JP7694192B2 - Packaging method - Google Patents
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Description
本発明は、包装方法に関する。 The present invention relates to a packaging method.
従来、内容物の酸化による変質、好気性菌の繁殖による品質低下などを防止して、長期保存を可能にするために、包装容器内の空気を窒素などの不活性ガスに置き換えながら内容物を充填密封する、いわゆる、ガス置換包装が知られている。ガス置換包装について、JIS Z 0108:2012には、「内容物の充填時に容器から空気を吸引排気し、代わりに窒素及び二酸化炭素のような不活性ガスで置換して密封し、又は不活性ガスで強制的に容器内空気を置換して密封し、物品の変質などを防止することを目的とする包装。容器には、ガスバリア性の優れた包装材料を用いる。」と記載されている(番号:1079)。 So far, so-called gas replacement packaging has been known, in which the air in a packaging container is replaced with an inert gas such as nitrogen while the contents are filled and sealed in order to prevent deterioration of the contents due to oxidation and deterioration of quality due to the proliferation of aerobic bacteria, and to enable long-term storage. Regarding gas replacement packaging, JIS Z 0108:2012 states, "When filling the contents, air is sucked out from the container and replaced with an inert gas such as nitrogen or carbon dioxide before sealing, or the air in the container is forcibly replaced with an inert gas and sealed, with the aim of preventing deterioration of the product. The container is made of a packaging material with excellent gas barrier properties" (No.: 1079).
また、このようなガス置換包装において、容器内酸素を完全に除去するのは困難であることから、例えば、特許文献1には、酸素バリア層とともに、酸素吸収機能を有する樹脂層を設けた積層体からなる包装容器に、内容物をガス置換包装することが提案されている。 In addition, since it is difficult to completely remove oxygen from within the container in this type of gas replacement packaging, for example, Patent Document 1 proposes that the contents be gas replacement packaged in a packaging container made of a laminate that has an oxygen barrier layer and a resin layer that has an oxygen absorbing function.
しかしながら、本発明者らの検討によれば、酸素吸収機能が付与された包装容器に内容物をガス置換包装した場合であっても、ガス置換包装後に容器内の酸素濃度が上昇する現象が観察され、この点に着目して鋭意検討を重ねたところ、内容物に含まれていた酸素が影響していることを見出した。そこで、本発明者らは、従来は全く考慮されていなかった内容物に含まれる酸素を可及的に除去することにより、ガス置換包装後に容器内に残存する酸素を低減させるべく、さらなる鋭意検討を重ねた結果、本発明を完成するに至った。 However, according to the inventors' research, even when the contents are gas-exchanged packaged in a packaging container with oxygen absorbing function, the oxygen concentration in the container increases after gas-exchange packaging. After extensive research focusing on this point, the inventors found that the oxygen contained in the contents had an effect. Therefore, the inventors conducted further extensive research to reduce the amount of oxygen remaining in the container after gas-exchange packaging by removing as much oxygen as possible from the contents, which had not been taken into consideration at all in the past, and as a result, they completed the present invention.
本発明に係る包装方法は、内容物を包装容器にガス置換包装するにあたり、前記内容物を減圧チャンバー内に収容して密封し、前記減圧チャンバー内を排気して、前記減圧チャンバー内を一次減圧度まで減圧した後、排気を継続させながら、前記減圧チャンバー内に不活性ガスを流入させ、しかる後に、排気を継続させながら、前記減圧チャンバー内への不活性ガスの流入を停止し、前記減圧チャンバー内を更に二次減圧度まで減圧し、次いで、前記減圧チャンバー内の排気を停止し、前記減圧チャンバー内に再び不活性ガスを流入させ、前記減圧チャンバー内の圧力を大気圧と同等とした後、前記減圧チャンバーから前記内容物を取り出して、ガス置換包装する方法である。 The packaging method of the present invention is a method for gas-flux packaging of contents in a packaging container, comprising the steps of: placing the contents in a vacuum chamber and sealing it; evacuating the vacuum chamber to reduce the pressure inside the vacuum chamber to a first reduced pressure; then, while continuing the exhaust, flowing an inert gas into the vacuum chamber; thereafter, while continuing the exhaust, stopping the flow of inert gas into the vacuum chamber and further reducing the pressure inside the vacuum chamber to a second reduced pressure; then, stopping the exhaust of the vacuum chamber and flowing inert gas into the vacuum chamber again to make the pressure inside the vacuum chamber equivalent to atmospheric pressure; and then removing the contents from the vacuum chamber and performing gas-flux packaging.
本発明によれば、内容物を包装容器にガス置換包装するに先立って、内容物に含まれる酸素を効率よく除去しておくことにより、ガス置換包装後に容器内に残存する酸素をより低減させることができる。 According to the present invention, by efficiently removing oxygen from the contents prior to gas-exchange packaging the contents in a packaging container, it is possible to further reduce the amount of oxygen remaining in the container after gas-exchange packaging.
以下、本発明に係る包装方法について、その実施形態を示しつつ説明する。 The packaging method according to the present invention will be described below with reference to an embodiment.
本発明の実施形態として示す包装方法は、内容物を包装容器にガス置換包装するに先立って、内容物に含まれる酸素を効率よく除去しておくことにより、ガス置換包装後の容器内に残存する酸素をより低減させて、内容物をより長期にわたって保存可能とするための包装方法である。 The packaging method shown as an embodiment of the present invention is a packaging method that efficiently removes oxygen from the contents before gas-exchange packaging the contents in a packaging container, thereby further reducing the amount of oxygen remaining in the container after gas-exchange packaging, allowing the contents to be stored for a longer period of time.
本実施形態において包装対象となる内容物は、例えば、饅頭、ロールパン、蒸しパン、最中、せんべい等の食品類を代表的な内容物として例示できるが、これらに限定されない。容器内に残存する酸素が保存に悪影響を及ぼし得る非食品類をも包装対象とすることができる。 In this embodiment, typical examples of the contents to be packaged include food items such as buns, rolls, steamed bread, monaka, and rice crackers, but are not limited to these. Non-food items whose preservation may be adversely affected by oxygen remaining in the container can also be packaged.
本実施形態にあっては、まず、真空ポンプに接続された減圧チャンバーに大気圧下で包装対象の内容物を収容する。包装対象の内容物を減圧チャンバーに収容する際は、当該内容物の大きさや、減圧チャンバーの容積などに応じて、当該内容物を複数まとめて収容してもよく、一つずつ個別に収容してもよい。 In this embodiment, the contents to be packaged are first placed under atmospheric pressure in a reduced pressure chamber connected to a vacuum pump. When placing the contents to be packaged in the reduced pressure chamber, the contents may be placed together or individually depending on the size of the contents and the volume of the reduced pressure chamber.
次いで、減圧チャンバーを閉じ、内容物を減圧チャンバー内に密封し、真空ポンプを作動させて減圧チャンバー内を排気する。そして、減圧チャンバー内が、一次減圧度になるまで減圧された時点で、排気を継続させながら、減圧チャンバー内に不活性ガスを流入させる。 Then, the vacuum chamber is closed, the contents are sealed inside the vacuum chamber, and the vacuum pump is operated to evacuate the inside of the vacuum chamber. Then, when the pressure inside the vacuum chamber has been reduced to the first degree of vacuum, an inert gas is introduced into the vacuum chamber while continuing to evacuate.
なお、不活性ガスは、内容物に対して化学的に不活性なものであれば特に限定されないが、例えば、窒素、二酸化炭素、アルゴン及びヘリウムからなる群から選択される少なくとも一種の不活性ガスを用いることができる。 The inert gas is not particularly limited as long as it is chemically inert to the contents, but for example, at least one inert gas selected from the group consisting of nitrogen, carbon dioxide, argon, and helium can be used.
このようにして、減圧チャンバー内に不活性ガスを流入させることにより、内容物の周囲が不活性ガスにガス置換され、内容物の内部と内容物の外周部で、酸素ガスの分圧に差が生じる。その結果、内容物の内部に含まれている酸素が、相対的に酸素ガス分圧の低い内容物の外周部雰囲気中に、効果的に拡散、放出されることになる。しかも、チャンバー内部はガスの排気が継続されているため、内容物の外周部に拡散、放出された酸素は、効果的に減圧チャンバー外に排出されるようになっている。 In this way, by flowing inert gas into the reduced pressure chamber, the atmosphere surrounding the contents is replaced with inert gas, and a difference in the partial pressure of oxygen gas occurs between the inside of the contents and the outer periphery of the contents. As a result, the oxygen contained inside the contents is effectively diffused and released into the atmosphere around the contents, where the oxygen gas partial pressure is relatively low. Moreover, because gas is continuously evacuated from inside the chamber, the oxygen diffused and released to the outer periphery of the contents is effectively discharged outside the reduced pressure chamber.
減圧チャンバーに接続された真空ポンプを作動させ、減圧チャンバー内を排気するにあたり、真空ポンプの排気速度は、一般に、減圧チャンバー内の減圧度が低い段階では排気速度が速く、減圧チャンバー内の減圧度が高くになるにつれて排気速度が徐々に遅くなっていく。このため、減圧度が低い段階で、内容物の外周部を不活性ガスでガス置換しようとすると、不活性ガスの流入量を多くする必要があり、減圧チャンバー内の減圧度が大きく変動しないようにしながら、真空ポンプの排気速度に見合った量の不活性ガスを減圧チャンバー内に流入させるには、その流量調整が煩雑になるだけでなく、不活性ガスを必要以上に流入させることにもなりコスト的にも不利である。 When a vacuum pump connected to a vacuum chamber is operated to evacuate the inside of the vacuum chamber, the exhaust speed of the vacuum pump is generally fast when the degree of vacuum inside the vacuum chamber is low, and the exhaust speed gradually slows down as the degree of vacuum inside the vacuum chamber increases. For this reason, if you try to replace the outer periphery of the contents with an inert gas when the degree of vacuum is low, it is necessary to increase the amount of inert gas flowing in. In order to flow an amount of inert gas into the vacuum chamber that matches the exhaust speed of the vacuum pump while preventing large fluctuations in the degree of vacuum inside the vacuum chamber, not only is it complicated to adjust the flow rate, but it also results in more inert gas than necessary being flowed in, which is cost-inefficient.
一方、高い減圧度でガス置換する場合は、内容物に含まれている酸素の除去効率が低下する傾向がある。これは、内容物の内部に含まれている酸素が、周囲の不活性ガス雰囲気中に拡散、放出されるよりも先に、流入不活性ガスの減圧チャンバー外への排出が優先されてしまうためと考えている。さらに、高い減圧度で内容物の外周部のガス置換を継続させると、内容物に本来備わっている水分やフレーバー成分などの内容物の風味などや品質に関わる成分の除去も促進されてしまい、内容物の品質低下を招く虞もある。 On the other hand, when gas replacement is performed at a high degree of reduced pressure, the efficiency of removing oxygen contained in the contents tends to decrease. This is thought to be because the inflowing inert gas is given priority for being discharged outside the reduced pressure chamber before the oxygen contained inside the contents diffuses and is released into the surrounding inert gas atmosphere. Furthermore, continuing gas replacement around the periphery of the contents at a high degree of reduced pressure also promotes the removal of components that affect the flavor and quality of the contents, such as moisture and flavor components that are inherent to the contents, which may lead to a deterioration in the quality of the contents.
これらのことを考慮すると、内容物の内部に残留している酸素を選択的に除去する条件として、一次減圧度は、絶対圧で、20kPa~80kPaであるのが好ましく、30kPa~70kPaであるのがより好ましい。 Taking these factors into consideration, the primary pressure reduction degree, in terms of absolute pressure, is preferably 20 kPa to 80 kPa, and more preferably 30 kPa to 70 kPa, as a condition for selectively removing oxygen remaining inside the contents.
また、減圧チャンバー内を排気する排気速度V1[L/min]は、真空ポンプの性能(標準大気圧下の排気速度、到達真空度)や減圧チャンバーの容積で変動し、減圧チャンバー内に不活性ガスを流入させる流入速度V2[L/min]も、減圧チャンバー内を排気する排気速度V1との関係で定められる。 The exhaust speed V1 [L/min] for exhausting the inside of the reduced pressure chamber varies depending on the performance of the vacuum pump (exhaust speed at standard atmospheric pressure, achieved vacuum) and the volume of the reduced pressure chamber, and the inflow speed V2 [L/min] for introducing the inert gas into the reduced pressure chamber is also determined in relation to the exhaust speed V1 for exhausting the inside of the reduced pressure chamber.
本実施形態にあっては、減圧チャンバー内を一次減圧度まで減圧した後に、排気を継続させながら、減圧チャンバー内に不活性ガスを流入させるに際し、減圧チャンバー内の減圧度(絶対圧)を真空計で計測し、その変動をモニタリングしながら、不活性ガスの流入速度(一次減圧度下の不活性ガス流入速度)V2を調整することができる。その際、V1=V2であれば、減圧チャンバー内の減圧度は一定の値で推移する。V1>V2であれば、減圧チャンバー内の減圧度は上昇し、V1<V2であれば、減圧チャンバー内の減圧度は低下する。いずれにしても、減圧チャンバー内の減圧度の変動が、一次減圧度について規定する前述の範囲内、すなわち、絶対圧で、好ましくは20kPa~80kPa、より好ましくは30kPa~70kPaの範囲内に収まるように、一次減圧度下の不活性ガス流入速度V2を調整するのが好ましい。 In this embodiment, after the pressure inside the vacuum chamber is reduced to the primary reduced pressure, the inert gas is introduced into the vacuum chamber while continuing to evacuate. The degree of reduced pressure (absolute pressure) inside the vacuum chamber is measured with a vacuum gauge, and the inlet speed of the inert gas (inlet speed of the inert gas under the primary reduced pressure) V2 can be adjusted while monitoring the fluctuation. In this case, if V1=V2, the degree of reduced pressure inside the vacuum chamber remains constant. If V1>V2, the degree of reduced pressure inside the vacuum chamber increases, and if V1<V2, the degree of reduced pressure inside the vacuum chamber decreases. In any case, it is preferable to adjust the inert gas inlet speed V2 under the primary reduced pressure so that the fluctuation of the degree of reduced pressure inside the vacuum chamber falls within the aforementioned range specified for the primary reduced pressure, that is, preferably within the range of 20 kPa to 80 kPa, more preferably 30 kPa to 70 kPa in absolute pressure.
また、減圧チャンバー内に不活性ガスを流入させるにあたり、その流入時間(一次減圧度下の不活性ガス流入時間)は、5秒~1200秒であるのが好ましく、10秒~600秒であるのがより好ましい。一次減圧度下の不活性ガス流入時間が、5秒未満の短い時間では、内容物の周囲を不活性ガスで十分にガス置換できずに、内容物に含まれている酸素の除去効率が低下する虞がある。一方、一次減圧度下の不活性ガス流入時間が、1200秒よりも長い場合には、内容物の水分やフレーバー成分などの除去が促進されてしまい、内容物の品質低下を招く虞がある。 When inert gas is introduced into the vacuum chamber, the inflow time (inert gas inflow time under the primary reduced pressure) is preferably 5 to 1200 seconds, and more preferably 10 to 600 seconds. If the inert gas inflow time under the primary reduced pressure is short, such as less than 5 seconds, the gas surrounding the contents may not be sufficiently replaced with inert gas, and the efficiency of removing oxygen contained in the contents may decrease. On the other hand, if the inert gas inflow time under the primary reduced pressure is longer than 1200 seconds, the removal of moisture and flavor components from the contents may be accelerated, resulting in a deterioration in the quality of the contents.
このようにして、減圧チャンバー内を適度に減圧するとともに、内容物の外周部を不活性ガスでガス置換することによって、内容物の風味を損ねたりすることなく、内容物に含まれる酸素を選択的に除去することが可能になるが、金属で構成された減圧チャンバーの装置内壁部にも酸素は吸着、又は、収着されているため、減圧チャンバー装置の内壁に吸着または収着した酸素の除去も行う必要もある。なぜなら、その後の工程で、減圧チャンバー内壁部に吸着、又は、収着されていた酸素が放出され、内容物に移行してしまう虞もあるからである。 In this way, by reducing the pressure inside the vacuum chamber appropriately and replacing the gas around the outer periphery of the contents with an inert gas, it is possible to selectively remove the oxygen contained in the contents without impairing the flavor of the contents. However, since oxygen is also adsorbed or sorbed on the inner walls of the vacuum chamber device, which are made of metal, it is also necessary to remove the oxygen adsorbed or sorbed on the inner walls of the vacuum chamber device. This is because there is a risk that the oxygen adsorbed or sorbed on the inner walls of the vacuum chamber device will be released in a subsequent process and transferred to the contents.
本実施形態にあっては、このような不具合を有効に回避するために、一次減圧度で減圧チャンバー内への不活性ガス流入停止後、減圧チャンバー内の減圧度を更に真空度の高い二次減圧度になるまで、減圧チャンバー内の排気を継続している。この排気により、減圧チャンバー内の減圧度をさらに高真空度にすることで、減圧チャンバー内壁部に吸着又は収着されていた酸素も、減圧装置内壁部からの放出、除去も促進されることになる。その結果、減圧チャンバーの内壁部に吸着又は収着されている酸素を減圧チャンバー外に排出でき、これによって、内容物への移行が考えられる酸素の除去が促進されることになる。 In this embodiment, in order to effectively avoid such a problem, after the inert gas flow into the vacuum chamber is stopped at the first vacuum level, the vacuum chamber is continuously evacuated until the vacuum level in the vacuum chamber reaches a second vacuum level with a higher vacuum level. This exhaust increases the vacuum level in the vacuum chamber to a higher vacuum level, and promotes the release and removal of oxygen adsorbed or sorbed on the inner wall of the vacuum chamber from the inner wall of the vacuum device. As a result, oxygen adsorbed or sorbed on the inner wall of the vacuum chamber can be discharged to the outside of the vacuum chamber, which promotes the removal of oxygen that may migrate to the contents.
このときの二次減圧度は、内容物の外観を損ねてしまったり、内容物の水分やフレーバー成分などの除去が促進されてしまったりしない範囲で、真空ポンプの性能に応じて適宜設定することができる。二次減圧度は、例えば、絶対圧で、0.1kPa~10kPaであるのが好ましく、1kPa~8kPaであるのがより好ましい。 The degree of secondary vacuum can be set appropriately according to the performance of the vacuum pump, so long as it does not impair the appearance of the contents or promote the removal of moisture and flavor components from the contents. For example, the degree of secondary vacuum is preferably 0.1 kPa to 10 kPa, and more preferably 1 kPa to 8 kPa, in absolute pressure.
減圧チャンバー内の減圧度が二次減圧度に達した後、減圧チャンバー内の排気を停止し、減圧チャンバー内に不活性ガスを再び流入させることにより、減圧チャンバー内の圧力を大気圧と同等に回復させる。この際、減圧チャンバー内への不活性ガスの流入速度は、減圧チャンバー内の内容物が、不活性ガスが流入することによって変形、崩壊、飛散するなどして、内容物の外観や品質に支障が生じない限り、特に限定されることはない。また、不活性ガス雰囲気下で減圧チャンバーを開放することによって、減圧チャンバー内の圧力を大気圧に戻す手段であっても良い。 After the degree of vacuum in the vacuum chamber reaches the second degree of vacuum, exhausting the vacuum chamber is stopped and the inert gas is again introduced into the vacuum chamber to restore the pressure in the vacuum chamber to atmospheric pressure. At this time, the flow rate of the inert gas into the vacuum chamber is not particularly limited, as long as the contents in the vacuum chamber are not deformed, disintegrated, or scattered by the inflow of the inert gas, resulting in a loss of appearance or quality of the contents. Alternatively, the pressure in the vacuum chamber may be returned to atmospheric pressure by opening the vacuum chamber under an inert gas atmosphere.
また、減圧チャンバー内の圧力を大気圧と同等とした後、さらに、減圧チャンバー内に不活性ガスを流入させて、減圧チャンバー内の圧力を大気圧以上に高めることもできる。この場合には、内容物に残存する酸素が不活性ガスで更に置換され、内容物からより多くの酸素を除去することが期待できるが、内容物の取り出し前は、減圧チャンバー内圧力を大気圧と同等となるように減圧させるのはいうまでもない。 After the pressure inside the vacuum chamber is made equal to atmospheric pressure, an inert gas can be introduced into the vacuum chamber to raise the pressure inside the vacuum chamber above atmospheric pressure. In this case, the oxygen remaining in the contents is further replaced with the inert gas, and it is expected that more oxygen can be removed from the contents. However, it goes without saying that the pressure inside the vacuum chamber is reduced to equal to atmospheric pressure before the contents are removed.
その後、減圧チャンバーから内容物を取り出して、ガス置換包装する。ガス置換包装に用いる包装容器としては、容器内に残存する酸素を吸収できるように、酸素吸収機能が付与された公知の包装容器を用いるのが好ましいが、そのような包装容器を用いずに、公知の酸素吸収剤を同封して容器内に残存する酸素が吸収されるようにしてもよい。 The contents are then removed from the vacuum chamber and packaged in gas replacement packaging. As the packaging container used for gas replacement packaging, it is preferable to use a known packaging container that has been given an oxygen absorbing function so that the oxygen remaining in the container can be absorbed, but it is also possible to enclose a known oxygen absorber in the container without using such a packaging container so that the oxygen remaining in the container can be absorbed.
以上のような本実施形態によれば、内容物を包装容器にガス置換包装するに先立って、内容物に含まれる酸素を効率よく除去しておくことによって、特に、包装対象の内容物が嵩高く、より多くの酸素が含まれているような場合であっても、内容物から放出されて容器内に残存する酸素を低減せしめ、包装容器に付与された酸素吸収機能や、容器内に同封された酸素吸収材によって十分に吸収できるようにして、内容物をより長期にわたって保存可能とすることができる。 According to this embodiment, by efficiently removing oxygen from the contents before packaging the contents in a packaging container with gas replacement, even when the contents to be packaged are bulky and contain a large amount of oxygen, the amount of oxygen released from the contents and remaining in the container can be reduced, and the oxygen can be sufficiently absorbed by the oxygen absorption function provided to the packaging container or the oxygen absorbing material enclosed in the container, allowing the contents to be preserved for a longer period of time.
以下、具体的な実施例を挙げて、本発明をより詳細に説明する。 The present invention will be explained in more detail below with specific examples.
[実施例1~7、比較例1~7]
容積70Lの減圧チャンバーに、標準大気圧下の排気速度200L/min、到達真空度0.067Paの真空ポンプを接続した。かかる減圧チャンバーに、重量50gの饅頭を1個収容し、減圧チャンバーを密封した後に、減圧チャンバー内を排気した。
[Examples 1 to 7, Comparative Examples 1 to 7]
A vacuum pump with a volume of 70 L was connected to the vacuum chamber, which had an exhaust speed of 200 L/min under standard atmospheric pressure and an ultimate vacuum of 0.067 Pa. One bun weighing 50 g was placed in the vacuum chamber, and the vacuum chamber was sealed, and then the inside of the vacuum chamber was evacuated.
減圧チャンバー内の圧力が一次減圧度に減圧された時点で、排気を継続させながら、流入速度V2、流入時間Tで、減圧チャンバー内に窒素ガスを流入させた。
このときの一次減圧度、流入速度V2、流入時間Tとともに、一次減圧度下の不活性ガスの流入が安定して行えたか、不安定であったかを表1及び表2に示した。
When the pressure in the vacuum chamber was reduced to the first reduced pressure, nitrogen gas was allowed to flow into the vacuum chamber at an inflow rate V2 and for an inflow time T while continuing evacuation.
Tables 1 and 2 show the primary reduced pressure, the inflow velocity V2, the inflow time T, and whether the inflow of the inert gas under the primary reduced pressure was stable or unstable.
その後、減圧チャンバー内の圧力が二次減圧度に減圧されるまで排気を継続し、排気を停止した後に、減圧チャンバー内に、一次減圧下の不活性ガスの流入速度と同流入速度で窒素ガスを流入させて、減圧チャンバー内の圧力を大気圧と同等になるまで回復させた。
このときの二次減圧度を表1及び表2に示す。
なお、比較例7では、二次減圧度まで減圧することなく、減圧チャンバー内の圧力を大気圧と同等になるまで回復させた。
Thereafter, evacuation was continued until the pressure in the vacuum chamber was reduced to the secondary vacuum level, and after evacuation was stopped, nitrogen gas was allowed to flow into the vacuum chamber at the same inflow rate as the inert gas in the primary vacuum level, thereby restoring the pressure in the vacuum chamber to the same level as atmospheric pressure.
The degree of secondary pressure reduction at this time is shown in Tables 1 and 2.
In Comparative Example 7, the pressure in the vacuum chamber was restored to the same level as atmospheric pressure without reducing the pressure to the second reduced pressure level.
減圧チャンバー内を窒素ガスで大気圧に回復させた後に、窒素ガス雰囲気下で減圧チャンバーから饅頭を取りだして、窒素ガスによりガス置換包装(酸素吸収性フィルム(東洋製罐株式会社製:オキシデック(登録商標))を用いたピロー包装)した。
なお、比較例1は、窒素ガスによるガス置換包装のみとし、内容物に含まれる酸素を除去する操作は不実施とした。
After the pressure inside the vacuum chamber was restored to atmospheric pressure with nitrogen gas, the buns were removed from the vacuum chamber under a nitrogen gas atmosphere and gas-replaced packaging was performed with nitrogen gas (pillow packaging using an oxygen-absorbing film (Oxydec (registered trademark) manufactured by Toyo Seikan Co., Ltd.)).
In Comparative Example 1, only the gas replacement packaging with nitrogen gas was performed, and no operation for removing oxygen from the contents was performed.
ガス置換包装後の容器内のヘッドスペースは82mLであった。ガス置換包装直後の容器内の酸素濃度、5℃で24時間保管した後の容器内の酸素濃度を表1及び表2に示す。
なお、酸素濃度の測定には、東レエンジニアリング製の酸素濃度計(LC-750F)を用いた。
The head space in the container after the gas replacement packaging was 82 mL. The oxygen concentration in the container immediately after the gas replacement packaging and the oxygen concentration in the container after storage at 5° C. for 24 hours are shown in Tables 1 and 2.
The oxygen concentration was measured using an oxygen concentration meter (LC-750F) manufactured by Toray Engineering.
また、ガス置換包装後の内容物の外観、5℃で24時間保管した後の内容物の風味について、次の評価基準で評価した。
[評価基準]
◎:5人の評価者の全員が合格と評価した。
〇:5人の評価者のうち3人以上が合格と評価した。
×:5人の評価者のうち合格と評価したのが2人以下であった。
評価結果を表1及び表2に示す。
In addition, the appearance of the contents after the gas replacement packaging and the flavor of the contents after storage at 5° C. for 24 hours were evaluated according to the following criteria.
[Evaluation Criteria]
⊚: All five evaluators rated it as acceptable.
Good: Three or more of the five evaluators rated it as good.
×: Two or less of the five evaluators rated it as "pass."
The evaluation results are shown in Tables 1 and 2.
以上、本発明について、好ましい実施形態を示して説明したが、本発明は、上述した実施形態にのみ限定されるものではなく、本発明の範囲で種々の変更実施が可能であることは言うまでもない。 The present invention has been described above with reference to preferred embodiments, but it goes without saying that the present invention is not limited to the above-described embodiments, and various modifications are possible within the scope of the present invention.
Claims (7)
前記内容物を減圧チャンバー内に収容して密封し、
前記減圧チャンバー内を排気して、前記減圧チャンバー内を一次減圧度まで減圧した後、排気を継続させながら、前記減圧チャンバー内に不活性ガスを流入させ、
しかる後に、排気を継続させながら、前記減圧チャンバー内への不活性ガスの流入を停止し、前記減圧チャンバー内を更に二次減圧度まで減圧し、
次いで、前記減圧チャンバー内の排気を停止し、前記減圧チャンバー内に再び不活性ガスを流入させ、前記減圧チャンバー内の圧力を大気圧と同等とした後、前記減圧チャンバーから前記内容物を取り出して、ガス置換包装することを特徴とする包装方法。 When packaging the contents in a packaging container,
The contents are placed in a vacuum chamber and sealed;
The inside of the decompression chamber is evacuated to reduce the pressure inside the decompression chamber to a first decompression level, and then an inert gas is introduced into the decompression chamber while continuing the evacuation;
Thereafter, while continuing the evacuation, the inlet of the inert gas into the vacuum chamber is stopped, and the pressure in the vacuum chamber is further reduced to a second reduced pressure;
Next, the exhaust of the vacuum chamber is stopped, and the inert gas is again introduced into the vacuum chamber to make the pressure in the vacuum chamber equal to atmospheric pressure. Thereafter, the contents are removed from the vacuum chamber and gas replacement packaging is performed.
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| JP2005029233A (en) | 2003-07-09 | 2005-02-03 | Dowa Mining Co Ltd | Packaging method and package of substrate with exposed surface of material |
| JP2015039357A (en) | 2013-08-23 | 2015-03-02 | 株式会社古川製作所 | Inert gas replacement packaging apparatus and inert gas replacement packaging method |
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| JP2005029233A (en) | 2003-07-09 | 2005-02-03 | Dowa Mining Co Ltd | Packaging method and package of substrate with exposed surface of material |
| JP2015039357A (en) | 2013-08-23 | 2015-03-02 | 株式会社古川製作所 | Inert gas replacement packaging apparatus and inert gas replacement packaging method |
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