JPH102668A - Drying device - Google Patents

Drying device

Info

Publication number
JPH102668A
JPH102668A JP17557396A JP17557396A JPH102668A JP H102668 A JPH102668 A JP H102668A JP 17557396 A JP17557396 A JP 17557396A JP 17557396 A JP17557396 A JP 17557396A JP H102668 A JPH102668 A JP H102668A
Authority
JP
Japan
Prior art keywords
drying
dried
air
conveyor
drying tower
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
JP17557396A
Other languages
Japanese (ja)
Other versions
JP2829278B2 (en
Inventor
Hiroyoshi Sueda
博能 末田
Kyoichi Yahagi
恭一 矢萩
Masao Suzuki
雅夫 鈴木
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.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki Heavy Industries 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 Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP8175573A priority Critical patent/JP2829278B2/en
Publication of JPH102668A publication Critical patent/JPH102668A/en
Application granted granted Critical
Publication of JP2829278B2 publication Critical patent/JP2829278B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Drying Of Solid Materials (AREA)

Abstract

PROBLEM TO BE SOLVED: To set a proper residence time and to increase drying efficiency by providing a drying tower to effect drying of an object to be dried by dry air while the object is upward moved, and a storage tank to temporarily store the object discharged from the drying tower and effect the circulation feed thereof to a feed conveyor, and partially discharge as a product, and setting proper residence time, and drying efficiency. SOLUTION: An object to be dried fed to a drying tower 3 is dried by dry air while the object is upward moved by a screw conveyor 9. Since drying air takes a route across a transfer passage for a dried object through a vertical portion and a horizontal partition 11 several times, drying efficiency is remarkably improved. An object to be processed discharged from a drying tower 3 to a storage tank 19 is temporarily stored therein and partially discharged as a product to the outside of a system by a product conveyor 23. The rest is fed in a circulating manner to a feed conveyor 1 by a scraper conveyor 22 and re-dried in a drying tower 3 together with a new object to be dried. Thus, a proper residence time for an object to be dried is set.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、乾燥装置に関し、
特に廃プラスチックや家庭ごみ、故紙等の可燃性廃棄物
を固形燃料化する際に、破砕された可燃性廃棄物を乾燥
処理する乾燥装置に関する。
TECHNICAL FIELD The present invention relates to a drying device,
Particularly, the present invention relates to a drying apparatus for drying crushed combustible waste when converting combustible waste such as waste plastic, household waste, waste paper, etc. into solid fuel.

【0002】[0002]

【従来の技術】従来、この種の乾燥装置としては、周面
に無数の通気孔を設けた横置円筒形の回転ドラムの周面
を、下部に熱風供給ダクト、又、上部に排気ダクトを設
けたハウジングで覆ったもの、あるいは上記回転ドラム
の軸心に、多数の通気孔を周面に設けた送気管を配置
し、かつ回転ドラムと送気管との間に多数の仕切壁を放
射状に取付けて多数の小室を形成したものが知られてい
る(特開昭63−49690号公報参照)。上記乾燥装
置は、適宜に傾斜させた回転ドラムの一端から被乾燥物
を回転ドラム又は各小室内に投入し、回転ドラムの回転
により被乾燥物を撹拌しつつ熱風により乾燥し、他端か
ら製品として排出するというものである。
2. Description of the Related Art Conventionally, as a drying apparatus of this type, a peripheral surface of a horizontal cylindrical rotary drum having an infinite number of ventilation holes on a peripheral surface, a hot air supply duct at a lower part, and an exhaust duct at an upper part. An air supply pipe provided with a number of vent holes on the peripheral surface is arranged at the axis of the rotating drum or the one covered with the provided housing, and a number of partition walls are radially provided between the rotating drum and the air supply pipe. It is known that a large number of small chambers are formed by mounting (see JP-A-63-49690). The drying device throws the object to be dried into the rotating drum or each small chamber from one end of the rotating drum which is appropriately inclined, dries the object to be dried by hot air while stirring the object to be dried by rotation of the rotating drum, and outputs the product from the other end. It is to be discharged as.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、従来の
乾燥装置では、被乾燥物の乾燥時間(滞留時間)は、出
口セキの開閉度によりある程度調節できるものの、適切
な滞留時間を設定することが困難となる不具合がある。
又、熱風が被乾燥物の移動方向を横切って1度しか接触
しないので、伝熱効率(乾燥効率)が低くなる不具合も
ある。そこで、本発明は、適切な滞留時間を設定でき、
かつ乾燥効率を格段に高め得る乾燥装置を提供すること
を目的とする。
However, in the conventional drying apparatus, the drying time (residence time) of the object to be dried can be adjusted to some extent by the degree of opening and closing of the outlet, but it is difficult to set an appropriate residence time. There is a defect.
Further, since the hot air contacts only once across the moving direction of the object to be dried, there is a problem that the heat transfer efficiency (drying efficiency) is reduced. Therefore, the present invention can set an appropriate residence time,
It is another object of the present invention to provide a drying apparatus capable of significantly improving the drying efficiency.

【0004】[0004]

【課題を解決するための手段】前記課題を解決するた
め、本発明の乾燥装置は、ホッパーから切り出される被
乾燥物を搬送する供給コンベヤと、供給コンベヤから供
給される被乾燥物を上方へ垂直に移送しながら同方向へ
通気される乾燥風により乾燥する乾燥塔と、乾燥塔へ乾
燥風を供給する乾燥風供給手段と、乾燥塔から排出され
る被乾燥物を一時的に貯留すると共に、前記供給コンベ
ヤに循環供給し、かつ一部を製品として払い出す貯留槽
とを備えることを特徴とする。前記ホッパーの切り出し
量は、貯留槽内の被乾燥物の多少に応じて調節可能に設
けられていることが好ましい。前記乾燥塔は、被乾燥物
と乾燥風の入口を下端部にかつ出口を上端部に設けた円
筒状の垂直な筒体と、筒体内に同軸的に配置され、それ
より適宜小径の円筒状を呈しかつ無数の通気孔を設けた
円筒状のケーシングを有するスクリューコンベヤと、筒
体とケーシングの間を軸方向へ2分割する縦仕切りと、
縦仕切りにより2分割された筒体とケーシングの間を交
互に径方向へ多段分割する横仕切りとからなることが好
ましい。前記乾燥風供給手段は、乾燥塔の入口における
乾燥風の温度及びその出口における乾燥風の圧力に応じ
て乾燥風の温度及び供給量をそれぞれ調節可能に設けら
れていることが好ましい。又、前記貯留槽の製品払い出
し量は、貯留槽内の被乾燥物の貯留量及び製品出口の被
乾燥物の水分量に応じて調節可能に設けられていること
が好ましい。
In order to solve the above-mentioned problems, a drying apparatus according to the present invention comprises a supply conveyor for transporting a material to be dried cut out from a hopper, and a drying device supplied from the supply conveyor. A drying tower that dries by a drying air that is aerated in the same direction while being transported to the drying tower, a drying air supply unit that supplies the drying air to the drying tower, and temporarily stores the material to be dried discharged from the drying tower. And a storage tank that circulates and supplies a part of the supply to the supply conveyor. It is preferable that the cutout amount of the hopper is provided so as to be adjustable according to the amount of the material to be dried in the storage tank. The drying tower is a cylindrical vertical cylinder having an inlet at the lower end and an outlet at the upper end of the material to be dried and the drying air, and is coaxially arranged in the cylinder, and has a cylindrical shape having a smaller diameter as appropriate. And a screw conveyor having a cylindrical casing provided with countless ventilation holes, and a vertical partition for axially dividing the space between the cylindrical body and the casing into two,
It is preferable to include a horizontal partition which alternately divides the cylindrical body and the casing which are divided into two by the vertical partition into multiple stages in the radial direction. The drying air supply means is preferably provided so that the temperature and the supply amount of the drying air can be adjusted according to the temperature of the drying air at the inlet of the drying tower and the pressure of the drying air at the outlet. Further, it is preferable that the product delivery amount of the storage tank is provided so as to be adjustable in accordance with the storage amount of the material to be dried in the storage tank and the moisture content of the material to be dried at the product outlet.

【0005】[0005]

【発明の実施の形態】以下、本発明の実施の形態につい
て図面を参照して説明する。図1,図2は本発明に係る
乾燥装置の実施の形態の一例である可燃性廃棄物の乾燥
設備を示す概略構成図、図1におけるII−II線拡大断面
図である。図中1は所要の大きさ(例えば40mm以下)
に破砕されてホッパー(図示せず)に収容され、エアー
ロックダンパー2により切り出し量が調節可能な可燃性
廃棄物(被乾燥物)を水平に搬送する供給コンベヤで、
この供給コンベヤ1で搬送される被乾燥物は、乾燥塔3
に供給される。乾燥塔3は、被乾燥物を上方へ垂直に移
送しながら同方向へ通気される乾燥風により乾燥するも
のであり、被乾燥物と乾燥風の入口4,5を下端部に、
かつ出口6を上端部に設けた円筒状の垂直な筒体7と、
筒体7内にそのほぼ全長に亘って同軸的に配置され、筒
体7より適宜小径の円筒状を呈し、かつ無数の通気孔を
設けた円筒状のケーシング8を有するスクリューコンベ
ヤ9と、筒体7とケーシング8の間を軸方向へ2分する
縦仕切り10(図2参照)と、縦仕切り10により2分
割された筒体7とケーシング8の間を交互に径方向へ多
段分割する横仕切り11と、筒体7の外周を覆う保温材
12(図2参照)とから構成されている。そして、乾燥
塔3の乾燥風の入口5には、乾燥風供給手段13から乾
燥風を供給するように構成されている。乾燥風供給手段
13は、外気を吸引して所要温度に加熱する熱風発生装
置14と、熱風発生装置14からの熱風と後述する乾燥
風循環路からの乾燥風を併わせて乾燥風の入口5へ供給
する熱風ファン15とからなり、又、乾燥風供給手段1
3は、乾燥風の入口5の温度を検出する温度計16から
の信号及び乾燥塔3の出口6の乾燥風の圧力を検出する
圧力計17からの信号を受け、熱風発生装置14の加熱
温度及び熱風ファン15の供給量をそれぞれ調節する乾
燥風制御器18を備えている。
Embodiments of the present invention will be described below with reference to the drawings. 1 and 2 are schematic configuration diagrams showing a combustible waste drying facility as an example of an embodiment of a drying apparatus according to the present invention, and are an enlarged sectional view taken along line II-II in FIG. In the figure, 1 is the required size (for example, 40 mm or less)
A supply conveyor for horizontally transporting combustible waste (dry matter), which is crushed into a hopper (not shown) and whose cut-out amount is adjustable by an air lock damper 2,
The material to be dried conveyed by the supply conveyor 1 is a drying tower 3
Supplied to The drying tower 3 is to dry the object to be dried by the drying air that is passed in the same direction while vertically transporting the object to be dried, and the inlets 4 and 5 for the object to be dried and the drying air are provided at the lower end,
A vertical cylindrical body 7 having an outlet 6 at an upper end thereof;
A screw conveyor 9 having a cylindrical casing 8 disposed coaxially over substantially the entire length thereof in the cylindrical body 7 and having a cylindrical shape having a diameter smaller than that of the cylindrical body 7 and provided with countless ventilation holes; A vertical partition 10 (see FIG. 2) for dividing the space between the body 7 and the casing 8 into two in the axial direction, and a horizontal partition for alternately dividing the space between the cylindrical body 7 and the casing 8 into two by the vertical partition 10 in the radial direction. It is composed of a partition 11 and a heat insulating material 12 (see FIG. 2) that covers the outer periphery of the cylindrical body 7. The drying air inlet 5 of the drying tower 3 is configured to supply the drying air from the drying air supply means 13. The drying air supply means 13 includes a hot air generating device 14 that sucks outside air and heats the air to a required temperature, and a drying air inlet 5 that combines hot air from the hot air generating device 14 and drying air from a drying air circulation path described later. And a hot air fan 15 for supplying air to the
3 receives a signal from a thermometer 16 for detecting the temperature of the inlet 5 of the drying air and a signal from a pressure gauge 17 for detecting the pressure of the drying air at the outlet 6 of the drying tower 3, and receives the heating temperature of the hot air generator 14. And a dry air controller 18 for adjusting the supply amount of the hot air fan 15.

【0006】乾燥塔3の出口6には、乾燥塔3から排出
される被乾燥物を一時的に貯留すると共に、前記供給コ
ンベヤ1に循環供給し、かつ一部を製品(乾燥物)とし
て払い出す貯留槽19が、ダクト20を介して接続され
ている。貯留槽19は、上記ダクト20が上端部に接続
されたタンク21と、このタンク21内に貯留された被
乾燥物を前記供給コンベヤ1へ循環供給するスクレーパ
コンベヤ22と、一部の被乾燥物を製品として払い出す
製品コンベヤ23とからなる。そして、タンク21に
は、その中に貯留される被乾燥物量のハイレベルとロー
レベルを検出するレベルスイッチ24,25が設けられ
ていると共に、製品コンベヤ23によって払い出される
被乾燥物の水分量を検出する水分計26が設けられてお
り、レベルスイッチ24,25からの信号が前記エアー
ロックダンパー2の切り出し量を制御するダンパー制御
器27に入力されると共に、レベルスイッチ25及び水
分計26からの信号が製品コンベヤ23の払い出し量を
制御する製品コンベヤ制御器28に入力されるように構
成されている。一方、貯留槽19に導入される乾燥風
は、タンク21の上端部から粉塵と一緒にサイクロン2
9に供給され、このサイクロン29において粉塵と分離
された後循環ファン30により吸引され、一部が脱臭装
置31を経て大気に放散されると共に、残部が乾燥風循
環路32を経て乾燥風供給手段13の熱風ファン15に
循環供給される。そして、サイクロン29から排出され
る粉塵は、製品コンベヤ23から排出されるものと一緒
にされて製品となる。
At the outlet 6 of the drying tower 3, the material to be dried discharged from the drying tower 3 is temporarily stored, circulated and supplied to the supply conveyor 1, and a part of the material is dried as a product (dried material). An outgoing storage tank 19 is connected via a duct 20. The storage tank 19 includes a tank 21 having the duct 20 connected to an upper end thereof, a scraper conveyor 22 for circulating the material to be dried stored in the tank 21 to the supply conveyor 1, and a part of the material to be dried. Conveyor as a product. The tank 21 is provided with level switches 24 and 25 for detecting a high level and a low level of the amount of the material to be dried stored in the tank 21. A moisture meter 26 for detection is provided, and signals from the level switches 24 and 25 are input to a damper controller 27 that controls the cut-out amount of the air lock damper 2, and the signals from the level switch 25 and the moisture meter 26 are provided. The signal is configured to be input to a product conveyor controller 28 that controls the payout amount of the product conveyor 23. On the other hand, the drying air introduced into the storage tank 19 flows from the upper end of the tank 21 together with the dust into the cyclone 2.
After being separated from dust in the cyclone 29, the dust is sucked by the circulation fan 30, a part of the dust is released to the atmosphere through the deodorizing device 31, and the remaining part is passed through the drying air circulation path 32 and the drying air supply means 13 hot air fans 15 are circulated and supplied. The dust discharged from the cyclone 29 is combined with the dust discharged from the product conveyor 23 to form a product.

【0007】上記構成の可燃性廃棄物の乾燥設備におい
て、ホッパーからエアーロックダンパー2及び供給コン
ベヤ1を経て乾燥塔3に供給された被乾燥物は、スクリ
ューコンベヤ9により上方へ垂直に移動されながら、乾
燥風供給手段13から供給された同方向へ通気する乾燥
風により乾燥される。この被乾燥物の乾燥に際し、乾燥
風は、縦仕切り10と横仕切り11によりその通気が制
限され、図1において白抜き矢印Aで示すように、被乾
燥物の移送路を数回横切るジグザグ状の経路となるの
で、乾燥効率が格段に高められる。又、温度計16によ
り乾燥風の入口5の温度を検出し、かつ圧力計17によ
り乾燥塔3の出口6の乾燥風の圧力を検出し、乾燥風制
御器18によって乾燥風供給手段13からの乾燥風の温
度及び圧力を制御し、被乾燥物の性状に合わせた温度及
び乾燥塔3内の状態にかかわらない供給量とする。乾燥
塔3から乾燥風と一緒に貯留槽19に排出された被処理
物は、その中に一時的に貯留されると共に、一部が製品
コンベヤ23により製品として系外に排出され、残部が
スクレーパコンベヤ22により供給コンベヤ1に循環供
給されてホッパーから供給される新たな被乾燥物と一緒
に乾燥塔3で再度乾燥される。この貯留槽19における
被乾燥物の一時的な貯留に際し、被乾燥物の貯留量がレ
ベルスイッチ25によりローレベルであると検出される
と、製品コンベヤ制御器28の制御によって製品コンベ
ヤ23による製品の払い出しが始まる一方、水分計26
による製品の水分量が所定の値(所定の乾燥状態)とな
るように、製品コンベヤ23による製品の払い出し量
(製品コンベヤの回転数)が製品コンベヤ制御器28に
よって制御される。又、被乾燥物が乾燥し難いものであ
る場合、製品払い出し量が被乾燥物の供給量より小さく
なるため、タンク内の被乾燥物の貯留レベルが上昇する
が、貯留レベルがハイレベルであるとレベルスイッチ2
4によって検出されると、ダンパー制御器27による制
御によってエアーロックダンパー2からの被乾燥物の切
り出しが停止され、循環運転しながら製品の払い出しが
行われ、貯留レベルがローレベルであるとレベルスイッ
チ25によって検出されると、ダンパー制御器27によ
る制御によってエアーロックダンパー2からの被乾燥物
の切り出しが再開される。なお、被乾燥物の乾燥状態
は、エアーロックダンパー2からの被乾燥物の切り出し
量を落すことによっても調整可能である。したがって、
被乾燥物の性状に応じて、乾燥時間(滞留時間)を大幅
に変化させることができる。一方、貯留槽19に導入さ
れた乾燥風は、その上部から粉塵と一緒にサイクロン2
9に供給されて粉塵と分離された後、循環ファン30に
より吸引されて一部が脱臭装置31を経て大気に放散さ
れる一方、残部が乾燥風循環路32を経て乾燥風供給手
段13へ循環供給される。したがって、排気が再利用さ
れることとなり、大幅に省エネルギー効果を高めること
ができる。そして、サイクロン29で分離された粉塵
は、製品コンベヤ23から排出されるものと一緒にさ
れ、製品となるものである。
In the flammable waste drying facility having the above-described configuration, the material to be dried supplied from the hopper to the drying tower 3 via the air lock damper 2 and the supply conveyor 1 is moved vertically upward by the screw conveyor 9. The drying is performed by the drying air supplied from the drying air supply means 13 and flowing in the same direction. In drying the object to be dried, the ventilation of the drying air is restricted by the vertical partition 10 and the horizontal partition 11, and zigzag-shaped across the transfer path of the object to be dried several times as shown by a white arrow A in FIG. Therefore, the drying efficiency is significantly improved. Further, the temperature of the drying air inlet 5 is detected by the thermometer 16, the pressure of the drying air at the outlet 6 of the drying tower 3 is detected by the pressure gauge 17, and the drying air controller 18 supplies the drying air from the drying air supply means 13. The temperature and pressure of the drying air are controlled to a temperature suitable for the properties of the material to be dried and a supply amount irrespective of the state in the drying tower 3. The object to be treated discharged from the drying tower 3 together with the drying air into the storage tank 19 is temporarily stored therein, a part of which is discharged as a product by the product conveyor 23 outside the system, and the remainder is scraper. It is circulated and supplied to the supply conveyor 1 by the conveyor 22, and is dried again in the drying tower 3 together with a new material to be dried supplied from the hopper. During the temporary storage of the material to be dried in the storage tank 19, when the storage amount of the material to be dried is detected to be low level by the level switch 25, the product conveyor 23 controls the product conveyor 23 to control the product by the product conveyor 23. While the dispensing starts, the moisture meter 26
Is controlled by the product conveyor controller 28 so that the product conveyor 23 discharges the product (the number of revolutions of the product conveyor) so that the moisture content of the product becomes a predetermined value (predetermined dry state). In addition, when the material to be dried is difficult to dry, the product delivery amount is smaller than the supply amount of the material to be dried, so the storage level of the material to be dried in the tank increases, but the storage level is high. And level switch 2
4, the control of the damper controller 27 stops the cutout of the material to be dried from the air lock damper 2 and discharges the product while circulating. If the storage level is low, the level switch is used. When the detection is performed by the damper controller 25, the cutout of the object to be dried from the air lock damper 2 is restarted under the control of the damper controller 27. Note that the drying state of the object to be dried can also be adjusted by reducing the amount of the object to be dried cut out from the air lock damper 2. Therefore,
The drying time (residence time) can be greatly changed according to the properties of the material to be dried. On the other hand, the drying air introduced into the storage tank 19 is supplied to the cyclone 2 together with dust from above.
After being supplied to 9 and separated from the dust, it is sucked by the circulation fan 30 and a part is radiated to the atmosphere through the deodorizing device 31 while the remainder is circulated to the dry air supply means 13 through the dry air circulation path 32. Supplied. Therefore, the exhaust gas is reused, and the energy saving effect can be greatly improved. The dust separated by the cyclone 29 is combined with the dust discharged from the product conveyor 23 to become a product.

【0008】[0008]

【発明の効果】以上、説明したように本発明の乾燥装置
によれば、被乾燥物が貯留槽を経て乾燥塔へ循環供給さ
れると共に、乾燥塔における乾燥風の移動経路が被乾燥
物の移送経路に沿うので、被乾燥物の適切な滞留時間を
設定することができると共に、乾燥効率を格段に向上す
ることができる。又、乾燥塔を垂直な筒体、無数の通気
孔を設けたケーシングを有するスクリューコンベヤ、筒
体とケーシング間を軸方向へ2分割する縦仕切り及び2
分割された筒体とケーシング間を交互に径方向へ多段分
割する横仕切りから構成することにより、乾燥塔が垂直
となると共に、乾燥風が被乾燥物の移送経路を複数回横
切りながら移動するので、設置スペースを小さくするこ
とができると共に、伝熱容量係数を格段に大きくするこ
とができる。
As described above, according to the drying apparatus of the present invention, the material to be dried is circulated and supplied to the drying tower through the storage tank, and the moving path of the drying air in the drying tower is the same as that of the material to be dried. Since it is along the transfer path, it is possible to set an appropriate residence time of the material to be dried, and it is possible to remarkably improve the drying efficiency. A vertical cylindrical body for the drying tower, a screw conveyor having a casing provided with an infinite number of ventilation holes, a vertical partition for axially dividing the cylindrical body and the casing into two parts;
Since the drying tower becomes vertical and the drying air moves a plurality of times through the transfer path of the material to be dried, by forming the horizontal partition in which the divided cylinder and the casing are alternately divided into multiple stages in the radial direction, the drying tower becomes vertical. In addition, the installation space can be reduced, and the heat transfer capacity coefficient can be significantly increased.

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

【図1】本発明に係る乾燥装置の実施の形態の一例であ
る可燃性廃棄物の乾燥設備を示す概略構成図である。
FIG. 1 is a schematic configuration diagram showing a combustible waste drying facility which is an example of an embodiment of a drying apparatus according to the present invention.

【図2】図1におけるII−II線拡大断面図である。FIG. 2 is an enlarged sectional view taken along line II-II in FIG.

【符号の説明】[Explanation of symbols]

1 供給コンベヤ 2 エアーロックダンパー 3 乾燥塔 4 入口 5 入口 6 出口 7 筒体 8 ケーシング 9 スクリューコンベヤ 10 縦仕切り 11 横仕切り 12 保温材 13 乾燥風供給手段 14 熱風発生装置 15 熱風ファン 16 温度計 17 圧力計 18 乾燥風制御器 19 貯留槽 20 ダクト 21 タンク 22 スクレーパコンベヤ 23 製品コンベヤ 24 レベルスイッチ 25 レベルスイッチ 26 水分計 27 ダンパー制御器 28 製品コンベヤ制御器 DESCRIPTION OF SYMBOLS 1 Supply conveyor 2 Air lock damper 3 Drying tower 4 Inlet 5 Inlet 6 Outlet 7 Cylindrical body 8 Casing 9 Screw conveyor 10 Vertical partition 11 Horizontal partition 12 Heat insulator 13 Dry air supply means 14 Hot air generator 15 Hot air fan 16 Thermometer 17 Pressure Total 18 Dry air controller 19 Storage tank 20 Duct 21 Tank 22 Scraper conveyor 23 Product conveyor 24 Level switch 25 Level switch 26 Moisture meter 27 Damper controller 28 Product conveyor controller

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 ホッパーから切り出される被乾燥物を搬
送する供給コンベヤと、供給コンベヤから供給される被
乾燥物を上方へ垂直に移送しながら同方向へ通気される
乾燥風により乾燥する乾燥塔と、乾燥塔へ乾燥風を供給
する乾燥風供給手段と、乾燥塔から排出される被乾燥物
を一時的に貯留すると共に、前記供給コンベヤに循環供
給し、かつ一部を製品として払い出す貯留槽とを備える
ことを特徴とする乾燥装置。
1. A supply conveyor for transporting a material to be dried cut out from a hopper, and a drying tower for drying the material to be dried supplied from the supply conveyor vertically by a drying air passed in the same direction while vertically moving the material to be dried. A drying air supply means for supplying drying air to the drying tower, and a storage tank for temporarily storing the material to be dried discharged from the drying tower, circulating and supplying the same to the supply conveyor, and discharging a part of the drying product. A drying device comprising:
【請求項2】 前記ホッパーの切り出し量が、貯留槽内
の被乾燥物の多少に応じて調節可能に設けられているこ
とを特徴とする請求項1記載の乾燥装置。
2. The drying apparatus according to claim 1, wherein the cut-out amount of the hopper is provided so as to be adjustable according to the amount of the material to be dried in the storage tank.
【請求項3】 前記乾燥塔が、被乾燥物と乾燥風の入口
を下端部にかつ出口を上端部に設けた円筒状の垂直な筒
体と、筒体内に同軸的に配置され、それより適宜小径の
円筒状を呈しかつ無数の通気孔を設けた円筒状のケーシ
ングを有するスクリューコンベヤと、筒体とケーシング
の間を軸方向へ2分割する縦仕切りと、縦仕切りにより
2分割された筒体とケーシングの間を交互に径方向へ多
段分割する横仕切りとからなることを特徴とする請求項
1又は2記載の乾燥装置。
3. The drying tower according to claim 1, wherein the drying tower is provided coaxially with a cylindrical vertical cylinder having an inlet at the lower end and an outlet at the upper end of the drying object and the drying air. A screw conveyor having a cylindrical casing having an appropriately small cylindrical shape and provided with an infinite number of ventilation holes, a vertical partition for dividing the space between the cylindrical body and the casing into two in the axial direction, and a cylinder divided into two by the vertical partition The drying device according to claim 1, further comprising a horizontal partition in which the body and the casing are alternately divided into multiple stages in the radial direction.
【請求項4】 前記乾燥風供給手段が、乾燥塔の入口に
おける乾燥風の温度及びその出口における乾燥風の圧力
に応じて乾燥風の温度及び供給量をそれぞれ調節可能に
設けられていることを特徴とする請求項1,2又は3記
載の乾燥装置。
4. The method according to claim 1, wherein the drying air supply means is provided such that the temperature and the supply amount of the drying air can be adjusted according to the temperature of the drying air at the inlet of the drying tower and the pressure of the drying air at the outlet thereof. The drying device according to claim 1, 2, or 3, wherein
【請求項5】 前記貯留槽の製品払い出し量が、貯留槽
内の被乾燥物の貯留量及び製品出口の被乾燥物の水分量
に応じて調節可能に設けられていることを特徴とする請
求項1,2,3又は4記載の乾燥装置。
5. The product dispensing amount of the storage tank is provided so as to be adjustable in accordance with the storage amount of the material to be dried in the storage tank and the moisture content of the material to be dried at the product outlet. Item 5. A drying device according to Item 1, 2, 3, or 4.
JP8175573A 1996-06-14 1996-06-14 Drying equipment Expired - Fee Related JP2829278B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8175573A JP2829278B2 (en) 1996-06-14 1996-06-14 Drying equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8175573A JP2829278B2 (en) 1996-06-14 1996-06-14 Drying equipment

Publications (2)

Publication Number Publication Date
JPH102668A true JPH102668A (en) 1998-01-06
JP2829278B2 JP2829278B2 (en) 1998-11-25

Family

ID=15998451

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8175573A Expired - Fee Related JP2829278B2 (en) 1996-06-14 1996-06-14 Drying equipment

Country Status (1)

Country Link
JP (1) JP2829278B2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61256179A (en) * 1985-05-07 1986-11-13 井関農機株式会社 Cereal grain drier

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61256179A (en) * 1985-05-07 1986-11-13 井関農機株式会社 Cereal grain drier

Also Published As

Publication number Publication date
JP2829278B2 (en) 1998-11-25

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