Method for removing perfluoro caprylic acid from dispersing liquid of perfluoro polymer by using two-section method
A perfluoropolymer and perfluorooctanoic acid technology, which is applied in the field of perfluorooctanoic acid removal in perfluoropolymer dispersions, can solve the problems of difficult extraction and washing, large adsorption capacity, and weak removal ability
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
specific Embodiment approach
[0019] The following examples are further illustrations of the present invention, but the present invention is not limited thereto.
[0020] If there is no special instruction, the size of the ion exchange column used in the examples is The height is 2000mm, and it is equipped with corresponding thermometers, pH meters, eluent circulation pumps, eluent storage tanks, pressure gauges, flow meters and corresponding pipelines. All types of ion exchange resins used are Zibo Dongda Chemical Co., Ltd. products, ion exchange resins with a D prefix in the model number are macroporous ion exchange resins, and those without a D prefix are gel type ion exchange resins. The ion exchange resin is all activated according to the prior art before being filled into the ion exchange column. The content of perfluorooctanoic acid in the raw material perfluoropolymer dispersion used in the examples is 1000-3500ppm.
[0021] The used ion exchange resin is regenerated as follows:
[0022] After ...
Embodiment 1
[0023] Embodiment 1: adopt D301 type anion exchange resin and D201 type anion exchange resin
[0024] Raw materials: 2000 kg of polytetrafluoroethylene dispersion (perfluorooctanoic acid content is 2500ppm).
[0025] Fill the D301-type and D201-type ion-exchange resins into two ion-exchange columns respectively, and the filling height is 2 / 3 of the ion-exchange column. Make the polytetrafluoroethylene dispersion pass through the D301 resin ion exchange column and the D201 resin ion exchange column successively at a flow rate of 3 times the resin volume / hour. The temperature of the polytetrafluoroethylene dispersion is lower than 50°C before entering the ion exchange column, and the pH value 9. After the first stage of adsorption with D301 weakly basic anion exchange resin, the concentration of perfluorooctanoic acid in it is 15ppm, and then after the second stage of adsorption with D201 strong basic anion exchange resin, the perfluorooctanoic acid (PFOA) in the polytetrafluor...
Embodiment 2
[0026] Embodiment 2: adopt D301 type anion exchange resin and 201 * 7 type anion exchange resin
[0027] Raw materials: 2000 kg of polytetrafluoroethylene dispersion (perfluorooctanoic acid content is 3000ppm).
[0028]Two ion exchange resins of type D301 and type 201×7 are respectively filled into two ion exchange columns, and the filling height is 1 / 3 of the ion exchange column. Make the raw material polytetrafluoroethylene dispersion pass through the D301 resin ion exchange column and the D201×7 resin ion exchange column successively at a flow rate of 2 times the resin volume / hour, and the temperature of the polytetrafluoroethylene dispersion before entering the ion exchange column is lower than 50°C , pH 8.5. After the first stage of adsorption with D301 weakly basic anion exchange resin, the concentration of perfluorooctanoic acid in it is 14ppm, and then the second stage of adsorption is carried out through 201×7 strong basic ion exchange resin, and the dispersion liqui...
PUM

Abstract
Description
Claims
Application Information

- R&D
- Intellectual Property
- Life Sciences
- Materials
- Tech Scout
- Unparalleled Data Quality
- Higher Quality Content
- 60% Fewer Hallucinations
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2025 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com