GB866421A - Distillation apparatus - Google Patents
Distillation apparatusInfo
- Publication number
- GB866421A GB866421A GB2894/59A GB289459A GB866421A GB 866421 A GB866421 A GB 866421A GB 2894/59 A GB2894/59 A GB 2894/59A GB 289459 A GB289459 A GB 289459A GB 866421 A GB866421 A GB 866421A
- Authority
- GB
- United Kingdom
- Prior art keywords
- column
- columns
- reboiler
- compressor
- mixture
- 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
- B01D1/00—Evaporating
- B01D1/28—Evaporating with vapour compression
- B01D1/284—Special features relating to the compressed vapour
- B01D1/2846—The compressed vapour is not directed to the same apparatus from which the vapour was taken off
-
- 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
- B01D3/30—Fractionating columns with movable parts or in which centrifugal movement is caused
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
Fractional distillation apparatus for use at subatmospheric pressure includes a reboiler, a condenser, a vacuum system and at least one distillation column, means being provided for compressing the vapour of the material being fractionated to a pressure not higher than the pressure in the reboiler during its <PICT:0866421/III/1> <PICT:0866421/III/2> passage through the distillation column or columns, or during its passage from one distillation column to the next when a plurality of columns are used in series. In Fig. 1 apparatus comprising two columns T1 and T2 each containing 60 plates can be used for the separation of a mixture of para- and orthonitrochlorobenzene. A vapour compressor B is included in the conduit from the top of T1 to the bottom of T2. Liquid mixture is fed by a pipe F to the bottom of T2 (or at any position in either column depending upon the composition of the mixture) and distillate is removed from a condenser C through a pipe D, the reflux from the bottom of T2 being pumped by pump P to the top of T1 while residue is removed from the reboiler R through a pipe W. By regulating the vacuum pump VP and compressor B the pressures in the columns can be controlled to avoid decomposition of the mixture being fractionated. Whatever the number of columns n only one reboiler, condenser and vacuum system is employed, while n-1 compressors are necessary, each column and the next having a compressor between them. In Fig. 2 the column T is of the rotary disc type in which discs a mounted upon a rotatable shaft s revolve between annular discs c fixed to the column wall. Vanes b attached to the discs a compress the vapour as it rises up through the column, thereby rendering unnecessary the use of a separate compressor whether one column is used or two, as in Fig. 1.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP866421X | 1958-04-28 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB866421A true GB866421A (en) | 1961-04-26 |
Family
ID=13892663
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2894/59A Expired GB866421A (en) | 1958-04-28 | 1959-01-27 | Distillation apparatus |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB866421A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3257372A (en) * | 1962-10-05 | 1966-06-21 | Phillips Petroleum Co | Preparation of soluble polymer and catalyst residues by concentration process |
EP0486866A1 (en) * | 1990-11-17 | 1992-05-27 | Bayer Ag | Process for the isolation of purified dinitrotoluenes |
EP1043050A3 (en) * | 1999-04-05 | 2001-03-07 | Nippon Shokubai Co., Ltd. | Method for refining easily polymerizable matter-containing substance and apparatus therefor |
-
1959
- 1959-01-27 GB GB2894/59A patent/GB866421A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3257372A (en) * | 1962-10-05 | 1966-06-21 | Phillips Petroleum Co | Preparation of soluble polymer and catalyst residues by concentration process |
EP0486866A1 (en) * | 1990-11-17 | 1992-05-27 | Bayer Ag | Process for the isolation of purified dinitrotoluenes |
EP1043050A3 (en) * | 1999-04-05 | 2001-03-07 | Nippon Shokubai Co., Ltd. | Method for refining easily polymerizable matter-containing substance and apparatus therefor |
US6635148B1 (en) | 1999-04-05 | 2003-10-21 | Nippon Shokubai | Method for refining easily polymerizable matter-contained substance and apparatus therefor |
US7253314B2 (en) | 1999-04-05 | 2007-08-07 | Nippon Shokubai Co., Ltd | Method for refining easily polymerizable matter-containing substance and apparatus therefor |
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