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US4931265A Expired / Lapsed US ⏱️ 0.0 years remaining

Conditioning process for dust-containing waste gas

Assignee: GEA Group AG
•
Filing: 1988-02-03
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Granted: 1990-06-05
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Expires: 2008-02-03
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Abstract

Abstract Disclosed is an improved process for the production of a sulfur trioxide conditioning gas, which consists in compensating the faulty "ambient gas temperature" in a simple and effective manner, such that all of the subsequent functions can take place at the established optimum temperature and can no longer be adversely affected by fluctuations in the ambient air temperature.

Inventors

  • 👤 Wilhelm Leussler

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 03:04
CPC Classifications
C; C01; C01B; C01B17/00; C01B17/69; C01B17/74; C01B17/76; B; B03; B03C; B03C3/00; B03C3/01; B03C3/013; Y; Y02; Y02P; Y02P20/00; Y02P20/10; Y02P20/129

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 241 words
A process for conditioning a dust containing gas stream prior to its introduction into an electrostatic separator comprising: introducing molten sulfur into a furnace; introducing combustion air into said furnace at a constant rate in an amount of 4.5 to 5 times that required for stoichiometric combustion of the maximum sulfur rate; combusting said sulfur in said furnace to produce a gas mixture containing air and SO 2 ; exhausting the gas mixture from the furnace; introducing said gas mixture into a catalytic converter; converting SO 2 to SO 3 in said catalytic converter; exhausting an SO 3 -containing gas stream from the catalytic converter; introducing the SO 3 -containing gas stream into the dust containing gas through distribution means; interrupting the sulfur feed when the temperature in the area of the distribution means falls below a critical value, the critical value being determined so as to avoid sulfuric acid corrosion; measuring a parameter of the gas stream when exhausted from the electrostatic separator and controlling the introduction of sulfur into said furnace in dependence on the measurement; maintaining a constant amount of thermal energy supplied to the furnace by controlling the sulfur feed rate and by controlling an amount of preheat added in a preheater to the combustion air prior to its introduction into said furnace, the amount of preheat being controlled in dependence on the sulfur feed rate; and regulating the temperature of combustion air supplied to the preheater.
Claim 2
Dependent Claim 241 words
A process for conditioning a dust containing gas stream prior to its introduction into an electrostatic separator comprising: introducing molten sulfur into a furnace; introducing combustion air into said furnace at a constant rate in an amount of 4.5 to 5 times that required for stoichiometric combustion of the maximum sulfur rate; combusting said sulfur in said furnace to produce a gas mixture containing air and SO 2 ; exhausting the gas mixture from the furnace; introducing said gas mixture into a catalytic converter; converting SO 2 to SO 3 in said catalytic converter; exhausting an SO 3 -containing gas stream from the catalytic converter; introducing the SO 3 -containing gas stream into the dust containing gas through distribution means; interrupting the sulfur feed when the temperature in the area of the distribution means falls below a critical value, the critical value being determined so as to avoid sulfuric acid corrosion; measuring a parameter of the gas stream when exhausted from the electrostatic separator and controlling the introduction of sulfur into said furnace in dependence on the measurement; maintaining a constant amount of thermal energy supplied to the furnace by controlling the sulfur feed rate and by controlling an amount of preheat added in a preheater to the combustion air prior to its introduction into said furnace, the amount of preheat being controlled in dependence on the sulfur feed rate; and regulating the temperature of combustion air supplied to the preheater.
Claim 3
Dependent Claim 28 words
The process of claim 1 wherein the amount of combustion air is regulated to a constant value by way of an aperture or orifice and a regulating valve.
Claim 4
Dependent Claim 30 words
The process of claim 1 wherein the temperature of the air introduced into the preheater is regulated in dependence on a temperature measured between an auxiliary-air heater and the preheater.
Claim 5
Dependent Claim 34 words
The process of claim 3 wherein a constant temperature is preset to a value which corresponds to that value reached without any preheating by the auxiliary air heater in case of maximum ambient temperature.
Claim 6
Dependent Claim 21 words
The process of claim 1 further comprising cooling the furnace when a temperature in the furnace indicates an overheated condition therein.
Claim 7
Dependent Claim 32 words
The process of claim 5 wherein the furnace is cooled by an air stream from the same source as the combustion air but which has by-passed the heater, preheater and regulating valve.
Claim 8
Dependent Claim 27 words
The process of claim 1 wherein the SO 3 requirement is determined by a measuring of the dust content in the gas out of the electrostatic separator.
Claim 9
Dependent Claim 22 words
The process of claim 1 wherein the SO 3 requirement is determined by measuring the gas amount out of the electrostatic separator.
Claim 10
Dependent Claim 35 words
The process of claim 1 wherein the sulfur feed rate is determined by measuring the amount of dust containing gas to be treated and the dust content in the gas stream leaving the electrostatic precipitator.
Claim 11
Dependent Claim 63 words
The process of claim 1 wherein the temperature of the gas stream is measured downstream of the converter prior to the distribution means and in the case of exceeding a preset limit immediately (a) the sulfur supply to the furnace is interrupted (b) any air preheating is stopped and (c) the duct by-passing the air preheaters and the regulating valve is completely opened.
Claim 12
Dependent Claim 22 words
The process of claim 1 wherein the temperature in the region of the distribution means is below said critical value during start-up.

References Cited (Backward Citations)

CA119878A Cited
US3517162A Cited
US3993429A Cited
US3993429B1 Cited
US4213447A Cited
SU789386A1 Cited
US4290480A Cited
EP0062930A1 Cited
US4466815A Cited
US4604516A Cited
US4706736A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1993-06-04 1993-12-04 1994-06-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1997-06-04 1997-12-04 1998-06-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2001-06-04 2001-12-04 2002-06-05 $7700.00 Window Closed / Lapsed

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