AR104100A1 - Plantas de destilación de alcohol de cereales - Google Patents
Plantas de destilación de alcohol de cerealesInfo
- Publication number
- AR104100A1 AR104100A1 ARP160100757A ARP160100757A AR104100A1 AR 104100 A1 AR104100 A1 AR 104100A1 AR P160100757 A ARP160100757 A AR P160100757A AR P160100757 A ARP160100757 A AR P160100757A AR 104100 A1 AR104100 A1 AR 104100A1
- Authority
- AR
- Argentina
- Prior art keywords
- column
- distributors
- plant
- accumulators
- rectifying
- Prior art date
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
- B01D3/001—Processes specially adapted for distillation or rectification of fermented solutions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/06—Evaporators with vertical tubes
- B01D1/08—Evaporators with vertical tubes with short tubes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/06—Evaporators with vertical tubes
- B01D1/10—Evaporators with vertical tubes with long tubes, e.g. Kestner evaporators
-
- 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
-
- 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
- B01D3/32—Other features of fractionating columns ; Constructional details of fractionating columns not provided for in groups B01D3/16 - B01D3/30
- B01D3/324—Tray constructions
- B01D3/326—Tray supports
-
- 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
- B01D3/42—Regulation; Control
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0003—Condensation of vapours; Recovering volatile solvents by condensation by using heat-exchange surfaces for indirect contact between gases or vapours and the cooling medium
- B01D5/0012—Vertical tubes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0027—Condensation of vapours; Recovering volatile solvents by condensation by direct contact between vapours or gases and the cooling medium
- B01D5/003—Condensation of vapours; Recovering volatile solvents by condensation by direct contact between vapours or gases and the cooling medium within column(s)
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0057—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes
- B01D5/006—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes with evaporation or distillation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0057—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes
- B01D5/006—Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes with evaporation or distillation
- B01D5/0063—Reflux condensation
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
Abstract
Mejoras en plantas de destilación de alcohol de cereales mediante la incorporación de una disposición interna de la columna de mosto y de la columna rectificadora con distribuidores y acumuladores dentro de la columna, logrando un proceso estable y seguro en amplios rangos de operación, garantizando la productividad de la planta y la calidad de los productos. La columna de mosto presenta platos perforados desmontables, de fácil acceso y limpieza a través de bocas de inspección. Al tener platos fácilmente desmontables y, además, una boca de inspección por cada plato con uniones tipo clamp, se facilita el acceso al interior de la columna para su limpieza y mantenimiento. La columna rectificadora es una columna especial de relleno con distribuidores de flujo, cuenta con un acumulador de alcohol intermedio y un condensador integrado a la columna que evita el uso de bombas. La disposición de distribuidores y acumuladores dentro de la columna rectificadora favorece la estabilidad operativa de la planta, permitiendo que un equipo de baja escala trabaje de manera similar a una columna de escala industrial. Las mejoras incluyen un sistema de automatización integrado con comunicación vía Internet para la autogestión de la planta con monitoreo remoto y operación autónoma.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ARP160100757A AR104100A1 (es) | 2016-03-21 | 2016-03-21 | Plantas de destilación de alcohol de cereales |
BR102017005784-4A BR102017005784A2 (pt) | 2016-03-21 | 2017-03-21 | Performance in central distillation of cereal alcohol |
US15/464,626 US10343081B2 (en) | 2016-03-21 | 2017-03-21 | Grain alcohol distillation plants |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ARP160100757A AR104100A1 (es) | 2016-03-21 | 2016-03-21 | Plantas de destilación de alcohol de cereales |
Publications (1)
Publication Number | Publication Date |
---|---|
AR104100A1 true AR104100A1 (es) | 2017-06-28 |
Family
ID=59256463
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ARP160100757A AR104100A1 (es) | 2016-03-21 | 2016-03-21 | Plantas de destilación de alcohol de cereales |
Country Status (3)
Country | Link |
---|---|
US (1) | US10343081B2 (es) |
AR (1) | AR104100A1 (es) |
BR (1) | BR102017005784A2 (es) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
IT201700042150A1 (it) * | 2017-04-14 | 2018-10-14 | Cristiano Galbiati | Separation equipment |
CN116983699B (zh) * | 2023-09-20 | 2023-12-01 | 河北金牛旭阳化工有限公司 | 一种甲醇精馏装置 |
Family Cites Families (30)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1973529A (en) * | 1934-09-11 | guinot | ||
US1937786A (en) * | 1933-12-05 | Process foe the simultaneous dis | ||
US1940699A (en) * | 1933-12-26 | Process and apparatus for con | ||
US1744504A (en) * | 1923-07-06 | 1930-01-21 | Us Ind Alcohol Co | Process of manufacture of absolute alcohol |
US2903251A (en) * | 1955-10-05 | 1959-09-08 | Koch Eng Co Inc | Sectional deck construction having spaced overlaps |
US2963423A (en) * | 1958-12-31 | 1960-12-06 | Exxon Research Engineering Co | Preparation of catalytic cracking feed stocks |
GB1407270A (en) * | 1972-11-30 | 1975-09-24 | Mobil Services Co Ltd | Method and apparatus for simultaneously fractionating a plurality of crude oils |
US3811843A (en) * | 1973-02-22 | 1974-05-21 | Foster Wheeler Corp | Solvent deasphalting |
US4303479A (en) * | 1977-10-07 | 1981-12-01 | The Goodyear Tire & Rubber Company | Distillation separation method |
IE48505B1 (en) * | 1978-10-28 | 1985-02-06 | Bp Chem Int Ltd | Improved method of producing ethanol-water azeotrope from crude ethanol |
US4217178A (en) * | 1978-11-07 | 1980-08-12 | Raphael Katzen Associates International, Inc. | Distillation system for motor fuel grade anhydrous alcohol |
US4568356A (en) * | 1978-11-09 | 1986-02-04 | Chambers John M | Process for making anhydrous alcohol for mixing with gasoline to make gasohol motor fuel |
US4256541A (en) * | 1979-05-29 | 1981-03-17 | National Distillers And Chemical Corp. | Production of anydrous alcohol |
US4328074A (en) * | 1980-11-12 | 1982-05-04 | Resources Conservation Company | Production of concentrated alcohol and distillery slop |
CA1197172A (en) * | 1982-11-24 | 1985-11-26 | Karl T. Chuang | Gas-liquid contacting apparatus |
US4894145A (en) * | 1988-07-19 | 1990-01-16 | Applied Automation, Inc. | Automatic control of feedstock vacuum towers |
US5277847A (en) * | 1989-03-08 | 1994-01-11 | Glitsch, Inc. | Method and apparatus for catalyst-downcomer-tray operation |
US5106544A (en) * | 1990-01-31 | 1992-04-21 | Glitsch, Inc. | Method of and apparatus for vapor distribution |
US5895608A (en) * | 1996-10-30 | 1999-04-20 | Koch Enterprises, Inc. | Downcomer for chemical process tower and method of forming the same |
DE19847115C1 (de) * | 1998-10-13 | 2000-05-04 | Basf Ag | Gegenstrom-Stripprohr |
US6095504A (en) * | 1999-03-24 | 2000-08-01 | Uop Llc | Supports for stacked fractionation tray end pieces |
US7070745B2 (en) * | 2000-12-11 | 2006-07-04 | Shell Oil Company | Multiple bed downflow reactor |
US7267746B1 (en) * | 2001-02-26 | 2007-09-11 | Uop Llc | Dividing wall distillation column control apparatus |
US7297236B1 (en) * | 2001-06-30 | 2007-11-20 | Icm, Inc. | Ethanol distillation process |
US7867365B2 (en) * | 2003-03-28 | 2011-01-11 | Thermal Kinetics Systems, Llc | Ethanol distillation with distillers soluble solids recovery apparatus |
DE102004015714B3 (de) * | 2004-03-29 | 2005-12-15 | Stockhausen Gmbh | Trennboden für eine Destillationskolonne |
US8540218B2 (en) * | 2007-04-27 | 2013-09-24 | Gtc Technology Us Llc | Fluid dispersion unit assembly and method |
US8101808B2 (en) * | 2007-12-27 | 2012-01-24 | Gevo, Inc. | Recovery of higher alcohols from dilute aqueous solutions |
US8043417B2 (en) * | 2008-06-30 | 2011-10-25 | Uop Llc | Column installed condenser |
US8480062B2 (en) * | 2009-05-15 | 2013-07-09 | Gtc Technology Us, Llc | Activated hinge-joint |
-
2016
- 2016-03-21 AR ARP160100757A patent/AR104100A1/es unknown
-
2017
- 2017-03-21 US US15/464,626 patent/US10343081B2/en not_active Expired - Fee Related
- 2017-03-21 BR BR102017005784-4A patent/BR102017005784A2/pt not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
BR102017005784A2 (pt) | 2017-09-26 |
US10343081B2 (en) | 2019-07-09 |
US20170266582A1 (en) | 2017-09-21 |
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