JPH04141080A - Soft type 'sake' and production thereof - Google Patents
Soft type 'sake' and production thereofInfo
- Publication number
- JPH04141080A JPH04141080A JP2262427A JP26242790A JPH04141080A JP H04141080 A JPH04141080 A JP H04141080A JP 2262427 A JP2262427 A JP 2262427A JP 26242790 A JP26242790 A JP 26242790A JP H04141080 A JPH04141080 A JP H04141080A
- Authority
- JP
- Japan
- Prior art keywords
- sake
- exchange membrane
- alcohol
- ions
- anion exchange
- 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
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- 238000011282 treatment Methods 0.000 claims abstract description 28
- 239000003011 anion exchange membrane Substances 0.000 claims abstract description 19
- 150000002500 ions Chemical class 0.000 claims abstract description 16
- 239000000203 mixture Substances 0.000 claims abstract description 14
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 claims abstract description 12
- VHRGRCVQAFMJIZ-UHFFFAOYSA-N cadaverine Chemical compound NCCCCCN VHRGRCVQAFMJIZ-UHFFFAOYSA-N 0.000 claims abstract description 10
- KIDHWZJUCRJVML-UHFFFAOYSA-N putrescine Chemical compound NCCCCN KIDHWZJUCRJVML-UHFFFAOYSA-N 0.000 claims abstract description 10
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 9
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims abstract description 9
- MLFHJEHSLIIPHL-UHFFFAOYSA-N isoamyl acetate Chemical compound CC(C)CCOC(C)=O MLFHJEHSLIIPHL-UHFFFAOYSA-N 0.000 claims abstract description 8
- PHTQWCKDNZKARW-UHFFFAOYSA-N isoamylol Chemical compound CC(C)CCO PHTQWCKDNZKARW-UHFFFAOYSA-N 0.000 claims abstract description 8
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 claims abstract description 8
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 claims abstract description 8
- KDYFGRWQOYBRFD-UHFFFAOYSA-N Succinic acid Natural products OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000004310 lactic acid Substances 0.000 claims abstract description 6
- 235000014655 lactic acid Nutrition 0.000 claims abstract description 6
- BJEPYKJPYRNKOW-REOHCLBHSA-N (S)-malic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O BJEPYKJPYRNKOW-REOHCLBHSA-N 0.000 claims abstract description 5
- 239000004475 Arginine Substances 0.000 claims abstract description 5
- QIVBCDIJIAJPQS-VIFPVBQESA-N L-tryptophane Chemical compound C1=CC=C2C(C[C@H](N)C(O)=O)=CNC2=C1 QIVBCDIJIAJPQS-VIFPVBQESA-N 0.000 claims abstract description 5
- KDXKERNSBIXSRK-UHFFFAOYSA-N Lysine Natural products NCCCCC(N)C(O)=O KDXKERNSBIXSRK-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000004472 Lysine Substances 0.000 claims abstract description 5
- 239000005700 Putrescine Substances 0.000 claims abstract description 5
- QIVBCDIJIAJPQS-UHFFFAOYSA-N Tryptophan Natural products C1=CC=C2C(CC(N)C(O)=O)=CNC2=C1 QIVBCDIJIAJPQS-UHFFFAOYSA-N 0.000 claims abstract description 5
- BJEPYKJPYRNKOW-UHFFFAOYSA-N alpha-hydroxysuccinic acid Natural products OC(=O)C(O)CC(O)=O BJEPYKJPYRNKOW-UHFFFAOYSA-N 0.000 claims abstract description 5
- ODKSFYDXXFIFQN-UHFFFAOYSA-N arginine Natural products OC(=O)C(N)CCCNC(N)=N ODKSFYDXXFIFQN-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000001630 malic acid Substances 0.000 claims abstract description 5
- 235000011090 malic acid Nutrition 0.000 claims abstract description 5
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims abstract description 4
- AYRXSINWFIIFAE-SCLMCMATSA-N Isomaltose Natural products OC[C@H]1O[C@H](OC[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C=O)[C@@H](O)[C@@H](O)[C@@H]1O AYRXSINWFIIFAE-SCLMCMATSA-N 0.000 claims abstract description 4
- WQZGKKKJIJFFOK-PHYPRBDBSA-N alpha-D-galactose Chemical compound OC[C@H]1O[C@H](O)[C@H](O)[C@@H](O)[C@H]1O WQZGKKKJIJFFOK-PHYPRBDBSA-N 0.000 claims abstract description 4
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 claims abstract description 4
- 229930182830 galactose Natural products 0.000 claims abstract description 4
- 239000008103 glucose Substances 0.000 claims abstract description 4
- 229940117955 isoamyl acetate Drugs 0.000 claims abstract description 4
- 229940035429 isobutyl alcohol Drugs 0.000 claims abstract description 4
- DLRVVLDZNNYCBX-RTPHMHGBSA-N isomaltose Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@@H]1OC[C@@H]1[C@@H](O)[C@H](O)[C@@H](O)C(O)O1 DLRVVLDZNNYCBX-RTPHMHGBSA-N 0.000 claims abstract description 4
- ODKSFYDXXFIFQN-BYPYZUCNSA-P L-argininium(2+) Chemical compound NC(=[NH2+])NCCC[C@H]([NH3+])C(O)=O ODKSFYDXXFIFQN-BYPYZUCNSA-P 0.000 claims abstract description 3
- KDXKERNSBIXSRK-YFKPBYRVSA-N L-lysine Chemical compound NCCCC[C@H](N)C(O)=O KDXKERNSBIXSRK-YFKPBYRVSA-N 0.000 claims abstract description 3
- KDYFGRWQOYBRFD-NUQCWPJISA-N butanedioic acid Chemical compound O[14C](=O)CC[14C](O)=O KDYFGRWQOYBRFD-NUQCWPJISA-N 0.000 claims abstract description 3
- SHZIWNPUGXLXDT-UHFFFAOYSA-N ethyl hexanoate Chemical compound CCCCCC(=O)OCC SHZIWNPUGXLXDT-UHFFFAOYSA-N 0.000 claims abstract 4
- 239000012528 membrane Substances 0.000 claims description 32
- 238000005341 cation exchange Methods 0.000 claims description 18
- 238000000909 electrodialysis Methods 0.000 claims description 16
- 238000000034 method Methods 0.000 claims description 15
- 230000007423 decrease Effects 0.000 claims description 8
- 235000011187 glycerol Nutrition 0.000 claims description 3
- 125000001453 quaternary ammonium group Chemical group 0.000 claims description 3
- 125000001174 sulfone group Chemical group 0.000 claims description 3
- 238000002407 reforming Methods 0.000 claims description 2
- 239000001384 succinic acid Substances 0.000 claims description 2
- 235000019658 bitter taste Nutrition 0.000 abstract description 11
- 235000019606 astringent taste Nutrition 0.000 abstract description 10
- 235000019640 taste Nutrition 0.000 abstract description 7
- 239000011734 sodium Substances 0.000 abstract description 3
- 206010019133 Hangover Diseases 0.000 abstract description 2
- 235000019992 sake Nutrition 0.000 abstract 7
- 239000003010 cation ion exchange membrane Substances 0.000 abstract 2
- 150000001768 cations Chemical class 0.000 abstract 2
- 239000007788 liquid Substances 0.000 description 20
- 238000012545 processing Methods 0.000 description 18
- 239000002699 waste material Substances 0.000 description 17
- 150000003839 salts Chemical class 0.000 description 16
- 241000209094 Oryza Species 0.000 description 7
- 235000007164 Oryza sativa Nutrition 0.000 description 7
- 235000009566 rice Nutrition 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 150000001413 amino acids Chemical class 0.000 description 6
- 238000004458 analytical method Methods 0.000 description 6
- 125000000129 anionic group Chemical group 0.000 description 4
- 238000011156 evaluation Methods 0.000 description 4
- 235000013334 alcoholic beverage Nutrition 0.000 description 3
- 150000001412 amines Chemical class 0.000 description 3
- 239000003957 anion exchange resin Substances 0.000 description 3
- 235000019629 palatability Nutrition 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- 230000001953 sensory effect Effects 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 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 2
- CHRJZRDFSQHIFI-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;styrene Chemical compound C=CC1=CC=CC=C1.C=CC1=CC=CC=C1C=C CHRJZRDFSQHIFI-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 235000011511 Diospyros Nutrition 0.000 description 2
- 244000236655 Diospyros kaki Species 0.000 description 2
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 2
- GXCLVBGFBYZDAG-UHFFFAOYSA-N N-[2-(1H-indol-3-yl)ethyl]-N-methylprop-2-en-1-amine Chemical compound CN(CCC1=CNC2=C1C=CC=C2)CC=C GXCLVBGFBYZDAG-UHFFFAOYSA-N 0.000 description 2
- 229910002651 NO3 Inorganic materials 0.000 description 2
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 2
- 125000002091 cationic group Chemical group 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 238000010612 desalination reaction Methods 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- 230000035622 drinking Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- RGXWDWUGBIJHDO-UHFFFAOYSA-N ethyl decanoate Chemical compound CCCCCCCCCC(=O)OCC RGXWDWUGBIJHDO-UHFFFAOYSA-N 0.000 description 2
- 239000000796 flavoring agent Substances 0.000 description 2
- 230000014509 gene expression Effects 0.000 description 2
- FUZZWVXGSFPDMH-UHFFFAOYSA-N hexanoic acid Chemical compound CCCCCC(O)=O FUZZWVXGSFPDMH-UHFFFAOYSA-N 0.000 description 2
- 239000003456 ion exchange resin Substances 0.000 description 2
- 229920003303 ion-exchange polymer Polymers 0.000 description 2
- -1 nitrate ions Chemical class 0.000 description 2
- 150000007524 organic acids Chemical class 0.000 description 2
- 235000005985 organic acids Nutrition 0.000 description 2
- 238000009928 pasteurization Methods 0.000 description 2
- KJFMBFZCATUALV-UHFFFAOYSA-N phenolphthalein Chemical compound C1=CC(O)=CC=C1C1(C=2C=CC(O)=CC=2)C2=CC=CC=C2C(=O)O1 KJFMBFZCATUALV-UHFFFAOYSA-N 0.000 description 2
- 238000001223 reverse osmosis Methods 0.000 description 2
- YGSDEFSMJLZEOE-UHFFFAOYSA-N salicylic acid Chemical compound OC(=O)C1=CC=CC=C1O YGSDEFSMJLZEOE-UHFFFAOYSA-N 0.000 description 2
- 238000004448 titration Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- ZPLCXHWYPWVJDL-UHFFFAOYSA-N 4-[(4-hydroxyphenyl)methyl]-1,3-oxazolidin-2-one Chemical compound C1=CC(O)=CC=C1CC1NC(=O)OC1 ZPLCXHWYPWVJDL-UHFFFAOYSA-N 0.000 description 1
- 240000006439 Aspergillus oryzae Species 0.000 description 1
- 235000002247 Aspergillus oryzae Nutrition 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 229930006000 Sucrose Natural products 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 238000005349 anion exchange Methods 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 238000004128 high performance liquid chromatography Methods 0.000 description 1
- 229910001410 inorganic ion Inorganic materials 0.000 description 1
- 239000003014 ion exchange membrane Substances 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- PGSADBUBUOPOJS-UHFFFAOYSA-N neutral red Chemical compound Cl.C1=C(C)C(N)=CC2=NC3=CC(N(C)C)=CC=C3N=C21 PGSADBUBUOPOJS-UHFFFAOYSA-N 0.000 description 1
- FJKROLUGYXJWQN-UHFFFAOYSA-N papa-hydroxy-benzoic acid Natural products OC(=O)C1=CC=C(O)C=C1 FJKROLUGYXJWQN-UHFFFAOYSA-N 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229960004889 salicylic acid Drugs 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000005720 sucrose Substances 0.000 description 1
- 235000000346 sugar Nutrition 0.000 description 1
- 150000008163 sugars Chemical class 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 235000019583 umami taste Nutrition 0.000 description 1
Abstract
Description
本発明は、苦味、渋味、雑味の改善されたソフトタイプ
の清酒、およびその製造法、改質法に関する。The present invention relates to a soft type sake with improved bitterness, astringency, and off-taste, and a method for producing and modifying the same.
従来より、特殊な麹菌や酵母を用いたり、特殊な処理を
施すことにより、清酒の嗜好性の改善が行われている。
通常の清酒を処理することにより改質する方法としては
、現在までに、逆浸透膜を用いた清酒の品質改良法(特
開昭59−183686号)や、清酒中のアニオン性成
分をアニオン交換樹脂または交換膜にて除去する方法(
特開昭55−77885号)が提案されている。
また、上記に示した清酒の嗜好性の改善目的とは別の目
的として、例えば、腐敗変質防止のため酒類をイオン交
換樹脂処理する方法(特公昭314989号)、酒類中
のサリチル酸やカドミウムをイオン交換樹脂にて除去す
る方法(特公昭48−18833号、特公昭51−50
77号)、および酒類の着色をキレート性イオン交換樹
脂にて除去する方法(特公昭61−48912号)等の
例が挙げられるが、これらは全く清酒の嗜好性の改善を
目的としたものではない。
また、澱粉や米麹から調製した糖化液をイオン交換膜等
によって処理した後清酒となす方法も知られている(特
開昭57−129700号、特開昭57−159500
号、特開昭58−882号、特開昭58−43780号
)が、これらの方法は、清酒の製造に用いる糖化液から
米由来の不適当なリン分等や無機イオン等を除去する目
的で1テうものであり、本願と目的を異にする。Traditionally, the palatability of sake has been improved by using special koji molds and yeast, or by applying special treatments. To date, methods for improving the quality of sake by processing ordinary sake include a method for improving the quality of sake using a reverse osmosis membrane (Japanese Unexamined Patent Publication No. 183686/1986), and anion exchange of anionic components in sake. Method of removing with resin or exchange membrane (
JP-A-55-77885) has been proposed. In addition to the above-mentioned purpose of improving the palatability of sake, for example, there is a method of treating alcoholic beverages with ion exchange resin to prevent spoilage (Japanese Patent Publication No. 314989), which removes salicylic acid and cadmium from alcoholic beverages with ions. Method of removing with exchange resin (Special Publication No. 48-18833, Special Publication No. 51-50
77) and a method for removing the coloration of alcoholic beverages using a chelating ion exchange resin (Special Publication No. 48912/1989), but these methods are not aimed at improving the palatability of sake at all. do not have. In addition, a method is known in which a saccharified solution prepared from starch or rice malt is treated with an ion exchange membrane, etc., and then made into sake (Japanese Patent Application Laid-Open Nos. 57-129700, 1983-159500).
JP-A No. 58-882, JP-A No. 58-43780), these methods are intended to remove inappropriate phosphorus, etc. and inorganic ions derived from rice from the saccharification liquid used in the production of sake. The purpose of this application is different from that of the present application.
前述の逆浸透膜を用いて清酒の品質を改良する方法(特
開昭59−183686号)は、単にアルコール含量を
減少せしめた低アルコール飲料を提供することを目的に
しており、発明の目的を異にしている。また、清酒中の
アニオン性成分をアニオン交換樹脂または交換膜にて除
去する方法(特開昭55−77885号)は、清酒の渋
味の改善が未だ不充分であり、何ら目的とするソフトタ
イプの清酒は得られないものであった。
そこで、さらに別の処理方法により、苦味、渋味、雑味
の改善されたソフトタイプの清酒の提供が待たれていた
。The above-mentioned method for improving the quality of sake using a reverse osmosis membrane (Japanese Patent Application Laid-Open No. 183686/1986) aims simply to provide a low-alcohol beverage with a reduced alcohol content, and does not meet the purpose of the invention. It's different. In addition, the method of removing anionic components in sake using an anion exchange resin or an exchange membrane (Japanese Patent Application Laid-open No. 77885/1985) is still insufficient in improving the astringency of sake, and is not suitable for soft-type sake for any purpose. Sake was unobtainable. Therefore, it has been desired to provide a soft type of sake with improved bitterness, astringency, and off-taste using a different processing method.
本発明者らは、上記問題点を解決するために鋭意研究し
た結果、清酒をカチオン交換膜およびアニオン交換膜を
有する電気透析処理することにより、苦味、渋味、雑味
の改善された従来知られている清酒とは違ったソフトタ
イプの清酒が製造されることを知り本願発明を完成する
に至った。
即ち、本発明は、原清酒組成に比較して、日本酒度、ア
ルコール(%)、エキス分、イソマルトース、グルコー
ス、ガラクトース、グリセリン、n−プロピルアルコー
ル、イソブチルアルコール、イソアミルアルコール、酢
酸イソアミル、カプロン酸エチルの組成含量が実質的に
変化せず、コハク酸、乳酸、リンゴ酸、Na”イオン、
K3イオン、トリプトファン、アルギニン、リジン、プ
トレシン、カダベリンの組成含量が減少したことを特徴
とする新規なソフトタイプの清酒である。
また本発明は、清酒をカチオン交換膜およびアニオン交
換膜を有する電気透析処理することを特徴とするソフト
タイプの清酒の製造法、または清酒の改質法である。
本発明の新規なソフトタイプの清酒とは、上記に記載し
た特定の組成成分を、原清酒組成と比較して減少せしめ
たものであり、これにより、清酒本来の旨味を有しなが
ら苦味、渋味、雑味の改善されたバランスの取れた従来
にない新規な清酒が得られたものであり、例えば、原清
酒組成と比較して日本酒度、アルコール(%)、エキス
分、イソマルトース、グルコース、ガラクトース、グリ
セリン、n−プロピルアルコール、イソブチルアルコー
ル、イソアミルアルコール、酢酸イソアミル、カプリン
酸エチルの組成含量が実質的に変化せず、コハク酸、乳
酸が20〜60%減少し、リンゴ酸が25〜80%減少
し、Na”イオンが40〜85%減少し、K゛イオン5
0〜95%減少し、トリプトファンが30〜80%減少
し、アルギニンが10〜40%減少し、リジンが5〜3
0%減少し、プトレシン、カダベリンが80〜90%減
少した清酒が特に好ましい例として挙げられる。
本願発明の新規なソフトタイプの清酒を製造するに当た
っては、原清酒をカチオン交換膜およびアニオン交換膜
を有する電気透析処理すればよい。
本願発明で用いられる原清酒は、通常の清酒の製造法に
従って製造され、ろ過されたものが挙げられ、例えば、
米、米麹等を原料として醗酵せしめ、絞りを行ったもの
で、好ましくは−引きや、火入れ、オリ下げを行ったも
のが例示され、さらに、−引きや、火入れ、活性炭処理
、オリ下げ処理等を行ってもよい、i!I常、日本酒度
;−4〜+7、アルコール分(%);14〜20%、総
酸度;1.0〜2.5、アミノ酸度;1.θ〜2.5、
エキス分;2〜8の物性を有するものが多い。
本願に用いられるカチオン交換膜およびアニオン交換膜
を有する電気透析処理とは、少なくとも1枚ずつ以上の
カチオン交換膜およびアニオン交換膜を有するもので、
好ましくは、フィルタープレス型のものであり、カチオ
ン交換膜とアニオン交換膜が対になっているものが例示
される。具体的に説明すると、第1図に示される通り、
電気透析器の中はアニオン交換膜(1)およびカチオン
交換膜(2)により仕切られた原清酒処理室(3)と塩
廃液流路(4および4゛)を交互に配置し、陰極側末端
の塩廃液流路(4)では陰極側に陰極用II (5)に
て陰極およびそれを取り巻く電極液室(7)に仕切られ
ており、同様に、陽極側末端の塩廃液流路(4”)では
陽極側に陽極用1!1(6)にて陽極およびそれを取り
巻く電極液室(7)に仕切られている。第1図の構成の
電気透析器においては、本願の電気透析処理に有効に用
いられる有効膜は、アニオン交換膜(1)およびカチオ
ン交換膜(2)であり、通常、有効膜面積とは、何方か
一方の面積をいう、また、陰極用膜(5)および陽極用
膜(6)は、電極液から原清酒処理室または塩廃液流路
への硝酸イオン等のイオンの移行防止や、電極液中への
原清酒処理室または塩廃液流路からの塩素イオンの移行
防止のため、通常カチオン交換膜が用いられる。原清酒
は、原清酒溜(8)よりポンプにより電気透析器中の原
清酒処理室(3)に導入され、該原清酒処理室から集め
られて導出され、原清酒溜に循環される。
また、塩廃液は、塩廃液溜(9)よりポンプにより電気
透析器中の塩廃液流路(4および4°)に導入され、次
いで該塩廃液流路から集められて導出され、塩廃液溜に
循環される。塩廃液としては通常蒸留水等を用い、電気
透析器外に導出された塩廃液はそのまま捨てるか又は循
環せしめればよい、電気透析処理を行う場合には、上記
電極に通電する。
適当量の電気透析処理が行い得るように原清酒の流量を
調節すればよく、また複数の電気透析器を用いたり、原
清酒を循環して電気透析するとよく、特に装置が簡単で
あることから、原清酒を目的とする組成含量となるまで
循環して電気透析することが好ましい。
カチオン交換膜としては、カチオン性を存するものであ
ればよく、特に限定されないが、好ましくはスチレンジ
ビニルベンゼンコポリマーの担体にスルホン基を導入し
たものが例示される。さらに、分画分子量が約1000
以下であればより好ましい、また、アニオン交換膜とし
ては、アニオン性を有するものであればよく、特に限定
されないが、好ましくはスチレンジビニルベンゼンコポ
リマーの担体に4級アンモニウムを導入したものが例示
される。さらに、分画分子量が約1000以下であれば
より好ましい9以上のカチオン交換膜およびアニオン交
換膜における担体は、カチオン基またはアニオン基を保
持し、且つ分画分子量として1000位以下である担体
であれば適宜選択でき、これらの交換膜を適宜組み合わ
せたアシプレ7クス・カートリッジ<tfL化成社製、
AC−23Qタイプ)が有利に利用できて好ましい。
電気透析処理を行うに際しては、目的とするソフトタイ
プの清酒の組成含量に基づき、適宜の処理条件を選択す
ればよいが、例えばその処理条件としては、電気透析器
の有効膜面積の単位面積当りの電流(を流密度)と時間
の積が、0.03〜30A′sec/cm”程度の範囲
であり、原清酒の処理量と有効膜面積の比が、0.5〜
5mj!/cm”程度の範囲である条件が例示される。
その場合に、処理する原清酒のpHや温度も関係するが
、原清酒のpHは、通常pH4〜4.5程度であること
から特に大きく変化がなければ問題とならない、処理温
度は、電気透析処理やポンプによる循環等により清酒の
温度が上昇し清酒を変質させないように、室温以下であ
って凍結しない温度の範囲で行えば好ましいが、通常5
〜15℃程度が例示される。電圧は、原清酒の質と、そ
の時に流す電流の量に従って決まり、その時の有効膜単
位面積当りの電流(電流密度)が0.05〜5mA /
c m ”程度であるので、適宜の電圧とすればよい
、また、原清酒の流速が遅すぎると部分的な電気分解を
起こし清酒の品質に好ましくないことから、通常は原清
酒の膜面線速を5 Cm / 36(程度以上とするこ
とが好ましい0以上の条件の具体的な処理条件の1例を
示すと、例えば有効膜面積;400cm!の電気透析器
を用い、電圧;9■、電流;0.05A、処理温度;1
0℃、処理pH14,1,流速;300m1/mjn
(10cm / 3eC) 、原清酒処理量;11の条
件で、約15〜約90分間循環し処理する方法が挙げら
れる。
このようにして得られた目的の組成を有するソフトタイ
プの清酒は、そのまま容器に充填するか、または滅菌処
理等の公知の処理を行った後容器に充填すればよい。As a result of intensive research to solve the above-mentioned problems, the present inventors have found that by electrodialyzing sake with a cation-exchange membrane and an anion-exchange membrane, bitterness, astringency, and off-taste are improved. After learning that a softer type of sake can be produced that is different from the standard sake, the present invention was completed. That is, the present invention provides sake content, alcohol (%), extract content, isomaltose, glucose, galactose, glycerin, n-propyl alcohol, isobutyl alcohol, isoamyl alcohol, isoamyl acetate, caproic acid compared to the original sake composition. The compositional content of ethyl remains virtually unchanged, succinic acid, lactic acid, malic acid, Na'' ions,
This is a new soft-type sake characterized by a reduced content of K3 ions, tryptophan, arginine, lysine, putrescine, and cadaverine. The present invention also provides a method for producing soft type sake, or a method for reforming sake, which is characterized by subjecting sake to electrodialysis treatment using a cation exchange membrane and an anion exchange membrane. The novel soft-type sake of the present invention is one in which the specific compositional components described above are reduced compared to the original sake composition, and as a result, it retains the original umami flavor of sake while retaining bitterness and astringency. The result is a new sake with a good balance and improved taste and off-taste.For example, compared to the original sake composition, the sake content, alcohol (%), extract content, isomaltose, and glucose The composition contents of , galactose, glycerin, n-propyl alcohol, isobutyl alcohol, isoamyl alcohol, isoamyl acetate, and ethyl caprate remained virtually unchanged, succinic acid and lactic acid decreased by 20-60%, and malic acid decreased by 25-60%. 80% decrease, Na'' ion decreases by 40-85%, K'' ion 5
0-95% decrease, tryptophan 30-80% decrease, arginine 10-40% decrease, lysine 5-3
Particularly preferred examples include sake in which putrescine and cadaverine are reduced by 80 to 90%. In producing the novel soft-type sake of the present invention, raw sake may be subjected to electrodialysis treatment using a cation exchange membrane and an anion exchange membrane. The raw sake used in the present invention may be one that is produced according to a normal sake manufacturing method and filtered, for example,
Rice, rice malt, etc. are fermented and squeezed as raw materials, and preferred examples include those that have been subjected to -pulling, pasteurization, and straining, and further include -pulling, pasteurization, activated carbon treatment, and straining etc., i! I, Sake level: -4 to +7, Alcohol content (%): 14 to 20%, Total acidity: 1.0 to 2.5, Amino acid level: 1. θ~2.5,
Extract content: Many have physical properties of 2 to 8. The electrodialysis treatment having a cation exchange membrane and an anion exchange membrane used in this application is one having at least one cation exchange membrane and at least one anion exchange membrane,
Preferably, it is a filter press type, and an example is one in which a cation exchange membrane and an anion exchange membrane are paired. To explain specifically, as shown in Figure 1,
Inside the electrodialyzer, the raw sake processing chamber (3) and the salt waste liquid channels (4 and 4゛), which are separated by an anion exchange membrane (1) and a cation exchange membrane (2), are arranged alternately. The salt waste liquid flow path (4) is partitioned into a cathode and the surrounding electrode liquid chamber (7) by a cathode II (5) on the cathode side, and similarly, the salt waste liquid flow path (4) at the end of the anode side is partitioned into a cathode and an electrode liquid chamber (7) surrounding it by a cathode II (5). ”), the anode side is partitioned into an anode and an electrode solution chamber (7) surrounding it by an anode 1!1 (6). The effective membranes that are effectively used for this purpose are the anion exchange membrane (1) and the cation exchange membrane (2), and the effective membrane area usually refers to the area of one of them. The anode membrane (6) prevents the transfer of ions such as nitrate ions from the electrode solution to the raw sake processing chamber or the salt waste liquid flow path, and prevents the transfer of ions such as nitrate ions from the raw sake processing chamber or the salt waste liquid flow path into the electrode solution. A cation exchange membrane is usually used to prevent the migration of raw sake.The raw sake is introduced from the raw sake distiller (8) into the raw sake processing chamber (3) in the electrodialyzer by a pump, and is collected from the raw sake processing chamber. The salt waste liquid is introduced from the salt waste liquid tank (9) into the salt waste liquid flow paths (4 and 4°) in the electrodialyzer by a pump, and then the salt waste liquid is The salt waste liquid is collected and drawn out from the waste liquid channel and circulated to the salt waste liquid reservoir. Distilled water or the like is normally used as the salt waste liquid, and the salt waste liquid drawn out of the electrodialyzer may be discarded as is or circulated. When performing electrodialysis treatment, electricity is applied to the above electrodes.The flow rate of unprocessed sake may be adjusted so that an appropriate amount of electrodialysis treatment can be performed, and multiple electrodialyzers may be used or unprocessed sake may be circulated In particular, since the equipment is simple, it is preferable to perform electrodialysis by circulating the raw sake until the desired composition is reached.As the cation exchange membrane, any membrane that has cationic properties can be used. Although not particularly limited, a preferred example is a styrene divinylbenzene copolymer carrier with a sulfone group introduced therein.
The following is more preferable; the anion exchange membrane is not particularly limited as long as it has anionic properties, but a preferred example is one in which quaternary ammonium is introduced into a styrene divinylbenzene copolymer carrier. . Further, the carrier in the 9 or more cation exchange membrane and anion exchange membrane, which is more preferable if the molecular weight cut off is about 1000 or less, may be a carrier that holds a cationic group or anionic group and has a molecular weight cutoff of 1000 or less. Acipre 7X Cartridge (manufactured by tfL Kasei Co., Ltd.), which combines these exchange membranes as appropriate, can be selected as appropriate.
AC-23Q type) can be advantageously used and is preferred. When performing electrodialysis treatment, appropriate treatment conditions may be selected based on the compositional content of the target soft-type sake. For example, the treatment conditions may include: The product of current (flow density) and time is in the range of about 0.03 to 30 A'sec/cm'', and the ratio of the processing amount of raw sake to the effective membrane area is in the range of 0.5 to 30 A'sec/cm''.
5mj! An example is a condition in the range of 1/cm". In that case, the pH and temperature of the raw sake to be treated are also relevant, but the pH of the raw sake is usually around pH 4 to 4.5, so the condition is particularly large. There is no problem if there is no change; it is preferable to keep the processing temperature below room temperature and at a temperature that does not freeze, so that the temperature of the sake does not increase due to electrodialysis treatment or circulation using a pump and deteriorate the quality of the sake. Usually 5
An example is about 15°C. The voltage is determined according to the quality of the original sake and the amount of current applied at that time, and the current per unit area of the effective membrane (current density) at that time is 0.05 to 5 mA /
cm'', so you can set the voltage appropriately.Also, if the flow rate of the raw sake is too slow, it will cause partial electrolysis, which is unfavorable for the quality of the sake, so the membrane surface line of the raw sake is usually An example of a specific treatment condition where the speed is preferably 0 or more is 5 Cm / 36 (about 5 Cm / 36 or more). For example, using an electrodialyzer with an effective membrane area of 400 cm, and a voltage of 9 Current: 0.05A, processing temperature: 1
0°C, treatment pH 14.1, flow rate: 300ml/mjn
(10cm/3eC), raw sake processing amount; 11 conditions, and a method of circulating for about 15 to about 90 minutes. The soft-type sake having the desired composition thus obtained may be directly filled into containers, or may be filled into containers after being subjected to a known treatment such as sterilization.
次いで本発明の実施例を挙げて本発明を具体的に説明す
るが、本発明は何らこれにより限定されるものではない
。
実施例1
カチオン交換膜およびアニオン交換膜を有する電気透析
処理装置として、卓上脱塩装置(旭化成社製、商品名;
マイクロアシライザー03)を用い、この卓上脱塩装置
にアニオン交換膜(スチレンジビニルベンゼンに4級ア
ンモニウムを導入したもの)とカチオン交換膜(スチレ
ンジビニルベンゼンにスルホン基を導入したもの)を複
数枚交互に配置したカートリッジ型の交換III(旭化
成社製、商品名;AC230−400、有効カチオン交
換膜およびアニオン交換膜を交互に各10枚有するもの
、有効通電膜面積;400cm”)を装着した。
即ち、処理装置の概要は第1図に示される通り、アニオ
ン交換11(1)およびカチオン交換膜(2)により仕
切られた原清酒処理室(3)と塩廃液流路(4および4
°)を交互に配置し、原清酒を原清酒処理室(3)内に
ポンプにて導入せしめ、電気透析処理された後装置外に
導出され、外部の液溜に集められて再度原清酒処理室(
3)内に導入される循環法によった。1回に処理する原
清酒は、11とした。
また、塩廃液流路(4および4°)には蒸留水等を導入
して、循環せしめた。
処理装置の両端の電極に以下の条件にて通電して15.
30分、60分、90分、120分間の各時間、処理し
た〔電圧9v、電流0.05A、流速300mj/m
i n (10cm/sec ) 、温度約lO℃〕。
なお、電気透析処理に供した原清酒は、総米1000g
(揚米840 g、麹米220g)、汲水1320g
、乳酸1.4g、酵母0.5gを三段仕込みにより醗酵
させ、約148目に絞り、次いで−引き、火入れ、おり
下げを行ったものを用いた。この原清酒は、18.5%
(V/V)のアルコール分を含有し、pHは4.1であ
つた。
各処理時間にて処理した清酒の官能評価を行った。また
、−殻成分分析値、有機酸、イオン、糖類、アミノ酸、
アミンの各種組成分析、および香気成分分析を行った。
官能評価の評価方法は、味、香り、総合の項目について
、3段階評価(1点:良い、2点:普通、3点:悪い)
をして、その平均点を算出した。
また、併せてコメントを求め、その標準的なコメントを
記載した。なお、日本酒の味の評価としては、苦味、渋
味、雑味が代表的な表現であり、このうち雑味とは、苦
味、渋味を含めた総合的な味のバランスが日本酒として
取れているか否かに関する表現である。
一般成分分析値の分析法は国税庁所定分析法によった。
即ち、アルコールは蒸留したものをアルコール浮ひょう
計で測定した0日本酒度は、日本酒度浮ひょう計で測定
した。総酸度はブロムチモ−ルブルーとニュートラルレ
ッドの混合指示薬を用い水酸化ナトリウムで滴定するこ
とにより測定した。アミノ酸度は、フェノールフタレイ
ン指示薬と中性ホルマリンを用いて水酸化ナトリウムで
滴定することにより測定した。エキス分は蒸留残渣を蔗
糖変針で測定した。
有機酸、イオン、II類、アミノ酸、アミンの各種組成
の分析は、高速液体クロマトグラフィーで分析した。ま
た香気成分の分析は、ガスクロマトグラフィーで分析し
た。
官能評価の結果は、第1表に示される通り、原・清酒に
わずかながら、苦味、渋味、雑味が感じられたのに対し
、清酒を15分間〜90分間処理した場合には、苦味、
渋味、雑味が感じられず、さっばりしたソフトタイプの
清酒となっていた。なお、120分間処理した清酒にお
いては、水っぽいとの評価であり好ましくはなかったが
、上記のいずれの処理の清酒においても飲酒後の熟柿香
がなかった。また、本発明の電気透析処理においては、
その処理前後において清酒の色は変化しなかった。
第1表
また、−殻成分分析値、有ll酸、イオン、I!類、ア
ミノ酸、アミンおよび香気成分の各分析結果を第2表に
示した。
第2表
試験例
実施例1と同様の方法で60分間の電気透析処理した清
酒と、以下の参考例の清酒を比較した。
参考例;原清酒をアニオン交換樹脂(三菱化成社製、W
A−30)のカラム(IX30cm)に、5V=25の
流速にて通過させ、適当な酸度を存する分画である通液
後1500〜2000ml目の500mj!の分画を用
いた。
その結果は、以下の第3表および第4表に示される遺り
本願の清酒が参考例に示されるアニオン交換樹脂処理の
清酒に比較して、より好ましいものであり、各成分の組
成も相違したものであった。
第3表Next, the present invention will be specifically explained with reference to Examples, but the present invention is not limited thereto in any way. Example 1 A tabletop desalination device (manufactured by Asahi Kasei Co., Ltd., trade name;
Micro Acylyzer 03) is used, and multiple anion exchange membranes (styrene divinylbenzene with quaternary ammonium introduced) and cation exchange membranes (styrene divinylbenzene with sulfone groups introduced) are alternately installed in this tabletop desalination device. A cartridge-type replacement III (manufactured by Asahi Kasei Co., Ltd., product name: AC230-400, having 10 effective cation exchange membranes and 10 anion exchange membranes alternately, effective current-carrying membrane area: 400 cm) was installed. As shown in Figure 1, the outline of the processing equipment consists of a raw sake processing chamber (3) separated by an anion exchange membrane (1) and a cation exchange membrane (2), and a salt waste liquid channel (4 and 4).
°) are arranged alternately, and the unprocessed sake is introduced into the unprocessed sake processing chamber (3) using a pump, and after being subjected to electrodialysis treatment, it is led out of the device, collected in an external reservoir, and processed again under unprocessed sake. Room (
3) by the circulation method introduced within. The number of raw sake processed at one time was 11. In addition, distilled water or the like was introduced into the salt waste liquid channels (4 and 4°) and circulated. 15. Electrify the electrodes at both ends of the processing device under the following conditions.
Treatment was performed for 30 minutes, 60 minutes, 90 minutes, and 120 minutes [voltage 9 V, current 0.05 A, flow rate 300 mj/m
in (10 cm/sec), temperature approximately 10°C]. The raw sake subjected to electrodialysis treatment was 1000g of total rice.
(840 g of fried rice, 220 g of koji rice), 1320 g of water
, 1.4 g of lactic acid, and 0.5 g of yeast were fermented in three stages, squeezed to about 148 mesh, then strained, pasteurized, and drained. This original sake is 18.5%
(V/V) alcohol content, and the pH was 4.1. A sensory evaluation of the sake treated at each treatment time was performed. In addition, - shell component analysis values, organic acids, ions, sugars, amino acids,
Various compositional analyzes of amines and aroma component analyzes were conducted. The sensory evaluation method is a three-level evaluation (1 point: good, 2 points: average, 3 points: bad) for taste, aroma, and overall items.
The average score was calculated. We also asked for comments and listed the standard comments. The typical expressions for evaluating the taste of sake are bitterness, astringency, and miscellaneous taste.Among these, miscellaneous taste is defined as the overall taste balance of sake, including bitterness and astringency. It is an expression regarding whether there is a person or not. The analysis method for general component analysis values was based on the analysis method prescribed by the National Tax Agency. That is, the alcohol was distilled and measured with an alcohol buoyancy meter. Total acidity was measured by titration with sodium hydroxide using a mixed indicator of bromothymol blue and neutral red. Amino acid content was determined by titration with sodium hydroxide using a phenolphthalein indicator and neutral formalin. The extract content was measured from the distillation residue using a sucrose needle. The various compositions of organic acids, ions, class II, amino acids, and amines were analyzed using high performance liquid chromatography. The aroma components were analyzed using gas chromatography. As shown in Table 1, the results of the sensory evaluation showed that the original sake had a slight bitterness, astringency, and off-taste, but when the sake was processed for 15 to 90 minutes, the bitterness was reduced. ,
The sake was light and soft, with no bitterness or off-flavors. The sake treated for 120 minutes was evaluated as watery, which was not preferable, but the sake treated with any of the above treatments had no ripe persimmon aroma after drinking. Furthermore, in the electrodialysis treatment of the present invention,
The color of the sake did not change before and after the treatment. Table 1 also shows - shell component analysis values, llic acids, ions, I! Table 2 shows the analysis results for amino acids, amino acids, amines, and aroma components. Table 2 Test Examples Sake treated with electrodialysis for 60 minutes in the same manner as in Example 1 was compared with sake of the following reference example. Reference example: Raw sake is treated with anion exchange resin (manufactured by Mitsubishi Chemical Corporation, W
A-30) column (IX 30 cm) at a flow rate of 5 V = 25, and the 1500 to 2000 ml fraction after passing, which is a fraction with an appropriate acidity, is 500 mj! fraction was used. The results show that the sake of the present invention shown in Tables 3 and 4 below is more preferable than the sake treated with anion exchange resin shown in the reference example, and the composition of each component is also different. That's what I did. Table 3
本願発明によれば、従来の清酒には見られない苦味、渋
味、雑味の改善されたソフトタイプの清酒が提供できる
ものである。また、本願発明のソフトタイプの清酒は、
清酒独特の山吹色を失わずに有し老ね難い清酒である。
さらに、本願発明のソフトタイプの清酒は、二日酔いし
にくり、飲酒後の熟柿香を伴わないという効果を有する
。
本願発明のソフトタイプの清酒の製造法は、極めて簡単
な処理により従来にないソフトタイプの清酒が提供でき
るものであり、また、処理条件や処理時間を変えること
により簡単に種々のソフトタイプの清酒が提供できるも
のであり、電気透析処理であるため、樹脂等の再生処理
を行う必要がないものである。According to the present invention, it is possible to provide a soft-type sake with improved bitterness, astringency, and off-taste that are not found in conventional sake. In addition, the soft type sake of the present invention is
It is a sake that does not age well without losing its unique golden color. Furthermore, the soft type sake of the present invention has the effect of preventing hangovers and not having a ripe persimmon aroma after drinking. The method for producing soft-type sake of the present invention can provide unprecedented soft-type sake through extremely simple processing, and can easily produce various soft-type sake by changing the processing conditions and processing time. Since it is an electrodialysis treatment, there is no need to perform a regeneration treatment for the resin or the like.
第1図は、本願の電気透析処理装置の概要を示す、(1
)はアニオン交換膜を、(2)はカチオン交換膜を示し
、(3)は原清酒処理室を、(4および4′)は塩廃液
流路を示す。FIG. 1 shows an outline of the electrodialysis treatment apparatus of the present application, (1
) shows the anion exchange membrane, (2) shows the cation exchange membrane, (3) shows the raw sake processing chamber, and (4 and 4') shows the salt waste liquid flow path.
Claims (5)
%)、エキス分、イソマルトース、グルコース、ガラク
トース、グリセリン、n−プロピルアルコール、イソブ
チルアルコール、イソアミルアルコール、酢酸イソアミ
ル、カプロン酸エチルの組成含量が実質的に変化せず、
コハク酸、乳酸、リンゴ酸、Na^+イオン、K^+イ
オン、トリプトファン、アルギニン、リジン、プトレシ
ン、カダベリンの組成含量が減少したことを特徴とする
新規なソフトタイプの清酒。(1) Compared to the original sake composition, sake content, alcohol (
%), extract content, isomaltose, glucose, galactose, glycerin, n-propyl alcohol, isobutyl alcohol, isoamyl alcohol, isoamyl acetate, and ethyl caproate composition contents are not substantially changed,
A novel soft-type sake characterized by reduced compositional contents of succinic acid, lactic acid, malic acid, Na^+ ions, K^+ ions, tryptophan, arginine, lysine, putrescine, and cadaverine.
60%減少し、リンゴ酸が25〜80%減少し、Na^
+イオンが40〜85%減少し、K^+イオンが50〜
95%減少し、トリプトファンが30〜80%減少し、
アルギニンが10〜40%減少し、リジンが5〜30%
減少し、プトレシン、カダベリンが80〜90%減少し
た請求項(1)記載のソフトタイプの清酒。(2) Compared to the original sake composition, succinic acid and lactic acid are 20~
60% reduction, malic acid 25-80% reduction, Na^
+ ions decrease by 40~85%, K^+ ions decrease by 50~
95% reduction, tryptophan 30-80% reduction,
Arginine decreases by 10-40%, lysine by 5-30%
The soft type sake according to claim 1, wherein putrescine and cadaverine are reduced by 80 to 90%.
する電気透析処理することを特徴とするソフトタイプの
清酒の製造法。(3) A method for producing soft sake, which comprises subjecting sake to electrodialysis using a cation exchange membrane and an anion exchange membrane.
約1000以下であり、アニオン交換膜が四級アンモニ
ウム基を有し分画分子量が約1000以下である請求項
(3)記載の製造法。(4) The production according to claim (3), wherein the cation exchange membrane has a sulfone group and a molecular weight cutoff of about 1000 or less, and the anion exchange membrane has a quaternary ammonium group and a molecular weight cutoff of about 1000 or less. Law.
する電気透析処理によりソフトタイプの清酒となす清酒
の改質方法。(5) A method for reforming sake, which produces soft sake by electrodialysis treatment using a cation exchange membrane and an anion exchange membrane.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2262427A JPH06104054B2 (en) | 1990-09-29 | 1990-09-29 | Soft type sake and its manufacturing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2262427A JPH06104054B2 (en) | 1990-09-29 | 1990-09-29 | Soft type sake and its manufacturing method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04141080A true JPH04141080A (en) | 1992-05-14 |
JPH06104054B2 JPH06104054B2 (en) | 1994-12-21 |
Family
ID=17375636
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2262427A Expired - Lifetime JPH06104054B2 (en) | 1990-09-29 | 1990-09-29 | Soft type sake and its manufacturing method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06104054B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000184878A (en) * | 1998-12-19 | 2000-07-04 | Satoru Tabata | Production of liquors and sweet food |
JP2010252788A (en) * | 2009-03-31 | 2010-11-11 | Takara Shuzo Co Ltd | Production method of clear refined sake and clear refined sake |
JP2016195570A (en) * | 2015-04-03 | 2016-11-24 | サントリーホールディングス株式会社 | Bottled alcoholic beverage |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5577885A (en) * | 1978-12-06 | 1980-06-12 | Toshiyuki Oota | Preparation of alcohol-containing drink |
-
1990
- 1990-09-29 JP JP2262427A patent/JPH06104054B2/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5577885A (en) * | 1978-12-06 | 1980-06-12 | Toshiyuki Oota | Preparation of alcohol-containing drink |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000184878A (en) * | 1998-12-19 | 2000-07-04 | Satoru Tabata | Production of liquors and sweet food |
JP2010252788A (en) * | 2009-03-31 | 2010-11-11 | Takara Shuzo Co Ltd | Production method of clear refined sake and clear refined sake |
JP2016195570A (en) * | 2015-04-03 | 2016-11-24 | サントリーホールディングス株式会社 | Bottled alcoholic beverage |
Also Published As
Publication number | Publication date |
---|---|
JPH06104054B2 (en) | 1994-12-21 |
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