TW200906755A - Method for producing alkali-free glass - Google Patents

Method for producing alkali-free glass Download PDF

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TW200906755A
TW200906755A TW097113728A TW97113728A TW200906755A TW 200906755 A TW200906755 A TW 200906755A TW 097113728 A TW097113728 A TW 097113728A TW 97113728 A TW97113728 A TW 97113728A TW 200906755 A TW200906755 A TW 200906755A
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Taiwan
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mass
glass
alkali
free glass
earth metal
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TW097113728A
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Chinese (zh)
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TWI401228B (en
Inventor
Mineko Yamamoto
Yasuo Hayashi
Hideki Kushitani
Tomoyuki Tsujimura
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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
    • C03C3/00Glass compositions
    • C03C3/04Glass compositions containing silica
    • C03C3/076Glass compositions containing silica with 40% to 90% silica, by weight
    • C03C3/089Glass compositions containing silica with 40% to 90% silica, by weight containing boron
    • C03C3/091Glass compositions containing silica with 40% to 90% silica, by weight containing boron containing aluminium
    • 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
    • C03C1/00Ingredients generally applicable to manufacture of glasses, glazes, or vitreous enamels
    • 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

Abstract

Disclosed is a method for producing a highly uniform and highly flat alkali-free glass which has only a few bubbles therein. Specifically disclosed is a method for producing an alkali-free glass, wherein a glass raw material containing a silicon source, an alkaline earth metal source and a boron source is melted and molded. This method for producing an alkali-free glass is characterized in that a material containing 15-100% by mole (in terms of MO, and hereinafter M represents an alkaline earth metal element) of a hydroxide of an alkaline earth metal relative to 100% by mole (in terms of MO) of the alkaline earth metal source is used as the alkaline earth metal source.

Description

200906755 九、發明說明 【發明所屬之技術領域】 本發明係有關無鹼玻璃之製造方法。 【先前技術】 液晶顯示裝置等之顯示器用之玻璃基板被要求實質上 不含有鹼金屬,因此該玻璃基板係使用無鹼玻璃。該玻璃 基板被要求耐藥品性、耐久性高、玻璃中氣泡較少、均質 性高、平坦度高。 但是無鹼玻璃之玻璃原料實質上不含有驗金屬化合物 ,因此該玻璃原料不易熔融。因此,玻璃原料之主成分的 砂砂必須使用粒徑較小者。 欲將溶解性、耐藥品性及耐久性賦予無鹼玻璃時,其 組成可含有B203。B2〇3之原料從價廉、取得容易的觀點 ,可使用原硼酸(有時僅稱爲硼酸)。 但是使用含有原硼酸的玻璃原料時,有時產生以下的 問題。 (1 )原硼酸之存在下,粒徑較小之矽砂容易凝集, 投入熔融窯之玻璃原料的投入量容易不穩定。因此,熔融 窯内之熔融玻璃之溫度不穩定,或溶融玻璃之循環·滯留 時間不穩定。結果’玻璃原料之熔融不均勻,或熔融玻璃 之組成不均勻。 (2 )玻璃原料含有鹼土金屬化合物時,溶解窯之玻 璃原料投入口有熔融之原硼酸與鹼土金屬化合物凝集,容 -5- 200906755 易產生團塊。原硼酸及鹼土金屬化合物係促進矽砂之熔融 的成分,因此產生團塊時,熔融窯内之玻璃原料之熔融不 均,或熔融玻璃之組成不均。 產生(1 )或(2 )的問題時,熔融玻璃之均質性變差 ,因此成形之無鹼玻璃之均質性、平坦度降低。又因循環 •滯留時間不穩定,因此以清澄劑由熔融窯内之熔融玻璃 中去除氣泡之前,熔融玻璃之一部份自熔融窯流出。玻璃 原料之熔融不均勻,因此對於較慢熔融之矽砂之清澄劑的 效果不足,無法充分去除熔融玻璃中之氣泡。 爲了提高無鹼玻璃之均質性,提案控制鹼土金屬化合 物(碳酸緦及白雲石)之粒徑的玻璃原料(專例文獻1 ) 。但是專例文獻1之玻璃原料完全未考慮較慢熔融之矽砂 。矽砂之熔融較慢時,未熔融狀態之矽砂會被玻璃融液中 所產生之氣泡捕捉,聚集於玻璃融液之表層附近,因此玻 璃融液之表層與其外之部分之Si〇2成分之組成比產生差 異,玻璃之均質性可能降低。 [專例文獻1]特開2003 -4064 1號公報 【發明內容】 [發明欲解決的課題] 本發明係提供可得到玻璃中氣泡少,且均質性及平坦 度優之無鹼玻璃的製造方法。 [解決課題的手段] -6- 200906755 爲了達成上述目的’本發明採用以下的構成。 本發明之無鹼玻璃之製造方法,其係將含有矽源、鹼 土金屬源及硼源之玻璃原料熔融、成形之無鹼玻璃的製造 方法,其特徵係前述鹼土金屬源爲使用相對於鹼土金屬源 1 0 0莫耳% ( Μ 0換算,但是Μ係鹼土金屬元素,以下相 同),含有鹼土金屬之氫氧化物15〜100莫耳% ( ΜΟ換 算)者。 作爲鹼土金屬源之前述鹼土金屬較佳爲Mg、Ca、Sr 及B a中之任1種或2種以上的元素。 前述硼源較佳爲使用在硼源1〇〇質量% (b2o3換算) 中含有無水硼酸1 〇〜1 0 0質量% ( B 2 Ο 3換算)者。 前述玻璃原料較佳爲使用以氧化物基準之質量百分比 表示,具有下述組成(1 )之成爲無鹼玻璃的玻璃原料, 特佳爲具有下述組成(2 )或(3 )之成爲無鹼玻璃的玻璃 原料。200906755 IX. Description of the Invention [Technical Field of the Invention] The present invention relates to a method for producing an alkali-free glass. [Prior Art] A glass substrate for a display such as a liquid crystal display device is required to have substantially no alkali metal. Therefore, the glass substrate is made of an alkali-free glass. The glass substrate is required to have high chemical resistance, high durability, less bubbles in the glass, high homogeneity, and high flatness. However, the glass raw material of the alkali-free glass does not substantially contain the metal-detecting compound, so the glass raw material is not easily melted. Therefore, the sand of the main component of the glass raw material must use the smaller particle size. When the solubility, chemical resistance, and durability are to be imparted to the alkali-free glass, the composition may contain B203. The raw material of B2〇3 can be used from the viewpoint of being inexpensive and easy to obtain, and orthoboric acid (sometimes called only boric acid) can be used. However, when a glass raw material containing orthoboric acid is used, the following problems may occur. (1) In the presence of orthoboric acid, the cerium sand having a small particle size tends to aggregate, and the amount of the glass raw material to be fed into the melting kiln is likely to be unstable. Therefore, the temperature of the molten glass in the melting kiln is unstable, or the cycle and residence time of the molten glass are unstable. As a result, the melting of the glass raw material was uneven, or the composition of the molten glass was uneven. (2) When the glass raw material contains an alkaline earth metal compound, the raw material of the glass raw material in the dissolution kiln is melted and the ortho-boric acid and the alkaline earth metal compound are aggregated, and the mixture is prone to agglomerate -5-200906755. The orthoboric acid and the alkaline earth metal compound promote the melting of the cerium sand. Therefore, when agglomerates are generated, the glass raw materials in the melting kiln are not uniformly melted, or the composition of the molten glass is uneven. When the problem of (1) or (2) occurs, the homogeneity of the molten glass is deteriorated, so that the homogeneity and flatness of the formed alkali-free glass are lowered. Further, due to the cycle • the residence time is unstable, a part of the molten glass flows out of the melting kiln before the bubbles are removed from the molten glass in the melting kiln by the clearing agent. Since the melting of the glass raw material is not uniform, the effect of the clearing agent for the slow-melting molten sand is insufficient, and the bubbles in the molten glass cannot be sufficiently removed. In order to improve the homogeneity of the alkali-free glass, it is proposed to control the glass raw material of the particle size of the alkaline earth metal compound (cerium carbonate and dolomite) (Special Document 1). However, the glass raw material of the special document 1 does not consider the slower molten sand at all. When the melting of the strontium sand is slow, the unmelted strontium sand is trapped by the bubbles generated in the glass melt and gathers near the surface layer of the glass melt, so the surface layer of the glass melt and the Si〇2 component of the outer portion thereof The composition ratio is different, and the homogeneity of the glass may be lowered. [Problem to be Solved by the Invention] [Technical Problem] The present invention provides a method for producing an alkali-free glass which has few bubbles in glass and is excellent in homogeneity and flatness. . [Means for Solving the Problem] -6-200906755 In order to achieve the above object, the present invention adopts the following configuration. The method for producing an alkali-free glass according to the present invention is a method for producing an alkali-free glass obtained by melting and molding a glass raw material containing a source of cerium, an alkaline earth metal, and a boron source, characterized in that the alkaline earth metal source is used relative to an alkaline earth metal. Source 1 0 0 摩尔% ( Μ 0 conversion, but Μ alkaline earth metal elements, the same below), containing alkaline earth metal hydroxide 15 to 100 mol % (ΜΟ conversion). The alkaline earth metal as the source of the alkaline earth metal is preferably one or two or more elements selected from the group consisting of Mg, Ca, Sr and Ba. The boron source is preferably used in an amount of 1% by mass (in terms of b2o3) of the boron source, and 1 to 30% by mass of anhydrous boric acid (in terms of B 2 Ο 3 ). The glass raw material is preferably a glass raw material having an alkali-free glass having the following composition (1), and particularly preferably having the following composition (2) or (3) to be alkali-free. Glass raw material for glass.

Si〇2: 50 〜66質量%,ΑΙ2〇3: 1〇·5〜22 質量 %’ B2〇3 :5〜12質量%’ Mg〇: 〇〜8質量%,CaO: 〇〜14.5質量 °/〇’ 81'0:0〜24質量。/。,;^0:0〜13.5質量%’ \^0 + €&0 + 81*0 + 3&0:9〜29.5質量°/。...(1)Si〇2: 50 to 66% by mass, ΑΙ2〇3: 1〇·5~22% by mass 'B2〇3: 5 to 12% by mass' Mg〇: 〇~8 mass%, CaO: 〇~14.5 mass °/ 〇' 81'0: 0~24 quality. /. , ^0: 0~13.5 mass%' \^0 + €&0 + 81*0 + 3&0:9~29.5 mass °/. ...(1)

Si02: 58 〜66 質量 %,ai2〇3: 15 〜22 質量%,B2〇3 :5〜12質量%’ Mg〇: 〇〜8質量%,Ca〇: 〇〜9質量%, 200906755Si02: 58 to 66% by mass, ai2〇3: 15 to 22% by mass, B2〇3: 5 to 12% by mass' Mg〇: 〇~8 mass%, Ca〇: 〇~9 mass%, 200906755

SrO: 3〜12.5質量%,BaO: 0〜2 質量 %,SrO: 3 to 12.5% by mass, BaO: 0 to 2% by mass,

MgO + CaO + SrO + BaO : 9 〜18 質鼍。/。 (2)MgO + CaO + SrO + BaO : 9 〜 18 鼍. /. (2)

Si02: 50 〜61.5 質量%,A1203: 1〇5 〜18 質量 %, B2〇3: 7〜10 質量 %,MgO: 2〜5 質量 %,CaO: 0〜14.5 質量%,SrO: 0〜24質量%,BaO: 0〜135質量%,Si02: 50 to 61.5% by mass, A1203: 1〇5 to 18% by mass, B2〇3: 7 to 10% by mass, MgO: 2 to 5% by mass, CaO: 0 to 14.5% by mass, SrO: 0 to 24% by mass %, BaO: 0 to 135 mass%,

MgO + CaO + SrO + BaO : 16〜29.5 質量。/。…(3) [發明之效果] 依據本發明之無鹼玻璃之製造方法時,可得到玻璃中 热泡少’且均負性及平坦度優之無驗坡璃。 [實施發明之最佳形態] 無驗玻璃係藉由將含有矽源、鹼土金屬源及硼源之玻 璃原料熔融、成形來製造。無鹼玻璃例如以下述製造。 (1 )將砂源、驗土金屬源及硼源,與必要時之A120: 、清澄劑等’以成爲目標之無鹼玻璃之組成的比例予以混 合’調製玻璃原料。 要時具有與目標之無鹼玻璃 (Π)將該玻璃原料及必 200906755 之組成相同組成的玻璃片’由熔融窯之玻璃原料投入口連 續投入熔融窯内,以1 5 00〜1 600°C熔融形成熔融玻璃。玻 璃片係指無鹼玻璃之製造過程等所排出的玻璃屑。 · (Π i )將該熔融玻璃藉由浮法等公知成形法’成爲所 定厚度予以成形。 (iv )成形後之玻璃帶經慢慢冷卻後,切斷成所定之 大小,得到板狀之無鹼玻璃。 (矽源) 製造無鹼玻璃時之玻璃原料所含有之矽源可使用矽砂 。矽砂只要是可用於製造玻璃者,即可使用。 矽砂之平均粒徑D5Q(等量粒徑)較佳爲15〜60μπι’ 更佳爲20〜45μηι。 矽砂之平均粒徑D 5 〇爲1 5 μ m以上時,可抑制矽砂之 凝集,可得到氣泡少,均質性、平坦度高的無鹼玻璃。砂 砂之平均粒徑D 5 Q爲6 0 μ m以下時,矽砂容易均勻熔融, 可得到氣泡更少,均質性、平坦度更高的無鹼玻璃。平均 粒徑係藉由例如雷射繞射/散射法計測粒度分布來測定。 (鹼土金屬源) 鹼土金屬源可使用鹼土金屬化合物。鹼土金屬例如有 Mg、Ca、Sr及Ba中任1種或2種以上的元素。驗土金屬 化合物之具體例有 MgC03、CaC03、BaC03、SrC〇3、( Mg ’ Ca) C03 (白雲石)等之碳酸鹽或MgO、CaO、Ba〇 200906755 、SrO 等之氧化物或 Mg(OH) 2、Ca(OH) 2、Ba(OH) 2 ' Sr ( OH ) 2等之氫氧化物,但是本發明中,較佳爲鹼土 金屬源之一部份或全部含有鹼土金屬之氫氧化物。 鹼土金屬之氫氧化物之含量係在鹼土金屬源100莫耳 % (MO換算,但是Μ係鹼土金屬元素)中,較佳爲15〜 1 0 0莫耳% ( Μ 0換算),更佳爲3 0〜1 〇 〇莫耳% ( Μ 0換 算)’更佳爲60〜100莫耳% ( ΜΟ換算)。上述氫氧化 物之含量未達1 5莫耳%時,玻璃原料融解時,砂砂中所含 之Si02成分的未融解量增加,此未融解之Si〇2會在玻璃 融液中產生氣泡時,被此氣泡包圍,在玻璃融液之表層附 近聚集。因此玻璃融液之表層與表層以外之部分之間, S i ◦ 2之組成比產生差異,玻璃之均質性降低,同時平坦性 也降低,故不佳。 隨著鹼土金屬源中之氫氧化物之莫耳比増加,玻璃原 料之融解時之Si〇2成分之未融解量會降低,因此上述氫 氧化物之莫耳比越高越佳。 鹼土金屬源具體而言可使用鹼土金屬之氫氧化物與碳 酸鹽之混合物、鹼土金屬之氫氧化物單獨等。碳酸鹽較佳 爲使用例如MgC〇3、CaC〇3及(Mg’ Ca) C03(白雲石) 中任一種以上。鹼土金屬之氫氧化物較佳爲使用Mg(OH)2 或Ca ( OH ) 2之至少其中之一,特佳爲使用Mg (OH)2。 (硼源) 其次,作爲硼源之硼化合物例如有原硼酸(H3 B 0 3 ) -10- 200906755 、偏硼酸(Η Β Ο 2 )、四硼酸(Η 2 B 4 Ο 7 )、無水硼酸(無 水B2〇3)等。 通常之無鹼玻璃之製造時’從廉價、取得容易的觀點 ,可使用原硼酸。 本發明中,硼源使用無水硼酸時,硼源1 0 0質量。/〇 ( b2o3換算)中,較佳爲含有10〜1〇〇質量%(02〇3換算) 。無水硼酸爲1 0質量%以上,可抑制玻璃原料之凝集’可 得到氣泡之降低效果、均質性、平坦度之提升效果。無水 硼酸之更佳的範圍係2 0〜1 0 0質量%之範圍。無水硼酸以 外之硼化合物從廉價、取得容易的觀點,可使用原硼酸。 (其他原料) 其他原料例如有Al2〇3等。爲了改善熔融性、清澄性 、成形性,作爲清澄劑等可含有Ζ η Ο、S Ο 3、F、C 1、S η Ο 2 (玻璃原料) ϊ皮璃原料係混合前述各原料之粉末狀的混合物。 玻璃原料之組成係具有目標之組成之成爲無鹼玻璃的 組成。玻璃原料之組成較佳爲具有後述之組成(1 )之成 爲無驗玻璃的組成,特佳爲具有後述之組成(2 )或(3 ) 之成爲無鹼玻璃的組成。 (無鹼玻璃) -11 - 200906755 本發明之製造方法製得之無鹼玻璃係其組成中含有來 自矽源之Si〇2及來自硼源之b2〇3。無鹼玻璃係指實質上 不含Na20、κ20等之鹼金屬氧化物的玻璃。 以下說明無鹼玻璃之較佳的組成。 無鹼玻璃係具有作爲顯示器用玻璃基板的特性(熱膨 脹係數:25\1〇-7〜60><1〇-7/。(:'耐藥品性、耐久性等), 從適合板玻璃之成形的觀點,較佳爲以氧化物基準之質量 百分比表示具有下述組成(1 )的無鹼玻璃。 無鹼玻璃(1 0 0質量% )中,S i Ο 2 : 5 0〜6 6質量%、 Al2〇3: 10.5 〜22質量%、B203: 5〜12質量%、MgO: 〇〜 8質量%、CaO: 〇〜14_5質量%、SrO: 0〜24質量%、 BaO: 〇 〜13.5 質量 %、MgO + CaO + SrO + BaO: 9〜29.5 質量 % · · . ( 1 )。 又’無鹼玻璃係應變點爲64〇t以上’熱膨脹係數、 密度小,抑制蝕刻用之緩衝氟酸(BHF )造成的白濁,對 鹽酸等藥品之耐久性優異,熔融.成形容易,且適合浮法 成形的觀點,特佳爲以氧化物基準之質量百分比表示,具 有下述組成(2 )的無鹼玻璃。 無鹼玻璃(1 〇 〇質量% )中,S i 0 2 : 5 8〜6 6質量% ' Al2〇3: 15〜22 質量 %、B2〇3: 5〜12 質量%、MgO: 0〜8 質量%、CaO: 〇〜9 質量 %、SrO: 3 〜12_5 質量%、BaO: 0〜2 質量%、MgO + CaO + SrO + BaO: 9〜18 質量%··. (2) 〇MgO + CaO + SrO + BaO : 16 to 29.5 by mass. /. (3) [Effects of the Invention] According to the method for producing an alkali-free glass of the present invention, it is possible to obtain a glass having no heat blister in the glass and having excellent uniformity and flatness. [Best Mode for Carrying Out the Invention] The glass-free material is produced by melting and molding a glass raw material containing a source of cerium, an alkaline earth metal source, and a boron source. The alkali-free glass is produced, for example, as follows. (1) Mixing a sand source, a soil-measuring metal source, and a boron source with a ratio of A120:, a clearing agent, etc., if necessary, to the composition of the target alkali-free glass. When necessary, the glass piece having the same composition as the target alkali-free glass (Π) of the glass raw material and the composition of the must-have 200906755 is continuously fed into the melting kiln from the glass raw material input port of the melting kiln to 1 500 00 to 1 600 ° C. Melt to form molten glass. The glass flakes refer to the glass cullet discharged from the manufacturing process of the alkali-free glass. (Π i ) The molten glass is formed into a predetermined thickness by a known molding method such as a float method. (iv) After the formed glass ribbon is slowly cooled, it is cut into a predetermined size to obtain a plate-shaped alkali-free glass. (矽源) 矽 sand can be used as a source of glass in the production of alkali-free glass. As long as it can be used to make glass, it can be used. The average particle diameter D5Q (equivalent particle diameter) of the cerium sand is preferably 15 to 60 μπι', more preferably 20 to 45 μm. When the average particle diameter D 5 〇 of the enamel is 15 μm or more, aggregation of the cerium sand can be suppressed, and an alkali-free glass having less bubbles and high homogeneity and flatness can be obtained. When the average particle diameter D 5 Q of the sand is 60 μm or less, the cerium is easily melted uniformly, and an alkali-free glass having less bubbles and higher homogeneity and flatness can be obtained. The average particle size is determined by measuring the particle size distribution by, for example, a laser diffraction/scattering method. (Alkaline earth metal source) An alkaline earth metal compound can be used as the alkaline earth metal source. The alkaline earth metal is, for example, one or two or more elements selected from the group consisting of Mg, Ca, Sr and Ba. Specific examples of the soil-measuring metal compound include carbonates such as MgC03, CaC03, BaC03, SrC〇3, (Mg'Ca) C03 (dolomite), or oxides of MgO, CaO, Ba〇200906755, SrO, or Mg(OH). 2, Ca(OH) 2, Ba(OH) 2 'Sr ( OH ) 2 or the like hydroxide, but in the present invention, it is preferred that some or all of the alkaline earth metal source contains an alkaline earth metal hydroxide . The content of the hydroxide of the alkaline earth metal is preferably from 15 to 100% by mol (in terms of Μ 0), preferably more than 100% by mol of the alkaline earth metal source (in terms of MO, but lanthanide alkaline earth metal element). 3 0~1 〇〇 耳 % ( Μ 0 conversion) 'better 60 to 100 mA % ( ΜΟ conversion). When the content of the above hydroxide is less than 15 mol%, when the glass raw material is melted, the unmelted amount of the SiO2 component contained in the sand is increased, and the unmelted Si〇2 is generated in the glass melt. Surrounded by this bubble, it gathers near the surface of the glass melt. Therefore, there is a difference in the composition ratio of S i ◦ 2 between the surface layer of the glass melt and the portion other than the surface layer, and the homogeneity of the glass is lowered, and the flatness is also lowered, which is not preferable. As the molar ratio of the hydroxide in the alkaline earth metal source increases, the amount of undecomposed Si 2 component in the glass raw material is lowered, so that the higher the molar ratio of the above hydrogen oxide is. As the alkaline earth metal source, specifically, a mixture of a hydroxide of an alkaline earth metal and a carbonate, a hydroxide of an alkaline earth metal, or the like can be used. The carbonate is preferably any one or more of, for example, MgC〇3, CaC〇3, and (Mg' Ca) C03 (dolomite). The hydroxide of the alkaline earth metal is preferably at least one of Mg(OH)2 or Ca(OH)2, and particularly preferably Mg(OH)2. (Boron source) Next, boron compounds as a boron source are, for example, orthoboric acid (H3B 0 3 )-10-200906755, metaboric acid (Η Β Ο 2 ), tetraboric acid (Η 2 B 4 Ο 7 ), anhydrous boric acid ( Anhydrous B2〇3) and the like. In the production of a general alkali-free glass, orthoboric acid can be used from the viewpoint of being inexpensive and easy to obtain. In the present invention, when the boron source is anhydrous boric acid, the boron source is 100 mass. In the case of /〇 (b2o3 conversion), it is preferable to contain 10 to 1% by mass (02〇3 conversion). When the anhydrous boric acid is at least 10% by mass, the aggregation of the glass raw material can be suppressed, and the effect of reducing the bubble, the homogeneity, and the flatness can be obtained. A more preferable range of anhydrous boric acid is in the range of 20 to 100% by mass. Raw boronic acid can be used from the viewpoint that it is inexpensive and easy to obtain from the boron compound other than anhydrous boric acid. (Other raw materials) Other raw materials include, for example, Al2〇3. In order to improve the meltability, the clarification property, and the formability, it may contain Ζ Ο Ο, S Ο 3, F, C 1 , and S Ο Ο 2 (glass raw materials) as a clearing agent or the like. mixture. The composition of the glass raw material has the composition of the target and becomes the composition of the alkali-free glass. The composition of the glass raw material is preferably a composition having the composition (1) to be described later as a non-glass, and particularly preferably a composition having an alkali-free glass having the composition (2) or (3) described later. (Alkaloid-free glass) -11 - 200906755 The alkali-free glass obtained by the production method of the present invention contains Si〇2 from a source and b2〇3 from a boron source. The alkali-free glass means a glass which does not substantially contain an alkali metal oxide such as Na20 or κ20. The preferred composition of the alkali-free glass will be described below. The alkali-free glass has characteristics (thermal expansion coefficient: 25\1〇-7 to 60><1〇-7/. (: 'chemical resistance, durability, etc.) as a glass substrate for a display, and is suitable for a sheet glass. From the viewpoint of molding, it is preferred to represent an alkali-free glass having the following composition (1) by mass percentage based on an oxide. In an alkali-free glass (100% by mass), S i Ο 2 : 5 0 to 6 6 %, Al2〇3: 10.5 to 22% by mass, B203: 5 to 12% by mass, MgO: 〇~8 mass%, CaO: 〇~14_5 mass%, SrO: 0 to 24 mass%, BaO: 〇~13.5 mass %, MgO + CaO + SrO + BaO: 9 to 29.5 mass% · · (1) Further, 'the alkali-free glass strain point is 64 〇t or more', the thermal expansion coefficient and the density are small, and the buffered fluoric acid for etching is suppressed ( The white turbidity caused by BHF is excellent in durability to a chemical such as hydrochloric acid, and it is easy to melt and form, and is suitable for float forming. It is particularly preferably expressed by mass percentage based on oxide, and has no alkali of the following composition (2). Glass. Alkali-free glass (1 〇〇 mass%), S i 0 2 : 5 8~6 6 mass% ' Al2〇3: 15~22 quality %, B2〇3: 5 to 12% by mass, MgO: 0 to 8% by mass, CaO: 〇~9% by mass, SrO: 3 to 12_5% by mass, BaO: 0 to 2% by mass, MgO + CaO + SrO + BaO: 9~18% by mass. (2) 〇

Si〇2爲58質量%以上,無鹼玻璃之應變點上升,耐 -12- 200906755 藥品性良好,且熱膨脹係數降低。s i 0 2爲6 6質量%以下 ,玻璃之熔融性良好,玻璃質化(devitrification )特性良 好。 A1203爲1 5質量%以上,可抑制無鹼玻璃之相分離, 熱膨脹係數降低,應變點上升。 A12 Ο 3爲2 2質量%以下,玻璃之熔融性良好。 B2〇3係抑制BHF所造成之無鹼玻璃之白濁’不會使 高溫之黏性升高的狀態下,使無鹼玻璃之熱膨脹係數及密 度降低。 B203爲5質量%以上’無鹼玻璃之耐BHF性良好。 B 2 Ο 3爲1 2質量%以下’無鹼玻璃之耐酸性良好’同時應 變點上升。Si〇2 is 58% by mass or more, and the strain point of the alkali-free glass rises, and the resistance to -12-200906755 is good, and the coefficient of thermal expansion is lowered. s i 0 2 is 6% by mass or less, and the glass has good meltability and good devitrification characteristics. When A1203 is 15% by mass or more, phase separation of the alkali-free glass can be suppressed, the coefficient of thermal expansion is lowered, and the strain point is increased. A12 Ο 3 is 22% by mass or less, and the glass has good meltability. The B2〇3 system suppresses the white turbidity of the alkali-free glass caused by BHF, and the thermal expansion coefficient and density of the alkali-free glass are lowered without increasing the viscosity of the high temperature. B203 is 5% by mass or more. The alkali-free glass has good BHF resistance. B 2 Ο 3 is 12% by mass or less. The alkali-resistant glass has good acid resistance, and the strain point increases.

MgO係抑制無鹼玻璃之熱膨脹係數、密度之上昇’提 高玻璃原料之熔融性。The MgO system suppresses the increase in the thermal expansion coefficient and the density of the alkali-free glass to improve the meltability of the glass raw material.

MgO爲8質量%以下,抑制BHF之白濁,抑制無鹼玻 璃之相分離(phase separation)。MgO is 8% by mass or less, suppresses white turbidity of BHF, and suppresses phase separation of alkali-free glass.

CaO係提高玻璃原料之熔融性。 C a 0爲9質量%以下,無鹼玻璃之熱膨脹係數降低’ 玻璃質化特性良好。CaO improves the meltability of the glass raw material. C a 0 is 9% by mass or less, and the coefficient of thermal expansion of the alkali-free glass is lowered'. The glassy properties are good.

SrO爲3質量%以上,可抑制無鹼玻璃之相分離’抑 制BHF之無鹼玻璃之白濁。 ..When SrO is 3% by mass or more, phase separation of the alkali-free glass can be suppressed, and white turbidity of the alkali-free glass of BHF can be suppressed. ..

SrO爲1 2.5質量%以下,無鹼玻璃之熱膨脹係數降低SrO is 12.5 mass% or less, and the coefficient of thermal expansion of the alkali-free glass is lowered.

BaO 係抑制無鹼玻璃之相分離,提高熔融性’提高玻 -13- 200906755 璃質化特性。 B a 0爲2質量%以下,無鹼玻璃之密度降低’熱 係數降低。The BaO system suppresses the phase separation of the alkali-free glass and improves the meltability, and improves the vitreous properties of the glass. B a 0 is 2% by mass or less, and the density of the alkali-free glass is lowered, and the thermal coefficient is lowered.

Mg〇 + Ca〇 + SrO + BaO爲9質量%以上’玻璃之熔 良好。MgO + CaO + SrO + BaO爲18質量%以下’無驗玻 密度降低。 組成(2 )中,爲了改善熔融性、清澄性 '成形 因此無鹼玻璃(1〇〇質量% )中,Zn〇、、F、 Sn02之總量可含有5質量%以下。玻璃片之處理需要 的步驟,因此除去P b Ο、A S 2 Ο3、S b 2 0 3以雜質等形態 可避免所混入者’且不含有這些雜質爲佳。 本發明之無鹼玻璃從作爲顯示器用玻璃基板的特 異,耐還原性、均質性、氣泡抑制優異’適合浮法之 的觀點,以氧化物基準之質量百分比表示’特佳爲具 述組成(3 )的無鹼玻璃。 無鹼玻璃(100質量%)中,Si〇2: 50〜61·5質邏 Al2O3:10.5〜18質量%、B2O3:7〜10質量°/。、MgO 5質量%、〇3〇:0〜14.5質量%、31*〇:0~24質量 BaO: 〇〜135 質量 %、Mg〇 + Ca〇 + Sr〇 + Ba〇: 16 〜29 量 % . . . ( 3 )。 S i 0 2爲5 0質量%以上’無驗玻璃之耐酸性良好 度降低,應變點降低’熱膨脹係數下降’楊氏模數上 Si02爲6 1.5質量%以下’無驗玻璃之玻璃質化特性良 A12 0 3爲1 0.5質量°/°以上’抑制無鹼玻璃之相分 :膨脹 融性 璃之 性, C1、 較多 之不 性優 成形 有下 [% ' :2〜 [%、 .5質 ,密 升。 好。 離, -14 - 200906755 提高應變點,楊氏模數提高。Al2〇3爲1 8質量°/。以下’無 鹼玻璃之玻璃質化特性、耐酸性及耐B H F性良好。 B2〇3爲7質量%以上’使無鹼玻璃之密度降低’提高 耐B H F性,提高熔融性,玻璃質化特性良好’使熱膨脹 係數降低。 使具有上述效果之Β2〇3爲質量%以下時’無驗玻 璃之應變點上升,楊氏模數上升,耐酸性良好。 M g Ο爲2質量%以上,使無鹼玻璃之密度降低’不必 提高熱膨脹係數,且應變點不會過度降低’提高溶融性。 M g Ο爲5質量%以下’可抑制無鹼玻璃之相分離’玻 璃質化特性、耐酸性及耐B HF性良好。 C a Ο係不必提高無鹼玻璃之密度’不必提高熱膨脹係 數,且應變點不會過度降低’提咼溶融性。 C a Ο爲1 4.5質量%以下,無鹼玻璃之玻璃質化特性良 好,熱膨脹係數降低,密度降低’耐酸性及耐鹼性良好。 S r 0係不必提高無鹼玻璃之密度’不必提高熱膨脹係 數,且應變點不會過度降低’提高熔融性。Mg〇 + Ca〇 + SrO + BaO is 9% by mass or more. The glass is well melted. MgO + CaO + SrO + BaO is 18% by mass or less. In the composition (2), in order to improve the meltability and the clarity, the total amount of Zn〇, F, and Sn02 may be 5% by mass or less in the alkali-free glass (% by mass). Since the steps required for the treatment of the glass piece are removed, it is preferable to remove P b Ο, A S 2 Ο 3, and S b 2 0 3 in the form of impurities, etc., and it is preferable to avoid the inclusion of the impurities. The alkali-free glass of the present invention is specific to the glass substrate for display, and is excellent in resistance to reduction, homogeneity, and bubble suppression, and is expressed as a mass percentage based on oxides from the viewpoint of suitable floatation. Alkali-free glass. In the alkali-free glass (100% by mass), Si〇2: 50 to 61·5 is composed of Al2O3: 10.5 to 18% by mass, and B2O3: 7 to 10% by mass. MgO 5 mass%, 〇3〇: 0 to 14.5 mass%, 31*〇: 0 to 24 mass BaO: 〇~135 mass%, Mg〇+ Ca〇+ Sr〇+ Ba〇: 16 to 29% by volume. . . ( 3 ). S i 0 2 is 50% by mass or more. 'The acid resistance of the glass is reduced, the strain point is lowered, and the coefficient of thermal expansion is decreased. The Si02 of the Young's modulus is 6 1.5% by mass or less. The vitrification characteristics of the glass without the glass. Good A12 0 3 is 1 0.5 mass ° / ° or more 'Suppressing the phase of alkali-free glass: the property of swelling and melting glass, C1, more non-excellent forming is under [% ' : 2~ [%, .5 Quality, dense rise. it is good. From, -14 - 200906755 Increase the strain point and increase the Young's modulus. Al2〇3 is 18 mass%/. The following alkali-free glass has good vitrification characteristics, acid resistance, and B H F resistance. B2〇3 is 7% by mass or more 'The density of the alkali-free glass is lowered'. The BH F resistance is improved, the meltability is improved, and the vitrification property is improved. The thermal expansion coefficient is lowered. When Β2〇3 having the above-described effects is 9% by mass or less, the strain point of the non-inspected glass rises, the Young's modulus increases, and the acid resistance is good. When M g Ο is 2% by mass or more, the density of the alkali-free glass is lowered. 'The thermal expansion coefficient is not necessarily increased, and the strain point is not excessively lowered'. The meltability is improved. M g Ο is 5% by mass or less 'the phase separation of the alkali-free glass can be suppressed', and the glass properties, acid resistance, and B HF resistance are good. The C a lanthanide does not have to increase the density of the alkali-free glass. It is not necessary to increase the coefficient of thermal expansion, and the strain point is not excessively lowered. When C a Ο is 4.5% by mass or less, the alkali-free glass has good vitrification characteristics, a low thermal expansion coefficient, and a low density, and the acid resistance and alkali resistance are good. The S r 0 does not have to increase the density of the alkali-free glass. It is not necessary to increase the coefficient of thermal expansion, and the strain point is not excessively lowered.

SrO爲24質量%以下,無鹼玻璃之玻璃質化特性良好 ’熱膨脹係數降低’密度降低’耐酸性及耐鹼性良好。 B aO係抑制無鹼玻璃之相分離’提高玻璃質化特性, 提高耐藥品性。 B a Ο爲1 3 . 5質量%以下’無鹼玻璃之密度降低’熱膨 膜係數降低,提高楊氏模數’熔融性良好’耐B H F性良 好。 -15- 200906755SrO is 24% by mass or less, and the alkali-free glass has good vitrification characteristics. 'The coefficient of thermal expansion is lowered' and the density is lowered. The acid resistance and alkali resistance are good. B aO suppresses phase separation of alkali-free glass. It improves vitrification characteristics and improves chemical resistance. B a Ο is 13.5% by mass or less 'The density of the alkali-free glass is lowered' The thermal expansion film coefficient is lowered, and the Young's modulus is improved, and the meltability is good, and the B H F resistance is good. -15- 200906755

MgO + CaO + SrO + BaO爲16質量%以上,玻璃之熔融性 良好。MgO + CaO + SrO + BaO爲29.5質量%以下,無鹼玻璃 之密度、熱膨脹係數降低。 組成(3 )中,爲了改善溶融性、清澄性、成形性’ 在無驗玻璃(100質量%)中,ZnO、S Ο 3 ' F' Cl、S η Ο 2 之總量可含有5質量%以下。玻璃片之處理需要較多的步 驟,因此除去P b 0、A s 2 Ο 3、S b 2 Ο 3以雜質等形態之不可避 免所混入者,且不含有這些雜質爲佳。 如以上說明,依據本發明之無鹼玻璃之製造方法時, 鹼土金屬源爲使用鹼土金屬之氫氧化物在鹼土金屬源1〇〇 莫耳% (MO換算,但是Μ爲鹼土金屬元素)中,含有15 〜100 .莫耳% ( ΜΟ換算)者,因此玻璃融液中之Si02之 未融解量大幅減少,同時氣泡之產生量減少,因此可改善 Si02之偏析,可得到均質性、平坦度高的無鹼玻璃。 本發明使用鹼土金屬之氫氧化物(該氫氧化物係在玻 璃之液相生成前(約400°c )放出H20,因此不易影響液 相生成),相較於使用鹼土金屬之碳酸鹽(該碳酸鹽係在 玻璃之液相生成(6 0 0〜8 0 0 °C )時,釋出C Ο 2 )之習知時 ,玻璃融液中之氣泡之產生量減少,玻璃中之氣泡減少。 添加鹼土金屬之氫氧化物,使玻璃融液之液性由酸性 傾向於鹼性側,因此Si02之反應性升高,Si02之未融解 量減低。 如上述,本發明可相乘地實現未融解之Si〇2量之降 低與氣泡產生量降低,可得到均質性、平坦度優的無鹼玻 -16- 200906755 璃。 本發明中,硼源爲使用硼源1 00質量% ( B2〇3換算) 中含有無水硼酸10〜100質量% ( B2〇3換算)者時,可得 到玻璃中之氣泡更少,均質性及平坦度更高的無鹼玻璃。 特別是硼源使用原硼酸時,在原硼酸之存在下,粒徑 較小之矽砂易凝集。矽砂之凝集係因玻璃原料所含之水分 所引起的,爲了抑制矽砂之凝集,只要減少玻璃原料所含 的水分即可。換言之,減少分子中含有許多水分子之原硼 酸的量,增加無水硼酸的量,可得到氣泡少,均質性及平 坦度高的無鹼玻璃。 玻璃原料含有鹼土金屬化合物時,有時在溶解窯之玻 璃原料投入口有熔融的原硼酸與鹼土金屬化合物產生凝集 。原硼酸與鹼土金屬化合物之凝集係在玻璃原料投入口被 加熱之原硼酸失去1個水分子,成爲偏硼酸,此偏硼酸在 1 5 0 °C以上液化,與鹼土金屬化合物接触所引起的。因此 ,使用由偏硼酸再失去水分子之狀態的無水硼酸時,可抑 制偏硼酸與驗土金屬化合物之凝集,可得到氣泡少,均質 性及平坦度高的無鹼玻璃。 本發明之無鹼玻璃之製造方法中,如上述使用無水硼 酸時’可得到以下的效果。 (i )抑制玻璃原料中之水分量,因此玻璃原料熔融 時之水的氣化熱減少。藉此減少之氣化熱的分量可減少在 熔融窯消耗之能量,可達到省能源化,提高生產性。 (ii )因減少熔融玻璃中之水分(β_〇Η ),因此清澄 -17- 200906755 劑所含之氯(c 1 )因下述反應成爲H c 1,可抑制揮散。藉 此可降低清澄劑的量’減少含有H C1之排氣體的處理負擔 oir + cr —HCiT + ο2· ° (iii)原硼酸失去1個水分子所生成的偏硼酸容易揮 散’但是無水硼酸不易揮散’可降低硼源的量’可減少含 有偏硼酸之排氣體的處理負擔。 【實施方式】 [實施例] 以下舉實施例具體說明本發明,但是本發明不限於這 些實施例。 〔實驗1〕 調製矽源、鹼土金屬源、硼源及其他原料’使具有以 氧化物基準之質量百分比表不’ Si〇2: 60質量%、Al2〇3 :17 質量 %、B2〇3: 8 質量%、MgO: 3 質量%、CaO: 4 質量%、S r Ο : 8質量%之組成的無鹼玻璃’作爲玻璃母組 成原料,再對於該玻璃母組成原料玻璃化後之1 00質量% 混合作爲清澄劑之C1 1 .〇質量%作爲玻璃原料。 砂源係使用平均粒徑D 5 Q爲2 6 l·1 m、最小徑〜最大徑 爲5〜ι〇〇μιη的矽砂。平均粒徑D5Q係以雷射繞射/散射法 -18- 200906755 (HORIBA LA9 5 0WET)計測粒度分布來測定。 鹼土金屬源係如表1使用Mg(OH) 2、Ca(OH) 2、 白雲石((Mg,Ca) C03) 、MgC03、CaC03及碳酸緦之 化合物’表1中,鹼土金屬化合物中之氫氧化物量以MO 換算來表示。 硼源係如表1所示,使用無水硼酸(無水B2〇3 )或 原硼酸(h3bo3 )。 其次’如圖1 ( a )所示,將玻璃化後之質量成爲 250g之量的玻璃原料置入高度9〇nim、外徑70mm之有 底円筒形之白金鍺製的坩堝〗4中。將該坩堝1 4置入加熱 爐內’坩堝1 4内不必強制攪拌,由加熱爐之側面吹入露 點8 0 °C之空氣,同時以;[5 5 〇 〇C (相當於玻璃黏度η爲 10 g η =2.5的溫度)加熱1小時,使玻璃原料1 2熔融。熔 融玻璃以各坩堝i 4冷卻後,如圖1 ( b )所示,由坩堝14 内之無鹼玻璃16之中央部切成長24mm、寬35mm、厚度 1 m m的板狀試料1 8。 如圖2所不,對於長24mm、寬35mm之試料18之中 央部之長18mm、寬15mm的區域(上側之空白1.5mm、 左右之空白l〇mm)以直徑3mm營光X線之光束照射長6 處x寬5處之合計3 〇處,測定各處之無鹼玻璃的組成。 30處之組成中,由Si02 (質量% )之最大値減去 Si〇2 (質量%)之最小値,計算組成差(ASi〇2)。 5十算g式料18之中央部之長24mm、寬10mm之區域之 歹5留於玻璃内之氣泡之最大長度爲5μιη以上之氣泡數,求 -19- 200906755 得玻璃每 求取 Si〇2)的 4 0 0 0 mm X 傾斜的爐 之玻璃表 倂於表2 1 k g之氣泡數。 玻璃原料溶解時,未溶融殘留之矽砂(未融解 比例。未融解S i Ο 2係將2 5 0 g之原料添加於長度 寬20mm之白金板,以具有 800〜1500 °C之溫度 加熱1小時後,藉由在1 4 0 0〜1 5 0 0 °C之溫度區域 面所殘留之矽砂所佔有面積來測定。這些結果合 、圖3及圖4所不。 -20- 200906755 I I i硼源 h3bo3 h3b〇3 h3b〇3 無水B 2 〇 3 1 無水B 1 1無水b 2o3」 1 η,β〇3 1 丨鹸土金屬源 I 3 _ ft M <n 醭 ~H Μ Ε- 实 Μ 澳 鸹 Ν 鸹 § it S r C O ^ 03 sr ri N CNJ w 寸 CJ N 寸 n 寸 03 Ν I I C a C〇3 〇 10 o o m ο CD W MgC03 o o o o σ ο Ν fH 白雲石 I U3 CM o o in n o ο Ο I C a <OH> 2 〇 o •H o o τΗ — ο Mg (OH) 2 10 ΙΛ OJ — C) W ΙΛ lA N »—1 CVJ »-Η ο 删 iwlS 纒fr (0 r—4 L, to ΙΛ Φ <c r- Ift <r> Λ Φ ο 1實施例l ] 1實施例2 1 cn 援 κ 1實施例4 1 vr> 莩 m 1實施例6 1 1比較例1 1 -21 - 200906755 表2 △Si02 未融解Si02 5//m以上之氣泡數 (質量%) (%) (玻璃每lkg) 實施例1 2. 0 18 30X10^ 實施例2 1. 7 14 2 ΟΧΙΟ4 實施例3 1. 0 3 10X104 實施例4 1. 7 10 15X1 Ο4 實施例5 1. 0 8 10Χ104 實施例6 0. 5 5 5X10* 比較例1 3. 0 25 5 ΟΧ 104 表1中,Δ S i Ο 2越小,表示組成之偏差越小’換言之 ,無鹼玻璃之均質性佳。如表1、圖3及圖4所示可知鹼 土金屬源之一部份使用氫氧化物的實施例1〜6係Δ~〇2 爲0.5〜2.0質量%’未融解之Si〇2重爲3〜18 %’而且氣 泡數爲5χ104〜3〇χ 104個’相較於比較例1時’ ASiOj、 未融解之S i 02量及氣泡數大幅降低。此乃是驗土金屬源 使用氫氧化物’因此玻璃融液之液性由酸性側傾向鹼性側 ,藉此提高砂砂中之S i 0 2之反應性’結果未融解S i 0 2量 減少。 可知硼源使用無水硼酸(B 2 0 3 )時’未融解之s丨0 2 量及氣泡數降低’且均質性佳。鹼土金屬源之全部使用氫 氧化物時,ASi02、未融解之Si〇2量及氣泡數均可減少。 由上述可知,使用本發明之玻璃之製造方法’可製得 大幅提高玻璃之均質性,再降低氣泡數’同時平坦度優異 的無鹼玻璃。 -22- 200906755 [產業上之利用性] 藉由本發明之製造方法所得之無鹼玻璃係玻璃中,氣 泡少,均質性、平坦度高。而且含有B2〇3,因此耐藥品 性及耐久性也優異。 該無鹼玻璃可作爲液晶顯示裝置等之顯示器用之玻璃 基板等使用。 於茲引用2007年4月17曰所提出申請之日本申請專 利2007-108086號之說明書、申請專利範圍、圖面及摘要 之全部内容’揭示於本發明之說明書中。 【圖式簡單說明】 [圖1 ]圖1係表示實施例之無鹼玻璃之製造方法的槪 略圖。 [圖2 ]圖2係表示試料之組成之測定處的模式圖。 [圖3 ]圖3係表示實驗例1〜6之Δ S i 0 2 (質量% )的 曲線圖。 [圖4]圖4係表示實驗例1〜6之5μηι以上之氣泡數( 個· k g _1 )的曲線圖。 【主要元件符號說明】 1 2 :玻璃原料 1 6 :無鹼玻璃 -23-MgO + CaO + SrO + BaO is 16% by mass or more, and the glass has good meltability. MgO + CaO + SrO + BaO is 29.5% by mass or less, and the density and thermal expansion coefficient of the alkali-free glass are lowered. In the composition (3), in order to improve the meltability, the clearness, and the formability, the total amount of ZnO, S Ο 3 'F' Cl, and S η Ο 2 may be 5% by mass in the non-glass (100% by mass). the following. Since the processing of the glass piece requires a large number of steps, it is preferable to remove P b 0, A s 2 Ο 3, and S b 2 Ο 3 in the form of impurities, which are inevitably mixed, and it is preferable not to contain these impurities. As described above, in the method for producing an alkali-free glass according to the present invention, the alkaline earth metal source is a hydroxide using an alkaline earth metal in an alkaline earth metal source of 1% by mol (in terms of MO, but lanthanum is an alkaline earth metal element). Containing 15 to 100% of the molar % (in terms of ΜΟ conversion), the amount of SiO 2 in the glass melt is greatly reduced, and the amount of bubbles is reduced, so that segregation of SiO 2 can be improved, and homogeneity and flatness can be obtained. Alkali-free glass. The present invention uses a hydroxide of an alkaline earth metal (the hydroxide releases H20 before the liquid phase formation of the glass (about 400 ° C), so that it does not easily affect the liquid phase formation), compared to the carbonate using an alkaline earth metal (this When the carbonate is formed in the liquid phase of the glass (600 to 800 °C), when C Ο 2 is released, the amount of bubbles generated in the glass melt is reduced, and the bubbles in the glass are reduced. The alkali metal hydroxide is added so that the liquidity of the glass melt is acidic from the alkaline side, so the reactivity of SiO 2 is increased, and the amount of SiO 2 is not melted. As described above, the present invention can multiply the reduction of the amount of unmelted Si〇2 and the decrease in the amount of generation of bubbles, and obtain an alkali-free glass having excellent homogeneity and flatness. In the present invention, when the boron source is used in an amount of 10 to 100% by mass (in terms of B2〇3) containing anhydrous boric acid in a boron source of 100% by mass (in terms of B2〇3), bubbles in the glass are obtained, and homogeneity is obtained. An alkali-free glass with a higher flatness. In particular, when orthoboric acid is used as the boron source, in the presence of orthoboric acid, the cerium sand having a small particle size is easily aggregated. The agglutination of the sand is caused by the moisture contained in the glass raw material, and in order to suppress the aggregation of the sand, it is only necessary to reduce the water contained in the glass raw material. In other words, the amount of ortho-boric acid containing a large amount of water molecules in the molecule is reduced, and the amount of anhydrous boric acid is increased to obtain an alkali-free glass having less bubbles, high homogeneity and high flatness. When the glass raw material contains an alkaline earth metal compound, molten ortho-boric acid and an alkaline earth metal compound may be aggregated in the glass raw material input port of the dissolution kiln. The agglutination of ortho-boric acid and an alkaline earth metal compound loses one water molecule in the ortho-boric acid heated by the glass raw material input port, and becomes metaboric acid. The metaboric acid is liquefied at 150 ° C or higher and is brought into contact with the alkaline earth metal compound. Therefore, when anhydrous boronic acid in which the water molecules are lost by the metaboric acid is used, aggregation of the metaboric acid and the soil-measuring metal compound can be suppressed, and an alkali-free glass having less bubbles, high homogeneity and flatness can be obtained. In the method for producing an alkali-free glass of the present invention, when the above-mentioned anhydrous boric acid is used, the following effects can be obtained. (i) The amount of water in the glass raw material is suppressed, so that the heat of vaporization of water when the glass raw material is melted is reduced. By reducing the amount of heat of vaporization, the energy consumed in the melting kiln can be reduced, energy saving and productivity can be achieved. (ii) Since the water (β_〇Η) in the molten glass is reduced, the chlorine (c 1 ) contained in the clearing -17-200906755 agent is H c 1 due to the following reaction, and the volatilization can be suppressed. Thereby, the amount of the clearing agent can be reduced 'reducing the processing burden of the exhaust body containing H C1 oir + cr — HCiT + ο2 · ° (iii) the boric acid generated by the orthoboric acid losing one water molecule is easily volatilized' but the anhydrous boric acid is not easy The volatilization 'reducing the amount of boron source' can reduce the processing burden of the exhaust body containing metaboric acid. [Embodiment] [Embodiment] Hereinafter, the present invention will be specifically described by way of Examples, but the present invention is not limited to these Examples. [Experiment 1] Modulation of lanthanum source, alkaline earth metal source, boron source and other raw materials 'has a mass percentage based on oxides as 'Si〇2: 60% by mass, Al2〇3: 17% by mass, B2〇3: 8% by mass, MgO: 3% by mass, CaO: 4% by mass, S r Ο : 8 % by mass of the alkali-free glass 'as a glass mother component raw material, and then 100% of the glass raw material is vitrified % Mixed as a clearing agent C1 1 .〇% by mass as a glass raw material. The sand source is a strontium sand having an average particle diameter D 5 Q of 2 6 l·1 m and a minimum diameter to a maximum diameter of 5 to ι 〇〇 μηη. The average particle diameter D5Q was measured by measuring the particle size distribution by laser diffraction/scattering method -18-200906755 (HORIBA LA9 5 0WET). The alkaline earth metal source is as shown in Table 1. Mg(OH) 2, Ca(OH) 2, dolomite ((Mg, Ca) C03), MgC03, CaC03 and cesium carbonate compounds are shown in Table 1, hydrogen in alkaline earth metal compounds. The amount of oxide is expressed in terms of MO. The boron source was as shown in Table 1, and anhydrous boric acid (anhydrous B2〇3) or orthoboric acid (h3bo3) was used. Next, as shown in Fig. 1 (a), a glass raw material having a vitrified mass of 250 g was placed in a crucible-shaped platinum crucible having a height of 9 〇nim and an outer diameter of 70 mm. Put the crucible 14 into the heating furnace. There is no need to force stirring in the furnace. The air from the side of the furnace is blown into the dew point of 80 °C, and at the same time; [5 5 〇〇C (corresponding to the glass viscosity η is The temperature of 10 g η = 2.5 was heated for 1 hour to melt the glass raw material 12 . After the molten glass was cooled by each of the crucibles 4, as shown in Fig. 1 (b), a plate-like sample 18 having a thickness of 24 mm, a width of 35 mm, and a thickness of 1 m was cut from the central portion of the alkali-free glass 16 in the crucible 14. As shown in Fig. 2, a region of 18 mm in length and 15 mm in width at the center of the sample 18 having a length of 24 mm and a width of 35 mm (the blank of the upper side is 1.5 mm, and the space of the left and right sides is 〇mm) is irradiated with a beam of light having a diameter of 3 mm. The total length of 6 places x width 5 places 3 〇, the composition of the alkali-free glass everywhere. In the composition of 30 points, the minimum 値 of Si〇2 (% by mass) was subtracted from the maximum Si of SiO 2 (% by mass), and the composition difference (ASi 〇 2) was calculated. 5, the length of the central portion of the material 18 is 24 mm, the width of 10 mm, the maximum length of the bubbles left in the glass is 5 μmη or more, and the number of bubbles is -19-200906755. The glass of the 4 0 0 mm X tilted furnace is shown in Table 2 for the number of bubbles of 1 kg. When the glass raw material is dissolved, the residual lanthanum sand is not melted (unmelted ratio. Undissolved S i Ο 2 is a raw material of 260 g added to a platinum plate having a length of 20 mm and heated at a temperature of 800 to 1500 ° C. After an hour, it is measured by the area occupied by the strontium sand remaining in the temperature region of 1 400 to 1 500 ° C. These results are combined, as shown in Fig. 3 and Fig. 4. -20- 200906755 II i Boron source h3bo3 h3b〇3 h3b〇3 anhydrous B 2 〇3 1 anhydrous B 1 1 anhydrous b 2o3” 1 η,β〇3 1 alumina metal source I 3 _ ft M <n 醭~H Μ Ε- real鸹Ν 鸹Ν 鸹 it it S r CO ^ 03 sr ri N CNJ w inch CJ N inch n inch 03 Ν IIC a C〇3 〇10 oom ο CD W MgC03 oooo σ ο Ν fH Dolomite I U3 CM oo in no ο Ο IC a <OH> 2 〇o •H oo τΗ — ο Mg (OH) 2 10 ΙΛ OJ — C) W ΙΛ lA N »—1 CVJ »-Η ο Delete iwlS 纒fr (0 r—4 L , to ΙΛ Φ <c r- Ift <r> Λ Φ ο 1 embodiment l ] 1 embodiment 2 1 cn κ 1 Example 4 1 vr> 莩m 1 Example 6 1 1 Comparative Example 1 1 - 21 - 200906755 Table 2 △Si02 Unmelted Si02 5//m Number of bubbles above (% by mass) (%) (glass per lkg) Example 1 2. 0 18 30X10^ Example 2 1. 7 14 2 ΟΧΙΟ4 Example 3 1. 0 3 10X104 Example 4 1. 7 10 15X1 Ο4 Example 5 1. 0 8 10Χ104 Example 6 0. 5 5 5X10* Comparative Example 1 3. 0 25 5 ΟΧ 104 In Table 1, the smaller Δ S i Ο 2 is, the smaller the deviation of composition is indicated. In other words, no The homogeneity of the alkali glass is good. As shown in Table 1, Figure 3 and Figure 4, it can be seen that one part of the alkaline earth metal source uses hydroxide. Examples 1 to 6 are Δ~〇2 of 0.5 to 2.0% by mass. The weight of Si〇2 is 3~18%' and the number of bubbles is 5χ104~3〇χ 104's compared with the case of Comparative Example 1 'ASiOj, the amount of undissolved S i 02 and the number of bubbles are greatly reduced. The earth metal source uses hydroxides. Therefore, the liquidity of the glass melt is inclined from the acidic side to the alkaline side, thereby increasing the reactivity of S i 0 2 in the sand sand. As a result, the amount of undissolved S i 0 2 is reduced. It can be seen that when the boron source is used as the boronic acid (B 2 0 3 ), the amount of the unmelted s 丨 0 2 and the number of bubbles is decreased, and the homogeneity is good. When all of the alkaline earth metal source uses hydrogen oxide, the amount of ASi02, the amount of undissolved Si〇2, and the number of bubbles can be reduced. As described above, the use of the method for producing a glass of the present invention can produce an alkali-free glass which greatly improves the homogeneity of the glass and further reduces the number of bubbles while having excellent flatness. -22-200906755 [Industrial Applicability] The alkali-free glass-based glass obtained by the production method of the present invention has a small amount of bubbles, and has high homogeneity and flatness. Moreover, since it contains B2〇3, it is excellent also in chemical resistance and durability. The alkali-free glass can be used as a glass substrate for a display such as a liquid crystal display device. The entire contents of the specification, the scope of the application, the drawings and the abstract of the Japanese Patent Application No. 2007-108086, filed on Apr. 17, 2007, are hereby incorporated by reference. BRIEF DESCRIPTION OF THE DRAWINGS [Fig. 1] Fig. 1 is a schematic view showing a method of producing an alkali-free glass according to an embodiment. Fig. 2 is a schematic view showing a measurement portion of a composition of a sample. Fig. 3 is a graph showing Δ S i 0 2 (% by mass) of Experimental Examples 1 to 6. 4] FIG. 4 is a graph showing the number of bubbles (number·k g _1 ) of 5 μηι or more in Experimental Examples 1 to 6. FIG. [Main component symbol description] 1 2 : Glass raw material 1 6 : Alkali-free glass -23-

Claims (1)

200906755 十、申請專利範圍 1 · 一種無鹼玻璃之製造方法,其係將含有矽源、鹼土 金屬源及硼源之玻璃原料熔融、成形而製成無鹼玻瑀的製 造方法’其特徵係前述鹼土金屬源爲使用相對於鹼土金屬 源1 00莫耳% ( MO換算,但是μ係鹼土金屬元素,以下 相同)中,含有鹼土金屬之氫氧化物1 5〜1 00莫耳% ( ΜΟ 換算)者。 2 ·如申請專利範圍第1項之無鹼玻璃之製造方法,其 中該硼源爲使用相對於硼源1 〇〇質量% ( Β2〇3換算)中, 含有硼酸酐10〜100質量% (Β2〇3換算)者。 3 .如申請專利範圍第1或2項之無鹼玻璃之製造方法 ,其中該玻璃原料爲使用以氧化物基準之質量百分比表示 ,具有下述組成(1 )之作爲無鹼玻璃的玻璃原料, 8102:50~66質量%,八12〇3:1〇.5〜22質量%,82〇3 :5〜12質量%,MgO: 0〜8質量%’ CaO: 0〜14.5質量 %,S r ◦ : 0 〜2 4 質量 %,B a 0 : 〇 〜1 3 _ 5 質量 °/。, MgO + CaO + SrO + BaO : 9 〜29.5 質量 %…(1)。 4.如申請專利範圍第1或2項之無鹼玻璃之製造方法 ,其中該玻璃原料爲使用以氧化物基準之質量百分比表示 ,具有下述組成(2 )之作爲無鹼玻璃的玻璃原料, Si02: 58 〜66 質量%,Ah〇3: 15 〜22 質量 %,B2〇3 ·· 5〜1 2質量。/。,M g Ο : 〇〜8質量% ’ c a 0 ·_ 〇〜9質量%, SrO: 3 〜12.5質量%,BaO: 0〜2質量%, MgO + CaO + SrO + BaO : 9〜18 質量%…(2)。 -24- 200906755 瞼玻璃之製造方法 之質量百分比表示 玻璃原料, 0.5〜18 質量%, %,CaO : 0〜14_5 3 . 5質量%, 5 .如申請專利範圍第1或2項之無 ,其中該玻璃原料爲使用以氧化物基準: ,具有下述組成(3 )之作爲無鹼玻璃的 Si02: 50 〜61.5 質量%,Al2〇3: 1 B 2 〇 3 : 7〜10質量%,MgO: 2〜5質量 質量%,S r Ο ·· 0〜2 4質量%,B a Ο : 0〜1 MgO + CaO + SrO + BaO : 16 〜29.5質量%...(3)。200906755 X. Patent Application No. 1 · A method for producing an alkali-free glass, which is a method for producing a non-alkali glass bottle by melting and forming a glass material containing a source of lanthanum, an alkaline earth metal, and a boron source. The alkaline earth metal source is used in an amount of 100% by mol relative to the alkaline earth metal source (in terms of MO, but the μ alkaline earth metal element, the same applies hereinafter), and the hydroxide containing the alkaline earth metal is 1 5 to 1 00 mol% ( 换算 conversion) By. 2. The method for producing an alkali-free glass according to the first aspect of the invention, wherein the boron source is used in an amount of 1% by mass relative to the boron source (in terms of Β2〇3), and 10 to 100% by mass of boric anhydride is contained (Β2) 〇3 conversion). 3. The method for producing an alkali-free glass according to claim 1 or 2, wherein the glass raw material is a glass raw material having an alkali-free glass having the following composition (1), which is expressed by mass percentage based on an oxide. 8102: 50 to 66% by mass, eight 12 〇 3:1 〇. 5 to 22% by mass, 82 〇 3 : 5 to 12% by mass, MgO: 0 to 8% by mass 'CaO: 0 to 14.5% by mass, S r ◦ : 0 ~ 2 4% by mass, B a 0 : 〇~1 3 _ 5 Quality °/. , MgO + CaO + SrO + BaO : 9 to 29.5 mass % (1). 4. The method for producing an alkali-free glass according to claim 1 or 2, wherein the glass raw material is a glass raw material having an alkali-free glass having the following composition (2), which is expressed by mass percentage based on an oxide. Si02: 58 to 66% by mass, Ah〇3: 15 to 22% by mass, B2〇3 ··5 to 1 2 by mass. /. , M g Ο : 〇~8 mass% ' ca 0 ·_ 〇~9 mass%, SrO: 3 to 12.5% by mass, BaO: 0 to 2 mass%, MgO + CaO + SrO + BaO : 9 to 18% by mass …(2). -24- 200906755 The mass percentage of the manufacturing method of the bismuth glass indicates the glass raw material, 0.5 to 18% by mass, %, CaO: 0 to 14_5 3. 5 mass%, 5. As in the patent application range No. 1 or 2, The glass raw material is used as an oxide: SiO 2 having an alkali-free glass having the following composition (3): 50 to 61.5% by mass, Al 2 〇 3: 1 B 2 〇 3 : 7 to 10% by mass, MgO: 2 to 5 mass%, S r Ο ·· 0 to 2 4 mass%, B a Ο : 0 to 1 MgO + CaO + SrO + BaO : 16 to 29.5 mass% (3).
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