Gas concentrator with improved water rejection capability
A feed gas drying system is described for a PSA or VPSA oxygen concentrator. A membrane dryer is inserted into the feed gas path to the concentrator absorbent beds, such that the moisture in the feed gas is directed to a part of the dryer exposed to the concentrator exhaust, thus achieving efficient operation of the membrane dryer with no loss of concentrator feed gas.
1. An oxygen concentrator comprising;
at least one of a compressor or vacuum pump section,
at least one of a PSA, VSA, or VPSA section including adsorbent beds for gas separation to produce oxygen rich product gas; and,
a membrane dryer mounted in the concentrator with the dryer's inlet side disposed in the gas feed path between the compressor or vacuum pump and the adsorbent beds and the dryer's sweep side disposed to be swept by nitrogen rich exhaust gas from the gas separation section, wherein the sweep gas is at least 90% of the feed gas; wherein
the oxygen concentrator is portable.
2. The concentrator of claim 1 further comprising a condenser and water trap disposed upstream of the absorbent beds.
3. The concentrator of claim 1 further comprising at least one desiccant layer of adsorbent disposed in the gas feed upstream of the adsorbent beds.
4. The concentrator of claim 2 further comprising at least one desiccant layer of adsorbent disposed in the gas feed upstream of the absorbent beds.
5. The concentrator of claim 1 wherein the dryer is adapted to further function as an exhaust gas acoustic muffler.
6. The concentrator of claim 1 wherein the purge flow from the membrane dryer is connected to a vacuum port of a pump in a VPSA system whereby the pressure drop across the membrane is enhanced due to the presence of a vacuum during bed evacuation and purge.
7. The concentrator of claim 6 further comprising a condenser and water trap disposed upstream of the absorbent beds.
8. The concentrator of claim 6 further comprising at least one desiccant layer of adsorbent disposed upstream of the absorbent beds.
9. The concentrator of claim 7 further comprising at least one desiccant layer of adsorbent disposed upstream of the absorbent beds.
10. The concentrator of claim 1 further comprising structured adsorbent in the adsorbent beds.
11. The concentrator of claim 1 wherein a portion of the sweep gas is routed directly from the membrane dryer feed stream in conjunction with the sweep gas from the gas separation exhaust.
12. The concentrator of claim 1 wherein the amount of sweep gas is controlled to achieve a target dew point level.