JPH0143690B2 - - Google Patents
Info
- Publication number
- JPH0143690B2 JPH0143690B2 JP681984A JP681984A JPH0143690B2 JP H0143690 B2 JPH0143690 B2 JP H0143690B2 JP 681984 A JP681984 A JP 681984A JP 681984 A JP681984 A JP 681984A JP H0143690 B2 JPH0143690 B2 JP H0143690B2
- Authority
- JP
- Japan
- Prior art keywords
- melt
- glass
- orifice
- hollow spheres
- expanding
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/10—Forming beads
- C03B19/107—Forming hollow beads
- C03B19/1075—Forming hollow beads by blowing, pressing, centrifuging, rolling or dripping
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
Description
【発明の詳細な説明】
この発明は、ガラス中空球体の製造方法及び製
造装置に関する。さらに詳しくは任意の球径の薄
肉のガラス中空球体が連続的にかつ均一径で得ら
れる中空球体の製造方法及び製造装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for manufacturing glass hollow spheres. More specifically, the present invention relates to a method and apparatus for manufacturing hollow spheres that can continuously and uniformly obtain thin-walled glass hollow spheres of any spherical diameter.
従来、中空球体の製造方法としては、ことに微
小中空球体の分野において種々提案されており、
溶融体の流れに高速のガスを噴射し吹き飛ばして
球殻体を形成させる方法、揮発性成分や発泡剤を
含有させた後加熱して球殻体を形成させる方法、
芯材を用い後で芯材を除去する方法等が知られて
いる。 Conventionally, various methods for manufacturing hollow spheres have been proposed, particularly in the field of micro hollow spheres.
A method in which a spherical shell is formed by injecting and blowing a high-speed gas into a flow of a melt; a method in which a volatile component or a foaming agent is added and then heated to form a spherical shell;
A method is known in which a core material is used and the core material is later removed.
この発明は、これらの従来の方法とは全く異な
る新規な中空球体の製造方法と提供するものであ
る。この発明の発明者らは、ガラス中空球体をガ
ラス溶融体に気体を吹き込んで風船状に膨張させ
て作製することに想着し種々の実験を試みた。ま
ず、第1図に示すように輪状口7よりガラス溶融
体1をチユーブ状に懸垂しつつその内部に矢印の
ごとく気体2を吹き込んで風船状の溶融体3とす
ると共にその外周より矢印のごとく気流5を吹き
込んで溶融体3を寸断させることにより中空球体
6を作製することを種々条件を変えて行なつた。
しかしこの方法においては、ガラス中空球体は得
られるが、気流5の乱れによつて溶融体3が搖れ
て中空球体の球径や形状が不安定になる恐れがあ
り発生個数も比較的小なく、また中空球体もその
直径が常に輪状口7よりも大きいものしか得られ
ずそれにより設計の自由度が阻害されるという問
題があつた。 The present invention provides a novel method for manufacturing hollow spheres that is completely different from these conventional methods. The inventors of this invention came up with the idea of producing a glass hollow sphere by blowing gas into a glass melt to expand it into a balloon shape, and tried various experiments. First, as shown in Fig. 1, a glass melt 1 is suspended in a tube shape from an annular opening 7, and gas 2 is blown into the tube as shown by the arrow to form a balloon-shaped melt 3. The hollow spheres 6 were produced by blowing the air stream 5 into pieces to shred the melt 3 under various conditions.
However, in this method, although glass hollow spheres can be obtained, there is a risk that the molten body 3 will be shaken by the turbulence of the airflow 5 and the diameter and shape of the hollow spheres will become unstable, and the number of glass hollow spheres generated is also relatively small. Further, there is a problem in that the diameter of the hollow sphere is always larger than the annular opening 7, which hinders the degree of freedom in design.
この発明の発明者らは、更に検討、研究を行な
つた結果、上記気流をオリフイスに導きこのオリ
フイスを通じて更に溶融体を膨出、寸断させるこ
とにより、任意の球径で均一径のガラス中空球体
が連続的に多数作製できる事実を見出しこの発明
に到達した。 As a result of further study and research, the inventors of the present invention found that by guiding the airflow to an orifice and further expanding and cutting the molten material through this orifice, a glass hollow sphere with a uniform diameter can be produced. This invention was achieved by discovering the fact that a large number of can be produced continuously.
かくしてこの発明によれば、ガラス溶融体に気
体を吹き込んで風船状に膨張させつつオリフイス
に近接させると共に、上記溶融体の外周に沿つて
オリフイスを通過する気流を供給することにより
風船状の溶融体の一部をオリフイスから膨出させ
つつ寸断して中空球状とし、これを固化すること
を特徴とするガラス中空球体の製造方法が提供さ
れる。 Thus, according to the present invention, by blowing gas into the glass melt to expand it into a balloon shape and bring it close to the orifice, and by supplying an airflow that passes through the orifice along the outer periphery of the melt, the balloon-shaped melt is formed. Provided is a method for producing a glass hollow sphere, which comprises blowing out a part of the glass from an orifice and cutting it into hollow spheres, which are then solidified.
以下、添付図面により、この発明の方法を具体
例を挙げて説明する。第2図は、この発明の方法
を説明する第1図相当図である。図において、ガ
ラス溶融体1を輪状口7から袋状に懸垂しつつ袋
状に懸垂しつつ気体2をその内部に吹き込んで風
船状に膨張させてオリフイス4に近接させる。同
時に風船状の溶融体3の外周に沿つてオリフイス
4を通過する気流5を供給することにより溶融体
の一部3′がオリフイス4より膨出し寸断されて
中空球体の溶融体が得られ、これを冷却固化させ
て所望のガラス中空球体6が作製される。そし
て、溶融体1、気体2及び気流5を連続的に供給
することにより、連続的にガラス中空球体6が得
られる。 Hereinafter, the method of the present invention will be explained by giving specific examples with reference to the accompanying drawings. FIG. 2 is a diagram corresponding to FIG. 1 for explaining the method of the present invention. In the figure, a glass melt 1 is suspended like a bag from an annular opening 7, and gas 2 is blown into it to expand it into a balloon shape and bring it close to an orifice 4. At the same time, by supplying an air flow 5 that passes through the orifice 4 along the outer circumference of the balloon-shaped melt 3, a part 3' of the melt bulges out from the orifice 4 and is cut into pieces to obtain a hollow spherical melt. A desired glass hollow sphere 6 is produced by cooling and solidifying. Then, by continuously supplying the melt 1, the gas 2, and the air flow 5, the glass hollow spheres 6 are continuously obtained.
この発明におけるガラス溶融体としては、気体
の吹込みにより風船状に膨張しうる粘度を有する
ガラス溶融体であればよく、その粘度としては通
常300〜5000cPが適当であり、500〜2000cPが好
ましい。また用いるガラス材料としては当該分野
で公知の種々のものが挙げられる。そしてこの発
明の方法によれば、ガラス組成の如何を問わず適
当な粘度の溶融体を用いることにより、種々の中
空球体を得ることができる。 The glass melt in this invention may be any glass melt having a viscosity that allows it to expand into a balloon shape when gas is blown into it, and its viscosity is usually 300 to 5000 cP, preferably 500 to 2000 cP. In addition, various glass materials known in the art may be used as the glass material. According to the method of the present invention, various hollow spheres can be obtained by using a melt having an appropriate viscosity regardless of the glass composition.
一方、この発明に用いる溶融体を膨張させる気
体及びオリフイスへ流出する気流としては、通常
空気が簡便であり、これ以外に不活性ガスを用い
てもよい。かような気体及び気流は通常、溶融体
を冷却固化又は粘度上昇する恐れがないように加
温しておくことが好ましい。 On the other hand, as the gas for expanding the melt used in this invention and the air flow flowing out to the orifice, air is usually convenient, and an inert gas may also be used. It is generally preferred that such gases and air streams be heated so as to prevent the melt from solidifying or increasing its viscosity upon cooling.
この発明の方法によれば、薄肉(通常、厚み
5μm〜500μm)で均一な球径(通常1mm〜15mm)
の中空球体が連続的に多数(数十〜数千個/秒)
製造できる。なお、オリフイスの口径としては風
船状の溶融体の大きさにもよるが通常、口径1〜
10mmの細孔を用いるのが適当である。通常、中空
球体の直径/オリフイス口径=0.4〜1.4の中空球
体が得られる。 According to the method of this invention, thin wall (usually thick
5μm to 500μm) and uniform ball diameter (usually 1mm to 15mm)
Continuously large number of hollow spheres (several tens to thousands of spheres/second)
Can be manufactured. The diameter of the orifice depends on the size of the balloon-shaped melt, but usually the diameter is 1 to 1.
It is appropriate to use pores of 10 mm. Usually, a hollow sphere with a diameter of hollow sphere/orifice diameter of 0.4 to 1.4 is obtained.
この発明の他の観点によれば、上記中空球体の
製造方法に好適な製造装置が提供される。すなわ
ち加熱手段を備えた溶融炉と、該溶融炉からのガ
ラス溶融体を袋状に懸垂しうる輪状口を有しかつ
溶融体膨張用の気体供給口を内設した溶融体膨出
管と、該膨出管の下方にかつ該膨出管の輪状口に
同軸に位置する溶融体寸断用オリフイスと、前記
膨出管から膨出するガラス溶融体の外周の沿つて
該オリフイスへ流出する気流の流路を構成する成
形空間、とを備えてなるガラス中空球体の製造装
置が提供される。 According to another aspect of the invention, a manufacturing apparatus suitable for the method for manufacturing hollow spheres described above is provided. That is, a melting furnace equipped with a heating means, a melt expansion tube having an annular opening capable of suspending a glass melt from the melting furnace in a bag shape, and having a gas supply port for expanding the melt inside, A melt shredding orifice located below the expansion tube and coaxial with the annular mouth of the expansion tube, and an air flow flowing out to the orifice along the outer circumference of the glass melt expanding from the expansion tube. Provided is an apparatus for manufacturing a glass hollow sphere, comprising a molding space that constitutes a flow path.
第3図により、この発明の製造装置の具体例に
ついて説明する。図において、9は、電気炉を示
し、この中に8の溶融槽があり、その中には電気
炉により溶融された、粘度500〜2000cPのガラス
溶融体4が貯留されている。溶融槽8には、気体
供給管2aがあり、溶融槽底部の位置は、V形状
になり、溶融ガラスを所望の流量で供給できるよ
う、バルブの役をはたすよう構成されてなる。 A specific example of the manufacturing apparatus of the present invention will be explained with reference to FIG. In the figure, reference numeral 9 indicates an electric furnace, in which there is a melting tank 8, in which a glass melt 4 having a viscosity of 500 to 2000 cP, which has been melted by the electric furnace, is stored. The melting tank 8 has a gas supply pipe 2a, and the bottom of the melting tank has a V-shape and is configured to function as a valve so that molten glass can be supplied at a desired flow rate.
気体供給管先端部2bは、内径2mm外径5mmを
備えて、溶融槽先端部8a(内径7mm)と同心円
にあり、その空間の輪状口7からガラス溶融体が
袋状に懸垂し気体供給管2aからの気体2によ
り、膨出する溶融体3を得る。ノズル8aの下方
には気体供給管先端部2bと同軸に位置する口径
5mmのオリフイス4が設けられている。膨出する
溶融体3をオリフイスで寸断する気流5は、気流
供給管5aから供給され、膨出する溶融体3の外
周に沿つて流れ、オリフイス4を通る。その際、
溶融体は寸断され中空球状の溶融体6が吐出され
る。なお10は、オリフイス4部の温度低下を防
ぐための電気炉である。 The gas supply pipe tip 2b has an inner diameter of 2 mm and an outer diameter of 5 mm, and is located concentrically with the melting tank tip 8a (inner diameter 7 mm), and the glass melt is suspended in a bag shape from the annular opening 7 of the space, and the gas supply pipe A bulging melt 3 is obtained by the gas 2 from 2a. An orifice 4 with a diameter of 5 mm is provided below the nozzle 8a and is located coaxially with the gas supply pipe tip 2b. The airflow 5 that cuts the expanding melt 3 at the orifice is supplied from the air flow supply pipe 5a, flows along the outer periphery of the expanding melt 3, and passes through the orifice 4. that time,
The melt is shredded and a hollow spherical melt 6 is discharged. Note that 10 is an electric furnace for preventing the temperature of the four orifices from decreasing.
また、上記装置によれば、輪状口7の内径や外
径を調整したり、オリフイス口径を調整すること
により、種々の肉厚や球径の中空球体を製造する
ことができ、溶融体の供給量、それぞれの気体の
供給量を適宜変更することによつてこれらを制御
することもできる。通常の気体供給量の条件とし
ては例えば、オリフイス口径及び輪状口内径が3
mmで溶融体供給量が1.68g/分(粘度900〜
1100cP)の場合には、気体供給装置からの気体
流量Aは約2〜20ml/秒で、気流供給装置からの
気体流量Bは、約20〜130ml/秒とするのが適当
であり、気体流量がいずれもこれ以下であると、
中空球体がオリフイス出口に多数付着して不適当
である。また、気体流量Aが20ml/秒を越えた場
合には、気体流量Bが20〜80ml/秒の範囲で非周
期的な間欠が発生しそれ以上においてもオリフイ
スからの膨出部分が微粒化して中空球体が得られ
ず不適当である。また気体流量Aが上記範囲にあ
つても、気体流量Bが上記範囲を越えると、やは
りオリフイス出口から微粒化が起り中空球体が得
られず不適当である。 Further, according to the above-mentioned apparatus, by adjusting the inner diameter and outer diameter of the annular opening 7 and adjusting the orifice diameter, hollow spheres with various wall thicknesses and spherical diameters can be manufactured, and the molten material can be supplied with various thicknesses and diameters. These can also be controlled by appropriately changing the supply amount of each gas. For example, the orifice diameter and annular mouth inner diameter are 3.
mm and the melt supply rate is 1.68 g/min (viscosity 900~
1100cP), the gas flow rate A from the gas supply device is approximately 2 to 20 ml/sec, and the gas flow rate B from the air flow supply device is approximately 20 to 130 ml/sec. are less than this,
Many hollow spheres adhere to the orifice outlet, which is inappropriate. In addition, when the gas flow rate A exceeds 20 ml/sec, non-periodic intermittent occurrence occurs when the gas flow rate B is in the range of 20 to 80 ml/sec, and even beyond that, the bulging part from the orifice becomes atomized. It is unsuitable because a hollow sphere cannot be obtained. Further, even if the gas flow rate A is within the above range, if the gas flow rate B exceeds the above range, atomization will still occur from the orifice outlet, making it impossible to obtain hollow spheres, which is inappropriate.
ただし、溶融体供給量やオリフイス口径等によ
つても気体供給量の条件は適宜変動するため上記
範囲に特に限定されることはない。通常、溶融体
膨張用の気体の流量Aを1とした場合、気流の流
量Bを20〜100とするのが適当である。 However, the conditions for the gas supply amount vary depending on the melt supply amount, orifice diameter, etc., and therefore are not particularly limited to the above range. Normally, when the flow rate A of the gas for expanding the melt is 1, it is appropriate that the flow rate B of the air flow is 20 to 100.
このようにして得られたガラス中空球体は、そ
の均一性、軽量性から、各種プラスチツク用充填
材や複合構造材セメントの軽量骨材、小型フロー
ト、断熱材、誘電材料、吸着性担体、マイクロカ
プセル等の用途に適用することができる。 Due to its uniformity and lightness, the glass hollow spheres obtained in this way can be used as fillers for various plastics, lightweight aggregates for composite structural cement, small floats, heat insulating materials, dielectric materials, adsorbent carriers, and microcapsules. It can be applied to other uses.
以上の説明から理解されるように、この発明の
製造方法や製造装置によれば、種々のガラス中空
球体を連続的に多数製造することができ、種々の
用途に有用であることが判る。 As understood from the above description, the manufacturing method and manufacturing apparatus of the present invention can continuously manufacture a large number of various glass hollow spheres, and are found to be useful for various uses.
以下、実施例によりこの発明によつて得られた
中空球体について説明する。 Hereinafter, hollow spheres obtained by the present invention will be explained with reference to Examples.
実施例 1
廃ビンガラスを、溶融槽に入れ、電気炉内で
1500℃に加熱し、粘度3000cPに設定したガラス
溶融体を第3図の装置を用いて下記の条件で中空
球体とした。Example 1 Waste bottle glass was placed in a melting tank and heated in an electric furnace.
A glass melt heated to 1500° C. and set to have a viscosity of 3000 cP was made into a hollow sphere using the apparatus shown in FIG. 3 under the following conditions.
溶融ガラス供給量 12g/分
気体吹出量 10c.c./秒
気流供給量 60c.c./秒
オリフイス口径 4mm
この時中空球体の発生個数は60個/秒で得られ
た中空球体の性状は、4〜4.5mm、膜厚約15μであ
つた。Molten glass supply rate: 12 g/min Gas blowing rate: 10 c.c./sec Air flow supply rate: 60 c.c./sec Orifice diameter: 4 mm At this time, the number of hollow spheres generated is 60/sec. The properties of the hollow spheres obtained are as follows: It was 4 to 4.5 mm, and the film thickness was about 15 μm.
実施例 2
低融点ガラスを、溶融槽に入れ、電気炉で800
℃に加熱し、粘度800cPに設定し、実施例と同様
にして中空球体を製造した。この時の中空球体の
発生個数は110個/秒でその直径は2.5〜3.0mmで
膜厚は、8μであつた。Example 2 Low melting point glass was placed in a melting tank and heated at 800 °C in an electric furnace.
℃, the viscosity was set to 800 cP, and hollow spheres were produced in the same manner as in the example. At this time, the number of hollow spheres generated was 110/second, the diameter was 2.5 to 3.0 mm, and the film thickness was 8 μm.
第1図は、この発明の製造方法を比較説明する
ための断面を含む構成説明図、第2図はこの発明
の製造方法を例示する断面を含む構成説明図、第
3図はこの発明の製造装置の一例を示す断面を含
む構成説明図である。
1……ガラス溶融体、2……気体、3……風船
状の溶融体、4……オリフイス、5……気流、6
……ガラス中空球体、7……輪状口、8……溶融
槽、9……電気炉。
FIG. 1 is a configuration explanatory diagram including a cross section for comparatively explaining the manufacturing method of the present invention, FIG. 2 is a configuration explanatory diagram including a cross section illustrating the manufacturing method of the present invention, and FIG. FIG. 2 is a configuration explanatory diagram including a cross section showing an example of the device. 1... Glass melt, 2... Gas, 3... Balloon-shaped melt, 4... Orifice, 5... Air flow, 6
... Glass hollow sphere, 7 ... Annular mouth, 8 ... Melting tank, 9 ... Electric furnace.
Claims (1)
張させつつオリフイスに近接させると共に、上記
溶融体の外周に沿つてオリフイスを通過する気流
を供給することにより風船状の溶融体の一部をオ
リフイスから膨出させつつ寸断して中空球状と
し、これを固化することを特徴とするガラス中空
球体の製造方法。 2 加熱手段を備えた溶融炉と、該溶融炉からの
ガラス溶融体を袋状に懸垂しうる輪状口を有しか
つ溶融体膨張用の気体供給口を内設した溶融体膨
出管と、該膨出管の下方にかつ該膨出管の輪状口
に同軸に位置する溶融体寸断用オリフイスと、前
記膨出管から膨出するガラス溶融体の外周の沿つ
て該オリフイスへ流出する気流の流路を構成する
成形空間、とを備えてなるガラス中空球体の製造
装置。[Scope of Claims] 1. A balloon-shaped molten body is created by blowing gas into the glass molten body to expand it into a balloon shape and bringing it close to an orifice, and supplying an air flow that passes through the orifice along the outer periphery of the molten body. A method for manufacturing a glass hollow sphere, which comprises: expanding a part of the glass from an orifice and cutting it into hollow spheres, and solidifying the hollow spheres. 2. A melting furnace equipped with a heating means, a melt expansion tube having an annular opening capable of suspending the glass melt from the melting furnace in a bag shape, and having a gas supply port for expanding the melt inside, A melt shredding orifice located below the expansion tube and coaxial with the annular mouth of the expansion tube, and an air flow flowing out to the orifice along the outer circumference of the glass melt expanding from the expansion tube. A manufacturing device for a glass hollow sphere, comprising a molding space that constitutes a flow path.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP681984A JPS60151234A (en) | 1984-01-17 | 1984-01-17 | Method and apparatus for manufacturing glass hollow spherical body |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP681984A JPS60151234A (en) | 1984-01-17 | 1984-01-17 | Method and apparatus for manufacturing glass hollow spherical body |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60151234A JPS60151234A (en) | 1985-08-09 |
| JPH0143690B2 true JPH0143690B2 (en) | 1989-09-22 |
Family
ID=11648815
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP681984A Granted JPS60151234A (en) | 1984-01-17 | 1984-01-17 | Method and apparatus for manufacturing glass hollow spherical body |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60151234A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10011513B2 (en) * | 2015-05-07 | 2018-07-03 | The United States Of America, As Represented By The Secretary Of The Navy | Apparatuses and methods for forming hollow spheres |
-
1984
- 1984-01-17 JP JP681984A patent/JPS60151234A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60151234A (en) | 1985-08-09 |
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