KR860009120A - 저알콜함량 음료의 제조를 위한 연속 재순환 방법 - Google Patents

저알콜함량 음료의 제조를 위한 연속 재순환 방법 Download PDF

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Publication number
KR860009120A
KR860009120A KR1019860003940A KR860003940A KR860009120A KR 860009120 A KR860009120 A KR 860009120A KR 1019860003940 A KR1019860003940 A KR 1019860003940A KR 860003940 A KR860003940 A KR 860003940A KR 860009120 A KR860009120 A KR 860009120A
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South Korea
Prior art keywords
total pressure
semipermeable membrane
alcohol
psi
alcohol content
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KR1019860003940A
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KR890001591B1 (ko
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고다드 라이트 월리암
고다드 라이트 윌리암
Original Assignee
얼라이드 코오포레이숀
로이 에치. 마센질
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Publication of KR860009120A publication Critical patent/KR860009120A/ko
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/52—Polyethers
    • B01D71/521—Aliphatic polyethers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/52—Polyethers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/025—Reverse osmosis; Hyperfiltration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
    • B01D69/12—Composite membranes; Ultra-thin membranes
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12H—PASTEURISATION, STERILISATION, PRESERVATION, PURIFICATION, CLARIFICATION OR AGEING OF ALCOHOLIC BEVERAGES; METHODS FOR ALTERING THE ALCOHOL CONTENT OF FERMENTED SOLUTIONS OR ALCOHOLIC BEVERAGES
    • C12H3/00—Methods for reducing the alcohol content of fermented solutions or alcoholic beverage to obtain low alcohol or non-alcoholic beverages
    • C12H3/04—Methods for reducing the alcohol content of fermented solutions or alcoholic beverage to obtain low alcohol or non-alcoholic beverages using semi-permeable membranes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2315/00—Details relating to the membrane module operation
    • B01D2315/12—Feed-and-bleed systems
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2323/00—Details relating to membrane preparation
    • B01D2323/30—Cross-linking

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • Biochemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Health & Medical Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Zoology (AREA)
  • Nanotechnology (AREA)
  • Food Science & Technology (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)

Abstract

내용 없음

Description

저알콜함량 음료의 제조를 위한 연속 재순환 방법
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
첨부도면은 본 발명 방법의 단일흐름 선도.

Claims (9)

  1. 물 및 알콜성음료의 재순환류인 공급혼합물을 낮은 총압력에 대한 총압력에 의존하며 높은 총압력에 대한 총압력에 본질적으로 무관한 알콜에 대한 삼투율을 나타내는 반투막에 알콜과 물로 구성되는 삼투물과 감소된 알콜함량의 상기 음료로 구성되는 잔유물을 형성하기 위해 선택된 역삼투분리조건으로 통과시키고, 상기 반투막과 접촉하여 상기 공급혼합물을 형성하기전에 첨가된 새로운 음료와 물을 혼합하도록 상기 잔유물의 대부분을 재순환 시키는 것으로 구성되는 알콜성 음료의 알콜함량 감소를 위한 연속 재순환방법.
  2. 제1항에 있어서, 상기 방법이 약 50 내지 250psi(345 내지 1724kPa)의 총압력으로 수행됨을 특징으로 하는 방법.
  3. 제2항에 있어서, 상기 총압력에서의 알콜에 대한 반투막배제율 이 약 40 내지 75％임을 특징으로 하는 방법.
  4. 제1항에 있어서, 상기 분리 조건이 약 5 내지 20℃의 온도와 약 200 내지 1000psi(1380 내지 6895kPa)의 적용압력을 포함함을 특징으로 하는 방법.
  5. 제1항에 있어서, 제품으로 회수되어진 잔유물의 백분율이 약 1 내지 20％ 임을 특징으로 하는 방법.
  6. 제1항에 있어서, 상기 반투막이 비다공성 박막 중합 베리어로 구성됨을 특징으로 하는 방법.
  7. 제6항에 있어서, 상기 비다공성 박막 중합 베리어가 중합지지체위에 복합되어짐을 특징으로 하는 방법.
  8. 제6항에 있어서, 상기 비다공성 박막 중합 베리어가 톨루엔디이소시아너이트로 가교시킨 아민 변성 폴리에피할로히드린, 또는 이소프탈로일 클로라이드로 가교시킨 아민변성 폴리에피할로히드린, 또는 이소프탈로일 클로라이드로 가교시킨 폴리 에틸렌이민으로 구성됨을 특징으로 하는 방법.
  9. 제1항에 있어서, 상기 반투막이 400psi 총압력으로 97％이상의 클로라이드 이온 배제율을 갖음을 특징으로 하는 방법.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019860003940A 1985-05-20 1986-05-19 저알콜함량 음료의 제조를 위한 연속재 순환 방법 KR890001591B1 (ko)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US736,047 1985-05-20
US736047 1985-05-20
US06/736,047 US4617127A (en) 1985-05-20 1985-05-20 Production of low alcoholic content beverages

Publications (2)

Publication Number Publication Date
KR860009120A true KR860009120A (ko) 1986-12-20
KR890001591B1 KR890001591B1 (ko) 1989-05-09

Family

ID=24958291

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019860003940A KR890001591B1 (ko) 1985-05-20 1986-05-19 저알콜함량 음료의 제조를 위한 연속재 순환 방법

Country Status (13)

Country Link
US (1) US4617127A (ko)
EP (1) EP0202590B1 (ko)
JP (1) JPS61268170A (ko)
KR (1) KR890001591B1 (ko)
CN (1) CN86104029A (ko)
AU (1) AU588875B2 (ko)
CA (1) CA1275270C (ko)
DE (1) DE3674458D1 (ko)
DK (1) DK165172C (ko)
ES (1) ES8707562A1 (ko)
NZ (1) NZ216217A (ko)
PT (1) PT82614B (ko)
ZA (1) ZA863668B (ko)

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US4717482A (en) * 1985-05-20 1988-01-05 Allied Corporation Production of low alcoholic content beverages
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US5013447A (en) * 1989-07-19 1991-05-07 Sepracor Process of treating alcoholic beverages by vapor-arbitrated pervaporation
US4933198A (en) * 1985-10-11 1990-06-12 Lee Eric K L Production of low-ethanol beverage by membrane extraction
FR2592058B1 (fr) * 1985-12-19 1990-05-04 Migros Federation Cooperatives Procede de desalcoolisation partielle ou totale du vin et/ou du cidre et dispositif pour la mise en oeuvre de ce procede
DE3600352A1 (de) * 1986-01-09 1987-07-16 Norbert Barth Verfahren zur herstellung von vergorenen getraenken, insbesondere wein, mit verringertem alkoholgehalt
US4834998A (en) * 1986-12-22 1989-05-30 Heublein, Inc. Ultrafiltration of red wines
US4888189A (en) * 1987-08-17 1989-12-19 Ariel Vineyards, Inc. Simultaneous double reverse osmosis process for production of low and non-alcoholic beverages
US4999209A (en) * 1987-08-17 1991-03-12 Ariel Vineyards, Inc. Low and non-alcoholic beverages produced by simultaneous double reverse osmosis
DE3804236A1 (de) * 1988-02-11 1989-08-24 Gft Ges Fuer Trenntechnik Verfahren zur reduktion des alkoholgehaltes von alkoholischen getraenken
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DE4003404A1 (de) * 1990-02-05 1991-08-08 Moselland Eg Winzergenossensch Gaerprodukt mit vermindertem ethanolgehalt
US5938928A (en) * 1991-08-01 1999-08-17 Nonap Pty. Ltd. Osmotic distillation process using a membrane laminate
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ATE171390T1 (de) * 1992-05-08 1998-10-15 Clark Robert Smith Vorrichtung und verfahren für die trennung von verbindungen aus einer lösung
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US5824223A (en) * 1995-11-08 1998-10-20 Rentiers Machinery Proprietary Ltd. Methods and apparatus for osmotic distillation
US6112908A (en) * 1998-02-11 2000-09-05 Rentiers Machinery Pty, Ltd. Membrane laminates and methods for their preparation
GB9820935D0 (en) 1998-09-25 1998-11-18 Pall Corp Filtration system
US20030039721A1 (en) 2001-07-26 2003-02-27 Pankaj Shah Process for enhancing the body and taste of malt beverages
WO2003074650A1 (en) * 2002-03-05 2003-09-12 Velo Spa Process and apparatus for wine treatment to reduce its contents of volatile acidity
DE10217530B4 (de) * 2002-04-19 2006-04-20 Degussa Ag Verfahren zur Aufreinigung von Cyanamid-haltigen Lösungen
US7122709B2 (en) * 2003-03-13 2006-10-17 3M Innovative Properties Company Method for obtaining ethanol
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DE102004028832A1 (de) * 2004-03-04 2005-09-22 Warsteiner Brauerei Haus Cramer Kg Bier mit verändertem Restextraktgehalt
EP1571200A1 (de) * 2004-03-04 2005-09-07 Warsteiner Brauerei Haus Cramer KG Bier mit verändertem Restextraktgehalt
DE102004028728B4 (de) * 2004-06-14 2008-03-27 Warsteiner Brauerei Haus Cramer Kg Verfahren zur Herstellung von Bier mit veränderten Bierinhaltsstoffen
ATE539143T1 (de) * 2004-10-21 2012-01-15 Diageo North America Inc Verfahren zur herstellung von gereinigten getränkeprodukten
FR2939446B1 (fr) * 2008-12-05 2011-04-22 Valagro Carbone Renouvelable Utilisation de coton recycle pour produire de l'ethanol, et procede de production.
CN101548774B (zh) * 2009-04-10 2012-12-26 广东加多宝饮料食品有限公司 一种中草药凉茶浓缩液的加工方法
CA2783847C (en) * 2012-07-24 2014-09-30 Luc Hobson Reduced calorie beverage or food product and process and apparatus for making same
MX2017006379A (es) 2014-11-17 2017-08-21 Massachusetts Inst Technology Control de concentracion en sistemas de filtracion y metodos asociados.
US10603635B2 (en) 2016-05-04 2020-03-31 Massachusetts Institute Of Technology Multi-stage reverse osmosis systems and methods
CN109593619A (zh) * 2018-11-29 2019-04-09 南京九思高科技有限公司 一种同时制取无醇葡萄酒和高度酒的系统和方法
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Also Published As

Publication number Publication date
DK229586D0 (da) 1986-05-16
EP0202590A2 (en) 1986-11-26
PT82614B (pt) 1992-07-31
ES8707562A1 (es) 1987-08-01
JPH029791B2 (ko) 1990-03-05
JPS61268170A (ja) 1986-11-27
DK165172B (da) 1992-10-19
CA1275270C (en) 1990-10-16
NZ216217A (en) 1988-09-29
KR890001591B1 (ko) 1989-05-09
AU588875B2 (en) 1989-09-28
EP0202590B1 (en) 1990-09-26
CN86104029A (zh) 1987-02-25
AU5759086A (en) 1986-11-27
DK165172C (da) 1993-03-08
ZA863668B (en) 1986-12-30
EP0202590A3 (en) 1987-02-04
DE3674458D1 (de) 1990-10-31
ES555097A0 (es) 1987-08-01
PT82614A (en) 1986-06-01
DK229586A (da) 1986-11-21
US4617127A (en) 1986-10-14

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