USH1322H - Method for manufacturing dextrose grained confections - Google Patents
Method for manufacturing dextrose grained confections Download PDFInfo
- Publication number
- USH1322H USH1322H US07/818,657 US81865792A USH1322H US H1322 H USH1322 H US H1322H US 81865792 A US81865792 A US 81865792A US H1322 H USH1322 H US H1322H
- Authority
- US
- United States
- Prior art keywords
- dextrose
- syrup
- fructose
- whip
- mixture
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
- 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 title claims abstract description 84
- 239000008121 dextrose Substances 0.000 title claims abstract description 82
- 238000000034 method Methods 0.000 title claims abstract description 18
- 235000009508 confectionery Nutrition 0.000 title claims abstract description 16
- 238000004519 manufacturing process Methods 0.000 title abstract description 11
- 235000020357 syrup Nutrition 0.000 claims abstract description 93
- 239000006188 syrup Substances 0.000 claims abstract description 93
- 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 claims abstract description 83
- RFSUNEUAIZKAJO-ARQDHWQXSA-N Fructose Chemical compound OC[C@H]1O[C@](O)(CO)[C@@H](O)[C@@H]1O RFSUNEUAIZKAJO-ARQDHWQXSA-N 0.000 claims abstract description 42
- 229930091371 Fructose Natural products 0.000 claims abstract description 40
- 239000005715 Fructose Substances 0.000 claims abstract description 40
- 239000006185 dispersion Substances 0.000 claims abstract description 16
- 239000013078 crystal Substances 0.000 claims abstract description 12
- 239000007791 liquid phase Substances 0.000 claims abstract description 10
- 239000013081 microcrystal Substances 0.000 claims abstract description 9
- 238000010899 nucleation Methods 0.000 claims abstract description 9
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 4
- 239000000203 mixture Substances 0.000 claims description 54
- 235000015145 nougat Nutrition 0.000 claims description 28
- 235000003599 food sweetener Nutrition 0.000 claims description 26
- 239000003765 sweetening agent Substances 0.000 claims description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- 238000002156 mixing Methods 0.000 claims description 11
- 239000003795 chemical substances by application Substances 0.000 claims description 5
- 239000012071 phase Substances 0.000 claims description 2
- 239000007787 solid Substances 0.000 abstract description 5
- 238000003860 storage Methods 0.000 abstract description 2
- 244000299461 Theobroma cacao Species 0.000 description 21
- 235000019534 high fructose corn syrup Nutrition 0.000 description 21
- 239000004615 ingredient Substances 0.000 description 19
- 229920002472 Starch Polymers 0.000 description 17
- 235000019698 starch Nutrition 0.000 description 17
- 235000019219 chocolate Nutrition 0.000 description 14
- 239000000796 flavoring agent Substances 0.000 description 13
- 235000019634 flavors Nutrition 0.000 description 13
- 239000008107 starch Substances 0.000 description 13
- BJHIKXHVCXFQLS-UYFOZJQFSA-N keto-D-fructose Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)C(=O)CO BJHIKXHVCXFQLS-UYFOZJQFSA-N 0.000 description 12
- 240000008042 Zea mays Species 0.000 description 11
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 11
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 11
- 235000005822 corn Nutrition 0.000 description 11
- 238000004904 shortening Methods 0.000 description 11
- 244000235659 Rubus idaeus Species 0.000 description 10
- 238000002425 crystallisation Methods 0.000 description 10
- 230000008025 crystallization Effects 0.000 description 10
- 108010082495 Dietary Plant Proteins Proteins 0.000 description 9
- 238000003756 stirring Methods 0.000 description 8
- 235000009470 Theobroma cacao Nutrition 0.000 description 7
- 235000008504 concentrate Nutrition 0.000 description 7
- 239000012141 concentrate Substances 0.000 description 7
- 235000014510 cooky Nutrition 0.000 description 7
- 239000003925 fat Substances 0.000 description 7
- 235000019197 fats Nutrition 0.000 description 7
- 235000011034 Rubus glaucus Nutrition 0.000 description 6
- 235000009122 Rubus idaeus Nutrition 0.000 description 6
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- 229920002261 Corn starch Polymers 0.000 description 5
- 229930006000 Sucrose Natural products 0.000 description 5
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 5
- 238000005273 aeration Methods 0.000 description 5
- 238000010411 cooking Methods 0.000 description 5
- 239000008120 corn starch Substances 0.000 description 5
- 239000005720 sucrose Substances 0.000 description 5
- 235000014121 butter Nutrition 0.000 description 4
- 235000015810 grayleaf red raspberry Nutrition 0.000 description 4
- 238000010348 incorporation Methods 0.000 description 4
- 235000021579 juice concentrates Nutrition 0.000 description 4
- 235000013379 molasses Nutrition 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 235000006679 Mentha X verticillata Nutrition 0.000 description 3
- 235000002899 Mentha suaveolens Nutrition 0.000 description 3
- 235000001636 Mentha x rotundifolia Nutrition 0.000 description 3
- 235000018290 Musa x paradisiaca Nutrition 0.000 description 3
- LKDRXBCSQODPBY-ZXXMMSQZSA-N alpha-D-fructopyranose Chemical compound OC[C@]1(O)OC[C@@H](O)[C@@H](O)[C@@H]1O LKDRXBCSQODPBY-ZXXMMSQZSA-N 0.000 description 3
- 235000015895 biscuits Nutrition 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000011049 filling Methods 0.000 description 3
- 235000013305 food Nutrition 0.000 description 3
- 108090000623 proteins and genes Proteins 0.000 description 3
- 102000004169 proteins and genes Human genes 0.000 description 3
- 235000000346 sugar Nutrition 0.000 description 3
- 240000006890 Erythroxylum coca Species 0.000 description 2
- 241000234295 Musa Species 0.000 description 2
- 244000290333 Vanilla fragrans Species 0.000 description 2
- 235000009499 Vanilla fragrans Nutrition 0.000 description 2
- 235000012036 Vanilla tahitensis Nutrition 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 235000008957 cocaer Nutrition 0.000 description 2
- ZPUCINDJVBIVPJ-LJISPDSOSA-N cocaine Chemical compound O([C@H]1C[C@@H]2CC[C@@H](N2C)[C@H]1C(=O)OC)C(=O)C1=CC=CC=C1 ZPUCINDJVBIVPJ-LJISPDSOSA-N 0.000 description 2
- 239000013065 commercial product Substances 0.000 description 2
- 235000021433 fructose syrup Nutrition 0.000 description 2
- 230000002068 genetic effect Effects 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 150000004682 monohydrates Chemical class 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 235000019198 oils Nutrition 0.000 description 2
- 229940071440 soy protein isolate Drugs 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 150000008163 sugars Chemical class 0.000 description 2
- 230000008719 thickening Effects 0.000 description 2
- 239000008371 vanilla flavor Substances 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 229920000945 Amylopectin Polymers 0.000 description 1
- 229920000856 Amylose Polymers 0.000 description 1
- 229920002245 Dextrose equivalent Polymers 0.000 description 1
- 102000002322 Egg Proteins Human genes 0.000 description 1
- 108010000912 Egg Proteins Proteins 0.000 description 1
- 244000307700 Fragaria vesca Species 0.000 description 1
- 235000016623 Fragaria vesca Nutrition 0.000 description 1
- 235000011363 Fragaria x ananassa Nutrition 0.000 description 1
- 240000003183 Manihot esculenta Species 0.000 description 1
- 235000016735 Manihot esculenta subsp esculenta Nutrition 0.000 description 1
- 102000014171 Milk Proteins Human genes 0.000 description 1
- 108010011756 Milk Proteins Proteins 0.000 description 1
- 240000008790 Musa x paradisiaca Species 0.000 description 1
- 240000006394 Sorghum bicolor Species 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 235000020303 café frappé Nutrition 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 238000007385 chemical modification Methods 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 230000002255 enzymatic effect Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- -1 fatty acid triglycerides Chemical class 0.000 description 1
- 239000010685 fatty oil Substances 0.000 description 1
- 230000009969 flowable effect Effects 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 239000007970 homogeneous dispersion Substances 0.000 description 1
- 239000008172 hydrogenated vegetable oil Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000006317 isomerization reaction Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 239000008368 mint flavor Substances 0.000 description 1
- 238000004091 panning Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 235000014594 pastries Nutrition 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 239000002985 plastic film Substances 0.000 description 1
- 229920006255 plastic film Polymers 0.000 description 1
- 229920001592 potato starch Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000012460 protein solution Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 235000012094 sugar confectionery Nutrition 0.000 description 1
- 150000004043 trisaccharides Chemical class 0.000 description 1
- 235000013311 vegetables 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
- A23G3/00—Sweetmeats; Confectionery; Marzipan; Coated or filled products
- A23G3/34—Sweetmeats, confectionery or marzipan; Processes for the preparation thereof
- A23G3/36—Sweetmeats, confectionery or marzipan; Processes for the preparation thereof characterised by the composition containing organic or inorganic compounds
-
- 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
- A23G3/00—Sweetmeats; Confectionery; Marzipan; Coated or filled products
- A23G3/02—Apparatus specially adapted for manufacture or treatment of sweetmeats or confectionery; Accessories therefor
- A23G3/0205—Manufacture or treatment of liquids, pastes, creams, granules, shred or powder
-
- 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
- A23G3/00—Sweetmeats; Confectionery; Marzipan; Coated or filled products
- A23G3/34—Sweetmeats, confectionery or marzipan; Processes for the preparation thereof
- A23G3/36—Sweetmeats, confectionery or marzipan; Processes for the preparation thereof characterised by the composition containing organic or inorganic compounds
- A23G3/364—Sweetmeats, confectionery or marzipan; Processes for the preparation thereof characterised by the composition containing organic or inorganic compounds containing microorganisms or enzymes; containing paramedical or dietetical agents, e.g. vitamins
- A23G3/368—Sweetmeats, confectionery or marzipan; Processes for the preparation thereof characterised by the composition containing organic or inorganic compounds containing microorganisms or enzymes; containing paramedical or dietetical agents, e.g. vitamins containing vitamins, antibiotics
-
- 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
- A23G3/00—Sweetmeats; Confectionery; Marzipan; Coated or filled products
- A23G3/34—Sweetmeats, confectionery or marzipan; Processes for the preparation thereof
- A23G3/36—Sweetmeats, confectionery or marzipan; Processes for the preparation thereof characterised by the composition containing organic or inorganic compounds
- A23G3/38—Sucrose-free 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
- A23G3/00—Sweetmeats; Confectionery; Marzipan; Coated or filled products
- A23G3/34—Sweetmeats, confectionery or marzipan; Processes for the preparation thereof
- A23G3/36—Sweetmeats, confectionery or marzipan; Processes for the preparation thereof characterised by the composition containing organic or inorganic compounds
- A23G3/42—Sweetmeats, confectionery or marzipan; Processes for the preparation thereof characterised by the composition containing organic or inorganic compounds characterised by the carbohydrates used, e.g. polysaccharides
-
- 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
- A23G3/00—Sweetmeats; Confectionery; Marzipan; Coated or filled products
- A23G3/34—Sweetmeats, confectionery or marzipan; Processes for the preparation thereof
- A23G3/50—Sweetmeats, confectionery or marzipan; Processes for the preparation thereof characterised by shape, structure or physical form, e.g. products with supported structure
- A23G3/52—Aerated, foamed, cellular or porous products
Definitions
- This invention relates to a method useful in the manufacture of confections having a grained texture and which are derived from saccharide syrups, particularly fondants and nougats.
- glucose is included in the frappes that are usually incorporated in the fondant to form a creme.
- high fructose corn syrup or fructose in sugar confectionery in general is also disclosed by Minifie at pp. 481-482.
- British Patent No. 1,236,895 discloses the preparation of fondants containing dextrose in which a hot aqueous solution of dextrose and at least one sugar other than dextrose is cooled to crystallize dextrose therefrom.
- the patent discloses that crystallization may be induced by adding hydrated dextrose crystals.
- This invention relates to a method of preparing a dextrose grained nougat confection comprising:
- a mixture comprised of a sweetener syrup and a proteinaceous whipping agent, said sweetener syrup comprising dextrose and fructose and being supersaturated with respect to dextrose, but containing sufficient water to dissolve said whipping agent;
- a dextrose grained nougat confection having excellent organoleptic properties can be produced by seeding an aerated sweetener syrup containing dextrose and fructose with dextrose seed crystals.
- the fructose in the syrup is insufficient, in relation to the dextrose content and moisture content, to prohibit formation of dextrose microcrystals, but is sufficient to maintain a stable liquid phase upon storage of the confection.
- the first step in preparing a dextrose grained confection of this invention is obtaining a high solids sweetener syrup comprised of dextrose and fructose.
- the dextrose and fructose can be derived from a variety of sources.
- Dextrose is available commercially in the anhydrous or monohydrate crystalline form, or as a syrup, including syrups containing a mixture of dextrose and another material, e.g. high fructose corn syrup and 64 D.E. corn syrup.
- Dextrose is generally obtained by the hydrolysis of starch, e.g. from corn. The production and properties of dextrose and corn syrups are discussed by H. M. Pancoast et al., Handbook of Sugars, pp. 157-287 (AVI Publ. Co., Westport, Conn., 2d ed., 1980), the disclosure of which is incorporated by reference herein.
- Substantially pure dextrose, as crystalline monohydrate or high solids syrup e.g.
- Corn syrups are characterized by dextrose equivalent (D.E.) with the high conversion syrups having a high D.E. and a high concentration of dextrose. Lower conversion syrups may be useful, but are not preferred. Corn syrups are typically an inexpensive source of dextrose and thus may be a preferred source of dextrose for this reason.
- D.E. dextrose equivalent
- the fructose may be derived from crystalline fructose, a high fructose corn syrup, or an invert syrup. Crystalline fructose is also an item of commerce, but has historically been much less plentiful than dextrose and corn syrups. The crystallization of fructose is disclosed in U.S. Pat. Nos. 3,883,365 (Forsberg et al. ), 3,928,062 (Yamauchi), 4,199,374 (Dwivedi et al. ), and 4,643,773 (Day). Crystalline fructose is distinguished from materials containing significant amounts of amorphous fructose or corn syrup by-products, e.g., the semi-crystalline fructose disclosed in U.S. Pat. No.
- Crystalline fructose is available commercially at a purity in excess of 99.0% as the anhydrous crystalline form of beta-D-fructose, for example KRYSTAR® brand crystalline fructose available from A. E. Staley Manufacturing Company, Decatur, Ill.
- the fructose may also be obtained by the use of high fructose corn syrup or an invert syrup.
- high fructose corn syrup HFCS
- HFCS high fructose corn syrup
- d.s. dry solids
- 60% e.g., the two most common HFCS are at a nominal 42% or 55% d.s. fructose.
- High fructose corn syrups are items of commerce as disclosed by H. M. Pancoast et al., Handbook of Sugars, pp. 176-177 and 232-233.
- the Type A high fructose corn syrup referred to therein and having 42% d.s.
- fructose is the product of enzymatic isomerization of a glucose syrup that generally has from 5-8% higher saccharities (e.g. di-saccharides, tri-saccharides, and so on).
- the Type B high fructose syrup contains 55% d.s. fructose and is typically obtained by chromatographic fractionation of a Type A syrup, but can be obtained by other means of fructose enrichment of a Type A syrup (e.g. crystallization of dextrose from a Type A syrup).
- Invert syrup is obtained by the "inversion", i.e. hydrolysis, of sucrose.
- the dextrose and fructose are used to prepare a sweetener syrup that is supersaturated with respect to dextrose.
- the water used to prepare the syrup can be from any potable source or can be supplied by one of the sweetener syrups described above. Dry or liquid sweeteners can be combined in any order.
- Crystalline fructose and crystalline dextrose can be mixed with a syrup separately or premixed together before mixing with the syrup.
- the precise ratio of dextrose to fructose may vary widely depending upon the precise characteristics desired in the resulting product, but there will generally be a major amount by weight (e.g. more than 50% d.s.b.) of dextrose and a minor amount by weight (e.g.
- fructose e.g. a ratio of dextrose to fructose of from about 1.5:1 to about 2.5:1.
- the precise amount of water in the syrup will depend upon the ratio of dextrose to fructose and the texture desired of the resulting fondant, but will generally range from about 10% to about 20% by weight. If processing of the syrup will involve vaporization of a significant amount of the water, such vaporization should be taken into account in choosing the initial water content of the syrup.
- the dispersion Prior to incorporation of the resulting confectionary dispersion into a comestible product, and preferably prior to seeding with dextrose crystals, the dispersion may be mixed with a variety of functional ingredients. Such functional ingredients include flavors and colors of choice.
- the dispersion will be mixed with a proteinaceous whipping agent, such as a milk or egg protein or, preferably, a soy protein isolate, and then aerated.
- a suitable soy protein isolate is VERSA-WHIP® brand whipping protein from A. E. Staley Manufacturing Company, Decatur, Ill.
- a nougat will also typically contain a fat component comprised of a fat and/or oil, e.g.
- Typical fats and oils consist essentially of fatty acid triglycerides as discussed by T. H. Applewhite, "Fats and Fatty Oils", Encyclopedia of Chemical Technology, Vol. 9, pp. 795-831 (Kirk-Othmer, eds., John Wiley & Sons, Inc., N.Y., N.Y., 3rd ed., 1980), the disclosure of which is incorporated herein by reference.
- the aeration of the mixture suspends a gas, typically air, in the mixture to yield a texture characteristic of nougat.
- the degree of aeration will depend upon the texture desired of the resulting confection, but will typically range from about 0.2 to about 1.0 g/cc.
- a nougat for a biscuit cookie filling will typically have a density of about 0.55 to 0.6 and for a nougat deposited in a chocolate shell, a density of about 0.7 to 0.75.
- Aeration can be accomplished by a variety of methods, as discussed by Minifie, Chocolate, Cocoa and Confectionery, above, at pp. 474-476, the disclosure of which is incorporated herein by reference. Suitable methods of aeration include mechanical aeration either with a planetary beater at atmospheric pressure or by injection of pressurized air into a continuous pressure whisk.
- the dispersion may also contain a starch to provide thickening or a set to the dispersion.
- a starch capable of thickening or setting, as desired, is acceptable, but thin-boiling common starches are preferred.
- Common starches are known in the art to be conventional genetic varieties as opposed to unconventional genetic varieties having unconventional traits, e.g. waxy corn starch (essentially amylopectin) and high amylose corn starch.
- An especially preferred starch is SOFT-SET® corn starch, a commercial product of the A. E. Staley Manufacturing Company.
- Other suitable starches include unmodified (i.e. no chemical modification) and modified (e.g. substituted, crosslinked, thin-boiling, and oxidized) common tapioca and common potato starches.
- the starch of the mixture is gelatinized generally by cooking.
- Preferred mixtures contain "cook-up" starches which are gelatinized during a cooking period after mixing with the sweetener system.
- a preferred cook-up starch is MIRA-SET® 285, a commercial product of A. E. Staley Manufacturing Company, Cooking under atmospheric pressure in a heated vessel will simultaneously fully hydrate the starch and remove excess moisture. Pressure cooking can also be used, particularly when it is desired to minimize water loss from the mixture and reduce evaporation costs.
- the supersaturated syrup is seeded with dextrose crystals to initiate the crystallization of dextrose and thus form microcrystals of dextrose dispersed in a liquid phase.
- the precise particle size of the dextrose seed will vary depending upon the texture desired in the resulting confection, but will generally range from about 50 to about 100 micrometers.
- the seeding will be accomplished by mixing the seed with the syrup by means which obtain a substantially homogeneous dispersion of the dextrose seed throughout the syrup.
- the dispersion After seeding and incorporation of any functional ingredients, the dispersion is ready for incorporation into a comestible product.
- the dispersion can be deposited into a plurality of molds where it is allowed to firm or set. In molding, the bulk mixture, still in a flowable state, is divided among a number of molds.
- the molds can be of any construction suitable for the intended purpose.
- Starch molds can be employed. Starch molds are formed by making a plurality of depressions of the desired shape in a bed of starch.
- the dispersion can be directly incorporated into a food product. It can be used as the filling for a sandwich type cookie or deposited on a cookie base which is then coated or enrobed with chocolate or icing.
- the dispersion can itself be coated or enrobed in chocolate or other food coating. Techniques of filling, coating and/or enrobing are described in B. W. Minifie, Chocolate, Cocoa and Confectionery: Science and Technology, pp. 128-138, 142-179, and 401-414 (AVI Publ. Co., Westport, Conn., 1980, 2d ed.).
- the comestible article After incorporation, the comestible article will be stored for a limited time to allow completion of crystallization to the extent desired.
- the time required for completion of crystallization will depend upon the particular formulation chosen, but will generally be from about 10 minutes to about 24 hours.
- the temperature of the mixture during the crystallization period may vary, but will generally be close to ambient temperature to allow crystallization to proceed to the desired degree. In confections at high dry solids and with moderate dextrose levels, it may be desirable to heat seeded mixture to obtain the desired crystallization.
- Target density is 0.7-0.75.
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Inorganic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Molecular Biology (AREA)
- Microbiology (AREA)
- Confectionery (AREA)
Abstract
A method of manufacturing dextrose grained confections is provided. The confections are prepared from a high solids syrup comprised of dextrose and fructose, said syrup being supersaturated with respect to dextrose. The method comprises seeding said syrup with dextrose seed crystals and allowing dextrose to crystallize from said syrup onto said dextrose seed crystals to produce a dispersion of dextrose microcrystals dispersed in the liquid phase of said syrup. The resulting dispersion of microcrystals is incorporated into a comestible article in which moisture transfer from the dispersion to the surrounding environment is limited. The comestible article is stable upon storage because the amount of fructose in said syrup is insufficient to prohibit the formation of said microcrystals of dextrose, but is sufficient to maintain the stability of said liquid phase during said storing.
Description
This invention relates to a method useful in the manufacture of confections having a grained texture and which are derived from saccharide syrups, particularly fondants and nougats.
Processes and recipes for various confections, including fondants, cremes and the like, are disclosed and discussed by B. W. Minifie, Chocolate, Cocoa and Confectionery: Science and Technology, pp. 390-402, 424-425, and 481-483 (AVI Publ. Co., Westport Conn., 1980, 2d ed.). The use of sucrose along with dextrose (e.g. corn syrup) in making fondant and in remelting fondant in the making of a creme is disclosed. Specific recipes disclose the use of corn syrup having sucrose dissolved therein which are concentrated to supersaturate with respect to sucrose. The supersaturated syrup is then beaten to induce crystallization of the sucrose. It is also disclosed that glucose is included in the frappes that are usually incorporated in the fondant to form a creme. The use of high fructose corn syrup or fructose in sugar confectionery in general is also disclosed by Minifie at pp. 481-482.
British Patent No. 1,236,895 (Rostagno) discloses the preparation of fondants containing dextrose in which a hot aqueous solution of dextrose and at least one sugar other than dextrose is cooled to crystallize dextrose therefrom. The patent discloses that crystallization may be induced by adding hydrated dextrose crystals.
This invention relates to a method of preparing a dextrose grained nougat confection comprising:
preparing a mixture comprised of a sweetener syrup and a proteinaceous whipping agent, said sweetener syrup comprising dextrose and fructose and being supersaturated with respect to dextrose, but containing sufficient water to dissolve said whipping agent;
aerating the sweetener syrup of said mixture to disperse therein a discontinuous gas phase contained within a continuous aqueous liquid phase;
seeding said sweetener syrup with dextrose seed crystals and allowing dextrose to crystallize from said sweetener syrup onto said dextrose seed crystals to produce a dispersion of dextrose microcrystals dispersed in said aqueous liquid phase of said sweetener syrup;
incorporating said mixture after said aerating and seeding into a comestible article and storing said comestible article, wherein the amount of fructose in said sweetener syrup is insufficient to prohibit the formation of said microcrystals of dextrose, but is sufficient to maintain the stability of said aqueous liquid phase during said storing.
It has been found that a dextrose grained nougat confection having excellent organoleptic properties can be produced by seeding an aerated sweetener syrup containing dextrose and fructose with dextrose seed crystals. The fructose in the syrup is insufficient, in relation to the dextrose content and moisture content, to prohibit formation of dextrose microcrystals, but is sufficient to maintain a stable liquid phase upon storage of the confection.
The first step in preparing a dextrose grained confection of this invention is obtaining a high solids sweetener syrup comprised of dextrose and fructose. The dextrose and fructose can be derived from a variety of sources.
Dextrose is available commercially in the anhydrous or monohydrate crystalline form, or as a syrup, including syrups containing a mixture of dextrose and another material, e.g. high fructose corn syrup and 64 D.E. corn syrup. Dextrose is generally obtained by the hydrolysis of starch, e.g. from corn. The production and properties of dextrose and corn syrups are discussed by H. M. Pancoast et al., Handbook of Sugars, pp. 157-287 (AVI Publ. Co., Westport, Conn., 2d ed., 1980), the disclosure of which is incorporated by reference herein. Substantially pure dextrose, as crystalline monohydrate or high solids syrup (e.g. about 70% by weight) are preferred for use herein. Corn syrups are characterized by dextrose equivalent (D.E.) with the high conversion syrups having a high D.E. and a high concentration of dextrose. Lower conversion syrups may be useful, but are not preferred. Corn syrups are typically an inexpensive source of dextrose and thus may be a preferred source of dextrose for this reason.
The fructose may be derived from crystalline fructose, a high fructose corn syrup, or an invert syrup. Crystalline fructose is also an item of commerce, but has historically been much less plentiful than dextrose and corn syrups. The crystallization of fructose is disclosed in U.S. Pat. Nos. 3,883,365 (Forsberg et al. ), 3,928,062 (Yamauchi), 4,199,374 (Dwivedi et al. ), and 4,643,773 (Day). Crystalline fructose is distinguished from materials containing significant amounts of amorphous fructose or corn syrup by-products, e.g., the semi-crystalline fructose disclosed in U.S. Pat. No. 4,517,021 (Schollmeier) Crystalline fructose is available commercially at a purity in excess of 99.0% as the anhydrous crystalline form of beta-D-fructose, for example KRYSTAR® brand crystalline fructose available from A. E. Staley Manufacturing Company, Decatur, Ill.
The fructose may also be obtained by the use of high fructose corn syrup or an invert syrup. By "high fructose corn syrup" (HFCS) is meant a corn syrup containing at least about 40% fructose by weight of dry solids (d.s.), typically from about 40% to about 60% (e.g., the two most common HFCS are at a nominal 42% or 55% d.s. fructose). High fructose corn syrups are items of commerce as disclosed by H. M. Pancoast et al., Handbook of Sugars, pp. 176-177 and 232-233. The Type A high fructose corn syrup referred to therein and having 42% d.s. fructose is the product of enzymatic isomerization of a glucose syrup that generally has from 5-8% higher saccharities (e.g. di-saccharides, tri-saccharides, and so on). The Type B high fructose syrup contains 55% d.s. fructose and is typically obtained by chromatographic fractionation of a Type A syrup, but can be obtained by other means of fructose enrichment of a Type A syrup (e.g. crystallization of dextrose from a Type A syrup). Invert syrup is obtained by the "inversion", i.e. hydrolysis, of sucrose.
The dextrose and fructose are used to prepare a sweetener syrup that is supersaturated with respect to dextrose. The water used to prepare the syrup can be from any potable source or can be supplied by one of the sweetener syrups described above. Dry or liquid sweeteners can be combined in any order. Crystalline fructose and crystalline dextrose can be mixed with a syrup separately or premixed together before mixing with the syrup. The precise ratio of dextrose to fructose may vary widely depending upon the precise characteristics desired in the resulting product, but there will generally be a major amount by weight (e.g. more than 50% d.s.b.) of dextrose and a minor amount by weight (e.g. less than 50% by weight d.s.b. ) of fructose, e.g. a ratio of dextrose to fructose of from about 1.5:1 to about 2.5:1. The precise amount of water in the syrup will depend upon the ratio of dextrose to fructose and the texture desired of the resulting fondant, but will generally range from about 10% to about 20% by weight. If processing of the syrup will involve vaporization of a significant amount of the water, such vaporization should be taken into account in choosing the initial water content of the syrup.
Prior to incorporation of the resulting confectionary dispersion into a comestible product, and preferably prior to seeding with dextrose crystals, the dispersion may be mixed with a variety of functional ingredients. Such functional ingredients include flavors and colors of choice. In the case of a nougat, the dispersion will be mixed with a proteinaceous whipping agent, such as a milk or egg protein or, preferably, a soy protein isolate, and then aerated. A suitable soy protein isolate is VERSA-WHIP® brand whipping protein from A. E. Staley Manufacturing Company, Decatur, Ill. A nougat will also typically contain a fat component comprised of a fat and/or oil, e.g. a partially hydrogenated vegetable oil, in a minor amount, typically from about 5% to 10% by weight of the composition. Typical fats and oils consist essentially of fatty acid triglycerides as discussed by T. H. Applewhite, "Fats and Fatty Oils", Encyclopedia of Chemical Technology, Vol. 9, pp. 795-831 (Kirk-Othmer, eds., John Wiley & Sons, Inc., N.Y., N.Y., 3rd ed., 1980), the disclosure of which is incorporated herein by reference.
The aeration of the mixture suspends a gas, typically air, in the mixture to yield a texture characteristic of nougat. The degree of aeration will depend upon the texture desired of the resulting confection, but will typically range from about 0.2 to about 1.0 g/cc. A nougat for a biscuit cookie filling will typically have a density of about 0.55 to 0.6 and for a nougat deposited in a chocolate shell, a density of about 0.7 to 0.75. Aeration can be accomplished by a variety of methods, as discussed by Minifie, Chocolate, Cocoa and Confectionery, above, at pp. 474-476, the disclosure of which is incorporated herein by reference. Suitable methods of aeration include mechanical aeration either with a planetary beater at atmospheric pressure or by injection of pressurized air into a continuous pressure whisk.
The dispersion may also contain a starch to provide thickening or a set to the dispersion. Any type of starch capable of thickening or setting, as desired, is acceptable, but thin-boiling common starches are preferred. Common starches are known in the art to be conventional genetic varieties as opposed to unconventional genetic varieties having unconventional traits, e.g. waxy corn starch (essentially amylopectin) and high amylose corn starch. An especially preferred starch is SOFT-SET® corn starch, a commercial product of the A. E. Staley Manufacturing Company. Other suitable starches include unmodified (i.e. no chemical modification) and modified (e.g. substituted, crosslinked, thin-boiling, and oxidized) common tapioca and common potato starches.
The starch of the mixture is gelatinized generally by cooking. Preferred mixtures contain "cook-up" starches which are gelatinized during a cooking period after mixing with the sweetener system. A preferred cook-up starch is MIRA-SET® 285, a commercial product of A. E. Staley Manufacturing Company, Cooking under atmospheric pressure in a heated vessel will simultaneously fully hydrate the starch and remove excess moisture. Pressure cooking can also be used, particularly when it is desired to minimize water loss from the mixture and reduce evaporation costs.
The supersaturated syrup is seeded with dextrose crystals to initiate the crystallization of dextrose and thus form microcrystals of dextrose dispersed in a liquid phase. The precise particle size of the dextrose seed will vary depending upon the texture desired in the resulting confection, but will generally range from about 50 to about 100 micrometers. The seeding will be accomplished by mixing the seed with the syrup by means which obtain a substantially homogeneous dispersion of the dextrose seed throughout the syrup.
After seeding and incorporation of any functional ingredients, the dispersion is ready for incorporation into a comestible product. The dispersion can be deposited into a plurality of molds where it is allowed to firm or set. In molding, the bulk mixture, still in a flowable state, is divided among a number of molds. The molds can be of any construction suitable for the intended purpose. Starch molds can be employed. Starch molds are formed by making a plurality of depressions of the desired shape in a bed of starch.
The dispersion can be directly incorporated into a food product. It can be used as the filling for a sandwich type cookie or deposited on a cookie base which is then coated or enrobed with chocolate or icing. The dispersion can itself be coated or enrobed in chocolate or other food coating. Techniques of filling, coating and/or enrobing are described in B. W. Minifie, Chocolate, Cocoa and Confectionery: Science and Technology, pp. 128-138, 142-179, and 401-414 (AVI Publ. Co., Westport, Conn., 1980, 2d ed.).
After incorporation, the comestible article will be stored for a limited time to allow completion of crystallization to the extent desired. The time required for completion of crystallization will depend upon the particular formulation chosen, but will generally be from about 10 minutes to about 24 hours. The temperature of the mixture during the crystallization period may vary, but will generally be close to ambient temperature to allow crystallization to proceed to the desired degree. In confections at high dry solids and with moderate dextrose levels, it may be desirable to heat seeded mixture to obtain the desired crystallization.
The following examples will illustrate the invention, but should not be construed to limit the invention unless otherwise expressly noted. Those skilled in the art will understand that variations of the same may be made within the scope and spirit of the invention. In this specification and claims, all parts, percentages, ratios and the like are by weight unless otherwise indicated in context.
______________________________________
Ingredients Percent
______________________________________
Bob Syrup
ISOSWEET ® 180 high fructose corn syrup
66.10
(42% fructose, d.s.b. and 80% d.s.,
A. E. Staley Manufacturing Company)
STALEYDEX ® 333 crystalline dextrose
19.20
(A. E. Staley Manufacturing Company)
KRYSTAR 300 crystalline fructose
12.80
SOFT-SET corn starch 1.90
100.00
Nougat
Bob syrup 79.81
ISOSWEET 180 high fructose corn syrup
7.80
KAOMEL ® partially hydrogenated vegetable
5.20
shortening (Van den Bergh Foods)
Water 2.80
STALEYDEX ® 111 crystalline dextrose
2.60
(A. E. Staley Manufacturing Company)
VERSA-WHIP 500 vegetable protein
1.30
Color (1% solution W. J. 06515)
.45
Flavor (Flavors of N. America #877.010/WN)
.04
100.00
______________________________________
1. Cook bob syrup ingredients in steam jacketed kettle to 200° F. Remove from kettle.
2. Blend the VERSA-WHIP 500 in with the ISOSWEET 180, add the water and stir in well. Pour into large bowl of Hobart mixer.
3. Add bob syrup on top of VERSA-WHIP 500/ISOSWEET 180/water mixture and whip with wire whip on speed 3 for 1 minute. Take density.
4. Replace wire whip with paddle blade. Add color and flavor. Mix well on speed 1.
5. Slowly add melted KAOMEL in a steady stream. Mix well. Scrape bowl thoroughly.
6. Add STALEYDEX 111 (the seed) and mix well. Scrape bowl. Mix about 15-20 seconds more. Remove from mixer.
7. Take final density. Target density is 0.7-0.75.
8. Let nougat cool to 90° F. Deposit into chocolate shells.
______________________________________
Parts by
Ingredients Weight
______________________________________
Bob Syrup
KRYSTAR 300 crystalline fructose
1,680
STALEYDEX 333 crystalline dextrose
2,432
SOFT-SET corn starch 45
Water 483
Whipping Solution
KRYSTAR 300 crystalline fructose
150
VERSA-WHIP 500 vegetable protein
47
Water (at 130° F.)
137
After-Whip
Cocoa 94
KAOMEL shortening 377
STALEYDEX 111 crystalline dextrose
94
______________________________________
1. Add water and 1,080 parts by weight of KRYSTAR 300 to kettle and mix well (no heat).
2. Then add STALEYDEX 333. Mix in well and scrape down any hang-ups on the stirrer blades.
3. Add SOFT-SET starch and stir into cold syrup.
4. Heat the above to 185° F., then discontinue heat.
5. Add the remaining KRYSTAR and stir in.
1. Add KRYSTAR 300 to 37 parts by weight water and stir in.
2. Add protein and stir into smooth concentrate.
3. Add 100 parts by weight hot water and stir into smooth dilution.
1. Combine 2,717 parts by weight of hot bob syrup with 344 parts by weight of protein solution.
2. Using a 20 qt. bowl of Hobart mixer and paddle beater, whip on speed 2 for 4 minutes, then go to speed 3 for about 1 minute to density of 0.5-0.55.
1. Add cocoa powder and mix in for about 1 minute, scrape bowl to complete mixing.
2. Add shortening and mix in uniformly, about 1 minute.
3. Add seed dextrose and complete mixing.
4. Final density target is 0.55-0.6.
5. Pump and fill shells at 80°-90° F.
______________________________________
Ingredients Percent
______________________________________
Part I (Bob Syrup)
ISOSWEET 180 high fructose corn syrup
50.00
STALEYDEX 333 crystalline dextrose
25.00
KRYSTAR 300 crystalline fructose
25.00
100.00
Part II (Whipping Concentrate)
ISOSWEET 180 high fructose corn syrup
80.00
VERSA-WHIP 500 vegetable protein
20.00
100.00
Part III (Nougat)
Part I (bob syrup) 80.50
Part II (whipping concentrate)
6.50
KAOMEL shortening 7.50
STALEYDEX 111 crystalline dextrose
2.60
Red raspberry juice concentrate (68° Brix,
2.00
Sanofi Bio-Industries)
Natural raspberry flavor (WONF #11783,
.90
California Brands Flavors)
100.00
______________________________________
1. Heat part I 200° F. to dissolve sweeteners.
2. In part II, blend the VERSA-WHIP 500 in with ISOSWEET 180 until it is a smooth dispersion. Place in bowl of Hobart mixer.
3. Weigh part I on top of part II in bowl and whip for 11/2 minutes with a wire whip on speed 3. Target density is 0.7-0.75.
4. Add the red raspberry juice concentrate and raspberry flavor. Mix in well on speed 1.
5. Add the melted KAOMEL in a slow steady stream while mixing on speed 1.
6. Add the STALEYDEX 111 and mix in well on speed 1. Scrape down bowl and complete mixing until product looks uniform.
7. Remove from mixer. Let cool to 90° F. and fill into hollow chocolate shells.
______________________________________
Ingredients Percent
______________________________________
Part I (Bob Syrup)
ISOSWEET 180 high fructose corn syrup
50.00
STALEYDEX 333 crystalline dextrose
25.00
KRYSTAR 300 crystalline fructose
25.00
100.00
Part II (Whipping Concentrate)
ISOSWEET 180 high fructose corn syrup
80.00
VERSA-WHIP 500 vegetable protein
20.00
100.00
Part III (Nougat)
Part I (bob syrup) 80.50
Part II (whipping concentrate)
6.50
KAOMEL shortening 7.50
STALEYDEX 111 crystalline dextrose
2.60
Red raspberry juice concentrate (68° Brix,
2.00
Sanofi Bio-Industries)
Natural raspberry flavor (WONF #11783,
.90
California Brands Flavors)
100.00
______________________________________
1. Heat part I to 200° F. to dissolve sweeteners.
2. In part II, blend the VERSA-WHIP 500 in with ISOSWEET 180 until it is a smooth dispersion. Place in bowl of Hobart mixer.
3. Weigh part I on top of part II in bowl and whip for 2 minutes with a wire whip on speed 3. Target density is 0.55-0.6.
4. Add the red raspberry juice concentrate and raspberry flavor. Mix in well on speed 1.
5. Add the melted KAOMEL in a slow steady stream while mixing on speed 1.
6. Add the STALEYDEX 111 and mix in well on speed 1. Scrape down bowl and complete mixing until product looks uniform.
7. Fill pastry bag and top cookie bases with the fresh nougat.
8. Enrobe with chocolate or confectioner's coating.
______________________________________
Ingredients Percent
______________________________________
Bob Syrup
ISOSWEET 180 high fructose corn syrup
58.00
STALEYDEX 333 crystalline dextrose
20.00
KRYSTAR 300 crystalline fructose
22.00
100.00
Nougat
Bob syrup 76.00
KAOMEL shortening 7.50
ISOSWEET 180 high fructose corn syrup
5.20
STALEYDEX 111 crystalline dextrose
2.60
Coca 2.60
Butter (unsalted) 2.50
Molasses 2.00
VERSA-WHIP 500 vegetable protein
1.30
Vanilla flavor .30
100.00
______________________________________
1. Cook bob syrup ingredients in steam jacked kettle to 200° F. to dissolve sweeteners.
2. Blend VERSA-WHIP 500 with ISOSWEET 180 (5.20%) and put into large bowl of Hobart mixer.
3. Weigh bob syrup on top of VERSA-WHIP 500/ISOSWEET 180 blend. Whip with wire whip on speed 3 for 2 minutes. Target density is 0.55-0.6.
4. Add cocoa, vanilla and molasses. Mix in well. Scrape bowl.
5. Add melted fat (shortening and butter) in a slow steady stream. Mix in well. Scrape bowl.
6. Add STALEYDEX 111. Mix in well. Scrape bowl.
7. Remove from mixer. Deposit onto cookie wafer.
______________________________________
Ingredients Percent
______________________________________
Bob Syrup
ISOSWEET 180 high fructose corn syrup
50.00
STALEYDEX 333 crystalline dextrose
25.00
KRYSTAR 300 crystalline fructose
25.00
100.00
Nougat
Bob syrup 80.30
KAOMEL shortening 7.50
ISOSWEET 180 high fructose corn syrup
7.80
STALEYDEX 111 crystalline dextrose
2.60
VERSA-WHIP 500 vegetable protein
1.30
Mint green color .46
Natural and artificial mint flavor
.04
100.00
______________________________________
1. Cook bob syrup ingredients in steam jacketed kettle to 200° F. to dissolve sweeteners.
2. Blend the VERSA-WHIP 500 in with the ISOSWEET 180 for the nougat. Put into large bowl of Hobart mixer.
3. Weigh bob syrup on top of VERSA-WHIP 500/ISOSWEET 180 blend. Whip with wire whip on speed 3 for 80 seconds. Target density is 0.7-0.75.
4. Blend in flavor and color on speed 1 until mixed in.
5. Slowly add melted fat in a steady stream. Mix in well. Scrape bowl.
6. Add STALEYDEX 111 and mix in well. Scrape bowl.
7. Remove from mixer. Let cool to 90° F. and fill into hollow chocolate shells.
______________________________________
Ingredients Percent
______________________________________
Bob Syrup
ISOSWEET 180 high fructose corn syrup
58.00
STALEYDEX 333 crystalline dextrose
20.00
KRYSTAR 300 crystalline fructose
22.00
100.00
Nougat
Bob syrup 76.00
KAOMEL shortening 7.50
ISOSWEET 180 high fructose corn syrup
5.20
STALEYDEX 111 crystalline dextrose
2.60
Coca 2.60
Butter (unsalted) 2.50
Molasses 2.00
VERSA-WHIP 500 vegetable protein
1.30
Vanilla flavor .30
100.00
______________________________________
1. Cook bob syrup in steam jacketed kettle to 200° F. to dissolve sweeteners.
2. Blend VERSA-WHIP 500 with ISOSWEET 180 for the nougat and put into large bowl of Hobart mixer.
3. Weigh bob syrup on top of VERSA-WHIP 500/ISOSWEET 180 blend. Whip with wire whip on speed 3 for 80 seconds. Target density is 0.7-0.75.
4. Add cocoa, vanilla and molasses. Mix in well. Scrape bowl.
5. Add melted fat (shortening and butter) in a slow steady stream. Mix in well. Scrape bowl.
6. Add STALEYDEX 111. Mix in well. Scrape bowl.
7. Remove from mixer. Let cool to 90° F. and fill into hollow chocolate shells.
______________________________________
Ingredients Amount
______________________________________
Bob Syrup
SWEETOSE 43 corn syrup 1000 gm
STALEYDEX 333 crystalline dextrose
1600 gm
KRYSTAR 300 crystalline fructose
800 gm
Water 200 gm
Whipping Mixture
200° F. bob syrup 2000 gm
Banana puree @ 42° Brix
200 gm
VERSA-WHIP 500 vegetable protein
30 gm
After-Whip Addition
Banana flavor (natural, WONF #9/70A522,
2 ml
Dragoco, Inc.)
Yellow #5 (10% solution) artificial color
3 ml
Citric acid, fine crystals
5 gm
STALEYDEX 111 (seed) dextrose
60 gm
KAOMEL shortening (melted @ 110° F.)
60 gm
______________________________________
1. Heat ingredients for bob syrup to 260° F.-270° F. and then cool to 200° F.
2. Mix banana puree and VERSA-WHIP 500 protein to a smooth concentrate and add to hot bob syrup in 11 quart bowl of Hobart mixer.
3. Immediately whip for 3 minutes, using Hobart speed 3 and wire beater. Final density will be about 0.55.
4. Add after-whip ingredients in order listed with stirring on speed 1.
5. Lightly spray plastic sheeting with PAM cooking spray, pour mixture and size down to thickness between the plastic film and freeze for about 10 minutes (center temperature approximately 85° F.). Then cut into desired pieces, e.g. with circular knife.
______________________________________
Ingredients Amount
______________________________________
Bob Syrup
SWEETOSE 43 corn syrup 1000 gm
STALEYDEX 333 crystalline dextrose
2200 gm
KRYSTAR 300 crystalline fructose
400 gm
Whipping Mixture
250° F. bob syrup 2000 gm
ISOSWEET 180 high fructose syrup
100 gm
VERSA-WHIP 500 vegetable protein
30 gm
After-Whip Addition
Red #40 (10% soln.) artificial color
10 ml
Citric acid, fine crystals 15 gm
Strawberry flavor (Natural Type #9/70G199,
25 ml
Dragoco, Inc.)
STALEYDEX 111 (seed) dextrose
60 gm
______________________________________
1. Heat ingredients of bob syrup to 260° F.
2. Place hot bob syrup in 11 quart mixing bowl of Hobart mixer.
3. Mix ISOSWEET 180 and VERSA-WHIP 500 into smooth concentrate and add to hot bob syrup.
4. Immediately whip for 11/2 minutes, using Hobart speed 3 and wipe beater. Final density will be about 0.8.
5. Add after-whip ingredients in order listed with stirring at speed 1.
6. Deposit in dry, warm moulding starch. Hold hopper temperature at 200° F. Hold overnight (heat at 120°-130° F. hot room temperature if desired). Shake out, allow to cool, and pan with chocolate.
Claims (1)
1. A method of preparing a dextrose gained nougat confection comprising:
preparing a mixture comprised of a major amount of a sweetener syrup and a minor amount of a proteinaceous whipping agent, said sweetener syrup comprising dextrose and fructose and being supersaturated with respect to dextrose, but containing sufficient water to dissolve said whipping agent;
aerating the sweetener syrup of said mixture to disperse therein a discontinuous gas phase contained within a continuous aqueous liquid phase;
mixing said aerated sweetener syrup with a minor amount of a fat component to disperse said fat component therein;
seeding said aerated mixture of fat component and sweetener syrup with dextrose seed crystals and allowing dextrose to crystallize from said sweetener syrup onto said dextrose seed crystals to produce a dispersion of dextrose microcrystals dispersed in said aqueous liquid phase of said syrup;
incorporating said mixture after said aerating and seeding into a comestible article and storing said comestible article, wherein the amount of fructose in said sweetener syrup is insufficient to prohibit the formation of said microcrystals of dextrose, but is sufficient to maintain the stability of said aqueous liquid phase during said storing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/818,657 USH1322H (en) | 1992-01-08 | 1992-01-08 | Method for manufacturing dextrose grained confections |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/818,657 USH1322H (en) | 1992-01-08 | 1992-01-08 | Method for manufacturing dextrose grained confections |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| USH1322H true USH1322H (en) | 1994-06-07 |
Family
ID=25226082
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US07/818,657 Abandoned USH1322H (en) | 1992-01-08 | 1992-01-08 | Method for manufacturing dextrose grained confections |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | USH1322H (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6180158B1 (en) * | 1998-06-12 | 2001-01-30 | General Mills, Inc. | Process for aerated confection |
| US6387432B1 (en) * | 1998-06-12 | 2002-05-14 | General Mills, Inc. | Dried marshmallow methods of preparation for increasing bowl life |
| US6436455B2 (en) * | 1998-06-15 | 2002-08-20 | General Mills, Inc. | Multi-colored aerated confectionery products |
| EP1312266A1 (en) * | 2001-11-16 | 2003-05-21 | Unilever N.V. | Process for producing a sugar-containing, aerated product and product so prepared |
| US20030152678A1 (en) * | 2002-01-15 | 2003-08-14 | Mars, Incorporated | Method of chocolate coating soft confectionery centers |
| US20110008487A1 (en) * | 2008-03-03 | 2011-01-13 | Aude Bousquet | gelled food product with high carbohydrate intake efficiency |
-
1992
- 1992-01-08 US US07/818,657 patent/USH1322H/en not_active Abandoned
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6180158B1 (en) * | 1998-06-12 | 2001-01-30 | General Mills, Inc. | Process for aerated confection |
| US6387432B1 (en) * | 1998-06-12 | 2002-05-14 | General Mills, Inc. | Dried marshmallow methods of preparation for increasing bowl life |
| US6436455B2 (en) * | 1998-06-15 | 2002-08-20 | General Mills, Inc. | Multi-colored aerated confectionery products |
| EP1312266A1 (en) * | 2001-11-16 | 2003-05-21 | Unilever N.V. | Process for producing a sugar-containing, aerated product and product so prepared |
| US20030152678A1 (en) * | 2002-01-15 | 2003-08-14 | Mars, Incorporated | Method of chocolate coating soft confectionery centers |
| US7232584B2 (en) | 2002-01-15 | 2007-06-19 | Mars, Incorporated | Method of chocolate coating soft confectionery centers |
| US20110008487A1 (en) * | 2008-03-03 | 2011-01-13 | Aude Bousquet | gelled food product with high carbohydrate intake efficiency |
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