WO2000069805A1 - Processes for preparing pesticidal intermediates - Google Patents

Processes for preparing pesticidal intermediates Download PDF

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Publication number
WO2000069805A1
WO2000069805A1 PCT/EP2000/004595 EP0004595W WO0069805A1 WO 2000069805 A1 WO2000069805 A1 WO 2000069805A1 EP 0004595 W EP0004595 W EP 0004595W WO 0069805 A1 WO0069805 A1 WO 0069805A1
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WIPO (PCT)
Prior art keywords
formula
acid addition
addition salt
process according
preparation
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PCT/EP2000/004595
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French (fr)
Inventor
Jean-Erick Ancel
Gilles Perrin-Janet
Pierre Leroy
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Bayer CropScience SA
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Aventis CropScience SA
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Priority to IL14605400A priority Critical patent/IL146054A0/en
Priority to DE60012172T priority patent/DE60012172T2/en
Priority to US10/030,324 priority patent/US6509503B1/en
Priority to AU52146/00A priority patent/AU766505B2/en
Priority to BR0010540-6A priority patent/BR0010540A/en
Priority to AT00936766T priority patent/ATE271027T1/en
Priority to JP2000618224A priority patent/JP2002544251A/en
Priority to EP00936766A priority patent/EP1177165B1/en
Publication of WO2000069805A1 publication Critical patent/WO2000069805A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C209/00—Preparation of compounds containing amino groups bound to a carbon skeleton
    • C07C209/30—Preparation of compounds containing amino groups bound to a carbon skeleton by reduction of nitrogen-to-oxygen or nitrogen-to-nitrogen bonds
    • C07C209/42—Preparation of compounds containing amino groups bound to a carbon skeleton by reduction of nitrogen-to-oxygen or nitrogen-to-nitrogen bonds by reduction of nitrogen-to-nitrogen bonds
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C241/00—Preparation of compounds containing chains of nitrogen atoms singly-bound to each other, e.g. hydrazines, triazanes
    • C07C241/02—Preparation of hydrazines

Definitions

  • This invention relates to novel processes for preparing intermediates (particularly certain aniline compounds and phenylhydrazine derivatives) useful in the preparation of pesticides.
  • 3,5-Dihaloanilines and particularly 3,5-dichloroaniline are important synthetic intermediates for a number of valuable compounds including agrochemical fungicides for example as described in US Patent Publication Numbers 3755350 and 3903090, or German Patent
  • the present invention accordingly provides a process (A) for the preparation of a substituted aniline of formula (I):
  • R.1 and R-2 each independently represent a halogen atom; or an acid addition salt thereof; which process comprises the hydrogenolysis of a substituted phenylhydrazine of formula (II):
  • halogen atoms are selected from fluorine, chlorine, bromine and iodine.
  • the acid addition salts referred to in the invention are preferably the salts formed from strong acids such as mineral acids, for example sulphuric acid or hydrochloric acid.
  • the hydrogenolysis may be performed using a metal or metal salt selected from Raney nickel (a nickel-aluminium alloy) optionally in the presence of iron, manganese, cobalt, copper, zinc or chromium; stannous chloride; zinc in the presence of acetic acid; and a molybdenum (III) salt.
  • the reaction may also be carried out using Raney nickel, platinum or palladium (which may be supported on charcoal or other inert material) in the presence of hydrogen gas. When the reaction is performed with hydrogen gas a pressure of 2 to 20 bars (preferably 5 to 10 bars) is generally used.
  • the hydrogenolysis is preferably performed using Raney nickel.
  • the reaction may be performed in the absence or presence of a solvent, but is generally conducted in a solvent which may be selected from alcohols such as methanol, ethanol, propanol, isopropanol, butanol, isobutanol or tertiary butanol; ethers; aromatic hydrocarbons and water (or mixtures thereof). Methanol and ethanol are preferred solvents.
  • the reaction temperature is generally from 20 C to 150 C, preferably from 20 C to 90 C.
  • the amount of catalyst employed is generally from 0.01 to 3 molar equivalents (preferably from 0.05 to 2 molar equivalents), although when the reaction is carried out under an atmosphere of hydrogen, a smaller amount generally gives satisfactory results.
  • Process (A) seeks to enable substituted aniline compounds of formula (I) and their acid addition salts thereof to be obtained in high yield from readily available starting materials. Furthermore the reaction can be very simple and economical to perform, and product isolation can be straightforward. Another advantage of this method is that these compounds of formula (I) may be prepared at moderate temperatures and pressures, whereas prior art methods require high temperatures and pressures.
  • halogen atoms which represent Rl,R2 and X in formula (III) so that the group X is more reactive than R and R ⁇
  • substituted phenylhydrazines of formula (II) and salts thereof having the various combinations of halogen atoms Particularly preferred compounds are those wherein R and R2 in formulae (I) and (II) each represent a chlorine atom.
  • Compounds of formula (III) are generally known.
  • hydrazine hydrate is used in the process.
  • a base such as a trialkylamine (for example triethylamine) is optionally present.
  • a particularly preferred compound of formula (III) is 1,3,5- trichlorobenzene.
  • the reaction may be conducted in a solvent chosen from cyclic and aliphatic ethers such as tetrahydrofuran, 1 ,4-dioxan or 1 ,2- dimethoxy ethane; N-methylpyrrolidone; dimethyl sulphoxide; N,N- dimethylformamide; sulpholane; N,N,N',N'-tetramethylurea; aromatic hydrocarbons which may be substituted with one or more alkyl groups or chlorine atoms, such as chlorobenzene or xylene; and pyridine.
  • a solvent chosen from cyclic and aliphatic ethers such as tetrahydrofuran, 1 ,4-dioxan or 1 ,2- dimethoxy ethane; N-methylpyrrolidone; dimethyl sulphoxide; N,N- dimethylformamide; sulpholane; N,N,N',N'-tetramethylurea; aromatic hydrocarbons which
  • Preferred solvents include pyridine, tetrahydrofuran, N,N,N',N'-tetramethylurea and 1 ,4-dioxan (pyridine and tetrahydrofuran are especially preferred).
  • the amount of solvent used is generally from 1 to 10ml (preferably from 4 to 8ml) per gramme of compound of formula (III).
  • the process is generally performed in an autoclave or other sealed vessel.
  • the reaction temperature is generally from 50 C to 250 C, preferably from 120 C to 200 C.
  • the reaction is generally conducted using from 1 to 20 molar equivalents (preferably 4 to 8 molar equivalents) of the hydrazine source.
  • a catalyst may optionally be used to increase the rate of the reaction, and when present is generally chosen from alkali and alkaline earth metal fluorides such as potassium fluoride.
  • the amount of catalyst employed is generally from 0.05 to 2 molar equivalents (preferably from 0.5 to 1 molar equivalents).
  • the reaction may also be effected in the presence of copper or a copper salt, preferably copper (I) chloride.
  • Process (B) is particularly useful for the preparation of the valuable intermediate 3,5- dichlorophenylhydrazine from 1 ,3,5-trichlorobenzene, because the reaction proceeds in high yield and isomer purity and provides together with the other processes of the present invention an efficient method for obtaining synthetically valuable intermediate compounds.
  • process (B) when process (B) is used for the preparation of 3,5- dichlorophenylhydrazine from 1,3,5-trichlorobenzene, the reaction proceeds with excellent regioselectivity.
  • processes (A) and (B) can be combined to prepare a substituted aniline of formula (I) or an acid addition salt thereof from a compound of formula (III).
  • Example 1 The procedure of Example 1 was repeated but using two equivalents of Raney nickel and heating at 60°C for 3 hours in methanol to give the title compound in >90%> yield.
  • Example 6 Preparation of 3,5-dichlorophenylhydrazine The procedure of Example 3 was repeated but using 6 equivalents of hydrazine hydrate to give after 6 hours at 200 C, the title compound in

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

Abstract

The invention relates to processes for the preparation of compounds of formula (I), wherein R?1 and R2¿ each independently represent a halogen atom.

Description

Processes For Preparing Pesticidal Intermediates
This invention relates to novel processes for preparing intermediates (particularly certain aniline compounds and phenylhydrazine derivatives) useful in the preparation of pesticides.
3,5-Dihaloanilines and particularly 3,5-dichloroaniline are important synthetic intermediates for a number of valuable compounds including agrochemical fungicides for example as described in US Patent Publication Numbers 3755350 and 3903090, or German Patent
Publication No.2906574.
Various methods for preparing these compounds (particularly 3,5- dichloroaniline) are known, for example as described in Japanese patent publication numbers 05194330 and 60048500, and US patent publication number 4508922. However these procedures are generally inefficient, slow and suffer from poor selectivity and low yields. Furthermore they generally require the use of ammonia at high temperatures and/or pressures. There remains a need to develop new methods for obtaining these compounds particularly to find procedures which are safe to operate, efficient and can be performed at moderate temperatures and pressures.
The present applicants have surprisingly discovered novel processes for the preparation of certain substituted anilines and phenylhydrazines which do not suffer from these disadvantages, thus providing a new method for preparing valuable synthetic intermediates.
The present invention accordingly provides a process (A) for the preparation of a substituted aniline of formula (I):
Figure imgf000003_0001
(I) wherein R.1 and R-2 each independently represent a halogen atom; or an acid addition salt thereof; which process comprises the hydrogenolysis of a substituted phenylhydrazine of formula (II):
Figure imgf000004_0001
(II) wherein R* and R^ are as hereinbefore defined, or an acid addition salt thereof, in the presence of a metal or metal compound (for example a metal salt) under reducing conditions.
Unless otherwise specified in the present specification halogen atoms are selected from fluorine, chlorine, bromine and iodine.
The acid addition salts referred to in the invention are preferably the salts formed from strong acids such as mineral acids, for example sulphuric acid or hydrochloric acid.
The hydrogenolysis may be performed using a metal or metal salt selected from Raney nickel (a nickel-aluminium alloy) optionally in the presence of iron, manganese, cobalt, copper, zinc or chromium; stannous chloride; zinc in the presence of acetic acid; and a molybdenum (III) salt. The reaction may also be carried out using Raney nickel, platinum or palladium (which may be supported on charcoal or other inert material) in the presence of hydrogen gas. When the reaction is performed with hydrogen gas a pressure of 2 to 20 bars (preferably 5 to 10 bars) is generally used. The hydrogenolysis is preferably performed using Raney nickel.
The reaction may be performed in the absence or presence of a solvent, but is generally conducted in a solvent which may be selected from alcohols such as methanol, ethanol, propanol, isopropanol, butanol, isobutanol or tertiary butanol; ethers; aromatic hydrocarbons and water (or mixtures thereof). Methanol and ethanol are preferred solvents.
The reaction temperature is generally from 20 C to 150 C, preferably from 20 C to 90 C. The amount of catalyst employed is generally from 0.01 to 3 molar equivalents (preferably from 0.05 to 2 molar equivalents), although when the reaction is carried out under an atmosphere of hydrogen, a smaller amount generally gives satisfactory results.
Process (A) seeks to enable substituted aniline compounds of formula (I) and their acid addition salts thereof to be obtained in high yield from readily available starting materials. Furthermore the reaction can be very simple and economical to perform, and product isolation can be straightforward. Another advantage of this method is that these compounds of formula (I) may be prepared at moderate temperatures and pressures, whereas prior art methods require high temperatures and pressures.
According to a further feature of the present invention there is provided a process (B) for the preparation of a substituted phenylhydrazine of formula (II) as defined above, or an acid addition salt thereof, which comprises the reaction of a compound of formula
(III):
Figure imgf000005_0001
(III) wherein R and R2 are as hereinbefore defined and X represents a halogen atom, with hydrazine or an acid addition salt or source thereof.
By appropriate selection of the halogen atoms which represent Rl,R2 and X in formula (III) so that the group X is more reactive than R and R^, it is possible to obtain substituted phenylhydrazines of formula (II) and salts thereof having the various combinations of halogen atoms. Particularly preferred compounds are those wherein R and R2 in formulae (I) and (II) each represent a chlorine atom. Compounds of formula (III) are generally known. Preferably hydrazine hydrate is used in the process. When an acid addition salt of hydrazine is employed a base such as a trialkylamine (for example triethylamine) is optionally present.
A particularly preferred compound of formula (III) is 1,3,5- trichlorobenzene.
The reaction may be conducted in a solvent chosen from cyclic and aliphatic ethers such as tetrahydrofuran, 1 ,4-dioxan or 1 ,2- dimethoxy ethane; N-methylpyrrolidone; dimethyl sulphoxide; N,N- dimethylformamide; sulpholane; N,N,N',N'-tetramethylurea; aromatic hydrocarbons which may be substituted with one or more alkyl groups or chlorine atoms, such as chlorobenzene or xylene; and pyridine. Preferred solvents include pyridine, tetrahydrofuran, N,N,N',N'-tetramethylurea and 1 ,4-dioxan (pyridine and tetrahydrofuran are especially preferred). The amount of solvent used is generally from 1 to 10ml (preferably from 4 to 8ml) per gramme of compound of formula (III).
The process is generally performed in an autoclave or other sealed vessel.
The reaction temperature is generally from 50 C to 250 C, preferably from 120 C to 200 C. The reaction is generally conducted using from 1 to 20 molar equivalents (preferably 4 to 8 molar equivalents) of the hydrazine source. A catalyst may optionally be used to increase the rate of the reaction, and when present is generally chosen from alkali and alkaline earth metal fluorides such as potassium fluoride. The amount of catalyst employed is generally from 0.05 to 2 molar equivalents (preferably from 0.5 to 1 molar equivalents). The reaction may also be effected in the presence of copper or a copper salt, preferably copper (I) chloride.
The process of the invention for the preparation of substituted phenylhydrazines of formula (II) and their acid addition salts represents in certain aspects an improvement over the prior art. Process (B) is particularly useful for the preparation of the valuable intermediate 3,5- dichlorophenylhydrazine from 1 ,3,5-trichlorobenzene, because the reaction proceeds in high yield and isomer purity and provides together with the other processes of the present invention an efficient method for obtaining synthetically valuable intermediate compounds.
Moreover when process (B) is used for the preparation of 3,5- dichlorophenylhydrazine from 1,3,5-trichlorobenzene, the reaction proceeds with excellent regioselectivity.
According to a further feature of the invention processes (A) and (B) can be combined to prepare a substituted aniline of formula (I) or an acid addition salt thereof from a compound of formula (III).
The following non-limiting examples illustrate the invention. Each product was shown to be identical to a known reference sample of the compound. Example 1
Preparation of 3,5-dichloroaniline from 3,5- dichlorophenylhydrazine Raney nickel (2g of a slurry in water) was added to a solution of 3,5-dichlorophenylhydrazine (lg) in methanol (5ml) and heated at 60 C for 2 hours. The cooled mixture was filtered and evaporated to give the title compound in 100% yield. Example 2
Preparation 3,5-dichloroaniline from 3,5- dichlorophenylhydrazine
The procedure of Example 1 was repeated but using two equivalents of Raney nickel and heating at 60°C for 3 hours in methanol to give the title compound in >90%> yield.
Example 3
Preparation of 3,5-dichlorophenylhydrazine A mixture of 1,3,5-trichlorobenzene (2.53g), hydrazine hydrate (3.48g, 5 molar equivalents) and pyridine (12ml) was heated in an autoclave (purged with argon) for 6 hours at 180 C. The mixture was cooled, the excess hydrazine decanted and the organic phase evaporated in vacuo to give the title compound in 60%> yield. It was shown that 65%> of the starting material had been consumed, thus indicating that the reaction had occurred with high selectivity. Example 4
Preparation of 3,5-dichlorophenylhydrazine The procedure of Example 3 was repeated but using 6 equivalents of hydrazine hydrate gave the title compound in 63% yield. It was shown that 11% of the starting material had been consumed, thus indicating that the reaction had occurred with good selectivity.
Example 5
Preparation of 3,5-dichlorophenylhydrazine The procedure of Example 3 was repeated but using 6 equivalents of hydrazine hydrate to give after 10 hours at 180 C, the title compound in 76%) yield. It was shown that 77% of the starting material had been consumed, thus indicating that the reaction had occurred with high selectivity.
Example 6 Preparation of 3,5-dichlorophenylhydrazine The procedure of Example 3 was repeated but using 6 equivalents of hydrazine hydrate to give after 6 hours at 200 C, the title compound in
82%o yield. It was shown that 83% of the starting material had been consumed, thus indicating that the reaction had occurred with high selectivity.

Claims

1. A process for the preparation of a substituted aniline of formula (I):
Figure imgf000008_0001
(I) wherein RI and R^ each independently represent a halogen atom; or an acid addition salt thereof; which process comprises the hydrogenolysis of a substituted phenylhydrazine of formula (II):
Figure imgf000008_0002
(II) wherein R* and R^ are as defined above, or an acid addition salt thereof, in the presence of a metal or metal compound under reducing conditions.
2. A process according to claim 1 in which the hydrogenolysis is performed using Raney nickel.
3. A process for the preparation of a substituted phenylhydrazine of formula (II) as defined in claim 1 or an acid addition salt thereof, which comprises the reaction of a compound of formula (III):
Figure imgf000008_0003
(III) wherein Rl and R^ are as defined in claim 1 and X represents a halogen atom, with hydrazine or an acid addition salt or source thereof.
4. A process according to claim 3 in which hydrazine hydrate is used.
5. A process according to claim 1 or 2 in which the compound of formula (II) is prepared by a process according to claim 3 or 4.
6. A process according to any one of the preceding claims wherein RI and R^ represent chlorine.
7. A process according to claims 1,2,5 or 6 which further comprises converting the substituted aniline of formula (I) or an acid addition salt thereof into an agriculturally fungicidal compound.
PCT/EP2000/004595 1999-05-13 2000-05-11 Processes for preparing pesticidal intermediates Ceased WO2000069805A1 (en)

Priority Applications (8)

Application Number Priority Date Filing Date Title
IL14605400A IL146054A0 (en) 1999-05-13 2000-05-11 Processes for preparing pesticidal intermediates
DE60012172T DE60012172T2 (en) 1999-05-13 2000-05-11 PROCESS FOR PREPARING INTERMEDIATE PRODUCTS FOR PESTICIDES
US10/030,324 US6509503B1 (en) 1999-05-13 2000-05-11 Process for preparing pesticidal intermediates
AU52146/00A AU766505B2 (en) 1999-05-13 2000-05-11 Processes for preparing pesticidal intermediates
BR0010540-6A BR0010540A (en) 1999-05-13 2000-05-11 Process for the preparation of a substituted aniline, and, for the preparation of a substituted phenylhydrazine
AT00936766T ATE271027T1 (en) 1999-05-13 2000-05-11 METHOD FOR PRODUCING INTERMEDIATE PRODUCTS FOR PESTICIDES
JP2000618224A JP2002544251A (en) 1999-05-13 2000-05-11 Method for producing pesticide intermediate
EP00936766A EP1177165B1 (en) 1999-05-13 2000-05-11 Processes for preparing pesticidal intermediates

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB9911180.9 1999-05-13
GBGB9911180.9A GB9911180D0 (en) 1999-05-13 1999-05-13 Processes for preparing pesticidal intermediates

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EP (2) EP1437343A3 (en)
JP (1) JP2002544251A (en)
CN (1) CN1350516A (en)
AR (1) AR023979A1 (en)
AT (1) ATE271027T1 (en)
AU (1) AU766505B2 (en)
BR (1) BR0010540A (en)
DE (1) DE60012172T2 (en)
DK (1) DK1177165T3 (en)
GB (1) GB9911180D0 (en)
HU (1) HUP0201401A3 (en)
IL (1) IL146054A0 (en)
PL (1) PL354712A1 (en)
RU (1) RU2243207C2 (en)
WO (1) WO2000069805A1 (en)
ZA (1) ZA200108578B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004054961A1 (en) * 2002-12-16 2004-07-01 Basf Aktiengesellschaft Process for the preparation of substituted halogenated aniline
CN107033025A (en) * 2017-06-07 2017-08-11 李博强 A kind of preparation method of 2,4,6 trinitrophenyl-hydrazine
CN107033026A (en) * 2017-06-07 2017-08-11 李博强 A kind of preparation method of p-nitrophenyl hydrazine hydrochloride

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU731777B2 (en) * 1998-11-30 2001-04-05 Nihon Nohyaku Co., Ltd. Aniline derivative and process for producing the same
CN106045876B (en) * 2016-06-07 2018-02-09 四川福思达生物技术开发有限责任公司 A kind of synthetic method of p-hydrochloride
CN106748801B (en) * 2016-12-28 2019-03-01 华东师范大学 A kind of synthetic method of 3,5-dichloroaniline

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004054961A1 (en) * 2002-12-16 2004-07-01 Basf Aktiengesellschaft Process for the preparation of substituted halogenated aniline
US7176334B2 (en) 2002-12-16 2007-02-13 Basf Aktiengesellschaft Process for the preparation of substituted halogenated aniline
KR101048928B1 (en) * 2002-12-16 2011-07-12 바스프 에스이 Process for preparing substituted halogenated aniline
CN107033025A (en) * 2017-06-07 2017-08-11 李博强 A kind of preparation method of 2,4,6 trinitrophenyl-hydrazine
CN107033026A (en) * 2017-06-07 2017-08-11 李博强 A kind of preparation method of p-nitrophenyl hydrazine hydrochloride

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DK1177165T3 (en) 2004-08-30
PL354712A1 (en) 2004-02-09
HUP0201401A2 (en) 2002-08-28
ZA200108578B (en) 2003-01-20
RU2243207C2 (en) 2004-12-27
EP1437343A3 (en) 2004-12-22
AU766505B2 (en) 2003-10-16
AR023979A1 (en) 2002-09-04
EP1177165A1 (en) 2002-02-06
US6509503B1 (en) 2003-01-21
JP2002544251A (en) 2002-12-24
BR0010540A (en) 2002-02-19
DE60012172T2 (en) 2005-08-25
IL146054A0 (en) 2002-07-25
CN1350516A (en) 2002-05-22
EP1177165B1 (en) 2004-07-14
GB9911180D0 (en) 1999-07-14
DE60012172D1 (en) 2004-08-19
ATE271027T1 (en) 2004-07-15
AU5214600A (en) 2000-12-05
EP1437343A2 (en) 2004-07-14

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