WO2016110724A1 - Glass frit composition and ceramic inkjet ink comprising the same - Google Patents

Glass frit composition and ceramic inkjet ink comprising the same Download PDF

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Publication number
WO2016110724A1
WO2016110724A1 PCT/IB2015/000007 IB2015000007W WO2016110724A1 WO 2016110724 A1 WO2016110724 A1 WO 2016110724A1 IB 2015000007 W IB2015000007 W IB 2015000007W WO 2016110724 A1 WO2016110724 A1 WO 2016110724A1
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WO
WIPO (PCT)
Prior art keywords
glass frit
mixture
frit composition
pigment
inkjet ink
Prior art date
Application number
PCT/IB2015/000007
Other languages
French (fr)
Inventor
Tri Ratna TULADHAR
Domenico DI LONARDO
Fabio Enzo FENZI
Original Assignee
Fenzi Spa
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fenzi Spa filed Critical Fenzi Spa
Priority to ES15705093T priority Critical patent/ES2896048T3/en
Priority to EP15705093.1A priority patent/EP3242915B1/en
Priority to PCT/IB2015/000007 priority patent/WO2016110724A1/en
Publication of WO2016110724A1 publication Critical patent/WO2016110724A1/en

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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D11/00Inks
    • C09D11/30Inkjet printing inks
    • C09D11/32Inkjet printing inks characterised by colouring agents
    • C09D11/322Pigment inks
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C17/00Surface treatment of glass, not in the form of fibres or filaments, by coating
    • C03C17/006Surface treatment of glass, not in the form of fibres or filaments, by coating with materials of composite character
    • C03C17/007Surface treatment of glass, not in the form of fibres or filaments, by coating with materials of composite character containing a dispersed phase, e.g. particles, fibres or flakes, in a continuous phase
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C3/00Glass compositions
    • C03C3/04Glass compositions containing silica
    • C03C3/062Glass compositions containing silica with less than 40% silica by weight
    • C03C3/064Glass compositions containing silica with less than 40% silica by weight containing boron
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C3/00Glass compositions
    • C03C3/04Glass compositions containing silica
    • C03C3/062Glass compositions containing silica with less than 40% silica by weight
    • C03C3/064Glass compositions containing silica with less than 40% silica by weight containing boron
    • C03C3/066Glass compositions containing silica with less than 40% silica by weight containing boron containing zinc
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C3/00Glass compositions
    • C03C3/04Glass compositions containing silica
    • C03C3/076Glass compositions containing silica with 40% to 90% silica, by weight
    • C03C3/097Glass compositions containing silica with 40% to 90% silica, by weight containing phosphorus, niobium or tantalum
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C8/00Enamels; Glazes; Fusion seal compositions being frit compositions having non-frit additions
    • C03C8/02Frit compositions, i.e. in a powdered or comminuted form
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C8/00Enamels; Glazes; Fusion seal compositions being frit compositions having non-frit additions
    • C03C8/02Frit compositions, i.e. in a powdered or comminuted form
    • C03C8/04Frit compositions, i.e. in a powdered or comminuted form containing zinc
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C8/00Enamels; Glazes; Fusion seal compositions being frit compositions having non-frit additions
    • C03C8/02Frit compositions, i.e. in a powdered or comminuted form
    • C03C8/08Frit compositions, i.e. in a powdered or comminuted form containing phosphorus
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C8/00Enamels; Glazes; Fusion seal compositions being frit compositions having non-frit additions
    • C03C8/14Glass frit mixtures having non-frit additions, e.g. opacifiers, colorants, mill-additions
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C8/00Enamels; Glazes; Fusion seal compositions being frit compositions having non-frit additions
    • C03C8/14Glass frit mixtures having non-frit additions, e.g. opacifiers, colorants, mill-additions
    • C03C8/16Glass frit mixtures having non-frit additions, e.g. opacifiers, colorants, mill-additions with vehicle or suspending agents, e.g. slip
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D11/00Inks
    • C09D11/02Printing inks
    • C09D11/10Printing inks based on artificial resins
    • C09D11/106Printing inks based on artificial resins containing macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • 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
    • B41M5/0041Digital printing on surfaces other than ordinary paper
    • B41M5/0047Digital printing on surfaces other than ordinary paper by ink-jet printing
    • 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
    • B41M5/0041Digital printing on surfaces other than ordinary paper
    • B41M5/007Digital printing on surfaces other than ordinary paper on glass, ceramic, tiles, concrete, stones, etc.
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C2217/00Coatings on glass
    • C03C2217/20Materials for coating a single layer on glass
    • C03C2217/29Mixtures
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C2217/00Coatings on glass
    • C03C2217/40Coatings comprising at least one inhomogeneous layer
    • C03C2217/43Coatings comprising at least one inhomogeneous layer consisting of a dispersed phase in a continuous phase
    • C03C2217/44Coatings comprising at least one inhomogeneous layer consisting of a dispersed phase in a continuous phase characterized by the composition of the continuous phase
    • C03C2217/45Inorganic continuous phases
    • C03C2217/452Glass
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C2217/00Coatings on glass
    • C03C2217/40Coatings comprising at least one inhomogeneous layer
    • C03C2217/43Coatings comprising at least one inhomogeneous layer consisting of a dispersed phase in a continuous phase
    • C03C2217/46Coatings comprising at least one inhomogeneous layer consisting of a dispersed phase in a continuous phase characterized by the dispersed phase
    • C03C2217/48Coatings comprising at least one inhomogeneous layer consisting of a dispersed phase in a continuous phase characterized by the dispersed phase having a specific function
    • C03C2217/485Pigments
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C2217/00Coatings on glass
    • C03C2217/70Properties of coatings
    • C03C2217/72Decorative coatings
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C2218/00Methods for coating glass
    • C03C2218/10Deposition methods
    • C03C2218/11Deposition methods from solutions or suspensions
    • C03C2218/119Deposition methods from solutions or suspensions by printing

Definitions

  • the present invention concerns a glass frit composition and a process for producing the same. Furthermore, the present invention concerns a ceramic inkjet ink comprising said glass frit composition and a process for producing said ink. Additionally, the present invention concerns a method for printing on ceramic substrate such as glass, by using said ink.
  • inorganic ceramic paints containing glass frit and inorganic pigments are printed on ceramic surfaces by silk-screen, roller coating, spray coating and curtain coating.
  • Typical paint viscosities for such applications are within the range lOOs-lOOOs mPa.s (system dependent).
  • These ceramic paints have high solid contents > 50% and particle size in the range of 2-10 ⁇ .
  • the object of the present invention is to provide an ink which is able to meet said strict requirements.
  • the present invention concerns a method for printing on ceramic substrate such as glass, by using said ink.
  • the present invention relates to a glass frit composition and a ceramic inkjet ink which can be obtained by said processes.
  • FIG. 2 shows (a) a comparative mixture of additives, pigments and glass frit composition, and (b) a mixture of additives, pigments and glass frit composition according to the present invention
  • FIG. 3 shows (a) a comparative ink on a glass surface, and (b) the ceramic inkjet ink on a glass surface according to the present invention.
  • the subject of the invention therefore is a glass frit composition
  • a glass frit composition comprising:
  • said glass frit composition being in the form of particles having a volume particle size distribution Dv 90 of less than 2 ⁇ , as measured by laser diffraction.
  • wt. % weight percent of the total weight of the glass frit composition.
  • the glass frit composition has the form of particles.
  • the shape of the particles can be any shape.
  • the size of the particle is defined by their
  • volume particle size distribution is to be understood as defining the relative amount by volume, of particles present according to size.
  • the volume particle size distribution is designated as Dv 90 , defining the distribution of the size (or diameter) of 90 percent of the particles by volume.
  • This parameter is measured by laser diffraction, unless otherwise defined.
  • the laser diffraction methods depend upon analysis of the "halo" of diffracted light produced when a laser beam passes through a dispersion of particles in air or in a liquid.
  • the angle of diffraction increases as particle size decreases, so that this method is particularly good for measuring sizes between 0.1 and 3,000 ⁇ . Advances in sophisticated data processing and automation have allowed this to become the dominant method used in industrial particle-size distribution determination.
  • This technique is relatively fast and can be performed on very small samples.
  • a particular advantage is that the technique can generate a continuous measurement for analyzing process streams.
  • Laser diffraction measures particle size distributions by measuring the angular variation in intensity of light scattered as a laser beam passes through a dispersed particulate sample. Large particles scatter light at small angles relative to the laser beam and small particles scatter light at large angles.
  • the angular scattering intensity data is then analyzed to calculate the size of the particles responsible for creating the scattering pattern, using the Mie theory of light scattering. The particle size is reported as a volume equivalent sphere diameter.
  • the glass frit composition of the invention is in the form of particles having a volume particle size distribution Dv9 0 of less than 1 ⁇ , as measured by laser diffraction. This allows to further reduce the risk of sedimentation over time, when the glass frit particles are used in ink compositions, thus improving their stability.
  • said particles have a volume particle size distribution Dv9o of 0.1-1 ⁇ .
  • Dv9o volume particle size distribution
  • the glass frit composition of the invention further comprises up to 7 wt. % of ZrO, CaO, BaO, MgO, P 2 0 5 , Fe 2 0 3 , SrO, or a mixture thereof.
  • the glass frit composition of the invention is such as to be lead-free.
  • the glass frit composition of the invention is designed to achieve great performances although the absence of lead, as both bismuth oxide and zinc oxide at the given amounts showed to be valid substitute of lead oxide.
  • zinc oxide is cheaper than bismuth oxide, so that from the economical point of view the former is preferable.
  • a higher bismuth oxide content is preferred when a higher chemical resistance is required by the final applications.
  • the glass frit composition of the invention comprises:
  • the glass frit composition of the invention comprises:
  • the glass frit composition of the invention also comprises up to 2 wt. % of ZrO, more preferably up to 1.6 wt. % of ZrO.
  • first embodiments can be lithium-free.
  • Lithium oxide assists the melting of the frit and has a significant influence on the expansion coefficient and contraction rates. For these reasons the presence of lithium oxide can not be suitable for some specific applications. In these cases, said first embodiments can be successfully used, because these compositions allow to better control linear expansion of the frit.
  • the glass frit composition of the invention comprises:
  • the glass frit composition of the invention comprises:
  • the glass frit composition of the invention also comprises up to 5 wt. % of a mixture of CaO, BaO, MgO, and P 2 0 5 .
  • the glass frit composition of the invention comprises:
  • the glass frit composition of the invention comprises:
  • the glass frit composition of the invention also comprises up to 5 wt. % of a mixture of Fe 2 0 3 , and SrO.
  • the glass frit composition of the invention comprises: - 30-40 wt. % Si0 2 ,
  • the glass frit composition of the invention comprises:
  • the glass frit composition consists of:
  • said glass frit composition being in the form of particles having a volume particle size distribution Dv9o of less than 2 ⁇ , as measured by laser diffraction.
  • the present invention concerns a process for producing the glass frit composition as above described, said process comprising the steps of: 1) mixing the oxides of the glass frit composition;
  • 'milling' is to be understood as a process of grinding materials. Dry-milling is a milling process occurring without solvent. Wet-milling occurs with a solvent.
  • step 4) results in a highly stable glass frit composition with no or negligible sedimentation and having the desired volume particle size distribution Dv 9 o of less than 2 ⁇ .
  • step 4) is carried out in a fluidized jet mill.
  • jet milling is to be understood as a process of using highly compressed air or other gasses, usually in a vortex motion, to impact fine particles against each other in a chamber.
  • step 5 is carried out in the presence of a dispersant agent and a solvent.
  • the dispersant agent and solvent allow to prevent the fine frit particles from re- aggregating.
  • Step 5) is preferably carried out by mixing in a high shear mixer and then wet-milling in a high speed mill with special grinding chamber components such as zirconia, silicon nitrite and/or silicon carbide.
  • the wet-milling can be carried out in batch in multipass operation until the desired particle size is obtained.
  • said high speed mill is a horizontal bead mill, with a Zirconia grinding chamber.
  • the wet-milling can be carried out in batch in multipass operation until the desired particle size is obtained.
  • the glass frit composition of step 5) comprises 50-70 wt.% of dry-milled frit, up to 10 wt.% of a dispersant agent, and 20-45 wt.% of a solvent.
  • the glass frit composition of step 5) comprises 60- 70 wt.% of dry-milled frit, 1-3 wt. of a dispersant agent, and 29-37 wt.% of a solvent.
  • the dispersant agent is a copolymer with acidic group (Disperbyk 110TM, Disperbyk 111TM), alkylol ammonium salt of copolymer with acidic groups (Disperbyk- 180TM), solution of high molecular weight block copolymers with pigment affinic groups (Disperbyk 182TM, Disperbyk 184TM, Disperbyk 190TM), copolymer with pigment affinic groups (Disperbyk 191TM, Disperbyk 192TM, Disperbyk 194TM, Tego Dispers 7502TM, Tego Dispers 752WTM), block-copolymer with pigment affinic groups (Disperbyk 2155TM), solution of alkylol ammonium salt of a higher
  • the solvent can be one or more alcohols, such as methyl alcohol, ethyl alcohol, propyl alcohols, butyl alcohols; glycols, such as methyl glycol (MG), ethyl glycol, propyl glycol, butyl glycol (BG); glycol ethers, such as methoxy propanol (PM), ethoxy propanol (EP), diacetone propanol (DAA), methoxy butanol, dipropylene glycol monomethyl ether (DPM), tripropylene glycol methyl ether (TPM), propylene glycol mono methyl ether (PM), di or tri propylene glycol mono propyl ether (DPnP, TPnP), butyl diglycol (BDG); esters, such as methyl acetate, ethyl acetate (ETAC), propyl acetate(IPAC), butyl acetate (BUAC), methoxy propyl acetate (PMA), ethyl
  • the solvent is an alcohol, selected from methyl alcohol, ethyl alcohol, propyl alcohol, and butyl alcohol, a glycol selected from methyl glycol, ethyl glycol, propyl glycol, and butyl glycol, a glycol ether selected from methoxy propanol, ethoxy propanol, diacetone propanol, methoxy butanol, dipropylene glycol monomethyl ether, tripropylene glycol methyl ether, propylene glycol mono methyl ether, di- or tri-propylene glycol mono propyl ether, and butyl diglycol, an ester selected from methyl acetate, ethyl acetate, propyl acetate, butyl acetate, methoxy propyl acetate, and ethyl-3-ethoxy-propanol, a ketone selected from acetone, methyl ethyl ketone, methyl butyl ketone,
  • the solvent is a glycol selected from methyl glycol, ethyl glycol, propyl glycol, and butyl glycol, a glycol ether selected from methoxy propanol, ethoxy propanol, diacetone propanol, methoxy butanol, dipropylene glycol monomethyl ether, tripropylene glycol methyl ether, propylene glycol mono methyl ether, di- or tri-propylene glycol mono propyl ether, and butyl diglycol, or a mixture thereof.
  • a glycol selected from methyl glycol, ethyl glycol, propyl glycol, and butyl glycol
  • a glycol ether selected from methoxy propanol, ethoxy propanol, diacetone propanol, methoxy butanol, dipropylene glycol monomethyl ether, tripropylene glycol methyl ether, propylene glycol mono methyl ether, di- or tri-
  • the solvent is butyl diglycol.
  • the glass frit composition of step 5) comprises 60-70 wt.% of dry-milled frit, 1-3 wt.% of an alkylol ammonium salt of copolymer with acidic groups, polyvinylpyrrolidone, or a mixture thereof, and 29-37 wt.% of butyl diglycol.
  • Step 5 is preferably carried out by mixing in a high shear mixer and then wet-milling in a high speed mill (e.g. NETZSCH model LMZ10 horizontal sand mill, with a Zirconia grinding chamber), for up to 24 hours until the desired particle size is obtained.
  • a high speed mill e.g. NETZSCH model LMZ10 horizontal sand mill, with a Zirconia grinding chamber
  • the present invention concerns a ceramic inkjet ink comprising:
  • wt. % weight percent of the total weight of the ceramic inkjet ink.
  • the ceramic inkjet ink composition according to the present invention shows advantageous properties, so that, at jetting, the following undesired effects are conveniently prevented: drop splattering, bleed and spread after landing on hard ceramic surfaces, such as glass. Additionally, the edge definition of the printed image during drying and tempering is retained.
  • the ceramic inkjet ink composition according to the present invention has a high chemical resistance, e.g. resistance to acid, base, UV, a high mechanical resistance, e.g. scratch, abrasion, durability.
  • the pigment can be any inorganic colour pigment.
  • the inorganic pigments powder is produced by high temperature calcination.
  • the pigments can be oxides of metals such as cobalt, iron, nickel, copper, titanium dioxide for different colours.
  • Suitable inorganic pigments are Cobalt chromite Blue green Spinel (Shepherd Blue 211, Shepherd Blue 30C527), Cobalt Aluminate Blue Spinel (Rockwood Cobalt Blue 28, Rockwood Cobalt blue 419, Shepherd Blue 214, Shepherd Blue 299, Shepherd Blue 385, Shepherd Blue 424), Iron oxide (SiOF 1020, SiOF 3029M, SiOF 2019M, SiOF 3021M, Bayferrox 120, Bayferrox 180, Rockwood Ferroxide 206M), Manganese Ferrite (Rockwood FM2400), Nickel Antimony Titanium Yellow Rutile (Shepherd Yellow 25, Shepherd Yellow 195), Copper Chromite Black Spinel (Shepherd Black 1 GM, Shepherd Black 430), manganese ferrite (Rockwood FM2400), White: Huntsman Ti0 2 A-HR; DuPont Ti-Pure® R-101, DuPont Ti-Pure® R-102, Green: Cobalt Titanate Green Spinel (Shepherd
  • These pigments are heat resistant inorganic pigments, chemically inert and stable to ultraviolet light. They have high durability and hiding power.
  • the pigment type, size and its particle interaction can be adjusted during formulation to meet the final tempered colour of the ink as well as fulfil the requirement of hiding power (optical property used to describe the light-scattering efficiency of a white pigment) and opacity (degree to which light is not allowed to pass through).
  • the pigment has a volume particle size distribution Dv 9 o of less than 1 ⁇ .
  • Commercially available inorganic pigments have indeed a particle size greater than 2-3 microns, therefore said particle size is reduced to make the pigments suitable for inkjet printing.
  • the pigment is milled and grinded in the presence of a dispersant agent and a solvent, thus resulting in a pigment paste having a pigment volume particle size distribution Dv9 0 of less than 2 ⁇ , preferably less than 1 ⁇ .
  • a bead/ball mill mixer is used with 1.75 mm zirconia grinding beads.
  • the combination of the dispersant agent and grinding step is crucial to obtain highly stable pigment paste with negligible/no sedimentation over long time.
  • the ceramic inkjet ink can also comprise additives, such as carriers, rheology agents, surfactants, anti-settling/static agents, flow and levelling agents, de-foaming/de- aeration agents, and resins.
  • additives such as carriers, rheology agents, surfactants, anti-settling/static agents, flow and levelling agents, de-foaming/de- aeration agents, and resins.
  • Appropriate additives can improve the surface grip after drying at temperature equal to or above 150°C, for manual handling.
  • Said additives can be in an amount up to 10 wt. % in order to improve jetting and substrate-adhesion performances.
  • wt. % it is meant weight percent of the total weight of the ceramic inkjet ink.
  • Suitable carriers can be mixtures of alkane waxes with a low melting point of 40-100°C, being-solid at room temperature. Examples of such carriers are low melting paraffin wax.
  • the carriers can be a mixture of linear Cio-C 24 alkanes, preferably linear Cio- C 22 alkanes, more preferably linear Ci 2 -Ci 8 alkanes.
  • Suitable surfactants can be a solution of polyether-modified polydimethylsiloxane (commercially available as BYK-301, BYK-302, BYK 306, BYK 337, BYK 341), polyether modified polydimethylsiloxane (commercially available as BYK-307, BYK 333), solution of a polyester-modified polydimethylsiloxane (commercially available as BYK-310, BYK-313) solution of polyester-modified polymethylalkylsiloxane (commercially available as BYK-315) polyether modified dimethylpolysiloxane (commercially available as BYK378), or a mixture thereof.
  • polyether-modified polydimethylsiloxane commercially available as BYK-301, BYK-302, BYK 306, BYK 337, BYK 341
  • polyether modified polydimethylsiloxane commercially available as BYK-307, BYK 333
  • Suitable flow and leveling agents can be polymeric, non silicone (commercially available as Dynoadd F-l, Dynoadd F-100, Dynoadd F-101, Dynoadd F-102), solution of polyester modified acrylic polymer (commercially available as Dynoadd F201), special dimethyl polysiloxanes (commercially available as Tego Flow ATF 2), polyether siloxane copolymer (commercially available as Tego Glide 100, Tego Wet 240), or a mixture thereof.
  • Suitable deaerating/defoaming agents can be Silicone free (commercially available as BYK 051, BYK 052, BYK 053, BYK 054, BYK 055, BYK 057, BYK 1752, BYK-A 535), emulsion of hydrophobic solids, emulsifiers and foam destroying polysiloxanes (commercially available as BYK-610), Fluoro-modified silicone defoamer (commercially available as Dynoadd F-470), non-silicone anionic (commercially available as Dynoadd F- 603), organo-modified polysiloxane (commercially available as Tego Airex 900, Deaerating organic polymers with tip of silicone (commercially available as Tego Airex 990, Tego Airex 991), silicone free deaerator (commercially available as Tego Airex 920), solution of polyacrylate (commercially available as Tego Flow ZFS 460), or a mixture thereof.
  • Suitable rheology and anti-settling agents can be solution of modified urea (commercially available as BYK 410, BYK 420), solution of urea modified polyurethane (commercially available as BYK-425), solution of polyurethane with a highly branched structure (commercially available as BYK-428), solution of high molecular urea modified polar polyamide (commercially available as BYK-430, BYK-431), hybridised amide (commercially available as Disparlon AQH 800), non-ionic polyurethane based thickener (commercially available as Tego ViscoPlus 3000, Tego ViscoPlus 3030, Tego Viscoplus 3060), fumed silica (Aerosil), or a mixture thereof;
  • Suitable resins can be hydroxypropyl cellulose, hydroxyethyl cellulose, hydroxymethyl cellulose, nitrocellulose, methacrylic copolymer, or a mixture thereof.
  • the present invention concerns a process for producing the ceramic inkjet ink as above described, said process comprising the steps of:
  • step 5 preparing a glass frit composition according to the process above described, wherein in step 5) the wet-milling is carried out in the presence of a dispersant agent and a solvent;
  • step c) mixing the pigment paste of step a) and the glass frit composition of step b) in a bead mixer;
  • step d) filtering the mixture of step d) through a micrometer pore size filter, thereby obtaining a ceramic inkjet ink having a viscosity of 6-20 mPa.s at jetting temperature and jetting conditions.
  • the pigment paste of step a) is prepared as above described.
  • the pigment paste of step a) comprises 45-85 wt. % pigment, 2-20 wt. % dispersant agent and 10-55 wt. % solvent.
  • the micrometer pore size filter is a 20-micrometer pore size filter.
  • wt. % it is meant weight percent of the total weight of the pigment paste.
  • the pigment paste of step a) comprises 50-80 wt. % pigment, 3- 10 wt. % dispersant agent and 15-45 wt. % solvent.
  • Exemplary pigment pastes are the following:
  • Dispersant agent Disperbyk 180TM: 4%
  • Dispersant agent Disperbyk 194NTM: 8%
  • Dispersant agent Disperbyk 194NTM: 8%
  • Dispersant agent Lubrizol J955TM: 8%
  • Dispersant agent Lamberti Flujet 12/36TM: 10%
  • Dispersant agent Disperbyk 194NTM: 5%
  • the present invention concerns a ceramic inkjet ink obtainable by the process as above described, said inkjet ink having a viscosity of 6-20 mPa.s at jetting temperature and jetting conditions, a surface tension of 20-40 mN/m at 5-60°C, and a volume particle size distribution Dvgo of less than 2 ⁇ , as measured by laser diffraction.
  • the present invention concerns a method for printing a ceramic substrate, comprising the step of inkjet printing a ceramic substrate with an inkjet ink as above described.
  • said ceramic substrate is a glass substrate.
  • said method comprises:
  • a glass frit having the following composition has been prepared:
  • a glass frit having the following composition has been prepared:
  • a glass frit having the following composition has been prepared:
  • Glass frit pastes have been prepared by using the glass frits of Examples 1-4.
  • Each glass frit of Examples 1-4 has been suitably jet milled before been mixed with the dispersant agent and solvent, at the following amounts:
  • the three components are initially mixed in a high shear mixer and then wet-milled in horizontal high speed mill with Zirconia grinding chamber in multi-pass operations for fixed time. This resulted in a highly stable frit with no or minimal sedimentation with a volume particle size distribution Dv9o of less than 2 ⁇ .
  • the glass frit paste 1 prepared as per Example 5 has been used to produce the following inkjet inks:
  • the above inkjet inks have been prepared by wet-mixing mill frit and pigment paste in bead mill mixer for 20 min, and then filtering the resulting inks by using a 20-micrometer pore size filter.
  • Printing on the glass was performed in single pass and multipass (several layers) in order to achieve sufficient thickness to meet the final requirements such as optical density after high temperature heat treatment or tempering at temperature above 500°C.
  • the ink rheology is tailored to achieve controlled shear thinning behaviour to reduce particle sedimentation during storage and drop spread/bleeding on glass substrate.
  • Low shear viscosity (at shear rates ⁇ 50 1/s) is deliberately maintained at least several times greater than that of the high shear steady viscosity of 6-20 mPa.s (at shear rate > 1000 1/s) at the jetting temperature.
  • Static surface tension is 20-40 mN/m to meet the printhead and substrate requirements.

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Abstract

A glass frit composition and a process for producing the same are described. Furthermore, a ceramic inkjet ink comprising said glass frit composition and a process for producing said ink are disclosed. Additionally, a method for printing on ceramic substrate such as glass, by using said ink is provided.

Description

"GLASS FRIT COMPOSITION AND CERAMIC INKJET INK COMPRISING THE SAME"
FIELD OF THE INVENTION
The present invention concerns a glass frit composition and a process for producing the same. Furthermore, the present invention concerns a ceramic inkjet ink comprising said glass frit composition and a process for producing said ink. Additionally, the present invention concerns a method for printing on ceramic substrate such as glass, by using said ink.
STATE OF THE ART
Traditionally, inorganic ceramic paints containing glass frit and inorganic pigments are printed on ceramic surfaces by silk-screen, roller coating, spray coating and curtain coating. Typical paint viscosities for such applications are within the range lOOs-lOOOs mPa.s (system dependent). These ceramic paints have high solid contents > 50% and particle size in the range of 2-10 μπι.
To date, digital printing ceramic paints are being explored with limited success. Standard commercial inkjet systems have much strict requirements in terms of both physical and chemical properties to meet printhead and jetting criteria.
The object of the present invention is to provide an ink which is able to meet said strict requirements.
SUMMARY OF THE INVENTION
The above object has been achieved by a glass frit composition as described in claim 1, and a ceramic inkjet ink comprising said glass frit composition.
In a further aspect, a process for producing said glass frit composition is provided.
In another aspect, a process for producing said ceramic inkjet ink is provided.
In an additional aspect, the present invention concerns a method for printing on ceramic substrate such as glass, by using said ink.
In an even further aspect, the present invention relates to a glass frit composition and a ceramic inkjet ink which can be obtained by said processes.
The characteristics and the advantages of the present invention will become apparent from the following detailed description and from the working examples provided for illustrative purposes and from the accompanying Figures, wherein: - Figure 1 shows (a) a mixture of pigments and glass frit composition obtained according a comparative process, and (b) a mixture of pigments and glass frit composition obtained according to the process of the present invention;
- Figure 2 shows (a) a comparative mixture of additives, pigments and glass frit composition, and (b) a mixture of additives, pigments and glass frit composition according to the present invention; and
- Figure 3 shows (a) a comparative ink on a glass surface, and (b) the ceramic inkjet ink on a glass surface according to the present invention.
DETAILED DESCRIPTION OF THE INVENTION
The subject of the invention therefore is a glass frit composition comprising:
- 20-49 wt. % Si02,.
- 3-20 wt. % B203,
- 1-9 wt. % Na20,
- 0.1-5 wt. % K20,
- 1-7 wt. % Ti02,
- 0.01-5 wt. % A1203, and
- a mixture of:
i) 50-60 wt. % Bi203, and 7-35 wt. % ZnO, or
ii) 7-15 wt. % ZnO, and up to 5 wt. % Li20,
iii) 45-55 wt. % Bi203, and up to 5 wt. % Li20, or
iv) 40-45 wt. % Bi203, 0.5-3 wt. % ZnO, and up to 4 wt. % Li20,
said glass frit composition being in the form of particles having a volume particle size distribution Dv90 of less than 2 μηι, as measured by laser diffraction.
With "wt. %" it is meant weight percent of the total weight of the glass frit composition. In the context of the present invention, the glass frit composition has the form of particles.
The shape of the particles can be any shape. The size of the particle is defined by their
"volume particle size distribution".
For the purposes of the present invention, the term "volume particle size distribution" is to be understood as defining the relative amount by volume, of particles present according to size. The volume particle size distribution is designated as Dv90, defining the distribution of the size (or diameter) of 90 percent of the particles by volume. This parameter is measured by laser diffraction, unless otherwise defined. The laser diffraction methods depend upon analysis of the "halo" of diffracted light produced when a laser beam passes through a dispersion of particles in air or in a liquid. The angle of diffraction increases as particle size decreases, so that this method is particularly good for measuring sizes between 0.1 and 3,000 μπι. Advances in sophisticated data processing and automation have allowed this to become the dominant method used in industrial particle-size distribution determination. This technique is relatively fast and can be performed on very small samples. A particular advantage is that the technique can generate a continuous measurement for analyzing process streams. Laser diffraction measures particle size distributions by measuring the angular variation in intensity of light scattered as a laser beam passes through a dispersed particulate sample. Large particles scatter light at small angles relative to the laser beam and small particles scatter light at large angles. The angular scattering intensity data is then analyzed to calculate the size of the particles responsible for creating the scattering pattern, using the Mie theory of light scattering. The particle size is reported as a volume equivalent sphere diameter.
The upper boundary of 2 μπι makes the above glass frit particles particularly suitable for the digital inkjet printheads typically having nozzle openings of about 15-50 μπι, because problems of clogging are advantageously prevented. At the same time, the risk of sedimentation over time is conveniently reduced, thus giving a long-term storage stability. Preferably, the glass frit composition of the invention is in the form of particles having a volume particle size distribution Dv90 of less than 1 μπι, as measured by laser diffraction. This allows to further reduce the risk of sedimentation over time, when the glass frit particles are used in ink compositions, thus improving their stability.
More preferably, said particles have a volume particle size distribution Dv9o of 0.1-1 μηι. In fact, even if in terms of stability over time the particle size is desirable to be as small as possible, however, for values below 0.1 μπι, the final colour intensity of the inkjet ink, once printed on a ceramic surface, can be negatively affected. For example, when a black inorganic pigment is used, the resulting printed surface could fade to greyish.
Preferably, the glass frit composition of the invention further comprises up to 7 wt. % of ZrO, CaO, BaO, MgO, P205, Fe203, SrO, or a mixture thereof.
It should be appreciated that the glass frit composition of the invention is such as to be lead-free. In fact, the glass frit composition of the invention is designed to achieve great performances although the absence of lead, as both bismuth oxide and zinc oxide at the given amounts showed to be valid substitute of lead oxide. Particularly, zinc oxide is cheaper than bismuth oxide, so that from the economical point of view the former is preferable. However, a higher bismuth oxide content is preferred when a higher chemical resistance is required by the final applications.
In first embodiments, the glass frit composition of the invention comprises:
- 20-30 wt. % Si02,
- 3-10 wt. % B203,
- 1-5 wt. % Na20,
- 0.1-2 wt. K20,
- 1-5 wt. % Ti02,
- 0.01-5 wt. % A1203, and
- a mixture of i) 50-60 wt. % Bi203, and 7-35 wt. % ZnO.
Preferably, the glass frit composition of the invention comprises:
- 20-30 wt. % Si02,
- 3-10 wt. % B203,
- 1-5 wt. % Na20,
- 0.1-2 wt. K20,
- 1-5 wt. % Ti02,
- 0.01-4 wt. % A1203, and
- a mixture of i) 50-55 wt. % Bi203, and 8-11 wt. % ZnO.
Preferably, the glass frit composition of the invention also comprises up to 2 wt. % of ZrO, more preferably up to 1.6 wt. % of ZrO.
These first embodiments can be lithium-free. Lithium oxide assists the melting of the frit and has a significant influence on the expansion coefficient and contraction rates. For these reasons the presence of lithium oxide can not be suitable for some specific applications. In these cases, said first embodiments can be successfully used, because these compositions allow to better control linear expansion of the frit.
In second embodiments, the glass frit composition of the invention comprises:
. 40-49 wt. % Si02,
- 10-20 wt. % B203,
- 5-9 wt. % Na20,
- 2-5 wt. % K20, - 1-5 wt. % Ti02,
- 0.1-1 wt. % A1203, and
- a mixture of ii) 7-15 wt. % ZnO, and up to 5 wt. % Li20.
Preferably, the glass frit composition of the invention comprises:
- 40-49 wt. % S1O2,
- 10-20 wt. % B203,
- 5-9 wt. % Na20,
- 2-5 wt. % K20,
- 1-5 wt. % Ti02,
- 0.1-1 wt. % A1203, and
- a mixture of ii) 9-13 wt. % ZnO, and up to 5 wt. % Li20.
More preferably, the glass frit composition of the invention also comprises up to 5 wt. % of a mixture of CaO, BaO, MgO, and P205.
In third embodiments, the glass frit composition of the invention comprises:
- 30-40 wt. % Si02,
- 3-10 wt. % B203,
- 1-5 wt. % Na20,
- 0.1-2 wt. % K20,
- 2-7 wt. % Ti02,
- 0.01-0.5 wt. % A1203, and
- a mixture of iii) 45-55 wt. % Bi203, and up to 5 wt. % Li20.
Preferably, the glass frit composition of the invention comprises:
- 30-40 wt. % Si02,
- 3-10 wt. % B203,
- 1-5 wt. % Na20,
- 0.1-2 wt. % K20,
- 2-7 wt. % Ti02,
- 0.01-0.5 wt. % A1203, and
- a mixture of iii) 45-50 wt. % Bi203, and up to 4 wt. % Li20.
More preferably, the glass frit composition of the invention also comprises up to 5 wt. % of a mixture of Fe203, and SrO.
In fourth embodiments, the glass frit composition of the invention comprises: - 30-40 wt. % Si02,
- 3-10 wt. % B203,
- 1-5 wt. % Na20,
- 0.1-2 wt. % K20,
- 3-7 wt. % Ti02,
- 0.01-1 wt. % A1203, and
- a mixture of iv) 40-45 wt. % Bi203, 0.5-3 wt. % ZnO, and up to 4 wt. % Li20.
Preferably, the glass frit composition of the invention comprises:
- 30-40 wt. % Si02,
- 3-10 wt. % B203,
- 1-5 wt. % Na20,
- 0.1-2 wt. % K20,
- 3-7 wt. % Ti02,
- 0.01-1 wt. % A1203, and
- a mixture of iv) 41-44 wt. % Bi203, 1-3 wt. % ZnO, and up to 3 wt. % Li20.
In other preferred embodiments, the glass frit composition consists of:
- 20-49 wt. % Si02,
- 3-20 wt. % B203,
- 1-9 wt. % Na20,
- 0.1-5 wt. % K20,
- 1-7 wt. % Ti02,
- 0.01-1 wt. % A1203,
- up to 5 wt. % of CaO, BaO, MgO, P205, Fe203, SrO, or a mixture thereof, and
- a mixture of:
i) 50-60 wt. % Bi203, and 7-12 wt. % ZnO, or
ii) 7-15 wt. % ZnO, and up to 5 wt. % Li20, or
iii) 45-55 wt. % Bi203, and up to 5 wt. % Li20, or
iv) 40-45 wt. % Bi203, 0.5-3 wt. % ZnO, and up to 4 wt. % Li20,
said glass frit composition being in the form of particles having a volume particle size distribution Dv9o of less than 2 μπι, as measured by laser diffraction.
In a further aspect, the present invention concerns a process for producing the glass frit composition as above described, said process comprising the steps of: 1) mixing the oxides of the glass frit composition;
2) melting the mixed oxides to obtain a melted mixture;
3) cooling the obtained melted mixture;
4) dry-milling the so-cooled mixture to obtain a milled frit having a volume particle size distribution Dvgo of less than 8 μη , preferably of 5 to 8 μηι; and
5) wet-milling the dry-milled frit to achieve a volume particle size distribution Dv90 of less than 2 μηι.
For the purposes of the present invention, 'milling' is to be understood as a process of grinding materials. Dry-milling is a milling process occurring without solvent. Wet-milling occurs with a solvent.
The combination of step 4) and step 5) results in a highly stable glass frit composition with no or negligible sedimentation and having the desired volume particle size distribution Dv9o of less than 2 μηι.
Preferably, step 4) is carried out in a fluidized jet mill. For the purposes of the present invention, jet milling is to be understood as a process of using highly compressed air or other gasses, usually in a vortex motion, to impact fine particles against each other in a chamber.
Preferably, step 5) is carried out in the presence of a dispersant agent and a solvent.
The dispersant agent and solvent allow to prevent the fine frit particles from re- aggregating.
Step 5) is preferably carried out by mixing in a high shear mixer and then wet-milling in a high speed mill with special grinding chamber components such as zirconia, silicon nitrite and/or silicon carbide.
The wet-milling can be carried out in batch in multipass operation until the desired particle size is obtained.
In preferred embodiments, said high speed mill is a horizontal bead mill, with a Zirconia grinding chamber.
The wet-milling can be carried out in batch in multipass operation until the desired particle size is obtained.
More preferably, the glass frit composition of step 5) comprises 50-70 wt.% of dry-milled frit, up to 10 wt.% of a dispersant agent, and 20-45 wt.% of a solvent.
In particularly preferred embodiments, the glass frit composition of step 5) comprises 60- 70 wt.% of dry-milled frit, 1-3 wt. of a dispersant agent, and 29-37 wt.% of a solvent. Preferably, the dispersant agent is a copolymer with acidic group (Disperbyk 110™, Disperbyk 111™), alkylol ammonium salt of copolymer with acidic groups (Disperbyk- 180™), solution of high molecular weight block copolymers with pigment affinic groups (Disperbyk 182™, Disperbyk 184™, Disperbyk 190™), copolymer with pigment affinic groups (Disperbyk 191™, Disperbyk 192™, Disperbyk 194™, Tego Dispers 7502™, Tego Dispers 752W™), block-copolymer with pigment affinic groups (Disperbyk 2155™), solution of alkylol ammonium salt of a higher molecular weight acidic polymer (Anti-terra-250™), structured acrylate copolymer with pigment affinic groups (Disperbyk 2010™, Disperbyk 2015™), polyvinylpyrrolidone (PVP K-15™, PVP K-30™, PVP K- 60™), polymeric hyperdispersant (Solsperse J930™, Solsperse J945™, Solsperse J955™, Solsperse J980™, Solsperse J981™, Solsperse J944™, Solsperse J950™, Solsperse J955™), or a mixture thereof.
The solvent can be one or more alcohols, such as methyl alcohol, ethyl alcohol, propyl alcohols, butyl alcohols; glycols, such as methyl glycol (MG), ethyl glycol, propyl glycol, butyl glycol (BG); glycol ethers, such as methoxy propanol (PM), ethoxy propanol (EP), diacetone propanol (DAA), methoxy butanol, dipropylene glycol monomethyl ether (DPM), tripropylene glycol methyl ether (TPM), propylene glycol mono methyl ether (PM), di or tri propylene glycol mono propyl ether (DPnP, TPnP), butyl diglycol (BDG); esters, such as methyl acetate, ethyl acetate (ETAC), propyl acetate(IPAC), butyl acetate (BUAC), methoxy propyl acetate (PMA), ethyl-3-ethoxy-propanol (EEP); ketones, such as acetone, methyl ethyl ketone (MEK), methyl butyl ketone, cyclohexanone; aromatics, such as toluene, xylene, solvent naptha; aliphatics, such as cyclohexane, petroleum ether, white spirit, turpentine, water, or a mixture thereof.
Preferably, the solvent is an alcohol, selected from methyl alcohol, ethyl alcohol, propyl alcohol, and butyl alcohol, a glycol selected from methyl glycol, ethyl glycol, propyl glycol, and butyl glycol, a glycol ether selected from methoxy propanol, ethoxy propanol, diacetone propanol, methoxy butanol, dipropylene glycol monomethyl ether, tripropylene glycol methyl ether, propylene glycol mono methyl ether, di- or tri-propylene glycol mono propyl ether, and butyl diglycol, an ester selected from methyl acetate, ethyl acetate, propyl acetate, butyl acetate, methoxy propyl acetate, and ethyl-3-ethoxy-propanol, a ketone selected from acetone, methyl ethyl ketone, methyl butyl ketone, and cyclohexanone, an aromatic solvent selected from toluene, xylene, and solvent naptha, an aliphatic solvent selected from cyclohexane, petroleum ether, white spirit, and turpentine, or a mixture thereof.
More preferably, the solvent is a glycol selected from methyl glycol, ethyl glycol, propyl glycol, and butyl glycol, a glycol ether selected from methoxy propanol, ethoxy propanol, diacetone propanol, methoxy butanol, dipropylene glycol monomethyl ether, tripropylene glycol methyl ether, propylene glycol mono methyl ether, di- or tri-propylene glycol mono propyl ether, and butyl diglycol, or a mixture thereof.
In particularly preferred embodiments, the solvent is butyl diglycol.
In the most preferred embodiments, the glass frit composition of step 5) comprises 60-70 wt.% of dry-milled frit, 1-3 wt.% of an alkylol ammonium salt of copolymer with acidic groups, polyvinylpyrrolidone, or a mixture thereof, and 29-37 wt.% of butyl diglycol.
Step 5) is preferably carried out by mixing in a high shear mixer and then wet-milling in a high speed mill (e.g. NETZSCH model LMZ10 horizontal sand mill, with a Zirconia grinding chamber), for up to 24 hours until the desired particle size is obtained. This results in a highly stable glass frit composition with no or negligible sedimentation and having the desired volume particle size distribution Dv9o of less than 2 μηι.
In another aspect, the present invention concerns a ceramic inkjet ink comprising:
- 20-60 wt. % of a glass frit composition as above described,
- 0-20 wt % of a pigment having a volume particle size distribution Dv9o of less than 2 μιτι, as measured by laser diffraction,
- 20-60 wt. % of a solvent, and
- up to 5 wt % of a dispersant agent.
With "wt. %" it is meant weight percent of the total weight of the ceramic inkjet ink.
The ceramic inkjet ink composition according to the present invention shows advantageous properties, so that, at jetting, the following undesired effects are conveniently prevented: drop splattering, bleed and spread after landing on hard ceramic surfaces, such as glass. Additionally, the edge definition of the printed image during drying and tempering is retained.
Moreover, the ceramic inkjet ink composition according to the present invention has a high chemical resistance, e.g. resistance to acid, base, UV, a high mechanical resistance, e.g. scratch, abrasion, durability. For the purposes of the present invention, the pigment can be any inorganic colour pigment. The inorganic pigments powder is produced by high temperature calcination. The pigments can be oxides of metals such as cobalt, iron, nickel, copper, titanium dioxide for different colours.
Examples of suitable inorganic pigments are Cobalt chromite Blue green Spinel (Shepherd Blue 211, Shepherd Blue 30C527), Cobalt Aluminate Blue Spinel (Rockwood Cobalt Blue 28, Rockwood Cobalt blue 419, Shepherd Blue 214, Shepherd Blue 299, Shepherd Blue 385, Shepherd Blue 424), Iron oxide (SiOF 1020, SiOF 3029M, SiOF 2019M, SiOF 3021M, Bayferrox 120, Bayferrox 180, Rockwood Ferroxide 206M), Manganese Ferrite (Rockwood FM2400), Nickel Antimony Titanium Yellow Rutile (Shepherd Yellow 25, Shepherd Yellow 195), Copper Chromite Black Spinel (Shepherd Black 1 GM, Shepherd Black 430), manganese ferrite (Rockwood FM2400), White: Huntsman Ti02 A-HR; DuPont Ti-Pure® R-101, DuPont Ti-Pure® R-102, Green: Cobalt Titanate Green Spinel (Shepherd Green 223), Cobalt Chromite Blue Green Spinel (Shepherd Green 187 B).
These pigments are heat resistant inorganic pigments, chemically inert and stable to ultraviolet light. They have high durability and hiding power.
The pigment type, size and its particle interaction can be adjusted during formulation to meet the final tempered colour of the ink as well as fulfil the requirement of hiding power (optical property used to describe the light-scattering efficiency of a white pigment) and opacity (degree to which light is not allowed to pass through).
Preferably, the pigment has a volume particle size distribution Dv9o of less than 1 μπι. Commercially available inorganic pigments have indeed a particle size greater than 2-3 microns, therefore said particle size is reduced to make the pigments suitable for inkjet printing.
Particularly, the pigment is milled and grinded in the presence of a dispersant agent and a solvent, thus resulting in a pigment paste having a pigment volume particle size distribution Dv90 of less than 2 μιη, preferably less than 1 μπι.
Preferably, a bead/ball mill mixer is used with 1.75 mm zirconia grinding beads.
The combination of the dispersant agent and grinding step is crucial to obtain highly stable pigment paste with negligible/no sedimentation over long time.
Optionally, the ceramic inkjet ink can also comprise additives, such as carriers, rheology agents, surfactants, anti-settling/static agents, flow and levelling agents, de-foaming/de- aeration agents, and resins. Appropriate additives can improve the surface grip after drying at temperature equal to or above 150°C, for manual handling.
Said additives can be in an amount up to 10 wt. % in order to improve jetting and substrate-adhesion performances. With "wt. %" it is meant weight percent of the total weight of the ceramic inkjet ink.
Suitable carriers can be mixtures of alkane waxes with a low melting point of 40-100°C, being-solid at room temperature. Examples of such carriers are low melting paraffin wax. Alternatively, the carriers can be a mixture of linear Cio-C24 alkanes, preferably linear Cio- C22 alkanes, more preferably linear Ci2-Ci8 alkanes.
Suitable surfactants can be a solution of polyether-modified polydimethylsiloxane (commercially available as BYK-301, BYK-302, BYK 306, BYK 337, BYK 341), polyether modified polydimethylsiloxane (commercially available as BYK-307, BYK 333), solution of a polyester-modified polydimethylsiloxane (commercially available as BYK-310, BYK-313) solution of polyester-modified polymethylalkylsiloxane (commercially available as BYK-315) polyether modified dimethylpolysiloxane (commercially available as BYK378), or a mixture thereof.
Suitable flow and leveling agents can be polymeric, non silicone (commercially available as Dynoadd F-l, Dynoadd F-100, Dynoadd F-101, Dynoadd F-102), solution of polyester modified acrylic polymer (commercially available as Dynoadd F201), special dimethyl polysiloxanes (commercially available as Tego Flow ATF 2), polyether siloxane copolymer (commercially available as Tego Glide 100, Tego Wet 240), or a mixture thereof.
Suitable deaerating/defoaming agents can be Silicone free (commercially available as BYK 051, BYK 052, BYK 053, BYK 054, BYK 055, BYK 057, BYK 1752, BYK-A 535), emulsion of hydrophobic solids, emulsifiers and foam destroying polysiloxanes (commercially available as BYK-610), Fluoro-modified silicone defoamer (commercially available as Dynoadd F-470), non-silicone anionic (commercially available as Dynoadd F- 603), organo-modified polysiloxane (commercially available as Tego Airex 900, Deaerating organic polymers with tip of silicone (commercially available as Tego Airex 990, Tego Airex 991), silicone free deaerator (commercially available as Tego Airex 920), solution of polyacrylate (commercially available as Tego Flow ZFS 460), or a mixture thereof. Suitable rheology and anti-settling agents can be solution of modified urea (commercially available as BYK 410, BYK 420), solution of urea modified polyurethane (commercially available as BYK-425), solution of polyurethane with a highly branched structure (commercially available as BYK-428), solution of high molecular urea modified polar polyamide (commercially available as BYK-430, BYK-431), hybridised amide (commercially available as Disparlon AQH 800), non-ionic polyurethane based thickener (commercially available as Tego ViscoPlus 3000, Tego ViscoPlus 3030, Tego Viscoplus 3060), fumed silica (Aerosil), or a mixture thereof;
Suitable resins can be hydroxypropyl cellulose, hydroxyethyl cellulose, hydroxymethyl cellulose, nitrocellulose, methacrylic copolymer, or a mixture thereof.
In an additional aspect, the present invention concerns a process for producing the ceramic inkjet ink as above described, said process comprising the steps of:
a) preparing a pigment paste by milling and grinding pigment particles in the presence of a dispersant agent and a solvent to achieve a pigment volume particle size distribution Dv9o of less than 2 μηι;
b) preparing a glass frit composition according to the process above described, wherein in step 5) the wet-milling is carried out in the presence of a dispersant agent and a solvent;
c) mixing the pigment paste of step a) and the glass frit composition of step b) in a bead mixer;
d) adding a solvent to obtain a mixture having a solid content 30-60 wt. % on the total weight of the mixture; and
e) filtering the mixture of step d) through a micrometer pore size filter, thereby obtaining a ceramic inkjet ink having a viscosity of 6-20 mPa.s at jetting temperature and jetting conditions.
Preferably, the pigment paste of step a) is prepared as above described.
More preferably, the pigment paste of step a) comprises 45-85 wt. % pigment, 2-20 wt. % dispersant agent and 10-55 wt. % solvent.
Preferably, in step e) the micrometer pore size filter is a 20-micrometer pore size filter. With "wt. %" it is meant weight percent of the total weight of the pigment paste.
In preferred embodiments, the pigment paste of step a) comprises 50-80 wt. % pigment, 3- 10 wt. % dispersant agent and 15-45 wt. % solvent. Exemplary pigment pastes are the following:
- Black pigment paste 1
Pigment: Shepherd 1G = 79%
Dispersant agent: Disperbyk 180™: 4%
Solvent: DPM = 17%
- Black pigment paste 2
Pigment: Shepherd 1G = 50%
Dispersant agent: Disperbyk 194N™: 8%
Solvent: Butyl diglycol = 42%
- Black pigment paste 3
Pigment: Shepherd 1G = 54%
Dispersant agent: Disperbyk 194N™: 8%
Solvent: Butyl diglycol = 39%
- Blue pigment paste
Pigment: Shepherd 299 = 55%
Dispersant agent: Lubrizol J955™: 8%
Solvent: Butyl diglycol = 43%
- Red pigment paste
Pigment: SiOF 3092M = 50%
Dispersant agent: Lamberti Flujet 12/36™: 10%
Solvent: Butyl diglycol = 40%
- White pigment paste
Pigment: Ti02 A-Hr = 52%
Dispersant agent: Disperbyk 194N™: 5%
Solvent: Butyl diglycol = 43%
In an even further aspect, the present invention concerns a ceramic inkjet ink obtainable by the process as above described, said inkjet ink having a viscosity of 6-20 mPa.s at jetting temperature and jetting conditions, a surface tension of 20-40 mN/m at 5-60°C, and a volume particle size distribution Dvgo of less than 2 μιη, as measured by laser diffraction. In another aspect, the present invention concerns a method for printing a ceramic substrate, comprising the step of inkjet printing a ceramic substrate with an inkjet ink as above described. Preferably, said ceramic substrate is a glass substrate.
Particularly, said method comprises:
I) jetting the ceramic inkjet ink according to the present invention onto a ceramic substrate, preferably glass; and
II) drying the jetted ink on the substrate at temperature≥ 150°C.
It should be understood that all aspects identified as preferred and advantageous for the glass frit composition and the ceramic inkjet ink are to be deemed as similarly preferred and advantageous also for the respective processes of production and method of printing of the present invention.
It should be also understood that all the combinations of preferred aspects of the glass frit composition, ceramic inkjet ink, their processes of production, as well as their uses in printing ceramic substrates, as above reported, are to be deemed as hereby disclosed.
Below are working examples of the present invention provided for illustrative purposes. EXAMPLES
Example 1.
A glass frit having the following composition has been prepared:
Figure imgf000015_0001
Example 2.
A glass frit having the following composition has been prepared:
wt.%
SiC-2 45.1
ZnO 12.5
B203 18.6
Na20 7.92
K20 4.2
CaO 2.5
Ti02 3.4
Figure imgf000016_0001
Example 3.
A glass frit having the following composition has been prepared:
Example 4.
A glass frit having the
Figure imgf000016_0002
Example 5.
Glass frit pastes have been prepared by using the glass frits of Examples 1-4.
Each glass frit of Examples 1-4 has been suitably jet milled before been mixed with the dispersant agent and solvent, at the following amounts:
- Glass frit paste 1:
• 65 wt. % jet milled glass frit
• 1.75 wt. % polyvinylpyrrolidone 33.25 wt. % butyl diglycol
- Glass frit paste 2:
• 60 wt. % jet milled glass frit
• 3 wt. % Disperbyk 180™
• 27 wt. % butyl diglycol
The three components are initially mixed in a high shear mixer and then wet-milled in horizontal high speed mill with Zirconia grinding chamber in multi-pass operations for fixed time. This resulted in a highly stable frit with no or minimal sedimentation with a volume particle size distribution Dv9o of less than 2 μιη.
Example 6.
The glass frit paste 1 prepared as per Example 5 has been used to produce the following inkjet inks:
Inkjet ink 6a wt. % Solid content % Properties
Glass frit paste 1 57.2 50
Black pigment paste 2 24.3 η25°ο = 22 mPa.s,
a25°c - 28 mN/m
Surfactant BYK 378 0.3
Dv9o = 1.8 μπι
Butyl glycol 18.2
Inkjet ink 6b wt. % Solid content % Properties
Glass frit paste 1 57.2 50
Black pigment paste 3 24.3 η25°ο = 23 mPa.s,
o25°c = 25 mN/m
Surfactant BYK 378 0.5
Dv9o = 1.8 μιτι
Butyl glycol 18.2 Inkjet ink 6c wt. % Solid content % Properties
Glass frit paste 1 45.0 40
Black pigment paste 1 14.0 η25°ο = 13 mPa.s,
a25°c = 25 mN/m
Surfactant BYK 337 0.5
Dv9o = 1.3 μιη
Methacrylic copolymer 4.0
resin
Dipropylene glycol 38.5
monomethylether,
Butyl Glycol
where r|25°c is the viscosity at 25°C and a25°c is the surface tension at 25°C.
The above inkjet inks have been prepared by wet-mixing mill frit and pigment paste in bead mill mixer for 20 min, and then filtering the resulting inks by using a 20-micrometer pore size filter.
Example 7.
Jetting performances
The jetting of these inks at the jetting temperature of 30-45°C with standard commercial inkjet printing system showed reliable jetting.
Overall performance of the inks were very good satisfying low mistings and satellites and good jetting reliability. No nozzle blockage, print failures was observed.
Printing on the glass was performed in single pass and multipass (several layers) in order to achieve sufficient thickness to meet the final requirements such as optical density after high temperature heat treatment or tempering at temperature above 500°C.
Final printed pattern on the glass showed good colour, hiding power and good mechanical and chemical resistance.
Example 8.
Influence of choice of components and process steps on final ink properties
Non-optimised mixing and milling steps result in non-homogeneous mixture between frits and pigments and hence sedimentations of pigments (Figure la). Conversely, the inkjet inks prepared according to the present invention, after 1 month, show a very stable and homogeneous mixture, without pigment sedimentation (Figure lb).
Similarly, the non-optimisation of components, i.e. dispersant agent and solvent, results in non-homogeneous mixture between frits and pigments and hence sedimentation and flocculation (Figure 2a). Conversely, the inkjet inks prepared according to the present invention, after 1 week, show a very stable and homogeneous mixture, without pigment sedimentation (Figure 2b).
The ink rheology is tailored to achieve controlled shear thinning behaviour to reduce particle sedimentation during storage and drop spread/bleeding on glass substrate.
· Low shear viscosity (at shear rates < 50 1/s) is deliberately maintained at least several times greater than that of the high shear steady viscosity of 6-20 mPa.s (at shear rate > 1000 1/s) at the jetting temperature.
o This delays/prevent ink sedimentation during storage,
o The viscosity of the ink in the printhead channel prior to jetting drops to 6- 20 mPa.s meeting printhead bulk viscosity requirements creating optimum condition for drop ejection and generate reliable drop in-flight,
o After the drop lands on the substrate, the viscosity is quickly increased thus
minimising drop spread upon impact
maintaining drop edge definition
Prevent ink fingering/dendrite instability formation which sometime forms as a result of air-stream caused by fast linear carriage movement of printhead during printing or marangoni stress, or contaminated glass substrate (Figure 3a, comparative, and 3b, according to the invention).
Static surface tension is 20-40 mN/m to meet the printhead and substrate requirements.
· The static surface tension satisfies the drop contact angle on substrate.
• The choice of the surfactant is carefully controlled to achieve final static value. Uniform distribution of the particles during drying is obtained, thus preventing particle migration towards the edges or to the centre.

Claims

1. A glass frit composition comprising:
- 20-49 wt. % Si02,
- 3-20 wt. % B203,
- 1-9 wt. % Na20,
- 0.1-5 wt. % K20,
- 1-7 wt. % Ti02,
- 0.01-5 wt. % A1203, and
- a mixture of:
i) 50-60 wt. % Bi203, and 7-35 wt. % ZnO, or
ii) 7-15 wt. % ZnO, and up to 5 wt. % Li20, or
iii) 45-55 wt. % Bi203, and up to 5 wt. % Li20, or
iv) 40-45 wt. % Bi203, 0.5-3 wt. % ZnO, and up to 4 wt. % Li20,
said glass frit composition being in the form of particles having a volume particle size distribution Dv90 of less than 2 μπι, as measured by laser diffraction.
2. The glass frit composition according to claim 1, further comprising up to 7 wt. % of ZrO, CaO, BaO, MgO, P205, Fe203, SrO, or a mixture thereof.
3. The glass frit composition according to claim 1 or 2, comprising:
- 20-30 wt. % Si02,
- 3-10 wt. % B203,
- 1-5 wt. % Na20,
- 0.1-2 wt. % K20,
- 1-5 wt. % Ti02,
- 0.01-5 wt. % A1203, and
- a mixture of i) 50-60 wt. % Bi203, and 7-35 wt. % ZnO.
4. The glass frit composition according to claim 1 or 2, comprising:
- 40-49 wt. % Si02,
- 10-20 wt. % B203, - 5-9 wt. % Na20,
- 2-5 wt. % K20,
- 1-5 wt. % Ti02,
- 0.1-1 wt. % A1203, and
- a mixture of ii) 7-15 wt. % ZnO, and up to 5 wt. % Li20.
5. The glass frit composition according to claim 1 or 2, comprising:
- 30-40 wt. % Si02,
- 3-10 wt. % B203,
- 1-5 wt. % Na20,
- 0.1-2 wt. % K20,
- 2-7 wt. % Ti02,
- 0.01-0.5 wt. % A1203, and
- a mixture of iii) 45-55 wt. % Bi203, and up to 5 wt. % Li20.
6. The glass frit composition according to claim 1 or 2, comprising:
- 30-40 wt. % Si02,
- 3-10 wt. % B203,
- 1-5 wt. % Na20,
- 0.1-2 wt. % K20,
- 3-7 wt. % Ti02,
- 0.01-1 wt. % A1203, and
- a mixture of iv) 40-45 wt. % Bi203, 0.5-3 wt. % ZnO, and up to 4 wt. % Li20.
7. The glass frit composition according to any one of claims 1-6, said glass frit composition being in the form of particles having a volume particle size distribution Dv9o of less than 1 μηι, as measured by laser diffraction.
8. A process for producing the glass frit composition of claim 1, comprising the steps of:
1) mixing the oxides of the glass frit composition;
2) melting the mixed oxides to obtain a melted mixture;
3) cooling the obtained melted mixture; 4) dry-milling the so-cooled mixture to obtain a milled frit having a volume particle size distribution Dv90 of less than 8 μπι, preferably of 5 to 8 μηι; and
5) wet-milling the dry-milled frit to achieve a volume particle size distribution Dv9o of less than 2 μηι.
9. A ceramic inkjet ink comprising:
- 20-60 wt. % of a glass frit composition according to any one of claims 1-7,
- 0-20 wt % of a pigment having a volume particle size distribution Dv9o of less than 2 μπι, as measured by laser diffraction,
- 20-60 wt. % of a solvent, and
- up to 5 wt % of a dispersant agent.
10. The inkjet ink of claim 9, wherein the pigment has a volume particle size distribution Dv9o of less than 1 μηι.
11. The inkjet ink of claim 9 or 10, wherein the dispersant agent is a copolymer with acidic group, alkylol ammonium salt of copolymer with acidic groups, solution of high molecular weight block copolymers with pigment affinic groups, copolymer with pigment affinic groups, block-copolymer with pigment affinic groups, solution of alkylol ammonium salt of a higher molecular weight acidic polymer, structured acrylate copolymer with pigment affinic groups, polyvinylpyrrolidone, polymeric hyperdispersant or a mixture thereof.
12. The inkjet ink of any one of claims 9-11, wherein the solvent is an alcohol, selected from methyl alcohol, ethyl alcohol, propyl alcohol, and butyl alcohol, a glycol selected from methyl glycol, ethyl glycol, propyl glycol, and butyl glycol, a glycol ether selected from methoxy propanol, ethoxy propanol, diacetone propanol, methoxy butanol, dipropylene glycol monomethyl ether, tripropylene glycol methyl ether, propylene glycol mono methyl ether, di- or tri-propylene glycol mono propyl ether, and butyl diglycol, an ester selected from methyl acetate, ethyl acetate, propyl acetate, butyl acetate, methoxy propyl acetate, and ethyl-3-ethoxy-propanol, a ketone selected from acetone, methyl ethyl ketone, methyl butyl ketone, and cyclohexanone, an aromatic solvent selected from toluene, xylene, and solvent naptha, an aliphatic solvent selected from cyclohexane, petroleum ether, white spirit, and turpentine, water or a mixture thereof.
13. A process for producing the ceramic inkjet ink of claim 9, comprising the steps of: a) preparing a pigment paste by milling and grinding pigment particles in the presence of a dispersant agent and a solvent to achieve a pigment volume particle size distribution Dv9o of less than 2 μιτι;
b) preparing a glass frit composition according to the process of claim 8, wherein in step 5) the wet-milling is carried out in the presence of a dispersant agent and a solvent;
c) mixing the pigment paste of step a) and the glass frit composition of step b) in a bead mixer;
d) adding a solvent to obtain a mixture having a solid content 30-60 wt. % on the total weight of the mixture; and
e) filtering the mixture of step d) through a micrometer pore size filter, thereby obtaining a ceramic inkjet ink having a viscosity of 6-20 mPa.s at jetting temperature and jetting conditions.
14. The process of claim 13, wherein the pigment paste of step a) comprises 45-85 wt. % pigment, 2-20 wt. % dispersant agent and 10-55 wt. % solvent.
15. A ceramic inkjet ink obtainable by the process of claim 13 or 14, said inkjet ink having a viscosity of 6-20 mPa.s at jetting temperature and jetting conditions, a surface tension of 20-40 mN/m at 5-60°C, and a volume particle size distribution Dv90 of less than 2 μηι, as measured by laser diffraction.
16. A method for printing a ceramic substrate, comprising the step of inkjet printing a ceramic substrate with a inkjet ink according to any one of claims 9-12 and 15.
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CN113354281B (en) * 2021-08-09 2021-12-07 广东兴辉陶瓷集团有限公司 Dew dry particle and dew effect glaze ink, preparation method thereof, rock plate and preparation method thereof
CN113354281A (en) * 2021-08-09 2021-09-07 广东兴辉陶瓷集团有限公司 Dew dry particle and dew effect glaze ink, preparation method thereof, rock plate and preparation method thereof
EP4166616A1 (en) 2021-10-18 2023-04-19 Schott Ag Ceramic printing ink, in particular for inkjet printing, for producing a coating on a glass-ceramic material and coated glass ceramic plate
DE102021126968A1 (en) 2021-10-18 2023-04-20 Schott Ag Ceramic printing ink, in particular for inkjet printing, for producing a coating on a glass ceramic and coated glass ceramic plate
FR3128217A1 (en) 2021-10-19 2023-04-21 Eurokera S.N.C. Glazed mineral substrate and method of manufacturing such a substrate
WO2023066945A1 (en) 2021-10-19 2023-04-27 Eurokera S.N.C Enamelled mineral substrate and method for making same
DE202022002828U1 (en) 2021-10-19 2023-08-17 Eurokera S.N.C. Enamelled mineral substrate
EP4204373B1 (en) 2021-10-19 2024-01-03 Eurokera S.N.C. Enamelled mineral substrate and method for making same
ES2955477A1 (en) * 2023-01-10 2023-12-01 Tecglass Sl PROCEDURE FOR OBTAINING AND APPLYING A DIGITAL INK FOR PRINTING ON A GLASS THAT HAS A FUNCTIONAL FILM AND INK OBTAINED THROUGH SUCH PROCEDURE (Machine-translation by Google Translate, not legally binding)
WO2024149920A1 (en) * 2023-01-10 2024-07-18 Tecglass Sl Method for obtaining and applying a digital ink for printing on a piece of glass having a functional film and ink obtained using the method

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