反应详情

The reaction is effected in a reactor arrangement of a first reactor of type E with a downstream reactor of type C. Before the start of the reaction, the first reactor is filled with a solution of 24.4% by weight of tert-butyl hydroperoxide and 12.7% by weight of potassium hydroxide in water. 33.6 kg/h of a solution of 70% by weight of tert-butyl hydroperoxide in water, 27.2 kg/h of a solution of 45% by weight of potassium hydroxide in water, 38.0 kg/h of water and 18.4 kg/h of isobutyroyl chloride are then fed to the first reactor. Cooling with cooling water keeps the internal temperature in the first reactor at 11° C. and in the second reactor at 12° C. The reaction mixture withdrawn from the second reactor is mixed with 8.0 kg/h of isododecane and the organic phase is removed. The organic phase is washed successively with an 8% by weight solution of sodium hydroxide in water, with a solution of 10% by weight of sodium sulphite in water comprising acetic acid and with a 1% by weight solution of sodium hydrogencarbonate in water, and then dried by stripping in a packed column at 20° C. and 47 mbar. 33.4 kg/h of a 75% by weight solution of tert-butyl peroxyisobutyrate in isododecane are obtained (92.8% based on isobutyroyl chloride). The space-time yield is 2.69 kg/l·h.

1. customThe reaction is effected in a reactor
2. customBefore the start of the reaction
3. customat 11° C.
4. customat 12° C
5. customThe reaction mixture withdrawn from the second reactor
6. additionis mixed with 8.0 kg/h of isododecane
7. customthe organic phase is removed
8. washThe organic phase is washed successively with an 8% by weight solution of sodium hydroxide in water, with a solution of 10% by weight of sodium sulphite in water
9. dry with materialwith a 1% by weight solution of sodium hydrogencarbonate in water, and then dried
10. customby stripping in a packed column at 20° C.