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Sommaire du brevet 1264763 

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  • lorsque la demande peut être examinée par le public;
  • lorsque le brevet est émis (délivrance).
(12) Brevet: (11) CA 1264763
(21) Numéro de la demande: 1264763
(54) Titre français: PREPARATION DES ETHERS DE DIPHENYLE
(54) Titre anglais: PROCESS FOR THE PREPARATION OF DIPHENYL ETHERS
Statut: Périmé et au-delà du délai pour l’annulation
Données bibliographiques
(51) Classification internationale des brevets (CIB):
  • C7C 205/38 (2006.01)
  • C7C 201/12 (2006.01)
(72) Inventeurs :
  • SEHRING, RICHARD (Allemagne)
  • BUCK, WOLFGANG (Allemagne)
(73) Titulaires :
  • SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
(71) Demandeurs :
  • SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
(74) Agent: NORTON ROSE FULBRIGHT CANADA LLP/S.E.N.C.R.L., S.R.L.
(74) Co-agent:
(45) Délivré: 1990-01-23
(22) Date de dépôt: 1983-03-16
Licence disponible: S.O.
Cédé au domaine public: S.O.
(25) Langue des documents déposés: Anglais

Traité de coopération en matière de brevets (PCT): Non

(30) Données de priorité de la demande:
Numéro de la demande Pays / territoire Date
P 32 09 878.2 (Allemagne) 1982-03-18

Abrégés

Abrégé anglais


ABSTRACT
An improved process for the preparation of herbicidal diphenyl
ethers of the generic formula I
<IMG> (I)
in which R1, R2, X1,and X2 have a range of possible meanings. The described
process reacts a compound of formula IV with a phenol of formula VI
(IV) <IMG> (VI)
in the presence of a base and of a phase transfer catalyst. The resulting
product is reacted with an amine of formula NHR2 in an alcohol containing
ether groups, such as diethylene glycol, to provide a compound of formula I.
This process avoids the impurities, particularly coloured ones, and by-
products obtained by the known processes for compounds ot this type.

Revendications

Note : Les revendications sont présentées dans la langue officielle dans laquelle elles ont été soumises.


- 22 -
THE EMBODIMENTS OF THE INVENTION IN WHICH AN EXCLUSIVE
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. A two step process for the preparation of compounds of
formula (I)
<IMG> (I)
wherein
n is an integer from 1 to 3,
R1 represents hydrogen, halogen, alkyl or alkoxy with 1
to 8 carbon atoms, trifluoromethyl, acetyl or cyano,
R2 represents hydrogen; alkyl, alkenyl or alkynyl with
up to 16 carbon atoms; an alkyl group with 2 to 6 carbon atoms
substituted by hydroxy, C1-4 alkoxy, phenoxy, halophenoxy, C1-4
alkylphenoxy, C1-4 alkoxyphenoxy, nitrophenoxy, cyanophenoxy,
amino or C1-4 alkylthio; optionally halosubstituted benzyl,
NR3R4, CHR3-COOR4 or CHR3-CONR4R5, wherein R3, R4 and R5, which
may be the same or different, represent hydrogen or C1-8 alkyl
groups, and
X1 and X2, which may be thc same or different, represent
hydrogen or halogen and X1 also represents methyl,
in which process technical grade materials are used and in which
the formation of undesirable colored by-products is substantially
avoided, which comprises:

- 23 -
(a) in a first step reacting a nitrobenzene of formula (IV)
<IMG> (IV)
in which X1 and X2 are as defined above, with a phenol of the
formula (VI)
<IMG> (VI)
in which R1 and n are as defined above, at a temperature between
60°C and 150°C, and in the presence of a phase transfer catalyst
and of an aqueous alkaline or alkaline earth metal base to provide
a compound of formula (II):
<IMG> (II),

- 24 -
27888-4
and recovering the compound of formula (II), and
(b) in a second step reacting the thus obtained compound of
formula (II), if desired without further purification, in an
alcohol containing ether groups as solvent, with an amine of the
formula (III)
H2NR2 (III)
in which R2 is as defined above, to provide a compound of
formula (I).
2. A process according to claim 1 wherein step (a) is
carried out at a temperature between 80 and 120°C.
3. A process as claimed in claim 1, characterised in that,
in step (a), 2,3,4-trichloronitrobenzene is used as the nitro-
benzene of formula (IV) and phenol or 4-fluorophenyl is used as
the phenol of formula (VI) and in step(b) arnmonia or methylamine
is used as the amine of formula (III).
4. A process as claimed in claim 1, characterised in that,
in step (a), 2,4-dichloro-3-methylnitrobenzene is used as the
nitrobenzene of formula (IV), phenol or 4-fluorophenol is used as
the phenol of formula (VI) and, in step (b), arnmonia or methyl-
amine is used as the amine of formula (III).

-25-
27888-4
5. A process according to claim 1 wherein, as a further
step, the phase transfer catalyst is recovered and reused.
6. A process according to claim 1 wherein the alkali metal
base is used.
7. A process according to claim 6 wherein the alkali metal
base is sodium or potassium hydroxide.
8. A process according to claim 1 wherein the phase trans-
fer catalyst is chosen from a triethylbenzylammonium, tetrabutyl-
ammonium, methyltrioctylammonium, or tetrabutylphosphonium salt.
9. A process according to claim 8 wherein the phase
transfer catalyst is chosen from tetrabutylammonium hydrogen
sulphate, and tetrabutylphosphonium chloride.

Description

Note : Les descriptions sont présentées dans la langue officielle dans laquelle elles ont été soumises.


-- 2 --
The invention relates to an improved process
for the preparation of diphenyl ethers of general
formula
Xl NHR2
( l)n ~ X~ ~I2 (I)
wherein
n is an integer from 1 to 3,
Rl represents hydrogen, halogen, alkyl or alkoxy
with 1 to 8 carbon atoms, trifluoromethyl, acetyl
or cyano,
R2 represents hydrogen; alkyl, alkenyl or alkynyl
with up to 16 carbon atoms; an alkyl group with 2
to 6 carbon atoms substituted by hydroxyl Cl 4 alkoxy,
phenoxy, halophenoxy, Cl 4 alkylphenoxy, Cl 4 alkoxyphenoxy,
nitrophenoxy, cyanophenoxy, amino or Cl 4 alkylthio;
optionally halosubstituted benzyl, NR3R4, CHR3-COOR~
or CHR3-CONR4R5, wherein R3, R4 and R5, which may
be the same or different, represent hydrogen or Cl 8
alkyl groups, and
Xl and X2, which may be the ~-same or di~ferant/
represent hydeogen or halogen arld Xl a~ rep~e(3~nt~s
methy 1 .
n will only assume the values 2 and 3 if R
represents halogen or alkyl. The term "halogen"
refers to fluorine, chlorine, bromine and iodine.
The preferred halogens are fluorine, chlorine and
bromine, particularly fluorine and chlorine. When
Rl, R2, R3, R4 and R5 represent or contain hydrocarbon
gro~ps, these may possibly also be branched. However,
these groups preferably contain 1 to 2 carbon atoms.
.,j ,.

` ` ~2~;~7~:3
Within the scope of the definitions given herein-
before, Rl preferably represents hydrogen, fluorine,
chlorine, bromine or methyl, R2 represents hydrogen,
Cl 4 alkyl, allyl, 2-hydroxyethyl, 4-fluoro- or 4-
chlorobenzyl or dimethylamino. R3 is preferably
hydrogen or methyl whilst R4 is Cl 4 alkyl. The
preferred definitions of Xl/X2 are chlorine/hydrogen,
methyl/hydrogen, chlorine/bromine and bromine/chlorine.
If n represents 2 or 3, there may be different groups
Rl present at the same time. Some of the compounds
of general formula I are known (DE-OS P 29 38 595).
They are distinguished by their excellent herbicidal
action.
According to DE-OS 29 38 595 the compounds
of general formula I can be obtained by reacting
a nitrodiphenoxybenzene of general formula
(Rl)n~
wherein n, Rl, Xl and X2 are a~ hereinbefore defined,
with an amine of formula
H2NR2 (III)
wherein R2 is as hereinbefore defined, at elevated
temperature. The compounds of formula II are prepared
by reacting a compound of general formula

~ Ei4763
Xl Cl
Ll
Cl ~ NO2 ~IV)
X2
wherein Xl and X2 are as hereinbefore defined, for
example 2,3,4-trichlorobenzene, 2,4-dichloro-3-methyl-
nitrobenzene and 2,3,4,5-tetrachloronitrobenzene,
with a corresponding phenoxide of general formula
(Rl)2
~ OKat (V)
(wherein Kat is one equivalent of a cation). Preferably,
the alkali metal phenoxides are used, particularly
the sodium phenoxide, or the phenol and, for example,
an alkali metal carbonate. In the case of simple
phenols, particularly unsubstituted phenol, the corres-
ponding phenol may servc ~s a rea~tion mec~lum. Ilowever,
it is par~icul~rly pre~crred to use dlmeth~lsulphoxide
as solvent
The two chlorine atoms in the 2- and 4-positions,
which can be exchanged for phenoxy groups, show a
clearly graduated reactivity.
The known process is less suitable for use
on an industrial scale. In the production of the
starting substances of formula II, strongly coloured
by--products are formed which make it difficult or

~2~497~i3
-- 5 --
impossible to carry out further processing directly.
further problem is presented by phenolic by-products,
e g. cleavage products of the type
Xl OH
(Rl)n X~
An extensive purifying operation is needed to eliminate
the by-products.
The reaction of the compounds of formula II
to yield the end products of formula I according
to the prior art requires, in some cases, an autoclave
reaction in solvents such as toluene, dioxan or chlorinated
hydrocarbons. Substantial reaction times (about
12 to 20 hours) are generally required.
It has now been found that the compounds of
formula I can be obtained with greater purity, in
a shorter time and with less elaborate apparatus,
if a nitrobenzene of formula IV is heterogeneously
reacted, in the presence of a phase transfer catalyst,
with a phen~l of formula
(Rl)n Ol~ ~VX)
wherein Rl and n are as hereinbefore defined, with
the addition of an aqueous alkaline or alkaline earth
metal base, at elevated temperature, to ~orm the
corresponding 2,4-diphenoxy compound of formula II,
which i5 then reacted, in a hiyh-boiling alcohol

~L26~7~i3
-- 6 --
containing ether groups, with an amine o~ formula
III to form the corresponding compound of formula
I.
If desired, the first reaction step, which
produces the diphenoxy compounds of formula II, may
also be carried out with the addition of inert, water-
immiscible solvents. The critical advantage of the
reaction according to the invention consists in the
use of a conventional phase transfer catalyst. Thanks
to the addition of such a catalyst, a very pure product
of formula II is obtained in an excellent yield at
temperatures of between 60 and 150C, preferably
between 80 and 120C, more particularly between 90
and 110C. The phase transfer catalyst can be recovered
almost totally. The reaction components of formulae
IV and VI are used in a molar ratio of from 1:1.8
to 1:2.5. Preferably, the phenol is used in a slight
excess (molar ratio 1:2.1 to 1:2.4) and a quantity
of a~ueous base, preferably strong sodium or potassium
hydroxide solution, corresponding to the quantity
of phenol is used. The quantity of phase transfer
catalyst may vary within wide limits. It has proved
advantageous to use about 0.005 to 0.12, preferably
from 0.01 to 0.06 mol of catalyst per mol of phenol.
Suitable phase transfer catalysts include, for example,
triethylbenzylammonium chloride or bromide; tetrabutyl-
ammonium chloride, bromide, hydrogen sulphate, hydroxide;
methyl trioctylammonium chloride; tetra~u~ylphos~honium
bromide. Nllmerous other ~iuitahle ~ha~.se t.~nsE@r
catalysts arè mentioned in the monograph by E.V.
Dehmlow and S.S. Dehmlow, "Phase Transfer Catalysis",
Verlag Chemie, Weinheim (1980), particularly page
38 and pages 39-43.
The second reaction step, the reaction of the
diphenoxy compounds of formula Il to yield the end
products of formula I, is, surprisingly, particularly
successful if ether alcohols are ~sed as the reaction
medium. Suitable compounds of this kind include,

~264763
-- 7 --
in particular, aliphatic or cycloaliphatic compounds,
e.g. diethylene glycol, triethylene glycol, dipropylene
glycol, diethylene glycol monomethyl ether, monoethy~
ether, monopropyl ether, monobutyl ether, monobenzyl
ether, lower monoalkyl ethers of triethylene glycol
or of dipropylene glycol and partial ethers of other
polyhydric alcohols. The reaction temperature is
between about 20 and 180C, preferably between about
40 and 170C; it depends largely on the amine of
formula III used. Whereas methylamine, for example,
can be reacted at ambient temperature, a higher temperature
is required when ammonia is used so that the reaction
can be completed with a few hours. A slight increase
in the ammonia pressure to 3 to 4 bar can be used
to per~orm the reaction at temperatures of about
120 to 130C without taking any longer.
The end products are obtained in very pure
form and in very good yields.
In the Examples which follow, the process is
described more fully, without being restricted to
the embodiments described.

~ 6;~
-- 8
Preparation of diphenoxy__ompounds of formula II
Example (a)
2-Chloro-4-nitro-1,3-diphenoxybenzene
216.2 g (2.3 mol) of phenol, 226.5 g (1 mol)
of 95.5% 2,3,4-trichloronitrobenzene and 10.0 9 of
tetrabutylammonium hydrogen sulphate are heated to
100C in a flask with a stirrer. Within 10 minutes,
187.5 9 of 49% sodium hydroxide solution are added
dropwise, with vigorous stirring. The reaction mixture
is then kept at about 110C for 4 hours. After it
has cooled to about 90C, 1 litre of toluene is added
and then water is added. The aqueous phase is separated
off. The toluene phase is extracted twice with 100 ml
of 2N hydrochloric acid. The toluene layer is separated
off and concentrated by evaporation ln vacuo. According
to gas chromatography, 94.1% of the residue consists
of the title compound. From the crude product, 97.4%
of theory of pure end product is obtained, m.p. 106-
107C.
The catalyst can be recovered from the hydrochloric
acid phase n a yield of more than 90% and sufficiently
pure to be usecl again in the form of the hydrochloride.
Example (b)
3-Methyl-2,4-diphenoxy-nitrobenzene
20.6 y (0.l mol) of 2,4-dichloro-3-methyl-nitro
benzene, 21.6 g (a . ~25 mol) of phenol and 9.3 c~ o(
95% tetrabutylpllosE7honium chlc7rld~ ~0.03 mol) are
placed in a stirring app~ratus and heated to 110C.
27 g (0.3 mol) of 50~ sodium hydroxide solution are
added dropwise to the mixture, with stirring, and
the eesulting mixture is stirred for 2 to 3 hours
at reflux temperature. After cooliny, 100 ml of
toluene and 50 ml of water are added. The mixture
is stirred thoroughly and then the phases are separated.
The toluene solution is extracted with 2N hydrochloric
acid and then with 2N sodium hydroxide solution,

4~7~;3
g
then dried and concentrated by evaporation. A brown
oil is obtained (yield 31.7 g = 99~ of theory) which
crystallises when stirred with a little isopropanol.
The yellowish solid is suction filtered and dried,
m.p. 55-57C.
Some of the tetrabutylphosphonium chloride
is recovered from the acidic washing liquid.

~26~763
-- 10 --
The following compounds may be Qbtained accoedingly.
R" ~ Ll ~ ~/` R
R " ' -r
''2
Example R ~ R." R" ' ;~ 2 Mp
3 H H H Cl Cl 152C
4 4-~ H H Cl H
4-CF3 H H Cl El
6 2-C1 4-Cl El Cl l-l
7 2-C1 4-C1 5-Cl Cl H
8 2-C1 4-Br 5-Cl Cl ri
9 2-CH3 4-Cl H Cl El
2-C1 4-SCEi3 5-Cl Cl H
11 2-CH3 4-CH3 H Cl E~
12 2-CI`I H H Cl H
13 4-F ll 11 Cl-l,, ll
14 4-CF~ El E~ Ct ~
2-F 4-CH~ El CH-~ H
16 2-CH~ 4-CH3 H Cl-l
17 ~ Cl 1~ ~I Cl~
18 2-C1 5-Cl E~. Ei3 I-i
19 4-oCH3 El ~I CH H
3-CF3 H u CH3 ~

~2~i4t76~
Exar~lple R ~ R" R!' r Xl X Mp roCl
21 4-CN H H CH~ T
2Z 4-Br H H CH3 H
23 4-J H H 3
24 3-CH3 5-CH3 H CH3 H
4-oCH3 H H Cl H
26 2-CH3 4-oCH3 H Cl H
27 2-C1 4-Br 5-Cl Cl Cl
28 4-oCH3 H H Cl Cl
29 2-CH3 3-OCH3 4-oCH3 Cl H
2-CH3 4-Cl H Cl Cl
31 4-CH(CH3)2 H H Cl H
32 2-CH3 4-oC2H5 H CH3
33 4-OC3~7 H H Cl Cl
34 3-CF3 H H Cl Cl
2-C1 4-Br 5-Cl H Cl
36 4-Cl H H Cl H
37 4-Cl H H CH H
3a 3-C1 5-Cl H Cri 3
39 2-F H H CH~ t!
2-~
41 2-CI-~3 tl H CH~ H
42 3-CH3 H H CH~ ~T

126~7i~
- 12 -
P ration of the end roducts of formula I
re~a P
Example 1
2-Chloro-3- henoxv-6-nitroaniline
P
173 9 of 2-chloro-4-nitro-1,3-diphenoxybenzene
(crude product according to Example ~a)) are dissolved
in S00 ml of triethylene glycol. At 165C, ammonia
is passed through the solution for 6 hours. Thin
layer chromatography then shows that none of the
starting product remains. Whilst the solution is
cooled with ice, 250 ml of 2N sodium hydroxide solution
and 300 ml of water are added. The reaction product
is precipitated and is then suction filtered. 95%
of theory of crude product is obtained, which is
shown by gas chromatography to contain 95.8~ of the
title compound. The total yield over both steps
is 95.3% of theory, m.p. 81-82C (from isopropyl
alcohol).
The same result is achieved using diethylene
glycol or diethylene glycol monobutyl ether as the
solvent instead of triethylene glycol.
In the case of less volatile or more reactive
amines, it is sufficient if the components are reacted
at temperatures of between ambient temperature and
about 160C.
Example 2
2-Methyl-6-nitro-3-phenoxy-N-methylaniline
N~C~I3
~0~ ~
32.1 9 (0.1 mol) of 3-methyl-2,4-diphenoxynitro-

~6~L76~
- 13 -
benzene are dissolved in 100 ml of diethylene glycol.
Methyl amine is slowly introduced into the solution,
with stirring, at 100C. The progress of thè reaction
is monitored by thin layer chromatography (ready-
made TLC plates made by Merck of Darmstadt, silica
gel 60 F254, toluene/heptan 1:1).
After 3L hours the reaction has ended. After
cooling, the product is precipitated by the addition
of 2N sodium hydroxide, with trituration, then suction
filtered and washed with water. Yellow solid; m.p.
60-62C.
Yield: 23 g (89.2% of theory)

` 2~763
-- 14 --
~ ~ r-~
Ov a~ ~ ) ~ ~
CW~
D
O xN c~ ~ ~ ~ r
O
~ I X~ ~ ~ V ~: ~
' q q q q q
~ ~ ~ ~.C X ~: ~ r~
C~
~r: ~ ~ ~ J ;~
. r I r~ r ~ rl rl
~O~ _ ~ L~ r ~ X ~~l r I X
~I H
O
a
Ll ~ r~ J ~ O C- 0 a~, o ~

~_ - 15 -
O D D 1` 0 J N
($~ D
N N N N N3~N V V ~ _,~ ~\ ~T ~
X 3:: X ~ C ) X 3:~
'X C~ V ~ V V C~
~ 5 X ~ X ~ X r~
X rI~
r ~ rr~
r~ 1;~ r~ t ~ t rr~ ~J ,r~ --t N
~ r-l r-l r-l r-lr~l ~I r-l r I N' N N N t~' N
X

763
-- 16 --
~_
o o~ ~ ~ C ~ O
._ I .i I I I ~ I
~O 0 ," ~ 0 ~ 0
1~ ~ 0 r i a:
O
L~
X~
~ ~ ~ W ~ ~ ~ ~ X ~:~ V
X ~ ~ V V ~ v ~ c~ V ~ ::C ~ X
~ ~ "~
X V C~ C~ V V C~ ~ V V V V V V V V C~ V
~-~
r~
_ ~ ~ J ~ ~ ~t ~ X ~~C X ~ ~ ~\U~
V C~ ~ V t~ r
I O
O
~ ~O ~, 0 tJ~ Or t~ t~ ~ t~ t~ ~ C() ~<~ _t ~ -t
F~

- 1 7 -` ~L26~63
U~
C~ O Lr~ ~1
o ~ ~ o~ ~ ~t~
`t I I o I I t~\
O N t~ ~0 Ir~ ~~t--1 r~ (\1 (~ 15~ 0~ tD ~t
N C~ ~/ .a~ 0 N
O ~ O O O O O
~ t~
~J r~ I X
a~ 1 4 I~r4 X ~ ~ ~ 4 ~ C~
N
X~: X, ~ C ~ ~ ~ X X ~ ~ ~ ~ ~'
t~ t ~ t~ t ~ t-~ t~ t~ ,~, t-~t ~ ~ ~ t~ t1
~~.4 ~.4 ~ 4 X X ~ ~ ~ I; 3 ~ I T X ~ ~ ~ X
--
_ ~ ~ X4 ~ X X X
~ N
~ o
~4 1_ X 3 ~ ~4 ~ S\ t ~4 1--4
~<~
~t~ ~t~ r
W I~ -4 ~ r.
O ~C.) t~ C) C.) C_) C.)~.~ ~'t~ ) r_ C~ C~
~ r~ \I r.~J N r~ 4
a
t- ~ ~ ~ ~O ~ 0 ~ O ~ t~ C~ r.
t~ ~ ~ ~ ~ ~ ~ ~ ~ t.~ ~r~ lr~
~c
r~

~L2~763
- 18
, ~
O ~ O N 0 0 ~ t C N ~ X
OO^O^O^O^ OOOOOyOOOO ~
~r
N ~ N O
D ~ ~ X~ N ~0
C C~ V ~ ~
~8
X ~ ~ ~ C ~ -- ::C.,C~C~4 ~ X ~ ~ ~C 3:: ~ h
~e ~
X V ~ VC.) C.) C,)C C U ~ C ~ ~ ~~ . ~
~a~
~ l C ~ C XC~C ~X W l C ~ C ~ C l C ~ C ~ ~\ X
a) ~ ~
,~ a
. .
-IW-~ ~ ~
C~ ~ ~ O
X ~ C~ C ~ C wCW ~ C ~ W W rl J
tU fd
r. r' ~1 o 1 ~ rl c~ r,l vl ~I cl ~ r~
f~ w~ ~ J J N t~ ~ ~,;t ~t J J~t ;t N ,1 0
r~ ,~
fV O ~I N t~ J ~ ~ C0 C~O rl ~`Jr~ J ~ *
r~ ~o ~ ~o ~o ~o ~o ~o ~o ~o
r~ .

64~63
-- 19 --
Table ~I
Compounds of formula
Cl l~nIR2
~,~0 _~N02
(The compounds are obtained in the form of oils)
No. R2 RF values 27C
Acetone/
Heptane Toluene
1: 1
1 C2HS 0.51 0.46
2 n-C3H7 0.615 0.47
3 i-C3H7 0.61 0.45
4 n-C4H9 0.625 0,50
i-C4H9 0.60 0.51
6 HO-CH2-CH2 0.445 0.01
7 CH( 2 5)2
8 -CH2-C-CH 0.31
* 5 toluene/cyclohexan~

~2~ 63
- 20 -
Table III
Compounds of formula
Cl NHR2
C:l _~Q_~ N02
No. R2 X2 Properties/m.p.
1 CH3 Cl red crystals m.p. 101C
C H Cl light brown oil,
2 2 5 uniform according
to thin layer
chromatography
3 i-C3H7 Cl m p. 83C
Cl orange oil, uniform
4 n-C4Hg according to thin
layer chromatography
n C12 25 Cl m p. 43~C
6 n C18 37 Cl 47 - 48C
7 -cH2-cH2-oH Cl dark oil
8 -CH~C2H5)2 Cl
CH =CH-CH H Rf 0.51 (ready-made
2 silica gel TLC plates,
6n F~5~, eluant toluene
CH~C2H5)2

~26~ii3
- 21 -
Table IV
From 1,3-diphenoxybenzenes of formula
Cl O ~ Rl
R ~ O ~ )/ _ NO2
wherein Rl has the meaning given below, the following
compounds of formula
Cl NH-R2
- Rl ~ O _'<~ NO 2
are prepared:
No. Rl R2 Rf values 27C
Acetone Toluene
~ Heptane
1 CH3 C~13 0.61 0.~5
2 CH3 C~l2~1~ 0.63 0.515
3 OCH3 n C3H7 0.29

Dessin représentatif
Une figure unique qui représente un dessin illustrant l'invention.
États administratifs

2024-08-01 : Dans le cadre de la transition vers les Brevets de nouvelle génération (BNG), la base de données sur les brevets canadiens (BDBC) contient désormais un Historique d'événement plus détaillé, qui reproduit le Journal des événements de notre nouvelle solution interne.

Veuillez noter que les événements débutant par « Inactive : » se réfèrent à des événements qui ne sont plus utilisés dans notre nouvelle solution interne.

Pour une meilleure compréhension de l'état de la demande ou brevet qui figure sur cette page, la rubrique Mise en garde , et les descriptions de Brevet , Historique d'événement , Taxes périodiques et Historique des paiements devraient être consultées.

Historique d'événement

Description Date
Inactive : Renversement de l'état périmé 2012-12-05
Inactive : CIB désactivée 2011-07-26
Inactive : CIB désactivée 2011-07-26
Inactive : CIB désactivée 2011-07-26
Le délai pour l'annulation est expiré 2007-01-23
Inactive : CIB dérivée en 1re pos. est < 2006-03-11
Inactive : CIB de MCD 2006-03-11
Inactive : CIB de MCD 2006-03-11
Lettre envoyée 2006-01-23
Accordé par délivrance 1990-01-23

Historique d'abandonnement

Il n'y a pas d'historique d'abandonnement

Historique des taxes

Type de taxes Anniversaire Échéance Date payée
TM (catégorie 1, 8e anniv.) - générale 1998-01-23 1997-12-16
TM (catégorie 1, 9e anniv.) - générale 1999-01-25 1998-12-16
TM (catégorie 1, 10e anniv.) - générale 2000-01-24 1999-12-20
TM (catégorie 1, 11e anniv.) - générale 2001-01-23 2000-12-19
TM (catégorie 1, 12e anniv.) - générale 2002-01-23 2001-12-19
TM (catégorie 1, 13e anniv.) - générale 2003-01-23 2002-12-17
TM (catégorie 1, 14e anniv.) - générale 2004-01-23 2004-01-14
TM (catégorie 1, 15e anniv.) - générale 2005-01-24 2004-12-07
Titulaires au dossier

Les titulaires actuels et antérieures au dossier sont affichés en ordre alphabétique.

Titulaires actuels au dossier
SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
Titulaires antérieures au dossier
RICHARD SEHRING
WOLFGANG BUCK
Les propriétaires antérieurs qui ne figurent pas dans la liste des « Propriétaires au dossier » apparaîtront dans d'autres documents au dossier.
Documents

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Description du
Document 
Date
(yyyy-mm-dd) 
Nombre de pages   Taille de l'image (Ko) 
Page couverture 1993-09-14 1 17
Abrégé 1993-09-14 1 17
Revendications 1993-09-14 4 80
Dessins 1993-09-14 1 8
Description 1993-09-14 20 393
Dessin représentatif 2001-08-05 1 4
Avis concernant la taxe de maintien 2006-03-19 1 172
Taxes 1996-12-18 1 61
Taxes 1995-12-18 1 101
Taxes 1993-12-19 1 33
Taxes 1994-12-15 1 97
Taxes 1992-11-26 1 21
Taxes 1992-01-08 1 39