Method of fractionating oxidic nanoparticles by crossflow membrane filtration
View Patent ↗A method of fractionating a dispersion of oxidic nanoparticles wherein at least one step of the method is a membrane crossflow filtration step, the flow of the dispersion over the membrane being brought about by means of driven rotating parts; and dispersions of oxidic nanoparticles that are obtainable by the method.
1. A method of fractionating a dispersion comprising predominantly oxidic nanoparticles and also coarser oxidic particles, thereby obtaining a finer fraction of oxidic nanoparticles, the method comprising
filtrating via a membrane cross rotation filtration device, which comprises causing the dispersion to flow over a membrane by driven rotating parts,
wherein the membrane cross rotation filtration device comprises a filtration media part and a rotor part that are stacked one above the other in a sandwich formation, and the membrane cross rotation filtration device further comprises a rotation shaft that drives the rotor part, the rotation shaft positioned in the middle of the sandwich formation,
wherein the dispersion is stirred directly over the membrane,
wherein the dispersion is caused to flow over the membrane with an average flow velocity of between 5 and 25 m/s, and
wherein said filtrating produces a retentate and a filtrate, and said finer fraction of oxidic nanoparticles is present in the filtrate.
2. A method according to claim 1 , wherein the membrane has a pore diameter of between 0.01 μm and 5 μm.
3. A method according to claim 1 , wherein the membrane has a pore diameter of between 0.1 μm and 1 μm.
4. A method according to claim 1 , wherein the dispersion is caused to flow over the membrane with an average flow velocity of 8 m/s to 25 m/s.
5. A method according to claim 1 , wherein the dispersion is caused to flow over the membrane with an average flow velocity of 10 m/s to 25 m/s.
6. A method according to claim 1 , wherein the oxidic nanoparticles are particles of at least one of titanium oxide, cerium oxide, aluminum oxide, silicon dioxide, zirconium dioxide, zinc oxide, indium tin oxide, antimony tin oxide, and barium titanate.
7. A method according to claim 1 , wherein a grinding step is carried out after the filtrating step.
8. A method according to claim 7 , wherein the grinding step is performed with a ball mill, stirred ball mill or wet-jet mill.
9. A method according to claim 1 , wherein the retentate is washed via a diafiltration.
10. A method according to claim 9 , wherein the retentate is subjected to a grinding step which is carried out after the filtrating step.
11. A method according to claim 1 , wherein the filtrate is concentrated in a subsequent separation step.
12. A method according to claim 11 , wherein the subsequent separation step is an ultrafiltration step.
13. A method according to claim 11 , wherein the subsequent separation step produces a clear fraction, which clear fraction is recycled.
14. A method according to claim 1 , wherein the filtrating step takes place with periodic backwashing of the membrane.
15. A method according to claim 1 , wherein the dispersion has been diluted from a previous dispersion prior to the filtrating step.
16. A method according to claim 1 , wherein at least 50% of the finer fraction of oxidic nanoparticles have a particle diameter of less than or equal to 80 nm.
17. A method according to claim 1 , wherein at least 50% of the finer fraction of oxidic nanoparticles have a particle diameter of less than or equal to 50 nm.
18. A method according to claim 1 , wherein at least 50% of the finer fraction of oxidic nanoparticles have a particle diameter of less than or equal to 30 nm.