WO2012016397A1 - 用于喷墨直接制版的墨水及其制备方法 - Google Patents

用于喷墨直接制版的墨水及其制备方法 Download PDF

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Publication number
WO2012016397A1
WO2012016397A1 PCT/CN2010/078063 CN2010078063W WO2012016397A1 WO 2012016397 A1 WO2012016397 A1 WO 2012016397A1 CN 2010078063 W CN2010078063 W CN 2010078063W WO 2012016397 A1 WO2012016397 A1 WO 2012016397A1
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WIPO (PCT)
Prior art keywords
ink
propylene glycol
monomethyl ether
glycol monomethyl
core funnel
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Application number
PCT/CN2010/078063
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English (en)
French (fr)
Inventor
李会玲
秦明明
宋延林
Original Assignee
中国科学院化学研究所
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Application filed by 中国科学院化学研究所 filed Critical 中国科学院化学研究所
Priority to CN201080016033.5A priority Critical patent/CN102725361B/zh
Priority to US13/814,178 priority patent/US8921459B2/en
Priority to EP10855535.0A priority patent/EP2592121B1/en
Priority to JP2013523460A priority patent/JP5657795B2/ja
Publication of WO2012016397A1 publication Critical patent/WO2012016397A1/zh

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    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D11/00—Inks
    • C09D11/30—Inkjet printing inks
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D11/00—Inks
    • C09D11/02—Printing inks
    • C09D11/10—Printing inks based on artificial resins
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D11/00—Inks
    • C09D11/30—Inkjet printing inks
    • C09D11/38—Inkjet printing inks characterised by non-macromolecular additives other than solvents, pigments or dyes

Definitions

  • the present invention relates to the field of inks, and relates to an environmentally friendly ink for improving image resolution, and more particularly to an environmentally friendly ink for direct inkjet printing which can be used for inkjet printing direct plate making technology (CTP) and a method for preparing the same.
  • CTP direct plate making technology
  • CTP technology which represents the development direction of international advanced printing plate making, omits the traditional photographic imaging process and simplifies the plate making process, but still has not got rid of the idea of photographic chemical imaging. There is still a problem of chemical waste pollution in post-treatment.
  • Ink is used as the core material of inkjet printing direct plate making technology.
  • the inkjet inks reported so far include water-soluble ink solution, thermosetting ink, ultraviolet (UV) curing ink, etc., but the printing yield of the printing plate of the above ink is printed. (force) in 1 to 20,000 copies, the image quality and resolution of printed matter is low, so the development of an environmentally friendly, high-resolution ink is the key to determining the direction of CTP printing.
  • Weak solvent inks are popular solvent inks in recent years. The main reason is that weak solvent inks are not only very low in taste, but also have fine ink particles. The inkjet printing is beautiful. The most important feature of weak solvent inks is environmental friendliness, mainly due to the reduction of volatiles (V0C) and the elimination of many toxic organic solvents (such as cyclohexanone, butanone, etc.) in weak solvent inks. The production workshop no longer requires ventilation. Weak solvent inks are very popular in developed countries, and traditional solvent inks have barely found a market in Europe and the United States.
  • the ink-jet printed images of water-based inks are not easy to dry and absorbed by the media, making them mainly used for paper and Various types of fibers (cloth) are used as substrates and coated media.
  • Screens usually made of aqueous ink are mainly used indoors because of poor weather resistance.
  • the invention combines water and a specific weak solvent as a solvent of the ink, further reduces the toxicity caused by the weak solvent in the ink, and combines the precision and the outdoor weather resistance to prepare an ink with low cost and high environmental performance. Summary of the invention
  • One of the objects of the present invention is to overcome the drawbacks of the existing inkjet CTP method and to solve the limitation of inkjet CTP.
  • the problem of development and application is to provide an environmentally friendly ink for inkjet printing direct plate making technology for inkjet printing direct plate making technology.
  • the ink is printed on the surface of the aluminum plate, and can be plated and produced. Has good printing durability and image resolution.
  • Another object of the present invention is to provide a method of preparing an environmentally friendly ink for direct printing of ink jet printing.
  • the base-aluminum plate base for inkjet printing has a high specific surface energy, and both the inorganic solution and the organic solution can be well spread and wetted on the surface, so that the general inkjet ink is printed on the aluminum plate base.
  • the invention utilizes the high surface energy of the water system, and ensures that the ink system mixed with the weak solvent forms a small spray point and uniform shape during the inkjet printing process (the high surface tension of the ink promotes the droplets during the ink ejection process).
  • the formation and shape are uniform; at the same time, the volatilization and high precision performance of the weak solvent are utilized, and the diffusion of the ink on the surface of the high specific surface energy of the aluminum plate base is effectively reduced, and the image resolution is improved.
  • the environmentally friendly ink for direct printing of inkjet printing of the present invention is prepared from a crosslinkable resin and a mixed solvent, and the ink is printed on an aluminum plate base surface by an inkjet printer to form a printed image and obtain inkjet printing directly.
  • the prepared printing plate forms a high-resolution image after heat curing, and can be directly printed on the machine, which saves the post-processing process and obtains a high-quality inkjet printing plate.
  • the environment-friendly ink for direct printing of inkjet printing and capable of improving image resolution is based on the total amount of ink, and the composition and content of the ink are:
  • the crosslinkable resin is at least one selected from the group consisting of commercially available epoxy resins, phenol resins, polyvinyl alcohol resins and the like. These resins are thermally cured and can only be cured after reaching a certain temperature. There is no cross-linking of the ink during use, which causes the print head of the inkjet printer to clog.
  • the weak solvent is at least one selected from the group consisting of propylene glycol monomethyl ether, propylene glycol monomethyl ether acetate, propylene glycol monomethyl ether propionate, propylene glycol monomethyl ether butyrate, and the like.
  • the conductivity of the deionized water is preferably a conductivity of less than 10 microsiemens/cm.
  • the ink of the present invention is a filtrate obtained by removing insoluble matter and/or impurities in the ink mixture by a multistage filtration method.
  • the preparation method of the environmentally-friendly ink for inkjet printing direct plate making and improving image resolution is as follows:
  • the method comprises: based on the total amount of ink, in terms of mass percentage, 5% to 20% can be Cross-linking resin, 5% to 25% weak solvent and 55% to 90% deionized water are stirred and mixed at room temperature. After the crosslinkable resin is completely dissolved, multi-stage filtration is performed to remove insoluble matter in the mixed solution and/or Impurity, income The filtrate obtained is the ink of the present invention.
  • the multi-stage filtration may use a filter membrane to filter the mixed liquid multiple times, or sequentially filter the mixed liquid with a sand core funnel and a filter membrane, preferably sequentially filtering the mixed liquid with a sand core funnel and a filter membrane, specifically For the purpose of: first removing the insoluble matter and/or impurities in the mixed liquid by using a sand core funnel, and filtering by using a microporous filter to further remove the more insoluble matter and/or impurities in the mixed liquid, and the obtained
  • the filtrate is the ink of the present invention.
  • the filtration is carried out by using a sand core funnel.
  • the preferred filtration scheme is to first filter the glass sand core funnel (G1 type glass sand core funnel) with a pore diameter of 20-30 micrometers, and then use the glass sand with a pore diameter of 3 - 4 micrometers.
  • the core funnel (G4 glass core funnel) was filtered.
  • the PTFE microporous microporous membrane having a pore size of 0.22 micrometers is firstly filtered by using a polytetrafluoroethylene microporous membrane having a pore diameter of 0.45 micrometers. The pore filter was filtered.
  • the crosslinkable resin in the ink has good amphiphilicity and heat curing property
  • the water has the characteristics of slow volatilization, ensuring that the ink does not easily evaporate and dry
  • the weak solvent has the basic physical properties consistent with the inkjet printer, and basically conforms to the inkjet.
  • the printing ink industry standard QB/T 2730. 1-2005, so that the prepared ink has the characteristics of moderate diffusion performance, high printing plate resolution, good ink oleophilicity, rapid ink application and high printing durability.
  • the ink of the present invention is printed on an aluminum plate base and cured at 150 ° C for 2 minutes to obtain a high-resolution printing plate which can be directly printed on the machine without any other chemical treatment.
  • the ink of the present invention is used in a computer direct inkjet printing plate CTP7600 plate making system (for example, refer to Chinese invention patent application 200510132248. 4 (CN1800982A), invention name: a CTP direct plate making method and apparatus using the principle of inkjet imaging),
  • the obtained printing plate can achieve a dot reproduction rate of over 98% and a resolution higher than 175 LPI.
  • the printing result on the machine proves that the ink is fast, the dot information is full, and the printing durability reaches 50,000 sheets.
  • Fig. 1 is a photomicrograph showing a pattern of ink printed on a surface of an aluminum plate according to Embodiment 1 of the present invention.
  • Fig. 2 is an electron micrograph showing the pattern of the ink printed on the surface of the aluminum plate according to the embodiment 2 of the present invention.
  • the micrograph of the ink printed on the surface of the aluminum plate is patterned using a microscope.
  • the polyvinyl alcohol resin (Beijing Oriental Petrochemical Co., Ltd. organic chemical plant), 5% propylene glycol monomethyl ether and 90% deionized water (conductivity less than 10 microsiemens/cm)
  • the mixture was stirred and stirred at room temperature, and after the polyvinyl alcohol resin was completely dissolved, the insoluble matter and/or impurities in the solution were removed by filtration using a filter for several times, and the obtained filtrate was the ink.
  • the ink prepared by the above is used in a computer direct inkjet printing plate CTP7600 plate making system (refer to the Chinese invention patent CN: 200510132248. 4, the invention name: a CTP direct plate making method and equipment using the principle of inkjet imaging),
  • the resulting printing plate can achieve a dot reproduction rate of over 98% and a resolution higher than 175 LPI, and the printing durability reaches 50,000 sheets. Under the microscope observation, it was shown that the obtained printing plate consisted of microscopic ink dots, as shown in Fig. 1.
  • Example 2 Example 2
  • the phenolic resin (Tangshan Jinsha Chemical Co., Ltd.), 25% of propylene glycol monomethyl ether and 55% of deionized water (conductivity less than 10 microsiemens/cm) constituting 20% of the total mass of the ink were stirred and mixed at room temperature. After all the phenol resin is dissolved, the insoluble matter and/or impurities in the solution are removed by filtration through a filter for a plurality of times, and the obtained filtrate is the ink.
  • the ink prepared by the above is used in a computer direct inkjet printing plate CTP7600 plate making system (refer to the Chinese invention patent CN: 200510132248. 4, the invention name: a CTP direct plate making method and equipment using the principle of inkjet imaging),
  • the resulting printing plate can achieve a dot reproduction rate of over 98% and a resolution higher than 175 LPI, and the printing durability reaches 50,000 sheets.
  • the ink dots of the obtained printing plate are as shown in Fig. 2.
  • the phenolic resin, 15% of propylene glycol monomethyl ether and 75% of deionized water (conductivity less than 10 microsiemens/cm) constituting 10% of the total mass of the ink are stirred and mixed at room temperature, and are further dissolved after the phenolic resin is completely dissolved.
  • the insoluble matter and/or impurities in the solution are removed by filtration, and the obtained filtrate is the ink.
  • the microporous filter is a glass sand core funnel (G1 type glass sand core funnel) having a pore size of 20 ⁇ m, a glass sand core funnel having a pore size of 3 ⁇ m (G4 type glass core funnel), and a pore diameter of 0.45 ⁇ m.
  • the polytetrafluoroethylene microporous membrane and the polytetrafluoroethylene microporous membrane having a pore size of 0.22 micrometers were filtered.
  • Epoxy resin (Shanghai Lujia Waterborne Coating Co., Ltd.), which constitutes 10% of the total ink quality, 15% Propylene glycol monomethyl ether acetate and 75% deionized water (conductivity less than 10 microsiemens/cm) are stirred and mixed at room temperature. After all the epoxy resin is dissolved, multi-stage filtration is performed to remove insolubles from the solution and/or Impurities, the resulting filtrate is the ink.
  • the multi-stage filtration is a glass sand core funnel (G1 type glass core funnel) having a pore size of 30 ⁇ m, a glass sand core funnel having a pore diameter of 4 ⁇ m (G4 type glass core funnel), and a pore diameter of 0.45 ⁇ m.
  • the polytetrafluoroethylene microporous membrane and the polytetrafluoroethylene microporous membrane having a pore size of 0.22 micrometers were filtered.
  • the microporous filter is a glass sand core funnel (G1 type glass core funnel) having a pore size of 25 ⁇ m, a glass sand core funnel having a pore size of 3 ⁇ m (G4 type glass core funnel), and a pore diameter of 0.45 ⁇ m.
  • the polytetrafluoroethylene microporous membrane and the polytetrafluoroethylene microporous membrane having a pore size of 0.22 micrometers were filtered.
  • a mixture of a polyvinyl alcohol resin and a phenolic resin (a mass ratio of a polyvinyl alcohol resin to a phenol resin of 1:1) constituting 15% of the total mass of the ink, 25% of propylene glycol monomethyl ether, and 60% of deionized water (conductance) The ratio is less than 10 microsiemens/cm) and the mixture is stirred at room temperature. After the polyvinyl alcohol resin and the phenol resin are all dissolved, the insoluble matter and/or impurities in the solution are removed by multistage filtration, and the obtained filtrate is the ink.
  • the multi-stage filtration is a glass sand core funnel (G1 type glass sand core funnel) having a pore diameter of 27 ⁇ m, a glass sand core funnel (G4 type glass sand core funnel) having a pore diameter of 3.5 ⁇ m, and a pore diameter of 0.
  • G1 type glass sand core funnel having a pore diameter of 27 ⁇ m
  • G4 type glass sand core funnel having a pore diameter of 3.5 ⁇ m
  • a 45 micron polytetrafluoroethylene microporous membrane and a polytetrafluoroethylene microporous membrane having a pore size of 0.22 micrometers were filtered.
  • a mixture of a polyvinyl alcohol resin and a phenolic resin (a mass ratio of a polyvinyl alcohol resin to a phenol resin of 2:1) constituting 10% of the total mass of the ink, 25% of propylene glycol monomethyl ether, and 65% of deionized water (conductance) The ratio is less than 10 microsiemens/cm) and the mixture is stirred at room temperature. After the polyvinyl alcohol resin and the phenol resin are all dissolved, the insoluble matter and/or impurities in the solution are removed by multistage filtration, and the obtained filtrate is the ink.
  • the microporous filter is a glass sand core funnel (G1 type glass sand core funnel) having a pore size of 22 ⁇ m, a glass sand core funnel having a pore size of 3 ⁇ m (G4 type glass core funnel), and a pore diameter of 0.45 ⁇ m.
  • the polytetrafluoroethylene microporous membrane and the polytetrafluoroethylene microporous membrane having a pore size of 0.22 micrometers were filtered.
  • Example 8 Phenolic resin, 15% propylene glycol monomethyl ether acetate and 70% deionized water (conductivity less than 10 microsiemens/cm) constituting 15% of the total mass of the ink are stirred and mixed at room temperature, after all the phenolic resin is dissolved. The insoluble matter and/or impurities in the solution are removed by multistage filtration, and the obtained filtrate is the ink.
  • the microporous filter is a glass sand core funnel (G1 type glass core funnel) having a pore size of 25 ⁇ m, a glass sand core funnel having a pore size of 3 ⁇ m (G4 type glass core funnel), and a pore diameter of 0.45 ⁇ m.
  • the polytetrafluoroethylene microporous membrane and the polytetrafluoroethylene microporous membrane having a pore size of 0.22 micrometers were filtered.
  • the phenolic resin constituting 20% of the total mass of the ink, 15% of propylene glycol monomethyl ether propionate and 65% of deionized water (conductivity less than 10 microsiemens/cm) are stirred and mixed at room temperature until the phenolic resin is completely dissolved. Thereafter, multi-stage filtration is performed to remove insolubles and/or impurities in the solution, and the obtained filtrate is the ink.
  • the microporous filter is a glass sand core funnel (G1 type glass core funnel) having a pore size of 25 ⁇ m, a glass sand core funnel having a pore size of 3 ⁇ m (G4 type glass core funnel), and a pore diameter of 0.45 ⁇ m.
  • the polytetrafluoroethylene microporous membrane and the polytetrafluoroethylene microporous membrane having a pore size of 0.22 micrometers were filtered.
  • the phenolic resin constituting 20% of the total mass of the ink, 25% of propylene glycol monomethyl ether butyrate and 55% of deionized water (conductivity less than 10 microsiemens/cm) are stirred and mixed at room temperature until all the phenolic resin is dissolved. Thereafter, multi-stage filtration is performed to remove insolubles and/or impurities in the solution, and the obtained filtrate is the ink.
  • the microporous filter is a glass sand core funnel (G1 type glass core funnel) having a pore size of 25 ⁇ m, a glass sand core funnel having a pore size of 3 ⁇ m (G4 type glass core funnel), and a pore diameter of 0.45 ⁇ m.
  • the polytetrafluoroethylene microporous membrane and the polytetrafluoroethylene microporous membrane having a pore size of 0.22 micrometers were filtered.
  • Epoxy resin, 15% propylene glycol monomethyl ether propionate and 70% deionized water (conductivity less than 10 microsiemens/cm) constituting 15% of the total mass of the ink are stirred and mixed at room temperature until epoxy resin After all the dissolution, the insoluble matter and/or impurities in the solution are removed by multistage filtration, and the obtained filtrate is the ink.
  • the microporous filter is a glass sand core funnel (G1 type glass core funnel) having a pore size of 25 ⁇ m, a glass sand core funnel having a pore size of 3 ⁇ m (G4 type glass core funnel), and a pore diameter of 0.45 ⁇ m.
  • the polytetrafluoroethylene microporous membrane and the polytetrafluoroethylene microporous membrane having a pore size of 0.22 micrometers were filtered.
  • Epoxy resin, 25% propylene glycol monomethyl ether butyrate and 55% deionized water (conductivity less than 10 microsiemens/cm) constituting 20% of the total mass of the ink are stirred and mixed at room temperature until epoxy resin All dissolved After the solution, the insoluble matter and/or impurities in the solution are removed by multistage filtration, and the obtained filtrate is the ink.
  • the microporous filter is a glass sand core funnel (G1 type glass core funnel) having a pore size of 25 ⁇ m, a glass sand core funnel having a pore size of 3 ⁇ m (G4 type glass core funnel), and a pore diameter of 0.45 ⁇ m.
  • the polytetrafluoroethylene microporous membrane and the polytetrafluoroethylene microporous membrane having a pore size of 0.22 micrometers were filtered.
  • the microporous filter is a glass sand core funnel (G1 type glass core funnel) having a pore size of 25 ⁇ m, a glass sand core funnel having a pore size of 3 ⁇ m (G4 type glass core funnel), and a pore diameter of 0.45 ⁇ m.
  • the polytetrafluoroethylene microporous membrane and the polytetrafluoroethylene microporous membrane having a pore size of 0.22 micrometers were filtered.
  • a mixture of phenolic resin, 25% propylene glycol monomethyl ether and propylene glycol monomethyl ether propionate (the mass ratio of propylene glycol monomethyl ether to propylene glycol monomethyl ether propionate is 1:1) 65% of deionized water (conductivity less than 10 microsiemens/cm) is stirred and mixed at room temperature. After all the phenolic resin is dissolved, multi-stage filtration is performed to remove insolubles and/or impurities in the solution, and the obtained filtrate is as described. Ink.
  • the microporous filter is a glass sand core funnel (G1 type glass core funnel) having a pore size of 25 ⁇ m, a glass sand core funnel having a pore size of 3 ⁇ m (G4 type glass core funnel), and a pore diameter of 0.45 ⁇ m.
  • the polytetrafluoroethylene microporous membrane and the polytetrafluoroethylene microporous membrane having a pore size of 0.22 micrometers were filtered.
  • a mixture of phenolic resin, 20% propylene glycol monomethyl ether and propylene glycol monomethyl ether butyrate (the mass ratio of propylene glycol monomethyl ether to propylene glycol monomethyl ether butyrate is 1:1) and 65% of deionized water (conductivity less than 10 microsiemens/cm) is stirred and mixed at room temperature. After all the phenolic resin is dissolved, multi-stage filtration is performed to remove insolubles and/or impurities in the solution, and the obtained filtrate is as described. Ink.
  • the microporous filter is a glass sand core funnel (G1 type glass core funnel) having a pore size of 25 ⁇ m, a glass sand core funnel having a pore size of 3 ⁇ m (G4 type glass core funnel), and a pore diameter of 0.45 ⁇ m.
  • the polytetrafluoroethylene microporous membrane and the polytetrafluoroethylene microporous membrane having a pore size of 0.22 micrometers were filtered.
  • the microporous filter is a glass sand core funnel (G1 type glass core funnel) having a pore size of 25 ⁇ m, a glass sand core funnel having a pore size of 3 ⁇ m (G4 type glass core funnel), and a pore diameter of 0.45 ⁇ m.
  • the polytetrafluoroethylene microporous membrane and the polytetrafluoroethylene microporous membrane having a pore size of 0.22 micrometers were filtered.
  • the microporous filter is a glass sand core funnel (G1 type glass core funnel) having a pore size of 25 ⁇ m, a glass sand core funnel having a pore size of 3 ⁇ m (G4 type glass core funnel), and a pore diameter of 0.45 ⁇ m.
  • the polytetrafluoroethylene microporous membrane and the polytetrafluoroethylene microporous membrane having a pore size of 0.22 micrometers were filtered.
  • a phenolic resin constituting 15% of the total mass of the ink
  • a mixture of propylene glycol monomethyl ether, propylene glycol monomethyl ether acetate and propylene glycol monomethyl ether butyrate constituting 20% of the total mass of the ink
  • Acetate The mass ratio of propylene glycol monomethyl ether butyrate is 1:1:2), and the deionized water (conductivity is less than 10 microsiemens/cm) which constitutes 65% of the total mass of the ink is stirred and mixed at room temperature.
  • the microporous filter is a glass sand core funnel (G1 type glass core funnel) having a pore size of 25 ⁇ m, a glass sand core funnel having a pore size of 3 ⁇ m (G4 type glass core funnel), and a pore diameter of 0.45 ⁇ m.
  • the polytetrafluoroethylene microporous membrane and the polytetrafluoroethylene microporous membrane having a pore size of 0.22 micrometers were filtered.

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Inks, Pencil-Leads, Or Crayons (AREA)
  • Ink Jet Recording Methods And Recording Media Thereof (AREA)
  • Ink Jet (AREA)

Description

用于喷墨直接制版的墨水及其制备方法
技术领域
本发明属于墨水领域，涉及提高图像分辨率的环保型墨水， 更具体涉及可用 于喷墨打印直接制版技术（CTP) 的喷墨打印直接制版的环保型墨水及其制备方 法。 背景技术
近年来代表国际先进印刷制版发展方向的 CTP 技术省略了传统的感光成像 过程， 简化了制版工序， 但仍未摆脱感光化学成像的思路， 后处理仍存在化学废 液污染问题。随着国际上很多强制性环保标准的出台， 环保型直接制版技术的研 究已成为世界印刷前沿领域新的热点。墨水作为喷墨打印直接制版技术的核心材 料， 目前报道的喷墨墨水包括水溶性墨水溶液、 热固油墨、 紫外光 (UV)固化油墨 等， 但上述墨水所制印版的印刷品的耐印量（力）在 1〜2万份， 印刷品的成像 质量和分辨率低， 因此发展一种环保、高分辨率的墨水是决定 CTP印刷制版方向 的关键。
弱溶剂墨水是近年来很受欢迎的溶剂墨水，主要原因是弱溶剂墨水不但味道 很低而且墨水颗粒很细， 喷墨打印的画面精美。弱溶剂墨水的最大特点是对环境 的友好性， 主要体现在可挥发物 （V0C ) 的减少和不再采用许多有毒害的有机溶 剂 （比如环己酮、 丁酮等溶剂）， 在弱溶剂墨水的生产车间不再需要通风装置。 弱溶剂墨水在发达国家很受欢迎， 传统溶剂墨水在欧洲和美国几乎找不到市场。 弱溶剂墨水已成为墨水行业发展的必然趋势 [戴斌， 乔旭， 丙二醇醚酯类溶剂的 生产及发展， 安徽化工， 2007， 33， 3， 4-6. ]。 弱溶剂墨水介于水性和溶剂型墨 水之间， 兼顾两者的优点， 具有环保、 高精度和户外耐侯性。 但是由于弱溶剂墨 水的主要成分： 二元醇醚酯类溶剂的生产工艺复杂， 生产流程长， 导致此类溶剂 的市场供应较少， 成本相对较高。 水性墨水的主要特点是成本低廉、 没有污染， 印刷品色彩鲜艳，但是因为其主要组分水的挥发速度慢， 由水性墨水喷墨打印的 画面不易干燥和被介质吸收， 使其主要应用于纸张以及各种纤维类 (布)为底材、 有涂层的介质上。 通常由水性墨水制作的画面因为耐侯性差而主要应用在户内。 本发明通过水与特定弱溶剂混合作为墨水的溶剂，进一步降低墨水中弱溶剂带来 的毒性， 并兼顾精度和户外耐候性， 制备低成本、 高环保性能的墨水。 发明内容
本发明的目的之一在于克服现有喷墨 CTP方法中的缺陷， 解决限制喷墨 CTP 大力发展和应用的问题，从而提供一种用于喷墨打印直接制版技术的喷墨打印直 接制版的环保型墨水， 使用该墨水在铝版基表面上打印， 可进行制版， 制得的印 版具有良好的耐印力和图像分辨率。
本发明的目的之二在于提供用于喷墨打印直接制版的环保型墨水的制备方 法。
用于喷墨打印制备印版的基底一 -铝版基具有高比表面能， 无机溶液和有机 溶液均能在其表面有很好的铺展和浸润，因此一般的喷墨墨水打印到铝版基表面 上形成图文时墨水扩散严重， 图像分辨率相对较低。本发明利用水体系的高表面 能， 能确保水与弱溶剂混合的墨水体系在喷墨打印过程中形成的喷射墨点小， 形 状均一（墨水的表面张力高会促进墨水喷射过程中的液滴形成与形状均一）；同时 利用弱溶剂的挥发和高精度性能，有效降低墨水在铝版基的高比表面能表面上的 扩散， 提高图像分辨率。
本发明的用于喷墨打印直接制版的环保型墨水是由可交联树脂及混合溶剂 制备得到的，将该墨水通过喷墨打印机打印在铝版基表面， 形成打印图像并获得 喷墨打印直接制备的印版， 热固化后形成高分辨率图像， 可直接上机印刷， 节省 了后处理过程， 获得了高质量喷墨打印印版。
本发明的用于喷墨打印直接制版并能提高图像分辨率的环保型墨水，以墨水 的总量为基准， 以质量百分比计， 该墨水的组分及含量为：
可交联树脂 5 %〜20 %
弱溶剂 5 %〜25 %
去离子水 55 %〜90 %
所述的可交联树脂选自市售的环氧树脂、酚醛树脂、聚乙烯醇树脂等所组成 的组中的至少一种。这些树脂存在热固化方式，只能在达到一定温度后才能固化， 不会出现在使用过程中墨水交联而造成喷墨打印机的打印喷头堵塞。
所述的弱溶剂选自丙二醇单甲醚、丙二醇单甲醚醋酸酯、丙二醇单甲醚丙酸 酯、 丙二醇单甲醚丁酸酯等所组成的组中的至少一种。
所述的去离子水的电导率优选为电导率低于 10 微西门子 /厘米。
本发明的墨水是通过多级过滤方法除去制备墨水混合液中不溶物和 /或杂质 后得到的滤液。
本发明的用于喷墨打印直接制版并能提高图像分辨率的环保型墨水的制备 方法是： 该方法包括： 以墨水的总量为基准， 以质量百分比计， 将 5 %〜20 %的 可交联树脂、 5 %〜25 %的弱溶剂和 55 %〜90 %的去离子水在室温下搅拌混合， 待可交联树脂全部溶解后进行多级过滤除去混合液中的不溶物和 /或杂质， 所得 到的滤液即为本发明所述的墨水。
所述的多级过滤可采用滤膜对混合液进行多次过滤，或者依次用砂芯漏斗和 滤膜对混合液进行过滤，优选是依次用砂芯漏斗和滤膜对混合液进行过滤， 具体 而言： 先采用砂芯漏斗进行过滤除去混合液中的不溶物和 /或杂质， 再采用微米 孔径的滤膜进行过滤进一步除去混合液中的更微小的不溶物和 /或杂质， 所得到 的滤液即为本发明所述的墨水。
所述的采用砂芯漏斗进行过滤， 优选过滤方案为先采用孔径为 20-30 微米 的玻璃砂芯漏斗 （G1型玻璃砂芯漏斗） 进行过滤后， 再采用孔径为 3 - 4 微米 的玻璃砂芯漏斗 （G4型玻璃砂芯漏斗） 进行过滤。
所述的采用微米孔径的滤膜进行过滤， 优选方案为先采用孔径为 0. 45 微米 的聚四氟乙烯微孔滤膜进行过滤后， 再采用孔径为 0. 22 微米的聚四氟乙烯微孔 滤膜进行过滤。
由于所述墨水中可交联树脂具有良好的双亲性和热固化性能， 水具有挥发 慢的特点，保证了墨水不容易挥发干涸， 弱溶剂具有符合喷墨打印机的基本物理 性能， 基本符合喷墨打印墨水行业标准 (QB/T 2730. 1-2005)， 从而所制备的墨水 具有扩散性能适中、印版分辨率高、墨迹亲油性好、上墨迅速和耐印力高的性能。
本发明的墨水打印到铝版基上， 在 150 °C下固化 2分钟， 即得到高分辨率 可直接上机印刷的印版， 不需其它化学处理。
本发明的墨水在计算机直接喷墨打印制版 CTP7600制版系统 （如可参考中 国发明专利申请 200510132248. 4 (CN1800982A), 发明名称： 一种利用喷墨成像 原理的 CTP直接制版方法和设备） 中使用， 所制得的印版能够达到 98%以上的网 点再现率和高于 175 LPI的分辨率， 上机印刷结果证明上墨快， 网点信息全， 耐 印力达到五万印张。 附图说明
图 1为本发明实施例 1的墨水在铝版基表面打印形成图案的显微镜照片。 图 2为本发明实施例 2的墨水在铝版基表面打印形成图案的电镜照片。 具体实施方式
以下实施例中墨水在铝版基表面打印形成图案的显微镜照片采用显微镜
(Olympus BX51 正置显微镜）及连接到显微镜上的图像传感器 CCD (中国， 唯 视图像有限公司 MicroVision MV-VS 078FC)进行观察和图像记录。 墨水在铝版 基表面打印形成图案的电镜照片采用场发射电子显微镜观察， （日本， JEOL JSM-6700) o 实施例 1
将构成墨水总质量 5%的聚乙烯醇树脂 （北京东方石油化工有限公司有机化 工厂）、 5%的丙二醇单甲醚及 90%的去离子水 （电导率低于 10 微西门子 /厘米） 在室温下搅拌混合，待聚乙烯醇树脂全部溶解后利用滤膜进行多次过滤除去溶液 中的不溶物和 /或杂质， 得到的滤液为所述的墨水。
取上述制备得到的墨水在计算机直接喷墨打印制版 CTP7600制版系统 （具 体可参考中国发明专利 CN: 200510132248. 4, 发明名称： 一种利用喷墨成像原 理的 CTP直接制版方法和设备）中使用，所制得的印版能够达到 98%以上的网点 再现率和高于 175 LPI的分辨率， 耐印力达到五万印张。 在显微镜观察下， 显示 所制得的印版由微观墨点组成， 如图 1所示。 实施例 2
将构成墨水总质量 20%的酚醛树脂 （唐山金沙化工有限公司）、 25%的丙二 醇单甲醚及 55%的去离子水（电导率低于 10 微西门子 /厘米)在室温下搅拌混合， 待酚醛树脂全部溶解后利用滤膜进行多次过滤除去溶液中的不溶物和 /或杂质， 得到的滤液为所述的墨水。
取上述制备得到的墨水在计算机直接喷墨打印制版 CTP7600制版系统 （具 体可参考中国发明专利 CN: 200510132248. 4, 发明名称： 一种利用喷墨成像原 理的 CTP直接制版方法和设备）中使用，所制得的印版能够达到 98%以上的网点 再现率和高于 175 LPI的分辨率， 耐印力达到五万印张。 在电子显微镜观察下， 所制得的印版的墨点如图 2所示。 实施例 3
将构成墨水总质量 10%的酚醛树脂、 15%的丙二醇单甲醚及 75%的去离子水 (电导率低于 10 微西门子 /厘米）在室温下搅拌混合， 待酚醛树脂全部溶解后进 行多级过滤除去溶液中的不溶物和 /或杂质， 得到的滤液为所述的墨水。 所述多 级过滤为依次用孔径为 20微米的玻璃砂芯漏斗（G1型玻璃砂芯漏斗）、孔径为 3 微米的玻璃砂芯漏斗 （G4型玻璃砂芯漏斗）、 孔径为 0. 45 微米的聚四氟乙烯微 孔滤膜和孔径为 0. 22 微米的聚四氟乙烯微孔滤膜进行过滤。
实施例 4
将构成墨水总质量 10%的环氧树脂 （上海绿嘉水性涂料有限公司）、 15%的 丙二醇单甲醚醋酸酯及 75%的去离子水（电导率低于 10 微西门子 /厘米）在室温 下搅拌混合， 待环氧树脂全部溶解后进行多级过滤除去溶液中的不溶物和 /或杂 质， 得到的滤液为所述的墨水。 所述多级过滤为依次用孔径为 30微米的玻璃砂 芯漏斗（G1型玻璃砂芯漏斗）、 孔径为 4微米的玻璃砂芯漏斗（G4型玻璃砂芯漏 斗）、孔径为 0. 45 微米的聚四氟乙烯微孔滤膜和孔径为 0. 22 微米的聚四氟乙烯 微孔滤膜进行过滤。 实施例 5
将构成墨水总质量 15%的聚乙烯醇树脂、 15%的丙二醇单甲醚及 70%的去离 子水（电导率低于 10 微西门子 /厘米）在室温下搅拌混合， 待聚乙烯醇树脂全部 溶解后进行多级过滤除去溶液中的不溶物和 /或杂质，得到的滤液为所述的墨水。 所述多级过滤为依次用孔径为 25微米的玻璃砂芯漏斗 （G1型玻璃砂芯漏斗）、 孔径为 3微米的玻璃砂芯漏斗 （G4型玻璃砂芯漏斗）、 孔径为 0. 45 微米的聚四 氟乙烯微孔滤膜和孔径为 0. 22 微米的聚四氟乙烯微孔滤膜进行过滤。 实施例 6
将构成墨水总质量 15%的聚乙烯醇树脂与酚醛树脂的混合物 (聚乙烯醇树脂 与酚醛树脂的质量比为 1:1 )、 25%的丙二醇单甲醚及 60%的去离子水（电导率低 于 10 微西门子 /厘米）在室温下搅拌混合， 待聚乙烯醇树脂与酚醛树脂全部溶解 后进行多级过滤除去溶液中的不溶物和 /或杂质， 得到的滤液为所述的墨水。 所 述多级过滤为依次用孔径为 27微米的玻璃砂芯漏斗 （G1型玻璃砂芯漏斗）、 孔 径为 3. 5微米的玻璃砂芯漏斗 （G4型玻璃砂芯漏斗）、 孔径为 0. 45 微米的聚四 氟乙烯微孔滤膜和孔径为 0. 22 微米的聚四氟乙烯微孔滤膜进行过滤。 实施例 7
将构成墨水总质量 10%的聚乙烯醇树脂与酚醛树脂的混合物（聚乙烯醇树脂 与酚醛树脂的质量比为 2:1 )、 25%的丙二醇单甲醚及 65%的去离子水（电导率低 于 10 微西门子 /厘米）在室温下搅拌混合， 待聚乙烯醇树脂与酚醛树脂全部溶解 后进行多级过滤除去溶液中的不溶物和 /或杂质， 得到的滤液为所述的墨水。 所 述多级过滤为依次用孔径为 22微米的玻璃砂芯漏斗 （G1型玻璃砂芯漏斗）、 孔 径为 3微米的玻璃砂芯漏斗 （G4型玻璃砂芯漏斗）、 孔径为 0. 45 微米的聚四氟 乙烯微孔滤膜和孔径为 0. 22 微米的聚四氟乙烯微孔滤膜进行过滤。 实施例 8 将构成墨水总质量 15%的酚醛树脂、 15%的丙二醇单甲醚醋酸酯及 70%的去 离子水（电导率低于 10 微西门子 /厘米）在室温下搅拌混合， 待酚醛树脂全部溶 解后进行多级过滤除去溶液中的不溶物和 /或杂质， 得到的滤液为所述的墨水。 所述多级过滤为依次用孔径为 25微米的玻璃砂芯漏斗 （G1型玻璃砂芯漏斗）、 孔径为 3微米的玻璃砂芯漏斗 （G4型玻璃砂芯漏斗）、 孔径为 0. 45 微米的聚四 氟乙烯微孔滤膜和孔径为 0. 22 微米的聚四氟乙烯微孔滤膜进行过滤。 实施例 9
将构成墨水总质量 20%的酚醛树脂、 15%的丙二醇单甲醚丙酸酯及 65%的去 离子水（电导率低于 10 微西门子 /厘米）在室温下搅拌混合， 待酚醛树脂全部溶 解后进行多级过滤除去溶液中的不溶物和 /或杂质， 得到的滤液为所述的墨水。 所述多级过滤为依次用孔径为 25微米的玻璃砂芯漏斗 （G1型玻璃砂芯漏斗）、 孔径为 3微米的玻璃砂芯漏斗 （G4型玻璃砂芯漏斗）、 孔径为 0. 45 微米的聚四 氟乙烯微孔滤膜和孔径为 0. 22 微米的聚四氟乙烯微孔滤膜进行过滤。 实施例 10
将构成墨水总质量 20%的酚醛树脂、 25%的丙二醇单甲醚丁酸酯及 55%的去 离子水（电导率低于 10 微西门子 /厘米）在室温下搅拌混合， 待酚醛树脂全部溶 解后进行多级过滤除去溶液中的不溶物和 /或杂质， 得到的滤液为所述的墨水。 所述多级过滤为依次用孔径为 25微米的玻璃砂芯漏斗 （G1型玻璃砂芯漏斗）、 孔径为 3微米的玻璃砂芯漏斗 （G4型玻璃砂芯漏斗）、 孔径为 0. 45 微米的聚四 氟乙烯微孔滤膜和孔径为 0. 22 微米的聚四氟乙烯微孔滤膜进行过滤。 实施例 11
将构成墨水总质量 15%的环氧树脂、 15%的丙二醇单甲醚丙酸酯及 70%的去 离子水（电导率低于 10 微西门子 /厘米）在室温下搅拌混合， 待环氧树脂全部溶 解后进行多级过滤除去溶液中的不溶物和 /或杂质， 得到的滤液为所述的墨水。 所述多级过滤为依次用孔径为 25微米的玻璃砂芯漏斗 （G1型玻璃砂芯漏斗）、 孔径为 3微米的玻璃砂芯漏斗 （G4型玻璃砂芯漏斗）、 孔径为 0. 45 微米的聚四 氟乙烯微孔滤膜和孔径为 0. 22 微米的聚四氟乙烯微孔滤膜进行过滤。 实施例 12
将构成墨水总质量 20%的环氧树脂、 25%的丙二醇单甲醚丁酸酯及 55%的去 离子水（电导率低于 10 微西门子 /厘米）在室温下搅拌混合， 待环氧树脂全部溶 解后进行多级过滤除去溶液中的不溶物和 /或杂质， 得到的滤液为所述的墨水。 所述多级过滤为依次用孔径为 25微米的玻璃砂芯漏斗 （G1型玻璃砂芯漏斗）、 孔径为 3微米的玻璃砂芯漏斗 （G4型玻璃砂芯漏斗）、 孔径为 0. 45 微米的聚四 氟乙烯微孔滤膜和孔径为 0. 22 微米的聚四氟乙烯微孔滤膜进行过滤。 实施例 13
将构成墨水总质量 10%的环氧树脂、 25%的丙二醇单甲醚与丙二醇单甲醚醋 酸酯的混合物 （丙二醇单甲醚与丙二醇单甲醚醋酸酯的质量比为 1:1 ) 及 65%的 去离子水（电导率低于 10 微西门子 /厘米）在室温下搅拌混合， 待环氧树脂全部 溶解后进行多级过滤除去溶液中的不溶物和 /或杂质，得到的滤液为所述的墨水。 所述多级过滤为依次用孔径为 25微米的玻璃砂芯漏斗 （G1型玻璃砂芯漏斗）、 孔径为 3微米的玻璃砂芯漏斗 （G4型玻璃砂芯漏斗）、 孔径为 0. 45 微米的聚四 氟乙烯微孔滤膜和孔径为 0. 22 微米的聚四氟乙烯微孔滤膜进行过滤。 实施例 14
将构成墨水总质量 10%的酚醛树脂、 25%的丙二醇单甲醚与丙二醇单甲醚丙 酸酯的混合物 （丙二醇单甲醚与丙二醇单甲醚丙酸酯的质量比为 1:1 ) 及 65%的 去离子水（电导率低于 10 微西门子 /厘米）在室温下搅拌混合， 待酚醛树脂全部 溶解后进行多级过滤除去溶液中的不溶物和 /或杂质，得到的滤液为所述的墨水。 所述多级过滤为依次用孔径为 25微米的玻璃砂芯漏斗 （G1型玻璃砂芯漏斗）、 孔径为 3微米的玻璃砂芯漏斗 （G4型玻璃砂芯漏斗）、 孔径为 0. 45 微米的聚四 氟乙烯微孔滤膜和孔径为 0. 22 微米的聚四氟乙烯微孔滤膜进行过滤。 实施例 15
将构成墨水总质量 15%的酚醛树脂、 20%的丙二醇单甲醚与丙二醇单甲醚丁 酸酯的混合物 （丙二醇单甲醚与丙二醇单甲醚丁酸酯的质量比为 1:1 ) 及 65%的 去离子水（电导率低于 10 微西门子 /厘米）在室温下搅拌混合， 待酚醛树脂全部 溶解后进行多级过滤除去溶液中的不溶物和 /或杂质，得到的滤液为所述的墨水。 所述多级过滤为依次用孔径为 25微米的玻璃砂芯漏斗 （G1型玻璃砂芯漏斗）、 孔径为 3微米的玻璃砂芯漏斗 （G4型玻璃砂芯漏斗）、 孔径为 0. 45 微米的聚四 氟乙烯微孔滤膜和孔径为 0. 22 微米的聚四氟乙烯微孔滤膜进行过滤。 实施例 16
将构成墨水总质量 10%的环氧树脂、 25%的丙二醇单甲醚醋酸酯与丙二醇单 甲醚丙酸酯的混合物 （丙二醇单甲醚醋酸酯与丙二醇单甲醚丙酸酯的质量比为
1:2) 及 65%的去离子水 （电导率低于 10 微西门子 /厘米） 在室温下搅拌混合， 待环氧树脂全部溶解后进行多级过滤除去溶液中的不溶物和 /或杂质， 得到的滤 液为所述的墨水。 所述多级过滤为依次用孔径为 25微米的玻璃砂芯漏斗 （G1型 玻璃砂芯漏斗）、 孔径为 3微米的玻璃砂芯漏斗 （G4型玻璃砂芯漏斗）、 孔径为 0. 45 微米的聚四氟乙烯微孔滤膜和孔径为 0. 22 微米的聚四氟乙烯微孔滤膜进 行过滤。 实施例 17
将构成墨水总质量 15%的酚醛树脂、 25%的丙二醇单甲醚醋酸酯与丙二醇单 甲醚丁酸酯的混合物 （丙二醇单甲醚醋酸酯与丙二醇单甲醚丁酸酯的质量比为 2:1 ) 及 60%的去离子水 （电导率低于 10 微西门子 /厘米） 在室温下搅拌混合， 待酚醛树脂全部溶解后进行多级过滤除去溶液中的不溶物和 /或杂质， 得到的滤 液为所述的墨水。 所述多级过滤为依次用孔径为 25微米的玻璃砂芯漏斗 （G1型 玻璃砂芯漏斗）、 孔径为 3微米的玻璃砂芯漏斗 （G4型玻璃砂芯漏斗）、 孔径为 0. 45 微米的聚四氟乙烯微孔滤膜和孔径为 0. 22 微米的聚四氟乙烯微孔滤膜进 行过滤。 实施例 18
将构成墨水总质量 15%的酚醛树脂， 及构成墨水总质量 20%的丙二醇单甲 醚、 丙二醇单甲醚醋酸酯与丙二醇单甲醚丁酸酯的混合物（丙二醇单甲醚： 丙二 醇单甲醚醋酸酯： 丙二醇单甲醚丁酸酯的质量比为 1:1:2)， 和构成墨水总质量的 65%的去离子水 （电导率低于 10 微西门子 /厘米）在室温下搅拌混合， 待酚醛树 脂全部溶解后进行多级过滤除去溶液中的不溶物和 /或杂质， 得到的滤液为所述 的墨水。 所述多级过滤为依次用孔径为 25微米的玻璃砂芯漏斗 （G1型玻璃砂芯 漏斗）、 孔径为 3微米的玻璃砂芯漏斗（G4型玻璃砂芯漏斗）、 孔径为 0. 45 微米 的聚四氟乙烯微孔滤膜和孔径为 0. 22 微米的聚四氟乙烯微孔滤膜进行过滤。

Claims

权利要求书
1.一种用于喷墨打印直接制版的环保型墨水，其特征是， 以墨水的总量为基 准， 以质量百分比计， 该墨水的组分及含量为：
可交联树脂 5 %〜20 %
弱溶剂 5 %〜25 %
去离子水 55 %〜90 %
所述的可交联树脂选自环氧树脂、酚醛树脂和聚乙烯醇树脂所组成的组中的 至少一种；
所述的弱溶剂选自丙二醇单甲醚、丙二醇单甲醚醋酸酯、丙二醇单甲醚丙酸 酯和丙二醇单甲醚丁酸酯所组成的组中的至少一种。
2.根据权利要求 1所述的用于喷墨打印直接制版的环保型墨水， 其特征是： 所述的去离子水的电导率低于 10 微西门子 /厘米。
3.—种根据权利要求 1或 2所述的用于喷墨打印直接制版的环保型墨水的制 备方法， 其特征是， 该方法包括： 以墨水的总量为基准， 以质量百分比计， 将 5 %〜20 %的可交联树脂、 5 %〜25 %的弱溶剂和 55 %〜90 %的去离子水在室温下 搅拌混合， 待可交联树脂全部溶解后进行多级过滤除去混合液中的不溶物和 /或 杂质， 所得到的滤液即为所述的墨水；
所述的可交联树脂选自环氧树脂、酚醛树脂和聚乙烯醇树脂所组成的组中的 至少一种；
所述的弱溶剂选自丙二醇单甲醚、丙二醇单甲醚醋酸酯、丙二醇单甲醚丙酸 酯和丙二醇单甲醚丁酸酯所组成的组中的至少一种。
4.根据权利要求 3所述的制备方法，其特征是： 所述的去离子水的电导率低 于 10 微西门子 /厘米。
5、 根据权利要求 3所述的制备方法， 其特征是： 所述多级过滤是依次用砂 芯漏斗和滤膜对混合液进行过滤。
6、 根据权利要求 5所述的制备方法， 其特征是： 所述滤膜是微米孔径的滤
PCT/CN2010/078063 2010-08-06 2010-10-25 用于喷墨直接制版的墨水及其制备方法 WO2012016397A1 (zh)

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Families Citing this family (6)

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CN104668575B (zh) 2014-12-02 2019-01-04 中国科学院化学研究所 一种可分散于弱溶剂中的纳米银粉及其制备导电油墨的应用
US9796191B2 (en) 2015-03-20 2017-10-24 Corning Incorporated Method of inkjet printing decorations on substrates
CN104845444A (zh) * 2015-04-25 2015-08-19 桐城运城制版有限公司 一种环保油墨
CN106336733B (zh) * 2015-07-13 2019-12-10 中国科学院化学研究所 一种喷墨打印直接制版用的水基墨水控制液及其制备方法
CN106915169A (zh) * 2015-12-25 2017-07-04 康宁股份有限公司 在基板上喷墨印刷装饰的方法
GB2581894B (en) 2017-10-16 2022-07-13 Videojet Technologies Inc A continuous inkjet ink composition

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001034394A1 (en) * 1999-11-07 2001-05-17 Aprion Digital Ltd A fluid for preparation of printing plates and method for use of same
CN1324901A (zh) * 2000-05-22 2001-12-05 伊利诺斯器械工程公司 新型喷墨油墨和印刷方法
WO2002094571A1 (en) * 2001-05-18 2002-11-28 Kodak Polychrome Graphics, L.L.C. A method of preparing an inkjet ink imaged lithographic printing plate
CN1800982A (zh) 2005-12-27 2006-07-12 中国科学院化学研究所 一种利用喷墨成像原理的ctp直接制版方法和设备
JP2009249578A (ja) * 2008-04-09 2009-10-29 Mimaki Engineering Co Ltd インク組成物

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4959661A (en) * 1989-09-28 1990-09-25 Olin Hunt Specialty Products Inc. Ink-jet printing process
US5156675A (en) * 1991-05-16 1992-10-20 Xerox Corporation Ink for ink jet printing
JPH08324145A (ja) 1995-05-29 1996-12-10 Nikken Kagaku Kenkyusho:Kk 直描型平版印刷版
JP2007276442A (ja) 2005-09-30 2007-10-25 Fujifilm Corp 直描型平版印刷版用原版及び直描型平版印刷版
CN100509970C (zh) * 2005-12-27 2009-07-08 中国科学院化学研究所 一种用于喷墨ctp制版技术的纳米颜料墨水
JPWO2008007550A1 (ja) * 2006-07-14 2009-12-10 コニカミノルタホールディングス株式会社 製版方法及び平版印刷版
JP2008075017A (ja) * 2006-09-22 2008-04-03 Fujifilm Corp インク組成物および平版印刷版の作製方法
JP2009114358A (ja) * 2007-11-07 2009-05-28 Sakata Corp Ｃｔｐ版用オフセット印刷インキ組成物
JP5187398B2 (ja) 2008-08-19 2013-04-24 コニカミノルタホールディングス株式会社 インクジェット製版方法
CN101418157A (zh) * 2008-12-11 2009-04-29 中国科学院化学研究所 喷墨打印计算机直接制版用纳米颜料墨水及其制备方法

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001034394A1 (en) * 1999-11-07 2001-05-17 Aprion Digital Ltd A fluid for preparation of printing plates and method for use of same
CN1324901A (zh) * 2000-05-22 2001-12-05 伊利诺斯器械工程公司 新型喷墨油墨和印刷方法
WO2002094571A1 (en) * 2001-05-18 2002-11-28 Kodak Polychrome Graphics, L.L.C. A method of preparing an inkjet ink imaged lithographic printing plate
CN1800982A (zh) 2005-12-27 2006-07-12 中国科学院化学研究所 一种利用喷墨成像原理的ctp直接制版方法和设备
JP2009249578A (ja) * 2008-04-09 2009-10-29 Mimaki Engineering Co Ltd インク組成物

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
DAI BIN; QIAO XU: "Production and Development of Propylene Glycol Ether Ester Series Solvents", ANHUI CHEMICAL INDUSTRY, vol. 33, no. 3, 2007, pages 4 - 6
See also references of EP2592121A4 *

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