High pressure oxygen production system

• US 4,636,226 A
• Filed: 08/26/1985
• Issued: 01/13/1987
• Est. Priority Date: 08/26/1985
• Status: Expired due to Fees

• Current Assignee: Command Center Incorporated (Security Partners, LLC)
• Original Assignee: VBM Corporation
• Inventors: Canfora, Philip H.
• Primary Examiner(s): Spitzer, Robert
• Application Number:
  US06/769,479
• Time in Patent Office: 505 Days
• Field of Search: 55/23-26, 55/31, 55/33, 55/35, 55/58, 55/59, 55/62, 55/68, 55/74, 55/75, 55/161-163, 55/179, 55/180, 55/303, 55/316, 55/387, 55/389, 138/30, 138/31
• US Class Current: 95/138
• CPC Class Codes: B01D 2256/12 Oxygen
• CPC Class Codes: B01D 2259/402 using two beds
• CPC Class Codes: B01D 53/04 with stationary adsorbents B01D53/025 takes precedence
• CPC Class Codes: B01D 53/047 Pressure swing adsorption
• CPC Class Codes: B01D 53/053 with storage or buffer vessel

Abstract

A cross-over valve (24) alternately supplies compressed air from a source of compressed air (A) to a pair of beds (26, 28) filled with a molecular sieve material. An oxygen rich gas component separated from the compressed air by the molecular sieve beds is channeled to a separated gas reservoir (C). To use the oxygen in the reservoir, the compressed air is directed against a barrier, such as bellows (52), located within the separated gas reservoir to compress the oxygen rich gas component held therein. The oxygen rich gas component is then supplied at this elevated pressure to welding or other downstream equipment. In this manner, the oxygen separator may operate sixteen hours to provide a supply of oxygen for an eight hour shift. The oxygen is supplied to the downstream equipment at a higher pressure which is increased over and above the supply pressure from the oxygen separation device.

Claims

1. A method of supplying a selected gaseous component at a first relatively high pressure, the method comprising:

supplying a gaseous mixture at a second, relatively high pressure;

separating the selected gaseous component from the mixture and supplying the separated, selected gaseous component to a separated gas reservoir at a first, relatively low pressure;

after receiving the selected gaseous component in the reservoir, contracting the effective volume of the gaseous reservoir under motive force supplied by the gaseous mixture such that the pressure of the selected gaseous component is increased to the first relatively high pressure;

removing the motive force of the gaseous mixture allowing the effective volume of the gaseous reservoir to expand and the pressure of the gaseous component therein to decrease such that additional selected gaseous component at the first, relatively low pressure is received therein;

cyclically repeating the effective volume contracting and expanding steps such that the pressure of the selected gaseous component is cyclically increased to the first relatively high pressure.

2. The method as set forth in claim 1 further including passing the selected gaseous component at the first relatively high pressure from the separated gas reservoir into an accumulator during the effective volume decreasing step and blocking the selected gaseous component from flowing from the accumulator back into the separated gas reservoir during the effective volume expanding step.

3. The method as set forth in claim 1 wherein the gaseous mixture is air and the selected gaseous component is oxygen.

4. The method as set forth in claim 3 wherein the effective volume contracting step includes inflating an expansion chamber within the separated gas reservoir with the compressed air.

5. The method as set forth in claim 1 wherein the effective volume contracting step includes utilizing the gaseous mixture to move a physical separation barrier to contract the effective volume of the separated gas reservoir.

6. An apparatus for supplying a selected gaseous component, the apparatus comprising:

a compressor means for supplying a gaseous mixture at a relatively high pressure;

a gas separating means for selectively separating at least one preselected gaseous component from the gaseous mixture, the gas separating means being operatively connected with the compressor means for receiving the gaseous mixture therefrom at the relatively high pressure and having a separated gas outlet through which the separated gaseous component is supplied at a relatively low pressure; and

,

a pressure increasing means for increasing the pressure of a separated gaseous component to a pressure which is higher than said relatively low pressure, the pressure increasing means being operatively connected with the compressor means to receive motive power from the relatively high pressure gaseous mixture received therefrom and being operatively connected with the gas separating means to receive the separated gaseous component and increase the pressure thereof above the relatively low pressure.

7. The apparatus as set forth in claim 6 wherein the pressure increasing means includes:

a separated gas reservoir for receiving the separated gaseous components from the gas separating means;

an expansible chamber disposed within the separated gas reservoir, an interior of the expansible chamber being isolated from the interior of the separated gas reservoir, and operatively connected with the compressor means for selectively receiving the gaseous mixture at the relatively high pressure to increase a volume of the expansible chamber and decrease a volume of the separated gas reservoir available for receipt of the separated gaseous component such that the pressure of the received, separated gaseous component is increased above the relatively low pressure by the selective increasing in the volume of the expansible chamber under the motive force of the relatively high pressure gaseous mixture from the compressor means.

8. The apparatus as set forth in claim 7 wherein the expansible chamber includes a flexible bladder.

9. The apparatus as set forth in claim 7 wherein the expansible chamber includes a movable barrier which is operatively disposed between the separated gaseous component received from the separating means at the relatively low pressure and the gaseous mixture received from the compressor means at a relatively high pressure.

10. The apparatus as set forth in claim 9 wherein the movable barrier includes a piston slidably mounted in the separated gas reservoir.

11. The apparatus as set forth in claim 7 wherein the pressure increasing means further includes a pressure multiplier means for multiplying the force exerted by the gaseous mixture such that the pressure of the separated gaseous component within the separated gas reservoir is increased to a pressure which is greater than the relatively high pressure of the gaseous mixture from the compressor means.

12. A gaseous component supplying apparatus for supplying a selected gaseous component at a relatively high pressure, the apparatus comprising:

a gas separating means for separating and supplying a preselected gaseous component at a relatively low pressure;

a separated gas reservoir for receiving the preselected gaseous component, the separated gas reservoir being operatively connected with the gas separating means;

an effective volume means for selectively contracting an effective volume of the separated gas reservoir available to receive the preselected gaseous component therein; and

,

a control means for cyclically disconnecting and connecting the effective volume means with a source of fluid at a relatively high pressure such that (i) when the effective volume means is connected with the relatively high pressure fluid source, the effective volume of the separated gas reservoir is contracted under motive force from the relatively high pressure fluid compressing the gaseous component received therein and (ii) when the effective volume means is disconnected from the relatively high pressure fluid source, the effective volume of the separated gas reservoir is permitted to expand to facilitate the receipt of the preselected gaseous component therein at the relatively low pressure, whereby the preselected gaseous component is cyclically received at the relatively low pressure and compressed to a higher pressure.

13. The apparatus as set forth in claim 12 wherein the source of fluid under pressure is a compressor means for supplying a gaseous mixture at the relatively high pressure, the compressor means being operatively connected both with the effective volume means to provide motive power thereto and with the gas separating means to supply the gaseous mixture thereto from whch the gas separating means separates the preselected gaseous component.

14. The apparatus as set forth in claim 13 wherein the gas separating means includes a gas distribution means for distributing the gaseous mixture between at least two beds of a physical separation medium which separate at least the preselected gaseous component from the mixture, the gas distribution means being connectable with the compressor means.

15. The appartus as set forth in claim 12 wherein the effective volume means includes a bladder which is selectively inflated with the relatively high pressure fluid.

16. The apparatus as set forth in claim 12 wherein the effective volume means includes a piston which is slidably mounted in the separated gas reservoir and which is selectively urged by the relatively high pressure fluid to compress the preselected gaseous component.

17. The apparatus as set forth in claim 12 wherein the effective volume means includes a liquid which is selectively urged into the separated gas reservoir.

18. The apparatus as set forth in claim 12 wherein the effective volume means includes a pressure multiplier for multiplying the pressure of the relatively high pressure fluid such that the preselected gaseous component is compressed to a pressure which is higher than the relatively high pressure.