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US4144040A Expired / Lapsed US ⏱️ 0.0 years remaining

Method and apparatus for demisting gases

Assignee: Bakaert NV SA
•
Filing: 1976-09-13
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Granted: 1979-03-13
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Expires: 1996-09-13
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Abstract

Abstract Method and apparatus for demisting gases wherein a stream of gas containing submicron liquid particles is caused to pass through a filter material comprising at least in part a material having a porosity of at least 0.985.

Inventors

  • 👤 Jozef Claes
  • 👤 Roger De Bruyne

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 17:14
CPC Classifications
B; B01; B01D; B01D46/00; B01D46/0002; B01D46/0012; B01D39/00; B01D39/14; B01D39/20; B01D39/2027; B01D39/2041; B01D39/2044; B01D46/0027; B01D46/003; B01D46/0031; B01D46/24; B01D53/00; B01D53/26; B01D53/266

Claims Analysis

Total Claims: 23
Claim 1
Independent Claim 131 words
Filtration apparatus for the removal of liquid particles from a stream of gas comprising filtration means including a plurality of adjacent non-woven metal fiber webs, means for passing a stream of gas containing liquid particles at least some of which are of submicron dimensions through said filter means at a velocity of less than 70 cm/sec, means for removing from said filtration means said stream of gas from which at least some of said particles including at least some of said submicron particles have been removed, and outlet means for the removed liquid, the diameter of the fibers in successive ones of said webs decreasing in the direction of flow of the gas stream, said filtration means having a porosity of at least 0.985 and being moistenable by said liquid particles.
Claim 2
Dependent Claim 131 words
Filtration apparatus for the removal of liquid particles from a stream of gas comprising filtration means including a plurality of adjacent non-woven metal fiber webs, means for passing a stream of gas containing liquid particles at least some of which are of submicron dimensions through said filter means at a velocity of less than 70 cm/sec, means for removing from said filtration means said stream of gas from which at least some of said particles including at least some of said submicron particles have been removed, and outlet means for the removed liquid, the diameter of the fibers in successive ones of said webs decreasing in the direction of flow of the gas stream, said filtration means having a porosity of at least 0.985 and being moistenable by said liquid particles.
Claim 3
Dependent Claim 17 words
Apparatus as in claim 1 and wherein said filtration means has a porosity of 0.99 during filtration.
Claim 4
Dependent Claim 18 words
Apparatus as claimed in claim 1 wherein the said filter material has a porosity of at least 0.995.
Claim 5
Dependent Claim 14 words
Apparatus as claimed in claim 1 wherein said metal fibers are stainless steel fibres.
Claim 6
Dependent Claim 15 words
Apparatus as claimed in claim 1 wherein the webs comprise fibers having a rough surface.
Claim 7
Dependent Claim 17 words
Apparatus as claimed in claim 1 wherein the filter material has a thickness not exceeding 10 cms.
Claim 8
Dependent Claim 24 words
Apparatus as claimed in claim 1 wherein the filter material is in the form of concentrically arranged hollow cylinders having concentric free spaces therebetween.
Claim 9
Dependent Claim 20 words
Apparatus as claimed in claim 7 wherein the filter material is retained by means of a framework of wire netting.
Claim 10
Dependent Claim 18 words
Apparatus as claimed in claim 1 wherein the web comprises fibres having a diameter of 1 to 50μ.
Claim 11
Dependent Claim 18 words
Apparatus as claimed in claim 9 wherein the web comprises fibres having a diameter of 1 to 10μ.
Claim 12
Independent Claim 114 words
A method for filtering a stream of gas at high efficiency for removing liquid particles at least some of which are of submicron dimensions therefrom comprising passing the stream of gas at a velocity of less than 70 cm/sec through a filter material comprising a plurality of adjacent non-woven metal fiber webs moistenable by said liquid particles, the diameter of the fibres in successive webs decreasing in the direction of flow of the gas stream and the webs having a porosity of at least 0.985 whereby at least some of said particles including at least some of said submicron particles are removed from the gas stream, and removing captured liquid from the filter material.
Claim 13
Independent Claim 114 words
A method for filtering a stream of gas at high efficiency for removing liquid particles at least some of which are of submicron dimensions therefrom comprising passing the stream of gas at a velocity of less than 70 cm/sec through a filter material comprising a plurality of adjacent non-woven metal fiber webs moistenable by said liquid particles, the diameter of the fibres in successive webs decreasing in the direction of flow of the gas stream and the webs having a porosity of at least 0.985 whereby at least some of said particles including at least some of said submicron particles are removed from the gas stream, and removing captured liquid from the filter material.
Claim 14
Dependent Claim 18 words
A method as in claim 11 and wherein said filter material has a porosity of 0.985 during filtration.
Claim 15
Dependent Claim 18 words
A method as in claim 11 and wherein said filter material has a porosity of at least 0.995.
Claim 16
Dependent Claim 14 words
A method as in claim 11 and wherein said fibers are stainless steel fibers.
Claim 17
Dependent Claim 14 words
A method as in claim 11 and wherein said fibers have a rough surface.
Claim 18
Dependent Claim 17 words
A method as in claim 11 and wherein said fibrous web has been needle punched or pressed.
Claim 19
Dependent Claim 19 words
A method as in claim 11 and wherein said fibrous web has a thickness not greater than 10 cm.
Claim 20
Dependent Claim 25 words
A method as in claim 11 and wherein said filter material is in the form of concentrically arranged hollow cylinders having concentric free spaces therebetween.
Claim 21
Dependent Claim 22 words
A method as in claim 18 and wherein said filter material includes a framework of wire netting for retaining said filter material.
Claim 22
Dependent Claim 17 words
A method as in claim 11 and wherein said fibers have a diameter of 1 to 50μ.
Claim 23
Dependent Claim 17 words
A method as in claim 20 and wherein said fibers have a diameter of 1 to 10μ.

References Cited (Backward Citations)

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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1982-03-12 1982-09-11 1983-03-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-03-12 1986-09-11 1987-03-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-03-12 1990-09-11 1991-03-13 $7700.00 Window Closed / Lapsed

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