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JPH0437358B2 - - Google Patents
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JPH0437358B2 - - Google Patents

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Publication number
JPH0437358B2
JPH0437358B2 JP58186368A JP18636883A JPH0437358B2 JP H0437358 B2 JPH0437358 B2 JP H0437358B2 JP 58186368 A JP58186368 A JP 58186368A JP 18636883 A JP18636883 A JP 18636883A JP H0437358 B2 JPH0437358 B2 JP H0437358B2
Authority
JP
Japan
Prior art keywords
shell
hot air
grain
path
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 - Lifetime
Application number
JP58186368A
Other languages
Japanese (ja)
Other versions
JPS6078280A (en
Inventor
Soichi Yamamoto
Masaki Funayama
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.)
YAMAMOTO Manufacturing
Original Assignee
YAMAMOTO Manufacturing
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 YAMAMOTO Manufacturing filed Critical YAMAMOTO Manufacturing
Priority to JP18636883A priority Critical patent/JPS6078280A/en
Publication of JPS6078280A publication Critical patent/JPS6078280A/en
Publication of JPH0437358B2 publication Critical patent/JPH0437358B2/ja
Granted legal-status Critical Current

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  • Drying Of Solid Materials (AREA)

Description

【発明の詳細な説明】 本発明は、殻槽内に張込んだ殻粒を循環流動さ
せて、それに乾燥風を送給することで乾燥する殻
粒通風乾燥装置についての改良に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a ventilation drying device for shell grains that circulates and flows the shell grains filled in a shell tank and dries them by supplying drying air thereto.

上述の殻粒通風乾燥装置は、殻槽内に張込んだ
殻粒が、排気路を構成する網体等の通気性の隔壁
と導風路を構成する網体等の通気性の隔壁とで殻
槽の底部に形成される殻粒流下路に流れ込み、そ
の殻粒流下路の下端の流出口に設けたドラムシヤ
ツター(またはロータリーバルブ)による流出量
に規制された速度で該殻粒流下路を流下し、その
殻粒流下路の下端の流出口から流出したところ
で、コンベア及び昇降機(バケツトエレベータ
ー)で再び殻槽の上部に戻されることにより循環
流動し、その循環流動の間の、前述の殻粒流下路
を流下する間に、前記導風路側から該殻粒流下路
を横切るように排気路が吹抜けていく乾燥風を浴
びることで順次乾燥されていくようにしてある。
In the above-mentioned shell grain ventilation drying device, the shell grains placed in the shell tank are separated by an air-permeable partition wall such as a net that constitutes an exhaust path and an air-permeable partition wall such as a net that constitutes an air guide path. The shell particles flow into the shell flow passage formed at the bottom of the shell tank, and flow at a speed regulated by the outflow amount by a drum shutter (or rotary valve) provided at the outlet at the lower end of the shell flow passage. At the point where it flows out from the outlet at the lower end of the shell particle flow path, it is returned to the upper part of the shell tank by a conveyor and an elevator (bucket elevator), causing a circulation flow. During the circulation flow, the above-mentioned While the grains are flowing down the shell flow passage, they are successively dried by being exposed to drying air that blows through the exhaust passage from the air guiding passage side so as to cross the shell grain flow passage.

このことから、乾燥能率を高めるために、一回
の循環行程の間に、殻粒に対し乾燥風を浴びせる
時間を長くするよう、殻粒流下路を流下していく
速度を遅くすると、全体の殻粒の循環に時間がか
かるようになつて能率をかえつて低下させるよう
になり、乾燥能率を高めることがむづかしい問題
がある。
From this, in order to increase the drying efficiency, it is possible to increase the time during which drying air is exposed to the shell grains during one circulation process, and to slow down the speed at which the shell grains flow down the flow path. There is a problem in that it takes time to circulate the shells, which actually reduces efficiency, making it difficult to increase drying efficiency.

また、殻粒流下路を流下する殻粒に対して乾燥
風を浴びせる時間を長くする手段として、殻粒流
下路の上方に乾燥風の供給路を配設し、その殻粒
流下路の下端側に排気路に通ずる排気口を設け
て、乾燥風が殻粒流下路内を縦方向に流過してい
くようにする手段が特開昭57−174680号公報によ
り知らされているが、この手段は、乾燥風が透過
する殻粒層の厚さが、殻粒流下路の縦方向の長さ
に対応するようになつて、著しく厚くなること
で、この厚い殻粒層を乾燥風が透過するようにす
るため乾燥風の供給圧力を非常に大きくしなけれ
ばならず、コスト高になる別の問題が生じてく
る。
In addition, as a means to extend the time during which drying air is applied to the shell grains flowing down the shell grain flow passage, a drying air supply passage is provided above the shell grain flow passage, and the lower end side of the shell grain flow lower passage is Japanese Unexamined Patent Publication No. 174680/1983 discloses a method of providing an exhaust port communicating with the exhaust passage so that the drying air flows vertically through the shell flow passage. The thickness of the shell grain layer through which the drying wind permeates corresponds to the longitudinal length of the shell flow path and becomes significantly thicker, allowing the drying wind to pass through this thick shell grain layer. In order to do this, the supply pressure of the drying air must be made very high, which creates another problem that increases costs.

また、殻粒流下路を、排気路に接する通気性の
隔壁と熱風の導風路を構成する通気性の隔壁とを
対向させて、それらの隔壁の間に形成すること
で、導風路から吹き出されて排気路に流れる熱風
が、殻粒流下路を横切つて吹き流れる形態に構成
しておいて、その殻粒流下路を流下する殻粒に対
して浴びせる熱風の量を多くするには、殻粒流下
路の巾となる排気路側の隔壁と導風路側の隔壁と
の対向間隔を狭くして、熱風が吹き抜ける方向に
おける殻粒の層を薄くする手段がある。しかし、
この手段では、殻粒流下路の上端から下端に至る
までの全域を同じ温度の熱風が吹き抜けることか
ら、供給する熱風の温度を上げたときに、殻粒が
殻粒流下路を流下してく間に次第に昇温していく
ことで、殻粒流下路の下端側において殻粒の温度
が高くなつて、殻粒に変化を生ぜしめるようにな
るので、供給する熱風の温度に制約を生ぜしめる
問題がある。
In addition, by forming the shell particle flow downstream path between the air-permeable partition walls that are in contact with the exhaust path and the air-permeable partition walls that constitute the hot air guide path, and between these partitions, To increase the amount of hot air that is blown out and flowing into the exhaust passage across the shell grain flow passage, and to blow the hot air toward the shell grains flowing down the shell grain flow passage. There is a method of thinning the layer of shell grains in the direction in which the hot air blows through by narrowing the facing interval between the partition wall on the exhaust passage side and the partition wall on the air guiding passage side, which is the width of the shell flow lower passage. but,
With this method, hot air of the same temperature blows through the entire area from the upper end to the lower end of the shell flow passage, so when the temperature of the hot air to be supplied is increased, the shell grains flow down the shell flow passage. As the temperature gradually increases, the temperature of the shell grains becomes higher at the lower end of the shell flow path, causing changes in the shell grains, which creates a problem that limits the temperature of the hot air that is supplied. There is.

本発明は、従来手段に生じているこれらの問題
を解消せしめるためになされたものであつて、殻
粒流下路を流下する殻粒に対する熱風の送給が効
率よく行なえるよう、殻粒流下路をそれの一側か
ら他側に向けて横切るように吹き流れる熱風によ
り行なわれるようにして、熱風が透過する方向の
殻粒の層の厚さを薄くして熱風を浴びる時間が長
くなる形態としながら、その殻粒流下路を流下す
る殻粒層を透過する熱風量を増大させるために、
殻粒層を薄くするのが、殻粒の昇温による変質を
生ぜしめることなく行なえるようにして、殻粒の
乾燥が能率よく行なえるようになる新たな手段を
提供することを目的とする。
The present invention has been made in order to solve these problems occurring in the conventional means. This is done by hot air blowing across the shell from one side to the other, and the thickness of the layer of shell grains in the direction through which the hot air passes is made thinner so that the time spent exposed to the hot air is extended. However, in order to increase the amount of hot air that passes through the shell grain layer flowing down the shell grain flow path,
The purpose of the present invention is to provide a new means for efficiently drying shell grains by thinning the shell grain layer without causing deterioration of the shell grains due to temperature rise. .

本発明においては、この目的を達成するための
手段として、通気性の隔壁により殻槽の内腔底部
を前後に横切るよう機体の前後の機壁間に設ける
排気路と、通気性の隔壁により前記排気路に平行
して機体の前後の機壁間に設ける熱風の導風路と
で、それらの対向する通気性の隔壁の間に上端側
が殻槽の底部に通ずる殻粒流下路を形成して、そ
の殻粒流下路の入口部位に、殻粒流下路に流入し
ていく殻粒を左右に分流して再び合流させる殻粒
案内壁を、通気性の隔壁により風胴状に形成して
装設し、その殻粒案内壁の内腔を、殻槽の前後方
向の外面に設けた連通ダクトを介して熱風生成装
置と連通させたことを特徴とする殻粒通風乾燥装
置を提起するものである。
In the present invention, as means for achieving this object, an exhaust passage is provided between the front and rear walls of the fuselage so as to cross the bottom of the inner cavity of the shell tank back and forth by means of a breathable partition, and A hot air guide path is provided between the front and rear machine walls of the aircraft in parallel with the exhaust path, and a shell particle flow downward path is formed between these opposing ventilation partition walls, with the upper end leading to the bottom of the shell tank. At the inlet of the lower shell flow passage, a shell guide wall is installed in which the shell grains flowing into the lower flow passage are diverted to the left and right and then merged again.The shell grain guide wall is formed in the shape of a wind trunk with an air permeable partition wall. This invention proposes a shell grain ventilation drying device characterized in that the inner cavity of the shell grain guide wall is communicated with a hot air generating device through a communication duct provided on the outer surface of the shell tank in the front and back direction. be.

次に実施の一例を図面に従い詳述する。 Next, an example of implementation will be described in detail with reference to the drawings.

第1図において、1は殻粒通風乾燥装置Aの機
体で、上下に高い箱状に形成してある。
In FIG. 1, reference numeral 1 denotes the body of the shell and grain ventilation drying apparatus A, which is shaped like a box with vertically high heights.

2は前記機体1の内腔に装設せる殻槽で、それ
の周壁は機体1の前後の機壁10及び左右の機壁
11,11を共用している。
Reference numeral 2 denotes a shell tank installed in the inner cavity of the fuselage 1, and its peripheral wall shares the front and rear walls 10 and the left and right walls 11, 11 of the fuselage 1.

a・aは前記殻槽2の底部に形成した殻粒流下
路で、機体1に左右の機壁11,11の上下の中
間部位の内面からそれぞれ機体1内腔の底部の左
右における中央部位に向け傾斜して下降する通気
性の隔壁20,20を機体1の前後の機壁10,
10間に渡るように設けて、殻槽2の底部の左右
の両側部位に殻槽2の底部を前後に横切るよう設
ける排気路b,bと、通気性の隔壁30により筒
状に形成して前記排気路b,bの中間部位に、殻
槽2の底部内腔を前後に横切るよう機体1の前後
の機壁10,10間に渡架される導風路cとを、
平行させて装設することで、左右に対向する排気
路bの隔壁20と導風路cの隔壁30とによつ
て、左右に狭く区劃されて上下に長く連続する状
態に形成してある。そして、この殻粒流下路a,
aの各下端は、前記排気路b,bを形成している
左右の傾斜する通気性の隔壁20,20の各下縁
20a,20aで形成される流出口21に合流
し、この流出口21に設けられるドラムシヤツタ
ー4の周壁40により各別に閉塞され、そのドラ
ムシヤツター4が回転してそれの周壁40に設け
た開口41と対面することで、該殻粒流下路a,
a内の殻粒がその開口41を介してドラムシヤツ
ター4の内部に流入し、さらにドラムシヤツター
4が回転して開口41が流出口21の下方に位置
する状態となることにより排出されていくように
なつている。
a and a are shell particle flow passages formed at the bottom of the shell tank 2, from the inner surfaces of the upper and lower intermediate parts of the left and right machine walls 11, 11 to the left and right central parts of the bottom of the inner cavity of the fuselage 1, respectively. Air permeable bulkheads 20, 20 that slope downward toward the front and rear walls 10 of the fuselage 1,
It is formed into a cylindrical shape with exhaust passages b, b provided across the bottom of the shell tank 2 in the front and back directions on both sides of the bottom of the shell tank 2, and an air-permeable partition wall 30. An air guide path c is provided between the front and rear machine walls 10 of the fuselage 1 so as to cross the bottom inner cavity of the shell tank 2 back and forth between the exhaust channels b and b,
By installing them in parallel, the partitions are narrowly partitioned from side to side by the partition wall 20 of the exhaust path b and the partition wall 30 of the air guide path c, which face each other from side to side, and are formed in a long continuous state in the vertical direction. . Then, this shell particle flow path a,
Each lower end of a merges with the outlet 21 formed by the lower edges 20a, 20a of the left and right inclined ventilation partition walls 20, 20 forming the exhaust passages b, b, and the outlet 21 Each drum shutter 4 is closed by a peripheral wall 40 of a drum shutter 4 provided in each of the shells, and when the drum shutter 4 rotates and faces the opening 41 provided in its peripheral wall 40, the shell particle flow downstream path a,
The shell grains in a flow into the drum shutter 4 through the opening 41, and are discharged by rotating the drum shutter 4 so that the opening 41 is located below the outlet 21. It's starting to go well.

5は前記ドラムシヤツター4の回転作動で流出
口21から流出する殻粒を機体1の外部に搬出す
るスクリユーコンベアで、スクリユー50と搬送
樋51とよりなり、それの搬送方向の終端部は、
機体1の前面側の機壁10から前方に突出し、そ
の機壁10の前面側に立設された昇降機12の下
部に接続連通し、さらに該昇降機12の上部に搬
送方向の始端側が接続しているコンベア13を介
し殻槽2の上部に連通している。
Reference numeral 5 denotes a screw conveyor for conveying shell grains flowing out from the outlet 21 to the outside of the machine body 1 by the rotation of the drum shutter 4, and is composed of a screw 50 and a conveying gutter 51, and its terminal end in the conveying direction is ,
It protrudes forward from a machine wall 10 on the front side of the machine body 1, is connected to and communicates with the lower part of an elevator 12 erected on the front side of the machine wall 10, and is further connected to the upper part of the elevator 12 at the starting end side in the transport direction. It communicates with the upper part of the shell tank 2 via a conveyor 13.

6,6は、殻槽2の底部に形成せる前述の殻粒
流下路a,aの各入口部位に配位して殻槽2内に
装設せる殻粒案内壁で、殻槽2の上部側から各殻
粒流下路aの入口に向けて流下していく殻粒を第
1図にて2重線の矢印にて示している如く左右に
分流するよう、上面側を正面視で傘状に形成し、
機体1の前後の機壁10,10間に渡架すること
については、従前のこの種の殻粒案内壁の同様で
あるが、網体または目抜板などの通気性の隔壁に
より風胴状に形成してある。
Reference numerals 6 and 6 denote shell grain guide walls installed in the shell tank 2 and arranged at the respective inlets of the above-mentioned shell grain flow channels a and a formed at the bottom of the shell tank 2; The upper surface side is shaped like an umbrella when viewed from the front so that the shell grains flowing down from the side toward the entrance of each shell grain flow passage a are divided into left and right sides as shown by the double-lined arrow in Fig. 1. formed into;
The structure of the bridge between the front and rear machine walls 10, 10 of the aircraft body 1 is the same as in the case of previous shell guide walls of this type, but the air-permeable bulkheads such as nets or perforated boards are used to create a wind trunk-like structure. It is formed in

しかして、この殻粒案内壁6,6の内腔は、第
2図及び第3図に示している如く、機体1の後面
側の機壁10に設けた連通口60,60と、その
機体10の外面に設けたダクト61ならびに前述
の機壁10に設けた連通口62を介して導風路c
と連通し、その導風路cは、第2図に示している
如く、機体1の前面側の機壁10に設けた連通口
31及びその機壁10の前面に設けたダクト32
を介し熱風生成装置7に連通し、また、前述した
排気路b,bは、機体1の後面側の機壁10に設
けた連通口80,80及びその機壁10の外面に
設けたダクト81を介して、排風機8(吸引フア
ン)の吸引口に連通させてある。
As shown in FIG. 2 and FIG. The air guide path c
As shown in FIG.
The above-mentioned exhaust passages b, b are connected to the hot air generating device 7 via the communication ports 80, 80 provided in the machine wall 10 on the rear side of the machine body 1, and the duct 81 provided on the outer surface of the machine wall 10. It is connected to the suction port of the exhaust fan 8 (suction fan) via the exhaust fan 8 (suction fan).

そしてこれにより、排風機8が作動して排気路
b,bが負圧になると、導風路c内の空気及び殻
粒案内壁6で囲われた空間d,d内の空気が、第
1図で細線の矢印の如く流動することで、熱風生
成装置7(バーナー装置)から導風路c内に送給
される熱風(乾燥風)が、前記細線の矢印のうち
の長い細線の矢印に沿い殻粒流下路aを横切るよ
うに排気路bに向けて流れ、同時に、第2図で2
重線の矢印に示している如く、連通口62からダ
クト61及び連通口60を経て、殻粒案内壁6で
囲われた空間d,d内に流れ、その熱風が前記第
1図で短い細線で示した矢印に沿い排気路b,b
に流れるようになつて、この殻粒案内壁6で囲わ
れる空間d,dが、殻粒流下路a,aの入口に向
けて流下していく殻粒に対し乾燥風を送給する補
助導風路となるようにしてある。
As a result, when the exhaust fan 8 is operated and the exhaust paths b and b become negative pressure, the air in the air guide path c and the air in the spaces d and d surrounded by the shell grain guide walls 6 are By flowing as shown by the thin arrows in the figure, the hot air (dry air) sent from the hot air generating device 7 (burner device) into the air guide path c flows in the direction of the long thin arrow among the thin arrows. Along the grain flow, the grains flow toward the exhaust passage b across the lower passage a, and at the same time, 2
As shown by the double-lined arrow, the hot air flows from the communication port 62 through the duct 61 and the communication port 60 into the spaces d and d surrounded by the shell grain guide walls 6, and the hot air flows as indicated by the short thin line in FIG. Exhaust path b, b along the arrow shown in
The spaces d, d surrounded by the shell grain guide walls 6 serve as auxiliary guides for supplying drying air to the shell grains flowing down toward the entrance of the shell grain flow paths a, a. It is designed to serve as a wind path.

なお、第1図において2重の鎖線で示した矢印
は、殻粒案内壁6で形成される補助導風路たる空
間d内の静圧が、排気路b,bとの距離の関係
で、導風路c内の静圧よりも低くなることから、
前述の第2図の2重線の矢印で示した経路を経な
いで、導風路cから直接空間d内に向かう乾燥風
の流れを示している。この流れは、前述の第2図
の2重線の矢印で示した乾燥風の流れに比してそ
の量が遥かに小さい。
In addition, the arrow shown by the double chain line in FIG. Since it is lower than the static pressure in the air guide path c,
This shows the flow of drying air directly from the air guide path c into the space d without passing through the path indicated by the double-lined arrow in FIG. 2 described above. The amount of this flow is much smaller than that of the dry air flow indicated by the double-lined arrow in FIG. 2 described above.

このように構成してある実施例装置は次のよう
に作用する。
The thus constructed embodiment apparatus operates as follows.

ドラムシヤツター4および排出用のスクリユー
コンベア5および昇降機12等の作動により、殻
槽2内に張込んだ殻粒が、殻槽2の底部に装設し
てある殻粒流下路a,aを流過して再び殻槽2の
上部に戻るよう循環流動している状態において、
熱風生成装置(バーナー装置)7を作動させると
ともに排風機(吸引フアン)8を作動させれば、
熱風生成装置7で生成した熱風(乾燥風)が、通
気性の隔壁30で形成した導風路cから、殻粒流
下路a,aを横切つて排気路bに向かうように流
れて、その間に殻粒流下路a,a内を流下する殻
粒層を透過し、これにより、殻粒に対し熱風を浴
びせた状態となつて、殻粒の乾燥作動を行なうよ
うになる。
By the operation of the drum shutter 4, the screw conveyor 5 for discharge, the elevator 12, etc., the shell grains filled in the shell tank 2 are moved through the shell grain flow channels a, a installed at the bottom of the shell tank 2. In a state where the fluid is circulating and flowing through it and returning to the upper part of the shell tank 2,
If the hot air generator (burner device) 7 is activated and the exhaust fan (suction fan) 8 is activated,
The hot air (dry air) generated by the hot air generator 7 flows from the air guide path c formed by the air-permeable partition 30, crosses the shell grain flow lower paths a, a, and heads toward the exhaust path b. The air passes through the shell layer flowing down in the shell flow paths a, a, and as a result, the shell is exposed to hot air, thereby drying the shell.

このとき、殻粒に対する熱風の供給は、排風機
8の作動により、導風路c内とそれにダクト61
を介して連通する傘状の殻粒案内壁6で囲われた
空間d,d内が負圧になつて、この空間d,d内
にも熱風生成装置7で生成した熱風が流入してく
ることから、導風路cを形成する通気性の隔壁3
0から吹き出されて殻粒流下路a,aを横切り排
気路bに向かう熱風と、前記空間dを形成する通
気性の隔壁よりなる殻粒案内壁6から吹き出され
て排気路bに向かう熱風との二者によつて行なわ
れる。
At this time, hot air is supplied to the shell grains through the air guide path c and into the duct 61 by the operation of the exhaust fan 8.
The spaces d, d surrounded by the umbrella-shaped shell guide walls 6 communicating through the space become negative pressure, and the hot air generated by the hot air generator 7 flows into these spaces d, d as well. Therefore, the air permeable partition wall 3 forming the air guide path c
Hot air is blown out from the shell grain flow path a, crosses the shell grain flow downstream paths a, and heads toward the exhaust path b, and hot air is blown out from the grain guide wall 6, which is made of an air-permeable partition wall that forms the space d, and heads toward the exhaust path b. It is carried out by two parties.

このため、殻粒層を透過する熱風の、透過方向
と直交する方向における面積が、空間dを形成す
る傘状の殻粒案内壁6の排気路bと対面する部分
6aだけ広げられたことになつて、この部分6a
から吹き出される熱風の分だけ多量の熱風を殻粒
に浴せるようになる。
Therefore, the area of the hot air passing through the shell grain layer in the direction perpendicular to the transmission direction is expanded by the portion 6a of the umbrella-shaped shell guide wall 6 that forms the space d, facing the exhaust path b. This part 6a
The shell grains are exposed to a large amount of hot air by the amount of hot air blown from the shell.

そして、この空間dを形成する傘状の殻粒案内
壁6は、殻粒流下路aの入口部位に、その流下路
a内に流入していく殻粒を左右に分流するように
設けられることから、この傘状の殻粒案内壁6の
熱風を吹き出す前述の部分6aとそれに対向する
排気路bの隔壁20との間に形成される殻粒流下
路a′はそれの熱風透過方向の厚さが、前述の導風
路cの隔壁30と排気路bの隔壁20との間に形
成される殻粒流下路a′の略半分の厚さとなる。
The umbrella-shaped shell guide wall 6 forming this space d is provided at the entrance of the shell flow path a so as to divide the shell grains flowing into the flow path a left and right. Therefore, the shell grain flow path a' formed between the above-mentioned portion 6a of the umbrella-shaped shell grain guide wall 6 from which hot air is blown out and the partition wall 20 of the exhaust passage b that opposes it has a thickness in the hot air transmission direction. The thickness is approximately half that of the grain flow lower passage a' formed between the partition wall 30 of the air guide passage c and the partition wall 20 of the exhaust passage b.

このため、殻粒流下路aの入口部付近における
熱風の透過方向の殻粒層の厚さが、導風路cの隔
壁30と排気路bの隔壁20との間に形成される
殻粒流下路a′における熱風透過方向の殻粒層の厚
さの略半分に薄くなつて、熱風が透過するときの
抵抗を半減させるので、この殻粒案内壁6の前記
部分6aから排気路bに向けて吹き出す熱風の量
が著しく多くなる。
For this reason, the thickness of the shell layer in the hot air transmission direction near the entrance of the shell flow lower passage a is the same as that of the shell grain layer formed between the partition wall 30 of the air guiding passage c and the partition wall 20 of the exhaust passage b. The thickness of the shell grain layer in the hot air transmission direction in path a' is reduced to approximately half, and the resistance when the hot air passes through is halved, so that the shell grain layer is thinned from the portion 6a of the shell grain guide wall 6 toward the exhaust path b. The amount of hot air blown out increases significantly.

そして、このことから、殻粒流下路aを流下す
る殻粒は、まず、殻粒流下路aの入口部位におい
て、透過抵抗が半減して透過量が多くなつた熱風
を浴び、この入口部位を流過して殻粒流下路a内
を流下するようになると、殻粒層の厚さが所定の
厚さに戻つて透過抵抗が増大してくることで透過
量が少なくなつた熱風を、連続して浴びるように
なる。
From this, the shell grains flowing down the shell grain flow path a are first exposed to the hot air whose permeation resistance is halved and the permeation amount is increased at the entrance of the shell grain flow path a, and this inlet region is When the hot air flows through the shell grain flow passage a, the thickness of the shell grain layer returns to a predetermined thickness and the permeation resistance increases, so that the hot air, whose permeation amount has decreased, is continuously Then, you will be able to take a bath.

以上説明したように、本発明による殻粒通風乾
燥装置は、殻粒を流下さす間に熱風を浴びせるた
めの殻粒流下路aを、熱風を吹き出す導風路cの
隔壁30と熱風を排出する排気路bの隔壁20と
を左右から対向さすことで、熱風が流下する殻粒
を横切つて透過していく形態に構成しておいて、
その殻粒流下路aの入口部位に、その殻粒流下路
aに流入していく殻粒を左右に分流して再び合流
させる殻粒案内壁6を、通気性の隔壁で風胴状に
装設して、それの内腔を熱風生成装置7に連通さ
せてあることから、殻粒流下路aに流入していく
殻粒の熱風透過方向における殻粒層の厚さが、殻
粒流下路aの入口部位において一たん薄くなつ
て、入口部位を流過したところで殻粒流下路aの
巾の厚さに戻るようになる。そして、入口部位で
殻粒層が薄くなつたところを、殻粒案内壁6から
吹出される熱風が透過して排気路bに流れるよう
になるので、殻粒流下路aを流下する殻粒は、熱
風の供給を受けても高温に昇温することのない流
下の初期において多量の熱風を浴び、しかるの
ち、殻粒流下路aの左右の間隔巾に対応する厚さ
の殻粒層を透過する所定の透過量の熱風を浴びな
がら殻粒流下路aを流下していくようになる。
As explained above, the shell grain ventilation drying device according to the present invention has a shell grain flow path a for blowing hot air while the shell grains are flowing down, a partition wall 30 of an air guide path c for blowing out hot air, and a partition wall 30 for blowing out hot air to discharge the hot air. By arranging the partition walls 20 of the exhaust passage b to face each other from the left and right, the hot air is configured to pass across the flowing shell grains,
At the entrance of the lower shell flow passage a, a shell guide wall 6 is installed in the shape of a wind trunk with an air permeable partition wall, which separates the shell grains flowing into the lower shell flow passage a to the left and right and joins them again. The thickness of the shell grain layer in the hot air transmission direction of the shell grains flowing into the shell grain flow lower passage a is the same as that of the shell grain flow lower passage a. It becomes thin once at the inlet part a, and after passing through the inlet part, it returns to the thickness equal to the width of the shell grain flow lower passage a. Then, the hot air blown from the shell grain guide wall 6 passes through the thin shell layer at the inlet portion and flows into the exhaust passage b, so that the shell grains flowing down the shell grain flow passage a are , is exposed to a large amount of hot air at the beginning of the flow, when the temperature does not rise to a high temperature even when hot air is supplied, and then passes through the shell grain layer with a thickness corresponding to the width of the left and right spacing of the shell grain flow downstream passage a. The shell grains flow down the flow path a while being exposed to a predetermined permeation amount of hot air.

従つて、殻粒流下路を流下する殻粒に対する熱
風の送給が、効率的に行なわれるよう、殻粒流下
路をそれの一側から他側に向けて横切るように吹
き流れる熱風により行なわれるようにして、熱風
が透過する方向の殻粒の層の厚さを薄くして熱風
を浴びる時間が長くなる形態としながら、その殻
粒流下路を流下する殻粒層を透過する熱風量を増
大させるために、殻粒層を薄くするのが、殻粒の
昇温による変質を生ぜしめることなく行なえるよ
うになつて、殻粒の乾燥を能率よく行なえるよう
になる。
Therefore, in order to efficiently supply hot air to the shell grains flowing down the shell grain flow path, the hot air is blown across the shell grain flow path from one side to the other side. In this way, the thickness of the shell grain layer in the direction through which the hot air permeates is made thinner so that the time of exposure to hot air is extended, while increasing the amount of hot air that passes through the shell grain layer flowing down the shell grain flow path. In order to achieve this, the shell grain layer can be made thinner without altering the quality of the shell grains due to an increase in temperature, and the shell grains can be dried more efficiently.

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

第1図は本発明を実施させる殻粒通風乾燥装置
の一部破断した正面図、第2図は第1図の−
線で切断した同上装置の要部の横断平面図、第3
図は同上装置の後端側の一部破断した側面図であ
る。 図面符号の説明、A……殻粒通風乾燥装置、a
……殻粒流下路、b……排気路、c……導風路、
d……空間、1……機体、10……前後の機壁、
11……左右の機壁、12……昇降機、13……
コンベア、2……殻槽、20……通気性の隔壁、
20a…下縁、21……流出口、30……通気性
の隔壁、31……連通口、32……ダクト、4…
…ドラムシヤツター、40……周壁、41……開
口、5……スクリユーコンベア、50……スクリ
ユー、51……搬送樋、6……殻粒案内壁、6a
……部分、60……連通口、61……ダクト、6
2……連通口、7……熱風生成装置(バーナー装
置)、8……排風機(吸引フアン)、80……連通
口、81……ダクト。
FIG. 1 is a partially cutaway front view of a grain shell ventilation drying device for carrying out the present invention, and FIG.
Transverse plan view of the main parts of the same device cut along a line, No. 3
The figure is a partially cutaway side view of the rear end side of the same device. Explanation of drawing symbols, A...Shell grain ventilation drying device, a
...Shell particle flow down passage, b... Exhaust passage, c... Air guide passage,
d... Space, 1... Aircraft, 10... Front and rear aircraft walls,
11...Left and right aircraft walls, 12...Elevator, 13...
Conveyor, 2...shell tank, 20...breathable bulkhead,
20a...lower edge, 21...outlet, 30...breathable partition, 31...communication port, 32...duct, 4...
... Drum shutter, 40 ... Peripheral wall, 41 ... Opening, 5 ... Screw conveyor, 50 ... Screw, 51 ... Conveying gutter, 6 ... Shell guide wall, 6a
...Part, 60...Communication port, 61...Duct, 6
2...Communication port, 7...Hot air generation device (burner device), 8...Exhaust fan (suction fan), 80...Communication port, 81...Duct.

Claims (1)

【特許請求の範囲】[Claims] 1 通気性の隔壁20により殻槽2の内腔底部を
前後に横切るよう機体1の前後の機壁10,10
間に設ける排気路bと、通気性の隔壁30により
前記排気路bに平行して機体1の前後の機壁1
0,10間に設ける熱風の導風路cとで、それら
の対向する通気性の隔壁20,30の間に上端側
が殻槽2の底部に通ずる殻粒流下路aを形成し
て、その殻粒流下路aの入口部位に、殻粒流下路
aに流入していく殻粒を左右に分流して再び合流
させる殻粒案内壁6を、通気性の隔壁により風胴
状に形成して装設し、その殻粒案内壁6の内腔
を、殻槽2の前後方向の外面に設けた連通ダクト
61を介して熱風生成装置7と連通させたことを
特徴とする殻粒通風乾燥装置。
1 The front and rear machine walls 10, 10 of the machine body 1 are arranged so as to cross the inner cavity bottom of the shell tank 2 in the front and rear directions by the breathable partition wall 20.
Aircraft walls 1 at the front and rear of the aircraft body 1 are parallel to the exhaust path b by means of an exhaust path b provided in between and an air permeable bulkhead 30.
With the hot air guide path c provided between 0 and 10, a shell particle flow downward path a whose upper end side communicates with the bottom of the shell tank 2 is formed between the opposing air permeable partition walls 20 and 30, A shell guide wall 6 is installed at the inlet of the lower grain flow passage a to separate the shell grains flowing into the lower shell flow passage a to the left and right and join them again. The shell grain ventilation drying device is characterized in that the inner cavity of the shell grain guide wall 6 is communicated with a hot air generating device 7 via a communication duct 61 provided on the outer surface of the shell tank 2 in the front-rear direction.
JP18636883A 1983-10-05 1983-10-05 Cereal grain ventilating drier Granted JPS6078280A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18636883A JPS6078280A (en) 1983-10-05 1983-10-05 Cereal grain ventilating drier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18636883A JPS6078280A (en) 1983-10-05 1983-10-05 Cereal grain ventilating drier

Publications (2)

Publication Number Publication Date
JPS6078280A JPS6078280A (en) 1985-05-02
JPH0437358B2 true JPH0437358B2 (en) 1992-06-19

Family

ID=16187153

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18636883A Granted JPS6078280A (en) 1983-10-05 1983-10-05 Cereal grain ventilating drier

Country Status (1)

Country Link
JP (1) JPS6078280A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62147896U (en) * 1986-03-12 1987-09-18
JPS6431992U (en) * 1987-08-21 1989-02-28

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6015869B2 (en) * 1977-09-30 1985-04-22 井関農機株式会社 grain dryer
JPS57174680A (en) * 1981-04-17 1982-10-27 Tatsumoto Akihiro Grain dryer
JPS5854092U (en) * 1981-10-08 1983-04-12 金子農機株式会社 Circulating grain dryer

Also Published As

Publication number Publication date
JPS6078280A (en) 1985-05-02

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