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US4982672A Expired / Lapsed US ⏱️ 0.0 years remaining

Low NOX incineration process

Assignee: PETROCON ENGINEERING Inc
•
Filing: 1990-02-23
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Granted: 1991-01-08
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Expires: 2010-02-23
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Abstract

Abstract A process for low NOX incineration which involves incinerating hazardous waste to produce a gaseous stream, adding combustible material to produce a combustible gas stream having combustible material in excess of the oxygen in the combustible gas stream, incinerating the combustible gas stream in a reducing atmosphere to produce a heated oxygen-depleted gaseous stream, converting at least a portion of the heat in the oxygen depleted stream into steam, adding air to the oxygen depleted stream to produce a stoichiometric excess of oxygen in the resultant stream relative to combustible material present in the resultant stream, passing the resultant stream over an oxidizing catalyst to produce an oxidized gaseous stream, removing heat from the oxidized stream, and venting the resultant cooled stream. A system for carrying out the foregoing process is also provided.

Inventors

  • 👤 Ronald D. Bell

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 20:05
CPC Classifications
F; F23; F23J; F23J15/00; F23J15/006; F01; F01K; F01K23/00; F01K23/02; F01K23/06; F01K23/10; F01K23/103; F22; F22B; F22B1/00; F22B1/02; F22B1/18; F22B1/1861; F23C; F23C6/00; F23C6/04; F23C6/042; F23C9/00; F23G; F23G5/00; F23G5/006; F23G5/44; F23G5/46; F23J2215/00; F23J2215/20; F23J2215/60; F23J2219/00; F23J2219/10

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 224 words
A process for low NO x hazardous waste incineration which comprises incinerating hazardous waste in the presence of air and fuel in a primary incineration zone to produce a first effluent gas stream, the amount of air supplied to said primary zone being in stoichiometric excess with respect to combustible materials provided by the fuel and waste being incinerated, whereby said first effluent gas stream also has excess oxygen with respect to combustible material therein; adding combustible materials to said first effluent gas stream to provide a combustible gas stream having a combustible material content in excess of the oxygen in said combustible gas stream and incinerating said combustible gas stream in a secondary incineration zone at a temperature in the range of 2000° to 2400° F. and under the reducing conditions arising from said excess combustible material content, to produce a heated oxygen-depleted gaseous effluent stream; converting at least a portion of the heat in said oxygen-depleted stream into steam, thereby cooling said stream; adding air to said cooled oxygen-depleted stream to produce a stoichiometric excess of oxygen in the resultant stream relative to combustible material present in said resultant stream and passing said resultant stream over an oxidizing catalyst to produce an oxidized gaseous stream; removing heat from said oxidized stream, and venting the resultant cooled stream of low NO x content.
Claim 2
Dependent Claim 224 words
A process for low NO x hazardous waste incineration which comprises incinerating hazardous waste in the presence of air and fuel in a primary incineration zone to produce a first effluent gas stream, the amount of air supplied to said primary zone being in stoichiometric excess with respect to combustible materials provided by the fuel and waste being incinerated, whereby said first effluent gas stream also has excess oxygen with respect to combustible material therein; adding combustible materials to said first effluent gas stream to provide a combustible gas stream having a combustible material content in excess of the oxygen in said combustible gas stream and incinerating said combustible gas stream in a secondary incineration zone at a temperature in the range of 2000° to 2400° F. and under the reducing conditions arising from said excess combustible material content, to produce a heated oxygen-depleted gaseous effluent stream; converting at least a portion of the heat in said oxygen-depleted stream into steam, thereby cooling said stream; adding air to said cooled oxygen-depleted stream to produce a stoichiometric excess of oxygen in the resultant stream relative to combustible material present in said resultant stream and passing said resultant stream over an oxidizing catalyst to produce an oxidized gaseous stream; removing heat from said oxidized stream, and venting the resultant cooled stream of low NO x content.
Claim 3
Dependent Claim 24 words
A process as defined in claim 1, wherein said hazardous waste is incinerated in said first incineration zone at a temperature of 1500°-2000° F.
Claim 4
Dependent Claim 28 words
A process as defined in claim 1, wherein said oxygen-depleted stream is cooled to a temperature of about 450° F. during said conversion of the heat to steam.
Claim 5
Dependent Claim 28 words
A process as defined in claim 1, wherein the space velocity of said resultant stream passing over said oxidizing catalyst is about 30,000 to 50,000 hr. -1 .
Claim 6
Dependent Claim 35 words
A process as defined in claim 1, wherein said air is added to said oxygen-depleted stream in an amount to provide a stoichiometric excess of oxygen present in the resultant stream of 10 to 50%.
Claim 7
Dependent Claim 25 words
A process as defined in claim 1, wherein the cooled gas vented to the atmosphere is at a temperature of about 300° to 400° F.
Claim 8
Dependent Claim 23 words
A process as defined in claim 1, wherein the cooled gas vented to the atmosphere has a NOX content of less than 50ppm.
Claim 9
Dependent Claim 19 words
A process as defined in claim 1, wherein the oxygen-depleted gaseous stream is treated to remove acidic components therefrom;
Claim 10
Dependent Claim 19 words
A process as defined in claim 1, wherein the oxygen-depleted gaseous stream is treated to remove solid components therefrom.
Claim 11
Dependent Claim 32 words
A process as defined in claim 1, wherein the oxygen-depleted gaseous stream is treated to remove acidic components therefrom, and wherein the oxygen-depleted gaseous stream is treated to remove solid components therefrom.

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) 1994-01-07 1994-07-09 1995-01-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1998-01-07 1998-07-09 1999-01-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2002-01-07 2002-07-09 2003-01-08 $7700.00 Window Closed / Lapsed

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