CN117107548B - Preparation method and application of composite deacidification material with high alkali reserve and hydrophobicity after deacidification treatment of paper - Google Patents

Preparation method and application of composite deacidification material with high alkali reserve and hydrophobicity after deacidification treatment of paper Download PDF

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CN117107548B
CN117107548B CN202310963515.0A CN202310963515A CN117107548B CN 117107548 B CN117107548 B CN 117107548B CN 202310963515 A CN202310963515 A CN 202310963515A CN 117107548 B CN117107548 B CN 117107548B
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deacidification
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composite
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hydrophobicity
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CN117107548A (en
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范以宁
张奉孝
陆海孟
孟磊
李文哲
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Nanjing Weita Cultural Heritage Protection Technology Co ltd
Nanjing University
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Nanjing University
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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
    • D21H25/00After-treatment of paper not provided for in groups D21H17/00 - D21H23/00
    • D21H25/18After-treatment of paper not provided for in groups D21H17/00 - D21H23/00 of old paper as in books, documents, e.g. restoring
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F292/00Macromolecular compounds obtained by polymerising monomers on to inorganic materials
    • 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
    • D21H25/00After-treatment of paper not provided for in groups D21H17/00 - D21H23/00
    • D21H25/02Chemical or biochemical treatment
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/64Paper recycling

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Abstract

The invention discloses a preparation method and application of a composite deacidification material with high alkali reserves and hydrophobicity after deacidification treatment of paper, and belongs to the technical field of deacidification treatment of precious paper cultural relics and the like. The composite deacidification material is prepared from nano alkaline compound magnesium hydroxide Mg (OH) 2 Or calcium hydroxide Ca (OH) 2 The surface coating fluoroalkyl methacrylate polymer (PPFOEMA). The PPFOEMA polymer is coated to enable the composite deacidification material to be suspended and dispersed in fluorocarbon medium in high stability for high-efficiency deacidification treatment of paper; the composite deacidification material is easy to uniformly infiltrate into the fiber gaps of the paper, and the PPFOEMA polymer coated on the surfaces of the nano particles can delay the release of alkaline compounds, so that the deacidified paper is still slightly alkaline under the condition of high alkali reserves, has excellent hydrophobicity and certain reinforcement effect, and is convenient for long-term storage.

Description

一种使纸张脱酸处理后具有高碱储量和疏水性的复合脱酸材 料的制法和应用A composite deacidification material that has high alkali storage and hydrophobicity after deacidification of paper Material preparation methods and applications

技术领域Technical field

本发明涉及一种使纸张经脱酸处理后具有高碱储量和疏水性的复合脱酸材料的制法和应用,该复合脱酸材料应用于珍贵纸质文物、档案和图书等的脱酸处理。The invention relates to a method and application of a composite deacidification material that enables paper to have high alkali reserves and hydrophobicity after deacidification treatment. The composite deacidification material is used in the deacidification treatment of precious paper cultural relics, archives, books, etc. .

背景技术Background technique

纸张是记录信息最常见的基材,承担着人类文明与发展传承的重要任务,是人类历史发展中不可或缺的重要组成部分。然而,目前全世界有数以亿计的纸张材料正在经受严重的老化和退化(Trends in Microbiology,2010,18:538-542),其主要原因是存在于纸张中的酸性物质。纸张中的酸性物质一般来源于造纸过程中的酸性施胶剂、储存环境中酸性气体如硫氧化物和氮氧化物以及细菌代谢产生的有机酸,这些酸性物质会加速纸张纤维素的水解,导致纤维素聚合度下降、纸张变黄和脆化,严重危及纸质文物的寿命。因此,对脆弱纸质文献资料进行脱酸和加固处理已刻不容缓。Paper is the most common base material for recording information. It bears the important task of inheriting human civilization and development, and is an indispensable and important part of the development of human history. However, hundreds of millions of paper materials around the world are currently undergoing severe aging and degradation (Trends in Microbiology, 2010, 18:538-542). The main reason is the acidic substances present in paper. Acidic substances in paper generally come from acidic sizing agents in the papermaking process, acidic gases such as sulfur oxides and nitrogen oxides in the storage environment, and organic acids produced by bacterial metabolism. These acidic substances will accelerate the hydrolysis of paper cellulose, leading to The polymerization degree of cellulose decreases, and the paper turns yellow and brittle, seriously endangering the life of paper cultural relics. Therefore, it is urgent to deacidify and strengthen fragile paper documents.

纸张脱酸工艺按碱性脱酸材料所处介质的不同分为水相脱酸、有机相脱酸和气相脱酸。其中,水相脱酸工艺因其具有安全、高效、操作简便等优点而得以大规模应用,如德国韦驮法(Journal of Colloid and Interface Science,2022,607:992-1004)和奥地利Vienna法(Chimia International Journal for Chemistry,2001,55:981-989)等。然而,水相脱酸后的纸张会起皱;而有机相脱酸所用甲醇、异丙醇等有机介质不仅易燃易爆,而且对人体及环境不友好。为了克服以上缺点,近年来利用惰性有机介质来悬浮分散碱性脱酸材料已逐渐成为大规模纸张脱酸的主流工艺。这其中最具代表性的是采用全氟庚烷介质的Bookkeeper法(Microporous and Mesoporous Materials,2020,293:109786)。全氟庚烷等全氟类烷烃具有不易燃、不易爆、化学稳定性好、易挥发无残留、渗透性好等优点(Journalof Photochemistry and Photobiology A:Chemistry,2010,214:86-91)。但是,全氟烷烃类介质表面张力低、憎水又憎油,使得碱性脱酸材料很难均匀且稳定地悬浮分散在其中(CN20161025757.2),这会造成纸张脱酸不均匀、脱酸效果差、脱酸材料利用率低等一系列问题。我们前已公开的发明较好地解决了碱性脱酸材料在氟碳介质中高稳定悬浮分散的问题(CN114753186A,一种在氟碳介质中高稳定悬浮分散的纸张脱酸复合材料及其制备方法和应用;CN108589411A,一种凹凸棒土复合材料及其应用)。The paper deacidification process is divided into aqueous phase deacidification, organic phase deacidification and gas phase deacidification according to the medium in which the alkaline deacidification material is located. Among them, the aqueous phase deacidification process has been applied on a large scale because of its advantages of safety, efficiency, and easy operation, such as the German Vienna method (Journal of Colloid and Interface Science, 2022, 607:992-1004) and the Austrian Vienna method ( Chimia International Journal for Chemistry,2001,55:981-989) etc. However, the paper after aqueous phase deacidification will wrinkle; and the organic media such as methanol and isopropyl alcohol used in organic phase deacidification are not only flammable and explosive, but also unfriendly to the human body and the environment. In order to overcome the above shortcomings, the use of inert organic media to suspend and disperse alkaline deacidification materials has gradually become the mainstream process for large-scale paper deacidification in recent years. The most representative one is the Bookkeeper method using perfluoroheptane medium (Microporous and Mesoporous Materials, 2020, 293:109786). Perfluoroheptane and other perfluorinated alkanes have the advantages of being non-flammable, non-explosive, good chemical stability, easy to volatilize without residue, and good permeability (Journal of Photochemistry and Photobiology A: Chemistry, 2010, 214:86-91). However, perfluoroalkane media have low surface tension, are hydrophobic and oleophobic, making it difficult for alkaline deacidification materials to be uniformly and stably suspended and dispersed in it (CN20161025757.2), which will cause uneven deacidification of paper and There are a series of problems such as poor effect and low utilization rate of deacidification materials. Our previously disclosed invention has better solved the problem of highly stable suspension and dispersion of alkaline deacidification materials in fluorocarbon media (CN114753186A, a paper deacidification composite material with high stability suspension and dispersion in fluorocarbon media and its preparation method and Application; CN108589411A, an attapulgite composite material and its application).

现有的纸张脱酸技术均是基于酸-碱中和原理发展而来的,即采用碱性物质来中和纸张中的酸性物质,以抑制纸张纤维素的酸催化水解,从而延长其寿命。众所周知,经脱酸处理后的纸张要想长时间不返酸就必须要储存一定量的碱性物质,碱储量的定义和定量测定方法可以按国标GB/T 24998-2010方法。储藏的这部分碱性物质被用于中和脱酸后纸张后续保存过程中因自然老化而产生的酸性物质,可降低纸张老化速度,延长纸张保存年限。但是,经脱酸处理后纸张过高的碱储量往往会使纸张具有过高的pH,值,而过高的pH值也会对纸张寿命造成不利影响(Carbohydrate Polymers,2019,209:250-257)。因此,如何使脱酸处理后的纸张具有高碱储量和合适的pH值,即如何使储藏在纸张中的碱性物质有一定的缓释性,是我们需要解决的一个重要问题。Existing paper deacidification technologies are developed based on the acid-alkali neutralization principle, that is, alkaline substances are used to neutralize acidic substances in paper to inhibit acid-catalyzed hydrolysis of paper cellulose, thereby extending its life. As we all know, if paper after deacidification treatment does not return to acid for a long time, it must store a certain amount of alkaline substances. The definition and quantitative determination method of alkali reserves can be based on the national standard GB/T 24998-2010 method. This part of the stored alkaline substances is used to neutralize the acidic substances produced due to natural aging of the paper during subsequent storage after deacidification, which can reduce the aging speed of the paper and extend the storage life of the paper. However, the excessively high alkali reserve of paper after deacidification treatment will often cause the paper to have an excessively high pH value, and an excessively high pH value will also adversely affect the life of the paper (Carbohydrate Polymers, 2019, 209:250-257 ). Therefore, how to make the deacidified paper have a high alkali reserve and a suitable pH value, that is, how to make the alkaline substances stored in the paper have a certain degree of sustained release, is an important issue we need to solve.

纸张最主要成份纤维素是一种天然的吸湿材料,一般表现为亲水性;同时纤维素之间交联形成的三维网状的丰富微孔结构具有毛细凝聚作用,从而表现出较强的吸水性和润湿性。吸水后的纸张不但强度大幅度下降,而且更易与空气中的酸性物质相结合,从而加速纸张的老化。与之相比,疏水性的纸张就不容易吸水,同时具有良好的自清洁和抗腐蚀等特性。特别地,疏水性纸张还可以有效地防止批量脱酸过程中纸张彼此之间的黏附(International Journal of Biological Macromolecules,2022,207:232-241;Cellulose,2022,29:8863-8877),从而有利于对纸张进行大规模和有效的脱酸处理。因此,如何使得脱酸后的纸张具有一定的疏水性是我们需要解决的另一个重要问题。Cellulose, the main component of paper, is a natural hygroscopic material and is generally hydrophilic. At the same time, the three-dimensional network-like rich microporous structure formed by cross-linking between cellulose has capillary cohesion, thus showing strong water absorption. properties and wettability. Not only does the strength of paper after absorbing water drop significantly, it is also more likely to combine with acidic substances in the air, thereby accelerating the aging of the paper. In contrast, hydrophobic paper does not absorb water easily and has good self-cleaning and anti-corrosion properties. In particular, hydrophobic paper can also effectively prevent papers from adhering to each other during batch deacidification (International Journal of Biological Macromolecules, 2022, 207: 232-241; Cellulose, 2022, 29: 8863-8877), thus having It is conducive to large-scale and effective deacidification treatment of paper. Therefore, how to make the deacidified paper have a certain degree of hydrophobicity is another important issue we need to solve.

发明内容Contents of the invention

本发明的目的不仅仅是提供一种在氟碳介质中高稳定悬浮分散的复合脱酸材料的制备方法,而且是提供一种脱酸处理后的纸张兼具高碱储量和疏水性特点的复合脱酸材料的制备方法,以进一步创新地发展现有的技术。本发明提出的技术方案是使无机纳米碱性脱酸材料预先吸附能够发生聚合反应的氟代烷基甲基丙烯酸酯(PFOEMA)单体,再经原位聚合形成复合脱酸材料。经该复合脱酸材料脱酸处理后的纸张在高碱储量下仍呈弱碱性,同时具有一定的疏水性。该复合脱酸材料是以碱性化合物氢氧化镁Mg(OH)2或氢氧化钙Ca(OH)2为核、氟代烷基甲基丙烯酸酯聚合物(PPFOEMA)为壳的“核-壳”结构,不仅在氟碳介质中具有高稳定的悬浮分散性,而且该复合材料易均匀地渗入纸张纤维缝隙中。包覆在碱性化合物Mg(OH)或Ca(OH)2纳米颗粒表面的PPFOEMA聚合物外壳能延缓内核中碱性物质的释放,经该复合材料脱酸处理后的纸张在具有高碱储量下仍呈弱碱性;并且,渗入纸张纤维缝隙中的复合脱酸材料表层所存在的PPFOEMA聚合物具有一定的疏水性;再者,渗入纸张纤维缝隙中的复合脱酸材料还可以提高纸张的机械强度。本发明的另一个目的在于提供上述方法制备获得的复合脱酸材料在纸张脱酸中的应用。The object of the present invention is not only to provide a method for preparing a composite deacidification material that is highly stable suspended and dispersed in a fluorocarbon medium, but also to provide a composite deacidification material that has the characteristics of high alkali storage and hydrophobicity after deacidification treatment. Preparation methods of acid materials to further innovatively develop existing technologies. The technical solution proposed by the present invention is to pre-adsorb the fluoroalkyl methacrylate (PFOEMA) monomer capable of polymerization on the inorganic nano-alkaline deacidification material, and then polymerize it in situ to form a composite deacidification material. The paper deacidified by the composite deacidification material is still weakly alkaline under high alkali reserves and has a certain degree of hydrophobicity. The composite deacidification material is a "core-shell" with the alkaline compound magnesium hydroxide Mg(OH) 2 or calcium hydroxide Ca(OH) 2 as the core and fluoroalkyl methacrylate polymer (PPFOEMA) as the shell. "Structure, not only has highly stable suspension and dispersion in fluorocarbon media, but also the composite material can easily penetrate into the gaps of paper fibers evenly. The PPFOEMA polymer shell coated on the surface of the alkaline compound Mg(OH) or Ca(OH) 2 nanoparticles can delay the release of alkaline substances in the core. The paper after deacidification of the composite material has a high alkali reserve. It is still weakly alkaline; and the PPFOEMA polymer present on the surface of the composite deacidification material that penetrates into the paper fiber gaps has a certain degree of hydrophobicity; furthermore, the composite deacidification material that penetrates into the paper fiber gaps can also improve the mechanical properties of the paper. strength. Another object of the present invention is to provide the application of the composite deacidification material prepared by the above method in paper deacidification.

为了解决上述技术问题,本发明所采用的技术方案如下:In order to solve the above technical problems, the technical solutions adopted by the present invention are as follows:

一种使纸张经脱酸处理后具有高碱储量和疏水性的复合脱酸材料的制备方法,步骤如下:A method for preparing a composite deacidification material that enables paper to have high alkali storage and hydrophobicity after deacidification treatment. The steps are as follows:

1)向氢氧化钠(NaOH)水溶液中加入水合肼(N2H4·H2O)水溶液,获得沉淀剂溶液;1) Add hydrazine hydrate (N 2 H 4 ·H 2 O) aqueous solution to sodium hydroxide (NaOH) aqueous solution to obtain a precipitant solution;

2)配置含有钙离子(Ca2+)或镁离子(Mg2+)和氟代烷基甲基丙烯酸酯的乙醇(CH3CH2OH)溶液;2) Prepare an ethanol (CH 3 CH 2 OH) solution containing calcium ions (Ca 2+ ) or magnesium ions (Mg 2+ ) and fluoroalkyl methacrylate;

3)混合搅拌步骤1)和步骤2)的溶液,置于反应釜中控温反应;3) Mix and stir the solutions of steps 1) and 2), and place them in a reaction kettle for temperature-controlled reaction;

4)反应后的混合物经离心分离、洗涤、干燥,得到固体复合脱酸材料。4) The reacted mixture is centrifuged, washed, and dried to obtain a solid composite deacidification material.

所述的使纸张经脱酸处理后具有高碱储量和疏水性的复合脱酸材料的制备方法,固体复合脱酸材料中的碱性化合物为氢氧化镁、氢氧化钙中的任一种。According to the preparation method of a composite deacidification material that makes paper have high alkali reserve and hydrophobicity after deacidification treatment, the alkaline compound in the solid composite deacidification material is any one of magnesium hydroxide and calcium hydroxide.

所述的使纸张经脱酸处理后具有高碱储量和疏水性的复合脱酸材料的制备方法,碱性化合物占固体复合脱酸材料的质量分数为50~95%。According to the method for preparing a composite deacidification material with high alkali reserve and hydrophobicity after deacidification treatment of paper, the mass fraction of the alkaline compound in the solid composite deacidification material is 50 to 95%.

所述的使纸张经脱酸处理后具有高碱储量和疏水性的复合脱酸材料的制备方法,反应釜中控温反应的温度为150℃,反应时间为12h。According to the preparation method of the composite deacidification material that makes paper have high alkali reserve and hydrophobicity after deacidification treatment, the temperature of the temperature-controlled reaction in the reactor is 150°C, and the reaction time is 12 hours.

所述方法获得的使纸张经脱酸处理后具有高碱储量和疏水性的复合脱酸材料。The composite deacidification material obtained by the method enables the paper to have high alkali reserve and hydrophobicity after deacidification treatment.

所述使纸张经脱酸处理后具有高碱储量和疏水性的复合脱酸材料应用于纸张脱酸。The composite deacidification material with high alkali reserve and hydrophobicity after deacidification treatment of paper is used for deacidification of paper.

所述的应用,先将复合脱酸材料分散在氟碳介质中,经超声处理,然后用于纸张脱酸。In the described application, the composite deacidification material is first dispersed in a fluorocarbon medium, subjected to ultrasonic treatment, and then used for paper deacidification.

所述的氟碳介质为全氟辛烷、全氟庚烷、全氟壬烷、全氟丁基四氢呋喃、全氟环醚、全氟环己烷、全氟甲基环己烷、全氟甲苯、全氟-2,7-二甲基辛烷中的一种或多种。The fluorocarbon medium is perfluorooctane, perfluoroheptane, perfluorononane, perfluorobutyltetrahydrofuran, perfluorocyclic ether, perfluorocyclohexane, perfluoromethylcyclohexane, and perfluorotoluene , one or more of perfluoro-2,7-dimethyloctane.

所述的应用,具体步骤为:The specific steps for the described application are:

(1)将复合脱酸材料分散在氟碳介质中,超声处理30min制成悬浮液,复合脱酸材料浓度为3.0~10.0g/L;(1) Disperse the composite deacidification material in the fluorocarbon medium, and conduct ultrasonic treatment for 30 minutes to form a suspension. The concentration of the composite deacidification material is 3.0 to 10.0g/L;

(2)将待脱酸的纸张浸泡在步骤(1)得到的悬浮液中,浸泡30min,然后室温晾干,完成纸张脱酸处理。(2) Soak the paper to be deacidified in the suspension obtained in step (1) for 30 minutes, and then dry it at room temperature to complete the paper deacidification treatment.

所述氟代烷基甲基丙烯酸酯(PFOEMA)的化学式如下(1)和(2):The chemical formulas of the fluoroalkyl methacrylate (PFOEMA) are as follows (1) and (2):

(1)中:n的值为4~11;(2)中:n的值为0~3,x的值为0~2。In (1): the value of n is 4 to 11; in (2): the value of n is 0 to 3, and the value of x is 0 to 2.

进一步地,所述的氟代烷基甲基丙烯酸酯为2-(全氟辛基)乙基甲基丙烯酸酯,具有(3)所示结构;Further, the fluoroalkyl methacrylate is 2-(perfluorooctyl)ethyl methacrylate, which has the structure shown in (3);

本发明提供的纸张经脱酸处理后具有高碱储量和疏水性的复合脱酸材料,是由沉淀剂氢氧化钠和水合肼水溶液来沉淀钙离子(Ca2+)或镁离子(Mg2+),先生成碱性化合物Ca(OH)2或Mg(OH)2,继之预吸附氟代烷基甲基丙烯酸酯(PFOEMA)单体,再经原位聚合反应生成氟代烷基甲基丙烯酸酯(PPFOEMA)聚合物制备而成。实验结果表明该复合脱酸材料是以碱性化合物Ca(OH)2或Mg(OH)2纳米颗粒为核、PPFOEMA聚合物为壳的“核-壳”结构Ca(OH)2@PPFOEMA或Mg(OH)2@PPFOEMA(见附图1和附图2),不仅在氟碳介质中表现出高稳定的悬浮分散性(见附图3),而且在脱酸处理过程中复合脱酸材料易均匀地渗入纸张纤维缝隙中(见附图4)。如表1所示,经脱酸处理后的纸张具有高碱储量466.29mmol/kg,而包覆在碱性化合物Mg(OH)2或Ca(OH)2纳米颗粒表面的PPFOEMA聚合物外壳能延缓内核中碱性物质的释放,使得经脱酸处理后的纸张在具有高碱储量下仍呈弱碱性(pH值介于7~8之间);并且,渗入纸张纤维缝隙中的复合脱酸材料表层的PPFOEMA聚合物所具有的疏水性使得经脱酸处理后的纸张具有一定的疏水性,与水的稳定接触角由脱酸处理前的25°大幅度地增至脱酸处理后的130°;特别地,渗入纸张纤维缝隙中的复合脱酸材料还可以提高纸张的机械强度。The paper provided by the invention is a composite deacidification material with high alkali reserve and hydrophobicity after deacidification treatment. The precipitant sodium hydroxide and hydrazine hydrate aqueous solution are used to precipitate calcium ions (Ca 2+ ) or magnesium ions (Mg 2+ ), first generate the basic compound Ca(OH) 2 or Mg(OH) 2 , then pre-adsorb the fluoroalkyl methacrylate (PFOEMA) monomer, and then undergo in-situ polymerization to generate fluoroalkyl methyl Prepared from acrylate (PPFOEMA) polymer. Experimental results show that the composite deacidification material is a "core-shell" structure Ca(OH) 2 @PPFOEMA or Mg with alkaline compound Ca(OH ) 2 or Mg(OH) 2 nanoparticles as the core and PPFOEMA polymer as the shell. (OH) 2 @PPFOEMA (see Figure 1 and Figure 2) not only shows highly stable suspension and dispersion in fluorocarbon media (see Figure 3), but also the composite deacidification material is easy to dissolve during the deacidification process. Evenly penetrate into the paper fiber gaps (see attached picture 4). As shown in Table 1, the deacidified paper has a high alkali reserve of 466.29mmol/kg, and the PPFOEMA polymer shell coated on the surface of the alkaline compound Mg(OH) 2 or Ca(OH) 2 nanoparticles can delay The release of alkaline substances in the core makes the deacidified paper still weakly alkaline (pH value between 7 and 8) with high alkali reserves; and, the composite deacidification that penetrates into the gaps in the paper fibers The hydrophobicity of the PPFOEMA polymer on the surface of the material makes the paper after deacidification treatment have a certain degree of hydrophobicity. The stable contact angle with water increases significantly from 25° before deacidification treatment to 130° after deacidification treatment. °; In particular, the composite deacidification material that penetrates into the gaps between paper fibers can also improve the mechanical strength of the paper.

相比于现有技术,本发明的有益效果为:Compared with the existing technology, the beneficial effects of the present invention are:

1)复合脱酸材料表面包覆的氟代烷基甲基丙烯酸酯聚合物(PPFOEMA)使其能在氟碳介质中高稳定地悬浮分散,且该复合材料易均匀地渗入纸张纤维缝隙中,而包覆在碱性化合物Mg(OH)2或Ca(OH)2纳米颗粒表面的PPFOEMA聚合物外壳能延缓内核中碱性物质的释放,经该复合材料脱酸处理后的纸张在具有高碱储量下仍呈弱碱性;本发明不仅解决了脱酸材料在氟碳介质中悬浮分散稳定性差的难题,而且还解决了目前现存的脱酸材料在脱酸处理后的纸张中碱储量低、易返酸或碱储量高但纸张表面pH过高等问题;1) The fluoroalkyl methacrylate polymer (PPFOEMA) coated on the surface of the composite deacidification material enables it to be suspended and dispersed in a fluorocarbon medium with high stability, and the composite material can easily penetrate into the gaps of paper fibers evenly, and The PPFOEMA polymer shell coated on the surface of the alkaline compound Mg(OH) 2 or Ca(OH) 2 nanoparticles can delay the release of alkaline substances in the core. The paper after deacidification of the composite material has high alkali reserves. It is still weakly alkaline even under deacidification conditions; the present invention not only solves the problem of poor suspension and dispersion stability of deacidification materials in fluorocarbon media, but also solves the problem of low alkali reserves and easy to use of existing deacidification materials in paper after deacidification treatment. Problems such as acid return or high alkali storage but the pH of the paper surface is too high;

2)本发明制备的复合脱酸材料表面包覆的PPFOEMA聚合物具有疏水性,脱酸处理过程中均匀地渗入纸张纤维缝隙中的复合脱酸材料使得纸张表面也表现出强疏水性而利于纸张的保存;2) The PPFOEMA polymer coated on the surface of the composite deacidification material prepared by the present invention is hydrophobic. During the deacidification process, the composite deacidification material evenly penetrates into the gaps in the paper fibers so that the surface of the paper also exhibits strong hydrophobicity, which is beneficial to the paper. preservation;

3)本发明采用原位聚合反应法制备的表面包覆PPFOEMA聚合物的纳米碱性Ca(OH)2或Mg(OH)2复合材料,方法简捷,步骤简易,合成效率高,所制备的复合脱酸材料用于纸张脱酸处理,具有纸张脱酸效果好、碱储量高且表面pH适中、疏水性好和加固作用显著等特点。3) The present invention adopts the in-situ polymerization reaction method to prepare the nano-alkaline Ca(OH) 2 or Mg(OH) 2 composite material surface-coated with PPFOEMA polymer. The method is simple, the steps are simple, and the synthesis efficiency is high. The prepared composite The deacidification material is used for paper deacidification treatment and has the characteristics of good paper deacidification effect, high alkali reserve, moderate surface pH, good hydrophobicity and significant reinforcement effect.

附图说明Description of drawings

图1为实施例2的Mg(OH)2@PPFOEMA样品的扫描电镜(SEM)图,其中PPFOEMA为2-(全氟辛基)乙基甲基丙烯酸酯聚合物;Figure 1 is a scanning electron microscope (SEM) image of the Mg(OH) 2 @PPFOEMA sample of Example 2, where PPFOEMA is a 2-(perfluorooctyl)ethyl methacrylate polymer;

图2为Mg(OH)2(a)、实施例2制备的Mg(OH)2@PPFOEMA(b)和PFOEMA单体(c)的红外光谱图,其中PFOEMA为2-(全氟辛基)乙基甲基丙烯酸酯;Figure 2 shows the infrared spectra of Mg(OH) 2 (a), Mg(OH) 2 @PPFOEMA (b) prepared in Example 2 and PFOEMA monomer (c), where PFOEMA is 2-(perfluorooctyl) Ethyl methacrylate;

图3为实施例2制备的复合脱酸材料Mg(OH)2@PPFOEMA悬浮液光学照片(图3A)和对比例1Mg(OH)2的悬浮液光学照片(图3B);Figure 3 is an optical photograph of the suspension of the composite deacidification material Mg(OH) 2 @PPFOEMA prepared in Example 2 (Fig. 3A) and the optical photograph of the suspension of Mg(OH) 2 in Comparative Example 1 (Fig. 3B);

图4为纸张脱酸前的(图4A)和经实施例18制备的复合脱酸材料Mg(OH)2@PPFOEMA脱酸处理后的SEM图(图4B);Figure 4 is a SEM image of the paper before deacidification (Figure 4A) and after deacidification treatment of the composite deacidification material Mg(OH) 2 @PPFOEMA prepared in Example 18 (Figure 4B);

图5为纸张脱酸前的(a)和经实施例18制备的复合脱酸材料Mg(OH)2@PPFOEMA脱酸处理后的(b)以及再经老化处理后的(c)与水稳定接触角。Figure 5 shows (a) before paper deacidification, (b) after deacidification of the composite deacidification material Mg(OH) 2 @PPFOEMA prepared in Example 18, and (c) after aging treatment and water stability. Contact angle.

具体实施方式Detailed ways

为使本发明的目的、技术方案和优点更加清楚,下面结合具体实施例对本发明进一步进行描述。以下实施例中如无特殊说明,所用的技术手段均为本领域技术人员所熟知的常规手段。In order to make the purpose, technical solutions and advantages of the present invention clearer, the present invention will be further described below in conjunction with specific embodiments. Unless otherwise specified in the following examples, the technical means used are conventional means well known to those skilled in the art.

实施例1Example 1

将0.429g四水乙酸镁在超声波(功率70w,频率40Khz)作用下溶于20mL无水乙醇中,并加入0.1g 2-(全氟辛基)乙基甲基丙烯酸酯(PFOEMA)单体,常温下搅拌后备用;将0.16g氢氧化钠溶于20mL水溶液中,并向其中加入4mL质量分数为80%的水合肼配成沉淀液;将沉淀液缓慢滴入上述备用液并于室温下搅拌30min,然后将该混合溶液移入内衬为聚四氟乙烯的100mL反应釜中并于150℃下反应12h,待其冷却至室温后离心分离、洗涤以去除杂质,得复合脱酸材料Mg(OH)2@PPFOEMA,其中的氢氧化镁在固体复合脱酸材料中的质量分数为90~95%。Dissolve 0.429g magnesium acetate tetrahydrate in 20mL absolute ethanol under the action of ultrasonic waves (power 70w, frequency 40Khz), and add 0.1g 2-(perfluorooctyl)ethyl methacrylate (PFOEMA) monomer, Stir at room temperature and set aside; dissolve 0.16g sodium hydroxide in 20mL aqueous solution, and add 4mL of hydrazine hydrate with a mass fraction of 80% to prepare a precipitate; slowly drop the precipitate into the above standby solution and stir at room temperature 30min, then move the mixed solution into a 100mL reactor lined with polytetrafluoroethylene and react at 150°C for 12h. After cooling to room temperature, centrifuge and wash to remove impurities to obtain the composite deacidification material Mg(OH ) 2 @PPFOEMA, the mass fraction of magnesium hydroxide in the solid composite deacidification material is 90 to 95%.

实施例2Example 2

将0.429g四水乙酸镁在超声波(功率70w,频率40Khz)作用下溶于20mL无水乙醇中,并加入0.2g 2-(全氟辛基)乙基甲基丙烯酸酯(PFOEMA)单体,常温下搅拌后备用;将0.16g氢氧化钠溶于20mL水溶液中,并向其中加入4mL质量分数为80%的水合肼配成沉淀液;将沉淀液缓慢滴入上述备用液并于室温下搅拌30min,然后将该混合溶液移入内衬为聚四氟乙烯的100mL反应釜中并于150℃下反应12h,待其冷却至室温后离心分离、洗涤以去除杂质,得复合脱酸材料Mg(OH)2@PPFOEMA,其中的氢氧化镁在固体复合脱酸材料中的质量分数为80~85%。Dissolve 0.429g magnesium acetate tetrahydrate in 20mL absolute ethanol under the action of ultrasonic waves (power 70w, frequency 40Khz), and add 0.2g 2-(perfluorooctyl)ethyl methacrylate (PFOEMA) monomer, Stir at room temperature and set aside; dissolve 0.16g sodium hydroxide in 20mL aqueous solution, and add 4mL of hydrazine hydrate with a mass fraction of 80% to prepare a precipitate; slowly drop the precipitate into the above standby solution and stir at room temperature 30min, then move the mixed solution into a 100mL reactor lined with polytetrafluoroethylene and react at 150°C for 12h. After cooling to room temperature, centrifuge and wash to remove impurities to obtain the composite deacidification material Mg(OH ) 2 @PPFOEMA, the mass fraction of magnesium hydroxide in the solid composite deacidification material is 80 to 85%.

实施例3Example 3

将0.429g四水乙酸镁在超声波(功率70w,频率40Khz)作用下溶于20mL无水乙醇中,并加入0.3g 2-(全氟辛基)乙基甲基丙烯酸酯(PFOEMA)单体,常温下搅拌后备用;将0.16g氢氧化钠溶于20mL水溶液中,并向其中加入4mL质量分数为80%的水合肼配成沉淀液;将沉淀液缓慢滴入上述备用液并于室温下搅拌30min,然后将该混合溶液移入内衬为聚四氟乙烯的100mL反应釜中并于150℃下反应12h,待其冷却至室温后离心分离、洗涤以去除杂质,得复合脱酸材料Mg(OH)2@PPFOEMA,其中的氢氧化镁在固体复合脱酸材料中的质量分数为70~75%。Dissolve 0.429g magnesium acetate tetrahydrate in 20mL absolute ethanol under the action of ultrasonic waves (power 70w, frequency 40Khz), and add 0.3g 2-(perfluorooctyl)ethyl methacrylate (PFOEMA) monomer, Stir at room temperature and set aside; dissolve 0.16g sodium hydroxide in 20mL aqueous solution, and add 4mL of hydrazine hydrate with a mass fraction of 80% to prepare a precipitate; slowly drop the precipitate into the above standby solution and stir at room temperature 30min, then move the mixed solution into a 100mL reactor lined with polytetrafluoroethylene and react at 150°C for 12h. After cooling to room temperature, centrifuge and wash to remove impurities to obtain the composite deacidification material Mg(OH ) 2 @PPFOEMA, the mass fraction of magnesium hydroxide in the solid composite deacidification material is 70 to 75%.

实施例4Example 4

将0.429g四水乙酸镁在超声波(功率70w,频率40Khz)作用下溶于20mL无水乙醇中,并加入0.4g 2-(全氟辛基)乙基甲基丙烯酸酯(PFOEMA)单体,常温下搅拌后备用;将0.16g氢氧化钠溶于20mL水溶液中,并向其中加入4mL质量分数为80%的水合肼配成沉淀液;将沉淀液缓慢滴入上述备用液并于室温下搅拌30min,然后将该混合溶液移入内衬为聚四氟乙烯的100mL反应釜中并于150℃下反应12h,待其冷却至室温后离心分离、洗涤以去除杂质,得复合脱酸材料Mg(OH)2@PPFOEMA,其中的氢氧化镁在固体复合脱酸材料中的质量分数为60~65%。Dissolve 0.429g magnesium acetate tetrahydrate in 20mL absolute ethanol under the action of ultrasonic waves (power 70w, frequency 40Khz), and add 0.4g 2-(perfluorooctyl)ethyl methacrylate (PFOEMA) monomer, Stir at room temperature and set aside; dissolve 0.16g sodium hydroxide in 20mL aqueous solution, and add 4mL of hydrazine hydrate with a mass fraction of 80% to prepare a precipitate; slowly drop the precipitate into the above standby solution and stir at room temperature 30min, then move the mixed solution into a 100mL reactor lined with polytetrafluoroethylene and react at 150°C for 12h. After cooling to room temperature, centrifuge and wash to remove impurities to obtain the composite deacidification material Mg(OH ) 2 @PPFOEMA, the mass fraction of magnesium hydroxide in the solid composite deacidification material is 60 to 65%.

实施例5Example 5

将0.429g四水乙酸镁在超声波(功率70w,频率40Khz)作用下溶于20mL无水乙醇中,并加入0.5g 2-(全氟辛基)乙基甲基丙烯酸酯(PFOEMA)单体,常温下搅拌后备用;将0.16g氢氧化钠溶于20mL水溶液中,并向其中加入4mL质量分数为80%的水合肼配成沉淀液;将沉淀液缓慢滴入上述备用液并于室温下搅拌30min,然后将该混合溶液移入内衬为聚四氟乙烯的100mL反应釜中并于150℃下反应12h,待其冷却至室温后离心分离、洗涤以去除杂质,得复合脱酸材料Mg(OH)2@PPFOEMA,其中的氢氧化镁在固体复合脱酸材料中的质量分数为50~55%。Dissolve 0.429g magnesium acetate tetrahydrate in 20mL absolute ethanol under the action of ultrasonic waves (power 70w, frequency 40Khz), and add 0.5g 2-(perfluorooctyl)ethyl methacrylate (PFOEMA) monomer, Stir at room temperature and set aside; dissolve 0.16g sodium hydroxide in 20mL aqueous solution, and add 4mL of hydrazine hydrate with a mass fraction of 80% to prepare a precipitate; slowly drop the precipitate into the above standby solution and stir at room temperature 30min, then move the mixed solution into a 100mL reactor lined with polytetrafluoroethylene and react at 150°C for 12h. After cooling to room temperature, centrifuge and wash to remove impurities to obtain the composite deacidification material Mg(OH ) 2 @PPFOEMA, the mass fraction of magnesium hydroxide in the solid composite deacidification material is 50 to 55%.

实施例6Example 6

将0.429g四水乙酸镁在超声波(功率70w,频率40Khz)作用下溶于20mL无水乙醇中,并加入0.2g全氟环己基甲基丙烯酸酯(PFCHMA)单体,常温下搅拌后备用;将0.16g氢氧化钠溶于20mL水溶液中,并向其中加入4mL质量分数为80%的水合肼配成沉淀液;将沉淀液缓慢滴入上述备用液并于室温下搅拌30min,然后将该混合溶液移入内衬为聚四氟乙烯的100mL反应釜中并于150℃下反应12h,待其冷却至室温后离心分离、洗涤以去除杂质,得复合脱酸材料Mg(OH)2@PPFCHMA(PPFCHMA表示全氟环己基甲基丙烯酸酯聚合物),其中的氢氧化镁在固体复合脱酸材料中的质量分数为80~85%。Dissolve 0.429g magnesium acetate tetrahydrate in 20mL absolute ethanol under the action of ultrasonic waves (power 70w, frequency 40Khz), and add 0.2g perfluorocyclohexyl methacrylate (PFCHMA) monomer, stir at room temperature and set aside; Dissolve 0.16g sodium hydroxide in 20mL aqueous solution, and add 4mL of hydrazine hydrate with a mass fraction of 80% to prepare a precipitate; slowly drop the precipitate into the above standby solution and stir at room temperature for 30 minutes, and then mix The solution was moved into a 100mL reaction kettle lined with polytetrafluoroethylene and reacted at 150°C for 12 hours. After cooling to room temperature, it was centrifuged and washed to remove impurities to obtain the composite deacidification material Mg(OH) 2 @PPFCHMA(PPFCHMA Represents perfluorocyclohexyl methacrylate polymer), in which the mass fraction of magnesium hydroxide in the solid composite deacidification material is 80 to 85%.

实施例7Example 7

将0.429g四水乙酸镁在超声波(功率70w,频率40Khz)作用下溶于20mL无水乙醇中,并加入0.2g甲基丙烯酸(N-甲基全氟己烷磺酰胺基)乙酯(C6SA)单体,常温下搅拌后备用;将0.16g氢氧化钠溶于20mL水溶液中,并向其中加入4mL质量分数为80%的水合肼配成沉淀液;将沉淀液缓慢滴入上述备用液并于室温下搅拌30min,然后将该混合溶液移入内衬为聚四氟乙烯的100mL反应釜中并于150℃下反应12h,待其冷却至室温后离心分离、洗涤以去除杂质,得复合脱酸材料Mg(OH)2@PC6SA(PC6SA表示甲基丙烯酸(N-甲基全氟己烷磺酰胺基)乙酯聚合物),其中的氢氧化镁在固体复合脱酸材料中的质量分数为80~85%。Dissolve 0.429g magnesium acetate tetrahydrate in 20mL absolute ethanol under the action of ultrasonic waves (power 70w, frequency 40Khz), and add 0.2g (N-methylperfluorohexanesulfonamide) ethyl methacrylate (C 6 SA) monomer, stir at room temperature and set aside; dissolve 0.16g sodium hydroxide in 20 mL aqueous solution, and add 4 mL of hydrazine hydrate with a mass fraction of 80% to prepare a precipitate; slowly drip the precipitate into the above set aside The solution was stirred at room temperature for 30 minutes, and then the mixed solution was moved into a 100 mL reaction kettle lined with polytetrafluoroethylene and reacted at 150°C for 12 hours. After cooling to room temperature, it was centrifuged and washed to remove impurities to obtain a composite. Deacidification material Mg(OH) 2 @PC 6 SA (PC 6 SA represents methacrylic acid (N-methylperfluorohexanesulfonamide) ethyl ester polymer), in which magnesium hydroxide is in the solid composite deacidification material The mass fraction in is 80~85%.

实施例8Example 8

将0.429g四水乙酸镁在超声波(功率70w,频率40Khz)作用下溶于20mL无水乙醇中,并加入0.2g丙烯酸全氟烷基乙酯(TEAc-8)单体,常温下搅拌后备用;将0.16g氢氧化钠溶于20mL水溶液中,并向其中加入4mL质量分数为80%的水合肼配成沉淀液;将沉淀液缓慢滴入上述备用液并于室温下搅拌30min,然后将该混合溶液移入内衬为聚四氟乙烯的100mL反应釜中并于150℃下反应12h,待其冷却至室温后离心分离、洗涤以去除杂质,得复合脱酸材料Mg(OH)2@PTEAc-8(PTEAc-8表示丙烯酸全氟烷基乙酯聚合物),其中的氢氧化镁在固体复合脱酸材料中的质量分数为80~85%。Dissolve 0.429g magnesium acetate tetrahydrate in 20mL absolute ethanol under the action of ultrasonic waves (power 70w, frequency 40Khz), and add 0.2g perfluoroalkyl ethyl acrylate (TEAc-8) monomer, stir at room temperature and set aside. ; Dissolve 0.16g sodium hydroxide in 20mL aqueous solution, and add 4mL of hydrazine hydrate with a mass fraction of 80% to prepare a precipitate; slowly drip the precipitate into the above standby solution and stir at room temperature for 30min, and then add the The mixed solution was moved into a 100mL reactor lined with polytetrafluoroethylene and reacted at 150°C for 12 hours. After cooling to room temperature, it was centrifuged and washed to remove impurities to obtain the composite deacidification material Mg(OH) 2 @PTEAc- 8 (PTEAc-8 represents perfluoroalkyl ethyl acrylate polymer), in which the mass fraction of magnesium hydroxide in the solid composite deacidification material is 80 to 85%.

实施例9Example 9

将0.429g四水乙酸镁在超声波(功率70w,频率40Khz)作用下溶于20mL无水乙醇中,并加入0.2g甲基丙烯酸三氟乙酯(FMA)单体,常温下搅拌后备用;将0.16g氢氧化钠溶于20mL水溶液中,并向其中加入4mL质量分数为80%的水合肼配成沉淀液;将沉淀液缓慢滴入上述备用液并于室温下搅拌30min,然后将该混合溶液移入内衬为聚四氟乙烯的100mL反应釜中并于150℃下反应12h,待其冷却至室温后离心分离、洗涤以去除杂质,得复合脱酸材料Mg(OH)2@PFMA(PFMA为甲基丙烯酸三氟乙酯聚合物),其中的氢氧化镁在固体复合脱酸材料中的质量分数为80~85%。Dissolve 0.429g magnesium acetate tetrahydrate in 20mL absolute ethanol under the action of ultrasonic waves (power 70w, frequency 40Khz), and add 0.2g trifluoroethyl methacrylate (FMA) monomer, stir at room temperature and set aside; Dissolve 0.16g sodium hydroxide in 20mL aqueous solution, and add 4mL of hydrazine hydrate with a mass fraction of 80% to prepare a precipitate; slowly drip the precipitate into the above standby solution and stir at room temperature for 30 minutes, and then add the mixed solution Move it into a 100mL reaction kettle lined with polytetrafluoroethylene and react at 150°C for 12 hours. After cooling to room temperature, centrifuge and wash to remove impurities to obtain the composite deacidification material Mg(OH) 2 @PFMA (PFMA is Trifluoroethyl methacrylate polymer), in which the mass fraction of magnesium hydroxide in the solid composite deacidification material is 80 to 85%.

实施例10Example 10

将0.316g乙酸钙在超声波(功率70w,频率40Khz)作用下溶于20mL无水乙醇中,并加入0.1g 2-(全氟辛基)乙基甲基丙烯酸酯(PFOEMA)单体,常温下搅拌后备用;将0.16g氢氧化钠溶于20mL水溶液中,并向其中加入4mL质量分数为80%的水合肼配成沉淀液;将沉淀液缓慢滴入上述备用液并于室温下搅拌30min,然后将该混合溶液移入内衬为聚四氟乙烯的100mL反应釜中并于150℃下反应12h,待其冷却至室温后离心分离、洗涤以去除杂质,得复合脱酸材料Ca(OH)2@PPFOEMA,其中的氢氧化钙在固体复合脱酸材料中的质量分数为90~95%。Dissolve 0.316g calcium acetate in 20mL absolute ethanol under the action of ultrasonic waves (power 70w, frequency 40Khz), and add 0.1g 2-(perfluorooctyl)ethyl methacrylate (PFOEMA) monomer at room temperature. Stir and set aside; dissolve 0.16g sodium hydroxide in 20mL aqueous solution, and add 4mL of hydrazine hydrate with a mass fraction of 80% to prepare a precipitate; slowly drop the precipitate into the above standby solution and stir at room temperature for 30 minutes. The mixed solution was then moved into a 100 mL reactor lined with polytetrafluoroethylene and reacted at 150°C for 12 hours. After cooling to room temperature, it was centrifuged and washed to remove impurities to obtain the composite deacidification material Ca(OH) 2 @PPFOEMA, the mass fraction of calcium hydroxide in the solid composite deacidification material is 90 to 95%.

实施例11Example 11

将0.316g乙酸钙在超声波(功率70w,频率40Khz)作用下溶于20mL无水乙醇中,并加入0.2g 2-(全氟辛基)乙基甲基丙烯酸酯(PFOEMA)单体,常温下搅拌后备用;将0.16g氢氧化钠溶于20mL水溶液中,并向其中加入4mL质量分数为80%的水合肼配成沉淀液;将沉淀液缓慢滴入上述备用液并于室温下搅拌30min,然后将该混合溶液移入内衬为聚四氟乙烯的100mL反应釜中并于150℃下反应12h,待其冷却至室温后离心分离、洗涤以去除杂质,得复合脱酸材料Ca(OH)2@PPFOEMA,其中的氢氧化钙在固体复合脱酸材料中的质量分数为80~85%。Dissolve 0.316g calcium acetate in 20mL absolute ethanol under the action of ultrasonic waves (power 70w, frequency 40Khz), and add 0.2g 2-(perfluorooctyl)ethyl methacrylate (PFOEMA) monomer at room temperature. Stir and set aside; dissolve 0.16g sodium hydroxide in 20mL aqueous solution, and add 4mL of hydrazine hydrate with a mass fraction of 80% to prepare a precipitate; slowly drop the precipitate into the above standby solution and stir at room temperature for 30 minutes. The mixed solution was then moved into a 100 mL reactor lined with polytetrafluoroethylene and reacted at 150°C for 12 hours. After cooling to room temperature, it was centrifuged and washed to remove impurities to obtain the composite deacidification material Ca(OH) 2 @PPFOEMA, the mass fraction of calcium hydroxide in the solid composite deacidification material is 80 to 85%.

实施例12Example 12

将0.316g乙酸钙在超声波(功率70w,频率40Khz)作用下溶于20mL无水乙醇中,并加入0.3g 2-(全氟辛基)乙基甲基丙烯酸酯(PFOEMA)单体,常温下搅拌后备用;将0.16g氢氧化钠溶于20mL水溶液中,并向其中加入4mL质量分数为80%的水合肼配成沉淀液;将沉淀液缓慢滴入上述备用液并于室温下搅拌30min,然后将该混合溶液移入内衬为聚四氟乙烯的100mL反应釜中并于150℃下反应12h,待其冷却至室温后离心分离、洗涤以去除杂质,得复合脱酸材料Ca(OH)2@PPFOEMA,其中的氢氧化钙在固体复合脱酸材料中的质量分数为70~75%。Dissolve 0.316g calcium acetate in 20mL absolute ethanol under the action of ultrasonic waves (power 70w, frequency 40Khz), and add 0.3g 2-(perfluorooctyl)ethyl methacrylate (PFOEMA) monomer at room temperature. Stir and set aside; dissolve 0.16g sodium hydroxide in 20mL aqueous solution, and add 4mL of hydrazine hydrate with a mass fraction of 80% to prepare a precipitate; slowly drop the precipitate into the above standby solution and stir at room temperature for 30 minutes. The mixed solution was then moved into a 100 mL reactor lined with polytetrafluoroethylene and reacted at 150°C for 12 hours. After cooling to room temperature, it was centrifuged and washed to remove impurities to obtain the composite deacidification material Ca(OH) 2 @PPFOEMA, the mass fraction of calcium hydroxide in the solid composite deacidification material is 70 to 75%.

实施例13Example 13

将0.316g乙酸钙在超声波(功率70w,频率40Khz)作用下溶于20mL无水乙醇中,并加入0.4g 2-(全氟辛基)乙基甲基丙烯酸酯(PFOEMA)单体,常温下搅拌后备用;将0.16g氢氧化钠溶于20mL水溶液中,并向其中加入4mL质量分数为80%的水合肼配成沉淀液;将沉淀液缓慢滴入上述备用液并于室温下搅拌30min,然后将该混合溶液移入内衬为聚四氟乙烯的100mL反应釜中并于150℃下反应12h,待其冷却至室温后离心分离、洗涤以去除杂质,得复合脱酸材料Ca(OH)2@PPFOEMA,其中的氢氧化钙在固体复合脱酸材料中的质量分数为60~65%。Dissolve 0.316g calcium acetate in 20mL absolute ethanol under the action of ultrasonic waves (power 70w, frequency 40Khz), and add 0.4g 2-(perfluorooctyl)ethyl methacrylate (PFOEMA) monomer at room temperature. Stir and set aside; dissolve 0.16g sodium hydroxide in 20mL aqueous solution, and add 4mL of hydrazine hydrate with a mass fraction of 80% to prepare a precipitate; slowly drop the precipitate into the above standby solution and stir at room temperature for 30 minutes. The mixed solution was then moved into a 100 mL reactor lined with polytetrafluoroethylene and reacted at 150°C for 12 hours. After cooling to room temperature, it was centrifuged and washed to remove impurities to obtain the composite deacidification material Ca(OH) 2 @PPFOEMA, the mass fraction of calcium hydroxide in the solid composite deacidification material is 60 to 65%.

实施例14Example 14

将0.316g乙酸钙在超声波(功率70w,频率40Khz)作用下溶于20mL无水乙醇中,并加入0.5g 2-(全氟辛基)乙基甲基丙烯酸酯(PFOEMA)单体,常温下搅拌后备用;将0.16g氢氧化钠溶于20mL水溶液中,并向其中加入4mL质量分数为80%的水合肼配成沉淀液;将沉淀液缓慢滴入上述备用液并于室温下搅拌30min,然后将该混合溶液移入内衬为聚四氟乙烯的100mL反应釜中并于150℃下反应12h,待其冷却至室温后离心分离、洗涤以去除杂质,得复合脱酸材料Ca(OH)2@PPFOEMA,其中的氢氧化钙在固体复合脱酸材料中的质量分数为50~55%。Dissolve 0.316g calcium acetate in 20mL absolute ethanol under the action of ultrasonic waves (power 70w, frequency 40Khz), and add 0.5g 2-(perfluorooctyl)ethyl methacrylate (PFOEMA) monomer at room temperature. Stir and set aside; dissolve 0.16g sodium hydroxide in 20mL aqueous solution, and add 4mL of hydrazine hydrate with a mass fraction of 80% to prepare a precipitate; slowly drop the precipitate into the above standby solution and stir at room temperature for 30 minutes. The mixed solution was then moved into a 100 mL reactor lined with polytetrafluoroethylene and reacted at 150°C for 12 hours. After cooling to room temperature, it was centrifuged and washed to remove impurities to obtain the composite deacidification material Ca(OH) 2 @PPFOEMA, the mass fraction of calcium hydroxide in the solid composite deacidification material is 50 to 55%.

实施例15Example 15

取实施例2中的1.0g Mg(OH)2@PPFOEMA均匀分散于200mL全氟辛烷中,超声(功率70w,频率40Khz)处理30min,得高稳定悬浮分散的复合脱酸材料-全氟辛烷分散体系。Take 1.0g Mg(OH) 2 @PPFOEMA in Example 2 and disperse it evenly in 200mL perfluorooctane, and treat it with ultrasonic (power 70w, frequency 40Khz) for 30 minutes to obtain a highly stable suspended and dispersed composite deacidification material - perfluorooctane. alkane dispersion system.

图2为氢氧化镁(a)、Mg(OH)2@PPFOEMA复合脱酸材料(b)、2-(全氟辛基)乙基甲基丙烯酸酯单体(c)的红外光谱图。氢氧化镁(a)中3700cm-1处的吸收峰对应于-OH振动吸收;2-(全氟辛基)乙基甲基丙烯酸酯(c)中1241cm-1、1205cm-1和1149cm-1处的吸收峰对应于-CF2振动吸收,1725cm-1处的吸收峰对应于-C=O振动吸收,1639cm-1处的吸收峰对应于C=C的振动吸收。Mg(OH)2@PPFOEMA复合脱酸材料(b)既有3700cm-1处的-OH振动吸收峰,也有1241cm-1、1205cm-1、1149cm-1的-CF2振动吸收峰,但没有出现1639cm-1处的C=C的振动吸收峰,表明2-(全氟辛基)乙基甲基丙烯酸酯中的CH2=C-发生了聚合反应,形成-(CH2-C-)n-聚合物;并且,复合脱酸材料的红外光谱图中C=O吸收峰由1725cm-1位移到1735cm-1处,表明2-(全氟辛基)乙基甲基丙烯酸酯聚合物包覆在氢氧化镁表面,二者之间存在一定的相互作用,形成稳定的核-壳结构复合脱酸材料Mg(OH)2@PPFOEMA。该复合脱酸材料在全氟辛烷中能高稳定地悬浮分散,其稳定悬浮分散时间不低于10天,样品的光学照片如图3A所示。Figure 2 shows the infrared spectra of magnesium hydroxide (a), Mg(OH) 2 @PPFOEMA composite deacidification material (b), and 2-(perfluorooctyl)ethyl methacrylate monomer (c). The absorption peak at 3700cm -1 in magnesium hydroxide (a) corresponds to -OH vibration absorption; 1241cm -1 , 1205cm -1 and 1149cm -1 in 2-(perfluorooctyl)ethyl methacrylate (c) The absorption peak at 1725cm -1 corresponds to -CF2 vibration absorption, the absorption peak at 1725cm -1 corresponds to -C=O vibration absorption, and the absorption peak at 1639cm -1 corresponds to C=C vibration absorption. Mg(OH) 2 @PPFOEMA composite deacidification material (b) has both the -OH vibration absorption peak at 3700cm -1 and the -CF 2 vibration absorption peak at 1241cm -1 , 1205cm -1 , and 1149cm -1 , but they do not appear. The vibration absorption peak of C=C at 1639cm -1 indicates that CH 2 =C- in 2-(perfluorooctyl)ethyl methacrylate has undergone a polymerization reaction to form -(CH 2 -C-) n -polymer; and, the C=O absorption peak in the infrared spectrum of the composite deacidification material shifts from 1725cm -1 to 1735cm -1 , indicating that 2-(perfluorooctyl)ethyl methacrylate polymer coating On the surface of magnesium hydroxide, there is a certain interaction between the two, forming a stable core-shell structure composite deacidification material Mg(OH) 2 @PPFOEMA. The composite deacidification material can be suspended and dispersed in perfluorooctane with high stability, and its stable suspension and dispersion time is not less than 10 days. The optical photo of the sample is shown in Figure 3A.

对比例1Comparative example 1

将0.429g四水乙酸镁在超声波(功率70w,频率40Khz)作用下溶于20mL无水乙醇中常温下搅拌后备用;将0.16g氢氧化钠溶于20mL水溶液中,并向其中加入4mL质量分数为80%的水合肼配成沉淀液;将沉淀液缓慢滴入上述备用液并于室温下搅拌30min,然后将该混合溶液移入内衬为聚四氟乙烯的100mL反应釜中并于150℃下反应12h,待其冷却至室温后离心分离、洗涤以去除杂质,得到纯Mg(OH)2;将1.0g Mg(OH)2分散于200mL全氟辛烷中,超声处理30min,再静置30min后其中的Mg(OH)2就发生了明显的沉降,其光学照片如图3B所示。Dissolve 0.429g magnesium acetate tetrahydrate in 20mL absolute ethanol under the action of ultrasonic waves (power 70w, frequency 40Khz) and stir at room temperature before use; dissolve 0.16g sodium hydroxide in 20mL aqueous solution, and add 4mL mass fraction to it Prepare a precipitate for 80% hydrazine hydrate; slowly drop the precipitate into the above standby solution and stir at room temperature for 30 minutes. Then move the mixed solution into a 100 mL reaction kettle lined with polytetrafluoroethylene and incubate at 150°C. React for 12 hours, wait for it to cool to room temperature, then centrifuge and wash to remove impurities to obtain pure Mg(OH) 2 ; disperse 1.0g Mg(OH) 2 in 200 mL of perfluorooctane, sonicate for 30 min, and then let stand for 30 min. Afterwards, the Mg(OH) 2 in it underwent obvious sedimentation, and its optical photo is shown in Figure 3B.

对比例2Comparative example 2

将0.429g四水乙酸镁在超声波(功率70w,频率40Khz)作用下溶于20mL无水乙醇中,并加入0.2g十二烷基硫酸钠(SDS)单体,常温下搅拌后备用;将0.16g氢氧化钠溶于20mL水溶液中,并向其中加入4mL质量分数为80%的水合肼配成沉淀液;将沉淀液缓慢滴入上述备用液并于室温下搅拌30min,然后将该混合溶液移入内衬为聚四氟乙烯的100mL反应釜中并于150℃下反应12h,待其冷却至室温后离心分离、洗涤以去除杂质,得复合脱酸材料Mg(OH)2@SDS;将1.0g Mg(OH)2@SDS均匀分散于200mL全氟辛烷中,超声分散30min,再静置30min后其中的固体颗粒就发生了明显的沉降。Dissolve 0.429g magnesium acetate tetrahydrate in 20mL absolute ethanol under the action of ultrasonic waves (power 70w, frequency 40Khz), and add 0.2g sodium dodecyl sulfate (SDS) monomer, stir at room temperature and set aside; add 0.16 g of sodium hydroxide was dissolved in 20 mL of aqueous solution, and 4 mL of hydrazine hydrate with a mass fraction of 80% was added to prepare a precipitate; the precipitate was slowly dropped into the above standby solution and stirred at room temperature for 30 min, and then the mixed solution was transferred into In a 100mL reaction kettle lined with polytetrafluoroethylene, react at 150°C for 12 hours. After cooling to room temperature, centrifuge and wash to remove impurities to obtain the composite deacidification material Mg(OH) 2 @SDS; add 1.0g Mg(OH) 2 @SDS was evenly dispersed in 200 mL of perfluorooctane, dispersed ultrasonically for 30 minutes, and then allowed to stand for 30 minutes before the solid particles settled significantly.

实施例16Example 16

将0.316g乙酸钙在超声波(功率70w,频率40Khz)作用下溶于20mL无水乙醇中,并加入0.2g全氟环己基甲基丙烯酸酯(PFCHMA)单体,常温下搅拌后备用;将0.16g氢氧化钠溶于20mL水溶液中,并向其中加入4mL质量分数为80%的水合肼配成沉淀液;将沉淀液缓慢滴入上述备用液并于室温下搅拌30min,然后将该混合溶液移入内衬为聚四氟乙烯的100mL反应釜中并于150℃下反应12h,待其冷却至室温后离心分离、洗涤以去除杂质,得复合脱酸材料Ca(OH)2@PPFCHMA,将1.0g Ca(OH)2@PPFCHMA均匀分散于200mL全氟环醚中,超声处理30min,得高稳定悬浮分散的复合脱酸材料-全氟环醚分散体系。Dissolve 0.316g calcium acetate in 20mL absolute ethanol under the action of ultrasonic waves (power 70w, frequency 40Khz), and add 0.2g perfluorocyclohexyl methacrylate (PFCHMA) monomer, stir at room temperature and set aside; add 0.16 g of sodium hydroxide was dissolved in 20 mL of aqueous solution, and 4 mL of hydrazine hydrate with a mass fraction of 80% was added to prepare a precipitate; the precipitate was slowly dropped into the above standby solution and stirred at room temperature for 30 min, and then the mixed solution was transferred into In a 100mL reaction kettle lined with polytetrafluoroethylene, react at 150°C for 12 hours. After cooling to room temperature, centrifuge and wash to remove impurities to obtain the composite deacidification material Ca(OH) 2 @PPFCHMA. Add 1.0g Ca(OH) 2 @PPFCHMA was uniformly dispersed in 200 mL of perfluorocyclic ether, and ultrasonic treatment was performed for 30 minutes to obtain a highly stable suspended and dispersed composite deacidification material-perfluorocyclic ether dispersion system.

实施例17Example 17

将0.429g四水乙酸镁在超声波(功率70w,频率40Khz)作用下溶于20mL无水乙醇中,并加入0.2g全氟环己基甲基丙烯酸酯(PFCHMA)单体,常温下搅拌后备用;将0.16g氢氧化钠溶于20mL水溶液中,并向其中加入4mL质量分数为80%的水合肼配成沉淀液;将沉淀液缓慢滴入上述备用液并于室温下搅拌30min,然后将该混合溶液移入内衬为聚四氟乙烯的100mL反应釜中并于150℃下反应12h,待其冷却至室温后离心分离、洗涤去除杂质得复合脱酸材料Mg(OH)2@PPFCHMA,将1.0g Mg(OH)2@PPFCHMA均匀分散于200mL全氟环醚中,超声处理30min,得高稳定悬浮分散的复合脱酸材料-全氟环醚分散体系。Dissolve 0.429g magnesium acetate tetrahydrate in 20mL absolute ethanol under the action of ultrasonic waves (power 70w, frequency 40Khz), and add 0.2g perfluorocyclohexyl methacrylate (PFCHMA) monomer, stir at room temperature and set aside; Dissolve 0.16g sodium hydroxide in 20mL aqueous solution, and add 4mL of hydrazine hydrate with a mass fraction of 80% to prepare a precipitate; slowly drop the precipitate into the above standby solution and stir at room temperature for 30 minutes, and then mix The solution was moved into a 100mL reaction kettle lined with polytetrafluoroethylene and reacted at 150°C for 12 hours. After cooling to room temperature, it was centrifuged and washed to remove impurities to obtain the composite deacidification material Mg(OH) 2 @PPFCHMA. 1.0g Mg(OH) 2 @PPFCHMA was evenly dispersed in 200 mL of perfluorocyclic ether, and ultrasonic treatment was performed for 30 minutes to obtain a highly stable suspended and dispersed composite deacidification material-perfluorocyclic ether dispersion system.

实施例18Example 18

取实施例15中复合脱酸材料用于纸张脱酸,此时复合脱酸材料-全氟辛烷分散体系中复合脱酸材料浓度为5g/L。The composite deacidification material in Example 15 is used for paper deacidification. At this time, the concentration of the composite deacidification material in the composite deacidification material-perfluorooctane dispersion system is 5g/L.

取表面平均pH值为4.02酸性纸张,浸泡在含复合脱酸材料Mg(OH)2@PPFOEMA的全氟辛烷介质中,用镊子轻轻摆动纸张,浸泡30min后将纸张取出,室温条件下晾干24h。用国标GB/T 1545.2-2003法检测经复合脱酸材料Mg(OH)2@PPFOEMA处理后的纸张的表面pH值为7.56,而碱储量为466.29mmol/kg(见表1),表明经该复合脱酸材料处理后的纸张在具有较高的碱储量下仍呈弱碱性。Take the acidic paper with an average surface pH value of 4.02, soak it in the perfluorooctane medium containing the composite deacidification material Mg(OH) 2 @PPFOEMA, gently swing the paper with tweezers, soak it for 30 minutes, take out the paper, and dry it at room temperature. Dry for 24h. The surface pH value of the paper treated with the composite deacidification material Mg(OH) 2 @PPFOEMA was tested using the national standard GB/T 1545.2-2003 method to be 7.56, while the alkali reserve was 466.29mmol/kg (see Table 1), indicating that the The paper treated with the composite deacidification material is still weakly alkaline even with high alkali reserves.

将上述经脱酸处理后的纸张再经105℃干热老化72h。用国标GB/T1545.2-2003法检测纸张的pH值为7.49,而碱储量为456.87mmol/kg,表明经脱酸处理并再经干热老化处理后的纸张仍具有较高的碱储量且仍呈弱碱性。与之相比,未经脱酸处理的纸张经干热老化处理后平均pH值为3.69,表明经复合脱酸材料Mg(OH)2@PPFOEMA材料处理后的纸张具有较好的脱酸效果和抗返酸能力。The above deacidified paper was then dry-heat aged at 105°C for 72 hours. The pH value of the paper tested using the national standard GB/T1545.2-2003 method is 7.49, and the alkali reserve is 456.87mmol/kg, indicating that the paper after deacidification and dry heat aging treatment still has a high alkali reserve and Still slightly alkaline. In comparison, the average pH value of paper without deacidification treatment after dry heat aging treatment was 3.69, indicating that the paper treated with the composite deacidification material Mg(OH) 2 @PPFOEMA material has better deacidification effect and Anti-acid reflux ability.

将上述脱酸处理前后的纸张及脱酸处理后经干热老化的纸张进行疏水性(水接触角)的测定,测定的数据如图5和表1所示。The hydrophobicity (water contact angle) of the paper before and after the above-mentioned deacidification treatment and the dry-heat aging paper after the deacidification treatment was measured. The measured data are shown in Figure 5 and Table 1.

从图5中可以看出:未经脱酸处理的纸张在10min内与水的接触角从最初的117°急剧下降到25°,但经脱酸处理后及脱酸处理后再经干热老化处理后的纸张与水的接触角为138°,且在20min内基本保持不变,表明经复合脱酸材料处理后的纸张表现出优异的疏水性。It can be seen from Figure 5 that the contact angle of paper without deacidification with water dropped sharply from the initial 117° to 25° within 10 minutes, but after deacidification and dry heat aging The contact angle between the treated paper and water was 138° and remained basically unchanged within 20 minutes, indicating that the paper treated with the composite deacidification material showed excellent hydrophobicity.

将上述脱酸处理前后的纸张及脱酸处理前后经干热老化的纸张进行机械性能(耐折度、抗张强度及撕裂度)的测定,数据如表1所示。结果表明经复合脱酸材料Mg(OH)2@PPFOEMA处理后纸张的机械性能较未处理的纸张有一定程度的提高,即使再经干热老化处理,其机械性能也仍然优于未经脱酸处理的纸张。The mechanical properties (folding resistance, tensile strength and tearing strength) of the paper before and after the above-mentioned deacidification treatment and the dry-heat aged paper before and after the deacidification treatment were measured. The data are shown in Table 1. The results show that the mechanical properties of paper treated with the composite deacidification material Mg(OH) 2 @PPFOEMA are improved to a certain extent compared with untreated paper. Even after dry heat aging treatment, its mechanical properties are still better than those without deacidification. Handled paper.

表1纸张样品的性能数据Table 1 Performance data of paper samples

以上所述仅为本发明的优选实施例而已,并不用于限制本发明,对于本领域的技术人员来说,本发明可以有各种更改和变化。凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above descriptions are only preferred embodiments of the present invention and are not intended to limit the present invention. For those skilled in the art, the present invention may have various modifications and changes. Any modifications, equivalent substitutions, improvements, etc. made within the spirit and principles of the present invention shall be included in the protection scope of the present invention.

Claims (8)

1.一种使纸张经脱酸处理后具有高碱储量和疏水性的复合脱酸材料的制备方法,其特征在于,步骤如下:1. A method for preparing a composite deacidification material with high alkali reserve and hydrophobicity after deacidification treatment of paper, characterized in that the steps are as follows: 1)向氢氧化钠水溶液中加入水合肼水溶液,获得沉淀剂溶液;1) Add hydrazine hydrate aqueous solution to the sodium hydroxide aqueous solution to obtain a precipitant solution; 2)配置含有钙、镁离子和氟代烷基甲基丙烯酸酯的乙醇溶液;2) Prepare an ethanol solution containing calcium, magnesium ions and fluoroalkyl methacrylate; 3)混合搅拌步骤1)和步骤2)的溶液,置于反应釜中控温150℃,反应12h;3) Mix and stir the solution in steps 1) and 2), place it in a reaction kettle, control the temperature at 150°C, and react for 12 hours; 4)反应后的混合物经离心分离、洗涤、干燥,得到固体复合脱酸材料。4) The reacted mixture is centrifuged, washed, and dried to obtain a solid composite deacidification material. 2.根据权利要求1所述的使纸张经脱酸处理后具有高碱储量和疏水性的复合脱酸材料的制法,其特征在于,固体复合脱酸材料中的碱性化合物为氢氧化镁、氢氧化钙中的任一种。2. The method for making a composite deacidification material with high alkali reserve and hydrophobicity after deacidification treatment of paper according to claim 1, characterized in that the alkaline compound in the solid composite deacidification material is magnesium hydroxide. , any one of calcium hydroxide. 3.根据权利要求1所述的使纸张经脱酸处理后具有高碱储量和疏水性的复合脱酸材料的制法,其特征在于,碱性化合物占固体复合脱酸材料的质量分数为50~95%。3. The method for making a composite deacidification material with high alkali reserve and hydrophobicity after deacidification of paper according to claim 1, characterized in that the mass fraction of the alkaline compound in the solid composite deacidification material is 50 ~95%. 4.权利要求1-3任一项所述方法获得的使纸张经脱酸处理后具有高碱储量和疏水性的复合脱酸材料。4. A composite deacidification material obtained by the method of any one of claims 1 to 3, which enables the paper to have high alkali reserve and hydrophobicity after deacidification treatment. 5.权利要求4所述使纸张经脱酸处理后具有高碱储量和疏水性的复合脱酸材料应用于纸张脱酸。5. The composite deacidification material according to claim 4, which allows the paper to have high alkali reserve and hydrophobicity after deacidification treatment, is used for paper deacidification. 6.根据权利要求5所述的应用,其特征在于,先将复合脱酸材料分散在氟碳介质中并超声处理30min以获得稳定的悬浮液,然后用于纸张脱酸。6. The application according to claim 5, characterized in that the composite deacidification material is first dispersed in a fluorocarbon medium and ultrasonic treated for 30 minutes to obtain a stable suspension, and then used for paper deacidification. 7.根据权利要求6所述的应用,其特征在于,所述的氟碳介质为全氟辛烷、全氟庚烷、全氟壬烷、全氟丁基四氢呋喃、全氟环醚、全氟环己烷、全氟甲基环己烷、全氟甲苯、全氟-2,7-二甲基辛烷中的一种或多种。7. Application according to claim 6, characterized in that the fluorocarbon medium is perfluorooctane, perfluoroheptane, perfluorononane, perfluorobutyltetrahydrofuran, perfluorocyclic ether, perfluorocarbon One or more of cyclohexane, perfluoromethylcyclohexane, perfluorotoluene, and perfluoro-2,7-dimethyloctane. 8.根据权利要求6所述的应用,其特征在于,具体步骤为:8. The application according to claim 6, characterized in that the specific steps are: (1)将复合脱酸材料分散在氟碳介质中,超声处理30min后制成悬浮液,复合脱酸材料浓度为3.0~10.0g/L;(1) Disperse the composite deacidification material in the fluorocarbon medium, and prepare a suspension after ultrasonic treatment for 30 minutes. The concentration of the composite deacidification material is 3.0 to 10.0g/L; (2)将待脱酸的纸张浸泡在步骤(1)得到的悬浮液中,浸泡30min,然后室温晾干,完成纸张脱酸处理。(2) Soak the paper to be deacidified in the suspension obtained in step (1), soak for 30 minutes, and then dry at room temperature to complete the paper deacidification treatment.
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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1551757A (en) * 1967-01-23 1968-12-27
KR20090067315A (en) * 2007-12-21 2009-06-25 주식회사 코오롱 Core-shell structured polymer beads and preparation method thereof
CN104652173A (en) * 2015-02-04 2015-05-27 江志鑫 Book treatment method
CN113863053A (en) * 2021-09-30 2021-12-31 杭州众材科技股份有限公司 Entire paper deacidification method
CN114753186A (en) * 2022-04-15 2022-07-15 南京大学 Paper deacidification composite material with high-stability suspension dispersion in fluorocarbon medium and preparation method and application thereof
CN115787350A (en) * 2022-11-04 2023-03-14 国家图书馆 Paper fluorine-containing deacidification liquid

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1551757A (en) * 1967-01-23 1968-12-27
KR20090067315A (en) * 2007-12-21 2009-06-25 주식회사 코오롱 Core-shell structured polymer beads and preparation method thereof
CN104652173A (en) * 2015-02-04 2015-05-27 江志鑫 Book treatment method
CN113863053A (en) * 2021-09-30 2021-12-31 杭州众材科技股份有限公司 Entire paper deacidification method
CN114753186A (en) * 2022-04-15 2022-07-15 南京大学 Paper deacidification composite material with high-stability suspension dispersion in fluorocarbon medium and preparation method and application thereof
CN115787350A (en) * 2022-11-04 2023-03-14 国家图书馆 Paper fluorine-containing deacidification liquid

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