A PROCESS OF PREPARATION OF THE BACTERIA-FREE FOAMABLE OIL-IN-WATER EMULSION INCLUDING CHOCOLATE

Abstract: A bacteria-free foamable oil-in-water emulsion includ­ ing chocolate is prepared by forming emulsion containing (1) 15-50 wt% of oil, (2) 3-30 wt% of enzyme-treated choc­ olate component, (3) sodium caseinate, (4) defatted milk solid, (5) sugar component and (6) 3-10 wt% of emulsifier based on the oil and by sterilizing the said emulsion by heating at ultra high temperature. The bacteria-free foam­ able oil-in-water emulsion including chocolate has long time stability and high foamability, and it meets the current demand for baking or confectionary products having soft­ ness and wetness.

Description: A PROCESS OF PREPARATION OF THE BACTERIA-FREE FOABLE OIL-IN-WATER EMULSION INCLUDING CHOCOLATE BACKGROUND OF THE INVENTION (1) Field of the Invention The present invention relates a process for making creamy bacteria-free foamable oil-in-water emulsion including chocolate, which has long time stability and high foamability, and which meets the current demand for baking or confectionary products having softness and wetness. (2) Description of the Prior Art There are nany sorts of chocolate-including food products which comprise chocolate, raw cream, milk, nuts, and sugar, such as Ganache, Gianduya, Pralinen etc. Ganache is a mixture of chocolate and cream and /or ilk. Generally it is prepared by adding boiled cream or milk to melted chocolate, mixing the well, and leaving the mixture in cooling room for 24 hours before to use. Ganache is mainly used by painting or squeezing. It is possible to control Ganache softness by changing the ratio of chocolate. Gianduya is a paste which is prepared by kneading grinded mixture of equivalent nuts and sugar with chocolate, cocoa, and butter. Gianduya is used for coating on cakes, filling of chocolate cakes, and filling of cakes with butter cream. Pralinen is a sort of nugar. It is obvious that chocolate has wide varaety of applying fields and an important role as cake material. As entioned above, the softness of Ganache is controlled by changing chocolate ratio. It is remarkable that such control is now very popular. Recently there is a demand for confectionary products having softness and wetness. The tendency is the same with Ganache. Therefore, recent Ganache becomes softer and wetter by controlling aqueous phase to increase the contents of silk. In view of the situation, the inventors of the present invention studied Ganache and found following problems. Firstly, while chocolate itself has long stability for including little water and much sugar, Ganache including creai and milk has low stability on account of high-content of water and dairy products and lowlevel of sugar. This is because 102 - 103 /g of bacteria exist in chocolate and cacao mass. Secondary, it is difficult to obtain constantly the Ganache having desired softness by controling chocolate ratio. The third problem is that foamability of cream is lost when chocolate is mixed with boiled cream. Very soft Ganache is sometimes able to be whipped, but this is not for foamability of cream but for airation of mixing. Therefore, Ganache has never whip cream-milk foamability. Furthermore, the layer of whipped Ganache is easy to crack in the course of time. In attempt to avoid the undesirable effect of cracks, particularly in large fancy cakes, it has been commonly carried out that shaved chocolate is sprinkled over the surface of the cakes in order to prevent that purchaser's desire reduces when cracks are occured. SUMMARY OF THE INVENTION Inventors of the present invention seriously recognized aforenoted problems, especially crack problem that is very significant restriction using chocolate in the field of confectionary, and studied to solve these problems,, and accomplished the invention. The process of preparation of the bacteria-free foamable oil-in-water emulsion of the present invention comprises; (a) forming emulsion containing (1)'15 - 50 wt% of oil (2) 3 - 30 wt% of enzyme-treated chocolate component (3) sodium caseinate (4) defatted milk solid (5) sugar component (6) 3 - O wt of emulsifier based on the oil (b) sterilizing the said emulsion by heating at ultra high temperature. DETAILED DESCRIPTION OF THE INVENTION For the oil of the present invention, it is preferable to use the mixed oil of lauric acid type oil having 30 - 38t rising melting point and non lauric type oil. The mixed oil preferably comprises at least 20 wtZ (ore preferably 40 wtZ3 of lauric acid type oil. Using such preferable oil gives a good emulsion products having good foaiability and standup quality. As the lauric acid type oil that has 30 - 38 t rising melting point, there are, for example, coconut oil, palm kernel oil, and their hardened oil, their fractionated oil, their ester-exchanged oil. As the non lauric acid type oil, there are represented animal oil, vegitable oil, their hardened oil, their mixed oil or their various processed oil. Such non lauric acid type oil preferably has 20 - 55 SFI at 10 C and 25 - 40C rising melting point. Examples of the non lauric acid type oil are fish oil, whale oil, rape seed oil, their hardened oil, their fractionated oil, their ester-exchanged oil. It is particularly preferred in the present invention to use the mixed oil including 5 - 30 wt% of saturated of unsaturated fatty acid (including higher unsaturated fatty acid) that has more than 20 carbon atoms in the whole structured fatty acid. On the cakes using emulsion products of above defined oil, no cracks occur in the course of time. The content of the oil is 15 - 50 wtX in the whole emultion of the present invention. If the content is below 15 wt%, standup quality becomes weak, and if the content is over 50 wt%, the emulsion solidifies like brick and becomes unfoamable to lose practical utility. The enzyme-treated chocolate component used in the present invention is obtained by adding enzyme to 20 - 50 % aqueous chocolate solution, stirring at 20 - 90 , preferably 40 - 70t, for 0.2 - 15 hours, and if necessary, removing water by adequate means. As the chocolate used in the present invention, there are, for example, cacao mass, cacao butter, cacao powder, sweet chocolate, milk chocolate, cover chocolate. Such chocolate includes hydrocarbon as solid component. The suitable enzyme used in the present invention is amylase, for example, cc -amylase, 8 -amylase, glucoamylase, or combination of them. It is preferable to add 5 - 1000 DUN of 2-amylase to 1 g of chocolate, 10 - 1000 AUN of ss-amylase to 1 g of chocolate, 3 - 1000 U of glucoamylase to 1 g of chocolate. When combination of amylases is used, it is preferable to add the said amount of each amylase. Activity of enzyme to 1 g of chocolate (A) is calculated by following formula: (A) = (activity) X (the amount of added amylase) X 0.01 where activity is mesured by dextrinogenic unit of Nagase (cc-amylase), amylolytic unit of Nagase (ss- amylase), Somogyi-Nelson (glucoamylase), and the amount of added amylase is weight percernt based on solid chocolate. The enzyme-treated chocolate components can be selected according to desired flavor. It is possible to select as the need of the demand one or combination of chocolate such as cacao butter, cacao mass, cacao powder, sweet chocolate, milk chocolate, cover chocolate to create desired flavor and taste. It is desirable to include 25 wt% of cacao butter in the whole chocolate component to obtain good flavor and taste. The content of the chocolate component is 3 - 30 wt% in the whole emulsion of the present invention. If the content is below 3 wt%, the chocolate flavor of the emulsion is too weak, and if the content is over 30 wtX, the balance between the chocolate component and other components in the emulsion destroyes to be unable to obtain a desired flavor product. As the suitable sugar component used in the present invention, there are, for example, sucrose (cane sugar), fructose (fruit sugar), maltose (malt sugar), dextrose (grape sugar), liquid sugar, glucose syrup (mizuame). The selection of the sugar component mainly depends on the selection of the chocolate component. The desirable content of the sugar is 10 - 30 wtX in the whole emulsion of the present invention. If the content of the sugar component is below 10 wtZ, the emulsion has strong bitterness to be unable to obtain a mild flavor product, and if the content is over 30 wt%, the emulsion has over sweetness and insufficient foamability. Sodium caseinate is effective to maintenance of the emulsion structure. The effect of sodium caseinate is exhibited in the range of 0.5 - 4 wt in the whole emulsion of the present invention. If the content of sodium caseinate is below 0.5 wt%, the effect is not found, if the content is over 4 wt%, the flavor of sodium caseinate harms the flavor of the chocolate. As the defatted milk solid used in the present invention, there are, for example, milk, defatted milk, skim milk powder, whey powder, or soybean protein. The suitable content of the defatted milk solid is 2 - 6 wt% in the whole emulsion of the present invention. If the content of the defatted milk solid is below 2 wt%, the effect of the defatted milk solik is insufficient, and if the content is over 6 wt%, the emulsion has too strong milk flavor. The range (2 - 6 wtX) of the defatted milk solid in the whole emulsion emphasises the flavor of chocolate. As the emulsifier used in the present invention, there are, for exmaple, lecithin, monoglyceride, sorbitan fatty acid ester, propylene glycol fatty acid ester1 sugar fatty acid ester, polyglycerol fatty acid ester, polyoxyethylene fatty acid ester, polyoxyethylene sorbitan fatty acid ester, glycerol or polyglycerol condensed fatty acid ester. It is preferred to use the combination of hydrophiric emulsifier and lipophiric emulsifier, particularly preferred the combination of lecithin and monoglyceride and third emulsifier(s) which is one or more selected from the group comprising sugar fatty acid ester, polyoxyethylene fatty acid ester, polyoxyethylene sorbitan fatty acid ester, and polyglycerol fatty acid ester. The content of the emulsifier is needed 3 - 10 wt% based on the oil of the present invention. If the content of the emulsifier is below 3 wt% as conventional, it is obtained unfoamable emulsion or low foamable emulsion which has plasticity not to obtain topping satisfactory in standup quality. If the content is over 10 wtZ, the emulsion has high viscocity and causes plasticization. The more preferable content of the emulsifier is 6 - 7 wt% based on the oil of the present invention. In the present invention, if necessary, it is possible to add stabilizer during preparing the emulsion. As the suitable stabilizer, there are, for example, locust bean gum, carrageenan, gelatin, crystalline cellulose, xanthen gum. Especially, crystalline cellulose is preferable for its palatable taste. The preferable content of the stabilizer is 0.05 - 3 wt% in the whole emulsion of the present invention. It is known to add phosphoric acid salts to the creamy emulsion. In the present invention, it is possible to add phosphoric acid salts to the emulsion. As the suitable phosphoric acid salts, there are, for example, sodium polyphosphate, sodium metaphosphate, sodium orthophosphate, sodium pyrophosphate, or the combination of them. Especially, sodium tripolyphosphate, sodium hexametaphosphate, trisodium orthophosphate are preferable. The preferable content of the phosphoric acid salt is 0.02 - 0.1 wt% in the whole emulsion of the present invention. In production of the emulsion of the present invention, these components are emulsified under conventional oil-in-water emulsion preparing conditions. At this time, it is preferable to contain 40 - 60 wtZ of solid components in the whole emulsion. The resulted emulsion is subjected to the process of sterilizing by heating at ultra high temperature (UHT sterilizing process). The UHT sterilizing process is able to carry out by means of commercial UHT sterilizing equipments. As the suitable indirect heating type UllT sterilizing equipments, there are, for example, APV Ultramatic UHT Treatment System (The A.P.V. Company LTD), Thermutator UHT System (Cherry Burrell), Sterideal UHT System (Stork), Contherm Scraped-Surface Heat Exchange System (ALFA-LAVAL), and as the suitable direct heating type UHT sterilizing equipments, there are, for example, APV Uperisation Continuous Sterilization System (The A.P.V. Company LTD), VTIS Sterilizing plant (ALFA-LAVAL), Laguiharre UHT System (Laguiharre), Pararisator UHT System (Paash Silkeborg), Vac-Heat UHT System (Crepaco). The preferable embodiment of the present invention is as follows. Oil phase is obtained by adding lipophiric emulsifier to the oil which comprises at least 20 wt% lauric acid type oil that has rising melting point of 30 - 38t and including 5 - 30% saturated or unsaturated fatty acid that has more than 20 carbon atoms in the whole structured fatty acid, and solubilizing by heating. Aqueous phase is obtained by adding and dissolving the hydrophilic emulsifier, the enzyme-treated chocolate component, the sodium caseinate, the defatted milk solid, the sugar component, and the phosphoric acid salts, the stabilizer if necessary, at the ratio above-mentioned to water. 15 - 50 weight parts of oil phase and 85 - 50 weight parts of aqueous phase are mixed in the mixing chamber to obtain oil-in-water pre-emulsion. Resulted pre-emulsion is homogenized in the homogenizer to obtain oil-in-water emulsion. It is able to use various type of homogenizers such as highpressure homogenizer, centrifuge homogenizer, ultrasonic homogenizer in the present invention. Especially, preferable homogenizer in the invention is high-pressure homogenizer. In the case of using high-pressure homogenizer, the homogenize pressure is important. In the present invention, the preferable pressure is about 50 - 100 kg/ ci. Resulted homogenized emulsion is sterilized in UHT sterilizing equipment, again homogenized under the pressure 10 - 50 kg/d, cooled to about 5t, packed into proper containers such as @ tetra pack containers under the condition without bacteria to obtian the emulsion product of the present invention. The bacteria-free foamable oil-in-water emulsion of the present invention can be widely used as chocolate materials for various purposes, namely for kneading as it is, for nappe on whipping, for topping on whipping and plasticising, and for filling. The softness of the product can be controlled without changing chocolate ratio. In the process of the present invention, it is unnecessary to boil cream. For the product of the present invention is bacteria-free, it can be used in any cases sanitarily. The whipped bacteriafree foamable oil-in-water emulsion of the present invention has no cracks for 3 - 5 days after nappe and topping on the fancy cakes and leaving at 15Y, or after nappe and topping on the fancy cakes and freezing at -25 t for 2 - 4 weeks and melting at 10 t and leaving at 15t. On the contrary the conventional products has cracks for 1 day under the same conditions. The emulsion products of the present invention have long storage life and commercially high-value. Further, according to the process of the present invention, even if a large quantity of chocolate component is used, by using the enzyme-treated chocolate component as the chocolate component, the viscosity of the emulsion can be controlled in the low level and thereby the UHT sterilizing process and the homogenizing process can be conducted very easily. The present invention is further illustrated by the following examples. EXAMPLES Oil phase was prepared by melting at 70t 25 parts of hardened cotton seed oil haivng rising melting point 35t, and adding 0.4 part of glycerine fatty acid ester (iodine value 20), and 0.5 part of lecithin. Enzyme-treated cacao mass ws prepared by adding cc-amylase (SPITASE cp-l NAGASE SANGYO) at rate of 10 DUN to 1 g of cacao mass, stirring for 2 hours at 65t , removing water by freez-drying. Aqueous phase was prepared by adding and dissolving 0.4 part of sugar fatty acid ester (HLB 11), 3 parts of skim milk powder, 0.6 part of sodium caseinate, 15 parts of enzyme-treated cacao mass, 15 parts of sucrose, 0.1 part of crystalline cellulose, and 0.1 part of sodium hexametaphosphate to 40 parts of water. Aqueous phase was heated to 40 'C, C, and mixed with oil phase. The mixture was agitated by the propeller agitator at about 50t for 10 - 15 minutes to obtain pre-emulsion. Resulted pre-emulsion was homogenized by homogenizer on the pressure of 100 kg/ a to obtain oil-in-water emulsion. The oil-inwater emulsion was maintained at about 50 C and sterilized by VTIS sterilizing plant (ALFA LAVAL) at 140 for 2 seconds, and again homogenized by homogenizer, and cooled at aobut 5 t to obtain the bacteria-free foamable oil-in-water emulsion of the present invention (emulsion product No. 1 in Table 1). Emulsion products No. 2 - 5 which have various emulsion components were prepared by using the same operation conditions as emulsion product No. 1 (in Tabel 1). Emulsion products No. 1 - 5 were aged in the refrigerator for 20 hours. Tests results of emulsion products No. 1 - 5 are shown in Table 2. The viscocity of emulsion products No. 1 - 5 did not rise after 3 months leaving at 5t. 500 ml of each emulsion products No. 1 - 5 was whipped by whipper. Every whipped product had good foamability. Fancy cakes having 18 cm diameter were made of such whipped products and other cake materials. After leaving cakes at 15 t for 5 days, no cracks were found, and their colour, flavor, and shape did not change. After freezing the cake at -25 c for 2 weeks, then melting them at lOc for 6 hours, and leaving them at 15C for 3 days, the state of cakes was good as first. COMPARATIVE EXAMPLES The emulsion products No. 6 - 8 which are not included in the present invention were prepared using the same operation conditions described above. In these emulsion products, viscosity rised in the course of time, foamability was low, the balance of flavors was lost and only chocolate flavor was exaggerated. Work efficiency of making cakes with these emusion products was low. Coating whipped products on cakes is difficult. After leaving or freezing them as described above, the colour of cakes turned brown-black. As a consequence, the commercial value of these emulsion products was very low. Table 1 EMI16.1 No. <SEP> 1 <SEP> No. <SEP> 2 <SEP> No. <SEP> 3 <SEP> No. <SEP> 4 <SEP> No. <SEP> 5 <SEP> No. <SEP> 6 <SEP> No. <SEP> 7 <SEP> No. <SEP> 8 <tb> Oil <SEP> composition <tb> hardened <SEP> cotton <SEP> seed <SEP> oil <SEP> (1) <SEP> 25 <SEP> 15 <SEP> 15 <SEP> 40 <SEP> 30 <SEP> 20 <tb> hardened <SEP> coconut <SEP> oil <SEP> (2) <SEP> 25 <SEP> 15 <SEP> 30 <tb> Chocolate <SEP> component <tb> &alpha; <SEP> - <SEP> amylase <SEP> treated <SEP> cacao <SEP> mass <SEP> (3) <SEP> 15 <tb> ss <SEP> - <SEP> amylase <SEP> treated <SEP> cacao <SEP> powder <SEP> (4) <SEP> 10 <SEP> 5 <tb> gluco-amylase <SEP> treated <SEP> cacao <SEP> powder <SEP> (5) <SEP> 5 <SEP> 5 <SEP> 20 <tb> &alpha; <SEP> - <SEP> amylase, <SEP> ss <SEP> - <SEP> amylase <SEP> treated <SEP> sweet <SEP> chocolate <SEP> (6) <SEP> 30 <SEP> 3 <tb> non <SEP> enzyme <SEP> treated <SEP> cacao <SEP> powder <SEP> 15 <tb> Sodium <SEP> caseinate <SEP> 0.6 <SEP> 0.6 <SEP> 2 <SEP> 1 <SEP> 1 <SEP> 0.6 <SEP> 1 <SEP> 0.2 <tb> Defatted <SEP> milk <SEP> solid <tb> defatted <SEP> skim <SEP> milk <SEP> powder <SEP> 3 <SEP> 4 <SEP> 3 <SEP> 2 <SEP> 0.2 <tb> soybean <SEP> protein <SEP> 2 <SEP> 1 <SEP> 3 <SEP> 1 <tb> Sugar <SEP> components <tb> sucrose <SEP> 15 <SEP> 8 <SEP> 20 <SEP> 10 <SEP> 15 <SEP> 20 <SEP> 20 <tb> fluctose <SEP> 8 <SEP> 15 <tb> Emulsifier <tb> lecithin <SEP> 0.4 <SEP> 1 <SEP> 0.2 <SEP> 0.6 <SEP> 0.4 <SEP> 0.5 <SEP> 0.3 <SEP> 0.5 <tb> glyceline <SEP> fatty <SEP> acid <SEP> ester <SEP> (Iodine <SEP> value <SEP> 20) <SEP> 0.4 <SEP> 0.5 <SEP> 0.3 <SEP> 0.7 <SEP> 1 <SEP> 0.6 <SEP> 0.3 <SEP> 0.5 <tb> sugar <SEP> fatty <SEP> acid <SEP> ester <SEP> (HLB <SEP> 11) <SEP> 0.4 <SEP> 0.2 <SEP> 0.4 <SEP> 0.1 <SEP> 0.3 <SEP> 0.1 <SEP> 0.4 <tb> polyoxyethylene <SEP> (8) <SEP> stealate <SEP> (HLB <SEP> 11) <SEP> 0.2 <SEP> 0.1 <SEP> 0.3 <tb> polyglyceline <SEP> fatty <SEP> acid <SEP> ester <SEP> (HLB <SEP> 10.5) <SEP> 0.3 <SEP> 0.2 <SEP> 0.1 <SEP> 0.3 <tb> Cristalline <SEP> sellulose <SEP> 0.1 <SEP> 0.1 <SEP> 0.1 <SEP> 0.05 <SEP> 0.1 <SEP> 0.1 <SEP> 0.1 <tb> Sodium <SEP> hexametaphosphate <SEP> 0.1 <SEP> 0.1 <SEP> 0.05 <SEP> 0.2 <SEP> 0.1 <SEP> 0.1 <SEP> 0.1 <tb> content <SEP> of <SEP> all <SEP> solid <SEP> components <SEP> 60.0 <SEP> 55.8 <SEP> 58.4 <SEP> 51.6 <SEP> 56.8 <SEP> 65.2 <SEP> 65.2 <SEP> 64.9 <SEP> 62.6 <tb> NOTES (1) rising melting point 35t (2) rising melting point 32c (3) This enzyme-treated chocolate was prepared by <RTI ID=17.3> addingcc-amylase (spitase cp-l NAGASE SAh'GYO) to 20% cacao mass aqueous solution (oil content 53%) at the rate of 10 DUN of z-amylase to 1 g of cacao mass, stirring at 65 C for 2 hours, then removing water by freeze-drying. (4) This enzyme-treated chocolate was prepared by adding ss - amylase (maltozyme 206 NAGASE SANGYO) to 30% cacao powder aqueous solution (oil content 23%) at the rate of 20 AUN of ss - amylase to 1 g of cacao powder, stirring at 60 C for 15 hours, then drying by heated air. (5) This enzyme-treated chocolate was prepared by adding glucoamylase (glucozyme AMINO SEIYAKU) to 30% cacao powder aqueous solution (oil content 23k) at the rate of 6 U of glucoamylase to 1 g of cacao powder, stirring at 55 C for 8 hours, then removing water by freeze-drying. (6) This enzyme-treated chocolate was prepared by adding -amylase (spitase cp-l NAGASE SANGYO) and ss - amylase (maltozyme 206 NAGASE SANGYO) to 40% sweet chocolate aqueous solution (oil content 26.5%) at the rate of 5 DUN of cc-amylase and 15 AUN of ss -amylase to 1 g of sweet chocolate, stirring at 60t for 10 hours. Table 2 Fancy cake test EMI18.1 No. <SEP> 1 <SEP> No. <SEP> 2 <SEP> No. <SEP> 3 <SEP> No. <SEP> 4 <SEP> No. <SEP> 5 <SEP> No. <SEP> 6 <SEP> No. <SEP> 7 <SEP> No. <SEP> 8 <tb> viscocity <SEP> (new <SEP> product) <SEP> (cps) <SEP> 80 <SEP> 70 <SEP> 45 <SEP> 100 <SEP> 50 <SEP> S <SEP> 30 <SEP> 120 <tb> whipping <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> C <SEP> C <SEP> C <tb> viscocity <SEP> (after <SEP> 3 <SEP> months <SEP> at <SEP> 5 C) <SEP> 90 <SEP> 90 <SEP> 60 <SEP> 120 <SEP> 80 <SEP> S <SEP> S <SEP> S <tb> (cps) <tb> (new <SEP> product) <tb> coating <SEP> property <SEP> A <SEP> B <SEP> B <SEP> A <SEP> A <SEP> C <SEP> A <SEP> A <tb> standup <SEP> quality <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> C <SEP> B <SEP> B <tb> colour <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <tb> flavor <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> C <SEP> A <SEP> A <tb> (after <SEP> 5 <SEP> days <SEP> at <SEP> 15 <SEP> C <SEP> ) <tb> standup <SEP> quality <SEP> A <SEP> A <SEP> A <SEP> B <SEP> A <SEP> B <SEP> B <SEP> B <tb> colour <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> C <SEP> A <SEP> A <tb> flavor <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> C <SEP> A <SEP> A <tb> cracks <SEP> A <SEP> A <SEP> A <SEP> B <SEP> A <SEP> A <SEP> B <SEP> A <tb> (after <SEP> freezing <SEP> and <SEP> melting) <tb> standup <SEP> quality <SEP> A <SEP> A <SEP> A <SEP> B <SEP> A <SEP> B <SEP> B <SEP> B <tb> colour <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> C <SEP> A <SEP> A <tb> flavor <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> C <SEP> A <SEP> A <tb> cracks <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> C <SEP> C <SEP> A <tb> UTILITY <SEP> A <SEP> A <SEP> A <SEP> A <SEP> A <SEP> C <SEP> C <SEP> C <tb> A: good B: average C: bad S: solid

Claims: hHAT IS CLAIMED IS: 1. A process of preparation of the bacteria-free foamable oil-in-water emulsion including chocolate, comprising (a) forming emulsion containing (1) 15 - 50 wt% of oil (2) 3 - 30 wtZ of enzyme-treated chocolate component (3) sodium caseinate (4) defatted milk solid (5) sugar component (6) 3 - 10 wtZ of emulsifier based on the oil (b) sterilizing the said emulsion by heating at ultra high temperature. 2. A process for making creamy bacteria-free foamable oil-in-water emulsion including chocolate according to claim 1, wherein said oil is a mixed oil of lauric type oil having 30 - 38 t rising melting point and nonlauric type oil. 3. A process for making creamy bacteria-free foamable oil-in-water emulsion including chocolate according to claim 2. wherein said mixed oil includes at least 20 wt% of lauric type oil. 4. A process for making creamy bacteria-free foamable oil-in-water emulsion including chocolate according to claim 2, wherein said mixed oil includes at least 40 wt% of lauric type oil. 5. A process for making creamy bacteria-free foamable oil-in-water emulsion including chocolate according to claim 3 or 4, wherein said mixed oil is the oil including 5 - 30 wt% of saturated or unsaturated fatty acid (including higher unsaturated fatty acid) having more than 20 carbon atoms.

Inventors: GOTO, YOICHI, MORI, MICHIO, MUTO, KUNIO, USAMI, SHOZO
Applicants: ASAHI DENKA KOGYO KABUSHIKI KAISHA
Application year: 1984
Main classification: A23G1
IPC codes: A23G9, A23G1