US2871003A - Fractionator bubble cap - Google Patents
Fractionator bubble cap Download PDFInfo
- Publication number
- US2871003A US2871003A US537129A US53712955A US2871003A US 2871003 A US2871003 A US 2871003A US 537129 A US537129 A US 537129A US 53712955 A US53712955 A US 53712955A US 2871003 A US2871003 A US 2871003A
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- chimney
- deck
- apertures
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- bubble cap
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- 239000007788 liquid Substances 0.000 description 21
- 239000000463 material Substances 0.000 description 7
- 239000012530 fluid Substances 0.000 description 3
- 238000005194 fractionation Methods 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 229910000975 Carbon steel Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000010962 carbon steel Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003209 petroleum derivative Substances 0.000 description 1
- 238000004525 petroleum distillation Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/16—Fractionating columns in which vapour bubbles through liquid
- B01D3/18—Fractionating columns in which vapour bubbles through liquid with horizontal bubble plates
- B01D3/20—Bubble caps; Risers for vapour; Discharge pipes for liquid
Definitions
- An object of the invention is a fractionating apparatus which will have high eificiency over a wide range of operating variables.
- a particular object is a variable opening bubble cap for use in fractionating apparatus.
- Figure 2 shows a plane view of the bubble cap means
- Figure 3 shows another embodiment of the bubble cap means of this invention.
- Figure 4 shows a plane view of the bubble cap means of Figure 3.
- Figure 5 sets out, in schematic form, a fractionating apparatus utilizing the bubble cap means of the invention.
- Conduit 12 permits the entry of material into the shell, for example, a mixture of hydrocarbons to be separated into an overhead fraction and a bottoms fraction.
- the lighter liquid may be introduced through conduit 12 and the heavier liquid may be introduced through a conduit 13 near the top of shell 11.
- Material may leave the interior of shell 11 by way of conduits 16 and 17.
- the shell there is disposed a plurality of horizontal bubble cap decks or trays 18, 19 and 21 respective? ly. It is to be understood that more than three decks may be used, or, insome cases, only one deck may be present.
- the decks are in vertical spaced relationship usually spaced uniformly throughout the height of the shell 11. However, for a particular operation there may be some variation in the spacing of the decks. To maintain the liquid on the deck, the decks are disposed as close to horizontal as is possible under commercial equipment conditions.
- Each deck is provided with a weir 22, 23 and 24 respectively. This weir maintains a depth of liquid on the deck at a predetermined level. Also, each deck is provided with a downcomer means 26, 27, and 28 respectively which carries the overflow of liquid from one deck down to the next lower deck. The lower end of the downcomer is below the level of liquid on the lower deck in order to prevent by-passing of thevapor or liquid up the downcomer.
- Each deck is provided with a number of apertures 31, 32 and 33 shown on deck 18. These apertures 31, etc. permit communication between the upper side of the deck and the space below the deck. Vapor or liquid coming up the shell from deck .19, for example, pass through apertures 31, etc. into bubble cap means 36, 37 and 38 respectively, mounted on deck 18. The bubble cap means 36, etc. are positioned coaxially over the apertures 31, etc.
- the feed would enter the fractionating apparatus through conduit 12, would be vaporized. by heating coils not shown set in the bottom of shell 11. Liquid would be maintained on decks 18, 19 and 21 by the addition of reflux not shown at the upper end of 'shell 11 and also by condensation due to temperature drop over the height of the shell. Vapors passup the apertures, pass through the bubble forming means in bubblecap means through the pool of liquid maintained on the deck by the weirs. Excess liquid is passed down from one deck to the other over the weir and through downcomers. 1
- the bubble cap means comprises a chimney 41 which is fastened to deck 18 by means of rivets 42, etc. Other methods of fastening the chimney to the deck will be obvious.
- Chimney 41 extends vertically above the deck to a height about equal to the height of weir 22. In some modifications, chimney 41 may extend below deck 18 for a dis tance. It is preferred not to operate in this fashion in order to avoid formation of dead spaces beneath the decks.
- Chimney 41 is provided with slots 43, 44, 46 and 47. These slots extend from the top of chimney 41 to a point close to the bottom of the chimney or may even ex tend all the way to deck 18. The end of the slot or the deck provides a means for preventing fall of disc-like member 49 through aperture 31. Other methods of retaining disc-like member 49 in chimney 41 may readily be devised.
- a disc-like member 49 is positioned transversely within the interior of chimney 41.
- Disc member 49 is capable of up and down movement in slots 44, etc. Lugs or extensions 51, 52 and 53, and a fourth extension, not
- Cross members 56 and 57 may be tack welded to the top of chimney 41 or may be fastened therein by other readily apparent means.
- n1ember. 49 is soproportioned within the chimney 4 1 thatit essentially; prevents how of fluid in the chimney beyondwor: above the. disc-member. It-may be described in anotherway. as-being made to a slidingfit within chimney 41.
- Chimney 41 is provided with aplurality of rows of apertures, which apertures are. substantially. circular in cross-section.
- Each row of apertures consists ot'a number of' apertures having thesam'ediameter, i. e., equi-size, which aresetin a. uniformspacing, i. e., equi-distant around the periphery of chimney 4i.
- Theiaperturesin each rowofaholes areat anessentiallyconstantelevation abovethedeck 18, for example,.apertures 61, etc. in the lowest: rowof apertures in chimney 41 all have the same diameterand are setapart uniformly in equal distancein aplane-whiclris parallel to the plane of'deck 18.
- aperture 61 is the smallest in diameter, aperture 62, etc. in the next higher row is larger than aperture 6i; aperture 63in the row next above that containingaperture 62 is larger. than aperture 62.
- Aperture 64-inthe highest row isthe largest, of'all. It 'is' to -be understood that the change .insize of apertures in adjacent rows is not necessarily uniform. It'may'be desirable, in some cases, to have two or even three rows of apertures of the same diameter. Or itmay bedesirablmin some cases, tohave two orthree rows of progressively changing diameter and then several rows.
- Figures 3 and 4 show a simpler form of the bubble cap'm'eans of the invention.
- the bubble'cap meanst may be formed? from economical thin sheets of material such as may be used in heavy duty cans.
- the disc member is retained within the chimney by means of posts passing through a simple cross member which clamps to the top of. the chimney.
- the apertures may readily be punched o'ut of the' thin can-like material.
- chimney 71 is formed of a sheet material such as maybe described as a' can-type sheet and chimney 71 may be described as can-like.
- Chimney 71 isv fastened to deck 72 byv spot welding preferably. Chimney '71 is provided with.
- Each row of. apertures has a different diameter progressively increasing from aperture 73 to aperture 77.
- Disc member 79 which has essentially the same area as the chimney transverse area in order to avoid by-passing of fluid along the walls of chimney 71, has joined to it four post-like members 81, 82, 83 and 84. These post-like members may be hollow tubes or may be solid pins which are driven intov holes in. disc member 79.
- Each post 81,. etc, is provided. at its upper end with a cap 86, 87, and 88 respectively.
- Cross-bar members 91 and 92 are provided at the top of chimney 71. These members may be made in a fashion similar to the top of a coffee can with the sectors punched out to form cross bars 91 and 92, the lip'of the can then fitting over the outer edge of chimney- 71.
- the chimney extends above the deck to a point substantially equal to the height of the weir, in order to provide some depth of liquid between the top of the highest row of apertures and the top of the pool of liquid.
- the largest apertures are provided with small extensions or spurs 98 and 99, for example, which break the bubble passing through the apertureinto two. or more smaller bubbles. These spurs may readily. beformed, in. the case of the embodiment shown in Figure 3, in thestamping operation;
- Example A bubble cap of the type of'this invention was designed for petroleum distillation. tower. In this tower; 280 pounds per hour of hydrocarbonv vapor passes through each bubble cap. The maximum allowable vapor velocity of' the tower" was three feet per second. The average density: of' the hydrocarbon vapor in the tower was 0l 3 pound per standard cubic foot and the pressure drop across each deck was taken at 0.1 p. s. i.
- each aperture in each deck was 4.03 inches in order to provide a clear chimney diameter of 4 inches.
- Each chimney was 4 inches in overall height corresponding to-the height of the weir on eachd'eck.
- Cross-bar means were provided at the top of each. chimney so that the bottom side of the disc positioned transversely in each chimney was 3.5 inches above. the. deck whenthedisc. wasat maximum height within the chimney.
- the chimney wasmade. of ordinary carbon steel at a thickness of 0.35 inch.
- The. lowermost row was at an. elevation of one-fourth inch, deck to midwpointaeach hole was one-sixteenth inch in diam: eter. and the holes were uniformly spaced around the chimney on one-quarter inch centers.
- the next upper row. was set at a one-fourth inch center-to-center. distance above the first. row; each aperture was one-eighth inch in. diameter. and the apertures were set on one-fourth inch centers around the chimney.
- the next upper row- (third from the bottom) was set at one-fourth inch center-to.- center. above. the second row; each aperture Was threesixteenthsin. diameter and set on one-quarter inch centers around the chimney.
- The. fourthv row of holes was set one-half inch centerto-center. above. the third. row; each aperture was. onefourth inch in diameter and the apertures were set on-onehalf inch. centers aroundthe periphery.
- the fifththrough eighth (last) row of apertures seton one-half inch. spacing. vertically, centerrto-center, above thenext lower hole.
- the fifth row of holes had the same diameter andthe same spacingras. thefourth row.
- the sixth, seventh, .and eighth rows had: the same diameters of aperturesand the. same spacing, namely three-eighths diameters set on one-half inchcenters.
- A. contacting. apparatus comprising an outer shell provided, with: ingress. and. egress conduits for material to enter and: leave the interior of said". shell, a plurality. of, horizontal decksv in vertical. spaced relationship in, said shell, each of' said decks being provided with weir.
- said bubble cap means comprise a chimney extending essentially vertically to a height above the desk about equal to said weir height, a disc-like member positioned transversely within said chimney and capable of up and down movement over substantially all the height of said chimney above said deck, said disc member preventing essentially any flow of fluid in the chimney beyond the disc member, means for maintaining said disc member essentially horizontal in said chimney, means for stopping the downward movement of said disc member, means for stopping the upward movement of said disc member, and said chimney being provided with a plurality of rows of substantially circular apertures, each row consisting of a plurality of equi-size apertures in substantial equi -distant spacing at a constant elevation above the deck, and the apertures in said rows progressively increasing in size, the smallest apertures being
- a contacting apparatus comprising an outer shell provided with ingress and egress conduits for material to enter and leave the interior of said shell, a plurality of horizontal decks in vertical spaced relationship in said shell, each of said decks being provided with weir means for maintaining a depth of liquid thereon, with downcomer means for transferring liquid from a deck to the next lower deck, with apertures communicating with the spacebelow the deck, and bubble cap means positioned coaxially over said apertures, wherein the bubble cap means comprises can-like chimney extending from the deck to an elevation substantially equal to said weir height, a disc member positioned transversely within said chimney having essentially the same area as the chimney transverse area and capable of up and down movement in said chimney, cross-bar members positioned across the upper end of said chimney to prevent further upward movement of said disc-member, a plurality of post-like members joined to the upper side of said disc-member and extending through apertures provided in said crossmembers, said post-like members having means which contact said cross-members to prevent movement of said disc
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Description
27, 1959 R. B. GALBREATH 2,871,003
FRACTIONATOR BUBBLE CAP Filed Sept. 28. 1955 2 Sheets-Sheet 1 Richmond 8. Galbreal/r INVEN TOR.
ATTORNEY of Figure 1.
United States Patent 2,371,003 FRACTIONATOR BUBBLE CAP Richmond B. Galbreath, New Orleans, La., assignor, by mesne assignments, to The American Oil Company, a corporation of Maryland Application September 28, 1955, Serial No. 537,129
3 Claims. (31. 261-114) the well known bubble cap trays or decks, the vapors pass up through a chimney-like riser through slots in the bell of the cap and thence through the pool of liquid maintained on the deck. Such bubble cap fractionators are designed for one set of conditions; change in operations away from the design conditions results in a rapid decrease in fractionation efficiency of the apparatus because of the fixed slot area of the bubble cap bells. At-
tempts have been made to overcome this by the use of chimney-like members provided with discs set transverse to the chimney height, which discs ride up and down in the chimney, permitting more or less of the slots in the chimneywall to be exposed to vapor. While this is an improvement, where fluctuations in operations occur, over the regular bubble cap, efficiency of this type of chimney cap changes because of the larger and larger bubbles produced as the disc moves farther and farther up the chimney.
An object of the invention is a fractionating apparatus which will have high eificiency over a wide range of operating variables. A particular object is a variable opening bubble cap for use in fractionating apparatus. A
further object is a contacting apparatus provided with bubble caps permitting high efiiciency when used for liquid-liquid contacting as well as vapor-liquid contact ing. Other objects will become apparentin the course of the detailed description.
The invention is described in connection with the illustrative embodiments set out in the annexed figures which form apart of this specification- Figure 1 sets out a cross-section of a bubble cap means.
Figure 2 shows a plane view of the bubble cap means Figure 3 shows another embodiment of the bubble cap means of this invention.
Figure 4 shows a plane view of the bubble cap means of Figure 3.
Figure 5 sets out, in schematic form, a fractionating apparatus utilizing the bubble cap means of the invention.
In FigureS, the outer shell of the contacting apparatus is represented by numeral 11. Conduit 12 permits the entry of material into the shell, for example, a mixture of hydrocarbons to be separated into an overhead fraction and a bottoms fraction. Or, in a liquid-liquid contacting, the lighter liquid may be introduced through conduit 12 and the heavier liquid may be introduced through a conduit 13 near the top of shell 11. Material may leave the interior of shell 11 by way of conduits 16 and 17.
"ice
Within the shell there is disposed a plurality of horizontal bubble cap decks or trays 18, 19 and 21 respective? ly. It is to be understood that more than three decks may be used, or, insome cases, only one deck may be present. The decks are in vertical spaced relationship usually spaced uniformly throughout the height of the shell 11. However, for a particular operation there may be some variation in the spacing of the decks. To maintain the liquid on the deck, the decks are disposed as close to horizontal as is possible under commercial equipment conditions.
Each deck is provided with a weir 22, 23 and 24 respectively. This weir maintains a depth of liquid on the deck at a predetermined level. Also, each deck is provided with a downcomer means 26, 27, and 28 respectively which carries the overflow of liquid from one deck down to the next lower deck. The lower end of the downcomer is below the level of liquid on the lower deck in order to prevent by-passing of thevapor or liquid up the downcomer.
Each deck is provided with a number of apertures 31, 32 and 33 shown on deck 18. These apertures 31, etc. permit communication between the upper side of the deck and the space below the deck. Vapor or liquid coming up the shell from deck .19, for example, pass through apertures 31, etc. into bubble cap means 36, 37 and 38 respectively, mounted on deck 18. The bubble cap means 36, etc. are positioned coaxially over the apertures 31, etc.
Thus, in the fractionation of a petroleum hydrocarbon mixture, the feed would enter the fractionating apparatus through conduit 12, would be vaporized. by heating coils not shown set in the bottom of shell 11. Liquid would be maintained on decks 18, 19 and 21 by the addition of reflux not shown at the upper end of 'shell 11 and also by condensation due to temperature drop over the height of the shell. Vapors passup the apertures, pass through the bubble forming means in bubblecap means through the pool of liquid maintained on the deck by the weirs. Excess liquid is passed down from one deck to the other over the weir and through downcomers. 1
In Figure 1, there is set out one particular form of the improved bubble cap means of the invention. The bubble cap means comprises a chimney 41 which is fastened to deck 18 by means of rivets 42, etc. Other methods of fastening the chimney to the deck will be obvious. Chimney 41 extends vertically above the deck to a height about equal to the height of weir 22. In some modifications, chimney 41 may extend below deck 18 for a dis tance. It is preferred not to operate in this fashion in order to avoid formation of dead spaces beneath the decks. Chimney 41 is provided with slots 43, 44, 46 and 47. These slots extend from the top of chimney 41 to a point close to the bottom of the chimney or may even ex tend all the way to deck 18. The end of the slot or the deck provides a means for preventing fall of disc-like member 49 through aperture 31. Other methods of retaining disc-like member 49 in chimney 41 may readily be devised.
A disc-like member 49 is positioned transversely within the interior of chimney 41. Disc member 49 is capable of up and down movement in slots 44, etc. Lugs or extensions 51, 52 and 53, and a fourth extension, not
end of chimney 41 to prevent disc member 49 rising out as r noosof chimney 41. Cross members 56 and 57 may be tack welded to the top of chimney 41 or may be fastened therein by other readily apparent means.
)isc. n1ember. 49 is soproportioned within the chimney 4 1 thatit essentially; prevents how of fluid in the chimney beyondwor: above the. disc-member. It-may be described in anotherway. as-being made to a slidingfit within chimney 41.
'The diametenorsize of the apertures in the rowsof holesincreases more or lessprogressively as the row is farther from-the deck. Thus, in Figure 1, aperture 61 is the smallest in diameter, aperture 62, etc. in the next higher row is larger than aperture 6i; aperture 63in the row next above that containingaperture 62 is larger. than aperture 62. Aperture 64-inthe highest row isthe largest, of'all. It 'is' to -be understood that the change .insize of apertures in adjacent rows is not necessarily uniform. It'may'be desirable, in some cases, to have two or even three rows of apertures of the same diameter. Or itmay bedesirablmin some cases, tohave two orthree rows of progressively changing diameter and then several rows.
havingthe same diameter apertures. in general, the size of: the apertures in each rowof' apertures progressively increases with the smallest apertures being nearest the deck; each row has apertures at least as large as the next lower row. It is preferred to have a chimney wherein each higher row has: a somewhat larger aperture size than the next lower row.
Figures 3 and 4: show a simpler form of the bubble cap'm'eans of the invention. In this embodiment, the bubble'cap meanstmay be formed? from economical thin sheets of material such as may be used in heavy duty cans. Instead of using machined slots, the disc member is retained within the chimney by means of posts passing through a simple cross member which clamps to the top of. the chimney. The apertures may readily be punched o'ut of the' thin can-like material. Thus chimney 71 is formed of a sheet material such as maybe described as a' can-type sheet and chimney 71 may be described as can-like. Chimney 71 isv fastened to deck 72 byv spot welding preferably. Chimney '71 is provided with. four rows'of: apertures73', 74, 76 and 77. Each row of. apertures has a different diameter progressively increasing from aperture 73 to aperture 77. Disc member 79, which has essentially the same area as the chimney transverse area in order to avoid by-passing of fluid along the walls of chimney 71, has joined to it four post-like members 81, 82, 83 and 84. These post-like members may be hollow tubes or may be solid pins which are driven intov holes in. disc member 79. Each post 81,. etc, is provided. at its upper end with a cap 86, 87, and 88 respectively. Cross-bar members 91 and 92 are provided at the top of chimney 71. These members may be made in a fashion similar to the top of a coffee can with the sectors punched out to form cross bars 91 and 92, the lip'of the can then fitting over the outer edge of chimney- 71. Posts 81', etc.
extend through holes- 94', etc. provided in cross bars' 91 41 somewhat less than that of the depth of pool of liqpid maintained on the deck by the weir, for example, 22. The chimney extends above the deck to a point substantially equal to the height of the weir, in order to provide some depth of liquid between the top of the highest row of apertures and the top of the pool of liquid. Thus there is nopractical advantage to having the chimney; more than substantially equal to the height of the weir. I
Sinceitistdesirabl'e to have the bubbles issuingfrom the apertures as smallas possible becausethe fractionation eificiency is, in large part, determinedby the vapor'bubbleliquid interph'ase, it-is desirable at times to provide means for reducing the size of the bubbles issuing from the large apertures. Thus in Figure 1, the largest apertures are provided with small extensions or spurs 98 and 99, for example, which break the bubble passing through the apertureinto two. or more smaller bubbles. These spurs may readily. beformed, in. the case of the embodiment shown in Figure 3, in thestamping operation;
Example A bubble cap of the type of'this invention was designed for petroleum distillation. tower. In this tower; 280 pounds per hour of hydrocarbonv vapor passes through each bubble cap. The maximum allowable vapor velocity of' the tower" was three feet per second. The average density: of' the hydrocarbon vapor in the tower was 0l 3 pound per standard cubic foot and the pressure drop across each deck was taken at 0.1 p. s. i.
The diameter of' each aperture in each deck was 4.03 inches in order to provide a clear chimney diameter of 4 inches. Each chimney was 4 inches in overall height corresponding to-the height of the weir on eachd'eck. Cross-bar means were provided at the top of each. chimney so that the bottom side of the disc positioned transversely in each chimney was 3.5 inches above. the. deck whenthedisc. wasat maximum height within the chimney. In order to permit operationunder these conditions, the chimney wasmade. of ordinary carbon steel at a thickness of 0.35 inch.
Eight rows of apertures were provided. The. lowermost row was at an. elevation of one-fourth inch, deck to midwpointaeach hole was one-sixteenth inch in diam: eter. and the holes were uniformly spaced around the chimney on one-quarter inch centers. The next upper row. was set at a one-fourth inch center-to-center. distance above the first. row; each aperture was one-eighth inch in. diameter. and the apertures were set on one-fourth inch centers around the chimney. The next upper row- (third from the bottom) was set at one-fourth inch center-to.- center. above. the second row; each aperture Was threesixteenthsin. diameter and set on one-quarter inch centers around the chimney.
The. fourthv row of holes. was set one-half inch centerto-center. above. the third. row; each aperture was. onefourth inch in diameter and the apertures were set on-onehalf inch. centers aroundthe periphery. The fifththrough eighth (last) row of apertures seton one-half inch. spacing. vertically, centerrto-center, above thenext lower hole. The fifth row of holes had the same diameter andthe same spacingras. thefourth row. The sixth, seventh, .and eighth rowshad: the same diameters of aperturesand the. same spacing, namely three-eighths diameters set on one-half inchcenters.
Thus having; described the invention, what is claimedis;
l. A. contacting. apparatus comprising an outer shell provided, with: ingress. and. egress conduits for material to enter and: leave the interior of said". shell, a plurality. of, horizontal decksv in vertical. spaced relationship in, said shell, each of' said decks being provided with weir. means for maintaining a depth of liquid thereon, .with downcomer means for transferring liquid from a deck to the next' l'ower deck, with apertures communicating withthe space below the deck, and bubble cap means positioned coaxially over said apertures, wherein said bubble cap means comprise a chimney extending essentially vertically to a height above the desk about equal to said weir height, a disc-like member positioned transversely within said chimney and capable of up and down movement over substantially all the height of said chimney above said deck, said disc member preventing essentially any flow of fluid in the chimney beyond the disc member, means for maintaining said disc member essentially horizontal in said chimney, means for stopping the downward movement of said disc member, means for stopping the upward movement of said disc member, and said chimney being provided with a plurality of rows of substantially circular apertures, each row consisting of a plurality of equi-size apertures in substantial equi -distant spacing at a constant elevation above the deck, and the apertures in said rows progressively increasing in size, the smallest apertures being nearest the deck and each row having apertures at least as large as the next lower row.
2. The apparatus of claim 1 wherein the chimney wall is provided with bar members at the top of said chimney to stop upward movement of said disc-means and a plurality of vertical slots ending at about the deck elevation of said chimney and said disc member is provided with extensions adapted to ride in said slots.
3. A contacting apparatus comprising an outer shell provided with ingress and egress conduits for material to enter and leave the interior of said shell, a plurality of horizontal decks in vertical spaced relationship in said shell, each of said decks being provided with weir means for maintaining a depth of liquid thereon, with downcomer means for transferring liquid from a deck to the next lower deck, with apertures communicating with the spacebelow the deck, and bubble cap means positioned coaxially over said apertures, wherein the bubble cap means comprises can-like chimney extending from the deck to an elevation substantially equal to said weir height, a disc member positioned transversely within said chimney having essentially the same area as the chimney transverse area and capable of up and down movement in said chimney, cross-bar members positioned across the upper end of said chimney to prevent further upward movement of said disc-member, a plurality of post-like members joined to the upper side of said disc-member and extending through apertures provided in said crossmembers, said post-like members having means which contact said cross-members to prevent movement of said disc-member beyond the lower end of said chimney, said chimney being provided with a plurality of rows of circular apertures, each horizontal row consisting of equi-size apertures in equi-distant spacing around the chimney, the apertures in said rows increasing in size with the smallest apertures being in the row nearest the deck and each row having apertures at least as large as the next lower row.
References Cited in the file of this patent UNITED STATES PATENTS 1,780,563 Messer Nov. 4, 1930 1,824,836 Piggot Sept. 29, 1931 2,271,764 Heil Feb. 3, 1942 2,428,889 Nutter Oct. 14, 1947 2,466,162 Dupuy Apr. 5, 1949 FOREIGN PATENTS 92,960 Austria June 11, 1923
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US537129A US2871003A (en) | 1955-09-28 | 1955-09-28 | Fractionator bubble cap |
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US537129A US2871003A (en) | 1955-09-28 | 1955-09-28 | Fractionator bubble cap |
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US2871003A true US2871003A (en) | 1959-01-27 |
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US537129A Expired - Lifetime US2871003A (en) | 1955-09-28 | 1955-09-28 | Fractionator bubble cap |
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Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2982527A (en) * | 1956-12-31 | 1961-05-02 | Gulf Oil Corp | Gas-liquid contact apparatus |
US3385577A (en) * | 1964-12-29 | 1968-05-28 | Acme Process Equipment Co | Bubble cap with controlled cover disc |
US3394927A (en) * | 1963-06-10 | 1968-07-30 | Houilleres Bassin Du Nord | Tray for gas-liquid contact columns |
US3434700A (en) * | 1967-04-24 | 1969-03-25 | American Air Filter Co | Gas-liquid contact apparatus for gas cleaners |
US3633882A (en) * | 1968-10-08 | 1972-01-11 | Mitsui Shipbuilding Eng | Vapor-liquid contacting apparatus |
EP0129198A1 (en) * | 1983-06-17 | 1984-12-27 | Air Products And Chemicals, Inc. | Perforated bubble caps for enhanced vapor/liquid contact on a distillation tray |
US20090200690A1 (en) * | 2006-06-13 | 2009-08-13 | Bogdan Vladimirovich Maleta | Mass Transfer Device |
US20100219060A1 (en) * | 2006-06-13 | 2010-09-02 | Bogdan Maleta | Mass-exchange contact device |
CN105228713A (en) * | 2013-03-11 | 2016-01-06 | 巴斯夫欧洲公司 | The method of mass transport process is carried out in tower |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT92960B (en) * | 1922-02-14 | 1923-06-11 | Josef Ondracek | Automatic closing device for the capsule bottoms of rectification columns. |
US1780563A (en) * | 1924-11-15 | 1930-11-04 | Messer Adolf | Apparatus for separating liquids into constituents possessing a low boiling point and constituents possessing a high boiling point by distillation and rectification |
US1824836A (en) * | 1927-05-25 | 1931-09-29 | Piggot Charles Snowden | Bonnet for rectifying columns |
US2271764A (en) * | 1940-08-01 | 1942-02-03 | Carl E Heil | Jet |
US2428889A (en) * | 1945-08-20 | 1947-10-14 | Nutter Irvin Earl | Bubble cap |
US2466162A (en) * | 1946-07-03 | 1949-04-05 | Cedar Corp N O | Display and demonstration apparatus |
-
1955
- 1955-09-28 US US537129A patent/US2871003A/en not_active Expired - Lifetime
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT92960B (en) * | 1922-02-14 | 1923-06-11 | Josef Ondracek | Automatic closing device for the capsule bottoms of rectification columns. |
US1780563A (en) * | 1924-11-15 | 1930-11-04 | Messer Adolf | Apparatus for separating liquids into constituents possessing a low boiling point and constituents possessing a high boiling point by distillation and rectification |
US1824836A (en) * | 1927-05-25 | 1931-09-29 | Piggot Charles Snowden | Bonnet for rectifying columns |
US2271764A (en) * | 1940-08-01 | 1942-02-03 | Carl E Heil | Jet |
US2428889A (en) * | 1945-08-20 | 1947-10-14 | Nutter Irvin Earl | Bubble cap |
US2466162A (en) * | 1946-07-03 | 1949-04-05 | Cedar Corp N O | Display and demonstration apparatus |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2982527A (en) * | 1956-12-31 | 1961-05-02 | Gulf Oil Corp | Gas-liquid contact apparatus |
US3394927A (en) * | 1963-06-10 | 1968-07-30 | Houilleres Bassin Du Nord | Tray for gas-liquid contact columns |
US3385577A (en) * | 1964-12-29 | 1968-05-28 | Acme Process Equipment Co | Bubble cap with controlled cover disc |
US3434700A (en) * | 1967-04-24 | 1969-03-25 | American Air Filter Co | Gas-liquid contact apparatus for gas cleaners |
US3633882A (en) * | 1968-10-08 | 1972-01-11 | Mitsui Shipbuilding Eng | Vapor-liquid contacting apparatus |
EP0129198A1 (en) * | 1983-06-17 | 1984-12-27 | Air Products And Chemicals, Inc. | Perforated bubble caps for enhanced vapor/liquid contact on a distillation tray |
US4510023A (en) * | 1983-06-17 | 1985-04-09 | Air Products And Chemicals, Inc. | Perforated bubble caps for enhanced vapor/liquid contact on a distillation tray |
US20090200690A1 (en) * | 2006-06-13 | 2009-08-13 | Bogdan Vladimirovich Maleta | Mass Transfer Device |
US20100219060A1 (en) * | 2006-06-13 | 2010-09-02 | Bogdan Maleta | Mass-exchange contact device |
US8333940B2 (en) * | 2006-06-13 | 2012-12-18 | Bogdan Maleta | Mass-exchange contact device |
CN105228713A (en) * | 2013-03-11 | 2016-01-06 | 巴斯夫欧洲公司 | The method of mass transport process is carried out in tower |
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