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US5486341A Expired / Lapsed US ⏱️ 0.0 years remaining

Entrainment separator for high velocity gases

Assignee: Alstom Power Inc
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Filing: 1994-06-09
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Granted: 1996-01-23
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Expires: 2014-06-09
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Abstract

Abstract Sulfur oxides (SO x ) are scrubbed from combustion effluents with aqueous limestone slurries with greater efficiency due to the use of an improved entrainment separator. In the preferred embodiment of a single-loop, counter-current limestone wet scrubber operating at bulk gas flow rates of greater than 4.5 meters per second, a vertical stream of flue gas is freed of a substantial portion of slurry droplets and diverted for effective mist removal by a well-drained, horizontal-flow mist eliminator. The entrainment separator is a single-pass device with individual blades aligned for effective operation with reduced droplet impingement on the upper walls (e.g., roof) of the scrubber and to permit periodic washing.

Inventors

  • 👤 Gerald E. Bresowar

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 16:13
CPC Classifications
B; B01; B01D; B01D45/00; B01D45/04; B01D45/08; B01D45/10; B01D47/00; B01D47/06; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/501; B01D53/504; B01D2277/00; B01D2277/20; F; F23; F23J; F23J2215/00; F23J2215/20; F23J2219/00; F23J2219/40

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 176 words
An improved wet scrubbing process for reducing the concentration of SO 2 in flue gases, comprising: (a) directing a flow of flue gas upwardly through a scrubbing tower; (b) introducing a spray of droplets of an aqueous slurry of finely-divided calcium carbonate, calcium sulfate, calcium sulfite, and other non-reactive inerts to contact the flue gas in a vertical scrubbing section, the slurry descending through the tower countercurrently to the flow of flue gas and being collected as a liquid after contact; and (c) passing the flue gas through a single pass entrainment separator positioned above and across the vertical scrubbing section at an angle within the range of about 10° to about 45 degrees relative to the horizontal effective to reduce or consolidate a substantial quantity of droplets entrained in the gas and to also turn the direction of flow of the flue gas from the vertical said entrainment separator includes individual single-pass separator blades, said individual blades are oriented at an angle within the range of about 35° to about 55 degrees from the vertical.
Claim 2
Dependent Claim 176 words
An improved wet scrubbing process for reducing the concentration of SO 2 in flue gases, comprising: (a) directing a flow of flue gas upwardly through a scrubbing tower; (b) introducing a spray of droplets of an aqueous slurry of finely-divided calcium carbonate, calcium sulfate, calcium sulfite, and other non-reactive inerts to contact the flue gas in a vertical scrubbing section, the slurry descending through the tower countercurrently to the flow of flue gas and being collected as a liquid after contact; and (c) passing the flue gas through a single pass entrainment separator positioned above and across the vertical scrubbing section at an angle within the range of about 10° to about 45 degrees relative to the horizontal effective to reduce or consolidate a substantial quantity of droplets entrained in the gas and to also turn the direction of flow of the flue gas from the vertical said entrainment separator includes individual single-pass separator blades, said individual blades are oriented at an angle within the range of about 35° to about 55 degrees from the vertical.
Claim 3
Dependent Claim 44 words
A process according to claim 1 wherein the entrainment separator is effective to reduce the quantity of droplets by at least 40% and to turn the direction of flow of the flue gases by at least 45° from the vertical axis of the tower.
Claim 4
Dependent Claim 24 words
A process according to claim 1 wherein the flue gas is passed through a well-drained, horizontal flow mist eliminator downstream of the entrainment separator.
Claim 5
Dependent Claim 20 words
A process according to claim 1 wherein the vertical bulk gas velocity is greater than about 4.5 meters per second.
Claim 6
Dependent Claim 38 words
A process according to claim 1 wherein the entrainment separator causes a pressure drop of less than about 0.15 inches of water, and removes or consolidates at least 40% of droplets smaller than about 100μ Sauter mean diameter.
Claim 7
Dependent Claim 50 words
A process according to claim 1 wherein the entrainment separator utilizes single pass separator blades to collect droplets by impingement and to turn the gas in a direction most suitable for further mist elimination, the individual blades being held parallel to one another in each of a plurality of assemblies.
Claim 8
Dependent Claim 30 words
A process according to claim 1 wherein and the spacing between individual blades will typically be from about 40 to about 70% of the minor dimension of the individual blades.
Claim 9
Dependent Claim 47 words
A process according to claim 1 wherein the entrainment separator comprises a plurality of assemblies of individual blades, said assemblies being oriented at an angle in the range of from about 120° to about 150° with respect to one another, whereby said assemblies form a chevron pattern.
Claim 10
Dependent Claim 27 words
A process according to claim 1 wherein the blades are washed periodically by spraying wash water directly onto the blades from both the top and the bottom.

References Cited (Backward Citations)

DE3008718A1 Cited
JPS62282625A Cited
DE3706533A1 Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1999-01-22 1999-07-24 2000-01-23 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2003-01-22 2003-07-24 2004-01-23 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2007-01-22 2007-07-24 2008-01-23 $7700.00 Window Closed / Lapsed

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