JPH03164436A - Method and device for controlling molten glass level in glass melting device - Google Patents

Method and device for controlling molten glass level in glass melting device

Info

Publication number
JPH03164436A
JPH03164436A JP20350090A JP20350090A JPH03164436A JP H03164436 A JPH03164436 A JP H03164436A JP 20350090 A JP20350090 A JP 20350090A JP 20350090 A JP20350090 A JP 20350090A JP H03164436 A JPH03164436 A JP H03164436A
Authority
JP
Japan
Prior art keywords
glass
weight
glass melting
melting device
entire
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.)
Granted
Application number
JP20350090A
Other languages
Japanese (ja)
Other versions
JP2998977B2 (en
Inventor
Shigeru Asanuma
浅沼 茂
Hiroaki Takahara
宏明 高原
Shinji Namita
伸司 波田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hoya Corp
Original Assignee
Hoya Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hoya Corp filed Critical Hoya Corp
Publication of JPH03164436A publication Critical patent/JPH03164436A/en
Application granted granted Critical
Publication of JP2998977B2 publication Critical patent/JP2998977B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • 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
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B3/00Charging the melting furnaces

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Glass Melting And Manufacturing (AREA)

Abstract

PURPOSE:To keep the molten glass level in a glass melting device constant at all times by obtaining the amt. of molten glass in the melting device from the weight difference between the device itself and the device contg. molten glass and adjusting the amt. of glass raw material to be charged with the difference from the set value. CONSTITUTION:The glass melting device A consists of a crucible 1 having a molten glass discharge pipe 4, a heater 8 for the crucible, a heater 9 for the pipe 4, a heating furnace 5 for the crucible 1 and a base 10 for carrying the members, and the device A is placed on a weigher 11 such as a load cell. The glass raw powder 2 is charged into the crucible 1 from its feeder 13, heated and melted by the heater 8 to form molten glass 3 in the crucible 1. At this time, the weight of the entire melting device plus the molten glass 3 is measured by the weigher 11, the difference from the weight of the device A is obtained, and the amt. of molten glass 3 is obtained. A controller is driven based on the difference between the obtained molten glass amt. and the preset molten glass amt., the amt. of the raw glass to be supplied to the crucible from the feeder 13 is adjusted, and the level of the molten glass 3 in the crucible is always kept constant.

Description

【発明の詳細な説明】 (産業Lの利用分野〕 本発明は、ガラス溶融装置内のガラスの}夜位を調節す
る方法とその装置に関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Application in Industry L) The present invention relates to a method and apparatus for adjusting the temperature of glass in a glass melting apparatus.

〔従来の技術] 一般に,ガラスの溶融装置には、溶融ガラスの液位を検
出するための液面計が設置されている。
[Prior Art] Generally, a glass melting apparatus is equipped with a liquid level gauge for detecting the liquid level of molten glass.

この液面計を用いて、78融ガラスの液位を一定のレベ
ルに制御することにより、溶融装置内のガラスの}丸れ
が均一になりかつ溶融ガラスの流出圧力が一定になるの
で、溶融ガラスの品質の安定を図ることができると共に
、オーバーフローが防止されるので、操業の安全を図る
ことができる。
By controlling the liquid level of 78 molten glass to a constant level using this liquid level gauge, the glass in the melting device will be uniformly rounded and the outflow pressure of the molten glass will be constant. Since the quality of the glass can be stabilized and overflow can be prevented, operational safety can be ensured.

この液面計としては、接触抵抗式、放射線式,、jノ−
ザ式、マイクロ波弐等のいろいろなタイプのものが知ら
れている。
This liquid level gauge includes contact resistance type, radiation type, and j-node type.
Various types are known, such as the Z-type and the Microwave-2 type.

〔発明が解決しようとする課題] しかしながら、接触抵抗式液面計は、溶融ガラスの粘度
が大きい場合は精度が悪く、更に、この液面計の電極を
炉内に挿入ずるための炉体開口部から、炉内の反応ガス
が吹き出して炉体を侵食するので、炉体の損傷が大であ
る。
[Problems to be Solved by the Invention] However, the contact resistance type level gauge has poor accuracy when the viscosity of the molten glass is high, and furthermore, the contact resistance type level gauge has poor accuracy when the viscosity of the molten glass is high. The reactant gas inside the furnace blows out from the inside and erodes the furnace body, causing serious damage to the furnace body.

また、放射線式液面計の場合は、作業者の安全確保のた
め、漏れ線量を残らすようアイソトープ線源とアクセブ
ターの配置に留意しなければならず、充分なスペースと
日常管理が必要である。
In addition, in the case of radiation-type liquid level gauges, in order to ensure the safety of workers, care must be taken in the placement of the isotope source and acceptor to ensure that leakage radiation remains, and sufficient space and daily management are required. .

レーザ式液面計の場合も炉体に開口部が必要であるので
、前記接触抵抗式液面計と同様に、炉体の}員傷が大で
ある。
In the case of a laser type liquid level gauge, an opening is required in the furnace body, and as with the contact resistance type liquid level gauge, the furnace body is seriously damaged.

マイクロ波式液面計の場合は、導波管取付けのための開
口部が必要であるので、炉体の損傷が大である.更に、
導波管に付着した揮発物の除去等のメンテナンスが必要
である。
In the case of microwave level gauges, an opening is required for installing the waveguide, which can cause serious damage to the furnace body. Furthermore,
Maintenance such as removing volatile substances attached to the waveguide is required.

更に、これらの液面計はいずれも、投入原料が由状乙、
:なる投入場所近辺では、正確な液位の測定が困難であ
る。また、液面計によっては検出可能な液位の範囲が狭
いという欠点がある。
In addition, all of these liquid level gauges depend on the input raw material,
: It is difficult to accurately measure the liquid level near the injection site. Additionally, some liquid level meters have the disadvantage that the range of liquid levels that can be detected is narrow.

そこで本発明は、上記欠点をもつ液面計を用いないで、
液位を調節し、一定レベルに保持することができる方法
と装置を提供することを目的とする。
Therefore, the present invention does not use the liquid level gauge having the above-mentioned drawbacks, but
The object is to provide a method and a device by which the liquid level can be adjusted and maintained at a constant level.

〔課題を解決するための手段] この目的を達或するために、本発明によるガラス溶融装
置の液位調節方法は、所定のガラス重量を設定し、ガラ
スを含むガラス溶融装置全体の重量を秤量し、このガラ
ス溶融装置全体の重量からガラス溶融装考の風袋重量を
差し引いてガラス重量を求め、このガラス重量と、前記
の設定したガラス重量とを比較し、この比較に基づいて
、ガラス溶融装置へのガラス原料の補充投入量を調節す
ることを特徴としている. 他の発明による液位調節方法は、所定重量のガラスを含
むガラス溶融装置全体の重量を設定し、ガラスを含むガ
ラス溶融装置全体の重量を秤量し、設定したガラス溶融
装置全体の乗鼠と、秤量したガラス溶融装置全体の重量
とを比較し、この比較に基づいて、ガラス溶融装置への
ガラス原料の補充投入量を調節することを特徴としてい
る.他の発明によるガラス溶融装置の液位羽節装置は、
ガラスを含むガラス溶融装置全体の重量を秤量する秤量
装置と、ガラス溶融装置へガラス原料を投入する原料投
入機に付設された投入量調節装置ど、前記秤量装置と投
入量調節装置との間に接続配置され、秤量装置によって
秤量されたガラス溶融装置全体の重量からガラス溶融装
置の風袋重量を差し引いてガラス重量を求め、このガラ
ス重量と設定されたガラス重量との比較に基づいて投入
量調節装置を制御する制御装置とを備えていることを特
徴としている. 更に、他の発明による液位gJ1節装置は、ガラスを含
むガラス溶融装置全体の重量を秤量する秤量装誼と、ガ
ラス溶融装置へガラス原料を投入する原料投入機に付設
された投入量調節装置と、前記秤量装置と投入量調節装
置との間に接続配置され、設定されたガラス溶融装置全
体の重量と、秤量装置によって秤量されたガラス溶融装
置全体の重量とを比較し、この比較に基づいて投入量調
節装置を制御する制御装置とを備えていることを特徴と
している. 〔実施例〕 次に、図を参照して本発明の実施例を詳しく説明する. 第1図は、本実施例によるガラス溶融装置Aの縦斯面を
示している.第l図において、1は投入された未溶融ガ
ラス原料2を溶融するガラス溶融ルツボ、3は溶融ガラ
ス、4はこのガラス溶融ルッポ1の底部に接続された流
出パイプである.ガラス溶融ルツボ1と流出パイプ4は
それぞれ、炉体5,6によって取囲まれ、支持台7を介
して炉体5に支持されている.炉体5と6は互いに連結
されている.ガラス溶融ルッポ1と炉体5の間、および
流出バイプ4と炉体6の間にはそれぞれ、加熱用ヒータ
8,9が設けられている.10は炉体基部である. 前記のガラス溶融ルツボ1、未溶融ガラス原料2、溶融
ガラス3、流出パイブ4、炉体5.6、支持台7、加熱
用ヒータ8,9および炉体基部10からなるガラス溶融
装置Aの全重量は、3個所または4個所で秤量装置とし
てのロードセル(ひずみゲージ)11で支持され、この
ロードセル11は制御装置12に接続されている。この
制御装置12はロードセルl1からの信号に基づいて、
ガラス溶融装置Aの重量を検出する重量検出部と、この
重量から、予め測定してあるガラス溶融装置Aの空の重
量、すなわち風袋重量を差し引いてガラスの重量を求め
る演算部と、表示部と、このガラスの重量に基づいて、
原料投入機13に付設された投入量調節装置14を制御
する制御部とを備え、プログラミング可能である。前記
原料投入機l3は例えば電磁フィーダやスクリューフィ
ーダであり、投入量調節装置14は制御−装置l2から
供給された信号に基づいて、原料投入機13の振動数ま
たは回転数、作動時間等を制御してガラス原料の投入量
を調節する。
[Means for Solving the Problem] In order to achieve this object, the method for adjusting the liquid level of a glass melting apparatus according to the present invention includes setting a predetermined weight of glass, and weighing the entire weight of the glass melting apparatus including the glass. Then, the glass weight is determined by subtracting the tare weight of the glass melting device from the weight of the entire glass melting device, and this glass weight is compared with the glass weight set above, and based on this comparison, the glass melting device is It is characterized by adjusting the amount of glass raw material added to the glass. A liquid level adjustment method according to another invention includes: setting the weight of the entire glass melting device containing a predetermined weight of glass; weighing the entire weight of the glass melting device including the glass; and weighing the entire set glass melting device; The weighed weight of the entire glass melting apparatus is compared with that of the entire glass melting apparatus, and based on this comparison, the amount of glass raw material to be replenished into the glass melting apparatus is adjusted. A liquid level barb device for a glass melting device according to another invention includes:
A weighing device that weighs the entire weight of the glass melting device including glass, and a charging amount adjusting device attached to a raw material feeder that feeds glass raw materials into the glass melting device, between the weighing device and the charging amount adjusting device. The tare weight of the glass melting device is subtracted from the weight of the entire glass melting device that is connected and arranged and weighed by the weighing device to obtain the glass weight, and the input amount adjustment device is adjusted based on the comparison between this glass weight and the set glass weight. It is characterized by being equipped with a control device that controls the Furthermore, the liquid level gJ1 regulating device according to another invention includes a weighing device for weighing the entire weight of the glass melting device including glass, and an input amount adjusting device attached to a raw material feeder that feeds glass raw materials into the glass melting device. The weight of the entire glass melting apparatus connected and arranged between the weighing device and the input amount adjusting device is compared with the weight of the entire glass melting device weighed by the weighing device, and based on this comparison, It is characterized by being equipped with a control device that controls the input amount adjusting device. [Example] Next, an example of the present invention will be described in detail with reference to the drawings. FIG. 1 shows the longitudinal plane of the glass melting apparatus A according to this embodiment. In FIG. 1, 1 is a glass melting crucible for melting the input unmelted glass raw material 2, 3 is molten glass, and 4 is an outflow pipe connected to the bottom of this glass melting pot 1. The glass melting crucible 1 and the outflow pipe 4 are surrounded by furnace bodies 5 and 6, respectively, and are supported by the furnace body 5 via a support stand 7. Furnace bodies 5 and 6 are connected to each other. Heaters 8 and 9 are provided between the glass melting pipe 1 and the furnace body 5, and between the outflow pipe 4 and the furnace body 6, respectively. 10 is the base of the furnace body. The entire glass melting apparatus A consists of the glass melting crucible 1, the unmelted glass raw material 2, the molten glass 3, the outflow pipe 4, the furnace body 5.6, the support stand 7, the heaters 8 and 9, and the furnace body base 10. The weight is supported at three or four locations by load cells (strain gauges) 11 serving as weighing devices, and this load cell 11 is connected to a control device 12 . Based on the signal from the load cell l1, this control device 12
a weight detection section that detects the weight of the glass melting device A; a calculation section that calculates the weight of the glass by subtracting the empty weight of the glass melting device A measured in advance, that is, the tare weight from this weight; and a display section. , based on the weight of this glass,
It is equipped with a control unit that controls the input amount adjusting device 14 attached to the raw material input machine 13, and is programmable. The raw material feeder l3 is, for example, an electromagnetic feeder or a screw feeder, and the feed amount adjustment device 14 controls the vibration frequency or rotational speed, operating time, etc. of the raw material feeder 13 based on the signal supplied from the control device l2. to adjust the input amount of glass raw materials.

上記構造のガラス溶融装置の場合には予め、所定のガラ
ス重量が制御装置l2に入力(設定)される.この所定
のガラス重量は、ガラス溶融ルッポl内のガラスの所望
の液位に相当する重量、すなわち液位が所望のレベルに
あるときのガラス重量でもよいし、投入を開始すべき重
量でもよい。
In the case of the glass melting apparatus having the above structure, a predetermined glass weight is input (set) to the control device l2 in advance. This predetermined glass weight may be the weight corresponding to the desired liquid level of the glass in the glass melter, ie, the glass weight when the liquid level is at the desired level, or it may be the weight at which charging should begin.

更に、ガラス7が入っていない溶融装置Aの空の重量(
風袋重量)をロードセルIIによって予め秤量しておく
。次に、原料投入機13から原料を投入した後、溶融装
置Aの溶融中の全重量をロードセル11によって秤量し
、制御装置12において、前記全重量から風袋重量を差
し引くことにより、ガラス重量(未溶融ガラス原料2を
含む)を求める.このガラス重量と、設定したガラス重
量との比較に基づいて、制御装置12は投入量調節装置
l4を制御し、原料投入機l3からの補充投入量を調節
する.それによって、ガラス溶融ルッポl内のガラス3
の液位を所望のレベルに保持することができる。
Furthermore, the empty weight of melting device A without glass 7 (
The tare weight) is weighed in advance using a load cell II. Next, after inputting raw materials from the raw material input device 13, the total weight of the melting device A during melting is weighed by the load cell 11, and the control device 12 subtracts the tare weight from the total weight to calculate the glass weight (unused). (including molten glass raw material 2). Based on the comparison between this glass weight and the set glass weight, the control device 12 controls the input amount adjusting device l4 to adjust the replenishment input amount from the raw material input device l3. Thereby, the glass 3 in the glass melting
can maintain the liquid level at a desired level.

上記のように溶融ガラス装置A全体の重量を秤?してガ
ラスの投入量を調節するようにしたので、従来のような
多くの欠点を有する液面計を用いないで、溶融ガラスの
液位を制御することができる。
Weigh the entire weight of molten glass equipment A as above? Since the amount of glass input is adjusted by using the molten glass, the liquid level of the molten glass can be controlled without using a liquid level gauge which has many drawbacks as in the prior art.

依って、この液位制御方法は、任意の液位で、正確な液
位制御を可能にする。また、炉体に開口部を設ける必要
がないので、侵食による炉体の損傷を生じない。更に、
作業者の安全確保のための充分なスペースや日常管理が
不要であり、秤量装置11のメンテナンスが簡単である
.更に、未溶融ガラス原料2も含めて秤量することがで
きる。
Therefore, this liquid level control method enables accurate liquid level control at any liquid level. Further, since there is no need to provide an opening in the furnace body, damage to the furnace body due to erosion does not occur. Furthermore,
There is no need for sufficient space or daily management to ensure worker safety, and maintenance of the weighing device 11 is easy. Furthermore, the unmolten glass raw material 2 can also be weighed.

次に、第2図を参照して、前記実施例によるガラス液位
調節方法の具体例について説明する。
Next, with reference to FIG. 2, a specific example of the method for adjusting the glass liquid level according to the embodiment described above will be described.

先ず、ガラス原料を投入する前に、制御装置12の演算
部において、投入開始重量設定値W■を10kgに設定
し、原料投入機l3の投入量を一回の投入指令当りo.
s lCgに設定する.更に、ガラス溶融装置Aの風袋
重量を入力し、その都度の秤量重量からこの風袋重量を
差し引くようにセットする(風袋引き).それによって
、表示部に表示されるガラス重量現在値W■はOlcg
になる.次に、原?!′−1投入機I3G、二よってガ
ラス原FTを12kg投入し(力゛ラス重量現在値wr
y = 12kg ) 、ガラス溶融ルッポ1の温度を
iooo’cに保持して溶融3゛る。
First, before charging the glass raw materials, the charging start weight set value W■ is set to 10 kg in the calculation section of the control device 12, and the charging amount of the raw material charging machine 13 is set to 0.0 kg per charging command.
Set to s lCg. Furthermore, input the tare weight of the glass melting apparatus A, and set it to subtract this tare weight from the weighed weight each time (tare subtraction). As a result, the current glass weight value W shown on the display is Olcg
become. Next, Hara? ! '-1 Input machine I3G, 2 Input 12 kg of glass raw material FT (force glass current weight wr
y = 12 kg), the temperature of the glass melting tube 1 is maintained at iooo'c and the glass is melted 3゜.

その後、流出パイブ4の温度を950″Cに設定し、}
容L11!ガラスを浦。出する。}容融ガラスの流出に
より、ガラス重量現在値W,,が10kg以下になると
、制御装置12によって原料投入指令が発せられ、投入
量調節装濯14が原料投入機13を作動させ、0.5k
gのガラス原料を投入する。その結果、ガラス本星現在
値Wrvは10kgを超える。
After that, set the temperature of the outflow pipe 4 to 950″C,
Yong L11! Ura the glass. put out }When the current value of the glass weight W,, becomes 10 kg or less due to the outflow of molten glass, the control device 12 issues a raw material input command, the input amount adjustment device 14 operates the raw material input machine 13, and
g of glass raw material is added. As a result, the glass main star current value Wrv exceeds 10 kg.

その後再び、ガラス重量現在値W,vがtokg以下に
なると、原ギ1投入指令が発せられ、0.5kgの原料
が投入される。これを繰り返すことにより5,ガラス電
量現在値W■を、10kg+0.5 kgから10kg
までの範囲に維持することが可能である。
Thereafter, when the current glass weight value W,v becomes less than tokg again, a raw material 1 loading command is issued, and 0.5 kg of raw material is loaded. By repeating this, the current value of glass electricity W■ can be changed from 10 kg + 0.5 kg to 10 kg.
It is possible to maintain the range up to

このように流出バイブ4からの流出に伴う減少分を補充
投入することにより、液面計を用いることなく、ガラス
の液位を一定に保ち、かつガラスの品貢の安定と操業の
安全を図ることができる。
By replenishing the amount decreased due to the outflow from the outflow vibrator 4 in this way, the liquid level of the glass can be kept constant without using a liquid level gauge, and the supply of glass can be stabilized and the operation be safe. be able to.

次に、ガラス液位調節方法の変形例について説明する。Next, a modification of the glass liquid level adjustment method will be described.

この変形例では、所定重量のガラスを含むガラス溶融装
置A全体の重量が、ガラス溶融装置重量設定値(csr
)として制御装置12に入力される。このガラスの所定
重量は、ガラス溶融ルッポi内のガラスの所望の液位に
相当する重量、すなわち液位が所望のレベルにあるとき
のガラスの重量でもよいし、投入を開始すべき重量でも
よい。制御装置12では、ロードセル11によって測定
された、ガラスを含むガラス溶融装置A全体のその都度
の重景(ガラス溶融装置電量現在値GpV)と、前記の
ガラス溶融装置重量設定値(G3F)とが比較される.
この比較に基づいて、投入量調節装置l4を制御し、原
料投入機l3からの補充投入量を調節することにより、
溶融ガラスの液位を調節する. この方法の具体例を第3図に基づいて説明すると、先ず
、所定重量のガラスを含むガラス溶融装置A全体の重量
を、ガラス溶融装置重量設定値G■として制御装瀝12
の演算部に人力する。この場合、所定重量のガラス原料
を原料投入機13によって投入し、このガラスを含むガ
ラス溶融装置全体の重量を秤量し、この重量をガラス溶
融装置重量設定値G 5 pとする。更に、所望のガラ
ス重量とガラス溶融装置Aの風袋重量が予め判っている
場合(こは、ガラス}容融装置を秤量しないでガラス7
容融装置重量設定値G,,を入力してもよい。このとき
、ガラス溶融装置Aの風袋重量を150 kg、ガラス
の重量を10kgとすると、ガラス溶融装置重量設定値
G1は160 kgとなる。
In this modification, the weight of the entire glass melting apparatus A including a predetermined weight of glass is determined by the glass melting apparatus weight setting value (csr
) is input to the control device 12 as follows. This predetermined weight of glass may be the weight corresponding to the desired liquid level of the glass in the glass melter Lupo i, i.e. the weight of the glass when the liquid level is at the desired level, or it may be the weight at which charging should start. . In the control device 12, a detailed view of the entire glass melting apparatus A including glass measured by the load cell 11 (glass melting apparatus electric power current value GpV) and the above-mentioned glass melting apparatus weight setting value (G3F) are calculated. Will be compared.
Based on this comparison, by controlling the input amount adjusting device l4 and adjusting the replenishment input amount from the material inputting machine l3,
Adjust the liquid level of molten glass. A specific example of this method will be explained based on FIG.
The calculation section is manually operated. In this case, a predetermined weight of glass raw material is charged by the raw material feeder 13, the weight of the entire glass melting apparatus including this glass is weighed, and this weight is set as the glass melting apparatus weight setting value G 5 p. Furthermore, if the desired glass weight and the tare weight of the glass melting device A are known in advance (in this case, the glass melting device A), the glass 7.
The melter weight setting value G, , may also be input. At this time, assuming that the tare weight of the glass melting apparatus A is 150 kg and the weight of the glass is 10 kg, the glass melting apparatus weight setting value G1 is 160 kg.

制御装置12;よ、ガラスを含むガラス溶融装置A全体
のその都度の重量(ガラス溶融装置重量現在値G F 
v )が、前記ガラス溶融装置重量設定値G,,以下に
なったときに、原料投入機13によってガラス原料を0
.5kg補充投入するようにプログラミングされている
. 溶融ガラスの流出を開始した後、ロードセル11によっ
て測定されたガラス溶融装置重量現在値GPvが160
 kg以下になると、制御装置12によってガラス原料
投入指令が発せられ、投入量調節装置■4および原料投
入機13によってガラス原料が0.5kg補充投入され
る。それによって、ガラス溶融装置重量現在値GPvが
約160.5 kgとなり(ガラス重量が約10.5k
gになり)、その後再びガラス溶融装夏重量現在値が1
60kg以下になると、原料投入指令が発せられ、0.
5kgの原料が投入される。
Control device 12: The respective weight of the entire glass melting apparatus A including the glass (glass melting apparatus weight current value GF
v) becomes equal to or less than the glass melting device weight set value G,, the raw material feeder 13 removes the glass raw material to 0.
.. It is programmed to refill 5 kg. After the molten glass starts flowing out, the current weight GPv of the glass melting device measured by the load cell 11 is 160.
kg or less, the control device 12 issues a glass raw material charging command, and the charging amount adjusting device 4 and the raw material charging machine 13 replenish 0.5 kg of glass raw material. As a result, the current weight of the glass melting equipment GPv is approximately 160.5 kg (the glass weight is approximately 10.5 kg).
g), and then the current value of the summer weight of the glass melter is 1
When the weight falls below 60kg, a raw material input command is issued and the weight is 0.
5 kg of raw material is input.

これを繰り返すことにより、ガラス液位が一定に保持さ
れる. 次に、第4図、第5図および第6図を参隔して、ガラス
溶融装置八の秤量構造の変形例を説明する。
By repeating this, the glass liquid level is kept constant. Next, a modification of the weighing structure of the glass melting apparatus 8 will be described with reference to FIGS. 4, 5, and 6.

第4図の場合には、ガラス溶融装置Aを架台XOaに載
せて上側から吊り下げて秤量している。
In the case of FIG. 4, the glass melting apparatus A is placed on a pedestal XOa and suspended from above for weighing.

そのため、架台IQaとロードセルllaは吊り下げ捧
l5で連結されている。
Therefore, the pedestal IQa and the load cell lla are connected by a suspension l5.

第5図の場合には、ガラス?8融装置Aの炉体5の上縁
に、断面L字形のホルダー16が取付けられ、このホル
ダー16が吊り下げ捧17を介してロードセルllbに
吊り下げられている.第6図の場合には、ガラス溶融装
置Aを載せる架台10bの一端がロードセルlieによ
って支持され、他端が定置された軸1Bに、上下方向に
所定の範囲内で揺動可能に支持されている。この場合、
ロードセルllcは1個所または2個所に配置するだけ
でよい. なお、前記秤量構造の場合には、ロードセルの数と配置
位置は任意に選択可能である.以上、実施例について説
明したが、本発明は上記以外のいろいろな種類のガラス
溶融装置に適用可能である.例えば、溶融槽、脱泡槽お
よび攪拌機構付均質化槽を備えた多槽式のガラス溶融装
置も、炉体基部上に設置してその重量を秤量することが
できる.この場合、溶融槽、脱泡槽および均質化槽は炉
体基部上に並べて配置され、均質化槽の底に流出パイプ
が接続される. 更に、加熱用ヒータとしては通常カンタル線、SiC抵
抗発熱体等が用いられるが、他の発熱手段を用いてもさ
しつかえない。
In the case of Figure 5, glass? A holder 16 having an L-shaped cross section is attached to the upper edge of the furnace body 5 of the melting apparatus A, and this holder 16 is suspended from the load cell Ilb via a hanging rod 17. In the case of FIG. 6, one end of the pedestal 10b on which the glass melting apparatus A is mounted is supported by a load cell ie, and the other end is supported by a fixed shaft 1B so as to be able to swing vertically within a predetermined range. There is. in this case,
Load cells only need to be placed in one or two locations. In addition, in the case of the above-mentioned weighing structure, the number and arrangement position of load cells can be arbitrarily selected. Although the embodiments have been described above, the present invention can be applied to various types of glass melting apparatuses other than those described above. For example, a multi-vessel glass melting apparatus equipped with a melting tank, a defoaming tank, and a homogenizing tank with a stirring mechanism can also be installed on the base of the furnace body and its weight can be measured. In this case, the melting tank, defoaming tank, and homogenization tank are arranged side by side on the base of the furnace body, and the outflow pipe is connected to the bottom of the homogenization tank. Furthermore, although a Kanthal wire, a SiC resistance heating element, etc. are usually used as the heater, other heating means may also be used.

更に、両加熱用ヒータにフレキシブルな平iJ41を接
続し、この平曙線の他端を加熱用ヒータの柏電用電線に
接続すると共に、外部の適当な支持装置で支持すること
ができる。それによって、給電4. 用電線の重量が炉体に作用しなくなり、ガラス溶融装置
の秤量に対する給電用電線の重量の影響を除去すること
ができる. 更に、ロードセル以外の秤量装置、例えば電磁はかり等
を用いることができる。
Further, a flexible flat iJ41 can be connected to both heaters, and the other end of the flat wire can be connected to the electric wire of the heater, and can be supported by an appropriate external support device. Thereby, power supply 4. The weight of the power supply wire no longer acts on the furnace body, and the influence of the weight of the power supply wire on the weight of the glass melting equipment can be eliminated. Furthermore, weighing devices other than load cells, such as electromagnetic scales, can be used.

〔発明の効果〕〔Effect of the invention〕

本発明は、液面計を用いないで、ガラス溶融装置の重量
に基づいて投入量を制御することにより、ガラスの液位
を[ffするようにしたので、広い範囲内の任意の液位
で、正確な液位調節を行うことができ、その結果溶融ガ
ラスの品質の安定と操業の安全を図ることができる。ま
た、炉体の損傷を生じることがなく、作業者の安全確保
が不要で、メンテナンスが簡単である。
In the present invention, the liquid level of the glass is adjusted to [ff] by controlling the amount of input based on the weight of the glass melting device without using a liquid level gauge, so that the liquid level can be set at any liquid level within a wide range. , accurate liquid level adjustment can be performed, and as a result, the quality of molten glass can be stabilized and operation safety can be ensured. Furthermore, the furnace body is not damaged, there is no need to ensure the safety of workers, and maintenance is simple.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の実施例によるガラス溶融装置を示す縦
断面図、第2図はガラス液位調節方法を示すフローチャ
ート、第3図はガラス液位調節方法の変形例を示すフロ
ーチャート、第4図、第5図および第6図はいろいろな
秤量構造を示す概略図である. 1・・・ガラス溶融ルッポ、 2・・・未溶融ガラス原
料、 3・・・溶融ガラス、 4・・・流出パイプ、 
 5,6・・・炉体、  7・・・支持台、  8.9
・・・加熱用ヒータ、  10・・・炉体基部、  I
Oa,tob・・・架台、11.lla,llb,IL
c・ ・・ロードセル(秤量装置)、  12・・・制
御装置、  l3・・・原料投入機、  l4・・・投
入量調節装置、15.17・・・吊り下げ棒、 16・
・・ホルダー  18・・・軸、 A・・・ガラス溶融
装置
FIG. 1 is a longitudinal sectional view showing a glass melting apparatus according to an embodiment of the present invention, FIG. 2 is a flowchart showing a method for adjusting the glass liquid level, FIG. 3 is a flowchart showing a modification of the method for adjusting the glass liquid level, and FIG. Figures 5 and 6 are schematic diagrams showing various weighing structures. 1...Glass molten Lupo, 2...Unmelted glass raw material, 3... Molten glass, 4...Outflow pipe,
5, 6...furnace body, 7...support stand, 8.9
... Heating heater, 10... Furnace body base, I
Oa, tob... mount, 11. lla, llb, IL
c...Load cell (weighing device), 12...Control device, l3...Raw material feeder, l4...Input amount adjustment device, 15.17...Hanging rod, 16.
...Holder 18...Shaft, A...Glass melting device

Claims (1)

【特許請求の範囲】 1、所定のガラス重量を設定し、 ガラスを含むガラス溶融装置全体の重量を秤量し、 このガラス溶融装置全体の重量からガラス溶融装置の風
袋重量を差し引いてガラス重量を求め、このガラス重量
と、前記の設定したガラス重量とを比較し、 この比較に基づいて、ガラス溶融装置へのガラス原料の
補充投入量を調節することを特徴とする、ガラス溶融装
置のガラス液位調節方法。 2、所定重量のガラスを含むガラス溶融装置全体の重量
を設定し、 ガラスを含むガラス溶融装置全体の重量を秤量し、 設定したガラス溶融装置全体の重量と、秤量したガラス
溶融装置全体の重量とを比較し、この比較に基づいて、
ガラス溶融装置へのガラス原料の補充投入量を調節する
ことを特徴とする、ガラス溶融装置のガラス液位調節方
法。 3、ガラスを含むガラス溶融装置全体の重量を秤量する
秤量装置と、 ガラス溶融装置へガラス原料を投入する原料投入機に付
設された投入量調節装置と、 前記秤量装置と投入量調節装置との間に接続配置され、
秤量装置によって秤量されたガラス溶融装置全体の重量
からガラス溶融装置の風袋重量を差し引いてガラス重量
を求め、このガラス重量と設定されたガラス重量との比
較に基づいて投入量調節装置を制御する制御装置とを備
えていることを特徴とするガラス溶融装置のガラス液位
調節装置。 4、ガラスを含むガラス溶融装置全体の重量を秤量する
秤量装置と、 ガラス溶融装置へガラス原料を投入する原料投入機に付
設された投入量調節装置と、 前記秤量装置と投入量調節装置との間に接続配置され、
設定されたガラス溶融装置全体の重量と、秤量装置によ
って秤量されたガラス溶融装置全体の重量とを比較し、
この比較に基づいて投入量調節装置を制御する制御装置
とを備えていることを特徴とするガラス溶融装置のガラ
ス液位調節装置。
[Claims] 1. Set a predetermined glass weight, weigh the entire glass melting device including the glass, and calculate the glass weight by subtracting the tare weight of the glass melting device from the weight of the entire glass melting device. , the glass liquid level of the glass melting apparatus is characterized in that the glass weight is compared with the glass weight set above, and based on this comparison, the amount of supplementary glass raw material input into the glass melting apparatus is adjusted. Adjustment method. 2. Set the weight of the entire glass melting device containing a predetermined weight of glass, weigh the entire glass melting device including glass, and calculate the set weight of the entire glass melting device and the weighed weight of the entire glass melting device. and based on this comparison,
A method for adjusting a glass liquid level in a glass melting device, the method comprising adjusting the amount of glass raw material added to the glass melting device. 3. A weighing device that weighs the entire weight of the glass melting device including glass; A charge amount adjustment device attached to a raw material feeder that feeds glass raw materials into the glass melting device; and a combination of the weighing device and the charge amount adjustment device. placed connected between
Control that subtracts the tare weight of the glass melting device from the weight of the entire glass melting device weighed by the weighing device to obtain the glass weight, and controls the input amount adjusting device based on a comparison between this glass weight and a set glass weight. A glass liquid level adjusting device for a glass melting device, characterized in that it is equipped with a device. 4. A weighing device that weighs the entire weight of the glass melting device including the glass, a charging amount adjusting device attached to a raw material feeder that feeds glass raw materials into the glass melting device, and a combination of the weighing device and the charging amount adjusting device. placed connected between
Compare the set weight of the entire glass melting device with the weight of the entire glass melting device weighed by the weighing device,
A glass liquid level adjusting device for a glass melting apparatus, comprising: a control device that controls the input amount adjusting device based on this comparison.
JP20350090A 1989-08-31 1990-07-31 Method and device for controlling molten glass level in glass melting device Expired - Fee Related JP2998977B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP22623689 1989-08-31
JP1-226236 1989-08-31

Publications (2)

Publication Number Publication Date
JPH03164436A true JPH03164436A (en) 1991-07-16
JP2998977B2 JP2998977B2 (en) 2000-01-17

Family

ID=16842028

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20350090A Expired - Fee Related JP2998977B2 (en) 1989-08-31 1990-07-31 Method and device for controlling molten glass level in glass melting device

Country Status (2)

Country Link
JP (1) JP2998977B2 (en)
DE (1) DE4027679A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014104190A1 (en) * 2012-12-27 2014-07-03 AvanStrate株式会社 Method for manufacturing glass plate and glass plate manufacturing apparatus

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4443991C1 (en) 1994-12-12 1996-04-04 Hartmut Geisel Weighing system for free-falling glass in glass container mfg. machine
DE10116075C1 (en) * 2001-03-30 2002-05-29 Conducta Endress & Hauser Process for producing a blown glass body comprises determining the position of the surface of a glass melt in an adjusting position of an immersion tube, controlling the position, and bombarding the immersion tube with a blowing pressure
CN103605382B (en) * 2013-11-06 2016-01-20 沈阳理工大学 A kind of Automatic control device of powder height
MX369215B (en) * 2014-05-15 2019-10-30 Colorobbia Mexico S A De C V Submerged combustion furnace for producing frit and method for producing frit.

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014104190A1 (en) * 2012-12-27 2014-07-03 AvanStrate株式会社 Method for manufacturing glass plate and glass plate manufacturing apparatus
CN104066689A (en) * 2012-12-27 2014-09-24 安瀚视特控股株式会社 Method for manufacturing glass plate and glass plate manufacturing apparatus

Also Published As

Publication number Publication date
DE4027679A1 (en) 1991-04-04
JP2998977B2 (en) 2000-01-17

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