CO6311085A2 - EVAPORATOR OF EFFECTS AND MULTIPLE STAGES USED BY THE CONDENSATION ENERGY FOR THE CONCENTRATION OF VINASES - Google Patents
EVAPORATOR OF EFFECTS AND MULTIPLE STAGES USED BY THE CONDENSATION ENERGY FOR THE CONCENTRATION OF VINASESInfo
- Publication number
- CO6311085A2 CO6311085A2 CO10149230A CO10149230A CO6311085A2 CO 6311085 A2 CO6311085 A2 CO 6311085A2 CO 10149230 A CO10149230 A CO 10149230A CO 10149230 A CO10149230 A CO 10149230A CO 6311085 A2 CO6311085 A2 CO 6311085A2
- Authority
- CO
- Colombia
- Prior art keywords
- evaporator
- concentration
- evaporation
- vinases
- column
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/26—Multiple-effect evaporating
-
- 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
- B01D3/001—Processes specially adapted for distillation or rectification of fermented solutions
- B01D3/002—Processes specially adapted for distillation or rectification of fermented solutions by continuous methods
-
- 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
-
- 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
- B01D3/148—Fractional distillation or use of a fractionation or rectification column by two or more of a fractionation, separation or rectification step in combination with at least one evaporator
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Distillation Of Fermentation Liquor, Processing Of Alcohols, Vinegar And Beer (AREA)
Abstract
EVAPORADOR DE CONCENTRACIÓN DE VINASA PARA DESTILERÍAS EN GENERAL se aplica preferiblemente en la destilería (1) de etanol, cuyos equipos constituyentes permiten lograr el proceso de concentración de vinasa (2) utilizando el depósito regulador (T1) de evaporación como rehervidor de las columnas (C1 y C2), así como también el depósito regulador (T2) de la evaporación como condensador de las columnas mencionadas (C1 y C2), sin consumo extra de energía o vapor (3) y agua (4), por la utilización de bombas (5) para el movimiento del producto; precalentadores (no representados) para el calentamiento del vino (6); un calentador final (no representado) para lograr el último calentamiento del vino (6); una columna (C1) responsable de la primera destilación; depósitos reguladores (T) que ejecutan la evaporación de la vinasa; separadores (S) que disocian los vapores de los líquidos en el evaporador; una columna (C2) responsable de la segunda destilación; el condensador evaporador (7) que condensa los vapores de los últimos efectos y el sistema de remoción de aire (8) del equipo por medio de vacío. VINASE CONCENTRATION EVAPORATOR FOR DISTILLERIES IN GENERAL is preferably applied in the distillery (1) of ethanol, whose constituent equipment allows to achieve the process of concentration of vinases (2) using the evaporation regulator tank (T1) as a column reboiler ( C1 and C2), as well as the evaporation regulating tank (T2) as a condenser of the mentioned columns (C1 and C2), without extra consumption of energy or steam (3) and water (4), by the use of pumps (5) for product movement; preheaters (not shown) for heating the wine (6); a final heater (not shown) to achieve the last heating of the wine (6); a column (C1) responsible for the first distillation; regulatory deposits (T) that carry out the evaporation of the kinase; separators (S) that dissociate the vapors of the liquids in the evaporator; a column (C2) responsible for the second distillation; the evaporator condenser (7) that condenses the vapors of the last effects and the air removal system (8) of the equipment by means of vacuum.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BRPI0801519-8A BRPI0801519B1 (en) | 2008-05-12 | 2008-05-12 | "system for concentration of vinasse without extra consumption of steam coupled with ethanol distillery." |
Publications (1)
Publication Number | Publication Date |
---|---|
CO6311085A2 true CO6311085A2 (en) | 2011-08-22 |
Family
ID=41318299
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CO10149230A CO6311085A2 (en) | 2008-05-12 | 2010-11-26 | EVAPORATOR OF EFFECTS AND MULTIPLE STAGES USED BY THE CONDENSATION ENERGY FOR THE CONCENTRATION OF VINASES |
Country Status (5)
Country | Link |
---|---|
AU (1) | AU2009245991B2 (en) |
BR (1) | BRPI0801519B1 (en) |
CO (1) | CO6311085A2 (en) |
WO (1) | WO2009137898A1 (en) |
ZA (1) | ZA201004697B (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BR102012025224B1 (en) * | 2012-09-24 | 2016-03-01 | Citrotec Indústria E Comércio Ltda | Concentration system fed by the thermal potential of the hot exhaust gases from the biomass boiler chimneys. |
BR202013007747Y1 (en) * | 2013-03-06 | 2019-04-24 | Citrotec Indústria E Comércio Ltda | IMPROVING THE INTEGRATED VINEYA CONCENTRATION PLANT WITH THE ETHANOL DISTILLERY |
CN105152250B (en) * | 2015-10-22 | 2017-05-17 | 哈尔滨工大金涛科技股份有限公司 | Multi-effect industrial wastewater evaporating and concentrating device and method |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB453222A (en) * | 1933-12-05 | 1936-09-07 | Emile Augustin Barbet | Improved method for the direct distillation and rectification of wines with the double effect of the heating steam |
FR2546528B1 (en) * | 1983-05-27 | 1985-08-23 | Laguilharre Sa | IMPROVEMENT IN DISTILLATION FACILITIES OF A LIQUID SUCH AS WINE AND SIMULTANEOUS CONCENTRATION OF THE DISTILLATION RESIDUE |
BRPI0600553A (en) * | 2006-02-24 | 2007-11-20 | Siemens Ltda | process and system for the production of alcohol by multiple effect distillation |
-
2008
- 2008-05-12 BR BRPI0801519-8A patent/BRPI0801519B1/en not_active IP Right Cessation
-
2009
- 2009-05-11 AU AU2009245991A patent/AU2009245991B2/en not_active Ceased
- 2009-05-11 WO PCT/BR2009/000124 patent/WO2009137898A1/en active Application Filing
-
2010
- 2010-07-05 ZA ZA2010/04697A patent/ZA201004697B/en unknown
- 2010-11-26 CO CO10149230A patent/CO6311085A2/en active IP Right Grant
Also Published As
Publication number | Publication date |
---|---|
BRPI0801519A2 (en) | 2012-02-22 |
BRPI0801519B1 (en) | 2015-05-05 |
AU2009245991B2 (en) | 2014-03-27 |
ZA201004697B (en) | 2011-03-30 |
WO2009137898A1 (en) | 2009-11-19 |
AU2009245991A1 (en) | 2009-11-19 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
FG | Application granted |