JP2006300498A - Coil type drier - Google Patents

Coil type drier Download PDF

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Publication number
JP2006300498A
JP2006300498A JP2005150103A JP2005150103A JP2006300498A JP 2006300498 A JP2006300498 A JP 2006300498A JP 2005150103 A JP2005150103 A JP 2005150103A JP 2005150103 A JP2005150103 A JP 2005150103A JP 2006300498 A JP2006300498 A JP 2006300498A
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JP
Japan
Prior art keywords
coil
container
processed material
drain
drying
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Pending
Application number
JP2005150103A
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Japanese (ja)
Inventor
Kazutaka Yamamoto
和孝 山本
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YAMAMOTO GIKEN KOKI KK
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YAMAMOTO GIKEN KOKI KK
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Priority to JP2005150103A priority Critical patent/JP2006300498A/en
Publication of JP2006300498A publication Critical patent/JP2006300498A/en
Pending legal-status Critical Current

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  • Drying Of Solid Materials (AREA)
  • Treatment Of Sludge (AREA)
  • Accessories For Mixers (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To prevent efficiency degradation by setting a coil rotation direction in a certain direction or by reducing a reverse rotation time by decreasing a moving speed of a processing object by a torsional angle of a coil. <P>SOLUTION: In this coil type drier, drying efficiency can be remarkably increased by stabilization of load capacity in a casing and uniform movement of a processing object by cutting the torsion of a heating coil into pieces and by forming agitating blades with feeding action in the cut parts. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明はコイルのネジレ角による処理物の移動速度を遅くする事により、コイル回転方向を一定方向、又は、逆転時間の減少によりコイル内に発生するドレーンが逆転により排出停止状態を、少時間にする事による効率低下を防ぐ手段である。  In the present invention, by slowing down the moving speed of the processed object due to the coil twist angle, the direction of the coil rotation is fixed, or the drain generated in the coil due to the decrease in the reverse rotation time makes the discharge stop state by the reverse rotation in a short time. This is a means to prevent the efficiency from being reduced.

乾燥の原理より云えば、スクリューコイルの回転数は通常2〜10R/Mが適当とされているが、この回転数にて運転すれば処理物が投入口より排出口への到着時間は10〜30分程度と思われるが、通常乾燥に要する時間は殆ど1時間以上である。この為スクリューコイル逆回転の動作により、処理物を逆送させ滞留時間を延ばしているが、その間のドレーンの排出量は減り能力は減少し、容器内の処理物の片寄現象が起こっている。  According to the principle of drying, the rotational speed of the screw coil is normally 2 to 10 R / M. However, if the rotational speed of the screw coil is operated, the arrival time of the processed material from the inlet to the outlet is 10 to 10. Although it seems to be about 30 minutes, the time required for normal drying is almost 1 hour or more. For this reason, the treatment product is reversely rotated by the reverse rotation of the screw coil to extend the staying time. However, the drainage amount during that time is reduced, the capacity is reduced, and the collateral phenomenon of the treatment product in the container occurs.

送りを遅くする為、図1の(A)コイルピッチを小とした場合はコイル外周に図1の(B)の如く処理物が附着し、共まわり現象が起こりコイル接触が不十分となる為、伝熱量が小さくなり乾燥効果が小さくなる。又、中央シャフトの方向に処理物が落ちにくく乾燥効果は著しく落ちる。微紛物に関しても処理物に水分が多い場合は殆どこの現象が通常起こっており、又シャフト、及びコイルサポート部の清掃は困難となる。  If the coil pitch in Fig. 1 (A) is made small to slow down the feed, the treated material will be attached to the outer circumference of the coil as shown in Fig. 1 (B), causing a co-rotation phenomenon and insufficient coil contact. The amount of heat transfer is reduced and the drying effect is reduced. In addition, the processed material is less likely to fall in the direction of the central shaft, and the drying effect is significantly reduced. In the case of fine powders, this phenomenon usually occurs when the processed material contains a lot of moisture, and it is difficult to clean the shaft and the coil support part.

コイルピッチを大とした場合、処理物はシャフト側に落下、処理物の殆どコイル上面に附着しなくはなるが、送り速度が早くなり再々羽根回転方向は変える必要が出る為、コイル内のドレーン排出は困難な状況となり熱効率は下がり乾燥が悪くなる欠点がある。  When the coil pitch is increased, the processed material falls to the shaft side, and almost all of the processed material does not attach to the upper surface of the coil, but the feed speed becomes faster and the blade rotation direction needs to be changed again. Discharging is difficult, and heat efficiency is lowered, resulting in poor drying.

コイルネジ方向は連続式とバッチ式とにより異なるが、以下の方式が考えられる。
(1)右ネジ、継ぎ材、右ネジ、継ぎ材、の繰り返し
(2)右ネジ、継ぎ材、右ネジ、継ぎ材、繰り返し後、左ネジ、継ぎ材、左ネジ、継ぎ材、の繰り返し
(3)右ネジ、継ぎ材、左ネジ、継ぎ材、右ネジ、継ぎ材、左ネジ、継ぎ材
以上様々全ての組合せ方式
Although the coil screw direction differs depending on the continuous type and the batch type, the following methods are conceivable.
(1) Repeat of right screw, joint material, right screw, joint material (2) Repeat of right screw, joint material, right screw, joint material, repeated left screw, joint material, left screw, joint material ( 3) All combinations of right screw, joint material, left screw, joint material, right screw, joint material, left screw, joint material and more

図1は従来のコイル式乾燥機で、コイルが連続のコイル状になっている為、8より投入した処理物は9に到着する時間が短く乾燥が不十分な製品が出る。これをふせぐ為図2のコイルピッチAを小さく、Dの継ぎ材によりコイルによる処理物の送りは完全に途切れ、処理物の押付圧による移動のみの運動に変わり、移動速度は減少し継ぎ材の部分で図2のCの方向に処理物は落下し、落下運動及びシャフトとの衝突動作により、処理物の拡散効果を発揮し、乾燥を促進します。尚、コイルの伝熱面積を多くする為、図1のA寸法よりも図2のA寸法を小さくするのは手段の一つです。  FIG. 1 shows a conventional coil dryer, which has a continuous coil shape, so that the processed material introduced from 8 has a short time to reach 9 and results in an insufficiently dried product. In order to prevent this, the coil pitch A in FIG. 2 is reduced, and the feed of the processed material by the coil is completely interrupted by the joint material of D, and the movement is only moved by the pressing pressure of the processed material. The processed material falls in the direction of C in Fig. 2, and the effect of diffusing the processed material is exerted by the falling motion and the collision with the shaft to promote drying. In order to increase the heat transfer area of the coil, it is one of the means to make the A dimension in FIG. 2 smaller than the A dimension in FIG.

図5は、請求項3の参考図です。左ネジ、継ぎ材、右ネジ、継ぎ材、の繰り返しにて、組合せる場合出来るだけ加熱コイルにドレーンが溜まりにくい状態にする方が効果が良くなる故、この方法を使いますと、1ブロック当りの加熱コイル長さを短く形成する事が可能であり、ドレーンのつまりを防ぐ手段として使います。  FIG. 5 is a reference diagram of claim 3. When it is combined by repeating the left screw, joint material, right screw, and joint material, it is more effective to make it difficult for the heating coil to collect drainage. It is possible to shorten the length of the heating coil and use it as a means to prevent drain clogging.

Claims (3)

蒸気を保有するジャケット付、又はジャケットなしのもので容器内に水分の含んだ汚泥又は粉体、又は残渣類(以後処理物と云う)を保留し、その中に攪拌・混合・搬送動作を行う羽根を具備したコイルを円筒ネジ式に巻きつけ、さらにこのコイルにも蒸気を入れながら回転させる事により処理物を加熱、水分蒸発させる乾燥機において、従来のコイルをエンドレス、つまり全ネジ式に巻きつけている方式を数本のネジ式を1ブロックとし、又はネジレ寸法をゼロ、つまりネジレ無しとした各々のコイルを1ブロックとし、数ブロック継ぎ合わせた構造熱源体とする事により一定方向の回転で処理物の容器内の移動速度調整可能となり滞留時間の調整も可能なコイル式乾燥装置。  With or without a jacket that holds steam, hold sludge or powder containing moisture, or residues (hereinafter referred to as treated products) in a container, and perform stirring, mixing, and conveying operations in the container. In a dryer that heats the processed material and evaporates moisture by winding a coil with blades around a cylindrical screw and rotating the coil while steaming it, the conventional coil is wound endlessly, that is, fully threaded. Rotating in a certain direction by using several screw types as one block, or by setting each coil with zero torsion, that is, each coil with no twist, as a structure heat source body joined together by several blocks A coil-type drying device that can adjust the moving speed of the processed material in the container and adjust the residence time. 装置内に蒸気供給用ヘッドパイプを設け、このパイプより各々の1〜数ブロックに1ヶ所蒸気を供給し、他方ドレーン収穫用ヘッドパイプには各供給箇所よりのドレーンを回収出来る構造とする事により請求項1項の変形装置として、高能率の乾燥能力が得られるコイル式乾燥装置。  By providing a steam supply head pipe in the device, supplying steam to each one to several blocks from this pipe, while drain drain head pipe has a structure that can collect the drain from each supply point A coil-type drying device capable of obtaining a high-efficiency drying capability as the deformation device according to claim 1. この程の乾燥方式には連続投入方式、つまり容器の片端より処理物を連続投入し、他端より乾燥品処理物を連続排出する方式と一括投入方式、つまり容器内に処理物を排出口を閉としたまま一括投入し、乾燥時間内滞留させた後、排出口を開として処理物を排出する方式、のどちらが適応するコイル式乾燥装置。  In this drying method, a continuous charging method, that is, a process product is continuously input from one end of the container, and a dry product processed product is continuously discharged from the other end, and a batch input method, that is, an outlet for discharging the processed material in the container is provided. Coil-type drying device that can be applied either in a closed manner, after being put in a lump and staying within the drying time, and then opening the outlet and discharging the processed material.
JP2005150103A 2005-04-19 2005-04-19 Coil type drier Pending JP2006300498A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2005150103A JP2006300498A (en) 2005-04-19 2005-04-19 Coil type drier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2005150103A JP2006300498A (en) 2005-04-19 2005-04-19 Coil type drier

Publications (1)

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JP2006300498A true JP2006300498A (en) 2006-11-02

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JP2005150103A Pending JP2006300498A (en) 2005-04-19 2005-04-19 Coil type drier

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101004154B1 (en) 2010-02-26 2010-12-27 대일개발 주식회사 Method for remediating contaminated soil using subcritical water

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101004154B1 (en) 2010-02-26 2010-12-27 대일개발 주식회사 Method for remediating contaminated soil using subcritical water

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