JPS60140013A - Microwave heating process - Google Patents

Microwave heating process

Info

Publication number
JPS60140013A
JPS60140013A JP25100983A JP25100983A JPS60140013A JP S60140013 A JPS60140013 A JP S60140013A JP 25100983 A JP25100983 A JP 25100983A JP 25100983 A JP25100983 A JP 25100983A JP S60140013 A JPS60140013 A JP S60140013A
Authority
JP
Japan
Prior art keywords
powder
microwave
combustion
powder material
explosion
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
JP25100983A
Other languages
Japanese (ja)
Other versions
JPH0333962B2 (en
Inventor
Takakiyo Ike
池 隆清
Hideaki Tamai
玉井 秀昭
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.)
New Japan Radio Co Ltd
Japan Radio Co Ltd
Original Assignee
New Japan Radio Co Ltd
Japan Radio Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by New Japan Radio Co Ltd, Japan Radio Co Ltd filed Critical New Japan Radio Co Ltd
Priority to JP25100983A priority Critical patent/JPS60140013A/en
Publication of JPS60140013A publication Critical patent/JPS60140013A/en
Publication of JPH0333962B2 publication Critical patent/JPH0333962B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Incineration Of Waste (AREA)
  • Constitution Of High-Frequency Heating (AREA)
  • Gasification And Melting Of Waste (AREA)

Abstract

PURPOSE:To provide a microwave heating process with a better thermal efficiency and having no danger of explosion by a method wherein a combustive condition of dried powder material is sensed to adjust a feeding amount of microwave and supplying amount of air. CONSTITUTION:Powder material A is agitated by an agitator device 3 and heated by a microwave from a wave guide pipe 2. In case that a heating is rapidly progressed, the danger of explosion is found, so that the powder material A of non-dried condition is fed at the feeding port 7 automatically in response to the condition of combustion in the heating furnace 1 sensed by a sensor 20, a temperature in the heating furnace 1 is decreased and at the same time the generated heat made by a combustion is utilized for a drying of the non-dried powder material A. In this case, the control device 21 controls the microwave oscillator 22 in response to the output value from the sensor 20 to adjust a microwave power and at the same time the opening or closing of the lid 10 is controlled to adjust the air supply volume. With this arrangement, it is possible to get a microwave heating process without any risk of explosion.

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明は液体を含んだ粉状物、あるいは粉状物の固形化
した物質等の粉状物をマイクロ波を用いて乾燥させ更に
燃焼させるだめのマイクロ波加熱方法に関する。
[Detailed Description of the Invention] [Field of Application of the Invention] The present invention is a method for drying a powdery material such as a powdery material containing a liquid or a solidified substance of the powdery material using microwaves and then combusting it. The present invention relates to a microwave heating method.

〔発明の背景〕[Background of the invention]

一般に液体を含んだ粉状物を乾燥し、更に燃焼させる方
法としては、粉状物を連続的に、しかも大量に乾燥・燃
焼するに適しているところからロータリーキルン方式が
用いられている。このロータリーキルン方式は円筒形の
パイプを回転させながらドラム内部の攪拌羽根(送p出
し兼用)によりドラムの回転に従って粉状物をかき上げ
ながら落下し、繰り返して熱風と接触しながら移送乾燥
し、燃焼させるものである。この乾燥・燃焼用の加熱源
として電熱高温ガス等が用いられている。
Generally, a rotary kiln method is used as a method for drying and burning a powdery material containing a liquid because it is suitable for continuously drying and burning a large amount of powdery material. In this rotary kiln system, a cylindrical pipe is rotated, and a stirring blade inside the drum (also used as a feeder) is used to scrape up and drop powder as the drum rotates, and the powder is repeatedly transferred and dried while coming into contact with hot air, and then combusted. It is something that makes you Electrically heated high temperature gas or the like is used as a heating source for this drying/combustion.

ところが、このロータリーキルン方式は前述の如くパイ
プを回転させて粉状物の加熱・燃焼と輸送を同時に行な
っているため、燃焼が進むに従って湿度を失い更に燃焼
に伴い微勝化するため粉状物が舞い上りやすく々る。こ
のため排出される排気中にはかなりの微粉が含まれるこ
とになる。そこで排気ガスはサイクロンで微粉捕集して
から排気するようにしているが完全に除去できないので
微粉が大気中に放出されるのを防止するため排気系にフ
ィルタ等を設けなければならないことが多い。しかも、
サイクロンやフィルタ等を設けた場合には、サイクロン
やフィルタ等は常に完全に機能させるため結露しない温
度に保っておく必要がある。また粉状物は一般に熱伝導
が悪く、しかもこれを外部から高熱高温ガス等全供給し
加熱するため、熱効率が悪く、粉状物の完全に乾燥・燃
焼するに大きな加熱装置を用いなければならない。
However, as mentioned above, in this rotary kiln system, the pipes are rotated to heat, burn, and transport the powder at the same time, so as the combustion progresses, the powder loses moisture and becomes more concentrated as the combustion progresses. It's easy to fly up. Therefore, the emitted exhaust gas contains a considerable amount of fine powder. Therefore, the exhaust gas is collected with a cyclone before being exhausted, but it cannot be completely removed, so it is often necessary to install a filter in the exhaust system to prevent the fine powder from being released into the atmosphere. . Moreover,
If a cyclone or filter is installed, it is necessary to keep the cyclone or filter at a temperature that does not cause condensation so that it can function fully at all times. Furthermore, powdery materials generally have poor thermal conductivity, and since they are heated by supplying high-temperature gas etc. from the outside, thermal efficiency is poor, and a large heating device must be used to completely dry and burn the powdery materials. .

そのため粉状物の乾燥・燃焼に設備が過剰となるという
欠点を有している。
Therefore, it has the disadvantage that it requires excessive equipment for drying and burning powdery materials.

また、前述のロータリーキルン方式のように粉状物が飛
散することがないという利点を有しているところから粉
状物をオーブン等に入れて静的に外部加熱装置を用いて
加熱乾燥させる方法も用いられている。しかし、数關以
下の径の粒子のある種の粉状物は、静的な状態で加熱乾
燥すると粉状物が固化しオープン内に入った粉状物全体
が大きな1つの塊となってしまい、後の作業が困難にな
るという欠点を有している。
In addition, unlike the rotary kiln method mentioned above, which has the advantage of not scattering the powder, there is also a method in which the powder is placed in an oven or the like and statically heated and dried using an external heating device. It is used. However, if some types of powder with particles with a diameter of several inches or less are heated and dried in a static state, the powder will solidify and the entire powder that enters the open will become one large lump. , it has the disadvantage that subsequent work becomes difficult.

そこで近年熱源としてマイクロ波を用い、しかも攪拌翼
を使用して加熱乾燥・燃焼時に粉状物を攪拌し粉状物が
大きな塊とならないようにすると共に粉状物の攪拌時に
粉状物の飛散を生じさせない第一1・図に示す如きマイ
クロ波加熱装置が提案されている。すなわち、導電性で
円筒形状を有する加熱炉1.2は、図示しないマイクロ
波発振器からアイソレータ、パワーモニタ、整合器、仕
切窓放電検出器等の回路素子を経由して送られてくるマ
イクロ波を加熱炉1内に照射するためのマイクロ波照射
口となる導波管2が接続されている。捷た、加熱炉1の
中央には、下端に攪拌翼3aが設けられた攪拌装置3が
設けられている。この攪拌装置3はベアリング4で軸受
けされ、モータ5によりゆっくりと回転するように構成
されておシ、この攪拌装置3の回転は攪拌翼3aを回転
させ、これによって加熱乾燥、燃焼中の粉状物の塊状化
を防止している。また、ベアリング4にマイクロ波が流
れないようにこのベアリング4にチョーク6が設けられ
ており、ベアリング4の破損を防止している。また、加
熱炉1には乾燥すべき粉状物Aを内部に投入するための
投入ロアと、加熱炉1内で発生する蒸気等のガスを排気
するための排気口8が設けられている。これら投入ロア
と排気口8の内径はそれぞれ使用マイクロ波の波長の1
/2以下に設定され、マイクロ波が洩れるのを防止して
いる。また、加熱炉1の下部には燃焼の際に必要な空気
を供給するための給気口9が設けられている。この給気
口9には図示矢印Aに示す方向に着脱可能な蓋10が設
けられておp、この蓋10は給気口9′t−開閉する機
能を有している。
Therefore, in recent years, microwaves have been used as a heat source, and stirring blades have been used to stir the powder during heating drying and combustion to prevent the powder from forming large lumps, and to prevent the powder from scattering when stirring the powder. A microwave heating device as shown in Figure 1 has been proposed, which does not cause this. That is, the heating furnace 1.2, which is conductive and has a cylindrical shape, receives microwaves sent from a microwave oscillator (not shown) via circuit elements such as an isolator, a power monitor, a matching device, and a partition window discharge detector. A waveguide 2 serving as a microwave irradiation port for irradiating the inside of the heating furnace 1 is connected. A stirring device 3 having stirring blades 3a at the lower end is provided in the center of the heated furnace 1. This stirring device 3 is supported by a bearing 4 and is configured to be rotated slowly by a motor 5.The rotation of this stirring device 3 rotates stirring blades 3a, thereby heating and drying and burning powder. Prevents things from clumping. Further, a choke 6 is provided on the bearing 4 to prevent microwaves from flowing into the bearing 4, thereby preventing the bearing 4 from being damaged. Further, the heating furnace 1 is provided with a charging lower for charging the powder material A to be dried into the heating furnace 1, and an exhaust port 8 for exhausting gas such as steam generated within the heating furnace 1. The inner diameters of these input lower and exhaust ports 8 are each one of the wavelength of the microwave used.
/2 or less to prevent microwaves from leaking. Furthermore, an air supply port 9 is provided at the bottom of the heating furnace 1 for supplying air necessary for combustion. This air supply port 9 is provided with a lid 10 that can be attached and removed in the direction shown by the arrow A in the figure, and this lid 10 has the function of opening and closing the air supply port 9't.

このような第1図に示される従来のマイクロ波加熱装置
によって粉状物全加熱乾燥、燃焼するには次の如く行な
われる。すなわち、給気口9を蓋10で一部をふさぎ投
入ロアから液体な含む粉状体あるいは粉状体固形物等の
粉状物Aを投入し、その後攪拌装置3を駆動して攪拌翼
3aをゆつく9回転させながら、導波管2からマイクロ
波を照射する。この導波管2から照射されるマイクロ波
は、粉状物Aに吸収され、この粉状物Aは発熱し乾燥す
る。この乾燥時に攪拌翼3aはゆつく9回転するので、
粉状物Aは固化していても1個の塊状にはならず微粒の
粉状体に戻される。また、攪拌翼3aがゆっくりと回転
するため乾燥した粉状物Aが飛散することなく排気口8
から排出されるガスには粉状物の含有し々い粉状物から
蒸発するガスのみとなる。この粉状物の乾燥が完了した
後更に粉状物にマイクロ波を照射すると粉状物Aは温度
が上昇し燃え出す。この燃焼の際に多くの酸素を必要と
するので給気口9の蓋10を開き燃焼用空気等を供給す
る。この粉状物の燃焼時には燃焼に伴って相当の熱が生
じ燃焼は急に高まる。したがって、このような従来のマ
イクロ波加熱装置による加熱方法によると多量の可燃性
ガスを発生するような種類の粉状物にあっては爆発の危
険性があるという欠点を有している。
Complete heating, drying, and combustion of a powder material using the conventional microwave heating apparatus shown in FIG. 1 is performed as follows. That is, the air supply port 9 is partially covered with the lid 10, and the powder A, such as a liquid powder or a powder solid, is introduced from the input lower, and then the stirring device 3 is driven and the stirring blades 3a are fed. Microwaves are irradiated from the waveguide 2 while rotating slowly nine times. The microwave irradiated from the waveguide 2 is absorbed by the powder A, and the powder A generates heat and dries. During this drying, the stirring blade 3a slowly rotates 9 times, so
Even if the powder A is solidified, it does not become a single lump and is returned to a fine powder. In addition, since the stirring blade 3a rotates slowly, the dry powder A is not scattered and the exhaust port 8
The only gas emitted from the tank is the gas evaporated from the powdery material containing the powdery material. When the powder A is further irradiated with microwaves after the drying of the powder is completed, the temperature of the powder A rises and it starts to burn. Since a large amount of oxygen is required for this combustion, the lid 10 of the air supply port 9 is opened to supply combustion air and the like. During the combustion of this powdered material, a considerable amount of heat is generated as a result of the combustion, and the combustion rate rapidly increases. Therefore, the conventional heating method using a microwave heating device has the disadvantage that there is a risk of explosion if the powdery material generates a large amount of flammable gas.

また、従来のマイクロ波加熱装置にあっては発生した熱
が排気ガスと共に急速に排気口8から外部に放出される
のでエネルギーの無駄な放出が行なわれ、熱効率が悪い
という欠点を有している。
Furthermore, in conventional microwave heating devices, the generated heat is rapidly released to the outside from the exhaust port 8 along with the exhaust gas, which results in wasteful release of energy and has the disadvantage of poor thermal efficiency. .

〔発明の目的〕[Purpose of the invention]

本発明の目的は熱効率の良い爆発の危険性のないマイク
ロ波加熱方法を提供することにある。
An object of the present invention is to provide a microwave heating method that is thermally efficient and has no risk of explosion.

〔発明の概要〕[Summary of the invention]

本発明は、加熱炉内に投入された粉状物に攪拌しながら
加熱・乾燥し、この乾燥された粉状物の燃焼状態を検出
して所定燃焼状態を越えたときにマイクロ波供給量及び
供給空気量を調整すると共に適量の未乾燥粉状物を自動
的に投入し、さらに攪拌しながら乾燥・燃焼させること
により、熱効率會良くしようというものである。
The present invention heats and dries the powdered material put into a heating furnace while stirring it, detects the combustion state of the dried powdered material, and detects when the combustion state of the dried powder exceeds a predetermined combustion state. The aim is to improve thermal efficiency by adjusting the amount of air supplied, automatically adding an appropriate amount of undried powder, and drying and burning it while stirring.

〔発明の実施例〕[Embodiments of the invention]

以下、本発明の実施例について説明する。 Examples of the present invention will be described below.

第2図には本発明に係るマイクロ波加熱方法に用いられ
るマイクロ波加熱装置が示されている。
FIG. 2 shows a microwave heating device used in the microwave heating method according to the present invention.

図中第1図図示従来例と同一の符号に付されているもの
は同一の部品・同一の機能を有するものである。図にお
いて、第1図図示従来例と異なる点は、排気口8に粉状
物Aの燃焼状態を知るためのセンサ20が設けられてい
る点である。また、21は制御装置、22はマイクロ波
発振器である。
Components in the figure that are denoted by the same reference numerals as those in the conventional example shown in FIG. 1 are the same parts and have the same functions. In the figure, the difference from the conventional example shown in FIG. 1 is that a sensor 20 is provided at the exhaust port 8 to determine the combustion state of the powdery substance A. Further, 21 is a control device, and 22 is a microwave oscillator.

このように構成されるマイクロ波加熱装置を用いたマイ
クロ波加熱方法は次の如くである。
A microwave heating method using the microwave heating device configured as described above is as follows.

〔第1段階〕 制御装置21からの制御信号によυモータ5が回転駆動
され攪拌装置3により粉状物Aは攪拌される。この時、
同時に粉状物Aには導波管2を介してマイクロ波が照射
され粉状物は加熱される。
[First stage] The υ motor 5 is rotationally driven by a control signal from the control device 21, and the powdery material A is stirred by the stirring device 3. At this time,
At the same time, the powder A is irradiated with microwaves through the waveguide 2 to heat the powder.

この粉状物Aの温度が上昇すると、粉状物Aに含まれて
いる液体は蒸発し排気口8から排出される。
When the temperature of the powder A increases, the liquid contained in the powder A evaporates and is discharged from the exhaust port 8.

このように粉状物Aは次第に乾燥される。この際粉状物
Aは攪拌翼3aによって攪拌されるので固化することは
防がれ均一に乾燥される。
In this way, the powder A is gradually dried. At this time, the powder A is stirred by the stirring blade 3a, so that it is prevented from solidifying and is dried uniformly.

〔第2段階〕 次に充分乾燥された粉状物Aに更にマイクロ波を照射す
ると粉状物Aは燃焼する。この粉状物Aが燃焼するには
多量の酸素を必要とするので給気口9の蓋10を開き、
給気する。粉状物Aの燃焼が始まると燃焼に伴って相当
の熱が生じ、この燃焼熱の相乗効果によシ燃焼は急に高
まる。あまp燃焼が急に進むと、排気口8が設けられて
いるとはいえ加熱炉1は閉構造となっているため、内気
圧の急膨張による爆発の危険性もあり、好ましくない。
[Second stage] Next, when the sufficiently dried powder A is further irradiated with microwaves, the powder A is combusted. Since this powder A requires a large amount of oxygen to burn, open the lid 10 of the air supply port 9,
Supply air. When the combustion of the powder material A begins, a considerable amount of heat is generated as a result of the combustion, and the synergistic effect of this combustion heat causes the combustion to rapidly increase. If the combustion progresses rapidly, the heating furnace 1 has a closed structure even though the exhaust port 8 is provided, so there is a risk of explosion due to the rapid expansion of the internal pressure, which is not preferable.

そこで、センサ20によって検出される加熱炉1内の燃
焼状態に従って自動的に新た表未乾燥の粉状物Aを投入
ロアから投入して加熱炉1内の温度ケ下げると同時に燃
焼に伴う発熱を新しく投入された未乾燥の粉状物Aの乾
燥に利用する。
Therefore, according to the combustion state inside the heating furnace 1 detected by the sensor 20, new undried powder A is automatically introduced from the charging lower to lower the temperature inside the heating furnace 1 and at the same time reduce the heat generated due to combustion. It is used to dry the newly introduced undried powder material A.

この際センサ20からの出力値によって制御装置21は
マイクロ波発振器22を制御してマイクロ波電力を調整
すると共に蓋10の開閉を制御し空気の供給量を調整す
る。なおこのセンサ20は温度センサ、湿度センサ、圧
力センサ等でよい。
At this time, the control device 21 controls the microwave oscillator 22 to adjust the microwave power based on the output value from the sensor 20, and also controls the opening and closing of the lid 10 to adjust the amount of air supplied. Note that this sensor 20 may be a temperature sensor, humidity sensor, pressure sensor, or the like.

未乾燥の粉状物へを投入するこの第2段階は、燃焼に伴
って生ずる残査が少い場合には、数回繰返し行っても良
く、必要に応じて繰返しが可能である。
This second step of charging the undried powder may be repeated several times if the amount of residue generated due to combustion is small, and can be repeated as necessary.

〔第3段階〕 次に、粉状物Aは燃焼すると、その体積がVI。[Third stage] Next, when powder A burns, its volume becomes VI.

〜17’20に減少するので、燃焼中に未乾燥の粉状物
Aを投入しても加熱炉1内の粉状物の量を一定に保つこ
とはできる。しかし、長時間運転すると残査も次第に増
加して来、未乾燥の粉状物Aを投入できる厳が次第に減
少してくるため、一定時間経過したら、あるいは一定量
粉状物を供給したら未乾燥の粉状物Aの投入を止め、マ
イクロ波及び供給空気量を制御して粉状物全全部燃焼さ
せる。
17'20, the amount of powder in the heating furnace 1 can be kept constant even if undried powder A is introduced during combustion. However, if the operation continues for a long time, the amount of residue will gradually increase, and the capacity to feed the undried powder A will gradually decrease. The injection of powder A is stopped, and the amount of microwave and air supply is controlled to burn all of the powder.

〔第4段階〕 次に、全部燃焼させると残査を加熱炉1内から排出し、
全工程を完了する。
[Fourth stage] Next, after all the combustion is completed, the residue is discharged from the heating furnace 1,
Complete the entire process.

なお、第2段階の最終状態において制御装置21によっ
て第3段階の操作を連続的に行っても同様の効果を期待
できることQまいう筐でもない。
Note that it is not possible to expect the same effect even if the control device 21 performs the third stage operation continuously in the final state of the second stage.

したがって、本実施例によれば未乾燥の粉状物全効率良
く且つ爆発の危険性なく燃焼させることができる。
Therefore, according to this embodiment, the undried powder can be burned with high efficiency and without the risk of explosion.

〔発明の効果〕〔Effect of the invention〕

以上説明したように、本発明によれば熱効率全長くし、
しかも爆発の危険なく燃焼させることができる。
As explained above, according to the present invention, the thermal efficiency is increased over the entire length,
Moreover, it can be burned without the risk of explosion.

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

第1図は従来のマイクロ波加熱装置の構成図、第2図は
本発明に係るマイクロ波加熱方法に用いるマイクロ波加
熱装置の構成図、第3図は本発明の実施FJk示すフロ
ーダイヤグラムである。 1・・・加熱炉、2・・・導波管、3・・・攪拌装置、
7・・・投入口、8・・・排気口、9・・・給気口、2
0・・・センサ、21・・・制御装置、22・・・マイ
クロ波発振器。 代理人 鵜 沼 辰 之 (ほか1名) (11) 第1図
Fig. 1 is a block diagram of a conventional microwave heating device, Fig. 2 is a block diagram of a microwave heating device used in the microwave heating method according to the present invention, and Fig. 3 is a flow diagram showing implementation FJk of the present invention. . 1... Heating furnace, 2... Waveguide, 3... Stirring device,
7...Inlet port, 8...Exhaust port, 9...Air supply port, 2
0...Sensor, 21...Control device, 22...Microwave oscillator. Agent Tatsuyuki Unuma (and 1 other person) (11) Figure 1

Claims (1)

【特許請求の範囲】[Claims] (1)液体を含んだ粉状体あるいは粉状体の可燃固形物
等の粉状物を攪拌しながらマイクロ波を照射して加熱・
乾−44させる第1のステップと、前記粉状物の乾#う
状態が所定状態になると新らたに粉状物を供給すると共
に前記マイクロ波の照射量と供給空気量を制御して攪拌
し々から加熱・乾煉沙させる第2のステップと、前記第
2のステップにおいて順次供給された粉状体の量が所定
陰に達すると新たに粉状物を供給するのをやめ、炉内の
粉状物を完全に燃焼させる第3のステップとからなるこ
とを特徴とするマイクロ波加熱方法。
(1) Powder containing liquid or powdered combustible solids is heated and heated by irradiating it with microwaves while stirring.
A first step of drying the powder, and when the drying state of the powder reaches a predetermined state, a new powder is supplied, and the amount of microwave irradiation and the amount of supplied air are controlled and agitated. The second step is to gradually heat and dry the bricks, and when the amount of powder sequentially supplied in the second step reaches a predetermined value, the supply of new powder is stopped and the inside of the furnace is and a third step of completely burning the powdery material.
JP25100983A 1983-12-27 1983-12-27 Microwave heating process Granted JPS60140013A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25100983A JPS60140013A (en) 1983-12-27 1983-12-27 Microwave heating process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25100983A JPS60140013A (en) 1983-12-27 1983-12-27 Microwave heating process

Publications (2)

Publication Number Publication Date
JPS60140013A true JPS60140013A (en) 1985-07-24
JPH0333962B2 JPH0333962B2 (en) 1991-05-21

Family

ID=17216279

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25100983A Granted JPS60140013A (en) 1983-12-27 1983-12-27 Microwave heating process

Country Status (1)

Country Link
JP (1) JPS60140013A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63116013A (en) * 1986-10-31 1988-05-20 Toshiba Corp Garbage incinerator
JPS6458910A (en) * 1987-08-31 1989-03-06 Matsushita Electric Ind Co Ltd Refuse disposer

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63116013A (en) * 1986-10-31 1988-05-20 Toshiba Corp Garbage incinerator
JPS6458910A (en) * 1987-08-31 1989-03-06 Matsushita Electric Ind Co Ltd Refuse disposer

Also Published As

Publication number Publication date
JPH0333962B2 (en) 1991-05-21

Similar Documents

Publication Publication Date Title
JP5896073B1 (en) Drying processing equipment
JP2006008736A (en) Carbonization treatment apparatus for organic waste
JPS60140013A (en) Microwave heating process
JPH03100439A (en) Method for controlling microwave heating and drying machine
US4508039A (en) Method of and system for incinerating sludge
JP3867259B2 (en) Method for controlling oxygen concentration in garbage drying device
JP2004191010A (en) Wood pellet fuel combustion system
JP2004191017A (en) Wood pellet fuel combustion system
JP3867258B2 (en) Product ignition prevention mechanism and product ignition prevention method in drying equipment
JP2913453B2 (en) Sludge drying equipment
JPH0256566B2 (en)
JP2017225958A (en) Water content controlling method of dry sludge and carbonization treatment facility of sludge
JP2656668B2 (en) Method and apparatus for reducing moisture contained in waste
RU2170396C1 (en) Method of drying hydrolyzed lignin and device for realization of this method
JPH0144565Y2 (en)
JP3479651B1 (en) Rotary carbonization equipment
RU18762U1 (en) GRAIN DRYER
JPH01239308A (en) Microwave incinerator
JPS62237213A (en) Combustion substance feeding method for fluidized bed heat reaction device and fluidized bed heat reaction device
RU2046876C1 (en) Device for preparing asphalt/concrete mixture
JPS61153308A (en) Incineration of waste ion exchange resin or the like effected by microwave
JP3015936B2 (en) Drying equipment
SU1064094A1 (en) Drying plant for pulverulent materials
US10788206B2 (en) Rotary batch decoater
RU2183873C2 (en) Plant for thermochemical treatment of combustible powdered and crushed radioactive wastes