JPH0114091B2 - - Google Patents

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Publication number
JPH0114091B2
JPH0114091B2 JP58200186A JP20018683A JPH0114091B2 JP H0114091 B2 JPH0114091 B2 JP H0114091B2 JP 58200186 A JP58200186 A JP 58200186A JP 20018683 A JP20018683 A JP 20018683A JP H0114091 B2 JPH0114091 B2 JP H0114091B2
Authority
JP
Japan
Prior art keywords
gas
transfer pipe
packaging
pipe
measuring 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
Application number
JP58200186A
Other languages
Japanese (ja)
Other versions
JPS6099818A (en
Inventor
Shunichi Kudo
Takemine Chiba
Tetsuhiko Maruyama
Teruyoshi Komatsu
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Komatsu Ltd
MEIJI NYUGYO KK
Original Assignee
Komatsu Ltd
MEIJI NYUGYO KK
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Komatsu Ltd, MEIJI NYUGYO KK filed Critical Komatsu Ltd
Priority to JP20018683A priority Critical patent/JPS6099818A/en
Publication of JPS6099818A publication Critical patent/JPS6099818A/en
Publication of JPH0114091B2 publication Critical patent/JPH0114091B2/ja
Granted legal-status Critical Current

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  • Containers And Plastic Fillers For Packaging (AREA)
  • Vacuum Packaging (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

この発明は粉粒体をガス置換して包装するに際
し、残留酸素量を可及的に少なくすると共に、粉
粒体の飛散を防止することを目的としたガス置換
包装方法および装置に関するものである。 従来粉粒体のガス置換包装においては、包装容
器内の空気を抽出した後不活性ガスを充填する方
法が一般的に行われているが、斯かる方法におい
ては粉粒体ブロツクの内部に包含している空気を
除去することがむつかしく、前記ガス置換方法に
おける残存酸素率は通常3%以上とされていた。
また従来、豆菓子などの窒素封入包装方法におい
て、開放シユートの一方から豆菓子と窒素ガスと
を供給し、開放シユートの他方で製袋して包装す
る際に、窒素ガスをオーバーフローさせるように
した方法が知られていた(特公昭60―35094号)。 然し乍ら、前記豆菓子など比較的粒度の大きい
物では、空気と窒素ガスとの置換が容易であると
しても、粉乳のような粒度の小さい粉粒体にあつ
ては、前記開放型シユートによるガス置換は困難
であつた。そこでこの発明の発明者は、粉粒体を
予め脱酸素処理することについて研究したけれど
も、脱酸素後の取扱いが適切でなければ残存酸素
量をきわめて少なくすること(例えば1%以下に
する)ができなかつた。 然るにこの発明は脱酸素後の粉粒体の計量、移
送および包装の為の供給に際し、悉く不活性ガス
の雰囲気中で行うと共に、不活性ガスの吹き込み
について過度の流速を与えないように配慮すると
ともに、常時ガス圧を陽圧に保持させることによ
つて前記問題点を解決したのである。特に不活性
ガスに一定値以上の流速を付与しない為に、ノズ
ルを複数にすると共に、移送路に工夫を加え、か
つ必要ガス量よりも多いガス量を与えて急速な吸
入動作時にも陽圧を保ち、少なくとも外気の流入
を防止し得る状態に保持して所期の目的を達成し
たものである。尚、この発明は特にステイツクパ
ツクの包装に好適である。 即ちこの発明は、ホツパー2内に予め脱酸素処
理した粉粒体1をホツパー2の下部から計量器3
の計量盤4の計量孔5内へ流下させる。このよう
にして計量盤4が軸6を中心にして回転し、前記
計量孔5が上部の移送管7の直上に停止したなら
ば、ノズル8から窒素ガスを矢示14のように吹
きつけて、計量孔5内の粉粒体1を矢示15のよ
うに移送管7内へ落下させる。この粉粒体1は移
送管7の下端に連結した下部の移送管7a内を下
降し、更に移送管7aの下端に連結した供給管9
を経て筒状袋16内へ供給される。前記において
移送管7,7aの上部側壁には夫々ノズル8a,
8bが挿入開口され、矢示17,18のように窒
素ガスを吹き込むので、前記移送管7,7aおよ
び供給管9(これらの管により移送路を形成す
る)内は窒素ガスが充満し、かつ陽圧に保持され
ている。従つて余剰ガスは移送管7aの上部へ植
設した排気管19から外界へ放出される。前記排
気管19は、例えば直径10mm、長さ1000mmであつ
て(袋の容積は例えば0.06である)、包装袋が
下降する時に、移送路内の空間が瞬間的に減圧さ
れるので、前記排気管19内のガスは吸入状態に
なり、不活性ガスは移送路内へ逆流し、外気は排
気管19の中間部まで下降して、急速に移送路内
の減圧は復元される。従つて排気管19により、
移送路内の減圧度の増大、又は外気の侵入が阻止
される。ついで定量の粉粒体が筒状袋16内へ入
ると、当該筒状袋16は袋用フイルム20と共に
1袋分下降し、その上部が熱板22とローラー1
0によつて筒状に形成され、筒状袋の上端は予備
シール部11によつてシールされると共に、筒状
袋16の下端は熱板12によつて本シールされ
る。又既に密封された前記筒状袋16の下部に連
なる袋16aはカツター13によつて熱シール部
分から切断される。 次にこの発明の包装方法を実施する装置の一例
を添付図面について説明する。 断面が漏斗状の粉粒体ホツパー2の下部に計量
器3の一側が連設され、計量器3内には計量盤4
が回転自在に架設され、計量器3の一側下部には
下方を小径にした筒状の移送管7の上端が連設し
てあり、該移送管7の下端部には筒状の下部移送
管7aの上端が偏心して遊嵌してあり、前記計量
器3にガス吹込み用ノズル8を設け、前記計量器
3に連設した移送管7とこれにつらなる移送管7
aには、各々ガス吹き込み用のノズル8a,8b
が臨ませてある。前記移送管7aの上部には、排
気管19を添えた蓋25が被冠してある。前記排
気管19は、袋詰時に生じる急激な減圧時に不活
性ガスを自動吸入して、空気の流入を防止する為
の内圧調整用であつて、自動吸入時に必要な容量
をもたせてある。一方フイルム供給部21から移
送された包装フイルム20が順次筒状に形成され
るように、包装フイルム20の両端を熱板22お
よびローラー10で挾持して溶着すると共に、供
給管9に嵌装してあり、供給管9の下方には筒状
に形成された包装袋16を所定間隔毎に押圧して
加熱溶着する予備シール部11、熱板12が設け
てあり、更に下方には熱溶着部で切断するための
カツター13が設けてある。図中24はフイルム
案内ロールである。 この実施例では、ホツパー2に連設した計量器
3にガス吹き込みノズル8を臨ませたが、ノズル
の設置場所には限定されない。また計量器自体に
はノズルを臨ませない装置であつてもよい。又移
送管7,7aには、各々1本のガス吹き込みノズ
ル8a,8bを臨ませたが、その数および吹き込
み量に限定を受けるものではない。 前記において不活性ガスは窒素ガスを用いた
が、炭酸ガス又は窒素ガスと炭酸ガスの併用でも
よいことは勿論である。前記実施例においてはホ
ツパー2を用いたけれども、ホツパーに代えて容
器又は袋を用いることができる。 次に前記の実施における残存酸素率を計測した
所、表1の結果を得た。 条件:(1) 充填量15g/包 (2) 充填能力30包/分 (3) 窒素ガス吹き出しノズル数3本 (4) 粉粒体は、脱脂粉乳
The present invention relates to a gas exchange packaging method and apparatus for reducing the amount of residual oxygen as much as possible and preventing scattering of powder and granules when packaging them by replacing gas with gas. . Conventionally, in gas exchange packaging for powder and granular materials, a method is generally used in which the air inside the packaging container is extracted and then filled with inert gas. It is difficult to remove the air that is present, and the residual oxygen rate in the gas replacement method is usually 3% or more.
Furthermore, conventionally, in the nitrogen filled packaging method for bean confectionery, etc., the bean confectionery and nitrogen gas were supplied from one side of the open chute, and the nitrogen gas was allowed to overflow when bags were made and packaged from the other side of the open chute. The method was known (Special Publication No. 35094, Showa 60). However, even if it is easy to replace air and nitrogen gas with relatively large particles such as the bean confectionery mentioned above, in the case of small powders such as powdered milk, it is difficult to replace the gas with the open chute. was difficult. Therefore, the inventor of this invention conducted research on deoxidizing powder and granules in advance, but if the handling after deoxidization is not appropriate, the amount of residual oxygen may be extremely low (for example, below 1%). I couldn't do it. However, in this invention, when measuring, transporting, and supplying the deoxidized powder or granular material for packaging, all of the steps are carried out in an inert gas atmosphere, and care is taken not to give an excessive flow rate to the blowing of the inert gas. At the same time, the above-mentioned problem was solved by constantly maintaining the gas pressure at a positive pressure. In particular, in order not to apply a flow rate higher than a certain value to the inert gas, we have used multiple nozzles and have devised the transfer path, and also provided a larger amount of gas than the required amount to provide positive pressure even during rapid suction operations. The desired purpose was achieved by maintaining the structure in a state where it could at least prevent the inflow of outside air. The present invention is particularly suitable for packaging staple packs. That is, in this invention, the granular material 1 which has been deoxidized in advance in the hopper 2 is transferred from the lower part of the hopper 2 to the measuring device 3.
into the measuring hole 5 of the measuring board 4. In this way, when the measuring plate 4 rotates around the shaft 6 and the measuring hole 5 stops directly above the upper transfer pipe 7, nitrogen gas is sprayed from the nozzle 8 as shown by the arrow 14. , the powder 1 in the measuring hole 5 is dropped into the transfer pipe 7 as shown by the arrow 15. This granular material 1 descends in a lower transfer pipe 7a connected to the lower end of the transfer pipe 7, and further flows through a supply pipe 9 connected to the lower end of the transfer pipe 7a.
It is supplied into the cylindrical bag 16 through the. In the above, the upper side walls of the transfer pipes 7 and 7a are provided with nozzles 8a and 8a, respectively.
8b is inserted and opened and nitrogen gas is blown in as shown by arrows 17 and 18, so that the transfer pipes 7 and 7a and the supply pipe 9 (these pipes form a transfer path) are filled with nitrogen gas, and Maintained under positive pressure. Therefore, the excess gas is discharged to the outside world from the exhaust pipe 19 installed above the transfer pipe 7a. The exhaust pipe 19 has a diameter of, for example, 10 mm and a length of 1000 mm (the volume of the bag is, for example, 0.06 mm), and when the packaging bag descends, the space within the transfer path is momentarily depressurized, so that the exhaust pipe 19 is 10 mm in diameter and 1000 mm in length. The gas in the pipe 19 enters the suction state, the inert gas flows back into the transfer path, the outside air descends to the middle of the exhaust pipe 19, and the reduced pressure in the transfer path is quickly restored. Therefore, by the exhaust pipe 19,
An increase in the degree of vacuum in the transfer path or an infiltration of outside air is prevented. Next, when a certain amount of powder or granules enters the cylindrical bag 16, the cylindrical bag 16 is lowered by one bag along with the bag film 20, and the upper part of the cylindrical bag 16 is touched by the hot plate 22 and the roller 1.
The upper end of the cylindrical bag 16 is sealed by a preliminary sealing part 11, and the lower end of the cylindrical bag 16 is permanently sealed by a hot plate 12. Further, the bag 16a which is connected to the lower part of the already sealed cylindrical bag 16 is cut off from the heat-sealed portion by the cutter 13. Next, an example of an apparatus for carrying out the packaging method of the present invention will be described with reference to the accompanying drawings. One side of a measuring device 3 is connected to the lower part of the powder hopper 2 having a funnel-shaped cross section, and a measuring board 4 is installed inside the measuring device 3.
A cylindrical transfer pipe 7 with a smaller diameter at the bottom is connected to the lower end of one side of the measuring instrument 3, and a cylindrical lower transfer pipe 7 is connected to the lower end of the transfer pipe 7. The upper end of the pipe 7a is eccentrically fitted and loosely fitted, and the measuring device 3 is provided with a gas blowing nozzle 8, and the measuring device 3 is provided with a transfer pipe 7 connected to the measuring device 3, and the transfer pipe 7 connected thereto.
a has nozzles 8a and 8b for blowing gas, respectively.
is coming. A lid 25 with an exhaust pipe 19 is placed on top of the transfer pipe 7a. The exhaust pipe 19 is used to adjust the internal pressure to prevent air from flowing in by automatically inhaling inert gas when the pressure is rapidly reduced during bagging, and is provided with a capacity necessary for automatic inhalation. On the other hand, both ends of the packaging film 20 transferred from the film supply section 21 are sandwiched and welded by the hot plate 22 and the roller 10 so that the packaging film 20 is sequentially formed into a cylindrical shape, and the packaging film 20 is fitted into the supply pipe 9. Below the supply pipe 9, there are provided a preliminary sealing part 11 and a hot plate 12 for pressing and heat-welding the cylindrical packaging bag 16 at predetermined intervals, and further below a heat-welding part. A cutter 13 for cutting is provided. In the figure, 24 is a film guide roll. In this embodiment, the gas blowing nozzle 8 faces the meter 3 connected to the hopper 2, but the location of the nozzle is not limited. Further, the measuring device itself may be a device in which no nozzle is exposed. Further, although one gas blowing nozzle 8a, 8b is provided to each of the transfer pipes 7, 7a, the number and blowing amount thereof are not limited. Although nitrogen gas was used as the inert gas in the above, it goes without saying that carbon dioxide gas or a combination of nitrogen gas and carbon dioxide gas may also be used. Although the hopper 2 was used in the above embodiment, a container or a bag may be used instead of the hopper. Next, the residual oxygen rate in the above implementation was measured, and the results shown in Table 1 were obtained. Conditions: (1) Filling amount: 15g/bag (2) Filling capacity: 30 bags/minute (3) Number of nitrogen gas blowing nozzles: 3 (4) Powder is skim milk powder

【表】 (注) 充填後9日目の測定値、表中吹
出量は三本のノズルの合計量である。
また筒状袋(ステイツクパツク)包装における
充填用原料粉乳の脱酸素剤使用による前処理効果
を試験した所、表2の結果を得た。 条件:(1) 充填試料8.8g/包 (2) 窒素ガス吹き出しノズル数3本 (3) 脱酸素剤は商品名「エージレス」(三
菱瓦斯化学(株)を使用)
[Table] (Note) Measured values on the 9th day after filling. The amount of air flow in the table is the total amount from the three nozzles.
In addition, we tested the effect of pretreatment of raw milk powder for filling in cylindrical bag packaging by using an oxygen scavenger, and the results shown in Table 2 were obtained. Conditions: (1) Filled sample 8.8g/bag (2) Number of nitrogen gas blowing nozzles: 3 (3) Oxygen scavenger is brand name "Ageless" (used by Mitsubishi Gas Chemical Co., Ltd.)

【表】 (注) 充填後9日目の測定値
即ちこの発明によれば、予め脱酸素処理した粉
粒体を不活性ガス雰囲気中で計量器、移送管およ
び供給管を経て包装袋内へ送入すると共に、前記
移送路のガスは常に陽圧に保たれたので、脱酸素
処理後粉粒体が外気にふれるおそれなく、包装袋
内の残存酸素量をきわめて少なく保ち得る効果が
ある。 またこの発明の装置によれば、不活性ガスを複
数のノズルによつて吹き込んだので、移送管およ
び供給管内は常に陽圧にも拘らず、ガスの急激な
流れがなく粉粒体の逆流するおそれがないなどの
効果がある。 また、急激な減圧を不活性ガスの自動吸入で緩
和し、供給管内への空気の流入を防止する為に必
要とする容量の排気管を、供給管の上部に立設し
たので、袋詰に生じる瞬間的減圧に際しては、排
気管内の不活性ガスが供給管内へ吸入される。こ
の際排気管の容量が適切にしてあるので、空気を
吸入するおそれはないなどの効果もある。 次にこの発明の方法の実施例について説明す
る。粉乳25Kgに通気性袋に包装した脱酸素剤(エ
ージレス)160gを添えてホツパー内で24時間放
置した所(必要に応じて撹拌する)、残存酸素率
1%以下となつた。そこでこの粉乳を8.8g宛計量
すると共に、移送管および供給管を経て包装袋内
へ装入するに当り、ノズル8,8a,3bの三箇
所から窒素ガスを夫々30/min、送り込む。こ
の場合に包装袋の容量は0.06であつた。この包
装袋をシールしてこの発明の方法を完了した。こ
のようにして得た包装袋を9日間放置後、袋10個
について残存酸素率を測定した所、平均0.6%で
あつた。
[Table] (Note) Measured values on the 9th day after filling In other words, according to the present invention, powder and granules that have been deoxidized in advance are transferred into a packaging bag through a measuring device, a transfer pipe, and a supply pipe in an inert gas atmosphere. Since the gas in the transfer path was always maintained at a positive pressure during the delivery, there was no fear that the powder or granules would come into contact with the outside air after deoxidation treatment, and the amount of residual oxygen in the packaging bag could be kept extremely low. Furthermore, according to the device of the present invention, inert gas is blown through multiple nozzles, so there is no rapid flow of gas and no backflow of powder or granules, even though there is always positive pressure inside the transfer pipe and supply pipe. There is an effect that there is no fear. In addition, an exhaust pipe with the necessary capacity is installed above the supply pipe to alleviate sudden pressure reduction with automatic inhalation of inert gas and prevent air from entering the supply pipe, making it easy to pack. During the instantaneous pressure reduction that occurs, the inert gas in the exhaust pipe is sucked into the supply pipe. At this time, the exhaust pipe has an appropriate capacity, so there is no risk of inhaling air. Next, an example of the method of this invention will be described. When 25 kg of milk powder was added with 160 g of oxygen absorber (Ageless) packaged in a breathable bag and left in a hopper for 24 hours (stirring as necessary), the residual oxygen rate was less than 1%. Therefore, this powdered milk is weighed to 8.8 g, and nitrogen gas is fed at 30/min from three nozzles 8, 8a, and 3b, respectively, when it is charged into a packaging bag via a transfer pipe and a supply pipe. In this case, the capacity of the packaging bag was 0.06. The packaging bag was sealed to complete the method of the invention. After the packaging bags thus obtained were left for 9 days, the residual oxygen percentage was measured for 10 bags, and the average was 0.6%.

【図面の簡単な説明】[Brief explanation of drawings]

第1図はこの発明の実施に用いる装置の一部を
切断した正面図、第2図は同じく製袋部の拡大斜
視図、第3図は同じく計量器の断面拡大図、第4
図は同じく計量盤の平面拡大図、第5図は同じく
供給管と筒状袋との関係を示す一部断面拡大図で
ある。 1…粉粒体、2…ホツパー、3…計量器、4…
計量盤、7,7a…移送管、8,8a,8b…ノ
ズル、9…供給管、16…筒状袋、19…排気
管。
FIG. 1 is a partially cutaway front view of the apparatus used to carry out the present invention, FIG. 2 is an enlarged perspective view of the bag making section, FIG. 3 is an enlarged sectional view of the measuring instrument, and FIG.
The figure is an enlarged plan view of the measuring board, and FIG. 5 is an enlarged partial cross-sectional view showing the relationship between the supply pipe and the cylindrical bag. 1... Powder, 2... Hopper, 3... Measuring device, 4...
Measuring board, 7, 7a... Transfer pipe, 8, 8a, 8b... Nozzle, 9... Supply pipe, 16... Cylindrical bag, 19... Exhaust pipe.

Claims (1)

【特許請求の範囲】 1 予め脱酸素処理した粉粒体を定量宛計量し、
これを包装袋内へ移送する際、計量器よりの排出
移送路およびこれに連設した移送路から夫々不活
性ガスを吹き込んで移送路内を陽圧の不活性ガス
雰囲気とすると共に、当該不活性ガス量は袋詰時
に生じる瞬間的減圧を不活性ガスの自動吸入で緩
和し移送路内に空気を吸入しないようにすること
を特徴としたガス置換包装方法。 2 陽圧は、計量器、移送路および包装袋と移送
路との間〓より外気を吸入しない程度に外気との
圧力差を設けた特許請求の範囲第1項記載のガス
置換包装方法。 3 予め脱酸素処理した粉粒体を収容するホツパ
ーの下部に計量器を連設し、該計量器の排出側に
粉粒体移送用の移送管の一端を連設し、前記移送
管の他端に供給管の一端を連設し、供給管の他端
を包装袋内へ挿入すると共に、前記計量器および
移送管の一部に不活性ガスノズルを開口し、前記
供給管の上部に瞬間的減圧による急激な吸入に見
合う容量の排気管を直立設置したことを特徴とす
るガス置換包装装置。 4 計量器は計量孔を有する回転円盤の一側上部
にホツパーの供給口との連結部を設け、他側下部
に移送管との連結部を設けた特許請求の範囲第3
項記載のガス置換包装装置。 5 計量器に設けたガスノズルは計量器の排出側
上部に設けた特許請求の範囲第3項記載のガス置
換包装装置。 6 移送管は上部移送管と下部移送管とにより構
成し、上部移送管の下端を下部移送管の上端部内
側へ偏心して挿入連結した特許請求の範囲第3項
記載のガス置換包装装置。 7 移送管に開口するガスノズルは上部移送管お
よび下部移送管の夫々の上側壁より突入させ、開
口端を斜下方に向けた特許請求の範囲第3項又は
第6項記載のガス置換包装装置。 8 供給管は包装袋の内側へ挿入され、包装袋の
内壁が摺接下降できる程度の外径とした特許請求
の範囲第3項記載のガス置換包装装置。
[Claims] 1. Weighing the granular material that has been deoxidized in advance to a fixed amount,
When transferring this into the packaging bag, inert gas is blown into the discharge transfer path from the measuring device and the transfer path connected thereto to create a positive pressure inert gas atmosphere in the transfer path, and A gas replacement packaging method characterized by reducing the amount of active gas by automatically inhaling inert gas to reduce the instantaneous pressure reduction that occurs during bagging, thereby preventing air from being inhaled into the transfer path. 2. The gas replacement packaging method according to claim 1, wherein the positive pressure is such that a pressure difference between the measuring device, the transfer path, the packaging bag, and the transfer path is such that outside air is not sucked in from the outside air. 3. A measuring device is connected to the lower part of the hopper that stores the powder and granular material that has been subjected to deoxidation treatment in advance, and one end of a transfer pipe for transferring the powder and granular material is connected to the discharge side of the measuring device, and other than the transfer pipe One end of the supply pipe is connected to the end, and the other end of the supply pipe is inserted into the packaging bag. At the same time, an inert gas nozzle is opened in the measuring device and a part of the transfer pipe, and a momentary gas is applied to the upper part of the supply pipe. A gas displacement packaging device characterized by having an upright exhaust pipe with a capacity suitable for rapid suction due to reduced pressure. 4. Claim 3, wherein the measuring device is a rotary disk having a measuring hole, and has a connecting portion to the supply port of the hopper at the upper part of one side, and a connecting portion to the transfer pipe at the lower part of the other side.
Gas displacement packaging equipment as described in Section 1. 5. The gas displacement packaging device according to claim 3, wherein the gas nozzle provided in the measuring device is provided at the upper part of the discharge side of the measuring device. 6. The gas exchange packaging device according to claim 3, wherein the transfer pipe is constituted by an upper transfer pipe and a lower transfer pipe, and the lower end of the upper transfer pipe is eccentrically inserted and connected inside the upper end of the lower transfer pipe. 7. The gas exchange packaging device according to claim 3 or 6, wherein the gas nozzle opening into the transfer pipe is projected from the upper side wall of each of the upper transfer pipe and the lower transfer pipe, and the opening end is directed obliquely downward. 8. The gas exchange packaging device according to claim 3, wherein the supply pipe is inserted into the inside of the packaging bag and has an outer diameter such that the inner wall of the packaging bag can slide down.
JP20018683A 1983-10-26 1983-10-26 Gas replacing packaging method and device Granted JPS6099818A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20018683A JPS6099818A (en) 1983-10-26 1983-10-26 Gas replacing packaging method and device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20018683A JPS6099818A (en) 1983-10-26 1983-10-26 Gas replacing packaging method and device

Publications (2)

Publication Number Publication Date
JPS6099818A JPS6099818A (en) 1985-06-03
JPH0114091B2 true JPH0114091B2 (en) 1989-03-09

Family

ID=16420222

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20018683A Granted JPS6099818A (en) 1983-10-26 1983-10-26 Gas replacing packaging method and device

Country Status (1)

Country Link
JP (1) JPS6099818A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005193985A (en) * 2004-01-06 2005-07-21 Tna Australia Pty Ltd Packer and former

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6099819A (en) * 1983-10-26 1985-06-03 明治乳業株式会社 Gas replacing packaging method
JP5503445B2 (en) * 2010-07-29 2014-05-28 パウダーテック株式会社 Organic oxygen scavenger manufacturing apparatus and organic oxygen scavenger manufacturing method

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5433186A (en) * 1977-08-17 1979-03-10 Daido Oxygen Method and device for packing by sealing together with inert gas

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5433186A (en) * 1977-08-17 1979-03-10 Daido Oxygen Method and device for packing by sealing together with inert gas

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005193985A (en) * 2004-01-06 2005-07-21 Tna Australia Pty Ltd Packer and former
JP4628780B2 (en) * 2004-01-06 2011-02-09 ティー・エヌ・エー オーストラリア ピィー・ティー・ワイ リミテッド Packaging machine and former

Also Published As

Publication number Publication date
JPS6099818A (en) 1985-06-03

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