US2007161814A1PendingUtilityA1
Process for carbonylating phenylalkyl derivatives by means of carbon monoxide
Assignee: SANOFI AVENTIS DEUTSCHLANDPriority: Jun 30, 2004Filed: Dec 19, 2006Published: Jul 12, 2007
Est. expiryJun 30, 2024(expired)· nominal 20-yr term from priority
C07C 51/12C07C 45/63C07C 57/30C07C 59/64C07C 49/697
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Claims
Abstract
The invention is directed a process of preparing a compound of formula (I), wherein R 1 , R 2 , R 3 and z are as defined herein.
Claims
exact text as granted — not AI-modified1 . A process for preparing a compound of formula I
wherein:
R1 and R2 are each independently —(C 1 -C 4 )-alkyl;
R3 is —C(O)—(C 1 -C 4 )-alkyl, which is monosubstituted by Cl or Br, or —C(O)—(C 3 -C 10 )-cycloalkyl; and
Z is hydrogen or —(C 1 -C 10 )-alkyl;
comprising reacting a compound of formula II
wherein:
R1 and R3 are each as defined in formula I;
X is Cl, Br or —OH; and
R4 is R2 or together with X form ═CH 2 or ═CH—(Cl—C 3 )-alkyl;
with carbon monoxide or a carbon monoxide-releasing compound in the presence of concentrated sulfuric acid, hydrogen fluoride or a superacid or mixtures thereof, and then
a) adding water to give the compound of formula I wherein Z is hydrogen, or
b) adding (C 1 -C 10 )-alkyl-OH when X is Cl or Br, or R4 together with X form ═CH 2 or ═CH—(C 1 -C 3 )-alkyl, to give the compound of formula I wherein Z is —(C 1 -C 10 )-alkyl.
2 . The process according to claim 1 for preparing the compound of formula I, wherein
R1 and R2 are both methyl, R3 is —C(O)-propyl monosubstituted by Cl, or —C(O)-cyclopropyl; and Z is hydrogen or —(C 1 -C 4 )-alkyl.
3 . The process according to claim 1 , wherein the carbon monoxide-releasing compound is selected from the group of formic acid, a formate salt with an inorganic or organic cation or metal carbonyl, or a mixture thereof.
4 . The process according to claim 1 , wherein the superacid used is an acid from the group of perchloric acid, chlorosulfonic acid, fluorosulfonic acid, trifluoromethanesulfonic acid, perfluorobutane-1-sulfonic acid, Lewis acid or a conjugated protic acid-Lewis acid complex.
5 . The process according to claim 4 , wherein the Lewis acid is SO 3 , aluminum trichloride, or antimony pentafluoride.
6 . The process according to claim 4 , wherein the conjugated protic acid-Lewis acid complex is sulfuric acid and SO 3 complex, sulfuric acid and boric acid complex, fluorosulfonic acid and antimony pentafluoride complex, trifluoromethanesulfonic acid and antimony pentafluoride complex, hydrogen fluoride and antimony pentafluoride complex, HF and TaF 5 complex, BF 3 and HF complex, BF 3 and H 3 PO 4 complex, fluorosulfonic acid and SO 3 complex, HSO 3 F, HF and SbF 5 , complex, or HSO 3 F, SO 3 and SbF 5 .
7 . The process according to claim 1 , wherein the superacid is an immobilized superacid.
8 . The process according to claim 7 , wherein the immobilized superacid is immobilized trifluoromethanesulfonic acid or fluorosulfonic acid.
9 . The process according to claim 1 , wherein the process is carried out in the presence of a solvents selected from liquid sulfur dioxide, supercritical carbon dioxide, sulfolane, n-alkanes having from 4 to 12 carbon atoms, chlorobenzene, fluorobenzene, toluene, cumene, halogenated hydrocarbons, methyl acetate, ethyl acetate or n-butyl acetate.
10 . The process according to claim 1 , wherein the process is carried out in the presence of an additive which is converted rapidly under contact with carbon monoxide to metal carbonyls.
11 . The process according to claim 10 , wherein the additive is copper(l) oxide, silver(l) oxide, silver nitrate, iron pentacarbonyl Fe(CO) 5 , disodium tetracarbonylferrate(−2) Na 2 Fe(CO) 4 , octacarbonyidicobalt(O) Co 2 (CO) 8 or nickel tetracarbonyl Ni(CO) 4 .
12 . The process according to claim 1 , wherein the process is carried out at a CO pressure of from 1 bar to 500 bar, or at a reaction temperature of from −70° C. to +100° C.
13 . The process according to claim 1 , wherein from 0.1 mol to 5.0 mol of the compound of the formula II are used per liter of superacid, in particular from 0.3 mol to 3.0 mol.
14 . The process according to claim 10 , wherein the additive is used in an amount of from 5 mol % to 100 mol % based on the compound of formula II.
15 . The process according to claim 1 , wherein the compound of formula II is reacted with carbon monoxide or a carbon monoxide-releasing compound in the presence of water, water being present in an amount of from 2 mol % to 800 mol % based on the compound of the formula II, and of concentrated sulfuric acid or hydrogen fluoride or of a superacid or mixtures thereof.
16 . The process according to claim 15 , wherein the compound of formula II where X is bromine, R1 is methyl, R2 is methyl and R3 is 4-chlorobutyryl is reacted with carbon monoxide in the presence of trifluoromethanesulfonic acid and water, water being present in an amount of from 50 mol % to 500 mol % based on the compound of the formula II.
17 . The process according to claim 16 , wherein water is used in an amount of from 90 mol % to 300 mol %, in particular about 200 mol %, based on the compound of formula II.
18 . A compound of formula X
wherein Y is chlorine or bromine, and
R1 and R5 are each independently —(C 1 -C 4 )-alkyl.
19 . The compound according to claim 18 , wherein
Y is a chlorine atom and R1 and R5 are each methyl.
20 . A process for preparing the compound according to claim 18 , comprising
a) reacting a compound of formula III wherein Y is chlorine or bromine, and R1 and R4 are each independently —(C 1 -C 4 )-alkyl, with oxygen in the presence of cobalt(II) acetate tetrahydrate and N-hydroxyphthalimide, or b) reacting a compound of formula XI wherein Y is hydrogen, chlorine or bromine, X is chlorine or bromine, R1 and R4 are each independently —(C 1 -C 4 )-alkyl or R4 and X together form ═CH 2 or ═CH—(C 1 -C 3 )-alkyl; with water.
21 . A process for preparing a compound of formula VIII
wherein Y is hydrogen, chlorine or bromine, and R1 and R4 are each independently —(C 1 -C 4 )-alkyl,
comprising illuminating a compound of formula III
in the presence of N-bromosuccinimide or 1,3-dibromo-5,5-dimethylhydantoin and with heating.
22 . The process according to claim 21 , wherein the compound of the formula III is used wherein Y is chlorine, and R1 and R4 are each methyl.
23 . A process for preparing a compound of formula VIII
wherein Y is hydrogen, chlorine or bromine, and R1 and R4 are each independently —(C 1 -C 4 )-alkyl,
comprising illuminating a compound of formula III
in an aqueous biphasic mixture, wherein the aqueous phase comprises a bromine salt and the other phase is a liquid which is insoluble or only sparingly soluble in water.
24 . The process according to claim 23 , wherein the aqueous biphasic mixture consists of water and dichloromethane, and sodium bromate is present in the aqueous phase.
25 . The process according to claim 23 , wherein HBr is metered into the aqueous phase.
26 . A process for preparing a compound of formula IX
wherein Y is hydrogen, chlorine or bromine, and R1 and R4 are each independently —(C 1 -C 4 )-alkyl,
comprising reacting a compound of formula III
wherein Y is hydrogen, chlorine or bromine, and R1 and R4 are each independently —(C 1 -C 4 )-alkyl, to give a compound of formula IIIa
free-radically chlorinating the compound of formula IIIa at the benzylic position, with sulfuryl chloride or tert-butyl hypochlorite to give the compound of the formula IX.
27 . The process according to claim 26 , wherein the compound of the formula III is used wherein Y is chlorine atom, and R1 and R4 are each methyl.Cited by (0)
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