초록

The present invention is a pressure adsorber vessel that employs a radial adsorbent bed with a variable perforated flow distributor to provide an effective uniform fluid flow though the adsorbent bed.

대표청구항 ▼

What is claimed: 1. A vessel for use in pressure swing adsorption gas separation comprising a generally cylindrical elongated outer shell having first and second ends closed by end plates, at least one annular shaped bed containing particulate material disposed longitudinally between the outer shel

What is claimed: 1. A vessel for use in pressure swing adsorption gas separation comprising a generally cylindrical elongated outer shell having first and second ends closed by end plates, at least one annular shaped bed containing particulate material disposed longitudinally between the outer shell and the central axis of the shell providing an outer passage between the shell and the outer peripheral surface of the bed with an inner passage between the inner peripheral surface of the bed and an annular elongated wall disposed at the central area of the shell, means adapted for introducing a gas into the vessel to pass through said bed and then removing the gas after passing through the bed, the improvement comprising a perforated annular distributor adjacent to at least one peripheral surface of the bed and said flow distributor having a variable perforation geometry pattern, wherein the perforated distributor is annular shaped and comprises at least two sections with each section having a different perforation size. 2. The vessel of claim 1 wherein outer passage is non-uniform and conical in shape with the apex away from the gas entry section of the vessel. 3. The vessel of claim 1, wherein the perforated distributor has three sections. 4. The vessel of claim 1, wherein the shape of the perforation are selected from the group consisting of circles, squares, triangles, rectangles and combination thereof. 5. The vessel of claim 4 wherein the shape of the perforations are circles, the flow distributor has three longitudinal sections with a first section having an open area of between about 1% and about 10%, a second section having an open area of between about 10% and 25% and a third section having an open area of between about 25% and 50%. 6. The vessel of claim 5 wherein the three sections have the same longitudinal length. 7. The vessel of claim 1 wherein the particulate material of the bed is uniform. 8. The vessel of claim 1 wherein the particulate material varies from fine particles at one longitudinal section to coarse particles at the opposite longitudinal section. 9. The vessel of claim 8 wherein the finer particles are at the bottom section and coarser particles are at the opposite end. 10. The vessel of claim 8 wherein the shape of the perforations are circles, the flow distributor has three longitudinal sections with a first section having an open area of between about 1% and about 10%, a second section having an open area of between about 10% and 25% and a third section having an open area of between about 25% and 50%. 11. The vessel of claim 8 wherein the bed section for each particle size is at least 10% of the bed length. 12. The vessel of claim 8 wherein the three sections have the same longitudinal length. 13. The vessel of claim 1 wherein the peripheral longitudinal top section contains an open area smaller than the open area of the remaining longitudinal length of the flow adsorber. 14. The vessel of claim 13 wherein the shape of the perforations are circles, the flow distributor has three longitudinal sections with a first section having an open area of between about 1% and about 10%, a second section having an open area of between about 10% and 25% and a third section having an open area of between about 25% and 50%. 15. The vessel of claim 14 wherein the three sections have the same longitudinal length. 16. The vessel of claim 1 wherein the bottom volume section of the particulate material of the bed comprises finer particles as compared to particles above said bottom volume section that contains coarse particles. 17. The vessel of claim 16 wherein the shape of the perforations are circles, the flow distributor has three longitudinal sections with a first section having an open area of between about 1% and about 10%, a second section having an open area of between about 10% and 25% and a third section having an open area of between about 25% and 50%. 18. The vessel of claim 1 wherein the flow distributor has an input end and has dividing baffle means at said input end. 19. The vessel of claim 18 wherein the shape of the perforations are circles, the flow distributor has three longitudinal sections with a first section having an open area of between about 1% and about 10%, a second section having an open area of between about 10% and 25% and a third section having an open area of between about 25% and 50%. 20. A vessel for use in pressure swing adsorption gas separation comprising a generally cylindrical elongated outer shell having first and second ends closed by end plates, at least one annular shaped bed containing particulate material disposed longitudinally between the outer shell and the central axis of the shell providing an outer passage between the shell and the outer peripheral surface of the bed with an inner passage between the inner peripheral surface of the bed and an annular elongated wall disposed at the central area of the shell, means adapted for introducing a gas into the vessel to pass through said bed and then removing the gas after passing through the bed, the improvement comprising a perforated annular distributor adjacent to at least one peripheral surface of the bed and said flow distributor having a variable perforation geometry pattern, wherein at least one perforated plate is embedded within the top section of the particulate material. 21. The vessel of claim 20 wherein the perforated plate is in the shape of a T with the horizontal section of the plate being flushed with the top surface of the particulate material. 22. The vessel of claim 21 wherein the shape of the perforations are circles, the flow distributor has three longitudinal sections with a first section having an open area of between about 1% and about 10%, a second section having an open area of between about 10% and 25% and a third section having an open area of between about 25% and 50%.