JP3231197B2 - Method for producing ceramics from waste and ceramic firing furnace - Google Patents

Method for producing ceramics from waste and ceramic firing furnace

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Publication number
JP3231197B2
JP3231197B2 JP29771694A JP29771694A JP3231197B2 JP 3231197 B2 JP3231197 B2 JP 3231197B2 JP 29771694 A JP29771694 A JP 29771694A JP 29771694 A JP29771694 A JP 29771694A JP 3231197 B2 JP3231197 B2 JP 3231197B2
Authority
JP
Japan
Prior art keywords
temperature
furnace
molded body
heating means
heated
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
JP29771694A
Other languages
Japanese (ja)
Other versions
JPH08157251A (en
Inventor
節一 笠井
清一 阿部
正治 岡田
悟 芝軒
博 田島
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
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Publication of JPH08157251A publication Critical patent/JPH08157251A/en
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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)

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。
The present invention relates to municipal solid waste, sewage sludge,
The present invention relates to a method for producing ceramics from wastes such as industrial wastes and a ceramic 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 researches have been conducted for the purpose of disposing and reusing waste such as municipal solid waste, sewage sludge, industrial waste, and the like.
As described in Japanese Patent Publication No. 7, there is a method in which waste such as municipal waste and sewage sludge is melted and vitrified, and a ceramic is produced using the 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 component.

【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 structure, when firing a molded body, 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 compact 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, so that a time for heat transfer is inevitably required. For this reason, there has been a problem that the time required for sintering increases as the size of the compact increases, and the amount of 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。
[0004] Other heating means for heating the compact include:
There is a microwave firing furnace using microwaves. The microwave firing furnace has better thermal efficiency than conventional firing furnaces 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。
[0005] However, the heating condition of the microwave firing furnace differs depending on the shape of the furnace and the size, shape, material and the like of the object to be heated. General ceramics are composites of different materials, and there are materials that absorb microwaves well and materials that hardly absorb microwaves depending on the materials used. Further, there is a material having a property of easily absorbing microwaves at a temperature equal to or higher than the critical temperature even when stable heating is performed. Among such materials, there is a material whose temperature rises runaway and melts. 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 solves the above-mentioned problems. By using a microwave heating means which is an internal heating method and a heating means of an external heating method together, an object to be heated made of 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 ceramic 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30分で600℃
の温度上昇をなす温度勾配で成形体が溶融する直前の適
当温度にまで急速に昇温させ、その後に外部加熱手段に
より成形体を4時間で200℃の温度上昇をなす温度勾
配で焼結温度まで緩速に昇温させるか、あるいは、マイ
クロ波加熱によって成形体を15分で600℃の温度上
昇をなす温度勾配で成形体が溶融する直前の適当温度に
まで急速に昇温させ、その後に外部加熱手段により成形
体を3時間で200℃の温度上昇をなす温度勾配で焼結
温度まで緩速に昇温させるか、あるいは、マイクロ波加
熱によって成形体を45分で850℃の温度上昇をなす
温度勾配で成形体が溶融する直前の適当温度にまで急速
に昇温させ、その後に外部加熱手段により成形体を4時
間で100℃の温度上昇をなす温度勾配で焼結温度まで
緩速に昇温させるか、あるいは、マイクロ波加熱によっ
て成形体を30分で850℃の温度上昇をなす温度勾配
で成形体が溶融する直前の適当温度にまで急速に昇温さ
せ、その後に外部加熱手段により成形体を2時間で10
0℃の温度上昇をなす温度勾配で焼結温度まで緩速に昇
温させて成形体の成分を緻密に焼結してセラミックスを
形成するものである。
SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, a method for producing ceramics using waste as a raw material according to the present invention comprises melting and processing waste such as municipal waste, sewage sludge, and fly ash. After cooling and solidifying to produce waste molten glass,
A molded body containing the waste molten glass as a raw material component is formed, the molded body forming an object to be heated is arranged in a firing furnace, and the molded body is irradiated with microwaves from a microwave heating means, thereby being heated by microwave. 600 ° C in 30 minutes
Just before the compact melts due to the temperature gradient
The temperature is rapidly raised to this temperature, and then the external heating
The temperature of the molded product increases by 200 ° C in 4 hours.
Slowly raise the temperature to the sintering temperature
The molded body is heated to 600 ° C in 15 minutes by microwave heating.
The temperature gradient rises to an appropriate temperature just before the compact melts.
Temperature and then molded by external heating means
The body is sintered with a temperature gradient of 200 ° C in 3 hours
Either slowly raise the temperature to
A temperature rise of 850 ° C in 45 minutes by heat.
Rapidly rises to the appropriate temperature just before the molded body melts due to temperature gradient
And then heat the molded body at 4:00
Up to the sintering temperature with a temperature gradient of 100 ° C
Either increase the temperature slowly or use microwave heating.
Temperature gradient of 850 ° C in 30 minutes
The temperature rises quickly to the appropriate temperature just before the
After that, the molded body is heated by an external heating means for 10 hours in 2 hours.
Slowly rise to sintering temperature with a temperature gradient of 0 ° C
The ceramics are formed by sintering the components of the compact
To form .

【0008】本発明のセラミックス焼成炉は、廃棄物溶
融ガラスを原料成分として含有する成形体を被加熱物と
し、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
照射して成形体を急速に昇温させ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て緩速に加熱
する外部加熱手段とを備え、マイクロ波加熱手段による
昇温が30分で600℃の温度上昇をなす温度勾配で、
外部加熱手段による昇温が4時間で200℃の温度上昇
をなす温度勾配であるか、あるいはマイクロ波加熱手段
による昇温が15分で600℃の温度上昇をなす温度勾
配で、外部加熱手段による昇温が3時間で200℃の温
度上昇をなす温度勾配であるものである。
A ceramic firing furnace according to the present invention is characterized in that a molded body containing waste molten glass as a raw material component is an object to be heated, and a closed space surrounded by a heat insulating wall forms a furnace chamber for storing the object to be heated. A microwave heating means for irradiating microwaves to the object to be heated in the furnace chamber to rapidly raise the temperature of the compact, and an external means for heating the object to be heated in the furnace chamber and applying heat to the object slowly. Heating means, and microwave heating means
With a temperature gradient in which the temperature rises to 600 ° C in 30 minutes,
Temperature rise by external heating means 200 ° C in 4 hours
Temperature gradient or microwave heating means
Temperature rise of 600 ° C in 15 minutes
The temperature is raised to 200 ° C in 3 hours by the external heating means.
This is a temperature gradient that increases in degree .

【0009】本発明のセラミックス焼成炉は、廃棄物溶
融ガラスを原料成分として含有する成形体を被加熱物と
し、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して成形体を急速に昇温させる焼成
用マイクロ波加熱手段と、第2焼成領域において被加熱
物に熱を加えて緩速に加熱する外部加熱手段とを備え、
焼成用マイクロ波加熱手段による昇温が45分で850
℃の温度上昇をなす温度勾配で、外部加熱手段による昇
温が4時間で100℃の温度上昇をなす温度勾配である
か、あるいは焼成用マイクロ波加熱手段による昇温が3
0分で850℃の温度上昇をなす温度勾配で、外部加熱
手段による昇温が2時間で100℃の温度上昇をなす温
度勾配であるものである。
In the ceramic firing furnace of the present invention, a formed body containing waste molten glass as a raw material component is used as an object to be heated, and a drying zone is formed in a furnace chamber for storing the object to be heated from a furnace inlet to a furnace outlet. A furnace body in which a first baking region and a second baking region are continuously formed; a conveying means for conveying the object to be heated from the furnace inlet to the furnace outlet in the furnace chamber; Drying microwave heating means for irradiating waves, microwave heating means for irradiating the object to be heated with microwaves in the first firing area to rapidly raise the temperature of the molded body, and heating in the second firing area. External heating means for applying heat to the object to be heated and slowly heating the object,
Temperature rise by microwave heating means for firing is 850 in 45 minutes
A temperature gradient that raises the temperature by an external heating means
A temperature gradient where the temperature rises by 100 ° C in 4 hours
Or the temperature rise by the microwave heating means for firing is 3
External heating with a temperature gradient of 850 ° C in 0 minutes
The temperature at which the temperature rise by means increases the temperature by 100 ° C in 2 hours.
Is a degree gradient .

【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 method of the present invention for producing ceramics from wastes, when a compact placed in a firing furnace is first irradiated with microwaves, the compact itself generates heat and heat is generated. Compared to the case where heat is transferred from the inner side to the outer side of the
The temperature of the molded body rapidly rises and reaches a suitable temperature shortly before melting. Thereafter, when the molded body is heated by the external heating means, heat is transmitted from the outside to the inside of the molded body, and the molded body is slowly heated to the final temperature and sintered.

【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 in combination, it is possible to easily stabilize the dense ceramics while using as a raw material a waste glass made of a variety of substances having 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 sintering furnace of the present invention, a pre-heating treatment for rapidly heating the compact to an appropriate temperature by the microwave heating means and a slow heating of the compact to the sintering temperature by the external heating means. Since the post-heating treatment is performed in combination, dense ceramics can be stably formed in a short time from waste molten glass.

【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 compact is moved from the furnace inlet to the furnace outlet in the furnace chamber by the transfer means. During this time, in the drying region, the molded body is dried while maintaining the molded body in a low temperature range by microwave heating. In the first sintering region, the preheating treatment is performed by rapidly heating to an appropriate temperature just before melting the molded body by microwave heating. In the second firing region, the compact is slowly heated to the final temperature by the external heating means and sintered. For this reason, dense ceramics can be continuously and stably formed from 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。
An embodiment of the present invention will be described below. In FIG. 1, a microwave oscillator 3 is connected to a microwave firing furnace 1 via a waveguide 2 and an exhaust fan 5 is connected via a flue 4. An electric furnace 6 is arranged inside the microwave firing 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 as needed. The furnace body 7 forms a furnace chamber 9 in which a closed space surrounded by a heat insulating material 7a houses a molded body 8 which is 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 this embodiment, the waste molten glass includes general waste such as municipal waste, sewage sludge and fly ash, and industrial waste such as mine debris, river sediment, construction sludge and the like. Is obtained by cooling and solidifying a molten slag obtained by subjecting the waste to melting treatment, and is formed into a sintered material by pulverizing to a suitable 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 the powdery granules of the waste molten glass, mixed and kneaded to form a clay,
The molded body 8 is formed by drying. The mixing ratio between the molten glass waste and the molding material in this kneaded material can be set arbitrarily according to the characteristics of the target ceramics, and it is 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 clay, it is possible to combine various materials in addition to the above, not only conventional ceramic raw materials, but also unused resources and It is also possible to use the industrial waste as it is by pulverizing it to an appropriate particle size without turning it into a slag, or to combine refined raw materials, organic substances such as wood powder, and carbon.

【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 this embodiment, the compact 8 is made of a mixture of 80% municipal solid waste slag and 20% clay at 200 × 200 × 2.
It is formed in a 00 cube. Hereinafter, the operation of the above configuration will be described. FIG. 2 shows the relationship between the sintering temperature and the sintering time, in which the molded body 8 is sintered 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. The molded body 8 is heated to an appropriate temperature (100 ° C.) by the microwave heating, and dried at this temperature for about 4 hours. Thereafter, the molded body 8 is heated to an appropriate temperature (700 ° C.) slightly before melting by pre-firing by strengthening the microwave heating. At this time, according to the microwave heating, the molded body itself generates heat, and heat is transmitted from the inside to the outside of the molded body 8,
The temperature of the molded body 8 is rapidly increased in a short time (about 30 minutes) as compared with the case where heat is transferred from another substance to the molded body 8. still,
When the heating element is arranged on the inner side surface of the heat insulating material 7a, the heating element generates heat by being irradiated with the microwave, and 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。
Thereafter, the molded body 8 is heated to a sintering temperature by electric resistance heat generated from the electric heating element 11, and ceramics are formed by sintering the components of the molded body 8. At this time, heat is transmitted from the outside to the inside of the molded body 8, and is slowly fired (4 hours) until it reaches the sintering temperature (900 ° C.). ) And sinter. The electric furnace 6 is preheated as required.

【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 microwave and the heating from the outside by the electric heating element 11 in combination, it is possible to use the waste molten glass as a raw material, which is composed of various substances whose components are not fixed. 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 in the furnace can be reduced by reducing the atmosphere in the furnace to a reduced pressure or a vacuum by means of the exhaust fan 5 or other means. FIG. 3 shows the relationship between the sintering temperature and the sintering time when the inside of the furnace is in a reduced pressure state.

【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 configuration of a continuous firing furnace according to another embodiment of the present invention. The continuous firing furnace 21 includes a microwave drying furnace 22 serving as a drying area, a microwave firing furnace 23 serving as a first firing area, and a gas firing furnace 24 serving as a second firing area, and forms a continuous space. I have. A microwave oscillator 26 is connected to the microwave drying furnace 22 and the microwave firing furnace 23 via a waveguide 25, and a fixed heat insulating material 23a is arranged in the microwave firing furnace 23. 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 carts 30 are arranged in the furnace from the furnace inlet to the furnace outlet. The carts 30 constitute a conveying means for conveying a molded body 31 to be heated, and are formed by a heat insulating material 32. A furnace chamber 33 is provided. The electric wave absorber doors 34 are provided at the furnace entrance and the furnace exit. The molded body 31 in the present embodiment is obtained by forming a mixture of fly ash slag 60% and clay 40% into a 200 × 200 × 200 cube.

【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, in which the compact 8 is fired with a temperature gradient as shown in FIG. The compact 31 is placed in the furnace chamber 33 of the truck 30 and a plurality of trucks 30 are sequentially fed into the furnace to form the compact 3.
1 is moved from the furnace inlet to the furnace outlet by the carriage 31. During this time, the microwave drying furnace 22 forming the drying area
In, the compact 31 is dried by irradiating the compact 31 with microwaves emitted from the microwave oscillator 26 and maintaining the compact 31 in a low temperature range (100 ° C.) for 4 hours. In the microwave firing furnace 23 forming the first firing area, the molded body 31 is heated by microwave heating to an appropriate temperature (950) just before melting.
(° C.) to perform preliminary firing. In the gas firing furnace 24 forming the second firing area, the gas burner 27
The molded body 31 is slowly heated to the final temperature (1
(050 ° C.), and the main firing is performed, and thereafter, the leveling firing is performed for 1 hour to sinter the components of the molded body 31. For this reason, dense ceramics can be continuously and stably formed from 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 reducing the atmosphere in the furnace to a reduced pressure state or a vacuum state by exhausting by the exhaust fan 29 or other means. FIG. 6 shows the relationship between the firing temperature and the firing time when the inside of the furnace is in a reduced pressure state.

【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 a microwave heating means and an external heating type heating means together, it is possible to use a raw material made of a variety of materials having a variable component called waste molten glass. However, dense ceramics can be easily and stably formed in a short time.

【図面の簡単な説明】[Brief description of the 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 ceramic 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 sintering temperature and a sintering time when the inside of a furnace is in a normal pressure state in the embodiment.

【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 a relationship between a sintering temperature and a sintering time when the inside of the furnace is in a reduced pressure state in the 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 ceramic 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 a relationship between a sintering temperature and a sintering 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 a relationship between a sintering temperature and a sintering time when the inside of the furnace is depressurized in the 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 DESCRIPTION OF SYMBOLS 1 Microwave firing furnace 3 Microwave oscillator 6 Electric furnace 9 Furnace room 11 Electric heating element

───────────────────────────────────────────────────── フロントページの続き (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 (56)参考文献 特開 平6−87677(JP,A) 米国特許4375441(US,A) (58)調査した分野(Int.Cl.7,DB名) C04B 35/00,35/64 B09B 3/00 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Shoji Okada 2-47, Shikitsuhigashi, Namiwa-ku, Osaka-shi, Osaka Prefecture Inside Kubota Corporation (72) Inventor Satoru Shibaken Shikitsu-higashi, Namiwa-ku, Osaka, Osaka 1-2-47, Kubota Co., Ltd. (72) Hiroshi Tajima, Inventor Hiroshi Tajima 1-2-47, Shibutsu Higashi, Naniwa-ku, Osaka, Osaka (72) Inventor Tetsuo Kiyota, Naniwa-ku, Osaka, Osaka No. 2-47 Tsuto Kubota Co., Ltd. (56) References JP-A-6-87677 (JP, A) US Patent 4,375,441 (US, A) (58) Fields investigated (Int. Cl. 7 , DB Name) C04B 35 / 00,35 / 64 B09B 3/00

Claims (3)

(57)【特許請求の範囲】(57) [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30分で600℃の温
度上昇をなす温度勾配で成形体が溶融する直前の適当温
度にまで急速に昇温させ、その後に外部加熱手段により
成形体を4時間で200℃の温度上昇をなす温度勾配で
焼結温度まで緩速に昇温させるか、 あるいは、マイクロ波加熱によって成形体を15分で6
00℃の温度上昇をなす温度勾配で成形体が溶融する直
前の適当温度にまで急速に昇温させ、その後に外部加熱
手段により成形体を3時間で200℃の温度上昇をなす
温度勾配で焼結温度まで緩速に昇温させるか、 あるいは、マイクロ波加熱によって成形体を45分で8
50℃の温度上昇をなす温度勾配で成形体が溶融する直
前の適当温度にまで急速に昇温させ、その後に外部加熱
手段により成形体を4時間で100℃の温度上昇をなす
温度勾配で焼結温度まで緩速に昇温させるか、 あるいは、マイクロ波加熱によって成形体を30分で8
50℃の温度上昇をなす温度勾配で成形体が溶融する直
前の適当温度にまで急速に昇温させ、その後に外部加熱
手段により成形体を2時間で100℃の温度上昇をなす
温度勾配で焼結温度まで緩速に昇温させて成形体の成分
を緻密に焼結して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 product such as municipal solid waste, sewage sludge, fly ash and the like is melt-processed, 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. and, placed in a firing furnace the molded body forming the object to be heated is irradiated with microwaves in the molded body from the microwave heating means, of 600 ° C. for 30 minutes moldings by microwave heating temperature
A suitable temperature immediately before the compact melts due to the temperature gradient
Temperature rapidly, and then external heating means
The molded body is heated at a temperature gradient of 200 ° C. in 4 hours.
Either slowly raise the temperature to the sintering temperature, or heat the compact by microwave heating for 6 minutes in 15 minutes.
Immediately after the molded body melts due to a temperature gradient of a temperature rise of 00 ° C
Rapidly raise the temperature to the appropriate temperature before, and then externally heat
The temperature of the molded body is increased by 200 ° C. in 3 hours by means of
The temperature is gradually increased to the sintering temperature by a temperature gradient, or the molded body is heated by microwave heating for 8 minutes in 45 minutes.
Immediately after the compact is melted by a temperature gradient that raises the temperature by 50 ° C.
Rapidly raise the temperature to the appropriate temperature before, and then externally heat
The temperature of the molded body is increased by 100 ° C. in 4 hours by means of
The temperature is gradually increased to the sintering temperature by a temperature gradient, or the molded body is heated by microwave heating for 8 minutes in 30 minutes.
Immediately after the compact is melted by a temperature gradient that raises the temperature by 50 ° C.
Rapidly raise the temperature to the appropriate temperature before, and then externally heat
The molded body is heated to 100 ° C. in 2 hours by means
Slowly raise the temperature to the sintering temperature with a temperature gradient to form the components of the compact.
A method for producing ceramics from waste materials, characterized in that ceramics are formed by densely sintering ceramics .
【請求項2】 廃棄物溶融ガラスを原料成分として含有
する成形体を被加熱物とし、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して成形体を急速に昇温さ
せるマイクロ波加熱手段と、炉室内に位置して被加熱物
に熱を加えて緩速に加熱する外部加熱手段とを備え、マイクロ波加熱手段による昇温が30分で600℃の温
度上昇をなす温度勾配で、外部加熱手段による昇温が4
時間で200℃の温度上昇をなす温度勾配であ るか、 あるいはマイクロ波加熱手段による昇温が15分で60
0℃の温度上昇をなす温度勾配で、外部加熱手段による
昇温が3時間で200℃の温度上昇をなす温度勾配であ
ことを特徴とするセラミックス焼成炉。
2. A furnace body which comprises a molded body containing waste molten glass as a raw material component, and a closed space surrounded by a heat insulating wall forms a furnace chamber for accommodating the heated object; Microwave heating means for irradiating the object with microwaves to rapidly raise the temperature of the molded body, and external heating means for heating the object to be heated, which is located in the furnace chamber and slowly heating the object, Temperature rise of 600 ° C in 30 minutes by microwave heating means
The temperature rise by the external heating means is 4 degrees.
Time temperature gradient der forms a temperature increase of 200 ° C. Luke, or heating by microwave heating means 15 min 60
With a temperature gradient of 0 ° C, with external heating means
A temperature gradient in which the temperature rises to 200 ° C in 3 hours.
Ceramics firing furnace, characterized in that that.
【請求項3】 廃棄物溶融ガラスを原料成分として含有
する成形体を被加熱物とし、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して成形体
を急速に昇温させ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て緩速に加熱する
外部加熱手段とを備え、焼成用マイクロ波加熱手段による昇温が45分で850
℃の温度上昇をなす温度勾配で、外部加熱手段による昇
温が4時間で100℃の温度上昇をなす温度勾配である
か、 あるいは焼成用マイクロ波加熱手段による昇温が30分
で850℃の温度上昇をなす温度勾配で、外部加熱手段
による昇温が2時間で100℃の温度上昇をなす温度勾
配である ことを特徴とするセラミックス焼成炉。
3. A molded object containing waste molten glass as a raw material component is to be heated, and a drying zone, a first firing zone, and a second firing zone are provided from a furnace inlet to a furnace outlet in a furnace chamber for storing the heated object. A furnace body formed continuously with a firing region, a conveying means for conveying the object to be heated from the furnace inlet to the furnace outlet in the furnace chamber, and a drying unit for irradiating the object with microwaves in the drying region. A microwave heating means, a firing microwave heating means for irradiating the object to be heated with microwaves in the first firing region to rapidly raise the temperature of the molded body, and a second heating means.
External heating means for applying heat to the object to be heated in the firing region to slowly heat the object, and the temperature rise by the microwave heating means for firing is 850 in 45 minutes.
A temperature gradient that raises the temperature by an external heating means
A temperature gradient where the temperature rises by 100 ° C in 4 hours
Or, alternatively the heating 30 minutes by firing for microwave heating means
External heating means with a temperature gradient of 850 ° C.
Temperature rise of 100 ° C in 2 hours
Ceramics firing furnace which is a distribution.
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 JPH08157251A (en) 1996-06-18
JP3231197B2 true JP3231197B2 (en) 2001-11-19

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CN104197700B (en) * 2014-09-19 2016-02-17 重庆科技学院 A kind of stepped start-stop system blocks thermal shocking sintering resistance furnace entirely

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