JPH04370195A - Method for deacidifying oil and fat - Google Patents

Method for deacidifying oil and fat

Info

Publication number
JPH04370195A
JPH04370195A JP14858591A JP14858591A JPH04370195A JP H04370195 A JPH04370195 A JP H04370195A JP 14858591 A JP14858591 A JP 14858591A JP 14858591 A JP14858591 A JP 14858591A JP H04370195 A JPH04370195 A JP H04370195A
Authority
JP
Japan
Prior art keywords
oils
fats
oil
deacidifying
fat
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.)
Granted
Application number
JP14858591A
Other languages
Japanese (ja)
Other versions
JP2987234B2 (en
Inventor
Toshiyuki Hirokawa
敏幸 廣川
Kenji Miki
研司 三木
Shoshi Maruzeni
丸銭 詔司
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.)
Adeka Corp
Original Assignee
Asahi Denka Kogyo 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 Asahi Denka Kogyo KK filed Critical Asahi Denka Kogyo KK
Priority to JP3148585A priority Critical patent/JP2987234B2/en
Publication of JPH04370195A publication Critical patent/JPH04370195A/en
Application granted granted Critical
Publication of JP2987234B2 publication Critical patent/JP2987234B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To obtain a deacidifying method of oil and fat capable of suppressing production of emulsion and deacidifying in good state when oil and fat are deacidified by Jenice method. CONSTITUTION:In a method for carrying out deacidification of oils and fats using an aqueous alkali solution by Jenice method, an aqueous alkali solution to which 1.0-10.0wt.% water soluble alcohol is added is used as the aqueous alkali solution.

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、油脂の脱酸方法に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for deoxidizing fats and oils.

【0002】0002

【従来の技術】油脂の脱酸は、油脂中の遊離脂肪酸の除
去を主目的としているが、同時にガム質、色素、金属等
の微量成分を除去し、漂白、硬化、脱臭等の次工程の効
率を良好にするものである。即ち、脱酸精製の良否が油
脂の品質向上の主要因の一つで、脱酸は油脂精製工程の
重要な工程である。
[Prior Art] The main purpose of deacidification of fats and oils is to remove free fatty acids from fats and oils, but it also removes trace components such as gums, pigments, and metals, which can be used in subsequent processes such as bleaching, curing, and deodorization. This improves efficiency. That is, the quality of deacidification and refining is one of the main factors in improving the quality of fats and oils, and deacidification is an important step in the refining process of fats and oils.

【0003】油脂の脱酸方法は、大別して蒸留脱酸法と
アルカリ脱酸法があるが、遊離脂肪酸の除去以外に、付
帯効果の大きいアルカリ脱酸法が主流になっている。ア
ルカリ脱酸法は、従来、連続遠心分離法による脱酸が主
体であったが、最近この方法よりもコストが安く、中性
油の損失の少ないゼニス法が使用されるようになってき
ている。
[0003] Methods for deoxidizing fats and oils can be broadly classified into distillation deoxidation methods and alkaline deoxidation methods, but the alkali deoxidation method is the mainstream, as it has a large additional effect in addition to removing free fatty acids. Traditionally, alkaline deoxidation methods have mainly involved deoxidation using continuous centrifugation, but recently the Zenith method, which is cheaper than this method and causes less loss of neutral oil, has come into use. .

【0004】ゼニス法は、下記のリン酸処理工程、脱酸
工程及び漂白工程の3つの半連続工程からなっている。 リン酸処理工程:真空下で油脂にリン酸を添加すること
により、ガム質等を取り除く工程。 脱酸工程:ゼニス法の中心部で、水酸化ナトリウム水溶
液を満たした中和カラムの底部より油脂を導入し、導入
した油脂を0.5〜3.0mmの油滴にして水酸化ナト
リウム水溶液中を上昇させて遊離脂肪酸を取り除く工程
The Zenith process consists of three semi-continuous steps: a phosphoric acid treatment step, a deacidification step and a bleaching step. Phosphoric acid treatment process: A process in which gums, etc. are removed by adding phosphoric acid to fats and oils under vacuum. Deacidification step: At the center of the Zenith method, fats and oils are introduced from the bottom of the neutralization column filled with an aqueous sodium hydroxide solution, and the introduced fats and oils are made into oil droplets of 0.5 to 3.0 mm and placed in an aqueous sodium hydroxide solution. The process of removing free fatty acids by increasing the

【0005】漂白工程:油脂に残存する石鹸分を除き、
活性白土にて油脂の色調を良好にする工程。現在、ゼニ
ス法は、魚油、豚脂、牛脂、ヤシ油、ナタネ油、パーム
油等の油脂の脱酸方法として実用化が図られている。し
かし、パーム油等の植物油脂は脱酸時にエマルジョンが
生成し易く、実用化が難しい。特に、高酸価の油脂は脱
酸を行うとすぐにエマルジョンが生成するという状態で
、いまだに実用化されていない。
[0005] Bleaching process: Removes soap content remaining in fats and oils,
A process to improve the color tone of oils and fats using activated clay. Currently, the Zenith method is being put into practical use as a method for deoxidizing fats and oils such as fish oil, lard, beef tallow, coconut oil, rapeseed oil, and palm oil. However, vegetable oils such as palm oil tend to form emulsions during deacidification, making it difficult to put them into practical use. In particular, oils and fats with high acid values form emulsions immediately upon deacidification, and have not yet been put to practical use.

【0006】また、特開昭50−103506号公報に
は、水溶性アルコールを添加したアルカリ水溶液で油脂
を脱酸する方法が記載されているが、該公報に記載の脱
酸方法は、遠心分離機を利用して油脂と石鹸分を分離す
るもので、ゼニス法のように遠心分離機を使用せずに油
脂と石鹸分を分離するものではない。
[0006] Furthermore, JP-A-50-103506 describes a method of deoxidizing fats and oils with an alkaline aqueous solution to which a water-soluble alcohol has been added. This method uses a machine to separate fats and soaps from fats and oils, and does not use a centrifuge to separate fats and soaps like the Zenith method.

【0007】[0007]

【発明が解決しようとする課題】ゼニス法で、パーム油
等の植物油脂の脱酸を行うと、脱酸時にエマルジョンが
生成し、アルカリ水溶液と油脂を分離することができず
、脱酸油の収率の低下、脱酸油の石鹸含量の増加といっ
た問題が起こり、次工程の漂白、硬化、脱臭の効率が悪
くなる原因になる。このため、ゼニス法で油脂の脱酸を
行う場合、脱酸時のエマルジョンの生成を抑える方法の
開発が望まれていた。
[Problems to be Solved by the Invention] When vegetable oils such as palm oil are deacidified using the Zenith method, an emulsion is formed during deoxidation, making it impossible to separate the alkaline aqueous solution and the oil. Problems such as a decrease in yield and an increase in the soap content of the deoxidized oil occur, which causes a decrease in the efficiency of the next steps of bleaching, curing, and deodorization. Therefore, when deacidifying fats and oils using the Zenith method, it has been desired to develop a method that suppresses the formation of emulsions during deacidification.

【0008】従って、本発明の目的は、ゼニス法で油脂
を脱酸する際に、エマルジョンの生成を抑制し、良好に
脱酸することができる油脂の脱酸方法を提供することに
ある。
[0008] Accordingly, an object of the present invention is to provide a method for deacidifying fats and oils by suppressing the formation of emulsions when deacidifying fats and oils using the Zenith method and capable of achieving good deoxidation.

【0009】[0009]

【課題を解決するための手段】本発明者らは、鋭意研究
した結果、ゼニス法で油脂を脱酸する際に、アルカリ水
溶液中に特定量の水溶性アルコールを添加することによ
り、上記目的を達成できることを知見した。本発明は、
上記知見に基づきなされたもので、アルカリ水溶液を用
いて油脂の脱酸を行うゼニス法による油脂の脱酸方法に
おいて、アルカリ水溶液として、水溶性アルコールを1
.0〜10.0重量%添加したアルカリ水溶液を用いる
ことを特徴とする油脂の脱酸方法を提供するものである
[Means for Solving the Problems] As a result of intensive research, the present inventors have found that the above objective can be achieved by adding a specific amount of water-soluble alcohol to an alkaline aqueous solution when deoxidizing fats and oils using the Zenith method. I learned that it can be achieved. The present invention
This was done based on the above knowledge, and in the Zenith method of deoxidizing fats and oils using an alkaline aqueous solution, one water-soluble alcohol is added as an alkaline aqueous solution.
.. The present invention provides a method for deoxidizing fats and oils, which is characterized by using an aqueous alkali solution containing 0 to 10.0% by weight.

【0010】以下、本発明の油脂の脱酸方法について詳
述する。本発明で用いられる水溶性アルコールとしては
、エタノール、プロパノール、イソプロパノール等が挙
げられる。上記水溶性アルコールの添加量は、アルカリ
水溶液中1.0〜10.0重量%、好ましくは3.0〜
10.0重量%である。
[0010] The method for deoxidizing fats and oils of the present invention will be described in detail below. Examples of the water-soluble alcohol used in the present invention include ethanol, propanol, isopropanol, and the like. The amount of the water-soluble alcohol added is 1.0 to 10.0% by weight, preferably 3.0 to 10.0% by weight in the alkaline aqueous solution.
It is 10.0% by weight.

【0011】上記水溶性アルコールの添加量が1.0重
量%未満では、濃度が低すぎてエマルジョンの生成を抑
制することができない。また、上記水溶性アルコールの
添加量が10.0重量%を超えても、エマルジョン生成
の抑制効果の向上はほとんど認められない。また、本発
明で用いられるアルカリ水溶液としては、水酸化ナトリ
ウム水溶液、水酸化カリウム水溶液等が挙げられる。ま
た、上記アルカリ水溶液は、アルカリ濃度が0.05〜
2規定のものが好ましい。
[0011] If the amount of the water-soluble alcohol added is less than 1.0% by weight, the concentration is too low and the formation of an emulsion cannot be suppressed. Furthermore, even if the amount of the water-soluble alcohol added exceeds 10.0% by weight, little improvement in the effect of suppressing emulsion formation is observed. Furthermore, examples of the alkaline aqueous solution used in the present invention include a sodium hydroxide aqueous solution and a potassium hydroxide aqueous solution. Further, the alkaline aqueous solution has an alkaline concentration of 0.05 to
2 standard is preferred.

【0012】本発明の油脂の脱酸方法は、ゼニス法にお
ける脱酸工程において用いられるアルカリ水溶液として
、上記水溶性アルコールを1.0〜10.0重量%添加
した上記アルカリ水溶液を用いて油脂を脱酸する以外は
、通常のゼニス法と同じ工程である。本発明の油脂の脱
酸方法は、魚油、豚脂、牛脂等の動物油脂、ナタネ油、
パーム油、ヤシ油、サル脂、シア脂等の植物油脂に使用
できる。
[0012] The method for deoxidizing fats and oils of the present invention is to deoxidize fats and oils using the aqueous alkaline solution to which 1.0 to 10.0% by weight of the water-soluble alcohol is added as the alkaline aqueous solution used in the deoxidizing step in the Zenith method. The process is the same as the normal Zenith method except for deoxidation. The method for deoxidizing fats and oils of the present invention includes animal fats and oils such as fish oil, lard, and beef tallow, rapeseed oil,
Can be used with vegetable oils such as palm oil, coconut oil, monkey fat, shea butter, etc.

【0013】[0013]

【実施例】以下に実施例を挙げて、更に本発明を説明す
るが、本発明はこれらに限定されるものではない。尚、
以下の%は特に指定の無い限り重量基準である。 実施例1〜3 サル脂原油(AV;5.69)3kgに対して65℃で
リン酸を0.3%添加し、15分間攪拌し、油不溶解物
を取り除いた。
[Examples] The present invention will be further explained with reference to Examples below, but the present invention is not limited thereto. still,
The following percentages are by weight unless otherwise specified. Examples 1 to 3 0.3% phosphoric acid was added to 3 kg of sal fat crude oil (AV; 5.69) at 65° C., and the mixture was stirred for 15 minutes to remove oil-insoluble substances.

【0014】次いで、エタノールを1.0%、3.0%
、5.0%添加した0.5規定の水酸化ナトリウム水溶
液(75℃)8リットルの入っているカラム(ゼニス脱
酸塔)の底から、リン酸処理した油脂を導入(30ml
/min )し、導入した油脂を多孔板で直径1〜2m
mの油滴にして水酸化ナトリウム水溶液中を上昇させて
脱酸を行った。
[0014] Next, ethanol was added at 1.0% and 3.0%.
A phosphoric acid-treated fat and oil was introduced from the bottom of a column (Zenith deoxidation tower) containing 8 liters of a 0.5 N aqueous sodium hydroxide solution (75°C) containing 5.0% of phosphoric acid (30 ml).
/min), and the introduced oil and fat are spread on a perforated plate with a diameter of 1 to 2 m.
Deoxidation was carried out by forming oil droplets of m in size and raising the droplets in an aqueous sodium hydroxide solution.

【0015】その結果(脱酸時のエマルジョン発生率、
得られた脱酸油の酸価、石鹸含量、及び収率)を下記表
1に示す。 実施例4〜7 エタノール添加量を3.0%と固定し、水酸化ナトリウ
ム水溶液の濃度を0.05、0.15、0.35、0.
70規定とした以外は実施例1と同様な処理を行った。
Results (emulsion generation rate during deoxidation,
The acid value, soap content, and yield of the obtained deacidified oil are shown in Table 1 below. Examples 4 to 7 The amount of ethanol added was fixed at 3.0%, and the concentration of the sodium hydroxide aqueous solution was changed to 0.05, 0.15, 0.35, 0.
The same process as in Example 1 was performed except that the standard was 70.

【0016】その結果を下記表2に示す。 比較例1〜4 0.15、0.35、0.50、0.70規定の水酸化
ナトリウム水溶液(アルコール無添加)にリン酸処理し
たサル脂を導入した以外は実施例1と同様にして脱酸を
行った。
The results are shown in Table 2 below. Comparative Examples 1 to 4 Same as Example 1 except that phosphoric acid treated monkey fat was introduced into 0.15, 0.35, 0.50, 0.70 N aqueous sodium hydroxide solution (no alcohol added). Deacidification was performed.

【0017】その結果を下記表2に示す。尚、実施例2
及び比較例1の結果は、便宜上、下記の表1及び表2の
両方に記載した。また、下記の表1及び表2における*
1、*2及び*3は次の注釈を示す。*1  エマルジ
ョン発生率(%)は、図1のようにして測定。即ち、油
脂の脱酸直後のカラム(ゼニス脱酸塔)内の油相量L及
びエマルジョン相量lを求め、下式により算出。
The results are shown in Table 2 below. In addition, Example 2
The results of Comparative Example 1 are listed in both Table 1 and Table 2 below for convenience. In addition, * in Table 1 and Table 2 below
1, *2 and *3 indicate the following notes. *1 Emulsion occurrence rate (%) was measured as shown in Figure 1. That is, the oil phase amount L and emulsion phase amount L in the column (Zenith deoxidation tower) immediately after deoxidizing fats and oils are determined, and calculated using the following formula.

【0018】     エマルジョン発生率(%)=〔l/(L+l)
〕×100*2  石鹸はオレイン酸ナトリウムとして
計算。 *3  脱酸油の収率(%)は、下式により算出。 〔(脱酸油の重量)/(原油の重量)〕×100
Emulsion incidence (%) = [l/(L+l)
]×100*2 Soap is calculated as sodium oleate. *3 The yield (%) of deoxidized oil is calculated using the formula below. [(Weight of deoxidized oil)/(Weight of crude oil)] x 100

【00
19】
00
19]

【表1】〔アルコール添加量とエマルジョン発生率との
関係〕
[Table 1] [Relationship between amount of alcohol added and emulsion generation rate]

【0020】[0020]

【表2】〔水酸化ナトリウム水溶液の濃度とエマルジョ
ン発生率との関係〕
[Table 2] [Relationship between concentration of sodium hydroxide aqueous solution and emulsion generation rate]

【0021】[0021]

【発明の効果】本発明の油脂の脱酸方法によれば、ゼニ
ス法で油脂を脱酸する際に、従来脱酸時に発生していた
エマルジョンが発生せずに、良好に脱酸することができ
る。
[Effects of the Invention] According to the method for deacidifying fats and oils of the present invention, when deacidifying fats and oils using the Zenith method, the emulsion that conventionally occurs during deoxidation is not generated, and the deoxidation can be performed well. can.

【図面の簡単な説明】[Brief explanation of drawings]

【図1】図1は、エマルジョン発生率の算出手段を示す
説明図である。
FIG. 1 is an explanatory diagram showing means for calculating the emulsion incidence rate.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  アルカリ水溶液を用いて油脂の脱酸を
行うゼニス法による油脂の脱酸方法において、アルカリ
水溶液として、水溶性アルコールを1.0〜10.0重
量%添加したアルカリ水溶液を用いることを特徴とする
油脂の脱酸方法。
Claim 1: In a Zenith method of deoxidizing fats and oils using an aqueous alkaline solution, an aqueous alkaline solution to which 1.0 to 10.0% by weight of a water-soluble alcohol is added is used as the aqueous alkaline solution. A method for deoxidizing fats and oils.
JP3148585A 1991-06-20 1991-06-20 Deacidification of fats and oils Expired - Fee Related JP2987234B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3148585A JP2987234B2 (en) 1991-06-20 1991-06-20 Deacidification of fats and oils

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3148585A JP2987234B2 (en) 1991-06-20 1991-06-20 Deacidification of fats and oils

Publications (2)

Publication Number Publication Date
JPH04370195A true JPH04370195A (en) 1992-12-22
JP2987234B2 JP2987234B2 (en) 1999-12-06

Family

ID=15456040

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3148585A Expired - Fee Related JP2987234B2 (en) 1991-06-20 1991-06-20 Deacidification of fats and oils

Country Status (1)

Country Link
JP (1) JP2987234B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0979860A1 (en) * 1998-08-11 2000-02-16 Societe Des Produits Nestle S.A. Fat refining
JP2006083343A (en) * 2004-09-17 2006-03-30 Kao Corp Method for producing fat and oil including reduced amount of free fatty acid

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0979860A1 (en) * 1998-08-11 2000-02-16 Societe Des Produits Nestle S.A. Fat refining
WO2000009637A1 (en) * 1998-08-11 2000-02-24 Societe Des Produits Nestle S.A. Process for refining fatty substances
AU752423B2 (en) * 1998-08-11 2002-09-19 Societe Des Produits Nestle S.A. Process for refining fatty substances
US6506916B2 (en) 1998-08-11 2003-01-14 Nestec S.A. Process for refining fatty substances
JP2006083343A (en) * 2004-09-17 2006-03-30 Kao Corp Method for producing fat and oil including reduced amount of free fatty acid
JP4568565B2 (en) * 2004-09-17 2010-10-27 花王株式会社 Method for producing fats and oils with reduced free fatty acids

Also Published As

Publication number Publication date
JP2987234B2 (en) 1999-12-06

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