JPS6362535A - Production of emulsifying agent - Google Patents

Production of emulsifying agent

Info

Publication number
JPS6362535A
JPS6362535A JP61207480A JP20748086A JPS6362535A JP S6362535 A JPS6362535 A JP S6362535A JP 61207480 A JP61207480 A JP 61207480A JP 20748086 A JP20748086 A JP 20748086A JP S6362535 A JPS6362535 A JP S6362535A
Authority
JP
Japan
Prior art keywords
weight
parts
starch
emulsifier
lecithin
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP61207480A
Other languages
Japanese (ja)
Other versions
JPH0570494B2 (en
Inventor
Takao Hanno
半野 敬夫
Kazuhiro Okuma
一裕 大隈
Yasuhiro Hoshii
干井 康弘
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Matsutani Chemical Industries Co Ltd
Original Assignee
Matsutani Chemical Industries Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsutani Chemical Industries Co Ltd filed Critical Matsutani Chemical Industries Co Ltd
Priority to JP61207480A priority Critical patent/JPS6362535A/en
Publication of JPS6362535A publication Critical patent/JPS6362535A/en
Publication of JPH0570494B2 publication Critical patent/JPH0570494B2/ja
Granted legal-status Critical Current

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  • Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
  • Dairy Products (AREA)
  • Grain Derivatives (AREA)
  • Edible Oils And Fats (AREA)
  • General Preparation And Processing Of Foods (AREA)
  • Jellies, Jams, And Syrups (AREA)
  • Seasonings (AREA)

Abstract

PURPOSE:To enhance the stability of emulsion by emulsifying lecithin and polyglycerin-aliphatic acid ester in a starch decomposition soln. and also dissolving artificial starch and xanthane-gum to prepare an emulsifying agent. CONSTITUTION:An emulsifying agent is finally produced by emulsifying lecithin and polyglycerin-fatty acid ester in a starch decomposition soln. and dissolving artificial starch and xanthane-gum. In this case, as a representative example, the composition contg. 0.3-1wt% lecithin, 1-3wt% polyglycerin-oleic acid ester, 3-10wt% hydroxypropyl-starch and 0.1-0.4wt% xanthane-gum is shown. The obtained emulsifying agent has nearly the same emulsifying stability as gum arabi even in a wide pH range.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は乳化剤の製造法に関し、更に詳しくはアラビア
・ガムに代替出来る優れた乳化安定性を有する乳化剤の
製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for producing an emulsifier, and more particularly to a method for producing an emulsifier having excellent emulsion stability and capable of replacing gum arabic.

〔従来の技術〕[Conventional technology]

従来アラビア・ガムを食品の乳化安定剤として使用する
と、広いp H領域において安定な乳化物を得ることが
でき、さらに食塩などの電解質の存在下でもO/W型乳
化ができその乳化物は脂肪球が小さく、且つ界面エネル
ギーを低下させるなど、他の乳化剤にはその類をみない
優れた乳化剤である。そしてこれらの特性を活かして、
香料製剤、洋菓子、粉末油脂、ドレッシング等の食品製
造並びに医薬品、工業品分野でも汎用乳化剤として重要
視されてきた。しかしながら、最近にいたって再三にわ
たりアラビア・ガムの生産・入荷量が減少して入手が甚
だ困難となり、さらに原木が枯死して数年間は復帰不能
とも言われるようになった。
Conventionally, when gum arabic is used as an emulsion stabilizer for foods, stable emulsions can be obtained in a wide pH range, and O/W type emulsification can be performed even in the presence of electrolytes such as salt, and the emulsions can contain fats. It is an excellent emulsifier unlike any other emulsifier, with small spheres and low interfacial energy. And by taking advantage of these characteristics,
It has been considered important as a general-purpose emulsifier in food production such as flavor preparations, Western confectionery, powdered oils and fats, and dressings, as well as in the fields of pharmaceuticals and industrial products. However, in recent years, the production and arrival of gum arabic have repeatedly decreased, making it extremely difficult to obtain gum arabic, and the logs have died, and it has come to be said that it will not be possible to return to production for several years.

本発明者はこの要望に応えるために代替品を開発し先に
出願したが、この乳化安定剤は乳化時のオイル径が大き
いこと、溶解時の粘性が高いためホモミキサー処理が困
難であること、乳化物の安定性がやや低いこと、乳化物
を冷蔵保存中にゲル化し易いことなどが課題となってき
た。
In order to meet this demand, the present inventor developed an alternative product and filed an application earlier, but this emulsion stabilizer has a large oil diameter when emulsified and high viscosity when dissolved, making it difficult to process with a homomixer. However, problems have arisen in that the stability of emulsions is somewhat low and that emulsions tend to gel during refrigerated storage.

〔本発明の目的並びに概要〕[Object and outline of the present invention]

本発明者は上記の要望に応えるために、さらに優れた乳
化剤の開発について研究を継続し、澱粉分解物溶液にレ
シチンとポリグリセリン脂肪酸エステルを溶解・乳化し
且つ、化工澱粉及びキサンタン・ガムを溶解することに
よって、所期の目的を達成出来ることを見出し、芸に本
発明を完成するに至った。
In order to meet the above-mentioned needs, the present inventor continued research on the development of an even better emulsifier, and dissolved and emulsified lecithin and polyglycerin fatty acid ester in a starch decomposition product solution, as well as dissolved modified starch and xanthan gum. They discovered that the intended purpose could be achieved by doing so, and successfully completed the present invention.

〔発明の構成〕[Structure of the invention]

本発明の乳化剤の製造法は、基本的には、澱粉分解物の
溶液にレシチンとポリグリセリン脂肪酸エステルを溶解
・乳化させ且つ化工澱粉とキサンタン・ガムを溶解する
方法である。この際澱粉分解物水溶液にこれ等各成分を
乳化溶解させる順序は何等限定されず、上記各所定の成
分が最終的に澱粉分解物水/8液に乳化、溶解していれ
ば良い。
The method for producing the emulsifier of the present invention is basically a method of dissolving and emulsifying lecithin and polyglycerol fatty acid ester in a solution of starch decomposition product, and dissolving modified starch and xanthan gum. At this time, the order in which these components are emulsified and dissolved in the starch decomposition product aqueous solution is not limited in any way, as long as the above-mentioned respective predetermined components are finally emulsified and dissolved in the starch decomposition product water/8 liquid.

たとえばレシチンを乳化させ、その後ポリグリセリン脂
肪酸エステルを乳化させ、次いで他の成分を添加溶解さ
せても良いし、また澱粉分解物の溶液に他成分の全部ま
たは一部を添加し溶解・乳化させても良い。これ等各方
法の中では、澱粉分解物の水溶液にレシチンとポリグリ
セリン脂肪酸エステルを溶解・乳化させた後、他成分を
添加し溶解する方法が特に好ましい。また本発明の乳化
剤は粉末化適性が優れているので、噴霧乾燥等の手段と
組み合わせることによって、容易に乳化剤粉末を得るこ
とが出来る。さらに一部の成分を添加せずに粉末化して
おき、該成分は粉末化後に添加し粉体混合することによ
っても充分に所期の乳化効果を発揮することが出来る。
For example, you can emulsify lecithin, then emulsify polyglycerin fatty acid ester, and then add and dissolve other ingredients, or add all or part of other ingredients to a solution of starch decomposition product and dissolve and emulsify. Also good. Among these methods, particularly preferred is a method in which lecithin and polyglycerol fatty acid ester are dissolved and emulsified in an aqueous solution of starch decomposition product, and then other components are added and dissolved. Furthermore, since the emulsifier of the present invention has excellent powderability, emulsifier powder can be easily obtained by combining it with means such as spray drying. Further, the desired emulsifying effect can be sufficiently exerted by powdering some components without adding them, and adding the components after powdering and mixing the powders.

この際の噴霧乾燥手段としても特に限定されず各種の従
来から知られている手段がいずれも採用される。
The spray drying means at this time is not particularly limited, and any of various conventionally known means may be employed.

本発明に於いて使用する澱粉分解物とは、澱粉を常法に
より加水分解したものであり、その加水分解の条件は通
常α−アミラーゼ又は酸を用いるもので、加水分解の程
度は、DB3〜25、好ましくは4〜15の範囲である
。また澱粉としても従来から知られている各種のものが
使用出来、たとえば、コーンスターチ、タピオカ澱粉、
甘苦澱粉、ジャガイモ澱粉、ワキシーコーンスターチ等
を具体例として例示出来る。
The starch decomposition product used in the present invention is obtained by hydrolyzing starch by a conventional method, and the hydrolysis conditions are usually those using α-amylase or acid, and the degree of hydrolysis is DB3 to 25, preferably in the range of 4-15. In addition, various kinds of starches that are conventionally known can be used, such as corn starch, tapioca starch,
Specific examples include bittersweet starch, potato starch, and waxy corn starch.

この澱粉分解物の水溶液の濃度は、目的物や乳化剤の用
途等により一定しないが、通常15〜60重量%、好ま
しくは30〜55重景%程度とすれば良い。
The concentration of the aqueous solution of the starch decomposition product varies depending on the object, the use of the emulsifier, etc., but it is usually about 15 to 60% by weight, preferably about 30 to 55% by weight.

またレシチンとしては、通常使用されているものが広い
範囲で使用出来、大豆レシチン、卵黄レシチン等を具体
例として挙げることが出来、その使用量は澱粉分解物1
00重量部に対し0.1〜5重量部、好ましくは0.5
〜3重量部程度である。またポリグリセリン脂肪酸エス
テルの使用量は澱粉分解物100重壁部に対し0.2〜
10重量部、好ましくは1〜5重量部である。この際レ
シチンの添加量が上記範囲よりも少ないと乳化液の油滴
径が大きくなるために、分離し易くなる傾向があって好
ましくな(、また逆に上記範囲よりも多くなり過ぎると
食品用として風味が劣化する傾向があり好ましくない。
In addition, as lecithin, commonly used lecithin can be used in a wide range, and specific examples include soybean lecithin and egg yolk lecithin.
0.1 to 5 parts by weight, preferably 0.5 parts by weight
~3 parts by weight. In addition, the amount of polyglycerol fatty acid ester used is 0.2 to 0.2 to 100 heavy wall parts of the starch decomposition product.
The amount is 10 parts by weight, preferably 1 to 5 parts by weight. At this time, if the amount of lecithin added is less than the above range, the diameter of the oil droplets in the emulsion becomes large, which tends to cause separation, which is undesirable. This is undesirable because the flavor tends to deteriorate as a result.

ポリグリセリン脂肪酸エステルとしては、通常の市販品
即ち、ポリグリセリンの水酸基の内いくつかを、ステア
リン酸、オレイン酸、ラウリン酸等の脂肪酸で直接エス
テル化したものも、油脂とのエステル交換法によって製
造したものも、いずれも有効に使用することが可能であ
り、その使用量は澱粉分解物100重量部に対し0.2
〜IO重量部、好ましくは0.8〜5重量部である。こ
の際のポリグリセリン脂肪酸エステルの添加量が上記範
囲よりも少なくなると乳化液の油滴径が大きくなり、ま
た上記範囲よりも多くなり過ぎても効果は増加しない。
Polyglycerin fatty acid esters are commercially available products, such as those in which some of the hydroxyl groups of polyglycerin are directly esterified with fatty acids such as stearic acid, oleic acid, and lauric acid, and also products produced by transesterification with oils and fats. Both of these can be used effectively, and the amount used is 0.2 parts by weight per 100 parts by weight of starch decomposition product.
~IO parts by weight, preferably 0.8 to 5 parts by weight. If the amount of polyglycerol fatty acid ester added is less than the above range, the oil droplet diameter of the emulsion will become large, and if it is too much than the above range, the effect will not increase.

化工澱粉としては各種のものが使用出来、その代表例と
してヒドロキシアルキル・ジスクーチ。
Various types of modified starches can be used, and hydroxyalkyl discouche is a typical example.

フォスフェート好ましくはヒドロキシプロピル・ジスク
ーチ・フォスフェート、ヒドロキシアルキル・スターチ
好ましくはヒドロキシプロピル・スターチ、ジスクーチ
・フォスフェート等を例示出来、これ等は1種または2
種以上の混合系で使用される。この中ではヒドロキシプ
ロピル・ジスクーチ・フォスフェートが最も好ましい。
Examples of the phosphate include hydroxypropyl discouchi phosphate, hydroxyalkyl starch, preferably hydroxypropyl starch, discouchy phosphate, etc.
Used in a mixed system of more than one species. Among these, hydroxypropyl discouti phosphate is most preferred.

使用量は澱粉分解物100重量部に対し3〜25重量部
、好ましくは5〜15重量部程度である。使用量が上記
範囲よりも少ないと、充分な乳化安定効果を得ることが
出来ず、また上記範囲よりも多いと乳化剤の粘性が高過
ぎる傾向があって好ましくない。
The amount used is about 3 to 25 parts by weight, preferably about 5 to 15 parts by weight, per 100 parts by weight of the starch decomposition product. If the amount used is less than the above range, a sufficient emulsion stabilizing effect cannot be obtained, and if it is more than the above range, the viscosity of the emulsifier tends to be too high, which is not preferable.

キサンタン・ガムとしても公知の各種のものが使用され
、また各種の市販品がいずれも有効に使用される。その
配合割合は澱粉分解物100重量部に対し0.1〜5重
量部、好ましくは0.1〜0.5重量部である。この際
上記範囲よりも少ないと乳化液が分離し易くなり、また
逆に多くなると乳化液の粘性が高くなって望ましくない
Various types of xanthan gums also known as xanthan gums are used, and various commercially available products can be used effectively. The mixing ratio thereof is 0.1 to 5 parts by weight, preferably 0.1 to 0.5 parts by weight, per 100 parts by weight of the starch decomposition product. In this case, if the amount is less than the above range, the emulsion will tend to separate, and if it is too much, the viscosity of the emulsion will increase, which is undesirable.

本発明乳化剤を製造するに際しては、澱粉分解物水溶液
に最終的に、レシチンとポリグリセリン脂肪酸エステル
を乳化させ、また化工澱粉とキサンクン・ガムとを溶解
させれば良くこれ等各成分の乳化、溶解の順序は特に重
要ではないが、澱粉分解物の水i8 ?(lにレシチン
ポリグリセリン脂肪酸エステルを乳化させ、ついで残り
の成分を溶解させる方法が好ましい、また溶解時の液温
は60°C以上が溶解速度が速いことと、ポリグリセリ
ン脂肪酸エステルの溶解乳化が容易であり、加えて冷水
不溶性の化工澱粉の溶解にも都合が良いので、最も好ま
しい。
When producing the emulsifier of the present invention, it is sufficient to finally emulsify lecithin and polyglycerin fatty acid ester in an aqueous solution of starch decomposition product, and also to dissolve modified starch and xanthin gum. The order of water i8 of starch decomposition products is not particularly important, but the order of water i8? (It is preferable to emulsify lecithin polyglycerol fatty acid ester in l and then dissolve the remaining components. Also, the solution temperature at the time of dissolution is 60°C or higher because the dissolution rate is fast, and the dissolution and emulsification of polyglycerol fatty acid ester is This is the most preferred method because it is easy to use and is also convenient for dissolving modified starches that are insoluble in cold water.

本発明乳化剤の有効成分の濃度や各成分の種類は、乳化
剤の使用目的、使用条件により適宜に決定されれば良く
、たとえばその代表的な一例を示すと、50%4度の澱
粉分解物中にレシチンが0.3〜1重量%、ポリグリセ
リン・オレイン酸エステルが1〜3重量%、ヒドロキシ
プロピル・スターチが3〜10重量%、キサンタン・ガ
ムが0.1〜0.4重量%含有された組成を挙げること
が出来る。
The concentration of the active ingredient and the type of each ingredient in the emulsifier of the present invention may be appropriately determined depending on the purpose of use and conditions of use of the emulsifier. Contains 0.3-1% by weight of lecithin, 1-3% by weight of polyglycerin oleate, 3-10% by weight of hydroxypropyl starch, and 0.1-0.4% by weight of xanthan gum. The following compositions can be mentioned.

本発明に於いては、上記組成の液状の乳化剤をそのまま
使用しても良く、またこれを乾燥して粉末として使用し
ても良い、たとえ冷水不溶性の化工澱粉を使用したもの
でも、−旦加温溶解したものは粉末化後でも冷水可溶性
となる。この澱粉分解物の溶液にレシチンとポリグリセ
リン脂肪酸エステルを乳化させ、これに化工澱粉とキサ
ンクン・ガムを粉体混合してもよいが、この場合は化工
澱粉は冷水可溶のアルファー型を用いると、冷水可溶の
乳化剤となるので最も好ましい。
In the present invention, the liquid emulsifier having the above composition may be used as it is, or it may be dried and used as a powder. Those dissolved in warm water remain soluble in cold water even after being powdered. Lecithin and polyglycerin fatty acid ester may be emulsified in this starch decomposition product solution, and modified starch and xanthin gum may be mixed in powder form. , is the most preferable because it becomes a cold water soluble emulsifier.

本発明乳化剤を使用するに際しては、乳化すべき物質た
とえば油等の含有量により、適宜にそき量並びに濃度を
変化して使用すれば良い。
When using the emulsifier of the present invention, the amount and concentration may be changed as appropriate depending on the content of the substance to be emulsified, such as oil.

また本発明乳化剤には、必要に応じ従来からアラビア・
ガムと併用されて来た各種の添加剤を配合することが出
来る。この際の添加剤としては、たとえばデキストリン
、カゼイン等を例示することが出来またアラビア・ガム
を併用することが出来る。
In addition, the emulsifier of the present invention may include conventional Arabic
Various additives that have been used together with gum can be blended. Examples of additives in this case include dextrin and casein, and gum arabic can also be used in combination.

〔発明の効果〕〔Effect of the invention〕

本発明法により得られる乳化剤は、アラビア・ガムと同
等またはそれ以上の各種の乳化特性を有し、乳化力、乳
化安定性、電解質共存下での0/W乳化性等については
アラビア・ガムとほぼ同し様な優れた効果を示し、また
広いpHR1域に於いてもアラビア・ガムとほぼ同じ様
な乳化安定性がある。また乳化すべき油分としても植物
性、フレーバーオイル、鉱物油等広い範囲で乳化出来、
その乳化物の粒径も非常に小さいと言う特性がある。
The emulsifier obtained by the method of the present invention has various emulsifying properties equivalent to or better than gum arabic, and has the same emulsifying power, emulsion stability, O/W emulsifying property in the coexistence of electrolytes, etc. as gum arabic. It shows almost the same excellent effects and also has almost the same emulsion stability as gum arabic even in a wide pH range of 1. In addition, a wide range of oils can be emulsified, including vegetable oils, flavor oils, and mineral oils.
The particle size of the emulsion is also very small.

従って従来アラビア・ガムが使用されて来た分野すべて
に本発明乳化剤は使用することが出来、たとえば香料製
剤、乳化香料、粉末香料、粉末油脂、調味料、菓子、ベ
ーカリ−1乳製品、医療製剤等に有効に使用される。
Therefore, the emulsifier of the present invention can be used in all fields in which gum arabic has traditionally been used, such as flavor preparations, emulsified flavors, powdered flavors, powdered oils and fats, seasonings, confectionery, bakery products, dairy products, and medical preparations. It is effectively used for such purposes.

〔実施例〕〔Example〕

以下に実施例を示して本発明法を具体的に説明する。 The method of the present invention will be specifically explained below with reference to Examples.

実施例1 DElo、5の澱粉分解物(松谷化学工業株式会社製「
パインデノクス#2」)の30%水溶液1000重量部
に、レシチン3重量部、テトラグリセリン・ペンタオレ
エート(坂本薬品株式会社rPo−310J ’)5重
量部を添加して乳化し、これにヒドロキシプロピル・ジ
スターチ・フォスフェート (スエーデン国・スタデッ
クス社製「ファリネックスVA−70J)25重量部、
キサンクン・ガム0.5重量部を溶解して乳化剤溶液を
製造した。このものの乳化安定特性を下記の方法で測定
した結果を下記に示す。
Example 1 Starch decomposition product of DElo, 5 (manufactured by Matsutani Chemical Co., Ltd.
3 parts by weight of lecithin and 5 parts by weight of tetraglycerin pentaoleate (Sakamoto Pharmaceutical Co., Ltd. rPo-310J') were added to 1000 parts by weight of a 30% aqueous solution of Pinedenox #2''), and emulsified. Distarch phosphate (“Farinex VA-70J” manufactured by Stadex, Sweden) 25 parts by weight,
An emulsifier solution was prepared by dissolving 0.5 parts by weight of xanthin gum. The emulsion stability properties of this product were measured by the following method, and the results are shown below.

アラビア・ガム及び、上記実施例1の30%濃度の希釈
品を調製し、その50gをホモジナイザー用容器に取り
、オレンジオイルl Qccを加え、ホモミキサーで攪
拌し、次いでユニバーサル・ホモジナイザーを用いて1
2000〜13000rpmで90秒間乳化を行った。
Prepare gum arabic and a 30% diluted product of Example 1 above, place 50 g of it in a homogenizer container, add 1 Qcc of orange oil, stir with a homomixer, and then mix with a universal homogenizer.
Emulsification was performed for 90 seconds at 2000-13000 rpm.

これを試験管に移し、5℃で1週間静置、次いで37℃
で1週間静置したが分離は起こらなかった。
Transfer this to a test tube and leave it at 5°C for 1 week, then at 37°C.
Although it was left standing for one week, no separation occurred.

さらに15%アルコールに分散しても凝集せず、10%
食塩水に分散しても乳化破壊が起こらなかった。また1
0%しょ糖液(クエン酸によりpH3,0に調製)に分
散しても乳化破壊が起こらなかった。
Further, even when dispersed in 15% alcohol, it does not aggregate, and 10%
Even when dispersed in saline, no demulsification occurred. Also 1
Even when dispersed in 0% sucrose solution (adjusted to pH 3.0 with citric acid), no demulsification occurred.

実施例2 実施例1の乳化剤溶液を二ロ社製のプロダクション・マ
イナー型の噴霧乾燥機を用いて、熱風温度170℃、排
風温度100℃で噴霧乾燥して、乳化剤粉末を得た。
Example 2 The emulsifier solution of Example 1 was spray-dried using a Production Minor type spray dryer manufactured by Niro Corporation at a hot air temperature of 170°C and an exhaust air temperature of 100°C to obtain an emulsifier powder.

粉末乳化剤の各種条件下に於ける乳化安定性を試験した
。結果を下記に示す。
The emulsion stability of the powder emulsifier under various conditions was tested. The results are shown below.

粉末乳化剤12重量部を70℃の温水28重量部に溶解
し、これにそれぞれ、下記の各物質を添加し実施例1と
同様に乳化して安定性を確認した。
12 parts by weight of the powder emulsifier were dissolved in 28 parts by weight of 70°C warm water, and each of the following substances was added thereto and emulsified in the same manner as in Example 1 to confirm stability.

いずれも安定性良好であった。All had good stability.

a、低pH領域 食酢         10重量部 サラダ油       50重量部 す、蛋白質共存 カゼイン・ナトリウム 10重量部 サラダ油       50重量部 C9塩類共存 食塩        1.5重量部 サラダ油       50重量部 実施例3 DE8.1の澱粉分解物(松谷化学工業株式会社「パイ
ンデソクス#1」)の45%水溶液1500fft1部
にレシチン9重量部とへキサグリセリン・トリステアレ
ート(坂本薬品株式会社製rTS−500J)12重量
部を添加して乳化し、これを実施例2と同様に噴霧乾燥
して得た粉末500重量部に対して、ヒドロキシプロピ
ル・ジスターチ・フォスフェート(スエーデン国スタデ
フクス社製「ファリネックスVA−70CJ)のアルフ
ァー化物を60重量部とキサンタン・ガム1.2重量部
を粉体混合して、乳化剤粉末を製造した。
a. Low pH range vinegar 10 parts by weight Salad oil 50 parts Sodium casein coexisting with protein 10 parts by weight Salad oil 50 parts C9 salt coexisting table salt 1.5 parts by weight Salad oil 50 parts Example 3 Starch decomposition product with DE8.1 9 parts by weight of lecithin and 12 parts by weight of hexaglycerin tristearate (rTS-500J, manufactured by Sakamoto Pharmaceutical Co., Ltd.) were added to 1 part of 1,500 fft of a 45% aqueous solution of (Matsutani Chemical Co., Ltd. "Pinedesox #1") and emulsified. , to 500 parts by weight of the powder obtained by spray drying this in the same manner as in Example 2, 60 parts by weight of a pregelatinized product of hydroxypropyl distarch phosphate ("Farinex VA-70CJ" manufactured by Stadevx, Sweden) was added. and 1.2 parts by weight of xanthan gum were mixed together to prepare an emulsifier powder.

この乳化剤粉末を用いて下記配合の各種の乳化物を試作
し同様にアラビア・ガムを用いたものと比較したが優れ
た安定性を示すことをbvtvシた。
Using this emulsifier powder, various emulsions having the following formulations were trial-produced and compared with those using gum arabic, and BVTV showed that they exhibited superior stability.

a、乳化香料 粉末乳化剤       15重量部 プロピレン・グリコール 10重量部 水           35重量部 オレンジ・オイル    1o重ff1413b、タラ
ウディー香料 乳化剤粉末       20重量部 5AIB         14重量部オレンジ・オイ
ル     6重量部 水           60重量部 C0粉末香辛料
a, Emulsified fragrance powder emulsifier 15 parts by weight Propylene glycol 10 parts by weight Water 35 parts by weight Orange oil 1 o weight ff1413b, Taraudi fragrance emulsifier powder 20 parts by weight 5 AIB 14 parts by weight Orange oil 6 parts by weight Water 60 parts by weight C0 powder spice

Claims (4)

【特許請求の範囲】[Claims] (1)澱粉分解物溶液にレシチンとポリグリセリン脂肪
酸エステルを乳化し、且つ化工澱粉とキサンタン・ガム
を溶解することを特徴とする乳化剤の製造法。
(1) A method for producing an emulsifier, which comprises emulsifying lecithin and polyglycerin fatty acid ester in a starch decomposition product solution, and dissolving modified starch and xanthan gum.
(2)澱粉加水分解物のDEが3〜25の範囲のものの
1種または2種以上を使用し、化工澱粉としてヒドロキ
シプロピル・ジスターチ・フォスフェート、ヒドロキシ
プロピル・スターチ及びジスターチ・フォスフェートの
少なくとも1種を使用する特許請求の範囲第1項の乳化
剤の製造法。
(2) One or more starch hydrolysates with a DE of 3 to 25 are used, and the modified starch is at least one of hydroxypropyl distarch phosphate, hydroxypropyl starch, and distarch phosphate. A method for producing an emulsifier according to claim 1, which uses seeds.
(3)澱粉加水分解物100重量部に対しレシチンが0
.1〜5重量部であり、且つポリグリセリン脂肪酸エス
テルが0.2〜10重量部であり、化工澱粉が3〜25
重量部であり、キサンタン・ガムが0.1〜5重量部で
ある特許請求の範囲第1項または第2項の乳化剤の製造
法。
(3) 0 lecithin per 100 parts by weight of starch hydrolyzate
.. 1 to 5 parts by weight, polyglycerin fatty acid ester is 0.2 to 10 parts by weight, and modified starch is 3 to 25 parts by weight.
The method for producing an emulsifier according to claim 1 or 2, wherein the amount of xanthan gum is 0.1 to 5 parts by weight.
(4)乳化剤の溶液を乾燥することを特徴とする特許請
求の範囲第1項、第2項、または第3項の乳化剤の製造
法。
(4) The method for producing an emulsifier according to claim 1, 2, or 3, which comprises drying the emulsifier solution.
JP61207480A 1986-09-03 1986-09-03 Production of emulsifying agent Granted JPS6362535A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61207480A JPS6362535A (en) 1986-09-03 1986-09-03 Production of emulsifying agent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61207480A JPS6362535A (en) 1986-09-03 1986-09-03 Production of emulsifying agent

Publications (2)

Publication Number Publication Date
JPS6362535A true JPS6362535A (en) 1988-03-18
JPH0570494B2 JPH0570494B2 (en) 1993-10-05

Family

ID=16540447

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61207480A Granted JPS6362535A (en) 1986-09-03 1986-09-03 Production of emulsifying agent

Country Status (1)

Country Link
JP (1) JPS6362535A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0436393A (en) * 1990-06-01 1992-02-06 Tsukishima Shokuhin Kogyo Kk Emulsified oil or fat composition
EP0577379A3 (en) * 1992-07-02 1994-06-08 Gen Foods Inc Method for processing fat-containing food sauce
WO2000013513A1 (en) * 1998-09-04 2000-03-16 Nexus A/S Masa-based products comprising polyglycerol fatty acid ester and/or modified starch
US6248338B1 (en) 1996-07-08 2001-06-19 National Starch And Chemical Investment Holding Corporation Starchy cleaning and cosmetic care preparations
JP2007267683A (en) * 2006-03-31 2007-10-18 Taiyo Kagaku Co Ltd Crowdy composition
US7785650B2 (en) 2001-05-15 2010-08-31 Mcneil-Ppc, Inc. Method for dip coating dosage forms
WO2012035978A1 (en) * 2010-09-14 2012-03-22 学校法人神奈川大学 Emulsifier and production method therefor, and production method for emulsion
US8309118B2 (en) 2001-09-28 2012-11-13 Mcneil-Ppc, Inc. Film forming compositions containing sucralose
JP2021136909A (en) * 2020-03-04 2021-09-16 日清食品ホールディングス株式会社 Method for producing emulsified powder

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0436393A (en) * 1990-06-01 1992-02-06 Tsukishima Shokuhin Kogyo Kk Emulsified oil or fat composition
EP0577379A3 (en) * 1992-07-02 1994-06-08 Gen Foods Inc Method for processing fat-containing food sauce
US6248338B1 (en) 1996-07-08 2001-06-19 National Starch And Chemical Investment Holding Corporation Starchy cleaning and cosmetic care preparations
WO2000013513A1 (en) * 1998-09-04 2000-03-16 Nexus A/S Masa-based products comprising polyglycerol fatty acid ester and/or modified starch
US7785650B2 (en) 2001-05-15 2010-08-31 Mcneil-Ppc, Inc. Method for dip coating dosage forms
US8309118B2 (en) 2001-09-28 2012-11-13 Mcneil-Ppc, Inc. Film forming compositions containing sucralose
JP2007267683A (en) * 2006-03-31 2007-10-18 Taiyo Kagaku Co Ltd Crowdy composition
JP4660413B2 (en) * 2006-03-31 2011-03-30 太陽化学株式会社 Cloudy composition
WO2012035978A1 (en) * 2010-09-14 2012-03-22 学校法人神奈川大学 Emulsifier and production method therefor, and production method for emulsion
JP2012061385A (en) * 2010-09-14 2012-03-29 Kanagawa Univ Emulsifier and production method therefor, and production method for emulsion
US9637559B2 (en) 2010-09-14 2017-05-02 Kanagawa University Emulsifier and production method therefor, and production method for emulsion
JP2021136909A (en) * 2020-03-04 2021-09-16 日清食品ホールディングス株式会社 Method for producing emulsified powder

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