JPH07106139B2 - Method for producing sake and fermented seasoning using low inhibition reverse osmosis membrane - Google Patents
Method for producing sake and fermented seasoning using low inhibition reverse osmosis membraneInfo
- Publication number
- JPH07106139B2 JPH07106139B2 JP27369791A JP27369791A JPH07106139B2 JP H07106139 B2 JPH07106139 B2 JP H07106139B2 JP 27369791 A JP27369791 A JP 27369791A JP 27369791 A JP27369791 A JP 27369791A JP H07106139 B2 JPH07106139 B2 JP H07106139B2
- Authority
- JP
- Japan
- Prior art keywords
- sake
- reverse osmosis
- osmosis membrane
- liquor
- permeate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000012528 membrane Substances 0.000 title claims description 29
- 238000004519 manufacturing process Methods 0.000 title claims description 21
- 235000011194 food seasoning agent Nutrition 0.000 title claims description 19
- 238000001223 reverse osmosis Methods 0.000 title claims description 16
- 230000005764 inhibitory process Effects 0.000 title claims description 8
- 239000012466 permeate Substances 0.000 claims description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- 230000000903 blocking effect Effects 0.000 claims description 6
- 239000003795 chemical substances by application Substances 0.000 claims description 5
- 238000005342 ion exchange Methods 0.000 claims description 5
- 238000001914 filtration Methods 0.000 claims description 3
- 150000003839 salts Chemical class 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 235000019640 taste Nutrition 0.000 description 21
- 241000209094 Oryza Species 0.000 description 9
- 235000007164 Oryza sativa Nutrition 0.000 description 9
- 235000001014 amino acid Nutrition 0.000 description 9
- 229940024606 amino acid Drugs 0.000 description 9
- 150000001413 amino acids Chemical class 0.000 description 9
- 235000009566 rice Nutrition 0.000 description 9
- 238000010586 diagram Methods 0.000 description 8
- 235000000346 sugar Nutrition 0.000 description 7
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 6
- 238000000855 fermentation Methods 0.000 description 6
- 230000004151 fermentation Effects 0.000 description 6
- 239000003456 ion exchange resin Substances 0.000 description 6
- 229920003303 ion-exchange polymer Polymers 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 239000004278 EU approved seasoning Substances 0.000 description 5
- 230000006866 deterioration Effects 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 235000013555 soy sauce Nutrition 0.000 description 4
- 102000004190 Enzymes Human genes 0.000 description 3
- 108090000790 Enzymes Proteins 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- 235000013361 beverage Nutrition 0.000 description 3
- 239000000284 extract Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 150000007524 organic acids Chemical class 0.000 description 3
- 235000005985 organic acids Nutrition 0.000 description 3
- 150000008163 sugars Chemical class 0.000 description 3
- BWGNESOTFCXPMA-UHFFFAOYSA-N Dihydrogen disulfide Chemical compound SS BWGNESOTFCXPMA-UHFFFAOYSA-N 0.000 description 2
- YBHQCJILTOVLHD-YVMONPNESA-N Mirin Chemical compound S1C(N)=NC(=O)\C1=C\C1=CC=C(O)C=C1 YBHQCJILTOVLHD-YVMONPNESA-N 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 230000032683 aging Effects 0.000 description 2
- 235000019658 bitter taste Nutrition 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 239000000796 flavoring agent Substances 0.000 description 2
- 235000019634 flavors Nutrition 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 235000018102 proteins Nutrition 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 235000019583 umami taste Nutrition 0.000 description 2
- 240000006439 Aspergillus oryzae Species 0.000 description 1
- 235000002247 Aspergillus oryzae Nutrition 0.000 description 1
- WHUUTDBJXJRKMK-UHFFFAOYSA-N Glutamic acid Natural products OC(=O)C(N)CCC(O)=O WHUUTDBJXJRKMK-UHFFFAOYSA-N 0.000 description 1
- CKLJMWTZIZZHCS-REOHCLBHSA-N L-aspartic acid Chemical compound OC(=O)[C@@H](N)CC(O)=O CKLJMWTZIZZHCS-REOHCLBHSA-N 0.000 description 1
- WHUUTDBJXJRKMK-VKHMYHEASA-N L-glutamic acid Chemical compound OC(=O)[C@@H](N)CCC(O)=O WHUUTDBJXJRKMK-VKHMYHEASA-N 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- 235000014680 Saccharomyces cerevisiae Nutrition 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000008122 artificial sweetener Substances 0.000 description 1
- 235000021311 artificial sweeteners Nutrition 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 235000003704 aspartic acid Nutrition 0.000 description 1
- OQFSQFPPLPISGP-UHFFFAOYSA-N beta-carboxyaspartic acid Natural products OC(=O)C(N)C(C(O)=O)C(O)=O OQFSQFPPLPISGP-UHFFFAOYSA-N 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 150000002016 disaccharides Chemical class 0.000 description 1
- PXEDJBXQKAGXNJ-QTNFYWBSSA-L disodium L-glutamate Chemical compound [Na+].[Na+].[O-]C(=O)[C@@H](N)CCC([O-])=O PXEDJBXQKAGXNJ-QTNFYWBSSA-L 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 235000013922 glutamic acid Nutrition 0.000 description 1
- 239000004220 glutamic acid Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 230000005923 long-lasting effect Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 150000002772 monosaccharides Chemical class 0.000 description 1
- 235000013923 monosodium glutamate Nutrition 0.000 description 1
- 150000007523 nucleic acids Chemical class 0.000 description 1
- 102000039446 nucleic acids Human genes 0.000 description 1
- 108020004707 nucleic acids Proteins 0.000 description 1
- 229920001542 oligosaccharide Polymers 0.000 description 1
- 150000002482 oligosaccharides Chemical class 0.000 description 1
- -1 organic acid salts Chemical class 0.000 description 1
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 102200129509 rs186996510 Human genes 0.000 description 1
- 230000001953 sensory effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229940073490 sodium glutamate Drugs 0.000 description 1
- 235000019614 sour taste Nutrition 0.000 description 1
- 235000013599 spices Nutrition 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000006188 syrup Substances 0.000 description 1
- 235000020357 syrup Nutrition 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 235000019607 umami taste sensations Nutrition 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Treatment Of Liquids With Adsorbents In General (AREA)
- Seasonings (AREA)
- Alcoholic Beverages (AREA)
- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
Description
【0001】[0001]
【産業上の利用分野利用】本発明は、低阻止逆浸透圧膜
を用いた清酒及び醗酵調味料の製造法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing sake and fermented seasonings using a low inhibition reverse osmosis membrane.
【0002】[0002]
【発明の背景】清酒の需要が停滞、又は下降の傾向を示
すようになって久しい。その間、需要喚起のため清酒の
多様化への努力をしているが、依然として新規の需要層
(若者、女性)の開拓までには到っていないのが現状で
ある。米を原料とし、かつ酒税法の枠内において、従来
の製造法によって生成された清酒は、自ずから、その嗜
好性(呈味)に限界があり、その魅力ある飲料に成り難
いものと考えられる。BACKGROUND OF THE INVENTION The demand for sake has been stagnant or has been declining for a long time. During that time, efforts have been made to diversify sake to stimulate demand, but the current situation is that it has not yet cultivated new demand groups (young people and women). Sake made from rice as a raw material and produced according to the conventional manufacturing method within the framework of the liquor tax law is naturally limited in its taste (taste), and is considered to be difficult to be an attractive beverage.
【0003】また、近年の高級化志向から、雑味のない
酒質と、マイルドで芳香を有するものが好まれ、更に
は、鮮度の高い食品趣向としていわゆる「生酒」のニー
ズも高まってきている。[0003] Further, in recent years, with the intention of upsizing, the taste of sake with no unpleasant taste and mild and aromatic flavors are preferred. Furthermore, as a taste of food with high freshness, there is an increasing need for so-called "sake". .
【0004】[0004]
【発明が解決しようとする課題】しかし、これらの要求
に答える清酒は、質の高い原料米を高精白して醸造をし
なければならず、その価格は、コスト比率の大きい原料
米コストに大きく影響される結果となっていた。上述の
ように厳しい環境下にある清酒業界においては、これら
問題点の早期解決が急務となっていた。However, sake that meets these demands requires high-quality raw rice to be highly refined and brewed, and its price is much higher than the cost of raw rice, which has a large cost ratio. The result was affected. As mentioned above, in the sake industry, which is in a severe environment, there is an urgent need for early resolution of these problems.
【0005】そこで、本願発明は、これら問題点の解決
を目的としてなされたもので、従来の製法により醸造さ
れた清酒をベースとし、低阻止逆浸透圧膜やイオン交換
剤を用いて新規な清酒、および酒質改善した清酒の製造
方法、更にはこれを用いた醗酵調味料の製造方法を提供
するものである。Therefore, the present invention has been made for the purpose of solving these problems, and is based on the sake brewed by the conventional production method, and uses a low blocking reverse osmosis membrane and an ion exchanger as a novel sake. , And a method for producing sake with improved liquor quality, and a method for producing a fermented seasoning using the same.
【0006】[0006]
【課題を解決するための手段】以下に、本願発明に係る
清酒の製造方法、及び醗酵調味料の製造方法について説
明する。従来の製法により生成した清酒を、加圧下(2
〜3MPa)で低阻止逆浸透圧膜を用いて透過酒と非透
過酒に分離する。ここで用いられる低阻止逆浸透圧膜と
は、限外濾過膜と逆浸透圧膜の中間的領域の性質を有す
る膜であり、分子量数百位の物質の一部を通過させ、分
子量1000以上の物質は阻止するポアサイズの膜をい
う。かかる膜は、特にルーズRO膜と言われている。こ
の膜に、清酒を透過させると分子量数百位の物質(単糖
類、二糖類、オリゴ糖、アミノ酸、有機酸、等)の一部
が分離分別され、透過酒と透過しない非透過酒とが得ら
れる。非透過酒は、再び前記の透過を繰り返すことによ
り、清酒中の呈味成分の濃度が高まる。例えば、低精白
米によって生成された清酒は、米中に蛋白質が高いた
め、その酒も当然、アミノ酸(タンパク質)が高くなる
と同時に、酸やエキス分も高まことになる。このような
清酒は、雑味が強く、酒質が重く舌に抵抗のある酒とな
り、現代人の嗜好に反するものとなる。[Means for Solving the Problems] A method for producing sake and a method for producing a fermented seasoning according to the present invention will be described below. Sake produced by the conventional method is added under pressure (2
Separation into permeated liquor and non-permeated liquor using a low inhibition reverse osmosis membrane at ~ 3 MPa). The low-inhibition reverse osmosis membrane used here is a membrane having a property in an intermediate region between an ultrafiltration membrane and a reverse osmosis membrane, and allows a part of a substance having a molecular weight of several hundreds to pass therethrough and has a molecular weight of 1000 or more. Substance refers to a blocking pore-size membrane. Such a film is particularly called a loose RO film. When sake is permeated into this membrane, some of the substances with a molecular weight of several hundreds (monosaccharides, disaccharides, oligosaccharides, amino acids, organic acids, etc.) are separated and separated, and permeated sake and non-permeated sake that does not permeate are separated. can get. In non-permeated liquor, the concentration of taste components in sake is increased by repeating the above-mentioned permeation. For example, sake made from low-polished rice has a high protein content in rice, and naturally, the sake also has a high amino acid (protein) content, as well as a high acid content and extract content. Such sake becomes a sake with a strong miscellaneous taste, heavy liquor quality, and resistance to the tongue, which is against the taste of modern people.
【0007】一方、透過酒は、アミノ酸、有機酸、糖
類、エキスの一部が除去されるため淡麗な酒質となる。
次に前記の非透過酒に、イオン交換剤を接触させる。こ
こでイオン交換剤としては、強酸性のイオン交換樹脂を
用いる。これにより、雑味の原因となる清酒中のアミノ
酸、酒質劣化因子のジスルフィド、又は着色起因物質の
金属イオン、有機酸塩のプラス荷電物質等が除去され
る。なお、酸は増加するが、糖類は、イオン交換樹脂に
吸着されないため残存する。この結果、酒質が淡麗で高
甘味、高酸味を呈する清酒となる。On the other hand, permeated liquor has a clean liquor quality because some amino acids, organic acids, sugars and extracts are removed.
Next, the non-permeable alcohol is brought into contact with an ion exchange agent. Here, a strongly acidic ion exchange resin is used as the ion exchange agent. As a result, amino acids in sake, disulfide of a deterioration factor of sake quality, metal ions of a substance causing coloration, positively charged substances of organic acid salts, etc., which cause an unpleasant taste, are removed. The acid increases, but the saccharide remains because it is not adsorbed by the ion exchange resin. As a result, the sake becomes a sake with a clean liquor quality and high sweetness and high acidity.
【0008】さらに、かかる清酒に水を添加し、淡麗で
マイルドな低アルコール濃度(10%前後)の清酒とし
てもよい。また、前記非透過酒のみを繰り返して透過す
ることにより、高濃度の清酒を得るとができる。透過酒
と非透過酒との容積比が1:1の時の非透過酒を2倍濃
縮酒とし、この濃縮倍率を高めれば、雑味と若干の苦味
のある味の濃い清酒が得らる。この清酒を成分調節し、
活性炭素濾過した後、常温下で2〜3ケ月間熟成させる
と、老香のある独得の風味を呈するいわゆる古酒タイプ
の清酒が得られる。[0008] Further, water may be added to such sake to obtain a sake with a clean and mild low alcohol concentration (around 10%). Further, a high-concentration sake can be obtained by repeatedly permeating only the non-permeable sake. When the volume ratio of permeation liquor to non-permeation liquor is 1: 1 and the non-permeation liquor is made into 2 times concentrated liquor, if this concentration ratio is increased, it becomes a tasty sake with a bitter taste and a little bitter taste. . Adjust the ingredients of this sake,
After filtering with activated carbon, aging at room temperature for 2 to 3 months gives a so-called old sake type sake with a long-lasting unique flavor.
【0009】さらに、濃縮倍率を4倍以上にし、食塩お
よび副資材等を添加することにより、完全な醗酵調味料
とすることができる。清酒は、昔より和風料理の隠し味
として利用されてきたものである。かかる醗酵調味料
は、清酒の呈味成分のバランスを崩さずに濃縮されたも
のであり、化学調味料や人工甘味料を添加した従来の調
味料とは大きく異なり、米や麹菌や酵母菌などの分解か
ら成る完全な天然調味料として安全かつ現代の嗜好にマ
ッチしたものとなる。Further, by making the concentration ratio 4 times or more and adding salt and auxiliary materials, it is possible to obtain a complete fermented seasoning. Sake has been used as a hidden taste in Japanese cuisine since ancient times. Such a fermented seasoning is concentrated without disturbing the balance of the taste components of sake, and is significantly different from conventional seasonings to which chemical seasonings and artificial sweeteners are added, and rice, koji mold, yeast, etc. As a complete natural seasoning consisting of the decomposition of, it will be safe and match modern tastes.
【0010】さらにまた、前記透過酒に、透過前の清酒
や、又は他の清酒を適宜の割合でブレンド(混合)する
ことにより、酒質を改善したいわゆる辛口の清酒を製造
することができる。前記透過酒は、酒質の雑味成分の主
因となるアミノ酸、酸味を呈する有機酸、および甘味成
分の糖類などの大半は除去され、このままでも、すっき
りした淡麗な清酒として飲料に敵するが、さらにこれ
に、低精白米によって生成された雑味の多い清酒や、醗
酵が悪い酸味の強い清酒や、又は醗酵不十分で糖類の高
いいわゆる甘だれのする清酒などにブレンドすれば、酒
質の改善をもすることができる。Furthermore, by blending (mixing) the above-mentioned permeated sake with sake before permeation or other sake at an appropriate ratio, so-called dry sake with improved liquor quality can be produced. The permeation liquor is almost free of amino acids, which are the main causes of the taste components of liquor quality, organic acids exhibiting sourness, and sugars such as sweetening components, and even as it is, it competes with beverages as a clean and refined sake. , Furthermore, if it is blended with sake with a lot of miscellaneous taste produced by low-polished rice, sake with a strong acidity that fermentation is bad, or so-called sweet sake with a high fermentation and sugar content, Can be improved.
【0011】[0011]
【実施例】次に、上記各種清酒及び醗酵調味料の製造法
に対して、表、及び図面を参照しながら、幾つかの実施
例について、以下に詳細に説明する。 (イ)低濃度清酒の製造。図1は、低阻止逆浸透圧膜
(ルーズRO膜。)による清酒の処理を示した概念図で
ある。EXAMPLES Next, some examples of the methods for producing the various types of sake and fermented seasonings will be described in detail below with reference to the tables and drawings. (B) Production of low-concentration sake. FIG. 1 is a conceptual diagram showing the treatment of sake with a low blocking reverse osmosis membrane (loose RO membrane).
【0012】貯溜槽Aに被処理の普通酒(原酒)1を注
入し溜置する。これを圧送ポンプ2でルーズRO膜3が
配置された濾過装置4に注送し、透過処理する。透過酒
5は貯溜槽Bに溜め置き、非透過酒6は、貯溜槽Aに戻
して循環させる。濃縮倍率は、透過酒5の容量から決定
される。The ordinary sake (raw sake) 1 to be processed is poured into the storage tank A and stored therein. This is pumped by the pressure pump 2 to the filtration device 4 in which the loose RO membrane 3 is arranged, and is permeated. The permeated liquor 5 is stored in the storage tank B, and the non-permeated liquor 6 is returned to the storage tank A for circulation. The concentration ratio is determined from the volume of the permeation liquor 5.
【0013】[0013]
【表1】 [Table 1]
【0014】上記の表1は、透過酒5と非透過酒(濃縮
倍率2倍)6の成分を比較して示したものである。かか
る結果から分かるように、透過酒5は、各種成分が著し
く減少している。すなわち、酸度で約50%、アミノ酸
度で約63%、直糖で約80%が減少し、さらに、清酒
の劣化成分であるジスルフィド、3DG等も極端に少な
くなっている。ところで、生酒は、酵素の残存が見ら
れ、これが熟成中に作用して、糖分やアミノ酸を増加さ
せ、酒質を劣化させる原因となっている。したがって、
酒質の維持から、これを抑えるため、低温貯蔵が必要と
なる。Table 1 above shows a comparison of the components of the permeated liquor 5 and the non-permeated liquor (concentration factor of 2) 6. As can be seen from these results, the permeated liquor 5 contains various components significantly reduced. That is, the acidity is reduced by about 50%, the amino acidity is reduced by about 63%, and the direct sugar is reduced by about 80%, and disulfide, 3DG, etc., which are deterioration components of sake, are extremely reduced. By the way, in sake, residual enzymes are observed, which act during aging to increase sugars and amino acids and cause deterioration of sake quality. Therefore,
From the maintenance of liquor quality, low temperature storage is necessary to suppress this.
【0015】しかし、ルーズRO膜3を透過させると、
この酵素は完全に除去することができ、酒質の劣化を防
止することができる。図2は、イオン交換剤(本実施例
では強酸性のイオン交換樹脂を用いた。)による前記非
透過酒6の処理を示した概念図である。貯溜槽C内の非
透過酒6をイオン交換樹脂7に接触させ、貯溜槽Dに溜
め置き、水8を目標とする成分値まで希釈し、その後火
入れ処理9をして低濃度酒10を製造する。However, when the loose RO membrane 3 is permeated,
This enzyme can be completely removed, and deterioration of liquor quality can be prevented. FIG. 2 is a conceptual diagram showing the treatment of the impermeable liquor 6 with an ion exchange agent (a strongly acidic ion exchange resin was used in this example). The non-permeable liquor 6 in the storage tank C is brought into contact with the ion-exchange resin 7 and stored in the storage tank D, and the water 8 is diluted to the target component value, and then the firing treatment 9 is performed to produce the low-concentration liquor 10. To do.
【0016】[0016]
【表2】 [Table 2]
【0017】上記の表2は、前記低濃度酒の製造したと
きの各成分を示したものである。その結果、アルコール
濃度10%から8%位になるまで加水すると酒質が良
く、甘味と酸味のバランスの良いさわやかな味、いわば
ワイン風の清酒が得られた。 (ロ)濃厚酒と醗酵調味料の製造。Table 2 above shows the components of the low-concentration sake produced. As a result, when the alcohol concentration was increased from 10% to about 8%, the quality of the sake was good, and a refreshing taste with a good balance of sweetness and acidity, that is, wine-like sake was obtained. (B) Production of concentrated sake and fermented seasonings.
【0018】図3は、濃厚酒、及び醗酵調味料の製造過
程を示す概念図である。先ず、前記図1に示したごとく
ルーズRO膜3を透過しなかった清酒(非透過酒)6を
貯溜槽Aに戻すようにして循環させ、濃縮された非透過
酒6を製造し、貯溜槽Eに貯溜する。この時、濃縮倍率
は、目標とする酒質を考慮して適宜定められる。次に、
この非透過酒6の成分、呈味を調整処理11した後、お
り下げ及び火入れ処理12をして濃厚酒13を製造す
る。FIG. 3 is a conceptual diagram showing the production process of concentrated sake and fermented seasoning. First, as shown in FIG. 1, sake (non-permeated liquor) 6 that has not permeated the loose RO membrane 3 is returned to the storage tank A and circulated to produce concentrated non-permeated liquor 6, which is then stored in the storage tank. Store in E. At this time, the concentration ratio is appropriately determined in consideration of the target liquor quality. next,
After the components 11 and the taste of the non-permeable liquor 6 are adjusted, the liquor is lowered and fired 12 to produce a concentrated liquor 13.
【0019】[0019]
【表3】 [Table 3]
【0020】上記表3は、2倍、及び4倍の濃厚酒13
を活性炭素濾過をし、常温下に3ヶ月放置した時の、官
能審査の結果を示すものである。その結果、2倍濃縮酒
位がもっとも濃厚酒として飲料に適するものであった。
ただ使用する普通清酒の成分によっては、濃厚酒の成分
が変化することから、脱酸、又は補酸する必要がある。
しかしながら酒税法上、清酒への糖分の添加はできない
ため、使用する普通清酒の糖分は、2.5 〜3.5 %位が必
要となる。また、4倍に濃縮した場合は、清酒としての
イメージがなくなってしまう。The above Table 3 shows the concentrated sake 13 which is twice and four times as thick.
The result of sensory evaluation is shown when the product was filtered with activated carbon and left at room temperature for 3 months. As a result, the double-concentrated liquor level was most suitable for beverages as concentrated liquor.
However, depending on the components of ordinary sake, the components of concentrated sake change, so it is necessary to deoxidize or supplement acid.
However, according to the Liquor Tax Law, it is not possible to add sugar to sake, so the sugar content of ordinary sake used should be around 2.5-3.5%. In addition, when it is concentrated four times, the image of sake is lost.
【0021】そこで、このように濃縮した非透過酒6
に、副資材を添加して調整処理14した後、おり下げ及
び火入れ処理12をして天然の醗酵調味料15を製造す
ることができる。Then, the non-permeation liquor 6 thus concentrated
Then, after the auxiliary treatment is added and the adjustment treatment 14 is performed, the hanging process and the firing treatment 12 are performed to produce the natural fermentation seasoning 15.
【0022】[0022]
【表4】 [Table 4]
【0023】上記表4は、4倍濃縮酒と本醸造醤油、お
よび本格派みりんとの成分値を比較したものである。か
かる比較には、原料、製法が異なるため多少無理がある
が、参考推察するに、本製法の醗酵調味料は、醤油とみ
りんの中間的な性格を有し、また、遊離アミノ酸は多い
が、呈味性のアミノ酸であるグルタミン酸やアスパラギ
ン酸は醤油よりは少ない。そのため、醤油程や旨味はや
や薄いが、味のバランスは良くすぐれた醗酵調味料が得
られた。場合によっては、これに食塩10%位を添加し
たり、旨味増強のグルタミン酸ソーダや核酸系調味料を
添加したり、また、用途により、水飴、糊料、スパイス
の添加すれば、すぐれた醗酵調味料を製造することもで
きる。 (ハ)淡麗辛口タイプ、又は酒質改善の清酒の製造。Table 4 above compares the component values of 4-fold concentrated sake, honjo soy sauce, and authentic mirin. In this comparison, the raw materials and the manufacturing method are different, which makes it somewhat unreasonable, but by reference inference, the fermentation seasoning of this manufacturing method has an intermediate character between soy sauce and mirin, and there are many free amino acids. The tasteful amino acids glutamic acid and aspartic acid are less than soy sauce. As a result, a fermented seasoning having a good balance of tastes and a good taste, although the soy sauce and umami taste were slightly weak, was obtained. Depending on the case, about 10% of salt is added to it, or sodium glutamate or nucleic acid-based seasoning that enhances umami is added, or if you add starch syrup, paste, or spice depending on the application, excellent fermentation It can also be manufactured. (C) Manufacture of light dry type or sake with improved quality.
【0024】図4は、淡麗辛口タイプ又は酒質改善の清
酒の製造過程を示す概念図である。ルーズRO膜を透過
させた透過酒5と原酒又は他の清酒1とを、目標とする
成分にブレンド処理16をした後、おり下げ及び火入れ
処理12をしてブレンド酒(淡麗辛口酒、又は酒質改善
酒)17を製造する。FIG. 4 is a conceptual diagram showing a process for producing a pure dry type or sake with improved quality. After the permeation liquor 5 that has permeated the loose RO membrane and the raw liquor or other sake 1 are blended 16 to the target ingredients, the blended liquor (light dry sake or 17) is produced.
【0025】[0025]
【表5】 [Table 5]
【0026】上記表5は、吟醸酒(精白度50%)、普
通清酒(精白度70%)、又は低精白米酒(精白度90
%)のそれぞれの生酒と、前述の透過酒5とを3:1の
割合でブレンドした結果を示したものである。なお、醗
酵がスムーズに行われなかった異常な清酒の改良につい
ても、ルーズRO膜を透過させ、それを適宜ブレンドす
ることにより酒質の改善をすることもできる。Table 5 above shows ginjo sake (50% whiteness), normal sake (70% whiteness), or low-polished rice sake (90% whiteness).
%), And the result of blending each of the above-mentioned sake liquor 5 with the above-mentioned permeation liquor 5 at a ratio of 3: 1. Regarding the abnormal improvement of sake in which fermentation was not smoothly carried out, the quality of sake can be improved by permeating through the loose RO membrane and blending it appropriately.
【0027】[0027]
【効果】以上、本発明の製造方法によれば、下記に列挙
する効果が得られる。 ルーズRO膜処理によって、低精白米より製造した清
酒に存する雑味、重い味の主要因となるタンパク質を簡
単、且つ他の酒質に影響なく除去することができる。そ
の結果、低酸度、低アミノ酸度、及び無残存酵素で官能
的にも淡麗な雑味の少ない酒質を持つ清酒を製造するこ
とができる。As described above, according to the manufacturing method of the present invention, the effects listed below can be obtained. By the loose RO membrane treatment, it is possible to easily remove proteins, which are the main factors of the sour taste and heavy taste, in the sake produced from low-polished rice without affecting the quality of other sake. As a result, it is possible to produce sake which has a low acidity, a low amino acid content, and a residual enzyme, and which has a liquor quality that is functionally clean and has a low taste.
【0028】イオン交換樹脂にて清酒を処理すること
により、脱アミノ酸、及び劣化因子の除去することがで
きる。この結果、雑味の少ない爽やかな清酒、いわばワ
インタイプのような、多様な清酒を製造することができ
る。 ルーズRO膜処理を繰り返すことによって非透過酒を
濃縮するため、天然エキス分の多い多用途の、かつ安全
な天然醗酵調味料を製造することができる。By treating sake with an ion exchange resin, deamino acids and deterioration factors can be removed. As a result, it is possible to produce a variety of refined sake such as refreshing sake with little miscellaneous taste, that is, wine type. Since the impervious liquor is concentrated by repeating the loose RO membrane treatment, a versatile and safe natural fermented seasoning containing a large amount of natural extract can be produced.
【図1】低阻止逆浸透圧膜による清酒の処理を示した概
念図である。FIG. 1 is a conceptual diagram showing the treatment of sake with a low inhibition reverse osmosis membrane.
【図2】イオン交換剤による前記非透過酒6の処理を示
した概念図である。FIG. 2 is a conceptual diagram showing the treatment of the impervious sake 6 with an ion exchange agent.
【図3】濃厚酒、及び醗酵調味料の製造過程を示す概念
図である。FIG. 3 is a conceptual diagram showing a production process of concentrated sake and a fermented seasoning.
【図4】淡麗辛口タイプ、又は酒質改善の清酒の製造過
程を示す概念図である。FIG. 4 is a conceptual diagram showing a manufacturing process of a light dry type or sake with improved liquor quality.
1・・・ 原酒 3・・・ ルーズRO膜 5・・・ 透過
酒 6・・・ 非透過酒(濃縮酒) 7・・・ イオン交換樹脂1 ... Raw liquor 3 ... Loose RO membrane 5 ... Transparent liquor 6 ... Non-permeable liquor (concentrated liquor) 7 ... Ion exchange resin
フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C12G 3/08 102 C12H 1/00 Continuation of the front page (51) Int.Cl. 6 Identification code Office reference number FI Technical display area C12G 3/08 102 C12H 1/00
Claims (4)
圧膜を用いた清酒の製造法。 (イ) 低阻止逆浸透圧膜を用いて加圧下で清酒を透過酒
と非透過酒とに分離する第一工程、 (ロ) 前記非透過酒を、イオン交換剤に接触させる第二
工程、 (ハ) 水を添加する第三工程、1. A method for producing sake using a low blocking reverse osmosis membrane, which comprises the combination of the following steps. (A) a first step of separating sake into permeate and non-permeate under pressure using a low inhibition reverse osmosis membrane; (b) a second step of contacting the non-permeate with an ion exchange agent, (C) Third step of adding water,
圧膜を用いた清酒の製造法。 (イ) 低阻止逆浸透圧膜を用いて加圧下で清酒を透過酒
と非透過酒とに分離する第一工程、 (ロ) 前記非透過酒に清酒を適宜に調整添加する第二工
程、 (ハ) 活性炭素濾過する第三工程、2. A method for producing sake using a low blocking reverse osmosis membrane, which comprises combining the following steps. (A) a first step of separating sake into permeate and non-permeate under pressure using a low inhibition reverse osmosis membrane, (b) a second step of appropriately adjusting and adding sake to the non-permeate, (C) Third step of filtering activated carbon,
圧膜を用いた清酒の製造法。 (イ) 低阻止逆浸透圧膜を用いて加圧下で清酒を透過酒
と非透過酒とに分離する第一工程、 (ロ) 前記透過酒に清酒を適宜に調整添加する第二工
程、3. A method for producing sake using a low blocking reverse osmosis membrane, which comprises the combination of the following steps. (A) a first step of separating sake into permeate and non-permeate under pressure using a low inhibition reverse osmosis membrane, (b) a second step of appropriately adjusting and adding sake to the permeate,
圧膜を用いた醗酵調味料の製造法。 (イ) 低阻止逆浸透圧膜を用いて加圧下で清酒を透過酒
と非透過酒とに分離する第一工程、 (ロ) 前記非透過酒のみを、低阻止逆浸透圧膜を複数回
循環通過させ適宜の濃度濃縮させる第二工程、 (ハ) 成分を調整し、食塩を適宜添加する第三工程、4. A method for producing a fermented seasoning using a low inhibition reverse osmosis membrane, which comprises the combination of the following steps. (A) a first step of separating sake into permeate and non-permeate liquor under pressure using a low-inhibition reverse osmosis membrane; Second step of circulating and concentrating to an appropriate concentration, (c) Third step of adjusting components and adding salt appropriately,
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27369791A JPH07106139B2 (en) | 1991-10-22 | 1991-10-22 | Method for producing sake and fermented seasoning using low inhibition reverse osmosis membrane |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27369791A JPH07106139B2 (en) | 1991-10-22 | 1991-10-22 | Method for producing sake and fermented seasoning using low inhibition reverse osmosis membrane |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH05111373A JPH05111373A (en) | 1993-05-07 |
| JPH07106139B2 true JPH07106139B2 (en) | 1995-11-15 |
Family
ID=17531297
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP27369791A Expired - Lifetime JPH07106139B2 (en) | 1991-10-22 | 1991-10-22 | Method for producing sake and fermented seasoning using low inhibition reverse osmosis membrane |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07106139B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100404694C (en) * | 2000-12-28 | 2008-07-23 | 达尼斯科甜味剂股份有限公司 | Separation method |
| JP4190191B2 (en) * | 2002-02-26 | 2008-12-03 | 宝ホールディングス株式会社 | Sake production method |
| JP4557581B2 (en) * | 2004-03-30 | 2010-10-06 | 宝酒造株式会社 | New mirin and process for producing the same |
| CN104560586A (en) * | 2013-12-12 | 2015-04-29 | 李仪 | Temperature-controlled reverse osmosis white wine purifying device and method |
-
1991
- 1991-10-22 JP JP27369791A patent/JPH07106139B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH05111373A (en) | 1993-05-07 |
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