JP3976112B2 - Method for producing diglyceride-containing oil / fat composition and oil / fat composition using the same - Google Patents
Method for producing diglyceride-containing oil / fat composition and oil / fat composition using the same Download PDFInfo
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- JP3976112B2 JP3976112B2 JP31074399A JP31074399A JP3976112B2 JP 3976112 B2 JP3976112 B2 JP 3976112B2 JP 31074399 A JP31074399 A JP 31074399A JP 31074399 A JP31074399 A JP 31074399A JP 3976112 B2 JP3976112 B2 JP 3976112B2
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- oil
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- diglyceride
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- 238000004519 manufacturing process Methods 0.000 title description 11
- 239000003921 oil Substances 0.000 claims description 43
- 235000019198 oils Nutrition 0.000 claims description 43
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- 238000002407 reforming Methods 0.000 claims description 4
- 239000003925 fat Substances 0.000 description 33
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- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 18
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- 238000005809 transesterification reaction Methods 0.000 description 4
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- IIZPXYDJLKNOIY-JXPKJXOSSA-N 1-palmitoyl-2-arachidonoyl-sn-glycero-3-phosphocholine Chemical compound CCCCCCCCCCCCCCCC(=O)OC[C@H](COP([O-])(=O)OCC[N+](C)(C)C)OC(=O)CCC\C=C/C\C=C/C\C=C/C\C=C/CCCCC IIZPXYDJLKNOIY-JXPKJXOSSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
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- RZRNAYUHWVFMIP-HXUWFJFHSA-N glycerol monolinoleate Natural products CCCCCCCCC=CCCCCCCCC(=O)OC[C@H](O)CO RZRNAYUHWVFMIP-HXUWFJFHSA-N 0.000 description 2
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- FCCDDURTIIUXBY-UHFFFAOYSA-N lipoamide Chemical compound NC(=O)CCCCC1CCSS1 FCCDDURTIIUXBY-UHFFFAOYSA-N 0.000 description 2
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- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 244000299461 Theobroma cacao Species 0.000 description 1
- FZWLAAWBMGSTSO-UHFFFAOYSA-N Thiazole Chemical group C1=CSC=N1 FZWLAAWBMGSTSO-UHFFFAOYSA-N 0.000 description 1
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Landscapes
- Fats And Perfumes (AREA)
Description
【0001】
【発明の属する技術分野】
本発明は、油脂とモノグリセライドをエステル交換することにより、短時間且つ簡便にジグリセライド含有油脂を製造する方法に関するものであり、またこの製造方法を利用したパーム油の改質に関するものである。
【0002】
【従来の技術】
天然油脂の主成分はトリグリセライドであるが、その他副成分として、ジグリセライド、モノグリセライド、遊離脂肪酸やリン脂質等の複合脂質等が含まれている。この中でジグリセライドは、産業上、基剤として化粧品、医薬品等の分野で利用されており、食品分野においても油脂の物性改良剤として利用されている。
【0003】
これらジグリセライドは、油脂から分別して得ることもできるが、アルカリ触媒を用いた化学的反応や、リパーゼ等の酵素を用いた生化学的反応を利用して製造することもできる。化学的反応を利用した製造法では、動植物油脂または所定の脂肪酸とグリセリンとを原料として、水酸化ナトリウム等の触媒を用いて、200℃以上の高温で反応させる方法が一般的である。一方、生化学的反応を利用した製造方法では、リパーゼを触媒として油脂を加水分解する方法や、所定の脂肪酸とグリセリンとをエステル合成させる方法(特開昭64−71495、特開平4−330289)等がある。更には、化学的反応と生化学的反応を組み合わせた方法(特開平10−234392)も提案されている。
【0004】
一方、安価で供給されるパーム油はその利用が増大しているが、パーム油特有の結晶性の問題から十分に有効利用されているとは言い難い。パーム油を改質する手段としては、分別、硬化、エステル交換などの方法が挙げられる。中でも化学的エステル交換反応を利用したランダム化により、結晶性に深く関わっている対称型のトリグリセライドを再配列化するため、パーム油の結晶性を改善することが出来る。また、他の油脂との混合系でのランダム化反応によって可塑性油脂として有用な機能を付与する提案もなされている(特開昭53−208号、同57−74041号、同57−12950号)。
【0005】
【発明が解決しようとする課題】
しかしながら上記の化学的反応を用いたジグリセライドの製造方法においては、いずれもグリセリンを原料とするために、グリセリンと油脂、あるいは脂肪酸との相互溶解性が低いことが大きな問題点であり、一般的に、200℃以上という高温での反応が必要である。そのためコスト高となり経済的な点で好ましくなく、また高温の反応による重合物の生成等の副反応の危険性があるという問題点がある。
【0006】
また、生化学的反応による製造方法では反応温度は低いものの、例えば油脂を加水分解する方法では、反応が進むにつれジグリセライドよりもモノグリセライドが多く生成し、目的とするジグリセライドの収率を高めることは困難であり、同時に相当量の脂肪酸が生成するという問題点があった。またエステル合成反応を利用した場合は、前述のごとくグリセリンと脂肪酸等の相互溶解性の低さからくる不均一反応のために、反応時間が長く効率性が悪いという問題がある。使用する酵素量を増やせば反応時間を短縮することは可能であるが、一般的に酵素は高価であり現実的な方策とは言えない。さらに、収率を高めるためには、反応中に脱水処理を必要とするなどプロセスも煩雑である。また、両者の利点を組み合わした提案もなされてはいるが、根本的な解決には至っていないのが実情である。
このような現状から、短時間、且つ簡便にジグリセライド含有量を高めた油脂組成物を製造する新たな方法が望まれていた。
【0007】
一方、パーム油の改質方法においても、前述した改質方法では、可塑性油脂としての機能は改善されるものの、ランダム化反応で副生成した3飽和トリグリセライドに起因する口溶け性の悪化や結晶の粗大化が避けられず、実用上充分とは言い難いのが現状であり、これら欠点を克服したパーム油の改質方法が望まれていた。
【0008】
【課題を解決するための手段】
本発明者らは、上記のジグリセライド製造に関する問題を解決すべく鋭意研究した結果、油脂(トリグリセライド)と相互溶解性に優れたモノグリセライドとをエステル交換反応することによって、極めて短時間で且つ簡便にジグリセライド含有油脂を得ることが出来ることを見出し、さらにはこの方法をパーム油の改質に応用することで優れた品質の改質パーム油組成物が得られることを見いだし、本発明を完成させた。
【0009】
即ち、本発明の第1は、モノグリセライドと油脂をエステル交換することを特徴とするジグリセライド含有油脂の製造方法に関するものである。
【0011】
発明の第3はモノグリセライドとパーム油をエステル交換することを特徴とするパーム油の改質に関するものである。
【0013】
【発明の実施の形態】
本発明に用いる油脂は、一般にトリグリセライドを主体とするものであるが、当然のことながらモノグリセライド、ジグリセライド等の副成分を含有しても良い。用いる油脂の種類は、特に限定されないが、具体的には、コーン油、ナタネ油、大豆油、オリーブ油、紅花油、綿実油、ヒマワリ油、米糠油、パーム油、パーム核油等の植物油、ハイエルシンナタネ油等の十字化油、魚油、牛脂、豚脂、乳脂、卵黄油等の動物油等の天然油脂の他、それらのエステル交換油、硬化油、分別油等の加工油脂等が挙げられ、これらを単独或いは2種類以上混合して用いることが出来る。この中で、パーム油或いはその分別油を原料とした場合は、パーム油由来の結晶性を著しく改善することを目的とする事もできる。
【0014】
また、本発明に用いるモノグリセライドは、副成分としてトリグリセライド、ジグリセライド等を含有しても良く、その構成脂肪酸についても特に制限はない。後述するように、得られる油脂組成物の物性に応じて選択することも出来るが、食用乳化剤として市販されている安価な反応モノグリセライドや蒸留モノグリセライド等を用いてもかまわない。
【0015】
本発明のエステル交換反応は、通常のナトリウムメチラート等のアルカリ金属系触媒を用いる化学的反応、リパーゼ等の酵素的を用いる生物学的反応、のどちらの反応でも利用することが出来、何れの場合もモノグリセライドとトリグリセライドの相互溶解性が高いことから、極めて短時間で反応を完了することが可能である。
【0016】
本発明における反応の原料となる油脂とモノグリセライドの比は特に限定されないが、使用するモノグリセライドの量比を調整することで、反応後のジグリセライド含有量を制御する事が可能である。例えば出発原料中のモノグリセライド含有量が5重量%である場合、反応後のジグリセライド含有量は、約15重量%となる。一般に使用するモノグリセライドの量が多くなれば、反応後のジグリセライドの収率は高くなるが、モノグリセライドの量が多すぎると反応後に残存するモノグリセライドの量も多くなる。これらの観点から、使用するモノグリセライドの量は50重量%以下が好ましく、さらに好ましくは5〜40重量%である。
【0017】
反応終了後、残存する脂肪酸やモノグリセライドは、減圧スチーミング、分子蒸留器或いはクロマトグラフィー等の一般的な方法を用いて除去することが出来るが、用途に応じてモノグリセライドは含有させたままでも良い。また除去したモノグリセライドは、原料として再利用することも可能である。
【0018】
本発明で得られるジグリセライド含有油脂組成物では、その組成を調整することにより、油脂加工食品に要求される個々の物性、例えば稠度や融点等を調整することが可能である。この様な組成の調整には、反応時の原料の選定が重要であるが、さらには反応後に硬化、分別処理等といった通常の油脂加工技術を組み合わせることも出来る。
【0019】
硬化処理を行う場合は、用途に応じて非選択的水添でも選択的異性化水添であっても良く、例えば、選択的異性化水添においては、硫黄で被毒したニッケル触媒を用いる方法やメチオニン等の含硫アミノ酸、チアゾール環含有化合物、メタ重亜硫酸ソーダ又はカリウム等の硫黄化合物を添加する方法が例示されるが、これらに限定されない。
【0020】
分別処理を行う場合は、無溶剤分別法、n−ヘキサン又はアセトン等の有機溶剤を用いる方法、又は界面活性剤水溶液を用いる方法の何れの方法でも良く、またこれらに限定されない。
【0021】
本発明のジグリセライド含有油脂組成物は単独で使用することもできるが、必要に応じて他の油脂と混合して用いることも出来る。混合のために用いられる油脂は特に限定されず、コーン油、ナタネ油、大豆油、オリーブ油、紅花油、綿実油、ヒマワリ油、米糠油、パーム油、パーム核油等の植物油、ハイエルシンナタネ油等の十字化油、魚油、牛脂、豚脂、乳脂、卵黄油等の動物油等の天然の油脂、またはこれらを原料として分別、水添、エステル交換等を行った加工油脂、或いはこれらの混合油が使用できる。
【0022】
本発明で得られる油脂組成物、或いは改質パーム油組成物は、油脂を含有する食品一般に使用することが出来、具体的には、マーガリン、ショートニング、チョコレート類、フライ油、バタークリーム等の他に、水中油型乳化物としてはホイップクリーム、アイスクリーム、フラワーペースト、マヨネーズ等が例示される。
【0023】
【実施例】
以下に実施例を挙げて本発明を詳細に説明するが、これらの実施例は本発明を何ら制限するものではない。尚、以下の記載において「部」、「%」は全て「重量部」、「重量%」を意味する。
【0024】
(実施例1)
ハイオレイックサフラワー60部、モノオレイン40部を用い、常法に従いナトリウムメチラートを触媒として80℃で30分反応した。反応後の組成は、遊離脂肪酸1.2%、モノグリセライド23.0%、ジグリセライド52.1%、トリグリセライド23.6%であった。
【0025】
次いで、水蒸気蒸留を行い遊離脂肪酸及びモノグリセライドを除去した。得られたジグリセライド含有油脂組成物の組成は、モノグリセライド0.2%、ジグリセライド68.6%、トリグリセライド31.2%であった。
【0026】
(比較例1)
ハイオレイックサフラワー80部、グリセリン20部を用い、水酸化ナトリウムを触媒として減圧下80℃で1時間反応したが、反応はほとんど進行しなかった。
【0027】
(実施例2)
ハイオレイックサフラワー60部、モノオレイン40部、固定化リパーゼ(リポザイムIM、ノボノルディスク株式会社製)10部を用い、モレキュラーシーブスの存在下40℃で反応させたところ、約2時間で反応組成物中のジグリセライド含有量が50%となった。
【0028】
(比較例2)
オレイン酸85部、グリセリン15部、固定化リパーゼ(リポザイムIM、ノボノルディスク株式会社製)10部を用い、モレキュラーシーブスの存在下40℃で反応させたところ、反応組成物中のジグリセライド含有量が50%となるのに約5時間もの時間を要した。
【0029】
(実施例3)
パーム油45部、パーム軟質油(IV=62)45部、グリセリンモノ脂肪酸エステル(商品名:エマルジーMS、理研ビタミン株式会社製)10部を用い、常法に従いナトリウムメチラートを触媒として80℃で30分反応した。次いで水蒸気蒸留を行い遊離脂肪酸及びモノグリセライドを除去した。得られた改質パーム油組成物中のジグリセライド含量は28.7%であった。
【0030】
(比較例2)
実施例3のグリセリンモノ脂肪酸エステルの替わりに極度硬化菜種油10部を用いた以外は、実施例1記載と同様の操作を行った。得られた油脂組成物中のジグリセリド含有量は4.2%であった。
【0031】
(実施例4)
<油相の調整>
実施例3で得られた改質パーム油組成物70部と、菜種油30部、レシチン0.5部を60℃に加熱溶解した。
【0032】
<マーガリンの作成>
調整された油相部83.5%に撹拌しながら水16.5%を添加し、20分間乳化を行った後、ミニコンビネーターで冷却捏和してマーガリンを作成した。このマーガリンの乳化状態及びキメ、ツヤ、ノビ等の組織状態は非常に良好であった。
【0033】
(比較例4)
<油相の調整>
比較例2で得られた油脂70部と菜種油30部、レシチン0.5部を60℃に加熱溶解した。
【0034】
<マーガリンの作成>
調整された油相部83.5%に撹拌しながら水16.5%を添加し、20分間乳化を行った後、ミニコンビネーターで冷却捏和してマーガリンを作成した。このマーガリンの乳化状態は良好であったが、実施例4で得られたマーガリンに比べてキメ、ツヤ、ノビ等の組織状態は大きく劣っていた。
【0035】
【発明の効果】
以上述べたように、本発明の方法によれば、短時間で且つ簡便に高純度のジグリセライド含有油脂組成物を得ることが出来る。更には、パーム油を原料とすることにより得られる改質パーム油組成物は、結晶性が著しく改善され、これらを用いてなる油脂製品全般の製造上極めて有用である。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for producing a diglyceride-containing fat and oil in a short time and simply by transesterifying the fat and monoglyceride, and also relates to the modification of palm oil using this production method.
[0002]
[Prior art]
The main component of natural fats and oils is triglyceride, but diglycerides, monoglycerides, complex lipids such as free fatty acids and phospholipids, etc. are included as other accessory components. Among them, diglyceride is industrially used as a base in the fields of cosmetics, pharmaceuticals and the like, and is also used as a physical property improving agent for fats and oils in the food field.
[0003]
These diglycerides can be obtained by separation from fats and oils, but can also be produced by using a chemical reaction using an alkali catalyst or a biochemical reaction using an enzyme such as lipase. In the production method using a chemical reaction, a method of reacting animal and vegetable oils or fats or a predetermined fatty acid and glycerin as raw materials at a high temperature of 200 ° C. or higher using a catalyst such as sodium hydroxide is common. On the other hand, in the production method utilizing biochemical reaction, a method of hydrolyzing fats and oils using lipase as a catalyst, or a method of ester synthesis of a predetermined fatty acid and glycerin (JP-A 64-71495, JP-A-4-330289) Etc. Furthermore, a method combining a chemical reaction and a biochemical reaction (Japanese Patent Laid-Open No. 10-234392) has also been proposed.
[0004]
On the other hand, the use of palm oil supplied at low cost is increasing, but it cannot be said that it is sufficiently effectively used due to the crystallinity problem specific to palm oil. Examples of means for modifying palm oil include methods such as fractionation, curing, and transesterification. Above all, by re-arranging symmetrical triglycerides deeply related to crystallinity by randomization using chemical transesterification, the crystallinity of palm oil can be improved. In addition, proposals have been made to impart useful functions as plastic fats and oils by a randomization reaction in a mixed system with other fats and oils (Japanese Patent Laid-Open Nos. 53-208, 57-74041, and 57-12950). .
[0005]
[Problems to be solved by the invention]
However, in the production method of diglyceride using the above chemical reaction, since glycerin is used as a raw material, it is a big problem that the mutual solubility between glycerin and fat or fatty acid is low. The reaction at a high temperature of 200 ° C. or higher is necessary. Therefore, there is a problem that the cost is high, which is not preferable from an economical point of view, and there is a risk of side reactions such as formation of a polymer by a high temperature reaction.
[0006]
In addition, although the reaction temperature is low in the production method by biochemical reaction, for example, in the method of hydrolyzing fats and oils, as the reaction proceeds, more monoglyceride is produced than diglyceride, and it is difficult to increase the yield of the desired diglyceride. At the same time, a considerable amount of fatty acid is generated. Further, when the ester synthesis reaction is used, there is a problem that the reaction time is long and the efficiency is low due to the heterogeneous reaction resulting from the low mutual solubility of glycerin and fatty acid as described above. Although it is possible to shorten the reaction time by increasing the amount of enzyme used, the enzyme is generally expensive and cannot be said to be a practical measure. Furthermore, in order to increase the yield, the process is complicated such as requiring dehydration during the reaction. In addition, although a proposal that combines the advantages of both has been made, the reality is that it has not yet reached a fundamental solution.
From such a current situation, a new method for producing an oil and fat composition having a high diglyceride content in a short time and simply has been desired.
[0007]
On the other hand, in the reforming method of palm oil, the above-described reforming method improves the function as a plastic fat, but deteriorates the solubility in the mouth due to the trisaturated triglyceride produced as a by-product in the randomization reaction and the coarseness of crystals. However, it is difficult to say that it is practically sufficient, and a palm oil reforming method that overcomes these drawbacks has been desired.
[0008]
[Means for Solving the Problems]
As a result of diligent research to solve the above-mentioned problems relating to the production of diglyceride, the present inventors conducted a transesterification reaction between fats and oils (triglyceride) and monoglyceride having excellent mutual solubility, so that diglyceride can be easily and extremely quickly. The present inventors have found that oils and fats can be obtained, and have found that a modified palm oil composition of excellent quality can be obtained by applying this method to the modification of palm oil, thereby completing the present invention.
[0009]
That is, the first of the present invention relates to a method for producing diglyceride-containing fats and oils characterized by transesterifying monoglyceride and fats and oils.
[0011]
The third aspect of the present invention relates to the modification of palm oil characterized by transesterifying monoglyceride and palm oil.
[0013]
DETAILED DESCRIPTION OF THE INVENTION
The fats and oils used in the present invention are mainly composed of triglycerides, but of course may contain subcomponents such as monoglycerides and diglycerides. The type of fats and oils to be used is not particularly limited. Specifically, corn oil, rapeseed oil, soybean oil, olive oil, safflower oil, cottonseed oil, sunflower oil, rice bran oil, palm oil, palm kernel oil and other vegetable oils, Hyelsin Cross oils such as rapeseed oil, natural fats and oils such as animal oil such as fish oil, beef tallow, pork fat, milk fat and egg yolk oil, as well as processed fats and oils such as transesterified oil, hardened oil and fractionated oil, etc. Can be used alone or in admixture of two or more. In this, when palm oil or its fractionated oil is used as a raw material, it can also aim at remarkably improving the crystallinity derived from palm oil.
[0014]
Moreover, the monoglyceride used for this invention may contain a triglyceride, a diglyceride, etc. as a subcomponent, and there is no restriction | limiting in particular also about the constituent fatty acid. As will be described later, it can be selected according to the physical properties of the obtained oil and fat composition, but inexpensive reaction monoglyceride, distilled monoglyceride and the like which are commercially available as edible emulsifiers may be used.
[0015]
The transesterification reaction of the present invention can be used in any of a chemical reaction using a normal alkali metal catalyst such as sodium methylate and a biological reaction using an enzyme such as lipase. In this case, since the mutual solubility of monoglyceride and triglyceride is high, the reaction can be completed in an extremely short time.
[0016]
Although the ratio of the fats and monoglycerides used as the raw material for the reaction in the present invention is not particularly limited, the diglyceride content after the reaction can be controlled by adjusting the ratio of the monoglyceride used. For example, when the monoglyceride content in the starting material is 5% by weight, the diglyceride content after the reaction is about 15% by weight. Generally, when the amount of monoglyceride used is increased, the yield of diglyceride after the reaction is increased. However, when the amount of monoglyceride is too large, the amount of monoglyceride remaining after the reaction is also increased. From these viewpoints, the amount of monoglyceride to be used is preferably 50% by weight or less, more preferably 5 to 40% by weight.
[0017]
After completion of the reaction, the remaining fatty acid and monoglyceride can be removed using a general method such as vacuum steaming, molecular distillation or chromatography, but the monoglyceride may remain contained depending on the application. The removed monoglyceride can be reused as a raw material.
[0018]
In the diglyceride-containing oil and fat composition obtained in the present invention, by adjusting the composition, it is possible to adjust individual physical properties required for the oil and fat processed food, such as consistency and melting point. For the adjustment of such a composition, selection of raw materials at the time of reaction is important, but furthermore, normal oil processing techniques such as hardening and fractionation after reaction can be combined.
[0019]
When performing the curing treatment, it may be non-selective hydrogenation or selective isomerization hydrogenation depending on the application. For example, in selective isomerization hydrogenation, a method using a nickel catalyst poisoned with sulfur. And sulfur-containing amino acids such as methionine, thiazole ring-containing compounds, sodium metabisulfite, and sulfur compounds such as potassium are exemplified, but the method is not limited thereto.
[0020]
When performing the fractionation treatment, any method of a solventless fractionation method, a method using an organic solvent such as n-hexane or acetone, or a method using an aqueous surfactant solution may be used, but the method is not limited thereto.
[0021]
The diglyceride-containing oil and fat composition of the present invention can be used alone, but can also be used by mixing with other oils and fats as necessary. Oils and fats used for mixing are not particularly limited, vegetable oils such as corn oil, rapeseed oil, soybean oil, olive oil, safflower oil, cottonseed oil, sunflower oil, rice bran oil, palm oil, palm kernel oil, Hyelcin rapeseed oil, etc. Crude oil, fish oil, beef tallow, pork tallow, milk fat, animal oil such as egg yolk oil, etc., or processed oils and fats that have been separated, hydrogenated, transesterified etc. Can be used.
[0022]
The oil or fat composition or modified palm oil composition obtained in the present invention can be used in general for foods containing oil and fat, specifically, margarine, shortening, chocolates, frying oil, butter cream, etc. In addition, examples of the oil-in-water emulsion include whipped cream, ice cream, flower paste, mayonnaise and the like.
[0023]
【Example】
EXAMPLES The present invention will be described in detail below with reference to examples, but these examples do not limit the present invention in any way. In the following description, “parts” and “%” all mean “parts by weight” and “% by weight”.
[0024]
Example 1
Using 60 parts of high oleic safflower and 40 parts of monoolein, the reaction was carried out at 80 ° C. for 30 minutes using sodium methylate as a catalyst according to a conventional method. The composition after the reaction was 1.2% free fatty acid, 23.0% monoglyceride, 52.1% diglyceride, and 23.6% triglyceride.
[0025]
Subsequently, steam distillation was performed to remove free fatty acids and monoglycerides. The composition of the obtained diglyceride-containing oil and fat composition was 0.2% monoglyceride, 68.6% diglyceride, and 31.2% triglyceride.
[0026]
(Comparative Example 1)
Although 80 parts of high oleic safflower and 20 parts of glycerin were used and reacted for 1 hour at 80 ° C. under reduced pressure using sodium hydroxide as a catalyst, the reaction hardly proceeded.
[0027]
(Example 2)
When reaction was performed at 40 ° C. in the presence of molecular sieves using 60 parts of high oleic safflower, 40 parts of monoolein and 10 parts of immobilized lipase (Lipozyme IM, manufactured by Novo Nordisk Co., Ltd.), the reaction took about 2 hours. The diglyceride content in the composition was 50%.
[0028]
(Comparative Example 2)
When 85 parts of oleic acid, 15 parts of glycerin, and 10 parts of immobilized lipase (Lipozyme IM, manufactured by Novo Nordisk Co., Ltd.) were reacted at 40 ° C. in the presence of molecular sieves, the diglyceride content in the reaction composition was It took about 5 hours to reach 50%.
[0029]
(Example 3)
45 parts of palm oil, 45 parts of palm soft oil (IV = 62), 10 parts of glycerin monofatty acid ester (trade name: Emergy MS, manufactured by Riken Vitamin Co., Ltd.), and at 80 ° C. using sodium methylate as a catalyst according to a conventional method Reacted for 30 minutes. Subsequently, steam distillation was performed to remove free fatty acids and monoglycerides. The diglyceride content in the obtained modified palm oil composition was 28.7%.
[0030]
(Comparative Example 2)
The same operation as described in Example 1 was performed except that 10 parts of extremely hardened rapeseed oil was used in place of the glycerin monofatty acid ester of Example 3. The diglyceride content in the obtained oil and fat composition was 4.2%.
[0031]
Example 4
<Oil phase adjustment>
70 parts of the modified palm oil composition obtained in Example 3, 30 parts of rapeseed oil, and 0.5 parts of lecithin were dissolved by heating at 60 ° C.
[0032]
<Making Margarine>
While stirring, 16.5% of water was added to 83.5% of the adjusted oil phase part, emulsified for 20 minutes, and then cooled and kneaded with a mini-combinator to prepare margarine. The margarine emulsified state and the textured state of texture, gloss, nobi and the like were very good.
[0033]
(Comparative Example 4)
<Oil phase adjustment>
70 parts of fats and oils obtained in Comparative Example 2, 30 parts of rapeseed oil and 0.5 parts of lecithin were dissolved by heating at 60 ° C.
[0034]
<Making Margarine>
While stirring, 16.5% of water was added to 83.5% of the adjusted oil phase part, emulsified for 20 minutes, and then cooled and kneaded with a mini-combinator to prepare margarine. The emulsified state of margarine was good, but the textured state of texture, luster, nobi and the like was greatly inferior to the margarine obtained in Example 4.
[0035]
【The invention's effect】
As described above, according to the method of the present invention, a highly pure diglyceride-containing oil and fat composition can be obtained in a short time and simply. Furthermore, the modified palm oil composition obtained by using palm oil as a raw material has remarkably improved crystallinity, and is extremely useful in the production of fats and oils products using these.
Claims (2)
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| JP31074399A JP3976112B2 (en) | 1999-03-29 | 1999-11-01 | Method for producing diglyceride-containing oil / fat composition and oil / fat composition using the same |
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| JP11-85577 | 1999-03-29 | ||
| JP8557799 | 1999-03-29 | ||
| JP31074399A JP3976112B2 (en) | 1999-03-29 | 1999-11-01 | Method for producing diglyceride-containing oil / fat composition and oil / fat composition using the same |
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| JP3976112B2 true JP3976112B2 (en) | 2007-09-12 |
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| CN101270375B (en) * | 2008-05-22 | 2011-11-09 | 清华大学 | Technique for preparing 1,3-diglyceride with enzyme in tert-butanol system |
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| JP4524547B2 (en) * | 2003-07-16 | 2010-08-18 | 株式会社カネカ | Oil and fat composition manufacturing method and oil and fat composition using the same |
| WO2009144858A1 (en) | 2008-05-29 | 2009-12-03 | 花王株式会社 | Method for producing fat or oil containing large amount of diacylglycerol |
| JP5550282B2 (en) * | 2008-08-04 | 2014-07-16 | 花王株式会社 | Process for producing fats and oils with high diacylglycerol content |
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