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JPH0475751B2 - - Google Patents
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JPH0475751B2 - - Google Patents

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Publication number
JPH0475751B2
JPH0475751B2 JP63070473A JP7047388A JPH0475751B2 JP H0475751 B2 JPH0475751 B2 JP H0475751B2 JP 63070473 A JP63070473 A JP 63070473A JP 7047388 A JP7047388 A JP 7047388A JP H0475751 B2 JPH0475751 B2 JP H0475751B2
Authority
JP
Japan
Prior art keywords
nuts
pressure
temperature
extraction
present
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 - Lifetime
Application number
JP63070473A
Other languages
Japanese (ja)
Other versions
JPH01243969A (en
Inventor
Shoshichiro Inada
Joji Ogasawara
Giichi Tsubakimoto
Shoichi Takahashi
Toshiro Izuno
Katsuyoshi Kato
Hirofumi Ochi
Norio Yoda
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.)
Sumitomo Seika Chemicals Co Ltd
Ezaki Glico Co Ltd
Original Assignee
Sumitomo Seika Chemicals Co Ltd
Ezaki Glico Co Ltd
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 Sumitomo Seika Chemicals Co Ltd, Ezaki Glico Co Ltd filed Critical Sumitomo Seika Chemicals Co Ltd
Priority to JP63070473A priority Critical patent/JPH01243969A/en
Publication of JPH01243969A publication Critical patent/JPH01243969A/en
Publication of JPH0475751B2 publication Critical patent/JPH0475751B2/ja
Granted legal-status Critical Current

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  • General Preparation And Processing Of Foods (AREA)
  • Seeds, Soups, And Other Foods (AREA)
  • Extraction Or Liquid Replacement (AREA)

Description

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

(産業上の利用分野) 本発明は、新規なナツツ類食品及びその製造法
に関するものであり、詳しくは、亜臨界または超
臨界状態の二酸化炭素(以下、CO2と表記する)
を抽剤としてナツツ類の渋味、異味、異臭成分等
を所望の割合で抽出除去し、さらに、この処理に
よりナツツ類自身の膨化も可能としたものであ
る。 (従来の技術ならびに発明が解決しようとする問
題点) ナツツ類とは通常殻果類、堅果類とも称せら
れ、クルミ、アーモンド、カシユーナツツ、マカ
デミアナツツ、プラジルナツツ、ヘーゼルナツ
ツ、松の実等の木の実を総称したもので、いずれ
も種子の部分は脂肪分に富み栄養価も高く、食用
に供せられるものである。 これらナツツ類はそのまま、あるいは焙煎、煮
込み、その他の加工法によつて和、洋、中華料理
に使用される他、菓子、酒類のつまみとしても愛
用されているが、これらナツツ類の中には渋味、
異味、異臭成分等がその表面部分に多く含まれて
いたり、また表面部分に含まれる脂肪分が劣化し
ていてこのために品質評価が低いものも少なくな
い。 ナツツ類は一般に歯ごたえがあり、食感として
硬い感じを与えるものであるが、最近はその嗜好
の多様化から、軟らかな歯触りのものが好まれる
傾向が生じている。そのほか、ナツツは他の食
品、菓子と組み合わされて使用される場合、組み
合わす相手によつては、ナツツが硬いと異物感を
与えるため、軟らかな歯触りのナツツが求められ
ることがあるが、未だにその要請を充したものが
なかつた。 (問題点を解決するための手段) 本発明者らは、前記問題点を克服して工業的に
有利に渋味、異味、異臭成分等を抽出除去すると
同時に食感をも改良した新規なナツツ類の製造法
について鋭意検討した結果、亜臨界または超臨界
状態のCO2を抽剤として使用すれば、容易にこれ
らを抽出除去でき、さらにこの処理によつて得ら
れるナツツ類を、それら自身の形状を保つたまま
膨化させることも可能であり、従来にないナツツ
類食品が得られることを見出し、本発明を完成す
るに至つた。本発明においては、亜臨界または超
臨界状態のCO2は圧力50〜500Kg/cm2、好ましくは
60〜300Kg/cm2、温度25〜100℃、好ましくは25〜
70℃のものが好適に用いられる。また、抽出時間
は1〜10時間が適当である。 本発明において、亜臨界状態とは、サブクリテ
イカル(Sub−critical)あるいは、ニアー・ク
リテイカルリキツド(Near−critical liquid)状
態とも呼ばれ、その定義付けについては統一的な
ものは詳らかではないが、一般常識的には、1.00
>温度(T)/臨界温度(Tc)>0.95の領域と解する
のが普偏的である。CO2においては、これは30℃
〜16℃程度に相当する。この領域は明らかに超臨
界領域ではなく、単純なる液相領域でもない。液
相領域から超臨界領域への境界域として大きな物
性上の変化、ゆらぎが発生する領域であり、甚だ
不安定かつ性状的に活性化された領域であり、明
らかに安定な液相、超臨界相と著しく様相の異な
る一つの注目すべき領域として認識されていると
ころである。 また超臨界域におけるCO2は31.0℃、72.9atm
の臨界点以上の状態にあり、液体に近い密度とガ
ス体に近い大きな拡散係数を有するため種々の化
合物を速やか、かつ大量に抽出でき、しかも抽剤
の分離が容易であるという特徴を有する。 CO2の圧力、温度は原料に用いるナツツの種類
または渋味、異味、異臭成分等の抽出度合に応じ
て、上記範囲内で、圧力、温度、時間を適宜選択
すればよい。殊に、加圧時間については、本発明
ナツツ類食品の膨化度を所望のものとするため、
適宜、長く又は短くし、抽出槽の放圧に際して
は、抽出時の温度を保ちながら、かつ、急激な放
圧によりナツツ類食品の原形を崩さないように段
階的に常圧に戻すなどの処理をするのが有効であ
る。 なお、本発明において異味、異臭成分とは収斂
味、酸化臭、カビ臭のごときものを総称したもの
である。 本発明を実施するには、常法によればよい。例
えば、まず所定の圧力まで圧縮したCO2を所定の
抽出温度まで加熱し、亜臨界または超臨界状態に
して抽出槽下部へ導入する。抽出槽内には予め原
料のナツツ類を仕込み、CO2による抽出を行なつ
た後、抽出対象物を含んだCO2を減圧弁を通して
減圧し、セパレーターに導き、抽出物をCO2から
分離する。抽出物と分離されたCO2はコンデンサ
で冷却、液化され、再圧縮されてリサイクルす
る。 (作 用) 亜臨界または超臨界状態のCO2は液体に近い密
度とガス体に近い大きな拡散係数を有し、この特
性の故に種々の化合物殊に油性物質を速やかにか
つ大量に効率よく抽出できる。しかしながら、圧
力、温度が低すぎると液化CO2となるため、抽出
能力が小さくなり、また逆に高すぎると装置費が
かさみ、経済性に問題が出る他、減圧操作に時間
がかかつたり、ナツツ類中の有効成分である油分
やフレーバー成分がCO2へ溶解してしまい、減圧
と同時に、放出されてしまう等、工業的実施の上
で不利である。 ナツツ類の渋味、異味等の成分は主としてナツ
ツ類の表層部分に存在するが、これを本発明によ
り抽出除去操作を行なつた場合、時間経過に伴つ
て、それらの原料の表面層から次第に内部に向け
抽出作用が進行すると思われるので、その程度は
実験的に抽出条件を決定することによつて適宜に
制御する。 また、この方法によつて原料であるナツツ類が
適宜の程度に膨化した形状となるのは前記抽出除
去の際、原料組織内部に亜臨界または超臨界状態
のCO2が入り込み、最終的にガス状のCO2へ減圧
する際のCO2の体積膨脹によるためと考えられ
る。 (実施例) 以下実施例を示して本発明をさらに詳細に説明
する。 実施例 1 アーモンド生豆1000gを2抽出槽に仕込み、
圧力220Kg/cm2、温度43℃のCO2を抽剤として3時
間抽出を行ない常温大気圧下で分離したところ、
抽出除去量は12.1gであつた。抽出槽内の温度を
43℃に保ちながら抽出槽の圧力を大気圧まで段階
的に下げ、脱脂アーモンド生豆を得た。この処理
の後のアーモンド生豆はその原形が崩れておらず
表面部分が膨化し軟らかくなつていた。 また、このアーモンド生豆については、これを
引き続き常法通りにローストしその風味について
官能検査を実施した。この結果については表1に
示した。 表1は本発明品及び対照品(無処理品)につい
て社内専門家パネル20名により風味、食感につい
て、それぞれ官能検査により評価を行なつた結果
を平均値で示したものである。
(Industrial Application Field) The present invention relates to a novel nut food and a method for producing the same, and specifically relates to subcritical or supercritical carbon dioxide (hereinafter referred to as CO 2 ).
is used as an extractant to extract and remove astringency, off-taste, off-odor components, etc. from nuts at a desired ratio, and furthermore, through this treatment, it is possible to expand the nuts themselves. (Prior art and problems to be solved by the invention) Nuts are usually called shells or nuts, and are a general term for nuts such as walnuts, almonds, cashew nuts, macadamia nuts, plagill nuts, hazel nuts, and pine nuts. The seeds are rich in fat and have high nutritional value, making them edible. These nuts are used as they are or by roasting, stewing, or other processing methods in Japanese, Western, and Chinese cuisine, and are also used as snacks for sweets and alcoholic beverages. is astringent,
There are many products that have low quality evaluations because they contain a large amount of off-taste and odor components in their surface parts, or because the fat content contained in their surface parts has deteriorated. Nuts are generally chewy and have a hard texture, but recently, as people's tastes have diversified, there has been a tendency to prefer those with a soft texture. In addition, when nuts are used in combination with other foods or sweets, depending on the partner, nuts with a soft texture may be required, as hard nuts give a foreign body sensation. As yet, there was nothing that met that request. (Means for Solving the Problems) The present inventors have overcome the above-mentioned problems and have developed a new nut product that extracts and removes astringency, off-taste, and off-flavor components in an industrially advantageous manner, and at the same time improves the texture. As a result of intensive studies on the production method of nuts, we found that they can be easily extracted and removed by using subcritical or supercritical CO 2 as an extractant, and that the nuts obtained by this process can be used to produce their own The inventors discovered that it is possible to expand the nut food while maintaining its shape, and that an unprecedented nut food can be obtained, leading to the completion of the present invention. In the present invention, CO 2 in a subcritical or supercritical state is at a pressure of 50 to 500 Kg/cm 2 , preferably
60~300Kg/ cm2 , temperature 25~100℃, preferably 25~
A temperature of 70°C is preferably used. Moreover, the extraction time is suitably 1 to 10 hours. In the present invention, the subcritical state is also referred to as a sub-critical or near-critical liquid state, and there is no uniform definition of it. However, according to common sense, 1.00
>Temperature (T)/critical temperature (Tc)>0.95 is considered to be universal. In CO2 this is 30℃
Equivalent to ~16℃. This region is clearly not a supercritical region, nor is it simply a liquid phase region. This is the boundary region between the liquid phase region and the supercritical region, where large changes and fluctuations occur in physical properties, and it is a region that is extremely unstable and activated in terms of properties. It is now recognized as a remarkable area with a strikingly different appearance. Also, CO 2 in the supercritical region is 31.0℃ and 72.9atm.
Because it has a density close to that of a liquid and a large diffusion coefficient close to that of a gas, various compounds can be extracted quickly and in large quantities, and the extractant can be easily separated. The pressure and temperature of CO 2 may be appropriately selected within the above range depending on the type of nuts used as raw materials or the degree of extraction of astringency, off-taste, off-odor components, etc. In particular, regarding the pressurization time, in order to obtain the desired swelling degree of the nut food of the present invention,
The length may be increased or shortened as appropriate, and when releasing the pressure in the extraction tank, the pressure is returned to normal pressure in stages while maintaining the temperature at the time of extraction and so as not to destroy the original shape of the nut food due to sudden pressure release. It is effective to do so. In the present invention, off-taste and off-odor components are a general term for things such as astringent taste, oxidized odor, and mold odor. The present invention may be carried out by conventional methods. For example, CO 2 compressed to a predetermined pressure is first heated to a predetermined extraction temperature and brought into a subcritical or supercritical state and introduced into the lower part of the extraction tank. Raw materials such as nuts are placed in the extraction tank in advance, and after extraction with CO 2 , the pressure of the CO 2 containing the extraction target is reduced through a pressure reducing valve and led to a separator, where the extract is separated from the CO 2 . . The CO 2 separated from the extract is cooled in a condenser, liquefied, recompressed and recycled. (Function) CO 2 in a subcritical or supercritical state has a density close to that of a liquid and a large diffusion coefficient close to that of a gas, and because of these characteristics, it can quickly and efficiently extract various compounds, especially oily substances, in large quantities. can. However, if the pressure and temperature are too low, the CO 2 becomes liquefied, which reduces the extraction capacity, and if the pressure and temperature are too high, the equipment cost increases, causing problems in economic efficiency, and depressurization takes a long time. This is disadvantageous in industrial practice, as oil and flavor components, which are the active ingredients in nuts, dissolve in CO 2 and are released at the same time as the pressure is reduced. The components that give nuts such as astringency and off-taste mainly exist in the surface layer of nuts, but when these are extracted and removed according to the present invention, over time they are gradually removed from the surface layer of the raw material. Since it is thought that the extraction action progresses towards the inside, the degree of extraction is appropriately controlled by experimentally determining the extraction conditions. In addition, the reason why the raw material nuts are swollen to an appropriate degree by this method is that CO 2 in a subcritical or supercritical state enters the raw material structure during the extraction and removal, and eventually gas is released. This is thought to be due to the volume expansion of CO 2 when the pressure is reduced to . (Example) The present invention will be explained in further detail by referring to Examples below. Example 1 1000g of raw almond beans was put into two extraction tanks,
Extraction was performed for 3 hours using CO 2 as an extractant at a pressure of 220 Kg/cm 2 and a temperature of 43°C, and the product was separated at room temperature and atmospheric pressure.
The amount removed by extraction was 12.1 g. The temperature inside the extraction tank
While maintaining the temperature at 43°C, the pressure in the extraction tank was gradually lowered to atmospheric pressure to obtain defatted raw almond beans. After this treatment, the raw almond beans did not lose their original shape, but the surface part swelled and became soft. In addition, the raw almond beans were subsequently roasted in a conventional manner and a sensory test was conducted on the flavor. The results are shown in Table 1. Table 1 shows the average values of the flavor and texture evaluations of the products of the present invention and the control products (untreated products) by a panel of 20 in-house experts through sensory tests.

【表】【table】

【表】 上表によれば食感は本発明の方法によるものが
有意に軟らかいとされており、また風味について
も本発明の方法によるものの方が高い評価を得て
いる。 実施例 2 ブラジルナツツ生豆920gを2抽出槽に仕込
み、圧力240Kg/cm2、温度46℃のCO2を抽剤として
3時間抽出を行ない、常温大気圧下で分離したと
ころ、抽出除去量は15.3gであつた。実施例1と
同様の抽出槽内減圧操作によりブラジルナツツ生
豆を得た。この処理ずみブラジルナツツ生豆の原
形は崩れておらず、実施例1と同様表面部分が膨
化し軟らかくなつていた。 また、この処理ずみブラジルナツツ生豆の風味
及び食感について、社内専門家パネル20名によ
り、それぞれ官能検査を実施した。その結果を平
均値で示したものが表2である。
[Table] According to the above table, the food texture obtained by the method of the present invention is said to be significantly softer, and the flavor obtained by the method of the present invention is also evaluated to be higher. Example 2 920g of Brazilian nut raw beans were placed in two extraction tanks, and extracted for 3 hours using CO2 at a pressure of 240Kg/cm 2 and a temperature of 46°C as an extractant, and separated at room temperature and atmospheric pressure. It was 15.3g. Brazil nut raw beans were obtained by the same vacuum operation in the extraction tank as in Example 1. The original shape of the treated Brazilian nut green beans remained intact, and the surface portions were swollen and soft, as in Example 1. In addition, a sensory test was conducted by a panel of 20 in-house experts regarding the flavor and texture of the processed Brazilian nut green beans. Table 2 shows the results as average values.

【表】 上表によれば、風味、食感とも本発明の方法に
よるものの方が有意に好まれていることががわか
る。 実施例 3 実施例1で得たアーモンドを常法通りにロース
トした後1/4〜1/8の大きさに破砕してアーモンド
細粒を調製した。このアーモンド細粒をテンパリ
ング処理をしたチヨコレート生地中にチヨコレー
ト生地:アーモンド=9:1の重量比率で混合
し、ミキサーで撹拌した後、凍結乾燥装置により
減圧してチヨコレートを膨化させると同時に冷却
を行ないチヨコレート部分を固化させて、気泡入
りチヨコレートを作成した。 比較例 1 実施例1で得たアーモンドを使用する代わり
に、無処理の通常のアーモンドを使用して、上記
と同様にして気泡入りチヨコレートを作成した。
実施例3及び比較例1で作られたアーモンド入り
チヨコレート菓子について社内専門家パネル20名
により、それぞれ官能検査を実施した。その結果
を平均値で示したものが表3である。
[Table] According to the above table, it can be seen that the food prepared by the method of the present invention is significantly preferred in both flavor and texture. Example 3 The almonds obtained in Example 1 were roasted in a conventional manner and then crushed to 1/4 to 1/8 size to prepare fine almond granules. These fine almond granules are mixed into the tempered Chiyocolate dough at a weight ratio of Chiyocolate dough: Almonds = 9:1, stirred with a mixer, and then depressurized with a freeze dryer to expand the Chiyocolate and cooled at the same time. The Chiyokolate portion was solidified to create a bubble-filled Chiyocolate. Comparative Example 1 Instead of using the almonds obtained in Example 1, untreated regular almonds were used to prepare an aerated tyokolate in the same manner as above.
A sensory test was conducted on the almond-containing chiyocolate confectionery prepared in Example 3 and Comparative Example 1 by a panel of 20 in-house experts. Table 3 shows the results as average values.

【表】 上表によれば、風味、食感とも本発明の方法に
よるものの方が好まれる傾向にあり、特に食感の
面で著しい結果となつた。 (発明の効果) 本発明の方法により、下記の優れた効果が奏せ
られる。 (1) 亜臨界または超臨界状態のCO2を抽剤として
渋味、異味、異臭成分を抽出除去するだけでナ
ツツ類の品質が改良され、さらにこれら原料自
身が膨化して従来にない優れた品質の新規なナ
ツツ類食品として、つまみ等に用いられ、ある
いはスナツク菓子、デザート等の菓子、食品用
の新しい素材として利用できることが可能とな
つた。 本件処理においては、わずかな圧力・温度の
変化によつて抽剤との分離も容易であるうえ、
不活性雰囲気下に比較的低温での処理が可能で
あり、またCO2による静菌ないし殺菌効果まで
が期待できるので安全かつ衛生的であること、
取扱操作が簡単で効率の良い脂質分離ができる
ことなど数々の利点を享受することができる。
従つてナツツ類からの渋味、異味、異臭成分等
の抽出除去及び膨化には最も適した方法であ
る。 (2) 不活性雰囲気下に比較的低温で不要成分の抽
出除去が可能であり、また残留有機溶媒の問題
が全くなく安全かつ衛生的であり、原料の変質
を伴わない。 (3) 原料原形を崩さない状態で不要成分を除去す
ることも可能である。
[Table] According to the above table, there was a tendency for the products prepared by the method of the present invention to be preferred in both flavor and texture, and the results were particularly remarkable in terms of texture. (Effects of the Invention) The method of the present invention provides the following excellent effects. (1) The quality of nuts can be improved simply by extracting and removing astringent, off-taste, and off-flavor components using CO 2 in a subcritical or supercritical state as an extractant, and furthermore, these raw materials themselves can be expanded to create an unprecedented and excellent product. It has become possible to use it as a nut food with a new quality, such as snacks, or as a new material for confectionery such as snacks, desserts, and foods. In this process, separation from the extractant is easy due to slight changes in pressure and temperature, and
It is safe and hygienic, as it can be processed at relatively low temperatures in an inert atmosphere, and can be expected to have a bacteriostatic or sterilizing effect due to CO2 .
It offers many advantages such as easy handling and efficient lipid separation.
Therefore, it is the most suitable method for extracting and removing astringency, off-taste, off-odor components, etc. from nuts, and for puffing. (2) It is possible to extract and remove unnecessary components at relatively low temperatures in an inert atmosphere, and there is no problem with residual organic solvents, making it safe and hygienic, and does not involve deterioration of raw materials. (3) It is also possible to remove unnecessary components without destroying the original form of the raw material.

Claims (1)

【特許請求の範囲】 1 ナツツ類を仕込んだ抽出槽において圧力220
〜240Kg/cm2程度、温度43〜46℃程度の二酸化炭素
により、3時間程度抽出した後、前記温度を保持
して段階的に常圧に戻すことにより得られたこと
を特徴とするナツツ類食品。 2 ナツツ類を仕込んだ抽出槽において圧力220
〜240Kg/cm2程度、温度43〜46℃程度の二酸化炭素
により、3時間程度抽出した後、前記温度を保持
して段階的に常圧に戻すことを特徴とするナツツ
類食品の製造法。
[Claims] 1. In the extraction tank containing nuts, the pressure is 220
Nuts characterized by being obtained by extracting with carbon dioxide at a temperature of about 43 to 46°C at a temperature of about 43 to 46°C for about 3 hours, and then gradually returning the pressure to normal pressure while maintaining the temperature. food. 2 Pressure 220 in the extraction tank containing nuts
A method for producing a nut food, which comprises extracting with carbon dioxide at a temperature of about 43 to 46° C. at a temperature of about 43 to 46° C. for about 3 hours, and then gradually returning the pressure to normal pressure while maintaining the temperature.
JP63070473A 1988-03-23 1988-03-23 Nuts food and production thereof Granted JPH01243969A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63070473A JPH01243969A (en) 1988-03-23 1988-03-23 Nuts food and production thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63070473A JPH01243969A (en) 1988-03-23 1988-03-23 Nuts food and production thereof

Publications (2)

Publication Number Publication Date
JPH01243969A JPH01243969A (en) 1989-09-28
JPH0475751B2 true JPH0475751B2 (en) 1992-12-01

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Family Applications (1)

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JP63070473A Granted JPH01243969A (en) 1988-03-23 1988-03-23 Nuts food and production thereof

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Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1336146C (en) * 1989-09-29 1995-07-04 Chand Arjun Passey Process for preparing low-calorie nuts
JPH069479A (en) * 1992-06-26 1994-01-18 Kyodo Kumiai Okinawa Pref Gov Kinousei Shokuhin Kaihatsu Center A method for extracting curcumin from ukon @(3754/24)curcuma longa l.)
CN100413951C (en) * 2006-05-22 2008-08-27 西北农林科技大学 Supercritical CO2 Extraction Process of Almond Oil
WO2017023223A1 (en) * 2015-08-05 2017-02-09 Aromsa Besin Aroma Ve Katki Maddeleri Sanayi Ve Ticaret Anonim Sirketi Production method of hazelnut extract containing ethyl alcohol by supercritical extraction
WO2017023226A1 (en) * 2015-08-06 2017-02-09 Aromsa Besin Aroma Ve Katki Maddeleri Sanayi Ve Ticaret Anonim Sirketi Production method of ethyl alcohol-free hazelnut extract by supercritical extraction
CN109953922A (en) * 2019-04-16 2019-07-02 中国热带农业科学院南亚热带作物研究所 A kind of macadamia nut green peel extract and its preparation method and application

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6394951A (en) * 1986-10-07 1988-04-26 Seitetsu Kagaku Co Ltd Production of food of nuts or beans

Also Published As

Publication number Publication date
JPH01243969A (en) 1989-09-28

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