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Title:
PACKAGING METHOD AND PACKAGING COMPRISING A CLOSED OXYGEN-SCAVENGING CONTAINER CONTAINING AN OXYGEN-SENSITIVE SUBSTANCE
Document Type and Number:
WIPO Patent Application WO/2013/087239
Kind Code:
A1
Abstract:
The method for packaging an oxygen-sensitive substance into a container, comprises the following steps : - the oxygen-sensitive substance is introduced into the container, - a de-oxygenating gas containing at least 75% of molecular hydrogen is introduced inside the container containing the oxygen-sensitive substance, - the container containing the oxygen-sensitive substance and the de-oxygenating gas is hermetically closed with a closure, and a catalyst is used inside the container and/or in the container wall and/or in the closure for promoting a reaction between molecular hydrogen and molecular oxygen inside the container.

Inventors:
HERMANS AN (BE)
Application Number:
PCT/EP2012/068173
Publication Date:
June 20, 2013
Filing Date:
September 14, 2012
Export Citation:
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Assignee:
SEDA DE BARCELONA SA (ES)
HERMANS AN (BE)
International Classes:
A23L3/3436
Domestic Patent References:
WO1999005922A11999-02-11
WO2008090354A12008-07-31
Foreign References:
DE102005055632A12007-05-24
US3437427A1969-04-08
GB1188170A1970-04-15
EP0301719A11989-02-01
EP0507207A21992-10-07
Attorney, Agent or Firm:
MATKOWSKA, Franck (9 rue Jacques Prévert, Villeneuve d'Ascq, FR)
Download PDF:
Claims:
CLAIMS

1 . A method for packaging an oxygen-sensitive substance into a container, said method comprising the following steps :

- the oxygen-sensitive substance is introduced into the container, - a de-oxygenating gas containing at least 75% of molecular hydrogen is introduced inside the container containing the oxygen- sensitive substance,

- the container containing the oxygen-sensitive substance and the de-oxygenating gas is hermetically closed with a closure,

and wherein a catalyst is used inside the container and/or in the container wall and/or in the closure for promoting a reaction between molecular hydrogen and molecular oxygen.

2. The method of claim 1 , wherein the closed container containing the oxygen-sensitive substance comprises an internal residual space free from oxygen-sensitive substance and filled with the de- oxygenating gas, said residual space having a volume of not more than 100ml, and more preferably of not more than 30ml.

3. The method of claim 1 or 2, wherein the container is permeable to oxygen.

4. The method of claim 3, wherein the container is made of a polymeric material.

5. The method of any one of claims 1 to 4, wherein the de- oxygenating gas is a mixture of an inert gas and molecular hydrogen.

6. The method of claim 5, wherein the inert gas is nitrogen.

7. The method of any one of claims 1 to 6, wherein the de- oxygenating gas is containing at least 94% of molecular hydrogen.

8. The method of any one of claims 1 to 4, wherein the de- oxygenating gas is containing not less than 99% of molecular hydrogen, and preferably 100% of molecular hydrogen.

9. The method of any one of claims 1 to 8, wherein the catalyst is a redox catalyst.

10. The method of any one of claims 1 to 8, wherein the catalyst is a metal of the Group VIII.

1 1 . The method of any one of claims 1 to 8, wherein the catalyst is palladium or platinum.

12. A packaging comprising a container that is closed by a closure and that is containing an oxygen-sensitive substance and a de- oxygenating gas containing at least from 75% of molecular hydrogen, said packaging also comprising a catalyst inside the container and/or in the container wall and/or in the closure for promoting a reaction between molecular hydrogen and molecular oxygen.

13. The packaging of claim 12, wherein the closed container containing the oxygen-sensitive substance comprises an internal residual space free from oxygen-sensitive substance and filled with the de- oxygenating gas, said residual space having a volume of not more than 100ml, and more preferably of not more than 30ml.

14. The packaging of claim 12 or 13, wherein the container is permeable to oxygen.

15. The packaging of claim 14, wherein the container is made of a polymeric material.

16. The packaging of any one of claims 12 to 15, wherein the de- oxygenating gas is a mixture of an inert gas and molecular hydrogen.

17. The packaging of claim 16, wherein the inert gas is nitrogen.

18. The packaging of any one of claims 12 to 17, wherein the de- oxygenating gas is containing at least 94% of molecular hydrogen.

19. The packaging of any one of claims 12 to 15, wherein the de- oxygenating gas is containing not less than 99% of molecular hydrogen, and preferably 100% of molecular hydrogen.

20. The packaging of any one of claims 12 to 19, wherein the catalyst is a redox catalyst.

21 .The packaging of any one of claims 12 to 20, wherein the catalyst is a metal of the Group VIII.

22. The packaging of any one of claims 12 to 20, wherein the catalyst is palladium or platinum.

23. The method of any one of claims 1 to 1 1 or the packaging of any one of claims 12 to 22, wherein the oxygen sensitive substantive is selected from the group : food product, beverage, medical substance.

Description:
PACKAGING METHOD AND PACKAGING COMPRISING A CLOSED OXYGEN-SCAVENGING CONTAINER CONTAINING AN OXYGEN- SENSITIVE SUBSTANCE Technical Field

The invention relates to a novel packaging comprising a closed oxygen-scavenging container containing an oxygen-sensitive substance that can be altered by oxygen, and to a packaging method for obtaining this novel packaging. The oxygen-sensitive substance can be more particularly, but not only, a food substance or a beverage such as for example juice, beer, wine, a medical product...

Prior Art

The shelf-life of an oxygen-sensitive substance, like for example food substance or beverage, contained in a container can be detrimentally shortened by the presence of oxygen inside the container.

In order to increase the shelf-life of an oxygen-sensitive substance in a container, it is usual to flush the container containing the substance with an inert de-oxygenating gas, and more especially with nitrogen and/or carbon dioxide, in such a way to remove and replace the oxygen initially contained in the container by a volume of said inert gas.

Such a packaging method can eventually be practised with containers that are not permeable to molecular oxygen, like for example air- tightly closed glass containers, but are not sufficiently efficient for containers that are permeable to molecular oxygen, such as for example plastic containers, and in particular PET(polyethylene terephtalate) containers. With containers that are permeable to oxygen, the oxygen-sensitive substance is detrimentally oxidized by the molecular oxygen that comes from the outside of the container and that penetrates inside the container.

For solving this problem, it has already been proposed to add a catalyst inside the container for promoting a reaction between molecular hydrogen and molecular oxygen inside the container, and to flush the container containing the oxygen-sensitive substance with a mixture of an inert gas like nitrogen and/or carbon dioxide with a small volume of molecular hydrogen. The oxygen inside the container is scavenged by the molecular hydrogen that reacts with the oxygen for producing water. Such a solution is disclosed for example in publication GB 1 188 170, wherein the catalyst is a redox catalyst and the container is flushed for example with a gas containing 95% N 2 and 5% H 2 , or in PCT application WO 99/05922 wherein the catalyst is a platinum group metal and the container is flushed with a mixture of inert gas and 3% H 2 .

One skilled in the art in the field of packaging knows that a flammability limit of molecular hydrogen in air in ambient condition is 4% H 2 by volume, and that above this limit of 4%H 2 , the gas mixture containing H 2 becomes flammable in ambient condition. Consequently, up to date, one skilled in the art in the field of packaging has always considered that when a mixture of inert gas, like nitrogen, and hydrogen is flushed inside a container, for safety reasons the volume of H 2 in the gas mixture has to be very low, typically not more than 5.5%H 2 , in order to be sure that the gas mixture in the container is always below this flammability limit .

But one drawback of practising low volume of H 2 is that the molecular H 2 is very quickly consumed in the reaction with oxygen inside the container and that the shelf-life of the oxygen-sensitive substance is actually not strongly increased.

Another solution to increase the shelf-life of a packaged oxygen- sensitive substance is to use containers having high gas barrier properties, in particular oxygen and/or carbon dioxide barrier properties. In particular, it is now common to use multilayered plastic containers, that include at least one gas barrier layer. For example, in the field of bottle packaging, a typical and common multilayered wall structure for a hollow rigid container is a three-layer wall: two internal and external layers made of PET, and one intermediate gas barrier layer sandwiched between the two PET layers.

A first known type of barrier layer is made of, or comprises, polymers that have excellent gas-barrier properties, in particular to O2 and/or CO2, and is generally referred as "passive barrier layer". Among the polymers used for making passive barrier layers, homo- or copolymers of polyamides are commonly used. Among these polyamides, the so-called "MXD6" or "MXD6 nylon" (specific polyamide material manufactured by Mitsubishi Gas Chemical Company, Japan) is preferably used, i.e. a poly(m- xylyleneadipamide) produced by the polycondensation of a diamine component composed mainly of m-xylylenediamine and a dicarboxylic acid component composed mainly of adipic acid.

A second known type of barrier layer, which has been more recently developed, is made of, or comprises, polymeric composition that has oxygen-scavenging properties, and is generally referred as "active barrier layer". Generally speaking, an active barrier layer reacts with the oxygen and "captures" the oxygen when the oxygen penetrates into the layer. Such active barrier layer is thus progressively "consumed" in use.

Examples of polymeric compositions used for making active barrier layer are described notably in European patent application EP-A-0 301 719 or in European patent application EP-A-0 507 207. Said polymeric compositions generally comprise an oxidizable polymer and a transition metal catalyst. In EP-A-0 301 719, the preferred oxidizable polymers are polyamides, and especially MXD6. In EP-0 507 207, one preferred oxidizable polymer is polybutadiene. In both cases, preferred transition metal catalysts are transition metal salts, an in particular cobalt stearate. Other known metal salts used for making such composition are rhodium, manganese, copper, iron.

With multilayered containers having at least one gas barrier layer comprising a polyamide (e.g. MXD6) and a polyester (e.g. PET), very good results can be achieved in terms of shelf life of the packaged substance. More especially when the barrier layer comprises a polyamide (e.g. MXD6), polyester (e.g. PET), and a catalyst such as a cobalt salt, the multilayered container can be used for storing oxygen-sensitive products, such as beer, fruit juice, or the like. The shelf life of packaged product widely depends of the amount of polyamide in the packaging article and of the thickness of the barrier layer.

In return, the use of gas barrier polymer, like polyamide in the container wall renders the recycling of the container more difficult. In addition, when polyamide is used, in particular for making a monolayer container, there is a risk of formation of haze in the container wall due to the orientation of the polyamide during the process for making the container. Said haze formation in the container wall is obviously detrimental for all the applications where it is important to have a transparent container, - i.e. a container whose wall has no eye-visible whitening or haze, in order to have a better appearance of the packaged product.

In order to improve the O2 scavenging performance of a plastic container, it is also known to close the container with a closure cap comprising a layer or liner having O2 scavenging properties.

Another recent route for making a container having oxygen scavenging properties is described in PCT application WO 2008/090354. The O2 scavenging properties are obtained by using an active substance, such as for example a hydride, that is capable of chemically reacting with water and generating molecular hydrogen in situ inside the container, and by making said molecular hydrogen react with oxygen which may ingress the container. This solution is interesting because only very small amount of H 2 is continuously generated in-situ inside the container and in contrast with the aforesaid solution of flushing a mixture of inert gas and hydrogen, the H 2 generation is achieved over a longer period which dramatically improves the shelf-life. One drawback of this solution is however the use of an additional active substance, such as for example a hydride, that can prejudicially contaminate the substance stored in the container.

Objective of the invention

One objective of the invention is to propose a novel solution for packaging an oxygen-sensitive substance in a closed container with an increased shelf-life in comparison with the solution of the prior art wherein the oxygen initially contained in the container is removed by flushing a mixture of inert gas, like nitrogen, and not more than 5.5% of hydrogen.

Summary of the invention

This objective is achieved by the novel method of claim 1 , for packaging an oxygen-sensitive substance into a container, said method comprising the following steps :

- the oxygen-sensitive substance is introduced into the container,

- a de-oxygenating gas containing at least 75% of molecular hydrogen is introduced inside the container containing the oxygen- sensitive substance,

- the container containing the oxygen-sensitive substance and the de-oxygenating gas is hermetically closed with a closure , and wherein a catalyst is used inside the container and/or in the container wall and/or in the closure for promoting a reaction between molecular hydrogen and molecular oxygen.

Another object of the invention is the packaging defined in claim

12. Said packaging comprises a closed container that is containing an oxygen-sensitive substance and a de-oxygenating gas containing at least from 75% of molecular hydrogen, and said packaging also comprising a catalyst inside the container and/or in the container wall and/or in the closure for promoting a reaction between molecular hydrogen and molecular oxygen.

It is the merit of the invention to have overcome the prejudice of the prior art to practice only very small volume of H 2 for safety reasons, and to have tried and demonstrated that very high level of H 2 , i.e. at least 75% H 2 , and preferably almost 100% H 2 , could also be practiced without flammability risk in ambient condition, and with a strong increase of the shelf-life of the packaged substance.

The wording "container" used therein and in the claims means any container that can be used for storing a substance. Within the scope of the invention, the container can be a rigid container, like for example a rigid bottle, a jar, a rigid vessel, a rigid flask, a rigid tube. The container can also be flexible, like for example a pouch or a container made from a film or sheet. The container can be a monolayer container or a multilayer container. The container can be made of any material.

For practising the invention, a large number of catalysts that are known to catalyze the reaction of hydrogen with oxygen can be used, including many transition metals, metal borides (such as nickel boride), metal carbides (such as titanium carbide), metal nitrides (such as titanium nitride), and transition metal salts and complexes. Group VIII metals are particularly efficacious. Of the Group VIII metals, palladium and platinum are especially preferred because of their low toxicity and extreme efficiency in catalyzing the conversion of hydrogen and oxygen to water with little or no byproduct formation. The catalyst is preferably a redox catalyst.

The catalyst can be positioned inside the container, and/ or can be positioned inside a closure for hermetically closing the container, for example in a liner, and/or can be part of the material constituting the container.

Short description of the drawings

Other characteristics and advantages of the invention will appear more clearly on reading the following detailed description which is made by way of non-exhaustive and non-limiting example, and with reference to the accompanying drawings, in which:

- Figures 1 to 4 are graphs showing O 2 concentration (%) over time in the headspace respectively of the bottles of comparative examples 1 , comparative example 2, example 1 and example 2.

- Figures 5 to 8 are graphs showing the O 2 dissolved concentration over time in the water stored in respectively the bottles of comparative examples 1 , comparative example 2, example 1 and example 2.

- Figure 9 is a tertiary diagram for hydrogen, oxygen and nitrogen, with flammability envelope for ambient conditions. Detailed description of the invention

The following detailed description is focused on the testing of different packaging method using rigid bottles for storing water and closed by an add-on closure. Nevertheless, it must be underlined that the scope of the invention is not limited to this particular type of container, but can be extended to any receptacle that can be used for storing a substance and that can be hermetically closed once the flushing step has been performed. Within the scope of the invention, the substance can be any oxygen-sensitive substance that can be altered by oxygen, such as for example wine, beer, fruit juice, sauces, soft drinks, medical substances, etc...

Experimental tests

Comparative example 1

A 200ml glass bottle is filled with tap water (water saturated with O2). After filling, the headspace (residual internal space between the top level of the water and the top opening of the bottle) is not more than 30ml, and is about 20ml.

The bottle is then put in a chamber that is continuously supplied with a de-oxygenating gas containing 94.5%N 2 and 5.5 %H 2 by volume, until the concentration of oxygen in the head space is less than 1 %.

A 2cm 2 palladium wad" is glued in the headspace. A "palladium wad" "is a piece of nonwoven substrate onto which finely divided elemental Palladium is anchored.

The bottle is then hermetically closed with a metallic crown cork. The headspace of the closed bottle contains about 0.7%O2, 93.8%N 2 and

5.5%H 2 .

Comparative example 2

A 330ml PET bottle is filled with de-aerated water (less than 300ppb O2). After filling, the headspace (residual internal space between the top level of the water and the top opening of the bottle) is about 30ml.

The bottle is then put in a chamber that is continuously supplied with a de-oxygenating gas containing 94.5%N 2 and 5.5%H 2 by volume, until the concentration of oxygen in the bottle headspace is about 0.5%.

A 2cm 2 palladium wad" (same as comparative example 1 ) is glued in the headspace.

The bottle is then hermetically closed with an aluminium seal. The headspace of the closed bottle contains about 0.5% O2, 94.0%N 2 and 5.5%H 2 by volume.

Example 1

A 330ml PET bottle is filled with de-aerated water (less than 300ppb O2). After filling, the headspace (residual internal space between the top level of the water and the top opening of the bottle) is not more than about 30ml, and is about 10ml to 15 ml.

A 2cm 2 palladium wads" (same as comparative example 1 ) is glued in the headspace.

A metal screw cap with valve system is mounted on the bottle, the bottle being hermitically closed by the valve system. The valve system is used for evacuating the air contained in the bottle headspace, until bottle is being completely filled by the water (no more headspace containing air).

The valve system is used for introducing in the bottle a de- oxygenating gas that is containing not less than 99.9% H 2 .

The headspace of the closed bottle is equal to the initial headspace volume and contains not less than 99.5% H 2 and 0.5% O 2 .

Example 2

A 330ml bottle made from a PET copolymer (PET commercialized under reference "Wellman Ti818" ) mixed with about 2ppm palladium is filled with de-aerated water (less than 300ppb O 2 ). After filling, the headspace (residual internal space between the top level of the water and the top opening of the bottle) is not more than about 30ml, and is about 10ml to 15 ml. A metal screw cap with valve system is mounted on the bottle, the bottle being hermitically closed by the valve system. The valve system is used for evacuating the air contained in the bottle headspace, until bottle is being completely filled by the water (no more headspace containing air).

The valve system is used for introducing in the bottle a de- oxygenating gas that is containing not less than 99.9% H 2 .

The headspace of the closed bottle is equal to the initial headspace volume and contains not less than 99.5% H 2 and 0.5% O 2 .

Bottle testing

OxySense® test- O? ingress(%) in headspace

The O2 ingress (%) at 22°C in the headspace of the bottles of comparative examples 1 and 2 and in the headspace of the bottles of Examples 1 and 2 has been measured by using the well-known non invasive OxySense® test.

The testing apparatus is OxySense® instrument 210T.

One Oxy2Dot® has been attached inside the bottle in the bottle headspace prior to filling the bottle with water.

To make the measurements, the fibre optic pen of the OxySense® instrument is aligned with the Oxy2Dot® (from the outside of the bottle) making sure that the tip of the pen is almost making contact with bottle. The signal level on the OxySense® software is adjusted by using the up/down arrows. Then the capture button is pressed to obtain the oxygen concentration in the bottle headspace. The oxygen concentration is measured repeatedly over time.

OxySense® test- dissolved O? concentration (ppm)

The dissolved O2 concentration at 22°C in the water contained in the bottles of comparative examples 1 and 2 and in the water contained in the bottles of Examples 1 and 2 has been also measured by using the well-known non invasive OxySense® test. For making the measurement, one Oxy2Dot® has been attached inside the bottle, prior to filling the bottle with water, and in such a way that after water filling, the Oxy2Dot® is immerged in the water contained in the bottle.

The measurement of dissolved O2 concentration in ppm in the water is performed with the same OxySense® instrument.

Experimental Results- figures 1 to 8

The results of O2 ingress (%) measurements in headspace for the bottles of comparative examples 1 and 2 are shown respectively on the graphs of figures 1 and 2, and the results of O2 ingress (%) measurements in headspace for the bottles of Examples 1 and 2 are shown respectively on the graphs of figures 3 and 4.

The results of dissolved O2 concentration (ppm) for the bottles of comparative examples 1 and 2 are shown respectively on the graphs of figures 5 and 6, and the results of dissolved O2 concentration (ppm) for the bottles of Examples 1 and 2 are shown respectively on the graphs of figures 7 and 8.

Figures 2 and 6 show that with a PET bottle having a wall permeable to oxygen the O2 concentration in the headspace and the dissolved O2 concentration are increasing rapidly after 20 days and the dissolved O2 concentration is higher than 1 ppm after roughly 45 days. In contrast with a glass bottle (figures 1 and 5) that is impermeable to oxygen, the oxygen contained in the tap water and in the headspace is consumed rapidly. These comparative examples 1 and 2 demonstrate that the standard solution of flushing the bottle headspace with a gas containing 94.5%N 2 and 5.5%H 2 can be efficient for glass bottles that are not permeable to oxygen, but is not suitable in term of shelf life for PET bottles that are permeable to oxygen.

Figures 3, 4, 7 and 8 (bottle headspace with not less than 99.5%H 2 ) show that with a PET bottle having a wall permeable to oxygen the O2 concentration in the headspace and the dissolved O2 concentration are increasing only after 60 days, the dissolved O2 concentration being still less than 1 ppm after 80 days. In comparison with comparative example 2 (figures 2 and 6), the shelf life has been dramatically increased. This increase of the shelf life is due to the consumption of the oxygen (O2 scavenging) in a reaction with hydrogen for producing water, this reaction being catalyzed by the palladium.

One skilled in the art in the field of packaging knows that flushing a bottle headspace with a gas containing 94.5%N 2 and 5.5%H 2 , like in the comparative examples 1 and 2, is safe in terms a flammability, and prior to the invention there was a prejudice for one skilled in the art in the field of packaging to mandatory practise low level of hydrogen, typically not more than about 5.5% for safety reasons.

The graph of figure 9 is a tertiary diagram for hydrogen, oxygen and nitrogen, with flammability envelope (F) for ambient conditions in dotted line. Actually, this graph of figure 9 shows that there are actually two flammability limits: a lower flammability limit (LFL) of 4%H 2 in air and an upper flammability limit (UFL) in air of 75%, and that above this upper flammability limit (UFL) in air of 75%, the working conditions are outside the flammability envelope (F) and there is no risk of that the hydrogen becomes flammable in ambient condition.

It is thus the merit of the invention to have overcome the prejudice of the prior art to mandatory use low levels of hydrogen (not more than about 5.5%) and in contrast to use on the contrary very high level of hydrogen (not less than 75%) without prejudice for the flammability of hydrogen in ambient condition and with a strong improvement of the shelf life.

Although the use of a deoxygenating gas containing not less than 99.9% is H 2 is preferred, one can also practise the invention with a de- oxygenating gas contains at least 75% H 2 , and more particularly at least 94% H 2 .

In Examples 1 and 2, palladium has been used as catalyst for promoting the reaction between oxygen and hydrogen for producing water. The invention is however not limited to this particular catalyst, and can be practice with any other catalyst that promotes such a reaction. A large number of catalysts that are known to catalyze the reaction of hydrogen with oxygen can be used, including many transition metals, metal borides (such as nickel boride), metal carbides (such as titanium carbide), metal nitrides (such as titanium nitride), and transition metal salts and complexes. Group VIII metals are particularly efficacious. Of the Group VIII metals, palladium and platinum are especially preferred because of their low toxicity and extreme efficiency in catalyzing the conversion of hydrogen and oxygen to water with little or no byproduct formation. The catalyst is preferably a redox catalyst.

The catalyst can be positioned inside the container like in example 1 , and/or can be part of the material constituting the container like in example 2 and/ or can be positioned inside a closure for hermetically closing the container, for example in a liner.