WO2000034216A1 - Process for preparing trichloroalkane derivatives - Google Patents
Process for preparing trichloroalkane derivatives Download PDFInfo
- Publication number
- WO2000034216A1 WO2000034216A1 PCT/GB1999/003942 GB9903942W WO0034216A1 WO 2000034216 A1 WO2000034216 A1 WO 2000034216A1 GB 9903942 W GB9903942 W GB 9903942W WO 0034216 A1 WO0034216 A1 WO 0034216A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- alkyl
- process according
- hydrogen
- alkenyl
- trichloroalkane
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B82—NANOTECHNOLOGY
- B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
- B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
-
- 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
- C07C29/62—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by introduction of halogen; by substitution of halogen atoms by other halogen atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C17/00—Preparation of halogenated hydrocarbons
- C07C17/26—Preparation of halogenated hydrocarbons by reactions involving an increase in the number of carbon atoms in the skeleton
- C07C17/272—Preparation of halogenated hydrocarbons by reactions involving an increase in the number of carbon atoms in the skeleton by addition reactions
- C07C17/275—Preparation 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
Definitions
- the present invention relates to a process for preparing trichloroalkane derivatives by the photochemically initiated addition of chloroform to an alkene derivative.
- the process is of particular use for the production of 4,4,4-trichlorobutane derivatives which are important intermediates and products in the chemical industry.
- 4,4,4-trichlorobutane derivatives are useful as intermediates in the manufacture of pesticidal compounds of the type described in, for example, WO 95/24403.
- 4,4,4-Trichlorobutane derivatives may also be used as intermediates in the manufacture of compounds having useful solvent properties.
- a process for the production of a trichloroalkane derivative comprising reacting an alkene derivative with chloroform, characterised in that the process is initiated by photochemical cleavage of an initiator of formula (I):
- Z is chloro or fluoro
- X is hydrogen, C, ⁇ alkyl, C,_ 6 haloalkyl, -O-O-C(O)-Y or -O-O-Y
- Y is hydrogen, C w alkyl or C ⁇ haloalkyl.
- Alkyl is straight or branched chain and is, for example, methyl, ethyl, w-propyl, w-butyl, H-pentyl, w-hexyl, .sO-propyl, /7-butyl, sec-butyl, wo-butyl, tert-butyl or «e ⁇ -pentyl.
- Haloalkyl groups are alkyl groups which are optionally substituted with one or more of the same or different halogen atoms. Halogen is fluorine, chlorine, bromine or iodine.
- the process of the invention may provide higher yields of the trichloroalkane derivative and fewer by-products than corresponding processes, for example, those using thermal initiation, or photochemical processes performed in the absence of an initiator or with an initiator not having a trihalocarbonyl group.
- the three Z groups in the initiator of formula (I) may be the same or different.
- CZ 3 may be, for example, CF 2 C1, however CZ 3 is preferably CC1 3 .
- X is preferably C w haloalkyl or -O-O-Y, wherein Y is C w haloalkyl.
- Haloalkyl is preferably CF 2 C1, more preferably CC1 3 .
- Preferred examples of initiators of formula (I) include 1,3-dichloro-l, 1,3,3- tetrafluoroacetone, chloral and, especially, hexachloroacetone.
- the alkene derivative used in the process of the invention preferably has a terminal double bond.
- the process of the invention is of particular use for the production of 4,4,4-trichlorobutane derivatives, as illustrated in Scheme I below, wherein Z and X are as described above for formula (I);
- W is C, ⁇ alkyl, C w alkenyl, OR 1 or NR 2 R 3 ;
- R 1 is hydrogen, C, ⁇ alkyl, C 2 . 6 alkenyl, C 6 . l0 aryl or R 4 C(O);
- R 2 and R 3 are, independently, hydrogen, C,. 6 alkyl, C ⁇ alkenyl or C 6 . 10 aryl; and
- R 4 is C,. 6 alkyl, C 2.6 alkenyl, C 6.I0 aryl, C, ⁇ alkyloxy, C 2 . 6 alkenyloxy or C 6 . I0 aryloxy.
- Alkenyl moieties may be in the form of straight or branched chains and, where appropriate, may be of either (E)- or (Z)-conf ⁇ guration. Examples include vinyl and allyl.
- Aryl is phenyl or naphthyl. Therefore, in a preferred aspect of the invention the alkene derivative is a compound of formula (II):
- W is C ⁇ alkyl, C 2 . 6 alkenyl, OR 1 or NR 2 R 3 ;
- R 1 is hydrogen, C,. 6 alkyl, C 2.6 alkenyl, C 6 ., 0 aryl or R C(O);
- R 2 and R 3 are, independently, hydrogen, C,. 6 alkyl, C 2 ⁇ alkenyl or C 6.
- R 4 is C,. 6 alkyl, C 2 . 6 alkenyl, C 6 . 10 aryl, C, ⁇ alkyloxy, C 2.6 alkenyloxy or C 6 ., 0 aryloxy.
- Initiation of the process of the invention is preferably achieved by irradiating the reaction mixture with light of a wavelength of from about 200 to about 600nm, more preferably 200 to 350nm, for example a wavelength of 254nm.
- the light may be supplied by a low, medium or high pressure mercury lamp.
- the reaction is preferably conducted at a temperature of about 0 to about 150°C and a temperature of from 25 to 150°C (such as 25 to 70°C) is particularly preferred.
- the period of the reaction may be from about 30minutes to about 24hours, depending upon the volume of reactants and the temperature used. Generally a period of from about lhour to 12hours is sufficient.
- EXAMPLE 1 This Example illustrates various preparations of 4,4,4-trichlorobutanol and the tabulated results show the increased 'yield on conversion' obtained when using the process of the invention compared to the corresponding process in the absence of an initiator.
- the general procedure used in each case was the same: Chloroform was degassed for lhour with nitrogen immediately prior to use. A photochemical cell fitted with a condenser was charged with chloroform, allyl alcohol and (where appropriate) an initiator. The reaction mass was then degassed with nitrogen for a further 15minutes. The vessel was covered in aluminium foil and a uv screen was fitted. The reaction mixture was heated to the stated temperature using an oil bath, whereupon irradiation was carried out for the stated period of time, using light of the stated wavelength. Analysis of the reaction mixture was carried out by GC analysis.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Nanotechnology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Composite Materials (AREA)
- Condensed Matter Physics & Semiconductors (AREA)
- General Physics & Mathematics (AREA)
- Materials Engineering (AREA)
- Crystallography & Structural Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
Claims
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP99956225A EP1137618A1 (en) | 1998-12-09 | 1999-11-25 | Process for preparing trichloroalkane derivatives |
AU12868/00A AU1286800A (en) | 1998-12-09 | 1999-11-25 | Process for preparing trichloroalkane derivatives |
JP2000586666A JP2002531537A (en) | 1998-12-09 | 1999-11-25 | Process for producing trichloroalkane derivatives |
KR1020017007013A KR20010101129A (en) | 1998-12-09 | 1999-11-25 | Process for preparing trichloroalkane derivatives |
IL14330699A IL143306A0 (en) | 1998-12-09 | 1999-11-25 | Process for preparing trichloroalkane derivatives |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GBGB9827133.1A GB9827133D0 (en) | 1998-12-09 | 1998-12-09 | Chemical process |
GB9827133.1 | 1998-12-09 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2000034216A1 true WO2000034216A1 (en) | 2000-06-15 |
Family
ID=10843943
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/GB1999/003942 WO2000034216A1 (en) | 1998-12-09 | 1999-11-25 | Process for preparing trichloroalkane derivatives |
Country Status (8)
Country | Link |
---|---|
EP (1) | EP1137618A1 (en) |
JP (1) | JP2002531537A (en) |
KR (1) | KR20010101129A (en) |
AU (1) | AU1286800A (en) |
GB (1) | GB9827133D0 (en) |
IL (1) | IL143306A0 (en) |
WO (1) | WO2000034216A1 (en) |
ZA (1) | ZA200104182B (en) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CH271369A (en) * | 1945-12-15 | 1950-10-31 | Us Rubber Co | A process for preparing a halogenated olefinic compound. |
US4475003A (en) * | 1982-09-13 | 1984-10-02 | Basf Aktiengesellschaft | Preparation of 1,1,1-trichloromethyl compounds |
GB2303368A (en) * | 1995-07-17 | 1997-02-19 | Zeneca Ltd | Trichlorobutyl acetate production |
GB2315068A (en) * | 1996-07-08 | 1998-01-21 | Zeneca Ltd | Preparation of 4,4,4-trichlorobutan-1-ol |
-
1998
- 1998-12-09 GB GBGB9827133.1A patent/GB9827133D0/en not_active Ceased
-
1999
- 1999-11-25 AU AU12868/00A patent/AU1286800A/en not_active Abandoned
- 1999-11-25 JP JP2000586666A patent/JP2002531537A/en active Pending
- 1999-11-25 IL IL14330699A patent/IL143306A0/en unknown
- 1999-11-25 KR KR1020017007013A patent/KR20010101129A/en not_active Application Discontinuation
- 1999-11-25 EP EP99956225A patent/EP1137618A1/en not_active Withdrawn
- 1999-11-25 WO PCT/GB1999/003942 patent/WO2000034216A1/en not_active Application Discontinuation
-
2001
- 2001-05-22 ZA ZA200104182A patent/ZA200104182B/en unknown
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CH271369A (en) * | 1945-12-15 | 1950-10-31 | Us Rubber Co | A process for preparing a halogenated olefinic compound. |
US4475003A (en) * | 1982-09-13 | 1984-10-02 | Basf Aktiengesellschaft | Preparation of 1,1,1-trichloromethyl compounds |
GB2303368A (en) * | 1995-07-17 | 1997-02-19 | Zeneca Ltd | Trichlorobutyl acetate production |
GB2315068A (en) * | 1996-07-08 | 1998-01-21 | Zeneca Ltd | Preparation of 4,4,4-trichlorobutan-1-ol |
Also Published As
Publication number | Publication date |
---|---|
EP1137618A1 (en) | 2001-10-04 |
AU1286800A (en) | 2000-06-26 |
KR20010101129A (en) | 2001-11-14 |
JP2002531537A (en) | 2002-09-24 |
ZA200104182B (en) | 2002-08-22 |
GB9827133D0 (en) | 1999-02-03 |
IL143306A0 (en) | 2002-04-21 |
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