Process for producing rolled-in type emulsified fat and oil composition

Abstract: A process for producing a rolled-in type emulsified fat and oil composition by emulsifying 2 to 20 % by weight of protein, 30 to 75 % by weight of fat and oil and 18 to 65 % by weight of water into an oil-­ in-water type emulsion, which comprises adding 0.1 to 5 % by weight, based on the fat and oil, of phospholipid which comprises mono acyl glycero phospholipid at least 40 % by weight based on the total phospholipid as at least one emulsifier component to thereby give the aimed oil-in-water type emulsion is disclosed.

Description: This invention relates to a process for producing a rolled-in type emulsified fat and oil composition, improved in puffing properties and nutritional value and stability. A rolled-in type emulsified fat and oil composition to be used in, for example, puff pastry, danish pastry or croissant would form thin layers in a dough, through repeated folding and rolling, to thereby impart a large volume and a crispy texture to the final baked product. When no thin layer structure can be adequately formed, neither the desired volume nor the crispy texture can be achieved. In order to form the aimed thin layers, a rolled-in type emulsified fat and oil composition should have an appropriate consistency, elasticity and flexibility suitable for each dough. Rolled-in type emulsified fat and oil compositions may be broadly classified into a water-in-oil type emulsified composition including margarine and an oil-in-water type one. Since the former has a continuous phase comprising a fat and an oil, it shows a large change in consistency depending on the temperature. Thus it is required to produce such products with the use of a specific device, for example, a complector or a high-pressure combinator or to employ such a fat and oil composition as to cause a less SFI change depending on the temperature in order to widen the application temperature range thereof, though the latter method brings about a poor meltability in the mouth. On the other hand, since the latter has a continuous phase comprising water, it shows less change in consistency depending on the temperature and thus has a wide application temperature range. However it is required to incorporate therein a fat and an oil at a high content in order to give a consistency suitable for a dough. It is further required to add a thickener to the aqueous phase thereof. Furthermore it is required at present to add a preservative thereto to thereby improve the shelf stability. With the recent concern for health, the consumption of fat-rich products such as puff pastry, danish pastry and croissant has been stagnant. In order to counteract these situations, it is required to lower the fat and oil composition content of a product or the fat content of a rolled-in type emulsified fat composition. However every known process therefor is accompanied by some troubles such as failure to form the aimed layer structure, an undesirable texture or a poor volume. As an example of an oil-in-water type emulsified composition containing protein. US-A-4,012,533 discloses a whipped cream dessert comprising 10 to 32 % of a fat and 1.5 to 7 % of a composition of a water-soluble protein, a sweetener, an emulsifier and a gum stabilizer, while JP-A-79849/1982 discloses an oil-in water type emulsified composition wherein a partially hydrolyzed soybean protein is used as an emulsifier. However, the former product is produced by dissolving the small amount of water-soluble protein in a large amount of water, emulsifying the resulting solution with the use of the emulsifier and stabilizer and then whipping the obtained emulsion, and the latter is emulsified by using the partially hydrolyzed soybean protein of an improved emulsifying capability. Thus these compositions do not employ a common protein in an oil-in-water type emulsified composition. It is usually very difficult to stably emulsify a composition of a high protein content. In the case of a kneaded-in or folded-in type oil-in-water type emulsified composition comprising a fat, a starch, water and a gum disclosed in JP-A-166345/1986, for example, stabilizers, namely starch and gum are added. However, the product thus obtained has a gelatinous and poor texture. When it is to be roiled in, in addition, it is liable to adhere to the dough to therby form no layer. EP-A-0,284,026 discloses a process for the preparation of an emulsified fat composition comprising: (i) cheese, (ii) fat, (iii) water, (iv) 0.1 to 5% by weight of monoacylglycerophospholipid(s), based on the fat, and (v) 0.5 to 5% by weight of molten salt(s), based on the cheese, wherein the amount of cheese is 10 to 75% by weight and the amount of fat lies between 20 and 85% by weight of the emulsified fat composition. It is the object of the present invention to provide a process for producing a rolled-in type emulsified fat and oil composition of a low fat and oil content which is capable of giving an excellent layer structure as well as a desirable volume. According to the present invention this object is attained with a process for producing a rolled-in type emulsified fat and oil composition by emulsifying 7 to 15 % by weight of protein, 40 to 60% by weight of fat and oil having an elevated melting point of 30 to 37° C, and 25 to 50% by weight of water into an oil-in-water type emulsion which comprises adding 0.1 to 5% by weight, based on the fat and oil, of phospholipid which comprises at least 40% by weight of monoacylglycero phospholipid, based on the total phospholipid, as at least one emulsifier component to thereby give the aimed oil-in-water type emulsion with the proviso that the protein does not originate from cheese. Preferred embodiments of the present invention are set forth in the dependent claims. The process of the present invention enables the production of a rolled-in type emulsified fat and oil composition which contains less fat and oil and yet has a comparable, or even superior, volume and texture when compared with conventional ones. The process for producing the rolled-in type emulsified fat and oil composition of the present invention is further advantageous in that it enables the use of a large amount of protein, which would even undesirable effects on the fermentation or flexibility of a dough, to be incorporated into a baked product to thereby elevate the nutritional value thereof. According to the process of the present invention, it is also possible to substain a stable emulsion after ultrahigh-temperature flash pasteurization or in the presence of edible sodium chloride which improves the shelf stability of the product. The protein to be used in the present invention may be either in a natural state, a salt such as a sodium salt or treated with protease, so long as it originates from an edible material such as milk, soybean or egg albumen and provided that it does not originate from cheese, it is used in an amount of 7 to 15% by weight, based on the emulsified fat and oil composition. A low protein content may be employed when the fat and oil content is high while the water content is low. However a protein content of less than 7% cannot give the animal effects. The amount of the protein to be used would increase with a decrease in fat and oil content and with an increase in water content. When the fat and oil content is 40% by weight or above, a stable emulsion can hardly be obtained by using 15% by weight or more of protein. When a hardly soluble protein, such as natural casein, is selected as the protein, it is preferable to add 0.5 to 15 % by weight, based on the protein, of molten salt(s) such as sodium citrate, sodium tetrapolyphosphate or sodium tripolyphosphate thereto. Any animal or vegetable fat and oil may be employed in the present invention without restriction, so long as it is a common edible fat and oil. Examples thereof include palm oil, beef tallow, coconut oil, corn oil, rapeseed oil and milk fat which are optionally hardened and/or fractionated. In order to give an excellent meltability in the mouth, these fats and oils are combined together in such a manner as to give an elevated melting point of 30 to 37° C. In order to fully achieve the effects of the present invention, it is preferable to employ fat and oil in as small an amount as possible. However, no satisfactory rolling-in properties can be obtained unless 40% by weight of fat and oil is used. On the other hand, a fat and oil content exceeding 60% by weight would largely depart from the object of the present invention. Accordingly the rolled-in type emulsified fat and oil composition of the present invention comprises fat and oil in an amount of 40 to 60% by weight. And water may be used so long as it is potable. When the fat and oil content is 60% by weight or below, a water content of 25% by weight or below cannot give any stable emulsion. On the other hand, a water content exceeding 50% by weight would result in unsatisfactory rolling-in properties. Accordingly the rolled-in type emulsified fat and oil composition of the present invention comprises 25 to 50% by weight of water. The fatty acid of the mono acyl glycero phospholipid(s) (i.e., lyso phosphatide(s)), used as the essential component of the emulsifier in the present invention, are preferably those having eight or more carbon atoms. In each mono acyl glycero phospholipid, the acyl group may be located in either α - or β -position. As the mono acyl glycero phospholipid(s), both of natural ones of L-form and synthetic racemates may be used. It is known that natural mono acyl glycero phospholipid(s) are present in living organisms together with diacyl glycero phospholipid(s) in, for example, lipids of cereals such as soybean, rapeseed, corn or wheat and of animal cells. Mono acyl glycero phospholipid(s) may be further produced by hydrolyzing diacyl glycero phospholipids present in animal lipids such as yolk or vegetable lipids such as soybean with phospholipase A-2 obtained from swine pancreatic juice or snake venoms or phospholipase A-1 obtained from bacteria: removing the fatty acids thus formed with, for example, acetone: and purifying the residue by, for example, silica gel chromatography, if required (cf. JP-A-13263/1971. JP-A-136966/1977 and JP-A-51853/1983). In this case, the mono acyl glycero phospholipid(s) thus obtained may be hydrogenated in an appropriate solvent in the presence of a catalyst such as nickel to thereby give a surfactant of a higher oxidation stability. It is described in J. Amer. Oil Chem. Soc., 886 - 888, Oct. 1981 that mono acyl glycero phospholipid(s) of various compositions can be obtained by changing the conditions under which the phospholipase A-2 is employed. Alternatively mono acyl glycero phospholipid(s) can be obtained from materials prepared by fractionating diacyl glycero phospholipids with the use of a solvent such as ethyl alcohol. Further methods for preparing phosphatidylcholine such as the one with the use of yolk (cf. J. Biol. Chem., 188, 471 - 476 (1951)) as well as those as described in JP-A-16/1985, JP-A-42655/1984, JP-A-123496/1982 and JP-A-23997/1981 can be applied to the present invention. Every natural mono acyl glycero phospholipid as mentioned above has a levo-rotatory optical activity and has turned out to be safe when orally administered to animals (cf. J. Sci. Food and Agr., 32, 451 - 458). The glycero phospholipid(s) to be used in the present invention can be analyzed by, for example, thin layer chromatography, TLC-FID analyser (Iatro Scan method) or high-performance liquid chromatography. It is preferable that the mono acyl glycero phospholipid(s) to be used in the present invention, which can be obtained by the methods as described above, substantially comprise lyso phosphatidylcholine (i.e. mono acyl phosphatidylcholine). The mono acyl glycero phospholipid(s) may further contain lyso phosphatidylethanolamine and a small amount of one or more mono acyl glycero phospholipid(s) selected from among lyso phosphatidylinositol, lyso phosphatidic acid and lyso phosphatidylserine. The phospholipid(s) (a) which comprise mono acyl glycero phospholipid(s) (c) prepared from natural materials often contain diacyl phospholipid(s) (b) corresponding to the mono acyl glycero phospholipid(s) (c) depending on the employed preparation processes. In such a case, it is preferable that the content of the mono acyl glycero phospholipid(s) (c) is 40% by weight or above, preferably 50% by weight or above, based on the total phospholipids (a). Phospholipid(s) which contain relatively large amount of mono acyl glycero phospholipid(s) may be used together with crude soybean phospholipid(s) containing oily component(s). In this case, it is preferable that the phospholipid(s) which contain mono acyl glycero phospholipid(s) are dispersed in an aqueous phase while the crude soybean phospholipids are dispersed in an oily phase. As described above, the emulsifier(s) to be used in the present invention comprise phospholipid(s) which contain mono acyl glycero phospholipid(s) as an essential component. Preferable examples of emulsifiers to be used therewith include polyglycerol fatty acid esters, sucrose fatty acid esters, sorbitol fatty acid esters and glycerol fatty acid monoesters. With the use of these esters, the object of the present invention can be achieved at a relatively low cost. Examples of the polyglycerol fatty acid esters to be preferably used in the present invention together with said phospholipid(s) are mono-, di- or polyesters or polyglycerols having a degree of polymerization of 4 to 10 with saturated and/or unsaturated fatty acids having 14 to 22 carbon atoms and mixtures thereof. Polyglycerol fatty acid esters of fatty acids having 13 or less carbon atoms would exhibit a bitter taste, while those of fatty acids having 23 or more carbon atoms are hardly available in general. Examples of the sucrose fatty acid esters to be preferably used in the present invention together with said phospholipid(s) are mono-, di- or polyesters of sucrose with saturated and/or unsaturated fatty acids having 12 to 22 carbon atoms and mixtures thereof. Sucrose fatty acid esters of fatty acids having 11 or less carbon atoms would exhibit only limited emulsifying effects, while those of fatty acids having 23 or more carbon atoms are hardly available in general. Examples of the sorbitol fatty acid esters to be preferably used in the present invention together with said phospholipid(s) are mono-, di- or polyesters or sorbitol, sorbitan or sorbide with saturated and/or unsaturated fatty acids having 12 to 22 carbon atoms and mixtures thereof. Sorbitol fatty acid esters of fatty acids having 11 or less carbon atoms would exhibit only limited emulsifying effects, while those of fatty acids having 23 or more carbon atoms are hardly available in general. Examples of the glycerol fatty acid monoesters to be preferably used in the present invention together with said phospholipid(s) are monoesters of glycerol with saturated and/or unsaturated fatty acids having 12 to 22 carbon atoms and mixtures mainly comprising the monoesters together with a small amount of di- and/or triesters. Glycerol fatty acid monoesters of fatty acids having 11 or less carbon atoms would exhibit only limited emulsifying effects, while those of fatty acids having 23 or more carbon atoms are hardly available in general. It is preferable that the emulsifier composition to be used in the present invention comprises said phospholipid(s) and polyglycerol fatty acid ester(s), sucrose fatty acid ester(s) or sorbitol fatty acid ester(s) in a weight ratio of 30 : 70 to 100 : 0; or said phospholipid(s) and glycerol fatty acid monoester(s) at a weight ratio of 50 : 50 to 100 : 0. When the amount of said phospholipid(s) is smaller, the effects of the present invention are not enough. Said phospholipid(s) are used in an amount of 0.1 to 5% by weight based on the fat or oil. When they are less than 0.1% by weight, the effects of the present invention cannot be achieved. The addition of the same in an amount exceeding 5% by weight is disadvantageous from the economical viewpoint since it brings about no change in the effects and sometimes alters the taste. Generally speaking, the required amount of said phospholipid(s) would decrease with an increase in the content of the mono acyl glycero phospholipid(s). When the above emulsifier(s) are to be used together with said phospholipid(s), the total amount of the emulsifier mixture is 0.1 to 5 % by weight based on the fat or oil. The addition of the same in an amount exceeding 5 % by weight is disadvantageous from the economical viewpoint since it brings about no change in the effects and sometimes alters the taste. In the process of the present invention, surfactants other than those cited above may be employed as emulsifiers. By using the abovementioned phospholipid(s) as at least one emulsifying component, it becomes possible to obtain a stable emulsion even at a high protein content and to give a rolled-in type emulsified fat and oil composition of excellent rolling-in properties at a lower fat and oil content than conventional ones. Further the product thus obtained sustains a stable emulsion even at a high temperature of 100°C or above or in the presence of a large amount of edible sodium chloride. Thus the shelf stability thereof can be improved by subjecting the same to ultrahigh-temperature flash pasteurization or by employing a high edible sodium chloride concentration. Namely, the rolled-in type emulsified fat and oil composition of the present invention can contain 6 to 30 % by weight of edible sodium chloride based on the total water content in the oil-in-water type emulsion. The rolled-in type emulsified fat and oil composition prepared according to the present invention, which essentially comprises protein, fat and oil, water and mono acyl glycero phospholipid, may further contain additives such as perfumes, seasonings, spices, sugars and vitamins, in addition to the abovementioned edible sodium chloride. Although starches, gums and preservatives may be added thereto, it is preferable not to use these materials from the viewpoint of the object of the present invention. The rolled-in type emulsified fat and oil composition prepared according to the present invention may be produced in the following manner. The phospholipid(s) which contain mono acyl glycero phospholipid(s) and the abovementioned compatible emulsifier(s), if required, are added to an aqueous phase or to fat(s) and oil(s) and dissolved or dispersed therein. It is preferable that hydrophilic emulsifier(s) are added to an aqueous phase while lipophilic one(s) are added to fat(s) and oil(s). Then protein(s), molten salt(s), edible sodium chloride and other additives, if required, are further added to the aqueous phase, which is then heated to 60°C or above to thereby dissolve the protein(s) and other additives. Fat(s) and oil(s) are added to the aqueous phase and the resulting mixture is emulsified by stirring at a high rate in a homomixer, by using a pressurized homogenizer, by using a colloid mill, by ultrasonically treating or by combining some of these procedures to therby give an oil-in-water type emulsion. The emulsion thus obtained may be used as a product as such. Alternatively it may be further subjected to ultrahigh-temperature flash pasteurization and then used as a product. The ultrahigh-temperature flash pasteurization may be preferably carried out by heating the oil-in-water type emulsion to 110 to 150°C for 2 s to 4 min. The emulsion thus pasteurized may be further homogenized under sterile conditions to thereby give a product. The sterile homogenization may be carried out by a conventional method. To further illustrate the present invention, the following Examples will be given. In the following Examples, the term phospholipids means those mainly comprising mono acyl glycero phospholipid(s) and di acyl phospholipid(s). Example 1 Commercially available soybean phospholipids were subjected to precipitation with acetone and fractionation with aqueous ethanol to thereby give phospholipids comprising 70 % of di acyl phosphatidylcholine. The phospholipids were treated with swine pancreatic phospholipase A-2 (Lecitase 10-L®,). The fatty acids thus formed were removed with acetone and fractionated with an alcohol. After being further fractionated with a silicic acid column and an alcohol, phospholipids comprising 95 % of lyso phosphatidylcholine and 2 % of lyso phosphatidylethanolamine, i.e., total mono acyl glycero phospholipid content of 97 %, was obtained. 0.5 kg of the phospholipids and 9.5 kg of egg albumen were added to 30 kg of water and dissolved therein by heating to 60°C. 6 kg of hardened palm oil having a melting point of 45°C, 15 kg of palm oil, 33 kg of hardened soybean oil having a melting point of 36°C and 6 kg of refined soybean oil were added thereto and the obtained mixture was emulsified with a homomixer at 15,000 rpm and at 60°C for 10 min to thereby give an oil-in-water type emulsified fat and oil composition. Example 2 Defatted phospholipids were obtained by subjecting soybean phospholipids to precipitation with acetone. The defatted phospholipids were treated with Lecitase 10L® and phospholipids were extracted therefrom with a mixture of isopropyl alcohol and hexane and treated with acetone to thereby defat the same. The defatted phospholipids were extracted with an alcohol to thereby give phospholipids rich in mono acyl glycero phospholipids. These phospholipids comprised 48 % of lyso phosphatidylcholine and 11 % of lyso phosphatidylethanolamine as the main components and showed a total mono acyl glycero phospholipid content of 62 %. 0.6 kg of the phospholipids, 8 kg of casein, 0.3 kg of sodium citrate, 0.3 kg of sodium tetrapolyphosphate and 2.8 kg of edible sodium chloride were added to 28 kg of water and dissolved therein by heating to 60°C. 60 kg of the same fat and oil composition as the one used in Example 1 were added thereto and the obtained mixture was emulsified with a homomixer at 15,000 rpm and at 60°C for 10 min to thereby give an oil-in-water type emulsified fat and oil composition. Example 3 10 kg of the phospholipid obtained in Example 2 and 290 kg of sodium caseinate were added to 900 kg of water and dissolved therin by heating to 60°C. Then 120 kg of hardened palm oil having a melting point of 45°C, 200 kg of palm oil, 400 kg of hardened soybean oil having a melting point of 36°C and 80 kg of refined soybean oil were added thereto. The resulting mixture was emulsified by stirring with a propeller mixer at 200 rpm and at 60°C for 15 min. The emulsion thus obtained was treated with a Contherm scraping UHT pasteurizer at 130°C for 10 s. Then it was cooled to 40°C in a cooler and homogenized under sterile conditions at a homogenizing pressure of 50 kg/cm 2 . It was packed into a container under sterile conditions to thereby give an oil-in-water type emulsified fat and oil composition. Example 4 0.6 kg of the phospholipids obtained in Example 2, 12 kg of lactalbumin and 4.4 kg of edible sodium chloride were added to 43 kg of water and dissolved therein by heating to 60°C. Then 40 kg of the same fat composition as used in Example 3 were added thereto and the obtained mixture was emulsified with a homomixer at 15,000 rpm at 60°C for 10 min to thereby give an oil-in-water type emulsified fat and oil composition. Examples 5 to 8 The procedure of Example 1 was repeated except that the phospholipids were substituted with an emulsifier mixture comprising the phospholipids used in Example 1 and SY Gleaster MS 500® at a ratio (by weight, the same will apply hereinafter) of 5/5 (Example 5); an emulsifier mixture comprising the phospholipids used in Example 1 and SE-S 1670® at a ratio of 5/5 (Example 6); an emulsifier mixture comprising the phospholipids used in Example 1 and Emusol S-10-F® at a ratio of 7/3 (Example 7); and an emulsifier mixture comprising the phospholipids used in Example 1 and Emulsy MS® at a ratio of 7/3 (Example 8). Thus an oil-in-water type emulsified fat and oil composition was obtained in each case. The Emulsol S-10-F® and Emulsy MS® were dissolved in a fat and oil prior to the use. The emulsifiers employed in the above Examples together with the phospholipids were as follows. SY Gleaster MS-500®: Mfd. by Sakamoto Yakuhin K. K., hexaglycerol monostearate, HLB: 11.6. SE-S 1670®: Mfd. by Mitsubishi Chemical Food Ltd., sucrose monostearate, HLB: 15. Emusol S-10-F®: Mfd. by Kao Corp., sorbitan monostearate, HLB: 4.7. Emulsy MS®: Mfd. by Riken Vitamin K. K., glycerol monostearate, HLB: 2.5. Examples 9 to 12 The procedure of Example 2 was repeated except that the phospholipids were substituted with an emulsifier mixture comprising the phospholipids used in Example 1 and SY Gleaster MS 500® at a ratio of 5/5 (Example 9); an emulsifier mixture comprising the phospholipids used in Example 1 and SE-S 1670® at a ratio of 5/5 (Example 10); an emulsifier mixture comprising the phospholipids used in Example 1 and Emusol S-10-F® at a ratio of 7/3 (Example 11); and an emulsifier mixture comprising the phospholipids used in Example 1 and Emulsy MS® at a ratio of 7/3 (Example 12). Thus an oil-in-water type emulsified fat and oil composition was obtained in each case. The Emusol S-10-F® and Emulsy MS® were dissolved in a fat and oil prior to the use. The following table shows the contents of proteins, fats and oils, water, emulsifiers, edible sodium chloride and molten salts in the emulsified fat and oil compositions produced in Examples 1 to 12. Each product had a homogeneous and smooth texture and a consistency suitable for rolling-in at 5 to 20°C. Ex. No. 1, 5∼8 2, 9∼12 3 4 Component; protein 9.5 8 14.5 12 fat and oil 60 60 40 40 water 30 28 45 43 emulsifier 0.5 0.6 0.5 0.6 edible sodium chloride 0 2.8 0 4.4 molten salt 0 0.6 0 0 0.8 kg of the phospholipids of Example 2 and 0.1 kg of CMC were added to 16.5 kg of water and dissolved therein by heating to 60°C. Then 82.6 kg of the same fat and oil composition as used in Example 2 were added thereto and the obtained mixture was emulsified in the same manner as described in Example 2 to thereby give a rolled-in type emulsified fat and oil composition, which was used as a control. The rolling-in properties of the control product into a puff pastry prepared in the following manner was compared with those of the products of the present invention produced in Examples 1 to 12. As a result, each of the rolled-in type emulsified fat and oil composition prepared according to the present invention was comparable or even superior to the control product flexibility, volume and texture. The following table shows the results of the comparison. Dough composition: hard flour 50 parts soft flour 50 parts edible sodium chloride 0.5 part water 52 parts shortening 5 parts Preparation: Dough mixing: at low rate for 2 min and at high rate for 5 min. Amount of rolled-in type emulsified fat and oil composition to be folded in: 70 % by weight based on flour Folding: into four, four times. Molding: rolling to 2 mm in thickness followed by rapping. Baking: at 200°C for 15 min. Control Examples 1 2 3 4 5 6 7 8 9 10 11 12 1 ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ 2 ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ 3 ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ o ○ Note: 1 ○ Spreadability 2 ○ Floating 3 ○ Texture Comparative Example 1 0.5 kg of the phospholipids of Example 2 and 1.5 kg of sodium caseinate were added to 70 kg of water and dissolved therein by heating to 60°C. 28 kg of the same fat composition as used in Example 2 were added thereto and the obtained mixture was emulsified in the same manner as described in Example 2 to thereby give an oil-in-water type emulsified composition. The obtained product was homogeneous and smooth but flowable and could not be rolled in. Comparative Example 2 0.5 kg of the phospholipids of Example 2 and 21.5 kg of sodium caseinate were added to 48 kg of water and dissolved therein by heating to 60°C. 30 kg of the same fat and oil composition as used in Example 2 were added thereto and the obtained mixture was tentatively emulsified in the same manner as the one described in Example 2. However no emulsion could be formed. Comparative example 3 0.8 kg of the phospholipids pf Example 2 and 7.2 kg of sodium caseinate were added to 17 kg of water and dissolved therein by heating to 60°C. 75 kg of the same fat and oil composition as used in Example 2 were added thereto and the obtained mixture was tentatively emulsified in the same manner as described in Example 2. However no emulsion could be formed. Comparative Example 4 0.8 kg of the phospholipids of Example 2 and 1.5 kg of sodium caseinate were added to 16.5 kg of water and dissolved therein by heating to 60°C. 81.2 kg of the same fat and oil composition one used in Example 2 were added thereto and the obtained mixture was emulsified In the same manner as described in Example 2 to thereby give an oil-in-water type emulsified fat and oil composition. The obtained product containing a large amount of fat and oil showed rolling-in properties nearly comparable to those of the above control product. Thus the addition of the protein exerted no effect. Comparative Example 5 The procedure of Example 1 was repeated except that no phospholipid was added. As a result, no emulsion could be formed. Comparative Examples 6 to 9 The procedure of Example 1 was repeated except that the phospholipids were substituted with SY Gleaster MS500® (Comparative Example 6), SE-S 1670® (Comparative Example 7), Emusol S-10-F® (Comparative Example 8), and Emulsy MS® (Comparative Example 9). As a result, no emulsion could be formed in each case. Comparative Examples 10 to 13 The procedure of Example 2 was repeated except that the phospholipids were substituted with SY Gleaster MS500® (Comparative Example 10), SE-S 1670® (Comparative Example 11), Emusol S-10-F® (Comparative Example 12), and Emulsy MS® (Comparative Example 13). As a result, no emulsion could be formed in each case.

Claims: A process for producing a rolled-in type emulsified fat and oil composition by emulsifying 7 to 15% by weight of protein, 40 to 60% by weight of fat and oil having an elevated melting point of 30 to 37° C, and 25 to 50% by weight of water into an oil-in-water type emulsion which comprises adding 0.1 to 5% by weight, based on the fat and oil, of phospholipid which comprises at least 40% by weight of monoacylglycero phospholipid based on the total phospholipid, as at least one emulsifier component, to thereby give the aimed oil-in-water type emulsion with the proviso that the protein does not originate from cheese. The process according to claim 1, wherein said oil-in-water type emulsion is heated to 110 to 150°C for 25 s to 4 min. The process according to claim 2, wherein said oil-in-water emulsion is homogenized under sterile conditions after heating the same. The process according to claim 1, wherein 6 to 30% by weight based on the water content of said oil-in-water type emulsion of edible sodium chloride is added. The process according to claim 1, wherein 0.5 to 15% by weight, based on the protein, of molten salt is added. The process according to claim 5, wherein said molten salt is selected from the group consisting of sodium citrate, sodium tetrapolyphosphate and sodium tripolyphosphate. The process according to claim 1, wherein said protein is a protease-treated protein. The process according to claim 1, wherein said phospholipid (a) substantially comprises lyso phosphatidylcholine, and when said phospholipid (a) further comprises diacyl phospholipid (b) the monoacylglycero phospholipid (c) amounts to at least 40% by weight based on the total glycero phospholipid content. The process according to claim 1, which comprises adding 0.1 to 5% by weight based on said fat and oil, of an emulsifier mixture composed of said phospholipid and one or more emulsifiers selected from the group consisting of polyglycerol fatty acid esters, sucrose fatty acid esters and sorbitol fatty acid esters in a weight ratio of 30:70 to 100:0. The process according to claim 1, which comprises adding 0.1 to 5% by weight, based on said fat and oil, of an emulsifier mixture composed of said phospholipid and glycerol fatty acid monoesters at a weight ratio of 50:50 to 100:0.

Inventors: KATO MASAAKI, SHINOHARA KATUMI, SUGIYAMA HIROMU, KATO, MASAAKI, SHINOHARA, KATUMI, SUGIYAMA, HIROMU, KATO, MASAAKI ASAHI DENKA KOGYO KABUSHIKI KAISHA, SHINOHARA, KATUMI ASAHI DENKA KOGYO KABUSHIKI KAIS, SUGIYAMA, HIROMU ASAHI DENKA KOGYO KABUSHIKI KAIS
Applicants: ASAHI DENKA KOGYO KK, ASAHI DENKA KOGYO KABUSHIKI KAISHA
Application year: 1989
Main classification: A23D7
IPC codes: A23D7, A21D2