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GB866421A - Distillation apparatus - Google Patents

Distillation apparatus

Info

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
Application number
GB2894/59A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
FUMITAKE YOSHIDA
Original Assignee
FUMITAKE YOSHIDA
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by FUMITAKE YOSHIDA filed Critical FUMITAKE YOSHIDA
Publication of GB866421A publication Critical patent/GB866421A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/28Evaporating with vapour compression
    • B01D1/284Special features relating to the compressed vapour
    • B01D1/2846The compressed vapour is not directed to the same apparatus from which the vapour was taken off
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14Fractional distillation or use of a fractionation or rectification column
    • B01D3/30Fractionating 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.
GB2894/59A 1958-04-28 1959-01-27 Distillation apparatus Expired GB866421A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (5)

* Cited by examiner, † Cited by third party
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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