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WO2018043361A1 - Method for producing chemically toughened glass - Google Patents

Method for producing chemically toughened glass Download PDF

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Publication number
WO2018043361A1
WO2018043361A1 PCT/JP2017/030617 JP2017030617W WO2018043361A1 WO 2018043361 A1 WO2018043361 A1 WO 2018043361A1 JP 2017030617 W JP2017030617 W JP 2017030617W WO 2018043361 A1 WO2018043361 A1 WO 2018043361A1
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Prior art keywords
glass
alkali
water vapor
inorganic salt
acid
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PCT/JP2017/030617
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French (fr)
Japanese (ja)
Inventor
祐輔 藤原
出 鹿島
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AGC Inc
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Asahi Glass Co Ltd
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    • 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
    • C03C21/00Treatment of glass, not in the form of fibres or filaments, by diffusing ions or metals in the surface
    • GPHYSICS
    • G06COMPUTING OR CALCULATING; COUNTING
    • G06FELECTRIC DIGITAL DATA PROCESSING
    • G06F3/00Input arrangements for transferring data to be processed into a form capable of being handled by the computer; Output arrangements for transferring data from processing unit to output unit, e.g. interface arrangements
    • G06F3/01Input arrangements or combined input and output arrangements for interaction between user and computer
    • G06F3/03Arrangements for converting the position or the displacement of a member into a coded form
    • G06F3/041Digitisers, e.g. for touch screens or touch pads, characterised by the transducing means
    • GPHYSICS
    • G02OPTICS
    • G02FOPTICAL DEVICES OR ARRANGEMENTS FOR THE CONTROL OF LIGHT BY MODIFICATION OF THE OPTICAL PROPERTIES OF THE MEDIA OF THE ELEMENTS INVOLVED THEREIN; NON-LINEAR OPTICS; FREQUENCY-CHANGING OF LIGHT; OPTICAL LOGIC ELEMENTS; OPTICAL ANALOGUE/DIGITAL CONVERTERS
    • G02F1/00Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics
    • G02F1/01Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics for the control of the intensity, phase, polarisation or colour 
    • G02F1/13Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics for the control of the intensity, phase, polarisation or colour  based on liquid crystals, e.g. single liquid crystal display cells
    • G02F1/133Constructional arrangements; Operation of liquid crystal cells; Circuit arrangements
    • G02F1/1333Constructional arrangements; Manufacturing methods

Definitions

  • the present invention relates to a method for producing chemically strengthened glass.
  • Chemically strengthened glass is used as a cover glass for various display devices.
  • Patent Document 1 discloses that Na in glass and K in the inorganic salt are brought into contact with a specific inorganic salt containing potassium nitrate.
  • a method is disclosed in which a chemical strengthening treatment is performed by ion-exchange of and then an acid and alkali treatment is performed.
  • Patent Document 1 describes that the surface strength of glass is remarkably improved without subjecting the glass surface after chemical strengthening treatment to etching treatment using polishing or hydrofluoric acid.
  • Patent Document 1 does not disclose a glass manufacturing method for improving the touch feeling with a finger.
  • an object of the present invention is to provide a method for producing chemically tempered glass for improving the function of touch comfort.
  • the method for producing chemically strengthened glass according to the first aspect of the present invention includes a step of preparing a glass containing alkali ions, and another alkali ion larger than the ion radius of the alkali ions contained in the glass, and is 10 wt%.
  • a step of ion exchange with ions is a step of preparing a glass containing alkali ions, and another alkali ion larger than the ion radius of the alkali ions contained in the glass, and is 10 wt%.
  • Drawing 1 is a mimetic diagram showing a manufacturing process in a manufacturing method of chemically strengthened glass concerning the present invention.
  • FIG. 2 is a schematic diagram of an experimental system for forming an atmosphere in an ion exchange process.
  • the method for producing chemically strengthened glass according to the present invention (hereinafter also abbreviated as the method of the present invention) (A) preparing a glass containing alkali ions; (B) preparing an inorganic salt containing other alkali ions larger than the ion radius of the alkali ions contained in the glass and having a pH of 8 or more and 14 or less when a 10 wt% aqueous solution is formed; (C) ion exchange between the alkali ions contained in the glass and other alkali ions contained in the inorganic salt in an atmosphere having a dew point temperature of 39 ° C. or higher; It is characterized by including. Each step will be described below.
  • the glass used in the method of the present invention only needs to contain alkali ions, and various glasses can be used as long as they have a composition that can be strengthened by molding and chemical strengthening treatment. Among them, it is preferable to contain sodium, and specific examples include aluminosilicate glass, soda lime glass, borosilicate glass, lead glass, alkali barium glass, aluminoborosilicate glass, and the like.
  • the method for producing the glass is not particularly limited, and a desired glass raw material is charged into a continuous melting furnace, and the glass raw material is heated and melted preferably at 1500 to 1600 ° C., clarified, and then supplied to a molding apparatus. It can be manufactured by forming into a plate shape and slowly cooling.
  • various methods can be employed for forming the glass.
  • various forming methods such as a down draw method (for example, an overflow down draw method, a slot down method and a redraw method), a float method, a roll-out method, and a press method can be employed.
  • the float method is preferred in that cracks are likely to occur on at least a part of the glass surface, and the effects of the present invention are more prominent.
  • the thickness of the glass is not particularly limited, but is usually preferably 5 mm or less, more preferably 3 mm or less, and even more preferably 1 mm or less for effective chemical strengthening treatment. Preferably, 0.7 mm or less is particularly preferable.
  • the shape of the glass used in the method of the present invention is not particularly limited.
  • various shapes of glass such as a flat plate shape having a uniform plate thickness, a shape having a curved surface on at least one of the front surface and the back surface, and a three-dimensional shape having a bent portion can be employed.
  • the composition expressed by mol% on the basis of oxide is SiO 2 2 to 50 to 74%, Al 2 O 3 to 1 to 10%, Na 2 O to 6 to 14%, K 2 O to 3 to 11%, MgO to 2 to 15%, CaO to 0 to 6% and ZrO 2 to 5%
  • the total content of SiO 2 and Al 2 O 3 is 75% or less
  • the total content of Na 2 O and K 2 O is 12 to 25%
  • the content of MgO and CaO the total is 7-15% glass
  • composition viewed in mole percent on the oxide basis is,
  • the composition expressed by mass% based on the oxide is 65 to 75% for SiO 2 and 0.002 for Al 2 O 3 .
  • Gala containing 1-5%, MgO 1-6%, CaO 1-15% and Na 2 O + K 2 O 10-18% The composition expressed by mass% based on the oxide is SiO 2 60-72%, Al 2 O 3 1-10%, MgO 5-12%, CaO 0.1-5%, It contains 13 to 19% Na 2 O and 0 to 5% K 2 O, and RO / (RO + R 2 O) is 0.20 or more and 0.42 or less (wherein RO is an alkaline earth metal oxide) , R 2 O represents an alkali metal oxide.)
  • the composition expressed in mol% based on the oxide is 55.5 to 80% for SiO 2 and 12 to 20% for Al 2 O 3.
  • the chemically strengthened glass produced by the method of the present invention has an ion-exchanged compressive stress layer on the glass surface.
  • the surface of glass is ion exchanged to form a surface layer in which compressive stress remains.
  • alkali metal ions Li ions and / or Na ions
  • other alkali ions Na ions and / or larger ions
  • chemical strengthening treatment is performed by ion exchange by bringing the glass containing alkali ions into contact with an inorganic salt containing other alkali ions larger than the ion radius of alkali ions contained in the glass. . Therefore, the inorganic salt used in the method of the present invention contains other alkali ions larger than the ionic radius of the alkali ions contained in the glass.
  • the inorganic salt has a pH of 8 or more, preferably 9 or more, more preferably 10 or more, when a 10 wt% aqueous solution is used. Moreover, pH is 14 or less, Preferably it is 13 or less, More preferably, it is 12 or less.
  • pH of the inorganic salt is measured with a pH meter at 25 ° C.
  • the pH of the inorganic salt can be adjusted to a desired range by a known method.
  • a method for adjusting the pH of the inorganic salt specifically, for example, when the alkali ion contained in the glass is Na ion, the inorganic salt is an inorganic salt containing potassium nitrate (KNO 3 ), and Examples thereof include a method of adding at least one salt selected from the group consisting of K 2 CO 3 , Na 2 CO 3 , KHCO 3 , and NaHCO 3 .
  • the melting point of potassium nitrate is 330 ° C., and the melting point is below the strain point (usually 500 to 600 ° C.) of the glass to be chemically strengthened.
  • salts excluding potassium nitrate (hereinafter sometimes referred to as “flux”) have a property of cutting a glass network represented by Si—O—Si bonds. Since the temperature at which the chemical strengthening treatment is performed is as high as several hundred degrees Celsius, the covalent bond between Si—O of the glass is appropriately broken at that temperature, and the formation of the uneven layer due to the lowering of density described later tends to proceed.
  • the degree of breaking the covalent bond varies depending on the chemical composition treatment conditions such as the glass composition, the type of salt (flux) used, the temperature and time for the chemical strengthening treatment, but the four covalent bonds extending from Si. Of these, it is considered preferable to select conditions that are sufficient to break one or two bonds.
  • the inorganic salt includes, for example, alkali chlorides or alkali borates such as sodium chloride, potassium chloride, sodium borate or potassium borate within a range not inhibiting the effects of the present invention. But you can. These may be added alone or in combination of two or more.
  • the sum of the carbonate anion concentration and the hydrogen carbonate anion concentration obtained by the following formula in the inorganic salt is preferably 4 mol% or more, more preferably 6 mol% or more. This concentration is preferably 4 mol% or more because the amount of water in the molten salt in the chemical strengthening treatment can be increased and the formation reaction of the uneven layer on the glass surface described later can be promoted.
  • ⁇ (Carbonate anion concentration) + (hydrogen carbonate anion concentration) ⁇ (mol%) ⁇ (amount of carbonate anion in inorganic salt) + (amount of hydrogen carbonate anion in inorganic salt) ⁇ (mol) / (in inorganic salt) Total anion) (mol) x 100
  • the value of the carbonate anion concentration detected in the measurement corresponds to the sum of the carbonate anion concentration and the hydrogen carbonate anion concentration. Further, the sum of the carbonate anion concentration and the hydrogen carbonate anion concentration is not more than the sum of the saturated carbonate anion concentration and the saturated bicarbonate anion concentration.
  • glass is immersed in a molten salt, and alkali ions (Li ions or Na ions) in the glass are ion-exchanged with other alkali ions (Na ions or K ions) having a large ion radius in the molten salt ( Is performed).
  • alkali ions Li ions or Na ions
  • Na ions or K ions alkali ions having a large ion radius in the molten salt
  • the density of the chemically strengthened glass gradually increases from the outer edge of the intermediate layer 30 (bulk) existing in the center of the glass toward the surface of the compressive stress layer. There is no clear boundary between 20 and 20 where the density changes rapidly.
  • the intermediate layer is a layer present in the center of the glass and sandwiched between the compressive stress layers. Unlike the compressive stress layer, this intermediate layer is a layer that is not ion-exchanged.
  • dew point a dew point temperature
  • the density of the uneven layer 10 is lower than the density inside the glass, it is also referred to as a low density layer.
  • the thickness of the uneven layer 10 can be increased by increasing the amount of water vapor in the molten salt in the chemical strengthening treatment.
  • Examples of the method of bringing the glass into contact with the inorganic salt include a method of applying a paste-like inorganic salt, a method of spraying an inorganic salt aqueous solution onto the glass, or a method of immersing the glass in a salt bath of a molten salt heated to a melting point or higher.
  • the method of immersing in molten salt is preferable.
  • Molten salt can be produced by a known process.
  • the inorganic salt is a molten salt containing potassium nitrate and a flux
  • it can be obtained by preparing a potassium nitrate molten salt and then adding the flux to the potassium nitrate molten salt.
  • it can be obtained by mixing potassium nitrate and a flux and then melting a mixed salt of the potassium nitrate and the flux.
  • the molten salt used in the method of the present invention preferably has a Na concentration of 500 ppm by weight or more, more preferably 1000 ppm by weight or more. It is more preferable that the Na concentration in the molten salt is 2000 ppm by weight or more because the uneven layer is easily deepened by the acid treatment step described later.
  • concentration It is permissible until a desired surface compressive stress (CS) is obtained.
  • the molten salt that has been subjected to the chemical strengthening treatment one or more times contains sodium eluted from the glass. Therefore, if the Na concentration is already within the above range, glass-derived sodium may be used as it is as the Na source, or when the Na concentration is insufficient or when an unused molten salt is used for the chemical strengthening treatment. It can be prepared by adding an inorganic sodium salt such as sodium nitrate.
  • the chemical strengthening treatment (ion exchange step) in the present invention can be specifically performed by the following procedure. First, the glass is preheated, and the above-described molten salt is adjusted to a temperature at which chemical strengthening is performed. Next, the preheated glass is immersed in the molten salt for a predetermined time, and then the glass is pulled up from the molten salt and allowed to cool. In addition, it is preferable to perform shape processing according to a use, for example, mechanical processing, such as a cutting
  • the preheating temperature of glass depends on the temperature immersed in the molten salt, but is generally preferably 100 ° C. or higher.
  • the chemical strengthening temperature is preferably not more than the strain point of the glass to be tempered (usually 500 to 600 ° C.), particularly preferably 350 ° C. or more in order to obtain a higher compressive stress layer depth, shortening the processing time and promoting the formation of the uneven layer Therefore, 400 ° C. or higher is more preferable, and 430 ° C. or higher is more preferable.
  • the immersion time of the glass in the molten salt is preferably 1 minute to 10 hours, more preferably 5 minutes to 8 hours, and even more preferably 10 minutes to 4 hours. In such a range, a chemically strengthened glass excellent in the balance between strength and depth of the compressive stress layer can be obtained, which is preferable.
  • the ion exchange process is performed in an atmosphere with a dew point temperature of 39 ° C or higher.
  • the dew point temperature is preferably 50 ° C. or higher, more preferably 60 ° C. or higher, further preferably 70 ° C. or higher, more preferably 80 ° C. or higher, and particularly preferably 90 ° C. or higher.
  • the dew point temperature is preferably set to be equal to or lower than the temperature of the inorganic salt (molten salt) for performing ion exchange.
  • the following may be considered as the reason why the uneven layer is formed on the chemically strengthened glass obtained by performing chemical strengthening treatment in a molten salt having a large amount of water vapor (water content).
  • carbonate ions forming the molten salt react with water, hydrogen carbonate ions and hydroxide ions are generated as shown in the following formula.
  • hydroxide ions are ions that promote the cutting of the glass network, it is considered that the formation of an uneven layer on the glass surface is promoted by generating more hydroxide ions.
  • the dew point temperature may be such that the dew point temperature at least near the interface of the molten salt is within the above range, and the vicinity of the interface means an atmosphere in an area of 200 mm or less from the interface of the molten salt.
  • the dew point can be measured with a Vaisala DRYCAP® DMT346 dew point converter.
  • the dew point in this specification is a value when it is considered that an equilibrium is established between the molten salt and the atmosphere in the vicinity of the molten salt interface.
  • the dew point can be achieved by introducing water vapor into the molten salt and / or the atmosphere in the vicinity of the interface of the molten salt before and / or simultaneously with the ion exchange step. That is, water vapor itself or a gas containing water vapor may be bubbled directly into the molten salt, or a gas containing water vapor or water vapor may be introduced into the space above the molten salt. Moreover, it is also possible to send water (liquid) itself directly into the molten salt within a range where no steam explosion occurs.
  • the molten salt When introducing water vapor or a gas containing water vapor or water (liquid) (hereinafter, simply referred to as “water vapor”), the molten salt may or may not be stirred. Stirring is preferable in terms of shortening.
  • the time from the introduction of water vapor, etc. until equilibrium is reached varies depending on the amount of gas or liquid to be introduced, the water vapor concentration, the method of introduction, etc., but it cannot be generally stated, but the dew point of the above atmosphere is stable and constant. Can be judged as having reached equilibrium.
  • a gas that does not affect the chemical strengthening treatment can be used.
  • a dry gas A such as air, nitrogen gas, carbon dioxide gas or the like is introduced into heated water 24.
  • the gas B gas containing water vapor
  • steam with high humidity.
  • the water 24 used as a water vapor supply source it is preferable to use pure water such as ion-exchanged water from the viewpoint of suppressing scale accumulation on piping and the like.
  • the water 24 is heated by, for example, a water bath using a water tank 25.
  • examples thereof include introducing gas B containing water vapor into (molten salt 26), or (3) introducing water (liquid) directly into inorganic salt (molten salt 26).
  • a water vapor supply unit a bubbling unit, or an introduction unit for introducing water (liquid) may be appropriately provided according to the apparatus, and is not particularly limited.
  • the amount of water vapor supplied in the gas introduced per 1 cm 3 is preferably 0.04 mg / min or more, and more preferably 0.08 mg / min or more.
  • the flow rate of water introduced per 1 cm 3 is preferably 0.04 mg / min or more, and more preferably 0.08 mg / min or more.
  • the amount of water vapor supplied in the gas introduced per 1 cm 3 is preferably 0.04 mg / min or more, and 0.08 mg / min or more. Is more preferable.
  • the thickness of the concavo-convex layer 10 is about 100 to 200 nm in the conventional ion exchange process in which water vapor is not introduced, whereas in the method of the present invention, the pH when the aqueous solution is 10 wt% is 8 or more and 14 or less.
  • the thickness can be increased to 300 nm or more by ion exchange in an atmosphere having a dew point temperature of 39 ° C. or higher using a salt.
  • the uneven layer 10 can be removed by, for example, an acid treatment step and an alkali treatment step described later.
  • the thickness of the uneven layer 10 is preferably 300 nm or more from the viewpoint of the amount of glass surface removal.
  • the average depth of cracks and latent scratches on the glass surface generated in the glass processing process including the glass manufacturing process and the chemical strengthening process is about 500 nm. Therefore, the thickness of the uneven layer 10 is more preferably 500 nm or more, and further preferably 600 nm or more.
  • the thickness of the concavo-convex layer can be determined from the period ( ⁇ ) measured by the X-ray reflectivity method (X-ray-Reflectometry: XRR).
  • the density of the uneven layer is preferably lower than the density of the region (bulk) deeper than the ion-exchanged compressive stress layer from the viewpoint of glass surface removability.
  • the density of the uneven layer can be obtained from the critical angle ( ⁇ c) measured by XRR.
  • ⁇ c critical angle measured by XRR.
  • SEM scanning electron microscope
  • the thickness of the concavo-convex layer 10 is set to be equal to or greater than the average depth of cracks and latent scratches existing on the glass surface. Tempered glass can be obtained.
  • the formed concavo-convex layer 10 may be removed by a step of contacting with an acid or an acid / alkali described later in the step of removing a part of the surface of the glass. In this case, if all the cracks and latent scratches on the glass surface are shallower than the thickness of the concavo-convex layer, all the cracks and latent scratches can be removed in the step of contacting with alkali.
  • the surface strength of the chemically strengthened glass can be increased by removing cracks and latent scratches on the glass surface that cause a decrease in strength in the chemically strengthened glass.
  • the method of the present invention preferably further includes a step of washing the glass between the step of ion exchange and the step of removing part of the surface of the glass.
  • the glass is cleaned using industrial water or ion exchange water. Use the treated water if necessary. Of these, ion-exchanged water is preferred.
  • the washing conditions vary depending on the washing solution used, but when ion-exchanged water is used, washing at 0 to 100 ° C. is preferable from the viewpoint of completely removing the attached salt.
  • Various cleaning methods include, for example, a method of immersing chemically tempered glass in a water tank containing ion-exchanged water, a method of exposing the glass surface to running water, and a method of spraying a cleaning liquid toward the glass surface by a shower. The method is mentioned.
  • the method of the present invention may further include a step of removing a part of the surface of the glass ion-exchanged by the ion-exchange step.
  • the method of the present invention preferably includes a step of contacting the glass with an acid (acid treatment step) as a step of removing a part of the surface of the glass, and a step of contacting the glass with an alkali after the acid treatment step ( An alkali treatment step) may be further included.
  • a step of contacting the glass with an acid as a step of removing a part of the surface of the glass after the ion exchange step or the washing step.
  • the acid treatment is performed by immersing the chemically strengthened glass in an acidic solution, whereby Na and / or K on the surface of the chemically strengthened glass can be replaced with H.
  • the surface of the glass further has a concavo-convex layer in which the surface layer of the compressive stress layer is altered, specifically, the density is reduced.
  • the solution used for the acid treatment is not particularly limited as long as it is acidic, and may be less than pH 7.
  • the acid used may be a weak acid or a strong acid. Specifically, acids such as hydrochloric acid, nitric acid, sulfuric acid, phosphoric acid, acetic acid, oxalic acid, carbonic acid or citric acid are preferred. These acids may be used alone or in combination.
  • the temperature at which the acid treatment is performed varies depending on the type, concentration, and time of the acid used, but is preferably 100 ° C. or less.
  • the time for the acid treatment varies depending on the type, concentration and temperature of the acid used, but is preferably 10 seconds to 5 hours from the viewpoint of productivity, and more preferably 1 minute to 2 hours.
  • the concentration of the solution used for the acid treatment varies depending on the type of acid used, the time, and the temperature, but is preferably a concentration at which there is little concern about container corrosion, and specifically 0.1 to 20% by weight.
  • an alkali treatment step may be included after the acid treatment step. More preferably, after the acid treatment step, before the alkali treatment step, a step of washing the same glass as the step of washing described above is performed.
  • Alkali treatment is performed by immersing chemically strengthened glass in a basic solution, whereby a part of the uneven layer formed in the acid treatment step can be removed. Thereby, while improving the intensity
  • the solution used for the alkali treatment is not particularly limited as long as it is basic, and may have a pH exceeding 7, and a weak base or a strong base may be used.
  • bases such as sodium hydroxide, potassium hydroxide, potassium carbonate and sodium carbonate are preferred. These bases may be used alone or in combination.
  • the temperature at which the alkali treatment is performed varies depending on the type, concentration and time of the base used, but is preferably 0 to 100 ° C, more preferably 10 to 80 ° C, and particularly preferably 20 to 60 ° C. If it is this temperature range, there is no possibility that glass will corrode and it is preferable.
  • the alkali treatment time varies depending on the type, concentration and temperature of the base used, it is preferably 10 seconds to 5 hours from the viewpoint of productivity, and more preferably 1 minute to 2 hours.
  • the concentration of the solution used for the alkali treatment varies depending on the type of base used, the time, and the temperature, but is preferably 0.1% by weight to 20% by weight from the viewpoint of glass surface removability.
  • a part of the concavo-convex layer 10 may be removed by the alkali treatment.
  • the thicker the uneven layer the easier the glass surface is removed.
  • the alkali treatment a part of the concavo-convex layer into which H has penetrated is removed, whereby a chemically strengthened glass with improved surface strength can be obtained.
  • the method of the present invention it is present on the glass surface by chemical strengthening treatment in an atmosphere having a dew point of 39 ° C. or higher using an inorganic salt having a pH of 8 or more and 14 or less when a 10 wt% aqueous solution is used.
  • the thickness of the concavo-convex layer 10 can be made deeper than the depth of cracks and latent scratches. Therefore, it is considered that cracks and latent scratches existing on the glass surface can be removed together with the concavo-convex layer, which contributes further by improving the surface strength of the glass.
  • the chemically strengthened glass obtained by the method of the present invention has a very high surface strength.
  • the compressive stress value of the compressive stress layer and the depth of the compressive stress layer of the chemically tempered glass can be measured using an EPMA (electron probe micro analyzer) or a surface stress meter (for example, FSM-6000 manufactured by Orihara Seisakusho). .
  • EPMA electron probe micro analyzer
  • surface stress meter for example, FSM-6000 manufactured by Orihara Seisakusho.
  • the removal amount (thickness) of the glass surface (concave layer) after the step of removing a part of the glass surface is to measure the weight before and after the chemical treatment with an analytical electronic balance and convert the thickness using the following formula: It can ask for.
  • (Removed thickness per side) [(weight before removing part of glass surface) ⁇ (weight after removing part of glass surface)] / (glass specific gravity) / treated area / 2 At this time, the glass specific gravity is calculated as 2.50 (g / cm 3 ).
  • the surface compressive stress value (CS, unit: MPa) of glass and the depth (DOL, unit: ⁇ m) of the compressive stress layer were measured using a surface stress meter (FSM-6000) manufactured by Orihara Seisakusho.
  • Examples 1 to 5 Potassium nitrate, potassium carbonate and sodium nitrate were added to a stainless steel (SUS) pot and heated to 450 ° C. with a mantle heater to prepare a molten salt having the composition shown in Table 1.
  • Table 1 shows the pH of the inorganic salt (pH of the 10 wt% aqueous solution) when the 10 wt% aqueous solution was used. Water vapor was included in the molten salt by flowing air introduced into water heated to 95 ° C. in an atmosphere near the interface of the molten salt.
  • Air was used as the dried gas A, and the air was humidified by passing the air through water 24 heated to 95 ° C. by a water tank 25 to obtain humidified gas (air) B containing water vapor.
  • air air
  • this gas B containing water vapor into the space above the inorganic salt (molten salt) 26 of the tank that performs the chemical strengthening treatment through the route heated by the ribbon heater, the dew point was controlled in the ion exchange process. .
  • the amount of water vapor supplied per cm 3 and the dew points near the interface of the molten salt are as shown in Table 1.
  • Glass A composition (expressed as mol% based on oxide): SiO 2 68.74%, Al 2 O 3 2.96%, Na 2 O 14.20%, K 2 O 0.15%, MgO 6.16% , CaO 7.75%
  • Glass B composition (expressed as mol% based on oxide): SiO 2 64.4%, Al 2 O 3 10.5%, Na 2 O 16.0%, K 2 O 0.6%, MgO 8.3% , ZrO 2 0.2%
  • Glass C composition (mole% based on oxide): SiO 2 67.0%, Al 2 O 3 13.0%, Na 2 O 14.0%, B 2 O 3 4.0%, K 2 O ⁇ 1.0%, MgO 2.0%, CaO ⁇ 1.0%
  • nitric acid nitric acid 1.38 (manufactured by Kanto Chemical Co., Ltd.) diluted with ion-exchanged water] was prepared in a beaker, and the temperature was adjusted to the temperature shown in Table 1 using a water bath. Under the conditions shown in Table 1, acid treatment was performed by immersing the glass obtained in the ion exchange treatment step in prepared nitric acid. Thereafter, the glass was washed with water and subjected to an alkali treatment step.
  • a 4.0% by weight sodium hydroxide aqueous solution [48% sodium hydroxide solution (manufactured by Kanto Chemical Co., Ltd.) diluted with ion-exchanged water] was prepared in a beaker, and the temperature was adjusted to the temperature shown in Table 1 using a water bath. .
  • the glass washed after the acid treatment step was immersed in the prepared aqueous sodium hydroxide solution and subjected to alkali treatment. Then, the glass was washed with water to wash the alkali on the glass surface. Thereafter, it was dried by air blow.
  • Table 1 shows the sodium content without adding potassium carbonate to the molten salt in the ion exchange step.
  • the pH of the 10 wt% aqueous solution was as shown in Table 1 in terms of the amount of water vapor supplied per cm 3 and the dew points near the molten salt interface.
  • the obtained chemically tempered glass was washed with water and then dried by air blow to obtain chemically tempered glasses of Comparative Examples 2, 4, and 6.
  • Table 1 shows the processing conditions and evaluation results of the glass.
  • the pH when the 10 wt% aqueous solution of the inorganic salt used in the ion exchange step is 8 or more and 14 or less, and the dew point in the ion exchange step is controlled to 39 ° C. or more, so that it is comfortable to touch. It was found that chemically strengthened glass was obtained.
  • chemically tempered glass having a very good touch feeling can be obtained without chemical etching and etching treatment using polishing or hydrofluoric acid. That is, it is possible to obtain a chemically strengthened glass excellent in touch feeling without appearance defects due to expansion of latent scratches accompanying etching treatment with hydrofluoric acid or the like, and polishing scratches accompanying polishing.
  • the method for producing chemically strengthened glass of the present invention can be applied to any glass and has high versatility. And since a process can be advanced by immersion in a solution, it is efficient at the point of being easy to respond

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Abstract

The present invention provides a method for producing a chemically toughened glass, which improves the texture to the touch of the glass. The present invention relates to a method for producing a chemically toughened glass, which comprises: a step for preparing a glass containing alkali ions; a step for preparing an inorganic salt which contains other alkali ions that have a larger ionic radius than the alkali ions contained in the glass, and which has a pH of 8 to 14 (inclusive) when formed into a 10 wt% aqueous solution; and a step for performing ion exchange between the alkali ions contained in the glass and the other alkali ions contained in the inorganic salt in an atmosphere having a dew point of 39°C or higher.

Description

化学強化ガラスの製造方法Method for producing chemically strengthened glass

 本発明は化学強化ガラスの製造方法に関する。 The present invention relates to a method for producing chemically strengthened glass.

 様々なディスプレイ装置のカバーガラスとして化学強化ガラスが用いられている。化学強化ガラスの強度を向上させる手法の一つとして、特許文献1には、硝酸カリウムを含む特定の無機塩に、ナトリウムを含むガラスを接触させることによって、ガラス中のNaと前記無機塩中のKとをイオン交換することで化学強化処理を行い、その後、酸とアルカリによる処理を行う方法が開示されている。特許文献1には、化学強化処理後のガラス表面に対して、研磨やフッ酸等を用いたエッチング処理をせずとも、ガラスの面強度が飛躍的に向上することが記載されている。 Chemically strengthened glass is used as a cover glass for various display devices. As one method for improving the strength of chemically strengthened glass, Patent Document 1 discloses that Na in glass and K in the inorganic salt are brought into contact with a specific inorganic salt containing potassium nitrate. A method is disclosed in which a chemical strengthening treatment is performed by ion-exchange of and then an acid and alkali treatment is performed. Patent Document 1 describes that the surface strength of glass is remarkably improved without subjecting the glass surface after chemical strengthening treatment to etching treatment using polishing or hydrofluoric acid.

国際公開第2015/008763号International Publication No. 2015/008763

 近年、カバーガラス越しに指を使って画面を拡大・縮小する機能が普及している。そのため、カバーガラスには、単なる強度だけではなく、指でのさわり心地という機能が求められている。しかしながら、特許文献1には、指でのさわり心地を改善するためのガラスの製造方法についての開示はない。 In recent years, the function of enlarging / reducing the screen using a finger through the cover glass has become widespread. Therefore, the cover glass is required to have a function of not only a simple strength but also a touch feeling with a finger. However, Patent Document 1 does not disclose a glass manufacturing method for improving the touch feeling with a finger.

 したがって、本発明は上記実情に鑑み、さわり心地の機能を向上するための化学強化ガラスの製造方法を提供することを目的とする。 Therefore, in view of the above circumstances, an object of the present invention is to provide a method for producing chemically tempered glass for improving the function of touch comfort.

 本発明の第一の態様の化学強化ガラスの製造方法は、アルカリイオンを含むガラスを準備する工程と、前記ガラスに含まれる前記アルカリイオンのイオン半径よりも大きい他のアルカリイオンを含み、10wt%水溶液としたときのpHが8以上14以下となる無機塩を準備する工程と、露点温度が39℃以上の雰囲気で、前記ガラスに含まれる前記アルカリイオンと前記無機塩に含まれる前記他のアルカリイオンとをイオン交換する工程とを含むことを特徴とする。 The method for producing chemically strengthened glass according to the first aspect of the present invention includes a step of preparing a glass containing alkali ions, and another alkali ion larger than the ion radius of the alkali ions contained in the glass, and is 10 wt%. A step of preparing an inorganic salt having a pH of 8 or more and 14 or less when an aqueous solution is used, and the alkali ion contained in the glass and the other alkali contained in the inorganic salt in an atmosphere having a dew point temperature of 39 ° C. or more. And a step of ion exchange with ions.

 本発明によれば、ガラスのさわり心地を向上するための化学強化ガラスの製造方法を提供することができる。 According to the present invention, it is possible to provide a method for producing chemically tempered glass for improving the touch feeling of glass.

図1は、本発明に係る化学強化ガラスの製造方法における製造工程を表す模式図である。Drawing 1 is a mimetic diagram showing a manufacturing process in a manufacturing method of chemically strengthened glass concerning the present invention. 図2は、イオン交換する工程における雰囲気を形成するための実験系の模式図である。FIG. 2 is a schematic diagram of an experimental system for forming an atmosphere in an ion exchange process.

 以下、本発明を詳細に説明するが、本発明は以下の実施形態に限定されるものではなく、本発明の要旨を逸脱しない範囲において、任意に変形して実施することができる。また本明細書において数値範囲を示す「~」とは、その前後に記載された数値を下限値及び上限値として含む意味で使用される。 Hereinafter, the present invention will be described in detail. However, the present invention is not limited to the following embodiments, and can be arbitrarily modified without departing from the gist of the present invention. In the present specification, “to” indicating a numerical range is used in the sense of including the numerical values described before and after the numerical value as a lower limit value and an upper limit value.

 本明細書において、「wt%」、「質量%」および「重量%」はそれぞれ同義である。 In the present specification, “wt%”, “mass%”, and “wt%” have the same meaning.

<化学強化ガラスの製造方法>
 本発明に係る化学強化ガラスの製造方法(以下、本発明の方法とも略す)は、
(a)アルカリイオンを含むガラスを準備する工程と、
(b)前記ガラスに含まれる前記アルカリイオンのイオン半径よりも大きい他のアルカリイオンを含み、10wt%水溶液としたときのpHが8以上14以下となる無機塩を準備する工程と、
(c)露点温度が39℃以上の雰囲気で、前記ガラスに含まれる前記アルカリイオンと前記無機塩に含まれる他のアルカリイオンとをイオン交換する工程と、
 を含むことを特徴とする。以下各工程について説明する。
<Method for producing chemically strengthened glass>
The method for producing chemically strengthened glass according to the present invention (hereinafter also abbreviated as the method of the present invention)
(A) preparing a glass containing alkali ions;
(B) preparing an inorganic salt containing other alkali ions larger than the ion radius of the alkali ions contained in the glass and having a pH of 8 or more and 14 or less when a 10 wt% aqueous solution is formed;
(C) ion exchange between the alkali ions contained in the glass and other alkali ions contained in the inorganic salt in an atmosphere having a dew point temperature of 39 ° C. or higher;
It is characterized by including. Each step will be described below.

[(a)アルカリイオンを含むガラスを準備する工程]
 本発明の方法で使用されるガラスはアルカリイオンを含んでいればよく、成形、化学強化処理による強化が可能な組成を有するものである限り、種々の組成のものを使用することができる。中でもナトリウムを含んでいることが好ましく、具体的には、例えば、アルミノシリケートガラス、ソーダライムガラス、ボロシリケートガラス、鉛ガラス、アルカリバリウムガラス、アルミノボロシリケートガラス等が挙げられる。
[(A) Step of preparing glass containing alkali ions]
The glass used in the method of the present invention only needs to contain alkali ions, and various glasses can be used as long as they have a composition that can be strengthened by molding and chemical strengthening treatment. Among them, it is preferable to contain sodium, and specific examples include aluminosilicate glass, soda lime glass, borosilicate glass, lead glass, alkali barium glass, aluminoborosilicate glass, and the like.

 ガラスの製造方法は特に限定されず、所望のガラス原料を連続溶融炉に投入し、ガラス原料を好ましくは1500~1600℃で加熱溶融し、清澄した後、成形装置に供給した上で溶融ガラスを板状に成形し、徐冷することにより製造することができる。 The method for producing the glass is not particularly limited, and a desired glass raw material is charged into a continuous melting furnace, and the glass raw material is heated and melted preferably at 1500 to 1600 ° C., clarified, and then supplied to a molding apparatus. It can be manufactured by forming into a plate shape and slowly cooling.

 なお、ガラスの成形には種々の方法を採用することができる。例えば、ダウンドロー法(例えば、オーバーフローダウンドロー法、スロットダウン法およびリドロー法等)、フロート法、ロールアウト法およびプレス法等の様々な成形方法を採用することができる。中でも、ガラス面の少なくとも一部にクラックが発生しやすく、本発明の効果がより顕著にみられる点で、フロート法が好ましい。 It should be noted that various methods can be employed for forming the glass. For example, various forming methods such as a down draw method (for example, an overflow down draw method, a slot down method and a redraw method), a float method, a roll-out method, and a press method can be employed. Of these, the float method is preferred in that cracks are likely to occur on at least a part of the glass surface, and the effects of the present invention are more prominent.

 ガラスの厚みは、特に制限されるものではないが、化学強化処理を効果的に行うために、通常5mm以下であることが好ましく、3mm以下であることがより好ましく、1mm以下であることがさらに好ましく、0.7mm以下が特に好ましい。 The thickness of the glass is not particularly limited, but is usually preferably 5 mm or less, more preferably 3 mm or less, and even more preferably 1 mm or less for effective chemical strengthening treatment. Preferably, 0.7 mm or less is particularly preferable.

 また、本発明の方法で使用されるガラスの形状は特に限定されない。例えば、均一な板厚を有する平板形状、表面と裏面のうち少なくとも一方に曲面を有する形状および屈曲部等を有する立体的な形状等の様々な形状のガラスを採用することができる。 Further, the shape of the glass used in the method of the present invention is not particularly limited. For example, various shapes of glass such as a flat plate shape having a uniform plate thickness, a shape having a curved surface on at least one of the front surface and the back surface, and a three-dimensional shape having a bent portion can be employed.

 本発明の方法で使用されるガラスの組成としては特に限定されないが、例えば、以下のガラス組成が挙げられる。
(1)酸化物基準のモル%で表示した組成で、SiOを50~80%、Alを1~25%、LiOを0~10%、NaOを0~18%、KOを0~10%、MgOを0~15%、CaOを0~10%およびZrOを0~5%を含むガラス
(2)酸化物基準のモル%で表示した組成が、SiOを50~74%、Alを1~10%、NaOを6~14%、KOを3~11%、MgOを2~15%、CaOを0~6%およびZrOを0~5%含有し、SiOおよびAlの含有量の合計が75%以下、NaOおよびKOの含有量の合計が12~25%、MgOおよびCaOの含有量の合計が7~15%であるガラス
(3)酸化物基準のモル%で表示した組成が、SiOを68~80%、Alを4~10%、NaOを5~15%、KOを0~1%、MgOを4~15%およびZrOを0~1%含有するガラス
(4)酸化物基準のモル%で表示した組成が、SiOを67~75%、Alを0~4%、NaOを7~15%、KOを1~9%、MgOを6~14%およびZrOを0~1.5%含有し、SiOおよびAlの含有量の合計が71~75%、NaOおよびKOの含有量の合計が12~20%であり、CaOを含有する場合その含有量が1%未満であるガラス
(5)酸化物基準の質量%で表示した組成が、SiOを65~75%、Alを0.1~5%、MgOを1~6%、CaOを1~15%含有し、NaO+KOが10~18%であるガラス
(6)酸化物基準の質量%で表示した組成が、SiOを60~72%、Alを1~10%、MgOを5~12%、CaOを0.1~5%、NaOを13~19%、KOを0~5%含有し、RO/(RO+RO)が0.20以上、0.42以下(式中、ROとはアルカリ土類金属酸化物、ROはアルカリ金属酸化物を示す。)であるガラス
(7)酸化物基準のモル%で表示した組成が、SiOを55.5~80%、Alを12~20%、NaOを8~25%、Pを2.5%以上、アルカリ土類金属RO(ROはMgO+CaO+SrO+BaOである)を1%以上含有するガラス
(8)モル%で表示した組成が、SiOを57~76.5%、Alを12~18%、NaOを8~25%、Pを2.5~10%、アルカリ土類金属ROを1%以上含有するガラス
(9)酸化物基準のモル%で表示した組成が、SiOを56~72%、Alを8~20%、Bを3~20%、NaOを8~25%、KOを0~5%、MgOを0~15%、CaOを0~15%、SrOを0~15%、BaOを0~15%およびZrOを0~8%含有するガラス
(10)酸化物基準のモル%で表示した組成で、SiOを50~80%、Alを1~25%、LiOを1~15%、NaOを5~18%、KOを0~10%、MgOを0~15%、CaOを0~10%およびZrOを0~5%を含むガラス
Although it does not specifically limit as a composition of the glass used with the method of this invention, For example, the following glass compositions are mentioned.
(1) Composition expressed as mol% based on oxide, SiO 2 50-50%, Al 2 O 3 1-25%, Li 2 O 0-10%, Na 2 O 0-18% A glass containing 0 to 10% of K 2 O, 0 to 15% of MgO, 0 to 10% of CaO and 0 to 5% of ZrO 2 (2) The composition expressed by mol% on the basis of oxide is SiO 2 2 to 50 to 74%, Al 2 O 3 to 1 to 10%, Na 2 O to 6 to 14%, K 2 O to 3 to 11%, MgO to 2 to 15%, CaO to 0 to 6% and ZrO 2 to 5%, the total content of SiO 2 and Al 2 O 3 is 75% or less, the total content of Na 2 O and K 2 O is 12 to 25%, the content of MgO and CaO the total is 7-15% glass (3) composition viewed in mole percent on the oxide basis is, SiO 2 and 68-8 %, The Al 2 O 3 4 ~ 10% , a Na 2 O 5 ~ 15%, the K 2 O 0 to 1%, glass 4-15% and the ZrO 2 and MgO containing 0 to 1% (4) composition viewed in mole percent on the oxide basis is, the SiO 2 67 ~ 75%, the Al 2 O 3 0 ~ 4% , 7 ~ 15% of Na 2 O, the K 2 O 1 ~ 9%, a MgO 6 to 14% and 0 to 1.5% of ZrO 2 , the total content of SiO 2 and Al 2 O 3 is 71 to 75%, the total content of Na 2 O and K 2 O is 12 to When the CaO content is 20%, the glass content is less than 1%. (5) The composition expressed by mass% based on the oxide is 65 to 75% for SiO 2 and 0.002 for Al 2 O 3 . Gala containing 1-5%, MgO 1-6%, CaO 1-15% and Na 2 O + K 2 O 10-18% (6) The composition expressed by mass% based on the oxide is SiO 2 60-72%, Al 2 O 3 1-10%, MgO 5-12%, CaO 0.1-5%, It contains 13 to 19% Na 2 O and 0 to 5% K 2 O, and RO / (RO + R 2 O) is 0.20 or more and 0.42 or less (wherein RO is an alkaline earth metal oxide) , R 2 O represents an alkali metal oxide.) (7) The composition expressed in mol% based on the oxide is 55.5 to 80% for SiO 2 and 12 to 20% for Al 2 O 3. A composition containing 8 to 25% of Na 2 O, 2.5% or more of P 2 O 5 and glass containing 8% or more of an alkaline earth metal RO (RO is MgO + CaO + SrO + BaO) (8) mol%. the SiO 2 57 ~ 76.5%, an Al 2 O 3 12 ~ 18% , a Na 2 O 8 25%, P 2 O 5 2.5-10%, the composition was displayed in mole percent of the glass (9) oxide basis, containing 1% or more alkaline earth metals RO, the SiO 2 56 ~ 72%, Al 2 O 3 8-20%, B 2 O 3 3-20%, Na 2 O 8-25%, K 2 O 0-5%, MgO 0-15%, CaO 0-15 %, the SrO 2 0 ~ 15%, a BaO 0 ~ 15% and ZrO 2 in a composition that displays in mole percent of glass (10) oxide basis contains 0 to 8% of SiO 2 50 ~ 80%, Al 2 O 3 1-25%, Li 2 O 1-15%, Na 2 O 5-18%, K 2 O 0-10%, MgO 0-15%, CaO 0-10% And glass containing 0-5% of ZrO 2

[(b)前記ガラスに含まれる前記アルカリイオンのイオン半径よりも大きい他のアルカリイオンを含み、10wt%水溶液としたときのpHが8以上14以下となる無機塩を準備する工程]
 本発明の方法で製造される化学強化ガラスは、ガラス表面に、イオン交換された圧縮応力層を有する。イオン交換法では、ガラスの表面をイオン交換し、圧縮応力が残留する表面層を形成させる。具体的には、ガラス転移点以下の温度でイオン交換によりガラス表面のイオン半径が小さなアルカリ金属イオン(Liイオン及び/またはNaイオン)をイオン半径のより大きい他のアルカリイオン(Naイオン及び/またはKイオン)に置換する。これにより、ガラスの表面に圧縮応力が残留し、ガラスの強度が向上する。
[(B) Step of preparing an inorganic salt containing other alkali ions larger than the ionic radius of the alkali ions contained in the glass and having a pH of 8 or more and 14 or less when a 10 wt% aqueous solution is obtained]
The chemically strengthened glass produced by the method of the present invention has an ion-exchanged compressive stress layer on the glass surface. In the ion exchange method, the surface of glass is ion exchanged to form a surface layer in which compressive stress remains. Specifically, alkali metal ions (Li ions and / or Na ions) having a small ion radius on the glass surface are exchanged with other alkali ions (Na ions and / or larger ions) at a temperature below the glass transition point by ion exchange. (K ion). Thereby, compressive stress remains on the surface of the glass, and the strength of the glass is improved.

 本発明の方法においては、ガラスに含まれるアルカリイオンのイオン半径よりも大きい他のアルカリイオンを含む無機塩に、先述したアルカリイオンを含むガラスを接触させてイオン交換をすることにより化学強化処理する。したがって、本発明の方法で用いる無機塩は前記ガラスに含まれる前記アルカリイオンのイオン半径よりも大きい他のアルカリイオンを含む。 In the method of the present invention, chemical strengthening treatment is performed by ion exchange by bringing the glass containing alkali ions into contact with an inorganic salt containing other alkali ions larger than the ion radius of alkali ions contained in the glass. . Therefore, the inorganic salt used in the method of the present invention contains other alkali ions larger than the ionic radius of the alkali ions contained in the glass.

 無機塩は、10wt%水溶液としたときのpHが8以上であり、好ましくは9以上であり、より好ましくは10以上である。また、pHが14以下であり、好ましくは13以下であり、より好ましくは12以下である。無機塩のpHを前記範囲とすることにより、水酸化物イオンによるガラスネットワークの切断が促進されやすく、後述する低密度化による凹凸層の形成が進行しやすくなる。無機塩のpHは25℃においてpHメーターにより測定する。 The inorganic salt has a pH of 8 or more, preferably 9 or more, more preferably 10 or more, when a 10 wt% aqueous solution is used. Moreover, pH is 14 or less, Preferably it is 13 or less, More preferably, it is 12 or less. By setting the pH of the inorganic salt within the above range, the cutting of the glass network by hydroxide ions is easily promoted, and the formation of the uneven layer due to the reduction in density described later is facilitated. The pH of the inorganic salt is measured with a pH meter at 25 ° C.

 無機塩のpHは公知の方法で所望の範囲に調整することができる。無機塩のpHの調整方法としては、具体的には、例えば、ガラスに含まれるアルカリイオンがNaイオンである場合、無機塩は、硝酸カリウム(KNO)を含有する無機塩であって、さらに、KCO、NaCO、KHCO、およびNaHCOからなる群より選ばれる少なくとも一種の塩を添加する等の方法が挙げられる。 The pH of the inorganic salt can be adjusted to a desired range by a known method. As a method for adjusting the pH of the inorganic salt, specifically, for example, when the alkali ion contained in the glass is Na ion, the inorganic salt is an inorganic salt containing potassium nitrate (KNO 3 ), and Examples thereof include a method of adding at least one salt selected from the group consisting of K 2 CO 3 , Na 2 CO 3 , KHCO 3 , and NaHCO 3 .

 例えば、無機塩に硝酸カリウムを含む場合、硝酸カリウムの融点は330℃であり、化学強化を行うガラスの歪点(通常500~600℃)以下に融点を有している。また、上記塩のうち硝酸カリウムを除いた塩(以下、「融剤」と称することもある。)は、Si-O-Si結合に代表されるガラスのネットワークを切断する性質を有する。化学強化処理を行う温度は数百℃と高いので、その温度下でガラスのSi-O間の共有結合は適度に切断され、後述する低密度化による凹凸層の形成が進行しやすくなる。 For example, when potassium nitrate is included in the inorganic salt, the melting point of potassium nitrate is 330 ° C., and the melting point is below the strain point (usually 500 to 600 ° C.) of the glass to be chemically strengthened. Among the above salts, salts excluding potassium nitrate (hereinafter sometimes referred to as “flux”) have a property of cutting a glass network represented by Si—O—Si bonds. Since the temperature at which the chemical strengthening treatment is performed is as high as several hundred degrees Celsius, the covalent bond between Si—O of the glass is appropriately broken at that temperature, and the formation of the uneven layer due to the lowering of density described later tends to proceed.

 なお、共有結合を切断する度合いはガラス組成や用いる塩(融剤)の種類、化学強化処理を行う温度、時間等の化学強化処理条件によっても異なるが、Siから伸びている4本の共有結合のうち、1~2本の結合が切れる程度の条件を選択することが好ましいものと考えられる。 The degree of breaking the covalent bond varies depending on the chemical composition treatment conditions such as the glass composition, the type of salt (flux) used, the temperature and time for the chemical strengthening treatment, but the four covalent bonds extending from Si. Of these, it is considered preferable to select conditions that are sufficient to break one or two bonds.

 無機塩は、硝酸カリウム及び融剤の他に、本発明の効果を阻害しない範囲で、例えば、塩化ナトリウム、塩化カリウム、ホウ酸ナトリウム若しくはホウ酸カリウム等のアルカリ塩化塩またはアルカリホウ酸塩などを含んでもよい。これらは単独で添加しても、複数種を組み合わせて添加してもよい。 In addition to potassium nitrate and flux, the inorganic salt includes, for example, alkali chlorides or alkali borates such as sodium chloride, potassium chloride, sodium borate or potassium borate within a range not inhibiting the effects of the present invention. But you can. These may be added alone or in combination of two or more.

 無機塩中の下式により得られる炭酸アニオン濃度と炭酸水素アニオン濃度との和は4mol%以上が好ましく、6mol%以上がより好ましい。該濃度が4mol%以上であることで、化学強化処理における溶融塩中の水分量を増やし、後述するガラス表面における凹凸層の形成反応を促進できることから好ましい。
  {(炭酸アニオン濃度)+(炭酸水素アニオン濃度)}(mol%)={(無機塩中の炭酸アニオン量)+(無機塩中の炭酸水素アニオン量)}(mol)/(無機塩中の全アニオン量)(mol)×100
The sum of the carbonate anion concentration and the hydrogen carbonate anion concentration obtained by the following formula in the inorganic salt is preferably 4 mol% or more, more preferably 6 mol% or more. This concentration is preferably 4 mol% or more because the amount of water in the molten salt in the chemical strengthening treatment can be increased and the formation reaction of the uneven layer on the glass surface described later can be promoted.
{(Carbonate anion concentration) + (hydrogen carbonate anion concentration)} (mol%) = {(amount of carbonate anion in inorganic salt) + (amount of hydrogen carbonate anion in inorganic salt)} (mol) / (in inorganic salt) Total anion) (mol) x 100

 なお、溶融塩中の炭酸アニオン濃度と炭酸水素アニオン濃度を直接測定することはできないため、溶融塩を一部取り出し、二酸化炭素メータTiN-9004を用いて市販標準液(NaHCO)を純水で希釈して検量線を作成した後、純水で130倍に希釈した試料溶液を測定する。 Since the carbonate anion concentration and the hydrogen carbonate anion concentration in the molten salt cannot be directly measured, a part of the molten salt is taken out, and a commercially available standard solution (NaHCO 3 ) with pure water using a carbon dioxide meter TiN-9004. After preparing a calibration curve by dilution, a sample solution diluted 130 times with pure water is measured.

 このとき、炭酸水素アニオンはすべて炭酸アニオンに変換されることから、測定で検出された炭酸アニオン濃度の値が、炭酸アニオン濃度と炭酸水素アニオン濃度との和に相当する。また、炭酸アニオン濃度と炭酸水素アニオン濃度との和は、飽和炭酸アニオン濃度と飽和炭酸水素アニオン濃度との和以下となる。 At this time, since all the hydrogen carbonate anions are converted into carbonate anions, the value of the carbonate anion concentration detected in the measurement corresponds to the sum of the carbonate anion concentration and the hydrogen carbonate anion concentration. Further, the sum of the carbonate anion concentration and the hydrogen carbonate anion concentration is not more than the sum of the saturated carbonate anion concentration and the saturated bicarbonate anion concentration.

[(c)露点温度が39℃以上の雰囲気で、前記ガラスに含まれる前記アルカリイオンと前記無機塩に含まれる他のアルカリイオンとをイオン交換する工程]
 次に、露点温度が39℃以上の雰囲気で、工程(a)で調製したガラスに含まれる前記アルカリイオンと工程(b)で調製した無機塩に含まれる他のアルカリイオンとをイオン交換して化学強化処理を行う。
[(C) Step of ion-exchange between the alkali ions contained in the glass and other alkali ions contained in the inorganic salt in an atmosphere having a dew point temperature of 39 ° C. or higher]
Next, in an atmosphere having a dew point temperature of 39 ° C. or higher, the alkali ions contained in the glass prepared in step (a) and the other alkali ions contained in the inorganic salt prepared in step (b) are ion-exchanged. Perform chemical strengthening treatment.

 化学強化処理は、ガラスを溶融塩に浸漬し、ガラス中のアルカリイオン(LiイオンまたはNaイオン)を、溶融塩中のイオン半径の大きい他のアルカリイオン(NaイオンまたはKイオン)とイオン交換(置換)することで行われる。このイオン交換によってガラス表面の組成を変化させ、ガラス表面が高密度化した圧縮応力層20を形成することができる[図1(a)~(b)]。このガラス表面の高密度化によって圧縮応力が発生することから、ガラスを強化することができる。 In the chemical strengthening treatment, glass is immersed in a molten salt, and alkali ions (Li ions or Na ions) in the glass are ion-exchanged with other alkali ions (Na ions or K ions) having a large ion radius in the molten salt ( Is performed). By this ion exchange, the composition of the glass surface can be changed to form the compressive stress layer 20 having a high density on the glass surface [FIGS. 1 (a) to 1 (b)]. Since compressive stress is generated by increasing the density of the glass surface, the glass can be strengthened.

 なお実際には、化学強化ガラスの密度は、ガラスの中心に存在する中間層30(バルク)の外縁から圧縮応力層表面に向かって徐々に高密度化してくるため、中間層30と圧縮応力層20との間には、密度が急激に変化する明確な境界はない。ここで中間層とは、ガラス中心部に存在し、圧縮応力層に挟まれる層を表す。この中間層は圧縮応力層とは異なり、イオン交換がされていない層である。 Actually, the density of the chemically strengthened glass gradually increases from the outer edge of the intermediate layer 30 (bulk) existing in the center of the glass toward the surface of the compressive stress layer. There is no clear boundary between 20 and 20 where the density changes rapidly. Here, the intermediate layer is a layer present in the center of the glass and sandwiched between the compressive stress layers. Unlike the compressive stress layer, this intermediate layer is a layer that is not ion-exchanged.

 本発明の方法では、10wt%水溶液としたときのpHが8以上14以下の無機塩を用い、露点温度(以下、単に「露点」と称することがある。)が39℃以上の雰囲気で化学強化処理することにより、溶融塩中の水蒸気量を十分に増加させてガラス表面に凹凸層10を形成することができる[図1(b)~(c)]。ここで、凹凸層10の密度は、ガラス内部の密度よりも低いことから、低密度層ともいう。凹凸層10の厚みは、化学強化処理における溶融塩中の水蒸気量を増やすことにより厚くすることができる。 In the method of the present invention, an inorganic salt having a pH of 8 or more and 14 or less when a 10 wt% aqueous solution is used, and chemical strengthening is performed in an atmosphere having a dew point temperature (hereinafter sometimes simply referred to as “dew point”) of 39 ° C. or more. By performing the treatment, it is possible to sufficiently increase the amount of water vapor in the molten salt to form the uneven layer 10 on the glass surface [FIGS. 1 (b) to (c)]. Here, since the density of the uneven layer 10 is lower than the density inside the glass, it is also referred to as a low density layer. The thickness of the uneven layer 10 can be increased by increasing the amount of water vapor in the molten salt in the chemical strengthening treatment.

 無機塩にガラスを接触させる方法としては、ペースト状の無機塩を塗布する方法、無機塩の水溶液をガラスに噴射する方法、または融点以上に加熱した溶融塩の塩浴にガラスを浸漬させる方法などが挙げられるが、これらの中では、溶融塩に浸漬させる方法が好ましい。 Examples of the method of bringing the glass into contact with the inorganic salt include a method of applying a paste-like inorganic salt, a method of spraying an inorganic salt aqueous solution onto the glass, or a method of immersing the glass in a salt bath of a molten salt heated to a melting point or higher. Among these, the method of immersing in molten salt is preferable.

 溶融塩は公知の工程により製造することができる。例えば、無機塩が硝酸カリウムと融剤を含む溶融塩である場合、硝酸カリウム溶融塩を調製し、次いで該硝酸カリウム溶融塩へ融剤を添加することで得ることができる。また、別の方法として、硝酸カリウムと融剤を混合し、次いで該硝酸カリウムと融剤との混合塩を溶融することで得ることができる。 Molten salt can be produced by a known process. For example, when the inorganic salt is a molten salt containing potassium nitrate and a flux, it can be obtained by preparing a potassium nitrate molten salt and then adding the flux to the potassium nitrate molten salt. As another method, it can be obtained by mixing potassium nitrate and a flux and then melting a mixed salt of the potassium nitrate and the flux.

 本発明の方法で用いる溶融塩は、Na濃度が好ましくは500重量ppm以上であり、より好ましくは1000重量ppm以上である。溶融塩におけるNa濃度が2000重量ppm以上であることで、後述する酸処理工程により、凹凸層が深化しやすくなるためさらに好ましい。Na濃度の上限としては特に制限はなく、所望の表面圧縮応力(CS)が得られるまで許容できる。 The molten salt used in the method of the present invention preferably has a Na concentration of 500 ppm by weight or more, more preferably 1000 ppm by weight or more. It is more preferable that the Na concentration in the molten salt is 2000 ppm by weight or more because the uneven layer is easily deepened by the acid treatment step described later. There is no restriction | limiting in particular as an upper limit of Na density | concentration, It is permissible until a desired surface compressive stress (CS) is obtained.

 なお、化学強化処理を1回以上行なった溶融塩にはガラスから溶出したナトリウムが含まれている。したがって、Na濃度が既に上記範囲内であれば、ガラス由来のナトリウムをそのままNa源として用いてもよいし、Na濃度が満たない場合や、化学強化処理に未使用の溶融塩を用いる場合には、硝酸ナトリウム等の無機ナトリウム塩を添加することにより調製することができる。 Note that the molten salt that has been subjected to the chemical strengthening treatment one or more times contains sodium eluted from the glass. Therefore, if the Na concentration is already within the above range, glass-derived sodium may be used as it is as the Na source, or when the Na concentration is insufficient or when an unused molten salt is used for the chemical strengthening treatment. It can be prepared by adding an inorganic sodium salt such as sodium nitrate.

 本発明における化学強化処理(イオン交換する工程)は、具体的には次の手順で行うことができる。まずガラスを予熱し、先述した溶融塩を、化学強化を行う温度に調整する。次いで予熱したガラスを溶融塩中に所定の時間浸漬したのち、ガラスを溶融塩中から引き上げ、放冷する。なお、ガラスには、化学強化処理の前に、用途に応じた形状加工、例えば、切断、端面加工および穴あけ加工などの機械的加工を行うことが好ましい。 The chemical strengthening treatment (ion exchange step) in the present invention can be specifically performed by the following procedure. First, the glass is preheated, and the above-described molten salt is adjusted to a temperature at which chemical strengthening is performed. Next, the preheated glass is immersed in the molten salt for a predetermined time, and then the glass is pulled up from the molten salt and allowed to cool. In addition, it is preferable to perform shape processing according to a use, for example, mechanical processing, such as a cutting | disconnection, an end surface processing, and a drilling process, before a chemical strengthening process to glass.

 ガラスの予熱温度は、溶融塩に浸漬する温度に依存するが、一般に100℃以上であることが好ましい。化学強化温度は、被強化ガラスの歪点(通常500~600℃)以下が好ましく、より高い圧縮応力層深さを得るためには特に350℃以上が好ましく、処理時間の短縮及び凹凸層形成促進のために400℃以上がより好ましく、430℃以上がさらに好ましい。 The preheating temperature of glass depends on the temperature immersed in the molten salt, but is generally preferably 100 ° C. or higher. The chemical strengthening temperature is preferably not more than the strain point of the glass to be tempered (usually 500 to 600 ° C.), particularly preferably 350 ° C. or more in order to obtain a higher compressive stress layer depth, shortening the processing time and promoting the formation of the uneven layer Therefore, 400 ° C. or higher is more preferable, and 430 ° C. or higher is more preferable.

 ガラスの溶融塩への浸漬時間は1分~10時間が好ましく、5分~8時間がより好ましく、10分~4時間がさらに好ましい。かかる範囲において、強度と圧縮応力層の深さのバランスに優れた化学強化ガラスを得ることができ、好ましい。 The immersion time of the glass in the molten salt is preferably 1 minute to 10 hours, more preferably 5 minutes to 8 hours, and even more preferably 10 minutes to 4 hours. In such a range, a chemically strengthened glass excellent in the balance between strength and depth of the compressive stress layer can be obtained, which is preferable.

 イオン交換する工程は、露点温度が39℃以上の雰囲気で行う。該露点温度は50℃以上が好ましく、60℃以上がより好ましく、70℃以上がさらに好ましく、80℃以上であればよりさらに好ましく、90℃以上であれば特に好ましい。該露点温度を39℃以上とすることにより、化学強化処理における溶融塩中の水蒸気量(水分量)を十分に増加させて、ガラス表面における凹凸層10の形成が促進され、ガラスの指さわり心地を向上することができる。また該露点温度の上限は、イオン交換を行う無機塩(溶融塩)の温度以下とすることが好ましい。 The ion exchange process is performed in an atmosphere with a dew point temperature of 39 ° C or higher. The dew point temperature is preferably 50 ° C. or higher, more preferably 60 ° C. or higher, further preferably 70 ° C. or higher, more preferably 80 ° C. or higher, and particularly preferably 90 ° C. or higher. By setting the dew point temperature to 39 ° C. or higher, the amount of water vapor (moisture amount) in the molten salt in the chemical strengthening treatment is sufficiently increased, the formation of the uneven layer 10 on the glass surface is promoted, and the touch feeling of the glass Can be improved. Further, the upper limit of the dew point temperature is preferably set to be equal to or lower than the temperature of the inorganic salt (molten salt) for performing ion exchange.

 水蒸気量(水分量)の多い溶融塩中で化学強化処理することにより、得られる化学強化ガラスに凹凸層が形成される理由について、次のことが考えられる。溶融塩を形成する炭酸イオンは水と反応すると、下記式に示すように炭酸水素イオンと水酸化物イオンが生成する。 The following may be considered as the reason why the uneven layer is formed on the chemically strengthened glass obtained by performing chemical strengthening treatment in a molten salt having a large amount of water vapor (water content). When carbonate ions forming the molten salt react with water, hydrogen carbonate ions and hydroxide ions are generated as shown in the following formula.

Figure JPOXMLDOC01-appb-C000001
Figure JPOXMLDOC01-appb-C000001

 ここで、溶融塩中の水分量が多いと、上記式における平衡が右に傾き、炭酸水素イオンと水酸化物イオンが多く生成する。水酸化物イオンはガラスネットワークの切断を促進するイオンであることから、より多くの水酸化物イオンが生成することで、ガラス表面の凹凸層の形成が促進されるものと考えられる。 Here, when the amount of water in the molten salt is large, the equilibrium in the above formula is tilted to the right, and a large amount of hydrogen carbonate ions and hydroxide ions are generated. Since hydroxide ions are ions that promote the cutting of the glass network, it is considered that the formation of an uneven layer on the glass surface is promoted by generating more hydroxide ions.

 露点温度は、溶融塩の少なくとも界面近傍における露点温度が前記範囲内であればよく、界面近傍とは、溶融塩の界面から200mm以下の領域の雰囲気を意味する。ヴァイサラDRYCAP(登録商標) DMT346露点変換器によって露点を測定することができる。なお本明細書における露点とは、溶融塩と溶融塩界面近傍の雰囲気との間に平衡が成り立ったとみなした時の値である。 The dew point temperature may be such that the dew point temperature at least near the interface of the molten salt is within the above range, and the vicinity of the interface means an atmosphere in an area of 200 mm or less from the interface of the molten salt. The dew point can be measured with a Vaisala DRYCAP® DMT346 dew point converter. In addition, the dew point in this specification is a value when it is considered that an equilibrium is established between the molten salt and the atmosphere in the vicinity of the molten salt interface.

 イオン交換する工程の前及び/又はイオン交換する工程と同時に、溶融塩及び/又は溶融塩の界面近傍の雰囲気に水蒸気を導入することで、前記露点を達成することができる。すなわち、溶融塩に直接水蒸気そのものや、水蒸気を含む気体をバブリングしてもよく、溶融塩上部の空間に水蒸気や水蒸気を含む気体を導入してもよい。また、水蒸気爆発が起きない範囲で、水(液体)そのものを溶融塩に直接送り込むことも可能である。 The dew point can be achieved by introducing water vapor into the molten salt and / or the atmosphere in the vicinity of the interface of the molten salt before and / or simultaneously with the ion exchange step. That is, water vapor itself or a gas containing water vapor may be bubbled directly into the molten salt, or a gas containing water vapor or water vapor may be introduced into the space above the molten salt. Moreover, it is also possible to send water (liquid) itself directly into the molten salt within a range where no steam explosion occurs.

 水蒸気や水蒸気を含む気体、水(液体)(以後、単に「水蒸気等」と称することがある。)の導入に際し、溶融塩を攪拌してもしなくてもよいが、平衡に達するまでの時間を短縮する点で、攪拌する方が好ましい。 When introducing water vapor or a gas containing water vapor or water (liquid) (hereinafter, simply referred to as “water vapor”), the molten salt may or may not be stirred. Stirring is preferable in terms of shortening.

 水蒸気等を導入してから平衡に達するまでの時間は、導入する気体または液体の量や水蒸気濃度、導入方法等によって異なることから一概に言えないものの、上記雰囲気の露点が安定し、一定となれば平衡に達したものと判断することができる。 The time from the introduction of water vapor, etc. until equilibrium is reached varies depending on the amount of gas or liquid to be introduced, the water vapor concentration, the method of introduction, etc., but it cannot be generally stated, but the dew point of the above atmosphere is stable and constant. Can be judged as having reached equilibrium.

 水蒸気を含む気体は、化学強化処理に影響を及ぼさない気体を用いることができ、例えば図2に示すように、空気、窒素ガス、炭酸ガス等の乾燥した気体Aを加熱した水24中に導入することにより、水蒸気を含んだ湿度の高い気体(水蒸気を含む気体)Bとすることができる。 As the gas containing water vapor, a gas that does not affect the chemical strengthening treatment can be used. For example, as shown in FIG. 2, a dry gas A such as air, nitrogen gas, carbon dioxide gas or the like is introduced into heated water 24. By doing it, it can be set as the gas B (gas containing water vapor | steam) B containing the water vapor | steam with high humidity.

 水蒸気供給源として使用する水24は、配管等のスケール堆積を抑制する点で、イオン交換水等の純水を用いることが好ましい。また、水24は、例えば、水槽25を用いたウォーターバス等により加熱される。 As the water 24 used as a water vapor supply source, it is preferable to use pure water such as ion-exchanged water from the viewpoint of suppressing scale accumulation on piping and the like. The water 24 is heated by, for example, a water bath using a water tank 25.

 水蒸気等の導入方法として、より具体的には、(1)水蒸気供給部から無機塩(溶融塩26)の上部の空間に水蒸気を含む気体Bを導入すること、(2)バブリング部から無機塩(溶融塩26)の中に水蒸気を含む気体Bを導入すること、又は(3)水(液体)を直接無機塩(溶融塩26)に導入すること、等が挙げられる。中でも上記(1)又は(2)によって、該雰囲気を形成することが好ましい。 More specifically, as a method of introducing water vapor or the like, (1) introducing gas B containing water vapor into the space above the inorganic salt (molten salt 26) from the water vapor supply unit, and (2) inorganic salt from the bubbling unit. Examples thereof include introducing gas B containing water vapor into (molten salt 26), or (3) introducing water (liquid) directly into inorganic salt (molten salt 26). Among these, it is preferable to form the atmosphere by the above (1) or (2).

 なお、水蒸気供給部、バブリング部又は水(液体)を導入する導入部は装置に合わせて適宜設ければよく、特に制限されない。 In addition, a water vapor supply unit, a bubbling unit, or an introduction unit for introducing water (liquid) may be appropriately provided according to the apparatus, and is not particularly limited.

 溶融塩の上部の空間に水蒸気を含む気体を導入する場合には、1cm当たりに導入する気体中の水蒸気供給量は0.04mg/分以上が好ましく、0.08mg/分以上がより好ましい。 When a gas containing water vapor is introduced into the space above the molten salt, the amount of water vapor supplied in the gas introduced per 1 cm 3 is preferably 0.04 mg / min or more, and more preferably 0.08 mg / min or more.

 水(液体)を直接溶融塩に導入する場合には、1cm当たりに導入する水の流量は0.04mg/分以上が好ましく、0.08mg/分以上がより好ましい。 When water (liquid) is directly introduced into the molten salt, the flow rate of water introduced per 1 cm 3 is preferably 0.04 mg / min or more, and more preferably 0.08 mg / min or more.

 無機塩の中(溶融塩中)に水蒸気を含む気体を直接バブリングする場合には、1cm当たりに導入する気体中の水蒸気供給量は0.04mg/分以上が好ましく、0.08mg/分以上がより好ましい。 When a gas containing water vapor is directly bubbled in an inorganic salt (in a molten salt), the amount of water vapor supplied in the gas introduced per 1 cm 3 is preferably 0.04 mg / min or more, and 0.08 mg / min or more. Is more preferable.

 凹凸層10の厚みは、水蒸気を導入しない従来のイオン交換する工程では100~200nm程度であるのに対し、本発明の方法においては10wt%水溶液としたときのpHが8以上14以下となる無機塩を用い、露点温度が39℃以上の雰囲気でイオン交換することにより、該厚みを300nm以上にすることができる。 The thickness of the concavo-convex layer 10 is about 100 to 200 nm in the conventional ion exchange process in which water vapor is not introduced, whereas in the method of the present invention, the pH when the aqueous solution is 10 wt% is 8 or more and 14 or less. The thickness can be increased to 300 nm or more by ion exchange in an atmosphere having a dew point temperature of 39 ° C. or higher using a salt.

 凹凸層10は、例えば、後述する酸処理工程およびアルカリ処理工程により除去することができる。凹凸層10の厚みはガラス表面除去量の観点から300nm以上が好ましい。 The uneven layer 10 can be removed by, for example, an acid treatment step and an alkali treatment step described later. The thickness of the uneven layer 10 is preferably 300 nm or more from the viewpoint of the amount of glass surface removal.

 また、ガラス製造工程や化学強化処理工程を含むガラス加工工程において発生するガラス表面のクラックや潜傷の平均深さは約500nmである。したがって、凹凸層10の厚みは、500nm以上がより好ましく、600nm以上がさらに好ましい。 In addition, the average depth of cracks and latent scratches on the glass surface generated in the glass processing process including the glass manufacturing process and the chemical strengthening process is about 500 nm. Therefore, the thickness of the uneven layer 10 is more preferably 500 nm or more, and further preferably 600 nm or more.

 凹凸層の厚みはX線反射率法(X-ray-Reflectometry:XRR)によって測定した周期(Δθ)から求めることができる。 The thickness of the concavo-convex layer can be determined from the period (Δθ) measured by the X-ray reflectivity method (X-ray-Reflectometry: XRR).

 凹凸層の密度はガラス表面除去性の観点から、イオン交換された圧縮応力層よりも深い領域(バルク)の密度に比べて低いことが好ましい。凹凸層の密度はXRRによって測定した臨界角(θc)により求めることができる。なお、簡易的には走査型電子顕微鏡(SEM)でガラスの断面を観察することによって、凹凸層の形成と層の厚みを確認することも可能である。 The density of the uneven layer is preferably lower than the density of the region (bulk) deeper than the ion-exchanged compressive stress layer from the viewpoint of glass surface removability. The density of the uneven layer can be obtained from the critical angle (θc) measured by XRR. In addition, it is also possible to confirm the formation of the concavo-convex layer and the thickness of the layer by simply observing a cross section of the glass with a scanning electron microscope (SEM).

 なお、目的に応じて、凹凸層10を除去する工程を設けてもよい。凹凸層10の厚みは、ガラス表面に存在するクラックや潜傷の平均深さ以上とし、該凹凸層10の一部を除去することにより該クラックや潜傷を除去し、面強度に優れた化学強化ガラスを得ることができる。 In addition, you may provide the process of removing the uneven | corrugated layer 10 according to the objective. The thickness of the concavo-convex layer 10 is set to be equal to or greater than the average depth of cracks and latent scratches existing on the glass surface. Tempered glass can be obtained.

 形成された凹凸層10は、ガラスの表面の一部を除去する工程のうち、後述する酸、または酸・アルカリに接触させる工程により除去してもよい。この場合、ガラス表面のクラックや潜傷の深さがすべて凹凸層の厚みよりも浅ければ、アルカリに接触させる工程でそれらクラック及び潜傷をすべて除去することができる。 The formed concavo-convex layer 10 may be removed by a step of contacting with an acid or an acid / alkali described later in the step of removing a part of the surface of the glass. In this case, if all the cracks and latent scratches on the glass surface are shallower than the thickness of the concavo-convex layer, all the cracks and latent scratches can be removed in the step of contacting with alkali.

 化学強化ガラスにおける強度の低下の原因となるガラス面のクラックや潜傷を除去することにより、化学強化ガラスの面強度をより高いものにすることができる。 The surface strength of the chemically strengthened glass can be increased by removing cracks and latent scratches on the glass surface that cause a decrease in strength in the chemically strengthened glass.

[洗浄する工程]
 本発明の方法では、イオン交換する工程とガラスの表面の一部を除去する工程との間にガラスを洗浄する工程をさらに含むことが好ましい。洗浄する工程では、工水またはイオン交換水等を用いてガラスの洗浄を行う。工水は必要に応じて処理したものを用いる。中でもイオン交換水が好ましい。
[Washing process]
The method of the present invention preferably further includes a step of washing the glass between the step of ion exchange and the step of removing part of the surface of the glass. In the cleaning step, the glass is cleaned using industrial water or ion exchange water. Use the treated water if necessary. Of these, ion-exchanged water is preferred.

 洗浄の条件は用いる洗浄液によっても異なるが、イオン交換水を用いる場合には0~100℃で洗浄することが付着した塩を完全に除去させる点から好ましい。洗浄する方法としては、例えば、イオン交換水等が入っている水槽に化学強化ガラスを浸漬する方法、ガラス表面を流水にさらす方法、およびシャワーにより洗浄液をガラス表面に向けて噴射する方法等、様々な方法が挙げられる。 The washing conditions vary depending on the washing solution used, but when ion-exchanged water is used, washing at 0 to 100 ° C. is preferable from the viewpoint of completely removing the attached salt. Various cleaning methods include, for example, a method of immersing chemically tempered glass in a water tank containing ion-exchanged water, a method of exposing the glass surface to running water, and a method of spraying a cleaning liquid toward the glass surface by a shower. The method is mentioned.

[ガラスの表面の一部を除去する工程]
 本発明の方法は、前記イオン交換する工程によりイオン交換されたガラスの表面の一部を除去する工程をさらに含んでもよい。本発明の方法は、ガラスの表面の一部を除去する工程として、ガラスを酸に接触させる工程(酸処理工程)を含むことが好ましく、酸処理工程の後に、ガラスをアルカリに接触させる工程(アルカリ処理工程)をさらに含んでもよい。
[Step of removing part of the glass surface]
The method of the present invention may further include a step of removing a part of the surface of the glass ion-exchanged by the ion-exchange step. The method of the present invention preferably includes a step of contacting the glass with an acid (acid treatment step) as a step of removing a part of the surface of the glass, and a step of contacting the glass with an alkali after the acid treatment step ( An alkali treatment step) may be further included.

 本発明の方法では、前記イオン交換する工程または前記洗浄する工程の後に、ガラスの表面の一部を除去する工程として、ガラスを酸に接触させる工程を行うことが好ましい。 In the method of the present invention, it is preferable to perform a step of contacting the glass with an acid as a step of removing a part of the surface of the glass after the ion exchange step or the washing step.

(酸処理工程)
 酸処理としては、酸性の溶液中に、化学強化ガラスを浸漬させることによって行い、これにより化学強化ガラス表面のNa及び/又はKをHに置換することができる。すなわち、ガラス表面には圧縮応力層の表層が変質した、具体的には低密度化された、凹凸層をさらに有することとなる。
(Acid treatment process)
The acid treatment is performed by immersing the chemically strengthened glass in an acidic solution, whereby Na and / or K on the surface of the chemically strengthened glass can be replaced with H. In other words, the surface of the glass further has a concavo-convex layer in which the surface layer of the compressive stress layer is altered, specifically, the density is reduced.

 酸処理に用いる溶液は酸性であれば特に制限されずpH7未満であればよく、用いられる酸が弱酸であっても強酸であってもよい。具体的には、塩酸、硝酸、硫酸、リン酸、酢酸、シュウ酸、炭酸またはクエン酸等の酸が好ましい。これらの酸は単独で用いても、複数を組み合わせて用いてもよい。 The solution used for the acid treatment is not particularly limited as long as it is acidic, and may be less than pH 7. The acid used may be a weak acid or a strong acid. Specifically, acids such as hydrochloric acid, nitric acid, sulfuric acid, phosphoric acid, acetic acid, oxalic acid, carbonic acid or citric acid are preferred. These acids may be used alone or in combination.

 酸処理を行う温度は、用いる酸の種類や濃度、時間によっても異なるが、100℃以下で行うことが好ましい。酸処理を行う時間は、用いる酸の種類や濃度、温度によっても異なるものの、10秒~5時間が生産性の点から好ましく、1分~2時間がより好ましい。 The temperature at which the acid treatment is performed varies depending on the type, concentration, and time of the acid used, but is preferably 100 ° C. or less. The time for the acid treatment varies depending on the type, concentration and temperature of the acid used, but is preferably 10 seconds to 5 hours from the viewpoint of productivity, and more preferably 1 minute to 2 hours.

 酸処理を行う溶液の濃度は、用いる酸の種類や時間、温度によって異なるものの、容器腐食の懸念が少ない濃度が好ましく、具体的には0.1重量%~20重量%が好ましい。 The concentration of the solution used for the acid treatment varies depending on the type of acid used, the time, and the temperature, but is preferably a concentration at which there is little concern about container corrosion, and specifically 0.1 to 20% by weight.

(アルカリ処理工程)
 本発明の製造方法では、酸処理工程を経た後、アルカリ処理工程を含んでもよい。酸処理工程の後、アルカリ処理工程の前に、先述した洗浄する工程と同様のガラスを洗浄する工程を経ることがより好ましい。
(Alkali treatment process)
In the production method of the present invention, an alkali treatment step may be included after the acid treatment step. More preferably, after the acid treatment step, before the alkali treatment step, a step of washing the same glass as the step of washing described above is performed.

 アルカリ処理としては、塩基性の溶液中に、化学強化ガラスを浸漬させることによって行い、これにより前記酸処理工程で形成された凹凸層の一部を除去することができる。これにより、ガラスの強度を向上させると共に、所望の指触り感を得ることができる。 Alkali treatment is performed by immersing chemically strengthened glass in a basic solution, whereby a part of the uneven layer formed in the acid treatment step can be removed. Thereby, while improving the intensity | strength of glass, desired touch feeling can be obtained.

 アルカリ処理に用いる溶液は塩基性であれば特に制限されずpH7超であればよく、弱塩基を用いても強塩基を用いてもよい。具体的には、水酸化ナトリウム、水酸化カリウム、炭酸カリウム、炭酸ナトリウム等の塩基が好ましい。これらの塩基は単独で用いても、複数を組み合わせて用いてもよい。 The solution used for the alkali treatment is not particularly limited as long as it is basic, and may have a pH exceeding 7, and a weak base or a strong base may be used. Specifically, bases such as sodium hydroxide, potassium hydroxide, potassium carbonate and sodium carbonate are preferred. These bases may be used alone or in combination.

 アルカリ処理を行う温度は、用いる塩基の種類や濃度、時間によっても異なるが、0~100℃が好ましく、10~80℃がより好ましく、20~60℃が特に好ましい。かかる温度範囲であればガラスが腐食するおそれがなく好ましい。 The temperature at which the alkali treatment is performed varies depending on the type, concentration and time of the base used, but is preferably 0 to 100 ° C, more preferably 10 to 80 ° C, and particularly preferably 20 to 60 ° C. If it is this temperature range, there is no possibility that glass will corrode and it is preferable.

 アルカリ処理を行う時間は、用いる塩基の種類や濃度、温度によっても異なるものの、10秒間~5時間が生産性の点から好ましく、1分間~2時間がより好ましい。 Although the alkali treatment time varies depending on the type, concentration and temperature of the base used, it is preferably 10 seconds to 5 hours from the viewpoint of productivity, and more preferably 1 minute to 2 hours.

 アルカリ処理を行う溶液の濃度は、用いる塩基の種類や時間、温度によって異なるものの、ガラス表面除去性の観点から0.1重量%~20重量%が好ましい。 The concentration of the solution used for the alkali treatment varies depending on the type of base used, the time, and the temperature, but is preferably 0.1% by weight to 20% by weight from the viewpoint of glass surface removability.

 凹凸層10の一部は、上記アルカリ処理により除去される場合もある。この場合、凹凸層が厚いほどガラス表面が除去されやすい。上記アルカリ処理により、Hが侵入した凹凸層の一部が除去され、これにより面強度が向上した化学強化ガラスを得ることができる。 A part of the concavo-convex layer 10 may be removed by the alkali treatment. In this case, the thicker the uneven layer, the easier the glass surface is removed. By the alkali treatment, a part of the concavo-convex layer into which H has penetrated is removed, whereby a chemically strengthened glass with improved surface strength can be obtained.

 特に本発明の方法においては、10wt%水溶液としたときのpHが8以上14以下となる無機塩を用いて露点温度が39℃以上の雰囲気で化学強化処理することにより、ガラス表面に存在していたクラックや潜傷の深さよりも凹凸層10の厚みを深くすることができる。そのため、ガラス表面に存在していたクラックや潜傷を凹凸層と共に除去することができ、ガラスの面強度向上により一層寄与すると考えられる。なお、アルカリ処理の後にも、先と同様の方法で洗浄する工程を経ることが好ましい。 In particular, in the method of the present invention, it is present on the glass surface by chemical strengthening treatment in an atmosphere having a dew point of 39 ° C. or higher using an inorganic salt having a pH of 8 or more and 14 or less when a 10 wt% aqueous solution is used. The thickness of the concavo-convex layer 10 can be made deeper than the depth of cracks and latent scratches. Therefore, it is considered that cracks and latent scratches existing on the glass surface can be removed together with the concavo-convex layer, which contributes further by improving the surface strength of the glass. In addition, it is preferable to pass through the process wash | cleaned by the method similar to the previous after alkali treatment.

<化学強化ガラス>
 本発明の方法によれば、従来の化学強化処理と比べて、凹凸層をより深く形成できることから、該凹凸層を除去した後に得られる化学強化ガラスの表層にはクラックや潜傷がより少ない。そのため、本発明の方法により得られる化学強化ガラスは、非常に高い面強度を有する。
<Chemical tempered glass>
According to the method of the present invention, since the uneven layer can be formed deeper than the conventional chemical strengthening treatment, the surface layer of the chemically strengthened glass obtained after removing the uneven layer has fewer cracks and latent scratches. Therefore, the chemically strengthened glass obtained by the method of the present invention has a very high surface strength.

[圧縮応力層]
 化学強化ガラスの圧縮応力層の圧縮応力値および圧縮応力層の深さは、EPMA(electron probe micro analyzer)または表面応力計(例えば、折原製作所製FSM-6000)等を用いて測定することができる。
[Compressive stress layer]
The compressive stress value of the compressive stress layer and the depth of the compressive stress layer of the chemically tempered glass can be measured using an EPMA (electron probe micro analyzer) or a surface stress meter (for example, FSM-6000 manufactured by Orihara Seisakusho). .

[ガラス表面(凹凸層)の除去量]
 ガラスの表面の一部を除去する工程後のガラス表面(凹凸層)の除去量(厚み)は、薬液処理前後の重量を分析用電子天秤により測定し、次の式を用いて厚み換算することにより求めることができる。
 (片面あたりの除去量厚み)=[(ガラスの表面の一部を除去する工程前重量)-(ガラスの表面の一部を除去する工程後重量)]/(ガラス比重)/処理面積/2
 このとき、ガラス比重を2.50(g/cm)として計算する。
[Removal amount of glass surface (uneven layer)]
The removal amount (thickness) of the glass surface (concave layer) after the step of removing a part of the glass surface is to measure the weight before and after the chemical treatment with an analytical electronic balance and convert the thickness using the following formula: It can ask for.
(Removed thickness per side) = [(weight before removing part of glass surface) − (weight after removing part of glass surface)] / (glass specific gravity) / treated area / 2
At this time, the glass specific gravity is calculated as 2.50 (g / cm 3 ).

 以下に実施例を挙げ、本発明を具体的に説明するが、本発明はこれらに限定されない。 Hereinafter, the present invention will be specifically described with reference to examples, but the present invention is not limited thereto.

<評価方法>
 本実施例における各種評価は以下に示す分析方法により行った。
<Evaluation method>
Various evaluations in this example were performed by the following analysis methods.

(ガラスの評価:表面応力)
 ガラスの表面圧縮応力値(CS、単位はMPa)および圧縮応力層の深さ(DOL、単位はμm)は折原製作所社製表面応力計(FSM-6000)を用いて測定した。
(Evaluation of glass: surface stress)
The surface compressive stress value (CS, unit: MPa) of glass and the depth (DOL, unit: μm) of the compressive stress layer were measured using a surface stress meter (FSM-6000) manufactured by Orihara Seisakusho.

(指さわり心地)
 洗浄後のガラス基板を3名で触診した。3名ともさわり心地が良いと感じたものを○、それ以外を×とした。
(Fingering comfort)
The glass substrate after washing was palpated by three people. All three were touched and felt good, and the others were marked X.

(除去量)
 ガラスの除去量厚みは、薬液処理(酸処理およびアルカリ処理)前後の重量を分析用電子天秤(HR-202i、AND社製)により測定し、次の式を用いて厚み換算することにより求めた。
 (片面あたりの除去量厚み)=[(処理前重量)-(処理後重量)]/(ガラス比重)/処理面積/2
 このとき、ガラス比重を2.50(g/cm)として計算した。
(Removal amount)
The glass removal amount thickness was determined by measuring the weight before and after chemical treatment (acid treatment and alkali treatment) with an analytical electronic balance (HR-202i, manufactured by AND) and converting the thickness using the following formula. .
(Removed thickness per side) = [(weight before treatment) − (weight after treatment)] / (glass specific gravity) / treated area / 2
At this time, the glass specific gravity was calculated as 2.50 (g / cm 3 ).

<実施例1~5>
(イオン交換する工程)
 ステンレススチール(SUS)製のポットに硝酸カリウム、炭酸カリウムおよび硝酸ナトリウムを加え、マントルヒーターで450℃まで加熱して表1に示す組成の溶融塩を調製した。10wt%水溶液としたときの無機塩のpH(10wt%水溶液のpH)は、表1に示す通りであった。溶融塩の界面近傍の雰囲気中に95℃に加熱した水中に導入した空気を流すことにより、溶融塩中に水蒸気を含ませた。
<Examples 1 to 5>
(Ion-exchange process)
Potassium nitrate, potassium carbonate and sodium nitrate were added to a stainless steel (SUS) pot and heated to 450 ° C. with a mantle heater to prepare a molten salt having the composition shown in Table 1. Table 1 shows the pH of the inorganic salt (pH of the 10 wt% aqueous solution) when the 10 wt% aqueous solution was used. Water vapor was included in the molten salt by flowing air introduced into water heated to 95 ° C. in an atmosphere near the interface of the molten salt.

 実験系を図1に示す。乾燥した気体Aとして空気を用い、該空気を水槽25によって95℃に加熱された水24中に該空気を通すことで加湿し、加湿された水蒸気を含む気体(空気)Bとした。この水蒸気を含む気体Bをリボンヒーターで加熱された経路を通して化学強化処理を行う槽の無機塩(溶融塩)26の上部の空間に導入することで、イオン交換する工程における露点の制御を行った。1cm当たりの水蒸気供給量および溶融塩の界面近傍の各露点は表1に示す通りであった。 The experimental system is shown in FIG. Air was used as the dried gas A, and the air was humidified by passing the air through water 24 heated to 95 ° C. by a water tank 25 to obtain humidified gas (air) B containing water vapor. By introducing this gas B containing water vapor into the space above the inorganic salt (molten salt) 26 of the tank that performs the chemical strengthening treatment through the route heated by the ribbon heater, the dew point was controlled in the ion exchange process. . The amount of water vapor supplied per cm 3 and the dew points near the interface of the molten salt are as shown in Table 1.

 下記に示す組成の50mm×50mm×0.7mmのガラス板を用意し、350~400℃に予熱した後、表1に示す条件により溶融塩に浸漬してイオン交換処理(化学強化処理)した後、室温付近まで冷却することにより化学強化処理を行った。得られた化学強化ガラスは水洗い後、実施例1および2については、エアブローにより乾燥して化学強化ガラスを得た。また、実施例3~5については、得られた化学強化ガラスを水洗い後、下記の酸処理工程およびアルカリ処理工程に供した。
 ガラスA組成(酸化物基準のモル%表示):SiO 68.74%、Al 2.96%、NaO 14.20%、KO 0.15%、MgO 6.16%、CaO 7.75%
 ガラスB組成(酸化物基準のモル%表示):SiO 64.4%、Al 10.5%、NaO 16.0%、KO 0.6%、MgO 8.3%、ZrO 0.2%
 ガラスC組成(酸化物基準のモル%表示):SiO 67.0%、Al 13.0%、NaO 14.0%、B 4.0%、KO<1.0%、MgO 2.0%、CaO<1.0%
After preparing a glass plate of 50 mm × 50 mm × 0.7 mm having the composition shown below, preheating to 350 to 400 ° C., and then immersing in molten salt under the conditions shown in Table 1 and performing ion exchange treatment (chemical strengthening treatment) The chemical strengthening treatment was performed by cooling to near room temperature. The obtained chemically strengthened glass was washed with water, and Examples 1 and 2 were dried by air blow to obtain chemically strengthened glass. In Examples 3 to 5, the chemically strengthened glass obtained was washed with water and then subjected to the following acid treatment step and alkali treatment step.
Glass A composition (expressed as mol% based on oxide): SiO 2 68.74%, Al 2 O 3 2.96%, Na 2 O 14.20%, K 2 O 0.15%, MgO 6.16% , CaO 7.75%
Glass B composition (expressed as mol% based on oxide): SiO 2 64.4%, Al 2 O 3 10.5%, Na 2 O 16.0%, K 2 O 0.6%, MgO 8.3% , ZrO 2 0.2%
Glass C composition (mole% based on oxide): SiO 2 67.0%, Al 2 O 3 13.0%, Na 2 O 14.0%, B 2 O 3 4.0%, K 2 O < 1.0%, MgO 2.0%, CaO <1.0%

(酸処理工程)
 6.0重量%の硝酸[硝酸1.38(関東化学社製)をイオン交換水で希釈]をビーカーに用意し、ウォーターバスを用いて表1に示す温度に温度調整した。表1に示す条件にて、前記イオン交換処理する工程で得られたガラスを調製した硝酸中に浸漬して酸処理を行った。その後該ガラスを水洗いし、アルカリ処理工程に供した。
(Acid treatment process)
6.0% by weight of nitric acid [nitric acid 1.38 (manufactured by Kanto Chemical Co., Ltd.) diluted with ion-exchanged water] was prepared in a beaker, and the temperature was adjusted to the temperature shown in Table 1 using a water bath. Under the conditions shown in Table 1, acid treatment was performed by immersing the glass obtained in the ion exchange treatment step in prepared nitric acid. Thereafter, the glass was washed with water and subjected to an alkali treatment step.

(アルカリ処理工程)
 4.0重量%の水酸化ナトリウム水溶液[48%水酸化ナトリウム溶液(関東化学社製)をイオン交換水で希釈]をビーカーに用意し、ウォーターバスを用いて表1に示す温度に温度調整した。酸処理工程の後に洗浄したガラスを、調製した水酸化ナトリウム水溶液中に浸漬し、アルカリ処理を行った。その後該ガラスを水洗いしてガラス表面のアルカリを洗浄した。その後エアブローにより乾燥した。
(Alkali treatment process)
A 4.0% by weight sodium hydroxide aqueous solution [48% sodium hydroxide solution (manufactured by Kanto Chemical Co., Ltd.) diluted with ion-exchanged water] was prepared in a beaker, and the temperature was adjusted to the temperature shown in Table 1 using a water bath. . The glass washed after the acid treatment step was immersed in the prepared aqueous sodium hydroxide solution and subjected to alkali treatment. Then, the glass was washed with water to wash the alkali on the glass surface. Thereafter, it was dried by air blow.

<比較例1、3および5>
 化学強化炉上部の露点を制御しなかったこと以外は、それぞれ実施例1、4および5と同様にイオン交換処理する工程を行い、化学強化ガラスを得た。このとき、10wt%水溶液のpH、1cm当たりの水蒸気供給量および溶融塩の界面近傍の各露点は表1に示す通りであった。イオン交換処理する工程後、比較例5については、得られた化学強化ガラスを水洗い後、実施例5と同様に酸処理工程およびアルカリ処理工程を行った。
<Comparative Examples 1, 3, and 5>
Except that the dew point at the upper part of the chemical tempering furnace was not controlled, a step of ion exchange treatment was performed in the same manner as in Examples 1, 4 and 5, respectively, to obtain chemically tempered glass. At this time, the pH of the 10 wt% aqueous solution, the amount of water vapor supplied per cm 3 and the dew points near the interface of the molten salt were as shown in Table 1. After the ion exchange treatment step, in Comparative Example 5, the obtained chemically strengthened glass was washed with water, and then the acid treatment step and the alkali treatment step were performed in the same manner as in Example 5.

<比較例2、4および6>
 イオン交換する工程における溶融塩に炭酸カリウムを加えず、ナトリウムの含有量を表1に示す通りとした。10wt%水溶液のpHは、1cm当たりの水蒸気供給量および溶融塩の界面近傍の各露点は表1に示す通りであった。50mm×50mm×0.7mmのガラス組成A、B、Cの板を用意し、350~400℃に予熱した後、表1に示す条件により溶融塩に浸漬してイオン交換処理(化学強化処理)した後、室温付近まで冷却することにより化学強化処理を行った。得られた化学強化ガラスは水洗い後、エアブローにより乾燥して、比較例2、4および6の化学強化ガラスを得た。
<Comparative Examples 2, 4 and 6>
Table 1 shows the sodium content without adding potassium carbonate to the molten salt in the ion exchange step. The pH of the 10 wt% aqueous solution was as shown in Table 1 in terms of the amount of water vapor supplied per cm 3 and the dew points near the molten salt interface. Prepare 50mm x 50mm x 0.7mm glass composition A, B, and C plates, preheat them to 350-400 ° C, then immerse them in molten salt under the conditions shown in Table 1 to perform ion exchange treatment (chemical strengthening treatment) Then, chemical strengthening treatment was performed by cooling to near room temperature. The obtained chemically tempered glass was washed with water and then dried by air blow to obtain chemically tempered glasses of Comparative Examples 2, 4, and 6.

 上記で得られた化学強化ガラスについて各種評価を行なった。ガラスの処理条件及び評価結果を表1に示す。 Various evaluations were performed on the chemically strengthened glass obtained above. Table 1 shows the processing conditions and evaluation results of the glass.

Figure JPOXMLDOC01-appb-T000002
Figure JPOXMLDOC01-appb-T000002

 表1に示すように、実施例1~5の化学強化ガラスは、指さわり心地がよいことがわかった。一方、イオン交換する工程における露点を39℃以上に制御しなかった比較例1、3および5の化学強化ガラスは指さわり心地が悪かった。また、イオン交換する工程に用いる無機塩について、10wt%水溶液としたときのpHが8未満である比較例2、4および6の化学強化ガラスは指さわり心地が悪かった。 As shown in Table 1, it was found that the chemically tempered glasses of Examples 1 to 5 had good finger touch comfort. On the other hand, the chemically tempered glasses of Comparative Examples 1, 3, and 5 in which the dew point in the ion exchange process was not controlled to 39 ° C. or higher were uncomfortable to touch. In addition, regarding the inorganic salt used in the ion exchange step, the chemically tempered glasses of Comparative Examples 2, 4 and 6 having a pH of less than 8 when made into a 10 wt% aqueous solution were uncomfortable to touch.

 これらの結果から、イオン交換する工程に用いる無機塩の10wt%水溶液としたときのpHを8以上14以下とし、イオン交換する工程における露点を39℃以上に制御することにより、指さわり心地のよい化学強化ガラスが得られることがわかった。 From these results, the pH when the 10 wt% aqueous solution of the inorganic salt used in the ion exchange step is 8 or more and 14 or less, and the dew point in the ion exchange step is controlled to 39 ° C. or more, so that it is comfortable to touch. It was found that chemically strengthened glass was obtained.

 本発明を特定の態様を参照して詳細に説明したが、本発明の精神と範囲を離れることなく様々な変更および修正が可能であることは、当業者にとって明らかである。なお、本出願は、2016年9月2日付けで出願された日本特許出願(特願2016-172069)に基づいており、その全体が引用により援用される。また、ここに引用されるすべての参照は全体として取り込まれる。 Although the present invention has been described in detail with reference to specific embodiments, it will be apparent to those skilled in the art that various changes and modifications can be made without departing from the spirit and scope of the invention. This application is based on a Japanese patent application filed on September 2, 2016 (Japanese Patent Application No. 2016-172069), which is incorporated by reference in its entirety. Also, all references cited herein are incorporated as a whole.

 本発明の化学強化ガラスの製造方法によれば、化学強化後に研磨やフッ酸等を用いたエッチング処理をせずに非常に指触り感の良い化学強化ガラスを得ることができる。すなわち、フッ酸等によるエッチング処理に伴う潜傷の拡大による外観不良や、研磨に伴う研磨傷のない、指触り感に優れた化学強化ガラスを得ることができる。 According to the method for producing chemically tempered glass of the present invention, chemically tempered glass having a very good touch feeling can be obtained without chemical etching and etching treatment using polishing or hydrofluoric acid. That is, it is possible to obtain a chemically strengthened glass excellent in touch feeling without appearance defects due to expansion of latent scratches accompanying etching treatment with hydrofluoric acid or the like, and polishing scratches accompanying polishing.

 本発明の化学強化ガラスの製造方法は、あらゆるガラスに適用可能であり汎用性が高い。そして溶液への浸漬により処理を進めることができるため、様々なガラス形状や大面積のガラスに対応しやすい等の点で効率的である。さらに、フッ酸等を用いたエッチング処理に比べ、安全性が高くまた低コストである。 The method for producing chemically strengthened glass of the present invention can be applied to any glass and has high versatility. And since a process can be advanced by immersion in a solution, it is efficient at the point of being easy to respond | correspond to various glass shapes and large area glass. Further, the safety is high and the cost is low as compared with the etching process using hydrofluoric acid or the like.

10   凹凸層
20   圧縮応力層
30   中間層
24   水
25   水槽
26   溶融塩
10 Concavity and convexity layer 20 Compressive stress layer 30 Intermediate layer 24 Water 25 Water tank 26 Molten salt

Claims (9)

 アルカリイオンを含むガラスを準備する工程と、
 前記ガラスに含まれる前記アルカリイオンのイオン半径よりも大きい他のアルカリイオンを含み、10wt%水溶液としたときのpHが8以上14以下となる無機塩を準備する工程と、
 露点温度が39℃以上の雰囲気で、前記ガラスに含まれる前記アルカリイオンと前記無機塩に含まれる前記他のアルカリイオンとをイオン交換する工程とを含む化学強化ガラスの製造方法。
Preparing a glass containing alkali ions;
Preparing an inorganic salt containing other alkali ions larger than the ion radius of the alkali ions contained in the glass and having a pH of 8 or more and 14 or less when a 10 wt% aqueous solution is formed;
A method for producing chemically tempered glass, comprising a step of ion-exchanging the alkali ions contained in the glass and the other alkali ions contained in the inorganic salt in an atmosphere having a dew point temperature of 39 ° C. or higher.
 前記イオン交換する工程における雰囲気は、水蒸気供給部から前記無機塩の上部の空間に水蒸気を含む気体が導入されることで形成され、前記水蒸気を含む気体の導入量は、1cmあたりの水蒸気供給量が0.04mg/分以上である請求項1に記載の化学強化ガラスの製造方法。 The atmosphere in the ion exchange step is formed by introducing a gas containing water vapor from the water vapor supply unit into the space above the inorganic salt, and the amount of the gas containing water vapor is the water vapor supply per 1 cm 3. The method for producing chemically strengthened glass according to claim 1, wherein the amount is 0.04 mg / min or more.  前記イオン交換する工程における雰囲気は、バブリング部から前記無機塩の中に水蒸気を含む気体が導入されることで形成され、前記水蒸気を含む気体の導入量は、1cmあたりの水蒸気供給量が0.04mg/分以上である請求項1に記載の化学強化ガラスの製造方法。 The atmosphere in the ion exchange step is formed by introducing a gas containing water vapor into the inorganic salt from a bubbling part, and the amount of the gas containing water vapor is 0 for the water supply rate per 1 cm 3. The method for producing chemically tempered glass according to claim 1, which is 0.04 mg / min or more.  前記イオン交換をされた前記ガラスの表面の一部を除去する工程をさらに含む請求項1~3のいずれか1項に記載の化学強化ガラスの製造方法。 The method for producing chemically strengthened glass according to any one of claims 1 to 3, further comprising a step of removing a part of the surface of the glass subjected to the ion exchange.  前記ガラスの表面の一部を除去する工程は、前記ガラスを酸に接触させる工程を含む請求項1~4のいずれか1項に記載の化学強化ガラスの製造方法。 The method for producing chemically tempered glass according to any one of claims 1 to 4, wherein the step of removing a part of the surface of the glass includes a step of bringing the glass into contact with an acid.  前記ガラスの表面の一部を除去する工程は、前記酸に接触させる工程の後にガラスをアルカリに接触させる工程をさらに含む請求項5に記載の化学強化ガラスの製造方法。 6. The method for producing chemically strengthened glass according to claim 5, wherein the step of removing a part of the surface of the glass further includes a step of bringing the glass into contact with an alkali after the step of bringing into contact with the acid.  前記酸に接触させる工程と前記アルカリに接触させる工程との間に、前記ガラスを洗浄する工程、をさらに含む請求項6に記載の化学強化ガラスの製造方法。 The method for producing chemically tempered glass according to claim 6, further comprising a step of washing the glass between the step of contacting with the acid and the step of contacting with the alkali.  前記イオン交換する工程と前記ガラスの表面の一部を除去する工程との間に、前記ガラスを洗浄する工程、をさらに含む請求項1~7のいずれか1項に記載の化学強化ガラスの製造方法。 The production of chemically strengthened glass according to any one of claims 1 to 7, further comprising a step of washing the glass between the step of ion exchange and the step of removing a part of the surface of the glass. Method.  前記アルカリに接触させる工程の後に、前記ガラスを洗浄する工程、をさらに含む請求項6~8のいずれか1項に記載の化学強化ガラスの製造方法。 The method for producing chemically tempered glass according to any one of claims 6 to 8, further comprising a step of washing the glass after the step of contacting with the alkali.
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