Method and apparatus for recovering dielectric fluids used for immersion cooling
A method of and system for recovering a dielectric fluid used for immersion cooling of electronic devices, the method including filtering the dielectric fluid to remove a first group of solid contaminants; distilling the filtered dielectric fluid in one or more distillation tanks to produce a vaporized dielectric fluid; separating the vaporized dielectric fluid from less volatile contaminants, such that the vaporized dielectric fluid is introduced as a condensate into a circulation tank; circulating the condensate by pumping the condensate from the circulation tank through one or more filters; filtering the circulating condensate through the filter(s) to remove a second group of contaminants; and returning the filtered condensate to the circulation tank.
1. A method of recovering a liquid dielectric used for immersion cooling of at least one electronic device, the method comprising:
filtering the liquid dielectric to remove a first group of solid contaminants;
distilling the filtered liquid dielectric in at least one distillation tank to produce a vaporized dielectric gas;
condensing the vaporized dielectric gas in the at least one distillation tank at a calibrated temperature to produce a condensate;
separating the condensate from less volatile contaminants, wherein the condensate is introduced into a circulation tank disposed downstream of the distillation tank;
circulating the condensate by pumping the condensate through the circulation tank disposed downstream of the distillation tank;
filtering the circulating condensate using at least one filter disposed downstream of the distillation tank to remove a second group of contaminants; and
returning the filtered condensate to the circulation tank disposed downstream of the distillation tank.
2. The method of claim 1 , wherein filtering the liquid dielectric to remove the first group comprises introducing the liquid dielectric into a mechanical filtration process disposed upstream of the distillation tank.
3. The method of claim 2 , wherein the mechanical filtration process comprises filtering the liquid dielectric through a plurality of mechanical particle filters of diminishing filter pore size.
4. The method of claim 3 , wherein the mechanical filtration process comprises filtering the liquid dielectric through the plurality of mechanical particle filters arranged serially from a largest pore size to a smallest pore size.
5. The method of claim 1 , wherein filtering the liquid dielectric to remove the first group comprises introducing the liquid dielectric into a filter with a desiccant.
6. The method of claim 1 , wherein filtering the liquid dielectric to remove the first group comprises introducing the liquid dielectric into a mixed carbon filter.
7. The method of claim 1 further comprising:
collecting the less volatile contaminants at a bottom portion of the at least one distillation tank.
8. The method of claim 7 , wherein the at least one distillation tank comprises a first distillation tank in fluid communication with a second distillation tank and producing and separating the vaporized dielectric gas comprises:
heating liquid dielectric in the first distillation tank to a first calibrated temperature to vaporize the liquid dielectric;
collecting the condensate of the vaporized dielectric gas in the second distillation tank; and
heating the collected condensate in the second distillation tank to a second calibrated temperature to vaporize the collected condensate.
9. The method of claim 8 , wherein the second calibrated temperature is less than the first calibrated temperature.
10. The method of claim 1 , wherein condensing comprises providing, within the at least one distillation tank, at least one fluid-cooled condensing coil on which the vaporized dielectric gas condenses.
11. The method of claim 10 , wherein collecting the condensate comprises gravity feeding the condensate from a surface of the fluid-cooled condensing coil to the circulation tank.
12. The method of claim 1 , wherein filtering the circulating condensate comprises filtering the circulating condensate through at least one filter with a desiccant.
13. The method of claim 1 , wherein filtering the circulating condensate comprises filtering the circulating condensate through at least one mixed carbon filter.
14. The method of claim 1 , wherein filtering the circulating condensate comprises filtering the circulating condensate through at least one mechanical particle filter.
15. The method of claim 14 , wherein filtering the circulating condensate comprises filtering the circulating condensate through a plurality of mechanical particle filters of diminishing filter pore size.
16. The method of claim 15 , wherein filtering the circulating condensate comprises filtering the circulating condensate through the plurality of mechanical particle filters arranged serially from a largest pore size to a smallest pore size.
17. The method of claim 1 further comprising interrupting distilling if a pressure in any of the at least one distillation tank exceeds an allowable pressure.
18. The method of claim 1 further comprising interrupting distilling if a level of the filtered liquid dielectric in any of the at least one distillation tank is less than a minimum allowable fluid level.
19. The method of claim 1 further comprising interrupting circulating the condensate through the circulation tank when at least one of a desired electrical resistivity, a predetermined infra-red spectroscopy, or a predetermined optical transmittance is measured in the circulating condensate.