JPH0333962B2 - - Google Patents

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Publication number
JPH0333962B2
JPH0333962B2 JP25100983A JP25100983A JPH0333962B2 JP H0333962 B2 JPH0333962 B2 JP H0333962B2 JP 25100983 A JP25100983 A JP 25100983A JP 25100983 A JP25100983 A JP 25100983A JP H0333962 B2 JPH0333962 B2 JP H0333962B2
Authority
JP
Japan
Prior art keywords
powder
powdery
heating
combustion
amount
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
Application number
JP25100983A
Other languages
Japanese (ja)
Other versions
JPS60140013A (en
Inventor
Takakyo Ike
Hideaki Tamai
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.)
Japan Radio Co Ltd
Original Assignee
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 Japan Radio Co Ltd filed Critical 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

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  • Gasification And Melting Of Waste (AREA)
  • Incineration Of Waste (AREA)

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た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 and further burning powdery substances such as powdery substances containing liquid or solidified substances using microwaves. 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
がらドラム内部の撹拌羽根(送り出し兼用)によ
りドラムの回転に従つ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. This rotary kiln system rotates a cylindrical pipe while stirring the powder inside the drum (which also serves as a feeder).As the drum rotates, the powder is stirred up and dropped, and it 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
送を同時に行なつているため、燃焼が進むに従つ
て湿度を失い更に燃焼に伴い微粉化するため粉状
物が舞い上りやすくなる。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
系にフイルタ等を設けなければならないことが多
い。しかも、サイクロンやフイルタ等を設けた場
合には、サイクロンやフイ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つておく必要が
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を供給し加熱する
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。
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。
However, as mentioned above, this rotary kiln system rotates the pipe to heat, burn, and transport the powder at the same time, so as the combustion progresses, it loses moisture and further becomes pulverized as it burns. Things tend to fly up. Therefore, the exhaust gas that is discharged 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, etc. in the exhaust system to prevent the fine powder from being released into the atmosphere. . Moreover, when a cyclone, filter, etc. are provided, it is necessary to keep the cyclone, filter, etc. at a temperature that does not cause dew condensation so that the cyclone, filter, etc. always function perfectly. 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 large heating equipment must be used to completely dry and burn the powdery materials. .
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mm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
物が固化しオーブン内に入つた粉状物全体が大き
な1つの塊となつてしまい、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 millimeters or less are heated and dried in a static state, the powder will solidify and the entire powder that enters the oven 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
も撹拌翼を使用して加熱乾燥・燃焼時に粉状物を
撹拌し粉状物が大きな塊とならないようにすると
共に粉状物の撹拌時に粉状物の飛散を生じさせな
い第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。ま
た、加熱炉1の中央には、下端に撹拌翼3aが設
けられた撹拌装置3が設けられている。この撹拌
装置3はベアリング4で軸受けされ、モータ5に
よりゆつくりと回転するように構成されており、
この撹拌装置3の回転は撹拌翼3aを回転させ、
これによつて加熱乾燥、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口7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。これら投入口7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が設けられており、この蓋10
は給気口9を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 FIG. 1 has been proposed which does not cause this. That is, the heating furnaces 1 and 2, which are conductive and have a cylindrical shape, receive 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. Furthermore, in the center of the heating furnace 1, there is provided a stirring device 3 having stirring blades 3a at its lower end. This stirring device 3 is supported by a bearing 4 and is configured to rotate slowly by a motor 5.
This rotation of the stirring device 3 rotates the stirring blades 3a,
This prevents the powder from clumping during heating, drying, and combustion. 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. The heating furnace 1 also has an input port 7 for charging the powder material A to be dried into the heating furnace 1 .
An exhaust port 8 is provided for exhausting gas such as steam generated inside. The inner diameter of these input port 7 and exhaust port 8 is 1/2 of the wavelength of the microwave used.
The settings are as follows to prevent microwave leakage. 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 is removable in the direction shown by the arrow A in the figure.
has the function of opening and closing the air supply port 9.

このような第1図に示される従来のマイクロ波
加熱装置によつて粉状物を加熱乾燥、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口7から液体を含む粉状
体あるいは粉状体固形物等の粉状物Aを投入し、
その後撹拌装置3を駆動して撹拌翼3aをゆつく
り回転させながら、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。この乾燥時に撹拌翼3aはゆつくり回
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、撹
拌翼3aがゆつ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な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
焼に伴つて相当の熱が生じ燃焼は急に高まる。し
たがつて、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つては爆発の危険性
があるという欠点を有している。
The heating, drying, and combustion of a powdered material using the conventional microwave heating apparatus shown in FIG. 1 is carried out as follows. That is, the air supply port 9 is partially closed with a lid 10, and the powder A such as a powder containing liquid or a powder solid is introduced from the input port 7.
Thereafter, microwaves are irradiated from the waveguide 2 while the stirring device 3 is driven to slowly rotate the stirring blades 3a. 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 rotates slowly, so that even if the powder A is solidified, it does not become a single lump but is returned to a fine powder. Furthermore, since the stirring blades 3a rotate slowly, the dried powder A is not scattered, and the gas discharged from the exhaust port 8 contains only the gas evaporated from the powder, which does not contain any powder. When the powder A is further irradiated with microwaves after the drying of the powder is completed, the temperature of the powder A increases 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, heating methods using such conventional microwave heating devices have the disadvantage that there is a risk of explosion when it comes to powdery materials that generate large amounts of flammable gas. .

また、従来のマイクロ波加熱装置にあつては発
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 the case of conventional microwave heating devices, the generated heat is rapidly released to the outside from the exhaust port 8 together 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を撹拌
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
撹拌しながら乾燥・燃焼させることにより、熱効
率を良くしようというものである。
The present invention heats and dries powdered material put into a heating furnace while stirring it, detects the combustion state of this dried powdered material, and detects when the combustion state 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. Also,
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りモータ5が
回転駆動され撹拌装置3により粉状物Aは撹拌さ
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。
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。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は撹拌翼3aによつて撹拌されるの
で固化することは防がれ均一に乾燥される。
[First stage] The 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, the powder A is simultaneously irradiated with microwaves through the waveguide 2, and the powder is heated.
When the temperature of the powder A increases, the liquid contained in the powder A evaporates and is discharged from the exhaust port 8. 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つて相当の熱が生じ、この燃
焼熱の相乗効果により燃焼は急に高まる。あまり
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は閉構造となつているため、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。そこで、センサ20によつて検出される加
熱炉1内の燃焼状態に従つて自動的に新たな未乾
燥の粉状物Aを投入口7から投入して加熱炉1内
の温度を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。
この際センサ20からの出力値によつて制御装置
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。
[Second stage] Next, when the sufficiently dried powder A is further irradiated with microwaves, the powder A is combusted. This powder A
Since a large amount of oxygen is required for combustion, the lid 10 of the air supply port 9 is opened to 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 too quickly, there is a risk of explosion due to rapid expansion of internal pressure, which is undesirable since the heating furnace 1 has a closed structure even though the exhaust port 8 is provided. Therefore, according to the combustion state inside the heating furnace 1 detected by the sensor 20, a new undried powder material A is automatically introduced from the inlet 7 to lower the temperature inside the heating furnace 1. The heat generated by combustion is used to dry the newly added undried powder A.
At this time, the control device 21 controls the microwave oscillator 22 based on the output value from the sensor 20 to adjust the microwave power, 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Aを投入するこの第2段階は、
燃焼に伴つて生ずる残査が少い場合には、数回繰
返し行つても良く、必要に応じて繰返しが可能で
ある。
This second stage of introducing the undried powder A is
When the amount of residue generated due to combustion is small, the process may be repeated several times, 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1/10
〜1/20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
できる量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を全部燃焼させる。
[Third stage] Next, when powder A is burnt, its volume decreases to 1/10
Since the amount decreases to ~1/20, the amount of powder in the heating furnace 1 can be kept constant even if undried powder A is added during combustion. However, if the operation continues for a long time, the amount of residue will gradually increase, and the amount of undried powder A that can be fed will gradually decrease. The injection of powder A is stopped, and the microwave and the amount of air supplied are controlled to completely burn 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, when the entire mixture is combusted, the residue is discharged from the heating furnace 1, and the entire process is completed.

なお、第2段階の最終状態において制御装置2
1によつて第3段階の操作を連続的に行つても同
様の効果を期待できることはいうまでもない。
Note that in the final state of the second stage, the control device 2
It goes without saying that the same effect can be expected even if the operation of the third stage is performed continuously according to No. 1.

したがつて、本実施例によれば未乾燥の粉状物
を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, undried powder can be burned efficiently 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を
良くし、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, thermal efficiency can be improved and combustion can be performed without the risk of explosion.

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

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
の実施例を示すフローダイヤグラムである。 1……加熱炉、2……導波管、3……撹拌装
置、7……投入口、8……排気口、9……給気
口、20……センサ、21……制御装置、22…
…マイクロ波発振器。
Figure 1 is a configuration 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 an embodiment of the present invention. DESCRIPTION OF SYMBOLS 1... Heating furnace, 2... Waveguide, 3... Stirring device, 7... Input port, 8... Exhaust port, 9... Air supply port, 20... Sensor, 21... Control device, 22 …
...Microwave oscillator.

Claims (1)

【特許請求の範囲】[Claims] 1 液体を含んだ粉状体あるいは紛状体の可燃固
形物等の粉状物を撹拌しながらマイクロ波を照射
して加熱・乾燥させる第1のステップと、前記粉
状物の乾燥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撹拌しながら加熱・乾燥させ
る第2のステツプと、前記第2のステツプにおい
て順次供給された粉状体の量が所定量に達すると
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のステツプとからなるこ
とを特徴とするマイクロ波加熱方法。
1. A first step of heating and drying a powdery material such as a powdery material containing a liquid or a powdery combustible solid material by irradiating microwaves while stirring the powdery material, and heating and drying the powdery material such as a powdery material containing a liquid or a powdery combustible solid material, and a step of heating and drying the powdery material such as a powdery material containing a liquid or a powdery combustible solid material. When the condition is reached, there is a second step in which a new powder is supplied, and the amount of microwave irradiation and the amount of air supplied are controlled to heat and dry the powder while stirring; Microwave heating is characterized by a third step in which the supply of new powder is stopped when the amount of powder in the furnace reaches a predetermined amount, and the powder in the furnace is completely burned. Method.
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 JPS60140013A (en) 1985-07-24
JPH0333962B2 true 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)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2554639B2 (en) * 1986-10-31 1996-11-13 株式会社東芝 Kitchen waste incinerator
JPH0810051B2 (en) * 1987-08-31 1996-01-31 松下電器産業株式会社 Garbage disposal

Also Published As

Publication number Publication date
JPS60140013A (en) 1985-07-24

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