Water vapor distillation apparatus, method and system

Patent metadata

Field	Value
Publication number	US-10919782-B2
Application number	US-201615095679-A
Country	US
Kind code	B2
Filing date	Apr 11, 2016
Priority date	Jun 7, 2007
Publication date	Feb 16, 2021
Grant date	Feb 16, 2021

Abstract

A fluid vapor distillation apparatus. The apparatus includes a source fluid input, and an evaporator condenser apparatus. The evaporator condenser apparatus includes a substantially cylindrical housing and a plurality of tubes in the housing. The source fluid input is fluidly connected to the evaporator condenser and the evaporator condenser transforms source fluid into steam and transforms compressed steam into product fluid. Also included in the fluid vapor distillation apparatus is a heat exchanger fluidly connected to the source fluid input and a product fluid output. The heat exchanger includes an outer tube and at least one inner tube. Also included in the fluid vapor distillation apparatus is a regenerative blower fluidly connected to the evaporator condenser. The regenerative blower compresses steam, and the compressed steam flows to the evaporative condenser where compressed steam is transformed into product fluid. The fluid vapor distillation apparatus also includes a control system.

First claim

What is claimed is:

1. A fluid vapor distillation system comprising:
a counter-flow tube-in-tube heat exchanger comprising a plurality of inner tubes inserted into and aligned with an outer tube;
an evaporator condenser comprising a housing, wherein the counter-flow heat exchanger is wrapped around the housing and
a control system for controlling the fluid vapor distillation system comprising:
at least one controller programmed to control one or more processes in the fluid vapor distillation system, the fluid vapor distillation system programmed to include;
an idle state wherein the at least one controller is off;
a fill state wherein a source valve is opened and source fluid enters a sump in the fluid vapor distillation system;
a heat state wherein a heater in the sump is operated at a maximum level until fluid in the sump reaches a predetermined temperature;
a heat exchanger prime state wherein the source valve is opened at a predetermined duty cycle;
a start pump state wherein a bearing feed pump is run at a predetermined speed and a blower motor speed is increased until the blower motor reaches a predetermined speed; and
a run state wherein the fluid vapor distillation system produces product water; and
a blowdown level sensor in communication with a blowdown controller and a source flow controller, said blowdown level sensor sending signals related to a blowdown level to said blowdown controller and said source flow controller indicative of said blowdown level,
wherein said source flow controller is programmed to actuate said source flow valve to maintain the blowdown level at a first target, and
wherein said blowdown controller is programmed to actuate said blowdown valve to maintain the blowdown level at a second target, the second targeting being lower than the first target.

2. The fluid vapor distillation system of claim 1 further comprising:
a source fluid input;
wherein the source fluid input is fluidly connected to the evaporator condenser and the evaporator condenser transforms source fluid into steam and transforms compressed steam into product fluid.

3. The fluid vapor distillation system of claim 2 further comprising:
a regenerative blower fluidly connected to the evaporator condenser, whereby the regenerative blower compresses steam, and whereby compressed steam flows to the evaporative condenser whereby compressed steam is transformed into product fluid.

4. The fluid vapor distillation system of claim 3 wherein the outer tube is a source fluid flow path and the plurality of inner tubes are a product fluid flow path.

5. The fluid vapor distillation system of claim 3 wherein the heat exchanger further comprises two ends, and at each end a connector is attached, whereby one of the connectors forms a connection to the evaporator condenser.

6. The fluid vapor distillation system of claim 5 further comprising packing inside the tubes.

7. The fluid vapor distillation system of claim 6 wherein the packing is a rod.

8. The fluid vapor distillation system of claim 7 wherein the evaporator condenser further comprises a steam chest fluidly connected to the plurality of tubes.

9. The fluid vapor distillation system of claim 8 wherein the regenerative blower further comprises an impeller assembly driven by a magnetic drive coupling.

10. The fluid vapor distillation system of claim 9 wherein the control system comprises at least two processors, a motor control engine processor and an ARM processor.

11. The fluid vapor distillation system of claim 10 wherein the fluid vapor distillation apparatus further comprises a conductivity meter and a conductivity cell to determine the conductivity of the product fluid.

12. A fluid vapor distillation system comprising:
an evaporator/condenser comprising:
a sump that receives source water via a source valve;
an evaporative section that receives source water from the sump and produces low pressure vapor and blowdown water; and
a condenser section that receives high pressure vapor and produces product water;

a blower receiving low pressure vapor from the evaporator section and providing high pressure vapor to the condenser section and comprising a low-pressure temperature sensor and a high-pressure temperature sensor; and
a control system for controlling the fluid vapor distillation system comprising:
at least one controller programmed to control one or more processes in the fluid vapor distillation system, the fluid vapor distillation system programmed to include;
an idle state wherein the at least one controller is off;
a fill state wherein the source valve is opened and source fluid enters the sump in the fluid vapor distillation system;
a heat state wherein a heater in the sump is operated at a maximum level until at least one of the low-pressure temperature sensor and high-pressure temperature sensor reaches a predetermined temperature;
a heat exchanger prime state wherein the source valve is opened at a predetermined duty cycle;
a start pump state wherein a bearing feed pump is run at a predetermined speed, and a blower motor speed is increased until the blower motor speed reaches a preset range; and
a run state wherein the fluid vapor distillation system produces product water.

13. The fluid vapor distillation system of claim 12 wherein the controller exits the run state and enters a flow measurement state where a product flow rate and a blowdown flow rate are determined.

14. The fluid vapor distillation system of claim 13 , wherein the controller enters the flow measurement state at a predetermined interval and returns to the run state after the product flow rate and the blowdown flow rate are determined.

15. The fluid vapor distillation system of claim 13 further comprising a product collection container with a product level sensor, the product container receiving product water from the condenser section and providing product water to a product valve
wherein the controller empties the product container to a predetermined first value, then closes the product valve and monitors a signal from the product level sensor to determine the product flow rate.

16. The fluid vapor distillation system of claim 13 further comprising a blowdown collection container with a blowdown level sensor, the blowdown container receiving blowdown water from the evaporator section and providing blowdown water to a blowdown valve
wherein the controller empties the blowdown container to a predetermined first value, then closes the blowdown valve and monitors a signal from the blowdown level sensor to determine the blowdown flow rate.

17. The fluid vapor distillation system of claim 16 wherein the controller alerts the user if the blowdown flow rate exceeds a preset range of values.

18. The fluid vapor distillation system of claim 16 wherein the controller transitions the fluid vapor distillation system to idle if the blowdown flow rate exceeds a preset level.

19. The fluid vapor distillation system of claim 15 wherein the controller alerts the user if the product flow rate is outside of a preset range of product flow values.

20. The fluid vapor distillation system of claim 12 further comprising a standby state, where the blower motor is stopped and the heater maintains the low-pressure temperatures at a predetermined target value.

Assignees

• Deka Products Lp

Inventors

• Kamen Dean
• Larocque Ryan K
• Lagenfeld Christopher C
• Ent Stephen M
• Schnellinger Andrew A
• Bhay Mithun R
• Smith Stanley B
• Clapp Otis L

Classifications

• C02F2303/10

  Energy recovery · CPC title

• C02F2103/06

  Contaminated groundwater or leachate · CPC title

• C02F1/18

  Transportable devices to obtain potable water · CPC title

• C02F1/16

  using waste heat from other processes · CPC title

• C02F1/08

  Thin film evaporation · CPC title