JP3369781B2 - Method for producing glass powder used by mixing with ceramic powder - Google Patents

Method for producing glass powder used by mixing with ceramic powder

Info

Publication number
JP3369781B2
JP3369781B2 JP08096795A JP8096795A JP3369781B2 JP 3369781 B2 JP3369781 B2 JP 3369781B2 JP 08096795 A JP08096795 A JP 08096795A JP 8096795 A JP8096795 A JP 8096795A JP 3369781 B2 JP3369781 B2 JP 3369781B2
Authority
JP
Japan
Prior art keywords
powder
raw material
mixing
glass
glass powder
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP08096795A
Other languages
Japanese (ja)
Other versions
JPH08277124A (en
Inventor
栗原光一郎
博之 伊藤
隆 坪井
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hitachi Metals Ltd
Original Assignee
Hitachi Metals Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hitachi Metals Ltd filed Critical Hitachi Metals Ltd
Priority to JP08096795A priority Critical patent/JP3369781B2/en
Publication of JPH08277124A publication Critical patent/JPH08277124A/en
Application granted granted Critical
Publication of JP3369781B2 publication Critical patent/JP3369781B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • 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
    • C03C12/00Powdered glass; Bead compositions

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、ガラス粉末の製造方法
に関する。
FIELD OF THE INVENTION The present invention relates to a method for producing glass powder.

【0002】[0002]

【従来の技術】従来、例えば電子部品搭載用基板にセラ
ミック粉末と混合して用いられるガラス粉末の製造は、
図2に示すように、目標組成となるように原料粉末を秤
量し、白金坩堝に移し、各々の原料粉末の溶融温度以上
に加熱し、完全に溶融させ、均質化させた後、溶融物を
水中や金属板上に滴下させることにより急冷固化させ、
更に所定の粒径になるように粉砕する方法によってい
た。
2. Description of the Related Art Conventionally, for example, the production of glass powder which is used by being mixed with ceramic powder for a substrate for mounting electronic parts is
As shown in FIG. 2, the raw material powders were weighed so as to obtain the target composition, transferred to a platinum crucible, heated to a melting temperature or higher of each raw material powder, completely melted, and homogenized, It is rapidly cooled and solidified by dropping it in water or on a metal plate,
Further, a method of pulverizing so as to have a predetermined particle size was used.

【0003】[0003]

【発明が解決しようとする課題】しかし、従来の製造方
法では、各々の原料粉末を溶融温度以上に加熱、均質化
する必要があるが、通常のガラスの原料粉末には酸化ケ
イ素が含まれ、酸化ケイ素を完全に溶融するには白金坩
堝中で1400〜1500℃程度の高温に加熱し、均質
化させるために攪拌する必要がある。このため製造で使
用する炉は特殊であり高価なものにならざるをえず、製
造コストを低減するには限界があるという問題点があっ
た。
However, in the conventional manufacturing method, it is necessary to heat and homogenize each raw material powder at a temperature equal to or higher than the melting temperature. However, the usual glass raw material powder contains silicon oxide, In order to completely melt the silicon oxide, it is necessary to heat it in the platinum crucible to a high temperature of about 1400 to 1500 ° C. and stir it for homogenization. For this reason, there is a problem that the furnace used for manufacturing is special and expensive, and there is a limit to reducing the manufacturing cost.

【0004】更に、前述の工程によれば、異なった組成
のガラス粉末を少量生産する場合、組成が変わる毎に炉
や急冷装置の清掃を行わなければならず、単位重量当た
りの製造コストが非常に大きくなることがあり、少量多
品種への対応はほとんど不可能という問題点があった。
そこで、本発明は製造コストが安く、かつ、少量多品種
生産にも対応可能なガラス粉末製造方法を提供すること
を目的とする。
Further, according to the above-mentioned process, when a small amount of glass powder having a different composition is produced, the furnace and the quenching device have to be cleaned every time the composition changes, and the manufacturing cost per unit weight is very high. However, there is a problem that it is almost impossible to support a large number of small varieties.
Therefore, it is an object of the present invention to provide a glass powder manufacturing method which can be manufactured at low cost and can be used for small-quantity multi-product production.

【0005】[0005]

【課題を解決するための手段】従来のガラス粉末の製造
方法は、目標組成になるように原料粉末を混合して、全
ての原料粉末が溶融する温度まで昇温して、更に攪拌を
行うことが必要とされていた。この溶融工程について本
発明者らは鋭意検討を行った結果、原料粉末全ては完全
に溶融しない温度、つまり一部が粉末の状態でも、原料
粉末のガラス化及び均質化は充分行われることを見い出
し本発明に想到した。
In the conventional method for producing glass powder, the raw material powders are mixed so as to have a target composition, the temperature is raised to a temperature at which all the raw material powders are melted, and further stirring is performed. Was needed. As a result of intensive studies conducted by the present inventors on this melting step, they found that the raw material powder is sufficiently vitrified and homogenized even at a temperature at which all the raw material powders are not completely melted, that is, even when a part of the raw material powder is in a powder state. The present invention was conceived.

【0006】すなわち本発明は、目標組成となるように
粒径1μm以下の各ガラス原料粉末を秤量し、混合した
後、前記混合粉末を原料粉末全てが溶融する完全溶融温
度未満の1000℃以下で熱処理し、ガラス粉末状のままと
なすことを特徴とするセラミックス粉末と混合して用い
られるガラス粉末の製造方法である。ここで前記熱処理
した粉末を粉砕しても良い。
That is, according to the present invention, each glass raw material powder having a particle size of 1 μm or less is weighed so as to have a target composition and mixed, and then the mixed powder is melted at 1000 ° C. or less, which is lower than a complete melting temperature at which all the raw material powders are melted. A method for producing glass powder, which is used by mixing with ceramics powder, which is characterized in that it is heat-treated and remains in a glass powder form. Here, the heat-treated powder may be crushed.

【0007】[0007]

【作用】本発明において、熱処理工程は、従来のガラス
粉末製造工程での溶融攪拌工程と粉砕工程に相当する。
原料粉の完全溶融温度未満での熱処理により、原料粉末
間で原子の移動、拡散を起こさせ、ガラス化反応及び均
質化を促進させ、かつ、生成したガラスは粉末形状であ
るため、粉砕工程は通常不必要である。しかし、より微
細な粒径のガラス粉末が必要なときには粉砕工程が必要
となる。前記ガラス化反応及び均質化を十分起こさせる
ためには、原料粉末は十分混合したものが必要である。
また、反応性は原料粉末の粒径や表面状態、目的とする
ガラス組成や粒径等に依存するため、熱処理条件の温度
及び時間は前記のパラメーターに応じて適宜決められ
る。
In the present invention, the heat treatment process corresponds to the melting and stirring process and the crushing process in the conventional glass powder manufacturing process.
By heat treatment below the complete melting temperature of the raw material powder, atoms are moved and diffused between the raw material powders, the vitrification reaction and homogenization are promoted, and the produced glass is in a powder form, so the pulverization step is Usually unnecessary. However, when a glass powder having a finer particle size is required, a crushing process is required. In order to sufficiently cause the vitrification reaction and homogenization, the raw material powders must be sufficiently mixed.
Further, since the reactivity depends on the particle size and surface condition of the raw material powder, the desired glass composition and particle size, etc., the temperature and time of the heat treatment conditions are appropriately determined according to the above parameters.

【0008】また使用する原料粉末は微細な方が原子間
の移動、拡散が起こりやすく、一次粒子の粒径は1μm
以下が好ましい。但し、ホウ酸のように水に可溶のもの
はボールミルでの混合時に溶解して他の粒子の表面部に
付着するので特に粒径を考慮する必要はない。溶融点の
高い酸化ケイ素の含有量の多い原料を用いる場合ほど、
高温での熱処理が必要となる。また、生成するガラス粉
末の粒径は熱処理温度が高くなるほど大きくなる傾向が
ある。尚、原料粉の一部が、炭酸塩や酸化物の結晶相と
してガラス粉末中に残る場合も、これは前述の熱処理温
度が適当でないためであって、本発明に含まれるもので
ある。
If the raw material powder used is finer, migration and diffusion between atoms are more likely to occur, and the particle size of the primary particles is 1 μm.
The following are preferred. However, it is not necessary to take the particle size into consideration because a substance soluble in water, such as boric acid, is dissolved during mixing in a ball mill and adheres to the surface of other particles. When using a raw material with a high content of silicon oxide with a high melting point,
Heat treatment at high temperature is required. Further, the particle size of the produced glass powder tends to increase as the heat treatment temperature increases. Even when a part of the raw material powder remains in the glass powder as a crystal phase of a carbonate or an oxide, this is because the above-mentioned heat treatment temperature is not appropriate and is included in the present invention.

【0009】[0009]

【実施例】以下に、実施例に基づいて、図1に示す工程
の流れに沿って詳述する。 (実施例1)酸化物換算で表1の組成になるように、酸
化アルミニウム、酸化ケイ素、炭酸カルシウム、炭酸ス
トロンチウム、酸化鉛、炭酸ナトリウム、炭酸カリウム
の原料粉末を合計で1kgになるように秤量した。これ
らを5リットルのボールミルポットに入れて、純水を加
えて20時間ボールミル混合を行った。次にポットから
スラリーを取り出し、ステンレス製のバットに移し、乾
燥機中、120℃で水分を蒸発させた。乾燥固化した混
合粉を乳鉢で解砕した後、アルミナ製のこう鉢の中に入
れて大気中、800℃で2時間の熱処理を行った。熱処
理した粉末をθ/2θ法によりX線回折装置で回折パタ
ーンを調べたところ、図3に示すようにガラス特有のハ
ローのみが観察された。
Embodiments will be described in detail below with reference to the flow of steps shown in FIG. (Example 1) The raw material powders of aluminum oxide, silicon oxide, calcium carbonate, strontium carbonate, lead oxide, sodium carbonate, and potassium carbonate were weighed so as to have a total composition of 1 kg so as to have the composition of Table 1 in terms of oxide. did. These were placed in a 5 liter ball mill pot, pure water was added, and ball mill mixing was performed for 20 hours. Next, the slurry was taken out of the pot, transferred to a stainless steel vat, and water was evaporated at 120 ° C. in a dryer. After the dried and solidified mixed powder was crushed in a mortar, it was placed in an alumina mortar and heat-treated in the air at 800 ° C. for 2 hours. When the diffraction pattern of the heat-treated powder was examined by an X-ray diffraction apparatus by the θ / 2θ method, only halo peculiar to glass was observed as shown in FIG.

【0010】[0010]

【表1】 [Table 1]

【0011】(実施例2)酸化物換算で表2の組成にな
るように、酸化アルミニウム、酸化ケイ素、炭酸カルシ
ウム、炭酸ストロンチウム、ホウ酸の原料粉末を合計で
1kgになるように秤量した後、実施例1と同一の工程
により混合、解砕し、熱処理を行った。但し、熱処理は
850℃の温度で2時間行った。次に、熱処理した粉末
の粒径を細かくするために、粉末を5リットルのボール
ミルポットに入れて、純水を加えて20時間ボールミル
により解砕した。次にポットからスラリーを取り出し、
ステンレス製のバットに移し、乾燥機中、120℃で水
分を蒸発させた。乾燥固化した粉砕粉を乳鉢で解砕し、
解砕した粉末をθ/2θ法によりX線回折装置で回折パ
ターンを調べたところ、図4に示すようにガラス特有の
ハローのみが観察された。
(Example 2) Raw material powders of aluminum oxide, silicon oxide, calcium carbonate, strontium carbonate, and boric acid were weighed so as to have a total composition of 1 kg so as to have the composition shown in Table 2 in terms of oxide. Mixing, crushing, and heat treatment were performed in the same steps as in Example 1. However, the heat treatment was performed at a temperature of 850 ° C. for 2 hours. Next, in order to reduce the particle size of the heat-treated powder, the powder was put in a 5 liter ball mill pot, pure water was added, and the powder was crushed by a ball mill for 20 hours. Then remove the slurry from the pot,
It was transferred to a stainless steel vat and the water was evaporated at 120 ° C. in a dryer. Crush the dried and solidified powder in a mortar,
When the diffraction pattern of the crushed powder was examined by an X-ray diffractometer by a θ / 2θ method, only halo peculiar to glass was observed as shown in FIG.

【0012】[0012]

【表2】 [Table 2]

【0013】[0013]

【発明の効果】本発明によると、従来の製造方法に比べ
て、使用する炉は、通常のセラミックス製品など粉末冶
金法で用いる一般的なもので良く、最高温度も1000
℃以下で十分なため、設備コストが大幅に低減できる。
また、高価な白金坩堝も不要で、安価なアルミナこう鉢
での生産ができる。更に、粉砕工程が必須工程ではなく
なる。従って、製造コストの著しい低減が可能となる。
また、アルミナこう鉢の変更と炉の温度設定の変更のみ
でガラス材質の変更が可能であり、少量多品種にも対応
できる。
According to the present invention, as compared with the conventional manufacturing method, the furnace used may be a general one used in powder metallurgy such as ordinary ceramic products, and the maximum temperature is 1000.
Since the temperature is not higher than ℃, the equipment cost can be reduced significantly.
In addition, an expensive platinum crucible is not required, and it is possible to produce in an inexpensive alumina mortar. Furthermore, the crushing step is no longer an essential step. Therefore, the manufacturing cost can be significantly reduced.
Also, the glass material can be changed only by changing the alumina mortar and changing the temperature setting of the furnace, and it is possible to support a large variety of small quantities.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明におけるガラス粉末の製造工程を示す図
である。
FIG. 1 is a diagram showing a manufacturing process of glass powder in the present invention.

【図2】従来の技術におけるガラス粉末の製造工程を示
す図である。
FIG. 2 is a diagram showing a manufacturing process of glass powder in a conventional technique.

【図3】本発明における製造したガラス粉末のX線回折
パターン図である。
FIG. 3 is an X-ray diffraction pattern diagram of the manufactured glass powder in the present invention.

【図4】本発明における製造したガラス粉末のX線回折
パターン図である。
FIG. 4 is an X-ray diffraction pattern diagram of the manufactured glass powder in the present invention.

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭56−114837(JP,A) 特開 昭63−222039(JP,A) 米国特許3082102(US,A) (58)調査した分野(Int.Cl.7,DB名) C04B 35/00 - 35/84 C03B 8/00 C03C 10/00 ─────────────────────────────────────────────────── --Continued from the front page (56) References JP 56-114837 (JP, A) JP 63-222039 (JP, A) US Patent 3082102 (US, A) (58) Fields investigated (Int .Cl. 7 , DB name) C04B 35/00-35/84 C03B 8/00 C03C 10/00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 目標組成となるように粒径1μm以下の
ガラス原料粉末を秤量し、混合した後、前記混合粉末
を原料粉末全てが溶融する完全溶融温度未満の1000℃以
で熱処理し、ガラス粉末状のままとなすことを特徴と
するセラミックス粉末と混合して用いられるガラス粉末
の製造方法。
1. A glass raw material powder having a particle diameter of 1 μm or less is weighed so as to have a target composition and mixed, and then the mixed powder is melted at a temperature of 1000 ° C. or less below a complete melting temperature at which all the raw material powder is melted.
A method for producing glass powder, which is used by mixing with ceramics powder, which is characterized in that it is heat-treated below and remains as glass powder.
【請求項2】 前記熱処理した粉末を粉砕することを特
徴とする請求項1に記載のセラミックス粉末と混合して
用いられるガラス粉末の製造方法。
2. Mixing with the ceramic powder according to claim 1 , characterized in that the heat-treated powder is crushed.
Method for producing glass powder used .
JP08096795A 1995-04-06 1995-04-06 Method for producing glass powder used by mixing with ceramic powder Expired - Lifetime JP3369781B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP08096795A JP3369781B2 (en) 1995-04-06 1995-04-06 Method for producing glass powder used by mixing with ceramic powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP08096795A JP3369781B2 (en) 1995-04-06 1995-04-06 Method for producing glass powder used by mixing with ceramic powder

Publications (2)

Publication Number Publication Date
JPH08277124A JPH08277124A (en) 1996-10-22
JP3369781B2 true JP3369781B2 (en) 2003-01-20

Family

ID=13733292

Family Applications (1)

Application Number Title Priority Date Filing Date
JP08096795A Expired - Lifetime JP3369781B2 (en) 1995-04-06 1995-04-06 Method for producing glass powder used by mixing with ceramic powder

Country Status (1)

Country Link
JP (1) JP3369781B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102992632B (en) * 2012-11-10 2015-01-07 江苏瑞德新能源科技有限公司 Lead-free glass powder for aluminium paste of solar cell

Also Published As

Publication number Publication date
JPH08277124A (en) 1996-10-22

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