JP4724094B2 - Margarine and shortening with low trans fatty acid content - Google Patents

Margarine and shortening with low trans fatty acid content Download PDF

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JP4724094B2
JP4724094B2 JP2006310029A JP2006310029A JP4724094B2 JP 4724094 B2 JP4724094 B2 JP 4724094B2 JP 2006310029 A JP2006310029 A JP 2006310029A JP 2006310029 A JP2006310029 A JP 2006310029A JP 4724094 B2 JP4724094 B2 JP 4724094B2
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敏弘 多治見
重平 栗山
佳郎 宮本
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Sakamoto Yakuhin Kogyo Co Ltd
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Description

本発明は、トランス脂肪酸の含有量が低く、安定性に優れたマーガリン、ショートニングに関するものである。   The present invention relates to margarine and shortening having a low trans fatty acid content and excellent stability.

従来、マーガリンおよびショートニングでは、好ましい硬さ、広い温度範囲での良好な可塑性、クリーミング性等を得るために、天然の動植物油脂に水素添加油脂を配合することが一般的に行われている。水素添加油脂を配合する方法は、マーガリン、ショートニングの融点を上昇させる典型的な方法であるが、完全水素添加油脂以外の水素添加油脂、即ち部分水素添加油脂には、通常、構成脂肪酸中にトランス脂肪酸が10〜50重量%程度含まれている。一方、天然油脂中にはトランス脂肪酸が殆ど存在せず、動物由来の油脂に10重量%未満含まれているにすぎない。トランス脂肪酸は、血液中のLDLコレステロールや中性脂肪の増加を促し、心臓血管病を引き起こすことが示唆されている。そのため、トランス脂肪酸を含まない、あるいは低減したマーガリン、ショートニングが望まれている。   Conventionally, in margarine and shortening, hydrogenated fats and oils are generally blended with natural animal and vegetable fats and oils in order to obtain preferable hardness, good plasticity in a wide temperature range, creaming properties, and the like. The method of blending hydrogenated fats and oils is a typical method for increasing the melting point of margarine and shortening. However, hydrogenated fats and oils other than fully hydrogenated fats and oils, that is, partially hydrogenated fats and oils, are usually converted into constituent fatty acids. About 10 to 50% by weight of fatty acid is contained. On the other hand, there are almost no trans fatty acids in natural fats and oils, and the fats and oils derived from animals contain only less than 10% by weight. It has been suggested that trans fatty acids promote the increase of LDL cholesterol and neutral fat in the blood and cause cardiovascular disease. Therefore, margarine and shortening containing no or reduced trans fatty acids are desired.

トランス脂肪酸を含まない、あるいは低減したマーガリン、ショートニング等の可塑性油脂組成物を得る方法としては、天然油脂を分別することによって得られる分別油脂を、適宜配合する方法(特許文献1)が行われているが、この方法では、好ましい硬さ、広い温度範囲での可塑性等を自由に設定することが難しい。例えば、液体油や分別軟部油等の低融点油脂に、極度硬化油や分別硬部油等の高融点油脂を配合するだけでは、広い温度域での可塑性を得るために、多量の高融点油脂を配合する必要があり、極めて口溶けの悪いものとなってしまう。更に、好ましい硬さを出すために、ラード、牛脂、パーム油等の高融点の天然油脂を用いた場合、これらの高融点の天然油脂は、粗大結晶化を生じやすい油脂であるため、製造後経日的に硬さが変化したり、滑らかさが低下して、ざらついた食感となってしまう。また、その他の方法としては、分別油脂と極度硬化油からなる油脂配合物をリパーゼによりエステル交換して部分的水素添加油脂の代替として利用する方法(特許文献2)、部分的水素添加油脂に液体油、パーム油系油脂を加えた油脂配合物をエステル交換し、トランス脂肪酸を低減した油脂として利用する方法(特許文献3)がある。しかし、この方法では、エステル交換を行うための反応設備が必要であり、また、リパーゼ等の高価な触媒を使用し、反応制御も行わねばならず、操作が煩雑で、コストが上昇するという問題点があった。   As a method for obtaining a plastic oil composition such as margarine or shortening that does not contain or reduce trans fatty acid, a method of appropriately mixing fractionated fats and oils obtained by fractionating natural fats and oils (Patent Document 1) is performed. However, in this method, it is difficult to freely set a preferable hardness, plasticity in a wide temperature range, and the like. For example, in order to obtain plasticity in a wide temperature range simply by blending high melting point oil such as extremely hardened oil and fractionated hard part oil with low melting point oil such as liquid oil and fractionated soft part oil, a large amount of high melting point fat and oil Needs to be blended, and it becomes extremely poorly melted in the mouth. Furthermore, when using high melting point natural fats and oils such as lard, beef tallow and palm oil in order to obtain a preferable hardness, these high melting point natural fats and oils are prone to coarse crystallization, so The hardness changes over time or the smoothness decreases, resulting in a rough texture. In addition, as other methods, a method of using a fat composition comprising fractionated fat and extremely hardened oil as a substitute for partially hydrogenated fat by transesterifying with lipase (Patent Document 2), liquid to partially hydrogenated fat There is a method (Patent Document 3) in which an oil / fat mixture to which oil and palm oil-based fat / oil are added is transesterified and used as a fat / fat with reduced trans fatty acid. However, this method requires a reaction facility for transesterification, and requires an expensive catalyst such as lipase, and also requires reaction control, which is complicated and increases costs. There was a point.

特開2004−121114号公報JP 2004-121114 A 特開2006−160906号公報JP 2006-160906 A 特開2005−120386号公報JP-A-2005-120386

従って、本発明では、エステル交換の様な特殊工程を経ることなく低コストで簡単に製造でき、高融点油脂による粗大結晶化や口溶けの悪化がなく、経日的な安定性にも優れ、且つ、トランス脂肪酸含有量が低いマーガリン、ショートニングおよび、これを用いてなる外観、食感の良好な食品を提供することを目的とするものである。   Therefore, in the present invention, it can be easily produced at low cost without passing through a special process such as transesterification, there is no deterioration of coarse crystallization or melting in the mouth due to a high melting point oil and fat, and excellent stability over time, and It is an object of the present invention to provide margarine, shortening having a low trans fatty acid content, and a food having a good appearance and texture using the same.

本発明者が鋭意研究を重ねた結果、マーガリン、ショートニングに油脂を30%以上含有させて、高融点油脂の使用量を減らし、特定の脂肪酸組成を有したポリグリセリン脂肪酸エステルを含有させることで、上記課題が達成されることを見出し、本発明を完成するに至った。   As a result of extensive research by the inventor, margarine and shortening contain 30% or more of fats and oils, reduce the amount of high melting point oils and fats, and contain polyglycerin fatty acid esters having a specific fatty acid composition. The inventors have found that the above problems can be achieved and have completed the present invention.

即ち、本発明は、20℃で液体である油脂を30%以上含有させ、更に、ポリグリセリン脂肪酸エステルを構成する脂肪酸に、(A)ベヘン酸を必須とする炭素数が16〜22の飽和脂肪酸から選択される一種または二種以上と、(B)炭素数が8〜14の飽和脂肪酸および炭素数が16〜22の不飽和脂肪酸から選択される一種または二種以上と、を有し、構成脂肪酸(A)および(B)の総モル量において、構成脂肪酸(A)のモル比率が0.3〜0.9、且つベヘン酸0.2〜0.8、構成脂肪酸(B)のモル比率が0.1〜0.7、となるポリグリセリン脂肪酸エステルであり、そのエステル化率が40%以上であって、前記ポリグリセリン脂肪酸エステルを含有させることを特徴としたマーガリンやショートニングに関する。 That is, the present invention contains 30% or more of oils and fats that are liquid at 20 ° C., and (A) a saturated fatty acid having 16 to 22 carbon atoms in which behenic acid is essential in the fatty acid constituting the polyglycerol fatty acid ester. And one or more selected from (B) a saturated fatty acid having 8 to 14 carbon atoms and one or two or more selected from unsaturated fatty acids having 16 to 22 carbon atoms. In the total molar amount of the fatty acids (A) and (B), the molar ratio of the constituent fatty acid (A) is 0.3 to 0.9, and the behenic acid 0.2 to 0.8, the molar ratio of the constituent fatty acid (B) The present invention relates to margarine and shortening, characterized in that the polyglycerin fatty acid ester is 0.1 to 0.7, the esterification rate is 40% or more, and the polyglycerin fatty acid ester is contained.

本発明は、前記マーガリンまたはショートニングを用いてなる食品である。   The present invention is a food product using the margarine or shortening.

本発明によれば、トランス脂肪酸含有量が低く、高融点油脂による粗大結晶化や口溶けの悪化がなく、経日的に、高融点油脂が沈殿したり、液体油が分離する等の固液分離を生じることもない安定性に優れたマーガリン、ショートニングおよび、これを用いてなる食品を提供することができる。   According to the present invention, the content of trans fatty acid is low, there is no deterioration of coarse crystallization or melting in the mouth due to high melting point oil and fat, and high melting point oil or fat precipitates or liquid oil separates over time. It is possible to provide margarine, shortening, and a food product using the same, which are excellent in stability without causing odor.

本発明を実施形態に基づき以下に説明する。本実施形態のポリグリセリン脂肪酸エステルは、所定の脂肪酸を構成脂肪酸とし、その構成脂肪酸のモル比率が限定されたものとなっている。ポリグリセリン脂肪酸エステルを構成する脂肪酸は、ベヘン酸を必須とする炭素数が16〜22の飽和脂肪酸から選択される一種または二種以上と、炭素数が8〜14の飽和脂肪酸および炭素数が16〜22の不飽和脂肪酸から選択される一種または二種以上とを有している。 The present invention will be described below based on embodiments. The polyglycerol fatty acid ester of the present embodiment has a predetermined fatty acid as a constituent fatty acid, and the molar ratio of the constituent fatty acid is limited. The fatty acid constituting the polyglycerin fatty acid ester is one or two or more selected from saturated fatty acids having 16 to 22 carbon atoms essential for behenic acid , saturated fatty acids having 8 to 14 carbon atoms, and 16 carbon atoms. 1 type or 2 types or more selected from -22 unsaturated fatty acids.

炭素数が16〜22の飽和脂肪酸、炭素数が8〜14の飽和脂肪酸、および炭素数が16〜22の不飽和脂肪酸は、この炭素数および飽和または不飽和の条件に当てはまるものであれば、特に限定されるものではないが、主として直鎖脂肪酸が選択される。炭素数が16〜22の飽和脂肪酸には、パルミチン酸、ステアリン酸、アラキン酸、ベヘン酸等が、炭素数が8〜14の飽和脂肪酸には、カプリル酸、カプリン酸、ラウリン酸、ミリスチン酸が、炭素数16〜22の不飽和脂肪酸には、パルミトレイン酸、オレイン酸、エライジン酸、リノール酸、リノレン酸、アラキドン酸、エルカ酸、エイコサペンタエン酸、ドコサヘキサエン酸が、例示される。   If the saturated fatty acid having 16 to 22 carbon atoms, the saturated fatty acid having 8 to 14 carbon atoms, and the unsaturated fatty acid having 16 to 22 carbon atoms are applicable to the conditions of the carbon number and saturated or unsaturated, Although not particularly limited, linear fatty acids are mainly selected. Saturated fatty acids having 16 to 22 carbon atoms include palmitic acid, stearic acid, arachidic acid, and behenic acid, and saturated fatty acids having 8 to 14 carbon atoms include caprylic acid, capric acid, lauric acid, and myristic acid. Examples of the unsaturated fatty acid having 16 to 22 carbon atoms include palmitoleic acid, oleic acid, elaidic acid, linoleic acid, linolenic acid, arachidonic acid, erucic acid, eicosapentaenoic acid, and docosahexaenoic acid.

ポリグリセリン脂肪酸エステルの構成脂肪酸中における各脂肪酸のモル比率は、
(A):ベヘン酸を必須とする炭素数が16〜22の飽和脂肪酸から選択される一種または二種以上、
(B):炭素数が8〜14の飽和脂肪酸および炭素数が16〜22の不飽和脂肪酸から選択される一種または二種以上、
であり、(A)および(B)の総モル量において、(A)のモル比率が0.3〜0.9、且つベヘン酸0.2〜0.8、(B)のモル比率が0.1〜0.7、となる必要がある。特に、(A)のモル比率が0.6〜0.9であることがより好適である。
The molar ratio of each fatty acid in the constituent fatty acids of the polyglycerin fatty acid ester is
(A): one or two or more selected from saturated fatty acids having 16 to 22 carbon atoms and essentially containing behenic acid ,
(B): one or more selected from saturated fatty acids having 8 to 14 carbon atoms and unsaturated fatty acids having 16 to 22 carbon atoms,
In the total molar amount of (A) and (B), the molar ratio of (A) is 0.3 to 0.9 and behenic acid 0.2 to 0.8, and the molar ratio of (B) is 0. .1 to 0.7. In particular, the molar ratio of (A) is more preferably 0.6 to 0.9.

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は、その平均重合度が限定されるものではないが、2〜20であると良い。ここで、平均重合度は、末端基分析法による水酸基価から算出されるポリグリセリンの平均重合度(n)である。詳しくは、次式(式1)および(式2)から平均重合度が算出される。
(式1)分子量=74n+18
(式2)水酸基価=56110(n+2)/分子量
上記(式2)中の水酸基価とは、ポリグリセリンに含まれる水酸基数の大小の指標となる数値であり、1gのポリグリセリンに含まれる遊離ヒドロキシル基をアセチル化するために必要な酢酸を中和するのに要する水酸化カリウムのミリグラム数をいう。水酸化カリウムのミリグラム数は、社団法人日本油化学会編纂「日本油化学会制定、基準油脂分析試験法(I)、2003年度版」に準じて算出される。
The average degree of polymerization of the polyglycerol constituting the polyglycerol fatty acid ester is not limited, but is preferably 2 to 20. Here, the average degree of polymerization is the average degree of polymerization (n) of polyglycerin calculated from the hydroxyl value by end group analysis. Specifically, the average degree of polymerization is calculated from the following formulas (Formula 1) and (Formula 2).
(Formula 1) Molecular weight = 74n + 18
(Formula 2) Hydroxyl value = 56110 (n + 2) / Molecular weight The hydroxyl value in the above (Formula 2) is a numerical value that serves as an index of the number of hydroxyl groups contained in polyglycerin, and is contained in 1 g of polyglycerin. The number of milligrams of potassium hydroxide required to neutralize the acetic acid required to acetylate the hydroxyl group. The number of milligrams of potassium hydroxide is calculated according to Japan Oil Chemists 'Society edited by “The Japan Oil Chemists' Society, Standard Oil Analysis Test Method (I), 2003 edition”.

本実施形態のポリグリセリン脂肪酸エステルは、エステル化率が高まるほど、油脂組成物の固液分離防止効果および油脂組成物中での分散性が高まることになるので、エステル化率が40%以上である必要がある。ここで、エステル化率とは、末端基分析法による水酸基価から算出されるポリグリセリンの平均重合度(n)、このポリグリセリンが有する水酸基数(n+2)、ポリグリセリンに付加している脂肪酸のモル数(M)としたとき、(M/(n+2))×100=エステル化率(%)で算出される値である。なお、水酸基価とは、上述の水酸基価と同様に算出される値である。   Since the polyglycerin fatty acid ester of this embodiment increases the esterification rate, the solid-liquid separation preventing effect of the oil / fat composition and the dispersibility in the oil / fat composition increase, so the esterification rate is 40% or more. There must be. Here, the esterification rate is the average degree of polymerization of polyglycerol (n) calculated from the hydroxyl value by end group analysis, the number of hydroxyl groups (n + 2) of this polyglycerol, and the fatty acid added to the polyglycerol. When the number of moles is (M), (M / (n + 2)) × 100 = value calculated by esterification rate (%). The hydroxyl value is a value calculated in the same manner as the hydroxyl value described above.

本実施形態のポリグリセリン脂肪酸エステルは、公知のエステル化反応により製造することができる。例えば、脂肪酸とポリグリセリンとを水酸化ナトリウム等のアルカリ触媒の存在下におけるエステル化反応により製造することができる。エステル化反応は、仕込んだ脂肪酸のほぼ全てがエステル化するまで反応させる。即ち、遊離の脂肪酸が殆どなくなるまで十分に反応させる。   The polyglycerol fatty acid ester of the present embodiment can be produced by a known esterification reaction. For example, a fatty acid and polyglycerin can be produced by an esterification reaction in the presence of an alkali catalyst such as sodium hydroxide. The esterification reaction is performed until almost all of the charged fatty acid is esterified. That is, the reaction is sufficiently performed until almost no free fatty acid is consumed.

本実施形態におけるマーガリン、ショートニングに用いられる20℃で液体の油脂は、30%以上含有させる必要があり、より好ましくは50%以上含有させると良い。20℃で液体の油脂とは、限定されるものではないが、例えば大豆油、ナタネ油、コーン油、ゴマ油、シソ油、亜麻仁油、落花生油、紅花油、高オレイン酸紅花油、綿実油、ぶどう種子油、マカデミアナッツ油、ヘーゼルナッツ油、かぼちゃ種子油、クルミ油、椿油、茶実油、エゴマ油、オリーブ油、カラシ油、米油、米糠油、小麦麦芽油、サフラワー油、ひまわり油およびこれらの分別油脂が例示される。更に、ジグリセライドおよび/またはモノグリセライドが含有または調合されているものであっても良い。また、油脂にはステロールやステロールエステル等が任意に含有されていても良い。その他油脂として、パーム油、パーム核油、カカオ脂、ヤシ油、ラード、乳脂、鶏脂、牛脂およびこれらの分別油脂を適宜使用することができる。   The oil / fat that is liquid at 20 ° C. used for margarine and shortening in the present embodiment needs to be contained in an amount of 30% or more, more preferably 50% or more. Examples of oils and fats that are liquid at 20 ° C. include, but are not limited to, soybean oil, rapeseed oil, corn oil, sesame oil, perilla oil, linseed oil, peanut oil, safflower oil, safflower oil with high oleic acid, cottonseed oil, grape Seed oil, macadamia nut oil, hazelnut oil, pumpkin seed oil, walnut oil, coconut oil, tea seed oil, egoma oil, olive oil, mustard oil, rice oil, rice bran oil, wheat germ oil, safflower oil, sunflower oil and fractionation thereof Oils and fats are exemplified. Furthermore, diglyceride and / or monoglyceride may be contained or formulated. Moreover, sterol, sterol ester, etc. may contain arbitrarily in fats and oils. As other fats and oils, palm oil, palm kernel oil, cocoa butter, coconut oil, lard, milk fat, chicken fat, beef tallow, and fractionated fats and oils thereof can be appropriately used.

本実施形態におけるマーガリン、ショートニングには必要に応じ、一般的にマーガリン、ショートニングに使用されている他の原料、例えば、プロピレングリコール脂肪酸エステル、ソルビタン脂肪酸エステル、ショ糖脂肪酸エステル、リン脂質等の乳化剤、トコフェロール、L−アスコルビン酸パルミチン酸エステル、茶抽出物等の酸化防止剤、カロチン等の着色料、脱脂粉乳、クリーム等の乳成分、蔗糖、液糖、はちみつ、ブドウ糖、果糖、黒糖、麦芽糖、乳糖、水飴、ソルビトール、エリスリトール、異性化液糖、ショ糖結合飴、オリゴ糖、トレハロース、ヘミセルロース等の糖類、水、食塩、酸味料、調味料、香料、重合リン酸塩等の乳化安定剤、ローカストビーンガム、カラギーナン、アルギン酸類、ペクチン、キサンタンガム、寒天、グルコマンナン、ゼラチン、化工澱粉、澱粉等の増粘安定剤等を、適宜使用することができる。   In the present embodiment, if necessary for margarine and shortening, margarine, other raw materials generally used for shortening, for example, propylene glycol fatty acid ester, sorbitan fatty acid ester, sucrose fatty acid ester, emulsifier such as phospholipid, Tocopherol, L-ascorbic acid palmitate, antioxidants such as tea extract, coloring agents such as carotene, milk components such as skim milk powder, cream, sucrose, liquid sugar, honey, glucose, fructose, brown sugar, maltose, lactose , Syrup, sorbitol, erythritol, isomerized liquid sugar, sucrose-bonded syrup, oligosaccharides, trehalose, hemicellulose and other saccharides, water, salt, acidulant, seasoning, flavor, polymerized phosphate and other emulsion stabilizers, locust Bean gum, carrageenan, alginic acids, pectin, xanthan gum, Heaven, glucomannan, gelatin, modified starch, a thickening stabilizer such as starch, etc., can be appropriately used.

本実施形態のポリグリセリン脂肪酸エステルを添加したマーガリン、ショートニングは、経日的な油脂の粗大結晶化や固液分離が抑えられるため、可塑性、展延性、ショートニング性、クリーミング性等の物理的性質が好適に付与されてなり、食品に使用することが可能である。   The margarine and shortening to which the polyglycerin fatty acid ester of the present embodiment is added can suppress physical crystallization and solid-liquid separation of oils and fats over time, so that physical properties such as plasticity, spreadability, shortening property, and creaming property are present. It is suitably applied and can be used for food.

本実施形態におけるポリグリセリン脂肪酸エステルは、その使用量の増加と共により多くの液体の油脂を配合でき、高融点油脂による口溶けの悪化や固液分離を抑制できる。ポリグリセリン脂肪酸エステルの使用量は、油脂組成物中、0.01〜10.0重量%となる量であると良く、より好ましくは0.5重量%以上である。   The polyglycerin fatty acid ester in the present embodiment can be blended with more liquid oils and fats with an increase in the amount of use thereof, and can suppress deterioration of mouth melting and solid-liquid separation due to high melting point oils and fats. The usage-amount of polyglyceryl fatty acid ester may be the quantity used as 0.01-10.0 weight% in an oil-fat composition, More preferably, it is 0.5 weight% or more.

本実施形態のマーガリン、ショートニングは、ポリグリセリン脂肪酸エステルの含有量が少量であるので、食品の風味の悪化が抑えられる。本発明のマーガリン、ショートニングを利用してなる食品としては、通常のマーガリン、ショートニングを用いる食品であれば、特に限定はないが、具体的には、食パン、菓子パン、デニッシュ・ペストリー、パイ、シュー、ドーナツ、ケーキ、クッキー、ワッフル、マフィン、ハードビスケット、スコーン等のベーカリー製品に使用することができる。また、これらの用途における本発明のマーガリン、ショートニングの使用量は、使用用途により異なるものであり、特に限定されるものではない。   Since the margarine and shortening of this embodiment have a small amount of polyglycerin fatty acid ester, the deterioration of the flavor of food can be suppressed. The margarine and shortening food of the present invention is not particularly limited as long as it is a normal margarine or shortening food, but specifically, bread, confectionery bread, Danish pastry, pie, shoe, It can be used for bakery products such as donuts, cakes, cookies, waffles, muffins, hard biscuits and scones. Moreover, the usage-amount of the margarine and shortening of this invention in these uses changes with use uses, and is not specifically limited.

以下に実施例に基づいて本発明を具体的に説明するが、本発明は、実施例に限定されるものではない。尚、実施例及び比較例において、平均重合度が10のポリグリセリンに阪本薬品工業株式会社製「ポリグリセリン#750」を、平均重合度が6のポリグリセリンに阪本薬品工業株式会社製「ポリグリセリン#500」を、平均重合度が4のポリグリセリンに阪本薬品工業株式会社製「ポリグリセリン#310」を使用した。   EXAMPLES The present invention will be specifically described below based on examples, but the present invention is not limited to the examples. In Examples and Comparative Examples, “polyglycerin # 750” manufactured by Sakamoto Yakuhin Kogyo Co., Ltd. was used for polyglycerin having an average polymerization degree of 10, and “polyglycerin” manufactured by Sakamoto Yakuhin Kogyo Co., Ltd. was used for polyglycerin having an average polymerization degree of 6. “Polyglycerin # 310” manufactured by Sakamoto Yakuhin Kogyo Co., Ltd. was used as polyglycerin having an average degree of polymerization of “# 500”.

<実施例1>
平均重合度が10のポリグリセリン100gとカプリン酸82.6g、ベヘン酸326.4gから成る混合脂肪酸を反応容器に入れ、水酸化ナトリウムによるアルカリ性および窒素気流下、250℃で反応させ、エステル化率90%のポリグリセリン脂肪酸エステルを得た。
<Example 1>
Esterification rate: 100 g of polyglycerin having an average degree of polymerization of 10 and a mixed fatty acid consisting of 82.6 g of capric acid and 326.4 g of behenic acid are placed in a reaction vessel and reacted at 250 ° C. in an alkaline and nitrogen stream with sodium hydroxide. 90% polyglycerol fatty acid ester was obtained.

<実施例2>
平均重合度が4のポリグリセリン100gとミリスチン酸103.0g、ベヘン酸307.3gから成る混合脂肪酸を反応容器に入れ、水酸化ナトリウムによるアルカリ性および窒素気流下、250℃で反応させ、エステル化率70%のポリグリセリン脂肪酸エステルを得た。
<Example 2>
Esterification rate: 100 g of polyglycerin having an average degree of polymerization of 4, mixed fatty acid consisting of 103.0 g of myristic acid and 307.3 g of behenic acid was placed in a reaction vessel and reacted at 250 ° C. in an alkaline and nitrogen stream with sodium hydroxide. 70% polyglycerol fatty acid ester was obtained.

<実施例3>
平均重合度が10のポリグリセリン100gとオレイン酸81.2g、ベヘン酸391.7gから成る混合脂肪酸を反応容器に入れ、水酸化ナトリウムによるアルカリ性および窒素気流下、250℃で反応させ、エステル化率90%のポリグリセリン脂肪酸エステルを得た。
<Example 3>
Esterification rate: 100 g of polyglycerin having an average degree of polymerization of 10 and a mixed fatty acid consisting of 81.2 g of oleic acid and 391.7 g of behenic acid are placed in a reaction vessel and reacted at 250 ° C. in an alkaline and nitrogen stream with sodium hydroxide. 90% polyglycerol fatty acid ester was obtained.

<実施例4>
平均重合度が10のポリグリセリン100gとステアリン酸86.3g、ベヘン酸310.0g、オレイン酸85.7gから成る混合脂肪酸を反応容器に入れ、水酸化ナトリウムによるアルカリ性および窒素気流下、250℃で反応させ、エステル化率95%のポリグリセリン脂肪酸エステルを得た。
<Example 4>
A mixed fatty acid consisting of 100 g of polyglycerin having an average degree of polymerization of 10 and 86.3 g of stearic acid, 310.0 g of behenic acid, and 85.7 g of oleic acid is placed in a reaction vessel, and at 250 ° C. under alkaline and nitrogen flow with sodium hydroxide. The reaction was performed to obtain a polyglycerol fatty acid ester having an esterification rate of 95%.

<実施例5>
平均重合度が6のポリグリセリン100gとラウリン酸38.4g、ステアリン酸54.5g、ベヘン酸195.8gから成る混合脂肪酸を反応容器に入れ、水酸化ナトリウムによるアルカリ性および窒素気流下、250℃で反応させ、エステル化率60%のポリグリセリン脂肪酸エステルを得た。
<Example 5>
A mixed fatty acid consisting of 100 g of polyglycerin having an average degree of polymerization of 6 and 38.4 g of lauric acid, 54.5 g of stearic acid, and 195.8 g of behenic acid is placed in a reaction vessel, and at 250 ° C. under alkaline and nitrogen flow with sodium hydroxide. The reaction was performed to obtain a polyglycerol fatty acid ester having an esterification rate of 60%.

<実施例6>
平均重合度が4のポリグリセリン100gとカプリン酸53.3g、ステアリン酸263.8g、ベヘン酸105.3gから成る混合脂肪酸を反応容器に入れ、水酸化ナトリウムによるアルカリ性および窒素気流下、250℃で反応させ、エステル化率80%のポリグリセリン脂肪酸エステルを得た。
<Example 6>
A mixed fatty acid composed of 100 g of polyglycerin having an average degree of polymerization of 4 and 53.3 g of capric acid, 263.8 g of stearic acid, and 105.3 g of behenic acid was placed in a reaction vessel, and the mixture was alkalinized with sodium hydroxide and under a nitrogen stream at 250 ° C. Reaction was performed to obtain a polyglycerol fatty acid ester having an esterification rate of 80%.

<比較例1>
平均重合度が10のポリグリセリン100gとパルミチン酸81.9gを反応容器に入れ、水酸化ナトリウムによるアルカリ性および窒素気流下、250℃で反応させ、エステル化率20%のポリグリセリン脂肪酸エステルを得た。
<Comparative Example 1>
100 g of polyglycerin having an average degree of polymerization of 10 and 81.9 g of palmitic acid were placed in a reaction vessel and reacted at 250 ° C. in an alkaline and nitrogen stream with sodium hydroxide to obtain a polyglycerin fatty acid ester having an esterification rate of 20%. .

<比較例2>
平均重合度が6のポリグリセリン100gとパルミチン酸102.4g、ステアリン酸を113.6gから成る混合脂肪酸を反応容器に入れ、水酸化ナトリウムによるアルカリ性および窒素気流下、250℃で反応させ、エステル化率50%のポリグリセリン脂肪酸エステルを得た。
<Comparative example 2>
Esterification is performed by adding a mixed fatty acid consisting of 100 g of polyglycerin having an average polymerization degree of 6, 102.4 g of palmitic acid and 113.6 g of stearic acid to a reaction vessel at 250 ° C. in an alkaline and nitrogen stream with sodium hydroxide. A 50% polyglycerol fatty acid ester was obtained.

以上の実施例および比較例のポリグリセリン脂肪酸エステルを表1に示した。尚、表1中、モル比率は、ポリグリセリン脂肪酸エステルを構成する脂肪酸の全モル量に対する各構成脂肪酸の比率である。表1に示したポリグリセリン脂肪酸エステルを次の試験例1に基づき、マーガリンでの安定性に対する効果を確認した。   The polyglycerol fatty acid esters of the above Examples and Comparative Examples are shown in Table 1. In Table 1, the molar ratio is the ratio of each constituent fatty acid to the total molar amount of fatty acid constituting the polyglycerol fatty acid ester. Based on the following Test Example 1, the polyglycerin fatty acid ester shown in Table 1 was confirmed to have an effect on the stability with margarine.

Figure 0004724094
Figure 0004724094

[試験例1]
マーガリンの安定性
表2に示す配合に従い、精製パーム油と大豆油からなる原料油脂に対して実施例および比較例のエステルを1重量%含有させた油脂組成物とし、80℃まで加温、溶解したものを油相とした。一方、水に食塩、脱脂粉乳、大豆レシチン、香料を加えて溶解し、70℃まで加温したものを水相とした。油相中に水相を徐々に加えて油中水型に乳化した後、通常のマーガリン製造工程に従い、冷却、捏和によりマーガリンを調製した。次いで、マーガリンを容器に充填し、20℃のインキュベータ内にて1日保存後、状態を目視にて確認した。また、表3に示すナタネ極度硬化油と大豆油を原料油脂とした配合のマーガリンについても同様に、各実施例および比較例のエステルを1重量%含有させてマーガリンを調製し、20℃のインキュベータ内にて1日保存後、状態を目視にて確認した。
[Test Example 1]
Stability of margarine According to the formulation shown in Table 2, an oil / fat composition containing 1% by weight of the ester of Examples and Comparative Examples with respect to raw oil / fat composed of refined palm oil and soybean oil was heated to 80 ° C. and dissolved. This was used as the oil phase. On the other hand, salt, skim milk powder, soybean lecithin, and flavor were added to water, dissolved, and heated to 70 ° C. to obtain an aqueous phase. After gradually adding an aqueous phase to the oil phase and emulsifying it into a water-in-oil type, margarine was prepared by cooling and kneading in accordance with a normal margarine production process. Next, the container was filled with margarine and stored in a 20 ° C. incubator for 1 day, and the state was visually confirmed. Similarly, for margarine formulated with rapeseed extremely hardened oil and soybean oil as raw material fats and oils shown in Table 3, margarine was prepared by containing 1% by weight of the esters of each Example and Comparative Example, and an incubator at 20 ° C. After storage for 1 day, the state was visually confirmed.

Figure 0004724094
Figure 0004724094

Figure 0004724094
Figure 0004724094

試験例1の評価を、マーガリンの状態を基準に次の通り行った。
◎:固液分離は全く見られなく、均一な状態である。
○:表面に斑点上の液体油が若干見られる。
△:表面にかなりの液体油が見られる。
×:固液分離が発生し、完全に分離している。
試験例1の結果を表4に示す。
Evaluation of Test Example 1 was performed as follows based on the state of margarine.
A: Solid-liquid separation is not seen at all, and it is in a uniform state.
○: Some liquid oil on the surface is spotted.
Δ: A considerable amount of liquid oil is observed on the surface.
X: Solid-liquid separation occurs and is completely separated.
The results of Test Example 1 are shown in Table 4.

Figure 0004724094
Figure 0004724094

表4に示す通り、比較例1、2のエステルを添加したマーガリンは、固液分離が生じた。一方、本願発明のポリグリセリン脂肪酸エステルである実施例のエステルを添加したマーガリンは何れも固液分離が生じておらず、均一で滑らかな状態であった。   As shown in Table 4, solid-liquid separation occurred in the margarine to which the esters of Comparative Examples 1 and 2 were added. On the other hand, none of the margarine to which the ester of the example which is the polyglycerin fatty acid ester of the present invention was added had a solid-liquid separation, and was in a uniform and smooth state.

次に、以下の試験例2に基づき、実施例および比較例のエステルを添加して調製したマーガリンを用いて、ロールパンを焼成し、得られたロールパンの内相のキメ、食感について確認試験を行う。   Next, based on Test Example 2 below, using margarine prepared by adding the esters of Examples and Comparative Examples, the bread roll was baked, and the confirmation test for texture and texture of the inner phase of the roll bread thus obtained was conducted. Do.

[試験例2]
表5に示す配合に従い、強力粉、薄力粉、砂糖、イーストフード、食塩、脱脂粉乳を混合後、イースト、全卵を加えミキシングする。その後、実施例および比較例のマーガリンを加え、28℃になるよう捏上げ、50分予備発酵をさせる。続いて、パンチ後、フロアタイム30分で発酵を行い、分割し、ベンチタイム30分後、成形してホイロ38℃・50分、焼成200℃・10分でロールパンを作成する。このロールパンの内相のキメ、食感について確認試験を行う。この試験の代表結果を表6に示す。
[Test Example 2]
In accordance with the formulation shown in Table 5, after mixing strong powder, soft flour, sugar, yeast food, salt, and skim milk powder, yeast and whole eggs are added and mixed. Then, the margarine of an Example and a comparative example is added, and it raises to 28 degreeC, and makes 50 minutes pre-fermentation. Then, after punching, fermentation is performed at a floor time of 30 minutes, divided, and after a bench time of 30 minutes, it is molded to produce a roll bread at a proof of 38 ° C. for 50 minutes and a baking temperature of 200 ° C. for 10 minutes. A confirmation test is performed on the texture and texture of the inner phase of this bread roll. Table 6 shows the representative results of this test.

Figure 0004724094
Figure 0004724094

試験例2の評価を、ロールパンの内相のキメ、食感を基準に次の通り行う。
○:良好
△:やや劣る
×:劣る
Evaluation of Test Example 2 is performed as follows based on the texture and texture of the inner phase of the roll.
○: Good △: Slightly inferior ×: Inferior

Figure 0004724094
Figure 0004724094

表6に示す通り、固液分離を生じていた比較例1のマーガリンを用いたロールパンは内相のキメが悪く、食感は硬いものとなる。一方、本願発明のポリグリセリン脂肪酸エステルである実施例のエステルを添加したマーガリンを用いたロールパンは内相のキメが良好で、ソフトで柔らかい食感となる。   As shown in Table 6, the roll using the margarine of Comparative Example 1 that had caused solid-liquid separation had a poor texture in the inner phase, and the texture was hard. On the other hand, roll bread using margarine to which the ester of the embodiment which is the polyglycerin fatty acid ester of the present invention is added has a good texture of the inner phase, and has a soft and soft texture.

続いて、表1に示した実施例および比較例のエステルを以下の試験例3に基づき、ショートニングでの安定性に対する効果を確認した。   Subsequently, the effects of the esters of Examples and Comparative Examples shown in Table 1 on the stability in shortening were confirmed based on Test Example 3 below.

[試験例3]
ショートニングの安定性
80℃に加熱した精製パーム油と大豆油を30:70の割合で混合し、これに実施例および比較例のエステルを1重量%、3重量%含有させ、80℃まで加熱、溶解した後、通常のショートニング製造工程に従い、冷却、捏和し、ショートニングを得た。次いで、ショートニングを容器に充填し、20℃のインキュベータ内にて1日テンパリングを行った後、状態を目視にて確認した。また、ナタネ極度硬化油と大豆油を3:97の割合で混合し、実施例および比較例のエステルを1重量%、3重量%含有させて調製したショートニングについても、20℃のインキュベータ内にて1日テンパリングを行った後、状態を目視にて確認した。
[Test Example 3]
Stability of shortening Refined palm oil heated to 80 ° C. and soybean oil were mixed at a ratio of 30:70, and 1% by weight and 3% by weight of the esters of Examples and Comparative Examples were added thereto, and heated to 80 ° C. After dissolution, cooling and kneading were performed according to a normal shortening manufacturing process to obtain a shortening. Subsequently, the shortening was filled in the container, and after tempering for one day in a 20 ° C. incubator, the state was visually confirmed. Also, shortening prepared by mixing rapeseed extremely hardened oil and soybean oil in a ratio of 3:97 and containing 1% by weight and 3% by weight of the esters of Examples and Comparative Examples was performed in an incubator at 20 ° C. After tempering for one day, the state was visually confirmed.

試験例3の評価を、ショートニングの状態を基準に次の通り行った。
◎:固液分離は全く見られなく、均一な状態である。
○:表面に斑点上の液体油が若干見られる。
△:表面にかなりの液体油が見られる。
×:固液分離が発生し、完全に分離している。
試験例3の結果を表7に示す。
Evaluation of Test Example 3 was performed as follows based on the shortening state.
A: Solid-liquid separation is not seen at all, and it is in a uniform state.
○: Some liquid oil on the surface is spotted.
Δ: A considerable amount of liquid oil is observed on the surface.
X: Solid-liquid separation occurs and is completely separated.
The results of Test Example 3 are shown in Table 7.

Figure 0004724094
Figure 0004724094

表7に示す通り、比較例1、2は固液分離を生じていた。一方、本願発明のポリグリセリン脂肪酸エステルである実施例のエステルを添加したショートニングは何れも固液分離が生じておらず、均一で滑らかな状態であった。   As shown in Table 7, Comparative Examples 1 and 2 caused solid-liquid separation. On the other hand, the shortening to which the ester of the example which is the polyglycerin fatty acid ester of the present invention was added had no solid-liquid separation, and was in a uniform and smooth state.

次に、以下の試験例4に基づき、実施例および比較例のエステルを3重量%添加して調製したショートニングを用いて、バターケーキを焼成し、得られたバターケーキの内相のキメ、食感について確認試験を行った。   Next, the butter cake was baked using the shortening prepared by adding 3 wt% of the esters of Examples and Comparative Examples based on Test Example 4 below, and the texture and food of the inner phase of the resulting butter cake were baked. A confirmation test was conducted for feeling.

[試験例4]
ケーキ生地の作成は表8に示す配合に従い、シュガーバッター法に準じて行った。したがって、ポリグリセリン脂肪酸エステルを添加して調製したショートニングを数分間攪拌後、砂糖を加えて比重が0.8になるまで攪拌した。次に、全卵を4回に分けて加え、均一に混合されるまで攪拌した。これに、薄力粉、ベーキングパウダー、水を加え均一になるまで攪拌し、ケーキ生地とした。このケーキ生地をパウンド型に入れ、オーブンで約50分間焼成し、バターケーキを作成した。得られたバターケーキの内相のキメ、食感について確認試験を行った。この試験の代表結果を表9に示す。
[Test Example 4]
The cake dough was produced according to the formulation shown in Table 8 and according to the sugar batter method. Therefore, the shortening prepared by adding the polyglycerin fatty acid ester was stirred for several minutes, then added with sugar and stirred until the specific gravity reached 0.8. Next, the whole egg was added in four portions and stirred until evenly mixed. To this, weak flour, baking powder and water were added and stirred until uniform to obtain a cake dough. This cake dough was put in a pound mold and baked in an oven for about 50 minutes to prepare a butter cake. A confirmation test was conducted on the texture and texture of the inner phase of the obtained butter cake. The representative results of this test are shown in Table 9.

Figure 0004724094
Figure 0004724094

試験例4の評価を、バターケーキの内相のキメ、食感を基準に次の通り行った。
○:良好
△:やや劣る
×:劣る
Evaluation of Test Example 4 was performed as follows based on the texture and texture of the inner phase of the butter cake.
○: Good △: Slightly inferior ×: Inferior

Figure 0004724094
Figure 0004724094

表9に示す通り、固液分離を生じていた比較例のショートニングを用いたバターケーキは内相のキメが悪く、食感は硬いものとなった。一方、本願発明のポリグリセリン脂肪酸エステルである実施例のエステルを添加したショートニングを用いたバターケーキは内相のキメが良好で、ソフトで柔らかい食感となった。   As shown in Table 9, the butter cake using the shortening of the comparative example, which had caused solid-liquid separation, had a poor texture in the inner phase and a hard texture. On the other hand, the butter cake using the shortening to which the ester of the example which is the polyglycerin fatty acid ester of the present invention was added had a good texture of the inner phase and had a soft and soft texture.

Claims (2)

20℃で液体である油脂を30%以上含有し、且つ、下記条件を満たすポリグリセリン脂肪酸エステルを含有するマーガリンまたはショートニング。
ポリグリセリン脂肪酸エステルの構成脂肪酸及び構成脂肪酸中における各脂肪酸のモル比率が、
(A):ベヘン酸を必須とする炭素数が16〜22の飽和脂肪酸から選択される一種または二種以上
(B):炭素数が8〜14の飽和脂肪酸及び炭素数が16〜22の不飽和脂肪酸から選択される一種または二種以上
であり、(A)および(B)の総モル量において、(A)のモル比率が0.3〜0.9、且つベヘン酸0.2〜0.8(B)のモル比率が0.1〜0.7であるとともに、
そのエステル化率が40%以上
A margarine or shortening containing 30% or more of an oil that is liquid at 20 ° C. and containing a polyglycerin fatty acid ester that satisfies the following conditions.
The molar ratio of each fatty acid in the constituent fatty acid and the constituent fatty acid of the polyglycerol fatty acid ester is
(A): One or more selected from saturated fatty acids having 16 to 22 carbon atoms that essentially require behenic acid (B): Saturated fatty acids having 8 to 14 carbon atoms and imperfections having 16 to 22 carbon atoms One or more selected from saturated fatty acids, and in the total molar amount of (A) and (B), the molar ratio of (A) is 0.3 to 0.9, and behenic acid 0.2 to 0 .8 , the molar ratio of (B) is 0.1 to 0.7 ,
The esterification rate is 40% or more .
請求項1に記載のマーガリンまたはショートニングを用いてなる食品。

A food comprising the margarine or shortening according to claim 1.

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