JP3077061U - Continuous drying equipment - Google Patents
Continuous drying equipmentInfo
- Publication number
- JP3077061U JP3077061U JP2000007451U JP2000007451U JP3077061U JP 3077061 U JP3077061 U JP 3077061U JP 2000007451 U JP2000007451 U JP 2000007451U JP 2000007451 U JP2000007451 U JP 2000007451U JP 3077061 U JP3077061 U JP 3077061U
- Authority
- JP
- Japan
- Prior art keywords
- drying
- duct
- dried
- product
- hot air
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Drying Of Solid Materials (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
(57)【要約】
【課題】 含水率の高いおから、食品残渣などの有機性
廃棄物等を安定して乾燥粒状体とするために、乾燥物の
一部を水分調整剤として返送し投入物と混合し機内で解
砕、攪拌、乾燥を促進させ、気流乾燥ダクト内で乾燥状
体を調整出来る連続乾燥装置を提供する。
【解決手段】 投入口(7)より投入された未乾燥物は
気流乾燥下降ダクト(9)より返送された水分調整剤と
しての乾燥物の一部と混合され、熱風入口(3)方向に
移動する。高速回転する攪拌羽根(6)により機内で解
砕、拡散しながら熱風と接触し乾燥が促進され、比重が
軽くなった物から気流に乗り、出口(4)より竪型の気
流乾燥上昇ダクト(8)に吸い込まれていく。この気流
乾燥上昇ダクト(8)内でも気体の流速の制御により二
度目の乾燥物と未乾燥物の分離が行われる。気流乾燥下
降ダクト(9)まで到達した乾燥物は重力の慣性力と固
気分離装置(2)内に誘引される吸引力との強弱により
三度目の分離が行われる。
(57) [Summary] [PROBLEMS] To return organic wastes such as food residues and other organic wastes with a high moisture content to dry granules in a stable manner, a part of the dried products is returned as a water conditioner and put in. Provided is a continuous drying apparatus capable of mixing with a product, promoting crushing, stirring, and drying in the machine, and adjusting a dried material in a flash drying duct. SOLUTION: An undried product supplied from an input port (7) is mixed with a part of a dried product as a moisture regulator returned from a flash drying and lowering duct (9), and moves toward a hot air inlet (3). I do. The high-speed rotating stirring blades (6) disintegrate and diffuse in the machine while being in contact with hot air to promote drying. The material whose specific gravity has become lighter enters the airflow, and a vertical airflow drying duct (from the outlet (4)). 8) is sucked. The second drying of the dried product and the undried product are also performed in the airflow drying up duct (8) by controlling the gas flow rate. The dried matter reaching the air-flow drying lowering duct (9) is separated for the third time by the strength of the inertia force of gravity and the suction force induced in the solid-gas separation device (2).
Description
【0001】[0001]
この発明は、例えばおから、食品残渣などの有機性廃棄物等を効率よく連続し て乾燥させるための連続乾燥装置に関するものである。 The present invention relates to a continuous drying apparatus for efficiently and continuously drying organic wastes such as okara and food residues.
【0002】[0002]
従来から、連続乾燥装置としては、ロ−タリ−式乾燥機で熱風を吹込み、回転 により乾燥物が移動しながら乾燥する方式、円筒内部をスクリュ−コンベア−で 移動しながら外部より加熱蒸気で間接的に加熱し乾燥する方式、又は熱風と乾燥 物が高速で移動しながら乾燥する気流乾燥機(例えば特開2000−65476 号)等が一般的である。 Conventionally, as a continuous drying device, a rotary dryer dries hot air, and the dried material is dried while moving by rotation, while the inside of the cylinder is moved by a screw conveyor and heated steam is supplied from outside. In general, a method of indirect heating and drying, or a flash dryer (for example, JP-A-2000-65476) in which hot air and a dried material are dried while moving at a high speed is generally used.
【0003】[0003]
このように有機性廃棄物等を回転式で連続乾燥する方式は、装置が長大に成り 乾燥むらをなくすためには必要以上に乾燥しなければ成らない。 As described above, in the method of continuously drying organic waste or the like by a rotary method, it is necessary to dry more than necessary in order to eliminate the drying of the apparatus due to its large size.
【0004】 また、気流乾燥機でも事前の水分調整が必要であり、固気分離装置で固形分を 回収する場合、サイクロン等は遠心力を利用して分離するために未乾燥で比重が 重たい物まで回収してしまう。[0004] Furthermore, a flash dryer also needs to adjust the water content in advance, and when recovering solids with a solid-gas separator, cyclones and the like are undried and have a high specific gravity because they are separated by centrifugal force. Will be collected.
【0005】[0005]
本考案は、以上の目的を達成するために、投入口(7)より投入された未乾燥 物は気流乾燥下降ダクト(9)より返送された水分調整剤としての乾燥物の一部 と混合され、熱風入口(3)方向に送りスクリュ−(5)により移動する。高速 回転する攪拌羽根(6)により機内で解砕、拡散しながら熱風と接触し乾燥が促 進され、比重が軽くなった物から気流に乗り、固気出口(4)より竪型の気流乾 燥上昇ダクト(8)に吸い込まれていく。この気流乾燥上昇ダクト(8)内でも 気体の流速の制御により二度目の乾燥物と未乾燥物の分離が行われる。気流乾燥 下降ダクト(9)まで到達した乾燥物は重力の慣性力と固気分離装置(2)内に 誘引される吸引力との強弱により三度目の分離が行われる。 According to the present invention, in order to achieve the above object, the undried material supplied from the inlet (7) is mixed with a part of the dried material as a water conditioning agent returned from the flash drying duct (9). Is moved by the feed screw (5) in the direction of the hot air inlet (3). The high-speed rotating stirring blades (6) disintegrate and spread inside the machine while contacting with the hot air to promote drying. The material whose specific gravity becomes lighter enters the airflow, and the vertical airflow drying from the solid-air outlet (4). It is sucked into the drying rise duct (8). The second drying of the dried product and the undried product are also performed in the airflow drying up duct (8) by controlling the gas flow rate. Flash drying The dried product that has reached the descending duct (9) is separated for the third time by the strength of the inertia force of gravity and the suction force induced in the solid-gas separation device (2).
【0006】[0006]
本考案の実施例を添付図面にもとづき説明する。乾燥機(1)の一方に熱風発 生装置に連通している熱風入口(3)が有り、他方には気流乾燥上昇ダクト(8 )に連通している固気出口(4)が有る。 An embodiment of the present invention will be described with reference to the accompanying drawings. One of the dryers (1) has a hot air inlet (3) communicating with the hot air generator, and the other has a solid air outlet (4) communicating with the flash drying duct (8).
【0007】 内部には駆動装置に連結した攪拌羽根(6)と、投入口(7)と気流乾燥下降 ダクト(9)に連通した送りスクリュ−(5)が有る。There are a stirring blade (6) connected to the driving device, and a feed screw (5) communicating with the inlet (7) and the flash drying down duct (9).
【0008】 竪型の気流乾燥上昇ダクト(8)と連通した気流乾燥下降ダクト(9)は途中 より誘引フアンに接続された排気口(13)、乾燥物の排出口(12)を備えた 固気分離装置(2)に連通している。[0008] A flash drying duct (9) communicating with the vertical flash drying duct (8) is provided with an exhaust port (13) connected to an inducing fan and a dried product discharge port (12) from the middle. It communicates with the gas separation device (2).
【0009】 固気分離装置(2)の入口側には固気分離用調整弁(10)が有る。[0009] At the inlet side of the solid-gas separation device (2), there is a regulating valve (10) for solid-gas separation.
【0010】[0010]
以上に説明したように、本考案の有機性廃棄物等の連続乾燥装置は、乾燥機( 1)の内部に水分調整された未乾燥物が搬送され、解砕、攪拌、表面積の拡大、 熱風との接触、乾燥が促進される。気流に乗りきれない重たい未乾燥物は下に落 下し送りスクリュ−(5)により熱風入口(3)方向に搬送されここで一度目の 分離が行われる。二度目の分離は竪型の気流乾燥上昇ダクト(8)で上昇気流に 乗れた物と乗れない物に分離される。気流乾燥下降ダクト(9)内では、乾燥物 は重力の慣性力と固気分離装置(2)内に誘引される吸引力との強弱により三度 目の分離が行われ、装置の小型化、熱効率の向上、作業の省力化等の効果を有し 、有機性廃棄物等の連続乾燥に適した乾燥が出来る。 As described above, the continuous drying apparatus for organic waste and the like according to the present invention transports the undried substance whose water content has been adjusted inside the dryer (1), and crushes, agitates, expands the surface area, and generates hot air. Contact and drying are promoted. The heavy undried material that cannot catch the air flow falls down and is conveyed to the hot air inlet (3) by the feed screw (5), where the first separation is performed. The second separation is carried out by the vertical airflow drying rising duct (8) to separate those that got on the updraft and those that couldn't. In the airflow drying and lowering duct (9), the dried matter is separated for the third time by the strength of the inertia force of gravity and the suction force induced in the solid-gas separation device (2). It has the effect of improving thermal efficiency and saving labor, and can perform drying suitable for continuous drying of organic waste and the like.
【図1】本考案の平面図である。FIG. 1 is a plan view of the present invention.
【図2】本考案の立面図である。FIG. 2 is an elevation view of the present invention.
【符号の説明】 1 乾燥機 2 固気分離装置 3 熱風入口 4 固気出口 5 送りスクリュ− 6 攪拌羽根 7 投入口 8 気流乾燥上昇ダクト 9 気流乾燥下降ダクト 10 固気分離用調整弁 11 ダクト 12 排出口 13 排気口 14 駆動装置[Description of Signs] 1 Dryer 2 Solid-Gas Separation Device 3 Hot Air Inlet 4 Solid-Gas Outlet 5 Feed Screw 6 Stirring Blade 7 Input Port 8 Airflow Drying Up Duct 9 Airflow Drying Downduct 10 Adjustment Valve 11 Exhaust port 13 Exhaust port 14 Drive unit
Claims (1)
気流乾燥下降ダクト(9)に連通し乾燥物の一部を水分
調整用に混合返送する送りスクリュ−(5)と攪拌羽根
(6)を内蔵した乾燥装置(1)の一方に熱風発生装置
に連通した熱風入口(3)、他方に気流乾燥上昇ダクト
(8)と気流乾燥下降ダクト(9)に連通した固気出口
(4)を備え、気流乾燥下降ダクト(9)の途中に固気
分離装置(2)に連通したダクト(11)を備えた固気
分離装置(2)を包含することを特徴とする連続乾燥装
置。1. A feed screw (5), which communicates with an inlet (7) and a flash drying descent duct (9) inside a dryer (1) to mix and return a part of the dried product for moisture adjustment. A hot air inlet (3) communicating with a hot air generating device is connected to one side of a drying device (1) having a built-in stirring blade (6), and a solid air communicating with a flash drying up duct (8) and a flash drying down duct (9) on the other side. A continuity characterized by comprising a solid-gas separator (2) with an outlet (4) and a duct (11) communicating with the solid-gas separator (2) in the middle of the gas-flow drying down duct (9). Drying equipment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000007451U JP3077061U (en) | 2000-10-18 | 2000-10-18 | Continuous drying equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000007451U JP3077061U (en) | 2000-10-18 | 2000-10-18 | Continuous drying equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
JP3077061U true JP3077061U (en) | 2001-05-11 |
Family
ID=43210090
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2000007451U Expired - Fee Related JP3077061U (en) | 2000-10-18 | 2000-10-18 | Continuous drying equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3077061U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003096452A (en) * | 2001-07-19 | 2003-04-03 | Soruteko Kk | Composition for soil consisting of industrial waste |
-
2000
- 2000-10-18 JP JP2000007451U patent/JP3077061U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003096452A (en) * | 2001-07-19 | 2003-04-03 | Soruteko Kk | Composition for soil consisting of industrial waste |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |