JPH06113761A - Production of nonwashing rice - Google Patents

Production of nonwashing rice

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Publication number
JPH06113761A
JPH06113761A JP4290834A JP29083492A JPH06113761A JP H06113761 A JPH06113761 A JP H06113761A JP 4290834 A JP4290834 A JP 4290834A JP 29083492 A JP29083492 A JP 29083492A JP H06113761 A JPH06113761 A JP H06113761A
Authority
JP
Japan
Prior art keywords
rice
carbon dioxide
lipid content
lipid
yield
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
JP4290834A
Other languages
Japanese (ja)
Inventor
Yoichiro Ono
野 陽 一 郎 小
Masamitsu Ito
藤 真 実 伊
Kitoku Saegusa
枝 樹 徳 三
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.)
Hitachi Plant Technologies Ltd
Original Assignee
Hitachi Plant Technologies 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 Hitachi Plant Technologies Ltd filed Critical Hitachi Plant Technologies Ltd
Priority to JP4290834A priority Critical patent/JPH06113761A/en
Publication of JPH06113761A publication Critical patent/JPH06113761A/en
Pending legal-status Critical Current

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  • Cereal-Derived Products (AREA)
  • Extraction Or Liquid Replacement (AREA)

Abstract

PURPOSE:To provide nonwashing rice needless to wash, also capable of improving its polishing yield. CONSTITUTION:In an extraction tank 12, rice 10 is brought into contact with liquid carbon dioxide or carbon dioxide in a supercritical state to extract the lipid component in the rice 10 into the carbon dioxide to effect dissolution of such component in the carbon dioxide. The pressure of the resultant carbon dioxide is reduced using a backpressure valve 16 and the carbon dioxide is brought to the inlet of a separatory tank 14 where the lipid component is separated from the carbon dioxide because the depressurized carbon dioxide less dissolves the lipid component. The carbon dioxide freed from the lipid component is passed through a filter 20, an activated carbon adsorption column 22, into a condenser 24 where it is liquefied again and returned to a high-pressure pump 26. With such carbon dioxide circulation, the lipid content of the rice can be reduced to about 0.8wt.%, a level attained by further washing normal polished rice (89-90% in polishing yield).

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、無洗米の製造方法に係
り、特に、米の脂質分を脱脂する無洗米の製造方法に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing non-washed rice, and more particularly to a method for producing non-washed rice by defatting the lipid content of rice.

【0002】[0002]

【従来の技術】一般に、刈り取られた稲は、脱穀された
後、籾が取り除かれ玄米となる。玄米は3%程度の脂質
分を含み、その大部分は玄米表層部に存在しており、こ
の脂質分が米の美味みを落とす要因になっている。この
為、通常、玄米を精米機にかけ、玄米の表層部を10%
程度(精米歩留90%)削り取り、これにより玄米の脂
質分を3%程度から1%程度まで落としたものを販売し
ている。
2. Description of the Related Art Generally, mowed rice is threshed and then unhulled to become brown rice. Brown rice contains about 3% of lipid content, and most of it exists in the surface layer of brown rice, and this lipid content is a factor that reduces the taste of rice. For this reason, brown rice is usually put on a rice polishing machine and the surface layer of brown rice is 10%.
About 90% of rice yield is scraped off, and the rice with the lipid content of brown rice reduced from 3% to 1% is sold.

【0003】ちなみに、精米によって削りとられ、粉状
になったものが糠である。また、このように精米された
米を炊飯する場合、米を水で洗米し、精米時付着した糠
を洗い流した後、一定量の水を加えたものを炊飯に供し
ているが、大量に洗米する工場の食堂のようなところで
は、洗米に手間が掛かるだけではなく、洗米によって発
生する廃水は、糠に起因するBODが高く、河川等の環
境汚染の要因になっている。家庭で発生する洗米廃水に
ついても同様である。
By the way, the bran is the one that has been scraped off by milling and turned into a powder. When cooking rice that has been polished in this way, the rice is washed with water, the bran that has adhered during rice polishing is washed off, and then a certain amount of water is added to the rice for cooking. In a place like a cafeteria of a factory, washing rice is not only time-consuming, but waste water generated by washing rice has a high BOD due to the bran, which causes environmental pollution of rivers and the like. The same applies to the rice rinsing wastewater generated at home.

【0004】このような背景から、特公平02─265
448の公報に見られるように、玄米を精米した後、水
洗、乾燥を行ったものを販売し、炊飯時洗米せずにその
まま使用できるようにした方法がある。
From such a background, Japanese Patent Publication No. 02-265
As disclosed in Japanese Patent No. 448, there is a method in which brown rice is polished, washed with water and dried, and then sold so that it can be used as it is without being washed when cooking rice.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、従来の
技術には次のような欠点がある。 (イ)玄米の精米、水洗、乾燥までを行なったものを販
売し、炊飯時、洗米による廃水がでないようにした方法
は、前記乾燥の工程で米に亀裂が生じやすく商品価値で
見劣り、また前記水洗の工程で洗米廃水が出ることにか
わりはない。 (ロ)玄米の脂質分を3%程度から1%程度まで落とす
為に、玄米の精米工程で玄米表層部を10%程度も削り
取る必要がある。玄米表層部を削り取って発生した糠に
は糖質が4〜5%も含まれているにもかかわらず、糠と
して廃棄されており、米の利用率低下につながってい
る。
However, the conventional techniques have the following drawbacks. (B) The method of selling brown rice that has been polished, washed with water and dried so as to prevent waste water from washing during rice cooking is liable to cause cracks in the rice during the drying process, and is inferior in commercial value. There is no change in the waste water of rice washing from the washing step. (B) In order to reduce the lipid content of brown rice from about 3% to about 1%, it is necessary to scrape about 10% of the surface layer of brown rice in the rice polishing process of brown rice. Although the bran generated by scraping off the surface layer of brown rice contains 4-5% of sugar, it is discarded as bran, leading to a decrease in rice utilization.

【0006】また、精米することで栄養素であるビタミ
ンB1 が80%除かれ、更に、洗米すると大部分なくな
ってしまうように、精米だけでなく洗米によっても栄養
価を下げる原因になっている。このように、精米した米
は味や消化吸収率は改善されるが、精米歩留が悪くなる
と共に、玄米に比べ栄養価はかなり減少する。この為、
胚芽米やビタミンB1強化米等が販売されているが、
味、価格の面で充分とは言いがたい。
In addition, 80% of vitamin B 1 which is a nutrient is removed by polishing rice, and further, it is mostly lost by washing rice, which is a cause of lowering nutritional value not only by polishing rice but also by washing rice. Thus, the polished rice has improved taste and digestion and absorption rate, but the yield of polished rice is deteriorated and the nutritional value is considerably reduced as compared with brown rice. Therefore,
Although germinated rice and rice with vitamin B 1 enrichment are sold,
In terms of taste and price, it is hard to say.

【0007】本発明はこのような事情に鑑みてなされた
もので、洗米の必要がなく、しかも精米歩留を向上でき
る無洗米の製造方法を提供することを目的とする。
The present invention has been made in view of the above circumstances, and an object thereof is to provide a method for producing non-washed rice which does not require washing and can improve the yield of polished rice.

【0008】[0008]

【課題を解決する為の手段】本発明は、前記目的を達成
する為に、玄米を所定の歩留に精米した米を、液状又は
超臨界状態の二酸化炭素と接触させ、前記米の脂質分を
前記二酸化炭素で抽出すると共に、前記脂質分が前記二
酸化炭素に溶解させることを特徴とする。
[Means for Solving the Problems] In order to achieve the above-mentioned object, the present invention comprises contacting a rice obtained by milling brown rice with a predetermined yield with liquid carbon dioxide in a liquid or supercritical state to obtain a lipid content of the rice. Is extracted with the carbon dioxide, and the lipid component is dissolved in the carbon dioxide.

【0009】[0009]

【作用】本発明によれば、二酸化炭素に圧力50〜30
0kg/cm2 、温度0〜100℃、の条件を付与し、
前記二酸化炭素を液状または超臨界状態にする。次に、
玄米を所定の歩留に精米した米を、前記条件を有する二
酸化炭素と接触させ、前記米の脂質分を前記二酸化炭素
中に抽出すると共に、前記脂質分を前記二酸化炭素に溶
解させる。
According to the present invention, carbon dioxide has a pressure of 50 to 30.
The conditions of 0 kg / cm 2 and temperature 0 to 100 ° C. are applied,
The carbon dioxide is brought into a liquid state or a supercritical state. next,
Rice obtained by milling brown rice to a predetermined yield is contacted with carbon dioxide having the above conditions to extract the lipid content of the rice into the carbon dioxide and dissolve the lipid content in the carbon dioxide.

【0010】これにより、前記米から脂質分が脱脂され
る。
As a result, the lipid content of the rice is defatted.

【0011】[0011]

【実施例】以下添付図面に従って本発明に係る無洗米の
製造方法の好ましい実施例について詳説する。図1に示
すように、米10の脂質分を二酸化炭素に抽出し溶解さ
せる耐圧容器としての抽出槽12と、前記米10の脂質
分を溶解した前記二酸化炭素から前記米10の脂質分を
分離させる耐圧容器としての分離槽14が設けられてい
る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A preferred embodiment of the method for producing non-washed rice according to the present invention will be described in detail below with reference to the accompanying drawings. As shown in FIG. 1, the extraction tank 12 as a pressure-resistant container for extracting and dissolving the lipid content of the rice 10 in carbon dioxide, and the lipid content of the rice 10 is separated from the carbon dioxide in which the lipid content of the rice 10 is dissolved. A separation tank 14 is provided as a pressure resistant container.

【0012】前記抽出槽12出口から背圧弁16を介し
て、配管18により前記分離槽14入口に接続され、前
記分離槽14出口からフィルタ20、活性炭吸着槽2
2、凝縮器24、高圧ポンプ26、熱交換器28を介し
て、配管30により前記抽出槽12入口に接続され、前
記二酸化炭素の循環系路を形成している。また、前記高
圧ポンプ26入口には液化二酸化炭素のボンベ32が配
管34により接続され、二酸化炭素を前記循環系路に供
給するようになっている。
The outlet of the extraction tank 12 is connected to the inlet of the separation tank 14 by a pipe 18 through the back pressure valve 16, and the outlet of the separation tank 14 is connected to the filter 20 and the activated carbon adsorption tank 2
2, a condenser 24, a high-pressure pump 26, and a heat exchanger 28, and is connected to the inlet of the extraction tank 12 by a pipe 30 to form a carbon dioxide circulation system passage. A liquefied carbon dioxide cylinder 32 is connected to the inlet of the high-pressure pump 26 by a pipe 34 to supply carbon dioxide to the circulation system passage.

【0013】次に、このように構成された装置の作用に
ついて説明すると、先ず、玄米を所定の歩留に精米した
米10を予め前記抽出槽12に入れておく。そして、液
化二酸化炭素ボンベ32から二酸化炭素を高圧ポンプ2
6に供給し、前記二酸化炭素を所定の圧力に加圧した
後、熱交換器28に送る。前記熱交換器28では前記二
酸化炭素を所定の温度に加温し、前記抽出槽12に供給
する。
Next, the operation of the apparatus thus constructed will be described. First, the rice 10 obtained by milling brown rice to a predetermined yield is put in the extraction tank 12 in advance. Then, a high-pressure pump 2 for supplying carbon dioxide from the liquefied carbon dioxide cylinder 32
6, the carbon dioxide is pressurized to a predetermined pressure, and then sent to the heat exchanger 28. In the heat exchanger 28, the carbon dioxide is heated to a predetermined temperature and supplied to the extraction tank 12.

【0014】前記抽出槽12では、予め前記抽出槽12
に入れておいた前記米10と前記二酸化炭素とを接触
し、前記米10の脂質分を前記二酸化炭素に抽出すると
共に、前記脂質分を前記二酸化炭素に溶解させる。前記
米10の脂質分を溶解した前記二酸化炭素は、背圧弁1
6に送られ、前記背圧弁16で前記二酸化炭素の圧力が
減圧され、ガス化した後、分離槽14に送られる。
In the extraction tank 12, the extraction tank 12 is previously
The rice 10 stored in the above is contacted with the carbon dioxide, and the lipid content of the rice 10 is extracted into the carbon dioxide and the lipid content is dissolved in the carbon dioxide. The carbon dioxide in which the lipid content of the rice 10 is dissolved is the back pressure valve 1
6, the pressure of the carbon dioxide is reduced by the back pressure valve 16, gasified, and then sent to the separation tank 14.

【0015】前記ガス化した二酸化炭素は、脂質の溶解
度が低くなる為、前記分離槽14に送られたガス化した
前記二酸化炭素は、溶解している前記脂質分を分離槽1
4内に分離する(前記分離槽に分離された脂質分を図1
中に符号36で示す)。前記分離槽14で脂質分を分離
した前記のガス化した二酸化炭素は、フィルタ20及び
活性炭吸着塔22に送られ、抽出時、同伴した不純物を
除去した後、凝縮器24で再び液化されて高圧ポンプ2
6に戻る。
Since the gasified carbon dioxide has a low solubility of lipids, the gasified carbon dioxide sent to the separation tank 14 separates the dissolved lipid component from the separation tank 1.
4 (the lipid content separated in the separation tank is shown in FIG.
Designated by reference numeral 36). The gasified carbon dioxide from which the lipid content has been separated in the separation tank 14 is sent to the filter 20 and the activated carbon adsorption tower 22, and the impurities that are entrained during the extraction are removed and then liquefied again in the condenser 24 to obtain a high pressure. Pump 2
Return to 6.

【0016】以上、上記装置に二酸化炭素を所定の条件
下で循環させることにより、前記米10の脂質分を脱脂
することができる。 〔実例〕上記装置を用いて米から脂質分を脱脂した一例
を以下に示す。千葉産コシヒカリの玄米を、精米歩留8
7%〜100%(玄米)となるようにう精米した米をサ
ンプルとして調製した。
As described above, the lipid content of the rice 10 can be defatted by circulating carbon dioxide in the above device under predetermined conditions. [Example] An example of defatting lipid components from rice using the above-mentioned device is shown below. Koshihikari brown rice from Chiba, rice yield 8
Rice that had been milled to 7% to 100% (brown rice) was prepared as a sample.

【0017】また、抽出槽で前記米の脂質分を抽出、溶
解する二酸化炭素に圧力250kg/cm2 、温度35
℃の条件を付与し、超臨界状態とした。また、前記米に
接触する前記二酸化炭素の量は、前記米1kgに対し前
記二酸化炭素5kgとした。前記米を上記条件のもとで
上記装置で処理した結果を図2に示した。
In addition, in the extraction tank, the lipid content of the rice is extracted and dissolved in carbon dioxide to give a pressure of 250 kg / cm 2 and a temperature of 35.
The condition of ° C was applied to make the supercritical state. Further, the amount of carbon dioxide contacting the rice was 5 kg of carbon dioxide for 1 kg of rice. The results of treating the rice with the above apparatus under the above conditions are shown in FIG.

【0018】図2の白丸で示した曲線Aは、上記装置で
処理した米の脂質量と精米歩留との関係を示し、黒丸で
示した曲線Bは、従来の精米方法で処理した米の脂質量
と精米歩留との関係を示している。通常の白米(精米歩
留89〜90%)を、更に洗米した後の米の脂質量は
0.8%程度であり、所謂、無洗米として要求される米
の脂質量を0.8%程度とすると、本発明による方法の
場合、精米歩留93〜95%に調整した米を、上記装置
及び上記条件下で処理すれば、処理後の米の脂質量を
0.8%程度にすることができる。
The curve A shown by white circles in FIG. 2 shows the relationship between the lipid content of the rice treated by the above-mentioned apparatus and the rice polishing yield, and the curve B shown by black circles shows the relationship between the rice treated by the conventional rice polishing method. It shows the relationship between the amount of lipids and rice yield. Normal white rice (polished rice yield 89-90%) has a lipid content of about 0.8% after further washing, and so-called non-washed rice has a lipid content of about 0.8%. Then, in the case of the method according to the present invention, if the rice adjusted to a rice polishing yield of 93 to 95% is treated under the above apparatus and under the above conditions, the lipid content of the treated rice will be about 0.8%. You can

【0019】即ち、5分づき米から7分づき米程度であ
っても、通常の白米(精米歩留89〜90%)を洗米し
た時の脂質量と同等になる。この結果から明らかなよう
に、本発明による方法によれば、従来の方法に比べ精米
歩留を4〜5%増加することができるので、米の利用率
が向上する。また、精米歩留93〜95%の米のビタミ
ンB1 の含有量は0・31〜0.40%あり、従来の精
米方法では洗米後でビタミンB1 は大部分なくなってし
まうのに対し、本発明による方法によれば玄米の半分以
上が残存しており、栄養価の面でも優れていた。
That is, even if the rice is from 5 minutes to 7 minutes, the amount of lipid is the same as that when the normal white rice (rice polishing yield 89 to 90%) is washed. As is clear from this result, according to the method of the present invention, the rice polishing yield can be increased by 4 to 5% as compared with the conventional method, so that the utilization rate of rice is improved. In addition, the content of vitamin B 1 in rice with a rice polishing yield of 93 to 95% is 0.31 to 0.40%, whereas vitamin B 1 is largely lost after washing with the conventional rice polishing method. According to the method of the present invention, more than half of the brown rice remained, which was excellent in nutritional value.

【0020】[0020]

【発明の効果】以上、説明したように本発明に係る無洗
米の製造方法によれば、玄米を所定の歩留に精米した米
と、液状又は超臨界状態の二酸化炭素とを接触させるこ
とにより、前記米の脂質分を、通常の白米(精米歩留8
9〜90%)を、更に洗米した時の米の脂質量である
0.8%程度まで脱脂することができるので、洗米しな
いで炊飯に供することができる。
As described above, according to the method for producing non-washed rice according to the present invention, by contacting the brown rice polished with a predetermined yield with carbon dioxide in a liquid or supercritical state. , The lipid content of the rice is converted to normal white rice (polished rice yield 8
9 to 90%) can be defatted to a lipid content of about 0.8% when the rice is further washed, so that the rice can be cooked without being washed.

【0021】また、精米時、米の脂質分を下げる為に、
玄米の表面を削り取る割合が少なくてすみ、精米歩留を
増加でき、米の利用率の向上を図れると共に、ビタミン
1の残存率も多く、栄養価の高い米を提供することが
できる。
Further, in order to reduce the lipid content of rice at the time of rice polishing,
The rate of scraping off the surface of brown rice is small, the yield of polished rice can be increased, the utilization rate of rice can be improved, and the residual rate of vitamin B 1 is high, so that rice with high nutritional value can be provided.

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

【図1】本発明に係る無洗米の製造方法の説明図FIG. 1 is an explanatory view of a method for producing non-washed rice according to the present invention.

【図2】本発明の効果を示す脂質と精米歩留の関係図FIG. 2 is a diagram showing the relationship between lipid and rice yield showing the effect of the present invention.

【符号の説明】[Explanation of symbols]

10…米 12…抽出槽 14…分離槽 10 ... Rice 12 ... Extraction tank 14 ... Separation tank

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 玄米を所定の歩留に精米した米を、液状
又は超臨界状態の二酸化炭素と接触させて、前記米の脂
質分を前記二酸化炭素で抽出・溶解することを特徴とす
る無洗米の製造方法。
1. A method in which rice obtained by polishing brown rice to a predetermined yield is contacted with carbon dioxide in a liquid or supercritical state, and the lipid content of the rice is extracted and dissolved with the carbon dioxide. Method for manufacturing washed rice.
【請求項2】 前記抽出工程での二酸化炭素は、温度0
〜100℃、圧力50〜300kg/cm2 の条件で、
液状又は超臨界状態であることを特徴とする請求項1の
無洗米の製造方法。
2. The carbon dioxide in the extraction step has a temperature of 0.
Under the conditions of ~ 100 ° C and pressure of 50-300 kg / cm 2 ,
The method for producing non-washed rice according to claim 1, which is in a liquid state or a supercritical state.
【請求項3】 前記米の脂質分の抽出・溶解後、前記二
酸化炭素の圧力を減圧し、前記二酸化炭素から前記脂質
分を分離させることを特徴とする請求項1の無洗米の製
造方法。
3. The method for producing non-washed rice according to claim 1, wherein after extracting and dissolving the lipid content of the rice, the pressure of the carbon dioxide is reduced to separate the lipid content from the carbon dioxide.
JP4290834A 1992-10-05 1992-10-05 Production of nonwashing rice Pending JPH06113761A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4290834A JPH06113761A (en) 1992-10-05 1992-10-05 Production of nonwashing rice

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4290834A JPH06113761A (en) 1992-10-05 1992-10-05 Production of nonwashing rice

Publications (1)

Publication Number Publication Date
JPH06113761A true JPH06113761A (en) 1994-04-26

Family

ID=17761093

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4290834A Pending JPH06113761A (en) 1992-10-05 1992-10-05 Production of nonwashing rice

Country Status (1)

Country Link
JP (1) JPH06113761A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100359646B1 (en) * 2000-10-05 2002-11-04 김현효 Recycling System and Method of Supercritical Carbon Dioxide
WO2004058376A1 (en) * 2002-12-30 2004-07-15 Korea Supercritical Extraction Co., Ltd. Extractor using co2 gas
JP2004535495A (en) * 2001-07-04 2004-11-25 デグサ アクチエンゲゼルシャフト Physical treatment of starch (-derivative)
KR20060118220A (en) * 2005-05-16 2006-11-23 주식회사 유맥스 Method for production of fat removal powder from raw materials of edible oil and fat removal powder thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100359646B1 (en) * 2000-10-05 2002-11-04 김현효 Recycling System and Method of Supercritical Carbon Dioxide
JP2004535495A (en) * 2001-07-04 2004-11-25 デグサ アクチエンゲゼルシャフト Physical treatment of starch (-derivative)
WO2004058376A1 (en) * 2002-12-30 2004-07-15 Korea Supercritical Extraction Co., Ltd. Extractor using co2 gas
KR20060118220A (en) * 2005-05-16 2006-11-23 주식회사 유맥스 Method for production of fat removal powder from raw materials of edible oil and fat removal powder thereof

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