GB813348A - Improvements in or relating to a coalescing method for the removal of finely dividedliquid particles from gases - Google Patents

Improvements in or relating to a coalescing method for the removal of finely dividedliquid particles from gases

Info

Publication number
GB813348A
GB813348A GB24312/56A GB2431256A GB813348A GB 813348 A GB813348 A GB 813348A GB 24312/56 A GB24312/56 A GB 24312/56A GB 2431256 A GB2431256 A GB 2431256A GB 813348 A GB813348 A GB 813348A
Authority
GB
United Kingdom
Prior art keywords
particles
finely
gases
mist
dividedliquid
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
GB24312/56A
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.)
ALEXIS EUGENE JACKSON
VADIM STEPHEN MAKAROFF
Original Assignee
ALEXIS EUGENE JACKSON
VADIM STEPHEN MAKAROFF
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 ALEXIS EUGENE JACKSON, VADIM STEPHEN MAKAROFF filed Critical ALEXIS EUGENE JACKSON
Publication of GB813348A publication Critical patent/GB813348A/en
Expired legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
    • B01D45/06—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by reversal of direction of flow
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24—HEATING; RANGES; VENTILATING
    • F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
    • F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
    • F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
    • F24F3/1411—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by absorbing or adsorbing water, e.g. using an hygroscopic desiccant

Abstract

813,348. Separating liquid particles from gases. MAKAROFF, V. S., and JACKSON, A. E. Aug. 8, 1956 [Aug. 16, 1955; July 23, 1956], No. 24312/56. Class 123(3) Finely-divided liquid particles forming a mist in a gas are separated by passing the gas through a body 2 of porous material supported on a grid 3 in a chamber 7, the material being adsorptive or absorptive with respect to the liquid constituting the droplets. When separating oil mist, suitable materials are flaked asbestos or diatomaceous earth. The apparatus is operated continuously, the mist particles coalescing and collecting in the mass 2 and eventually dripping therefrom into the bottom of the chamber whence they are drained through a pipe 4. Dry gas discharges through a pipe 6. Specification 30,004/10 [Class 123] is referred to.
GB24312/56A 1955-08-16 1956-08-08 Improvements in or relating to a coalescing method for the removal of finely dividedliquid particles from gases Expired GB813348A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US813348XA 1955-08-16 1955-08-16

Publications (1)

Publication Number Publication Date
GB813348A true GB813348A (en) 1959-05-13

Family

ID=22163519

Family Applications (1)

Application Number Title Priority Date Filing Date
GB24312/56A Expired GB813348A (en) 1955-08-16 1956-08-08 Improvements in or relating to a coalescing method for the removal of finely dividedliquid particles from gases

Country Status (1)

Country Link
GB (1) GB813348A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3246455A (en) * 1962-02-12 1966-04-19 King Eng Corp Gas dispersoid separator
GB2194180A (en) * 1984-11-23 1988-03-02 Domnick Hunter Filters Ltd Liquid/gas separation

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3246455A (en) * 1962-02-12 1966-04-19 King Eng Corp Gas dispersoid separator
GB2194180A (en) * 1984-11-23 1988-03-02 Domnick Hunter Filters Ltd Liquid/gas separation

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