JPH05146773A - Heating and drying device - Google Patents
Heating and drying deviceInfo
- Publication number
- JPH05146773A JPH05146773A JP3312063A JP31206391A JPH05146773A JP H05146773 A JPH05146773 A JP H05146773A JP 3312063 A JP3312063 A JP 3312063A JP 31206391 A JP31206391 A JP 31206391A JP H05146773 A JPH05146773 A JP H05146773A
- Authority
- JP
- Japan
- Prior art keywords
- vessel
- condensation
- wall material
- microwave
- rotary container
- 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
Links
Landscapes
- Processing Of Solid Wastes (AREA)
- Treatment Of Sludge (AREA)
- Drying Of Solid Materials (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は厨房や病院等で発生する
生ごみを簡便に処理する小規模な装置、あるいは食品・
飼料・粉体等の乾燥装置に利用される。The present invention relates to a small-scale device for easily treating food waste generated in kitchens, hospitals, etc.
Used for drying equipment for feed, powder, etc.
【0002】[0002]
【従来の技術】加熱乾燥を行なう場合、通常分離された
液体は気体として大気に放出されている。このような蒸
気が含んでいる臭気を分離液とともに凝縮して外部に出
さないようにしている場合もある。これは大型の冷却プ
ラントによる場合が多く、乾燥部と凝縮部が分離してい
るもので、小型な構造に適したものはなかった。2. Description of the Related Art When heat drying is carried out, the separated liquid is usually discharged as a gas to the atmosphere. In some cases, the odor contained in such vapor is condensed together with the separated liquid so as not to be discharged to the outside. This is often due to a large cooling plant, where the drying part and the condensing part are separated, and there was no one suitable for a small structure.
【0003】[0003]
【発明が解決しようとする課題】小型に適した電力乾燥
の場合、ヒータによる接触加熱かマイクロ波による非接
触加熱が一般的であるが、ヒータによる接触加熱は加熱
乾燥が不均一で、部分的に被乾燥物の分解が起こり臭気
成分が発生する問題があった。またマイクロ波を用いた
場合もマイクロ波の電界の強度分布が不均一で、同じ問
題が生じていた。In the case of electric power drying suitable for a small size, contact heating by a heater or non-contact heating by a microwave is generally used. However, contact heating by a heater causes uneven heating and drying, and partial heating. However, there is a problem in that the material to be dried is decomposed and odorous components are generated. Also, when microwaves are used, the intensity distribution of the electric field of microwaves is non-uniform and the same problem occurs.
【0004】本発明は上記問題点を改良し、乾燥部の周
囲に凝縮部を設けて小型な構成に適したものとするとと
もに、この構成で臭気の発生を低減する手段を提供する
ことを目的とする。It is an object of the present invention to improve the above-mentioned problems and to provide a condensing section around the drying section, which is suitable for a compact structure, and to provide means for reducing the generation of odor with this structure. And
【0005】[0005]
【課題を解決するための手段】本発明は、収納する傾斜
して設けた回転容器と、加熱手段と、前記回転容器の周
囲に設けた凝縮部とを有し、前記回転容器の壁材の厚み
方向の熱伝導が前記凝縮部の壁材の熱伝導率よりも小で
ある構成とした。According to the present invention, there is provided an inclined rotary container for accommodating, a heating means, and a condensing section provided around the rotary container. The thermal conductivity in the thickness direction is smaller than the thermal conductivity of the wall material of the condensation section.
【0006】[0006]
【作用】加熱された被乾燥物は水蒸気を発生し乾燥す
る。加熱乾燥操作を続けると水分と加熱手段の伝熱量の
分布が均等でないため、被乾燥物の部分的温度上昇によ
る少量の分解物の発生を完全に避けることはできない。
また被乾燥物は上部から乾燥するため底部の被乾燥物は
乾燥しにくい。このため、回転容器をコンクリートミキ
サー車のように傾斜回転させ、内部の被乾燥物を上下方
向にも撹半すれば均一に乾燥できる。このとき加熱され
た被乾燥物と回転容器の接触が激しいため被乾燥物の熱
は回転容器を加熱する。回転容器の断熱が悪いと、被乾
燥物の熱はこれを通して凝縮部に伝わり、凝縮部を加熱
し凝縮性能を低下させる。本発明は回転容器の断熱を凝
縮部の断熱よりも大としているので、凝縮部の温度は低
下し凝縮性能は良いものとなる。このため、本発明では
均一に加熱され分解物の発生が少ないと共に、発生した
分解物がほとんど凝縮するので外部に臭気を出さない。The heated material to be dried generates steam to be dried. When the heating and drying operation is continued, the distribution of moisture and the amount of heat transfer of the heating means is not uniform, so that the generation of a small amount of decomposition products due to the partial temperature rise of the material to be dried cannot be completely avoided.
Also, since the material to be dried is dried from the top, the material to be dried at the bottom is difficult to dry. Therefore, if the rotary container is tilted and rotated like a concrete mixer truck and the material to be dried inside is also stirred vertically, the material can be uniformly dried. At this time, since the heated object to be dried and the rotary container are in heavy contact with each other, the heat of the object to be dried heats the rotary container. If the heat insulation of the rotating container is poor, the heat of the material to be dried is transmitted to the condensing part through it, heating the condensing part and deteriorating the condensing performance. According to the present invention, the heat insulation of the rotary container is made larger than the heat insulation of the condensing part, so that the temperature of the condensing part is lowered and the condensing performance becomes good. For this reason, in the present invention, the decomposition products are uniformly heated and the decomposition products are little generated, and the generated decomposition products are almost condensed, so that no odor is emitted to the outside.
【0007】[0007]
【実施例】以下、本発明の一実施例を添付図面に基づい
て説明する。図1において、1はマイクロ波反射材料で
作られた凝縮槽で、被乾燥物例えば、生ごみ2は凝縮部
1の開閉する扉3より投入され回転容器4に入れられて
いる。回転容器4はステンレスの2重真空容器、あるい
は耐熱発泡プラスチックを用いた断熱容器でも良い。マ
イクロ波はマイクロ波発振器5で発振され導波管6を通
って開口7より回転容器4の内部に放射され強い電界を
形成する。回転容器4の下部はモータ8と連結する回転
テーブル9である。回転軸10と凝縮槽1の底部は液シ
ール軸受け11である。回転容器4上部の扉3は凝縮槽
1の上部に設けた凝縮蓋12に載置されている。凝縮蓋
12と回転容器4上部の間に回転容器4内部と凝縮槽1
の連通部13が形成されている。凝縮槽1の外部は冷却
用の送風機14で冷却されている。凝縮槽1の下部に凝
縮水の排水管15がある。凝縮水は下水管に排出され
る。凝縮しない水蒸気は送風機16で吸引され、ヒータ
17を有する触媒18で排気の中の臭気成分となる分解
物が酸化され排出する。凝縮蓋12の上部には上昇した
水蒸気の温度検知部19が設けられている。送風機14
の冷却風の一部は空気孔20よりマイクロ波シール扉2
1と凝縮蓋22の空間を通り空気孔22より排出され
る。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the accompanying drawings. In FIG. 1, reference numeral 1 is a condensing tank made of a microwave reflecting material, and an object to be dried, for example, raw garbage 2 is put into a rotary container 4 through a door 3 that opens and closes the condensing unit 1. The rotating container 4 may be a stainless double vacuum container or a heat insulating container made of heat-resistant foamed plastic. The microwave is oscillated by the microwave oscillator 5, passes through the waveguide 6, and is radiated from the opening 7 into the inside of the rotary container 4 to form a strong electric field. The lower part of the rotary container 4 is a rotary table 9 connected to the motor 8. The rotary shaft 10 and the bottom of the condensing tank 1 are liquid seal bearings 11. The door 3 above the rotary container 4 is placed on a condensation lid 12 provided at the top of the condensation tank 1. Between the condensation lid 12 and the upper part of the rotary container 4, the inside of the rotary container 4 and the condensation tank 1
The communication part 13 of is formed. The outside of the condensing tank 1 is cooled by a blower 14 for cooling. At the bottom of the condensing tank 1, there is a drain pipe 15 for condensed water. Condensed water is discharged to the sewer pipe. The water vapor that does not condense is sucked by the blower 16, and the catalyst 18 having the heater 17 oxidizes and decomposes the decomposed product that becomes the odor component in the exhaust gas. Above the condensation lid 12, a temperature detector 19 for rising water vapor is provided. Blower 14
Part of the cooling air from the air vent 20 is the microwave seal door 2
1 and the space of the condensation lid 22 and discharged from the air holes 22.
【0008】上記構成の本発明の動作を以下に説明す
る。生ごみ2は扉3より回転容器4に投入される。この
ような状態でマイクロ波発振器5がマイクロ波を発振す
ると、2450MHzのマイクロ波が導波管6から、回
転容器4へ入りこの空間に高い電界を作る。金属壁では
マイクロ波は反射し、ほとんど生ごみ2中の水分に吸収
される。マイクロ波は生ごみの上方から浸透し、生ごみ
の底部では減衰している。さらに金属製の回転容器の底
部は電界強度が弱いため、生ごみの不均一乾燥の原因と
なる。このため、傾斜した軸をモータで回転させること
により、コンクリートミキサー車のように回転容器4を
回転させる。生ごみ2は回転しながら上下反転し均一に
乾燥される。The operation of the present invention having the above configuration will be described below. The garbage 2 is put into the rotary container 4 through the door 3. When the microwave oscillator 5 oscillates a microwave in such a state, a microwave of 2450 MHz enters the rotating container 4 from the waveguide 6 and creates a high electric field in this space. The microwaves are reflected by the metal wall and are almost absorbed by the water in the food waste 2. Microwaves penetrate from above the garbage and are attenuated at the bottom of the garbage. Further, the electric field strength is weak at the bottom of the metal rotating container, which causes uneven drying of the food waste. Therefore, by rotating the inclined shaft with a motor, the rotating container 4 is rotated like a concrete mixer truck. The garbage 2 is turned upside down while rotating and dried uniformly.
【0009】水蒸気は連通部13を通り凝縮槽1へ排出
される。凝縮槽1の金属壁は送風機14で冷却されてい
るので水蒸気は凝縮して下方の排水管15に流下する。
排水は生ごみが均一に加熱されているので有機物の含有
量が少なく下水道を汚染しない。凝縮しない水蒸気は生
ごみ2の分解ガスを多少含んでいるので、予めヒータ1
7で予熱されている触媒18で酸化され無臭化される。The water vapor is discharged to the condensing tank 1 through the communicating portion 13. Since the metal wall of the condensing tank 1 is cooled by the blower 14, the water vapor is condensed and flows down to the drain pipe 15 below.
Wastewater is heated uniformly so that it contains less organic substances and does not pollute the sewer. The water vapor that does not condense contains some decomposed gas from the food waste 2.
The catalyst 18 preheated in 7 is oxidized and deodorized.
【0010】また水蒸気の凝縮を行う理由は次の通りで
ある。水蒸気が多いと排気口16で凝縮し、漏れた場合
家屋を損傷し易い。また、触媒反応量は被処理ガスの触
媒内滞留時間で左右されるが、水蒸気の勢いが強いと臭
気成分は触媒15を高速ですり抜け反応しにくい。本発
明では水蒸気を凝縮させ体積を縮小しているので滞留時
間は長くなる。さらに水蒸気の凝縮とともに多量の臭気
成分も凝縮し、触媒の処理能力に余裕が生じる。The reason for condensing water vapor is as follows. If there is a large amount of water vapor, it will condense at the exhaust port 16 and if it leaks, it will easily damage the house. Further, the catalytic reaction amount depends on the residence time of the gas to be treated in the catalyst, but if the steam is strong, the odorous component does not easily pass through the catalyst 15 at a high speed to react. In the present invention, since the water vapor is condensed to reduce the volume, the residence time becomes long. Furthermore, a large amount of odorous components are condensed along with the condensation of water vapor, which leaves room for the processing capacity of the catalyst.
【0011】しかし、均一乾燥のため容器を斜め回転さ
せると、生ごみ2は回転しながら多量の熱を回転容器4
に伝える。停止している場合よりも熱は容器に伝わり易
いため、この熱が回転容器4の外側に伝われば、凝縮槽
1の水蒸気が加熱され凝縮しにくくなる。このため本発
明では回転容器を断熱性のものとして、生ゴミ2の熱が
凝縮槽1に伝わらないものとしている。凝縮槽1の材料
は逆に熱伝導の高いことが凝縮量を増加させるので望ま
しい。例えばステンレス(SUS430,板厚1mm)
製の回転容器では外側の温度が80℃になり凝縮率(発
生した水蒸気の内凝縮した割合)は50%程度である
が、真空断熱した2重のステンレス容器では外側の温度
は40℃となり95%の水分が凝縮し、臭気成分もこれ
に比例して減少し排気経路の臭気も減少する。プラスチ
ック系の断熱材ではこの中間であった。この意味で最も
望ましいのは真空断熱した2重のステンレス容器であ
る。However, when the container is rotated obliquely for uniform drying, the food waste 2 rotates and a large amount of heat is generated while the container 4 rotates.
Tell. Since heat is more easily transferred to the container than when it is stopped, if this heat is transferred to the outside of the rotary container 4, the water vapor in the condensing tank 1 will be heated and less likely to condense. Therefore, in the present invention, the rotary container is made of a heat insulating material so that the heat of the garbage 2 is not transferred to the condensing tank 1. On the contrary, it is desirable that the material of the condensing tank 1 has high heat conductivity because the amount of condensation increases. For example, stainless steel (SUS430, plate thickness 1mm)
In a rotating container made of steel, the outside temperature is 80 ° C, and the condensation rate (the rate of condensation of generated water vapor) is about 50%, but in a vacuum-insulated double stainless container, the outside temperature is 40 ° C, % Of water is condensed, the odor component is also reduced in proportion to this, and the odor in the exhaust path is also reduced. It was somewhere in the middle for plastic heat insulating materials. The most desirable in this sense is a vacuum-insulated double stainless steel container.
【0012】回転容器の凝縮槽1への放熱はマイクロ波
の浪費となるが、この点も断熱された回転容器4は電気
消費量を節約できる。The radiation of heat from the rotary container to the condensing tank 1 is a waste of microwaves, but in this respect as well, the rotary container 4 with heat insulation can save electricity consumption.
【0013】回転容器で発生した水蒸気の一部は凝縮蓋
12でも凝縮させるが、本発明のように凝縮蓋を斜めに
構成すれば、凝縮した水分はすべて凝縮槽1に流下す
る。水滴が回転容器4に落下するとこの気化にマイクロ
波エネルギーが再度消費され無駄になる。したがって凝
縮蓋12は少なくとも回転容器4の垂直延長上では凝縮
槽1に向かって傾斜していなければならない。また、本
実施例は加熱手段をマイクロ波としたが、より簡便な装
置としては熱風を用いても良い。回転容器4に上部から
熱風を生ごみに吹き込んでも同様の効果は得られる。A part of the water vapor generated in the rotary container is condensed also in the condensation lid 12, but if the condensation lid is constructed obliquely as in the present invention, all the condensed moisture flows down to the condensation tank 1. When the water drops fall into the rotary container 4, this vaporization consumes microwave energy again and is wasted. Therefore, the condensing lid 12 must be inclined toward the condensing tank 1 at least on the vertical extension of the rotary container 4. Further, although the heating means is a microwave in this embodiment, hot air may be used as a simpler device. The same effect can be obtained by blowing hot air into the rotary container 4 from above.
【0014】乾燥の進行は回転容器の4の上方に設けた
温度検知部19の温度、あるいは生ごみ2の重量変化、
凝縮槽1の湿度変化等の手段で検出される。この信号に
従って加熱し過ぎて電気が無駄にならないようにマイク
ロ波を停止すれば処理は終了する。The progress of drying depends on the temperature of the temperature detecting portion 19 provided above the rotary container 4 or the weight change of the food waste 2.
It is detected by means such as a change in humidity of the condensing tank 1. If the microwaves are stopped so that electricity is not wasted due to overheating according to this signal, the processing ends.
【0015】[0015]
【発明の効果】以上のように本発明によれば、被乾燥物
は乾燥し腐敗しにくいものとなるとともに、少ない消費
電力で重量が減少し容積も小さくなる。また、分離した
水分の含む有機物が少なく、下水を汚染しない。あるい
は発生した水蒸気をほとんど凝縮するので臭気の発生は
極めて少ないものとなる。As described above, according to the present invention, the material to be dried becomes less likely to be dried and rotted, and the weight and volume are reduced with less power consumption. In addition, the separated water-containing organic matter does not pollute sewage. Alternatively, since most of the generated steam is condensed, the generation of odor is extremely small.
【図1】本発明の一実施例の加熱乾燥装置の断面図FIG. 1 is a sectional view of a heating and drying apparatus according to an embodiment of the present invention.
1 凝縮槽 2 生ごみ 3 蓋 4 回転容器 5 マイクロ波発振器 14 送風機 1 Condensation tank 2 Garbage 3 Lid 4 Rotating container 5 Microwave oscillator 14 Blower
───────────────────────────────────────────────────── フロントページの続き (72)発明者 鵜飼 邦弘 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Kunihiro Ukai 1006 Kadoma, Kadoma-shi, Osaka Prefecture Matsushita Electric Industrial Co., Ltd.
Claims (2)
と、前記回転容器の生ごみを加熱する加熱手段と、前記
回転容器の周囲に設けた凝縮部と、前記凝縮部の冷却手
段と、前記回転容器と前記凝縮部間に連通部を有し、前
記回転容器の壁材の厚み方向の熱伝導が前記凝縮部の壁
材の熱伝導率よりも小である加熱乾燥装置。1. An inclined rotary container for storing food waste, a heating means for heating the food waste in the rotary container, a condensing section provided around the rotary container, and a cooling means for the condensing section. And a communication part between the rotary container and the condensing part, wherein the heat conduction in the thickness direction of the wall material of the rotary container is smaller than the heat conductivity of the wall material of the condensing part.
の加熱乾燥装置。2. The heating / drying apparatus according to claim 1, wherein the heating means is a microwave.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3312063A JP2692463B2 (en) | 1991-11-27 | 1991-11-27 | Garbage processing machine |
US07/928,436 US5335425A (en) | 1991-08-14 | 1992-08-12 | Dry-processing apparatus for heating and drying objects to be processed |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3312063A JP2692463B2 (en) | 1991-11-27 | 1991-11-27 | Garbage processing machine |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH05146773A true JPH05146773A (en) | 1993-06-15 |
JP2692463B2 JP2692463B2 (en) | 1997-12-17 |
Family
ID=18024785
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3312063A Expired - Fee Related JP2692463B2 (en) | 1991-08-14 | 1991-11-27 | Garbage processing machine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2692463B2 (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0924488A1 (en) | 1997-12-16 | 1999-06-23 | Paloma Industries, Ltd. | Garbage disposer |
US6012233A (en) * | 1997-11-19 | 2000-01-11 | Paloma Industries, Limited | Garbage disposer |
JP2005103355A (en) * | 2003-09-29 | 2005-04-21 | Sanyo Electric Co Ltd | Garbage treatment apparatus |
KR100820131B1 (en) * | 2006-09-29 | 2008-04-08 | 김희정 | Apparatus and method for processing food waste |
JP6288389B1 (en) * | 2017-01-26 | 2018-03-07 | 中国電力株式会社 | Silica gel regeneration equipment |
CN112254480A (en) * | 2020-10-31 | 2021-01-22 | 汕头市达兴钢结构有限公司如皋分公司 | Microwave dryer for dyeing steel plate |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02150687A (en) * | 1988-12-02 | 1990-06-08 | Sanyo Electric Co Ltd | Microwave drier |
-
1991
- 1991-11-27 JP JP3312063A patent/JP2692463B2/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02150687A (en) * | 1988-12-02 | 1990-06-08 | Sanyo Electric Co Ltd | Microwave drier |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6012233A (en) * | 1997-11-19 | 2000-01-11 | Paloma Industries, Limited | Garbage disposer |
EP0924488A1 (en) | 1997-12-16 | 1999-06-23 | Paloma Industries, Ltd. | Garbage disposer |
US6076271A (en) * | 1997-12-16 | 2000-06-20 | Paloma Industries, Ltd. | Garbage disposer |
CN1115287C (en) * | 1997-12-16 | 2003-07-23 | 百乐满工业株式会社 | Refuse treatment device for kitchen |
JP2005103355A (en) * | 2003-09-29 | 2005-04-21 | Sanyo Electric Co Ltd | Garbage treatment apparatus |
KR100820131B1 (en) * | 2006-09-29 | 2008-04-08 | 김희정 | Apparatus and method for processing food waste |
JP6288389B1 (en) * | 2017-01-26 | 2018-03-07 | 中国電力株式会社 | Silica gel regeneration equipment |
WO2018138825A1 (en) * | 2017-01-26 | 2018-08-02 | 中国電力株式会社 | Silica gel reclaiming device |
CN112254480A (en) * | 2020-10-31 | 2021-01-22 | 汕头市达兴钢结构有限公司如皋分公司 | Microwave dryer for dyeing steel plate |
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Publication number | Publication date |
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JP2692463B2 (en) | 1997-12-17 |
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