JPH0252542B2 - - Google Patents
Info
- Publication number
- JPH0252542B2 JPH0252542B2 JP7880883A JP7880883A JPH0252542B2 JP H0252542 B2 JPH0252542 B2 JP H0252542B2 JP 7880883 A JP7880883 A JP 7880883A JP 7880883 A JP7880883 A JP 7880883A JP H0252542 B2 JPH0252542 B2 JP H0252542B2
- Authority
- JP
- Japan
- Prior art keywords
- drying
- moisture value
- grain
- dried
- value
- 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
Links
- 238000001035 drying Methods 0.000 claims description 92
- 238000000034 method Methods 0.000 claims description 17
- 238000007664 blowing Methods 0.000 description 10
- 238000002485 combustion reaction Methods 0.000 description 8
- 238000005259 measurement Methods 0.000 description 5
- 239000002184 metal Substances 0.000 description 3
- 230000002159 abnormal effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 208000032368 Device malfunction Diseases 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 230000007257 malfunction Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
- Adjustment And Processing Of Grains (AREA)
Description
【発明の詳細な説明】
本発明は、乾燥中の被乾燥穀物の水分値を経時
的に測定して、予め設定された目標水分値に沿わ
せるように乾減率制御するものにおいて、被乾燥
穀物の水分値の測定誤差による過乾燥を未然に防
止することができる穀物乾燥制御方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention measures the moisture value of grains to be dried during drying over time and controls the drying loss rate so as to follow a preset target moisture value. The present invention relates to a grain drying control method that can prevent overdrying due to measurement errors in grain moisture values.
加温装置および送風装置を用いて穀物の乾燥を
行うにあたつては、穀物にあてる熱風温度やその
風量ばかりでなく、穀物自体の温度や水分発散量
が適当な範囲に維持されないと、品質の著しい低
下をまねいて食味が劣化したり、胴割れが発生し
たり、あるいは乾燥が効率よく行われない。 When drying grain using a heating device and blower, it is important to maintain not only the temperature and volume of the hot air applied to the grain, but also the temperature and amount of moisture released from the grain itself, to ensure quality. This can lead to a significant decrease in flavor, resulting in deterioration of taste, cracking of the shell, or inefficient drying.
そこで、本出願人は、被乾燥穀物の乾燥制御を
適正かつ確実に行うため、被乾燥穀物の毎時乾減
率を経時的に検出し、毎時乾減率を予め設定され
た乾減率以下に保ちながら乾燥する穀物乾燥方法
を開発して、相当の効果を得ている。そして、こ
の穀物乾燥方法は、特開昭55−150475号公報に記
載されていて本出願前公知である。 Therefore, in order to appropriately and reliably control the drying of grains to be dried, the applicant has determined that the hourly drying loss rate of the grains to be dried is detected over time, and the hourly drying loss rate is kept below a preset drying rate. We have developed a method of drying grains that allows them to dry while preserving the grain, and have achieved considerable results. This grain drying method is described in Japanese Patent Application Laid-Open No. 150475/1982 and was known before the filing of this application.
しかしながら、上記穀物乾燥方法においても、
乾燥中の被乾燥穀物の水分値を経時的に測定する
水分測定装置に金属片等の異物が介在したり、あ
るいはその装置が故障すると、測定水分値が被乾
燥穀物の実際の水分値より高く現われることがあ
るので、かかる場合には被乾燥穀物が過乾燥状態
に陥り、品質が著しくそこなわれるおそれがあつ
た。 However, even in the above grain drying method,
If a foreign object such as a metal piece is present in the moisture measuring device that measures the moisture value of the grain to be dried over time during drying, or if the device malfunctions, the measured moisture value may be higher than the actual moisture value of the grain to be dried. In such cases, the grain to be dried may become overdried, and its quality may be significantly impaired.
そこで、本発明は上記に鑑み、たとえ被乾燥穀
物の測定水分値に誤差が生じても、被乾燥穀物が
過乾燥状態に陥るのを未然に防止することができ
る穀物乾燥制御方法を得ることを目的とするもの
である。 Therefore, in view of the above, the present invention aims to provide a grain drying control method that can prevent the grain to be dried from falling into an overdrying state even if an error occurs in the measured moisture value of the grain to be dried. This is the purpose.
本発明は、上記目的を達成するため、特にその
方法を、乾燥中の被乾燥穀物の水分値を経時的に
測定し、この測定水分値を、予め設定された乾減
率による日標水分値に沿わせるように乾減率制御
するものにおいて、上記目標水分値による乾減率
制御の全工程時点あるいは最終時点またはその直
前時点の目標水分値と、その夫々の時点における
測定水分値の差が一定値以上の場合に乾燥を停止
させ、または乾燥の停止と同時に警報を発せしめ
ることを特徴とする穀物乾燥制御方法としたもの
であつて、かかる穀物乾燥制御方法によれば、乾
燥率制御の全工程時点あるいは終了段階におい
て、万一、測定水分値が金属片等の異物の混入で
高く現われる測定誤差が生じることがあつても、
かかる場合には乾燥の進行を直ちに停止させて、
被乾燥穀物が過乾燥状態に陥つて品質がそこなわ
れてまずくなつたり、乾燥穀物の収穫量が減収さ
れるのを未然に防止することができる効果を奏す
る。 In order to achieve the above-mentioned object, the present invention has a method in which the moisture value of grain to be dried is measured over time during drying, and the measured moisture value is converted into a daily standard moisture value based on a preset drying rate. In the case where the drying rate is controlled in accordance with the above target moisture value, the difference between the target moisture value at the entire process point, the final point, or the point just before that of the drying rate control using the target moisture value, and the measured moisture value at each point. This grain drying control method is characterized by stopping drying or issuing an alarm at the same time as drying stops when the temperature exceeds a certain value, and according to this grain drying control method, drying rate control is Even in the unlikely event that a high measurement error occurs in the measured moisture value due to the contamination of foreign objects such as metal pieces, during the entire process or at the final stage,
In such a case, immediately stop the drying process and
This has the effect of preventing the grain to be dried from falling into an over-dried state, deteriorating its quality and becoming unpalatable, and preventing the yield of dried grains from decreasing.
以下に本発明に係る穀物乾燥制御方法を図示の
実施例について説明する。 The grain drying control method according to the present invention will be described below with reference to the illustrated embodiments.
第1図には乾燥時間と被乾燥穀物の水分値との
関係が示されている。すなわち、横軸には乾燥時
間(時)が、縦軸には被乾燥穀物の水分値(%)
がとられており、全乾燥時間は、被乾燥穀物にあ
てる熱風の温度により、初期定温乾燥期A、乾減
率制御乾燥期B、仕上定温乾燥期Cに分けられ
る。乾減率制御乾燥期Bにおける直線Dは、予め
設定された乾減率による目標水分値を示してお
り、この目標水分値は、乾減率制御乾燥期Bの開
始時点とその終了時点における被乾燥穀物の水分
値および乾減率制御乾燥期Bの時間の関係によつ
て、例えば毎時乾減率1.0%、0.8%の如く予め設
定されるものである。なお、図中の黒点は毎時目
標水分値、白丸点は被乾燥穀物の測定水分値を示
している。 FIG. 1 shows the relationship between drying time and moisture content of the grain to be dried. In other words, the horizontal axis shows the drying time (hours), and the vertical axis shows the moisture value (%) of the grain to be dried.
The total drying time is divided into an initial constant-temperature drying period A, a drying loss rate control drying period B, and a final constant-temperature drying period C, depending on the temperature of the hot air applied to the grains to be dried. The straight line D in the drying rate controlled drying period B indicates the target moisture value based on the preset drying rate, and this target moisture value is based on the moisture content at the start and end of the drying rate controlled drying period B. Depending on the relationship between the moisture value of the dried grains and the time of the drying period B for controlling the drying loss rate, the hourly drying loss rate is set in advance to, for example, 1.0% or 0.8%. In addition, the black dots in the figure indicate the hourly target moisture value, and the white dots indicate the measured moisture value of the grain to be dried.
今、穀物の乾燥にあたり、初期定温乾燥期Aに
あつては、熱風の温度を一定に保つて被乾燥穀物
を通風乾燥する。そして、初期定温乾燥期Aの終
了時点、すなわち乾減率制御乾燥期Bの開始時点
においては、被乾燥穀物の水分値を例えば3回測
定し、その平均値をもつて乾減率制御乾燥期Bの
初期水分値を決定し、乾減率制御乾燥期Bの終期
目標水分値との関係で乾減率を求めて目標水分値
Dを設定する。乾減率制御乾燥期Bにおいては、
例えば1時間毎に被乾燥穀物の水分値を測定し、
その毎時測定水分値を目標水分値Dに沿うように
熱風温度または熱風量が制御され、乾燥が続けら
れる。乾減率制御乾燥期Bの終了時点は、目標水
分値Dが乾燥仕上り水分値より若干高い水分値、
例えば乾燥仕上り水分値が14%であれば15%に設
定されるが、乾減率制御乾燥期Bの終期に至つた
際には、被乾燥穀物の水分を例えば3回測定し
て、その平均値を検出する。そして、その平均水
分値に基いて以後所要時間の仕上定温乾燥期Cを
経て全乾燥工程が完了する。 Now, when drying the grains, in the initial constant temperature drying period A, the temperature of the hot air is kept constant and the grains to be dried are ventilated and dried. Then, at the end of the initial constant temperature drying period A, that is, at the start of the drying rate controlled drying period B, the moisture value of the grain to be dried is measured, for example, three times, and the average value is used as the drying rate controlled drying period. The initial moisture value of B is determined, and the drying rate is determined in relation to the final target moisture value of the drying period B, and the target moisture value D is set. In the drying period B with drying rate control,
For example, measuring the moisture value of dried grain every hour,
The hot air temperature or hot air volume is controlled so that the hourly measured moisture value is in line with the target moisture value D, and drying is continued. At the end of drying loss rate control drying period B, the target moisture value D is a moisture value slightly higher than the finished drying moisture value,
For example, if the finished drying moisture value is 14%, it is set to 15%, but when reaching the end of the drying period B, the moisture content of the grain to be dried is measured three times and the average value is set to 15%. Detect values. Then, based on the average moisture value, the entire drying process is completed through a finishing constant temperature drying period C for a required time.
ところで、上記乾減率制御乾燥期Bの全工程あ
るいはその終期において、被乾燥穀物の測定水分
値が実際の水分値より高く現われる測定誤差が生
じると、仕上定温乾燥が過剰となるので、このま
までは被乾燥穀物は過乾燥状態に陥るが、乾減率
制御乾燥期Bの全工程における毎時測定水分値ま
たは終期における測定水分値が一定値以上となつ
た場合には、熱風発生装置における燃焼を停止さ
せたり、あるいは熱風の送風を停止して、乾燥を
直ちに停止させるので、被乾燥穀物が過乾燥状態
に陥るのを未然に防止することができる。乾燥を
停止させる測定水分値は、乾減率制御乾燥期Bの
全工程における毎時目標水分値および終期の目標
水分値より例えば2〜3%程度にそれぞれ予め設
定される。なお、上記乾燥停止と同時に警報を発
せしめるようにしてもよい。 By the way, if a measurement error occurs in which the measured moisture value of the grain to be dried appears higher than the actual moisture value during the entire process or the final stage of the drying rate controlled drying period B, the final constant temperature drying will be excessive, so if it continues as it is, The grain to be dried becomes over-dried, but if the moisture value measured every hour during the entire process of drying rate control drying period B or the moisture value measured at the end of the drying period exceeds a certain value, combustion in the hot air generator is stopped. Since drying is immediately stopped by stopping the blowing of hot air or by stopping the blowing of hot air, it is possible to prevent the grain to be dried from becoming over-dried. The measured moisture value at which drying is to be stopped is set in advance to, for example, about 2 to 3% from the hourly target moisture value in all steps of the drying rate control drying period B and the target moisture value at the final stage. Note that an alarm may be issued at the same time as the drying is stopped.
第2図には本発明の方法を実施するための装置
が例示されている。 FIG. 2 illustrates an apparatus for carrying out the method of the invention.
すなわち、1は乾燥中の被乾燥穀物の水分を経
時的に測定する水分測定器、2は毎時目標水分値
を設定する目標水分値設定器、3は比較回路、4
は熱風発生装置の燃焼または送風制御回路、5は
その熱風発生装置であつて、上記比較回路3は水
分測定器1および目標水分値設定器2からの信号
を受けてこれを比較し、燃焼または送風制御回路
4に制御信号を送出し、該燃焼または送風制御回
路4は測定水分値が目標水分値に沿うように熱風
発生装置5から送風される熱風温度または熱風量
を制御するものである。 That is, 1 is a moisture measuring device that measures the moisture of the grain to be dried over time, 2 is a target moisture value setting device that sets a target moisture value every hour, 3 is a comparison circuit, and 4
Reference numeral 5 indicates a combustion or blowing control circuit for a hot air generator, and 5 indicates the hot air generator. A control signal is sent to the air blowing control circuit 4, and the combustion or air blowing control circuit 4 controls the temperature or amount of hot air blown from the hot air generator 5 so that the measured moisture value is in line with the target moisture value.
一方、6は他の比較回路、7は測定水分値上限
設定器であつて、上記比較回路6は水分測定器
1、比較回路3および測定水分値上限設定器7か
ら信号を受けて、乾減率制御乾燥期Bにおける測
定水分値がその測定時点の目標水分値Dよりも測
定水分値上限設定器7に設定された一定値以上に
現われた際に制御信号を送出するものである。8
は燃焼または送風停止回路、9は警報回路であつ
て、これらは比較回路6から送出される制御信号
を受け、測定水分値がその測定時点の目標水分値
より一定値以上高く現われた際に熱風発生装置5
における燃焼または送風を停止して、乾燥を直ち
に停止させる回路を構成するものである。 On the other hand, 6 is another comparison circuit, and 7 is a measured moisture value upper limit setter. A control signal is sent when the measured moisture value in the rate control drying period B exceeds the target moisture value D at the time of measurement by a certain value set in the measured moisture value upper limit setter 7. 8
9 is a combustion or air blowing stop circuit, and 9 is an alarm circuit that receives a control signal sent from the comparator circuit 6, and when the measured moisture value appears higher than the target moisture value at the measurement point by more than a certain value, the hot air is stopped. Generator 5
This constitutes a circuit that immediately stops drying by stopping combustion or air blowing.
叙上の如く構成された装置によれば、乾減率制
御乾燥期Bにおいて水分測定器1により被乾燥穀
物の水分値が経時的に測定され、目標水分値設定
器2によつて予め設定された目標水分値Dに沿う
ように乾減率制御装置が行われる。そして、乾減
率制御乾燥期Bの開始から終期に至るまでは、被
乾燥穀物の水分が経時的に測定されるが、万一、
水分測定器1に金属片等の異物が介在したり、あ
るいはその故障等によつて測定水分値が異常に高
く現われた場合には、比較回路6から制御信号が
送出され、熱風発生装置5における燃焼または送
風が停止して、乾燥が直ちに停止されるので、被
乾燥穀物が過乾燥状態に陥るのを未然に防止する
ことができる。また、これと同時に警報を発せし
めるようにしたものでは、異常状態を確実に察知
でき、異常状態の解消と所要の回復操作を遅滞な
く行うことができる。 According to the apparatus configured as described above, the moisture value of the grain to be dried is measured over time by the moisture measuring device 1 during the drying period B under drying rate control, and the moisture value is set in advance by the target moisture value setting device 2. The drying rate control device is operated in accordance with the target moisture value D. From the beginning to the end of the drying period B with controlled drying rate, the moisture content of the grain to be dried is measured over time, but in the unlikely event that
If a foreign object such as a metal piece is present in the moisture measuring device 1, or if the measured moisture value appears abnormally high due to a malfunction, a control signal is sent from the comparison circuit 6, and the control signal is sent to the hot air generator 5. Since the combustion or air blowing is stopped and the drying is immediately stopped, it is possible to prevent the grain to be dried from becoming overdried. Furthermore, if an alarm is issued at the same time, an abnormal state can be reliably detected, and the abnormal state can be resolved and necessary recovery operations can be performed without delay.
図面は本発明に係る穀物乾燥制御方法の一実施
例を示すものであつて、第1図はその方法を説明
するための乾燥時間と被乾燥穀物の水分値との関
係図、第2図は本発明の方法を実施する装置のブ
ロツク図である。
A……初期定温乾燥期、B……乾減率制御乾燥
期、C……仕上定温乾燥期、D……予め設定され
た乾減率による目標水分値、1……水分測定器、
2……目標水分値設定器、3……比較回路、4…
…熱風発生装置の燃焼または送風制御回路、5…
…熱風発生装置、6……比較回路、7……測定水
分値上限設定器、8……燃焼または送風停止回
路、9……警報回路。
The drawings show an embodiment of the grain drying control method according to the present invention, and FIG. 1 is a diagram showing the relationship between the drying time and the moisture value of the grain to be dried to explain the method, and FIG. 1 is a block diagram of an apparatus implementing the method of the invention; FIG. A...Initial constant temperature drying period, B...Drying loss rate control drying period, C...Final constant temperature drying period, D...Target moisture value based on preset drying rate, 1...Moisture measuring device,
2...Target moisture value setting device, 3...Comparison circuit, 4...
... Combustion or blowing control circuit of hot air generator, 5...
... Hot air generator, 6 ... Comparison circuit, 7 ... Measured moisture value upper limit setting device, 8 ... Combustion or blowing stop circuit, 9 ... Alarm circuit.
Claims (1)
し、この測定水分値を、予め設定された乾減率に
よる目標水分値に沿わせるように乾減率制御する
ものにおいて、上記目標水分値による乾減率制御
の全工程時点あるいは最終時点またはその直前時
点の目標水分値と、その夫々の時点における測定
水分値の差が一定値以上の場合には乾燥を停止さ
せ、または乾燥の停止と同時に警報を発せしめる
ことを特徴とする穀物乾燥制御方法。1. In a device that measures the moisture value of the grain to be dried during drying over time and controls the drying rate so that the measured moisture value follows a target moisture value based on a preset drying rate, the target moisture value is If the difference between the target moisture value at all process points, the final point, or the point immediately before the drying loss rate control based on value, and the measured moisture value at each point is greater than a certain value, drying is stopped, or drying is stopped. A grain drying control method characterized by simultaneously issuing an alarm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7880883A JPS59203646A (en) | 1983-05-04 | 1983-05-04 | Drying control of grain |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7880883A JPS59203646A (en) | 1983-05-04 | 1983-05-04 | Drying control of grain |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59203646A JPS59203646A (en) | 1984-11-17 |
| JPH0252542B2 true JPH0252542B2 (en) | 1990-11-13 |
Family
ID=13672140
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7880883A Granted JPS59203646A (en) | 1983-05-04 | 1983-05-04 | Drying control of grain |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59203646A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60213786A (en) * | 1984-04-06 | 1985-10-26 | 株式会社クボタ | How to prevent overdrying in grain dryers |
-
1983
- 1983-05-04 JP JP7880883A patent/JPS59203646A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59203646A (en) | 1984-11-17 |
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