JPH08157251A - Method for producing ceramics from waste and ceramics firing furnace - Google Patents

Method for producing ceramics from waste and ceramics firing furnace

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Publication number
JPH08157251A
JPH08157251A JP6297716A JP29771694A JPH08157251A JP H08157251 A JPH08157251 A JP H08157251A JP 6297716 A JP6297716 A JP 6297716A JP 29771694 A JP29771694 A JP 29771694A JP H08157251 A JPH08157251 A JP H08157251A
Authority
JP
Japan
Prior art keywords
furnace
heated
molded body
firing
waste
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.)
Granted
Application number
JP6297716A
Other languages
Japanese (ja)
Other versions
JP3231197B2 (en
Inventor
Setsuichi Kasai
節一 笠井
Seiichi Abe
清一 阿部
Masaharu Okada
正治 岡田
Satoru Shibanoki
悟 芝軒
Hiroshi Tajima
博 田島
Tetsuo Kiyota
哲夫 清田
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.)
Kubota Corp
Original Assignee
Kubota Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kubota Corp filed Critical Kubota Corp
Priority to JP29771694A priority Critical patent/JP3231197B2/en
Publication of JPH08157251A publication Critical patent/JPH08157251A/en
Application granted granted Critical
Publication of JP3231197B2 publication Critical patent/JP3231197B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Processing Of Solid Wastes (AREA)
  • Compositions Of Oxide Ceramics (AREA)

Abstract

(57)【要約】 【目的】 複合した材質をなす被加熱物であっても効率
良く安定して焼成することを目的とする。 【構成】 廃棄物溶融ガラスを原料成分として含有する
成形体8を形成し、被加熱物をなす前記成形体8を電気
炉6内に配置し、マイクロ波発振器3から成形体8にマ
イクロ波を照射し、マイクロ波加熱によって成形体8を
適当温度にまで昇温させ、その後に電気発熱体11によ
り成形体8を焼結温度にまで昇温させ、成形体31の成
分の焼結によりセラミックスを形成する。
(57) [Summary] [Purpose] The objective is to efficiently and stably bake even a material to be heated that is a composite material. A molded body 8 containing waste molten glass as a raw material component is formed, the molded body 8 serving as an object to be heated is placed in an electric furnace 6, and a microwave is applied from the microwave oscillator 3 to the molded body 8. Irradiation and microwave heating to raise the temperature of the molded body 8 to an appropriate temperature, and then the temperature of the molded body 8 to the sintering temperature by the electric heating element 11 to sinter the components of the molded body 31 to produce ceramics. Form.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、都市ごみ、下水汚泥、
産業廃棄物等の廃棄物を原料とするセラミックスの製造
方法およびセラミックス焼成炉に関する。
BACKGROUND OF THE INVENTION The present invention relates to municipal waste, sewage sludge,
The present invention relates to a method for producing ceramics made from wastes such as industrial wastes and a ceramics firing furnace.

【0002】[0002]

【従来の技術】近年、都市ごみ、下水汚泥、産業廃棄物
等の廃棄物の処分および再利用を目的とする種々の研究
が行われており、その一例として、特公平6−8767
7号公報に記載されているような、都市ごみ、下水汚泥
等の廃棄物を溶融処理してガラス化し、このガラスを原
料としてセラミックスを製造する方法がある。この方法
においては、原料成分として廃棄物溶融ガラスを含む成
形体を形成し、成形体を焼成炉内に配置して焼成するこ
とにより原料成分を焼結させている。
2. Description of the Related Art In recent years, various studies have been carried out for the purpose of disposal and reuse of waste such as municipal solid waste, sewage sludge, industrial waste, etc.
There is a method, as described in Japanese Patent Publication No. 7, in which waste such as municipal waste and sewage sludge is melt-treated to be vitrified, and ceramics are produced using this glass as a raw material. In this method, a formed body containing waste molten glass as a raw material component is formed, and the formed body is placed in a firing furnace and fired to sinter the raw material components.

【0003】[0003]

【発明が解決しようとする課題】上記した構成におい
て、成形体を焼成する場合には、成形体を徐々に昇温さ
せて800℃〜1100℃程度にまで加熱する必要があ
る。一方、従来の焼成炉における成形体に対する加熱は
外部から熱を加える、いわゆる外部加熱方式である。こ
の方式においては、被加熱物以外の物質から被加熱物で
ある成形体に熱が移動するので、必然的に熱伝達の時間
が必要となる。このため、成形体が大型化するに伴って
焼成に要する時間が長くなるとともに、エネルギーの消
費量が多くなる問題があった。
In the above-mentioned structure, when the molded body is fired, it is necessary to gradually raise the temperature of the molded body to about 800 ° C to 1100 ° C. On the other hand, the heating of the molded body in the conventional firing furnace is a so-called external heating method in which heat is applied from the outside. In this method, heat is transferred from a substance other than the object to be heated to the molded body which is the object to be heated, and thus a time for heat transfer is inevitably required. For this reason, there has been a problem that the time required for firing increases as the size of the molded body increases, and energy consumption increases.

【0004】成形体を加熱する他の加熱手段としては、
マイクロ波を利用するマイクロ波焼成炉がある。マイク
ロ波焼成炉は、従来の焼成炉に比べて熱効率が良く、熱
伝導の時間が不要であるために、プロセス時間を短くす
ることができる。
As another heating means for heating the molded body,
There is a microwave firing furnace that uses microwaves. The microwave firing furnace has higher thermal efficiency than the conventional firing furnace and does not require heat conduction time, so that the process time can be shortened.

【0005】しかし、マイクロ波焼成炉は、炉の形態
や、被加熱物の大きさ、形状、材質等により加熱状況が
異なる。一般的なセラミックスは異なる材質の複合体で
あり、用いる材質によりマイクロ波を良く吸収する物
や、吸収し難い物がある。また、安定した加熱を行って
も臨海温度以上において急激にマイクロ波を吸収し易く
なる物性を備えた材質があり、このような材質において
は温度が暴走的に上昇して溶融するものもある。このよ
うに、複合した材質を有する被加熱物から焼結体を安定
して得ることは非常に難しい。
However, the heating conditions of the microwave firing furnace differ depending on the form of the furnace, the size, shape, and material of the object to be heated. General ceramics are composites of different materials, and depending on the materials used, there are some that absorb microwaves well and those that do not. In addition, there are materials having physical properties that make it easy to absorb microwaves abruptly above the seaside temperature even when stable heating is performed, and some of these materials may melt due to a runaway increase in temperature. As described above, it is very difficult to stably obtain a sintered body from a heated object having a composite material.

【0006】本発明は上記課題を解決するもので、内部
加熱方式であるマイクロ波加熱手段と外部加熱方式の加
熱手段を併用することにより、複合した材質をなす被加
熱物であっても効率良く安定して焼成することができる
廃棄物を原料とするセラミックスの製造方法およびセラ
ミックス焼成炉を提供することを目的とする。
The present invention is to solve the above-mentioned problems, and by using the microwave heating means which is an internal heating method and the heating means which is an external heating method in combination, the object to be heated which is a composite material can be efficiently used. It is an object of the present invention to provide a method for producing ceramics from a waste material that can be stably fired and a ceramics firing furnace.

【0007】[0007]

【課題を解決するための手段】上記した課題を解決する
ために、本発明の廃棄物を原料とするセラミックスの製
造方法は、都市ごみ、下水汚泥、飛灰等の廃棄物を溶融
処理して後に冷却固化して廃棄物溶融ガラスを生成し、
前記廃棄物溶融ガラスを原料成分として含有する成形体
を形成し、被加熱物をなす前記成形体を焼成炉内に配置
し、マイクロ波加熱手段から成形体にマイクロ波を照射
し、マイクロ波加熱によって成形体を適当温度にまで昇
温させ、その後に外部加熱手段により成形体を焼結温度
にまで昇温させ、成形体の成分の焼結によりセラミック
スを形成するものである。
In order to solve the above-mentioned problems, the method for producing ceramics using waste as a raw material of the present invention is a method in which waste such as municipal waste, sewage sludge and fly ash is melt-treated. Later it solidifies by cooling to produce waste molten glass,
A molded body containing the waste molten glass as a raw material component is formed, and the molded body forming the object to be heated is placed in a firing furnace, and the molded body is irradiated with microwaves to perform microwave heating. The temperature of the molded body is raised to an appropriate temperature by means of, and then the molded body is heated to the sintering temperature by an external heating means to sinter the components of the molded body to form ceramics.

【0008】本発明のセラミックス焼成炉は、断熱壁で
囲んだ閉鎖空間が被加熱物を収納する炉室をなす炉体
と、炉室内の被加熱物に対してマイクロ波を照射するマ
イクロ波加熱手段と、炉室内に位置して被加熱物に熱を
加える外部加熱手段とを備えたものである。
The ceramics firing furnace of the present invention comprises a furnace body in which a closed space surrounded by a heat insulating wall constitutes a furnace chamber for containing an object to be heated, and microwave heating for irradiating microwaves to the object to be heated in the furnace chamber. And an external heating means located in the furnace chamber for applying heat to the object to be heated.

【0009】本発明のセラミックス焼成炉は、被加熱物
を収納する炉室内に炉入口から炉出口に向けて乾燥領域
と第1焼成領域と第2焼成領域とを連続して形成した炉
体と、炉室内において被加熱物を炉入口から炉出口に向
けて搬送する搬送手段と、乾燥領域において被加熱物に
対してマイクロ波を照射する乾燥用マイクロ波加熱手段
と、第1焼成領域において被加熱物に対してマイクロ波
を照射する焼成用マイクロ波加熱手段と、第2焼成領域
において被加熱物に熱を加える外部加熱手段とを備えた
ものである。
The ceramic firing furnace of the present invention has a furnace body in which a drying region, a first firing region and a second firing region are continuously formed from a furnace inlet to a furnace outlet in a furnace chamber for containing a material to be heated. A transport means for transporting the object to be heated from the furnace inlet to the furnace outlet in the furnace chamber, a microwave heating means for drying for irradiating the object to be heated with microwaves in the drying region, and a member to be heated in the first baking region. A heating microwave heating means for irradiating a heating object with microwaves and an external heating means for applying heat to the heating object in the second baking region are provided.

【0010】[0010]

【作用】上記した本発明の廃棄物を原料とするセラミッ
クスの製造方法によれば、始めに焼成炉内に配置した成
形体にマイクロ波を照射すると、成形体自体が発熱して
熱が成形体の内部側から外部側へと伝わり、他の物質か
ら被加熱物である成形体に熱が移動する場合に比べて、
成形体が急速に昇温し、溶融する少し前の適当温度にま
で短時間で達する。その後、成形体を外部加熱手段によ
って加熱すると、熱が成形体の外部側から内部側へと伝
わり、ゆっくりと最終温度にまで昇温して焼結される。
According to the above-described method for producing ceramics using the waste as a raw material of the present invention, when the molded body initially placed in the firing furnace is irradiated with microwaves, the molded body itself generates heat to generate heat. Compared to the case where heat is transferred from the inner side to the outer side and heat is transferred from other substances to the molded body that is the object to be heated
The temperature of the molded body rises rapidly and reaches a suitable temperature shortly before melting in a short time. After that, when the molded body is heated by the external heating means, heat is transferred from the outer side to the inner side of the molded body, and the temperature is slowly raised to the final temperature for sintering.

【0011】したがって、マイクロ波加熱手段と外部加
熱方式の加熱手段を併用することにより、廃棄物溶融ガ
ラスという成分の一定しない雑多な物質からなるものを
原料としながらも、容易に緻密なセラミックスを安定し
て短時間に形成することができる。
Therefore, by using the microwave heating means and the external heating type heating means together, it is possible to easily stabilize the dense ceramics while using the waste molten glass, which is a raw material made of various substances with inconsistent components. And can be formed in a short time.

【0012】本発明のセラミックス焼成炉によれば、マ
イクロ波加熱手段によって成形体を適当温度にまで急速
に加熱する前加熱処理と、外部加熱手段によって成形体
を焼結温度にまで緩速に加熱する後加熱処理とを組み合
わせて行うので、廃棄物溶融ガラスから緻密なセラミッ
クスを安定して短時間に形成することができる。
According to the ceramic firing furnace of the present invention, the preheating treatment for rapidly heating the compact to an appropriate temperature by the microwave heating means and the slow heating of the compact to the sintering temperature by the external heating means. Since it is performed in combination with the post-heating treatment, the dense ceramics can be stably formed from the waste molten glass in a short time.

【0013】本発明のセラミックス焼成炉によれば、成
形体は搬送手段によって炉室内を炉入口から炉出口に向
けて移動する。この間に、乾燥領域においては、マイク
ロ波加熱により成形体を低温度域に維持して成形体を乾
燥させる。第1焼成領域においては、マイクロ波加熱に
より成形体を溶融する少し前の適当温度にまで急速に加
熱して前加熱処理を行う。第2焼成領域においては、外
部加熱手段により成形体をゆっくりと最終温度にまで昇
温して焼結する。このため、廃棄物溶融ガラスから緻密
なセラミックスを連続して安定して短時間に形成するこ
とができる。
According to the ceramic firing furnace of the present invention, the molded body is moved in the furnace chamber from the furnace inlet to the furnace outlet by the conveying means. In the meantime, in the drying area, the formed body is dried by microwave heating while maintaining the formed body in the low temperature range. In the first firing region, the preheating treatment is performed by rapidly heating to a suitable temperature just before melting the molded body by microwave heating. In the second firing region, the molded body is slowly heated to the final temperature and sintered by the external heating means. Therefore, dense ceramics can be continuously and stably formed from the waste molten glass in a short time.

【0014】[0014]

【実施例】以下、本発明の一実施例を説明する。図1に
おいて、マイクロ波焼成炉1には導波管2を介してマイ
クロ波発振器3を接続するとともに、煙道4を介して排
気ファン5を接続している。マイクロ波焼成炉1の内部
には電気炉6を配置している。電気炉6の炉体7は断熱
材7aで形成されており、断熱材7aの内側面は必要に
応じて炭化ケイ素等のマイクロ波加熱に適した発熱体で
覆っても良い。炉体7は断熱材7aで囲んだ閉鎖空間が
被加熱物をなす成形体8を収納する炉室9を形成してお
り、炉室9内には外部の電源10に接続した複数の電気
発熱体11を設けている。成形体8は廃棄物溶融ガラス
を原料とするものである。
EXAMPLE An example of the present invention will be described below. In FIG. 1, a microwave oscillator 3 is connected to a microwave firing furnace 1 through a waveguide 2, and an exhaust fan 5 is connected through a flue 4. An electric furnace 6 is arranged inside the microwave baking furnace 1. The furnace body 7 of the electric furnace 6 is formed of a heat insulating material 7a, and the inner surface of the heat insulating material 7a may be covered with a heating element suitable for microwave heating such as silicon carbide if necessary. In the furnace body 7, a closed space surrounded by a heat insulating material 7a forms a furnace chamber 9 for accommodating a molded body 8 serving as an object to be heated. A body 11 is provided. The molded body 8 is made of waste molten glass as a raw material.

【0015】本実施例において、廃棄物溶融ガラスと
は、一般ごみである都市ごみ、下水汚泥、飛灰等の廃棄
物や、産業廃棄物である鉱山廃砕、河川の堆積物、建設
汚泥等の廃棄物を溶融処理して得られる溶融スラグを冷
却固化したものであり、適当粒度に粉砕して焼結材料に
形成したものである。
In the present embodiment, the waste molten glass means wastes such as municipal solid wastes, sewage sludge, fly ash, etc. which are general wastes, mine shredding, river sediments, construction sludges etc. which are industrial wastes. The molten slag obtained by melting the waste of 1. is cooled and solidified, and is formed into a sintered material by crushing to an appropriate particle size.

【0016】この廃棄物溶融ガラスの粉粒体に粘土やセ
メント等の成形材を加えて混合混練して坏土を成形し、
乾燥させて成形体8を形成する。この坏土における廃棄
物溶融ガラスと成形材との混合比は、目的とするセラミ
ックスの特性に応じて任意に設定することができ、成形
材を殆ど加えないものとすることも可能であり、坏土の
成分として成形発泡材、焼成発泡材、焼結材等を加える
ことも可能である。さらに、繊維状の補強材等を坏土の
成分として加えることも可能であり、上記の他にも種々
材質のものを組み合わせることができ、従来の窯業原料
は勿論のことに、未利用資源や産業廃棄物をスラグ化す
ることなくそのままを適当粒度に粉砕して使用すること
も可能であるし、精製原料、木材粉等の有機物、炭素等
を組み合わせることも可能である。
A molding material such as clay or cement is added to this waste molten glass powder and mixed and kneaded to form a kneaded clay,
The molded body 8 is formed by drying. The mixing ratio of the waste molten glass and the molding material in this kneaded clay can be arbitrarily set according to the characteristics of the target ceramics, and it is also possible to add almost no molding material. It is also possible to add a molded foam material, a fired foam material, a sintered material or the like as a component of the soil. Furthermore, it is also possible to add a fibrous reinforcing material or the like as a component of the kneaded clay, and various materials other than the above can be combined, so that not only conventional ceramic raw materials but also unused resources and It is possible to use the industrial waste as it is without slagging and crush it to an appropriate particle size, or to combine refined raw materials, organic substances such as wood powder, carbon and the like.

【0017】本実施例において成形体8は、都市ごみス
ラグ80%、粘土20%の混合物を200×200×2
00の立方体に形成したものである。以下、上記した構
成における作用を説明する。図2は焼成温度と焼成時間
の関係を示しており、図2に示すような温度勾配をもっ
て成形体8を焼成するものである。始めに、マイクロ波
発振器3において生起したマイクロ波を導波管2を通し
てマイクロ波焼成炉1に導き、電気炉6の炉室9内に配
置した成形体8にマイクロ波を照射する。このマイクロ
波加熱によって成形体8を適当温度(100℃)にまで
昇温させ、この温度で4時間程度の乾燥を行う。その後
に、マイクロ波加熱を強めて成形体8を、溶融する少し
前の適当温度(700℃)にまで加熱して予備焼成す
る。このとき、マイクロ波加熱によれば、成形体自体が
発熱して熱が成形体8の内部側から外部側へと伝わり、
他の物質から成形体8に熱が移動する場合に比べて、成
形体8が急速に短時間(30分程度)で昇温する。尚、
断熱材7aの内側面に発熱体を配置した場合には、マイ
クロ波の照射を受けて発熱体が発熱するので、その熱を
成形体8の加熱に利用することができる。
In the present embodiment, the molded body 8 is a mixture of 80% municipal waste slag and 20% clay of 200 × 200 × 2.
It is formed into a cube of 00. The operation of the above configuration will be described below. FIG. 2 shows the relationship between the firing temperature and the firing time, and the molded body 8 is fired with a temperature gradient as shown in FIG. First, the microwave generated in the microwave oscillator 3 is guided to the microwave firing furnace 1 through the waveguide 2, and the formed body 8 arranged in the furnace chamber 9 of the electric furnace 6 is irradiated with the microwave. By this microwave heating, the molded body 8 is heated to an appropriate temperature (100 ° C.) and dried at this temperature for about 4 hours. After that, the microwave heating is intensified to heat the molded body 8 to a suitable temperature (700 ° C.) just before melting, and pre-baking. At this time, according to the microwave heating, the molded body itself generates heat, and the heat is transmitted from the inner side to the outer side of the molded body 8,
Compared with the case where heat is transferred from another substance to the molded body 8, the molded body 8 rapidly rises in temperature in a short time (about 30 minutes). still,
When the heating element is arranged on the inner surface of the heat insulating material 7a, the heating element generates heat upon receiving the irradiation of microwaves, and thus the heat can be used for heating the molded body 8.

【0018】その後に、電気発熱体11から発する電気
抵抗熱により成形体8を焼結温度にまで昇温させて、成
形体8の成分の焼結によりセラミックスを形成する。こ
のとき、成形体8には熱が外部側から内部側へと伝わ
り、焼結温度(900℃)に達するまでゆっくり時間
(4時間)をかけて本焼成し、その後に均し焼成(1時
間)して焼結する。尚、電気炉6は必要に応じて予熱し
ている。
After that, the molded body 8 is heated to the sintering temperature by the electric resistance heat generated from the electric heating element 11, and the components of the molded body 8 are sintered to form ceramics. At this time, heat is transferred to the molded body 8 from the outer side to the inner side, and is slowly calcined for a long time (4 hours) until the sintering temperature (900 ° C.) is reached. ) And sinter. The electric furnace 6 is preheated as necessary.

【0019】したがって、マイクロ波による内部からの
加熱と、電気発熱体11による外部からの加熱を併用す
ることにより、廃棄物溶融ガラスという成分の一定しな
い雑多な物質からなるものを原料としながらも、容易に
緻密なセラミックスを安定して短時間に形成することが
できる。
Therefore, by using the heating from the inside by the microwaves and the heating from the outside by the electric heating element 11 in combination, the waste molten glass made of various substances whose components are not constant is used as a raw material, Dense ceramics can be easily and stably formed in a short time.

【0020】焼成に際しては、排気ファン5による排
気、または他の手段により炉内雰囲気を減圧状態もしく
は真空状態とすることにより、時間の短縮を図ることが
できる。図3は、炉内を減圧状態とした場合における焼
成温度と焼成時間の関係を示すものである。
At the time of firing, the time can be shortened by exhausting the exhaust fan 5 or by reducing the atmosphere in the furnace by other means. FIG. 3 shows the relationship between the firing temperature and the firing time when the pressure inside the furnace is reduced.

【0021】図4は本発明の他の実施例を示す連続焼成
炉の構成を示すものである。連続焼成炉21は、乾燥領
域をなすマイクロ波乾燥炉22と、第1焼成領域をなす
マイクロ波焼成炉23と、第2焼成領域をなすガス焼成
炉24からなり、連続した空間を形成している。マイク
ロ波乾燥炉22およびマイクロ波焼成炉23には導波管
25を介してマイクロ波発振器26を接続しており、マ
イクロ波焼成炉23には固定断熱材23aを配置してい
る。また、ガス焼成炉24にはガスバーナー27を設け
るとともに、煙道28を介して排気ファン29を接続し
ている。
FIG. 4 shows the structure of a continuous firing furnace showing another embodiment of the present invention. The continuous firing furnace 21 includes a microwave drying oven 22 that forms a drying area, a microwave firing furnace 23 that forms a first firing area, and a gas firing furnace 24 that forms a second firing area to form a continuous space. There is. A microwave oscillator 26 is connected to the microwave drying furnace 22 and the microwave baking furnace 23 via a waveguide 25, and a fixed heat insulating material 23 a is arranged in the microwave baking furnace 23. Further, a gas burner 27 is provided in the gas firing furnace 24, and an exhaust fan 29 is connected via a flue 28.

【0022】炉内には炉入口から炉出口に向けて複数の
台車30を配置しており、台車30は被加熱物である成
形体31を搬送する搬送手段をなし、断熱材32によっ
て形成した炉室33を有している。炉入口および炉出口
には電波吸収体扉34を二重に設けている。本実施例に
おける成形体31は、飛灰スラグ60%、粘土40%の
混合物を200×200×200の立方体に形成したも
のである。
A plurality of carriages 30 are arranged in the furnace from the furnace inlet to the furnace exit. The carriage 30 forms a conveying means for conveying the molded body 31, which is the object to be heated, and is formed by the heat insulating material 32. It has a furnace chamber 33. Double wave absorber doors 34 are provided at the furnace inlet and the furnace outlet. The molded body 31 in this example is a mixture of fly ash slag 60% and clay 40% formed into a cube of 200 × 200 × 200.

【0023】上記した構成における作用を説明する。図
5は焼成温度と焼成時間の関係を示しており、図5に示
すような温度勾配をもって成形体8を焼成するものであ
る。台車30の炉室33に成形体31を配置するととも
に、炉内に複数の台車30を順次に送り込み、成形体3
1を台車31によって炉入口から炉出口に向けて移動さ
せる。この間に、乾燥領域をなすマイクロ波乾燥炉22
においては、マイクロ波発振器26から発するマイクロ
波を成形体31に照射し、低温度域(100℃)に4時
間維持して成形体31を乾燥させる。第1焼成領域をな
すマイクロ波焼成炉23においては、マイクロ波加熱に
より成形体31を、溶融する少し前の適当温度(950
℃)にまで急速に加熱して予備焼成を行う。第2焼成領
域をなすガス焼成炉24においては、ガスバーナー27
により成形体31をゆっくり3時間かけて最終温度(1
050℃)にまで昇温して本焼成し、その後1時間の均
し焼成を行って成形体31の成分を焼結させる。このた
め、廃棄物溶融ガラスから緻密なセラミックスを連続し
て安定して短時間に形成することができる。
The operation of the above configuration will be described. FIG. 5 shows the relationship between the firing temperature and the firing time, and the molded body 8 is fired with a temperature gradient as shown in FIG. The molded body 31 is arranged in the furnace chamber 33 of the carriage 30 and a plurality of carriages 30 are sequentially fed into the furnace to form the molded body 3
1 is moved by the carriage 31 from the furnace inlet to the furnace outlet. In the meantime, the microwave drying furnace 22 forming a drying area
In the above, the compact 31 is irradiated with microwaves emitted from the microwave oscillator 26, and the compact 31 is dried by maintaining it in the low temperature range (100 ° C.) for 4 hours. In the microwave firing furnace 23 forming the first firing region, the molded body 31 is heated by microwaves at an appropriate temperature (950 ° C.) just before melting.
) Is rapidly heated to pre-baking. In the gas firing furnace 24 forming the second firing region, the gas burner 27
The molded body 31 is slowly heated to the final temperature (1
The temperature is increased to 050 ° C.) to perform the main firing, and then the average firing is performed for 1 hour to sinter the components of the molded body 31. Therefore, dense ceramics can be continuously and stably formed from the waste molten glass in a short time.

【0024】焼成に際しては、排気ファン29よる排
気、または他の手段により炉内雰囲気を減圧状態もしく
は真空状態とすることにより、時間の短縮を図ることが
できる。図6は、炉内を減圧状態とした場合における焼
成温度と焼成時間の関係を示すものである。
At the time of firing, the time can be shortened by setting the atmosphere in the furnace to a decompressed state or a vacuum state by exhausting with an exhaust fan 29 or other means. FIG. 6 shows the relationship between the firing temperature and the firing time when the pressure inside the furnace is reduced.

【0025】[0025]

【発明の効果】以上述べたように本発明によれば、マイ
クロ波加熱手段と外部加熱方式の加熱手段を併用するこ
とにより、廃棄物溶融ガラスという成分の一定しない雑
多な物質からなるものを原料としながらも、容易に緻密
なセラミックスを安定して短時間に形成することができ
る。
As described above, according to the present invention, by using the microwave heating means and the external heating type heating means in combination, the raw material is made of waste molten glass, which is a miscellaneous substance having a non-constant composition. However, the dense ceramics can be easily and stably formed in a short time.

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

【図1】本発明の一実施例におけるセラミックス焼成炉
の全体構成図である。
FIG. 1 is an overall configuration diagram of a ceramics firing furnace according to an embodiment of the present invention.

【図2】同実施例において炉内を常圧状態とした場合に
おける焼成温度と焼成時間の関係を示すグラフ図であ
る。
FIG. 2 is a graph showing a relationship between a firing temperature and a firing time when the inside of the furnace is in a normal pressure state in the example.

【図3】同実施例において炉内を減圧状態とした場合に
おける焼成温度と焼成時間の関係を示すグラフ図であ
る。
FIG. 3 is a graph showing the relationship between the firing temperature and the firing time when the pressure inside the furnace is reduced in the same example.

【図4】本発明の他の実施例における連続形式のセラミ
ックス焼成炉の全体構成図である。
FIG. 4 is an overall configuration diagram of a continuous type ceramics firing furnace according to another embodiment of the present invention.

【図5】同実施例において炉内を常圧状態とした場合に
おける焼成温度と焼成時間の関係を示すグラフ図であ
る。
FIG. 5 is a graph showing the relationship between the firing temperature and the firing time when the inside of the furnace is in a normal pressure state in the example.

【図6】同実施例において炉内を減圧状態とした場合に
おける焼成温度と焼成時間の関係を示すグラフ図であ
る。
FIG. 6 is a graph showing the relationship between the firing temperature and the firing time when the pressure inside the furnace is reduced in the same example.

【符号の説明】[Explanation of symbols]

1 マイクロ波焼成炉 3 マイクロ波発振器 6 電気炉 9 炉室 11 電気発熱体 1 Microwave firing furnace 3 Microwave oscillator 6 Electric furnace 9 Furnace chamber 11 Electric heating element

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C04B 35/64 B09B 3/00 303 H C04B 35/64 D (72)発明者 岡田 正治 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ内 (72)発明者 芝軒 悟 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ内 (72)発明者 田島 博 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ内 (72)発明者 清田 哲夫 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical indication C04B 35/64 B09B 3/00 303 H C04B 35/64 D (72) Inventor Masaharu Okada Osaka, Osaka Kubota Co., Ltd. 1-247 Shishitsu Higashi, Naniwa-ku, Japan (72) Inventor Satoru Shibaken 1-2-47 Shikitsu Higashi 1-Chome Shizutsu, Naniwa-ku, Osaka, Osaka (72) Inventor Hiroshi Tajima Kubota Co., Ltd. 1-47 Shikizu Higashi, Naniwa-ku, Osaka-shi, Osaka (72) Inventor Tetsuo Kiyota 1-2-47 Shikizu-Higashi, Naniwa-ku, Osaka-shi, Osaka

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 都市ごみ、下水汚泥、飛灰等の廃棄物を
溶融処理して後に冷却固化して廃棄物溶融ガラスを生成
し、前記廃棄物溶融ガラスを原料成分として含有する成
形体を形成し、被加熱物をなす前記成形体を焼成炉内に
配置し、マイクロ波加熱手段から成形体にマイクロ波を
照射し、マイクロ波加熱によって成形体を適当温度にま
で昇温させ、その後に外部加熱手段により成形体を焼結
温度にまで昇温させ、成形体の成分の焼結によりセラミ
ックスを形成することを特徴とする廃棄物を原料とする
セラミックスの製造方法。
1. A waste material such as municipal waste, sewage sludge, fly ash, etc. is melted and then cooled and solidified to produce a waste molten glass, and a molded body containing the waste molten glass as a raw material component is formed. Then, the molded body that constitutes the object to be heated is placed in a firing furnace, the molded body is irradiated with microwaves from the microwave heating means, the molded body is heated to an appropriate temperature by microwave heating, and then externally heated. A method for producing ceramics using waste as a raw material, which comprises heating the molded body to a sintering temperature by a heating means and sintering the components of the molded body to form ceramics.
【請求項2】 断熱壁で囲んだ閉鎖空間が被加熱物を収
納する炉室をなす炉体と、炉室内の被加熱物に対してマ
イクロ波を照射するマイクロ波加熱手段と、炉室内に位
置して被加熱物に熱を加える外部加熱手段とを備えたこ
とを特徴とするセラミックス焼成炉。
2. A furnace body in which a closed space surrounded by a heat insulating wall constitutes a furnace chamber for containing an object to be heated, microwave heating means for irradiating the object to be heated with microwaves, and a furnace chamber. A ceramics firing furnace, which is provided with an external heating means which is located and applies heat to an object to be heated.
【請求項3】 被加熱物を収納する炉室内に炉入口から
炉出口に向けて乾燥領域と第1焼成領域と第2焼成領域
とを連続して形成した炉体と、炉室内において被加熱物
を炉入口から炉出口に向けて搬送する搬送手段と、乾燥
領域において被加熱物に対してマイクロ波を照射する乾
燥用マイクロ波加熱手段と、第1焼成領域において被加
熱物に対してマイクロ波を照射する焼成用マイクロ波加
熱手段と、第2焼成領域において被加熱物に熱を加える
外部加熱手段とを備えたことを特徴とするセラミックス
焼成炉。
3. A furnace body in which a drying region, a first baking region and a second baking region are continuously formed from a furnace inlet to a furnace outlet in a furnace chamber for containing an object to be heated, and a furnace chamber to be heated. Conveying means for conveying the object from the furnace inlet to the furnace outlet, microwave heating means for irradiating the object to be heated with microwaves in the drying area, and microwave for the object to be heated in the first baking area. A ceramic firing furnace, comprising: a microwave heating means for irradiating a wave; and an external heating means for applying heat to an object to be heated in the second firing area.
JP29771694A 1994-12-01 1994-12-01 Method for producing ceramics from waste and ceramic firing furnace Expired - Fee Related JP3231197B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29771694A JP3231197B2 (en) 1994-12-01 1994-12-01 Method for producing ceramics from waste and ceramic firing furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29771694A JP3231197B2 (en) 1994-12-01 1994-12-01 Method for producing ceramics from waste and ceramic firing furnace

Publications (2)

Publication Number Publication Date
JPH08157251A true JPH08157251A (en) 1996-06-18
JP3231197B2 JP3231197B2 (en) 2001-11-19

Family

ID=17850251

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29771694A Expired - Fee Related JP3231197B2 (en) 1994-12-01 1994-12-01 Method for producing ceramics from waste and ceramic firing furnace

Country Status (1)

Country Link
JP (1) JP3231197B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020066460A (en) * 2001-02-10 2002-08-17 허창린 The block with a through hole using scraped ceramics and manufacturing method therof
JP2012081426A (en) * 2010-10-13 2012-04-26 Chugoku Electric Power Co Inc:The Wastewater sludge drying apparatus
CN104197700A (en) * 2014-09-19 2014-12-10 重庆科技学院 Stepping complete-shield thermal shock sintering resistance furnace

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4375441A (en) 1980-12-18 1983-03-01 The Standard Oil Company Method for producing sintered porous polymeric articles

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020066460A (en) * 2001-02-10 2002-08-17 허창린 The block with a through hole using scraped ceramics and manufacturing method therof
JP2012081426A (en) * 2010-10-13 2012-04-26 Chugoku Electric Power Co Inc:The Wastewater sludge drying apparatus
CN104197700A (en) * 2014-09-19 2014-12-10 重庆科技学院 Stepping complete-shield thermal shock sintering resistance furnace

Also Published As

Publication number Publication date
JP3231197B2 (en) 2001-11-19

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