JPS611987A - grain dryer - Google Patents
grain dryerInfo
- Publication number
- JPS611987A JPS611987A JP11976884A JP11976884A JPS611987A JP S611987 A JPS611987 A JP S611987A JP 11976884 A JP11976884 A JP 11976884A JP 11976884 A JP11976884 A JP 11976884A JP S611987 A JPS611987 A JP S611987A
- Authority
- JP
- Japan
- Prior art keywords
- hot air
- air temperature
- grain
- value
- 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.)
- Granted
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】
1、産業上の利用分野1
本発明は一般に穀物乾燥機に関し、特に被乾燥穀粒の特
質に応じて自動的に乾燥時間の設定を行なう穀物乾燥機
に関する。DETAILED DESCRIPTION OF THE INVENTION 1. Field of Industrial Application 1 The present invention generally relates to a grain dryer, and more particularly to a grain dryer that automatically sets a drying time according to the characteristics of the grain to be dried.
1−従来技術及びその問題点]
穀物乾燥機は、一般に、自動/手動水分計が機内循環す
る穀粒をリーンプリングして該穀粒の含水率を測定lノ
、該測定結果に従って乾燥機燃焼系を制御して熱風渦電
、乾燥時間等を調整するとともに、駆動系のみを駆動し
て通風乾燥f1業をも行なう。1-Prior art and its problems] Grain dryers generally use automatic/manual moisture meters to lean-pull grains circulating within the machine to measure the moisture content of the grains, and then dryer combustion is performed according to the measurement results. The system is controlled to adjust the hot air eddy current, drying time, etc., and the ventilation drying f1 operation is also performed by driving only the drive system.
ところで・上記のごどぎ構成の乾燥機を使用した乾燥作
業は、全体として綿密な乾燥81画の下に実施されるの
が一般的であり、−行程に要する乾燥時間幅を被乾燥穀
粒の種類や特質に応じて大幅に司変することは乾燥R1
画全体どして太きイ1狂いを生ずることどなる。そのた
め従来においては予め乾燥を施す穀粒の種類fりに胴割
れや表皮のシワ等の発生が防止可能な乾燥時間を設定し
ておき、該設定した乾燥時間を穀粒の種類別に割り振つ
−C乾燥作業を実施していた。しかしくZがら同一種類
の穀粒であっても初期含水率に大きなバラツキがある場
合などは、−11−に乾燥時間が設定されてしまうため
穀粒の胴割れ、表皮のシワ等の発生を防止することは囲
動であった。そこで穀粒の品質低小を17j来する胴割
れ等の介住を極力防止Jるとともに乾燥h−1画に11
!l した乾燥時間の設定が可能(7考案が従来より種
々提案され−CきA: 、、例えば自動水分L!で測定
した穀粒の初期含水率と張込f場や穀物種類等に応じて
自動的熱風温lα、乾燥11,1間の初期設定を行なっ
た1わ、乾燥途中でリンプリングした穀粒の含水率が所
定値〈例えば22%)に達りると該穀粒の種類、特質に
応じ−C前記熱用記石を可変し初期設定した乾燥時間を
調整づる方法など()その1つで゛ある。By the way, the drying work using the dryer with the above-mentioned configuration is generally carried out under a thorough drying process, and the drying time required for the process is Drying R1 varies greatly depending on the type and characteristics of
The whole picture is so thick that it becomes distorted. Therefore, conventionally, a drying time that can prevent the occurrence of shell cracking, skin wrinkles, etc. is set in advance for each type of grain to be dried, and the set drying time is allocated to each grain type. -C Drying work was being carried out. However, if there is a large variation in initial moisture content even if the grains are of the same type, the drying time will be set to -11-, which may cause cracks in the grain shell, wrinkles in the epidermis, etc. To prevent it was a siege. Therefore, we are trying to prevent as much as possible the occurrence of cracking of the shell, etc., which leads to a decrease in the quality of the grains, and at the same time, drying
! It is possible to set the drying time according to the initial moisture content of the grain measured by automatic moisture L!, the loading field, the type of grain, etc. Automatic hot air temperature lα, initial settings for drying 11, 1. When the moisture content of the limped grains reaches a predetermined value (for example, 22%) during drying, the type of the grains, One of the methods is to adjust the initially set drying time by varying the heating stone according to the characteristics.
しかしながら−1記のごとき考案に+13い−(は、乾
燥途中での穀粒の含水捧″が予め設定されている所定値
に達したとぎに初期設定した熱風温度を新たに設定しl
こ熱用渇爪に可変覆ることとしているため、同一種類の
該第1“lであっても初期含水率の相3Uにより乾燥開
始から前記所定含水率に達づるまでのh間が相違1!ざ
るを得ない。そのため初期設定した熱“用温痕での乾燥
作業から被乾燥穀粒の特質等に応じて可変した熱風温度
で行なう乾燥作業へと移行する時間にバラツギが多く能
率的な乾燥作業が回動であるばかりでなく、胴割れ等穀
粒の品質低下の原因を除去できないという問題点があっ
た。そのうえ初ll11設定した熱風温度を急激に可変
Jることにより乾燥機のバーブ燃焼系の燃焼状態が不安
定になるという別の問題点があった。However, there is an additional 13 problem with the idea as described in 1. (1) The initially set hot air temperature is set anew as soon as the moisture content of the grains during drying reaches a predetermined value.
Since the heating drying claw is variable, even if the first l is of the same type, there is a difference in the time from the start of drying until the predetermined moisture content is reached due to the phase 3U of initial moisture content. As a result, there is a lot of variation in the time it takes to transition from drying using the initially set heat trace to drying using a hot air temperature that is varied depending on the characteristics of the grain to be dried, making it difficult to achieve efficient drying. There was a problem that not only was the operation rotational, but it was also impossible to eliminate causes of grain quality deterioration such as shell cracking. Furthermore, there was another problem in that the combustion condition of the barb combustion system of the dryer became unstable due to the sudden change in the initially set hot air temperature.
[[1的1
従って本発明は従来の技術の」−記問題点を改善J−る
もので、ぞの目的(、土、胴割れ等の穀粒の品質低小の
原因を除去刃ることが可能で能率的な乾燥作業を行イ1
うことがC′き、乾燥機のバーナ燃焼系の燃焼状態が不
安定に4Tることを−b防+1′!lることが可能イf
穀物乾燥機を提供することにある。[[1] Therefore, the present invention aims to improve the problems described in the prior art, and its purpose is to eliminate causes of poor grain quality such as soil and shell cracks. It is possible to carry out efficient drying work.
-b +1' to prevent the combustion state of the burner combustion system of the dryer from becoming unstable by C'! It is possible to
Our goal is to provide grain dryers.
[構成]
−に記目的を達成覆るだめの本発明の特徴は、被乾燥穀
粒の乾燥機内への張込量及び該穀粒の種類に応じて熱J
!lil汎1度を設定J−る手段と、穀粒の種類や特質
に応じて設定された複数の熱風温m顧データを記憶する
記憶手段と、乾燥機内の実際熱風温度を検知する手段と
を有し、乾燥作業開始から所定時間が経過したことを認
識したときに、熱J前温度設定手段によって設定された
第1の熱風温度設定値を前記データの中から被乾燥穀粒
の種類や特質に応じて選択した第2の熱風温度設定値に
切換えるとともに、該第2の熱風温度設定値を目標値と
して該目標値と前記検知手段から与えられる検出値との
差分を演詐()該差分を徐々に解消りべく燃焼制御を行
なう演算手段を説()たごとき穀物乾燥機にある。[Configuration] A feature of the present invention is that the covering vessel achieves the object described in -.
! A means for setting a temperature of 1 degree, a storage means for storing a plurality of hot air temperature measurement data set according to the type and characteristics of grain, and a means for detecting the actual hot air temperature in the dryer. When it is recognized that a predetermined time has elapsed since the start of the drying operation, the first hot air temperature setting value set by the preheating temperature setting means is determined based on the type and characteristics of the grain to be dried from the data. The second hot air temperature setting value is switched to the second hot air temperature setting value selected according to the second hot air temperature setting value, and the difference between the target value and the detected value given by the detection means is calculated using the second hot air temperature setting value as the target value. A calculation means for controlling combustion to gradually eliminate the problem is found in the grain dryer.
し作用]
上記のごとき構成におい−C1乾燥作業開始時に穀粒の
乾燥機内への張込量及び該穀粒の種類に応じて初期nQ
定しl〔熱風温度を第1の目標値として熱風温度制御を
行なう。これとどもに乾燥作業開始時から所定時間経過
後は穀粒の種類、特質に応じて設定されている検数の熱
風温度値データの中から被乾燥穀粒の種類、特質に応じ
た1つのデータを選択し、該選択した熱風温rα値を第
2の目標faとして検出値との差分を演算し該差分を次
第に小さくJ−るようにして乾燥作業を継続するもので
ある。Initial nQ according to the amount of grain loaded into the dryer and the type of grain at the start of the C1 drying operation]
[Hot air temperature control is performed with the hot air temperature as the first target value. In both cases, after a predetermined period of time has elapsed from the start of the drying operation, one set of hot air temperature values according to the type and characteristics of the grains to be dried is selected from among the hot air temperature value data of the number set according to the type and characteristics of the grains. The drying operation is continued by selecting the data, calculating the difference from the detected value using the selected hot air temperature rα value as the second target fa, and making the difference gradually smaller.
[実施例] 以下図面により本発明の詳細な説明1−る。[Example] The following is a detailed explanation of the present invention with reference to the drawings.
第1図は本発明の第1へ・第4の実施例に従う穀物乾燥
機の全体斜視図、第2図は本発明の第1〜第4の実施例
に従うブロック図、第3図は本発明の第1〜第4の実施
例に従う穀物乾燥機の熱風温度値をパラメータとして成
立覆る乾燥時間と含水率との関係を示した図、第4図、
第5図は本発明の第4の実施例に従う穀物乾燥機の熱風
温度の制御方法示した図である。FIG. 1 is an overall perspective view of a grain dryer according to the first to fourth embodiments of the present invention, FIG. 2 is a block diagram according to the first to fourth embodiments of the present invention, and FIG. 3 is a block diagram according to the first to fourth embodiments of the present invention. FIG. 4 is a diagram showing the relationship between drying time and moisture content established using the hot air temperature value of the grain dryer as a parameter according to the first to fourth embodiments.
FIG. 5 is a diagram illustrating a method of controlling the hot air temperature of a grain dryer according to a fourth embodiment of the present invention.
まず本発明に従う第1の実施例について説明する。First, a first embodiment according to the present invention will be described.
第1図において、乾燥機1は図示しない]シト1−1−
ルユニツトを内蔵する操作ボックス3と、バーナ燃焼系
5とを有している。操作ボックス3はバーナ燃焼系5へ
の燃別供給吊を複数段階に設定するだめの燃料設定装置
7、調節完了スイッチ9、乾燥I!1内に外気通風を供
給するノアンの回転数を調節づるフン7ン調節装置11
、調節ランプ13、及び乾燥スイッチ、張込量スイツブ
=、穀物種類スイッチ、目標含水率設定スイッチ等の操
作スイッチ15を備えCいる、1
バーナ燃焼系5は、乾燥機1の機壁に取りイ1()られ
た燃¥31タンク17、該タンク17と電磁ポンプ19
及び電磁バルブ21を介して燃焼室23と連通ずる燃l
il管25、及び7ノ・ン(図示しない)等の外気通J
虱を供給する手段を備え内部に前記燃焼室23を有J−
る通風筒27どで構成されている。In FIG. 1, the dryer 1 is not shown]
It has an operation box 3 containing a burner unit and a burner combustion system 5. The operation box 3 includes a fuel setting device 7 for setting fuel supply to the burner combustion system 5 in multiple stages, an adjustment completion switch 9, and a drying I! 7 A fan adjustment device 11 that adjusts the rotation speed of the noan that supplies outside air ventilation into the interior of the 1
, an adjustment lamp 13, and operation switches 15 such as a drying switch, a loading amount switch, a grain type switch, and a target moisture content setting switch. 1() Fuel ¥31 tank 17, said tank 17 and electromagnetic pump 19
and a fuel tank communicating with the combustion chamber 23 via the electromagnetic valve 21.
Outside air vents such as il pipe 25 and 7 (not shown)
The combustion chamber 23 is provided with a means for supplying lice and has the combustion chamber 23 inside.
It is composed of a ventilation tube 27 and the like.
前記電磁ポンプ19又は電磁バルブ21は少なくともそ
のいずれか1方が前記二」ン1へロールコニツ(へ〈図
示しない)から出力される燃料供給量制御パルス信号に
よって開/閉駆動され燃料タンク17から流入する燃料
量を制御する。本発明に従う実施例においては、後述J
るように電磁バルブ21の方を所謂Aンタイム制御Jる
ことどしl、:、。At least one of the electromagnetic pump 19 and the electromagnetic valve 21 is driven to open/close by a fuel supply amount control pulse signal outputted from a roll tank (not shown) to the second tank 1, so that fuel flows from the fuel tank 17. control the amount of fuel used. In embodiments according to the present invention, J
The electromagnetic valve 21 is controlled by so-called A-time control so that the electromagnetic valve 21 is controlled.
第2図は前)ホした操作ボックス3に内蔵されている二
]ン]ヘロールコニットのブ[1ツク図を示したもので
、マイクロコンビコータtot、t、cpui 。FIG. 2 shows a block diagram of the second Herolconit built in the operation box 3 mentioned above.
1、メモリ103、入カポ−1へ105、入カポ−1−
107、出カポ−1へ108、出カポ−+−,109を
右覆る。1, memory 103, input capo-1 105, input capo-1-
107, turn to the output capo-1 108, turn the output capo-+-, 109 to the right.
CP U 101は、算術論理演綽及び比較演締を行な
う。CPU101の入力情報は、デジイタル入力回路!
′59、入力ボート105及びA/D変換回路61、入
力ボート107を介しで!−Jえられる。The CPU 101 performs arithmetic and logical operations and comparison operations. The input information of the CPU 101 is a digital input circuit!
'59, via input port 105, A/D conversion circuit 61, and input port 107! -J can be obtained.
デジイタル入力回路59を介してCPU101にりえら
れる情報には乾燥目標温度設定情報即ち熱風温1σ設定
情報63、安全センザ情報65、操作情報67がある。Information sent to the CPU 101 via the digital input circuit 59 includes drying target temperature setting information, that is, hot air temperature 1σ setting information 63, safety sensor information 65, and operation information 67.
熱風温を良設定情報(王C)63は、乾燥機1内の穀粒
循環系(図示しない)を循環Jる被乾燥穀粒の種類及び
張込量に応じて目盛をヒラ1〜Jることで(]標熱風渇
庶(T C>が自動的に設定される目標熱風温石設定ツ
マミ69から出力される。安全レンリ゛情報65は、例
えば]レベータモータ、上部ラセン、ロータリバルブ及
び−7=
下部ラセン等乾燥機駆動系の駆動状況を検出りる駆動系
安全レンリ一群71ど、点火ヒータ、燃11供給ポンプ
([”J] 15電磁ポンプ)等乾燥機燃焼系の駆動状
況を検出りる燃焼系安仝]?ンリ群73どから出力され
る。操作情報67 (J、乾燥(幾七−タの起動/停止
にや点火等をtJ”ehつたり目標含水率の61!定等
を行イ1うための操作スイッチ15から与えられる。The hot air temperature setting information (K) 63 sets the scale from 1 to 1 according to the type and amount of grains to be dried that circulate through the grain circulation system (not shown) in the dryer 1. Therefore, the target hot air temperature setting knob 69 automatically sets the target hot air temperature (TC). = Detects the driving status of the dryer drive system such as the lower spiral drive system.Detects the driving status of the dryer combustion system such as the ignition heater, fuel 11 supply pump (["J] 15 electromagnetic pump), etc. The operation information 67 is output from the combustion system safety group 73. It is given from the operation switch 15 for performing the following steps.
A/D変換回路11を介しでCP t、J 101にh
えられる情報には、乾燥機内実際温度検出センザ即ち熱
用渇庶検出しンリ−79から出力される乾燥機1内の実
際熱Jiiil湿度(T13)情報81ど、外気温度検
出センリ−83から出力される外気温度(1A)情報8
5及び自動水分品187から出力される穀粒の含水率情
報89どがある。CP t, h to J 101 via A/D conversion circuit 11
The information that can be obtained includes the actual heat and humidity (T13) information 81 in the dryer 1 outputted from the dryer 1 actual temperature detection sensor, that is, the heat exhaustion detection sensor 79, and the output from the outside air temperature detection sensor 83. Outside air temperature (1A) information 8
5 and grain moisture content information 89 output from the automatic moisture product 187.
CPU101から与えられる乾燥機燃焼系の駆動指令信
号は、出カポ−1〜109、j゛シイタル出力回路11
1を介しC燃料供給ポンプ19、燃わ1供給電磁バルブ
21、気化筒モータ37の駆動回路(図示しくくい)と
点火ヒータ35へ各々与えられる。CI” tJ 1
n 1から与えられる乾燥機駆動系の駆動指令信号は、
アナログ出力回路113を介しくファンモータ29の駆
動回路(図示しない)へLjλられる。The drive command signal for the dryer combustion system given from the CPU 101 is sent to the output ports 1 to 109 and the output circuit 11.
1 to a C fuel supply pump 19, a fuel 1 supply solenoid valve 21, a drive circuit (not shown) for a carburetor motor 37, and an ignition heater 35, respectively. CI” tJ 1
The drive command signal for the dryer drive system given from n1 is:
Ljλ is applied to the drive circuit (not shown) of the fan motor 29 via the analog output circuit 113.
メ[す103は制御プログラム等を内蔵し、又必要デー
タを記憶づる。メ14す103が記憶づるデータは、例
えば第3図に−C図示J−るごとき乾燥作業開始から所
定時間が経過したときに穀粒のトド類、特質tこ応じて
複数設定され夫々残りの乾燥時間が選択的に決定される
熱風温電値をパラメータどしたデータがある。The computer 103 contains control programs and the like, and also stores necessary data. A plurality of data stored in the main 103 are set when a predetermined period of time has elapsed from the start of the drying operation, as shown in FIG. There is data that uses the hot air thermoelectric value as a parameter to selectively determine the drying time.
CPtJ 101は、以下に述べる機能を有づる。CPtJ 101 has the functions described below.
■11標熱川濯痘設定ツマミ69から出力されIC被乾
燥穀粒の種類及び張込量に基づく目標熱風温i設定情報
(TC)63をデジイタル入力回路59、入力ボート1
05を介して取り込み、該情報をメモリ103に格納す
る。■熱m渇度検出1?ンη79から出力された実際熱
用濡度(T13)情11j81をA / D変換回路6
1、入力ボート107を介しで取り込む。■外気温)α
検出センザ83から出力された外気温度(1△)情報8
5を△/l′)変換回路61、入力ボート107を介し
く取り込む。■■で取り込んだ実際熱fqn温度(丁1
3 >情報81と■で取り込/υだ目標熱風温1a設定
情報(10)63との間の差温をTC−1’rl)t’
>式を用いて演算する。■乾燥作業開始から所定時間が
経過したことを認識づると被乾燥穀粒の)・ト類、特質
に応じてメモリ103に惰納されている前記複数の熱風
温度値データ(第3図にで図示)の中から1つを)買択
し、以後は該選択に基づいた熟思温石制御に移行する。■Target hot air temperature i setting information (TC) 63 outputted from the 11-marked Atagawa irrigation setting knob 69 and based on the type and amount of IC dried grains is input to the digital input circuit 59 and input boat 1.
05 and stores the information in the memory 103. ■Heat m thirst detection 1? The actual thermal wetness (T13) information 11j81 output from the input η79 is sent to the A/D conversion circuit 6.
1. Import via input port 107. ■Outside temperature) α
Outside air temperature (1△) information 8 output from the detection sensor 83
5 is taken in via the Δ/l′) conversion circuit 61 and the input port 107. Actual heat fqn temperature taken in ■■ (dou1
3 >Receive the difference temperature between information 81 and ■/υ target hot air temperature 1a setting information (10) 63 TC-1'rl)t'
> Calculate using the formula. ■When it is recognized that a predetermined period of time has passed since the start of the drying operation, the plurality of hot air temperature value data stored in the memory 103 (as shown in Fig. 3) are One of them (as shown) is selected, and from then on, the contemplation stone control is performed based on the selection.
これにより乾燥作業開始時に設定された乾燥時間は可変
される。■■で)パ択しlこ熱風温度値を目標値として
該目標値と熱風温石検出センリフ9から出力される消石
情報(7[3)81との2G分を逐次演算し、該演枠結
果に基づいて燃料供給電磁バルブ21へ出力する制御パ
ルス信号のAンタイム時間幅、ファンモータ29への駆
動指令信号を可変する1゜
上記構成の制御動作を1に第3図を(J1川して説明す
る。This allows the drying time set at the start of the drying operation to be varied. )) Select the hot air temperature value as the target value, and sequentially calculate 2G of the target value and the stone quenching information (7 [3) 81 output from the hot air hot stone detection sensor 9, and Based on the result, the A time width of the control pulse signal output to the fuel supply electromagnetic valve 21 and the drive command signal to the fan motor 29 are varied. I will explain.
乾燥作業開始に先立ち、Aペレータは被乾燥穀粒の種類
及び張込珀に従って目標熱風温度設定ツマミ69を所定
の11盛にレツ]〜覆る。CI”UIOlは、該設定ツ
マミ69からちえられる( T C’)設定情報63ど
操vIスイッヂ15から点火に閉覆る操作情報67が与
えられたことを認識りるとこれら情報に基づいて燃r1
供給電磁バルブ21に出力Jる制御パルス信号のAンタ
イノ\時間幅を可変Jる。、 CP jJ 101は、
熱風温度検出センサ79からりえられる実際熱[1(1
F3)情報81を逐次取り込み前記(1−C)設定情報
63との比較波0に基づいて?Tj磁バルブ21に出力
する制御パルス(:i ’l”jのAンタイム時間幅を
調整する。このようにL/て乾燥作業開始時から予め設
定された所定時間が経過するまでの間、CPU101は
乾燥作業開始時に設定された(王C)設定情報63を目
標値として熱風温石制御を継続Jる。CPU101は、
前記所定時間が経過したことを認識Jるとメモリ103
より第3図にて図示するごとぎ熱風温度値をパラメータ
どしたデータを呼び出刃。C= 11−
PUlolは、被乾燥穀粒の種類、特質等に応じて熱風
温石曲線■、■、■、■、・・・の中からいずれか1つ
の曲線を選択覆る。例えば被乾燥穀粒が特に)1割れし
やJい籾であるときは曲線■、胴割れじゃづい籾である
ときは曲線■、y1通の籾であるときは曲線■、胴割れ
しにくい籾であるとさは曲線■を夫々選択りることとな
る。前記■〜■の曲線中、最も熱J@温麻が低く乾燥時
間の良いものは曲線■て・あり、最も熟思温度が高く乾
燥時間の短いものは曲線■である。Prior to the start of the drying operation, the A pelleter turns the target hot air temperature setting knob 69 to a predetermined number of 11 according to the type of grain to be dried and the amount of grain to be dried. When the CI"UIOL recognizes that the operation information 67 for closing the ignition has been given from the setting knob 69 (TC') setting information 63 and the I switch 15, it sets the ignition r1 based on this information.
The time width of the control pulse signal output to the supply electromagnetic valve 21 is variable. , CP jJ 101 is
The actual heat received from the hot air temperature detection sensor 79 [1 (1
F3) Sequentially import the information 81 and compare it with the setting information 63 (1-C) Based on wave 0? The A time width of the control pulse (:i'l"j) output to the Tj magnetic valve 21 is adjusted. In this way, the CPU 101 The hot air heating stone control is continued using the (King C) setting information 63 set at the start of the drying work as the target value.The CPU 101
When it is recognized that the predetermined time has elapsed, the memory 103
Then call up the data with the hot air temperature value as a parameter as shown in Figure 3. C=11-PUlol selects and covers any one of the hot air hot stone curves ■, ■, ■, ■, . . . depending on the type, characteristics, etc. of the grain to be dried. For example, if the grains to be dried are (particularly) 1-split or J-shaped paddy, the curve ■, when the paddy is cracked, the curve ■, and when the paddy is y1, the curve ■, and the paddy that is difficult to crack. Therefore, each curve ■ is selected. Among the curves (■) to (■) above, the one with the lowest temperature and the best drying time is the curve (■), and the one with the highest contemplation temperature and the shortest drying time is the curve (■).
cpuiolは子連しIこ曲線■〜■の中から1つの曲
線を選択した後は、該曲線が示づ熱J虱温亀11iを目
標伯として熱風乾燥作業を継続することとなる。即ち乾
燥作業がダ1;了づるまでの間は検出センサ79から与
えられる熱P@温湿度 T B )情報81を前記目標
値に徐々に一致させるべく電磁バルブ21へ出力する制
御パルス信号のAンタイム時間幅を可変Jることとなる
。After cpuiol selects one curve from among the child curves (1) to (2), it continues the hot air drying operation with the heat temperature 11i indicated by the selected curve as the target value. That is, until the drying operation is completed, the heat P@temperature/humidity T B) provided from the detection sensor 79 is controlled by the control pulse signal A output to the electromagnetic valve 21 in order to gradually bring the information 81 into agreement with the target value. This means that the duration of the run time will be variable.
以上説明しlこ」、うに本発明に(Iう第1の実施例に
よれば、被乾燥穀粒の乾燥機内への張り込み時に該穀粒
の張込1や種類に応じて自動的に熱風温石が初Jll
iiQ定され乾燥作業開始から所定時間の経過とともに
、前記初期設定された熱風温度値が該穀粒のfφ類、特
質に応じた別の熱風温度値に切換えられ、該切換えられ
た温度値を目標値として徐々に実際熱風温石を目標値に
近づ(づるべく燃焼制御をすることとしたので、Aペレ
ータが手間のかかる熱風温度設定をJる必要のない乾燥
機を提供することがぐきる。According to the first embodiment of the present invention, when the grains to be dried are loaded into the dryer, hot air is automatically Atsushi's first Jll
iiQ is determined and as a predetermined time elapses from the start of drying work, the initially set hot air temperature value is switched to another hot air temperature value according to the fφ type and characteristics of the grain, and the switched temperature value is set as the target. Since the combustion control is performed so that the actual hot air temperature gradually approaches the target value, it is possible to provide a dryer that does not require the operator A to set the hot air temperature, which is a time-consuming process.
次に本発明に従う第2の実施例について説明する。本実
施例と前記第1の実施例との相違は、切換λ後の熱風温
度値を目標値とし該目標値に実際熱風温麿値を一致せ1
〕めるべく自動水分計87から逐次与えられる含水率情
報89に基づいてCPU 101が徐々に燃焼制御を覆
る点にある。Next, a second embodiment according to the present invention will be described. The difference between this embodiment and the first embodiment is that the hot air temperature value after switching λ is set as a target value, and the actual hot air temperature value is made to match the target value.
] The CPU 101 gradually overrides the combustion control based on the moisture content information 89 sequentially provided from the automatic moisture meter 87.
本発明に従う第3の実施例についで説明する。A third embodiment according to the present invention will now be described.
本実施例においては、CPU101が前記第2の実M1
例にillノる自動水分a187から−ljえられる含
水率情報89のバラツキを補正するために、所定時間内
に与えられる複数の含水率情報89の平均値をIHるこ
とどしたものである。In this embodiment, the CPU 101 controls the second real M1.
For example, in order to correct variations in the moisture content information 89 obtained from the automatic moisture content a 187, the average value of a plurality of moisture content information 89 given within a predetermined period of time is calculated as IH.
上記のごとぎ平均値を演n′?Iるブj法どしては、例
えば移動平均払や以下に説明りる一1I7フイルタ法な
どがある。−峙フィルタ法(五ノズ下のごとき粋式によ
って行41わねる。Operate the average value as above n'? Examples of such methods include the moving average payment method and the 11I7 filter method described below. - Vertical filter method (row 41 is twisted according to the style of Gonozu Shita).
1Jsn =4Ms (n−1) 十Msn15Ms
n:n回]]の測定顧にj、る61棹含水率is (
n−1) :n −1回「1(前回)の泪紳含水率
Msn:n回目の測定(171
n’=1.2.3.・・・
MS + =MS +
すなわちCPLJlolは、−1記h10含水率と、前
記第1の実施例で設定された切換え後の熱I!@温度曲
線■〜■によって決定される含水率どの2イ・分を求め
、該差分を解消Jべく実際熱温度を徐々に設定熱風温度
曲線に近づ(〕るべく燃焼制υ11を行なうものである
。1Jsn =4Ms (n-1) 1Jsn15Ms
n: n times]
n-1): n -1 times "1 (previous) water content Msn: nth measurement (171 n' = 1.2.3... MS + = MS + That is, CPLJlol is -1 Calculate the water content determined by the water content and the heat after switching set in the first embodiment and calculate the actual heat in order to eliminate the difference. Combustion control υ11 is performed in order to gradually bring the temperature closer to the set hot air temperature curve.
本発明に従う第4の実施例について説明Jる。A fourth embodiment according to the present invention will be explained.
本実施例においては第4図及び第5図に(図示するごど
く切換え後の熱風)温度値を目標値どじで実際熱風温度
を該目標値に近づ【−」るべく燃焼制御を行むうに際し
て切換え後の熟思d1配度曲線■〜■によって決定さ4
する含水率と測定含水率との差分を求め、該差分を解消
Jべく実際熱風温度を自動水分6187が含水率を測定
する毎に熱風温度に関しCはt2°C稈庶、燃料供給量
に関しでは数m女程石の微小な補正を行trうことどし
たしめである1゜L記のごとく燃焼制御を行なうことに
よって、急激イr熟思渇[真の可変にj、つ(牛づ゛る
バーナ燃焼系のハンチングを防11て゛きる。In this embodiment, combustion control is performed to bring the actual hot air temperature closer to the target value, as shown in FIGS. 4 and 5 (hot air after switching as shown). 4 determined by the d1 distribution curve ■~■ after switching.
Calculate the difference between the measured moisture content and the measured moisture content, and calculate the actual hot air temperature to eliminate the difference.Each time the automatic moisture 6187 measures the moisture content, the hot air temperature is t2°C, and the fuel supply amount is t2°C. By controlling the combustion as described in 1.L, which involves making a small correction of several meters, it is possible to reduce sudden irritation and thirst. 11 ways to prevent hunting in the burner combustion system.
1効宋]
以上説明【ノたJ、うに本発明によれば、第2の熱線渦
電設定値を1]標値としC該目標伯ど検出された実際熱
風温度値どの7分を演伸し該差分を徐々に′M潤すべく
燃焼制御を行なうことどしたので、胴割れ等穀粒の品質
低下の[1ハ囚を除去りることが可能で能キ的へ乾燥作
業を行なうことができ、しかb乾燥機のバーブ燃焼系の
燃焼状態が不安定にイすることb防1に可能な穀物乾燥
機を提供づることができる。According to the present invention, the second hot-ray eddy current setting value is set as the target value, and the detected actual hot air temperature value is calculated based on the target value. However, by controlling the combustion to gradually moisten the difference, it is possible to remove the problems that cause grain quality deterioration, such as cracking, and to efficiently carry out drying work. However, it is possible to provide a grain dryer that can prevent the combustion state of the barb combustion system of the dryer from becoming unstable.
第1図は本発明の第1〜第4の実施例(3」Yう穀物乾
燥機の全体斜視図、第2図は本発明の第1・〜第4の実
施例に従うブ[]ツク図、第3図は本発明の第1〜第4
の実施例に従う穀物乾燥機の熱風温度値をパラメータと
して成立する乾燥■)間と含水率との関係を示した図、
第4図、第5図は本発明の第4の実施例に従う穀物乾燥
機の熱風温石の制御方法を示した図である。
1・・・穀物乾燥機 2つ・・・ファンモータ
21・・・燃lit供給電口1バルブ
69・・・目標熱風温度設定 101・・・C[)(j
ツマミ 103・・・メ]モリ79・・・
熱風温石検出セン→ノ
16一FIG. 1 is an overall perspective view of a grain dryer according to the first to fourth embodiments (3) of the present invention, and FIG. 2 is a block diagram of a grain dryer according to the first to fourth embodiments of the present invention. , FIG. 3 shows the first to fourth embodiments of the present invention.
A diagram showing the relationship between drying time (■) and moisture content, which is established using the hot air temperature value of the grain dryer as a parameter according to the example of
FIGS. 4 and 5 are diagrams showing a method for controlling hot air heating stones in a grain dryer according to a fourth embodiment of the present invention. 1...Grain dryer 2...Fan motor 21...Fuel lit power supply port 1 valve 69...Target hot air temperature setting 101...C[)(j
Knob 103... Memo 79...
Hot air warm stone detection sensor→No.161
Claims (1)
じて熱風温度を設定する手段と、穀粒の種類や特質に応
じて設定された複数の熱風温度値データを記憶する記憶
手段と、乾燥機内の実際熱風温度を検知する手段とを有
し、乾燥作業開始から所定時間が経過したことを認識し
たときに、熱風温度設定手段によって設定された第1の
熱風温度設定値を前記データの中から被乾燥穀粒の種類
や特質に応じて選択した第2の熱風温度設定値に切換え
るとともに、該第2の熱風温度設定値を目標値として該
目標値と前記検知手段とから与えられる検出値との差分
を演算し該差分を徐々に解消すべく燃焼制御を行なう演
算手段を設けたことを特徴とする穀物乾燥機。Means for setting the hot air temperature according to the amount of grain to be dried in the dryer and the type of the grain, and storing a plurality of hot air temperature value data set according to the type and characteristics of the grain. The first hot air temperature setting value is set by the hot air temperature setting means when it is recognized that a predetermined time has elapsed from the start of the drying operation, the first hot air temperature setting value having a storage means and a means for detecting the actual hot air temperature in the dryer. is switched to a second hot air temperature setting value selected from the data according to the type and characteristics of the grain to be dried, and the second hot air temperature setting value is set as a target value and the target value and the detection means are 1. A grain dryer, characterized in that a calculation means is provided for calculating a difference between a detected value given by a value and a combustion control to gradually eliminate the difference.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59119768A JPH0633936B2 (en) | 1984-06-13 | 1984-06-13 | Grain dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59119768A JPH0633936B2 (en) | 1984-06-13 | 1984-06-13 | Grain dryer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS611987A true JPS611987A (en) | 1986-01-07 |
| JPH0633936B2 JPH0633936B2 (en) | 1994-05-02 |
Family
ID=14769710
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59119768A Expired - Lifetime JPH0633936B2 (en) | 1984-06-13 | 1984-06-13 | Grain dryer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0633936B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62206374A (en) * | 1986-03-04 | 1987-09-10 | 株式会社山本製作所 | Method of controlling drying of circulation type cereal drier |
| JPS63176988A (en) * | 1987-01-19 | 1988-07-21 | 金子農機株式会社 | Cereal drying control method |
| CN115672688A (en) * | 2022-11-16 | 2023-02-03 | 广州瑞松北斗汽车装备有限公司 | Drying control method and device for workpiece colloid, terminal equipment and medium |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS55123980A (en) * | 1979-03-16 | 1980-09-24 | Satake Eng Co Ltd | Automatic controller for grain drier |
| JPS5828975A (en) * | 1981-08-12 | 1983-02-21 | 辰本 韶弘 | Cereal drier |
| JPS5872873A (en) * | 1981-10-24 | 1983-04-30 | 辰本 韶弘 | Control system of drying of circulation type cereal drier |
| JPS58193082A (en) * | 1982-05-06 | 1983-11-10 | 辰本 韶弘 | Method of controlling hot air in cereal drier |
-
1984
- 1984-06-13 JP JP59119768A patent/JPH0633936B2/en not_active Expired - Lifetime
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS55123980A (en) * | 1979-03-16 | 1980-09-24 | Satake Eng Co Ltd | Automatic controller for grain drier |
| JPS5828975A (en) * | 1981-08-12 | 1983-02-21 | 辰本 韶弘 | Cereal drier |
| JPS5872873A (en) * | 1981-10-24 | 1983-04-30 | 辰本 韶弘 | Control system of drying of circulation type cereal drier |
| JPS58193082A (en) * | 1982-05-06 | 1983-11-10 | 辰本 韶弘 | Method of controlling hot air in cereal drier |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62206374A (en) * | 1986-03-04 | 1987-09-10 | 株式会社山本製作所 | Method of controlling drying of circulation type cereal drier |
| JPS63176988A (en) * | 1987-01-19 | 1988-07-21 | 金子農機株式会社 | Cereal drying control method |
| CN115672688A (en) * | 2022-11-16 | 2023-02-03 | 广州瑞松北斗汽车装备有限公司 | Drying control method and device for workpiece colloid, terminal equipment and medium |
| CN115672688B (en) * | 2022-11-16 | 2023-12-19 | 广州瑞松北斗汽车装备有限公司 | Drying control method and device for workpiece colloid, terminal equipment and medium |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0633936B2 (en) | 1994-05-02 |
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