JPS602181A - Preparation of raw sake - Google Patents

Preparation of raw sake

Info

Publication number
JPS602181A
JPS602181A JP58107764A JP10776483A JPS602181A JP S602181 A JPS602181 A JP S602181A JP 58107764 A JP58107764 A JP 58107764A JP 10776483 A JP10776483 A JP 10776483A JP S602181 A JPS602181 A JP S602181A
Authority
JP
Japan
Prior art keywords
sake
filtration
dextran
capillary
raw sake
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
JP58107764A
Other languages
Japanese (ja)
Inventor
Yasuo Uchida
内田 安雄
Takashi Miura
孝 三浦
Fumiaki Matsunaga
松永 文昭
Tetsuji Ishibashi
石橋 鉄治
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 Bakelite Co Ltd
Original Assignee
Sumitomo Bakelite 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 Bakelite Co Ltd filed Critical Sumitomo Bakelite Co Ltd
Priority to JP58107764A priority Critical patent/JPS602181A/en
Publication of JPS602181A publication Critical patent/JPS602181A/en
Pending legal-status Critical Current

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  • Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)

Abstract

PURPOSE:To obtain raw SAKE having superior quality of GENSHU (SAKE after brewing, not blended with other ingredients) of its own, distributable at normal temperature, less expensively, by filtering unheated ENSHU with a capillary polysulfone ultrafilter ultrafilter having specific properties. CONSTITUTION:A polysulfone resin having a repeating unit shown by the formula in the main chain of the molecule is dissolved in a solvent such as dimethylformamide, etc., made into a film by wet film forming process, etc., to prepare a capillary ultrafilter having 10-60wt% stopping ratio of dextran having 70,000mol.wt. and >=80wt% stopping ratio of dextran having 500,000mol.wt., 0.5-2m/m inner diameter and 0.1-1m/m thickness. A great number of the film are bundled, sealed with a resin at both end parts to prepare an inner-pressure filtration module, and unheated GENSHU is filtered with the module, to give the desired raw SAKE distributable at normal temperature.

Description

【発明の詳細な説明】 本発明は常温流通可能な生酒の製造方法に関するもので
ある。ここで生酒とはその製造工程において殺菌および
醗酵停止を目的とした火入れ処理を全く行わない清酒を
指すものである。清酒は一般にその製造工程において原
酒の火入れ処理を行うが、その処理中に蛋白混濁母物質
が会合し、いわゆる白はけと称する混濁物質を生ずる。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing raw sake that can be distributed at room temperature. Namazake here refers to sake that is not pasteurized at all in the manufacturing process for the purpose of sterilization and termination of fermentation. During the manufacturing process of sake, the raw sake is generally pasteurized, but during this process, protein turbid substances come together, producing a turbid substance called white flake.

この白ぼけを除く為おシ下げ処理を行うが、限外濾過法
により除菌と共に蛋白混濁母物質を除去することができ
れば、原酒のもつ独特な風味を保持した生酒を製造する
ことが可能である。本発明者らはかかる目的のため鋭意
検討を行い、本発明を為すに至ったものである。清酒の
限外濾過処理については既にいくつかの検討が為されて
いる。例えば、生酒の濾過においてはある種の膜では白
ぼけ防止効果が認められず、膜種によっては清酒を変質
する可能性の見られるものもあるが(例えば佐藤他、醗
酵工学、第55巻、84〜94頁、1977年)、白は
けを防止する効果のある安定な膜も見出されでいる( 
0hba、T、 etal、 J、 Brew、 So
c、 Japan、 Vo173、p951〜954.
1978)。しかし今日に至るも実際に限外濾過を用い
て常温流通可能な生酒を製造している例は報告されてい
ない。
In order to remove this whitishness, a process is performed, but if the ultrafiltration method can be used to sterilize and remove protein-turbid substances, it is possible to produce raw sake that retains the unique flavor of the original sake. be. The inventors of the present invention have conducted extensive studies for this purpose and have come up with the present invention. Several studies have already been carried out regarding ultrafiltration treatment of sake. For example, in the filtration of raw sake, certain types of membranes do not have the effect of preventing whitening, and some membrane types have the potential to alter the quality of sake (for example, Sato et al., Fermentation Engineering, Vol. 55, 84-94, 1977), and a stable film that is effective in preventing white flaking has also been discovered (
0hba, T, etal, J, Brew, So
c, Japan, Vo173, p951-954.
1978). However, to date, there have been no reports of actual use of ultrafiltration to produce raw sake that can be distributed at room temperature.

本発明者らはp遅効率が高く、扱いやすい膜であればか
かる目的のために実用的に使用され得るものと思料し、
ポリスルホン樹脂を用いてキャピラリー状分離膜を作成
し、生酒濾過の検討を行った。キャピラリー状の濾過膜
は 1)′クロスフロー濾過が行えること、2)液流速を高
くするととが出来るので膜面へのスケールの堆積を防げ
ること、 3)滞流部が少ないため洗浄が簡単であシ、原酒への影
響を極力おさえることができること、4)膜の充填密度
が高いため装置のイニシアルコストが低いこと などの利点が認められており、実用的には最も扱いやす
い濾過膜である。キャピラリー状濾過膜においてその内
径は小さい程充填密度は大きくなるが、圧力損失が大き
くなシ、沢過効率が低下する。
The present inventors believe that a membrane that has a high p-retardation efficiency and is easy to handle can be practically used for such purposes,
A capillary-like separation membrane was created using polysulfone resin, and the filtration of raw sake was investigated. Capillary-shaped filtration membranes 1) can perform cross-flow filtration, 2) increase the liquid flow rate to prevent scale build-up on the membrane surface, and 3) are easy to clean because there are few stagnant parts. It has been recognized that it has advantages such as being able to minimize the impact on the reeds and unprocessed sake, and 4) lowering the initial cost of the device due to the high packing density of the membrane, making it the easiest filtration membrane to handle in practice. . In a capillary-like filtration membrane, the smaller the inner diameter, the higher the packing density, but the greater the pressure loss and the lower the filtration efficiency.

又内径が大きければ圧力損失は小さくなるが、膜の耐圧
強度が減少し、又一定流速を保持するだめのポンプの負
荷が増大する。又−の分画分子量は小さければ混濁母物
質の阻止は完全になるが、ν過動率を下げると共に生酒
の風味、香味に悪影響を及はし、大きければ混濁母物質
の阻止が不完全になる。これらの諸条件の最もバランス
のとれたキャピラリー状濾過膜を得るべく検討し、本発
明者らは、分子量7QOOOのデキストランの阻止率が
10チ以上60チ以下、望ましくは251%以上35q
6以下でメジ、分子量が50QOOOのデキストランの
阻止率が80%以上、望ましくは90%であるとともに
、内径0.5〜2%、肉厚0,1〜1.0%、望ましく
は内径1.0%、肉厚0.3%であるキャピラリー状ポ
リサルホン濾過膜によシ火入れを行わない原酒を濾過す
れば、常温流通可能人生酒を製造し得ることを見出した
。尚ここでデキストランは多糖類の一種であシ、分子量
70. OOOおよU: 50QOOOのものとしてそ
れぞれファルマシア社のT−70およびT−500を用
いた。又阻止率の測定はデキストランの0.5 %水溶
液を0.6 kr/cf7Nの濾過圧で濾過し、次の式
よシ算出した。
Moreover, if the inner diameter is large, the pressure loss will be small, but the pressure resistance of the membrane will be reduced, and the load on the pump to maintain a constant flow rate will be increased. In addition, if the molecular weight fraction is small, the inhibition of cloudy matrix substances will be complete, but it will lower the ν hypermobility and have a negative effect on the flavor and aroma of raw sake, and if it is large, the inhibition of cloudy matrix substances will be incomplete. Become. In order to obtain a capillary-like filtration membrane with the best balance of these conditions, the present inventors have determined that the rejection rate of dextran having a molecular weight of 7 QOOO is 10 to 60 Q, preferably 251% to 35 Q.
6 or less, the rejection rate of dextran having a molecular weight of 50QOOO is 80% or more, preferably 90%, and the inner diameter is 0.5 to 2%, the wall thickness is 0.1 to 1.0%, and preferably the inner diameter is 1. We have discovered that by filtering raw sake that has not been pasteurized through a capillary polysulfone filtration membrane with a thickness of 0.0% and a wall thickness of 0.3%, it is possible to produce raw sake that can be distributed at room temperature. Note that dextran is a type of polysaccharide and has a molecular weight of 70. OOO and U: Pharmacia's T-70 and T-500 were used as 50QOOO, respectively. The rejection rate was measured by filtering a 0.5% aqueous solution of dextran at a filtration pressure of 0.6 kr/cf7N and calculating it using the following formula.

Ci ここでRは阻止率@)、CiおよびCpはそれぞれ原液
および濾過液のデキストラン濃度である。又ポリサルホ
ン樹脂は分子主鎖中の繰シ返し単位になる構造を含むも
ので、以下の説明ではUCC社製のUDEL P 17
00を用いたが、これに限られない。
Ci where R is the rejection rate @), Ci and Cp are the dextran concentrations of the stock solution and filtrate, respectively. In addition, polysulfone resin contains a structure that becomes a repeating unit in the main chain of the molecule, and in the following explanation, UDEL P 17 manufactured by UCC Co., Ltd.
00 is used, but it is not limited to this.

以下実施例について本発明を説明する。The present invention will be explained below with reference to Examples.

通常の湿式製膜法によシ、第1表に示した形状およびデ
キストラン阻止率を有するキャピラリー状濾過膜を製膜
し、これにより膜面積2.5 d、実効長100 cm
を有するモジュールを作成し、内圧濾過によシ火入れ前
の原酒を濾過したものであ−る。
A capillary-like filtration membrane having the shape and dextran rejection rate shown in Table 1 was formed by a normal wet membrane forming method, and the membrane area was 2.5 d and the effective length was 100 cm.
A module with this was created, and the unprocessed sake before pasteurization was filtered through internal pressure filtration.

濾過速度は入口圧3 kv / ad 、原酒流速1.
5 m/secの濾過条件で濃縮倍率20倍迄濃縮濾過
した時の平均濾過速度を示した。流通テストは盛夏時普
通トラックによシ東京−大阪間を往復運送した時の白は
け発生を観察したものである。又保存テストは20℃以
上の環境に18ケ月保存した時の白ぼけの発生を観察し
たものである。
The filtration rate is inlet pressure 3 kv/ad, unprocessed sake flow rate 1.
The average filtration speed is shown when concentration filtration is performed up to a concentration ratio of 20 times under the filtration condition of 5 m/sec. The distribution test was conducted by observing the appearance of white flakes when the product was transported back and forth between Tokyo and Osaka in a regular truck during the height of summer. In addition, the storage test was to observe the occurrence of white blur when stored in an environment of 20° C. or higher for 18 months.

本発明の実施例である実験例6及び7では、流通テスト
、保存テストで白ぼけの発生は無く、又濾過時の運転性
、作業性も良好であった。T−70阻止率が40%、T
−500の阻止率が95係である実験例1〜3では各テ
ストに於ける白はけの発生は認められなかったが、内径
又は肉厚が本発明の範囲外であるため、濾過時の運転性
、作業性等に劣るものであった。又実験例4〜5では流
通テスト又は保存テストにおいて白ぼけの発生がみられ
、本発明の目的を達することができなかった。
In Experimental Examples 6 and 7, which are examples of the present invention, there was no occurrence of white blur in distribution tests and storage tests, and the operability and workability during filtration were also good. T-70 blocking rate is 40%, T
In Experimental Examples 1 to 3, in which the rejection rate of -500 was 95, no white flaking was observed in each test, but since the inner diameter or wall thickness was outside the scope of the present invention, The drivability, workability, etc. were poor. Further, in Experimental Examples 4 and 5, white blurring was observed in the distribution test or the storage test, and the object of the present invention could not be achieved.

手続補正書(自発) 昭和58年 9月 1日′ 特許庁長官殿 1、事件の表示 昭和58年特許願第107764号 2、発明の名称 生酒の製造方法 3、補正をする者 事件との関係 特許出願人 住 所 東京都千代田区内幸町1丁目2番2号4、補正
の対象 明細書全文。
Procedural amendment (voluntary) September 1, 1980' Commissioner of the Japan Patent Office1, Indication of the case, 1982 Patent Application No. 1077642, Name of the invention, Process for producing raw sake3, Person making the amendment, Relationship with the case Patent applicant address: 1-2-2-4 Uchisaiwai-cho, Chiyoda-ku, Tokyo. Full text of the specification subject to amendment.

明 細 書 1、発明の名称 生酒の製造方法 2、特許請求の範囲 分子量7QOOOデキストランの阻止率が10多以上6
0チ以下であシ、分子量50QOOOのデキストランの
阻止率が80q6以上であり、内径0.5〜2.0%、
肉厚0.1〜1.0%である支持体を有しないキャピラ
リー状ポリサルホン限外濾過膜によシ火入れを行わない
原酒を流過するととを特徴とする常温流通可能な生酒の
製造方法 3、発明の詳細な説明 本発明は、常温流通可能な生酒の製造方法に関するもの
である。ζこで生酒とは、その出荷に至る迄の製造工程
において、殺菌および醗酵停止を目的とした熱処理を全
く行わない清酒を指すものである。清酒はその製造工程
において熟成醗酵して得たもろみを上槽濾過して生酒を
得るが、この生酒は独特の芳淳な香シを有し、優れた酒
質をもつものである。しかし混在するこうじ菌、混入す
る火落菌等のため極めて変質しやすく、酒質が損われや
すい。このためそのすぐれた酒質にも拘らず生酒は通常
の流通経路によシ消費者に供給することは出来ず、わず
かに低温に保持することによシ極めて限られた地域にお
いてのみ短期間の供給が可能であった。本発明の目的は
かかる微妙な生酒を常温において常時流通7せしめ、広
く市場に提供できる様な生酒の製造方法を発明すること
である。
Description 1, Title of the invention: Method for producing raw sake 2, Claims: Molecular weight 7: Rejection rate of QOOO dextran is 10 or more 6
0% or less, the rejection rate of dextran with a molecular weight of 50QOOO is 80q6 or more, and the inner diameter is 0.5 to 2.0%.
Method 3 for producing unpasteurized sake that can be distributed at room temperature, characterized by passing raw sake that is not pasteurized through a capillary-shaped polysulfone ultrafiltration membrane without a support and having a wall thickness of 0.1 to 1.0%. DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing raw sake that can be distributed at room temperature. ζ Here, raw sake refers to sake that is not subjected to any heat treatment for the purpose of sterilization and termination of fermentation during the manufacturing process up to shipment. In the manufacturing process of sake, the mash obtained through aging and fermentation is filtered through an upper tank to obtain raw sake, which has a unique aromatic aroma and is of excellent quality. However, due to the presence of koji bacteria and hiochi bacteria, it is extremely susceptible to deterioration and the quality of sake is likely to be impaired. For this reason, despite its excellent quality, raw sake cannot be supplied to consumers through normal distribution channels, and by keeping it at a slightly low temperature, it can only be used for a short period of time in extremely limited areas. supply was possible. The purpose of the present invention is to invent a method for producing Namazake that allows such delicate Namazake to be constantly distributed at room temperature and to be widely available on the market.

従来清酒はオリ引きと称する沈澱処理を行い、活性炭を
加えて一次濾過を行った後、殺菌を目的とした火入れ処
理を行うものである。火入れ処理を行うことによシ、醗
酵停止と共に火落菌の殺菌が行われ酒質が安定するが、
同時に生酒のもつ芳淳な香シは失われてしまう。火入れ
処理を行った原酒はゼラチン、柿渋などのオリ下げ剤を
加えて濾過し、会合性蛋白によるいわゆる白ボケを防止
し、更に必要な処理を加え、出荷時に更に加熱殺菌を行
って製品となるものである。この様な清酒製造の従来法
において生酒の芳香が火入工程において失われることは
明白であシ、芳香を保持するために火入工程を省略すれ
ば、火落菌による変質を招くことは従来の経験から明ら
かである。本発明者らは近年急速な展開を見ている限外
濾過法を清酒製造工程に採用することにより、芳香を保
持し、且つ変質を招かない生酒を製造し得るものと思料
した。清酒の限外流過については既にいくつかの検討が
為されているが、これらの検討では蛋白系混濁物質に由
来する白はけの防止効果に重点をおき、膜種によっては
防止効果のあることも報告されている。しかし火落菌に
よる生酒の変質については何れも検討が、されず、濾過
された生酒中に火落菌が存在しないことは確認されてい
ない。
Traditionally, sake undergoes a sedimentation process called orihiki, and after primary filtration with the addition of activated carbon, it undergoes a pasteurization process for the purpose of sterilization. Pasteurization stops fermentation and sterilizes hiochi bacteria, stabilizing the quality of sake.
At the same time, the rich aroma of raw sake is lost. After pasteurization, the unprocessed sake is filtered by adding gelatin and persimmon juice to prevent so-called white blur caused by associative proteins, and then subjected to the necessary treatments, and further heated and sterilized before shipping to become a product. It is something. In this conventional method of producing sake, it is obvious that the aroma of raw sake is lost during the pasteurization process, and if the pasteurization process is omitted to preserve the aroma, it is unlikely that deterioration due to hiochi bacteria will occur. It is clear from experience. The present inventors thought that by adopting the ultrafiltration method, which has seen rapid development in recent years, to the sake manufacturing process, it would be possible to produce raw sake that retains its aroma and does not cause deterioration. Several studies have already been conducted on ultra-flow filtration of sake, but these studies have focused on the prevention effect of white flakes caused by protein-based turbid substances, and it has been found that some film types have a prevention effect. has also been reported. However, no studies have been conducted on the deterioration of raw sake caused by Hiotoshi bacteria, and the absence of Hiotchi bacteria in filtered Namazake has not been confirmed.

又白埋は防止効果についても明確に膜種の限定は為され
ておらず、実際にかかる方法を用いて実用化を行った例
も報告されていない。
In addition, there are no clear restrictions on film types with regard to the effect of preventing white embedding, and there have been no reports of practical use of such a method.

本発明者らは流過効率が高く、扱いやすい膜であればか
かる目的のために実用的に使用され得るものと思料し、
ポリスルホン樹脂を用いてキャピラリー状分離膜を作成
し、生酒濾過の検討を行った。ポリサルホン樹脂膜は耐
薬品性が良好であり、実際に生酒中へ浸漬しても生酒へ
異臭、薬品臭などの変化を与えないことを確認したもの
である。
The present inventors believe that a membrane with high flow efficiency and easy handling can be practically used for such purposes,
A capillary-like separation membrane was created using polysulfone resin, and the filtration of raw sake was investigated. The polysulfone resin film has good chemical resistance, and it has been confirmed that even when actually immersed in raw sake, it does not impart any off-odor or chemical odor to the raw sake.

キャピラリー状の濾過膜は、 1)クロスフロー濾過が行えること、 2)液流速を高くすることが出来るので膜面へのスケ−
ルの堆積を防げること、 3)滞流部が少ないため洗浄が簡単であシ、原酒への影
響を極力おさえることができること、4)膜の充填密度
が高いため装置のイニシアルコストが低いこと などの利点が認められておシ、実用的には最も扱いやす
い濾過膜である。キャピラリー状濾過膜においてその内
径は小さい程充填密度は大きくなるが、圧力損失が大き
くなシ、濾過効率が低下する。
Capillary-shaped filtration membranes have the following advantages: 1) cross-flow filtration is possible, and 2) the liquid flow rate can be increased, so there is less scalability on the membrane surface.
3) It is easy to clean because there are few stagnation parts, and the influence on the raw beer can be minimized. 4) The initial cost of the equipment is low because the membrane is packed densely. It is recognized for its advantages and is the easiest filtration membrane to use in practice. In a capillary-like filtration membrane, the smaller the inner diameter, the higher the packing density, but the greater the pressure loss, the lower the filtration efficiency.

又内径が大きければ圧力損失は小さくなるが、膜の耐圧
強度が減少し、又一定流速を保持するためのポンプの負
荷が増大する。
Moreover, if the inner diameter is large, the pressure loss is reduced, but the pressure resistance of the membrane is reduced and the load on the pump for maintaining a constant flow rate is increased.

本発明者らはこれらの点を勘案し、各種形状のポリサル
ホンキャピラリー状膜を作成し試験を行ったが、内径0
.5〜2%、肉厚o、 i〜1.0%、望ましくは内径
1%、肉厚0.3%の形状のものが最も効率的であるこ
とを見出した。又膜の分画分子量については、大きすぎ
れば混濁母物質および菌類の阻止が不完全となり、小さ
すぎれば生酒の風味、香味に悪影響を及ばずことが分り
、本発明者らはこれらの諸條件の最もバランスのとれた
キャピラリー状濾過膜を得るべく検討を行い、分子量7
QOOOのデキストランの阻止率が10チ以上60チ以
下、望ましくは25%以上35チ以下であシ、分子量が
500,000のデキストランの阻止率が80−以上、
望ましくは90%以上であるキャピラリー状ポリサルホ
ン濾過膜によシ火入れを行わない原酒を濾過すれば、常
温流通可能な生酒を製造し得ることを見出した。尚ここ
でデキストランは多糖類の一種であり、分子量70.0
00および500.000のものとしてそれぞれファル
マシア社のT−70およびT−500を用いた。又阻止
率の測定はデキストランの0.5チ水溶液を0.6に7
/iの濾過圧で濾過し、次の式よシ算出した。
Taking these points into consideration, the inventors created and tested polysulfone capillary-like membranes of various shapes.
.. It has been found that a shape with an inner diameter of 1% and a wall thickness of 0.3% is most efficient. Regarding the molecular weight cutoff of the membrane, it has been found that if it is too large, the inhibition of turbid substances and fungi will be incomplete, and if it is too small, it will not have a negative effect on the flavor and aroma of raw sake, and the present inventors have determined that these conditions We conducted studies to obtain the most balanced capillary-like filtration membrane with a molecular weight of 7.
The rejection rate of QOOO dextran is 10% or more and 60% or less, preferably 25% or more and 35% or less, and the rejection rate of dextran with a molecular weight of 500,000 is 80% or more,
It has been found that by filtering raw sake that is not pasteurized through a capillary polysulfone filtration membrane, which preferably has a content of 90% or more, it is possible to produce raw sake that can be distributed at room temperature. Note that dextran is a type of polysaccharide and has a molecular weight of 70.0.
Pharmacia's T-70 and T-500 were used as 00 and 500.000, respectively. In addition, the rejection rate was measured by adding a 0.5% aqueous solution of dextran to 0.6%.
It was filtered at a filtration pressure of /i, and calculated according to the following formula.

Ci ここでRは阻止率@)、CiおよびCpはそれぞれ原液
および濾過液のデキスト270度である。又ポリサルホ
ン樹脂は分子主鎖中の繰り返し単位になる構造を含むも
ので、以下の説明ではUCC社製のUDELP 170
0を用いたが、これに限られない。
Ci where R is the rejection rate @), Ci and Cp are the dextrin 270 degrees of the stock solution and filtrate, respectively. In addition, polysulfone resin contains a structure that becomes a repeating unit in the main chain of the molecule, and in the following explanation, UDELP 170 manufactured by UCC Co., Ltd.
Although 0 is used, it is not limited to this.

以下実施例について本発明を説明する。The present invention will be explained below with reference to Examples.

実施例I UDELP 1700をジメチルホルムアミドに14%
重量パーセントの濃度に溶解し、この溶液を製膜原液と
して二重構造ノズルを用いて所定温度において湿式製膜
法によシ、内径1.0%、肉厚0.3%+のキャピラリ
ー状分離膜を製膜した。この膜を100本束ね、両端部
を樹脂で封止し、長さ50crrLの内圧式濾過モジュ
ールを作成した。このモジュールを用いてデキストラン
T−70およびT−500の阻止率を測定したところ、
それぞれ32チおよび95チであった。このモジュール
を用い、火入れを行わない生酒の濾過を行った。濾過條
件は温度10〜15℃、平均濾過圧4.5 k7 / 
cat テあシ、濾過速度は45t/イ・hrであった
。沢過して得た濾過池について生菌培養試験を行ったと
ころ、生菌数は0であシ、火落菌その他の生菌は認めら
れなかった。生酒および濾過池の分析テスト結果を第1
表に示す。酒質の変化は認められない。
Example I UDELP 1700 14% in dimethylformamide
The solution was dissolved in a concentration of 1.0% by weight, and this solution was used as a film-forming stock solution at a predetermined temperature using a double-structure nozzle for wet film-forming. A membrane was formed. 100 of these membranes were bundled and both ends were sealed with resin to create an internal pressure filtration module with a length of 50 crrL. When the rejection rate of dextran T-70 and T-500 was measured using this module,
They were 32 and 95 inches, respectively. This module was used to filter raw sake without pasteurization. Filtration conditions are temperature 10-15℃, average filtration pressure 4.5k7/
The filtration rate was 45 t/hr. When a viable bacteria culture test was conducted on the filtration pond obtained by filtration, the number of viable bacteria was 0, and no other viable bacteria such as Hiobacterium was observed. First analysis of raw sake and filtration pond analysis test results
Shown in the table. No change in alcohol quality was observed.

又パネルによる官能テストの結果も、濾過池は生酒の芳
香を保持しておシ良好な結果を得た。濾過池を消毒した
ガラスびんに詰め、20〜25℃の温度に12チ月間、
25〜32℃の温度に6ケ月間保存したが、酒質の変化
、混濁物の発生、テリの変化は見られなかった。又濾過
池を夏季通常トラックによシ東京−大阪間を往復し輸送
したが、何らの影響も見られなかった。又濾過池のさえ
は良好であった。
In addition, the results of a sensory test conducted by a panel showed that the filtration pond retained the aroma of raw sake, giving good results. Pack the filter into a sterilized glass bottle and keep it at a temperature of 20-25℃ for 12 months.
Although it was stored at a temperature of 25 to 32°C for 6 months, no change in alcohol quality, generation of turbidity, or change in texture was observed. In addition, the filtration pond was transported back and forth between Tokyo and Osaka by regular truck during the summer, but no adverse effects were observed. Also, the condition of the filtration basin was good.

第1表 分析結果 実施例2 実施例1と同様の操作によシ、製膜温度をかえて同一の
形状の分離膜を作成した。同一の手順によシこれをモジ
ュール化し、デキストランT−70およびT−500の
阻止率を測定したところ、それぞれ26チおよび85チ
であった。実施例1と同じ生酒を同−條件で濾過し、濾
過池を得た。濾過速度は52 t/d・hrであった。
Table 1 Analysis Results Example 2 Separation membranes of the same shape were produced by the same operations as in Example 1, but with different membrane forming temperatures. This was made into a module using the same procedure, and the inhibition rates of dextran T-70 and T-500 were measured to be 26 and 85, respectively. The same raw sake as in Example 1 was filtered under the same conditions to obtain a filter basin. The filtration rate was 52 t/d·hr.

この様にして得た濾過池(アルコール濃度20.4度)
を同じモジュールで濾過した用水を加えアルコール濃度
15.7度に希釈した。この様にして得た濾過池につい
て培養検査を行い生菌数を調べたが、生菌数は0であっ
た。又実施例1と同じく保存試験および流通試験を行っ
たが、何等異常は見られなかった。
Filtration pond obtained in this way (alcohol concentration 20.4 degrees)
was diluted to an alcohol concentration of 15.7 degrees by adding water filtered through the same module. The filter pond thus obtained was subjected to a culture test to determine the number of viable bacteria, but the number of viable bacteria was 0. In addition, a storage test and a distribution test were conducted in the same manner as in Example 1, but no abnormalities were observed.

Claims (1)

【特許請求の範囲】[Claims] 分子17QOOOデキストランの阻止率が10−以上6
0%以下であシ、分子量500,000のデキストラン
の阻止率が80%以上であり、内径0.5〜2.0′%
、肉厚01〜10%である支持体を有しないキャピラリ
ー状ポリサルホン限外沖過膜によシ火入れを行わない原
酒を濾過することを特徴とする常温流通可能な生酒の製
造方法
The inhibition rate of molecule 17QOOO dextran is 10- or more6
0% or less, the rejection rate of dextran with a molecular weight of 500,000 is 80% or more, and the inner diameter is 0.5 to 2.0%.
, a method for producing unpasteurized sake that can be distributed at room temperature, characterized by filtering raw sake that is not pasteurized through a capillary-shaped polysulfone ultrafiltration membrane without a support and having a wall thickness of 01 to 10%.
JP58107764A 1983-06-17 1983-06-17 Preparation of raw sake Pending JPS602181A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58107764A JPS602181A (en) 1983-06-17 1983-06-17 Preparation of raw sake

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58107764A JPS602181A (en) 1983-06-17 1983-06-17 Preparation of raw sake

Publications (1)

Publication Number Publication Date
JPS602181A true JPS602181A (en) 1985-01-08

Family

ID=14467399

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58107764A Pending JPS602181A (en) 1983-06-17 1983-06-17 Preparation of raw sake

Country Status (1)

Country Link
JP (1) JPS602181A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49117694A (en) * 1973-03-22 1974-11-11
JPS5170891A (en) * 1974-11-22 1976-06-18 Toyo Jozo Kk Seishuno seizoho
JPS5264495A (en) * 1975-11-19 1977-05-27 Yamanaka Giken Kougiyou Kk Process for treating fermented liquor
JPS57206378A (en) * 1981-06-12 1982-12-17 Kuraray Co Ltd Filtering method of sake

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49117694A (en) * 1973-03-22 1974-11-11
JPS5170891A (en) * 1974-11-22 1976-06-18 Toyo Jozo Kk Seishuno seizoho
JPS5264495A (en) * 1975-11-19 1977-05-27 Yamanaka Giken Kougiyou Kk Process for treating fermented liquor
JPS57206378A (en) * 1981-06-12 1982-12-17 Kuraray Co Ltd Filtering method of sake

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