JPS608434B2 - Grain low temperature drying equipment - Google Patents

Grain low temperature drying equipment

Info

Publication number
JPS608434B2
JPS608434B2 JP7106480A JP7106480A JPS608434B2 JP S608434 B2 JPS608434 B2 JP S608434B2 JP 7106480 A JP7106480 A JP 7106480A JP 7106480 A JP7106480 A JP 7106480A JP S608434 B2 JPS608434 B2 JP S608434B2
Authority
JP
Japan
Prior art keywords
grain
drying
frame
grains
exhaust
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
JP7106480A
Other languages
Japanese (ja)
Other versions
JPS56166948A (en
Inventor
金次郎 井上
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.)
TORYO KIKAI KK
ZAOO NETSUKI KK
Original Assignee
TORYO KIKAI KK
ZAOO NETSUKI 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 TORYO KIKAI KK, ZAOO NETSUKI KK filed Critical TORYO KIKAI KK
Priority to JP7106480A priority Critical patent/JPS608434B2/en
Publication of JPS56166948A publication Critical patent/JPS56166948A/en
Publication of JPS608434B2 publication Critical patent/JPS608434B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は穀類を低温度で且つ短時間で乾燥することが出
来る穀類低温乾燥装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a low-temperature grain drying device that can dry grains at low temperatures and in a short time.

従来籾などの穀類を乾燥する場合ら槽内に張り込んだ籾
に熱風を送り込み、昇降機により数回楯還させ乍ら乾燥
を行なっている。
Conventionally, when drying grains such as paddy, hot air is sent through the paddy placed in a tank, and the drying process is carried out by blowing hot air through the paddy and raising and lowering it several times using an elevator.

この場合、乾燥時間は、乾燥前の含水率が20〜26%
で乾燥後の含水率を14〜15%とする場合、熱風温度
が(籾の張り込み量と外気温度に左右されるが)53〜
63午○で6〜1幼時間必要としている。
In this case, the drying time is such that the moisture content before drying is 20-26%.
When the moisture content after drying is 14-15%, the hot air temperature is 53-15% (although it depends on the amount of paddy packed in and the outside temperature).
63pm and requires 6 to 1 preschool hours.

この乾燥時間を短縮するために熱風温度を高くすること
も考えられるが、籾表面からの急激な脱水と、穀温の高
まりによ畑岡割れ現象が生じ「破砕米の発生が多くなる
と共に光沢や品質の劣化を来す欠点がある。このような
欠点を除去するため、低温度で乾燥するいわゆる低温乾
燥装置も種々開発され提案されているが、今度は乾燥に
時間がかかりすぎるといった欠点があり実用化されてい
ないのが現状である。
In order to shorten this drying time, it may be possible to increase the temperature of the hot air, but rapid dehydration from the surface of the paddy and the rise in grain temperature cause the Hataoka cracking phenomenon, resulting in "more broken rice and a loss of luster." It has the drawback of deteriorating quality.In order to eliminate this drawback, various so-called low-temperature drying devices that dry at low temperatures have been developed and proposed, but they have the drawback of taking too long to dry. The current situation is that it has not been put into practical use.

本発明は上記に鑑みて案出されたものであり、低温度で
且つ短時間で乾燥することの出来る穀類乾燥装置を提供
することを目的としたもので、その要旨は上部に穀類投
入口を有する乾燥機に貯留槽と加温槽と、乾燥室および
集穀槽とを順次立体的に重設し、加温槽には一端が温風
発生装置と蓮適する温風蹟気枠を並設して各枠間に第一
流下路を形成すると共に、乾燥室には一側端が溢・湿度
調整装置と蓮通し他側端が閉塞された通風暖気枠と、池
側端が排気口に蓮適した排気枠とを各枠間に第二流下路
が形成せられるよう交互に並設すると共に、上記排気口
に吸引排風機を装備したことを特徴とする穀類低温乾燥
装置にある。
The present invention was devised in view of the above, and aims to provide a grain drying device that can dry grains at low temperatures and in a short time. A storage tank, a heating tank, a drying room, and a grain collecting tank are sequentially installed three-dimensionally in a dryer with a storage tank, a heating tank, a drying room, and a grain collection tank, and one end of the heating tank is equipped with a warm air frame that is suitable for a hot air generator and a lotus. In addition to forming a first flow path between each frame, the drying room has a ventilation heating frame with one end connected to the overflow/humidity adjustment device and a lotus passage, and the other end closed to the exhaust port. The low-temperature drying apparatus for grains is characterized in that exhaust frames suitable for a lotus are alternately arranged in parallel so that a second flow path is formed between each frame, and the exhaust port is equipped with a suction/exhaust fan.

以下図面に示す実施例に基づき本発明を詳細に説明する
The present invention will be described in detail below based on embodiments shown in the drawings.

図において1‘ま乾燥機本体で、上方に均分機2と穀類
投入口3を備えている。
In the figure, 1' is the main body of the dryer, which is equipped with an equalizer 2 and a grain input port 3 above.

4は貯留槽で投入口3より落下した穀類が一旦貯留され
、その下部に加湿槽5と乾燥室6とが上下に配設されて
いる。
Reference numeral 4 denotes a storage tank in which the grains that have fallen from the input port 3 are temporarily stored, and a humidification tank 5 and a drying chamber 6 are arranged above and below in the lower part of the storage tank.

加温槽5は断面三角形をした温風薄気枠7が並列して構
架され、穀類が通る第一流下路8が形成されており「各
温風噴気枠?の一端は閉塞されt他端は温風発生装置9
と連結し、送入ファン富覇で温風が送り込まれるように
構成されている。
The heating tank 5 is constructed of warm air thin air frames 7 with triangular cross sections arranged in parallel, forming a first flow path 8 through which the grains pass. is hot air generator 9
The structure is such that warm air is sent through the inlet fan Fuha.

乾燥室6には通風暖気枠1 1と排気枠】2とが交互に
並列的に配設され、各枠亀量と12との間に穀類の第二
流下路13が形成されておりL通風贋気枠11の一側端
は閉塞し、池側端はト温母線度調整装置i4と運通して
いる。又、排気枠12は上記通風贋気枠亀1とは逆に一
側端が閉塞し〜池側端は排気口亀6と蓮通しており、吸
引排風機亀61こより乾燥室6内の湿った空気が吸引さ
れるよう構成されている。
In the drying room 6, ventilation heating frames 11 and exhaust frames 2 are arranged alternately in parallel, and a second flow passage 13 for grains is formed between each frame weight and 12. One end of the faulty air frame 11 is closed, and the pond-side end communicates with the temperature generator i4. In addition, the exhaust frame 12 is closed at one end, contrary to the ventilation frame 1, and the pond-side end is connected to the exhaust port 6, so that the moisture in the drying chamber 6 is removed from the suction/exhaust mechanism 61. The structure is such that air is sucked out.

第二流下路亀3の下端にはロータリバルプ亀7を設け、
その下の集穀槽亀飢こ連通させており、集穀槽181こ
は、ロータリバルブより落下した穀類を昇降機19に送
り込むスクリューコンベア20が底部に配設されている
A rotary valve turtle 7 is provided at the lower end of the second downstream passage turtle 3,
The grain collecting tank 181 below is in communication with the grain collecting tank 181, and a screw conveyor 20 is disposed at the bottom of the grain collecting tank 181 to feed the grains that have fallen from the rotary valve to the elevator 19.

本発明による乾燥機は上記の様な構成であり、上部の投
入口3より落下し貯留槽4に一旦貯留された穀類は、ま
ず「乾燥室6の第二流下路亀3に入り通風乾燥される前
に「加温槽5において温風発生装置9からの温風を温風
暖気枠7の多孔21を通して受け加溢される。
The dryer according to the present invention has the above-mentioned configuration, and the grains that fall from the input port 3 at the top and are temporarily stored in the storage tank 4 first enter the second downstream passage turtle 3 of the drying chamber 6 and are ventilated and dried. Before heating, warm air from the hot air generator 9 is received in the heating tank 5 through the holes 21 of the hot air heating frame 7 and is flooded.

この加温はt温風噴気枠7を並設する事により形成され
た第一流下路8を流下する穀類を例えば外気溢十500
〜20ooの温風で加溢する事により行ない、しかも加
塩槽5は貯留槽4内に張り込んだ穀類の重量で半密閉状
態にあり、したがって、加温槽5内の穀類を均一に加温
できる。
This heating is performed by heating the grains flowing down the first flow passage 8 formed by arranging the warm air blower frames 7 in parallel,
This is carried out by flooding with ~20 oo of hot air, and the salting tank 5 is semi-sealed due to the weight of the grains loaded into the storage tank 4, so that the grains in the heating tank 5 are uniformly heated. can.

そして加温槽5において、20q○〜4100(外気温
が15qo〜21℃の場合)に加溢されると穀類内の水
分が膨張し、外皮に鯵出してくる。
When the heating tank 5 is heated to 20qo to 4100°C (when the outside temperature is 15qo to 21°C), the water inside the grain expands and the horse mackerel comes out on the outer skin.

次にこの状態になった穀類は排気枠12と通風暖気枠1
11こ挟まれた第二流下路13に達し、ここで、温・湿
度調整装置蔓4により、低湿度「低温度の温風を通風噂
気枠11の多孔23を通して受け乾燥されるものである
Next, the grains in this state are the exhaust frame 12 and the ventilation warming frame 1.
It reaches a second flow passage 13 sandwiched between 11 and 11, where the temperature/humidity adjusting device 4 receives and dries low-humidity, low-temperature warm air through the perforations 23 of the ventilation frame 11. .

ここで、第3図によって、温風の排気径路を説明すると
、排気口16に設けた吸引排風機16の吸引により排気
室22および該排気室22に蓮適する排気枠12内の圧
力が下がり「穀類を介して蓮適する通風頃気枠1 1内
の低温度、低温度の空気が、第二流下路13内の穀類が
重力により流下する方向に対して直角に穀類を横切り、
穀類の表面より水分を吸収し「多湿の風となって「排気
枠12を適して排気室22に吸引され、排気ロー5より
外気に排出される。
Here, to explain the hot air exhaust path with reference to FIG. 3, the pressure inside the exhaust chamber 22 and the exhaust frame 12 that fits into the exhaust chamber 22 decreases due to suction by the suction exhaust fan 16 provided at the exhaust port 16. The low-temperature air in the air frame 11 crosses the grains at right angles to the direction in which the grains in the second flow passage 13 flow down due to gravity,
Moisture is absorbed from the surface of the grains and becomes a humid wind, which is sucked into the exhaust chamber 22 through the exhaust frame 12 and discharged to the outside air through the exhaust row 5.

この時、同時に第二流下略13内の多量の塵挨も、排気
風と共に排気口15より排出される。
At this time, a large amount of dust in the second downstream section 13 is also discharged from the exhaust port 15 along with the exhaust air.

この乾燥室6内の通風噴気枠1 亀から噴出する風の温
度はほゞ外気温と同程度とし、又湿度は12%程度とし
た。普通、乾燥後の含水率は政府費付米の場合14%〜
15%以下とされているが「従来の燈油を使用した熱風
乾燥の場合、乾燥後の含水率を16%以下とすることは
技術的にも不可能(18%止り)であり、自ずから等級
にも悪影響を与えていた。
The temperature of the wind blowing out from the ventilation blower frame 1 in the drying chamber 6 was approximately the same as the outside temperature, and the humidity was approximately 12%. Normally, the moisture content after drying is 14% or more for government-funded rice.
Although it is supposed to be 15% or less, ``In the case of conventional hot air drying using kerosene, it is technically impossible to reduce the moisture content to 16% or less after drying (only 18%). was also having a negative impact.

しかし、本発明では「外気温に近い風としたため「湿度
を12%以下に設定することも容易であり「その目的を
良く達成出釆る。次に第二流下路蔓3内を流下した穀類
は通風噴気枠奮1の多孔23を通しても低温度の風を受
け、ある程度乾燥されて、ロータリバルブ17によって
集穀槽亀8の額斜壁24上に落下しト額斜壁面に沿って
移動して煩斜壁凹部25に集まり、スクリューコンベア
20‘こよって昇降機19まで運ばれる。
However, in the present invention, since the wind is close to the outside temperature, it is easy to set the humidity to 12% or less, and the purpose is well achieved. The grains also receive low-temperature wind through the perforations 23 of the ventilation fumarole frame 1, are dried to some extent, fall onto the sloped wall 24 of the grain collecting tank 8 by the rotary valve 17, and move along the sloped wall surface. They gather in the oblique wall recess 25 and are conveyed to the elevator 19 by the screw conveyor 20'.

昇降機竃9によって送り上げられた穀類は、均分機2に
よって貯留槽4中央まで運ばれ飛散盤26青こ落下し貯
留槽4内に均一に飛散貯留される。
The grains sent up by the elevator stove 9 are carried to the center of the storage tank 4 by the equalizer 2, fall onto a scattering plate 26, and are uniformly scattered and stored in the storage tank 4.

以上の工程が1サイクルであり、穀類の乾燥状態により
、上記サイクルを数回繰り返しL所定の含水率になるま
で乾燥を行なうものである。通常籾などの穀類の乾燥は
、穀温がある一定温度に高まるまでは、水分の蒸発はな
く「穀温のみが変化する。そしてち次に一定穀温に達す
ると表面の水分のみが蒸発し、穀温および乾燥速度は共
に一定に保たれる。
The above process is one cycle, and depending on the drying state of the grain, the above cycle is repeated several times until the grain reaches a predetermined moisture content. Normally, when drying grains such as paddy, water does not evaporate until the grain temperature reaches a certain temperature, and only the grain temperature changes.Then, once the grain temperature reaches a certain temperature, only the surface water evaporates. , grain temperature and drying rate are both kept constant.

しかし、この一定保持期間は、余程湿った穀類でなけれ
ば存在せず、通常次の過程に移る。
However, this holding period does not exist unless the grain is extremely moist, and the grain usually moves on to the next step.

すなわち、穀類内部より表面に水分が移動し、表面の水
分が温風により蒸発して持ち去られ穀温は上昇し、乾燥
速度は次第に減少する。このように、穀類の水分を蒸発
させるためには、穀溢をある一定温度まで上げてやらな
ければならないとされているが、本発明では乾燥室6の
第二流下路13内に穀類が流下し乾燥される前に「加温
槽5の温風噴気枠7の多孔21を通して温風により穀類
を均一に加溢することにより、穀頬内部の水分の表面へ
の移動を誘発させることになり、次の乾燥室6内での乾
燥時間を大中に短縮することができる。
That is, moisture moves from the inside of the grain to the surface, and the moisture on the surface is evaporated and carried away by hot air, raising the grain temperature and gradually decreasing the drying rate. In this way, in order to evaporate the moisture in the grains, it is said that the grain overflow must be raised to a certain temperature, but in the present invention, the grains are not allowed to flow down into the second flow path 13 of the drying chamber 6. By uniformly flooding the grains with warm air through the holes 21 of the hot air blower frame 7 of the heating tank 5 before drying, the moisture inside the grains is induced to move to the surface. , the next drying time in the drying chamber 6 can be greatly shortened.

しかも、乾燥時の送風温度を低温にでき「 したがって
、穀類の胴割れの発生をおさえることができ「かつ、穀
類表皮の変色もなく、均一な乾燥状態で仕上り、また、
高温で穀類成分が破壊されることは全くないため、良品
質の穀類を提供でき、乾燥終了後直ちに籾摺りができる
等の効果がある。
In addition, the air blowing temperature during drying can be kept low, thereby suppressing the occurrence of shell cracking of the grains.Also, there is no discoloration of the grain skin, and the finished product is uniformly dried.
Since grain components are not destroyed at high temperatures, high-quality grains can be provided, and the grain can be hulled immediately after drying.

又、第二流下路13を流下する間に、穀類内に多量に混
入している塵挨は、吸引9E風機!6により排気枠12
から吸い取られ、排気口15から大部分の塵挨が外部に
排出されるいわゆる吹流し方式を採用しているため「空
気循環方式のフィル夕‐で除去する場合のように目詰り
現象も発生せず、運転を停止して掃除をするといった手
数もなく、且つごみの混入がない乾燥穀類が得られると
いった諸効果もある。
Also, while flowing down the second flow path 13, a large amount of dust mixed into the grains is removed by the suction 9E blower! Exhaust frame 12 by 6
Since it uses a so-called windsock method in which most of the dust is sucked up from the air and discharged to the outside from the exhaust port 15, there is no clogging phenomenon that occurs when removing with an air circulation filter. There are also advantages such as there is no need to stop the operation and clean it, and dry grains that are free from contamination with dust can be obtained.

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

第1図は、本発明に係る乾燥機の縦断面図、第2図は、
前図のA−A断面図、第3図は、同じくB−B断面図、
第4図は、C−C断面図である。 1・・・・・・乾燥機本体、4・…・・貯留槽、5・・
・・・・加温槽、6・・・・・・乾燥室、7…・・・温
風贋気枠、8・…’・第一流下路、9…・・・温風発生
装置、11・…・・通風噴気枠、12…・・・排気枠、
13・…・・第二流下路、14・・・・・・溢・湿度調
整装贋、15・…・・排気口、16・・・・・・吸引排
風機、】8・・・・・・集穀槽、19・・・・・・昇降
機。 第1図 第2図 第3図 第4図
FIG. 1 is a longitudinal sectional view of a dryer according to the present invention, and FIG.
The previous figure is a cross-sectional view taken along line A-A, and FIG. 3 is a cross-sectional view taken along line B-B.
FIG. 4 is a sectional view taken along line C-C. 1...Dryer body, 4...Storage tank, 5...
...Heating tank, 6...Drying room, 7...Hot air counter, 8...', first flow path, 9...Hot air generator, 11 ...... Ventilation blow frame, 12... Exhaust frame,
13... Second flow passage, 14... Overflow/humidity adjustment device, 15... Exhaust port, 16... Suction exhaust fan, ]8...・Grain collection tank, 19... Lifting machine. Figure 1 Figure 2 Figure 3 Figure 4

Claims (1)

【特許請求の範囲】[Claims] 1 上部に穀類投入口を有する乾燥機に貯留槽と加温槽
と、乾燥室および集穀槽とを順次立体的に重設し、加温
槽には一端が温風発生装置と連通する温風噴気枠を並設
して各枠間に第一流下路を形成すると共に、乾燥室には
一側端が温・湿度調整装置と連通し他側端が閉塞された
通風噴気枠と、他側端が排気口に連通した排気枠とを各
枠間に第二流下路が形成せられるよう交互に並設すると
共に、上記排気口に吸引排風機を装備したことを特徴と
する穀類低温乾燥装置。
1 A storage tank, a heating tank, a drying room, and a grain collecting tank are sequentially installed three-dimensionally in a dryer that has a grain input port at the top, and the heating tank has a heating tank with one end communicating with a hot air generator. Wind blower frames are arranged in parallel to form a first flow path between each frame, and the drying room includes a ventilation blower frame with one end communicating with the temperature/humidity adjustment device and the other end closed. Low-temperature drying of grains, characterized in that exhaust frames whose side ends communicate with exhaust ports are alternately arranged in parallel so that a second flow path is formed between each frame, and the exhaust ports are equipped with a suction exhaust fan. Device.
JP7106480A 1980-05-28 1980-05-28 Grain low temperature drying equipment Expired JPS608434B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7106480A JPS608434B2 (en) 1980-05-28 1980-05-28 Grain low temperature drying equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7106480A JPS608434B2 (en) 1980-05-28 1980-05-28 Grain low temperature drying equipment

Publications (2)

Publication Number Publication Date
JPS56166948A JPS56166948A (en) 1981-12-22
JPS608434B2 true JPS608434B2 (en) 1985-03-02

Family

ID=13449716

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7106480A Expired JPS608434B2 (en) 1980-05-28 1980-05-28 Grain low temperature drying equipment

Country Status (1)

Country Link
JP (1) JPS608434B2 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58141191U (en) * 1982-03-15 1983-09-22 辰本 「あき」弘 grain dryer
JPS5940791U (en) * 1982-09-09 1984-03-15 静岡製機株式会社 Circulating grain dryer with pre-drying section
JPH02309178A (en) * 1989-05-22 1990-12-25 Iseki & Co Ltd Cereal drier
JPH04129095U (en) * 1991-05-10 1992-11-25 北斗工機株式会社 Grain drying equipment installation structure
JPH04129093U (en) * 1991-05-10 1992-11-25 北斗工機株式会社 Grain drying equipment installation structure
JP7344113B2 (en) * 2019-11-12 2023-09-13 日鉄鉱業株式会社 Water removal equipment for loose materials

Also Published As

Publication number Publication date
JPS56166948A (en) 1981-12-22

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