AR041326A1 - Proceso y dispositivo para obtener biodiesel - Google Patents
Proceso y dispositivo para obtener biodieselInfo
- Publication number
- AR041326A1 AR041326A1 ARP030103417A ARP030103417A AR041326A1 AR 041326 A1 AR041326 A1 AR 041326A1 AR P030103417 A ARP030103417 A AR P030103417A AR P030103417 A ARP030103417 A AR P030103417A AR 041326 A1 AR041326 A1 AR 041326A1
- Authority
- AR
- Argentina
- Prior art keywords
- esterification
- transesterification
- monoalcohol
- fatty acids
- mixture
- Prior art date
Links
Classifications
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- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
- C11C3/04—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fats or fatty oils
- C11C3/10—Ester interchange
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/03—Preparation of carboxylic acid esters by reacting an ester group with a hydroxy group
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
- C10L1/026—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for compression ignition
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
- C11C3/003—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fatty acids with alcohols
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00002—Chemical plants
- B01J2219/00004—Scale aspects
- B01J2219/00006—Large-scale industrial plants
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
- B01J2219/324—Composition or microstructure of the elements
- B01J2219/32491—Woven or knitted materials
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1003—Waste materials
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1011—Biomass
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/04—Diesel oil
-
- 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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Wood Science & Technology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Fats And Perfumes (AREA)
- Liquid Carbonaceous Fuels (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Fertilizers (AREA)
Abstract
Proceso exento de presión para la producción continua de ésteres de alquilo de ácidos grasos superiores, especialmente biodiesel, a partir de mezclas de partida de triglicéridos de ácidos grasos que contienen ácidos grasos libres, con unacombinación integrada de esterificación ácida y transesterificación básica que incluye: a) esterificar una o varias veces los ácidos grasos libres en sendos dispositivos de esterificación separados, comunicados entre sí, con un monoalcohol de C1 aC4 en presencia de un catalizador ácido y glicerina como agente de arrastre, a una temperatura de 60sC a 65sC, con formación de una mezcla de esterificación, b) purificar parcialmente la mezcla de esterificación mediante la separación parcial delagente de arrastre, el catalizador ácido y el monoalcohol de C1- a C4 no transformado, c) transesterificar al menos dos veces los triglicéridos de ácidos grasos en sendos dispositivos de transesterificación separados, comunicados entre sí, con unmonoalcohol de C1 a C4 en presencia de un catalizador básico, a 60sC a 65sC, con formación de una mezcla de transesterificación, d) purificar la mezcla de transesterificación mediante la separación del catalizador básico, el monoalcohol de C1 a C4no transformado y de la glicerina formada en la transesterificación, por medio de un tratamiento con agua en al menos un separador y posterior secado, en el que el monoalcohol de C1 a C4 utilizado para la esterificación, el agente de arrastreglicerina utilizado para la esterificación y el agua utilizada para la purificación de la mezcla de transesterificación se recuperan al menos parcialmente de las mezclas de esterificación y transesterificación y porque después de retirar loscatalizadores ácidos y básicos de las mezclas de esterificación y transesterificación se convierten para formar una sal apropiada como fertilizante. Dispositivo para obtener biodiesel que presenta una combinación integrada de unidades para laesterificación ácida y la transesterificación básica.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10243700A DE10243700A1 (de) | 2002-09-20 | 2002-09-20 | Verfahren und Vorrichtung zur Herstellung von Biodiesel |
Publications (1)
Publication Number | Publication Date |
---|---|
AR041326A1 true AR041326A1 (es) | 2005-05-11 |
Family
ID=31969316
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
ARP030103417A AR041326A1 (es) | 2002-09-20 | 2003-09-19 | Proceso y dispositivo para obtener biodiesel |
Country Status (11)
Country | Link |
---|---|
US (1) | US20050204612A1 (es) |
EP (1) | EP1542960A1 (es) |
CN (1) | CN100467438C (es) |
AR (1) | AR041326A1 (es) |
AU (1) | AU2003273840A1 (es) |
BR (1) | BR0314847A (es) |
CA (1) | CA2499821A1 (es) |
DE (1) | DE10243700A1 (es) |
MY (1) | MY148440A (es) |
PL (1) | PL209695B1 (es) |
WO (1) | WO2004029016A1 (es) |
Families Citing this family (94)
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AT513799B1 (de) | 2012-12-18 | 2020-02-15 | Mag Schell Klaus | Verfahren zur Herstellung eines Bio-Diesel-Kraftstoffes mit einem speziell ausgelegten Reaktor und quasi katalytisch wirksamer nanoskalig strukturierter Materialoberfläche des Reaktors |
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CN105693656B (zh) * | 2016-01-26 | 2018-08-28 | 浙江工业大学 | 一种环氧植物油增塑剂的生产装置 |
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US2383599A (en) * | 1942-10-17 | 1945-08-28 | Colgate Palmolive Peet Co | Treating fatty glycerides |
US2383581A (en) * | 1943-05-06 | 1945-08-28 | Colgate Palmolive Peet Co | Process for preparing fatty materials |
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DE3319590A1 (de) * | 1983-05-30 | 1984-12-06 | Henkel KGaA, 4000 Düsseldorf | Verfahren zur herstellung von fettsaeureestern kurzkettiger aliphatischer alkohole aus freie fettsaeuren enthaltenden fetten und/oder oelen |
DE3501761A1 (de) * | 1985-01-21 | 1986-07-24 | Henkel KGaA, 4000 Düsseldorf | Verfahren zur vorveresterung freier fettsaeuren in rohfetten und/oder -oelen |
DE4123928A1 (de) * | 1991-07-19 | 1993-01-21 | Metallgesellschaft Ag | Verfahren zum erzeugen von fettsaeure-methylester oder fettsaeure-aethylester und glycerin durch umesterung von oelen oder fetten |
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US5618972A (en) * | 1995-02-27 | 1997-04-08 | Uop | Process for continuous reaction and separation using fixed catalyst bed serially connected to simulated moving catalyst and adsorbent bed |
-
2002
- 2002-09-20 DE DE10243700A patent/DE10243700A1/de not_active Withdrawn
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2003
- 2003-09-08 PL PL376100A patent/PL209695B1/pl unknown
- 2003-09-08 CN CNB038252899A patent/CN100467438C/zh not_active Expired - Fee Related
- 2003-09-08 BR BR0314847-5A patent/BR0314847A/pt not_active IP Right Cessation
- 2003-09-08 EP EP03757803A patent/EP1542960A1/de not_active Withdrawn
- 2003-09-08 CA CA002499821A patent/CA2499821A1/en not_active Abandoned
- 2003-09-08 US US10/528,333 patent/US20050204612A1/en not_active Abandoned
- 2003-09-08 WO PCT/EP2003/009965 patent/WO2004029016A1/de active Application Filing
- 2003-09-08 AU AU2003273840A patent/AU2003273840A1/en not_active Abandoned
- 2003-09-19 MY MYPI20033580A patent/MY148440A/en unknown
- 2003-09-19 AR ARP030103417A patent/AR041326A1/es unknown
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CN100467438C (zh) | 2009-03-11 |
CA2499821A1 (en) | 2004-04-08 |
BR0314847A (pt) | 2005-08-09 |
AU2003273840A1 (en) | 2004-04-19 |
US20050204612A1 (en) | 2005-09-22 |
WO2004029016A1 (de) | 2004-04-08 |
MY148440A (en) | 2013-04-30 |
PL209695B1 (pl) | 2011-10-31 |
EP1542960A1 (de) | 2005-06-22 |
DE10243700A1 (de) | 2004-04-01 |
CN1741982A (zh) | 2006-03-01 |
PL376100A1 (en) | 2005-12-12 |
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