JPH06237687A - Method for drying grain - Google Patents

Method for drying grain

Info

Publication number
JPH06237687A
JPH06237687A JP5310593A JP5310593A JPH06237687A JP H06237687 A JPH06237687 A JP H06237687A JP 5310593 A JP5310593 A JP 5310593A JP 5310593 A JP5310593 A JP 5310593A JP H06237687 A JPH06237687 A JP H06237687A
Authority
JP
Japan
Prior art keywords
air
grain
temperature
exhaust
relative humidity
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.)
Granted
Application number
JP5310593A
Other languages
Japanese (ja)
Other versions
JP3271026B2 (en
Inventor
Satoru Akata
悟 赤田
Setsuo Sasaki
節夫 笹木
Kenji Usui
賢志 臼井
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.)
Hokoku Kogyo Co Ltd
Original Assignee
Hokoku Kogyo 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 Hokoku Kogyo Co Ltd filed Critical Hokoku Kogyo Co Ltd
Priority to JP5310593A priority Critical patent/JP3271026B2/en
Publication of JPH06237687A publication Critical patent/JPH06237687A/en
Application granted granted Critical
Publication of JP3271026B2 publication Critical patent/JP3271026B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To improve drying efficiency of grain. CONSTITUTION:Whether a dehumidifier 13 is operated or not is judged according to outside air conditions in a dehumidifier operation-judging part 12. When it is judged not to operate the dehumidifier 13, outside air is sucked in large air amounts and the discharge air is discharged. Thereby, consumed electric power of the dehumidifier becomes zero and drying efficiency is raised by large dehydration amount and air amount ratio of safety limit is secured. When it is judged to operate the dehumidifier, whether the grain is safe or not is judged according to discharge conditions in a grain safety judging part 16. When the operation is judged to be safe, whether fed air amount is large or small and discharged air is recycled or not are judged in a recycle and air amount judging part 18. Thereby, quality of grains is guaranteed and dehumidifying efficiency of the dehumidifier are increased and consumed electric power of a blower 7 is reduced by making air amount small to improve drying efficiency. When it is judged that the grain is not safe, air amount is made large and whether discharged air is recycled or not is judged and dehydrating amount is increased while satisfying air amount ratio of safety limit and guaranteeing quality of the grain to improve efficiency of the dehumidifier 13 and drying efficiency.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は穀物の品質を維持して穀
物の乾燥効率を向上するようにした穀物の乾燥方法に関
するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a grain drying method for maintaining grain quality and improving grain drying efficiency.

【0002】[0002]

【従来の技術】穀物として以下収穫米を例にして説明す
る。収穫米処理施設としては、収穫米の処理過程、すな
わち収穫米の貯留、乾燥および籾摺り工程での米の品質
を保証しなければならない。米の品質とは、貯留時にお
ける収穫米のかび、食味、胴割れ、籾摺り時における玄
米の肌ずれ等をいう。そして、米の水分が多く、かつ、
長期間貯留するとかびが発生し、また、乾燥のし過ぎい
わゆる過乾燥になると食味の低下および胴割れが発生
し、また、水分が多いと肌ずれが起きて食味が低下す
る。したがって、米の含有水分は米の品質に大きく影響
する。また、米自体は生き物であるので温度が高いと米
の呼吸が活発になって米内部のエネルギを消費(以下穀
物の劣化という)して米の品質が低下し、また、温度が
高いと微生物の繁殖が活発になってかび発生を引き起こ
し米の品質を低下させるので、貯留されている米の温度
自体も米の品質に大きく影響する。
2. Description of the Related Art Harvested rice will be described below as an example of grain. The harvested rice processing facility must guarantee the quality of the harvested rice during the treatment process of the harvested rice, that is, storage, drying and hulling of the harvested rice. The quality of rice refers to mold, taste, cracking of the harvested rice at the time of storage, skin deviation of brown rice at the time of hulling, and the like. And there is a lot of water in the rice, and
If it is stored for a long period of time, mold will be generated, and if it is overly dried, so-called overdrying will cause deterioration of taste and cracking of the body. Therefore, the water content of rice greatly affects the quality of rice. Also, since rice itself is a living thing, if the temperature is high, the respiration of rice becomes active and the energy inside the rice is consumed (hereinafter referred to as the deterioration of grains), and the quality of rice deteriorates. Since the reproductive activity of rice plants becomes active and causes mold development, which reduces the quality of rice, the temperature of the stored rice itself also has a great influence on the quality of rice.

【0003】そこで、農林水産省では収穫米の含有水分
を調整維持して収穫米の品質を保つための風量基準とし
て、収穫米(穀物の種類)の含有水分および貯留日数に
対して貯留米の単位重量当たりの風量が決められてい
る。これを安全限界風量比という。したがって、この安
全限界風量比を満たしておれば、例えば水分24%である
10tonの収穫米を三日間貯留しても安全であるという
具合に判定されることになる。
Therefore, the Ministry of Agriculture, Forestry and Fisheries of the Ministry of Agriculture, Forestry and Fisheries regulates the moisture content of the harvested rice and maintains the quality of the harvested rice as the air flow standard. The air volume per unit weight is fixed. This is called the safety limit air volume ratio. Therefore, if this safety limit air volume ratio is satisfied, for example, the water content is 24%.
It will be judged that it is safe to store 10 tons of harvested rice for 3 days.

【0004】次に、本発明の基本的な技術的考え方につ
いて説明する。穀物の乾燥効率ηは単位総消費電力WH当
たりの穀物からの脱水量Gkg でありこれを式で表すと次
の通りである。
Next, the basic technical idea of the present invention will be described. The grain drying efficiency η is the dehydration amount Gkg from the grain per unit total power consumption WH, which is expressed as follows.

【0005】 乾燥効率η=脱水量Gkg /総消費電力WH ‥‥‥‥‥‥‥‥‥‥‥‥(1式) ここで、穀物の乾燥に直接消費される電力は乾燥用空気
を送る送風機と乾燥用空気の湿度を調整する除湿器のコ
ンプレッサの動力であり、(1式)における総消費電力
WH=送風機の消費電力WH1 +除湿機の消費電力WH2 ‥‥
‥‥‥(2式)として表すことができる。また(1式)
における脱水量Gkg を式で表すと次の通りである。脱水
量Gkg =(排気の絶対湿度Mx−送風空気の絶対湿度My)
×送風量V×送風空気の比重γ‥‥‥‥(3式)
Drying efficiency η = dehydration amount Gkg / total power consumption WH ‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥ And the power of the compressor of the dehumidifier that adjusts the humidity of the drying air, and the total power consumption in (1 set)
WH = Blower power consumption WH1 + Dehumidifier power consumption WH2
It can be expressed as (2 types). Also (1 set)
The amount of dehydration Gkg in is expressed as follows. Dehydration Gkg = (Absolute humidity of exhaust Mx-Absolute humidity of blown air My)
× Ventilation amount V × Specific gravity of blown air γ ... (3 formulas)

【0006】そこで、乾燥効率ηを向上させるためには
総消費電力WHを少なくし、かつ、脱水量Gkg を多くする
ことが条件となる。穀物の乾燥方法において総消費電力
WHを少なくする手段としては送風量を少なくして送風機
の消費電力WH1 を少なくすることがあげられ、また、除
湿機のコンプレッサを停止して除湿器の消費電力WH2を
少なくすることがあげられる。
Therefore, in order to improve the drying efficiency η, it is necessary to reduce the total power consumption WH and increase the dehydration amount Gkg. Total power consumption in grain drying method
One way to reduce WH is to reduce the air flow to reduce the power consumption WH1 of the blower, and to stop the compressor of the dehumidifier to reduce power consumption WH2 of the dehumidifier.

【0007】次に、脱水量Gkg を多くする条件として上
記3式により、(排気の絶対湿度Mx−送風空気の絶対湿
度My)の値を大きくするか、送風量Vを多くするかのい
ずれかであるが、(排気の絶対湿度Mx−送風空気の絶対
湿度My)の値を大きくする条件は送風される空気中の水
分をできるかぎり除湿器によって除去して送風空気の絶
対湿度Myを低くすることにより達成されるので、上記除
湿器の消費電力WH2 を少なくすることと相反するものが
あり、また、送風量Vを多くすることも上記送風機の消
費電力WH1 を少なくすることとの間で相反するものがあ
る。したがって、乾燥効率ηを最大にするためには互い
に相反する関係にある脱水量Gkg と総消費電力WHをいか
に調整するかが要点になる。
Next, as a condition for increasing the dehydration amount Gkg, either the value of (absolute humidity Mx of exhaust gas−absolute humidity My of blown air My) is increased or the blown air amount V is increased by the above-mentioned three equations. However, the condition for increasing the value of (Absolute humidity of exhaust air Mx-Absolute humidity of blown air My) is to reduce the absolute humidity My of blown air by removing moisture in the blown air with a dehumidifier as much as possible. Therefore, there is a conflict with reducing the power consumption WH2 of the dehumidifier, and increasing the air flow rate V is also a conflict with reducing the power consumption WH1 of the blower. There is something to do. Therefore, in order to maximize the drying efficiency η, how to adjust the dehydration amount Gkg and the total power consumption WH, which are contradictory to each other, is a key point.

【0008】穀物の乾燥方法として当然に穀物の品質、
すなわち、安全限界風量比を考えなければならない。穀
物の品質に関する本発明の基本的な考えとして、穀物の
水分が非常に高い場合には穀物の品質を優先するように
する。すなわち、安全限界風量比を満足して穀物の品質
を維持するのに必要な風量を送風できる送風機を計画時
点で選定しておき、この送風機を定格運転することによ
り穀物の品質を維持し、一方において排気をリサイクル
するかどうかで乾燥効率を高めるようにする。
As a method of drying grains, naturally, quality of grains,
That is, the safety limit air volume ratio must be considered. The basic idea of the present invention regarding grain quality is to give priority to grain quality when the moisture content of the grain is very high. That is, at the time of planning, a blower that can blow the amount of air required to maintain the quality of the grain while satisfying the safety margin air volume ratio is selected, and the quality of the grain is maintained by operating this blower at the rated level. In order to improve the drying efficiency, whether the exhaust gas is recycled or not.

【0009】さて、除湿乾燥方式においては被乾燥物を
能率良く乾燥させるために乾燥用空気をリサイクルして
除湿乾燥器により送風空気の湿度を次第に下げながら乾
燥することが一般に行われている。しかしながら、被乾
燥物の種類によってはリサイクルによる乾燥のさせ方が
異なる。例えば、薬草のように水分が多く、かつ、薬草
の水分を十分に除去して粉末状にするような場合におい
て、水分の高い段階では排気される空気中に大量の水分
が含まれているのでその排気をそのまま排出し、水分が
ある一定量になった段階でその排気を再び除湿乾燥器に
導いて排気中の水分を除去しながら薬草の水分が十分に
除去されるまで排気のリサイクルを継続的に行うように
している。
In the dehumidifying / drying method, it is generally practiced to recycle the drying air and dry the dehumidifying dryer while gradually lowering the humidity of the blown air in order to efficiently dry the material to be dried. However, the method of drying by recycling differs depending on the type of the material to be dried. For example, when there is a lot of water like medicinal herbs and when the water of medicinal herbs is sufficiently removed to form a powder, a large amount of water is contained in the exhausted air when the water content is high. The exhaust gas is discharged as it is, and when the water content reaches a certain level, the exhaust gas is guided to the dehumidifying dryer again to remove the water content in the exhaust gas and continue to recycle the exhaust gas until the water content of the herbs is sufficiently removed. I try to do it.

【0010】また、特公昭59ー25134号公報に開示されて
いるように材木を乾燥させる場合には材木の乾燥特性、
すなわち材木の表面のみが乾燥してしまうと材木の芯部
にある水分が閉じ込められてしまい、乾燥時間が長くな
るので、材木の表面が過乾燥にならないように排気をリ
サイクルしたり排気をそのまま排出したりして温度と湿
度を調整しながら材木の芯部の水分を効率良く除去し材
木の乾燥を行うようにしている。
Further, when the timber is dried as disclosed in Japanese Patent Publication No. 59-25134, the drying characteristics of the timber,
That is, if only the surface of the timber is dried, the moisture in the core of the timber will be trapped and the drying time will be long, so you can recycle the exhaust or discharge the exhaust as it is so that the surface of the timber does not become overdried. By adjusting the temperature and humidity, the moisture in the core of the timber is efficiently removed and the timber is dried.

【0011】具体的には四つの段階に分けて木材の乾燥
を行うようにしている。図3を用いて説明すると、先ず
木材が製材されたばかりの水分が多い第一段階において
はダンパ2の開度調整をして一部の空気を補助凝縮器3
を通して放出する状態、ダンパ5を開いて外気を取り入
れる状態、脱湿蒸発器4凝縮器6をOFF の状態にし、乾
燥室1内で木材の水分を吸収し大量の水分を含んだ乾燥
用空気の一部を補助蒸発器3を通して外気に放出し、残
余の空気を脱湿蒸発器4で含有水分を蒸発させることな
く大量の水分を含んだ状態でダンパ5を通して吸引され
る外気と混合して絶対湿度を調節した後にOFF の状態に
ある凝縮器6を通過して送風機7により乾燥室1に再循
環する。この第一の段階は乾燥室1内の空気の絶対湿度
が外気の絶対湿度に略等しくなるまで継続される。これ
により、木材の表面が過乾燥にならないように乾燥が促
進される。次に、第二段階から第四段階ではダンパ2お
よび5を閉じた状態、脱湿蒸発器6および凝縮器4をON
の状態にし乾燥用空気を閉回路の状態で循環させ、この
循環している乾燥用空気中の水分を脱湿蒸発器6および
凝縮器4で次第に除去しながら木材の表面の過乾燥を抑
制しつつ木材の芯まで均一に乾燥するようにしている。
Specifically, the wood is dried in four stages. Explaining with reference to FIG. 3, first, in the first stage where the lumber has just been lumbered and the water content is high, the opening degree of the damper 2 is adjusted and a part of the air is supplied to the auxiliary condenser 3
To release outside air, open the damper 5 to take in the outside air, turn off the dehumidifying evaporator 4 condenser 6 and absorb the water content of the wood in the drying chamber 1 to remove the drying air containing a large amount of water. A part of the air is discharged to the outside air through the auxiliary evaporator 3, and the remaining air is mixed with the outside air sucked through the damper 5 in a state where a large amount of water is contained in the dehumidification evaporator 4 without evaporating the contained water. After adjusting the humidity, it passes through the condenser 6 in the OFF state and is recirculated to the drying chamber 1 by the blower 7. This first stage is continued until the absolute humidity of the air in the drying chamber 1 becomes substantially equal to the absolute humidity of the outside air. This promotes drying so that the surface of the wood does not become overdried. Next, in the second to fourth stages, the dampers 2 and 5 are closed, and the dehumidifying evaporator 6 and the condenser 4 are turned on.
In this state, the drying air is circulated in a closed circuit state, and moisture in the circulating drying air is gradually removed by the dehumidifying evaporator 6 and the condenser 4 to suppress overdrying of the surface of the wood. At the same time, the core of the wood is dried evenly.

【0012】また、図4(特開平3ー87589 号)に示す従
来の穀物の乾燥方法は設定湿度が外気の湿度よりも高い
ときにはダンパ9を閉じて外気の吸引を停止すると共に
ダンパ10を閉じ、閉回路の状態で乾燥用空気を循環させ
て次第に乾燥用空気の湿度を下げながら送風機7により
循環させ、貯留槽1内の穀物の過乾燥を防止しつつ穀物
を乾燥するようにしている。そして、設定湿度が外気の
湿度よりも低いときはダンパ9およびダンパ10を開いた
状態にし、ダンパ9から外気を吸引して除湿器8で除湿
し貯留槽1内の穀物を乾燥した後にダンパ10から大気中
に排気するようにして穀物の過乾燥を防止しながら乾燥
するようにしている。また、外気の湿度が非常に高く、
あるいは設定湿度に近いときにはダンパ9および10を半
開にして一部の空気を大気中に放出し残余の空気を循環
するようにして穀物の過乾燥を防止しながら乾燥するよ
うにしている。
In the conventional grain drying method shown in FIG. 4 (JP-A-3-87589), when the set humidity is higher than the humidity of the outside air, the damper 9 is closed to stop sucking the outside air and the damper 10 is closed. The drying air is circulated in a closed circuit state, and the humidity of the drying air is gradually lowered to be circulated by the blower 7 so that the grains in the storage tank 1 are prevented from being overdried and the grains are dried. When the set humidity is lower than the humidity of the outside air, the damper 9 and the damper 10 are opened, the outside air is sucked from the damper 9, the dehumidifier 8 dehumidifies, and the grain in the storage tank 1 is dried. The air is exhausted from the ground to prevent the grain from overdrying while drying. Also, the humidity of the outside air is very high,
Alternatively, when the humidity is close to the set humidity, the dampers 9 and 10 are opened halfway to release a part of the air into the atmosphere and circulate the remaining air so as to prevent the grain from overdrying and dry it.

【0013】[0013]

【発明が解決しょうとする課題】上記従来のリサイクル
方式の乾燥はいずれも乾燥効率の点で問題がある。先
ず、薬草の乾燥にあっては薬草の含有水分の高い段階で
は排気される空気中に大量の水分が含まれているのでそ
の排気をそのまま排出し、水分がある一定量になった段
階でその排気を再び除湿乾燥器に導いて排気中の水分を
除去しながら薬草の水分が十分に除去されるまで排気の
リサイクルを継続的に行うので、外気の条件が良いとき
でもその外気を利用することなく排気をリサイクルして
薬草の乾燥が完了するまで除湿器が継続的に運転され、
かつ、これに伴い送風機も連続的に定格運転されること
になり、本発明が対象にしている穀物の乾燥の観点から
見た場合に総消費電力が多く消費されて乾燥効率が低い
という問題がある。
The above-mentioned conventional recycling-type drying has problems in terms of drying efficiency. First of all, when drying the herbs, when the water content of the herbs is high, the exhaust air contains a large amount of water, so the exhaust air is discharged as it is, and when the water reaches a certain amount, Since the exhaust gas is guided to the dehumidifying dryer again to remove the water content in the exhaust gas, the exhaust gas is continuously recycled until the water content of the herbs is sufficiently removed. The dehumidifier is operated continuously until the medicinal herbs are completely dried by recycling the exhaust gas,
And, as a result, the blower is also continuously operated in rated operation, and when viewed from the viewpoint of drying the grain that is the subject of the present invention, a large amount of total power consumption is consumed and the drying efficiency is low. is there.

【0014】次に、図3に示した従来例は木材が製材さ
れたばかりの水分が多い第一段階においては乾燥室1内
で木材の水分を吸収し大量の水分を含んだ乾燥用空気の
一部を補助蒸発器3を通して外気に放出し、残余の空気
を脱湿蒸発器4で含有水分を蒸発させることなく大量の
水分を含んだ状態でダンパ5を通して吸引される外気と
混合して絶対湿度を調節した後にOFF の状態にある凝縮
器6を通過して送風機7により乾燥室1に再循環するの
で、送風湿度が高くなり結果として脱水量が少なくなり
穀物の乾燥の観点から見た場合に乾燥効率が低いという
問題がある。また、第二段階から第四段階では乾燥用空
気を閉回路の状態で循環させ、この循環している乾燥用
空気中の水分を脱湿蒸発器6および凝縮器4で次第に除
去しながら乾燥するので、穀物の乾燥の観点から見た場
合に、上記薬草の乾燥の場合と同様に外気の条件が良い
ときでもその外気を利用することなく排気をリサイクル
することから脱湿蒸発器6および凝縮器4と送風機7が
連続的に定格運転されて総消費電力が多くなり乾燥効率
が低いという問題がある。
Next, in the conventional example shown in FIG. 3, in the first stage in which the wood has just been lumbered and has a large amount of water, in the first stage, one of the drying air which absorbs the water of the wood in the drying chamber 1 and contains a large amount of water. Part of the air is discharged to the outside air through the auxiliary evaporator 3, and the remaining air is mixed with the outside air sucked through the damper 5 in a state where a large amount of water is contained in the dehumidification evaporator 4 without evaporating the contained water, thereby obtaining an absolute humidity. After adjusting the air conditioner, the air passes through the condenser 6 in the OFF state and is recirculated to the drying chamber 1 by the blower 7, so that the blast humidity becomes high, and as a result, the dehydration amount decreases, and when viewed from the viewpoint of grain drying. There is a problem that the drying efficiency is low. Further, in the second to fourth steps, the drying air is circulated in a closed circuit state, and the moisture in the circulating drying air is gradually removed by the dehumidifying evaporator 6 and the condenser 4 for drying. Therefore, from the viewpoint of drying grains, as in the case of drying the above-mentioned herbs, even when the conditions of the outside air are good, the exhaust gas is recycled without utilizing the outside air. 4 and the blower 7 are continuously in rated operation, resulting in a large total power consumption and a low drying efficiency.

【0015】また、穀物の乾燥である図4に示した従来
例は過乾燥防止を主目的としている関係上、設定湿度が
外気の湿度よりも高いとき(外気の条件がよいとき)は
湿度の高い空気を閉回路の状態で循環させて次第に乾燥
用空気の湿度を除湿器により下げながら送風機7により
循環させているので、脱水量が少ないと共に、除湿器お
よび送風機を連続定格運転しなければならないことから
総消費電力が多くなって乾燥効率が低いという問題があ
る。
Further, the conventional example shown in FIG. 4 for drying grains has a main purpose of preventing overdrying. Therefore, when the set humidity is higher than the humidity of the outside air (when the conditions of the outside air are good), the humidity Since high air is circulated in a closed circuit state and the humidity of the drying air is gradually lowered by the dehumidifier, the air is circulated by the blower 7, so that the dehydration amount is small and the dehumidifier and the blower must be continuously rated. Therefore, there is a problem that total power consumption increases and drying efficiency is low.

【0016】そして、上記従来例はいずれも送風量の制
御についての記載はなく、乾燥効率に関係する送風機の
消費電力を最小限にして乾燥効率を向上するという技術
の開示がない。
Further, none of the above-mentioned conventional examples describes the control of the air flow rate, and does not disclose the technique of improving the drying efficiency by minimizing the power consumption of the blower related to the drying efficiency.

【0017】本発明は上記問題に鑑みてなされたもので
あり、脱水量、総消費電力および穀物の品質を総合的に
みて乾燥効率を向上するようにした穀物の乾燥方法を提
供するものである。
The present invention has been made in view of the above-mentioned problems, and provides a method for drying a grain in which the drying efficiency is improved by comprehensively examining the dehydration amount, the total power consumption, and the quality of the grain. .

【0018】[0018]

【課題を解決するための手段】上記課題を解決するため
の本発明に係る手段は、除湿器を通過した乾燥用空気を
送風機により穀物を貯留している貯留槽に導いて穀物を
乾燥する穀物の乾燥方法において、前記貯留槽から排出
される排気の相対湿度および温度と穀物の平衡水分から
前記貯留槽内に貯留されている穀物の水分を判断し、該
判断された水分に対応して前記貯留槽内に供給される送
風量を制御することを特徴とするものである。
Means for Solving the Problems According to the present invention for solving the above-mentioned problems, the grain for drying the grain by introducing the drying air which has passed through the dehumidifier to a storage tank storing the grain by a blower. In the drying method, the moisture content of the grain stored in the storage tank is determined from the relative humidity and temperature of the exhaust gas discharged from the storage tank and the equilibrium moisture content of the grain, and the moisture content of the grain stored in the storage tank is determined according to the determined moisture content. It is characterized in that the amount of air blown into the storage tank is controlled.

【0019】[0019]

【作用】本発明はこのように構成したので、次の通りの
作用がある。すなわち、除湿器を通過した乾燥用空気を
送風機により穀物を貯留している貯留槽に導いて穀物を
乾燥するようにした該貯留槽から排出される排気の相対
湿度および温度と穀物の平衡水分から前記貯留槽内に貯
留されている穀物の水分を判断し、該判断された水分に
対応して前記貯留槽内に供給される送風量を制御するよ
うにしたので、この水分が低いと判断された場合には小
風量にして送風機の消費電力を低減し、水分が高いと判
断された場合には大風量にして脱水量を多くし、乾燥効
率を高くすることが可能になり、また、安全限界風量比
を満たすようにこの水分の判断基準と風量を設定するこ
とにより穀物の品質を維持することが可能になり、そし
て、排気条件により穀物の水分を判断することにより、
この排気条件と外気条件とを比較して排気をリサイクル
するかどうかの判断ができるようになり、送風空気の湿
度を低くし温度を高くして乾燥効率を高くすることが可
能になる。
Since the present invention is constructed in this way, it has the following actions. That is, the drying air that has passed through the dehumidifier is guided by a blower to a storage tank that stores grains to dry the grains, and the relative humidity and temperature of the exhaust gas discharged from the storage tank and the equilibrium moisture content of the grains are used. The water content of the grain stored in the storage tank is determined, and the amount of air blown into the storage tank is controlled according to the determined water content. If it is determined that the water content is high, it is possible to increase the amount of dewatering by increasing the air volume to increase the drying efficiency. It becomes possible to maintain the quality of the grain by setting the moisture judgment standard and the air volume so as to satisfy the limit air volume ratio, and by judging the moisture content of the grain by the exhaust condition,
By comparing the exhaust condition and the outside air condition, it becomes possible to judge whether or not to recycle the exhaust, and it is possible to lower the humidity of the blown air and raise the temperature to improve the drying efficiency.

【0020】[0020]

【実施例】以下本発明の一実施例について説明する。図
1において、検出器11により外気の相対湿度mx と温度
tx を検出し除湿器運転判断部12に入力し除湿器13を運
転するかどうかを判断する。この判断において図2に示
す穀物の平衡水分に関する相対湿度と温度との関係か
ら、例えば外気温度が5℃で外気相対湿度が55%から外
気温度が40℃で外気相対湿度が69%の(A)の範囲の外
気条件であれば、穀物の平衡水分との関係からこの条件
の外気により水分14%以下まで穀物を乾燥することがで
きるので除湿器13で外気の湿度を低くしなくても十分に
穀物を乾燥することができることになり、上記外気条件
の時に除湿器13を停止すると判断される。これにより除
湿器13の消費電力WH1 がゼロになり、かつ、外気取り入
れダンパ14を開いて外気を取り入れ、排気ダンパ15を開
いて排気し大風量の外気により乾燥することにより脱水
量Gを多くし、乾燥効率を向上することが可能になると
共に、上記外気条件で大風量を送風するので安全限界風
量比が満たされ、いかなる穀物の水分でも穀物の品質を
維持することが可能になる。
EXAMPLE An example of the present invention will be described below. In FIG. 1, the detector 11 detects the relative humidity mx and the temperature tx of the outside air and inputs it to the dehumidifier operation determination unit 12 to determine whether to operate the dehumidifier 13. In this judgment, from the relationship between the relative humidity and the temperature regarding the equilibrium moisture of the grain shown in FIG. 2, for example, when the outside air temperature is 5 ° C. and the outside air relative humidity is 55%, the outside air temperature is 40 ° C. and the outside air relative humidity is 69% (A If the outside air condition is within the range of), it is possible to dry the grain to a moisture content of 14% or less by the outside air in this condition due to the relationship with the equilibrium moisture content of the grain, so it is sufficient to reduce the humidity of the outside air with the dehumidifier 13. Therefore, the grain can be dried, and it is determined that the dehumidifier 13 is stopped under the above-mentioned outside air condition. As a result, the power consumption WH1 of the dehumidifier 13 becomes zero, and the outside air intake damper 14 is opened to take in the outside air, the exhaust damper 15 is opened and exhausted, and the amount of dehydration G is increased by drying with a large amount of outside air. The drying efficiency can be improved, and since a large air volume is blown under the above-mentioned outside air conditions, the safety limit air volume ratio is satisfied, and it becomes possible to maintain the grain quality regardless of the moisture content of any grain.

【0021】一方検出器11で検出された外気の相対湿度
mx と温度tx が図2の(B)および(C)の範囲であ
る場合には除湿器13を運転すると判断され、このとき穀
物安全性判断部16で穀物が安全であるかどうかが判断さ
れる。この穀物の安全性の判断は検出器17により排気の
相対湿度Mxと温度Txを検出してこの信号を穀物安全性判
断部16に入力することにより図2の平衡水分の関係から
逆に貯留槽1内の穀物の水分を知ることができる。例え
ば排気湿度Mxが80%、排気温度Txが20℃の場合には図2
の水分18%のライン上になり、貯留槽1内の穀物の水分
は18%であると判断される。
On the other hand, when the relative humidity mx and the temperature tx of the outside air detected by the detector 11 are in the ranges of (B) and (C) of FIG. 2, it is judged that the dehumidifier 13 is operated, and at this time, the grain safety. The sex determination unit 16 determines whether or not the grain is safe. The grain safety is judged by detecting the relative humidity Mx and temperature Tx of the exhaust gas by the detector 17 and inputting these signals to the grain safety judging section 16 from the equilibrium moisture relationship shown in FIG. You can know the water content of the grain in 1. For example, if the exhaust humidity Mx is 80% and the exhaust temperature Tx is 20 ° C,
The water content of the grain in the storage tank 1 is determined to be 18%.

【0022】そして、排気条件が図2の(B)の範囲に
あるとき、すなわち、排気温度5℃で排気相対湿度55%
ないし75%から排気温度40℃で排気相対湿度69%ないし
87%のとき貯留槽1内の穀物の水分は14%から18%の範
囲にあって小風量でも安全であると判断され、この判断
信号がリサイクル・風量判断部18に入力される。リサイ
クル・風量判断部18において、検出器11から入力される
外気相対湿度mx と温度tx および検出器17から入力さ
れる排気の相対湿度Mxと温度Txにより外気相対湿度mx
と排気の相対湿度Mxおよび外気温度tx と排気温度Txを
比較し、外気相対湿度mx が排気の相対湿度Mxに等しい
か高い時、およびまたは外気温度tx が排気温度Txに等
しいか低い時に送風機制御部20の小風量に出力されて送
風機7が制御され、小風量でかつ外気取り入れダンパ14
および排気ダンパ15を閉めて排気をリサイクル(以下こ
の条件をリサイクル小風量条件という)する。
When the exhaust conditions are within the range of FIG. 2B, that is, the exhaust temperature is 5 ° C., the exhaust relative humidity is 55%.
From 75% to exhaust temperature 40 ° C and exhaust relative humidity 69% to
When it is 87%, the water content of the grain in the storage tank 1 is in the range of 14% to 18%, and it is judged that it is safe even with a small air volume, and this judgment signal is input to the recycling / air volume judgment section 18. In the recycle / air flow rate determining unit 18, the outside air relative humidity mx and the temperature tx input from the detector 11 and the exhaust air relative humidity Mx and the temperature Tx input from the detector 17 are used to determine the outside air relative humidity mx.
And the relative humidity Mx of the exhaust gas and the outside air temperature tx are compared with the exhaust temperature Tx, and the blower control is performed when the outside air relative humidity mx is equal to or higher than the relative humidity Mx of the exhaust gas, and / or the outside air temperature tx is equal to or lower than the exhaust temperature Tx. The blower 7 is controlled by being output to the small air volume of the part 20, and the air intake damper 14 with a small air volume is provided.
Also, the exhaust damper 15 is closed to recycle the exhaust gas (hereinafter, this condition is referred to as a recycle small air flow condition).

【0023】このように、除湿器13が運転され穀物が安
全であると判断され、かつ、穀物の乾燥に対して排気の
方が条件がよいと判断されているので、小風量でも安全
限界風量比が満足されて穀物の品質が保証され、かつ、
風量を少なくして送風機7の消費電力WH1 を少なくし、
更に外気よりも相対湿度Mxが低く、およびまたは温度Tx
が高い排気をリサイクルして除湿器13で除湿することに
より、送風される空気の相対湿度myを更に低くして脱水
量Gを多くし乾燥効率を向上することが可能になる。
As described above, since the dehumidifier 13 is operated and it is determined that the grain is safe, and the exhaust condition is better for drying the grain, the safety limit air flow amount is small even if the air flow amount is small. The ratio is satisfied and the quality of the grain is guaranteed, and
The air volume is reduced to reduce the power consumption WH1 of the blower 7,
Furthermore, the relative humidity Mx is lower than the outside air, and / or the temperature Tx.
By recycling high exhaust gas and dehumidifying it with the dehumidifier 13, it is possible to further lower the relative humidity my of the air to be blown, increase the dehydration amount G, and improve the drying efficiency.

【0024】また、リサイクル・風量判断部18で外気相
対湿度mx が排気の相対湿度Mxよりも低い時、およびま
たは外気温度tx が排気温度Txよりも高い時に送風機制
御部20の大風量部に入力されて送風機7が制御され、大
風量でかつ外気取り入れダンパ14および排気ダンパ15を
開けて排気を排出(以下この条件を非リサイクル大風量
条件という)する。
In addition, when the outside air relative humidity mx is lower than the exhaust relative humidity Mx in the recycle / air flow rate determination unit 18 and / or when the outside air temperature tx is higher than the exhaust temperature Tx, it is input to the large air volume unit of the blower control unit 20. Then, the blower 7 is controlled to open the outside air intake damper 14 and the exhaust damper 15 with a large air volume to discharge the exhaust gas (hereinafter, this condition is referred to as a non-recycled large air volume condition).

【0025】すなわち、上記非リサイクル大風量条件に
なるということは穀物から十分に脱水されて、穀物の水
分の蒸発熱により空気の熱が奪われて排気温度Txが低下
しその水分を吸収して排気相対湿度Mxが上昇することを
意味しているので、条件のよい外気を取り入れて水分が
多くなっている排気を排出し、かつ、大風量にして脱水
量Gを多くすることにより乾燥効率を向上することが可
能になる。
That is, the above non-recycled large air volume condition means that the grain is sufficiently dehydrated, the heat of the air is taken away by the heat of evaporation of the moisture of the grain, the exhaust temperature Tx is lowered, and the moisture is absorbed. Since it means that the exhaust gas relative humidity Mx rises, the drying efficiency can be improved by taking in the air in good condition to discharge the exhaust gas with a large amount of water, and by increasing the air volume to increase the dehydration amount G. It will be possible to improve.

【0026】次に、穀物安全性判断部16で安全でないと
判断された場合にはその判断信号はリサイクル非リサイ
クル判断部19に入力されると共に、穀物の安全性を優先
して送風機制御部20の大風量部に入力されて送風機7が
制御される。すなわち、図2において排気温度Txが5℃
で排気相対湿度Mxが75%以上から排気温度Txが40℃で排
気相対湿度Mxが87%以上の(C)の範囲の時に穀物は安
全でない(高水分である)と判断され、この時には貯留
槽1に大風量を送風し安全限界風量比を満たして穀物の
安全を第一に図り、かつ、外気よりも相対湿度Mxが低
く、およびまたは温度Txが高い排気をリサイクルして除
湿器13で除湿することにより、送風される空気の相対湿
度myを更に低くして脱水量Gを多くし乾燥効率を向上
し、また、外気相対湿度mx が排気の相対湿度Mxよりも
低い時、およびまたは外気温度tx が排気温度Txよりも
高い時に大風量でかつ外気取り入れダンパ14および排気
ダンパ15を開けて排気を排出し、大風量にして脱水量G
を多くすることにより乾燥効率を向上することが可能に
なる。
Next, when the grain safety determination unit 16 determines that it is not safe, the determination signal is input to the recycle / non-recycle determination unit 19 and the blower control unit 20 gives priority to the safety of the grain. The air blower 7 is controlled by being input to the large air volume part. That is, in FIG. 2, the exhaust temperature Tx is 5 ° C.
When the exhaust relative humidity Mx is 75% or more and the exhaust temperature Tx is 40 ° C and the exhaust relative humidity Mx is 87% or more (C), it is judged that the grains are not safe (high moisture content) and stored at this time. A large amount of air is blown into the tank 1 to meet the safety limit air volume ratio, and the safety of the grain is given first, and the dehumidifier 13 recycles the exhaust having the relative humidity Mx lower than the outside air and / or the temperature Tx higher than the outside air. By dehumidifying, the relative humidity my of the blown air is further lowered to increase the dehydration amount G to improve the drying efficiency, and when the outside air relative humidity mx is lower than the exhaust relative humidity Mx, and / or outside air When the temperature tx is higher than the exhaust temperature Tx, the air volume is large, and the outside air intake damper 14 and the exhaust damper 15 are opened to exhaust the exhaust gas to a large air volume and dehydration amount G
By increasing the amount, it becomes possible to improve the drying efficiency.

【0027】このようにして、排気条件を検出器17で検
出し貯留槽1内の穀物の水分を判断することにより、こ
の排気条件を利用して外気条件と比較し排気をリサイク
ルするかどうかを判断すると共に送風量を判断して、脱
水量、総消費電力および穀物の品質を総合的にみて乾燥
効率を向上させることが可能になる。
In this way, the exhaust condition is detected by the detector 17 and the moisture content of the grain in the storage tank 1 is determined. By using this exhaust condition, it is compared with the outside air condition to determine whether the exhaust gas is recycled. It becomes possible to improve the drying efficiency by judging the air flow rate together with the judgment, and comprehensively considering the dehydration amount, the total power consumption and the grain quality.

【0028】上記説明において除湿器運転判断部12およ
び穀物安全性判断部16での判断設定基準として穀物の平
衡水分と湿度および温度との関係を図2に示したが、範
囲(A)、(B)、(C)はこれに限定されるものでは
なくこの範囲の設定は任意に行うことができる。
In the above description, the relationship between the equilibrium moisture content of the grain, the humidity and the temperature is shown in FIG. 2 as a criterion for the determination of the dehumidifier operation determination unit 12 and the grain safety determination unit 16, but the ranges (A), ( B) and (C) are not limited to this, and this range can be set arbitrarily.

【0029】[0029]

【発明の効果】以上詳述した通り本発明によれば、留槽
から排出される排気の相対湿度および温度と穀物の平衡
水分から前記貯留槽内に貯留されている穀物の水分を判
断し、このように判断された水分に対応して前記貯留槽
内に供給される送風量を制御するようにしたので、この
水分が低いと判断された場合には小風量にして送風機の
消費電力を低減し、水分が高いと判断された場合には大
風量にして脱水量を多くし、乾燥効率を高くすることが
でき、また、安全限界風量比を満たすようにこの水分の
判断基準と風量を設定することにより穀物の品質を維持
することができ、そして、排気条件により穀物の水分を
判断することにより、その排気条件と外気条件を比較し
て排気をリサイクルするかどうかの判断ができるように
なり、送風空気の湿度を低くし温度を高くして乾燥効率
を高くすることができる。
As described in detail above, according to the present invention, the moisture content of grains stored in the storage tank is determined from the relative humidity and temperature of the exhaust gas discharged from the distilling tank and the equilibrium moisture content of the grain, Since the amount of air blown into the storage tank is controlled in accordance with the water content thus determined, if the water content is determined to be low, the air flow rate is reduced to reduce the power consumption of the blower. However, if it is determined that the water content is high, a large air volume can be used to increase the dehydration amount to increase the drying efficiency, and the water content judgment criteria and air volume can be set to meet the safety limit air volume ratio. By doing so, the quality of the grain can be maintained, and by judging the moisture content of the grain by the exhaust condition, it becomes possible to compare the exhaust condition with the outside air condition and judge whether to recycle the exhaust. Of the blast air It is possible to reduce the degree by raising the temperature to increase the drying efficiency.

【0030】また、外気条件により除湿器を運転するか
どうかを除湿器運転判断部で判断し除湿器を運転しない
と判断した時には大風量で外気を吸引して乾燥した後に
その排気を排出することにより、除湿器の消費電力をゼ
ロにして総消費電力を少なくし、かつ、大量の外気によ
り穀物を乾燥して脱水量が多くなり乾燥効率を向上する
ことが可能になると共に、大量の空気を送風して安全限
界風量比が確保されて穀物の品質を維持することができ
る。
When the dehumidifier operation determination unit determines whether or not to operate the dehumidifier according to the outside air conditions, and when it is determined that the dehumidifier is not operated, the outside air is sucked in with a large air volume and dried, and then the exhaust gas is discharged. This makes it possible to reduce the power consumption of the dehumidifier to zero and reduce the total power consumption, and to dry the grain with a large amount of outside air to increase the dehydration amount and improve the drying efficiency. By blowing air, the safety limit air volume ratio is secured and the grain quality can be maintained.

【0031】一方において、除湿器を運転すると判断し
た時には穀物安全性判断部で穀物が安全であるかどうか
を排気条件により判断し、安全であると判断した場合に
は外気の温度および相対湿度と排気の温度および相対湿
度とを比較して外気の相対湿度が排気の相対湿度よりも
高いか、およびまたは外気温度が排気温度よりも低い時
に小風量で排気をリサイクルすることにより、穀物の品
質が保証され、かつ、相対湿度が外気よりも低く外気温
度よりも高い排気をリサイクルして送風湿度を低下させ
ると共に送風温度を高めて脱水量を増加させ、更に小風
量にして送風機の消費電力を少なくし乾燥効率を向上す
ることができる。
On the other hand, when it is determined that the dehumidifier is to be operated, the grain safety determination unit determines whether or not the grain is safe based on the exhaust conditions. If it is determined that the grain is safe, the temperature and the relative humidity of the outside air are determined. By comparing the temperature and relative humidity of the exhaust with the relative humidity of the outside air is higher than the relative humidity of the exhaust and / or when the outside air temperature is lower than the exhaust temperature, recycling the exhaust with a small air volume will improve the quality of the grain. Guaranteed and with a relative humidity lower than the outside air and higher than the outside temperature, the exhaust gas is recycled to lower the blast humidity and increase the blast temperature to increase the dehydration amount, and further reduce the air flow to reduce the power consumption of the blower. The drying efficiency can be improved.

【0032】また一方において、外気の相対湿度が排気
の相対湿度よりも低いか、およびまたは外気温度が排気
温度よりも高い時に大風量で外気を吸引して乾燥した後
にその排気を排出することにより、穀物の品質が保証さ
れ、かつ、相対湿度が排気よりも低く排気温度よりも高
い外気を取り入れて送風湿度を低下させると共に送風温
度を高め、大量の外気により乾燥して排気することによ
り脱水量を多くし乾燥効率を向上することができる。
On the other hand, when the relative humidity of the outside air is lower than the relative humidity of the exhaust gas and / or the outside air temperature is higher than the exhaust gas temperature, the outside air is sucked and dried with a large air volume, and then the exhaust gas is discharged. , The quality of grain is guaranteed, and the relative humidity is lower than the exhaust gas and higher than the exhaust temperature to reduce the blast humidity by increasing the blast temperature and to increase the blast temperature. And the drying efficiency can be improved.

【0033】そして、穀物が安全でないと判断した場合
には大風量にし外気条件と排気条件を比較して排気をリ
サイクルするかしないかを判断することにより、安全限
界風量比を満たして穀物の品質を保証しつつ脱水量を多
くし、かつ、リサイクルするかどうかを判断して送風湿
度を低下し送風温度を高め、乾燥効率を向上することが
できる。これにより、脱水量、総消費電力および穀物の
品質を総合的にみて乾燥効率を向上するようにした穀物
の乾燥方法を得ることができる。
When it is determined that the grain is not safe, a large air volume is set and the outside air condition and the exhaust condition are compared to determine whether or not the exhaust gas is recycled. It is possible to increase the amount of dehydration while ensuring the above, and determine whether or not to recycle, to lower the blast humidity, raise the blast temperature, and improve the drying efficiency. As a result, it is possible to obtain a grain drying method in which the drying efficiency is improved by comprehensively considering the dehydration amount, the total power consumption, and the grain quality.

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

【図1】本発明の一実施例を示すブロック線図である。FIG. 1 is a block diagram showing an embodiment of the present invention.

【図2】穀物の平衡水分と外気および排気の温度と相対
湿度の関係を示す図である。
FIG. 2 is a diagram showing the relationship between the equilibrium moisture content of grains, the temperature of outside air and the temperature of exhaust gas, and the relative humidity.

【図3】従来例のフロー線図である。FIG. 3 is a flow diagram of a conventional example.

【図4】他の従来例のフロー線図である。FIG. 4 is a flow diagram of another conventional example.

【符合の説明】[Explanation of sign]

1 貯留槽 7 送風機 11 検出器 12 除湿器運転判断部 13 除湿器 14 外気取り入れダンパ 15 排気ダンパ 16 穀物安全性判断部 17 検出器 18 リサイクル・風量判断部 19 リサイクル・非リサイクル判断部 mx 外気相対湿度 tx 外気温度 Mx 排気相対湿度 Tx 排気温度 My 送風湿度 1 Storage tank 7 Blower 11 Detector 12 Dehumidifier operation determination unit 13 Dehumidifier 14 Outside air intake damper 15 Exhaust damper 16 Grain safety determination unit 17 Detector 18 Recycle / air volume determination unit 19 Recycle / non-recycle determination unit mx Ambient air relative humidity tx outside temperature Mx exhaust relative humidity Tx exhaust temperature My blast humidity

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 除湿器を通過した乾燥用空気を送風機に
より穀物を貯留している貯留槽に導いて穀物を乾燥する
穀物の乾燥方法において、前記貯留槽から排出される排
気の相対湿度および温度と穀物の平衡水分から前記貯留
槽内に貯留されている穀物の水分を判断し、該判断され
た水分に対応して前記貯留槽内に供給される送風量を制
御することを特徴とする穀物の乾燥方法。
1. A method for drying grains, in which drying air that has passed through a dehumidifier is introduced into a storage tank that stores the grains by a blower to dry the grains, in which relative humidity and temperature of exhaust gas discharged from the storage tanks. And the grain moisture stored in the storage tank from the equilibrium moisture content of the grain and controlling the amount of air blown into the storage tank in accordance with the determined moisture. How to dry.
【請求項2】 除湿器を通過した乾燥用空気を送風機に
より穀物を貯留している貯留槽に導いて穀物を乾燥する
穀物の乾燥方法において、外気の温度および相対湿度と
前記貯留槽から排出される排気の温度および相対湿度と
を比較して外気の相対湿度が排気の相対湿度よりも高い
か、およびまたは外気温度が排気温度よりも低い時に小
風量で排気をリサイクルし、外気の相対湿度が排気の相
対湿度よりも低いか、およびまたは外気温度が排気温度
よりも高い時に大風量で外気を吸引して乾燥した後にそ
の排気を排出することを特徴とする穀物の乾燥方法。
2. A method for drying a grain, in which drying air that has passed through a dehumidifier is introduced into a storage tank storing the grain by a blower to dry the grain, and the temperature and relative humidity of the outside air and the discharge from the storage tank are used. When the relative humidity of the outside air is higher than the relative humidity of the exhaust air and / or the outside air temperature is lower than the exhaust temperature, the exhaust gas is recycled with a small air volume to determine the relative humidity of the outside air. A method for drying cereals, characterized in that, when the temperature is lower than the relative humidity of exhaust gas and / or the external air temperature is higher than the exhaust gas temperature, the external air is sucked and dried with a large amount of air and then the exhaust gas is discharged.
【請求項3】 除湿器を通過した乾燥用空気を送風機に
より穀物を貯留している貯留槽に導いて穀物を乾燥する
穀物の乾燥方法において、前記貯留槽から排出される排
気の相対湿度と温度により貯留槽内の穀物の水分を判断
し、水分が多いと判断したときには大風量にし、かつ、
外気の温度および相対湿度と前記貯留槽から排出される
排気の温度および相対湿度とを比較して外気の相対湿度
が排気の相対湿度よりも高いか、およびまたは外気温度
が排気温度よりも低い時に排気をリサイクルし、外気の
相対湿度が排気の相対湿度よりも低いか、およびまたは
外気温度が排気温度よりも高い時に外気を吸引して乾燥
した後にその排気を排出することを特徴とする穀物の乾
燥方法。
3. A relative humidity and temperature of exhaust gas discharged from the storage tank in a method of drying a grain by introducing drying air that has passed through a dehumidifier to a storage tank storing the grain by a blower. Determine the water content of the grains in the storage tank by using the
When the temperature and relative humidity of the outside air and the temperature and relative humidity of the exhaust gas discharged from the storage tank are compared, and the relative humidity of the outside air is higher than the relative humidity of the exhaust gas, or when the outside air temperature is lower than the exhaust temperature. Of cereals, characterized by recycling the exhaust and sucking the outside air and drying it after the outside air has a relative humidity lower than the exhaust relative humidity and / or an outside temperature higher than the exhaust temperature. Drying method.
【請求項4】 除湿器を通過した乾燥用空気を送風機に
より穀物を貯留している貯留槽に導いて穀物を乾燥する
穀物の乾燥方法において、穀物安全性判断部で穀物が安
全であるかどうかを排気条件により判断し、安全である
と判断した場合には外気の温度および相対湿度と排気の
温度および相対湿度とを比較して外気の相対湿度が排気
の相対湿度よりも高いか、およびまたは外気温度が排気
温度よりも低い時に小風量で排気をリサイクルし、外気
の相対湿度が排気の相対湿度よりも低いか、およびまた
は外気温度が排気温度よりも高い時に大風量で外気を吸
引して乾燥した後にその排気を排出し、また、穀物が安
全でないと判断した場合には大風量にし外気条件と排気
条件を比較して排気をリサイクルするかしないかを判断
することを特徴とする穀物の乾燥方法。
4. A grain drying method in which drying air that has passed through a dehumidifier is introduced by a blower to a storage tank that stores grains to dry the grains, and whether or not the grains are safe in a grain safety determination unit. If it is judged to be safe by comparing the temperature and relative humidity of the outside air with the temperature and relative humidity of the exhaust air, the relative humidity of the outside air is higher than the relative humidity of the exhaust air, and or When the outside air temperature is lower than the exhaust temperature, the exhaust air is recycled with a small air flow, and when the outside air relative humidity is lower than the exhaust air relative temperature or the outside air temperature is higher than the exhaust temperature, the outside air is sucked in with a large air flow rate. It is characterized by discharging the exhaust after drying, and if it is judged that the grain is not safe, make a large air volume and compare the outside air condition with the exhaust condition to judge whether the exhaust gas is recycled or not. How to dry grain.
【請求項5】 除湿器を通過した乾燥用空気を送風機に
より穀物を貯留している貯留槽に導いて穀物を乾燥する
穀物の乾燥方法において、外気条件により前記除湿器を
運転するかどうかを除湿器運転判断部で判断し除湿器を
運転しないと判断した時には大風量で外気を吸引して乾
燥した後にその排気を排出し、除湿器を運転すると判断
した時には穀物安全性判断部で穀物が安全であるかどう
かを排気条件により判断し、安全であると判断した場合
には外気の温度および相対湿度と排気の温度および相対
湿度とを比較して外気の相対湿度が排気の相対湿度より
も高いか、およびまたは外気温度が排気温度よりも低い
時に小風量で排気をリサイクルし、外気の相対湿度が排
気の相対湿度よりも低いか、およびまたは外気温度が排
気温度よりも高い時に大風量で外気を吸引して乾燥した
後にその排気を排出し、また、穀物が安全でないと判断
した場合には大風量にし外気条件と排気条件を比較して
排気をリサイクルするかしないかを判断することを特徴
とする穀物の乾燥方法。
5. A method for drying a grain, in which drying air that has passed through a dehumidifier is introduced into a storage tank that stores the grain by a blower to dry the grain, and dehumidification is performed depending on the outside air condition. When the dehumidifier operation judgment unit judges that the dehumidifier is not operated, it sucks the outside air with a large air volume to dry it and discharges the exhaust air, and when it is judged that the dehumidifier is operated, the grain safety judgment unit judges that the grain is safe. If it is safe, the temperature and relative humidity of the outside air are compared with the temperature and relative humidity of the exhaust gas, and the relative humidity of the outside air is higher than the relative humidity of the exhaust gas. And / or when the outside air temperature is lower than the exhaust temperature, the exhaust air is recycled with a small air flow, and the relative humidity of the outside air is lower than the relative humidity of the exhaust, and / or the outside air temperature is higher than the exhaust temperature. In addition, after sucking the outside air with a large air volume and drying it, the exhaust air is discharged, and if it is judged that the grain is not safe, make a large air volume and compare the outside air condition with the exhaust condition to recycle the exhaust gas. A method for drying a grain, which comprises judging.
JP5310593A 1993-02-18 1993-02-18 Grain drying method Expired - Fee Related JP3271026B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5310593A JP3271026B2 (en) 1993-02-18 1993-02-18 Grain drying method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5310593A JP3271026B2 (en) 1993-02-18 1993-02-18 Grain drying method

Publications (2)

Publication Number Publication Date
JPH06237687A true JPH06237687A (en) 1994-08-30
JP3271026B2 JP3271026B2 (en) 2002-04-02

Family

ID=12933516

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5310593A Expired - Fee Related JP3271026B2 (en) 1993-02-18 1993-02-18 Grain drying method

Country Status (1)

Country Link
JP (1) JP3271026B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11391518B2 (en) 2012-11-22 2022-07-19 Alfa Laval Corhex Ltd. Method of operating a heat exchanger

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11391518B2 (en) 2012-11-22 2022-07-19 Alfa Laval Corhex Ltd. Method of operating a heat exchanger

Also Published As

Publication number Publication date
JP3271026B2 (en) 2002-04-02

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