JP3120906B2 - Method for producing triglyceride containing β-palmitic acid - Google Patents
Method for producing triglyceride containing β-palmitic acidInfo
- Publication number
- JP3120906B2 JP3120906B2 JP04248769A JP24876992A JP3120906B2 JP 3120906 B2 JP3120906 B2 JP 3120906B2 JP 04248769 A JP04248769 A JP 04248769A JP 24876992 A JP24876992 A JP 24876992A JP 3120906 B2 JP3120906 B2 JP 3120906B2
- Authority
- JP
- Japan
- Prior art keywords
- palmitic acid
- triglyceride
- oil
- acid
- fat
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- UFTFJSFQGQCHQW-UHFFFAOYSA-N triformin Chemical compound O=COCC(OC=O)COC=O UFTFJSFQGQCHQW-UHFFFAOYSA-N 0.000 title claims description 33
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- IPCSVZSSVZVIGE-UHFFFAOYSA-N hexadecanoic acid Chemical compound CCCCCCCCCCCCCCCC(O)=O IPCSVZSSVZVIGE-UHFFFAOYSA-N 0.000 claims description 64
- 239000003921 oil Substances 0.000 claims description 34
- 235000019198 oils Nutrition 0.000 claims description 34
- 235000021314 Palmitic acid Nutrition 0.000 claims description 32
- WQEPLUUGTLDZJY-UHFFFAOYSA-N n-Pentadecanoic acid Natural products CCCCCCCCCCCCCCC(O)=O WQEPLUUGTLDZJY-UHFFFAOYSA-N 0.000 claims description 32
- 108090001060 Lipase Proteins 0.000 claims description 16
- 102000004882 Lipase Human genes 0.000 claims description 16
- 239000004367 Lipase Substances 0.000 claims description 16
- 235000019421 lipase Nutrition 0.000 claims description 16
- 238000000034 method Methods 0.000 claims description 10
- 150000003626 triacylglycerols Chemical class 0.000 claims description 9
- 235000019482 Palm oil Nutrition 0.000 claims description 8
- 239000002540 palm oil Substances 0.000 claims description 8
- 239000003054 catalyst Substances 0.000 claims description 5
- 235000021122 unsaturated fatty acids Nutrition 0.000 claims description 5
- 150000004670 unsaturated fatty acids Chemical class 0.000 claims description 5
- 239000002253 acid Substances 0.000 claims description 3
- 230000032050 esterification Effects 0.000 claims 1
- 238000005886 esterification reaction Methods 0.000 claims 1
- 239000002184 metal Substances 0.000 claims 1
- 239000003925 fat Substances 0.000 description 36
- 235000019197 fats Nutrition 0.000 description 35
- 238000005809 transesterification reaction Methods 0.000 description 20
- 235000014113 dietary fatty acids Nutrition 0.000 description 16
- 239000000194 fatty acid Substances 0.000 description 16
- 229930195729 fatty acid Natural products 0.000 description 16
- 238000010521 absorption reaction Methods 0.000 description 14
- 150000004665 fatty acids Chemical group 0.000 description 14
- 238000006243 chemical reaction Methods 0.000 description 13
- WQDUMFSSJAZKTM-UHFFFAOYSA-N Sodium methoxide Chemical compound [Na+].[O-]C WQDUMFSSJAZKTM-UHFFFAOYSA-N 0.000 description 10
- 239000005642 Oleic acid Substances 0.000 description 9
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 description 8
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 description 8
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 description 8
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 description 8
- 235000013305 food Nutrition 0.000 description 8
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 description 8
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 8
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 description 8
- 125000005456 glyceride group Chemical group 0.000 description 7
- 239000000843 powder Substances 0.000 description 6
- 108090000790 Enzymes Proteins 0.000 description 5
- 102000004190 Enzymes Human genes 0.000 description 5
- 241000700159 Rattus Species 0.000 description 5
- 238000007796 conventional method Methods 0.000 description 5
- 235000013350 formula milk Nutrition 0.000 description 5
- 235000020256 human milk Nutrition 0.000 description 5
- 210000004251 human milk Anatomy 0.000 description 5
- 238000002844 melting Methods 0.000 description 5
- 230000008018 melting Effects 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- OYHQOLUKZRVURQ-HZJYTTRNSA-N Linoleic acid Chemical compound CCCCC\C=C/C\C=C/CCCCCCCC(O)=O OYHQOLUKZRVURQ-HZJYTTRNSA-N 0.000 description 4
- UKMSUNONTOPOIO-UHFFFAOYSA-N docosanoic acid Chemical group CCCCCCCCCCCCCCCCCCCCCC(O)=O UKMSUNONTOPOIO-UHFFFAOYSA-N 0.000 description 4
- 235000020778 linoleic acid Nutrition 0.000 description 4
- OYHQOLUKZRVURQ-IXWMQOLASA-N linoleic acid Natural products CCCCC\C=C/C\C=C\CCCCCCCC(O)=O OYHQOLUKZRVURQ-IXWMQOLASA-N 0.000 description 4
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 3
- 241000235395 Mucor Species 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 235000021355 Stearic acid Nutrition 0.000 description 3
- 230000029087 digestion Effects 0.000 description 3
- 230000002255 enzymatic effect Effects 0.000 description 3
- 239000000796 flavoring agent Substances 0.000 description 3
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 3
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000008117 stearic acid Substances 0.000 description 3
- 239000000758 substrate Substances 0.000 description 3
- 125000005457 triglyceride group Chemical group 0.000 description 3
- 235000015112 vegetable and seed oil Nutrition 0.000 description 3
- 239000008158 vegetable oil Substances 0.000 description 3
- 241000228212 Aspergillus Species 0.000 description 2
- 235000021357 Behenic acid Nutrition 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 241000235527 Rhizopus Species 0.000 description 2
- 229940116226 behenic acid Drugs 0.000 description 2
- 235000013361 beverage Nutrition 0.000 description 2
- 239000000872 buffer Substances 0.000 description 2
- 239000007853 buffer solution Substances 0.000 description 2
- HVYWMOMLDIMFJA-DPAQBDIFSA-N cholesterol Chemical compound C1C=C2C[C@@H](O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@H]([C@H](C)CCCC(C)C)[C@@]1(C)CC2 HVYWMOMLDIMFJA-DPAQBDIFSA-N 0.000 description 2
- 235000019621 digestibility Nutrition 0.000 description 2
- 239000008157 edible vegetable oil Substances 0.000 description 2
- 238000006911 enzymatic reaction Methods 0.000 description 2
- -1 fatty acid triglycerides Chemical class 0.000 description 2
- 235000021050 feed intake Nutrition 0.000 description 2
- 235000013336 milk Nutrition 0.000 description 2
- 239000008267 milk Substances 0.000 description 2
- 210000004080 milk Anatomy 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 238000002407 reforming Methods 0.000 description 2
- 235000019786 weight gain Nutrition 0.000 description 2
- TWJNQYPJQDRXPH-UHFFFAOYSA-N 2-cyanobenzohydrazide Chemical compound NNC(=O)C1=CC=CC=C1C#N TWJNQYPJQDRXPH-UHFFFAOYSA-N 0.000 description 1
- 235000019737 Animal fat Nutrition 0.000 description 1
- 241000228245 Aspergillus niger Species 0.000 description 1
- 229920002261 Corn starch Polymers 0.000 description 1
- 239000004470 DL Methionine Substances 0.000 description 1
- 241000282412 Homo Species 0.000 description 1
- NHTMVDHEPJAVLT-UHFFFAOYSA-N Isooctane Chemical compound CC(C)CC(C)(C)C NHTMVDHEPJAVLT-UHFFFAOYSA-N 0.000 description 1
- 108010048733 Lipozyme Proteins 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 235000021360 Myristic acid Nutrition 0.000 description 1
- TUNFSRHWOTWDNC-UHFFFAOYSA-N Myristic acid Natural products CCCCCCCCCCCCCC(O)=O TUNFSRHWOTWDNC-UHFFFAOYSA-N 0.000 description 1
- 241000235403 Rhizomucor miehei Species 0.000 description 1
- 241000303962 Rhizopus delemar Species 0.000 description 1
- 229930006000 Sucrose Natural products 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- 239000007983 Tris buffer Substances 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 125000002252 acyl group Chemical group 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 235000008452 baby food Nutrition 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 230000037396 body weight Effects 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 235000014121 butter Nutrition 0.000 description 1
- 239000005018 casein Substances 0.000 description 1
- BECPQYXYKAMYBN-UHFFFAOYSA-N casein, tech. Chemical compound NCCCCC(C(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(CC(C)C)N=C(O)C(CCC(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(C(C)O)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(COP(O)(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(N)CC1=CC=CC=C1 BECPQYXYKAMYBN-UHFFFAOYSA-N 0.000 description 1
- 235000021240 caseins Nutrition 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 229960004874 choline bitartrate Drugs 0.000 description 1
- QWJSAWXRUVVRLH-UHFFFAOYSA-M choline bitartrate Chemical compound C[N+](C)(C)CCO.OC(=O)C(O)C(O)C([O-])=O QWJSAWXRUVVRLH-UHFFFAOYSA-M 0.000 description 1
- 229940110456 cocoa butter Drugs 0.000 description 1
- 235000019868 cocoa butter Nutrition 0.000 description 1
- 239000003240 coconut oil Substances 0.000 description 1
- 235000019864 coconut oil Nutrition 0.000 description 1
- 238000004440 column chromatography Methods 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 239000008120 corn starch Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 235000005911 diet Nutrition 0.000 description 1
- 230000037213 diet Effects 0.000 description 1
- JVSWJIKNEAIKJW-UHFFFAOYSA-N dimethyl-hexane Natural products CCCCCC(C)C JVSWJIKNEAIKJW-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000029142 excretion Effects 0.000 description 1
- 239000010685 fatty oil Substances 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 230000003100 immobilizing effect Effects 0.000 description 1
- FCCDDURTIIUXBY-UHFFFAOYSA-N lipoamide Chemical compound NC(=O)CCCCC1CCSS1 FCCDDURTIIUXBY-UHFFFAOYSA-N 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000000622 liquid--liquid extraction Methods 0.000 description 1
- 210000004185 liver Anatomy 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- FFEARJCKVFRZRR-UHFFFAOYSA-N methionine Chemical compound CSCCC(N)C(O)=O FFEARJCKVFRZRR-UHFFFAOYSA-N 0.000 description 1
- 229930182817 methionine Natural products 0.000 description 1
- 235000006109 methionine Nutrition 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000001575 pathological effect Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 230000001766 physiological effect Effects 0.000 description 1
- 235000020777 polyunsaturated fatty acids Nutrition 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000002250 progressing effect Effects 0.000 description 1
- 239000011833 salt mixture Substances 0.000 description 1
- 150000004671 saturated fatty acids Chemical class 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000005720 sucrose Substances 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- LENZDBCJOHFCAS-UHFFFAOYSA-N tris Chemical compound OCC(N)(CO)CO LENZDBCJOHFCAS-UHFFFAOYSA-N 0.000 description 1
- 235000019871 vegetable fat Nutrition 0.000 description 1
- 229940088594 vitamin Drugs 0.000 description 1
- 229930003231 vitamin Natural products 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 150000003722 vitamin derivatives Chemical class 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 230000004584 weight gain Effects 0.000 description 1
Landscapes
- Dairy Products (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明はグリセリドのβ位(2
位)にパルミチン酸(以下、β−パルミチン酸という)
を約50%結合した油脂の製造方法に関する。さらに詳
しくは、本発明は、触媒を用いたランダムエステル交換
反応と酵素を用いたエステル交換反応とを組み合わせた
植物油脂、特にパーム油の改質方法に関する。The present invention relates to a glyceride at the β-position (2
) Palmitic acid (hereinafter referred to as β-palmitic acid)
And a method for producing an oil or fat in which about 50% is bound . More specifically, the present invention relates to a method for reforming vegetable oils and fats , particularly palm oil, by combining a random transesterification reaction using a catalyst with a transesterification reaction using an enzyme.
【0002】[0002]
【従来の技術】従来、ナトリウムメチラートや苛性ソー
ダを触媒として用いて油脂を化学的にエステル交換反応
を行なう方法が知られている。しかし、この方法による
とトリグリセリドに結合しているアシル基をα位(1,3
位)、β位(2位)を問わず交換する傾向がある(ラン
ダムエステル交換)。これに対し、酵素によるエステル
交換も知られているが、酵素反応は、トリグリセリドを
構成する脂肪酸の鎖長や、位置に特異性があり、この特
異性を利用した酵素によるエステル交換も盛んに開発さ
れている。例えば、トリグリセリドのα位(1位及び3
位)にパルミチン酸とステアリン酸、β位(2位)にオ
レイン酸が結合しているカカオ脂の代用油脂等への応用
が試みられている(例えば特開昭52−104506号公報及び
特開昭57-27259号公報)これらの反応に用いられる代表
的な酵素として、Aspergillus niger, Mucormiehei
やRhizopus delemar 由来のリパーゼなどを列挙されて
いる。2. Description of the Related Art Conventionally, there has been known a method of chemically transesterifying fats and oils using sodium methylate or caustic soda as a catalyst. However, according to this method, the acyl group bonded to the triglyceride is changed to the α-position (1,3
Position) and the β position (2 position) tend to be exchanged (random transesterification). In contrast, enzymatic transesterification is also known, but the enzymatic reaction has specificity in the chain length and position of the fatty acids that make up triglyceride, and enzymatic transesterification utilizing this specificity is also actively developed. Have been. For example, the α-position of triglyceride (positions 1 and 3
Of cocoa butter, in which palmitic acid and stearic acid are bonded at the (position) and oleic acid at the β-position (position 2), have been tried (for example, JP-A-52-104506 and JP-A-52-104506). As a representative enzyme used in these reactions, Aspergillus niger , Mucormiehei
And lipases derived from Rhizopus delemar .
【0003】一方、高度不飽和脂肪酸などのある特定脂
肪酸の生理効果に対する研究が進んでおり、トリグリセ
リドにおける脂肪酸の結合位置による効果も明らかにな
りつつある。例えば、ベヘン酸の結合位置と吸収率の関
係で、β位にベヘン酸が結合したトリグリセリドの方が
吸収率が低い(森 弘之、食品加工技術、11,25-28,199
1)ことや、β位にリノール酸が結合したトリグリセリ
ドは、α位に結合したものよりも血中および肝臓中コレ
ステロールレベルを低下させる(Yamamoto,Atherosclero
sis, 13, 171-184,1971)等の生理効果が明らかになって
いる。特に、β位にパルミチン酸が結合したトリグリセ
リドは、α位にパルミチン酸が結合したトリグリセリド
にくらべ、はるかに高い吸収性を示すことが FilerやTo
marelliによって明らかにされている〔J.Nutr. 99,293-
298,(1969) J.Nutr. 95, 583-590,(1968)〕。Filer ら
は、β−パルミチン酸含量の異なる脂肪を添加した人工
調製乳を11人の乳児に与えて脂肪および脂肪酸の吸収率
を調べている。脂肪は、ラード(パルミチン酸の85%が
β位に結合)もしくはエステル交換ラード(パルミチン
酸の33.9%がβ位)をそれぞれ3.63g/100ml,3.72g/
100ml 添加した。その結果、パルミチン酸の吸収率はラ
ードで94%、エステル交換ラードで58%とβ−パルミチ
ン酸の比率が高い方が圧倒的に吸収率がすぐれていた。
さらに、β−パルミチン酸はミセル形成能が高いため、
ラードで88%、エステル交換ラードで40%とステアリン
酸の吸収率も高めた。また、Tomarelli らは、人乳ある
いはラード、バター、ココナッツ油の混合油を用いて、
飼料中に15%脂肪として添加し、ラットに投与した。脂
肪の吸収率とβ位の脂肪酸の比率の相関性を調べた結
果、パルミチン酸で顕著な相関性があり、ミリスチン酸
とオレイン酸で弱い相関性が認められた。ステアリン酸
には相関性がなかった。このようにトリグリセリドのβ
位にパルミチン酸が存在すると高い吸収性を示す。さら
に、母乳中に多く含まれることから、乳児にとって特に
重要な脂肪であるといわれている。On the other hand, studies on the physiological effects of certain fatty acids such as polyunsaturated fatty acids have been progressing, and the effects of fatty acid binding positions in triglycerides are becoming clear. For example, in terms of the relationship between the binding position of behenic acid and the absorption rate, the absorption rate of triglyceride with behenic acid bound at the β-position is lower (Hiroyuki Mori, Food Processing Technology, 11,25-28,199
1) Triglycerides with linoleic acid bound to the β-position lower blood and liver cholesterol levels than those linked to the α-position (Yamamoto, Atherosclero)
sis, 13, 171-184, 1971). In particular, triglycerides with palmitic acid bound to the β-position show much higher absorption than triglycerides with palmitic acid bound to the α-position.
(J. Nutr. 99, 293-
298, (1969) J. Nutr. 95, 583-590, (1968)]. Filer et al. Studied the absorption of fat and fatty acids by feeding 11 infants with artificial formulas supplemented with fats having different β-palmitic acid contents. Fats are 3.63 g / 100 ml and 3.72 g / lard of lard (85% of palmitic acid binds to β-position) or transesterified lard (33.9% of palmitic acid to β-position).
100 ml was added. As a result, the absorptivity of palmitic acid was 94% for lard and 58% for transesterified lard, and the higher the ratio of β-palmitic acid was, the more excellent the absorptivity was.
Furthermore, because β-palmitic acid has a high micelle-forming ability,
The absorption rate of stearic acid was also increased by 88% for lard and 40% for transesterified lard. Tomarelli et al. Also used human milk or a mixture of lard, butter, and coconut oil,
They were added to the diet as 15% fat and administered to rats. As a result of examining the correlation between the rate of absorption of fat and the ratio of fatty acids at the β-position, there was a remarkable correlation with palmitic acid, and a weak correlation with myristic acid and oleic acid. Stearic acid had no correlation. Thus, the β of triglyceride
The presence of palmitic acid at the position shows high absorbency. Furthermore, it is said to be a particularly important fat for infants because of its high content in breast milk.
【0004】[0004]
【発明が解決しようとする課題】パルミチン酸は、パー
ム油などの植物油に多く存在し食品素材として利用され
ている。しかし、その結合位置はα位であることが多い
(油脂化学便覧、p.20、1982丸善)。β−パルミチン酸
を高度に含有している代表的な油脂として、動物性油脂
であるラードを挙げることができるが、ラードを食品に
利用する場合、この油脂の持つ“けもの臭”が発現す
る。また、これを高度に脱臭しても時間とともに“もど
り臭”が発生し、従来その利用に問題があった。SUMMARY OF THE INVENTION Palmitic acid is abundant in vegetable oils such as palm oil and used as a food material. However, the binding position is often at the α-position (Oil Chemistry Handbook, p.20, 1982 Maruzen). A typical fat and oil highly containing β-palmitic acid is lard which is an animal fat and oil. When lard is used in foods, the “fat odor” of the fat and oil is exhibited. . In addition, even if it is highly deodorized, "return odor" is generated with time, and there has been a problem in its use in the past.
【0005】本発明の目的は、このような“けもの臭”
や“もどり臭”のない、β−パルミチン酸を高度に含有
するトリグリセリドを製造することにある。このように
して得られたβ−パルミチン酸高度含有トリグリセリド
を飲食品、特に育児用粉乳に配合し、吸収性の高い油脂
が配合された飲食品を提供することができる。It is an object of the present invention to provide such a "kemono smell".
Another object of the present invention is to produce a triglyceride having a high content of β-palmitic acid, which is free from "return odor". The thus obtained β- palmitic highly containing triglyceride foods and beverages, in particular incorporated into infant milk powder, provides a food or beverage highly absorbent oil is blended.
【0006】[0006]
【課題を解決するための手段】本発明者らは上記課題を
解決するために、その原料の油脂及び合成法について種
々検討したところ、原料のパーム油またはその分別油の
脂肪酸トリグリセリド(油脂)を化学的にランダムエス
テル交換してβ位(2位)にパルミチン酸を導入した
後、α位(1,3位)に特異的に作用するリパーゼを用
いてα位に任意の不飽和脂肪酸を導入するとβ−パルミ
チン酸を高度に含有するトリグリセリドが得られること
を見出して本発明を完成するに至った。また、この製造
法において原料の油脂としてパルミチン酸を高度に結合
しているがβ位にその結合量の少ないパーム油及びその
分別油を使用して相互にランダムエステル交換すると収
率よく人乳の脂肪と同程度のβ−パルミチン酸含有トリ
グリセリドを製造することもできた。Means for Solving the Problems In order to solve the above-mentioned problems, the present inventors have conducted various studies on the raw material fats and oils and the synthesis method, and found that the fatty acid triglyceride of the palm oil or the fractionated oil of the raw material was used. after introducing palmitic acid (oil) chemically random transesterification to β-position (2-position), alpha-position (1,3-position) in the optionally-position alpha with lipase specifically acting not The present inventors have found that the introduction of a saturated fatty acid gives a triglyceride highly containing β-palmitic acid, thereby completing the present invention. In addition, in this production method, palmitic acid is highly bound as a raw material fat, but random transesterification between palm oil and its fractionated oil at the β-position with a small amount of the binding results in good yield of human milk. It could also be produced β- palmitic San含 Yes triglycerides comparable to fat.
【0007】すなわち、本発明は、パーム油またはその
分別油(脂肪酸トリグリセリド)を触媒を用いて化学的
にランダムエステル交換することによって該トリグリセ
リドのβ位のパルミチン酸含量を約50%前後に高め、
次いでこのグリセリドを任意の不飽和脂肪酸と、α位に
特異性の高いリパーゼを用いて酵素化学的にエステル交
換を行ってα位に任意の不飽和脂肪酸を導入することよ
りなるβ−パルミチン酸を高度に含有するトリグリセリ
ドの製造方法に関する。本発明の方法によると脂肪酸ト
リグリセリドの摂取時の油脂の吸収を向上することがで
きる。That is, the present invention relates to palm oil or
The fractional oil ( fatty acid triglyceride ) is chemically and randomly transesterified using a catalyst to increase the palmitic acid content at the β-position of the triglyceride to about 50% ,
Next, this glyceride is converted into β-palmitic acid by introducing an arbitrary unsaturated fatty acid into the α-position by enzymatically transesterifying the unsaturated glyceride with any unsaturated fatty acid using a lipase having a high specificity at the α-position. The present invention relates to a method for producing a highly-containing triglyceride. According to the method of the present invention, the absorption of fats and oils when fatty acid triglycerides are taken can be improved.
【0008】本発明のこのような改質方法について詳述
する。本発明の方法の対象とされる脂肪酸トリグリセリ
ド(油脂)は、グリセリドに結合しているパルミチン酸
含量が25重量%以上、好ましくは50重量%以上の植
物油脂及びそれらの分別油脂が用いられる。このような
油脂としてパーム油やその分別油がある。本発明におい
ては、まず、化学的ランダムエステル交換を行なう。こ
のエステル交換は、上記油脂100重量部に対しアルカ
リ金属触媒(ナトリウムメチラート等)を0.01〜1
0重量部、好ましくは0.1〜1重量部加えてエステル
交換反応を行なう。上記反応における温度は20℃〜9
0℃の温度で行うのが良く、より、好ましくは40〜8
0℃の温度で行うのが良い。また、反応時間は、通常、
5分から10時間、好ましくは15〜40分とすれば良
い。このエステル交換はトリグリセリド相互の間でラン
ダムにエステル交換する。このようにしてβ−パルミチ
ン酸含量を高める。このようにしてβ−パルミチン酸含
量を約40〜60%、すなわち約50%とする。この約
50%とした理由は、リパーゼによるエステル交換時の
反応温度をできるだけ下げて成分の変質を防ぎ、しかも
得られるグリセリドを人乳油脂中のβ−パルミチン酸含
量に類似させるためである。 [0008] Such a reforming method of the present invention will be described in detail. Fatty acid triglycerides are subject of the process of the present invention (oil) palmitic acid content of 25 wt% or more bound to grayed Riserido, preferably 50 wt% or more vegetable oils and their fractionated oil and fat used. There are palm oil and its fractions oil as such fats and oils. In the present invention, first, chemical random transesterification is performed. In this transesterification, an alkali metal catalyst (such as sodium methylate) is used in an amount of 0.01 to 1 with respect to 100 parts by weight of the oil or fat.
0 parts by weight, preferably 0.1 to 1 part by weight, is added to carry out the transesterification reaction. The temperature in the above reaction is 20 ° C to 9 ° C.
It is preferably performed at a temperature of 0 ° C, more preferably 40 to 8
It is good to carry out at a temperature of 0 ° C. The reaction time is usually
The time may be from 5 minutes to 10 hours, preferably from 15 to 40 minutes. This transesterification runs between triglycerides.
Dam to you transesterification. Thus, the β-palmitic acid content is increased. Thus, β-palmitic acid containing
The amount is about 40-60%, ie about 50%. About this
The reason for 50% was that the transesterification by lipase
Reduce the reaction temperature as much as possible to prevent deterioration of components, and
The resulting glyceride is contained in human milk fats and oils containing β-palmitic acid.
This is to make the amount similar.
【0009】次に、上記油脂を酸もしくは水で洗浄し、
α位に特異性の高いリパーゼを用いて酵素化学的にα位
の脂肪酸のエステル交換を行なう。本発明に用いられる
リパーゼとしては、リゾプス(Rhizopus)属、アスペルギ
ルス (Aspergillus)属、ムコール (Mucor)属の微生物が
生産するリパーゼを使用することができ、また、少なく
ともこれらと同様な性質を持つリパーゼであれば上記以
外の物でも良く、何等差し支えない。このようなリパー
ゼは市販されており、例えばアマノA(天野製薬)、リ
ポザイム(NOVO社製) 等が用いられる。上記リパーゼの
使用形態は、特に限定されないが、効率の点からは、公
知の方法で担体に固定化して用いることが好ましく、ま
た、有機溶媒下で用いる場合は、化学修飾酵素等を用い
るのが好ましい。上記リパーゼの使用量は、反応条件や
希望する改質油の性質によって適宜決定すれば良く、特
に制限されるものではないが、例えば、油脂 100gに対
して0.01〜50g、好ましくは 0.1〜20g程度とすれば良
い。本発明における酵素的エステル交換反応は、油脂を
液状であるいは固相の場合は溶融して酵素反応を行って
もよい。またヘキサン、イソオクタン等の有機溶媒を用
い、リン酸、トリス等の緩衝液を加えてpHを 4.0〜10.0
に調整して行ってもよい。反応温度は、30〜60℃の温度
で行うのが良く、より好ましくは35〜45℃の温度で行う
のが良い。また、反応時間は、通常1時間から3日間、
好ましくは4〜24時間程度とすれば良い。また、エステ
ル交換には、オレイン酸、リノール酸等の不飽和脂肪酸
を使用するとα位にこれらの不飽和脂肪酸が導入され、
健康上好ましいトリグリセリドを得ることができる。Next, the above fats and oils are washed with acid or water,
The transesterification of the fatty acid at the α-position is performed enzymatically using a lipase having high specificity at the α-position. The lipase used in the present invention, Rhizopus (Rhizopus) genus Aspergillus (Aspergillus) genus, can Mucor (Mucor) microorganism of the genus uses lipase production, also, the lipase having a similar and at least these properties If it is, a thing other than the above may be used, and there is no problem. Such a lipase is commercially available, for example, Amano A (Amano Pharmaceutical), lipozyme (NOVO) and the like. The use form of the lipase is not particularly limited, but from the viewpoint of efficiency, it is preferable to use the lipase by immobilizing it on a carrier by a known method, and when using it in an organic solvent, it is preferable to use a chemically modified enzyme or the like. preferable. The amount of the lipase to be used may be appropriately determined depending on the reaction conditions and the properties of the desired reformed oil, and is not particularly limited. For example, 0.01 to 50 g, preferably about 0.1 to 20 g, per 100 g of fat or oil. It is good. The enzymatic transesterification in the present invention may be carried out by melting the fat or oil in the case of a liquid or solid phase. Also, using an organic solvent such as hexane and isooctane, a buffer such as phosphoric acid or Tris is added to adjust the pH to 4.0 to 10.0.
May be adjusted. The reaction is preferably carried out at a temperature of 30 to 60 ° C, more preferably at a temperature of 35 to 45 ° C. The reaction time is usually 1 hour to 3 days,
Preferably, it should be about 4 to 24 hours. In the transesterification, when unsaturated fatty acids such as oleic acid and linoleic acid are used, these unsaturated fatty acids are introduced at the α-position,
Health-friendly triglycerides can be obtained.
【0010】本発明でこのようにして得られた反応生成
物は液々分配などの処理をして反応液から抽出し、必要
であればカラムクロマトグラフィー等の手段によって精
製してβ−パルミチン酸含量の高い脂肪酸トリグリセリ
ドとして使用する。このようなβ−パルミチン酸含量の
高い脂肪酸トリグリセリドは、飲食品、例えば育児用粉
乳、離乳食、経管栄養剤、病態食等に配合する。配合割
合は、飲食品 100重量部に対し2〜30重量部程度が好ま
しい。The reaction product thus obtained in the present invention is subjected to treatment such as liquid-liquid distribution, extracted from the reaction solution, and if necessary, purified by means such as column chromatography to obtain β-palmitic acid. Used as a rich fatty acid triglyceride. Such a fatty acid triglyceride having a high β-palmitic acid content is blended in foods and drinks, for example, infant milk powder, baby food, tube feeding, pathological food, and the like. The compounding ratio is preferably about 2 to 30 parts by weight with respect to 100 parts by weight of food or drink.
【0011】本発明では、β位(2位)にランダムエス
テル交換してパルミチン酸を導入するには、パルミチン
酸含量の高い油脂を用いる必要がある。その結果、得ら
れた油脂は、例えば融点が45〜55℃というように高く、
一般に食用油脂として用いるには、好ましくない物性を
示す。従って、このトリグリセリドのα位 (1位,3
位)にオレイン酸あるいはリノール酸を導入してトリグ
リセリドの融点を下げ、食用油脂として好ましいものと
する。また、このようにして得られるトリグリセリドは
育児用粉乳等に用いるために構成脂肪酸が好ましいもの
となる。In the present invention, in order to introduce palmitic acid by random transesterification at the β-position (position 2), it is necessary to use an oil or fat having a high palmitic acid content. As a result, the obtained fats and oils have a high melting point of, for example, 45 to 55 ° C.,
In general, it shows unfavorable physical properties for use as an edible oil and fat. Therefore, the α-position of this triglyceride (1st, 3
Oleic acid or linoleic acid is introduced into the glycerol to lower the melting point of triglyceride, making it preferable as an edible oil and fat. In addition, the triglyceride thus obtained is preferably composed of fatty acids for use in infant milk powder and the like.
【0012】次に本発明の実施例を示して本発明を説明
する。Next, the present invention will be described with reference to embodiments of the present invention.
【実施例1】パーム油(グリセリド中のパルミチン酸含
量43.3%、β−パルミチン酸含量18.7%)100gに、ナト
リウムメチラートを 0.5%添加し、温度80℃で20分間ラ
ンダムエステル交換反応した後、常法により反応トリグ
リセリド(パルミチン酸含量43.1%、β−パルミチン酸
含量43.4%)を95g抽出した。この反応トリグリセリド
10gとオレイン酸(純度95%)40gを基質とし、酵素と
して 1,3位特異性を有する固定化リパーゼ(Mucor mieh
ei起源、NOVO社製)3gを用い、酵素に対し5wt%の緩
衝液(pH 8.0)を添加したn−ヘキサン中で、40℃で24
時間反応を行い、常法により酵素反応トリグリセリド
6.3gを得た。このトリグリセリドのパルミチン酸含量
は24.2%、β−パルミチン酸含量は43.3%であった。得
られたトリグリセリドは“けもの臭”等の異臭がなく、
また吸収率が高いものであった。Example 1 0.5 g of sodium methylate was added to 100 g of palm oil (palmitic acid content in glyceride: 43.3%, β-palmitic acid content: 18.7%), and subjected to random transesterification at 80 ° C. for 20 minutes. 95 g of the reaction triglyceride (palmitic acid content 43.1%, β-palmitic acid content 43.4%) was extracted by a conventional method. This reaction triglyceride
Using 10 g of oleic acid (purity 95%) as a substrate and immobilized lipase (Mucor mieh
ei origin, using NOVO Co.) 3 g, 5 wt% of buffer to enzyme (pH 8.0) in n- hexane was added, at 40 ° C. 24
The reaction is carried out for a time, and the enzyme reaction triglyceride is
6.3 g were obtained. The triglyceride had a palmitic acid content of 24.2% and a β-palmitic acid content of 43.3%. The resulting triglyceride has no off-flavors such as "kemono odor"
Further, the absorption rate was high.
【0013】[0013]
【実施例2】パーム高融点分別油(グリセリド中のパル
ミチン酸含量59.3%、β−パルミチン酸含量21.6%)100
gに、ナトリウムメチラートを 0.5%添加し、温度80℃
で30分間ランダムエステル交換反応した後、常法により
反応トリグリセリド(パルミチン酸含量59.3%、β−パ
ルミチン酸含量58.4%)を95g抽出した。この反応トリ
グリセリド10gとオレイン酸(純度95%)40gを基質と
し、酵素として 1,3位特異性を有する固定化リパーゼ(M
ucor miehei起源、NOVO社製)3gを用い、酵素に対し
5wt%の緩衝液(pH 8.0)を添加したn−ヘキサン中
で、40℃で24時間反応を行い、常法により酵素反応トリ
グリセリド 6.5gを得た。このトリグリセリドのパルミ
チン酸含量は30.2%、β−パルミチン酸含量は58.3%で
あった。得られたトリグリセリドは“けもの臭”等の異
臭がなく、また吸収率も高いものであった。Example 2 Fractionated oil having a high melting point in palm (palmitic acid content in glyceride: 59.3%, β-palmitic acid content: 21.6%) 100
g, add 0.5% of sodium methylate,
After 30 minutes of random transesterification reaction, 95 g of reacted triglyceride (palmitic acid content 59.3%, β-palmitic acid content 58.4%) was extracted by a conventional method. Using 10 g of this reaction triglyceride and 40 g of oleic acid (95% purity) as substrates, immobilized lipase (M
Using 3 g of ucor miehei ( manufactured by NOVO), the reaction was carried out at 40 ° C. for 24 hours in n-hexane to which a 5 wt% buffer solution (pH 8.0) was added to the enzyme, and the enzyme-reacted triglyceride was 6.5 g by a conventional method. I got The triglyceride had a palmitic acid content of 30.2% and a β-palmitic acid content of 58.3%. The obtained triglyceride had no off-flavor such as "kemono odor" and a high absorption rate.
【0014】[0014]
【実施例3】パーム高融点分別油(グリセリド中のパル
ミチン酸含量59.3%、β−パルミチン酸含量24.6%)100
gに、ナトリウムメチラートを 0.5%添加し、温度80℃
で30分間ランダムエステル交換反応した後、常法により
反応トリグリセリド(パルミチン酸含量59.3%、β−パ
ルミチン酸含量58.4%)を95g抽出した。この反応トリ
グリセリド10gとリノール酸(純度95%)40gを基質と
し、酵素として 1,3位特異性を有する固定化リパーゼ(M
ucor miehei起源、NOVO社製)3gを用い、酵素に対し
5wt%の緩衝液(pH 8.0)を添加したn−ヘキサン中
で、40℃で24時間反応を行い、常法により酵素反応トリ
グリセリド 7.8gを得た。このトリグリセリドのパルミ
チン酸含量は40.2%、β−パルミチン酸含量は58.4%で
あった。得られたトリグリセリドは“けもの臭”等の異
臭がなく、また吸収率も高いものであった。Example 3 Fractionated oil with high melting point in palm (palmitic acid content in glyceride: 59.3%, β-palmitic acid content: 24.6%) 100
g, add 0.5% of sodium methylate,
After 30 minutes of random transesterification reaction, 95 g of reacted triglyceride (palmitic acid content 59.3%, β-palmitic acid content 58.4%) was extracted by a conventional method. Using 10 g of this reaction triglyceride and 40 g of linoleic acid (95% purity) as substrates, immobilized lipase (M
Using 3 g of ucor miehei ( manufactured by NOVO), the reaction was carried out at 40 ° C. for 24 hours in n-hexane to which a 5 wt% buffer solution (pH 8.0) was added, and 7.8 g of enzyme-reacted triglyceride was obtained by a conventional method. I got The triglyceride had a palmitic acid content of 40.2% and a β-palmitic acid content of 58.4%. The obtained triglyceride had no off-flavor such as "kemono odor" and a high absorption rate.
【0015】[0015]
【参考例1】実施例1の方法で得られたα−オレイン
酸、β−パルミチン酸トリグリセリドを調製粉乳製造時
に脂肪中80%配合して吸収の高い油脂を含有する調製
粉乳を得た。REFERENCE EXAMPLE 1 α-Oleic acid and β-palmitic acid triglyceride obtained by the method of Example 1 were blended with 80% of the fat during the preparation of the prepared milk powder to obtain a milk powder containing a fat and oil having a high absorption.
【0016】[0016]
【参考例2】実施例2の方法で得られた酵素反応トリグ
リセリドを幼若ラットの飼料に添加し、吸収性を調べ
た。表1に実験飼料の組成を示す。Reference Example 2 The enzyme-reacted triglyceride obtained by the method of Example 2 was added to the feed of young rats, and the absorbability was examined. Table 1 shows the composition of the experimental feed.
【0017】ラットは3週齢のSD系雄ラット(日本チ
ャールズリバー(株))を用い、4週齢時に1群8匹の2
群に分け、表1の飼料をそれぞれ2週間給与した。飼育
期間中に飼料摂取量ならびに体重増加量を測定し、1週
間ごとの飼料効率を算出した。また、飼料給与後の12〜
14日目の3日間に採糞をし、未吸収のパルミチン酸量と
オレイン酸量を定量した。表2に飼料効率を、表3にパ
ルミチン酸とオレイン酸の見かけの消化吸収率を示す。The rats used were SD male rats of 3 weeks old (Charles River Japan Co., Ltd.).
The animals were divided into groups and fed the feeds shown in Table 1 for 2 weeks. During the breeding period, feed intake and body weight gain were measured, and feed efficiency was calculated every week. In addition, 12 ~
On the 14th day, feces were collected for 3 days, and the amount of unabsorbed palmitic acid and oleic acid were determined. Table 2 shows the feed efficiency, and Table 3 shows the apparent digestion and absorption rates of palmitic acid and oleic acid.
【0018】本成績から明らかなように本発明による油
脂を給与したラットは飼料効率が対照油脂(原料油脂)
に比べて改善され、成長が良いことが認められた。ま
た、パルミチン酸の消化吸収率も著しく改善された。し
たがって、パルミチン酸をトリグリセリド源として使用
する際には、本発明によって処理したトリグリセリドを
用いた方がはるかに消化吸収率の高い油脂を供給するこ
とができる。本成績は、ヒトに充分適用でき、吸収性が
高くしかも母乳に類似した調製粉乳用の油脂として利用
できる。As is clear from the results, the rats fed the fats and oils according to the present invention showed that the feed efficiency was comparable to the control fats (raw fats and oils).
And improved growth. In addition, the digestibility of palmitic acid was significantly improved. Therefore, when palmitic acid is used as a triglyceride source, the use of the triglyceride treated according to the present invention can supply a fat and oil having a much higher digestion and absorption rate. This result can be sufficiently applied to humans, has high absorbency, and can be used as a fat and oil for formula powder similar to breast milk.
【0019】[0019]
【表1】 実験飼料組成 ───────────────────────── 対照群 本発明群 ───────────────────────── カゼイン 20.0 20.0 DL−メチオニン 0.3 0.3 未処理油脂 10.0 ── 本発明油脂 ── 10.0 塩類混合* 3.5 3.5 ビタミン混合* 1.0 1.0 重酒石酸コリン 0.2 0.2 セルロース 5.0 5.0 コーンスターチ 15.0 15.0 ショ糖 45.0 45.0 ───────────────────────── * AIN-76組成[Table 1] Experimental feed composition ───────────────────────── Control group The present invention group ───────────── ──────────── Casein 20.0 20.0 DL-methionine 0.3 0.3 Untreated fat and oil 10.0 油 Fatty oil of the present invention ── 10.0 Salt mixture * 3.5 3.5 Vitamin mixture * 1.0 1.0 Choline bitartrate 0.2 0.2 Cellulose 5.0 5.0 Corn starch 15.0 15.0 Sucrose 45.0 45.0 ───────────────────────── * AIN-76 composition
【0020】[0020]
【表2】 飼料効率 (%) ────────────────────────── 1週目 2週目 ────────────────────────── 対照群 46.6±3.9 45.3±2.7 本発明群 50.8±2.2 * 47.5±2.7 * ────────────────────────── * 対照群に比べて有意差あり(p<0.05) 飼料効率(%)=体重増加量(g)÷飼料摂取量(g)×100 [Table 2] Feed efficiency (%) ────────────────────────── 1st week 2nd week ─────────対 照 Control group 46.6 ± 3.9 45.3 ± 2.7 Inventive group 50.8 ± 2.2 * 47.5 ± 2.7 * ────────────── ──────────── * Significantly different from control group (p <0.05) Feed efficiency (%) = weight gain (g) ÷ feed intake (g) x 100
【0021】[0021]
【表3】 パルミチン酸の見かけの消化吸収率(%) ───────────────── パルミチン酸 ───────────────── 対照群 80.0±3.4 本発明群 87.6±3.8 * ─────────────────* 対照油脂群に比べて有意差あり(p<0.01) みかけの消化吸収率(%)=(1日あたりの脂肪酸摂取
量−1日あたりの脂肪酸排泄量)÷1日あたりの脂肪酸
摂取量×100[Table 3] Apparent digestion and absorption rate of palmitic acid (%) パ ル Palmitic acid ──────────────── ─ Control group 80.0 ± 3.4 Inventive group 87.6 ± 3.8 * ───────────────── * Significantly different from control fat group (p <0.01) Apparent digestibility (%) = (Fatty acid intake per day−1 fatty acid excretion per day) ÷ fatty acid intake per day × 100
───────────────────────────────────────────────────── フロントページの続き (72)発明者 八尋 政利 東京都東村山市久米川町2−8−13 (56)参考文献 欧州特許出願公開376628(EP,A 2) 欧州公開496456(EP,A1) 欧州公開209327(EP,A1) ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Masatoshi Yahiro 2-8-13 Kumegawa-cho, Higashimurayama-shi, Tokyo (56) References European Patent Application Publication 376628 (EP, A2) European Publication 496456 (EP, A1) Europe Published 209327 (EP, A1)
Claims (1)
て化学的にランダムエステル交換してそのトリグリセリ
ド中のβ位のパルミチン酸含量を約50%に高め、次い
でこれをα位に特異的に作用するリパーセを用いて酵素
化学的に不飽和脂肪酸とエステル交換して該不飽和脂肪
酸をα位に導入することを特徴とする、β位のパルミチ
ン酸含量の高いトリグリセリドの製造法。 1. A method using palm oil or its fractionated oil as a catalyst.
Chemically and randomly transesterify the triglyceride.
The palmitic acid content at the β-position in the metal to about 50%,
This is done by using a lipase that acts specifically at the α-position
Chemically unsaturated esterification with unsaturated fatty acid
Β-palmichi characterized by introducing an acid into the α-position
A method for producing triglycerides having a high acid content.
Priority Applications (1)
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JP04248769A JP3120906B2 (en) | 1992-08-25 | 1992-08-25 | Method for producing triglyceride containing β-palmitic acid |
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JP04248769A JP3120906B2 (en) | 1992-08-25 | 1992-08-25 | Method for producing triglyceride containing β-palmitic acid |
Publications (2)
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JPH0670786A JPH0670786A (en) | 1994-03-15 |
JP3120906B2 true JP3120906B2 (en) | 2000-12-25 |
Family
ID=17183109
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JP04248769A Expired - Fee Related JP3120906B2 (en) | 1992-08-25 | 1992-08-25 | Method for producing triglyceride containing β-palmitic acid |
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Cited By (1)
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WO2011132734A1 (en) | 2010-04-22 | 2011-10-27 | 株式会社カネカ | Liquid oil and fat, and production method therefor |
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JP4175698B2 (en) | 1998-06-19 | 2008-11-05 | サントリー株式会社 | Novel triglyceride and composition containing the same |
RU2413430C2 (en) | 2005-04-27 | 2011-03-10 | Энзимотек Лтд. | Composition of fat base (versions) and method of its production (versions), composition of breast milk fat substitute and method of its production (version), baby formula |
KR100598607B1 (en) * | 2006-02-24 | 2006-07-07 | 주식회사 일신웰스 | Oil composition and preparation method thereof |
NZ579108A (en) | 2007-02-28 | 2011-02-25 | Loders Croklaan Bv | Process for producing 1,3,-dioleoyl-2-palmitoyl glyceride (OPO) |
DK2173197T3 (en) | 2007-07-25 | 2019-09-23 | Bunge Loders Croklaan B V | Course of action |
JP4850153B2 (en) * | 2007-09-03 | 2012-01-11 | サントリーホールディングス株式会社 | Novel triglyceride and composition containing the same |
EP3502247A1 (en) | 2014-05-20 | 2019-06-26 | Bunge Loders Croklaan B.V. | Process for immobilization of a lipase |
JP6904009B2 (en) * | 2017-03-31 | 2021-07-14 | 日油株式会社 | Oil and fat manufacturing method |
KR102401871B1 (en) | 2018-03-02 | 2022-05-25 | 후지세유 그룹 혼샤 가부시키가이샤 | 2nd place is palmitic acid-rich oil and fat composition manufacturing method |
JP2019162055A (en) * | 2018-03-19 | 2019-09-26 | 株式会社明治 | Composition for promoting energy metabolism |
CN110616234B (en) | 2018-06-20 | 2023-12-22 | 花臣有限公司 | Method for producing human milk fat substitute |
Family Cites Families (3)
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GB2178752B (en) * | 1985-07-12 | 1989-10-11 | Unilever Plc | Substitute milk fat |
US5000975A (en) * | 1988-12-29 | 1991-03-19 | American Home Products Corporation | Randomized palm oil fat composition for infant formulas |
DK0496456T3 (en) * | 1991-01-23 | 1995-08-07 | Unilever Plc | Breast milk-fat substitutes |
-
1992
- 1992-08-25 JP JP04248769A patent/JP3120906B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2011132734A1 (en) | 2010-04-22 | 2011-10-27 | 株式会社カネカ | Liquid oil and fat, and production method therefor |
Also Published As
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JPH0670786A (en) | 1994-03-15 |
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