JP3028474B2 - Method and apparatus for producing fine hollow glass spheres - Google Patents
Method and apparatus for producing fine hollow glass spheresInfo
- Publication number
- JP3028474B2 JP3028474B2 JP9185848A JP18584897A JP3028474B2 JP 3028474 B2 JP3028474 B2 JP 3028474B2 JP 9185848 A JP9185848 A JP 9185848A JP 18584897 A JP18584897 A JP 18584897A JP 3028474 B2 JP3028474 B2 JP 3028474B2
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- gas
- control
- air
- hollow glass
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- QXJJQWWVWRCVQT-UHFFFAOYSA-K calcium;sodium;phosphate Chemical compound [Na+].[Ca+2].[O-]P([O-])([O-])=O QXJJQWWVWRCVQT-UHFFFAOYSA-K 0.000 title description 7
- 238000000034 method Methods 0.000 title description 6
- 239000007789 gas Substances 0.000 claims description 39
- 239000000919 ceramic Substances 0.000 claims description 27
- 238000002485 combustion reaction Methods 0.000 claims description 25
- 239000002737 fuel gas Substances 0.000 claims description 23
- 239000000446 fuel Substances 0.000 claims description 18
- 239000011521 glass Substances 0.000 claims description 16
- 239000000843 powder Substances 0.000 claims description 14
- 238000005243 fluidization Methods 0.000 claims description 11
- 238000004519 manufacturing process Methods 0.000 claims description 9
- 239000002994 raw material Substances 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 14
- 239000004576 sand Substances 0.000 description 10
- 239000011449 brick Substances 0.000 description 3
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 239000000567 combustion gas Substances 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 230000004927 fusion Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 2
- 229910010271 silicon carbide Inorganic materials 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 244000025254 Cannabis sativa Species 0.000 description 1
- 102220579497 Macrophage scavenger receptor types I and II_F23C_mutation Human genes 0.000 description 1
- 241000276498 Pollachius virens Species 0.000 description 1
- 230000005856 abnormality Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229910052878 cordierite Inorganic materials 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- JSKIRARMQDRGJZ-UHFFFAOYSA-N dimagnesium dioxido-bis[(1-oxido-3-oxo-2,4,6,8,9-pentaoxa-1,3-disila-5,7-dialuminabicyclo[3.3.1]nonan-7-yl)oxy]silane Chemical compound [Mg++].[Mg++].[O-][Si]([O-])(O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2)O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2 JSKIRARMQDRGJZ-UHFFFAOYSA-N 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000005306 natural glass Substances 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/10—Forming beads
- C03B19/107—Forming hollow beads
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は、空気と燃料ガスの
混合ガスに、微粒中空ガラス球状体の原料の粉体を随伴
させて熱処理するセラミックスボール媒体内燃式流動床
炉方式の微粒中空ガラス球状体の製造方法及び装置に関
するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a ceramic ball medium internal combustion type fluidized bed furnace type fine-grained hollow glass sphere which is heat-treated by mixing powder of raw material for a fine-grained hollow glass sphere with a mixed gas of air and fuel gas. A method and apparatus for producing a body.
【0002】[0002]
【従来の技術】シラスバルーン等の製造装置として用い
られる内燃式流動床炉の起動および温度制御に関して
は、日本特許第849394号に示される方法がある。
これは、あらかじめ使用燃料の引火点以上に加熱した砂
媒体(レンガ粉)中に、空気と燃料ガスとの混合ガスを
吹き込み、高温流動状態を形成させ、温度を維持するも
のである。この温度維持は、熱電対に接続した制御器で
燃料ガスを電動弁で制御しており、設定温度±5℃程度
である。2. Description of the Related Art Japanese Patent No. 848394 discloses a method for starting and controlling the temperature of an internal combustion type fluidized bed furnace used as an apparatus for producing a shirasu balloon or the like.
In this method, a mixed gas of air and a fuel gas is blown into a sand medium (brick powder) heated in advance to the flash point of the used fuel to form a high-temperature fluid state and maintain the temperature. This temperature is maintained by controlling the fuel gas by a motor-operated valve by a controller connected to a thermocouple, and is at a set temperature of about ± 5 ° C.
【0003】[0003]
【発明が解決しようとする課題】従来技術の前記内燃式
流動床炉では、砂媒体の温度が燃料ガスの引火点以下の
状態で、高温流動時と同じ空燃比の混合ガスを導入する
と、砂媒体が着火源の役割を果たさないので混合ガスは
失火する。その失火対策として、空気と燃料ガスの混合
ガスを導入する前に、付属の予熱装置で砂媒体を引火点
以上に加熱する必要があった。そこで、北海道工業開発
試験所報告42,(1987)に示されるように、流動
部分の中心付近に横穴を空けて強力に加熱しなければな
らなかった。この予熱バーナーは、高温流動時には使用
しないので、砂の逆流入が起こり、流動化する砂の量が
経時変化するなど、高温流動の外乱要素となっていた。
また、流動時に予熱バーナーの取付口付近での熱損失に
より流動床内で10℃以上温度の低い部分が生じ、被加
熱物の加熱が不均一になるという欠点があった。また、
砂媒体にレンガ粉やケイ砂が使われているが、これら
は、流動時によく破砕するので、その破片が微粒中空ガ
ラス球状体製品(例えば、シラスバルーン)に混入する
という欠点がある。更に、温度維持に関しては、制御性
が比較的遅い電動弁を用いて燃料ガスのみを全開−全閉
制御しているので、最適燃焼空燃比の変動が外乱要素と
なり、設定温度±5℃程度となり温度制御性が劣る。In THE INVENTION Problems to be Solved by the internal combustion fluidized bed furnace of the prior art, a flash point below the state of the temperature of the fuel gas sand medium, when a mixed gas of the same air-fuel ratio at a high temperature fluidized sand The gas mixture will misfire because the medium does not serve as an ignition source. As a countermeasure against the misfiring, it was necessary to heat the sand medium to a temperature higher than the flash point with an attached preheating device before introducing a mixed gas of air and fuel gas. Therefore, as shown in Hokkaido Industrial Development Laboratory Report 42, (1987), it was necessary to open a side hole near the center of the flowing part and heat it vigorously. Since this preheating burner is not used at the time of high-temperature fluidization, the backflow of sand occurs, and the amount of sand to be fluidized changes with time.
In addition, there is a disadvantage that a portion having a low temperature of 10 ° C. or more is generated in the fluidized bed due to heat loss near the attachment port of the preheating burner during the flow, and the heating of the object to be heated becomes uneven. Also,
Although brick powder and silica sand in sand media are used, it is so well fracturing during flow, the debris fine hollow moth
There is a drawback of mixing in lath spheroid products (for example, shirasu balloon). Further, regarding temperature maintenance, since only the fuel gas is fully opened and fully closed using an electrically operated valve having relatively slow controllability, the fluctuation of the optimum combustion air-fuel ratio becomes a disturbance factor, and the set temperature becomes about ± 5 ° C. Poor temperature controllability.
【0004】[0004]
【課題を解決するための手段】上記課題を解決するため
に、予熱バーナーを使用せず、媒体にセラミックスボー
ルを用いた流動床炉を開発し、昇温時と高温流動時の最
適燃焼条件を細かく検討し、下記構成の発明をするに至
った。 (1)内燃式流動床炉内の媒体としてセラミックスボー
ルを用い、同セラミックスボールに燃料ガスと空気との
混合ガスを供給し、前記ガス燃焼熱でセラミックスボー
ルを900℃以上まで昇温し、設定温度±3℃以内で温
度制御を行うと同時に微粒中空ガラス球状体の原料粉体
を前記混合ガスに随伴させて供給して、微粒中空ガラス
球状体を製造することを特徴とする微粒中空ガラス球状
体の製造方法 。(2)前記(1)項記載の微粒中空ガラス球状体の製造
方法において、付属の予熱バーナーを使わずに、昇温時
に空気流量調節計と燃料ガス流量調節計に適切な流量設
定値を与えるダブルクロスリミット制御によりセラミッ
クスボールをガス燃焼熱で徐々に昇温させ、高温流動化
直前に流動床温度調節計のPID出力を強制的に減少さ
せるダイレクト制御に切替えることによって急激な温度
上昇を防止し高温流動化した後、空気と燃料ガスの混合
ガス総量をあらかじめ高温流動化用に設定された量に調
整す る可変空燃比制御を行い、さらに流動床温度調節計
のPID設定を昇温時と変更する可変PID制御を前記
ダブルクロスリミット制御と合わせて行うことによっ
て、前記混合ガスの引火点に満たないセラミックスボー
ルをガス燃焼熱で900℃以上まで昇温し、設定温度±
3℃以内の自動温度制御 を行うことを特徴とする微粒中
空ガラス球状体の製造方法。 (3)流動床媒体としてのセラミックスボールを有する
内燃式流動床炉と、同セラミックスボールに燃料ガスと
空気との混合ガスを供給するための混合ガス供給手段
と、前記ガス燃焼熱でセラミックスボールを900℃以
上まで昇温し、設定温度±3℃以内で温度制御を行う温
度制御手段と、前記温度制御と同時に微粒中空ガラス球
状体の原料粉体を前記混合ガスに随伴させて供給する原
料粉体供給手段とを備えていることを特徴とする微粒中
空ガラス球状体の製造装置。 (4)前記(3)項記載の微粒中空ガラス球状体の製造
装置において、昇温時に空気流量調節計と燃料ガス流量
調節計に適切な流量設定値を与えるダブルクロスリミッ
ト制御手段と、セラミックスボールをガス燃焼熱で徐々
に昇温させ、高温流動化直前に流動床温度調節計のPI
D出力を強制的に減少させるダイレクト制御手段と、空
気と燃料ガスの混合ガス総量をあらかじめ高温流動化用
に設定された量に調整する可変空燃比制御手段と、流動
床温度調節計のPID設定を昇温時と変更する可変PI
D制御手段と、さらに高温流動時のダブルクロスリミッ
ト制御手段を備え、前記混合ガスの引火点に満たないセ
ラミックスボールをガス燃焼熱で900℃以上まで昇温
し、設定温度±3℃以内の自動温度制御を行うようにし
たことを特徴とする微粒中空ガラス球状体の製造装置。 In order to solve the above-mentioned problems, a fluidized bed furnace using a ceramic ball as a medium without using a preheating burner has been developed. After careful examination , we came to the invention with the following structure.
Was. (1) Ceramic boa as a medium in an internal combustion type fluidized bed furnace
Of fuel gas and air on the ceramic ball
The mixed gas is supplied, and the ceramics
Temperature to 900 ° C or higher,
Of raw material powder for fine hollow glass spheres
Is supplied along with the mixed gas to form fine hollow glass.
Fine-grained hollow glass sphere characterized by producing spherical body
How to make the body . (2) Production of the fine hollow glass spheres according to the above (1)
Method, without using the attached preheating burner,
Air flow controller and fuel gas flow controller
The ceramic is controlled by the double cross limit control that gives a constant value.
Grass ball is gradually heated by the heat of gas combustion to fluidize it at high temperature.
Immediately before, the PID output of the fluidized bed temperature controller was forcibly reduced.
Sudden temperature by switching to direct control
Mixing air and fuel gas after preventing rise and fluidizing at high temperature
Adjust the total gas volume to the volume preset for high temperature fluidization.
Performed pollock Ru variable air-fuel ratio control, further fluidized bed temperature controller
Variable PID control to change the PID setting of
By performing this together with the double cross limit control,
And the ceramic body below the flash point of the mixed gas
Temperature to 900 ° C or more with gas combustion heat,
In fine particles characterized by automatic temperature control within 3 ° C
A method for producing an empty glass sphere. (3) Having ceramic balls as a fluidized bed medium
An internal combustion type fluidized bed furnace and the same ceramic balls with fuel gas
Mixed gas supply means for supplying a mixed gas with air
And heat the ceramic balls by 900 ° C or less
Temperature that rises to the top and performs temperature control within the set temperature ± 3 ° C
Degree control means and simultaneously with said temperature control, fine hollow glass spheres
To supply the raw material powder in the form of a solid with the mixed gas
Characterized by being provided with a powder supply means.
Equipment for manufacturing empty glass spheres. (4) Production of the fine hollow glass spheres according to the above (3)
When the temperature rises, the air flow controller and the fuel gas flow
Double cross limit to provide the controller with appropriate flow settings
Control means and the ceramic balls gradually with the heat of gas combustion
Immediately before fluidization at a high temperature.
Direct control means for forcibly reducing the D output;
The total gas mixture of gas and fuel gas is used for high-temperature fluidization in advance.
Variable air-fuel ratio control means for adjusting to the amount set in
Variable PI to change the PID setting of the floor temperature controller from when the temperature is raised
D control means and double cross limit
Control means for controlling the temperature below the flash point of the mixed gas.
Ramix ball heated to 900 ° C or more by gas combustion heat
And perform automatic temperature control within the set temperature ± 3 ° C.
An apparatus for producing fine hollow glass spheres.
【0005】本発明者らは前記のとおり媒体にセラミッ
クスボールを用いた流動床炉を開発し、昇温時と高温流
動時の最適燃焼条件を細かく検討した結果、昇温時と高
温流動時の最適燃焼条件が異なること、高温流動化の直
前に温度の急上昇が起こり危険性が高いことが明らかに
なった。そこで、それらの解決方法について実験を繰り
返した結果、流動床炉の媒体にセラミックスボールを用
いて、燃焼条件に細かく対応する可変空燃比制御、ダイ
レクト制御、可変PID制御及びダブルクロスリミット
燃焼制御による温度調節計の最適出力の設定を行なうこ
とで、安全に、しかも短時間で自動起動化が達成できる
ことを見出し、高温流動時の高精度温度制御も可能な微
粒中空ガラス球状体の製造方法及び装置を開発すること
に成功した。[0005] The inventors of the present invention have made ceramic media as described above.
Developed a fluidized-bed furnace using hot-ball
A close examination of the optimal combustion conditions during operation revealed that the optimal combustion conditions differed between when the temperature was raised and when the fluid flowed at a high temperature, and that there was a high risk of a sudden rise in temperature immediately before the fluidization at a high temperature. Therefore, as a result of repeating experiments on these solutions , ceramic balls were used for the fluidized bed furnace medium.
In addition, by setting the optimum output of the temperature controller by variable air-fuel ratio control, direct control, variable PID control and double cross limit combustion control that precisely corresponds to the combustion conditions, automatic startup can be performed safely and in a short time. It found that can be achieved, also fine high-precision temperature control during hot flow
We succeeded in developing a method and an apparatus for producing a hollow glass sphere .
【0006】昇温時と高温流動時では、媒体(セラミッ
クスボール)の潜熱、輻射熱の違いにより最適燃焼のP
ID制御条件と空燃比が異なるので、制御条件を変更し
なければならない。その変更を怠ると、炉温の急上昇に
よる媒体の融着や逆火が起こり危険な状態に陥り、流動
床炉の消耗、破損を生じ、制御不能になる。そこで、設
定温度から50℃低い温度で、自動的にPID制御条件
の変更とともに可変空燃比制御に切替わるように、ま
た、温度の変化率を認識し、変化率に応じて温度調節計
の最適出力を設定する回路を予めプログラムしておくこ
とで、温度急上昇を避け、安全に、しかも短時間で高温
流動化することが可能になった。[0006] The difference between the latent heat and the radiant heat of the medium (ceramic ball) between the time of temperature rise and the time of high-temperature flow is the optimum combustion P.
Since the ID control condition and the air-fuel ratio are different, the control condition must be changed. If the change is neglected, the fusion of the medium or flashback occurs due to a rapid rise in the furnace temperature, and a dangerous state occurs, and the fluidized-bed furnace is consumed and damaged, resulting in loss of control. Therefore, at the temperature lower by 50 ° C. from the set temperature, the PID control condition is automatically changed and the variable air-fuel ratio control is switched, and the rate of change of the temperature is recognized. By programming the circuit for setting the output in advance, it has become possible to avoid a sudden rise in temperature, and to achieve a safe and quick high-temperature fluidization.
【0007】高温流動時に空燃比を一定化すると、温度
調節計制御出力とともに変動する燃料ガス流量に応じて
空気量が変動するため、流動床を通過する燃焼ガス量が
変動する。これでは、被加熱物(微粒中空ガラス球状体
の原料粉体)の熱履歴が変動し一定品質の微粒中空ガラ
ス球状体製品が得られないので、燃焼ガス量をほぼ一定
にするために、空燃比を変動させて燃料ガス流量を制御
する可変空燃比制御を行った。この温度制御に重要なの
が、燃料ガス流量と空気量の正確な制御と計測である。
そのために、高精度で流量を制御できる空気作動式調節
弁(燃料ガス用、空気用)を用いた。更に、精度を上げ
るために、供給圧力を一定化させる自力式減圧弁(燃料
ガス用、空気用)を採用した。そして、流量計測用とし
て高精度のデジタルガス流量計を用いた。安全対策とし
て、炉下の温度、空気圧力、インバーター及び制御温度
の異常が生じた場合には、燃料ガスを緊急遮断するシス
テムを採用している。If the air-fuel ratio is made constant during high-temperature flow, the amount of air fluctuates in accordance with the fuel gas flow rate that fluctuates with the control output of the temperature controller, so that the amount of combustion gas passing through the fluidized bed fluctuates. In this case, the object to be heated ( fine-grained hollow glass sphere
Heat history of the raw material powder) is fluctuated and the quality of fine hollow particles
Since a spherical product was not obtained, variable air-fuel ratio control was performed in which the air-fuel ratio was varied to control the fuel gas flow rate in order to keep the amount of combustion gas substantially constant. Important to this temperature control is accurate control and measurement of the fuel gas flow rate and the air flow rate.
For this purpose, air-operated control valves (for fuel gas and air) that can control the flow rate with high precision were used. Further, in order to improve the accuracy, a self-acting pressure reducing valve (for fuel gas and for air) for stabilizing the supply pressure is employed. A high-precision digital gas flow meter was used for flow measurement. As a safety measure, a system is adopted that shuts off the fuel gas in the event of an abnormality in the temperature under the furnace, air pressure, inverter and control temperature.
【0008】また、本発明の装置には、予熱バーナーを
取り付けていないので、流動床部分が完全な円筒状であ
り、温度分布の均一化に適した構造をしている。これら
の機器および構造と高性能な温度調節計、燃料ガス調節
計、空気量調節計、空燃比設定器との組み合わせによ
り、高精度の温度制御が可能となった。以上の操作を自
動化することにより、短時間で安定な高温流動状態を形
成させることに成功した。更に、製品中への媒体破片の
混入を防止するために、媒体として耐熱衝撃性に優れた
炭化珪素ボール、コージェライトボールを用いた。これ
より、高温流動時に媒体の破砕がほとんど無くなり、高
品質の製品の製造が可能になった。本発明で用いられる
無機発泡物質の原料としては、ガラス質火山砕屑物、ガ
ラス質火山岩などの天然ガラスがあり、発泡源を有する
人工のガラスも発泡させることが可能となっている。 Further, since the apparatus of the present invention does not include a preheating burner, the fluidized bed portion has a completely cylindrical shape and has a structure suitable for uniform temperature distribution. By combining these devices and structures with high-performance temperature controllers, fuel gas controllers, air flow controllers, and air-fuel ratio setting devices, highly accurate temperature control has become possible. By automating the above operations, a stable high-temperature fluidized state was successfully formed in a short time. Furthermore, in order to prevent mixing of the medium fragments into the product, silicon carbide balls and cordierite balls having excellent thermal shock resistance were used as the medium. Thereby, the crushing of the medium during the high temperature fluidization was almost eliminated, and the production of a high quality product became possible. Used in the present invention
Raw materials for inorganic foaming materials include vitreous volcaniclastics and gas.
There is natural glass such as lath volcanic rock and has foam source
Artificial glass can also be foamed.
【0009】[0009]
【実施例】内径132mmの内筒からなる流動床部分
に、直径1.5mmのセラミックスボール(炭化珪素)
を1750g装填する。この流動床部分にプロパンガス
と空気の混合ガスを導入し着火後、一定空燃比でPID
制御してセラミックスボールを燃焼熱で昇温する。そし
て、セラミックスボールが設定温度(1000℃)から
50℃低い温度(950℃)になったところで、PID
制御条件が変更されるとともに可変空燃比制御に切替わ
り、設定温度1000℃±3℃以下で安定化した。着火
から設定温度に安定するまでの所要時間は12分間であ
った。被加熱物の粉体には、平均粒径4μmのシラス微
粉末(鹿児島県吉田町産)を用い、燃焼前の混合ガスに
随伴させて流動床に1.0kg/hで供給し、流動床で
急速加熱により発泡させ、平均粒径6.2μm、カサ比
重0.3の微細で軽量なシラスバルーンを製造すること
ができた。シラス微粉末の供給時においても、可変PI
D温度制御と可変空燃比制御により設定温度±3℃以下
に維持されており、不純物の無い高品質のシラスバルー
ンを製造することができた。EXAMPLE A ceramic ball (silicon carbide) having a diameter of 1.5 mm was placed on a fluidized bed portion having an inner cylinder having an inner diameter of 132 mm.
Are charged at 1750 g. After introducing a mixed gas of propane gas and air into the fluidized bed and igniting, the PID is maintained at a constant air-fuel ratio.
Under control, the temperature of the ceramic balls is raised by the heat of combustion. Then, when the temperature of the ceramic ball is lowered by 50 ° C. (950 ° C.) from the set temperature (1000 ° C.), the PID
As the control conditions were changed, the air conditioner was switched to variable air-fuel ratio control and stabilized at a set temperature of 1000 ° C. ± 3 ° C. or less. The time required from ignition to stabilization at the set temperature was 12 minutes. As the powder of the material to be heated, fine shirasu powder having an average particle diameter of 4 μm (produced by Yoshida-cho, Kagoshima Prefecture) was supplied to the fluidized bed at 1.0 kg / h in association with the mixed gas before combustion. To produce a fine and lightweight shirasu balloon having an average particle size of 6.2 μm and a bulk specific gravity of 0.3. Even when supplying fine Shirasu powder, variable PI
The D temperature control and the variable air-fuel ratio control maintained the temperature at or below the set temperature ± 3 ° C., and a high-quality shirasu balloon free of impurities could be manufactured.
【0010】[0010]
【発明の効果】本発明によれば、シラスバルーン等の微
粒中空ガラス球状体製品に、従来法のレンガ粉やケイ砂
等の砂媒体使用による場合の破片や不純物が混入するこ
とがほとんど無い。また、従来法におけるごとき炉温の
急上昇による媒体の融着は生じなく、流動床炉の消耗、
破損や制御不能となる危険が回避できる。 さらに、自動
的に短時間で高温流動化でき、高精度の流動床温度制御
が可能となり、自動化、省力化とともに高品質の製品の
製造が可能となる。 According to the present invention, fine particles such as shirasu balloons can be used.
Granular hollow glass spheroidal products, conventional brick powder and silica sand
Debris and impurities child contamination case of sand Courier equal
And almost no. In addition, the furnace temperature as in the conventional method
There is no fusion of the medium due to the sudden rise,
The risk of damage or loss of control can be avoided. Furthermore, high-temperature fluidization can be automatically performed in a short time, and fluidized-bed temperature control can be performed with high precision. As a result, high-quality products can be manufactured with automation and labor saving.
【図1】セラミックスボールを媒体に用いた内燃式流動
床炉の概要図である。FIG. 1 is a schematic diagram of an internal combustion type fluidized bed furnace using ceramic balls as a medium.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 神野 好孝 鹿児島県姶良郡隼人町小田1445番地1 鹿児島県工業技術センター内 (72)発明者 浜石 和人 鹿児島県姶良郡隼人町小田1445番地1 鹿児島県工業技術センター内 (72)発明者 吉村 景則 鹿児島県国分市川原岩坂1049番地 (72)発明者 刀根 俊二 北九州市小倉北区片野2丁目15番12号 審査官 徳永 英男 (56)参考文献 特開 平6−2811(JP,A) 特開 平7−315869(JP,A) 特開 昭50−47880(JP,A) 実開 昭61−96115(JP,U) 特公 昭51−22922(JP,B2) 特公 昭61−6289(JP,B2) 特公 昭63−65842(JP,B2) (58)調査した分野(Int.Cl.7,DB名) C03B 19/08 C03B 19/10 F23C 10/18 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Yoshitaka Kamino 1445-1, Oda, Hayato-cho, Aira-gun, Kagoshima Prefecture Inside the Kagoshima Industrial Technology Center (72) Kazuto Hamaishi 1445-1, Oda, Hayato-cho, Aira-gun, Kagoshima Kagoshima Prefectural Industrial Technology Center (72) Inventor Keinori Yoshimura 1049 Kawahara Iwasaka, Kokubu-shi, Kagoshima Prefecture (72) Inventor Shunji Tone 2--15-12 Katano, Kokurakita-ku, Kitakyushu City Examiner Hideo Tokunaga (56) References Special JP-A-6-2811 (JP, A) JP-A-7-315869 (JP, A) JP-A-50-47880 (JP, A) JP-A-61-96115 (JP, U) JP-B-51-22922 ( JP, B2) JP-B 61-6289 (JP, B2) JP-B 63-65842 (JP, B2) (58) Fields investigated (Int. Cl. 7 , DB name) C03B 19/08 C03B 19/10 F23C 10/18
Claims (4)
スボールを用い、同セラミックスボールに燃料ガスと空
気との混合ガスを供給し、前記ガス燃焼熱でセラミック
スボールを900℃以上まで昇温し、設定温度±3℃以
内で温度制御を行うと同時に微粒中空ガラス球状体の原
料粉体を前記混合ガスに随伴させて供給して、微粒中空
ガラス球状体を製造することを特徴とする微粒中空ガラ
ス球状体の製造方法。A ceramic ball is used as a medium in an internal combustion type fluidized bed furnace .
Supplying a mixed gas of air, ceramic in the gas combustion heat
The temperature was raised to 900 ° C. or higher Suboru original temperature control line Utodojini fine hollow glass within a set temperature ± 3 ° C.
The powder mixture is supplied along with the mixed gas to provide fine hollow particles.
A method for producing a fine hollow glass sphere, comprising producing a glass sphere.
造方法において、付属の予熱バーナーを使わずに、昇温
時に空気流量調節計と燃料ガス流量調節計に適切な流量
設定値を与えるダブルクロスリミット制御によりセラミ
ックスボールをガス燃焼熱で徐々に昇温させ、高温流動
化直前に流動床温度調節計のPID出力を強制的に減少
させるダイレクト制御に切替えることによって急激な温
度上昇を防止し高温流動化した後、空気と燃料ガスの混
合ガス総量をあらかじめ高温流動化用に設定された量に
調整する可変空燃比制御を行い、さらに流動床温度調節
計のPID設定を昇温時と変更する可変PID制御を前
記ダブルクロスリミット制御と合わせて行うことによっ
て、前記混合ガスの引火点に満たないセラミックスボー
ルをガス燃焼熱で900℃以上まで昇温し、設定温度±
3℃以内の自動温度制御を行うことを特徴とする微粒中
空ガラス球状体の製造方法。2. The method for producing a fine hollow glass sphere according to claim 1 , wherein the temperature is raised without using an attached preheating burner.
Sometimes an appropriate flow rate for air flow controllers and fuel gas flow controllers
The ceramic ball is gradually heated by the heat of gas combustion by the double cross limit control to give the set value,
Pressure of PID of fluidized bed temperature controller immediately before
Sudden temperature by switching to direct control
Temperature rise and fluidized at high temperature, then mix air and fuel gas.
Combined gas volume to the amount set in advance for high-temperature fluidization
Performs variable air-fuel ratio control for adjusting further fluidized bed temperature controller
Before variable PID control, which changes the PID setting of the gauge to that at the time of temperature rise
This can be performed in conjunction with the double cross limit control.
The temperature of the ceramic balls having a flash point less than the flash point of the mixed gas is raised to 900 ° C. or more by the heat of gas combustion, and the temperature is set at ± 10 ° C.
A method for producing a fine-grained hollow glass sphere, characterized by performing automatic temperature control within 3 ° C.
有する内燃式流動床炉と、同セラミックスボールに燃料
ガスと空気との混合ガスを供給するための混合ガス供給
手段と、前記ガス燃焼熱でセラミックスボールを900
℃以上まで昇温し、設定温度±3℃以内で温度制御を行
う温度制御手段と、前記温度制御と同時に微粒中空ガラ
ス球状体の原料粉体を前記混合ガスに随伴させて供給す
る原料粉体供給手段とを備えていることを特徴とする微
粒中空ガラス球状体の製造装置。3. A ceramic ball as a fluidized bed medium.
With an internal combustion type fluidized bed furnace and fuel on the ceramic balls
Mixed gas supply for supplying a mixed gas of gas and air
Means and a ceramic ball 900
Temperature rise to over ℃, and temperature control is performed within ± 3 ℃ of set temperature.
Temperature control means;
Spherical raw material powder is supplied along with the mixed gas.
And a raw material powder supply means .
造装置において、昇温時に空気流量調簡計と燃料ガス流
量調節計に適切な流量設定値を与えるダブル クロスリミ
ット制御手段と、セラミックスボールをガス燃焼熱で徐
々に昇温させ、高温流動化直前に流動床温度調節計のP
ID出力を強制的に減少させるダイレクト制御手段と、
空気と燃料ガスの混合ガス総量をあらかじめ高温流動化
用に設定された量に調整する可変空燃比制御手段と、流
動床温度調節計のPID設定を昇温時と変更する可変P
ID制御手段と、さらに高温流動時のダブルクロスリミ
ット制御手段を備え、前記混合ガスの引火点に満たない
セラミックスボールをガス燃焼熱で900℃以上まで昇
温し、設定温度±3℃以内の自動温度制御を行うように
したことを特徴とする微粒中空ガラス球状体の製造装
置。4. A method for producing a fine hollow glass sphere according to claim 3.
Air flow meter and fuel gas flow
Double cross limit that gives the flow controller an appropriate flow setting
And Tsu DOO control means, Xu ceramic balls in the gas combustion heat
The temperature of the fluidized bed temperature controller is increased immediately before fluidization at high temperature.
Direct control means for forcibly reducing ID output;
High-temperature fluidization of the total gas mixture of air and fuel gas in advance
Variable air-fuel ratio control means for adjusting to the amount set for
Variable P that changes the PID setting of the moving bed temperature controller to that when the temperature rises
ID control means and double cross limit at high temperature flow
Comprising a Tsu DOO control means, the ceramic balls is less than the flash point of the mixed gas was raised to above 900 ° C. In the gas combustion heat, so as to perform automatic temperature control within a set temperature ± 3 ° C.
An apparatus for producing a fine hollow glass sphere.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9185848A JP3028474B2 (en) | 1997-06-25 | 1997-06-25 | Method and apparatus for producing fine hollow glass spheres |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9185848A JP3028474B2 (en) | 1997-06-25 | 1997-06-25 | Method and apparatus for producing fine hollow glass spheres |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH1111960A JPH1111960A (en) | 1999-01-19 |
| JP3028474B2 true JP3028474B2 (en) | 2000-04-04 |
Family
ID=16177945
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9185848A Expired - Fee Related JP3028474B2 (en) | 1997-06-25 | 1997-06-25 | Method and apparatus for producing fine hollow glass spheres |
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| Country | Link |
|---|---|
| JP (1) | JP3028474B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004339028A (en) * | 2003-05-16 | 2004-12-02 | Rikogaku Shinkokai | Production method for fired body particle, and production plant for fired body particle |
| JP5145498B2 (en) * | 2008-09-08 | 2013-02-20 | 鹿児島県 | Manufacturing method of high strength, high sphericity shirasu balloon |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5122922B2 (en) | 2006-11-23 | 2013-01-16 | ハイデルベルガー ドルツクマシーネン アクチエンゲゼルシヤフト | Knife folder with a buckle folding unit in front and a method for folding a sheet of flat material |
| JP6365842B2 (en) | 2015-01-26 | 2018-08-01 | 株式会社荻原製作所 | Fluid conductivity and dielectric constant measuring device |
-
1997
- 1997-06-25 JP JP9185848A patent/JP3028474B2/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5122922B2 (en) | 2006-11-23 | 2013-01-16 | ハイデルベルガー ドルツクマシーネン アクチエンゲゼルシヤフト | Knife folder with a buckle folding unit in front and a method for folding a sheet of flat material |
| JP6365842B2 (en) | 2015-01-26 | 2018-08-01 | 株式会社荻原製作所 | Fluid conductivity and dielectric constant measuring device |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH1111960A (en) | 1999-01-19 |
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