Revaluation of aqueous waste streams in the propylene oxide/styrene co-production process
The present disclosure describes a method for the revaluation of aqueous waste streams generated in the propylene oxide and styrene co-production processes. In particular, it discloses a method of reducing the organic contaminant load from a highly contaminated aqueous stream and recovery from said stream of organic compounds that may be recirculated or used as fuel in the co-generation of energy, and which comprises: acidification of said aqueous stream with inorganic acid at a pH less than 4.5; separation of the two resulting phases at a temperature greater than 40° C.; washing of the organic phase produced in the previous step with an aqueous solution of excess acid and separation of the two resulting phases.
1. Method for the treatment of an alkaline aqueous stream with high organic matter content, from a propylene oxide/styrene production process, which comprises the following steps:
a. acidification of said alkaline aqueous stream with inorganic acid at a pH less than 4.5;
b. separation of the two phases resulting in step (a) at a temperature greater than 40° C.;
c. washing of the organic phase produced in step (b) with an acid aqueous solution, using an excess of acid in relation to the stoichiometric quantity corresponding to the sodium present in the organic phase;
d. separation of the two phases produced in (c).
2. Method according to claim 1 , wherein the acidification of step (a) is carried out with sulphuric acid.
3. Method according to claim 1 , wherein the separation of phases from step (b) is performed at a temperature greater than 50° C.
4. Method according to claim 1 , wherein the separation of phases from step (b) and/or (d) is carried out by decantation.
5. Method according to claim 1 , wherein the acid from step (c) is inorganic acid.
6. Method according to claim 5 , wherein the inorganic acid is sulphuric acid.
7. Method according to claim 1 , wherein the organic phase/aqueous phase ratio of step (c) is of between 1/2 and 3/1.
8. Method according to claim 7 , wherein the organic phase/aqueous phase ratio is of between 1/1 and 2/1.
9. Method according to claim 1 , wherein the excess acid from step (c) is of between 3 and 6% by weight.
10. Method according to claim 9 , wherein the excess acid is between 4.5 and 5.5% by weight.