenness of the paper, increase the beating degree to 27-29°SR, the tightness of the paper will be greatly improved, and the air permeability The surface sizing liquid is completely immersed in the paper sheet, and the surface sizing liquid is evenly coated on the paper page through the uniform extrusion of the surface sizing roller; the surface sizing liquid is made of acrylic latex, and the surface sizing liquid The concentration is 5%-6%. The amount of sizing is controlled at 18-22% of the base paper weight, that is, the amount of sizing is controlled at about 6g/m2 (before sizing, the tightness of the base paper is greatly improved, the air permeability of the paper is greatly reduced, the absorbency is reduced, and the amount of sizing is reduced) .

6)纸的定量控制在36-39g/m26) The basis weight of the paper is controlled at 36-39g/m2 .

7)干燥、卷取和分切包装。7) Drying, coiling and slitting and packaging.

8)纸张再经过机外单面涂布,涂布液为:丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为20-25%,上胶量为原纸定量的5-6%,即上胶量为2g/m2左右;8) The paper is coated on one side outside the machine again, and the coating liquid is: acrylic latex, the concentration of the described acrylic latex solution is 20-25%, and the amount of gluing is 5-6% of the base paper quantitative, that is, the amount of gluing About 2g/m2 ;

9)超级软压光:纸张经过单面涂布后,继续干燥,再经过超级软压光,压光压力控制在:50-60MPa。9) Super soft calendering: After the paper is coated on one side, continue to dry, and then go through super soft calendering, the calendering pressure is controlled at: 50-60MPa.

10)最终纸的定量控制在:38-42g/m210) The quantitative control of the final paper is: 38-42g/m2 .

11)卷取,分切,包装。11) Coiling, cutting and packaging.

对比例7Comparative example 7

1)浆料配比:将质量份为80份漂白针叶木浆、20份漂白阔叶木浆加入到碎浆机中进行碎解;1) Pulp ratio: 80 parts by mass of bleached softwood pulp and 20 parts of bleached hardwood pulp are added to a pulper for disintegration;

2)疏解和打浆:各种浆板经碎浆机混合碎解后经浸泡后再进行疏解和打浆,磨浆浓度控制在5.5-6.0%;打浆度控制在:16-18°SR,湿重≥8.5g。疏解和打浆完成后放到成浆池;2) Thinning and beating: All kinds of pulp boards are mixed and crushed by a pulper, then soaked and then deflated and beaten. The refining concentration is controlled at 5.5-6.0%; the beating degree is controlled at: 16-18°SR, wet weight ≥8.5g. Put it into the slurry tank after deflaking and beating;

3)配浆:将磨好的木浆在配浆池中按一定比例配置,再加入湿强剂,稀释到0.8-1.0%的浓度;湿强剂加入量:1.2%。3) Pulp blending: the ground wood pulp is prepared in a certain proportion in the pulp blending tank, and then wet strength agent is added to dilute to a concentration of 0.8-1.0%; the amount of wet strength agent added: 1.2%.

4)抄造:将配好的浆料稀释至0.1-0.2%浓度,抽到抄前池经冲浆泵上斜网成形、压榨、干燥;4) Papermaking: Dilute the prepared slurry to a concentration of 0.1-0.2%, pump it to the forebay pool, form it on the inclined screen through the pulp pump, squeeze it, and dry it;

5)表面施胶:经过前道烘干的纸页进入表面施胶装置进行表面施胶,施胶前定量控制在:29-31g/m2,紧度控制在:0.46-0.49g/m3,透气度:10000-19000CU,(本例中浆料配比里没有添加涤纶短纤或粘胶短纤,施胶前原纸紧度提高,纸透气度降低)表面施胶液完全浸没纸页,经过表面施胶辊的均匀挤压,表面施胶液均匀的涂在纸页上;施胶前定量控制在:29-32g/m2,表面施胶液选用丙烯酸胶乳,再添加一种黄色颜料,表面施胶液的浓度为5%-6%。上胶量控制在原纸定量的20-24%,,即上胶量控制在7g/m2左右(施胶前原纸紧度偏高,纸吸收性下降,上胶量减少)。5) Surface sizing: The paper sheets that have been dried in the previous process enter the surface sizing device for surface sizing. The quantitative control before sizing is: 29-31g/m2 , and the tightness is controlled at: 0.46-0.49g/m3 , air permeability: 10000-19000CU, (in this example, no polyester staple fiber or viscose staple fiber is added in the slurry ratio, the tightness of the base paper before sizing increases, and the air permeability of the paper decreases) The surface sizing solution completely immerses the paper, After the uniform extrusion of the surface sizing roller, the surface sizing liquid is evenly coated on the paper; the quantitative control before sizing is: 29-32g/m2 , the surface sizing liquid is made of acrylic latex, and a yellow pigment is added , the concentration of the surface sizing solution is 5%-6%. The amount of sizing is controlled at 20-24% of the base paper weight, that is, the amount of sizing is controlled at about 7g/m2 (the tightness of the base paper before sizing is high, the absorbency of the paper decreases, and the amount of sizing decreases).

6)纸的定量控制在36-39g/m26) The basis weight of the paper is controlled at 36-39g/m2 .

7)干燥、卷取和分切包装。7) Drying, coiling and slitting and packaging.

8)纸张再经过机外单面涂布,涂布液为:丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为20-25%,上胶量为原纸定量的5-6,即上胶量为2g/m2左右%;8) Paper is coated on one side outside the machine again, and the coating solution is: acrylic latex, the concentration of the described acrylic latex solution is 20-25%, and the amount of gluing is 5-6% of the base paper quantitatively, that is, the amount of gluing is About 2g/m2 %;

9)超级软压光:纸张经过单面涂布后,继续干燥,再经过超级软压光,压光压力控制在:50-60MPa。9) Super soft calendering: After the paper is coated on one side, continue to dry, and then go through super soft calendering, the calendering pressure is controlled at: 50-60MPa.

10)最终纸的定量控制在:38-42g/m210) The quantitative control of the final paper is: 38-42g/m2 .

11)卷取,分切,包装。11) Coiling, cutting and packaging.

对比例8Comparative example 8

1)浆料配比:将质量份为80份漂白针叶木浆、20份漂白阔叶木浆加入到碎浆机中进行碎解;1) Pulp ratio: 80 parts by mass of bleached softwood pulp and 20 parts of bleached hardwood pulp are added to a pulper for disintegration;

2)疏解和打浆:各种浆板经碎浆机混合碎解后经浸泡后再进行疏解和打浆,磨浆浓度控制在5.5-6.0%;打浆度控制在:16-18°SR,湿重≥8.5g。疏解和打浆完成后放到成浆池;2) Thinning and beating: All kinds of pulp boards are mixed and crushed by a pulper, then soaked and then deflated and beaten. The refining concentration is controlled at 5.5-6.0%; the beating degree is controlled at: 16-18°SR, wet weight ≥8.5g. Put it into the slurry tank after deflaking and beating;

3)配浆:将磨好的木浆在配浆池中按一定比例配置,再加入10份0.5dtex*4mm涤纶短纤混合,再加入湿强剂,稀释到0.8-1.0%的浓度;湿强剂加入量:1.2%。3) Pulp mixing: mix the ground wood pulp in a certain proportion in the pulp mixing tank, then add 10 parts of 0.5dtex*4mm polyester staple fiber to mix, then add wet strength agent, and dilute to a concentration of 0.8-1.0%; Amount of strong agent added: 1.2%.

4)抄造:将配好的浆料稀释至0.2-0.3%浓度,抽到抄前池经冲浆泵上斜网成形、压榨、干燥;4) Papermaking: Dilute the prepared slurry to a concentration of 0.2-0.3%, pump it to the forebay pool, form it on the inclined screen through the pulp pump, squeeze it, and dry it;

5))纸的定量控制在:27-29g/m2,紧度控制在:0.40-0.46g/m3,透气度:20000-40000CU。5)) Quantitative control of paper: 27-29g/m2 , tightness: 0.40-0.46g/m3 , air permeability: 20000-40000CU.

6)干燥、卷取和分切。6) Drying, coiling and slitting.

7)纸张再经过机外浸渍涂布,涂布液为:丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为20-25%,上胶量为原纸定量的38-42%,即上胶量控制在12g/m2左右%;7) The paper is dipped and coated outside the machine again, and the coating solution is: acrylic latex, the concentration of the described acrylic latex solution is 20-25%, and the amount of gluing is 38-42% of the base paper quantitative, that is, the amount of gluing is controlled Around 12g/m2 %;

8)超级软压光:纸张经过单面涂布后,继续干燥,再经过超级软压光,压光压力控制在:50-60MPa。8) Super soft calendering: After the paper is coated on one side, continue to dry, and then go through super soft calendering, and the calendering pressure is controlled at 50-60MPa.

9)最终纸的定量控制在:38-42g/m29) The quantitative control of the final paper is: 38-42g/m2 .

10)卷取,分切,包装。10) Coiling, cutting and packaging.

对比例9Comparative example 9

1)浆料配比:将质量份为80份漂白针叶木浆、25份漂白化机浆加入到碎浆机中进行碎解;1) Pulp ratio: 80 parts by mass of bleached softwood pulp and 25 parts of bleached mechanical pulp are added to a pulper for disintegration;

2)疏解和打浆:各种浆板经碎浆机混合碎解后经浸泡后再进行疏解和打浆,磨浆浓度控制在5.5-6.0%;打浆度控制在:18-20°SR,湿重≥8.5g。疏解和打浆完成后放到成浆池;2) Deflagging and beating: all kinds of pulp boards are mixed and crushed by a pulper, then soaked and then deflagrated and beaten. The refining concentration is controlled at 5.5-6.0%; the beating degree is controlled at: 18-20°SR, wet weight ≥8.5g. Put it into the slurry tank after deflaking and beating;

3)配浆:将磨好的木浆在配浆池中按一定比例配置,再加入湿强剂,稀释到0.8-1.0%的浓度;湿强剂加入量:1.5%。3) Pulp blending: the ground wood pulp is prepared in a certain proportion in the pulp blending tank, and then wet strength agent is added to dilute to a concentration of 0.8-1.0%; the amount of wet strength agent added: 1.5%.

4)抄造:将配好的浆料稀释至0.2-0.3%浓度,抽到抄前池经冲浆泵上斜网成形、压榨、干燥;4) Papermaking: Dilute the prepared slurry to a concentration of 0.2-0.3%, pump it to the forebay pool, form it on the inclined screen through the pulp pump, squeeze it, and dry it;

5)表面施胶:经过前道烘干的纸页进入表面施胶装置进行表面施胶,施胶前定量控制在:29-32g/m2,紧度控制在:0,50-0.53g/m3,透气度:5000-8000CU(没有化纤或粘胶纤维,使用部分化机浆后纸的紧度会明显提高,透气度会降低很多),表面施胶液完全浸没纸页,经过表面施胶辊的均匀挤压,表面施胶液均匀的涂在纸页上;表面施胶液选用丙烯酸胶乳,表面施胶液的浓度为5%-6%。上胶量控制在原纸定量的20-25%,即上胶量控制在7g/m2左右。5) Surface sizing: The paper sheets that have been dried in the previous process enter the surface sizing device for surface sizing. The quantitative control before sizing is: 29-32g/m2 , and the tightness is controlled at: 0,50-0.53g/m2 m3 , air permeability: 5000-8000CU (without chemical fiber or viscose fiber, the tightness of the paper will be significantly improved after using partial mechanical pulp, and the air permeability will be greatly reduced), the surface sizing solution is completely immersed in the paper, after surface application Uniform extrusion of the rubber roller, the surface sizing solution is evenly coated on the paper; the surface sizing solution is made of acrylic latex, and the concentration of the surface sizing solution is 5%-6%. The amount of gluing is controlled at 20-25% of the base paper weight, that is, the amount of gluing is controlled atabout 7g/m2.

6)纸的定量控制在36-39g/m26) The basis weight of the paper is controlled at 36-39g/m2 .

7)干燥、卷取和分切包装。7) Drying, coiling and slitting and packaging.

8)纸张再经过机外单面涂布,涂布液为:丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为20-25%,上胶量为原纸定量的5-6%,即上胶量为2g/m2左右;8) The paper is coated on one side outside the machine again, and the coating liquid is: acrylic latex, the concentration of the described acrylic latex solution is 20-25%, and the amount of gluing is 5-6% of the base paper quantitative, that is, the amount of gluing About 2g/m2 ;

9)超级软压光:纸张经过单面涂布后,继续干燥,再经过超级软压光,压光压力控制在:50-60MPa。9) Super soft calendering: After the paper is coated on one side, continue to dry, and then go through super soft calendering, the calendering pressure is controlled at: 50-60MPa.

10)最终纸的定量控制在:38-42g/m210) The quantitative control of the final paper is: 38-42g/m2 .

11)卷取,分切,包装。11) Coiling, cutting and packaging.

对比例10Comparative example 10

按中国发明专利(公开号:CN105155329A)和纸胶带原纸及其生产方法专利技术生产的纸张。Paper produced according to the patented technology of Chinese invention patent (publication number: CN105155329A) and paper tape base paper and its production method.

实施例1-6检测结果见表2,对比例1-10检测结果见表3。The test results of Examples 1-6 are shown in Table 2, and the test results of Comparative Examples 1-10 are shown in Table 3.

表2实施例1-6和纸胶带原纸性能检测Table 2 embodiment 1-6 and paper tape base paper property detection

Figure BDA0003552114810000161
Figure BDA0003552114810000161

表3对比例1-10和纸胶带原纸性能检测Table 3 Comparative Example 1-10 and Paper Tape Base Paper Performance Test

Figure BDA0003552114810000171
Figure BDA0003552114810000171

以上为对本发明实施例的描述,通过对所公开的实施例的上述说明,使本领域专业技术人员能够实现或使用本发明。对这些实施例的多种修改对本领域的专业技术人员来说将是显而易见的。本文中所定义的一般原理可以在不脱离本发明的精神或范围的情况下,在其它实施例中实现。因此,本发明将不会被限制于本文所示的这些实施列,而是要符合与本文所公开的原理和新颖点相一致的最宽的范围。The foregoing is a description of the embodiments of the present invention, and through the above descriptions of the disclosed embodiments, those skilled in the art can implement or use the present invention. Various modifications to these examples will be apparent to those skilled in the art. The general principles defined herein may be implemented in other embodiments without departing from the spirit or scope of the invention. Therefore, the present invention will not be limited to these embodiments shown herein, but will conform to the widest scope consistent with the principles and novel points disclosed herein.

Claims (11)

Translated fromChinese
1.一种高性能和纸胶带原纸,其特征在于,按质量份数计,该和纸胶带原纸的纤维浆料的配方由以下的纤维类原料组成:1. a high-performance washi tape base paper, is characterized in that, by mass parts, the formula of the fiber slurry of this washi tape base paper is made up of following fibrous raw materials:化学纤维5-20份,5-20 parts of chemical fiber,漂白短纤维木浆20-50份,20-50 parts of bleached short-fiber wood pulp,漂白长纤维木浆50-80份;50-80 parts of bleached long fiber wood pulp;所述原纸配方还包括湿强剂和表面施胶液,湿强剂的加入量为纤维总质量0.5-2.5%,所述湿强剂采用PAE和PPE中的一种或两种;The base paper formula also includes a wet strength agent and a surface sizing solution, the wet strength agent is added in an amount of 0.5-2.5% of the total fiber mass, and the wet strength agent adopts one or both of PAE and PPE;其中漂白短纤维木浆+漂白长纤维木浆为100份;所述的化学纤维的规格为:0.4-3.0dtex,长度为2-10mm;所述漂白短纤维木浆采用化学制浆法制得,漂白短纤维木浆的纤维长度为0.65-1.0mm,纤维的宽度为18-23μm,漂白长纤维木浆的纤维长度为1.50-3.0mm,纤维的宽度为28-35μm;所述化学纤维为涤纶纤维或粘胶纤维中的一种;Wherein bleached short-fiber wood pulp + bleached long-fiber wood pulp is 100 parts; the specification of the chemical fiber is: 0.4-3.0dtex, and the length is 2-10mm; the bleached short-fiber wood pulp is made by chemical pulping method, The fiber length of the bleached short-fiber wood pulp is 0.65-1.0 mm, and the fiber width is 18-23 μm; the fiber length of the bleached long-fiber wood pulp is 1.50-3.0 mm, and the fiber width is 28-35 μm; the chemical fiber is polyester one of fiber or viscose;该和纸胶带原纸的制备方法包括以下的步骤:The preparation method of this paper tape base paper comprises the following steps:1)木浆碎解:将漂白短纤维木浆、漂白长纤维木浆加入到碎浆机中进行碎解;1) Wood pulp disintegration: Add bleached short-fiber wood pulp and bleached long-fiber wood pulp to the pulper for disintegration;2)疏解和打浆:各种木浆经碎浆机混合碎解后经浸泡后再进行疏解和打浆,磨浆浓度控制在4.0-6.0%;打浆度控制在:16-200SR,湿重:≥7g;完成后放到成浆池;2) Thinning and beating: All kinds of wood pulp are mixed and crushed by a pulper, then soaked and then deflagged and beaten. The refining concentration is controlled at 4.0-6.0%; the beating degree is controlled at: 16-200 SR, wet weight : ≥7g; put it into the slurry tank after completion;3)配浆:将磨好的木浆在配浆池中按一定比例配置,加入化学纤维混合,再加入湿强剂;湿强剂稀释到0.5-2.5%的浓度再添加;3) Pulp blending: the ground wood pulp is prepared in a certain proportion in the pulp blending tank, mixed with chemical fibers, and then added with wet strength agent; the wet strength agent is diluted to a concentration of 0.5-2.5% before adding;4)抄造:将配好的浆料稀释至0.1-0.5%浓度,抽到抄前池经冲浆泵上斜网或圆网成形、压榨、干燥;4) Papermaking: Dilute the prepared slurry to a concentration of 0.1-0.5%, pump it into the forebay pool, and form it on the inclined screen or circular screen through the pulping pump, press, and dry;抄造后经过前道烘干的纸页进入表面施胶装置进行表面施胶,表面施胶液完全浸没纸页,经过表面施胶辊的均匀挤压,表面施胶液均匀的吸附在纸页里面,所述的表面施胶的表面施胶液为丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为5-10%,上胶量为原纸定量的30-50%;干燥后,纸张再经过机外单面涂布,涂布液为丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为20-25%,上胶量为原纸定量的4-6%。After papermaking, the paper sheets that have been dried in the previous process enter the surface sizing device for surface sizing. The surface sizing liquid is completely immersed in the paper sheet, and the surface sizing liquid is evenly squeezed by the surface sizing roller, and the surface sizing liquid is evenly adsorbed on the inside of the paper sheet. , the surface sizing solution of the surface sizing is acrylic latex, the concentration of the acrylic latex solution is 5-10%, and the amount of sizing is 30-50% of the base paper quantitative; after drying, the paper passes through the outside of the machine One-sided coating, the coating solution is acrylic latex, the concentration of the acrylic latex solution is 20-25%, and the amount of glue is 4-6% of the base paper weight.2.根据权利要求1所述的和纸胶带原纸,其特征在于,所述化学纤维的规格为:所述的化学纤维的规格为:0.5-1.7dtex,长度为4-5mm。2. The washi tape base paper according to claim 1, characterized in that, the specification of the chemical fiber is: the specification of the chemical fiber is: 0.5-1.7dtex, and the length is 4-5mm.3.根据权利要求1所述的和纸胶带原纸,其特征在于,所述化学纤维质量份数为8-12份。3. The washi tape base paper according to claim 1, wherein the chemical fiber mass fraction is 8-12 parts.4.根据权利要求1所述的和纸胶带原纸,其特征在于,所述漂白短纤维木浆质量份数为20-40份;漂白长纤维木浆质量份数为60-80份。4. The washi tape base paper according to claim 1, wherein the mass fraction of the bleached short-fiber wood pulp is 20-40 parts; the mass fraction of the bleached long-fiber wood pulp is 60-80 parts.5.根据权利要求4所述的和纸胶带原纸,其特征在于,漂白短纤维木浆的纤维长度为0.70-0.85mm,纤维的宽度为18-21μm,漂白长纤维木浆的纤维长度为1.80-2.5mm,纤维的宽度为30-33μm。5. Washi tape base paper according to claim 4, is characterized in that, the fiber length of bleached short-fiber wood pulp is 0.70-0.85 mm, the width of fiber is 18-21 μm, and the fiber length of bleached long-fiber wood pulp is 1.80 mm. -2.5mm, the width of the fiber is 30-33μm.6.根据权利要求1所述的和纸胶带原纸,其特征在于,所述原纸配方还包括染料;染料按颜色需要确定添加量。6. The base paper of washi tape according to claim 1, characterized in that, the base paper formula also includes dyes; the amount of dyes added is determined according to the needs of the color.7.根据权利要求1所述的和纸胶带原纸,其特征在于,所述湿强剂的加入量为纤维总质量的1.0-2.0%。7. The washi tape base paper according to claim 1, characterized in that, the addition of the wet strength agent is 1.0-2.0% of the total fiber mass.8.根据权利要求1所述的和纸胶带原纸,其特征在于,所述表面施胶液的总上胶量为原纸总质量的35-45%。8. The base paper of washi tape according to claim 1, characterized in that, the total sizing amount of the surface sizing solution is 35-45% of the total mass of the base paper.9.一种权利要求1-5、7和8任意一项所述和纸胶带原纸的生产方法,其特征在于,该方法包括以下的步骤:9. a production method of any one of claims 1-5, 7 and 8, characterized in that the method comprises the following steps:1)木浆碎解:将漂白短纤维木浆、漂白长纤维木浆加入到碎浆机中进行碎解;1) Wood pulp disintegration: Add bleached short-fiber wood pulp and bleached long-fiber wood pulp to the pulper for disintegration;2)疏解和打浆:各种木浆经碎浆机混合碎解后经浸泡后再进行疏解和打浆,磨浆浓度控制在4.0-6.0%;打浆度控制在:16-200SR,湿重:≥7g;完成后放到成浆池;2) Thinning and beating: All kinds of wood pulp are mixed and crushed by a pulper, then soaked and then deflagged and beaten. The refining concentration is controlled at 4.0-6.0%; the beating degree is controlled at: 16-200 SR, wet weight : ≥7g; put it into the slurry tank after completion;3)配浆:将磨好的木浆在配浆池中按一定比例配置,加入化学纤维混合,再加入湿强剂;湿强剂稀释到0.8-2.0%的浓度再添加;3) Pulp blending: the ground wood pulp is prepared in a certain proportion in the pulp blending tank, mixed with chemical fibers, and then added with wet strength agent; the wet strength agent is diluted to a concentration of 0.8-2.0% before adding;4)抄造:将配好的浆料稀释至0.1-0.5%浓度,抽到抄前池经冲浆泵上斜网或圆网成形、压榨、干燥;4) Papermaking: Dilute the prepared slurry to a concentration of 0.1-0.5%, pump it into the forebay pool, and form it on the inclined screen or circular screen through the pulping pump, press, and dry;5)表面施胶:经过前道烘干的纸页进入表面施胶装置进行表面施胶,表面施胶液完全浸没纸页,经过表面施胶辊的均匀挤压,表面施胶液均匀的吸附在纸页里面;所述的表面施胶的表面施胶液为丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为5-10%,上胶量为原纸定量的30-50%;5) Surface sizing: The paper sheets that have been dried in the previous process enter the surface sizing device for surface sizing, the surface sizing liquid is completely immersed in the paper sheet, and the surface sizing liquid is evenly squeezed by the surface sizing roller, and the surface sizing liquid is evenly adsorbed Inside the paper sheet; the surface sizing solution of the surface sizing is acrylic latex, the concentration of the acrylic latex solution is 5-10%, and the amount of sizing is 30-50% of the base paper quantitative;6)干燥、卷取;6) Drying and coiling;7)纸张再经过机外单面涂布,施胶液为:丙烯酸胶乳,所述的丙烯酸胶乳溶液的浓度为20-25%,上胶量为原纸定量的4-6%;7) The paper is coated on one side outside the machine, the sizing solution is: acrylic latex, the concentration of the acrylic latex solution is 20-25%, and the amount of sizing is 4-6% of the base paper;8)超级软压光:纸张经过单面涂布后,继续干燥,再经过超级软压光,压光压力控制在:30-60MPa;8) Super soft calendering: After the paper is coated on one side, continue to dry, and then go through super soft calendering, and the calendering pressure is controlled at: 30-60MPa;9)卷取,分切,包装。9) Coiling, cutting and packaging.10.根据权利要求9所述的方法,其特征在于,原纸配方还包括染料;染料按颜色需要确定添加量;在施胶液中添加相应的染料。10. The method according to claim 9, characterized in that the base paper formula also includes dyes; the amount of dyes added is determined according to the color requirements; corresponding dyes are added to the sizing solution.11.一种和纸胶带,其特征在于,该和纸胶带的原纸采用权利要求1-8任意一项所述和纸胶带原纸。11. A washi tape, characterized in that, the base paper of the washi tape adopts the base paper of any one of claims 1-8.
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