JP2010271021A - Exhaust air circulating type grain drier - Google Patents

Exhaust air circulating type grain drier Download PDF

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JP2010271021A
JP2010271021A JP2009125752A JP2009125752A JP2010271021A JP 2010271021 A JP2010271021 A JP 2010271021A JP 2009125752 A JP2009125752 A JP 2009125752A JP 2009125752 A JP2009125752 A JP 2009125752A JP 2010271021 A JP2010271021 A JP 2010271021A
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exhaust air
grain
drying
control
air circulation
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JP5428530B2 (en
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Eiji Nishino
栄治 西野
Naoki Mukoyama
直樹 向山
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Iseki and Co Ltd
Iseki Agricultural Machinery Mfg Co Ltd
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Iseki and Co Ltd
Iseki Agricultural Machinery Mfg Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a grain drier capable of efficiently promoting moisture equalization by keeping predetermined grain temperature while suppressing sweating of grain, in a case that the grain drier is stopped and kept in a predetermined high-temperature state by a resting process in grain dry processing by exhaust air circulation. <P>SOLUTION: The exhaust air circulating type grain drier includes a control part (F) which carries out exhaust air circulation drying control for making exhaust air diverge to the circulation side by switching valves (22, 23) and circulating the air in a grain drying part (3) to dry the grain by an exhaust air circulation ratio according to a detected moisture value of the grain, and drying resting control for stopping the grain drying if the detected moisture value reaches a separately-set resting reference moisture value. The control part (F) gradually opens the switching valves (22, 23) until all the air is exhausted in a predetermined moisture value range until the detected moisture value in the exhaust air circulation drying control reaches the resting reference moisture value, gradually decreases the exhaust air circulation ratio at predetermined speed, and then, carries out the drying resting control. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

本発明は、排風ダクトから分流した排風を還流ダクトによって穀物乾燥部に還流して穀粒等の排風循環乾燥を行う排風循環式穀物乾燥機に関するものである。   The present invention relates to an exhaust air circulation type grain dryer that performs exhaust air circulation drying of grains and the like by returning exhaust air diverted from an exhaust air duct to a grain drying section by a reflux duct.

特許文献1の例の如く、穀物乾燥部の排風を排出する排風ダクトから排風の一部を分流し、還流ダクトによって穀物乾燥部に還流することにより、熱風供給部による熱風とともに混合供給して排風循環乾燥を行う排風循環式穀物乾燥機が知られている。
この排風循環式穀物乾燥機は、水分計による穀物水分値に応じて排風の一定率を循環することにより、熱風排出に伴う加熱ロスを抑えつつ、所定の穀物乾燥速度によって穀物品質を確保しつつ効率よく穀物乾燥運転をすることができる。
As in the example of Patent Document 1, a part of the exhaust air is diverted from the exhaust duct that exhausts the exhaust air of the grain drying section, and is returned to the grain drying section by the reflux duct, thereby being mixed and supplied together with hot air from the hot air supply section. An exhaust air circulation type grain dryer that performs exhaust air circulation drying is known.
This exhaust air circulation type grain dryer ensures the quality of the grain at a predetermined grain drying speed while circulating a constant rate of exhaust air according to the moisture content of the grain measured by the moisture meter, while suppressing heating loss associated with hot air discharge. In addition, the grain drying operation can be performed efficiently.

また、乾燥ムラがある場合は、穀物乾燥機を停止してある程度の高温状態に保持する休止工程を設けることにより、穀粒相互間の水分移行を促して水分値を均一化することができる。   In addition, when there is unevenness in drying, by providing a pause process in which the grain dryer is stopped and kept at a certain high temperature, moisture transfer between grains can be promoted and the moisture value can be made uniform.

特開2008−224199号公報JP 2008-224199 A

しかしながら、排風循環によって高速乾燥を行っている間は穀物表面が高温高湿の状態であることから、いきなり休止工程に移行すると穀物が蒸れることがあり、これを避けるために通風を行うと穀温の低下を招き、効果的な水分移行が抑えられて乾燥ムラが解消されないという問題があった。   However, during high-speed drying by exhaust air circulation, the grain surface is in a high temperature and high humidity state. There was a problem that the temperature was lowered, effective moisture transfer was suppressed, and drying unevenness was not solved.

本発明の目的は、排風循環による穀物乾燥処理における休止工程により穀物乾燥機を停止してある程度の高温状態に保持する場合において、穀物の蒸れを抑えつつ、所定の穀温を維持することにより、効率よく水分均一化を促すことができる穀物乾燥機を提供することにある。   An object of the present invention is to maintain a predetermined grain temperature while suppressing the steaming of grains when the grain dryer is stopped and held at a certain high temperature by a pause process in the grain drying process by exhaust air circulation. An object of the present invention is to provide a grain dryer that can efficiently promote uniform moisture.

請求項1に係る発明は、熱風によって穀物を乾燥する穀物乾燥部(3)から排出された排風を切替弁(22,23)により循環側に分流し、この分流排風を穀物乾燥部(3)に循環して穀物乾燥をする排風循環乾燥制御と、この排風循環乾燥制御における検出する穀物水分値が別途設定の休止基準水分値に達すると穀物乾燥を停止する乾燥休止制御とを行う制御部(F)を備える排風循環式穀物乾燥機において、上記制御部(F)は、排風循環乾燥制御における検出水分値が休止基準水分値に到達するまでの所定の水分値範囲について切替弁(22,23)を全排出まで徐々に開いて排風循環率を所定速度で漸減させた後に乾燥休止制御を行うことを特徴とする。   The invention according to claim 1 divides the exhaust air discharged from the grain drying section (3) for drying the grains with hot air to the circulation side by the switching valve (22, 23), and the diverted exhaust air is separated into the grain drying section ( 3) Exhaust air circulation drying control that circulates and drys the grain, and drying pause control that stops grain drying when the grain moisture value detected in the exhaust wind circulation drying control reaches a separately set pause reference moisture value. In the exhaust air circulation type grain dryer provided with the control part (F) to perform, the said control part (F) is about the predetermined | prescribed moisture value range until the detected water value in exhaust air circulation drying control reaches a rest reference | standard water value. The switching valve (22, 23) is gradually opened to full discharge, and the exhaust air circulation rate is gradually decreased at a predetermined speed, and then drying stop control is performed.

上記排風循環式穀物乾燥機は、制御部により、検出する穀物水分値が休止基準水分値の近傍の所定の水分値に到達すると排風循環率が所定速度で漸減し、休止基準水分値に到達すると排風の全排出動作をするとともに穀物乾燥動作を停止する。   In the exhaust air circulation type grain dryer, when the grain moisture value to be detected reaches a predetermined moisture value in the vicinity of the pause reference moisture value, the exhaust wind circulation rate gradually decreases at a predetermined speed by the control unit, and becomes the pause reference moisture value. When reaching, the exhausting operation of the exhaust air is performed and the grain drying operation is stopped.

請求項2に係る発明は、熱風によって穀物を乾燥する穀物乾燥部(3)から排出された排風を切替弁(22,23)により循環側に分流し、この分流排風を穀物乾燥部(3)に循環して穀物乾燥をする排風循環乾燥制御と、この排風循環乾燥制御における経過時間が別途設定の休止基準時刻に達すると穀物乾燥を停止する乾燥休止制御とを行う制御部(F)を備える排風循環式穀物乾燥機において、上記制御部(F)は、排風循環乾燥制御における経過時間が休止基準時刻に到達するまでの所定の時間範囲について切替弁(22,23)を全排出まで徐々に開いて排風循環率を所定速度で漸減させた後に乾燥休止制御を行うことを特徴とする。   The invention according to claim 2 divides the exhaust air discharged from the grain drying section (3) for drying the grains with hot air to the circulation side by the switching valve (22, 23), and the diverted exhaust air is separated into the grain drying section ( 3) A control unit that performs exhaust air circulation drying control that circulates to dry the grain and drying suspension control that stops grain drying when an elapsed time in the exhaust air circulation drying control reaches a separately set suspension reference time. F) In the exhaust-air circulation type grain dryer provided with F), the said control part (F) is a switching valve (22, 23) about the predetermined time range until the elapsed time in exhaust-air circulation drying control reaches | attains reference | standard time of a stop. Is gradually opened until full discharge, and the exhaust air circulation rate is gradually reduced at a predetermined speed, and then drying suspension control is performed.

上記排風循環式穀物乾燥機は、制御部により、経過時間が休止基準水分値の近傍の所定の時間に到達すると排風循環率が所定速度で漸減し、休止基準時刻に到達すると排風の全排出動作をするとともに穀物乾燥動作を停止する。   When the elapsed time reaches a predetermined time in the vicinity of the pause reference moisture value, the exhaust wind circulation type grain dryer gradually reduces the exhaust wind circulation rate at a predetermined speed, and when the elapsed time reaches the pause reference time, The whole grain is discharged and the grain drying operation is stopped.

請求項3に係る発明は、請求項1または請求項2の構成において、前記制御部は、乾燥休止制御中は、切替弁の排出全閉制御を行うことを特徴とする。
上記排風循環式穀物乾燥機は、排出全閉の切替弁により、外気が遮断される。
According to a third aspect of the present invention, in the configuration of the first or second aspect, the control unit performs a discharge full-closed control of the switching valve during the drying pause control.
In the exhaust air circulation type grain dryer, the outside air is shut off by the switching valve for fully discharging.

請求項1に係る発明の排風循環式穀物乾燥機は、制御部により、検出水分値に応じた排風循環率で排風循環乾燥動作をし、検出水分値が休止基準水分値の近傍の所定の水分値に到達すると排風循環率が所定速度で漸減し、休止基準水分値に到達すると排風の全排出動作をするとともに穀物乾燥動作を停止することから、上記排風循環式穀物乾燥機は、休止基準水分値における穀物乾燥の停止時には、排風の還流による蒸れを抑えつつ、穀温を高く維持することができ、その結果、水分移行を促進して水分斑の均一化を図ることができる。   In the exhaust air circulation type grain dryer according to the first aspect of the invention, the control unit performs the exhaust air circulation drying operation at the exhaust air circulation rate according to the detected moisture value, and the detected moisture value is close to the pause reference moisture value. When the specified moisture value is reached, the exhaust air circulation rate gradually decreases at a predetermined speed, and when reaching the pause reference moisture value, the exhaust air is exhausted and the grain drying operation is stopped. The machine can keep the grain temperature high while suppressing the steaming due to the recirculation of the exhaust air when the grain drying is stopped at the resting standard moisture value. As a result, the moisture transfer is promoted and the moisture spots are made uniform. be able to.

請求項2に係る発明の排風循環式穀物乾燥機は、制御部により、検出水分値に応じた排風循環率で排風循環乾燥動作をし、その経過時間が休止基準水分値の近傍の所定の時間に到達すると排風循環率が所定速度で漸減し、休止基準時刻に到達すると排風の全排出動作をするとともに穀物乾燥動作を停止することから、上記排風循環式穀物乾燥機は、休止基準時刻における穀物乾燥の停止時には、排風の還流による蒸れを抑えつつ、穀温を高く維持することができ、その結果、水分移行を促進して水分斑の均一化を図ることができる。   The exhaust air circulation type grain dryer of the invention according to claim 2 performs the exhaust air circulation drying operation at the exhaust air circulation rate according to the detected moisture value by the control unit, and the elapsed time is in the vicinity of the pause reference moisture value. When the predetermined time is reached, the exhaust air circulation rate gradually decreases at a predetermined speed, and when the reference time is reached, the exhaust air circulation rate is exhausted and the grain drying operation is stopped. When the grain drying is stopped at the stop reference time, the grain temperature can be kept high while suppressing the sultry due to the return of the exhaust air, and as a result, the moisture transfer can be promoted and the moisture spots can be made uniform. .

請求項3に係る発明の排風循環式穀物乾燥機は、請求項1または請求項2の効果に加え、排出全閉の切替弁による外気遮断作用により、乾燥休止中の穀温保持が容易となり、また、外気による水分変動が抑えられる。   In addition to the effect of claim 1 or claim 2, the exhaust air circulation type grain dryer of the invention according to claim 3 makes it easy to maintain the grain temperature during the drying pause due to the outside air shut-off action by the switching valve for fully closing the discharge. In addition, moisture fluctuation due to outside air can be suppressed.

穀物乾燥機の穀物乾燥部の内部構成を説明する透視斜視図Perspective perspective view for explaining the internal configuration of the grain drying section of the grain dryer 穀物乾燥機の穀物乾燥部の内部構成を説明する正面図Front view explaining the internal configuration of the grain drying section of the grain dryer 排風排出部の要部背面斜視図Rear perspective view of the main part of the wind exhaust section 排風排出部の要部縦断面図Longitudinal section of the main part of the wind exhaust section 穀物乾燥部の通風流線を表す作用平面図Action plan view showing ventilation streamlines in grain drying section 乾燥機の動作制御のシステム構成図System configuration diagram of dryer operation control 乾燥機の動作制御のフローチャート1Flow chart 1 of operation control of dryer 乾燥機の動作制御のフローチャート2Flow chart 2 of operation control of dryer 開始時期の特性線図Characteristic diagram of start time 係数特性線図(a)および開始時期の特性線図(b)Coefficient characteristic diagram (a) and start time characteristic diagram (b)

上記技術思想に基づいて具体的に構成された実施の形態について以下に図面を参照しつつ説明する。
図1、図2は、それぞれ穀物乾燥機の穀物乾燥部の内部構成を説明する透視斜視図、正面図である。
穀物乾燥機は、機体の上部で穀粒を貯留する貯留部(不図示)から穀粒を受けつつ一定速度で下端から繰出しながら乾燥する穀物乾燥部3、この穀物乾燥部3で乾燥した穀粒を集めて再度貯留部に移送するための集穀部4とを設ける。そして貯留部に張り込まれた穀粒は穀物乾燥部3で乾燥されて集穀部4から再度貯留部に供給され調質される構成で外観が箱体状のいわゆる穀物循環式の構成である。そして、本実施の形態では、後述するバーナ5側を前側(前面)、排風ファン6側を後側(背面)と呼ぶ。
Embodiments specifically configured based on the above technical idea will be described below with reference to the drawings.
1 and 2 are a perspective view and a front view, respectively, for explaining the internal configuration of the grain drying unit of the grain dryer.
The grain dryer includes a grain drying unit 3 that receives grains from a storage unit (not shown) that stores the grains at the upper part of the machine body and feeds them from the lower end at a constant speed, and the grains dried by the grain drying unit 3 And a cereal collection unit 4 for transferring the collected product to the storage unit again. And the grain stuck in the storage part is a so-called grain circulation type structure in which the appearance is box-shaped with a structure that is dried in the grain drying part 3 and supplied to the storage part again from the grain collecting part 4 and tempered. . In the present embodiment, the burner 5 side, which will be described later, is called the front side (front surface), and the exhaust fan 6 side is called the rear side (back surface).

穀物乾燥部3については、機体の前面板3aと背面板3bとの間に左右の穀粒流下通路13,13を架設し、それぞれの穀粒流下通路13,13を挟むように、左右の外側の熱風室8,8と中央の排風室12とを形成する。左右の穀粒流下通路13,13は、熱風が透過可能な網材構成の穀粒通路であり、上端部を貯留部と連通し、両下端部を定量繰出弁14に合流して下方の集穀部4に臨む。また、左右の穀粒流下通路13,13によって囲まれた排風室12は、頂部を山形とする左右の傾斜ガイド部13a,13aによって両流れに形成する。この左右の傾斜ガイド部13a,13aは、前面板3aと背面板3bとの間に架設した左右のフレーム13b、13bによって支持する。   As for the grain drying unit 3, left and right grain flow passages 13 and 13 are installed between the front plate 3a and the back plate 3b of the fuselage, and the left and right outer sides are sandwiched between the grain flow passages 13 and 13, respectively. Hot air chambers 8 and 8 and a central air exhaust chamber 12 are formed. The left and right grain flow down passages 13 and 13 are grain passages having a net material structure through which hot air can permeate. It faces the grain part 4. In addition, the wind exhaust chamber 12 surrounded by the left and right grain flow down passages 13 and 13 is formed in both flows by left and right inclined guide portions 13a and 13a having a mountain shape at the top. The left and right inclined guide portions 13a and 13a are supported by left and right frames 13b and 13b installed between the front plate 3a and the back plate 3b.

穀物乾燥部3の前面位置には外気を加熱するバーナ5を備えて熱風を熱風室8に供給する熱風供給部Sを配置し、背面位置には排風室12から排風を吸引排出する排風ファン6を備える排風排出部Tを配置する。   A hot air supply unit S that includes a burner 5 that heats the outside air and supplies hot air to the hot air chamber 8 is disposed at the front surface of the grain drying unit 3, and exhaust air that sucks and exhausts the exhaust air from the exhaust air chamber 12 at the rear surface. An exhaust air discharge unit T including the wind fan 6 is disposed.

排風排出部Tは、要部の背面斜視図および縦断面図をそれぞれ図3、図4に示すように、背面板3bから箱体外側に排風ダクト20を突出して設け、排風ダクト20の上部に循環ダクト21を連結するとともに、排風ダクト20から前方に連通して背面板3bから箱体内側に向かって排風室12に導入筒6aを張出し、これをファン胴として固定翼6cと回転翼6bを取付けることにより排風ファン6をその先端が排風室12内に張出すように構成する。また、導入筒6aの上部にファンモータ61を配置し、背面側に伝動ベルト62を設けて回転翼6bを駆動する。   As shown in FIGS. 3 and 4, the exhaust air discharge portion T is provided with a discharge air duct 20 projecting from the back plate 3 b to the outside of the box as shown in FIGS. 3 and 4. A circulation duct 21 is connected to the upper part of the air duct, and an introduction tube 6a is extended from the back plate 3b toward the inside of the box body in the exhaust air chamber 12 through the exhaust air duct 20 and forwardly. By attaching the rotary blade 6b, the exhaust fan 6 is configured such that its tip projects into the exhaust chamber 12. Further, a fan motor 61 is disposed on the upper portion of the introduction cylinder 6a, and a transmission belt 62 is provided on the back side to drive the rotary blade 6b.

この伝動ベルト62は、外付けのファンモータ61によって回転翼6bを駆動することから、伝動ベルト62が排風ファン6のファン胴を貫通するための開口からの排風漏れが避けられないが、ファンモータ61が排風ファン6と一体的に排風室12に内設されることから、外気に対する排風漏れを生じることなく、外付けのファンモータ61による簡易なファン駆動部を構成することができる。   Since this transmission belt 62 drives the rotor blade 6b by an external fan motor 61, it is inevitable that the exhaust belt leaks from the opening through which the transmission belt 62 penetrates the fan body of the exhaust fan 6. Since the fan motor 61 is installed in the exhaust chamber 12 integrally with the exhaust fan 6, a simple fan drive unit by the external fan motor 61 is configured without causing exhaust air leakage to the outside air. Can do.

排風ダクト20内には第一調節弁23を設けて循環ダクト21を上方に連通し、この循環ダクト21には第二調節弁22を内設して両者を連動調節可能に排風を切替える切替弁として構成し、この循環ダクト21から熱風室8,8を前面板3aまで縦断する戻しダクト27,27を介して戻し排風を混合ダクトAに供給し、混合ダクトAでバーナ5からの熱風と混合して熱風室供給口Pより熱風室8,8に供給する。   A first control valve 23 is provided in the exhaust duct 20 to allow the circulation duct 21 to communicate upward, and a second control valve 22 is provided in the circulation duct 21 to switch exhaust air so that both can be adjusted in conjunction. Constructed as a switching valve, the return exhaust air is supplied to the mixing duct A from the circulation duct 21 through the return ducts 27, 27 that vertically cut the hot air chambers 8, 8 from the front plate 3a. It is mixed with hot air and supplied to the hot air chambers 8 and 8 through the hot air chamber supply port P.

そして、第一調節弁23は第一調節弁調節モータ23mでその開度を調節し、第二調節弁22は第二調節弁調節モータ22mでその開度を調節する構成であり、この2つの調節弁22,23で排風ファン6で排出された排風を箱体外側に排出案内する割合と循環ダクト21側に案内する割合を調節している。
例えば、排風を全て箱体外側に排出するときには第二調節弁22を全閉とすると共に、第一調節弁23を全開とし、排風を全て箱体内側に戻すときには第二調節弁22を全開とし第一調節弁23を全閉とする。
The first control valve 23 is adjusted by the first control valve adjustment motor 23m, and the second control valve 22 is adjusted by the second control valve adjustment motor 22m. The ratio of guiding the exhaust air discharged by the exhaust fan 6 to the outside of the box body and the ratio guiding it to the circulation duct 21 side are adjusted by the control valves 22 and 23.
For example, when exhausting all exhaust air to the outside of the box, the second control valve 22 is fully closed, and the first control valve 23 is fully open, and when returning all exhaust air to the inside of the box, the second control valve 22 is Fully open and the first control valve 23 fully closed.

また、排風ファン6やファンモータ61、伝動ベルト62の取付けおよびメンテナンスのために、上記循環ダクト21は着脱可能に構成する。本実施の形態では、着脱する部材は図示しないが、ノブボルト等で着脱可能としており、また、循環ダクト21と第二調節弁22は一体構成としている。   Further, the circulation duct 21 is configured to be detachable for mounting and maintenance of the exhaust fan 6, the fan motor 61, and the transmission belt 62. In this embodiment, although the member to be attached / detached is not shown, it can be attached / detached with a knob bolt or the like, and the circulation duct 21 and the second control valve 22 are integrally formed.

この循環ダクト21によって覆われる範囲の背面板3bに排風室12の形状の開口Wを形成し、かつ、左右の傾斜ガイド部13a,13aを支持して前面板3aに至る左右のフレーム13b、13bに沿って背面板3bから左右のガイドレール63,63を設け、この左右のガイドレール63,63によってモーターベースを吊るようにしてファンモータ外付けの排風ファン6を出し入れ可能に支持する。   The left and right frames 13b that form the openings W in the shape of the exhaust chamber 12 in the back plate 3b in the range covered by the circulation duct 21 and that support the left and right inclined guide portions 13a and 13a and reach the front plate 3a, The left and right guide rails 63 and 63 are provided from the back plate 3b along the line 13b. The left and right guide rails 63 and 63 support the exhaust fan 6 externally attached to the fan motor in such a manner that the motor base is suspended.

上記構成の穀物乾燥機は、穀物乾燥部3の通風流線を表す作用平面図を図5に示すように、穀物乾燥部3の排風室12内に導入筒6aを張り出し、この導入筒6aをファン胴とする排風ファン6を排風室12の内部に張り出して構成することにより、背面側への排風ダクト20の突出量が抑えられることから、穀粒流下通路13の必要寸法を確保しつつ、機体全長の短縮化が可能となる。また、循環ダクト21を備える場合についても、背面板3bから循環ダクト21の構成に必要な最小限度の突出寸法増加で済むことから、機体の全長寸法を抑えてコンパクトに構成することができる。   As shown in FIG. 5, the grain dryer having the above-described structure projects an introduction cylinder 6 a into the exhaust chamber 12 of the grain drying unit 3, as shown in FIG. 5. By projecting the exhaust fan 6 with the fan body extending inside the exhaust chamber 12, the amount of the exhaust duct 20 projecting to the rear side can be suppressed. It is possible to shorten the overall length of the aircraft while ensuring it. Further, in the case where the circulation duct 21 is provided, it is only necessary to increase the minimum projecting dimension necessary for the configuration of the circulation duct 21 from the back plate 3b.

また、排風排出部Tの排風ファン6の稼動により、熱風供給部Sから熱風が左右の熱風室8,8に供給され、この熱風が左右の穀粒流下通路13,13を通過することによって穀粒を乾燥し、その排風が排風室12から排風ファン6によって吸引排出され、また、排風の一部を循環ダクト21から左右の戻しダクト27,27を介して箱体前側に戻され、混合ダクトAで熱風と混合して熱風室8,8に供給することにより、高速乾燥が可能となる。   Further, by the operation of the exhaust air fan 6 of the exhaust air exhaust unit T, hot air is supplied from the hot air supply unit S to the left and right hot air chambers 8 and 8, and this hot air passes through the left and right grain flow passages 13 and 13. , And the exhausted air is sucked and discharged from the exhaust chamber 12 by the exhaust fan 6, and part of the exhaust air is forwarded from the circulation duct 21 through the left and right return ducts 27, 27. Then, the mixture is mixed with hot air in the mixing duct A and supplied to the hot air chambers 8 and 8, thereby enabling high-speed drying.

この場合において、穀粒流下通路13を通過した排風が排風室12の中央部に突出した位置から吸引されることから、穀粒流下通路13,13の乾燥作用が平均化されるので、上記穀物乾燥機は、穀粒流下通路13,13における穀物通過位置による乾燥斑を少なくすることができ、均一な乾燥が可能となる。   In this case, since the exhaust air that has passed through the grain flow passage 13 is sucked from the position protruding to the center of the exhaust chamber 12, the drying action of the grain flow passages 13, 13 is averaged. The grain dryer can reduce drying spots due to grain passing positions in the grain flow down passages 13 and 13, and can be uniformly dried.

図5の作用について、説明する。
排風は循環ダクト21から戻しダクト27,27及び混合ダクトAを経て箱体前側の熱風室に供給されるものと、戻しダクト27,27の後端部周囲にある熱風室8,8の開口部分Rから熱風室8,8の後ろ側に供給されるものがある。
The operation of FIG. 5 will be described.
The exhaust air is supplied from the circulation duct 21 to the hot air chamber on the front side of the box through the return ducts 27 and 27 and the mixing duct A, and the opening of the hot air chambers 8 and 8 around the rear ends of the return ducts 27 and 27. Some are supplied from the portion R to the rear side of the hot air chambers 8 and 8.

熱風はバーナ5から排風ファン6の作用と熱風室8,8の後ろ側に供給される排風の作用で、熱風室8,8の前後中央側に多く引き寄せられる。そのため、熱風が箱体内全体に平均化されて分布しやすくなり、また、排風との混合が良好になり、穀粒流下通路13,13における穀物通過位置による乾燥斑を少なくすることができ、均一な乾燥が可能となる。   Hot air is attracted to the front and rear center sides of the hot air chambers 8 and 8 by the action of the exhaust fan 6 from the burner 5 and the action of exhaust air supplied to the rear side of the hot air chambers 8 and 8. Therefore, the hot air is easily averaged and distributed throughout the box body, and the mixing with the exhaust air becomes good, and dry spots due to the grain passage positions in the grain flow passages 13 and 13 can be reduced. Uniform drying is possible.

その他の技術的な特長点をまとめると、以下のとおりである。
第1に、排風室12は、頂部を左右の傾斜ガイド部13a,13aによって山形に形成するとともに、それぞれの下部に穀粒流下通路13,13を形成し、これら左右の穀粒流下通路13,13の間に排風ファン6を配置してその上部の左右の傾斜ガイド部13a,13aの間に駆動用のファンモータ61を配置することにより、傾斜ガイド部13a,13aによって挟まれる空間に外付けのファンモータ61が収容されることから、無駄なスペースを生かして簡易な構成の乾燥装置をコンパクトに構成することができる。
Other technical features are summarized as follows.
1stly, while the wind exhaust chamber 12 forms the top part in the shape of a mountain by the left and right inclination guide parts 13a and 13a, it forms the grain flow passages 13 and 13 in each lower part, and these right and left grain flow passages 13 , 13 and the fan motor 61 for driving between the left and right inclined guide portions 13a, 13a at the upper portion thereof, and the space between the inclined guide portions 13a, 13a. Since the external fan motor 61 is accommodated, a drying device with a simple configuration can be configured in a compact manner by taking advantage of wasted space.

第2に、ファンモータ61は、背面板3bの内方に配置するとともに、排風ダクト20の排出側から分流する循環ダクト21を着脱可能に設けて熱風室8,8に戻し可能に構成するとともに、循環ダクト21によって覆われる範囲内の背面板3bに排風室12の開口Wを形成し、ファンモータ61のモーターベースを左右のガイドレール63,63で支持することにより、ファンモータ外付けの排風ファン6を背面板3bの開口から滑り込ませるようにして容易に組付けができ、また、特段の点検蓋を要することなく、循環ダクト21を取外すだけで、背面板3bの開口Wからファンモータ61と伝動ベルト62のメンテナンスが可能となる。   Secondly, the fan motor 61 is arranged inside the back plate 3b, and is configured to be detachably provided with a circulation duct 21 that diverges from the discharge side of the exhaust duct 20, so that it can be returned to the hot air chambers 8 and 8. At the same time, an opening W of the air exhaust chamber 12 is formed in the back plate 3b within the range covered by the circulation duct 21, and the motor base of the fan motor 61 is supported by the left and right guide rails 63, 63, so that the fan motor is externally attached. The exhaust fan 6 can be easily assembled by sliding it from the opening of the back plate 3b, and it is possible to remove the circulation duct 21 from the opening W of the back plate 3b without requiring a special inspection lid. Maintenance of the fan motor 61 and the transmission belt 62 is possible.

(乾燥制御)
乾燥機の動作制御は、システム構成図を図6に示すように、制御部Fの入力側には、温度センサTA、湿度センサHA、水分計10等の信号を入力し、これらの状態に応じて機器制御可能に、バーナ5、排風ファン6、切替弁を構成する第一調節弁23と第二調節弁22等の構成機器を出力側に接続する。
(Drying control)
As shown in FIG. 6, the operation control of the dryer is performed by inputting signals from the temperature sensor TA, the humidity sensor HA, the moisture meter 10 and the like to the input side of the control unit F, according to these states. Thus, component devices such as the burner 5, the exhaust fan 6, and the first control valve 23 and the second control valve 22 that constitute the switching valve are connected to the output side so that the devices can be controlled.

制御部Fによる具体的な乾燥制御について図7のフローチャート1に基づいて説明すると、乾燥作業中は水分計10で検出する穀物水分値に応じた排風循環率になるように第一調節弁23及び第二調節弁22とを調節制御する排風戻し制御を行なう。   The specific drying control by the control unit F will be described with reference to the flowchart 1 of FIG. 7. During the drying operation, the first control valve 23 is set so that the exhaust air circulation rate is in accordance with the grain moisture value detected by the moisture meter 10. And exhaust air return control for adjusting and controlling the second control valve 22.

排風循環により高速乾燥する乾燥方法において、張込まれた穀物水分の層ムラを除去するために、乾燥途中で休止乾燥を取込む場合に、所定の休止基準水分値で休止する設定については、この休止基準水分値の近傍(例えば、+0.5%)まで乾燥が進んだことを判定する制御処理ステップS1(以下において、「S1」の如く略記する。)により、条件を満たした時は、徐々に、即ち、時間毎に排風循環率を低下させ(S2a、S2b)るよう第一調節弁23及び第二調節弁22とを設定角度毎に調節制御し、、循環無し又は少量の循環量にした上で、休止水分値に到達した時点において、乾燥機を休止させる(S3a〜S3c)。バーナのポストパージの時間も含める。   In the drying method of high-speed drying by exhaust air circulation, in order to remove the layer unevenness of the cereal grain moisture, when setting the pause drying in the middle of drying, for setting to pause at a predetermined pause reference moisture value, When the condition is satisfied by the control processing step S1 (hereinafter abbreviated as “S1”) for determining that the drying has progressed to the vicinity (for example, + 0.5%) of the rest reference moisture value, The first control valve 23 and the second control valve 22 are adjusted and controlled for each set angle so that the exhaust air circulation rate is gradually decreased (S2a, S2b) every time, so that there is no circulation or a small amount of circulation. After the amount is reached, the dryer is paused when the pause moisture value is reached (S3a to S3c). Include burner post-purge time.

所定の経過時間によって休止する設定の場合は、図8のフローチャート2に示すように、休止基準水分値に代えて休止基準時刻(S12b)を用い、その時刻に近づくと(例えば、30分前から)排風循環率を徐々に低下させる(S11)るよう第一調節弁23及び第二調節弁22とを設定角度毎に調節制御する。   In the case of setting to pause at a predetermined elapsed time, as shown in the flowchart 2 of FIG. 8, the pause reference time (S12b) is used instead of the pause reference moisture value, and when that time approaches (for example, from 30 minutes before ) The first control valve 23 and the second control valve 22 are adjusted and controlled for each set angle so as to gradually reduce the exhaust air circulation rate (S11).

(休止工程)
乾燥機の休止制御は、排風の温度を監視することにより、胴割が発生しないレベルまで穀温を下げた後に行う。また、休止乾燥モード運転中の休止時は、空気の出入りを防止するために切替弁を全閉にする(S3c)。この全閉制御によって運転休止時に切替弁を閉じることで、空気の出入りを防ぎ、外気の影響を受けにくくすることで、余計な乾燥進行を防ぎ、機体内の穀物状態の均一化を進めることができる。
(Pause process)
Dryer pause control is performed after the temperature of the exhaust air is monitored and the grain temperature is lowered to a level at which no body split occurs. Further, at the time of a pause during the operation of the pause drying mode, the switching valve is fully closed to prevent air from entering and leaving (S3c). By closing the switching valve when the operation is stopped by this fully closed control, it is possible to prevent air from entering and exiting and to be less susceptible to the influence of outside air, to prevent excessive drying and to promote uniform grain condition in the machine. it can.

このように、上記排風循環式穀物乾燥機は、制御部により、検出水分値に応じた排風循環率で排風循環乾燥動作をし、検出水分値が休止基準水分値の近傍の所定の水分値に到達すると排風循環率が所定速度で漸減し、休止基準水分値に到達すると排風の全排出動作をするとともに穀物乾燥動作を停止する。   In this way, the exhaust air circulation type grain dryer performs the exhaust air circulation drying operation at the exhaust air circulation rate corresponding to the detected moisture value by the control unit, and the detected moisture value is a predetermined value near the pause reference moisture value. When the moisture value is reached, the exhaust air circulation rate is gradually reduced at a predetermined speed, and when the suspension reference moisture value is reached, the exhaust air is completely discharged and the grain drying operation is stopped.

したがって、上記排風循環式穀物乾燥機は、休止基準水分値における穀物乾燥の停止時には、排風の戻しによる蒸れを抑えつつ、穀温を高く維持することができ、その結果、水分移行を促進して水分斑の均一化を図ることができる。   Therefore, the above-described exhaust circulation type grain dryer can keep the grain temperature high while suppressing the steaming due to the return of the exhaust air when the grain drying is stopped at the suspension reference moisture value, thereby promoting the moisture transfer. Thus, the water spots can be made uniform.

(停止工程)
乾燥機の停止制御は、高速乾燥の場合は乾燥が速いので運転終了が夜半であることが多く、乾燥穀物の取出までの長時間の放置の間に、外気条件によって休止運転中に空気の出入りが起こると、通風部のみが乾燥が進んだり、あるいは水分が戻ったりすることがあることから、排風ダクトの排出側を閉じて外気の出入りを防止するモードを設け、乾燥が仕上がり、本機運転を終了する際は、切替弁を全閉に制御する(S5a〜S5c)。
(Stop process)
In the case of high-speed drying, the dryer is controlled so that drying is fast, so the end of the operation is often at night and during the prolonged operation until dry grain is taken out, air enters and exits during rest operation due to outside air conditions. If this happens, only the ventilation section may dry or the moisture may return.Therefore, a mode is provided to close the discharge side of the exhaust duct to prevent the outside air from entering and exiting. When the operation is finished, the switching valve is controlled to be fully closed (S5a to S5c).

(循環工程)
次に、排風循環の開始時期については、運転開始から所定時間の経過を待ってもごみが多い時は燃焼悪化を招き、また、運転開始からの穀物一巡を待っていると時間が無駄になることがあるので、図9の開始時期の特性線図に示すように、初期水分値に応じて排風循環開始時期を決定することにより、無駄時間を抑えつつ、バーナー燃焼を確保することができる。
(Circulation process)
Next, with regard to the start timing of the exhaust air circulation, the combustion deteriorates when there is a lot of dust even after a lapse of a predetermined time from the start of operation, and the time is wasted when waiting for the whole crop from the start of operation. Therefore, as shown in the characteristic diagram of the start time in FIG. 9, by determining the exhaust air circulation start time according to the initial moisture value, it is possible to ensure burner combustion while suppressing dead time. it can.

また、穀物の張込量により穀物の一巡時間を算出した上で、図10(a)の係数特性線図に示すように、上記の初期水分値による排風循環開始時期を係数化し、その係数を穀物の一巡時間に積算することにより、図10(b)の開始時期の特性線図に示すように、張込量と対応した排風循環開始時期を得ることができる。   Moreover, after calculating the round time of the grain based on the amount of grain, as shown in the coefficient characteristic diagram of FIG. 10 (a), the exhaust air circulation start timing based on the initial moisture value is coefficientized, and the coefficient Is accumulated in the cycle time of the grain, as shown in the characteristic diagram of the start time in FIG. 10B, the exhaust air circulation start time corresponding to the amount of tension can be obtained.

3 穀物乾燥部
5 バーナ
6 排風ファン
10 水分計
14 定量繰出弁
20 排風ダクト
21 循環ダクト
22 第二調節弁(切替弁)
23 第一調節弁(切替弁)
27 還流ダクト
F 制御部
3 Grain drying section 5 Burner 6 Exhaust fan 10 Moisture meter 14 Fixed feed valve 20 Exhaust duct 21 Circulation duct 22 Second control valve (switching valve)
23 First control valve (switching valve)
27 Reflux duct F Control part

Claims (3)

熱風によって穀物を乾燥する穀物乾燥部(3)から排出された排風を切替弁(22,23)により循環側に分流し、この分流排風を穀物乾燥部(3)に循環して穀物乾燥をする排風循環乾燥制御と、この排風循環乾燥制御における検出する穀物水分値が別途設定の休止基準水分値に達すると穀物乾燥を停止する乾燥休止制御とを行う制御部(F)を備える排風循環式穀物乾燥機において、
上記制御部(F)は、排風循環乾燥制御における検出水分値が休止基準水分値に到達するまでの所定の水分値範囲について切替弁(22,23)を全排出まで徐々に開いて排風循環率を所定速度で漸減させた後に乾燥休止制御を行うことを特徴とする排風循環式穀物乾燥機。
The exhaust air discharged from the grain drying section (3) for drying the grains by hot air is diverted to the circulation side by the switching valves (22, 23), and the diverted exhaust air is circulated to the grain drying section (3) to dry the grains. And a control unit (F) for performing the exhaust air circulation drying control and the dry suspension control for stopping the grain drying when the grain moisture value detected in the exhaust air circulation drying control reaches a separately set suspension reference moisture value. In the exhaust circulation type grain dryer,
The control unit (F) gradually opens the switching valve (22, 23) until the exhaust is exhausted for a predetermined moisture value range until the detected moisture value in the exhaust air circulation drying control reaches the pause reference moisture value. An exhaust air circulation type grain dryer characterized by performing drying suspension control after gradually decreasing the circulation rate at a predetermined speed.
熱風によって穀物を乾燥する穀物乾燥部(3)から排出された排風を切替弁(22,23)により循環側に分流し、この分流排風を穀物乾燥部(3)に循環して穀物乾燥をする排風循環乾燥制御と、この排風循環乾燥制御における経過時間が別途設定の休止基準時刻に達すると穀物乾燥を停止する乾燥休止制御とを行う制御部(F)を備える排風循環式穀物乾燥機において、
上記制御部(F)は、排風循環乾燥制御における経過時間が休止基準時刻に到達するまでの所定の時間範囲について切替弁(22,23)を全排出まで徐々に開いて排風循環率を所定速度で漸減させた後に乾燥休止制御を行うことを特徴とする排風循環式穀物乾燥機。
The exhaust air discharged from the grain drying section (3) for drying the grains by hot air is diverted to the circulation side by the switching valves (22, 23), and the diverted exhaust air is circulated to the grain drying section (3) to dry the grains. Exhaust air circulation drying control provided with a control unit (F) for performing the exhaust air circulation drying control, and when the elapsed time in the exhaust air circulation drying control reaches a separately set pause reference time, the grain suspension is stopped. In the grain dryer,
The control unit (F) gradually opens the switching valve (22, 23) until the total discharge for a predetermined time range until the elapsed time in the exhaust air circulation drying control reaches the pause reference time, and the exhaust air circulation rate is determined. An exhaust air circulation type grain dryer characterized by performing drying suspension control after being gradually reduced at a predetermined speed.
前記制御部(F)は、乾燥休止制御中は、切替弁(22,23)を排出全閉制御を行うことを特徴とする請求項1または請求項2のいずれかに記載の排風循環式穀物乾燥機。   3. The exhaust air circulation type according to claim 1, wherein the control unit (F) performs exhaust full-close control on the switching valve (22, 23) during the drying pause control. 4. Grain dryer.
JP2009125752A 2009-05-25 2009-05-25 Exhaust circulation type grain dryer Active JP5428530B2 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8726535B2 (en) 2008-12-16 2014-05-20 Pioneer Hi Bred International Inc Method, apparatus and system for controlling heated air drying

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JPS5424759A (en) * 1977-07-22 1979-02-24 Shizuoka Seiki Co Ltd Drying method for grain
JP2008133975A (en) * 2006-11-27 2008-06-12 Iseki & Co Ltd Exhaust recirculation type grain dryer
JP2009047315A (en) * 2007-07-20 2009-03-05 Iseki & Co Ltd Drying method

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5424759A (en) * 1977-07-22 1979-02-24 Shizuoka Seiki Co Ltd Drying method for grain
JP2008133975A (en) * 2006-11-27 2008-06-12 Iseki & Co Ltd Exhaust recirculation type grain dryer
JP2009047315A (en) * 2007-07-20 2009-03-05 Iseki & Co Ltd Drying method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8726535B2 (en) 2008-12-16 2014-05-20 Pioneer Hi Bred International Inc Method, apparatus and system for controlling heated air drying

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