JPS626558B2 - - Google Patents
Info
- Publication number
- JPS626558B2 JPS626558B2 JP53101365A JP10136578A JPS626558B2 JP S626558 B2 JPS626558 B2 JP S626558B2 JP 53101365 A JP53101365 A JP 53101365A JP 10136578 A JP10136578 A JP 10136578A JP S626558 B2 JPS626558 B2 JP S626558B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- polar
- lipids
- mixture
- phase
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 150000002632 lipids Chemical class 0.000 claims description 39
- 239000000203 mixture Substances 0.000 claims description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 26
- 235000013339 cereals Nutrition 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 4
- 239000012071 phase Substances 0.000 description 21
- 235000008429 bread Nutrition 0.000 description 12
- 235000013312 flour Nutrition 0.000 description 8
- 241000209140 Triticum Species 0.000 description 6
- 235000021307 Triticum Nutrition 0.000 description 6
- 230000005484 gravity Effects 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical group CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 3
- -1 diglycerides Chemical class 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000003995 emulsifying agent Substances 0.000 description 3
- 238000011049 filling Methods 0.000 description 3
- 235000013305 food Nutrition 0.000 description 3
- 238000002955 isolation Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000007792 addition Methods 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- MWKFXSUHUHTGQN-UHFFFAOYSA-N decan-1-ol Chemical compound CCCCCCCCCCO MWKFXSUHUHTGQN-UHFFFAOYSA-N 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 150000003904 phospholipids Chemical class 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 150000003626 triacylglycerols Chemical class 0.000 description 2
- 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
- 235000007319 Avena orientalis Nutrition 0.000 description 1
- 244000075850 Avena orientalis Species 0.000 description 1
- JIEJACFVMGPCON-UHFFFAOYSA-N CCCCCCCCCCCCCCCCCCCC(C(=O)C(C)O)(C(=O)O)O Chemical class CCCCCCCCCCCCCCCCCCCC(C(=O)C(C)O)(C(=O)O)O JIEJACFVMGPCON-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 108010068370 Glutens Proteins 0.000 description 1
- 240000005979 Hordeum vulgare Species 0.000 description 1
- 235000007340 Hordeum vulgare Nutrition 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 229930182558 Sterol Natural products 0.000 description 1
- 235000019714 Triticale Nutrition 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 229910001508 alkali metal halide Inorganic materials 0.000 description 1
- 239000008346 aqueous phase Substances 0.000 description 1
- OGBUMNBNEWYMNJ-UHFFFAOYSA-N batilol Chemical class CCCCCCCCCCCCCCCCCCOCC(O)CO OGBUMNBNEWYMNJ-UHFFFAOYSA-N 0.000 description 1
- ASGJEMPQQVNTGO-UHFFFAOYSA-N benzene chloroform Chemical compound C(Cl)(Cl)Cl.C1=CC=CC=C1.C1=CC=CC=C1 ASGJEMPQQVNTGO-UHFFFAOYSA-N 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- IDGUHHHQCWSQLU-UHFFFAOYSA-N ethanol;hydrate Chemical compound O.CCO IDGUHHHQCWSQLU-UHFFFAOYSA-N 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000002778 food additive Substances 0.000 description 1
- 235000013373 food additive Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000008240 homogeneous mixture Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 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
- 239000004973 liquid crystal related substance Substances 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- YNOVLNPSBVENJC-UHFFFAOYSA-M sodium 2-hydroxy-2-(2-hydroxypropanoyl)henicosanoate Chemical compound C(CCCCCCCCCCCCCCCCC)CC(C(=O)[O-])(O)C(C(O)C)=O.[Na+] YNOVLNPSBVENJC-UHFFFAOYSA-M 0.000 description 1
- 229960005480 sodium caprylate Drugs 0.000 description 1
- BYKRNSHANADUFY-UHFFFAOYSA-M sodium octanoate Chemical compound [Na+].CCCCCCCC([O-])=O BYKRNSHANADUFY-UHFFFAOYSA-M 0.000 description 1
- 238000010561 standard procedure Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 235000003702 sterols Nutrition 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 150000003899 tartaric acid esters Chemical class 0.000 description 1
- 238000004809 thin layer chromatography Methods 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
- 229940100445 wheat starch Drugs 0.000 description 1
- 241000228158 x Triticosecale Species 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B7/00—Separation of mixtures of fats or fatty oils into their constituents, e.g. saturated oils from unsaturated oils
-
- A—HUMAN NECESSITIES
- A21—BAKING; EDIBLE DOUGHS
- A21D—TREATMENT OF FLOUR OR DOUGH FOR BAKING, e.g. BY ADDITION OF MATERIALS; BAKING; BAKERY PRODUCTS
- A21D2/00—Treatment of flour or dough by adding materials thereto before or during baking
- A21D2/08—Treatment of flour or dough by adding materials thereto before or during baking by adding organic substances
- A21D2/14—Organic oxygen compounds
- A21D2/16—Fatty acid esters
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Food Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Bakery Products And Manufacturing Methods Therefor (AREA)
- Compounds Of Unknown Constitution (AREA)
- Fats And Perfumes (AREA)
- Cereal-Derived Products (AREA)
Description
本発明は極性および非極性穀類リピド混合物か
ら極性穀類リピドを単離する方法に関する。本発
明において使用される極性および非極性リピド混
合物は穀類から既知の方法を使用して回収可能な
リピド混合物である。すなわち、小麦は約2%の
リピドを含有し、その約半分はホスホリピドおよ
びガラクトリピドのような極性リピドであるが、
その他の半分は非極性であり主としてトリグリセ
ライドである。これらのリピドは、例えば、小麦
粉を有機溶媒で抽出するか、あるいは小麦粉−水
混合物を遠心分離することにより回収されること
ができる。有効な抽出剤は水で飽和されたブタノ
ールであり、これはリピドを小麦粉から約80%ま
で放出させる能力がある。その他の有用な抽出剤
はクロロホルム、1:1の比のベンゼン−クロロ
ホルム混合物、エタノール、水含量が90%までの
エタノール−水混合物および2:2:1の比のエ
タノール−ジエチルエーテル−水混合物である。
小麦殿粉の製造に際しては水溶性蛋白質の残分、
グルテンおよびリピドが得られる。この残分から
リピドが抽出により単離されうる。本発明の出発
物質として有用なリピド混合物を提供しうるその
他の穀類はライムギ、トリチケール(triticale)
(小麦とライムギとの雑種)、大麦、カラスムギお
よびとうもろこしである。
本発明によつて得られる極性リピド生成物は主
として食品添加物として使用されることが意図さ
れる。さらに前記生成物は現在パン焼き(ベーキ
ング)の際に使用されている乳化剤、例えばステ
アリル−ラクチル−ラクテート塩、酒石酸エステ
ルおよびモノグリセライドの代用として有利に使
用されることができる。それらはパンに対して改
良された穀類芳香および増大した容積ならびに改
良されたきめ(肌目)および保存性を与える。極
性の穀類リピドのパン焼きにおけるすぐれた効果
はすでに例えばマツク・リツチー((Mac
Ritchie)氏の報文「J.Sci.Fd Agric.第28巻
(1977年)第53〜58頁〕の記載により知られい
る。その他の用途は殿粉ベースの食品例えばペー
スト、マツシユポテト、粥用の添加物としての用
途であり、その際前記生成物は該食品に対して、
よりぽろぽろしたきめを与える。本発明は全抽出
物から非極性リピドを除去することに関する。こ
れは非極性リピドが前述の本発明による生成物の
所望の効果に対して反対に作用するからである。
従つて極性リピドの単離は該極性リピドが最高25
重量%の非極性リピドを含有する程度に有効であ
るのが望ましい。
本発明による方法は前述のリピド混合物を水と
リピド−水混合物が少なくとも50重量%の水を含
有するような量で混合し、その後該混合物を重力
分離に付し、極性リピドの主割合を含有する前記
の重力分離によつて得られる最も重い油状相を最
後に分離することを特徴とする。
本発明によれば、水好ましくは蒸留水は前記の
リピド混合物にリピド−水混合物が少なくとも50
重量%の水を含有するような量で添加される。本
発明によれば70重量%の水が適当な水含量である
ことが見出された。水含量が80重量%をこえる場
合には、得られる混合物の容積が重力分離におい
て困難をきたすほど大きくなるであろう。この混
合物の温度は前記の所望の相が取扱いに適当なコ
ンシステンシーを有するように25℃以上に保持さ
れるのが好ましい。しかしながら、脂肪の酸化を
防止するために温度は50℃以下であるのが好まし
い。相平衡は3〜6時間後に達成される。混合物
は次に重力分離、好ましくは遠心分離機中におけ
る重力分離に付される。遠心分離は水性相によつ
て分離された2つの油状相が形成されるまで続け
られる。少なくとも5000gにおいて遠心分離を行
なうのが好ましく、この場合各相を完全に分離す
るのに約1〜2時間を要する。前記分離機の速度
が10000gに高められる場合には完全な相分離は
約20〜30分間で行なわれうる。最上位の最も軽い
相はほとんどすべて非極性リピド、主としてトリ
グリセライドからなるが少量の脂肪酸、ジグリセ
ライドおよびステロールエステルをも含有する油
である。この相の下に純粋な水相がある。最下位
の最も重い相が所望の極性リピドを含有する淡黄
色に着色した油状相である。本発明によれば、薄
層クロマトグラフイーによりこの相は主としてガ
ラクトリピド(主としてジガラクトジグリセライ
ドおよび少量のモノガラクトジグリセライド)お
よびレシチンおよびリゾラシチンのようなホスホ
リピドからなることが見出された。驚くべきこと
に、この相は添加された水の量に応じて高い水含
量すなわち約50〜70重量%の水を含有することが
見出された。この事実にもかかわらず、前記の相
は水と混和しない。
上記の重い油状相はいわゆるL2−相中の薄板
状液晶相の分散物からなる。L2−相はすでにナ
トリウムカプリレート/デカノール/水のような
単純系において広汎に研究されており、そしてし
ばしば連続炭化水素環境中の水分子アグレゲート
を伴なつた反転ミセル状態として記載される。
極性リピドを含有する前記油状相中の非極性リ
ピドの含量は前記リピド抽出物中に添加される塩
が水に添加される場合には若干(例えば25〜10重
量%)減少せしめられることができる。前述のよ
うな水の塩含量は0.4〜4重量%が適当であり、
前記塩はアルカリ金属のハロゲン塩が適当であ
る。
実施例
この例は小麦粉からのリピド混合物の調製、極
性リピドの単離およびパン焼きにおける極性リピ
ドの使用に関する。
A 小麦粉からのリピドの調製
小麦粉10Kgをミキサー中水で飽和されたブタノ
ール40Kgと混合した。ミキサーは2時間作動させ
た。混合物の温度は20〜25℃であつた。前記混合
物を遠心分離機に移し、1800gにおいて1時間遠
心分離した。この時間の後約35の液体が得られ
た。この液体を50℃で加熱することにより蒸発さ
せ、約160gの重量の乾燥した残留物が得られ
た。食品に対する用途においては、前記液体混合
物中に有機溶媒が残留しないように蒸発が完全で
あることが重要である。
B 極性リピドの単離
前記の工程Aにより調製される種類のリピド混
合物300gを蒸留水700gと混合し、明らかに均質
な混合物が得られるまで撹拌した。この混合物を
4時間30℃において撹拌することなしに放置し
た。次に遠心分離に移し、5000gにおいて1時間
遠心分離した。水層で互いに分離された2つの抽
状相が得られた。最も重い油状相を分離した。こ
の油状相は容積が750mlであり、かつ70%の水含
量を有することが見出された。
C パン焼き
パン焼き実験はスウエーデイツシユ・シード・
アソシエーシヨン(スウエーデン)により規定さ
れた標準方法に従つて行なわれた。小麦粉はスウ
エーデンの製粉会社Kungso¨rnenにより製造され
たいわゆる製パン用混合物であつた。使用された
発酵およびベーキングオーブンは英国シモンズ社
製のものであつた。前記工程Bにより生成された
極性小麦リピドを前述の小麦粉の量の0.83重量%
の量に添加した。比較のために、ペンを(1)同様に
多量のナトリウムステアリル−ラクチル−ラクテ
ートを添加して、そして(2)その他の追加の乳化剤
の添加物なしに焼いた。次のような結果が得られ
た。表中、多孔性は1〜8の等級で表わされる
が、この際最も高い数値は微細多孔性を示す。パ
ンの中味すなわちパンの内側の柔らかい部分の弾
力性は1〜6の等級で表わされるが、6は弾力性
が極めてよいことを示す。パンの外観は1〜4の
等級であらわされるが、1が最もよい値であり申
し分のない外観であることを示す。
The present invention relates to a method for isolating polar cereal lipids from a mixture of polar and non-polar cereal lipids. The polar and non-polar lipid mixture used in the present invention is a lipid mixture that can be recovered from cereals using known methods. That is, wheat contains about 2% lipids, about half of which are polar lipids such as phospholipids and galactolipids;
The other half is nonpolar and primarily triglycerides. These lipids can be recovered, for example, by extracting the flour with an organic solvent or by centrifuging the flour-water mixture. An effective extractant is water-saturated butanol, which is capable of releasing up to about 80% of lipids from flour. Other useful extractants are chloroform, benzene-chloroform mixtures in a 1:1 ratio, ethanol, ethanol-water mixtures with a water content up to 90% and ethanol-diethyl ether-water mixtures in a 2:2:1 ratio. be.
When producing wheat starch, the remainder of water-soluble protein,
Gluten and lipids are obtained. Lipids can be isolated from this residue by extraction. Other grains that may provide lipid mixtures useful as starting materials for the present invention include rye, triticale,
(a hybrid of wheat and rye), barley, oats and corn. The polar lipid products obtained according to the invention are primarily intended for use as food additives. Furthermore, the products can advantageously be used as a substitute for the emulsifiers currently used in baking, such as stearyl-lactyl-lactate salts, tartaric acid esters and monoglycerides. They impart improved grain aroma and increased volume to bread as well as improved texture and shelf life. The excellent effects of polar cereal lipids in bread baking have already been demonstrated, for example by Mac
Ritchie, J.Sci.Fd Agric., Vol. 28 (1977), pp. 53-58. use as an additive for the food, in which case the product is used as an additive for the food;
Gives a more crumbly texture. The present invention relates to the removal of non-polar lipids from total extracts. This is because non-polar lipids act counter to the desired effects of the products according to the invention mentioned above.
Therefore, isolation of polar lipids is possible when the polar lipids are up to 25
It is desirable to be effective to the extent that it contains % by weight of non-polar lipids. The method according to the invention comprises mixing the aforementioned lipid mixture with water in an amount such that the lipid-water mixture contains at least 50% by weight of water, and then subjecting the mixture to gravity separation, which contains the main proportion of polar lipids. The heaviest oily phase obtained by said gravity separation is separated last. According to the invention, water, preferably distilled water, is added to said lipid mixture so that at least 50% of the lipid-water mixture is added to said lipid mixture.
It is added in such an amount that it contains % water by weight. According to the present invention, 70% water by weight has been found to be a suitable water content. If the water content exceeds 80% by weight, the volume of the resulting mixture will be large enough to make gravity separation difficult. Preferably, the temperature of the mixture is maintained above 25°C so that the desired phase has a suitable consistency for handling. However, it is preferred that the temperature is below 50°C to prevent oxidation of the fat. Phase equilibrium is achieved after 3-6 hours. The mixture is then subjected to gravity separation, preferably in a centrifuge. Centrifugation is continued until two oily phases are formed separated by an aqueous phase. Centrifugation is preferably carried out at at least 5000 g, in which case it takes about 1 to 2 hours to completely separate the phases. If the speed of the separator is increased to 10,000 g, complete phase separation can be achieved in about 20-30 minutes. The topmost, lightest phase is an oil consisting almost entirely of nonpolar lipids, primarily triglycerides, but also containing small amounts of fatty acids, diglycerides, and sterol esters. Beneath this phase is a pure water phase. The lowest, heaviest phase is a light yellow colored oily phase containing the desired polar lipids. According to the invention, it was found by thin layer chromatography that this phase consists primarily of galactolipids (mainly digalactodiglyceride and small amounts of monogalactodiglyceride) and phospholipids such as lecithin and lysolacitin. Surprisingly, it was found that this phase contains a high water content, ie about 50-70% by weight of water, depending on the amount of water added. Despite this fact, said phases are immiscible with water. The heavy oily phase mentioned above consists of a dispersion of lamellar liquid crystal phases in the so-called L2-phase. The L2-phase has already been extensively studied in simple systems such as sodium caprylate/decanol/water and is often described as an inverted micellar state with aggregates of water molecules in a continuous hydrocarbon environment. The content of non-polar lipids in the oily phase containing polar lipids can be reduced slightly (e.g. 25-10% by weight) if the salt added in the lipid extract is added to the water. . The appropriate salt content of water as mentioned above is 0.4 to 4% by weight,
The salt is suitably an alkali metal halide salt. EXAMPLE This example relates to the preparation of a lipid mixture from flour, the isolation of polar lipids and the use of polar lipids in bread baking. A. Preparation of lipids from wheat flour 10Kg of flour was mixed with 40Kg of butanol saturated with water in a mixer. The mixer was run for 2 hours. The temperature of the mixture was 20-25°C. The mixture was transferred to a centrifuge and centrifuged at 1800g for 1 hour. Approximately 35 g of liquid was obtained after this time. This liquid was evaporated by heating at 50° C., yielding a dry residue weighing approximately 160 g. In food applications, it is important that evaporation is complete so that no organic solvent remains in the liquid mixture. B. Isolation of polar lipids 300 g of a lipid mixture of the type prepared according to step A above were mixed with 700 g of distilled water and stirred until an apparently homogeneous mixture was obtained. The mixture was left at 30° C. for 4 hours without stirring. It was then transferred to a centrifuge and centrifuged at 5000g for 1 hour. Two extracted phases were obtained, separated from each other by an aqueous layer. The heaviest oily phase was separated. This oily phase was found to have a volume of 750 ml and a water content of 70%. C. Bread Baking Bread baking experiments are done using Swedish Date Seeds.
It was carried out according to the standard method specified by the Association (Sweden). The flour was a so-called bread mix produced by the Swedish flour milling company Kungso¨rnen. The fermentation and baking oven used was manufactured by Simmons, UK. The polar wheat lipids produced in step B were added to 0.83% by weight of the amount of flour mentioned above.
amount was added. For comparison, pens were baked (1) with the same amount of sodium stearyl-lactyl-lactate added and (2) without any other additional emulsifier additions. The following results were obtained. In the table, porosity is expressed on a scale of 1 to 8, with the highest value indicating microporosity. The elasticity of the inside of the bread, that is, the soft inner part of the bread, is expressed on a scale of 1 to 6, with 6 indicating extremely good elasticity. The appearance of bread is expressed on a scale of 1 to 4, with 1 being the best value and indicating perfect appearance.
【表】
さらにパンの中味のきめおよび焼き上つたパン
の味は極性小麦リピドを含有するベーキングバツ
チにおいてよりすぐれていることがわかつた。慣
用の乳化剤の添加がパンの中味の弾力性を低下さ
せることは周知であるが、これは本発明の上記の
比較実験により非常に明瞭に証明された。極性小
麦リピドは前記のような悪い効果は何も与えず、
パンの中味のよりすぐれた弾力性を与えた。[Table] Furthermore, it was found that the texture of the bread filling and the taste of the finished bread were better in the baking batches containing polar wheat lipids. It is well known that the addition of conventional emulsifiers reduces the elasticity of the bread filling, and this was very clearly demonstrated by the above comparative experiments of the present invention. Polar wheat lipids do not have any of the negative effects mentioned above,
It gave better elasticity to the bread filling.
Claims (1)
該リピド−水混合物が少なくとも50重量%の水を
含有するような量で混合し、この混合物を重力分
離に付しそして重力分離によつて得られる極性リ
ピドの主要部分を含有する、前記最も重い油状相
を分離することからなる、極性および非極性穀類
リピド混合物から極性リピドを単離する方法。1 Polar and non-polar cereal lipid mixture with water;
mixed in such an amount that the lipid-water mixture contains at least 50 wt. A method for isolating polar lipids from a mixture of polar and non-polar cereal lipids, comprising separating the oily phase.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SE7709374A SE417441B (en) | 1977-08-19 | 1977-08-19 | PROCEDURE FOR INSULATING POLERA LIPIDES FROM A MIXTURE OF POLERA AND OPOLERA CEREALICLIPIDES BY MIXING WITH THE WATER AND THEIR FOLLOWING Gravity Separation |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5452003A JPS5452003A (en) | 1979-04-24 |
| JPS626558B2 true JPS626558B2 (en) | 1987-02-12 |
Family
ID=20332052
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10136578A Granted JPS5452003A (en) | 1977-08-19 | 1978-08-18 | Method of isolating polar lipid from grain lipid mixture |
Country Status (7)
| Country | Link |
|---|---|
| JP (1) | JPS5452003A (en) |
| AU (1) | AU522378B2 (en) |
| CA (1) | CA1102795A (en) |
| DE (1) | DE2834999A1 (en) |
| FI (1) | FI782477A7 (en) |
| FR (1) | FR2400552A1 (en) |
| SE (1) | SE417441B (en) |
Families Citing this family (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2676936B1 (en) * | 1991-05-27 | 1993-11-05 | Inocosm Laboratoires | PROCESS FOR SEPARATING A COMPOUND RICH IN GLYCOLIPIDES LYSOPHOSPHOLIPIDES SHINGOLIPIDES AND CERAMIDES OF PLANT ORIGIN, AS WELL AS COSMETIC PRODUCTS OBTAINED BY THE IMPLEMENTATION OF THIS PROCESS. |
| US5928696A (en) * | 1994-08-16 | 1999-07-27 | Dr. Frische Gmbh | Process for extracting native products which are not water-soluble from native substance mixtures by centrifugal force |
| WO1997010050A1 (en) * | 1995-09-14 | 1997-03-20 | Unilever N.V. | Surface-active composition |
| FR2836335B1 (en) * | 2002-02-27 | 2004-12-03 | Intersnack Knabber Geback Gmbh | STARCH-BASED DEHYDRATED FLAKES COMPRISING 0.05% GLYCOLIPIDE (S) |
| US7226771B2 (en) | 2002-04-19 | 2007-06-05 | Diversa Corporation | Phospholipases, nucleic acids encoding them and methods for making and using them |
| PT1497418E (en) | 2002-04-19 | 2013-01-25 | Dsm Ip Assets Bv | Phospholipases, nucleic acids encoding them and methods for making and using them |
| CA3007908A1 (en) | 2003-03-07 | 2005-04-14 | Dsm Ip Assets B.V. | Hydrolases, nucleic acids encoding them and methods for making and using them |
| US20080070291A1 (en) | 2004-06-16 | 2008-03-20 | David Lam | Compositions and Methods for Enzymatic Decolorization of Chlorophyll |
| AU2005264938B2 (en) | 2004-06-16 | 2011-11-24 | Verenium Corporation | Compositions and methods for enzymatic decolorization of chlorophyll |
| EP1987142A4 (en) | 2006-02-02 | 2009-07-15 | Verenium Corp | Esterases and related nucleic acids and methods |
| EP2057274B1 (en) | 2006-09-21 | 2013-12-11 | DSM IP Assets B.V. | Phospholipases, nucleic acids encoding them and methods for making and using them |
| WO2010104444A1 (en) | 2009-03-11 | 2010-09-16 | Swedish Oat Fiber Ab | Method for separating neutral and polar lipids and an oil rich in polar lipids |
| UA109884C2 (en) | 2009-10-16 | 2015-10-26 | A POLYPEPTIDE THAT HAS THE ACTIVITY OF THE PHOSPHATIDYLINOSYTOL-SPECIFIC PHOSPHOLIPASE C, NUCLEIC ACID, AND METHOD OF METHOD | |
| UA111708C2 (en) | 2009-10-16 | 2016-06-10 | Бандж Ойлз, Інк. | METHOD OF OIL REFINING |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR1469392A (en) * | 1965-02-20 | 1967-02-10 | Inst Przemyslu Tluszczowego | Continuous process for the degumming of vegetable oils and for the production of lecithin from the phosphatide sludge obtained, and device for implementing this process |
| DE1923971B1 (en) * | 1969-05-10 | 1970-11-26 | Heinz Schumacher | Method and device for degumming vegetable oils |
-
1977
- 1977-08-19 SE SE7709374A patent/SE417441B/en not_active IP Right Cessation
-
1978
- 1978-08-04 AU AU38631/78A patent/AU522378B2/en not_active Expired
- 1978-08-10 DE DE19782834999 patent/DE2834999A1/en active Granted
- 1978-08-14 FI FI782477A patent/FI782477A7/en unknown
- 1978-08-14 CA CA309,300A patent/CA1102795A/en not_active Expired
- 1978-08-17 FR FR7824047A patent/FR2400552A1/en active Granted
- 1978-08-18 JP JP10136578A patent/JPS5452003A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| FI782477A7 (en) | 1979-02-20 |
| SE7709374L (en) | 1979-02-20 |
| AU3863178A (en) | 1980-02-07 |
| FR2400552A1 (en) | 1979-03-16 |
| CA1102795A (en) | 1981-06-09 |
| FR2400552B1 (en) | 1983-08-05 |
| AU522378B2 (en) | 1982-06-03 |
| JPS5452003A (en) | 1979-04-24 |
| DE2834999A1 (en) | 1979-03-01 |
| DE2834999C2 (en) | 1989-04-20 |
| SE417441B (en) | 1981-03-16 |
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