Method and apparatus for treatment of effluents from production plants of epoxy compounds

Patent metadata

Field	Value
Publication number	US-10883184-B2
Application number	US-201314379344-A
Country	US
Kind code	B2
Filing date	Mar 27, 2013
Priority date	Mar 27, 2012
Publication date	Jan 5, 2021
Grant date	Jan 5, 2021

Abstract

The invention relates to a process of abatement of the organic content of a depleted brine coming from epoxy compound production involving a vapour stripping step and a mineralisation with hypochlorite in two steps, at distinct pH and temperature conditions.

First claim

The invention claimed is:

1. A process of treatment in a plant comprising a chlor-alkali electrolysis unit, upstream of the chlor-alkali electrolysis unit comprising a pre-oxidation unit and an oxidation unit, the process consisting of the following sequential steps:
a) feeding fresh brine to the chlor-alkali electrolysis unit to obtain products;
b) oxidizing an organic raw material with the products obtained from step a), thereby obtaining an epoxy compound and a depleted brine;
c) extracting a waste stream consisting of the depleted brine from step b) and vapor stripping the waste stream to obtain a vapor-stripped stream;
d) pre-oxidating the vapor-stripped stream from step c) in the pre-oxidation unit with hypochlorite at pH 3.5 to 5 and at a temperature of 50 to 60° C.;
e) followed by oxidating the material from step d) in the oxidation unit by further adding hypochlorite at pH 3 to 4 and at a temperature of 80 to 95° C. until obtaining a fresh brine; and
f) feeding the fresh brine obtained from step e) to the chlor-alkali unit in step a).

2. The process according to claim 1 wherein said depleted brine has a COD higher than 10,000 mg/l of oxygen at an inlet of step c) and of 2,000 to 4,000 mg/l of oxygen at an outlet of step c).

3. The process according to claim 1 wherein said depleted brine has a COD of 400 to 1,500 mg/l of oxygen at an outlet of step d).

4. The process according to claim 1 wherein said fresh brine at an outlet of step e) has a COD not higher than 40 mg/l of oxygen.

5. The process according to claim 1 wherein said organic raw material is selected from the group consisting of propylene, allyl chloride and glycerine and said epoxy compound is propylene oxide or epichlorohydrin.

6. The process according to claim 1 wherein said pre-oxidation step with hypochlorite is carried out by feeding chlorine and alkali.

7. The process according to claim 1 wherein said pre-oxidation unit is an electrolysis cell of the undivided type.

8. The process according to claim 1 wherein said oxidation unit is an electrolysis cell.

9. The process according to claim 8 wherein said electrolysis cell is an alkali brine electrolysis cell of the undivided type.

10. The process according to claim 1 wherein said oxidation unit is a chlor-alkali electrolysis unit, consisting of an electrolysis cell equipped with a non-asbestos diaphragm separator comprising fluorinated polymer fibers.

11. The process according to claim 1 , wherein said vapor stripping step takes place at pH adjusted between 3 and 4.

Assignees

• Industrie De Nora Spa

Inventors

• Iacopetti Luciano
• Meneghini Giovanni
• Porcino Gaetano
• Faita Giuseppe

Classifications

• C02F1/20 Primary

  by degassing, i.e. liberation of dissolved gases (degasification of liquids in general B01D19/00; arrangement of degassing apparatus in boiler feed supply F22D) · CPC title

• C25B3/11

  Halogen containing compounds · CPC title

• C25B3/23

  Oxidation (halogenation C25B3/27) · CPC title

• C25B3/07

  Oxygen containing compounds · CPC title

• C25B15/085

  Removing impurities · CPC title