LV13003B - Method for processing vodka - Google Patents

Method for processing vodka Download PDF

Info

Publication number
LV13003B
LV13003B LVP-02-179A LV020179A LV13003B LV 13003 B LV13003 B LV 13003B LV 020179 A LV020179 A LV 020179A LV 13003 B LV13003 B LV 13003B
Authority
LV
Latvia
Prior art keywords
water
vodka
solution
carbon
alcohol
Prior art date
Application number
LVP-02-179A
Other languages
English (en)
Inventor
Jurijs Seflers
Original Assignee
Spirits Product Internat Intel
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Spirits Product Internat Intel filed Critical Spirits Product Internat Intel
Priority to LVP-02-179A priority Critical patent/LV13003B/lv
Priority to UAA200504159U priority patent/UA58609U/ru
Publication of LV13003B publication Critical patent/LV13003B/lv
Priority to MXPA05003492A priority patent/MXPA05003492A/es
Priority to PT03759064T priority patent/PT1549734E/pt
Priority to PCT/NL2003/000676 priority patent/WO2004031341A1/en
Priority to DE60319553T priority patent/DE60319553T2/de
Priority to DK03759064T priority patent/DK1549734T3/da
Priority to UAU201014290U priority patent/UA62593U/ru
Priority to ES03759064T priority patent/ES2302944T3/es
Priority to NZ539616A priority patent/NZ539616A/en
Priority to EA200500586A priority patent/EA007803B9/ru
Priority to AT03759064T priority patent/ATE388220T1/de
Priority to AU2003274813A priority patent/AU2003274813B2/en
Priority to EP03759064A priority patent/EP1549734B1/en
Priority to KR1020057005843A priority patent/KR20050074960A/ko
Priority to CA2500983A priority patent/CA2500983C/en
Priority to BRPI0315022-4A priority patent/BR0315022B1/pt
Priority to US10/530,202 priority patent/US20060134302A1/en
Priority to CNB2003801009427A priority patent/CN100415865C/zh
Priority to JP2004541336A priority patent/JP4494208B2/ja
Priority to NO20052151A priority patent/NO331332B1/no
Priority to HK06100307A priority patent/HK1082759A1/xx
Priority to ZA200503409A priority patent/ZA200503409B/en
Priority to CY20081100490T priority patent/CY1107940T1/el

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12HPASTEURISATION, STERILISATION, PRESERVATION, PURIFICATION, CLARIFICATION OR AGEING OF ALCOHOLIC BEVERAGES; METHODS FOR ALTERING THE ALCOHOL CONTENT OF FERMENTED SOLUTIONS OR ALCOHOLIC BEVERAGES
    • C12H6/00Methods for increasing the alcohol content of fermented solutions or alcoholic beverages
    • C12H6/02Methods for increasing the alcohol content of fermented solutions or alcoholic beverages by distillation
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12GWINE; PREPARATION THEREOF; ALCOHOLIC BEVERAGES; PREPARATION OF ALCOHOLIC BEVERAGES NOT PROVIDED FOR IN SUBCLASSES C12C OR C12H
    • C12G3/00Preparation of other alcoholic beverages
    • C12G3/04Preparation of other alcoholic beverages by mixing, e.g. for preparation of liqueurs
    • C12G3/06Preparation of other alcoholic beverages by mixing, e.g. for preparation of liqueurs with flavouring ingredients
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12GWINE; PREPARATION THEREOF; ALCOHOLIC BEVERAGES; PREPARATION OF ALCOHOLIC BEVERAGES NOT PROVIDED FOR IN SUBCLASSES C12C OR C12H
    • C12G3/00Preparation of other alcoholic beverages
    • C12G3/02Preparation of other alcoholic beverages by fermentation
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12HPASTEURISATION, STERILISATION, PRESERVATION, PURIFICATION, CLARIFICATION OR AGEING OF ALCOHOLIC BEVERAGES; METHODS FOR ALTERING THE ALCOHOL CONTENT OF FERMENTED SOLUTIONS OR ALCOHOLIC BEVERAGES
    • C12H1/00Pasteurisation, sterilisation, preservation, purification, clarification, or ageing of alcoholic beverages
    • C12H1/02Pasteurisation, sterilisation, preservation, purification, clarification, or ageing of alcoholic beverages combined with removal of precipitate or added materials, e.g. adsorption material
    • C12H1/04Pasteurisation, sterilisation, preservation, purification, clarification, or ageing of alcoholic beverages combined with removal of precipitate or added materials, e.g. adsorption material with the aid of ion-exchange material or inert clarification material, e.g. adsorption material
    • C12H1/0408Pasteurisation, sterilisation, preservation, purification, clarification, or ageing of alcoholic beverages combined with removal of precipitate or added materials, e.g. adsorption material with the aid of ion-exchange material or inert clarification material, e.g. adsorption material with the aid of inorganic added material

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Zoology (AREA)
  • Food Science & Technology (AREA)
  • Inorganic Chemistry (AREA)
  • Alcoholic Beverages (AREA)
  • Adornments (AREA)
  • Preparation Of Fruits And Vegetables (AREA)
  • Medicines Containing Plant Substances (AREA)
  • Seasonings (AREA)
  • Compounds Of Unknown Constitution (AREA)
  • Confectionery (AREA)
  • Seeds, Soups, And Other Foods (AREA)
  • Forging (AREA)
  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
  • Medicinal Preparation (AREA)
  • Crystals, And After-Treatments Of Crystals (AREA)
  • Detergent Compositions (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Description

LV 13003 CIIOCOE nPOH3BOACTBA BOflKH.
IlpefljiaraeMoe H3o6pereHHe othochtcs k jiHKepo-BOflOHHofi npOMbUDJieHHOCTH, B HaCTHOCTH, K Cn0C06aM ΠΟϋγΗβΗΗΛ BOAKH. B HacToamee βρβΜκ ιπΗροκο H3BecreH cnoco6 npoH3BOACTBa boakh nyreM nocjieAOeaTejibHoro cMeniHBaHHH boaho-ciihptoboh hchakocth c caxapHUM CHpOnOM H pa3JIHHHbIMH CHHTCTmeCKHMH Βρ0ΜΒΤΗ33Χ0ρΒΜΗ flJlH MaCKHpOBKH CHBjnnHoro 3anaxa cnHpTa h nocjie,nyioineH <ļ>HJibTpauHH CMecH. («Peuemypbi jiHKepo-BOflOHHbK h3A6Jihh h BOflOK» - M., Jlencan npoMhimjieHHOCTb, 1981).
TaKOH cnoco6 «κπβτοηηο TexHOJiornHecKH npocr, οαηβκο boakb, nojiyHeHHaa 3thm ciioco6om, HMeer HeAoeraroHHo bucokhc opraHOJieirniHecKHe noKa3aTejiH. Caxap oceaaer Ha noBepxHOCTH aKTHBHpoBaHHoro yrjix, hto nomoKaer ero aKTHBHOCTb h aQCop6uHOHHyio cnoco6Hoen>. BcjieflcrBHH aroro creneHb φΐϋΙΒΤρ3Ι1ΗΗ CMeCH CHHX(a6TCB Η B ΓΟΤΟΒΟΗ ΒΟβΚβ OmymaiOTCfl OCTaTOHHbie ΤΟΗ3 CHByuiHbix Mācēji. KpoMe τογο, BOAKa nojiyHeHHaa H3BecTHbiM cnocoOoM, HMeer CHjībHbifi ocrpbiH 3anax BBeaeHHOFO apoMaTH3aropa, hto npHAaer HanHTKy HeecTecTBeHHhiH «CHHTeTHHecKHit» 3anax. ApoMairoaTop c TenemieM BpeMeHH h «yjieryHHBaeTCB» h cooTBercTBeHHO b 3anaxe h Bicyce ycHjiHBaiOTCH cnHpTOBbie HOTbi. KpoMe τογο, Taicaa boakb HMeer ο6μηημη opAHHapHbifi eicyc h HeAOCTaTOHHO BbicoKHe opraHOjienTHHecKHe noKa3arejiH.
HjBecTeH TaioKe cnocoG npoH3BOACTea boakh nyreM nojiyHeHHB boaho-CnHpTOBOH MCHflKOCTH, $HJIbTpaUHH, 0Μβ1ΠΗΒ3ΗΗΗ BOAHO-CIIHpTOBOH HCHAKOCTH C caxapHbiM CHponoM h oerajībHbiMH κομποηθηταμη penenTypbi, b κοτοροΜ nOJiyHeHHyiO BOAHO-CnHpTOByiO HCHAKOCTb φΗΛΒΓργίΟΤ B KOJIOHHe c aKTHBHpOBaHHbIM JTJieM, Η B ΠΟΛ)ΤΗβΗΗ)ΠΟ OHHmeHHyiO BOAHO-CnHpTOByiO ACHAKOCTb bboabt caxapHbin CHpon h Apyrne HHipHAHeHTbi peuerrrypbi, nepeMeuiHeaiOT, BbmepacHBaiOT ao ΑΟοτιοκβΗΗΗ γομογθηηοογη η φκπΒτρ^αοτ nepeA P03JIHB0M (ΐΚΙΤβΗΤ Pocchh 2171281).
OpraHOAeiiTHHecKHe noKa3aTejiH stoh boakh Bbirne, neM y boakh, nojiyHeHHOh npeAbiAymHM cnocoSoM. B to xce epeMH, CHByuiHbie Macjia, coAepjKamnecB b βοαηο-οπηρτοβοη jkhakocth, Taicace o6pa3yioT Ha noBepxHOCTH aKTHBHpOBaHHOrO ynw nJieHKy, HTO npHBOAHT K yAAHHeHHK) ΤβΧΗΟΑΟΓΗΗβΟΚΟΓΟ -2- UHKJia, Τ.Κ. ΗβΟβχΟΛΗΜΟ CHHACaTb CKOpOCTb nOTOKa MCHAKOCTH Ηβρβ3 KOJIOHHy. CHHHCeHHe CKOpOCTH φHJIbTpa^HH πρΗΒΟΛΗΤ, ΟΟΟΤΒβΤΟΤΒβΗΗΟ, κ yxyfliueHHK) KanecTBa boakh. Iļejibio HacToamero Η3θβρβτβΗΗΗ HBJiaeTca yjiynmeHHe opraHOJienTHHecwHx noKa3aTejien boakh. B cooTBercTBHH c H3o6pereHHeM, b cnoco6e npOH3BOACTBa boakh nyreM nOJiyH6HHH BOflHO-enHpTOBOfi HCHflKOCTH, ee 06pa60TKH aKTHBHpOBaHHbIM yrjieM, φΗ,ΠΚΓρΕΙ-ΙΗΗ, CMeiUHBEHHH BOAHO-CnHpTOBOH 5KHAKOCTH C CaxapHbIM CHpOHOM H OCTajībHbIMH ΚΟΜΠΟΗΘΗΤΒΜΗ peiļemypbl, BOAHO-CnHpTOByK> IKHAKOCTb nocjie o6pa6oTKH βκτηβηροβοηηβιμ yrjieM oxnaacAaiOT ao TeMnepaTypw -10° -15° C, πρκ κοτοροΗ CMecb BbmepjKHBaiOT b TeneHHH 4-8 nacoB, a 3βτβΜ πρκ stoh TeMnepaType φΗΛΒτργιοτ, nocjie nero ee nepeKanHBaioT b eMKoerb jjnn bmacpackh ao AOCTHaceHHa TeMnepaiypbi 18 0 - 25 0 C, πρκ κοτοροϋ bboaht ocnuibHbie HHrpHflHeHTbi peijeinypbi h bhobL·, HenocpeACTBeHHO nepeA ρο3ληβομ, φιυκτργιοτ.
Cnoco6 OTjiHHaercH Taoce τβΜ, hto BO«y ajih boaho-ciihptoboh hchakocth nojiyHaiOT CMemHeaHHeM yMaraeHHOH boam h boam, o6pa6oraHHOH μθτοαομ o6paTHoro ocMOca, ηορμαπη30ββηηοη no noKa3aTejno mejiOHHocrH b npeAenax 2-3
Mr-3KB./jIHTp,
Cnoco6 OTjiHHaerca Taxace τθμ, ητο βοαηο-οπηρτοβυκ) 5κηακοοπ> o6pa6aTbmaiOT ακτηβηροβαηηημ yrjieM Ha yrojibHOH κολοηκθ co CKOpocrbio Φηακγρβηηη 40-50 Aan/nac.
Cnoco6 OTjiHMaerca TaioKe τθμ, hto oxnajKAeHHyio BOflHO-cnHpTOBjao MCHAKOCTb φΗΛΒΤρ)ΤΟΤ Ηβρβ3 Z-Kap60HOBbIH φΚΑΒΤρ.
Cnoco6 OTAHMaerca Taicace τβΜ, ητο φιυ^τρΒΗΗΐο boakh nepeA po3jihbom BeflyT nocAeAOBaTenbHO nepe3 paA ΜΗκροφΗΑΗτροΒ.
Cnoco6 ocymecTBjMerca cAeAyiomHM o6pa30M: JļjlX ΠρΗΓΟΤΟΒΛβΗΗΒ BOAbI flJM BOAHO-CnHpTOBOH 5KHAKOCTH ΓΟΤΟΒΗΤ CMeCb yMameHHOH boah h boam, o6pa6oTaHHoS μθτοαομ ofipaTHoro ocMOca HopMajiH30BaHHOH no noKa3aTejno meAOMHOCTH b npe,aejiax 2-3 mt-3kb./jihtp. 3aTeM nojīyneHHyK) BOAy CMeinneaiOT c 3thjiobhm cnnpTOM, nocae nero nojiyHeHHyio BOAHO-cnHpTOByio hchakoctb nponycKaK)T nepe3 yroAbHyio KOJiOHKy c aKTHBHpOBaHHbIM ynieM co CKopocn>io Φηαβτρβηηη 40-50 Aan/nac. 06pa6oTaHHyio CMecb HanpaBjiaioT b Terui0H30AHp0BaHHbiH oxjiaflHTeAb aah oxjiaacAeHHa ao -100 - 15 0 C, a 3aTeM πρκ stoh TeMneparype nepeKanneaioT b TenAopH30AHpoBaHHyio eMKOCTb, ΓΑβ BbmepacHBaiOT b TeneHHH 4-8 nacoB. Oxjia>KAēHHyK) CMecb nocae BbiAepacKH φιυΐΒτρ)τοτ nepe3 Z-Kap6oHOBbiH φκΑκτρ η nepeKanneaiOT b He TeimoH30AHpoBaHHyio eMKOCTb ffjw «0TAbixa» ao nocreneHHoro noBbimeHHa TeMnepaTypbi ao 18 0 -25 ° C. B nojiyneHHyio BOAHO-cnHproByio acHAKOCTb bboaht CaxapHbIH cnpon H, npH Heo6xOAHMOCTH, OCTaAbHbie ΚΟΜΠΟΗβΗΤΜ Κ0ΜΠ03ΗΙΙΗΗ H apoMaTHbifi οπκρτ. IlepeA po3ahbom nojiyHeHHyio BOAKy nocjieAOBareAbHo φΗΑΒΤρ)ΤΟΤ nepe3 paA ΜΗΚροφΗΛΜρΟΒ. Πρκ rny6oKOM ojuiaacAeHHH ao TeMneparypM -10 ° -15 0 C 3HanHTeabH0 yBejiHHHBaercH πλοτηοοπ» βοαηο-οπηρτοβοη hchakocth, πρκ 3tom Ha creHKax oxAaAHTeaa o6pa3yerca τοηκαη KpHCTanaHnecKaa naeHica, npeACTaBJiHKHAaa coGoh -3 - -3 - LV 13003 CMecb anbAerHAOB, cHBymHbix Mācēji h MeraHOJia. OHJībTpauHa npn TaKofi hh3koh TeMnepairype no3BOJwer eme JiyHine οηηογηπ» BOflHO-cnHpTOBjno 5κηακοοπ>, He pa3pymaa MOJieKyjwpHyio CHCTeMy Boaa - οπκρτ, o6pa30BaBinyioca πρκ OXJia}ĶQ6HHH ΒΟβΗΟ-ΟΠίφΤΟΒΟΗ 5KHAK0CTH. 3tOH HCe UeJIH CJiy>KHT Η ΠΟΟΤβΠβΗΗΟβ ecrecTBeHHoe HarpeeaHHe cMecH nocne φιυη>τρΒΗΗΗ c cooTBerrcTByiomeH Bbiflep)KKpoH.
Hnace npHBOflHTca npHMep κοΗκρβτΗΟΗ pecjumuHH cnoco6a. JĻlX πρΗΓΟΤΟΒΛβΗΗΒ BOflKH «CTOJIHHHaJI 3JIHT» HCnOJIb3yiOT CnHpT «JIlOKC», a BO«y nojiyHaiOT, CMeiDHBaa yMarHeHHyio BOfly c boaoh, npeABapirrejibHO o6pa6oTaHHofi cnocoSoM o6paTHoro ocMoca, H0pMajiH30BaHH0H no noKa3aTejno mejKrmocTH h npeaejiax 2-3 mt-skb./jihtp. B Kyna>KHOH cmkocth ομ&πηββιοτ οπηρτ h BOsy H3 paenera noji^eHH» CM6CH KpenocTbio 40%, nocjie nero CMecb nponycKaK)T nepe3 KOJiOHKy c aKTHBHpOBEHHblM JTJieM CO CKOpOCTbK) <ļ)HJIbTp31ļHH 40-50 flaJlAiaC.
Qnļ)HJibTpoBaHHyK) ΒΟΑΗο-οπΗρτοΒγκ» acHflKocrb nponycKaiOT nepe3 TenjiooOMeHHHK, noHHacaa ee TeMnepaTypy ao -100 -15 0 C, oxnaHweHHyio CMecb BbmepaCHBaiOT B TeiIJIOH30JIHpOBaHHOH eMKOCTH B ΤβΗβΗΗΗ 4-8 HaCOB B 3aBHCHMOCTH OT CKOpOCTH 06pa30BaHHB KpHCTajUIHHeCKOH IUieHKH Ha CTeHKaX eMKOCTH. OxjiaHcqeHHyK> BbiAepacaHHjAO CMecb φκ.ιπ>τρ5Αθτ nepe3 Z-Kap6oHOBbiS φιυπ>τρ, npH 3tom TeMnepaTypa CMecn noBbimaerca Ha 6-10 0 C, nojiyHeHHwfi φκπΒτρΕτ nepeKaHHBaiOT b HeH30jiHpoBaHHyio eMKoerb ajih «OTAbixa» ao nocTeneHHoro aocthjkchhh κομηετήοη TeMnepaiypbi 18 ° -25 °C.B nojiyHeHHyio BOAHO-CnHpTOByK> HCHAKOCTb BBOAHT 65,8% CaxapHbIH CHpon Η, ΙφΗ Heo6xOAHMOCTH, OCTaJIbHbie ΚΟΜΠΟΗΘΗΤΜ ΚΟΜΠ03ΗΙ1ΗΗ Η ΕρΟΜΒΤΗΜΗ CnHpT. riOJiyHeHHyiO ΚΟΜΠ03ΗΙ1ΗΙΟ ΒΜΟΤΑΗΒΕΪΟΤ Β ΤβΗβΗΗΗ 1-5 HECOB, a 3areM, nepeA po3JiHBOM, nojiyHeHHyio BOAKy nocjieAoeaTejibHO φΗΛκτρ^ηοτ Ha pane ΜΗΚροφΗΠΚΤρΟΒ Η ρ33ΛΗΒΕΚ)Τ. _rgTogappAKa HMeer caeiivK)mHgjTO|ca3aņgjiHi_
Kpenocrb (% 06) 40,0 Βηθιπηηη bha ITp03paHHaH, 6ecHBerHaa acHAKOCTb c 6jicckom
Bxyc Μηγκηη, rapMOHHHHbiH c OKpyraeHHbiMH
BOAOHHbIMH HOTEMH
ApOMaT BoAOHHbm 6e3 npHMecH 3anaxa CHByuiHbix Mācēji
AerycrnmHOHHbiH 6ajui nojiyHeHHOH boakh cocTaBtui 9,8. īlpeAJiaraeMbiH cnoco6 πο3βοληλ nojiyHHTb BOjjKy c ynyHiiieHHbiMH opraHOJienTHHecKHMH noica3aTejuiMH. -4- -4- LV 13003
OopMyjia ικοβρετβιιιιη 1. Cnoco6 npOH3BO«CTBa ΒΟΛΚΗ nyreM nOJiyHeHHH BOflHO-enHpTOBOH 5kh^kocth, ee o6pa6oTKH βκτηβηροββηηημ γτηβΜ, φιυΐΒτρ3ΐΐΗΗ, CMCUI HBaHHH ΒΟΑΗΟ-αΐΗρΤΟΒΟΗ MCHflKOCTH C CaxapHbIM ΟΗρΟΠΟΜ H rocTajībHbiMH κομποηθητεμη peuemypbi, oToneTCn τβΜ, hto BOflHO-cnHproByio acHjiKOCTb nocjie o6pa6oTKH βκτηβηροββηηημ yrjieM oxjia*AaioT ρ,ο TeMnepaiypbi -10 0 -15 0 C, πρκ κοτοροϋ CMecH BbmepjKHBaioT b τβπβΗΗΗ 4-8 HacoB, a 3areM npn otoh TeMnepaType φιυπ>τργκ)τ, nocjie nero nepeicaHHBaiOT b eMKoerb ajih BbmepacKH no AOcniaceHHa TeMnepaTypbi 18° - 25 0 C, πρκ κοτοροκ ββοαητ ocrajībHbie HHrpeAHeHTU Κ0ΜΠ03ΗΙ1ΗΗ H BHOBb, ΗβΠΟβρβΑβΤΒβΗΗΟ ΠβρβΛ p03JIHB0M, φΗΒΒΤρΤΙΟΤ.
2. Cnoeo6 ΠΟΠ.1, OTJIHHaiOII|HHC)I ΤβΜ, HTO BOfly nsa. BOflHO-CriHpTOBOH HCHflKOCTH nOJiyHaiOT CMeUIHBaHHeM γΜΒΓΗβΗΗΟΗ BOAbI H BOflbi, o6pa6oTaHHOH mctoaom oOpaTHoro ocMoca, HopMajuooBaHHOH no noKa3aTejno hicjiohhocth b npenejiax 2 -3 μγ-3κβ/λητρ. 3. Cnoeo6 ΠΟΠ. 1, OTJIHHaiOUHHCJI ΤβΜ, HTO BOflHO-CnHpTOByiO acHAKOCTb o6pa6aTbiBaiOT βκτηβηροββηηημ yrjieM Ha yrojibHOH κοηοΗκβ co cKopocTbio φΗΛκτρβηΗΗ 40-50 flaji/nac. 4. Cnoeo6 ΠΟ Π.1, OTJIHHaiOUHHCH ΤβΜ, HTO OXJia*neHHyiO BOflHO-CnHpTOByiO iKHAKOCTb φϋΠΒΤργίΟΤ Ηβρβ3 Z-Kap60HOBMH φΗΠΒΤρ. 5. Cnoco6 no n.l, OTjiHHaionļHHca τβΜ, hto φκίΐΒτρβηΗΐο boakh nepen p03JIHBOM Benyr Ηβρβ3 pan ΜΗκροφιυπ>τρθΒ. -5- -5- LV 13003
Cnoeo6 npOH3BOACTBa BOAKH Ρφρβτ IIpeAJiaraeMoe H3po6pereHHe othochtch k jiHKepo-BOflOHHofi npOMblUIJieHHOCTH, B HaCTHOCTH, K CnOCOOaM nOJiyqeHHB BOAKH. B cooTBeTCTBHH c H3o6pereHHeM, b cnoco6e nporaBoncTBa boakh nyreM ΠΟΛγΗβΗΗΒ BOAHO-enHprOBOH 5KHAK0CTH, ββ o6pa60TKH aKTHBHpOBaHHbIM γΤΆβΜ, φΗΛΜρ3ΑΗΗ, CMeiUHBaHH» BOAHO-CnHpTOBOH 3KHAKOCTH C CaxapHbIM ΟΗρΟΠΟΜ H ocTajībHbiMH KOMnoHeirraMH peuemypbi, BOAHO-cnHpTOByio ηοϊακοοπ» nocjie o6pa6oTKH aKTHBHpOBaHHbIM yrjieM oxna)KAaK>T ao TeMnepaTypw -100 -150 C, npH κοτοροΗ BbmepMCHBaioT b TeneHHH 4-8 nacoB, a 3aTeM npn 3toh TeMnepaType φιοκτργιοτ, nocjie nero ee nepeKanneaiOT b eMKOCTb ajm BHAepaacH ao AOCTH»ceHHH TeMnepaiypbi 18 0 - 25 ° C, πρκ κοτοροκ bboaht ocTanbHbie HHrpHAHeHTbl, H BHOBb, ΗβΠΟΟρβΑΟΤΒβΗΗΟ ΠβρβΑ pO3JIHB0M, φκΑΜργίΟΤ.
CnOCoG OTAHHaeTCB TaiOKe ΤβΜ, HTO BOAy AAS ΒΟΑΗΟ-ΟΠΗρΟΤΟΒΟΗ MCHAKOCTH nOJiyHaiOT CMeiUHBaHHeM γΜΗΓΗβΗΗΟΗ BOAbI H BOAbI, 06pa60TaHH0H MerOAOM o6paTHoro ocMOca, HopMajiH30BaHeHofi no noKasarejiio inejiOHHOCTH b npeaenax 2-3 MT-3KB./jIHip.
Cnoco6 OTjiHHaerca TaioKe τβΜ, hto BOAHO-cnHpTOByio ηιηακοοπ» o6pa6aTbiBaiOT βκτηβηροββηημμ yrjieM Ha yrojibHofi koaohkc co CKopocrbio φιυΐΒτρΒΑΗΗ 40-50 Aan/nac.
Cnoco6 oTJiHHaercH TaioKe τβΜ, hto οχικοκΑβΗΗγιο BOAHO-cnHpTOByio JKHAKOCTb φΗΛΚΤργίΟΤ Hepe3 Z-Kap60H0BbIH φΐ£ΙΠ>τρ.
Cnoco6 OTAHHaerca Tairace τβΜ, hto φιυη>τρΒΑΗΚ) boakh nepen po3jihbom ΒβΑγτ nocjieAOBareAbHO nepe3 paA Μκκροφιυπ>τροΒ. riHpeAJiaraeMbiH cnoco6 πο3βοαηλ nojiyHHTb βοακυ c yjiyHineHHbiMH opraHOJierrrHHecKHMH noicaaaTejiaMH.

Claims (5)

  1. LV 13003 IZGUDROJUMA FORMULA 1. Degvīna ražošanas paņēmiens, iegūstot ūdens-spirta šķidrumu, to apstrādājot ar aktivētu ogli, filtrējot, samaisot ūdens-spirta šķidrumu ar cukura sīrupu un pārējiem receptūras komponentiem, atšķiras ar to, ka ūdens-spirta šķidrumu pēc apstrādes ar aktivēto ogli atdzesē līdz -10° - -15° C temperatūrai, pie kuras maisījumu iztur 4-8 stundas, pēc tam pie šīs temperatūras filtrē, pēc tam pārsūknē tilpnē izturēšanai līdz 18° - 25°C temperatūras sasniegšanai, pie kuras ievada pārējos kompozīcijas ingredientus un vēlreiz, tieši pirms liešanas pudelēs, filtrē.
  2. 2. Paņēmiens pēc p. 1 atšķiras ar to, ka ūdeni priekš ūdens-spirta šķidruma iegūst sajaucot mīkstinātu ūdeni un ūdeni, kas apstrādāts ar apgrieztās osmozes metodi, normalizēts pēc sārmainuma rādītāja robežās 2-3 mg-ekv./litrā.
  3. 3. Paņēmiens pēc p. 1 atšķiras ar to, ka ūdens-spirta šķidrumu apstrādā ar aktivētu ogli ogles kolonā ar filtrēšanas ātrumu 40-50 dl/h.
  4. 4. Paņēmiens pēc p. 1 atšķiras ar to, ka atdzesēto ūdens-spirta šķidrumu filtrē caur “Z-carbon” filtru.
  5. 5. Paņēmiens pēc p. 1 atšķiras ar to, ka degvīna filtrēšanu pirms izliešanas pudelēs veic caur vairākiem mikrofiltriem.
LVP-02-179A 2002-10-03 2002-10-03 Method for processing vodka LV13003B (en)

Priority Applications (24)

Application Number Priority Date Filing Date Title
LVP-02-179A LV13003B (en) 2002-10-03 2002-10-03 Method for processing vodka
UAA200504159U UA58609U (ru) 2002-10-03 2003-03-10 Способ приготовления водки
JP2004541336A JP4494208B2 (ja) 2002-10-03 2003-10-03 ウォッカおよびウォッカの製造方法
EA200500586A EA007803B9 (ru) 2002-10-03 2003-10-03 Водка и способ получения водки
EP03759064A EP1549734B1 (en) 2002-10-03 2003-10-03 Vodka and a process for the production of vodka
PCT/NL2003/000676 WO2004031341A1 (en) 2002-10-03 2003-10-03 Vodka and a process for the production of vodka
DE60319553T DE60319553T2 (de) 2002-10-03 2003-10-03 Wodka und verfahren zur herstellung von wodka
DK03759064T DK1549734T3 (da) 2002-10-03 2003-10-03 Vodka og fremstillingsmåde til fremstilling af vodka
UAU201014290U UA62593U (en) 2002-10-03 2003-10-03 Vodka
ES03759064T ES2302944T3 (es) 2002-10-03 2003-10-03 Vodka y un procedimiento para la produccion de vodka.
NZ539616A NZ539616A (en) 2002-10-03 2003-10-03 Vodka and a process for the production of vodka
MXPA05003492A MXPA05003492A (es) 2002-10-03 2003-10-03 Vodka y un proceso para la produccion de vodka.
AT03759064T ATE388220T1 (de) 2002-10-03 2003-10-03 Wodka und verfahren zur herstellung von wodka
AU2003274813A AU2003274813B2 (en) 2002-10-03 2003-10-03 Vodka and a process for the production of vodka
PT03759064T PT1549734E (pt) 2002-10-03 2003-10-03 Vodca e um processo para a produção de vodca
KR1020057005843A KR20050074960A (ko) 2002-10-03 2003-10-03 보드카 및 보드카 제조 공정
CA2500983A CA2500983C (en) 2002-10-03 2003-10-03 Vodka and a process for the production of vodka
BRPI0315022-4A BR0315022B1 (pt) 2002-10-03 2003-10-03 Processo para preparar vodca e vodca
US10/530,202 US20060134302A1 (en) 2002-10-03 2003-10-03 Vodka and a process for the production of vodka
CNB2003801009427A CN100415865C (zh) 2002-10-03 2003-10-03 伏特加酒以及生产伏特加酒的方法
NO20052151A NO331332B1 (no) 2002-10-03 2005-05-02 Vodka samt fremgangsmate for fremstilling derav.
HK06100307A HK1082759A1 (en) 2002-10-03 2006-01-06 Vodka and a process for the production of vodka
ZA200503409A ZA200503409B (en) 2002-10-03 2006-01-24 Vodka and a process for the production of vodka
CY20081100490T CY1107940T1 (el) 2002-10-03 2008-05-09 Βοτκα και μεθοδος παρασκευης βοτκας

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
LVP-02-179A LV13003B (en) 2002-10-03 2002-10-03 Method for processing vodka

Publications (1)

Publication Number Publication Date
LV13003B true LV13003B (en) 2003-07-20

Family

ID=32064990

Family Applications (1)

Application Number Title Priority Date Filing Date
LVP-02-179A LV13003B (en) 2002-10-03 2002-10-03 Method for processing vodka

Country Status (23)

Country Link
US (1) US20060134302A1 (lv)
EP (1) EP1549734B1 (lv)
JP (1) JP4494208B2 (lv)
KR (1) KR20050074960A (lv)
CN (1) CN100415865C (lv)
AT (1) ATE388220T1 (lv)
AU (1) AU2003274813B2 (lv)
BR (1) BR0315022B1 (lv)
CA (1) CA2500983C (lv)
CY (1) CY1107940T1 (lv)
DE (1) DE60319553T2 (lv)
DK (1) DK1549734T3 (lv)
EA (1) EA007803B9 (lv)
ES (1) ES2302944T3 (lv)
HK (1) HK1082759A1 (lv)
LV (1) LV13003B (lv)
MX (1) MXPA05003492A (lv)
NO (1) NO331332B1 (lv)
NZ (1) NZ539616A (lv)
PT (1) PT1549734E (lv)
UA (2) UA58609U (lv)
WO (1) WO2004031341A1 (lv)
ZA (1) ZA200503409B (lv)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2946575A1 (en) 2014-04-21 2015-10-29 Devin Grant PETERSON Methods of making modified alcohol containing products
CN104371880B (zh) * 2014-11-26 2016-05-25 陕西科技大学 一种柿子味水果伏特加酒的固体发酵制备方法
CN104531487B (zh) * 2014-12-13 2016-05-25 安徽安特食品股份有限公司 一种加香型伏特加酒的制备方法
US20180216054A1 (en) * 2017-01-30 2018-08-02 Sidereal Pty Ltd. Method for purifying distilled spirits
US10934511B2 (en) * 2018-09-06 2021-03-02 Louise Wilkie Humic and fulvic black water based beverage for human consumption
EP3885426A1 (en) 2020-03-25 2021-09-29 ZHS IP Europe Sàrl A process for the production of vodka

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU863632A1 (ru) * 1979-12-25 1981-09-15 Московский Ликеро-Водочный Завод Способ производства водки "сибирска
RU2044045C1 (ru) * 1994-05-12 1995-09-20 Акционерное общество открытого типа - Московский завод "Кристалл" Способ производства водки "заздравная
RU2120965C1 (ru) * 1995-07-11 1998-10-27 Евгений Яковлевич Косицкий Водка "вятская"
US5618573A (en) * 1995-11-20 1997-04-08 Rtd Corporation Production of vodka by supercooling technology
GB2305935B (en) 1997-02-10 1997-10-01 Danisco Freeze distillation process and alcohol-containing product
RU2144949C1 (ru) * 1998-02-06 2000-01-27 Открытое акционерное общество "Владалко" Водка особая "лось"
RU2167932C1 (ru) * 1999-12-02 2001-05-27 Акционерное общество открытого типа "Брянскспиртпром" Способ производства водки
RU2175010C1 (ru) * 2000-04-06 2001-10-20 Бобрышев Сергей Юрьевич Способ производства водки
RU2186845C1 (ru) * 2000-12-01 2002-08-10 Общество с ограниченной ответственностью "Русская вино-водочная компания - Холдинг" Способ производства водки особой

Also Published As

Publication number Publication date
NO20052151L (no) 2005-05-02
CN1703501A (zh) 2005-11-30
CA2500983A1 (en) 2004-04-15
DK1549734T3 (da) 2008-06-30
DE60319553D1 (de) 2008-04-17
KR20050074960A (ko) 2005-07-19
EA200500586A1 (ru) 2005-10-27
ZA200503409B (en) 2006-03-29
PT1549734E (pt) 2008-06-17
CN100415865C (zh) 2008-09-03
EA007803B9 (ru) 2012-08-30
ATE388220T1 (de) 2008-03-15
AU2003274813B2 (en) 2008-06-05
UA58609U (ru) 2011-04-26
DE60319553T2 (de) 2008-11-27
JP2006508650A (ja) 2006-03-16
EP1549734B1 (en) 2008-03-05
JP4494208B2 (ja) 2010-06-30
WO2004031341A1 (en) 2004-04-15
UA62593U (en) 2011-09-12
ES2302944T3 (es) 2008-08-01
MXPA05003492A (es) 2005-08-16
US20060134302A1 (en) 2006-06-22
EP1549734A1 (en) 2005-07-06
NO331332B1 (no) 2011-11-28
BR0315022A (pt) 2005-09-06
CY1107940T1 (el) 2013-09-04
HK1082759A1 (en) 2006-06-16
EA007803B1 (ru) 2007-02-27
AU2003274813A1 (en) 2004-04-23
NZ539616A (en) 2007-05-31
CA2500983C (en) 2012-12-18
BR0315022B1 (pt) 2015-01-06

Similar Documents

Publication Publication Date Title
Liang et al. Cleaning of fouled ultrafiltration (UF) membrane by algae during reservoir water treatment
JPS58209975A (ja) アルコ−ル飲料の製法
LV13003B (en) Method for processing vodka
García-Martín et al. Sugar reduction in white and red musts with nanofiltration membranes
Kovaleva et al. Separation of molasses distillery slop on UFM-50®, UPM-50M®, OPMN-P®, and OFAM-K® porous membranes
Guilbaud et al. Comparison of Seawater and Freshwater Ultrafltration on Semi-Industrial Scale: Ballast Water Treatment Application
EP1403362B1 (fr) Procédé de désacidification de boissons
CA1205401A (en) Alcoholic beverages and method of manufacture
RU2005109528A (ru) Способ очистки грунта от нефтяных загрязнений
SU1565878A1 (ru) Способ производства водки "Столична кристалл
KR100541962B1 (ko) 나노여과를 이용한 주류의 제조방법
RU2268295C1 (ru) Способ производства советского шампанского
KR100833708B1 (ko) 해양 심층수 용매를 이용한 녹차 폴리페놀류 기능성물질들의 분리 추출 방법
RU2272831C1 (ru) Способ производства водки
RU2137831C1 (ru) Способ производства водки "русский бриллиант"
SU1110798A1 (ru) Способ шампанизации вина в непрерывном потоке
CN115667488A (zh) 用于生产伏特加的方法
RU2244736C2 (ru) Способ производства водки
SU190852A1 (ru) ЧЕЖГЯГЧЕСКАЯ •'§'»Ь":?атгкА
RU2304613C2 (ru) Способ производства водки
RU2055872C1 (ru) Способ производства водки "эфенди"
RU2006125139A (ru) Способ производства водки
LV12830A (lv) Method for production of alcoholic beverages
DK1046718T3 (da) Fremgangsmåde til rensning af rå roesaft
RU2000120786A (ru) Способ производства медового алкогольного напитка