MX375208B - Procedimiento continuo para preparar etilenglicol a partir de una fuente de carbohidratos. - Google Patents

Procedimiento continuo para preparar etilenglicol a partir de una fuente de carbohidratos.

Info

Publication number
MX375208B
MX375208B MX2017009161A MX2017009161A MX375208B MX 375208 B MX375208 B MX 375208B MX 2017009161 A MX2017009161 A MX 2017009161A MX 2017009161 A MX2017009161 A MX 2017009161A MX 375208 B MX375208 B MX 375208B
Authority
MX
Mexico
Prior art keywords
carbohydrate source
ethylene glycol
continuous process
hydrogen
stirred tank
Prior art date
Application number
MX2017009161A
Other languages
English (en)
Other versions
MX2017009161A (es
Inventor
Gerardus Johannes Maria Gruter
Der Waal Jan Cornelis Van
Original Assignee
Avantium Knowledge Centre Bv
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=52781246&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=MX375208(B) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Avantium Knowledge Centre Bv filed Critical Avantium Knowledge Centre Bv
Publication of MX2017009161A publication Critical patent/MX2017009161A/es
Publication of MX375208B publication Critical patent/MX375208B/es

Links

Classifications

    • 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
    • C07C29/132—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
    • 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053—Details of the reactor
    • B01J19/0066—Stirrers
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
    • C07B31/00—Reduction in general
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C31/00—Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
    • C07C31/18—Polyhydroxylic acyclic alcohols
    • C07C31/20—Dihydroxylic alcohols
    • C07C31/202—Ethylene glycol
    • 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
    • B01J2219/00027—Process aspects
    • B01J2219/00033—Continuous processes
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • C07C2523/24—Chromium, molybdenum or tungsten
    • C07C2523/30—Tungsten
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
    • C07C2523/89—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper combined with noble metals
    • 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)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

Se prepara el etilenglicol a partir de una fuente de carbohidratos mediante la reacción de la fuente de carbohidratos con hidrógeno en un procedimiento continuo; en donde el hidrógeno, la fuente de carbohidratos y un diluyente líquido se suministran continuamente en un reactor de tanque agitado continuo en donde un sistema catalizador está presente, cuyo sistema catalizador comprende un compuesto de tungsteno y por lo menos una hidrogenólisis de metal seleccionado de los grupos 8, 9 o 10 de la Tabla Periódica de Elementos, para lograr la reacción entre la fuente de carbohidratos e hidrógeno con etilenglicol; en donde se remueve continuamente una mezcla de productos que comprende etilenglicol y diluyente del reactor de tanque agitado continuo y en donde se agrega continuamente o periódicamente por lo menos un compuesto de tungsteno al reactor de tanque agitado continuo (CSTR).
MX2017009161A 2015-01-13 2016-01-13 Procedimiento continuo para preparar etilenglicol a partir de una fuente de carbohidratos. MX375208B (es)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
NL2014121 2015-01-13
PCT/NL2016/050029 WO2016114661A1 (en) 2015-01-13 2016-01-13 Continuous process for preparing ethylene glycol from a carbohydrate source

Publications (2)

Publication Number Publication Date
MX2017009161A MX2017009161A (es) 2018-02-01
MX375208B true MX375208B (es) 2025-03-06

Family

ID=52781246

Family Applications (1)

Application Number Title Priority Date Filing Date
MX2017009161A MX375208B (es) 2015-01-13 2016-01-13 Procedimiento continuo para preparar etilenglicol a partir de una fuente de carbohidratos.

Country Status (15)

Country Link
US (1) US10138184B2 (es)
EP (1) EP3245181B1 (es)
JP (1) JP6553743B2 (es)
KR (1) KR20170105063A (es)
CN (1) CN107406358B (es)
AU (1) AU2016207242B2 (es)
BR (1) BR112017014945B1 (es)
CA (1) CA2973556C (es)
LT (1) LT3245181T (es)
MX (1) MX375208B (es)
MY (1) MY185257A (es)
PL (1) PL3245181T3 (es)
SG (1) SG11201705686RA (es)
UA (1) UA118147C2 (es)
WO (1) WO2016114661A1 (es)

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EP3245183B1 (en) 2015-01-13 2019-10-23 Avantium Knowledge Centre B.v. Process for preparing ethylene glycol from a carbohydrate source
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WO2017070071A1 (en) 2015-10-20 2017-04-27 Shell Oil Company Process for the production of glycols
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US10472310B2 (en) 2016-06-03 2019-11-12 Iowa Corn Promotion Board Continuous processes for the highly selective conversion of sugars to propylene glycol or mixtures of propylene glycol and ethylene glycol
WO2018024787A1 (en) 2016-08-04 2018-02-08 Shell Internationale Research Maatschappij B.V. Process for the production of glycols
EP3507267B1 (en) * 2016-08-30 2021-02-17 Shell Internationale Research Maatschappij B.V. Magnetic separation and recycle of catalyst components in a bio-mass to glycols process
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ES2925554T3 (es) * 2018-03-14 2022-10-18 Avantium Knowledge Centre Bv Proceso para la producción de etilenglicol
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WO2020055831A1 (en) 2018-09-13 2020-03-19 Shell Oil Company Start-up process for the production of glycols
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US11319269B2 (en) 2020-09-24 2022-05-03 Iowa Corn Promotion Board Continuous processes for the selective conversion of aldohexose-yielding carbohydrate to ethylene glycol using low concentrations of retro-aldol catalyst
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BR112023004203A2 (pt) 2020-09-28 2023-04-11 Avantium Knowledge Centre Bv Processo para produzir etilenoglicol e/ou propilenoglicol e/ou glicerol
EP4326698B1 (en) 2021-04-21 2025-06-04 Avantium Knowledge Centre B.V. Process and equipment for producing glycols from carbohydrates and hydrogen with reactor off-gas treatment and hydrogen production
EP4466245A1 (en) * 2022-01-19 2024-11-27 T.En Process Technology, Inc. Processes for making ethylene glycol and/or propylene glycol from aldose- and/or ketose-yielding carbohydrates with integrated tungsten catalyst recovery
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WO2025026823A1 (en) 2023-08-01 2025-02-06 Avantium Knowledge Centre B.V. Process for reducing the amount of 2,3-pentanediol from propylene glycol
CN121605096A (zh) 2023-08-01 2026-03-03 阿凡田知识中心有限公司 降低乙二醇中1,2-戊二醇含量的方法
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MY184090A (en) 2014-05-19 2021-03-17 Iowa Corn Promotion Board Process for the continuous production of ethylene glycol from carbohydrates
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Also Published As

Publication number Publication date
LT3245181T (lt) 2020-02-25
CA2973556C (en) 2019-04-30
EP3245181A1 (en) 2017-11-22
KR20170105063A (ko) 2017-09-18
AU2016207242A1 (en) 2017-08-03
PL3245181T3 (pl) 2020-06-29
MX2017009161A (es) 2018-02-01
US20180002259A1 (en) 2018-01-04
CA2973556A1 (en) 2016-07-21
CN107406358A (zh) 2017-11-28
JP6553743B2 (ja) 2019-07-31
CN107406358B (zh) 2020-12-08
WO2016114661A1 (en) 2016-07-21
US10138184B2 (en) 2018-11-27
MY185257A (en) 2021-04-30
BR112017014945A2 (pt) 2018-03-13
SG11201705686RA (en) 2017-08-30
UA118147C2 (uk) 2018-11-26
AU2016207242B2 (en) 2018-09-13
EP3245181B1 (en) 2019-10-23
BR112017014945B1 (pt) 2021-06-08
JP2018501321A (ja) 2018-01-18

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