JPH0364189B2 - - Google Patents
Info
- Publication number
- JPH0364189B2 JPH0364189B2 JP60254519A JP25451985A JPH0364189B2 JP H0364189 B2 JPH0364189 B2 JP H0364189B2 JP 60254519 A JP60254519 A JP 60254519A JP 25451985 A JP25451985 A JP 25451985A JP H0364189 B2 JPH0364189 B2 JP H0364189B2
- Authority
- JP
- Japan
- Prior art keywords
- drying
- grain
- amount
- moisture content
- dryer
- 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
Links
Landscapes
- Adjustment And Processing Of Grains (AREA)
Description
[産業上の利用分野]
本発明は、熱風供給のための燃焼量が最良の燃
焼効率となる一定の状態のもとで、予め希望する
乾燥時間で所定の水分まで効率よく乾燥すること
ができる穀物乾燥方法に関する。
[従来の技術]
従来、自動乾燥制御機能を備えら穀物乾燥機
は、例えば、特開昭55−150475号公報に記載され
ていて、広く知られており、かつ用いられてい
る。
[発明が解決しようとする問題点]
ところで、上記従来の穀物乾燥機においては、
穀物の水分や温度等の乾燥制御要素によつて乾燥
制御を行つているので、乾燥所要時間が作業者の
希望する乾燥時間と相容れない場合が多い。この
ため、次の予定時間に割込み、作業に差支えるこ
とがあり、特に、乾燥仕上がり予定時刻が深夜や
早朝にあたる場合は、作業上はなはだ不便であ
る。
また、上記従来の穀物乾燥機においては、乾燥
熱風の温度を制御するため、燃焼量を増減制御し
ているが、燃焼量を減じた状態では燃焼効率が低
下するので、乾燥機の乾燥能力を最大限に活用す
ることができない欠点があつた。
そこで、本発明は、このような従来の実状に鑑
み、乾燥作業の開始にあたり、予め希望する乾燥
時間で穀物を所定の水分まで乾燥仕上げることが
でき、しかも、熱風供給のための燃焼量の増減制
御を行うことなく燃焼量を最良の燃焼効率となる
一定の状態として、乾燥機の乾燥能力を常に最大
限に活用して、効率のよい乾燥を行うことができ
る穀物乾燥方法を提供することを目的とするもの
である。
[問題点を解決するための手段]
本発明は、その目的を達成するための技術的手
段として次のように構成した。
すなわち、本発明に係る穀物乾燥方法は、穀物
の初期水分とその乾燥仕上り水分から乾燥所要水
分を算出し、乾燥所要水分、選択した乾減率およ
び熱風供給のための燃焼量を最良の燃焼効率とな
る乾燥機の乾燥能力を一定に保ち、その一定の乾
燥能力から希望する乾燥時間で乾燥が仕上る穀物
量を算出して、これを乾燥機の一乾燥作業におけ
る穀物張込量とすることを特徴とするものであ
る。
[作用]
本発明に係る穀物乾燥方法によれば、乾燥所要
水分の多少にかかわらず、予め希望する乾燥時間
で穀物は所定の水分まで乾燥される。すなわち、
穀物の初期水分と乾燥仕上り水分から算出された
乾燥所要水分によつて、乾燥所要水分が多いとき
は乾燥機の一乾燥作業における穀物張込量が少な
く、乾燥所要水分が少ないときは穀物張込量が多
いので、乾燥所要水分の多少にかかわらず乾燥時
間を同じにすることができ、これによつて予め希
望する乾燥時間で穀物の乾燥を終了させることが
できる。
そして、本発明に係る穀物乾燥方法によれば、
熱風供給のための燃焼量を増減制御せず、それを
最良の燃焼効率となる一定とした乾燥機の乾燥能
力のもとで乾燥が行われるので、乾燥効率の向上
を図ることができる。
[実施例]
次に本発明に係る穀物乾燥方法の一実施例につ
いて説明する。
通常、収穫された穀物の初期水分M1は26〜20
%、穀物の仕上り水分は15%前後、1日の作業サ
イクルにおいて都合のよい乾燥時間は14〜16時間
である。また、許容される乾減率(乾燥速度
ΔMmaxは、胴割れを生じさせないために0.8
%/時である。
そこで、穀物の乾燥仕上り水分M2は15.5%、
希望する乾燥時間Hrを14時間(当日の午後6時
から翌日の午前8時)とし、熱風供給のための燃
焼量を最良の燃焼効率となる一定とした乾燥機の
乾燥能力ηが20石%/時であるとすれば、穀物張
込量W(石)は、
W=η×Hr/M1−M2
である。ここにM1−M2は穀物の乾燥所要水分で
ある。
なお、この条件で穀物張込量を最小値Mmは、
Wm=η/ΔMmax=20/0.8=25(石)
乾燥時Hrが14時間で乾燥できる穀物の初期水分
値M1maxは、
M1=ΔMmax×Hr×M2
=0.8×14+15.5
=26.7(%)
である。
次表に、穀物の初期水分M1の各値に対する穀
物張込量W1、乾減率(乾燥速度)ΔMを示す。
なお、穀物の初期水分M1が28%以上の場合、お
よび、18%以下の場合は、穀物張込量Wを変えず
に乾燥時間Hrを調節する。よつて、表中にはそ
の数値に( )を付して表示している。
[Industrial Application Field] The present invention is capable of efficiently drying to a predetermined moisture content in a pre-desired drying time under a certain condition in which the combustion amount for hot air supply is the best combustion efficiency. Concerning grain drying methods. [Prior Art] Conventionally, a grain dryer equipped with an automatic drying control function is described in, for example, Japanese Unexamined Patent Publication No. 150475/1983, and is widely known and used. [Problems to be solved by the invention] By the way, in the above conventional grain dryer,
Since drying is controlled by drying control elements such as grain moisture and temperature, the required drying time is often inconsistent with the drying time desired by the operator. This may interrupt the next scheduled time and interfere with the work, which is particularly inconvenient when the scheduled drying finish time falls late at night or early in the morning. In addition, in the conventional grain dryer mentioned above, the amount of combustion is controlled to increase or decrease in order to control the temperature of the drying hot air, but when the amount of combustion is reduced, the combustion efficiency decreases, so the drying capacity of the dryer is reduced. There were drawbacks that prevented it from being utilized to its full potential. In view of these conventional circumstances, the present invention has been developed to dry and finish grains to a predetermined moisture content in a pre-desired drying time at the start of drying work, and to increase or decrease the amount of combustion for supplying hot air. To provide a grain drying method that can perform efficient drying by always maximizing the drying capacity of a dryer by keeping the amount of combustion in a constant state with the best combustion efficiency without controlling it. This is the purpose. [Means for Solving the Problems] The present invention is configured as follows as a technical means for achieving the object. That is, the grain drying method according to the present invention calculates the required moisture content for drying from the initial moisture content of the grain and its finished drying moisture content, and calculates the required moisture content, selected drying loss rate, and combustion amount for supplying hot air to achieve the best combustion efficiency. Keep the drying capacity of the dryer constant, calculate the amount of grain that can be finished drying in the desired drying time from that constant drying capacity, and use this as the amount of grain loaded in one drying operation of the dryer. This is a characteristic feature. [Function] According to the grain drying method according to the present invention, grains are dried to a predetermined moisture content in a previously desired drying time, regardless of the amount of moisture required for drying. That is,
Depending on the moisture requirement for drying calculated from the initial moisture content and finished moisture content of the grain, when the moisture requirement for drying is high, the amount of grain loaded in one drying operation of the dryer is small, and when the moisture required for drying is low, the amount of grain loaded in one drying operation is small. Since the amount is large, the drying time can be made the same regardless of the amount of moisture required for drying, and thereby the drying of the grain can be completed within a pre-desired drying time. According to the grain drying method according to the present invention,
Since drying is performed under the drying capacity of the dryer, which does not control the increase or decrease of the amount of combustion for supplying hot air and keeps it constant for the best combustion efficiency, it is possible to improve the drying efficiency. [Example] Next, an example of the grain drying method according to the present invention will be described. Typically, the initial moisture M1 of harvested grain is 26-20
%, the finishing moisture of the grain is around 15%, and the convenient drying time in a daily work cycle is 14 to 16 hours. In addition, the allowable drying loss rate (drying rate ΔMmax) is 0.8 to prevent shell cracking.
%/hour. Therefore, the dry finishing moisture content M2 of the grain is 15.5%,
The desired drying time Hr is 14 hours (from 6:00 pm on the same day to 8:00 am on the next day), and the drying capacity η of the dryer is 20 koku%, assuming that the combustion amount for hot air supply is constant for the best combustion efficiency. / hour, the grain filling amount W (stone) is W=η×Hr/M 1 −M 2 . Here, M 1 −M 2 is the moisture required for drying the grain. Under these conditions, the minimum grain loading amount Mm is Wm = η / ΔMmax = 20 / 0.8 = 25 (stones) The initial moisture value M 1 max of grain that can be dried in 14 hours at drying time is M 1 =ΔMmax×Hr× M2 =0.8×14+15.5=26.7(%). The following table shows the amount of grain loaded W 1 and the drying loss rate (drying rate) ΔM for each value of the initial moisture content M 1 of the grain.
Note that when the initial moisture content M1 of the grain is 28% or more and when it is 18% or less, the drying time Hr is adjusted without changing the grain loading amount W. Therefore, the figures are shown in parentheses in the table.
【表】
[発明の効果]
本発明は、前記のように、穀物の初期水分とそ
の乾燥仕上り水分から乾燥所要水分を算出し、乾
燥所要水分、選択した乾減率および熱風供給のた
めの燃焼量を最良の燃焼効率となる乾燥機の乾燥
能力を一定に保ち、その一定の乾燥能力から希望
のする乾燥時間で乾燥が仕上る穀物量を算出し
て、これを乾燥機の一乾燥作業における穀物張込
量とする穀物乾燥方法であるから、乾燥作業の開
始にあたり、予め希望する乾燥時間で穀物を所定
の水分まで乾燥仕上げをすることができ、しか
も、熱風供給のための燃焼量の増減制御を行うこ
となく燃焼量を最良の燃焼効率となる一定の状態
として、乾燥機の乾燥能力を常に最大限に活用し
て、効率のよい乾燥を行うことができる効率を奏
する。[Table] [Effects of the Invention] As described above, the present invention calculates the required moisture content for drying from the initial moisture content of the grain and its finished drying moisture content, calculates the required moisture content for drying, the selected drying loss rate, and the combustion for supplying hot air. Keep the drying capacity of the dryer constant to achieve the best combustion efficiency, calculate the amount of grain that can be finished drying in the desired drying time from that constant drying capacity, and calculate this as the amount of grain in one drying operation of the dryer. Since this is a grain drying method that uses the amount of pressure, it is possible to finish drying the grain to a predetermined moisture content in a pre-desired drying time at the start of the drying process.Moreover, it is possible to increase or decrease the amount of combustion to supply hot air. To achieve efficiency in which the drying capacity of a dryer can always be utilized to the maximum by keeping the combustion amount in a constant state with the best combustion efficiency without performing any oxidation.
Claims (1)
燥所要水分を算出し、乾燥所要水分、選択した乾
減率および熱風供給のための燃焼量を最良の燃焼
効率となる乾燥機の乾燥能力を一定に保ち、その
一定の乾燥能力から希望する乾燥時間で乾燥が仕
上る穀物量を算出して、これを乾燥機の一乾燥作
業における穀物張込量とすることを特徴とする穀
物乾燥方法。1. Calculate the required moisture content for drying from the initial moisture content of the grain and its finished drying moisture content, and then set the drying capacity of the dryer that provides the best combustion efficiency using the required moisture content, the selected drying loss rate, and the amount of combustion for supplying hot air. The grain drying method is characterized in that the amount of grain that can be dried in a desired drying time is calculated from the constant drying capacity, and this is used as the amount of grain loaded in one drying operation of the dryer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25451985A JPS62114664A (en) | 1985-11-13 | 1985-11-13 | Method of drying cereal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25451985A JPS62114664A (en) | 1985-11-13 | 1985-11-13 | Method of drying cereal |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62114664A JPS62114664A (en) | 1987-05-26 |
| JPH0364189B2 true JPH0364189B2 (en) | 1991-10-04 |
Family
ID=17266167
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP25451985A Granted JPS62114664A (en) | 1985-11-13 | 1985-11-13 | Method of drying cereal |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62114664A (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58106614A (en) * | 1981-12-18 | 1983-06-25 | Tatsumoto Akihiro | Drying control method for circulating type grain dryer |
-
1985
- 1985-11-13 JP JP25451985A patent/JPS62114664A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62114664A (en) | 1987-05-26 |
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