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JPS59130135A - Preparation of processed food of fat and oil - Google Patents

Preparation of processed food of fat and oil

Info

Publication number
JPS59130135A
JPS59130135A JP484083A JP484083A JPS59130135A JP S59130135 A JPS59130135 A JP S59130135A JP 484083 A JP484083 A JP 484083A JP 484083 A JP484083 A JP 484083A JP S59130135 A JPS59130135 A JP S59130135A
Authority
JP
Japan
Prior art keywords
butter
margarine
oil
processed food
fat
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
JP484083A
Other languages
Japanese (ja)
Other versions
JPH0341133B2 (en
Inventor
Kuniaki Koshiba
小柴 邦明
Takehiko Ofuji
武彦 大藤
Shoichi Kato
正一 加藤
Takeshi Kawashima
武志 河島
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.)
Kanegafuchi Chemical Industry Co Ltd
Original Assignee
Kanegafuchi Chemical Industry 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 Kanegafuchi Chemical Industry Co Ltd filed Critical Kanegafuchi Chemical Industry Co Ltd
Priority to JP484083A priority Critical patent/JPS59130135A/en
Publication of JPS59130135A publication Critical patent/JPS59130135A/en
Publication of JPH0341133B2 publication Critical patent/JPH0341133B2/ja
Granted legal-status Critical Current

Links

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  • Dairy Products (AREA)
  • Edible Oils And Fats (AREA)

Abstract

PURPOSE:To prepare a processed food of fats and oils for maintaining and manifesting taste of butter effectively, by belending continuously butter conditioned in a specific temperature range with margarine by a static type blender. CONSTITUTION:Butter conditioned at 10-23 deg.C is continuously blended with margarine by a static type blender, to prepare a processed food of fats and oils for maintaining and manifesting taste of butter effectively. In the operation, the margarine and butter in a given ratio of about 3/7-9/1 range are passed through the static type blender and blended uniformly. The static type blender has preferably 12-24 stirring elements.

Description

【発明の詳細な説明】 本発明は油脂加工食品の新規な製造法に関し、更に詳し
くはバター風味を効果的に維持・発現せしめる油脂加工
食品の製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a novel method for producing processed oil and fat foods, and more particularly to a method for producing processed oil and fat foods that effectively maintains and develops butter flavor.

食生活の多様化、高級化に伴ない、より風味に優れ、口
あfc9の良い食品が求められている。
With the diversification and increasing luxury of dietary habits, there is a demand for foods with superior flavor and a good mouth feel fc9.

かかる消費者の嗜好を反映して、製菓、製パン業界にお
いても味のあっさりした植物性マーガリンを製菓、製パ
ン材料として多用する一方、フレッシュバターの含有率
の高いコクのある所用コンパウンドマーガリンが重用さ
れている。
Reflecting these consumer preferences, in the confectionery and bread making industries, light-tasting vegetable margarine is frequently used as an ingredient for confectionery and bread making, while rich compound margarine with a high fresh butter content is increasingly used. has been done.

かかるコンパウンドマーガリンは、一般に、油脂と水相
とのW10型エマルジョン中にバターを添加し、加熱溶
解してバター(乳脂肪)を含むVO型エマルジョンとし
た後、高温殺菌を施し、しかる後に急冷可塑化して製造
される。
Such compound margarine is generally produced by adding butter to a W10 type emulsion of oil and fat and an aqueous phase, heating and melting it to form a VO type emulsion containing butter (milk fat), and then subjecting it to high temperature sterilization, followed by rapid cooling and plasticization. It is manufactured by converting it into

一方、洋菓子業界においてはバターとショートニングと
を混合してホイップさせ、所謂バタークリームと云われ
るものをケーキの間に挾んだり、あるいはトッピングと
して使用されている。
On the other hand, in the Western confectionery industry, butter and shortening are mixed together and whipped, and a so-called butter cream is sandwiched between cakes or used as a topping.

本発明者らは、上記バタークリームと同成分のものをコ
ンパウンドマーガリンを用いて作り、バター風味を比較
したところ、従来法で得られたコンパウンドマーガリン
を用いたものは明らかに劣るという結果を得た。そこで
本発明者らは更に研究を重ね、下記の如き知見を得た;
(1)  コンパウンドマーガリンを用すたバタークリ
ームがバターとショートニングとからなるバタークリー
ムに比し、バター風味において劣る理由については定か
でないが、従来法で製造されたコンパウンドマーガリン
は、バターに存在しているといわれる脂肪球が加熱殺菌
及び急冷可塑化工程で破壊され、バター特有の風味が損
なわれるものと推定される。
The present inventors made a butter cream with the same ingredients as the above butter cream using compound margarine and compared the butter flavor, and found that the butter cream made using compound margarine obtained by the conventional method was clearly inferior. . Therefore, the present inventors conducted further research and obtained the following findings;
(1) It is unclear why butter cream made using compound margarine is inferior in butter flavor to butter cream made from butter and shortening, but compound margarine produced using conventional methods does not It is presumed that the fat globules that are said to be present in butter are destroyed during the heat sterilization and rapid cooling plasticization processes, and the unique flavor of butter is impaired.

(2)一方、新鮮なバターの生菌数は、近時製造工程の
衛生管理がゆきとどいているf乙め、30〜50 mv
’9と意外に少すく、またその殆どがケース又はパウチ
と接する表面であって、内部の汚染は殆ど見られない。
(2) On the other hand, the number of viable bacteria in fresh butter is 30 to 50 mv due to good hygiene control in the manufacturing process these days.
'9, which is surprisingly small, and most of the contamination is on the surface that comes in contact with the case or pouch, so there is hardly any contamination inside.

かかる汚染程度ノ低イハターは加熱殺菌しなくても約O
〜5°Cで約2〜3カ月間は腐敗することなく維持でき
る。
Such a low degree of contamination is approximately O even without heat sterilization.
It can be maintained at ~5°C for about 2 to 3 months without spoiling.

本発明ばかがる知見に基づいて、バター風味を効果的に
維持発現させ得る油脂加工食品の製造法を提供するもの
である。
Based on the findings of the present invention, it is an object of the present invention to provide a method for producing processed oil and fat foods that can effectively maintain and develop butter flavor.

即ち、本発明は10〜23°Cに温調し几バターを静止
型混合機で連続的にマーガリンと混合することを特徴と
する油脂加工食品の製造法を内容とする。
That is, the present invention is directed to a method for producing an oil-and-fat processed food, which is characterized in that the temperature is controlled at 10 to 23° C., and melted butter is continuously mixed with margarine in a static mixer.

ここで云う静止型混合機としては、例えば東し製「ハイ
ミキサー」、ケエックス社製「スタティックミキサ」、
ノリタケカンパニーリミテド製「スタティックミキサー
」等が挙げられる。
The static mixers mentioned here include, for example, the "High Mixer" manufactured by Toshi, the "Static Mixer" manufactured by K-EX,
Examples include "Static Mixer" manufactured by Noritake Company Limited.

本発明に用いられるマーガリンは通常の方法で製造され
る。即ち、油相部(油脂、香料、乳化剤等ンを乳化タン
クに入れ、約60〜70’Cで加熱溶解する。油脂とし
ては一般的にマーガリンに使用される植物油、動物油、
それらの硬化油、精製油、ラムニス油、分別油等が全て
使用できる。香料としてはバターフレーバー、バニラ系
香料等を嗜好により微量添加するが、添加しなくとも差
し支えない。水溶性の香料は水相部に添加するのが良い
。乳化剤としてはモノグリ、レシチン等食品添加物とし
て許可されているものを単独又は適宜組み合せ、約0.
02〜5.0重量%の範囲で添加される。この他、ビタ
ミンその他の添加物を添加しても良い。
The margarine used in the present invention is produced by a conventional method. That is, the oil phase (fats, oils, fragrances, emulsifiers, etc.) is placed in an emulsification tank and heated and dissolved at about 60 to 70'C.The oils include vegetable oil, animal oil, which is generally used in margarine,
All of these hydrogenated oils, refined oils, rhum varnish oils, fractionated oils, etc. can be used. As a flavoring agent, a small amount of butter flavor, vanilla flavoring, etc. may be added depending on preference, but there is no problem even if it is not added. Water-soluble fragrances are preferably added to the aqueous phase. As the emulsifier, monoglycium, lecithin, and other permitted food additives may be used alone or in appropriate combinations, and approximately 0.
It is added in a range of 0.02 to 5.0% by weight. In addition, vitamins and other additives may be added.

上記油相部中に攪拌し乍ら水相部を加え、油中水型エマ
ルジョンを作る。水相部としては牛乳の他、水に金粉、
脱粉、塩等を添加し几もの等が用いられる。
A water phase is added to the oil phase while stirring to form a water-in-oil emulsion. In addition to milk, the water phase contains gold powder and water.
A refined method is used after removing powder and adding salt, etc.

得られた油中水型のエマルジョンをプレート型殺菌機等
の高温殺菌機で殺菌し、コンビネータ−、ボテーター、
パーツエフター等の捏和様により急冷可塑化する。
The obtained water-in-oil emulsion is sterilized using a high-temperature sterilizer such as a plate-type sterilizer, and then sterilized using a combinator, votator,
It is rapidly cooled and plasticized using a kneading method such as Parts Efter.

一方、約10〜23°C1好ましくは約17°C±3°
Cの温調庫で温調したバターを濃度30%〜70%のア
ルコールシャワートンネルを5〜10分間通して低温殺
菌する。バターの品温か高いと軟らかくなり、ケースか
ら出しベル1−コンベアに乗せる作業が困難となる。ペ
ネトレーション値で250程度が限界であり、好ましく
は150以下である。尚、生菌数が非常に少なめバター
を使用する場合は、この低温殺菌は省略しても差し支え
ない。
On the other hand, about 10-23°C1 preferably about 17°C±3°
The temperature-controlled butter in the temperature-controlled chamber C is pasteurized by passing it through an alcohol shower tunnel with a concentration of 30% to 70% for 5 to 10 minutes. If the temperature of the butter is high, it will become soft and it will be difficult to take it out of the case and put it on the bell 1 conveyor. The maximum penetration value is about 250, preferably 150 or less. In addition, when using butter with a very small number of viable bacteria, this pasteurization may be omitted.

殺菌したバターをモーノポンプ、コメットポンプ等の定
量ポンプで送り、上記可塑化したマーガリンと混合する
。バターの温度は約10〜23℃、好ましくは約17°
C±3°Cであって、低過ぎると硬9〈なシ、ポンプに
よる定量輸送が困難となる。ポンプの前に2軸のスクリ
ュー型移送機を取り付けることによりペネトレーション
値70以上であれば輸送が可能であるが、好ましくは1
00以上である。
The sterilized butter is fed with a metering pump such as a Mono pump or a Comet pump, and mixed with the plasticized margarine. The temperature of the butter is about 10-23°C, preferably about 17°C.
C±3°C, and if it is too low, it will become hard and difficult to transport at a constant rate using a pump. By installing a two-shaft screw type transfer device in front of the pump, transportation is possible if the penetration value is 70 or more, but preferably 1.
00 or more.

かぐして定量ポンプで送られ几マーガリンとバターとを
概ね3/7〜9/1の範囲内で所定の割合でスタティッ
クミキサーを通過させ均一に混合する。尚、上記割合は
限定的なものではないが、バター量が70%以上及び1
0%以下では、本発明の効果はあま9なくなる。即ち、
バター量が70%を越えると、従来法と比べてバター風
味に差がなくなり、10%未満ではバター風味かうすく
なシ、官能的に識別し難くなる。スタティックミキサー
の攪拌エレメントの数は12〜24の範囲で好適である
。ニレメン1〜数が上記範囲よりも小さいと、バターと
マーガリンが肉眼で識別できる場合が生じ、商品価値の
面から問題があり、逆に大きすぎると配管抵抗が増加し
、ポンプモーターに負荷がかかり得策でない。
The margarine and butter, which are smelt and fed by a metering pump, are passed through a static mixer at a predetermined ratio within the range of approximately 3/7 to 9/1 to be uniformly mixed. The above ratio is not limited, but if the amount of butter is 70% or more and 1
If it is less than 0%, the effect of the present invention will be less than 9%. That is,
If the amount of butter exceeds 70%, there will be no difference in butter flavor compared to the conventional method, and if it is less than 10%, the butter flavor will be weak and difficult to discern sensually. The number of stirring elements of the static mixer is preferably in the range of 12 to 24. If the number is smaller than the above range, butter and margarine may be distinguishable with the naked eye, which poses a problem in terms of product value.On the other hand, if it is too large, piping resistance will increase and load will be placed on the pump motor. It's not a good idea.

以下、本発明を実施例を挙げて説明するが、本発明はこ
れに限定されないことば勿論である。
The present invention will be described below with reference to Examples, but it goes without saying that the present invention is not limited thereto.

尚、以下においてパーセン)U重量パーセントである。In the following, percentages are expressed as U weight percentages.

実施例1 硬化魚油(M 、P 37°C)5%、硬化魚油(MP
30°C)30%、コーン油20%からなる油脂82.
55%を60°Cで加熱溶解し、これに乳化剤としてレ
シチン0.4%、香料としてバターフレーバー0.05
%を加えて油相部とし几。この油相部を攪拌しながら保
存料0.05%を含む水相部(牛乳)17%を加え油中
水型エマルジョンを得、プレーl−型殺菌機により殺菌
した。次いでボテーターを通し、急冷可塑化してマーガ
リンを得た。
Example 1 Hydrogenated fish oil (M, P 37°C) 5%, hydrogenated fish oil (MP
30°C) and 20% corn oil82.
55% was dissolved by heating at 60°C, and this was mixed with 0.4% lecithin as an emulsifier and 0.05% butter flavor as a flavoring agent.
% to make the oil phase. While stirring the oil phase, a 17% aqueous phase (milk) containing 0.05% preservative was added to obtain a water-in-oil emulsion, which was sterilized using a spray L-type sterilizer. Then, it was passed through a votator and rapidly cooled and plasticized to obtain margarine.

一方、17°C十3°Cの温調庫で2日間温調したバタ
ーをダンボール箱から取り出し、70%濃度のアルコー
ルシャワートンネルを5 分1tilして低温殺菌した
On the other hand, butter that had been temperature-controlled for 2 days at 17°C and 13°C was taken out of the cardboard box and pasteurized in a 70% alcohol shower tunnel for 5 minutes.

かぐして得られたバターをモーノポンプで送り、上記マ
ーガリンと混合した。混合割合はマーガリン70%、バ
ター30%とした。得られた混合物をスタティックミキ
サー(エレメント数12)を通過させて更に均一に混合
し、コンパウンドマーガリンを得た。
The butter obtained by smelting was sent using a Mono pump and mixed with the margarine. The mixing ratio was 70% margarine and 30% butter. The resulting mixture was passed through a static mixer (number of elements: 12) and mixed evenly to obtain compound margarine.

得うれたコンパウンドマーガリンはバター風味に冨み、
約5°Cの冷蔵庫に1力月貯蔵した後も腐敗は認められ
なかった。
The resulting compound margarine is rich in butter flavor,
No spoilage was observed even after one month of storage in a refrigerator at approximately 5°C.

比較例1 実施例1と同じ配合組成で油相部と水相部とを混合して
W10型エマルジョンを作り、これにバターを添加して
加熱溶解してバク−を含むW10型エマルジョンを得た
。次いで、これに高温殺菌(85°C)を施した後、ボ
テーターを通して急冷可塑化してコンパウンドマーガリ
ンを得た。
Comparative Example 1 A W10 emulsion was prepared by mixing an oil phase and an aqueous phase with the same composition as in Example 1, and butter was added thereto and melted by heating to obtain a W10 emulsion containing butter. . Next, this was subjected to high temperature sterilization (85°C), and then rapidly cooled and plasticized through a votator to obtain compound margarine.

得られたコンパウンドマーガリンは、実施例1で得られ
たものに比べ、著しくバター風味に劣るものであった。
The obtained compound margarine had a significantly inferior butter flavor compared to that obtained in Example 1.

比較例2 実施例1において、スタティックミキサーのエレメント
を6に設定し、同様の操作を実施した。
Comparative Example 2 In Example 1, the element of the static mixer was set to 6, and the same operation was performed.

得られたコンパウンドマーガリンはバター風味に富むも
のであったが、混合が不均一でバターとマーガリンとが
肉眼で識別され、商品的には不満足であった。
The obtained compound margarine had a rich buttery flavor, but the mixture was uneven and butter and margarine could be visually distinguished, making it unsatisfactory commercially.

比較例3 実施例1のスタティックミキサーの代わ9に、Bユニツ
I−を用いて、同様の操作を行なった。
Comparative Example 3 The same operation was carried out using B Units I- instead of the static mixer 9 in Example 1.

得うれたコンパウンドマーガリンは、実施例1で得られ
たものに比べ、バター風味において不充分なものであっ
之・ 実施例1及び比較例1〜3で作成したコンパウンドマー
ガリンを10名の専門的パネラ−によりバター風味の強
さについてテストを行なった。結果を第1表に示した。
The obtained compound margarine had insufficient butter flavor compared to that obtained in Example 1. - The strength of the butter flavor was tested. The results are shown in Table 1.

第  1  表 比較の対象      パネラ−の回答実施例1と比較
例1 10名全員が実施例1がバター風味が強いと答え
た。
Table 1 Target of Comparison Panelists' Answers Example 1 and Comparative Example 1 All 10 people answered that Example 1 had a strong butter flavor.

実施例1と比較例2 6名が有意差無し、残り4名は比
較例2がバター風味が強いと答え た。
Six people answered that there was no significant difference between Example 1 and Comparative Example 2, and the remaining four people answered that Comparative Example 2 had a stronger butter flavor.

実施例1と比較例3 10名全員が実施例1がバター風
味が強いと答えた。
Example 1 and Comparative Example 3 All 10 people answered that Example 1 had a strong butter flavor.

比較例1と比較例3 8名が比較例3がバター風味が強
いと答えた。残92名は有意差無 しと答えた。
Comparative Example 1 and Comparative Example 3 Eight people answered that Comparative Example 3 had a strong buttery flavor. The remaining 92 people answered that there was no significant difference.

次に、外観上の均一性と合わせて商品価値を判定した。Next, the commercial value was determined in conjunction with the uniformity of appearance.

その結果を第2表に示した。The results are shown in Table 2.

第  2  表Table 2

Claims (1)

【特許請求の範囲】 i、io’c〜23°Clこ温調したバターを静止型混
合機により連続的にマーガリンと混合することを特徴と
する油脂加工食品の製造法。 2、14°C〜20°Cに温調したバターである特許請
求の範囲第1項記載の製造法。 3、アルコールシャワーにより低温殺菌されたバターで
ある特許請求の範囲第1項又は第2項記載の製造法。 4、静止型混合機の攪拌エレメント数が12〜24の範
囲である特許請求の範囲第1項記載の製造法。
[Claims] A method for producing an oil-and-fat processed food, which comprises continuously mixing butter whose temperature has been adjusted to io'c to 23°Cl with margarine using a static mixer. 2. The manufacturing method according to claim 1, wherein the butter is temperature-controlled at 14°C to 20°C. 3. The manufacturing method according to claim 1 or 2, wherein the butter is pasteurized by an alcohol shower. 4. The manufacturing method according to claim 1, wherein the number of stirring elements of the static mixer is in the range of 12 to 24.
JP484083A 1983-01-13 1983-01-13 Preparation of processed food of fat and oil Granted JPS59130135A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP484083A JPS59130135A (en) 1983-01-13 1983-01-13 Preparation of processed food of fat and oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP484083A JPS59130135A (en) 1983-01-13 1983-01-13 Preparation of processed food of fat and oil

Publications (2)

Publication Number Publication Date
JPS59130135A true JPS59130135A (en) 1984-07-26
JPH0341133B2 JPH0341133B2 (en) 1991-06-21

Family

ID=11594880

Family Applications (1)

Application Number Title Priority Date Filing Date
JP484083A Granted JPS59130135A (en) 1983-01-13 1983-01-13 Preparation of processed food of fat and oil

Country Status (1)

Country Link
JP (1) JPS59130135A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01132336A (en) * 1987-11-17 1989-05-24 Snow Brand Milk Prod Co Ltd Production of milk fat-containing plastic oil and fat composition
US4840810A (en) * 1985-03-27 1989-06-20 Lever Brothers Company Process for the preparation of an edible fat-containing product
US4844928A (en) * 1985-03-27 1989-07-04 Lever Brothers Company Process for the preparation of an edible fat-containing product
JP2017051151A (en) * 2015-09-11 2017-03-16 株式会社Adeka Manufacturing method of plastic oil-and-fat composition for roll in
EP2555630B2 (en) 2010-04-08 2017-09-27 Arla Foods Amba Butter-derived spread and a method of producing it

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4840810A (en) * 1985-03-27 1989-06-20 Lever Brothers Company Process for the preparation of an edible fat-containing product
US4844928A (en) * 1985-03-27 1989-07-04 Lever Brothers Company Process for the preparation of an edible fat-containing product
JPH01132336A (en) * 1987-11-17 1989-05-24 Snow Brand Milk Prod Co Ltd Production of milk fat-containing plastic oil and fat composition
EP2555630B2 (en) 2010-04-08 2017-09-27 Arla Foods Amba Butter-derived spread and a method of producing it
JP2017051151A (en) * 2015-09-11 2017-03-16 株式会社Adeka Manufacturing method of plastic oil-and-fat composition for roll in

Also Published As

Publication number Publication date
JPH0341133B2 (en) 1991-06-21

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