JPH0141295B2 - - Google Patents
Info
- Publication number
- JPH0141295B2 JPH0141295B2 JP55060001A JP6000180A JPH0141295B2 JP H0141295 B2 JPH0141295 B2 JP H0141295B2 JP 55060001 A JP55060001 A JP 55060001A JP 6000180 A JP6000180 A JP 6000180A JP H0141295 B2 JPH0141295 B2 JP H0141295B2
- Authority
- JP
- Japan
- Prior art keywords
- gas
- oxygen
- moisture
- storage
- food
- 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.)
- Expired
Links
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- Storage Of Harvested Produce (AREA)
- Drying Of Solid Materials (AREA)
- Storage Of Fruits Or Vegetables (AREA)
Description
【発明の詳細な説明】
現在、一般に食糧、飼糧等を貯蔵するのは、予
め別途に熱風等によつて乾燥したものをサイロ等
貯蔵庫にいれて保存している。熱風等によつて食
糧、飼糧等を乾燥すれば、変質して味が低下する
のみならず、経済的にも不利であり、又手数がか
かる。更に、保存中に貯蔵庫に外部から湿つた空
気が進入したり、貯蔵庫内は外部の大気と大体同
一湿度であるため害虫やねづみ等のため損傷をう
けたり、又かび等の有害な物質も発生する。DETAILED DESCRIPTION OF THE INVENTION Currently, food, feed, etc. are generally stored by separately drying them with hot air or the like and storing them in a storage warehouse such as a silo. Drying food, fodder, etc. with hot air or the like not only deteriorates the quality and taste, but is also economically disadvantageous and time-consuming. Furthermore, humid air may enter the storage room from outside during storage, and since the humidity inside the storage room is roughly the same as the outside air, it may be damaged by pests, rats, etc., and harmful substances such as mold may also enter the storage room. Occur.
本発明は、生の状態にて食糧等を貯蔵庫に投入
して、熱風の代りに、乾燥ガスを貯蔵庫内に通気
循環させて、貯蔵庫内のガス湿度を著しく低い状
態におき、自然に常温あるいは低温にて乾燥させ
る方法である。 In the present invention, food etc. are put into a storage in a raw state, dry gas is circulated through the storage instead of hot air, the gas humidity inside the storage is extremely low, and the food is naturally brought to room temperature or This is a method of drying at low temperatures.
天日乾燥法おいては、湿度のある大気中にて自
然乾燥させるが、これは物の水分と大気の湿度と
の湿度差によつて乾燥させている。 In the solar drying method, the material is naturally dried in a humid atmosphere, and this is done due to the difference in humidity between the moisture of the material and the humidity of the atmosphere.
本発明は、湿度のある大気の代りに、乾燥ガス
を常温あるいは低温にて貯蔵庫内に吹きこみ食糧
の水分を蒸発させた排気ガスは別に設けられたガ
ス乾燥装置にて再び乾燥ガスとして循環再使用す
る。この場合、乾燥ガスを使用するため天日乾燥
のときより、被乾燥物と乾燥ガスとの湿度差が大
きく乾燥速度が早く天日乾燥の約10倍の早さで乾
燥できる。又加熱せずに、常温あるいは低温の乾
燥ガスを用いるため、食糧の変質をきたすことは
ない。又貯蔵庫中のガスは乾燥ガスのため、貯蔵
庫中に有害動物、害虫、発酵菌等は殆んど発生し
ない。又貯蔵内のガス中の酸素濃度が低く、ある
いは殆んどゼロを欲する場合には、チツソ等の不
活性ガスを使用する。この場合外部からの洩れ等
による酸素および貯蔵物からの蒸発水分を取除く
必要がある。外部に、酸素、水分を吸着するカー
ボンモレキラシーブ、シリカゲル等を入れた一対
の吸着塔を設け、これに使用ガスを通じ、吸脱着
を行つて水分および大部分を除いた酸素の一部あ
るいは乾燥ガスを吸着塔の上部より排出して再び
乾燥ガスとして循環再使用する。脱着された脱着
ガスは酸素および水分含有量の多いガスであるた
め、これを外部に廃棄する。この廃棄ガスに相当
するだけ、ガスを補給したい場合には、先の一対
の吸着塔に通気する循環ガスに、外部空気を混入
させることにより補給する。次に、本発明を図面
によつて更に詳細に説明する。 In the present invention, instead of humid air, dry gas is blown into the storage at room temperature or low temperature, and the exhaust gas that evaporates the moisture in the food is recycled as dry gas again in a separately provided gas drying device. use. In this case, since drying gas is used, there is a greater humidity difference between the material to be dried and the drying gas than in solar drying, and the drying speed is faster, which is approximately 10 times faster than solar drying. Furthermore, since dry gas at room temperature or low temperature is used without heating, the food does not deteriorate in quality. Furthermore, since the gas in the storage is dry gas, harmful animals, pests, fermentation bacteria, etc. are hardly generated in the storage. In addition, if the oxygen concentration in the gas in the storage is low or desired to be almost zero, an inert gas such as chloride gas is used. In this case, it is necessary to remove oxygen due to leakage from the outside and evaporated moisture from the stored material. A pair of adsorption towers containing carbon molecular sieves, silica gel, etc. that adsorb oxygen and moisture are installed externally, and the gas used is passed through these towers, where adsorption and desorption is performed to remove a portion of the oxygen and dry part of the oxygen. The gas is discharged from the top of the adsorption tower and recycled and reused as dry gas. Since the desorbed gas contains a large amount of oxygen and water, it is disposed of outside. If it is desired to replenish gas in an amount equivalent to this waste gas, replenishment is done by mixing external air into the circulating gas vented to the previous pair of adsorption towers. Next, the present invention will be explained in more detail with reference to the drawings.
貯蔵庫1中に投入口2より食糧等を投入し、密
閉した後に、ブローワー16によつてパイプ17
から空気あるいはチツソ、炭酸ガス等イナートガ
スを貯蔵庫内にふきこむ。排出されたガスはパイ
プ4を通して一対の吸着塔AあるいはA′のいづ
れかにバルブ5ああるいは5′を通じて通気され
る。 After putting food etc. into the storage 1 through the input port 2 and sealing it, the blower 16 blows the food into the pipe 17.
Inert gas such as air or carbon dioxide gas is blown into the storage chamber. The discharged gas is vented through a pipe 4 to either one of the pair of adsorption towers A or A' through a valve 5 or 5'.
A,A′はタイマによつて切りかえられ一方が
ガスを通気して吸着工程のときは、他方は真空ポ
ンプ10によつて減圧脱着工程を行う。 A and A' are switched by a timer, and when one is in the adsorption process by aerating gas, the other is in the depressurization desorption process by the vacuum pump 10.
ガス中の水分および酸素を取り除く目的のため
に、A,A′塔内には、水分および酸素を可逆的
に吸着、脱着し得る吸着剤、例えばカーボンモレ
キラシーブを収納しておく。A,A′塔内には、
上記吸着剤の他に、シリカゲル、ゼオライト、活
性炭等の他の吸着剤を層状に、或いは上記吸着剤
との混合層の形で収納してもよい。このようにし
たA,A′塔内にガスを通過させることによつて
露点−75℃迄乾燥された実質的に水分を含有せ
ず、酸素を少量しか、あるいは実質的に含有しな
いガスを製造できる。 For the purpose of removing moisture and oxygen from the gas, adsorbents capable of reversibly adsorbing and desorbing moisture and oxygen, such as carbon molecular sieves, are stored in the A and A' columns. Inside towers A and A',
In addition to the above adsorbents, other adsorbents such as silica gel, zeolite, and activated carbon may be accommodated in a layered form or in the form of a mixed layer with the above adsorbents. By passing the gas through the A and A' towers, a gas that is dried to a dew point of -75°C and contains substantially no moisture and only a small amount or substantially no oxygen is produced. can.
吸着塔Aの下部より吹きこまれたガスは塔内で
水分および酸素が吸着されて乾燥ガスとなりバル
ブ6を経てパイプ7、ブローワー16、パイプ1
7を経て貯蔵庫内に循環される。 The gas blown into the lower part of the adsorption tower A absorbs moisture and oxygen in the tower and becomes dry gas through the valve 6 to the pipe 7, the blower 16, and the pipe 1.
7 and then circulated into the storage.
吸着塔A内に、酸素吸着剤をも封入した場合に
は酸素を取除かれた乾燥ガスがバルブ6を経て排
出される。酸素は0.1%以下迄殆んど取除くこと
ができるが、酸素濃度はA,A′の切りかえ時間
によつてコントロールできる。 When an oxygen adsorbent is also enclosed in the adsorption tower A, the dry gas from which oxygen has been removed is discharged through the valve 6. Most of the oxygen can be removed to 0.1% or less, but the oxygen concentration can be controlled by changing the switching time of A and A'.
吸着塔A′に吸着工程が移つたときに、吸着塔
Aは脱着工程に入りバルブ5,6が閉じて、バル
ブ9が開き真空ポンプ10によつて塔内は減圧と
なる。この時バルブ8を通じて小量の乾燥ガスが
吸着塔A′より入り吸着されている水分および酸
素が完全に脱着される。脱着されたガスは、タン
ク11、パイプ12、バルブ13を経て、パイプ
4からの元ガスと混合されて吸着塔A内に通気さ
れる。吸着塔A,A′の吸脱着のくりかえしによ
つて排出される脱着ガス中の水分濃度は次第に濃
厚となりタンク11内に液体として溜り始め、ガ
スは乾燥ガスと液体水分とに完全分離されて、貯
蔵中の食糧からの蒸発水分は液体としてタンク1
1内に取出される。 When the adsorption step is transferred to adsorption tower A', adsorption tower A enters the desorption step, valves 5 and 6 are closed, valve 9 is opened, and the pressure inside the tower is reduced by the vacuum pump 10. At this time, a small amount of dry gas enters from the adsorption tower A' through valve 8, and the adsorbed moisture and oxygen are completely desorbed. The desorbed gas passes through the tank 11, the pipe 12, and the valve 13, is mixed with the original gas from the pipe 4, and is vented into the adsorption tower A. The moisture concentration in the desorbed gas discharged through repeated adsorption and desorption in the adsorption towers A and A' gradually becomes thicker and begins to accumulate as a liquid in the tank 11, and the gas is completely separated into dry gas and liquid moisture. Evaporated water from stored food is stored in tank 1 as a liquid.
It is taken out within 1.
吸着塔A,A′内に酸素吸着剤を納入してある
場合には、脱着ガスは酸素濃度が濃厚になつて
も、大気圧で液化せぬため、バルブ14を通して
外部に放出する。放出によつて系内が減圧になる
ため、これを避ける必要がある時には、バルブ1
5を通じて外部より空気を必要量を補給する。 If an oxygen adsorbent is provided in the adsorption towers A and A', the desorbed gas will not be liquefied at atmospheric pressure even if the oxygen concentration becomes high, and will be discharged to the outside through the valve 14. Since the pressure inside the system will be reduced due to the release, if it is necessary to avoid this, please use valve 1.
5, the required amount of air is supplied from the outside.
以上の操作によつて、貯蔵庫1内には常に乾燥
ガスが送入され、被乾燥物中の水分を蒸発させて
乾燥することができる。 By the above operation, drying gas is constantly fed into the storage 1, and the moisture in the dried material can be evaporated and dried.
露点−75℃の乾燥ガスを循環させる場合には被
乾燥壱を絶乾状態に迄乾燥できるが、食糧等では
其の必要がなく、かえつて其の品質を損うため、
ある一定の乾燥度に保つことが望しい。其のた
め、貯蔵庫内の被乾燥物の湿度計18をそう入し、
被乾燥物が一定の湿度になつたとき、吸着塔の運
転およびブローワー16の運転を自働的に止めて
放置し、何等かの理由で再び水分が上昇したとき
に、自働的に吸着塔およびブローワー16の運転
の開始することができる。又、チツソ等イナート
ガスによる運転の場合には酸素濃度計19によつ
て、乾燥ガス中の酸素濃度を検知し、吸着塔A,
A′の切りかえ時間をコントロールして、乾燥ガ
ス中の酸素濃度を一定に保つことができる。 When circulating a drying gas with a dew point of -75°C, the material to be dried can be dried to an absolutely dry state, but this is not necessary for foodstuffs, etc., and would actually impair their quality.
It is desirable to maintain a certain level of dryness. Therefore, put a hygrometer 18 of the material to be dried in the storage room,
When the humidity of the material to be dried reaches a certain level, the operation of the adsorption tower and the operation of the blower 16 are automatically stopped and left, and when the moisture content rises again for some reason, the adsorption tower is automatically stopped. And operation of the blower 16 can be started. In addition, in the case of operation using inert gas such as Chitsuso, the oxygen concentration in the dry gas is detected by the oxygen concentration meter 19, and the adsorption tower A,
By controlling the switching time of A′, the oxygen concentration in the drying gas can be kept constant.
実施例 図に示した方法にて、もみ米を乾燥した。Example The rice was dried using the method shown in the figure.
もみ米 10Kg
初期水分 24%
乾燥材 150m/mφ×1000m/mH
ローワー 100/分
空気温度30℃
吸着塔 50m/mφ×300m/mH 2塔
カーボンモレキラシーブ 300
g/塔
A,A′塔切替時間 10分
以上の条件にて12時間運転した結果、もみ米の
水分は約8%になつた。又、タンク11中には約
140gの水分が採取された。又、循環乾燥ガスの
水分は露点約−70℃であつた。 Rice 10Kg Initial moisture 24% Drying material 150m/mφ×1000m/mH Lower 100/min Air temperature 30℃ Adsorption tower 50m/mφ×300m/mH 2 towers Carbon molecular sieve 300
g/tower A, A' tower switching time 10 minutes As a result of operating for 12 hours under the above conditions, the moisture content of the rice was approximately 8%. Also, in tank 11 there are approximately
140g of water was collected. Further, the water content of the circulating drying gas had a dew point of about -70°C.
図面は、食糧、飼糧等の乾燥貯蔵法のフローシ
ートである。
1……貯蔵庫(乾燥機兼用)、2……原料投入
口、3……乾燥原料取出口、4……湿りガス出口
パイプ、5,5′……吸着塔入口ガスバルブ、6,
6′……吸着塔出口乾燥ガスバルブ、7……乾燥
ガス循環パイプ、8……吸着塔戻しガスバルブ、
9,9′……吸着塔減圧用バルブ、10……真空
ポンプ、11……凝縮水タンク、12……吸着塔
への循環ガスパイプ、13……吸着塔への循環バ
ルブ、14……ガス排出バルブ、15……ガス封
入バルブ、16……送風機、17……パイプ、1
8……湿度計、19……酸素濃度計、A,A′…
…吸着塔。
The drawing is a flow sheet of a dry storage method for food, feed, etc. 1... Storage (double use as dryer), 2... Raw material input port, 3... Dry raw material outlet, 4... Wet gas outlet pipe, 5, 5'... Adsorption tower inlet gas valve, 6,
6'...Adsorption tower outlet dry gas valve, 7...Dry gas circulation pipe, 8...Adsorption tower return gas valve,
9,9'... Valve for depressurizing the adsorption tower, 10... Vacuum pump, 11... Condensed water tank, 12... Circulation gas pipe to the adsorption tower, 13... Circulation valve to the adsorption tower, 14... Gas discharge Valve, 15...Gas filling valve, 16...Blower, 17...Pipe, 1
8...Hygrometer, 19...Oxygen concentration meter, A, A'...
...Adsorption tower.
Claims (1)
酸素を少量しかあるいは実質的に含有しないガ
スを貯蔵庫にふきこむ工程と、 ロ 貯蔵物から蒸発した水分および少量の酸素を
含むガスを、貯蔵庫より取り出す工程と、 ハ 貯蔵庫より取り出したガスを、水分および酸
素を可逆的に吸着、脱着し得る吸着剤と接触さ
せて、該ガスからガス中に含まれる水分および
酸素を吸着除去する工程と、 ニ 該ハ)の工程で得られた実質的に水分を含有
せず酸素を少量しかあるいは実質的に含有しな
いガスを貯蔵庫に循環ふきこむ工程と、 ホ 該ハ)の工程で水分および酸素を吸着した該
逆着剤を、吸着時の圧力よりも低い圧力の下に
該水分および酸素を含有しないガスの一部と接
触させて吸着した水分および酸素を脱着させる
工程 との組合せからなることを特徴とする食糧、飼糧
等の乾燥貯蔵方法。[Scope of Claims] 1. Storing food, feed, etc. in a storage and sealing it; b. Blowing into the storage a gas at room temperature or low temperature that contains substantially no moisture and only a small amount or substantially of oxygen; (b) A step in which gas containing moisture and a small amount of oxygen that has evaporated from the storage is taken out from the storage; (c) The gas taken out from the storage is brought into contact with an adsorbent that can reversibly adsorb and desorb moisture and oxygen; A step of adsorbing and removing moisture and oxygen contained in the gas from the gas, and (d) circulating the gas obtained in the step (c), which contains substantially no moisture and only a small amount or substantially of oxygen, to a storage. The reverse adsorbent that has adsorbed moisture and oxygen in the step of b) is brought into contact with a portion of the gas that does not contain moisture and oxygen under a pressure lower than the pressure during adsorption to adsorb it. 1. A dry storage method for food, feed, etc., characterized by comprising a step of desorbing moisture and oxygen.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6000180A JPS56158029A (en) | 1980-05-08 | 1980-05-08 | Drying and storing method of foodstuff and feedstuff |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6000180A JPS56158029A (en) | 1980-05-08 | 1980-05-08 | Drying and storing method of foodstuff and feedstuff |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56158029A JPS56158029A (en) | 1981-12-05 |
| JPH0141295B2 true JPH0141295B2 (en) | 1989-09-05 |
Family
ID=13129424
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6000180A Granted JPS56158029A (en) | 1980-05-08 | 1980-05-08 | Drying and storing method of foodstuff and feedstuff |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS56158029A (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62272936A (en) * | 1986-05-20 | 1987-11-27 | Tokiwa Denki:Kk | Dried food and production thereof |
| DE3760569D1 (en) * | 1986-07-08 | 1989-10-26 | Kohlensaeurewerk Deutschland | A process for drying of plant or animal substances |
| JPS63223481A (en) * | 1987-03-13 | 1988-09-16 | 日本真空技術株式会社 | Drier for cereals |
| JPH0733110Y2 (en) * | 1988-07-07 | 1995-07-31 | 株式会社松井製作所 | Dehumidifying and drying device using an inert gas as a drying medium |
| JPH0311002A (en) * | 1989-06-09 | 1991-01-18 | Hitachi Ltd | Production of dry flower-accommodating vessel and producing device |
| JP6775286B2 (en) * | 2015-09-29 | 2020-10-28 | 株式会社松井製作所 | Drying device and drying system equipped with it |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS52136729A (en) * | 1976-05-12 | 1977-11-15 | Ishimori Seifunshiyo Goumei | Method of storing grain* and apparatus therefor |
| JPS5372840A (en) * | 1976-12-09 | 1978-06-28 | Kuri Kagaku Sochi | Low temperature drying method for food |
-
1980
- 1980-05-08 JP JP6000180A patent/JPS56158029A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56158029A (en) | 1981-12-05 |
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