JPH0269149A - Production of processed unpolished rice - Google Patents

Production of processed unpolished rice

Info

Publication number
JPH0269149A
JPH0269149A JP63216320A JP21632088A JPH0269149A JP H0269149 A JPH0269149 A JP H0269149A JP 63216320 A JP63216320 A JP 63216320A JP 21632088 A JP21632088 A JP 21632088A JP H0269149 A JPH0269149 A JP H0269149A
Authority
JP
Japan
Prior art keywords
rice
brown rice
carbon dioxide
liquid
unpolished rice
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
Application number
JP63216320A
Other languages
Japanese (ja)
Other versions
JP2714405B2 (en
Inventor
Katsushi Hayakawa
克志 早川
Ikuo Kitamura
育夫 北村
Norimitsu Wakabayashi
若林 憲光
Tokuji Yotsuya
四家 徳次
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.)
Nisshin Seifun Group Inc
Resonac Gas Products Corp
Original Assignee
Showa Tansan Co Ltd
Nisshin Seifun Group Inc
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 Showa Tansan Co Ltd, Nisshin Seifun Group Inc filed Critical Showa Tansan Co Ltd
Priority to JP63216320A priority Critical patent/JP2714405B2/en
Publication of JPH0269149A publication Critical patent/JPH0269149A/en
Application granted granted Critical
Publication of JP2714405B2 publication Critical patent/JP2714405B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To obtain the title rice cookable into unpolished rice with high nutritive value and good eating feel through a simple method similar to the case with polished rice by removing part of the surface layer over the entire surface of unpolished rice followed by bringing the resultant unpolished rice into contact with a liquid CO2 or CO2 in the supercritical state. CONSTITUTION:Part of the surface layer, corresponding to rice bran (matrix skin, seed skin and/or paste powder layer), of unpolished rice is removed over the entire surface of unpolished rice grains. When said removal operation is to be made by e.g., beating in a mortar, it should be made under conditions milder than those in the case with normal rice cleaning treatment for obtaining polished rice. Thence, the resultant unpolished rice is brought into contact with a liquid CO2 or CO2 in the supercritical state. This state is pref. such that, as shown in the figure, the temperature is -20-100 deg.C and the pressure >=20kg/cm<2>. As a result, part of lipids as well as such offensive odors as of rice bran will be extracted or eliminated with the various constituents in the unpolished rice prevented from deterioration, thus obtaining the objective processed unpolished rice.

Description

【発明の詳細な説明】 [産業上の利用分野1 本発明は、加工玄米の製造法に関する。詳細には、本発
明は、精白米に対して採用されているのと同様な簡単な
方法で炊飯でき、しかも炊飯によって栄養価が損なわれ
ておらずかつ食感の良い玄米飯を得ることができる加工
玄米の製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application 1] The present invention relates to a method for producing processed brown rice. In detail, the present invention makes it possible to cook rice using a simple method similar to that used for polished rice, and to obtain brown rice that does not lose its nutritional value and has a good texture. Regarding the manufacturing method of processed brown rice.

[従来の技術) 玄米は精白米に比べて脂質、蛋白質、ミネラル、ビタミ
ン等の栄養素に富んでいるために健康食品的な見地から
近年そのを動性が見直されている。しかしながら、玄米
の胚乳部は果皮、種皮、糊粉層などのぬか層と呼ばれる
強靭な外皮で覆われているために、精白米に比べて胚乳
部■こ水が浸透しにくく、玄米を精白米に対して採用さ
れている通常の炊飯方法や調理器具を使用してそのまま
炊いたのでは、硬いパサパサした玄米飯しか得られない
。したがって、玄米を炊飯するにあたっては、通常、圧
力釜を使用するとか二度炊きする等の特殊な調理用具の
使用または手間のかかる炊飯方法が必要であり、それが
玄米の消費の拡大を阻む一つの要因になっている。
[Prior art] Since brown rice is richer in nutrients such as lipids, proteins, minerals, and vitamins than polished rice, its properties have recently been reconsidered from the standpoint of health food. However, because the endosperm of brown rice is covered with a tough outer skin called the bran layer, which includes pericarp, seed coat, and aleurone layer, it is difficult for water to penetrate into the endosperm compared to polished rice, and brown rice is converted into polished rice. If you cook rice as is using the usual cooking methods and cooking utensils used for rice, you will only get hard and dry brown rice. Therefore, cooking brown rice usually requires the use of special cooking utensils or time-consuming cooking methods, such as using a pressure cooker or double-cooking, and this is one of the obstacles to expanding the consumption of brown rice. This is due to two factors.

そこで、精白米と同じように短時間で簡単に炊飯できか
つ食感の良い玄米を提供しようとする試みが色々なされ
ている。そして現在知られている方法としては、 (1)玄米の果皮のほぼ全周に亘って切削刃により多数
の切削傷を設ける方法(特開昭63173548号)、 (2)玄米を過熱水蒸気で加熱し膨化させることによっ
て玄米外皮に亀裂を生じさせて易炊飯化する方法(特開
昭61−61775号)、(3)玄米を吸水、放置後に
蒸煮および圧偏して加工玄米を製造する方法(特開昭6
1−152251号)、 (4)玄米等を超臨界状態の二酸化炭素に接触させる方
法(特開昭59−78656号)等が挙げられる。
Therefore, various attempts have been made to provide brown rice that can be easily cooked in a short time and has a good texture just like polished rice. Currently known methods include: (1) creating many cutting scratches with a cutting blade almost all around the skin of brown rice (Japanese Patent Application Laid-open No. 63173548); (2) heating brown rice with superheated steam; A method for making rice easier to cook by causing cracks in the outer skin of brown rice by swelling it (Japanese Patent Application Laid-Open No. 61-61775); (3) A method for producing processed brown rice by absorbing water, leaving it to stand, then steaming and compressing it; Tokukai Showa 6
1-152251), (4) a method of bringing brown rice etc. into contact with carbon dioxide in a supercritical state (Japanese Unexamined Patent Publication No. 59-78656).

しかしながら、(1)の方法で得られた玄米を炊飯した
ものは、未だバサついて食感が劣り、(2)および(3
)の方法は、蒸気加熱によって玄米が100°C以上に
加熱され、更に(3)の場合には圧偏処理も伴うために
、玄米に含まれる各種栄養素の劣化、胚乳部の変質や損
傷、玄米粒の破壊、崩れ等を招き、かかる玄米を炊飯し
たものは、外観、食感、栄養価等が劣ったものであった
However, cooked brown rice obtained by method (1) is still dry and has poor texture;
In method (3), brown rice is heated to over 100°C by steam heating, and in the case of (3), pressure treatment is also involved, resulting in deterioration of various nutrients contained in brown rice, deterioration and damage to the endosperm, and The brown rice grains were destroyed, crumbled, etc., and the cooked brown rice was inferior in appearance, texture, nutritional value, etc.

また、(4)の方法では表層部の一部除去処理をしてい
ないので、玄米の吸水性の向上は未だ充分ではなく、し
かも玄米からの脱脂も充分ではないために、炊飯しに<
<、かつ異臭が強く、食感および保存性の劣るものであ
った。
In addition, since method (4) does not remove part of the surface layer, the water absorption of brown rice is not yet sufficiently improved, and the fat from the brown rice is not sufficiently removed.
<, and had a strong off-odor and poor texture and shelf life.

[発明の内容] 本発明者等は、精白米に使用されている調理器具をその
まま使用して精白米と同様な簡単な方法で炊飯でき、し
かも炊きあげたときに栄養価が高く且つ型崩れのない食
感の良い玄米飯になる玄米を製造することを目的として
研究を続けてきた。その結果、玄米の表面に特定の損傷
処理を施した後に液状または超臨界状態の二酸化炭素で
処理すると、上記の目的を達成できることを見出して本
発明を完成するに至った。
[Contents of the invention] The present inventors have discovered that rice can be cooked in the same simple way as polished rice using the same cooking utensils used for polished rice, and that it has high nutritional value and loses its shape when cooked. We have continued our research with the aim of producing brown rice that has a good texture and is free from grains. As a result, the present invention was completed by discovering that the above object can be achieved by subjecting the surface of brown rice to a specific damage treatment and then treating it with liquid or supercritical carbon dioxide.

すなわち、本発明は、玄米の表層部の一部を玄米の表面
全体にわたって剥離除去した後、液状または超臨界状態
の二酸化炭素に接触させることを特徴とする加工玄米の
製造法である。
That is, the present invention is a method for producing processed brown rice, which is characterized in that a part of the surface layer of the brown rice is peeled off over the entire surface of the brown rice, and then brought into contact with liquid or supercritical carbon dioxide.

玄米は、もみからもみがらを取り除いたものであり、構
造的に見ると果皮、種皮、糊粉層等のぬかと称されてい
る上層部分、米粒の下方基部にある少量の胚芽部分およ
び残りの大部分を占める中心にある胚乳部分とからなっ
ている。
Brown rice is made by removing the chaff from the rice grains, and its structure consists of the upper layers called bran, such as the pericarp, seed coat, and aleurone layer, a small amount of germ at the lower base of the rice grain, and the rest. It consists of a central endosperm part that occupies the majority.

玄米全粒に対する各部分の重量割合は、一般にぬか部分
約5〜7%、胚芽部分約2〜3%および残部が胚乳部分
(約92%前後)である。白米(精米、精白米)は玄米
からこのぬか部分および胚芽部分を搗精等の精米処理に
よって剥離して胚乳部分のみにしたものであり、普通米
では原料玄米に対して通常約90〜92%の精米歩留り
(搗精歩留り)となっている。
The weight ratio of each part to the whole grain of brown rice is generally about 5 to 7% for the bran part, about 2 to 3% for the germ part, and the rest for the endosperm part (about 92%). White rice (polished rice, milled white rice) is made by removing the bran and germ from brown rice through milling or other polishing processes, leaving only the endosperm. This is the rice milling yield (milling yield).

本発明において「玄米の表層部の一部を玄米の表面全体
にわたって剥離除去する」とは、玄米の上層部にある該
ぬかに相当する部分(果皮、種皮、糊粉層等)の一部を
、場合によってはその下方基部にある胚芽部分とともに
、玄米粒子の表面全体にわたって剥離除去することを意
味する。その際に、出来るだけ均一に該表層部の一部の
剥離除去を行うのが好ましい。
In the present invention, "peeling and removing part of the surface layer of brown rice over the entire surface of brown rice" means that part of the upper layer of brown rice corresponding to the bran (pericarp, seed coat, aleurone layer, etc.) is removed. , meaning exfoliation over the entire surface of the brown rice grain, possibly along with the germ part at its lower base. At that time, it is preferable to peel off and remove a portion of the surface layer as uniformly as possible.

果皮、種皮、糊粉層、胚芽部等の一部剥離除去に際して
は、搗精等の精米操作等において通常採用されているぬ
か部等の剥離除去方法や上記特開昭63−173548
号公報に記載されている切削刃による方法等を採用して
行うことができる。
When removing part of the pericarp, seed coat, aleurone layer, germ, etc., methods for peeling and removing the bran, etc., which are normally adopted in rice milling operations such as milling, or the above-mentioned JP-A-63-173548 can be used.
This can be carried out by employing the method using a cutting blade, etc., as described in the above publication.

搗精等により行う場合は白米を得る通常の精米処理にお
けるよりもその処理の程度を弱くして行う。表層部の一
部の剥離除去を、例えば搗精により行う場合は、摩擦方
式および研削方式等のいずれの搗精方式をも採用できる
When milling or the like is used, the degree of polishing is made weaker than in the normal rice milling process used to obtain polished rice. When removing a part of the surface layer by, for example, polishing, any polishing method such as a friction method or a grinding method can be employed.

本発明における玄米表層部の一部の剥離除去の程度を原
料玄米に対する歩留りで表わすと、通常、約99.8〜
95.0%、好ましくは約99.6〜98.0%の歩留
りになるまでその種皮、果皮、糊粉層、胚芽等を剥離す
るのがよい。上記の範囲の歩留りになるように玄米表面
を剥離させると、次工程での液状または超臨界状態の二
酸化炭素処理を施した後の玄米の吸水率が向上して白米
と同様な操作で簡単に炊飯できるようになると共に、炊
き上げたときに外観および食感が良く、かつ栄養価の高
い玄米飯になる。一方、玄米表1部の剥離除去の程度が
低過ぎると(歩留りが約99.8%より高いと)、次工
程でのnij記二酸二酸化炭素処理っても玄米の吸水率
が上昇せず炊飯が容易でなく、しかも炊きあがった玄米
飯の食感が劣る。また玄米表層部の剥離除去の程度が高
過ぎると(歩留りが約95.0%より低いと)、白米に
より近いものとなって脂質、蛋白質、ミネラル、ビタミ
ン等の栄養素の含有量が極めて少なくなり健康食品とし
ての玄米の意義が失われる。
The degree of peeling and removal of a part of the surface layer of brown rice in the present invention is usually expressed as a yield of about 99.8 to 99.8 to
The seed coat, pericarp, aleurone layer, germ, etc. are preferably peeled off until a yield of 95.0%, preferably about 99.6 to 98.0% is achieved. If the surface of brown rice is peeled to achieve a yield within the above range, the water absorption rate of the brown rice will improve after being treated with liquid or supercritical carbon dioxide in the next process, and it can be easily processed in the same way as white rice. To be able to cook rice, and to have brown rice with good appearance and texture and high nutritional value when cooked. On the other hand, if the degree of exfoliation removal of the first part of brown rice is too low (if the yield is higher than about 99.8%), the water absorption rate of brown rice will not increase even if it is treated with diacid and carbon dioxide in the next process. It is not easy to cook rice, and the texture of the cooked brown rice is inferior. Furthermore, if the degree of exfoliation of the surface layer of brown rice is too high (if the yield is lower than about 95.0%), it will become more similar to white rice and the content of nutrients such as lipids, proteins, minerals, and vitamins will be extremely low. The significance of brown rice as a health food will be lost.

玄米表層部の一部の剥離除去を、温度約S〜30°C1
好ましくは約lO〜25°Cで行うと、玄米の変質、劣
化等が生じない。
Remove part of the surface layer of brown rice at a temperature of about S to 30°C1
Preferably, if the temperature is about 10 to 25°C, brown rice will not change in quality or deteriorate.

また玄米表層部の一部の剥離除去に際しては、玄米中の
水分含量が、約12〜25重量%であるようにして処理
を行うのがよい。水分含量が上記の範囲内にある限り、
玄米をそのまま地理してもまたは水分を添加してもよい
。玄米の水分含量を特に約15〜20M量%にしておく
と玄米からの表層部の剥離除去が均一に行われ玄米粉の
砕は等が生じず好ましい。
Further, when removing a part of the surface layer of brown rice, it is preferable to carry out the treatment so that the water content in the brown rice is about 12 to 25% by weight. As long as the moisture content is within the above range,
Brown rice may be ground as is or water may be added. It is preferable to keep the moisture content of the brown rice at about 15 to 20 M% in particular so that the surface layer of the brown rice can be peeled off uniformly and the brown rice flour will not be crushed.

本発明では、上記のようにして表1部の一部を表面全体
にわたって剥離除去した玄米を、次に液状または超臨界
状態の二酸化炭素と接触さ也゛て処理する。
In the present invention, brown rice from which part of Table 1 has been peeled off over its entire surface as described above is then treated by contacting it with liquid or supercritical carbon dioxide.

本発明で使用する「液状または超臨界状態の二酸化炭素
」の内容を明確にするj;めに、以下に温度および圧力
と二酸化炭素の相状態との関係を第1図により説明する
In order to clarify the content of "liquid or supercritical carbon dioxide" used in the present invention, the relationship between temperature and pressure and the phase state of carbon dioxide will be explained below with reference to FIG.

二酸化炭素は、温度と圧力によって、第1図に示すよう
な固体状態、液体状態、超臨界状態および気体状態の各
相状態を呈する[ケミストリー・アンド・インダストリ
ー(Chemistry andIndusLry)第
19巻、第385−390頁(1982年7月)1゜第
1図中、TPは三重点であり、固体、液体および気体の
三相が共存する。また第1図中、CPは臨界点であり(
圧カフ2.8#9/ am”、温度31.1’C)、気
体、液体および超臨界状態の二酸化炭素が共存する。こ
の状態付近では、通常、気体状の一酸化炭素中に液状二
酸化炭素が微細な粒状状態で存在している。
Depending on the temperature and pressure, carbon dioxide exhibits various phase states such as a solid state, a liquid state, a supercritical state, and a gas state as shown in Fig. 1 [Chemistry and Industry (Chemistry and Industry) Vol. 19, No. 385 -Page 390 (July 1982) 1゜In Figure 1, TP is a triple point, and the three phases of solid, liquid, and gas coexist. Also, in Figure 1, CP is the critical point (
(pressure cuff 2.8 #9/am”, temperature 31.1'C), gas, liquid, and supercritical carbon dioxide coexist. Near this state, liquid carbon dioxide usually exists in gaseous carbon monoxide. Carbon exists in a fine granular state.

そして、本発明で使用する液状または超臨界状態の二酸
化炭素としては、第1図において斜線で示した部分から
なる液状または超臨界状態の二酸化炭素の内、温度が一
20〜+100°Cで、圧力が20&ζ/ c m ”
以上のものが好ましく、特に温度20−40°Oおよび
圧力100−400 k g/ c m ”のものが好
ましい。上記の−20〜++ o o ’cの温度およ
び20 k g/ c m ”以上の圧力の範囲内にあ
る液状または超臨界状態の二酸化炭素を使用すると、玄
米から脂質の一部が抽出されると共に糠臭等の異臭も除
去され、かつ玄米中に含まれる各種成分の変質、劣化等
が防止される。一方、二酸化炭素の温度が100℃より
高くなると、玄米中の澱粉、蛋白質、脂質、ミネラル、
ビタミン等が劣化したり変質したりして食感や栄養価等
の低下を招き望ましくない。また400kg/ cm”
より高い圧力の二酸化炭素を使用してもそれ以下の圧力
の二酸化炭素を使用する場合と比べてほぼ同程度の効果
が奏されるが、コストが高くなる。
The liquid or supercritical carbon dioxide used in the present invention includes liquid or supercritical carbon dioxide consisting of the shaded area in FIG. Pressure is 20&ζ/cm”
The above is preferred, and particularly preferred is the temperature of 20-40°O and the pressure of 100-400 kg/cm''. When using liquid or supercritical carbon dioxide within the pressure range of Deterioration etc. are prevented. On the other hand, when the temperature of carbon dioxide is higher than 100℃, the starch, protein, lipid, minerals in brown rice
It is undesirable that vitamins etc. deteriorate or change quality, resulting in a decrease in texture, nutritional value, etc. Also 400kg/cm”
Using carbon dioxide at a higher pressure has approximately the same effect as using carbon dioxide at a lower pressure, but at a higher cost.

液状または超臨界状態の二酸化炭素と玄米との接触は、
通常、約30分〜5時間かけて行うのがよい。処理時間
が約30分よりも短いと玄米からの脂質の抽出、糠臭等
の異臭の除去が不充分になる場合があり、逆に処理時間
が上記範囲よりも長いと脂質等の各成分の抽出や除去が
進み過ぎて栄養価や食感が低下する。その上、あまりに
も長い接触時間は処理コストの上昇をもたらす。
Contact between liquid or supercritical carbon dioxide and brown rice
Usually, it is best to do this for about 30 minutes to 5 hours. If the processing time is shorter than about 30 minutes, the extraction of lipids from brown rice and the removal of odor such as bran odor may be insufficient.On the other hand, if the processing time is longer than the above range, the extraction of lipids from brown rice and the removal of odor such as bran odor may be insufficient. Excessive extraction and removal will reduce nutritional value and texture. Moreover, too long a contact time results in increased processing costs.

本発明で玄米を液状または超臨界状態の二酸化炭素で処
理するにあたっては、玄米と二酸化炭素との接触が均一
にかつ円滑に行えるのであれば、いかなる方法および装
置も採用できる。
In the present invention, when brown rice is treated with carbon dioxide in a liquid or supercritical state, any method and apparatus can be employed as long as the brown rice and carbon dioxide can be brought into uniform and smooth contact.

かかる接触処理はバッチ法であっても連続法であっても
よい。
Such contact treatment may be a batch method or a continuous method.

以下に、本発明における液状または超臨界状態の二酸化
炭素による玄米の処理を、超臨界状態の二酸化炭素を使
用する場合を例にとって第2図により概略的にかつ例示
的に説明する。
Below, the treatment of brown rice with liquid or supercritical carbon dioxide in the present invention will be schematically and exemplified with reference to FIG. 2, taking as an example the case where supercritical carbon dioxide is used.

まず、ポンベl内に充填した液状二酸化炭素をポンプP
+によって加熱装置3を経て温水を流すことのできるジ
ャケット4aを備えた抽出槽4に圧送する。この際に二
酸化炭素の臨界点以上になるまでバルブcv−tを閉じ
ておくと抽出槽4の二酸化炭素は超臨界状態になる。
First, pump P
The mixture is fed under pressure via a heating device 3 to an extraction tank 4 equipped with a jacket 4a through which hot water can flow. At this time, if the valve cv-t is closed until the temperature exceeds the critical point of carbon dioxide, the carbon dioxide in the extraction tank 4 becomes supercritical.

抽出槽4内には表層部の一部を剥離除去した玄米をあら
かじめ充填しておき、ここで玄米と超臨界状態の二酸化
炭素との接触が行われる。
The extraction tank 4 is filled in advance with brown rice from which a portion of the surface layer has been peeled off, and here the brown rice is brought into contact with carbon dioxide in a supercritical state.

この際に加熱装置3の温度、ポンプP1およびバルブC
V−1により作動圧力を適宜調節することによって所望
の温度および圧力の超臨界状態二酸化炭素を形成するこ
とができる。抽出p14内で玄米を所定時間超臨界状態
の二酸化炭素と連続通気接触させ、バルブCV−1を開
いて玄米からの抽出物を含有する二酸化炭素をガス状で
分離槽5へと連続に導出させる。この際にバルブCV−
1の開き具合を適宜調節することによって抽出槽4内の
圧力を徐々に低下させることもまたはポンプP、の作動
圧力とバルブV、の開き具合を調節することによって急
激に低下させることもでき、本発明ではそのいずれもが
採用できる。
At this time, the temperature of heating device 3, pump P1 and valve C
Supercritical carbon dioxide at a desired temperature and pressure can be formed by appropriately adjusting the operating pressure using V-1. The brown rice is brought into continuous aeration contact with carbon dioxide in a supercritical state for a predetermined time in the extraction p14, and the valve CV-1 is opened to continuously lead out the carbon dioxide containing the extract from the brown rice to the separation tank 5 in gaseous form. . At this time, valve CV-
The pressure inside the extraction tank 4 can be gradually lowered by appropriately adjusting the opening of the pump P, or it can be lowered rapidly by adjusting the operating pressure of the pump P and the opening of the valve V. In the present invention, any of them can be adopted.

しかしながら圧力を徐々に低下させる方が加工玄米の外
観が損なわれず好ましい。玄米からの抽出物(脂質、臭
気物質、着色成分等)を含有する二酸化炭素から分離槽
5で該抽出物を分離する。抽出物を分離した後の二酸化
炭素はフィルター6を通して更に浄化した後、液化装置
7に導いて液化し、次いでポンプP1により加熱装置3
に再び導いて再度抽出槽4に循環させて玄米と接触させ
る。必要に応じて容器8内のエタノール等をポンプP2
によって抽出槽4に導入してエントレーナー処理を行う
However, it is preferable to gradually lower the pressure so that the appearance of processed brown rice is not impaired. A separation tank 5 separates the extract from brown rice from the carbon dioxide containing the extract (lipids, odorants, coloring components, etc.). The carbon dioxide after separating the extract is further purified through a filter 6, and then led to a liquefaction device 7 to be liquefied, and then transferred to a heating device 3 by a pump P1.
It is again guided to the extraction tank 4 and brought into contact with the brown rice. Pump P2 to pump ethanol, etc. in the container 8 as needed.
is introduced into the extraction tank 4 and subjected to entrainer treatment.

(発明の効果] y q−1!では玄米の表層部の一部を玄米の表面全体
、ニーpたって剥離除去した後に液状または超嶌界状!
7・二酸化炭素と接触させて加工玄米を製造して−・る
ので、該表層部の一部の剥離除去処理を何ら行わずにそ
のまま液状または超臨界状態の二酸化炭素に接触させた
場合に比べて、玄米からの脱脂、異臭物質等の除去がよ
り効率良くかつ均一に行われる。
(Effects of the invention) In yq-1!, a part of the surface layer of brown rice is removed by kneeling the whole surface of the brown rice, and then it becomes liquid or super-containing!
7. Processed brown rice is produced by contacting it with carbon dioxide, so compared to the case where the surface layer is brought into contact with liquid or supercritical carbon dioxide without any peeling and removal treatment. As a result, degreasing and removal of odor substances, etc. from brown rice are performed more efficiently and uniformly.

その結果、本発明により製造された加工玄米は吸水率が
高く、白米に使用されている調理器具を使用して白米と
同様の方法で簡単に炊飯でき、しかも炊き上がった玄米
板は糠臭等の異臭やパサつきがなく食感がよい。
As a result, the processed brown rice produced according to the present invention has a high water absorption rate, can be easily cooked in the same way as white rice using cooking utensils used for white rice, and the cooked brown rice plate does not have a bran odor. It has a good texture without any strange odor or dryness.

その上、本発明で製造された玄米は、脱脂率が高いこと
によって低カロリーであり、かつ脱脂率および脱臭率が
高いことによって長期間変質せずに貯蔵できる。
Furthermore, the brown rice produced according to the present invention has a high defatting rate, so it has low calories, and its high defatting rate and deodorizing rate allow it to be stored for a long period of time without deterioration.

更に、本発明では、過熱水蒸気を使用する従来技術にお
けるような高温処理を伴わないので、玄米中に含まれる
蛋白質、脂質、ビタミン、ミネラル等の栄養素の劣化、
胚乳部の変質や損傷等がなく栄養価が高くかつ食感の良
い玄米を製造することができる。
Furthermore, since the present invention does not involve high-temperature treatment unlike conventional techniques that use superheated steam, there is no deterioration of nutrients such as proteins, lipids, vitamins, and minerals contained in brown rice.
It is possible to produce brown rice with high nutritional value and good texture without deterioration or damage to the endosperm.

また、本発明では、従来技術におけるような玄米の圧偏
処理や形化処理を伴わないので、玄米の内部の損傷、崩
れ、空隙化等が生じず炊飯したときに外観の良い玄米板
が製造される。
In addition, the present invention does not involve pressurizing or shaping brown rice as in the prior art, so brown rice plates with a good appearance when cooked are produced without internal damage, collapse, or void formation in the brown rice. be done.

以下に図面を参照して実施例等によって本発明を具体的
に説明するが本発明はそれらの例によって限定されない
The present invention will be specifically explained below by examples and the like with reference to the drawings, but the present invention is not limited by these examples.

実施例1〜4および比較例1〜6 摩擦噴風式搗精機C3−25B(東洋精米機製作所層)
に玄米(水分台813重量%)を5に9/分の割合で供
給して搗精機ロールを100〜300m/分の周速度で
回転させて下記の表−1に示した歩留りになるように調
節しなから搗精を行って玄米の表層部を表面全体にわた
って均一に剥離除去した。
Examples 1 to 4 and Comparative Examples 1 to 6 Friction jet type rice miller C3-25B (Toyo Rice Mill Seisakusho layer)
Brown rice (moisture level: 813% by weight) was fed into the rice bowl at a rate of 5 to 9 minutes, and the milling machine roll was rotated at a circumferential speed of 100 to 300 m/minute to achieve the yield shown in Table 1 below. The surface layer of brown rice was peeled off uniformly over the entire surface by milling without adjustment.

次にこの表層部を一部剥離除去した玄米2000りを1
0Qの抽出槽4内に充填し、以下に述べる2方式での抽
出処理を行った。
Next, 2,000 liters of brown rice from which part of the surface layer has been peeled off is 1
It was filled into the 0Q extraction tank 4, and extracted using the two methods described below.

第1の方式は圧力58に9/cm2、温度20°Cの液
状二酸化炭素をポンプP1によってLOkg/hrで加
熱装置3に圧送して45°Cに加熱したのち、ジャケッ
ト4aに45°Cの温水を流した抽出槽4に導き、バル
ブCV−1を用いて抽出槽4内の圧力を200hg/c
m”(超臨界状態)に保持しつつ玄米と5時間連続通気
接触処理した。通気接触したさい脂質弁を含んだ圧力2
00Ja9/ cm”、温度45°Cの超臨界二酸化炭
素はバルブcv−iを調節して、ジャケラh5aに40
°Cの温水を流した分離槽5に導き、バルブcv−2を
調節して50kg/cm”に減圧した。
In the first method, liquid carbon dioxide at a pressure of 58/cm2 and a temperature of 20°C is pumped to the heating device 3 at LO kg/hr using a pump P1 and heated to 45°C. The hot water is led to the extraction tank 4, and the pressure inside the extraction tank 4 is set to 200 hg/c using the valve CV-1.
It was continuously aerated and contacted with brown rice for 5 hours while being maintained at a supercritical state. During the aerated contact, the pressure including the lipid valve was 2.
00Ja9/cm", supercritical carbon dioxide at a temperature of 45°C was added to Jakera h5a by adjusting the valve cv-i.
The mixture was introduced into a separation tank 5 in which hot water at a temperature of °C was flowed, and the pressure was reduced to 50 kg/cm'' by adjusting the valve CV-2.

分離槽5で玄米からの抽出物を分離した二酸化炭素はフ
ィルター6を通して浄化したのち液化装置7で液化して
温度5°C1圧力40kg7cm”の液状二酸化炭素を
液溜器2を介しポンプP、により加熱装置3に再循環し
た。液溜器2の液状二酸化炭素が不足したときは逐次ポ
ンベlから供給する(実施例1〜3)。
The carbon dioxide from which the extract from brown rice has been separated in the separation tank 5 is purified through a filter 6 and then liquefied in the liquefaction device 7, and the liquid carbon dioxide at a temperature of 5° C. and a pressure of 40 kg and 7 cm is passed through the liquid reservoir 2 and sent to the pump P. It was recirculated to the heating device 3. When the liquid carbon dioxide in the liquid reservoir 2 is insufficient, it is sequentially supplied from the pump 1 (Examples 1 to 3).

12の方式は58 k g/ c m ”、温度20°
Cの液状二酸化炭素をポンベlからポンプP、によって
10に9/hrで加熱装置3に送り出して25℃(液体
状a)に加熱したのち、ジャケット4aに25°Cの水
を流した抽出槽4に導き玄米と5時間連続通液接触処理
した。通液接触処理した際、脂質弁の含んだ液状二酸化
炭素はバルブCV−1を調節してジャケット5aに50
°Cの温水を流した分離槽5に噴射して液体の二酸化炭
素から気体の二酸化炭素に相変化させて脂質弁と気体状
二酸化炭素に分離した。バルブCV−2により501g
/cm”に調圧した気体状二酸化炭素はフィルター6を
通して浄化したのち液化装置7で液化して温度5°C1
圧力40に9/cm2の液状二酸化炭素を液溜器2を介
しポンプP、により加熱装置3に再循環した。
12 method is 58 kg/cm”, temperature 20°
The liquid carbon dioxide of C is sent from the pump l to the heating device 3 at a rate of 10 to 9/hr and heated to 25°C (liquid state a), and then water at 25°C is poured into the jacket 4a of the extraction tank. 4 and was subjected to continuous liquid flow contact treatment with brown rice for 5 hours. During the liquid contact treatment, the liquid carbon dioxide contained in the lipid valve is transferred to the jacket 5a by adjusting the valve CV-1.
The liquid carbon dioxide was injected into a separation tank 5 filled with warm water at 10°C to cause a phase change from liquid carbon dioxide to gaseous carbon dioxide, and the mixture was separated into a lipid valve and gaseous carbon dioxide. 501g with valve CV-2
The gaseous carbon dioxide whose pressure is regulated to 1/cm" is purified through a filter 6 and then liquefied in a liquefier 7 to a temperature of 5°C1.
Liquid carbon dioxide at a pressure of 40°/cm 2 was recycled via the reservoir 2 to the heating device 3 by means of a pump P.

液溜器2の液状二酸化炭素が不足したときは逐次ポンベ
Iから供給する(実施例4)。
When liquid carbon dioxide in the liquid reservoir 2 is insufficient, it is sequentially supplied from the pump I (Embodiment 4).

[吸水率の31定] 玄米10009を18°Cの水2000mQ中に浸して
30分毎にその100gを取り出してその吸水率を測定
しt二 。
[Water absorption constant 31] Brown rice 10009 was soaked in 2000 mQ of water at 18°C, 100 g of it was taken out every 30 minutes, and its water absorption rate was measured.

[玄米の炊飯方法] 玄米−合を水洗いしてから2時間水に浸した後水切りし
、水230ccを加えて日立家電製自動炊飯ジャーRZ
−480MTでそのまま炊飯した(炊飯時間20分)。
[How to cook brown rice] Wash brown rice, soak in water for 2 hours, drain, add 230cc of water, and use Hitachi Home Appliances automatic rice cooker RZ.
- Rice was cooked as is at 480MT (cooking time 20 minutes).

上記で得られた結果のうち、玄米の吸水率の経時変化に
ついては第3図に、玄米中の各成分の含有割合および食
感については下記の表−1に示す。
Among the results obtained above, the changes over time in the water absorption rate of brown rice are shown in Figure 3, and the content ratios and texture of each component in brown rice are shown in Table 1 below.

また、表層部の剥離除去処理および二酸化炭素処理を何
ら施してない玄米についても上記と同様にしてその吸水
率の経時変化、各成分の含有割合および炊飯したものの
食感を調べて、それらの結果を第3図および表−1に示
した(比較例1)。
In addition, for brown rice that had not undergone any peeling removal treatment on the surface layer or carbon dioxide treatment, we investigated the changes in water absorption over time, the content ratio of each component, and the texture of the cooked rice in the same manner as above, and examined the results. are shown in FIG. 3 and Table 1 (Comparative Example 1).

更jこ、上記実施例1〜3と同様にして表1部の剥離途
去処理を施しただけで二酸化炭素処理を行わない玄米に
ついてもその吸水率の、経時変化、各成分の含有割合お
よび炊飯米の食感を調べて、それらの結果を各々第3図
および表−1に示した(比較例2〜4)。
Similarly to Examples 1 to 3 above, for brown rice that was only subjected to the exfoliation treatment shown in Table 1 but not treated with carbon dioxide, changes in its water absorption rate over time, the content ratio of each component, and The texture of the cooked rice was examined and the results are shown in Figure 3 and Table 1 (Comparative Examples 2 to 4).

また、表層部の剥離除去処理を施さずに実施例1〜3と
同様に超臨界状態の二酸化炭素処理のみを施した玄米に
ついてもその吸水率、各成分の含有割合および炊飯米の
食感を上記と同様にして調べて、その結果を第3図およ
び表−1に示した(比較例5)。
In addition, the water absorption rate, the content ratio of each component, and the texture of cooked rice were also evaluated for brown rice that was subjected to only supercritical carbon dioxide treatment in the same manner as in Examples 1 to 3 without peeling and removing the surface layer. The test was conducted in the same manner as above, and the results are shown in FIG. 3 and Table 1 (Comparative Example 5).

また、表層部の剥離除去処理を施さずに実施例4と同様
に液状状態の二酸化炭素処理のみを施した玄米について
もその吸水率、各成分の含有割合および炊飯米の食感を
上記と同様にして調べて、その結果を第3図および表−
1に示した(比較例6)。
In addition, the water absorption rate, the content ratio of each component, and the texture of cooked rice were the same as above for brown rice that was subjected to only liquid carbon dioxide treatment in the same manner as in Example 4 without peeling and removing the surface layer. The results are shown in Figure 3 and Table -
1 (Comparative Example 6).

また、第3図において、I、n、IIIおよび■は各々
上記実施例1〜4で得られた玄米の吸水率の経時変化を
、モしてv−Xは各々上記比較例1〜6で得られた玄米
の吸水率の経時変化を示す 上記表=1および第3図の結果から、玄米表層部の一部
を表面全体にわたって剥離除去したのち液状または超臨
界状態の二酸化炭素で処理する本発明で製造された加工
玄米は、その一方の処理のみを施した玄米またはそのい
ずれの処理をも施さなかった玄米に比べて吸水率が大幅
に向上して通常の白米と同様に簡単に炊飯できるととも
に、炊飯したものは食感も大きく改良されていることが
わかる。しかも、本発明で製造された玄米は栄養価の点
でも、処理を施してない玄米に比べて何ら遜色がない。
In addition, in FIG. 3, I, n, III, and ■ represent the changes over time in the water absorption rate of the brown rice obtained in Examples 1 to 4, respectively, and v-X represents the changes over time in the water absorption rate of brown rice obtained in Examples 1 to 4, respectively. From the results shown in Table 1 and Figure 3 above, which show the changes in the water absorption rate of brown rice over time, it is clear that a part of the surface layer of brown rice is peeled off over the entire surface and then treated with liquid or supercritical carbon dioxide. The processed brown rice produced by the invention has significantly improved water absorption compared to brown rice that has undergone only one of the treatments or brown rice that has not undergone either of the treatments, and can be cooked as easily as regular white rice. It can also be seen that the texture of the cooked rice was greatly improved. Moreover, the brown rice produced according to the present invention is no inferior to untreated brown rice in terms of nutritional value.

【図面の簡単な説明】[Brief explanation of the drawing]

M1図は、二酸化炭素の圧力−温度とその相状態との関
係を示す図である。 第2図は、本発明の液状または超臨界状態の二酸化炭素
処理で使用される装置および工程の一実施態様を示す概
略図である。 第3図は、玄米の吸水率の経時変化を示すグラフである
。 第2図において、■は液状二酸化炭素を充填したボンベ
、2は液状二酸化炭素の液溜器、3は加熱装置、4は抽
出槽、4aは抽出槽のジャケット、5は分離槽、5aは
分離槽のジャケット、6はフィルター 7は液化装置、
8は溶剤タンク、P、およびP2はポンプ、CV−1お
よびCv−2は圧力調節バルブを示す。 第3図において、I〜■は本発明の実施例で得られた玄
米の吸水率の経時変化を、そしてV〜Xは比較例で得ら
れた玄米の吸水率の経時変化を示す。 第3図 ¥1図 温度(℃) 水中浸漬時間(分)
The M1 diagram is a diagram showing the relationship between pressure and temperature of carbon dioxide and its phase state. FIG. 2 is a schematic diagram showing one embodiment of the apparatus and process used in the liquid or supercritical carbon dioxide treatment of the present invention. FIG. 3 is a graph showing changes over time in the water absorption rate of brown rice. In Figure 2, ■ is a cylinder filled with liquid carbon dioxide, 2 is a liquid carbon dioxide reservoir, 3 is a heating device, 4 is an extraction tank, 4a is a jacket of the extraction tank, 5 is a separation tank, and 5a is a separation tank. Tank jacket, 6 is filter, 7 is liquefaction device,
8 is a solvent tank, P and P2 are pumps, and CV-1 and Cv-2 are pressure regulating valves. In FIG. 3, I to ■ indicate changes over time in the water absorption rate of brown rice obtained in the examples of the present invention, and V to X indicate changes over time in the water absorption rate of brown rice obtained in comparative examples. Figure 3¥1 Temperature (℃) Water immersion time (minutes)

Claims (1)

【特許請求の範囲】[Claims] 玄米の表層部の一部を玄米の表面全体にわたって剥離除
去した後、液状または超臨界状態の二酸化炭素に接触さ
せることを特徴とする加工玄米の製造法。
A method for producing processed brown rice, which comprises peeling and removing a portion of the surface layer of brown rice over the entire surface of the brown rice, and then contacting it with liquid or supercritical carbon dioxide.
JP63216320A 1988-09-01 1988-09-01 Manufacturing method of processed brown rice Expired - Fee Related JP2714405B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63216320A JP2714405B2 (en) 1988-09-01 1988-09-01 Manufacturing method of processed brown rice

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63216320A JP2714405B2 (en) 1988-09-01 1988-09-01 Manufacturing method of processed brown rice

Publications (2)

Publication Number Publication Date
JPH0269149A true JPH0269149A (en) 1990-03-08
JP2714405B2 JP2714405B2 (en) 1998-02-16

Family

ID=16686682

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2714405B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5700505A (en) * 1995-12-28 1997-12-23 Mei Research, Inc. Method of improving head rice yield
US8216628B2 (en) 2001-09-06 2012-07-10 Corn Products Development, Inc. Process for purifying starches

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5978656A (en) * 1982-10-26 1984-05-07 Nippon Sanso Kk Method for treating rice
JPS60133870A (en) * 1983-12-21 1985-07-17 Nippon Sanso Kk Production of japanese "sake"
JPS63173548A (en) * 1987-01-14 1988-07-18 Kinya Nakamura Processed unpolished rice

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5978656A (en) * 1982-10-26 1984-05-07 Nippon Sanso Kk Method for treating rice
JPS60133870A (en) * 1983-12-21 1985-07-17 Nippon Sanso Kk Production of japanese "sake"
JPS63173548A (en) * 1987-01-14 1988-07-18 Kinya Nakamura Processed unpolished rice

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5700505A (en) * 1995-12-28 1997-12-23 Mei Research, Inc. Method of improving head rice yield
US5845564A (en) * 1995-12-28 1998-12-08 Mei Research, Inc. Apparatus for improving head rice yield
US8216628B2 (en) 2001-09-06 2012-07-10 Corn Products Development, Inc. Process for purifying starches

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Publication number Publication date
JP2714405B2 (en) 1998-02-16

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