JPH0798957B2 - Method for producing fats and oils for emulsified foods - Google Patents

Method for producing fats and oils for emulsified foods

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Publication number
JPH0798957B2
JPH0798957B2 JP63247017A JP24701788A JPH0798957B2 JP H0798957 B2 JPH0798957 B2 JP H0798957B2 JP 63247017 A JP63247017 A JP 63247017A JP 24701788 A JP24701788 A JP 24701788A JP H0798957 B2 JPH0798957 B2 JP H0798957B2
Authority
JP
Japan
Prior art keywords
oil
oils
palm
raw material
fats
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.)
Expired - Lifetime
Application number
JP63247017A
Other languages
Japanese (ja)
Other versions
JPH0292997A (en
Inventor
博 日高
信雄 鷲
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.)
Fuji Oil Co Ltd
Original Assignee
Fuji Oil Co Ltd
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Filing date
Publication date
Application filed by Fuji Oil Co Ltd filed Critical Fuji Oil Co Ltd
Priority to JP63247017A priority Critical patent/JPH0798957B2/en
Publication of JPH0292997A publication Critical patent/JPH0292997A/en
Publication of JPH0798957B2 publication Critical patent/JPH0798957B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は乳化食品用油脂の製造法に関するものであ
り、より詳しくは、パーム油分画油を原料として、低温
で保存乃至撹拌しても安定な乳化状態を保つ乳化食品を
調製するのに好適な油脂を製造する方法に関するもので
ある。
TECHNICAL FIELD The present invention relates to a method for producing fats and oils for emulsified foods, and more specifically, it is stable when stored or stirred at low temperature using palm oil fractionated oil as a raw material. The present invention relates to a method for producing fats and oils suitable for preparing an emulsified food that maintains a stable emulsified state.

〔従来の技術〕[Conventional technology]

サラダ油等の主原料に使用される大豆油、菜種油、コー
ン油、米油、棉実油、紅花油、カポック油、落花生油、
サフラワー油、ヒマワリ油等の液体油は、カカオバタ
ー、シアバター、サル脂等の所謂植物バターに比べると
安価ではあるものの、パーム油及びその分画油に比べれ
ば一般により高価である。このため、従来からパーム油
又はその分画油をサラダ油原料の一部に使用することに
より原料油脂のコストを低下させることを意図して、多
くの提案がなされて来ている。
Soybean oil, rapeseed oil, corn oil, rice oil, cottonseed oil, safflower oil, kapok oil, peanut oil, used as the main raw material for salad oil, etc.
Although liquid oils such as safflower oil and sunflower oil are cheaper than so-called plant butters such as cocoa butter, shea butter and sal butter, they are generally more expensive than palm oil and fractionated oils thereof. Therefore, many proposals have heretofore been made with the intention of using palm oil or a fractionated oil thereof as a part of a raw material for salad oil to reduce the cost of the raw material oil and fat.

これら提案には、特開昭49−107304号、特開昭53−6340
3号、特開昭60−110246号、特開昭61−293389号、特開
昭61−296096号等があるが、特開昭63−198992号明細書
はそれら従前技術の多くについて種々の難点があること
を言及している。
These proposals include JP-A-49-107304 and JP-A-53-6340.
No. 3, JP-A-60-110246, JP-A-61-293389, JP-A-61-296096, etc., but JP-A-63-198992 describes various difficulties in many of the prior arts. That there is.

また該特開昭63−198992号明細書自体は、「『パーム
油、パームステアリン、パームオレイン』等の固定脂と
『なたね油、パーム分別液体油』等の液体油の混合物に
1,3選択性を有するリパーゼを触媒として酵素的エステ
ル交換反応を起こさせる液体油の製造法」を提案してお
り、該提案の「キーポイント」として、選択的なエステ
ル交換によって「飽和脂肪酸を2つ以上含むトリグリセ
ライドが減少」即ち「(S/S/S),(S/S/U)という組み
合わせのトリグリセリドが減少し、耐寒性が改善される
はずである」と主張し、エステル交換後は、「従来必要
であった分別操作がほぼ不要になった」と述べている。
Further, the specification of Japanese Patent Laid-Open No. 63-198992 itself describes a mixture of a fixed oil such as "palm oil, palm stearin, palm olein" and a liquid oil such as "rapeseed oil, palm fractionated liquid oil".
A method for producing a liquid oil in which an enzymatic transesterification reaction is caused by using a lipase having 1,3 selectivity as a catalyst is proposed, and as a "key point" of the proposal, "a saturated fatty acid is converted into a saturated fatty acid by selective transesterification". Decrease in triglyceride containing two or more ", that is," triglyceride in combination of (S / S / S) and (S / S / U) should be reduced, and cold resistance should be improved. ""The sorting operation that was necessary in the past has become almost unnecessary," he said.

このように、パーム油はそれがたとえパームオレインと
いわれる低融点画分であっても固形成分を含んでいて、
液体油製品の一部原料として使用するには、耐寒性を改
善する必要があったが、本発明者の知見では、特開昭63
−198992号の方法でも、低温保存後に生じる「にごり」
の問題は依然解決されていない。
Thus, palm oil contains solid components even if it is a low melting point fraction called palm olein,
Although it was necessary to improve cold resistance in order to use it as a part of a raw material for liquid oil products, the inventors of the present invention have found that it is not possible to improve the cold resistance.
-Even with the method of 198992, "smudge" that occurs after low-temperature storage
The problem of has not been solved yet.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

パームオレインを液体油と混合し、これに1,3位に選択
的に作用するエステル交換を実施した油脂については、
本発明者も従来から種々の検討を行っているが、本発明
者は、パーム油の液体油を配合して1,3位選択的なエス
テル交換を実施する方法は、サラダ油を目的物として得
る方法としてはあまり適した方法ではないと認識してい
る。その理由は、得られるエステル交換油はどうして
も長時間の低温保存によって「にごり」が生じる他に、
これをあえて使用してマヨネーズの調製をし冷蔵保存す
ると、乳化破壊がおこって油分離が生じること、その
原因を調べるために、エステル交換油そのものを、5℃
で1か月程度放置した状態を顕微鏡的レベルで観察する
と、針状の結晶が「毬栗」の毬(いが)のように成長し
た粗大な結晶になっているのが確認され、それが界面を
破壊する原因と推認されること、並びに「パームオレ
イン」を使用したエステル交換油の場合ですら、存在す
る(S/S/U)(S及びUはグリセリドを構成する飽和脂
肪酸残基及び不飽和脂肪酸残基であって、後掲表中でSS
Uと略記する場合と同様、残基の結合位置を特定しない
表現。S/S/S,S/U/U,U/U/Uなどについても以下同様)の
レベルは決して低くないばかりか、(S/S/S)の含量は
エステル交換後むしろ増大する、等の知見を得ているた
めである。
Regarding fats and oils in which palm olein was mixed with liquid oil and transesterification which selectively acts on the 1,3-position was carried out,
Although the present inventor has also made various studies from the past, the present inventor has found that a method of blending a liquid oil of palm oil and performing 1,3-position selective transesterification obtains a salad oil as a target product. We recognize that it is not a very suitable method. The reason is that the obtained transesterified oil will inevitably cause "turbidity" due to long-term low temperature storage,
If you dare to use this to prepare mayonnaise and store it in the refrigerator, emulsion depletion will occur and oil separation will occur.
When observed at a microscopic level for about a month, it was confirmed that the needle-shaped crystals were coarse crystals that grew like the pearls of "Kuri chestnut," and that was the interface. (S / S / U), where S and U are saturated fatty acid residues and Saturated fatty acid residue, SS in the table below
As in the case of abbreviated as U, an expression that does not specify the binding position of the residue. The same applies to S / S / S, S / U / U, U / U / U, etc.), but the (S / S / S) content increases after transesterification, etc. This is because we have obtained the knowledge of.

本発明者は、これらにごりの原因となる結晶化成分の存
在は事後分別でもしない限り不可避であって、コストア
ップの原因となる当該結晶化成分の除去(即ちサラダ油
としての使用)は断念したが、結晶化成分は存在してい
ても低温保存後それを微細な状態に止めおくことがもし
可能であれば、マヨネーズ等の乳化食品に使用すること
ができ、低温保存でも乳化破壊が避けられるのではない
か、と着想し、この着想に基づく種々の検討を行った。
この発明はその検討の結果到達したものであって、単に
U1成分レベルをもっと減少させるただけでは粗大結晶の
生成はさけられないが、加えて若干の(S/S/S)成分を
増大させることがむしろ結晶核の数を増大させるので結
晶の粗大化を防ぐのに有効である、等の知見を得て完成
された。
The present inventor is unavoidable unless there is a post-fractionation for the presence of a crystallization component that causes a turbidity, and abandoned removal of the crystallization component that causes a cost increase (that is, use as salad oil). , Even if a crystallization component is present, it can be used in an emulsion food such as mayonnaise if it can be kept in a fine state after low temperature storage, and emulsion destruction can be avoided even at low temperature storage. I thought that it might be, and conducted various studies based on this idea.
This invention has been reached as a result of the examination,
Even if the U 1 component level is further reduced, the formation of coarse crystals is unavoidable, but in addition, increasing a small amount of (S / S / S) components rather increases the number of crystal nuclei, so that coarse crystals are formed. It was completed by obtaining the knowledge that it is effective in preventing aging.

この発明は、最後の工程で結晶化成分除去のための分別
作業を必要としないばかりか、冷蔵保存で生じる結晶が
微細な状態にとどまる油脂、換言すれば、冷蔵保存して
も乳化破壊がおこらない乳化食品を製造するのに適した
油脂を製造することを目的とする。
This invention does not require a fractionation work for removing the crystallization component in the last step, and the oils and fats in which the crystals generated in refrigeration storage remain in a fine state, in other words, the emulsion destruction occurs even in refrigeration storage. It is intended to produce fats and oils suitable for producing non-emulsified foods.

〔問題点を解決するための手段及び作用〕[Means and Actions for Solving Problems]

この発明は、沃素価64〜70の軟質パーム油とこれより沃
素価の高い液体油脂との混合油の、1−,3−位を選択的
にエステル交換することを特徴とする乳化食品用油脂の
製造法である。
This invention relates to an oil and fat for emulsified foods characterized by selectively transesterifying 1-, 3-positions of a mixed oil of a soft palm oil having an iodine value of 64-70 and a liquid oil having a higher iodine value. Is a manufacturing method of.

即ちパーム油は、沃素価64以上のパーム分画油を使用で
き、好ましくは67以上の軟質パーム油を使用するのがよ
い。沃素価は低すぎるとU1成分を少なく抑制できず、あ
まり高すぎると後のエステル交換でU0成分となるPP0な
どのU1成分が少なくなりすぎて好ましくない。市販品と
してはdouble fracionation palm oleinとか、スーパー
オレインと呼ばれているものを使用でき、沃素価60〜62
のものから、67近辺のものまで種々市販されている。一
般には、パーム油の高融点部分を分別除去して低融点画
分(パームオレインを得、これをさらに分別し高融点画
分を除去して得ることができ、分別方法は溶剤分別法、
界面活性剤による分別法、乾式(無溶剤)分別法のいず
れによってもよい。パーム軟質油は上記よりもさらに多
段の分別工程を経て得ることは構わないが、一般には2
段の分別工程を経れば充分であり、また溶剤を用いる方
が沃素価の低いものをより容易に得ることができる。
That is, as the palm oil, palm fractionated oil having an iodine value of 64 or more can be used, and soft palm oil of 67 or more is preferably used. If the iodine value is too low, the U 1 component cannot be suppressed to a small amount, and if it is too high, the U 1 component such as PP 0 which becomes a U 0 component in the subsequent transesterification is too small, which is not preferable. As a commercially available product, double fracionation palm olein or what is called super olein can be used, and the iodine value is 60 to 62.
There are various types on the market, ranging from those around 67. Generally, the high melting point portion of palm oil is fractionally removed to obtain a low melting point fraction (perm olein is obtained, which can be further fractionated to remove the high melting point fraction, and the fractionation method is a solvent fractionation method,
Either a fractionation method using a surfactant or a dry (solventless) fractionation method may be used. The soft palm oil may be obtained through more stages of fractionation than the above, but generally 2
It suffices to go through the steps of fractionation, and the use of a solvent makes it possible to easily obtain one having a lower iodine value.

上記軟質パーム油よりも沃素価の高い液油油脂として
は、サラダ油等の主原料に使用される前述の大豆油、菜
種油、コーン油、米油、棉実油、紅花油、カポック油、
落花生油、サフラワー油、ヒマワリ油等の液体油が例示
される。
As the liquid oil fat having a higher iodine value than the soft palm oil, the above-mentioned soybean oil, rapeseed oil, corn oil, rice oil, cottonseed oil, safflower oil, kapok oil, which is used as a main raw material for salad oil and the like,
Liquid oils such as peanut oil, safflower oil and sunflower oil are exemplified.

上記軟質パーム油と液体油の配合比は、1:1〜1:5の範囲
が好ましい。前者の比が少なすぎると液体油の代替率が
低くて経済的効果が殆どなく、多すぎると、U1成分を少
なく抑制することができずやはり低温での長期保存や撹
拌による粗大結晶の生成を防止しがたい。
The blending ratio of the soft palm oil and the liquid oil is preferably in the range of 1: 1 to 1: 5. If the former ratio is too low, the substitution rate of liquid oil is low and there is almost no economic effect, and if it is too high, the U 1 component cannot be suppressed to a small extent, and coarse crystals are formed even after long-term storage at low temperature and stirring. Is hard to prevent.

上記軟質パーム油と液体油は調合後、1−,3−位選択性
のあるエステル交換処理を施すが、1−,3−位に選択的
に作用するリパーゼ若しくはリパーゼ製剤自体、或いは
それらを用いてエステル交換する方法は、例えば特開昭
52−104506号、特開昭55−71797号、特開昭55−84397
号、特開昭56−127094号、特開昭56−163196号、特開昭
57−78496号、特表昭59−500649号、特開昭60−19495号
等に記載されていて公知であり、特反応系中の水は可及
的減少した状態で行うのが副反応物の生成を抑制するた
めに好ましい。
The above-mentioned soft palm oil and liquid oil are subjected to transesterification treatment with 1-, 3-position selectivity after mixing, but lipase or lipase preparation itself which selectively acts at 1-, 3-position, or using them A method for transesterification is disclosed in
52-104506, JP-A-55-71797, JP-A-55-84397
JP-A-56-127094, JP-A-56-163196, JP-A-SHO
57-78496, JP-A-59-500649, JP-A-60-19495 and the like, which are publicly known, and it is a side reaction product that water in a special reaction system is reduced as much as possible. Is preferable for suppressing the generation of

尚この発明により得られる油脂はサラダ油の用途を目的
としないので、エステル交換反応後は分別は全く必要と
しない。この発明により得られる油脂は冷蔵して保存さ
れる乳化食品や撹拌しても乳化破壊しにくい食品素材に
利用でき、とりわけ、マヨネーズ等ドレッシングや、ク
リームチーズ様食品等の酸性水中油型クリーム類を調製
するための主要油脂原料として用いて、長期の低温保存
や撹拌等による乳化破壊を防止する効果が顕著である。
Since the fats and oils obtained according to the present invention are not intended for use as salad oil, no separation is necessary after the transesterification reaction. Oils and fats obtained by this invention can be used for emulsion foods that are refrigerated and stored and food materials that are not easily destroyed by emulsification even when stirred, and in particular, dressings such as mayonnaise and acidic oil-in-water creams such as cream cheese-like foods. It is used as a main raw material of oils and fats for preparation, and has a remarkable effect of preventing emulsion destruction due to long-term low temperature storage, stirring, and the like.

〔実施例等〕[Examples, etc.]

以下この発明を実施例、比較例、応用例等で説明する。 The present invention will be described below with reference to examples, comparative examples, application examples, and the like.

実施例1 市販パームスーパーオレイン(不二製油株販売「パーム
エース」;沃素価67.8)を菜種油と調合し、この1−,3
−位を選択的にエステル交換した油脂を得た。原料調合
油とエステル交換油のトリグリセリド組成は表−1に、
0℃のCold Test(A.O.C.S.法Cc11−53に準じる)結果
は表−2に、5℃の長時間保蔵による結晶生成量(目
視)は表−3に、及び、5℃の30日保蔵後の顕微鏡写真
は図面(ただし第1図のa及びbはエステル交換油、第
2図のa及びbは原料調合油であって、a及びbは、各
々パーム分画油/菜種油の比率が40/60及び30/70であ
る)に示した。選択的エステル交換処理自体は、U0成分
は増大させ(表−1)、かつ、Cold Testによる評価を
低下させ(にごりを増大させ)(表−2)る等、サラダ
油としての品質を却って低下させるものであったが、逆
に、低温長時間保蔵後の目立つ結晶サイズは単なる調合
油を保蔵した場合に比べて四分の一(配合比40/60の場
合)乃至十数分の一(配合比20/80の場合)の微細な大
きさに止める効果があり(図面参照)、また低温保蔵時
間増大に応じた結晶生成量の増大の程度も抑制されてい
た(表−3)。
Example 1 Commercially available palm super olein ("Palm Ace" sold by Fuji Oil Co., Ltd .; iodine value 67.8) was blended with rapeseed oil to prepare 1-, 3
A fat and oil in which the -position was selectively transesterified was obtained. Table 1 shows the triglyceride composition of the raw material blended oil and the transesterified oil.
The results of cold test at 0 ° C (according to AOCS method Cc11-53) are shown in Table-2, the amount of crystals formed by long-term storage at 5 ° C (visual inspection) is shown in Table-3, and after storage at 5 ° C for 30 days. The micrograph is a drawing (however, a and b in FIG. 1 are transesterified oils, a and b in FIG. 2 are raw material blended oils, and a and b have a palm fractionated oil / rapeseed oil ratio of 40 / 60 and 30/70). The selective transesterification process itself increased the U 0 component (Table-1) and decreased the Cold Test evaluation (increased turbidity) (Table-2). On the contrary, the conspicuous crystal size after storage at low temperature for a long time is one fourth (when the mixing ratio is 40/60) to one tenth (compared to the case of simply storing the blended oil). The compounding ratio was 20/80), and it had the effect of keeping it to a fine size (see the drawing), and the degree of increase in the amount of crystal formation corresponding to the increase in low temperature storage time was also suppressed (Table-3).

なお、5℃30日保蔵後の顕微鏡目視で目立つ結晶サイズ
は、エステル交換油の場合40/60の配合比でも50μ程度
以下であったのに対して、原料調合油の場合は20/80の
配合比でも100μ程度以上であった。
In addition, the crystal size that was noticeable by microscopic observation after storage at 5 ° C for 30 days was about 50μ or less at the compounding ratio of 40/60 in the case of transesterified oil, while it was 20/80 in the case of the raw material blended oil. The compounding ratio was about 100 μ or more.

比較例 実施例1の市販パームスーパーオレインに代えて、一段
分別油であるパームオレイン(沃素価56.8)を使用し、
これを菜種油と調合し、その1−,3−位を選択的にエス
テル交換した油脂を得る比較例も実施した(調合比は20
/80〜40/60)。
Comparative Example Palm olein (iodine value 56.8), which is a one-stage fractionated oil, was used in place of the commercial palm super olein of Example 1.
A comparative example was also prepared in which this was mixed with rapeseed oil to obtain fats and oils in which the 1- and 3-positions were selectively transesterified (compounding ratio was 20
/ 80-40 / 60).

この場合の、原料調合油とエステル交換油、ともに5℃
30日保蔵後の顕微鏡目視では、いずれも結晶が粗大であ
った(目立つ結晶サイズは配合比20/80で80μ程度、配
合比30/70で120μ程度、配合比40/60で200μ程度)。ト
リグリセリド組成は表−4に示した。
In this case, both raw material blended oil and transesterified oil are 5 ° C
The crystals were coarse when observed under a microscope after 30 days of storage (the outstanding crystal sizes were about 80μ at a compounding ratio of 20/80, about 120μ at a compounding ratio of 30/70, and about 200μ at a compounding ratio of 40/60). The triglyceride composition is shown in Table-4.

実施例2 沃素価64.5のパームスーパーオレインを調製し、これと
大豆油を30/70の比で調合し、この1−,3−位を選択的
にエステル交換した油脂を得た。この油脂は5℃30日保
蔵後の顕微鏡目視では、前期比較例の20/80配合のエス
テル交換油より微細な結晶状態に止まっていた。
Example 2 Palm super olein having an iodine value of 64.5 was prepared, and this was mixed with soybean oil in a ratio of 30/70 to obtain a fat or oil in which the 1-, 3-position was selectively transesterified. This oil / fat remained in a finer crystalline state than that of the transesterified oil of 20/80 blended in the previous Comparative Example, when observed under a microscope after storage at 5 ° C. for 30 days.

応用例1 実施例1及び比較例の「30/70」の配合比の原料調合油
とエステル交換油を使用し、該油脂70%、卵黄液15%、
食酢(酸度5%)、食塩3%、グルタミン酸ソーダ1
%、マスタード粉末1%を混合した後、乳化機を通し
て、マヨネーズを製造した。これを200ml容のガラスび
んに密封してから−5℃の室内に1週間保存し、油の分
離を判定したところ、次の表の結果を得た。
Application Example 1 Using a raw material blended oil and a transesterified oil having a blending ratio of "30/70" of Example 1 and Comparative Example, 70% of the fat and oil, 15% of yolk liquid
Vinegar (acidity 5%), salt 3%, sodium glutamate 1
% And mustard powder 1% were mixed and then passed through an emulsifying machine to produce mayonnaise. This was sealed in a 200 ml glass bottle and then stored in a room at -5 ° C for 1 week to determine the separation of oil. The results shown in the following table were obtained.

応用例2 実施例2で得られた油脂12部を、脱脂粉乳8部、水80
部、レシチン0.015部との混合物をホモミキサーにて70
℃30分間乳化殺菌した後100kg/cm2の条件下で均質化
し、次に品温22℃で乳酸醗酵させpHが4.6以下になった
時点で加熱撹拌して醗酵を止め、遠心分離して水分56%
のカードを得、それにカードに対し3%のラクトアルブ
ミン、適量の食塩、及び安定剤を加え、70℃の加熱撹拌
と100kg/cm2の均質化処理を行い、クリームチーズ様乳
化食品を得た。
Application Example 2 12 parts of the oil / fat obtained in Example 2, 8 parts of skimmed milk powder, 80 parts of water
Part, and a mixture of 0.015 parts of lecithin with a homomixer 70
℃ 30 minutes after emulsification and homogenization under the conditions of 100kg / cm 2 , lactic acid fermentation at a product temperature of 22 ℃ and when the pH becomes 4.6 or less, heat and stir to stop the fermentation, centrifuge to remove water 56%
The curd was obtained, 3% lactalbumin, an appropriate amount of salt and a stabilizer were added to the curd, and the mixture was heated and stirred at 70 ° C. and homogenized at 100 kg / cm 2 to obtain a cream cheese-like emulsified food. .

この乳化食品を冷蔵庫で一夜冷蔵後、18℃で「レオン包
餡機形式N207DD」に内在として供給し、同時に外皮とし
て練りパイ生地を供給し、ギロチン式にカットし、その
後200℃にて14時間焼成した。包餡機における操作では
2時間撹拌するも油のしみだしがなく、ギロチンカット
の切断面について焼成後に外材からの内材のこぼれがな
く、かつ焼成後も油の分離が認められなかった。しか
し、実施例2で軟質パーム油として、沃素価56.8のもの
を使用する他は、同様に大豆油と配合しエステル交換し
て得た油脂を、本応用例の原料油脂として使用すると、
包餡機における操作では1時間以内に油のしみだしがあ
り、ギロチンカットの切断面については焼成後に外材か
らの内材のこぼれがあり、かつ焼成後も油の若干の分離
が認められた。
After refrigerating this emulsified food overnight in the refrigerator, at 18 ℃, it is supplied as an internal to "Leon wrapping machine type N207DD", and at the same time, kneaded pie dough is supplied as the outer skin and cut into guillotine, then at 200 ℃ for 14 hours Baked. In the operation in the stuffing machine, no oil oozes out even after stirring for 2 hours, there is no spilling of the inner material from the outer material after firing on the cut surface of the guillotine cut, and no oil separation was observed even after firing. However, except that the soft palm oil having an iodine value of 56.8 was used in Example 2, and the oil / fat obtained by transesterification similarly with soybean oil was used as the raw material oil / fat of this application example,
With the operation in the gluing machine, oil oozes out within 1 hour, and the cut surface of the guillotine cut has spilled of the inner material from the outer material after firing, and some separation of the oil was observed after firing.

〔効果〕〔effect〕

以上説明のとおり、本発明方法によって得る油脂は、最
後の工程で分別作業を必要としないばかりか、冷蔵保存
や低温撹拌で生じる結晶が微細な状態にとどまる油脂で
あり、冷蔵保存やあまり高くない温度範囲での撹拌作業
で乳化破壊がおこらない乳化食品を製造するのに適して
いる。
As described above, the fats and oils obtained by the method of the present invention are fats and oils that do not require fractionation work in the last step, and that the crystals produced by refrigeration storage or low temperature stirring remain in a fine state, and refrigeration storage or not so high. It is suitable for producing emulsified foods that do not undergo emulsion destruction by stirring in the temperature range.

【図面の簡単な説明】[Brief description of drawings]

第1図(a,b)は各々本願実施例1におけるエステル交
換油とその原料調合油の5℃で30日保存後の結晶状態を
示す顕微鏡写真(200倍)であり、パーム軟質油と菜種
油の配合比が40/60の場合を示す。 第2図(a,b)は各々本願実施例1及び比較例における
エステル交換油とその原料調合油の5℃で30日保存後の
結晶状態を示す顕微鏡写真(200倍)であり、パーム軟
質油と菜種油の配合比が30/70の各場合を示す。
FIG. 1 (a, b) are micrographs (200 times) showing the crystalline state of the transesterified oil and the raw material blended oil thereof in Example 1 of the present application after storage at 5 ° C. for 30 days, respectively, and soft palm oil and rapeseed oil. The case where the compounding ratio is 40/60 is shown. 2 (a, b) are micrographs (200 times) showing the crystalline state of the transesterified oil and the raw material blended oil thereof in Example 1 and Comparative Example of the present invention after storage at 5 ° C. for 30 days, respectively. The case where the mixing ratio of oil and rapeseed oil is 30/70 is shown.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】沃素価64〜70の軟質パーム油とこれより沃
素価の高い液体油脂を1:1〜1:5で配合した混合油の、1
−,3−位を選択的にエステル交換することを特徴とする
乳化食品用油脂の製造法。
1. A mixed oil comprising a soft palm oil having an iodine value of 64-70 and a liquid oil having a higher iodine value than 1: 1 in a ratio of 1: 1 to 1: 5.
A method for producing an oil or fat for emulsified foods, which comprises selectively transesterifying the 3- and 3-positions.
JP63247017A 1988-09-29 1988-09-29 Method for producing fats and oils for emulsified foods Expired - Lifetime JPH0798957B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63247017A JPH0798957B2 (en) 1988-09-29 1988-09-29 Method for producing fats and oils for emulsified foods

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63247017A JPH0798957B2 (en) 1988-09-29 1988-09-29 Method for producing fats and oils for emulsified foods

Publications (2)

Publication Number Publication Date
JPH0292997A JPH0292997A (en) 1990-04-03
JPH0798957B2 true JPH0798957B2 (en) 1995-10-25

Family

ID=17157160

Family Applications (1)

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Country Link
JP (1) JPH0798957B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5601860A (en) * 1990-11-30 1997-02-11 American Home Products Corporation Corandomized fat compositions for infant formulas
JP3388838B2 (en) * 1993-11-18 2003-03-24 旭電化工業株式会社 Method for producing fat composition for confectionery
JP3773330B2 (en) * 1997-08-01 2006-05-10 旭電化工業株式会社 Vinyl chloride resin composition
JP4410699B2 (en) * 2005-02-23 2010-02-03 日清オイリオグループ株式会社 Oil and fat composition and method for producing oil and fat composition
JP4493585B2 (en) * 2005-11-25 2010-06-30 株式会社Adeka Oil and fat composition for kneading baked confectionery with oily ingredients
JP4501035B2 (en) * 2007-10-03 2010-07-14 日清オイリオグループ株式会社 Edible oil and fat composition
JP4651734B1 (en) * 2009-09-30 2011-03-16 日清オイリオグループ株式会社 Oil and fat manufacturing method
CN102503912B (en) * 2011-10-26 2013-11-27 邹平福海科技发展有限公司 High epoxide number environment-friendly plasticizer production process

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* Cited by examiner, † Cited by third party
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JPS49107304A (en) * 1973-02-14 1974-10-11
JP2687337B2 (en) * 1987-02-13 1997-12-08 味の素株式会社 Liquid oil manufacturing method

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