JP4674961B2 - Oil-in-water emulsion - Google Patents
Oil-in-water emulsion Download PDFInfo
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- JP4674961B2 JP4674961B2 JP2000374417A JP2000374417A JP4674961B2 JP 4674961 B2 JP4674961 B2 JP 4674961B2 JP 2000374417 A JP2000374417 A JP 2000374417A JP 2000374417 A JP2000374417 A JP 2000374417A JP 4674961 B2 JP4674961 B2 JP 4674961B2
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Description
【0001】
【発明の属する技術分野】
本発明は、乳成分を含有する水中油型乳化物に関するものである。詳しくは、特定の曇点を有するポリグリセリン脂肪酸エステルを含有した、殺菌後の熱安定性および乳化安定性に優れる水中油型乳化物に関するものである。
【0002】
【従来の技術】
乳成分を含むクリーム類は、コーヒーに使用されたり、起泡させてケーキなどにデコレーションとして使用されたりする。従来は、乳成分を含むクリーム類として、牛乳を遠心分離して脂肪分を濃縮したいわゆる天然の生クリームが用いられていた。天然の生クレームは、乳タンパク質や脂質などにより安定な水中油型乳化物を形成している。ところが、生クリームは高価である上に季節変動により品質が振れるため安定した製品の供給が困難である。このため、近年、食用油脂と無脂乳固形分、乳化剤、安定剤などを混合し、これを乳化することによって得られる合成クリーム類が開発されている。
【0003】
これらのクリーム類に要求される性質としては、品質が一定であり、高温殺菌後の冷却にも安定であること、保存中あるいは移送中の温度変化および振動により増粘や固化が起こらないことが挙げられる。
クリーム類は油脂あるいは乳脂肪の含有量の違いにより各種用途のものに分類されるが、この場合に要求される機能は各クリームで異なる。例えばコーヒークリームでは、コーヒーに投入した時のクリームの分散性が良いこと、フェザーリングおよびオイルオフが抑制されること、ホワイトナー性が良いことなどが重要である。また、ホイップドクリームでは、起泡時に適切なオーバーランが得られ、泡が安定であること、絞りやすく保型性が良いこと、風味、口どけが良いことなどが要求される。
【0004】
しかし、上記のような各種クリームに応じた特性が発現されるためには、先ず、原液の乳化安定性が必要であり、原液の乳化安定性が良好でなければ、目的とする機能は達成されにくい。特にホイップドクリームの場合は脂肪分含量が高いため、原液保存中に増粘が起こりやすくなる。
【0005】
【発明が解決しようとする課題】
このような、クリーム類のうち、高脂肪分であるホイップドクリームについては、乳化剤としてポリグリセリン脂肪酸エステルを添加する検討が行なわれてきた(特開平2−128644号公報、特開平5−23126号公報、特開平10−84900号公報など)。しかし、いずれの場合も耐熱性が弱く、保存時に乳化が壊れて離水が起こるなど物性面で満足できるものにはなっていない。
【0006】
従って、乳成分を含有するクリームの乳化安定性を向上させる技術の開発が望まれていた。
【0007】
【課題を解決するための手段】
本発明者は上記実情に鑑み、種々検討した結果、食用油脂を用いて調製される水中油型乳化物に、特定の曇点を有するポリグリセリン脂肪酸エステルを含有させることにより、乳エマルションの凝集が抑制され、殺菌後も安定な水中油型乳化の状態を保つことを見出し、本発明に到達するに至った。
【0008】
すなわち、本発明の要旨は、油脂と、乳成分を含む水相とからなる水中油型乳化物であって、20%塩化ナトリウム水溶液中1重量%濃度で測定した曇点が90℃以上であるポリグリセリン脂肪酸エステルを含有し、かつ水中油型乳化物中の油脂の含有量が20〜60重量%であることを特徴とする水中油型乳化物に存する。
【0009】
【発明の実施の形態】
以下、本発明を詳細に説明する。
本発明における水中油型乳化物は、油脂、乳成分、水、特定曇点のポリグリセリン脂肪酸エステルを必須成分とし、必要に応じ更にその他の成分から構成される。
【0010】
本発明で使用する油脂としては、食用のものであれば特に限定されず、例えば大豆油、ヤシ油、パーム油、菜種油、コーン油、オリーブ油、綿実油、サフラワー油、トウモロコシ油等の植物性油脂や乳脂、牛脂、豚脂、魚油などの動物性油脂が挙げられ、さらにこれらの油脂を硬化、分別、エステル交換処理した加工油脂が挙げられる。これらの油脂は単独でも混合しても用いることができる。水中油型乳化物中の油脂の量は20〜60重量%であり、好ましくは25〜45重量%である。油脂の量が20重量%未満ではホイップドクリームに充分な保形性が得られなかったり、コーヒークリームの粘性が低下する。一方、60重量%を越えると水中油型乳化物が増粘しやすくなるために良好な乳化が得られず好ましくない。
【0011】
本発明で用いられる乳成分は、通常、脱脂乳、脱脂粉乳、全粉乳、カゼイン、カゼインナトリウムなどが用いられるが、これらに限定されることはなく、乳蛋白質であれば任意のものが用いられる。水中油型乳化物中の乳成分の量は、通常0.4〜5.0重量%である。
本発明で用いられるポリグリセリン脂肪酸エステルは、20%塩化ナトリウム水溶液中1重量%濃度で測定した曇点が90℃以上である。ポリグリセリン脂肪酸エステルはポリグリセリンと脂肪酸との反応により得られるエステル体と未反応ポリグリセリンの混合物である。ポリグリセリン脂肪酸エステル中の残存ポリグリセリンの量は、70重量%以下であることが好ましい。このような曇点範囲を有するポリグリセリン脂肪酸エステルを得るためにはポリグリセリンに対して脂肪酸の仕込比率を小さくし、アルカリ触媒の量を減じ(例えば、K2CO3,KOH,Na2CO3,NaOHなどを、ポリグリセリンに対して5×10-7〜0.1モル倍用いる)て、2段階反応で後半の温度を高める方法、例えば、反応温度180〜260℃でのエステル化反応後に、さらに反応温度を10〜50℃上昇させて1〜4時間反応させる方法を用いることができる。(特開平7−145104号公報参照)。
【0012】
曇点測定法としては、通常、1〜30%の塩化ナトリウム又は硫酸ナトリウム水溶液にポリグリセリン脂肪酸エステルを溶解した後、測定する必要があり、その条件は対象となる試料の溶解性により異なるが、本発明の測定法について説明する。本発明の場合、先ず、ポリグリセリン脂肪酸エステルを1重量%となるように20重量%塩化ナトリウム水溶液に分散し、加熱しながら攪拌し、均一な水溶液とする。そして得られたポリグリセリン脂肪酸エステル均一水溶液を、0℃以上100℃以下の任意の温度で2〜5℃刻みに振とう攪拌・静置し、ポリグリセリン脂肪酸エステルが油状あるいはゲル状の如く分離し、不均一水溶液となる温度を測定する。この不均一状態となる温度を「曇点」と呼び、本発明ではその温度を求める。0℃未満では氷の融点以下、100℃を越えると水の沸点以上となるために、正確な水溶液状態の観察が難しく曇点測定が困難となる。曇点90℃以上とは、90℃以上で不均一水溶液となる場合と、100℃を越えても不均一水溶液とならない場合を含む。曇点は、100℃以上が好ましい。曇点100℃以上とは、100℃でも不均一水溶液とならない場合をいう。
【0013】
ポリグリセリン脂肪酸エステルを構成する脂肪酸の具体例としては、ミリスチン酸、パルミチン酸、ステアリン酸、ベヘン酸、オレイン酸などの炭素数14〜22の飽和または不飽和の脂肪酸が挙げられ、特にミリスチン酸を主成分とするものが好ましい。構成脂肪酸は脂肪酸の炭素数が同じものを使用しても炭素数が異なるものを複数混合したものを用いてもよい。ポリグリセリン脂肪酸エステルを構成するポリグリセリンの重合度としては、通常、平均重合度が2〜20、好ましくは平均重合度が4〜12である。水中油型乳化物中の20%塩化ナトリウム水溶液中1重量%で測定した曇点が90℃以上のポリグリセリン脂肪酸エステルの含有量は、通常、0.1〜1.0重量%である。
【0014】
本発明の水中油型乳化物は、通常、他の乳化剤を少なくとも1種併用する。この乳化剤は、クリームの製造に通常用いらるものであれば特に限定されないが、油に分散しやすいものが好ましく、例えば、レシチン、グリセリン脂肪酸脂肪酸エステル、ソルビタン脂肪酸エステル、ポリソルベート、有機酸モノグリセリド、プロピレングリコール脂肪酸エステル、HLBが0以上5未満の蔗糖脂肪酸エステル、HLBが8以下であるポリグリセリン脂肪酸エステルなどが例示できる。
【0015】
本発明の水中油型乳化物は、必要に応じて上述以外の他の添加剤、例えば、塩類、安定剤、着香料等を含有することができる。塩類としては、リン酸塩、クエン酸塩などが用いられる。安定剤としては、セルロース、カラギーナン、ローカストビーンガム、キサンタンガム、グアーガム等が用いられる。安定剤の量は、0.1〜1.0重量%、中でも0.2〜0.7重量%が好ましい。安定剤の量が0.1重量%未満では適当な粘性が得られないことがあり、逆に1.0重量%を越えると水中油型乳化物が増粘するので好ましくない。着香料としては、任意のものを用いることができる。例えば、バニラエッセンス、ミルクフレーバー、バターフレーバー等が挙げられる。
【0016】
本発明の水中油型乳化物は、通常、以下の方法で製造される。
まず、乳成分、20%塩化ナトリウム水溶液中1重量%で測定した曇点が90℃以上のポリグリセリン脂肪酸エステル、及び他の水溶性添加剤を水に溶解し、水相を調製する。水相中の乳成分の含有量は、通常、0.4〜5.0重量%であり、好ましくは0.5〜3.0重量%が適当である。乳成分の量が0.4重量%未満ではクリームとしての風味が充分でなく、5.0重量%を越えると水中油型乳化物が増粘するので好ましくない。水相中の20%塩化ナトリウム水溶液中1重量%で測定した曇点が90℃以上のポリグリセリン脂肪酸エステルの含有量は、通常、0.1〜1.0重量%である。
【0017】
また、油に分散しやすい乳化剤、及び他の油溶性添加剤を60〜70℃で油脂に溶解し、油相を調製する。乳化剤の油相中の含有量は、通常、0.1〜1.5重量%である。
ついで、調製した油相と水相を60〜70℃にて混合し、予備乳化を行い、ホモジナイザーを用いて60〜70℃にて均質化処理を行なった後に冷却する。
油相と水相の比率は、通常、1/4〜3/2(重量比)である。
【0018】
このようにして調製した水中油型乳化物は、更に、加熱による殺菌が施されるが、風味の維持や褐変を防止する点からも、UHT殺菌を施すのが好ましい。本発明で用いるUHT殺菌は、殺菌温度130〜150℃、殺菌時間5〜30秒に相当するような超高温殺菌である。UHT殺菌はクリームに直接蒸気を吹き込むスチームインジェクション式やクリームを水蒸気中に噴射して加熱するスチームインフュージョン式などの直接加熱方式、プレートやチューブなど表面熱交換器を用いる間接加熱方式など公知の方法で行うことができる。
【0019】
本発明の水中油型乳化物は、通常、乳製品として使用される。乳製品としては、例えば、アイスクリーム、カスタードクリーム、ホイップドクリーム、コーヒークリーム、クロテッドクリームなどが例示出来るが、好ましくは、ホイップドクリームである。尚、本発明の水中油型乳化物には、乳飲料は含まれない。
【0020】
【実施例】
次に、本発明を実施例によりさらに具体的に説明するが、本発明はその要旨を越えない限り、以下の実施例に限定されるものではない。なお、本実施例において特にことわりのない限り、重量%は水中油型乳化物に対する重量%である。
[製造例]
デカグリセリン(平均重合度9.15、平均分子量695、水酸基価900)188g(0.27モル)とミリスチン酸(純度99%、平均分子量228)62g(0.27モル)を加熱ジャケット付き攪拌型反応槽に仕込み、25%水酸化ナトリウム0.025g(対原料合計0.0025wt%)を加えて、窒素気流下、240℃に昇温して3時間反応させた後、更に260℃で4時間反応させてデカグリセリンミリスチン酸エステル234gを得た。
実施例1
60℃の水568.4g(56.84重量%)に砂糖90g(9.00重量%)、脱脂粉乳30g(3.00重量%)、グアーガム1g(0.10重量%)、デカグリセリンミリスチン酸エステル(曇点100℃以上)3g(0.30重量%)、ヘキサメタリン酸ナトリウム1g(0.10重量%)を添加し、溶解して水相部とした。別に70℃に加温した部分水添大豆油300g(30.00重量%)にレシチン0.6g(0.06重量%)、蔗糖ステアリン酸エステル(三菱化学フーズ(株)商品名リョートーシュガーエステルS−270、HLB2)3g(0.30重量%)、同じく蔗糖エルカ酸エステル(三菱化学フーズ(株)商品名リョートーシュガーエステルER−290、HLB2)3g(0.30重量%)を溶解して油相部とした。この中へ水相部を投入し、70℃で15分間プロペラ攪拌機により予備乳化した。この予備乳化液を均質機(APV GAULIN社製)を用いて一次圧150kg/cm2、2次圧50kg/cm2の加圧によって均質化した。次に得られた水中油型乳化物を130℃で殺菌し、直ちに氷水中で10℃以下に冷却し、冷蔵庫で一晩エージングすることによりホイップドクリームを得た。得られたクリームについて、粒径測定(HOLIBA−LA500)および目視観察によりクリームの状態について評価した結果、粒径分布はシャープな単一ピークであり、クリームが増粘している様子も観察されず乳化状態は良好であった。
比較例1
デカグリセリンミリスチン酸エステル(曇点100℃以上)の代わりにデカグリセリンステアリン酸エステル(三菱化学フーズ(株)商品名リョートーポリグリエステルS−28D、曇点50℃以下)3g(0.30重量%)を水相部に加えた以外は実施例と同様にして調製及び評価を行った。エージング後のクリームは増粘し固化し始めており、幅広い粒径分布であった。
【0021】
【発明の効果】
本発明の水中油型乳化物は殺菌を行なっても増粘、固化などが起こらず、耐熱性および乳化安定性に優れる。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an oil-in-water emulsion containing a milk component. Specifically, the present invention relates to an oil-in-water emulsion containing a polyglycerin fatty acid ester having a specific cloud point and excellent in heat stability and emulsification stability after sterilization.
[0002]
[Prior art]
Creams containing dairy ingredients are used for coffee or foamed and used as a decoration for cakes and the like. Conventionally, so-called natural fresh cream obtained by concentrating fat by centrifuging milk has been used as creams containing milk components. Natural raw claims form stable oil-in-water emulsions with milk proteins and lipids. However, fresh cream is expensive and its quality varies due to seasonal variations, making it difficult to supply a stable product. For this reason, synthetic creams obtained by mixing edible oils and fats, non-fat milk solids, emulsifiers, stabilizers and the like and emulsifying them have been developed in recent years.
[0003]
The properties required for these creams are that the quality is constant, that it is stable for cooling after high-temperature sterilization, and that no thickening or solidification occurs due to temperature changes and vibration during storage or transfer. Can be mentioned.
Creams are classified into those for various uses depending on the content of oil or milk fat, but the functions required in this case are different for each cream. For example, in the case of coffee cream, it is important that the dispersibility of the cream when it is put into coffee, that feathering and oil-off are suppressed, and that the whitener property is good. In addition, the whipped cream is required to have an appropriate overrun at the time of foaming, that the foam is stable, that it is easy to squeeze, has good shape-retaining properties, and has a good taste and mouthfeel.
[0004]
However, in order for the properties according to the various creams described above to be expressed, first, the emulsion stability of the stock solution is required. If the emulsion stability of the stock solution is not good, the intended function is achieved. Hateful. In the case of whipped cream in particular, the fat content is high, so that thickening easily occurs during storage of the stock solution.
[0005]
[Problems to be solved by the invention]
Among such creams, whipped cream having a high fat content has been studied to add a polyglycerol fatty acid ester as an emulsifier (JP-A-2-128644, JP-A-5-23126). Gazette, JP-A-10-84900, etc.). However, in either case, the heat resistance is weak, and the physical properties are not satisfactory, for example, the emulsification is broken during storage and water separation occurs.
[0006]
Therefore, development of the technique which improves the emulsification stability of the cream containing a milk component has been desired.
[0007]
[Means for Solving the Problems]
As a result of various investigations in view of the above circumstances, the present inventor has incorporated a polyglycerin fatty acid ester having a specific cloud point into an oil-in-water emulsion prepared using edible fats and oils, thereby aggregating a milk emulsion. It has been found that the oil-in-water emulsification state is maintained even after sterilization, and the present invention has been reached.
[0008]
That is, the gist of the present invention, the oil fat, with a oil-in-water emulsion consisting of an aqueous phase containing a milk component, cloud point measured in 1% strength by weight in a 20% aqueous solution of sodium chloride is 90 ° C. or higher It exists in the oil-in-water emulsion characterized by containing a certain polyglyceryl fatty acid ester, and content of fats and oils in an oil-in-water emulsion is 20 to 60 weight%.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the present invention will be described in detail.
The oil-in-water emulsion in the present invention comprises an oil and fat, a milk component, water, and a polyglycerin fatty acid ester having a specific cloud point as essential components, and further comprises other components as necessary.
[0010]
The fats and oils used in the present invention are not particularly limited as long as they are edible. For example, vegetable fats and oils such as soybean oil, coconut oil, palm oil, rapeseed oil, corn oil, olive oil, cottonseed oil, safflower oil, corn oil and the like And animal fats such as milk fat, beef tallow, pork fat and fish oil, and processed fats and oils obtained by curing, fractionating and transesterifying these fats. These fats and oils can be used alone or in combination. The amount of fats and oils in the oil-in-water emulsion is 20 to 60% by weight, preferably 25 to 45% by weight. If the amount of fat is less than 20% by weight, sufficient shape retention cannot be obtained for whipped cream, or the viscosity of coffee cream decreases. On the other hand, if it exceeds 60% by weight, the oil-in-water emulsion tends to increase in viscosity, so that good emulsification cannot be obtained, which is not preferable.
[0011]
As the milk component used in the present invention, skim milk, skim milk powder, whole milk powder, casein, casein sodium and the like are usually used, but not limited thereto, and any milk protein can be used. . The amount of the milk component in the oil-in-water emulsion is usually 0.4 to 5.0% by weight.
The polyglycerin fatty acid ester used in the present invention has a cloud point of 90 ° C. or higher measured at a concentration of 1% by weight in a 20% aqueous sodium chloride solution. The polyglycerol fatty acid ester is a mixture of an ester obtained by reaction of polyglycerol and a fatty acid and unreacted polyglycerol. The amount of residual polyglycerol in the polyglycerol fatty acid ester is preferably 70% by weight or less. In order to obtain a polyglycerin fatty acid ester having such a cloud point range, the ratio of fatty acid to polyglycerin is reduced and the amount of alkali catalyst is reduced (for example, K 2 CO 3 , KOH, Na 2 CO 3 , NaOH, etc. 5 × 10 −7 to 0.1 mol times with respect to polyglycerin), and a method of increasing the latter half temperature in a two-step reaction, for example, after an esterification reaction at a reaction temperature of 180 to 260 ° C. Further, a method of reacting for 1 to 4 hours by raising the reaction temperature by 10 to 50 ° C. can be used. (See JP-A-7-145104).
[0012]
As a cloud point measurement method, it is usually necessary to measure after dissolving a polyglycerol fatty acid ester in 1 to 30% sodium chloride or sodium sulfate aqueous solution, and the conditions differ depending on the solubility of the target sample, The measurement method of the present invention will be described. In the case of the present invention, first, polyglycerin fatty acid ester is dispersed in a 20 wt% sodium chloride aqueous solution so as to be 1 wt%, and stirred while heating to obtain a uniform aqueous solution. Then, the obtained polyglycerol fatty acid ester homogeneous aqueous solution is shaken and allowed to stand at an arbitrary temperature of 0 ° C. or more and 100 ° C. or less in increments of 2 to 5 ° C. to separate the polyglycerol fatty acid ester as an oil or gel. Measure the temperature at which the aqueous solution becomes heterogeneous. The temperature at which this non-uniform state occurs is called the “cloud point”, and the temperature is determined in the present invention. If it is less than 0 ° C., it is below the melting point of ice, and if it exceeds 100 ° C., it becomes more than the boiling point of water. The cloud point of 90 ° C. or higher includes a case where a non-uniform aqueous solution is obtained at 90 ° C. or higher and a case where the cloud point does not become a non-uniform aqueous solution even when the temperature exceeds 100 ° C. The cloud point is preferably 100 ° C. or higher. A cloud point of 100 ° C. or higher means a case where a non-uniform aqueous solution is not obtained even at 100 ° C.
[0013]
Specific examples of the fatty acid constituting the polyglycerin fatty acid ester include saturated or unsaturated fatty acids having 14 to 22 carbon atoms such as myristic acid, palmitic acid, stearic acid, behenic acid, oleic acid, etc. What has a main component is preferable. As the constituent fatty acid, fatty acids having the same carbon number may be used, or a mixture of a plurality of fatty acids having different carbon numbers may be used. As a polymerization degree of the polyglycerol which comprises polyglycerol fatty acid ester, an average polymerization degree is 2-20 normally, Preferably an average polymerization degree is 4-12. The content of polyglycerin fatty acid ester having a cloud point of 90 ° C. or higher measured at 1% by weight in a 20% aqueous sodium chloride solution in an oil-in-water emulsion is usually 0.1 to 1.0% by weight.
[0014]
The oil-in-water emulsion of the present invention usually uses at least one other emulsifier in combination. The emulsifier is not particularly limited as long as it is usually used in the production of cream, but is preferably easily dispersible in oil, for example, lecithin, glycerin fatty acid fatty acid ester, sorbitan fatty acid ester, polysorbate, organic acid monoglyceride, propylene Examples include glycol fatty acid esters, sucrose fatty acid esters having an HLB of 0 to less than 5, and polyglycerin fatty acid esters having an HLB of 8 or less.
[0015]
The oil-in-water emulsion of the present invention can contain other additives other than those described above, for example, salts, stabilizers, flavoring agents, and the like as necessary. As the salts, phosphate, citrate and the like are used. As the stabilizer, cellulose, carrageenan, locust bean gum, xanthan gum, guar gum and the like are used. The amount of the stabilizer is preferably 0.1 to 1.0% by weight, and more preferably 0.2 to 0.7% by weight. If the amount of the stabilizer is less than 0.1% by weight, an appropriate viscosity may not be obtained. Conversely, if the amount exceeds 1.0% by weight, the oil-in-water emulsion increases in viscosity, which is not preferable. Arbitrary things can be used as a flavoring agent. Examples include vanilla essence, milk flavor, butter flavor and the like.
[0016]
The oil-in-water emulsion of the present invention is usually produced by the following method.
First, a milk component, a polyglycerin fatty acid ester having a cloud point of 90 ° C. or higher measured at 1% by weight in a 20% sodium chloride aqueous solution, and other water-soluble additives are dissolved in water to prepare an aqueous phase. The content of the milk component in the aqueous phase is usually 0.4 to 5.0% by weight, preferably 0.5 to 3.0% by weight. If the amount of the milk component is less than 0.4% by weight, the flavor as a cream is not sufficient, and if it exceeds 5.0% by weight, the oil-in-water emulsion increases in viscosity, which is not preferable. The content of the polyglycerin fatty acid ester having a cloud point of 90 ° C. or higher measured at 1% by weight in a 20% aqueous sodium chloride solution in the aqueous phase is usually 0.1 to 1.0% by weight.
[0017]
Moreover, the emulsifier which is easy to disperse | distribute to oil, and another oil-soluble additive are melt | dissolved in fats and oils at 60-70 degreeC, and an oil phase is prepared. The content of the emulsifier in the oil phase is usually 0.1 to 1.5% by weight.
Next, the prepared oil phase and aqueous phase are mixed at 60 to 70 ° C., pre-emulsified, and homogenized at 60 to 70 ° C. using a homogenizer, and then cooled.
The ratio of the oil phase to the aqueous phase is usually 1/4 to 3/2 (weight ratio).
[0018]
The oil-in-water emulsion thus prepared is further sterilized by heating, but it is preferable to perform UHT sterilization from the viewpoint of maintaining the flavor and preventing browning. The UHT sterilization used in the present invention is an ultra-high temperature sterilization corresponding to a sterilization temperature of 130 to 150 ° C. and a sterilization time of 5 to 30 seconds. UHT sterilization is a known method such as a direct injection method such as a steam injection method in which steam is directly blown into the cream, a steam infusion method in which the cream is injected into steam, and an indirect heating method using a surface heat exchanger such as a plate or tube. Can be done.
[0019]
The oil-in-water emulsion of the present invention is usually used as a dairy product. Examples of dairy products include ice cream, custard cream, whipped cream, coffee cream, and clotted cream, but whipped cream is preferred. The oil-in-water emulsion of the present invention does not include milk drinks.
[0020]
【Example】
EXAMPLES Next, although an Example demonstrates this invention further more concretely, this invention is not limited to a following example, unless the summary is exceeded. In the examples, unless otherwise specified,% by weight is% by weight relative to the oil-in-water emulsion.
[Production example]
188 g (0.27 mol) of decaglycerin (average degree of polymerization 9.15, average molecular weight 695, hydroxyl value 900) and myristic acid (purity 99%, average molecular weight 228) 62 g (0.27 mol) with a heating jacket The reaction vessel was charged, 0.025 g of 25% sodium hydroxide (based on the total amount of raw materials: 0.0025 wt%) was added, the temperature was raised to 240 ° C. in a nitrogen stream and reacted for 3 hours, and then at 260 ° C. for 4 hours. The reaction was performed to obtain 234 g of decaglycerin myristic acid ester.
Example 1
608.4 g (56.84% by weight) of water at 60 ° C. 90 g (9.00% by weight) sugar, 30 g (3.00% by weight) skim milk powder, 1 g (0.10% by weight) guar gum, decaglycerin myristic acid 3 g (0.30 wt%) of an ester (cloud point of 100 ° C. or higher) and 1 g (0.10 wt%) of sodium hexametaphosphate were added and dissolved to obtain an aqueous phase portion. Separately, 300 g (30.00 wt%) of partially hydrogenated soybean oil heated to 70 ° C., 0.6 g (0.06 wt%) of lecithin, sucrose stearate (trade name Ryoto Sugar Ester, Mitsubishi Chemical Foods Co., Ltd.) S-270, HLB2) 3 g (0.30 wt%) and sucrose erucic acid ester (Mitsubishi Chemical Foods Co., Ltd. trade name Ryoto Sugar Ester ER-290, HLB2) 3 g (0.30 wt%) were dissolved. Oil phase part. The aqueous phase was put into this, and pre-emulsified with a propeller stirrer at 70 ° C. for 15 minutes. This pre-emulsified liquid was homogenized by pressurization with a primary pressure of 150 kg / cm 2 and a secondary pressure of 50 kg / cm 2 using a homogenizer (manufactured by APV Gaulin). Next, the obtained oil-in-water emulsion was sterilized at 130 ° C., immediately cooled to 10 ° C. or lower in ice water, and aged overnight in a refrigerator to obtain a whipped cream. About the obtained cream, as a result of evaluating the state of the cream by particle size measurement (HOLIBA-LA500) and visual observation, the particle size distribution is a sharp single peak, and the state in which the cream is thickened is not observed. The emulsified state was good.
Comparative Example 1
Instead of decaglycerin myristic acid ester (cloud point of 100 ° C. or higher), decaglycerin stearate ester (Mitsubishi Chemical Foods Co., Ltd. trade name Ryoto polyglycerester S-28D, cloud point of 50 ° C. or lower) 3 g (0.30% by weight) ) Was added and evaluated in the same manner as in Example except that was added to the aqueous phase. The cream after aging started to thicken and solidify and had a wide particle size distribution.
[0021]
【The invention's effect】
The oil-in-water emulsion of the present invention does not increase in viscosity or solidify even when sterilized, and is excellent in heat resistance and emulsion stability.
Claims (5)
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JPS58209947A (en) * | 1982-05-28 | 1983-12-07 | Asahi Denka Kogyo Kk | Preparation of acidic oil-in-water type emulsified fat |
JPH0648963B2 (en) * | 1985-03-11 | 1994-06-29 | アサヒフ−ズ株式会社 | Method for producing foamable oil-in-water emulsion composition |
JPS62275646A (en) * | 1986-02-04 | 1987-11-30 | Asahi Denka Kogyo Kk | Production of high-viscosity oil-in-water type emulsion |
JPS645465A (en) * | 1987-06-26 | 1989-01-10 | Nippon Oils & Fats Co Ltd | Gelatinous oil-in-water type emulsified composition |
JP2628902B2 (en) * | 1988-11-08 | 1997-07-09 | 旭電化工業株式会社 | Foamable oil-in-water emulsified fat |
JP2802945B2 (en) * | 1989-10-16 | 1998-09-24 | 雪印乳業株式会社 | Whipped cream and its manufacturing method |
JPH07108201B2 (en) * | 1991-01-09 | 1995-11-22 | 名古屋製酪株式会社 | Whipped cream composition |
JPH0678672A (en) * | 1992-08-31 | 1994-03-22 | Kanegafuchi Chem Ind Co Ltd | Oil-in-water type emulsion composition having high oil content |
JP3205415B2 (en) * | 1993-02-01 | 2001-09-04 | 鐘淵化学工業株式会社 | Foamable oil-in-water emulsion composition |
JP3202394B2 (en) * | 1993-03-24 | 2001-08-27 | 花王株式会社 | Foamable oil-in-water emulsion |
JP3301182B2 (en) * | 1993-11-24 | 2002-07-15 | 三菱化学株式会社 | Method for producing polyglycerin fatty acid ester |
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