Oxygen concentration system
View Patent ↗The present system is an adsorption system ( 100 ) for separating air into a concentrated gas component, which has an air supply, a compressor ( 115 ) for receiving and compressing the air supply, providing a compressed air supply, and molecular sieve material for separating the compressed air supply into a concentrated gas component. The adsorption system delivers at least 5 liters per minute (LPM) of concentrated gas component from the molecular sieve material in which the system has a specific total weight per LPM<9 lbs/LPM. Additionally, an output quantity of the concentrated gas is delivered by the adsorption system and a purging quantity of the concentrated gas is dispensed into a sieve chamber of the adsorption system undergoing a purge cycle. The purging quantity has a value equal to or less than the difference between the maximum quantity and the output quantity, and the purging quantity is controlled based on the output quantity.
1. An adsorption system ( 100 ) for separating air into a concentrated gas component, the system comprising:
a compressor ( 115 ) for receiving and compressing air from an air supply, providing a compressed air supply;
molecular sieve material for separating the compressed air supply into a concentrated gas component; and
an outlet delivering at least 95.7% pure concentrated gas component from the molecular sieve material, wherein the capacity of the compressor is matched to the capacity of the molecular sieve material.
2. The system of claim 1 , wherein the outlet delivers at least 96% pure concentrated gas component from the molecular sieve material.
3. The system of claim 1 , wherein the outlet delivers at least 96.4% pure concentrated gas component from the molecular sieve material.
4. The system of claim 1 , wherein the concentrated gas component is oxygen.
5. The system of claim 1 , wherein the capacity of the compressor being matched to the capacity of the molecular sieve material includes a rate at which the compressor provides the compressed air supply being matched to a rate at which the molecular sieve material processes the compressed air supply while maintaining a predetermined recovery rate of the concentrated gas component.
6. The system of claim 1 , wherein the capacity of the compressor and the capacity of the molecular sieve material are described by a volume per unit time at a given pressure.
7. An adsorption system ( 100 ) for separating air into a concentrated gas component, the system comprising:
a compressor ( 115 ) for receiving and compressing air from an air supply, providing a compressed air supply;
molecular sieve material for separating the compressed air supply into a concentrated gas component;
a first molecular sieve chamber ( 130 ) for receiving the molecular sieve material;
at second molecular sieve chamber ( 135 ) for receiving the molecular sieve material;
a supply chamber for receiving the compressed air supply and for communicating the compressed air supply to the first and the second molecular sieve chambers;
an outlet delivering a concentrated gas component from the molecular sieve material; and
a fixed orifice for communicating the concentrated gas component between the first molecular sieve chamber and the second molecular sieve chamber,
wherein the molecular sieve material has a total molecular sieve material weight, and wherein the total molecular sieve material weight per square inch of the area of the fixed orifice is less than <3,000 lbs/square inch.
8. An adsorption system ( 100 ) for separating air into a concentrated gas component, the system comprising:
a compressor ( 115 ) for receiving and compressing air from an air supply, providing a compressed air supply;
molecular sieve material for separating the compressed air supply into a concentrated gas component;
a first molecular sieve chamber ( 130 ) for receiving the molecular sieve material;
a second molecular sieve chamber ( 135 ) for receiving the molecular sieve material;
a supply chamber for receiving the compressed air supply and for communicating the compressed air supply to the first and the second molecular sieve chambers; and
an outlet delivering a concentrated gas component from the molecular sieve material,
wherein the capacity of the compressor is matched to the capacity of the molecular sieve material.
9. The system of claim 8 , wherein the molecular sieve material is capable of processing a first volume of gas at a first pressure in a first time period and the compressor generates a maximum of the first volume of gas at the first pressure in the first time period.
10. The system of claim 8 , wherein the capacity of the compressor being matched to the capacity of the molecular sieve material includes a rate at which the compressor provides the compressed air supply being matched to a rate at which the molecular sieve material processes the compressed air supply while maintaining a predetermined recovery rate of the concentrated gas component.
11. The system of claim 8 , wherein the capacity of the compressor and the capacity of the molecular sieve material are described by a volume per unit time at a given pressure.