JPS5853272B2 - Kokuruikansouchi - Google Patents

Kokuruikansouchi

Info

Publication number
JPS5853272B2
JPS5853272B2 JP8564075A JP8564075A JPS5853272B2 JP S5853272 B2 JPS5853272 B2 JP S5853272B2 JP 8564075 A JP8564075 A JP 8564075A JP 8564075 A JP8564075 A JP 8564075A JP S5853272 B2 JPS5853272 B2 JP S5853272B2
Authority
JP
Japan
Prior art keywords
grain
cylinder
spiral
grains
window
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
Application number
JP8564075A
Other languages
Japanese (ja)
Other versions
JPS5213869A (en
Inventor
利彦 佐竹
博光 柴田
卓一 小峰
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.)
Satake Engineering Co Ltd
Original Assignee
Satake Engineering 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 Satake Engineering Co Ltd filed Critical Satake Engineering Co Ltd
Priority to JP8564075A priority Critical patent/JPS5853272B2/en
Publication of JPS5213869A publication Critical patent/JPS5213869A/en
Publication of JPS5853272B2 publication Critical patent/JPS5853272B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は穀類乾燥装置の改良に係り、乾燥能率を高め斑
乾燥を防いで穀粒の乾燥度を均一化するために開発した
ものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement of a grain drying device, and was developed in order to improve the drying efficiency, prevent patchy drying, and uniformize the degree of dryness of grains.

従来の穀類乾燥装置は、原則として穀粒が密接状に連設
した高密度の穀層に対して乾燥用の通風を行うものが通
例であり、高密度に形成された穀層では空気抵抗が大き
いので通風が不充分であると共に、穀層の送風側の風よ
り排風側の風の方が多湿になるので送風側と排風側の両
数層間に斑乾燥が発生する欠陥がある。
Conventional grain drying equipment generally provides drying ventilation to a dense grain layer in which grains are closely connected, and the air resistance in the densely formed grain layer increases. Since it is large, ventilation is insufficient, and the wind on the exhaust side of the grain layer becomes more humid than the wind on the blast side, so there is a defect that uneven drying occurs between several layers on both the blast side and the exhaust side.

また、大風量の強風により風洞内を穀粒と共に吹送しな
がら乾燥する例もあるが、乾燥作用が瞬間に等しい短時
間なので超大風量と大熱量を使用しながらその大部分に
空費して乾燥効果が極めて微弱で実用性がなく現在では
全く影を消している。
In addition, there are cases where grains are dried by blowing them through the wind tunnel with strong winds, but since the drying action is instantaneous, the drying process uses extremely large air volumes and a large amount of heat, but most of it is wasted during drying. Its effects were extremely weak and it was of no practical use, so it has now completely disappeared.

また、本発明の円筒と螺旋に似たもので、その螺旋軸を
送風管となし管の周壁に噴風孔を作り管周に噴風しなか
ら穀粒を乾燥しようとする特公昭47−10001号の
例もあり、また円筒を多孔性材料によって形設して内部
の螺旋上の穀粒を円筒の列部から噴風して乾燥する実公
昭35−9467号の例もあるが、原則として密層の穀
粒を吹いても風は通過しにくいと共に、上記の両装置の
場合は、風の大部分が螺旋の上面に薄層に積載された穀
粒の上面にある螺旋空間を空しく通過し穀層に対しては
表面をかすめて素通りし穀層内部組織に対しては通風し
ないので、乾燥効果は殆んど期待できず事実上実用性の
乏しいものである。
In addition, there is a device similar to the cylinder and spiral of the present invention, in which the spiral axis is used as a blowing pipe, and a blowing hole is formed on the circumferential wall of the pipe, and air is blown around the pipe to dry the grains. There is an example of No. 10001, and there is also an example of Utility Model Publication No. 35-9467, in which a cylinder is formed of a porous material and the spiral grains inside are dried by blowing air from the rows of the cylinder. It is difficult for the wind to pass through the densely layered grains, and in the case of both of the above devices, most of the wind blows through the spiral space on the top surface of the grains, which are stacked in a thin layer on the top surface of the spiral. Since the air passes through the grain layer by grazing the surface and does not ventilate the internal structure of the grain layer, almost no drying effect can be expected and it is practically impractical.

以上のように風洞内に形成した粗薄な穀層すなわち散乱
状の粒群に対して通風する場合には風洞の通過時間が短
いために大部分の風と熱を無効に消費し、また、穀層を
通過する場合には穀粒密度が過大なために通風乾燥の効
果が得られず且均−乾燥が至難である。
As described above, when ventilation is applied to the coarse grain layer formed in the wind tunnel, that is, the scattered grain group, most of the wind and heat are consumed ineffectively because the passage time through the wind tunnel is short. When passing through the grain layer, the grain density is too high, so that the effect of ventilation drying cannot be obtained and uniform drying is extremely difficult.

本発明は螺旋板自体を多孔壁となしその下方から送風す
ることにより、多孔壁を貫通して螺旋に積載された穀粒
を散乱させて穀粒密度を適度に調整し粒群間を通風乾燥
しながら上部し、上部の排穀窓からタンク内に四散させ
、タンク内の栓流中に穀粒をテンパリングして穀粒の斑
乾燥を防止し穀粒の亀裂を防止するものである。
The present invention uses the spiral plate itself as a porous wall, and by blowing air from below, the grains stacked in a spiral are scattered through the porous wall, the grain density is adjusted appropriately, and the grains are ventilated and dried. The grains are dispersed into the tank through the upper threshing window, and the grains are tempered in the plug flow inside the tank to prevent uneven drying of the grains and cracking of the grains.

本発明は、螺旋の空間に散乱中の穀粒群に対して乾燥風
を吹きつけるので風量と熱量が有効に利用され、しかも
乾燥風を上方輸送に併用し別個の昇降機などの無駄を省
き、亀裂に対して安全で高能率の乾燥を可能とする等の
効果を奏するものである。
The present invention blows drying air onto the grains scattered in a spiral space, so air volume and heat capacity are effectively utilized, and the drying air is also used for upward transport, eliminating the need for separate elevators and the like. This provides effects such as being safe against cracks and enabling highly efficient drying.

本発明を実施例図について説明すると、第1図は送風乾
燥装置の構造であり、下方が漏斗形のホッパーをなすテ
ンパリングクンク1の内部に円筒2を立設し、その上下
部に設けた軸受3,4に軸架した管軸5に固着した板状
螺旋6を多孔壁となし、また多孔壁の通風孔は第5図、
第6図、第7図、第8図に示すように通孔の指向性を考
えて斜または直上または左右に傾斜した通孔を混在させ
たものなど、穀類の種類あるいは乾燥目的の種類に応じ
て様々な形状に形成される。
To explain the present invention with reference to embodiment figures, Fig. 1 shows the structure of a blow drying device, in which a cylinder 2 is erected inside a tempering cylinder 1 whose lower part forms a funnel-shaped hopper, and a cylinder 2 is provided at the upper and lower parts of the tempering cylinder 2. A plate-shaped spiral 6 fixed to a tube shaft 5 mounted on the bearings 3 and 4 is used as a porous wall, and the ventilation holes in the porous wall are as shown in FIG.
As shown in Figures 6, 7, and 8, depending on the type of grain or the type of drying purpose, such as a mixture of through holes that are diagonal, directly above, or tilted to the left and right in consideration of the directivity of the through holes. It is formed into various shapes.

円筒2の上部周壁には排穀窓Tを設け、下部周壁には給
穀窓9を設け、それぞれ円筒2に列接重合した筒状開閉
弁8,10をそれぞれ把杆11,12によって上下動で
きるようにし、円筒2の上方は延長屈曲して排穀管13
となし、その先端に排出口14とその途上に排気管15
を設けである。
A grain discharging window T is provided on the upper peripheral wall of the cylinder 2, and a grain feeding window 9 is provided on the lower peripheral wall, and cylindrical on-off valves 8 and 10, which are aligned and overlapped with the cylinder 2, are moved up and down by gripping rods 11 and 12, respectively. The upper part of the cylinder 2 is extended and bent so that the grain threshing pipe 13
There is an exhaust port 14 at the tip and an exhaust pipe 15 on the way.
This is provided.

円筒2の下側部には送風機16の送風管IT・を臨設し
た絵風窓18に金網19を設けて円筒2内の穀粒の漏出
を防止する。
On the lower side of the cylinder 2, a wire mesh 19 is provided in a picture window 18 in which a blow pipe IT of a blower 16 is installed to prevent the grains inside the cylinder 2 from leaking.

列部から円筒2内に穀粒を供給するにはホッパー20か
らスクリューコンベヤー21を経て給穀口22に送入す
る。
To feed the grains from the rows into the cylinder 2, they are fed from a hopper 20 through a screw conveyor 21 to a grain feeding port 22.

第1図では螺旋6を回転する構造を示すが、螺旋6は必
ずしも回転せず停止固定のままで用0する場合もあり、
また、第9図のように螺旋6をカム23とロッド24に
より斜上下に往復回動する場合もある。
Although FIG. 1 shows a structure in which the spiral 6 is rotated, the spiral 6 may not necessarily rotate and may remain stationary and unused.
Further, as shown in FIG. 9, the spiral 6 may be reciprocated diagonally up and down by a cam 23 and a rod 24.

また、螺旋管軸5は必ずしも管体でなく普通の軸体とし
て用いることもあるが、第4図は管軸5の周壁に多数の
噴風孔25を設けた実例で、円筒2の下端に設けた気室
26を給風口2γから送風し送風孔28から管軸5内に
送風する場合もある。
In addition, the spiral tube shaft 5 is not necessarily used as a tube but may be used as an ordinary shaft, but FIG. In some cases, air is blown from the provided air chamber 26 through the air supply port 2γ and into the tube shaft 5 from the air hole 28.

第5図、第6図、第7図、第8図はそれぞれ螺旋6の板
体多孔壁の別実施例で、各図とも上図は縦断面図、下図
は平面図である。
5, 6, 7, and 8 each show another embodiment of the plate-like porous wall of the spiral 6, and in each figure, the upper figure is a longitudinal sectional view, and the lower figure is a plan view.

第5図のものは螺旋6の上方に向って旋回上昇する方向
すなわち斜上方向に螺旋板体に開孔した多孔壁で穀粒を
噴上散乱させながら旋回上昇させる作用を有し、第6図
のものは板体に直上方向の円孔と左右両方向に斜上して
開孔した通風孔を混在させた多孔壁で穀粒の散乱を促す
ために有効である。
The one in FIG. 5 has a porous wall opened in the spiral plate body in the upward direction of the spiral 6, that is, in the diagonal upward direction, and has the effect of causing the grains to swirl and rise while blowing up and scattering them. The one shown in the figure is effective for promoting the scattering of grains with a porous wall that has a combination of circular holes directly above the plate and ventilation holes opening diagonally upward in both left and right directions.

第1図、第8図のものは共に風に対する抵抗を可及的僅
少にした実施例である。
Both FIGS. 1 and 8 are embodiments in which the resistance to wind is minimized as much as possible.

その他種々任意の形状の通気孔が本発明に応用される。Various other ventilation holes of arbitrary shapes can be applied to the present invention.

本発明はテンパリングクンク1内に送入した穀粒が円筒
2内で多孔壁の螺旋6により噴流状に散乱しながら乾燥
されてテンパリングクンク1に還元する一種の循環行程
を形成し穀層を適切な密度に疎開し、しかも長時間に亘
り通風できるようにし、均一で高能率の乾燥を行うと共
に適度のテンパリングを施しなから穀粒の亀裂損傷を防
止して良質な乾燥穀粒を高速に処理することができる効
果を奏するものである。
The present invention forms a kind of circulation process in which the grains fed into the tempering gun 1 are scattered in a jet shape by the spiral 6 of the porous wall in the cylinder 2 and are returned to the tempering gun 1, forming a kind of circulation process. The grain is evacuated to an appropriate density and ventilated for a long period of time, allowing for uniform and highly efficient drying, as well as moderate tempering to prevent cracking and damage to the grain and produce high-quality dried grain at high speed. This has the effect that it can be processed in a number of ways.

特許請求の範囲第3項のものは、本発明の排穀装置で、
循環乾燥を終了した際円筒の上下にそれぞれ開設した排
穀窓と給穀窓とを各開閉弁を閉じて穀粒を上方の排穀管
を経て排出口から系列に排出するものである。
Claim 3 is a grain threshing device of the present invention,
When the circulation drying is completed, the opening/closing valves of the grain threshing window and grain feeding window opened at the top and bottom of the cylinder are closed, and the grains are discharged in series from the discharge port through the grain threshing pipe in the upper part.

実施例国策1図につむ・で説明すると、把杆11゜12
を上方に引き上げると開閉弁8,10がそれぞれ排穀窓
γと給穀窓9を閉じ穀粒は全量排出口14から排出する
Examples of National Policies To explain in Figure 1, the following points are taken:
When the grains are pulled upward, the on-off valves 8 and 10 close the grain discharging window γ and the grain feeding window 9, respectively, and the grains are completely discharged from the discharge port 14.

この際排気管15から余剰風を排気する実施例である。This is an embodiment in which excess air is exhausted from the exhaust pipe 15 at this time.

本発明は構成費と設置場所を省くために昇降機などの揚
穀装置を全廃し、単に開閉弁の開閉切換だけで簡便に穀
粒を系列に取り出せる効果を併有するものである。
The present invention has the effect of completely eliminating grain lifting equipment such as elevators in order to save construction costs and installation space, and allowing grains to be easily taken out in series by simply switching the on-off valve on and off.

なお、本発明は円筒の上方に吸引して防塵を兼用して同
様の乾燥目的を達することも可能である。
In addition, in the present invention, it is also possible to achieve the same drying purpose by suctioning the air above the cylinder to also serve as dustproofing.

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

図面は本発明の例示図で、第1図は全体の縦断面図、第
3図はその要部拡大図、第2図、第4図、第9図は応用
実施例要部拡大図、第5図、第6図、第7図、第8図は
共に本発明要部の拡大図で、それぞれ上図が縦断面図、
下図が平面図である。 1・・・・・・テンパリングタンク、2・・・・・・円
筒、3・・・・・・軸受、4・・・・・・軸受、5・・
・・・・管軸、6・・・・・・螺旋、γ・・・・・・排
穀窓、8・・・・・・排穀窓開閉弁、9・・・・・・給
穀窓、10・・・・・・給穀窓開閉弁、11・・・・・
・把杆、12・・・・・・把杆、13・・・・・・排穀
管、14・・・・・・排出口、15・・・・・・排気管
、16・・・・・・送風機、1γ・・・・・・送風管、
18・・・・・・絵風窓、19・・・・・・金網、20
・・・・・・ホッパー、21・・・・・・スクリューコ
ンベヤー 22・・・・・・給穀口、23・・・・・
・カム、24・・・・・・ロッド、25・・・・・・噴
風口、26・・・・・・気室、2γ・・・・・・絵風口
、28・・・・・・送風千−
The drawings are illustrative diagrams of the present invention; FIG. 1 is an overall vertical cross-sectional view, FIG. 3 is an enlarged view of the main parts thereof, FIGS. 2, 4, and 9 are enlarged views of the main parts of applied embodiments, and FIG. 5, 6, 7, and 8 are all enlarged views of the main parts of the present invention, and the upper figure is a vertical cross-sectional view, respectively.
The figure below is a plan view. 1... Tempering tank, 2... Cylinder, 3... Bearing, 4... Bearing, 5...
...Pipe shaft, 6...Spiral, γ...Grain removal window, 8...Grain removal window opening/closing valve, 9...Grain feeding window , 10... Grain feeding window opening/closing valve, 11...
- Grip, 12... Grip, 13... Grain removal pipe, 14... Discharge port, 15... Exhaust pipe, 16... ...Blower, 1γ...Blow pipe,
18...Picture style window, 19...Wire mesh, 20
...Hopper, 21...Screw conveyor 22...Grain feeder, 23...
・Cam, 24...Rod, 25...Blower port, 26...Air chamber, 2γ...Picture port, 28...Blower Thousand

Claims (1)

【特許請求の範囲】 1 下方が漏斗形のホッパーをなすテンパリングタンク
内に立設した円筒の内面に沿って装設した薄板螺旋の板
体を多孔壁となし、前記螺旋の多孔壁面の下方から上方
に向って乾燥用風を通過するようにし、前記円筒の下部
周壁には前記タンク内の穀粒の給穀窓を設けると共に、
前記円筒の下側部に絵風口を設け、穀粒を前記円筒内の
薄板螺旋上で噴流状に散乱させるよう通風しながら乾燥
し上部排穀窓から前記タンク内に返還して環流させる循
環行程を形成したことを特徴とする穀類乾燥装置。 2、特許請求の範囲第1項のものにおいて、前記螺旋を
その主軸と共に回転または往復回動するように軸架した
ことを特徴とする穀類乾燥装置3 下方が漏斗形のホッ
パーをなすテンパリングタンク内に立設した円筒の内面
に沿って装設した薄板螺旋の板体を多孔壁となし、下方
から上方に向って送風し、前記円筒の下方を絵風口とな
し、上方の周壁に排穀窓を設けると共に、該周壁に沿い
上下動して前記排穀窓を開閉する開閉弁を設け、前記円
筒の上部を曲折して前記タンク列に排穀する排穀管とな
したことを特徴とする穀類乾燥装置。
[Scope of Claims] 1. A thin spiral plate installed along the inner surface of a cylinder installed upright in a tempering tank whose lower part forms a funnel-shaped hopper is used as a porous wall, and from below the perforated wall surface of the spiral. The drying air is allowed to pass upward, and a grain feeding window for grains in the tank is provided in the lower peripheral wall of the cylinder, and
A circulation process in which a picture opening is provided on the lower side of the cylinder, and the grains are dried while being ventilated so as to be scattered in a jet shape on the thin plate spiral inside the cylinder, and then returned to the tank through the upper grain threshing window and circulated. A grain drying device characterized by comprising: 2. A grain drying device according to claim 1, characterized in that the spiral is mounted on a shaft so that it rotates or reciprocates together with its main shaft.3 Inside a tempering tank whose lower part forms a funnel-shaped hopper. A thin spiral plate installed along the inner surface of an upright cylinder is used as a porous wall, and air is blown from the bottom to the top. and an on-off valve that moves up and down along the peripheral wall to open and close the grain threshing window, and the upper part of the cylinder is bent to form a grain threshing pipe for shredding grain into the tank row. Grain drying equipment.
JP8564075A 1975-07-11 1975-07-11 Kokuruikansouchi Expired JPS5853272B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8564075A JPS5853272B2 (en) 1975-07-11 1975-07-11 Kokuruikansouchi

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8564075A JPS5853272B2 (en) 1975-07-11 1975-07-11 Kokuruikansouchi

Publications (2)

Publication Number Publication Date
JPS5213869A JPS5213869A (en) 1977-02-02
JPS5853272B2 true JPS5853272B2 (en) 1983-11-28

Family

ID=13864413

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8564075A Expired JPS5853272B2 (en) 1975-07-11 1975-07-11 Kokuruikansouchi

Country Status (1)

Country Link
JP (1) JPS5853272B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2725839C2 (en) * 1977-06-08 1985-10-10 Roderich W. Dr.-Ing. 6100 Darmstadt Gräff Method and device for drying powdery bulk goods
KR101068998B1 (en) 2008-08-11 2011-09-30 금호석유화학 주식회사 Method for preparation of the N-substitution maleimide

Also Published As

Publication number Publication date
JPS5213869A (en) 1977-02-02

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