Patent US4910011A successfully refreshed from Google Patents.
US4910011A
Expired / Lapsed
US
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Process of purifying flue gases
Assignee: STADTWERKE MUNSTER A GERMAN CORP GmbH
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Filing: 1988-12-14
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Granted: 1990-03-20
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Expires: 2008-12-14
Abstract
Abstract In flue gases or other humid exhaust gases which are relatively cold and contain SO 2 , NO 2 and other gaseous pollutants, the SO 2 content is oxidized to SO 3 and the NO content is reduced by a catalytic treatment, the SO 3 content is condensed as sulfuric acid and other gaseous pollutants are removed by being scrubbed with aqueous liquids at low temperatures. In order to heat up the flue gas to the temperature required for the catalysis, the flue gas is heated up in a first heating-up stage by an indirect heat exchange with the catalytically treated gas before the catalytic treatment, the heated-up gas is heated up further in a second heating-up stage to the temperature required for the catalytic treatment, the catalytically treated gas which has been cooled in the first heating-up stage is cooled further in an indirect heat exchanger below the dew point temperature of sulfuric acid and is subsequently fed to an SO 3 condenser. The remaining sulfuric acid vapor is absorbed by sprayed dilute sulfuric acid to form a dilute sulfuric acid having a predetermined concentration, the gas leaving the SO 3 condenser is scrubbed in a scrubber with a sprayed aqueous liquid and is thus cooled to 40° to 60° C. and the purified gas is reheated to the required chimney inlet temperature.
Inventors
- 👤 Karl-Heinz Dorr
- 👤 Hugo Grimm
- 👤 Heinz Neumann
- 👤 Norbert Olhms
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 05:17
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/74; B01D53/86; B01D53/8637
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
216 words
In a process of purifying flue gases or other humid exhaust gases which contain SO 2 , NO x and other gaseous pollutants including HCl and HF, comprising oxidizing the SO 2 content to SO 3 reducing the NO x content by a catalytic treatment, condensing the SO 3 content as sulfuric acid and removing other gaseous pollutants including HCl and HF by scrubbing with aqueous liquids at low temperatures, the improvement comprising prior to the catalytic treatment heating up the flue gas in a first heating-up stage by an indirect heat exchange with catalytically treated gas from the catalytic treatment, heating up the heated-up gas from the first heating-up stage in a second heating-up stage to a temperature sufficient to conduct the catalytic treatment, cooling the catalytically treated gas in the first heating-up stage in an indirect heat exchanger below the dew point temperature of sulfuric acid and subsequently feeding same to an SO 3 condenser, absorbing the remaining sulfuric acid vapor by sprayed dilute sulfuric acid to form a dilute sulfuric acid, scrubbing the gas leaving the SO 3 condenser in a scrubber with a sprayed aqueous liquid and cooling same to 40° to 60° C., reheating the purified gas to a sufficient chimney inlet temperature for venting the purified gas from a chimney.
Claim 2
Dependent Claim
216 words
In a process of purifying flue gases or other humid exhaust gases which contain SO 2 , NO x and other gaseous pollutants including HCl and HF, comprising oxidizing the SO 2 content to SO 3 reducing the NO x content by a catalytic treatment, condensing the SO 3 content as sulfuric acid and removing other gaseous pollutants including HCl and HF by scrubbing with aqueous liquids at low temperatures, the improvement comprising prior to the catalytic treatment heating up the flue gas in a first heating-up stage by an indirect heat exchange with catalytically treated gas from the catalytic treatment, heating up the heated-up gas from the first heating-up stage in a second heating-up stage to a temperature sufficient to conduct the catalytic treatment, cooling the catalytically treated gas in the first heating-up stage in an indirect heat exchanger below the dew point temperature of sulfuric acid and subsequently feeding same to an SO 3 condenser, absorbing the remaining sulfuric acid vapor by sprayed dilute sulfuric acid to form a dilute sulfuric acid, scrubbing the gas leaving the SO 3 condenser in a scrubber with a sprayed aqueous liquid and cooling same to 40° to 60° C., reheating the purified gas to a sufficient chimney inlet temperature for venting the purified gas from a chimney.
Claim 3
Dependent Claim
167 words
A process according to claim 1, wherein the reheating of the purified gas to the chimney inlet temperature comprises reheating by a direct heat exchange with dilute sulfuric acid from the SO 3 condenser in a reheater, spraying dilute sulfuric acid from the reheater into the SO 3 condenser, cooling the catalytically treated gas in the indirect heat exchanger by a heat exchange with air or water, selecting the temperature of the purified gas in the reheater such that the water that has been absorbed in the scrubber will not condense and will remain in the exiting gas, adjusting the gas exit temperature from the indirect heat exchanger so that the temperature of the dilute sulfuric acid obtained in the SO 3 condenser approximately corresponds to the temperature of the purified gas in the reheater, and spraying sulfuric acid into the reheater at such a rate that the dilute sulfuric acid drained from the reheater is approximately at the gas exit temperature from the SO 3 condenser.
Claim 4
Dependent Claim
24 words
A process according to claim 2, further comprising increasing the temperature of the gas exiting from the reheater by an admixing of hot gas.
Claim 5
Dependent Claim
32 words
A process according to claim 1 or 2, further comprising increasing the temperature of the dilute sulfuric acid fed from the SO 3 condenser to the reheater by an indirect heat exchange.
Claim 6
Dependent Claim
44 words
A process according to claim 1, further comprising providing the dilute sulfuric acid with a concentration of 60 to 75% by weight and the dilute sulfuric acid fed from the SO 3 condenser to the reheater at a temperature from 70° to 110° C.
Claim 7
Dependent Claim
27 words
A process according to claim 1, further comprising reheating the purified gas to the chimney inlet temperature by an indirect heat exchange with the catalytically treated gas.
Claim 8
Dependent Claim
30 words
A process according to claim 6, further comprising providing the dilute sulfuric acid with a concentration of 60 to 90% by weight and a temperature of 100° to 140° C.
Claim 9
Dependent Claim
28 words
A process according to claim 1, wherein the aqueous liquid sprayed into the fine scrubber contains H 2 O 2 or H 2 S 2 O 8 .
Claim 10
Dependent Claim
26 words
A process according to claim 1, wherein the flue gas is heated up to a temperature of 400° to 530° C. in the first heating-up stage.
Claim 11
Dependent Claim
26 words
A process according to claim 1, wherein the catalytically treated gas is cooled to a temperature of 120° to 160° C. in the indirect heat exchanger.
Claim 12
Dependent Claim
46 words
A process according to claim 1, further comprising producing a subatmospheric pressure by a fan which precedes the chimney and automatically controlling the fan so that atmospheric pressure is obtained at least in a line for feeding the catalytically treated gas to the indirect heat exchanger.
References Cited (Backward Citations)
US3607034A
Cited
US3647360A
Cited
DE3407277A1
Cited
DE3514711A1
Cited
DE3601378A1
Cited
US4744967A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1993-03-19 | 1993-09-18 | 1994-03-20 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1997-03-19 | 1997-09-18 | 1998-03-20 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2001-03-19 | 2001-09-18 | 2002-03-20 | $7700.00 | Window Closed / Lapsed |