JP2002166161A - Apparatus for manufacturing inorganic spheroidized particle - Google Patents

Apparatus for manufacturing inorganic spheroidized particle

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Publication number
JP2002166161A
JP2002166161A JP2000365262A JP2000365262A JP2002166161A JP 2002166161 A JP2002166161 A JP 2002166161A JP 2000365262 A JP2000365262 A JP 2000365262A JP 2000365262 A JP2000365262 A JP 2000365262A JP 2002166161 A JP2002166161 A JP 2002166161A
Authority
JP
Japan
Prior art keywords
temperature
inorganic spheroidized
melting chamber
spheroidized particles
inorganic
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
JP2000365262A
Other languages
Japanese (ja)
Inventor
Kunio Fujii
邦夫 藤井
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.)
Chugai Ro Co Ltd
Original Assignee
Chugai Ro Co Ltd
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 Chugai Ro Co Ltd filed Critical Chugai Ro Co Ltd
Priority to JP2000365262A priority Critical patent/JP2002166161A/en
Publication of JP2002166161A publication Critical patent/JP2002166161A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide an apparatus manufacturing inorganic spheroidized particles, which can efficiently obtain excellent inorganic spheroidized particles by keeping the ambient temperature in a flame formation region of a melting chamber within a prescribed temperature range, and cope with various processing conditions such as the type and particle size of inorganic raw material powder, and retention time. SOLUTION: In an apparatus T for manufacturing inorganic spheroidized particles comprising a melting chamber 1 which has a burner 5 in its ceiling part 4 and of which the sidewall 2 is formed with a refractory, and a cooling chamber 8 which has a water-wall structure and is connected to the melting chamber, the melting chamber is divided into an upper zone A and a lower zone B, a plurality of cooling gas supply means 6 jetting cooling gas along the inner wall surfaces of the upper and lower zones A and B are installed in the circumferential direction, and the ambient temperature in the upper zone A is kept 300-600 deg.C lower than the melting temperature of the inorganic raw material powder.

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、シリカ等の無機質
球状化粒子製造装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for producing inorganic spheroidized particles such as silica.

【0002】[0002]

【従来の技術】たとえば、シリカ等の無機質原料粉体
を、酸素あるいは酸素富化空気を使用する燃焼装置から
の燃焼火炎中に通過させて溶融したのち冷却し、無機質
球状化粒子を得る技術は公知である。
2. Description of the Related Art For example, a technique for obtaining inorganic spheroidized particles by passing an inorganic raw material powder such as silica through a combustion flame from a combustion device using oxygen or oxygen-enriched air and melting the resulting powder is cooled. It is known.

【0003】ところで、良好な無機質球状化粒子を得る
ためには、燃焼火炎温度を当該無機質原料粉体の溶融温
度以上に維持する必要があるが、燃焼中は溶融室内の雰
囲気(溶融室内の燃焼ガス)を対流によって燃焼火炎内
に同伴することから、燃焼火炎温度は燃焼火炎形成域に
おける雰囲気温度により影響を受けることになる。
In order to obtain good inorganic spheroidized particles, it is necessary to maintain the combustion flame temperature at or above the melting temperature of the inorganic raw material powder. Since the gas is entrained in the combustion flame by convection, the combustion flame temperature is affected by the ambient temperature in the combustion flame formation region.

【0004】すなわち、溶融室内の燃焼火炎形成域にお
ける雰囲気温度を高く維持しすぎると、燃焼火炎温度が
上昇し、無機質球状化粒子の肥大率が高くなったり、溶
融室内の側壁への無機質球状化粒子の付着量が増大して
溶融室の清掃頻度が増え、生産性が低下する。
[0004] That is, if the ambient temperature in the combustion flame formation region in the melting chamber is maintained too high, the combustion flame temperature rises, the rate of enlargement of the inorganic spheroidized particles increases, and the inorganic spheroidizing on the side wall in the melting chamber. The amount of particles attached increases, the frequency of cleaning the melting chamber increases, and the productivity decreases.

【0005】逆に、溶融室内の燃焼火炎形成域における
雰囲気温度を低く維持しすぎると、燃焼火炎温度が低下
し、無機質原料粉体が充分に溶融されず、良品の無機質
球状化粒子を得ることができなくなる。
On the other hand, if the temperature of the atmosphere in the combustion flame forming region in the melting chamber is kept too low, the combustion flame temperature is lowered, the inorganic raw material powder is not sufficiently melted, and good-quality inorganic spheroidized particles are obtained. Can not be done.

【0006】したがって、良好な無機質球状化粒子を効
率よく得るためには、溶融室内の火炎形成域における雰
囲気温度を所定温度範囲内に維持することが非常に重要
である。
[0006] Therefore, in order to efficiently obtain good inorganic spheroidized particles, it is very important to maintain the ambient temperature in the flame forming region in the melting chamber within a predetermined temperature range.

【0007】そこで、無機質球状化粒子製造設備の一例
として、特開昭62−241542号公報には溶融室の
耐火物壁外面に水冷ジャケットを設け、冷却水量を変化
させて溶融室の耐火物壁面温度を600〜1000℃に
保持するとともに、この耐火物壁温度に応じた厚みの球
状化粒子によるコーティング層を形成して溶融室への無
機質球状化粒子の付着を防止する無機質球状化粒子製造
設備や、特開平11−71107号公報には装置全体を
水冷壁構造とするとともに、燃焼火炎の周囲に冷却空気
を供給し、燃焼ガスの対流を抑えて溶融室への無機質球
状化粒子の付着を防止する無機質球状化粒子製造設備が
開示されている。
Therefore, as an example of an apparatus for producing inorganic spheroidized particles, Japanese Patent Application Laid-Open No. 62-241542 discloses a water-cooling jacket provided on the outer surface of a refractory wall of a melting chamber and changing the amount of cooling water to change the amount of cooling water. A device for producing inorganic spheroidized particles for maintaining the temperature at 600 to 1000 ° C. and forming a coating layer of spheroidized particles having a thickness corresponding to the refractory wall temperature to prevent adhesion of the inorganic spheroidized particles to the melting chamber. Also, Japanese Patent Application Laid-Open No. 11-71107 discloses that the entire apparatus has a water-cooled wall structure, and cooling air is supplied around the combustion flame to suppress convection of the combustion gas to prevent the inorganic spheroidized particles from adhering to the melting chamber. An apparatus for producing inorganic spheroidized particles to be prevented is disclosed.

【0008】[0008]

【発明が解決しようとする課題】しかしながら、前記先
行技術は溶融室への無機質球状化粒子の付着を防止する
ことは可能であるが、両者とも溶融室内の火炎形成域に
おける雰囲気温度を制御していないので燃焼火炎温度を
当該無機質原料粉体の溶融温度以上に維持できず、良好
な無機質球状化粒子を効率よく得ることができないとい
う課題を有する。さらに、無機質原料粉体の種類や粒
径、滞留時間等の種々の処理条件に対応できないという
課題を有する。
However, the above prior art can prevent the adhesion of the inorganic spheroidized particles to the melting chamber, but both control the ambient temperature in the flame forming area in the melting chamber. Therefore, there is a problem that the combustion flame temperature cannot be maintained higher than the melting temperature of the inorganic raw material powder, and good inorganic spheroidized particles cannot be efficiently obtained. Furthermore, there is a problem that it is not possible to cope with various processing conditions such as the type, particle size, and residence time of the inorganic raw material powder.

【0009】したがって、本発明は、溶融室の火炎形成
域における雰囲気温度を所定温度範囲内に維持して良好
な無機質球状化粒子を効率よく得るとともに、無機質原
料粉体の種類や粒径、滞留時間等の種々の処理条件に対
応できる無機質球状化粒子製造設備を提供することを目
的とする。
Therefore, according to the present invention, good inorganic spheroidized particles can be efficiently obtained by maintaining the ambient temperature in the flame forming region of the melting chamber within a predetermined temperature range, and the type, particle size and retention of the inorganic raw material powder can be improved. An object of the present invention is to provide an inorganic spheroidized particle production facility that can cope with various processing conditions such as time.

【0010】[0010]

【課題を解決するための手段】本発明は、前記目的を達
成するために、天井部に燃焼装置を有し、側壁が耐火物
で形成された溶融室と、この溶融室に接続された水冷壁
構造の冷却室とからなる無機質球状化粒子製造装置にお
いて、前記溶融室を上部帯と下部帯とに区画し、かつ、
前記上部帯および下部帯の内壁面に沿って冷却気体を噴
出する冷却気体供給手段を円周方向に複数設けるととも
に、前記上部帯の雰囲気温度を無機質原料粉体の溶融温
度よりも300〜600℃低く維持する無機質球状化粒
子製造装置としたものである。
SUMMARY OF THE INVENTION In order to achieve the above object, the present invention provides a melting chamber in which a ceiling has a combustion device, a side wall is made of refractory, and a water cooling system connected to the melting chamber. In an apparatus for producing inorganic spheroidized particles comprising a cooling chamber having a wall structure, the melting chamber is partitioned into an upper zone and a lower zone, and
A plurality of cooling gas supply means for jetting a cooling gas along the inner wall surfaces of the upper band and the lower band are provided in the circumferential direction, and the atmosphere temperature of the upper band is set to 300 to 600 ° C. higher than the melting temperature of the inorganic raw material powder. This is an apparatus for producing inorganic spheroidized particles which is kept low.

【0011】また、前記冷却室の上部に直胴部と下端部
に先絞り状をなした漏斗部とを設けることが好ましい。
It is preferable that a straight body portion and a funnel portion having a tapered shape be provided at a lower end portion of the cooling chamber.

【0012】さらに、前記冷却室の下部に、一端部に外
気吸引口を有し、他端側に吸引手段を備えた捕集装置に
連通するダクトを設けることが好ましい。
Further, it is preferable that a duct communicating with a collecting device having an outside air suction port at one end and a suction means at the other end is provided below the cooling chamber.

【0013】[0013]

【発明の実施の形態】つぎに、本発明の実施の形態を図
にしたがって説明する。図1は、本発明にかかる無機質
球状化粒子製造装置Tを示し、大略、天井部4に燃焼装
置5を備え、側壁2が、たとえば、高純度アルミナ質等
の耐火物で形成された溶融室1と、この溶融室1の下部
に接続された水冷構造の冷却室8とから構成されてい
る。
Next, an embodiment of the present invention will be described with reference to the drawings. FIG. 1 shows an inorganic spheroidized particle manufacturing apparatus T according to the present invention, which is generally provided with a combustion device 5 on a ceiling part 4 and a side wall 2 formed of a refractory material such as high-purity alumina. 1 and a cooling chamber 8 of a water cooling structure connected to the lower part of the melting chamber 1.

【0014】前記溶融室1は、室内断面積が下方に行く
につれて段階的に大きくなっており、室内壁の各段差部
3には冷却気体供給手段6としてのノズルが円周方向に
複数個ずつ取り付けられており、このノズル6の先端に
形成した下方に開口する噴出孔7からの冷却気体(空
気)を下方に噴出して、側壁2の壁面温度を下げるよう
になっている。
The melting chamber 1 gradually increases in size as the cross-sectional area of the chamber goes downward, and a plurality of nozzles serving as cooling gas supply means 6 are provided at each stepped portion 3 of the indoor wall in the circumferential direction. The cooling gas (air) is ejected downward from an ejection hole 7 which is formed at the tip of the nozzle 6 and opens downward, thereby lowering the wall surface temperature of the side wall 2.

【0015】また、前記溶融室1は上部帯Aと下部帯B
とに区画され、上部帯Aには図示しない温度調節計と温
度検出手段とを備え、これら温度調節計と温度検出手段
からの温度信号により前記ノズル6からの冷却気体噴出
流量を調節し、上部帯Aの火炎形成域における雰囲気温
度を無機質原料粉体の溶融温度よりも300〜600℃
低く維持する。具体的には、無機質原料粉体がMgOの
場合、溶融温度は2800℃であるため2200〜25
00℃、TiO2の場合は同様にして1225〜152
5℃、Al23の場合は、同様にして1450〜175
0℃、SiO2の場合も同様1113〜1413℃に上
部帯Aの温度を制御する。
The melting chamber 1 has an upper band A and a lower band B
The upper zone A is provided with a temperature controller and a temperature detecting means (not shown), and the flow rate of the cooling gas ejected from the nozzle 6 is adjusted by a temperature signal from the temperature controller and the temperature detecting means. The temperature of the atmosphere in the flame formation zone of zone A is 300 to 600 ° C. lower than the melting temperature of the inorganic raw material powder.
Keep low. Specifically, when the inorganic raw material powder is MgO, the melting temperature is 2800 ° C.,
In the case of 00 ° C. and TiO 2 ,
In the case of 5 ° C. and Al 2 O 3 , 1450 to 175
In the case of 0 ° C. and SiO 2 , the temperature of the upper zone A is similarly controlled to 1113 to 1413 ° C.

【0016】なお、上部帯Aの雰囲気温度を無機質原料
粉体の溶融温度より300〜600℃低くする理由は、
300℃以下であると無機質球状化粒子の肥大率が高く
なったり、側壁2への溶融飛散粒子の付着量が増大して
側壁の清掃頻度が高くなり生産性が悪化し、逆に600
℃以上であると球状化率が悪く、かつ、品質も悪化する
からである。
The reason for lowering the ambient temperature of the upper zone A by 300 to 600 ° C. than the melting temperature of the inorganic raw material powder is as follows.
When the temperature is lower than 300 ° C., the enlargement rate of the inorganic spheroidized particles increases, the amount of the molten scattered particles attached to the side wall 2 increases, the frequency of cleaning the side wall increases, and the productivity deteriorates.
If the temperature is higher than ℃, the spheroidization ratio is poor and the quality is also deteriorated.

【0017】前記上部帯Aは燃焼装置5による火炎形成
部であることが好ましい。
It is preferable that the upper band A is a flame forming section formed by the combustion device 5.

【0018】また、前記下部帯Bは前記上部帯Aの燃焼
火炎温度を保持する目的で設置され、すなわち、連接す
る冷却室8の開口熱損失による温度低下を防止する目的
で設置されている。そして、前記冷却気体供給手段6か
らの冷却気体(空気)を下方に噴出して側壁2への無機
質球状化粒子の付着を防止している。
The lower zone B is provided for the purpose of maintaining the combustion flame temperature of the upper zone A, that is, for the purpose of preventing a decrease in temperature due to heat loss in the opening of the cooling chamber 8 connected thereto. Then, the cooling gas (air) from the cooling gas supply means 6 is jetted downward to prevent the inorganic spheroidized particles from adhering to the side wall 2.

【0019】前記溶融室1の天井部4に設けた燃焼装置
5であるバーナは、燃焼火炎の形成が均一で、安定燃焼
可能なものであれば限定されないが、図3に示すように
先端内面が末広がり形状の開口20aを有する原料粉体
供給管20の外周部に所定間隔をもって先端内面が末広
がり形状の開口21aを有する第1供給管21を配設し
て前記原料粉体供給管20との間に燃料ガス流路P1
形成するとともに、前記第1供給管21の外周部に所定
間隔をもって先端に直進部を有し、かつ、冷却水循環流
路23を備えた第2供給管22を配設して前記第1供給
管21と第2供給管22との間に酸素あるいは酸素富化
空気からなる燃焼用気体流路P2を形成し、前記原料粉
体供給管20、燃料ガス流路P1および燃焼用気体流路
2を、前記第2供給管22の先端部で、かつ、前記燃
焼用気体流路P2よりも前方に開口する凹部24aから
なる保炎部24を有するバーナが好適である。
The burner, which is the combustion device 5 provided on the ceiling 4 of the melting chamber 1, is not limited as long as it has a uniform combustion flame and can stably burn, but as shown in FIG. A first supply pipe 21 having an opening 21a having a divergent shape at the front end is disposed at an outer peripheral portion of the raw material powder supply pipe 20 having a divergent opening 20a. A fuel gas flow path P 1 is formed between the first supply pipe 21 and a second supply pipe 22 having a straight-moving portion at a tip thereof at a predetermined interval on an outer peripheral portion of the first supply pipe 21 and having a cooling water circulation flow path 23. And a combustion gas flow path P 2 made of oxygen or oxygen-enriched air is formed between the first supply pipe 21 and the second supply pipe 22. the road P 1 and the combustion gas channel P 2, the second test At the tip of the tube 22, and a burner having a flame stabilizing unit 24 composed of the recess 24a which opens to the front than the combustion gas flow path P 2 are suitable.

【0020】前記冷却室8は、水冷壁構造でコンパクト
な設置面積で十分な伝熱面積を確保するため、直胴部9
と下端部が先絞り状をなした漏斗部10とからなり、前
記溶融室1で球状化された無機質球状化粒子を、たとえ
ば、400℃に冷却するようになっている。
The cooling chamber 8 has a water-cooled wall structure, a compact installation area, and a sufficient heat transfer area.
And a funnel part 10 having a tapered end at the lower end. The inorganic spheroidized particles spherical in the melting chamber 1 are cooled to, for example, 400 ° C.

【0021】また、前記冷却室8の下部には、一端部に
外気吸引口11を有し、他端部が図示しない吸引手段を
備えた捕集装置に連通するダクト12が設けてある。
Further, a duct 12 having an outside air suction port 11 at one end and a communication end with a collection device having a suction means (not shown) is provided at the lower end of the cooling chamber 8 at the other end.

【0022】つぎに、前記構成からなる無機質球状化粒
子製造装置Tの操業について説明する。
Next, the operation of the apparatus T for producing inorganic spheroidized particles having the above configuration will be described.

【0023】前記原料粉体供給管20から、たとえば、
MgO粉体および空気あるいは純酸素か酸素富化空気等
の燃焼用気体の一部を、燃料ガス流路からLPG、LN
G等の気体燃料を、前記燃焼用気体流路から空気、純酸
素あるいは酸素富化空気等の残りの燃焼用気体をそれぞ
れ供給して点火する。
From the raw material powder supply pipe 20, for example,
A part of the combustion gas such as MgO powder and air or pure oxygen or oxygen-enriched air is supplied from the fuel gas passage to LPG, LN.
A gaseous fuel such as G is ignited by supplying the remaining combustion gas such as air, pure oxygen or oxygen-enriched air from the combustion gas flow path.

【0024】つまり、無機質原料粉体は、燃料ガスと燃
焼用気体とにより形成される高温の燃焼火炎中に燃焼用
気体の一部とともに供給され、燃焼火炎中で加熱され浮
遊状態で溶融して球状化する。この球状化溶融粒子はや
がて前記燃焼火炎域外へ飛散するが、上部帯Aはノズル
6からの冷却気体噴出量を室内温度(火炎形成域におけ
る雰囲気温度)に基づき制御することで当該無機質原料
粉体の溶融温度より300〜600℃低く維持されてい
る。したがって、燃焼火炎温度を当該無機質原料粉体の
溶融温度以上に保持できる。さらに、種々の処理条件に
応じた適正な燃焼火炎温度制御が可能となる。また、下
部帯Bで前記上部帯Aの燃焼火炎温度保持するととも
に、側壁2の内面近傍にはノズル6からの冷却気体が下
方に向かって供給されているため、燃焼火炎域から飛び
出した飛散粒子は側壁2の内面に融着(付着)すること
はない。
That is, the inorganic raw material powder is supplied together with a part of the combustion gas into a high-temperature combustion flame formed by the fuel gas and the combustion gas, and is heated in the combustion flame and melted in a floating state. Spheroidize. The spheroidized molten particles eventually scatter outside the combustion flame region. However, the upper zone A controls the amount of cooling gas jetted from the nozzle 6 based on the room temperature (atmosphere temperature in the flame formation region) to thereby control the inorganic raw material powder. Is maintained at 300 to 600 ° C. lower than the melting temperature. Therefore, the combustion flame temperature can be maintained at or above the melting temperature of the inorganic raw material powder. Furthermore, appropriate combustion flame temperature control according to various processing conditions becomes possible. In addition, the lower zone B holds the combustion flame temperature of the upper zone A, and the cooling gas from the nozzle 6 is supplied to the vicinity of the inner surface of the side wall 2 in a downward direction. Does not fuse (adhere) to the inner surface of the side wall 2.

【0025】前記のようにして、球状化された無機質球
状化粒子は冷却室8を落下中に約400℃に冷却されて
ダクト12内に落下して、外気吸引口11から吸引され
る空気によって約200℃まで冷却されて捕集装置に回
収されることになる。
The spheroidized inorganic spheroidized particles are cooled to about 400 ° C. while falling through the cooling chamber 8 and fall into the duct 12, and are dropped by the air sucked from the outside air suction port 11. It is cooled to about 200 ° C. and collected in the collection device.

【0026】また、前記ダクト12内に落下した無機質
球状化粒子は約400℃に冷却されているため、これを
200℃に冷却するに必要な吸引空気量は少なくてよ
く、高価な捕集装置の容量を増やす必要がないばかり
か、捕集装置内のバグフィルタも高温用である必要がな
いため安価なものを使用することができる。
Further, since the inorganic spheroidized particles dropped into the duct 12 are cooled to about 400 ° C., the amount of suction air necessary for cooling the particles to 200 ° C. may be small, and an expensive collecting device In addition to the need to increase the capacity, the bag filter in the collecting device does not need to be used for high temperatures, so that an inexpensive bag filter can be used.

【0027】なお、前記実施の形態では、燃焼装置5と
して1本のバーナを示したが、バーナ5を複数本設置
し、無機質球状化粒子の生産量に応じて本数を選ぶよう
にしてもよい。
In the above embodiment, one burner is shown as the burner 5, but a plurality of burners 5 may be provided, and the number of burners 5 may be selected according to the production amount of the inorganic spheroidized particles. .

【0028】[0028]

【発明の効果】以上の説明で明らかなように、本発明に
よれば、溶融室を上部帯と下部帯とに区画し、かつ、前
記上部帯および下部帯の壁面に沿って冷却気体を噴出す
る冷却気体供給手段を円周方向に複数設けて前記溶融室
の上部帯の雰囲気温度を無機質原料粉体の溶融温度より
も300〜600℃低く維持する構成としたので、溶融
室内の火炎形成域における雰囲気温度が前記冷却気体供
給手段からの冷却気体噴出量の調整により適正範囲に維
持できる。すなわち、燃焼火炎温度を無機質原料粉体の
溶融に最適な温度に保持でき、高品質の無機質球状化粒
子を得ることができる。
As is apparent from the above description, according to the present invention, the melting chamber is divided into an upper zone and a lower zone, and the cooling gas is jetted along the walls of the upper zone and the lower zone. A plurality of cooling gas supply means are provided in the circumferential direction to maintain the ambient temperature of the upper zone of the melting chamber lower by 300 to 600 ° C. than the melting temperature of the inorganic raw material powder. Can be maintained in an appropriate range by adjusting the cooling gas ejection amount from the cooling gas supply means. That is, the combustion flame temperature can be maintained at a temperature optimal for melting the inorganic raw material powder, and high-quality inorganic spheroidized particles can be obtained.

【0029】また、下部帯は連接する冷却室の開口熱損
失による火炎温度の低下を防止するとともに、冷却気体
供給手段からの冷却気体を炉壁面に沿って流すことで該
側壁温度を低く抑えることができるので、燃焼火炎から
の飛散溶融粒子が側壁に付着することを防止できる。
The lower zone prevents the flame temperature from being lowered due to the heat loss of the opening of the cooling chamber connected thereto, and suppresses the side wall temperature by flowing the cooling gas from the cooling gas supply means along the furnace wall. Therefore, it is possible to prevent the molten particles scattered from the combustion flame from adhering to the side wall.

【0030】なお、冷却帯上部に直胴部と下端部に先絞
り状をなした漏斗部とを設ければ、コンパクトな設置面
積で十分な伝熱面積を確保することができ、加熱されて
いる無機質球状化粒子の顕熱を所望の温度に冷却(抜
熱)できる。
By providing a straight body at the upper part of the cooling zone and a funnel part having a tapered shape at the lower end, a sufficient heat transfer area can be ensured with a compact installation area, and the heating area is reduced. The sensible heat of the inorganic spheroidized particles can be cooled (extracted) to a desired temperature.

【0031】さらに、前記冷却帯下部に、一端部に外気
吸引口を有し、他端部に捕集装置に連通するダクトを配
設することにより、前述の冷却された無機質球状化粒子
を外気吸引によってさらに冷却することができ、しか
も、吸引外気量は少量であるため捕集装置に連通する配
管を細くできるとともに、下流側の捕集装置の容量を増
やす必要がない等の効果を奏する。
Further, a duct having an outside air suction port at one end and a duct communicating with the collecting device at the other end is provided below the cooling zone, so that the cooled inorganic spheroidized particles can be removed from the outside air. The cooling can be further performed by suction, and the amount of outside air sucked is small, so that the piping communicating with the collecting device can be made thinner, and there is no need to increase the capacity of the collecting device on the downstream side.

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

【図1】 本発明にかかる無機質球状化粒子製造装置の
断面図。
FIG. 1 is a sectional view of an apparatus for producing inorganic spheroidized particles according to the present invention.

【図2】 図1の要部拡大断面図。FIG. 2 is an enlarged sectional view of a main part of FIG.

【図3】 図1の燃焼装置の断面図。FIG. 3 is a sectional view of the combustion device of FIG. 1;

【符号の説明】[Explanation of symbols]

1〜溶融室、2〜側壁、3〜段差部、4〜天井部、5〜
燃焼装置、6〜ノズル、7〜噴出孔、8〜冷却室、9〜
直胴部、10〜漏斗部、11〜外気吸引口、12〜ダク
ト、A〜上部帯、B〜下部帯、T〜無機質球状化粒子製
造装置。
1-melting chamber, 2-side wall, 3-step, 4-ceiling, 5
Combustion device, 6-nozzle, 7-outlet, 8-cooling room, 9-
Straight body portion, 10 funnel portion, 11 outside air suction port, 12 duct, A upper band, B lower band, T inorganic spheroidized particle manufacturing apparatus.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 天井部に燃焼装置を有し、側壁が耐火物
で形成された溶融室と、この溶融室に接続された水冷壁
構造の冷却室とからなる無機質球状化粒子製造装置にお
いて、 前記溶融室を上部帯と下部帯とに区画し、かつ、前記上
部帯および下部帯の内壁面に沿って冷却気体を噴出する
冷却気体供給手段を円周方向に複数設けるとともに、前
記上部帯の雰囲気温度を無機質原料粉体の溶融温度より
も300〜600℃低く維持することを特徴とする無機
質球状化粒子製造装置。
An inorganic spheroidized particle manufacturing apparatus comprising a melting chamber having a combustion device on a ceiling, a side wall formed of a refractory, and a cooling chamber having a water-cooled wall structure connected to the melting chamber. The melting chamber is divided into an upper band and a lower band, and a plurality of cooling gas supply means for jetting a cooling gas along inner wall surfaces of the upper band and the lower band are provided in a circumferential direction, and An apparatus for producing inorganic spheroidized particles, wherein the atmosphere temperature is maintained at 300 to 600 ° C. lower than the melting temperature of the inorganic raw material powder.
【請求項2】 前記冷却室が上部に直胴部と下端部に先
絞り状をなした漏斗部とを有することを特徴とする前記
請求項1に記載の無機質球状化粒子製造装置。
2. The apparatus for producing inorganic spheroidized particles according to claim 1, wherein the cooling chamber has a straight body portion at an upper portion and a funnel portion having a tapered shape at a lower end portion.
【請求項3】 前記冷却室の下部に、一端部に外気吸引
口を有し、他端側に吸引手段を備えた捕集装置に連通す
るダクトを設けたことを特徴とする前記請求項1または
2のいずれかに記載の無機質球状化粒子製造装置。
3. The cooling chamber according to claim 1, further comprising a duct having an outside air suction port at one end thereof and a suction device provided at the other end thereof with a suction means. Or the apparatus for producing inorganic spheroidized particles according to any one of the above items.
JP2000365262A 2000-11-30 2000-11-30 Apparatus for manufacturing inorganic spheroidized particle Pending JP2002166161A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000365262A JP2002166161A (en) 2000-11-30 2000-11-30 Apparatus for manufacturing inorganic spheroidized particle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000365262A JP2002166161A (en) 2000-11-30 2000-11-30 Apparatus for manufacturing inorganic spheroidized particle

Publications (1)

Publication Number Publication Date
JP2002166161A true JP2002166161A (en) 2002-06-11

Family

ID=18836068

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000365262A Pending JP2002166161A (en) 2000-11-30 2000-11-30 Apparatus for manufacturing inorganic spheroidized particle

Country Status (1)

Country Link
JP (1) JP2002166161A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114534634A (en) * 2022-01-18 2022-05-27 清华大学 Liquid fuel self-sustaining combustion flame synthesis burner

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114534634A (en) * 2022-01-18 2022-05-27 清华大学 Liquid fuel self-sustaining combustion flame synthesis burner

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