JP2978425B2 - Stirring method, stirrer and furnace in furnace - Google Patents

Stirring method, stirrer and furnace in furnace

Info

Publication number
JP2978425B2
JP2978425B2 JP7209560A JP20956095A JP2978425B2 JP 2978425 B2 JP2978425 B2 JP 2978425B2 JP 7209560 A JP7209560 A JP 7209560A JP 20956095 A JP20956095 A JP 20956095A JP 2978425 B2 JP2978425 B2 JP 2978425B2
Authority
JP
Japan
Prior art keywords
furnace
gas
stirrer
regenerator
stirring
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
Application number
JP7209560A
Other languages
Japanese (ja)
Other versions
JPH0953886A (en
Inventor
弘治 小椋
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.)
NIPPON GAISHI KK
Original Assignee
NIPPON GAISHI 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 NIPPON GAISHI KK filed Critical NIPPON GAISHI KK
Priority to JP7209560A priority Critical patent/JP2978425B2/en
Publication of JPH0953886A publication Critical patent/JPH0953886A/en
Application granted granted Critical
Publication of JP2978425B2 publication Critical patent/JP2978425B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Landscapes

  • Air Supply (AREA)
  • Tunnel Furnaces (AREA)

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、セラミック製品、
窯業製品の焼成等の技術分野で使用される炉内の攪拌方
法、攪拌装置およびこれを利用した炉に関するものであ
る。
The present invention relates to a ceramic product,
The present invention relates to a stirring method and a stirring device in a furnace used in a technical field such as firing of ceramic products, and a furnace using the same.

【0002】[0002]

【従来の技術】セラミック製品、窯業製品の焼成等に使
用される炉は、炉内の温度分布を均一化するために炉内
を攪拌することが好ましい。このため従来から図6に示
されるように、炉体1の天井に攪拌ファン2を設置し、
炉内を攪拌する方法が取られていた。ところがこの攪拌
ファン2を金属製とした場合には700 ℃〜900 ℃が使用
限界であり、中〜高温度域での使用は不可能である。ま
た攪拌ファン2をセラミック製とすると使用できる温度
域は拡がるものの高価となりしかも信頼性が不十分とな
る。さらに炉体1が大型となるとこの方法では十分に攪
拌することができなくなる。
2. Description of the Related Art In a furnace used for firing ceramic products and ceramic products, it is preferable to stir the inside of the furnace in order to make the temperature distribution in the furnace uniform. Therefore, as shown in FIG. 6, a stirring fan 2 is conventionally installed on the ceiling of the furnace body 1,
A method of stirring the inside of the furnace was used. However, when the stirring fan 2 is made of metal, its use limit is 700 ° C. to 900 ° C., and it cannot be used in a medium to high temperature range. Further, if the stirring fan 2 is made of ceramic, the temperature range in which it can be used is widened, but it is expensive and the reliability is insufficient. Further, when the furnace body 1 becomes large, it is not possible to sufficiently stir with this method.

【0003】また図7に示したように、炉体1の上下に
互い違いにバーナー3を設けておき、バーナーフレーム
により炉内を攪拌することも行なわれている。ところが
この方法では、攪拌を十分に行なわせようとすると炉内
のガス量が増加するとともに、炉内温度が上昇すること
となる。そして温度上昇を抑えるために過剰空気をバー
ナー3に供給すると更にガス量が増加し、排ガス処理設
備等の負担が増大することとなる。
As shown in FIG. 7, burners 3 are alternately provided above and below a furnace body 1, and the inside of the furnace is agitated by a burner frame. However, in this method, when sufficient stirring is performed, the amount of gas in the furnace increases and the temperature in the furnace increases. If excess air is supplied to the burner 3 in order to suppress a rise in temperature, the amount of gas further increases, and the burden on exhaust gas treatment equipment and the like increases.

【0004】[0004]

【発明が解決しようとする課題】本発明は上記した従来
の問題点を解決し、炉内のガス量の増加を招くことなく
炉内を均一に攪拌することができ、しかも中〜高温度域
でも使用することができる炉内の攪拌方法、攪拌装置お
よびこれを利用した炉を提供するためになされたもので
ある。
SUMMARY OF THE INVENTION The present invention solves the above-mentioned conventional problems and can uniformly stir the inside of the furnace without increasing the amount of gas in the furnace. The present invention has been made in order to provide a stirring method and a stirring apparatus in a furnace which can be used, and a furnace using the same.

【0005】[0005]

【課題を解決するための手段】上記の課題を解決するた
めになされた本発明の炉内の攪拌方法は、炉内のガスを
炉体に接続される一方の出入口から蓄熱器を介して吸引
したうえこの蓄熱器と対をなす蓄熱器を介して他方の出
入口から再び炉内へ吹き込む工程を、ガスの循環方向を
反転させつつ繰り返すことを特徴とするものである。ま
た本発明の炉内の攪拌装置は、炉内のガスを炉体に接続
される一方の出入口から吸引したうえ他方の出入口から
再び炉内へ吹き込むガス循環経路に、循環ファンと、ガ
スの循環方向を反転させる切替弁とを設けるとともに、
このガス循環経路の前記出入口の部分に一対の蓄熱器を
設けたことを特徴とするものである。更に本発明の炉
は、上記の炉内の攪拌装置を中温度域に配置したことを
特徴とするものである。
According to the present invention, there is provided a method for stirring a gas in a furnace, comprising the steps of:
Through the heat accumulator forming the regenerator paired after having sucked through the regenerator from one entrance to be connected to the furnace body out of the other
The step of blowing the gas into the furnace again from the inlet is repeated while reversing the gas circulation direction. Further, the stirrer in the furnace of the present invention connects the gas in the furnace to the furnace body.
A gas circulation path that is sucked from one of the entrances and then blown back into the furnace from the other entrance and exit is provided with a circulation fan and a switching valve for reversing the gas circulation direction,
It is characterized in that a pair of regenerators in a portion of the entrance of the gas circulation path. Further, the furnace according to the present invention is characterized in that the above-described stirring device in the furnace is arranged in a medium temperature range.

【0006】[0006]

【発明の実施の形態】以下にこれらの発明の実施の形態
を、図面を参照しつつ更に詳細に説明する。図1は本発
明の基本的な実施の形態を示すもので、1は炉体、4は
炉内のガスを吸引したうえ再び炉内へ吹き込むガス循環
経路である。このガス循環経路4は循環ファン5と切替
弁6とを備え、炉体1に接続される出入口の部分にセラ
ミックス等の耐熱材料よりなる一対の蓄熱器7、8を備
えている。
Embodiments of the present invention will be described below in more detail with reference to the drawings. FIG. 1 shows a basic embodiment of the present invention, in which 1 is a furnace body, and 4 is a gas circulation path which sucks gas in the furnace and blows the gas into the furnace again. The gas circulation path 4 includes a circulation fan 5 and a switching valve 6, and a pair of heat accumulators 7 and 8 made of a heat-resistant material such as ceramics at an entrance and exit connected to the furnace body 1.

【0007】この切替弁6は例えば30秒程度の短い周期
で切り替えられ、ガスの循環方向を反転させる機能を有
するもので、図1の状態では高温の炉内のガスが炉体1
に接続される一方の出入口から蓄熱器8を介して循環フ
ァン5に吸引され、他方の出入口から蓄熱器7を介して
再び炉内へ吹き込まれる。この間に蓄熱器8は高温に加
熱される。次にガスの循環方向が反転されると、蓄熱器
7を介して吸引された循環ガスが蓄熱器8によって加熱
されたうえで反対側の出入り口から炉内へ吹き込まれ
る。
[0007] The switching valve 6 is switched at a period shorter e.g. of about 30 seconds, and has a function of inverting the direction of circulation of the gas, gas furnace body 1 in high temperatures in the furnace in the state of FIG. 1
From one entrance to be connected is sucked into the circulation fan 5 through the regenerator 8 to be blown again into the furnace through the regenerator 7 from the other entrance. During this time, the regenerator 8 is heated to a high temperature. Next, when the circulation direction of the gas is reversed, the circulating gas sucked through the regenerator 7 is heated by the regenerator 8 and then blown into the furnace from the opposite entrance .

【0008】このように、本発明の炉内の攪拌方法及び
装置によれば、炉内から吸引した炉内ガスを循環方向を
反転させつつそのまま炉内へ吹き込むことにより炉内の
攪拌を行なうことができるので、炉内ガス量を増加させ
ることなく均一攪拌が可能となる。また高温の炉内ガス
は蓄熱器7、8により降温されたうえでガス循環経路4
に入り、再び昇温されて炉内に戻るので、熱損失が少な
いうえ、蓄熱器7、8をガス循環経路4の出入口の部分
に設けたことにより、循環ファン5や切替弁6等を流れ
るガス温度を炉内温度(例えば1200℃) よりもはるかに
低温(例えば300 ℃) に保つことができ、これらの材質
を金属製とすることができる。
As described above, according to the method and apparatus for stirring the inside of the furnace of the present invention, the furnace gas sucked from the furnace is circulated in the direction of circulation.
Since it is possible to stir the inside of the furnace by directly blowing it into the furnace while inverting it, uniform stirring can be performed without increasing the amount of gas in the furnace. The high-temperature gas in the furnace is cooled by the heat accumulators 7 and 8 and then cooled by the gas circulation path 4.
And the temperature rises again and returns to the inside of the furnace, so that the heat loss is small and the regenerators 7 and 8 are provided at the entrance and exit of the gas circulation path 4 to flow through the circulation fan 5 and the switching valve 6. The gas temperature can be kept much lower (for example, 300 ° C.) than the furnace temperature (for example, 1200 ° C.), and these materials can be made of metal.

【0009】図2は図1におけるロータリー式の単一の
切替弁6を、4個の弁からなる切替弁6に置換したもの
である。しかしその機能は図1について説明したと同様
である。
FIG. 2 is a diagram in which the single rotary type switching valve 6 in FIG. 1 is replaced with a switching valve 6 composed of four valves. However, its function is the same as that described with reference to FIG.

【0010】図3と図4は図1、図2におけるガス循環
経路4の蓄熱器7、8よりも炉外側の部分に、ガスの加
熱手段9を設けたものである。加熱手段9としてはバー
ナーのような直接加熱手段であっても、熱交換器のよう
な間接加熱手段であってもよい。このようなガスの加熱
手段9は、炉外のガス循環経路4が長く放熱量が大きい
ような場合に、循環ガスの温度低下を防止する機能を発
揮する。しかもこの加熱手段9は蓄熱器7、8よりも炉
外側の低温側の部分に設けられているため、特別な耐熱
性を要求されない利点がある。加熱手段9は実線で示す
ように1個であっても、鎖線で示すように2個以上とし
てもよい。なお、炉内を冷却したい場合には、加熱手段
9の代わりに冷却手段を設けることもできる。このよう
な加熱手段9や冷却手段を設けることによって、炉内を
攪拌しつつ炉内温度を制御することが可能となる。
FIGS. 3 and 4 show a gas circulating passage 4 in FIGS. 1 and 2 in which a gas heating means 9 is provided at a portion outside the regenerators 7 and 8 relative to the furnace. The heating means 9 may be a direct heating means such as a burner or an indirect heating means such as a heat exchanger. Such a gas heating means 9 has a function of preventing the temperature of the circulating gas from decreasing when the gas circulation path 4 outside the furnace is long and the amount of heat radiation is large. Moreover, since the heating means 9 is provided at a lower temperature side of the furnace than the regenerators 7 and 8, there is an advantage that special heat resistance is not required. The number of the heating means 9 may be one as shown by a solid line, or two or more as shown by a chain line. When the inside of the furnace is to be cooled, a cooling means can be provided instead of the heating means 9. By providing such heating means 9 and cooling means, it is possible to control the temperature inside the furnace while stirring the inside of the furnace.

【0011】図5は、上記したような炉内の攪拌装置を
中温度域に配置した炉を示している。この炉は右側から
順に予熱、焼成、冷却を行なうセラミック製品のトンネ
ル炉であり、予熱の最初の低温度域Aには単にファン10
により炉内ガスを吸引して反対側から炉内に噴出する攪
拌装置11が設けられている。しかしこの攪拌装置11は炉
内温度が700 ℃以上に上昇する中温度域ではファン10の
耐熱性の問題があるため、中温度域には本発明の蓄熱器
7、8を備えた攪拌装置が配置されている。なお、焼成
が行なわれる高温度域は多数のバーナー12による炉内攪
拌が採用されている。
FIG. 5 shows a furnace in which the above-described stirrer in the furnace is arranged in a medium temperature range. This furnace is a ceramic furnace for preheating, firing and cooling in order from the right side.
A stirrer 11 is provided for sucking the gas inside the furnace and ejecting it into the furnace from the opposite side. However, this stirrer 11 has a problem of heat resistance of the fan 10 in the middle temperature range where the temperature in the furnace rises to 700 ° C. or more. Therefore, the stirrer provided with the heat storage units 7 and 8 of the present invention is used in the middle temperature range. Are located. Note that in a high temperature range in which firing is performed, stirring in a furnace by a large number of burners 12 is employed.

【0012】このように構成された炉は、中温度域にお
ける炉内の攪拌を十分に行えるので、図5に右上がりの
ハッチングで示した良好な温度分布の焼成が行える。し
かし従来技術では中温度域における炉内の攪拌が不十分
となり勝ちであったため、図5に左上がりのハッチング
で示したように、良好な温度分布は得られなかった。こ
のため、本発明の炉によれば従来よりも均一な焼成が可
能となり、焼成品質の向上を図ることが可能となる。図
5では予熱側に本発明の蓄熱器7、8を備えた攪拌装置
を配置したが、製品によっては冷却側に本発明の攪拌装
置を配置することもでき、また高温度域に本発明の攪拌
装置を配置してもよいことはいうまでもない。
In the furnace configured as described above, the inside of the furnace can be sufficiently agitated in the middle temperature range, so that the firing with a favorable temperature distribution shown by hatching in FIG. 5 can be performed. However, in the prior art, the stirring in the furnace in the middle temperature range was insufficient and the system was won, so that a favorable temperature distribution could not be obtained as shown by the hatching in FIG. For this reason, according to the furnace of the present invention, it is possible to perform more uniform firing than before, and it is possible to improve the firing quality. In FIG. 5, the stirrer provided with the regenerators 7 and 8 of the present invention is arranged on the preheating side, but the stirrer of the present invention can be arranged on the cooling side depending on the product, and the stirrer of the present invention can be arranged in a high temperature region. It goes without saying that a stirring device may be provided.

【0013】[0013]

【発明の効果】以上に説明したように、本発明によれば
炉内のガス量の増加を招くことなく炉内を均一に攪拌す
ることができ、しかも中温度域〜高温度域の攪拌をも行
なうことができる利点がある。よって本発明は特に中温
度域や高温度域における焼成温度カーブを厳密に守る必
要のあるセラミック製品、窯業製品の焼成の技術分野に
おいて、価値の高いものである。
As described above, according to the present invention, the inside of the furnace can be uniformly stirred without increasing the gas amount in the furnace, and the stirring in the medium temperature range to the high temperature range can be performed. There is also an advantage that can be performed. Therefore, the present invention is particularly valuable in the technical field of firing ceramic products and ceramic products, which need to strictly observe the firing temperature curve in a middle temperature range or a high temperature range.

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

【図1】本発明の基本的な実施の形態を示す断面図であ
る。
FIG. 1 is a sectional view showing a basic embodiment of the present invention.

【図2】本発明の他の実施の形態を示す断面図である。FIG. 2 is a cross-sectional view showing another embodiment of the present invention.

【図3】本発明の他の実施の形態を示す断面図である。FIG. 3 is a cross-sectional view showing another embodiment of the present invention.

【図4】本発明の他の実施の形態を示す断面図である。FIG. 4 is a cross-sectional view showing another embodiment of the present invention.

【図5】請求項4の発明の実施の形態を示す平面図であ
る。
FIG. 5 is a plan view showing an embodiment of the invention of claim 4;

【図6】従来例を示す断面図である。FIG. 6 is a sectional view showing a conventional example.

【図7】他の従来例を示す断面図である。FIG. 7 is a sectional view showing another conventional example.

【符号の説明】 1 炉体、2 攪拌ファン、3 バー
ナー、4 ガス循環経路、5 循環ファン、6 切替
弁、7 蓄熱器、8 蓄熱器、9 加熱手段、10ファ
ン、11 攪拌装置、12 バーナー
[Description of Signs] 1 furnace body, 2 stirring fan, 3 burner, 4 gas circulation path, 5 circulation fan, 6 switching valve, 7 heat storage device, 8 heat storage device, 9 heating means, 10 fan, 11 stirring device, 12 burner

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 炉内のガスを炉体に接続される一方の出
入口から蓄熱器を介して吸引したうえこの蓄熱器と対を
なす蓄熱器を介して他方の出入口から再び炉内へ吹き込
む工程を、ガスの循環方向を反転させつつ繰り返すこと
を特徴とする炉内の攪拌方法。
The gas in the furnace is connected to one of the outlets connected to the furnace body.
A process in which the process of sucking the gas from the inlet through the regenerator and blowing it into the furnace again from the other port through the regenerator paired with the regenerator is repeated while reversing the gas circulation direction. Stirring method.
【請求項2】 炉内のガスを炉体に接続される一方の出
入口から吸引したうえ他方の出入口から再び炉内へ吹き
込むガス循環経路に、循環ファンと、ガスの循環方向を
反転させる切替弁とを設けるとともに、このガス循環経
路の前記出入口の部分に一対の蓄熱器を設けたことを特
徴とする炉内の攪拌装置。
2. The gas in the furnace is connected to one of the outlets connected to the furnace body.
A gas circulation path blown from the other entrance after having sucked from the inlet to again furnace, circulation fan and, provided with a switching valve for reversing the direction of circulation of the gas, a pair of heat storage in the portion of the entrance of the gas circulation path A stirrer in a furnace, provided with a vessel.
【請求項3】 ガス循環経路の蓄熱器よりも炉外側の部
分に、ガスの加熱または冷却手段を設けた請求項2記載
の炉内の攪拌装置。
3. The stirrer in a furnace according to claim 2, wherein a gas heating or cooling means is provided in a portion of the gas circulation path outside the furnace with respect to the regenerator.
【請求項4】 中温度域に、請求項2または請求項3記
載の炉内の攪拌装置を配置したことを特徴とする炉。
4. A furnace, wherein the stirrer in the furnace according to claim 2 or 3 is arranged in a medium temperature range.
JP7209560A 1995-08-17 1995-08-17 Stirring method, stirrer and furnace in furnace Expired - Fee Related JP2978425B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7209560A JP2978425B2 (en) 1995-08-17 1995-08-17 Stirring method, stirrer and furnace in furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7209560A JP2978425B2 (en) 1995-08-17 1995-08-17 Stirring method, stirrer and furnace in furnace

Publications (2)

Publication Number Publication Date
JPH0953886A JPH0953886A (en) 1997-02-25
JP2978425B2 true JP2978425B2 (en) 1999-11-15

Family

ID=16574855

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7209560A Expired - Fee Related JP2978425B2 (en) 1995-08-17 1995-08-17 Stirring method, stirrer and furnace in furnace

Country Status (1)

Country Link
JP (1) JP2978425B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107014212B (en) * 2017-04-19 2019-03-15 项玮 Heat storage type combustion and furnace gas forced circulation industrial furnace

Also Published As

Publication number Publication date
JPH0953886A (en) 1997-02-25

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