GB828955A - Fractional distillation tower - Google Patents
Fractional distillation towerInfo
- Publication number
- GB828955A GB828955A GB1956657A GB1956657A GB828955A GB 828955 A GB828955 A GB 828955A GB 1956657 A GB1956657 A GB 1956657A GB 1956657 A GB1956657 A GB 1956657A GB 828955 A GB828955 A GB 828955A
- Authority
- GB
- United Kingdom
- Prior art keywords
- perforations
- trays
- tray
- tower
- downcomer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
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
- B01D3/22—Fractionating columns in which vapour bubbles through liquid with horizontal sieve plates or grids; Construction of sieve plates or grids
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
<PICT:0828955/III/1> A fractionating tower contains horizontally-disposed perforated trays which have tabs projecting above their upper surface at an angle so that vapour flowing through the perforations in the trays cause liquid flowing down the tower to flow across the trays to a downcomer. In a preferred embodiment vapours ascending from the bottom of a tower pass first through the perforations 9 of the lowest tray 1 and subsequently through the perforations of trays 2 and 3, respectively. Descending liquid is caused to flow across each tray by the angle at which the ascending vapours pass through the perforations and then descends via a downcomer 4 to the lowermost tray 1 and then via downcomer 5 to a draw-off pan 6 and a conduit 7 to a thermosyphon reboiler (not shown) and returned to the tower via conduit 10. A trough 8 is situated below at a lower level than the perforations 9 of tray 1 and is capable of collecting at least a portion of any liquid dropping through the perforations 9 and conducting the liquid so collected into the draw-off pan 6.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1956657A GB828955A (en) | 1957-06-21 | 1957-06-21 | Fractional distillation tower |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1956657A GB828955A (en) | 1957-06-21 | 1957-06-21 | Fractional distillation tower |
Publications (1)
Publication Number | Publication Date |
---|---|
GB828955A true GB828955A (en) | 1960-02-24 |
Family
ID=10131527
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1956657A Expired GB828955A (en) | 1957-06-21 | 1957-06-21 | Fractional distillation tower |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB828955A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1419608B1 (en) * | 1960-10-11 | 1971-07-22 | Hoechst Ag | Mass transfer column bottom |
-
1957
- 1957-06-21 GB GB1956657A patent/GB828955A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1419608B1 (en) * | 1960-10-11 | 1971-07-22 | Hoechst Ag | Mass transfer column bottom |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3006623A (en) | Fluid distributor for packed columns | |
US4472325A (en) | Liquid distributor apparatus for a vapor-liquid contact column | |
US2795536A (en) | Liquid control for a fractionating column | |
US2116933A (en) | Fractionating column | |
GB1064287A (en) | Distributor plate for packed towers | |
EP0879626A3 (en) | Liquid distributor tray | |
US4490215A (en) | Process for fractionation reboiling | |
US4601788A (en) | Apparatus for fractionation reboiling | |
GB828955A (en) | Fractional distillation tower | |
US2809820A (en) | Low pressure drop liquid-vapor contacting tray | |
US3501400A (en) | Deentrainment distillation of hydrocarbons in stripping column having arrester plate and collar | |
GB823108A (en) | Improvements in or relating to gas/liquid contacting columns | |
GB1220653A (en) | Steam stripping system | |
US3017950A (en) | Bubble-plate structure for rectification columns | |
US4247368A (en) | Apparatus for distillation column side stream withdrawal | |
US2682395A (en) | Divided downcomer for trays of fractionating columns | |
US2725343A (en) | Vapor-liquid contact apparatus | |
GB982525A (en) | Gas and liquid contact device | |
GB1181487A (en) | Apparatus for Vacuum and Short-Path Vacuum Distillation. | |
GB823610A (en) | Improved vapour and liquid contact tower | |
US2703015A (en) | Device for determining entrainment from plate to plate in a bubble plate tower | |
US2983493A (en) | Fractionating column with stepped trays | |
US3297566A (en) | Gas oil reflux controller | |
US2201502A (en) | Fractionating column | |
US2684837A (en) | Apparatus for operating a vapor liquid contacting zone |