ES2421741T1 - Procedimiento para la reducción de la concentración de aldehído en una corriente gaseosa - Google Patents

Procedimiento para la reducción de la concentración de aldehído en una corriente gaseosa

Info

Publication number
ES2421741T1
ES2421741T1 ES12007339T ES12007339T ES2421741T1 ES 2421741 T1 ES2421741 T1 ES 2421741T1 ES 12007339 T ES12007339 T ES 12007339T ES 12007339 T ES12007339 T ES 12007339T ES 2421741 T1 ES2421741 T1 ES 2421741T1
Authority
ES
Spain
Prior art keywords
aldehyde
concentration
procedure
reducing
reaction vessel
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.)
Granted
Application number
ES12007339T
Other languages
English (en)
Other versions
ES2421741T3 (es
Inventor
Barbara F M Kimmich
Jeremy J Patt
Mark O Scates
Ronald D Shaver
James H Zink
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Celanese International Corp
Original Assignee
Celanese International Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Celanese International Corp filed Critical Celanese International Corp
Publication of ES2421741T1 publication Critical patent/ES2421741T1/es
Application granted granted Critical
Publication of ES2421741T3 publication Critical patent/ES2421741T3/es
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/18—Carbon
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/42—Platinum
    • 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
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/44—Palladium
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/74—Separation; Purification; Use of additives, e.g. for stabilisation
    • C07C29/88—Separation; Purification; Use of additives, e.g. for stabilisation by treatment giving rise to a chemical modification of at least one compound
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/10—Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide
    • C07C51/12—Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide on an oxygen-containing group in organic compounds, e.g. alcohols
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42—Separation; Purification; Stabilisation; Use of additives
    • C07C51/487—Separation; Purification; Stabilisation; Use of additives by treatment giving rise to chemical modification
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00—Preparation of carboxylic acid esters
    • C07C67/36—Preparation of carboxylic acid esters by reaction with carbon monoxide or formates
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00—Preparation of carboxylic acid esters
    • C07C67/48—Separation; Purification; Stabilisation; Use of additives
    • C07C67/60—Separation; Purification; Stabilisation; Use of additives by treatment giving rise to chemical modification
    • 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
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

Procedimiento que comprende: disponer una corriente de alimentación en fase gaseosa de un procedimiento decarbonilación, que comprende un reactivo carbonilable y una primera concentración de un aldehído; facilitar lacorriente de alimentación a un recipiente de reacción que contiene un catalizador sobre un soporte, que comprende,como mínimo, un metal del grupo 8 al grupo 11; llevar a cabo el contacto de la corriente de alimentación en fasegaseosa con el catalizador soportado dentro del recipiente de reacción, en condiciones suficientes para reducir laprimera concentración de aldehído para producir una corriente tratada, que comprende una segunda concentraciónde aldehído que es menor que la primera concentración de aldehído, y retirar la corriente tratada del recipiente dereacción, comprendiendo la corriente tratada una segunda concentración de aldehído que es menor que la primeraconcentración de aldehído.
ES12007339.0T 2006-04-14 2007-04-03 Procedimiento para la reducción de la concentración de aldehído en un flujo objetivo Active ES2421741T3 (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US79224406P 2006-04-14 2006-04-14
US792244P 2006-04-14

Publications (2)

Publication Number Publication Date
ES2421741T1 true ES2421741T1 (es) 2013-09-05
ES2421741T3 ES2421741T3 (es) 2015-10-23

Family

ID=38610082

Family Applications (1)

Application Number Title Priority Date Filing Date
ES12007339.0T Active ES2421741T3 (es) 2006-04-14 2007-04-03 Procedimiento para la reducción de la concentración de aldehído en un flujo objetivo

Country Status (21)

Country Link
US (1) US8076506B2 (es)
EP (2) EP2054366B1 (es)
JP (1) JP5486299B2 (es)
KR (1) KR101377835B1 (es)
CN (2) CN101511766A (es)
AR (1) AR060454A1 (es)
AU (1) AU2007238948B2 (es)
BR (1) BRPI0710016A2 (es)
CA (1) CA2649298C (es)
CL (1) CL2007001035A1 (es)
DE (1) DE12007339T8 (es)
ES (1) ES2421741T3 (es)
MX (1) MX2008013270A (es)
MY (1) MY155307A (es)
NO (1) NO20084790L (es)
NZ (1) NZ571943A (es)
RU (1) RU2437871C2 (es)
TW (1) TWI401241B (es)
UA (1) UA97362C2 (es)
WO (1) WO2007120554A2 (es)
ZA (1) ZA200808752B (es)

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US8575403B2 (en) 2010-05-07 2013-11-05 Celanese International Corporation Hydrolysis of ethyl acetate in ethanol separation process
US8710279B2 (en) 2010-07-09 2014-04-29 Celanese International Corporation Hydrogenolysis of ethyl acetate in alcohol separation processes
US9272970B2 (en) 2010-07-09 2016-03-01 Celanese International Corporation Hydrogenolysis of ethyl acetate in alcohol separation processes
US8664454B2 (en) 2010-07-09 2014-03-04 Celanese International Corporation Process for production of ethanol using a mixed feed using copper containing catalyst
US8846988B2 (en) 2010-07-09 2014-09-30 Celanese International Corporation Liquid esterification for the production of alcohols
US8907141B2 (en) 2011-04-26 2014-12-09 Celanese International Corporation Process to recover alcohol with secondary reactors for esterification of acid
US9024082B2 (en) 2011-04-26 2015-05-05 Celanese International Corporation Using a dilute acid stream as an extractive agent
WO2012149137A1 (en) 2011-04-26 2012-11-01 Celanese International Corporation Process for the production of ethanol from an acetic acid feed and a recycled ethyl acetate feed
US8884081B2 (en) 2011-04-26 2014-11-11 Celanese International Corporation Integrated process for producing acetic acid and alcohol
US9073816B2 (en) 2011-04-26 2015-07-07 Celanese International Corporation Reducing ethyl acetate concentration in recycle streams for ethanol production processes
US8754268B2 (en) 2011-04-26 2014-06-17 Celanese International Corporation Process for removing water from alcohol mixtures
US8927788B2 (en) 2011-04-26 2015-01-06 Celanese International Corporation Process to recover alcohol with reduced water from overhead of acid column
US8933278B2 (en) 2011-04-26 2015-01-13 Celanese International Corporation Process for producing ethanol and reducing acetic acid concentration
US8686200B2 (en) 2011-04-26 2014-04-01 Celanese International Corporation Process to recover alcohol from an acidic residue stream
US8927787B2 (en) 2011-04-26 2015-01-06 Celanese International Corporation Process for controlling a reboiler during alcohol recovery and reduced ester formation
US9024085B2 (en) 2011-04-26 2015-05-05 Celanese International Corporation Process to reduce ethanol recycled to hydrogenation reactor
CN103080053B (zh) 2011-04-26 2015-08-12 国际人造丝公司 使用叠置床反应器生产乙醇的方法
US9000232B2 (en) 2011-04-26 2015-04-07 Celanese International Corporation Extractive distillation of crude alcohol product
US8686199B2 (en) 2011-04-26 2014-04-01 Celanese International Corporation Process for reducing the concentration of acetic acid in a crude alcohol product
US8927784B2 (en) 2011-04-26 2015-01-06 Celanese International Corporation Process to recover alcohol from an ethyl acetate residue stream
US9000233B2 (en) 2011-04-26 2015-04-07 Celanese International Corporation Process to recover alcohol with secondary reactors for hydrolysis of acetal
US9024084B2 (en) 2011-04-26 2015-05-05 Celanese International Corporation Reduced energy alcohol separation process having controlled pressure
US8592635B2 (en) 2011-04-26 2013-11-26 Celanese International Corporation Integrated ethanol production by extracting halides from acetic acid
US8895786B2 (en) 2011-08-03 2014-11-25 Celanese International Corporation Processes for increasing alcohol production
US8829253B2 (en) 2011-08-19 2014-09-09 Celanese International Corporation Integrated process for producing ethanol from methanol
US8853467B2 (en) 2011-08-19 2014-10-07 Celanese International Corporation Integrated process for producing ethanol
US8853466B2 (en) 2011-08-19 2014-10-07 Celanese International Corporation Integrated process for producing ethanol from methanol
US8809599B2 (en) 2011-11-09 2014-08-19 Celanese International Corporation Integrated process for producing ethanol and water balance control
US8809598B2 (en) 2011-11-09 2014-08-19 Celanese International Corporation Producing ethanol using two different streams from acetic acid carbonylation process
US8686201B2 (en) 2011-11-09 2014-04-01 Celanese International Corporation Integrated acid and alcohol production process having flashing to recover acid production catalyst
US8704013B2 (en) 2011-11-09 2014-04-22 Celanese International Corporation Integrated process for producing ethanol
US8614359B2 (en) 2011-11-09 2013-12-24 Celanese International Corporation Integrated acid and alcohol production process
US8703868B2 (en) 2011-11-28 2014-04-22 Celanese International Corporation Integrated process for producing polyvinyl alcohol or a copolymer thereof and ethanol
US8697802B2 (en) 2011-11-28 2014-04-15 Celanese International Corporation Process for producing polyvinyl alcohol or a copolymer thereof
WO2013101305A1 (en) 2011-12-30 2013-07-04 Celanese International Corporation Pressure driven distillation for producing and recovering ethanol from hydrogenation process
US9353034B2 (en) 2012-02-07 2016-05-31 Celanese International Corporation Hydrogenation process with reduced residence time for vapor phase reactants
CA2976310A1 (en) 2015-02-25 2016-09-01 Sabic Global Technologies B.V. Process for removing impurities from acetic acid
CN109232223A (zh) * 2018-11-02 2019-01-18 江苏索普（集团）有限公司 一种合成醋酸的工艺

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Also Published As

Publication number Publication date
CN101511766A (zh) 2009-08-19
RU2008144960A (ru) 2010-05-20
ES2421741T3 (es) 2015-10-23
WO2007120554A2 (en) 2007-10-25
AU2007238948B2 (en) 2010-09-02
BRPI0710016A2 (pt) 2011-08-02
TWI401241B (zh) 2013-07-11
MX2008013270A (es) 2009-03-06
AR060454A1 (es) 2008-06-18
US8076506B2 (en) 2011-12-13
CL2007001035A1 (es) 2008-01-04
CA2649298C (en) 2011-10-11
EP2054366B1 (en) 2017-08-09
CA2649298A1 (en) 2007-10-25
KR101377835B1 (ko) 2014-03-24
ZA200808752B (en) 2010-08-25
EP2054366A2 (en) 2009-05-06
JP2009533434A (ja) 2009-09-17
DE12007339T8 (de) 2014-01-09
MY155307A (en) 2015-09-30
NZ571943A (en) 2010-07-30
WO2007120554A3 (en) 2009-04-16
EP2562153B1 (en) 2015-07-22
CN104529701A (zh) 2015-04-22
RU2437871C2 (ru) 2011-12-27
EP2562153A1 (en) 2013-02-27
KR20080112375A (ko) 2008-12-24
DE12007339T1 (de) 2013-07-11
UA97362C2 (ru) 2012-02-10
US20100204512A1 (en) 2010-08-12
NO20084790L (no) 2008-11-13
AU2007238948A1 (en) 2007-10-25
TW200800878A (en) 2008-01-01
JP5486299B2 (ja) 2014-05-07

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