MASS TRANSFER COLUMNS AND METHODS OF CONSTRUCTION
20220395764 ยท 2022-12-15
Assignee
Inventors
- David EWY (Goddard, KS, US)
- Darran HEADLEY (Wichita, KS, US)
- Erik LAYTON (Wichita, KS, US)
- Izak Nieuwoudt (Wichita, KS, US)
- Patrick QUOTSON (Wichita, KS, US)
Cpc classification
Y02C20/40
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
B01D53/18
PERFORMING OPERATIONS; TRANSPORTING
International classification
B01D3/32
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A mass transfer column is provided in which a shell is formed of one or more side walls having an exoskeleton. The exoskeleton includes a plurality of vertical trusses joined together by crossing rails. An inner skin is supported by the vertical trusses and rails and, together with a top and bottom of the shell, defines an open internal region that may be pressurized and in which mass transfer process may occur. Horizontally extending beams that may be in the form of trusses span the open internal reaion and are supported by the exoskeleton. Internals such as structured packing may be supported on the horizontally extending beams.
Claims
1. A mass transfer column comprising: a shell comprising at least one side wall and a top and a bottom joined to the side wall, the side wall comprising: a plurality of upright trusses that are spaced apart from each other and have opposed inner and outer faces; rails extending between and joined to adjacent ones of the upright trusses and having opposed inner and outer faces; and a skin supported by the upright trusses and rails and together with the top and the bottom defining an open internal region that may be pressurized and in which mass transfer processes may occur, the skin having an inner face and an outer face; a plurality of horizontally extending beams spanning the open internal region, each of the horizontally extending beams having opposite end segments; and seats supported by the shell and supporting the opposite end segments of the horizontally extending beams.
2. The mass transfer column of claim 1, including nozzles extending through the skin of the shell for introducing fluid into the open internal region and removing fluid from the open internal region.
3. The mass transfer column of claim 1, wherein the horizontally extending beams are trusses.
4. The mass transfer column of claim 1, wherein the seats are joined to the skin of the shell.
5. The mass transfer column of claim 1, wherein the seats comprise a portion of the rails.
6. The mass transfer column of claim 1, wherein the seats are joined to the inner faces of the upright trusses.
7. The mass transfer column of claim 1, including internals supported on the beams.
8. The mass transfer column of claim 1, wherein the end segments of the beams are joined to the upright trusses.
9. The mass transfer column of claim 1, wherein the beams each comprises two beam segments that are aligned end to end with their adjacent ends supported by a support column positioned within the open internal region.
10. A mass transfer column comprising: a shell comprising at least one side wall and a top and a bottom joined to the side wall, the side wall comprising: a plurality of upright trusses that are spaced apart from each other and have opposed inner and outer faces; rails extending between and joined to adjacent ones of the upright trusses and having opposed inner and outer faces; and a skin supported by the upright trusses and rails and together with the top and the bottom defining an open internal region that may be pressurized and in which mass transfer processes may occur, the skin having an inner face and an outer face; a plurality of horizontally extending trusses spanning the open internal region, each of the horizontally extending trusses having opposite end segments; seats supported by the shell and supporting the opposite end segments of the horizontally extending trusses; and nozzles extending through the skin of the shell for introducing fluid into the open internal region and removing fluid from the open internal region.
11. The mass transfer column of claim 10, wherein the seats are joined to the skin of the shell.
12. The mass transfer column of claim 10, wherein the seats comprise a portion of the rails.
13. The mass transfer column of claim 10, wherein the seats are joined to the inner faces of the upright trusses.
14. The mass transfer column of claim 10, including internals supported on the horizontally extending trusses.
15. The mass transfer column of claim 10, wherein the end segments of the horizontally extending trusses are joined to the upright trusses.
16. The mass transfer column of claim 10, wherein the horizontally extending trusses each comprises two segments that are aligned end to end with their adjacent ends supported by a support column positioned within the open internal region.
17. An absorber for removing carbon dioxide from a flue gas, the absorber comprising: a shell comprising at least one side wall and a top and a bottom joined to the side wall, the side wall comprising: a plurality of upright trusses that are spaced apart from each other and have opposed inner and outer faces; rails extending between and joined to adjacent ones of the upright trusses and having opposed inner and outer faces; and a skin supported by the upright trusses and rails and together with the top and the bottom defining an open internal region that may be pressurized and in which mass transfer processes may occur, the skin having an inner face and an outer face; a plurality of horizontally extending trusses spanning the open internal region, each of the horizontally extending trusses having opposite end segments; seats supported by the shell and supporting the opposite end segments of the horizontally extending trusses; nozzles extending through the skin of the shell for introducing fluid into the open internal region and removing fluid from the open internal region; and internals supported on the horizontally extending trusses.
18. The absorber of claim 17, wherein the internals comprise structured packing.
19. The absorber of claim 17, wherein the shell comprises four of said side walls joined together for form a square or rectangular configuration.
20. The absorber of claim 17, wherein the horizontally extending trusses overlap the upright trusses.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0009] In the accompanying drawings that form part of the specification and in which like reference numerals are used to indicated like components in the various views:
[0010]
[0011]
[0012]
[0013]
[0014]
[0015]
[0016]
[0017]
[0018]
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0019] Turning now to the drawings in greater detail and initially to
[0020] The mass transfer column 10 may be any type of column for processing fluid streams, usually liquid and vapor streams or two or more liquid streams having different densities, to obtain fractionation products, or to otherwise cause mass transfer and/or heat exchange between the fluid phases. Examples of suitable types of mass transfer columns 10 include, but are not limited to, absorber columns, separators, distillation columns, liquid-liquid extraction columns, scrubber columns, and evaporator columns. The mass transfer column 10 may be one in which crude atmospheric fractionating, lube or crude vacuum oil fractionation, catalytic or thermal cracking fractionating, coker or visbreaker fractionating, coker or cracking scrubbing, reactor off-gas scrubbing, gas quenching, edible oil deodorization, pollution control scrubbing, reactive distillation, or other types of processes occur.
[0021] As one specific example, the mass transfer column 10 may be an absorber that is used to remove carbon dioxide from a flue aas generated by a fossil fuel-based power plant. In such an application, the mass transfer column 10 may used as part of a system that may include another mass transfer column that receives the flue gas after it has been subjected to a NOx removal process and cools the ascending flue gas by countercurrent flow with descending water through mass transfer structures such as structured packing. The cooled flue gas is then directed as a side stream to the mass transfer column 10 that acts an absorber. The ascending cooled flue gas flows in the absorber countercurrently with a descending carbon dioxide absorbing solvent.
[0022] The rich solvent is removed as a bottoms and directed to one or more other mass transfer columns that act(s) as a stripper to separate the carbon dioxide from the rich solvent stream and to regenerate the solvent.
[0023] As shown in
[0024] The shell 12 of the mass transfer column 10 defines an open internal region 14 in which the desired mass transfer, heat exchange, and/or reaction between the fluid phases takes place. In one embodiment, the fluid phases within the mass transfer column 10 may include ascending vapor and descending liquid, such as when the mass transfer column 10 is acting as an absorber in a process for separating carbon monoxide from a flue gas. In other embodiments, the fluid phases within the mass transfer column 10 may comprise substantially any combination of ascending or descending liquid and ascending or descending vapor. In some embodiments, the fluid phases within the mass transfer column 10 may include ascending or descending liquids having different densities. The fluid phases within the mass transfer column 10 may move in a co-current manner, such that the vapor and liquid phases, or both liquid phases, move in the same direction along a longitudinal axis of the mass transfer column 10, or the fluid streams within the mass transfer column 10 may move in a counter-current manner, such that the vapor or liquid phase moves in the opposite direction as the other phase within the mass transfer column 10.
[0025] One or more fluid streams may be introduced into the mass transfer column 10 via one or more feed lines, such as through feed line nozzles 16 and 18 shown in
[0026] As also shown in
[0027] The mass transfer column 10 may also include typical components such as one or more heat exchangers for heating and/or cooling the fluid streams introduced into and/or withdrawn from the mass transfer column 10, a condenser for cooling the overhead vapor stream withdrawn from the mass transfer column 10 via the upper takeoff nozzle 20, and a reboiler for heating the bottom liquid stream withdrawn from the mass transfer column 10 via the lower takeoff nozzle 22. These components are not shown because of their conventional nature.
[0028] The shell 12 of the mass transfer column 10 has at least one side wall 24, and a top 26 and a bottom 28 that are joined to the side wall 24. The number of side walls 24 is dependent upon the cross sectional shape desired for the shell 12. For example, when the shell 12 has a circular cross section, a single side wall 24 may be used. When the shell 12 has a square or rectangular cross section, four of the side walls 24 are used. The side walls 24 each comprise an exoskeleton 30 that supports a skin 32. In one embodiment, the exoskeleton 30 comprises a plurality of upright trusses 34 that are spaced apart from each other and rails 36 that join together adjacent ones of the upright trusses 34. The upright trusses 34 and the rails 36 each have opposed inner and outer faces.
[0029] The upright trusses 34 may extend vertically and in parallel relationship to each other. The upright trusses 34 may each be formed by an inner cord 38 and an outer cord 40 that are spaced apart from each other and are interconnected by web members 42. The inner cord 38 and the outer cord 40 in each upright truss 34 may extend in parallel relationship to each other or, as illustrated in
[0030] The skin 32 is supported by the upright trusses 34 and rails 36 and, together with the top and bottom 26 and 28 define the open internal region 14 that may be pressurized and in which the mass transfer processes occur. The skin 32 has opposed inner and outer faces and the side feed line nozzles 16 and 18 extend through the skin 32. The upper take off nozzle 20 and the lower take off nozzle 22 normally extend through the top 26 and bottom 28, respectively, of the shell 12.
[0031] Turning more specifically to
[0032] Turing now to
[0033] In
[0034] In
[0035] In
[0036] In
[0037] It can thus be seen that the use of the exoskeleton 30 in the construction of the side wall(s) 24 provides the shell 12 with a high strength that is capable of withstanding high loads, which is particularly beneficial when the mass transfer column 10 is used in applications where the shell 12 has a width in the range of 40 to 100 feet and a height in the range of 50 to 300 feet. Fabricating the skin 32 and the vertical trusses 34 and rails 36 from metal or metal alloys provides great flexibility for locating and attaching the seats 58 for the horizontally extending beams 44 in the open internal region 14. Fabricating the horizontally extending beams 44 as trusses allows them to span large distances and support the various internals such as structured packing 46 that may be used within the mass transfer column 10.
[0038] From the foregoing, it will be seen that this disclosure is one well adapted to attain all the ends and objectives hereinabove set forth, together with other advantages that are inherent to the disclosure.
[0039] It will be understood that certain features and subcombinations are of utility and may be employed without reference to other features and subcombinations. This is contemplated by and is within the scope of the claims.
[0040] Since many possible embodiments may be made of the disclosure without departing from the scope thereof, it is to be understood that all matter herein set forth or shown in the accompanying drawings is to be interpreted as illustrative and not in a limiting sense.