JP4577812B2 - Dry storage facility - Google Patents

Dry storage facility Download PDF

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Publication number
JP4577812B2
JP4577812B2 JP2003208612A JP2003208612A JP4577812B2 JP 4577812 B2 JP4577812 B2 JP 4577812B2 JP 2003208612 A JP2003208612 A JP 2003208612A JP 2003208612 A JP2003208612 A JP 2003208612A JP 4577812 B2 JP4577812 B2 JP 4577812B2
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silo
cooling
drying
grain
cooler
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JP2005065513A (en
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俊也 永尾
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Yanmar Co Ltd
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Yanmar Co Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は米・麦・大豆などを対象穀物とし、荷受部・乾燥部・貯蔵部・調製出荷部などで構成されるカントリーエレベータなどの穀物乾燥貯蔵施設に関する。
【0002】
【従来の技術】
従来、乾燥させた籾などをサイロに貯蔵させ、出荷するときにサイロから籾などを取出して調整出荷していた。(例えば特許文献1参照)
【0003】
【特許文献1】
実開平5−29346号公報
【0004】
【発明が解決しようとする課題】
前記従来技術は、常温定湿空気をサイロに供給させる除湿機を設け、外気温度をセンサで検出して前記除湿機を運転し、外気温度の低下によって常温定湿空気をサイロに供給して除湿するから、サイロ内壁面に結露が発生するのを阻止して籾などの変質を防止できたが、火力を用いる乾燥空気または常温定湿空気などを利用して行う穀物の乾燥作業は、一次乾燥工程、仕上げ乾燥工程及び各工程後の冷却パスなどの各作業時間の短縮を容易に行い得ず、穀物の乾燥作業の簡略化並びに乾燥コストの低減などを容易に図り得ない等の問題がある。
【0005】
【課題を解決するための手段】
然るに、本発明は、請求項1の如く、穀物を受付ける荷受部(1)と、荷受後の穀物を乾燥機(9)にて乾燥する乾燥部(7)と、前記乾燥部(7)から搬入された穀物を貯蔵するサイロ(15)を備えた貯蔵部(11)とを有する乾燥貯蔵施設において、日除け用屋根(22)によって覆う冷却機(23)と、前記サイロ(15)の底部に設ける通気ルーバ(24)と、前記冷却機(23)から通気ルーバ(24)に冷却風を送給させる冷却バルブ(25)及び通気ダクト(26)と、前記サイロ(15)の内部に設置する測温ケーブルによって形成する温度センサ(28)と、前記サイロ(15)の上屋(31)に設ける排気ダクト(29)及び換気ファン(30)とを備え、前記冷却機(23)の冷却風によって前記サイロ(15)の内部の籾(27)を冷却するように構成する一方、複数の前記サイロ(15)の前記冷却バルブ(25)を自動制御する時間設定器(48)が設けられた冷却機(23)用の冷却コントローラ(49)と、施設管理用の集中コントローラ(50)とを備え、前記集中コントローラ(50)に前記冷却コントローラ(49)を接続させ、前記乾燥部(7)から穀物が投入された前記サイロ(15)に前記冷却機(23)の一定湿度の冷却風を送り、前記サイロ(15)の籾を強制冷却する構造であって、前記荷受部1から前記乾燥機(9)に投入して一次乾燥した穀物を前記サイロ(15)に搬入したときに、前記冷却機(23)を作動させて、前記サイロ(15)に前記冷却機(23)の冷却風を送って穀物を強制冷却し、一定時間が経過したときに前記冷却機(23)の冷却動作を停止させる一方、前記サイロ(15)から前記乾燥機(9)に投入して二次乾燥した穀物を前記サイロ(15)に搬入したときに、前記冷却機(23)を作動させて、前記サイロ(15)に冷却機(23)の冷却風を送って穀物を強制冷却し、一定時間が経過したときに前記冷却機(23)の冷却動作を停止させるように構成したもので、火力乾燥に必要な冷却パスを省略し得、従来の冷却パスに必要な時間を次の乾燥作業に充て得、また除湿(常温定湿)乾燥に必要な穀物のローテーション作業を省略し得、夜間作業を低減し得ると共に、従来よりも高い水分で穀物の一次貯蔵を行えて荷受能力の拡大などを容易に行い得、かつカビなどの発生を防いで穀物の品質劣化を防止し得るものである。
【0006】
【0007】
【発明の実施の形態】
以下本発明の実施例を図面に基づいて詳述する。図1はカントリーエレベータの説明図であり、個人別・荷口別に搬入される生籾を受付ける荷受部1を備え、荷受ホッパ2から荷受コンベア3及び昇降機4を介し搬入される荷受籾中より夾雑物を除去する粗選機5と、粗選後個人別・荷口別に荷口重量と水分が測定される荷受計量機6とを荷受部1に設ける。
【0008】
また、荷受後の生籾を胴割れを防止しながら乾燥する乾燥部7を備えるもので、前記荷受部1の荷受計量後の生籾を投入昇降機8を介して搬入させる連続流下構造の乾燥機9と、前記乾燥機9から半乾籾または乾燥籾を取出す乾燥機取出コンベア10とを乾燥部7に設け、該乾燥部7での半乾籾或いは乾燥籾を貯蔵部11に送り出すように構成している。
【0009】
さらに、前記貯蔵部11は、前記乾燥部7からの半乾籾或いは乾燥籾をサイロ昇降機12及び投入コンベア13、14を介して搬入して貯蔵するサイロ15と、前記サイロ15から取出コンベア16を介して取出した半乾籾を再び乾燥部7に送り出すサイロ取出昇降機17とを備え、サイロ15の乾燥籾をサイロ取出昇降機17を介して次工程の調製出荷部18に送出すように構成している。
【0010】
前記調節出荷部18は、前記サイロ15からの籾を昇降機17を介して搬入して脱ぷする籾摺機19と、良玄米を取出す揺動選別機20と、良玄米を投入する出荷タンク21などを備えている。
【0011】
さらに、図1、図2に示す如く、日除け用屋根22によって覆う冷却機23を外気が通り易い場所に設置させ、前記サイロ15底部の通気ルーバ24に冷却バルブ25及び通気ダクト26を介して冷却機23の冷却風を送給させ、サイロ15内部の数百トンの籾27を冷却風によって冷却すると共に、測温ケーブルによって形成する温度センサ28をサイロ15の内部に設置させ、排気ダクト29及び換気ファン30をサイロ15の上屋31に設ける。
【0012】
さらに、図2、図3に示す如く、コンプレッサ32と、ヒータ33と、空調ダクト34を、前記冷却機23の筐体35に内設させ、排熱ファン36を筐体35に設けると共に、フィルタ37と、高圧ファン38と、エアダンパ39と、除湿冷却コンデンサ40と、コンプレッサ32の排熱を利用した加温器41と、ヒータ33の加熱器42と、温度計43と湿度計44とを、前記空調ダクト34に内設させる。
【0013】
さらに、図4に示す如く、6基のサイロ15の冷却バルブ25及び換気ファン30を開及びオンにする第一乃至第六サイロスイッチ45と、コンプレッサ32及びヒータ33を自動制御する温度及び湿度設定器46、47と、冷却バルブ25を自動制御する時間設定器48とを、冷却機23の冷却コントローラ49に接続させると共に、荷受計量機6及び乾燥機9及びサイロ15の稼動状況を入力させる施設管理用の集中コントローラ50に冷却コントローラ49を接続させ、冷却バルブ25、換気ファン30,コンプレッサ32、ヒータ33、高圧ファン38などを作動させ、乾燥機9から籾を投入したサイロ15に一定湿度の冷却風を送り、サイロ15の籾を強制冷却するもので、図5のフローチャートに示す如く、前記荷受部1から乾燥機9に投入して一次乾燥した籾(穀物)をサイロ15に搬入したとき、冷却バルブ25を開にしかつ換気ファン30を作動させて前記サイロ15に冷却機23の冷却風を送って籾を強制冷却し、一定時間が経過したときに冷却バルブ25を閉にして前記冷却動作を停止させると共に、前記サイロ15から乾燥機9に投入して二次乾燥した(穀物)をサイロ15に搬入したとき、冷却バルブ25を開にしかつ換気ファン30を作動させて前記サイロ15に冷却機23の冷却風を送って籾を強制冷却し、一定時間が経過したときに冷却バルブ25を閉にして前記冷却動作を停止させる。
【0014】
上記から明らかなように、荷受穀物である籾を乾燥させて貯蔵する乾燥貯蔵施設において、乾燥工程の途中または終了段階で籾(穀物)をサイロ15に搬入して強制冷却するもので、火力乾燥に必要な放冷工程を省略し、従来の冷却パスに必要な時間を次の乾燥作業に充て、また除湿(常温定湿)乾燥に必要な籾のローテーション作業を一部省略し、夜間作業を低減させると共に、従来よりも高い水分で籾の一次貯蔵を行えて荷受能力の拡大などを行い、かつカビなどの発生を防いで籾の品質劣化を防止する。
【0015】
また、籾が乾燥終了水分に至るまでに乾燥工程を終了してサイロ15に搬入させ、乾燥仕上げ湿度に近い湿度の冷却風をサイロ15の籾に送給するもので、サイロ15の籾を冷却し乍ら除湿して乾燥させ、乾燥機9の運転時間を短縮し、籾の乾燥コストを容易に低減させると共に、仕上がり籾の水分を略均一にし、調整出荷(籾摺または精米など)の損失が少なくなるように穀物を乾燥及び貯蔵する。
【0016】
例えば、乾燥機9を連続流下式の火力乾燥構造とし、水分25%の生籾100トンを荷受する場合、乾燥機9の能力を、1時間当り25トンの流量で、1回通過当りの乾減率を2%とし、従来と本発明とを対比する。従来、17%まで一次乾燥を行い、その後一次貯蔵を行うので、25%−17%=8%の水分を乾燥によって除去することになる。さらに乾燥機通過回数(=パス数)を求めると、8%÷2%/パス=4パスとなり、これに放冷工程=冷却パスを加えるので、合計5パスが必要であった。これに対し、本発明の強制冷却を行うことによって、一次乾燥を19%で終了することが可能であり、25%−19%=6%の水分を除去すればよく、乾燥で必要なパス数は、6%÷2%/パス=3パスとなり、強制冷却を採用すれば、冷却パスは必要ではなく、従って3パスのみで一次乾燥を終えることができる。同じく上記条件下での乾燥に要する時間を試算する。従来、100トンの生籾を5パスした場合、乾燥時間は、100t×5パス÷25t/h=20時間となるのに対し、本発明の強制冷却した場合は、100t×3パス÷25t/h=12時間となり、以上から乾燥能力に余力を生み、従来に比べて量の多い、もしくは水分の高い生籾でも荷受可能となる。
【0017】
以下、火力乾燥方式における一次乾燥から仕上乾燥までを追って、工程と効果を示す。荷受けした生籾を通風貯蔵などを経て、乾燥機9を使って19%まで一次乾燥させ、水分19%の生籾を冷却パスすることなく、サイロ15で直接強制冷却する。送風空気の湿度は平衡含水率を維持する水分より若干低めに設定して送風する。延べ2〜3日で冷却を終了して通風を停止する。この時点で籾の水分は、通常1.5〜2.0%程度乾減する。これは乾燥機9による乾燥工程数1パス分に相当する。この時点で、冷却パス1回及び乾燥パス1回分、計2回分の運転短縮メリットを生む。17%でサイロ15から取り出した籾を再び乾燥機9で二次乾燥して仕上げる。籾の仕上げ水分は通常14.5%であるが、15%程度で、作業を終了する。また、この時、冷却パスは一次乾燥同様に省略できる。仕上げ乾燥後も再びサイロ15に投入して強制冷却を行う。この時、送風空気の湿度は仕上げ水分と釣り合う設定とし、乾燥終了水分と仕上げ水分の差=0.5%分の乾燥を行うと同時に、全体の水分誤差の収束効果も得られる。ここで冷却パス1回及び乾燥パス1回の計2回分の運転短縮メリットを生む。なお、常温定湿空気によって籾を乾燥させる除湿装置を使った貯蔵乾燥の場合、冷却による品質保持、また、ローテーション等の作業軽減による運営メリット、仕上げ水分の収束、そして、荷受集中に対する能力向上が期待できる。
【0018】
本発明のサイロ15を用いた強制冷却と従来の除湿乾燥との違いについて述べる。本発明のサイロ15を用いる冷却機23は、穀物冷却が本来の目的であるから、吸い込み空気の温度を下げる能力優先で設計する。また、数百tの穀物が収容されているサイロ15内部(通常高さ=20m)を、高い圧力抵抗に抗して下から上に向かって送風すべく、高圧ファン38を内蔵しており、反して送風量は200‰以下と、高圧力、小風量の機械であり、風量がわずかなので、除湿量も僅かである。これに対し、乾燥用除湿機は、穀物乾燥が目的であるから、温度は下げず、除湿機能優先の設計がされており、対象穀物は刻々変わるが、100t程度から2〜300t程度であるが、乾燥の為には理論的にある程度の風量が必要で、通常1000‰から1200‰程度を送風する。一方、圧力は150mmAq程度と、本発明のサイロ15冷却に比べてかなり低い圧力での運転となる。
【0019】
さらに籾を、冷却したときの物性変化は、ある温・湿度の空気と籾の水分の間には、相互の蒸気圧によって湿気平衡の関係が成立するから、例えば温度のみを下げたとすれば、雰囲気湿度は上昇し、籾は吸湿することになり、その含水率が増加して貯蔵性を損ねるから、本発明は、強制冷却を行う送風冷気の湿度を調節可能とし、温度を下げたときに籾の含水率が増加するのを防いでいる。また、乾燥機9での一連の乾燥作業において、乾燥途中の籾(穀物)をサイロ15に収納し、強制的に冷却することで籾の呼吸を沈静化し、籾の消耗劣化を抑える効果が得られると共に、前記冷却によってカビなどの微生物の繁殖が抑えられ、ロットの安全性が高められる等の大きなメリットがある。しかも、本発明の冷却機23は、従来の乾燥用除湿機ではないので、大きな除湿能力は持たないが、数パーセントの範囲で微妙な送風湿度の調整が可能であり、乾燥途中の冷却時にこの湿度設定を行うことで、水分低下=乾燥効果も期待できるもので、従来行われていない乾燥工程途中において、穀物冷却をすることにより、除湿乾燥と同じ現象が起こりますが、火力乾燥で暖められた籾に冷気を送ることで、乾燥効果が助長される。
【0020】
【発明の効果】
以上実施例から明らかなように本発明は、請求項1の如く、穀物を受付ける荷受部1と、荷受後の穀物を乾燥機9にて乾燥する乾燥部7と、乾燥部7から搬入された穀物を貯蔵するサイロ15を備えた貯蔵部11とを有する乾燥貯蔵施設において、日除け用屋根22によって覆う冷却機23と、サイロ15の底部に設ける通気ルーバ24と、冷却機23から通気ルーバ24に冷却風を送給させる冷却バルブ25及び通気ダクト26と、サイロ15の内部に設置する測温ケーブルによって形成する温度センサ28と、サイロ15の上屋31に設ける排気ダクト29及び換気ファン30とを備え、冷却機23の冷却風によってサイロ15の内部の籾27を冷却するように構成する一方、複数のサイロ15の冷却バルブ25を自動制御する時間設定器48が設けられた冷却機23用の冷却コントローラ49と、施設管理用の集中コントローラ50とを備え、集中コントローラ50に冷却コントローラ49を接続させ、乾燥部7から穀物が投入されたサイロ15に冷却機23の一定湿度の冷却風を送り、サイロ15の籾を強制冷却する構造であって、荷受部1から乾燥機9に投入して一次乾燥した穀物をサイロ15に搬入したときに、冷却機23を作動させて、サイロ15に冷却機23の冷却風を送って穀物を強制冷却し、一定時間が経過したときに冷却機23の冷却動作を停止させる一方、サイロ15から乾燥機9に投入して二次乾燥した穀物を前記サイロ15に搬入したときに、冷却機23を作動させて、サイロ15に冷却機23の冷却風を送って穀物を強制冷却し、一定時間が経過したときに冷却機23の冷却動作を停止させるように構成したもので、火力乾燥に必要な放冷工程を省略でき、従来の放冷工程に必要な時間を次の乾燥作業に充てることができ、また除湿(常温定湿)乾燥に必要な穀物のローテーション作業を省略でき、夜間作業を低減させるとこができると共に、従来よりも高い水分で穀物の一次貯蔵を行えて荷受能力の拡大などを容易に行うことができ、かつカビなどの発生を防いで穀物の品質劣化を防止できるものである。
【0021】
また、例えば、穀物が乾燥終了水分に至るまでに乾燥工程を終了して乾燥仕上げ湿度に近い湿度の冷却風を穀物に送給するもので、穀物を冷却し乍ら除湿して乾燥させるから、乾燥機9の運転時間を短縮でき、穀物の乾燥コストを容易に低減させることができると共に、仕上がり穀物の水分を略均一にし、調整出荷(籾摺または精米など)の損失が少なくなるように穀物を乾燥及び貯蔵できるものである。
【図面の簡単な説明】
【図1】カントリーエレベータの作業説明図。
【図2】サイロの説明図。
【図3】冷却機の説明図。
【図4】冷却制御回路。
【図5】冷却制御フローチャート。
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a grain dry storage facility such as a country elevator, which includes rice, wheat, soybeans, and the like as a target grain, and includes a cargo receiving unit, a drying unit, a storage unit, a preparation shipping unit, and the like.
[0002]
[Prior art]
Conventionally, dried cocoons are stored in a silo, and the cocoons are taken out from the silo before shipping. (For example, see Patent Document 1)
[0003]
[Patent Document 1]
Japanese Utility Model Publication No. 5-29346
[Problems to be solved by the invention]
The prior art is provided with a dehumidifier that supplies room temperature and constant humidity air to the silo, detects the outside air temperature with a sensor, operates the dehumidifier, and supplies the room temperature and constant humidity air to the silo when the outside air temperature decreases to dehumidify. Therefore, it was possible to prevent dew condensation from occurring on the inner wall surface of the silo and prevent alterations such as drought, but grain drying work using dry air using firepower or room temperature constant humidity air is the primary drying. There is a problem that it is not possible to easily shorten each work time such as a process, a finish drying process, and a cooling pass after each process, and it is not possible to easily simplify grain drying work and reduce drying costs. .
[0005]
[Means for Solving the Problems]
However, according to the present invention, as in claim 1, the cargo receiving portion (1) for receiving the grain, the drying portion (7) for drying the grain after receiving the cargo in the dryer (9 ), and the drying portion (7). In a dry storage facility having a storage part (11) with a silo (15) for storing incoming grain, a cooler (23) covered by a sun protection roof (22), and a bottom part of the silo (15) A ventilation louver (24) to be provided, a cooling valve (25) for supplying cooling air from the cooler (23) to the ventilation louver (24), a ventilation duct (26), and the silo (15). a temperature sensor (28) formed by the temperature measuring cable, the silo is provided in sheds (15) (31) and an exhaust duct (29) and ventilation fan (30), said chiller (23) cooling air By the silo (15) While configured to cool the part of the rice (27), the cooling valve (25) time setting unit for automatically controlling the plurality of the silo (15) (48) is provided cooler (23) for A cooling controller (49) and a centralized controller (50) for facility management are provided, the cooling controller (49) is connected to the centralized controller (50), and the grain is introduced from the drying unit (7). A cooling air having a constant humidity from the cooler (23) is sent to the silo (15) to forcibly cool the soot in the silo (15), and the silo (15) is charged into the dryer (9) from the load receiving part 1. When the primary dried grain is carried into the silo (15), the cooler (23) is operated and the cooling air of the cooler (23) is sent to the silo (15) to forcibly cool the grain. And after a certain time Sometimes the cooling operation of the cooler (23) is stopped, while when the grain that has been secondarily dried from the silo (15) into the dryer (9) is carried into the silo (15), The cooler (23) is operated, the cooling air of the cooler (23) is sent to the silo (15) to forcibly cool the grain, and the cooling operation of the cooler (23) is performed when a certain time has passed. It is configured to stop, the cooling pass required for thermal drying can be omitted, the time required for the conventional cooling pass can be devoted to the next drying operation, and the grains required for dehumidification (room temperature constant humidity) drying Rotation work can be omitted, night work can be reduced, primary storage of grains can be performed with higher moisture than before, and the capacity for receiving cargo can be easily increased. Quality deterioration can be prevented.
[0006]
[0007]
DETAILED DESCRIPTION OF THE INVENTION
Embodiments of the present invention will be described below in detail with reference to the drawings. FIG. 1 is an explanatory view of a country elevator, which includes a load receiving portion 1 for receiving a ginger carried by each individual and a loading port, and is a contaminant from a load receiving hopper 2 through a load receiving conveyor 3 and an elevator 4 during loading. The load receiving unit 1 is provided with a coarse selection machine 5 for removing water and a load receiving and weighing machine 6 for measuring the weight and moisture of the individual for each individual and after the rough selection.
[0008]
Further, the dryer includes a drying unit 7 that dries the ginger after receiving the cargo while preventing torso cracking, and has a continuous flow-down structure in which the ginger after receiving and weighing the cargo receiving unit 1 is carried in via the loading elevator 8. 9 and a dryer take-out conveyor 10 for taking out semi-dried rice cake or dried rice cake from the dryer 9 are provided in the drying unit 7, and the semi-dry rice cake or dried rice cake in the drying unit 7 is sent to the storage unit 11. is doing.
[0009]
Further, the storage unit 11 includes a silo 15 that carries the semi-dry rice cake or dried rice cake from the drying unit 7 via the silo elevator 12 and the input conveyors 13 and 14 and stores the take-out conveyor 16 from the silo 15. And a silo take-out elevator 17 for sending the semi-dry rice cake taken out via the silo take-out elevator 17 again to the drying unit 7. Yes.
[0010]
The adjustment shipping unit 18 includes a rice huller 19 that carries the rice cake from the silo 15 through the elevator 17 and removes it, a swing sorter 20 that takes out the good brown rice, and a shipping tank 21 into which the good brown rice is charged. Etc.
[0011]
Further, as shown in FIGS. 1 and 2, a cooler 23 covered with a awning roof 22 is installed in a place where outside air can easily pass, and the ventilation louver 24 at the bottom of the silo 15 is cooled via a cooling valve 25 and a ventilation duct 26. The cooling air of the machine 23 is fed to cool the several hundred tons of firewood 27 inside the silo 15 with the cooling air, and the temperature sensor 28 formed by the temperature measuring cable is installed inside the silo 15, and the exhaust duct 29 and A ventilation fan 30 is provided in the roof 31 of the silo 15.
[0012]
Further, as shown in FIGS. 2 and 3, a compressor 32, a heater 33, and an air conditioning duct 34 are provided in the casing 35 of the cooler 23, a heat exhaust fan 36 is provided in the casing 35, and a filter is provided. 37, a high-pressure fan 38, an air damper 39, a dehumidifying cooling condenser 40, a heater 41 using the exhaust heat of the compressor 32, a heater 42 of the heater 33, a thermometer 43, and a hygrometer 44. The air conditioning duct 34 is installed inside.
[0013]
Further, as shown in FIG. 4, first to sixth silo switches 45 for opening and turning on the cooling valves 25 and the ventilation fans 30 of the six silos 15, and the temperature and humidity settings for automatically controlling the compressor 32 and the heater 33. Facilities 46, 47 and a time setting device 48 for automatically controlling the cooling valve 25 are connected to the cooling controller 49 of the cooler 23, and the operation status of the load receiving weighing device 6, the dryer 9, and the silo 15 is input. The cooling controller 49 is connected to the central controller 50 for management, the cooling valve 25, the ventilation fan 30, the compressor 32, the heater 33, the high-pressure fan 38, etc. are operated, and the silo 15 into which the soot is introduced from the dryer 9 has a constant humidity. A cooling air is sent to forcibly cool the soot of the silo 15, and as shown in the flowchart of FIG. When the primary dried rice cake (cereal) that has been put into the machine 9 is carried into the silo 15, the cooling valve 25 is opened and the ventilation fan 30 is operated to send the cooling air of the cooling machine 23 to the silo 15 to send the rice cake. The cooling operation is stopped by forcibly cooling and the cooling valve 25 is closed when a certain time has elapsed, and the secondarily dried rice cake (cereal grains) that has been put into the dryer 9 from the silo 15 is carried into the silo 15. When this happens, the cooling valve 25 is opened and the ventilation fan 30 is operated to send the cooling air of the cooler 23 to the silo 15 to forcibly cool the soot. When a certain time has elapsed, the cooling valve 25 is closed. The cooling operation is stopped.
[0014]
As is clear from the above, in a dry storage facility that dries and stores the cereal that is the receiving grain, the cereal (grain) is carried into the silo 15 during the drying process or at the end of the drying process and forcibly cooled. The cooling process required for cooling is omitted, the time required for the conventional cooling pass is devoted to the next drying work, and some of the paddy rotation work required for dehumidification (room temperature and constant humidity) drying is partially omitted. In addition to reducing the quality of the cocoon, the primary storage of the cocoon can be carried out with higher moisture than before to increase the capacity for receiving cargo, and to prevent the occurrence of mold and the like.
[0015]
In addition, the drying process is completed by the time when the soot reaches the moisture content at which drying is completed, and the silo 15 is carried into the silo 15, and the cooling air having a humidity close to the drying finish humidity is supplied to the silo 15 so that the soot 15 is cooled. It is dehumidified and dried, shortening the operation time of the dryer 9 and easily reducing the drying cost of the koji, and making the finished koji moisture almost uniform, resulting in loss of adjusted shipment (such as rice hull or rice milling). Dry and store the grain so that there is less.
[0016]
For example, when the dryer 9 has a continuous flow-type thermal drying structure and receives 100 tons of ginger with a moisture content of 25%, the dryer 9 has a capacity of 25 tons per hour at a flow rate of 25 tons per hour. The reduction rate is 2%, and the conventional and the present invention are compared. Conventionally, primary drying is performed up to 17%, followed by primary storage, so that 25% -17% = 8% of water is removed by drying. Further, when the number of times of passing through the dryer (= number of passes) was obtained, it was 8% / 2% / pass = 4 passes, and since the cooling step = cooling pass was added thereto, a total of 5 passes were required. On the other hand, by performing forced cooling according to the present invention, the primary drying can be completed at 19%, and it is sufficient to remove 25% -19% = 6% of water, and the number of passes required for drying. Is 6% / 2% / pass = 3 passes, and if forced cooling is employed, the cooling pass is not necessary, and therefore primary drying can be completed in only 3 passes. Similarly, the time required for drying under the above conditions is estimated. Conventionally, when 5 passes of 100 tons of ginger, the drying time is 100 t × 5 passes ÷ 25 t / h = 20 hours, whereas when forced cooling is performed according to the present invention, 100 t × 3 passes ÷ 25 t / Since h = 12 hours, there is a surplus in drying capacity from the above, and even ginger with a larger amount or higher moisture than before can be received.
[0017]
Hereinafter, the steps and effects will be described following the primary drying to the final drying in the thermal drying system. The received ginger is subjected to ventilation storage and the like, and is firstly dried to 19% using a dryer 9, and the ginger having a moisture content of 19% is forcibly cooled directly in the silo 15 without passing through a cooling pass. The humidity of the blown air is set to be slightly lower than the moisture that maintains the equilibrium moisture content. Stop cooling in 2 to 3 days and stop ventilation. At this point, the moisture of the cocoon usually dries out by about 1.5 to 2.0%. This corresponds to one pass for the number of drying steps by the dryer 9. At this time, the operation shortening merit for two times of one cooling pass and one drying pass is produced. The cocoon taken out from the silo 15 at 17% is secondarily dried again by the dryer 9 and finished. The finishing moisture of the cocoons is usually 14.5%, but the work is finished at about 15%. At this time, the cooling pass can be omitted as in the primary drying. After finishing drying, it is again put into the silo 15 for forced cooling. At this time, the humidity of the blown air is set to be balanced with the finishing moisture, and the difference between the drying end moisture and the finishing moisture is dried by 0.5%, and at the same time, the convergence effect of the entire moisture error can be obtained. Here, a merit of shortening the operation for two times of one cooling pass and one drying pass is brought about. In addition, in the case of storage drying using a dehumidifier that dries soot with room temperature and constant humidity air, it is possible to maintain the quality by cooling, improve operational merits by reducing work such as rotation, converge the finished moisture, and improve the ability to concentrate on receiving goods. I can expect.
[0018]
The difference between forced cooling using the silo 15 of the present invention and conventional dehumidification drying will be described. The cooler 23 using the silo 15 of the present invention is designed with priority given to the ability to lower the temperature of the intake air because grain cooling is the original purpose. In addition, a high-pressure fan 38 is incorporated in order to blow the interior of the silo 15 (normal height = 20 m) containing grains of several hundred t from the bottom to the top against high pressure resistance, On the contrary, it is a machine with a high pressure and a small air volume of 200 ‰ or less, and since the air volume is small, the amount of dehumidification is also small. On the other hand, since the desiccator for drying is intended for grain drying, the temperature is not lowered and the dehumidifying function is designed with priority. The target grain changes every hour, but is about 100 to 2 to 300 t. For drying, a certain amount of air is theoretically required, and usually 1000 to 1200 ‰ is blown. On the other hand, the pressure is about 150 mmAq, which is an operation at a considerably lower pressure than the silo 15 cooling of the present invention.
[0019]
Furthermore, when the soot is cooled, the change in physical properties is that the moisture equilibrium between the air at a certain temperature and humidity and the moisture of the soot is established by the mutual vapor pressure. For example, if only the temperature is lowered, Atmospheric humidity rises and soot absorbs moisture, and its moisture content increases and impairs storage, so that the present invention makes it possible to adjust the humidity of the blown cold air for forced cooling, and when the temperature is lowered It prevents the moisture content of firewood from increasing. Further, in a series of drying operations in the dryer 9, the cocoon (grain) in the middle of drying is stored in the silo 15 and forcedly cooled to calm the cocoon respiration and suppress the deterioration of the cocoon consumption. In addition, the cooling has the great advantage that the propagation of microorganisms such as mold is suppressed and the safety of the lot is improved. Moreover, since the cooler 23 of the present invention is not a conventional drying dehumidifier, it does not have a large dehumidifying capacity, but it is possible to finely adjust the blast humidity within a range of several percent, and this cooling is performed during the drying. By setting the humidity, you can expect moisture reduction = drying effect, and the same phenomenon as dehumidification drying occurs by cooling the grain during the drying process that has not been done conventionally, but it is warmed by thermal drying By sending cool air to the cocoon, the drying effect is promoted.
[0020]
【The invention's effect】
As is apparent from the above embodiments, the present invention is carried in from the load receiving unit 1 for receiving grains, the drying unit 7 for drying the grains after receiving the cargo in the dryer 9, and the drying unit 7. In a dry storage facility having a storage unit 11 having a silo 15 for storing grain, a cooler 23 covered with a roof 22 for shading, a ventilation louver 24 provided at the bottom of the silo 15, and a cooling machine 23 to a ventilation louver 24. A cooling valve 25 and a ventilation duct 26 for supplying cooling air, a temperature sensor 28 formed by a temperature measuring cable installed inside the silo 15, an exhaust duct 29 and a ventilation fan 30 provided in the shed 31 of the silo 15. provided, while configured to cool the rice 27 inside the silo 15 by the cooling air of the cooling unit 23, the time setting for automatically controlling the cooling valve 25 of a plurality of silos 15 48 a cooling controller 49 for chiller 23 is provided, and a central controller 50 for facility management, to connect the cooling controller 49 to the centralized controller 50, the cooling silo 15 grain is turned from the drying section 7 The machine 23 is configured to send a cooling air with a constant humidity to forcibly cool the straw of the silo 15, and when the grain that has been primarily dried after being put into the dryer 9 from the load receiving unit 1 is carried into the silo 15, 23, the cooling air of the cooler 23 is sent to the silo 15 to forcibly cool the grain, and the cooling operation of the cooler 23 is stopped when a certain time has elapsed, while the silo 15 is put into the dryer 9 Then, when the secondary dried grain is carried into the silo 15, the cooler 23 is operated and the cooling air of the cooler 23 is sent to the silo 15 to forcibly cool the grain. Sometimes it is configured to stop the cooling operation of the cooler 23, the cooling step necessary for thermal drying can be omitted, the time required for the conventional cooling step can be used for the next drying operation, In addition, the rotation of grains necessary for dehumidification (room temperature and constant humidity) drying can be omitted, so that night work can be reduced, and primary storage of grains with higher moisture than before can be facilitated to increase the capacity for receiving goods. It is possible to prevent the occurrence of mold and the like, thereby preventing the deterioration of grain quality.
[0021]
In addition, for example, the drying process is completed by the time the cereal reaches the dry end moisture, and the cooling air having a humidity close to the drying finish humidity is supplied to the cereal, and the cereal is cooled and dehumidified and dried. Grains so that the operation time of the dryer 9 can be shortened, the cost of drying the grains can be easily reduced, the moisture of the finished grains is made substantially uniform, and the loss of adjusted shipment (such as rice hulls or milled rice) is reduced. Can be dried and stored.
[Brief description of the drawings]
FIG. 1 is an operation explanatory diagram of a country elevator.
FIG. 2 is an explanatory diagram of a silo.
FIG. 3 is an explanatory diagram of a cooler.
FIG. 4 is a cooling control circuit.
FIG. 5 is a cooling control flowchart.

Claims (1)

穀物を受付ける荷受部(1)と、荷受後の穀物を乾燥機(9)にて乾燥する乾燥部(7)と、前記乾燥部(7)から搬入された穀物を貯蔵するサイロ(15)を備えた貯蔵部(11)とを有する乾燥貯蔵施設において、
日除け用屋根(22)によって覆う冷却機(23)と、前記サイロ(15)の底部に設ける通気ルーバ(24)と、前記冷却機(23)から通気ルーバ(24)に冷却風を送給させる冷却バルブ(25)及び通気ダクト(26)と、前記サイロ(15)の内部に設置する測温ケーブルによって形成する温度センサ(28)と、前記サイロ(15)の上屋(31)に設ける排気ダクト(29)及び換気ファン(30)とを備え、前記冷却機(23)の冷却風によって前記サイロ(15)の内部の籾(27)を冷却するように構成する一方、
複数の前記サイロ(15)の前記冷却バルブ(25)を自動制御する時間設定器(48)が設けられた冷却機(23)用の冷却コントローラ(49)と、施設管理用の集中コントローラ(50)とを備え、前記集中コントローラ(50)に前記冷却コントローラ(49)を接続させ、前記乾燥部(7)から穀物が投入された前記サイロ(15)に前記冷却機(23)の一定湿度の冷却風を送り、前記サイロ(15)の籾を強制冷却する構造であって、
前記荷受部1から前記乾燥機(9)に投入して一次乾燥した穀物を前記サイロ(15)に搬入したときに、前記冷却機(23)を作動させて、前記サイロ(15)に前記冷却機(23)の冷却風を送って穀物を強制冷却し、一定時間が経過したときに前記冷却機(23)の冷却動作を停止させる一方、
前記サイロ(15)から前記乾燥機(9)に投入して二次乾燥した穀物を前記サイロ(15)に搬入したときに、前記冷却機(23)を作動させて、前記サイロ(15)に冷却機(23)の冷却風を送って穀物を強制冷却し、一定時間が経過したときに前記冷却機(23)の冷却動作を停止させるように構成したことを特徴とする乾燥貯蔵施設。
A receiving part (1) for receiving the grain, a drying part (7) for drying the grain after receiving in the dryer (9 ), and a silo (15) for storing the grain carried from the drying part (7) In a dry storage facility having a storage (11) with
Cooling air is supplied to the cooling louver (24) from the cooling machine (23) covered by the roof (22) for sun protection, the ventilation louver (24) provided at the bottom of the silo (15), and the cooling machine (23). A cooling valve (25), a ventilation duct (26), a temperature sensor (28) formed by a temperature measuring cable installed in the silo (15), and an exhaust gas provided in the shed (31) of the silo (15) and a duct (29) and ventilation fan (30), while adapted to cool the interior of the rice (27) of the silo (15) by the cooling air of the cooling machine (23),
A cooling controller (49) for the cooler (23) provided with a time setting device (48 ) for automatically controlling the cooling valves (25) of the plurality of silos (15), and a centralized controller (50 for facility management) ), The cooling controller (49) is connected to the centralized controller (50), and the silo (15) into which the grain is put from the drying unit (7) has a constant humidity of the cooler (23). The cooling air is sent and the silo (15) is forcibly cooled.
When the grain that has been primarily dried after being put into the dryer (9) from the cargo receiver 1 is carried into the silo (15), the cooler (23) is operated to cool the silo (15) with the cooling. The cooling air of the machine (23) is sent to forcibly cool the grains, and the cooling operation of the cooler (23) is stopped when a certain time has passed,
When the grain dried into the dryer (9) from the silo (15) and secondarily dried is carried into the silo (15), the cooler (23) is operated and the silo (15) A drying storage facility characterized in that the cooling air of the cooler (23) is sent to forcibly cool the grain, and the cooling operation of the cooler (23) is stopped when a certain time has passed.
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Citations (5)

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Publication number Priority date Publication date Assignee Title
JPS5645164A (en) * 1979-09-18 1981-04-24 Satake Eng Co Ltd Cooling apparatus of grain
JPS6038089B2 (en) * 1980-11-18 1985-08-30 味の素株式会社 Grain storage methods and equipment
JPH06170254A (en) * 1992-12-10 1994-06-21 Satake Eng Co Ltd Country elevator
JP2751795B2 (en) * 1993-08-31 1998-05-18 鹿島建設株式会社 Grain storage equipment
JP2004069089A (en) * 2002-08-02 2004-03-04 Sanei:Kk Drying method of agricultural product

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5645164A (en) * 1979-09-18 1981-04-24 Satake Eng Co Ltd Cooling apparatus of grain
JPS6038089B2 (en) * 1980-11-18 1985-08-30 味の素株式会社 Grain storage methods and equipment
JPH06170254A (en) * 1992-12-10 1994-06-21 Satake Eng Co Ltd Country elevator
JP2751795B2 (en) * 1993-08-31 1998-05-18 鹿島建設株式会社 Grain storage equipment
JP2004069089A (en) * 2002-08-02 2004-03-04 Sanei:Kk Drying method of agricultural product

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