Product pump for an oxygen concentrator
View Patent ↗A product pump for pumping separated product gas from an oxygen concentrator which produces oxygen-rich product gas by utilizing a vacuum swing adsorption (VSA) process. The oxygen concentrator comprises a cartridge containing an adsorbent material for separating the product gas from ambient air, a vacuum pump which provides a vacuum source, a valve for selectively connecting the vacuum pump to the cartridge and product pump, and a reservoir. The product pump comprises a pumping chamber having a product gas inlet and a product gas outlet, a piston movable in the chamber, a vacuum inlet in the chamber on an opposite side of the piston from the product gas inlet and outlet for providing a vacuum to cause the piston to draw product gas through the product gas inlet into the chamber, and a spring for providing a spring force to force the product gas out the product gas outlet.
1. A method of providing oxygen-rich gas separated from ambient air to a patient, the method comprising:
performing vacuum swing adsorption cycles in each of a plurality of adsorbent beds containing an adsorbent selective for nitrogen, each cycle including a feed phase, an evacuation phase, and a repressurization phase;
pumping separated oxygen to a reservoir, wherein the pumping comprises:
a) applying a vacuum to move a piston in a first direction to draw product gas into a pumping chamber while compressing a spring connected to the piston;
b) interrupting the vacuum to release the compression on the spring and drive the piston in a second direction to push the product gas from the pumping chamber into the storage reservoir; and
delivering product gas from the reservoir to the patient.
2. The method of claim 1 and further comprising:
controlling cycle rate of the vacuum swing adsorption cycles as a function of the product gas delivered to the patient.
3. The method of claim 1 wherein delivering product gas comprises delivering a pulse of product gas in response to inhalation by the patient.
4. The method of claim 1 and further comprising:
storing product gas produced by the cycles in the reservoir.
5. The method of claim 4 wherein the product gas is stored in the reservoir at a pressure of about 1.0 atm to about 2.0 atm.