Oxygen concentration system
View Patent ↗The present system is an adsorption system for separating air into a concentrated gas component, which has an air supply, a compressor 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 for separating air into a concentrated gas component, the system comprising:
a compressor for receiving and compressing air from an air supply, providing a compressed air supply;
a first molecular sieve chamber and a second molecular sieve chamber, each containing molecular sieve material for separating the compressed air supply into a concentrated gas component;
an active purge control device for varying an amount of the concentrated gas component communicated between the first molecular sieve chamber and the second molecular sieve chamber; and
an outlet delivering at least 5 liters per minute (LPM) of the concentrated gas component from the molecular sieve material, wherein the adsorption system has total weight, and wherein the adsorption system has a specific total weight per LPM<9 lbs/LPM.
2. The system of claim 1 , wherein the adsorption system produces a sound level during operation, and wherein the adsorption system has a specific sound level per LPM≦10 dBA/LPM.
3. The system of claim 1 , wherein the adsorption system utilizes power during operation, and wherein the adsorption system has a specific power level per LPM≦80 W/LPM.
4. The system of claim 1 , wherein the adsorption system comprises a pressure swing adsorption system.
5. The system of claim 1 , wherein the molecular sieve material has a Nitrogen adsorption capacity of at least 18 NI/kg and a selectivity N 2 /O 2 of at least 6.
6. An adsorption system for separating air into a concentrated gas component, the system comprising:
a compressor for receiving and compressing air from an air supply, providing a compressed air supply;
a first molecular sieve chamber and a second molecular sieve chamber, each containing molecular sieve material for separating the compressed air supply into a concentrated gas component;
an active purge control device for varying an amount of the concentrated gas component communicated between the first molecular sieve chamber and the second molecular sieve chamber; and
an outlet delivering at least 5 liters per minute (LPM) of the concentrated gas component from the molecular sieve material, wherein the molecular sieve material has total weight, and wherein the adsorption system has a specific total molecular sieve material weight per LPM≦0.7 lbs/LPM.
7. The system of claim 6 , wherein the adsorption system comprises a pressure swing adsorption system.
8. The system of claim 6 , wherein the molecular sieve material has a nitrogen adsorption capacity of at least 18 NI/kg and a selectivity N 2 /O 2 of at least 6.
9. An adsorption system for separating air into a concentrated gas component, the system comprising:
a compressor for receiving and compressing air from an air supply, providing a compressed air supply;
a first molecular sieve chamber and a second molecular sieve chamber, each containing molecular sieve material for separating the compressed air supply into a concentrated gas component;
an active purge control device for varying an amount of the concentrated gas component communicated between the first molecular sieve chamber and the second molecular sieve chamber; and
an outlet delivering at least 5 liters per minute (LPM) of the concentrated gas component from the molecular sieve material, wherein the adsorption system has total volume, and wherein the adsorption system has a specific volume per LPM<0.40 ft 3 /LPM.
10. The system of claim 9 , wherein the adsorption system comprises a pressure swing adsorption system.
11. The system of claim 9 , wherein the molecular sieve material has a nitrogen adsorption capacity of at least 18 NI/kg and a selectivity N 2 /O 2 of at least 6.
12. An adsorption system for separating air into a concentrated gas component, the system comprising:
a compressor for receiving and compressing air from an air supply, providing a compressed air supply;
a first molecular sieve chamber and a second molecular sieve chamber, each containing molecular sieve material for separating the compressed air supply into a concentrated gas component;
an active purge control device for varying an amount of the concentrated gas component communicated between the first molecular sieve chamber and the second molecular sieve chamber; and
an outlet delivering at least 5 liters per minute (LPM) of the concentrated gas component from the molecular sieve material, wherein the adsorption system produces a sound level during operation, and wherein the adsorption system has a specific sound level per LPM≦9.5 dBA/LPM.
13. The system of claim 12 , wherein the adsorption system comprises a pressure swing adsorption system.
14. The system of claim 12 , wherein the molecular sieve material has a nitrogen adsorption capacity of at least 18 NI/kg and a selectivity N 2 /O 2 of at least 6.
15. An adsorption system for separating air into a concentrated gas component, the system comprising:
a compressor for receiving and compressing air from an air supply, providing a compressed air supply;
a first molecular sieve chamber and a second molecular sieve chamber, each containing molecular sieve material for separating the compressed air supply into a concentrated gas component;
an active purge control device for varying an amount of the concentrated gas component communicated between the first molecular sieve chamber and the second molecular sieve chamber; and
an outlet delivering at least 5 liters per minute (LPM) of the concentrated gas component from the molecular sieve material, wherein the adsorption system utilizes power during operation, and wherein the adsorption system has a specific power level per LPM≦80 W/LPM.
16. The system of claim 15 , wherein the s adsorption system comprises a pressure swing adsorption system.
17. The system of claim 15 , wherein the molecular sieve material has a nitrogen adsorption capacity of at least 18 NI/kg and a selectivity N 2 /O 2 of at least 6.
18. An adsorption system for separating air into a concentrated gas component, the system comprising:
a compressor for receiving and compressing air from an air supply, providing a compressed air supply;
a first molecular sieve chamber and a second molecular sieve chamber, each containing molecular sieve material for separating the compressed air supply into a concentrated gas component;
an active purge control device for varying an amount of the concentrated gas component communicated between the first molecular sieve chamber and the second molecular sieve chamber; and
an outlet delivering at least 5 liters per minute (LPM) of at least 93% pure concentrated gas component from the molecular sieve material, wherein the adsorption system has total weight, wherein the system has a specific total weight per LPM<8 lbs/LPM, wherein the molecular sieve material has total weight, and wherein the adsorption system has a specific total molecular sieve material weight per LPM≦0.7 lbs/LPM, wherein the adsorption system has total volume, wherein the adsorption system has a specific volume per LPM<0.40 ft 3 /LPM, wherein the adsorption system produces a sound level during operation, wherein the adsorption system has a specific sound level per LPM≦10 dBA/LPM, wherein the adsorption system utilizes power during operation, and wherein the adsorption system has a specific power level per LPM≦80 W/LPM.
19. The system of claim 18 , wherein the adsorption system comprises a pressure swing adsorption system.
20. The system of claim 18 , wherein the molecular sieve material has a nitrogen adsorption capacity of at least 18 NI/kg and a selectivity N 2 /O 2 of at least 6.