JP2001091156A - Multistage drying device - Google Patents

Multistage drying device

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Publication number
JP2001091156A
JP2001091156A JP26486699A JP26486699A JP2001091156A JP 2001091156 A JP2001091156 A JP 2001091156A JP 26486699 A JP26486699 A JP 26486699A JP 26486699 A JP26486699 A JP 26486699A JP 2001091156 A JP2001091156 A JP 2001091156A
Authority
JP
Japan
Prior art keywords
drying
stage
drying surface
dried
hot gas
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
JP26486699A
Other languages
Japanese (ja)
Inventor
Masakumi Hiroe
正九三 廣江
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.)
AZU KIYARIA KK
Original Assignee
AZU KIYARIA KK
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 AZU KIYARIA KK filed Critical AZU KIYARIA KK
Priority to JP26486699A priority Critical patent/JP2001091156A/en
Publication of JP2001091156A publication Critical patent/JP2001091156A/en
Pending legal-status Critical Current

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  • Drying Of Solid Materials (AREA)

Abstract

PROBLEM TO BE SOLVED: To extremely prevent the generation of powder dust compared with this kind of a conventional drying device, to provide a flow passage with structure to be decreased in an influence exercised on a drop port for a substance to be dried without narrowing a flow passage for hot gas, and to increase the size of the whole of the device through planer enlargement without increasing only height. SOLUTION: This drying device is divided into a first chamber having a drying surface 7A; a second chamber having a drying surface 7B; a third chamber having a drying surface 7C; and a fourth chamber having a drying surface 7D. A step being low in a head between present and subsequent drying surfaces and a substance to be dried drop to a subsequent surface are formed at and in the drying surface 7A or 7D. Chambers are disposed in a helical stair-form state from a topmost step to a lowermost step through intercoupling the adjoining steps, and constitution is performed such that the substance to be dried is dropped, in order, from the topmost step to the lowermost step through a step low in a head. Further, the flow passage cross section of an opening part for a hot gas flow passage is enlarged as much as possible.

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、多段乾燥装置にお
けるおのおのの段の乾燥面を複数の乾燥面に分割し互い
に段差をつけて配設し、左右交互ジグザグ階段状もしく
は回り階段状の連続した段差を有する乾燥面を備えた多
段乾燥装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a multistage drying apparatus, in which the drying surface of each stage is divided into a plurality of drying surfaces, and the drying surfaces are arranged with a step difference therebetween. The present invention relates to a multi-stage drying apparatus provided with a drying surface having a step.

【0002】[0002]

【従来の技術】汚泥物質等を熱ガス等によって乾燥する
従来の多段乾燥装置として、実公平5−37194号公
報に記載されたものがある。この種の多段乾燥装置の構
成を図4(a),(b)により説明する。
2. Description of the Related Art As a conventional multi-stage drying apparatus for drying sludge material or the like by a hot gas, there is one disclosed in Japanese Utility Model Publication No. 5-37194. The configuration of this type of multi-stage drying apparatus will be described with reference to FIGS.

【0003】図4において、1はキャスタブル耐火材で
成形された乾燥室であり、上部一端側に被乾燥物導入口
2が、また、下部他端側に被乾燥物排出口3が、それぞ
れ配設されている。該被乾燥物導入口2には、供給ホッ
パー4aとスクリューコンベア5aを備えた供給装置6
aが、また、被乾燥物排出口3には、排出シュート4b
とスクリューコンベア5bを備えた排出装置6bが、そ
れぞれ連設されている。
In FIG. 4, reference numeral 1 denotes a drying chamber formed of a castable refractory material, and a drying object inlet 2 is provided at one upper end, and a drying object discharge port 3 is provided at the lower other end. Has been established. A supply device 6 having a supply hopper 4a and a screw conveyor 5a is provided in the drying object introduction port 2.
a, and a discharge chute 4b
And a discharge device 6b having a screw conveyor 5b are connected to each other.

【0004】乾燥室1内は、上面が乾燥面7となる耐熱
金属板8で高さ方向にほぼ等間隔に平行に区分されてい
る。また各段の金属板8の互いに反対側の一端は切欠か
れて上段と下段の乾燥面7を連通する連通口10が形成
され、この連通口10によって多段をなす各段の乾燥面
7が一連に連結されている。そして最上段の乾燥面7に
前記被乾燥物導入口2が連通され、最下段の連通口10
に被乾燥物排出口3が連通されている。さらに、最上段
から1段下と最下段の乾燥面7の一方の側壁を構成する
乾燥室1の側壁部には、それぞれ熱ガス導入口11とガ
ス排出口12とが開口されている。図示例における熱ガ
スの流路は、その流路断面幅が乾燥面7の横幅に対して
半分以下に絞られており、複数段の乾燥面7にて上段側
から下段側へ流れるように形成されている。なお、熱ガ
スの流通経路は、同示例とは逆に下段から上段へ流れる
ように形成してもよい。
The inside of the drying chamber 1 is divided in parallel at substantially equal intervals in the height direction by a heat-resistant metal plate 8 having an upper surface serving as a drying surface 7. The opposite ends of the metal plate 8 of each stage are cut out to form a communication port 10 that communicates the upper and lower drying surfaces 7. The communication surface 10 allows the drying surface 7 of each stage forming a multi-stage to be connected in series. It is connected to. The drying object introduction port 2 communicates with the uppermost drying surface 7, and the lowermost communication port 10
The drying object discharge port 3 is communicated with. Further, a hot gas inlet 11 and a gas outlet 12 are respectively opened in the side wall portion of the drying chamber 1 which forms one side wall of the drying surface 7 which is one step below the uppermost step and the lowermost step. The flow path of the hot gas in the illustrated example is formed such that the cross-sectional width of the flow path is narrowed to half or less of the width of the drying surface 7 and flows from the upper side to the lower side on the drying surfaces 7 in a plurality of stages. Have been. The flow path of the hot gas may be formed so as to flow from the lower stage to the upper stage, contrary to the example shown in FIG.

【0005】図中13は、互いにギヤで連動される垂直
方向の回転軸で、前記各段の金属板8を貫通して縦方向
に複数本並列され、該回転軸13の両端は前記乾燥室1
の上壁部及び下底部にそれぞれ回転自在に軸架されてい
る。さらに、各回転軸13には、各金属板8の乾燥面7
上に位置するように配置した複数の送り翼14が取付け
られ、この送り翼14の回転半径の一部が隣接送り翼1
4の回転半径の一部と重なるように回転軸13の間隔が
定められ、しかもこの送り翼14が隣接回転軸13のボ
ス部15に接触しないように、位置決めがなされてい
る。
[0005] In the figure, reference numeral 13 denotes vertical rotating shafts which are interlocked by gears. A plurality of rotating shafts penetrate the metal plates 8 of the respective stages and are arranged in parallel in the vertical direction. 1
Are rotatably mounted on the upper wall and the lower bottom, respectively. Further, each rotating shaft 13 has a dry surface 7 of each metal plate 8.
A plurality of feed wings 14 arranged so as to be positioned above are attached, and a part of the radius of rotation of the feed wings 14
The distance between the rotating shafts 13 is determined so as to overlap a part of the rotating radius of the rotating shaft 4, and the positioning is performed so that the feed blade 14 does not contact the boss 15 of the adjacent rotating shaft 13.

【0006】さらに、前記乾燥室1の内壁面のうち、少
なくとも、送り翼14の回転半径に沿う部分は、該送り
翼14の高さより高い囲壁として円弧状に湾曲形成され
ている。また、乾燥室1上には駆動用減速機付き電動機
19を配設したギヤボックス18が設けられ、これに内
装した不図示のギヤを介して前記複数の回転軸13を隣
接するもの同士交互に反対方向に回転連動するようにな
っている。
Further, at least a portion of the inner wall surface of the drying chamber 1 along the radius of rotation of the feed blade 14 is formed in a circular arc shape as an enclosing wall higher than the height of the feed blade 14. A gear box 18 provided with a motor 19 with a drive reduction gear is provided on the drying chamber 1, and the plurality of rotating shafts 13 are alternately arranged adjacent to each other via gears (not shown) provided in the gear box 18. It is designed to rotate in the opposite direction.

【0007】水分を多く含んだ被乾燥物は、供給ホッパ
ー4aから落下し、スクリューコンベア5aによってか
きまぜられながら、被乾燥物導入口2を通して乾燥室1
内に供給される。
The material to be dried containing a large amount of water falls from the supply hopper 4a, and is stirred through the screw conveyor 5a through the material to be dried 2 into the drying chamber 1.
Supplied within.

【0008】供給装置6aから供給される被乾燥物は、
乾燥室1の被乾燥物導入口2より最上段の金属板8の乾
燥面7上に供給され、乾燥面7上で図4(a)に示した
矢印の方向に送り翼14が回転して被乾燥物を回転方向
と壁面方向に押し出す。そして半径の一部が重なった次
の送り翼14で反対方向から押されて第3番目の送り翼
14の回転半径内に押し出され、乾燥面7上で攪拌され
ながら順次進行して先端の連通口10に面して端部仕切
り板23に設けられた被乾燥物落ち口20より次の段の
乾燥面7上に段差分だけ落下し同様にして順次下段の乾
燥面7へと進行する。
The material to be dried supplied from the supply device 6a is
It is supplied onto the drying surface 7 of the uppermost metal plate 8 from the drying object introduction port 2 of the drying chamber 1, and the feed blade 14 rotates on the drying surface 7 in the direction of the arrow shown in FIG. The material to be dried is extruded in the rotation direction and the wall direction. Then, it is pushed from the opposite direction by the next feed blade 14 having a part of the radius overlapped, pushed out into the radius of rotation of the third feed blade 14, and sequentially proceeds while being stirred on the drying surface 7 to communicate with the tip. From the object to be dried 20 provided on the end partition plate 23 facing the opening 10, it falls on the drying surface 7 of the next stage by a step difference, and similarly proceeds to the lower drying surface 7.

【0009】このとき、同時に乾燥室1の上部の熱ガス
導入口11より導入された熱ガスが、最上段の一段下の
金属板8から被乾燥物の進行方向と同方向に流れて被乾
燥物を加熱し、この熱ガスは蒸発水分を伴ない、最下段
を経て下方のガス排出口12より排出される。
At this time, the hot gas simultaneously introduced from the hot gas inlet 11 in the upper part of the drying chamber 1 flows from the metal plate 8 at the lowermost stage of the uppermost stage in the same direction as the moving direction of the object to be dried. The material is heated, and the hot gas is discharged from the lower gas outlet 12 via the lowermost stage, accompanied by the evaporated water.

【0010】被乾燥物は、下段に進むにつれて乾燥さ
れ、最下段の金属板8の連通口10より被乾燥物排出口
3に臨ませたスクリューコンベア5b上に落下し、スク
リューコンベア5bにより移送され、排出シュート4b
内を落下し乾燥室1の外部へ排出される。
The object to be dried is dried as it proceeds to the lower stage, falls from the communication port 10 of the lowermost metal plate 8 onto the screw conveyor 5b facing the outlet 3 for the object to be dried, and is transferred by the screw conveyor 5b. , Discharge chute 4b
It falls inside and is discharged to the outside of the drying chamber 1.

【0011】[0011]

【発明が解決しようとする課題】各乾燥段の間隔は、処
理容量を考慮に入れた加熱する熱ガスの流量とその通過
速度及び乾燥室全体の構造上の理由から決められるが、
この種のものとして従来技術における上下の乾燥段同士
の間隔は、700〜1500mmと大きいものであった。
このため、被乾燥物は上段から下段への落下中に粉塵を
発生して熱ガスに混入し、熱ガス系の機器を汚損する度
合いが大きかった。しかし、それでも多段乾燥装置は、
熱ガスに粉塵が混入する度合いが他の乾燥装置、例え
ば、流動式、ロータリーキルン式、等に比べて格段に少
ないのが大きな特徴で、特に熱ガスを循環使用するプロ
セスでは大きな利点となるものであった。そこで、さら
に粉塵の発生を抑えるために被乾燥物の落下部分に粉塵
発生防止用のシュート等を設けるという対策も試みられ
たが、粉塵発生防止用のシュートに被乾燥物が付着する
という問題点も新たに発生した。
The interval between the drying stages is determined by the flow rate of the hot gas to be heated in consideration of the processing capacity, the passing speed thereof, and the structural reason of the entire drying chamber.
As this kind, the distance between the upper and lower drying stages in the prior art was as large as 700 to 1500 mm.
For this reason, the material to be dried generates dust during falling from the upper stage to the lower stage, mixes with the hot gas, and contaminates the hot gas system equipment to a large degree. However, the multi-stage dryer is still
The major feature is that the degree to which dust is mixed into the hot gas is much smaller than other drying devices, for example, a flow type, a rotary kiln type, etc., which is a great advantage particularly in a process in which hot gas is circulated. there were. In order to further suppress the generation of dust, measures have been taken to provide a chute or the like for preventing the generation of dust in a falling portion of the object to be dried. However, a problem that the object to be dried adheres to the chute for preventing the generation of dust. Also newly occurred.

【0012】また、従来の構造の多段乾燥装置の規模に
は別の制約もあった。すなわち、段を形成する金属板の
熱膨張のため乾燥面をある程度の大きさ以上にすること
が構造上困難で、規模拡大の為には段数を増やす以外に
なく、規模拡大に伴なって熱ガス流量も多くなるので段
と段との間隔も大きくせざるをえないこととなった。し
たがって、乾燥装置自身の高さを高くする以外に方法が
なかった。
There is another restriction on the scale of the conventional multi-stage drying apparatus. In other words, it is structurally difficult to increase the size of the drying surface to a certain size due to the thermal expansion of the metal plate that forms the steps. As the gas flow rate also increased, the spacing between the stages had to be increased. Therefore, there has been no method other than increasing the height of the drying device itself.

【0013】さらに、図4(a)に示すように従来の構
造では、被乾燥物が次の乾燥段に移動する被乾燥物落ち
口は熱ガスの移動通路でもあり、前述のように、その流
路断面幅が乾燥面7の横幅に対して半分以下に絞られる
こととなり、熱ガスの段間の移動通路は、構造上大きく
とることはできず、そのため該箇所での熱ガスの流速は
速くなって、大きい段差を落下した被乾燥物の粉塵は、
熱ガスの流れに乗りやすいという問題点があった。
Further, as shown in FIG. 4 (a), in the conventional structure, the outlet of the object to be dried, which moves to the next drying stage, is also a hot gas transfer passage. The cross-sectional width of the flow path is reduced to half or less of the width of the drying surface 7, and the moving passage between the steps of the hot gas cannot be made large in terms of structure. The dust of the dried material that falls faster and falls down a large step,
There was a problem that it was easy to get on the flow of hot gas.

【0014】そこで、本発明の第1の目的は、従来のこ
の種の乾燥装置に比べて、格段に粉塵の発生を抑える多
段乾燥装置を提供することにある。
Accordingly, a first object of the present invention is to provide a multi-stage drying apparatus which significantly suppresses dust generation as compared with a conventional drying apparatus of this type.

【0015】本発明の第2の目的は、熱ガスの流路を狭
めることなく、かつ該流路が被乾燥物落ち口に影響を及
ぼす程度の少ない構造を有する多段乾燥装置を提供する
ことにある。
A second object of the present invention is to provide a multi-stage drying apparatus having a structure without narrowing the flow path of the hot gas and having such a structure that the flow path has little influence on the outlet of the material to be dried. is there.

【0016】本発明の第3の目的は、規模の拡大を計る
に当り、段数を増やし高さだけを高くするのではなく、
平面的なひろがりをもって装置全体の大型化が可能な多
段乾燥装置を提供することにある。
A third object of the present invention is not to increase the number of stages but only the height in order to increase the scale.
An object of the present invention is to provide a multi-stage drying apparatus capable of increasing the size of the entire apparatus with a planar spread.

【0017】[0017]

【課題を解決するための手段】上記目的を達成するた
め、請求項1に係る発明による多段乾燥装置は、乾燥室
内に高さ方向にほぼ等間隔で平行に多数の段を設け、各
段毎の乾燥面と、外周壁と、上段及び下段の各乾燥面を
つなぐ連通口とで熱ガスの流路を形成し、前記乾燥面上
に回転範囲が互いに重なり合うよう並列に、かつすべて
の段の乾燥面を垂直に貫通する回転軸に取付けてそれぞ
れの段毎に多数の送り翼を配設し、前記乾燥面上での該
送り翼の回転による攪拌送り及び上の乾燥面の前記連通
口端部に設けた被乾燥物落ち口から段差をつけた下の乾
燥面への落下により、被乾燥物を最上段より最下段まで
順次移行させながら前記熱ガスと接触させて乾燥させる
多段乾燥装置において、前記各段は、前記外周壁で囲ま
れており、内部に設けた仕切り壁で、それぞれ前記乾燥
面を有する複数の部屋に分割し、前記乾燥面には、それ
ぞれ上から下へ次の乾燥面との間で落差の小さい段差お
よび次の乾燥面への前記被乾燥物落ち口を設け、隣接す
る段同士を連結して最上段から最下段まで階段状に各部
屋を配設し、前記被乾燥物を最上段から最下段まで前記
落差の小さい段差を介して順次落下させるように構成す
ると共に、前記熱ガス流路用開口部の流路断面積を可及
的に大きくしたことを特徴とするものである。
In order to achieve the above object, a multi-stage drying apparatus according to the first aspect of the present invention is provided with a large number of stages in a drying chamber in parallel at substantially equal intervals in the height direction. A drying surface, an outer peripheral wall, and a communication port that connects the upper and lower drying surfaces form a flow path of hot gas, and the rotation ranges are arranged in parallel on the drying surface so that the rotation ranges overlap with each other, and in all the stages, A plurality of feed blades are provided at each stage by being attached to a rotating shaft that vertically penetrates the drying surface, and agitated feed by rotating the feed blades on the drying surface and the communication port end of the upper drying surface. In a multi-stage drying apparatus that is dried by contacting with the hot gas while sequentially moving the object to be dried from the uppermost stage to the lowermost stage by dropping the object to be dried from the outlet of the object to be dried provided in the section to the drying surface with a step. , Each of the steps is surrounded by the outer peripheral wall and installed inside. Divided into a plurality of rooms each having the drying surface, wherein the drying surface has a step with a small drop from the top to the next drying surface and the covering to the next drying surface. Providing a dried product outlet, arranging each room in a staircase from the uppermost stage to the lowermost stage by connecting adjacent stages, and passing the dried object from the uppermost stage to the lowermost stage through the small step of the head The structure is such that the hot gas flow path openings are configured to be dropped sequentially, and the flow path cross-sectional area of the opening for the hot gas flow path is made as large as possible.

【0018】[0018]

【発明の実施の形態】本発明の第1実施例を図1及び図
2を用いて説明する。本発明の乾燥室1の構成は、上記
した従来の技術の乾燥室1の構成と乾燥面を除きほぼ同
一であるため説明を省略する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A first embodiment of the present invention will be described with reference to FIGS. The configuration of the drying chamber 1 of the present invention is almost the same as the configuration of the above-described conventional drying chamber 1 except for the drying surface, and thus the description is omitted.

【0019】図1に示す第1実施例においては、従来の
一段一面の平坦な乾燥面7を、例えば段差を従来の1/
4の段差をつけて回り階段状に4分割した四つの乾燥面
に分割するものとした。すなわち、図1(a)に示すよ
うに各段は、二つの長手方向側壁21aと二つの横断方
向端壁21bで囲まれており、内部を一方の横断方向端
壁21bと、二つの長手方向側壁21aの一部と、乾燥
面幅と略同じ幅をもった次段への熱ガス流路用開口部を
備えた第1の横断方向仕切り壁24aとで囲まれた乾燥
面7Aを有する第1室と、一方の長手方向側壁21aの
一部と、乾燥面幅と略同じ幅をもった次段への熱ガス流
路用開口部を備えた第1及び第2の横断方向仕切り壁2
4a,24bの一部と、中央仕切り壁22とで囲まれた
乾燥面7Bを有する第2室と、他方の横断方向端壁21
bと、二つの長手方向側壁21aの一部と、乾燥面幅と
略同じ幅をもった次段への熱ガスの流路用開口部を備え
た第2の横断方向仕切り壁24bとで囲まれた乾燥面7
Cを有する第3室と、他方の長手方向側壁21aの一部
と、乾燥面幅と略同じ幅をもった次段への熱ガス流路用
開口部を備えた第1及び第2の横断方向仕切り壁24
a,24bの一部と、中央仕切り壁22とで囲まれた乾
燥面7Dを有する第4室とに分割する。
In the first embodiment shown in FIG. 1, the flat drying surface 7 of the conventional one step and one step, for example, the step is reduced by 1 /
It was divided into four dry surfaces divided into four steps in a stepwise manner with a step of 4. That is, as shown in FIG. 1 (a), each step is surrounded by two longitudinal side walls 21a and two transverse end walls 21b, and the inside is formed by one transverse end wall 21b and two longitudinal directions. A drying surface 7A having a drying surface 7A surrounded by a part of the side wall 21a and a first transverse partition wall 24a having an opening for a hot gas flow path to a next stage having substantially the same width as the drying surface width. First and second transverse partition walls 2 each having one chamber, a part of one of the longitudinal side walls 21a, and an opening for a hot gas flow path to a next stage having a width substantially equal to a dry surface width.
4a, 24b, a second chamber having a drying surface 7B surrounded by a central partition wall 22, and the other transverse end wall 21.
b, a part of the two longitudinal side walls 21a and a second transverse partition wall 24b having an opening for a flow path of hot gas to the next stage having a width substantially equal to the width of the dry surface. Dry surface 7
C, a part of the other longitudinal side wall 21a, and first and second traverses each having a hot gas passage opening to the next stage having a width substantially equal to the width of the dry surface. Directional partition wall 24
a, 24b and a fourth chamber having a dry surface 7D surrounded by a central partition wall 22.

【0020】各乾燥面7Aないし7Dには、二列の送り
翼14を設け、回転軸13に送り翼14を取付け、この
送り翼14の回転半径の一部が隣接送り翼14のそれと
重なるように回転軸13の間隔が定められ、しかもこの
送り翼14が隣接回転軸13のボス部15に接触しない
ように、位置決めがなされている。
On each of the drying surfaces 7A to 7D, two rows of feed blades 14 are provided, and the feed blades 14 are attached to the rotating shaft 13, so that a part of the radius of rotation of the feed blades 14 overlaps that of the adjacent feed blades 14. The distance between the rotating shafts 13 is determined, and the positioning is performed such that the feed blade 14 does not contact the boss 15 of the adjacent rotating shaft 13.

【0021】前記四つの乾燥面7Aないし7Dには、相
互に段差が設けられるが、この段差は従来の段差の1/
4となる。図1(b)で示したように、乾燥面7A1
り7B1 を低く、同じく7B1 より7C1 を低く、同じ
く7C1 より7D1 を低く、同じく7D1 より一つ下の
段の分割面の乾燥面7A2 を低くする。さらに次段にお
いて、同様に乾燥面7A2 より7B2 を、同じく7B2
より7C2 を、同じく7C2 より7D2 を、同じく7D
2 より7A3 を低くする。なお、各段を4つの面に分割
すると乾燥面7A2 は丁度乾燥面7A1 の、同じく7B
2 は7B1 の、同じく7C2 は7C1 の、同じく7D2
は7D1 の真下になる。したがって、各乾燥面7Aない
し7Dはその順番を繰返して回り階段状に配設される。
The four dry surfaces 7A to 7D have a phase
Steps are provided to each other, and this step is 1/1 of the conventional step.
It becomes 4. As shown in FIG. 1B, the dry surface 7A1 Yo
7B1 Lower, also 7B1 Than 7C1 Lower the same
7C1 More 7D1 Lower, also 7D1 One below
Drying surface 7A of split surface of stepTwo Lower. In the next step
And likewise dry surface 7ATwo Than 7BTwo And 7BTwo
Than 7CTwo And 7CTwo More 7DTwo And 7D
Two 7AThree Lower. Each step is divided into four surfaces
Then dry surface 7ATwo Is just dry surface 7A1 Of the same 7B
Two Is 7B1 Of the same 7CTwo Is 7C1 Of the same 7DTwo
Is 7D1 Directly below. Therefore, each dry surface 7A is not
7D is arranged in a stepwise manner by repeating the order.

【0022】ある段の乾燥面7上で送り翼14が、図1
(a)に示した矢印の方向に回転して被乾燥物を回転方
向と壁面方向に押し出す。そして該被乾燥物は半径の一
部が重なった次の送り翼14で反対方向から押されて第
3番目の送り翼14の回転半径内に押し出され、乾燥面
7上で攪拌されながら順次一方向に移動して、図2の斜
視図に示したように被乾燥物がどこからでも落ちないよ
うに乾燥面7の端部に設けた端部仕切り板23の一部を
切り欠いた被乾燥物落ち口20を介して1つ下の乾燥面
7に落ち、図1(b)に示すように7A1 から7B1
同じく7B1 から7C1 、同じく7C1 から7D1 、同
じく7D1 から7A2 へと順次移送される。例えば、被
乾燥物落ち口20の代表的寸法としては、高さ約150
mm、幅100〜200mmにする。一方、熱ガスは天井の
金属板8と、床の乾燥面7と、側壁21と、中央仕切り
壁22と、で囲まれた空間を上段から下段へと順次移送
される。
The feed wing 14 on the drying surface 7 of a certain stage
The object to be dried is rotated in the direction of the arrow shown in FIG. The object to be dried is pushed from the opposite direction by the next feed blade 14 whose radius partially overlaps, is pushed out into the radius of rotation of the third feed blade 14, and is sequentially stirred while being stirred on the drying surface 7. The object to be dried is cut in a part of an end partition plate 23 provided at the end of the drying surface 7 so that the object to be dried does not fall from anywhere as shown in the perspective view of FIG. falling port 20 via a fall in dry surface 7 of the lower one 1, 7A 1 as shown in FIG. 1 (b) From 7B 1 ,
7B 1 From 7C 1 , Also 7C 1 From 7D 1 , Also 7D 1 From 7A 2 Are sequentially transferred to. For example, as a representative size of the outlet 20 for the object to be dried, a height of about 150
mm and a width of 100 to 200 mm. On the other hand, the hot gas is sequentially transferred from the upper stage to the lower stage in a space surrounded by the metal plate 8 on the ceiling, the drying surface 7 on the floor, the side wall 21 and the center partition wall 22.

【0023】乾燥面7を分割してかつ相互に段差を設け
ることにより、乾燥面7を形成する金属板8の1つの板
材の寸法を小さくすると共に熱膨張が少なくとも一方向
に自由にできるようにした。また、1段の乾燥面7を4
つに分割した結果、段差も4つに分割することができ、
従来に対し隣接した二つの乾燥面、例えば乾燥面7A,
7B間の段差は1/4になり、被乾燥物落ち口20での
被乾燥物の落下に伴う粉塵の発生を抑えることができる
ようになった。熱ガスの流路も乾燥面7が回り階段状に
設置されているため、例えば乾燥面7A1 と7A2 との
間の高さは従来通りの高さを保つことができ、また熱ガ
スの流路用開口部断面積を可及的に大きくしたので従来
に対し被乾燥物落ち口20に比べて熱ガスの流路断面積
は大きくなり、被乾燥物の落下に熱ガスの流れが大きな
影響を与えることもない。さらに、多段乾燥装置の処理
容量を増大するには高さだけではなく、平面的なひろが
りを大きくすることができ、高さを抑えながら装置全体
の大型化も可能となった。
By dividing the drying surface 7 and providing steps to each other, the size of one of the metal plates 8 forming the drying surface 7 can be reduced, and the thermal expansion can be freely performed in at least one direction. did. Also, the drying surface 7 of one stage is
As a result of dividing into two, the step can also be divided into four,
Conventionally, two adjacent drying surfaces, for example, the drying surface 7A,
The step between 7B is reduced to 1/4, so that it is possible to suppress the generation of dust due to the falling of the object to be dried at the object to be dried 20. The hot gas flow path is also provided in a stepwise manner around the drying surface 7, so that, for example, the drying surface 7A 1 And 7A 2 Can maintain the same height as before, and the cross-sectional area of the hot gas passage opening is made as large as possible. The flow path cross-sectional area of the gas becomes large, and the flow of the hot gas does not greatly affect the falling of the object to be dried. Further, in order to increase the processing capacity of the multi-stage drying apparatus, not only the height but also the planar spread can be increased, and the entire apparatus can be enlarged while suppressing the height.

【0024】本発明の第2実施例を図3を用いて説明す
る。
A second embodiment of the present invention will be described with reference to FIG.

【0025】第2実施例においては、従来の一段一面の
平坦な乾燥面を従来の1/2の段差をつけて並列2分割
した二つの乾燥面としたものである。すなわち、図3
(a)に示すように各段は二つの長手方向側壁21aと
二つの横断方向端壁21bで囲まれており、内部は中央
の仕切り壁22で乾燥面7Aを有する第1室と乾燥面7
Bを有する第2室とに分割する。
In the second embodiment, the conventional dry flat surface of each step is divided into two parallel dry surfaces with a 1/2 step difference. That is, FIG.
As shown in (a), each step is surrounded by two longitudinal side walls 21a and two transverse end walls 21b, and the inside is a first chamber having a drying surface 7A with a central partition wall 22 and a drying surface 7A.
And a second chamber having B.

【0026】各乾燥面7A,7Bには、2列の送り翼1
4を設け、回転軸13に送り翼14を取付け、1実施例
と同じ配置にされている。
Each of the drying surfaces 7A and 7B has two rows of feed blades 1
4 and a feed wing 14 is attached to the rotating shaft 13 and has the same arrangement as in the first embodiment.

【0027】前記二つの乾燥面7A,7Bには、段差が
設けられるが、この段差は従来の段差の1/2となる。
図3(b)で示したように、乾燥面7A1 より7B1
低く、同じく7B1 より一つ下の段の分割面の乾燥面7
2 を低くする。さらに次段において乾燥面7A2 より
7B2 を低く、同じく7B2 より7A3 を低くする。な
お、各段を二つの面に分割すると乾燥面7A2 は丁度乾
燥面7A1 の、同じく7B2 は7B1 の真下になる。し
たがって、各乾燥面7A,7Bはその順番を繰り返して
ジグザグ階段状に配設される。
The two drying surfaces 7A and 7B are provided with a step, which is 差 of the conventional step.
As shown in FIG. 3B, the dry surface 7A 1 Than 7B 1 Lower, also 7B 1 Dry surface 7 of the division surface of the next lower stage
A 2 Lower. In the next stage, the drying surface 7A 2 Than 7B 2 Lower, also 7B 2 7A 3 Lower. When each step is divided into two surfaces, the dry surface 7A 2 Is just dry surface 7A 1 Of the same 7B 2 Is 7B 1 Directly below. Therefore, each of the drying surfaces 7A and 7B is arranged in a zigzag step shape by repeating the order.

【0028】他の部分については、第1実施例について
先に記載された所と実質的に同じものである。
The other parts are substantially the same as those described above for the first embodiment.

【0029】[0029]

【発明の効果】本発明によれば、従来に比して粉塵の発
生を抑えることができる。また、熱ガスの流路が大きく
なり、被乾燥物の落下に熱ガスの流れが影響を及ぼす程
度の少ない構造にすることができる。さらに、規模の拡
大を計るに当り、装置全体の大型化が可能となる。
According to the present invention, the generation of dust can be suppressed as compared with the prior art. In addition, the flow path of the hot gas becomes large, and a structure can be provided in which the flow of the hot gas does not affect the falling of the object to be dried. Further, in order to increase the scale, the size of the entire apparatus can be increased.

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

【図1】(a)は、従来の1/4段差をつけて回り階段
状に4分割した乾燥面を有する本発明の第1実施例によ
る多段乾燥装置要部の平面図、(b)は、図1(a)に
おけるA−A矢視断面説明図。
FIG. 1 (a) is a plan view of a main part of a multi-stage drying apparatus according to a first embodiment of the present invention having a drying surface divided into four steps in a stepwise manner with a conventional 段 step, and FIG. FIG. 1 is a cross-sectional explanatory view taken along the line AA in FIG.

【図2】本発明の第1実施例の一部破断斜視説明図。FIG. 2 is a partially cutaway perspective explanatory view of the first embodiment of the present invention.

【図3】(a)は、従来の1/2段差をつけてジグザグ
階段状に並列2分割した乾燥面を有する本発明の第2実
施例による多段乾燥装置要部の平面図、(b)は、図3
(a)におけるA−A矢視断面説明図。
FIG. 3 (a) is a plan view of a main part of a multi-stage drying apparatus according to a second embodiment of the present invention having a drying surface divided in two in a zigzag stepwise manner with a conventional half-step difference, and (b). Figure 3
FIG.

【図4】(a)は、従来の多段乾燥装置の一部破断平面
図、(b)は、図4(a)におけるA−A矢視断面説明
図。
4 (a) is a partially cutaway plan view of a conventional multi-stage drying apparatus, and FIG. 4 (b) is a cross-sectional explanatory view taken along the line AA in FIG. 4 (a).

【符号の説明】[Explanation of symbols]

1…乾燥室 2…被乾燥物導入口 3…被乾燥物排出口 4a…供給ホッパー 4b…排出シュート 5a,5b…スクリューコンベア 6a…供給装置 6b…排出装置 7…乾燥面 7A,7B,7C,7D…乾燥面 8…金属板 10…連通口 11…熱ガス導入口 12…ガス排出口 13…回転軸 14…送り翼 15…ボス部 18…ギヤボックス 19…駆動用減速電動機 20…被乾燥物落ち口 21…側壁 21a…長手方向側壁 21b…横断方向端壁 22…中央仕切り壁 23…端部仕切り板 24a…第1の横断方向仕切り壁 24b…第2の横断方向仕切り壁 DESCRIPTION OF SYMBOLS 1 ... Drying room 2 ... Dry material introduction port 3 ... Dry material discharge port 4a ... Supply hopper 4b ... Discharge chute 5a, 5b ... Screw conveyor 6a ... Supply device 6b ... Discharge device 7 ... Drying surface 7A, 7B, 7C, 7D ... Dry surface 8 ... Metal plate 10 ... Communication port 11 ... Heat gas introduction port 12 ... Gas discharge port 13 ... Rotating shaft 14 ... Feed blade 15 ... Boss 18 ... Gear box 19 ... Driving reduction motor 20 ... Dry matter Outlet 21 ... side wall 21a ... longitudinal side wall 21b ... transverse end wall 22 ... center partition wall 23 ... end partition plate 24a ... first transverse partition wall 24b ... second transverse partition wall

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 乾燥室内に高さ方向にほぼ等間隔で平行
に多数の段を設け、各段毎の乾燥面と、外周壁と、上段
及び下段の各乾燥面をつなぐ連通口とで熱ガスの流路を
形成し、前記乾燥面上に回転範囲が互いに重なり合うよ
う並列に、かつすべての段の乾燥面を垂直に貫通する回
転軸に取付けてそれぞれの段毎に多数の送り翼を配設
し、前記乾燥面上での該送り翼の回転による攪拌送り及
び上の乾燥面の前記連通口端部に設けた被乾燥物落ち口
から段差をつけた下の乾燥面への落下により、被乾燥物
を最上段より最下段まで順次移行させながら前記熱ガス
と接触させて乾燥させる多段乾燥装置において、 前記各段は、前記外周壁で囲まれており、内部に設けた
仕切り壁で、それぞれ前記乾燥面を有する複数の部屋に
分割し、前記乾燥面には、それぞれ上から下へ次の乾燥
面との間で落差の小さい段差および次の乾燥面への前記
被乾燥物落ち口を設け、隣接する段同士を連結して最上
段から最下段まで階段状に各部屋を配設し、前記被乾燥
物を最上段から最下段まで前記落差の小さい段差を介し
て順次落下させるように構成すると共に、前記熱ガス流
路用開口部の流路断面積を可及的に大きくしたことを特
徴とする多段乾燥装置。
1. A large number of stages are provided in a drying chamber in parallel at substantially equal intervals in the height direction, and heat is generated by a drying surface of each stage, an outer peripheral wall, and a communication port connecting the upper and lower drying surfaces. A gas flow path is formed, and a large number of feed blades are arranged for each stage by being mounted on a rotating shaft that passes through the drying surfaces in parallel so that the rotation ranges overlap with each other on the drying surface and vertically passes through the drying surfaces of all the stages. By setting the agitating feed by rotation of the feed blade on the drying surface and dropping the drying object provided at the end of the communication port of the upper drying surface to the lower drying surface with a step, In a multi-stage drying device for drying by contacting the hot gas while sequentially moving the object to be dried from the uppermost stage to the lowermost stage, each stage is surrounded by the outer peripheral wall, and a partition wall provided inside, Divided into a plurality of rooms each having the drying surface, the drying surface, From the top to the bottom, a step with a small drop between the next drying surface and the above-mentioned object to be dried to the next drying surface is provided, and the adjacent steps are connected to each other, and the stairs are connected from the top to the bottom. Each room is arranged in a shape, and the drying target is sequentially dropped from the uppermost stage to the lowermost stage through the small step, and the flow cross-sectional area of the opening for the hot gas flow path A multi-stage drying apparatus characterized by having as large as possible.
【請求項2】 最上段から最下段まで落差の小さい段差
をつけた階段状の前記乾燥面は、従来の1/4段差をつ
けて回り階段状に4分割した乾燥面であることを特徴と
する請求項1に記載の多段乾燥装置。
2. The drying step-like surface having a step with a small drop from the top to the bottom is a conventional drying surface divided into four steps in a stepwise manner with a conventional quarter-step. The multi-stage drying apparatus according to claim 1.
【請求項3】 最上段から最下段まで落差の小さい段差
をつけた階段状の前記乾燥面は、従来の1/2段差をつ
けてジグザグ階段状に並列2分割した乾燥面であること
を特徴とする請求項1に記載の多段乾燥装置。
3. The drying surface in the form of a step having a small step from the uppermost stage to the lowermost stage is a conventional drying surface which is divided into two parts in a zigzag stepwise manner with a conventional half step. The multistage drying apparatus according to claim 1, wherein
JP26486699A 1999-09-20 1999-09-20 Multistage drying device Pending JP2001091156A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26486699A JP2001091156A (en) 1999-09-20 1999-09-20 Multistage drying device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26486699A JP2001091156A (en) 1999-09-20 1999-09-20 Multistage drying device

Publications (1)

Publication Number Publication Date
JP2001091156A true JP2001091156A (en) 2001-04-06

Family

ID=17409317

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26486699A Pending JP2001091156A (en) 1999-09-20 1999-09-20 Multistage drying device

Country Status (1)

Country Link
JP (1) JP2001091156A (en)

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KR101524565B1 (en) * 2015-01-02 2015-06-01 주식회사 한국테크놀로지 Apparatus for Dust-Reduction by Supplying of Falling Coal in System for Drying Coal
KR101524568B1 (en) * 2015-01-02 2015-06-01 주식회사 한국테크놀로지 Apparatus for Supply Coal for Dust-Reduction in System for Drying Coal using Reheat Steam
KR101526284B1 (en) * 2015-01-02 2015-06-09 주식회사 한국테크놀로지 Apparatus for Alignment for Even Drying of Transportation Coal in System for Drying Coal using Reheat Steam
KR101526282B1 (en) * 2015-01-02 2015-06-09 주식회사 한국테크놀로지 Apparatus for Injection Dispersion of Reheat Steam in System for Drying Coal
KR101526283B1 (en) * 2015-01-02 2015-06-09 주식회사 한국테크놀로지 Apparatus for Removing Static Coal Residue on Transfer Plate in System for Drying Coal
KR101549888B1 (en) 2015-01-02 2015-09-03 주식회사 한국테크놀로지 Apparatus for Dispersion Supply and Dust-Reduction of Input Coal in System for Drying Coal using Reheat Steam
KR101549894B1 (en) 2015-01-02 2015-09-03 주식회사 한국테크놀로지 Apparatus for Conveying Coal in System for Drying Coal using Reheat Steam
KR101549883B1 (en) 2015-01-02 2015-09-03 주식회사 한국테크놀로지 Chamber for Supply Reheat Steam in System for Drying Coal using Reheat Steam
KR101549892B1 (en) 2015-01-02 2015-09-03 주식회사 한국테크놀로지 Device for Flattening of Transportation Coal in System for Drying Coal using Reheat Steam
WO2016108360A1 (en) * 2015-01-02 2016-07-07 주식회사 한국테크놀로지 Dust reduction apparatus depending on supply of falling coal in coal drying apparatus using reheat steam

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