Oxygen concentrator for high pressure oxygen delivery with oxygen circulation loop and improved portability

Patent metadata

Field	Value
Publication number	US-10137275-B2
Application number	US-201514598637-A
Country	US
Kind code	B2
Filing date	Jan 16, 2015
Priority date	Jan 16, 2014
Publication date	Nov 27, 2018
Grant date	Nov 27, 2018

Abstract

A portable oxygen concentrator is disclosed. An output of a high pressure compressor is fluidly coupled to an adsorbent device that increases the concentration of oxygen gas for storage in a high pressure accumulator. The adsorbent device is purged of the collected nitrogen via a valve fluidly coupled to the outlet of the high pressure compressor and the inlet of the adsorbent device. The outlet of the adsorbent device is fluidly coupled to the high pressure accumulator through a first valve. Additionally, a re-circulation loop fluidly couples the outlet of the adsorbent device to a valved inlet of the high pressure compressor.

First claim

What is claimed is:

1. A portable apparatus for concentrating and delivering high pressure oxygen to a ventilator, the apparatus comprising:
an enclosure defining an air inlet, an oxygen outlet and a flow pathway extending between the air inlet and the oxygen outlet;
a high pressure compressor disposed within the enclosure and integrated into the flow pathway, the high pressure compressor having a compressor inlet fluidly coupled to the air inlet, and a compressor outlet;
an adsorbent sieve bed disposed within the enclosure and integrated into the flow pathway, the sieve bed having a sieve bed inlet fluidly coupled to the compressor outlet of the high pressure compressor, and a sieve bed outlet, with the sieve bed being operative to remove nitrogen from air flowing therethrough;
a high pressure accumulator disposed within the enclosure and integrated into the flow pathway, the high pressure accumulator having an accumulator inlet fluidly coupled to the sieve bed outlet of the adsorbent sieve bed, and an accumulator outlet fluidly coupled to the oxygen outlet;
a first valve disposed within the enclosure and integrated into the flow pathway so as to be interposed between and fluidly coupled to both the sieve bed outlet of the sieve bed and the accumulator inlet of the accumulator, the first valve being operative to prevent flow from the high pressure accumulator to the sieve bed;
a third valve disposed within the enclosure and integrated into the flow pathway so as to be interposed between and fluidly coupled to both the air inlet and the compressor inlet of the high pressure compressor; and
an oxygen circulation loop having a first end fluidly coupled to the flow pathway between the third valve and the compressor inlet of the high pressure compressor, and a second end fluidly coupled to the flow pathway between the sieve bed outlet of the sieve bed and the first valve;
the oxygen circulation loop being operative to permit oxygen enriched gas to be circulated through the sieve bed, with the third valve being operative to prevent flow of the oxygen enriched gas to ambient via the air inlet;
the high pressure compressor, the sieve bed and the high pressure accumulator being sized and configured to allow the apparatus to operate at a pressure level in the range of from about 40-80 psi.

2. The apparatus of claim 1 wherein the high pressure compressor, the sieve bed and the high pressure accumulator are further sized and configured to allow the apparatus to operate in a manner wherein oxygen at a concentration of up to 100% is discharged from the oxygen outlet.

3. The apparatus of claim 1 further comprising an inlet filter disposed within the enclosure and integrated into the flow pathway so as to be interposed between and fluidly coupled to both the air inlet and the compressor inlet such that air drawn into the air inlet by the high pressure compressor is passed through the inlet filter.

4. The apparatus of claim 1 further comprising a second valve disposed within the enclosure and integrated into the flow pathway so as to be interposed between and fluidly coupled to both the accumulator outlet of the accumulator and the air outlet, the second valve being operative to meter the delivery of a concentrated oxygen gas from the high pressure accumulator to the air outlet in accordance with prescribed operational parameters of the apparatus, and to prevent flow of an exhaled breathing gas from the air outlet into the high pressure accumulator.

5. The apparatus of claim 1 further comprising an exhaust valve disposed within the enclosure and integrated into the flow pathway so as to be interposed between and fluidly coupled to both the compressor outlet of the high pressure compressor and the sieve bed inlet of the sieve bed, the exhaust valve further being in fluid communication with ambient air, and operative to exhaust nitrogen enriched gas produced by the sieve bed.

6. The apparatus of claim 1 further comprising:
a DC motor disposed within the enclosure and electrically connected to the high pressure compressor; and
a DC power source disposed within the enclosure and electrically connected to the DC motor.

7. The apparatus of claim 1 wherein the apparatus is configured to have a size and shape profile as allows it to be integrated into a backpack.

8. A portable apparatus for concentrating and delivering high pressure oxygen to a ventilator, the apparatus comprising:
an enclosure defining an air inlet, an air outlet and a flow pathway extending between the air inlet and the oxygen outlet;
a high pressure compressor disposed within the enclosure and integrated into the flow pathway, the high pressure compressor having a compressor inlet fluidly coupled to the air inlet, and a compressor outlet;
an adsorbent sieve bed disposed within the enclosure and integrated into the flow pathway, the sieve bed having a sieve bed inlet fluidly coupled to the compressor outlet of the high pressure compressor, and a sieve bed outlet, with the sieve bed being operative to remove nitrogen from air flowing therethrough;
a high pressure accumulator disposed within the enclosure and integrated into the flow pathway, the high pressure accumulator having an accumulator inlet fluidly coupled to the sieve bed outlet of the adsorbent sieve bed, and an accumulator outlet fluidly coupled to air outlet;
a first valve disposed within the enclosure and integrated into the flow pathway so as to be interposed between and fluidly coupled to both the sieve bed outlet of the sieve bed and the accumulator inlet of the accumulator, the first valve being operative to prevent flow from the high pressure accumulator to the sieve bed;
a second valve disposed within the enclosure and integrated into the flow pathway so as to be interposed between and fluidly coupled to both the accumulator outlet of the accumulator and the air outlet, the second valve being operative to meter the delivery of a concentrated oxygen gas from the high pressure accumulator to the air outlet in accordance with prescribed operational parameters of the apparatus, and to prevent flow from an exhaled breathing gas from the air outlet into the high pressure accumulator;
a third valve disposed within the enclosure and integrated into the flow pathway so as to be interposed between and fluidly coupled to both the air inlet and the compressor inlet of the high pressure compressor; and
an oxygen circulation loop having a first end fluidly coupled to the flow pathway between the third valve and the compressor inlet of the high pressure compressor, and a second end fluidly coupled to the flow pathway between the sieve bed outlet of the sieve bed and the first valve;
the oxygen circulation loop being operative to permit oxygen enriched gas to be circulated through the sieve bed, with the third valve being operative to prevent flow of the oxygen enriched gas to ambient via the air inlet.

9. The apparatus of claim 8 wherein the high pressure compressor, the sieve bed and the high pressure accumulator are sized and configured to allow the apparatus to operate at a pressure level in the range of from about 40-80 psi.

10. The apparatus of claim 9 wherein the high pressure compressor, the sieve bed and the high pressure accumulator are further sized and configured to allow the apparatus to operate at a flow rate of up to at least about 10 lpm.

11. The apparatus of claim 10 wherein the high pressure compressor, the sieve bed and the high pressure accumulator are further sized and configured to allow the apparatus to operate in a manner wherein oxygen at a concentration of up to 100% is discharged from the oxygen outlet.

12. The apparatus of claim 8 f

Assignees

• Breathe Technologies Inc
• Breathetechnologies Inc

Inventors

• Ahmad Samir S

Classifications

• A61M16/101 Primary

  using an oxygen concentrator · CPC title

• A61M2202/0208

  Oxygen · CPC title

• A61M2205/52

  with memories providing a history of measured variating parameters of apparatus or patient · CPC title

• A61M2205/82

  Internal energy supply devices · CPC title

• A61M2205/18

  with alarm · CPC title