JPH03191288A - Grain drying apparatus - Google Patents
Grain drying apparatusInfo
- Publication number
- JPH03191288A JPH03191288A JP32983789A JP32983789A JPH03191288A JP H03191288 A JPH03191288 A JP H03191288A JP 32983789 A JP32983789 A JP 32983789A JP 32983789 A JP32983789 A JP 32983789A JP H03191288 A JPH03191288 A JP H03191288A
- Authority
- JP
- Japan
- Prior art keywords
- air
- temperature
- drying
- humidity
- ordinary temperature
- 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
- 238000001035 drying Methods 0.000 title claims abstract description 37
- 241000209094 Oryza Species 0.000 abstract description 19
- 235000007164 Oryza sativa Nutrition 0.000 abstract description 19
- 235000013339 cereals Nutrition 0.000 abstract description 19
- 235000009566 rice Nutrition 0.000 abstract description 19
- 238000003860 storage Methods 0.000 abstract description 11
- 238000007791 dehumidification Methods 0.000 abstract description 5
- 238000001816 cooling Methods 0.000 abstract description 2
- 230000001105 regulatory effect Effects 0.000 abstract 5
- 235000021329 brown rice Nutrition 0.000 description 9
- 238000010586 diagram Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 4
- 238000005303 weighing Methods 0.000 description 4
- 239000000428 dust Substances 0.000 description 3
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000003801 milling Methods 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- 230000032258 transport Effects 0.000 description 2
- 241000973497 Siphonognathus argyrophanes Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 241000209140 Triticum Species 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000005496 tempering Methods 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
Description
【発明の詳細な説明】
r産業上の利用分野J
本発明は米或いは麦などを対象穀物とし、荷受部・乾燥
部・貯留部・調製出荷部などで構成されるカントリエレ
ベータなど穀物乾燥施設に関する。Detailed Description of the Invention r Industrial Field of Application J The present invention relates to grain drying facilities such as country elevators, which target grains such as rice or wheat, and are comprised of a receiving section, a drying section, a storage section, a preparation and shipping section, etc. .
「従来の技術」
例えば籾の乾燥作業の場合、高水分(水分24%程度)
の籾が多量に入荷するため乾燥を1次(水分17%程度
まで)と2次(水分路14.5%程度の仕上げ水分まで
)に分けて行って、籾の品質維持と施設の処理能力の向
上を図るようにしている。``Conventional technology'' For example, in the case of drying rice, high moisture content (approximately 24% moisture)
Because we receive a large amount of paddy, we separate the drying process into primary (down to about 17% moisture) and secondary drying (down to finishing moisture of about 14.5%) to maintain the quality of the paddy and reduce the processing capacity of the facility. We are trying to improve this.
「発明が解決しようとする問題点」
しかし乍らこのような乾燥にあって籾を目的の水分値ま
で乾燥する場合の温度制御は、その除去しようとする水
分値に基づくだけでなく、乾燥機に取入れられる空気の
湿度や温度の変化に大きく左右されるため、その都度こ
れら湿度や温度の変化にも応じて決定された温度条件の
もとで制御が行わねばならないという問題があった。``Problem to be solved by the invention'' However, in such drying, temperature control when drying paddy to a target moisture level is not only based on the moisture level to be removed, but also based on the dryer. The problem is that control must be performed under temperature conditions that are determined each time depending on changes in humidity and temperature, as the temperature is greatly affected by changes in the humidity and temperature of the air taken into the air.
「問題点を解決するための手段」
したがって本発明は、穀物乾燥機の外気取入口に、常温
定湿空気を供給する乾燥空気発生機を設けたものである
。"Means for Solving the Problems" Accordingly, the present invention provides a dry air generator for supplying normal temperature and constant humidity air to the outside air intake port of a grain dryer.
そして穀物乾燥機の乾燥温度制御手段に、発生機からの
供給空気の湿度及び温度データを入力させて、これらデ
ータ値に基づいて穀物乾燥機における乾燥温度の制御を
行うように構成したものである。The drying temperature control means of the grain dryer is configured to input humidity and temperature data of the air supplied from the generator, and to control the drying temperature in the grain dryer based on these data values. .
「作 用」
而して本発明によれば、乾燥機に取入れられる熱風用空
気の温度と湿度とを常温で一定湿度のものとさせて、こ
れら温度や湿度に影響されることなく穀物の水分値のみ
に基づいて正確な温度制御を可能とさせることができる
もので、温度制御を正確にして容易なものとさせること
ができて穀物の品質保持が図れる。"Function" According to the present invention, the temperature and humidity of the hot air taken into the dryer are kept constant at room temperature, and the moisture content of the grains is reduced without being affected by these temperatures and humidity. It is possible to perform accurate temperature control based only on the value, and temperature control can be made accurate and easy, and the quality of grain can be maintained.
「実施例」
以下本発明の一実施例を図面に基づいて詳述する。第1
図は乾燥部の説明図、第2図は施設全体の平面説明図、
第3図は同作業工程説明図であり、個人別・荷口別に搬
入される原料であ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、粗選後備人別・荷口別に筒口重量と水
分が測定される荷受計量機(6) と、前記計量機(6
)から生籾をビン投入昇降機(7)及びトップコンベア
(8)を介して搬入して乾燥前に一時滞荷させる貯蔵ビ
ン(9)・・・とを荷受部(11に設けている。``Example'' An example of the present invention will be described in detail below based on the drawings. 1st
The figure is an explanatory diagram of the drying section, Figure 2 is a plan explanatory diagram of the entire facility,
Figure 3 is an explanatory diagram of the same work process, which is equipped with a cargo receiving section (1) that receives raw paddy, which is the raw material brought in individually and by cargo, from a cargo receiving hopper (2) to a receiving conveyor (3) and an elevator (4). ); a rough sorter (5) that removes impurities from the paddy that is received through the grain picker; a receiving weighing machine (6) that measures the tube mouth weight and moisture content for each rough sorter and each consignment; and the weighing machine. (6
), storage bins (9) are provided in the cargo receiving section (11), into which raw paddy is carried in via a bin loading elevator (7) and a top conveyor (8) and temporarily stored therein before drying.
また、荷受後の生籾を乾燥と一時休止の繰り返しで粒内
水分の均一化を図って胴割れを防止しながら乾燥する乾
燥部(lO)を備えるもので、前記貯蔵ビン(9)から
生籾をボトムコンベア(11)及びビン排出昇降機(1
2)及びドライヤ投入昇降機(13)を介して搬入して
1回当り毎に所定%の含有水分を除去させる火力乾燥機
であるドライヤ(14)と、前記ドライヤ(14)から
取出した一時乾燥休止の籾をドライヤ取出コンベア(1
5)及び昇降機(16)と乾燥サイロ昇降機(17)及
び投入コンベア(18)を介して搬入する調質用タンク
である副サイロ(19)と、前記副サイロ(19)から
取出した半乾燥籾を乾燥サイロ取出コンベア(20)を
介して再び前記ドライヤ(14)に送り出す乾燥サイロ
取出昇降機(21)とを乾燥部(lO)に備え、該乾燥
部(10)での乾燥籾を貯留部(22)に送り出すよう
に構成している。In addition, it is equipped with a drying section (lO) that dries the raw paddy after receiving it by repeating drying and temporary suspension to equalize the moisture inside the grain and prevent shell cracking. The paddy is transferred to the bottom conveyor (11) and the bin discharge elevator (1).
2) and a dryer (14), which is a thermal dryer that is carried in via a dryer loading elevator (13) and removes a predetermined percentage of moisture each time, and a temporary drying stop that is taken out from the dryer (14). The paddy is removed from the dryer by the conveyor (1
5) and an elevator (16), a drying silo elevator (17), a sub-silo (19) which is a tempering tank carried in via a charging conveyor (18), and semi-dried paddy taken out from the sub-silo (19). The drying section (lO) is equipped with a drying silo take-out elevator (21) that sends the paddy to the dryer (14) again via the drying silo take-out conveyor (20), and the dried paddy in the drying section (10) is transferred to the storage section ( 22).
さらに前記貯留部(22)は、前記乾燥部(lO)から
の乾燥籾を前記コンベア(15)及び昇降機(161(
171及びコンベア(18)を介し搬入して貯留する貯
蔵サイロである主サイロ(23)と、前記サイロ(23
)より取出した乾燥籾をサイロ取出コンベア(24)及
び精選機投入昇降機(25)を介し搬入して乾燥籾より
夾雑物を除去分離する精選機(26)と、精選機(26
)から取出される精選初成いは脱拌米を売渡計量機(2
7)及び精選機取出昇降機(28)或いは脱秤米昇降機
(29)を介し投入する調節タンク(30)と、前記精
選機(26)から取出される芒付籾の脱芒を行う脱芒機
(31)と、売渡計量後の精選籾を精選サイロ投入コン
ベア(32)を介し主サイロ(23)に搬入する精選サ
イロ昇降機(33)とを備え、前記調節タンク(30)
の精選籾を次工程の調製出荷部(34)に送り出すよう
に構成している。Further, the storage section (22) stores dried paddy from the drying section (lO) through the conveyor (15) and the elevator (161(
171 and a main silo (23), which is a storage silo carried in and stored via a conveyor (18), and the silo (23).
) is transported through a silo take-out conveyor (24) and a sorting machine input elevator (25), and a sorting machine (26) that removes impurities from the dry paddy and separates it, and a sorting machine (26).
) The carefully selected first-grown and demixed rice is sold to a weighing machine (2).
7) and an adjustment tank (30) into which the rice is fed via the sorting machine take-out elevator (28) or the rice deweighing elevator (29), and an awning machine for removing the awns from the awned paddy taken out from the sorting machine (26). (31), and a selected silo elevator (33) for transporting selected paddy after weighing for sale to the main silo (23) via a selected silo input conveyor (32), and the adjustment tank (30)
The selected paddy is sent to the preparation and shipping section (34) for the next process.
前記調節出荷部(34)は、前記調節タンク(30)か
らの精選籾を籾昇降機(35)を介して搬入して脱拌す
る籾摺機(36)と、籾摺機(36)からの脱拌混合米
を混合米昇降機(37)を介して搬入して良玄米のみを
取出す揺動選別機(38)と、揺動選別機(38)から
の玄米を振動コンベア(39)及び玄米昇降機(40)
を介して搬入して所定粒子のものに粒選する粒選別機(
41)と、粒選後の玄米より石抜きを行う石抜機(42
)と、石抜き後の良玄米を良玄米用昇降機(43)を介
して投入するフレコン(フレキシブルコンテナ) (4
4)用の出荷タンク(45)と、包装出荷用タンク(4
6)と、前記粒選別機(41)から取出される未熟米を
未熟米昇降機(47)及び脱拌米昇降機(29)を介し
搬入する未熟米タンク(48)と、前記良玄米昇降機(
43)からの良玄米を精米機用昇降機(49)及び玄米
タンク(50)及び精米機151)を介し投入する白米
タンク(52)とを備えている。The adjustment and shipping section (34) includes a huller (36) that transports selected paddy from the adjustment tank (30) via a paddy elevator (35) and removes the rice from the huller (36), and A vibrating sorter (38) transports the demixed mixed rice through a mixed rice elevator (37) and extracts only good brown rice, and a vibrating conveyor (39) and a brown rice elevator convey the brown rice from the vibrating sorter (38). (40)
A grain sorter (
41) and a stone removal machine (42) that removes stones from brown rice after grain selection.
), and a flexible container (4) into which the good brown rice after destoning is fed via the good brown rice elevator (43).
4) and a packaging and shipping tank (45).
6), an unripe rice tank (48) into which the unripe rice taken out from the grain sorter (41) is carried in via the unripe rice elevator (47) and the demixing rice elevator (29), and the good brown rice elevator (48);
The machine is equipped with a rice milling machine elevator (49), a brown rice tank (50), and a polished rice tank (52) into which good brown rice from the rice milling machine 151) is fed.
なお、(53)は荷受室、(54)は事務室、(55)
は主操作室、(56)は前記貯蔵ビン(9)の送風機(
57)を内設する送風機室、(58)は前記貯蔵ビン(
9)に並設する除塵室、(59)は前記除塵室158)
に隣接させる湿式除塵設備、(60)は製品置場である
。In addition, (53) is the receiving room, (54) is the office, (55)
(56) is the main operation room, and (56) is the blower (
(57) is a blower room in which the storage bin (58) is installed;
(9) is the dust removal chamber installed in parallel with the dust removal chamber 158), (59) is the dust removal chamber 158)
(60) is a product storage area.
ところで、常温定湿の空気を供給する乾燥空気発生機(
61)を前記ビン(9)とドライヤ(14)に設けるも
ので、該発生機(61)は冷却除湿用エバポレータC6
2)と、常温復元用コンデンサ(63)と、除湿調節フ
ラップ(64)を介し湿り空気を取入れる外気取入ダク
ト(65)と、前記エバポレータ(62)及びコンデン
サ(63)で発生する常温除湿空気と前記ダクト(65
)からの湿り空気とを混合させた常温定湿空気の風量を
調節する定湿用ダンパー(66)とを備え、第4図に示
す如く前記貯蔵ビン(9)にあっては予備乾燥用の送風
機(57)に発生機(61)を接続させ、発生機(61
)での常温で一定湿度の空気を送風機(57)に吸込ま
せて各ビン室(9a)内に送り込むことにより、各ビン
室(9a)内に貯蔵される生籾間の水分差を減少させる
如く予備乾燥するように構成している。By the way, a dry air generator that supplies air at room temperature and constant humidity (
61) is provided in the bottle (9) and the dryer (14), and the generator (61) is connected to the cooling and dehumidifying evaporator C6.
2), a normal temperature restoration condenser (63), an outside air intake duct (65) that takes in humid air via a dehumidification adjustment flap (64), and a normal temperature dehumidification generated in the evaporator (62) and condenser (63). Air and said duct (65
), and the storage bin (9) is equipped with a damper for pre-drying (66) which adjusts the flow rate of room-temperature and constant-humidity air mixed with humid air from Connect the generator (61) to the blower (57),
), the air at room temperature and constant humidity is sucked into the blower (57) and sent into each bin room (9a), thereby reducing the moisture difference between the raw rice stored in each bin room (9a). It is designed to be pre-dried as described above.
また第1図に示す如く、前記ドライヤ(14)はコンデ
ンスタンク(67)内の籾を、ルーバーベツド構造の上
下通風床板+681 (691上で移動させるエンドレ
ス状のスラットチェン搬送体(70)に供給し、該搬送
体(70)による籾の流動中にバーナ(71)からの熱
風を送風機(72)により籾に供給して、所定の水分値
まで乾燥した籾を穀物乾燥取出口(73)を介し前記取
出コンベア(15)に取出すように設けたもので、該ド
ライヤ(14)の防音室(74)の外気取入口(74a
)に前記発生機(61)を設けて、該発生機(61)か
ら供給される常温で一定湿度の空気を前記送風機(72
)による吸込力でドライヤ(14)内に取入れて、定湿
の熱風でもって籾の乾燥を行うように構成している。As shown in FIG. 1, the dryer (14) supplies the paddy in the condensation tank (67) to an endless slat chain conveyor (70) that is moved on top and bottom ventilation floor plates +681 (691) with a louver bed structure. Then, while the paddy is flowing by the conveyor (70), hot air from the burner (71) is supplied to the paddy by the blower (72), and the paddy is dried to a predetermined moisture value and then passed through the grain drying outlet (73). The outside air intake port (74a) of the soundproof chamber (74) of the dryer (14) is
) is provided with the generator (61), and the air at normal temperature and constant humidity supplied from the generator (61) is supplied to the blower (72).
) is taken into the dryer (14) by suction force, and the paddy is dried using constant-humidity hot air.
そして第5図にも示す如(、前記防音室(74)の外気
取入口(74a)近傍に取入れる空気の温度と湿度を検
出する温度センサ(75)及び湿度センサ(76)を設
けると共に、前記コンデンスタンク(67)に該タンク
(67)内の籾の水分値を検出する水分センサ(77)
を設けて、前記発生機(61)の湿度調節機構(78)
とドライヤ(14)の熱風温度調節機構(79)とを駆
動制御する制御手段である中央制御装置(80)にこれ
ら各センサ(75) (761(771を出力接続させ
て、各センサ(751(76) (771の検出値に基
づいて前記発生機(61)の除湿制御或いはドライヤ(
14)の熱風温度制御を行わしめるように構成している
。As shown in FIG. 5, a temperature sensor (75) and a humidity sensor (76) are provided near the outside air intake port (74a) of the soundproof room (74) to detect the temperature and humidity of the air taken in. A moisture sensor (77) is provided in the condensation tank (67) to detect the moisture value of the paddy in the tank (67).
and a humidity adjustment mechanism (78) of the generator (61).
The outputs of these sensors (75) (761 (771) are connected to the central controller (80) which is a control means for driving and controlling the hot air temperature adjustment mechanism (79) of the dryer (14). 76) (Dehumidification control of the generator (61) or dryer (based on the detected value of 771)
14) The hot air temperature control is performed.
本実施例は上記の如く構成するものにして、前記貯蔵ビ
ン(9)での滞荷中に発生機(61)からの常温定湿空
気によって各ビン室(9a)内の籾の予備乾燥が行われ
るもので、この場合常温定湿空気を用いることによって
ビン室(9a)内の空気を加温せず、空気中の水分を除
去して一定湿度の乾いた空気を送って籾量に水分差の殆
どない略均−状態の平衡含水率まで自然に乾燥させて、
後工程のドライヤ(14)での作業の際、乾燥温度を品
質低下を起させることのない低い温度に抑えることがで
きて過乾燥となって胴割れ粒が多量に発生するなどの不
都合を防止している。The present embodiment is constructed as described above, and the paddy in each bin chamber (9a) is pre-dried by normal temperature and constant humidity air from the generator (61) while the paddy is stored in the storage bin (9). In this case, the air in the bin room (9a) is not heated by using normal temperature and constant humidity air, and the moisture in the air is removed and dry air with a constant humidity is sent to increase the amount of paddy. Naturally dry to an equilibrium moisture content with almost no difference,
During work in the dryer (14) in the post-process, the drying temperature can be kept low enough to avoid quality deterioration, thereby preventing inconveniences such as excessive drying and the generation of large amounts of cracked grains. are doing.
また、前記ドライヤ(14)にあっては前記発生機(6
1)からの常温定湿空気を取入れることによって、第6
図のフローチャートに示される如(外気温度及び湿度に
影響されることのないこれらを一定として籾の水分値の
みに応じて算出された温度にドライヤ(14)の熱風温
度が調節機構(79)により調節され乾燥が行われるも
ので、この際穀物の品質安全保証温度の上限となる例え
ば4G’Cの適正温度を越えるとき、前記調節機構(7
8)でもって取入空気の設定湿度をさらに小さくなる状
態に調節してこのドライヤ(14)の熱風温度を適正温
度以下とするものである。このようにドライヤ(14)
に取入れる空気の湿度及び温度を常に一定保持させるこ
とにより、籾の水分値と乾燥温度との単純な一つの関数
関係により正確に乾燥温度が算出されその温度設定が行
われ、この温度制御を簡単なものとさせることができる
。Moreover, in the dryer (14), the generator (6
By introducing normal temperature and constant humidity air from 1), the 6th
As shown in the flowchart in the figure, the temperature of the hot air from the dryer (14) is adjusted by the adjustment mechanism (79) to a temperature calculated only according to the moisture value of the paddy, keeping these constant and not affected by outside temperature and humidity. The adjustment mechanism (7
8) The set humidity of the intake air is further adjusted to a lower value, and the temperature of the hot air from this dryer (14) is kept below the appropriate temperature. Dryer like this (14)
By always keeping the humidity and temperature of the air taken into the rice constant, the drying temperature can be accurately calculated and set based on a simple functional relationship between the moisture value of the paddy and the drying temperature. It can be made simple.
「発明の効果」
以上実施例からも明らかなように本発明は、穀物乾燥機
(14)の外気取入口(74a)に、常温定湿空気を供
給する乾燥空気発生機(61)を設けたものであるから
、乾燥機(14)での取入空気を常温で一定湿度のもの
とさせることができて、取入空気に影響されることのな
い常に安定した良好な乾燥を可能にできる。"Effects of the Invention" As is clear from the above embodiments, the present invention provides a dry air generator (61) for supplying normal temperature and constant humidity air to the outside air intake port (74a) of the grain dryer (14). Therefore, the air taken into the dryer (14) can be kept at room temperature and constant humidity, making it possible to always perform stable and good drying without being affected by the air taken in.
そして、穀物乾燥機(14)の乾燥温度制御手段(80
)に、発生機(61)からの供給空気の湿度及び温度デ
ータを入力させて、これらデータ値に基づいて穀物乾燥
機(14)における乾燥温度の制御を行うものであるか
ら、取入空気の湿度及び温度を定数としての水分値のみ
に基づく温度制御が可能となって、この温度制御を容易
にして正確なものとさせることができて、穀物の品質保
持も図れるなど顕著な効果を奏する。The drying temperature control means (80) of the grain dryer (14)
) inputs the humidity and temperature data of the air supplied from the generator (61) and controls the drying temperature in the grain dryer (14) based on these data values. Temperature control based only on the moisture value with humidity and temperature as constants becomes possible, this temperature control can be made easy and accurate, and the quality of the grain can be maintained, which is a remarkable effect.
第1図は乾燥部の説明図、第2図は施設全体の平面説明
図、第3図は同作業工程説明図、第4図は貯蔵ビン部の
説明図、第5図は制御回路図、第6図はフローチャート
である。
(14)・・・ ドライヤ(乾燥機)(61)・・・
発 生 機(74al・・・外気取入口Fig. 1 is an explanatory diagram of the drying section, Fig. 2 is a plan explanatory diagram of the entire facility, Fig. 3 is an explanatory diagram of the work process, Fig. 4 is an explanatory diagram of the storage bin section, Fig. 5 is a control circuit diagram, FIG. 6 is a flowchart. (14)... Dryer (dryer) (61)...
Generator (74al...Outside air intake
Claims (2)
する乾燥空気発生機を設けたことを特徴とする穀物乾燥
装置。(1) A grain drying device characterized in that a dry air generator for supplying room-temperature and constant-humidity air is provided at an outside air intake port of the grain dryer.
供給空気の湿度及び温度データを入力させて、これらデ
ータ値に基づいて穀物乾燥機における乾燥温度の制御を
行うように構成したことを特徴とする第1項記載の穀物
乾燥装置。(2) The drying temperature control means of the grain dryer is configured to input humidity and temperature data of the air supplied from the generator, and control the drying temperature in the grain dryer based on these data values. 2. The grain drying device according to claim 1, characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1329837A JP2808030B2 (en) | 1989-12-19 | 1989-12-19 | Grain drying equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1329837A JP2808030B2 (en) | 1989-12-19 | 1989-12-19 | Grain drying equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03191288A true JPH03191288A (en) | 1991-08-21 |
JP2808030B2 JP2808030B2 (en) | 1998-10-08 |
Family
ID=18225784
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1329837A Expired - Fee Related JP2808030B2 (en) | 1989-12-19 | 1989-12-19 | Grain drying equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2808030B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0682120A (en) * | 1992-09-01 | 1994-03-22 | Kubota Corp | Drying storage method for agricultural and fishery product |
CN107521957A (en) * | 2017-08-31 | 2017-12-29 | 中山市程博工业产品设计有限公司 | A kind of novel band drying machine feeding rack |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62106280A (en) * | 1985-10-31 | 1987-05-16 | 株式会社 セキネ | Cereal drier |
-
1989
- 1989-12-19 JP JP1329837A patent/JP2808030B2/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62106280A (en) * | 1985-10-31 | 1987-05-16 | 株式会社 セキネ | Cereal drier |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0682120A (en) * | 1992-09-01 | 1994-03-22 | Kubota Corp | Drying storage method for agricultural and fishery product |
CN107521957A (en) * | 2017-08-31 | 2017-12-29 | 中山市程博工业产品设计有限公司 | A kind of novel band drying machine feeding rack |
CN107521957B (en) * | 2017-08-31 | 2019-07-12 | 中山市程博工业产品设计有限公司 | A kind of novel band drying machine feeding rack |
Also Published As
Publication number | Publication date |
---|---|
JP2808030B2 (en) | 1998-10-08 |
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