JPH047359B2 - - Google Patents

Info

Publication number
JPH047359B2
JPH047359B2 JP14924083A JP14924083A JPH047359B2 JP H047359 B2 JPH047359 B2 JP H047359B2 JP 14924083 A JP14924083 A JP 14924083A JP 14924083 A JP14924083 A JP 14924083A JP H047359 B2 JPH047359 B2 JP H047359B2
Authority
JP
Japan
Prior art keywords
centrifugal
separating
basket
deodorized
sterine
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
JP14924083A
Other languages
Japanese (ja)
Other versions
JPS6041694A (en
Inventor
Minoru Uchida
Yoshiaki Takagi
Kazunari Maeda
Takao Sakamoto
Akira Saito
Nobuaki Tanaka
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.)
Taisei Corp
Original Assignee
Taisei Corp
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 Taisei Corp filed Critical Taisei Corp
Priority to JP14924083A priority Critical patent/JPS6041694A/en
Priority to GB08402452A priority patent/GB2145418B/en
Publication of JPS6041694A publication Critical patent/JPS6041694A/en
Priority to MY8700865A priority patent/MY100003A/en
Publication of JPH047359B2 publication Critical patent/JPH047359B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07JSTEROIDS
    • C07J9/00Normal steroids containing carbon, hydrogen, halogen or oxygen substituted in position 17 beta by a chain of more than two carbon atoms, e.g. cholane, cholestane, coprostane

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Steroid Compounds (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は油脂の脱臭工程で副生する脱臭留出物
中のステリン類の分離方法に関する。 大豆油、菜種油、綿実油、サフラワー油、ヒマ
ワリ油、米ぬか油、トウモロコシ油、ヤシ油、パ
ーム油、パーム核油等の脱臭工程で副生する脱臭
スカム、脱臭スラツジ、ホツトウエル油滓等(以
下脱臭留出物という)にはステリン類、炭化水素
類、トコフエロール類、グリセリド類、遊離脂肪
酸等が共存している。 これらの脱臭留出物中に1〜35%位含まれてい
るステリン類はその乳化安定作用や皮膚上の湿潤
性保持などの効果から化粧品基剤として使われた
り、各種ステロイドホルモンの合成資源などの用
途で医薬品合成面への利用が考えられたりエビ、
うなぎや蚕などの飼料添加剤として使用するなど
の用途がある。 又、脱臭留出物中に0.1〜20%位含まれている
トコフエロール類は医薬、食品あるいは抗酸化剤
として有用な物質である。 脱臭留出物よりトコフエロール濃縮物を得るた
めの一般的方法ではステリン類を含んだままでの
処理が困難であることが多い。そこで最初にステ
リン類を分別することが必要になつている。通常
ステリン類の分離として工業的処理に適用できる
方法としては、 1) 溶剤分別結晶法 2) 二塩基性有機酸付加物法 3) 尿素付加物法 4) 金属塩化物付加物法 の4方法が考えられる。 このうち、溶剤分別結晶法では析出したステリ
ン類の結晶を分離する操作は、通常超遠心分離
(遠心効果3000以上)あるいは炉過によつて行な
われているが、これらの操作に使用する装置が大
型化し、また分離したステリン類の取扱に不都合
が生ずる場合が多いという欠点があつた。 また、これらの分離操作を行なう場合、ステリ
ン類の分離特性から脱臭留出物の15〜30倍の量の
溶剤を使用する必要がある。ところが、脂肪酸の
存在する状態でステリン類は溶剤に対してある程
度の溶解度を有するため、分離工程を経た脱臭留
出物中にステリン類が残存することによつて後工
程で析出し、影響を及ぼすことが多い、例えば溶
剤としてメタノールを使用した場合、脂肪酸の存
在下でステリン類の溶解度は約2%であり、溶媒
使用量が多くなる程ステリン類の残存量が多くな
る。そこで、後工程でのステリン類の析出はヘキ
サン、トルエン、キシレン等の第3成分を添加す
れば防ぐことができるが、この場合複数の溶剤を
回収する必要があるため溶剤回収装置が複雑化す
る。 本発明の目的は、分別結晶に用いる溶剤を少量
に抑えることができ、しかも小型の分離装置で効
率的にステリン類を分離することができる油脂脱
臭留出物中のステリン類の分離方法を提供するこ
とにある。 即ち、本発明の油脂脱臭留出物中のステリン類
の分離方法は、油脂の脱臭工程で副生する脱臭留
出物中のステリン類を溶剤分別結晶法により分離
する際に、分離の操作をバスケツト型遠心沈降機
を用いて遠心沈降分離する第一段階とバスケツト
型遠心濾過機を用いて遠心濾過する第二段階の二
段階で行なうことを特徴とするものである。 本発明においては、ステリン類の分離操作は、
遠心沈降分離と遠心過のそれぞれ単独もしくは
複数の操作を組合せることによつて構成される
が、ステリン類を濃縮単離するためにはこれら遠
心沈降分離と遠心過のそれぞれ1つの操作を組
合せることで充分な効果が得られ、更にこれらの
単位操作の特長を生かすために、遠心沈降分離と
遠心過をこの順で組合せて分離操作の基本的な
部分を構成することが好ましい。この様に、遠心
沈降分離と遠心過の組合せで行なわれる分離操
作によれば、少量の溶剤使用量で高効率にステリ
ン類を分離することができ、しかも各単位分離操
作に使用する装置を小型化できると共に作業も簡
便化し単離されたステリン類の取扱も極めて容易
となる。また、更にステリン類及び脱臭留出物中
の他の成分の回収率を向上させるために、遠心沈
降分離及び遠心過を複数組合せ、また固形分の
洗浄等の他の操作を付加することもできる。 本発明方法の好適な実施態様としては、下記の
フローシートによつて示される分離方法によつて
例示することができる。
The present invention relates to a method for separating sterine compounds from deodorized distillate produced as a by-product in the deodorizing process of fats and oils. Deodorized scum, deodorized sludge, hotwell oil soapstock, etc. (hereinafter referred to as deodorized Sterolins, hydrocarbons, tocopherols, glycerides, free fatty acids, etc. coexist in the distillate (referred to as distillate). These deodorized distillates contain about 1 to 35% of sterine compounds, which are used as cosmetic bases due to their emulsion-stabilizing effects and moisturizing properties on the skin, and as a resource for the synthesis of various steroid hormones. It is thought that it can be used for pharmaceutical synthesis, and shrimp,
It is used as a feed additive for eels, silkworms, etc. In addition, tocopherols, which are contained in the deodorized distillate in an amount of about 0.1 to 20%, are useful substances as medicines, foods, or antioxidants. In general methods for obtaining tocopherol concentrates from deodorized distillates, it is often difficult to process the tocopherols while they still contain sterins. Therefore, it is necessary to first separate the sterins. Generally, there are four methods that can be applied to industrial processing to separate sterolins: 1) Solvent fractionation crystallization method, 2) Dibasic organic acid adduct method, 3) Urea adduct method, and 4) Metal chloride adduct method. Conceivable. Among these methods, in the solvent fractional crystallization method, the operation to separate the precipitated sterine crystals is usually carried out by ultracentrifugation (centrifugal effect of 3000 or more) or furnace filtration, but the equipment used for these operations is The disadvantages are that it is large in size and that it is often difficult to handle the separated sterins. Furthermore, when performing these separation operations, it is necessary to use a solvent in an amount 15 to 30 times that of the deodorized distillate due to the separation characteristics of sterolins. However, in the presence of fatty acids, sterine compounds have a certain degree of solubility in solvents, so if sterine compounds remain in the deodorized distillate after the separation process, they will precipitate in the subsequent process and have an adverse effect. Often, for example, when methanol is used as a solvent, the solubility of sterins in the presence of fatty acids is about 2%, and the greater the amount of solvent used, the greater the amount of sterine remaining. Therefore, the precipitation of sterine compounds in the post-process can be prevented by adding a third component such as hexane, toluene, or xylene, but in this case, the solvent recovery equipment becomes complicated because multiple solvents need to be recovered. . An object of the present invention is to provide a method for separating sterine compounds in a deodorized oil and fat distillate, which can reduce the amount of solvent used in fractional crystallization and efficiently separate sterine compounds using a small-sized separation device. It's about doing. That is, the method for separating sterine compounds in a deodorized distillate of fats and oils according to the present invention involves performing a separation operation when separating sterine compounds in a deodorizing distillate produced as a by-product in the deodorizing process of fats and oils by a solvent fractional crystallization method. The method is characterized in that it is carried out in two stages: a first stage of centrifugal sedimentation using a basket-type centrifugal sedimenter, and a second stage of centrifugal filtration using a basket-type centrifugal filter. In the present invention, the separation operation of sterolins is carried out by
It is composed of centrifugal sedimentation and centrifugation, either alone or in combination, but in order to concentrate and isolate sterins, these centrifugal sedimentation and centrifugal filtration operations are combined. In order to obtain a sufficient effect and further take advantage of the features of these unit operations, it is preferable to combine centrifugal sedimentation and centrifugation in this order to constitute the basic part of the separation operation. In this way, the separation operation performed by a combination of centrifugal sedimentation and centrifugation makes it possible to separate sterenes with high efficiency using a small amount of solvent, and the equipment used for each unit separation operation can be made smaller. In addition, the work is simplified, and the isolated sterins are extremely easy to handle. Furthermore, in order to further improve the recovery rate of sterins and other components in the deodorized distillate, multiple combinations of centrifugal sedimentation and centrifugation, and other operations such as solid content washing may be added. . A preferred embodiment of the method of the present invention can be exemplified by the separation method shown in the flow sheet below.

【表】 ↓


[Table] ↓


Claims (1)

【特許請求の範囲】 1 油脂の脱臭工程で副生する脱臭留出物中のス
テリン類を溶剤分別結晶法により分離する際に、
分離の操作をバスケツト型遠心沈降機を用いて遠
心沈降分離する第一段階とバスケツト型遠心濾過
機を用いて遠心濾過する第二段階の二段階で行な
うことを特徴とする油脂脱臭留出物中のステリン
類の分離方法。 2 溶剤は炭素数1〜4の脂肪族アルコール、脂
肪族カルボン酸エステル、脂肪族ケトン又はこれ
らの混合物である特許請求の範囲第1項記載の油
脂脱臭留出物中のステリン類の分離方法。 3 遠心沈降分離はバスケツト型遠心沈降機を用
い遠心効果1000〜1500で行ない、遠心濾過はバス
ケツト型遠心濾過機を用い遠心効果700〜900で行
なう特許請求の範囲第1項記載の油脂脱臭留出物
中のステリン類の分離方法。
[Claims] 1. When separating sterine compounds in the deodorized distillate produced as a by-product in the deodorizing process of fats and oils by a solvent fractional crystallization method,
In an oil and fat deodorized distillate, the separation operation is carried out in two stages: a first stage of centrifugal sedimentation using a basket-type centrifugal sedimenter, and a second stage of centrifugal filtration using a basket-type centrifugal filter. Method for separating sterolins. 2. The method for separating sterins in a deodorized fat and oil distillate according to claim 1, wherein the solvent is an aliphatic alcohol having 1 to 4 carbon atoms, an aliphatic carboxylic acid ester, an aliphatic ketone, or a mixture thereof. 3. The oil and fat deodorizing distillation according to claim 1, wherein the centrifugal sedimentation is carried out using a basket-type centrifugal sedimenter at a centrifugal effect of 1000 to 1500, and the centrifugal filtration is carried out using a basket-type centrifugal filter at a centrifugal effect of 700 to 900. A method for separating sterine compounds in substances.
JP14924083A 1983-08-17 1983-08-17 Separation method for sterine compounds in deodorized oil and fat distillate Granted JPS6041694A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP14924083A JPS6041694A (en) 1983-08-17 1983-08-17 Separation method for sterine compounds in deodorized oil and fat distillate
GB08402452A GB2145418B (en) 1983-08-17 1984-01-31 Method of separating sterols from deodorisation distillates of oils
MY8700865A MY100003A (en) 1983-08-17 1987-06-23 Method of separating sterols from deodorization distillates of oils

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14924083A JPS6041694A (en) 1983-08-17 1983-08-17 Separation method for sterine compounds in deodorized oil and fat distillate

Publications (2)

Publication Number Publication Date
JPS6041694A JPS6041694A (en) 1985-03-05
JPH047359B2 true JPH047359B2 (en) 1992-02-10

Family

ID=15470942

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14924083A Granted JPS6041694A (en) 1983-08-17 1983-08-17 Separation method for sterine compounds in deodorized oil and fat distillate

Country Status (3)

Country Link
JP (1) JPS6041694A (en)
GB (1) GB2145418B (en)
MY (1) MY100003A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3009417A1 (en) * 2014-10-13 2016-04-20 LANXESS Deutschland GmbH Improved method for producing para-thymol

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB895145A (en) * 1957-08-28 1962-05-02 Eastman Kodak Co Separation of sterols
GB1008767A (en) * 1961-06-01 1965-11-03 Eastman Kodak Co Improvements in or relating to sterols and tocopherols
US3153055A (en) * 1962-03-20 1964-10-13 Eastman Kodak Co Process for separating tocopherols and sterols from deodorizer sludge and the like
US3153054A (en) * 1962-03-20 1964-10-13 Eastman Kodak Co Process for separating tocopherols and sterols from deodorizer sludge and the like
US3418335A (en) * 1966-04-12 1968-12-24 Gen Mills Inc Process for obtaining tocopherols

Also Published As

Publication number Publication date
MY100003A (en) 1988-10-26
GB2145418A (en) 1985-03-27
JPS6041694A (en) 1985-03-05
GB8402452D0 (en) 1984-03-07
GB2145418B (en) 1987-03-18

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