AU2003271582B2 - Method of packaging a frozen dessert - Google Patents
Method of packaging a frozen dessert Download PDFInfo
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- AU2003271582B2 AU2003271582B2 AU2003271582A AU2003271582A AU2003271582B2 AU 2003271582 B2 AU2003271582 B2 AU 2003271582B2 AU 2003271582 A AU2003271582 A AU 2003271582A AU 2003271582 A AU2003271582 A AU 2003271582A AU 2003271582 B2 AU2003271582 B2 AU 2003271582B2
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- Australia
- Prior art keywords
- product
- container
- gas
- receptacle
- pressure
- Prior art date
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- 238000000034 method Methods 0.000 title claims abstract description 35
- 235000021185 dessert Nutrition 0.000 title claims abstract description 15
- 238000004806 packaging method and process Methods 0.000 title claims abstract description 11
- 239000007789 gas Substances 0.000 claims abstract description 75
- 239000003380 propellant Substances 0.000 claims abstract description 36
- GQPLMRYTRLFLPF-UHFFFAOYSA-N Nitrous Oxide Chemical compound [O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 claims abstract description 15
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 6
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 3
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 12
- 239000001272 nitrous oxide Substances 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 239000000945 filler Substances 0.000 claims description 2
- 230000000630 rising effect Effects 0.000 claims description 2
- 238000011144 upstream manufacturing Methods 0.000 claims description 2
- 239000000047 product Substances 0.000 description 83
- 239000000203 mixture Substances 0.000 description 20
- 235000011837 pasties Nutrition 0.000 description 8
- 235000015243 ice cream Nutrition 0.000 description 6
- 235000013305 food Nutrition 0.000 description 5
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 230000008014 freezing Effects 0.000 description 4
- 238000007710 freezing Methods 0.000 description 4
- 238000002347 injection Methods 0.000 description 4
- 239000007924 injection Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000002184 metal Substances 0.000 description 3
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 2
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 2
- 238000002788 crimping Methods 0.000 description 2
- 230000001419 dependent effect Effects 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 238000009472 formulation Methods 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 239000012263 liquid product Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- MGWGWNFMUOTEHG-UHFFFAOYSA-N 4-(3,5-dimethylphenyl)-1,3-thiazol-2-amine Chemical compound CC1=CC(C)=CC(C=2N=C(N)SC=2)=C1 MGWGWNFMUOTEHG-UHFFFAOYSA-N 0.000 description 1
- QCVGEOXPDFCNHA-UHFFFAOYSA-N 5,5-dimethyl-2,4-dioxo-1,3-oxazolidine-3-carboxamide Chemical compound CC1(C)OC(=O)N(C(N)=O)C1=O QCVGEOXPDFCNHA-UHFFFAOYSA-N 0.000 description 1
- 102000002322 Egg Proteins Human genes 0.000 description 1
- 108010000912 Egg Proteins Proteins 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 235000013365 dairy product Nutrition 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 235000014103 egg white Nutrition 0.000 description 1
- 210000000969 egg white Anatomy 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 238000005429 filling process Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 235000020166 milkshake Nutrition 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000006188 syrup Substances 0.000 description 1
- 235000020357 syrup Nutrition 0.000 description 1
- -1 therefore not frozen Substances 0.000 description 1
- 239000002562 thickening agent Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 235000008939 whole milk Nutrition 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23G—COCOA; COCOA PRODUCTS, e.g. CHOCOLATE; SUBSTITUTES FOR COCOA OR COCOA PRODUCTS; CONFECTIONERY; CHEWING GUM; ICE-CREAM; PREPARATION THEREOF
- A23G9/00—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor
- A23G9/44—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor characterised by shape, structure or physical form
- A23G9/46—Aerated, foamed, cellular or porous products
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23G—COCOA; COCOA PRODUCTS, e.g. CHOCOLATE; SUBSTITUTES FOR COCOA OR COCOA PRODUCTS; CONFECTIONERY; CHEWING GUM; ICE-CREAM; PREPARATION THEREOF
- A23G9/00—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor
- A23G9/04—Production of frozen sweets, e.g. ice-cream
- A23G9/20—Production of frozen sweets, e.g. ice-cream the products being mixed with gas, e.g. soft-ice
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23G—COCOA; COCOA PRODUCTS, e.g. CHOCOLATE; SUBSTITUTES FOR COCOA OR COCOA PRODUCTS; CONFECTIONERY; CHEWING GUM; ICE-CREAM; PREPARATION THEREOF
- A23G9/00—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor
- A23G9/04—Production of frozen sweets, e.g. ice-cream
- A23G9/22—Details, component parts or accessories of apparatus insofar as not peculiar to a single one of the preceding groups
- A23G9/28—Details, component parts or accessories of apparatus insofar as not peculiar to a single one of the preceding groups for portioning or dispensing
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23G—COCOA; COCOA PRODUCTS, e.g. CHOCOLATE; SUBSTITUTES FOR COCOA OR COCOA PRODUCTS; CONFECTIONERY; CHEWING GUM; ICE-CREAM; PREPARATION THEREOF
- A23G9/00—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor
- A23G9/04—Production of frozen sweets, e.g. ice-cream
- A23G9/22—Details, component parts or accessories of apparatus insofar as not peculiar to a single one of the preceding groups
- A23G9/28—Details, component parts or accessories of apparatus insofar as not peculiar to a single one of the preceding groups for portioning or dispensing
- A23G9/281—Details, component parts or accessories of apparatus insofar as not peculiar to a single one of the preceding groups for portioning or dispensing at the discharge end of freezing chambers
- A23G9/283—Details, component parts or accessories of apparatus insofar as not peculiar to a single one of the preceding groups for portioning or dispensing at the discharge end of freezing chambers for filling containers with material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65B—MACHINES, APPARATUS OR DEVICES FOR, OR METHODS OF, PACKAGING ARTICLES OR MATERIALS; UNPACKING
- B65B31/00—Packaging articles or materials under special atmospheric or gaseous conditions; Adding propellants to aerosol containers
- B65B31/04—Evacuating, pressurising or gasifying filled containers or wrappers by means of nozzles through which air or other gas, e.g. an inert gas, is withdrawn or supplied
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Dispersion Chemistry (AREA)
- Mechanical Engineering (AREA)
- Confectionery (AREA)
- Vacuum Packaging (AREA)
- Containers And Packaging Bodies Having A Special Means To Remove Contents (AREA)
- Devices For Dispensing Beverages (AREA)
Abstract
The procedure, in which a container (1) has a propellant gas to dispense the product, uses a gas that is insoluble in the product to dispense it and a different gas to expand the product as it is dispensed. The expanding gas is preferably selected from nitrogen protoxide and carbon dioxide, and is dissolved in the frozen dessert product. The propellant gas is diazote or compressed air with a dewpoint below the minimum temperature at which the container is kept between packaging and use.
Description
WO 2004/026756 PCT/EP2003/009852 Method of packaging a frozen dessert The invention relates to a method of packaging a thick but malleable frozen dessert, and for dispensing it 5 under pressure in the expanded state, it being possible for the degree of expansion to be chosen independently of the consistency of the said dessert. When it is desired to dispense a frozen dessert in the 10 expanded state, that is to say in aerated form, it is known by Patent US A 4 421 778 to foam an ice-cream or milkshake mix in order to expand it, to fill receptacles with portions of the expanded mix, which receptacles are then placed in a freezer and where the 15 product is then preserved at freezing temperature. The product is spoonable at this temperature. In fact, the step of foaming at a positive temperature with the introduction of air creates an expanded state which is not stable. There is no indication that the product can 20 be introduced into a pressurized container or can be dispensed at the cold storage temperature from this container in the form of a frozen dessert in a stable expanded state. 25 Moreover, a method and an apparatus making it possible to introduce an expansion gas, nitrogen dioxide, into a liquid, therefore not frozen, mix at a high pressure for the purpose of entraining enough gas into the ice-cream in order to produce the desired expanded 30 state is known, for example, from Patent US A 4 659 575. The non-frozen mix which has been subjected to this pre-aeration is then withdrawn from a mixing tank containing it to a container for dispensing it after enough gas has been entrained, then it is 35 subsequently frozen at the dispensing location. To avoid the drawback of the instability of the expanded state of a liquid mix, it would be conceivable to put the product to be packaged in the liquid state -2 into the packaging receptacle and then to introduce into this receptacle a propellant gas which is slightly soluble in the said liquid product, after which the receptacle would be cooled to the dispensing temperature of the product, at which temperature it is pasty; in this case, the product is packaged in the unexpanded, pasty state and it is extruded under 5 the thrust of the propellant gas: at the outlet of the dispensing member, the product would be put in the expanded state by the expansion of the propellant gas dissolved in the said product. However, this procedure is not satisfactory for two reasons: - on the one hand, the amount of propellant gas dissolved in the product is difficult to control, such that the expanded state obtained is not constant and that the 10 amount of gas remaining available for propulsion of the product is therefore not constant either; and - on the other hand, the amount of propellant gas dissolved in the product is obviously dependent on the gas pressure, which is imposed by the extrudability of the pasty product, hence the result is that, for a given product, the expanded 15 state likely to be obtained on dispensing it is necessarily linked to the pressure of the propellant gas and to the nature of the said gas. Any discussion of the prior art throughout the specification should in no way be considered as an admission that such prior art is widely known or forms part of common general knowledge in the field. 20 It is an object of the present invention to overcome or ameliorate at least one of the disadvantages of the prior art, or to provide a useful alternative. The aim of a preferred embodiment of the present invention is to provide a method of packaging and dispensing a thick but malleable frozen dessert, by means of which, on the one hand, it is possible to package the said product in a pressurized receptacle with a 25 high enough pressure given the viscosity of the product, and, on the other hand, it is possible to choose the degree to which the product is expanded at the output of the pressurized receptacle independently of the pressure required for propulsion of the product from the receptacle and of the speed at which the product comes out of the receptacle.
- 3 By virtue of such a method, it especially becomes possible to dispense a frozen dessert, such as the one described for example in European Patent EP B 878 998 or in French Patent Application FR 02 05620, by choosing the degree of expansion that is desired for the product dispensed at the outlet of the receptacle; in fact, it is desirable not to 5 dispense such a frozen dessert in the form of a compact paste, but it is also desirable to prevent dispensing in the form of a foam which is too aerated. The invention is partly based on the fact that two different gases are chosen for dispensing, of which one has the propulsion function and the other the expansion function. The propellant gas is virtually insoluble in the product to be dispensed when in 10 the liquid state while the expansion gas is highly soluble in the said liquid product. The expansion of the dispensed product will then be dependent on the amount and on the solubility of the expansion gas introduced into the receptacle, while the ejection of the product will depend on the pressure of the propellant gas introduced into the receptacle. According to a first aspect, the invention provides a method of packaging a thick but 15 malleable frozen dessert, and for dispensing it under pressure in the expanded state, in which method the product is placed in a container equipped with a dispensing member, then, after having put the said dispensing member in the closed position, the said container is pressurized by a propellant gas to a pressure high enough to ensure suitable dispensing, given the consistency of the product to be dispensed and characteristics of 20 the dispensing member, wherein: a) a propellant gas which is virtually insoluble in the product to be dispensed is chosen; b) an expansion gas which is different from the propellant gas and highly soluble in the product 25 WO 2004/026756 PCT/EP2003/009852 -4 to be dispensed is. chosen in order to expand the product when it is dispensed, the amount of expansion gas used being defined depending on the degree of expansion desired on dispensing, the 5 expansion gas being homogeneously dissolved in the product to be dispensed by putting the expansion gas in contact with the said product in a freezer and c) the passage of the said product takes place in 10 the pasty state then it is dispensed by opening the dispensing member, the said product being expanded up to the desired degree, determined prior to filling, as described in step 1b, by expanding the expansion gas which is completely 15 dissolved therein. To implement the method, an ice-cream mix is treated in a freezer which is supplied with expansion gas so as to partially freeze and expand the said mix, under 20 temperature and pressure conditions promoting good dissolution of the expansion gas in the said mix. In practice, it is preferred to operate at a temperature of about -8'C to -12 0 C at the output and at a constant pressure equal to atmospheric pressure up to 10 bars 25 above atmospheric pressure in the freezer. A gas that is highly s-oluble in the mix, preferably chosen from nitrous oxide (N 2 0) and carbon dioxide, is used as an expansion gas. 30 The partly frozen and partly expanded mix is placed in the container by means of a metering device maintaining the initial pressure in the pipes and in the metering unit, for example by exerting a counterpressure 35 upstream from the dispensing member. This way of proceeding makes it possible to limit the expansion of the volume of the product during filling by partial expansion of the expansion gas.
WO 2004/026756 PCT/EP2003/009852 -5 According to a first embodiment of the filling step of the method, a metering nozzle moving with an up and down movement is used as filling device, allowing filling by rising from the bottom of the containers, of 5 the type called "bottom-up filler", so as to maximize the filling and to prevent the formation of pockets free of product. The container is filled, then closed by the dispensing member, sufficiently quickly to limit the expansion. 10 In a second embodiment, the product is filled through the dispensing member fixed beforehand to the container. In this case, the piston is positioned in the top of the container, against the dispensing 15 member, so as to limit the pockets of air in the product. This second embodiment is preferred, since it is more efficient in limiting the expansion at the time of filling. 20 In the method which has been defined above, a rigid receptacle is used as container, into which, on the one hand, the product to be packaged which contains the amount of expansion gas needed to obtain the desired expanded state of the dispensed product is introduced, 25 and, on the other hand, the propellant gas is introduced at the pressure desired for the dispensing. According to a first implementational embodiment of the method, a rigid cylindrical receptacle is used as 30 container, in which receptacle a sliding piston is placed, which divides the receptacle into two compartments, one of which is closed by the dispensing member while the other has a valve enabling the propellant gas to be injected and the pressure to be 35 maintained, the product containing the expansion gas being introduced into the receptacle before it is closed by the dispensing member, or through the dispensing member itself.
WO 2004/026756 PCT/EP2003/009852 -6 According to a second implementational embodiment, a rigid receptacle containing a flexible pouch is used. The container is equipped, on one side, with a dispensing member connected to the pouch, and, on the 5 other side, with a valve allowing the propellant gas to be injected and the pressure of the container to be maintained. According to this second implementational mode, the 10 rigid receptacle equipped internally with the flexible pouch connected to the outside by the dispensing member secured to the receptacle is used as container, the product containing the expansion gas is placed in the receptacle, through the dispensing member, inside the 15 pouch and the propellant gas is then injected into the rigid receptacle through the valve, outside the pouch. In the first implementational mode, it is possible, since a food product is to be packaged and dispensed, 20 to use a metal receptacle and sliding piston which could undergo a conventional sterilization treatment without any difficulty; advantageously, the receptacle and the sliding piston consist of the same metal, which prevents any problem of differential expansion and 25 maintains good sliding of the piston in the receptacle. However, the piston may also be made from a plastic, for example from a polyolefin, it being understood that since the product to be dispensed is a food product, the plastic used must be authorized for food packaging. 30 Advantageously, in this variant, a piston capable of sliding in the receptacle is used and the propellant gas is injected via the valve, the piston then bearing on the product: the degree of expansion of the 35 dispensed product is determined by the amount of expansion gas contained in the product injected by the dispensing member (expressed in 1 of gas per 100 1 of ice-cream mix for example) and the pressure is defined in order to optimize the time for filling the WO 2004/026756 PCT/EP2003/009852 -7 receptacle. Before injecting the propellant gas at a pressure greater than the pressure in the product compartment, the product to be dispensed, charged, at a pressure greater than atmospheric pressure, with 5 partially dissolved expansion gas, is prepared and, the said charged product is metered into the container and the propellant gas is injected into the said container in order to pressurize the product to be dispensed to a pressure greater than that for filling of the product. 10 Since the product to be dispensed is a food product, in order that the product is preserved satisfactorily during storage, acceptable propellant and expansion gases must of course be chosen, bearing in mind 15 existing food standards; according to the invention, nitrogen (N 2 ) or air having a dewpoint less than the minimum temperature to which the container will be exposed between manufacture of the product and its use can advantageously be chosen as propellant gas, and 20 nitrous oxide (N 2 0) as expansion gas. According to the invention, it has been found that good results were obtained with regard to the expansion degree and its stability when 80 to 200 1 of expansion 25 gas, especially N 2 0, per 100 1 of mix were used. Thus, expansion of about 5 to 35% by volume was obtained at the freezer (depending on the pressure in the said freezer) and about 50 to 100% by volume in the final product delivered. This difference in expansion is due 30 to the fact that most of the expansion gas is dissolved in the freezer during the expansion and freezing operation. This gas partially comes out of solution on leaving the freezer and much more strongly in the dispensing member of the container on dispensing at 35 ambient pressure. It is advantageous according to the invention to check that the expansion is as small as possible during filling so as to maximize the amount of product metered into the containers. On the other hand, it will be advantageous for the product leaving the WO 2004/026756 PCT/EP2003/009852 -8 dispensing member to have an expansion comparable to that which is common in ice-creams. This results from increasing the amount of product metered at constant volume. The best results were obtained at a constant 5 pressure of about 4 to 5 bar in the freezer and by maintaining a counterpressure of the same order, in the pipes feeding the metering element and in the latter. In order for the subject of the invention to be better 10 understood, two implementational embodiments, shown schematically in the appended drawing and corresponding to the packaging of a frozen dessert, will now be described by way of purely illustrative and non limiting examples. 15 In this drawing: Figures 1 to 3 and 7 and 8 show the steps of a first variant of the method according to the invention, 20 Figures 4 to 6 show the steps of a second variant of the method according to the invention, and Figures 9 to 11 show various types of valves for 25 filling with the propellant gas which can be used in the method according to the invention. With reference to the drawing, it can be seen that, for all of the figures, a cylindrical metal container is 30 denoted overall by 1 and comprises a bottom and an upper part 2 attached by crimping to the side wall of the said container; in the central region of this part 2, a dish is also attached by crimping, which dish bears, in its centre, a dispensing member 3 comprising 35 a rotating mechanism, which allows it to be opened and closed, by action on a manoeuvring fin 3a. Although this is not described in the examples corresponding to Figures 1 to 3, a translatable pusher could of course be used in place of the aforementioned rotating WO 2004/026756 PCT/EP2003/009852 -9 mechanism. Such a pusher is shown in connection with Figures 7 and 8. The dispensing member 3 comprises, at the outlet, a nozzle to shape the cross section of the column of dispensed product. The packaged product is in 5 the pasty state, and is thick but malleable. For the two variants shown in the drawing, the propellant gas used is nitrogen or compressed air having a dewpoint less than the minimum temperature to which the container will be exposed between manufacture of the 10 product and its use, and the expansion gas is nitrous oxide. In the following examples, the product placed in the receptacle 1 has the following formulation (% by 15 weight): Fat 10.9% Powdered whole milk 7.35% Derivatives of dairy origin 10.9% Glucose and glucose syrup 16.1% 20 Emulsifier 0.38% Thickener about 0.13% Egg white 0.05% Colourings and flavourings 0.08% Water 54.11% 25 Before the product is placed in the container 1, the said receptacle can be sterilized in a known manner, given that the packaged product is afood product. 30 Before being treated in the freezer, the mix is preferably desaerated under negative pressure (vacuum) in order to free it from the gas which may have been incorporated in it during its preparation. In this way it is possible to incorporate into the mix constant 35 quantities of soluble expansion gas, e.g. nitrous oxide. This measure allows to avoid density and expansion variations during filling, which could impair filling WO 2004/026756 PCT/EP2003/009852 - 10 of a given required amount of product into the container. In addition, this step has the advantage to allow direct recycling of the mix which would not be filled 5 in, in case of stop of the filling line if the filling process was interrupted. Before putting it in place, the product, whose mix formulation has been given above, is treated in a 10 freezer at a temperature of -8.5 0 C to -10'C, supplied with nitrous oxide instead of the air normally used for expansion, the amount of nitrous oxide introduced into the mix being from 140 to 145 1 of N 2 0 per 100 1 of mix. The product coming out of the freezer is packaged 15 in the container 1 at a pressure of 4 to 5 bar. The propellant gas (nitrogen or compressed air having a dewpoint less than -40'C) is then introduced at a pressure of about 10 bar through the valve 4. Once the product has been packaged, the product is brought to a 20 temperature of -150C to -20'C , preferably of less than or equal to -18 0 C, at which temperature the said product is in the pasty state. The internal volume of the empty container 1, without piston and without dispensing member, is about 0.8 litre and the volume of 25 product introduced into the container for subsequent dispensing is about 0.6 litre. This corresponds to about 0.9 litre of finished aerated soft ice cream dispensed out of the container. 30 Figures 1 to 3, 7 and 8 show the various steps of the first variant of the method according to the invention. In this variant, the container 1 has a valve 4 in its base and, internally, it has a sliding piston 5 (see Figure 1). In the drawing, for the purpose of 35 simplification, a piston 5, whose circular face is flat is shown; however, in a known manner, a piston can be used whose circular face is shaped so as to have, at its centre, a cavity allowing the part of the dispensing member 3 which projects inside the container WO 2004/026756 PCT/EP2003/009852 - 11 1 to be housed: in this way, the emptying rate of the receptacle during dispensing is improved. In a first example, the half-frozen unexpanded product 5 P is put in place in the container without the dish bearing the dispensing member 3 by means of a filling nozzle 6 moving with an up and down movement in the direction of the arrow fl, the filling being carried out from the bottom up by vertical translational 10 movement of the filling nozzle 6. The filling is carried out rapidly and, when the container is full, the dish bearing the dispensing member 3 is crimped (put in place in the direction f2). The piston 5 is then in the low position (see Figure 2) and the 15 pressure is P1. Nitrogen at a pressure P2 equal to about 8-10 bar (or compressed air having a dewpoint equal to or less than -40'C) is injected below the piston 5, the introduction taking place through the valve 4 (see Figure 3). 20 The temperature of the product in the container 1 is then lowered to a temperature of -15'C to -20 0 C , preferably equal to or less than -18 C, by passing the container filled with the product through a freezing tunnel, the temperature of which is -35 to -38 0 C, the 25 product to be dispensed thus taking on its pasty dispensing consistency. The product is thus stored and used by the consumer at a temperature of -15 0 C to -20 0 C. 30 In a second example, the product P is filled through the dispensing member 3 fastened beforehand to the container 1, as illustrated in Figure 7. In this case, the piston 5 is positioned before filling in the top of the container, against the dispensing member. As the 35 product P is introduced into the container, the piston 5 moves towards the bottom of the container 1 in the direction of the arrow Fl. The air contained between the piston and the bottom of the container is expelled through the valve 4. This method of proceeding makes it WO 2004/026756 PCT/EP2003/009852 - 12 possible to limit the pockets of air in the packaged product. The piston 5 is then in the low position (Figure 8) and the pressure is P1. Nitrogen at a pressure P2 equal to about 8-10 bar (or compressed air 5 having a dewpoint equal to or less than -40 0 C) is injected below the piston 5, the introduction taking place through the valve 4 (Figure 8). The temperature of the product in the container 1 is 10 then lowered to a temperature of -15'C to -20 0 C , preferably equal to or less than -18 0 C, by passing the container filled with the product through a freezing tunnel, the temperature of which is -35 to -38*C, the product to be dispensed thus taking on its pasty 15 dispensing consistency. The product is thus stored and used by the consumer at a temperature of -15 0 C to -20 0 C. The filling mode described in this second example is 20 preferred, since it is more efficient in limiting the expansion of the product at the time of filling. In the second variant shown in Figures 4 to 6, the container 1 has a valve 4 in its bottom, through which the propellant gas (nitrogen or compressed air having a 25 dewpoint less than the minimum temperature to which the container will be exposed between manufacture of the product and its use) can be injected. Where the dish which bears the dispensing member 3 has been crimped onto the container 1, a flexible pouch 8 (see Figure 4) 30 has been fastened inside the container 1. The partially frozen and expanded product P is then introduced into the pouch 8 through the dispensing member 3 in the open position (see Figure 5). The dispensing member 3 is closed and the propellant gas is injected at a pressure 35 of 8 to 15 bar, preferably of 8 to 10 bar through the valve 4 (see Figure 6). During filling, the pressure in the container 1 has therefore passed from atmospheric pressure to the pressure P1 10 bar above atmospheric pressure, then to the pressure P2 of 8 to 15 bar, WO 2004/026756 PCT/EP2003/009852 - 13 preferably of 8 to 10 bar above atmospheric pressure by the final injection of the propellant gas. Several solutions for the valve systems 4 are known and 5 have been used in the examples described. The first type, known by the name "Nicholson valve", is illustrated in Figure 9. In this case, the valve is applied to the bottle before injection of the 10 propellant gas, so as to be only partially engaged in the orifice made in the bottom of the container. The valve allows the propellant gas to pass at the time of the injection, then the valve is thrust into the orifice so as to close it completely and to maintain 15 the pressure in the container. The second type is known by the name "umbrella valve" and is described in Figure 10. This valve may also be inserted into the orifice made for this purpose under 20 the container before filling. The valve allows the propellant gas to pass at the time of injection, then, under the effect of the pressure created in this way in the container, the valve closes the orifice so as to maintain the pressure in the container. 25 In the third case, a "rope bung" valve, described in Figure 11, the propellant gas is injected into the orifice made for this purpose in the bottom of the container, then the valve (which in this case is more 30 like a plug) is inserted into the orifice so as to close it and to maintain the pressure in the container.
Claims (14)
- 3. Method according to claim 2 wherein said conditions are at a temperature of 25 about -8*C to -12'C at the output and at a constant pressure equal to atmospheric pressure up to 10 bars above atmospheric pressure in the freezer. - 15
- 4. Method according to claim 1, in which a gas that is highly soluble in the mix, selected from the group consisting of nitrous oxide (N 2 0) and carbon dioxide, is used as an expansion gas.
- 5. Method according to claim 1, in which nitrogen (N 2 ) or compressed air having a 5 dewpoint less than the minimum temperature to which the container will be subjected between manufacture of the product and its use is used as propellant gas.
- 6. Method according to any one of claims 1, 2, 3, 4 or 5, in which the partly frozen and partly expanded mix is placed in the container by means of a metering device ensuring the pressure is kept as close as possible to an initial pressure in the freezer, in 10 the pipes and in the metering unit.
- 7. Method according to claim 6 wherein exerting a counterpressure as close as possible upstream from the metering nozzle limits the expansion of the volume of the product during filling by partial expansion of the expansion gas.
- 8. Method according to one any of claims 1, 2, 3, 4 or 5, in which a metering nozzle 15 moving with an up and down movement is used as filling device, allowing filling by rising from the bottom of the container, of the type called "bottom-up filler", so as to optimize the filling and to prevent the formation of pockets free of product.
- 9. Method according to claim 1, in which the container is filled sufficiently quickly before expansion occurs or, alternatively, hermetically under pressure. 20 10. Method according to any one of claims 1, 2, 3 and 4, in which the container is filled through the dispensing member, a piston then being positioned just under the dispensing member. I1. Method according to any one of claims 1, 2, 3 and 4, in which a rigid receptacle is used as container, into which, on the one hand, the product to be packaged which 25 contains the amount of expansion gas needed to obtain the desired expanded state of the dispensed product is introduced, and, on the other hand, the propellant gas is introduced at the pressure desired for the dispensing. - 16
- 12. Method according to claim 11, in which a flexible pouch defining a volume connected to the dispensing member is used as container, which pouch is placed in a rigid receptacle, to which the dispensing member associated with the pouch is fastened, and the propellant gas is injected into the said receptacle, outside the pouch, the product 5 to be dispensed being introduced into the pouch.
- 13. Method according to claim 11, in which a rigid cylindrical receptacle is used as container, in which receptacle a sliding piston is placed, which divides the receptacle into two compartments, one of which is closed by the dispensing member while the other has a valve enabling the propellant gas to be injected, the product to be dispensed 10 being introduced into the receptacle from the side of the compartment closed by the dispensing member.
- 14. Method according to any one of claims I to 13, in which the temperature of the product is lowered to a value below -10 C.
- 15. Method according to claim 14 wherein the temperature of the product is lowered to 15 a value from -15*C to -20"C so that it takes on its packaging consistency, and it is stored and used by the consumer at this temperature.
- 16. A thick but malleable frozen dessert packaged and dispensed under pressure in the expanded state by the method of any one of claims 1 to 15.
- 17. Method for packaging a thick but malleable frozen dessert and for dispensing it 20 under pressure in the expanded state substantially as herein described with reference to any one of the embodiments of the invention illustrated in the accompanying drawings and/or examples.
- 18. A thick but malleable frozen dessert packaged and dispensed under pressure in the expanded state by the method substantially as herein described with reference to any one 25 of the embodiments of the invention illustrated in the accompanying drawings and/or examples.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP02020949A EP1400486B1 (en) | 2002-09-19 | 2002-09-19 | Process for packaging and dispensing frozen desserts |
EP02020949.0 | 2002-09-19 | ||
PCT/EP2003/009852 WO2004026756A1 (en) | 2002-09-19 | 2003-09-05 | Method of packaging a frozen dessert |
Publications (2)
Publication Number | Publication Date |
---|---|
AU2003271582A1 AU2003271582A1 (en) | 2004-04-08 |
AU2003271582B2 true AU2003271582B2 (en) | 2010-07-29 |
Family
ID=31896884
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU2003271582A Ceased AU2003271582B2 (en) | 2002-09-19 | 2003-09-05 | Method of packaging a frozen dessert |
Country Status (17)
Country | Link |
---|---|
US (1) | US20060042192A1 (en) |
EP (1) | EP1400486B1 (en) |
JP (1) | JP2005538732A (en) |
CN (1) | CN100482090C (en) |
AT (1) | ATE503717T1 (en) |
AU (1) | AU2003271582B2 (en) |
BR (1) | BR0314626A (en) |
CA (1) | CA2496691C (en) |
DE (1) | DE60239610D1 (en) |
ES (1) | ES2361223T3 (en) |
IL (1) | IL166709A0 (en) |
MX (1) | MXPA05002558A (en) |
NZ (1) | NZ539427A (en) |
PL (1) | PL374640A1 (en) |
RU (1) | RU2005111549A (en) |
WO (1) | WO2004026756A1 (en) |
ZA (1) | ZA200503117B (en) |
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BE1018274A3 (en) * | 2008-08-29 | 2010-08-03 | Ryckewaert Jan Jozef | SYSTEM AND METHOD FOR STERILIZING FOODSTUFFS IN THE FINAL PACK. |
EP2358743B1 (en) | 2008-12-16 | 2012-10-10 | Unilever PLC | Method for extracting hydrophobin from a solution |
US8394444B2 (en) | 2009-05-29 | 2013-03-12 | Conopco, Inc. | Oil-in-water emulsion |
US8357420B2 (en) | 2009-05-29 | 2013-01-22 | Conopco, Inc. | Oil-in-water emulsion |
US20100303971A1 (en) * | 2009-06-02 | 2010-12-02 | Whitewave Services, Inc. | Producing foam and dispersing creamer and flavor through packaging |
EP2266418A1 (en) * | 2009-06-26 | 2010-12-29 | Nestec S.A. | Container having ingredients for preparing a frozen confection, container holder and device for preparing a frozen confection |
IT1404123B1 (en) * | 2011-02-28 | 2013-11-15 | Carpigiani Group Ali Spa | MACHINE FOR THE PRODUCTION AND DISTRIBUTION OF LIQUID, SEMILIQUED AND / OR SEMISOLIDED PRODUCTS. |
PT2685839E (en) | 2011-03-16 | 2015-10-27 | Unilever Nv | Apparatus and method for dispensing frozen confections |
AU2013224258B2 (en) | 2012-02-24 | 2015-11-19 | Unilever Ip Holdings B.V. | Method and apparatus for dispensing frozen confections |
CN108471772B (en) | 2016-01-08 | 2021-11-09 | 联合利华知识产权控股有限公司 | Apparatus for delivering a frozen confection comprising particulate material |
WO2017118521A1 (en) | 2016-01-08 | 2017-07-13 | Unilever Plc | Apparatus for delivering frozen confection comprising particulate material |
CN108033125B (en) * | 2017-12-28 | 2020-01-24 | 杭州汇杰胶粘剂有限公司 | Environment-friendly storage tank body device and using method and application thereof |
KR102164809B1 (en) * | 2018-05-17 | 2020-10-14 | (주)이너보틀 | Method for manufacturing contanier and apparatus for manufacturing contanier |
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- 2002-09-19 AT AT02020949T patent/ATE503717T1/en not_active IP Right Cessation
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- 2003-09-05 BR BR0314626-0A patent/BR0314626A/en not_active IP Right Cessation
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- 2003-09-05 IL IL16670903A patent/IL166709A0/en unknown
- 2003-09-05 CA CA2496691A patent/CA2496691C/en not_active Expired - Fee Related
- 2003-09-05 MX MXPA05002558A patent/MXPA05002558A/en unknown
- 2003-09-05 RU RU2005111549/12A patent/RU2005111549A/en not_active Application Discontinuation
- 2003-09-05 WO PCT/EP2003/009852 patent/WO2004026756A1/en active Application Filing
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Also Published As
Publication number | Publication date |
---|---|
PL374640A1 (en) | 2005-10-31 |
US20060042192A1 (en) | 2006-03-02 |
DE60239610D1 (en) | 2011-05-12 |
CN100482090C (en) | 2009-04-29 |
RU2005111549A (en) | 2005-09-20 |
CN1681732A (en) | 2005-10-12 |
CA2496691C (en) | 2012-12-11 |
ZA200503117B (en) | 2006-07-26 |
ES2361223T3 (en) | 2011-06-15 |
CA2496691A1 (en) | 2004-04-01 |
WO2004026756A1 (en) | 2004-04-01 |
NZ539427A (en) | 2007-07-27 |
MXPA05002558A (en) | 2006-04-28 |
EP1400486B1 (en) | 2011-03-30 |
IL166709A0 (en) | 2006-01-15 |
JP2005538732A (en) | 2005-12-22 |
AU2003271582A1 (en) | 2004-04-08 |
ATE503717T1 (en) | 2011-04-15 |
EP1400486A1 (en) | 2004-03-24 |
BR0314626A (en) | 2005-07-26 |
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Legal Events
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FGA | Letters patent sealed or granted (standard patent) | ||
PC | Assignment registered |
Owner name: AUSTRALASIAN FOOD GROUP PTY LTD. Free format text: FORMER OWNER WAS: NESTEC S.A. |
|
MK14 | Patent ceased section 143(a) (annual fees not paid) or expired |