US4152399A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process and apparatus for thermally purifying effluent gases
Assignee: Bayer AG
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Filing: 1977-08-08
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Granted: 1979-05-01
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Expires: 1997-08-08
Abstract
Abstract In the thermal purification of effluent gases charged with noxious substances by burning them with air at high temperatures, the improvement which comprises drawing the effluent gases charged with noxious substances through a zone established by a device which provides protection against back-firing and a combustion zone which is resistant to bursts of pressure of up to about 10 bars, and burning the effluent gases in the combustion zone at a temperature of about 800° to 1000° C. To carry out the process there is provided an apparatus comprising a back-firing safety device followed by a heat exchanger and then a combustion chamber. Components of the heat exchanger are made resistant to pressures of up to about 10 bars and the safety device prevents back-firing to the plant wherein the effluent gases are produced.
Inventors
- 👤 Rolf Germerdonk
- 👤 Werner Huning
- 👤 Rudolf Cirkel
- 👤 Gunter Brinkmann
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 17:35
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; F; F23; F23D; F23D14/00; F23D14/46; F23D14/72; F23D14/82; F23G; F23G5/00; F23G5/50; F23G7/00; F23G7/06; F23G7/061; F23G7/065; F23G7/066; F23G2208/00
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
149 words
In the thermal purification of effluent gases charged with combustible noxious substances, wherein the composition of the effluent gas may happen to exceed the explosive limit, by drawing the effluent gas through a zone established by a device which provides protection against back-firing and burning them with air at high temperatures, the improvement which comprises preheating the effluent gas after having passed the device for protection against back-firing by indirect heat-exchange with purified gas after combustion, and burning the effluent gas in a combustion zone at a temperature of about 800°-1000° C., the combustion zone, heat-exchange zone and connecting tubes therebetween being resistant to bursts of pressure of up to 10 bars, the connecting tubes having straight lengths of at most 5× the diameter of the tubes and the heat-exchange zone containing bursting plates which, in the event of an explosion, break down thereby avoiding backward propagation of pressure.
Claim 2
Dependent Claim
149 words
In the thermal purification of effluent gases charged with combustible noxious substances, wherein the composition of the effluent gas may happen to exceed the explosive limit, by drawing the effluent gas through a zone established by a device which provides protection against back-firing and burning them with air at high temperatures, the improvement which comprises preheating the effluent gas after having passed the device for protection against back-firing by indirect heat-exchange with purified gas after combustion, and burning the effluent gas in a combustion zone at a temperature of about 800°-1000° C., the combustion zone, heat-exchange zone and connecting tubes therebetween being resistant to bursts of pressure of up to 10 bars, the connecting tubes having straight lengths of at most 5× the diameter of the tubes and the heat-exchange zone containing bursting plates which, in the event of an explosion, break down thereby avoiding backward propagation of pressure.
Claim 3
Dependent Claim
190 words
In an apparatus for thermally purifying effluent gases, comprising a combustion chamber, means for supplying effluent gases to said chamber, a heat exchanger for preheating the effluent gases with purified gases after combustion, and means for venting purified gases after heat exchange, the improvement which comprises a backfiring safety device located upstream of the heat exchanger, the heat exchanger being formed of normal steel and comprising inlet and outlet domes, a casing between said domes internally insulated with a compressed layer of ceramic fiber, a bellows expansion joint connecting said outlet dome with said casing, a plurality of tubes extending longitudinally within said casing, a tube plate adjacent the outlet dome except for passage of gas through said tubes, and a pair of bursting plates respectively adjacent the inlet and outlet domes at an angle of 90° to the direction of explosive thrust, the circumferences of the bursting plates corresponding to those of the tube plates so as to provide unobstructed pressure release, the domes, heat exchanger casing, tubes, tube plates and bellows joint being resistant to pressure of up to about 10 bars at temperatures up to 600° C.
Claim 4
Dependent Claim
190 words
In an apparatus for thermally purifying effluent gases, comprising a combustion chamber, means for supplying effluent gases to said chamber, a heat exchanger for preheating the effluent gases with purified gases after combustion, and means for venting purified gases after heat exchange, the improvement which comprises a backfiring safety device located upstream of the heat exchanger, the heat exchanger being formed of normal steel and comprising inlet and outlet domes, a casing between said domes internally insulated with a compressed layer of ceramic fiber, a bellows expansion joint connecting said outlet dome with said casing, a plurality of tubes extending longitudinally within said casing, a tube plate adjacent the outlet dome except for passage of gas through said tubes, and a pair of bursting plates respectively adjacent the inlet and outlet domes at an angle of 90° to the direction of explosive thrust, the circumferences of the bursting plates corresponding to those of the tube plates so as to provide unobstructed pressure release, the domes, heat exchanger casing, tubes, tube plates and bellows joint being resistant to pressure of up to about 10 bars at temperatures up to 600° C.
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) | 1982-04-30 | 1982-10-30 | 1983-05-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-04-30 | 1986-10-30 | 1987-05-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-04-30 | 1990-10-30 | 1991-05-01 | $7700.00 | Window Closed / Lapsed |