Manufacture of halonitrobenzenes

Claim 2

A process for the manufacture of halonitrobenzenes of the formula ##STR15## where R 1 and R 2 may be identical or different and each is halogen, and R 2 may also be hydrogen, by reacting halonitroanilines with alcohols and nitrosating agents at elevated temperatures in the presence of an acid, wherein halonitroanilines of the formula ##STR16## where R 1 and R 2 have the above meanings, are reacted with aliphatic, cycloaliphatic or araliphatic alcohols, which may be partly or wholly combined with the nitrosating agent, at not less than 35° C., in the presence of water.

Claim 3

A process as set forth in claim 1 wherein the reaction is carried out in the presence of from about 0.5 to 1,000 moles of water per mole of starting material II.

Claim 4

A process as set forth in claim 1, wherein the reaction is carried out with from 3 to 30 equivalents of alcohol per mole of starting material II.

Claim 5

A process as set forth in claim 1, wherein the reaction is carried out with alcohols of the formula R.sup.3 OH III where R 3 is alkyl of 1 to 5 carbon atoms or cyclohexyl, or aralkyl of 7 to 12 carbon atoms, or HO--R 4 --, where R 4 is alkylene of 2 to 4 carbon atoms, or R 3 is R 5 O--(R 4 O) n --R 4 --, where the individual R 4 's may be identical or different and each is alkylene of 2 to 4 carbon atoms, and R 5 is hydrogen or alkyl of 1 to 4 carbon atoms, and n is 4, 3, 2 or 1, and the above radicals may furthermore be substituted by alkyl or alkoxy each of 1 to 3 carbon atoms.

Claim 6

A process as set forth in claim 1, wherein the reaction is carried out with from 1.1 to 5 moles of alkyl nitrite, other nitrous acid esters and/or nitrous gases per mole of starting material II.

Claim 7

A process as set forth in claim 1, wherein the reaction is carried out with from 1.1 to 1.7 moles of alkyl nitrite or other nitrous acid esters or with from 1.5 to 5 moles of N 2 O 3 per mole of starting material II.

Claim 8

A process as set forth in claim 1, wherein the reaction is carried out with from 1.1 to 5 moles of monoglycol ester per mole of starting material II.

Claim 9

A process as set forth in claim 1, wherein the reaction is carried out with from 1.1 to 2.7 moles of monoglycol ester per mole of starting material II.

Claim 10

A process as set forth in claim 1, wherein the reaction is carried out with from 0.55 to 2.5 moles of diglycol ester per mole of starting material II.

Claim 11

A process as set forth in claim 1, wherein the reaction is carried out with from 5 to 100 moles of water per mole of starting material II.

Claim 12

A process as set forth in claim 1, wherein the reaction is carried out with from 1.5 to 15 equivalents of acid, based on starting material II.

Claim 13

A process as set forth in claim 1, wherein the reaction is carried out at from 35° C. to the boiling point of the mixture.

Claim 14

A process as set forth in claim 1, wherein the reaction is carried out at from 40° to 200° C.

Claim 15

A process as set forth in claim 1, wherein the reaction is carried out at from 45° to 100° C.