US2013233016A1PendingUtilityA1
Structured Packing
Est. expiryMar 6, 2032(~5.6 yrs left)· nominal 20-yr term from priority
B01J 2219/32244B01J 2219/32255B01J 2219/3306F25J 3/04412B01J 19/32F25J 2290/12F25J 3/04939B01J 2219/3313B01D 3/32B01J 2219/32483B01J 2219/32408B01J 2219/32213Y10T29/4935B01J 2219/32275F25J 3/04909F25J 3/04678B01J 2219/3221B01J 2219/32272B01J 2219/32237B01J 2219/3222B01J 2219/32268B01J 2219/32227
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Claims
Abstract
An apparatus for a heat transfer or mass transfer process, comprising a column or divided column having at least one pair of converging walls or wall portions and, within at least a region of the column or divided column bounded by at least one pair of converging walls or wall portions, a structured packing having a corrugation angle of at least about 50°; a method of heat and/or mass transfer applicable to the apparatus; and a method of installation of structured packing into a relevant apparatus.
Claims
exact text as granted — not AI-modified1 . An apparatus for a heat transfer or mass transfer process, comprising a column or divided column having at least one pair of converging walls or wall portions and, within at least a region of the column or divided column bounded by at least one pair of converging walls or wall portions, a structured packing having a corrugation angle of at least about 50°.
2 . The apparatus according to claim 1 , in which the column cross-section or divided column cross-section comprises at least one corner.
3 . The apparatus according to claim 2 , wherein the at least one corner or angle is an internal angle or less than or equal to about 120°.
4 . The apparatus according to claim 1 , in which the corrugation angle of the structured packing is from about 55° to about 65°.
5 . The apparatus according to claim 1 , wherein the corrugation angle of the structured packing is about 60°.
6 . The apparatus according to claim 1 , in which the column or divided column is a column division formed within a column having a circular cross-section by providing at least one dividing wall within the column which divides the cross-section of the column into at least two divisions such that the dividing wall converges with the wall of the column to form at least one corner.
7 . The apparatus according to claim 1 , wherein the column size is greater than about 0.5 m in diameter, where the column is of circular cross-section, or of greater than the equivalent cross-sectional area where the cross-section is of another shape.
8 . The apparatus according to claim 1 , wherein the mass transfer process is a cryogenic separation process in which air is separated into nitrogen-, oxygen- and argon-enriched streams.
9 . A method of heat and/or mass transfer, comprising supplying one or more fluids to a column or column division having at least one pair of converging walls or wall portions and which, within at least a region of the column or column division bounded by at least one pair of converging walls or wall portions, contains a structured packing having a corrugation angle of at least about 50° such that the one or more fluids contact the structured packing in order to effect heat transfer and/or mass transfer.
10 . The method according to claim 9 , wherein the column cross-section or column division cross-section comprises at least one corner.
11 . The method according to claim 9 , wherein the at least one corner or angle is an internal angle of less than or equal to about 120°.
12 . The method according to claim 9 , wherein the corrugation angle of the structured packing is from about 55° to about 65°.
13 . The method according to claim 9 , wherein the corrugation angle of the structured packing is about 60°.
14 . The method according to claim 9 , in which the column or column division is a column division formed within a column having a circular cross-section by providing at least one dividing wall within the column which divides the cross-section of the column into at least two divisions such that the dividing wall converges with the wall of the column to form at least one corner.
15 . The method according to claim 9 , wherein the column size is greater than about 0.5 m in diameter, where the column is of circular cross-section, or of greater than the equivalent cross-sectional area where the cross-section is of another shape.
16 . The method according to claim 9 , wherein the mass transfer process is a cryogenic separation process in which air is separated into nitrogen-, oxygen- and argon-enriched streams.
17 . A method of installation of structured packing into an apparatus for a heat and/or mass transfer process, which apparatus comprises a column or column division having at least one pair of converging walls or wall portions, comprising the steps of:
providing a structured packing having a corrugation angle of at least about 50°, and installing the said structured packing into at least a region of the column or column division bounded by at least one pair of converging walls or wall portions.
18 . The method according to claim 17 , wherein the corrugation angle of the structured packing is from about 55° to about 65°.
19 . The method according to claim 18 , wherein the corrugation angle of the structured packing is 60°.
20 . The method according to claim 17 , wherein the at least one pair of converging walls or wall portions converges towards an internal angle of less than or equal to about 120°.
21 . The method according to claim 17 , in which the column or column division is a column division formed within a column having a circular cross-section by providing at least one dividing wall within the column which divides the cross-section of the column into at least two divisions such that the dividing wall converges with the wall of the column to form at least one corner.
22 . The method according to claim 17 , wherein the column size is greater than about 0.5 m in diameter, where the column is of circular cross-section, or of greater than the equivalent cross-sectional area where the cross-section is of another shape.
23 . The method according to claim 17 , wherein the mass transfer process is a cryogenic separation process in which air is separated into nitrogen-, oxygen- and argon-enriched streams.Cited by (0)
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