JPS61138084A - Steam pipe type rotary drier with finishing drying section - Google Patents

Steam pipe type rotary drier with finishing drying section

Info

Publication number
JPS61138084A
JPS61138084A JP26004684A JP26004684A JPS61138084A JP S61138084 A JPS61138084 A JP S61138084A JP 26004684 A JP26004684 A JP 26004684A JP 26004684 A JP26004684 A JP 26004684A JP S61138084 A JPS61138084 A JP S61138084A
Authority
JP
Japan
Prior art keywords
drying section
steam pipe
dried
type rotary
steam
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
JP26004684A
Other languages
Japanese (ja)
Inventor
勇 藤原
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.)
Mitsui Engineering and Shipbuilding Co Ltd
Original Assignee
Mitsui Engineering and Shipbuilding 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 Mitsui Engineering and Shipbuilding Co Ltd filed Critical Mitsui Engineering and Shipbuilding Co Ltd
Priority to JP26004684A priority Critical patent/JPS61138084A/en
Publication of JPS61138084A publication Critical patent/JPS61138084A/en
Pending legal-status Critical Current

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  • Drying Of Solid Materials (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】 〔産業上の利用分野〕 本発明は乾燥効率の悪い部分に流動層乾燥装置からなる
仕上乾燥部を有する蒸気管式回転乾燥機に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a steam tube type rotary dryer having a finish drying section consisting of a fluidized bed dryer in a portion with poor drying efficiency.

〔従来技術〕[Prior art]

スチームチューブドライヤーとも称される従来の蒸気管
式回転乾燥機においては、回転するドラム内に導入した
被乾燥物を熱源である蒸気管からの伝熱により過熱して
水分を蒸発させ、その蒸発した水分をキャリヤーガスに
より糸外に排出乾燥させている。
In a conventional steam tube rotary dryer, also known as a steam tube dryer, the material to be dried introduced into a rotating drum is superheated by heat transfer from the steam tube, which is the heat source, to evaporate moisture. Moisture is removed from the yarn using a carrier gas and dried.

しかしながら、この方式の蒸気管式回転乾燥機では、キ
ャリヤーガスと被乾燥物との接触が悪いため、製品乾燥
度が低水分上要求された場合、減率乾燥域効率が必ずし
も良いものとはならないという欠点があった。
However, in this type of steam tube rotary dryer, the contact between the carrier gas and the material to be dried is poor, so when product dryness is required to be low in moisture, the lapse rate drying area efficiency is not necessarily good. There was a drawback.

〔発明の目的〕[Purpose of the invention]

そこで本発明は、前記従来の蒸気管式乾燥機の欠点を解
消し、蒸気管式回転乾燥機の特徴を最大限に生した恒率
乾燥域では従来通りの蒸気管式乾燥方式とし、効率の悪
い減率乾燥域では流動層乾燥方式をとり入れることによ
り、製品乾燥度が低水分上要求される場合にも充分対応
できる蒸気管式回転乾燥機を提供することを目的とした
ものである。
Therefore, the present invention eliminates the drawbacks of the conventional steam tube dryer, and uses the conventional steam tube drying method in the constant rate drying region, which maximizes the characteristics of the steam tube rotary dryer, to improve efficiency. The purpose of this invention is to provide a steam tube type rotary dryer that can sufficiently handle cases where product dryness is required to be low in moisture by incorporating a fluidized bed drying system in the poor lapse rate drying region.

〔発明の構成〕[Structure of the invention]

即ち、本発明の仕上乾燥部を有する蒸気管式回転乾燥機
は、回転するドラム内に蒸気管を熱源として配設した蒸
気管式回転乾燥機において、そのドラムの被乾燥物出口
の周囲にフードを設けると共に、そのフード内に流動層
乾燥装置を設けることにより構成される。
That is, the steam tube type rotary dryer having a finish drying section of the present invention is a steam tube type rotary dryer in which a steam tube is disposed in a rotating drum as a heat source, and a hood is provided around the outlet of the material to be dried in the drum. It is constructed by providing a fluidized bed drying device within the hood.

〔実施例〕〔Example〕

以下図面を参照して本発明の詳細な説明するが、第1図
は本発明の一実施例における蒸気管式回転乾燥機の側断
面図、第2図は第1図のA−A方向の正断面図、第3図
は第1図のドラムとフード部とのシール部を示す要部拡
大の側断面図である。
The present invention will be described in detail below with reference to the drawings. FIG. 1 is a side sectional view of a steam pipe rotary dryer according to an embodiment of the present invention, and FIG. 3 is a front sectional view, and FIG. 3 is an enlarged side sectional view of a main part showing the sealing portion between the drum and the hood portion of FIG. 1.

まず、この回転乾燥機は図示されていないモータ及びチ
ェノなどで駆動されるローラ1に支持されながらタイヤ
−2を介して回転するドラム3からなり、第1図に示す
そのドラム3の右側、即ち下流側には、圧力回転接手4
で接続された蒸気人口5が設けられ、この蒸気人口5か
ら導入された熱媒体である蒸気Sがこのドラム3を長手
方向に貫通して設けられた多数の蒸気管6内を循環して
被乾燥物Mに伝熱した後、ドレン出ロアから排出される
First, this rotary dryer consists of a drum 3 that rotates via tires 2 while being supported by a roller 1 driven by a motor and a chino (not shown). On the downstream side, there is a pressure rotary joint 4.
A steam pipe 5 connected to the drum 3 is provided, and steam S, which is a heat medium, introduced from the steam pipe 5 is circulated through a large number of steam pipes 6 provided to penetrate this drum 3 in the longitudinal direction, and is covered with steam. After the heat is transferred to the dried material M, it is discharged from the drain outlet lower part.

一方、この回転乾燥機により乾燥される被乾燥物Mは、
上流側に設けた被乾燥物人口9から導入され、キャリヤ
ーガス入口10から導入されたキャリヤーガスGにより
、矢印R方向に回転するドラム3を下流側に移動しなが
ら乾燥して下流側の被乾燥物出口11から取り出される
と共に、下流側上達したキャリヤーガスGはキャリヤー
ガス出口12から排出されるようになっている。
On the other hand, the dried material M to be dried by this rotary dryer is
The carrier gas G introduced from the drying target 9 provided on the upstream side and the carrier gas G introduced from the carrier gas inlet 10 dries the drum 3 rotating in the direction of arrow R while moving it downstream. The carrier gas G that is taken out from the material outlet 11 and has reached the downstream side is discharged from the carrier gas outlet 12.

なお、被乾燥物Mによっては、キャリヤーガスGの流れ
を上記実施例と逆方向に流すこともできる。
Note that, depending on the material M to be dried, the flow of the carrier gas G can also be made to flow in the opposite direction to that in the above embodiment.

そこで本発明では、ドラム3の被乾燥物出口11の周囲
にリング状の円筒からなるフード13を設けると共に、
そのフード13の下部に第2図に示すごとく流動床14
及びその下部の熱風導入ホッパー15からなる流動層乾
燥装置を設け、この熱風導入ホッパー15の下部から流
動床14を経由して図示されていないブロアー及びエア
ヒータからの熱風Hを導入して、被乾燥物出口11から
このフード13内に落下した被乾燥物Mを更に仕上乾燥
せしめ、その乾燥された製品をエアーロ・7クパルブ1
6経由取出すようになっている。
Therefore, in the present invention, a hood 13 made of a ring-shaped cylinder is provided around the dried material outlet 11 of the drum 3, and
At the bottom of the hood 13 is a fluidized bed 14 as shown in FIG.
A fluidized bed drying device is provided, which includes a hot air introduction hopper 15 at the bottom of the hot air introduction hopper 15, and hot air H from a blower and an air heater (not shown) is introduced from the bottom of the hot air introduction hopper 15 through the fluidized bed 14 to dry the dried material. The material M to be dried that has fallen into the hood 13 from the material outlet 11 is further dried, and the dried product is transferred to the Aero7 Cup 1.
It is designed to be taken out via 6.

以上のごとく、この回転乾燥機においては、第1図にて
Xで示す範囲が従来同様の蒸気管式乾燥部であり、Yで
示す範囲が仕上乾燥部になっている。
As described above, in this rotary dryer, the area indicated by X in FIG. 1 is the steam pipe type drying section similar to the conventional one, and the area indicated by Y is the finishing drying section.

なお、このフード13とドラム3との接合部は、第3図
に示すごと(回転するドラム3側外周に廻り止めボルト
17で取付けたシール18に対し、固定されたフード1
3側に押えスプリング19で押えられたシール20が接
触してシール性を保つようになっている。
The joint between the hood 13 and the drum 3 is as shown in FIG.
A seal 20 pressed by a pressing spring 19 is in contact with the third side to maintain sealing performance.

〔発明の効果〕〔Effect of the invention〕

従って、本発明の蒸気管式回転乾燥機は、従来の蒸気管
式乾燥機の特徴を最大限に生かしながら、乾燥効率の悪
い下流側に流動層乾燥方式を仕上乾燥部として取り入れ
ているので、上記仕上乾燥部に必要な熱は蒸気管式回転
乾燥機で加熱された被乾燥物の顕熱を最大限に利用する
ことができ、乾燥工程の大幅省エネ化が可能である。
Therefore, the steam tube type rotary dryer of the present invention takes full advantage of the features of the conventional steam tube type dryer while incorporating a fluidized bed drying method as a finishing drying section on the downstream side where drying efficiency is low. As the heat required for the finishing drying section, the sensible heat of the material to be dried heated in the steam tube rotary dryer can be utilized to the maximum extent, making it possible to significantly save energy in the drying process.

また、蒸気管式回転乾燥機と仕上乾燥部とが一体化され
ているので、乾燥機全体の長さを短かくできると共に、
仕上乾燥部での分級処理も可能になるという利点もある
In addition, since the steam tube rotary dryer and the finish drying section are integrated, the length of the entire dryer can be shortened, and
Another advantage is that classification processing can also be performed in the finishing drying section.

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

第1図は本発明の一実施例における蒸気管式回転乾燥機
の一部破断の側断面図、第2図は第1図のA−A方向の
正断面図、第3図は第1図のドラムとフード部とのシー
ル部を示す要部拡大の側断面図である。 1・・・ローラ、3・・・ドラム、6・・・蒸気管、1
1・・・被乾燥物出口、13・・・フード、14・・・
流動床、15・・・熱風導入ホッパー、H・・・熱風、
M・・・被乾燥物、R・・・回転方向、S・・・蒸気、
Y・・・仕上乾燥部。
FIG. 1 is a partially cutaway side sectional view of a steam tube rotary dryer according to an embodiment of the present invention, FIG. 2 is a front sectional view taken along the line A-A in FIG. 1, and FIG. FIG. 3 is an enlarged side sectional view of a main part showing a sealing part between the drum and the hood part. 1...roller, 3...drum, 6...steam pipe, 1
1... Outlet of dried material, 13... Hood, 14...
Fluidized bed, 15...Hot air introduction hopper, H...Hot air,
M...material to be dried, R...rotation direction, S...steam,
Y... Finishing drying section.

Claims (1)

【特許請求の範囲】[Claims] 回転するドラム内に蒸気管を熱源として配設した蒸気管
式回転乾燥機において、該ドラムの被乾燥物出口の周囲
にフードを設けると共に、該フード内に流動層乾燥装置
を設けたことを特徴とする仕上乾燥部を有する蒸気管式
回転乾燥機。
A steam tube type rotary dryer in which a steam tube is disposed as a heat source in a rotating drum, characterized in that a hood is provided around the outlet of the material to be dried in the drum, and a fluidized bed drying device is provided within the hood. A steam pipe rotary dryer with a finishing drying section.
JP26004684A 1984-12-11 1984-12-11 Steam pipe type rotary drier with finishing drying section Pending JPS61138084A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26004684A JPS61138084A (en) 1984-12-11 1984-12-11 Steam pipe type rotary drier with finishing drying section

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26004684A JPS61138084A (en) 1984-12-11 1984-12-11 Steam pipe type rotary drier with finishing drying section

Publications (1)

Publication Number Publication Date
JPS61138084A true JPS61138084A (en) 1986-06-25

Family

ID=17342547

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26004684A Pending JPS61138084A (en) 1984-12-11 1984-12-11 Steam pipe type rotary drier with finishing drying section

Country Status (1)

Country Link
JP (1) JPS61138084A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012026629A (en) * 2010-07-22 2012-02-09 Tsukishima Kikai Co Ltd Horizontal type tumble drier
JP2012026631A (en) * 2010-07-22 2012-02-09 Tsukishima Kikai Co Ltd Method for drying and classifying object to be treated
JP2012026632A (en) * 2010-07-22 2012-02-09 Tsukishima Kikai Co Ltd Method for drying and classifying object to be treated
JP2012026630A (en) * 2010-07-22 2012-02-09 Tsukishima Kikai Co Ltd Horizontal type tumble drier

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012026629A (en) * 2010-07-22 2012-02-09 Tsukishima Kikai Co Ltd Horizontal type tumble drier
JP2012026631A (en) * 2010-07-22 2012-02-09 Tsukishima Kikai Co Ltd Method for drying and classifying object to be treated
JP2012026632A (en) * 2010-07-22 2012-02-09 Tsukishima Kikai Co Ltd Method for drying and classifying object to be treated
JP2012026630A (en) * 2010-07-22 2012-02-09 Tsukishima Kikai Co Ltd Horizontal type tumble drier

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