JPS59104072A - Method of drying cereal - Google Patents

Method of drying cereal

Info

Publication number
JPS59104072A
JPS59104072A JP21319282A JP21319282A JPS59104072A JP S59104072 A JPS59104072 A JP S59104072A JP 21319282 A JP21319282 A JP 21319282A JP 21319282 A JP21319282 A JP 21319282A JP S59104072 A JPS59104072 A JP S59104072A
Authority
JP
Japan
Prior art keywords
drying
grain
hourly
dried
rate
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.)
Pending
Application number
JP21319282A
Other languages
Japanese (ja)
Inventor
金子 愛次郎
柴田 博光
加藤 尚久
渡辺 鉄四郎
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.)
Kaneko Agricultural Machinery Co Ltd
Original Assignee
Kaneko Agricultural Machinery 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 Kaneko Agricultural Machinery Co Ltd filed Critical Kaneko Agricultural Machinery Co Ltd
Priority to JP21319282A priority Critical patent/JPS59104072A/en
Publication of JPS59104072A publication Critical patent/JPS59104072A/en
Pending legal-status Critical Current

Links

Landscapes

  • Drying Of Solid Materials (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は、水分ムラか多く、かつ初期において正確な検
出水分値が得られない被乾燥穀物といえども、9#湛や
毎時乾減率が予め設定された所定値を満足するように乾
燥させることができる許りか、乾燥作業中において、穀
温および毎時乾減率の両方を同時に所定値以下に制御で
伴ない場合にあっても、設定された毎時乾減率を保つよ
うに加温装置又は送風装置を制御して被乾燥穀物を胴割
れ発生も少なく、能率的に乾燥させることができる穀物
乾燥方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a method for drying grains that have uneven moisture content and cannot obtain an accurate detected moisture value at the initial stage, but can be dried at a predetermined value with 9# water content or hourly drying rate. Even if both the grain temperature and the hourly drying rate are controlled to be below a predetermined value at the same time during the drying process, the set hourly drying rate The present invention relates to a method for drying grains that can efficiently dry grains with less occurrence of shell cracking by controlling a heating device or a blower device so as to maintain the drying temperature.

従来、胴割れの発生が少なく、かつ食味良好な乾燥穀物
を能不的に得るために、被乾燥?吻の穀温および毎時乾
減率を順次経時的に検出しながら、検出穀温および検出
毎時乾減率を穀物の有する含水率に順応して予め設定さ
れた15r定値以下に保ちつつ乾燥せしめる穀vl′J
乾燥方法は、さきに本出願人が特開昭55−15047
5号公報に記載された如く開発して公知である。
Conventionally, in order to obtain dried grains with less occurrence of shell cracking and good taste, drying is required. The grain temperature and hourly drying rate of the proboscis are sequentially detected over time, and the grain temperature and hourly drying rate are kept below a preset value of 15r in accordance with the moisture content of the grain. vl′J
The drying method was previously disclosed in Japanese Patent Application Laid-open No. 55-15047 by the present applicant.
It has been developed and known as described in Publication No. 5.

そして上記従来の穀物乾燥方法にあっては、被乾燥穀物
を飽くまで胴割れ発生が少なく、かつ食味が良好となる
よう自動乾燥させることを主目的としたものである。
The main purpose of the above-mentioned conventional grain drying method is to automatically dry the grain to be dried so as to minimize the occurrence of shell cracking and improve the taste.

ところで、収穫したI#物中に含まれた水分量は常に一
定ではなく、相肖綱′の差があって、この様に穀物間に
水分ムラが多い被乾燥穀物をそのまま、上記公知の穀物
乾燥方法を使用して乾燥せしめた際には、乾燥の初期に
おいて、経時的に検出した検出毎時乾減率はひんばんに
変化し、これに伴ない加温装置および送風装置もその都
度運転が制御1されるため和時乾減率を所定値以下とな
るように正確に制(111することか困難である。
By the way, the amount of moisture contained in the harvested I# grains is not always constant, and there are differences in compatibility, and the dried grains, which have a lot of moisture unevenness among the grains, are directly processed into the above-mentioned known grains. When drying using a drying method, the detected hourly drying loss rate detected over time changes rapidly in the early stage of drying, and the heating device and blower device must be operated each time. Since the drying rate is controlled 1, it is difficult to accurately control (111) the drying rate to be less than a predetermined value.

その上、被乾燥穀物の初期穀温が30℃以上、又は初期
水分が304以上の場合には被乾燥穀物間の水分ムラは
前にもまして多くなって益々正確な検出毎時乾減率の検
出が困難な許りか、この様な被乾燥穀物間を胴割れ発生
が少なく、かつ食味良好となるように所定値に基づいて
乾燥せしめた際には、乾燥時間が長くかかり実用件に適
さない場合がある。
Moreover, when the initial grain temperature of the grain to be dried is 30°C or higher or the initial moisture content is 30°C or higher, the moisture unevenness among the grains to be dried is greater than before, making the detection of the hourly drying rate more accurate. However, when drying grains to be dried according to a predetermined value to reduce cracking and improve taste, the drying time takes a long time and is not suitable for practical use. There is.

そこで、上記の穀′吻を実用に適するように乾燥速度を
早めて乾′燦させた際には、被乾燥穀物の検出穀温およ
び毎時乾減率の両方が予め設定された所定値以上となっ
て所定値以下に制御できず、その結果、胴割れが多く発
生するは勿論のこと食味も著しく低下されるという重大
な欠点が生ずる。
Therefore, when the above-mentioned grain proboscis is dried at a faster drying speed to make it suitable for practical use, both the detected grain temperature and the hourly drying rate of the grain to be dried are equal to or higher than a preset value. Therefore, it cannot be controlled to a predetermined value or less, and as a result, there are serious drawbacks in that not only many shell cracks occur but also the taste is significantly deteriorated.

そこで、本発明は、上記公知の穀物乾燥方法の欠点を解
決するために、被乾燥穀物間に水分ムラが多く検出毎時
乾減率が正確に検出できない乾燥初期にあっては、予め
設定された一定値の熱風温度で初期乾燥を行って被乾燥
穀物間の水分ムラを解消し、水分ムラが解消された以降
にあっては、被乾燥!9vlJの検出炉幅検出乾減率が
設定された所定値以下となるよう加温装置および送風装
置を制御して乾燥を行わせ、又初期穀温又は初期水分が
高い被乾燥穀物を早い速度で乾燥せしめた場合に、その
検出穀温2よび検出毎時乾減率の両方が同時に所定値以
下に制御できない時は、設定された毎時乾減率を保つよ
うに加温装置又は送風装−の両方或はその一方の運転を
制飢して仮乾燥穀物を胴割れ発生も少なく能率的に乾燥
させることができる穀物乾燥方法を得ることを目的とし
たものである。
SUMMARY OF THE INVENTION In order to solve the drawbacks of the known grain drying methods, the present invention aims to solve the above-mentioned drawbacks of the known grain drying methods. Initial drying is performed at a constant hot air temperature to eliminate moisture unevenness among grains to be dried. The heating device and the blower device are controlled so that the detected drying rate is below a predetermined value. In the case of drying, if both the detected grain temperature 2 and the detected hourly drying rate cannot be controlled to be below the predetermined value at the same time, both the heating device or the air blower should be adjusted to maintain the set hourly drying rate. Alternatively, it is an object of the present invention to provide a grain drying method that can efficiently dry provisionally dried grains with less occurrence of shell cracking by controlling one of the operations.

本発明は前記に鑑み、上記公知の穀物乾燥方法の欠点を
解決するために、その方法を、被1ii1’−v物の穀
温および毎時乾減率を順次経時的に検出し、被乾燥穀物
間に水分ムラの多い乾燥初期にあっては、予め設定され
た一定11pの熱風温度で初期乾燥を行い、被乾燥穀物
間の水分ムラが減少した以降にあっては、得られた検出
穀温および検出毎時乾減率が穀物の有する含水率に順応
して予め設定されたバr定値以下となるよう加温装置お
よび送風装置の一方又は両方を制御lしながら乾燥せし
めるか、又は被乾燥穀物の検出詐渦および検出毎時乾減
率の両方を同時に予め設定された所定11目以−トに制
御できない場合には加温装置又は送風装置の両方或は何
れか一方のみを制<dljLなII)も設定された毎時
乾減率を保ちつつ乾しを終了せしめた穀1勿乾燥方法と
したものでルンって、かかる穀物乾燥方法によれは、ψ
燥の初期に被乾燥W物量に水分ムラが多い場合にあって
も、速かに水分ムラを解消させて、検出毎時乾減率の検
出を正確ならしめ、被乾燥穀物の検出穀温および検出毎
時乾減率を予め設定された所定値以下となるよう加温装
置および送風装置を正確に開存11運転させ、胴割れの
発生が少なくかつ食味良好なV燥穀物を能率的に得るこ
とができる許りか、初期−幅又は初期水分の高い被乾燥
穀物であっても、食味が幾分低下されることを我慢すれ
ば胴割れ発生も少なく能率的に舒燥させることができる
効果を奏する。
In view of the above, and in order to solve the drawbacks of the known grain drying methods, the present invention has been developed by sequentially detecting the grain temperature and hourly drying loss rate of the grain to be dried over time. In the early stage of drying when there is a lot of moisture unevenness between grains, initial drying is performed at a preset constant hot air temperature of 11p, and after the moisture unevenness among the grains to be dried has decreased, the detected grain temperature obtained Then, dry the grain while controlling one or both of the heating device and the blower device so that the detected hourly drying loss rate is below a preset value according to the moisture content of the grain, or If it is not possible to simultaneously control both the detected vortex and the detected hourly drying rate to a predetermined 11th point or higher, control only one or both of the heating device and the blower device. ) is also a grain drying method that finishes drying while maintaining the set hourly drying loss rate.
Even if there is a lot of moisture unevenness in the amount of drying W material at the beginning of drying, the moisture unevenness can be quickly resolved to ensure accurate detection of the hourly drying loss rate, and the detection of grain temperature and detection of the dried grain. It is possible to accurately operate the heating device and the blower device so that the hourly drying loss rate is below a predetermined value set in advance, and to efficiently obtain V-dried grains with less occurrence of shell cracking and good taste. Even if the grain to be dried has a high initial width or initial moisture content, it is possible to sow efficiently with less occurrence of shell cracking as long as the taste is tolerated to some extent.

以下に本発明に係る穀物乾燥方法を実施させるためのブ
ロック回路について説明する。
A block circuit for carrying out the grain drying method according to the present invention will be explained below.

第1図において、1は乾燥時間中、被乾燥穀物の穀温を
経時的に検出して、その検出信号を比較回路4へ送るた
めの穀温検出器であって、本発明に係る毀温検出器1は
例えば1時間おきに被乾燥穀物の穀温を乾燥初期より乾
燥終了時迄経時的に検出するようになって′いる。2は
乾燥時間中、被乾燥穀物の毎時乾減率即ち乾燥速度を経
時的に検出して、その検出イg号を比較回路4へ送るた
めの毎時乾減率検出器であって、本発明に係る毎時乾減
率検出器2は例えば1時間おきに被乾燥穀物の毎時乾減
率即ち乾燥速度を乾燥初期より乾燥終了迄経時的に検出
するものである。
In FIG. 1, reference numeral 1 denotes a grain temperature detector for detecting the grain temperature of the grain to be dried over time during the drying time and sending the detected signal to the comparator circuit 4, which is a grain temperature detector according to the present invention. The detector 1 is designed to detect the grain temperature of the grain to be dried over time, for example every hour, from the beginning of drying to the end of drying. Reference numeral 2 denotes an hourly drying loss rate detector for detecting the hourly drying rate, that is, the drying rate of the grain to be dried over time during the drying time, and sending the detected value to the comparator circuit 4, which is an hourly drying rate detector of the present invention. The hourly drying loss rate detector 2 detects the hourly drying rate, that is, the drying speed, of the grain to be dried over time from the beginning of drying to the end of drying, for example, every hour.

3は穀温および毎時乾減率基準設定回路であって、この
回路3は被乾燥穀物間穀温および毎時乾減率が正確に検
出された時に、#物の有する含水率に順応して予め決定
された穀温基準値と毎時乾減率基準1直のイg号を夫々
比較回路4へ送る役目を持たせたものである。したがっ
て、上記穀温および毎時乾減率基準設定回路3は被乾燥
穀物間に水分ムラが多い乾燥の初期にあっては、穀温基
準値と毎時乾減率基準値の信号を比較回路3には送らず
、被乾燥tlIl間物間分ムラが減少された時点以降で
、これらの1ぎ号が比較回路4に送られるようになって
いる。本発明にあっては笑験餉に基づき、その時点を被
乾燥穀物の水分が例えはIj@21.5係と設定してい
る。
Reference numeral 3 denotes a grain temperature and hourly drying rate standard setting circuit, and when the intergrain temperature and hourly drying rate are accurately detected, the circuit 3 sets the standard setting circuit according to the moisture content of the object. It has the role of sending the determined grain temperature reference value and hourly drying rate reference number Ig of the first shift to the comparison circuit 4, respectively. Therefore, the grain temperature and hourly drying rate reference setting circuit 3 sends signals of the grain temperature reference value and the hourly drying rate reference value to the comparing circuit 3 at the beginning of drying when there is a lot of moisture unevenness among the grains to be dried. These signals are sent to the comparator circuit 4 after the unevenness between the pieces to be dried is reduced. In the present invention, based on experimental results, the moisture content of the grain to be dried is set to, for example, Ij@21.5.

又上記の1#縣および毎時乾減率基準設定回路3には、
第2図の乾燥曲線グラフに示されたように例えば初期乾
燥作業によって例えば略21.5%の水分となった被乾
1#8穀物を最終含水車路15%となる迄、穀温を略3
8℃以下に維持させることができる穀温基準表と、略2
1.5%の水分の被乾燥穀物を最終含水率略15係に仕
上げ乾燥させるための毎時乾減率例えば0.6%/時と
なるように決定された毎時乾減率基準1直 る。そして上記夫々の基準表の最低含水率を15係とな
し、上限を無限大とした理由は収穫した穀物を略154
位迄乾燥させる目的からである。
In addition, the above 1# and hourly drying rate standard setting circuit 3 includes:
As shown in the drying curve graph of Figure 2, for example, drying 1#8 grain whose moisture content has become approximately 21.5% due to the initial drying operation is reduced to approximately 100% until the final moisture content reaches 15%. 3
Grain temperature standard table that can be maintained at 8℃ or less and approximately 2
The hourly drying rate standard 1 is determined to be, for example, 0.6%/hour for finishing drying grains having a moisture content of 1.5% to a final moisture content of about 15%. The reason why the minimum moisture content in each of the above standard tables is set to 15% and the upper limit is set to infinity is that the harvested grain is approximately 154%.
This is for the purpose of drying it to a certain extent.

4は穀温検出器1および毎時乾減率検出器2より夫々経
時的に送られて来た信号と、v篇および毎時ψ゛減減率
基設設定回路より経時的に送られて来た信号とを比較し
て加温装置6および送風装置Iの制f卸回路5に信号を
送るための比較回路であって、超比較回路4は通常は被
乾燥穀物の穀温を例えば38℃に、又毎時乾減率を例え
0.6%/時以下となるよう制御するものであるか、乾
燥作業中において、穀温検出器1および毎時乾減率検出
回路2により夫々検出された穀温および毎時乾減率の数
値が予め設定された穀温基準表および毎時乾減率基準値
に決定された数値(例えは穀温38℃、毎時乾減率0.
6係/時)よりも大きくなった場合には速かに制御回路
5へ信号を送って加温装置6゛への燃料供給量又は送風
量M、7の送風量の両方或はその何れか一方のみを増減
制御卸して、検出毎時幹減率のみが予め設定された毎時
乾減率基準値(例えば0.6係/時)を保らように制御
して胴割れ発生の少ない乾I#、穀物を能率的に得さし
めるようにする。
4 are the signals sent over time from the grain temperature detector 1 and the hourly drying rate detector 2, and the signals sent over time from the v section and the hourly ψ゛ reduction rate base setting circuit. This is a comparator circuit for comparing the signal and sending a signal to the f-control circuit 5 of the heating device 6 and the blower I. , or the grain temperature detected by the grain temperature detector 1 and the hourly drying rate detection circuit 2 during the drying operation. and the grain temperature standard table in which the hourly drying rate values are set in advance and the values determined as the hourly drying rate reference values (for example, grain temperature is 38°C, hourly drying rate is 0.
6/hour), it immediately sends a signal to the control circuit 5 to control the amount of fuel supplied to the heating device 6' and/or the amount of air blown M and/or the amount of air blown 7. By increasing/decreasing only one side, the detected hourly trunk loss rate is controlled so that only the detected hourly trunk loss rate is maintained at a preset hourly drying rate reference value (for example, 0.6 sections/hour), which reduces the occurrence of trunk cracking. , so that grain can be harvested efficiently.

したがって、被乾燥穀物の穀温が穀温基準表の数値、(
例えば38℃)より高くなっても、加温装置6および送
風装置7を制御して穀温が穀温基準表の数餉以下にする
ことはない。又被乾燥穀物間圧水分ムラが多く発生する
期間にあっては、これら制御回路5と関係なく、加温装
#6および送風装置7を運転させて例えば48℃となる
ような一定温度の熱風幅1隻で被乾燥穀物間を水分ムラ
の発生が減少される水分(例えば略21.5%)迄初期
乾燥を行わせ、以後は自動制イ卸乾繰作朶に移行させる
ものである。
Therefore, the grain temperature of the dried grain is the value in the grain temperature standard table, (
For example, even if the grain temperature becomes higher than 38° C., the heating device 6 and the blower device 7 are not controlled to make the grain temperature a few degrees below the grain temperature reference table. In addition, during a period when there is a lot of pressure and moisture unevenness among grains to be dried, the heating device #6 and the blower device 7 are operated to generate hot air at a constant temperature of, for example, 48°C, regardless of the control circuit 5. Initial drying is carried out between grains to be dried in a width of one vessel until the moisture content is reduced to reduce the occurrence of moisture unevenness (for example, about 21.5%), and thereafter the process is shifted to an automatic wholesale drying vessel.

なお上記し1こ炉幅および毎時乾減率基準表(本発明の
所定値)および熱風温度は穀′吻量、外気招湿度、所望
の乾燥速度および被乾燥穀物等の条件に基づいて随時そ
の数値は変更されることは勿論である。
Note that the oven width, hourly drying rate standard table (predetermined values of the present invention) and hot air temperature mentioned above can be adjusted at any time based on conditions such as the amount of grain, the humidity introduced by the outside air, the desired drying speed, and the grain to be dried. Of course, the numerical values are subject to change.

次にその作用について説明する。Next, its effect will be explained.

今、初期含水ボが例えば29qbの被乾燥穀物を仕上り
含水出路15係となるよう乾けさせたい時には、先ず!
l;燥作菜の開始に際して水分計により被乾燥穀物の含
水率を測定し、被乾燥穀物間に相肖量の水分ムラがあっ
たら、加温装置6および送風装置7ケ運転させて、予め
設冗された一定値の熱風温度(例えば48℃)で初期乾
沫を行う。
Now, when you want to finish dried grain with an initial moisture content of, for example, 29 qb, and dry it so that it has a moisture content of 15, first!
l; At the start of drying, measure the moisture content of the grains to be dried using a moisture meter, and if there is uneven moisture content among the grains to be dried, operate the heating device 6 and the blower device 7 to dry the grains in advance. Initial drying is performed at a constant hot air temperature (for example, 48° C.).

ところで、この乾燥初期にあってもIF−1検出器1お
よび毎時If誠量率検出器により経時的に検出した検出
穀温数値および検出毎時転減車数1i1が比較回路4へ
毎号となって送られている。
By the way, even in this early stage of drying, the detected grain temperature value and the detected number of cars turning over per hour 1i1 detected over time by the IF-1 detector 1 and the hourly If accuracy rate detector are sent to the comparison circuit 4 every issue. It is being

したかつて、この乾燥初期作業により含水車路29%の
被乾燥穀物が含水率略21.5%位まで乾燥されてくる
と、被乾燥穀物間の水分ムラが著しく減少されて、穀温
検出器1および毎時乾減率検小器2により検出された穀
滉数111および毎時乾減率数値が安定する。この様な
状す、―になると穀温および毎時乾減率基準設定回路3
より経時的に、穀物の有する含水率に順応して第2図に
示された炉幅基準数1・a(例えば38℃)と毎時乾減
率基糸数値(例えば0.6%/11♀)が□回路に信号
となって比較回路4に送られここで比較される。
In the past, when the grains to be dried, which were 29% of the water-containing carriageway, were dried to a moisture content of about 21.5% through this initial drying process, the moisture unevenness among the grains to be dried was significantly reduced, and the grain temperature detector 1 and the hourly drying rate value detected by the hourly drying rate detector 2 become stable. In such a situation, the grain temperature and hourly drying rate standard setting circuit 3
Over time, the oven width standard number 1・a (e.g. 38°C) and the hourly drying rate basic thread value (e.g. 0.6%/11♀ ) becomes a signal in the □ circuit and is sent to the comparator circuit 4 where it is compared.

その結果、被乾燥穀物は上記−輻検小器1および毎時乾
減率基準表2の経時的検出作用で含水率21.5%〜1
5qb迄は穀幅が38℃ 以下に、又毎時乾減率も0.
6%/時以下となるよ5 fl+lI ri11回路5
へ信号が送られ、この制仰情号に糸ついて加温装置6お
よび送ノ虱装、1θ1の一方又は両方を夫々自動開側1
して熟眠rh1度或は送j虱穎:をw4督し、含水率が
略15%になる迄自jl乾味作柔か継続され乾燥を終了
するものである。
As a result, the moisture content of the dried grain was determined to be between 21.5% and 1% by the time-dependent detection function of the above-mentioned Radiation Inspection Instrument 1 and Hourly Drying Rate Standard Table 2.
Up to 5qb, the grain width is below 38℃ and the hourly drying rate is 0.
It will be less than 6%/hour5 fl+lI ri11 circuit 5
A signal is sent to the control information to automatically open one or both of the heating device 6 and the feeding device 1θ1, respectively.
Then, the drying process is continued until the moisture content reaches approximately 15%, and the drying process is completed.

又、上述の乾燥方法を用いて、初期穀温が30℃以上、
或は初期水分が30%以上の被乾燥e物を、口11記乾
楳方法の穀η^および毎時乾減率基準表に基づいて早く
乾燥させようとした場合に、検出毀妃2よび検出毎時乾
減率の両方が予め設定された所定値(例えば穀温38℃
、毎時I#減率0.6係/時)以下に制6111できな
く ノZってしまう場合が生ずる。この様なことか炉幅
検出器1および毎時乾減率検出器2により夫々検出され
たら、この時点において比較回路4が働いて毎時乾減率
のみを予め設定された毎時乾減率基準表の数値(例えば
0,6係/時)を保つように制御回路5へ信号が送られ
、加温装置6への燃料供給量又は送風袋に7による送i
tの両方又はその何れか一方を自egJr的に制御して
検出毎時乾減率のみが予め基準表に設定された毎時乾減
率の数1i&、 (例えば06%/時)を保って仮乾燥
穀物を能率的に、しかも胴割れ発生も少なく仕上げ含水
率例えば15係に乾燥させるものである。
In addition, using the above drying method, if the initial grain temperature is 30°C or higher,
Alternatively, if you try to quickly dry the material to be dried with an initial moisture content of 30% or more based on the grain η^ of the drying method described in Section 11 and the hourly drying loss rate standard table, Detection 2 and Detection Both hourly drying rates are set to predetermined values (e.g. grain temperature of 38°C).
, hourly I# reduction rate of 0.6 units/hour) or less may not be possible and the case may occur. If something like this is detected by the furnace width detector 1 and the hourly drying rate detector 2, at this point the comparison circuit 4 operates and calculates only the hourly drying rate from the preset hourly drying rate reference table. A signal is sent to the control circuit 5 to maintain the numerical value (for example, 0.6 coefficients/hour), and the amount of fuel supplied to the heating device 6 or the amount of fuel supplied to the air bag by 7 is sent to the control circuit 5.
Temporary drying is performed by automatically controlling both or either of t and the detected hourly drying rate while maintaining the hourly drying rate number 1i & (for example, 06%/hour) set in advance in the standard table. To efficiently dry grains with less cracking and to a finished moisture content of, for example, 15.

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

図u1は本発明に係る方法を火施するだめのブロック回
路図であり、第2図は予め設定された牧妃および毎時乾
絨駆基草i+Mを用い1こ軸片曲線グラフ図である。 1・・・穀温検出器、2・・・毎時乾減率検出器、3・
・・穀温および毎時乾減率基準設定回路、4・・・比較
回路、5・・・制御回路、6・・・加温装置、7・・・
送風装置%許出願人 金子農機株式会社 代理人弁理士   1−、アーコ 8   D   恭   蘂 −: ;  1 し−′とjl、i、、−ノ 手 続 イrR正 書 (方式) 1、事件の表示 cfXi、+1昭67−213192号2、発明の名称 穀物乾燥方法 3、 補正をする者 事件との関係 特許出願人 埼玉県羽生市西2丁目21番1o号 (146)  金子農機株式会社 代表者 金 子 愛次部 4、代理人 〒201 5、 補正命令の日付 昭和58年3月9日 6、 補正の対象 「図面の簡単な説明の欄」 7、補正の内容 fil  明細書第12頁第17行記載の「図面は」を
「第1図は」と補正します。
FIG. 1 is a block circuit diagram of a fire application method according to the present invention, and FIG. 2 is a single-axis single curve graph using a predetermined ratio and hourly dry carpet base i+M. 1... Grain temperature detector, 2... Hourly drying rate detector, 3.
... Grain temperature and hourly drying rate reference setting circuit, 4... Comparison circuit, 5... Control circuit, 6... Warming device, 7...
Patent attorney representing applicant Kaneko Agricultural Machinery Co., Ltd. for blower equipment % 1-, Arco 8 D Kyoto -: ; Indication cfXi, +1 1986-213192 No. 2, Name of the invention Grain drying method 3, Relationship with the case of the person making the amendment Patent applicant No. 2-21-1-1 Nishi, Hanyu City, Saitama Prefecture (146) Representative of Kaneko Agricultural Machinery Co., Ltd. Kaneko Aijibe 4, Agent 201-5, Date of amendment order March 9, 1980 6, Subject of amendment "Column for brief explanation of drawings" 7. Contents of amendment fil Specification, page 12, No. "The drawing is" written in line 17 will be corrected to "Figure 1 is".

Claims (1)

【特許請求の範囲】[Claims] 被乾燥穀物の穀温および毎時乾減率を順次経時的に検出
し、被乾燥穀物間に水分ムラの多い乾燥初期にあっては
、予め設定された一定値の熱風温度で初期乾燥を行い、
被乾燥穀物間の水分ムラが減少した以降にあっては、得
られた検出穀温および検出毎時乾減率が穀物の有する含
水率に順応して予め設定されたQt定愼以下となるよう
加温装置および送ノ虱装置の一方又は両方を開側1シな
がら乾燥せしめるか、又は被乾燥穀物の検出−温および
検出毎時乾減率の両方を同時に予め設定された所定値以
下に制資1りできない場合には加温装置又は送j戦装い
:の両方或は伺れか一方のみを制(財)しながら設定さ
れた毎時乾減率を保ち°つつ乾燥を終了せしめたこと馨
前畝とする穀の脅、燥方法。
The grain temperature and hourly drying rate of the grain to be dried are detected sequentially over time, and in the early stage of drying when there is a lot of moisture unevenness among the grains to be dried, initial drying is performed at a preset constant hot air temperature.
After the moisture unevenness among the grains to be dried is reduced, the detected grain temperature and the detected hourly drying loss rate are adjusted to the moisture content of the grain and are adjusted to be equal to or lower than the preset Qt constant pressure. Either one or both of the heating device and the feeding device are dried with the open side, or both the detection temperature and the detection hourly drying rate of the grain to be dried are simultaneously reduced to below a predetermined value. If this is not possible, drying should be completed while maintaining the set hourly drying rate while controlling either or both of the heating device and the feeder. Grain threats and drying methods.
JP21319282A 1982-12-05 1982-12-05 Method of drying cereal Pending JPS59104072A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21319282A JPS59104072A (en) 1982-12-05 1982-12-05 Method of drying cereal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21319282A JPS59104072A (en) 1982-12-05 1982-12-05 Method of drying cereal

Publications (1)

Publication Number Publication Date
JPS59104072A true JPS59104072A (en) 1984-06-15

Family

ID=16635058

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21319282A Pending JPS59104072A (en) 1982-12-05 1982-12-05 Method of drying cereal

Country Status (1)

Country Link
JP (1) JPS59104072A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57117773A (en) * 1981-01-14 1982-07-22 Kubota Ltd Automatic control of grain dryer
JPS57122278A (en) * 1981-01-22 1982-07-30 Akihiro Tatsumoto Operation control of grain dryer

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57117773A (en) * 1981-01-14 1982-07-22 Kubota Ltd Automatic control of grain dryer
JPS57122278A (en) * 1981-01-22 1982-07-30 Akihiro Tatsumoto Operation control of grain dryer

Similar Documents

Publication Publication Date Title
JP3140039B2 (en) Flash drying method and apparatus for tobacco raw materials
GB1415180A (en) Method of and apparatus for assessing the moisture of tobacco or the like
JPS59104072A (en) Method of drying cereal
JPS58217183A (en) Method and device for adjusting moisture in material
JPS59104074A (en) Method of drying cereal
US3376877A (en) Moist feed mix air permeability control
JPS59104071A (en) Method of drying cereal
JPS60181578A (en) Method of drying cereal
JPS59157477A (en) Method of drying cereal
JPS60181580A (en) Method of drying cereal
JPH0252542B2 (en)
JPS5826983A (en) Automatic controller for cereal drier
JPH068475Y2 (en) Drying control device in grain dryer
JPS60181577A (en) Method of drying cereal
JPS60181579A (en) Method of drying cereal
JP3409396B2 (en) Method for producing α-L-aspartyl-L-phenylalanine methyl ester
JPS59157476A (en) Method of drying cereal
JPS62178882A (en) Method of drying cereal
JPS60228889A (en) Method and device for drying cereal
JPH01167569A (en) Drying control method for cereal
SU1012987A1 (en) Method of automatic control of ventilated mill
JPS5828971A (en) Automatic controller for cereal drier
JPS60181576A (en) Method of drying cereal
JP3536696B2 (en) Coal moisture control method in humidification equipment
JPS5915787A (en) Drying facility for moist material