Patent Grant
7601374
This invention relates to the packaging of respiring biological materials.
Respiring biological materials, e.g. fruits and vegetables, consume oxygen (O2) and produce carbon dioxide (CO2) at rates which depend upon the stage of their development, the atmosphere surrounding them and the temperature. In modified atmosphere packaging (MAP), the objective is to produce a desired atmosphere around respiring materials by placing them in a sealed container whose permeability to O2 and CO2 is correlated with (i) the partial pressures of O2 and CO2 in the air outside the package, and (ii) the temperature, to produce a desired atmosphere within the container. In many cases, the container includes an atmosphere control member having a high permeability to O2 and CO2. In controlled atmosphere packaging (CAP), the objective is to produce a desired atmosphere around respiring materials by displacing some or all of the air within a container by one or more gases, e.g. nitrogen, O2, CO2 and ethylene, in desired proportions. Reference may be made, for example, to U.S. Pat. No. 3,360,380 (Bedrosian), U.S. Pat. No. 3,450,542 (Badran), U.S. Pat. No. 3,450,544 (Badran et al.), U.S. Pat. No. 3,798,333 (Cummin et al), U.S. Pat. No. 3,924,010 (Erb), U.S. Pat. No. 4,003,728 (Rath), U.S. Pat. No. 4,734,324 (Hill), U.S. Pat. No. 4,779,524 (Wade), U.S. Pat. No. 4,830,863 (Jones), U.S. Pat. No. 4,842,875 (Anderson), U.S. Pat. No. 4,879,078 (Antoon), U.S. Pat. No. 4,910,032 (Antoon), U.S. Pat. No. 4,923,703 (Antoon), U.S. Pat. No. 4,987,745 (Harris), U.S. Pat. No. 5,041,290 (Wallace et al.) U.S. Pat. No. 5,045,331 (Antoon), U.S. Pat. No. 5,063,753 (Woodruff), U.S. Pat. No. 5,160,768 (Antoon), U.S. Pat. No. 5,254,354 (Stewart), U.S. Pat. No. 5,333,394 (Herdeman), U.S. Pat. No. 5,433,335 (Raudalus et al.), U.S. Pat. No. 5,460,841 (Herdeman), U.S. Pat. No. 5,556,658 (Raudalus et al.), U.S. Pat. No. 5,658,607 (Herdeman) and U.S. Pat. No. 6,013,293 (De Moor), copending commonly assigned U.S. patent application Ser. No. 08/759,602 (Clarke et al.) and Ser. No. 09/121,082 (Clarke et al.), International Publication Nos. WO 94/12040 (Fresh Western), WO 96/38495 (Landec) and WO 00/04787 (Landec), and European Patent Applications Nos. 0,351,115 and 0,351,116 (Courtaulds). The disclosure of each of these patents, applications and publications is incorporated herein by reference.
The preferred packaging atmosphere for a respiring material often depends on the age of the material and the changes (if any) in the material which are desired. For example, the preferred O2 content during storage of unripe fruits is substantially lower than the preferred O2 content during subsequent ripening at a higher temperature. This fact causes problems for both MAP and CAP. For example, in MAP, although the O2permeability of the container generally increases with temperature (especially if it contains an atmosphere control member comprising a crystalline polymer having an appropriate melting point, as disclosed in U.S. patent applications Ser. Nos. 08/759,602 and 09/121,082 and International Publication Nos. WO 96/38459 and WO 00/04787), the increase is often insufficient to avoid the need for significant compromise between the preferred atmospheres at different stages. In CAP, it is theoretically possible to monitor the packaging atmosphere and to change it as often as is necessary to maintain the preferred level of O2 (and other gases). But this is difficult and expensive, and often impractical.
Many fruits are picked when they are unripe; transported and stored under conditions which prevent or retard ripening; and ripen shortly before sale. Many fruits ripen more rapidly when exposed to ethylene, and some (e.g. bananas, tomatoes, avocados, Bartlett pears, kiwis, melons, peppers and mangos) are ripened commercially by exposure to ethylene in ripening rooms. When the fruits have been placed in a sealed bag or other container for transport or storage, the container is opened to expose the fruits to the ethylene. Another problem associated with the use of ripening rooms is that the fruits can ripen too rapidly, especially when the fruits ripen through a climacteric and therefore undergo a very large increase in respiration rate and generate heat in the ripening room.
The transport, storage and ripening of bananas present particularly serious problems because
This conventional procedure suffers from a number of problems, for example:
A first area of the present invention is based on my realization that for bananas and other fruits which ripen when exposed to ethylene, one or more of the problems noted above can be mitigated or overcome by ripening fruits within a sealed container which provides a pathway for O2, CO2 and ethylene to enter or leave the container. The fruits can be ripened by exposing them to ethylene which (i) enters the container from an ethylene-containing atmosphere adjacent to the sealed container and/or (ii) is generated within the sealed container.
A second area of the present invention is concerned with situations in which the preferred packaging atmosphere has a zero or relatively low content of a particular gas during one stage and a relatively high content of that gas during another stage, in particular a relatively low O2 content during one stage and a relatively high O2 content during another stage. I have realized that in such situations, valuable results can be obtained by combining the techniques of MAP and CAP. For example, a container having a high O2 permeability can be placed either (i) in air when a packaging atmosphere of high O2 content is desired, or (ii) in a controlled atmosphere having a selected reduced O2 content when a packaging atmosphere of low O2 content is desired.
Some aspects of the present invention make use of both the first and second areas of the invention.
As noted above, some fruits generate ethylene as they ripen. Such ethylene is referred to herein as endogenous ethylene. The term “exogenous ethylene” is used herein to mean ethylene which is not derived from the fruits which are being ripened. Some other materials, for example acetylene, will also assist ripening of fruits which are ripened by exposure to ethylene. Reference may made for example to Burg et al, Molecular Requirements for the Biological Activity of Ethylene, Plant Physiology (Lancaster) (1967) 42: 144-155. The term “ethylenic ripening agent” is used herein to mean ethylene or another substance which also assists ripening of fruits which are ripened by exposure to ethylene. The abbreviation ERA is used herein for the term “ethylenic ripening agent”. The term “exogenous ERA” is used herein to mean ethylenic ripening agent which is not derived from the fruits which are being ripened.
The first area of the invention includes the following aspects.
The second area of the invention includes the following aspects.
This aspect of the invention is useful for the treatment of any respiring biological material, including but not limited to, fruits (e.g. fruits which have ripened through a climacteric, or unripe fruits which ripen through a climacteric) and vegetables.
In one embodiment of this aspect of the invention,
In another embodiment of this aspect of the invention,
In these two embodiments, it is preferred that, during at least one period of step (B), the O2 content of the packaging atmosphere reaches a value, which may be an equilibrium value, which is (i) more than 1%, preferably more than 2%, and (ii) less than 7%, preferably less than 5%, particularly less than 3.5%.
In another embodiment of this aspect of the invention, the first and second atmospheres differ in their content of some gas other than oxygen which will pass through the sealed container, for example CO2 or another gas having a desired effect on the respiring biological material, e.g. an insecticide, a fungicide or a mold-inhibiting compound. One of the atmospheres can contains 0% of the gas other than oxygen. In this embodiment, the O2 content of the first and second atmospheres can be the same or different. For example, this embodiment of the invention code be used to store the respiring material in the sealed package under preferred conditions during one of steps (B) and (C), and in the other step to use a controlled atmosphere to change the packaging atmosphere, for a relatively short time, to an atmosphere containing a desired amount of the gas other than oxygen, for example to contact the respiring material with an atmosphere containing a relatively high percentage of CO2, e.g. 15-30%, for a relatively limited period of time, e.g. for 5-48 or 15-30 hours. Such a method would be useful, for example, for the treatment of broccoli to control aphids.
The invention is particularly useful for the storage and/or ripening of bananas. Some embodiments of the invention make it possible to maintain bananas, before and/or after their climacteric, in a packaging atmosphere which enables storage and/or ripening of green bananas in a controlled fashion. Other embodiments of the invention make it possible to ripen bananas in a sealed container, for example in a conventional ripening room or in a closed container in which the bananas are being transported; and/or to harvest bananas at a later time than is now possible; and/or to store bananas, after their climacteric, within a desired range of color stages (e.g. within the range most attractive for retail sale) for a longer period than is possible under conventional practice.
Some embodiments of the invention which are particularly suitable for the ripening and/or storage of bananas have been described above. Other aspects of the invention which are particularly suitable for the ripening and/or storage of bananas include the following.
It is to be understood that this aspect of the invention includes containers which are as defined above but which are used for the packaging of fruits other than bananas. It is also to be understood that the containers defined above can be used to ripen fruits by exposing them to any exogenous ERA. When ripening fruits by exposing them to an exogenous ERA other than ethylene, the containers preferably have a permeability at 13° C. to that ERA per kg of bananas which is at least two times, preferably at least 3 times, particularly at least 4 times, the OP13/kg of the container.
In the Summary of the Invention above and in the Detailed Description of the Invention, the Examples, and the claims below, reference is made to particular features (including method steps) of the invention. It is to be understood that the disclosure of the invention in this specification includes all appropriate combinations of such particular features. For example, where a particular feature is disclosed in the context of a particular aspect or embodiment of the invention, or a particular claim, that feature can also be used, to the extent appropriate, in combination with and/or in the context of other particular aspects and embodiments of the invention, and in the invention generally.
In describing and claiming the invention below, the following abbreviations, definitions, and methods of measurement (in addition to those already given) are used.
OTR is O2 permeability. COTR is CO2 permeability. EtTR is ethylene transmission rate. OTR, COTR and EtTR values are given in ml/m2.atm.24 hrs; in some cases, the equivalent in cc/100 inch2.atm.24 hrs is given in parentheses. OTR and COTR values referred to herein can be measured using a permeability cell (supplied by Millipore) in which a mixture of O2, CO2 and helium is applied to the sample, using a pressure of 0.7 kg/cm2 (10 psi) except where otherwise noted, and the gases passing through the sample were analyzed for O2 and CO2 by a gas chromatograph. The cell could be placed in a water bath to control the temperature. The abbreviation P10 is used to mean the ratio of the oxygen permeability at a first temperature T1° C. to the oxygen permeability at a second temperature T2, where T2 is (T1-10)° C. T1 being 10° C. and T2 being 0° C. unless otherwise noted. The abbreviation R or R ratio is used to mean the ratio of CO2 permeability to O2 permeability, both permeabilities being measured at 20° C. unless otherwise noted. Pore sizes given in this specification are measured by mercury porosimetry or an equivalent procedure. Parts and percentages are by weight, except for percentages of gases, which are by volume; temperatures are in degrees Centigrade, and molecular weights are weight average molecular weights expressed in Daltons. For crystalline polymers, the abbreviation To is used to mean the onset of melting, the abbreviation Tp is used to mean the crystalline melting point, and the abbreviation ΔH is used to mean the heat of fusion. To, Tp and ΔH are measured by means of a differential scanning calorimeter (DSC) at a rate of 10° C./minute and on the second heating cycle. To and Tp are measured in the conventional way well known to those skilled in the art. Thus Tp is the temperature at the peak of the DSC curve, and To is the temperature at the intersection of the baseline of the DSC peak and the onset line, the onset line being defined as the tangent to the steepest part of the DSC curve below Tp.
The term “comprises” (and grammatical variations thereof) in relation to methods, materials, things etc. (for example packages, containers, and gas-permeable membranes) are used herein to mean that the methods, materials, things etc. can optionally include, in addition to the steps, features, components, etc., explicitly specified after the term “comprises” (and grammatical variations thereof), other steps, features, ingredients, etc. Where reference is made herein to a method comprising two or more steps, the steps can be carried out in any order, or simultaneously, except where the context excludes that possibility. The term “controlled atmosphere” is used herein to mean an atmosphere produced by adding further gases to an existing atmosphere (including the addition of additional quantities of a gas already present in the existing atmosphere), the further gases being added directly to the atmosphere (i.e. not passing through a permeable body before reaching the atmosphere). The term “closed container” is used herein to mean a large container, for example a conventional shipping or trucking container which can be loaded onto a ship or a truck, and which is sealed sufficiently to permit a controlled atmosphere to be maintained therein by conventional means well known to those skilled in the art. The term “shipping or trucking container” is used herein to mean a container which has a volume of at least 8 m3 and which can be loaded onto a ship or a truck. Such containers are well known to those skilled in the art of storing and transporting fruits, vegetables and other respiring materials, and are available in a range of standard sizes. The term “source of exogenous ERA” is used herein to mean a material, object or system which, either immediately or when activated, generates ERA. The term “latent source of exogenous ERA” is used herein to mean a material, object or system which is generating little or no ERA, but which can be activated so that it generates substantial quantities of exogenous ERA. The term “residue of a source of exogenous ERA” is used herein to mean a material, object or system which is not a part of a fruit and which remains after exogenous ERA has been generated from a source of exogenous ERA. The residue may be for example (i) a solid material which served as a support for exogenous ERA itself or for one or more precursors of exogenous ERA, or (ii) a liquid residue remaining after a solution of a precursor for an ERA, e.g. 2-chloroethyl phosphonic acid, has been used to generate exogenous ethylene and/or a solid residue resulting from the evaporation of solvent from such a solution. The term “residue of exogenous ERA” is used herein to denote a chemical compound which results from the reaction of exogenous ERA with the fruit being ripened (in which case it is optionally part of the ripe fruit) or with another substance within the sealed package. The term “ripening” is used herein to mean increasing ripeness; it includes, but is not limited to and generally does not mean, ripening to a point which results in a product which in a retail store would be sold as “ripe”. When applied to fruits which ripen through a climacteric, the term “ripening” means ripening the fruits at least through the climacteric. The term “unripe fruits” is used herein to mean fruits which require ripening before they can be sold in retail stores. When applied to fruits which ripen through a climacteric, the term “unripe fruits” means fruits which have not reached their climacteric. The term “banana” is used herein to include plantains.
Where reference is made herein to sealed packages and sealed containers, and to sealing bags and other containers containing biological materials, it is to be understood that the sealing can be, but generally is not, hermetic sealing. Conventional methods for sealing bags and other containers can conveniently be used in this invention. Such conventional methods include, for example, the use of a cable tie to seal the neck of a polymeric bag. A seal made by conventional methods is not a hermetic seal, and has the advantage that it permits equilibration of the pressures inside and outside the bag. If the bag is sealed hermetically, it will generally be desirable to include one or more pinholes in the bag, to achieve such equilibration. The less complete the sealing of the container, the less the influence of the permeability of the container on the packaging atmosphere within it. Thus, even a poor seal may be sufficient, or even desirable, for example when the desired O2 content of the packaging atmosphere lies between the O2 content of the atmosphere surrounding the package and the O2 content of the packaging atmosphere that would result if the seal was a hermetic seal. Under such circumstances, the sealing could be designed to permit a controlled amount of direct exchange between the packaging atmosphere and the atmosphere surrounding the container.
Control Members
The containers used in the present invention preferably, but not necessarily, include at least one atmosphere control member which provides a pathway for O2 and CO2, and which preferably comprises a gas-permeable membrane comprising (1) a microporous polymeric film, and (2) a polymeric coating on the microporous film. The atmosphere control member is preferably a control member as described in one or more of copending, commonly assigned U.S. patent application Ser. Nos. 08/759,602 and 09/121,082 and U.S. Pat. No. 6,013,293 incorporated by reference herein. The atmosphere control member or members generally provide at least 50%, preferably at least 75%, of the O2 permeability of the sealed container.
The microporous polymeric film preferably comprises a network of interconnected pores having an average pore size of less than 0.24 micron, with at least 70% of the pores having a pore size of less than 0.24 micron. Preferably the pores in the microporous film constitute 35 to 80% by volume of the microporous film. Preferred microporous films comprise a polymeric matrix comprising (i) an essentially linear ultrahigh molecular weight polyethylene having an intrinsic viscosity of at least 18 deciliters/g, or (ii) an essentially linear ultrahigh molecular weight polypropylene having an intrinsic viscosity of at least 6 deciliters/g, or (iii) a mixture of (i) and (ii). The microporous film may contain 30 to 90% by weight, based on the weight of the film, of a finely divided particulate substantially insoluble filler which is distributed throughout the film. A preferred process for preparing suitable microporous films comprises
The polymeric coating on the control member preferably comprises a is crystalline polymer having a peak melting temperature Tp of −5 to 40° C., e.g. 0 to 15° C. or 10 to 20° C., an onset of melting temperature To such that (Tp-To) is less than 10° C., and a heat of fusion of at least 5 J/g. The polymer preferably comprises a side chain crystalline polymer moiety comprising, and optionally consisting of, units derived from (i) at least one n-alkyl acrylate or methacrylate (or equivalent monomer, for example an amide) in which the n-alkyl group contains at least 12 carbon atoms, for example in amount 35-100%, preferably 50-100%, often 80-100%, and optionally (ii) one or more comonomers selected from acrylic acid, methacrylic acid, and esters of acrylic or methacrylic acid in which the esterifying group contains less than 10 carbon atoms. The preferred number of carbon atoms in the alkyl group of the units derived from (i) depends upon the desired melting point of the polymer. For the packaging of biological materials, it is often preferred to use a polymer having a relatively low melting point, for example a polymer in which the alkyl groups in the units derived from (i) contain 12 and/or 14 carbon atoms. The polymer can be a block copolymer in which one of blocks is a crystalline polymer as defined and the other block(s) is crystalline or amorphous. Preferred block copolymers comprise (i) polysiloxane polymeric blocks, and (ii) crystalline polymeric blocks having a Tp of −5 to 40° C. Such a polymer can be prepared by copolymerizing a mixture of reactants which comprises (i) at least one n-alkyl acrylate or methacrylate in which the n-alkyl group contains at least 12 carbon atoms and (ii) a polysiloxane having a copolymerizable group at one end thereof.
Other polymers which can be used to the coat the microporous film include cis-polybutadiene, poly (4-methylpentene), polydimethyl siloxane, and ethylene-propylene rubber.
The gas-permeable membrane preferably has one or more of the following properties
In one embodiment, the control member comprises
The O2 permeability of the container at 13° C. per kilogram of fruits therein (OP13/kg) is preferably at least 700, particularly have least 1000, especially at least 1500, ml/.atm.24 hrs. The R ratio of the container at 13° C. is preferably at least 2, particularly at least 3. The ethylene permeability of the container at 13° C. per kilogram of fruits therein (EtP13/kg) is preferably at least 3 times, particularly at least 4 times, the OP13/kg of the container.
The permeability of the container, whether or not it includes an atmosphere control member, can be influenced by perforating the container in order to make a plurality of pinholes therein.
Fruits
This invention is particularly useful for (but is not limited to) the ripening and/or storage of the wide range of fruits which ripen (or undergo other changes, for example, in the case of citrus fruits, de-greening) when exposed to ethylene, for example apples, apricots, avocados, bananas, blueberries, cherimoyas, dates, figs, kiwis, mangos, melons, peaches, papayas, pears, peppers, persimmons, and plums (all of which go through a climacteric when they ripen), as well as cherries, grapes, lemons, oranges, tomatoes and strawberries. Some aspects of the invention are especially useful for fruits which in commercial practice are ripened in ethylene-containing ripening rooms, for example avocados, bananas, Bartlett pears, kiwis, mangos, melons, peppers and tomatoes.
Storage of Unripe Fruits
When the invention is being used to store unripe fruits, it is possible to produce desired packaging atmospheres by the selection of containers which, when sealed around the quantities of fruits in question at the selected storage temperature, have appropriate permeabilities to O2 and CO2, and by the selection of an appropriate controlled atmosphere around the sealed packages. Those skilled in the art will have no difficulty, having regard to their own knowledge and the contents of this specification, in making appropriate selections to produce a desired packaging atmosphere or to make a desired compromise between (i) the cost and inconvenience of obtaining an entirely satisfactory combination of container and controlled atmosphere, and (ii) the disadvantage of storing the fruits in a packaging atmosphere which is in some ways unsatisfactory.
The table below sets out, for some of the fruits for which this invention is useful, ranges for the concentrations of O2 and CO2 which may be used during storage. The invention is, however, useful, for storing these and other fruits outside the ranges stated in the table below.
Ripening Unripe Fruits by Exposure to Exogenous ERA
In many aspects of the invention, unripe fruits are ripened by exposure to exogenous ERA while the fruits are in a sealed container. In some embodiments, the exogenous ERA enters the packaging atmosphere through the container from the atmosphere surrounding the sealed packages, for example as a result of
The amount of ERA in the packaging atmosphere should be sufficient to assist ripening. Thus the packaging atmosphere in each of the sealed packages should contain at least 2.5 ppm, typically but not necessarily 100 to 3000 ppm, preferably 250 to 1000 ppm, of ERA. When the exogenous ERA is added to or generated in the atmosphere surrounding the sealed packages, the concentration of ERA in the packaging atmosphere will increase gradually as the exogenous ERA passes through the sealed container, at a rate which depends upon the concentration of ERA in the surrounding atmosphere. If, therefore, a rapid initiation of ripening is desired, the concentration of ERA in the atmosphere surrounding the sealed packages is preferably least 500 ppm, particularly at least 1000 ppm. The table below shows the time taken to reach an ethylene concentration of 100 ppm in the packaging atmosphere of a sealed package of bananas according to the invention, when placed in a ripening room containing the indicated concentrations of ethylene.
An advantage of ripening fruits in a sealed container in accordance with the invention, by comparison with conventional ripening by means of a controlled atmosphere directly in contact with the fruits is that the ripe fruits can be substantially less dehydrated. It is believed that this is because ripening takes place in a more controlled fashion, resulting in lower peak temperatures in the fruits, which in turn results in the reduced dehydration. Thus, bananas typically lose 3 to 5% of their weight between packaging directly after harvest and being put on retail sale. I have found that, through use of the present invention, this weight loss can be substantially reduced, for example to less than 0.5%. Another benefit, when the ripening is carried out below room temperature, is reduced demand on the refrigeration equipment.
The temperature at which ripening is carried out and the concentration of ERA in the packaging atmosphere influence the rate at which ripening takes place. In general, slower ripening results in ripened fruits which remain in a desired range of ripeness for a longer period. On the other hand, rapid ripening may be desired, for example in view of delivery dates required by retail outlets. Thus, the atmosphere around the sealed packages may be above, at, or below ambient temperature. However, it is generally preferred that the atmosphere should be at a temperature less than 22° C., preferably less than 21° C., for example 16-21° C., or even lower, for example at a temperature less 18° C. or less than 16° C., e.g. at 14-15° C.
The atmosphere within the bags will change substantially during the ripening process, as the ripening fruits consume O2 and generate CO2. The packaging atmosphere, for at least part of the period before ripening fruits reach their climacteric, may contain at least 10%, preferably at least 12%, particularly 14 to 19%, of O2, and less than 10%, preferably less than 4%, of CO2, with the total quantity of O2 and CO2 being less than 20%, preferably less than 17%. For at least part of the period after ripening fruits have passed their climacteric, the packaging atmosphere may contain at least 0.8%, for example 1.5 to 6% or 1.5 to 3%, of O2, and less than 15%, preferably less than 7%, of CO2, with the total quantity of O2 and CO2 being less than 16%, preferably less than 10%.
When it is desired to ripen fruits while they are being transported, for example on a ship or a truck, ripening by means of a source of exogenous ERA placed within the sealed packages and/or by means of a source of exogenous ERA placed within a large closed container containing the sealed packages, is particularly useful. The ripening can be preceded by a storage period in which there is little or no ripening. The ripening and optional storage process can be controlled so that the fruits are at a desired state of ripeness when they reach their destination. During the process, there may be no need to alter the atmosphere around the sealed packages. However, when the fruits are stored before they are ripened, it may be desirable to restrict the amount of oxygen which enters the sealed packages during storage, in order to prevent or delay ripening. When the packages can be surrounded by a controlled atmosphere (for example while being transported in the hold of a suitably equipped ship), this result can be achieved by placing the sealed packages in a controlled atmosphere containing less than the 5 amount of oxygen present in air (about 21%), for example less than about 12%. The source of exogenous ERA can make ERA available immediately after packaging the bananas, or after a desired delay. Delayed release of ERA can result, for example, from the use of an exogenous ERA source which (i) is activated by an increase in moisture content (for example by water which reaches the ERA source as a result of capillary wicking of water through an intermediate body which separates a water reservoir from the ERA source), or (ii) is associated with (e.g. surrounded by or adsorbed onto) a material which releases ERA or one or more precursors for an ERA, after a set time or in response to some outside intervention, for example an increase in temperature.
Any convenient source of exogenous ERA can be used. I have obtained good results using 2-chloroethyl phosphonic acid, which is often referred to herein as 2CPA. 2CPA can be used in the form of an aqueous solution, for example of concentration 3-4%. The rate at which 2CPA generates ethylene increases with increasing pH of the aqueous solution, which can be adjusted, for example to more than 4, particularly more than 7, by the addition of suitable materials, for example buffer solutions and/or sodium bicarbonate solutions. In one embodiment, a 2CPA solution and a pH adjuster are adsorbed on the same or different absorbent pads, e.g. paper pads, and the pad(s) placed in the bottom of the bag and covered with a polymeric sheet before the unripe fruits are placed in the containers. In another embodiment, a solution of 2CPA is applied to the unripe fruits, for example by dipping or spraying, before they are placed in the bag. The invention also includes the possibility that ripe fruits are the source of exogenous ERA, the ripe fruits generating ethylene and being of the same family as, or a different family from, the unripe fruits which are to be ripened. For example, for ripening green bananas, the source of exogenous ERA could be a perforated container containing apples or bananas which have passed their climacteric.
As in the aspects of the invention which involve ripening in an exogenous ERA-containing atmosphere surrounding the sealed packages, the atmosphere within sealed bags containing a source of exogenous ERA will change during the ripening process. The packaging atmospheres, for at least part of the periods before and after the climacteric, are preferably as stated above when the sealed bags are surrounded by an exogenous ERA-containing atmosphere.
Quantities of Fruits
The invention can in principle be used for any quantity of fruits. In some embodiments, for example when the invention is used for storing and/or ripening green bananas, the sealed container preferably contains at least 4 kg, particularly at least 15 kg, especially 16 to 22 kg of bananas or other fruits. In other embodiments, smaller quantities are used, for example to increase the shelf life of bananas at a desired color stage.
The invention is illustrated in the following Examples, a number of which are comparative Examples, designated by the letter C before the number of the example. The bananas, bags and control members used in the Examples were as follows.
Bananas
The bananas were Cavendish bananas, from Ecuador in Examples 1A-B, C11-12, 2, C2, 4A-B and C41-42, from Costa Rica in Examples 5 A-C and C5, and from Colombia in the other Examples.
Bags
The large bags were about 0.96 m (38 in.) wide and about 1.2 m (50 in.) long, and were made from polyethylene film about 0.056 mm (2.2 mil) thick (available from Roplast Industries under the tradename RA 3030). The polyethylene film had an OTR at 13° C. of about 2915 (188) and at 22° C. of about 4,650 (300), and EtTR at 13° C. of about 11,400 (735) and at 22° C. of about 18,100 (1,170), an R ratio of about 4.5, and a P10 ratio (between 0 and 10° C.) of about 1.76. The small bags were about 0.3 m (12 in.) wide and about 0.46 m (18 in.) long, and were made from the same polyethylene film.
Control Members
The Type S control members were as described in copending commonly assigned U.S. application Ser. No. 09/121,082 and corresponding International Publication No. WO 00/04787 and comprised a microporous polyethylene film coated with a polysiloxane/SCC block copolymer. The Type S members had an OTR at 13° C. of about 3,803,850 (245,410) and at 22° C. of about 5,000,000 (324,000), an EtTR at 13° C. of about 16,280,000 (1,050,300) and at 22° C. of about 19,500,000 (1,260,000), an R ratio of about 3.8, and a P10 ratio (between 0 and 10° C.) of about 1.8. The microporous polyethylene film contained 50-60% silica, had a thickness of about 0.18 mm (0.007 inch), a tear strength of about 90g, a porosity of about 65%, an average pore size of about 0.1 micron and a largest pore size of 4-10 microns (available from PPG industries under the tradename Teslin SP 7). The block copolymer was prepared by the reaction of a polydimethyl siloxane terminated one end only by a methacryloxypropyl group (available from Gelest under the tradename MCR Ml 7), 40 parts, dodecyl acrylate, 26.8 parts and tetradecyl acrylate, 33.2 parts, as described in Example A7 of U.S. application Ser. No. 09/121,082 and corresponding International Publication No. WO 00/04787.
The Type A control members were as described in copending commonly assigned U.S. application Ser. No. 08/759,602 and corresponding International Publication No. WO 96/38495, and comprised the same microporous polyethylene film coated with an SCC polymer of dodecyl acrylate, 42 parts, tetradecyl acrylate, 53 parts, and acrylic acid, 5 parts. The Type A members had an OTR at 22° C. of about 1,705,000 (110,000), an R ratio of about 4, and a P10 ratio (between 0 and 10° C.) of about 1.4.
In each Example, the control member was secured to a portion of the bag in which one or more round holes had been cut. The effective area of the control member is about equal to the area of the hole or holes in the portion of the bag to which the control member is attached. However, in Examples 1A-B, C11-12, 2, C2, 3A-D and C31-33, the periphery of the control member was heat sealed to the interior of the bag, thus creating a control member of the kind described in U.S. Pat. No. 6,013,293. In the other Examples, the control member was secured to the exterior of the bag by means of a layer of a pressure sensitive adhesive on the peripheral margin of the control member.
The color stages referred to in the Examples are those accepted by the industry and as shown below.
Bananas are preferably at color stage 3.5 to 5 when put on retail sale.
Many of the Examples are summarized in Tables 1-8 below. In the Tables, when more than one result is given for a particular Example, this reflects the fact that more than one test was carried out under the same conditions.
Each of these Examples uses a large bag. In Examples C 11, 1A-B and 2, each bag has one S-type control member placed under two or more holes in the bag. In Example C11, the control member had an area of 1935 mm2 (3 in2) and was placed under two holes, each of diameter 20.6 mm (0.81 in.). In Example 1A, the control member had an area of 6450 mm2 (10 in2) and was placed under 6 holes, each of diameter 20.6 mm (0.81 in.). In Examples 1B and 2, the control member had an area of 12,900 mm2 (20 in2) and was placed under 6 holes, each of diameter 28.7 mm (1.13 in). Each bag was packed with about 20 kg (44 lb) of green bananas. The bananas had been harvested at week 11 and maintained at 13-14° C. for about 11 days after harvest before being packed. Except in Examples C12 and C2, excess air was extracted from the bags using a vacuum pump, and the bags were then sealed using tie wraps. In Examples C12 and C2, the bags were left open. The bags were maintained at 13° C. for an extended time, Examples 1A, 1B, C11 and C12 being terminated at day 62, and Examples 2 and C2 being terminated at day 40. The results are given in Table 1 below. In Example 2, traces of ethylene (generated by the ripening of the bananas) remained in the test chamber from Example 1 and caused the bananas to ripen more rapidly than in the otherwise substantially identical Example 1B. This demonstrates the desirability of excluding ethylene when long storage periods are needed (and conversely, the ability to accelerate ripening when desired).
Each of these Examples uses a large bag. In Examples C31-33 and 3, each bag has one S-type control member placed under one or more holes in the bag. In Example C31, the control member had an area of 967 mm2 (1.5 in2) and was placed under a single hole of diameter 20.6 mm (0.81 in.). In Example C32, the control member had an area of 1935 mm2 (3in2) and was placed under 2 holes, each of diameter 20.6 mm (0.81 in.). In Example C33, the control member had an area of 3225 mm2 (5 in2) and was placed under 4 holes, each of diameter 19 mm (0.75 in.). In Example 3, the control member had an area of 12,900 mm2 (20 in2) and was placed under 6 holes, each of diameter 25 mm (1 in.). In Example C34, the bag did not have a control member. Each bag was packed with about 18.1 kg (40 lb) of green bananas. The bananas had been harvested at week 13, and maintained at 13-14° C. for about 11 days after harvest before being packed. Except in Example C34, excess air was extracted from the bags using a vacuum pump, and then securely tied (the bags were not, however, as completely sealed as in Examples 1 and 2). In Example C34, the bags were left open. The sealed bags were cooled to about 13° C. and shipped to Gulfport, Mississippi, and then to San Francisco, Calif., maintaining the temperature at about 13° C. In San Francisco, 36 days after packing, half the bags in each Example were opened, and the other half left intact. All the bags were then exposed to exogenous ethylene (500-1000 ppm) in a commercial ripening room for about 24 hours. The bananas in the opened bags ripened rapidly in the expected way; thus by day 43, their color was 6, by day 46 their color was greater than 7, and by day 49, they were overripe. The bags which were still sealed were opened on day 49. The results for the bags opened on day 49 are shown in Table 2 below. These Examples demonstrate that bananas harvested at 13 weeks can be transported in a suitably designed bag, and can be ripened into an excellent product by exposure to exogenous ethylene, either through the bag or after opening the bag.
Each of these Examples uses a small bag. In Examples 4A-B, each bag has one A-type control member placed over four or five holes in the bag. In Example 4A, the control member had an area of 145 mm2 (5.7 in2) and was placed over four holes each of diameter 19 mm (0.75 in.). In Example 4B, the control member had an area of 4516 mm2 (7 in2) and was placed over 5 holes, each of diameter 19 mm (0.75 in.). In Example C41, the control member and the holes under it were as in Example 4A, except that the control member was an uncoated microporous film. In Example C42, the bag was intact except for 200 pinholes each about 0.5 mm (26 gauge) in diameter. Each bag was packed with about 1.35 kg (3 lb) of green bananas which had been maintained at 13-14° C. for about 11 days after harvest. Except in Example C42, excess air was extracted from the bags using a vacuum pump, and the bags were then securely tied. In Example C42, the bags were left open. After three days, to allow the packaging atmosphere to equilibrate, the bags were exposed to exogenous ethylene (500-1000 ppm) in a ripening room. The results are shown in Table 3 below. These Examples demonstrate that small quantities of bananas can be ripened in a suitably designed bag, and can remain in the bag in excellent condition for several days longer than bananas exposed to the air.
uncoated microporous film
These Examples show that the bananas generate heat more evenly when ripened in a container including an atmosphere control member. In each Example, a large bag was packed with about 18.1 kg (40 lb.) of green bananas. The green bananas had been harvested 13 days previously and had been stored at 13-14° C. since harvest. A temperature sensor (available from Sensitech, Beverly, Mass., under the tradename Temptale P) was inserted into one banana in each bag. In each of Examples 5A, 5B and 5C, the bag had two S-type control members, each having an area of 11,300 mm2 (17.5 in2). Each control member was placed over a single hole in the bag, the hole having an diameter of 70 mm (2.75 in.) in Example 5A, 74.4 mm (2.93 in.) in Example 5B, and 78.7 mm (3.1 in.) in Example 5C. In Example C5, the bag was perforated so that the bananas were surrounded by air. The bags were then sealed with rubber bands. The sealed bags were placed in a refrigerated room at about 13° C. After about 84 hours, the temperature of the room was raised to about 16.7° C. and after about 12 hours, an ethylene generator was used to provide an initial ethylene concentration in the room of 500-1000 ppm. About 24 hours after the generation of ethylene had begun, the room was vented. The temperature of the bananas was monitored for about 15 days, and reached a peak at about 60 hours after the generation of ethylene had begun. At that time, the concentration of O2 and CO2 was measured. The results are shown in Table 4 below. It will be seen that the peak temperature was substantially lower in the bags containing control members than in the perforated bag.
Each of these Examples uses a large bag having two S-type control members, each control member having an area of 11,300 mm2 (17.5 in2). Each control member was placed over seven holes in the bag, each hole of diameter 25.4 mm (1 in). A paper pad about 300×400 mm (12×16 in.) impregnated with an aqueous solution of 2CPA (3.9%) was placed in the bottom of each bag and covered with a sheet of polyethylene. The amount of the solution varied from Example to Example, and is shown in Table 5 below. About 18.1 kg (40 lb.) of green bananas were then placed in each bag, and the bags were sealed with rubber bands. The green bananas had been maintained at 13-14° C. for about 11 days after harvest. The sealed bags were left in a cold room at 13-14° C. The color stage of the bananas was monitored, and Table 5 below shows the time in days taken to reach color stages 4 and 5.5.
The procedure of Example 6 was followed except for the changes noted below.
Examples 8A-J and C 81-83 followed the same procedure as Examples 7A-C and C71-74 except for the changes noted below.
The procedure of Example 6 was followed, except for the changes noted below.
Table 9 below shows, for each of the bags in Examples 5A-C, 6A-E and 7A-E, the permeability of the bag to O2 and to ethylene (“Et” in Table 9), and the respective contributions of the control member and the remainder of the bag. For this calculation, the size of the bag, after sealing, was assumed to be 0.96×1.04 m (38 in.×41 in.), i.e. to have a total area of 2 m2 (3115 in2).
Three trials were carried out to compare bananas transported and ripened (a) conventionally in 12 conventional bags as controls, and (b) in accordance with the invention in 36 bags having atmosphere control members. Each bag was supported by a cardboard box. The conventional bags were about 1 m. (38.5 in.) by 1.25 m. (49.5 in.) and were made of polyethylene film about 0.18 mm (0.0007 in.) thick. Each conventional bag was perforated with about 312 holes, each about 12.5 mm (0.5 inch) in diameter. The bags used in accordance with the invention were about 1 m. (39.75 in.) by 1.2 m (46.25 in.) and were made of a film of a blend of polyethylene and ethylene/vinyl acetate copolymer about 0.05 mm (0.002 in.) thick. Each bag had two S-type atmosphere control members, each control member being about 145 mm (5.625 in.) by 120 mm (4.72 in.) and being secured to the bag by a layer of adhesive about 11 mm (0.44 in.) wide around its periphery. Under each atmosphere control member, the bag had seven holes each about 25 mm (1 in.) in diameter.
In Columbia, each bag was packed with about 20 kg. of green, freshly harvested bananas. The necks of the bags of the invention were sealed with rubber bands. The necks of the conventional bags were not closed. The bags were weighed and then transported at about 14.5° C. (58° F.) to Watsonville, Calif., U.S.A., where, 13 days after harvest, they were placed in a commercial ripening room containing ethylene for 24 hours at about 16.5° C. (62° F.). The room was then vented and maintained at about 16.5° C. (62° F.) for the next 24 hours, at about 15.5° C. (60° F.) for the next 48 hours, and at about 14.5° C. (58° F.) for the next 24 hours. The bananas were then maintained at about 21° C. (70° F.). The table below shows the average weight loss of the bags, and the color of the bananas in the bags, on the day indicated. The sealed bags were not opened until the day indicated in the table below.
The results reported in this table show clearly that the practice of the invention results in bananas which lose less weight through dehydration and which remain at a desired color stage for a longer time.
The invention defined by the claims below is narrower in scope than the invention disclosed in the Summary of Invention, Detailed Description and Examples above. I intend to file one or more continuing applications to claim some or all of the aspects and embodiments of the invention which are disclosed in the Summary of Invention, Detailed Description and Examples above, but not literally claimed by the claims in any patent issued on this application. Therefore, readers of this specification should be aware that I am not dedicating to the public any part of the invention broadly described in this specification, even if it does not fall within the literal scope of the claims in any patent issued on this application.
This application is a continuation-in-part of my copending, commonly assigned application Ser. No. 09/858,190, filed May 15, 2001, which claims priority under 37 CFR 1.78 (a)(5) from provisional Application Ser. No. 60/325,762 filed May 26, 2002. Application Ser. No. 60/325,762 has an effective filing date of May 26, 2000, and resulted from the conversion to a provisional application of application Ser. No. 09/580,379, filed May 26, 2000. This application is also related to International Application No. PCT/US 01/40732, filed May 15, 2001. The disclosure of each of the above-identified applications is incorporated herein by reference.
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| Number | Date | Country | |
|---|---|---|---|
| 20020127305 A1 | Sep 2002 | US |
| Number | Date | Country | |
|---|---|---|---|
| 60325762 | May 2002 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 09858190 | May 2001 | US |
| Child | 09989682 | US |
