Patent US4640681A successfully refreshed from Google Patents.
US4640681A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method and apparatus for the removal of harmful and waste materials by combustion
Assignee: Kloeckner Humboldt Deutz AG
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Filing: 1985-08-30
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Granted: 1987-02-03
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Expires: 2005-08-30
Abstract
Abstract A method and apparatus for the removal of hazardous and waste materials of low heat content, for example, refuse, by means of combustion wherein the combustion process is carried out in a furnace by the presence of added hot combustion air at a temperature sufficient so that the combustion and/or flue gas temperatures are at least 1250° C. In a preferred embodiment of the invention, the combustion process is combined with a process for the production of cement clinker and carried out parallel to the same, wherein air at about 800° C. is branched off for combustion of the hazardous substances from the cooler air of the cement clinker installation and introduced into the furnace. The hot flue gas of the combustion in the furnace is directed into the cement clinker installation. The invention further contemplates that calcium-containing carbonate carriers can be added to the refuse.
Inventors
- 👤 Eberhard Steinbiss
- 👤 Horst Herchenbach
- 👤 Albrecht Wolter
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 11:31
CPC Classifications
C; C04; C04B; C04B7/00; C04B7/36; C04B7/43; C04B7/44; C04B7/4407; C04B7/4446; C10; C10L; C10L10/00; C10L10/06; F; F23; F23G; F23G5/00; F23G5/006; F23G5/02; F23G5/027; F23G5/08; F23N; F23N5/00; F23N5/003; F23N5/006; F23G2201/00; F23G2201/30; F23G2201/303; F23G2201/304; F23G2206/00; F23G2206/20; F23G2206/201; Y; Y02; Y02E; Y02E20/00; Y02E20/30; Y02P; Y02P40/00; Y02P40/10; Y02P40/125
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
217 words
A method for the removal of hazardous substances from hazardous and waste materials which comprises: providing a process for manufacturing cement clinker which includes the steps of preheating the cement raw material, calcining the preheated raw material in a precalciner, sintering the calcined raw material in a kiln following said precalciner, and cooling the clinker thus produced in a cooler, diverting heated air from the cooler of the cement making process according to the heat content of the substances to be burned at temperatures in the range from 600° C. to 950° C. to a furnace in which said hazardous and waste materials are combusted under conditions sufficient to achieve a combustion temperature and flue gas temperatures in said furnace of at least 1250° C., withdrawing and discharging a portion of the hot flue gas from said kiln by means of a bypass, the amount of said portion depending on the relative amounts of hazardous materials contained in said furnace flue gas, directing the hot flue gas from said furnace into the precalciner of said cement making process for supplying heat thereto, and adding to said hazardous and waste material a quantity of calcium containing carbonate carriers such that the CaO content of the calcination product is in the range of between 30% to 70% by weight.
Claim 2
Independent Claim
217 words
A method for the removal of hazardous substances from hazardous and waste materials which comprises: providing a process for manufacturing cement clinker which includes the steps of preheating the cement raw material, calcining the preheated raw material in a precalciner, sintering the calcined raw material in a kiln following said precalciner, and cooling the clinker thus produced in a cooler, diverting heated air from the cooler of the cement making process according to the heat content of the substances to be burned at temperatures in the range from 600° C. to 950° C. to a furnace in which said hazardous and waste materials are combusted under conditions sufficient to achieve a combustion temperature and flue gas temperatures in said furnace of at least 1250° C., withdrawing and discharging a portion of the hot flue gas from said kiln by means of a bypass, the amount of said portion depending on the relative amounts of hazardous materials contained in said furnace flue gas, directing the hot flue gas from said furnace into the precalciner of said cement making process for supplying heat thereto, and adding to said hazardous and waste material a quantity of calcium containing carbonate carriers such that the CaO content of the calcination product is in the range of between 30% to 70% by weight.
Claim 3
Dependent Claim
55 words
A method for the removal of hazardous substances from hazardous and waste materials in accordance with the steps of claim 1: wherein the quantity of calcium containing carbonate carriers added to the waste material is such that the CaO content of the calcination product is in the range of between 40% and 50% by weight.
Claim 4
Dependent Claim
17 words
A method according to claim 1 wherein the combustion temperatures are between 1250° C. and 1500° C.
Claim 5
Dependent Claim
19 words
A method according to claim 1 wherein: said combustion is carried at temperatures between 1300° C. and 1400° C.
Claim 6
Dependent Claim
40 words
A method according to claim 1 which includes the step of adding at least a portion of the residue of the combustion process to the calcination material in the cement calcination installation and processing the same along with cement clinker.
Claim 7
Dependent Claim
25 words
A method according to claim 1 wherein said waste material is added to the furnace during gas shut-off of the inlet chamber of said furnace.
Claim 8
Dependent Claim
29 words
A method according to claim 1 which includes the step of blowing waste material into the hottest part of the cement calcination process by means of a carrier gas.
Claim 9
Dependent Claim
46 words
A method according to claim 1 which includes the steps of thermally decomposing the waste materials in a dry distillation process to produce a gas and a solid residue, burning said gas in the calcination zone, and passing said solid residue into the cement calcination furnace.
Claim 10
Dependent Claim
20 words
A method according to claim 1 which includes the step of melting the calcination product to produce a glassy condition.
Claim 11
Dependent Claim
14 words
A method according to claim 1 in which said furnace is a rotary kiln.
Claim 12
Dependent Claim
18 words
A method according to claim 1 which includes the step of adding a binder to the calcined product.
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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) | 1990-02-02 | 1990-08-04 | 1991-02-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1994-02-02 | 1994-08-04 | 1995-02-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1998-02-02 | 1998-08-04 | 1999-02-03 | $7700.00 | Window Closed / Lapsed |