JPS60205169A - Continuous treater for drying, etc. - Google Patents

Continuous treater for drying, etc.

Info

Publication number
JPS60205169A
JPS60205169A JP6188684A JP6188684A JPS60205169A JP S60205169 A JPS60205169 A JP S60205169A JP 6188684 A JP6188684 A JP 6188684A JP 6188684 A JP6188684 A JP 6188684A JP S60205169 A JPS60205169 A JP S60205169A
Authority
JP
Japan
Prior art keywords
cylindrical body
vertical cylindrical
screw
drying
microwave
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
JP6188684A
Other languages
Japanese (ja)
Other versions
JPH0123712B2 (en
Inventor
石浜 純
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.)
Niigata Engineering Co Ltd
Original Assignee
Niigata Engineering 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 Niigata Engineering Co Ltd filed Critical Niigata Engineering Co Ltd
Priority to JP6188684A priority Critical patent/JPS60205169A/en
Publication of JPS60205169A publication Critical patent/JPS60205169A/en
Publication of JPH0123712B2 publication Critical patent/JPH0123712B2/ja
Granted legal-status Critical Current

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  • Drying Of Solid Materials (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は、放射性廃棄物のような有害物質を含む含水物
の乾燥処理等に好適な乾燥等の連続処理装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a continuous processing apparatus for drying, etc. suitable for drying water-containing materials containing harmful substances such as radioactive waste.

放射性廃棄物を含む濃縮廃液、スラツジ、汚泥等、有害
物質を含む含水物を減容し、安定な同化体とするために
、含水物の濃縮、脱水、乾燥、焼却、溶融、固化等の処
理技術の研究開発が近年盛んに行なわれ、一部は既に実
用に供さj、ている。
Treatment of hydrated materials such as concentration, dehydration, drying, incineration, melting, solidification, etc. in order to reduce the volume of hydrated materials containing harmful substances, such as concentrated waste liquids containing radioactive waste, sludge, and sludge, and make them into stable assimilated substances. Research and development of technology has been actively conducted in recent years, and some of it has already been put into practical use.

ところで、上記のような有害物質を含む含水物を脱水乾
燥する場合、非揮発性の有害物質がダストとして飛散し
て排ガス中に混入するのを極力防止することが望咬しい
。ところが、含水物の脱水乾燥に一般的に使用される薄
膜乾燥機、ロータリキルン等の連続式処理装置では、装
置n内において含水物の攪拌を伴うため、乾燥ダストの
飛散が避けられず、ダストの排ガス中への混入を防止で
きない。このため、排ガス処理装置に、このダストの分
離捕集装置を付設する必要があった。また、回分式の処
理#cmとして真空凍結乾燥機、外熱式撹拌槽があるが
、前者は表面積を多くしなけfLはならない上、乾燥物
の移動、移し替えの際にそれらが飛散するおそれがあシ
、後者では、上記連続式処理装置同様、攪拌によるダス
ト飛散が問題となる。
By the way, when dehydrating and drying a water-containing material containing harmful substances as described above, it is desirable to prevent non-volatile harmful substances from scattering as dust and mixing into exhaust gas as much as possible. However, in continuous processing equipment such as thin film dryers and rotary kilns that are commonly used for dehydration and drying of water-containing materials, since the water-containing materials are stirred within the equipment, the scattering of dry dust is unavoidable. cannot prevent the mixture from entering the exhaust gas. Therefore, it was necessary to attach a separation and collection device for this dust to the exhaust gas treatment device. In addition, there are vacuum freeze dryers and externally heated stirring tanks for batch-type processing #cm, but the former requires a large surface area and does not have a high fL, and there is a risk that the dried materials will scatter when moving or transferring. However, in the latter case, dust scattering due to stirring becomes a problem, similar to the above-mentioned continuous processing apparatus.

そこで、上記従来の一般的な処理装置に代るものとして
、例えば、第り図に示すようが同軸型マイクロ波乾燥装
置が案出さ九ている。この乾燥装置は、金属製の円筒体
1と、誘電体で形成さnたスクリュー翼2を備えた回転
軸3から成シ、マイクロ波導入口4から円筒体l内にマ
イクロ波を導いて投入口5から投入された含水物な誘電
加熱処理し、排出口6から乾燥物として排出するもので
ある。
Therefore, as an alternative to the conventional general processing apparatus described above, for example, a coaxial microwave drying apparatus as shown in FIG. 2 has been devised. This drying device consists of a metal cylindrical body 1 and a rotating shaft 3 equipped with a screw blade 2 formed of a dielectric material, and the microwave is guided into the cylindrical body from a microwave inlet 4 to an input port. The water-containing material introduced from 5 is dielectrically heated and discharged from an outlet 6 as a dry material.

しかしながら、上記のような回転軸の軸線方向と同じ方
向にマイクロ波があたるいわゆる同軸型マイクロ波加熱
処理装置では、含水物の移動経路における位置によって
、マイクロ波電力の強さあるいは加熱温度を最適に制御
することが訃しく、加熱効率が悪いという問題があった
However, in the so-called coaxial microwave heat treatment equipment where microwaves are applied in the same direction as the axial direction of the rotating shaft, the strength of the microwave power or the heating temperature cannot be optimized depending on the position in the movement path of the water-containing material. There were problems in that it was difficult to control and the heating efficiency was poor.

本発明は、上記従来の事情に鑑みてなされたもので、マ
イクロ波によシ効率よく加熱処理するととができ、しか
も、加熱温度の制御等を容易になすことのできる乾燥等
の連続処理装置を提供することを目的とする。
The present invention has been made in view of the above-mentioned conventional circumstances, and is a continuous processing device for drying, etc., which can efficiently perform heat treatment using microwaves and can easily control the heating temperature. The purpose is to provide

上記目的を達成するために、本発明は、誘電体で形成さ
れた竪形円筒体をマイクロ波オーブン内罠配設し、との
竪形円筒体に、スクリュー翼を備え、駆動装置によシ回
転される回転軸を、その軸線な竪形円筒体の軸線に一致
させて設は九もので、竪形円筒体内をスクリュー翼によ
って移送される被処理物を、該円筒体の壁面を透過して
照射されるマイクロ波により効率よく加熱するようにし
たものである。
In order to achieve the above object, the present invention disposes a vertical cylindrical body made of a dielectric material in a trap in a microwave oven, and equips the vertical cylindrical body with a screw blade, which is driven by a drive device. There are nine ways to set the axis of rotation to coincide with the axis of the vertical cylindrical body, so that the workpiece transferred by the screw blade inside the vertical cylindrical body is transmitted through the wall surface of the cylindrical body. It is designed to heat efficiently using microwave irradiation.

以下、本発明の一実施例を第1図に基づいて説明する。An embodiment of the present invention will be described below with reference to FIG.

第1図において符号10で示すものはマイクロ波オーブ
ンである。このマイクロ波オーブン10は、金属によ環
形成さnた例えば円筒状の胴板11の上部と下部に、金
屑製の上蓋12と下蓋13が該上部と下部の開口なそ九
ぞれ閉塞して設けられて成るもので、その上蓋12と下
!13は、端部にねじ部が形成された複数の連結棒14
の上下端を該上蓋12と下蓋13の貫通孔に押通し、そ
の端部からナツトを螺着することによシ、互いに連結固
定され、かつ、胴板11の所定位置には、金属製の導波
管15の一端が接続され、との導波管15の他端にマイ
クロ波発振装置16が設けられている。
The reference numeral 10 in FIG. 1 is a microwave oven. This microwave oven 10 has an upper and a lower cover 12 and a lower cover 13 made of scrap metal, respectively, at the upper and lower parts of a body plate 11 formed of a metal ring and having a cylindrical shape, respectively. It is closed and is provided with an upper lid 12 and a lower! 13 is a plurality of connecting rods 14 each having a threaded end formed therein;
are connected and fixed to each other by pushing the upper and lower ends into the through holes of the upper cover 12 and lower cover 13 and screwing nuts from the ends, and metal One end of the waveguide 15 is connected to the other end of the waveguide 15, and a microwave oscillation device 16 is provided at the other end of the waveguide 15.

さらに、上記マイクロ波オーブン10内には、胴&11
よυ小径でセラミック、ガラス、テフロン等の誘電体で
形成された竪形円筒体17が、その軸線を該オーブン1
0の軸線に一致させて配設されておシ、この竪形円筒体
17もその上下か上記上蓋12と下蓋13によりそれぞ
れ閉塞されている。また、この竪形円筒体17の側壁の
下方位置Kl:l:、不活性ガスを該竪形円筒体17の
内部に供給するガス供給管18が接続される一方、上記
上蓋12には、有害物質を含む含水物等の被処理物を竪
形円筒体17内に供給する被処理物供給管19と、竪形
円筒体17内のガスを排出するためのガス排出管20が
それぞれ設けらnlかつ、上記下蓋13には、竪形円筒
体17内の処理物を装置外に排出する処理物排出管21
が接続さnている。そして、上記被処理物供給管19に
は、一端に被処理物を受け入nるホッパ22か設けらf
lたスクリューフィーダ23の他端が接続さ九るととも
に、上記ガス排出管20は凝縮器24に接続されている
。また、上記被処理物供給管19、処理物排出管21、
ガス供給管18、ガス排出管20はいずnもマイクロ波
に対してカットオフとなる大きさに形成されている1、 一方、上記竪形円筒体17の中心には、金属もしくは誘
電体により形成された回転軸25が、その軸線な竪形円
筒体17の軸線に一致させて配設さnている。この回転
軸25は、上記上蓋12と下蓋13とを貫通して図示し
ない軸受によって該上蓋12と下蓋13に回転自在に支
承されており、その上端には駆動モータ等の駆動装置2
6が連結さnている。また、この回転軸25には、セラ
ミック等の誘電体で形成さtl、たスクリュ−翼取シ付
けらnている。このスクリューR27は、その内縁27
aが回転軸25の外周面に固定され、その外縁27bが
竪形円筒体17の内周面に近接して位置する螺旋状のも
ので、その上面の螺旋面は外縁27b(pHが内縁27
a側より下方になるように傾斜している。
Furthermore, inside the microwave oven 10, there is a body &11.
A vertical cylindrical body 17 having a small diameter and made of a dielectric material such as ceramic, glass, or Teflon has its axis aligned with the oven 1.
This vertical cylindrical body 17 is also closed at the top and bottom by the upper cover 12 and lower cover 13, respectively. Further, at a lower position Kl:l: of the side wall of this vertical cylindrical body 17, a gas supply pipe 18 for supplying an inert gas into the inside of this vertical cylindrical body 17 is connected, while a harmful A workpiece supply pipe 19 for supplying a workpiece such as a water-containing substance containing a substance into the vertical cylindrical body 17 and a gas discharge pipe 20 for discharging the gas inside the vertical cylinder 17 are provided, respectively. In addition, the lower lid 13 is provided with a processed material discharge pipe 21 for discharging the processed material inside the vertical cylindrical body 17 to the outside of the apparatus.
is connected. The to-be-processed material supply pipe 19 is provided with a hopper 22 at one end for receiving the to-be-processed material.
The other end of the screw feeder 23 is connected, and the gas discharge pipe 20 is connected to a condenser 24. In addition, the above-mentioned processing material supply pipe 19, processing material discharge pipe 21,
The gas supply pipe 18 and the gas discharge pipe 20 are both formed to a size that cuts off microwaves 1. On the other hand, in the center of the vertical cylinder 17, there is a pipe formed of metal or dielectric material. A rotary shaft 25 is arranged so as to coincide with the axis of the vertical cylindrical body 17. The rotating shaft 25 passes through the upper lid 12 and the lower lid 13 and is rotatably supported by the upper lid 12 and the lower lid 13 by bearings (not shown).
6 is connected n. The rotary shaft 25 also has a screw blade holder made of a dielectric material such as ceramic. This screw R27 has an inner edge 27
a is fixed to the outer circumferential surface of the rotating shaft 25, and its outer edge 27b is located close to the inner circumferential surface of the vertical cylindrical body 17.
It is inclined downward from the a side.

なお、図中28は、導波管15から送られてくるマイク
ロ波を竪形円筒体17内に均等に分布させる金属製の分
配板であ〃、また、40は処理物を処理物排出管21に
導くスクレパであシ、29は排出バルブである。
In the figure, 28 is a metal distribution plate that evenly distributes the microwaves sent from the waveguide 15 within the vertical cylindrical body 17, and 40 is a metal distribution plate that distributes the processed material through the processed material discharge pipe. 21 is a scraper leading to the opening, and 29 is a discharge valve.

しかして、上記連続処理装置zにおいて、有害物質を含
む含水物等の被処理物を乾燥処理する場合は、まず、駆
動装置26を作動して回転軸25を回転させ、スクリュ
ー翼27を回転させる。次rで、ガス供給管18から不
活性ガスを竪形円筒体17内に供給するとともに、マイ
クロ波発振装置16を作動してマイクロ波を発振させ、
このマイクロ波を導波管15からマイクロ波オープンl
O内に導く。そして、スクリューフィーダ23を作動し
て、ホッパ22内に貯溜された被処理物を被処理物供給
管19から竪形円筒体17内に連続的に投入し、゛また
、排出バルブ29を所定のタイミングで開状態にする。
Therefore, in the continuous processing apparatus z, when drying a material to be processed such as a water-containing material containing harmful substances, first, the drive device 26 is activated to rotate the rotating shaft 25 and the screw blade 27 is rotated. . In the next step r, an inert gas is supplied from the gas supply pipe 18 into the vertical cylindrical body 17, and the microwave oscillation device 16 is activated to oscillate microwaves.
The microwave is opened from the waveguide 15.
Lead into O. Then, the screw feeder 23 is operated to continuously feed the processed material stored in the hopper 22 from the processed material supply pipe 19 into the vertical cylindrical body 17. Open at the right time.

すると、被処理物は、スクリュー翼27の上面の螺旋面
上に落下し、その傾斜と重力によって竪形円筒体17の
内周面側に移動せしめらnて該内周面に接しながら回動
し、次第に下方に移送される。マイクロ波オーブンIO
内に入ったマイクロ波は、誘電体で形成された竪形円筒
体17の@壁を透過してこの被処理物に直接吸収さnl
これによル、被処理物は、下方に移送されるにつれて徐
々に乾燥加熱され、所定の含水率の処理物となって処理
物排出121から連続的に排出される。また、被処理物
の乾燥加熱により生じた水蒸気は、同伴ガスとともにガ
ス排出管20から凝縮器24に導かnて冷却され、凝縮
分離される。
Then, the object to be processed falls onto the helical surface of the upper surface of the screw blade 27, and due to its inclination and gravity, is moved toward the inner peripheral surface of the vertical cylindrical body 17, and rotates while contacting the inner peripheral surface. and is gradually transported downward. microwave oven io
The microwaves that have entered the interior are transmitted through the wall of the vertical cylindrical body 17 made of dielectric material and are directly absorbed by the object to be treated.
As a result, the material to be treated is gradually dried and heated as it is transferred downward, and is continuously discharged from the material discharge 121 as a material having a predetermined moisture content. Further, the water vapor generated by drying and heating the object to be treated is guided along with the accompanying gas from the gas exhaust pipe 20 to the condenser 24, where it is cooled and condensed and separated.

ここで、上記連続処理装置にあっては、スクリューJi
!27の上に落下した被処理物は、比較的攪拌されるこ
となく下方に移送されるから、乾燥した被処理物がダス
トとして飛散することが少ない。
Here, in the above-mentioned continuous processing apparatus, the screw Ji
! Since the object to be processed that has fallen onto the 27 is transferred downward without being stirred relatively, the dried object to be processed is less likely to be scattered as dust.

また、マイクロ波は、誘電体で形成された竪形円筒体1
7の内部に、そのfi11壁の略全面から該側壁を透過
して入シ、誘電体で形成さ:nたスクリュー翼27も透
過するから、該スクリュー翼27の上面に乗って移送さ
れる被処理物は、その全周からマイクロ波を受けること
ができる。しかも、スクリュー翼27は竪形となってい
るため、従来の横形のスクリュー翼の場合に比べ、被処
理物の自由表面積ははるかに大きい。さらに、マイクロ
波は、被処理物に吸収さ九ると次第に減衰するものであ
シ、その浸透深さには限庭があるが、上記スクリューR
27の上面に乗った被処理物の層厚は比較的マイクロ波
が弱くなる回転軸25に近い部位程、薄くなっており、
層の中心にまでマイクロ波が浸透する。1.たがって、
被処理物の乾燥加熱効率は極めてよく、加熱温度の制御
等も容易となる。
Furthermore, microwaves are transmitted through a vertical cylindrical body 1 made of dielectric material.
The screw blade 27 formed of a dielectric material enters the inside of the fi 11 wall from almost the entire surface of the wall through the side wall thereof, and the screw blade 27 formed of a dielectric material also penetrates therethrough. The object to be treated can receive microwaves from its entire circumference. Furthermore, since the screw blades 27 are vertical, the free surface area of the workpiece is much larger than in the case of conventional horizontal screw blades. Furthermore, microwaves gradually attenuate once they are absorbed by the object to be treated, and there is a limit to the depth of their penetration;
The thickness of the layer of the object placed on the upper surface of 27 becomes thinner in areas closer to the rotating shaft 25, where the microwaves are relatively weaker.
Microwaves penetrate to the center of the layer. 1. Therefore,
The efficiency of drying and heating the object to be processed is extremely high, and the heating temperature can be easily controlled.

また、上記連続処理装置では、スクリュー翼27の回転
速度を変えることによって被処理物の竪形円筒体17内
における滞留時間を自由に調整することができる。、さ
らに、スクリューR27の上面の螺旋面は、その外縁2
7bが内縁27&より下方になるように傾斜せしめら九
でいるので、傾斜しそいないスクリュー翼では大きなピ
ンチにしないと落下しない被処理物も、小さなピッチで
落下させることができ、装置を小型化することができる
。装置の気密性の保持も容易である。ところで、上記に
おいて、スクリュー翼27は等ピッチで単一のものとし
た。しかし、被処理物の物性は、取シ扱うものによって
種々変化し1また乾燥加熱さnる過程においても、含水
率が減少するにつれて変化する。したがって、これに対
応するためにスクリュー翼27は種々の形状のものが用
いられる1、L2図は、スクリュー翼27の下方側のピ
ッチPIを上方側のピッチP2より小さくしたものであ
る。こ九は、スクリューR27の上方側においてtit
被処理物は含水量が多く流れが悪いが、スクリュー翼2
7の下方側では含水量が減少して流下速度が早くなシ、
ダストが発生するおそれがでてくるため、これを防止し
たものである。なお、このスクリュー1R270牛径方
向の傾きθけ、水平に対してj’〜1700が好ましい
。同様な目的で、第3図に示すように、スクリュー14
27の上段部分27cを傾斜形とし、下段部分27dを
水平形としてもよい。
Furthermore, in the continuous processing apparatus described above, by changing the rotational speed of the screw blades 27, the residence time of the object to be processed within the vertical cylindrical body 17 can be freely adjusted. , furthermore, the spiral surface of the upper surface of the screw R27 is
Since 7b is inclined so that it is below the inner edge 27&, even the objects to be processed, which would not fall without a large pinch with the screw blades that tend to incline, can be dropped at a small pitch, making the apparatus more compact. be able to. It is also easy to maintain the airtightness of the device. Incidentally, in the above description, the screw blades 27 are single and have equal pitches. However, the physical properties of the material to be treated vary depending on the material being handled, and also change as the moisture content decreases during the process of drying and heating. Therefore, in order to cope with this, screw blades 27 of various shapes are used. In Figures 1 and L2, the pitch PI on the lower side of the screw blades 27 is smaller than the pitch P2 on the upper side. This is the tit on the upper side of screw R27.
The material to be processed has a high water content and has poor flow, but the screw blade 2
7, the water content decreases and the flow rate becomes faster.
This is to prevent dust from being generated. Incidentally, the inclination θ of this screw 1R270 in the radial direction is preferably j' to 1700 with respect to the horizontal. For the same purpose, as shown in FIG.
The upper part 27c of 27 may be inclined, and the lower part 27d may be horizontal.

第≠図は、複数のスクリュー翼27を、その間にスペー
サ30を介在させて回転軸25に取シ付り−たものであ
る。この場合、被処理物の物性および乾燥加熱過程にお
けるその物性の変化に応じて上記のように水平形のスク
リュー翼と組み合わせたり、ピッチや長さ等を適宜選ぶ
と、被処理物は各スクリュー翼27上では比較的攪拌さ
れずに下方に移送されるか、スペーサ30が介在する不
連続部分ではダストの飛散が生じない程度に落下攪拌さ
j、ることになり、乾燥効率が高まる。第5図は、スク
リュー′!A27の外縁27bK複数のビャス31を設
けたものである。この各ピース31は、スクリューR2
7の半径方向に延びる複数の長孔31aを有するもので
、スクリュー翼27の外縁27bに核外@27bを貫通
して螺着された複数のポル)32aを、該長孔31aに
通し、これにナンド32bを螺合せしめることによ〕、
スクリュー翼27に係止されておシ、そのスクリュー翼
270半径方向への移動は自在となっている。このため
、ピース31は自重により竪形円筒体17の内周面に当
接して回動する。したがって、被処理物がスクリューR
27と島形円筒体17の内周面との間より落下すること
がなく、竪形円筒体17における被処理物のショートバ
スが防止さハるまた、このピース31を取υ付けること
により、スクリュー翼27全体の外径は自動的に竪形円
筒体17の内径に略一致するようKなるため、スクリュ
ーR27の外周を精密に加工する必要がなく、その製作
が極めて容易となる なお、ボルト32aとナンド32
bによってピース31を適当な位置に固定して竪形円筒
体17の内周面とスクリューR27との間隙を調整して
もよい。
In the figure, a plurality of screw blades 27 are mounted on a rotating shaft 25 with a spacer 30 interposed between them. In this case, depending on the physical properties of the workpiece and changes in its physical properties during the drying and heating process, the workpiece can be combined with horizontal screw blades as described above, or the pitch and length can be appropriately selected. 27, the dust is transferred downward without being stirred relatively, or in the discontinuous portion where the spacer 30 is interposed, the dust is dropped and stirred to the extent that dust does not scatter, thereby increasing drying efficiency. Figure 5 shows the screw'! A plurality of vias 31 are provided on the outer edge 27bK of A27. Each piece 31 has a screw R2
7 has a plurality of long holes 31a extending in the radial direction, and a plurality of holes 32a screwed to the outer edge 27b of the screw blade 27 by penetrating the outer core 27b are passed through the long holes 31a. By screwing the Nand 32b onto the
It is locked to the screw blade 27 and can freely move in the radial direction of the screw blade 270. Therefore, the piece 31 comes into contact with the inner peripheral surface of the vertical cylindrical body 17 and rotates due to its own weight. Therefore, the workpiece is screw R
27 and the inner peripheral surface of the island-shaped cylindrical body 17, and a short bath of the processed material in the vertical cylindrical body 17 is prevented.Furthermore, by attaching this piece 31, Since the outer diameter of the entire screw blade 27 automatically becomes approximately equal to the inner diameter of the vertical cylindrical body 17, there is no need to precisely process the outer periphery of the screw R27, making it extremely easy to manufacture. 32a and Nando 32
b may be used to fix the piece 31 at an appropriate position and adjust the gap between the inner circumferential surface of the vertical cylinder 17 and the screw R27.

一方、第7図の実施例では、マイクロ波オーブン10内
に分配板28を設けてマイクロ波の均等な伝播を図った
が、この分配板28の代シに1適当な駆動源によって回
転させら九る翼を設けてもよい。また、被処理物の含水
率が高いスクリューfA27の上段位置においては、被
処理物の局部加熱が生じゃすい逅、このような位置に照
射されるマイクロ波を、例えば、竪形円筒体17の側壁
外面から適当な間隔を隔てて配設した金属製の遮蔽体に
より減じて、この局部加熱を防いでもよい。
On the other hand, in the embodiment shown in FIG. 7, a distribution plate 28 is provided in the microwave oven 10 to ensure uniform propagation of microwaves. You may also provide nine wings. In addition, in the upper position of the screw fA27 where the moisture content of the workpiece is high, local heating of the workpiece may occur. This localized heating may be prevented by reducing it with a metal shield disposed at an appropriate distance from the outer surface of the sidewall.

さらに、W、を図に示すように、マイクロ波オープンI
O内に複数の竪形円筒体17を並列に配設し、との谷竪
形円筒体17間にスクリューコンベヤ33を設けるとと
もに、各竪形円筒体17に、スクリューlR27を備え
、駆動装置26により回転さnる回転軸25を設け、こ
れによシ被処理物の処理効率を高めてもよいし、また、
各竪形円筒体17を多孔質の誘電体によシ形叙し、ブロ
アもしくは真空ポンプ等の減圧装[34によりマイクロ
波オーブン10内を竪形円筒体17内よシ負圧にし、こ
れにより、乾燥加熱によって生じた水蒸気や分解ガス等
を竪形円筒体17の側壁から取〕出すようにすることも
できる。
Furthermore, W, as shown in the figure, microwave open I
A plurality of vertical cylindrical bodies 17 are arranged in parallel in O, a screw conveyor 33 is provided between the valley vertical cylindrical bodies 17, and each vertical cylindrical body 17 is provided with a screw lR27, and a drive device 26 A rotating shaft 25 may be provided to be rotated by a rotating shaft 25, thereby increasing the processing efficiency of the object to be processed.
Each vertical cylindrical body 17 is formed with a porous dielectric material, and the inside of the microwave oven 10 is made to have a negative pressure inside the vertical cylindrical body 17 using a pressure reducing device such as a blower or a vacuum pump. It is also possible to extract water vapor, decomposition gas, etc. generated by dry heating from the side wall of the vertical cylindrical body 17.

また、第7図は、複数のマイクロ波オーブン10を上下
に重ねて連設し、その中に上述の竪形円筒体17を配設
するととも゛に、各マイクロ波オーブン10間の境界部
IQaに対応した位置にあるスクリュー1&27の部位
27eの下面に、金属部材35を設けたものでア〕、各
マイクロ波オーブン10にはそれぞれマイクロ波発振装
置16が設けられ、また、この各マイクロ波発振装置1
6には温度コントローラ36が設けられている。そして
、この各温度コントローラ36によって、各マイクロ波
発振装置16で発生される各マイクロ波のΔ力電力を制
御し、各マイクロ波オーブン10での加熱温度を最適に
制御することができるようになっている。したがって、
神処坪物の物性は、その乾燥加熱過程において含水率が
低くなるにつれて変化するが、この変化に応じて各マイ
クロ波オーブン10での加熱温度を最適に調整すること
ができ、損失電力を最小限に押えることができる。なお
、ここで、各マイクロ波オーブン10間の境界部10a
は、金属によシ形成されている。i、fc1境界部10
aに対応した位置にあるスクリュー翼27の部位27e
の回転軸25t:i金属製が好ましいが、軸径がマイク
ロ波に対してカットオフとなる大きさでちれに、特に金
属製にする必要はない。
Further, FIG. 7 shows a plurality of microwave ovens 10 stacked one on top of the other, the above-mentioned vertical cylindrical body 17 being disposed therein, and a boundary portion IQa between each microwave oven 10. A metal member 35 is provided on the lower surface of the portion 27e of the screws 1 & 27 at positions corresponding to Device 1
6 is provided with a temperature controller 36. Each temperature controller 36 can control the Δ power of each microwave generated by each microwave oscillation device 16, and can optimally control the heating temperature in each microwave oven 10. ing. therefore,
The physical properties of Kamidokoro Tsubomono change as the moisture content decreases during the drying and heating process, but the heating temperature in each microwave oven 10 can be optimally adjusted according to this change, minimizing power loss. It can be held to a limit. In addition, here, the boundary part 10a between each microwave oven 10
is made of metal. i, fc1 boundary part 10
Part 27e of the screw blade 27 located at the position corresponding to a
Rotating shaft 25t: i is preferably made of metal, but it is not particularly necessary to make it metal as long as the shaft diameter is large enough to cut off microwaves.

さらに、境界部10aに対応した位置におるスクリュー
翼27の部位27eの上面に金属部材35を設けてもよ
い。この部分のピンチはマイクロ波に対してカットオフ
となるようにするのが好ましいが、マイクロ波が多少漏
nても支障Ifiないので、必ずしもそのようにする必
要はない。
Furthermore, a metal member 35 may be provided on the upper surface of the portion 27e of the screw blade 27 at a position corresponding to the boundary portion 10a. It is preferable that the pinch in this portion is a cutoff for microwaves, but it is not necessarily necessary to do so because even if some microwaves leak, there is no problem Ifi.

第r図は回転軸25を金属製とし、また、境界部10a
に対応し走位置に、金属製の短いスクリューR27fを
、回転軸25の略全長に亘って設けられた誘電体製のス
クリュー翼27gとは別個に設けたものである。ここで
、図中37はストッパ部材である。
In FIG. r, the rotating shaft 25 is made of metal, and the boundary portion 10a
A short metal screw R27f is provided at a running position corresponding to the rotary shaft 25, separately from a dielectric screw blade 27g provided over substantially the entire length of the rotating shaft 25. Here, 37 in the figure is a stopper member.

さらに1上記装置は、これらを耐熱鋼等によって形成す
ると共にガス供給管18に供給するガス体を適宜選択す
るなどKよシl留、焼却、触媒再生等の燃焼装置として
使用することができ、また被処理物の代りに触媒を用い
竪形円筒体17内に、ゼ;反応流体を流通するようにし
て移動層触媒反応装置としても使用できる。この場合、
処理温度によシ適当な誘電体を選択する必要があること
は熱論である。
Furthermore, the above device can be used as a combustion device for sludge distillation, incineration, catalyst regeneration, etc. by making them of heat-resistant steel or the like and selecting an appropriate gas body to be supplied to the gas supply pipe 18. Furthermore, it can also be used as a moving bed catalytic reaction device by using a catalyst instead of the object to be treated and allowing a reaction fluid to flow through the vertical cylindrical body 17. in this case,
It is a thermal theory that it is necessary to select an appropriate dielectric material depending on the processing temperature.

以上説明したように、本発明の乾燥等の連続処理装置に
あっては、有害物質を含む含水物等の被処理物をスクリ
ューgK上って移動させながらマイクロ波によシ加熱処
理するので、被処理物がダストとなって飛散することが
少ない。また、マイクロ波は、誘電体で形成された竪形
円筒体の内部に、その側壁の略全面から該側壁を透過し
て入るから、被処理物はその全周からマイクロ波を受け
ることができ、しかも、スクリュー翼Fi軸線を上下に
向けて配設されているから、被処理物の自由表面積は大
きい上、その層厚は、薄くなる。したがって、被処理物
の加熱効$は極めてよく、加熱温度の制御郷も容易であ
る。さらに、装置の滞留時間のy4整、小型化、気密性
の保持等も容易にできる。
As explained above, in the continuous processing apparatus for drying, etc. of the present invention, the material to be processed, such as a water-containing material containing harmful substances, is heated by microwaves while being moved up the screw gK. The processed material is less likely to become dust and scatter. Furthermore, since the microwaves enter the inside of the vertical cylinder made of dielectric material by passing through the sidewalls from almost the entire surface of the sidewalls, the object to be processed can receive the microwaves from the entire circumference. Moreover, since the screw blades Fi are disposed with their axes directed upward and downward, the free surface area of the workpiece is large and its layer thickness is thin. Therefore, the heating efficiency of the object to be processed is extremely good, and the heating temperature can be easily controlled. Furthermore, it is possible to easily adjust the residence time of the device, make it smaller, maintain airtightness, etc.

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

第1図は本発明の一実施例を示す断面図、第2図ないし
15図はスクリュー翼の他の構成を示すもので、第2図
は下方のピンチを上方よ如小さくした場合の断面図、第
3図は傾斜形の翼と水平形の興とを組み合わせた場合の
断面図、第μ図は複数のスクリュー汎なスペーサを介し
て組み合わせた場合の断面図、第5図(a)はスクリュ
ー翼の外縁にピースを設は光場合の断面図、15図(′
b)Vi同同面面図ある。まな、第6図ないし第を図は
そnぞれ他の実施例を示す断面図、第2図は従来の装置
を示す断面図である。 10・・・・・・マイクロ波オープン、16・・・・・
・マイクロ波発振装置、17・・・・・・警形円筒体、
25・曲・回転軸、26・・・・・・駆動装置、27・
・・・・・スクリュー翼、30・・・・・・スペーサ、
31・・・・・・ピース、34・・曲減圧装置。 第2図 第3図 第4図 第5図 (0) (bl
Fig. 1 is a cross-sectional view showing one embodiment of the present invention, Figs. 2 to 15 show other configurations of the screw blade, and Fig. 2 is a cross-sectional view when the lower pinch is made smaller than the upper one. , Fig. 3 is a sectional view when an inclined wing and a horizontal wing are combined, Fig. µ is a sectional view when they are combined via a plurality of screw spacers, and Fig. 5 (a) Figure 15 ('
b) Vi same side view. 6 to 9 are sectional views showing other embodiments, and FIG. 2 is a sectional view showing a conventional device. 10...Microwave open, 16...
・Microwave oscillator, 17... Police-shaped cylindrical body,
25. Curved/rotating shaft, 26... Drive device, 27.
...Screw wing, 30...Spacer,
31... Peace, 34... Song decompression device. Figure 2 Figure 3 Figure 4 Figure 5 (0) (bl

Claims (1)

【特許請求の範囲】 <iン マイクロ波オーブン内に1銹電体で形成さnt
竪形円筒体が配設され、5かつ、との竪形円筒体には、
スクリュー翼を備え、駆動装置により回転さ九る回転軸
が、その軸重を竪形円筒体の軸線に一致させて設けられ
て成ることを特徴とする乾燥等の連続処理装置。 (2)連設さ九た枚数のマイクロ波オーブン内に竪形円
筒体が配設さ九、かつ、この各マイクロ波オーブン間の
境界部に対応した位置にあるスクリュー翼の部位が、金
属で形成されるか、もしくは、該部位に金属部材が設け
られて成ることを特徴とする特許請求の範囲第1項記載
の乾燥等の連続処理装置。
[Claims]
A vertical cylindrical body is arranged, and the vertical cylindrical body with five and
1. A continuous processing device for drying, etc., characterized in that a rotating shaft is provided with screw blades and is rotated by a drive device so that its shaft load coincides with the axis of a vertical cylindrical body. (2) A vertical cylindrical body is disposed in nine consecutive microwave ovens, and the portion of the screw blade located at a position corresponding to the boundary between the microwave ovens is made of metal. 2. The continuous processing apparatus for drying, etc. according to claim 1, characterized in that a metal member is provided at said portion.
JP6188684A 1984-03-29 1984-03-29 Continuous treater for drying, etc. Granted JPS60205169A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6188684A JPS60205169A (en) 1984-03-29 1984-03-29 Continuous treater for drying, etc.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6188684A JPS60205169A (en) 1984-03-29 1984-03-29 Continuous treater for drying, etc.

Publications (2)

Publication Number Publication Date
JPS60205169A true JPS60205169A (en) 1985-10-16
JPH0123712B2 JPH0123712B2 (en) 1989-05-08

Family

ID=13184071

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6188684A Granted JPS60205169A (en) 1984-03-29 1984-03-29 Continuous treater for drying, etc.

Country Status (1)

Country Link
JP (1) JPS60205169A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008302281A (en) * 2007-06-06 2008-12-18 Shikoku Instrumentation Co Ltd Microwave chemical reactor and method
CN102393132A (en) * 2011-11-14 2012-03-28 山东博润工业技术有限公司 Vertical microwave drying coal furnace
JP2020512475A (en) * 2017-03-27 2020-04-23 スキャンシップ・アクティーゼルスカブ Microwave pyrolysis reactor
JP2020518782A (en) * 2017-03-27 2020-06-25 スキャンシップ・アクティーゼルスカブ Microwave pyrolysis reactor

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008302281A (en) * 2007-06-06 2008-12-18 Shikoku Instrumentation Co Ltd Microwave chemical reactor and method
CN102393132A (en) * 2011-11-14 2012-03-28 山东博润工业技术有限公司 Vertical microwave drying coal furnace
JP2020512475A (en) * 2017-03-27 2020-04-23 スキャンシップ・アクティーゼルスカブ Microwave pyrolysis reactor
JP2020518782A (en) * 2017-03-27 2020-06-25 スキャンシップ・アクティーゼルスカブ Microwave pyrolysis reactor
US11826717B2 (en) 2017-03-27 2023-11-28 Scanship As Microwave pyrolysis reactor

Also Published As

Publication number Publication date
JPH0123712B2 (en) 1989-05-08

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