PROCESS FOR PREPARING HYDRAZINE HYDRATE USING AN ABSORPTION COLUMN
The invention relates to a process for preparing hydrazine hydrate, comprising the following successive steps: a) preparation by means of an absorption column of an aqueous solution comprising dissolved ammonia and comprising at least one activator, by introduction into the absorption column of an aqueous solution comprising at least one activator and of fresh ammonia, then b) reaction within at least one reactor of the aqueous ammonia solution comprising at least one activator obtained in the preceding step with hydrogen peroxide and a ketone, then c) separation of the organic phase containing the azine from the aqueous phase from the stream formed on conclusion of the preceding step, then d) hydrolysis of the organic phase obtained in the preceding step to obtain hydrazine hydrate.
1 . Process for preparing hydrazine hydrate, comprising the following successive steps:
a) preparation by means of an absorption column of an aqueous solution comprising dissolved ammonia in a proportion of between 50% and 100% relative to the saturation of ammonia in pure water at the temperature of the column and comprising at least one activator, by introduction into the absorption column of an aqueous solution comprising at least one activator and of fresh ammonia; then
b) reaction within at least one reactor of the aqueous ammonia solution comprising at least one activator obtained in the preceding step with hydrogen peroxide and a ketone of formula R 1 R 2 CO, the groups R 1 and R 2 denoting, independently of one another, a methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl and octyl group; then
c) separation of the organic phase containing the azine from the aqueous phase from the stream formed on conclusion of the preceding step; then
d) hydrolysis of the organic phase obtained in the preceding step to obtain hydrazine hydrate.
2 . Process according to claim 1 , characterized in that, in step a), the aqueous solution comprising at least one activator is introduced at the top of the absorption column and the fresh ammonia is introduced in countercurrent, preferably at the bottom of the absorption column.
3 . Process according to claim 1 , characterized in that a stream of the reaction medium of the reactor of step b) feeds the absorption column of step a), this stream being injected at the top of the column.
4 . Process according to claim 1 , characterized in that the aqueous solution isolated in step c) is recycled into the absorption column of step a).
5 . Process according to claim 1 , characterized in that the absorption column of step a) is fed with one or more streams of ammonia that has been recycled within the process.
6 . Process according to claim 1 , characterized in that the ketone used in step b) is methyl ethyl ketone.
7 . Process according to claim 1 , characterized in that it comprises a step of regenerating and concentrating the aqueous phase from the separation step c).
8 . Process according to claim 1 , characterized in that it comprises a step of washing the organic phase, from the separation step c).
9 . Process according to claim 1 , characterized in that the process is carried out batchwise.
10 . Process according to claim 1 , characterized in that the process is carried out continuously.