Method for recovering fluorinated emulsifiers from aqueous phases
A technology in emulsifier and water phase, which is applied in the field of wastewater treatment and can solve problems such as blockage of exchange towers
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0029] Process waste water (polymerization mother liquor) to be treated comes from the polymerization process of tetrafluoroethylene, hexafluoroethylene and vinylidene fluoride terpolymer, wherein polymer latex particles account for 0.3% by weight, and perfluorooctanoic acid accounts for 0.1% by weight. p-Octylphenol-ethoxylate commercially available under the trade name TRITON X 100 (Rohm & Haas, CAS-Nr. 9002-93-1) was used.
[0030] Concentration of TRITON® (ppm)
[0031] The concentration of PFOA near breakthrough shows a "run-out" at higher concentrations of nonionic surfactant. At higher concentrations of nonionic surfactants, the ion exchange capacity tends to decrease.
Embodiment 2
[0033] The example was repeated except that commercially available fatty alcohol polyglycol ether(R) GENAPOL X 080 (Hoechst AG) was used as the nonionic surfactant.
[0034] Concentration of GENAPOL (ppm)
Embodiment 3
[0036] The steps of Example 2 were repeated, but the treated process wastewater (polymerization mother liquor) was from the polymerization process of a copolymer of tetrafluoroethylene and perfluoro(n-propyl-ethyl) ether. This wastewater contained 0.1% by weight of PFOA and 0.4% by weight of polymer latex particles.
[0037] Concentration of GENAPOL (ppm)
PUM
| Property | Measurement | Unit |
|---|---|---|
| diameter | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More