JPS6314759B2 - - Google Patents

Info

Publication number
JPS6314759B2
JPS6314759B2 JP55016870A JP1687080A JPS6314759B2 JP S6314759 B2 JPS6314759 B2 JP S6314759B2 JP 55016870 A JP55016870 A JP 55016870A JP 1687080 A JP1687080 A JP 1687080A JP S6314759 B2 JPS6314759 B2 JP S6314759B2
Authority
JP
Japan
Prior art keywords
oil
salcido
fat
salseed
flavor
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
JP55016870A
Other languages
Japanese (ja)
Other versions
JPS56115399A (en
Inventor
Yukinobu Murase
Shoshi Maruzeni
Fusayuki Saito
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 JP1687080A priority Critical patent/JPS56115399A/en
Publication of JPS56115399A publication Critical patent/JPS56115399A/en
Publication of JPS6314759B2 publication Critical patent/JPS6314759B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Fats And Perfumes (AREA)

Description

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

本発明は、サルシード油脂の新規な品質改良法
に関するものであり、さらに詳しくはサルシード
油脂の風味の新規な改良法に関するものである。 サルシード油脂は、シヨリアロブスタ
(Shorearobusta)の種子から抽出される油脂で
ある。その原油は天然色素を多量に含むため、暗
緑色を呈している。また、その上サルシード油脂
原油は特有の風味を有しているため、その精製に
おいては、非常に注意深い操作と経験を必要とす
るものであつた。特に種子が落実してから長期間
経てから搾油されたサルシード油脂の精製はなお
一層精製が困難であつた。 このようなサルシード油脂を精製するのに、脱
色の際に用いられる吸着剤の選択あるいは使用量
の増量等の工夫により、精製油の色調に関しては
かなり改良することができるが、特有の風味は従
来法においては未だ完全に除去されないか、ある
いは除去されるとしても極めてはやく風味の“も
どり”現象がおきてしまう。このような従来法に
よるサルシード精製油は製品として充分な性能を
有しているとは言い難いものであつた。 サルシード油脂特有の風味物質およびもどり劣
化を促進する物質(以下サルシード油脂風味劣化
物質と称す)の本体については不詳であるが、原
油中に含まれるクロロフイル類を主成分とする色
素やタンニン等のポリフエノール化合物が関与し
ていると推定される。 本発明の目的は、サルシード油脂に特有な風味
をほとんど完全に除去すること及び風味の“もど
り”劣化を防止することにある。この目的のため
に種々の検討を行なつた結果、かかるサルシード
油脂風味劣化物質は、その本質は明らかでない
が、油脂を溶融状態から冷却して結晶を析出せし
めると非結晶部に蓄積されるという事実を見い出
した。この知見に基づき本発明を完成するに至つ
た。 本発明のサルシード油脂の品質改良法は、上記
知見に基づきなされたもので、サルシードは原油
又はそれを分別して得られる軟質油を、該油脂の
2倍量以上(重量基準)の有機溶媒に溶解せし
め、次いでこの油脂含有有機系溶媒を冷却して上
記サルシード油脂の90〜98重量%を結晶析出せし
め、結晶部と液状部を分離し、結晶部を分取する
ことを特徴とするものである。 前述したように、サルシード油脂の風味劣化物
質は非結晶部に濃縮されるわけであるが、油脂単
体を、冷却後非結晶部を分離しただけではその濃
縮分離効果は小さい。そのため結晶化→結晶分離
という操作をくり返すことが必要となる。 しかしながら、本発明の方法に従い、サルシー
ド原油又はそれを分別して得られる軟質油を有機
溶媒に完全溶解したのち結晶化させて、結晶部の
みを分離した場合、サルシード油脂の風味劣化物
質濃縮分離効果が大きく、ほぼ1回の結晶化→結
晶分離という操作で目的を達成できる。 本発明において対象とするサルシード油脂と
は、サルシード原油又はサルシード軟質油で、望
ましくは脱ガム及び脱酸された油脂に適応するの
がより効果的である。 本発明において用いる有機溶媒としては、グリ
セリドの溶解度が温度変化に対して大きく変わ
り、しかもサルシード油脂風味劣化物質を低温に
おいても溶解しやすいものが使用される。望まし
い有機溶媒として、例えば、n―ヘキサン、アセ
トン、n―ヘキサン―エタノール混合系があげら
れる。n―ヘキサン―エタノール混合系において
は両者の混合比は重量基準で4:1〜20:1の範
囲が望ましい。溶媒量は原料サルシード油脂の2
倍量以上使用される。溶媒量が2倍量以下の場合
には、液状部が結晶部内にとり込まれて、目的と
する風味改良の効果が発揮できない。 また、油脂含有有機溶媒の冷却温度は、使用す
る溶媒の種類や量及び原料サルシード油脂の90〜
98%となるように適宜選択され、通常0℃から−
40℃までの間の温度を採れば前記条件を満たす。 結晶部の液状部からの分離は、過、遠心分離
などによつて行なうことができる。分取された結
晶部は、必要に応じて脱ガム、脱酸、漂白、脱臭
の各精製及び硬化、分別、エステル交換などの加
工が引きつづき行なわれる。 このようにして得られた精製サルシード油脂
は、従来の精製法に比して、風味が改善され、も
どり劣化が著しく防止されている。 以下、本発明の効果を実施例及び比較例をあげ
て更に詳しく説明する。 尚、風味の官能検査は以下の方法で行なつた。 精製油50gを100ml容ビーカに入れ、63℃にコ
ントロールされた空気恒温槽中に10日間放置した
ものを官能検査の試料とした。官能検査は10人の
パネラーで行ない、評価はサルシード特有の臭、
味を感じた人の人数で示した。 実施例 1 サルシード油脂原油(酸価5.3、ヨウ素価40.1)
を0.2%リン酸を用いた脱ガム及び遊離脂肪酸の
1.25当量の苛性ソーダを用いたアルカリ脱酸を常
法により行ない、サルシード油脂の脱酸油を得
た。この脱酸油100gにアセトン500gを加え、撹
拌しながら約50℃に加温完全溶解した。 次いで、ドライアイス―メタノール冷媒にて約
2時間かけて含油アセトンを−30℃に低速撹拌下
に冷却し、1時間この温度に保持し、結晶を析出
せしめた。その後、結晶部と液状部を過によつ
て分け、結晶部は−40℃に冷却されたアセトンで
洗浄した。このようにして得られた結晶部は97.6
gであつた。 得られた結晶部を常法に従い、活性白土脱色
(5wt%白土使用)及び減圧水蒸気蒸留による脱
臭を行なつた。この精製油を63℃の空気恒温槽に
10日放置して官能検査を行なつた結果を表―1に
示した。 比較例 1 実施例1で使用したサルシード油脂原油を0.2
%リン酸を用いた脱ガム、遊離脂肪酸の1.25当量
の苛性ソーダを用いたアルカリ脱酸、5%活性白
土を用いた漂白、及び脱臭を常法により行ない精
製油を得た。この精製油を実施例1と同様にして
官能検査を行なつた結果を表―1に示した。 実施例 2 サルシード油脂の脱酸油を常法により溶剤分別
して得たサルシード油脂の軟質油(ヨウ素62.0)
100gをn―ヘキサン500gに完全溶解後、低速撹
拌しながらドライアイス―メタノール冷媒にて約
2時間かけて−35℃まで冷却した。含油n―ヘキ
サンをこの温度に1時間保持し結晶を析出させた
後、結晶部と液状部を過によつて分離した。得
られた結晶部(96g)を常法により5%活性白土
を用いた漂白、脱臭を行ない精製油を得た。官能
検査の結果を表―1にしめした。 比較例 2 実施例2で使用したサルシード軟質油を常法に
従い2%活性白土による脱色及び脱臭を行ない精
製油を得た。官能検査の結果を表―1に示した。 実施例 3 実施例2で用いた軟質油100gをn―ヘキサン
250gに完全溶解後、低速撹拌しながらドライア
イス―メタノール溶媒にて約2時間かけて−15℃
まで冷却した。含油n―ヘキサンをこの温度に1
時間保持し結晶を析出させた後、結晶部と液状部
を過によつて分離した。得られた結晶部(92
g)を常法により5%の活性白土による漂白、脱
臭を行なつた。官能検査の結果を表―1に示し
た。
The present invention relates to a novel method for improving the quality of salseed oil and fat, and more particularly to a novel method for improving the flavor of salseed oil and fat. Salcido oil is an oil extracted from the seeds of Shorea robusta. The crude oil has a dark green color because it contains large amounts of natural pigments. Moreover, since salcido oil crude oil has a unique flavor, its refining requires very careful operation and experience. In particular, it has been even more difficult to purify salseed oil that has been extracted a long time after the seeds have ripened. When refining this type of salseed oil, the color tone of the refined oil can be considerably improved by selecting the adsorbent used during decolorization or increasing the amount used, but the unique flavor remains the same. In this method, it is still not completely removed, or even if it is removed, the flavor "returns" phenomenon occurs very quickly. Salcido refined oil obtained by such conventional methods cannot be said to have sufficient performance as a product. Although the nature of the flavor substances unique to salseed oil and the substances that promote its deterioration (hereinafter referred to as salseed oil flavor deteriorating substances) is unknown, the main components of salseed oil and fat are pigments mainly composed of chlorophylls and polyesters such as tannins. It is presumed that phenolic compounds are involved. The purpose of the present invention is to almost completely remove the flavor peculiar to salseed oil and fat, and to prevent flavor deterioration due to "recovery". As a result of various studies for this purpose, it was found that although the true nature of salcido oil flavor-degrading substances is not clear, it accumulates in amorphous areas when oils and fats are cooled from a molten state to precipitate crystals. I found out the truth. Based on this knowledge, we have completed the present invention. The method for improving the quality of salseed oil and fat of the present invention was made based on the above knowledge, and salseed is a method for dissolving crude oil or a soft oil obtained by fractionating it in an organic solvent of twice the amount (by weight) of the oil or fat. The oil-containing organic solvent is then cooled to crystallize 90 to 98% by weight of the Salcido oil and fat, the crystalline portion and the liquid portion are separated, and the crystalline portion is fractionated. . As mentioned above, the flavor-degrading substances in Salcido fats and oils are concentrated in the amorphous parts, but the effect of concentration and separation is small if only the amorphous parts are separated from the fats and oils after cooling. Therefore, it is necessary to repeat the operation of crystallization → crystal separation. However, when Salcido crude oil or the soft oil obtained by fractionating it is completely dissolved in an organic solvent and then crystallized and only the crystalline portion is separated according to the method of the present invention, the effect of concentrating and separating the flavor deteriorating substances of Salcido oil and fat is reduced. The goal can be achieved in a large scale with just one operation of crystallization and then crystal separation. The salcido oil and fat targeted in the present invention is salcido crude oil or salcido soft oil, and desirably it is more effective to apply it to a degummed and deoxidized oil or fat. The organic solvent used in the present invention is one in which the solubility of glyceride changes significantly with changes in temperature, and which can easily dissolve salcido oil and fat flavor deteriorating substances even at low temperatures. Desirable organic solvents include, for example, n-hexane, acetone, and n-hexane-ethanol mixed systems. In the n-hexane-ethanol mixed system, the mixing ratio of both is preferably in the range of 4:1 to 20:1 on a weight basis. The amount of solvent is 2 of the raw material salcido oil and fat.
More than double the amount is used. If the amount of solvent is less than twice the amount, the liquid part will be incorporated into the crystal part, and the desired flavor improvement effect will not be achieved. In addition, the cooling temperature of the oil-containing organic solvent should be determined based on the type and amount of the solvent used and the temperature of the raw material salcido oil.
Appropriately selected to be 98%, usually from 0℃ to -
The above conditions are met if the temperature is up to 40°C. Separation of the crystal part from the liquid part can be carried out by filtration, centrifugation, or the like. The separated crystal part is subsequently subjected to various purification processes such as degumming, deacidification, bleaching, and deodorization, as well as processing such as hardening, fractionation, and transesterification, as necessary. The refined salcido oil and fat obtained in this way has improved flavor and is significantly prevented from deterioration due to reflux, compared to conventional refining methods. Hereinafter, the effects of the present invention will be explained in more detail with reference to Examples and Comparative Examples. Incidentally, the flavor sensory test was conducted in the following manner. A sample for the sensory test was prepared by placing 50 g of refined oil in a 100 ml beaker and leaving it in an air constant temperature bath controlled at 63° C. for 10 days. The sensory test was conducted by 10 panelists, and the evaluation was based on the unique odor of Salcido,
It is indicated by the number of people who felt the taste. Example 1 Salcido oil crude oil (acid value 5.3, iodine value 40.1)
Degumming and removing free fatty acids using 0.2% phosphoric acid
Alkaline deacidification using 1.25 equivalents of caustic soda was carried out in a conventional manner to obtain a deacidified oil of salcido oil and fat. 500 g of acetone was added to 100 g of this deoxidized oil and heated to about 50° C. with stirring to completely dissolve it. Next, the oil-containing acetone was cooled to -30°C over about 2 hours using a dry ice-methanol refrigerant with slow stirring, and kept at this temperature for 1 hour to precipitate crystals. Thereafter, the crystalline part and the liquid part were separated by filtration, and the crystalline part was washed with acetone cooled to -40°C. The crystal part obtained in this way is 97.6
It was hot at g. The obtained crystalline portion was decolorized using activated clay (using 5 wt % clay) and deodorized by vacuum steam distillation according to conventional methods. This refined oil is placed in an air constant temperature bath at 63℃.
Table 1 shows the results of a sensory test after being left for 10 days. Comparative Example 1 Salcido oil crude oil used in Example 1 was 0.2
A refined oil was obtained by degumming using % phosphoric acid, alkaline deacidification using 1.25 equivalents of free fatty acid with caustic soda, bleaching using 5% activated clay, and deodorization using conventional methods. This refined oil was subjected to a sensory test in the same manner as in Example 1, and the results are shown in Table 1. Example 2 Soft oil of salseed oil (iodine 62.0) obtained by solvent fractionation of deacidified oil of salseed oil using a conventional method
After completely dissolving 100 g in 500 g of n-hexane, it was cooled to -35°C over about 2 hours using a dry ice-methanol refrigerant while stirring at low speed. The oil-containing n-hexane was maintained at this temperature for 1 hour to precipitate crystals, and then the crystal part and the liquid part were separated by filtration. The obtained crystalline portion (96 g) was bleached and deodorized using 5% activated clay in a conventional manner to obtain a refined oil. The results of the sensory test are shown in Table 1. Comparative Example 2 The Salcido soft oil used in Example 2 was decolorized and deodorized with 2% activated clay according to a conventional method to obtain a refined oil. The results of the sensory test are shown in Table 1. Example 3 100g of the soft oil used in Example 2 was mixed with n-hexane.
After completely dissolving in 250g, incubate at -15℃ for about 2 hours with dry ice-methanol solvent while stirring at low speed.
cooled to. Oil-containing n-hexane at this temperature 1
After holding for a period of time to precipitate crystals, the crystal part and liquid part were separated by filtration. The obtained crystal part (92
g) was bleached and deodorized using 5% activated clay in a conventional manner. The results of the sensory test are shown in Table 1.

【表】 表―1にみられるように本発明によれば、従来
法にくらべ著しくサルシード油脂の品質を改良で
きる。
[Table] As shown in Table 1, according to the present invention, the quality of salcido oil and fat can be significantly improved compared to the conventional method.

Claims (1)

【特許請求の範囲】 1 サルシード原油又はそれを分別して得られる
軟質油を、該油脂の2倍以上(重量基準)の有機
溶媒に溶解せしめ、次いでこの油脂含有有機溶媒
を冷却して上記サルシード油脂の90〜98%を結晶
析出せしめ、結晶部と液状部を分離し、結晶部を
分取することを特徴とするサルシード油脂の品質
改良法。 2 有機溶媒がn―ヘキサン、アセトン及びn―
ヘキサン―エタノール混合溶媒からなる群から選
ばれた一種である特許請求の範囲第1項記載のサ
ルシード油脂の品質改良法。 3 油脂含有有機溶媒の冷却温度が0〜−40℃で
ある特許請求の範囲第1又は2項記載のサルシー
ド油脂の品質改良法。
[Scope of Claims] 1 Salcido crude oil or a soft oil obtained by fractionating it is dissolved in an organic solvent with an amount of at least twice as much (by weight) as the oil and fat, and then this oil-containing organic solvent is cooled to dissolve the salcido oil and fat. A method for improving the quality of Salcido oil and fat, which is characterized by crystallizing 90 to 98% of the salcedo oil and fat, separating the crystalline part from the liquid part, and fractionating the crystalline part. 2 Organic solvents are n-hexane, acetone and n-
The method for improving the quality of salcido oil and fat according to claim 1, which is one selected from the group consisting of hexane-ethanol mixed solvents. 3. The method for improving the quality of salseed oil and fat according to claim 1 or 2, wherein the cooling temperature of the oil-containing organic solvent is 0 to -40°C.
JP1687080A 1980-02-14 1980-02-14 Quality improvement of sarseed oil Granted JPS56115399A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1687080A JPS56115399A (en) 1980-02-14 1980-02-14 Quality improvement of sarseed oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1687080A JPS56115399A (en) 1980-02-14 1980-02-14 Quality improvement of sarseed oil

Publications (2)

Publication Number Publication Date
JPS56115399A JPS56115399A (en) 1981-09-10
JPS6314759B2 true JPS6314759B2 (en) 1988-04-01

Family

ID=11928231

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1687080A Granted JPS56115399A (en) 1980-02-14 1980-02-14 Quality improvement of sarseed oil

Country Status (1)

Country Link
JP (1) JPS56115399A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4601857A (en) * 1983-07-26 1986-07-22 Nestec S. A. Process for fat fractionation with azeotropic solvents
EP0246324B1 (en) * 1985-01-22 1993-01-27 Japan as represented by Director-General, Agency of Industrial Science and Technology Method for obtaining lipids from fungus bodies

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49130404A (en) * 1973-04-18 1974-12-13
JPS533568A (en) * 1976-06-30 1978-01-13 Asahi Denka Kogyo Kk Cacao fat substitute
JPS5658444A (en) * 1979-10-19 1981-05-21 Fuji Oil Co Ltd Hard butter composition

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49130404A (en) * 1973-04-18 1974-12-13
JPS533568A (en) * 1976-06-30 1978-01-13 Asahi Denka Kogyo Kk Cacao fat substitute
JPS5658444A (en) * 1979-10-19 1981-05-21 Fuji Oil Co Ltd Hard butter composition

Also Published As

Publication number Publication date
JPS56115399A (en) 1981-09-10

Similar Documents

Publication Publication Date Title
JPS63191899A (en) Dewaxing of triglyceride oil
US4584141A (en) Process relating to triglyceride oils
CA2012544C (en) Process for refining glyceride oil using silica hydrogel
US4104288A (en) Method for producing hard butter fraction from shea fat
KR890001463B1 (en) Refined edible oil and process for its preparation
JPH0711285A (en) Method for purifying vegetable wax
US2553288A (en) Solvent treatment
US4981620A (en) In-line dewaxing of edible vegetable oils
JPH0425776B2 (en)
JPS6314759B2 (en)
CN113122381A (en) Method for improving freezing resistance of grease
US3345389A (en) Separation of fatty materials
DK154026B (en) APPLICATION OF A MANGOKEN FAT PRODUCT FRATION AS A REPLACEMENT FOR COCOA NUTS.
US4010183A (en) Anhydrous solvent separation in production of polyol monoacylates
JPS62256894A (en) Purification of oils and fats
JP4397116B2 (en) Cocoa butter ole infrastructure
US2684378A (en) Process for fractionating glyceridic mixtures obtained as hydrocarbon solutions
US2682550A (en) Solvent treatment
JPS62121796A (en) Method for improving quality of fat
JP3656863B2 (en) Process for producing fats and oils having a high content of highly unsaturated fatty acid residues
GB2144143A (en) Refining of palm oils
US2046345A (en) Method of producing concentrated phytosterin-containing products
US2608566A (en) Process for decolorizing a soybean oil miscella
GB2162530A (en) Bleaching and dewaxing vegetable oils
EP0269904B1 (en) Process for refining fat