WO1998013133A1 - Spray crystallised products and processes - Google Patents
Spray crystallised products and processes Download PDFInfo
- Publication number
- WO1998013133A1 WO1998013133A1 PCT/GB1997/002655 GB9702655W WO9813133A1 WO 1998013133 A1 WO1998013133 A1 WO 1998013133A1 GB 9702655 W GB9702655 W GB 9702655W WO 9813133 A1 WO9813133 A1 WO 9813133A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- substance
- liquid
- powder
- product
- fat
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 135
- 230000008569 process Effects 0.000 title claims description 21
- 239000007921 spray Substances 0.000 title claims description 21
- 239000000126 substance Substances 0.000 claims abstract description 163
- 239000007788 liquid Substances 0.000 claims abstract description 131
- 238000001816 cooling Methods 0.000 claims abstract description 36
- 239000002245 particle Substances 0.000 claims abstract description 36
- 239000007787 solid Substances 0.000 claims abstract description 32
- 239000000843 powder Substances 0.000 claims description 102
- 239000000203 mixture Substances 0.000 claims description 48
- 239000003925 fat Substances 0.000 claims description 47
- 235000019197 fats Nutrition 0.000 claims description 47
- 239000003921 oil Substances 0.000 claims description 38
- 239000001993 wax Substances 0.000 claims description 30
- 244000299461 Theobroma cacao Species 0.000 claims description 27
- 238000002156 mixing Methods 0.000 claims description 20
- 235000019219 chocolate Nutrition 0.000 claims description 17
- 235000014121 butter Nutrition 0.000 claims description 13
- 238000002425 crystallisation Methods 0.000 claims description 13
- 239000011782 vitamin Substances 0.000 claims description 13
- 229940088594 vitamin Drugs 0.000 claims description 13
- 229930003231 vitamin Natural products 0.000 claims description 13
- 235000013343 vitamin Nutrition 0.000 claims description 13
- 239000006071 cream Substances 0.000 claims description 11
- 239000013078 crystal Substances 0.000 claims description 11
- 239000003595 mist Substances 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 235000009470 Theobroma cacao Nutrition 0.000 claims description 10
- 239000000796 flavoring agent Substances 0.000 claims description 10
- 235000019634 flavors Nutrition 0.000 claims description 10
- 238000002844 melting Methods 0.000 claims description 9
- 230000008018 melting Effects 0.000 claims description 9
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 8
- 239000001301 oxygen Substances 0.000 claims description 8
- 229910052760 oxygen Inorganic materials 0.000 claims description 8
- 150000003722 vitamin derivatives Chemical class 0.000 claims description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 7
- 239000000839 emulsion Substances 0.000 claims description 7
- 235000013599 spices Nutrition 0.000 claims description 7
- 239000013526 supercooled liquid Substances 0.000 claims description 7
- 239000003570 air Substances 0.000 claims description 6
- 229940110456 cocoa butter Drugs 0.000 claims description 6
- 235000019868 cocoa butter Nutrition 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 6
- 238000005054 agglomeration Methods 0.000 claims description 5
- 230000002776 aggregation Effects 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 239000003755 preservative agent Substances 0.000 claims description 5
- 230000002335 preservative effect Effects 0.000 claims description 5
- 238000012545 processing Methods 0.000 claims description 5
- 239000001569 carbon dioxide Substances 0.000 claims description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 4
- 239000003995 emulsifying agent Substances 0.000 claims description 4
- 229920005989 resin Polymers 0.000 claims description 4
- 239000011347 resin Substances 0.000 claims description 4
- 238000000889 atomisation Methods 0.000 claims description 3
- 235000013312 flour Nutrition 0.000 claims description 3
- 230000002906 microbiologic effect Effects 0.000 claims description 3
- 229910052757 nitrogen Inorganic materials 0.000 claims description 3
- 229920002472 Starch Polymers 0.000 claims description 2
- 230000004075 alteration Effects 0.000 claims description 2
- 230000001427 coherent effect Effects 0.000 claims description 2
- 235000013365 dairy product Nutrition 0.000 claims description 2
- 239000000416 hydrocolloid Substances 0.000 claims description 2
- 235000019698 starch Nutrition 0.000 claims description 2
- 238000005496 tempering Methods 0.000 claims description 2
- 230000008901 benefit Effects 0.000 description 5
- 238000005538 encapsulation Methods 0.000 description 5
- 239000010985 leather Substances 0.000 description 5
- 239000005862 Whey Substances 0.000 description 3
- 102000007544 Whey Proteins Human genes 0.000 description 3
- 108010046377 Whey Proteins Proteins 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 230000015556 catabolic process Effects 0.000 description 3
- 238000006731 degradation reaction Methods 0.000 description 3
- 238000002194 freeze distillation Methods 0.000 description 3
- 238000004108 freeze drying Methods 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 235000015243 ice cream Nutrition 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000035515 penetration Effects 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- IIZPXYDJLKNOIY-JXPKJXOSSA-N 1-palmitoyl-2-arachidonoyl-sn-glycero-3-phosphocholine Chemical compound CCCCCCCCCCCCCCCC(=O)OC[C@H](COP([O-])(=O)OCC[N+](C)(C)C)OC(=O)CCC\C=C/C\C=C/C\C=C/C\C=C/CCCCC IIZPXYDJLKNOIY-JXPKJXOSSA-N 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 230000002301 combined effect Effects 0.000 description 1
- 210000002969 egg yolk Anatomy 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000000787 lecithin Substances 0.000 description 1
- 229940067606 lecithin Drugs 0.000 description 1
- 235000010445 lecithin Nutrition 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000010257 thawing Methods 0.000 description 1
- 239000002562 thickening agent Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B15/00—Solidifying fatty oils, fats, or waxes by physical processes
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23B—PRESERVATION OF FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES; CHEMICAL RIPENING OF FRUIT OR VEGETABLES
- A23B11/00—Preservation of milk or dairy products
- A23B11/30—Preservation of cream or cream preparations
- A23B11/302—Freezing; Subsequent melting
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23D—EDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS OR COOKING OILS
- A23D9/00—Other edible oils or fats, e.g. shortenings or cooking oils
- A23D9/02—Other edible oils or fats, e.g. shortenings or cooking oils characterised by the production or working-up
- A23D9/04—Working-up
- A23D9/05—Forming free-flowing pieces
-
- 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
- A23G1/00—Cocoa; Cocoa products, e.g. chocolate; Substitutes therefor
- A23G1/04—Apparatus specially adapted for manufacture or treatment of cocoa or cocoa products
- A23G1/042—Manufacture or treatment of liquids, creams, pastes, granules, shreds or powders
- A23G1/047—Transformation of liquids, pastes, creams, lumps, powders, granules or shreds into powders, granules or shreds; Manufacture or treatment of powders
-
- 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
- A23G1/00—Cocoa; Cocoa products, e.g. chocolate; Substitutes therefor
- A23G1/04—Apparatus specially adapted for manufacture or treatment of cocoa or cocoa products
- A23G1/18—Apparatus for conditioning chocolate masses for moulding
-
- 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
- A23G1/00—Cocoa; Cocoa products, e.g. chocolate; Substitutes therefor
- A23G1/30—Cocoa products, e.g. chocolate; Substitutes therefor
- A23G1/56—Liquid products; Solid products in the form of powders, flakes or granules for making liquid products, e.g. for making chocolate milk, drinks and the products for their preparation, pastes for spreading or milk crumb
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L15/00—Egg products; Preparation or treatment thereof
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L27/00—Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
- A23L27/70—Fixation, conservation, or encapsulation of flavouring agents
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
- A23L33/10—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
- A23L33/15—Vitamins
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
- A23P10/00—Shaping or working of foodstuffs characterised by the products
- A23P10/20—Agglomerating; Granulating; Tabletting
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
- A23P10/00—Shaping or working of foodstuffs characterised by the products
- A23P10/30—Encapsulation of particles, e.g. foodstuff additives
- A23P10/35—Encapsulation of particles, e.g. foodstuff additives with oils, lipids, monoglycerides or diglycerides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0004—Crystallisation cooling by heat exchange
- B01D9/0009—Crystallisation cooling by heat exchange by direct heat exchange with added cooling fluid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0018—Evaporation of components of the mixture to be separated
- B01D9/0027—Evaporation of components of the mixture to be separated by means of conveying fluid, e.g. spray-crystallisation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
- B01J2/006—Coating of the granules without description of the process or the device by which the granules are obtained
-
- 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
- A23G2200/00—COCOA; COCOA PRODUCTS, e.g. CHOCOLATE; SUBSTITUTES FOR COCOA OR COCOA PRODUCTS; CONFECTIONERY; CHEWING GUM; ICE-CREAM; PREPARATION THEREOF containing organic compounds, e.g. synthetic flavouring agents
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
Definitions
- the present invention relates to spray crystallised products and the processes for producing such products and, in particular, to new granulated fat and other products and methods.
- Cryogenic crystallisation of fats is known from EP 0393963 which describes apparatus and method for producing solid particles of fat for blending with dry ingredients such as animal feed.
- the method called spray crystallisation, involves using a high pressure pump to transfer liquid fat to a jet and using compressed air to atomise the stream into a fine mist.
- the atomised mist passes through a laser cut ring which sprays liquid nitrogen or carbon dioxide onto the mist so that the fat particles rapidly cool to produce crystals of fat.
- the resultant fat crystals are mixed, for example with whey powder or flour, to give dry, lump- free powder.
- a method of producing a granulated product having a soft texture comprising obtaining a substance in liquid form, the substance being solid at a given temperature, atomising the liquid substance, rapidly cooling the atomised liquid so that at least partially solid particles are formed and maintaining or returning the substance at or to substantially said given temperature so that said particles agglomerate to form a soft textured product.
- the method may include obtaining the substance in solid form and raising the temperature of the substance above said given temperature so that the substance melts to form a liquid.
- a soft textured product comprising an agglomeration of at least partially solid particles.
- particles are produced by spray crystallisation .
- a method of converting a substance which is solid at a given temperature to a substance which is soft textured at said given temperature comprising obtaining said substance in liquid form, atomising said liquid, rapidly cooling the atomised liquid to form at least partially solid particles and agglomerating said particles to form a coherent mass.
- the method may include obtaining the substance in solid form and melting said substance to form a liquid.
- the particles are agglomerated by maintaining or returning the particles at or to substantially said given temperature .
- the invention further provides an agglomerated product having a soft texture produced using a method of the invention.
- the substance may comprise a fat, oil and/or wax or a fat, oil and/or wax based composition.
- the substance may comprise a mixture of fats, oils and/or waxes or a mixture of fat, oil and/or wax and other components.
- the length of time for which said substance or particles are maintained at or returned to substantially said given temperature to cause agglomeration may depend on the substance used and the temperature.
- Said given temperature may be substantially ambient or room temperature.
- the atomising and rapid cooling is by means of spray crystallisation.
- the liquid substance is transferred to a jet by means of a high pressure pump.
- compressed air is used to atomise the stream of liquid into a mist.
- the atomised mist passes through a cryogenic cooling ring, where cryogenic liquid is introduced to rapidly cool the atomised mist.
- cryogenic liquid is sprayed onto the atomised mist.
- the cryogenic liquid comprises oxygen, nitrogen, air or carbon dioxide.
- the rapid cooling and agglomeration results in an alteration to the crystal structure of the substance.
- the process of the invention alters the substance from a solid to a soft textured product.
- the agglomerated product produced has several advantages due to its soft texture.
- the product can be used in mixes without requiring further
- a method of -producing a frozen or chilled powder product comprising obtaining a substance in liquid form, atomising the liquid substance, rapidly cooling the atomised liquid so that at least partially solid powder particles are formed and maintaining said powder at a temperature below room temperature.
- the method may include obtaining the substance in solid form and melting the substance to form a liquid.
- said powder is stored under substantially 5°C to give a chilled powder product or under substantially -18°C to give a frozen powder product, although it will be appreciated that the storing temperature may be chosen according to the required degree of cooling and the composition of the substance.
- the substance may comprise fat and/or oil such as butter, fractionated butters or cream.
- the frozen or chilled powder product produced has several advantages . Due to the soft nature of the powder produced, the product can be used straight from storage at chilled or deep freeze temperatures. For example, butter or butter mixes can be produced using this method which will spread straight from either the refrigerator or the freezer. It is believed that this technical effect is due to one or both of the following effects: the modification of the crystal structure during the process; the formation of powder particles with crystallised shells and super-cooled liquid centres.
- a frozen or chilled powder product comprising a plurality of powder particles having crystallised shells and super-cooled liquid centres.
- the powder particles may comprise fat and/or oil such as butter, fractioned butters or cream.
- the invention further provides a frozen or chilled powder product using the method of the invention.
- the frozen or chilled powder product can be mixed with powder in various mixes, for example in baking applications, and will have the advantages of behaving as a liquid in the mix and will improve the efficiency of the fat or other substance in the baking or other process due to the change in crystal structure which occurs as the super-cooled liquid centre crystallises when the temperature rises, for example during baking.
- the substance may comprise a substance which is solid at room temperature, typically a fat or oil based substance, and the method may include raising the temperature to melt the substance to form a liquid.
- the substance may comprise a substance which is liquid at room temperature.
- the substance may comprise a liquid egg based substance such as yolk, albumen, whole egg and/or mixtures thereof.
- the substance may comprise liquid butter and/or cream or other dairy substances or products and/or mixtures thereof.
- these substances can be processed into a frozen or chilled powder which is stored at frozen or chilled temperatures .
- Such base substances are normally damaged during the normal freezing process and the process of the invention minimises this damage.
- normal freezing of a liquid substance can cause the base substance to separate out and the water content to freeze separately.
- the spray crystallisation technique -of the invention inhibits this.
- the rate at which these products can be thawed is greatly increased when converted into a powder, so much so that the frozen powder can be introduced into a blender or mixer and mixes easily as it thaws.
- Thawing of a frozen powder product of the invention typically takes a few minutes in contrast to several hours for a normally frozen product of this kind to thaw into a usable product .
- liquid mixes such as ice cream mixes which can be processed by means of the method of the invention into a stable frozen powder.
- Such products can be consumed directly from the refrigerator or freezer and are sufficiently soft to consume immediately due to the combined effects of the crystal size and the supercooled liquid fractions.
- the products can be thawed to liquid in very short times either at ambient conditions or using microwaves. Some products have been shown to thaw to a liquid in a matter of seconds .
- the substance may comprise water so that using the method of the invention a frozen powder product can be produced which is a mixture of fine water crystals and supercooled liquid water.
- This product can be formed into various shapes or used for example to prepare an ice rink and the product freezes normally when the temperature rises in a controlled way.
- the frozen or chilled powder product produced can be shaped or handled more easily than a corresponding normally frozen product and can be caused to freeze normally by raising the temperature.
- the substance may comprise a sugar solution which is then processed into a frozen or chilled powder.
- a product can be used to modify or improve the rate at which certain solutions crystallise.
- Cream in the form of a frozen or chilled powder produced according to the fourth aspect of the invention or according to the fifth aspect of the invention can be further processed as follows : -
- the frozen powder may be mixed, for example using a high speed whisk, to change from frozen cream to butter and whey.
- the whey may be removed by passing both products over a mesh screen and the remaining solid material is butter.
- This process allows the raw material, i.e. cream, to be stored for extended periods, which is not possible with normally chilled cream, and still be capable of processing into butter.
- the additional benefit of this method is the fact that butter can be produced from a
- the frozen powder may be thawed under refrigeration i.e. at about 4 to 8°C and may then be whipped to give a comparable performance to cream that has been only chilled.
- frozen cream i.e. cream frozen by known methods, would not whip without the addition of stabilisers .
- a method of producing a powder product comprising mixing a first substance which is fat, oil and/or wax based with a second substance which is not fat, oil and/or wax based to form a liquid mixture, atomising the liquid mixture and rapidly cooling the atomised mixture so that at least partially solid powder particles are formed.
- the first and/or second substance may be melted or otherwise processed to form a liquid substance before, after or during the mixing.
- the substances are premixed at the melting stage.
- the first substance comprises fat, oil and/or wax.
- the second substance may comprise a liquid and/or a powder and may be fat, oil and/or wax soluble.
- the second substance may comprise a colour, flavour and/or vitamin substance.
- the second substance may comprise liquid flavour resins and/or emulsions, liquid colour resins and/or emulsions, liquid vitamins or vitamin emulsions, typically oil soluble vitamins.
- the method of the invention produces a stable powder with enhanced carrier protection against flavour and/or colour losses caused by moisture, oxygen and light. Also the release of v the active constituents, for example of the second substance, can be controlled by the fat mixture used.
- the method provides a stable powder product in which the powder substance is encapsulated by the first substance. Levels as high as 75% powder encapsulation have been achieved.
- the method allows the encapsulation of a variety of powders.
- the second substance may comprise a chemical in powder form.
- the method provides encapsulation of such chemicals either singly or in multiples and the release of these chemicals from the stable powder product produced can be controlled by the temperature required to melt the first substance.
- chemicals that would normally react with each other can be prevented from so reacting by processing according to the invention and due to the absence of water.
- the second substance may comprise a colour and/or flavour in powder form which can be encapsulated either singly or in multiples.
- the release of the colour and/or flavour from the stable powder product produced can be controlled by the temperature required to melt the first substance.
- the colours and/or flavours will have an added protection from degradation caused by moisture, oxygen and light.
- the second substance may comprise an unstable powder such as vitamins which can be encapsulated either singly or in multiples using the method of the invention.
- the release of the unstable powders involved can then be controlled by the temperature required to melt the first substance and again the powders will have an added protection from degradation caused by moisture, oxygen and light.
- the second substance may comprise one or more starches, flour and/or hydrocolloids typically in powder form with or without the addition of a suitable lecithin.
- the method provides encapsulation of such powders to provide a product with one or more of the following properties: the first substance coating allows these products to be mixed with hot or boiling liquids without subsequent lumping and poor mixing that normally occurs; the coating slows down the ability of the hot or boiling liquid to reach all of the thickening agent at once and this prevents lumps or particles of semi -dissolved or dispersed product being . formed. Additionally, the emulsion formed by mixing with hot liquid has enhanced viscosity caused by hydrogen bonding between the constituents which assists the stability of viscosity when the product is vigorously mixed. Thus, the method of the invention may include subsequent mixing with a hot or boiling liquid.
- the second substance may comprise an emulsifier and/or a preservative.
- the product produced by the method of the invention may be used for example in the leather industry.
- the product will be a stable powder at room temperature and will be more convenient to use, stable and will improve the oil/ fat/wax and preservative penetration into, for example, leather or the like.
- the second substance may comprise one or more spices or spice products, either in original form, milled or not milled, or blended with other ingredients such as salt.
- the encapsulation of the spice prevents attack from light, heat and oxygen and greatly reduces flavour loss.
- a high oil or first substance temperature typically in the region of 50 to 250°C, before or after the powders are added or the first and second substances are mixed, it is possible to reduce microbiological loading of the powder or second substance, for example of the spices or spice mixes, to an acceptable food grade level.
- the second substance may comprise one or more dried/freeze dried microbiological organisms, e.g. bacteria, yeasts, moulds or the like which can be encapsulated either singly or in multiples using the method of the invention.
- the rapid cooling would minimise further damage to these micro-organisms and the subsequently produced powders will have an added protection from degradation caused by moisture, oxygen and light.
- the release of these micro-organisms is controlled by the temperature required to melt the fat or by an interaction with a suitable enzyme.
- the invention includes a method of encapsulating a powder substance comprising the steps of mixing the powder substance with a fat, oil and/or wax based substance to form a liquid mixture, atomising the liquid mixture and rapidly cooling the atomised mixture.
- the substances and method may be substantially as described above.
- a method of producing a powder product adapted to be applied to a material such as leather comprising obtaining a liquid fat, oil and/or wax, atomising the liquid and rapidly cooling the atomised liquid so that a powder product is formed which is stable at room temperature.
- the product gives improved penetration when applied to leather or the like.
- the method may include mixing an emulsifier and/or a preservative with the liquid before atomisation.
- the method may include obtaining a fat, oil and/or wax in solid or other form and melting or otherwise processing it to form a liquid.
- the invention further provides a powder product formed using a method of the invention.
- a method of- treating a material such as leather or wooden and/or plastic surfaces comprising applying a powder product of the invention to a surface of the material, for example by rubbing.
- the powder may or may not be electrostatically charged.
- a method of encapsulating powder particles comprising mixing powder particles with a liquid substance to form a liquid mixture, atomising the liquid mixture and rapidly cooling the atomised mixture .
- the liquid substance comprises fat, oil and/or wax.
- a method of producing a vitamin product comprising mixing a vitamin based substance, either in liquid or powder form, with a liquid substance to form a liquid mixture, atomising the liquid mixture and rapidly cooling the atomised mixture.
- the liquid substance comprises fat, oil and/or wax.
- a method or producing a coloured and/or flavoured product comprising mixing a coloured and/or flavoured substance, either in liquid or powder form, with a liquid substance to form a liquid mixture, atomising the liquid mixture and rapidly cooling the atomised mixture.
- the liquid substance comprises fat, oil and/or wax .
- a method of making chocolate comprising obtaining cocoa butter or cocoa mass in liquid form, atomising the liquid, rapidly cooling the atomised liquid to form a powder and adding the powder during the chocolate making process ⁇ as part of the crumb making process or at the conching/tempering stage of chocolate production.
- This method assists in controlling and/or reducing the chocolate processing time due to the modification of the crystal structure of the cocoa butter or cocoa butter element.
- the invention includes chocolate made according to the above method.
- a method of producing a stable free flowing cocoa or chocolate based product comprising obtaining a cocoa or chocolate based liquid, atomising the liquid and rapidly cooling the atomised liquid to form a stable free flowing powder.
- the cocoa or chocolate based liquid may comprise fat and/or oil and/or mixtures such as cocoa butter, cocoa mass and various chocolate products.
- the product produced can be used as an ingredient in a variety of products such as in cereals, ice-cream, chocolate drinks, chilled products or the like.
- a fourteenth aspect of the invention there is provided a method of taking spray crystallised frozen powder, which may contain for example 5-95% water content, and introducing such powder directly to a freeze drier .
- this may facilitate the removal of this water more rapidly than usual and with reduced product damage during the freeze drying process .
- the invention includes products made according to any of the above described methods of the invention.
- the invention further provides apparatus for receiving a substance which is substantially solid at a given temperature, said apparatus comprising means for rapidly cooling said substance to produce a product which is substantially or relatively soft textured at said given temperature.
- said apparatus comprises means for atomising a liquid substance.
- the apparatus may comprise means for liquifying said solid substance.
- said substance is fat, oil and/or wax based, and preferably said soft textured product is spreadable.
- the substance may comprise any substance referred to herein.
- the invention further provides a product which has been at least partially solidified by spray crystallisation.
- such product is oleaginous.
- the steps of atomising and rapidly cooling in any of the methods described are preferably performed by conventional spray crystallisation techniques.
- a typical apparatus and method for performing spray crystallisation is described in EP 0393963 and the contents of that document are incorporated herein by reference.
- the atomisation may be by spraying and by means of an atomising nozzle through which liquid under pressure is pumped.
- the rate of spraying and size of the spray ejection apertures on the nozzle may be controlled or selected as desired to suit the particular requirements, for example depending on the nature of the liquid or mixture to be sprayed.
- the rapid cooling may be by means of directing one or more jets of cryogenic liquid, such as liquid nitrogen, oxygen, air or carbon dioxide, onto or towards the atomised spray.
- the size and arrangement of such jets may be controlled or selected as desired to suit the particular requirements and may be as
- the present invention is not intended to be restricted to the above embodiments which are described by way of example only.
- any features described and/or any of the steps of any method or process described may be combined in any combination and any features and/or steps described with reference to or defined by any aspect of the invention may be combined with any features and/or steps of any other aspect of the invention.
- the invention includes a method according to the first or fourth aspect of the invention comprising the further step of pre-mixing as described with reference to the sixth or ninth aspect of the invention.
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Polymers & Plastics (AREA)
- Food Science & Technology (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Nutrition Science (AREA)
- Crystallography & Structural Chemistry (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Wood Science & Technology (AREA)
- Thermal Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Mycology (AREA)
- Molecular Biology (AREA)
- Biophysics (AREA)
- Zoology (AREA)
- Fats And Perfumes (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Glanulating (AREA)
Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BR9711570-3A BR9711570A (en) | 1996-09-28 | 1997-09-26 | Products crystallized by spraying and processes |
CA002267275A CA2267275A1 (en) | 1996-09-28 | 1997-09-26 | Spray crystallised products and processes |
AU44676/97A AU4467697A (en) | 1996-09-28 | 1997-09-26 | Spray crystallised products and processes |
EP97943061A EP0934110A1 (en) | 1996-09-28 | 1997-09-26 | Spray crystallised products and processes |
PL97332631A PL332631A1 (en) | 1996-09-28 | 1997-09-26 | Spray-crystallised products and associated methods |
NO991537A NO991537L (en) | 1996-09-28 | 1999-03-29 | Spray crystallized products and processes |
Applications Claiming Priority (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GBGB9620294.0A GB9620294D0 (en) | 1996-09-28 | 1996-09-28 | Spray crystallised products and processes |
GB9620294.0 | 1996-09-28 | ||
GBGB9625413.1A GB9625413D0 (en) | 1996-09-28 | 1996-12-06 | Spray crystallised products and process |
GB9625413.1 | 1996-12-06 | ||
GBGB9702886.4A GB9702886D0 (en) | 1996-09-28 | 1997-02-12 | Spray crystallised products and processes |
GB9702886.4 | 1997-02-12 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1998013133A1 true WO1998013133A1 (en) | 1998-04-02 |
Family
ID=27268497
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/GB1997/002655 WO1998013133A1 (en) | 1996-09-28 | 1997-09-26 | Spray crystallised products and processes |
Country Status (8)
Country | Link |
---|---|
EP (1) | EP0934110A1 (en) |
AU (1) | AU4467697A (en) |
BR (1) | BR9711570A (en) |
CA (1) | CA2267275A1 (en) |
GB (1) | GB9702886D0 (en) |
NO (1) | NO991537L (en) |
PL (1) | PL332631A1 (en) |
WO (1) | WO1998013133A1 (en) |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1238589A1 (en) * | 2001-03-09 | 2002-09-11 | The BOC Group plc | Cryogenic processing methods and apparatus |
EP1285584A2 (en) | 2001-08-23 | 2003-02-26 | The BOC Group plc | Cryogenic crystallisation of fats |
WO2004008882A2 (en) * | 2002-07-18 | 2004-01-29 | Barry Callebaut A.G. | Gelatin substitute product and uses in food preparation |
AU785053B2 (en) * | 2000-01-06 | 2006-09-07 | Boc Group Plc, The | Preparation of food products |
WO2010099966A3 (en) * | 2009-03-06 | 2011-12-29 | Linde Aktiengesellschaft | Method for formulating cosmetics |
US20130192278A1 (en) * | 2010-09-29 | 2013-08-01 | Berend Jan Arends | Cryogenic spray process |
US9661864B2 (en) | 2005-02-17 | 2017-05-30 | Unilever Bcs Us, Inc. | Process for the preparation of a spreadable dispersion |
US9676150B2 (en) | 2011-08-10 | 2017-06-13 | British American Tobacco (Investments) Limited | Capsule formation |
US9924730B2 (en) | 2010-06-22 | 2018-03-27 | Unilever Bcs Us, Inc. | Edible fat powders |
US10219523B2 (en) | 2010-12-17 | 2019-03-05 | Upfield Us Inc. | Process of compacting a microporous fat powder and compacted fat powder so obtained |
US10238141B2 (en) | 2011-08-10 | 2019-03-26 | British American Tobacco (Investments) Limited | Capsule formation |
US11278038B2 (en) | 2003-07-17 | 2022-03-22 | Upfield Europe B.V. | Process for the preparation of an edible dispersion comprising oil and structuring agent |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2876249A1 (en) | 2004-10-11 | 2006-04-14 | Barry Callebaut Ag | Use of a cocoa butter e.g. to replace the dairy butter and oils in culinary preparations |
WO2018136064A1 (en) | 2017-01-19 | 2018-07-26 | Halliburton Energy Services, Inc. | Methods for controlling conductive aggregates |
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CH502834A (en) * | 1966-11-10 | 1971-02-15 | Nippon Shiryo Kogyo Kk | Spray crystallisation of microcrystalline su - pensions |
US3633283A (en) * | 1967-07-06 | 1972-01-11 | Nestle Sa Soc Ass Tech Prod | Drying apparatus |
US4281027A (en) * | 1978-11-10 | 1981-07-28 | Iwatani Sangyo Kabushiki Kaisha | Process for manufacturing cocoa powder |
EP0393963A2 (en) * | 1989-04-17 | 1990-10-24 | Canadian Oxygen Limited | Method and apparatus for cryogenic crystallization of fats |
EP0461930A1 (en) * | 1990-06-15 | 1991-12-18 | Merck & Co. Inc. | A crystallization method to improve crystal structure and size |
US5417153A (en) * | 1993-08-09 | 1995-05-23 | International Flavors & Fragrances Inc. | Fluidizing spray chilling system for producing encapsulated materials |
EP0709086A2 (en) * | 1994-10-28 | 1996-05-01 | Fuisz Technologies Ltd. | Discrete particles and method of making same |
-
1997
- 1997-02-12 GB GBGB9702886.4A patent/GB9702886D0/en active Pending
- 1997-09-26 PL PL97332631A patent/PL332631A1/en unknown
- 1997-09-26 BR BR9711570-3A patent/BR9711570A/en unknown
- 1997-09-26 CA CA002267275A patent/CA2267275A1/en not_active Abandoned
- 1997-09-26 EP EP97943061A patent/EP0934110A1/en not_active Withdrawn
- 1997-09-26 AU AU44676/97A patent/AU4467697A/en not_active Abandoned
- 1997-09-26 WO PCT/GB1997/002655 patent/WO1998013133A1/en not_active Application Discontinuation
-
1999
- 1999-03-29 NO NO991537A patent/NO991537L/en not_active Application Discontinuation
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CH502834A (en) * | 1966-11-10 | 1971-02-15 | Nippon Shiryo Kogyo Kk | Spray crystallisation of microcrystalline su - pensions |
US3633283A (en) * | 1967-07-06 | 1972-01-11 | Nestle Sa Soc Ass Tech Prod | Drying apparatus |
US4281027A (en) * | 1978-11-10 | 1981-07-28 | Iwatani Sangyo Kabushiki Kaisha | Process for manufacturing cocoa powder |
EP0393963A2 (en) * | 1989-04-17 | 1990-10-24 | Canadian Oxygen Limited | Method and apparatus for cryogenic crystallization of fats |
EP0461930A1 (en) * | 1990-06-15 | 1991-12-18 | Merck & Co. Inc. | A crystallization method to improve crystal structure and size |
US5417153A (en) * | 1993-08-09 | 1995-05-23 | International Flavors & Fragrances Inc. | Fluidizing spray chilling system for producing encapsulated materials |
EP0709086A2 (en) * | 1994-10-28 | 1996-05-01 | Fuisz Technologies Ltd. | Discrete particles and method of making same |
Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU785053B2 (en) * | 2000-01-06 | 2006-09-07 | Boc Group Plc, The | Preparation of food products |
EP1238589A1 (en) * | 2001-03-09 | 2002-09-11 | The BOC Group plc | Cryogenic processing methods and apparatus |
EP1285584A2 (en) | 2001-08-23 | 2003-02-26 | The BOC Group plc | Cryogenic crystallisation of fats |
EP1285584A3 (en) * | 2001-08-23 | 2003-03-12 | The BOC Group plc | Cryogenic crystallisation of fats |
AU2002300646B2 (en) * | 2001-08-23 | 2008-10-23 | The Boc Group Plc | Cryogenic crystallisation of solid fats |
WO2004008882A2 (en) * | 2002-07-18 | 2004-01-29 | Barry Callebaut A.G. | Gelatin substitute product and uses in food preparation |
WO2004008882A3 (en) * | 2002-07-18 | 2004-04-08 | Barry Callebaut A G | Gelatin substitute product and uses in food preparation |
US8932660B2 (en) * | 2002-07-18 | 2015-01-13 | Barry Callebaut Ag | Gelatin substitute product and uses in food preparation |
US11278038B2 (en) | 2003-07-17 | 2022-03-22 | Upfield Europe B.V. | Process for the preparation of an edible dispersion comprising oil and structuring agent |
US9661864B2 (en) | 2005-02-17 | 2017-05-30 | Unilever Bcs Us, Inc. | Process for the preparation of a spreadable dispersion |
WO2010099966A3 (en) * | 2009-03-06 | 2011-12-29 | Linde Aktiengesellschaft | Method for formulating cosmetics |
US9924730B2 (en) | 2010-06-22 | 2018-03-27 | Unilever Bcs Us, Inc. | Edible fat powders |
US20130192278A1 (en) * | 2010-09-29 | 2013-08-01 | Berend Jan Arends | Cryogenic spray process |
US9011951B2 (en) * | 2010-09-29 | 2015-04-21 | Conopco, Inc. | Cryogenic spray process |
US10219523B2 (en) | 2010-12-17 | 2019-03-05 | Upfield Us Inc. | Process of compacting a microporous fat powder and compacted fat powder so obtained |
US11071307B2 (en) | 2010-12-17 | 2021-07-27 | Upfield Europe B.V. | Process of compacting a microporous fat powder and compacted powder so obtained |
US9676150B2 (en) | 2011-08-10 | 2017-06-13 | British American Tobacco (Investments) Limited | Capsule formation |
US10238141B2 (en) | 2011-08-10 | 2019-03-26 | British American Tobacco (Investments) Limited | Capsule formation |
Also Published As
Publication number | Publication date |
---|---|
PL332631A1 (en) | 1999-09-27 |
CA2267275A1 (en) | 1998-04-02 |
EP0934110A1 (en) | 1999-08-11 |
BR9711570A (en) | 2001-07-24 |
NO991537L (en) | 1999-05-27 |
AU4467697A (en) | 1998-04-17 |
GB9702886D0 (en) | 1997-04-02 |
NO991537D0 (en) | 1999-03-29 |
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