Water vapor distillation apparatus, method and systems

Patent metadata

Field	Value
Publication number	US-11939237-B2
Application number	US-202017008483-A
Country	US
Kind code	B2
Filing date	Aug 31, 2020
Priority date	Jul 15, 2011
Publication date	Mar 26, 2024
Grant date	Mar 26, 2024

Abstract

A fluid vapor distillation system. The system includes a control system for controlling a fluid vapor distillation apparatus including a blow down controller for controlling a blow down valve, a source flow controller for controlling a source flow valve, and a blow down level sensor in communication with a blow down controller and a source flow controller, the blow down level sensor sends signals related to the blow down level to the blow down controller and the source flow controller indicative of the blow down level, wherein the source flow controller actuates the source flow valve based at least on the blow down level sensor signals, and wherein the blow down controller actuates the blow down valve based at least on the blow down level sensor signals, whereby the blow down level and the source flow level are maintained using the blow down level sensor signals as input.

First claim

What is claimed is:

1. A fluid vapor distillation apparatus comprising:
a source water input;
a product water output;
a compressor receiving water vapor and producing compressed vapor;
an evaporator condenser apparatus comprising;
an evaporator that receives source water, the evaporator transforms source water to water vapor and concentrate liquid;
a steam chest that receives concentrate liquid and water vapor and provides water vapor to the compressor; and
a condenser that receives compressed vapor from the compressor, the condenser transforming the compressed vapor to product water;

a heat exchanger comprising:
an outer tube fluidly connected to the source water input and the evaporator;
at least one inner tube fluidly connected to the evaporator condenser apparatus; and
a first end and a second end; and

a termination is attached to each of the first end and the second end, each of the terminations comprising:
a source water termination physically connected to the outer tube, the source water termination having a first port fluidly connected to the inside of the outer tube and a source water seal to the outer surface of the at least one inner tube;
a tube termination having at least a second port fluidly connected to the inside of the at least one inner tube port and a tube seal to the outer surface of the at least one inner tube;
wherein the tube termination is mechanically coupled to the source water termination; and
a leak path between the source water termination and the tube termination to the outside of the heat exchanger whereby fluid leaking past the source water seal or the tube seal may exit the heat exchanger.

2. The fluid vapor distillation apparatus of claim 1 , wherein the first port of the first end is fluidly connected to the source water inlet and first port of the second end is fluidly connected to the evaporator.

3. The fluid vapor distillation apparatus of claim 1 , wherein the second port of the second end is fluidly connected to the condenser and the second port of the first end is fluidly connected to the product water output, whereby the product water heats the source water.

4. The fluid vapor distillation apparatus of claim 3 , wherein the heat exchanger comprises 3 inner tubes.

5. The fluid vapor distillation apparatus of claim 1 , wherein the second port of the second end is fluidly connected to the steam chest and the second port of the first end is fluidly connected to a drain, whereby the concentrate fluid heats the source water.

6. The fluid vapor distillation apparatus of claim 1 , wherein the heat exchanger is wrapped in a spiral around the evaporator condenser apparatus.

7. The fluid vapor distillation apparatus of claim 1 , where the evaporator condenser apparatus further comprises a sump, plurality of tubes and an outer shell, the interior of plurality of tubes being fluidly connected to the sump and the steam chest and defining the evaporator, the condenser being defined by the exterior of the tubes and inside surface of the outer shell.

8. The fluid vapor distillation apparatus of claim 7 wherein said evaporator condenser apparatus further comprising packing inside the plurality tubes.

9. The fluid vapor distillation apparatus of claim 8 wherein said packing is a rod with a plurality of nubs that extend from the outer surface of the rod.

10. The fluid vapor distillation apparatus of claim 9 , wherein the rod may be 0.25 inch smaller diameter than an inside diameter of the tube.

11. The fluid vapor distillation apparatus of claim 1 , the evaporator condenser further comprising a tube sheet that separates the steam chest from the condenser and is sealed to the plurality of tubes.

12. The fluid vapor distillation apparatus of claim 11 , the evaporator condenser further comprising a compressed steam conduit that passes through the steam chest and the tube sheet to fluidly connect the compressor to the condenser.

13. The fluid vapor distillation apparatus of claim 11 , where the compressed steam conduit passes into the condenser section and includes openings to distribute the compressed steam along the length of the condenser.

14. A fluid vapor distillation apparatus comprising:
a source water input;
a product water output;
an evaporator condenser apparatus that transforms source water into water vapor and compressed water vapor into product water;
a compressor receiving water vapor and producing compressed vapor;
a heat exchanger comprising:
an outer tube;
at least one inner tube; and
a first end and a second end;

a termination is attached to each of the first end and the second end, each of the terminations comprising:
a source water termination physically connected to the outer tube, the source water termination having a first port fluidly connected to the inside of the outer tube and a source water seal to the outer surface of the at least one inner tube;
a tube termination having a second port fluidly connected to the inside of the at least one inner tube port and a tube seal to the outer surface of the at least one inner tube;
wherein the tube termination is mechanically coupled to the source water termination; and
a leak path between the source water termination and the tube termination to the outside of the heat exchanger whereby fluid leaking past the seal or the seal may exit the heat exchanger;

wherein the first port on the termination at the first end is fluidly connected to the source water inlet, and the second port on the termination at the first end is connected to the product water output and the first and second ports on the termination at the second end are fluidly connected to the evaporator condenser apparatus.

15. The fluid vapor distillation apparatus of claim 14 , wherein the source water seal to outside of the at least one inner tube is an O-ring.

16. The fluid vapor distillation apparatus of claim 14 , wherein the tube seal to outside of the at least one inner tube is an O-ring.

17. The fluid vapor distillation apparatus of claim 14 , wherein or the source water termination or the tube termination is made of a high temperature plastic.

18. The fluid vapor distillation apparatus of claim 14 , wherein the tube termination includes barb fittings.

19. The fluid vapor distillation apparatus of claim 14 , wherein the tube termination is mechanically attached to the source water termination.

Assignees

• Deka Products Lp

Inventors

• Kamen Dean
• Larocque Ryan K
• Langenfeld Christopher C
• Schnellinger Andrew A
• Bhat Prashant
• Clapp Otis L
• Smith Iii Stanley B
• Ent Stephen M

Classifications

• C02F1/041 Primary

  by means of vapour compression · CPC title

• B01D1/0058

  Use of waste energy from other processes or sources, e.g. combustion gas (for water treatment C02F1/16) · CPC title

• B01D1/2896

  Control, regulation · CPC title

• B01D3/007

  Energy recuperation; Heat pumps · CPC title

• B01D3/42

  Regulation; Control · CPC title