JPH08242765A - Oil and fat for producing plastic oil and fat composition and plastic oil and fat composition - Google Patents

Oil and fat for producing plastic oil and fat composition and plastic oil and fat composition

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Publication number
JPH08242765A
JPH08242765A JP7048203A JP4820395A JPH08242765A JP H08242765 A JPH08242765 A JP H08242765A JP 7048203 A JP7048203 A JP 7048203A JP 4820395 A JP4820395 A JP 4820395A JP H08242765 A JPH08242765 A JP H08242765A
Authority
JP
Japan
Prior art keywords
oil
fat
composition
plastic
hydrogenated
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.)
Pending
Application number
JP7048203A
Other languages
Japanese (ja)
Inventor
Atsushi Nago
敦 名郷
Katsukiyo Ueda
克清 上田
Tsugio Izumi
次夫 和泉
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
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 Fuji Oil Co Ltd filed Critical Fuji Oil Co Ltd
Priority to JP7048203A priority Critical patent/JPH08242765A/en
Publication of JPH08242765A publication Critical patent/JPH08242765A/en
Pending legal-status Critical Current

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  • Edible Oils And Fats (AREA)

Abstract

PURPOSE: To obtain an oil and fat for giving plastic oil and fat composition which is produced by transesterification of a formulated oil containing a specific amount of a liquid oil, an oil and fat originating from palm oil and a laurin- based oil and fat and is compatible with hardened fish oil and can give margarine, shortening or the like by admixing to other oil and fat. CONSTITUTION: A formulated oil containing 10-15wt.% of a liquid oil, an oil and fat originating from palm oil, preferably in an amount of 35-60wt.%, and a laurin-based oil and fat, preferably in an amount of 30-50wt.%, is transesterified to give the objective oil and fat, preferably having a fatty acid composition of 12-40wt.% palmitic acid residue, 10-20wt.% lauric acid residue and 10-15% of polyunsaturated fatty acid residues.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、可塑性油脂組成物製造
用油脂および可塑性油脂組成物、さらに詳しくは、魚油
硬化油と相溶性を有する可塑性油脂組成物製造用油脂お
よびそれを魚油硬化油と混合使用したマーガリン、ショ
ートニングのごとき可塑性油脂組成物に関する。
TECHNICAL FIELD The present invention relates to an oil and fat for producing a plastic oil and fat composition and a plastic oil and fat composition, and more specifically, an oil and fat for producing a plastic oil and fat composition having compatibility with a fish oil hydrogenated oil and a fish oil hydrogenated oil. The present invention relates to a plastic oil / fat composition such as margarine and shortening used by mixing.

【0002】[0002]

【従来の技術】従来より、製菓・製パン用に使用される
マーガリンやショートニングのごとき可塑性油脂組成物
の多くは魚油硬化油が配合使用されている。その理由の
一つとして、魚油硬化油は安価であることが挙げられる
が、特に、魚油硬化油が可塑性に優れ、製菓特性に優れ
るという点が挙げられる。しかしながら、近年、魚油硬
化油の原料となる小魚の漁獲量が激減し、魚油の生産量
が不足する傾向にあるため、可塑性油脂組成物に配合使
用される魚油硬化油は、その効果が得られる範囲内で可
及的少量が使用されている。そして、魚油硬化油に植物
性油脂の硬化油やパーム系油脂を混合使用した動植タイ
プの可塑性油脂組成物が製造されている。これら動植タ
イプの可塑性油脂組成物は魚油硬化油の良好な製菓特性
を利用し、かつ植物系油脂の優位性(耐熱性等)を持た
せようとしたものであるが、これらの動植物性油脂を使
用したマーガリンやショートニングにおいては魚油硬化
油本来の可塑性範囲の広さや、ホイップ能力(起泡力)
を著しく損ない、僅かに植物系油脂の物性を改良するの
みであった。このような状況下において、魚油硬化油と
相溶性のある特性を持った油脂が求められているが、か
かる特性を持つ油脂は存在せず、わずかな部分を豚脂や
パーム油にて代替しているのが現状である。最近、パー
ム系油脂とラウリン系油脂および液体油の配合油をエス
テル交換した油脂が提案されているが(特開昭60−2
7337号)、かかるエステル交換油脂では魚油硬化油
との相溶性が悪く、魚油硬化油との混合使用における製
菓特性が阻害される。
2. Description of the Related Art Conventionally, fish oil and hydrogenated oil have been compounded and used in many plastic oil and fat compositions such as margarine and shortening used for confectionery and bread making. One of the reasons is that hydrogenated fish oil is inexpensive, but in particular, hydrogenated fish oil is excellent in plasticity and confectionery characteristics. However, in recent years, the catch of small fish, which is a raw material for hydrogenated oil of fish oil, has been drastically reduced, and the production amount of fish oil tends to be insufficient. Therefore, the fish oil hydrogenated oil blended and used in the plastic fat composition has its effect. The smallest possible amount is used within the range. Then, a plastic oil / fat composition of an animal / plant type, which is a mixture of hardened fish oil and hardened vegetable oil or palm oil / fat, is produced. These animal and vegetable type plastic fats and oils compositions utilize the good confectionery characteristics of hydrogenated fish oil and are intended to have the superiority (heat resistance etc.) of vegetable fats and oils. In the margarine and shortening using, the wide range of plasticity of the fish oil hardened oil and the whipping ability (foaming power)
And the physical properties of vegetable fats and oils were only slightly improved. Under such circumstances, oils and fats having characteristics compatible with hydrogenated fish oil are required, but no oils and fats having such characteristics exist, and only a small portion is replaced with lard or palm oil. Is the current situation. Recently, an oil and fat obtained by transesterifying a mixed oil of palm oil and fat, lauric oil and liquid oil has been proposed (JP-A-60-2).
No. 7337), such a transesterified oil / fat has poor compatibility with hydrogenated fish oil, which impairs the confectionery properties in mixed use with hydrogenated fish oil.

【0003】[0003]

【発明が解決しようとする課題】このように、現在の技
術では魚油硬化油と相溶性、さらには相互作用効果によ
り、より良い製菓特性を持つ油脂は存在しておらず、こ
のような物性を持つ油脂が求められている。
As described above, according to the present technology, there is no oil or fat having better confectionery properties due to the compatibility with the hydrogenated oil of fish and the interaction effect. The oil and fat to have is demanded.

【0004】[0004]

【課題を解決するための手段】本発明者は、このような
事情に鑑み鋭意研究した結果、特定割合の液体油とパー
ム油起源の油脂およびラウリン系油脂との配合油をエス
テル交換することにより、特に、トリグリセリド中に該
配合油の脂肪酸残基を分散させることによって、上記す
る欠点を解決し得るという知見を得、本発明を完成する
に至った。
Means for Solving the Problems As a result of intensive studies in view of such circumstances, the present inventor has found that by transesterifying a blended oil of a specific proportion of liquid oil and fats and oils derived from palm oil and lauric fats and oils. In particular, it was found that the above-mentioned drawbacks can be solved by dispersing the fatty acid residue of the blended oil in triglyceride, and the present invention has been completed.

【0005】本発明は、10〜15重量%の液体油を含
み、かつパーム油起源の油脂およびラウリン系油脂を含
む配合油をエステル交換してなる可塑性油脂組成物製造
用油脂を提供するものである。
The present invention provides an oil and fat for producing a plastic oil and fat composition, which comprises 10 to 15% by weight of a liquid oil and transesterifies a compounded oil containing an oil and fat derived from palm oil and a lauric oil and fat. is there.

【0006】また、本発明は、魚油硬化油20〜80重
量%、液体油0〜40重量%および当該可塑性油脂組成
物製造用油脂80〜20重量%を含んでなる可塑性油脂
組成物も提供する。以下の説明において、「%」および
「部」は特に断らない限り重量%および重量部を意味す
る。
The present invention also provides a plastic oil / fat composition comprising 20 to 80% by weight of hydrogenated fish oil, 0 to 40% by weight of liquid oil, and 80 to 20% by weight of the oil or fat for producing the plastic oil or fat composition. . In the following description, "%" and "parts" mean% by weight and parts by weight, unless otherwise specified.

【0007】本発明において用いる液体油としては、多
価不飽和脂肪酸残基を多く持つ、大豆油、菜種油、コー
ン油、米糠油、綿実油等の植物性液体油またはこれらの
微水添油の何れを用いてもよい。本発明の可塑性油性組
成物製造用油脂における液体油の含量は10〜15%
で、液体油が少なすぎると、可塑性を示す範囲が狭くな
り、多すぎると耐熱性、ホイップ性が悪化する傾向を示
す。
The liquid oil used in the present invention is any of vegetable liquid oils such as soybean oil, rapeseed oil, corn oil, rice bran oil, cottonseed oil and the like, or polyhydrogenated oils thereof, which have many polyunsaturated fatty acid residues. May be used. The content of liquid oil in the fats and oils for producing the plastic oily composition of the present invention is 10 to 15%.
When the amount of the liquid oil is too small, the range showing the plasticity becomes narrow, and when it is too large, the heat resistance and the whipping property tend to be deteriorated.

【0008】パーム起源の油脂としては、パルミチン酸
残基を35%以上含有する油脂であって、パーム油自体
またはそれを分画して得られる分画油の何れを用いても
よい。また、ラウリン系油脂はラウリン酸残基を35%
以上、好ましくは35〜50%含有する油脂であって、
ヤシ油、パーム核油自体またはそれを分画して得られる
分画油、またそれらの硬化油の何れを用いてもよい。こ
れらは、一般に、パーム油起源の油脂を35〜60%、
ラウリン系油脂を30〜50%の割合で混合して配合油
とする。パーム油起源の油脂が少なすぎると、可塑性を
示す範囲が狭くなり、多すぎるとホイップ速度が遅くな
る。なお、パーム油起源の油脂およびラウリン系油脂
は、分別方法や分別条件により異なった脂肪酸組成を持
つ分画油が得られる場合があるので、最終的には脂肪酸
残基の組成により判断するのが好ましい。
As the oil and fat derived from palm, any oil or fat containing 35% or more of palmitic acid residues, and either palm oil itself or a fractionated oil obtained by fractionating the palm oil may be used. In addition, lauric oils and fats contain 35% lauric acid residues.
As described above, the fat or oil preferably contains 35 to 50%,
Any of coconut oil, palm kernel oil itself or a fractionated oil obtained by fractionating the same, or a hydrogenated oil thereof may be used. These are generally 35 to 60% of fats and oils derived from palm oil,
Laurin-based fats and oils are mixed at a ratio of 30 to 50% to prepare a blended oil. If the amount of oil and fat derived from palm oil is too small, the range of plasticity becomes narrow, and if it is too large, the whipping speed becomes slow. In addition, since palm oil-derived fats and oils and lauric fats and oils may be obtained as fractionated oils having different fatty acid compositions depending on the fractionation method and fractionation conditions, it is ultimately necessary to judge by the composition of fatty acid residues. preferable.

【0009】本発明の可塑性油脂組成物製造用油脂にお
けるエステル交換は、該液体油を配合油の混合物を自体
公知の方法に付して行うことができる。例えば、ナトリ
ウムメチラート等の金属触媒を用いる方法またはリパー
ゼを触媒とする方法のいずれによっても行うことができ
る。リパーゼは油脂に対しエステル交換活性を有するも
のであればどのような酵素であってもよく、公知のもの
として、例えば、リゾプス属リパーゼ、アスペルギルス
属リパーゼ、ムコール属リパーゼ、パンクレアチツクリ
パーゼ、米糠リパーゼ等が挙げられる。
The transesterification in the fats and oils for producing the plastic fat and oil composition of the present invention can be carried out by subjecting the liquid oil to a mixture of blended oils by a method known per se. For example, it can be carried out by either a method using a metal catalyst such as sodium methylate or a method using a lipase as a catalyst. The lipase may be any enzyme as long as it has a transesterification activity for fats and oils, and known ones include, for example, Rhizopus lipase, Aspergillus lipase, Mucor lipase, Pancreatic lipase, Rice bran lipase. Etc.

【0010】本発明において得られるエステル交換油
は、パルミチン酸残基が12〜40%、ラウリン酸残基
が10〜20%、多価不飽和脂肪酸残基が10〜15%
の脂肪酸組成を有することが好ましい。脂肪酸組成がこ
の範囲を外れると、可塑性を示す範囲が狭くなったり、
ホイップ速度が遅くなったりする。該エステル交換油
は、そのまま可塑性油脂組成物製造用油脂として用いる
ことができ、また、グリセリン脂肪酸エステル、蔗糖脂
肪酸エステル、ポリグリセリン脂肪酸エステル、レシチ
ンなどの添加剤を適宜添加してもよい。
The transesterified oil obtained in the present invention has palmitic acid residues of 12 to 40%, lauric acid residues of 10 to 20%, and polyunsaturated fatty acid residues of 10 to 15%.
It is preferred to have a fatty acid composition of When the fatty acid composition is out of this range, the range showing plasticity becomes narrow,
Whipping speed becomes slow. The transesterified oil can be used as it is as a fat or oil for producing a plastic fat or oil composition, and additives such as glycerin fatty acid ester, sucrose fatty acid ester, polyglycerin fatty acid ester, lecithin and the like may be appropriately added.

【0011】本発明の可塑性油脂組成物製造用油脂は、
自体公知の方法により、組成物全量に対して80〜20
%、好ましくは70〜30%の割合で魚油硬化油と混合
して、品質の良好なマーガリンやショートニングのごと
き可塑性油脂組成物を製造することができる。組成物中
の魚油硬化油の量は20〜80%とし、所望により、上
記したような液体油を40%までの割合で添加してもよ
い。該組成物における本発明の可塑性油脂組成物製造用
油脂の割合が少なすぎると、ホイップ速度における特長
が小さくなり、また、多すぎると可塑性を示す範囲がや
や狭くなる傾向を示す。該組成物には、所望により、通
常この種の組成物に使用されるグリセリン脂肪酸エステ
ル、ポリグリセリン脂肪酸エステル、蔗糖脂肪酸エステ
ル、レシチンなどの添加剤を適宜添加してもよい。
The fats and oils for producing the plastic fat and oil composition of the present invention are:
80 to 20 relative to the total amount of the composition by a method known per se
%, Preferably 70 to 30%, can be mixed with hydrogenated fish oil to produce a good quality plastic oil composition such as margarine or shortening. The amount of hydrogenated fish oil in the composition is 20-80%, and if desired, the liquid oil as described above may be added in a ratio of up to 40%. If the proportion of the fat / oil for producing a plastic fat / oil composition of the present invention in the composition is too small, the characteristics in the whipping speed will be small, and if it is too large, the range showing plasticity will tend to be narrowed slightly. If desired, additives such as glycerin fatty acid ester, polyglycerin fatty acid ester, sucrose fatty acid ester, and lecithin which are usually used in this type of composition may be appropriately added to the composition.

【0012】[0012]

【実施例】以下、実施例により本発明をさらに詳しく説
明するが、本発明はこれらの実施例に限定されるもので
はない。 実施例1および比較例1 パームステアリン(沃素価33)50部、パーム核油4
0部および大豆油10部の割合で混合し、ナトリウムメ
チラートを触媒としてランダムエステル交換を行った
後、水洗、脱水、精製して融点36℃のエステル交換油
を得た。このエステル交換油は融点、SFCを魚油硬化
油(融点36℃)に近似するように設定したものであ
る。かくして得た、エステル交換油、すなわち、本発明
における可塑性油脂組成物製造用油脂をコンビネーター
を用い、常法により、表1に示す配合でショートニング
を製造した。また、比較のための油脂として、同様に融
点、SFCを魚油硬化油(融点36℃)に近似するよう
に調製した大豆硬化油(融点36℃)を使用して同様に
実施した。乳化剤はオレイン酸系モノグリセリドとショ
糖脂肪酸エステルを各0.4%添加して製造した。
The present invention will be described in more detail with reference to the following examples, but the present invention is not limited to these examples. Example 1 and Comparative Example 1 50 parts of palm stearin (iodine value 33), palm kernel oil 4
After mixing 0 parts and 10 parts of soybean oil, random transesterification was carried out using sodium methylate as a catalyst, followed by washing with water, dehydration and purification to obtain a transesterified oil having a melting point of 36 ° C. This transesterified oil has a melting point and SFC set so as to approximate to hydrogenated fish oil (melting point 36 ° C.). The thus obtained transesterified oil, that is, the fat or oil for producing a plastic fat or oil composition according to the present invention, was used in a conventional manner to produce shortenings with the formulations shown in Table 1. Further, as a fat and oil for comparison, similarly, a soybean hydrogenated oil (melting point 36 ° C.) whose SFC and SFC were prepared so as to be similar to hydrogenated fish oil (melting point 36 ° C.) was used. The emulsifier was manufactured by adding 0.4% each of oleic acid type monoglyceride and sucrose fatty acid ester.

【0013】[0013]

【表1】 ショートニング油脂配合 対 照 実施例1 比較例1 エステル交換油 − 40% − 大豆硬化油(融点36℃) − − 20% 魚油硬化油(融点36℃) 80% 40 60大豆油 20 20 20 レオメーター値* 10℃ 1040 1100 1860 15℃ 510 530 800 20℃ 190 220 385 *不動工業(株)製、単位:g/0.785cm2 [Table 1] Comparison of shortening oil and fat blending Example 1 Comparative Example 1 Transesterified oil -40%-hydrogenated soybean oil (melting point 36 ° C) -20% fish hydrogenated oil fish oil (melting point 36 ° C) 80% 40 60 soybean oil 20 20 20 Rheometer value * 10 ℃ 1040 1100 1860 15 ℃ 510 530 800 20 ℃ 190 220 385 * Fudo Kogyo Co., Ltd., unit: g / 0.785cm 2

【0014】表1に示すごとく、対照の魚油硬化油を用
いたショートニングは、定温でも柔らかく広い可塑性範
囲を持っており、実施例1では魚油硬化油の50%をエ
ステル交換油、すなわち、本願発明における可塑性油脂
組成物製造用油脂に置換してもその特長は阻害されてい
ない。これに対し、比較例1の大豆硬化油による置換で
は、魚油硬化油の僅か25重量%を置き換えただけで大
きく硬さが変化し、ショートニングにおける魚油硬化油
の特長を阻害する。以下の表2に、ショートニングのホ
イップによるオーバーランの上昇速度を示す。数字は1
20rpmで攪拌したときの各ショートニングのオーバラ
ン(%、v/v)の経時変化を示したものである。
As shown in Table 1, the shortening using the control fish oil hydrogenated oil has a wide plasticity range that is soft even at a constant temperature. In Example 1, 50% of the fish oil hydrogenated oil was transesterified oil, that is, the present invention. Even if it is replaced with the oil / fat for producing the plastic oil / fat composition in 1), its characteristics are not impaired. On the other hand, when the soybean hydrogenated oil of Comparative Example 1 is substituted, the hardness changes greatly even if only 25% by weight of the fish oil hydrogenated oil is replaced, and the characteristics of the fish oil hydrogenated oil in shortening are impaired. Table 2 below shows the rate of overrun rise due to the shortening whip. The number is 1
It shows the change with time of overrun (%, v / v) of each shortening when stirred at 20 rpm.

【0015】[0015]

【表2】 オーバーラン(%) 5分 10分 15分 20分 25分 30分 対 照 81 137 182 227 245 265 実施例1 94 158 214 251 271 270 比較例1 44 91 140 181 213 241 [Table 2] Overrun (%) 5 minutes 10 minutes 15 minutes 20 minutes 25 minutes 30 minutes Reference 81 137 182 227 245 265 Example 1 94 158 214 251 271 270 Comparative Example 1 44 91 140 181 213 241

【0016】表2の結果においても魚油硬化油を用いた
対照のショートニングは、良好なホイップ性を示してい
るが、実施例1のエステル交換油、すなわち、本願発明
における可塑性油脂組成物製造用油脂の置換配合により
さらに改善され、極めて良好な物性を呈している。これ
に対し、比較例1の大豆硬化油による置換配合では、上
のレオメーター測定値による可塑性範囲の結果と同様に
魚油硬化油の物性を著しく阻害する。
In the results of Table 2, the shortening of the control using the hydrogenated fish oil also shows good whipping property, but the transesterified oil of Example 1, that is, the fat for producing the plastic fat composition according to the present invention. It was further improved by the substituting compound of (1) and exhibited extremely good physical properties. On the other hand, the substitution and blending with the soybean hydrogenated oil of Comparative Example 1 markedly impairs the physical properties of the fish oil hydrogenated oil, similar to the result of the plasticity range measured by the rheometer.

【0017】実施例2および比較例2〜4 表3に示す配合によりエステル交換油を調製し、実施例
1と同様に魚油硬化油(融点36℃)の50%を置換し
た配合にてショートニングの物性を検討した。これらエ
ステル交換油の融点、SFCは実施例1と同様に魚油硬
化油(融点36℃)に近似させて製造した。
Example 2 and Comparative Examples 2 to 4 Transesterified oils were prepared according to the formulations shown in Table 3 and, as in Example 1, 50% of hydrogenated hydrogenated fish oil (melting point 36 ° C.) was replaced to achieve shortening. The physical properties were examined. The melting points and SFCs of these transesterified oils were produced by approximating to hydrogenated fish oil (melting point 36 ° C.) as in Example 1.

【0018】[0018]

【表3】 エステル交換油配合 実施例2 比較例2 比較例3 比較例4 パームステアリン 50% − 40% 50% パーム油 − 60% − − パーム核油 40 40 − 10 硬化ヤシ油 − − 50 20 大豆油 10 − 10 20 パルミチン酸含量 33% 35% 29% 34% ラウリン酸含量 17% 17% 24% 14% 多価不飽和酸含量 10% 6% 9% 16% [Table 3] Transesterified oil blending Example 2 Comparative example 2 Comparative example 3 Comparative example 4 Palm stearin 50% -40% 50% Palm oil-60% -Palm kernel oil 40 40-10 Hardened palm oil-50 50 Soybean oil 10-10 20 Palmitic acid content 33% 35% 29% 34% Lauric acid content 17% 17% 24% 14% Polyunsaturated acid content 10% 6% 9% 16%

【0019】これらのショートニングの各温度における
硬さのレオメーターによる測定値を表4に示す。
Table 4 shows the values measured by a rheometer of the hardness of these shortenings at each temperature.

【表4】 レオメータ測定値* 10℃ 15℃ 20℃ 実施例2 1100 530 220 比較例2 1550 570 360 比較例3 1760 930 400 比較例4 920 410 105 *不動工業(株)製、単位:g/0.785cm2 [Table 4] Rheometer measurement value * 10 ° C 15 ° C 20 ° C Example 2 1100 530 220 Comparative Example 2 1550 570 360 Comparative Example 3 1760 930 400 Comparative Example 4 920 410 105 * Fudo Kogyo Co., Ltd., Unit: g / 0.785 cm 2

【0020】表3および4に示すごとく、多価不飽和脂
肪酸の影響は、比較例2、3および4の結果から判るよ
うに、10%未満ではショートニングの硬さが硬くな
り、逆に15%を超えると柔らかくなり耐熱性が劣る傾
向を示す。これらのショートニングの各温度におけるホ
イップ時のオーバーラン(%) 上昇速度を表5に示す。
As shown in Tables 3 and 4, the effect of polyunsaturated fatty acids is, as can be seen from the results of Comparative Examples 2, 3 and 4, when the content is less than 10%, the hardness of shortening becomes hard, and conversely 15%. If it exceeds, softening occurs and heat resistance tends to deteriorate. Table 5 shows the rate of overrun (%) rise during whipping at each temperature of these shortenings.

【0021】[0021]

【表5】 オーバーラン(%) 5分 10分 15分 20分 25分 30分 実施例2 94 158 214 251 271 273 比較例2 65 97 155 203 216 236 比較例3 89 151 210 249 268 270 比較例4 88 140 178 231 247 263 [Table 5] Overrun (%) 5 minutes 10 minutes 15 minutes 20 minutes 25 minutes 30 minutes Example 2 94 158 214 251 271 273 Comparative Example 2 65 97 155 203 216 236 Comparative Example 3 89 151 210 249 268 270 Comparative Example 4 88 140 178 231 247 263

【0022】表5から明らかなごとく、ホイップ性にお
いても、多価不飽和脂肪酸残基の含量が低い場合(比較
例2および3)はオーバーラン(%)の上昇速度が遅く
なる傾向を示す。また、ラウリン酸残基の含量は、比較
例3から判るように、余り多すぎるとホイップ性は良好
であるが、ショートニング自体が非常に硬くなる。
As is apparent from Table 5, even in the whipping property, when the content of the polyunsaturated fatty acid residue is low (Comparative Examples 2 and 3), the increasing rate of overrun (%) tends to be slow. Further, as can be seen from Comparative Example 3, the content of the lauric acid residue is too large, the whipping property is good, but the shortening itself becomes very hard.

【0023】実施例3〜5および比較例5および6 表6に示す配合にてエステル交換油を製造した。これら
のエステル交換油は硬化魚油(融点28℃)に、融点、
SFCを近似するように設定したものである。
Examples 3 to 5 and Comparative Examples 5 and 6 Transesterified oils were produced according to the formulations shown in Table 6. These transesterified oils are hydrogenated fish oil (melting point 28 ° C), melting point,
The SFC is set so as to approximate it.

【0024】[0024]

【表6】 エステル交換油配合 エステル交換油 No. パームオレイン 55% − 60% パーム油 − 50% − ヤシ油 35 − − パーム核油オレイン − 40 40 大豆油 10 10 − パルミチン酸含量 26% 26% 27% ラウリン酸含量 17 17 17 多価不飽和酸含量 12 13 8 エステル交換法 金属触媒 酵素触媒 金属触媒 [Table 6] Transesterified oil containing transesterified oil No. Palm olein 55% -60% Palm oil-50% -Palm oil 35- Palm oil olein-40 40 Soybean oil 10 10- Palmitic acid content 26% 26% 27% Lauric acid content 17 17 17 Polyunsaturated acid content 12 13 8 Transesterification method Metal catalysts Enzyme catalysts Metal catalysts

【0025】表6の配合によって製造したエステル交換
油と、融点28℃の魚油硬化油を用いて、表7の配合に
より、実施例1と同様にしてショートニングを製造し、
物性を比較した。
Using the transesterified oil produced by the formulation of Table 6 and hydrogenated fish oil having a melting point of 28 ° C., the shortening was produced in the same manner as in Example 1 by the formulation of Table 7.
The physical properties were compared.

【0026】[0026]

【表7】 ショートニング油脂配合 実施例3 実施例4 実施例5 比較例5 比較例6 エステル交換油 50 80 − − − エステル交換油 − − 50 − − エステル交換油 − − − − 50魚油硬化油 50 20 50 100 50 [Table 7] Shortening fat blending Example 3 Example 4 Example 5 Comparative Example 5 Comparative Example 6 Transesterified oil 50 80 --- Transesterified oil --50 --- Transesterified oil --- 50 Fish oil hydrogenated oil 50 20 50 100 50

【0027】これらのショートニングの各温度における
硬さのレオメーターによる測定値を表8に示す。
Table 8 shows the values of hardness of these shortenings measured by a rheometer at various temperatures.

【表8】 レオメーター測定値* 10℃ 15℃ 20℃ 実施例3 500 190 56 実施例4 560 210 61 実施例5 550 200 60 比較例5 500 190 56 比較例6 1000 370 125 *不動工業(株)製、単位:g/0.785cm2 [Table 8] Rheometer measurement value * 10 ° C 15 ° C 20 ° C Example 3 500 190 56 Example 4 560 210 61 Example 5 550 200 60 Comparative Example 5 500 190 56 Comparative Example 6 1000 370 125 * Fudo Kogyo ), Unit: g / 0.785cm 2

【0029】表6〜8から明らかなごとく、実施例3、
4および5と比較例5の魚油硬化油(融点28℃)との
比較により、エステル交換油、すなわち、本発明におけ
る可塑性油脂組成物製造用油脂は、混合による稠度変化
が無く、また硬化魚油に対して80重量%置換してもその
物性を損なわない。また、融点域の異なる魚油硬化油に
対しても本発明における可塑性油脂組成物製造用油脂は
有効であることが窺われる。実施例5より、使用するエ
ステル交換法が酵素法であっても良好な品質が得られ
る。これに対し、比較例6に示す多価不飽和脂肪酸含量
が本発明範囲を逸脱したエステル交換油は、50%置換
しても魚油硬化油の稠度を著しく損なう。
As is clear from Tables 6-8, Example 3,
By comparing 4 and 5 with the hydrogenated fish oil of Comparative Example 5 (melting point 28 ° C.), the transesterified oil, that is, the fat or oil for producing the plastic fat or oil composition of the present invention, does not change in consistency due to mixing, and is hardened fish oil. On the other hand, the substitution of 80% by weight does not impair the physical properties. Further, it can be said that the oil / fat for producing a plastic oil / fat composition of the present invention is effective for hydrogenated fish oils having different melting points. From Example 5, good quality can be obtained even if the transesterification method used is the enzymatic method. On the other hand, the transesterified oil having a polyunsaturated fatty acid content deviating from the range of the present invention as shown in Comparative Example 6 markedly impairs the consistency of hydrogenated fish oil even if it is replaced by 50%.

【0030】表9に、これらのショートニングの各温度
におけるホイップによるオーバーランの上昇速度を示
す。
Table 9 shows the rising speed of overrun by whipping at each temperature of these shortenings.

【表9】 オーバーラン(%) 5分 10分 15分 20分 25分 30分 実施例3 85 155 198 236 257 260 実施例4 80 141 190 220 241 270 実施例5 86 157 203 238 259 259 比較例5 77 136 182 213 234 253 比較例6 70 125 169 201 226 236 [Table 9] Overrun (%) 5 minutes 10 minutes 15 minutes 20 minutes 25 minutes 30 minutes Example 3 85 155 198 236 257 260 Example 4 80 141 190 220 241 270 Example 5 86 157 203 238 259 259 Comparative Example 5 77 136 182 213 234 253 Comparative Example 6 70 125 169 201 226 236

【0031】表9に示すごとく、オーバーランの上昇速
度においても実施例3、4および5の本発明における可
塑性組成物製造用油脂配合のショートニングは、比較例
5の魚油硬化油(融点28℃)に比べ、良好なホイップ
性を示すが、比較例6に示す、多価不飽和酸含量が本発
明範囲を逸脱したエステル交換油は、魚油硬化油(融点
28℃)に比べ劣っていた。
As shown in Table 9, the shortening of the fats and oils for producing a plastic composition of the present invention in Examples 3, 4 and 5 was also conducted at the rising rate of overrun in the hardened fish oil of Comparative Example 5 (melting point 28 ° C.). However, the transesterified oil having a polyunsaturated acid content deviating from the range of the present invention shown in Comparative Example 6 was inferior to hydrogenated fish oil (melting point 28 ° C.).

【0032】[0032]

【発明の効果】本発明によるエステル交換油、すなわ
ち、可塑性油脂組成物製造用油脂は魚油硬化油と混合し
て使用する場合、魚油硬化油の稠度を損なわず、良好な
ホイップ性を持ち、魚油硬化油との混合使用において良
好な品質を示す。
EFFECTS OF THE INVENTION The transesterified oil according to the present invention, that is, the fat for producing a plastic oil / fat composition, when used in combination with hydrogenated fish oil, has good whipping property without impairing the consistency of hydrogenated fish oil, and fish oil. It shows good quality when mixed with hardened oil.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 10〜15重量%の液体油を含み、かつ
パーム油起源の油脂およびラウリン系油脂を含む配合油
をエステル交換してなる可塑性油脂組成物製造用油脂。
1. An oil and fat for producing a plastic oil and fat composition, which comprises 10 to 15% by weight of a liquid oil and is transesterified with a compounded oil containing an oil and fat derived from palm oil and a lauric oil and fat.
【請求項2】 配合油におけるパーム油起源の油脂含量
が35〜60重量%、ラウリン系油脂含量が30〜50
重量%である、請求項1記載の可塑性油脂組成物製造用
油脂。
2. A blended oil having a palm oil-derived fat content of 35 to 60% by weight and a lauric fat content of 30 to 50.
The fat or oil for producing a plastic fat or oil composition according to claim 1, wherein the fat or oil is the weight percent.
【請求項3】 パルミチン酸残基が12〜40重量%、
ラウリン酸残基が10〜20重量%、多価不飽和脂肪酸
残基が10〜15重量%の脂肪酸組成を有する請求項1
または2記載の可塑性油脂組成物製造用油脂。
3. A palmitic acid residue is 12 to 40% by weight,
The fatty acid composition having a lauric acid residue content of 10 to 20% by weight and a polyunsaturated fatty acid residue content of 10 to 15% by weight.
Or the oil / fat for producing a plastic oil / fat composition according to 2.
【請求項4】 魚油硬化油20〜80重量%、液体油0
〜40重量%および請求項1〜3のいずれか1項記載の
可塑性油脂組成物製造用油脂80〜20重量%を含んで
なる可塑性油脂組成物。
4. Hardened fish oil 20 to 80% by weight, liquid oil 0
A plastic oil / fat composition comprising 40 to 40% by weight and 80 to 20% by weight of the oil / fat for producing a plastic oil / fat composition according to any one of claims 1 to 3.
JP7048203A 1995-03-08 1995-03-08 Oil and fat for producing plastic oil and fat composition and plastic oil and fat composition Pending JPH08242765A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7048203A JPH08242765A (en) 1995-03-08 1995-03-08 Oil and fat for producing plastic oil and fat composition and plastic oil and fat composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7048203A JPH08242765A (en) 1995-03-08 1995-03-08 Oil and fat for producing plastic oil and fat composition and plastic oil and fat composition

Publications (1)

Publication Number Publication Date
JPH08242765A true JPH08242765A (en) 1996-09-24

Family

ID=12796835

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7048203A Pending JPH08242765A (en) 1995-03-08 1995-03-08 Oil and fat for producing plastic oil and fat composition and plastic oil and fat composition

Country Status (1)

Country Link
JP (1) JPH08242765A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000024850A1 (en) * 1998-10-28 2000-05-04 Kaneka Corporation Fat compositions and process for producing the same
JP2001262181A (en) * 2000-03-23 2001-09-26 Kanegafuchi Chem Ind Co Ltd Plastic oil and fat composition
JP2005120386A (en) * 2004-12-06 2005-05-12 Kaneka Corp Oil and fat composition
KR100773195B1 (en) * 2006-08-10 2007-11-02 동서유지 주식회사 A composition of oil and fat and method for producing cbr having reduced trans fatty acid content thereof
WO2009008410A1 (en) * 2007-07-10 2009-01-15 The Nisshin Oillio Group, Ltd. Plastic fat composition
US10548334B2 (en) 2012-03-09 2020-02-04 Team Foods Colombia S.A. Cocoa butter substitute
CN114680186A (en) * 2020-12-29 2022-07-01 丰益(上海)生物技术研发中心有限公司 Oil composition with fine crystals

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000024850A1 (en) * 1998-10-28 2000-05-04 Kaneka Corporation Fat compositions and process for producing the same
JP2001262181A (en) * 2000-03-23 2001-09-26 Kanegafuchi Chem Ind Co Ltd Plastic oil and fat composition
JP2005120386A (en) * 2004-12-06 2005-05-12 Kaneka Corp Oil and fat composition
KR100773195B1 (en) * 2006-08-10 2007-11-02 동서유지 주식회사 A composition of oil and fat and method for producing cbr having reduced trans fatty acid content thereof
WO2009008410A1 (en) * 2007-07-10 2009-01-15 The Nisshin Oillio Group, Ltd. Plastic fat composition
US7927647B2 (en) 2007-07-10 2011-04-19 The Nisshin Oillio Group, Ltd. Plastic fat composition
US10548334B2 (en) 2012-03-09 2020-02-04 Team Foods Colombia S.A. Cocoa butter substitute
CN114680186A (en) * 2020-12-29 2022-07-01 丰益(上海)生物技术研发中心有限公司 Oil composition with fine crystals

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