← Back to Patent Explorer
US5138958A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for incinerating domestic refuse in a fluidized bed furnace

Assignee: General de Chauffe Cie
•
Filing: 1991-11-01
•
Granted: 1992-08-18
•
Expires: 2011-11-01
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A process for incinerating domestic refuse is implemented in a boiler comprising a fluidized bed furnace over which is a post-combustion chamber. The smoke passes through alternately upward and downward paths in which it is cooled in contact with walls provided with water tubes. Limestone is injected into the bed to fix the sulfur oxides and halogenated compounds and a jet of powdered lime is injected at the start of the third path to neutralize the remaining halogenated compounds; the flying particles deposited are recycled into the furnace. The temperature of the bed is held between 800° C. and 900° C. and the injection of secondary air is adjusted to obtain an oxygen concentration in the smoke between 5.5% and 7.5% to minimize the formation of nitrogen oxides, dioxins and furans.

Inventors

  • 👤 Roger Sinquin
  • 👤 Alexandre Petrovic

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 05:56
CPC Classifications
F; F23; F23G; F23G5/00; F23G5/44; F23G5/46; F22; F22B; F22B31/00; F22B31/0007; F22B31/0015; F22B31/003; F23G5/30; F23J; F23J15/00; F23J15/02; B; B01; B01D; B01D2258/00; B01D2258/02; B01D2258/0283; B01D2258/0291; F23G2203/00; F23G2203/50; F23G2203/501; F23G2206/00; F23G2206/20; F23G2206/203; F23G2207/00; F23G2207/10; F23G2207/101; F23G2207/103; F23G2207/30; F23G2207/60; F23G2900/00; F23G2900/55; F23G2900/55006; F23J2215/00; F23J2215/10; F23J2215/30; F23J2215/301; Y; Y02; Y02E; Y02E20/00; Y02E20/12

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 212 words
A process for incinerating domestic refuse and the like with intrinsic smoke cleaning in which the refuse previously broken down to an appropriate particle size is introduced into a dense fluidized bed fed with primary combustion supporting air from below in which the fixed parts burn and the volatile parts are released comprising, along with combustible gases, pollutants such as sulfur oxides and halogenated gases in particular and entrained solid particles; secondary combustion-supporting air is injected into a post-combustion chamber over the fluidized bed furnace in which said combustible gases burn to form smoke; and the thermal energy of the smoke is recovered in a boiler with walls provided with water tubes subdivided by baffles into successive alternately upward and downward vertical paths, the upward first path extending the post-combustion chamber, in which process, the boiler being divided into at least three smoke paths, limestone is introduced into the fluidized bed in at least stoichiometric excess relative to the sulfur-containing compounds, measured as sulfur oxides; powdered lime is injected at the start of the upward third path in quantities at least sufficient to neutralize the halogenated gases; powder solids are recovered at the lower level between the second and third paths and these powder solids are introduced into the fluidized bed furnace.
Claim 2
Dependent Claim 212 words
A process for incinerating domestic refuse and the like with intrinsic smoke cleaning in which the refuse previously broken down to an appropriate particle size is introduced into a dense fluidized bed fed with primary combustion supporting air from below in which the fixed parts burn and the volatile parts are released comprising, along with combustible gases, pollutants such as sulfur oxides and halogenated gases in particular and entrained solid particles; secondary combustion-supporting air is injected into a post-combustion chamber over the fluidized bed furnace in which said combustible gases burn to form smoke; and the thermal energy of the smoke is recovered in a boiler with walls provided with water tubes subdivided by baffles into successive alternately upward and downward vertical paths, the upward first path extending the post-combustion chamber, in which process, the boiler being divided into at least three smoke paths, limestone is introduced into the fluidized bed in at least stoichiometric excess relative to the sulfur-containing compounds, measured as sulfur oxides; powdered lime is injected at the start of the upward third path in quantities at least sufficient to neutralize the halogenated gases; powder solids are recovered at the lower level between the second and third paths and these powder solids are introduced into the fluidized bed furnace.
Claim 3
Dependent Claim 28 words
Process according to claim 1 wherein the temperature and the flowrate of the primary air are adjusted correlatively to maintain the fluidized bed in a predetermined temperature range.
Claim 4
Dependent Claim 17 words
Process according to claim 2 wherein said predetermined temperature range is between 800° C. and 900° C.
Claim 5
Dependent Claim 33 words
Process according to claim 1 in which the oxygen content of the smoke is analyzed continuously and the secondary air flowrate is adjusted to maintain this concentration at between 5.5% and 7.5% approx.
Claim 6
Dependent Claim 32 words
Process according to claim 1 wherein the stoichiometric ratio between the limestone injected into the bed and the sulfur content of the refuse, measured as sulfur oxides, is between 2.5 and 3.
Claim 7
Dependent Claim 17 words
Process according to claim 1 wherein a downward fourth smoke path follows on from the third path.
Claim 8
Dependent Claim 33 words
Process according to claim 6 wherein the smoke is cooled at the outlet from the fourth path to approximately 140° C. by passing it through an exchanger (economizer) supplying water to the boiler.
Claim 9
Dependent Claim 24 words
Process according to claim 7 wherein dust is extracted from the smoke between the economizer and a chimney for dispersing it into the atmosphere.
Claim 10
Dependent Claim 26 words
Process according to claim 1 in which the lime is injected in a vertically upwards direction by pneumatic means at the start of the third path.

References Cited (Backward Citations)

EP0005965A1 Cited
US4422410A Cited
SE453777B Cited
FR2583305A1 Cited
EP0238048A1 Cited
EP0358760A1 Cited
US4913097A Cited
EP0388284A1 Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1995-08-18 1996-02-17 1996-08-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1999-08-18 2000-02-17 2000-08-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2003-08-18 2004-02-17 2004-08-18 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag