Title of Invention	OXYGEN SCAVENGING COMPOSITION
Abstract	The present invention provides an Oxygen scavenging composition as a concentrate master batch to act as active and passive barrier, said composition comprising a resin carrier which is an alloy of PET with PTN, or PBN or PBT, mixed micron sized and nano-sized iron particles, an alkali metal bisulphate and ascorbate, a metal halide and additives. The iron particle mixture with a particle size in the range of 1 to 50 micron along with nano sized iron particles of 5 to 50 nanometers (nm) having an additional enhanced rate of oxygen absorption. The oxygen scavenging composition also includes metal halide and ascorbates and bisulphates of alkali metals. The oxygen scavenging composition of the present invention as a master batch in a polyester carrier resin containing barrier, color and U.V. light absorbing additives is used in food packaging applications of human consumption, especially those oxygen sensitive food items including alcoholic beverages, fruit beverages etc, where the oxygen permeation levels are to be maintained at very low levels.

Title of Invention

OXYGEN SCAVENGING COMPOSITION

Abstract

The present invention provides an Oxygen scavenging composition as a concentrate master batch to act as active and passive barrier, said composition comprising a resin carrier which is an alloy of PET with PTN, or PBN or PBT, mixed micron sized and nano-sized iron particles, an alkali metal bisulphate and ascorbate, a metal halide and additives. The iron particle mixture with a particle size in the range of 1 to 50 micron along with nano sized iron particles of 5 to 50 nanometers (nm) having an additional enhanced rate of oxygen absorption. The oxygen scavenging composition also includes metal halide and ascorbates and bisulphates of alkali metals. The oxygen scavenging composition of the present invention as a master batch in a polyester carrier resin containing barrier, color and U.V. light absorbing additives is used in food packaging applications of human consumption, especially those oxygen sensitive food items including alcoholic beverages, fruit beverages etc, where the oxygen permeation levels are to be maintained at very low levels.

Full Text	FORM-2 THE PATENTS ACT, 1970 (39 of 1970) & THE PATENTS RULES, 2003 COMPLETE Specification (See section 10 and rule 13) OXYGEN SCAVENGING COMPOSITION FUTURA POLYESTERS LIMITED an Indian Company of Paragon Condominium, 3rd floor, Pandurang Budhkar Marg, Mumbai 400 013, Maharashtra, India THE FOLLOWING SPECIFICATION PARTICULARLY DESCRIBES THE INVENTION AND THE MANNER IN WHICH IT IS TO BE PERFORMED. OXYGEN SCAVENGING COMPOSITION Technical Field This invention relates to polyester resins used in food packaging applications for foods and other items for human consumption. Particularly, this invention relates to polyester resins used for packaging oxygen sensitive food items including alcoholic beverages, fruit beverages and the like, where the oxygen permeation levels are to be maintained at very low levels. Background In this specification the term 'polyester resin' or 'carrier resin' or 'resin carrier' is understood to mean and include any thermoplastic homo polymer or a co polymer and particularly, a PET(Polyethylene Terephthalate) resin or a PTN(Polytrimethylene Naphthalate) resin or PBN(Polybutylene Naphthalate) resin or a Polytrimethylene Terephthalate (PTT) resin or PBT(Polybutylene Terephthalate) resin or a combination or alloy blend of any of these alone or with a naphthalate or butylene compound and includes all linear or branched polyesters. Preferably, the term 'carrier resin' or 'resin carrier' is a resin having a lower melting point than the resin included in the term 'polyester resin'. Polyester resins and carrier resins are typically prepared by processes well known in the art which typically comprise reacting a diol such as 1,3 propanediol, 1,4 butenediol, ethylene glycol, trimethylene glycol, or resorcinol with a dicarboxylic acid such as terephthalic acid, isopththalic acid, or its esters such as phthalic esters or naphthalic esters in a melt phase polymerization step in an approximate 1:1 stoichiometric reaction, preferably in the presence of a catalyst such as antimony or titanium compounds. Melt phase polymerization is followed by post polymerization steps such as crystallization in the temperature range of 100 to 150 degrees Celsius and solid phase polymerization in the temperature range of 195 to 235 degrees Celsius either in a discontinuous batch process or a continuous solid state process. These steps increase the intrinsic viscosity of the resin to a value suitable for conversion into a desired packaging material. 2 These resins are converted to walled containers for food items and other items by typically by an extrusion, a blow molding process or an injection molding or stretch blow molding process or the resin is extruded in the form of a film which is in turn used for making containers such as pouches for packaging food and other items. Hereinafter, the term 'container' will deem to include all containers whether rigid walled or flexible walled, of any shape or size and dimension and includes a pouch, a blister pack, a pharmaceutical pack, a bottle, and a lidded container. One of the parameters affecting the efficiency of these containers is its oxygen transmission and absorption property. Gases affect items packaged in these containers in two primary ways. Each resin has its own gas transmission rate and a walled container, depending on the thickness of the wall and other parameters, will transmit moisture and gases according to a predetermined 'transmission rate'. Secondly, many packaged items release gases in the packed state and these gases again need to be dealt with. Gases, particularly, oxygen effect the items stored within these containers, in that, they effect the freshness, taste and cause deterioration of the nutrients and flavor components of items, particularly food and medicinal products. Also the formation of oxidative byproducts affects product quality. One of the measures used to attenuate the affect of gases is the use of preservatives like sorbates, ascorbates, benzoates, and sulfur dioxide. The use of such preservatives is now being seriously questioned. In fact, the use of preservatives is increasingly being banned. Another method of preventing the ingress of oxygen is the use of 'passive barrier' methods. "Passive" gas barrier protection is offered by certain polymeric layers like ethylene vinyl alcohol (EVOH) or polyvinylidene dichloride (PVDC). In passive barrier there is only a physical blocking of oxygen ingress or egress from the container and there is no reaction with the oxygen. Oxygen scavenging by polymer barrier films especially in the form of multi layers is well known and described in several prior art references including the following US Patents : 5,648,020, 5,498,364, 5,425,986, 5,399,289, 5,350,622 which deal with an oxygen barrier layer in a multi layered container. Such layers are generally of EVOH, PVDC, polyisoprene and the like. 3 Yet another method of reducing oxygen is the use of oxygen scavenging agents in the resin, which act as a barrier to oxygen or which absorb oxygen entrapped in the container. These are referred to popularly as 'active barrier protection agents'. "Active" Oxygen barrier agents or scavenging agents act as barriers to oxygen. In active oxygen protection there is reaction with the oxygen by the oxygen scavenging agent and this scavenging process protects an oxygen sensitive product by not only preventing oxygen from reaching the product from the outside but also absorbing oxygen present within a container. The benefits of oxygen scavenging are numerous. Reduced oxygen enhances freshness, retains taste and protects nutrients and flavor components of food products. Also the formation of oxidative by-products which may affect product quality are decreased. It also eliminates the need of using preservatives like sorbates, ascorbates, benzoates, sulfur dioxide and the like. Various types of oxygen scavengers are used in packaging systems in order to protect them from the detrimental effects of oxygen exposure. There are primarily three types of oxygen scavengers, which are widely utilized. The most conventional approach is the use of metal based absorbers such as iron or its lower oxides, Cobalt or Copper based metals or their lower oxides. Here, the finely divided metal or its lower oxide gets oxidized to its higher state by oxygen in the presence of appropriate humidity or moisture conditions. The second approach of oxygen scavenging is by making use of low molecular weight organic compounds like ascorbic acid or sodium ascorbate which bind oxygen by oxidizing carbon-carbon double bonds. The third method incorporates a polymeric based oxygen scavenging resin along with a catalyst. The polymeric system binds oxygen through oxidation of the polymer chain. Irrespective of the type of oxygen absorber, oxygen scavengers have to satisfy certain other requirements. For instance, the oxygen scavengers should not be themselves affected during the process of extrusion, they should not impair the look of the container, they should not affect the clarity of the container and finally they should conform to existing packaging processes and equipment. A variety of oxygen scavengers have been suggested both in mono layer and multi layer containers. For example, in the OXBAR barrier system the oxygen scavenging 4 component is a polyamide like MXD-6 nylon coupled with a transition metal catalyst (e.g. cobalt). This type of oxygen scavenger has been described in US Patents 5,759,653, 5,239,016, 5,049,624, 5,034,252, 5,021,515 et al., EP 380,830, 380,319, 301,719 and in New Zealand Patent 227,779. US Patents 5,518,792 and 5,405,880 suggest Oxygen scavengers based on polypropylene, US 5,399,289, 5,310,497 and 5,211,875, EP 0520257 and WO 95/04776) have suggested polybutadiene, US patents 5,700,554 and 5,529,833 disclose polyisoprene , (US 5,492,742, 5,364,555, 6,465,065 & 6,391,406 and EP 328336, disclose monomelic and oligomeric oxidizable compounds such as ascorbic acids and ascorbates, salicylic acid , US 5,529,833 discloses the use of chelates squalene and unsaturated fatty acids; US Patent discloses 5,776,361; WO 94/12590 discloses polyterpenes and dihydroantharcene. Compositions comprising copolyamides consisting of 50 % polyamide segments and active oxygen scavenging polyolefin oligomer segments are disclosed in US 6,506,463. Mixture of polymers which comprises at least 40 % of 2,6-naphthalate units and up to 60 % ethylene terephthalate units giving high oxygen barrier are described in US 6,534,169. AmosorbDFC oxygen scavengers from BP Amoco are block polycondensates comprising predominantly polycondensate segments and an oxygen scavenging amount of polyolefin oligomer segments like polybutadiene especially in the presence of a transition metal catalyst, such as cobalt and optionally with benzophenone are described in US 6,558,762, and 6,365,247 Chevron Phillips in association with Cryovac Corp. has developed an oxygen scavenging polymer (OSP) which claims distinction from other oxygen scavenging polymers in that scavenging is conducted without the generation of degradation products that may easily migrate out of the polymer matrix which in turn could cause negative organoleptic effects. The OSP system is a blend of two components - 90% blend is an oxidizable polymer, ethylene methacrylate cyclohexnyl methyl acrylate (EMCM) as the oxidizable resin and 10 % is a catalyst master batch consisting of a cobalt salt and a proprietary photoinitiator (PI). The oxygen scavenging process is catalyzed by the formation of free radicals triggered by the UV activation process. Refer US Patents 5,627,239 & 5,736,616, and WO 9948963,98/51758 and 98/51759. 5 ActiTUF developed by M & G Polymers has a proprietary oxygen scavenger technology which gets activated only when the container is filled with beverage. Inert thin film barrier coatings like ActisTM film of amorphous carbon, Diamond-Like-Carbon (DLC), Bairocade a thermo set epoxy amine, Plasma-Enhanced Chemical Vapor Deposition (PECVD) of silicon dioxide, Glaskin silicon dioxide etc. are generally used for good barrier properties for gases like oxygen, carbon dioxide and the like. Nanocomposites like clays dispersed in a polymer matrix which create a tortuous path for the passage of gas provide effective barrier improvement. AegisOX is a polymerized nanocomposite nylon resin specially formulated for high oxygen and carbon dioxide barrier performance. Triton has a patented technology based on the inclusion of inert inorganic fillers that exhibit a platelet nanostructure which can be easily compounded with a base resin like PET to improve the barrier property. Also in the emerging gas barrier technology Liquid Crystal Polymers play an important role. Most of these commercial oxygen scavengers are capable of absorbing significantly less than 0.4ml of oxygen per gram of the copolymer. The oxidation of iron Fe is the basis for some widely used oxygen scavenger systems. Oxygen absorption occurs in two stages and requires water vapor to be present. The Fe first combines with oxygen and water to form ferrous hydroxide. Further reaction with oxygen and water forms ferric hydroxide which gets stabilized as hydrated ferric oxide 4Fe + 6H20 + 302 -> 4Fe(OH)3 -» 2Fe203.6H20 The amount of oxygen adsorbed is a function of initial Fe powder morphology and its specific surface area. By stoichiometry for typical materials one gram of Fe will absorb approximately 300cc of oxygen. Iron based oxygen absorbers have been suggested in US Patents 4,127,503 of Nov.28,1978 which describes iron based oxygen absorbers having a metal powder, preferably iron, covered with a metal halide. Ageless developed by Mitsubishi Corp. is 6 composed of finely divided ferrous oxide, a chloride salt and a humectant sealed inside a permeable paper or plastic packet much like that used for silica gel but unlike silica gel the packets cannot be reused once exhausted. US 4,192,773 describes metal halide coated iron powder as oxygen scavengers. Other oxygen-scavenging systems are disclosed in US 4,299,719 which states that ferrous carbonate can be combined with a mixture of a reduced iron powder and a metal halide; or an alkali metal hydroxide and/or an alkaline earth metal hydroxide or calcium oxide to give oxygen absorbing composition and US 4,510,162 which discloses an oxygen absorbent composition comprising iron particles and yeast mixed together with moisture, the moisture being provided by a vinegar/water solution or a mixture of ascorbic acid and sodium bisulfate. US 4,711,741 makes use of iron in combination with halogen containing oxy acid salts like NaClO4 or NaCl03 as a composition for oxygen absorbing. Oxygard is a polymer based oxygen scavenger containing about 75 % polyolefin and 25 % reduced iron and is described in US Patent 5,153,038. US 5,928,560 claims acceleration of oxygen absorption rate in the iron system, besides water, by the addition of an acid. US 6,899,822 describes an oxygen absorbing composition for use as a component of a plastic packaging material which includes in relatively sufficient proportions iron, acidifier and electrolyte with the latter two components at high concentrations. US 6,780,916 deals with a resin composition of film forming polyester of PET, PEN, PBT & PTT containing an oxygen scavenger comprising iron particles as the preferred metal amongst other metals and having a size of between about 1 to 70 microns . Though the color and haze values are discussed for the stretch blow molded bottles no information is available on the oxygen scavenging capacity of the resin. 7 US 6,666,988 and 6,508,955 describe an iron-based oxygen scavenging packet which exhibits an increased rate of oxygen absorption in the presence of an accelerator comprising water. The addition of an electrolyte, either dissolved in the water or added as a solid in the oxygen scavenger packet, further increases the rate of oxygen uptake. Electrolytes like NaCl, MgCl2 & CaCl2 are suggested. JP 62-215,010 discloses a deodorizing fiber obtained by treating thermoplastic fibers with inorganic particles of divalent ferrous iron and L-ascorbic acid. US 6,616,861 claims a rapid rate of oxygen absorption by introducing an alcohol-water mixture as an activator for iron-based absorber systems US 6,586,514 describes oxygen-scavenging compositions comprising an oxidizable metal component, an electrolyte component and a solid, non-electrolytic, acidifying component. Examples of oxidizable metals disclosed include iron, zinc, copper, aluminum, and tin. Examples of suitable electrolyte components include various electrolytic alkali, alkaline earth and transition metal halides, sulfates, nitrates, carbonates, sulfites and phosphates, such as sodium chloride, potassium bromide, calcium carbonate, magnesium sulfate and cupric nitrate. All the aforesaid prior art suggestions require that to obtain sufficient oxygen absorption in active-barrier packaging, high loadings of scavenger compositions, including the iron particle based compositions, are often necessary. This typically requires that wall structures of the bottles containing a scavenging composition be relatively thick which results in other undesirable characteristics. From the prior art on iron based oxygen scavengers it is clear that iron based oxygen scavengers have been used predominantly for food packaging applications and sparingly for demanding applications like for packaging beer, fruit juices, ketchup and the like in polyester bottles wherein because of the nature of the products, the permissible oxygen permeation level is very low. There is a need for an oxygen scavenging agent and a resin blend for food packaging applications, for foods required particularly for human consumption, especially oxygen 8 sensitive food items such as alcoholic beverages (beer), fruit beverages, where oxygen levels permitted are relatively very low. An object of this invention is to provide packaging media with an oxygen scavenging composition of the present invention for storing human consumption food items. Another object of this in invention is to provide an oxygen scavenging composition, which does not substantially affect the color of the article , typically a bottle or other polymer container made from the resin incorporating such an agent. Another object of this invention is to provide such an oxygen scavenging agent which will perform with desired results with relatively lesser amount of loadings. Yet another object of the invention is to provide an oxygen scavenging composition which is easy to handle, store and utilize, which does not warrant elaborate precautions and practices. The applicants have surprisingly found that the use of fine iron particles in the micron range combined with nano sized iron particles either alone or in combination with a halide promoter and an acid salt catalyst enhances the oxygen absorption rate of an oxygen scavenging composition and meets with the objects of this invention. According to one embodiment of the invention even better advantage is obtained by incorporating the oxygen scavenger as a master batch in a carrier resin comprising a passive barrier component like PTN or an alloy blend of PET with PTN or PET with PBN and deriving the advantage of both active and passive oxygen barrier properties . The primary feature of the present invention is the provision of an oxygen scavenging composition comprising a judicious mixture of micron size and nano-sized iron particles and additives dispersed uniformly in a suitable non reactive carrier resin having a passive barrier component of an alloy blend of PET with PTN or PBN or PBT and the like, as a master batch having a lower melting point to facilitate easy and uniform dispersion of the active component in a passive barrier medium acting as the carrier. 9 Therefore, the oxygen scavenging composition in accordance with this invention acts both as an active and a passive barrier and is triggered by moisture / water for its reaction with oxygen. Yet another feature of the present invention is the development of a master batch containing a carrier resin comprising alloy blends of PET with PTN, PBN or PBT or their copolyesters as the carrier and having a maximum high loading (of ~ 25 %) of the oxygen scavenger incorporated in it. One more feature of the present invention is to have in the carrier resin used for the master batch, passive barrier additives, amber or other color pigment composition and ultraviolet light absorbers which are critical for sensitive packaging applications like (beer). A particular feature of the present invention is the benefit of delayed action of oxygen absorption arising from the presence of a mixture of relatively coarse and fine micron sized iron particles in addition to the nano sized particles. One more claim of the present invention is the additional passive oxygen scavenging action performed by the carrier resin like the alloy of PET with PTN, PBN or PBT and their blends but more preferably by the alloy of PTN with PET blend due to their excellent passive barrier action towards gases. Summary of the invention According to this invention there is provided an oxygen scavenging composition for polyester resins comprising a resin carrier; and iron particles mixture dispersed in the said resin carrier said iron particle mixture consisting of [i] micron sized iron particles having particle size in the range of 1 to 50 microns; [ii] nano sized iron particles having particle size in the range of 5 to 50 nano meters. 10 In accordance with one embodiment of this invention, the micron sized iron particles are in die range of 1 to 10 microns. In accordance with another embodiment of this invention, the micron sized iron particles are in the range of 15 to 30 microns. In accordance with still another embodiment of this invention, the micron sized iron particles are a mixture of iron particles in the range of 1 to 10 microns and 15 to 30 microns. Typically, the carrier resin is a polyester resin. Preferably, the carrier resin is an alloy of PET with PTN, its co polyesters or its blends or an alloy of PET with PBN, its co polyesters or its blends in a ratio of a maximum of 75:25 %. Typically, the ratio of the mass of carrier resin to the mass of said mixture of iron particles may be in the range of 1: 0.01 to 1: 0.08 and the ratio of the mass of the micron sized iron particles to the mass of the nano sized iron particles may be in the range of 1:0.10 to 1: 0.20. According to another aspect of this invention there is provided an oxygen scavenging composition for polyester resins comprising a resin carrier; iron particles mixture dispersed in the said carrier said iron particle mixture consisting of [i] micron sized iron particles having particle size in the range of 1 to 50 microns; [ii] nano sized iron particles having particle size in the range of 5 to 50 nano meters; and at least one oxidation reaction accelerator. Typically, the oxidation reaction accelerator is at least one alkali metal bisulfate. selected from a group of alkali metal bisulfates consisting of sodium bisulfate, calcium bisulfate, potassium bisulfate, and magnesium bisulfate. 11 Preferably, the oxidation reaction accelerator is at least one compound selected from a group consisting of sodium bisulfate and potassium bisulfate. In accordance with another embodiment of the invention the oxidation reaction accelerator can be a metal halide selected from a group of metal halides consisting of Barium chloride, , Calcium chloride, , Iron(II) chloride, Iron(III) chloride, , Lithium chloride, Magnesium chloride, Magnesium fluoride, , Potassium bromide, Potassium chloride, Potassium iodide, , Sodium bromide, Sodium chloride, Sodium iodide, Strontium chloride, Zinc chloride. Preferably, the oxidation reaction accelerator is at least one metal halide selected from a group consisting of sodium chloride and potassium chloride. Still preferably, the oxidation reaction accelerator is a mixture of at least one alkali metal bisulfate and at least one metal halide. In accordance with another embodiment of the invention the oxidation reaction accelerator can be an ascorbate compound selected from sodium ascorbate, potassium ascorbate, sodium ascorbate. magnesium ascorbate, calcium ascorbate, zinc ascorbate, chromium ascorbate, Typically, the ratio of the mass of the carrier resin to the mass of the oxidation reaction accelerator is in the range of 1: 0.001 to 1:0.01. In accordance with another embodiment of the invention the iron particles are pre-treated with C3 to C8 alcohols selected from a group consisting of n-propanol, n-butanol, pentanol, hexanol, septanol and octanol, Isopropyl alcohol, Isobutyl alcohol, Sec- butyl alcohol, Tertiary butyl alcohol, Isopentyl alcohol, Tertiary pentyl alcohol, Neopentyl alcohol, Cyclopentyl alcohol, Cyclohexyl alcohol and Allyl alcohols, typically, under refiuxing conditions. In accordance with another aspect of this invention there is provided an oxygen scavenging composition for polyester resins comprising a resin carrier; 12 iron particles mixture dispersed in the said carrier said iron particle mixture consisting of [i] micron sized iron particles having particle size in the range of 1 to 50 microns; [ii] nano sized iron particles having particle size in the range of 5 to 50 nano meters; an oxidation reaction accelerator; and barrier additives. In accordance with yet another aspect of this invention there is provided an oxygen scavenging composition for polyester resins comprising a resin carrier; iron particles mixture dispersed in the said carrier said iron particle mixture consisting of [i] micron sized iron particles having particle size in the range of 1 to 50 microns; [ii] nano sized iron particles having particle size in the range of 5 to 50 nano meters; an oxidation reaction accelerator; barrier additives; color imparting additives, and ultraviolet light absorbers. Typically, the barrier additive is at least one barrier additive selected from a group containing sub micronic size particles of clay and sub micronic sized particles of silica. In accordance with an aspect of this invention there is provided a method of preparing an oxygen scavenging composition for polyester resins comprising the steps of (i) preparing an intimate mixture of dried micron sized iron particles having particle size in the range of 1 to 50 microns and dried nano sized iron particles having particle size in the range of 5 to 50 nano meters to form an iron particle mix; (ii) uniformly dispersing the said iron particle mix upto a maximum of 25% in a resin carrier to form a master batch; and (iii) storing the said master batch in an inert atmosphere until required for adding in a polyester resin for imparting oxygen scavenging property. Typically, the step of dispersing the said iron particle mix in the resin carrier is performed by adding the iron particle mix to the resin carrier in a extruder after thoroughly mixing the said iron particle mix , maintaining the extruder at a temperature 13 between 260 degrees Celsius and 285 degrees Celsius, extruding the strand of iron mix dispersed carrier resin, cooling the strand and cutting strand into master batch chips. In accordance with yet another aspect of this invention there is provided a method of imparting oxygen scavenging properties to a polyester resin comprising the steps of (i) preparing a master batch containing an oxygen scavenging composition comprising a resin carrier; and iron particles mixture dispersed in the said resin carrier said iron particle mixture consisting of [a] micron sized iron particles having particle size in the range of 1 to 50 microns; [b] nano sized iron particles having particle size in the range of 5 to 50 nano meters (ii) adding the said master batch to dry polyester resin prior to extrusion/injection molding/stretch blow molding the polyester resin such that the final quantity of the iron particle mix in the polyester resin is in the region of 2500 ppm to 3500 ppm. Therefore the present invention discloses an iron-based active oxygen scavenging composition comprising a mixture of iron particles of 1 to 50 micron and preferably a mixture of 1 to 10 micron and 15 to 30 micron along with nano sized iron particles of 5 to 50 nanometers (nm). Accordingly, the present invention provides an Oxygen scavenging composition which acts both as an active and passive barrier, said composition comprising a resin carrier, mixed micron size and nano-sized iron particles, and optionally at least one alkali bisulphate, and/or a metal halide, and/or ascorbic acid or a metal ascorbate and other desired additives. Typically, the metal ascorbate is at least one ascorbate selected from a group consisting of sodium ascorbate, potassium ascorbate, sodium ascorbate, magnesium ascorbate, calcium ascorbate, zinc ascorbate, chromium ascorbate, The resin carrier is selected preferably from an alloy blend of Polyethylene terephthalate (PET) with Polytrimethylene Naphthalate (PTN), Polybutylene Naphthalate(PBN), 14 Polybutyiene Terephthalate (PBT), Isophthalic acid modified PET like PETI or their copolyesters and their alloy blends preferably PET with PTN or PET with PBN due to their excellent passive barrier properties. The iron particle mixture with a particle size in the range of 1 to 50 micron and preferably a mixture of 1 to 10 micron and 15 to 30 micron along with nano sized iron particles of 5 to 50 nanometers (nm) surprisingly have a synergistically an additional enhanced rate of oxygen absorption. The oxygen scavenging composition for additional benefit also includes metal halide, ascorbates and bisulfates of alkali metals. In an embodiment of the present invention, the oxygen scavenging composition comprises a carrier in the form of a polyester resin selected from an alloy of PET with PTN or PBN or their copolyesters and their blends but preferably PET with PTN or PET with PBN at a maximum of 75:25 % composition. In another preferred embodiment of the present invention, the percentage of oxygen scavenger that is incorporated in said composition is up to a maximum of 25 %. In yet another embodiment of the present invention, an electrolyte in the form of a metal halide to facilitate the oxidation of iron particles and bisulfates of alkali metals is incorporated in said composition. In order to accelerate the oxidation reaction, an acidic component is incorporated in said oxygen scavenging composition in the form of bisulfate of alkali metals and ascorbates of alkali metals. Bisulfates and ascorbates being acidic in nature, they accelerate the iron oxidation reaction by promoting the formation of hydronium ions (H3O+). This hydronium ion helps in abstracting the electrons from iron and facilitates the formation of Fe2+, which is a prerequisite for its reaction with oxygen and act as the oxygen scavenger. The oxidation reaction is provided in the following sequence. 15 Advantageously, the iron particles used in the present invention are pre-treated with C3 to C8 alcohols preferably selected from Propanol, Butanol and the like, under refluxing conditions. These alcohols are effective reductants under dehydrogenation conditions and cause the renewal of the surface of iron particles i.e. they increase the exposure of the number of iron atoms per surface area which helps to increase the oxidation efficiency of iron. Still advantageously, the oxygen scavenging composition of the present invention is compounded with carrier resins containing appropriate quantities of barrier additives, green, blue and amber color compositions, ultraviolet light absorbers and the like. In an embodiment of the present invention, the said composition has an enhanced oxygen absorbing capacity of well over 0.4ml/gm. In another embodiment of the present invention the oxygen scavenging composition comprising polyester resin is achieved by making use of melt mixing equipments like twin screw extruders. In yet another embodiment of the present invention, the pelletized master batch of the oxygen scavenging composition is dried and stored under an inert atmosphere such as nitrogen for further use. The oxygen scavenging composition of the present invention gets triggered by the presence of moisture / water. Appropriate quantities of the oxygen scavenging composition in accordance with this invention can be incorporated in a dried polyester resin preferably selected from a group consisting of an alloy of PET with PTN or PBN or PBT or their copolyesters and blends preferably PET with PBN or PBT and more preferably with PTN prior to extrusion/injection molding/stretch blow molding. The quantities should be such that the final quantity of the iron particle mix in the polyester resin should be in the region of 2500 ppm to 3500 ppm. 16 PTN's excellent passive barrier property compared to the other polymers towards gases are well known. Table - I gives the comparison of the oxygen permeability of the different polyesters. As a carrier for the oxygen scavenger in the present invention PTN is preferred for the master batch because of its superior barrier property towards oxygen and the presence of PTN will augment the function of the iron particle mixture of the present invention. TABLE - I Comparison of the Barrier Property of different Polyesters towards Oxygen Values are for biaxially oriented films and expressed as cc-mil/100in2/24hrs.atm Polyester Type O2 Permeability % Improvement Times better than in O2 barrier over (i.e. lower PET permeability) PET for02 PET 4.2 - - PTT 3.1 35 1.35 PEN 2.33 80 1.80 PTN 0.525 700 8.00 The present invention, the active oxygen scavenger developed and described in die present invention has increased oxygen absorption rate and is effective in its application at lesser loadings thereby improving the characteristics of the packaging eg. botde. Since the oxygen scavenging composition in accordance with tiiis invention is activated by contact with water or water vapor, mono layered single walled barrier bottles or containers made of polyester resin impregnated with the oxygen scavenging composition can be useful for packing highly oxygen sensitive food items such as alcoholic beverages, fruit juices and health beverages which require total absence of oxygen for the duration of intended shelf life. 17 A particular feature of the invention is that since part of the iron composition is nano sized and similar in size to the wavelength of light they do not affect the clarity of the container. Also the presence of nano sized iron particles in the master batch developed and described herein surprisingly also acts as a passive barrier in addition to its main active barrier function. The invention is further explained in the form of following examples. However, this examples should not in any way be considered as limiting the scope of the invention, since, this examples are of exemplary in nature. Example 1 20 g of iron powder consisting of a mixture of particle sizes of ~6 micron, -24 micron and 10 nm in the ratio of 10:70:20 were refluxed with the n-butanol for 12 hours. 200 mg of sodium bisulfate, 80 mg of sodium chloride were added along with 6 ml of water and further refluxed for 3 hours. Following this the alcohol was distilled off and the mixed iron powder impregnated with the bisulfate and the metal halide was dried at 75°C and the resulting dry powder was stored under nitrogen. This dry oxygen scavenger was found to be capable of absorbing oxygen in the presence of moisture. The iron particle mix component of the oxygen scavenging composition was incorporated in carrier resin preforms and bottles made therefrom were tested for oxygen absorption by the gas chromatographic method. The efficiency data of the Oxygen Scavenging component of the present invention in relation to known compositions was tabulated in the following Table - II, which was evaluated by a specially designed manometric method to provide a qualitative figure of oxygen absorption by Oxygen Scavenger also by a gas chromatographic procedure to obtain quantitative values in comparison with the theoretical values. 18 TABLE - II Oxygen Absorbing Efficiency mm Hg RISE IN %02 OXYGEN S.NO SAMPLE MANOMETER ABSORBED(GC) ABSORBEDml/gOFSAMPLE REMARKS Oxygen 122-147 11-60 40-42 Accelerated 1 Scavenger test by heating Powder (OS) to 60°C- does of the present invention not represent the saturationvalue. In a live situation slow reactionis preferred. Amosorb 60-65 - 0.29 Accelerated 2 Oxygen test Scavenger (OS) Powder Oxygen 50 to 55 10 to 15 0.91 Accelerated 3 Scavenging test composition of the present invention as a master batch Oxygen 11-16 70-92 0.18-0.83 Values are for 4 Scavenger OS levels of composition 1000 to 3500 of the presentinvention inperforms ppm in preforms. Preforms with 2 to 5 - 0.36 3000 ppm in 5 Amosorboxygenscavenger performs 6 OScompositionof the presentinvention inBottles 43 to 80 0.32 to 0.74 Values are for OS levels of 2500 to 3500ppm in bottles Note: (i) In U tube manometer the mm Hg rise is directly proportional to the quantity of Oxygen absorbed by the oxygen scavenger. 19 (ii) For gas chromatographic (GC) procedure, oxygen scavenger incorporated performs or bottles are powdered or cut into pieces and a known quantity is taken in a vial. To this a known quantity of water is added and heated to 60°C for 2 hours for acceleration of oxygen absorption. The head space air sample is analyzed by GC at definite time intervals. (iii) The theoretical quantity of oxygen capable of being absorbed by the oxygen scavenger is based on the oxygen absorption value of 300 ml per gram of iron. (iv) The ml/g value is another way of expressing the oxygen scavenging capacity which helps to compare with the published values for oxygen scavenger samples of the prior art. The delayed action by the presence of the mixed micron sized iron particles as described in this invention is elaborated in the following Table - III. Example 1 was repeated with different compositions of the mixture of micron sized iron particles. Nano sized particles were not added so that the influence of the proportion of different sizes of micron particles can be clearly seen. TABLE - III Comparison of the oxygen absorbing rate by different micron size iron particles. Sr.No. Ratio of Oxygen absorption, cc/g Micronsize,~6 micron :~24 micron of sample after 2 hours. 1. 100:0 9.52 2. 0:100 22.8 3. 20:80 17.75 4. 30:70 14.92 5. 40:60 11.86 It is seen from the table that the oxygen absorption rate distinctly differs with the micron size and that the rate is less for the finer micron size. This delayed action is 20 advantageous for the alcoholic beverage like beer in the container as the oxygen scavengers capacity will last throughout the period of storing the alcoholic beer and protect the beer from oxygen ingress. The oxygen scavenger (OS) incorporated in the master batch with a carrier resin was blended with PET having different passive barrier additives and injection molded into preforms and subsequently stretch blow molded into bottles. The OS containing preforms and bottles were tested for their oxygen absorption capability by GC. Results are given in Table - IV. TABLE - IV Oxygen Absorption by the OS in Preforms and Bottles by GC Method Serial No. Preforms or Bottles Weight, g Volume, ml % Oxygen Absorption Ppm Oxygen Absorption 1 Preform Amber Colored ' 28 - 27-34 15-18 2 Bottle Amber Colored' 28 500 41-48 23-27 3 Bottle Amber Colored ' 20 250 51 24 4 Preform Amber Colored 2 28 - 42 24 5 Preform Colorless 2 28 - 40 31 6 Bottle Amber Colored 2 28 500 65 23 7 Bottle Colorless2 28 500 61 32 8 Preform Amber Colored 3 30/33 - 36/38 20/21 9 Bottle Amber Colored 3 30 500 44 25 10 Preform Amber Colored4 30 - 32 18 11 Bottle Amber Colored 4 30 500 45 25 Resin Recipe: 1. Oxygen Scavenger at 2400 ppm (24:6 micron of 2000:400) in a PET carrier resin consisting of 0.63% naphthalate additive 21 2. Oxygen Scavenger at 2200 ppm (24:6 micron of 2000:200) in a PET carrier resin containing 5 % PTN 3. Oxygen Scavenger at 3400 ppm in a PET carrier resin containing 8 % PTN and 1000 ppm nano silica as an additional passive barrier additive 4. Oxygen Scavenger at 3400 ppm in a PET carrier resin containing 8 % PTN and 500 ppm each of nano silica and nano clay as additional passive barrier additives. It follows from the table that the oxygen absorption by the OS in the bottles are generally about 40 - 65 % of the theoretical absorption which is understandable as the oxygen absorbing iron is dispersed in the polymer matrix and may not be easily available for combination with oxygen especially in the short period of testing time. Example 2: Example 1 was repeated except that the ratio of iron particles was changed to 70:10:20 of 6 micron, 24 micron and 10 nm Example 3: Example 1 was repeated by changing the ratio of iron particles to 10:20:70 of 6 micron, 24 micron and l0 nm Example 4: Example 1 was repeated by replacing NaCl with KC1 Example 5: Example 1 was repeated by replacing KHSO4 with NaHS04 Example 6: Example 1 was repeated by replacing both NaCl & KHSO4 with KC1 and NaHS04 Example 7: Example 1 was repeated wherein in addition to the metal halides 20 mg of sodium ascorbate was also added. 22 In Examples 1 to 7 the carrier resin for making the MB was PET-PTN alloy. The Oxygen Scavenging capacities in these experiments followed the order Example 7>1>5>4>2>3>6. Similar experiments i.e. 1 to 7 were carried out with PET-PBN alloy instead of the PET-PTN alloy. Though the trend of Oxygen Scavenging capacities were same in these experiments the Oxygen Scavenging efficiency was observed to be ~ 10% less than that observed with PET-PTN alloy as the carrier. Experiments were also conducted to judge the performance of the Oxygen Scavenging composition with different % compositions of PTN as well as in different size of bottles. The oxygen absorption results obtained by Gas Chromatography are given in Table-V. TABLE - V Oxygen Scavenger's function with variation in % PTN and Bottle Size Serial No. Preforms / Bottles Weight, g Volume, ml % Oxygen Absorption PpmOxygenAbsorption 1 Preform ' 28 - 29.76 16.67 2 Bottle ' 28 500 37.50 21.00 3 Preform2 28 - 27.33 15.30 4 Bottle l 28 500 34.43 19.28 5 Preform J 24 - 34.10 19.10 6 Bottle i 24 330 43.84 24.55 7 PreformJ 28 - 35.95 20.13 8 BottleJ 28 500 44.18 24.74 9 Preform 33 - 38.2 21.39 10 Bottle i 33 650 44.6 24.98 Resin Recipe: 1 25 % PTN in PET-PTN carrier resin Fe OS particles at 2500 ppm 2 15 % PTN in PET-PTN carrier resin Fe OS particles at 2500 ppm 3 8 % PTN in PET-PTN carrier resin Fe OS particles at 3400 ppm 23 As can be seen from the Table above the various preforms and bottles which contain the oxygen scavenger show sufficient oxygen absorption which is satisfactory taking into consideration the presence of the oxygen scavenger iron particles mixture well dispersed in the polymer matrix. Several advantages arise as a result of the oxygen scavenging composition of the present invention. 1. The composition increases the oxygen absorbing rates due to the presence of nano sized iron particles which are so small and their aspect ratio is so high that properties improve with lower loadings of the oxygen scavenger as compared to the use of only micron sized particles. 2. The oxygen scavenging composition of the present invention enhances the barrier properties of the polyester resin by slowing down the permeation of gas molecules through the resin matrix. 3. The oxygen scavenging composition of the present invention is of low cost and has an improved efficiency. 4. The oxygen scavenging composition of the present invention is used to provide active as well as passive oxygen barred packaging containers that can increase the shelf-life of oxygen-sensitive human consumption products by absorbing oxygen present inside the head-space of the container as well as from the container wall in addition to absorbing oxygen permeating from the outside. 5. In the present composition, the limitations in the form of coloration, bottle blowing difficulty, loss of strength in the bottles and decreased barrier performance in the bottles are overcome by adopting the oxygen scavenging composition having a combination of nano and micron sized metal particles. 6. In the present composition, the presence of mixed micron size particles of iron in addition to the nano sized particles, helps in a delayed action of the oxygen scavenger to take care of the oxygen ingress during prolonged storage. 7. The polyester carriers like an alloy of PET with PTN, PBN and PBT used in making the master batch containing the oxygen scavenger also play a role by their passive barrier effect in oxygen ingress. The preferred carrier resin is a PET-PTN alloy blend due to its excellent barrier property. 24 8. The Fe based OS particles in the PET-PTN carrier resin is stable and in the bottle gets triggered by moisture / water thus giving a reasonable shelf life for the resin and bottle. While considerable emphasis has been placed herein on the interrelationships between the component parts of the preferred embodiments of the oxygen scavenging composition disclosed hereinabove and to polyester resin made having the said composition incorporated therein, it will be appreciated that many embodiments can be made and that many changes can be made in the preferred embodiments without departing from the principles laid down in the invention. These and other changes in the preferred embodiment as well as other embodiments of the invention will be apparent to those skilled in the art from the disclosure herein, whereby it is to be distinctly understood that the foregoing descriptive matter is to be interpreted merely as illustrative of the invention and not as a limitation. 25 We Claim: [1] An oxygen scavenging composition for polyester resins comprising a resin carrier; and iron particles mixture dispersed in the said resin carrier said iron particle mixture consisting of [i] micron sized iron particles having particle size in the range of 1 to 50 microns; [ii] nano sized iron particles having particle size in the range of 5 to 50 nano meters. [2] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the micron sized iron particles are in the range of 1 to 10 microns. [3] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the micron sized iron particles are in the range of 15 to 30 microns. [4] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the micron sized are a mixture of iron particles in the range of 1 to 10 microns and 15 to 30 microns. [5] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the micron sized are a mixture of iron particles in the range of 1 to 10 microns and 15 to 30 microns and the ratio of the quantity of iron particles in the range of 1 to 10 microns to the ratio of the particles in the range of 15 to 30 microns lies between 1: 0.10 and 1:0.80. [6] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the ratio of the mass of the micron sized iron particles to the mass of the nano sized iron particles is in the range of 1: 0.10 to 1:0.20. [7] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the ratio of the mass of carrier resin to the mass of said mixture of iron particles is in the range of 1: 0.01 to 1: 0.08. 26 [8] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the carrier resin is a polyester resin having a maximum melting point temperature in the range of 228 to 230° C. [9] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the carrier resin is an alloy of PET with PTN, its co polyesters or its blends. [10] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the carrier resin is a an alloy of PET with PBN, its co polyesters or its blends. [11] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the carrier resin is PET with PBN or PTN in a ratio of a maximum of 75:25 % . [12] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the carrier resin is PTN. [13] An oxygen scavenging composition for polyester resins comprising a resin carrier; iron particles mixture dispersed in the said carrier said iron particle mixture consisting of [i] micron sized iron particles having particle size in the range of 1 to 50 microns; [ii] nano sized iron particles having particle size in the range of 5 to 50 nano meters; and an oxidation reaction accelerator. [14] An oxygen scavenging composition for polyester resins as claimed in claim 14, in which the oxidation reaction accelerator is at least one alkali metal bisulfate. selected from a group of alkali metal bisulfates consisting of sodium bisulfate, calcium bisulfate, potassium bisulfate, magnesium bisulfate. [15] An oxygen scavenging composition for polyester resins as claimed in claim 13, in which the oxidation reaction accelerator is at least one compound selected from a group consisting of sodium bisulfate and potassium bisulfate. 27 [16] An oxygen scavenging composition for polyester resins as claimed 13, in which the oxidation reaction accelerator is a metal halide. [17] An oxygen scavenging composition for polyester resins as claimed 13, in which the oxidation reaction accelerator is at least one metal halide selected from a group of metal halides consisting of Barium chloride, Calcium chloride, , Iron(II) chloride, Iron(III) chloride. Lithium chloride, Magnesium chloride, Magnesium fluoride, , Potassium bromide. Potassium chloride, Potassium iodide, , Sodium bromide, Sodium chloride. Sodium iodide. Strontium chloride, and Zinc chloride. [18] An oxygen scavenging composition for polyester resins as claimed 13, in which the oxidation reaction accelerator is at least one metal halide selected from a group consisting of sodium chloride and potassium chloride. [19] An oxygen scavenging composition for polyester resins as claimed 13, in which the oxidation reaction accelerator is a mixture of at least one alkali metal bisulfate, at least one metal halide. [20] An oxygen scavenging composition for polyester resins as claimed 13, in which the oxidation reaction accelerator is ascorbic acid. [21] An oxygen scavenging composition for polyester resins as claimed 13. in which the oxidation reaction accelerator is at least one metal ascorbate. [22] An oxygen scavenging composition for polyester resins as claimed 13, in which the oxidation reaction accelerator is at least one metal ascorbate selected from a group consisting of sodium ascorbate. potassium ascorbate. sodium ascorbate, magnesium ascorbate, calcium ascorbate, zinc ascorbate, chromium ascorbate, [23] An oxygen scavenging composition for polyester resins as claimed 13, in which the oxidation reaction accelerator is a mixture of at least one alkali metal bisulfate, and at least one metal ascorbate. 28 [24] An oxygen scavenging composition for polyester resins as claimed 13, in which the oxidation reaction accelerator is a mixture of at least one alkali metal halide and at least one metal ascorbate. [25] An oxygen scavenging composition for polyester resins as claimed 13, in which the oxidation reaction accelerator is a mixture of at least one alkali metal bisulfate, at least one metal halide and at least one metal ascorbate. [26] An oxygen scavenging composition for polyester resins as claimed 13, in which the ratio of the mass of the carrier resin to the mass of the oxidation reaction accelerator is in the range of 1: 0.001 to 1: 0.01. [27] An oxygen scavenging composition for polyester resins as claimed 1, in which the iron particles are pre-treated with C3 to C8 alcohols selected from a group consisting of n-propanol, n-butanol, pentanol, hexanol, septanol and octanol, Isopropyl alcohol, Isobutyl alcohol, Sec- butyl alcohol , Tertiary butyl alcohol, Isopentyl alcohol , Tertiary pentyl alcohol, Neopentyl alcohol, Cyclopentyl alcohol, Cyclohexyl alcohol and Allyl alcohols. [28] An oxygen scavenging composition for polyester resins as claimed 1, in which the iron particles are pre-treated with C3 to C8 alcohols under refluxing conditions. [29] An oxygen scavenging composition for polyester resins comprising a resin carrier; iron particles mixture dispersed in the said carrier said iron particle mixture consisting of [i] micron sized iron particles having particle size in the range of 1 to 50 microns; [ii] nano sized iron particles having particle size in the range of 5 to 50 nano meters; an oxidation reaction accelerator; and barrier additives. [30] An oxygen scavenging composition for polyester resins comprising a resin carrier; iron particles mixture dispersed in the said carrier 29 said iron particle mixture consisting of [i] micron sized iron particles having particle size in the range of 1 to 50 microns; [ii] nano sized iron particles having particle size in the range of 5 to 50 nano meters; an oxidation reaction accelerator; barrier additives; color imparting additives, and ultraviolet light absorbers. [31] An oxygen scavenging composition for polyester resins as claimed in claim 30, in which the barrier additive is at least one barrier additive selected from a group containing sub micronic size particles of clay and sub micronic sized particles of silica. [32] A method of preparing an oxygen scavenging composition for polyester resins comprising the steps of (i) preparing an intimate mixture of dried micron sized iron particles having particle size in the range of 1 to 50 microns and dried nano sized iron particles having particle size in the range of 5 to 50 nano meters to form an iron particle mix; (ii) uniformly dispersing the said iron particle mix upto a maximum of 25% in a resin carrier to form a master batch ; and (iii) storing the said master batch in an inert atmosphere until required for adding in a polyester resin for imparting oxygen scavenging property. [33] A method of preparing an oxygen scavenging composition for polyester resins comprising the steps of (i) preparing an intimate mixture of dried micron sized iron particles having particle size in the range of 1 to 50 microns and dried nano sized iron particles having particle size in the range of 5 to 50 nano meters to form an iron particle mix adding at least one oxidation reaction accelerator to the iron particle mix to form a dry homogenous mixture; (ii) uniformly dispersing the said homogenous mixture upto a maximum of 25% in a resin carrier to form a master batch : (iii) storing the said master batch in an inert atmosphere until required for adding in a polyester resin for imparting oxygen scavenging property. 30 [34] A method of preparing an oxygen scavenging composition for polyester resins as claimed in clam 33. wherein the homogenous mixture is refluxed with at least one alcohol from the C3 to C8 group of alcohols and the resultant mixture is dried at upto 75 degrees Celsius. [35] A method of preparing an oxygen scavenging composition for polyester resins as claimed in claim 33, in which the step of dispersing the said iron particle mix in the resin carrier is performed by adding the iron particle mix to the resin carrier in an extruder after thoroughly mixing the said iron particle mix , maintaining the extruder at a temperature between 260 degrees Celsius and 285 degrees Celsius, extruding the strand of iron mix dispersed carrier resin, cooling the strand and cutting strand into master batch chips. [36] A method of imparting oxygen scavenging properties to a polyester resin comprising the steps of (i) preparing a master batch containing an oxygen scavenging composition comprising a resin carrier; and iron particles mixture dispersed in the said resin carrier said iron particle mixture consisting of [a] micron sized iron particles having particle size in the range of 1 to 50 microns; [b] nano sized iron particles having particle size in the range of 5 to 50 nano meters (ii) adding the said master batch to dry polyester resin prior to extrusion/injection molding/stretch blow molding the polyester resin such that the final quantity of the iron particle mix in the polyester resin is in the region of 2500 ppm to 3500 ppm. [37] A method of imparting oxygen scavenging properties to a polyester resin as claimed in claim 36, in which the melting point of the carrier resin is at most between 228 degrees Celsius and 230 degrees Celsius and the melting point of the polyester resin lies between 246 degrees Celsius and 250 degrees Celsius. [38] A polyester resin having incorporated therein an oxygen scavenging composition as claimed in claim 1. 31 [39] A polyester resin having incorporated therein an oxygen scavenging composition as claimed in claim 13. [40] A polyester resin having incorporated therein an oxygen scavenging composition as claimed in claim 29. [ 41] A container defined by at least one wall, wherein the wall comprises a polyester resin having an oxygen scavenging composition as claimed in claim 1. [42] A container defined by at least one wall, wherein the wall comprises a polyester resin having an oxygen scavenging composition as claimed in claim 13. [43] A container defined by at least one wall, wherein the wall comprises a polyester resin having an oxygen scavenging composition as claimed in claim 44. 32 Abstract The present invention provides an Oxygen scavenging composition as a concentrate master batch to act as active and passive barrier, said composition comprising a resin carrier which is an alloy of PET with PTN, or PBN or PBT, mixed micron sized and nano-sized iron particles, an alkali metal bisulphate and ascorbate , a metal halide and additives. The iron particle mixture with a particle size in the range of 1 to 50 micron along with nano sized iron particles of 5 to 50 nanometers (nm) having an additional enhanced rate of oxygen absorption. The oxygen scavenging composition also includes metal halide and ascorbates and bisulphates of alkali metals. The oxygen scavenging composition of the present invention as a master batch in a polyester carrier resin containing barrier, color and U.V. light absorbing additives is used in food packaging applications of human consumption, especially those oxygen sensitive food items including alcoholic beverages, fruit beverages etc, where the oxygen permeation levels are to be maintained at very low levels.

Full Text

FORM-2
THE PATENTS ACT, 1970
(39 of 1970)
&
THE PATENTS RULES, 2003
COMPLETE
Specification
(See section 10 and rule 13)
OXYGEN SCAVENGING COMPOSITION
FUTURA POLYESTERS LIMITED
an Indian Company
of Paragon Condominium, 3rd floor, Pandurang Budhkar Marg,
Mumbai 400 013, Maharashtra, India
THE FOLLOWING SPECIFICATION PARTICULARLY DESCRIBES THE
INVENTION AND THE MANNER IN WHICH IT IS TO BE PERFORMED.

OXYGEN SCAVENGING COMPOSITION Technical Field
This invention relates to polyester resins used in food packaging applications for foods and other items for human consumption.
Particularly, this invention relates to polyester resins used for packaging oxygen sensitive food items including alcoholic beverages, fruit beverages and the like, where the oxygen permeation levels are to be maintained at very low levels.
Background
In this specification the term 'polyester resin' or 'carrier resin' or 'resin carrier' is understood to mean and include any thermoplastic homo polymer or a co polymer and particularly, a PET(Polyethylene Terephthalate) resin or a PTN(Polytrimethylene Naphthalate) resin or PBN(Polybutylene Naphthalate) resin or a Polytrimethylene Terephthalate (PTT) resin or PBT(Polybutylene Terephthalate) resin or a combination or alloy blend of any of these alone or with a naphthalate or butylene compound and includes all linear or branched polyesters. Preferably, the term 'carrier resin' or 'resin
carrier' is a resin having a lower melting point than the resin included in the term 'polyester resin'.
Polyester resins and carrier resins are typically prepared by processes well known in the
art which typically comprise reacting a diol such as 1,3 propanediol, 1,4 butenediol, ethylene glycol, trimethylene glycol, or resorcinol with a dicarboxylic acid such as terephthalic acid, isopththalic acid, or its esters such as phthalic esters or naphthalic esters in a melt phase polymerization step in an approximate 1:1 stoichiometric reaction, preferably in the presence of a catalyst such as antimony or titanium compounds. Melt phase polymerization is followed by post polymerization steps such as crystallization in the temperature range of 100 to 150 degrees Celsius and solid phase polymerization in the temperature range of 195 to 235 degrees Celsius either in a discontinuous batch
process or a continuous solid state process. These steps increase the intrinsic viscosity of the resin to a value suitable for conversion into a desired packaging material.
2

These resins are converted to walled containers for food items and other items by typically by an extrusion, a blow molding process or an injection molding or stretch blow molding process or the resin is extruded in the form of a film which is in turn used for making containers such as pouches for packaging food and other items. Hereinafter, the term 'container' will deem to include all containers whether rigid walled or flexible walled, of any shape or size and dimension and includes a pouch, a blister pack, a pharmaceutical pack, a bottle, and a lidded container.
One of the parameters affecting the efficiency of these containers is its oxygen transmission and absorption property. Gases affect items packaged in these containers in two primary ways. Each resin has its own gas transmission rate and a walled container, depending on the thickness of the wall and other parameters, will transmit moisture and gases according to a predetermined 'transmission rate'. Secondly, many packaged items release gases in the packed state and these gases again need to be dealt with. Gases, particularly, oxygen effect the items stored within these containers, in that, they effect the freshness, taste and cause deterioration of the nutrients and flavor components of items, particularly food and medicinal products. Also the formation of oxidative byproducts affects product quality.
One of the measures used to attenuate the affect of gases is the use of preservatives like sorbates, ascorbates, benzoates, and sulfur dioxide. The use of such preservatives is now being seriously questioned. In fact, the use of preservatives is increasingly being banned.
Another method of preventing the ingress of oxygen is the use of 'passive barrier' methods. "Passive" gas barrier protection is offered by certain polymeric layers like ethylene vinyl alcohol (EVOH) or polyvinylidene dichloride (PVDC). In passive barrier there is only a physical blocking of oxygen ingress or egress from the container and there is no reaction with the oxygen. Oxygen scavenging by polymer barrier films especially in the form of multi layers is well known and described in several prior art references including the following US Patents : 5,648,020, 5,498,364, 5,425,986, 5,399,289, 5,350,622 which deal with an oxygen barrier layer in a multi layered container. Such layers are generally of EVOH, PVDC, polyisoprene and the like.
3

Yet another method of reducing oxygen is the use of oxygen scavenging agents in the resin, which act as a barrier to oxygen or which absorb oxygen entrapped in the container. These are referred to popularly as 'active barrier protection agents'. "Active" Oxygen barrier agents or scavenging agents act as barriers to oxygen. In active oxygen protection there is reaction with the oxygen by the oxygen scavenging agent and this scavenging process protects an oxygen sensitive product by not only preventing oxygen from reaching the product from the outside but also absorbing oxygen present within a container.
The benefits of oxygen scavenging are numerous. Reduced oxygen enhances freshness, retains taste and protects nutrients and flavor components of food products. Also the
formation of oxidative by-products which may affect product quality are decreased. It also eliminates the need of using preservatives like sorbates, ascorbates, benzoates, sulfur dioxide and the like.
Various types of oxygen scavengers are used in packaging systems in order to protect them from the detrimental effects of oxygen exposure. There are primarily three types of oxygen scavengers, which are widely utilized. The most conventional approach is the use of metal based absorbers such as iron or its lower oxides, Cobalt or Copper based metals or their lower oxides. Here, the finely divided metal or its lower oxide gets oxidized to its higher state by oxygen in the presence of appropriate humidity or moisture conditions. The second approach of oxygen scavenging is by making use of low molecular weight organic compounds like ascorbic acid or sodium ascorbate which bind oxygen by oxidizing carbon-carbon double bonds. The third method incorporates a polymeric based oxygen scavenging resin along with a catalyst. The polymeric system binds oxygen through oxidation of the polymer chain. Irrespective of the type of oxygen absorber, oxygen scavengers have to satisfy certain other requirements. For instance, the oxygen scavengers should not be themselves affected during the process of extrusion, they should not impair the look of the container, they should not affect the clarity of the container and finally they should conform to existing packaging processes and equipment.
A variety of oxygen scavengers have been suggested both in mono layer and multi layer containers. For example, in the OXBAR barrier system the oxygen scavenging
4

component is a polyamide like MXD-6 nylon coupled with a transition metal catalyst (e.g. cobalt). This type of oxygen scavenger has been described in US Patents 5,759,653, 5,239,016, 5,049,624, 5,034,252, 5,021,515 et al., EP 380,830, 380,319, 301,719 and in New Zealand Patent 227,779.
US Patents 5,518,792 and 5,405,880 suggest Oxygen scavengers based on polypropylene, US 5,399,289, 5,310,497 and 5,211,875, EP 0520257 and WO 95/04776) have suggested polybutadiene, US patents 5,700,554 and 5,529,833 disclose polyisoprene , (US 5,492,742, 5,364,555, 6,465,065 & 6,391,406 and EP 328336, disclose monomelic and oligomeric oxidizable compounds such as ascorbic acids and ascorbates, salicylic acid , US 5,529,833 discloses the use of chelates squalene and unsaturated fatty acids; US Patent discloses 5,776,361; WO 94/12590 discloses polyterpenes and dihydroantharcene. Compositions comprising copolyamides consisting of 50 % polyamide segments and active oxygen scavenging polyolefin oligomer segments are disclosed in US 6,506,463. Mixture of polymers which comprises at least 40 % of 2,6-naphthalate units and up to 60 % ethylene terephthalate units giving high oxygen barrier are described in US 6,534,169.
AmosorbDFC oxygen scavengers from BP Amoco are block polycondensates comprising predominantly polycondensate segments and an oxygen scavenging amount of polyolefin oligomer segments like polybutadiene especially in the presence of a transition metal catalyst, such as cobalt and optionally with benzophenone are described in US 6,558,762, and 6,365,247
Chevron Phillips in association with Cryovac Corp. has developed an oxygen scavenging polymer (OSP) which claims distinction from other oxygen scavenging polymers in that scavenging is conducted without the generation of degradation products that may easily migrate out of the polymer matrix which in turn could cause negative organoleptic effects. The OSP system is a blend of two components - 90% blend is an oxidizable polymer, ethylene methacrylate cyclohexnyl methyl acrylate (EMCM) as the oxidizable resin and 10 % is a catalyst master batch consisting of a cobalt salt and a proprietary photoinitiator (PI). The oxygen scavenging process is catalyzed by the formation of free radicals triggered by the UV activation process. Refer US Patents 5,627,239 & 5,736,616, and WO 9948963,98/51758 and 98/51759.
5

ActiTUF developed by M & G Polymers has a proprietary oxygen scavenger technology which gets activated only when the container is filled with beverage.
Inert thin film barrier coatings like ActisTM film of amorphous carbon, Diamond-Like-Carbon (DLC), Bairocade a thermo set epoxy amine, Plasma-Enhanced Chemical Vapor Deposition (PECVD) of silicon dioxide, Glaskin silicon dioxide etc. are generally used for good barrier properties for gases like oxygen, carbon dioxide and the like.
Nanocomposites like clays dispersed in a polymer matrix which create a tortuous path for the passage of gas provide effective barrier improvement. AegisOX is a polymerized nanocomposite nylon resin specially formulated for high oxygen and carbon dioxide barrier performance. Triton has a patented technology based on the inclusion of inert inorganic fillers that exhibit a platelet nanostructure which can be easily compounded with a base resin like PET to improve the barrier property.
Also in the emerging gas barrier technology Liquid Crystal Polymers play an important role.
Most of these commercial oxygen scavengers are capable of absorbing significantly less than 0.4ml of oxygen per gram of the copolymer.
The oxidation of iron Fe is the basis for some widely used oxygen scavenger systems. Oxygen absorption occurs in two stages and requires water vapor to be present. The Fe first combines with oxygen and water to form ferrous hydroxide. Further reaction with oxygen and water forms ferric hydroxide which gets stabilized as hydrated ferric oxide 4Fe + 6H20 + 302 -> 4Fe(OH)3 -» 2Fe203.6H20
The amount of oxygen adsorbed is a function of initial Fe powder morphology and its specific surface area. By stoichiometry for typical materials one gram of Fe will absorb approximately 300cc of oxygen.
Iron based oxygen absorbers have been suggested in US Patents 4,127,503 of Nov.28,1978 which describes iron based oxygen absorbers having a metal powder, preferably iron, covered with a metal halide. Ageless developed by Mitsubishi Corp. is
6

composed of finely divided ferrous oxide, a chloride salt and a humectant sealed inside a permeable paper or plastic packet much like that used for silica gel but unlike silica gel the packets cannot be reused once exhausted.
US 4,192,773 describes metal halide coated iron powder as oxygen scavengers.
Other oxygen-scavenging systems are disclosed in US 4,299,719 which states that ferrous carbonate can be combined with a mixture of a reduced iron powder and a metal halide; or an alkali metal hydroxide and/or an alkaline earth metal hydroxide or calcium oxide to give oxygen absorbing composition and US 4,510,162 which discloses an oxygen absorbent composition comprising iron particles and yeast mixed together with moisture, the moisture being provided by a vinegar/water solution or a mixture of ascorbic acid and sodium bisulfate.
US 4,711,741 makes use of iron in combination with halogen containing oxy acid salts like NaClO4 or NaCl03 as a composition for oxygen absorbing.
Oxygard is a polymer based oxygen scavenger containing about 75 % polyolefin and 25 % reduced iron and is described in US Patent 5,153,038.
US 5,928,560 claims acceleration of oxygen absorption rate in the iron system, besides water, by the addition of an acid.
US 6,899,822 describes an oxygen absorbing composition for use as a component of a plastic packaging material which includes in relatively sufficient proportions iron, acidifier and electrolyte with the latter two components at high concentrations.
US 6,780,916 deals with a resin composition of film forming polyester of PET, PEN, PBT & PTT containing an oxygen scavenger comprising iron particles as the preferred metal amongst other metals and having a size of between about 1 to 70 microns . Though the color and haze values are discussed for the stretch blow molded bottles no information is available on the oxygen scavenging capacity of the resin.
7

US 6,666,988 and 6,508,955 describe an iron-based oxygen scavenging packet which exhibits an increased rate of oxygen absorption in the presence of an accelerator comprising water. The addition of an electrolyte, either dissolved in the water or added as a solid in the oxygen scavenger packet, further increases the rate of oxygen uptake. Electrolytes like NaCl, MgCl2 & CaCl2 are suggested.
JP 62-215,010 discloses a deodorizing fiber obtained by treating thermoplastic fibers with inorganic particles of divalent ferrous iron and L-ascorbic acid.
US 6,616,861 claims a rapid rate of oxygen absorption by introducing an alcohol-water mixture as an activator for iron-based absorber systems
US 6,586,514 describes oxygen-scavenging compositions comprising an oxidizable metal component, an electrolyte component and a solid, non-electrolytic, acidifying component. Examples of oxidizable metals disclosed include iron, zinc, copper, aluminum, and tin. Examples of suitable electrolyte components include various electrolytic alkali, alkaline earth and transition metal halides, sulfates, nitrates, carbonates, sulfites and phosphates, such as sodium chloride, potassium bromide, calcium carbonate, magnesium sulfate and cupric nitrate.
All the aforesaid prior art suggestions require that to obtain sufficient oxygen absorption in active-barrier packaging, high loadings of scavenger compositions, including the iron particle based compositions, are often necessary. This typically requires that wall structures of the bottles containing a scavenging composition be relatively thick which results in other undesirable characteristics.
From the prior art on iron based oxygen scavengers it is clear that iron based oxygen scavengers have been used predominantly for food packaging applications and sparingly for demanding applications like for packaging beer, fruit juices, ketchup and the like in polyester bottles wherein because of the nature of the products, the permissible oxygen permeation level is very low.
There is a need for an oxygen scavenging agent and a resin blend for food packaging applications, for foods required particularly for human consumption, especially oxygen
8

sensitive food items such as alcoholic beverages (beer), fruit beverages, where oxygen levels permitted are relatively very low.
An object of this invention is to provide packaging media with an oxygen scavenging composition of the present invention for storing human consumption food items.
Another object of this in invention is to provide an oxygen scavenging composition, which does not substantially affect the color of the article , typically a bottle or other polymer container made from the resin incorporating such an agent.
Another object of this invention is to provide such an oxygen scavenging agent which will perform with desired results with relatively lesser amount of loadings. Yet another object of the invention is to provide an oxygen scavenging composition which is easy to handle, store and utilize, which does not warrant elaborate precautions and practices.
The applicants have surprisingly found that the use of fine iron particles in the micron range combined with nano sized iron particles either alone or in combination with a halide promoter and an acid salt catalyst enhances the oxygen absorption rate of an oxygen scavenging composition and meets with the objects of this invention.
According to one embodiment of the invention even better advantage is obtained by incorporating the oxygen scavenger as a master batch in a carrier resin comprising a passive barrier component like PTN or an alloy blend of PET with PTN or PET with PBN and deriving the advantage of both active and passive oxygen barrier properties .
The primary feature of the present invention is the provision of an oxygen scavenging composition comprising a judicious mixture of micron size and nano-sized iron particles and additives dispersed uniformly in a suitable non reactive carrier resin having a passive barrier component of an alloy blend of PET with PTN or PBN or PBT and the like, as a master batch having a lower melting point to facilitate easy and uniform dispersion of the active component in a passive barrier medium acting as the carrier.
9

Therefore, the oxygen scavenging composition in accordance with this invention acts both as an active and a passive barrier and is triggered by moisture / water for its reaction with oxygen.
Yet another feature of the present invention is the development of a master batch containing a carrier resin comprising alloy blends of PET with PTN, PBN or PBT or their copolyesters as the carrier and having a maximum high loading (of ~ 25 %) of the oxygen scavenger incorporated in it.
One more feature of the present invention is to have in the carrier resin used for the master batch, passive barrier additives, amber or other color pigment composition and ultraviolet light absorbers which are critical for sensitive packaging applications like (beer).
A particular feature of the present invention is the benefit of delayed action of oxygen absorption arising from the presence of a mixture of relatively coarse and fine micron sized iron particles in addition to the nano sized particles.
One more claim of the present invention is the additional passive oxygen scavenging action performed by the carrier resin like the alloy of PET with PTN, PBN or PBT and their blends but more preferably by the alloy of PTN with PET blend due to their excellent passive barrier action towards gases.
Summary of the invention
According to this invention there is provided an oxygen scavenging composition for polyester resins comprising
a resin carrier; and
iron particles mixture dispersed in the said resin carrier
said iron particle mixture consisting of
[i] micron sized iron particles having particle size in the range of 1 to 50 microns;
[ii] nano sized iron particles having particle size in the range of 5 to 50 nano meters.
10

In accordance with one embodiment of this invention, the micron sized iron particles are in die range of 1 to 10 microns.
In accordance with another embodiment of this invention, the micron sized iron particles are in the range of 15 to 30 microns.
In accordance with still another embodiment of this invention, the micron sized iron particles are a mixture of iron particles in the range of 1 to 10 microns and 15 to 30 microns.
Typically, the carrier resin is a polyester resin.
Preferably, the carrier resin is an alloy of PET with PTN, its co polyesters or its blends or an alloy of PET with PBN, its co polyesters or its blends in a ratio of a maximum of 75:25 %.
Typically, the ratio of the mass of carrier resin to the mass of said mixture of iron
particles may be in the range of 1: 0.01 to 1: 0.08 and the ratio of the mass
of the micron sized iron particles to the mass of the nano sized iron particles may be in the range of 1:0.10 to 1: 0.20.
According to another aspect of this invention there is provided an oxygen scavenging
composition for polyester resins comprising
a resin carrier;
iron particles mixture dispersed in the said carrier
said iron particle mixture consisting of
[i] micron sized iron particles having particle size in the range of 1 to 50 microns;
[ii] nano sized iron particles having particle size in the range of 5 to 50 nano meters; and at least one oxidation reaction accelerator.
Typically, the oxidation reaction accelerator is at least one alkali metal bisulfate. selected from a group of alkali metal bisulfates consisting of sodium bisulfate, calcium bisulfate, potassium bisulfate, and magnesium bisulfate.
11

Preferably, the oxidation reaction accelerator is at least one compound selected from a group consisting of sodium bisulfate and potassium bisulfate.
In accordance with another embodiment of the invention the oxidation reaction accelerator can be a metal halide selected from a group of metal halides consisting of Barium chloride, , Calcium chloride, , Iron(II) chloride, Iron(III) chloride, , Lithium chloride, Magnesium chloride, Magnesium fluoride, , Potassium bromide, Potassium chloride, Potassium iodide, , Sodium bromide, Sodium chloride, Sodium iodide, Strontium chloride, Zinc chloride.
Preferably, the oxidation reaction accelerator is at least one metal halide selected from a group consisting of sodium chloride and potassium chloride.
Still preferably, the oxidation reaction accelerator is a mixture of at least one alkali metal bisulfate and at least one metal halide.
In accordance with another embodiment of the invention the oxidation reaction accelerator can be an ascorbate compound selected from sodium ascorbate, potassium ascorbate, sodium ascorbate. magnesium ascorbate, calcium ascorbate, zinc ascorbate, chromium ascorbate,
Typically, the ratio of the mass of the carrier resin to the mass of the oxidation reaction accelerator is in the range of 1: 0.001 to 1:0.01.
In accordance with another embodiment of the invention the iron particles are pre-treated with C3 to C8 alcohols selected from a group consisting of n-propanol, n-butanol, pentanol, hexanol, septanol and octanol, Isopropyl alcohol, Isobutyl alcohol, Sec- butyl alcohol, Tertiary butyl alcohol, Isopentyl alcohol, Tertiary pentyl alcohol, Neopentyl alcohol, Cyclopentyl alcohol, Cyclohexyl alcohol and Allyl alcohols, typically, under refiuxing conditions.
In accordance with another aspect of this invention there is provided an oxygen scavenging composition for polyester resins comprising a resin carrier;
12

iron particles mixture dispersed in the said carrier said iron particle mixture consisting of
[i] micron sized iron particles having particle size in the range of 1 to 50 microns;
[ii] nano sized iron particles having particle size in the range of 5 to 50 nano meters; an oxidation reaction accelerator; and barrier additives.
In accordance with yet another aspect of this invention there is provided an oxygen
scavenging composition for polyester resins comprising
a resin carrier;
iron particles mixture dispersed in the said carrier
said iron particle mixture consisting of
[i] micron sized iron particles having particle size in the range of 1 to 50 microns;
[ii] nano sized iron particles having particle size in the range of 5 to 50 nano meters; an oxidation reaction accelerator; barrier additives; color imparting additives, and ultraviolet light absorbers.
Typically, the barrier additive is at least one barrier additive selected from a group containing sub micronic size particles of clay and sub micronic sized particles of silica.
In accordance with an aspect of this invention there is provided a method of preparing an oxygen scavenging composition for polyester resins comprising the steps of
(i) preparing an intimate mixture of dried micron sized iron particles having particle size in the range of 1 to 50 microns and dried nano sized iron particles having particle size in the range of 5 to 50 nano meters to form an iron particle mix;
(ii) uniformly dispersing the said iron particle mix upto a maximum of 25% in a resin carrier to form a master batch; and
(iii) storing the said master batch in an inert atmosphere until required for adding in a polyester resin for imparting oxygen scavenging property.
Typically, the step of dispersing the said iron particle mix in the resin carrier is performed by adding the iron particle mix to the resin carrier in a extruder after thoroughly mixing the said iron particle mix , maintaining the extruder at a temperature
13

between 260 degrees Celsius and 285 degrees Celsius, extruding the strand of iron mix dispersed carrier resin, cooling the strand and cutting strand into master batch chips.
In accordance with yet another aspect of this invention there is provided a method of imparting oxygen scavenging properties to a polyester resin comprising the steps of
(i) preparing a master batch containing an oxygen scavenging composition comprising a resin carrier; and iron particles mixture dispersed in the said resin carrier said iron particle mixture consisting of
[a] micron sized iron particles having particle size in the range of 1 to 50 microns;
[b] nano sized iron particles having particle size in the range of 5 to 50 nano meters
(ii) adding the said master batch to dry polyester resin prior to extrusion/injection molding/stretch blow molding the polyester resin such that the final quantity of the iron particle mix in the polyester resin is in the region of 2500 ppm to 3500 ppm.
Therefore the present invention discloses an iron-based active oxygen scavenging composition comprising a mixture of iron particles of 1 to 50 micron and preferably a mixture of 1 to 10 micron and 15 to 30 micron along with nano sized iron particles of 5 to 50 nanometers (nm).
Accordingly, the present invention provides an Oxygen scavenging composition which acts both as an active and passive barrier, said composition comprising a resin carrier, mixed micron size and nano-sized iron particles, and optionally at least one alkali bisulphate, and/or a metal halide, and/or ascorbic acid or a metal ascorbate and other desired additives.
Typically, the metal ascorbate is at least one ascorbate selected from a group consisting of sodium ascorbate, potassium ascorbate, sodium ascorbate, magnesium ascorbate, calcium ascorbate, zinc ascorbate, chromium ascorbate,
The resin carrier is selected preferably from an alloy blend of Polyethylene terephthalate (PET) with Polytrimethylene Naphthalate (PTN), Polybutylene Naphthalate(PBN),
14

Polybutyiene Terephthalate (PBT), Isophthalic acid modified PET like PETI or their copolyesters and their alloy blends preferably PET with PTN or PET with PBN due to their excellent passive barrier properties.
The iron particle mixture with a particle size in the range of 1 to 50 micron and preferably a mixture of 1 to 10 micron and 15 to 30 micron along with nano sized iron particles of 5 to 50 nanometers (nm) surprisingly have a synergistically an additional enhanced rate of oxygen absorption. The oxygen scavenging composition for additional benefit also includes metal halide, ascorbates and bisulfates of alkali metals.
In an embodiment of the present invention, the oxygen scavenging composition comprises a carrier in the form of a polyester resin selected from an alloy of PET with PTN or PBN or their copolyesters and their blends but preferably PET with PTN or PET with PBN at a maximum of 75:25 % composition.
In another preferred embodiment of the present invention, the percentage of oxygen scavenger that is incorporated in said composition is up to a maximum of 25 %.
In yet another embodiment of the present invention, an electrolyte in the form of a metal halide to facilitate the oxidation of iron particles and bisulfates of alkali metals is incorporated in said composition.
In order to accelerate the oxidation reaction, an acidic component is incorporated in said oxygen scavenging composition in the form of bisulfate of alkali metals and ascorbates of alkali metals. Bisulfates and ascorbates being acidic in nature, they accelerate the iron oxidation reaction by promoting the formation of hydronium ions (H3O+). This hydronium ion helps in abstracting the electrons from iron and facilitates the formation of Fe2+, which is a prerequisite for its reaction with oxygen and act as the oxygen scavenger. The oxidation reaction is provided in the following sequence.

15

Advantageously, the iron particles used in the present invention are pre-treated with C3 to C8 alcohols preferably selected from Propanol, Butanol and the like, under refluxing conditions. These alcohols are effective reductants under dehydrogenation conditions and cause the renewal of the surface of iron particles i.e. they increase the exposure of the number of iron atoms per surface area which helps to increase the oxidation efficiency of iron.
Still advantageously, the oxygen scavenging composition of the present invention is compounded with carrier resins containing appropriate quantities of barrier additives, green, blue and amber color compositions, ultraviolet light absorbers and the like.
In an embodiment of the present invention, the said composition has an enhanced oxygen absorbing capacity of well over 0.4ml/gm.
In another embodiment of the present invention the oxygen scavenging composition comprising polyester resin is achieved by making use of melt mixing equipments like twin screw extruders.
In yet another embodiment of the present invention, the pelletized master batch of the oxygen scavenging composition is dried and stored under an inert atmosphere such as nitrogen for further use.
The oxygen scavenging composition of the present invention gets triggered by the presence of moisture / water.
Appropriate quantities of the oxygen scavenging composition in accordance with this invention can be incorporated in a dried polyester resin preferably selected from a group consisting of an alloy of PET with PTN or PBN or PBT or their copolyesters and blends preferably PET with PBN or PBT and more preferably with PTN prior to extrusion/injection molding/stretch blow molding. The quantities should be such that the final quantity of the iron particle mix in the polyester resin should be in the region of 2500 ppm to 3500 ppm.
16

PTN's excellent passive barrier property compared to the other polymers towards gases are well known.
Table - I gives the comparison of the oxygen permeability of the different polyesters. As a carrier for the oxygen scavenger in the present invention PTN is preferred for the master batch because of its superior barrier property towards oxygen and the presence of PTN will augment the function of the iron particle mixture of the present invention.
TABLE - I Comparison of the Barrier Property of different Polyesters towards
Oxygen
Values are for biaxially oriented films and expressed as cc-mil/100in2/24hrs.atm

Polyester Type O2 Permeability % Improvement Times better than
in O2 barrier over (i.e. lower
PET permeability) PET for02
PET 4.2 - -
PTT 3.1 35 1.35
PEN 2.33 80 1.80
PTN 0.525 700 8.00
The present invention, the active oxygen scavenger developed and described in die present invention has increased oxygen absorption rate and is effective in its application at lesser loadings thereby improving the characteristics of the packaging eg. botde.
Since the oxygen scavenging composition in accordance with tiiis invention is activated by contact with water or water vapor, mono layered single walled barrier bottles or containers made of polyester resin impregnated with the oxygen scavenging composition can be useful for packing highly oxygen sensitive food items such as alcoholic beverages, fruit juices and health beverages which require total absence of
oxygen for the duration of intended shelf life.
17

A particular feature of the invention is that since part of the iron composition is nano sized and similar in size to the wavelength of light they do not affect the clarity of the container. Also the presence of nano sized iron particles in the master batch developed and described herein surprisingly also acts as a passive barrier in addition to its main active barrier function.
The invention is further explained in the form of following examples. However, this examples should not in any way be considered as limiting the scope of the invention, since, this examples are of exemplary in nature.
Example 1
20 g of iron powder consisting of a mixture of particle sizes of ~6 micron, -24 micron and 10 nm in the ratio of 10:70:20 were refluxed with the n-butanol for 12 hours. 200 mg of sodium bisulfate, 80 mg of sodium
chloride were added along with 6 ml of water and further refluxed for 3 hours. Following this the alcohol was distilled off and the mixed iron powder impregnated with the bisulfate and the metal halide was dried at 75°C and the resulting dry powder was stored under nitrogen. This dry oxygen scavenger was found to be capable of absorbing oxygen in the presence of moisture.
The iron particle mix component of the oxygen scavenging composition was incorporated in carrier resin preforms and bottles made therefrom were tested for oxygen absorption by the gas chromatographic method.
The efficiency data of the Oxygen Scavenging component of the present invention in relation to known compositions was tabulated in the following Table - II, which was evaluated by a specially designed manometric method to provide a qualitative figure of oxygen absorption by Oxygen Scavenger also by a gas chromatographic procedure to obtain quantitative values in comparison with the theoretical values.
18

TABLE - II Oxygen Absorbing Efficiency

mm Hg RISE IN %02 OXYGEN
S.NO SAMPLE MANOMETER ABSORBED(GC) ABSORBEDml/gOFSAMPLE REMARKS
Oxygen 122-147 11-60 40-42 Accelerated
1 Scavenger test by heating
Powder (OS) to 60°C- does
of the present invention not represent the saturationvalue. In a live situation slow reactionis preferred.
Amosorb 60-65 - 0.29 Accelerated
2 Oxygen test
Scavenger
(OS) Powder
Oxygen 50 to 55 10 to 15 0.91 Accelerated
3 Scavenging test
composition
of the present invention as a master batch
Oxygen 11-16 70-92 0.18-0.83 Values are for
4 Scavenger OS levels of
composition 1000 to 3500
of the presentinvention inperforms ppm in preforms.
Preforms with 2 to 5 - 0.36 3000 ppm in
5 Amosorboxygenscavenger performs
6 OScompositionof the presentinvention inBottles 43 to 80 0.32 to 0.74 Values are for OS levels of 2500 to 3500ppm in bottles
Note:
(i) In U tube manometer the mm Hg rise is directly proportional to the quantity of Oxygen absorbed by the oxygen scavenger.
19

(ii) For gas chromatographic (GC) procedure, oxygen scavenger incorporated performs or bottles are powdered or cut into pieces and a known quantity is taken in a vial. To this a known quantity of water is added and heated to 60°C for 2 hours for acceleration of oxygen absorption. The head space air sample is analyzed by GC at definite time intervals.
(iii) The theoretical quantity of oxygen capable of being absorbed by the oxygen scavenger is based on the oxygen absorption value of 300 ml per gram of iron.
(iv) The ml/g value is another way of expressing the oxygen scavenging capacity which helps to compare with the published values for oxygen scavenger samples of the prior art.
The delayed action by the presence of the mixed micron sized iron particles as described in this invention is elaborated in the following Table - III. Example 1 was repeated with different compositions of the mixture of micron sized iron particles. Nano sized particles were not added so that the influence of the proportion of different sizes of micron particles can be clearly seen.
TABLE - III Comparison of the oxygen absorbing rate by different micron size iron particles.

Sr.No. Ratio of Oxygen absorption, cc/g
Micronsize,~6 micron :~24 micron of sample after 2 hours.
1. 100:0 9.52
2. 0:100 22.8
3. 20:80 17.75
4. 30:70 14.92
5. 40:60 11.86
It is seen from the table that the oxygen absorption rate distinctly differs with the micron size and that the rate is less for the finer micron size. This delayed action is
20

advantageous for the alcoholic beverage like beer in the container as the oxygen scavengers capacity will last throughout the period of storing the alcoholic beer and protect the beer from oxygen ingress.
The oxygen scavenger (OS) incorporated in the master batch with a carrier resin was blended with PET having different passive barrier additives and injection molded into preforms and subsequently stretch blow molded into bottles. The OS containing preforms and bottles were tested for their oxygen absorption capability by GC. Results are given in Table - IV.
TABLE - IV Oxygen Absorption by the OS in Preforms and Bottles by GC Method

Serial No. Preforms or Bottles Weight, g Volume, ml % Oxygen Absorption Ppm Oxygen Absorption
1 Preform Amber Colored ' 28 - 27-34 15-18
2 Bottle Amber Colored' 28 500 41-48 23-27
3 Bottle Amber Colored ' 20 250 51 24
4 Preform Amber Colored 2 28 - 42 24
5 Preform Colorless 2 28 - 40 31
6 Bottle Amber Colored 2 28 500 65 23
7 Bottle Colorless2 28 500 61 32
8 Preform Amber Colored 3 30/33 - 36/38 20/21
9 Bottle Amber Colored 3 30 500 44 25
10 Preform Amber Colored4 30 - 32 18
11 Bottle Amber Colored 4 30 500 45 25
Resin Recipe:
1. Oxygen Scavenger at 2400 ppm (24:6 micron of 2000:400) in a PET carrier resin consisting of 0.63% naphthalate additive
21

2. Oxygen Scavenger at 2200 ppm (24:6 micron of 2000:200) in a PET carrier resin containing 5 % PTN
3. Oxygen Scavenger at 3400 ppm in a PET carrier resin containing 8 % PTN and 1000 ppm nano silica as an additional passive barrier additive
4. Oxygen Scavenger at 3400 ppm in a PET carrier resin containing 8 % PTN and 500 ppm each of nano silica and nano clay as additional passive barrier additives.
It follows from the table that the oxygen absorption by the OS in the bottles are generally about 40 - 65 % of the theoretical absorption which is understandable as the oxygen absorbing iron is dispersed in the polymer matrix and may not be easily available for combination with oxygen especially in the short period of testing time.
Example 2:
Example 1 was repeated except that the ratio of iron particles was changed to 70:10:20
of 6 micron, 24 micron and 10 nm
Example 3:
Example 1 was repeated by changing the ratio of iron particles to 10:20:70 of 6 micron,
24 micron and l0 nm
Example 4:
Example 1 was repeated by replacing NaCl with KC1
Example 5:
Example 1 was repeated by replacing KHSO4 with NaHS04
Example 6:
Example 1 was repeated by replacing both NaCl & KHSO4 with KC1 and NaHS04
Example 7:
Example 1 was repeated wherein in addition to the metal halides 20 mg of sodium
ascorbate was also added.
22

In Examples 1 to 7 the carrier resin for making the MB was PET-PTN alloy. The Oxygen Scavenging capacities in these experiments followed the order Example 7>1>5>4>2>3>6.
Similar experiments i.e. 1 to 7 were carried out with PET-PBN alloy instead of the PET-PTN alloy. Though the trend of Oxygen Scavenging capacities were same in these experiments the Oxygen Scavenging efficiency was observed to be ~ 10% less than that observed with PET-PTN alloy as the carrier.
Experiments were also conducted to judge the performance of the Oxygen Scavenging composition with different % compositions of PTN as well as in different size of bottles. The oxygen absorption results obtained by Gas Chromatography are given in Table-V.
TABLE - V Oxygen Scavenger's function with variation in % PTN and Bottle
Size

Serial No. Preforms / Bottles Weight, g Volume, ml % Oxygen Absorption PpmOxygenAbsorption
1 Preform ' 28 - 29.76 16.67
2 Bottle ' 28 500 37.50 21.00
3 Preform2 28 - 27.33 15.30
4 Bottle l 28 500 34.43 19.28
5 Preform J 24 - 34.10 19.10
6 Bottle i 24 330 43.84 24.55
7 PreformJ 28 - 35.95 20.13
8 BottleJ 28 500 44.18 24.74
9 Preform 33 - 38.2 21.39
10 Bottle i 33 650 44.6 24.98
Resin Recipe:
1 25 % PTN in PET-PTN carrier resin Fe OS particles at 2500 ppm
2 15 % PTN in PET-PTN carrier resin Fe OS particles at 2500 ppm
3 8 % PTN in PET-PTN carrier resin Fe OS particles at 3400 ppm
23

As can be seen from the Table above the various preforms and bottles which contain the oxygen scavenger show sufficient oxygen absorption which is satisfactory taking into consideration the presence of the oxygen scavenger iron particles mixture well dispersed in the polymer matrix.
Several advantages arise as a result of the oxygen scavenging composition of the present invention.
1. The composition increases the oxygen absorbing rates due to the presence of nano sized iron particles which are so small and their aspect ratio is so high that properties improve with lower loadings of the oxygen scavenger as compared to the use of only micron sized particles.
2. The oxygen scavenging composition of the present invention enhances the barrier properties of the polyester resin by slowing down the permeation of gas molecules through the resin matrix.
3. The oxygen scavenging composition of the present invention is of low cost and has an improved efficiency.
4. The oxygen scavenging composition of the present invention is used to provide active as well as passive oxygen barred packaging containers that can increase the shelf-life of oxygen-sensitive human consumption products by absorbing oxygen present inside the head-space of the container as well as from the container wall in addition to absorbing oxygen permeating from the outside.

5. In the present composition, the limitations in the form of coloration, bottle blowing difficulty, loss of strength in the bottles and decreased barrier performance in the bottles are overcome by adopting the oxygen scavenging composition having a combination of nano and micron sized metal particles.
6. In the present composition, the presence of mixed micron size particles of iron in addition to the nano sized particles, helps in a delayed action of the oxygen scavenger to take care of the oxygen ingress during prolonged storage.
7. The polyester carriers like an alloy of PET with PTN, PBN and PBT used in making the master batch containing the oxygen scavenger also play a role by their passive barrier effect in oxygen ingress. The preferred carrier resin is a PET-PTN alloy blend due to its excellent barrier property.
24

8. The Fe based OS particles in the PET-PTN carrier resin is stable and in the bottle gets triggered by moisture / water thus giving a reasonable shelf life for the resin and bottle.
While considerable emphasis has been placed herein on the interrelationships between the component parts of the preferred embodiments of the oxygen scavenging composition disclosed hereinabove and to polyester resin made having the said composition incorporated therein, it will be appreciated that many embodiments can be made and that many changes can be made in the preferred embodiments without departing from the principles laid down in the invention. These and other changes in the preferred embodiment as well as other embodiments of the invention will be apparent to those skilled in the art from the disclosure herein, whereby it is to be distinctly understood that the foregoing descriptive matter is to be interpreted merely as illustrative of the invention and not as a limitation.
25

We Claim:
[1] An oxygen scavenging composition for polyester resins comprising
a resin carrier; and
iron particles mixture dispersed in the said resin carrier
said iron particle mixture consisting of
[i] micron sized iron particles having particle size in the range of 1 to 50 microns;
[ii] nano sized iron particles having particle size in the range of 5 to 50 nano meters.
[2] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the micron sized iron particles are in the range of 1 to 10 microns.
[3] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the micron sized iron particles are in the range of 15 to 30 microns.
[4] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the micron sized are a mixture of iron particles in the range of 1 to 10 microns and 15 to 30 microns.
[5] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the micron sized are a mixture of iron particles in the range of 1 to 10 microns and 15 to 30 microns and the ratio of the quantity of iron particles in the range of 1 to 10 microns to the ratio of the particles in the range of 15 to 30 microns lies between 1: 0.10 and 1:0.80.
[6] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the ratio of the mass of the micron sized iron particles to the mass of the nano sized iron particles is in the range of 1: 0.10 to 1:0.20.
[7] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the ratio of the mass of carrier resin to the mass of said mixture of iron particles is in the range of 1: 0.01 to 1: 0.08.
26

[8] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the carrier resin is a polyester resin having a maximum melting point temperature in the range of 228 to 230° C.
[9] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the carrier resin is an alloy of PET with PTN, its co polyesters or its blends.
[10] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the carrier resin is a an alloy of PET with PBN, its co polyesters or its blends.
[11] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the carrier resin is PET with PBN or PTN in a ratio of a maximum of 75:25 % .
[12] An oxygen scavenging composition for polyester resins as claimed in claim 1, in which the carrier resin is PTN.
[13] An oxygen scavenging composition for polyester resins comprising
a resin carrier;
iron particles mixture dispersed in the said carrier
said iron particle mixture consisting of
[i] micron sized iron particles having particle size in the range of 1 to 50 microns;
[ii] nano sized iron particles having particle size in the range of 5 to 50 nano meters; and an oxidation reaction accelerator.
[14] An oxygen scavenging composition for polyester resins as claimed in claim 14, in which the oxidation reaction accelerator is at least one alkali metal bisulfate. selected from a group of alkali metal bisulfates consisting of sodium bisulfate, calcium bisulfate, potassium bisulfate, magnesium bisulfate.
[15] An oxygen scavenging composition for polyester resins as claimed in claim 13, in
which the oxidation reaction accelerator is at least one compound selected from a group consisting of sodium bisulfate and potassium bisulfate.
27

[16] An oxygen scavenging composition for polyester resins as claimed 13, in which the oxidation reaction accelerator is a metal halide.
[17] An oxygen scavenging composition for polyester resins as claimed 13, in which the oxidation reaction accelerator is at least one metal halide selected from a group of metal halides consisting of Barium chloride, Calcium chloride, , Iron(II) chloride, Iron(III) chloride. Lithium chloride, Magnesium chloride, Magnesium fluoride, , Potassium bromide. Potassium chloride, Potassium iodide, , Sodium bromide, Sodium chloride. Sodium iodide. Strontium chloride, and Zinc chloride.
[18] An oxygen scavenging composition for polyester resins as claimed 13, in which the oxidation reaction accelerator is at least one metal halide selected from a group consisting of sodium chloride and potassium chloride.
[19] An oxygen scavenging composition for polyester resins as claimed 13, in which the oxidation reaction accelerator is a mixture of at least one alkali metal bisulfate, at least one metal halide.
[20] An oxygen scavenging composition for polyester resins as claimed 13, in which the oxidation reaction accelerator is ascorbic acid.
[21] An oxygen scavenging composition for polyester resins as claimed 13. in which the oxidation reaction accelerator is at least one metal ascorbate.
[22] An oxygen scavenging composition for polyester resins as claimed 13, in which the oxidation reaction accelerator is at least one metal ascorbate selected from a group consisting of sodium ascorbate. potassium ascorbate. sodium ascorbate, magnesium ascorbate, calcium ascorbate, zinc ascorbate, chromium ascorbate,
[23] An oxygen scavenging composition for polyester resins as claimed 13, in which the oxidation reaction accelerator is a mixture of at least one alkali metal bisulfate, and at least one metal ascorbate.
28

[24] An oxygen scavenging composition for polyester resins as claimed 13, in which the oxidation reaction accelerator is a mixture of at least one alkali metal halide and at least one metal ascorbate.
[25] An oxygen scavenging composition for polyester resins as claimed 13, in which the oxidation reaction accelerator is a mixture of at least one alkali metal bisulfate, at least one metal halide and at least one metal ascorbate.
[26] An oxygen scavenging composition for polyester resins as claimed 13, in which the ratio of the mass of the carrier resin to the mass of the oxidation reaction accelerator is in the range of 1: 0.001 to 1: 0.01.
[27] An oxygen scavenging composition for polyester resins as claimed 1, in which the iron particles are pre-treated with C3 to C8 alcohols selected from a group consisting of n-propanol, n-butanol, pentanol, hexanol, septanol and octanol, Isopropyl alcohol, Isobutyl alcohol, Sec- butyl alcohol , Tertiary butyl alcohol, Isopentyl alcohol , Tertiary pentyl alcohol, Neopentyl alcohol, Cyclopentyl alcohol, Cyclohexyl alcohol and Allyl alcohols.
[28] An oxygen scavenging composition for polyester resins as claimed 1, in which the iron particles are pre-treated with C3 to C8 alcohols under refluxing conditions.
[29] An oxygen scavenging composition for polyester resins comprising
a resin carrier;
iron particles mixture dispersed in the said carrier
said iron particle mixture consisting of
[i] micron sized iron particles having particle size in the range of 1 to 50 microns;
[ii] nano sized iron particles having particle size in the range of 5 to 50 nano meters; an oxidation reaction accelerator; and barrier additives.
[30] An oxygen scavenging composition for polyester resins comprising
a resin carrier;
iron particles mixture dispersed in the said carrier
29

said iron particle mixture consisting of
[i] micron sized iron particles having particle size in the range of 1 to 50 microns;
[ii] nano sized iron particles having particle size in the range of 5 to 50 nano meters; an oxidation reaction accelerator; barrier additives; color imparting additives, and ultraviolet light absorbers.
[31] An oxygen scavenging composition for polyester resins as claimed in claim 30, in which the barrier additive is at least one barrier additive selected from a group containing sub micronic size particles of clay and sub micronic sized particles of silica.
[32] A method of preparing an oxygen scavenging composition for polyester resins comprising the steps of
(i) preparing an intimate mixture of dried micron sized iron particles having particle size in the range of 1 to 50 microns and dried nano sized iron particles having particle size in the range of 5 to 50 nano meters to form an iron particle mix;
(ii) uniformly dispersing the said iron particle mix upto a maximum of 25% in a resin carrier to form a master batch ; and
(iii) storing the said master batch in an inert atmosphere until required for adding in a polyester resin for imparting oxygen scavenging property.
[33] A method of preparing an oxygen scavenging composition for polyester resins comprising the steps of
(i) preparing an intimate mixture of dried micron sized iron particles having particle size in the range of 1 to 50 microns and dried nano sized iron particles having particle size in the range of 5 to 50 nano meters to form an iron particle mix adding at least one oxidation reaction accelerator to the iron particle mix to form a dry homogenous mixture;
(ii) uniformly dispersing the said homogenous mixture upto a maximum of 25% in a resin carrier to form a master batch :
(iii) storing the said master batch in an inert atmosphere until required for adding in a polyester resin for imparting oxygen scavenging property.
30

[34] A method of preparing an oxygen scavenging composition for polyester resins as claimed in clam 33. wherein the homogenous mixture is refluxed with at least one alcohol from the C3 to C8 group of alcohols and the resultant mixture is dried at upto 75 degrees Celsius.
[35] A method of preparing an oxygen scavenging composition for polyester resins as claimed in claim 33, in which the step of dispersing the said iron particle mix in the resin carrier is performed by adding the iron particle mix to the resin carrier in an extruder after thoroughly mixing the said iron particle mix , maintaining the extruder at a temperature between 260 degrees Celsius and 285 degrees Celsius, extruding the strand of iron mix dispersed carrier resin, cooling the strand and cutting strand into master batch chips.
[36] A method of imparting oxygen scavenging properties to a polyester resin comprising the steps of
(i) preparing a master batch containing an oxygen scavenging composition comprising a resin carrier; and
iron particles mixture dispersed in the said resin carrier said iron particle mixture consisting of
[a] micron sized iron particles having particle size in the range of 1 to 50 microns;
[b] nano sized iron particles having particle size in the range of 5 to 50 nano meters
(ii) adding the said master batch to dry polyester resin prior to extrusion/injection molding/stretch blow molding the polyester resin such that the final quantity of the iron particle mix in the polyester resin is in the region of 2500 ppm to 3500 ppm.
[37] A method of imparting oxygen scavenging properties to a polyester resin as claimed in claim 36, in which the melting point of the carrier resin is at most between 228 degrees Celsius and 230 degrees Celsius and the melting point of the polyester resin lies between 246 degrees Celsius and 250 degrees Celsius.
[38] A polyester resin having incorporated therein an oxygen scavenging composition as claimed in claim 1.
31

[39] A polyester resin having incorporated therein an oxygen scavenging composition as claimed in claim 13.
[40] A polyester resin having incorporated therein an oxygen scavenging composition as claimed in claim 29.
[ 41] A container defined by at least one wall, wherein the wall comprises a polyester resin having an oxygen scavenging composition as claimed in claim 1.
[42] A container defined by at least one wall, wherein the wall comprises a polyester resin having an oxygen scavenging composition as claimed in claim 13.
[43] A container defined by at least one wall, wherein the wall comprises a polyester resin having an oxygen scavenging composition as claimed in claim 44.

32

Abstract
The present invention provides an Oxygen scavenging composition as a concentrate master batch to act as active and passive barrier, said composition comprising a resin carrier which is an alloy of PET with PTN, or PBN or PBT, mixed micron sized and nano-sized iron particles, an alkali metal bisulphate and ascorbate , a metal halide and additives. The iron particle mixture with a particle size in the range of 1 to 50 micron along with nano sized iron particles of 5 to 50 nanometers (nm) having an additional enhanced rate of oxygen absorption. The oxygen scavenging composition also includes metal halide and ascorbates and bisulphates of alkali metals. The oxygen scavenging composition of the present invention as a master batch in a polyester carrier resin containing barrier, color and U.V. light absorbing additives is used in food packaging applications of human consumption, especially those oxygen sensitive food items including alcoholic beverages, fruit beverages etc, where the oxygen permeation levels are to be maintained at very low levels.

Documents:

1196-MUM-2005-ABSTRACT(GRANTED)-(1-5-2009).pdf

1196-mum-2005-abstract.doc

1196-mum-2005-abstract.pdf

1196-MUM-2005-CANCELLED PAGES(3-1-2008).pdf

1196-MUM-2005-CLAIMS(GRANTED)-(1-5-2009).pdf

1196-mum-2005-claims.doc

1196-mum-2005-claims.pdf

1196-mum-2005-correspondance-received.pdf

1196-MUM-2005-CORRESPONDENCE(3-1-2008).pdf

1196-MUM-2005-CORRESPONDENCE(IPO)-(18-5-2009).pdf

1196-mum-2005-description (complete).pdf

1196-MUM-2005-DESCRIPTION(GRANTED)-(1-5-2009).pdf

1196-MUM-2005-FORM 18(2-7-2007).pdf

1196-MUM-2005-FORM 2(GRANTED)-(1-5-2009).pdf

1196-MUM-2005-FORM 2(TITLE PAGE)-(26-9-205).pdf

1196-MUM-2005-FORM 2(TITLE PAGE)-(GRANTED)-(1-5-2009).pdf

1196-MUM-2005-FORM 3(3-1-2008).pdf

1196-mum-2005-form-1.pdf

1196-mum-2005-form-2.doc

1196-mum-2005-form-2.pdf

1196-mum-2005-form-26.pdf

1196-mum-2005-form-3.pdf

1196-MUM-2005-SPECIFICATION(AMENDED)-(3-1-2008).pdf

« Previous Patent

Next Patent »

Patent Number

234047

Indian Patent Application Number

1196/MUM/2005

PG Journal Number

25/2009

Publication Date

19-Jun-2009

Grant Date

01-May-2009

Date of Filing

26-Sep-2005

Name of Patentee

FUTURA POLYESTERS LIMITED

Applicant Address

Paragon Condominium, 3rd Floor, Pandurang Budhkar Marg, Mumbai 400 013,

Inventors:

#	Inventor's Name	Inventor's Address
1	KULKARNI SANJAY TAMMAJI	No.1, Kamarajar Salai, Manali, Chennai 600 068, Tamil Nadu,
2	BISHT HARISH	No.1, Kamarajar Salai, Manali, Chennai 600 068, Tamil Nadu,

PCT International Classification Number

C08K3/28

PCT International Application Number

N/A

PCT International Filing date

PCT Conventions:

#	PCT Application Number	Date of Convention	Priority Country
1	985/CHE/2004	2004-09-27	India