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GB477955A - Improved method of fractional distillation - Google Patents

Improved method of fractional distillation

Info

Publication number
GB477955A
GB477955A GB18757/36A GB1875736A GB477955A GB 477955 A GB477955 A GB 477955A GB 18757/36 A GB18757/36 A GB 18757/36A GB 1875736 A GB1875736 A GB 1875736A GB 477955 A GB477955 A GB 477955A
Authority
GB
United Kingdom
Prior art keywords
plates
vapours
gutters
towards
conduits
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
GB18757/36A
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.)
Eastman Kodak Co
Original Assignee
Eastman Kodak Co
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 Eastman Kodak Co filed Critical Eastman Kodak Co
Priority to GB18757/36A priority Critical patent/GB477955A/en
Priority to US151715A priority patent/US2176498A/en
Priority to DEE49919D priority patent/DE715418C/en
Priority to FR825680D priority patent/FR825680A/en
Publication of GB477955A publication Critical patent/GB477955A/en
Expired legal-status Critical Current

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
    • B01D3/10—Vacuum distillation
    • 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
    • B01D3/12—Molecular distillation
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

<PICT:0477955/III/1> A process of high vacuum distillation for liquids such as fish oils consists in moving the liquid condensate in cocurrent with the distillate vapours, and then in countercurrent in a conduit protected from the vapours before being again exposed to the vapours. Apparatus suitable for the purpose comprises a series of baffle plates 2 in a column 1, each provided with a central aperture 2<1> turned at the edge to form gutters 3. Between the plates 2 are arranged smaller plates 5 provided with central apertures 6 masked by plates 7 supported a short distance above them. The outer edges of the plates 5 are turned to form gutters 10, which are connected by conduits 9 to the tops of the plates 2, while the gutters 3 are connected by conduits 8 to the tops of the plates 5. The ascending vapours pass through the holes 2<1> in plates 2 and turning outwards towards the column 1 sweep liquid condensate on the plates 2 towards holes 4, through which it passes to the undersides of the plates, where it is swept by the vapours moving inwards into gutters 3, giving up some of its volatile constituents to the vapours. The liquid passes down conduits 8 in countercurrent to the vapours on to the plates 5, where the inward flowing vapours sweep it towards the holes 6 through which it passes on to the undersides of the plates, where it is swept towards the gutters 10 by the outward flowing vapours, yielding some volatile constituents to the vapours. The liquid flows from gutters 10 down conduits 9 in countercurrent to the vapours on to the plates 2, where the process described above takes place again.
GB18757/36A 1936-07-06 1936-07-06 Improved method of fractional distillation Expired GB477955A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
GB18757/36A GB477955A (en) 1936-07-06 1936-07-06 Improved method of fractional distillation
US151715A US2176498A (en) 1936-07-06 1937-07-02 Vacuum rectifying column
DEE49919D DE715418C (en) 1936-07-06 1937-07-03 Process and device for fractional high vacuum distillation
FR825680D FR825680A (en) 1936-07-06 1937-07-06 Improved distillation process and apparatus including application

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB18757/36A GB477955A (en) 1936-07-06 1936-07-06 Improved method of fractional distillation

Publications (1)

Publication Number Publication Date
GB477955A true GB477955A (en) 1938-01-06

Family

ID=10117879

Family Applications (1)

Application Number Title Priority Date Filing Date
GB18757/36A Expired GB477955A (en) 1936-07-06 1936-07-06 Improved method of fractional distillation

Country Status (4)

Country Link
US (1) US2176498A (en)
DE (1) DE715418C (en)
FR (1) FR825680A (en)
GB (1) GB477955A (en)

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR943785A (en) * 1946-03-19 1949-03-17 Mo Och Domsjoe Ab Improvements in distillation and rectification columns and method of distillation using these columns
US2671053A (en) * 1947-06-20 1954-03-02 Shell Dev Method and apparatus for high vacuum distillation
NL68103C (en) * 1948-07-28
US2894599A (en) * 1956-05-18 1959-07-14 Sylvan V Leininger Oil separator and muffler
US2963872A (en) * 1957-03-14 1960-12-13 Union Carbide Corp Process and apparatus for the separation of gas mixtures
US3092480A (en) * 1958-09-17 1963-06-04 Diaz-Compain Jeronimo Entrainment separator arrangements
US3262684A (en) * 1965-03-19 1966-07-26 Sinclair Research Inc Distillation column
US3620283A (en) * 1969-02-04 1971-11-16 Artisan Ind Falling film evaporator stripper
DE2112110A1 (en) * 1971-03-13 1972-10-05 Montz Gmbh Julius Column tray with openings and bells or valves arranged above them
JPS5995903A (en) * 1982-11-24 1984-06-02 Nippon Kayaku Co Ltd Baffle tray column
AT405024B (en) * 1996-07-23 1999-04-26 Schrems Martin Dr METHOD FOR TREATING A LIQUID, IN PARTICULAR TO SEPARATE DIFFERENT COMPONENTS CONTAINED IN THE LIQUID, AND DEVICE FOR CARRYING OUT THIS METHOD
JP6362041B1 (en) * 2017-01-31 2018-07-25 Toto株式会社 Water discharge device
CN110312558B (en) * 2017-03-20 2021-10-15 朗泽科技有限公司 Methods and systems for product recovery and cell recycling
US11091415B2 (en) 2019-02-08 2021-08-17 Lanzatech, Inc. Process for recovering close boiling products

Also Published As

Publication number Publication date
FR825680A (en) 1938-03-10
DE715418C (en) 1941-12-20
US2176498A (en) 1939-10-17

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