JPH061995A - Production of sesame oil - Google Patents
Production of sesame oilInfo
- Publication number
- JPH061995A JPH061995A JP18588692A JP18588692A JPH061995A JP H061995 A JPH061995 A JP H061995A JP 18588692 A JP18588692 A JP 18588692A JP 18588692 A JP18588692 A JP 18588692A JP H061995 A JPH061995 A JP H061995A
- Authority
- JP
- Japan
- Prior art keywords
- oil
- sesame
- raw
- acid value
- liquid separation
- 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
Links
- 239000008159 sesame oil Substances 0.000 title claims abstract description 16
- 235000011803 sesame oil Nutrition 0.000 title claims abstract description 16
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- 241000207961 Sesamum Species 0.000 claims abstract description 21
- 235000003434 Sesamum indicum Nutrition 0.000 claims abstract description 21
- 239000007788 liquid Substances 0.000 claims abstract description 14
- 238000000926 separation method Methods 0.000 claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 230000032683 aging Effects 0.000 claims abstract description 7
- 239000010779 crude oil Substances 0.000 claims description 22
- 238000009874 alkali refining Methods 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 8
- 239000003921 oil Substances 0.000 abstract description 31
- 235000019198 oils Nutrition 0.000 abstract description 31
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 abstract description 9
- 239000002253 acid Substances 0.000 abstract description 9
- 239000000126 substance Substances 0.000 abstract description 9
- 238000004065 wastewater treatment Methods 0.000 abstract description 5
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 abstract description 4
- 239000003513 alkali Substances 0.000 abstract description 4
- 238000004332 deodorization Methods 0.000 abstract description 4
- 238000000746 purification Methods 0.000 abstract description 4
- 239000007864 aqueous solution Substances 0.000 abstract description 3
- 150000003904 phospholipids Chemical class 0.000 abstract description 3
- 235000011121 sodium hydroxide Nutrition 0.000 abstract description 3
- 229910000147 aluminium phosphate Inorganic materials 0.000 abstract description 2
- 235000021588 free fatty acids Nutrition 0.000 abstract description 2
- 125000000217 alkyl group Chemical group 0.000 abstract 1
- 238000007670 refining Methods 0.000 description 7
- 229920000715 Mucilage Polymers 0.000 description 6
- 239000000853 adhesive Substances 0.000 description 6
- 239000000796 flavoring agent Substances 0.000 description 6
- 235000019634 flavors Nutrition 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 4
- 239000010517 refined sesame oil Substances 0.000 description 4
- 239000002893 slag Substances 0.000 description 3
- 238000005119 centrifugation Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 229930186217 Glycolipid Natural products 0.000 description 1
- 235000019484 Rapeseed oil Nutrition 0.000 description 1
- 235000019658 bitter taste Nutrition 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- -1 chromaticity Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000004042 decolorization Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000003205 fragrance Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 210000003097 mucus Anatomy 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 235000012424 soybean oil Nutrition 0.000 description 1
- 239000003549 soybean oil Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Fats And Perfumes (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、ごま油の製造法に関す
るものである。FIELD OF THE INVENTION The present invention relates to a method for producing sesame oil.
【0002】[0002]
【従来の技術】ごま油を製造する際には、通常、ごま種
子を焙煎し、圧搾し、場合によっては溶剤抽出してごま
原油とする。圧搾して得られる原油を圧搾油、抽出して
得られる原油を抽出油と呼ぶ。従来は圧搾油のみが用い
られていたが、最近は圧搾油と抽出油の混合油が用いら
れることが多くなった。ごま精製油は、この混合原油に
対し、脱酸、水洗、脱色、脱臭の各精製工程を施して得
られる。脱酸および水洗をアルカリ精製と称している。
また、脱色工程は用途によっては省略されることがあ
る。これらの精製工程は、大豆油や菜種油の場合と大略
同じ方法であるが、ごま油はとくに芳香を大切にするこ
とから、軽度に行われることが多い。2. Description of the Related Art In the production of sesame oil, sesame seeds are usually roasted, pressed and, in some cases, solvent extracted to obtain sesame crude oil. Crude oil obtained by pressing is called pressed oil, and crude oil obtained by extracting is called extracted oil. Conventionally, only compressed oil was used, but recently, mixed oils of compressed oil and extracted oil have been often used. Sesame refined oil can be obtained by subjecting this mixed crude oil to respective purification steps of deoxidation, washing with water, decolorization and deodorization. Deoxidation and washing with water are called alkaline refining.
Further, the decolorizing step may be omitted depending on the application. These refining steps are almost the same as those for soybean oil and rapeseed oil, but sesame oil is often carried out lightly because the fragrance is particularly important.
【0003】[0003]
【発明が解決しようとする課題】ごま原油には、かなり
の油滓またはオリと称される粘質物が含まれ、これらを
取り除く必要がある。従来はアルカリ精製に先だって、
原油をそのまま長時間静置したり、水を添加し粘質物を
水和、凝集させる、いわゆる脱ガム法が試みられたが、
いずれもうまく分離できず、ごま油の歩留りが悪くなっ
たり、その後の精製処理に手間どることが多く、精製効
率が悪かった。そのため、原油を直接アルカリ精製する
方法がとられているのが現状である。[Problems to be Solved by the Invention] Sesame crude oil contains a considerable amount of mucilage called slag or slag, which must be removed. Conventionally, prior to alkali refining,
The so-called degumming method was tried in which the crude oil was allowed to stand for a long time as it was, or water was added to hydrate and agglomerate the mucilage.
Both could not be separated well, the yield of sesame oil was poor, and the subsequent refining treatment was often troublesome, resulting in poor refining efficiency. Therefore, at present, a method of directly refining crude oil with an alkali is adopted.
【0004】この粘質物には、高融点のワックス様物
質、リン脂質、糖類、糖脂質、蛋白質等(以下、ワック
ス様物質等という)が含まれ、水を添加する脱ガム法で
は、油と粘質物部分および中間層ができ、このワックス
様物質等を含んだ粘質物部分が油層とからみ合って、粘
質物の分離・除去を困難なものにしている。また、この
工程から出る廃水中には、からみ合った部分が混入する
ため、その処理にかなりの負荷がかかり、製造者の大き
な課題となっている。This mucilage contains a wax-like substance having a high melting point, phospholipids, saccharides, glycolipids, proteins and the like (hereinafter referred to as wax-like substance), and in the degumming method in which water is added, it becomes oil. A mucilage portion and an intermediate layer are formed, and the mucilage portion containing the wax-like substance is entangled with the oil layer, which makes it difficult to separate and remove the mucus. Further, since the entangled portions are mixed in the wastewater discharged from this process, a considerable load is imposed on the treatment, which is a major problem for manufacturers.
【0005】かかる実情に鑑み、本発明者らはごま油の
製造法において、油滓またはオリの多い品質の悪いごま
原油からでも、品質、風味の良好な製品油を歩留り良く
得ることができ、しかも廃水処理の負荷が軽減できる技
術の開発を目的に鋭意検討し、本発明を完成するに至っ
た。In view of such circumstances, the inventors of the present invention were able to obtain a product oil having a good quality and flavor with a good yield even in a sesame oil production method, even from a poor quality sesame crude oil containing a large amount of oil slag or The present invention has been completed through intensive studies for the purpose of developing a technique capable of reducing the load of wastewater treatment.
【0006】[0006]
【課題を解決するための手段】すなわち本発明は、ごま
油の製造法において、アルカリ精製工程に先だってごま
原油を30〜70℃に保ち、1分以上静置熟成後、水を
添加することなく固液分離させることを特徴とするごま
油の製造法である。[Means for Solving the Problems] That is, according to the present invention, in the method for producing sesame oil, the sesame crude oil is kept at 30 to 70 ° C. prior to the alkali refining step, and after aging for one minute or more, it is solidified without adding water. It is a method for producing sesame oil, which is characterized by liquid separation.
【0007】本発明でいうアルカリ精製とは、原油にア
ルカリとして苛性ソーダの水溶液等を添加して、遊離脂
肪酸、残存リン脂質、有色物質等を遠心分離等により分
離する工程をいう。遠心分離は、4000〜7000rp
m で連続的に行う。The alkali refining referred to in the present invention is a step of adding an aqueous solution of caustic soda as an alkali to crude oil and separating free fatty acids, residual phospholipids, colored substances and the like by centrifugation or the like. Centrifugation is 4000-7000rp
m continuously.
【0008】本発明は、かかるアルカリ精製に先だっ
て、ごま原油を30〜70℃、好ましくは40〜60℃
に保ち、1分間以上静置熟成後、水を添加することなく
固液分離することに特徴がある。温度が30℃未満で
は、原油の粘性が上がり、遠心分離機の固液分離能力が
落ちてしまう。また70℃を超えると、粘質物中に含ま
れるワックス様物質等の一部が原油中に溶け、熟成時間
を長くしても固液分離が不能となる。熟成時間は1分間
以上必要で、それに満たないとワックス様物質等の結晶
成長が妨げられ、ワックス様物質等がからみ合って分離
を困難なものにする。ワックス様物質等を分離した原油
は、次のアルカリ精製工程へ送られ、その後脱臭等の工
程を経て、ごま精製油が作られる。In the present invention, prior to such alkali refining, sesame crude oil is treated at 30 to 70 ° C, preferably 40 to 60 ° C.
It is characterized in that the solid-liquid separation is carried out without adding water after keeping it for 1 minute or more and aging it by standing still. When the temperature is lower than 30 ° C, the viscosity of crude oil increases, and the solid-liquid separation ability of the centrifuge decreases. On the other hand, when the temperature exceeds 70 ° C, a part of the wax-like substance contained in the mucilage is dissolved in the crude oil and solid-liquid separation becomes impossible even if the aging time is lengthened. The aging time is 1 minute or more, and if it is less than that, crystal growth of the wax-like substance or the like is hindered, and the wax-like substance or the like becomes entangled with each other to make separation difficult. The crude oil from which the wax-like substance and the like have been separated is sent to the next alkali refining step, and then subjected to steps such as deodorization to produce refined sesame oil.
【0009】[0009]
実施例1 圧搾油と抽出油が混合されたごま原油を約60℃に保持
し、静置タンクで5分間静置熟成した後、水を添加する
ことなく、遠心分離機(回転数6000rpm )で連続的
に固液分離した。分離された油はリン酸を対油0.05
wt%添加し、濃度16°ボーメの苛性ソーダ水溶液を原
油の酸価当量110%添加してアルカリ精製し、脱臭し
てごま精製油を得た。得られた精製油の色度(ロビーボ
ンド、1インチセル。以下同じ)および酸価は、各々4
0Y/5.0Rおよび0.09で、風味はまろやかで良
好であった。Example 1 Sesame crude oil in which the compressed oil and the extracted oil were mixed was maintained at about 60 ° C. and aged for 5 minutes in a stationary tank, and then a centrifugal separator (rotation speed 6000 rpm) was used without adding water. Solid-liquid separation was performed continuously. Separated oil is phosphoric acid vs. oil 0.05
wt% was added, and a caustic soda aqueous solution having a concentration of 16 ° Baume was added by 110% of the acid value equivalent of crude oil for alkali refining and deodorization to obtain sesame refined oil. The chromaticity (lobby bond, 1 inch cell; the same applies hereinafter) and acid value of the obtained refined oil are 4 respectively.
At 0Y / 5.0R and 0.09, the flavor was mellow and good.
【0010】実施例2 実施例1と同じごま原油を約60℃に保ち、静置タンク
で1分間静置熟成した後、水を添加することなく、実施
例1と同様に遠心分離処理し固液分離した。その後、実
施例1と同様にアルカリ精製し、脱臭してごま精製油を
得た。色度および酸価は実施例1とほぼ同様で、風味も
問題なかった。Example 2 The same sesame crude oil as in Example 1 was maintained at about 60 ° C. and aged for 1 minute in a stationary tank, and then centrifuged and solidified in the same manner as in Example 1 without adding water. The liquid was separated. Then, it refine | purified with an alkali like Example 1 and deodorized, and the refined sesame oil was obtained. The chromaticity and acid value were almost the same as in Example 1, and the flavor was not a problem.
【0011】比較例1 実施例1と同じごま原油を固液分離の工程を経ることな
く、直接アルカリ精製した。アルカリ精製の条件は実施
例1と同じで、その後実施例1と同様にしてごま精製油
を得た。色度および酸価は、各々40Y/8.4Rおよ
び0.22で、風味はやや苦味を有していた。Comparative Example 1 The same sesame crude oil as in Example 1 was directly alkali-refined without going through the solid-liquid separation step. The conditions for alkali refining were the same as in Example 1, and then the same procedure as in Example 1 was carried out to obtain a sesame refined oil. The chromaticity and acid value were 40Y / 8.4R and 0.22, respectively, and the flavor had a slightly bitter taste.
【0012】比較例2 実施例1と同じごま原油を約60℃にし、熟成せずに水
を添加することなく、遠心分離機により実施例1と同様
に固液分離した。以降の工程は実施例1と同様とした。
その結果、得られたごま精製油の色度、酸価は各々40
Y/6.7R、0.15で、全体の色調はやや透明度が
落ち、風味はやや重い感じがした。Comparative Example 2 The same sesame crude oil as in Example 1 was heated to about 60 ° C., solid-liquid separated in the same manner as in Example 1 by a centrifuge without adding water without aging. The subsequent steps were the same as in Example 1.
As a result, the obtained sesame refined oil had a chromaticity and an acid value of 40, respectively.
With Y / 6.7R, 0.15, the overall color tone was slightly less transparent, and the flavor was a little heavy.
【0013】比較例3 実施例1と同じごま原油を約90℃に保持し、以下実施
例1と同様にしてごま精製油を得た。常温にした時、全
体にややくもりを生じ、ごま精製油として不適であっ
た。Comparative Example 3 The same sesame crude oil as in Example 1 was kept at about 90 ° C., and a refined sesame oil was obtained in the same manner as in Example 1. When it was kept at room temperature, it was slightly cloudy and was not suitable as a refined sesame oil.
【0014】比較例4 実施例1と同じごま原油を約15℃に保持し、5分間静
置熟成後、遠心分離機により固液分離処理したが、分離
状態が悪く固液分離不能であった。Comparative Example 4 The same sesame crude oil as in Example 1 was kept at about 15 ° C. and aged for 5 minutes and then subjected to solid-liquid separation treatment by a centrifuge, but the separation state was poor and solid-liquid separation was impossible. .
【0015】評価 本発明の固液分離法と従来法による製品油の品質、廃水
処理における原単位、精製歩留りを比較評価した(表1
参照)。表中で、電力使用量および精製歩留りの差は、
ごま油の実生産において大量処理する際、極めて大きな
利点となる。Evaluation The quality of the product oil by the solid-liquid separation method of the present invention and the conventional method, the basic unit in wastewater treatment, and the refining yield were comparatively evaluated (Table 1).
reference). In the table, the difference in power consumption and refining yield is
This is a great advantage when mass-processing sesame oil in actual production.
【0016】[0016]
【表1】 [Table 1]
【0017】[0017]
【発明の効果】本発明の手法を用いれば、ごま油の製造
において、製品油の色度、酸価、風味等の品質が従来法
と比べ良好となり、しかも精製歩留りのアップが図ら
れ、廃水処理の負荷も軽減される。Industrial Applicability According to the method of the present invention, in the production of sesame oil, the quality of product oil such as chromaticity, acid value, flavor and the like is improved as compared with the conventional method, and further, the purification yield is increased and the wastewater treatment is performed. The load on is also reduced.
Claims (1)
工程に先だってごま原油を30〜70℃に保ち、1分以
上静置熟成後、水を添加することなく固液分離すること
を特徴とするごま油の製造法。1. A sesame oil characterized in that, in the method of producing sesame oil, sesame crude oil is kept at 30 to 70 ° C. prior to the alkali refining step, and after aging for one minute or more, solid-liquid separation is performed without adding water. Manufacturing method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4185886A JPH07116463B2 (en) | 1992-06-19 | 1992-06-19 | Method of producing refined sesame oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4185886A JPH07116463B2 (en) | 1992-06-19 | 1992-06-19 | Method of producing refined sesame oil |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH061995A true JPH061995A (en) | 1994-01-11 |
| JPH07116463B2 JPH07116463B2 (en) | 1995-12-13 |
Family
ID=16178604
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4185886A Expired - Fee Related JPH07116463B2 (en) | 1992-06-19 | 1992-06-19 | Method of producing refined sesame oil |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07116463B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009144123A (en) * | 2007-12-18 | 2009-07-02 | Nisshin Oillio Group Ltd | Sesame oil production method |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57177098A (en) * | 1981-01-26 | 1982-10-30 | United Oilseed Products Ltd | Method of degumming vegetable crude oils |
| JPS5821492A (en) * | 1981-07-29 | 1983-02-08 | 九鬼産業株式会社 | Manufacture of splash-hard sesame oil |
-
1992
- 1992-06-19 JP JP4185886A patent/JPH07116463B2/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57177098A (en) * | 1981-01-26 | 1982-10-30 | United Oilseed Products Ltd | Method of degumming vegetable crude oils |
| JPS5821492A (en) * | 1981-07-29 | 1983-02-08 | 九鬼産業株式会社 | Manufacture of splash-hard sesame oil |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009144123A (en) * | 2007-12-18 | 2009-07-02 | Nisshin Oillio Group Ltd | Sesame oil production method |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH07116463B2 (en) | 1995-12-13 |
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