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GB916882A - Method and apparatus for the continuous separation of sublimed products from hot carrier gases - Google Patents

Method and apparatus for the continuous separation of sublimed products from hot carrier gases

Info

Publication number
GB916882A
GB916882A GB266560A GB266560A GB916882A GB 916882 A GB916882 A GB 916882A GB 266560 A GB266560 A GB 266560A GB 266560 A GB266560 A GB 266560A GB 916882 A GB916882 A GB 916882A
Authority
GB
United Kingdom
Prior art keywords
elements
cooling
heating
stream
oil
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
GB266560A
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.)
HAPPEL GmbH
Original Assignee
HAPPEL GmbH
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 HAPPEL GmbH filed Critical HAPPEL GmbH
Publication of GB916882A publication Critical patent/GB916882A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/54Preparation of carboxylic acid anhydrides
    • C07C51/573Separation; Purification; Stabilisation; Use of additives
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D7/00Sublimation
    • B01D7/02Crystallisation directly from the vapour phase

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

<PICT:0916882/III/1> <PICT:0916882/III/2> Sublimable solid substances such as maleic anhydride, phthalic anhydride and naphthalene are condensed as solids from a stream of gas containing said substances in gaseous form by passing said stream into contact successively with a plurality of heat exchange elements and alternately heating and cooling each of said elements so that whilst sublimate is condensing on some elements it is melting off other elements for removal. In Fig. 4 in addition to the elements 2 for both heating and cooling, elements 18 are provided for cooling only, their temperature being such as to result in the condensation of the substance in liquid form. Heating and cooling are provided by means of oil respectively circulated through a steam energized heater 11 and a cooler 13 by means of pumps 10 and 12. The cooling oil for the elements 18 is circulated by a pump 19 through an oil/air cooler 20. The elements 2 comprise banks of horizontal finned tubes through which the oil flows in a series/parallel manner (Figs. 1 and 2, not shown). The tubes can alternatively be connected in serpentine fashion, and where smooth, unfinned tubes are employed, they may be arranged vertically. The elements may be mounted on guide rails so as to be retractable for cleaning. Troughs 3 are provided to collect molten sublimate, these and the outlet tubes therefrom being provided with heating jackets which are supplied with oil from the heating circuit. In Fig. 5 the heating circuit is eliminated by the inclusion in the cooling circuit of heat exchangers 26 which may employ steam as the heating medium or may be heated electrically. In a further embodiment (not illustrated) heat exchangers 26 may themselves be eliminated by including electrical heating elements within the tubes making up elements 2. The cooler 22 in these modifications must be capable of removing the additional heat imparted to the cooling medium. In the above embodiments valves 8, 9 and valves 28 are individually controllable either manually or automatically on a time basis or on a temperature basis, i.e. when the cooling becomes inefficient due to deposited condensate.ALSO:Maleic anhydride and phthalic anhydride are condensed as solids from a stream of gas containing said substances, which may be derived from the catalytic oxidation of benzene or naphthalene, by passing said stream into contact successively with a plurality of heat exchange elements and alternately heating and cooling each of said elements so that whilst sublimate is condensing on some elements, it is being melted off other elements for removal. Naphthalene may be similarly recovered from a stream of gas. Suitable apparatus is described (see Group III).
GB266560A 1959-02-11 1960-01-25 Method and apparatus for the continuous separation of sublimed products from hot carrier gases Expired GB916882A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DEG26358A DE1084239B (en) 1959-02-11 1959-02-11 Method and device for the continuous separation of sublimation products from hot carrier gases

Publications (1)

Publication Number Publication Date
GB916882A true GB916882A (en) 1963-01-30

Family

ID=7122899

Family Applications (1)

Application Number Title Priority Date Filing Date
GB266560A Expired GB916882A (en) 1959-02-11 1960-01-25 Method and apparatus for the continuous separation of sublimed products from hot carrier gases

Country Status (3)

Country Link
DE (1) DE1084239B (en)
FR (1) FR1245875A (en)
GB (1) GB916882A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4765966A (en) * 1986-02-03 1988-08-23 Ultra-Centrifuge Nederland N.V. Sublimation apparatus
WO2011100081A1 (en) 2010-02-12 2011-08-18 Exxonmobil Chemical Patents Inc. A Corporation Of The State Of Delaware Processes utilizing switch condensers

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1196578B (en) * 1962-02-27 1965-07-08 Leybold Hochvakuum Anlagen Freeze-drying process with recovery of volatile components
US4066420A (en) 1976-05-07 1978-01-03 Dr. C. Otto & Comp. G.M.B.H. Process for the gasification of solid fuels
GB1593610A (en) * 1977-06-24 1981-07-22 Chevron Res Process for recovering maleic anhydride by condensation
SE425215B (en) * 1980-09-12 1982-09-13 Jacob Weitman SET AND DEVICE FOR TREATING A HEATED CONTAMINATED GAS
DE3512930A1 (en) * 1985-04-11 1986-10-16 GEA Luftkühlergesellschaft Happel GmbH & Co, 4630 Bochum Desublimation unit
DE4427872C1 (en) * 1994-08-06 1996-02-01 Gea Luftkuehler Happel Gmbh Sepn. of a vaporised prod., esp. phthalic anhydride
DE19703681A1 (en) * 1997-01-31 1998-08-06 Linde Ag Method and device for removing condensable components from gases and / or gas mixtures
DE112005003542A5 (en) * 2005-04-19 2008-02-28 Creaphys Gmbh Vacuum apparatus and method for gas phase processing a substance

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4765966A (en) * 1986-02-03 1988-08-23 Ultra-Centrifuge Nederland N.V. Sublimation apparatus
WO2011100081A1 (en) 2010-02-12 2011-08-18 Exxonmobil Chemical Patents Inc. A Corporation Of The State Of Delaware Processes utilizing switch condensers
US20130001448A1 (en) * 2010-02-12 2013-01-03 Exxonmobil Chemical Patents Inc. Processes Utilizing Switch Condensers

Also Published As

Publication number Publication date
DE1084239B (en) 1960-06-30
FR1245875A (en) 1960-11-10

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