Patent US4750436A successfully refreshed from Google Patents.
US4750436A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method and plant for the treatment of contaminated soils and similar material
Assignee: O&K Orenstein and Koppel GmbH
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Filing: 1987-07-10
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Granted: 1988-06-14
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Expires: 2007-07-10
Abstract
Abstract In order to create a technically more effective and more economical method of decontamination by which complete decomposition of all injurious substances is obtained in simple fashion, it is proposed, in connection with a method and a plant for the treatment of contaminated soils, that the drying can be combined in a mill passed through by hot gases with a crushing of the material to a particle size of 0 to 10 mm, that after the drying the material, together with the gaseous phase, be treated in the form of a solid/gas dispersion in a heating and decontamination path with burner, with a temperature within the range of 800° C. to 1200° C. and then be separated in a cyclone separator stage from the gaseous phase which contains all injurious substances, said phase being recycled with the burner for the complete decomposition of the injurious substances, a partial stream of the combustion gases being fed to the combined drying and comminuting stage and the purified solids being removed after a cooling the cooling air of which is fed to the burner as preheated primary air.
Inventors
- 👤 Hans-Dietmar Maury
- 👤 Wolfgang Buslowski
- 👤 Bernold Kraft
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 08:12
CPC Classifications
F; F23; F23G; F23G7/00; F23G7/14; B; B09; B09C; B09C1/00; B09C1/06; Y; Y10; Y10S; Y10S241/00; Y10S241/10
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
209 words
A method for treatment of contaminated soils and similar material, particularly in coke-oven locations, by removal and decontamination of the material, and refilling of the place of removal with purified earth, in which method the material removed is dried and then treated thermally at a high temperature, comprising the steps of drying the material in a mill and passing hot gases through the mill; comminuting the material in the mill to a particle size of 0 to 10 mm and allowing a substantial part of injurious substances of the material to be transferred into the gaseous phase; after the drying, treating the material together with the gaseous phase in the form of a solid/gas dispersion in a heating and decontamination conduit provided with a burner, the treating being done at a temperature within the range of 800° to 1200° C.; in a cyclone separator stage, separating the material from the gaseous phase which contains injurious substances; recycling the gaseous phase via the burner for a complete decomposition of the injurious substance; feeding a partial stream of the combustion gases back to the mill; cooling purified solids of the material via cooling air, and thereafter removing the solids; and applying the cooling air to the burner as preheated primary air.
Claim 2
Independent Claim
209 words
A method for treatment of contaminated soils and similar material, particularly in coke-oven locations, by removal and decontamination of the material, and refilling of the place of removal with purified earth, in which method the material removed is dried and then treated thermally at a high temperature, comprising the steps of drying the material in a mill and passing hot gases through the mill; comminuting the material in the mill to a particle size of 0 to 10 mm and allowing a substantial part of injurious substances of the material to be transferred into the gaseous phase; after the drying, treating the material together with the gaseous phase in the form of a solid/gas dispersion in a heating and decontamination conduit provided with a burner, the treating being done at a temperature within the range of 800° to 1200° C.; in a cyclone separator stage, separating the material from the gaseous phase which contains injurious substances; recycling the gaseous phase via the burner for a complete decomposition of the injurious substance; feeding a partial stream of the combustion gases back to the mill; cooling purified solids of the material via cooling air, and thereafter removing the solids; and applying the cooling air to the burner as preheated primary air.
Claim 3
Dependent Claim
79 words
The method according to claim 1 wherein between the mill and the decontamination path there is a further cyclone separator stage, the method comprising further steps of adding one part of gas from the further separator stage to the combustion gases for feeding to the mill, and adding the remainder of the gas from the further separator stage directly to the burner; and concurrently thermally treating the solids which have been removed from the material in the decontamination conduit.
Claim 4
Dependent Claim
25 words
The method according to claim 2, further comprising a step, via use of said further cyclone separator stage, of separating contaminated gas from the solids.
Claim 5
Dependent Claim
26 words
The method according to claim 1 further comprising a step, employing the mill, of crushing the material to a particle size of 0 to 3 mm.
Claim 6
Dependent Claim
21 words
The method according to claim 1, wherein said cooling of the solids is effected at a temperature of about 150° C.
Claim 7
Dependent Claim
25 words
The method according to claim 1, wherein said cooling is followed by steps of filtering combustion gases and discharging excess combustion gases to the atmosphere.
Claim 8
Independent Claim
191 words
A system for implementing a process of treating contaminated soils and similar material by removal, decontamination and refilling by employing drying apparatus and an apparatus for the thermal treatment of the material, in combination with a cyclone separator for separating solids from a gaseous phase and a burner to which the gaseous phase is fed, wherein the system comprises a mill which is heated by the combustion gas of the burner and serves as combined drying and comminuting stage, there being a heating and decontamination conduit connecting with the burner; and wherein the mill is heated by the combustion gas of the burner, the conduit including a tube separated from the burner flame for carrying solid/gas dispersion to provide the thermal treatment; the system further comprising a multi-stage cooling device for cooling cleaned solid material; a device for feeding the cooling air from a preheating in the cooling device to the burner; a recycle plant connected between a gas outlet of the cyclone separator and the burner and the decontamination conduit; and a cooling and dust-removing device, there being an outlet of the cooling and dust-removing device for excess combustion gas.
Claim 9
Independent Claim
191 words
A system for implementing a process of treating contaminated soils and similar material by removal, decontamination and refilling by employing drying apparatus and an apparatus for the thermal treatment of the material, in combination with a cyclone separator for separating solids from a gaseous phase and a burner to which the gaseous phase is fed, wherein the system comprises a mill which is heated by the combustion gas of the burner and serves as combined drying and comminuting stage, there being a heating and decontamination conduit connecting with the burner; and wherein the mill is heated by the combustion gas of the burner, the conduit including a tube separated from the burner flame for carrying solid/gas dispersion to provide the thermal treatment; the system further comprising a multi-stage cooling device for cooling cleaned solid material; a device for feeding the cooling air from a preheating in the cooling device to the burner; a recycle plant connected between a gas outlet of the cyclone separator and the burner and the decontamination conduit; and a cooling and dust-removing device, there being an outlet of the cooling and dust-removing device for excess combustion gas.
Claim 10
Dependent Claim
44 words
The system according to claim 7, comprising a further cyclone separator inserted behind the mill and before the decontamination conduit, a gas outlet of the further cyclone separator extending via the tube connecting plant to the burner and the mill in two partial streams.
Claim 11
Dependent Claim
29 words
The system according to claim 7, wherein the cooling device for the purified solids comprises three cooling stages each having a cooling path followed by a cyclone separator stage.
Claim 12
Dependent Claim
21 words
The system according to claim 7, further comprising a conveyor worm connected to the cooling device for removal of the solids.
Claim 13
Dependent Claim
25 words
The system according to claim 7, wherein the cooling and dust-removal device for excess combustion gas comprises a plurality of evaporation coolers followed by filters.
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) | 1991-06-14 | 1991-12-14 | 1992-06-14 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1995-06-14 | 1995-12-14 | 1996-06-14 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1999-06-14 | 1999-12-14 | 2000-06-14 | $7700.00 | Window Closed / Lapsed |