US2002095951A1PendingUtilityA1
Method and apparatuses for the production of synthetic air products and related gases
Priority: Jan 19, 2001Filed: Jan 19, 2001Published: Jul 25, 2002
Est. expiryJan 19, 2021(expired)· nominal 20-yr term from priority
Inventors:Bao Ha
F25J 2205/90F25J 2210/42F25J 2215/50F25J 3/0426F25J 3/04636F25J 2215/40F25J 2200/72F25J 2210/50F25J 2210/04F25J 3/04254F25J 3/044
35
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Claims
Abstract
Processes and apparatuses are disclosed for the production of a synthetic air product with a variable oxygen content and a varying level of impurities.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . A process for the production of a synthetic air product comprising the steps of:
supplying a feed gas; enhancing the oxygen content of the feed gas; passing the feed gas to a cryogenic distillation column; rectifying the feed gas in the distillation column to remove impurities; and, extracting a synthetic air product at least a real or theoretical tray above where the feed gas is passed to the column.
2 . The process of claim 1 further comprising compressing the feed gas.
3 . The process of claim 1 wherein the step of enhancing the oxygen content of the feed gas comprises mixing an oxygen stream with the feed gas.
4 . The process of claim 2 wherein the oxygen content of the feed gas is enhanced prior to fully compressing the feed gas.
5 . The process of claim 1 wherein the oxygen content of the feed gas is enhanced prior to fully rectifying the feed gas.
6 . The process of claim 1 wherein the oxygen content of the feed gas is enhanced prior to fully cooling the feed gas.
7 . The process of claim 1 wherein the oxygen content of the feed gas is enhanced at a point in the distillation column.
8 . The process of claim 7 wherein the synthetic air product is extracted at least one real or theoretical tray above the point in the distillation column.
9 . The process of claim 1 wherein the feed gas is cooled to generally about a dew point of the feed gas.
10 . The process of claim 1 the feed gas is air.
11 . The process of claim 1 wherein the step of enhancing the oxygen content further comprises mixing an oxygen supply with the feed gas.
12 . The process of claim 11 wherein the oxygen supply is greater than 90% by volume.
13 . The process of claim 1 wherein the step of rectifying the feed gas further comprises more than one tray.
14 . The process of claim 1 further comprising the step of removing a nitrogen enriched product.
15 . The process of claim 14 wherein the nitrogen enriched product is removed along an upper portion of the column.
16 . The process of claim 1 wherein the synthetic air product extracted has an oxygen content of about 15% by volume to about 40% by volume.
17 . The process of claim 1 wherein the synthetic air product extracted has an oxygen content of about 20% by volume to about 30% by volume.
18 . The process of claim 1 wherein the synthetic air product extracted has an oxygen content of about 21% by volume.
19 . The process of claim 1 wherein the step of supplying the feed gas further comprises mixing an oxygen supply with an other supply prior to rectifying.
20 . The process of claim 19 wherein at least one of the oxygen supply and the other supply is a liquid.
21 . The process of claim 19 wherein the other supply is a nitrogen supply.
22 . A cryogenic process for the production of a synthetic air product including the steps of supplying a feed gas; substantially removing CO2 and moisture from the feed gas; mixing the feed gas with an oxygen content enhancing stream; cooling the feed gas, passing the feed gas into a distillation column; and, removing a synthetic air product.
23 . The process of claim 22 further comprising compressing the feed gas.
24 . The process of claim 22 wherein the step of supplying the feed gas further comprises mixing an oxygen supply and an other supply.
25 . The process of claim 24 wherein at least one of the oxygen supply and the other supply is a liquid.
26 . The process of claim 25 wherein at least one of oxygen supply and the other supply is a gas.
27 . The process of claim 24 wherein the other supply is a nitrogen supply.
28 . An apparatus for producing a synthetic air product comprising:
a column having an upper portion, a lower portion, a top, a bottom, and at least one tray; a feed gas supply line connected to the column; an oxygen content enhancing line connected to the feed gas supply line; and, a product withdraw line connected to a portion of the column for removing a synthetic air product.
29 . The apparatus of claim 29 further comprising a line connected to the lower portion of the column to remove rich liquid.
30 . The apparatus of claim 29 wherein the oxygen content enhancing line is connected to the column.
31 . The apparatus of claim 29 wherein the feed gas supply line further comprises a connection to an oxygen supply and an other supply.
32 . The apparatus of claim 35 wherein at least one of the other supply and the oxygen supply is a liquid.
33 . The apparatus of claim 35 wherein the other supply is a nitrogen supply.
34 . The apparatus of claim 29 wherein the product withdraw line removes a synthetic air product with an oxygen content of about 15% by volume to about 40% by volume.
35 . The apparatus of claim 29 wherein the product withdraw line removes a synthetic air product with an oxygen content of about 20% by volume to about 30% by volume.
36 . The apparatus of claim 29 wherein the product withdraw line removes a synthetic air product with an oxygen content of about 21% by volume.Join the waitlist — get patent alerts
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