JP2001337195A - Molten glass falling velocity control mechanism - Google Patents

Molten glass falling velocity control mechanism

Info

Publication number
JP2001337195A
JP2001337195A JP2000160164A JP2000160164A JP2001337195A JP 2001337195 A JP2001337195 A JP 2001337195A JP 2000160164 A JP2000160164 A JP 2000160164A JP 2000160164 A JP2000160164 A JP 2000160164A JP 2001337195 A JP2001337195 A JP 2001337195A
Authority
JP
Japan
Prior art keywords
molten glass
falling
falling speed
input power
calculator
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.)
Pending
Application number
JP2000160164A
Other languages
Japanese (ja)
Inventor
Nobuhiro Yasutake
伸洋 安武
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.)
IHI Corp
Original Assignee
IHI 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 IHI Corp filed Critical IHI Corp
Priority to JP2000160164A priority Critical patent/JP2001337195A/en
Publication of JP2001337195A publication Critical patent/JP2001337195A/en
Pending 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
    • C03B5/26Outlets, e.g. drains, siphons; Overflows, e.g. for supplying the float tank, tweels
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B7/00Distributors 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
    • C03B7/08Feeder spouts, e.g. gob feeders
    • C03B7/094Means for heating, cooling or insulation
    • C03B7/096Means for heating, cooling or insulation for heating

Landscapes

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

Abstract

PROBLEM TO BE SOLVED: To facilitate operation control of a glass melting furnace. SOLUTION: This mechanism is equipped with a falling velocity computing unit 14 for obtaining the falling velocity of molten glass G falling from a falling nozzle 8 to a solidified body vessel 11 as a process value, a falling velocity setter 19 for setting the target value of the falling velocity of the molten glass G, a velocity difference computing unit 20 for obtaining deviation of the process value relative to the target value of the falling velocity, based on signals from the falling velocity computing unit 14 and the falling velocity setter 19, an input power computing unit 21 for obtaining input power energy to be supplied to an induction heating coil 9, based on a signal 20s from the velocity difference computing unit 20, and a heating device 16 for supplying power E1 to the induction heating coil 9, based on a signal 21s from the input power computing unit 21. In the mechanism, the input power energy into the induction heating coil 9 is increased or decreased, by using the deviation of the process value relative to the target value of the falling velocity as a control parameter.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は溶融ガラス流下速度
制御機構に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a molten glass falling speed control mechanism.

【0002】[0002]

【従来の技術】原子力施設から発生する放射性廃液は、
廃液処理設備によってガラス固化処理された後、廃棄物
保管施設に保管される。
2. Description of the Related Art Radioactive liquid waste generated from nuclear facilities is:
After being vitrified by waste liquid treatment equipment, it is stored in a waste storage facility.

【0003】図2は廃液処理設備を構成するガラス溶融
炉の一例であり、このガラス溶融炉は、上下方向中間部
分から下方へ向かって水平開口断面が徐々に縮小する形
状の溶融空間1を有し且つ耐火材により形成された溶融
炉本体2を備えている。
FIG. 2 shows an example of a glass melting furnace which constitutes a waste liquid treatment facility. This glass melting furnace has a melting space 1 whose horizontal opening cross section gradually decreases downward from an intermediate portion in the vertical direction. And a melting furnace main body 2 formed of a refractory material.

【0004】溶融炉本体2の上部には、原料供給管3、
廃液供給管4、及び排気管5が溶融空間1に連通するよ
うに接続されている。
In the upper part of the melting furnace body 2, a raw material supply pipe 3,
The waste liquid supply pipe 4 and the exhaust pipe 5 are connected so as to communicate with the melting space 1.

【0005】溶融炉本体2内には、溶融空間1の上下方
向中間部で向き合う一対の主電極6と、溶融空間1の底
部近傍に位置する底部電極7とが、溶融空間1に貯留さ
れる溶融ガラスGに浸漬するように設けられている。
[0005] In the melting furnace body 2, a pair of main electrodes 6 facing each other at an intermediate portion in the vertical direction of the melting space 1 and a bottom electrode 7 located near the bottom of the melting space 1 are stored in the melting space 1. It is provided so as to be immersed in the molten glass G.

【0006】溶融炉本体2の下部には、溶融空間1に連
通する流下ノズル8と、該流下ノズル8を取り囲む誘導
加熱コイル9と、流下ノズル8に対して冷却用空気を吹
き付け得る空気噴射管10とが設けられている。
[0006] At the lower part of the melting furnace body 2, a downflow nozzle 8 communicating with the melting space 1, an induction heating coil 9 surrounding the downflow nozzle 8, and an air injection pipe capable of blowing cooling air to the downflow nozzle 8. 10 are provided.

【0007】また、溶融炉本体2の下方には、金属製の
固化体容器11が載置される荷重検出器12を有し且つ
流下ノズル8の直下へ移動可能な搬送台車13が設けら
れている。
Below the melting furnace main body 2, there is provided a transport trolley 13 having a load detector 12 on which a solidified metal container 11 is placed and movable directly below the falling nozzle 8. I have.

【0008】更に、ガラス溶融炉には、荷重検出器12
から出力される荷重検出信号12sに基づき瞬時重力を
時間で微分して流下ノズル8より固化体容器11へ流出
する溶融ガラスGの流下速度を求める流下速度演算器1
4と、該流下速度演算器14から出力される流下速度信
号14sに基づき溶融ガラスGの流下速度を表示する溶
融ガラス流速計15と、前記の誘導加熱コイル9に電力
E1を供給する第1の加熱装置16と、両主電極6,6
あるいは一方の主電極6及び底部電極7に電力E2を供
給する第2の加熱装置17とが付帯している。
Further, a load detector 12 is provided in the glass melting furnace.
Velocity calculator 1 for differentiating instantaneous gravity with time based on the load detection signal 12s output from the controller to obtain the velocity of the molten glass G flowing out of the flow-down nozzle 8 into the solidified container 11.
4, a molten glass current meter 15 for displaying the flowing speed of the molten glass G based on the flowing speed signal 14s output from the flowing speed calculator 14, and a first power supply E1 to the induction heating coil 9. Heating device 16 and both main electrodes 6, 6
Alternatively, a second heating device 17 for supplying electric power E2 to one of the main electrode 6 and the bottom electrode 7 is provided.

【0009】図2に示すガラス溶融炉では、原料供給管
3から溶融空間1へ送給した原料ガラスを、溶融炉本体
2に付帯するヒータ(図示せず)によって溶融させ、ま
た、両主電極6,6あるいは一方の主電極6及び底部電
極7に電力E2を供給し、溶融空間1の溶融ガラスGを
ジュール熱によって固化しないように保温する。
In the glass melting furnace shown in FIG. 2, the raw material glass fed from the raw material supply pipe 3 to the melting space 1 is melted by a heater (not shown) attached to the main body 2 of the melting furnace. Electric power E2 is supplied to 6, 6, or one of the main electrode 6 and the bottom electrode 7, and the molten glass G in the molten space 1 is kept warm so as not to be solidified by Joule heat.

【0010】このとき、流下ノズル8内でガラスが固化
して、溶融空間1から外部への溶融ガラスGの流出が抑
止される。
At this time, the glass is solidified in the downflow nozzle 8 and the outflow of the molten glass G from the molten space 1 to the outside is suppressed.

【0011】この状態で、原料供給管3から溶融空間1
へガラス原料を送給すると、当該原料ガラスが溶融ガラ
スGに溶融し、また、廃液供給管4から溶融空間1へ廃
液を送給すると、当該廃液が溶融ガラスGに混入され
る。
In this state, the raw material supply pipe 3 and the melting space 1
When the glass raw material is supplied to the molten glass G, the raw glass melts into the molten glass G. When the waste liquid is supplied from the waste liquid supply pipe 4 to the melting space 1, the waste liquid is mixed into the molten glass G.

【0012】廃液のガラス固化処理にあたっては、搬送
台車13に固化体容器11を搭載し、該固化体容器11
が流下ノズル8の直下に位置するように搬送台車13を
移動させておく。
In the vitrification treatment of the waste liquid, the solidified container 11 is mounted on a carrier 13 and the solidified container 11
The transport carriage 13 is moved so that is located immediately below the downflow nozzle 8.

【0013】更に、誘導加熱コイル9へ電力E1を供給
することにより流下ノズル8を加熱し、該流下ノズル8
内で固化しているガラスを溶融させて、廃液が混入した
溶融ガラスGを、流下ノズル8から固化体容器11へ流
出させる。
Further, by supplying electric power E1 to the induction heating coil 9, the downstream nozzle 8 is heated, and the downstream nozzle 8 is heated.
The glass solidified therein is melted, and the molten glass G mixed with the waste liquid flows out from the downflow nozzle 8 to the solidified container 11.

【0014】このとき、荷重検出器12からの荷重検出
信号12sに基づき、流下ノズル8から固化体容器11
へ流下する溶融ガラスGの流下速度が、流下速度演算器
14により求められ、該流下速度演算器14からの流下
速度信号14sに応じた溶融ガラスGの流下速度が溶融
ガラス流速計15に表示される。
At this time, based on the load detection signal 12s from the load detector 12, the solidified container 11
The falling speed of the molten glass G flowing down is calculated by the falling speed calculator 14, and the falling speed of the molten glass G according to the falling speed signal 14s from the falling speed calculator 14 is displayed on the molten glass current meter 15. You.

【0015】誘導加熱コイル9への電力E1の供給を中
断すると、流下ノズル8の温度が徐々に低下し、当該流
下ノズル8内でガラスが固化し、溶融空間1から外部へ
の溶融ガラスGの流出が抑止され、固化体容器11内に
充填された溶融ガラスGは、自然風冷によって固化し、
ガラス固化体が形成される。
When the supply of the electric power E1 to the induction heating coil 9 is interrupted, the temperature of the falling nozzle 8 gradually decreases, the glass solidifies in the falling nozzle 8, and the molten glass G from the melting space 1 to the outside is melted. The outflow is suppressed, and the molten glass G filled in the solidified container 11 is solidified by natural air cooling,
A vitrified body is formed.

【0016】固化体容器11への溶融ガラス充填時に
は、一方の主電極6及び底部電極7に対する投入電力量
を一定にした状態で、運転員が溶融ガラス流速計15の
表示、溶融ガラスGの温度などを確認しながら、誘導加
熱コイル9に対する投入電力量を増減して、溶融ガラス
Gの流下速度を制御している。
At the time of filling the molten glass into the solidified container 11, the operator operates the display of the molten glass anemometer 15 and the temperature of the molten glass G while keeping the input power to one of the main electrode 6 and the bottom electrode 7 constant. While confirming the above, the amount of electric power supplied to the induction heating coil 9 is increased or decreased to control the flow rate of the molten glass G.

【0017】[0017]

【発明が解決しようとする課題】しかしながら、流下ノ
ズル8から固化体容器11へ溶融ガラスGを流下させる
際に、誘導加熱コイル9に対する投入電力量を増減する
か否かは、運転員の判断に委ねられており、また、誘導
加熱コイル9への投入電力量を増減させてから、溶融ガ
ラスGの流下速度が変化するまでに応答遅れが生じるた
め、ガラス溶融炉の運転操作には熟練を要する。
However, when the molten glass G is caused to flow down from the downflow nozzle 8 to the solidified container 11, it is determined by the operator whether or not the amount of electric power supplied to the induction heating coil 9 should be increased or decreased. Also, since the response delay occurs after the amount of electric power supplied to the induction heating coil 9 is increased or decreased and before the flow rate of the molten glass G changes, the operation of the glass melting furnace requires skill. .

【0018】本発明は上述した実情に鑑みてなしたもの
で、ガラス溶融炉の運転操作を容易にすることを目的と
している。
The present invention has been made in view of the above circumstances, and has as its object to facilitate operation of a glass melting furnace.

【0019】[0019]

【課題を解決するための手段】上記目的を達成するた
め、本発明の溶融ガラス流下速度制御機構では、溶融炉
本体から流下ノズルを経て固化体容器へ流入した溶融ガ
ラスの重量を検出する荷重検出器と、該荷重検出器から
の信号に基づき流下ノズルより固化体容器へ流下する溶
融ガラスの流下速度をプロセス値として求める流下速度
演算器と、溶融ガラスの流下速度の目標値を設定する流
下速度設定器と、流下速度演算器及び流下速度設定器か
らの信号に基づき流下速度の目標値に対するプロセス値
の偏差を求める速度差演算器と、該速度差演算器からの
信号に基づき流下ノズル加熱用コイルへ供給すべき投入
電力量を求める投入電力演算器と、該投入電力演算器か
らの信号に基づき流下ノズル加熱用コイルへ電力を供給
する加熱装置とを備えている。
In order to achieve the above object, a molten glass falling speed control mechanism according to the present invention comprises a load detecting device for detecting the weight of molten glass flowing from a melting furnace body into a solidified container via a falling nozzle. A flow rate calculating device for calculating the flow rate of the molten glass flowing down from the flow down nozzle to the solidified body container as a process value based on a signal from the load detector, and a flow down rate for setting a target value of the flow rate of the molten glass. A setting device, a speed difference calculator for calculating a deviation of a process value from a target value of the falling speed based on signals from the falling speed calculator and the falling speed setter, and a falling nozzle heating device based on a signal from the speed difference calculator. An input power calculator for calculating the input power to be supplied to the coil, and a heating device for supplying power to the downstream nozzle heating coil based on a signal from the input power calculator. To have.

【0020】本発明の溶融ガラス流下速度制御機構にお
いては、流下速度の目標値に対するプロセス値の偏差に
基づき、投入電力演算器から加熱装置へ信号が出力さ
れ、流下ノズル加熱用コイルへの投入電力量を調整す
る。
In the molten glass falling speed control mechanism of the present invention, a signal is output from the input power calculator to the heating device based on the deviation of the process value from the target value of the flowing speed, and the input power to the falling nozzle heating coil is output. Adjust the volume.

【0021】[0021]

【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0022】図1は本発明の溶融ガラス流下速度制御機
構の実施の形態の一例を示すものであり、図中、図2と
同一の符号を付した部分は同一物を表している。
FIG. 1 shows an example of an embodiment of a molten glass falling speed control mechanism according to the present invention. In FIG. 1, the same reference numerals as in FIG. 2 denote the same parts.

【0023】この溶融ガラス流下速度制御機構は、前述
の荷重検出器12、流下速度演算器14、溶融ガラス流
速計15、第1の加熱装置16、及び第2の加熱装置1
7に加えて、流下速度設定器19、速度差演算器20、
投入電力演算器21を備えている。
The molten glass falling speed control mechanism includes the load detector 12, the falling speed calculator 14, the molten glass flow meter 15, the first heating device 16, and the second heating device 1.
7, a falling speed setting device 19, a speed difference calculator 20,
An input power calculator 21 is provided.

【0024】流下速度設定器19は、予め設定した溶融
ガラスGの目標流下速度に応じて、目標流下速度信号1
9sを出力するように構成されている。
The falling speed setting device 19 is adapted to set a target falling speed signal 1 according to a preset target falling speed of the molten glass G.
It is configured to output 9 s.

【0025】速度差演算器20は、流下速度演算器14
からの流下速度信号14s及び流下速度設定器19から
の目標流下速度信号19sに基づき、現時点での溶融ガ
ラスGの流下速度の目標値に対するプロセス値の偏差を
求め、当該偏差に応じた速度差信号20sを出力する機
能を有している。
The speed difference calculator 20 is provided with a falling speed calculator 14.
Of the process value with respect to the target value of the flowing speed of the molten glass G at the present time based on the falling speed signal 14s from the controller and the target falling speed signal 19s from the falling speed setting device 19, and a speed difference signal corresponding to the difference. It has the function of outputting 20s.

【0026】投入電力演算器21は、速度差演算器20
からの速度差信号20sに基づき、誘導加熱コイル9へ
供給すべき投入電力量を求め、第1の加熱装置16に対
して投入電力量信号21sを出力するように構成されて
いる。
The input power calculator 21 includes a speed difference calculator 20.
Based on the speed difference signal 20 s from the controller, an input power amount to be supplied to the induction heating coil 9 is obtained, and an input power amount signal 21 s is output to the first heating device 16.

【0027】以下、図1に示す溶融ガラス流下速度制御
機構の作動を説明する。
The operation of the molten glass falling speed control mechanism shown in FIG. 1 will be described below.

【0028】第2の加熱装置17により一定値の電力E
2を主電極6及び底部電極7へ供給しながら、第1の加
熱装置16から電力E1を誘導加熱コイル9へ供給して
流下ノズル8を加熱すると、溶融炉本体2内の溶融ガラ
スGが固化体容器11へ流下しはじめ、流下速度演算器
14が、荷重検出器12からの荷重検出信号12sに基
づき、溶融ガラスGの流下速度を求めて、流下速度信号
14sを出力する。
A constant electric power E is generated by the second heating device 17.
When electric power E1 is supplied from the first heating device 16 to the induction heating coil 9 to heat the downflow nozzle 8 while supplying 2 to the main electrode 6 and the bottom electrode 7, the molten glass G in the melting furnace body 2 is solidified. At the beginning of flowing down into the body container 11, the flowing speed calculator 14 calculates the flowing speed of the molten glass G based on the load detection signal 12s from the load detector 12, and outputs a flowing speed signal 14s.

【0029】また、速度差演算器20が、流下速度演算
器14からの流下速度信号14sと流下速度設定器19
からの目標流下速度信号19sに基づき、現時点での溶
融ガラスGの流下速度の目標値に対するプロセス値の偏
差を求める。
The speed difference calculator 20 is provided with a falling speed signal 14 s from the falling speed calculator 14 and a falling speed setting device 19.
The deviation of the process value from the target value of the flowing speed of the molten glass G at the current time is obtained based on the target flowing speed signal 19s from the target.

【0030】上記の目標値とプロセス値とに偏差が生じ
ている場合には、速度差演算器20から速度差信号20
sが出力され、投入電力演算器21が、速度差信号20
sに基づき誘導加熱コイル9へ供給すべき投入電力量を
求め、第1の加熱装置16に対して投入電力量信号21
sを出力する。
If there is a deviation between the target value and the process value, a speed difference signal 20
s is output, and the input power calculator 21 outputs the speed difference signal 20
s based on the input power amount signal to be supplied to the induction heating coil 9, and the input power amount signal 21 to the first heating device 16.
Output s.

【0031】溶融ガラスGの粘度が高めで、流下速度の
プロセス値が目標値よりも低い場合には、投入電力量信
号21sに応じて、第1の加熱装置16から誘導加熱コ
イル9へ供給される電力E1が増加し、溶融ガラスGの
粘度が低くなるように、流下ノズル8の加熱状態が調整
され、溶融ガラスGの流下速度の向上が図られる。
When the viscosity of the molten glass G is high and the process value of the falling speed is lower than the target value, the molten glass G is supplied from the first heating device 16 to the induction heating coil 9 in accordance with the supplied electric energy signal 21s. The heating state of the flow-down nozzle 8 is adjusted so that the electric power E1 increases and the viscosity of the molten glass G decreases, and the flow-down speed of the molten glass G is improved.

【0032】溶融ガラスGの粘度が低めで、流下速度の
プロセス値が目標値よりも高い場合には、投入電力量信
号21sに応じて、第1の加熱装置16から誘導加熱コ
イル9へ供給される電力E1が減少し、溶融ガラスGの
粘度が高くなるように、流下ノズル8の加熱状態が調整
され、溶融ガラスGの流下速度の抑制が図られる。
When the viscosity of the molten glass G is relatively low and the process value of the falling speed is higher than the target value, the molten glass G is supplied from the first heating device 16 to the induction heating coil 9 in accordance with the supplied electric energy signal 21s. The heating state of the flow-down nozzle 8 is adjusted so that the electric power E1 decreases and the viscosity of the molten glass G increases, so that the flow-down speed of the molten glass G is suppressed.

【0033】このように、図1に示す溶融ガラス流下速
度制御機構においては、溶融ガラスGの流下速度の目標
値に対するプロセス値の偏差を制御パラメータとして、
誘導加熱コイル9への投入電力量を増減させるので、目
標値に応じた流下速度で溶融ガラスGを流下させること
が可能になる。
As described above, in the molten glass falling speed control mechanism shown in FIG. 1, the deviation of the process value from the target value of the falling speed of the molten glass G is used as a control parameter.
Since the amount of electric power supplied to the induction heating coil 9 is increased or decreased, it is possible to cause the molten glass G to flow down at a flow rate according to the target value.

【0034】なお、本発明の溶融ガラス流下速度制御機
構は上述した実施の形態のみに限定されるものではな
く、本発明の要旨を逸脱しない範囲内において変更を加
え得ることは勿論である。
It should be noted that the molten glass falling speed control mechanism of the present invention is not limited to the above-described embodiment, but may be modified without departing from the scope of the present invention.

【0035】[0035]

【発明の効果】以上述べたように、本発明の溶融ガラス
流下速度制御機構では、溶融ガラスの流下速度の目標値
に対するプロセス値の偏差に基づき、投入電力演算器か
ら加熱装置へ信号が出力され、流下ノズル加熱用コイル
への投入電力量を調整するので、ガラス溶融炉の運転操
作が容易になり且つ運転員の負担が軽減されるという、
優れた効果を奏し得る。
As described above, in the molten glass falling speed control mechanism of the present invention, a signal is output from the input power calculator to the heating device based on the deviation of the process value from the target value of the falling speed of the molten glass. Since the amount of power supplied to the downflow nozzle heating coil is adjusted, the operation of the glass melting furnace is facilitated and the burden on the operator is reduced.
Excellent effects can be achieved.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の溶融ガラス流下速度制御機構の実施の
形態の一例を備えたガラス溶融炉を示す概念図である。
FIG. 1 is a conceptual diagram showing a glass melting furnace provided with an example of an embodiment of a molten glass falling speed control mechanism of the present invention.

【図2】ガラス溶融炉の一例を示す概念図である。FIG. 2 is a conceptual diagram illustrating an example of a glass melting furnace.

【符号の説明】[Explanation of symbols]

2 溶融炉本体 8 流下ノズル 9 誘導加熱コイル(流下ノズル加熱用コイル) 11 固化体容器 12 荷重検出器 12s 荷重検出信号 14 流下速度演算器 14s 流下速度信号 16 第1の加熱装置 19 流下速度設定器 19s 目標流下速度信号 20 速度差演算器 20s 速度差信号 21 投入電力演算器 21s 投入電力信号 E1 電力 G 溶融ガラス 2 Melting furnace body 8 Downflow nozzle 9 Induction heating coil (downflow nozzle heating coil) 11 Solidified container 12 Load detector 12s Load detection signal 14 Downflow speed calculator 14s Downflow speed signal 16 First heating device 19 Downflow speed setting device 19s Target falling speed signal 20 Speed difference calculator 20s Speed difference signal 21 Input power calculator 21s Input power signal E1 Power G Molten glass

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 溶融炉本体から流下ノズルを経て固化体
容器へ流入した溶融ガラスの重量を検出する荷重検出器
と、該荷重検出器からの信号に基づき流下ノズルより固
化体容器へ流下する溶融ガラスの流下速度をプロセス値
として求める流下速度演算器と、溶融ガラスの流下速度
の目標値を設定する流下速度設定器と、流下速度演算器
及び流下速度設定器からの信号に基づき流下速度の目標
値に対するプロセス値の偏差を求める速度差演算器と、
該速度差演算器からの信号に基づき流下ノズル加熱用コ
イルへ供給すべき投入電力量を求める投入電力演算器
と、該投入電力演算器からの信号に基づき流下ノズル加
熱用コイルへ電力を供給する加熱装置とを備えてなるこ
とを特徴とする溶融ガラス流下速度制御機構。
1. A load detector for detecting the weight of molten glass flowing from a melting furnace body into a solidified container via a flow-down nozzle, and a melt flowing down from the flow-down nozzle to the solidified container based on a signal from the load detector. A falling speed calculator for calculating the falling speed of the glass as a process value, a falling speed setter for setting a target value for the falling speed of the molten glass, and a target for the falling speed based on signals from the falling speed calculator and the falling speed setter. A speed difference calculator for determining the deviation of the process value from the value,
An input power calculator for calculating an input power to be supplied to the downstream nozzle heating coil based on a signal from the speed difference calculator; and supplying power to the downstream nozzle heating coil based on a signal from the input power calculator. A molten glass flow-down speed control mechanism comprising a heating device.
JP2000160164A 2000-05-30 2000-05-30 Molten glass falling velocity control mechanism Pending JP2001337195A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000160164A JP2001337195A (en) 2000-05-30 2000-05-30 Molten glass falling velocity control mechanism

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000160164A JP2001337195A (en) 2000-05-30 2000-05-30 Molten glass falling velocity control mechanism

Publications (1)

Publication Number Publication Date
JP2001337195A true JP2001337195A (en) 2001-12-07

Family

ID=18664394

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000160164A Pending JP2001337195A (en) 2000-05-30 2000-05-30 Molten glass falling velocity control mechanism

Country Status (1)

Country Link
JP (1) JP2001337195A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CZ301795B6 (en) * 2006-11-20 2010-06-23 Preciosa, A. S. Discharge device for withdrawing molten glass from a chamber for further processing
JP2010163291A (en) * 2009-01-13 2010-07-29 Ihi Corp Glass melting furnace

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CZ301795B6 (en) * 2006-11-20 2010-06-23 Preciosa, A. S. Discharge device for withdrawing molten glass from a chamber for further processing
JP2010163291A (en) * 2009-01-13 2010-07-29 Ihi Corp Glass melting furnace

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