Method for enhancing cyclonic vessel efficiency with polymeric additives
View Patent ↗The present invention is directed to a novel method and system for enhancing the efficiency of hydraulic centrifugal separators (cyclones) in the removal of fine size particles from a liquid carrying medium. More particularly, it is concerned with improvements in the removal efficiency of any number of cyclonic devices that rely on the use of centrifugal force to separate fine size particles of differing density from the liquid carrying medium by addition of polymeric additives, both before, and, as necessary, inside the cyclone body.
1. A method for combining specific polymeric additives in a liquid stream containing fine suspended solid particles to enhance hydraulic centrifugal separator (cyclone) performance, the cyclone having an upsteam feed inlet coupled to a mixing chamber having an overflow outlet, a conical section being coupled to and terminating opposite the mixing chamber in a downstream discharge apex, the method comprising the steps of:
(a). introducing a liquid cationic coagulant, if necessary, into the liquid stream at a first distance upstream of the cyclone;
(b). introducing a an anionic copolymer blend solution into the liquid stream at a second distance upsteam of the cyclone;
(c). introducing an initial dose of cationic copolymer solution into the liquid stream at a third distance upstream of the feed inlet;
(d). introducing a second dose of the cationic copolymer solution at a fourth distance upstream of the cyclone feed inlet; then
(e). syphoning off through the overflow outlet an outflow fluid stream into a cone bottom tank;
(f). introducing additional cationic copolymer solution, if needed, through a polymer ring located just above the apex;
(g). remove flocculated solids settling in bottom of cone bottom tank; and
(h). discharge cyclone underflow solids through the apex.
2. The method for recovering fine size particles according to claim 1 , wherein the particles are granite, limestone, sandstone, or igneous rock.
3. A method for recovering fine size particles according to claim 2 , wherein
the hydraulic centrifugal separator discharges from 85–99.9% of all suspended solids, regardless of initial size, from the apex.
4. The method for recovering fine size particles according to claim 1 , wherein the
particles are phosphatic clays.
5. A method according to claim 2 or 4 wherein the cationic coagulant
is a DADMAC type polymer with molecular weight of 200,000–500,000, and 100% charge, and active solids content of from 20% to dry powder (90+%).
6. A method according to claim 5 , wherein the cationic coagulant
is diluted with water before injection into the fluid stream.
7. The method for recovering fine size particles according to claim 1 , wherein
the particles are red mud solids left from the flashing operation in the Bayer Process.
8. A method according to claim 7 , wherein
the anionic copolymer is an anionic hydroxamated polyacrylamide.
9. A method according to claim 4 , wherein
the degree of hydroxamation of said polymer ranges from 1 to about 90 mole percent.
10. A method according to claim 7 , wherein
the cationic copolymer ranges in charge from 2.5–60 mole %.
11. The method for recovering fine size particles according to claim 1 , wherein
the particles are neutralization tailings from the titanium dioxide Chloride/Sulfate Process.
12. A method according to claim 2 , 4 , or 11 wherein the anionic copolymer blend solution further comprises
an emulsion that is inverted to 0.25–0.50% solution strength and aged before injection into the process stream.
13. A method according to claim 12 , wherein
the anionic copolymer blend solution has an anionic charge ranges from 1–95 mole %.
14. A method according to claim 2 , 4 , 7 , or 11 wherein the cationic copolymer further comprises
an emulsion that is inverted to 0.25–0.50% solution strength and aged before injection.
15. A method according to claim 14 , wherein
the majority of the polymer solution is injected via a polymer ring immediately upstream of the feed inlet.
16. A method according to claim 15 , wherein the cationic copolymer is in a range of 40–65 mole %.
17. A method according to claim 2 , 4 , 7 , or 11 wherein
an additional dosage of cationic copolymer solution may be added via a polymer ring just upstream of the apex.
18. A method according to claim 2 , 4 , 7 , or 11 wherein
materials discharged from the cyclone and cone bottom tank may be sent to a rotating screen (trommel), or pug mill for additional dewatering and material blending.
19. A method according to claim 11 , wherein the anionic copolymer further comprises
structured nonionic polymer with a anionic charge of 0–2 mole %.
20. A method according to claim 2 , 4 , 7 , or 11 wherein
an additional upper cone section can be added to increase cyclone efficiency.
21. The method for recovering fine size particle according to claim 1 , wherein magnitudes of the first and second distances
are chosen for thorough mixing of the coagulant and copolymer with the fluid stream.
22. The method for recovering fine size particles according to claim 21 , wherein magnitudes of the first and second distances
are chosen for optimal mixing with the fluid stream.
23. The method for recovering fine size particle according to claim 21 , wherein the third distance less than the second and first distances.
24. The method for recovering fine size particles according to claim 1 , wherein the third distance is between two feet and ten feet (2′–10′).
25. The method for recovering fine size particles according to claim 1 , wherein the fourth distance is directly in front of the feed inlet.
26. A method for combining specific polymeric additives in a liquid stream containing fine suspended solid particles to enhance cyclone performance, comprising the following steps of:
(a). introducing a liquid cationic coagulant, if necessary, into the liquid stream containing fine size particles, at sufficient distance from the cyclone for proper mixing:
(b). introducing an anionic copolymer blend solution into the liquid stream at optimum distance before the cyclone for proper mixing/dosing;
(c). introducing an initial dose of cationic copolymer solution into the liquid stream, at a distance of 10′ to 2′ in front of the cyclone feed inlet;
(d). introducing a second dose of the cationic copolymer solution directly in front of the cyclone feed inlet; then
(e). syphoning off through an overflow outlet an overflow fluid stream into a cone bottom tank;
(f). introducing additional cationic copolymer solution, if needed, through a polymer ring located just above the apex;
(g). removing flocculated solids settling in a bottom of the cone bottom tank through an automated dump valve controlled by level probes in said tank, with gravity flow, pump, or screw auger; and
(h). discharging cyclone underflow solids through the apex into material bin, conveyor, or stockpile.