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JP3618966B2 - Glass outflow method and glass outflow device - Google Patents
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JP3618966B2 - Glass outflow method and glass outflow device - Google Patents

Glass outflow method and glass outflow device Download PDF

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Publication number
JP3618966B2
JP3618966B2 JP18247097A JP18247097A JP3618966B2 JP 3618966 B2 JP3618966 B2 JP 3618966B2 JP 18247097 A JP18247097 A JP 18247097A JP 18247097 A JP18247097 A JP 18247097A JP 3618966 B2 JP3618966 B2 JP 3618966B2
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Japan
Prior art keywords
melting tank
glass
outflow
liquid level
molten glass
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JP18247097A
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Japanese (ja)
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JPH1129330A (en
Inventor
裕之 久保
昌之 冨田
瑞和 余語
勇 執行
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Canon Inc
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Canon Inc
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    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B5/00Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
    • C03B5/16Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
    • C03B5/24Automatically regulating the melting process
    • C03B5/245Regulating the melt or batch level, depth or thickness
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/50Glass production, e.g. reusing waste heat during processing or shaping
    • Y02P40/57Improving the yield, e-g- reduction of reject rates

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Control Of Non-Electrical Variables (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は溶融したガラスを溶融/流出させる方法及びその装置に関する。
【0002】
【従来の技術】
ガラス材料を溶かし、溶融したガラスの溶融温度の調整、組成の均質化を行い、均質化された溶融ガラスを流出させて取り出すためのガラス溶融槽は溶融しているガラスを均質化させるために温度(粘性)管理を高い温度範囲精度で行い、かつ、溶融ガラスの容量を調整する必要がある。
【0003】
従来のガラス溶融槽の液面管理は流出したガラスの重量計測による方法、ガラスに含まれる放射線物質(γ線)の透過を検出して液面を測定する方法などがある。
【0004】
【発明が解決しようとする課題】
カメラなどの光学機器に使用するレンズは光学技術の進歩により非球面レンズを多用する製品が多くなり、また、光ピックアップ技術を用いた画像読み取り機能を備えた情報機器にも小型のレンズを組み込む構成が多くなってきた。
【0005】
また、プリンタなどの画像形成機器内にはトーリックレンズ等の複雑な形状の光学曲面を有した光学素子を多く採用する可能性がある。
【0006】
このような非球面レンズは機器の使用環境の多様化に応じて、環境変化に対する適応性に優れるガラス材料を使用する。
【0007】
ガラス材料を溶融槽内で溶融し、ガラスを流出させ、流出したガラスを次の工程で上記のレンズ形状、光学素子形状に加工する場合に、流出したガラスの流出温度(粘性)、流出容量を所定温度範囲内,及び所定の容量範囲内に流出させる必要がある。
【0008】
特に、流出した溶融ガラスを次の工程でプレス成形して光学素子形状に成形するプレス成形工程を採用する場合には流出する溶融ガラスの温度、流出容量は成形される光学素子の精度に大きな影響を及ぼす。
【0009】
溶融槽の流出部から均質化されたガラスを流出させて成形工程に移送する生産プロセスでは、流出部からの流出に応じて溶融槽の液面位置を所定範囲内に調整することが均質な溶融ガラスを得るためには必要である。
【0010】
即ち、溶融ガラスを流出する流出ノズルの液面圧力を一定にして、流出ガラスの重量精度を保つことにより成形するガラス成形品の容量を正確に制御することができる。
【0011】
本発明の課題はガラス材料を溶融して溶融ガラスを流出させる溶融槽の液面を、流出ガラスの流出に応じて調整し、溶融槽内のガラスの状態を均一条件に保てるようにしたガラスの流出方法及び装置を提案することにある。
【0012】
さらに、本発明は溶融槽からガラスを流出させて溶融槽内の溶融ガラスの容量が減少した場合に、可及的速やかに溶融槽の液面を所定位置に回復させることのできるガラス流出装置を提案する。
【0013】
【課題を解決するための手段】
本発明は、上記課題解決のために、流出部から流出する溶融ガラスを溶融する第一の溶融槽に、該第一の溶融槽の溶融ガラス液面より上位位置に保持され、ガラス材料を投入して溶融する第二の溶融槽を接続し、前記第一の溶融槽内の溶融ガラスの減少に応じて、前記第二の溶融槽の液面レベルを変位させ、第二の溶融槽内の所定液面近傍に設置した流路より、溶融ガラスをオーバーフローさせることにより前記第二の溶融槽から前記第一の溶融槽へ溶融ガラスを送り込み、前記流出部からの流出に応じた前記第一の溶融槽の液面調整を行うようにしたガラス流出方法を提案する。
【0014】
さらに、本発明は、前記第一の溶融槽の液面上限位置を検出する手段の信号に応じて前記第二の溶融槽の液面を変位させて、前記第二の溶融槽から前記第一の溶融槽へ溶融ガラスを送り込むようにしたガラス流出方法を提案する。
【0016】
又、流出部から流出する溶融ガラスを溶融する第一の溶融槽と、該第一の溶融槽の溶融ガラス液面より上位位置に接続され、ガラス材料を投入して溶融する第二の溶融槽と、前記第二の溶融槽の液面レベルを変位させ、第二の溶融槽内の所定液面近傍に設置した流路より、溶融ガラスをオーバーフローさせることにより前記第二の溶融槽から前記第一の溶融槽へ溶融ガラスを送り込み、前記流出部からの流出に応じた前記第一の溶融槽の液面調整を行うようにしたことを特徴としたガラス流出装置の提案により生産性の向上を図る。
【0019】
また、流出部を備える第一のガラス溶融槽の液面より上位位置に液面を有した第二のガラス溶融槽を設け、前記第一と第二の溶融槽を接続手段で接続し、前記第二の溶融槽の液面を変位させることにより前記接続手段を介して前記第一の溶融槽の液面の調整を行うようにしたガラス流出装置の提案により流出ガラスを次工程でプレス成形して光学素子形状に成形する生産方法に好ましい装置を提案する。
【0023】
【発明の実施の形態】
以下に図を参照して本発明の第一の実施例を説明する。
【0024】
図1は本発明を実施するガラス溶融/流出装置の要部構成図、図2は各部制御の制御ブロック図である。
【0025】
図1,2において、符号1はガラス溶融装置を示し、2は溶融装置室内、4は第一のガラス溶融槽、6は第二のガラス溶融槽である。
【0026】
前記第一のガラス溶融槽4と第二のガラス溶融槽6とはガラス流路8により接続し、前記第二のガラス溶融槽6は前記第一のガラス溶融槽4よりも上位位置に配置し、ガラス流路8により接続して第二ガラス溶融槽6内の溶融ガラスが第一溶融槽4内へ流入するように構成する。
【0027】
前記第一溶融槽4は流出ノズル4aを備えた流出槽4Aと、前記第二の溶融槽6からの溶融ガラスを受け入れて溶融ガラスの清澄作用を行う清澄槽4Bとに区分され、両槽は流通路4Cにより接続している。
【0028】
10は前記第一溶融槽4内の溶融ガラスであり、10Aは該ガラス10のガラス液面を示す。
【0029】
前記第一溶融槽4及びノズル4aの周囲には加熱手段のヒータ12及び温度検出手段(不図示)が配置されて第一溶融槽内の溶融ガラスの温度(粘性)を所定の温度範囲内に調整している。
【0030】
更に前記第二の溶融槽6及び前記ガラス流路8の周囲にも加熱手段と温度検出手段(不図示)を配置して各部のガラス溶融温度の管理を行う。
【0031】
14は流出槽4A内に設置した攪拌手段の攪拌部材であり、不図示モータにより回転駆動される。
【0032】
16は溶融装置1全体を覆い装置の機密性と断熱性を保つ遮蔽部材である。
【0033】
18はガラス材料を前記第二ガラス溶融槽6内に投入する投入口である。
【0034】
20は前記第一ガラス溶融槽4のガラス液面10Aの位置を検出するためのフロート部材であり、フロート部20A、軸部20Bを有し、軸部20Bが前記遮蔽部材16の天井部に支持部材20Cにより軸支されて外部に表出している。
【0035】
前記フロート部材20の軸部20Bの先端部は位置検出センサ手段22に接続している。
【0036】
前記位置検出センサ手段22は複数の検出位置を示すマイクロスイッチや、非接触形式の光センサ等で構成する。
【0037】
本例においては、フロート部材20Aの上限位置を示すセンサ22Aとフロート部材の下限位置を示すセンサ22Bで構成する。
【0038】
上記センサ22A,22Bは保持部材22Cにより両者が所定距離の間隔を空けて前記遮蔽部材16上に取り付けられており、該センサ22A,22Bの間に前記フロート軸部20Bの先端部に取りつけたプローブ部20Dが配置されておりフロート部20Aの上下移動に応じてプローブ部20Dがセンサ20Aまたは20Bに接触することにより該センサ20A,20Bから信号を出力して、第一溶融槽4のガラス液面10Aの位置が検出される。
【0039】
24は制御手段であり前記センサ22A,22Bからの信号を受けて後述する制御動作を行う。
【0040】
26は前記第二の溶融槽6内に入れて液面上を上下移動するプランジャである。該プランジャ26はその上部に軸部26Aを取り付け、該軸部26Aは前記遮蔽部材16を貫通し、取り付け部材28に取り付けたモータ30の回転軸30Aに固定してある。
【0041】
前記モータ30はモータ駆動手段30Aにより正逆回転及び回転速度の制御を受け、これによりプランジャ26は第一溶融槽6内を上下移動し、その結果、第二溶融槽6の液面位置が上下移動する。
【0042】
32は前記プランジャ26の上下移動位置を検出する位置検出センサ、26Bは前記軸26Aに取り付けたセンサードグである。
【0043】
該位置検出センサ32はプランジャ位置制御手段26Bに接続している。
【0044】
次に本例の作動を図3,4を更に参照して説明する。
【0045】
まず、初期状態設定のために、前記ガラス材料投入口18から溶融ガラスのガラス材料を投入して第二溶融槽6内に溶融ガラスを満たし、該第二溶融槽6内の溶融ガラスをガラス流路8を介して第一溶融槽4に送り込んで、第一溶融槽4のフロート部材20Aが図1の状態、即ち、液面検出用プローブ20Dが液面上限センサ22Aの出力を検知する位置に達する状態に設定する。
【0046】
その後、各部の温度管理と前記攪拌手段14により流出ノズルから流出する溶融ガラスが所定の溶融状態になるように調整する。
【0047】
一の溶融槽4のガラス液面が上限位置を示すセンサ22Aの信号を出力すると前記制御手段24からガラス材料投入停止の信号が出力する。
【0048】
この状態で、第二溶融槽6内のプランジャ26は、前記第一、第二溶融槽4,6内の液面上限位置に溶融ガラスが満たされている位置に設定し、プランジャ26の位置は位置検出手段(26B、32)により初期位置(フロート部材20Aの上限位置)に設定される。
【0049】
以上の設定により、流出ノズル4aからのガラス流出準備状態が完了する。
【0050】
本例においては、流出ノズル4aからのガラス流出量を 毎分3.0ccとし、流出ノズル4Aの温度を先端オリフイス部温度を1150℃、ノズル中間部温度を900℃に設定した。
【0051】
ノズル部からの流出調整はノズル温度調整を制御手段12Bにより行う。
【0052】
流出ノズル先端オリフイスの下部に不図示の溶融ガラスを受ける受け型部材を配置し、順次、溶融ガラスを流出させる。
【0053】
流出ノズル4Aからの溶融ガラスの流出にともない、第一溶融槽4内の溶融ガラスの量が減少し(図3)、ガラス液面の下降につれて、フロート部材20も下降する。
【0054】
フロート部材20Aの下降によりプローブ部材20Dも下降し、ガラス液面10Aが下限位置センサ22Bと接触すると第一溶融槽液面制御手段22Eからの信号に基ずいて、前記制御手段24からモータ駆動制御手段30Aの起動を行い、モータ30の回転によりプランジャ26の下降を開始する。
【0055】
前記プランジャ26の第二溶融槽6内への下降動作により、該プランジャ26の下降容積に応じて該第二溶融槽内のガラス液面は上昇し、第二溶融槽6内の溶融ガラスはガラス流路8を介して第一溶融槽4内へ流入する。
【0056】
それに連れて、第一溶融槽4の液面位置10Aも上昇し、プローブ部材20Dは液面上限位置センサ22Aと接触して液面の上限位置を検出し、前記第一溶融槽液面制御手段22Eからの信号によりモータ駆動制御手段30Aを介してモータ30の回転を止める。
【0057】
第一溶融槽4のガラス液面が上限位置に回復したら、次に第二溶融槽6の液面位置の回復のために、前記モータ30の回転操作によりプランジヤ26を上昇させて初期位置に戻す。(図4)
【0058】
その後、ガラス材料投入口18からガラス材料を投入し、第二溶融槽6内の溶融ガラスの容量を初期液面位置まで回復させる。
【0059】
前記プランジャ26により第一溶融槽4内に送り込まれた溶融ガラスは順次、清澄槽4B、流出槽4Aを経て均質化されて流出ノズル4aまで送られて流出操作が行われる。
【0060】
以上のように、本発明は、流出部4aから流出する溶融ガラスを溶融する第一の溶融槽4にガラス材料を投入して溶融する第二の溶融槽6を接続し、前記第二の溶融槽6の液面レベルを変位させることにより前記第二溶融槽6から前記第一溶融槽4へ溶融ガラスを送り込み、前記流出部からの流出に応じた前記第一溶融槽の液面調整を行うようにしてガラス流出部4aとガラス液面位置10Aとの距離(ガラス液面深さ)を常に一定範囲に保つことにより流出ガラスの均質性を保つことができる。
【0061】
さらに、本発明は、流出部4aを備える第一の溶融槽4の液面位置10Aより上位位置の液面を有した第二の溶融槽6を設け、前記第一の溶融槽4の液面10Aを検出する手段20Aの信号に応じて前記第二の液面を変位させて、前記第二溶融槽から前記第一の溶融槽へ溶融ガラスを送り込むようにしたことによりガラス流出部から均質な溶融ガラスを得ることができた。
【0062】
更にまた、流出部から流出する溶融ガラスを溶融する第一の溶融槽4にガラス材料を投入溶融する第二の溶融槽6を接続し、前期第二の溶融槽6内を進退移動して、前記第二の溶融槽6から前記第一の溶融槽4へ溶融ガラスを送り込む手段26,30を設け、前記送り込み手段により前記第一の溶融槽4の液面調整を行うようにしたガラス流出装置により均質性の安定したガラスを得ることができた。
【0063】
また、流出部を備える第一のガラス溶融槽の液面より上位位置に液面を有した第二のガラス溶融槽を設け、前記第一と第二の溶融槽を接続手段で接続し、前記第二の溶融槽の液面を変位させることにより前記接続手段を介して前記第一の溶融槽の液面の調整を行うようにしたガラス流出装置の提案により流出ガラスを次工程でプレス成形して光学素子形状に成形する生産方法に好ましい装置を提案することができた。
【0064】
更に、本発明は、投入したガラス材料を溶融する第一の溶融槽に、ガラス流出部を備える第二のガラス溶融槽を接続し、前記第二のガラス溶融槽内の溶融ガラスの減少に応じて、前記第二の溶融槽内の容積を調整することにより前記第一の溶融槽の溶融ガラスの容量を常に所定容量範囲内に調整することにより流出ガラスの品質の安定性を得ることができた。
【0065】
次に本発明の応用例を図5に示す、該例は前記第一実施例の第一溶融槽に第二の液面調整手段を配置することにより流出槽の液面調整の応答性の向上を図ったものである。
【0066】
図5において、図1に示す符号と同一符号は同じ機能の部品を示し、以下に追加した部品の説明をする。
【0067】
符号40は第二のプランジャであり、前記第一溶融槽4の清澄槽4B内に進退移動できるように軸部40Aが遮蔽部材を貫通し、その先端部が第二のモータ42の回転軸に接続している。
【0068】
44は前記第二プランジャ40の移動位置を検出する位置検出用センサであり、制御手段46に接続する。
【0069】
前記制御手段46は第一のプランジャ26の位置検出センサ32、第一,第二モータ30、42、前記液面検出手段22の各手段の信号線を接続している。
【0070】
図6は図5の装置の制御系ブロック図である。
【0071】
まず、第一及び第二の各プランジャ26、40を上昇位置に設定し、第二溶融槽6内にガラス材料を投入し、溶融ガラスを順次第一溶融槽に送り込んで、第一、第二溶融槽を溶融ガラスで充満させ、かつ、各槽及び流出ノズル4aの温度管理を行う。
【0072】
前記流出ノズル4aの温度調整及び、溶融槽4Aの液面が初期設定の高さ位置に設定後、溶融ガラスの流出操作を行い、成形用ガラスを順次流出させる。
【0073】
溶融槽4A内のガラスの流出に伴い、液面位置が低下し、これにより流出ノズル4aのガラスの流出圧力が変化する。
【0074】
溶融ガラスの流出に伴い、第一溶融槽4A内の溶融ガラスの液面が下降し、前記流出圧力がガラス容量に影響を及ぼさない時点において、フロート部材20Aによる液面下限位置をセンサ22の信号で検出し、第一溶融槽液面制御手段22Eの信号を制御手段46に入力し、制御手段46は第一モータ30の駆動制御手段を起動させて第一プランジャ26を下降操作し、第二溶融槽6内の溶融ガラスを第一溶融槽内に送り込んで第一溶融槽4の液面の上昇を実行する。
【0075】
本装置においては、第一溶融槽4の液面位置の早急なる回復のために、前記液面位置検出手段22からの信号に基ずいて前記制御手段46から第二プランジャ40の作動信号が出力し、これにより、第二のモータ42の駆動制御手段48により第二プランジャ40も上昇位置から下降操作し、第一溶融槽4の清澄槽4B内に進入操作が行われる。
【0076】
この操作により、第一プランジャ26の動作による第二溶融槽6からの第一溶融槽内への溶融ガラスの送り込みによる液面上昇と平行的に、第二プランジャ40による清澄槽4B内の液面上昇が行われて、溶融槽4Aの液面位置が急速に上昇し、溶融槽4A内の液圧の低下を防ぎ、流出ノズルからは一定品質の溶融ガラスを流出させることができる。
【0077】
【発明の効果】
以上のように本発明は、流出部から流出する溶融ガラスの品質が安定した流出方法をえることができた。
【図面の簡単な説明】
【図1】本発明を実施する装置の主要部の構成を示す図。
【図2】図1の装置を作動制御する制御ブロック図。
【図3】図1の装置の動作の説明のための図。
【図4】図1の装置の動作の説明のための図。
【図5】本発明の他の実施例の構成説明図。
【図6】図5の装置の作動制御の制御ブロック図。
【符号の説明】
4 第一溶融槽
6 第二溶融槽
8 ガラス流路
10A ガラス液面
12 加熱手段
20 液面検出手段
22 センサ
24 制御手段
26 プランジャ
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method and apparatus for melting / outflowing molten glass.
[0002]
[Prior art]
The glass melting tank for melting the glass material, adjusting the melting temperature of the molten glass, homogenizing the composition, and letting out the homogenized molten glass to flow out is the temperature to homogenize the molten glass It is necessary to perform (viscosity) management with high temperature range accuracy and to adjust the capacity of the molten glass.
[0003]
Conventional liquid surface management of the glass melting tank includes a method by measuring the weight of the outflowed glass, and a method of measuring the liquid surface by detecting the transmission of radiation material (γ rays) contained in the glass.
[0004]
[Problems to be solved by the invention]
Lenses used in optical equipment such as cameras are increasingly used for aspheric lenses due to advances in optical technology, and small lenses are also incorporated into information equipment equipped with an image reading function using optical pickup technology. Has increased.
[0005]
Further, in an image forming apparatus such as a printer, there is a possibility that many optical elements having an optical curved surface having a complicated shape such as a toric lens may be employed.
[0006]
Such an aspherical lens uses a glass material having excellent adaptability to environmental changes in accordance with the diversification of the usage environment of the device.
[0007]
When the glass material is melted in the melting tank, the glass flows out, and when the outflowed glass is processed into the above lens shape and optical element shape in the next step, the outflow temperature (viscosity) and outflow capacity of the outflowed glass are determined. It is necessary to flow out within a predetermined temperature range and a predetermined capacity range.
[0008]
In particular, when adopting a press molding process in which the molten glass that has flowed out is press-molded in the next step and formed into an optical element shape, the temperature of the molten glass that flows out and the outflow capacity greatly affect the accuracy of the molded optical element. Effect.
[0009]
In a production process in which the homogenized glass is discharged from the outflow part of the melting tank and transferred to the molding process, the liquid surface position of the melting tank is adjusted within a predetermined range according to the outflow from the outflow part. It is necessary to obtain glass.
[0010]
That is, it is possible to accurately control the capacity of the glass molded product to be molded by keeping the liquid surface pressure of the outflow nozzle that flows out of the molten glass constant and maintaining the weight accuracy of the outflow glass.
[0011]
An object of the present invention is to adjust the liquid level of a melting tank that melts a glass material and causes molten glass to flow out according to the outflow of the flowing glass, so that the state of the glass in the melting tank can be maintained in a uniform condition. It is to propose an outflow method and apparatus.
[0012]
Furthermore, the present invention provides a glass outflow apparatus that can restore the liquid level of the melting tank to a predetermined position as quickly as possible when the glass flows out of the melting tank and the capacity of the molten glass in the melting tank decreases. suggest.
[0013]
[Means for Solving the Problems]
In order to solve the above-mentioned problems, the present invention holds a glass material in a first melting tank that melts molten glass flowing out from an outflow portion, at a position higher than the molten glass liquid level of the first melting tank. And connecting the second melting tank to be melted, and according to the decrease of the molten glass in the first melting tank, the liquid level of the second melting tank is displaced , than the channel that is placed near a predetermined liquid level, fed molten glass to said first molten bath from said second molten bath by Rukoto overflow the molten glass, the first corresponding to the outflow from the outflow portion A glass outflow method is proposed in which the liquid level of the melting tank is adjusted.
[0014]
Furthermore, the present invention provides a method for displacing the liquid level of the second melting tank in accordance with a signal from the means for detecting the upper limit position of the liquid level of the first melting tank, and from the second melting tank to the first A glass outflow method is proposed in which molten glass is fed into the melting tank.
[0016]
Also, a first melting tank for melting the molten glass flowing out from the outflow part, and a second melting tank connected to a position higher than the molten glass liquid surface of the first melting tank and charged with glass material and melted And displacing the liquid level of the second melting tank, and overflowing the molten glass from the flow path installed near the predetermined liquid level in the second melting tank, from the second melting tank to the first Productivity is improved by the proposal of a glass outflow device characterized in that molten glass is fed into one melting tank and the liquid level of the first melting tank is adjusted according to the outflow from the outflow part. Plan.
[0019]
In addition, a second glass melting tank having a liquid level at a position higher than the liquid level of the first glass melting tank provided with the outflow portion is provided, and the first and second melting tanks are connected by a connecting means, According to the proposal of a glass outflow device that adjusts the liquid level of the first melting tank through the connecting means by displacing the liquid level of the second melting tank, the outflow glass is press-formed in the next step. Thus, an apparatus preferable for a production method for forming into an optical element shape is proposed.
[0023]
DETAILED DESCRIPTION OF THE INVENTION
A first embodiment of the present invention will be described below with reference to the drawings.
[0024]
FIG. 1 is a block diagram of the main part of a glass melting / outflow apparatus embodying the present invention, and FIG. 2 is a control block diagram of each part control.
[0025]
1 and 2, reference numeral 1 denotes a glass melting apparatus, 2 denotes a melting apparatus chamber, 4 denotes a first glass melting tank, and 6 denotes a second glass melting tank.
[0026]
The first glass melting tank 4 and the second glass melting tank 6 are connected by a glass flow path 8, and the second glass melting tank 6 is arranged at a higher position than the first glass melting tank 4. The glass is connected by the glass flow path 8 so that the molten glass in the second glass melting tank 6 flows into the first melting tank 4.
[0027]
The first melting tank 4 is divided into an outflow tank 4A provided with an outflow nozzle 4a and a clarification tank 4B that receives the molten glass from the second melting tank 6 and performs a clarification action of the molten glass. It is connected by the flow passage 4C.
[0028]
Reference numeral 10 denotes molten glass in the first melting tank 4, and reference numeral 10 </ b> A denotes a glass liquid level of the glass 10.
[0029]
A heater 12 and a temperature detection means (not shown) are arranged around the first melting tank 4 and the nozzle 4a so that the temperature (viscosity) of the molten glass in the first melting tank is within a predetermined temperature range. It is adjusted.
[0030]
Further, heating means and temperature detection means (not shown) are also arranged around the second melting tank 6 and the glass flow path 8 to manage the glass melting temperature of each part.
[0031]
Reference numeral 14 denotes a stirring member of stirring means installed in the outflow tank 4A, and is rotated by a motor (not shown).
[0032]
Reference numeral 16 denotes a shielding member that covers the entire melting apparatus 1 and maintains the confidentiality and heat insulation of the apparatus.
[0033]
Reference numeral 18 denotes an inlet for introducing a glass material into the second glass melting tank 6.
[0034]
Reference numeral 20 denotes a float member for detecting the position of the glass liquid surface 10A of the first glass melting tank 4, which has a float portion 20A and a shaft portion 20B, and the shaft portion 20B is supported on the ceiling portion of the shielding member 16 It is pivotally supported by the member 20C and exposed to the outside.
[0035]
The tip of the shaft portion 20B of the float member 20 is connected to the position detection sensor means 22.
[0036]
The position detection sensor means 22 is constituted by a micro switch indicating a plurality of detection positions, a non-contact type optical sensor, or the like.
[0037]
In this example, a sensor 22A indicating the upper limit position of the float member 20A and a sensor 22B indicating the lower limit position of the float member are configured.
[0038]
The sensors 22A and 22B are mounted on the shielding member 16 with a predetermined distance between them by a holding member 22C, and a probe attached to the tip of the float shaft portion 20B between the sensors 22A and 22B. The portion 20D is arranged, and the probe portion 20D comes into contact with the sensor 20A or 20B according to the vertical movement of the float portion 20A, so that signals are output from the sensors 20A and 20B, and the glass liquid level of the first melting tank 4 The position of 10A is detected.
[0039]
Reference numeral 24 denotes a control means which receives a signal from the sensors 22A and 22B and performs a control operation which will be described later.
[0040]
A plunger 26 is placed in the second melting tank 6 and moves up and down on the liquid surface. The plunger 26 has a shaft portion 26 </ b> A attached to an upper portion thereof, and the shaft portion 26 </ b> A passes through the shielding member 16 and is fixed to a rotating shaft 30 </ b> A of a motor 30 attached to an attachment member 28.
[0041]
The motor 30 is subjected to forward / reverse rotation and rotational speed control by the motor driving means 30A, whereby the plunger 26 moves up and down in the first melting tank 6, and as a result, the liquid surface position of the second melting tank 6 moves up and down. Moving.
[0042]
32 is a position detection sensor for detecting the vertical movement position of the plunger 26, and 26B is a sensor dog attached to the shaft 26A.
[0043]
The position detection sensor 32 is connected to the plunger position control means 26B.
[0044]
Next, the operation of this example will be described with further reference to FIGS.
[0045]
First, in order to set an initial state, a glass material of molten glass is charged from the glass material charging port 18, the molten glass is filled in the second melting tank 6, and the molten glass in the second melting tank 6 is poured into the glass flow. The float member 20A of the first melting tank 4 is fed to the first melting tank 4 through the path 8, and the liquid level detecting probe 20D detects the output of the liquid level upper limit sensor 22A in the state shown in FIG. Set to reach state.
[0046]
Then, the temperature control of each part and the stirring means 14 are adjusted so that the molten glass flowing out from the outflow nozzle is in a predetermined molten state.
[0047]
When the glass liquid level of the first melting tank 4 outputs a signal of the sensor 22A indicating the upper limit position, a signal for stopping the glass material input is output from the control means 24.
[0048]
In this state, the plunger 26 in the second melting tank 6 is set at a position where the liquid glass upper limit position in the first and second melting tanks 4 and 6 is filled with molten glass, and the position of the plunger 26 is The initial position (the upper limit position of the float member 20A) is set by the position detection means (26B, 32).
[0049]
With the above settings, the glass outflow preparation state from the outflow nozzle 4a is completed.
[0050]
In this example, the glass outflow rate from the outflow nozzle 4a was set to 3.0 cc / min, the temperature of the outflow nozzle 4A was set to 1150 ° C., and the nozzle intermediate portion temperature was set to 900 ° C.
[0051]
Adjustment of the outflow from the nozzle is performed by the control means 12B.
[0052]
A receiving member for receiving molten glass (not shown) is arranged below the outlet nozzle tip orifice, and the molten glass is sequentially discharged.
[0053]
As the molten glass flows out from the outflow nozzle 4A, the amount of molten glass in the first melting tank 4 decreases (FIG. 3), and the float member 20 also descends as the glass liquid level falls.
[0054]
When the float member 20A is lowered, the probe member 20D is also lowered, and when the glass liquid level 10A comes into contact with the lower limit position sensor 22B, the motor drive control is performed from the control means 24 based on the signal from the first melting tank liquid level control means 22E. The means 30 </ b> A is activated, and the lowering of the plunger 26 is started by the rotation of the motor 30.
[0055]
As the plunger 26 descends into the second melting tank 6, the glass liquid level in the second melting tank rises according to the descending volume of the plunger 26, and the molten glass in the second melting tank 6 is glass. It flows into the first melting tank 4 through the flow path 8.
[0056]
Accordingly, the liquid level position 10A of the first melting tank 4 also rises, and the probe member 20D contacts the liquid level upper limit position sensor 22A to detect the upper limit position of the liquid level, and the first melting tank liquid level control means. The rotation of the motor 30 is stopped via the motor drive control means 30A by a signal from 22E.
[0057]
When the glass liquid level in the first melting tank 4 is restored to the upper limit position, the plunger 26 is raised by the rotation operation of the motor 30 and returned to the initial position in order to restore the liquid level position in the second melting tank 6. . (Fig. 4)
[0058]
Thereafter, the glass material is charged from the glass material charging port 18, and the capacity of the molten glass in the second melting tank 6 is recovered to the initial liquid level position.
[0059]
The molten glass fed into the first melting tank 4 by the plunger 26 is sequentially homogenized through the clarification tank 4B and the outflow tank 4A, and sent to the outflow nozzle 4a to perform the outflow operation.
[0060]
As described above, according to the present invention, the second melting tank 6 for melting the molten glass flowing out from the outflow portion 4a is connected to the first melting tank 4 for melting the glass material, and the second melting By displacing the liquid level of the tank 6, the molten glass is fed from the second melting tank 6 to the first melting tank 4, and the liquid level of the first melting tank is adjusted according to the outflow from the outflow portion. Thus, the uniformity of the outflow glass can be maintained by always maintaining the distance (glass liquid surface depth) between the glass outflow portion 4a and the glass liquid surface position 10A within a certain range.
[0061]
Furthermore, this invention provides the 2nd melting tank 6 which has the liquid level higher than the liquid level position 10A of the 1st melting tank 4 provided with the outflow part 4a, The liquid level of said 1st melting tank 4 The second liquid surface is displaced according to the signal of the means 20A for detecting 10A, and the molten glass is fed from the second melting tank to the first melting tank, so that the glass outflow portion is uniform. Molten glass could be obtained.
[0062]
Furthermore, the second melting tank 6 for charging and melting the glass material is connected to the first melting tank 4 for melting the molten glass flowing out from the outflow part, and the inside of the second melting tank 6 is moved forward and backward. Means 26 and 30 for feeding molten glass from the second melting tank 6 to the first melting tank 4 are provided, and the liquid level of the first melting tank 4 is adjusted by the feeding means. Thus, a glass with uniform homogeneity could be obtained.
[0063]
In addition, a second glass melting tank having a liquid level at a position higher than the liquid level of the first glass melting tank provided with the outflow portion is provided, and the first and second melting tanks are connected by a connecting means, According to the proposal of a glass outflow device that adjusts the liquid level of the first melting tank through the connecting means by displacing the liquid level of the second melting tank, the outflow glass is press-formed in the next step. Thus, an apparatus suitable for a production method for forming into an optical element shape could be proposed.
[0064]
Furthermore, the present invention connects a second glass melting tank having a glass outflow portion to a first melting tank for melting the charged glass material, and responds to a decrease in the molten glass in the second glass melting tank. By adjusting the volume in the second melting tank, it is possible to obtain the stability of the quality of the outflow glass by always adjusting the capacity of the molten glass in the first melting tank within a predetermined capacity range. It was.
[0065]
Next, an application example of the present invention is shown in FIG. 5. In this example, the second liquid level adjusting means is arranged in the first melting tank of the first embodiment to improve the liquid level adjustment responsiveness of the outflow tank. Is intended.
[0066]
In FIG. 5, the same reference numerals as those shown in FIG. 1 denote parts having the same function, and the added parts will be described below.
[0067]
Reference numeral 40 denotes a second plunger, and the shaft portion 40A penetrates the shielding member so that the shaft portion 40A can move forward and backward in the clarification tank 4B of the first melting tank 4. Connected.
[0068]
A position detection sensor 44 detects the movement position of the second plunger 40 and is connected to the control means 46.
[0069]
The control means 46 connects signal lines of the position detection sensor 32 of the first plunger 26, the first and second motors 30 and 42, and the liquid level detection means 22.
[0070]
FIG. 6 is a control system block diagram of the apparatus of FIG.
[0071]
First, the first and second plungers 26 and 40 are set at the ascending position, the glass material is put into the second melting tank 6, and the molten glass is sequentially fed into the first melting tank, and the first and second The melting tank is filled with molten glass, and the temperature of each tank and the outflow nozzle 4a is controlled.
[0072]
After the temperature adjustment of the outflow nozzle 4a and the liquid level of the melting tank 4A are set to the initial height position, the molten glass is discharged and the forming glass is sequentially discharged.
[0073]
With the outflow of the glass in the melting tank 4A, the liquid surface position is lowered, thereby changing the outflow pressure of the glass of the outflow nozzle 4a.
[0074]
As the molten glass flows out, the liquid level of the molten glass in the first melting tank 4A descends, and when the outflow pressure does not affect the glass capacity, the lower limit position of the liquid level by the float member 20A is determined by the signal from the sensor 22. And the signal of the first melting tank liquid level control means 22E is input to the control means 46. The control means 46 activates the drive control means of the first motor 30 to lower the first plunger 26, and the second The molten glass in the melting tank 6 is sent into the first melting tank and the liquid level of the first melting tank 4 is raised.
[0075]
In the present apparatus, an operation signal for the second plunger 40 is output from the control means 46 on the basis of a signal from the liquid level position detection means 22 for quick recovery of the liquid level position in the first melting tank 4. As a result, the second plunger 40 is also lowered from the raised position by the drive control means 48 of the second motor 42, and the entry operation is performed into the clarification tank 4 </ b> B of the first melting tank 4.
[0076]
By this operation, the liquid level in the clarification tank 4B by the second plunger 40 in parallel with the rise in liquid level due to the feeding of the molten glass from the second melting tank 6 into the first melting tank by the operation of the first plunger 26. Ascending is performed, the liquid surface position of the melting tank 4A rapidly rises, a decrease in the liquid pressure in the melting tank 4A is prevented, and molten glass of a certain quality can be discharged from the outflow nozzle.
[0077]
【The invention's effect】
As described above, the present invention can provide an outflow method in which the quality of the molten glass flowing out from the outflow portion is stable.
[Brief description of the drawings]
FIG. 1 is a diagram showing a configuration of a main part of an apparatus for carrying out the present invention.
FIG. 2 is a control block diagram for controlling the operation of the apparatus shown in FIG.
FIG. 3 is a diagram for explaining the operation of the apparatus shown in FIG. 1;
4 is a diagram for explaining the operation of the apparatus of FIG. 1;
FIG. 5 is a diagram illustrating the configuration of another embodiment of the present invention.
6 is a control block diagram of operation control of the apparatus of FIG. 5;
[Explanation of symbols]
4 First Melting Tank 6 Second Melting Tank 8 Glass Flow Channel 10A Glass Liquid Level 12 Heating Means 20 Liquid Level Detection Means 22 Sensor 24 Control Means 26 Plunger

Claims (4)

流出部から流出する溶融ガラスを溶融する第一の溶融槽に、該第一の溶融槽の溶融ガラス液面より上位位置に保持され、ガラス材料を投入して溶融する第二の溶融槽を接続し、前記第一の溶融槽内の溶融ガラスの減少に応じて、前記第二の溶融槽の液面レベルを変位させ、第二の溶融槽内の所定液面近傍に設置した流路より、溶融ガラスをオーバーフローさせることにより前記第二の溶融槽から前記第一の溶融槽へ溶融ガラスを送り込み、前記流出部からの流出に応じた前記第一の溶融槽の液面調整を行うようにしたことを特徴としたガラス流出方法。Connected to the first melting tank that melts the molten glass that flows out from the outflow section, is held at a higher position than the molten glass liquid surface of the first melting tank, and the glass material is charged and melted. And according to the decrease of the molten glass in the first melting tank, the liquid level of the second melting tank is displaced , from the flow path installed near the predetermined liquid level in the second melting tank, overflow the molten glass feeding the molten glass into the first molten bath from said second molten bath by Rukoto, so as to perform the liquid level adjustment of the first molten bath in accordance with the outflow from the outflow portion A glass outflow method characterized by that. 前記第一の溶融槽の液面上限位置を検出する手段の信号に応じて前記第二の溶融槽の液面を変位させて、前記第二の溶融槽から前記第一の溶融槽へ溶融ガラスを送り込むようにしたことを特徴とした請求項1に記載のガラス流出方法。The molten glass is displaced from the second melting tank to the first melting tank by displacing the liquid level of the second melting tank in accordance with a signal from the means for detecting the liquid surface upper limit position of the first melting tank. The glass outflow method according to claim 1, wherein: 流出部から流出する溶融ガラスを溶融する第一の溶融槽と、該第一の溶融槽の溶融ガラス液面より上位位置に接続され、ガラス材料を投入して溶融する第二の溶融槽と、前記第二の溶融槽の液面レベルを変位させ、第二の溶融槽内の所定液面近傍に設置した流路より、溶融ガラスをオーバーフローさせることにより前記第二の溶融槽から前記第一の溶融槽へ溶融ガラスを送り込み、前記流出部からの流出に応じた前記第一の溶融槽の液面調整を行うようにしたことを特徴としたガラス流出装置。A first melting tank for melting the molten glass flowing out from the outflow part, a second melting tank connected to a higher position than the molten glass liquid surface of the first melting tank, and charged with a glass material; The liquid level of the second melting tank is displaced, and the first glass is allowed to overflow from the second melting tank by causing the molten glass to overflow from a flow path installed near a predetermined liquid level in the second melting tank. A glass outflow apparatus, wherein molten glass is fed into a melting tank and the liquid level of the first melting tank is adjusted in accordance with the outflow from the outflow portion. 流出部を備える第一のガラス溶融槽の液面より上位位置に液面を有した第二のガラス溶融槽を設け、前記第一と第二の溶融槽を接続手段で接続し、前記第二の溶融槽の液面を変位させることにより前記接続手段を介して前記第一の溶融槽の液面の調整を行うようにしたことを特徴とした請求項3に記載のガラス流出装置。A second glass melting tank having a liquid level at a position higher than the liquid level of the first glass melting tank provided with an outflow portion is provided, and the first and second melting tanks are connected by connecting means, and the second 4. The glass outflow device according to claim 3, wherein the liquid level of the first melting tank is adjusted via the connecting means by displacing the liquid level of the melting tank.
JP18247097A 1997-07-08 1997-07-08 Glass outflow method and glass outflow device Expired - Fee Related JP3618966B2 (en)

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