US5118282A
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Process for the selective noncatalytic reduction of the emission of pollutants from oil-fired boiler plants
Assignee: EMISSIONS-REDUZIERUNGS-CONCEPTE GmbH
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Filing: 1990-09-17
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Granted: 1992-06-02
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Expires: 2010-09-17
Abstract
Abstract In this process for the selective noncatalytic reduction of the emission of pollutants from oil-fired boiler plants, chemical compounds which affect the combustion process are admixed, in solutions miscible with the liquid fuel, in metered amounts to the liquid fuel or to the combustion air, among these compounds being salts of organic acids, such as naphthenates, octoates, tallates, salts of sulfonic acids, saturated or unsaturated fatty acids, such as oleic acid, and tall oil, with metals from the group of K, Ba, Mg, Ca, Ce, Mn, Fe; rare earth metals; organometallic compounds, such as carbonyl compounds, mixed cyclopentadienylcarbonyl compounds, or aromatic complexes of the transition metals Fe or Mn. For the purpose of minimizing the NO x values in the waste gas and the dust load with economical consumption of chemicals, a reducing agent is introduced in metered quantities into the firebox (burner chamber) via a boiler metering system with the use of the liquid or also gaseous carrier stream as an aqueous solution of urea or also urea precursors, such as ammonia or ammonium carbonate, which can also contain further ingredients, such as alkanols, alkanecarboxylic acids, alkanals, or alkanones.
Inventors
- 👤 Thomas Reynolds
- 👤 Jan-Dirk Meurer
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 09:08
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/54; B01D53/56; C; C10; C10L; C10L1/00; C10L1/10; C10L10/00; C10L10/02; C10L1/12; C10L1/1233; C10L1/1241; C10L1/125; C10L1/1266; C10L1/14; C10L1/16; C10L1/1616; C10L1/18; C10L1/182; C10L1/1822; C10L1/1824; C10L1/185; C10L1/1857; C10L1/188; C10L1/1881; C10L1/1886; C10L1/1888; C10L1/22; C10L1/222; C10L1/2227; C10L1/24; C10L1/2431; C10L1/2437; C10L1/30; C10L1/301; C10L1/305
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
170 words
A process for the selective noncatalytic reduction of the emission of pollutants from an oil-fired boiler plant, with metered introduction of chemical compounds affecting the combustion process to one of the liquid fuel and the combustion air, among said chemical compounds being salts of organic acids, including naphthenates, octoates, tallates, salts of sulfonic acids, saturated or unsaturated fatty acids, including oleic acids, and tall oil with metals selected from the group consisting of K, Ba, Mg, Ca, Ce, Mn, Fe; and rare earth metals; organometallic compounds including carbonyl compounds, mixed cyclopentadienylcarbonyl compounds; or aromatic complexes of the transition metals Fe or Mn, in solutions miscible with the liquid fuel, characterized by adding a reducing agent in metered amounts into the firebox of the plant by way of a boiler metering system with the use of a fluid carrier stream in the form of an aqueous solution of urea or also urea precursors, including ammonia or ammonium carbonate, which can also contain further ingredients, including alkanols, alkanecarboxylic acids, alkanals, or alkanones.
Claim 2
Dependent Claim
170 words
A process for the selective noncatalytic reduction of the emission of pollutants from an oil-fired boiler plant, with metered introduction of chemical compounds affecting the combustion process to one of the liquid fuel and the combustion air, among said chemical compounds being salts of organic acids, including naphthenates, octoates, tallates, salts of sulfonic acids, saturated or unsaturated fatty acids, including oleic acids, and tall oil with metals selected from the group consisting of K, Ba, Mg, Ca, Ce, Mn, Fe; and rare earth metals; organometallic compounds including carbonyl compounds, mixed cyclopentadienylcarbonyl compounds; or aromatic complexes of the transition metals Fe or Mn, in solutions miscible with the liquid fuel, characterized by adding a reducing agent in metered amounts into the firebox of the plant by way of a boiler metering system with the use of a fluid carrier stream in the form of an aqueous solution of urea or also urea precursors, including ammonia or ammonium carbonate, which can also contain further ingredients, including alkanols, alkanecarboxylic acids, alkanals, or alkanones.
Claim 3
Dependent Claim
15 words
A process according to claim 1, characterized by using heavy fuel oil at the fuel.
Claim 4
Dependent Claim
52 words
A process according to claim 1, characterized in that the chemical compounds affecting the combustion process are introduced in the form of solutions miscible with the liquid fuel without a miscibility gap by way of a burner metering system controlled in response to at least one of the load and the emissions.
Claim 5
Dependent Claim
37 words
A process according to claim 1, characterized in that an aqueous urea solution is added in metered amounts as the reducing agent, this solution being diluted in the boiler metering system to 20-0.5% by weight of urea.
Claim 6
Dependent Claim
32 words
A process according to claim 1, characterized in that the addition of the reducing agent into the firebox is introduced into the firebox, as well as the concentration of the reducing agent.
Claim 7
Dependent Claim
34 words
A process according to claim 5, characterized in that the boiler metering system is controlled by means of metering lances for the reducing agent, movable in the firebox with reference to the burner positions.
Claim 8
Dependent Claim
50 words
A process according to claim 5, characterized in that the reducing agent is injected so that, in dependence on the load condition of the furnace plant, the NO x content of the waste gases is minimized with at least one of a given carbon black content and a dust content.
Claim 9
Dependent Claim
38 words
A process according to claim 1, characterized in that an aqueous urea solution is added in metered amounts as the reducing agent, this solution being diluted in the boiler metering system to 10-2% by weight of the urea.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1995-06-02 | 1995-12-02 | 1996-06-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1999-06-02 | 1999-12-02 | 2000-06-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2003-06-02 | 2003-12-02 | 2004-06-02 | $7700.00 | Window Closed / Lapsed |