Product gas concentrator and method associated therewith

Patent metadata

Field	Value
Publication number	US-9375674-B2
Application number	US-201414202536-A
Country	US
Kind code	B2
Filing date	Mar 10, 2014
Priority date	Oct 25, 2005
Publication date	Jun 28, 2016
Grant date	Jun 28, 2016

Abstract

Various equipment and methods associated with providing a concentrated product gas are provided. In one embodiment, the equipment includes an input device first and second sieve tanks, a variable restrictor, and a controller. In one embodiment, the method includes: a) selecting a desired output setting for the concentrated product gas from a plurality of output settings, b) separating one or more adsorbable components from a pressurized source gaseous mixture via first and second sieve tanks in alternating and opposing pressurization and purging cycles to form the concentrated product gas, and c) selectively controlling a variable restrictor based at least in part on the desired output setting to selectively provide flow between the first and second sieve tanks such that the flow for at least one output setting is different from the flow for at least one other output setting in relation to corresponding pressurization cycles.

First claim

The invention claimed is:

1. A method of providing a concentrated product gas, comprising:
a) selecting a desired output setting for the concentrated product gas from a plurality of output settings;
b) separating one or more adsorbable components from a pressurized source gaseous mixture via first and second sieve tanks in alternating and opposing pressurization and purging cycles to form the concentrated product gas; and
c) selectively controlling at least two flow paths between the first and second sieve tanks of a valve assembly based at least in part on the desired output setting to selectively provide flow between the first and second sieve tanks, wherein the valve assembly includes a plurality of flow paths between the first and second sieve tanks, such that the flow between the first and second sieve tanks for at least one output setting is different from the flow between the first and second sieve tanks for at least one other output setting in relation to corresponding pressurization cycles.

2. The method of claim 1 , further comprising:
d) selectively controlling a bleed valve in series with a first orifice to selectively provide a first adjustable component of the flow between the first and second sieve tanks in c).

3. The method of claim 2 , further comprising:
e) providing a continuous component of the flow between the first and second sieve tanks in c) via a second orifice in parallel with the series combination of the first orifice and bleed valve.

4. The method of claim 2 , further comprising:
e) selectively controlling a pressure equalization valve in parallel with the series combination of the first orifice and bleed valve to selectively provide a second adjustable component of the flow between the first and second sieve tanks in c).

5. The method of claim 1 , further comprising:
d) defining an adjustable bleed delay period in relation to the start of pressurization cycles during which flow between the first and second sieve tanks is limited;
e) selectively controlling the valve assembly based at least in part on the adjustable bleed delay period, wherein the adjustable bleed delay period for at least one output setting is different from the adjustable bleed delay period for at least one other output setting in relation to corresponding pressurization cycles;
f) defining an adjustable bleed duration period in relation to expiration of the adjustable bleed delay period during which flow between the first and second sieve tanks is increased; and
g) selectively controlling the valve assembly based at least in part on the adjustable bleed duration period, wherein the adjustable bleed duration period for at least one output setting is different from the adjustable bleed duration period for at least one other output setting in relation to corresponding pressurization cycles.

6. The method of claim 1 , further comprising:
d) detecting a pressure for the concentrated product gas;
e) selectively controlling the valve assembly based at least in part on the detected pressure in relation to a bleed pressure threshold, the bleed pressure threshold for at least one output setting being different from the bleed pressure threshold for at least one other output setting in relation to corresponding pressurization cycles;
f) defining an adjustable bleed duration period during which flow between the first and second sieve tanks is increased after a determination that the detected pressure is above the bleed pressure threshold; and
g) selectively controlling the valve assembly based at least in part on the adjustable bleed duration period, wherein the adjustable bleed duration period for at least one output setting is different from the adjustable bleed duration period for at least one other output setting in relation to corresponding pressurization cycles.

7. The method of claim 1 , wherein the at least two sieve tank flow paths selectively allow gas to flow from one sieve tank to the other sieve tank via one or more of the at least two sieve tank flow paths without preventing the flow of concentrated product gas to a user.

8. The method of claim 1 , wherein the at least two sieve tank flow paths selectively allow gas to flow from one sieve tank to the other sieve tank via one or more of the at least two sieve tank flow paths while allowing the flow of concentrated product gas to a user.

9. The method of claim 1 , wherein the at least two sieve tank flow paths comprise:
a bleed flow path comprising a bleed valve in series with a first orifice to selectively provide a bleed flow of product gas from the pressurizing sieve tank to the purging sieve tank to assist regeneration of the purging sieve tank; and
an equalization flow path comprising a pressure equalization valve in parallel with the series combination of the bleed valve and the first orifice to selectively equalize pressure between the sieve tanks when the pressurizing sieve tank is near the end of the pressurizing cycle and the purging sieve tank is near the end of the purging cycle.

10. The method of claim 9 , wherein the product gas flow through the bleed flow path is less than the product gas flow through the equalization flow path.

11. The method of claim 1 , wherein selectively controlling comprises:
opening a first flow path of one of the at least two sieve tank flow paths to allow a bleed flow of product gas from the pressurizing sieve tank to the purging sieve tank to assist regeneration of the purging sieve tank; and
opening a second flow path of another of the at least two sieve tank flow paths to allow an equalization flow between the sieve tanks when the pressurizing sieve tank is near the end of the pressurizing cycle and the purging sieve tank is near the end of the purging cycle.

12. The method of claim 11 , wherein selectively controlling comprises:
opening the first flow path and the second flow path simultaneously for a predetermined time.

13. The method of claim 1 , wherein the valve assembly further includes an output flow path to provide concentrated product gas to a user independent of the at least two sieve tank flow paths.

14. The method of claim 13 , wherein the at least two sieve tank flow paths and the output flow path each have separate parallel portions.

15. A method of providing a concentrated product gas, comprising:
a) selecting a desired output setting for the concentrated product gas from a plurality of output settings;
b) separating one or more adsorbable components from a pressurized source gaseous mixture via first and second sieve tanks in alternating and opposing pressurization and purging cycles to form the concentrated product gas; and
c) selectively controlling at least two flow paths between the first and second sieve tanks of a valve assembly based at least in part on the desired output setting to selectively provide flow between the first and second sieve tanks, wherein the valve assembly includes:
state A to provide a bleed rate flow path between the first and second sieve tanks; and
state B to provide a pressure equalization flow path between the first and second sieve tanks; and

such that the flow between the first and second sieve tanks for at least one output setting is different from the flow between the first and second sieve tanks for at least one other output setting in relation to corresponding pressurization cycles.

16. The method of claim 15 , further comprising:
d) selectively controlling a bleed valve in series with a first orifice to selectively provide a first adjustable component of the flow between the first and second sieve tanks in c).

Assignees

• Invacare Corp

Inventors

• Sprinkle Thomas B
• Daniels William J
• Drobnak Thomas A
• Felty David G
• Hodos Valentine A
• Fabian Martin J
• Shelnutt Samuel J
• Olszewski Jonathon R

Classifications

• B01D53/0407 Primary

  Constructional details of adsorbing systems · CPC title

• Y02C10/08

  Cross-Sectional Technologies · mapped topic

• B01D2259/40043

  Purging · CPC title

• B01D2257/102

  Nitrogen · CPC title

• A61M2016/0036

  in the breathing tube and used in both inspiratory and expiratory phase · CPC title