Distillation apparatus
A modular distillation apparatus including at least one heat exchanger that preheats contaminated liquids: a heater that heats the contaminated liquid from the heat exchanger; an evaporator condenser adapted o boil the contaminated liquid coming out of the heater to produce water vapor and contaminant concentrate, and condenser the water vapor into distilled water; a vacuum chamber capable of operating at below atmospheric pressure, the vacuum chamber housing the evaporator condenser and including at least one partition to separate the distilled water from the contaminate concentrate; a vapor compressor operably associated with the vacuum chamber to receive water vapor from the evaporator condenser in the vacuum chamber and pump the water vapor at pressure back through the evaporator condenser, wherein the heat exchanger recovers sensible heat from outgoing condensed distilled water and contaminant concentrate recycled from the vacuum chamber.
1. A distillation apparatus for producing distillate from a contaminated liquid, comprising:
a vacuum chamber and associated vacuum pump for creating a vacuum therein;
an evaporator-condenser positioned within said vacuum chamber, said evaporator-condenser having a plurality of plates, each of said plurality of plates having a first surface for facilitating evaporation of the contaminated liquid into a vapor, and a second surface for facilitating condensation of a compressed vapor into a distillate;
at least one partition positioned within said vacuum chamber for separating the distillate from the contaminated liquid;
a vapor compressor for receiving the vapor from said vacuum chamber at a first temperature and pumping the compressed vapor back into said vacuum chamber at a higher temperature;
at least one heat exchanger that recovers sensible heat from at least one of the distillate and a concentrate pumped from said vacuum chamber and preheats incoming contaminated liquid using the recovered heat; and
a start-up heater for further heating the preheated contaminated liquid from said at least one heat exchanger before the preheated contaminated liquid enters said vacuum chamber,
wherein condensation of the compressed vapor into the distillate by said second surface of said plurality of plates releases latent heat from the compressed vapor into said evaporator-condenser thereby evaporating the preheated contaminated liquid, and
wherein said evaporator-condenser is a rising film or a falling film heat exchanger.
2. The distillation apparatus of claim 1 , wherein said vacuum chamber includes at least one transparent and removable panel.
3. The distillation apparatus of claim 1 , wherein said vapor compressor re-circulates a portion of the vapor inside said vacuum chamber.
4. The distillation apparatus of claim 1 , wherein each of said plurality of plates is non-porous.
5. The distillation apparatus of claim 4 , wherein at least one of said first surface and said second surface of said plurality of plates is hydrophilic.
6. The distillation apparatus of claim 1 , wherein said vacuum chamber further includes at least one baffle to accelerate vapor velocity within said vacuum chamber and separate droplets of boiling liquid residues from the vapor.
7. The distillation apparatus of claim 1 , wherein said vapor compressor maintains a higher pressure on said second surface than on said first surface of each of said plurality of plates.
8. The distillation apparatus of claim 1 , wherein each of said plurality of plates has a thickness between 0.1 mm and 0.25 mm.
9. The distillation apparatus of claim 1 , further comprising pumps for pumping the contaminated liquid through said at least one heat exchanger and into said vacuum chamber, and the distillate and concentrate from said vacuum chamber through said at least one heat exchanger.
10. The distillation apparatus of claim 1 , wherein a higher pressure on said second surface of said plurality of plates in said evaporator-condenser than a pressure on said first side of said plurality of plates ensures fail safe distillation.
11. The distillation apparatus of claim 1 , wherein the distillation apparatus operates as a standalone unit.
12. The distillation apparatus of claim 1 , wherein said evaporator-condenser boils the contaminated liquid in a temperature range of 40° C. to 100° C.
13. The distillation apparatus of claim 1 , wherein the distillation apparatus may be transported with one or more distillation apparatus in international standard organization (ISO) shipping containers.
14. The distillation apparatus of claim 1 , wherein said vapor compressor is integral to said vacuum chamber.
15. A distillation apparatus for producing distillate from a contaminated liquid, comprising:
a vacuum chamber having an evaporator-condenser positioned therein, said evaporator-condenser having a plurality of non-porous plates, each of said plurality of non-porous plates having a thickness between 0.1 mm and 0.25 mm, a first surface for facilitating evaporation of the contaminated liquid into a vapor and a concentrate, and a second surface for facilitating condensation of a compressed vapor into a distillate;
a vapor compressor for extracting the vapor from said vacuum chamber and transferring the compressed vapor back into said vacuum chamber;
at least one heat exchanger that recovers heat from the distillate and the concentrate exiting said vacuum chamber and preheats incoming contaminated liquid using the recovered heat; and
a heater for further heating the preheated contaminated liquid from said heat exchanger before the preheated contaminated liquid enters said vacuum chamber
wherein said plurality of non-porous plates have hydrophilic outer surfaces.
16. The distillation apparatus of claim 15 , wherein condensation of the compressed vapor into the distillate by said second surface of said plurality of plates releases heat from the compressed vapor into said evaporator-condenser thereby further heating the preheated contaminated liquid.
17. The distillation apparatus of claim 15 , wherein said vacuum chamber includes at least one transparent panel.
18. The distillation apparatus of claim 15 , wherein said evaporator-condenser boils the contaminated liquid in a temperature range of 40° C. to 100° C.
19. A method of producing distillate from a contaminated liquid, comprising the steps of:
positioning an evaporator-condenser having a plurality of plates within a vacuum chamber, said evaporator-condenser being a rising film or a falling film heat exchanger;
creating a vacuum in said vacuum chamber;
pumping a contaminated liquid into a heat exchanger for preheating the contaminated liquid using recovered heat;
initially heating the preheated contaminated liquid from said heat exchanger before the preheated contaminated liquid enters said vacuum chamber;
facilitating evaporation of the contaminated liquid into a vapor and a concentrate by contacting the contaminated liquid with a first surface of a plate of said plurality of plates;
separating the distillate from the contaminated liquid using at least one partition positioned within said vacuum chamber;
extracting the vapor from said vacuum chamber at a first temperature;
compressing the extracted vapor and transferring the compressed vapor back into said vacuum chamber at a higher temperature;
facilitating condensation of the compressed vapor into a distillate with a second surface of a plate of said plurality of plates; and
heating the preheated contaminated liquid within said evaporator-condenser using latent heat released from the compressed vapor.
20. The method of producing distillate from a contaminated liquid of claim 19 , further comprising the step of recovering sensible heat from at least one of the distillate and the concentrate leaving said vacuum chamber; and using the recovered sensible heat for preheating the contaminated liquid in said heat exchanger.
21. The method of producing distillate from a contaminated liquid of claim 19 , further comprising the step of accelerating vapor condensation inside said vacuum chamber using at least one baffle positioned therein.
22. The method of producing distillate from a contaminated liquid of claim 20 , further comprising the step of re-circulating the vapor inside said vacuum chamber to accelerate vapor condensation on said plurality of plates.
23. The method of producing distillate from a contaminated liquid of claim 19 , further comprising the step of pumping the distillate from said vacuum chamber and through said heat exchanger.
24. The method of producing distillate from a contaminated liquid of claim 19 , wherein the step of facilitating evaporation occurs in a temperature range of 40° C. to 100° C.