WO2007134499A1 - Graft copolymer, process of preparation and use thereof, colorant release agent and articles thereof - Google Patents

Graft copolymer, process of preparation and use thereof, colorant release agent and articles thereof Download PDF

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Publication number
WO2007134499A1
WO2007134499A1 PCT/CN2006/003486 CN2006003486W WO2007134499A1 WO 2007134499 A1 WO2007134499 A1 WO 2007134499A1 CN 2006003486 W CN2006003486 W CN 2006003486W WO 2007134499 A1 WO2007134499 A1 WO 2007134499A1
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Prior art keywords
styrene
acrylic acid
graft copolymer
starch
poly
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PCT/CN2006/003486
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French (fr)
Chinese (zh)
Inventor
Powen Chung
Original Assignee
Shanghai Difang Textile Technological Flocking Co., Ltd.
Shanghai Newtech Fabric Printing Co., Ltd.
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Application filed by Shanghai Difang Textile Technological Flocking Co., Ltd., Shanghai Newtech Fabric Printing Co., Ltd. filed Critical Shanghai Difang Textile Technological Flocking Co., Ltd.
Publication of WO2007134499A1 publication Critical patent/WO2007134499A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B41PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
    • B41MPRINTING, DUPLICATING, MARKING, OR COPYING PROCESSES; COLOUR PRINTING
    • B41M5/00Duplicating or marking methods; Sheet materials for use therein
    • B41M5/025Duplicating or marking methods; Sheet materials for use therein by transferring ink from the master sheet
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B41PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
    • B41MPRINTING, DUPLICATING, MARKING, OR COPYING PROCESSES; COLOUR PRINTING
    • B41M5/00Duplicating or marking methods; Sheet materials for use therein
    • B41M5/025Duplicating or marking methods; Sheet materials for use therein by transferring ink from the master sheet
    • B41M5/03Duplicating or marking methods; Sheet materials for use therein by transferring ink from the master sheet by pressure
    • 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
    • C08F251/00Macromolecular compounds obtained by polymerising monomers on to polysaccharides or derivatives thereof
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06PDYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
    • D06P5/00Other features in dyeing or printing textiles, or dyeing leather, furs, or solid macromolecular substances in any form
    • D06P5/003Transfer printing

Definitions

  • This invention relates to the technical field of pigment release agents used in the transfer printing process in the textile printing and dyeing industry.
  • the present invention relates to a novel poly[acrylic acid (styrene)-starch graft copolymer paste used in a pigment release agent for cold transfer printing paper (ie, a dye release agent) and preparation thereof
  • a pigment release agent comprising the above graft copolymer and an article having a coating formed from the pigment release agent, such as a cold transfer printing paper.
  • the cold transfer printing paper with the separation layer prepared by the pigment spacer coating coating according to the present invention can be applied to natural fiber fabrics such as cellulose fibers, wool, cotton, silk, etc., and can also be used for polyester, nylon, Acrylic fiber and other synthetic fabrics. Background technique
  • Transfer printing (hereinafter sometimes referred to as "transfer") has become a new method of industrial decoration and textile printing.
  • the method comprises the following steps: printing a suitable dye ink on a special paper by printing to print a pattern or text to be printed, and printing the dyed side of the transfer paper with the printed fabric.
  • the film is transferred to the fabric by pressure and wetting to dissolve the dye oil from the paper.
  • the transfer printing method can be classified into a dry transfer method, that is, a thermal transfer type and a pressure sensitive transfer type, and a wet transfer method, that is, a cold transfer peeling method and a solvent transfer peeling type.
  • a dry transfer method that is, a thermal transfer type and a pressure sensitive transfer type
  • a wet transfer method that is, a cold transfer peeling method and a solvent transfer peeling type.
  • the earliest transfer printing process was a sublimation hot melt transfer printing as one of the thermal transfer methods.
  • the transfer rate of the ink, the printed color is transmitted through or through the release layer.
  • the thin film is in contact with the paper base and the amount of peeling is insufficient.
  • the peeling film is excessively hydrophobic. Due to the wet transfer of the water-based dye, the excessive hydrophobicity of the peeling film causes the substrate to be inconsistent with the surface tension of the paper. The integrity and clarity of the printed pattern; 3. Back-sticking and blocking, the ink does not stick and re-stick after a short period of film formation, but when the film is unloaded after printing, it is found that the back side of the paper is stuck to the front side, resulting in Serious problem of wetness in the surface; 4.
  • the present invention is directed to the limitations of the transfer layer or the release layer of the conventional transfer printing ink.
  • a new poly(acrylic acid ester-styrene)-starch graft copolymer and a pigment release agent for cold transfer printing paper containing the graft copolymer, having a separation layer made by using the pigment release agent The cold transfer printing paper used in the cold transfer printing process can isolate the penetration of the ink into the paper and improve the ink transfer rate; has the proper hydrophobicity and hydrophilic printability, ensures the complete printing of the substrate, and makes the printed pattern complete and clear; Produces the problem of wet inside the surface; has a good pH adaptation range; the dye pattern is well adhered, and no color fading occurs.
  • the invention promotes the further development of the printing and dyeing industry towards the environmentally friendly economy.
  • One aspect of the present invention is to provide a novel poly[acrylic acid]-styrene]-starch graft copolymer.
  • a second aspect of the present invention provides a process for producing the above poly(acrylic acid)-starch graft copolymer.
  • the three aspects of the present invention are the use of the above-described graft copolymer which can be used to prepare a novel pigment release agent for cold transfer printing paper.
  • the cold transfer printing paper with the separation layer prepared by coating with the pigment isolating agent can be applied to natural fiber fabrics such as cellulose fibers, wool, cotton, silk, etc., and can also be used for synthetic fibers such as polyester, nylon, acrylic and the like. On the fabric, a clear, brightly printed product is produced.
  • a dye separating agent comprising the above graft copolymer.
  • a fifth aspect of the invention relates to an article having a coating formed of the above-described pigment release agent, such as a cold transfer printing paper.
  • Figure 1 is an infrared spectrum of a poly [acrylic acid-butyl acrylate-styrene]-starch ternary graft copolymer prepared in Example 1.
  • poly(acrylic acid)-starch graft copolymer means a material obtained by graft copolymerization of poly[acrylic acid]-styrene and starch.
  • poly [acrylic acid]-styrene is a terpolymer of acrylic acid, (meth) acrylate or styrene, or a binary copolymer of (meth) acrylate or styrene.
  • (Meth)acrylic acid” in the present invention means acrylic acid or methacrylic acid, (meth) acrylate means acrylate or methacrylate, and styrene includes substituted and unsubstituted styrene.
  • a graft copolymer of a terpolymer of acrylic acid, acrylate or styrene and starch is preferred.
  • the acrylate and methacrylate respectively include an alkyl ester of acrylic acid and methacrylic acid, preferably a C1-C10 mercapto ester, more preferably a propyl group and a butyl ester.
  • the poly[acrylic acid (styrene)-styrene graft copolymer of the present invention has a weight average molecular weight of from 2,500 to 30,000 Daltons, and the structural formula of the graft copolymer is expressed as:
  • AGU represents a structural unit constituting starch
  • n represents a repeating number of the structural unit
  • Poly [Acryl ic acid (Acryiate)-Styrene] represents poly[propionate-styrene].
  • the hydroxyl group at the C2 and C6 positions, the active sequence is the hydroxyl group at the C3 position > the hydroxyl group at the C2 position > the hydroxyl group at the C6 position, which is initiated by most people using a peroxide, a guanamine nitrate or a redox system initiator to initiate free radical living polymerization.
  • the reaction mechanism infers that poly[acrylic acid]-styrene is mainly grafted at the C3 position of the starch molecule.
  • the poly[acrylic acid (styrene)-styrene graft copolymer of the present invention is prepared by an emulsion polymerization method. Specifically, the following two steps are included: controlling monomer concentration, initiator concentration, emulsifier concentration, polymerization temperature to form poly[acrylic acid]-styrene; oxidizing starch by an initiator to produce starch Under the condition of free radicals, poly[acrylic acid (styrene)-styrene] is graft-copolymerized with starch to form a poly[acrylic acid (styrene)-styrene]-graft copolymer. The grafting rate is over 25 %, and the product is hydrophilic at this time.
  • the raw material monomers acrylic acid, (meth) acrylate and styrene are industrial first-grade products, which are commercially available directly from the market.
  • the concentration of the monomer is controlled such that the ratio of (meth)acrylic acid, (meth) acrylate, and styrene is approximately 1: 10: 2. 5.
  • the monomer concentration was controlled so that the ratio of (meth) acrylate to styrene was about 4:1.
  • the control range of the mass of the monomer component added is: 35 to 40 parts of (meth) acrylate, 4 to 6 parts of (meth) acrylate, benzene 10 to 20 parts of ethylene.
  • the control range of the mass of the monomer component is: 35 to 50 parts for (meth) acrylate and 10 to 20 parts for phenylethyl group.
  • the preferred concentration is 0.35%.
  • the emulsifiers used in the polymerization system can be: higher fatty alcohol sulfates, such as sodium lauryl sulfate, sodium cetyl sulfate, sodium octadecanoate (this material is an anionic emulsifier and an acrylic emulsion phase). Melt, etc. And sorbitan monooleate, laurate, monostearate, etc., the purity is industrial grade first or more. In the usual conditions not for special paper bases and fabrics, sodium decanoate and sorbitan monooleate and monostearate are preferred as complex emulsifiers.
  • a preferred octadecyl sulfate and sorbitan monooleate, mono-hard acid and triethanolamine are used as a composite emulsifier, if 100 parts of a graft copolymer, an emulsifier, is to be prepared.
  • the dosage range is controlled by: sorbitan monooleate ⁇ 0.25 parts, sodium octadecanoate ⁇ 0.1 parts, triethanolamine ⁇ 0.2 parts
  • the concentration of the initiator in the system is usually 0.05% to 0.2%, preferably 0.15%.
  • the initiator may use a strong oxidizing agent such as a persulfate clock, ammonium persulfate, benzoyl peroxide, hydrogen peroxide or the like; or an ionic initiator such as azobisisobutyronitrile, azobisisovaleral or the like; ⁇ salt; or redox system initiator, such as persulfate clock-sodium bisulfite, ammonium persulfate-sodium bisulfite, potassium persulfate-ferrous sulfate, potassium persulfate-sodium thiosulfate, etc., purity Industrial first-class products and chemically pure, analytically pure.
  • a preferred persulfate clock-sodium bisulfite initiator is taken as an example.
  • the amount of the initiator is controlled in the range of: sodium hydrogen sulfite to 0.1 part, potassium persulfate to 0.05. Share.
  • the starch used in the present invention is a modified starch having a degree of etherification of 0.7-1.2, usually an etherified starch obtained by using propylene oxide as an etherifying agent and epichlorohydrin as a crosslinking agent, which can be directly purchased from the market or It is prepared by one of ordinary skill in the art using conventional means.
  • the amount of the starch is from 18 to 25 parts, preferably 25 parts, per 100 parts by mass of the starch graft copolymer.
  • the grafting rate is above 25% to ensure hydrophilicity.
  • a monomer mixture composed of (meth)acrylic acid, (meth) acrylate and styrene, or composed of (meth) acrylate and styrene is added to an emulsion system composed of an emulsifier and an initiator. , we (for (meth)acrylic acid, (meth) acrylate and styrene ternary systems) or 60 ° C (for (meth) acrylate and styrene binary systems) initiated polymerization.
  • the temperature of the system is automatically increased.
  • the modified starch with a degree of etherification of 0.7 to 1.2 is added, and the temperature is controlled at 70 to 85 °C, and the reaction is continued for 1 to 2 hours.
  • the system reaches a certain viscosity requirement, that is, the temperature is stopped to stop the reaction, and a poly[acrylic acid (styrene)-styrene]-graft copolymer is obtained, and the graft ratio is 25% or more.
  • the emulsion sample after the completion of the above reaction is added with a certain amount of absolute ethanol to cause precipitation, and filtration is performed.
  • the precipitated product was added to a 0.5 mol / L NaOH solution, the ungrafted starch was separated by stirring at 50 ° C for 1 hour, and the filtered precipitated product was packed in a paper bag and placed in a Soxhlet extractor to extract with toluene. The agent was reflux-extracted for 24 hours to remove the homopolymer of styrene and acrylic acid and acrylate.
  • the poly[acrylic acid (styrene)-styrene graft copolymer obtained by the above process is dispersed in the emulsion, and in the case of direct use of the emulsion, it is required to be measured by a rotational viscometer at 25 °C.
  • the content of the homopolymer is 0.3%, and the homopolymer content is 0. 3 %.
  • the graft copolymer emulsion thus obtained can be used as it is, or can be isolated, dried and purified by means known in the art.
  • the graft copolymer thus obtained can be used for preparing the pigment release agent for cold transfer printing paper of the present invention, which comprises the above-mentioned graft copolymer of poly[acrylic acid]-styrene and starch, sulfated oil. , phosphate esters and silica or palygorskite as fillers.
  • the pigment release agent for cold transfer printing paper can be applied to various printing machines such as flexographic printing machines, gravure printing machines, screen printing machines, and the like, and printing transfer printing papers for various fabrics.
  • the pigment release agent for cold transfer printing paper prepared according to the present invention contains, by mass percentage: poly [acrylic acid (styrene)-styrene]-starch graft copolymer 35% - 85 %; silica as a filler 0.05% -0.5% or palygorskite 3 % - 9 %; sulphated oil as additive auxiliaries 0.2% - 1.8 %, defoamer 0.1 % - 0.8 %, wetting agent 0.5% -2%, The balance is water.
  • a small amount of a solid substance is added as a filler, and a smaller amount of a liquid substance is added as an auxiliary agent for improving certain properties of the system and being convenient for application.
  • the filler materials are mainly ultrafine powder grade silica (such as vapor phase silica, nano silica) or silicate or palygorskite, depending on the targeted fabric. Choose to use.
  • the sulfated oily substance includes, for example, castor oil sulfate, sodium stearyl sulfate, etc., and sodium oleoate is usually used.
  • the antifoaming agent includes a phosphate such as tributyl phosphate and an alcohol such as n-octanol.
  • Tributyl phthalate is preferred under the usual conditions not for special paper bases and fabrics.
  • a wetting agent carboxypyrrolidone or the like, may be optionally added depending on the intended fabric.
  • the fillers and auxiliaries of the present invention are commercially available, and the purity is industrial. CP grade or AR grade.
  • the method of preparing the above-described pigment release agent for cold transfer printing paper is as follows.
  • an auxiliary agent and a filler are added to obtain a pigment release agent for cold transfer printing paper of the present invention.
  • the above-mentioned dye release agent is obtained by adding a sulfated oil, a phosphate ester, and silica or palygorite as a filler to the graft copolymer.
  • the pigment release agent produced as described above is excellent in compatibility with the dye component, has good latex stability, and has high film formation and light stability.
  • the printing paper insulation layer has an adverse effect, so the concentration of the acrylic monomer is controlled to be ⁇ 6%, the polymerization molecular weight of the styrene-acrylic acid is more than 30,000, and the grafting ratio is more than 25%.
  • the pigment spacer has good chemical stability and mechanical stability, and has excellent printability. And its rheological properties are ideal for all types of coating equipment. It guarantees good operation even under the most demanding parts, provides excellent wet rub resistance, and avoids malfunctions such as misprints and paper breaks during paper printing.
  • the preparation process of the pigment release agent for cold transfer printing paper is specifically described as follows: triethanolamine, sodium lauryl sulfate (sodium lauryl sulfate) and water are used as an emulsion, and sulfurous acid is added under stirring. Sodium hydrogen hydride and potassium persulfate, heated to 50 ° C as an initiator, mixed with (meth)acrylic acid, (meth) acrylate (such as butyl acrylate, ethyl methacrylate) and styrene monomer The addition of the initiating emulsifier initiates polymerization. The temperature of the system is automatically increased.
  • the modified starch with a degree of etherification of 0.7 to 1.2 is added.
  • the temperature is controlled at 70 85 ° C, and the reaction is continued for 1 h to 2 h to achieve acrylic acid.
  • - Graft copolymerization of styrene copolymer with starch the graft ratio is about 28%.
  • an ultrafine powder grade silica or silicate or palygorskite, castor oil sodium sulfate, and tributyl phosphate is added to the above copolymer emulsion, and if necessary, a wetting agent, carboxypyrrolidone, is added, and the water is adjusted to 100%.
  • the pigment release agent for the cold transfer printing paper is a milky white liquid having a viscosity of 300 to 1600 Pa ⁇ s, and the Charon Cup No. 2 cup has a flow rate of 20 to 70 seconds at 25 °C.
  • the pigment release agent for cold transfer printing paper according to the present invention can be applied to natural fiber fabrics such as cellulose fibers, wool, cotton, silk, or cold transfer printing paper for synthetic fiber fabrics such as polyester, nylon, acrylic, and inkjet transfer.
  • Cold transfer printing paper and cold transfer printing Art The original cold transfer printing paper caused the dye and paper fibers to be fixed due to the imbalance and incompleteness of the hydrophilicity and hydrophobicity of the release agent, so that the residual color of the transferred paper was nearly 50%, even after 86 years.
  • Foreign manufacturers who study wet transfer also have low transfer rate due to incompleteness of the release agent and incompletely shielding the pigment, and the residual amount of paper-based dyes is too large, which wastes raw materials and seriously pollutes the environment.
  • the main component of the pigment release agent used in the cold transfer printing paper of the present invention is a polymer graft copolymer coated on a paper base of transfer printing paper, a film-like medium can be formed, and a temporary shielding can be produced.
  • the dye When the dye is printed on the printing tool, it does not have a strong affinity with the paper base of the transfer printing paper, and can promote the transfer of the dye ink to the fabric.
  • the pigment release agent of the present invention has an excellent effect on inkjet transfer printing. Since digital inkjet printing, the entire image is composed of fine color dots, a higher jet dot density is required. This is the resolution of the usual title. Different base fabrics have different resolution requirements. The yarn count, density and fabric texture of the fabric all affect the resolution.
  • inkjet printing requires a layer of contact on the surface of the fabric to color the dots, and then through steaming, water washing, and finally finishing the printing process. Even the production capacity of the Netherlands ST0YK company is only 4. 6m7h. This process limits the development of digital inkjet.
  • the ink jet is discharged, and the yield can be greatly improved.
  • the transfer coating of the present invention is capable of accepting color points of dpi 360 - 720 and ultra fine 720 dpi X 720 dpi color points.
  • the image fineness on textiles reaches the Dutch ST0YK reactive dye inkjet printing standard.
  • the above-mentioned pigment release agent for cold transfer printing paper can be applied to various printing machines such as flexographic printing machines, gravure printing machines, screen printing machines, and the like, and printing transfer papers for various types of fabrics.
  • fine, colorful, and layered transfer printing paper can be printed by a rotary screen printing machine, a flat screen printing machine, a gravure printing machine, a flexographic printing machine, a flatbed offset printing machine, and an inkjet printer.
  • Flexographic printing is a method of printing ink through an anilox roller using a flexible resin plate, which has a embossing property, and is a flexible rubber surface in terms of its printing characteristics. In contact with printing paper, it has offset characteristics. From the transfer paper material, it uses water-based ink and can be printed by the cell, which has gravure characteristics. Flexo printing is a light pressure printing process with a printing line pressure of about lkgf / cm. At the same time, the thickness of the ink layer of flexographic printing is about 5 ⁇ 10% Q iM. The printing plate image of the gravure printing is lower than the surface of the printing plate, and the hierarchical density of the graphic is represented by the depth and density of the concave mesh.
  • the gravure is direct printing, and the ink in the concave portion of the printing plate is directly transferred to the substrate to form an image portion.
  • the ink is coated on the printing plate, and then the ink in the blank surface of the printing plate is scraped off with a doctor blade to fill the concave portion.
  • the ink in the lower part is kept down and transferred to the surface of the substrate by printing pressure to complete the printing.
  • the gravure printed line pressure is ll ⁇ 18kgf/cm.
  • the rotary screen printing process is a printing method between the gravure roll printing and the flat screen printing in terms of its printing characteristics.
  • the article according to the invention has a coating formed from the pigment release agent of the invention.
  • the article may, for example, be a cold transfer printing paper having a coating formed on the surface of the paper base by the pigment release agent of the present invention.
  • the "paper base” herein may be any paper base commonly used in the art, such as writing paper, offset paper, printing paper, glossy paper, wrapping paper, printing paper, and the like.
  • the dye release agent of the present invention is applied onto a paper base by a known coating means such as doctor blade coating, web coating, extrusion coating, roll coating or the like to form a cold transfer printing paper.
  • Such cold transfer printing paper not only has the function of shielding carrier, but also has good printing adaptability and transferability, and at the same time, it has anti-seepage, heavy-duty resistance, rapid transfer pattern to fabric and adapting to roll during transfer.
  • the paper is formed into the necessary moisture resistance and tear resistance.
  • the transfer printing paper coated with the release agent of the invention also solves the problem that the amount of dye residue on the paper is too large when the transfer printing paper is transferred, so that the transfer rate is over 90%, which not only saves the dyeing material, but also Reduced environmental pollution. Therefore, the present invention promotes the further development of the printing and dyeing industry toward the environmentally friendly economy.
  • the sulphuric acid is added in an amount of 0. 1 part of sulphuric acid.
  • the sulphuric acid is added to the sulphuric acid.
  • the poly [(meth) acrylate-styrene] - starch binary graft copolymer was prepared in the experimental reactor, first 0.25 parts of triethanolamine, 5.8 parts of water and 0.1 parts of dodecane Sodium sulphate was injected into an emulsion, and 0.1 parts of azobisisobutyronitrile (AIBN) was added under stirring, and the temperature was raised to 60 ° C as an initiator; 40 parts of methyl methacrylate and styrene 10 were added.
  • AIBN azobisisobutyronitrile
  • the monomer mixed droplets are added to the initiator emulsion, and after the polymerization is initiated, the system is automatically heated to 90 Torr, that is, the modified starch (hydroxyl shielded) having a degree of etherification of 0.7 to 1.2 is added, and the temperature is controlled. Under the condition of 75 ⁇ 85 °C, the reaction was continued for lh-2h to realize the graft copolymerization of methacrylate-styrene copolymer and ⁇ : powder.
  • the weight average molecular weight is about 15,000 Daltons.
  • the molecular weight of the polymerization is 30,000 or more, the graft ratio is about 32%, and the hydrophilicity is good.
  • the pigment spacer for the cold transfer printing paper is a blue-light milky white liquid with a solid content of about 48% and a viscosity of 800 to 900 Pa ⁇ s.
  • the flow rate of the 2nd cup of the Zahn Cup is 25 - 40 seconds at 25 °C. .
  • the pigment spacer emulsion was subjected to nuclear magnetic resonance (NMR) experiments using the following apparatus and method, and the NMR actual map is shown in Fig. 2.
  • NMR nuclear magnetic resonance
  • the chemical shift ⁇ is 1. 5 ⁇ 2.
  • 5ppm of the proton peak is mainly A signal peak of methylene and methine on the acrylic-butyl acrylate-styrene copolymer backbone grafted onto the powder.
  • the proton peak with a ⁇ of 3.3 to 4.01 ppm is mainly produced by hydrogen atoms on the carbon of the ester group in the starch molecule, CI, C4, C5, C6 and butyl acrylate.
  • a peak having a ⁇ of about 4.7 ppm is caused by hydrogen in residual water molecules in the emulsion.
  • the peak of ⁇ of 5.0 ⁇ 6.2 ppm is the signal peak of the shield peak in the hydroxyl group attached to C6 in the starch molecule and the residual initiator emulsifier in other systems.
  • is
  • the peak of 9.55ppm is the proton peak of the aldehyde group formed at the C2 position after the ring-opening bond between the C2 and C3 under the action of the graft copolymerization counterinitiator, and C3 becomes the grafting site. From the above analysis, it was found that the acrylic acid-butyl acrylate-styrene copolymer was grafted on the C3 of the starch molecule to form a poly[acrylic acid-butyl acrylate-styrene]-starch graft copolymer. The graft ratio is about 32%.
  • Castor oil sodium sulfate is 0.7%
  • Tributyl phosphate 0.2%
  • Modified starch 180kg, controlled temperature at 70 ⁇ 85 °C, continue to react for lh-2h, achieve graft copolymerization of acrylic acid-styrene copolymer and starch, weight average molecular weight is about 19000 Daltons. The molecular weight of the polymerization reaches 35,000 or more.
  • Copolymerization here Grade silica added to the emulsion vapor 3kg, sodium castor oil 2 kg, after stirring uniformly the foregoing, tributyl phosphate added 4kg, and finally water was adjusted to 1000kg (100%), cold transfer printing paper that is cotton Type pigment spacer.
  • the pigment spacer for the cotton type cold transfer printing paper is a milky white liquid with a viscosity of ⁇ 900pa's, and the flow rate of the 2nd cup of the Chaen Cup is about 40 seconds at 25 °C.
  • Tributyl phosphate is 0.1%
  • the water is 4.4%.
  • the viscosity is 900 ⁇ 1200pa ⁇ s, and the flow rate of the 2nd cup of the Zahn Cup is 25 seconds at 25 °C.
  • the pigment release agent for the cotton type cold transfer printing paper is a milky white liquid with a viscosity of 900 ⁇ 1200 Pa ⁇ s, and the Chaen Cup 2 at 25 ° C
  • the flow rate of the cup is about 70 seconds.
  • the graft ratio is about 28%.
  • Castor oil bowl sodium is 5 %
  • Tributyl phosphate is 0.2%
  • the water is 6.8%.
  • the viscosity is 500 ⁇ 700pa ⁇ s, and the flow rate of the fourth coated cup is 30 seconds at 25 °C.
  • 2.5kg of triethanolamine, 58kg of water and 0.9KG of sodium hexadecyl sulfate are injected into the emulsion, and lkg sodium hydrogen sulfite and 0.5kg potassium persulfate are added under stirring to raise the temperature to 50.
  • the pigment release agent for the cotton type cold transfer printing paper is a base light milky white liquid having a viscosity of 500 to 700 Pa s, and the flow rate of the fourth coated cup is 30 seconds at 25 °C.
  • Wool (protein fiber) type fabrics are used as pigment release agents for cold transfer printing paper.
  • Castor oil bowl sodium is 0.4%
  • Tributyl phosphate is 0.5%
  • Modified starch with a degree of 0.7-1.2 (hydroxyl shielded) 250kg, controlled temperature at 70 ⁇ 85°C ⁇ , continued reaction for lh-2h, achieving graft copolymerization of acrylic acid-styrene copolymer and starch, heavy The average molecular weight is about 22,000 Daltons.
  • 2 kg of fumed silica and 4 kg of sodium sesame oil were added to the copolymer emulsion. After the above materials were uniformly stirred, 5 kg of tributyl phosphate was added, and finally water was adjusted to 1000 kg (100%), which was used for cold transfer printing paper. Hair pigment spacers.
  • the pigment release agent for this type of cold transfer printing paper is a milky white liquid with a viscosity of 950 ⁇ HOOpa ⁇ s, and the flow rate of the 2nd cup of the Zahn Cup is 25 - 35 seconds under the condition of 25 inches.
  • the grafting ratio is over 38%.
  • Synthetic fiber (polyester, nylon and acrylic) type pigment spacer for cold transfer printing paper
  • Castor oil bowl sodium is 0.9%
  • Tributyl phosphate is 0.7%
  • Pyrrolidone wetting agent PH316 emulsion is 2%
  • the poly[(meth)acrylate-styrene]-starch graft copolymer prepared in Example 2 was 820 kg, and the copolymer emulsion was added with 4 kg of vapor phase silica, 9 kg of castor oil sodium sulfate, and the above shield was evenly stirred. Then, add 2 kg of carboxypyrrolidone wetting agent PH316, 7 kg of tributyl phosphate, and finally adjust to 1000 kg (100%) with water, which is a synthetic fiber type pigment release agent for cold transfer printing paper.
  • the pigment spacer for the synthetic fiber type cold transfer printing paper is a milky white liquid having a viscosity of ⁇ 900pa's, and the flow rate of the 2nd cup of the Zahn Cup at 25 °C is 30-40 seconds.
  • the PE-2 dye release agent prepared in the above examples can be applied to a paper base for use in a rotary screen printing machine, a flat screen printing machine, a gravure printing machine, a flexographic printing machine, a flatbed offset printing press, and an ink jet printer.
  • a transfer paper using the pigment isolating agent the transfer printing paper printed by the above various printing and printing equipment can be completely peeled and peeled to various fabrics when it is pressed and applied with the fabric. on.
  • the above examples all emphasize the viscosity range below 1200 pa ⁇ s, and the flow rate of the 2nd cup of the Zahn Cup at 25 °C is 30 - 40 seconds. If the above viscosity cannot be maintained, the release of the dye on the paper base will be poor, and the dyeing rate of the product will not be improved. For example, the plasticity is poor in the printing of the concave plate, and the sharpness of the pattern should be lacking.
  • the flow rate of the 2nd cup of the Zahn Cup is positioned at 30 - 40 seconds to ensure the thixotropic fluidity between the blade and the paper and the paste during coating. It is very difficult to apply the pigment spacer such as the lack of the above viscosity meter flow rate. Adapt to the printing conditions of the latter.
  • Paper specifications 60g single-sided writing paper, width 1800 wake (Anmu Huangshan Jinma Paper Mill)
  • PE - 2 pulp index Fineness 2. 5 ⁇ ⁇ , viscosity 400 ⁇ 550 cp, 25 °C ⁇ under the cup of the cup No. 2 cup flow rate ⁇ 45 seconds.
  • the PE-2 slurry was uniformly coated on the surface of the paper with a professional coater to form a pigment barrier layer. Then, by printing on the side of the paper coated with the pigment isolation layer, Form a cold transfer printing paper.
  • Paper specifications 60g writing paper, (Shandong Weifang Paper Mill)
  • Coating slurry 97 parts of PE-2 slurry, 1 part of polyvinylpyrrolidone, 2 parts of Germany 3011 oil.
  • the PE-2 slurry was first treated with a homogenizer, and the fineness of the particles was measured with a fineness scraper, and the fineness was 0.25 ⁇ m.
  • the coating method is coated with West Bay BABC-CK machine blanket, 9 g per m 2 , 30-40 min per minute.
  • PE - 2 pulp index Viscosity: 450 cps, No. 4 painted cups at 25 ° C for 45 s.
  • the rubber blanket is used as the pressure bearing material and the knife coating method.
  • Coating amount 7-9 g/m 2 , Huangshan Paper Company
  • the Penta Screenl 25 mesh round mesh has an opening ratio of 15%, which is suitable for fine pattern printing.
  • the printing line pressure was 1.5 kg/cm.
  • the following formulation was used: viscosity 950 cps, No. 4 coating cup at 25 ° C for 1 minute and 20 seconds, using a round mesh 105 mesh online coating. Coating amount 12-15 g / m 2 , using Shandong Qingzhou paper mill single glue 90 g web.
  • PE - 2 slurry index Viscosity HOOcp, flow rate of No. 4 coating cup at 280s at 25 °C.
  • the fabric was padded and wetted in a NaOH alkaline agent of Baume 36.5, passed through a three-roll mill, one immersion and two rolling, the rolling ratio was ⁇ 60%, and the rolling speed was 2.5/min.
  • the pigment prepared in Example 3 was used.
  • the release agent ie PE-2 slurry
  • PE-2 slurry index viscosity 880cp
  • the flow rate of No. 4 coating cup is 119s at 25°C
  • the fabric is wetted by padding in a mixed solution of Baume 36 NaOH and Na 2 Si0 3 , through a three-roll mill, a dip Two rolling, the remnant rate is ⁇ 65%, using the PE prepared in Example 4
  • the transfer rate on the fabric is about 92%.
  • PE-2 plasma indicators ? Viscosity 630cp, under conditions of 25'C flow cup No. 4 finish 167s, fabric Baume 37 ⁇ 304 with Na 2 C0 3 solution was padded wetted mixture, through a three roll The car, one dip and two rolling, had a ranch rate of ⁇ 55%. Using the PE-2 pulp pigment release agent prepared in Example 5, the transfer rate on the fabric was about 95%.
  • alkyl emulsifiers mentioned in the examples are higher fatty alcohol sulfates; such emulsifiers are more emulsifiable, but are more stable than soap emulsifiers, and are anionic and moisturizing and increasing. Dissolving function.
  • the paste composed of [acrylic acid]-styrene grafted with starch solves the problem of tension and balance between the hydrophobic layer and the hydrophilic layer of the barrier layer coated with the front transfer paper.
  • the cold transfer printing paste provides barrier separation during transfer and hydrophilic printability during printing.
  • the research invention of the present invention effectively solves the application of cold transfer printing on various fibers and the use on various printing apparatuses.

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Abstract

A copolymer obtainable by poly[acrylic acid (acrylate)-styrene] grafted on starch,the process of preparation and use thereof are provided. The poly[acrylic acid (acrylate)-styrene] is (meth)acrylic -(meth)acrylate- styrene terpolymer.The graft copolymer has a molecular weight in the range of 2500-30000 Dalton and is of the formula : Wherein AGU represents a structure unit of starch, n represents the recurring number of the structure unit, and poly[acrylic acid (acrylate)-styrene] represents poly[acrylic acid(acrylic ester)-styrene]. A cold-pressing transfer printing paper is also provided.The coating of the above graft copolymer is applied on the surface of the transfer printing paper.

Description

接枝共聚物及其制法和用途、 色素隔离剂及其制 技术领域  Graft copolymer, preparation method and use thereof, pigment release agent and preparation thereof
本发明涉及纺织印染行业中转移印花工艺所使用的色素隔离剂 的技术领域。具体而言,本发明涉及冷转移印花紙用色素隔离剂(即 染料隔离剂) 中使用的一种新的聚 [丙烯酸(酯) -苯乙烯] -淀 粉接枝共聚物糊状物及其制备方法和用途, 还涉及含有上述接枝共 聚物的色素隔离剂以及具有由所述的色素隔离剂形成的涂层的制 品, 例如冷转移印花纸。 经本发明所述的色素隔离剂涂层处理后制 成的具有隔离层的冷转移印花紙, 可以应用于纤维素纤维、 毛、棉、 丝绸等天然纤维织物上, 也可用于涤纶、 锦纶、 腈纶等合成纤维织 物上。 背景技术  This invention relates to the technical field of pigment release agents used in the transfer printing process in the textile printing and dyeing industry. In particular, the present invention relates to a novel poly[acrylic acid (styrene)-starch graft copolymer paste used in a pigment release agent for cold transfer printing paper (ie, a dye release agent) and preparation thereof The method and use also relate to a pigment release agent comprising the above graft copolymer and an article having a coating formed from the pigment release agent, such as a cold transfer printing paper. The cold transfer printing paper with the separation layer prepared by the pigment spacer coating coating according to the present invention can be applied to natural fiber fabrics such as cellulose fibers, wool, cotton, silk, etc., and can also be used for polyester, nylon, Acrylic fiber and other synthetic fabrics. Background technique
转移印花(下文中, 有时也筒称 "转印") 已成为日用工业装饰 和纺织品印花加工的一种新方法。 它包括下述步骤: 用印刷方法将 合适的染料油墨在特种纸上印刷所要印花的图案或文字, 印制成转 印花纸, 再将这种转印花纸上有染料的一面与被印的织物密合, 通 过压力与润湿作用使染料油 、从纸上溶解剥离, 从而将转移印花纸 上的图案或文字转印到织物上。  Transfer printing (hereinafter sometimes referred to as "transfer") has become a new method of industrial decoration and textile printing. The method comprises the following steps: printing a suitable dye ink on a special paper by printing to print a pattern or text to be printed, and printing the dyed side of the transfer paper with the printed fabric. The film is transferred to the fabric by pressure and wetting to dissolve the dye oil from the paper.
目前转移印花方法可分为干转印法即热转印式与压敏转印式,以 及湿转印法, 即冷转移剥离与溶剂转移剥离式这两大类。 最早的转 移印花工艺是作为热转印法之一的升华法热熔转移印花。据英国《染 色家协会会志》 1971年和日本《加工技术》 1972年 "转移印花"专 辑介绍, 一般升华法热熔转移印花时, 从转移印花纸转印到织物上 的染料不能被纤维全部吸收, 总有一部分染料残留在织物表面和纸 基上, 成为转移印花工艺得色率较低、 印花织物色牢度较差的主要 原因。 有试^ £明, 在 200°C或更低的温度下, 仅有 39种染料能用 于转移印花紙的制造, 而经过转移印花后的纸基上残留将近 20 % - 30 %的染料。 因此, 在以后的年代里, 对转移印花的最大关注就在 于如何把纸基上残留的染料减到最少, 既有利于节省成本, 又有助 于解决染料残留物对环境的污染, 这样就发明了湿法冷转移印花工 艺。 升华法热熔转移印花工艺仅能处理化纤类织物, 尤其是涤纶纤 维织物, 而纤维素纤维和羊毛、 丝绸以及棉等天然纤维必须采用湿 法冷转移印花工艺进行处理。 在湿法冷转移印花工艺中, 为了使染 料能从转移印花纸上充分转移, 要先在纸基上涂上一层转移层或剥 离层(参见日本特许 22094号公拫 )。 特别是上世纪 70年代后, 出 现了多种转移印花油墨的转移层或剥离层, 但都有其局限性: 1.油 墨的转移率, 已印刷上的色料透过或穿过剥离层的薄层薄膜接触到 纸基而造成剥离量不足; 2.剥离膜疏水状过度, 由于湿法冷转移使 用水性染料, 剥离膜的过度疏水导致承印物与纸基表面张力不一致 无法完整印刷, 严重破坏印刷图案的完整与清晰; 3.回粘和粘连, 油墨干燥成膜后的短时间没有粘连和返粘的现象, 但在印后放卷进 行加工时就发现纸张背面与正面粘连在一起, 造成表干内湿的严重 问题; 4.耐 pH值低,被印纸张与已润湿的织物重叠压印时, 由于纸 张剥离层不耐强碱, 造成转移印花后的布面花纹渗透严重, 花型模 糊, 图案不清; 5.附着牢度差, 被印染料图案由于附着牢度差, 用 手搓擦就能造成掉色, 污染严重。 以上这些局限了 70年代后出现的 各类转移印花油墨的实际应用价值, 同时也由于以上原因使它并不 能真正完整地体现或应用到冷转移印花工艺上, 再转印到各种纤维 上。 发明内容 At present, the transfer printing method can be classified into a dry transfer method, that is, a thermal transfer type and a pressure sensitive transfer type, and a wet transfer method, that is, a cold transfer peeling method and a solvent transfer peeling type. The earliest transfer printing process was a sublimation hot melt transfer printing as one of the thermal transfer methods. According to the British "Dyeing Association Association" in 1971 and Japan's "Processing Technology" 1972 "Transfer Printing" album introduction, the general sublimation method hot melt transfer printing, the transfer of transfer printing paper to the fabric of the dye can not be all Absorption, there is always a part of the dye remaining on the surface of the fabric and the paper base, which is the main color yield of the transfer printing process, and the color fastness of the printed fabric is poor. the reason. At the temperature of 200 ° C or lower, only 39 dyes can be used for the transfer printing paper, and nearly 20% - 30% of the dye remains on the paper base after the transfer printing. Therefore, in the years to come, the biggest concern for transfer printing is how to minimize the residual dye on the paper base, which is conducive to cost savings and helps to solve the environmental pollution of dye residues. The wet cold transfer printing process. Sublimation hot melt transfer printing process can only process chemical fiber fabrics, especially polyester fiber fabrics, while cellulose fibers and natural fibers such as wool, silk and cotton must be processed by wet cold transfer printing. In the wet cold transfer printing process, in order to allow the dye to be sufficiently transferred from the transfer printing paper, a transfer layer or a release layer is first applied to the paper base (see Japanese Patent No. 22094). Especially after the 1970s, there have been a variety of transfer or release layers for transfer printing inks, but they all have their limitations: 1. The transfer rate of the ink, the printed color is transmitted through or through the release layer. The thin film is in contact with the paper base and the amount of peeling is insufficient. 2. The peeling film is excessively hydrophobic. Due to the wet transfer of the water-based dye, the excessive hydrophobicity of the peeling film causes the substrate to be inconsistent with the surface tension of the paper. The integrity and clarity of the printed pattern; 3. Back-sticking and blocking, the ink does not stick and re-stick after a short period of film formation, but when the film is unloaded after printing, it is found that the back side of the paper is stuck to the front side, resulting in Serious problem of wetness in the surface; 4. Low pH resistance, when the printed paper is overprinted with the wetted fabric, the paper peeling layer is not resistant to strong alkali, causing serious penetration of the pattern after transfer printing. The type is fuzzy, the pattern is unclear; 5. The adhesion fastness is poor, and the dye pattern to be printed is poor in adhesion, and it can be discolored by hand rubbing, and the pollution is serious. These limitations limit the practical application value of various types of transfer printing inks that appeared after the 1970s. At the same time, due to the above reasons, it cannot be completely embodied or applied to the cold transfer printing process and then transferred to various fibers. Summary of the invention
针对以往的转移印花油墨的转移层或剥离层的局限性,本发明开 发出新的聚 [丙烯酸(酯) -苯乙烯] -淀粉接枝共聚物及含有这 种接枝共聚物的冷转移印花纸用色素隔离剂, 通过使用这种色素隔 离剂制成的具有隔离层的冷转移印花纸用于冷转移印花工艺可以隔 离油墨对纸张的渗透, 提高油墨转移率; 具有恰当的疏水性与亲水 适印性, 保证承印物完整印刷, 使印刷图案完整与清晰; 不产生表 干内湿的问题; 具有较好的 pH适应范围; 染料图案附着好, 不发生 掉色现象。 该发明促进了印染行业向环保经济的方向进一步发展。 The present invention is directed to the limitations of the transfer layer or the release layer of the conventional transfer printing ink. A new poly(acrylic acid ester-styrene)-starch graft copolymer and a pigment release agent for cold transfer printing paper containing the graft copolymer, having a separation layer made by using the pigment release agent The cold transfer printing paper used in the cold transfer printing process can isolate the penetration of the ink into the paper and improve the ink transfer rate; has the proper hydrophobicity and hydrophilic printability, ensures the complete printing of the substrate, and makes the printed pattern complete and clear; Produces the problem of wet inside the surface; has a good pH adaptation range; the dye pattern is well adhered, and no color fading occurs. The invention promotes the further development of the printing and dyeing industry towards the environmentally friendly economy.
本发明的笫一个方面是提供一种新的聚 [丙烯酸(酯) -苯乙烯 ] -淀粉接枝共聚物。  One aspect of the present invention is to provide a novel poly[acrylic acid]-styrene]-starch graft copolymer.
本发明的第二个方面是提供上述的聚 [丙烯酸(酯) -苯乙烯] -淀粉接枝共聚物的制备方法。  A second aspect of the present invention provides a process for producing the above poly(acrylic acid)-starch graft copolymer.
本发明的笫三个方面是提供上述的接枝共聚物的用途,上述的接 枝共聚物可以用来制备冷转移印花纸用的新的色素隔离剂。 经这种 色素隔离剂涂层后制成的具有隔离层的冷转移印花纸, 可以应用于 纤维素纤维、 毛、 棉、 丝绸等天然纤维织物上, 也可用于涤纶、 锦 纶、腈纶等合成纤维织物上,从而制成图案清晰, 鲜艳的印花制品。  The three aspects of the present invention are the use of the above-described graft copolymer which can be used to prepare a novel pigment release agent for cold transfer printing paper. The cold transfer printing paper with the separation layer prepared by coating with the pigment isolating agent can be applied to natural fiber fabrics such as cellulose fibers, wool, cotton, silk, etc., and can also be used for synthetic fibers such as polyester, nylon, acrylic and the like. On the fabric, a clear, brightly printed product is produced.
本发明的第四个方面提供了含有上述的接枝共聚物的色素隔离 剂。  According to a fourth aspect of the invention, there is provided a dye separating agent comprising the above graft copolymer.
本发明的第五个方面涉及具有由上述的色素隔离剂形成的涂层 的制品, 例如冷转移印花紙。 附图说明  A fifth aspect of the invention relates to an article having a coating formed of the above-described pigment release agent, such as a cold transfer printing paper. DRAWINGS
图 1为实施例 1制备的聚 [丙烯酸-丙烯酸丁酯-苯乙烯] ― 淀粉三元接枝共聚物的红外光谱谱图。  BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is an infrared spectrum of a poly [acrylic acid-butyl acrylate-styrene]-starch ternary graft copolymer prepared in Example 1.
图 2为实施例 3制备的色素隔离剂乳液的核磁共振旙图。 具体实施方式 2 is a nuclear magnetic resonance spectrum of the pigment release agent emulsion prepared in Example 3. detailed description
下面, 对本发明的各方面进行详细描述。  In the following, various aspects of the invention are described in detail.
首先, 描迷本发明的聚 [丙烯酸(酯) -苯乙烯] -淀粉接枝 共聚物及其制备方法。  First, the poly[acrylic acid]-styrene graft copolymer of the present invention and a process for producing the same are described.
本发明中, 术语 "聚 [丙烯酸(酯) -苯乙烯] -淀粉接枝共 聚物" 是指由聚 [丙烯酸(酯) -苯乙烯 ]和淀粉进行接枝共聚得 到的物质。 其中, 聚 [丙烯酸(酯) -苯乙烯]为丙烯酸、 (甲基) 丙烯酸酯、 苯乙烯的三元共聚物, 或者为 (甲基) 丙烯酸酯、 苯乙 烯的二元共聚物。 本发明中的 "(甲基)丙烯酸"表示丙烯酸或者甲 基丙烯酸, (甲基) 丙烯酸酯表示丙烯酸酯或者甲基丙烯酸酯,苯乙 烯包括取代和未取代苯乙烯。 本发明中, 优选丙烯酸、 丙烯酸酯、 苯乙烯的三元共聚物与淀粉形成的接枝共聚物。  In the present invention, the term "poly(acrylic acid)-starch graft copolymer" means a material obtained by graft copolymerization of poly[acrylic acid]-styrene and starch. Among them, poly [acrylic acid]-styrene is a terpolymer of acrylic acid, (meth) acrylate or styrene, or a binary copolymer of (meth) acrylate or styrene. "(Meth)acrylic acid" in the present invention means acrylic acid or methacrylic acid, (meth) acrylate means acrylate or methacrylate, and styrene includes substituted and unsubstituted styrene. In the present invention, a graft copolymer of a terpolymer of acrylic acid, acrylate or styrene and starch is preferred.
本发明中, 丙烯酸酯和甲基丙烯酸酯分别包括丙烯酸和甲基丙 烯酸的烷基酯, 优选 C1-C10垸基酯, 更优选丙基和丁基酯。  In the present invention, the acrylate and methacrylate respectively include an alkyl ester of acrylic acid and methacrylic acid, preferably a C1-C10 mercapto ester, more preferably a propyl group and a butyl ester.
本发明中的聚 [丙烯酸(酯) -苯乙烯] -淀粉接枝共聚物, 重均分子量在 2500 ~ 30000道尔顿之间, 该接枝共聚物的结构式表 示为:  The poly[acrylic acid (styrene)-styrene graft copolymer of the present invention has a weight average molecular weight of from 2,500 to 30,000 Daltons, and the structural formula of the graft copolymer is expressed as:
Figure imgf000006_0001
Figure imgf000006_0001
其中, AGU表示构成淀粉的结构单元, n表示该结构单元的重复数, Poly [Acryl ic acid (Acryiate) -Styrene]表示聚 [丙埽酸(酯) - 苯乙烯]。 根据张力田 1992年编著的 《变性淀粉》和龙剑英、 龙翔 云、 叶国授所发表的论文 "淀粉分子电子结构的量子化学研究(I) : 结构单元、 糖苷键和氢键的特性,, (广西科学. 2002年第九卷第一 期 34页 -37页- 42页)等, 普遍认为淀粉分子的反应活性中心为 C3 位、 C2位和 C6位羟基,活性顺序是 C3位羟基 > C2位羟基 > C6位羟 基, 由大多数人认同的使用过氧化物, 硝酸铈胺或氧化还原体系引 发剂引发自由基活性聚合的反应机理推知, 聚 [丙烯酸(酯) -苯 乙烯]主要接枝在淀粉分子的 C3位位置。 Wherein AGU represents a structural unit constituting starch, n represents a repeating number of the structural unit, and Poly [Acryl ic acid (Acryiate)-Styrene] represents poly[propionate-styrene]. According to Zhang Tiantian's 1992, "Transformed Starch" and Long Jianying, Long Xiangyun, and Ye Guoxun's paper "Quantum Chemistry Research on the Electronic Structure of Starch Molecules (I): Characteristics of Structural Units, Glycosidic Bonds and Hydrogen Bonds , (Guangxi Science. Vol. 9, No. 1, 2002, pp. 34-37-42), etc. It is generally believed that the reactive center of starch molecules is C3. The hydroxyl group at the C2 and C6 positions, the active sequence is the hydroxyl group at the C3 position > the hydroxyl group at the C2 position > the hydroxyl group at the C6 position, which is initiated by most people using a peroxide, a guanamine nitrate or a redox system initiator to initiate free radical living polymerization. The reaction mechanism infers that poly[acrylic acid]-styrene is mainly grafted at the C3 position of the starch molecule.
本发明中的聚 [丙烯酸(酯) -苯乙烯] 一淀粉接枝共聚物是 用乳液聚合方法制备的。 具体来讲, 包括下述两个步骤: 控制单体 浓度、引发剂浓度、乳化剂浓度、聚合温度,以生成聚[丙烯酸(酯) -苯乙烯]; 通过引发剂氧化淀粉, 在使淀粉产生自由基的条件下, 使聚 [丙烯酸(酯) -苯乙烯]与淀粉发生接枝共聚反应, 生成聚 [丙烯酸(酯) -苯乙烯] -淀粉接枝共聚物。 接枝率达到 25 %以 上, 这时产品的亲水性好。  The poly[acrylic acid (styrene)-styrene graft copolymer of the present invention is prepared by an emulsion polymerization method. Specifically, the following two steps are included: controlling monomer concentration, initiator concentration, emulsifier concentration, polymerization temperature to form poly[acrylic acid]-styrene; oxidizing starch by an initiator to produce starch Under the condition of free radicals, poly[acrylic acid (styrene)-styrene] is graft-copolymerized with starch to form a poly[acrylic acid (styrene)-styrene]-graft copolymer. The grafting rate is over 25 %, and the product is hydrophilic at this time.
本发明中, 原料单体丙烯酸、(甲基)丙烯酸酯和苯乙烯为工业 用一级品, 可以从市场上直接购得。  In the present invention, the raw material monomers acrylic acid, (meth) acrylate and styrene are industrial first-grade products, which are commercially available directly from the market.
当制备上迷的聚丙烯酸-(甲基)丙烯酸酯 -苯乙烯三元共聚物 时, 控制单体的浓度, 使得(曱基)丙烯酸、 (甲基)丙烯酸酯和苯 乙烯的用量比例大约为 1: 10: 2. 5。 而当制备上述的聚 [ (甲基) 丙烯酸酯-苯乙烯]二元共聚物时, 控制单体浓度, 使得(甲基) 丙烯酸酯和苯乙烯的用量比例大约为 4: 1。  When preparing the polyacrylic acid-(meth)acrylate-styrene terpolymer, the concentration of the monomer is controlled such that the ratio of (meth)acrylic acid, (meth) acrylate, and styrene is approximately 1: 10: 2. 5. When the above poly((meth)acrylate-styrene] binary copolymer was prepared, the monomer concentration was controlled so that the ratio of (meth) acrylate to styrene was about 4:1.
具体来讲, 如果要制备 100份的三元接枝共聚物, 加入单体组 分质量的控制范围为: (甲基)丙烯酸酯 35 ~ 40份, (甲基)丙烯酸 4 ~ 6份, 苯乙烯 10 ~ 20份。 要制备 100份的二元接枝共聚物, 加 入单体组分质量的控制范围为: (甲基) 丙烯酸酯 35 ~ 50份, 苯乙 婦 10 ~ 20份。  Specifically, if 100 parts of the ternary graft copolymer is to be prepared, the control range of the mass of the monomer component added is: 35 to 40 parts of (meth) acrylate, 4 to 6 parts of (meth) acrylate, benzene 10 to 20 parts of ethylene. To prepare 100 parts of the binary graft copolymer, the control range of the mass of the monomer component is: 35 to 50 parts for (meth) acrylate and 10 to 20 parts for phenylethyl group.
本发明中,乳液聚合用的乳化剂在体系中的浓度通常为 0. 2 % - 0. 6 %,优选浓度为 0. 35 %。 聚合反应的乳化体系可以采用的乳化剂 有: 高级脂肪醇硫酸酯, 如十二烷基硫酸钠、 十六烷基硫酸钠、 十 八烷 酸钠(该材料系阴离子乳化剂与丙烯酸类乳化相融)等, 以 及山梨醇酐单油酸酯、 月桂酸酯、 单硬脂酸酯等, 純度均为工业用 一级品以上。 在不针对特殊纸基和织物的通常条件下, 优先选用十 八坑 酸钠和山梨醇酐单油酸酯和单硬脂酸酯作为复合乳化剂。 5%。 The preferred concentration is 0.35%. The emulsifiers used in the polymerization system can be: higher fatty alcohol sulfates, such as sodium lauryl sulfate, sodium cetyl sulfate, sodium octadecanoate (this material is an anionic emulsifier and an acrylic emulsion phase). Melt, etc. And sorbitan monooleate, laurate, monostearate, etc., the purity is industrial grade first or more. In the usual conditions not for special paper bases and fabrics, sodium decanoate and sorbitan monooleate and monostearate are preferred as complex emulsifiers.
本发明中, 以优选的十八烷基硫酸钠和山梨醇酐单油酸酯、 单 硬月旨酸和三乙醇胺作为复合乳化剂为例, 如果要制备 100份的接枝 共聚物, 乳化剂用量的控制范围为: 山梨醇酐单油酸酯 ~ 0.25份, 十八烷 酸钠 ~ 0.1份, 三乙醇胺 ~ 0.2份  In the present invention, a preferred octadecyl sulfate and sorbitan monooleate, mono-hard acid and triethanolamine are used as a composite emulsifier, if 100 parts of a graft copolymer, an emulsifier, is to be prepared. The dosage range is controlled by: sorbitan monooleate ~ 0.25 parts, sodium octadecanoate ~ 0.1 parts, triethanolamine ~ 0.2 parts
本发明中, 引发剂在体系中的浓度通常为 0.05% ~0.2%, 优 选浓度为 0.15%。 引发剂可使用强氧化剂,如过硫酸钟,过硫酸铵, 过氧化苯甲酰, 过氧化氢等; 或偶氛类引发剂如偶氮二异丁腈、 偶 氮二异戊醛等; 或铈盐; 或氧化还原体系引发剂, 如过硫酸钟-亚 硫酸氢钠, 过硫酸铵一亚硫酸氢钠、 过硫酸钾一硫酸亚铁、 过硫酸 钾一硫代硫酸钠等, 纯度均为工业用一级品及化学纯、 分析纯。 对 于聚 [(甲基)丙烯酸- (甲基)丙烯酸酯-苯乙烯] -淀粉接枝共 聚, 优先选用过硫酸钾或过硫酸钟 -亚硫酸氢钠作为聚合反应的引 发剂; 而对于聚 [(甲基)丙烯酸酯-苯乙烯] -淀粉接枝共聚, 优 先选用偶氮二异丁腈作为聚合反应的引发剂。 在接枝中, 当聚合分 子量达到 3万以上时, 亲水性较好。  In the present invention, the concentration of the initiator in the system is usually 0.05% to 0.2%, preferably 0.15%. The initiator may use a strong oxidizing agent such as a persulfate clock, ammonium persulfate, benzoyl peroxide, hydrogen peroxide or the like; or an ionic initiator such as azobisisobutyronitrile, azobisisovaleral or the like;铈 salt; or redox system initiator, such as persulfate clock-sodium bisulfite, ammonium persulfate-sodium bisulfite, potassium persulfate-ferrous sulfate, potassium persulfate-sodium thiosulfate, etc., purity Industrial first-class products and chemically pure, analytically pure. For poly[(meth)acrylic acid-(meth)acrylate-styrene]-starch graft copolymerization, potassium persulfate or sodium persulfate-sodium bisulfite is preferred as the initiator for the polymerization reaction; (Meth) acrylate-styrene]-starch graft copolymerization, azobisisobutyronitrile is preferred as the initiator of the polymerization reaction. In the grafting, when the amount of the polymerized molecules reaches 30,000 or more, the hydrophilicity is good.
本发明中, 以优选的过硫酸钟-亚硫酸氢钠引发剂为例, 对于 100质量份的接枝共聚物, 引发剂用量控制范围为: 亚硫酸氢钠 ~ 0.1份, 过硫酸钾~ 0.05份。  In the present invention, a preferred persulfate clock-sodium bisulfite initiator is taken as an example. For 100 parts by mass of the graft copolymer, the amount of the initiator is controlled in the range of: sodium hydrogen sulfite to 0.1 part, potassium persulfate to 0.05. Share.
本发明中使用的淀粉为醚化度 0.7-1.2的改性淀粉,通常是用 环氧丙烷为醚化剂、 环氧氯丙烷为交联剂得到的醚化淀粉, 能直接 从市场上购买或由本领域普通技术人员利用常规手段制得。  The starch used in the present invention is a modified starch having a degree of etherification of 0.7-1.2, usually an etherified starch obtained by using propylene oxide as an etherifying agent and epichlorohydrin as a crosslinking agent, which can be directly purchased from the market or It is prepared by one of ordinary skill in the art using conventional means.
本发明中, 相对于 100质量份的淀粉接枝共聚物而言, 淀粉的 用量为 18~25份, 优选为 25份。 接枝率在 25%以上, 才能保证亲 水性。 本发明中, 将由(曱基)丙烯酸、(甲基)丙烯酸酯和苯乙烯构 成、 或由 (甲基)丙烯酸酯和苯乙烯构成的单体混合物加入由乳化 剂和引发剂构成的乳液体系中, we (对于 (甲基)丙烯酸、(甲基) 丙烯酸酯和苯乙烯三元体系)或 60°C (对于(甲基)丙烯酸酯和苯 乙烯二元体系)条件下引发聚合。 体系温度自动升高, 当体系温度 达到 85°C时,即加入醚化度 0. 7 - 1. 2的改性淀粉,控制温度在 70 ~ 85 °C H牛下, 继续反应 1 ~ 2小时, 当体系达到一定的粘度要求时, 即降温停止反应, 得到聚 [丙烯酸(酯) -苯乙烯] -淀粉接枝共 聚物, 接枝率在 25 %以上。 In the present invention, the amount of the starch is from 18 to 25 parts, preferably 25 parts, per 100 parts by mass of the starch graft copolymer. The grafting rate is above 25% to ensure hydrophilicity. In the present invention, a monomer mixture composed of (meth)acrylic acid, (meth) acrylate and styrene, or composed of (meth) acrylate and styrene is added to an emulsion system composed of an emulsifier and an initiator. , we (for (meth)acrylic acid, (meth) acrylate and styrene ternary systems) or 60 ° C (for (meth) acrylate and styrene binary systems) initiated polymerization. The temperature of the system is automatically increased. When the temperature of the system reaches 85 °C, the modified starch with a degree of etherification of 0.7 to 1.2 is added, and the temperature is controlled at 70 to 85 °C, and the reaction is continued for 1 to 2 hours. When the system reaches a certain viscosity requirement, that is, the temperature is stopped to stop the reaction, and a poly[acrylic acid (styrene)-styrene]-graft copolymer is obtained, and the graft ratio is 25% or more.
对于聚〖丙烯酸(酯) -苯乙烯] -淀粉接枝共聚物产物的确 定, 为了排除物理混合的情况, 取上述反应完成后的乳液样品加入 一定量的无水乙醇使其发生沉淀, 向过滤后的沉淀产物加入 0. 5mol / L的 NaOH溶液, 50°C 下搅拌 1小时分离未接枝的淀粉, 过滤 后的沉淀产物用纸袋装好, 置于索氏萃取器中以甲苯为萃取剂回流 萃取 24小时以除去苯乙烯及丙烯酸、 丙烯酸酯的均聚物, 最后纸袋 中的产物干燥固化后即得到纯接枝产物。 对固化的純接枝产物进行 红外光 i瞽分析,观察谱图上 1726 cnf1的羰基 (C-0)的特征吸收峰等非 淀粉分子的吸收峰,确定形成了聚 [丙烯酸(酯) -苯乙烯] -淀粉 接枝共聚物。 For the determination of the product of the poly(acrylic acid)-starch graft copolymer, in order to eliminate the physical mixing, the emulsion sample after the completion of the above reaction is added with a certain amount of absolute ethanol to cause precipitation, and filtration is performed. After the precipitated product was added to a 0.5 mol / L NaOH solution, the ungrafted starch was separated by stirring at 50 ° C for 1 hour, and the filtered precipitated product was packed in a paper bag and placed in a Soxhlet extractor to extract with toluene. The agent was reflux-extracted for 24 hours to remove the homopolymer of styrene and acrylic acid and acrylate. Finally, the product in the paper bag was dried and solidified to obtain a pure graft product. Infrared photodetection of the solidified grafted product was carried out to observe the absorption peaks of non-starch molecules such as the characteristic absorption peak of the carbonyl (C-0) of 1726 cnf 1 on the spectrum, and it was confirmed that poly [acrylic acid] was formed. Styrene]-starch graft copolymer.
经过上述过程得到的聚 [丙烯酸(酯) -苯乙烯 ] ―淀粉接枝 共聚物呈分散在乳液中的状态, 在乳液直接使用的情况下, 要求在 25 °C条件下旋转粘度计测量得到的粘度为 300 ~ 1600pa 's,pH值 7 ~ 9 , 而通过丙酮和水萃取单体自身聚合、未接到淀粉分子上而形成的 均聚物, 测得均聚物的含量 0. 3 %。  The poly[acrylic acid (styrene)-styrene graft copolymer obtained by the above process is dispersed in the emulsion, and in the case of direct use of the emulsion, it is required to be measured by a rotational viscometer at 25 °C. The content of the homopolymer is 0.3%, and the homopolymer content is 0. 3 %.
这样得到的接枝共聚物乳液可以直接使用, 也可以用本领域公 知的手段进行分离、 干燥、 提纯后使用。  The graft copolymer emulsion thus obtained can be used as it is, or can be isolated, dried and purified by means known in the art.
下面, 描述本发明的接枝共聚物在转移印花中的用途。 这样得到的接枝共聚物可以用来制备本发明的冷转移印花紙用 的色素隔离剂, 它包含上述的聚 [丙烯酸(酯) -苯乙烯〗与淀粉 构成的接枝共聚物、 硫酸化油、 磷酸酯以及作为填料的二氧化硅或 坡缕石。 所述的冷转移印花纸用色素隔离剂可以应用于柔性版印刷 机、 凹版印刷机、 网屏印花机等各种印刷机,印刷各类织物专用的转 移印花纸。 Next, the use of the graft copolymer of the present invention in transfer printing will be described. The graft copolymer thus obtained can be used for preparing the pigment release agent for cold transfer printing paper of the present invention, which comprises the above-mentioned graft copolymer of poly[acrylic acid]-styrene and starch, sulfated oil. , phosphate esters and silica or palygorskite as fillers. The pigment release agent for cold transfer printing paper can be applied to various printing machines such as flexographic printing machines, gravure printing machines, screen printing machines, and the like, and printing transfer printing papers for various fabrics.
按照本发明制备的冷转移印花纸用的色素隔离剂, 按质量百分 比含有: 聚 [丙烯酸(酯) -苯乙烯] -淀粉接枝共聚物 35% - 85 %; 作为填料的二氧化硅 0.05% -0.5%或坡缕石 (palygorskite) 3 % - 9 %; 作为助剂的硫酸化油类物展 0.2 % - 1.8 %、 消泡剂 0.1 % - 0.8 % , 润湿剂 0.5% -2%, 余量为水。  The pigment release agent for cold transfer printing paper prepared according to the present invention contains, by mass percentage: poly [acrylic acid (styrene)-styrene]-starch graft copolymer 35% - 85 %; silica as a filler 0.05% -0.5% or palygorskite 3 % - 9 %; sulphated oil as additive auxiliaries 0.2% - 1.8 %, defoamer 0.1 % - 0.8 %, wetting agent 0.5% -2%, The balance is water.
本发明中, 添加少量的固态物质作为填料, 而添加较少量的液 态物质作为助剂, 用于改善体系的某些性质, 便于应用。  In the present invention, a small amount of a solid substance is added as a filler, and a smaller amount of a liquid substance is added as an auxiliary agent for improving certain properties of the system and being convenient for application.
本发明中, 填料类物质主要为超微粉体级的二氧化硅(如气相 级二氧化硅、纳米级二氧化硅)或硅酸盐或坡缕石(palygorskite), 视针对性织物而异选择使用。  In the present invention, the filler materials are mainly ultrafine powder grade silica (such as vapor phase silica, nano silica) or silicate or palygorskite, depending on the targeted fabric. Choose to use.
本发明中, 硫酸化油类物质包括如蓖麻油硫酸酯, 十八烷基硫 酸钠等, 通常使用蓖麻油疏酸钠。  In the present invention, the sulfated oily substance includes, for example, castor oil sulfate, sodium stearyl sulfate, etc., and sodium oleoate is usually used.
本发明中, 消泡剂包括磷酸酯类如磷酸三丁酯、醇类如正辛醇。 在不针对特殊纸基和织物的通常条件下, 优选鱗酸三丁酯。  In the present invention, the antifoaming agent includes a phosphate such as tributyl phosphate and an alcohol such as n-octanol. Tributyl phthalate is preferred under the usual conditions not for special paper bases and fabrics.
本发明中, 根据针对性织物的不同, 可以选择性添加润湿剂羧 基吡咯烷酮等。  In the present invention, a wetting agent, carboxypyrrolidone or the like, may be optionally added depending on the intended fabric.
本发明中的填料和助剂均可从市场上购买, 纯度均为工业 用 .CP级或 AR级.  The fillers and auxiliaries of the present invention are commercially available, and the purity is industrial. CP grade or AR grade.
制备上述冷转移印花紙用的色素隔离剂的方法如下。在本发明制 备的聚 [丙烯酸(酯) -苯乙烯 ] -淀粉接枝共聚物中加入助剂与 填料, 即得到本发明的冷转移印花纸用的色素隔离剂。 具体来讲, 上述的色素隔离剂是通过在所述的接枝共聚物中加入硫酸化油、 磷 酸酯以及作为填料的二氧化硅或坡缕石得到的。 The method of preparing the above-described pigment release agent for cold transfer printing paper is as follows. In the poly[acrylic acid (styrene)-starch graft copolymer prepared by the present invention, an auxiliary agent and a filler are added to obtain a pigment release agent for cold transfer printing paper of the present invention. Specifically, The above-mentioned dye release agent is obtained by adding a sulfated oil, a phosphate ester, and silica or palygorite as a filler to the graft copolymer.
按照上述生产的色素隔离剂与染料组分的相容性优良,乳胶稳定 性好, 成膜和光稳定性高。 但是应注意, 在聚〖丙烯酸(酯) -苯 乙烯] -淀粉接枝共聚物体系的丙烯酸(酯) -苯乙烯共聚过程中, 如果接枝度过高,涂膜会变硬,对冷转移印花纸隔离层有不良影响, 因此要控制丙烯酸单体的浓度< 6%,苯丙的聚合分子量在 3万以上, 接枝率达到 25 %以上。 该色素隔离剂有较好的化学稳定性和机械稳 定性, 具有极佳的适印性。 而且它的流变特性非常适用于各种类型 的涂布设备。 即使是在最苛刻的奈件下也能保证良好运转, 能提供 优异的抗湿摩擦性, 避免了纸张印花生产时的错版、 断纸等故障。  The pigment release agent produced as described above is excellent in compatibility with the dye component, has good latex stability, and has high film formation and light stability. However, it should be noted that in the process of copolymerization of poly(acrylic acid)-starch graft copolymer system, if the degree of grafting is too high, the coating film will become hard and cold transfer The printing paper insulation layer has an adverse effect, so the concentration of the acrylic monomer is controlled to be < 6%, the polymerization molecular weight of the styrene-acrylic acid is more than 30,000, and the grafting ratio is more than 25%. The pigment spacer has good chemical stability and mechanical stability, and has excellent printability. And its rheological properties are ideal for all types of coating equipment. It guarantees good operation even under the most demanding parts, provides excellent wet rub resistance, and avoids malfunctions such as misprints and paper breaks during paper printing.
以优选方案为模型,具体描述冷转移印花纸用的色素隔离剂制备 操作如下: 将三乙醇胺、 十二烷基硫酸钠(月桂醇硫酸钠)与水构成 乳化液, 在搅拌条件下加入亚硫酸氢钠和过硫酸钾, 升温到 50°C作 为引发剂, 将(甲基)丙烯酸, (甲基) 丙烯酸酯(如丙烯酸丁酯, 曱基丙烯酸乙酯等)与苯乙烯单体混合液滴加入该引发乳化剂中, 引发聚合。 体系温度自动升高, 当温度达到 85°C, 加入醚化度 0. 7 - 1. 2的改性淀粉, 控制温度在 70 85°C条件下, 继续反应 lh-2h, 实现丙烯酸(酯) -苯乙烯共聚体与淀粉的接枝共聚, 接枝率在 28 %左右。 再在上述共聚乳液中加入超微粉体级的二氧化硅或硅酸盐 或坡缕石、 蓖麻油硫酸钠、 磷酸三丁酯, 视需要, 加入润湿剂羧基 吡咯烷酮, 用水调整到 100 % , 即获得冷转移印花纸用的色素隔离 剂。 该冷转移印花纸用的色素隔离剂呈乳白色液体, 粘度为 300 ~ 1600pa · s, 察恩杯 2号杯在 25 °C时的流速为 20 - 70秒。  Taking the preferred scheme as a model, the preparation process of the pigment release agent for cold transfer printing paper is specifically described as follows: triethanolamine, sodium lauryl sulfate (sodium lauryl sulfate) and water are used as an emulsion, and sulfurous acid is added under stirring. Sodium hydrogen hydride and potassium persulfate, heated to 50 ° C as an initiator, mixed with (meth)acrylic acid, (meth) acrylate (such as butyl acrylate, ethyl methacrylate) and styrene monomer The addition of the initiating emulsifier initiates polymerization. The temperature of the system is automatically increased. When the temperature reaches 85 ° C, the modified starch with a degree of etherification of 0.7 to 1.2 is added. The temperature is controlled at 70 85 ° C, and the reaction is continued for 1 h to 2 h to achieve acrylic acid. - Graft copolymerization of styrene copolymer with starch, the graft ratio is about 28%. Further, an ultrafine powder grade silica or silicate or palygorskite, castor oil sodium sulfate, and tributyl phosphate is added to the above copolymer emulsion, and if necessary, a wetting agent, carboxypyrrolidone, is added, and the water is adjusted to 100%. That is, a pigment spacer for cold transfer printing paper is obtained. The pigment release agent for the cold transfer printing paper is a milky white liquid having a viscosity of 300 to 1600 Pa·s, and the Charon Cup No. 2 cup has a flow rate of 20 to 70 seconds at 25 °C.
本发明所述的冷转移印花紙用色素隔离剂可以应用于纤维素纤 维、 毛、 棉、 丝绸等天然纤维织物, 或涤纶、 锦纶、 腈纶等合成纤 维织物用的冷转移印花纸、 喷墨转移冷转移印花纸及冷转移印花工 艺上。 原先冷转移印花纸由于隔离剂的亲水性与疏水性不平衡及不 完整性, 导致染料与纸张纤维发生固着现象, 以致转印完毕的纸张 残余色料几近 50 % , 即使 86年就开始研究湿法转移的国外厂家也 因为隔离剂得不完整性与不彻底屏蔽色素而导致转移率低, 纸基染 料残留量过大, 而既浪费原料又严重污染环境。 由于本发明的冷转 移印花紙所用色素隔离剂的主体成分是一种高分子接枝共聚物, 涂 布在转移印花紙的纸基上, 能形成类似膜状的介质, 可以产生暂溶 性的屏蔽, 使染料在印刷工具印制花纹时, 与转移印花纸的纸基不 产生强有力的亲和性, 并能促使染料油墨 ί艮快剥离转印到织物上。 尤其是本发明所述的色素隔离剂应用于喷墨转移印花有着优异的效 果。 由于数码喷墨印花中, 整个图像是由细小的色点组成, 要求有 较高的喷射墨点密度。 这就是通常称谓的分辨率。 不同的基布对分 辨率的要求也不同。 织物的纱支, 密度和织物组织规格都会影响分 辨率, 因而目前世界上喷墨印花都需在织物表面上一层接触层, 以 便墨点着色, 然后通过蒸化、 水洗, 最后完成印花工序。 即使荷兰 ST0YK公司设备生产能力也仅有 4. 6m7h。 这种工艺限制了数码喷墨 的发展。 而涂布本发明的冷转移涂层后, 喷墨就筒单了, 产量也能 大幅度提高。 本发明的转移涂层, 能够接受 dpi 360 - 720的色点, 及超精细 720 dpi X 720 dpi色点。 纺织品上图像精细度达到荷兰 ST0YK公司活性染料喷墨印花标准。 The pigment release agent for cold transfer printing paper according to the present invention can be applied to natural fiber fabrics such as cellulose fibers, wool, cotton, silk, or cold transfer printing paper for synthetic fiber fabrics such as polyester, nylon, acrylic, and inkjet transfer. Cold transfer printing paper and cold transfer printing Art. The original cold transfer printing paper caused the dye and paper fibers to be fixed due to the imbalance and incompleteness of the hydrophilicity and hydrophobicity of the release agent, so that the residual color of the transferred paper was nearly 50%, even after 86 years. Foreign manufacturers who study wet transfer also have low transfer rate due to incompleteness of the release agent and incompletely shielding the pigment, and the residual amount of paper-based dyes is too large, which wastes raw materials and seriously pollutes the environment. Since the main component of the pigment release agent used in the cold transfer printing paper of the present invention is a polymer graft copolymer coated on a paper base of transfer printing paper, a film-like medium can be formed, and a temporary shielding can be produced. When the dye is printed on the printing tool, it does not have a strong affinity with the paper base of the transfer printing paper, and can promote the transfer of the dye ink to the fabric. In particular, the pigment release agent of the present invention has an excellent effect on inkjet transfer printing. Since digital inkjet printing, the entire image is composed of fine color dots, a higher jet dot density is required. This is the resolution of the usual title. Different base fabrics have different resolution requirements. The yarn count, density and fabric texture of the fabric all affect the resolution. Therefore, in the world, inkjet printing requires a layer of contact on the surface of the fabric to color the dots, and then through steaming, water washing, and finally finishing the printing process. Even the production capacity of the Netherlands ST0YK company is only 4. 6m7h. This process limits the development of digital inkjet. After the cold transfer coating of the present invention is applied, the ink jet is discharged, and the yield can be greatly improved. The transfer coating of the present invention is capable of accepting color points of dpi 360 - 720 and ultra fine 720 dpi X 720 dpi color points. The image fineness on textiles reaches the Dutch ST0YK reactive dye inkjet printing standard.
上述的冷转移印花纸用色素隔离剂可以应用于柔性版印刷机、 凹版印刷机、网屏印花机等各种印刷机,印刷各类织物专用的转移印 花纸。 具体来讲, 可通过圆网印花机、 平网印花机、 凹版印刷机、 柔版印刷机、 平板胶印机和喷墨打印机印制精细、 多彩、 层次丰富 的转移印花纸。  The above-mentioned pigment release agent for cold transfer printing paper can be applied to various printing machines such as flexographic printing machines, gravure printing machines, screen printing machines, and the like, and printing transfer papers for various types of fabrics. Specifically, fine, colorful, and layered transfer printing paper can be printed by a rotary screen printing machine, a flat screen printing machine, a gravure printing machine, a flexographic printing machine, a flatbed offset printing machine, and an inkjet printer.
柔性版印刷是使用柔性树脂印版、 通过网紋传墨辊传递油墨施 印的方法, 具有凸印特性, 从其印刷特性来说, 它是柔性的橡胶面 与印刷纸张接触, 具有胶印特性, 从转印纸材料说、 它使用水性油 墨, 并能通过网穴印刷, 具有凹印特性。 柔印是一种轻压力印刷工 艺, 其印刷线压力为 lkgf /cm左右。 同时柔版印刷的墨层厚度约为 5~10%QiM。 凹版印刷的印版图文部份低于印版表面, 以凹下网穴的 深浅疏密大小表现图文的层次密度。 凹版属于直接印刷, 印版凹入 部分的油墨直接转移到承印物上形成图象部分, 印刷时, 油墨涂布 在印版上, 然后用刮刀刮去印版表面空白处的油墨, 填入凹下部分 的油墨保¾下来, 经印刷压力作用转印到承印物表面完成印刷。 凹 印的印刷线压力为 ll ~ 18kgf/cm。但由于凹版的着墨是印版直接在 墨槽中接触油墨, 没有传墨系统, 对纸面涂层材料要求较严。 圆网 印花工艺就其印花特点来说, 是介于凹版辊筒印花和平网印花之间 的一种印花方式。 Flexographic printing is a method of printing ink through an anilox roller using a flexible resin plate, which has a embossing property, and is a flexible rubber surface in terms of its printing characteristics. In contact with printing paper, it has offset characteristics. From the transfer paper material, it uses water-based ink and can be printed by the cell, which has gravure characteristics. Flexo printing is a light pressure printing process with a printing line pressure of about lkgf / cm. At the same time, the thickness of the ink layer of flexographic printing is about 5~10% Q iM. The printing plate image of the gravure printing is lower than the surface of the printing plate, and the hierarchical density of the graphic is represented by the depth and density of the concave mesh. The gravure is direct printing, and the ink in the concave portion of the printing plate is directly transferred to the substrate to form an image portion. When printing, the ink is coated on the printing plate, and then the ink in the blank surface of the printing plate is scraped off with a doctor blade to fill the concave portion. The ink in the lower part is kept down and transferred to the surface of the substrate by printing pressure to complete the printing. The gravure printed line pressure is ll ~ 18kgf/cm. However, since the inking of the gravure is that the printing plate directly contacts the ink in the ink tank, there is no ink transfer system, and the paper coating material is required to be strict. The rotary screen printing process is a printing method between the gravure roll printing and the flat screen printing in terms of its printing characteristics.
按照本发明的制品具有由本发明的色素隔离剂形成的涂层。该制 品例如可以是冷转移印花纸,,具有在纸基表面的、 由本发明的色素 隔离剂形成的涂层。 这里的 "紙基" 可以是本领域通常使用的任何 纸基, 例如书写纸、 胶版纸、 印刷纸、 有光纸、 包装纸、 打印纸等。 用公知的涂布手段如刮刀涂布、 园网涂布、 挤压涂布、 辊涂等, 将 本发明的色素隔离剂涂布于纸基上形成冷转移印花纸。 这样的冷转 移印花纸不仅具有屏蔽载体的作用, 使得有良好的印刷适应性和转 移性, 同时在转印时, 还具有防渗化、 耐重压、 快速转印花紋图案 到织物上以及适应卷筒纸形成生产所必备的抗湿性、抗撕裂等特点。 涂有本发明所述隔离剂的转移印花纸, 还解决了转移印花纸在转移 印花时, 纸上染料残留量过大的难题, 使得转移率达到 90%以上, 不仅节省了染化料, 而且减少了对环境的污染。 因此本发明促进了 印染行业向环保经济的方向进一步发展。  The article according to the invention has a coating formed from the pigment release agent of the invention. The article may, for example, be a cold transfer printing paper having a coating formed on the surface of the paper base by the pigment release agent of the present invention. The "paper base" herein may be any paper base commonly used in the art, such as writing paper, offset paper, printing paper, glossy paper, wrapping paper, printing paper, and the like. The dye release agent of the present invention is applied onto a paper base by a known coating means such as doctor blade coating, web coating, extrusion coating, roll coating or the like to form a cold transfer printing paper. Such cold transfer printing paper not only has the function of shielding carrier, but also has good printing adaptability and transferability, and at the same time, it has anti-seepage, heavy-duty resistance, rapid transfer pattern to fabric and adapting to roll during transfer. The paper is formed into the necessary moisture resistance and tear resistance. The transfer printing paper coated with the release agent of the invention also solves the problem that the amount of dye residue on the paper is too large when the transfer printing paper is transferred, so that the transfer rate is over 90%, which not only saves the dyeing material, but also Reduced environmental pollution. Therefore, the present invention promotes the further development of the printing and dyeing industry toward the environmentally friendly economy.
以下提供实施例以更具体地描述本发明,但是本发明不受这些实 施例的任何限制。在实施例中,除非特别指明, "份"是指 "重量份"。 在下列的实施例中粘度的测定参照国家标准 GB/T1723-93《涂料 粘度测定法》使用察恩杯 涂饰杯测定。 The examples are provided below to more specifically describe the invention, but the invention is not limited by these examples. In the examples, "parts" means "parts by weight" unless otherwise specified. In the following examples, the measurement of the viscosity was carried out in accordance with the national standard GB/T1723-93 "Coating viscosity measurement method" using a Zahn cup coated cup.
实施例 1  Example 1
聚 [丙烯酸 -丙烯酸丁酯 -苯乙烯] -淀粉三元接枝共聚物制 备  Preparation of poly [acrylic acid-butyl acrylate-styrene]-starch ternary graft copolymer
在实验用反应釜中, 先将 0. 25份三乙醇胺、 5· 8份水和 0. 1份 十二垸 1^酸钠注入制成乳化液, 在搅拌条件下加入 0. 1份亚硫酸 氢钠和 0. 05份过硫酸钾, 升温到 50。C作为引发剂; 将丙烯酸丁酯 40份、 丙烯酸 4份与苯乙烯 10份单体混合液滴加到引发剂乳液中, 引发聚合后, 体系自动升温至 85°C , 即加入醚化度 0. 7 - 1. 2的改 性淀粉(羟基已屏蔽) 25份, 控制温度在 70 ~ 85°C 下, 继续反 应 lh-2h, 接枝率在 32 %左右, 实现丙烯酸(酯) -苯乙烯共聚体 与淀粉的接枝共聚, 得到用于制备色素隔离剂的聚 [丙烯酸(酯) -苯乙烯] -淀粉接枝共聚物乳液, 其中的接枝共聚物的重均分子 量约为 19000道尔顿。 将该乳液的固化物在如下条件下测定红外光 谱, 得到的红外光谱讲图见图 1。  The sulphuric acid is added in an amount of 0. 1 part of sulphuric acid. The sulphuric acid is added to the sulphuric acid. Sodium hydrogenate and 0.05 parts potassium persulfate, heated to 50. C as initiator; 40 parts of butyl acrylate, 4 parts of acrylic acid and 10 parts of styrene were added dropwise to the initiator emulsion. After the polymerization was initiated, the system was automatically heated to 85 ° C, ie, the degree of etherification was added. 7 - 1. 2 modified starch (hydroxyl shielded) 25 parts, control temperature is 70 ~ 85 ° C, continue to react lh-2h, grafting rate is about 32%, to achieve acrylic (styrene) - styrene The graft copolymerization of the copolymer and the starch gives a poly[acrylic acid]-styrene graft copolymer emulsion for preparing a pigment spacer, wherein the graft copolymer has a weight average molecular weight of about 19,000 Daer. pause. The infrared ray spectrum of the cured product of the emulsion was measured under the following conditions, and the obtained infrared spectrum is shown in Fig. 1.
仪器: NICOLET NEXUS 470; Instrument: NICOLET NEXUS 470;
方法: 多次衰减全反射 TR ); Method: multiple attenuation total reflection TR);
分辨率: 4cm—1; 扫描: 64 SCANS Resolution: 4cm- 1 ; Scan: 64 SCANS
从图 1可以看出 1103 cm-\ 1020 cm— 1是淀粉分子红外吸收峰, 756 cm_1、 696 cm— 1是笨环上的上 C-H振动吸收造成的,而 1726 cm— 1是羰 基(C=0)的特征吸收峰, 1726 cm"1, 1444 cm— 1155 cnf1表明聚合物 分子中有丙烯酸酯的结构单元,由以上分析可见丙烯酸(酯)、 苯乙 烯共聚物接枝在淀粉分子上形成了聚 [丙烯酸(酯) -苯乙烯 ] - 淀粉接枝共聚物。 在丙烯酸酯与苯乙烯与淀粉接枝时, 丙烯酸酯与 苯乙烯二者的聚合分子量达到 3万以上, 其三元共聚接枝率在 30 % 左右。 实施例 2 It can be seen from Fig. 1 that 1103 cm-\1020 cm- 1 is the infrared absorption peak of starch molecules, 756 cm _1 and 696 cm- 1 are caused by the upper CH vibration absorption on the stupid ring, and 1726 cm- 1 is the carbonyl group (C). The characteristic absorption peak of =0), 1726 cm" 1 , 1444 cm - 1155 cnf 1 indicates that there are structural units of acrylate in the polymer molecule. From the above analysis, it is seen that the acrylic acid (meth) and styrene copolymer are grafted on the starch molecule. Poly[acrylic acid (styrene)-starch graft copolymer is formed. When acrylate and styrene are grafted with starch, the polymerization molecular weight of acrylate and styrene is more than 30,000, and the ternary copolymerization thereof The grafting rate is around 30%. Example 2
聚 [ (甲基) 丙烯酸酯 -苯乙烯] -淀粉二元接枝共聚物制备 在实验用反应釜中, 先将 0. 25份三乙醇胺、 5. 8份水和 0. 1份 十二烷 H酸钠注入制成乳化液, 在搅拌条件下加入 0. 1份偶氮二 异丁腈 (AIBN) , 升温到 60°C作为引发剂; 将甲基丙烯酸甲酯 40份、 与苯乙烯 10份单体混合液滴加到引发剂乳液中, 引发聚合后,体系 自动升温至 90Ό, 即加入醚化度 0. 7 - 1. 2的改性淀粉(羟基已屏 蔽) 20份, 控制温度在 75 ~ 85 °C条件下, 继续反应 lh- 2h, 实现甲 基丙烯酸酯-苯乙烯共聚体与^:粉的接枝共聚。 重均分子量约为 15000道尔顿。 聚合分子量在 3万以上, 接枝率在 32 %左右, 亲水 性良好。  1份的十二烷之间。 The poly [(meth) acrylate-styrene] - starch binary graft copolymer was prepared in the experimental reactor, first 0.25 parts of triethanolamine, 5.8 parts of water and 0.1 parts of dodecane Sodium sulphate was injected into an emulsion, and 0.1 parts of azobisisobutyronitrile (AIBN) was added under stirring, and the temperature was raised to 60 ° C as an initiator; 40 parts of methyl methacrylate and styrene 10 were added. The monomer mixed droplets are added to the initiator emulsion, and after the polymerization is initiated, the system is automatically heated to 90 Torr, that is, the modified starch (hydroxyl shielded) having a degree of etherification of 0.7 to 1.2 is added, and the temperature is controlled. Under the condition of 75 ~ 85 °C, the reaction was continued for lh-2h to realize the graft copolymerization of methacrylate-styrene copolymer and ^: powder. The weight average molecular weight is about 15,000 Daltons. The molecular weight of the polymerization is 30,000 or more, the graft ratio is about 32%, and the hydrophilicity is good.
实施例 3  Example 3
色素隔离剂的制备  Preparation of pigment spacer
在实施例 1中所得到的聚〖丙烯酸(酯) -苯乙烯] -淀粉接 枝共聚物 75份共聚乳液中加入超微粉体级的二氧化硅 0. 3份、蓖麻 油硫酸钠 0. 3份、 坡缕石 ( palygorskite ) 1 适量的水, 在搅 拌均匀上述物质后, 再加入磷酸三丁酯 0. 3份及! ½吡^各坑酮 0. 2 份, 最后用水调整到 100份(100 % ), 即为冷转移印花纸用的色素 隔离剂 (下文称为 "PE - 2 ¾" )。  3份的蓖麻油硫酸0. 0. 3 parts of castor oil sodium sulfate 0. 3 parts of eucalyptus oil sodium sulfate 0. 3份和三丁的三丁酯。 3 parts, palygorskite (palygorskite) 1 amount of water, after stirring the above substances, then added tributyl phosphate 0.3 parts and! 1⁄2 pyridine ketone 0. 2 parts, and finally adjusted to 100 parts (100%) with water, which is a pigment release agent for cold transfer printing paper (hereinafter referred to as "PE - 2 3⁄4").
这种冷转移印花纸用的色素隔离剂呈兰光乳白色液体, 固含量 在 48 %左右, 粘度为 800 ~ 900pa · s, 25 °C奈件下察恩杯 2号杯流 速为 30 - 40秒。  The pigment spacer for the cold transfer printing paper is a blue-light milky white liquid with a solid content of about 48% and a viscosity of 800 to 900 Pa·s. The flow rate of the 2nd cup of the Zahn Cup is 25 - 40 seconds at 25 °C. .
该色素隔离剂乳液使用下述仪器和方法进行核磁共振(简称 NMR ) 实验, NMR实 普图如图 2所示。  The pigment spacer emulsion was subjected to nuclear magnetic resonance (NMR) experiments using the following apparatus and method, and the NMR actual map is shown in Fig. 2.
仪器: Bruker DMX500核磁共振仪;  Instrument: Bruker DMX500 NMR;
方法: 重水 D20体系乳液, MIL Method: Heavy water D 2 0 system emulsion, MIL
从图 2可以看到,化学位移 δ为 1. 5 ~ 2. 5ppm的质子峰主要是淀 粉上所接枝的丙烯酸 -丙烯酸丁酯 -苯乙烯共聚物骨架上的亚甲基和 次甲基的信号峰。 δ为 3.3~4.01ppm的质子峰主要是淀粉分子中 CI, C4, C5, C6 和丙烯酸丁酯中酯基的与氧原子相连的碳上的氢原子 所产生的。 δ为 4.7ppm左右的峰是由于乳液中残余的水分子中的氢 造成的。 δ为 5.0 ~ 6.2 ppm的语峰是淀粉分子中与 C6相连的羟基中 的盾子峰和其他体系中残余的引发剂乳化剂等的信号峰。 δ为It can be seen from Fig. 2 that the chemical shift δ is 1. 5 ~ 2. 5ppm of the proton peak is mainly A signal peak of methylene and methine on the acrylic-butyl acrylate-styrene copolymer backbone grafted onto the powder. The proton peak with a δ of 3.3 to 4.01 ppm is mainly produced by hydrogen atoms on the carbon of the ester group in the starch molecule, CI, C4, C5, C6 and butyl acrylate. A peak having a δ of about 4.7 ppm is caused by hydrogen in residual water molecules in the emulsion. The peak of δ of 5.0 ~ 6.2 ppm is the signal peak of the shield peak in the hydroxyl group attached to C6 in the starch molecule and the residual initiator emulsifier in other systems. δ is
9.55ppm的傅峰是淀粉分子在接枝共聚反 引发剂的作用下 C2 -C3 之间开环断键后在 C2位置所形成的醛基上的质子峰, 而 C3则成为 接枝位点。 由以上分析可见, 丙烯酸-丙烯酸丁酯-苯乙烯共聚物 接枝在淀粉分子的 C3上,形成了聚[丙烯酸 -丙烯酸丁酯 -苯乙烯] -淀粉接枝共聚物。 接枝率在 32%左右。 The peak of 9.55ppm is the proton peak of the aldehyde group formed at the C2 position after the ring-opening bond between the C2 and C3 under the action of the graft copolymerization counterinitiator, and C3 becomes the grafting site. From the above analysis, it was found that the acrylic acid-butyl acrylate-styrene copolymer was grafted on the C3 of the starch molecule to form a poly[acrylic acid-butyl acrylate-styrene]-starch graft copolymer. The graft ratio is about 32%.
实施例 4  Example 4
全棉型织物应用冷转移印花纸用色素隔离剂  Cotton fabrics for pigment transfer agents for cold transfer printing paper
按质量百分比配方:  Formulated by mass percentage:
聚 [丙烯酸(酯) -苯乙烯] -淀粉接枝共聚物 ~72。/0, 气相级二氧化桂为 0.3%, Poly [acrylic acid - styrene] - starch graft copolymer ~ 72. / 0 , gas phase grade osmolality is 0.3%,
蓖麻油硫酸钠为 0.7%  Castor oil sodium sulfate is 0.7%
磷酸三丁酯为 0.2%  Tributyl phosphate is 0.2%
用水调整到 100%.  Adjust water to 100%.
工业用反应釜中, 先将 2.5kg三乙醇胺、 58kg水和 lkg山梨醇 酐单油酸酯注入制成乳化液, 在搅拌条件下加入 lkg亚硫酸氢钠和 0.5kg过硫酸钾, 升温到 50°C作为引发剂; 将丙烯酸丁酯 400kg、 丙烯酸 40kg与苯乙烯 100kg单体混合液滴加到引发剂乳液中,引发 聚合后, 体系自动升温到 85°C, 即加入醚化度 0.7-1.2的改性淀 粉(羟基已屏蔽) 180kg, 控制温度在 70~85°C条件下, 继续反应 lh-2h, 实现丙烯酸(酯) -苯乙烯共聚体与淀粉的接枝共聚, 重均 分子量约为 19000道尔顿。 聚合分子量达到 3.5万以上。 在此共聚 乳液中加入气相级二氧化硅 3kg、蓖麻油硫酸钠 2kg、在搅拌均匀上 述物质后, 再加入磷酸三丁酯 4kg, 最后用水调整到 1000kg (100 % ), 即为冷转移印花纸用棉型色素隔离剂。这种棉型冷转移印花纸 用的色素隔离剂呈乳白色液体, 粘度为 ~ 900pa ' s, 25°C条件下察 恩杯 2号杯流速为 40秒左右。 In the industrial reactor, 2.5kg of triethanolamine, 58kg of water and lkg sorbitan monooleate are firstly injected into an emulsion, and lkg sodium hydrogen sulfite and 0.5kg potassium persulfate are added under stirring to raise the temperature to 50. °C as initiator; 400kg of butyl acrylate, 40kg of acrylic acid and 100kg of styrene were added dropwise to the initiator emulsion. After the polymerization was initiated, the system was automatically heated to 85 °C, ie, the degree of etherification was 0.7-1.2. Modified starch (hydroxyl shielded) 180kg, controlled temperature at 70~85 °C, continue to react for lh-2h, achieve graft copolymerization of acrylic acid-styrene copolymer and starch, weight average molecular weight is about 19000 Daltons. The molecular weight of the polymerization reaches 35,000 or more. Copolymerization here Grade silica added to the emulsion vapor 3kg, sodium castor oil 2 kg, after stirring uniformly the foregoing, tributyl phosphate added 4kg, and finally water was adjusted to 1000kg (100%), cold transfer printing paper that is cotton Type pigment spacer. The pigment spacer for the cotton type cold transfer printing paper is a milky white liquid with a viscosity of ~900pa's, and the flow rate of the 2nd cup of the Chaen Cup is about 40 seconds at 25 °C.
实施例 5  Example 5
人工合成纤维素纤维应用冷转移印花纸用色素隔离剂  Synthetic cellulose fiber using pigment release agent for cold transfer printing paper
按质量百分比配方:  Formulated by mass percentage:
聚 [丙烯酸(酯) -苯乙烯] -淀粉接枝共聚物 ~85%, 二氧化硅 0.5 % ,  Poly [acrylic acid-styrene]-starch graft copolymer ~85%, silica 0.5%,
蓖麻油减酸钠为 10%  Castor oil sodium reduction is 10%
磷酸三丁酯为 0.1%,  Tributyl phosphate is 0.1%,
水为 4.4%.  The water is 4.4%.
粘度为 900 ~ 1200pa · s, 25°C条件下察恩杯 2号杯流速为 70 秒。  The viscosity is 900 ~ 1200pa · s, and the flow rate of the 2nd cup of the Zahn Cup is 25 seconds at 25 °C.
工业用反应釜中, 先将 2.5kg二乙胺基乙醇、 58kg水和 lkg十 六烷基硫酸钠(鲸蜡醇硫酸钠)注入制成乳化液, 在搅拌条件下加入 lkg硫代硫酸钠和 0.5kg过硫酸钟, 升温到 50°C作为引发剂; 将丙 烯酸丁酯 400kg、 丙烯酸 60kg与苯乙烯 180kg单体混合液滴加到引 发剂乳液中,引发聚合后,体系自动升温至 85°C,即加入醚化度 0.7 In an industrial reactor, 2.5 kg of diethylaminoethanol, 58 kg of water and lkg of sodium cetyl sulfate (sodium cetyl sulfate) are firstly injected into an emulsion, and lkg sodium thiosulfate and lkg are added under stirring. 0.5kg persulfate clock, heating to 50 °C as initiator; 400 kg of butyl acrylate, 60 kg of acrylic acid and 180 kg of styrene were added dropwise to the initiator emulsion, and after the polymerization was initiated, the system was automatically heated to 85 ° C. , that is, the degree of etherification is 0.7
-1.2的改性淀粉(羟基已屏蔽) 210kg,控制温度在 70~85°C条件 下, 继续反应 lh-2h, 实现丙烯酸(酯) -苯乙烯共聚体与淀粉的 接枝共聚,重均分子量约为 22000道尔顿。。在此共聚乳液中加入气 相级二氧化硅 5kg、 蓖麻油硫酸钠 100kg、 在搅拌均匀上迷物质后, 再加入磷酸三丁酯 lkg, 最后用水调整到 1000kg (100% ), 即为冷 转移印花纸用棉型色素隔离剂。 这种棉型冷转移印花纸用的色素隔 离剂呈乳白色液体, 粘度为 900 ~ 1200pa · s, 25°C条件下察恩杯 2 号杯流速为 70秒左右。 接枝率在 28%左右。 -1.2 modified starch (hydroxyl shielded) 210kg, controlled temperature at 70~85 °C, continue to react for lh-2h, achieve graft copolymerization of acrylic acid (styrene)-styrene copolymer and starch, weight average molecular weight It is about 22,000 Daltons. . Add 5kg of vapor phase grade silica and 100kg of castor oil sodium sulfate to the copolymer emulsion. After stirring the substance, add l-butyl phosphate lkg, and finally adjust the water to 1000kg (100%), which is cold transfer printing. Paper type pigment spacer for paper. The pigment release agent for the cotton type cold transfer printing paper is a milky white liquid with a viscosity of 900 ~ 1200 Pa · s, and the Chaen Cup 2 at 25 ° C The flow rate of the cup is about 70 seconds. The graft ratio is about 28%.
实施例 6  Example 6
真丝绸类织物应用冷转移印花纸用色素隔离剂  Silk fabrics for cold transfer printing paper
按质量百分比配方:  Formulated by mass percentage:
聚 [丙烯酸(酯) -苯乙烯] -淀粉接枝共聚物 ~ 82 % , 坡缕石 (palygorskite) 6%,  Poly [acrylic acid (styrene)-styrene]-starch graft copolymer ~ 82 %, palygorskite 6%,
蓖麻油碗酸钠为 5 %  Castor oil bowl sodium is 5 %
磷酸三丁酯为 0.2%,  Tributyl phosphate is 0.2%,
水为 6.8%.  The water is 6.8%.
粘度为 500~ 700pa · s, 25 °C条件下四号涂饰杯流速为 30秒。 工业用反应釜中, 先将 2.5kg三乙醇胺、 58kg水和 0.9KG十六 烷基硫酸钠注入制成乳化液, 在搅拌条件下加入 lkg亚硫酸氢钠和 0.5kg过硫酸钾, 升温到 50°C作为引发剂; 将丙烯酸丁酯 400kg、 丙烯酸 40kg与苯乙烯 180kg单体混合液滴加到引发剂乳液中,引发 聚合后, 体系自动升温到 85°C, 即加入醚化度 0.7 - 1.2的改性淀 粉(羟基已屏蔽) 200kg, 控制温度在 70~85°C条件下, 继续反应 lh-2h, 实现丙烯酸(酯) -笨乙烯共聚体与淀粉的接枝共聚, 重均 分子量约为 18000道尔顿。 丙烯酸酯与苯乙烯的聚合分子量在 3.2 万左右。 在此共聚乳液中加入坡缕石(palygorskite) 6%、 蓖麻油 硫酸钠 50kg、 在搅拌均匀上述物质后, 再加入礫酸三丁酯 2kg, 最 后用水调整到 1000kg (100% ), 即为冷转移印花纸用棉型色素隔离 剂。 这种棉型冷转移印花纸用的色素隔离剂呈垒光乳白色液体, 粘 度为 500 ~ 700pa■ s, 25 °C条件下四号涂饰杯流速为 30秒。  The viscosity is 500~700pa · s, and the flow rate of the fourth coated cup is 30 seconds at 25 °C. In the industrial reactor, 2.5kg of triethanolamine, 58kg of water and 0.9KG of sodium hexadecyl sulfate are injected into the emulsion, and lkg sodium hydrogen sulfite and 0.5kg potassium persulfate are added under stirring to raise the temperature to 50. °C as initiator; 400kg of butyl acrylate, 40kg of acrylic acid and 180kg of styrene were added dropwise to the initiator emulsion. After the polymerization was initiated, the system was automatically heated to 85 °C, ie, the degree of etherification was 0.7 - 1.2. Modified starch (hydroxyl shielded) 200kg, controlled temperature at 70~85 °C, continue to react for lh-2h, to achieve graft copolymerization of acrylic acid-stupyl ethylene copolymer with starch, weight average molecular weight is about 18,000 Daltons. The polymerization molecular weight of acrylate and styrene is about 32,000. Add 6% palygorskite and 50 kg of castor oil sodium sulfate to the copolymer emulsion. After stirring the above materials, add 2 kg of tributyl glutamate. Finally, adjust the water to 1000 kg (100%), which is cold. A cotton type pigment release agent for transfer printing paper. The pigment release agent for the cotton type cold transfer printing paper is a base light milky white liquid having a viscosity of 500 to 700 Pa s, and the flow rate of the fourth coated cup is 30 seconds at 25 °C.
实施例 7  Example 7
羊毛(蛋白类纤维)型织物应用冷转移印花纸用色素隔离剂 按质量百分比配方:  Wool (protein fiber) type fabrics are used as pigment release agents for cold transfer printing paper.
聚 [丙烯酸(酯) -苯乙烯] -淀粉接枝共聚物 ~75%, 气相级二氧化硅 0.2%, Poly[acrylic acid (styrene)-starch graft copolymer ~75%, Gas phase grade silica 0.2%,
蓖麻油碗酸钠为 0.4%  Castor oil bowl sodium is 0.4%
磷酸三丁酯为 0.5%,  Tributyl phosphate is 0.5%,
用水调整到 100%.  Adjust water to 100%.
工业用反应釜中, 先将 2.5kg三乙醇胺、 58kg水和 lkg聚氧乙 烯山梨醇酐单油酸酯注入制成乳化液, 在搅拌条件下加入 lkg亚硫 酸氢钠和 0.5kg过硫酸钾, 升温到 50°C作为引发剂; 将丙烯酸乙酯 340kg, 丙烯酸 60kg与苯乙烯 100kg单体混合液滴加到引发剂乳液 中, 引发聚合后, 体系自动升温到 85°C, 即加入醚化度 0.7-1.2 的改性淀粉(羟基已屏蔽) 250kg, 控制温度在 70~85°C^ 下, 继续反应 lh-2h, 实现丙烯酸(酯) -苯乙烯共聚体与淀粉的接枝 共聚, 重均分子量约为 22000道尔顿。 在此共聚乳液中加入气相二 氧化硅 2kg、 蓖麻油硫酸钠 4kg、在搅拌均匀上述物质后,再加入磷 酸三丁酯 5kg, 最后用水调整到 1000kg (100% ), 即为冷转移印花 纸用毛型色素隔离剂。 这种毛型冷转移印花纸用的色素隔离剂呈乳 白色液体, 粘度为 950 ~ HOOpa · s, 25Ό条件下察恩杯 2号杯流速 为 30 - 35秒。 接枝率达到 38 %以上。 In the industrial reactor, 2.5 kg of triethanolamine, 58 kg of water and lkg of polyoxyethylene sorbitan monooleate are firstly injected into an emulsion, and lkg of sodium hydrogen sulfite and 0.5 kg of potassium persulfate are added under stirring. The temperature is raised to 50 ° C as an initiator; 340 kg of ethyl acrylate, 60 kg of acrylic acid and 100 kg of styrene are mixed and added dropwise to the initiator emulsion. After the polymerization is initiated, the system is automatically heated to 85 ° C, ie, etherification is added. Modified starch with a degree of 0.7-1.2 (hydroxyl shielded) 250kg, controlled temperature at 70~85°C^, continued reaction for lh-2h, achieving graft copolymerization of acrylic acid-styrene copolymer and starch, heavy The average molecular weight is about 22,000 Daltons. 2 kg of fumed silica and 4 kg of sodium sesame oil were added to the copolymer emulsion. After the above materials were uniformly stirred, 5 kg of tributyl phosphate was added, and finally water was adjusted to 1000 kg (100%), which was used for cold transfer printing paper. Hair pigment spacers. The pigment release agent for this type of cold transfer printing paper is a milky white liquid with a viscosity of 950 ~ HOOpa · s, and the flow rate of the 2nd cup of the Zahn Cup is 25 - 35 seconds under the condition of 25 inches. The grafting ratio is over 38%.
实施例 8  Example 8
合成纤维(涤纶、 锦纶和腈纶)型应用冷转移印花纸用色素隔 离剂  Synthetic fiber (polyester, nylon and acrylic) type pigment spacer for cold transfer printing paper
按质量百分比配方:  Formulated by mass percentage:
聚 [(甲基) 丙烯酸酯 -苯乙烯] -淀粉接枝共聚物 ~ 82 % , 二氧化硅 0.4 %,  Poly [(meth) acrylate-styrene]-starch graft copolymer ~ 82 %, silica 0.4%,
蓖麻油碗酸钠为 0.9%  Castor oil bowl sodium is 0.9%
磷酸三丁酯为 0.7%,  Tributyl phosphate is 0.7%,
吡咯烷酮润湿剂 PH316 乳液为 2%,  Pyrrolidone wetting agent PH316 emulsion is 2%,
用水调整到 100%. 实施例 2所制备的聚 [ (甲基)丙烯酸酯 -苯乙烯] -淀粉接枝 共聚物 820 kg, 其共聚乳液中加入气相级氧化硅 4kg、 蓖麻油硫酸 钠 9kg、在搅拌均匀上述物盾后,再加入羧基吡咯綻酮润湿剂 PH316 乳液 2 kg, 磷酸三丁酯 7kg, 最后用水调整到 1000kg ( 100 % ), 即 为冷转移印花紙用合成纤维型色素隔离剂。 这种合成纤维型冷转移 印花纸用的色素隔离剂呈乳白色液体, 粘度为 ~ 900pa ' s , 25 °C条 件下察恩杯 2号杯流速为 30― 40秒。 Adjust water to 100%. The poly[(meth)acrylate-styrene]-starch graft copolymer prepared in Example 2 was 820 kg, and the copolymer emulsion was added with 4 kg of vapor phase silica, 9 kg of castor oil sodium sulfate, and the above shield was evenly stirred. Then, add 2 kg of carboxypyrrolidone wetting agent PH316, 7 kg of tributyl phosphate, and finally adjust to 1000 kg (100%) with water, which is a synthetic fiber type pigment release agent for cold transfer printing paper. The pigment spacer for the synthetic fiber type cold transfer printing paper is a milky white liquid having a viscosity of ~900pa's, and the flow rate of the 2nd cup of the Zahn Cup at 25 °C is 30-40 seconds.
上述实施例所制备的 PE - 2色素隔离剂均可涂布在纸基上供圆 网印花机、 平网印花机、 凹版印刷机、 柔版印刷机、 平板胶印机和 喷墨打印机使用。 凡采用色素隔离剂的转印纸, 通过上述各种印刷 印花设备印制的转移印花纸, 均能在与织物密合施压转印时, 完整 地«纹、 图案转印剥离到各类织物上。  The PE-2 dye release agent prepared in the above examples can be applied to a paper base for use in a rotary screen printing machine, a flat screen printing machine, a gravure printing machine, a flexographic printing machine, a flatbed offset printing press, and an ink jet printer. For the transfer paper using the pigment isolating agent, the transfer printing paper printed by the above various printing and printing equipment can be completely peeled and peeled to various fabrics when it is pressed and applied with the fabric. on.
上述实施案例都强调了粘度范围在 1200 pa · s以下, 25 °C条件 下察恩杯 2号杯流速 30 - 40秒。如果不能保持上述粘度,就会导致 纸基上的隔离剂对染料的吸附较差, 无法对该产品的上染率提升, 例如在凹板印刷时塑性很差, 图案缺 ^目应的清晰度, 察恩杯 2号 杯流速定位于 30 - 40秒是为保证涂布时刮刀与纸面及浆料间的触 变性流动性, 涂布色素隔离剂如缺乏上述的粘度计流速, 是十分难 以适应后道的印刷条件的。  The above examples all emphasize the viscosity range below 1200 pa · s, and the flow rate of the 2nd cup of the Zahn Cup at 25 °C is 30 - 40 seconds. If the above viscosity cannot be maintained, the release of the dye on the paper base will be poor, and the dyeing rate of the product will not be improved. For example, the plasticity is poor in the printing of the concave plate, and the sharpness of the pattern should be lacking. The flow rate of the 2nd cup of the Zahn Cup is positioned at 30 - 40 seconds to ensure the thixotropic fluidity between the blade and the paper and the paste during coating. It is very difficult to apply the pigment spacer such as the lack of the above viscosity meter flow rate. Adapt to the printing conditions of the latter.
实施例 9  Example 9
冷转移印花纸色素隔离剂在冷转移印花纸上的应用  Application of Cold Transfer Printing Paper Pigment Release Agent on Cold Transfer Printing Paper
纸张规格: 60g单面书写纸, 幅宽 1800醒(安黴黄山金马造纸 厂)  Paper specifications: 60g single-sided writing paper, width 1800 wake (Anmu Huangshan Jinma Paper Mill)
PE - 2浆指标: 细度 2. 5 μ ιη, 粘度 400 ~ 550cp, 25 °C ^下察 恩杯 2号杯流速为 ~ 45秒。  PE - 2 pulp index: Fineness 2. 5 μ ιη, viscosity 400 ~ 550 cp, 25 °C ^ under the cup of the cup No. 2 cup flow rate ~ 45 seconds.
将 PE - 2浆用专业涂布机均匀涂布在纸张表面, 形成色素隔离 层。 再通过印刷机在该纸张涂有色素隔离层的一面上印上图案, 就 形成冷转移印花纸。 The PE-2 slurry was uniformly coated on the surface of the paper with a professional coater to form a pigment barrier layer. Then, by printing on the side of the paper coated with the pigment isolation layer, Form a cold transfer printing paper.
实施例 10  Example 10
冷转移印花纸色素隔离剂在喷墨转移印花紙上的应用  Application of Cold Transfer Printing Paper Pigment Release Agent on Inkjet Transfer Printing Paper
纸张规格: 60g书写纸, (山东潍坊造纸厂)  Paper specifications: 60g writing paper, (Shandong Weifang Paper Mill)
涂布浆: PE- 2浆 97份, 聚乙烯吡咯梡酮 1份, 德国 3011油 2份。  Coating slurry: 97 parts of PE-2 slurry, 1 part of polyvinylpyrrolidone, 2 parts of Germany 3011 oil.
PE-2 浆先用均质机处理, 颗粒细度用细度刮板仪测量, 其细 度达到 0.25微米。 涂布方式采用西德 BABC- CK机橡毯涂布, 每 m2 涂布 9克, 每分钟涂布 30 - 40m。 The PE-2 slurry was first treated with a homogenizer, and the fineness of the particles was measured with a fineness scraper, and the fineness was 0.25 μm. The coating method is coated with West Bay BABC-CK machine blanket, 9 g per m 2 , 30-40 min per minute.
实施例 11  Example 11
涂布色素隔离剂的冷转移印花纸在柔性版印刷中的应用  Application of cold transfer printing paper coated with pigment release agent in flexographic printing
PE - 2浆指标:粘度: 450cps, 25°C条件下 4号涂饰杯流秒 45s。 采用橡毯为承压物, 刀涂法。 涂布量: 7-9 g/m2, 黄山纸业公司PE - 2 pulp index: Viscosity: 450 cps, No. 4 painted cups at 25 ° C for 45 s. The rubber blanket is used as the pressure bearing material and the knife coating method. Coating amount: 7-9 g/m 2 , Huangshan Paper Company
50 - 60克重卷筒纸。 50 - 60 g heavy web.
实施例 11 '  Example 11 '
涂布色素隔离剂的冷转移印花纸在四版印刷中的应用  Application of Cold Transfer Printing Paper Coated with Pigment Release Agent in Four-page Printing
涂布 PE- 2浆时采用以下配方: 粘度: 560cps, 25'C条件下 4 号涂饰杯流秒 90s, 采用刮刀单涂或逆辊式涂布。 涂布量 7-12 g The following formula is applied when applying PE-2 slurry: Viscosity: 560 cps, No. 4 coating cup flow seconds 90s under 25'C condition, single or reverse roll coating with a doctor blade. Coating amount 7-12 g
/m2, 福建南平星光牌新闻卷筒纸 29 - 56克。 /m 2 , Fujian Nanping Xingguang brand news roll paper 29-56 grams.
实施例 13  Example 13
涂布色素隔离剂的冷转移印花紙在圆网印花中的应用  Application of cold transfer printing paper coated with pigment release agent in rotary screen printing
为了生产户外用品的转移花纸, 采用 Penta Screenl25目圆网, 开孔率为 15%, 适用于精细花型的印花。 印刷线压力为 1.5kg/cm。 在涂布 PE- 2浆时, 采用下述配方: 粘度 950cps, 25°C条件下 4号 涂饰杯 1分 20秒, 采用圆网 105目空网上涂层。 涂布量 12-15 g /m2, 使用山东青州纸厂单胶 90克卷筒纸。 In order to produce transfer paper for outdoor products, the Penta Screenl 25 mesh round mesh has an opening ratio of 15%, which is suitable for fine pattern printing. The printing line pressure was 1.5 kg/cm. In the application of PE-2 slurry, the following formulation was used: viscosity 950 cps, No. 4 coating cup at 25 ° C for 1 minute and 20 seconds, using a round mesh 105 mesh online coating. Coating amount 12-15 g / m 2 , using Shandong Qingzhou paper mill single glue 90 g web.
实施例 14 冷转移印花纸色素隔离剂在全棉纱卡织物的冷转移印花中的应 用 Example 14 Application of cold transfer printing paper pigment release agent in cold transfer printing of cotton gauze fabric
织物规格: 12x 10的全棉纱卡, 白度 74 ~ 79, 毛效 >9,  Fabric specifications: 12x 10 cotton gauze, whiteness 74 ~ 79, gross effect >9,
PE - 2浆指标:粘度 HOOcp, 25°C条件下 4号涂饰杯流速 280s。 织物在波美度 36.5的 NaOH碱剂中浸轧润湿, 通过三辊轧车, 一浸二轧, 軋余率为〜 60%, 轧液车速为 2.5/min, 利用实施例 3 制备的色素隔离剂 (即 PE- 2浆), 织物上的转移率约为 95 %。  PE - 2 slurry index: Viscosity HOOcp, flow rate of No. 4 coating cup at 280s at 25 °C. The fabric was padded and wetted in a NaOH alkaline agent of Baume 36.5, passed through a three-roll mill, one immersion and two rolling, the rolling ratio was ~60%, and the rolling speed was 2.5/min. The pigment prepared in Example 3 was used. The release agent (ie PE-2 slurry) has a transfer rate of approximately 95% on the fabric.
实施例 15  Example 15
冷转移印花纸色素隔离剂在全棉灯芯绒织物的冷转移印花中的 应用  Application of cold transfer printing paper pigment release agent in cold transfer printing of cotton corduroy fabric
织物规格: 16 X 21的 16条全棉灯芯绒,白度 73,黄度指数 6.58, 毛效〉 9.8,  Fabric specifications: 16 X 21 of 16 cotton corduroy, whiteness 73, yellowness index 6.58, gross effect > 9.8,
PE-2浆指标:粘度 880cp, 25°C条件下 4号涂饰杯流速 119s, 织物在波美度 36的 NaOH与 Na2Si03混和溶液中浸轧润湿,通过 三辊轧车, 一浸二轧, 礼余率为~65%, 利用实施例 4制备的 PE-PE-2 slurry index: viscosity 880cp, the flow rate of No. 4 coating cup is 119s at 25°C, the fabric is wetted by padding in a mixed solution of Baume 36 NaOH and Na 2 Si0 3 , through a three-roll mill, a dip Two rolling, the remnant rate is ~65%, using the PE prepared in Example 4
2浆色素隔离剂, 织物上的转移率约为 92%。 2 pulp pigment release agent, the transfer rate on the fabric is about 92%.
实施例 16  Example 16
冷转移印花纸色素隔离剂在纯纺天丝织物的冷转移印花中的应 用  Application of Cold Transfer Printing Paper Pigment Release Agent in Cold Transfer Printing of Pure Spinning Tencel Fabric
织物规格: 21x 21的纯纺天丝 (Tencel)—再生纤维素纤维, 白度 76, 毛效 ~10,  Fabric specifications: 21x 21 pure spinning Tencel - regenerated cellulose fiber, whiteness 76, hair effect ~10,
PE-2浆指标:粘度 630cp, 25'C条件下 4号涂饰杯流速 167s, 织物在波美度 37的 ^3?04与 Na2C03混和溶液中浸轧润湿, 通过 三辊軋车, 一浸二轧, 礼余率为~55%, 利用实施例 5制备的 PE- 2浆色素隔离剂, 织物上的转移率约为 95%。 PE-2 plasma indicators:? Viscosity 630cp, under conditions of 25'C flow cup No. 4 finish 167s, fabric Baume 37 ^ 304 with Na 2 C0 3 solution was padded wetted mixture, through a three roll The car, one dip and two rolling, had a ranch rate of ~55%. Using the PE-2 pulp pigment release agent prepared in Example 5, the transfer rate on the fabric was about 95%.
通过以上三个冷转移印¾纸色素隔离剂在纯纺织物的冷转移印 花中的应用实例,可以看出 PE色素隔离剂的使用,使得染料从转印 纸转移到织物上的转移率 4艮高, 到达 90%以上, 而且印花纸上的 PE 色素隔离剂涂层具有恰当地疏水性, 保证承印物完整印刷, 使印刷 图案的完整与清晰; 不产生粘连、返潮等问题; 具有较好的 pH适应 范围; 染料图案附着好, 不发生掉色现象。 尽量减少了残余染料对 环境的污染, 促进了印染行业向环保经济的方向进一步发展。 实施 例中所提到的烷基类乳化剂系高级脂肪醇硫酸酯类物;这类乳化剂 的乳化性 ί艮强,但较皂类乳化剂稳定,由于属阴离子性同时具润湿与 增溶功能。 Through the application examples of the above three cold transfer printing 3⁄4 paper pigment spacers in cold transfer printing of pure textiles, it can be seen that the use of PE pigment release agent makes the dye transfer from The transfer rate of paper transferred to the fabric is 4艮 high, reaching more than 90%, and the PE pigment release agent coating on the printing paper is properly hydrophobic, ensuring complete printing of the substrate, making the printing pattern complete and clear; Adhesion, moisture retreat and other issues; have a good pH adaptation range; dye pattern adhesion, no color loss phenomenon. Minimize the pollution of residual dyes to the environment and promote the further development of the printing and dyeing industry towards the environmental protection economy. The alkyl emulsifiers mentioned in the examples are higher fatty alcohol sulfates; such emulsifiers are more emulsifiable, but are more stable than soap emulsifiers, and are anionic and moisturizing and increasing. Dissolving function.
该 [丙烯酸(酯) -苯乙烯 ]与淀粉接枝构成的糊料解决了以 前转印纸所涂隔离层疏水层与亲水层之间的张力谐致与平衡难 题。 为冷转移印花糊提供了转移时的屏蔽隔离与印刷时的亲水适 印性。 本发明的研究发明切实解决了冷转移印花在各种纤维上的 应用及各种印刷设备上的使用。  The paste composed of [acrylic acid]-styrene grafted with starch solves the problem of tension and balance between the hydrophobic layer and the hydrophilic layer of the barrier layer coated with the front transfer paper. The cold transfer printing paste provides barrier separation during transfer and hydrophilic printability during printing. The research invention of the present invention effectively solves the application of cold transfer printing on various fibers and the use on various printing apparatuses.

Claims

权 利 要 求 Rights request
1.聚〖丙烯酸(酯) -苯乙烯]与淀粉构成的接枝共聚物, 所述的聚 [丙 烯酸(酯) -苯乙烯]为(甲基)丙烯酸、 (甲基)丙烯酸酯、 苯乙烯的三 元共聚物,所述的接枝共聚物的重均分子量在 2500 ~ 30000道尔顿之间, 接枝率平均在 25 % - 40 %之间, 该接枝共聚物的结构式表示为: 1. A graft copolymer composed of polyacrylic acid (styrene)-styrene, which is (meth)acrylic acid, (meth)acrylic acid ester, styrene The terpolymer has a weight average molecular weight of from 2,500 to 30,000 Daltons and an average grafting ratio of from 25% to 40%. The structural formula of the graft copolymer is expressed as:
Figure imgf000024_0001
Figure imgf000024_0001
其中, AGU表示构成淀粉的结构单元, n表示该结构单元的重复数, Poly [Acryl ic acid (Acrylate) -Styrene]表示聚 [丙烯酸(酯) -苯乙 烯 ], 所述的聚 [丙烯酸(酯) -苯乙烯]接枝在淀粉分子的 C3位位置、 C2位位置和 C6位位置, 并且接枝在淀粉分子的 C3位位置的物质占主要 Wherein, AGU represents a structural unit constituting starch, n represents a repeating number of the structural unit, and Poly [Acryl ic acid (Acrylate)-Styrene] represents poly[acrylic acid]-styrene, and the poly[acrylic acid (ester) - Styrene] grafted at the C3 position, C2 position and C6 position of the starch molecule, and the substance grafted at the C3 position of the starch molecule is dominant
2.权利要求 1所述的接枝共聚物, 是丙烯酸、 丙烯酸酯、 苯乙烯的三元 共聚物与淀粉形成的接枝共聚物。 The graft copolymer according to claim 1, which is a graft copolymer of a terpolymer of acrylic acid, acrylate or styrene and starch.
3. 权利要求 1所述的接枝共聚物, 其中的(甲基)丙烯酸酯是(甲基) 丙烯酸的 CI- C10烷基酯。 The graft copolymer according to claim 1, wherein the (meth) acrylate is a CI-C10 alkyl ester of (meth)acrylic acid.
4. 权利要求 1所述的接枝共聚物, 其中的(甲基)丙烯酸酯是丙烯酸丙 酯和 /或丙烯酸丁酯。 The graft copolymer according to claim 1, wherein the (meth) acrylate is propyl acrylate and/or butyl acrylate.
5.杈利要求 1 - 4中任一项所述的接枝共聚物的制备方法,包括下述两个 步骤: (1 )控制单体浓度、 引发剂浓度、 乳化剂浓度、 聚合温度, 以生 成聚 [丙烯酸(酯 ) -苯乙烯 ]; ( 2 )通过引发剂氧化淀粉, 在使淀粉产 生自由基的条件下, 使聚 [丙烯酸(酯) -苯乙烯 ]与淀粉发生接枝共 应, 生成聚 [丙烯酸(酯) -苯乙烯] -淀粉接枝共聚物, 接枝率 在 25% -40%之间。 5. The method for preparing a graft copolymer according to any one of claims 1 to 4, comprising the following two steps: (1) controlling a monomer concentration, an initiator concentration, an emulsifier concentration, and a polymerization temperature, Producing poly[acrylic acid (styrene)-styrene]; (2) oxidizing the starch by an initiator, and grafting the poly[acrylic acid (styrene)-styrene] with the starch under the condition that the starch generates a radical, Formation of poly[acrylic acid]-styrene graft copolymer, graft ratio Between 25% and 40%.
6.权利要求 5所述的制备方法, 其特征在于, 在步骤(1)中, 将作为单 体的由(甲基)丙烯酸、 (甲基)丙烯酸酯和苯乙烯构成或(甲基)丙烯 酸酯和苯乙烯构成的单体混合物加入由乳化剂聚氧乙烯山梨醇酐单油酸 酯成的乳液体系中, 对于上述的三元体系, 在 50°C的温度下, 对于上述 的二元体系, 在 60°C的温度下, 引发聚合, 生成聚 [丙晞酸(酯) -苯 乙烯], 随着共^^应的进行, 体系温度自动升高。 The method according to claim 5, wherein in the step (1), (meth)acrylic acid, (meth) acrylate, and styrene or (meth)acrylic acid are used as a monomer. a monomer mixture of an ester and styrene is added to an emulsion system formed by an emulsifier polyoxyethylene sorbitan monooleate. For the above ternary system, at a temperature of 50 ° C, for the above binary system At a temperature of 60 ° C, polymerization is initiated to form poly [propionate-styrene], and the temperature of the system is automatically increased as the total amount proceeds.
7.权利要求 5的制备方法, 其特征在于, 在步骤(2)中, The preparation method according to claim 5, wherein in the step (2),
当体系温度达到 85°C时, 加入醚化度 0.7-1.2的改性淀粉, 控制温度 在 70~85°C ^下, 继续反应 1~2小时, 当体系达到粘度要求时, 停 止反应, 得到聚 [丙烯酸(酯) -苯乙烯] -淀粉接枝共聚物。 When the temperature of the system reaches 85 °C, the modified starch with a degree of etherification of 0.7-1.2 is added, the temperature is controlled at 70-85 ° C ^, and the reaction is continued for 1-2 hours. When the system reaches the viscosity requirement, the reaction is stopped. Poly[acrylic acid]-styrene]-starch graft copolymer.
8.权利要求 1 - 4中任一项所述的接枝共聚物的用途,用于制备冷转移印 花紙用的色素隔离剂。 Use of the graft copolymer according to any one of claims 1 to 4 for the preparation of a pigment release agent for cold transfer printing paper.
9.色素隔离剂,含有权利要求 1-4中任一项所述的接枝共聚物、 蓖麻油 硫酸酯、 磷酸酯以及作为填料的二氧化硅或坡缕石。 A pigment release agent comprising the graft copolymer according to any one of claims 1 to 4, castor oil sulfate, phosphate, and silica or palygorite as a filler.
10.权利要求 9所述的色素隔离剂, 其中, 以重量百分比计, 含有所述的 接枝共聚物 35 % - 85 %、 蓖麻油硫酸酯 0.2-1.8 %、 磷酸酯 0.1-0.8 %、 二氧化硅 0.05 % - 0.5质量%或坡缕石 3― 9质量%, 余量为水。 The dye release agent according to claim 9, wherein the graft copolymer contains 35 % -85 % by weight, 0.2-1.8 % of castor oil sulfate, 0.1 - 0.8 % of phosphate, and 2 parts by weight. The silica is 0.05% - 0.5% by mass or the palygorskite is 3.9 % by mass, and the balance is water.
11.权利要求 9或 10的色素隔离剂, 其用于包括全棉、 毛、 丝的天然纤 维织物,纤维素纤维织物,以及包括涤纶、 锦纶和晴纶的合成纤维织物用 的冷转移印花纸及冷转移印花工艺上。 The pigment release agent according to claim 9 or 10, which is used for a natural fiber fabric comprising cotton, wool, silk, a cellulose fiber fabric, and a cold transfer printing paper for a synthetic fiber fabric comprising polyester, nylon and acrylic. Cold transfer printing process.
12.权利要求 9或 10的色素隔离剂, 其用于柔性版印刷机、 版印刷机、 网屏印花机、 喷墨打印机, 印刷织物专用的转移印花纸。 12. The pigment release agent of claim 9 or 10 for use in a flexographic printing press, a printing press, Screen printing machine, inkjet printer, transfer printing paper for printing fabrics.
13.制品, 具有由权利要求 9或 10所迷的色素隔离剂形成的涂层。 13. An article having a coating formed from the pigment release agent of claim 9 or 10.
14.权利要求 13 的制品, 是冷转移印花纸, 其在纸基表面具有所述的 涂层。 14. The article of claim 13 which is a cold transfer printing paper having said coating on the surface of the paper base.
PCT/CN2006/003486 2006-05-16 2006-12-19 Graft copolymer, process of preparation and use thereof, colorant release agent and articles thereof WO2007134499A1 (en)

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