JPH10183165A - Oil/fat for margarine and shortening and products thereof - Google Patents
Oil/fat for margarine and shortening and products thereofInfo
- Publication number
- JPH10183165A JPH10183165A JP8342909A JP34290996A JPH10183165A JP H10183165 A JPH10183165 A JP H10183165A JP 8342909 A JP8342909 A JP 8342909A JP 34290996 A JP34290996 A JP 34290996A JP H10183165 A JPH10183165 A JP H10183165A
- Authority
- JP
- Japan
- Prior art keywords
- oil
- fat
- margarine
- shortening
- lipase
- 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.)
- Granted
Links
- 235000019197 fats Nutrition 0.000 title claims abstract description 46
- 235000013310 margarine Nutrition 0.000 title claims abstract description 32
- 238000004904 shortening Methods 0.000 title claims abstract description 32
- 239000003264 margarine Substances 0.000 title claims abstract description 31
- 239000003921 oil Substances 0.000 claims abstract description 44
- 235000019198 oils Nutrition 0.000 claims abstract description 44
- 108090001060 Lipase Proteins 0.000 claims abstract description 32
- 239000004367 Lipase Substances 0.000 claims abstract description 32
- 102000004882 Lipase Human genes 0.000 claims abstract description 32
- 235000019421 lipase Nutrition 0.000 claims abstract description 32
- 238000005809 transesterification reaction Methods 0.000 claims abstract description 18
- IPCSVZSSVZVIGE-UHFFFAOYSA-N palmitic acid group Chemical group C(CCCCCCCCCCCCCCC)(=O)O IPCSVZSSVZVIGE-UHFFFAOYSA-N 0.000 claims abstract description 15
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 claims abstract description 13
- 235000014113 dietary fatty acids Nutrition 0.000 claims abstract description 12
- 229930195729 fatty acid Natural products 0.000 claims abstract description 12
- 239000000194 fatty acid Substances 0.000 claims abstract description 12
- 150000004665 fatty acids Chemical class 0.000 claims abstract description 12
- 235000021281 monounsaturated fatty acids Nutrition 0.000 claims abstract description 9
- 150000004671 saturated fatty acids Chemical class 0.000 claims abstract description 9
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 claims abstract description 8
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 claims abstract description 8
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 claims abstract description 8
- 239000005642 Oleic acid Substances 0.000 claims abstract description 8
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 claims abstract description 8
- 235000021314 Palmitic acid Nutrition 0.000 claims abstract description 8
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 claims abstract description 8
- 239000007788 liquid Substances 0.000 claims abstract description 8
- 125000005456 glyceride group Chemical group 0.000 claims abstract description 7
- WQEPLUUGTLDZJY-UHFFFAOYSA-N n-Pentadecanoic acid Natural products CCCCCCCCCCCCCCC(O)=O WQEPLUUGTLDZJY-UHFFFAOYSA-N 0.000 claims abstract description 7
- 241000588810 Alcaligenes sp. Species 0.000 claims abstract description 6
- UFTFJSFQGQCHQW-UHFFFAOYSA-N triformin Chemical compound O=COCC(OC=O)COC=O UFTFJSFQGQCHQW-UHFFFAOYSA-N 0.000 claims abstract description 6
- 235000019482 Palm oil Nutrition 0.000 claims description 20
- 239000002540 palm oil Substances 0.000 claims description 20
- 239000000203 mixture Substances 0.000 claims description 16
- 235000013311 vegetables Nutrition 0.000 claims description 7
- PORPENFLTBBHSG-MGBGTMOVSA-N 1,2-dihexadecanoyl-sn-glycerol-3-phosphate Chemical group CCCCCCCCCCCCCCCC(=O)OC[C@H](COP(O)(O)=O)OC(=O)CCCCCCCCCCCCCCC PORPENFLTBBHSG-MGBGTMOVSA-N 0.000 claims description 5
- 235000003441 saturated fatty acids Nutrition 0.000 claims description 4
- 150000001875 compounds Chemical class 0.000 claims 1
- 239000003925 fat Substances 0.000 abstract description 42
- 239000013078 crystal Substances 0.000 abstract description 29
- 230000000704 physical effect Effects 0.000 abstract description 6
- 230000007547 defect Effects 0.000 abstract description 2
- 235000015112 vegetable and seed oil Nutrition 0.000 abstract description 2
- 239000008158 vegetable oil Substances 0.000 abstract description 2
- 230000000052 comparative effect Effects 0.000 description 19
- 239000002957 persistent organic pollutant Substances 0.000 description 18
- PVNIQBQSYATKKL-UHFFFAOYSA-N tripalmitin Chemical compound CCCCCCCCCCCCCCCC(=O)OCC(OC(=O)CCCCCCCCCCCCCCC)COC(=O)CCCCCCCCCCCCCCC PVNIQBQSYATKKL-UHFFFAOYSA-N 0.000 description 18
- 239000003054 catalyst Substances 0.000 description 11
- 239000003795 chemical substances by application Substances 0.000 description 9
- 229960001947 tripalmitin Drugs 0.000 description 9
- 239000005909 Kieselgur Substances 0.000 description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 8
- 230000015572 biosynthetic process Effects 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- 108090000790 Enzymes Proteins 0.000 description 6
- 102000004190 Enzymes Human genes 0.000 description 6
- 235000019484 Rapeseed oil Nutrition 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- DCXXMTOCNZCJGO-UHFFFAOYSA-N tristearoylglycerol Chemical compound CCCCCCCCCCCCCCCCCC(=O)OCC(OC(=O)CCCCCCCCCCCCCCCCC)COC(=O)CCCCCCCCCCCCCCCCC DCXXMTOCNZCJGO-UHFFFAOYSA-N 0.000 description 6
- 241000588986 Alcaligenes Species 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 235000019485 Safflower oil Nutrition 0.000 description 4
- 238000004332 deodorization Methods 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 235000014593 oils and fats Nutrition 0.000 description 4
- 235000005713 safflower oil Nutrition 0.000 description 4
- 239000003813 safflower oil Substances 0.000 description 4
- 239000011362 coarse particle Substances 0.000 description 3
- 238000010791 quenching Methods 0.000 description 3
- 230000000171 quenching effect Effects 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- WQDUMFSSJAZKTM-UHFFFAOYSA-N Sodium methoxide Chemical compound [Na+].[O-]C WQDUMFSSJAZKTM-UHFFFAOYSA-N 0.000 description 2
- 235000019486 Sunflower oil Nutrition 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- 239000002600 sunflower oil Substances 0.000 description 2
- 150000003626 triacylglycerols Chemical class 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- LDVVTQMJQSCDMK-UHFFFAOYSA-N 1,3-dihydroxypropan-2-yl formate Chemical compound OCC(CO)OC=O LDVVTQMJQSCDMK-UHFFFAOYSA-N 0.000 description 1
- 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 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 108010048733 Lipozyme Proteins 0.000 description 1
- 241000235403 Rhizomucor miehei Species 0.000 description 1
- 241000303962 Rhizopus delemar Species 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000011437 continuous method Methods 0.000 description 1
- 235000005687 corn oil Nutrition 0.000 description 1
- 239000002285 corn oil Substances 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 235000021588 free fatty acids Nutrition 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 239000000787 lecithin Substances 0.000 description 1
- 229940067606 lecithin Drugs 0.000 description 1
- 235000010445 lecithin Nutrition 0.000 description 1
- FCCDDURTIIUXBY-UHFFFAOYSA-N lipoamide Chemical compound NC(=O)CCCCC1CCSS1 FCCDDURTIIUXBY-UHFFFAOYSA-N 0.000 description 1
- 150000002943 palmitic acids Chemical class 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 235000020183 skimmed milk Nutrition 0.000 description 1
- 239000003549 soybean oil Substances 0.000 description 1
- 235000012424 soybean oil Nutrition 0.000 description 1
- 125000005457 triglyceride group Chemical group 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23D—EDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS, COOKING OILS
- A23D9/00—Other edible oils or fats, e.g. shortenings, cooking oils
- A23D9/02—Other edible oils or fats, e.g. shortenings, cooking oils characterised by the production or working-up
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23D—EDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS, COOKING OILS
- A23D7/00—Edible oil or fat compositions containing an aqueous phase, e.g. margarines
- A23D7/001—Spread compositions
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
- C11C3/04—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fats or fatty oils
- C11C3/10—Ester interchange
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明はマーガリン・ショートニ
ング用油脂およびそれでできた製品に関する。詳細には
本発明は結晶粗大化が解消され、長期間に渡って物性の
安定した、パーム、パームステアリンなどのパーム系油
脂を原料としたマーガリン・ショートニング用油脂およ
びそれでできた製品に関する。本発明では、「マーガリ
ン」はマーガリン類の日本農林規格(JAS)に、「シ
ョートニング」はショートニングの日本農林規格(JA
S)にそれぞれ定義にされる意味で用いている。The present invention relates to margarine shortening fats and oils and products made therefrom. More specifically, the present invention relates to a fat and oil for margarine and shortening using palm-based fats such as palm and palm stearin as raw materials, which have eliminated crystal coarsening and have stable physical properties over a long period of time, and products made therefrom. In the present invention, "margarine" refers to the Japanese Agricultural and Forestry Standards (JAS) for margarines, and "shortening" refers to the Japanese Agricultural and Forestry Standards for shortening (JAS).
S) is used in the meaning defined as each.
【0002】[0002]
【従来の技術】パーム系油脂は常温で半固体ないし固体
であるために可塑性油脂原料として利用されているが、
マーガリン・ショートニング原料油脂にそれらを用いた
とき、製品の貯蔵中に粗大な粒子の結晶の発現が観察さ
れることがある。これは製品の物性を悪化させるととも
に、食感にもザラツキを与え好ましくない。2. Description of the Related Art Palm-based fats and oils are used as plastic fats and oils because they are semi-solid or solid at room temperature.
When they are used in margarine shortening feedstock fats, the appearance of coarse particle crystals during storage of the product may be observed. This undesirably deteriorates the physical properties of the product and gives a rough texture to the texture.
【0003】特開昭55−110195号公報には、パ
ーム油をエステル交換し対称型ジ飽和モノオレイックグ
リセリド含量10%以下で融点25〜45℃の油脂をつ
くる改質パーム油の製造法が示されている。また、パー
ム油の粗大結晶形成の原因が対称型ジ飽和モノオレイッ
クトリグリセリドであることを発見したとし、それを1
0%以下の含量にすることを目的としている。Japanese Unexamined Patent Publication No. 55-110195 discloses a method for producing a modified palm oil which transesterifies palm oil to produce a fat or oil having a symmetrical di-saturated monooleic glyceride content of 10% or less and a melting point of 25 to 45 ° C. It is shown. Furthermore, they found that the cause of the formation of coarse crystals of palm oil was symmetrical di-saturated monooleic triglyceride.
The purpose is to reduce the content to 0% or less.
【0004】特開平2−219581号公報には、パー
ム25%以上含有油脂をリパーゼでエステル交換して対
称型2飽和モノオレイックトリグリセリド含量10%以
下で、33.3℃以上の固体脂含量が2%以下のソフト
タイプのマーガリン・ショートニング用油脂をつくるこ
とが示されている。また、特開平4−75590号公報
では、リパーゼは1,3位置特異性でなければいけない
としている。さらにまた、エステル交換には化学触媒を
用いてランダムにエステル交換する方法もあるが、この
方法では触媒除去の工程が必要で廃触媒処理の問題があ
る。また、油脂が着色するため、脱色する必要もある。JP-A-2-219581 discloses that a fat or oil containing at least 25% of palm is transesterified with a lipase and has a symmetrical 2-saturated monooleic triglyceride content of 10% or less and a solid fat content of 33.3 ° C. or more. It has been shown to produce less than 2% soft type margarine shortening fat. Japanese Patent Application Laid-Open No. 4-75590 discloses that lipase must have 1,3-position specificity. Furthermore, transesterification includes a method in which transesterification is performed at random using a chemical catalyst. However, this method requires a step of removing the catalyst, and has a problem of waste catalyst treatment. In addition, since the fats and oils are colored, they need to be decolorized.
【0005】[0005]
【発明が解決しようとする課題】本発明はパーム系油脂
をマーガリン・ショートニング用油脂として利用するに
際し、パーム系油脂の欠点である結晶粗大化が解消さ
れ、長期間に渡って物性の安定したマーガリン・ショー
トニング用油脂を提供することを目的とする。さらに、
本発明は上記マーガリン・ショートニング用油脂ででき
たマーガリンまたはショートニングを提供することを目
的とする。SUMMARY OF THE INVENTION In the present invention, when palm oils and fats are used as margarine and shortening oils and fats, the disadvantage of palm oils and fats is that crystal defects such as crystal coarsening are eliminated, and margarine which has stable physical properties for a long period of time. -To provide a shortening fat or oil. further,
An object of the present invention is to provide margarine or shortening made of the above-mentioned fat or oil for margarine shortening.
【0006】[0006]
【課題を解決するための手段】本発明者らは、POPが
集積し粗大な結晶を形成するというパーム系油脂の特性
を解消するために鋭意研究し、POPの含量ではなく、
PPO/POP≧0.5とすればパーム系油脂をマーガ
リン・ショートニング用油脂に用いたときに粗大結晶形
成を防止できることを発見した。Means for Solving the Problems The present inventors have made intensive studies to solve the property of palm fats and oils that POPs accumulate and form coarse crystals.
It has been discovered that when PPO / POP ≧ 0.5, the formation of coarse crystals can be prevented when palm fats and oils are used for margarine and shortening fats and oils.
【0007】パーム系油脂をマーガリン・ショートニン
グ原料に用いたときに粗大結晶形成防止には、エステル
交換が利用できる。エステル交換に用いるリパーゼは通
常これまではトリグリセリドのsn−1(3)位とsn
−2位のエステル結合を識別する、いわゆる1,3位特
異性のものであった。しかし、これではPPO/POP
≧0.5とはならず、それゆえ粗大結晶形成防止効果が
小さい。化学触媒を用いてランダムエステル交換し、P
PO/POP≧0.5とする方法もあるが、この方法で
は触媒除去の工程が必要で廃触媒の処理の問題もある。
また、油脂が着色するため脱色する必要もある。[0007] Transesterification can be used to prevent the formation of coarse crystals when a palm-based fat is used as a raw material for margarine shortening. The lipase used for transesterification is usually the sn-1 (3) position of triglyceride and the sn
It was a so-called 1,3-position specificity that identifies the ester bond at the -2 position. However, this is PPO / POP
≧ 0.5, and therefore the effect of preventing the formation of coarse crystals is small. Random transesterification using chemical catalyst, P
Although there is a method of setting PO / POP ≧ 0.5, this method requires a catalyst removal step, and has a problem of treating a spent catalyst.
In addition, since the fats and oils are colored, they need to be decolorized.
【0008】PPO/POP≧0.5となる1,3位置
特異性でないリパーゼ、特にAlcaligenes
sp.由来のリパーゼ、さらに好ましくはAlcali
genes sp.由来のリパーゼを珪藻土に固定化し
た酵素剤を用いてエステル交換する。該酵素を用いると
化学触媒や1,3位置特異性リパーゼを用いてエステル
交換するよりも0.2%以上多くトリパルミチンが生成
される。トリパルミチンは融点が44〜65℃と高いた
め結晶生成時の核となる。結晶はこの結晶核を中心に成
長するため、結晶核が多ければそれだけ結晶が分散し微
細なものとなると考えられる。Lipases not having 1,3-position specificity such that PPO / POP ≧ 0.5, especially Alcaligenes
sp. Derived lipase, more preferably Alcali
genes sp. The lipase derived is transesterified using an enzyme agent immobilized on diatomaceous earth. When this enzyme is used, 0.2% or more of tripalmitin is produced as compared with transesterification using a chemical catalyst or 1,3-position specific lipase. Tripalmitin has a high melting point of 44 to 65 ° C., and serves as a nucleus during crystal formation. Since the crystal grows around this crystal nucleus, it is considered that the more the crystal nucleus, the more the crystal is dispersed and becomes finer.
【0009】よって、Alcaligenes sp.
由来リパーゼを珪藻土に固定化した酵素剤を用いてエス
テル交換した油脂は1,3位置特異性のリパーゼやケミ
カルエステル交換により得られたものより結晶性が優れ
ている。1,3位置特異性でないリパーゼ、特にアルカ
リゲネス属由来リパーゼを珪藻土に固定化した酵素剤を
用いてエステル交換した油脂で見られる結晶性改善の効
果は、トリパルミチン含量が1,3位置特異性のリパー
ゼによるエステル交換やケミカルエステル交換により得
られたものより0.2%以上多いときに見られる。Therefore, Alcaligenes sp.
Fats and oils transesterified using an enzyme agent in which a derived lipase is immobilized on diatomaceous earth have better crystallinity than those obtained by lipase having 1,3-position specificity or chemical transesterification. The effect of improving the crystallinity seen in oils and fats transesterified using an enzyme agent in which a lipase that is not 1,3-position specific, particularly a lipase derived from the genus Alcaligenes, is immobilized on diatomaceous earth, has a tripalmitin content of 1,3-position specific. It is observed when the amount obtained by transesterification with lipase or chemical transesterification is 0.2% or more.
【0010】本発明は、パーム系油脂および植物液体油
由来の、トリパルミチン含量が1,3位置特異性リパー
ゼや化学触媒によるエステル交換により生成する量より
0.2%以上多く生成する1,3位置特異性でないリパ
ーゼ、特にAlcaligenes sp.由来のリパ
ーゼ、さらに好ましくはAlcaligenes s
p.由来のリパーゼを珪藻土に固定化した酵素剤を用い
てエステル交換することによって得られた、飽和脂肪酸
28〜37重量%およびモノ不飽和脂肪酸40〜50重
量%の油脂組成物であって、ジパルミトイルモノオレオ
イルグリセリドの構成比率がPPO/POP≧0.5
〔ただし、PPOとはトリグリセリドを構成する3つの
脂肪酸のうち、1,3位(または2,3位)にパルミチ
ン酸が、3位(または1位)にオレイン酸が結合したも
のをいい、POPとは1,3位にパルミチン酸、2位に
オレイン酸が結合したものをいう。〕であることを特徴
とするマーガリン・ショートニング用油脂である。[0010] The present invention relates to 1,3,3,3,4,5,5,5,5,5,6,9,10,13,15 or 15 or more palmipin or vegetable liquid oils whose tripalmitin content is 0.2% or more larger than that produced by transesterification with a 1,3-regiospecific lipase or a chemical catalyst. Lipases that are not regiospecific, especially Alcaligenes sp. Lipase, more preferably Alcaligenes s
p. A fat / oil composition comprising 28-37% by weight of saturated fatty acid and 40-50% by weight of monounsaturated fatty acid, obtained by subjecting a lipase of interest to transesterification using an enzyme agent immobilized on diatomaceous earth, comprising dipalmitoyl. Monooleoyl glyceride is composed of PPO / POP ≧ 0.5
[However, PPO is a fatty acid in which palmitic acid is bonded to the 1,3-position (or 2,3-position) and oleic acid is bonded to the 3-position (or 1-position) among the three fatty acids constituting the triglyceride. "Means that palmitic acid is bonded to the 1,3-position and oleic acid is bonded to the 2-position. ] It is a fat for margarine shortening characterized by the following.
【0011】上記PPO/POPについて、パルミチン
酸残基とオレイン酸残基を規定するものである。パーム
油はパルミチン酸32〜59%、オレイン酸27〜52
%が主要な脂肪酸であり、トリグリセリドはPOP25
〜35%、POO15〜25%が主となる。また、植物
油を配合すると、POO、POP、OOOといったもの
が主要トリグリセリドとなる。POO、OOOについて
は結晶粗大化の問題に対する関与は低いため、本発明に
おいてパルミチン酸が2つ、オレイン酸が1つのトリグ
リセリドについて上記の通り規定するものである。The above PPO / POP defines a palmitic acid residue and an oleic acid residue. Palm oil is palmitic acid 32-59%, oleic acid 27-52
% Is the major fatty acid and triglyceride is POP25
~ 35%, POO 15 ~ 25% are main. In addition, when vegetable oil is blended, POO, POP, and OOO become main triglycerides. Since POO and OOO are less involved in the problem of crystal coarsening, triglycerides having two palmitic acids and one oleic acid are specified as described above in the present invention.
【0012】本発明で用いるパーム系油脂はパーム油の
ほかにパームステアリンも含まれ、単独で、あるいは植
物液体油を配合して使用される。パーム油と混合して使
用する植物液体油は、パーム油と混合したとき本発明で
特定する脂肪酸組成である飽和脂肪酸28〜37重量%
およびモノ不飽和脂肪酸40〜50重量%を達成できる
ものであれば特に限定されない。例えば、ナタネ油、ダ
イズ油、コーン油、サフラワー油、ハイオレイックサフ
ラワー油、ヒマワリ油、ハイオレイックヒマワリ油が例
示される。The palm-based fat used in the present invention contains palm stearin in addition to palm oil, and is used alone or in combination with a vegetable liquid oil. The vegetable liquid oil used by mixing with palm oil, when mixed with palm oil, has a fatty acid composition specified by the present invention of 28 to 37% by weight of a saturated fatty acid composition.
There is no particular limitation as long as the monounsaturated fatty acid can achieve 40 to 50% by weight. For example, rapeseed oil, soybean oil, corn oil, safflower oil, high oleic safflower oil, sunflower oil, high oleic sunflower oil are exemplified.
【0013】本発明は、パーム系油脂および植物液体油
由来の飽和脂肪酸28〜37重量%およびモノ不飽和脂
肪酸40〜50重量%の油脂組成物であって、ジパルミ
トイルモノオレオイルグリセリドの構成比率がPPO/
POP≧0.5であることを特徴とするマーガリン・シ
ョートニング用油脂である。The present invention relates to an oil / fat composition comprising 28 to 37% by weight of a saturated fatty acid and 40 to 50% by weight of a monounsaturated fatty acid derived from palm oil or vegetable liquid oil, wherein dipalmitoyl monooleoyl glyceride is constituted. Is PPO /
A margarine shortening fat or oil, wherein POP ≧ 0.5.
【0014】本発明で特定する脂肪酸組成は、飽和脂肪
酸28〜37重量%、モノ不飽和脂肪酸40〜50重量
%であり、上記パーム系油脂と植物液体油を混合し、上
記脂肪酸組成となるようにする。飽和脂肪酸28重量%
より少ない、またモノ不飽和脂肪酸50重量%より多い
と、PPO/POP≧0.5が達成され難くなる。飽和
脂肪酸37重量%より多い、またモノ不飽和脂肪酸40
重量%より少ないとマーガリン・ショートニング用油脂
としては固体脂含量が多すぎ、口どけ、作業性の面で問
題がある。The fatty acid composition specified in the present invention is 28 to 37% by weight of a saturated fatty acid and 40 to 50% by weight of a monounsaturated fatty acid. To 28% by weight of saturated fatty acids
If the amount is less than 50% by weight or monounsaturated fatty acid, it is difficult to achieve PPO / POP ≧ 0.5. More than 37% by weight of saturated fatty acids and 40 monounsaturated fatty acids
If the amount is less than% by weight, the solid fat content of the margarine shortening fat is too high, and there is a problem in mouthfeel and workability.
【0015】上記脂肪酸組成は、具体的に例示すると、
パーム油とナタネ油を混合した場合、その配合率は7:
3〜10:0(重量比)、パームステアリンとナタネ油
を混合した場合、その配合率は5:5〜6:4(重量
比)で達成される。The above fatty acid composition is specifically exemplified as follows:
When palm oil and rapeseed oil are mixed, the compounding ratio is 7:
When palm stearin and rapeseed oil are mixed at a ratio of 3 to 10: 0 (weight ratio), the mixing ratio is achieved at a ratio of 5: 5 to 6: 4 (weight ratio).
【0016】本発明は、パーム系油脂および植物液体油
由来の、1,3位置特異性でないリパーゼ、特に1,3
特異性でないリパーゼがAlcaligenes s
p.由来のリパーゼ、さらに好ましくはAlcalig
enes sp.由来のリパーゼを珪藻土に固定化した
酵素剤を用いてエステル交換することによって得られた
組成物であって、ジパルミトイルモノオレオイルグリセ
リドの構成比率がPPO/POP≧0.5であることを
特徴とするマーガリン・ショートニング用油脂である。The present invention relates to lipases derived from palm oils and vegetable liquid oils which are not 1,3-position specific, especially 1,3
Non- specific lipases are found in Alcaligenes
p. Derived lipase, more preferably Alcalig
ene sp. A composition obtained by transesterifying a lipase derived from a diatomaceous earth using an enzyme agent immobilized on diatomaceous earth, wherein the composition ratio of dipalmitoyl monooleoyl glyceride is PPO / POP ≧ 0.5. For margarine and shortening.
【0017】本発明のマーガリン・ショートニング用油
脂はパーム系油脂と植物液体油を混合して、脂肪酸組成
が飽和脂肪酸28〜37重量%、モノ不飽和脂肪酸40
〜50重量%になるように調製し、ついで油脂組成物を
エステル交換して組成物中のジパルミトイルモノオレオ
イルグリセリドの構成比率をPPO/POP≧0.5と
することにより製造することができる。このとき、トリ
パルミチン含量が1,3位置特異性リパーゼが化学触媒
によるエステル交換により生成する量よりも0.2%以
上多く含まれる。The fats and oils for margarine shortening of the present invention are obtained by mixing palm-based fats and vegetable liquid oils and having a fatty acid composition of 28 to 37% by weight of saturated fatty acids and 40 of monounsaturated fatty acids.
5050% by weight, and then transesterifying the oil / fat composition to make the composition ratio of dipalmitoyl monooleoyl glyceride in the composition PPO / POP ≧ 0.5. . At this time, the content of tripalmitin is 0.2% or more larger than the amount of 1,3-regiospecific lipase produced by transesterification with a chemical catalyst.
【0018】本発明で用いるエステル交換反応はバッチ
式でも連続方式でもよい。しかし、バッチ式では副反応
として起こる加水分解により生成する遊離脂肪酸の量が
多くなるため、好ましくは固定化リパーゼ剤を充填した
カラムによる連続方式がよい。The transesterification reaction used in the present invention may be of a batch type or a continuous type. However, in the batch method, the amount of free fatty acids generated by hydrolysis occurring as a side reaction increases, so that a continuous method using a column filled with an immobilized lipase agent is preferable.
【0019】本発明は上記マーガリン・ショートニング
用油脂を用いて公知の製造方法で製造されたマーガリン
またはショートニングである。The present invention is a margarine or shortening produced by a known production method using the above-mentioned fat or oil for margarine shortening.
【0020】[0020]
【実施例】本願発明の詳細を実施例で説明する。本願発
明はこれら実施例によって何ら限定されるものではな
い。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in detail with reference to embodiments. The present invention is not limited by these examples.
【0021】実施例1 1,3位置特異性のないAlcaligenes s
p.由来珪藻土固定化リパーゼ剤〔名糖産業(株)「L
ipase QLC」〕を45℃に保ったカラムに充填
し、基質としてパーム油とナタネ油を3:1(重量比)
で混合した油脂をSV1.0で供給しエステル交換反応
を行った。エステル交換油は脱臭により精製した。Example 1 Alcaligenes s without 1,3-position specificity
p. Lipase agent immobilized from diatomaceous earth [Meito Sangyo Co., Ltd. "L
ipase QLC ”] in a column maintained at 45 ° C., and using palm oil and rapeseed oil as substrates in a ratio of 3: 1 (weight ratio).
The oils and fats mixed in the above were supplied at an SV of 1.0 to carry out a transesterification reaction. The transesterified oil was purified by deodorization.
【0022】比較例1 1,3位置特異性Rhizopus delemar由
来固定化リパーゼ剤〔天野製薬(株)「Lipase
D」〕を45℃に保ったカラムに充填し、実施例1と同
様にエステル交換し、脱臭した。Comparative Example 1 Immobilized lipase from Rhizopus delemar with 1,3-position specificity [Lipase, Amano Pharmaceutical Co., Ltd.
D "] was packed in a column maintained at 45 ° C, transesterified and deodorized in the same manner as in Example 1.
【0023】比較例2 パーム油とナタネ油を3:1(重量比)で混合し脱臭に
より精製した。Comparative Example 2 Palm oil and rapeseed oil were mixed at a ratio of 3: 1 (weight ratio) and purified by deodorization.
【0024】比較例3 パーム油とナタネ油を3:1(重量比)で混合した油脂
を触媒としてナトリウムメトキシド0.25%の存在下
で80℃、30分間反応してランダムエステル交換し
た。エステル交換油は水洗して触媒を除去し、脱色、脱
臭を行い精製した。COMPARATIVE EXAMPLE 3 Random transesterification was carried out by reacting palm oil and rapeseed oil at a mixing ratio of 3: 1 (weight ratio) at 80 ° C. for 30 minutes in the presence of 0.25% sodium methoxide as a catalyst. The transesterified oil was washed with water to remove the catalyst, decolorized and deodorized, and purified.
【0025】実施例1、比較例1〜3で得られた油脂の
脂肪酸組成を表1に、PPO/POPを表2に、トリパ
ルミチン含有率を表3に示す。The fatty acid compositions of the fats and oils obtained in Example 1 and Comparative Examples 1 to 3 are shown in Table 1, PPO / POP is shown in Table 2, and tripalmitin content is shown in Table 3.
【0026】[0026]
【表1】 C16 C18 C18:1 C18:2 C18:3 その他 ────────────────────────────────── 32.7 4.5 44.9 12.6 2.9 2.2 (%) ──────────────────────────────────[Table 1] C16 C18 C18: 1 C18: 2 C18: 3 Others ────────────────────────────────── 32.7 4.5 44.9 12.6 2.9 2.2 (%) ───────────────────────────── ─────
【0027】[0027]
【表2】 実施例1 比較例1 比較例2 比較例3 ────────────────────────────── PPO(%) 9.3 5.8 2.9 9.6 POP(%) 15.3 14.9 23.8 4.8 ────────────────────────────── PPO/POP 0.60 0.39 0.12 2.00 ──────────────────────────────Table 2 Example 1 Comparative Example 1 Comparative Example 2 Comparative Example 3 ────────────────────────────── PPO (%) 9.3 5.8 2.9 9.6 POP (%) 15.3 14.9 23.8 4.8 ────────────────────── ──────── PPO / POP 0.60 0.39 0.12 2.00 ─────────────────────────── ───
【0028】[0028]
【表3】 実施例1 比較例1 比較例2 比較例3 ─────────────────────────────────── トリパルミチン含有率(%) 3.8 3.1 4.2 3.5 ───────────────────────────────────[Table 3] Example 1 Comparative Example 1 Comparative Example 2 Comparative Example 3 ─ Tripalmitin content (%) 3.8 3.1 4.2 3.5 ────────────────────────────── ─────
【0029】実施例2 1,3位置特異性のない、Alcaligenes s
p.由来珪藻土固定化リパーゼ剤〔名糖産業(株)「L
ipase PLC」〕を45℃に保ったカラムに充填
し、基質としてパーム油とハイオレイックサフラワー油
を3:1(重量比)で混合した油をSV1.0供給しエ
ステル交換反応を行った。エステル交換油は脱臭により
精製した。Example 2 Alcaligenes s without 1,3-position specificity
p. Lipase agent immobilized from diatomaceous earth [Meito Sangyo Co., Ltd. "L
ipase PLC "] was packed in a column maintained at 45 ° C., and an oil obtained by mixing palm oil and high oleic safflower oil at a ratio of 3: 1 (weight ratio) as a substrate was supplied at an SV of 1.0 to perform a transesterification reaction. . The transesterified oil was purified by deodorization.
【0030】比較例4 1,3位置特異性のMucor miehei由来固定
化リパーゼ剤〔ノボ・ノルディスク「Lipozyme
IM60」〕を45℃に保ったカラムに充填し、実施
例2と同様にエステル交換し、脱臭した。Comparative Example 4 An immobilized lipase agent derived from Mucor miehei having 1,3-position specificity [Novo Nordisk "Lipozyme"
IM60 "] was packed in a column kept at 45 ° C, transesterified and deodorized in the same manner as in Example 2.
【0031】比較例5 パーム油とハイオレイックサフラワー油を3:1(重量
比)で混合し、脱臭により精製した。Comparative Example 5 Palm oil and high oleic safflower oil were mixed at a ratio of 3: 1 (weight ratio) and purified by deodorization.
【0032】実施例2、比較例4、5で得られた油脂の
脂肪酸組成を表4に、PPO/POPを表5に、トリパ
ルミチン含有率を表6に示す。Table 4 shows the fatty acid composition of the fats and oils obtained in Example 2, Comparative Examples 4 and 5, Table 5 shows PPO / POP, and Table 6 shows the tripalmitin content.
【0033】[0033]
【表4】 C16 C18 C18:1 C18:2 C18:3 その他 ────────────────────────────────── 32.4 4.3 49.4 10.8 0.5 2.6 (%) ──────────────────────────────────[Table 4] C16 C18 C18: 1 C18: 2 C18: 3 Others ────────────────────────────────── 32.4 4.3 49.4 10.8 0.5 2.6 (%) ───────────────────────────── ─────
【0034】[0034]
【表5】 実施例2 比較例4 比較例5 ─────────────────────── PPO(%) 11.6 3.2 3.0 POP(%) 12.5 20.8 24.3 ─────────────────────── PPO/POP 0.93 0.15 0.12 ───────────────────────Table 5 Example 2 Comparative Example 4 Comparative Example 5 @ PPO (%) 11.6 3.2 3.0 POP (%) 12.5 20.8 24.3 PPO / POP 0.93 0.15 0.12 ────────────────────
【0035】[0035]
【表6】 実施例2 比較例4 比較例5 ──────────────────────────────── トリパルミチン含有率(%) 3.3 2.6 3.5 ────────────────────────────────Table 6 Example 2 Comparative Example 4 Comparative Example 5 ト リ Tripalmitin content ( %) 3.3 2.6 3.5 ────────────────────────────────
【0036】試験例1 実施例1、比較例1、2、3を融解後急冷捏和機を用い
て窒素ガスを加えながら急冷・練り合わせを行い、ショ
ートニングを調製した。これを10℃、20℃に保ち粗
大結晶形成の有無をスライドガラス上に30μmの厚さ
に塗布し偏光顕微鏡で観察した。結果を表7に示す。Test Example 1 After melting Example 1 and Comparative Examples 1, 2, and 3, quenching and kneading were performed by using a quenching kneader while adding nitrogen gas to prepare a shortening. This was kept at 10 ° C. and 20 ° C., and the presence or absence of formation of coarse crystals was applied on a slide glass to a thickness of 30 μm and observed with a polarizing microscope. Table 7 shows the results.
【0037】[0037]
【表7】 〇:直径5μm以下の結晶が80%以上で、 直径50μm以上の粗大結晶はほとんどない。 △:直径50μm以上の粗大結晶がわずかに見られる。 ×:直径50μm以上の粗大結晶が50%以上見られる。[Table 7] 〇: 80% or more of crystals having a diameter of 5 μm or less, and almost no large crystals having a diameter of 50 μm or more. Δ: Coarse crystals having a diameter of 50 μm or more are slightly observed. ×: 50% or more of coarse crystals having a diameter of 50 μm or more are observed.
【0038】試験例2 実施例2、比較例4、5にモノグリセリド、レシチンを
加え融解後、水、食塩、脱脂粉乳を加えて予備乳化す
る。これを急冷捏和機で急冷・練り合わせを行いテンパ
リングしてマーガリンを調製した。これを5℃、10℃
に保ち、粗大結晶形成の有無を試験例1と同様に観察し
た。結果を表8に示す。Test Example 2 Monoglyceride and lecithin were added to Example 2, Comparative Examples 4 and 5, and after melting, water, salt, and skim milk were added to carry out preliminary emulsification. This was quenched and kneaded by a quenching kneader, and then tempered to prepare margarine. 5 ℃, 10 ℃
, And the formation of coarse crystals was observed in the same manner as in Test Example 1. Table 8 shows the results.
【0039】[0039]
【表8】 〇:直径5μm以下の結晶が80%以上で、 直径50μm以上の粗大結晶はほとんどない。 △:直径50μm以上の粗大結晶がわずかに見られる。 ×:直径50μm以上の粗大結晶が50%以上見られる。[Table 8] 〇: 80% or more of crystals having a diameter of 5 μm or less, and almost no large crystals having a diameter of 50 μm or more. Δ: Coarse crystals having a diameter of 50 μm or more are slightly observed. ×: 50% or more of coarse crystals having a diameter of 50 μm or more are observed.
【0040】[0040]
【発明の効果】パーム系油脂は常温で半固体ないし固体
であるために可塑性油脂原料として利用されているが、
マーガリン・ショートニング原料油脂にそれらを用いた
とき、製品の貯蔵中に粗大な粒子の結晶の発現が観察さ
れることがある。しかし、マーガリン・ショートニング
原料油脂にそれらパーム油を用いたとき、製品の貯蔵中
に粗大な粒子の結晶の発現が観察されることがある。こ
れは製品の物性を悪化させるとともに、食感にもザラツ
キを与え好ましくない。本発明によればこのパーム系油
脂の欠点である結晶粗大化が解消され、長期間に渡って
物性の安定したマーガリン・ショートニング用油脂を提
供することができる。本発明は上記マーガリン・ショー
トニング用油脂でできたマーガリンまたはショートニン
グを提供することができる。As described above, palm oils and fats are used as plastic oils and fats because they are semi-solid or solid at room temperature.
When they are used in margarine shortening feedstock fats, the appearance of coarse particle crystals during storage of the product may be observed. However, when these palm oils are used as a raw oil for margarine shortening, crystals of coarse particles may be observed during storage of the product. This undesirably deteriorates the physical properties of the product and gives a rough texture to the texture. According to the present invention, it is possible to provide a margarine and shortening fat or oil in which the crystal coarsening which is a drawback of the palm-based fat or oil is eliminated and physical properties are stable for a long period of time. The present invention can provide margarine or shortening made of the above margarine shortening fat.
Claims (3)
和脂肪酸28〜37重量%、モノ不飽和脂肪酸40〜5
0重量%の油脂組成物で、ジパルミトイルモノオレオイ
ルグリセリドの構成比率がPPO/POP≧0.5〔た
だし、PPOとはトリグリセリドを構成する3つの脂肪
酸のうち、1,2位(または2,3位)にパルミチン酸
が、3位(または1位)にオレイン酸が結合したものを
いい、POPとは1,3位にパルミチン酸、2位にオレ
イン酸が結合したものをいう。〕であり、1,3位特異
性でないリパーゼを用いてエステル交換することによっ
て得られたものであることを特徴とするマーガリン・シ
ョートニング用油脂。1. Saturated fatty acids 28 to 37% by weight derived from palm oil and vegetable liquid oil, monounsaturated fatty acids 40 to 5
In a fat composition of 0% by weight, the composition ratio of dipalmitoyl monooleoyl glyceride is PPO / POP ≧ 0.5 [provided that PPO is the first, second or third fatty acid among the three fatty acids constituting the triglyceride. Palmitic acid is bonded at the 3rd position (position 3) with oleic acid at the 3rd position (or 1st position), and POP is a compound having palmitic acid bonded at the 1st and 3rd positions and oleic acid bonded at the 2nd position. ] The oil and fat for margarine shortening obtained by transesterification using a lipase having no specificity at the 1,3-position.
aligenessp.由来のリパーゼである請求項1
のマーガリン・ショートニング用油脂。2. A lipase which is not 1,3-position specific is Alc
aligenes sp. 2. A lipase of origin.
Oil for margarine shortening.
トニング用油脂でできたマーガリンまたはショートニン
グ。3. A margarine or shortening made of the margarine shortening fat or oil according to claim 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP34290996A JP4497561B2 (en) | 1996-12-24 | 1996-12-24 | Fats and oils for margarine shortening and products made thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP34290996A JP4497561B2 (en) | 1996-12-24 | 1996-12-24 | Fats and oils for margarine shortening and products made thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH10183165A true JPH10183165A (en) | 1998-07-14 |
JP4497561B2 JP4497561B2 (en) | 2010-07-07 |
Family
ID=18357467
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Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP34290996A Expired - Fee Related JP4497561B2 (en) | 1996-12-24 | 1996-12-24 | Fats and oils for margarine shortening and products made thereof |
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JP (1) | JP4497561B2 (en) |
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JP2002180084A (en) * | 2000-12-15 | 2002-06-26 | Snow Brand Milk Prod Co Ltd | Oil and fat mixture or oil and fat composition not forming granular crystal |
WO2009150951A1 (en) * | 2008-06-09 | 2009-12-17 | 日清オイリオグループ株式会社 | Plastic fat composition |
JP2010130919A (en) * | 2008-12-02 | 2010-06-17 | Nisshin Oillio Group Ltd | Oil-and-fat composition |
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Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001072992A (en) * | 1999-09-06 | 2001-03-21 | Snow Brand Milk Prod Co Ltd | Preparation of fat or fat composition free from generation of granular crystal |
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