JPS60105686A - Method for modifying phospholipid - Google Patents
Method for modifying phospholipidInfo
- Publication number
- JPS60105686A JPS60105686A JP21335283A JP21335283A JPS60105686A JP S60105686 A JPS60105686 A JP S60105686A JP 21335283 A JP21335283 A JP 21335283A JP 21335283 A JP21335283 A JP 21335283A JP S60105686 A JPS60105686 A JP S60105686A
- Authority
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- Japan
- Prior art keywords
- phospholipid
- water
- hydrogenated
- hydrogenation
- added
- 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.)
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Links
Abstract
Description
【発明の詳細な説明】
本発明は、リン脂質あるいはリン脂質を含む油脂を水素
添加する際、白色で無臭の高品質の水素添加リン脂質委
るbはリン脂質を含む油脂の水素添加物を製造する方法
に関する。DETAILED DESCRIPTION OF THE INVENTION When hydrogenating phospholipids or fats and oils containing phospholipids, the present invention provides hydrogenated products of white, odorless, and high quality hydrogenated phospholipids. Relating to a method of manufacturing.
リン脂質、通称レシチンは、通常、植物または動物資源
から抽出にょシ得られ、その成分は、例エバ、ホスファ
チジル・コリン、ホスファチジル・エタノールアミン、
ホスファチジル・イノシトールなどのリン脂質混合物か
らなる。代表的なものに、卵黄レシチン、大豆レシチン
などが知られている。レシチンは、その構造上、親水・
親油性の官能基を同一分子内に持っため、両性界面活性
作用を持っており、食品、化粧品、医薬品1朶など様々
な用途に使用されている。例えば、パン、チョコレート
、マーガリンの老化防止剤、化粧品のなめらかさを増す
エモリエントとしてである。Phospholipids, commonly known as lecithin, are usually extracted from plant or animal sources, and their components include e.g. phosphatidylcholine, phosphatidylethanolamine,
It consists of a mixture of phospholipids such as phosphatidyl inositol. Representative examples include egg yolk lecithin and soybean lecithin. Due to its structure, lecithin is hydrophilic and
Because it has a lipophilic functional group in the same molecule, it has amphoteric surfactant action and is used in a variety of applications, including food, cosmetics, and pharmaceutical products. For example, as an anti-aging agent in bread, chocolate and margarine, and as a smoothing emollient in cosmetics.
ところが、このレシチンが使用される場合の添加量は、
大力が0.1〜0.3チ程度であり、1チ以上使用され
るのは希である。However, when this lecithin is used, the amount added is
The power is about 0.1 to 0.3 inches, and it is rare that more than 1 inch is used.
この原因は、一つには、レシチンを適用することにより
製品に黄〜褐色の色がつくこと、また、魚くさい臭い、
あるいは豆臭がするためであ°る。One of the reasons for this is that applying lecithin gives the product a yellow to brown color, and it also causes a fishy odor.
Or maybe it's because it smells like beans.
また他方、色や臭いのつかない低濃度の使用ですませた
場合でも、レシチンの不安定性のため劣化褐変しやすく
、與品には劣化するにつれ、着色やアミン臭の発生が起
こ、す、添加された製品が褐色がかシ、不快な臭いを発
するからである。この弊害は、食品よりはむしろ、ファ
イン・ケミカルである化粧品、医薬品製剤において影響
が顕著である。On the other hand, even when used at a low concentration that does not cause color or odor, the instability of lecithin causes deterioration and browning, and as the product deteriorates, coloration and amine odor may occur. This is because the product becomes brownish and gives off an unpleasant odor. This adverse effect is more noticeable in cosmetics and pharmaceutical preparations, which are fine chemicals, rather than in foods.
リン脂質の酸化は、−説には脂肪酸側鎖の不飽和部位が
、熱、光、金属、pHなどの影響を受けて自動酸化され
、pov、covが発生し、さらに1このカルボニール
基がアミノ基、主にホスファチジル・エタノールアミン
の一級アミノ基と縮重合を起こし、次第に重合、分解を
起こし、着色、臭気発生の原因となるとも考えられてい
る。The oxidation of phospholipids is based on the theory that unsaturated sites in fatty acid side chains are autooxidized under the influence of heat, light, metals, pH, etc., generating pov and cov, and furthermore, this carbonyl group becomes amino It is also thought that it causes condensation polymerization with groups, mainly the primary amino groups of phosphatidyl/ethanolamine, and gradually polymerizes and decomposes, causing coloration and odor generation.
この劣化、褐変現象を防止し、かつ、色、臭いのないレ
シチンとするために、色々な改質がなされているが、原
因となる不飽和部位を極力少なくするのが最も効果的で
あると考えられる。Various modifications have been made to prevent this deterioration and browning phenomenon and to make lecithin free of color and odor, but it is believed that the most effective method is to minimize the unsaturated sites that cause this phenomenon. Conceivable.
不飽和部位の還元、すなわち、水素添加反応がそれであ
る。この還元反応を行なった場合、生成物は天然に存在
するものであり、改質によって新たに合成物をつくって
しまう危険も全く発生しないきいえる。また、当然なが
ら色、臭りの除去も期待できる。以上のような水素添加
レシチンの製造については、すでに試みがある。This is the reduction of unsaturated sites, that is, the hydrogenation reaction. When this reduction reaction is performed, the product is a naturally occurring product, and there is no risk of creating a new synthetic product through modification. Naturally, it can also be expected to remove color and odor. Attempts have already been made to produce hydrogenated lecithin as described above.
一つは卵黄レシチンのアルコール中での還元である。こ
れは卵黄レシチンの同定のために水添されたもので、今
世紀初頭に行なわれた。One is the reduction of egg yolk lecithin in alcohol. This was hydrogenated to identify egg yolk lecithin, which was done in the early part of this century.
実際には、すでに赤茶色の中性脂質を含まないリン脂質
のみのレシチン2〜52をエタノールに溶かし、パラジ
ウムを触媒として水添している。In reality, lecithins 2 to 52, which are reddish-brown and contain only phospholipids and do not contain neutral lipids, are dissolved in ethanol and hydrogenated using palladium as a catalyst.
次に、大豆レシチン(中性脂質を含む)の例示みられる
。これは、レシチンをベンゼン、ヘキサン、エーテル、
あるいはこれらとアルコールとの混合溶媒に溶かし、白
金属触媒を添加し、温度25〜65C1水素圧1〜3に
57/cIIlテ水素添加を行な込、水素添加大豆レシ
チンを得ているものである。Next, there is an example of soybean lecithin (containing neutral lipids). This converts lecithin into benzene, hexane, ether,
Alternatively, hydrogenated soybean lecithin is obtained by dissolving it in a mixed solvent of these and alcohol, adding a platinum metal catalyst, and performing hydrogenation at a temperature of 25 to 65C and a hydrogen pressure of 1 to 3. .
しかしながら、以上述べた今までの方法には、次の短所
がみられる。However, the conventional methods described above have the following disadvantages.
それは、上記の方法では水素添加により、レシチンが原
料由来の赤色または褐色を呈したままという点である。The reason is that in the above method, due to hydrogenation, the lecithin retains its red or brown color derived from the raw material.
この欠点は、とくに大豆レシチンに多くみられ、また、
卵黄レシチンにおいても、リン脂質含有率が高くなるに
したがって赤色を強く帯びてしまうのである。This defect is particularly common in soybean lecithin, and
Even in egg yolk lecithin, as the phospholipid content increases, the color becomes more intensely red.
この原因は、大豆レシチンの場合、主に水素添加前のレ
シチンがすでに劣化しており、茶褐色を呈しているため
であり、また、卵黄レシチンにおいては、水素添加前の
レシチンは劣化していないが、水素添加時に50〜9o
cのリン脂質にとっては、過酷な温度で水素添加を行な
うために1水素添加中に劣化する七考見られる。The reason for this is that in the case of soybean lecithin, the lecithin before hydrogenation has already deteriorated and has a brownish color, and in the case of egg yolk lecithin, the lecithin before hydrogenation has not deteriorated, but , 50~9o during hydrogenation
For the phospholipids of C, there is a possibility that they deteriorate during hydrogenation because the hydrogenation is carried out at harsh temperatures.
これら赤褐色の水素添加レシチンでは、乳液やクリーム
など化粧品や医薬部外品に、一般的な添加a夏である1
〜5w/w%を添加し、保湿、潤滑剤として使用した場
合、製品が赤色味を帯び、外観、臭気について多くの問
題があり、消費者や鯛造者に低品質として受け取られ、
あまり好ましくない。These reddish-brown hydrogenated lecithins are commonly added to cosmetics and quasi-drugs such as emulsions and creams.
When ~5w/w% is added and used as a moisturizer or lubricant, the product takes on a reddish tinge, causing many problems with appearance and odor, and is perceived by consumers and sea bream producers as being of low quality.
I don't like it very much.
本発明者らは、上述のように水素添加して赤褐色となる
欠点を改良すべく鋭意研究の結果、水を用いることによ
って、全く思いかけずも白色の水素添加品を作ることに
成功し、本発明を完成するに至った。As a result of intensive research to improve the above-mentioned drawback of hydrogenation resulting in a reddish-brown color, the inventors of the present invention unexpectedly succeeded in creating a white hydrogenated product by using water. The present invention has now been completed.
以下、本発明について詳細に説明する。The present invention will be explained in detail below.
本発明は、リン脂質およびリン脂質を含む油脂を溶解す
る溶媒ないしは触媒に水を混合し水素添加する、白色の
水素添加リン脂質を製造する方法である。The present invention is a method for producing white hydrogenated phospholipids, in which water is mixed with a solvent or a catalyst that dissolves phospholipids and fats and oils containing phospholipids, and the mixture is hydrogenated.
原料リン脂質は、大豆レシチン、卵黄レシチン、コーン
レシチンなど、リン脂質を含む油脂ならばなんでもよい
。また、リン脂質の含有率についても、リン脂質2〜1
00 w/w%、中性脂質98〜Ow/w%の範囲であ
ればよいが、水の効果が顕著に発揮できるのは、リン脂
質50〜100 w/w%、中性脂質0〜50 w/w
%である。The raw material phospholipid may be any oil or fat containing phospholipid, such as soybean lecithin, egg yolk lecithin, and corn lecithin. In addition, regarding the content of phospholipids, phospholipids 2 to 1
00 w/w% and neutral lipids in the range of 98 to 0 w/w%, but the effect of water can be clearly demonstrated when phospholipids are in the range of 50 to 100 w/w% and neutral lipids are in the range of 0 to 50 w/w%. w/w
%.
リン脂質を溶解するにm−る溶媒は、メタノール、エタ
ノール、インプロピルアルコールなどアルコール類、ま
たは、これらとヘキサン、ベンゼンなどとの混合溶媒な
ど、水を溶解し、かつ、リン脂質、中性脂質を溶解する
溶媒ならば可能である。溶媒の量については、あまり影
響を受けないが、薄くても濃くても水添効率がよくなく
、好まし込濃度は10〜60w/w%である。Solvents for dissolving phospholipids include alcohols such as methanol, ethanol, and inpropyl alcohol, or mixed solvents of these with hexane, benzene, etc., which dissolve water and are suitable for phospholipids and neutral lipids. This is possible if the solvent dissolves the The amount of solvent is not affected much, but hydrogenation efficiency is not good whether it is thin or thick, and the preferred concentration is 10 to 60 w/w%.
また、水の添加率は、水素添加されるリン脂質に対して
5〜f 00 w/wチの範囲ならばよいが、より効果
的には10〜50w/w%である。Further, the addition rate of water may be in the range of 5 to f 00 w/w to the phospholipid to be hydrogenated, but is more effectively 10 to 50 w/w%.
実際の操作としては、リン脂質またはリン脂質を含む油
脂を、水を含む溶媒にて10〜60 w/wチに溶解す
る。これに、触媒Pdを脂質に対し0.1〜5 w 7
w %添加し、H1圧2に+7/cI/を以上にて水添
する。水添終了後、この溶液を濾過し、触媒を除いた後
、溶媒回収を行ない水素添加レシチンを得る。In actual operation, phospholipids or fats and oils containing phospholipids are dissolved at 10 to 60 w/w in a solvent containing water. To this, the catalyst Pd is added to the lipid at 0.1 to 5 w 7
w % and hydrogenated at H1 pressure 2 +7/cI/ or more. After the hydrogenation is completed, the solution is filtered to remove the catalyst, and the solvent is recovered to obtain hydrogenated lecithin.
このようにして得られた水素添加リン脂質を、安定性の
高い白色の水素添加リン脂質とするためには、ヨウ素価
401/100f以下であればよいが、ヨウ素価はあま
り白色度には影響せず、水の効果が大である。In order to make the hydrogenated phospholipid obtained in this way a highly stable white hydrogenated phospholipid, the iodine value should be 401/100f or less, but the iodine value does not have much effect on whiteness. The effect of water is great.
水の効果について理論的考察はなされてbないが、一つ
には、リン脂質の着色の原因であり、親水基であるコリ
ン基またはエタノールアミノ基の周漫に水が集まり、イ
オン部を水和するため、着色の進行を防ぐのではないか
と考えられた。Although there has been no theoretical consideration of the effect of water, one reason is that water gathers around the hydrophilic choline group or ethanolamino group, which is the cause of the coloration of phospholipids. It was thought that this would prevent the progress of discoloration.
以上により、得られる水素添加リン脂質は、以下の実施
例に示すごとく、白色に改質されていることがわかる。From the above, it can be seen that the hydrogenated phospholipid obtained is modified to have a white color, as shown in the examples below.
実施例1
卵黄レシチン(水分0.7%、リン脂質98.6 %、
ヨウ素価72f7100f、過酸化物価Omeq/に9
)2502に、水50fを添加したインプロパツール9
38−を加え、50Cで20分間攪拌溶解した。これに
、10%Pd−活性炭102を加え、2を容オートクレ
ーブに入れた。水素圧30ゆ/C!IG 、液温70〜
85Cにて120分間、水素添加を行なつfc(100
0rpm、タービン羽根式)。Example 1 Egg yolk lecithin (moisture 0.7%, phospholipids 98.6%,
Iodine value 72f7100f, peroxide value Omeq/9
)2502 with 50f of water added to Improper Tool 9
38- was added, and the mixture was stirred and dissolved at 50C for 20 minutes. To this, 10% Pd-activated carbon 102 was added, and 2 volumes were placed in an autoclave. Hydrogen pressure 30 Yu/C! IG, liquid temperature 70~
Hydrogenation was carried out at 85C for 120 minutes at fc (100
0 rpm, turbine blade type).
反応終了後、残水素ガスを大気中へ放出し、反応液に窒
素圧I J / all Gの加圧を行ない、加圧濾過
にて触媒を除いた。次いで、得られた清澄溶液を減圧濃
縮にて溶媒を回収した。溶融している某添物をトレーに
流し込み、室温まで冷却して固化させた。この固化水添
物を粉砕し、12メツシュパス品とした後、室温での真
空乾燥により溶媒を完全に除去し、白色の水素添加レシ
チンを得た。収量2371、水分1.1チ、リン脂質9
8.5%、ヨウ素価5f7100?であった。After the reaction was completed, residual hydrogen gas was released into the atmosphere, the reaction solution was pressurized to a nitrogen pressure of I J / all G, and the catalyst was removed by pressure filtration. Next, the resulting clear solution was concentrated under reduced pressure to recover the solvent. A certain molten additive was poured into a tray, cooled to room temperature, and solidified. This solidified hydrogenated product was pulverized into a 12-mesh pass product, and the solvent was completely removed by vacuum drying at room temperature to obtain a white hydrogenated lecithin. Yield 2371, moisture 1.1, phospholipid 9
8.5%, iodine value 5f7100? Met.
実施例2
卵黄レシチン(水分0.5%、リン脂質98.0 %、
ヨウ素価75 r/100 t、過酸化物価Omeq/
ゆ)250tに、水75−を添加したインプロパツール
938 mlを加え、50Cで20分間攪拌溶解した。Example 2 Egg yolk lecithin (moisture 0.5%, phospholipids 98.0%,
Iodine value 75 r/100 t, peroxide value Omeq/
938 ml of Improper Tool to which 75 ml of water had been added was added to 250 t of water, and the mixture was stirred and dissolved at 50 C for 20 minutes.
次いで、10チPd−活性炭7.51を加え、101容
オートクレーブに入れた。水素圧7 kg/ crl
G 。Then, 7.5 l of 10% Pd-activated carbon was added and placed in a 101 volume autoclave. Hydrogen pressure 7 kg/crl
G.
液温65〜75Cにて水素添加を行なった。攪拌はター
ビン羽根式で70 Orpmで行なった。反応終了後、
実施例1と全く同様の処理をし、水素添加レシチン23
02を得た。水分1.0%、リン脂質98.2倭、ヨウ
素価209”/j00fであった。Hydrogenation was performed at a liquid temperature of 65 to 75C. Stirring was performed using a turbine blade at 70 rpm. After the reaction is complete,
Hydrogenated lecithin 23 was treated in exactly the same manner as in Example 1.
I got 02. The water content was 1.0%, the phospholipid content was 98.2%, and the iodine value was 209''/j00f.
実施例3
卵黄レシチン(水分0.5 q6、リン脂質66.8
%、ヨウ素価759/100f、過C3化物価o me
q/kg)300fに、水150ゴを添加したインプロ
パノール696 mlを加え、50Cで20分間攪拌溶
解した。次いで、10%Pd−活性炭7.5fを加え、
10を容オートクレーブに入れた。水素圧10kg/d
、液温65〜75Cにて水素添加を行なった。Example 3 Egg yolk lecithin (moisture 0.5 q6, phospholipid 66.8
%, iodine value 759/100f, perc3ide value o me
q/kg) 300f was added with 696 ml of inpropanol to which 150 g of water was added, and the mixture was stirred and dissolved at 50 C for 20 minutes. Then, 7.5f of 10% Pd-activated carbon was added,
10 was placed in the autoclave. Hydrogen pressure 10kg/d
, hydrogenation was carried out at a liquid temperature of 65 to 75C.
攪拌はタービン羽根式で70 Orpmで行なった。Stirring was performed using a turbine blade at 70 rpm.
反応終了後、実施例1と全く同様の処理をし、水素添加
レシチン2822を得た。水分0.9%、すつた。After the reaction was completed, the same treatment as in Example 1 was carried out to obtain hydrogenated lecithin 2822. Water content: 0.9%.
実施例4
大豆レシチン(水分0.3%、リン脂質63.5 m、
ヨウ素価q2t71oay、過酸化物価1.8meq/
に9) 150 tに、水30−を添加したベンゼン、
エタノール(3:1)混合溶媒1000rnlに溶解し
た。次いで、10%Pd−活性炭11グを加え、2を容
オートクレーブに入れた。水素圧80kg/d1液温7
0〜85Uにて水素添加を行なった。Example 4 Soybean lecithin (moisture 0.3%, phospholipid 63.5 m,
Iodine value q2t71oay, peroxide value 1.8meq/
9) 150 t of benzene with 30 - of water added,
It was dissolved in 1000 rnl of ethanol (3:1) mixed solvent. Then, 11 g of 10% Pd-activated carbon was added and placed in a 2-volume autoclave. Hydrogen pressure 80kg/d1 Liquid temperature 7
Hydrogenation was performed at 0-85U.
攪拌はタービン羽根式で100 Orpmで行なった。Stirring was performed using a turbine blade at 100 rpm.
反応終了後、実施例1と同様の処理を行な−、水素添加
レシチン1302を得た。水分2.1%、リン脂質63
.8%、ヨウ素価3 meq / kgであった。After the reaction was completed, the same treatment as in Example 1 was carried out to obtain hydrogenated lecithin 1302. Moisture 2.1%, phospholipid 63
.. 8%, and the iodine value was 3 meq/kg.
実施例5〜9
高純度卵黄レシチン(水分0.5%、ヨウ素価72y
/ 100 f、リン月旨質98.0%)xoorに・
インプロパツール1125−を加え溶解する。次いで、
10%Pd−活性炭92に152の水を混合、湿潤させ
、レシチン溶解液と混合した後、水素添加装置へ移し、
水素圧7 kglcrl、 fi温65 ’Cの条件下
で、ヨウ素価20F/’100rとなるように水素を吸
収させた。また、同様にqy、s。Examples 5-9 High purity egg yolk lecithin (moisture 0.5%, iodine value 72y
/ 100 f, Linzuki quality 98.0%) to xoor・
Add Improper Tool 1125- and dissolve. Then,
152 water was mixed with 10% Pd-activated carbon 92 to moisten it, and after mixing with the lecithin solution, the mixture was transferred to a hydrogenation device.
Under the conditions of a hydrogen pressure of 7 kglcrl and a fi temperature of 65'C, hydrogen was absorbed to give an iodine value of 20F/'100r. Similarly, qy, s.
f、60 S+、150 fの水を添加したものについ
ても水素添加を行なった。水素添加後の溶液は、濾過に
て触媒を除き、エバポレーターにて溶媒回収を行なった
後、室温にて真空乾燥を行なった。Hydrogenation was also performed on the samples to which water was added at f, 60 S+, and 150 f. After hydrogenation, the catalyst was removed from the solution by filtration, the solvent was recovered by an evaporator, and then the solution was vacuum-dried at room temperature.
得られた水素添加品の色、吸光度の測定結果、および臭
いの測定結果は、表1のとおりであった。The color, absorbance measurement results, and odor measurement results of the obtained hydrogenated product are as shown in Table 1.
比較例1
実施例5〜9と同様に、水を添加しないものについて水
素添加を行なった。水素添加後の溶液は、濾過にて触媒
を除き、エバポレーターにて溶媒回収を行なった後、室
温にて真空乾燥を行なった。Comparative Example 1 Hydrogenation was performed in the same manner as Examples 5 to 9 without adding water. After hydrogenation, the catalyst was removed from the solution by filtration, the solvent was recovered by an evaporator, and then the solution was vacuum-dried at room temperature.
得られた水素添加品の色、吸光度の測定結果および臭い
の測定結果は、表1のとおシであった。The color, absorbance measurement results, and odor measurement results of the obtained hydrogenated product were as shown in Table 1.
表1 各水添加率の色、吸光度、臭いの測定結果※1
スガ試験機(株)製5M−3型カラーコンピュータにて
60メツシュバス品を測定
*2 水素添加レシチン12をクロロホルムに溶かし2
5−として吸光度を測定
実施例10〜14
高純度卵黄レシチン(水分0.6チ、リン脂質98.6
%)100グに、水501を添加したメタノール・水混
合溶媒500tntを加え溶解する。次いで、10%P
d−活性炭52をレシチン溶解液と混合した後、水素添
加装置へ移し、水素圧80kli+/(mで、ヨウ素価
5r/100f以下をめざして水素添加を行なった。ま
た、同様に1002.1502.2001.300fを
添加したものについても水素添加を行なった。水素添加
後の溶液から濾過にて触媒を除き、エバポレーターにて
溶媒回収を行なった。Table 1 Color, absorbance, and odor measurement results for each water addition rate *1
Measurement of 60 mesh bath products using a 5M-3 color computer manufactured by Suga Test Instruments Co., Ltd. *2 Dissolve hydrogenated lecithin 12 in chloroform 2
Measurement of absorbance as 5-Examples 10 to 14 Highly purified egg yolk lecithin (moisture 0.6%, phospholipid 98.6%)
%) and 500 tnt of a mixed solvent of methanol and water to which 501 g of water was added and dissolved. Then 10% P
After mixing the d-activated carbon 52 with the lecithin solution, it was transferred to a hydrogenation device and hydrogenated at a hydrogen pressure of 80kli+/(m) aiming at an iodine value of 5r/100f or less.Also, 1002.1502. Hydrogenation was also performed on the solution to which 2001.300f had been added.The catalyst was removed from the solution after hydrogenation by filtration, and the solvent was recovered using an evaporator.
得られた水素添加品の色、吸光度の測置結果および臭い
の結果は、表2のとおりであった。The color, absorbance measurement results, and odor results of the obtained hydrogenated product are as shown in Table 2.
比較例2
実施例10〜14と同様に、水を添加しないものについ
て水素添〃口を行なった。水素添加後の溶液は、濾過に
て触媒を除き、エバポレーターにて溶媒回収を行なった
後、室温にて真空乾燥を行なった。Comparative Example 2 Hydrogenation was performed in the same manner as Examples 10 to 14 without adding water. After hydrogenation, the catalyst was removed from the solution by filtration, the solvent was recovered by an evaporator, and then the solution was vacuum-dried at room temperature.
得られた水素添加品の色、吸光度の測定結果および臭い
の測定結果は、表2のとおりであった。The color, absorbance measurement results, and odor measurement results of the obtained hydrogenated product are as shown in Table 2.
表 2 各水添加率の色、吸光度と臭いの測定結果*1
スガ試験機(株)製5M−3型カラーコンピュータに
て60メツシュバス品を測定
※2 水素添加レシチン12をクロロホルムに浴かし2
5ゴとして吸光度を61り定
水の添加150%以上では、ヨウ素価5まで吸水素不可
であった。Table 2 Color, absorbance and odor measurement results for each water addition rate*1
Measurement of 60 mesh bath products using a 5M-3 color computer manufactured by Suga Test Instruments Co., Ltd. *2 Hydrogenated lecithin 12 was soaked in chloroform 2
When the absorbance was 61 and the addition of constant water was 150% or more, hydrogen absorption up to an iodine value of 5 was not possible.
Claims (1)
に水素添加することを特徴とするリン脂質の改質方法。A method for modifying phospholipids, which comprises hydrogenating fats and oils containing b#'i phospholipids in the presence of water.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21335283A JPS60105686A (en) | 1983-11-15 | 1983-11-15 | Method for modifying phospholipid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21335283A JPS60105686A (en) | 1983-11-15 | 1983-11-15 | Method for modifying phospholipid |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60105686A true JPS60105686A (en) | 1985-06-11 |
JPS628439B2 JPS628439B2 (en) | 1987-02-23 |
Family
ID=16637737
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP21335283A Granted JPS60105686A (en) | 1983-11-15 | 1983-11-15 | Method for modifying phospholipid |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60105686A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000247987A (en) * | 1998-12-28 | 2000-09-12 | Ymc Co Ltd | Highly hydrogenated lecithin |
-
1983
- 1983-11-15 JP JP21335283A patent/JPS60105686A/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000247987A (en) * | 1998-12-28 | 2000-09-12 | Ymc Co Ltd | Highly hydrogenated lecithin |
Also Published As
Publication number | Publication date |
---|---|
JPS628439B2 (en) | 1987-02-23 |
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