Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS5822078B2 - Advanced refining method for wool wax - Google Patents
[go: Go Back, main page]

JPS5822078B2 - Advanced refining method for wool wax - Google Patents

Advanced refining method for wool wax

Info

Publication number
JPS5822078B2
JPS5822078B2 JP8986179A JP8986179A JPS5822078B2 JP S5822078 B2 JPS5822078 B2 JP S5822078B2 JP 8986179 A JP8986179 A JP 8986179A JP 8986179 A JP8986179 A JP 8986179A JP S5822078 B2 JPS5822078 B2 JP S5822078B2
Authority
JP
Japan
Prior art keywords
exchange resin
wool wax
solution
wool
ion exchange
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
Application number
JP8986179A
Other languages
Japanese (ja)
Other versions
JPS5614598A (en
Inventor
小泉洋介
上田一夫
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Asahi Dow Ltd
Original Assignee
Asahi Dow Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Asahi Dow Ltd filed Critical Asahi Dow Ltd
Priority to JP8986179A priority Critical patent/JPS5822078B2/en
Publication of JPS5614598A publication Critical patent/JPS5614598A/en
Publication of JPS5822078B2 publication Critical patent/JPS5822078B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Fats And Perfumes (AREA)

Description

【発明の詳細な説明】 本発明は粗羊毛蝋を非極性有機溶剤の溶液として、カチ
オン交換樹脂及び/又はアニオン交換樹脂、及び光照射
の組み合せにより処理する羊毛蝋の高度精製方法に関す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for highly refining wool wax, which comprises treating crude wool wax as a solution of a non-polar organic solvent with a combination of a cation exchange resin and/or anion exchange resin and light irradiation.

精製羊毛蝋は、医薬品の軟膏基料や、化粧品のクリーム
、ローション、シャンプー、リンス等に用いられる有用
な物質である。
Refined wool wax is a useful substance used as a base for pharmaceutical ointments and cosmetic creams, lotions, shampoos, conditioners, etc.

その原料である羊毛洗浄廃液より回収された粗羊毛蝋は
、不純物として、 ■ 塵埃、土砂、植物質等の夾雑物 ■ 羊の汗の成分と考えられる無機塩類 ■ 糞尿、血液及びこれ等酸化物に由来するタンパク質
系分解物、色素類 ■ 主成分のロウエステルの分解物である遊離脂肪酸遊
離アルコール 等を多く含んでいる。
Crude wool wax, which is the raw material, recovered from wool washing waste liquid contains impurities such as: ■ Contaminants such as dust, earth and sand, and vegetable matter ■ Inorganic salts that are thought to be components of sheep sweat ■ Manure, blood, and other oxides Contains a large amount of free fatty acids, free alcohols, etc., which are the decomposed products of wax ester, the main ingredient.

このため着色や獣臭が著しく、そのままでは利用価値が
低い為精製の必要がある。
Because of this, it has a significant coloration and animal odor, and has low utility value as it is, so it needs to be purified.

従来この粗羊毛蝋の精製は、 (1)温水と混合し遠心分離により夾雑物、スイント水
可溶不純分を除く。
Conventionally, this crude wool wax is purified by: (1) Mixing with warm water and centrifuging to remove impurities and water-soluble impurities.

(2)リン酸、硫酸等の酸類、次亜塩素酸ソーダ等の漂
白剤を含む温水を加えて加熱混合し、遠心分離により水
層を除く。
(2) Add warm water containing acids such as phosphoric acid and sulfuric acid, and bleaching agents such as sodium hypochlorite, heat and mix, and remove the aqueous layer by centrifugation.

(3)苛性ソーダ、炭酸ソーダ等のアルカリ類、過酸化
水素等の漂白剤等を含む温水を加えて加熱混合し、遠心
分離により水層を除く。
(3) Add warm water containing alkalis such as caustic soda and soda carbonate, and bleaching agents such as hydrogen peroxide, heat and mix, and remove the aqueous layer by centrifugation.

(4)温水により洗浄し、過剰のアルカリ、漂白剤等を
除去する。
(4) Wash with warm water to remove excess alkali, bleach, etc.

(5)その後必要に応じて白土処理を行う。(5) After that, perform white clay treatment as necessary.

というような一連の操作により行われてきた。This was done through a series of operations.

一般に羊毛蝋の精製においては、着色と酸価の低減が最
も重要であり、特に上記の様な従来の精製法では、 (1)製品の精製度が原料の粗羊毛蝋の品質に大きく左
右される。
In general, when refining wool wax, coloring and reducing the acid value are the most important.Especially, with the conventional refining methods such as those mentioned above, (1) the degree of purification of the product is greatly influenced by the quality of the crude wool wax that is the raw material; Ru.

(2)極めて操作が煩雑であり、多大の時間を要する。(2) The operation is extremely complicated and takes a lot of time.

(3)タンパク質等の分子量の大きな不純物が除去され
にくい。
(3) Impurities with large molecular weights such as proteins are difficult to remove.

(4)羊毛蝋の収率が70%程度と低い。(4) The yield of wool wax is as low as about 70%.

(5)汚染された廃水が多量にでる。(5) A large amount of contaminated wastewater is produced.

(6)獣臭がとれにくい。(6) Difficult to remove animal odor.

等の欠点がある。There are drawbacks such as.

本発明者等は、これ等の問題点を解決し簡単に、しかも
高精製度り羊毛域を収率よく得る方法を見出すべく研究
した結果、本発明の方法に到達した。
The present inventors conducted research to find a method for solving these problems and easily obtaining high-purity wool in a high yield, and as a result, they arrived at the method of the present invention.

すなわち本発明は、羊毛域を精製するに当り、羊毛域を
非極性有機溶剤の溶液となし、光照射した後、カチオン
交換樹脂及び/又は弱塩基型アニオン交換樹脂に通液す
る事を特徴とする羊毛域の高度精製方法である。
That is, the present invention is characterized in that when refining a wool region, the wool region is made into a solution of a non-polar organic solvent, and after being irradiated with light, the solution is passed through a cation exchange resin and/or a weakly basic anion exchange resin. This is an advanced refining method for wool.

本発明は通常法の様に実施される。The invention is carried out in a conventional manner.

羊毛域を有機溶剤の溶液となし、不溶分を除きH型に再
生したカチオン交換樹脂及び/又はOH型に再生したア
ニオン交換樹脂、及び光照射の組み合せにより処理する
The wool region is treated with a solution of an organic solvent, a cation exchange resin regenerated into an H type after removing insoluble matter and/or an anion exchange resin regenerated into an OH type, and a combination of light irradiation.

処理温度は20〜60℃の範囲で好ましくは、30〜4
0℃の範囲、溶液の濃度は5〜50wt%の範囲で好ま
しくは5〜30wt%の範囲である。
The treatment temperature is in the range of 20 to 60°C, preferably 30 to 4°C.
In the range of 0°C, the concentration of the solution is in the range of 5 to 50 wt%, preferably in the range of 5 to 30 wt%.

また樹脂層の通液速度は、0.5〜2C1/l交換樹脂
/)1r)の範囲が望ましい。
Further, the liquid passing rate through the resin layer is preferably in the range of 0.5 to 2C1/l exchanged resin/)1r).

光による処理の場合、光源として300〜450 nm
の波長を含む光が好ましく、光照射の時間は5〜15分
が望ましい。
In the case of light treatment, 300-450 nm as a light source
It is preferable to use light having a wavelength of 5 to 15 minutes.

さらには光の照射は空気あるいは酸素の存在下に行なわ
れる。
Furthermore, the light irradiation is performed in the presence of air or oxygen.

上記の処理により得られた羊毛域の有機溶剤の溶液から
、有機溶剤を留去して精製羊毛蝋が得られる。
A purified wool wax is obtained by distilling off the organic solvent from the solution of the organic solvent in the wool region obtained by the above treatment.

カチオン交換樹脂及び/又はアニオン交換樹脂、及び光
照射との組み合せによる処理とは次の5種の組み合せ処
理である。
The treatment using a combination of a cation exchange resin and/or anion exchange resin and light irradiation is the following five types of combination treatment.

(1) 羊毛域の有機溶剤の溶液に光を照射した後、
カチオン交換樹脂層に通液し、次いでアニオン交換樹脂
層に通液する処理、 (2)羊毛域の有機溶剤の溶液に光を照射した後、アニ
オン交換樹脂層に通液し、次いでカチオン交換樹脂層に
通液する処理、 (3)羊毛域の有機溶剤の溶液に光を照射した後、アニ
オン交換樹脂とカチオン交換樹脂の混合よりなる樹脂層
に通液する処理、 (4)羊毛域の有機溶剤の溶液に光を照射した後、カチ
オン交換樹脂層に通液する処理、 (5)羊毛域の有機溶剤の溶液に光を照射した後、アニ
オン交換樹脂層に通液する処理、 上記の全ての組み合せ処理により、従来法よりはるかに
簡便な操作で、極めて高品位の精製羊毛蝋を高収率にて
得ることができる。
(1) After irradiating the organic solvent solution in the wool area with light,
(2) After irradiating the organic solvent solution in the wool region with light, the solution is passed through the anion exchange resin layer, and then the cation exchange resin layer. (3) After irradiating a solution of an organic solvent in the wool region with light, a treatment in which the solution is passed through a resin layer made of a mixture of an anion exchange resin and a cation exchange resin; (4) A treatment in which a solution of an organic solvent in the wool region A process of irradiating a solvent solution with light and then passing the liquid through a cation exchange resin layer; (5) A process of irradiating a solution of an organic solvent in the wool region with light and then passing the liquid through an anion exchange resin layer; all of the above. By the combined treatment, extremely high-quality purified wool wax can be obtained in high yield with a much simpler operation than conventional methods.

羊毛域に光を照射した場合、過酸化物価が増大し、羊毛
域の品質に好ましくない影響を及ぼす事があるが、イオ
ン交換樹脂、なかでも強酸性イオン交換樹脂はこの過酸
化物価を減少させる効果を有する。
When light is irradiated onto wool, the peroxide value increases, which can have an unfavorable effect on the quality of the wool.Ion exchange resins, especially strongly acidic ion exchange resins, reduce this peroxide value. have an effect.

本発明において使用されるイオン交換樹脂は、カチオン
交換樹脂としては強酸性MR型の樹脂、例えばアンバー
リスト15、アンバーリス)XN1004、アンバーラ
イト200C等(いずれも日本オルガノ製)が望ましく
、アニオン交換樹脂としては、弱塩基性MR型の樹脂(
例えばアンバーライトIRA94、アンバーライトIR
A93、アンバーリス)A−21等(いずれも日本オル
ガノ製)が望ましい。
The ion exchange resin used in the present invention is preferably a strongly acidic MR type resin such as Amberlyst 15, Amberlyst) As a weakly basic MR type resin (
For example, Amberlight IRA94, Amberlight IR
A93, Amberlis) A-21, etc. (all manufactured by Nippon Organo) are desirable.

本発明において使用される溶剤は、ベンゼン、n−ヘキ
サン等の羊毛域を溶解し得る非極性有機溶剤でなければ
ならず、メチルエチルケトン等のケトン類、クロロポル
ム等の塩素系溶剤、ブタノール等のアルコール系溶剤で
は、その溶剤の極性により一旦吸着した不純物が溶離さ
れやすくなるため良好な結果が得られない。
The solvent used in the present invention must be a non-polar organic solvent such as benzene or n-hexane that can dissolve wool, ketones such as methyl ethyl ketone, chlorinated solvents such as chloroporm, alcohol-based solvents such as butanol, etc. When using a solvent, good results cannot be obtained because impurities once adsorbed are likely to be eluted due to the polarity of the solvent.

本発明において使用されるカチオン交換樹脂の再生は、
メタノール、エタノール等の低級アルコールで行うこと
がよ(、更に好ましくは塩化水素、硫酸等の酸を含有す
る低級アルコールで行うことがよい。
Regeneration of the cation exchange resin used in the present invention includes:
It is preferable to use a lower alcohol such as methanol or ethanol (and more preferably a lower alcohol containing an acid such as hydrogen chloride or sulfuric acid).

またアニオン交換樹脂の再生は、メタノール、エタノー
ル等の低級アルコールで行つことがよく、更に好ましく
は、苛性ソーダ、苛性カリ等の塩基を含有する低級アル
コールで行うことがよい。
Further, the anion exchange resin is preferably regenerated using a lower alcohol such as methanol or ethanol, and more preferably using a lower alcohol containing a base such as caustic soda or caustic potash.

カチオン交換樹脂、アニオン交換樹脂の両樹脂とも、メ
タノール等で非極性有機溶剤を置換し、カチオン交換樹
脂は塩酸、硫酸等の酸水溶液で、アニオン交換樹脂は苛
性ソーダ、苛性カリ等の塩基水溶液で再生することも可
能であるが、再生能が前記の酸あるいは塩基を含有する
低級アルコールより低(、また廃水の処理が必要となる
For both cation exchange resins and anion exchange resins, non-polar organic solvents are replaced with methanol, etc., and cation exchange resins are regenerated with acid aqueous solutions such as hydrochloric acid and sulfuric acid, and anion exchange resins are regenerated with base aqueous solutions such as caustic soda and caustic potash. However, the regeneration ability is lower than that of lower alcohols containing acids or bases (and wastewater treatment is required).

本発明により得られた羊毛域は従来の方法により得られ
た羊毛域より格段に色相がよく、獣臭が少なく、灰分、
酸価、過酸化物価も少なく、品質の優れたものである。
The wool region obtained by the present invention has a much better hue than the wool region obtained by conventional methods, has less animal odor, and has a lower ash content.
It has low acid value and peroxide value, and is of excellent quality.

次に実施例により本発明をさらに詳しく説明するが、こ
れは本発明を限定するものではなく、本発明の性質を変
えない範囲内に於て変更し得るものである。
Next, the present invention will be explained in more detail with reference to Examples, which are not intended to limit the present invention, but may be modified without changing the nature of the present invention.

以下の実施例、比較例中の%は全て重量%を示し、ガー
ドナー色度、酸価、過酸化物価の測定は、基準油脂分析
試験法(日本油化学協会編)に記載の方法によった。
All percentages in the following Examples and Comparative Examples indicate weight percent, and Gardner chromaticity, acid value, and peroxide value were measured using the methods described in Standard Oil and Fat Analysis Test Methods (edited by Japan Oil Chemists' Association). .

比較例 1 粗羊毛蝋の10%n−ヘキサン溶液1600Pに毎分0
.41の空気をバブリングしながら室温にて高圧水銀灯
(100W)を10分間照射した后溶媒を留去し羊毛蝋
を得た。
Comparative example 1 10% n-hexane solution of crude wool wax at 1600P per minute
.. The mixture was irradiated with a high-pressure mercury lamp (100 W) at room temperature for 10 minutes while bubbling air of 41, and then the solvent was distilled off to obtain wool wax.

原料粗羊毛蝋と上記の方法により得られた羊毛蝋のガー
ドナー色度、酸価、過酸化物価を表−1に示す。
Table 1 shows the Gardner color, acid value, and peroxide value of the raw wool wax and the wool wax obtained by the above method.

比較例 2 強酸性MR型イオン交換樹脂(アンバーリスト15)の
1601をメタノールのスラリーとして内径22mmφ
のジャケット付カラムに充填した。
Comparative Example 2 Strongly acidic MR type ion exchange resin (Amberlyst 15) 1601 was made into a methanol slurry with an inner diameter of 22 mmφ.
It was packed into a jacketed column.

これにメタノールを通液し樹脂を洗浄した後、IN塩化
水素のメタノール溶液の約31を通液して樹脂をH型に
再生した。
After washing the resin by passing methanol through it, about 3 liters of a methanol solution of IN hydrogen chloride was passed therethrough to regenerate the resin into H type.

その後メタノールにより樹脂層中の塩化水素を除き、最
後にn−ヘキサンでメタノールを置換した。
Thereafter, hydrogen chloride in the resin layer was removed with methanol, and finally methanol was replaced with n-hexane.

別のジャケット付カラム(内径22mmφ)に弱酸性M
R型イオン交換樹脂(アンバーライトIRA94)16
0rをメタノールのスラリーとして充填しIN塩化水素
のメタノール溶液の代りにIN苛性ソーダのメタノール
溶液を用いる他は上記と同様の処理をすることにより樹
脂をOH型に再生した。
Weakly acidic M was added to another jacketed column (inner diameter 22 mmφ).
R-type ion exchange resin (Amberlite IRA94) 16
The resin was regenerated into an OH type by the same treatment as above except that 0r was filled as a methanol slurry and a methanol solution of IN caustic soda was used instead of a methanol solution of IN hydrogen chloride.

粗羊毛蝋の10%n−へキサン溶液の16002を最初
上記の強酸性イオン交換樹脂層に通液した後、次いで弱
塩基性イオン交換樹脂層に通液した。
16002, a 10% n-hexane solution of crude wool wax, was first passed through the above-mentioned strongly acidic ion exchange resin layer, and then passed through the weakly basic ion exchange resin layer.

通液時、樹脂層の温度は30℃に保ち、通液速度は20
0cc/hrで行った。
During liquid passage, the temperature of the resin layer was kept at 30°C, and the liquid passage rate was 20°C.
It was carried out at 0cc/hr.

流出液を集めてn−へキサンを留去し得られた羊毛蝋の
カードナー色度、酸価、過酸化物価、収率を表−1に示
す。
The effluent was collected and n-hexane was distilled off, and the Cardner color, acid value, peroxide value, and yield of the wool wax obtained are shown in Table 1.

原料粗羊毛蝋は比較例1と同じものを使用した。The raw material crude wool wax used was the same as in Comparative Example 1.

実施例 1 比較例2と同様にして強酸性イオン交換樹脂(アンバー
リスト15)をH型に、弱塩基性イオン交換樹脂(アン
バーライ)IRA94)をOHWにそれぞれ再生した。
Example 1 In the same manner as in Comparative Example 2, a strongly acidic ion exchange resin (Amberlyst 15) was regenerated into H type, and a weakly basic ion exchange resin (Amberlyst IRA94) was regenerated into OHW.

粗羊毛蝋の10%n−ヘキサン溶液1600Pに、毎分
0,41の空気をバブリングしながら高圧水銀灯(10
0W)を10分間照射し、次いで上記の強酸性イオン交
換樹脂層に通液し、最後に弱塩基性イオン交換樹脂層に
通液した。
A high-pressure mercury lamp (10%
0W) for 10 minutes, then the solution was passed through the above-mentioned strongly acidic ion exchange resin layer, and finally the solution was passed through the weakly basic ion exchange resin layer.

通液速度は200cc/hr、温度は30℃で行った。The liquid flow rate was 200 cc/hr, and the temperature was 30°C.

粗羊毛蝋の10%n−ヘキサン溶液の通液が終ったら約
500CCのへキサンを通液する。
After passing the 10% n-hexane solution of crude wool wax, about 500 cc of hexane is passed through.

全ての流出液を集めてn−ヘキサンを留去し、得られた
羊毛蝋のガードナー色度、酸価、過酸化物価、収率な表
−1に示す。
All the effluents were collected and n-hexane was distilled off, and the Gardner color, acid value, peroxide value, and yield of the wool wax obtained are shown in Table 1.

比較例 3 粗羊毛蝋の10%n−ヘキサン溶液の通液順序を、最初
光反応槽、次いで強酸性イオン交換樹脂層、最後に弱塩
基性イオン交換樹脂層という順序に代えて、最初強酸性
イオン交換樹脂層、次いで光反応槽、最後に弱塩基性イ
オン交換樹脂層という順序にする他は実施例1と同様に
して精製を行った。
Comparative Example 3 The order in which a 10% n-hexane solution of crude wool wax was passed was changed to first a photoreaction tank, then a strongly acidic ion exchange resin layer, and finally a weakly basic ion exchange resin layer. Purification was carried out in the same manner as in Example 1, except that the ion exchange resin layer was followed by the photoreaction tank, and finally the weakly basic ion exchange resin layer.

得られた羊毛蝋のカードナー色度、酸価、過酸化物価、
収率を表−1に示す。
Cardner chromaticity, acid value, peroxide value of the obtained wool wax,
The yield is shown in Table-1.

比較例1では過酸化物価が非常に高く、ガードナー色度
も高い、比較例2でもガードナー色度が高い。
Comparative Example 1 has a very high peroxide value and a high Gardner chromaticity, and Comparative Example 2 also has a high Gardner chromaticity.

比較例3ではガードナー色度、酸価は極めて低いが、過
酸化物価が原料より高い。
In Comparative Example 3, the Gardner chromaticity and acid value are extremely low, but the peroxide value is higher than that of the raw material.

これに比べて実施例1では、ガードナー色度酸価が極め
て低く、過酸化物価も低く良質の羊毛蝋が得られる。
In comparison, in Example 1, a high-quality wool wax with extremely low Gardner chromatic acid value and low peroxide value was obtained.

実施例及び比較例3 イオン交換樹脂と光照射の組み合せ方による性能の違い
を比較した。
Example and Comparative Example 3 Differences in performance depending on the combination of ion exchange resin and light irradiation were compared.

比較例2と同様にして強酸性イオン交換樹脂(アンバー
リス)15)をH型に、弱塩基性イオン交換樹脂(アン
バーライトIRA94)をOH型にそれぞれ再生し、以
下の実施、例である組合せ(1入(2)と比較例である
組合せ(3)〜(5)の実験に使用した。
In the same manner as in Comparative Example 2, the strongly acidic ion exchange resin (Amberlyth) 15) was regenerated into the H type, and the weakly basic ion exchange resin (Amberlite IRA94) was regenerated into the OH type, and the following combinations were carried out and examples. (Used in the experiments of 1-pack (2) and combinations (3) to (5) as comparative examples.

組み合せ(1)では、粗羊毛蝋の20%を10%n−ヘ
キサン溶液として、まず高圧水銀灯にて光を照射し、次
いで強酸性イオン交換樹脂の301に通液し、最後に弱
塩基性イオン交換樹脂の301に通液した。
In combination (1), 20% of crude wool wax is made into a 10% n-hexane solution, first irradiated with light using a high-pressure mercury lamp, then passed through strong acidic ion exchange resin 301, and finally weakly basic ion The solution was passed through exchange resin 301.

組み合せ(2)では、粗羊毛蝋の209を10%n〜ヘ
キサン溶液として、まず高圧水銀灯にて光を照射し次い
で、強酸性イオン交換樹脂の302と弱塩基性イオン交
換樹脂の301を混合した樹脂層に通液した。
In combination (2), crude wool wax 209 was made into a 10% n-hexane solution, first irradiated with light using a high-pressure mercury lamp, and then strongly acidic ion exchange resin 302 and weakly basic ion exchange resin 301 were mixed. A liquid was passed through the resin layer.

組み合せ(3)では、粗羊毛蝋の202を10%n−ヘ
キサン溶液として、まず強酸性イオン交換樹脂の309
に通液し、次いで高圧水銀灯にて光を・照射し、最後に
弱塩基性イオン交換樹脂の301に通液した。
In combination (3), crude wool wax 202 is made into a 10% n-hexane solution, and then strongly acidic ion exchange resin 309 is added.
The solution was then irradiated with light from a high-pressure mercury lamp, and finally the solution was passed through a weakly basic ion exchange resin 301.

組み合せ(4)では、粗羊毛蝋の202を10%n−へ
キサン溶液として、まず強酸性イオン交換樹脂の302
に通液し、次いで弱塩基性イオン交換樹脂の301に通
液し、最後に高圧水銀灯にて光を照射した。
In combination (4), crude wool wax 202 is made into a 10% n-hexane solution, and then strongly acidic ion exchange resin 302 is added.
The solution was then passed through a weakly basic ion exchange resin 301, and finally irradiated with light using a high pressure mercury lamp.

組み合せ(5)では、粗羊毛蝋の202を10%n−ヘ
キサン溶液として、まず強酸性イオン交換樹脂の30?
と弱塩基性イオン交換樹脂の30f!′を混合した樹脂
層に通液し、次いで高圧水銀灯にて光を照射した。
In combination (5), crude wool wax 202 is made into a 10% n-hexane solution, and then strongly acidic ion exchange resin 30?
and 30f of weakly basic ion exchange resin! A liquid was passed through the resin layer mixed with ', and then light was irradiated with a high-pressure mercury lamp.

組み合せ(1)〜(5)により処理した溶液からn−へ
キサンを留去し、得られた羊毛蝋のガードナー色度、酸
価、過酸化物価を表−2に示した。
N-hexane was distilled off from the solutions treated with combinations (1) to (5), and the Gardner color, acid value, and peroxide value of the wool wax obtained are shown in Table 2.

各組み合せにおいて、光照射は100Wの高圧水銀灯を
用いて10分間行った。
In each combination, light irradiation was performed for 10 minutes using a 100 W high pressure mercury lamp.

また羊毛蝋のイオン交換樹脂への通液は、樹脂を17m
mφのカラムに充填し30℃の温度で100cc/hr
の速度で行なった。
In addition, when passing wool wax through an ion exchange resin, the resin is 17 m
Packed in mφ column and 100cc/hr at 30℃
was done at a speed of

いずれの組み合せにおいても、ガードナー色度が著しく
改善され、酸価も1以下に減少するが、組合せ(3)〜
(5)は過酸化物価の減少が充分でないか、むしろ上昇
する。
In any combination, the Gardner chromaticity is significantly improved and the acid value is reduced to 1 or less, but combinations (3) to
In (5), the peroxide value is not sufficiently reduced, or rather increases.

組合せ(1)〜(2)はガードナー色度のみでなく、酸
価、過酸化物価も著しく低い値を示し、光照射の後にカ
チオンおよび/またはアニオン交換樹脂の処理を行うの
が望ましい事を示している。
Combinations (1) and (2) showed significantly low values not only in Gardner chromaticity but also in acid value and peroxide value, indicating that it is desirable to perform treatment with a cation and/or anion exchange resin after light irradiation. ing.

Claims (1)

【特許請求の範囲】 1 羊毛蝋を精製するに自す、羊毛蝋を非極性有機溶剤
の溶液となし、光照射した後、カチオン交換樹脂及び/
又は、弱塩基型アニオン交換樹脂に通液する事を特徴と
する羊毛蝋の高度精製方法。 2 光源として300〜450 nmの波長を含む光を
用いる事を特徴とする特許請求の範囲第1項記載の羊毛
蝋の高度精製方法。
[Claims] 1. To purify wool wax, wool wax is made into a solution of a non-polar organic solvent, and after being irradiated with light, a cation exchange resin and/or
Alternatively, an advanced purification method for wool wax characterized by passing the solution through a weakly basic anion exchange resin. 2. The method for highly refining wool wax according to claim 1, wherein light having a wavelength of 300 to 450 nm is used as a light source.
JP8986179A 1979-07-17 1979-07-17 Advanced refining method for wool wax Expired JPS5822078B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8986179A JPS5822078B2 (en) 1979-07-17 1979-07-17 Advanced refining method for wool wax

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8986179A JPS5822078B2 (en) 1979-07-17 1979-07-17 Advanced refining method for wool wax

Publications (2)

Publication Number Publication Date
JPS5614598A JPS5614598A (en) 1981-02-12
JPS5822078B2 true JPS5822078B2 (en) 1983-05-06

Family

ID=13982557

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8986179A Expired JPS5822078B2 (en) 1979-07-17 1979-07-17 Advanced refining method for wool wax

Country Status (1)

Country Link
JP (1) JPS5822078B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017047708A1 (en) 2015-09-18 2017-03-23 日本精工株式会社 Electric power steering device

Also Published As

Publication number Publication date
JPS5614598A (en) 1981-02-12

Similar Documents

Publication Publication Date Title
JP3902282B2 (en) Method for producing high purity glycerin
JPS5822078B2 (en) Advanced refining method for wool wax
US2898350A (en) Ozonolysis of coal-tar products
JPS5811478B2 (en) Wool wax refining method
JPS61281159A (en) Production of orange pigment
JPH0510349B2 (en)
JPS63190840A (en) Purification of solanesol
JPH02115299A (en) Purification of natural wax
JPS5811480B2 (en) Advanced purification method for wool wax
JPS632430B2 (en)
Palkin et al. The Resin Acids of American Turpentine Gum. The Preparation of the Pimaric Acids from Pinus Palustris1
JPS5921364A (en) Preparation of soybean or soybean protein having improved quality
JPH01135735A (en) Method for recovering glycerin
JPS5811479B2 (en) Wool wax refining method
CN113443992B (en) Preparation method of methyl salicylate with low phenol content
JP2694184B2 (en) Beeswax refining method
JPH0119826B2 (en)
JPS5811477B2 (en) How to bleach wool wax
JP3189023B2 (en) Method for purifying arabinogalactan-containing composition
SU1636333A1 (en) Method of graphite oxide preparation
AT206422B (en) Process for cleaning water-immiscible, synthetic alcohols
JPS638347A (en) Production of higher alcohol
DE1668952C (en) Process for the production of pure phenols from crude phenols, which were obtained from the cleavage of hydroperoxides of alkyl aromatic hydrocarbons
WO2000020367A1 (en) Process for the preparation of sorbic acid
JPS6384457A (en) Production of lemon oil free from phototoxicity