JP2008290922A - Apparatus for producing glass beads - Google Patents

Apparatus for producing glass beads Download PDF

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JP2008290922A
JP2008290922A JP2007140136A JP2007140136A JP2008290922A JP 2008290922 A JP2008290922 A JP 2008290922A JP 2007140136 A JP2007140136 A JP 2007140136A JP 2007140136 A JP2007140136 A JP 2007140136A JP 2008290922 A JP2008290922 A JP 2008290922A
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glass
melting furnace
downward
oxygen burner
fluid
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Koji Matsui
宏司 松井
Tatsuya Okamoto
達哉 岡本
Shingo Yamada
真悟 山田
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Daido Steel Co Ltd
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Daido Steel Co Ltd
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<P>PROBLEM TO BE SOLVED: To provide an apparatus capable of producing small-lots of various types of glass beads with good energy efficiency and in a short time by a direct process. <P>SOLUTION: This apparatus comprises a glass melting furnace, fluid injection nozzles for injecting a fluid to a glass melt falling under self weight from an outflow port of the glass melting furnace, and a chamber provided surrounding the outflow port and the fluid injection nozzles. The glass melting furnace has an oxygen burner attached downward to the ceiling wall, and raw materials for glass and auxiliary materials are supplied to the glass melting furnace by gas conveyance. The oxygen burner is ignited downward, and raw materials for glass and auxiliary materials are supplied downward into the flame for melting. The resulting glass melt is temporarily stored in the bottom section of the furnace, and it is allowed to fall under self weight from the outflow port as it is. The glass melt falling under self weight is dispersed by injecting a high-speed fluid from the fluid injection nozzles. The dispersed glass particles are made spherical by the surface tension thereof and cooled, and the resulting glass beads are collected in the chamber. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明はガラスビーズの製造装置に関し、更に詳しくは天井壁に特定の酸素バーナを下向きで取付けた小型のガラス溶解炉を備え、所謂小ロット多品種のガラスビーズをエネルギ効率良く且つ短時間で製造することができる装置に関する。   The present invention relates to a glass bead manufacturing apparatus, and more specifically, a small glass melting furnace having a specific oxygen burner mounted downward on a ceiling wall, so-called small lot, multi-type glass beads can be manufactured in an energy efficient and short time. It relates to a device that can do.

従来、ガラスビーズの製造装置として、直接法によるものと、間接法によるものとが知られている。直接法によるガラスビーズの製造装置は、ガラス溶解炉を用いてガラス原料及び副原料(以下これらをガラス原料等という)からガラス溶解物を生成させ、このガラス溶解物から直接にガラスビーズを製造する装置である(例えば特許文献1参照)。また間接法によるガラスビーズの製造装置は、ガラス溶解炉を用いてガラス原料等からガラス溶解物を生成させ、このガラス溶解物から一旦ガラス粒子やガラスロッド等を製造した後、かかるガラス粒子やガラスロッド等から、これらを再加熱したり、またこれらに機械的な力を加えて、ガラスビーズを製造する装置である(例えば特許文献2及び3参照)。   Conventionally, as a glass bead manufacturing apparatus, a direct method and an indirect method are known. An apparatus for producing glass beads by a direct method uses a glass melting furnace to produce a glass melt from a glass raw material and an auxiliary raw material (hereinafter referred to as glass raw materials) and directly produces glass beads from the glass melt. Device (see, for example, Patent Document 1). In addition, the glass bead manufacturing apparatus using the indirect method generates a glass melt from a glass raw material using a glass melting furnace, and once the glass particles or glass rods are manufactured from the glass melt, the glass particles or glass This is an apparatus for manufacturing glass beads by reheating these from a rod or the like or applying mechanical force to them (see, for example, Patent Documents 2 and 3).

直説法によるガラスビーズの製造装置は、間接法によるガラスビーズの製造装置に比べて、手間がかからず、効率的にガラスビーズを製造できるという利点がある。しかし、従来のガラスビーズの製造装置は、それが直接法によるものであっても、ガラス溶解炉として、炉内上流部に溶解ゾーンが形成され、また炉内中流部から下流部にかけて清澄ゾーン(ガス抜きゾーン)が形成された相当に長大なものを用い、その最上流部から炉内に投入したガラス原料等を、該ガラス溶解炉の側壁に取付けたバーナの燃焼による炉内輻射を利用して溶解するため、1)バーナとして酸素バーナを燃焼させる場合であっても、エネルギ効率が悪い、2)炉内に投入するガラス原料等には融点の異なる様々なものが含まれており、これらのなかで融点の低いものは溶解が早いが、融点の高いものは溶解が遅いので、全体としての均質溶解が難しく、均質溶解にかかる時間が長い、3)ガラス溶解炉の炉内に生成するガラス溶解物の上部に未溶解のガラス原料等の低温物が存在するため、ガラス溶解物中に発生するガスが抜け難く、ガス抜きにかかる時間が長い、という問題があり、またかかる問題に起因し、結果としてガラス溶解炉が長大なものとなって、炉内のガラス溶解物の入れ替えが誠に厄介であるため、4)小ロット多品種のガラスビーズの製造に著しく不向きという問題がある。
特開昭52−42512号公報 特開2000−119028 特開2004−224679
Compared to the glass bead manufacturing apparatus using the indirect method, the glass bead manufacturing apparatus using the direct method has the advantage of being able to manufacture glass beads efficiently without taking time and effort. However, even if the conventional glass bead manufacturing apparatus is based on the direct method, a melting zone is formed in the upstream part of the furnace as a glass melting furnace, and the clarification zone (from the middle part in the furnace to the downstream part) Using a considerably long one with a degassing zone), the glass raw material charged into the furnace from the uppermost stream part is used in the furnace radiation by burning of the burner attached to the side wall of the glass melting furnace. 1) Poor energy efficiency even when oxygen burner is burned as the burner. 2) Glass materials to be put into the furnace include various materials with different melting points. Among them, those having a low melting point dissolve quickly, but those having a high melting point dissolve slowly, so that homogeneous melting as a whole is difficult and takes a long time for homogeneous melting. 3) Generated in a glass melting furnace. Gala Due to the presence of undissolved glass raw materials at the top of the melt, there is a problem that the gas generated in the glass melt is difficult to escape and the time required for degassing is long. As a result, the glass melting furnace becomes long, and replacement of the glass melt in the furnace is extremely troublesome. 4) There is a problem that the glass melting furnace is extremely unsuitable for the production of small lots of various types of glass beads.
JP 52-42512 A JP 2000-119028 A JP 2004-224679 A

本発明が解決しようとする課題は、直接法により小ロット多品種のガラスビーズをエネルギ効率良く且つ短時間で製造することができる装置を提供する処にある。   The problem to be solved by the present invention is to provide an apparatus capable of producing glass beads of a large variety of small lots in an energy efficient manner in a short time by a direct method.

前記の課題を解決する本発明は、ガラス溶解炉と、該ガラス溶解炉の流出口から自重落下する途中のガラス溶解物を臨んで設けられた流体噴射ノズルと、該流出口及び該流体噴射ノズルを囲んで設けられたチャンバとを備え、該ガラス溶解炉は天井壁に下向きで取付けられた酸素バーナを有し、該酸素バーナには酸素濃度90容量%以上の支燃ガスが供給され、またガラス原料及び副原料が気体搬送により供給されるようになっていて、該酸素バーナを下向きで燃焼させると共にガラス原料及び副原料をその火炎中に下向きで供給して溶解し、生成したガラス溶解物を炉内底部に一時的に貯留して、そのまま該流出口から自重落下させつつ、自重落下する途中のガラス溶解物に該流体噴射ノズルから高速流体を噴射して該ガラス溶解物を分散させ、分散させたガラス粒子をその表面張力により球状化すると共に冷却して、生成したガラスビーズを該チャンバで捕集するようにして成ることを特徴とするガラスビーズの製造装置に係る。   The present invention that solves the above problems includes a glass melting furnace, a fluid injection nozzle provided facing a glass melt that falls by its own weight from an outlet of the glass melting furnace, the outlet, and the fluid injection nozzle The glass melting furnace has an oxygen burner mounted downward on the ceiling wall, and the oxygen burner is supplied with a combustion-supporting gas having an oxygen concentration of 90% by volume or more. Glass raw material and auxiliary raw material are supplied by gas conveyance, and the oxygen burner is burned downward, and the glass raw material and auxiliary raw material are supplied downward into the flame and melted to form a glass melt. Is temporarily stored in the bottom of the furnace, and the glass melt is dispersed by spraying a high-speed fluid from the fluid jet nozzle onto the glass melt that is falling by its own weight while dropping itself from the outlet. Thereby, the glass particles dispersed by cooling with spheroidized by the surface tension thereof, according the generated glass beads manufacturing apparatus for a glass bead, characterized by comprising as to collect in the chamber.

本発明に係るガラスビーズの製造装置は、ガラス溶解炉と、このガラス溶解炉の流出口から自重落下する途中のガラス溶解物を臨んで設けられた流体噴射ノズルと、これらの流出口及び流体噴射ノズルを囲んで設けられたチャンバとを備えている。本発明に係るガラスビーズの製造装置において、ガラス溶解炉は、天井壁に下向きで取付けられた酸素バーナを有している。酸素バーナには酸素濃度90容量%以上の支燃ガスが供給されるようになっており、またガラス原料等が、通常はガラス原料及び副原料を混合した粉粒状のガラス原料等が気体搬送により供給されるようになっていて、この酸素バーナを下向きで燃焼させるときにガラス原料等をその火炎中に下向きで供給して溶解するようになっている。かかる酸素バーナそれ自体としては、公知のものを転用でき、例えば特開平8−312938号公報、特開2000−55340号公報及び特開2000−103656号公報等に記載されているような酸素バーナを転用できる。これらの酸素バーナは、先端部におけるノズル構造が、中心部から外周部に向かい、例えば燃料供給ノズル、一次支燃ガス供給ノズル、被処理物(ガラス原料等)供給ノズル及び二次支燃ガス供給ノズルのように、複数の供給ノズルが同心円状に配列されたものからなっている。   An apparatus for producing glass beads according to the present invention includes a glass melting furnace, a fluid injection nozzle provided facing a glass melt in the middle of dropping from the outlet of the glass melting furnace, and the outlet and fluid injection. And a chamber provided around the nozzle. In the glass bead manufacturing apparatus according to the present invention, the glass melting furnace has an oxygen burner attached downward to the ceiling wall. The oxygen burner is supplied with a combustion support gas having an oxygen concentration of 90% by volume or more, and the glass raw material is usually a granular glass raw material mixed with a glass raw material and an auxiliary raw material by gas conveyance. When the oxygen burner is burned downward, glass raw materials and the like are supplied downward into the flame and melted. As such an oxygen burner itself, a known one can be used. For example, an oxygen burner described in JP-A-8-312938, JP-A-2000-55340, JP-A-2000-103656, and the like can be used. Can be diverted. In these oxygen burners, the nozzle structure at the tip is directed from the center to the outer periphery, for example, a fuel supply nozzle, a primary combustion gas supply nozzle, an object to be treated (glass raw material etc.) supply nozzle, and a secondary combustion gas supply Like a nozzle, it consists of a plurality of supply nozzles arranged concentrically.

前記のような酸素バーナをガラス溶解炉の天井壁に下向きで取付け、これに酸素濃度90容量%以上の支燃ガスを供給して下向きで燃焼させると、火炎それ自体の温度が高くなるだけでなく、その火炎は炉内底部に一時的に貯留されるガラス溶解物の湯面をも加熱する。かかる火炎中にガラス原料等を下向きで供給すると、該ガラス原料等は極めて短時間で溶解する。しかもこのとき、下向きで燃焼する高温の火炎中に下向きで供給したガラス原料等の水分は一気に蒸発し、炭酸化合物の形態をとるものは分解してガスを放出するので、炉内底部に一時的に貯留されるガラス溶解物中でのガス発生量は著しく低くなる。その上、かかるガラス溶解物は一時的ではあっても炉内底部に貯留され、ここで均質化とガス抜きが促されるので、従来のガラス溶解炉のように清澄ゾーン(ガス抜きゾーン)を経由するまでもなく、そのまま流出口から自重落下させても、それからガラスビーズを直接に製造するのに何ら支障はない。直接法により小ロット多品種のガラスビーズをエネルギ効率良く且つ短時間で製造することができるのである。   If the above-mentioned oxygen burner is mounted downward on the ceiling wall of the glass melting furnace and supplied with a supporting gas having an oxygen concentration of 90% by volume or more and burned downward, the temperature of the flame itself will only increase. The flame also heats the molten metal surface temporarily stored in the bottom of the furnace. When glass raw material or the like is supplied downward in such a flame, the glass raw material or the like dissolves in a very short time. In addition, at this time, moisture such as glass raw material supplied downward in a high-temperature flame that burns downward evaporates all at once, and those in the form of carbonate compounds decompose and release gas, so they are temporarily released at the bottom of the furnace. The amount of gas generated in the glass melt stored in is significantly reduced. In addition, such glass melts are stored at the bottom of the furnace, even temporarily, where homogenization and degassing are encouraged, so they pass through the refining zone (degassing zone) as in conventional glass melting furnaces. Needless to say, even if the glass beads are directly dropped from the outlet, there is no problem in directly manufacturing the glass beads. By the direct method, glass lots of various types of small lots can be produced in an energy efficient manner in a short time.

前記した酸素バーナには昇降手段を設け、該昇降手段の作動によりそれらの先端部とガラス溶解炉の炉内底部に一時的に貯留されるガラス溶解物の湯面との間の距離を可変となるようにするのが好ましい。酸素バーナの燃焼量を調節するだけでなく、酸素バーナの先端部と炉内底部のガラス溶解物の湯面との間の距離をも変えることによって、炉内底部のガラス溶解物、なかでもその湯面の加熱をより自在に制御できるようにするのである。酸素バーナの燃焼量を調節すると、それらの火炎長さが変わり、火炎の先端部と炉内底部のガラス溶解物の湯面との間の距離が変わることが多いが、この距離が適正でない場合は、かかる距離を前記の昇降手段により適正に制御できる。   The above-mentioned oxygen burner is provided with elevating means, and by operating the elevating means, the distance between the tip portion thereof and the molten metal surface of the glass melt temporarily stored in the bottom of the glass melting furnace is variable. It is preferable to do so. In addition to adjusting the amount of combustion of the oxygen burner, by changing the distance between the tip of the oxygen burner and the molten metal surface of the glass melt at the bottom of the furnace, the glass melt at the bottom of the furnace, especially its The heating of the hot water surface can be controlled more freely. Adjusting the amount of combustion of the oxygen burners changes their flame length and often changes the distance between the flame front and the glass melt surface at the bottom of the furnace. Can properly control the distance by the lifting means.

ガラス溶解炉から生成したガラス溶解物を自重落下させるための流出口は、通常は該ガラス溶解炉の炉底壁(炉床壁)に、好ましくはその中央部に開設するが、炉側壁の下部に開設することもできる。本発明に係るガラスビーズの製造装置において、流体噴射ノズルは、前記のような流出口から自重落下する途中のガラス溶解物を臨んで設けられている。かかる流体噴射ノズルは、自重落下する途中のガラス溶解物を挟んで又は囲んで斜め下向きに二つ以上設けるのが好ましく、これらの流体噴射ノズルから高速流体を自重落下する途中のガラス溶解物を焦点として噴射するようにするのがより好ましい。流体噴射ノズルから噴射する高速流体としては、高速ガスが好ましいが、なかでも高速の空気又は不活性ガスがより好ましい。   The outlet for dropping the glass melt generated from the glass melting furnace by its own weight is usually opened at the bottom wall (hearth wall) of the glass melting furnace, preferably at the center thereof, but at the bottom of the side wall of the furnace Can also be opened. In the glass bead manufacturing apparatus according to the present invention, the fluid ejecting nozzle is provided to face the glass melt that falls by its own weight from the outlet as described above. It is preferable that two or more such fluid injection nozzles are provided obliquely downward with sandwiching or enclosing the glass melt in the middle of falling by its own weight, and focus the glass melt in the middle of dropping the high-speed fluid from these fluid jet nozzles. It is more preferable to inject as As the high-speed fluid ejected from the fluid ejection nozzle, high-speed gas is preferable, but high-speed air or inert gas is more preferable.

本発明に係るガラスビーズの製造装置において、チャンバは前記したような流出口及び流体噴射ノズルを囲んで設けられている。ガラス溶解炉の天井壁に下向きで取付けた酸素バーナを下向きで燃焼させると共にガラス原料等をその火炎中に下向きで供給して溶解し、生成したガラス溶解物を炉内底部に一時的に貯留して、そのまま流出口から自重落下させつつ、自重落下する途中のガラス溶解物に流体噴射ノズルから高速流体を噴射して該ガラス溶解物を分散させ、分散させたガラス粒子をその表面張力により球状化すると共に冷却して、生成したガラスビーズをチャンバで捕集するようになっているのである。   In the glass bead manufacturing apparatus according to the present invention, the chamber is provided so as to surround the outlet and the fluid ejection nozzle as described above. An oxygen burner attached downward on the ceiling wall of the glass melting furnace is burned downward and glass raw materials are supplied downward into the flame to melt, and the generated glass melt is temporarily stored at the bottom of the furnace. The glass melt is sprayed from the fluid injection nozzle to the glass melt that is falling by its own weight, and the glass melt is dispersed, and the dispersed glass particles are spheroidized by the surface tension. Then, it cools and collects the generated glass beads in the chamber.

本発明に係るガラスビーズの製造装置によると、直接法により小ロット多品種のガラスビーズをエネルギ効率良く且つ短時間で製造することができるという効果がある。   According to the glass bead manufacturing apparatus of the present invention, there is an effect that it is possible to manufacture a small lot of various types of glass beads in an energy efficient and short time by a direct method.

図1は本発明に係るガラスビーズの製造装置を一部縦断面で略示する全体図である。図示したガラスビーズの製造装置は、ガラス溶解炉11と、ガラス溶解炉11の流出口12から自重落下する途中のガラス溶解物Bを臨んで設けられた流体噴射ノズル51,52と、流出口12及び流体噴射ノズル51,52を囲んで設けられたチャンバ61とを備えている。ガラス溶解炉11は、横断面がほぼ正方形で、全体としてはやや縦長の、外観が直方体様を呈しており、その天井壁に酸素バーナ21が下向きで取付けられていて、酸素バーナ21が直下に臨む炉内底部に生成したガラス溶解物Aが一時的に貯留されるようになっている。酸素バーナ21はシリンダ機構22を介して天井壁に取付けられており、昇降可能となっていて、その先端部と炉内底部のガラス溶解物Aの湯面との間の距離が可変となっている。   FIG. 1 is an overall view schematically showing in part a longitudinal section of a glass bead manufacturing apparatus according to the present invention. The glass bead manufacturing apparatus shown in the figure includes a glass melting furnace 11, fluid jet nozzles 51 and 52 provided facing a glass melt B in the middle of dropping from its outlet 12 of the glass melting furnace 11, and an outlet 12. And a chamber 61 provided to surround the fluid ejection nozzles 51 and 52. The glass melting furnace 11 has a substantially square cross section, and is a little vertically long as a whole, and has a rectangular parallelepiped appearance. An oxygen burner 21 is attached downward on the ceiling wall, and the oxygen burner 21 is directly below. The melted glass A produced at the bottom of the furnace facing is temporarily stored. The oxygen burner 21 is attached to the ceiling wall via the cylinder mechanism 22 and can be moved up and down. The distance between the tip of the glass burner 21 and the molten metal surface of the glass melt A at the bottom of the furnace is variable. Yes.

酸素バーナ21は前記したような複数の供給ノズルが同心円状に配列されたものからなっている。かかる酸素バーナ21には吸着式酸素発生装置31から燃焼制御ユニット32を介し酸素濃度90容量%以上の支燃ガスが供給されるようになっており、また燃料タンク33から燃焼制御ユニット32を介し燃料ガスが供給されるようになっている。更に酸素バーナ21には粉粒状のガラス原料等が気体搬送で供給されるように気体搬送系41が接続されている。気体搬送系41の上流側にはドライヤ付きコンプレッサ42が接続されており、その途中にガラス原料等供給系43が接続されている。ガラス原料等供給系43は、ガラス原料等貯留用のホッパ44、ホッパ44に接続された定量切出装置45、定量切出装置45に接続された振動篩46、振動篩46に接続された定量供給装置47を備え、また振動篩46で篩分けられた粗大物を破砕して振動篩46の上流側に戻す破砕機48を備えている。ホッパ44、定量切出装置45、振動篩46及び定量供給装置47を経由し、また必要に応じ破砕機48をも経由してガラス原料等供給系43から気体搬送系41へ粉粒状のガラス原料等を定量供給しつつ、更に酸素バーナ21へと供給するようになっている。図示したガラスビーズの製造装置では、ガラス溶解炉11の天井壁に下向きで取付けた酸素バーナ21へ燃料ガス及び酸素濃度90容量%以上の支燃ガスを供給して下向きで燃焼させ、その火炎中に粉粒状のガラス原料等を下向きで供給して溶解するようになっている。   The oxygen burner 21 is composed of a plurality of supply nozzles arranged concentrically as described above. The oxygen burner 21 is supplied with combustion-supporting gas having an oxygen concentration of 90% by volume or more from the adsorption-type oxygen generator 31 via the combustion control unit 32, and from the fuel tank 33 via the combustion control unit 32. Fuel gas is supplied. Further, a gas conveyance system 41 is connected to the oxygen burner 21 so that powdery glass raw materials and the like are supplied by gas conveyance. A compressor 42 with a dryer is connected to the upstream side of the gas transport system 41, and a glass raw material supply system 43 is connected in the middle thereof. The glass raw material supply system 43 includes a glass raw material storage hopper 44, a quantitative cutting device 45 connected to the hopper 44, a vibrating sieve 46 connected to the quantitative cutting device 45, and a fixed quantity connected to the vibrating sieve 46. A crusher 48 is provided that includes a supply device 47 and crushes the coarse material sieved by the vibrating sieve 46 and returns it to the upstream side of the vibrating sieve 46. Powdered glass raw material from the glass raw material supply system 43 to the gas conveying system 41 via the hopper 44, the quantitative cutting device 45, the vibrating sieve 46 and the quantitative supply device 47, and also via the crusher 48 as necessary. Etc. are supplied to the oxygen burner 21 while being supplied in a fixed quantity. In the glass bead manufacturing apparatus shown in the figure, a fuel gas and a supporting gas having an oxygen concentration of 90% by volume or more are supplied to the oxygen burner 21 mounted downward on the ceiling wall of the glass melting furnace 11 and burned downward. A powdery glass raw material or the like is supplied downward and melted.

ガラス溶解炉11から生成したガラス溶解物Aを自重落下させるための流出口12は、ガラス溶解炉11の炉底壁の中央部に開設されている。また流体噴射ノズル51,52は、流出口12から自重落下する途中のガラス溶解物Bを両側から挟む対称位置にて斜め下向きに二つ設けられており、これらの流体噴射ノズル51,52から高速流体としての高速空気を自重落下する途中のガラス溶解物Bを焦点Fとして噴射するようになっている。そしてチャンバ61は前記したような流出口12及び流体噴射ノズル51,52を囲んで設けられている。   An outlet 12 for dropping the glass melt A generated from the glass melting furnace 11 under its own weight is established at the center of the bottom wall of the glass melting furnace 11. Further, two fluid ejection nozzles 51 and 52 are provided obliquely downward at symmetrical positions sandwiching the glass melt B in the middle of falling from the outlet 12 from both sides. Glass melt B in the midst of dropping its own high-speed air as a fluid is jetted as a focal point F. The chamber 61 is provided so as to surround the outlet 12 and the fluid ejection nozzles 51 and 52 as described above.

図示した本発明に係るガラスビーズの製造装置では、ガラス溶解炉11の天井壁に下向きで取付けた酸素バーナ21を下向きで燃焼させると共にガラス原料等をその火炎中に下向きで供給して溶解し、生成したガラス溶解物Aを炉内底部に一時的に貯留して、そのまま流出口12から自重落下させつつ、自重落下する途中のガラス溶解物Bに流体噴射ノズル51,52から高速空気を噴射してガラス溶解物を分散させ、分散させたガラス粒子をその表面張力により球状化すると共に冷却して、生成したガラスビーズCをチャンバ61で捕集するようになっているのである。   In the illustrated apparatus for producing glass beads according to the present invention, the oxygen burner 21 attached downward to the ceiling wall of the glass melting furnace 11 is burned downward and the glass raw material is supplied downward into the flame to be melted. The generated glass melt A is temporarily stored in the bottom of the furnace, and the high speed air is sprayed from the fluid jet nozzles 51 and 52 to the glass melt B in the midst of falling by its own weight while dropping itself from the outlet 12 as it is. Then, the glass melt is dispersed, and the dispersed glass particles are spheroidized by the surface tension and cooled, and the generated glass beads C are collected in the chamber 61.

本発明に係るガラスビーズの製造装置を一部縦断面で略示する全体図。BRIEF DESCRIPTION OF THE DRAWINGS FIG.

符号の説明Explanation of symbols

11 ガラス溶解炉
12 流出口
21 酸素バーナ
22 シリンダ機構
31 吸着式酸素発生装置
33 燃料タンク
41 気体搬送系
43 ガラス原料等供給系
44 ホッパ
45 定量切出装置
46 振動篩
47 定量供給装置
51,52 流体噴射ノズル
61 チャンバ
DESCRIPTION OF SYMBOLS 11 Glass melting furnace 12 Outlet 21 Oxygen burner 22 Cylinder mechanism 31 Adsorption-type oxygen generator 33 Fuel tank 41 Gas conveyance system 43 Glass raw material supply system 44 Hopper 45 Fixed amount cutting device 46 Vibrating sieve 47 Fixed supply device 51, 52 Fluid Injection nozzle 61 chamber

Claims (4)

ガラス溶解炉と、該ガラス溶解炉の流出口から自重落下する途中のガラス溶解物を臨んで設けられた流体噴射ノズルと、該流出口及び該流体噴射ノズルを囲んで設けられたチャンバとを備え、該ガラス溶解炉は天井壁に下向きで取付けられた酸素バーナを有し、該酸素バーナには酸素濃度90容量%以上の支燃ガスが供給され、またガラス原料及び副原料が気体搬送により供給されるようになっていて、該酸素バーナを下向きで燃焼させると共にガラス原料及び副原料をその火炎中に下向きで供給して溶解し、生成したガラス溶解物を炉内底部に一時的に貯留して、そのまま該流出口から自重落下させつつ、自重落下する途中のガラス溶解物に該流体噴射ノズルから高速流体を噴射して該ガラス溶解物を分散させ、分散させたガラス粒子をその表面張力により球状化すると共に冷却して、生成したガラスビーズを該チャンバで捕集するようにして成ることを特徴とするガラスビーズの製造装置。   A glass melting furnace, a fluid injection nozzle provided facing a glass melt in the middle of falling from the outlet of the glass melting furnace, and a chamber provided surrounding the outlet and the fluid injection nozzle The glass melting furnace has an oxygen burner mounted downward on the ceiling wall. The oxygen burner is supplied with a combustion supporting gas having an oxygen concentration of 90% by volume or more, and glass raw materials and auxiliary raw materials are supplied by gas conveyance. The oxygen burner is burned downward, and the glass raw material and auxiliary raw material are supplied downward into the flame and melted, and the generated glass melt is temporarily stored in the bottom of the furnace. Then, while dropping the weight of the glass from the outlet as it is, a high-speed fluid is sprayed from the fluid jet nozzle onto the glass melt that is falling by its own weight to disperse the glass melt, and the dispersed glass particles are dispersed. It cooled with spheroidizing due to surface tension, the manufacturing apparatus of glass beads of glass beads, characterized by comprising as to collect in the chamber generated. 酸素バーナに昇降手段が設けられており、該昇降手段の作動により該酸素バーナの先端部とガラス溶解炉の炉内底部に一時的に貯留されるガラス溶解物の湯面との間の距離が可変となるようにした請求項1記載のガラスビーズの製造装置。   The oxygen burner is provided with elevating means, and the distance between the tip of the oxygen burner and the molten metal surface of the glass melt temporarily stored in the bottom of the glass melting furnace by the operation of the elevating means is 2. The apparatus for producing glass beads according to claim 1, wherein the apparatus is variable. 流体噴射ノズルが斜め下向きに二つ以上設けられており、これらから高速流体を自重落下する途中のガラス溶解物を焦点として噴射するようにした請求項1又は2記載のガラスビーズの製造装置。   The apparatus for producing glass beads according to claim 1 or 2, wherein two or more fluid injection nozzles are provided obliquely downward, and a high-speed fluid is sprayed from a glass melt on its way as a focal point. 高速流体が高速ガスである請求項1〜3のいずれか一つの項記載のガラスビーズの製造装置。   The apparatus for producing glass beads according to any one of claims 1 to 3, wherein the high-speed fluid is a high-speed gas.
JP2007140136A 2007-05-28 2007-05-28 Apparatus for producing glass beads Pending JP2008290922A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012096942A (en) * 2010-10-29 2012-05-24 Asahi Glass Co Ltd In-flight melting burner, melting method of glass raw material, method of producing molten glass, method of producing glass bead, method of manufacturing glass product, in-flight melting device and device for manufacturing glass product
CN104860535A (en) * 2015-05-05 2015-08-26 江油市明瑞反光材料科技有限公司 Production process of large sizes and high refraction of glass beads

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5242512A (en) * 1975-09-30 1977-04-02 Nippon Electric Glass Co Method of production of glass bead
JPH08312938A (en) * 1995-05-18 1996-11-26 Daido Steel Co Ltd Fusion-treatment of incinerated fly ash

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5242512A (en) * 1975-09-30 1977-04-02 Nippon Electric Glass Co Method of production of glass bead
JPH08312938A (en) * 1995-05-18 1996-11-26 Daido Steel Co Ltd Fusion-treatment of incinerated fly ash

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012096942A (en) * 2010-10-29 2012-05-24 Asahi Glass Co Ltd In-flight melting burner, melting method of glass raw material, method of producing molten glass, method of producing glass bead, method of manufacturing glass product, in-flight melting device and device for manufacturing glass product
CN104860535A (en) * 2015-05-05 2015-08-26 江油市明瑞反光材料科技有限公司 Production process of large sizes and high refraction of glass beads

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