JPH07197075A - Refinement of crude edible vegetable oil - Google Patents

Refinement of crude edible vegetable oil

Info

Publication number
JPH07197075A
JPH07197075A JP5352171A JP35217193A JPH07197075A JP H07197075 A JPH07197075 A JP H07197075A JP 5352171 A JP5352171 A JP 5352171A JP 35217193 A JP35217193 A JP 35217193A JP H07197075 A JPH07197075 A JP H07197075A
Authority
JP
Japan
Prior art keywords
chlorophyll
acid
amount
oil
crude oil
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.)
Pending
Application number
JP5352171A
Other languages
Japanese (ja)
Inventor
Yoshimitsu Kon
潤 今義
Akio Oishi
章夫 大石
Masaji Oonuki
全事 大貫
Hirotaka Yo
宏宇 葉
Natsuko Ichikawa
奈津子 市川
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.)
Honen Corp
Original Assignee
Honen 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 Honen Corp filed Critical Honen Corp
Priority to JP5352171A priority Critical patent/JPH07197075A/en
Publication of JPH07197075A publication Critical patent/JPH07197075A/en
Pending legal-status Critical Current

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  • Edible Oils And Fats (AREA)
  • Fats And Perfumes (AREA)

Abstract

PURPOSE:To refine a crude edible vegetable oil economically advantageously by simply and effectively reducing the amount of the adsorbent used in a decolorization step by adding sulfuric acid to a crude edible vegetable oil and simultaneously effecting the separation of soap and the removal of a chlorophyll pigment in an alkali refining step. CONSTITUTION:This refinement process comprises adding sulfuric acid as the acid used in the acid treatment in a step of refining a crude edible vegetable oil with an aqueous alkali solution, and simultaneously effecting the separation of soap and the removal of a chlorophyll pigment in the alkali refinement step. According to this process, a suitable amount (>=0.05%) of concentrated sulfuric acid is added to a crude edible vegetable oil of 30-60 deg.C, and the resulting mixture is agitated for 10-60 min. An alkali is then added to the mixture to neutralize it, and the formed free fatty acid soap is separated. A chlorophyll pigment also can be removed effectively and simultaneously. When the amount of the sulfuric acid added is 0.05% or below, the effect of removing a chlorophyll pigment can not be attained, whereas, when this amount is excessive, the quality of the finished oil is adversely affected.

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、食用植物原油中のクロ
ロフィル系色素の分解除去、特にアルカリ水溶液を用い
る脱酸工程の酸処理において、酸として硫酸を使用し、
アルカリ脱酸工程における石鹸の分離と共にクロロフィ
ル系色素分解物を除去する食用植物原油の精製法に関す
るものである。ここでいう酸処理とは、油糧種子から圧
搾及び、又は抽出で採油した食用植物粗油を水和によっ
て析出する親水性ガム質を除去する脱ガム工程を経た食
用植物原油につき、油溶性ガム質として油脂中に金属と
結合した状態で溶解しているフォスファチド等の不純物
中の金属をキレートできる各種の酸を用いて油溶性ガム
質を親水性に変えて分離しやすくする処理をいう。従
来、この目的としてリン酸、酢酸、クエン酸、修酸、マ
レイン酸、タンニン酸、酒石酸などの酸が用いられてき
た。この際、酸の添加量は、原油中の油溶性ガム質残存
量に応じて適宜変え、アルカリ中和にて生成した遊離脂
肪酸石鹸の乳化を防止して、分離性が最も良い状態を作
るために適した量を使用するのが一般的である。
FIELD OF THE INVENTION The present invention uses sulfuric acid as an acid in the decomposition and removal of chlorophyll-based pigments in edible plant crude oil, especially in the acid treatment in the deoxidation step using an alkaline aqueous solution.
The present invention relates to a method for refining edible plant crude oil which removes chlorophyll-based pigment decomposition products as well as separating soap in an alkaline deoxidizing step. The acid treatment referred to here is an edible vegetable crude oil that has been subjected to a degumming step of removing a hydrophilic gum substance that is precipitated by squeezing and / or extraction of edible vegetable crude oil from oil seeds, and an oil-soluble gum. As a quality, it refers to a treatment in which an oil-soluble gum substance is made hydrophilic by using various acids capable of chelating a metal in impurities such as phosphatide dissolved in a state of being bound to a metal in fats and oils to facilitate separation. Conventionally, acids such as phosphoric acid, acetic acid, citric acid, oxalic acid, maleic acid, tannic acid and tartaric acid have been used for this purpose. At this time, the addition amount of the acid is appropriately changed according to the amount of the oil-soluble gum substance remaining in the crude oil to prevent the emulsification of the free fatty acid soap generated by the alkali neutralization and to make the state of the best separability. It is common to use an amount suitable for.

【0002】[0002]

【従来の技術】これまでクロロフィル系色素を多く含ん
だ食用植物精製油は、緑色が強く商品価値が低いばかり
でなく、日光、蛍光灯などの光による保存中の劣化を受
けやすいため食用植物原油の精製において、このクロロ
フィル系色素をより経済的に、しかも極力除去すること
が重要な技術であった。
BACKGROUND OF THE INVENTION Up to now, refined edible plant oils containing a large amount of chlorophyll pigment have not only a strong green color and low commercial value, but also are susceptible to deterioration during storage due to sunlight, fluorescent light, etc. It was an important technique to purify the chlorophyll-based dye more economically and as much as possible in the purification.

【0003】その方法としては、食用植物原油中の着色
成分を除去して淡色に仕上げる脱色工程で活性白土等の
吸着剤に吸着させて除去する方法が一般的である。
[0003] As a method therefor, it is common to remove a coloring component in edible plant crude oil by adsorbing it on an adsorbent such as activated clay in a decoloring step of finishing to a light color.

【0004】[0004]

【発明が解決しようとする課題】従来知られている脱色
工程での活性白土吸着による処理では、食用植物原油中
に含まれるクロロフィル系色素の量が多いほど吸着剤の
使用量が増え、コストアップとなり、しかも廃白土の量
が増えて産業廃棄物の増大となる。これらの欠点を生じ
ることなくクロロフィル系色素を除去する精製法が要望
されていた。
In the treatment by active clay adsorption in the conventionally known decolorization process, the larger the amount of chlorophyll pigment contained in the edible plant crude oil, the more the amount of the adsorbent used and the cost increase. In addition, the amount of white clay will increase and the amount of industrial waste will increase. There has been a need for a purification method that removes chlorophyll-based dyes without causing these drawbacks.

【0005】これに対して、1)脱色工程での吸着剤の
使用量を軽減するため活性白土と活性炭の二段階で脱色
してクロロフィル等の色素類を除去する方法(特開昭5
6−21554号公報)、2)脱酸工程前に濃硫酸を添
加混合し、クロロフィル系色素の90%以上を析出さ
せ、これを除去し、次いで湯洗いする方法(特公平1−
50357号公報)等が提案されている。
On the other hand, 1) a method for removing pigments such as chlorophyll by decolorizing in two steps of activated clay and activated carbon in order to reduce the amount of the adsorbent used in the decolorization step (Japanese Patent Laid-Open No. Sho 5).
6-21554), 2) A method in which concentrated sulfuric acid is added and mixed before the deoxidation step to precipitate 90% or more of the chlorophyll-based dye, which is removed and then washed with hot water (Patent Publication 1-
No. 50357) has been proposed.

【0006】しかしながら、1)の方法では脱酸油中に
含まれるクロロフィル系色素が多いほど吸着剤の使用量
が増える傾向は変わらず、処理後の廃白土、廃活性炭の
処理の大幅な改善にはならない。2)の方法では、脱ガ
ム原油をアルカリ水溶液を用いる脱酸工程に入る直前に
濃硫酸処理し、析出物を遠心分離等で分離除去した後に
湯洗いすることによりクロロフィル系色素を除去するも
ので、脱色工程での吸着剤処理の負荷を軽減する利点が
あるものの、この処理に遠心分離、湯洗いという工程が
付加され処理が煩雑になり、設備の変更や作業効率の低
下が伴うと共に、湯洗い工程で油と温水が激しい乳化物
を形成し、油水の分離が極めて困難に陥り、作業不可能
となることもある。さらに、この湯洗い分離工程で手間
取ると油中のトコフェロールの分解も激しくなり、精製
油の品質劣化をもたらす原因となることも予想される、
等の問題点も多く、さらに簡易な方法が求められてい
た。
However, in the method 1), the more the amount of the chlorophyll-based pigment contained in the deoxidized oil, the more the amount of the adsorbent used does not change, and the treatment of the waste clay and the activated carbon after treatment is greatly improved. Don't In the method 2), the degummed crude oil is treated with concentrated sulfuric acid immediately before entering the deoxidation step using an aqueous alkaline solution, and the precipitate is separated and removed by centrifugation or the like, followed by washing with hot water to remove the chlorophyll-based pigment. Although it has the advantage of reducing the load of adsorbent treatment in the decolorization process, the process of centrifugation and hot water washing is added to this process, which complicates the process, changes equipment, and lowers work efficiency. In the washing process, oil and hot water form a violent emulsion, which makes separation of oil and water extremely difficult, which makes work impossible. Furthermore, if it takes time in this hot water separation step, the decomposition of tocopherols in the oil will become severe, and it is expected that it will cause deterioration of the quality of the refined oil.
There are many problems such as the above, and a simpler method has been demanded.

【0007】本発明の目的は、食用植物原油中のクロロ
フィル系色素を除去するに際しての、かかる問題点を克
服し、煩雑な工程を付与することなく、簡易にしかも効
果的にクロロフィル系色素を除去して脱色工程で使用す
る吸着剤を削減して、産業廃棄物量の減少及び製品の歩
留まり向上を図ることができる食用植物原油の精製法を
提供せんとするものである。
The object of the present invention is to remove chlorophyll-based pigments in edible plant crude oil by overcoming such problems and removing chlorophyll-based pigments easily and effectively without adding complicated steps. Then, the adsorbent used in the decolorization process is reduced to provide a method for refining edible plant crude oil which can reduce the amount of industrial waste and improve the product yield.

【0008】[0008]

【課題を解決するための手段】上記課題を解決するため
に、本発明者らは鋭意検討を重ねた結果、食用植物原油
のアルカリ水溶液を用いる脱酸工程の酸処理において、
酸として硫酸を使用することによって、アルカリ脱酸工
程における石鹸分の分離と同時に効果的にクロロフィル
系色素を除去できることを見出し、本発明を完成した。
In order to solve the above problems, the inventors of the present invention have conducted extensive studies, and as a result, in the acid treatment in the deoxidation step using an alkaline aqueous solution of edible plant crude oil,
The inventors have found that the use of sulfuric acid as an acid allows the chlorophyll-based dye to be effectively removed at the same time as the separation of the soap component in the alkaline deoxidizing step, and has completed the present invention.

【0009】すなわち、本発明は、食用植物原油のアル
カリ水溶液を用いる脱酸工程の酸処理において、硫酸を
添加して原油を攪拌してクロロフィル系色素を一次分解
し、さらにアルカリ中和によって分解を進め、アルカリ
によって生成した遊離脂肪酸石鹸と共にクロロフィル系
色素を除去することを特徴とする食用植物原油の精製法
である。食用植物原油に添加する硫酸の量は0.05%
以上で、クロロフィル系色素の油中濃度に応じて適量添
加することを特徴とするものである。添加する硫酸の量
は、原油中のクロロフィル系色素含量が30ppm 以下で
あれば0.05%以上で好ましくは0.1%前後、30
〜50ppm であれば0.1〜0.2%、50〜70ppm
であれば0.2〜0.3%、70〜100ppm であれば
0.3〜0.5%と順次増量するとよい。
That is, according to the present invention, in the acid treatment of the deoxidation step using an alkaline aqueous solution of edible plant crude oil, sulfuric acid is added to stir the crude oil to primarily decompose the chlorophyll-based pigment, and further decompose by alkali neutralization. This is a method for refining edible plant crude oil, which is characterized by removing chlorophyll pigments together with free fatty acid soap produced by alkali. The amount of sulfuric acid added to edible vegetable crude oil is 0.05%
As described above, the chlorophyll-based pigment is characterized by being added in an appropriate amount according to the concentration in the oil. The amount of sulfuric acid to be added is 0.05% or more, preferably around 0.1%, and 30% if the content of chlorophyll pigment in the crude oil is 30 ppm or less.
If ~ 50ppm, 0.1-0.2%, 50-70ppm
If it is 70 to 100 ppm, the amount should be increased sequentially to 0.3 to 0.5%.

【0010】従来、酸処理としてリン酸、酢酸、クエン
酸、修酸、マレイン酸、タンニン酸、酒石酸などの酸が
用いられてきたが、これらを用いる場合はクロロフィル
系色素の除去に対する効果は極めて少ないか、殆どな
い。
Conventionally, acids such as phosphoric acid, acetic acid, citric acid, oxalic acid, maleic acid, tannic acid and tartaric acid have been used as an acid treatment, but when these are used, the effect on the removal of chlorophyll dyes is extremely high. Few or almost none.

【0011】例えば、菜種種子に含まれるクロロフィル
は、搾油の工程で大部分がマグネシウム原子の外れたフ
ェオフィチンに変化して油中に溶け込んでくる。強酸で
ある硫酸は、そのフェオフィチンに作用して、フェオフ
ィチンに結合している親油性のフィチル基を切断して親
水性のフェオフォルビドへと変化させる。フェオフォル
ビドは、その後のアルカリ処理によって変化がさらに進
み、除去しやすい物質に分解されたり、あるいはそのま
まの状態で、遊離脂肪酸石鹸に吸着されて除去される。
本発明によれば、他の食用植物原油に含まれるクロロフ
ィルも同様に変化して除去される。
For example, most of the chlorophyll contained in rapeseed seeds is converted into pheophytin from which magnesium atoms have been removed in the oil pressing step and dissolved in the oil. Sulfuric acid, which is a strong acid, acts on the pheophytin to cleave the lipophilic phytyl group bound to pheophytin and convert it to hydrophilic pheophorbide. Pheophorbide is further changed by the subsequent alkali treatment and decomposed into a substance that can be easily removed, or it is adsorbed by the free fatty acid soap and removed as it is.
According to the present invention, chlorophyll contained in other edible plant crude oils is similarly changed and removed.

【0012】本発明の場合は、30〜60℃の食用植物
原油をアルカリ水溶液を用いる脱酸工程の酸処理におい
て、濃硫酸の0.05%以上の適量を添加し、10〜6
0分攪拌する。その後常法に従いアルカリを添加、中和
し、遊離脂肪酸石鹸を分離除去する。この時、同時にク
ロロフィル系色素も効果的に除去できる。
In the case of the present invention, an edible vegetable crude oil at 30 to 60 ° C. is treated with an alkaline aqueous solution in an acid treatment in a deoxidation step by adding an appropriate amount of 0.05% or more of concentrated sulfuric acid to give 10 to 6
Stir for 0 minutes. After that, an alkali is added and neutralized according to a conventional method to separate and remove free fatty acid soap. At this time, the chlorophyll-based dye can also be effectively removed at the same time.

【0013】硫酸の添加量は、食用植物原油のクロロフ
ィル系色素含量により調整するが、添加量が0.05%
以下であるとクロロフィル系色素の除去効果がなく、添
加量が過多であると仕上げ油の品質に悪影響を及ぼす。
The amount of sulfuric acid added is adjusted depending on the chlorophyll-based pigment content of edible plant crude oil.
If the amount is less than the above, the effect of removing the chlorophyll-based dye is not provided, and if the amount added is too large, the quality of the finishing oil is adversely affected.

【0014】本発明は、油糧種子(大豆、菜種、とうも
ろこし、ひまわり、綿実、紅花、胡麻、米糠、等)や果
肉(パーム)から搾油された食用植物原油に適用でき
る。
The present invention is applicable to oil seeds (soybean, rapeseed, corn, sunflower, cottonseed, safflower, sesame, rice bran, etc.) and edible plant crude oil extracted from pulp (palm).

【0015】[0015]

【実施例】以下に本発明の実施例を示すが、本発明の主
旨はもとより、これに限定されるものではない。
EXAMPLES Examples of the present invention will be shown below, but the present invention is not limited to the gist of the present invention.

【0016】実施例1 菜種種子から圧搾及び抽出で採油した菜種粗油を水和に
よってガム質を除去した脱ガム菜種原油でクロロフィル
系色素含量の異なるもの4種類(原油A:6.5ppm ,
原油B:35.4ppm ,原油C:42.6ppm ,原油
D:54.8ppm)に対して種々の量の98%濃硫酸を
添加し、40℃にて40分攪拌した後、常法に従いアル
カリ脱酸を行った。原油中のクロロフィル含量に適した
量の硫酸を添加することにより、4種類の原油の脱酸工
程後のクロロフィル系色素は1ppm程度まで低減され
た。
Example 1 Degummed rapeseed crude oil obtained by degumming rapeseed crude oil obtained by pressing and extraction from rapeseed seeds and having different chlorophyll pigment contents (crude oil A: 6.5 ppm,
Crude oil B: 35.4 ppm, crude oil C: 42.6 ppm, crude oil D: 54.8 ppm) was added with various amounts of 98% concentrated sulfuric acid, and the mixture was stirred at 40 ° C. for 40 minutes, and then alkali-treated according to a conventional method. Deoxidation was performed. By adding sulfuric acid in an amount suitable for the chlorophyll content in crude oil, the amount of chlorophyll-based pigments after the deoxidation process of four types of crude oil was reduced to about 1 ppm.

【0017】比較例1 実施例1で用いた4種類の脱ガム菜種原油に対して種々
の量の75%リン酸を添加し、以後実施例1と同様の処
理をした。4種類の原油の脱酸工程後のクロロフィル系
色素は添加したリン酸の量に関わらずほとんど低減され
なかった。
Comparative Example 1 Various amounts of 75% phosphoric acid were added to the four kinds of degummed rapeseed crude oil used in Example 1, and the same treatment as in Example 1 was performed thereafter. The chlorophyll-based pigments after the deoxidation step of the four crude oils were hardly reduced regardless of the amount of phosphoric acid added.

【0018】これら、実施例1及び比較例1による脱酸
後のクロロフィル系色素含量を表1に示す。
Table 1 shows the content of the chlorophyll dye after deoxidation according to Example 1 and Comparative Example 1.

【表1】 [Table 1]

【0019】実施例2 実施例1で用いた4種類の脱ガム菜種原油に対して98
%の濃硫酸0.14%を添加し、40℃にて40分攪拌
した後、常法に従いアルカリ脱酸を行った。原油のクロ
ロフィル系色素含量の違いにより、脱酸後の油のクロロ
フィル系色素含量も0.1から1.1ppm と異なった。
Example 2 98 for the four types of degummed rapeseed crude oil used in Example 1
% Concentrated sulfuric acid 0.14% was added, the mixture was stirred at 40 ° C. for 40 minutes, and then alkali deoxidation was performed according to a conventional method. Due to the difference in the chlorophyll pigment content of the crude oil, the chlorophyll pigment content of the oil after deoxidation also differed from 0.1 to 1.1 ppm.

【0020】実施例2による脱酸後のクロロフィル系色
素含量を表2に示す。
Table 2 shows the chlorophyll dye content after deoxidation according to Example 2.

【表2】 [Table 2]

【0021】実施例3 実施例1で原油Bを98%濃硫酸0.14%で処理して
得られた脱酸油に対して1.5%の活性白土を用いて常
法に従い脱色処理を行った後脱臭処理をして脱臭仕上精
製油とした。脱臭仕上精製油の風味、酸化安定性、耐熱
性、などの食用油として備えなければならない品質レベ
ルは通常品と変わらなかった。
Example 3 The decolorized oil obtained by treating crude oil B with 98% concentrated sulfuric acid 0.14% in Example 1 was subjected to a decolorization treatment using 1.5% activated clay. After that, deodorization treatment was performed to obtain a deodorized finished refined oil. The quality level of the refined deodorized finished refined oil such as flavor, oxidative stability and heat resistance, which must be provided as an edible oil, was the same as that of ordinary products.

【0022】比較例2 比較例1で原油Bを75%リン酸0.14%で処理して
得られた脱酸油に対して1.5%の活性白土を用いて常
法に従い脱色処理を行った後脱臭処理をして脱臭仕上精
製油とした。脱臭仕上精製油でもクロロフィル含量が高
く濃い緑色を呈していた。
Comparative Example 2 The decolorized oil obtained by treating crude oil B with 75% phosphoric acid 0.14% in Comparative Example 1 was subjected to a decolorization treatment using 1.5% of activated clay according to a conventional method. After that, deodorization treatment was performed to obtain a deodorized finished refined oil. The refined deodorized oil also had a high chlorophyll content and a dark green color.

【0023】実施例3及び比較例2で製造した菜種脱色
油、脱臭仕上精製油について、クロロフィル系色素含量
等の測定結果を表3に示す。
Table 3 shows the measurement results of the chlorophyll-based pigment content and the like of the rapeseed decolorized oil and deodorized finished refined oil produced in Example 3 and Comparative Example 2.

【0024】[0024]

【表3】 注)脱酸油は実施例1及び比較例1で得られたものであ
る。
[Table 3] Note) The deoxidized oil was obtained in Example 1 and Comparative Example 1.

【0025】[0025]

【発明の効果】以上の結果から明らかなように、本発明
により、食用植物原油精製の脱酸工程で効果的なクロロ
フィル系色素の除去が可能となった。このことにより食
用植物原油中のクロロフィル系色素を除去するに際し
て、煩雑な工程を付与することなく、現行の脱酸工程で
簡易に、しかも効果的にクロロフィル系色素を除去で
き、脱色工程での吸着剤の使用量を大幅に削減する経済
的な食用植物原油の精製法を提供できる。
As is clear from the above results, the present invention enables effective removal of chlorophyll pigments in the deoxidation step of edible plant crude oil refining. By this, when removing chlorophyll-based pigments in edible plant crude oil, it is possible to remove chlorophyll-based pigments easily and effectively in the current deoxidation step without adding a complicated step, and adsorption in the decolorization step It is possible to provide an economical method for refining edible plant crude oil, which greatly reduces the amount of the agent used.

フロントページの続き (72)発明者 葉 宏宇 静岡県清水市追分1−7−40 株式会社ホ ーネンコーポレーション社宅 (72)発明者 市川 奈津子 静岡県静岡市小鹿809−2Front Page Continuation (72) Inventor Kou Ha 1-7-40 Oiwake Shimizu City Shizuoka Prefecture Honen Corporation Co., Ltd. (72) Inventor Natsuko Ichikawa 809-2 Oka, Shizuoka City, Shizuoka Prefecture

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 食用植物原油をアルカリ水溶液を用いる
脱酸工程の酸処理において、酸として硫酸を添加し、ア
ルカリ脱酸工程における石鹸の分離と共にクロロフィル
系色素を除去することを特徴とする食用植物原油の精製
法。
1. An edible plant characterized by removing sulfuric acid as an acid in the acid treatment of an edible plant crude oil using an aqueous alkaline solution in the deoxidation process to remove soap and chlorophyll-based pigment in the alkaline deoxidation process. Crude oil refining method.
【請求項2】 食用植物原油に添加する硫酸の添加量は
0.05%以上で、クロロフィル系色素の油中濃度に応
じて適量を添加することを特徴とする請求項第1に記載
した食用植物原油の精製法。
2. The edible plant according to claim 1, wherein the amount of sulfuric acid added to the edible plant crude oil is 0.05% or more, and an appropriate amount is added according to the concentration of the chlorophyll-based pigment in the oil. Refining plant crude oil.
JP5352171A 1993-12-30 1993-12-30 Refinement of crude edible vegetable oil Pending JPH07197075A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5352171A JPH07197075A (en) 1993-12-30 1993-12-30 Refinement of crude edible vegetable oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5352171A JPH07197075A (en) 1993-12-30 1993-12-30 Refinement of crude edible vegetable oil

Publications (1)

Publication Number Publication Date
JPH07197075A true JPH07197075A (en) 1995-08-01

Family

ID=18422270

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5352171A Pending JPH07197075A (en) 1993-12-30 1993-12-30 Refinement of crude edible vegetable oil

Country Status (1)

Country Link
JP (1) JPH07197075A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001016084A1 (en) * 1999-09-02 2001-03-08 Cargill, Incorporated Removal of gum and chlorophyll-type compounds from vegetable oils
WO2010077694A1 (en) * 2008-12-08 2010-07-08 Sapphire Energy, Inc. Removal of nitrogen from a chlorophyll or pheophytin containing biomass
CN105154220A (en) * 2015-07-31 2015-12-16 崇州市白头甘泉工业油脂厂 Degumming alkali-refining method for grease

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001016084A1 (en) * 1999-09-02 2001-03-08 Cargill, Incorporated Removal of gum and chlorophyll-type compounds from vegetable oils
US6376689B1 (en) 1999-09-02 2002-04-23 Cargill, Incorporated Removal of gum and chlorophyll-type compounds from vegetable oils
WO2010077694A1 (en) * 2008-12-08 2010-07-08 Sapphire Energy, Inc. Removal of nitrogen from a chlorophyll or pheophytin containing biomass
CN105154220A (en) * 2015-07-31 2015-12-16 崇州市白头甘泉工业油脂厂 Degumming alkali-refining method for grease

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