WO2009131282A1 - Method for production of beer using unhulledand rice and rice beer thereof - Google Patents
Method for production of beer using unhulledand rice and rice beer thereof Download PDFInfo
- Publication number
- WO2009131282A1 WO2009131282A1 PCT/KR2008/006178 KR2008006178W WO2009131282A1 WO 2009131282 A1 WO2009131282 A1 WO 2009131282A1 KR 2008006178 W KR2008006178 W KR 2008006178W WO 2009131282 A1 WO2009131282 A1 WO 2009131282A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- rice
- wort
- beer
- malt
- produced
- Prior art date
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- 241000209094 Oryza Species 0.000 title claims abstract description 97
- 235000007164 Oryza sativa Nutrition 0.000 title claims abstract description 97
- 235000009566 rice Nutrition 0.000 title claims abstract description 97
- 235000013405 beer Nutrition 0.000 title claims abstract description 69
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 23
- 102000004190 Enzymes Human genes 0.000 claims abstract description 40
- 108090000790 Enzymes Proteins 0.000 claims abstract description 40
- 238000000034 method Methods 0.000 claims abstract description 35
- 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 claims abstract description 31
- 235000008694 Humulus lupulus Nutrition 0.000 claims abstract description 21
- 235000013339 cereals Nutrition 0.000 claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000009835 boiling Methods 0.000 claims abstract description 17
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims abstract description 13
- 238000001914 filtration Methods 0.000 claims abstract description 11
- 239000000463 material Substances 0.000 claims abstract description 11
- 230000000415 inactivating effect Effects 0.000 claims abstract description 5
- 238000000855 fermentation Methods 0.000 claims description 16
- 230000004151 fermentation Effects 0.000 claims description 16
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 11
- 238000007654 immersion Methods 0.000 claims description 3
- 239000002244 precipitate Substances 0.000 claims description 2
- 239000000796 flavoring agent Substances 0.000 abstract description 40
- 235000019634 flavors Nutrition 0.000 abstract description 40
- 244000025221 Humulus lupulus Species 0.000 abstract description 20
- 235000007340 Hordeum vulgare Nutrition 0.000 abstract description 8
- 235000019640 taste Nutrition 0.000 abstract description 7
- 230000001953 sensory effect Effects 0.000 abstract description 4
- 240000005979 Hordeum vulgare Species 0.000 abstract 1
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 18
- 229920002472 Starch Polymers 0.000 description 16
- 235000019698 starch Nutrition 0.000 description 16
- 239000008107 starch Substances 0.000 description 16
- 235000014680 Saccharomyces cerevisiae Nutrition 0.000 description 11
- 235000019441 ethanol Nutrition 0.000 description 10
- 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 description 9
- 230000000052 comparative effect Effects 0.000 description 9
- 239000008103 glucose Substances 0.000 description 9
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 7
- 241000209219 Hordeum Species 0.000 description 7
- LQZZUXJYWNFBMV-UHFFFAOYSA-N dodecan-1-ol Chemical compound CCCCCCCCCCCCO LQZZUXJYWNFBMV-UHFFFAOYSA-N 0.000 description 6
- 239000000706 filtrate Substances 0.000 description 6
- 150000001875 compounds Chemical class 0.000 description 5
- -1 ester compounds Chemical class 0.000 description 5
- 235000015097 nutrients Nutrition 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- 235000014101 wine Nutrition 0.000 description 5
- 230000001476 alcoholic effect Effects 0.000 description 4
- 102000004169 proteins and genes Human genes 0.000 description 4
- 108090000623 proteins and genes Proteins 0.000 description 4
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 3
- 235000019658 bitter taste Nutrition 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 238000004821 distillation Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- PHTQWCKDNZKARW-UHFFFAOYSA-N isoamylol Chemical compound CC(C)CCO PHTQWCKDNZKARW-UHFFFAOYSA-N 0.000 description 3
- 229930186179 lupulin Natural products 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 235000019991 rice wine Nutrition 0.000 description 3
- WRMNZCZEMHIOCP-UHFFFAOYSA-N 2-phenylethanol Chemical compound OCCC1=CC=CC=C1 WRMNZCZEMHIOCP-UHFFFAOYSA-N 0.000 description 2
- FERIUCNNQQJTOY-UHFFFAOYSA-N Butyric acid Chemical compound CCCC(O)=O FERIUCNNQQJTOY-UHFFFAOYSA-N 0.000 description 2
- 241000209140 Triticum Species 0.000 description 2
- 235000021307 Triticum Nutrition 0.000 description 2
- 235000013334 alcoholic beverage Nutrition 0.000 description 2
- 150000001413 amino acids Chemical class 0.000 description 2
- UAHWPYUMFXYFJY-UHFFFAOYSA-N beta-myrcene Chemical compound CC(C)=CCCC(=C)C=C UAHWPYUMFXYFJY-UHFFFAOYSA-N 0.000 description 2
- 150000001720 carbohydrates Chemical class 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000002779 inactivation Effects 0.000 description 2
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 description 2
- 210000001161 mammalian embryo Anatomy 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000035515 penetration Effects 0.000 description 2
- 235000019997 soju Nutrition 0.000 description 2
- 239000011782 vitamin Substances 0.000 description 2
- 235000013343 vitamin Nutrition 0.000 description 2
- 229940088594 vitamin Drugs 0.000 description 2
- 229930003231 vitamin Natural products 0.000 description 2
- IWTBVKIGCDZRPL-LURJTMIESA-N 3-Methylbutanol Natural products CC[C@H](C)CCO IWTBVKIGCDZRPL-LURJTMIESA-N 0.000 description 1
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 241000218235 Cannabaceae Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- DYZCESKLDGNPIY-UHFFFAOYSA-N Humulen Natural products CC1=CCCC(=C)CCC(C)(C)C=C/C1 DYZCESKLDGNPIY-UHFFFAOYSA-N 0.000 description 1
- VZMXLSLKOHIKTQ-UHFFFAOYSA-N Humulon Natural products CC(C)CC(=O)C1=C(O)C(O)(CC=C(C)C)C(=O)C(CC=C(C)C)=C1O VZMXLSLKOHIKTQ-UHFFFAOYSA-N 0.000 description 1
- RMFGNMMNUZWCRZ-UHFFFAOYSA-N Humulone Natural products CC(C)CC(=O)C1=C(O)C(O)(CC=C(C)C)C(O)=C(CC=C(C)C)C1=O RMFGNMMNUZWCRZ-UHFFFAOYSA-N 0.000 description 1
- 241000218228 Humulus Species 0.000 description 1
- OLHLJBVALXTBSQ-UHFFFAOYSA-N Lupulone Natural products CC(C)CC(=O)C1C(=O)C(CC=C(C)C)C(=O)C(CC=C(C)C)(CC=C(C)C)C1=O OLHLJBVALXTBSQ-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 108091005804 Peptidases Proteins 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 239000004365 Protease Substances 0.000 description 1
- 102100037486 Reverse transcriptase/ribonuclease H Human genes 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- 244000042295 Vigna mungo Species 0.000 description 1
- 235000010716 Vigna mungo Nutrition 0.000 description 1
- 235000011453 Vigna umbellata Nutrition 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- VYBREYKSZAROCT-UHFFFAOYSA-N alpha-myrcene Natural products CC(=C)CCCC(=C)C=C VYBREYKSZAROCT-UHFFFAOYSA-N 0.000 description 1
- 230000002421 anti-septic effect Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229940098396 barley grain Drugs 0.000 description 1
- HAVYZKHVTLAPDZ-RCHZWEEESA-N beta-Humulene Natural products C\C1=C\CC(C)(C)\C=C\CC(=C)CCC1 HAVYZKHVTLAPDZ-RCHZWEEESA-N 0.000 description 1
- WPVSVIXDXMNGGN-UHFFFAOYSA-N beta-bitter acid Natural products CC(C)CC(=O)C1=C(O)C(CC=C(C)C)(CC=C(C)C)C(=O)C(CC=C(C)C)=C1O WPVSVIXDXMNGGN-UHFFFAOYSA-N 0.000 description 1
- 230000003115 biocidal effect Effects 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 235000011089 carbon dioxide Nutrition 0.000 description 1
- 239000012159 carrier gas Substances 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000009194 climbing Effects 0.000 description 1
- 235000013325 dietary fiber Nutrition 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000013467 fragmentation Methods 0.000 description 1
- 238000006062 fragmentation reaction Methods 0.000 description 1
- BXWQUXUDAGDUOS-UHFFFAOYSA-N gamma-humulene Natural products CC1=CCCC(C)(C)C=CC(=C)CCC1 BXWQUXUDAGDUOS-UHFFFAOYSA-N 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 238000002290 gas chromatography-mass spectrometry Methods 0.000 description 1
- 230000035784 germination Effects 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 150000004251 humulene derivatives Chemical class 0.000 description 1
- VMSLCPKYRPDHLN-OAQYLSRUSA-N humulone Chemical compound CC(C)CC(=O)C1=C(O)C(CC=C(C)C)=C(O)[C@](O)(CC=C(C)C)C1=O VMSLCPKYRPDHLN-OAQYLSRUSA-N 0.000 description 1
- 239000010903 husk Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000011630 iodine Substances 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- 229940035429 isobutyl alcohol Drugs 0.000 description 1
- CPJRRXSHAYUTGL-UHFFFAOYSA-N isopentenyl alcohol Chemical compound CC(=C)CCO CPJRRXSHAYUTGL-UHFFFAOYSA-N 0.000 description 1
- LSDULPZJLTZEFD-UHFFFAOYSA-N lupulone Chemical compound CC(C)CC(=O)C1=C(O)C(CC=C(C)C)=C(O)C(CC=C(C)C)(CC=C(C)C)C1=O LSDULPZJLTZEFD-UHFFFAOYSA-N 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004949 mass spectrometry Methods 0.000 description 1
- 238000001819 mass spectrum Methods 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229940067107 phenylethyl alcohol Drugs 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 229940100486 rice starch Drugs 0.000 description 1
- 239000000932 sedative agent Substances 0.000 description 1
- 230000001624 sedative effect Effects 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 239000012257 stirred material Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 229920001864 tannin Polymers 0.000 description 1
- 239000001648 tannin Substances 0.000 description 1
- 235000018553 tannin Nutrition 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12C—BEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
- C12C7/00—Preparation of wort
- C12C7/04—Preparation or treatment of the mash
- C12C7/047—Preparation or treatment of the mash part of the mash being unmalted cereal mash
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12C—BEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
- C12C11/00—Fermentation processes for beer
- C12C11/02—Pitching yeast
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12C—BEER; PREPARATION OF BEER BY FERMENTATION; PREPARATION OF MALT FOR MAKING BEER; PREPARATION OF HOPS FOR MAKING BEER
- C12C12/00—Processes specially adapted for making special kinds of beer
Definitions
- the present invention relates to a method for producing a rice beer and a rice beer produced thereby, and more particularly to a method for producing using enzymes released from rice bran and malt without adding a special enzyme and to a rice beer produced thereby which is rich in nutrients.
- Beer is a fermented alcoholic drink which is being widely drunk mainly by young people in Korea. Beer is generally produced by a two-step fermentation process which comprises germinating barley or wheat, saccharifying the starch of barley or wheat into glucose by various enzymes, including saccharifying enzymes produced during the germination, adding hops to the saccharified material, boiling the hopped material to prepare a wort, adding brewer's yeast to the wort to produce alcohol, and aging the alcohol while allowing carbonic acid gas to remain.
- grain alcoholic wines (unrefined rice wine, refined rice wine, clear rice wine, etc.) are conventionally produced with a grain raw material (starchy raw material) using, as a fermenting agent, either nuruk, which is a starter for preparing Korean alcoholic drinks, or koji which is a recently developed improved nuruk.
- the produced grain alcoholic wines are drunk as they are, or distilled to produce distilled liquors (distilled Soju and diluted Soju).
- Korean Patent No. 10-0651266 discloses a technology relating to a beer which targets young people and is prepared by adding rice so as to combine the characteristics of Korean traditional wines with the characteristics of oriental beer.
- the disclosed technology has problems in that, because a special enzyme is added from the outside, a high production cost is required, and in that the rice-derived flavor is not specially added.
- the present invention provides a method for producing a rice beer, the method comprising the sequential steps of: immersing mixed grains of unhulled rice and malt in water at a temperature ranging from 48 0 C to 53 0 C to release saccharifying enzymes; gelatinizing and saccharifying the grains at a temperature ranging from 62 0 C to 68 0 C; inactivating the saccharifying enzymes and filtering the saccharified material to obtain a wort; adding hops to the wort and boiling the hopped wort; and adding yeast to the wort and fermenting the wort.
- the present invention also provides a rice beer produced by the above method for producing the rice beer.
- Step 1 a step of immersing mixed grains of unhulled rice and malt in water at a tem- perature between 48 and 53 0 C to release saccharifying enzymes
- Step 1 is a step of immersing mixed grains of unhulled rice and malt in water at a temperature between 48 and 53 0 C to release saccharifying enzymes.
- unhulled rice is richer in nutrients than polished rice (white rice), and the rice bran comprising the rice embryo comprises about 45% carbohydrate, about 25% dietary fiber, about 16% fat, about 14% protein and a trace amount of vitamins and minerals including calcium, magnesium and phosphorus and contains a large amount of enzymes required for saccharification.
- the present invention is characterized by the use of unhulled rice and has technical characteristics distinguishable from those of some beers produced by adding rice as a sub-material. Specifically, because saccharifying enzymes contained in rice bran perform the gelatinization and saccharification of starch in corporation with saccharifying enzymes contained in malt, the saccharification process in the present invention can be carried out at a temperature lower than those in general beer production methods in which the saccharification process is carried out only using malt. The need to separately add saccharifying enzymes from the outside in order to facilitate saccharification is eliminated. In addition, because unhulled rice is used, components which are not contained in polished rice increase the aroma components of beer, whereby a beer having an excellent flavor can be produced.
- malt is a barley grain obtained by germinating unhulled barley under the action of moisture, heat and oxygen, contains saccharides such as starch, vitamins and various enzymes and imparts the inherent flavor of malt to beer. Malt releases enzymes required for saccharification and various other enzymes to degrade proteins into amino acids and degrades the starch of rice bean into fermentable glucose in corporation with the saccharifying enzymes.
- mixed grains of unhulled rice and malt are immersed in water at a temperature ranging 48 0 C to 53 0 C to release saccharifying enzymes. In this case, the release of enzymes can be efficiently achieved and the activity of protease can increase to produce amino acids showing a nutty taste.
- the content of water is preferably in the range of 500-600 wt% based on the amount of the mixed grains of unhulled rice and malt, but is not limited to a particular range.
- the weight ratio of unhulled rice and malt in the mixed grains is preferably in the range of 45-55 wt% unhulled rice: 55-45 wt% malt, but is not limited to a particular range. If unhulled rice is used in an amount of less than 45 wt%, the flavor of the resulting beer will be poor, and the content is more than 55 wt%, the product characteristics of the resulting beer will not be sufficiently exhibited, the amount of malt added is relatively reduced.
- the immersion time is preferably in the range of 12-18 minutes, but is not limited to a particular range.
- saccharifying enzymes can be economically released from unhulled rice and malt.
- Step 2 a step of gelatinization and saccharification at a temperature of 62 0 C to 68 0 C after immersion
- Step 2 is a step of gelatinizing and saccharifidying the grains at a temperature of 62
- gelatinizing means that water is added to a starch consisting of dense particles and the temperature of the starch is increased to swell the starch, thus creating the space between the particles and forming the colloidal state.
- the penetration of enzymes into gelatinized starch can be more easily achieved compared to the penetration into raw starch to increase the availability of the starch, whereby the starch can be easily converted into fermentable glucose.
- gelatinization and saccharification processes are carried out at a temperature lower than a gelatinization temperature of about 70 0 C which is applied in the prior art method for producing beer.
- saccharifying enzymes are present in a sufficient amount, because they are derived from not only malt, but also rice.
- the saccharification process is carried out by a special step of lowering the temperature of the grains.
- the gelatinization process is carried out at a temperature of 62 0 C to 68 0 C which is lower than the conventional gelatinization temperature, and thus a separate saccarification process is not additionally designed and the saccharification process can be carried out at the gelatinization temperature.
- the gelatinization process can be carried out at a low temperature as described above, the volatility of flavor components can be reduced, so that the flavor components can be captured in a relatively large amount.
- the time of gelatinization and saccharification is preferably in the range of 100-140 minutes, but is not limited to a particular range. In this case, the gelatinization and saccharification process is carried out in a cost-effective way.
- fermentable glucose refers to a glucose which can be used by yeast in a metabolic process.
- yeast intakes fermentable glucose to produce the alcohol and carbon dioxide required for beer.
- Step 3 a step of inactivating saccharifying enzymes and filtering the saccharified material after gelatinization and saccharification
- Step 3 is a step of inactivating saccharifying enzymes and filtering the saccharified material after gelatinization and saccharification.
- the inactivation of the saccharifying enzymes is preferably carried out at a temperature of 72 0 C to 78 0 C for 10 minutes to 20 minutes, but the inactivation conditions are not limited to particular conditions.
- the shells of unhulled rice and malt are removed through filtration, and thus the precipitation of impurities during the production of beer can be prevented.
- the filtration process is preferably carried out by transferring the wort, in which the saccharifying enzymes have been inactivated, into a filter tank, and then allowing the transferred wort to stand in the filter tank.
- the filtration process is preferably carried out until a clear filter is obtained.
- Step 4 a step of adding hops to the filtered wort and boiling the wort
- Step 4 is a step of adding hops to the filtered wort and boiling the wort.
- the wort In the boiling process, the wort is concentrated, while the bitter components and aroma of hops are leached, coagulable proteins or tannic materials are deposited, and the activity of enzymes is inactivated.
- Hops humulus lupulus, L which are used in the present invention are a perennial dioecious climbing plant belonging to the family Cannabinaceae and are used as a material for beer. Hops include lupulin comprising humulen, myrcene, humulon, lupulon, a hop resin, etc. Lupulin in hops functions to cause its unique flavor and bitter taste which impart a distinctive flavor and pleasant bitter taste to beer and exhibit antibiotic, sedative and antiseptic effects, thus increasing the storage stability of beer.
- the tannins contained in hops function to impart a bitter taste to beer in the same manner as lupulin and are balanced by the good taste of barley, and therefore, act to decrease a greasy feeling when taken along with greasy food.
- bitter hops are added to the filtrate which is then boiled for 60-120 minutes in order to sufficiently impart the aroma and taste of bitter hops to beer.
- aroma hops are preferably added at 10-20 minutes before the end of boiling.
- the sugar content of the wort is preferably in the range of 11 to 12 Brix, but is not limited to a particular range.
- the inventive method for producing the rice beer preferably additionally comprises, after the boiling step, a step of removing the precipitate.
- Step 5 a step of adding yeast and fermenting the wort after boiling
- Step 5 is a step of adding yeast and fermenting the wort after boiling.
- Yeast grows and propagates using fermentable glucose contained in the wort while producing the alcohol and carbon dioxide required for the production of beer.
- a method for carrying out the fermentation of the wort preferably comprises the steps of primarily fermenting the wort at a temperature of 12-18 0 C for 6-8 days to an alcohol content of 3-4%; and secondarily fermenting the wort at 0-2 0 C for 2-3 weeks to an alcohol content of 4-5%, but is not limited to a particular method.
- alcohol and carbon dioxide are suitably blended, thus producing a beer having an excellent flavor.
- the present invention provides a rice beer produced according to the above method for producing the rice beer.
- the rice beer of the present invention is produced using unhulled rice as a main raw material and has a high rice content, it combines the inherent flavor of rice bran with the nutty taste of white rice and the flavor of hops and barley, and thus has excellent sensory characteristics.
- unhulled rice is added such that saccharifying enzymes can be released from rice bran, thus increasing usable saccharifying enzymes.
- the gelatinization and saccharification of starch can be performed at the same time, and the saccharification process can be carried out at a relatively low temperature.
- the rice beer of the present invention is produced using unhulled rice as a main raw material, it is richer in nutrients than polished white rice.
- the rice beer of the present invention has excellent sensory characteristics, because the inherent flavor of rice bran, the nutty taste of white rice and the flavor of hops and barley are harmonized with each other. Best Mode for Carrying out the Invention
- Each of unhulled rice and malt was crushed, and 2 kg of the crushed unhulled rice was mixed with 2 kg of the crushed malt.
- 22 L of brewing water corresponding to about 5.5 times the amount of the mixed grains of the crushed unhulled rice and the crushed malt was added to a brewing tank and heated to 53 0 C.
- 4 kg of the mixture of the crushed unhulled rice and the crushed malt was added to the brewing water, and the temperature of the brewing water was maintained at 50 0 C for 15 minutes to release enzymes required for saccharification.
- the temperature of the brewing water was increased to 65 0 C.
- the starch of the unhulled rice was gelatinized for about 120 minutes, while a saccharification process of converting rice starch and malt starch into fermentable glucose was carried out.
- an iodine test was carried out to check the degree of saccharification. Then, the saccharified material was heated to 75 0 C, and the saccharifying enzymes were inactivated, thus stopping the saccharification process.
- the obtained mash was transferred into a filtration tank, in which the mash was allowed to stand and a filter layer was produced using husks.
- the turbid filtrate was returned to the filtration tank and filtered therein, until a clear filtrate was obtained.
- the clear filtrate was obtained, it was transferred into a boiling tank and boiled therein at about 100 0 C for 90 minutes.
- the filtrate reached a temperature of 95 0 C or above, it started to boil, and at this time, 4 g of bitter hops were added.
- 4.5 g of aroma hops were added.
- the sugar content of the wort was 12 Brix, and the boiled wort was allowed to stand for a given period of time. Then, the sludge including coagulated proteins was removed by precipitation for 15 minutes using centrifugation (a whirlpool process). After completion of the precipitation process, the wort was cooled to 18 0 C using a heat exchanger and transferred into a fermentation tank. When about half of the wort was transferred into the fermentation tank, previously activated yeast was introduced into the fermentation tank.
- the activated yeast was obtained by adding 40 g of dry yeast to water and activating it at 24 0 C for 24 hours. After the wort was completely transferred into the fermentation tank, it was primarily fermented for 1 week while maintaining the temperature of the fermentation tank at 15 0 C. During the primary fermentation period, the pressure of gas in the fermentation tank was maintained at about 1.5-2 psi, and after completion of the primary fermentation, the beer had an alcohol content of about 4%. After completion of the primary fermentation, the temperature of the fermentation tank was lowered to 1 0C and maintained at that temperature for 1 day, and then the yeast was removed. Then, the wort was secondarily fermented while maintaining the temperature of the fermentation tank at 1 0 C. The secondary fermentation was carried out for 2 weeks, and after completion of the secondary fermentation, the beer had an alcohol content of 4.5%. Mode for the Invention
- a beer was produced using white rice in the same manner as in Example 1, except that white rice was used instead of unhulled rice (the mixing ratio of white rice to malt was 50:50).
- Test Example 1 Analysis of flavor components of beer
- the stirred material was separated into a dichloromethane layer and a water layer using a separatory funnel, and sodium sulfate was added to the separated dichloromethane layer. Then, the dichloromethane layer was stored in a refrigerator at 5 0 C for 12 hours to remove the remaining water.
- a vigorous column was connected, and the sample was concentrated to a volume of 1 ml at 50 0 C, and then concentrated to 0.4 ml by charging nitrogen gas.
- the analysis of the separated flavor components was performed using GC-MS. In the
- GC analysis a DB-wax was used, the injector temperature was maintained at 250 0 C, the oven temperature was maintained at 50 0 C for 2 minutes, elevated to 200 0 C at a rate of 3 °C/min, and then maintained at 250 0 C for 10 minutes, helium was used as a carrier gas, and the 1 ⁇ Jl of the sample was injected in the splitless mode.
- the MS analysis for the identification of the flavor components was performed in the following conditions: MS ionization voltage: 70 eV; source temperature: 280 0 C, and mass spectrum range: 50-550 m/z.
- the flavor components were identified by comparing authentic compounds with the Kovats gas chromatographic retention index I, and then comparing the mass spectrometry fragmentation pattern (Willy 6th edition MS spectra library) of each component with those of authentic components.
- the amount of the flavor components was expressed as the ratio of the peak area of each component to the peak area of 1-dodecanol used as the internal standard.
- Alcohols including phenyl ethyl alcohol, isoamyl alcohol and isobutyl alcohol, ester compounds, including ethyl acetate, and organic acids, including butanoic acid, which are the characteristic flavor components of beer, were detected in the produced beers, and the contents of most of these components were higher in Example 1 than in Comparative Examples 1 and 2.
- lactone compounds including -hexalactone, -nonalactone and -decalactone
- flavor components including 1-butanol, 3-methyl-but-3-en-l-ol and 3-methylbutanol, which were not detected in Comparative Example 1, and many compounds and flavor components which were not detected in Comparative Example 2, were detected in Example 1.
- unhulled rice is added such that saccharifying enzymes can be released from rice bran, thus increasing usable saccharifying enzymes.
- the gelatinization and saccharification of starch can be performed at the same time, and the saccharification process can be carried out at a relatively low temperature.
- the rice beer of the present invention is produced using unhulled rice as a main raw material, it is richer in nutrients than polished white rice.
- the rice beer of the present invention has excellent sensory characteristics, because it combines the inherent flavor of rice bran with the nutty taste of white rice and the flavor of hops and barley.
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Abstract
The present invention relates to a method for producing a rice beer and a rice beer produced thereby, the method comprising the steps of: immersing mixed grains of unhulled rice and malt in water at a temperature ranging from 48 0C to 53 0C to release saccharifying enzymes; gelatinizing and saccharifying the grains at a temperature ranging from 62 0C to 68 0C inactivating the saccharifying enzymes and filtering the saccharified material to obtain a wort; adding hops to the wort and boiling the hopped wort; and adding yeast to the wort and fermenting the wort. In the method, the rice beer can be produced without using a special enzyme, and thus the production cost can be reduced and the content of rice in the rice beer can be increased. The produced rice beer combines the inherent flavor of rice bran with the nutty taste of white rice and the flavor of hops and barley, and thus has excellent sensory characteristics.
Description
Description
METHOD FOR PRODUCTION OF BEER USING UN- HULLED AND RICE AND RICE BEER THEREOF
Technical Field
[1] The present invention relates to a method for producing a rice beer and a rice beer produced thereby, and more particularly to a method for producing using enzymes released from rice bran and malt without adding a special enzyme and to a rice beer produced thereby which is rich in nutrients. Background Art
[2] Beer is a fermented alcoholic drink which is being widely drunk mainly by young people in Korea. Beer is generally produced by a two-step fermentation process which comprises germinating barley or wheat, saccharifying the starch of barley or wheat into glucose by various enzymes, including saccharifying enzymes produced during the germination, adding hops to the saccharified material, boiling the hopped material to prepare a wort, adding brewer's yeast to the wort to produce alcohol, and aging the alcohol while allowing carbonic acid gas to remain.
[3] Meanwhile, in the production of oriental alcoholic wines excluding compounded alcoholic wines, grain alcoholic wines (unrefined rice wine, refined rice wine, clear rice wine, etc.) are conventionally produced with a grain raw material (starchy raw material) using, as a fermenting agent, either nuruk, which is a starter for preparing Korean alcoholic drinks, or koji which is a recently developed improved nuruk. The produced grain alcoholic wines are drunk as they are, or distilled to produce distilled liquors (distilled Soju and diluted Soju).
[4] Meanwhile, Korean Patent No. 10-0651266 discloses a technology relating to a beer which targets young people and is prepared by adding rice so as to combine the characteristics of Korean traditional wines with the characteristics of oriental beer. The disclosed technology has problems in that, because a special enzyme is added from the outside, a high production cost is required, and in that the rice-derived flavor is not specially added.
Disclosure of Invention
Technical Problem
[5] It is, therefore, an object of the present invention to provide a production method enabling a rice beer having an excellent flavor to be produced without adding a special enzyme and a rice beer produced thereby. Technical Solution
[6] To achieve the above object, the present invention provides a method for producing a
rice beer, the method comprising the sequential steps of: immersing mixed grains of unhulled rice and malt in water at a temperature ranging from 48 0C to 53 0C to release saccharifying enzymes; gelatinizing and saccharifying the grains at a temperature ranging from 62 0C to 68 0C; inactivating the saccharifying enzymes and filtering the saccharified material to obtain a wort; adding hops to the wort and boiling the hopped wort; and adding yeast to the wort and fermenting the wort.
[7] The present invention also provides a rice beer produced by the above method for producing the rice beer.
[8]
[9] Hereinafter, each step of the production method according to the present invention will be described in detail.
[10] Step 1 : a step of immersing mixed grains of unhulled rice and malt in water at a tem- perature between 48 and 53 0C to release saccharifying enzymes
[11] Step 1 is a step of immersing mixed grains of unhulled rice and malt in water at a temperature between 48 and 53 0C to release saccharifying enzymes.
[12] The distribution of nutrients in unhulled rice is about 66% in the rice embryo, about
29% in the rice bran and about 5% in white rice. Thus, unhulled rice is richer in nutrients than polished rice (white rice), and the rice bran comprising the rice embryo comprises about 45% carbohydrate, about 25% dietary fiber, about 16% fat, about 14% protein and a trace amount of vitamins and minerals including calcium, magnesium and phosphorus and contains a large amount of enzymes required for saccharification.
[13] The present invention is characterized by the use of unhulled rice and has technical characteristics distinguishable from those of some beers produced by adding rice as a sub-material. Specifically, because saccharifying enzymes contained in rice bran perform the gelatinization and saccharification of starch in corporation with saccharifying enzymes contained in malt, the saccharification process in the present invention can be carried out at a temperature lower than those in general beer production methods in which the saccharification process is carried out only using malt. The need to separately add saccharifying enzymes from the outside in order to facilitate saccharification is eliminated. In addition, because unhulled rice is used, components which are not contained in polished rice increase the aroma components of beer, whereby a beer having an excellent flavor can be produced.
[14] Meanwhile, malt is a barley grain obtained by germinating unhulled barley under the action of moisture, heat and oxygen, contains saccharides such as starch, vitamins and various enzymes and imparts the inherent flavor of malt to beer. Malt releases enzymes required for saccharification and various other enzymes to degrade proteins into amino acids and degrades the starch of rice bean into fermentable glucose in corporation with the saccharifying enzymes.
[15] Meanwhile, in the present invention, mixed grains of unhulled rice and malt are immersed in water at a temperature ranging 48 0C to 53 0C to release saccharifying enzymes. In this case, the release of enzymes can be efficiently achieved and the activity of protease can increase to produce amino acids showing a nutty taste.
[16] Meanwhile, the content of water is preferably in the range of 500-600 wt% based on the amount of the mixed grains of unhulled rice and malt, but is not limited to a particular range.
[17] Meanwhile, the weight ratio of unhulled rice and malt in the mixed grains is preferably in the range of 45-55 wt% unhulled rice: 55-45 wt% malt, but is not limited to a particular range. If unhulled rice is used in an amount of less than 45 wt%, the flavor of the resulting beer will be poor, and the content is more than 55 wt%, the product characteristics of the resulting beer will not be sufficiently exhibited, the amount of malt added is relatively reduced.
[18] Meanwhile, the immersion time is preferably in the range of 12-18 minutes, but is not limited to a particular range. In this case, saccharifying enzymes can be economically released from unhulled rice and malt.
[19]
[20] Step 2: a step of gelatinization and saccharification at a temperature of 62 0C to 68 0C after immersion
[21] Step 2 is a step of gelatinizing and saccharifidying the grains at a temperature of 62
0C to 68 0C.
[22] As used herein, the term "gelatinizing" means that water is added to a starch consisting of dense particles and the temperature of the starch is increased to swell the starch, thus creating the space between the particles and forming the colloidal state. In the present invention, the penetration of enzymes into gelatinized starch can be more easily achieved compared to the penetration into raw starch to increase the availability of the starch, whereby the starch can be easily converted into fermentable glucose.
[23] Meanwhile, in the present invention, gelatinization and saccharification processes are carried out at a temperature lower than a gelatinization temperature of about 70 0C which is applied in the prior art method for producing beer. In this case, saccharifying enzymes are present in a sufficient amount, because they are derived from not only malt, but also rice.
[24] Also, after the gelatinization process, the saccharification process is carried out by a special step of lowering the temperature of the grains. In the present invention, the gelatinization process is carried out at a temperature of 62 0C to 68 0C which is lower than the conventional gelatinization temperature, and thus a separate saccarification process is not additionally designed and the saccharification process can be carried out at the gelatinization temperature.
[25] Also, because the gelatinization process can be carried out at a low temperature as described above, the volatility of flavor components can be reduced, so that the flavor components can be captured in a relatively large amount.
[26] Meanwhile, the time of gelatinization and saccharification is preferably in the range of 100-140 minutes, but is not limited to a particular range. In this case, the gelatinization and saccharification process is carried out in a cost-effective way.
[27] Meanwhile, starch is converted into fermentable glucose through the saccharification process, and as used herein, the term "fermentable glucose" refers to a glucose which can be used by yeast in a metabolic process. In the present invention, yeast intakes fermentable glucose to produce the alcohol and carbon dioxide required for beer.
[28]
[29] Step 3: a step of inactivating saccharifying enzymes and filtering the saccharified material after gelatinization and saccharification
[30] Step 3 is a step of inactivating saccharifying enzymes and filtering the saccharified material after gelatinization and saccharification. The inactivation of the saccharifying enzymes is preferably carried out at a temperature of 72 0C to 78 0C for 10 minutes to 20 minutes, but the inactivation conditions are not limited to particular conditions.
[31] Meanwhile, in the present invention, the shells of unhulled rice and malt are removed through filtration, and thus the precipitation of impurities during the production of beer can be prevented. In this case, the filtration process is preferably carried out by transferring the wort, in which the saccharifying enzymes have been inactivated, into a filter tank, and then allowing the transferred wort to stand in the filter tank. The filtration process is preferably carried out until a clear filter is obtained.
[32]
[33] Step 4: a step of adding hops to the filtered wort and boiling the wort
[34] Step 4 is a step of adding hops to the filtered wort and boiling the wort. In the boiling process, the wort is concentrated, while the bitter components and aroma of hops are leached, coagulable proteins or tannic materials are deposited, and the activity of enzymes is inactivated.
[35] Hops (humulus lupulus, L) which are used in the present invention are a perennial dioecious climbing plant belonging to the family Cannabinaceae and are used as a material for beer. Hops include lupulin comprising humulen, myrcene, humulon, lupulon, a hop resin, etc. Lupulin in hops functions to cause its unique flavor and bitter taste which impart a distinctive flavor and pleasant bitter taste to beer and exhibit antibiotic, sedative and antiseptic effects, thus increasing the storage stability of beer. Furthermore, the tannins contained in hops function to impart a bitter taste to beer in the same manner as lupulin and are balanced by the good taste of barley, and therefore, act to decrease a greasy feeling when taken along with greasy food.
[36] Meanwhile, in the present invention, when the filtrate starts to boil, bitter hops are added to the filtrate which is then boiled for 60-120 minutes in order to sufficiently impart the aroma and taste of bitter hops to beer. Also, aroma hops are preferably added at 10-20 minutes before the end of boiling.
[37] Meanwhile, after completion of the boiling process, the sugar content of the wort is preferably in the range of 11 to 12 Brix, but is not limited to a particular range.
[38] Meanwhile, the inventive method for producing the rice beer preferably additionally comprises, after the boiling step, a step of removing the precipitate.
[39]
[40] Step 5: a step of adding yeast and fermenting the wort after boiling
[41] Step 5 is a step of adding yeast and fermenting the wort after boiling.
[42] Yeast grows and propagates using fermentable glucose contained in the wort while producing the alcohol and carbon dioxide required for the production of beer.
[43] Meanwhile, a method for carrying out the fermentation of the wort preferably comprises the steps of primarily fermenting the wort at a temperature of 12-18 0C for 6-8 days to an alcohol content of 3-4%; and secondarily fermenting the wort at 0-2 0C for 2-3 weeks to an alcohol content of 4-5%, but is not limited to a particular method. In this case, alcohol and carbon dioxide are suitably blended, thus producing a beer having an excellent flavor.
[44] Meanwhile, the present invention provides a rice beer produced according to the above method for producing the rice beer.
[45] Because the rice beer of the present invention is produced using unhulled rice as a main raw material and has a high rice content, it combines the inherent flavor of rice bran with the nutty taste of white rice and the flavor of hops and barley, and thus has excellent sensory characteristics.
Advantageous Effects
[46] As described above, in the inventive method for producing the rice beer, unhulled rice is added such that saccharifying enzymes can be released from rice bran, thus increasing usable saccharifying enzymes. Thus, the gelatinization and saccharification of starch can be performed at the same time, and the saccharification process can be carried out at a relatively low temperature. Also, because the rice beer of the present invention is produced using unhulled rice as a main raw material, it is richer in nutrients than polished white rice. In addition, the rice beer of the present invention has excellent sensory characteristics, because the inherent flavor of rice bran, the nutty taste of white rice and the flavor of hops and barley are harmonized with each other. Best Mode for Carrying out the Invention
[47] Hereinafter, the present invention will be described in further detail with reference to
the following examples. However, the scope of the present invention is not limited only to these examples and encompasses the modification of technical ideas equivalent to the examples.
[48]
[49] Example 1: Production of beer using unhulled rice (unhulled rice: malt= 50:50)
[50] Each of unhulled rice and malt was crushed, and 2 kg of the crushed unhulled rice was mixed with 2 kg of the crushed malt. 22 L of brewing water corresponding to about 5.5 times the amount of the mixed grains of the crushed unhulled rice and the crushed malt was added to a brewing tank and heated to 53 0C. Then, 4 kg of the mixture of the crushed unhulled rice and the crushed malt was added to the brewing water, and the temperature of the brewing water was maintained at 50 0C for 15 minutes to release enzymes required for saccharification.
[51] After the enzymes were released, the temperature of the brewing water was increased to 65 0C. At that temperature, the starch of the unhulled rice was gelatinized for about 120 minutes, while a saccharification process of converting rice starch and malt starch into fermentable glucose was carried out. After the saccharification was carried out, an iodine test was carried out to check the degree of saccharification. Then, the saccharified material was heated to 75 0C, and the saccharifying enzymes were inactivated, thus stopping the saccharification process.
[52] The obtained mash was transferred into a filtration tank, in which the mash was allowed to stand and a filter layer was produced using husks. In the filtration process, the turbid filtrate was returned to the filtration tank and filtered therein, until a clear filtrate was obtained. After the clear filtrate was obtained, it was transferred into a boiling tank and boiled therein at about 100 0C for 90 minutes. When the filtrate reached a temperature of 95 0C or above, it started to boil, and at this time, 4 g of bitter hops were added. At 15 minutes before the end of the boiling, 4.5 g of aroma hops were added. After completion of the boiling process, the sugar content of the wort was 12 Brix, and the boiled wort was allowed to stand for a given period of time. Then, the sludge including coagulated proteins was removed by precipitation for 15 minutes using centrifugation (a whirlpool process). After completion of the precipitation process, the wort was cooled to 18 0C using a heat exchanger and transferred into a fermentation tank. When about half of the wort was transferred into the fermentation tank, previously activated yeast was introduced into the fermentation tank.
[53] The activated yeast was obtained by adding 40 g of dry yeast to water and activating it at 24 0C for 24 hours. After the wort was completely transferred into the fermentation tank, it was primarily fermented for 1 week while maintaining the temperature of the fermentation tank at 15 0C. During the primary fermentation period, the pressure of gas in the fermentation tank was maintained at about 1.5-2 psi, and after completion of the
primary fermentation, the beer had an alcohol content of about 4%. After completion of the primary fermentation, the temperature of the fermentation tank was lowered to 1 0C and maintained at that temperature for 1 day, and then the yeast was removed. Then, the wort was secondarily fermented while maintaining the temperature of the fermentation tank at 1 0C. The secondary fermentation was carried out for 2 weeks, and after completion of the secondary fermentation, the beer had an alcohol content of 4.5%. Mode for the Invention
[54] Comparative Example 2: Production of beer using rice (white rice: malt= 50:50s)
[55] A beer was produced using white rice in the same manner as in Example 1, except that white rice was used instead of unhulled rice (the mixing ratio of white rice to malt was 50:50).
[56]
[57] Test Example 1 : Analysis of flavor components of beer
[58] The flavor components of the beers produced in Example 1 and Comparative
Examples 1 and 2 were analyzed.
[59] The extraction of flavor components from the beers was performed using a solvent- assisted flavor evaporation (SAFE) apparatus. 1-dodecanol was used as an internal standard, and 400 μJl of 1-dodecanol was diluted in 2 ml of dichloromethane as a solvent. 5 jΛ of the internal standard dilution was added to 100 ml of the beer sample to be analyzed, and flavor components were extracted from the beer sample using the SAFE apparatus.
[60] The internal pressure of the SAFE apparatus was reduced, and the prepared beer sample was placed in a distillation flask and heated to 45 0C in a water bath. When the beer sample was heated under reduced pressure, the flavor components were distilled, and the distilled components were cooled and captured by a flask opposite to the distillation flask, whereas the non-volatile components remained in the distillation flask. The cooled and captured flavor components were dissolved at room temperature, and then transferred into an Erlenmeyer flask together with 50 ml of dichloromethane and stirred for 1 hour so as to be absorbed into dichloromethane. The stirred material was separated into a dichloromethane layer and a water layer using a separatory funnel, and sodium sulfate was added to the separated dichloromethane layer. Then, the dichloromethane layer was stored in a refrigerator at 5 0C for 12 hours to remove the remaining water. To the flask from which water has been removed and which contained the sample, a vigorous column was connected, and the sample was concentrated to a volume of 1 ml at 50 0C, and then concentrated to 0.4 ml by charging nitrogen gas.
[61] The analysis of the separated flavor components was performed using GC-MS. In the
GC analysis, a DB-wax was used, the injector temperature was maintained at 250 0C, the oven temperature was maintained at 50 0C for 2 minutes, elevated to 200 0C at a rate of 3 °C/min, and then maintained at 250 0C for 10 minutes, helium was used as a carrier gas, and the 1 μJl of the sample was injected in the splitless mode.
[62] The MS analysis for the identification of the flavor components was performed in the following conditions: MS ionization voltage: 70 eV; source temperature: 280 0C, and mass spectrum range: 50-550 m/z. The flavor components were identified by comparing authentic compounds with the Kovats gas chromatographic retention index I, and then comparing the mass spectrometry fragmentation pattern (Willy 6th edition MS spectra library) of each component with those of authentic components.
[63] The amount of the flavor components was expressed as the ratio of the peak area of each component to the peak area of 1-dodecanol used as the internal standard.
[64] Table 1
[65] *Peak area of each compound/Peak area of Internal standard [66] The flavor components of the rice beer produced using mixed grains of unhulled rice: malt= 50:50 (Example 1).
[67] Table 2
[68] *Peak area of each compound/peak area of internal standard [69] The flavor components of beer containing no rice (general beer: Comparative Example 1).
[70] Table 3
[Table 3] [Table ]
[71] *Peak area of each compound/peak area of internal standard [72] The flavor components of the beer produced using mixed grains of malt: rice=50:50 (Comparative Example X).
[73] [74] As can be seen in Tables above, the results of analyzing the flavor components of the beers showed that, in Example 1 (Table 1), 34 flavor components were analyzed,
whereas in Comparative Example (Table 2), 30 flavor components were analyzed, and in Comparative Example 2 (Table 3), 22 flavor components were analyzed.
[75] Alcohols, including phenyl ethyl alcohol, isoamyl alcohol and isobutyl alcohol, ester compounds, including ethyl acetate, and organic acids, including butanoic acid, which are the characteristic flavor components of beer, were detected in the produced beers, and the contents of most of these components were higher in Example 1 than in Comparative Examples 1 and 2.
[76] Also, lactone compounds, including -hexalactone, -nonalactone and -decalactone, and flavor components, including 1-butanol, 3-methyl-but-3-en-l-ol and 3-methylbutanol, which were not detected in Comparative Example 1, and many compounds and flavor components which were not detected in Comparative Example 2, were detected in Example 1.
[77] The above results revealed that the rice beer produced by the inventive method for producing the rice beer contains increased flavor components, and thus is rich in aroma. Industrial Applicability
[78] According to the inventive method for preparing a rice beer, unhulled rice is added such that saccharifying enzymes can be released from rice bran, thus increasing usable saccharifying enzymes. Thus, the gelatinization and saccharification of starch can be performed at the same time, and the saccharification process can be carried out at a relatively low temperature. Also, because the rice beer of the present invention is produced using unhulled rice as a main raw material, it is richer in nutrients than polished white rice. In addition, the rice beer of the present invention has excellent sensory characteristics, because it combines the inherent flavor of rice bran with the nutty taste of white rice and the flavor of hops and barley.
Claims
[1] A method for producing a rice beer, the method comprising the sequential steps of: immersing mixed grains of unhulled rice and malt in water at a temperature ranging from 48 0C to 53 0C to release saccharifying enzymes; gelatinizing and saccharifying the grains at a temperature ranging from 62 0C to
68 0C; inactivating the saccharifying enzymes and filtering the saccharified material to obtain a wort; adding hops to the wort and boiling the hopped wort; and adding yeast to the wort and fermenting the wort.
[2] The method of Claim 1, wherein water is used in an amount of 500-600 wt% based on the weight of the mixed grains of unhulled rice and malt.
[3] The method of Claim 1, wherein the weight ratio of unhulled rice and malt in the mixed grains is 45-55: 55:45.
[4] The method of Claim 1, wherein the immersion step is carried out for 12-18 minutes.
[5] The gelatinization and saccharification step is carried out for 100-140 minutes.
[6] The method of Claim 1, wherein the sugar content of the wort after the boiling step is 11-12 Brix. [7] The method of Claim 1, wherein the method additionally comprises, after the boiling step, a step of removing a precipitate. [8] The method of Claim 1, wherein the fermentation step comprises the sequential sub-steps of: primarily fermenting the wort at 12 0C to 18 0C for 6 to 8 days to an alcohol content of 3 to 4%; and secondarily fermenting the wort at 0 0C to 2 0C for 2 to 3 weeks to an alcohol content of 4 to 5%. [9] A rice beer produced according to the method of Claim 1.
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- 2008-04-23 KR KR1020080037734A patent/KR101002740B1/en active IP Right Grant
- 2008-11-25 WO PCT/KR2008/006178 patent/WO2009131282A1/en active Application Filing
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Cited By (8)
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ITTV20100057A1 (en) * | 2010-04-06 | 2011-10-07 | Anis Srl M | PROCEDURE FOR BEER PRODUCTION |
CN103087862A (en) * | 2013-02-04 | 2013-05-08 | 王珍奎 | Alcohol-taste fermented beverage and preparation method thereof |
CN104109591A (en) * | 2014-05-23 | 2014-10-22 | 刘凯 | Chinese magnoliavine fruit beer brewing method |
CN104109591B (en) * | 2014-05-23 | 2016-11-16 | 麒麟啤酒(珠海)有限公司 | A kind of Fructus Schisandrae Chinensis beer-brewing method |
CN106661523A (en) * | 2014-07-11 | 2017-05-10 | 朝日啤酒株式会社 | Beer-like beverage |
CN112280628A (en) * | 2019-07-22 | 2021-01-29 | 中山医学大学 | Method for producing litchi flower beer |
CN115637203A (en) * | 2022-11-14 | 2023-01-24 | 深圳市云达亿科科技有限公司 | Rice fat millet white beer and preparation method thereof |
JP7303364B1 (en) * | 2022-12-26 | 2023-07-04 | アサヒビール株式会社 | beer-taste beverages |
Also Published As
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KR20090112057A (en) | 2009-10-28 |
KR101002740B1 (en) | 2010-12-21 |
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