JPH0252981A - Microwave drying device for granular body - Google Patents

Microwave drying device for granular body

Info

Publication number
JPH0252981A
JPH0252981A JP20002388A JP20002388A JPH0252981A JP H0252981 A JPH0252981 A JP H0252981A JP 20002388 A JP20002388 A JP 20002388A JP 20002388 A JP20002388 A JP 20002388A JP H0252981 A JPH0252981 A JP H0252981A
Authority
JP
Japan
Prior art keywords
treated
microwave
powder
granular body
granular material
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.)
Pending
Application number
JP20002388A
Other languages
Japanese (ja)
Inventor
Tsuneo Muranaka
恒男 村中
Hirotaka Koyama
博隆 小山
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.)
Toshiba Corp
Original Assignee
Toshiba 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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP20002388A priority Critical patent/JPH0252981A/en
Publication of JPH0252981A publication Critical patent/JPH0252981A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To permit efficient microwave drying of granular body to be treated which is provided with a small microwave loss coefficient by a method wherein a mixer, consisting of microwave absorbing material and mixing the granular body to be treated, is provided in a vessel receiving the granular body to be treated. CONSTITUTION:A mixer or vanes 17, for example, which mixes granular body 10 to be treated, is provided in a vessel 18 while the vanes 17 are constituted of a microwave absorbing material or a material having a large microwave loss coefficient such as the ceramics of SiC, SiN, ferrite material for example. When an electric power source is impressed on a microwave oscillating source 1 to oscillate microwaves and the microwaves are sent into an oven 7 through a waveguide 2 to project them against the granular bodies 10 to be treated and the mixer or the vanes 17, the vanes 17 absorb the microwaves and generate heat. At the same time, the vanes 17 generating heat are driven by a motor 20 to rotate and mix the granular body 10 and, therefore the generated heat is transferred to the granular body 10 and/or contacted directly with the granular body 10 to be treated.

Description

【発明の詳細な説明】 [発明の目的] (産業上の利用分野) この発明は、粉粒体用マイクロ波乾燥装置に関する。[Detailed description of the invention] [Purpose of the invention] (Industrial application field) The present invention relates to a microwave drying device for powder and granular materials.

(従来の技術) 近年、化学工業、薬品製造業、食品工業等の分野や廃棄
物処理の分野等において、物品の保管や処理技術等から
水分を多く含む多量の粉体酸るいは粒状体を成る含水率
以下に乾燥する要求が多くなってきている。
(Prior art) In recent years, in fields such as the chemical industry, drug manufacturing industry, food industry, and waste treatment, large amounts of powder, sour, or granular materials containing a large amount of moisture have been produced due to storage and processing techniques of goods. There is an increasing demand for drying to a moisture content below .

この場合、マイクロ波を利用して乾燥を行なう粉粒体用
マイクロ波乾燥装置が使用されるが、この種の装置の不
連続式処理用のものの例は、従来第5図に示すような構
成となっている。
In this case, a microwave drying device for powder and granular material is used that uses microwaves to dry the material, but an example of this type of device for discontinuous processing has conventionally been constructed as shown in Fig. 5. It becomes.

図中の符号1はマグネトロンやクライストロンのような
マイクロ波発振源、2は導波管、3は空気封止板4を固
定する固定板、5.8はパツキン、6はマイクロ波オー
ブン7内の天井に取付けられた電波攪拌用のスターラフ
アン、9はオーブン7の側面に設けられた開閉自在の扉
、10は容器18内に入れられた被処理粉粒体、11は
真空ポンプ、12は真空計、13は排気管、14はバル
ブ、15はリークバルブである。
In the figure, 1 is a microwave oscillation source such as a magnetron or klystron, 2 is a waveguide, 3 is a fixing plate that fixes the air sealing plate 4, 5.8 is a packing, and 6 is a microwave oscillation source in the microwave oven 7. A stirrer fan for radio stirring is attached to the ceiling, 9 is a door that can be opened and closed on the side of the oven 7, 10 is a powder to be processed placed in a container 18, 11 is a vacuum pump, and 12 is a vacuum In total, 13 is an exhaust pipe, 14 is a valve, and 15 is a leak valve.

このような装置を使用して、被処理粉粒体10を加熱・
乾燥するには、被処理粉粒体10が入っている容器18
をオーブン7内に収容した後、真空ポンプ11を動作さ
せてオーブン7内を減圧し、真空状態にする。
Using such a device, the powder and granular material 10 to be treated is heated and
To dry, the container 18 containing the powder and granular material 10 to be treated is
After placing the oven 7 in the oven 7, the vacuum pump 11 is operated to reduce the pressure inside the oven 7 and create a vacuum state.

その後、リークバルブ15を調節して所定真空度に達し
たら、マイクロ波発振源1からマイクロ波電力を発生さ
せ被処理粉粒体1・0に照射する。例えば、被処理粉粒
体10を40℃にて処理したい場合は、オーブン7内の
真空度を約55Torrに保持するようにリークバルブ
15を調節すれば良い。
Thereafter, when the leak valve 15 is adjusted to reach a predetermined degree of vacuum, microwave power is generated from the microwave oscillation source 1 and irradiated onto the powder and granular material 1.0 to be processed. For example, if it is desired to process the granular material 10 to be processed at 40° C., the leak valve 15 may be adjusted to maintain the degree of vacuum in the oven 7 at approximately 55 Torr.

(発明が解決しようとする課題) ところが、上記のような従来の装置には、尚、次のよう
な改良すべき課題がある。
(Problems to be Solved by the Invention) However, the conventional device as described above still has the following problems to be improved.

(1) 被処理粉粒体10のマイクロ波損失係数が小さ
い場合、被処理粉粒体10自身が殆ど発熱しないため、
目的9温度まで昇温しない。
(1) When the microwave loss coefficient of the powder to be treated 10 is small, the powder to be treated 10 itself hardly generates heat;
Purpose 9 Do not raise the temperature to the temperature.

(2) マイクロ波損失係数が小さい被処理粉粒体10
に含まれる水分を乾燥する場合、水分が10%程度以上
のときは、水分自身がマイクロ波を吸収するため昇温し
で蒸発するが、水分が10%程度以下になると、マイク
ロ波を殆ど吸収しなくなり、乾燥が不十分となる。
(2) Powder to be treated 10 with a small microwave loss coefficient
When drying the water contained in water, if the water content is about 10% or more, the water itself will absorb microwaves and evaporate as the temperature rises, but if the water content is less than 10%, most of the microwaves will be absorbed. This will result in insufficient drying.

尚、連続処理する場合の従来の技術として、特開昭57
−31776号公報記載の発明があるが、上記と同様な
課題を有している。
In addition, as a conventional technique for continuous processing, Japanese Patent Application Laid-Open No. 57
There is an invention described in Japanese Patent No.-31776, but it has the same problem as above.

この発明は、マイクロ波損失係数が小さい被処理粉粒体
を効率良くマイクロ波で乾燥することが出来る粉粒体用
マイクロ波乾燥装置を提供することを目的とする。
An object of the present invention is to provide a microwave drying apparatus for powder and granular materials that can efficiently dry powder and granular materials having a small microwave loss coefficient using microwaves.

[発明の構成] (課題を解決するだめの手段) この発明は、被処理粉粒体が収容される容器内に、マイ
クロ波吸収材からなり被処理粉粒体を攪拌する攪拌器が
設けられてなる粉粒体用マイクロ波乾燥装置である。
[Structure of the Invention] (Means for Solving the Problem) This invention provides a method in which a stirrer made of a microwave absorbing material and for stirring the powder and granular material to be treated is provided in a container in which the powder and granular material to be treated is stored. This is a microwave drying device for powder and granular materials.

(作用) この発明によれば、マイクロ波損失係数の小さい被処理
粉粒体でも、マイクロ波を吸収して発熱する攪拌器にて
加熱され、成るいはそれに接触して水分蒸発させられる
ので、効率良く絶乾状態近くまで乾燥することが出来る
(Function) According to the present invention, even powder particles to be treated with a small microwave loss coefficient can be heated by a stirrer that absorbs microwaves and generates heat, or come into contact with the stirrer to evaporate water. It can be efficiently dried to near absolute dryness.

(実施例) 以下、図面を参照して、この発明の一実施例を詳細に説
明する。
(Example) Hereinafter, an example of the present invention will be described in detail with reference to the drawings.

この発明によるマイクロ波加熱装置は、第1図に示すよ
うに構成され、従来例(第5図)と同一箇所は同一符号
を付すことにする。
The microwave heating device according to the present invention is constructed as shown in FIG. 1, and the same parts as in the conventional example (FIG. 5) are given the same reference numerals.

即ち、円筒状酸るいは直方体状などの形状を有するマイ
クロ波オーブン7の一側面には1.被処理粉粒体10の
出し入れを行なうための扉9が開閉自在に設けられてい
る。又、オーブン7の天井には、オーブン7と導波管2
との間の空気遮断を行なうためのマイクロ波損失の小さ
い誘電体製の空気封止板4、及びこの空気封止板4を固
定するための固定板3が設けられている。尚、扉9とオ
ーブン7との間、及び空気封止板4とオーブン7との間
には、当然、空気漏れがないようにバ・ソキン5.8が
用いられている。
That is, one side of the microwave oven 7 having a cylindrical shape or a rectangular parallelepiped shape has 1. A door 9 is provided which can be opened and closed to take in and take out the granular material 10 to be processed. Moreover, the oven 7 and the waveguide 2 are installed on the ceiling of the oven 7.
An air sealing plate 4 made of a dielectric material with low microwave loss and a fixing plate 3 for fixing the air sealing plate 4 are provided. Incidentally, between the door 9 and the oven 7 and between the air sealing plate 4 and the oven 7, a bar socket 5.8 is naturally used to prevent air leakage.

導波管2の一端には、マイクロ波発振源1が接続されて
おり、このマイクロ波発振源1にて発生したマイクロ波
電力は導波管2を介してオーブン7内に導入され、被処
理粉粒体10及び後述の攪拌器に照射される。
A microwave oscillation source 1 is connected to one end of the waveguide 2, and the microwave power generated by the microwave oscillation source 1 is introduced into the oven 7 via the waveguide 2 and The granular material 10 and a stirrer described below are irradiated.

更に、オーブン7内の底部には支持台1つが設けられ、
この支持台19の上面には被処理粉粒体10が収容され
る容器18が載せられている。この容器18の材質は金
属、誘電体どちらでも良いが、マイクロ波吸収効率を向
上させるには誘電体が良く、更にマイクロ波損失係数の
小さい材質(例えば石英、テフロン、ポリプロピレンな
ど)成るいは大きい材質(例えば5iCSSiNフエラ
イト系材料などのセラミック)のいずれでも良い。
Furthermore, one support stand is provided at the bottom of the oven 7,
A container 18 in which the granular material 10 to be processed is accommodated is placed on the upper surface of the support base 19 . The material of this container 18 may be either metal or dielectric, but in order to improve the microwave absorption efficiency, dielectric is preferable, and it is also made of a material with a small microwave loss coefficient (for example, quartz, Teflon, polypropylene, etc.) or a large material. Any material (for example, ceramic such as 5iCSSiN ferrite material) may be used.

又、容器18内には、被処理粉粒体10を攪拌する攪拌
器例えば羽根17が設けられ、この羽根17はシャフト
16の一端に固着され、このシャフト16の他端はオー
ブン7の天井を貫通して回転装置例えばモータ20に接
続されている。こうして、羽根17はモータ20により
駆動され回転自在になっている。
Further, in the container 18, a stirrer, for example, a blade 17, for stirring the powder and granular material 10 to be processed is provided. It is connected to a rotating device, such as a motor 20, through it. In this way, the blades 17 are driven by the motor 20 and are rotatable.

この羽根17は、マイクロ波吸収材即ちマイクロ波損失
係数の大きい材料、例えば5iC1SLNフエライト系
材料などのセラミックからなっている。
The blade 17 is made of a microwave absorbing material, that is, a material with a large microwave loss coefficient, for example, a ceramic such as a 5iC1SLN ferrite material.

尚、被処理粉粒体10としては、微粉末からビーズ等も
含み、形状も球状物、多角形、円・角柱物、中空物等任
意であり、大きさも0.1μm程度から数cm迄であり
、形や大きさに応じて攪拌器の大きさや形、個数を選定
する。つまり、攪拌器が粉粒体とよく接触するようにす
れば良い。
The powder and granular material 10 to be treated includes anything from fine powder to beads, etc., and can have any shape such as spherical, polygonal, circular/prismatic, hollow, etc., and the size can range from about 0.1 μm to several cm. Yes, the size, shape, and number of stirrers are selected depending on the shape and size. In other words, the stirrer should be in good contact with the granular material.

更に、オーブン7の他の側面には、排気管13及びバル
ブ14を介して真空ポンプ11が接続されている。この
真空ポンプ11は、オーブン7内の空気及び被処理粉粒
体10から発生した蒸気などを排気するためのものであ
る。そして、排気管13には真空計12とリークバルブ
15が接続されているが、真空計12はオーブン7内の
真空度を見るためのものであり、リークバルブ15はオ
ブン7内の真空度を所定の圧力にするためのものである
Furthermore, a vacuum pump 11 is connected to the other side of the oven 7 via an exhaust pipe 13 and a valve 14. This vacuum pump 11 is for exhausting the air in the oven 7 and the steam generated from the granular material 10 to be processed. A vacuum gauge 12 and a leak valve 15 are connected to the exhaust pipe 13. The vacuum gauge 12 is for checking the degree of vacuum inside the oven 7, and the leak valve 15 is for checking the degree of vacuum inside the oven 7. This is to create a predetermined pressure.

さて次に、上記のこの発明の装置を用いて、被処理粉粒
体10の乾燥を行なうには、先ず、被処理粉粒体10を
入れた容器18を、扉9を開けてオーブン7内に収容し
支持台19上に載せる。その後、マイクロ波発振源1に
電源を印加してマイクロ波を発振させ、導波管2を介し
てマイクロ波をオーブン7内へ送り込み被処理粉粒体1
0及び攪拌器である羽根17に照射する。すると、羽根
17がマイクロ波を吸収して発熱する。
Next, in order to dry the granular material 10 to be treated using the apparatus of the present invention, first, the container 18 containing the granular material 10 to be treated is placed in the oven 7 with the door 9 opened. and place it on the support stand 19. Thereafter, power is applied to the microwave oscillation source 1 to oscillate microwaves, and the microwaves are sent into the oven 7 through the waveguide 2 and the powder and granular material to be processed 1
0 and the blade 17, which is a stirrer, are irradiated. Then, the blade 17 absorbs the microwave and generates heat.

同時に、発熱した羽根17はモータ20により駆動され
て回転し被処理粉粒体10を攪拌するので、発熱した熱
が被処理粉粒体10へ伝わり、又、被処理粉粒体10に
直接接触することになる。この結果、被処理粉粒体10
の水分が蒸発させられ、乾燥される。
At the same time, the blades 17 that generate heat are driven by the motor 20 and rotate to agitate the powder and granular material 10 to be treated, so that the generated heat is transmitted to the powder and granular material 10 to be treated, and also comes into direct contact with the powder and granular material 10 to be treated. I will do it. As a result, the powder to be treated 10
The water is evaporated and dried.

尚、これまでの説明は、減圧し沸点を下げて加熱するこ
とで説明してきたが、通常の大気圧でのマイクロ波加熱
に適用しても同等問題ないことは言うまでもない。
In addition, although the explanation so far has been based on heating by reducing the pressure and lowering the boiling point, it goes without saying that the same problem will not arise even if it is applied to microwave heating at normal atmospheric pressure.

(変形例) 第2図乃至第4図はこの発明の変形例を示したもので、
上記実施例と同様効果が得られる。
(Modified Examples) Figures 2 to 4 show modified examples of this invention.
The same effects as in the above embodiment can be obtained.

先ず、第2図の場合は、上記実施例とは逆に羽根17を
固定し、支持台21をモータ22にて駆動することによ
り容器18を回転させるように構成したものである。こ
の場合も、結果的には容器18内の被処理粉粒体10は
発熱する攪拌器により直接攪拌され、加熱・乾燥が行な
われる。
First, in the case of FIG. 2, contrary to the above embodiment, the blade 17 is fixed and the container 18 is rotated by driving the support base 21 with a motor 22. In this case as well, as a result, the granular material 10 to be treated in the container 18 is directly stirred by the heat-generating stirrer, and heated and dried.

又、第3図及び第4図の場合は、被処理粉粒体10を連
続乾燥処理する場合に好適な装置°であり、特に含水率
が20%以上の粉粒体を数%以下まで連続乾燥するのに
好適なものである。即ち、マイクロ波オーブン23内は
少なくとも1個の仕切板24により複数室(例えばA室
、B室)に分けられ、各室A、Bにはそれぞれ天井外側
にマイクロ波発振源1が導波管2を介して接続され、天
井内側にスタラファン6が取付けられている。仕切板2
4は、動作時に水蒸気が左の室に行くのを抑制するため
の役目も果たしている。
In addition, in the case of Fig. 3 and Fig. 4, the apparatus is suitable for continuously drying the powder and granular material 10 to be treated, and in particular, it is suitable for continuously drying the powder and granular material with a moisture content of 20% or more to a few percent or less. It is suitable for drying. That is, the inside of the microwave oven 23 is divided into a plurality of rooms (for example, room A and room B) by at least one partition plate 24, and in each room A and B, the microwave oscillation source 1 is installed outside the ceiling through a waveguide. 2, and a star fan 6 is installed inside the ceiling. Partition plate 2
4 also serves to prevent water vapor from going to the left chamber during operation.

オーブン23内には長尺の誘電体製の断面U字状容器2
5が配設され、この容器25の一端に対応して、被処理
粉粒体10の導入口26がオーブン23の天井を貫通し
て設けられている。図示していないが容器25の他端に
は、被処理粉粒体10の排出口が設けられている。そし
て、容器25内には導入口26から被処理粉粒体10が
入れられるが、更にこの被処理粉粒体10を攪拌するた
めの攪拌器であるスクリュー27a、27bが設けられ
、このスクリュー27a、27bのシャフト28はオー
ブン23の外のモータ29により回転駆動される。
Inside the oven 23 is a long dielectric container 2 with a U-shaped cross section.
5 is disposed, and an inlet 26 for the granular material 10 to be processed is provided penetrating through the ceiling of the oven 23 corresponding to one end of the container 25 . Although not shown, the other end of the container 25 is provided with a discharge port for the granular material 10 to be processed. The powder and granular material 10 to be treated is introduced into the container 25 from the inlet 26, and screws 27a and 27b, which are stirrers for stirring the powder and granular material 10 to be treated, are further provided. , 27b are rotationally driven by a motor 29 outside the oven 23.

この場合、スクリュー27aが位置するA室内では、被
処理粉粒体10は含水率が例えば20%以上と高い段階
なので、マイクロ波により被処理粉粒体10の水分自体
がマイクロ波を吸収して発熱する。従って、スクリュー
27aの材質はマイクロ波を吸収しなくても良く、セラ
ミック又は樹脂などの低損失誘電体からなっている。
In this case, in the chamber A where the screw 27a is located, the powder and granular material 10 to be treated has a high moisture content, for example, 20% or more, so the water content of the granular material 10 to be treated is absorbed by the microwave. I get a fever. Therefore, the material of the screw 27a does not need to absorb microwaves, and is made of a low-loss dielectric such as ceramic or resin.

一方、スクリュー27bが位置するB室内では、被処理
粉粒体10の含水率が低くなっているので、スクリュー
27bの材質はマイクロ波吸収材からなっている。又、
シャフト28は金属酸るいは誘電体からなっている。図
中の30は排気口である。
On the other hand, in the B chamber where the screw 27b is located, the water content of the granular material 10 to be processed is low, so the material of the screw 27b is made of a microwave absorbing material. or,
The shaft 28 is made of metal or dielectric. 30 in the figure is an exhaust port.

被処理粉粒体10の乾燥に当たっては、導入口26から
容器23内に被処理粉粒体10が入れられるが、A室内
では被処理粉粒体10はマイクロ波によりその内部の水
分自体が発熱し、蒸発しながらスクリュー27aの作用
により左方へ移動されていく。そしてB室内では、マイ
クロ波吸収材からなり発熱しているスクリュー27bに
被処理粉粒体10が直接触れて加熱され、又、水分自体
がこのスクリュー27bに触れて蒸発し、乾燥が行われ
る。
When drying the powder and granular material 10 to be treated, the powder and granular material 10 to be treated is put into the container 23 from the inlet 26, but inside the chamber A, the water inside the powder and granular material 10 itself is heated by microwaves. Then, while evaporating, it is moved to the left by the action of the screw 27a. In the B chamber, the granular material 10 to be processed directly comes into contact with a heat-generating screw 27b made of a microwave absorbing material and is heated, and the moisture itself comes into contact with this screw 27b and evaporates, thereby performing drying.

この連続乾燥処理に好適な装置は、第3図及び第4図で
はいわゆる横型であるが、縦型にしても良い。いずれに
しても、この連続乾燥処理装置は処理前の含水率が比較
的高い場合(約20%以上)に好適であり、処理後は数
%成るいは1%以下に出来る。
Although the apparatus suitable for this continuous drying process is of a so-called horizontal type in FIGS. 3 and 4, it may be of a vertical type. In any case, this continuous drying treatment apparatus is suitable when the moisture content before treatment is relatively high (approximately 20% or more), and can be reduced to several percent or 1% or less after treatment.

尚、上記実施例や変形例では攪拌器として羽根17やス
クリュー27a、27bを使用したが、攪拌器はこれら
に限定されることなく、耐熱誘電体(セラミック)の表
面にSiCのようなマイクロ波吸収材の板又は膜等を付
着したものや、その外面に他の保護膜を塗布して被処理
粉粒体1oを汚染しないようにしたものでも良い。
In the above embodiments and modified examples, the blades 17 and the screws 27a, 27b were used as the stirrer, but the stirrer is not limited to these, and the stirrer is not limited to these. It may be one with an absorbent plate or film attached thereto, or one with another protective film applied to its outer surface so as not to contaminate the granular material 1o to be treated.

[発明の効果] 以上説明したようにこの発明によれば、容器内の被処理
粉粒体が、マイクロ波吸収材からなる攪拌器により攪拌
されるので、マイクロ波損失係数の小さい被処理粉粒体
であっても、マイクロ波により加熱される攪拌器に触れ
て水分が蒸発し、乾燥効率が著しく向上する。
[Effects of the Invention] As explained above, according to the present invention, the powder to be treated in the container is stirred by the stirrer made of a microwave absorbing material, so that the powder to be treated has a small microwave loss coefficient. Even when drying a drying body, moisture evaporates when it comes into contact with a stirrer heated by microwaves, significantly improving drying efficiency.

この結果、殆ど成るいは全くマイクロ波を吸収しない被
処理粉粒体でも、はぼ絶乾近くまで乾燥させることが出
来る。そして、攪拌器自体が発熱材であるので、余分の
部品を要せず、比較的簡単に装置を構成出来る。
As a result, even powder particles to be treated that absorb little or no microwaves can be dried to near absolute dryness. Furthermore, since the stirrer itself is a heat generating material, no extra parts are required and the apparatus can be constructed relatively easily.

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

第1図はこの発明の一実施例に係る粉粒体用マイクロ波
乾燥装置を示す断面図、第2図及び第3図はこの発明の
変形例を示す断面図、第4図は第3図のイーイ′線に沿
って切断し矢印方向に見た断面図、第5図は従来の粉粒
体用マイクロ波乾燥装置を示す断面図である。 1・・・マイクロ波発振源、7・・・マイクロ波オーブ
ン、10−”被処理粉粒体、17.27a、27b・・
・攪拌器、18.23・・・容器。 出願人代理人 弁理士 鈴江武彦 第1図 第 図
FIG. 1 is a cross-sectional view showing a microwave drying device for powder and granular materials according to an embodiment of the present invention, FIGS. 2 and 3 are cross-sectional views showing modified examples of the present invention, and FIG. FIG. 5 is a sectional view showing a conventional microwave drying apparatus for powder and granular materials. DESCRIPTION OF SYMBOLS 1... Microwave oscillation source, 7... Microwave oven, 10-" Powder to be processed, 17.27a, 27b...
- Stirrer, 18.23... Container. Applicant's agent Patent attorney Takehiko Suzue Figure 1

Claims (1)

【特許請求の範囲】[Claims] マイクロ波発振源と、このマイクロ波発振源が接続され
たマイクロ波オーブンと、このオーブン内に配置され被
処理粉粒体が収容される容器とを具備する粉粒体用マイ
クロ波乾燥装置において、上記容器内に、マイクロ波吸
収材からなり上記被処理粉粒体を攪拌する攪拌器が設け
られてなることを特徴とする粉粒体用マイクロ波乾燥装
置。
A microwave drying device for powder and granular material, comprising a microwave oscillation source, a microwave oven connected to the microwave oscillation source, and a container disposed within the oven and containing the powder and granular material to be treated, A microwave drying apparatus for powder or granular material, characterized in that a stirrer made of a microwave absorbing material and for stirring the powder or granular material to be treated is provided in the container.
JP20002388A 1988-08-12 1988-08-12 Microwave drying device for granular body Pending JPH0252981A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20002388A JPH0252981A (en) 1988-08-12 1988-08-12 Microwave drying device for granular body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20002388A JPH0252981A (en) 1988-08-12 1988-08-12 Microwave drying device for granular body

Publications (1)

Publication Number Publication Date
JPH0252981A true JPH0252981A (en) 1990-02-22

Family

ID=16417527

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20002388A Pending JPH0252981A (en) 1988-08-12 1988-08-12 Microwave drying device for granular body

Country Status (1)

Country Link
JP (1) JPH0252981A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005103355A (en) * 2003-09-29 2005-04-21 Sanyo Electric Co Ltd Garbage treatment apparatus
JP4875146B2 (en) * 2006-04-21 2012-02-15 ベアルン・イノヴァシオン−ドゥディユー・ベルナール Sludge drying method and apparatus for carrying out the method
JP2018013278A (en) * 2016-07-20 2018-01-25 ヤマト科学株式会社 Containment apparatus
CN113634210A (en) * 2021-07-01 2021-11-12 江苏大学 Microwave hydrothermal treatment device and method for organic wastes

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005103355A (en) * 2003-09-29 2005-04-21 Sanyo Electric Co Ltd Garbage treatment apparatus
JP4875146B2 (en) * 2006-04-21 2012-02-15 ベアルン・イノヴァシオン−ドゥディユー・ベルナール Sludge drying method and apparatus for carrying out the method
KR101394623B1 (en) * 2006-04-21 2014-05-13 베아른 이노바씨옹 - 드디으 베르나르 Method of drying sludge and device for implementing the method
JP2018013278A (en) * 2016-07-20 2018-01-25 ヤマト科学株式会社 Containment apparatus
CN113634210A (en) * 2021-07-01 2021-11-12 江苏大学 Microwave hydrothermal treatment device and method for organic wastes

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