GB1251800A - - Google Patents
Info
- Publication number
- GB1251800A GB1251800A GB5342967A GB1251800DA GB1251800A GB 1251800 A GB1251800 A GB 1251800A GB 5342967 A GB5342967 A GB 5342967A GB 1251800D A GB1251800D A GB 1251800DA GB 1251800 A GB1251800 A GB 1251800A
- Authority
- GB
- United Kingdom
- Prior art keywords
- column
- pot
- liquid
- wash
- base
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/143—Fractional distillation or use of a fractionation or rectification column by two or more of a fractionation, separation or rectification step
- B01D3/146—Multiple effect distillation
-
- 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
- C12H6/00—Methods for increasing the alcohol content of fermented solutions or alcoholic beverages
- C12H6/02—Methods for increasing the alcohol content of fermented solutions or alcoholic beverages by distillation
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Food Science & Technology (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Alcoholic Beverages (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
1,251,800. Alcoholic beverages; distillation of alcoholic liquors. IRISH DISTILLERS Ltd. and W. H. A. WEBB. 29 Jan., 1969 [23 Nov., 1967] No. 53429/67. Heading B1B. A self-flavoured spirit similar to whisky, brandy, rum or calvados is produced by continuously passing a fermented liquor of low alcohol content through a pot wherein it is heated for a determined time in order to develop desired flavours, and distilling the effluent stream from the pot in a fractionating column to separate a fraction of the required high alcohol content. The pot is preferably made of or lined with, copper. In an example, "Irish" whisky is produced from distillery wash, containing about 6% by weight of alcohol, by heat-treatment and distillation in the apparatus shown. The wash is pumped from tank 2 into pot 8, which is heated by steam coil 10, where the wash is boiled under reflux. After a residence time of 5 hours, the wash overflows from pot 8 and is pumped to plate-type distillation column 16. Steam is introduced into the base of column 18 through injector 18, and the spent wash is discharged from the base. Some of the condensate from reflux condenser 22 is pumped to pot 26 where the liquid is maintained at the boiling point by electrical heater 28. After a residence time of 95 minutes, the liquid overflows to column 32 (a glass tube with stainless steel rings) heated by electrical element 34. Spent lees are discharged from the base of column 32. Some of the overhead condensate from reflux condenser 38 is pumped to pot 42 where the liquid is maintained at the boiling point by electrical element 41. After a residence time of 185 minutes, the liquid overflows into distillation column 44 (a thermally insulated glass tube filled with stainless steel rings) which is heated by electrical element 46. Liquid withdrawn from the base of column 44 is returned to pot 26. Some of the overhead condensate from reflux condenser 48 is pumped to column 56 (of similar design to column 44). Some of the overhead condensate from reflux condenser 58 is returned to pot 42. The liquid withdrawn from the base of column 56, which is passed through cooler 62 and collected in receiver 64, is the required whisky product. It is necessary to operate the apparatus for some days before equilibrium is reached, and the characteristics of the various fractions are established. An apparatus suitable for the continuous production of "Scotch" whisky is described with Fig. 3 (not shown); this apparatus comprises two pots and associated columns. The liquid and vapour withdrawn from the head and base, respectively, of the first column are used to preheat the feed wash. The level of liquid in the pots and in the sumps of the columns is automatically controlled.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB5342967 | 1967-11-23 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1251800A true GB1251800A (en) | 1971-10-27 |
Family
ID=10467780
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB5342967A Expired GB1251800A (en) | 1967-11-23 | 1967-11-23 |
Country Status (2)
Country | Link |
---|---|
JP (1) | JPS4821520B1 (en) |
GB (1) | GB1251800A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0812607A2 (en) * | 1996-06-14 | 1997-12-17 | Vittorio Capovilla | Process for after-treatment of crude distillate |
WO2017025747A1 (en) * | 2015-08-10 | 2017-02-16 | Pale Blue Dot Energy Limited | Distillation systems, apparatus and methods |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102006049175A1 (en) * | 2006-10-18 | 2008-06-05 | Gea Wiegand Gmbh | Plant for distilling drinking alcohol, in particular whiskey |
CN107619747B (en) * | 2017-10-30 | 2021-02-05 | 无锡葆元康健康科技有限公司 | Processing technology of fen-flavor liquor |
-
1967
- 1967-11-23 GB GB5342967A patent/GB1251800A/en not_active Expired
-
1968
- 1968-11-25 JP JP8568868A patent/JPS4821520B1/ja active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0812607A2 (en) * | 1996-06-14 | 1997-12-17 | Vittorio Capovilla | Process for after-treatment of crude distillate |
EP0812607A3 (en) * | 1996-06-14 | 1998-01-07 | Vittorio Capovilla | Process for after-treatment of crude distillate |
WO2017025747A1 (en) * | 2015-08-10 | 2017-02-16 | Pale Blue Dot Energy Limited | Distillation systems, apparatus and methods |
GB2557514A (en) * | 2015-08-10 | 2018-06-20 | Pale Blue Dot Energy Ltd | Distillation systems, apparatus and methods |
Also Published As
Publication number | Publication date |
---|---|
JPS4821520B1 (en) | 1973-06-29 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PCNP | Patent ceased through non-payment of renewal fee |