Electro-Kinetic Separation of Solid Particles from Alkylated Aromatics
US-2018214892-A1 · Aug 2, 2018 · US
US10427074B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10427074-B2 |
| Application number | US-201815951241-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 12, 2018 |
| Priority date | Apr 19, 2017 |
| Publication date | Oct 1, 2019 |
| Grant date | Oct 1, 2019 |
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Apparatuses and processes for use in electrostatic filtration are provided. The apparatuses and processes provided herein promote effective and efficient removal of solid matters even in feeds containing a relatively substantial amount of water through the use of a water spreading resistant coating.
Opening claim text (preview).
The invention claimed is: 1. An electrostatic separator, comprising: a vessel containing a plurality of dielectric elements arranged as a bed; wherein the elements are coated with a water spreading resistant material, comprising one of siloxanes, fluorocarbon, and polystyrene and having a water contact angle on a flat surface of 75°-120°; and an electrode for applying an electric potential gradient across said bed. 2. The separator of claim 1 , wherein the water spreading resistant material comprises polystyrene. 3. The separator of claim 1 , wherein the dielectric elements are glass beads. 4. The separator of claim 1 , wherein the water contact angle on a flat surface is from 85°-115°. 5. A method for removing solids from a hydrocarbon stream, comprising: providing a hydrocarbon stream with an amount of suspended solids; feeding the hydrocarbon stream to the electrostatic separator of claim 1 ; applying a voltage across the electrostatic separator to induce an electric field thereby causing a percentage of the suspended solids to stick to the plurality of dielectric beads arranged as a bed; and purging the bed to remove the separated solids. 6. The method of claim 5 , wherein the hydrocarbon stream contains dispersed water particles. 7. The method of claim 6 , wherein the dispersed water particles make up 1% or less by weight of the hydrocarbon stream. 8. The method of claim 6 , wherein the voltage across the electrostatic separator remains substantially constant over time for a given distance from the electrode. 9. The method of claim 5 , wherein the water spreading resistant material is polystyrene. 10. The method of claim 5 , wherein the water spreading resistant material has a water contact angle on a flat surface from 75°-120°. 11. The method of claim 10 , wherein the water contact angle on a flat surface is from 85°-115°. 12. The method of claim 5 , wherein the hydrocarbon stream has a non-petroleum particle content from 2500 wppm to 30000 wppm. 13. The method of claim 5 , further comprising recovering a filtered hydrocarbon stream. 14. The method of claim 13 , wherein the filtered hydrocarbon stream has a non-petroleum particle content of 500 wppm to 1200 wppm.
using open-gradient differential dielectric separation, i.e. using electrodes of special shapes for non-uniform field creation, e.g. Fluid Integrated Circuit [FIC] · CPC title
Dielectrophoresis, i.e. dielectric particles migrating towards the region of highest field strength · CPC title
Separation of insoluble materials · CPC title
by electric or magnetic means · CPC title
Electrostatic separation not provided for in any single one of the other main groups of this subclass · CPC title
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