JPS5943137B2 - hard butter - Google Patents
hard butterInfo
- Publication number
- JPS5943137B2 JPS5943137B2 JP12698779A JP12698779A JPS5943137B2 JP S5943137 B2 JPS5943137 B2 JP S5943137B2 JP 12698779 A JP12698779 A JP 12698779A JP 12698779 A JP12698779 A JP 12698779A JP S5943137 B2 JPS5943137 B2 JP S5943137B2
- Authority
- JP
- Japan
- Prior art keywords
- component
- ratio
- oil
- oils
- fractionated
- 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
Links
Landscapes
- Dairy Products (AREA)
- Edible Oils And Fats (AREA)
Description
【発明の詳細な説明】
本発明は、融解性状の極めて優れたラウリン系バードバ
ターに関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a lauric bird butter with extremely excellent melting properties.
従来ヤシ油、パーム核油等の名称で知られるラウリン系
油脂は、それらを適当な条件下で分別して得られる分画
油または硬化油若しくはエステル交換油等がバードバク
−として利用されている。Conventionally, lauric oils and fats known as coconut oil, palm kernel oil, etc. are used as bird bags, such as fractionated oils, hydrogenated oils, or transesterified oils obtained by fractionating them under appropriate conditions.
これらのうち、特に溶剤分別して得られる分画油は、通
常そのままで、またはそれを水素添加したものが専ら利
用されている。Among these, the fractionated oil obtained by solvent fractionation is usually used as it is or after hydrogenation.
このような従来のバードパll−は一応使用されている
ものの、未だ満足すべき融解性状を有したものとはいえ
ない。Although such conventional bird palls have been used to some extent, they cannot yet be said to have satisfactory melting properties.
本発明者らは、以上の点に鑑み鋭意研究を重ねた結果、
トリグリセリドを構成する結合脂肪酸基の炭素数合計量
の特定成分が、一定の範囲内で存在するラウリン系油脂
の分画油は、それを水素添加したとき極めて優れた融解
性状を呈するという知見を得た。As a result of intensive research in view of the above points, the present inventors found that
We have obtained the knowledge that fractionated oils of lauric fats and oils in which the total number of carbon atoms in the bound fatty acid groups constituting triglycerides exist within a certain range exhibit extremely excellent melting properties when they are hydrogenated. Ta.
本発明は、かかる知見に基づいて完成されたものである
。The present invention was completed based on this knowledge.
即ち、本発明はラウリン系油脂を分別して得られる分画
油のトリグリセリド組成において、トリグリセリドを構
成する結合脂肪酸基の炭素数の合計量(以下、TG−C
と略す)36成分に対するTG−C38成分の割合が8
2係(重量基準、以下同じ)以下で、TG−C36成分
に対するTG−C34成分の割合が30%以下であり、
かつ、TG−C40成分に対するTG−C42成分の割
合が65係以下であるラウリン系油脂の分画硬化油から
成るバードパl−である。That is, the present invention provides a triglyceride composition of a fractionated oil obtained by fractionating lauric fats and oils.
) The ratio of TG-C38 component to 36 components is 8
The ratio of the TG-C34 component to the TG-C36 component is 30% or less at the 2nd scale (weight basis, the same applies hereinafter),
In addition, Bird Pal is made of a fractionated hydrogenated oil of lauric oil and fat in which the ratio of the TG-C42 component to the TG-C40 component is 65 parts or less.
本発明によれば、本発明に規定する範囲を満足するラウ
リン系油脂の分画油は、′例えばn−へキサンの如き比
較的低極性溶剤によって得ることができ、アセトンの如
き比較的極性の高い溶剤では得ることができない。According to the present invention, a fractionated oil of lauric fats and oils that satisfies the range specified in the present invention can be obtained using a relatively low polar solvent such as n-hexane, and a relatively low polar solvent such as acetone. It cannot be obtained with expensive solvents.
いまパーム核油に例をとると、分別前のトリクリ−21
Jド組成の1例は以下の如くである。Taking palm kernel oil as an example, TRIC-21 before separation
An example of a J-do composition is as follows.
上記組成を有したパーム核油をn−へキサンで分別処理
して得られる分画油のトリクリセリド組成の結果は、後
記製造例1に示すとおりであり、−万アセトンで分別処
理して得られる分画油の結果は、後記製造比較例3に示
すとおりである。The results of the tricryceride composition of the fractionated oil obtained by fractionating palm kernel oil having the above composition with n-hexane are as shown in Production Example 1 below, and the results obtained by fractionating palm kernel oil with -10,000 acetone. The results of the fractionated oil are as shown in Comparative Production Example 3 below.
これら両者の結果を比較すると明らかな様に、TG−C
38/TG−C36の割合は、n−へキサン使用の場合
76係であるのに対し、アセトンの場合89係であって
異なる。As is clear from comparing these two results, TG-C
The ratio of 38/TG-C36 is 76 when n-hexane is used, whereas it is 89 when acetone is used.
この結果が融解性状に坤*おいて差を有することは図−
2に示すとおりである。This result shows that there is a difference in the melting properties as shown in the figure.
As shown in 2.
また本発明によると、TG−C36成分に対するTG−
C34成分の割合が30%を越えると全体に軟らかくな
り、水素添加しても20°〜25℃での固体脂含有指数
(SCI)値が低く、全体として融解性状としてのシャ
ープさに欠ける傾向にある。Further, according to the present invention, TG-C36 component
When the proportion of C34 component exceeds 30%, the product becomes soft as a whole, and even when hydrogenated, the solid fat content index (SCI) value at 20° to 25°C is low, and the overall melting properties tend to lack sharpness. be.
さらに、TG−C40成分に対するTG−C42成分の
割合が65係を越えると、水素添加した硬化油は高融点
部分を生じ、0融けの悪いものとなる。Furthermore, if the ratio of the TG-C42 component to the TG-C40 component exceeds 65%, the hydrogenated hardened oil will have a high melting point portion and will have poor melting properties.
これはTG−C42成分中の結合脂肪酸に炭素数18の
不飽和脂肪酸が含まれており、これが水素添加の結果飽
和脂肪酸となって0融けを悪化させる原因になるものと
考えられる。This is thought to be because the bound fatty acids in the TG-C42 component include unsaturated fatty acids with 18 carbon atoms, which become saturated fatty acids as a result of hydrogenation and become a cause of worsening zero melting.
これらの現象は、後記製造例1に準じて実施し結晶部の
収率を上げることにより生ずることが以下の実験結果か
ら窺われる。It can be seen from the following experimental results that these phenomena are caused by increasing the yield of crystalline portions by carrying out production according to Production Example 1 described later.
このうち実験4で得た両分を極度水素添加したものの融
解性状を測定した結果、その固体脂含有指数は
10 ℃ 76%
20 ℃ 75%
25 ℃ 69%
27.58C60%
30 ℃ 35%
35 ℃ 7%
37、5℃ 2%
40 ℃ 0%
であって、後記製造比較例3とほぼ同程度の性状を示し
不良であった。As a result of measuring the melting properties of the two parts obtained in Experiment 4 which were subjected to extreme hydrogenation, the solid fat content index was
10 °C 76% 20 °C 75% 25 °C 69% 27.58C60% 30 °C 35% 35 °C 7% 37. The display was defective.
。なお、油脂のトリクリ上リド組成を測定する方法とし
て薄層クロマトグラフィー(TLC)法等があるが、本
発明においてはガスクロマトグラフィーにより以下の機
器及び条件で測定した。. Note that thin layer chromatography (TLC) is a method for measuring the trichloride composition of fats and oils, and in the present invention, measurement was performed using gas chromatography using the following equipment and conditions.
機 器:■島津製作所、ModelC4CM
検 出 器:FID 350℃
力 ラ ム:3FIEIIIφ×50cm ガラス
充 填 剤:シリコン0V−172%クロモゾルブ
W、担持60〜
80mesh(西尾工業■製)
温 度=225℃〜345℃昇温(5℃、/分
フ
キャリャーガス二N2100m1Z分
試料調整:2.5%CCl4溶液、50μmヲ注入
尚、当然ながら測定値は既知試料の測定結果により、ガ
スクロマトグラフ測定値を重量%に換算した。Equipment: ■Shimadzu Corporation, Model C4CM Detector: FID 350℃ Power Ram: 3FIEIIIφ x 50cm Glass filler: Silicon 0V-172% Chromosolve W, supported 60-80mesh (manufactured by Nishio Kogyo ■) Temperature = 225℃ Temperature increase to ~345℃ (5℃, /min) Carrier gas 2N2100ml 1Z minute Sample preparation: 2.5% CCl4 solution, 50μm injection Converted.
以下に本発明の製造例、製造比較例を例示する。Production examples of the present invention and comparative production examples are illustrated below.
製造例 1
脱酸処理を施したパーム核油1部(重量基準、以下同じ
)を加部融解後n−ヘキサン9部に溶解し、攪拌しなが
ら一16℃まで△0.5℃/分の温度勾配で冷却して析
出する結晶を戸別した。Production Example 1 1 part of deoxidized palm kernel oil (based on weight, the same applies hereinafter) was partially melted and then dissolved in 9 parts of n-hexane, and heated at △0.5°C/min from -16°C with stirring. The crystals precipitated by cooling with a temperature gradient were separated from each other.
次いで該結晶に一18℃に冷却したn−ヘキサン2部を
加え、十分洗浄した後戸別し、脱溶剤して以下の性状を
有する分画油0.56部(収率56%)を得た。Next, 2 parts of n-hexane cooled to -18°C was added to the crystals, thoroughly washed, separated, and the solvent was removed to obtain 0.56 parts (yield 56%) of a fractionated oil having the following properties. .
融点(Spt、)3x、5℃ 沃素価(IV)6.0
6上記分画油を極度水素添加することにより、図−1に
示すとおり極めて融解性状に優れたSCI値を有するハ
ードバターが得られた。Melting point (Spt,) 3x, 5℃ Iodine value (IV) 6.0
6 By subjecting the above fractionated oil to extreme hydrogenation, hard butter having extremely excellent melting properties and an SCI value was obtained as shown in Figure 1.
融点 33.3℃ IV、 0.57製造比較
例 1
製造例]において、同様にして得た結晶を炉別した後、
該結晶に一18℃のn−ヘキサン2部を加え洗浄後脱溶
剤して、以下の性状を有する分画油0.6部を得た。Melting point: 33.3°C
The crystals were washed with 2 parts of n-hexane at -18°C and then the solvent was removed to obtain 0.6 parts of a fractionated oil having the following properties.
融点 30.6℃ IV、 9.79上記分画油
を極度水素添加した硬化油は、図−1に示すとおり、高
融点部分を有する融解性状の悪いものであった。Melting point: 30.6°C IV, 9.79 The hardened oil obtained by extremely hydrogenating the above fractionated oil had a high melting point portion and poor melting properties, as shown in Figure 1.
融点 34.3℃ IV、 0.40製造比較
例 2
製造比較例1において、60.05℃57分の温度勾配
で冷却した以外全て同様にして分画油0.49部を得た
。Melting point: 34.3°C IV, 0.40 Comparative Production Example 2 0.49 part of a fractionated oil was obtained in the same manner as in Comparative Production Example 1 except that the oil was cooled with a temperature gradient of 60.05°C and 57 minutes.
融点 31.0℃ IV、 9.80この分画
油を極度水素添加した硬化油は、図−2は示すとおり高
融点部分を有する融解性状の悪いものであった。Melting point: 31.0°C IV, 9.80 The hardened oil obtained by extremely hydrogenating this fractionated oil had poor melting properties and had a high melting point portion, as shown in Figure 2.
融点 34.8℃ IV、 0.31裳造比較
例 3
製造例1において、n−へキサンの代りにアセトン(含
水率0.2%)を使用し、同様にして一4℃で析出する
結晶を分離後、該結晶に一6℃のアセトン2部を加え充
分洗浄した後1戸別し脱溶剤して以下の分画油0.56
部を得た。Melting point: 34.8°C IV, 0.31 Comparative example of fabrication 3 In Production Example 1, acetone (water content 0.2%) was used instead of n-hexane, and crystals precipitated at -4°C in the same manner. After separating the crystals, add 2 parts of acetone at -6°C, wash thoroughly, and then remove the solvent and obtain the following fractionated oil: 0.56
I got the department.
融点 30.7℃ IV、 10.4この分画
油を極度水素添加した硬化油の
SCI値は図−2に示すとおり、他の製造比較例の場合
と同様不満足な性状を呈していた。Melting point: 30.7°C IV, 10.4 As shown in Figure 2, the SCI value of the hardened oil obtained by subjecting this fractionated oil to extreme hydrogenation exhibited unsatisfactory properties as in the case of other comparative production examples.
融点 34.2℃ IV、 0.21チヨコレ
一ト裂造例
以下に示す配合にて常法通りロール掛けし、コンチング
した後、型に流し冷却後型から離してチョコレートを得
た。Melting point: 34.2°C IV, 0.21 pieces Chocolate making example: After rolling and conching in a conventional manner, the mixture was poured into a mold, cooled, and separated from the mold to obtain chocolate.
配合(重量基準)
粉 糖 42.5 部
ココアパウダー 6.5
脱脂粉乳 20.0 部
へ−ドバJ−31,0
レシチン 0・4
バードバク−として、本発明製造例1で得たものを使用
したチョコレートは、スナップ性良く、0融げの艮好な
ものであった。Blend (based on weight) Powdered sugar 42.5 parts Cocoa powder 6.5 Skim milk powder 20.0 parts - Doba J-31.0 Lecithin 0.4 Bird Bak - The one obtained in Production Example 1 of the present invention was used The chocolate had good snap properties and no melting.
これに対し各製造比較例1〜3で得たものを使用したチ
ョコレートは、0融けの悪いものであった。On the other hand, the chocolates obtained in Comparative Manufacturing Examples 1 to 3 had 0 poor melting properties.
図−1及び2は固体脂含有指数(SCI )を示すグラ
フであって、本明細書中に例示する製造例1及び製造比
較例1〜4で得られた分画油の硬化油のSCI値である
。Figures 1 and 2 are graphs showing the solid fat content index (SCI), and are the SCI values of hydrogenated oils of fractionated oils obtained in Production Example 1 and Production Comparative Examples 1 to 4 exemplified herein. It is.
Claims (1)
リセリド組成において、トリグリセリドを構成する結合
脂肪酸基の炭素数の合計量(以下、TG−Cと略す)3
6成分に対するTG−C38成分の割合が82係(重量
基準、以下同じ)以下で、TG−C36成分に対するT
G−C34成分の割合が30%以下であり、かつ、TG
−C40成分に対するTG−C42成分の割合が65%
以下であるラウリン系油脂の分画硬化油から成るバード
バター。1. In the triglyceride composition of the fractionated oil obtained by fractionating lauric fats and oils, the total number of carbon atoms of the bonded fatty acid groups constituting the triglyceride (hereinafter abbreviated as TG-C) 3
The ratio of the TG-C38 component to the 6 components is below the 82nd ratio (based on weight, the same applies hereinafter), and the ratio of the TG-C38 component to the TG-C36 component is below 82
The proportion of G-C34 component is 30% or less, and TG
-The ratio of TG-C42 component to C40 component is 65%
Bird butter is made from the following fractionated hydrogenated lauric oils:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12698779A JPS5943137B2 (en) | 1979-10-01 | 1979-10-01 | hard butter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12698779A JPS5943137B2 (en) | 1979-10-01 | 1979-10-01 | hard butter |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5651951A JPS5651951A (en) | 1981-05-09 |
| JPS5943137B2 true JPS5943137B2 (en) | 1984-10-19 |
Family
ID=14948842
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12698779A Expired JPS5943137B2 (en) | 1979-10-01 | 1979-10-01 | hard butter |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5943137B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4815746B2 (en) * | 2004-01-27 | 2011-11-16 | 不二製油株式会社 | Cool oil |
-
1979
- 1979-10-01 JP JP12698779A patent/JPS5943137B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5651951A (en) | 1981-05-09 |
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