Continuous hydrodynamic cavitation crystallization
A device and process for crystallizing a compound using hydrodynamic cavitation comprises the steps of mixing at least one stream of a feed stock solution containing the compound to be crystallized. The feed stock solution is caused to flow through the cavitation zone of a rotor-stator type hydrodynamic cavitation device. Cavitation events and resulting shock waves generated in the cavitation zone cause nucleation and the production of seed crystals within the solution. Possible recirculation of the solution through the cavitation device promotes crystallization at the sites of the seed crystals resulting in increasing larger crystals. The resulting crystalized compound can be extracted from the solution and used in product manufacturing and industrial processes. The rotor-stator design allows for high flow rates, high applied energy and robust service with minimized wear.
1. A method of crystallizing a compound within a solution using controlled hydrodynamic cavitation, the method comprising the steps of:
obtaining a cavitation apparatus having an inlet, an outlet, and an internal cavitation zone;
causing the solution to flow through the cavitation apparatus in such a way that the solution moves through the cavitation zone;
generating cavitation within the solution in the cavitation zone to induce nucleation of the compound to form seed crystals;
distributing the seed crystals substantially uniformly throughout the solution;
promoting crystallization of the compound around the seed crystals to produce crystals within the solution; and
separating the crystals from the solution.
2. The method of claim 1 , wherein the compound to be crystallized is an inorganic material.
3. The method of claim 1 , wherein the compound to be crystallized is an organic material.
4. The method of claim 1 wherein the step of promoting crystallization of the compound comprises recycling the solution through the cavitation device.
5. The method of claim 1 further comprising the step of modifying the temperature of the solution within the cavitation device to control the rate of nucleation and cavitation.
6. The method of claim 1 wherein the step of promoting crystallization of the compound comprises moving the solution through a second cavitation device after seed crystals are formed in the solution.
7. The method of claim 1 wherein the compound comprises calcium carbonate.
8. The method of claim 1 further comprising the step of controlling the rate of flow of the solution through the cavitation device to control nucleation and crystallization.
9. The method of claim 1 wherein the step of distributing the seed crystals comprises subjecting the seed crystals to cavitation induced shock waves within the cavitation zone.
10. The method of claim 1 further comprising the step of adjusting the temperature of the solution prior to generating cavitation events in the solution to super saturate the solution with the compound.
11. The method of claim 10 wherein the step of adjusting the temperature comprises lowering the temperature.
12. A method of crystalizing calcium carbonate comprising the steps of:
mixing calcium oxide with water and carbon dioxide to form a feed stock solution;
moving the feed stock solution through a cavitation zone at a predetermined rate;
generating cavitation events within the solution in the cavitation zone, the cavitation events creating energetic shock waves that propagate through the solution;
the energetic shock waves promoting nucleation of calcium carbonate seed crystals within the solution;
distributing the seed crystals substantially uniformly throughout the solution;
promoting crystallization of calcium carbonate at the sites of the seed crystals to form calcium carbonate crystals;
monitoring the size and distribution of crystals formed in the solution;
discontinuing the crystallization of calcium carbonate within the solution when the crystals formed in the solution reach a predetermined size and a predetermined distribution in the solution; and
extracting the calcium carbonate crystals from the solution for use.
13. The method of claim 12 wherein the step of distributing the seed crystals substantially uniformly throughout the solution comprises subjecting the seed crystals to cavitation induced shockwaves within the cavitation zone.
14. The method of claim 12 wherein the step of promoting crystallization of calcium carbonate comprises recirculating the solution and seed crystals through the cavitation zone.
15. The method of claim 12 further comprising reducing the temperature of the solution to supersaturate the solution.
16. A method of inducing controllable nucleation and crystallization of a compound within a solution to produce crystals of the compound having a predetermined size range and a predetermined distribution throughout the solution, the method comprising the steps of:
(a) establishing a treatment zone within a controlled cavitation reactor, the treatment zone having a dimension that results in relatively low shear when the solution is moved through the treatment zone at a predetermined rate;
(b) passing the solution through the treatment zone at or below the predetermined rate to minimize shear within the solution;
(c) inducing cavitation events in the solution within the treatment zone to cause energetic shockwaves to move through the solution to promote nucleation and consequent formation of seed crystals in the compound within the solution;
(d) distributing the seed crystals substantially uniformly throughout the solution;
(e) promoting crystallization within the solution wherein crystals of the compound grow larger at the sites of the seed crystals;
(f) observing the size and distribution of the crystals within the solution;
(g) discontinuing crystallization of the compound within the solution when the crystals reach a size within a predetermined range and a predetermined distribution throughout the solution.