JP3077066B2 - Each production method of glass gob and its intermediate - Google Patents
Each production method of glass gob and its intermediateInfo
- Publication number
- JP3077066B2 JP3077066B2 JP03271689A JP27168991A JP3077066B2 JP 3077066 B2 JP3077066 B2 JP 3077066B2 JP 03271689 A JP03271689 A JP 03271689A JP 27168991 A JP27168991 A JP 27168991A JP 3077066 B2 JP3077066 B2 JP 3077066B2
- Authority
- JP
- Japan
- Prior art keywords
- glass
- glass gob
- producing
- outflow pipe
- molten glass
- 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
Links
- 239000011521 glass Substances 0.000 title claims description 138
- 238000004519 manufacturing process Methods 0.000 title claims description 37
- 239000006060 molten glass Substances 0.000 claims description 77
- 238000000465 moulding Methods 0.000 claims description 34
- 238000000034 method Methods 0.000 claims description 16
- 238000001816 cooling Methods 0.000 claims description 10
- 239000007789 gas Substances 0.000 description 16
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 206010040925 Skin striae Diseases 0.000 description 8
- 239000011148 porous material Substances 0.000 description 6
- 238000012986 modification Methods 0.000 description 5
- 230000004048 modification Effects 0.000 description 5
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 229910001260 Pt alloy Inorganic materials 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000004031 devitrification Methods 0.000 description 1
- 239000005303 fluorophosphate glass Substances 0.000 description 1
- 101150086005 gob-1 gene Proteins 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 239000005368 silicate glass Substances 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
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
- C03B19/1005—Forming solid beads
- C03B19/1055—Forming solid beads by extruding, e.g. dripping molten glass in a gaseous atmosphere
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/02—Other methods of shaping glass by casting molten glass, e.g. injection moulding
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B40/00—Preventing adhesion between glass and glass or between glass and the means used to shape it, hold it or support it
- C03B40/04—Preventing adhesion between glass and glass or between glass and the means used to shape it, hold it or support it using gas
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B7/00—Distributors for the molten glass; Means for taking-off charges of molten glass; Producing the gob, e.g. controlling the gob shape, weight or delivery tact
- C03B7/10—Cutting-off or severing the glass flow with the aid of knives or scissors or non-contacting cutting means, e.g. a gas jet; Construction of the blades used
- C03B7/12—Cutting-off or severing a free-hanging glass stream, e.g. by the combination of gravity and surface tension forces
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B7/00—Distributors for the molten glass; Means for taking-off charges of molten glass; Producing the gob, e.g. controlling the gob shape, weight or delivery tact
- C03B7/14—Transferring molten glass or gobs to glass blowing or pressing machines
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/50—Glass production, e.g. reusing waste heat during processing or shaping
- Y02P40/57—Improving the yield, e-g- reduction of reject rates
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Glass Compositions (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、切断刃を使用せずに溶
融ガラスからガラスゴブとその中間体を製造する方法に
関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a glass gob and its intermediate from molten glass without using a cutting blade.
【0002】[0002]
【従来の技術】従来から切断刃で溶融ガラスを切断する
と表面にキズや汚れを生じることから、切断刃を使用せ
ずに溶融ガラスを切断してガラスゴブを製造する方法が
種々提案されており、その一例として特開平2−345
25号公報および特開平2−14839号公報に開示さ
れたものが知られている。特開平2−34525号公報
に開示されたガラスゴブの製造方法は、流出パイプから
流下する溶融ガラスを、成形型内で受け、所定量の溶融
ガラスが成形型内に鋳込まれた時に成形型を急速に降下
させることによって流下する溶融ガラスと鋳込まれた溶
融ガラスを切断分離して溶融ガラス塊(以下ガラスゴブ
中間体と称する)を製造するものである。そして、この
ガラスゴブ中間体は成形型にて軟化点以下に冷却固化さ
れ、この固化したもの(以下ガラスゴブと称する)を成
形型から取り出して加熱、プレス成形することによりレ
ンズ、プリズム等所望形状の製品の製作が行われる。一
方、特開平2−14839号公報に開示されたガラスゴ
ブの製造方法は、流出パイプから溶融ガラスを成形型内
に滴下させてガラスゴブ中間体を製造し、これを空気、
不活性ガス等の気体によって冷却固化させてガラスゴブ
を製造するものである。2. Description of the Related Art Various methods have been proposed for producing a glass gob by cutting molten glass without using a cutting blade, since cutting the molten glass with a cutting blade causes scratches and stains on the surface. For example, Japanese Patent Application Laid-Open No. 2-345
No. 25 and JP-A-2-14839 are known. A method for manufacturing a glass gob disclosed in Japanese Patent Application Laid-Open No. 2-34525 is a method for receiving molten glass flowing down from an outflow pipe in a molding die, and forming the molding die when a predetermined amount of molten glass is cast into the molding die. The molten glass that flows down and the cast molten glass are cut and separated by rapidly descending to produce a molten glass lump (hereinafter, referred to as a glass gob intermediate). Then, the glass gob intermediate is cooled and solidified to a softening point or lower in a molding die, and the solidified product (hereinafter, referred to as a glass gob) is taken out from the molding die, heated, and press-molded to obtain a product having a desired shape such as a lens and a prism. Is made. On the other hand, a method for manufacturing a glass gob disclosed in Japanese Patent Application Laid-Open No. 2-14839 discloses a method for manufacturing a glass gob intermediate by dropping molten glass from an outflow pipe into a molding die,
The glass gob is manufactured by cooling and solidifying with a gas such as an inert gas.
【0003】[0003]
【発明が解決しようとする課題】上記した通り特開平2
−34525号公報によるガラスゴブの製造方法は、成
形型を急速に降下させることにより流出パイプから流出
する溶融ガラスと成形型内に鋳込まれた溶融ガラスを引
きちぎって溶融ガラス塊、すなわちガラスゴブ中間体を
製造し、これを冷却することによりガラスゴブを製造す
るものである。したがって、ガラスゴブ中間体の引きち
ぎられた部分に細長く伸びた部分が形成され、この部分
は細長いために冷却が早く、粘性が高くなるため、後に
ガラスゴブ中間体に吸収された時不均質な部分を形成す
る。そして、この不均質部分はガラスゴブ中間体の冷却
によって得られるガラスゴブの内部に脈理を発生させる
という問題があった。特開平2−14839号公報に開
示されたガラスゴブの製造方法は、滴下によって溶融ガ
ラスを切断分離し、表面張力を利用して球形化すること
により、細長く伸びた切断部を吸収するものである。し
かしながら、落下しようとするガラスゴブ中間体の粘性
が高い場合、ガラスゴブの表面張力が小さくなり、切断
性能が低下する。それ故にガラスゴブ中間体の分離が瞬
時に行われず、ガラスゴブ中間体が流出パイプから流下
する溶融ガラスと細い糸状につながった状態で落下す
る。つまり、ガラスゴブ中間体が上方の溶融ガラスから
糸を引いた状態となる。この糸引き状態を起こした時の
ガラスゴブ中間体は、上方の溶融ガラスから糸を引きな
がら落下して行くために、いずれ切断されるものの糸引
き部分がその後ガラスゴブ中間体に吸収されるため、得
られたガラスゴブ中間体に糸状の不均質部分を生じる。
そして、このガラスゴブ中間体を冷却することによって
得られたガラスゴブの内部に上記したと同様、脈理が発
生するという問題があった。As described above, Japanese Unexamined Patent Application Publication No.
The method for producing a glass gob according to JP-A-34525 discloses a method in which a molten glass flowing out of an outflow pipe and a molten glass poured into a molding die are separated by rapidly lowering a molding die to form a molten glass lump, that is, a glass gob intermediate. The glass gob is manufactured by manufacturing and cooling it. Therefore, an elongated portion is formed at the torn portion of the glass gob intermediate, and since this portion is elongated, it cools quickly and has a high viscosity, so that when it is later absorbed by the glass gob intermediate, an inhomogeneous portion is formed. I do. Then, there is a problem that the heterogeneous portion generates striae inside the glass gob obtained by cooling the glass gob intermediate. The method for manufacturing a glass gob disclosed in Japanese Patent Application Laid-Open No. 2-14839 is to cut and separate molten glass by dropping and to make the glass into a spherical shape by using surface tension, thereby absorbing the elongated and elongated cut portion. However, when the viscosity of the glass gob intermediate to be dropped is high, the surface tension of the glass gob becomes small, and the cutting performance decreases. Therefore, the separation of the glass gob intermediate is not instantaneous, and the glass gob intermediate falls in a state of being connected to the molten glass flowing down from the outflow pipe in a thin thread form. In other words, the glass gob intermediate is in a state where the thread is pulled from the upper molten glass. The glass gob intermediate at the time of this stringing state falls while pulling a thread from the upper molten glass, so that although the stringing portion is eventually absorbed by the glass gob intermediate, it is obtained. The resulting glass gob intermediate produces thread-like non-uniformities.
Then, as described above, there is a problem that striae are generated inside the glass gob obtained by cooling the glass gob intermediate.
【0004】したがって、本発明は上記したような従来
の問題点に鑑みてなされたもので、その目的とするとこ
ろは、切断刃を使用することなく溶融ガラスを切断する
ことができ、またキズ、汚れ、脈理等の不良の発生を防
止することができるようにしたガラスゴブとその中間体
の各製造方法を提供することにある。Accordingly, the present invention has been made in view of the above-mentioned conventional problems, and an object of the present invention is to cut molten glass without using a cutting blade. It is an object of the present invention to provide a method for producing a glass gob and an intermediate thereof which can prevent the occurrence of defects such as dirt and striae.
【0005】[0005]
【課題を解決するための手段】本発明は上記目的を達成
するためになされたもので、その第1の発明は、流出パ
イプから流出した溶融ガラスを、該流出パイプの下方に
配置された受部によって受けて、所定重量のガラスゴブ
中間体を製造する方法であって、前記流出パイプの先端
と受部の距離を、前記ガラスゴブ中間体の重量に基づい
て定められた距離に一定に保ちつつ、所定粘度の溶融ガ
ラスを前記流出パイプより流下させて該溶融ガラスの先
端を前記受部により受け、該溶融ガラスにくびれ部を形
成し、このくびれ部より先端側の溶融ガラスの重量が一
定の重量に達したときに、前記くびれ部より先端側の溶
融ガラスが分離するようにして前記ガラスゴブ中間体を
得ることを特徴とする。第2の発明は、上記第1の発明
において、前記ガラスゴブ中間体の重量を、前記流出パ
イプの先端と受部の間の距離を変えることにより調節す
ることを特徴とする。第3の発明は、上記第1または第
2の発明において、前記流出パイプの温度を制御するこ
とにより、該流出パイプから流下する溶融ガラスの粘度
を調整することを特徴とする。第4の発明は、上記第
1、第2または第3の発明において、前記流出パイプか
ら流出する溶融ガラスの粘度を、35ポアズ以上とする
ことを特徴とする。第5の発明は、上記第1、第2、第
3または第4の発明において、前記流出パイプの先端の
外径が2.0〜5.4mm、当該流出パイプの内径が
1.0〜2.0mmであることを特徴とする。第6の発
明は、上記第1、第2、第3、第4または第5の発明に
おいて、前記受部を溶融ガラスを受ける位置に移動した
後、該受部によって前記流下パイプから流下する溶融ガ
ラスを受けてガラスゴブ中間体を得、前記溶融ガラスを
受けた受部を該溶融ガラスを受ける位置から移動する工
程を、複数の受部を用いて順次繰り返し、所定の重量を
有するガラスゴブ中間体を連続して製造することを特徴
とする。第7の発明は、上記第1、第2、第3、第4、
第5または第6の発明によって製造されたガラスゴブ中
間体を冷却してガラスゴブを製造することを特徴とす
る。第8の発明は、上記第7の発明において、前記ガラ
スゴブ中間体を冷却するまでの間に所望の形状に成形し
て前記形状を有するガラスゴブを得ることを特徴とす
る。第9の発明は、上記第8の発明において、成形型を
用い、前記ガラスゴブ中間体を気体の層を介して該成形
型に収容して前記成形を行うことを特徴とする。第10
の発明は、上記第9の発明において、前記成形型は前記
溶融ガラスを受ける受部と、前記ガラスゴブ中間体を収
容する凹部とを有することを特徴とする。第11の発明
は、上記第10の発明において、前記凹部の開口縁に前
記受部が形成されており、前記ガラスゴブ中間体の分離
によって該ガラスゴブ中間体が前記凹部に落ちるように
して収容される成形型を用いることを特徴とする。第1
2の発明は、上記第10または11の発明において、前
記凹部が、上方に広がるテーパ状であることを特徴とす
る。第13の発明は、上記第10、第11または第12
の発明において、前記流出パイプの中心線が、前記成形
型の凹部の開口縁と接する位置で前記溶融ガラスを受け
るとともに、溶融ガラスの分離を行うことを特徴とす
る。第14の発明は、上記第10、第11、第12また
は第13の発明において、前記成形型に収容したガラス
ゴブ中間体を、該ガラスゴブ中間体の表面が軟化点以下
の温度に達するまで該成形型に収容した状態で冷却する
ことを特徴とする。Means for Solving the Problems The present invention has been made to achieve the above-mentioned object, and a first invention of the present invention is to receive molten glass flowing out of an outflow pipe below the outflow pipe. A method for producing a glass gob intermediate having a predetermined weight, while receiving a distance between a tip of the outflow pipe and a receiving part, at a distance determined based on the weight of the glass gob intermediate, The molten glass having a predetermined viscosity is caused to flow down from the outflow pipe, and the distal end of the molten glass is received by the receiving portion to form a constricted portion in the molten glass. , The molten glass on the front end side of the constricted portion is separated to obtain the glass gob intermediate. According to a second aspect, in the first aspect, the weight of the glass gob intermediate is adjusted by changing a distance between a tip of the outflow pipe and a receiving portion. According to a third invention, in the first or second invention, the viscosity of the molten glass flowing down from the outflow pipe is adjusted by controlling the temperature of the outflow pipe. In a fourth aspect based on the first, second or third aspect, the viscosity of the molten glass flowing out of the outflow pipe is 35 poise or more. In a fifth aspect based on the first, second, third, or fourth aspect, the outer diameter of the tip of the outflow pipe is 2.0 to 5.4 mm, and the inner diameter of the outflow pipe is 1.0 to 2 mm. .0 mm. In a sixth aspect based on the first, second, third, fourth, or fifth aspect, after the receiving portion is moved to a position for receiving the molten glass, the molten portion flows down from the downflow pipe by the receiving portion. The step of receiving the glass to obtain a glass gob intermediate, the step of moving the receiving portion receiving the molten glass from the position where the molten glass is received is sequentially repeated using a plurality of receiving portions, and a glass gob intermediate having a predetermined weight is formed. It is characterized by being manufactured continuously. According to a seventh aspect of the present invention, the first, second, third, fourth,
The glass gob is produced by cooling the glass gob intermediate produced by the fifth or sixth invention. An eighth invention is characterized in that, in the seventh invention, a glass gob having the above shape is obtained by forming the glass gob intermediate into a desired shape before cooling. A ninth invention is characterized in that, in the eighth invention, the glass gob intermediate is housed in the molding die via a gas layer to perform the molding. Tenth
According to a ninth aspect of the present invention, in the ninth aspect, the mold has a receiving portion for receiving the molten glass and a concave portion for accommodating the glass gob intermediate. In an eleventh aspect based on the tenth aspect, the receiving portion is formed at an opening edge of the concave portion, and the glass gob intermediate is received in the concave portion by separation of the glass gob intermediate. It is characterized by using a molding die. First
A second invention is characterized in that, in the tenth or eleventh invention, the recess has a tapered shape extending upward. The thirteenth invention is directed to the tenth, eleventh, or twelfth aspect.
In the invention, the center line of the outflow pipe receives the molten glass at a position where the center line contacts an opening edge of a concave portion of the molding die, and separates the molten glass. According to a fourteenth aspect, in the tenth, eleventh, twelfth, or thirteenth aspect, the glass gob intermediate housed in the molding die is molded until the surface of the glass gob intermediate reaches a temperature equal to or lower than the softening point. It is characterized in that it is cooled while being housed in a mold.
【0006】[0006]
【作用】第1の発明において、流出パイプより流出され
自重によって下降する溶融ガラスは受部によって受け止
められ、くびれ部が生じる。そして、くびれ部より先端
側の溶融ガラスが所定重量になったときにくびれ部より
先端側が自然に分離する。このような溶融ガラスの分離
が起こるまで流出パイプと受部は一定の距離に保たれて
いるので、常に一定重量のガラスゴブ中間体が得られ
る。第5の発明において、流出パイプの先端の外径を
2.0〜5.4mm、内径を1.0〜2.0mmとした
ことにより、溶融ガラスが滴下状態とならず、キズ、汚
れ、脈理等が発生しない。第6の発明において、受部を
複数用いることにより、連続的に製造することができ、
生産性を向上させることができる。第9の発明におい
て、成形型の凹部内に吹き出す気体はガラスゴブ中間体
と凹部との間に気体層を形成し、得られるガラスゴブの
表面にキズや汚れがつかないようにする。なお、この時
成形されるガラスゴブの形状は、成形型の凹部形状によ
って決まり、凹部がラッパ状をしている場合は、真球度
の高い球状となる。これは、凹部内に吹き上げられる気
流によって凹部内面に接触することなく浮上し続け回転
しながら冷却、硬化するためである。また、凹部の断面
形状が凹面鏡状をしている場合は、この凹部内に落下し
たガラスゴブ中間体は回転せず成形型の成形面の形状に
近い形となる。第10の発明において、成形型は溶融ガ
ラスを受ける受部と、ガラスゴブ中間体を収容する凹部
を有しているので、装置を簡素化することができる。In the first aspect of the invention, the molten glass flowing out of the outflow pipe and descending by its own weight is received by the receiving portion, and a narrow portion is generated. Then, when the molten glass on the distal end side of the constricted portion has a predetermined weight, the distal end side of the constricted portion is naturally separated. The outflow pipe and the receiving portion are kept at a fixed distance until such a separation of the molten glass occurs, so that a glass gob intermediate having a constant weight is always obtained. In the fifth invention, the outer diameter of the tip of the outflow pipe is set to 2.0 to 5.4 mm and the inner diameter is set to 1.0 to 2.0 mm, so that the molten glass does not fall into a dripping state, and scratches, dirt, and pulse are generated. There is no reason. In the sixth invention, by using a plurality of receiving portions, it is possible to manufacture continuously,
Productivity can be improved. In the ninth invention, the gas blown into the concave portion of the mold forms a gas layer between the glass gob intermediate and the concave portion, so that the surface of the obtained glass gob is not scratched or stained. The shape of the glass gob formed at this time is determined by the shape of the concave portion of the molding die. When the concave portion has a trumpet shape, the glass gob is spherical with high sphericity. This is because the air current blown into the concave portion keeps floating without contacting the inner surface of the concave portion and cools and hardens while rotating. When the cross-sectional shape of the concave portion is a concave mirror shape, the glass gob intermediate that has fallen into the concave portion does not rotate and has a shape close to the shape of the molding surface of the mold. In the tenth invention, since the molding die has the receiving portion for receiving the molten glass and the concave portion for accommodating the glass gob intermediate, the apparatus can be simplified.
【0007】[0007]
【実施例】以下本発明を図面に示す実施例に基づいて詳
細に説明する。図1(a)〜(e)は本発明に係るガラ
スゴブとその中間体の製造方法の各工程とこの方法に使
用する製造装置の縦断面図である。同図において、この
製造装置は、上端が不図示の溶融ガラス槽に接続された
白金または白金合金製の流出パイプ1と、流出パイプ1
を加熱するヒータ3と、流出パイプ1の温度を検出する
熱電対4と、流出パイプ1の下方に配置された耐熱鋼
(例えばステンレス)製の成形型5とを備え、流出パイ
プ1の温度を熱電対4によって検出し、その検出信号に
より温度制御装置(図示せず)が流出パイプ1の温度を
制御するように構成されている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail based on an embodiment shown in the drawings. 1 (a) to 1 (e) are longitudinal sectional views of each step of a method for producing a glass gob and an intermediate thereof according to the present invention and a production apparatus used for this method. In this figure, the production apparatus includes an outflow pipe 1 made of platinum or a platinum alloy, the upper end of which is connected to a molten glass tank (not shown).
A heater 3, a thermocouple 4 for detecting the temperature of the outflow pipe 1, and a mold 5 made of heat-resistant steel (for example, stainless steel) disposed below the outflow pipe 1; The temperature is detected by the thermocouple 4 and a temperature control device (not shown) controls the temperature of the outflow pipe 1 based on the detection signal.
【0008】前記成形型5は上面が流出パイプ1から流
下する溶融ガラス2を受ける受部6を形成し、上面中央
部には流出パイプ1から流下して切断されたガラスゴブ
中間体9を収容する凹部7が凹設され、また内部中央に
は上端が前記凹部7に連通し、下端が成形型5の下面に
開口する細孔8が形成されている。前記凹部7は、上方
に広がるテーパ状で、広がり角θは好ましくは5°〜3
0°(本実施例では15°)とされ、内面が鏡面仕上げ
されている。前記細孔8は凹部7内に収容されるガラス
ゴブ中間体9を冷却、浮上させるための気体Aを凹部7
内に吹き出させるもので、配管によって気体供給源に接
続されている。気体Aとしてはガラスゴブ中間体9と実
質的に反応しない気体、例えば窒素、アルゴンガス等が
挙げられる。成形型5は、本実施例の場合半径20m
m、高さ40mmの円柱状で、凹部7の開口径が20m
m、受部6の幅が10mm、細孔8の内径が3mmにそ
れぞれ設定されている。そして、このような構成からな
る成形型5は流出パイプ1の下方に距離hだけ離間し
て、かつ中心が流出パイプ1の中心から凹部7の開口半
径だけずれて配置されている。したがって、流出パイプ
1の中心線は凹部7の開口縁と接している。The molding die 5 has a receiving portion 6 whose upper surface receives the molten glass 2 flowing down from the outflow pipe 1, and accommodates a glass gob intermediate 9 cut down from the outflow pipe 1 in the center of the upper surface. A concave portion 7 is provided, and a fine hole 8 having an upper end communicating with the concave portion 7 and a lower end opening on the lower surface of the mold 5 is formed in the center of the inside. The concave portion 7 has a tapered shape expanding upward, and the spread angle θ is preferably 5 ° to 3 °.
The angle is set to 0 ° (15 ° in this embodiment), and the inner surface is mirror-finished. The pores 8 allow the gas A for cooling and floating the glass gob intermediate 9 accommodated in the concave portion 7 to pass through the concave portion 7.
It is blown into the inside and is connected to a gas supply source by piping. Examples of the gas A include a gas that does not substantially react with the glass gob intermediate 9, for example, nitrogen, argon gas, and the like. The molding die 5 has a radius of 20 m in this embodiment.
m, a column with a height of 40 mm, and an opening diameter of the recess 7 of 20 m.
m, the width of the receiving portion 6 is set to 10 mm, and the inner diameter of the pore 8 is set to 3 mm. The molding die 5 having such a configuration is disposed below the outflow pipe 1 by a distance h and its center is shifted from the center of the outflow pipe 1 by the opening radius of the concave portion 7. Therefore, the center line of the outflow pipe 1 is in contact with the opening edge of the recess 7.
【0009】次に上記構成からなる製造装置によるガラ
スゴブとその中間体の製造方法について説明する。先
ず、溶融ガラス2を流出パイプ1から流下させる(図1
(a))。流出パイプ1から流下する溶融ガラス2はヒ
ータ3によって加熱され、所望の温度と粘性となるよう
に制御されている。なお、この工程以後のガラスゴブの
製造までは、ガラスゴブ中間体9と実質的に反応しない
気体Aが細孔8を通って成形型5の凹部7内に供給され
ている。 流出パイプ1から流下する溶融ガラス2は、
先端が受部6によって受け止められ、途中部分がくびれ
て徐々に細くなり(図1(b))、一定重量に達すると
くびれ部12の最も細くなった部分が表面張力によって
流下する溶融ガラス2から切れ、しかしてガラスゴブ中
間体9が得られる(図1(c))。 この切断直後のガ
ラスゴブ中間体9は表面が軟化点以上の温度を保ってい
るため、糸を引いている切断部13は自重および表面張
力によって下がりガラスゴブ中間体9に吸収される。ま
た、受部6上のガラスゴブ中間体9は、略半分が凹部7
の開口に臨んでいるため、流下する溶融ガラス2から切
り離されると、凹部7内に滑り落ちて収容される(図1
(d))。流出パイプ1と受部6の距離hは、短すぎる
と表面張力による分離ができずまた逆に長すぎると溶融
ガラス2が滴下状態となるため溶融ガラス2の粘性や流
出パイプ1の外径、内径等を考慮して適宜決定する。ま
た、前記距離hを短くすると、溶融ガラス2が分離され
るまでの時間が長くなり、得られるガラスゴブ中間体9
の重量は大きくなる。逆に、距離hを長くすると、得ら
れるガラスゴブ中間体9の重量は小さくなる。ガラスゴ
ブ中間体9は落下直後不定形ではあるが、凹部7に吹き
上げられている上記した気体Aによって受け止められ、
凹部内面と殆ど接触せず僅かに浮いた状態で回転される
ことにより段々と球形化する。そして、このガラスゴブ
中間体9は、凹部7内で浮上したまま冷却され、表面が
軟化点以下の温度まで冷えることによりガラスゴブ14
となる(図1(e))。なお、成形型5は流出パイプ1
から流下する溶融ガラス2の滴下によって分離形成され
たガラスゴブ中間体9を受け取ると同時に横方向に水平
移動し、流出パイプ1の下方には新しい空の成形型が移
動してきて停止し、次のガラスゴブ中間体に備える。Next, a method for producing a glass gob and an intermediate thereof by the production apparatus having the above configuration will be described. First, the molten glass 2 is caused to flow down from the outflow pipe 1 (FIG. 1).
(A)). The molten glass 2 flowing down from the outflow pipe 1 is heated by the heater 3 and controlled to have a desired temperature and viscosity. Until the production of the glass gob after this step, the gas A which does not substantially react with the glass gob intermediate 9 is supplied into the concave portion 7 of the mold 5 through the pores 8. The molten glass 2 flowing down from the outflow pipe 1
The leading end is received by the receiving portion 6, the middle portion is narrowed and gradually narrowed (FIG. 1 (b)), and when the weight reaches a certain value, the narrowest portion of the narrowed portion 12 flows from the molten glass 2 flowing down by surface tension. The glass gob intermediate 9 is obtained (FIG. 1 (c)). Since the surface of the glass gob intermediate 9 immediately after the cutting is maintained at a temperature equal to or higher than the softening point, the cut portion 13 where the thread is pulled is lowered by its own weight and surface tension, and is absorbed by the glass gob intermediate 9. In addition, approximately half of the glass gob intermediate 9 on the receiving portion 6 has the concave portion 7.
1, when separated from the flowing molten glass 2, it slides down and is accommodated in the recess 7 (FIG. 1).
(D)). If the distance h between the outflow pipe 1 and the receiving portion 6 is too short, separation by surface tension cannot be performed, and if it is too long, the molten glass 2 drops, so that the viscosity of the molten glass 2 and the outer diameter of the outflow pipe 1 It is appropriately determined in consideration of the inner diameter and the like. Further, when the distance h is shortened, the time until the molten glass 2 is separated becomes longer, and the obtained glass gob intermediate 9
Weight is increased. Conversely, when the distance h is increased, the weight of the obtained glass gob intermediate 9 decreases. Although the glass gob intermediate 9 is indefinite immediately after falling, it is received by the above-mentioned gas A blown up in the concave portion 7,
By rotating in a slightly floating state with little contact with the inner surface of the concave portion, the shape gradually becomes spherical. Then, the glass gob intermediate 9 is cooled while floating in the concave portion 7 and the surface thereof is cooled to a temperature below the softening point, whereby the glass gob 14 is cooled.
(FIG. 1 (e)). The molding die 5 is used for the outflow pipe 1
Upon receiving the glass gob intermediate 9 separated and formed by the dropping of the molten glass 2 flowing down from the pipe, it moves horizontally in the horizontal direction at the same time, and a new empty mold moves below the outflow pipe 1 and stops. Prepare for intermediate.
【0010】(実施例1)溶融ガラス2として、成分揮
発の激しい鉛ケイ酸塩系ガラスを用い、流出パイプ1の
内径を2mm、先端の外径を5mm、流出パイプ1から
成形型5までの距離hを18mmとし、ヒータ3によっ
て溶融ガラス2の温度を1000°C、粘性を約80ポ
アズに保持し、細孔8から毎分1.0リットルの窒素A
を吹き出してガラスゴブ中間体9を経て球形のガラスゴ
ブ14の製造を行なった。こうして得られたガラスゴブ
14の重量は280mgであった。また、その内部に脈
理等の品質不良はなく、ガラスゴブとして好ましいもの
であった。次に、実施例2〜6として溶融ガラス2の種
類、流出パイプ1の内径、流出パイプ1の下端部の外
径、細孔8から吹き出す気体(窒素)Aの吹き出し量、
溶融ガラス2の温度および粘性を変えてガラスゴブの製
造を行なった。(Embodiment 1) As a molten glass 2, a lead silicate glass whose components are intensely volatile is used. The inner diameter of the outflow pipe 1 is 2 mm, the outer diameter of the tip is 5 mm, and The distance h was 18 mm, the temperature of the molten glass 2 was maintained at 1000 ° C. and the viscosity was about 80 poise by the heater 3, and 1.0 liters of nitrogen A
Was blown through the glass gob intermediate 9 to produce a spherical glass gob 14. The weight of the glass gob 14 thus obtained was 280 mg. In addition, there was no quality defect such as striae inside, and it was preferable as a glass gob. Next, as Examples 2 to 6, the type of the molten glass 2, the inner diameter of the outflow pipe 1, the outer diameter of the lower end of the outflow pipe 1, the amount of gas (nitrogen) A blown out from the pores 8,
A glass gob was manufactured by changing the temperature and viscosity of the molten glass 2.
【0011】下記表1は上記実施例1〜6をまとめたも
ので、いずれの実施例においても判定結果は良好でガラ
スゴブにキズ、汚れ、脈理等の発生は見当たらなかっ
た。The following Table 1 summarizes the above Examples 1 to 6. In all Examples, the judgment results were good, and no occurrence of scratches, stains, striae, etc. was found on the glass gob.
【0012】[0012]
【表1】 [Table 1]
【0013】実施例2で用いたフツリン酸系ガラスは、
非常に成分揮発が激しいものであるため、これ以上下げ
ると失透を起こす虞れのある低い温度に設定した。しか
し、それでも多少成分揮発を起こすため、溶融ガラス2
の粘性を正確に測定できなかった。しかし、成分揮発に
よる変質は得られたガラスゴブ14の極表面にのみ存在
し、また内部には脈理等の発生もないため実用上の問題
はなかった。実施例3〜6は、流出パイプ1の先端から
成形型5(受部6)までの距離hを、それぞれ変えて行
なったものである。この結果、実施例3〜6では、前記
距離hを変えることにより、ガラスゴブの重量を320
〜370mgと調節することができた。また、ガラスゴ
ブにキズ、汚れ、脈理等が発生せずガラスゴブとして好
ましいものであった。The fluorophosphate glass used in Example 2 is as follows:
Since the component volatilization is extremely severe, the temperature was set to a low temperature at which there is a risk of devitrification when the temperature is further reduced. However, since the components still volatilize somewhat, the molten glass 2
Could not be measured accurately. However, there was no practical problem since the alteration due to the volatilization of the components was present only on the very surface of the obtained glass gob 14 and there was no striae or the like inside. In Examples 3 to 6, the distance h from the tip of the outflow pipe 1 to the molding die 5 (receiving portion 6) was changed. As a result, in Examples 3 to 6, by changing the distance h, the weight of the glass
It could be adjusted to 3370 mg. In addition, the glass gob was preferable as a glass gob without causing scratches, dirt, striae and the like.
【0014】次に本発明者は本発明方法と従来方法とを
比較するため、上記特開2平一14839号公報に開示
された従来技術によってガラスゴブを製造した。この従
来技術は、本発明による受け部6を設けず単に溶融ガラ
スを流下させて分離し成形型に落下させることによりガ
ラスゴブを形成するもので、溶融ガラスの種類、流出パ
イプの内径、流出パイプの下端部の外径、細孔から吹き
出す気体(窒素)の吹き出し量をそれぞれ上記実施例1
〜6と同一に設定したところ、下記表2に示す判定結果
が得られた。Next, the present inventor manufactured a glass gob according to the conventional technique disclosed in the above-mentioned Japanese Patent Application Laid-Open No. Hei 2-14839 in order to compare the method of the present invention with the conventional method. In this prior art, a glass gob is formed by simply causing molten glass to flow down, separate, and drop into a mold without providing a receiving portion 6 according to the present invention. The type of molten glass, the inner diameter of an outflow pipe, the outflow pipe In Example 1 above, the outer diameter of the lower end and the amount of gas (nitrogen) blown out from the pores were determined.
6 were obtained, and the determination results shown in Table 2 below were obtained.
【0015】[0015]
【表2】 [Table 2]
【0016】表2の判定結果から明らかなように比較例
1〜6のガラスゴブでは、その内部に脈理がたびたび発
生した。結論として、本発明は、溶融ガラス2の粘性が
あまり低くない場合においても、溶融ガラス2を受部6
で受け、表面張力による溶融ガラス2の切断を完全に終
え、且つ糸引き状態の切断部を吸収するに十分な時間を
与えることができるため、従来技術と異なり不均質部分
の発生を防止し得るものである。したがって、溶融ガラ
ス2の粘性をあまり低くする必要はなく、溶融ガラス2
の温度を比較的低下させることができた。このため、本
発明は特に成分の揮発が激しいガラスに対して有用であ
ることが明かとなった。As is clear from the determination results in Table 2, striae frequently occurred in the glass gobs of Comparative Examples 1 to 6. In conclusion, the present invention provides for receiving the molten glass 2 even when the viscosity of the molten glass 2 is not very low.
And the cutting of the molten glass 2 by the surface tension can be completely completed, and sufficient time can be given to absorb the cut portion in the stringing state. Therefore, unlike the related art, it is possible to prevent the generation of an inhomogeneous portion. Things. Therefore, it is not necessary to make the viscosity of the molten glass 2 very low.
Could be relatively lowered. For this reason, it has become clear that the present invention is particularly useful for glass in which components are highly volatile.
【0017】図2〜図7はそれぞれ本発明に用いられる
受部6の他の実施例を示すものである。FIGS. 2 to 7 show other embodiments of the receiving portion 6 used in the present invention.
【0018】図2(a)、(b)は成形型5の外周の一
部に成形型5の上面と同一平面を形成する受部6を一体
的に突設し、この受部6上に落下したガラスゴブ中間体
9を進退移動自在な押し棒20によって凹部7内に落と
し込むようにしたものである。2 (a) and 2 (b), a receiving portion 6 which forms the same plane as the upper surface of the molding die 5 is integrally provided on a part of the outer periphery of the molding die 5, and the receiving portion 6 is provided on the receiving portion 6. The fallen glass gob intermediate 9 is dropped into the recess 7 by a push rod 20 which can move forward and backward.
【0019】図3は図2に示した実施例の変形例で、リ
ング状に形成された受部6を成形型5の外周に嵌合固定
したものである。FIG. 3 shows a modification of the embodiment shown in FIG. 2 in which a ring-shaped receiving portion 6 is fitted and fixed to the outer periphery of a molding die 5.
【0020】図4は流出パイプ1の直下で成形型5の上
方に受部6を成形型5とは別個に固定配置し、この受部
6上に落下したガラスゴブ中間体9を、ノズル21から
噴射される気体によって凹部7に落とし込むようにした
ものである。FIG. 4 shows that the receiving part 6 is fixedly disposed separately from the molding die 5 directly below the outflow pipe 1 and above the molding die 5, and the glass gob intermediate body 9 dropped on this receiving part 6 is passed through the nozzle 21. The gas is injected into the recess 7.
【0021】図5は流出パイプ1の直下で成形型5の上
方に受部6を軸22を中心として上下方向に回動自在に
配設し、この受部6を水平状態から二点鎖線で示すよう
に傾斜させることによりガラスゴブ中間体9を凹部7に
落とし込むようにしたものである。FIG. 5 shows that the receiving portion 6 is disposed above the molding die 5 directly below the outflow pipe 1 so as to be rotatable up and down around a shaft 22. The receiving portion 6 is shown by a two-dot chain line from a horizontal state. The glass gob intermediate 9 is dropped into the recess 7 by being inclined as shown.
【0022】図6は図1に示した実施例の変形例で、成
形型5の上面に設けられた受部6を成形型5の中心に向
かって傾斜する斜面に形成したものである。FIG. 6 shows a modification of the embodiment shown in FIG. 1, in which a receiving portion 6 provided on the upper surface of a molding die 5 is formed on a slope inclined toward the center of the molding die 5.
【0023】図7は成形型5の上面を受部6とし、受部
6上のガラスゴブ中間体9を凹部7内に移す際、成形型
5を矢視線方向に急速に水平移動させ、慣性を利用して
ガラスゴブ中間体9を凹部7内に落下収納するようにし
たものである。この場合、成形型5はターンテーブルの
上面外周部に円周方向に等間隔をおいて複数個配設され
ており、ターンテーブルが一定角度ずつ間欠的に回動さ
れるように構成されているので、この回動を利用してガ
ラスゴブ中間体9を落下させればよい。FIG. 7 shows the upper surface of the molding die 5 as the receiving portion 6, and when the glass gob intermediate 9 on the receiving portion 6 is moved into the concave portion 7, the molding die 5 is rapidly moved horizontally in the direction of the arrow to reduce the inertia. The glass gob intermediate 9 is dropped and stored in the concave portion 7 by utilizing. In this case, a plurality of molds 5 are arranged at equal intervals in the circumferential direction on the outer peripheral portion of the upper surface of the turntable, and the turntable is configured to be intermittently rotated by a predetermined angle. Therefore, the glass gob intermediate 9 may be dropped using this rotation.
【0024】なお、本発明において、受部6と、受部6
からガラスゴブ中間体9を凹部7に移す方法としては上
記した実施例に特定されるものではなく、本発明の要旨
を逸脱しない範囲において種々の変形、変更が可能であ
る。また、本発明は成形型5内にガラスゴブ中間体9を
収納して気体Aにより冷却することによりガラスゴブ1
4を製造するようにしたが、これに限らず受部6上に放
置して自然冷却させるようにしてもよい。In the present invention, the receiving portion 6 and the receiving portion 6
The method of transferring the glass gob intermediate 9 into the recess 7 from is not limited to the above-described embodiment, and various modifications and changes can be made without departing from the gist of the present invention. The present invention also provides a glass gob 1 by storing a glass gob intermediate 9 in a mold 5 and cooling it with gas A.
4 is manufactured, but the present invention is not limited to this, and it may be left on the receiving portion 6 and naturally cooled.
【0025】[0025]
【発明の効果】以上述べたように本発明に係るガラスゴ
ブ中間体の製造方法にあっては、流出パイプの先端と受
部の距離を、ガラスゴブ中間体の重量に基づいて定めら
れた距離に一定に保ちつつ、所定粘度の溶融ガラスを前
記流出パイプより流下させて該溶融ガラスの先端を前記
受部により受け止め、この溶融ガラスにくびれ部を形成
し、該くびれ部より先端側の溶融ガラスの重量が一定の
重量に達したときに、くびれ部より先端側の溶融ガラス
を分離することによりガラスゴブ中間体を製造するよう
にしたので、常に一定重量のガラスゴブ中間体を得るこ
とができる。すなわち、流出パイプと受部の距離を一定
に保っておくと、受部に受け止められた溶融ガラスは所
定重量になるとくびれ部より先端側が自然に切れて流出
パイプから分離するので、重量が一定したガラスゴブ中
間体を製造することができる。また本発明に係るガラス
ゴブの製造方法は、上記したガラスゴブ中間体の冷却に
際して成形型の凹部内に気体を吹き込みガラスゴブ中間
体を浮かせるようにしているので、表面にキズや汚れの
ないガラスゴブを製造することができる。また、成形型
に溶融ガラスを受ける受部と、ガラスゴブ中間体を収容
する凹部を設けているので、ガラスゴブとその中間体の
製造装置を簡素化することができる。As described above, in the method for manufacturing a glass gob intermediate according to the present invention, the distance between the tip of the outflow pipe and the receiving portion is fixed to a distance determined based on the weight of the glass gob intermediate. The molten glass having a predetermined viscosity is caused to flow down from the outflow pipe while receiving the tip of the molten glass by the receiving portion, and a constricted portion is formed in the molten glass. When a certain weight is reached, the glass gob intermediate is manufactured by separating the molten glass on the tip side from the constricted portion, so that a glass gob intermediate having a constant weight can always be obtained. In other words, if the distance between the outflow pipe and the receiving portion is kept constant, the molten glass received by the receiving portion will be cut off naturally at the tip side from the constricted portion at a predetermined weight and separated from the outflow pipe, so that the weight is constant. A glass gob intermediate can be produced. In the method for manufacturing a glass gob according to the present invention, a gas is blown into the concave portion of the mold during the cooling of the above-mentioned glass gob intermediate so that the glass gob intermediate is floated. be able to. Further, since the receiving portion for receiving the molten glass and the concave portion for accommodating the glass gob intermediate are provided in the mold, the manufacturing apparatus for the glass gob and the intermediate can be simplified.
【図1】(a)〜(e)は本発明に係るガラスゴブとそ
の中間体の製造方法の各工程とこの方法に使用する製造
装置の縦断面図である。1 (a) to 1 (e) are longitudinal sectional views of each step of a method for producing a glass gob and an intermediate thereof according to the present invention, and a production apparatus used for this method.
【図2】(a)、(b)は本発明に用いられる受部の他
の実施例を示す断面図および平面図である。FIGS. 2A and 2B are a cross-sectional view and a plan view showing another embodiment of a receiving portion used in the present invention.
【図3】図2に示した受部の変形例を示す平面図であ
る。FIG. 3 is a plan view showing a modification of the receiving portion shown in FIG.
【図4】本発明の受部の更に他の実施例を示す断面図で
ある。FIG. 4 is a sectional view showing still another embodiment of the receiving portion of the present invention.
【図5】本発明の受部の更に他の実施例を示す断面図で
ある。FIG. 5 is a sectional view showing still another embodiment of the receiving portion of the present invention.
【図6】図1に示した実施例の変形例を示す断面図であ
る。FIG. 6 is a sectional view showing a modification of the embodiment shown in FIG. 1;
【図7】本発明の受部の更に他の実施例を示す断面図で
ある。FIG. 7 is a sectional view showing still another embodiment of the receiving portion of the present invention.
1 流出パイプ 2 溶融ガラス 3 ヒーター 4 熱電対 5 成形型 6 受部 7 凹部 8 細孔 9 ガラスゴブ中間体 14 ガラスゴブ DESCRIPTION OF SYMBOLS 1 Outflow pipe 2 Molten glass 3 Heater 4 Thermocouple 5 Mold 6 Reception part 7 Depression 8 Pores 9 Glass gob intermediate 14 Glass gob
Claims (14)
該流出パイプの下方に配置された受部によって受けて、
所定重量のガラスゴブ中間体を製造する方法であって、 前記流出パイプの先端と受部の距離を、前記ガラスゴブ
中間体の重量に基づいて定められた距離に一定に保ちつ
つ、所定粘度の溶融ガラスを前記流出パイプより流下さ
せて該溶融ガラスの先端を前記受部により受け、該溶融
ガラスにくびれ部を形成し、このくびれ部より先端側の
溶融ガラスの重量が一定の重量に達したときに、前記く
びれ部より先端側の溶融ガラスが分離するようにして前
記ガラスゴブ中間体を得る ことを特徴とするガラスゴブ
中間体の製造方法。1. The molten glass flowing out of an outflow pipe,
And received by receiving portion disposed below the outflow pipe,
A method for producing a glass gob intermediate having a predetermined weight, wherein a distance between a tip of the outflow pipe and a receiving portion is set to the glass gob.
Maintain a fixed distance based on the weight of the intermediate
First, molten glass having a predetermined viscosity is allowed to flow down from the outflow pipe.
And the tip of the molten glass is received by the receiving portion.
A constriction is formed in the glass, and
When the weight of the molten glass reaches a certain weight,
Make sure that the molten glass on the tip side
A method for producing a glass gob intermediate, comprising obtaining the glass gob intermediate.
出パイプの先端と受部の間の距離を変えることにより調
節することを特徴とする請求項1記載のガラスゴブ中間
体の製造方法。2. The weight of the glass gob intermediate is
Adjust by changing the distance between the tip of the outlet pipe and the receiving part.
The method for producing a glass gob intermediate according to claim 1, wherein
より、該流出パイプから流下する溶融ガラスの粘度を調
整することを特徴とする請求項1または2記載のガラス
ゴブ中間体の製造方法。3. Controlling the temperature of said outlet pipe.
Control the viscosity of the molten glass flowing down from the outflow pipe.
The method for producing a glass gob intermediate according to claim 1 or 2, wherein:
の粘度を、35ポアズ以上とすることを特徴とする請求
項1,2または3記載のガラスゴブ中間体の製造方法。 4. A molten glass flowing out of the outflow pipe.
Wherein the viscosity is 35 poise or more.
Item 10. The method for producing a glass gob intermediate according to item 1, 2 or 3 .
5.4mm、当該流出パイプの内径が1.0〜2.0m
mである請求項1〜4のうちのいずれか1項記載のガラ
スゴブ中間体の製造方法。 5. An outer diameter of a tip of the outflow pipe is 2.0 to 2.0.
5.4 mm, the inner diameter of the outflow pipe is 1.0 to 2.0 m
The method for producing a glass gob intermediate according to any one of claims 1 to 4, wherein m is m .
動した後、該受部によって前記流下パイプから流下する
溶融ガラスを受けてガラスゴブ中間体を得、前記溶融ガ
ラスを受けた受部を該溶融ガラスを受ける位置から移動
する工程を、複数の受部を用いて順次繰り返し、所定の
重量を有するガラスゴブ中間体を連続して製造すること
を特徴とする請求項1〜5のうちのいずれか1項記載の
ガラスゴブ中間体の製造方法。 6. The receiving part is moved to a position for receiving molten glass.
After moving, it flows down from the downflow pipe by the receiving part
Upon receiving the molten glass, a glass gob intermediate is obtained.
Move the receiving part that received the lath from the position that receives the molten glass
Is sequentially repeated using a plurality of receiving portions, and a predetermined
The method for producing a glass gob intermediate according to any one of claims 1 to 5, wherein the glass gob intermediate having a weight is continuously produced.
載された方法によって製造されたガラスゴブ中間体を冷
却してガラスゴブを製造することを特徴とするガラスゴ
ブの製造方法。7. The method according to claim 1, wherein
A method for producing a glass gob, comprising cooling a glass gob intermediate produced by the method described above to produce a glass gob.
間に所望の形状に成形して前記形状を有するガラスゴブ
を得ることを特徴とする請求項7記載のガラスゴブの製
造方法。 8. The process until the glass gob intermediate is cooled
A glass gob having the above-mentioned shape by being formed into a desired shape in between
The method for producing a glass gob according to claim 7, wherein
気体の層を介して該成形型に収容して前記成形を行うこ
とを特徴とする請求項8記載のガラスゴブの製造方法。9. A glass gob intermediate using a mold.
The above-mentioned molding is carried out while being housed in the mold through a gas layer.
The method for producing a glass gob according to claim 8, wherein
受部と、前記ガラスゴブ中間体を収容する凹部とを有す
ることを特徴とする請求項9記載のガラスゴブの製造方
法。 10. The mold receives the molten glass.
It has a receiving portion and a concave portion for accommodating the glass gob intermediate.
The method for producing a glass gob according to claim 9, wherein:
れており、前記ガラスゴブ中間体の分離によって該ガラ
スゴブ中間体が前記凹部に落ちるようにして収容される
成形型を用いることを特徴とする請求項10記載のガラ
スゴブの製造方法。 11. The receiving portion is formed at an opening edge of the concave portion.
The glass gob intermediate is separated by the glass
Sgob intermediate is stored as falling into the recess
The glass according to claim 10, wherein a mold is used.
Sugob manufacturing method.
あることを特徴とする請求項10または11記載のガラ
スゴブの製造方法。 12. The recess has a tapered shape extending upward.
The glass according to claim 10 or 11, wherein
Sugob manufacturing method.
型の凹部の開口縁と接する位置で前記溶融ガラスを受け
るとともに、溶融ガラスの分離を行うことを特徴とする
請求項10,11または12記載のガラスゴブの製造方
法。 13. The molding apparatus according to claim 13 , wherein a center line of said outflow pipe is formed by said molding.
The molten glass is received at a position in contact with the opening edge of the concave portion of the mold.
And separates molten glass
A method for producing a glass gob according to claim 10, 11 or 12.
Law.
体を、該ガラスゴブ中間体の表面が軟化点以下の温度に
達するまで該成形型に収容した状態で冷却することを特
徴とする請求項10,11,12,13のうちのいずれ
か1項記載のガラスゴブの製造方法。 14. An intermediate glass gob housed in said mold.
The glass gob intermediate to a temperature below the softening point.
It is characterized in that it is cooled while it is housed in the mold until it reaches
Any one of claims 10, 11, 12, and 13 as a signature
The method for producing a glass gob according to claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP03271689A JP3077066B2 (en) | 1991-05-20 | 1991-05-20 | Each production method of glass gob and its intermediate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP03271689A JP3077066B2 (en) | 1991-05-20 | 1991-05-20 | Each production method of glass gob and its intermediate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH05147949A JPH05147949A (en) | 1993-06-15 |
| JP3077066B2 true JP3077066B2 (en) | 2000-08-14 |
Family
ID=17503479
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP03271689A Expired - Lifetime JP3077066B2 (en) | 1991-05-20 | 1991-05-20 | Each production method of glass gob and its intermediate |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3077066B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6827424B2 (en) | 2000-11-01 | 2004-12-07 | Canon Kabushiki Kaisha | Print apparatus and print method |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5738701A (en) * | 1995-04-05 | 1998-04-14 | Minolta Co., Ltd. | Glass gob production device and production method |
| JP2798208B2 (en) * | 1995-05-19 | 1998-09-17 | 株式会社オハラ | Glass gob molding method |
| JP4881579B2 (en) * | 2000-06-30 | 2012-02-22 | Hoya株式会社 | Optical glass and optical product using the same |
| US6494061B1 (en) * | 2000-08-21 | 2002-12-17 | Owens-Brockway Glass Container Inc. | Apparatus and method for conveying gobs of glass to a glass container forming machine |
| JP3929237B2 (en) * | 2000-09-21 | 2007-06-13 | Hoya株式会社 | Glass lump manufacturing method and manufacturing apparatus, glass molded product manufacturing method, and optical element manufacturing method |
| JP3853622B2 (en) * | 2001-09-20 | 2006-12-06 | Hoya株式会社 | Manufacturing method of glass molded body, manufacturing method of press-molded product, manufacturing method of glass optical element, and manufacturing apparatus of glass molded body |
| JP2008285413A (en) * | 2001-12-14 | 2008-11-27 | Hoya Corp | Method for producing glass molded body and method for producing optical element |
| US8091387B2 (en) | 2003-03-19 | 2012-01-10 | Hoya Corporation | Method of manufacturing glass articles, method of manufacturing glass gobs, and method of manufacturing optical elements |
| JP2009179532A (en) * | 2008-01-31 | 2009-08-13 | Ohara Inc | Method and apparatus for producing glass gob |
| US8616339B2 (en) | 2008-12-08 | 2013-12-31 | Mitsubishi Electric Corporation | Elevator control device |
| JP2011011937A (en) * | 2009-06-30 | 2011-01-20 | Ohara Inc | Method for manufacturing optical element |
| WO2019146000A1 (en) * | 2018-01-23 | 2019-08-01 | 日本電気硝子株式会社 | Airflow levitation type glass body production device and airflow levitation type glass body production method |
-
1991
- 1991-05-20 JP JP03271689A patent/JP3077066B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6827424B2 (en) | 2000-11-01 | 2004-12-07 | Canon Kabushiki Kaisha | Print apparatus and print method |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH05147949A (en) | 1993-06-15 |
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