JPS59140871A - Treatment of raw material for brewing - Google Patents

Treatment of raw material for brewing

Info

Publication number
JPS59140871A
JPS59140871A JP58014011A JP1401183A JPS59140871A JP S59140871 A JPS59140871 A JP S59140871A JP 58014011 A JP58014011 A JP 58014011A JP 1401183 A JP1401183 A JP 1401183A JP S59140871 A JPS59140871 A JP S59140871A
Authority
JP
Japan
Prior art keywords
brewing
carbon dioxide
white rice
line
rice bran
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
JP58014011A
Other languages
Japanese (ja)
Other versions
JPH0314418B2 (en
Inventor
Nobuyoshi Ito
伊東 延義
Masayuki Taniguchi
正幸 谷口
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.)
Japan Oxygen Co Ltd
Nippon Sanso Corp
Original Assignee
Japan Oxygen Co Ltd
Nippon Sanso Corp
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 Japan Oxygen Co Ltd, Nippon Sanso Corp filed Critical Japan Oxygen Co Ltd
Priority to JP58014011A priority Critical patent/JPS59140871A/en
Publication of JPS59140871A publication Critical patent/JPS59140871A/en
Publication of JPH0314418B2 publication Critical patent/JPH0314418B2/ja
Granted legal-status Critical Current

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Abstract

PURPOSE:To enable the effective utilization of white bran as a raw material for brewing, by contacting the white bran produced by the polishing of brewing- grade rice with carbon dioxide of liquid state or supercritical state. CONSTITUTION:White bran produced by the polishing of rice for brewing is made to contact with carbon dioxide of liquid state or supercritical state at 0- 100 deg.C and 35-300kg/cm<2> pressure for several - several tens minutes to obtain a raw material for brewing.

Description

【発明の詳細な説明】 この発明はm造用原料を搗精する際に副生ずる白糠の処
理方法に係り、白糠を液状あるいは超臨界状態の炭酸ガ
スに接触せしめて白糠中の粗脂肪分等を除去し、この白
糠を醸造用原料に利用できるようにするものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for treating white rice bran, which is produced as a by-product when milling raw materials for manufacturing, by bringing the white rice bran into contact with carbon dioxide gas in a liquid or supercritical state to remove crude fat, etc. in the white rice bran. The purpose is to remove this white bran so that it can be used as a raw material for brewing.

清酒の製造にあっては、醸造用原料米を搗精して精白度
70〜75%の醸造用白米としたのち、この醸造用白米
を蒸さようし、製麹等の工程に送られる。ここで精白層
を70〜75%程麿まで搗精するのは、白米の表層部に
酒に異味、異臭を与える粗脂肪分が集中して存在してい
るためであり、醸造用白米としては粗脂肪分を極力含ま
ないことが望ましいためである。
In the production of sake, raw rice for brewing is milled to produce white rice for brewing with a polishing degree of 70 to 75%, and then this white rice for brewing is steamed and sent to processes such as koji making. The reason why the white rice layer is milled to about 70-75% is because there is a concentration of crude fat on the surface layer of the white rice that gives off-flavors and off-flavors to sake, and it is not suitable for use as white rice for brewing. This is because it is desirable to contain as little fat as possible.

ところが、上述9ように高度に搗精すれば、当然多量の
白糠が副生、する。この白糠には粗脂肪分が多く含まれ
ているので、従来は工業用糊の製造原料や、これに酵素
を加えて糖化し白糠糖化、液としたり、さらにアルコー
ル醗酵させて添加用アルコールとしたりしており、付加
価値の高い利用は行われておらず、酒造コストの上昇を
招いていた。
However, if the rice is milled to a high degree as described in 9 above, naturally a large amount of white rice bran will be produced as a by-product. Since this white rice bran contains a large amount of crude fat, it has traditionally been used as a raw material for manufacturing industrial glue, or by adding enzymes to saccharify it to form a liquid, or by fermenting it with alcohol to make alcohol for addition. Therefore, high value-added use was not carried out, leading to an increase in sake brewing costs.

特に、最近日本酒の高級化が進み、原料米を精白1ψ5
0%程度まで搗精したうえ醸造すること(吟醸酒)も多
くなってきており、白糠の有効な利用方法が切望されて
いる状況である。
In particular, with the recent advancement in the quality of Japanese sake, the raw rice has been polished to 1ψ5
It is becoming increasingly common for white rice bran to be refined to around 0% and then brewed (ginjo-shu), and there is a strong need for effective ways to use white bran.

この発明は上記事情に鑑みてなされたもので、従来低付
加価値の用途しかなかった白糠を付加価値の高い醸造用
原料として利用し得るようにした白糠の処理方法を提供
することを目的とするものである。
This invention was made in view of the above circumstances, and aims to provide a method for processing white rice bran, which allows white rice bran, which has conventionally only been used for low value-added purposes, to be used as a high-value-added raw material for brewing. It is something.

以下、この発明の詳細な説明する。The present invention will be explained in detail below.

この発明の白糠の処理方法は、白糠を液状または超臨界
状態の炭酸ガスに接触させるものである。
The method for treating white rice bran of this invention is to bring white rice bran into contact with carbon dioxide gas in a liquid or supercritical state.

まず、この発明に用いられる炭酸ガスの性状について説
明する。第1図は炭酸ガスの圧カ一温度@1ffl(P
T−ダイアグラム)P示すもので、炭酸ガスの温度、圧
力に応じた各状態(液体、固体、気体)が表示されてい
る。図中TPは、三重点で三相が共存する温度、圧力を
示し、CPは、臨界点で圧力(Pc)73.8バシル(
72,84%)、温度(’f c ) 31.06℃で
ある。この発明で用いられる炭酸ガスは、第1図中、斜
憧で示した範囲にあるもので、液状炭酸ガス、好ましく
はその温度での蒸気圧以上に加圧した炭酸ガス、および
超臨界状態の炭酸ガスである。ここで超臨界状態とは、
臨界点(CP)以上の圧力、温度の領域を指す0 そして、このような状態の炭酸ガスは、第2図に示すよ
うに極めて低粘度である。第2図のグラフは種々の圧力
下にある炭酸ガスおよび水の粘度の温度依存性を示した
ものであるが、液状および超臨界状態の炭酸ガスは水に
比較して1/1o〜1 / 401/J低粘度であり、
浸透性、溶解性に丁ぐ71ていることかわかる。
First, the properties of carbon dioxide gas used in this invention will be explained. Figure 1 shows the pressure temperature of carbon dioxide @1ffl (P
T-diagram) P shows each state (liquid, solid, gas) of carbon dioxide gas depending on its temperature and pressure. In the figure, TP indicates the temperature and pressure at which three phases coexist at the triple point, and CP indicates the pressure (Pc) at the critical point of 73.8 Basil (
72.84%) and temperature ('f c ) 31.06°C. The carbon dioxide gas used in this invention falls within the range indicated by the diagonal in Figure 1, and includes liquid carbon dioxide gas, preferably carbon dioxide gas pressurized above the vapor pressure at that temperature, and carbon dioxide gas in a supercritical state. It is carbon dioxide gas. Here, the supercritical state is
0 refers to a region of pressure and temperature above the critical point (CP). Carbon dioxide in such a state has an extremely low viscosity, as shown in FIG. The graph in Figure 2 shows the temperature dependence of the viscosity of carbon dioxide and water under various pressures, and the viscosity of carbon dioxide in liquid and supercritical states is 1/1 to 1/1 of that of water. 401/J low viscosity,
It can be seen that there is a difference in permeability and solubility.

次に、白糠について説明する。玄米をh4精すると1ま
ず肚芽と衣皮が除7J)2’して白米となり、この除虫
じる糠はその色力)ら赤糠と言わnる。よた、1m遣用
日米とするにに、この白米をざらに搗精して精白度を7
5シフ0%とする。こUJ搗搗精よって白米の粗脂肪分
を多く含む設層か削り取らn1顛迫に適した白米となる
。こり際、生じる糠は白色であり、白糠とぎわnる。し
たがって、白糠は粗脂肪分UJ多い粉状白木といえる。
Next, Shiranuka will be explained. When brown rice is milled, the buds and coat are removed to produce white rice, and this rice bran is called red rice bran because of its color. In order to use 1m of Japanese rice, this white rice is coarsely milled to a polishing degree of 7.
5 shift is 0%. This UJ combing rice has a high crude fat content, making it a white rice that is suitable for layered or shaved rice. The rice bran that is produced during roasting is white and is very white. Therefore, white bran can be said to be a powdery white wood with a high crude fat content UJ.

そして、この白糠を液状または超臨界状の炭酸ガスで処
理し、粗脂肪分寺を除去する。具不的に(ゴ、面す、耐
圧答dに白糠を所定敵収容する。次に上記状態の炭酸ガ
スi 7JI+えて洗浄処理する。この際の炭酸ガスU
J渦度は09100℃、圧力は65シロ00りと22”
Lる。外部から(1!芹等の外力を加える心安はないが
、必要に応じて静かに攪拌してもよく、ざらには炭改ガ
スを耐圧容器内に連続的に循#42!せて洗浄Tるよう
にしてもよく、また連続式で白糠を仇浄することもでさ
る。処理時間は数分〜数十分の範囲で用途等によって適
宜決めらnる。
This white rice bran is then treated with liquid or supercritical carbon dioxide gas to remove crude fat fractions. Concretely (go, face, pressure resistant answer d) contain a certain amount of white rice bran. Next, the carbon dioxide gas i 7JI + in the above state is cleaned. At this time, the carbon dioxide gas U
J vorticity is 09100°C, pressure is 65 siro 00 22"
L. Although it is not safe to apply external force such as external force (1! Seri), you may stir gently if necessary. Alternatively, the white rice bran can be purged continuously.The treatment time can be determined as appropriate depending on the use, etc., in the range of several minutes to several tens of minutes.

炭酸ガスUJ温度および圧力か高い程炭酸ガスの抽出H
し刀か増加し、抽出速度も速くなって好ましいカ、1M
1度が100”Cを越えると白糠のデンプンVJ変注が
始まり、好ましくなく、また圧力が600製を越えると
容器の耐圧性や作業(/J女金牲などlZJ点で不都合
となる。したかつて、通常は圧カフ0〜600υ、′t
IA度10−100’CI/J軸FIAで作業が行わn
る。
Carbon dioxide gas UJ The higher the temperature and pressure, the more carbon dioxide extraction H
Increased power and faster extraction speed, 1M
If the temperature exceeds 100"C, VJ conversion of white bran starch will begin, which is undesirable, and if the pressure exceeds 600"C, it will be inconvenient in terms of pressure resistance of the container and work (/J women's sacrifice, etc.). Previously, the pressure cuff was usually 0~600υ,'t
Work is done with IA degree 10-100'CI/J axis FIA n
Ru.

一定時間処理が行わnたのち、炭酸ガスが耐圧谷器力)
ら排出ざn、ついで耐圧容器内力圧力を常圧よで減じT
:後、白糠を取り出T。
After the treatment has been carried out for a certain period of time, the carbon dioxide gas will be released under pressure)
Then, reduce the internal pressure of the pressure vessel to normal pressure.
: After that, take out the white rice bran.

以上の処理によって、白糠中の粗脂肪分は勿−り事、臭
気成分等も炭酸ガスによって抽出ざn1炭ばガス中に移
行して除去ざrLる。:fた、精白度91%程度(/J
梢木状態でも上記処理方法により脱脂Tることもμ■龍
であるが、(特庫昭57−187B57号逐照)白糠を
扱うことによって、より迅速に月見側か可能となる。T
なわち、白糠は粉状であるので衣l槓が人さく、炭酸ガ
スによる粗脂肪分の抽出速度が高く、この結果高い抽出
効率(除去効率)が得られる。
By the above treatment, not only the crude fat in the white rice bran but also the odor components are extracted by the carbon dioxide gas and transferred to the charcoal bag gas for removal. :Fta, polishing level about 91% (/J
It is also possible to degrease even treetops using the above treatment method, but by treating white rice bran (Special Collection No. 57-187B57), it becomes possible to remove the oil more quickly from the moon viewing side. T
In other words, since white rice bran is in powder form, it is difficult to coat and mix, and the rate of extraction of crude fat by carbon dioxide gas is high, resulting in high extraction efficiency (removal efficiency).

このようにして処理された白糠は、粗脂肪分や興奥成分
が除去されており、実質的に高度精白米を粉砕したもの
と同一であり、醸造用白米として、充分に□使用できる
ものとなる。
The white rice bran processed in this way has the crude fat and oxidation components removed, and is essentially the same as pulverized highly polished rice, and can be fully used as white rice for brewing. Become.

また、吹酸ガスは、周知のように食品衛生上安全なもの
であり、全く無害であり、処理後の白糠中への残留肇考
慮する必要もない。
Furthermore, as is well known, blown acid gas is safe from a food hygiene perspective, is completely harmless, and there is no need to consider whether it remains in the white rice bran after treatment.

以下実施例を示して、この発明を具体的に説明する。The present invention will be specifically explained below with reference to Examples.

〔実施例〕 □精白度91%の白米(粗脂肪分0.5%)を精白度7
0%まで搗精し、この除虫じた白糠をサンプルとした。
[Example] □ White rice with a polishing degree of 91% (crude fat content 0.5%) was polished to a polishing degree of 7
The rice bran was milled to 0%, and this white rice bran was used as a sample.

このダンプル40gを濾紙製の袋に入し、袋ごと内容1
itt200m/!のオートフレニブ中に入れた。つい
で、炭酸ガス約130gをオートクレーブ中に導入し、
圧力100驚、温度40℃で20分間サンプルに接触せ
しめ、処理を行った。
Put 40g of this dumpling into a filter paper bag, and each bag contains 1
itt200m/! was placed in the autoflenib. Next, approximately 130 g of carbon dioxide gas was introduced into the autoclave.
The sample was treated by being brought into contact with the sample for 20 minutes at a pressure of 100 ampoules and a temperature of 40°C.

なお、処理中攪拌は行わなかった。炭酸ガス絡オ−トク
レーブから排出し、ついで白糠を取り出し、このものf
−試料として、エーテル抽出法により粗脂肪含量を求め
たところ、次の結果を得た。
Note that stirring was not performed during the treatment. Discharge from the carbon dioxide gas-fed autoclave, then take out the white rice bran, and
- When the crude fat content of the sample was determined by ether extraction method, the following results were obtained.

φ 本発明法によって処理した白糠 0.1  wt%
 4゜・ 未処理の白糠         1.36w
t%・ 精白麿70%の白米      0.13wt
%また、このようにして脱脂処理された白糠を醸造試験
に供したところ、臭気等の悪影響は何んら生じなかった
φ White rice bran treated by the method of the present invention 0.1 wt%
4゜・Untreated Shiranuka 1.36w
t%・70% white rice 0.13wt
% Also, when the white rice bran thus degreased was subjected to a brewing test, no adverse effects such as odor occurred.

以上説明したように、この発明の白糠の処理方法は、白
糠を液状または超臨界状態の炭酸ガスに接触させるもの
であるので、白糠中の粗脂肪分や臭気成分がほぼ完全に
除去される。したがって、処理された白糠は醸造用白米
の一種として付加価値の高い醸造用途に使用しえるよう
になり、醸造用白米の歩留りが大幅に向上する。また、
処理条件が温和であって、白糠中のデンプン等に変質を
来すこともない。さらに、炭酸ガスは食品衛生上全く無
害であり、この処理による食品衛生上の問題を招くこと
もない。また炭酸ガスは安価ηλ手できるとともに循環
して使用することにより、消費量が少なくて済み、処理
費用も安くて済むなどのすぐねた利点を有する。
As explained above, the method for treating white rice bran of the present invention involves bringing white rice bran into contact with liquid or supercritical carbon dioxide gas, so that the crude fat and odor components in white rice bran are almost completely removed. Therefore, the treated white rice bran can be used for high value-added brewing purposes as a type of white rice for brewing, and the yield of white rice for brewing can be greatly improved. Also,
The processing conditions are mild and do not cause any deterioration of the starch in the white rice bran. Furthermore, carbon dioxide gas is completely harmless in terms of food hygiene, and this treatment does not pose any food hygiene problems. Furthermore, carbon dioxide gas has the immediate advantage that it can be produced at a low cost, ηλ, and that it can be used in circulation, resulting in less consumption and lower processing costs.

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

第1図は炭酸ガスの圧力一温度線図、第2図は炭酸ガス
の粘度の温度依存性を示すグラフである。 第1図 −60−40−20020406080to。 ミ1゛幣(’C) 第2図 一一−チi’lt @ IoC1 手続補正書1発〕 58.3. 1 昭和   年   月   日 1、 事件の表示 昭和58 年特許願第14011号 2、発明の名称 醸造原料の処理方法 3、補正をする者 特許出願人 日本酸素株式会社 4、代理人 6、補正の内容 (1)特許請求の範囲r別紙の通り訂正する。 (2)  明則薔第1負@9汀目の「醸造用原料」を「
醸臘用原料米」に訂正する。 (3)  明1III舊第/頁@//行目、出3頁第1
行目、第3頁第2行目、第3貝第3行目、第3貞第t−
5行目、愚3頁第70行目、第3頁第1/行目、第3頁
第72行目、第3貝第l3行目、第3頁第1/行目、第
3jt第1を行目、@33頁第20目、第≠貞第12〜
13訂目、第3頁第75行目、第を負第76行目、第ダ
貞処/9行目、第3貝第3行目、第5貞第10行目、第
5貞第11行目、第3jt第15行目、第5貞第10付
目、第6貝第7行目、第6頁第77行目、第6頁第20
行目、第7貞第//σ目、第7貝第lざ行目、第7頁第
2Q行目、gざ頁第5行目および第δ貞第6行目の「炭
酸ガス」を「二酸化炭素」に訂正する。 (4)  明細書第/頁第16〜77行目の「送られる
。」を「送る。J&:訂正する。 (5)  明細lll第6弟第≠目の「英英成分」を「
臭気酸分」に訂正する。 2、特許請求の範囲 調造用原料米に搗精する際に生じる日砿七液状または鰯
臨界状鯨の二酸化炭當に接触させることン t−特徴とする醸造原料の処理方法。
FIG. 1 is a pressure-temperature diagram of carbon dioxide gas, and FIG. 2 is a graph showing the temperature dependence of the viscosity of carbon dioxide gas. Figure 1-60-40-20020406080to. Mi 1゛ ('C) Figure 2 11-chi'lt @ IoC1 Procedural Amendment 1] 58.3. 1 Month, day, 1939 1, Indication of the case, Patent Application No. 14011 of 1982, 2, Name of the invention, Process for processing brewing raw materials 3, Person making the amendment, Patent applicant Nippon Sanso Co., Ltd. 4, Agent 6, Contents of the amendment (1) Claims r amended as shown in the attached sheet. (2) “Brewing raw materials” of Akinorihara 1st negative @ 9th
Corrected to ``raw material rice for fermentation''. (3) Mei 1 III, No. 1/page @ // line, page 3, No. 1
line, 3rd page, 2nd line, 3rd shell, 3rd line, 3rd page t-
5th line, 3rd page, 70th line, 3rd page, 1st/line, 3rd page, 72nd line, 3rd shell, 3rd line, 3rd page, 1st/line, 3rd jt 1st Line 20, page 33, ≠ Tei 12~
13th edition, page 3, line 75, negative line 76, line 9, 3rd shell, 3rd line, 5th line 10, 5th line 11 Line, 3rd jt, line 15, 5th Tei, 10th annex, 6th shell, line 7, page 6, line 77, page 6, 20
"Carbon dioxide" in line 7, line 7 // σ, line 7, line 2, page 7, line 2Q, page 5, and line 6 of δ. Corrected to "carbon dioxide." (4) Change “Send.” from line 16 to page 77 of the specification to “Send. J&:”. (5) Change “English component” to “Send.
Corrected to ``smelly acid content.'' 2. Claims: A method for processing brewing raw materials, characterized in that the raw materials for brewing are brought into contact with Nippon Shichi liquid or Sardine carbon dioxide produced when milling raw rice for brewing.

Claims (1)

【特許請求の範囲】[Claims] 醸造用原料米を搗精する際に生じる白糠を液状または超
臨界状態の炭酸ガスに接触させることを特徴とする醸造
原料の処理方法。
A method for processing brewing raw materials characterized by bringing white bran produced when milling raw rice for brewing into contact with carbon dioxide gas in a liquid or supercritical state.
JP58014011A 1983-01-31 1983-01-31 Treatment of raw material for brewing Granted JPS59140871A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58014011A JPS59140871A (en) 1983-01-31 1983-01-31 Treatment of raw material for brewing

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58014011A JPS59140871A (en) 1983-01-31 1983-01-31 Treatment of raw material for brewing

Publications (2)

Publication Number Publication Date
JPS59140871A true JPS59140871A (en) 1984-08-13
JPH0314418B2 JPH0314418B2 (en) 1991-02-26

Family

ID=11849252

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58014011A Granted JPS59140871A (en) 1983-01-31 1983-01-31 Treatment of raw material for brewing

Country Status (1)

Country Link
JP (1) JPS59140871A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5251098A (en) * 1975-10-23 1977-04-23 Yokoyama Eng:Kk Method of making "sake"
JPS5516200A (en) * 1978-07-14 1980-02-04 Coal Industry Patents Ltd Device for mining
JPS5726585A (en) * 1980-06-10 1982-02-12 Studiengesellschaft Kohle Mbh Removal of bitter substance from used beer yeast

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5251098A (en) * 1975-10-23 1977-04-23 Yokoyama Eng:Kk Method of making "sake"
JPS5516200A (en) * 1978-07-14 1980-02-04 Coal Industry Patents Ltd Device for mining
JPS5726585A (en) * 1980-06-10 1982-02-12 Studiengesellschaft Kohle Mbh Removal of bitter substance from used beer yeast

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