JP2993253B2 - Method for producing animal fats and oils with low cholesterol content - Google Patents

Method for producing animal fats and oils with low cholesterol content

Info

Publication number
JP2993253B2
JP2993253B2 JP3357002A JP35700291A JP2993253B2 JP 2993253 B2 JP2993253 B2 JP 2993253B2 JP 3357002 A JP3357002 A JP 3357002A JP 35700291 A JP35700291 A JP 35700291A JP 2993253 B2 JP2993253 B2 JP 2993253B2
Authority
JP
Japan
Prior art keywords
cholesterol
oil
oils
fat
hexane
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 - Fee Related
Application number
JP3357002A
Other languages
Japanese (ja)
Other versions
JPH05171177A (en
Inventor
章 富沢
元威 村上
明典 重松
真美 川成
正信 神武
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.)
YUKIJIRUSHI NYUGYO KK
Original Assignee
YUKIJIRUSHI NYUGYO KK
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 YUKIJIRUSHI NYUGYO KK filed Critical YUKIJIRUSHI NYUGYO KK
Priority to JP3357002A priority Critical patent/JP2993253B2/en
Publication of JPH05171177A publication Critical patent/JPH05171177A/en
Application granted granted Critical
Publication of JP2993253B2 publication Critical patent/JP2993253B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、動物性油脂からそれに
含まれるコレステロールを除去して、コレステロールを
除去もしくは低減した動物性油脂の製造法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing animal fats and oils in which cholesterol is removed or reduced by removing cholesterol contained therein from animal fats and oils.

【0002】[0002]

【従来の技術】近年、食肉やバターなどの動物性脂肪食
品を多量に摂取すると、動物性油脂中に含まれるコレス
テロールが動脈硬化、心筋梗塞、脳卒中などを発症する
原因になることから、コレステロール含量を低減した動
物性油脂食品が要望されている。
2. Description of the Related Art In recent years, when a large amount of animal fat food such as meat and butter is consumed, cholesterol contained in animal fats and oils causes arteriosclerosis, myocardial infarction, stroke, etc. There is a demand for animal fats and oils foods in which the amount is reduced.

【0003】従来、動物性油脂に含まれているコレステ
ロールを除去するための試みが主として食品業界に於い
て行われている。例えば、乳脂肪からのコレステロール
除去に関しては、超臨界ガス抽出法(特開昭62−13404
2)、微生物や酵素による分解法(特開昭57-86257)な
どが提案されている。しかしながら、これらの方法は処
理操作が複雑かつ高度な技術及び装置を必要としてお
り、コストの面で実用化に至っていない。
Conventionally, attempts to remove cholesterol contained in animal fats and oils have been made mainly in the food industry. For example, regarding the removal of cholesterol from milk fat, a supercritical gas extraction method (JP-A-62-13404)
2), a decomposition method using a microorganism or an enzyme (JP-A-57-86257) and the like have been proposed. However, these methods have complicated processing operations and require advanced technology and equipment, and have not been put into practical use in terms of cost.

【0004】また、活性炭などの吸着剤を利用してコレ
ステロールを吸着除去する方法(特開昭61−136598)も
提案されているが、異臭や異味を生じるため実用化され
ていない。
[0004] A method of adsorbing and removing cholesterol using an adsorbent such as activated carbon has also been proposed (JP-A-61-136598), but it has not been put to practical use because it produces off-flavors and off-flavors.

【0005】[0005]

【発明が解決しようとする課題】本発明は、従来法では
成しえなかった、動物性油脂よりコレステロールを工業
的に効率よく除去し、コレステロール含量を低減した精
製動物性油脂を高い収率で得る方法を提供することを課
題とする。
DISCLOSURE OF THE INVENTION The present invention provides a high-yield purified animal fat / oil having a reduced cholesterol content by industrially efficiently removing cholesterol from an animal fat / oil which could not be achieved by the conventional method. It is an object to provide a method for obtaining the information.

【0006】[0006]

【課題を解決するための手段】本発明は、上記課題を解
決するために鋭意研究の結果、連続的に、クロマトグラ
フィーによる分離を行うことのできる擬似移動床式クロ
マト分離装置(以下SMBという)を用いて、混合溶媒
系、特にヘキサン、エタノール及び水よりなる混合溶媒
系もしくはヘキサン、アセトン、エタノール及び水より
なる混合溶媒系を選択し、SMBの操作条件を最適化す
ることにより効率よく動物性油脂よりコレステロールを
除去することができるという知見に基づいて成されたも
のである。
Means for Solving the Problems The present invention has been made as a result of intensive studies to solve the above problems, and as a result, a simulated moving bed type chromatograph (hereinafter referred to as SMB) capable of continuously performing chromatographic separation. Using a mixed solvent system, especially a mixed solvent system consisting of hexane, ethanol, and water or a mixed solvent system consisting of hexane, acetone, ethanol, and water, and optimizing the operating conditions of SMB This is based on the finding that cholesterol can be removed from fats and oils.

【0007】従来から行われていた、カラムクロマトグ
ラフィーに於いては、コレステロールを分画するために
ヘキサン及びジエチルエーテルなどの混合溶媒系を用
い、その混合比を段階的に変化させトリグリセリドとコ
レステロールを段階的に分取していた。また、この操作
は回分的に行われるため、1度の操作で大量に試料を処
理しようとすれば、大口径のカラムと多大な労力を必要
とした。しかし、SMBを用い最適な溶媒系を選択する
ことによって、連続的に、大量にかつ効率よくコレステ
ロールを、動物性油脂より除去することに成功したもの
である。
In the conventional column chromatography, a mixed solvent system such as hexane and diethyl ether is used to fractionate cholesterol, and the mixing ratio is changed stepwise to convert triglyceride and cholesterol. It was sorted in stages. In addition, since this operation is performed batchwise, processing a large amount of samples in one operation requires a large-diameter column and a great deal of labor. However, by selecting an optimal solvent system using SMB, the cholesterol has been successfully removed from animal fats and oils continuously and efficiently.

【0008】擬似移動床式クロマト分離装置の原理およ
び装置は公知のものであり、稼働条件は任意の純度、処
理量、処理速度、回収液濃度等により適宜設定すること
ができる。一般に原料に対する溶離液の比を大にするこ
とにより、それぞれの純度、回収率は向上するが、使用
溶媒量など、コストの面から考えると、その比は、4以
下、好ましくは1〜2を使用する。
[0008] The principle and apparatus of a simulated moving bed type chromatographic separation apparatus are known, and the operating conditions can be appropriately set according to any purity, processing amount, processing speed, concentration of the recovered liquid and the like. Generally, by increasing the ratio of the eluent to the raw material, the purity and the recovery rate of each are improved, but from the viewpoint of cost such as the amount of solvent used, the ratio is 4 or less, preferably 1-2. use.

【0009】本発明における原料の動物性油脂には、ラ
ード、牛脂、魚油、乳脂などのほか、これらの加工油脂
である、バター、バターオイル、硬化油などが用いられ
る。これらは、前記した有機溶媒に溶解される。その濃
度は、10〜70 W/V%程度とすることが処理効率の面から
みて望ましい。この濃度が高すぎると分離が悪くなり、
低すぎると使用溶媒量が増えるので好ましくない。ま
た、本発明の混合溶媒中のヘキサン、エタノール及び水
の混合割合は、100:0 〜10:0〜0.1 等が、またヘキサ
ン、アセトン、エタノール及び水の混合割合は、100:0
〜20:0〜10:0〜0.1 が好ましい。
The animal fats and oils used as raw materials in the present invention include lard, beef tallow, fish oil, milk fat and the like, as well as processed oils and fats such as butter, butter oil and hardened oil. These are dissolved in the above-mentioned organic solvent. The concentration is desirably about 10 to 70 W / V% from the viewpoint of processing efficiency. If this concentration is too high, separation will be poor,
If it is too low, the amount of the solvent used increases, which is not preferable. The mixing ratio of hexane, ethanol and water in the mixed solvent of the present invention is 100: 0 to 10: 0 to 0.1 and the like, and the mixing ratio of hexane, acetone, ethanol and water is 100: 0.
-20: 0-10: 0-0.1 is preferred.

【0010】本発明で得られたコレステロール含量の低
減された動物性油脂は、これを飲食品に含有させること
によってコレステロール含量の低減された飲食品を得る
ことができる。特に動物性油脂としてバターまたはバタ
ーオイルを用い、油中のコレステロール含量を低減させ
て、これをバター、マーガリン、還元乳、チーズ、アイ
スクリーム等の製造のさい、原料として用いてこれらの
乳製品を製造するとコレステロール含量の低減された乳
製品を得ることができ、健康食品として有用なものとな
る。
[0010] The animal fats and oils with reduced cholesterol content obtained by the present invention can be obtained as foods and beverages with reduced cholesterol content by incorporating them into foods and beverages. In particular, butter or butter oil is used as an animal fat, and the cholesterol content in the oil is reduced.These dairy products are used as raw materials for the production of butter, margarine, reduced milk, cheese, ice cream, etc. When manufactured, dairy products with reduced cholesterol content can be obtained, making them useful as health foods.

【0011】次に本発明の実施例を挙げさらに具体的に
説明するが、本発明はこの実施例に限定されるものでは
ない。
Next, the present invention will be described in more detail with reference to Examples, but the present invention is not limited to these Examples.

【0012】[0012]

【実施例1】バターオイル500gをヘキサン:エタノー
ル:水混液(100:2:0.02)1000mlに溶解しSMB処理液
とした。溶離液は同様に、ヘキサン:エタノール:水混
液(100:2:0.02)4160mlを使用した。SMBは、カラム
の直径25mm長さ 460mmの6塔型で、各々シリカゲルSIL-
120-S50 (YMC社製)を充填した。運転条件は、処理
液供給量1.91ml/min、溶離液供給量7.93ml/min、エキス
トラクト抜き出し量2.72ml/min、ラフィネート抜き出し
量7.11ml/min、カラム温度40℃、ステップ時間 33.76分
とした。その結果目的回収液として、エキストラクトに
コレステロール含有画分溶液1430ml、ラフィネートにコ
レステロール除去画分溶液3730mlをそれぞれ得た。この
ラフィネートを濃縮乾固して、コレステロール低減油脂
481gを得た。
Example 1 500 g of butter oil was dissolved in 1000 ml of a hexane: ethanol: water mixed solution (100: 2: 0.02) to obtain an SMB treatment solution. Similarly, the eluent used was 4160 ml of a hexane: ethanol: water mixture (100: 2: 0.02). SMB is a 6-column type with a column diameter of 25 mm and a length of 460 mm.
120-S50 (YMC) was charged. The operating conditions were as follows: 1.91 ml / min of processing liquid supply, 7.93 ml / min of eluent supply, 2.72 ml / min of extract extraction, 7.11 ml / min of raffinate extraction, column temperature 40 ° C., step time 33.76 minutes. . As a result, 1430 ml of a cholesterol-containing fraction solution was obtained as an extract, and 3730 ml of a cholesterol-removed fraction solution was obtained as a raffinate. The raffinate is concentrated to dryness to reduce cholesterol-reducing fats and oils.
481 g was obtained.

【0013】実施例1で得たコレステロール低減油脂と
原料のバターオイルをヘキサンに溶解しHPLCにてコ
レステロール含量を測定した。結果を以下に示す。
The cholesterol-reducing fat and oil obtained in Example 1 and the raw material butter oil were dissolved in hexane, and the cholesterol content was measured by HPLC. The results are shown below.

【0014】[0014]

【実施例2】ラード200gをヘキサン:エタノール:水混
液(100:2:0.02) 1000mlに溶解し、SMB処理液とし
た。溶離液は同様に、ヘキサン:エタノール:水混液
(100:2:0.02) 3650mlを使用した。SMBは、カラムの
直径25mm長さ 460mmの6塔型で、各々シリカゲルSIL-12
0-S50 (YMC社製)を充填した。運転条件は、処理液
供給量2.85ml/min、溶離液供給量10.37ml/min 、エキス
トラクト抜き出し量3.67ml/min、ラフィネート抜き出し
量9.56ml/min、カラム温度40℃、ステップ時間 25.11分
とした。その結果目的回収液として、エキストラクトに
コレステロール含有画分溶液1290ml、ラフィネートにコ
レステロール除去画分溶液3360mlをそれぞれ得た。この
ラフィネートを濃縮乾固して、コレステロール低減油脂
188gを得た。
Example 2 200 g of lard was dissolved in 1000 ml of a mixture of hexane: ethanol: water (100: 2: 0.02) to obtain an SMB treatment solution. Similarly, 3650 ml of a mixture of hexane: ethanol: water (100: 2: 0.02) was used as the eluent. SMB is a 6-column type with a column diameter of 25 mm and a length of 460 mm.
0-S50 (YMC) was charged. The operating conditions were as follows: processing liquid supply amount 2.85 ml / min, eluent supply amount 10.37 ml / min, extract extraction amount 3.67 ml / min, raffinate extraction amount 9.56 ml / min, column temperature 40 ° C., step time 25.11 minutes. . As a result, 1290 ml of a cholesterol-containing fraction solution was obtained as an extract, and 3360 ml of a cholesterol-removed fraction solution was obtained as a raffinate. The raffinate is concentrated to dryness to reduce cholesterol-reducing fats and oils.
188 g were obtained.

【0015】実施例2で得たコレステロール低減油脂と
原料のラードとをヘキサンに溶解しHPLCにてコレス
テロール含量を測定した。結果を以下に示す。
[0015] The cholesterol-reducing oil and fat obtained in Example 2 and lard as a raw material were dissolved in hexane, and the cholesterol content was measured by HPLC. The results are shown below.

【0016】[0016]

【実施例3】バターオイル100gをヘキサン:エタノー
ル:水混液(100:2:0.02) 1000mlに溶解しSMB処理液
とした。溶離液は同様に、ヘキサン:エタノール:水混
液(100:2:0.02) 3700mlを使用した。SMBは、カラム
の直径25mm長さ 460mmの6塔型で、各々シリカゲルSIL-
120-S50 (YMC社製)を充填した。運転条件は、処理
液供給量2.74ml/min、溶離液供給量10.14ml/min 、エキ
ストラクト抜き出し量4.38ml/min、ラフィネート抜き出
し量8.50ml/min、カラム温度40℃、ステップ時間 25.77
分とした。その結果目的回収液として、エキストラクト
にコレステロール含有画分溶液1600ml、ラフィネートに
コレステロール除去画分溶液3100mlをそれぞれ得た。こ
のラフィネートを濃縮乾固して、コレステロール低減油
脂481gを得た。
Example 3 100 g of butter oil was dissolved in 1000 ml of a hexane: ethanol: water mixed solution (100: 2: 0.02) to obtain an SMB treatment liquid. Similarly, 3700 ml of a mixture of hexane: ethanol: water (100: 2: 0.02) was used as the eluent. SMB is a 6-column type with a column diameter of 25 mm and a length of 460 mm.
120-S50 (YMC) was charged. The operating conditions were as follows: processing solution supply rate 2.74 ml / min, eluent supply rate 10.14 ml / min, extract extraction rate 4.38 ml / min, raffinate extraction rate 8.50 ml / min, column temperature 40 ° C., step time 25.77.
Minutes. As a result, 1600 ml of a cholesterol-containing fraction solution was obtained as an extract and 3100 ml of a cholesterol-removed fraction solution was obtained as a raffinate. The raffinate was concentrated to dryness to obtain 481 g of a cholesterol-reducing oil and fat.

【0017】実施例3で得たコレステロール低減油脂と
バターオイルをヘキサンに溶解しHPLCにてコレステ
ロール含量を測定した。結果を以下に示す。
The cholesterol-reducing oil and butter oil obtained in Example 3 were dissolved in hexane, and the cholesterol content was measured by HPLC. The results are shown below.

【0018】[0018]

【参考例1】実施例1で得たコレステロール低減バター
オイル40重量%と脱脂乳60重量%を混合、乳化し還元ク
リームを調製した。さらにこの還元クリームを8℃に冷
却、8時間エージング後、通常のバター製造機によりコ
レステロール低減バターを製造した。ここで製造したコ
レステロール低減バターは、良好な風味を有するもので
あった。
Reference Example 1 40% by weight of the cholesterol-reduced butter oil obtained in Example 1 and 60% by weight of skim milk were mixed and emulsified to prepare a reduced cream. Further, this reduced cream was cooled to 8 ° C. and aged for 8 hours, and then a cholesterol-reduced butter was produced using a conventional butter producing machine. The cholesterol-reducing butter produced here had a good flavor.

【0019】[0019]

【参考例2】実施例1で得たコレステロール低減バター
オイル81重量%と脱脂乳17.6重量%および食塩 1.4重量
%を混合し、85℃で殺菌後、さらに60℃に冷却した。こ
の混合物を通常マーガリン製造に使用されている密閉型
表面掻取式熱交換機で冷却し、風味良好なコレステロー
ル低減バターを得た。
Reference Example 2 81% by weight of the cholesterol-reduced butter oil obtained in Example 1, 17.6% by weight of skim milk and 1.4% by weight of salt were mixed, sterilized at 85 ° C, and further cooled to 60 ° C. This mixture was cooled with a closed-type surface scraping heat exchanger usually used for the production of margarine to obtain a cholesterol-reducing butter having a good taste.

【0020】[0020]

【発明の効果】本発明の方法によると動物性油脂中のコ
レステロールを簡単を操作で短時間のうちに除去するこ
とができ、コレステロール含量の低減された動物性油脂
を高い収率で製造することができる。さらに、本発明の
方法によると、大量の動物性油脂を連続的に処理するこ
とができ、工業的有利な方法である。
According to the method of the present invention, cholesterol in animal fats and oils can be removed in a short time by a simple operation, and animal fats and oils with reduced cholesterol content can be produced in high yield. Can be. Further, according to the method of the present invention, a large amount of animal fats and oils can be continuously treated, which is an industrially advantageous method.

フロントページの続き (72)発明者 神武 正信 埼玉県坂戸市鶴舞3−11−13 (56)参考文献 特開 昭63−39991(JP,A) 特開 昭57−122099(JP,A) 特開 平3−100459(JP,A) (58)調査した分野(Int.Cl.6,DB名) C11B 3/10 A23D 9/007 C11B 3/00 G01N 30/44 G01N 30/46 Continuation of front page (72) Inventor Masanobu Jinbu 3-11-13 Tsurumai, Sakado-shi, Saitama (56) References JP-A-63-39991 (JP, A) JP-A-57-122099 (JP, A) Hei 3-100459 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) C11B 3/10 A23D 9/007 C11B 3/00 G01N 30/44 G01N 30/46

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 動物性油脂をヘキサン、エタノール及び
水よりなる混合溶媒もしくはヘキサン、アセトン、エタ
ノール及び水よりなる混合溶媒に溶解し、擬似移動床式
クロマト分離装置に供給し、コレステロール除去動物性
油脂画分とコレステロール含有画分とに分画し、得られ
たコレステロール除去動物性油脂画分より有機溶媒を除
去することを特徴とするコレステロール含量の低い動物
性油脂の製造法。
1. An animal oil or fat comprising hexane, ethanol and
Mixed solvent of water or hexane, acetone, eta
Cholesterol-free animal oil / fat fraction obtained by dissolving in a mixed solvent consisting of phenol and water , supplying the mixture to a simulated moving bed type chromatographic separator, and separating it into a cholesterol-free animal oil / fat fraction and a cholesterol-containing fraction. A method for producing an animal fat or oil having a low cholesterol content, characterized by removing an organic solvent.
【請求項2】 動物性油脂がラード、牛脂、魚油、乳脂
またはそれらの加工油脂である請求項1記載の製造法
2. Animal fats and oils such as lard, beef tallow, fish oil and milk fat
The method according to claim 1, which is a processed oil or fat thereof .
JP3357002A 1991-12-24 1991-12-24 Method for producing animal fats and oils with low cholesterol content Expired - Fee Related JP2993253B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3357002A JP2993253B2 (en) 1991-12-24 1991-12-24 Method for producing animal fats and oils with low cholesterol content

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3357002A JP2993253B2 (en) 1991-12-24 1991-12-24 Method for producing animal fats and oils with low cholesterol content

Publications (2)

Publication Number Publication Date
JPH05171177A JPH05171177A (en) 1993-07-09
JP2993253B2 true JP2993253B2 (en) 1999-12-20

Family

ID=18451872

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2993253B2 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
PE20070482A1 (en) 2005-08-26 2007-06-08 Ocean Nutrition Canada Ltd METHOD TO REMOVE AND / OR REDUCE STEROLS FROM OILS
US7977498B2 (en) 2005-08-26 2011-07-12 Ocean Nutrition Canada Limited Reduction of sterols and other compounds from oils
US9428711B2 (en) 2013-05-07 2016-08-30 Groupe Novasep Chromatographic process for the production of highly purified polyunsaturated fatty acids
EP2883860B1 (en) 2013-12-11 2016-08-24 Novasep Process Chromatographic method for producing polyunsaturated fatty acids
KR102165406B1 (en) 2014-01-07 2020-10-14 노바셉 프로세스 Process for purifying aromatic amino acids
KR102222043B1 (en) * 2020-08-07 2021-03-04 주식회사 동원에프앤비 Method of krill oil preparation and composition of krill oil

Also Published As

Publication number Publication date
JPH05171177A (en) 1993-07-09

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