ES2554979T3 - Proceso para la preparación de fluoroalquenos C3-7 por deshidrohalogenación mediada por base de fluoroalcanos C3-7 hidrohalogenados - Google Patents

Proceso para la preparación de fluoroalquenos C3-7 por deshidrohalogenación mediada por base de fluoroalcanos C3-7 hidrohalogenados Download PDF

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Publication number
ES2554979T3
ES2554979T3 ES07848577.8T ES07848577T ES2554979T3 ES 2554979 T3 ES2554979 T3 ES 2554979T3 ES 07848577 T ES07848577 T ES 07848577T ES 2554979 T3 ES2554979 T3 ES 2554979T3
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fluoroalkenes
hydrohalogenated
fluoroalkanes
dehydrohalogenation
mediated
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Andrew Paul Sharratt
Robert Elliott Low
John Charles Mccarthy
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Mexichem Fluor SA de CV
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Mexichem Fluor SA de CV
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C21/00Acyclic unsaturated compounds containing halogen atoms
    • C07C21/02Acyclic unsaturated compounds containing halogen atoms containing carbon-to-carbon double bonds
    • C07C21/18Acyclic unsaturated compounds containing halogen atoms containing carbon-to-carbon double bonds containing fluorine
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/61Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups
    • C07C45/63Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by introduction of halogen; by substitution of halogen atoms by other halogen atoms
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/25Preparation of halogenated hydrocarbons by splitting-off hydrogen halides from halogenated hydrocarbons
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/013Preparation of halogenated hydrocarbons by addition of halogens
    • C07C17/04Preparation of halogenated hydrocarbons by addition of halogens to unsaturated halogenated hydrocarbons
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/093Preparation of halogenated hydrocarbons by replacement by halogens
    • C07C17/18Preparation of halogenated hydrocarbons by replacement by halogens of oxygen atoms of carbonyl groups
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/093Preparation of halogenated hydrocarbons by replacement by halogens
    • C07C17/20Preparation of halogenated hydrocarbons by replacement by halogens of halogen atoms by other halogen atoms
    • C07C17/202Preparation of halogenated hydrocarbons by replacement by halogens of halogen atoms by other halogen atoms two or more compounds being involved in the reaction
    • C07C17/206Preparation of halogenated hydrocarbons by replacement by halogens of halogen atoms by other halogen atoms two or more compounds being involved in the reaction the other compound being HX
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/26Preparation of halogenated hydrocarbons by reactions involving an increase in the number of carbon atoms in the skeleton
    • C07C17/272Preparation of halogenated hydrocarbons by reactions involving an increase in the number of carbon atoms in the skeleton by addition reactions
    • C07C17/275Preparation of halogenated hydrocarbons by reactions involving an increase in the number of carbon atoms in the skeleton by addition reactions of hydrocarbons and halogenated hydrocarbons

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Catalysts (AREA)

Abstract

Un proceso de preparación de un compuesto de fórmula CF3CF>=CHX, en donde X es H o F, proceso que comprende deshidrohalogenar un compuesto de fórmula CF3CFYCH2X o CF3CFHCYHX, en donde Y es F, Cl, Br o I, en presencia de una base seleccionada de un hidróxido de metal alcalino y un hidróxido de metal alcalinotérreo, llevándose a cabo el proceso en un disolvente que comprende N-metilpirrolidona.

Description

imagen1
imagen2
imagen3
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imagen5
acetona. En una vía de síntesis tal, la acetona puede clorarse (por ejemplo, usando cloro sobre un catalizador de cromia) para producir 1,1,1-tricloroacetona, que puede clorarse adicionalmente (por ejemplo, usando PCl5 -véase Advanced Organic Chemistry (Ed M B Smith y J March), Quinta Edición, página 1195) para producir 1,1,1,2,2pentacloropropano, como se ilustra a continuación.
imagen6
Puede prepararse HFC-1225ye deshidrohalogenando un compuesto de fórmula CF3CFYCH2F o CF3CFHCYFH, en las que Y es F, Cl, Br o I, preferentemente F o Cl, lo más preferentemente F. Así, HFC-1225ye se prepara 10 actualmente lo más preferentemente por la deshidrofluoración de CF3CFHCF2H (HFC-236ea) o CF3CF2CH2F (HFC236cb), como se ilustra a continuación.
imagen7
15 HFC-1225ye existe como dos isómeros geométricos, como se ilustra a continuación.
imagen8
Tanto HFC-236ea como HFC-236cb pueden obtenerse de Apollo Chemicals Ltd. Alternativamente, HFC-236ea, por 20 ejemplo, puede prepararse convenientemente hidrogenando hexafluoropropileno del siguiente modo.
CF3CF=CF2 + H2 → CF3CHFCHF2
Los (hidro)fluoroalquenos que pueden prepararse por la presente invención tienen numerosas utilidades, por 25 ejemplo, como refrigerantes, monómeros, materias primas y disolventes.
La invención se ilustrará ahora, pero no se limita, por los siguientes ejemplos. La invención se define por las reivindicaciones que siguen a los ejemplos.
30 Ejemplos
Ejemplos comparativos 1-7
Se cargaron disolvente (10 g), hidróxido de metal alcalino (10 g) y (si se usa) catalizador (0,25 g) a un recipiente de
35 Hastalloy C de 50 ml equipado con indicadores de temperatura y de presión y un agitador cruciforme. El recipiente se selló y la presión se probó con nitrógeno. Entonces se cargó una alimentación de o bien CF3CFHCF2H (HFC236ea) o bien CF3CF2CH2F (HFC-236cb) (10-15 g, 97 %) desde una pequeña bomba de alimentación y el contenido se calentó a 150 ºC durante los tiempos especificados en la Tabla 1 con agitación. Al final del experimento, los productos volátiles y cualquier alimentación sin convertir se recuperaron mediante destilación para el análisis por
40 CG-EM. Los resultados se ilustran en la Tabla 1.
7
Tabla 1: 236ea/cb → 1225ye
Expt Nº
Isómero HFC236 Disolvente Base Catalizador Tiempo (h) Conversión (%) Z1225ye (%) E1225ye (%) 1225 zc (%)
1
ea agua KOH - 3,5 57,8 46,7 5,7 0
2
ea agua NaOH - 4,5 20,8 14,9 1,7 0
3
ea agua KOH - 19 21,4 15,9 1,3 0
4
ea agua KOH 18-corona-6 2,5 57,5 49,3 4,1 0
5
ea PEG300 KOH - 3 50,4 41 2,8 0
6
cb agua KOH - 19 1,3 0,52 0 N/A
7
cb agua KOH - 22 1,5 0,42 0 N/A
Ejemplos 8-22
5 Se cargaron base, disolvente y catalizador, si se usó, al recipiente de reacción. El recipiente de reacción se selló, se probó la presión y se evacuó. Entonces se transfirió una cantidad previamente pesada de la alimentación orgánica al reactor. El reactor y su contenido se pesaron entonces antes de calentarse de temperatura ambiente a 150 ºC durante 45 minutos con agitación. Esta temperatura se mantuvo con agitación a 1500 rpm durante 6 horas. Después de este periodo, el reactor y su contenido se enfriaron a 10 ºC durante 30 minutos y la tasa de agitación se redujo a
10 200 rpm.
Al día siguiente, el reactor y su contenido se volvieron a pesar y a continuación el reactor se volvió a calentar a 50 ºC listo para la recuperación de productos. Los productos y cualquier material de partida sin reaccionar se recuperaron mediante destilación en una bomba de muestra previamente pesada y enfriada (-78 ºC) evacuada. El peso de los
15 productos recuperados se determinó antes de analizarse por CG-EM. La CG-EM se calibró usando muestras de alimentación y de producto si estuvieron disponibles. Se cuantificaron los desconocidos usando factores de respuesta relativa promedio. Los resultados se presentan en las Tablas 2-4.
8
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imagen11

Claims (1)

  1. imagen1
ES07848577.8T 2006-12-19 2007-12-18 Proceso para la preparación de fluoroalquenos C3-7 por deshidrohalogenación mediada por base de fluoroalcanos C3-7 hidrohalogenados Active ES2554979T3 (es)

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Application Number Priority Date Filing Date Title
GB0625214 2006-12-19
GBGB0625214.2A GB0625214D0 (en) 2006-12-19 2006-12-19 Process
PCT/GB2007/004840 WO2008075017A2 (en) 2006-12-19 2007-12-18 Process for the preparation of c3-7 fluoroalkenes by base-mediated dehydrohalogenatation of hydrohalogenated c3 -7 fluoroalkanes

Publications (1)

Publication Number Publication Date
ES2554979T3 true ES2554979T3 (es) 2015-12-28

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Application Number Title Priority Date Filing Date
ES21165666T Active ES2963129T3 (es) 2006-12-19 2007-12-18 Proceso para la preparación de 2,3,3,3-tetrahidrofluoropropeno
ES07848577.8T Active ES2554979T3 (es) 2006-12-19 2007-12-18 Proceso para la preparación de fluoroalquenos C3-7 por deshidrohalogenación mediada por base de fluoroalcanos C3-7 hidrohalogenados
ES15186285T Active ES2874904T3 (es) 2006-12-19 2007-12-18 Proceso para la preparación de 2,3,3,3-tetrafluoropropeno
ES21165589T Active ES2964858T3 (es) 2006-12-19 2007-12-18 Proceso para la preparación de 2,3,3,3-tetrahidrofluoropropeno

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ES15186285T Active ES2874904T3 (es) 2006-12-19 2007-12-18 Proceso para la preparación de 2,3,3,3-tetrafluoropropeno
ES21165589T Active ES2964858T3 (es) 2006-12-19 2007-12-18 Proceso para la preparación de 2,3,3,3-tetrahidrofluoropropeno

Country Status (16)

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US (3) US8410325B2 (es)
EP (5) EP2121548B1 (es)
JP (3) JP5391076B2 (es)
KR (3) KR101450159B1 (es)
CN (2) CN101563308A (es)
AU (1) AU2007336066A1 (es)
BR (1) BRPI0720532A2 (es)
CA (1) CA2673585C (es)
DK (2) DK3872058T3 (es)
ES (4) ES2963129T3 (es)
GB (1) GB0625214D0 (es)
MX (1) MX2009006433A (es)
PL (1) PL2121548T3 (es)
RU (2) RU2466121C2 (es)
WO (1) WO2008075017A2 (es)
ZA (1) ZA200904246B (es)

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