JPS61155217A - Production of boron oxide - Google Patents

Production of boron oxide

Info

Publication number
JPS61155217A
JPS61155217A JP27676884A JP27676884A JPS61155217A JP S61155217 A JPS61155217 A JP S61155217A JP 27676884 A JP27676884 A JP 27676884A JP 27676884 A JP27676884 A JP 27676884A JP S61155217 A JPS61155217 A JP S61155217A
Authority
JP
Japan
Prior art keywords
vessel
boric acid
container
heating
boron oxide
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
JP27676884A
Other languages
Japanese (ja)
Inventor
Kazuhide Nakazato
中里 一英
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.)
RASUKATSUTO KAGAKU KK
Original Assignee
RASUKATSUTO KAGAKU KK
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 RASUKATSUTO KAGAKU KK filed Critical RASUKATSUTO KAGAKU KK
Priority to JP27676884A priority Critical patent/JPS61155217A/en
Publication of JPS61155217A publication Critical patent/JPS61155217A/en
Pending legal-status Critical Current

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

PURPOSE:To economize the fuel cost in comparison with a conventional method and to enable the use of an inexpensive crucible by heating boric acid in a heated vessel from the outside part, discharging the foamy boron oxide which is swelled up in the specified temp. range to the outside of the vessel from the upper side of the vessel and collecting it. CONSTITUTION:Boric acid is introduced into a heating vessel 1 (e.g. made of stainless or ceramic) and the heating vessel 1 is heated with a heater 4. While boric acid in the vessel is dehydrated, it becomes a solution-like state at about 150-200 deg.C and furthermore becomes slightly viscous liquid body C in accompanying to the advance of the dehydration. When the water content reaches about <=10% (10-2%) and the temp. of liquid reaches about >=250 deg.C (250-450 deg.C), the above-mentioned liquid body C becomes the foamy bodies D and swelled up. The blowing-up foamy bodies D are discharged naturally and continuously from a takeout port 2 of the upper part of the vessel to collect them in a pan body 3 by continuing the heating so that the temp. is maintained at about 250-450 deg.C until the liquid body C is all evaporated.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はホウ酸から酸化ホウ素を製造する酸化ホウ素の
製造法、さらに詳しくは、ホウ酸は、加熱して脱水する
過程中、含量が90%〜98%(含水量10%〜2%)
位の間において泡吹き状態に変化する性質を利用した酸
化ホウ素の製造法に関するものである。
Detailed Description of the Invention (Industrial Application Field) The present invention relates to a method for producing boron oxide from boric acid. %~98% (moisture content 10%~2%)
This invention relates to a method for producing boron oxide that takes advantage of its property of changing to a bubbling state between two positions.

(従来の技術) 酸化ホウ素は、通常ホウ酸を加熱脱水して造られるもの
で、別名、無水ホウ酸とも称されている。
(Prior Art) Boron oxide is usually produced by heating and dehydrating boric acid, and is also called boric anhydride.

ホウ酸を加熱脱水し″CFR化ホウ素を製造する場合、
J I 5K−8431−61の規定の如く、含量85
%程度、したがって含水量15九程度の酸化ホウ素を得
るものであれば、ホウ酸を230℃前後の温度に所定時
間加熱すれば良く、この時のホウ酸の変化状態はや〜粘
ちゅうな液状であるため、その製造は容易であり、また
、真空脱水法を併用すれば200℃程度の低い温度でも
製造可能である。
When producing CFR boron by heating and dehydrating boric acid,
Content 85 as specified in J I 5K-8431-61
If you want to obtain boron oxide with a water content of about 159%, it is sufficient to heat boric acid to a temperature of around 230°C for a certain period of time, and the state of change of boric acid at this time is a slightly to viscous liquid. Therefore, it is easy to manufacture, and can be manufactured at a temperature as low as about 200° C. if a vacuum dehydration method is also used.

しかし乍ら、含量90%以上、したがって含水flO%
以下の酸化ホウ素を得ようとするときには、種々の問題
に直面する。
However, the content is more than 90%, therefore the water content flO%
Various problems are encountered when trying to obtain the following boron oxides.

すなわち、ホウ酸は加熱脱水により酸化ホウ素に変化す
る過程において、まづ150℃〜200℃で溶液状にな
り、その後脱水が進むにつれて次才に粘ちゅう化し、含
量で90%〜98%位(含水量゛ 10%〜2%位)、
温度で250℃〜450℃(加熱速度により多少の差が
ある)の間は粘着性の強い泡を吹いた状態(泡状に膨れ
上がる状態)となる。
In other words, in the process of boron oxide being transformed by thermal dehydration, boric acid first becomes a solution at 150°C to 200°C, and then becomes viscous as the dehydration progresses, resulting in a content of about 90% to 98% ( Moisture content (around 10% to 2%),
When the temperature is between 250° C. and 450° C. (there are some differences depending on the heating rate), a highly sticky foam is blown (a state in which it swells into a foam).

その後は酸化ホウ素(無水ホウ酸)の融点(577℃)
に近ずくにつれて再び溶融状態となり、触点な越えると
水飴や溶融ガラス状の粘ちゅうな液状に溶融する。
After that, the melting point of boron oxide (boric anhydride) (577℃)
As it approaches the point, it becomes molten again, and when it crosses the point, it melts into a viscous liquid like starch syrup or molten glass.

ホウ酸は上記のような性質であり、含量90光以上(含
水fil 10 X以下)のば化ボウ累を製造する場合
、従来はルツボを使用し、このルツボ内へホウ酸を入れ
、融点(577℃)以上の温度でホウ酸を長時間に亘り
加熱して水飴などのような粘ちゅう液状に溶融させ、こ
れをルツボから別の容器に流し出して冷却し、或いはル
ツボに入れたま又外側から冷却する製造法が一般に採用
されている。
Boric acid has the above-mentioned properties, and when producing a chemical compound with a content of 90 or more (water content of less than 10 Boric acid is heated for a long time at a temperature of 577℃ or higher to melt it into a viscous liquid like starch syrup, and then poured out of the crucible into another container and cooled, or it can be poured into the crucible and left outside. A manufacturing method in which the material is cooled is generally adopted.

(発明が解決しようとする問題点) 上記した従来技術によれば、きわめて純度の高い(含量
98%以上)酸化ホウ素を得ることができるが、この製
造法には次のような問題を有している。
(Problems to be Solved by the Invention) According to the above-mentioned conventional technology, boron oxide with extremely high purity (content of 98% or more) can be obtained, but this production method has the following problems. ing.

(イ)従来法はホウ酸を水飴のような粘ちゅうな液状に
なるまで浴融させるものであるから、ホウ酸をきわめて
高温(700℃以上)になるまで、゛かつ、長時開用け
て加熱する必要がある。したがって、製造に長時間装す
ると共に燃料費が尚くなる。
(b) The conventional method involves melting boric acid in a bath until it becomes a viscous liquid like starch syrup. It is necessary to heat it. Therefore, manufacturing takes a long time and fuel costs increase.

(ロ)ルツボ内で溶融させた製品の取り出し作業が煩雑
である。
(b) The work of taking out the melted product in the crucible is complicated.

(ハ)ホウ酸およびホウ酸塩は高温において金属酸化物
を溶解することは周知の事実であり、このため、従来法
によればルツボの材質を十分に選定しないとルツボの溶
解によって製品に不純物が混入したり、ルツボの耐久性
等についても問題が生じることになる。そこで、従来、
通常は白金ルツボを使用していたため、局側になる問題
を有している。
(c) It is a well-known fact that boric acid and borates dissolve metal oxides at high temperatures.For this reason, if the material of the crucible is not carefully selected in the conventional method, impurities may be added to the product due to melting of the crucible. Contamination may occur, and problems may arise regarding the durability of the crucible. Therefore, conventionally,
Usually, a platinum crucible was used, so there was a problem with the local side.

に)酸化ホウ素は、用途により含量90%〜98%程度
(含水量10%〜5%程度)で十分適応できる場合が多
くあるが、従来法のように水飴のような粘ちゅうな液状
になるまで加熱すると含量は98%以上のものになり、
したがって、その分だけムダな労費を掛けることになる
場合が生じることになる。
(ii) Boron oxide can often be used at a content of 90% to 98% (water content of 10% to 5%), depending on the application, but as with conventional methods, it becomes a viscous liquid like starch syrup. When heated to 98% or more,
Therefore, there may be cases where unnecessary labor costs are incurred.

従って、本発明は上記した(イ)〜に)の問題を解決す
ることを技術的課屈とするものである。
Therefore, the technical challenge of the present invention is to solve the problems (a) to (b) above.

(問題点を解決するための手段) 上記問題点を解決するため、本発明は、ホウ酸を容器に
入れて加熱脱水1−ると、ホウ酸が最終段階において融
点を越えた時点で水飴のような粘ちゆうな液状に変化す
る過程中において、含量が90%〜98X程度(含水量
LUX〜2′)。)の間にあっては泡状に吹き上げてく
る性質を有していることに着目し、この段階、すなわち
、泡状体のまま容器の上部から11次連続的に容器外へ
泡状体を排出させて捕集するものである。
(Means for Solving the Problems) In order to solve the above problems, the present invention provides that boric acid is placed in a container and heated for dehydration.When the boric acid exceeds its melting point in the final stage, it becomes starch syrup. During the process of changing into a viscous liquid, the content is about 90% to 98X (water content LUX to 2'). ), we focused on the fact that it has the property of blowing up in the form of foam. It is collected by

すなわち、本発明は、ホウ酸を加熱容器に入れて容器の
外部から加熱し、該加熱によりホウ酸が変化して泡状に
膨れ上がってくる過程において、該泡状体を容器の上部
側から容器外へ順次排出させて捕集することを特徴とす
るものである。
That is, in the present invention, boric acid is placed in a heating container and heated from the outside of the container, and in the process in which the boric acid changes due to the heating and swells into a foam, the foam is heated from the upper side of the container. It is characterized by being sequentially discharged outside the container and collected.

(作 用) ホウ酸を加熱容器に入れ、容器外部よりバーナー等の熱
源で加熱すると、容器内のホウ酸は脱水しながら150
°d〜200℃の温゛度で溶液状となり、次いで脱水が
進むにつれて次矛に粘ちゅう化し、含水量が10%以下
(10%〜2%)で、液温か250℃程度以上(250
℃〜450℃)の温度(但し、加熱速度により若干の差
がある)に達すると前記液状体は泡状になって膨れ上が
ってくる。そして、加熱を継続することにより、上記泡
状体は容器の爾さ以上に吹き上げて(るので、容器の上
部側に取出口を設けて置けば、該取出口から階ふれて容
器外に自然に、かつ連続的に排出されるので、この排出
された泡状体を適当な受皿等で捕集できる。
(Function) When boric acid is placed in a heating container and heated from outside the container with a heat source such as a burner, the boric acid in the container dehydrates and becomes 150%
It becomes a solution at a temperature of ~200°C, and then becomes viscous as dehydration progresses, with a water content of 10% or less (10% to 2%) and a liquid temperature of about 250°C or higher (250°C or more).
℃~450℃) (However, there is a slight difference depending on the heating rate), the liquid material becomes foamy and swells. By continuing to heat the foam, it will blow up beyond the height of the container, so if an outlet is provided at the top of the container, it will spill out from the outlet and naturally flow out of the container. Since the foam is discharged quickly and continuously, the discharged foam can be collected with a suitable tray or the like.

そして、この泡状体は瞬時にして放冷固化するもので、
必要に応じ固化した泡状体を適宜粉砕すれば粉末の酸化
ホウ素が製造できる。
This foam instantly solidifies as it cools.
Powdered boron oxide can be produced by appropriately crushing the solidified foam as required.

(実施例) 以下、図面を参照して本発明の実施例につき説明するに
、矛/図は本発明の一実施例を示し、1は加熱容器で、
容器1はステンレスやセラミックその他の耐熱材で、所
望の径および高さを有する円筒形に造られている。この
場合、容器1の材質や大きさ、或いは形状等は任意に変
えられるものである。2は容器1の開口上端近くに設け
た取出口で、実施例の取出口2は容器1の上端部を凹状
に切欠し、核部に樋体を固設して構成しである。
(Example) Hereinafter, an example of the present invention will be described with reference to the drawings. The figure shows an example of the present invention, 1 is a heating container,
The container 1 is made of stainless steel, ceramic, or other heat-resistant material, and is formed into a cylindrical shape with a desired diameter and height. In this case, the material, size, shape, etc. of the container 1 can be changed arbitrarily. Reference numeral 2 denotes an outlet provided near the upper end of the opening of the container 1. The outlet 2 of the embodiment is constructed by cutting out the upper end of the container 1 in a concave shape and fixing a gutter body to the core.

実施例では取出口2を1個設けたものを図示したが、取
出口2の数は任意に増加することかでさ、また、取出口
2の構造等も逸宜変えても艮いものである。3は取出口
2の下部に位置させて配役した受皿体、4はバーナー等
の加熱器で、加熱器4は容器1の側面および底面を全体
的に加熱し得るように適当に配分して配設すると艮い。
In the embodiment, a device with one outlet 2 is shown, but the number of outlets 2 may be increased arbitrarily, and the structure of the outlet 2 may also be changed as needed. . Reference numeral 3 indicates a saucer body positioned at the bottom of the outlet 2, and 4 indicates a heater such as a burner, which is appropriately distributed and arranged so as to heat the entire side and bottom surface of the container 1. It's weird to set it up.

なお、図示しないが、容器1内の適当部に温度計を配設
し、容器1内のホウ酸の溶液の温度を検知できるように
しても艮い。
Although not shown in the drawings, a thermometer may be disposed at an appropriate location within the container 1 so that the temperature of the boric acid solution within the container 1 can be detected.

次に酸化ホウ素の製造法につき説明するに、矛3図(イ
)のように原料のホウ酸A(粉末で、含水蓋約43.7
%)を容器1内罠適量入れ、加熱器4で容器1を加熱す
ると、容器1内のホウ酸は加熱され、時間の経過に伴な
って次矛に昇温し、脱水を開始する。そして、ホウrR
Aは次矛に溶解し、150℃〜200℃程度の温度下で
、第3図(ロ)のようにまづ浴液状Bになり、つづいて
脱水が進むにつれて溶液Bは次矛に粘ちゅう化し、才3
図(ハ)のように、や〜粘ちゅうな溶液C状になる。次
いで、脱水がさらに進み、含量90%以上、したがって
含水量が10%以下で、かつ、液温が250℃程度以上
(但し、加熱速度により若干のづれが生じる)になると
上記溶液Cは矛3図に)のように粘着性の強い泡状に膨
れて次オに吹き上げてくる。この泡状体りの吹き上げ状
態は液温か約240℃〜500℃8夏の間継続する。そ
のため、容器1内の溶gcの温度を240℃〜500℃
、好ましくは250℃〜450℃の範囲に維持させるよ
うに加熱器4の熱量を適当に加減して容器1内の溶液C
が無くなるまで加熱を継続する。なお、この場合におい
て、溶液Cの温度が高(なり過ぎて融点(577℃)を
越えると泡状体りは消えて第3図(ホ)のように水飴の
如き粘ちゅうな液状EK溶融する。
Next, to explain the manufacturing method of boron oxide, as shown in Figure 3 (a), the raw material boric acid A (powder, with a water content of about 43.7
%) is placed in a container 1 and the container 1 is heated by the heater 4, the boric acid in the container 1 is heated, and as time passes, the temperature rises rapidly and dehydration begins. And Hou rR
A dissolves in the liquid, and at a temperature of about 150°C to 200°C, it first becomes liquid B as shown in Figure 3 (b), and then as dehydration progresses, solution B becomes viscous in the liquid. 3 years old
As shown in the figure (c), it becomes a somewhat viscous solution C-shaped. Next, as the dehydration progresses further and the water content reaches 90% or higher, the water content reaches 10% or lower, and the liquid temperature reaches approximately 250°C or higher (however, there may be a slight deviation depending on the heating rate), the above solution C becomes As shown in the figure), it swells into a sticky foam and blows up into the next layer. This foamy state continues for eight summers at a temperature of about 240°C to 500°C. Therefore, the temperature of the molten gc in container 1 is set at 240°C to 500°C.
The temperature of the solution C in the container 1 is adjusted appropriately to maintain the temperature in the range of 250°C to 450°C.
Continue heating until it disappears. In this case, if the temperature of solution C becomes too high and exceeds the melting point (577°C), the foam disappears and EK melts into a viscous liquid like starch syrup, as shown in Figure 3 (e). .

而して、上記したとおり、液温を約り40℃〜500℃
程度に維持することにより、容器1内の溶液Cは順次泡
状化して容器1の上方へ吹き上がり、泡状体りはオ/図
示のように取出口2から溢ふれ出て、容器1外に自然に
、かつ連続的に排出されて垂下し、受皿体3に捕集され
、酸化ホウ素な得る。
As mentioned above, the liquid temperature is approximately 40°C to 500°C.
By maintaining the solution C in the container 1 at a certain level, the solution C in the container 1 gradually becomes foamy and blows up to the top of the container 1, and the foam overflows from the outlet 2 as shown in the figure and flows out of the container 1. The boron oxide is naturally and continuously discharged and hangs down, and is collected in the tray body 3, where boron oxide is obtained.

上記により製造される酸化ホウ素の含水量は10′)6
〜2%位の品質であり、との含水量の度合は溶液Cの温
度を240℃〜500℃程度の範囲において加減するこ
とにより任意に調整することができる(但し、加熱速度
により若干の差が生じる)。
The water content of boron oxide produced by the above method is 10')6
The quality is about ~2%, and the degree of water content can be adjusted arbitrarily by adjusting the temperature of solution C in the range of about 240°C to 500°C (however, there may be slight differences depending on the heating rate). ).

そして、上記捕−した泡状体りを適当に粉砕することに
より所望メツシュの粉末状の酸化ホウ素が得られる。
Then, by appropriately crushing the captured foam, powdery boron oxide having a desired mesh can be obtained.

次にオコ図は本発明の別実施例を示し、この実施例は、
前記実施例の方法により泡状に吹き上がって′容器1の
上部の取出口2から容器1外へ排出された泡状体Eが受
皿体3上に垂下する過程中において、該泡状体Eをバー
ナー等の加熱器4aにより直火で加熱して酸化ホウ素を
得るもので、他の製造工程は前記矛1実施例と同一方法
により行い、線図において17図と同一符号を付した部
分は同一構成部分を示すものである。
Next, the Oko diagram shows another embodiment of the present invention, and this embodiment is as follows:
During the process in which the foam E, which has been blown up in the form of foam and discharged from the outlet 2 at the top of the container 1 to the outside of the container 1 by the method of the embodiment, hangs down onto the tray body 3, the foam E Boron oxide is obtained by heating with direct flame using a heater 4a such as a burner.Other manufacturing steps are carried out by the same method as in the first embodiment, and the parts in the diagram with the same symbols as in Figure 17 are It shows the same component parts.

該実施例の方法によると、泡状体Eは加熱器4aの直火
で加熱されて更に脱水し、この加熱脱水により水飴のよ
うな粘ちゅうな液状に7溶融して受皿体3に補集される
According to the method of this embodiment, the foam E is further dehydrated by being heated by the direct flame of the heater 4a, and by this heating and dehydration, it is melted into a viscous liquid like starch syrup and collected in the saucer body 3. be done.

したがって、該実施例によれば、含水量が2九以下の酸
化ホウ素を製造することが可能である。
Therefore, according to this example, it is possible to produce boron oxide having a water content of 29 or less.

(効 果) 本発明方法は以上説明したとおりであり、本発明によれ
ば次のような効果を期待することができる。
(Effects) The method of the present invention is as explained above, and according to the present invention, the following effects can be expected.

(d)ホウ酸を水飴状に溶融することなく、泡状体で容
器外へ排出させて捕集するものであるから、従来法に比
較して製造時間を短縮させることができる。
(d) Since boric acid is collected by being discharged from the container in a foam form without being melted into starch syrup, the production time can be shortened compared to conventional methods.

(b)従来法のような高温加熱を必要としないので、加
熱容器の材質の選定が容易であると共に燃費を大巾に節
減し得る。
(b) Since high-temperature heating unlike the conventional method is not required, the material of the heating container can be easily selected and fuel consumption can be greatly reduced.

(C)泡状体を容器外へ自然に排出できるので、製品の
取り出し作業を簡単かつ迅速良好に行なえる。
(C) Since the foam can be naturally discharged out of the container, the product can be easily and quickly taken out.

(d)泡状体で捕集するものであるから、含量90%〜
98X程度(含水量10X〜2%程度)の範囲内で任意
の品質の酸化ホウ素を自由に調整して効能良く製造し得
る。
(d) Since it is collected using a foam, the content is 90% or more.
Boron oxide of any quality within the range of about 98X (water content of about 10X to 2%) can be freely adjusted and efficiently produced.

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

矛/図は本発明に係る酸化ホウ素の製造法の一実施例を
示す概略縦断面図、3ア記図は本発明の別実施例を示−
fm略平面図、3・3図何j〜(ホ)は容器内に入れた
ホウ酸の加熱脱水による変化状態を示す説明図である。 1・・・・・・加熱容器、2・・・・・・取出口、3・
・・・・・受皿体、4.4a・・・・・・加熱器、A・
・・・・・ホウ酸、D・・・・・・泡状体。 特許出願人    日本ラスカット株式会社\r (イ)   (ロ)   (ハ) (ニ)    (ホ) C、D     E 手続補正書 昭和60年2月72日 1、事件の表示 %願餡59−276768号 2、発明の名称 酸化ホウ素の製造法 3、補正をする者 事件との関係  特許出願人 住 所  東京部品用区内品用3丁目5番3号代表者 
坪 1)興 平 4、代理人 5、補正命令の日付 自     発 6備止の対象 明#I書の発明の詳細な説明の樒 7、補正の岡谷 、  il+明細誉3′2負矛zu行の「触点」を「融
点」と補正する。
Figure 3 is a schematic longitudinal sectional view showing one embodiment of the method for producing boron oxide according to the present invention, and figure 3A shows another embodiment of the present invention.
fm schematic plan view, Figures 3 and 3 are explanatory diagrams showing changes in the state of boric acid placed in a container due to heat dehydration. 1... Heating container, 2... Outlet, 3.
...Saucer body, 4.4a... Heater, A.
...boric acid, D...foam. Patent Applicant Nihon Ruscut Co., Ltd.\r (a) (b) (c) (d) (e) C, D E Procedural Amendment February 72, 1985 1, Case Indication Percentage Request No. 59-276768 2. Name of the invention Method for manufacturing boron oxide 3. Relationship with the case of the person making the amendment Patent applicant address 3-5-3 Tokyo Parts Industry Representative
Tsubo 1) Kohei 4, Agent 5, Date of amendment order 6 Reference 6 Detailed explanation of the invention in Book I # 7, Amendment Okaya, il + Specification 3'2 Negative contradiction zu line Correct the "touch point" of "melting point".

Claims (1)

【特許請求の範囲】[Claims] (1)ホウ酸を加熱容器に入れて外部から加熱し、該加
熱によりホウ酸が変化して泡状に膨れ上がってくる過程
において、該膨れ上がってくる泡状体を前記容器の上部
側から容器外へ順次排出させて捕集することを特徴とす
る酸化ホウ素の製造法。
(1) Boric acid is placed in a heating container and heated from the outside, and during the process in which the boric acid changes due to the heating and swells into a foam, the swollen foam is removed from the upper side of the container. A method for producing boron oxide, characterized by sequentially discharging and collecting it outside a container.
JP27676884A 1984-12-27 1984-12-27 Production of boron oxide Pending JPS61155217A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27676884A JPS61155217A (en) 1984-12-27 1984-12-27 Production of boron oxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27676884A JPS61155217A (en) 1984-12-27 1984-12-27 Production of boron oxide

Publications (1)

Publication Number Publication Date
JPS61155217A true JPS61155217A (en) 1986-07-14

Family

ID=17574082

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27676884A Pending JPS61155217A (en) 1984-12-27 1984-12-27 Production of boron oxide

Country Status (1)

Country Link
JP (1) JPS61155217A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6325216A (en) * 1986-07-16 1988-02-02 ソチエ−タ・キミカ・ラルデレッロ・エセ・ピ・ア Manufacture of boron oxide

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6325216A (en) * 1986-07-16 1988-02-02 ソチエ−タ・キミカ・ラルデレッロ・エセ・ピ・ア Manufacture of boron oxide
US4908196A (en) * 1986-07-16 1990-03-13 Societa Chimica Larderello S.P.A. Boric oxide preparation method

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