JPS6117462B2 - - Google Patents
Info
- Publication number
- JPS6117462B2 JPS6117462B2 JP14550778A JP14550778A JPS6117462B2 JP S6117462 B2 JPS6117462 B2 JP S6117462B2 JP 14550778 A JP14550778 A JP 14550778A JP 14550778 A JP14550778 A JP 14550778A JP S6117462 B2 JPS6117462 B2 JP S6117462B2
- Authority
- JP
- Japan
- Prior art keywords
- oxygen
- chamber
- containing substance
- water
- storage device
- 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
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 21
- 239000001301 oxygen Substances 0.000 claims description 21
- 229910052760 oxygen Inorganic materials 0.000 claims description 21
- 229940123973 Oxygen scavenger Drugs 0.000 claims description 17
- 239000000126 substance Substances 0.000 claims description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- 239000007789 gas Substances 0.000 claims description 15
- 238000010521 absorption reaction Methods 0.000 claims description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 229910001873 dinitrogen Inorganic materials 0.000 description 4
- 235000009419 Fagopyrum esculentum Nutrition 0.000 description 3
- 240000008620 Fagopyrum esculentum Species 0.000 description 3
- QIGBRXMKCJKVMJ-UHFFFAOYSA-N Hydroquinone Chemical compound OC1=CC=C(O)C=C1 QIGBRXMKCJKVMJ-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000006096 absorbing agent Substances 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- WQGWDDDVZFFDIG-UHFFFAOYSA-N pyrogallol Chemical compound OC1=CC=CC(O)=C1O WQGWDDDVZFFDIG-UHFFFAOYSA-N 0.000 description 2
- 230000001953 sensory effect Effects 0.000 description 2
- 241000238631 Hexapoda Species 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229930002875 chlorophyll Natural products 0.000 description 1
- 235000019804 chlorophyll Nutrition 0.000 description 1
- ATNHDLDRLWWWCB-AENOIHSZSA-M chlorophyll a Chemical compound C1([C@@H](C(=O)OC)C(=O)C2=C3C)=C2N2C3=CC(C(CC)=C3C)=[N+]4C3=CC3=C(C=C)C(C)=C5N3[Mg-2]42[N+]2=C1[C@@H](CCC(=O)OC\C=C(/C)CCC[C@H](C)CCC[C@H](C)CCCC(C)C)[C@H](C)C2=C5 ATNHDLDRLWWWCB-AENOIHSZSA-M 0.000 description 1
- 238000006392 deoxygenation reaction Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 description 1
- GRWZHXKQBITJKP-UHFFFAOYSA-L dithionite(2-) Chemical compound [O-]S(=O)S([O-])=O GRWZHXKQBITJKP-UHFFFAOYSA-L 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000011491 glass wool Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 229940079877 pyrogallol Drugs 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
- 230000005070 ripening Effects 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- DHCDFWKWKRSZHF-UHFFFAOYSA-N sulfurothioic S-acid Chemical compound OS(O)(=O)=S DHCDFWKWKRSZHF-UHFFFAOYSA-N 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Landscapes
- Storage Of Fruits Or Vegetables (AREA)
- Storage Of Harvested Produce (AREA)
Description
本発明は穀類の貯蔵装置に関し、さらに詳しく
は穀類貯蔵庫内でガスを循環しガス中の酸素を脱
酸素剤で除去しうるようにした穀類の貯蔵装置の
改良に関する。
穀類の貯蔵に際してはその呼吸作用に影響する
雰囲気中の酸素を必要限度まで下げ穀類の仮死状
態をつくれば穀類の熟成(追熟)を防ぎ,カビ防
止,防虫になり、また栄養素の酸化劣化を防ぐこ
とができる。
そこで本発明者は穀類貯蔵庫内の酸素を除去す
べく貯蔵庫内のガスを循環しガス中の酸素を脱酸
素剤で除去する方法について種々検討した。脱酸
素剤は通常ガスバリヤー性の袋内に入れられてお
り使用時に開封して用いられるが、開封と同時に
酸素吸収を開始するので、できるだけすみやかに
装填しなければならない欠点がある。特に穀類の
貯蔵には多量の脱酸素剤を必要とするので取り扱
いを容量にすることが望まれる。
本発明はこの課題を解決したものである。すな
わち本発明は密閉しうる穀類貯蔵庫,含水物質
室,脱酸素室及び送風機が循環路を形成してな
り、脱酸素室として水分の非存在下では実質的に
酸素を吸収しないか、又は酸素吸収速度のおそい
脱酸素剤を収容したものであり、系内のガスを循
環することによつて穀類貯蔵庫内の酸素を除去し
うるようにした穀類の貯蔵装置である。
本発明において脱酸素剤は水分の非存在下では
実質的に酸素を吸収しないか、又は酸素吸収速度
のおそいものがあればすべて使用しうる。かかる
脱酸素剤の例としては各種の還元剤,例えば鉄,
亜ニチオン酸塩,チオ硫酸塩,ハイドロキノン,
ピロガロール等を主体とするものであつて水分を
実質的に含有しないものなどがあげられる。
本発明において含水物質は上記の脱酸素剤に水
分を供給して酸素吸収能を発現させるものであれ
ばよく特に制限はないが、平衡温度75以上の物質
が好ましい。例えばグラスウール,ゼオライト,
スポンジ,バルブくず,鉄石の砕いたものに水を
含ませたもの等があげられる。
穀類貯蔵庫は通常サイロが用いられる。脱酸素
室,含水物質室はそれぞれ脱酸素剤,含水物質を
収容する室である。この両室は循環ガスが含水物
質室を通り脱酸素室に入るように配列されるのが
好ましい。とくに含水物質室が脱酸素室と一体化
され、脱酸素室内に包含されてなり該脱酸素室の
下部が含水物質収容部分、上部が脱酸素剤収容部
分であつて下部から上部へ向つて循環ガスが通る
ようにしたものは好適に用いられる。
本発明においては穀類貯蔵庫,含水物質室,脱
酸素室および送風機がその要件となつているが、
必要に応じ他の機構を備えることができる。例え
ば除塵室,清浄室,内気排出口,混合ガス供給
弁、マノメーター監視板などがあげられる。
次に本発明の装置の一例を図面によつて説明す
る。第1図中,1はサイロ,2は送風機,3は脱
酸素室,4は含水物質収容部分,5は脱酸素剤収
容部分,6は窒素ガスボンベである。系内のガス
は送風機2によつて循環され、ガスが含水物質部
分4を経て脱酸素剤収容部分5を通ることによつ
て系内の酸素が除去される。
本発明は脱酸素剤の装填時に酸素を吸収せず、
系内に密浮しガスを循環してはじめて酸素を吸収
するように構成されているので、本発明によれば
脱酸素剤の損失がなく、かつ取扱いが容易なの
で、穀類を好適に貯蔵することができる。
以下に本発明の装置を用いて穀類を貯蔵した例
を示す。
実施例
第1図の装置を用いて試験をした。内容積約14
m2の鋼製サイロにテストサンプルとして玄そば5t
(約10m3)を投入し、脱酸素剤室に脱酸素剤を入
れた。サイロ内部,脱酸素室内部,ブロワー内
部,配管内部等を含め貯蔵装置系内の空気容積は
約10m3であつた。脱酸素した場合の体積減少によ
る負圧のため機器の変形,外気の流入を防ぐため
循環配管に窒素ガスボンベを設け、圧力調節弁に
より常時230〜310mmHgの窒素ガスを導入した。
循環配管にサンプリング口を設け、循環空気中の
酸素濃度,温度,湿度等を測定した。準備終了
後,系内を密封しブロワーを運転し空気循環を始
めたときを「スタート」時点とし、経日的にサイ
ロ内のサンプル(玄そば)を取出し、水分量
(%)、過酸化物価指数(meq/Kg),クロロフイ
ルム(%)等の測定データと官能テストによりサ
ンプルの品質評価を行なつた。その結果を第1表
及び第2表に示す。第1表は酸素濃度変化測定結
果,第2表は玄そば貯蔵テスト結果を示す。
なお比較のため含水物質を用いない場合も同様
に試験した。その結果を第1表,第2表に併記す
る。
The present invention relates to a grain storage device, and more particularly to an improvement in a grain storage device that allows gas to be circulated within the grain storage and oxygen contained in the gas to be removed by an oxygen scavenger. When storing grains, reducing the oxygen in the atmosphere that affects their respiration to the necessary limit and creating a state of suspended animation will prevent grains from ripening (over-ripening), prevent mold and insects, and prevent oxidative deterioration of nutrients. It can be prevented. Therefore, in order to remove the oxygen in the grain storage, the present inventors have studied various methods of circulating the gas in the storage and removing the oxygen in the gas using an oxygen scavenger. Oxygen scavengers are usually placed in gas barrier bags and are opened before use, but they start absorbing oxygen as soon as the bag is opened, so they have the disadvantage that they must be loaded as quickly as possible. In particular, storage of grains requires a large amount of oxygen scavenger, so it is desirable to have a large capacity for handling. The present invention solves this problem. That is, in the present invention, a sealable grain storage, a moisture-containing substance chamber, a deoxidizing chamber, and a blower form a circulation path, and the deoxidizing chamber substantially absorbs no oxygen in the absence of moisture or absorbs no oxygen. This is a grain storage device that accommodates a slow-speed oxygen scavenger and is capable of removing oxygen within the grain storage by circulating gas within the system. In the present invention, any oxygen scavenger can be used as long as it does not substantially absorb oxygen in the absence of moisture or has a slow oxygen absorption rate. Examples of such oxygen scavengers include various reducing agents such as iron,
dithionite, thiosulfate, hydroquinone,
Examples include those mainly containing pyrogallol and the like and containing substantially no water. In the present invention, the water-containing substance is not particularly limited as long as it supplies moisture to the oxygen scavenger to exhibit oxygen absorption ability, but a substance having an equilibrium temperature of 75 or higher is preferable. For example, glass wool, zeolite,
Examples include sponges, valve scraps, crushed ironstone soaked in water, etc. Silos are usually used for grain storage. The oxygen scavenger chamber and the water-containing substance chamber are chambers that contain an oxygen scavenger and a water-containing substance, respectively. Preferably, the chambers are arranged such that the circulating gas passes through the hydrous chamber and into the deoxygenation chamber. In particular, the water-containing substance chamber is integrated with the deoxidizing chamber and is contained within the deoxidizing chamber, and the lower part of the deoxidizing chamber is a part for accommodating the hydrated substance, and the upper part is the part for accommodating the deoxidizing agent, which circulates from the lower part to the upper part. Those that allow gas to pass through are preferably used. The present invention requires a grain storage, a moisture-containing substance chamber, a deoxidizing chamber, and a blower.
Other mechanisms can be provided as necessary. Examples include dust removal room, clean room, inside air outlet, mixed gas supply valve, manometer monitoring board, etc. Next, an example of the apparatus of the present invention will be explained with reference to the drawings. In FIG. 1, 1 is a silo, 2 is a blower, 3 is a deoxidizing chamber, 4 is a water-containing substance storage area, 5 is an oxygen scavenger storage area, and 6 is a nitrogen gas cylinder. The gas in the system is circulated by the blower 2, and oxygen in the system is removed by passing the gas through the water-containing material section 4 and through the oxygen scavenger storage section 5. The present invention does not absorb oxygen when loading the oxygen scavenger,
Since the present invention is configured so that oxygen is absorbed only after tightly floating gas is circulated within the system, there is no loss of oxygen scavenger and it is easy to handle, so grains can be stored appropriately. I can do it. An example of storing grain using the apparatus of the present invention will be shown below. Example A test was conducted using the apparatus shown in FIG. Inner volume approx. 14
5 tons of brown soba as a test sample in a m2 steel silo
(approximately 10 m 3 ) and put the oxygen absorber into the oxygen absorber chamber. The air volume inside the storage system, including the inside of the silo, inside the deoxidation chamber, inside the blower, inside the piping, etc., was approximately 10 m 3 . In order to prevent deformation of equipment and inflow of outside air due to negative pressure due to volume reduction during deoxidation, a nitrogen gas cylinder was installed in the circulation piping, and nitrogen gas of 230 to 310 mmHg was constantly introduced using a pressure control valve.
A sampling port was installed in the circulation piping to measure oxygen concentration, temperature, humidity, etc. in the circulating air. After preparation is complete, the system is sealed and the blower is operated to start air circulation. This is the "start" point. Samples (brown soba) are taken from the silo over time and the moisture content (%) and peroxide value are measured. The quality of the samples was evaluated using measurement data such as index (meq/Kg) and chlorofilm (%) and sensory tests. The results are shown in Tables 1 and 2. Table 1 shows the oxygen concentration change measurement results, and Table 2 shows the brown soba storage test results. For comparison, a similar test was conducted without using a water-containing substance. The results are listed in Tables 1 and 2.
【表】【table】
【表】
本発明によるものの方が、スタート時点に比べ
水分量の低下もなく、POVの変化も少なくクロ
ロフイルの減退も少なかつた。また、官能テスト
でも優位差がはつきりついた。[Table] Compared to the starting point, the product according to the present invention had no decrease in water content, less change in POV, and less loss of chlorophyll. In addition, the superiority was clearly evident in the sensory test.
第1図は本発明の装置の一例を示したものであ
り、図中1はサイロ、2は送風機、3は脱酸素
室、4は含水物質収容部分、5は脱酸素剤収容部
分、6は窒素ガスボンベである。
FIG. 1 shows an example of the apparatus of the present invention, in which 1 is a silo, 2 is a blower, 3 is a deoxidizing chamber, 4 is a water-containing substance storage area, 5 is an oxygen scavenger storage area, and 6 is a deoxidizer storage area. It is a nitrogen gas cylinder.
Claims (1)
室及び送風機が循環路を形成してなり、脱酸素室
が水分の非存在下では実質的に酸素を吸収しない
か、又は酸素吸収速度のおそい脱酸素剤を収容し
たものであり、系内のガスを循環することによつ
て穀類貯蔵庫内の酸素を除去しうるようにした穀
類の貯蔵装置。 2 循環ガスが含水物質室を通り脱酸素室に入る
ように両室が配列されてなる特許請求の範囲第1
項記載の貯蔵装置。 3 含水物質室が脱酸素室と一体化され脱酸素室
に包含されてなり、該脱酸素室の下部が含水物質
室収容部分、上部が脱酸素剤収容部分であつて下
部から上部へ向つて循環ガスが通るようにした特
許請求の範囲第2項記載の貯蔵装置。 4 含水物質室が平衡温度75%以上の含水物質を
収容したものである特許請求の範囲第1,2又は
3項記載の貯蔵装置。[Scope of Claims] 1 A sealable grain storage, a moisture-containing substance chamber, a deoxidizing chamber, and a blower form a circulation path, and the deoxidizing chamber does not substantially absorb oxygen in the absence of moisture, or Or a grain storage device that contains an oxygen scavenger with a slow oxygen absorption rate and is capable of removing oxygen in the grain storage by circulating gas within the system. 2. Claim 1, wherein both chambers are arranged so that the circulating gas passes through the water-containing substance chamber and enters the deoxidizing chamber.
Storage device as described in Section. 3. The water-containing substance chamber is integrated with and included in the oxygen-absorbing chamber, and the lower part of the oxygen-absorbing chamber is the water-containing substance chamber housing part, and the upper part is the oxygen scavenger housing part, from the lower part to the upper part. 3. A storage device according to claim 2, wherein the storage device is adapted to allow circulating gas to pass therethrough. 4. The storage device according to claim 1, 2 or 3, wherein the water-containing substance chamber contains a water-containing substance having an equilibrium temperature of 75% or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14550778A JPS5571444A (en) | 1978-11-25 | 1978-11-25 | Equipment for storing grain |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14550778A JPS5571444A (en) | 1978-11-25 | 1978-11-25 | Equipment for storing grain |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5571444A JPS5571444A (en) | 1980-05-29 |
| JPS6117462B2 true JPS6117462B2 (en) | 1986-05-07 |
Family
ID=15386841
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14550778A Granted JPS5571444A (en) | 1978-11-25 | 1978-11-25 | Equipment for storing grain |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5571444A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0325850U (en) * | 1989-07-25 | 1991-03-18 |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0571986U (en) * | 1991-03-29 | 1993-09-28 | 一彌 中山 | Writer |
-
1978
- 1978-11-25 JP JP14550778A patent/JPS5571444A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0325850U (en) * | 1989-07-25 | 1991-03-18 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5571444A (en) | 1980-05-29 |
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