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CN116536964A - Preparation method of multilayer laminated paper and multilayer laminated paper - Google Patents

Preparation method of multilayer laminated paper and multilayer laminated paper Download PDF

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Publication number
CN116536964A
CN116536964A CN202310511328.9A CN202310511328A CN116536964A CN 116536964 A CN116536964 A CN 116536964A CN 202310511328 A CN202310511328 A CN 202310511328A CN 116536964 A CN116536964 A CN 116536964A
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CN
China
Prior art keywords
paper
beating
laminated paper
layer laminated
latex
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Pending
Application number
CN202310511328.9A
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Chinese (zh)
Inventor
杨欣
张便芝
刘泽覃
邢新月
潘桂云
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Gold East Paper Jiangsu Co Ltd
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Gold East Paper Jiangsu Co Ltd
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Publication date
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Priority to CN202310511328.9A priority Critical patent/CN116536964A/en
Publication of CN116536964A publication Critical patent/CN116536964A/en
Pending legal-status Critical Current

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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H27/00Special paper not otherwise provided for, e.g. made by multi-step processes
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F11/00Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F11/00Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines
    • D21F11/06Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines of the cylinder type
    • D21F11/08Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines of the cylinder type paper or board consisting of two or more layers
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/21Macromolecular organic compounds of natural origin; Derivatives thereof
    • D21H17/24Polysaccharides
    • D21H17/28Starch
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/33Synthetic macromolecular compounds
    • D21H17/34Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H19/00Coated paper; Coating material
    • D21H19/10Coatings without pigments
    • D21H19/14Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H19/00Coated paper; Coating material
    • D21H19/10Coatings without pigments
    • D21H19/14Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12
    • D21H19/20Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12 comprising macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP 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
    • D21H27/00Special paper not otherwise provided for, e.g. made by multi-step processes
    • D21H27/30Multi-ply
    • D21H27/32Multi-ply with materials applied between the sheets

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Paper (AREA)

Abstract

The application provides a preparation method of multilayer laminated paper and the multilayer laminated paper, and relates to the technical field of papermaking. The preparation method of the multilayer laminated paper comprises the steps of spraying starch solution and latex with a Tg value not more than 2 and not less than-2 on the surfaces to be combined of the multilayer formed paper, laminating the sprayed multilayer formed paper, carrying out multiple combined pressing, and drying the paper subjected to combined pressing to obtain the multilayer laminated paper. According to the method, the starch solution and the latex are sprayed, so that the multi-layer forming paper has higher cohesive force after lamination, the latex with the Tg value not more than 2 and not less than-2 is selected to improve the flexibility of the dried multi-layer laminating paper, and the multi-layer combination squeezing can improve the tightness of the paper formed by lamination, so that the effect of improving the interlayer bonding strength of the multi-layer laminating paper is achieved.

Description

多层叠合纸的制备方法及多层叠合纸Preparation method of multi-layer laminated paper and multi-layer laminated paper

技术领域technical field

本申请涉及造纸技术领域,特别是涉及一种多层叠合纸的制备方法及多层叠合纸。The present application relates to the technical field of papermaking, in particular to a method for preparing multilayer laminated paper and the multilayer laminated paper.

背景技术Background technique

多层叠合纸是为多层叠合结构,具有高克重的特点,可作为电子器件定位基材、餐盘纸、乐高产品生产用纸等,在多个领域发挥作用。以电子器件定位基材为例,贴片电容(MLCC)在组装到主板上时需要有基材定位,传统的定位基材的塑胶制品,但随着MLCC产品的小型化发展,塑料制品在作为小尺寸MLCC产品的定位基材时打孔的边角难打磨成圆角,而且塑料制品容易产生静电问题,会吸附这些越来越小的电子MLCC产品,所以塑料制品逐渐被高克重的多层叠合纸所替代。Multi-layer laminated paper is a multi-layer laminated structure with a high grammage. It can be used as a positioning substrate for electronic devices, dinner plate paper, paper for Lego product production, etc., and plays a role in many fields. Taking the positioning substrate of electronic devices as an example, chip capacitors (MLCC) need to have substrate positioning when they are assembled on the motherboard. The traditional plastic products for positioning the substrate, but with the miniaturization of MLCC products, plastic products are used as When positioning substrates for small-sized MLCC products, it is difficult to round the corners of punched holes, and plastic products are prone to static electricity problems, which will absorb these smaller and smaller electronic MLCC products, so plastic products are gradually being replaced by more and more heavy-weight products. Laminated paper instead.

多层叠合纸在应用时常常需要经过加工处理,例如打孔、冲压等,这对多层叠合纸的层间结合强度有较高的要求。相关的多层叠合纸的层间结合通常是依靠纤维纸浆的羟基结合、以及在层间喷淋淀粉实现的,但这种方法仅能够满足克重相对较低的多层叠合纸的要求,在多层叠合纸的克重较高,例如克重大于600g/m2时,上述方法并不足以使得多层叠合纸具有足够高的层间结合强度,容易导致高克重的多层叠合纸在加工过程中出现分层现象,出现分层的多层叠合纸在使用时容易引发其他问题,例如在填充MLCC产品时这些MLCC产品可能会被夹在分层中而无法使用。Multi-layer laminated paper often needs to be processed during application, such as punching, punching, etc., which has higher requirements for the interlayer bonding strength of multi-layer laminated paper. The inter-layer bonding of related multi-layer laminated paper is usually achieved by the combination of hydroxyl groups of fiber pulp and spraying starch between layers, but this method can only meet the requirements of multi-layer laminated paper with relatively low grammage. The grammage of the multilayer laminated paper is relatively high, for example, when the grammage is greater than 600g/m 2 , the above method is not enough to make the multilayer laminated paper have a sufficiently high interlayer bonding strength, which will easily lead to the high grammage of the multilayer laminated paper. Delamination occurs during processing, and the delaminated multi-layer laminated paper is likely to cause other problems when used. For example, when filling MLCC products, these MLCC products may be caught in the delamination and cannot be used.

发明内容Contents of the invention

本申请主要解决的技术问题是如何提高多层叠合纸的层间结合强度。The technical problem mainly solved by this application is how to improve the bonding strength between layers of laminated paper.

为解决上述技术问题,本申请采用的一个技术方案是:提供一种多层叠合纸的制备方法,包括:In order to solve the above technical problems, a technical solution adopted by the present application is to provide a method for preparing multi-layer laminated paper, including:

进行打浆、配浆,得到抄纸所需纸浆;Perform beating and pulping to obtain the pulp required for papermaking;

将纸浆分别送至造纸机的多个纸网上,使纸浆脱水成型,得到多层成型纸;Send the pulp to multiple paper nets of the paper machine to dehydrate and form the pulp to obtain multi-layer formed paper;

将喷淋剂喷淋在多层成型纸的待结合表面上,喷淋剂包括淀粉液和胶乳,胶乳的Tg值不大于2并且不小于-2;Spray the spray agent on the surface to be bonded of the multi-layer forming paper, the spray agent includes starch liquid and latex, and the Tg value of the latex is not greater than 2 and not less than -2;

将喷淋后的多层成型纸叠合并进行多道组合压榨;Stack the sprayed multi-layer molding paper and perform multi-channel combined pressing;

将经过组合压榨后的纸张烘干,得到多层叠合纸。Dry the combined pressed paper to obtain multi-layer laminated paper.

在一些实施例中,胶乳为丙烯酸类胶乳、丁腈类胶乳、羧基丁苯类胶乳、苯丙类胶乳中的任意一种。In some embodiments, the latex is any one of acrylic latex, nitrile latex, carboxylated styrene-butadiene latex, and styrene-acrylic latex.

在一些实施例中,胶乳的喷淋量为每吨纸喷淋3.0kg-3.5kg。In some embodiments, the spray amount of latex is 3.0kg-3.5kg per ton of paper.

在一些实施例中,淀粉液的制备过程包括:In some embodiments, the preparation process of starch liquid comprises:

将原淀粉与水混合成浓度为1%-10%的淀粉溶液;mixing raw starch with water to form a starch solution with a concentration of 1%-10%;

在90℃-100℃下将淀粉溶液糊化成淀粉液。The starch solution is gelatinized into starch liquid at 90°C-100°C.

在一些实施例中,淀粉液的喷淋量为每吨纸喷淋30kg-35kg。In some embodiments, the spray amount of the starch liquid is 30kg-35kg per ton of paper.

在一些实施例中,在进行多道组合压榨的步骤中,将纸张的紧度压榨至不小于0.9g/m3In some embodiments, in the step of performing multiple combined pressing, the tightness of the paper is pressed to not less than 0.9 g/m 3 .

在一些实施例中,在进行多道组合压榨的步骤中,多道压榨的压力呈逐渐上升的趋势。In some embodiments, during the step of performing multi-pass combined pressing, the pressure of the multi-pass pressed tends to increase gradually.

在一些实施例中,每层成型纸的克重控制在85g/m2 -95g/m2的范围内In some embodiments, the grammage of each layer of forming paper is controlled within the range of 85g/m 2 -95g/m 2

在一些实施例中,进行打浆、配浆的步骤包括:In some embodiments, the steps of beating and pulping include:

采用锥形磨浆机进行第一段打浆,以将浆料中的纤维分丝帚化;Use a conical refiner for the first stage of beating to separate the fibers in the pulp into filaments;

采用单盘磨打浆机进行第二段打浆,并在第二段打浆过程中加入打浆助剂,使得打浆助剂能够与纤维充分接触。A single-disk mill beater is used for the second stage of beating, and beating aids are added during the second stage of beating, so that the beating aids can fully contact the fibers.

在一些实施例中,第一段打浆的打浆浓度为8%-12%,打浆度为20°SR-30°SR;第二段打浆的打浆浓度为3%-5%,打浆度为38°SR-42°SR,打浆助剂的添加量为纤维绝干质量的10%-20%。In some embodiments, the beating concentration of the first stage of beating is 8%-12%, and the beating degree is 20°SR-30°SR; the beating concentration of the second stage beating is 3%-5%, and the beating degree is 38° For SR-42°SR, the amount of beating aid added is 10%-20% of the absolute dry mass of the fiber.

在一些实施例中,进行打浆、配浆的步骤还包括:在完成第二段打浆后,加入浆内淀粉和湿强剂,浆内淀粉按每吨纸6kg-15kg的量添加,湿强剂按每吨纸1kg-2kg的量添加,以将浆料浓度稀释至1%-2%;再按每吨纸20kg-35kg的量添加烷基烯酮二聚体。In some embodiments, the steps of beating and pulping further include: after the second stage of beating is completed, adding starch in the pulp and a wet strength agent, the starch in the pulp is added in an amount of 6kg-15kg per ton of paper, and the wet strength agent Add in an amount of 1kg-2kg per ton of paper to dilute the slurry concentration to 1%-2%; then add alkyl ketene dimer in an amount of 20kg-35kg per ton of paper.

为解决上述技术问题,本申请采用的另一个技术方案是:提供一种多层叠合纸,多层叠合纸通过上述的多层叠合纸的制备方法制得。In order to solve the above technical problems, another technical solution adopted by the present application is to provide a multi-layer laminated paper, which is produced by the above-mentioned preparation method of the multi-layer laminated paper.

区别于现有技术,本申请提供的多层叠合纸的制备方法及多层叠合纸的有益效果是:Different from the prior art, the preparation method of the multi-layer laminated paper provided by the present application and the beneficial effects of the multi-layer laminated paper are:

本申请通过在多层成型纸的待结合表面上喷淋淀粉液、以及Tg值不大于2并且不小于-2的胶乳,然后将喷淋后的多层成型纸叠合并进行多道组合压榨,再将经过组合压榨后的纸张烘干得到多层叠合纸;其中,喷淋淀粉液和胶乳能够使多层成型纸在叠合后具有更高的内聚力,选用Tg值不大于2并且不小于-2的胶乳能够提高干燥后的多层叠合纸的柔韧度,多道组合压榨能够提高叠合而成的纸张的紧度,从而实现提高多层叠合纸的层间结合强度的效果。In this application, starch liquid and latex with a Tg value not greater than 2 and not less than -2 are sprayed on the surface of the multi-layer forming paper to be bonded, and then the sprayed multi-layer forming paper is stacked and multi-channel combined pressing is carried out. Then dry the combined and pressed paper to obtain multi-layer laminated paper; among them, spraying starch liquid and latex can make the multi-layer formed paper have higher cohesion after lamination, and the selected Tg value is not greater than 2 and not less than - The latex of 2 can improve the flexibility of the multi-layer laminated paper after drying, and the multi-pass combined pressing can increase the tightness of the laminated paper, thereby achieving the effect of improving the interlayer bonding strength of the multi-layer laminated paper.

附图说明Description of drawings

为了更清楚地说明本申请实施例中的技术方案,下面将对实施例中所需要使用的附图作简单地介绍。显而易见地,下面描述中的附图仅仅是本申请的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to illustrate the technical solutions in the embodiments of the present application more clearly, the following will briefly introduce the drawings that are used in the embodiments. Apparently, the drawings in the following description are only some embodiments of the present application, and those skilled in the art can obtain other drawings according to these drawings without creative efforts.

图1是本申请一些实施例提供的多层叠合纸的制备方法的流程示意图;Fig. 1 is a schematic flow chart of the preparation method of multi-layer laminated paper provided by some embodiments of the present application;

图2是本申请一些实施例提供的打浆流程示意图;Fig. 2 is a schematic diagram of the beating process provided by some embodiments of the present application;

图3是本申请一些实施例提供的多层叠合纸的制备方法的流程示意图;Fig. 3 is a schematic flow chart of the preparation method of multi-layer laminated paper provided by some embodiments of the present application;

图4是本申请一些实施例提供的多层叠合纸的结构示意图。Fig. 4 is a schematic structural view of a multi-layer laminated paper provided by some embodiments of the present application.

具体实施方式Detailed ways

以下描述中,为了说明而不是为了限定,提出了诸如特定系统结构、技术之类的具体细节,以便透彻理解本申请实施例。然而,本领域的技术人员应当清楚,在没有这些具体细节的其它实施例中也可以实现本申请。在其它情况中,省略对众所周知的系统、装置、电路以及方法的详细说明,以免不必要的细节妨碍本申请的描述。In the following description, specific details such as specific system structures and technologies are presented for the purpose of illustration rather than limitation, so as to thoroughly understand the embodiments of the present application. It will be apparent, however, to one skilled in the art that the present application may be practiced in other embodiments without these specific details. In other instances, detailed descriptions of well-known systems, devices, circuits, and methods are omitted so as not to obscure the description of the present application with unnecessary detail.

为使本申请的上述目的、特征和优点能够更为明显易懂,下面结合附图,对本申请的具体实施方式做详细的说明。可以理解的是,所描述的实施例仅是本申请的一部分实施例,而不是全部的实施例。基于本申请中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本申请保护的范围。In order to make the above purpose, features and advantages of the present application more obvious and understandable, the specific implementation manners of the present application will be described in detail below in conjunction with the accompanying drawings. It should be understood that the described embodiments are only some of the embodiments of the present application, but not all of the embodiments. Based on the embodiments in this application, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the scope of protection of this application.

应当理解,在本申请说明书和所附权利要求书中使用的术语“包括”、“含有”、“具有”以及它们的任何变形,意图都在于覆盖不排他的包含。例如包含了一系列步骤或单元的过程、方法、系统、产品或设备没有限定于已列出的步骤或单元,而是可选地还包括没有列出的步骤或单元,或可选地还包括对于这些过程、方法、产品或设备固有的其它步骤或单元。It should be understood that the terms "comprising", "comprising", "having" and any variations thereof used in the specification and appended claims of this application are intended to cover a non-exclusive inclusion. For example, a process, method, system, product or device comprising a series of steps or units is not limited to the listed steps or units, but optionally also includes unlisted steps or units, or optionally further includes For other steps or units inherent in these processes, methods, products or apparatuses.

本申请提供一种多层叠合纸的制备方法。The application provides a method for preparing multilayer laminated paper.

请参阅图1,图1是本申请一些实施例提供的多层叠合纸的制备方法的流程示意图。Please refer to FIG. 1 . FIG. 1 is a schematic flowchart of a method for preparing multi-layer laminated paper provided in some embodiments of the present application.

多层叠合纸的制备方法包括:The preparation method of multi-layer laminated paper comprises:

S11、打浆、配浆。S11, beating and blending.

进行打浆、配浆,得到抄纸所需纸浆。其中,进行打浆的浆料可以包括硫酸盐漂白针叶木和硫酸盐漂白阔叶木。针叶木纤维长度较长(2-4mm),能够为纸张提供足够的强度,而阔叶木纤维较短(小于1mm),能够使得纸张具有更佳的表面触感及柔软度,通过采用针叶木浆与阔叶木浆进行组配能够满足不同产品的要求。Perform beating and pulping to obtain the pulp required for papermaking. Wherein, pulp for beating may include bleached kraft softwood and kraft bleached hardwood. The fiber length of coniferous wood is longer (2-4mm), which can provide sufficient strength for paper, while the fiber length of hardwood wood is shorter (less than 1mm), which can make paper have better surface touch and softness. By using softwood pulp and The combination of hardwood pulp can meet the requirements of different products.

可选地,取硫酸盐漂白针叶木10 -30份,例如15份、20份、25份等,取硫酸盐漂白阔叶木70 -90份,例如75份、80份、85份等,进行混合打浆。Optionally, take 10-30 parts of sulfate bleached coniferous wood, such as 15 parts, 20 parts, 25 parts, etc., and take 70-90 parts of sulfate bleached hardwood, such as 75 parts, 80 parts, 85 parts, etc., and mix beating.

一些实施例可以采用分段打浆的方式,请结合参阅图2,图2是本申请一些实施例提供的打浆流程示意图。Some embodiments may adopt a segmented beating method. Please refer to FIG. 2 . FIG. 2 is a schematic diagram of a beating process provided by some embodiments of the present application.

打浆流程包括:The beating process includes:

S21、第一段打浆。S21, the first stage of beating.

在第一段打浆过程中,可以将打浆浓度控制在8%-12%,例如9%、10%、11%等。打浆浓度是指打浆时纸浆在水中的浓度。本段打浆可以采用锥形磨浆机将上述混合纸浆打浆至20°SR-30°SR,例如21°SR、23°SR、25°SR、27°SR、29°SR等,以将纸浆中的纤维进行分丝帚化。In the first beating process, the beating concentration can be controlled at 8%-12%, such as 9%, 10%, 11% and so on. The beating consistency refers to the concentration of pulp in water during beating. In this section of beating, a conical refiner can be used to beat the above mixed pulp to 20°SR-30°SR, such as 21°SR, 23°SR, 25°SR, 27°SR, 29°SR, etc. The fibers are divided into filaments.

其中的“°SR”是打浆度的单位,打浆度亦称叩解度,是衡量纸浆质量的指标之一,可以表示在网上抄造纸张时,浆料滤水快慢的程度。Among them, "°SR" is the unit of beating degree, also known as beating degree, which is one of the indicators to measure the quality of pulp. It can indicate the degree of pulp drainage when making paper online.

S22、第二段打浆。S22, the second stage of beating.

第二段打浆在第一段打浆完成后进行。在第二段打浆过程中,可以将打浆浓度控制在3%-5%,例如3.5%、4%、4.5%等。第二段打浆过程中加入打浆助剂,打浆助剂的添加量为纸浆纤维的绝干质量的10%-20%,例如12%、14%、16%、18%等。打浆助剂可以是碱、表面活性剂、CMC、改性木素等,具体可以根据成纸要求选用任意一种或几种。例如可以采用苛性钠和磷酸钠作为打浆助剂提高纸张强度。The second stage of beating is carried out after the first stage of beating is completed. In the second beating process, the beating concentration can be controlled at 3%-5%, such as 3.5%, 4%, 4.5% and so on. In the second beating process, a beating aid is added, and the amount of the beating aid is 10%-20% of the absolute dry mass of the pulp fiber, such as 12%, 14%, 16%, 18%, etc. The beating aid can be alkali, surfactant, CMC, modified lignin, etc., and any one or several of them can be selected according to the requirements of paper making. For example, caustic soda and sodium phosphate can be used as beating aids to improve paper strength.

第二段打浆可以采用盘磨打浆机进行打浆,以保证打浆助剂能够与纸浆限位充分接触。第二段打浆的打浆度控制在38°SR-42°SR,例如39°SR、40°SR、41°SR等。In the second stage of beating, a disc refiner and beater can be used for beating, so as to ensure that the beating aid can fully contact the pulp limit. The beating degree of the second stage of beating is controlled at 38°SR-42°SR, such as 39°SR, 40°SR, 41°SR, etc.

打浆是对纸浆纤维进行加工的过程,通过机械作用使得纤维相互揉搓摩擦,将粗长的纤维切短、压溃及分丝帚化,达到一定的打浆度、湿重和水化程度以及强度等指标,有利于大大增加纤维的外比表面积,使得纤维的刚性下降,弹性削弱,塑性增加,纤维变得更为柔软而有可塑性,也能使得纤维分子链中暴露出更多的羟基,促进了纤维间氢键的形成,使得浆料更符合纸张的不同性能要求。纸张的打浆过程和强度对纸张的韧性、耐破性和撕裂性都起着非常重要的作用。Beating is the process of processing pulp fibers. Through mechanical action, the fibers are rubbed and rubbed against each other, and the thick and long fibers are cut short, crushed and divided into filaments to achieve a certain beating degree, wet weight, hydration degree and strength, etc. Index, which is beneficial to greatly increase the external specific surface area of the fiber, so that the rigidity of the fiber decreases, the elasticity is weakened, the plasticity is increased, the fiber becomes softer and more plastic, and it can also expose more hydroxyl groups in the fiber molecular chain, which promotes The formation of hydrogen bonds between fibers makes the pulp more suitable for different performance requirements of paper. The beating process and strength of paper play a very important role in the toughness, burst resistance and tear resistance of paper.

本申请实施例通过采用锥形磨浆机和盘磨打浆机进行两段打浆的方式,可以提高纸浆纤维的分丝帚化程度,有利于改善成纸质量。需要说明的是,在本申请其他实施例中,打浆也可以设计为单段或两段以上的方式,每段打浆可以根据需要采用具有对应特性的设备,并不限于此实施例。In the embodiment of the present application, by using a conical refiner and a disc refiner to perform two-stage beating, the degree of fibrous separation of pulp fibers can be improved, which is beneficial to improving the quality of paper. It should be noted that in other embodiments of the present application, the beating can also be designed in a single-stage or more than two-stage manner, and each stage of beating can use equipment with corresponding characteristics as required, and is not limited to this embodiment.

请继续参阅图1。在打浆之后进行配浆,配浆过程中可以往浆料内添加适量的助剂,以提升成纸强度。Please continue with Figure 1. The pulp is mixed after beating, and an appropriate amount of additives can be added to the pulp during the pulping process to improve the strength of the paper.

具体地,在完成第二段打浆后,可以往浆料中加入浆内淀粉和湿强剂。其中,浆内淀粉可以是阳离子氧化淀粉。浆内淀粉(绝干浆)可以按每吨纸6kg-15kg的量添加,例如7kg/t、9kg/t、11kg/t、13kg/t等。湿强剂能与纤维素、半纤维素形成交联、不溶水和共价键的网络结构,可使纸张在润湿状态仍能维持不低的强度,可以是甲醛树脂、聚酰胺环氧氯丙烷树脂、聚乙烯亚胺等。湿强剂(绝干浆)可以按每吨纸1kg-2kg的量添加,例如1.2kg/t、1.4kg/t、1.6kg/t、1.8kg/t等。Specifically, after the second stage of beating is completed, starch in the slurry and a wet strength agent can be added to the slurry. Wherein, the starch in pulp can be cationic oxidized starch. The starch in the pulp (absolutely dry pulp) can be added in an amount of 6kg-15kg per ton of paper, such as 7kg/t, 9kg/t, 11kg/t, 13kg/t, etc. The wet strength agent can form a cross-linked, water-insoluble and covalent bond network structure with cellulose and hemicellulose, so that the paper can still maintain a high strength in a wet state. It can be formaldehyde resin, polyamide epoxy chloride Propane resin, polyethyleneimine, etc. Wet strength agent (absolutely dry pulp) can be added in an amount of 1kg-2kg per ton of paper, such as 1.2kg/t, 1.4kg/t, 1.6kg/t, 1.8kg/t, etc.

浆内淀粉和湿强剂的添加量可以根据情况适当调整,以将浆料浓度稀释至1%-2%。在稀释后,再按每吨纸20kg-35kg的量添加烷基烯酮二聚体(AKD),例如23kg/t、26kg/t、29kg/t、32kg/t等,以进一步提升成纸强度。The addition amount of starch and wet strength agent in the slurry can be adjusted appropriately according to the situation, so as to dilute the slurry concentration to 1%-2%. After dilution, add alkyl ketene dimer (AKD) at an amount of 20kg-35kg per ton of paper, such as 23kg/t, 26kg/t, 29kg/t, 32kg/t, etc., to further increase the paper strength .

在完成打浆、配浆后,可将得到的浆料进行除气消泡,然后进行精筛,以得到可用于造纸的纸浆。除气消泡可以利用机械设备(如除气罐、脱气器)或在纸浆中添加化学品(如除气剂、消泡剂)或两者共用来实现,用于去除纸浆中的空气。精筛可以利用对应的纸浆筛选设备完成。After beating and pulping, the obtained slurry can be degassed and defoamed, and then finely screened to obtain pulp that can be used for papermaking. Degassing and defoaming can be achieved by using mechanical equipment (such as degassing tank, degasser) or adding chemicals (such as degassing agent, defoaming agent) to the pulp or both to remove the air in the pulp. Fine screening can be done with corresponding pulp screening equipment.

S12、纸张成型。S12. Paper molding.

在得到可用于造纸的纸浆,可利用造纸设备制得成型纸。具体地,将纸浆分别送至造纸机的多个纸网上,使纸浆脱水成型,得到多层成型纸。例如,将纸浆喷至圆网造纸机的多个圆网笼上挂浆,形成多层成型纸。After the pulp that can be used for papermaking is obtained, papermaking equipment can be used to make molding paper. Specifically, the pulp is sent to multiple paper wires of the paper machine respectively, and the pulp is dehydrated and shaped to obtain multi-layer molded paper. For example, the pulp is sprayed onto a plurality of cylinders of a cylinder paper machine to form a multi-layer forming paper.

其中,造纸机的纸网数量决定了最终制得的多层叠合纸的层数,本申请采用的造纸机的纸网数量为两个或两个以上,包括但不限于三个、五个、七个、十个等,成型纸的数量越多,叠合制得的多层叠合纸的层数就越多,克重就越重。Among them, the number of paper webs of the paper machine determines the number of layers of the final multi-layer laminated paper. The number of paper webs of the paper machine used in this application is two or more, including but not limited to three, five, Seven, ten, etc., the more the number of forming paper, the more layers of laminated paper made by lamination, and the heavier the weight.

S13、喷淋助剂。S13. Spray additives.

多层成型纸会在后续制备过程中叠合形成多层叠合纸,为保证多层叠合纸具有足够高的层间结合强度,以避免在加工时出现分层现象,本申请实施例在成型纸制得后,将喷淋剂喷淋在多层成型纸的待结合表面上,以提高多层成型纸叠合后的结合强度。需要说明的是,待结合表面指的是成型纸用于与其他成型纸结合形成多层叠合纸的表面。喷淋液可以平均地喷淋至各层成型纸的待结合表面上。The multi-layer forming paper will be laminated in the subsequent preparation process to form a multi-layer laminated paper. In order to ensure that the multi-layer laminated paper has a sufficiently high interlayer bonding strength to avoid delamination during processing, the embodiment of the present application is made in the forming paper After the preparation, the spraying agent is sprayed on the surface of the multi-layer molding paper to be bonded, so as to improve the bonding strength of the multi-layer molding paper after lamination. It should be noted that the surface to be bonded refers to the surface of the forming paper used to combine with other forming papers to form a multi-layer laminated paper. The spray liquid can be evenly sprayed onto the surface to be bonded of each layer of forming paper.

本申请实施例提供的喷淋剂包括淀粉液和胶乳。其中,淀粉液由原淀粉和水构成。淀粉液的制备过程包括:将原淀粉与水混合成浓度为1%-10%的淀粉溶液,例如3%、5%、7%等;然后在90℃-100℃下,例如91℃、93℃、95℃、97℃、99℃等,将该淀粉溶液糊化成淀粉液。The spray agent provided in the embodiment of the present application includes starch liquid and latex. Wherein, the starch solution is composed of raw starch and water. The preparation process of the starch liquid includes: mixing the original starch and water into a starch solution with a concentration of 1%-10%, such as 3%, 5%, 7% and so on; °C, 95 °C, 97 °C, 99 °C, etc., the starch solution is gelatinized into starch liquid.

其中,原淀粉是指不经过任何化学方法处理,也不改变淀粉内在的物理和化学特性而生产的各类淀粉;糊化是指淀粉受热后形成均匀糊状物的现象,糊化后,淀粉的粘度会急剧增大。Among them, raw starch refers to all kinds of starch produced without any chemical treatment and without changing the inherent physical and chemical properties of starch; gelatinization refers to the phenomenon that starch forms a uniform paste after being heated. After gelatinization, starch The viscosity will increase sharply.

申请人研究发现,将浓度为1%-10%的淀粉溶液在90℃-100℃下糊化形成的淀粉液喷淋至成型纸的待结合表面上,可以有效提高制得的多层叠合纸的层间结合强度。The applicant's research found that spraying the starch solution formed by gelatinization of a starch solution with a concentration of 1%-10% at 90°C-100°C onto the surface to be bonded of the forming paper can effectively improve the quality of the multi-layer laminated paper produced. interlayer bonding strength.

胶乳的选用要求是Tg值不大于2并且不小于-2,例如Tg值为-1、Tg值为0、Tg值为1等,Tg值指的是玻璃态转化温度,申请人研究发现,Tg值处于这一范围内的胶乳在制成喷淋剂喷淋至成型纸的待结合表面后,能够提高成纸在干燥后的柔韧度。The requirement for the selection of latex is that the Tg value is not greater than 2 and not less than -2, for example, the Tg value is -1, the Tg value is 0, the Tg value is 1, etc. The Tg value refers to the glass transition temperature. The applicant found that Tg The latex with a value within this range can improve the flexibility of the formed paper after drying after it is made into a spray agent and sprayed onto the surface of the formed paper to be bonded.

其中,胶乳可以采用不同类型的水性胶乳。胶乳的选用还可以结合参考其粘结性能。申请人进一步研究发现,Tg值处于上述范围内的丙烯酸类胶乳、丁腈类胶乳、羧基丁苯类胶乳和苯丙类胶乳可以满足要求。Among them, the latex can adopt different types of water-based latex. The selection of latex can also refer to its bonding performance. Further research by the applicant has found that acrylic latex, nitrile latex, carboxylated styrene-butadiene latex and styrene-acrylic latex with Tg values within the above range can meet the requirements.

其中,羧基丁苯胶乳是以丁二烯、苯乙烯加少量羧酸及其它助剂,通过乳液聚合生成的共聚物,是一种水分散体,具有较高的粘结力和结膜强度,机械及化学稳定性好,流动性、贮存稳定性均佳,填充量大等优点。残留苯类单体甚微,属环保型产品。Among them, carboxylated styrene-butadiene latex is a copolymer produced by emulsion polymerization with butadiene, styrene and a small amount of carboxylic acid and other additives. It is a water dispersion with high cohesive force and conjunctival strength. It has good chemical stability, good fluidity and storage stability, and large filling capacity. The residual benzene monomer is very small, and it is an environmentally friendly product.

丁腈胶乳由丁二烯和丙烯腈乳液共聚制得,由于共聚物分子链中含有腈基,因而具有良好的耐油性、耐溶剂及化学药品性,与纤维有良好的黏合力,与淀粉有良好的相容性。Nitrile latex is prepared by copolymerization of butadiene and acrylonitrile emulsion. Since the molecular chain of the copolymer contains nitrile groups, it has good oil resistance, solvent resistance and chemical resistance, and has good adhesion to fibers and has good adhesion to starch. Good compatibility.

苯丙类胶乳由苯乙烯和丙烯酸酯单体经乳液共聚而得,具有附着力好、胶膜透明、耐水、耐油、耐热、耐老化的特性,可以与淀粉配合作为胶黏剂使用。Styrene-acrylic latex is obtained by emulsion copolymerization of styrene and acrylate monomers. It has good adhesion, transparent film, water resistance, oil resistance, heat resistance, and aging resistance. It can be used as an adhesive in combination with starch.

丙烯酸胶乳包括纯丙烯酸树脂和丙烯酸乙酯-苯乙烯的共聚物,有利于提高喷淋层的硬度、拉伸强度、耐水性、附着力及耐擦洗性。Acrylic latex includes pure acrylic resin and ethyl acrylate-styrene copolymer, which is beneficial to improve the hardness, tensile strength, water resistance, adhesion and scrub resistance of the spray layer.

本申请实施例提供的喷淋剂中的胶乳可以为丙烯酸类胶乳、丁腈类胶乳、羧基丁苯类胶乳、苯丙类胶乳中的任意一种。The latex in the spray agent provided in the embodiment of the present application may be any one of acrylic latex, nitrile latex, carboxylated styrene-butadiene latex, and styrene-acrylic latex.

进一步地,申请人还发现,层间喷淋的喷淋剂在后续的压榨过程中,可能会随着纸卷脱水流入到纸机的白水系统,由于部分白水会在造纸过程中直接回用,转移到白水中的喷淋剂可能会影响整个白水系统的洁净度,而且在生产环境温度较高时还容易导致细菌滋生。因此,本申请实施例提供的喷淋剂可选地仅由上述的淀粉液和一种胶乳构成,即只喷淋一种淀粉液和一种胶乳,以尽可能地减少喷淋剂的成分数。Furthermore, the applicant also found that the spraying agent for interlayer spraying may flow into the white water system of the paper machine along with the dehydration of the paper roll during the subsequent pressing process. Since part of the white water will be directly reused in the papermaking process, The spray agent transferred to the white water may affect the cleanliness of the whole white water system, and it is easy to cause bacterial growth when the production environment temperature is high. Therefore, the spray agent provided by the embodiment of the present application may optionally only consist of the above-mentioned starch liquid and a kind of latex, that is, only spray a kind of starch liquid and a kind of latex, so as to reduce the number of components of the spray agent as much as possible .

可选地,淀粉液的喷淋量为每吨纸喷淋30kg-35kg,例如31kg/t、32kg/t、33kg/t、34kg/t等。胶乳的喷淋量为每吨纸喷淋3.0kg-3.5kg,例如3.1kg/t、3.2kg/t、3.3kg/t、3.4kg/t等。其中,胶乳的喷淋量可以为淀粉液的喷淋量的8%-12%,例如9%、10%、11%等。Optionally, the spraying amount of the starch solution is 30kg-35kg per ton of paper, such as 31kg/t, 32kg/t, 33kg/t, 34kg/t, etc. The spray amount of latex is 3.0kg-3.5kg per ton of paper, such as 3.1kg/t, 3.2kg/t, 3.3kg/t, 3.4kg/t, etc. Wherein, the spraying amount of the latex can be 8%-12% of the spraying amount of the starch liquid, such as 9%, 10%, 11% and so on.

需要说明的是,淀粉液和胶乳可以分别喷淋至成型纸上,也可以混合成溶液再喷淋至成型纸上。其中,由淀粉液和胶乳混合形成的喷淋液的配比依据上述的胶乳和淀粉液的喷淋量比决定,即胶乳与淀粉液的比值为8%-12%,制得的喷淋液的浓度可以为0.9%-1.2%,例如0.93%、0.97%、1.03%、1.08%、1.15%等。It should be noted that the starch solution and the latex can be sprayed onto the molding paper separately, or they can be mixed into a solution and then sprayed onto the molding paper. Wherein, the proportioning of the spray liquid formed by mixing the starch liquid and the latex is determined according to the spray amount ratio of the above-mentioned latex and the starch liquid, that is, the ratio of the latex to the starch liquid is 8%-12%, and the prepared spray liquid The concentration can be 0.9%-1.2%, such as 0.93%, 0.97%, 1.03%, 1.08%, 1.15% and so on.

S14、组合压榨。S14. Combination pressing.

在喷淋完成后,将喷淋后的多层成型纸叠合并进行多道组合压榨。具体可以将喷淋后的多层成型纸转移至烘缸表面,利用压辊与烘缸配合对叠合的多层成型纸进行压榨脱水,经过一次压榨后的叠合纸随烘缸转移至下一压辊进行下一次压榨脱水,如此重复多次,以将纸张的紧度压榨至不小于0.9g/m3After the spraying is completed, the sprayed multi-layer molded papers are stacked and pressed in multiple passes. Specifically, the sprayed multi-layer molding paper can be transferred to the surface of the drying cylinder, and the laminated multi-layer molding paper can be pressed and dehydrated by using the pressure roller and the drying cylinder. A press roll is used for the next press dehydration, and this is repeated many times to press the tightness of the paper to not less than 0.9g/m 3 .

其中,压榨的次数可以根据实际情况调整,例如可以压榨3次、4次、5次、6次、7次等,同理,压力也可以相应调整,具体的压榨压力可以控制在0.1MPa-1.0MPa范围内,例如0.2MPa、0.4MPa、0.6MPa等,只要在实现脱水的同时将纸张压榨至预设紧度即可。Among them, the number of pressing can be adjusted according to the actual situation, for example, it can be pressed 3 times, 4 times, 5 times, 6 times, 7 times, etc. Similarly, the pressure can also be adjusted accordingly, and the specific pressing pressure can be controlled at 0.1MPa-1.0 Within the range of MPa, such as 0.2MPa, 0.4MPa, 0.6MPa, etc., as long as the paper is pressed to the preset tightness while achieving dehydration.

可选地,在组合压榨步骤中,多道压榨的压力呈逐渐上升的趋势,例如在3道组合压榨中,第1道压榨至第3道压榨的压力依次为0.2MPa、0.4MPa、0.6MPa。Optionally, in the combined pressing step, the pressure of the multi-pass pressing is gradually increasing. For example, in the 3-pass combined pressing, the pressures from the first pressing to the third pressing are 0.2MPa, 0.4MPa, 0.6MPa in turn .

需要说明的是,上述的“呈逐渐上升的趋势”并非限定组合压榨中的多道压榨的压力必定逐渐增大,而是指组合压榨的压力整体呈上升趋势。例如,组合压榨数为5道,其中第1、2道压榨压力为0.2MPa,第3道压榨压力为0.4MPa,第4、5道压榨压力为0.6MPa。又如,组合压榨数为5道,其中第1、2道压榨压力为0.2MPa,第3、4道压榨压力为0.4MPa,第5道压榨压力为0.6MPa。组合压榨的具体压榨次数和压榨压力可以根据需要进行调整,在此不一一示出。It should be noted that the above-mentioned "gradually increasing trend" does not mean that the pressure of the multi-pass pressing in the combined pressing must gradually increase, but means that the pressure of the combined pressing is on the rise as a whole. For example, the number of combined pressing is 5, of which the pressing pressure of the 1st and 2nd lanes is 0.2MPa, the pressing pressure of the 3rd lane is 0.4MPa, and the pressing pressure of the 4th and 5th lanes is 0.6MPa. For another example, the number of combined pressing is 5, of which the pressing pressure of the 1st and 2nd lanes is 0.2MPa, the pressing pressure of the 3rd and 4th lanes is 0.4MPa, and the pressing pressure of the 5th lane is 0.6MPa. The specific pressing times and pressing pressure of combined pressing can be adjusted according to needs, which are not shown here one by one.

当然,多道压榨的压力也可以设置为依次增大,例如5道压榨的压力依次为0.2MPa、0.3MPa、0.4MPa、0.5MPa、0.6MPa。同理,组合压榨的具体压榨次数和压榨压力可以根据需要进行调整,在此不一一示出。Certainly, the pressure of multiple pressings can also be set to increase sequentially, for example, the pressures of 5 pressings are 0.2MPa, 0.3MPa, 0.4MPa, 0.5MPa, 0.6MPa in sequence. Similarly, the specific pressing times and pressing pressure of combined pressing can be adjusted according to needs, which are not shown here one by one.

S15、烘干。S15, drying.

将经过组合压榨后的纸张烘干,得到多层叠合纸。其中,多层叠合纸的每层成型纸的克重通过上述各步骤控制在85g/m2 -95g/m2的范围内,例如87g/m2、90g/m2、93g/m2,以保证制得的多层叠合纸纸带的整体厚度均一性。在烘干后可以对多层叠合纸进行压光等表面处理,然后卷取。Dry the combined pressed paper to obtain multi-layer laminated paper. Wherein, the grammage of each layer of forming paper of the multi-layer laminated paper is controlled within the range of 85g/m 2 -95g/m 2 through the above steps, such as 87g/m 2 , 90g/m 2 , 93g/m 2 , and The overall thickness uniformity of the prepared multi-layer laminated paper tape is guaranteed. After drying, the multi-layer laminated paper can be subjected to surface treatment such as calendering, and then rolled.

需要说明的是,上述的多层叠合纸的制备方法仅示出了部分关键性步骤。多层叠合纸的制备流程实际还可包括一些其他步骤。请参阅图3,图3是本申请一些实施例提供的多层叠合纸的制备方法的流程示意图。It should be noted that the above-mentioned method for preparing multi-layer laminated paper only shows some key steps. The production process of multi-layer laminated paper can actually include some other steps. Please refer to FIG. 3 . FIG. 3 is a schematic flowchart of a method for preparing multi-layer laminated paper provided in some embodiments of the present application.

多层叠合纸的制备流程包括:The preparation process of multi-layer laminated paper includes:

取硫酸盐漂白针叶木10 -30份,依次进行散浆A1、调配A2、除渣A3和打浆A4四个步骤的处理;其中的散浆A1步骤可通过散浆设备完成;浆料经过散浆A1后转移至成浆塔中,进行调配A2,成浆塔是造纸行业用于贮存和调配浆料的一种常压容器;然后进一步利用过滤设备进行除渣A3,后再进行打浆A4,打浆的具体流程可参阅上文。Take 10-30 parts of kraft bleached coniferous wood, and sequentially carry out the treatment of the four steps of loose pulp A1, deployment A2, slag removal A3 and beating A4; wherein the step of loose pulp A1 can be completed by the loose pulp equipment; After A1 is transferred to the pulping tower for blending A2, the pulping tower is a kind of normal-pressure container used for storing and blending pulp in the paper industry; then further use filtering equipment to remove slag A3, and then beat A4 to make pulp The specific process can be found above.

取硫酸盐漂白阔叶木70 -90份,依次进行散浆B1、调配B2、除渣B3和打浆B4四个步骤的处理。两种纸浆的上述处理步骤基本相同,且两种纸浆的处理可同步进行。Take 70-90 parts of sulfate-bleached broad-leaved wood, and sequentially carry out four steps of pulping B1, blending B2, slag removal B3 and beating B4. The above-mentioned processing steps of the two pulps are basically the same, and the processing of the two pulps can be carried out synchronously.

两种纸浆处理完成后进行配浆,具体包括成浆C1和添加试剂C2,即两种浆料一并汇入成浆池中混合,并网成浆池中添加相应的试剂,具体试剂请参阅上文关于配浆的说明,在此不作赘述。试剂添加完成后再进行贮浆C3,即将浆料转移至贮浆池中,使得上述两种纸浆和添加的试剂在贮浆池中混合均匀。然后再进行抄前准备C4,即将混合均匀的浆料转移至面/底层抄前池,准备抄造纸张,此时抄前池中的浆料已经处于稳定状态,浆料内的空气已经被排出,并且纤维配比、浓度等标准已达到抄造要求。After the two kinds of pulp are processed, the pulp is blended, specifically including pulping C1 and adding reagent C2, that is, the two pulps are mixed together in the pulping tank and mixed, and the corresponding reagents are added in the grid-connected pulping tank. For specific reagents, please refer to The above description about the slurry preparation will not be repeated here. Pulp storage C3 is carried out after the addition of reagents is completed, that is, the slurry is transferred to the pulp storage tank, so that the above two pulps and the added reagents are mixed evenly in the pulp storage tank. Then carry out pre-copying preparation C4, that is, transfer the uniformly mixed slurry to the surface/bottom forecourt, and prepare for papermaking. At this time, the slurry in the forecourt has been in a stable state, and the air in the slurry has been discharged. And the fiber ratio, concentration and other standards have met the requirements of copying.

进一步进行抄送C5,即利用冲浆泵将达到抄造要求的浆料抽送至纸机,并进行网前筛C6,即利用筛选器件进行精筛,精筛后的浆料进入纸机流浆箱,然后上网脱水成型,得到成型纸。Further carry out copying C5, that is, use the pulp pump to pump the pulp that meets the papermaking requirements to the paper machine, and perform screen C6, that is, use the screening device to perform fine screening, and the finely screened pulp enters the headbox of the paper machine , and then dehydrated and formed on the Internet to obtain a formed paper.

进一步再对成型纸进行喷淋助剂C7,即将喷淋剂喷淋在成型纸的待结合表面上,然后再进行多层叠合C8,将喷淋完毕后的多层成型纸叠合起来,叠合的多层成型纸经过压榨C9步骤,压榨至预设紧度,后再依次经过干燥C10、复卷C11,得到多层叠合纸。Further spray the molded paper with auxiliary agent C7, that is, spray the spray agent on the surface of the molded paper to be bonded, and then perform multi-layer lamination C8, stack the multi-layered molded paper after spraying, and stack The laminated multi-layer forming paper is pressed to a predetermined tightness through pressing C9 step, and then sequentially passed through drying C10 and rewinding C11 to obtain a multi-layer laminated paper.

以下为通过本申请提供的多层叠合纸的制备方法制得的部分多层叠合纸示例。The following are some examples of multi-layer laminated paper prepared by the method for preparing multi-layer laminated paper provided in this application.

对比例:进行打浆、配浆后,在纸间喷淋淀粉液。根据喷淋淀粉液的吨纸用量平均喷淋相应的量在各层间,然后再经过叠合、压榨、干燥后成纸。具体请参阅上文,在此不作赘述,下述实施例同理。Comparative example: After beating and pulping, spray starch liquid between the papers. According to the amount of sprayed starch liquid per ton of paper, the corresponding amount is sprayed on average between each layer, and then laminated, pressed, and dried to form paper. For details, please refer to the above, which will not be repeated here, and the following embodiments are the same.

实施例1:进行打浆、配浆后,在纸间喷淋淀粉液和丙烯酸类胶乳,然后再经过叠合、压榨、干燥后成纸。Embodiment 1: After beating and pulping, spray starch liquid and acrylic latex between the papers, and then laminate, press, and dry to form paper.

实施例2:进行打浆、配浆后,在纸间喷淋淀粉液和丁腈类胶乳,然后再经过叠合、压榨、干燥后成纸。Embodiment 2: After beating and pulping, spray starch liquid and nitrile latex between the papers, and then form paper after lamination, pressing and drying.

实施例3:进行打浆、配浆后,在纸间喷淋淀粉液和羧基丁苯类胶乳,然后再经过叠合、压榨、干燥后成纸。Example 3: After beating and pulping, spray starch liquid and carboxylated styrene-butadiene latex between the papers, and then laminate, press, and dry to form paper.

实施例4:进行打浆、配浆后,在纸间喷淋淀粉液和苯丙类胶乳,然后再经过叠合、压榨、干燥后成纸。Embodiment 4: After beating and pulping, spray starch liquid and styrene-acrylic latex between the papers, and then laminate, press, and dry to form paper.

其中,实施例1-4的淀粉液用量等同于对比例。对比例及实施例1-4均制作出3层和10层多层叠合纸,并分别裁切成相应的规格,以便进行测试。可以理解的是,3层和10层仅是便于进行测试选择的层数,并不能作为对多层叠合纸层数的限定。Wherein, the starch liquid consumption of embodiment 1-4 is equal to comparative example. Both Comparative Example and Examples 1-4 produced 3-layer and 10-layer multi-layer laminated paper, and cut them into corresponding specifications for testing. It can be understood that 3 layers and 10 layers are only the number of layers that are convenient for testing and selection, and cannot be used as a limit to the number of layers of laminated paper.

本申请实施例采用的第一种测试方法是利用纸张内聚力检测仪检测多层叠合纸的内聚力。由于纸张内聚力检测仪的量程有限,第一种测试方法用于测试3层的多层叠合纸。对于10层的多层叠合纸,本申请采用第二种测试方法进行测试,具体为:取一定长度的纸带,在直径2-3cm的圆辊上沿正反方向各缠绕5圈以上,根据纸带的分层现象评估其层间结合强度。The first test method adopted in the embodiment of the present application is to use a paper cohesion tester to detect the cohesion of multi-layer laminated paper. Due to the limited range of the paper cohesion tester, the first test method is used to test 3-layer multi-layer laminated paper. For 10-layer multi-layer laminated paper, this application adopts the second test method for testing, specifically: take a certain length of paper tape, and wind it on a round roller with a diameter of 2-3cm for more than 5 turns in the forward and reverse directions, according to The delamination phenomenon of the paper tape evaluates its interlayer bonding strength.

其中,测试用纸是将复卷后的多层叠合纸裁切成25mm宽(3层纸样)和8mm宽(10层纸样)的纸带,在恒温恒湿室放置24h后通过上述测试方法进行测试。测试结果如下:Among them, the test paper is to cut the multi-layer laminated paper after rewinding into paper strips with a width of 25mm (3-layer paper sample) and 8mm wide (10-layer paper sample), and place it in a constant temperature and humidity room for 24 hours. test. The test results are as follows:

上述内聚力是利用纸张内聚力检测仪测试3层纸样后测得的,来回折叠效果是利用上述第二种测试方法测试10层纸样后测得的。可以看出,通过在纸层间喷淋淀粉液和胶乳,可以大幅提升多层叠合纸的层间结合强度,并且能够提高多层叠合纸的纸张柔韧度。The above cohesion is measured after testing 3-layer paper samples with a paper cohesion tester, and the back and forth folding effect is measured after using the second test method above to test 10-layer paper samples. It can be seen that by spraying starch liquid and latex between the paper layers, the interlayer bond strength of the multilayer laminated paper can be greatly improved, and the paper flexibility of the multilayer laminated paper can be improved.

本申请进一步提供一种多层叠合纸,该多层叠合纸通过上述的多层叠合纸的制备方法制得。The present application further provides a multi-layer laminated paper, which is prepared by the above-mentioned preparation method of the multi-layer laminated paper.

请参阅图4,图4是本申请一些实施例提供的多层叠合纸的结构示意图。Please refer to FIG. 4 . FIG. 4 is a schematic structural diagram of a multi-layer laminated paper provided by some embodiments of the present application.

本申请实施例提供的多层叠合纸10具有多层纸层100,多层纸层在叠合前喷淋有上述的喷淋液,并且叠合后经过多道压榨使得多层叠合纸10的紧度不小于0.9g/m3。其中,每层纸层100的克重不小于85g/m2并且不大于95g/m2,以使得多层叠合纸10具有良好的整体厚度均一性。The multi-layer laminated paper 10 provided by the embodiment of the present application has a multi-layer paper layer 100, and the multi-layer paper layer is sprayed with the above-mentioned spray liquid before lamination, and after lamination, it is pressed through multiple passes to make the multi-layer laminated paper 10 The tightness is not less than 0.9g/m 3 . Wherein, the grammage of each paper layer 100 is not less than 85 g/m 2 and not more than 95 g/m 2 , so that the multi-layer laminated paper 10 has good overall thickness uniformity.

应当理解,在此本申请说明书和所附权利要求书中所使用的术语仅仅是出于描述特定实施例的目的而并不意在限制本申请。例如,除非上下文清楚地指明其它情况,否则单数形式的“一”、“一个”、“一层”及“该”意在包括复数形式。又如本申请的描述中“多层”的含义是两层或两层以上,除非另有明确具体的限定。It should be understood that the terminology used in the specification and appended claims herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the application. For example, the singular forms "a", "an", "a layer" and "the" are intended to include the plural forms unless the context clearly dictates otherwise. As another example, in the description of the present application, "multi-layer" means two or more layers, unless otherwise specifically defined.

需要说明的是,通过上述多层叠合纸的制备方法还可以制得其他结构的多层叠合纸,其亦在本申请的专利保护范围内,为避免赘述,在此不一一列出。It should be noted that multilayer laminated papers of other structures can also be produced through the above-mentioned preparation method of multilayer laminated paper, which are also within the scope of patent protection of the present application, and will not be listed here to avoid repeating them.

在本申请的描述中,参考术语“一个实施例”、“一些实施例”、“示例”、“具体示例”、或“一些示例”等的描述意指结合该实施例或示例描述的具体特征、结构、材料或者特点包含于本申请的至少一个实施例或示例中。在本说明书中,对上述术语的示意性表述不必须针对的是相同的实施例或示例。而且,描述的具体特征、结构、材料或者特点可以在任一个或多个实施例或示例中以合适的方式结合。此外,在不相互矛盾的情况下,本领域的技术人员可以将本说明书中描述的不同实施例或示例以及不同实施例或示例的特征进行结合和组合。In the description of this application, reference to the terms "one embodiment," "some embodiments," "example," "specific examples," or "some examples" means that specific features described in connection with that embodiment or example , structure, material or characteristic is included in at least one embodiment or example of the present application. In this specification, the schematic representations of the above terms are not necessarily directed to the same embodiment or example. Furthermore, the described specific features, structures, materials or characteristics may be combined in any suitable manner in any one or more embodiments or examples. In addition, those skilled in the art can combine and combine different embodiments or examples and features of different embodiments or examples described in this specification without conflicting with each other.

综上所述,本申请通过在多层成型纸的待结合表面上喷淋淀粉液和胶乳,然后将喷淋后的多层成型纸叠合并进行多道组合压榨,再将经过组合压榨后的纸张烘干得到多层叠合纸,能够提高多层叠合纸的层间结合强度和柔韧度。In summary, this application sprays starch liquid and latex on the surface of the multi-layer forming paper to be combined, then stacks the sprayed multi-layer forming paper and performs multi-channel combined pressing, and then combines the pressed The paper is dried to obtain a multi-layer laminated paper, which can improve the interlayer bonding strength and flexibility of the multi-layer laminated paper.

以上所述仅为本申请的实施方式,并非因此限制本申请的专利范围,凡是利用本申请说明书及附图内容所作的等效结构或等效流程变换,或直接或间接运用在其他相关的技术领域,均同理包括在本申请的专利保护范围内。The above is only the implementation of the application, and does not limit the patent scope of the application. Any equivalent structure or equivalent process conversion made by using the specification and drawings of the application, or directly or indirectly used in other related technologies fields, are all included in the scope of patent protection of this application in the same way.

Claims (12)

1.一种多层叠合纸的制备方法,其特征在于,包括:1. A preparation method for multilayer laminated paper, characterized in that, comprising: 进行打浆、配浆,得到抄纸所需纸浆;Perform beating and pulping to obtain the pulp required for papermaking; 将所述纸浆分别送至造纸机的多个纸网上,使所述纸浆脱水成型,得到多层成型纸;Sending the pulp to a plurality of paper nets of a paper machine, dehydrating and forming the pulp to obtain a multi-layer formed paper; 将喷淋剂喷淋在多层所述成型纸的待结合表面上,所述喷淋剂包括淀粉液和胶乳,所述胶乳的Tg值不大于2并且不小于-2;Spraying a spraying agent on the surface to be bonded of multiple layers of the forming paper, the spraying agent includes starch liquid and latex, and the Tg value of the latex is not greater than 2 and not less than -2; 将喷淋后的多层所述成型纸叠合并进行多道组合压榨;Stacking the multi-layer molding paper after spraying and performing multi-channel combined pressing; 将经过组合压榨后的纸张烘干,得到所述多层叠合纸。drying the combined pressed paper to obtain the multi-layer laminated paper. 2.根据权利要求1所述的多层叠合纸的制备方法,其特征在于,所述胶乳为丙烯酸类胶乳、丁腈类胶乳、羧基丁苯类胶乳、苯丙类胶乳中的任意一种。2. The preparation method of multilayer laminated paper according to claim 1, wherein the latex is any one of acrylic latex, nitrile latex, carboxylated styrene-butadiene latex, and styrene-acrylic latex. 3.根据权利要求2所述的多层叠合纸的制备方法,其特征在于,所述胶乳的喷淋量为每吨纸喷淋3.0kg-3.5kg。3. The method for preparing multi-layer laminated paper according to claim 2, characterized in that the spraying amount of the latex is 3.0kg-3.5kg per ton of paper. 4.根据权利要求1所述的多层叠合纸的制备方法,其特征在于,所述淀粉液的制备过程包括:4. the preparation method of multi-layer laminated paper according to claim 1, is characterized in that, the preparation process of described starch liquid comprises: 将原淀粉与水混合成浓度为1%-10%的淀粉溶液;mixing raw starch with water to form a starch solution with a concentration of 1%-10%; 在90℃-100℃下将所述淀粉溶液糊化成所述淀粉液。The starch solution is gelatinized into the starch liquid at 90°C-100°C. 5.根据权利要求4所述的多层叠合纸的制备方法,其特征在于,所述淀粉液的喷淋量为每吨纸喷淋30kg-35kg。5. The method for preparing multi-layer laminated paper according to claim 4, characterized in that the amount of starch liquid sprayed is 30kg-35kg per ton of paper. 6.根据权利要求1所述的多层叠合纸的制备方法,其特征在于,在所述进行多道组合压榨的步骤中,将纸张的紧度压榨至不小于0.9g/m36 . The method for preparing multi-layer laminated paper according to claim 1 , characterized in that, in the step of performing multi-pass combined pressing, the tightness of the paper is pressed to not less than 0.9 g/m 3 . 7.根据权利要求6所述的多层叠合纸的制备方法,其特征在于,在所述进行多道组合压榨的步骤中,多道压榨的压力呈逐渐上升的趋势。7. The method for preparing multi-layer laminated paper according to claim 6, characterized in that, in the step of performing multi-pass combined pressing, the pressure of multi-pass pressed tends to increase gradually. 8.根据权利要求1所述的多层叠合纸的制备方法,其特征在于,每层所述成型纸的克重控制在85g/m2-95g/m2的范围内。8. The method for preparing multi-layer laminated paper according to claim 1, characterized in that the grammage of each layer of the molded paper is controlled within the range of 85g/m 2 -95g/m 2 . 9.根据权利要求1所述的多层叠合纸的制备方法,其特征在于,所述进行打浆、配浆的步骤包括:9. The preparation method of multi-layer laminated paper according to claim 1, characterized in that, the step of beating and pulping comprises: 采用锥形磨浆机进行第一段打浆,以将浆料中的纤维分丝帚化;Use a conical refiner for the first stage of beating to separate the fibers in the pulp into filaments; 采用单盘磨打浆机进行第二段打浆,并在所述第二段打浆过程中加入打浆助剂,使得打浆助剂能够与所述纤维充分接触。A single disc mill beater is used for the second stage of beating, and a beating aid is added during the second stage of beating, so that the beating aid can fully contact the fibers. 10.根据权利要求9所述的多层叠合纸的制备方法,其特征在于,所述第一段打浆的打浆浓度为8%-12%,打浆度为20°SR-30°SR;所述第二段打浆的打浆浓度为3%-5%,打浆度为38°SR-42°SR,所述打浆助剂的添加量为所述纤维的绝干质量的10%-20%。10. The preparation method of multilayer laminated paper according to claim 9, characterized in that, the beating concentration of the first section of beating is 8%-12%, and the degree of beating is 20°SR-30°SR; The beating concentration of the second stage of beating is 3%-5%, the degree of beating is 38°SR-42°SR, and the addition amount of the beating aid is 10%-20% of the absolute dry mass of the fiber. 11.根据权利要求9所述的多层叠合纸的制备方法,其特征在于,所述进行打浆、配浆的步骤还包括:在完成所述第二段打浆后,加入浆内淀粉和湿强剂,所述浆内淀粉按每吨纸6kg-15kg的量添加,所述湿强剂按每吨纸1kg-2kg的量添加,以将浆料浓度稀释至1%-2%;再按每吨纸20kg-35kg的量添加烷基烯酮二聚体。11. The preparation method of multi-layer laminated paper according to claim 9, characterized in that, the step of beating and pulping further comprises: after completing the second stage of beating, adding starch in pulp and wet strength The starch in the slurry is added in an amount of 6kg-15kg per ton of paper, and the wet strength agent is added in an amount of 1kg-2kg per ton of paper to dilute the slurry concentration to 1%-2%; Alkene ketene dimer is added in the amount of 20kg-35kg per ton of paper. 12.一种多层叠合纸,其特征在于,所述多层叠合纸通过权利要求1-11任一项所述的多层叠合纸的制备方法制得。12. A multi-layer laminated paper, characterized in that the multi-layer laminated paper is produced by the method for preparing multi-layer laminated paper according to any one of claims 1-11.
CN202310511328.9A 2023-05-08 2023-05-08 Preparation method of multilayer laminated paper and multilayer laminated paper Pending CN116536964A (en)

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CN1316030A (en) * 1998-09-03 2001-10-03 斯托拉·科帕伯格斯·伯格斯拉格斯公司 Paper or paperboard laminate and method to produce such laminate
US20060065379A1 (en) * 2004-09-29 2006-03-30 Babcock Bruce W White top paperboard
CN102912689A (en) * 2012-10-18 2013-02-06 山东晨鸣纸业集团股份有限公司 White-surface coated craft paper and production method thereof
CN102995501A (en) * 2012-11-02 2013-03-27 吉安集团股份有限公司 Curtain type coating craft paper and preparation method thereof
CN106245412A (en) * 2016-08-30 2016-12-21 广东华凯科技股份有限公司 A kind of manufacture method of multilayer handsheet
CN106948208A (en) * 2017-03-09 2017-07-14 华南理工大学 A kind of environmentally friendly light basis weight coated duplex board with grey back and preparation method thereof
CN112609488A (en) * 2020-12-25 2021-04-06 镇江大东纸业有限公司 Method for producing multilayer paper with high interlayer bonding strength
CN114687250A (en) * 2022-02-11 2022-07-01 广西金桂浆纸业有限公司 Paper and processing method thereof

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1316030A (en) * 1998-09-03 2001-10-03 斯托拉·科帕伯格斯·伯格斯拉格斯公司 Paper or paperboard laminate and method to produce such laminate
US20060065379A1 (en) * 2004-09-29 2006-03-30 Babcock Bruce W White top paperboard
CN102912689A (en) * 2012-10-18 2013-02-06 山东晨鸣纸业集团股份有限公司 White-surface coated craft paper and production method thereof
CN102995501A (en) * 2012-11-02 2013-03-27 吉安集团股份有限公司 Curtain type coating craft paper and preparation method thereof
CN106245412A (en) * 2016-08-30 2016-12-21 广东华凯科技股份有限公司 A kind of manufacture method of multilayer handsheet
CN106948208A (en) * 2017-03-09 2017-07-14 华南理工大学 A kind of environmentally friendly light basis weight coated duplex board with grey back and preparation method thereof
CN112609488A (en) * 2020-12-25 2021-04-06 镇江大东纸业有限公司 Method for producing multilayer paper with high interlayer bonding strength
CN114687250A (en) * 2022-02-11 2022-07-01 广西金桂浆纸业有限公司 Paper and processing method thereof

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