US2001032814A1PendingUtilityA1
Shallow bed fluid treatment apparatus
Priority: Jan 27, 2000Filed: Jan 25, 2001Published: Oct 25, 2001
Est. expiryJan 27, 2020(expired)· nominal 20-yr term from priority
B01J 2219/185B01F 35/7182G01N 30/6069G01N 30/02B01J 2219/1943B01J 47/022B01F 25/40B01F 25/41B33Y 80/00B01J 8/0278B01D 15/14G01N 30/6017B01D 15/08B01J 8/025
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Claims
Abstract
A column apparatus containing a shallow bed of material between fluid transporting fractals of large active surface area results in highly efficient processing with small equipment size.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . In a fluid processing system in which a fluid is caused to flow from a distributer, through a bed of processing material, to a collector, the improvement which comprises:
providing said bed as a column having greater diameter than height; and providing said distributor and said collector as structure comprising fractal elements.
2 . An improvement according to claim 1 , wherein the ratio of said diameter to said height is at least 2:1.
3 . An improvement according to claim 1 , wherein said distributor provides a population of fluid exits having a density greater than about 200 per square foot at a fluid/distributor interface.
4 . An improvement according to claim 3 , wherein said density is greater than about 200 per square inch.
5 . An improvement according to claim 1 , said system being configured and arranged to produce process fluid flow through said bed in response to a pressure drop across said bed of less than 5 psi.
6 . An improvement according to claim 1 , in combination with a second fluid processing system in which fluid is caused to flow from a second distributer, through a second resin bed, to a second collector, wherein said second distributor and second collector comprise fractal structure.
7 . A fluid processing system comprising:
a first processing bed with an inlet end, an outlet end, and a diameter at least twice the distance between said inlet end and said outlet end; a first fluid distributor constructed and arranged to introduce fluid at said inlet end of said processing at a density of at least 200 distribution exits per square foot; and a first fluid collector constructed and arranged to collect once processed fluid at said outlet end of said processing bed.
8 . A system according to claim 7 , wherein said collector is constructed and arranged to collect fluid through collection inlets at a density of at least 200 per square foot.
9 . A system according to claim 8 , wherein said distributor and said collector are fractals.
10 . A system according to claim 8 , wherein the ratio of diameter to height of said processing bed is at least 10:1.
11 . A system according to claim 7 , wherein said system is constructed and arranged to produce processing flow conditions with a pressure drop across said bed of less than 5 psi.
12 . A system according to claim 7 , further comprising:
a second processing bed with an inlet side, an outlet side, and a diameter at least twice the distance between said inlet side and said outlet side; a second fluid distributor constructed and arranged to introduce said once processed fluid at said inlet side of said second bed, said second distributor having a density of at least 200 distribution exits per square foot; and a second fluid collector constructed and arranged to collect twice processed fluid at said outlet side of said second processing bed.
13 . A system according to claim 12 , wherein said first and second fluid distributors comprise fractal structure.
14 . A system according to claim 13 , wherein said first and second fluid collectors comprise fractal structure.
15 . A system according to claim 14 , wherein said recursive fractal elements may be characterized as having an “H” shape.Join the waitlist — get patent alerts
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