US4062926A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Sulfur dioxide removal using thermally crushed nahcolite
Assignee: ExxonMobil Oil Corp
•
Filing: 1975-03-19
•
Granted: 1977-12-13
•
Expires: 1995-03-19
Abstract
Abstract Sulfur dioxide is removed from a gas stream, such as that generated by the combustion of a sulfur-containing fuel or ore processing, by introducing particulate nahcolite into the gas stream in a high temperature zone. The high temperature zone provides an environment for the size reduction of the particulate nahcolite and an effective environment for the removal of the sulfur dioxide. The size reduction of particulate nahcolite is accomplished by a thermal crushing process.
Inventors
- 👤 John H. Knight
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-06 22:50
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/508
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
191 words
A method of removing sulfur dioxide from a gas stream generated by the combustion of a sulfur-containing fuel, comprising: generating a gas stream containing sulfur dioxide by the combustion of a sulfur-containing fuel in a high temperature combustion zone; maintaining said high temperature combustion zone at a temperature of from about 2,000° F. to about 4,000° F. by said combustion; introducing into said gas stream in said high temperature combustion zone an amount of nahcolite sufficient to provide a stoichiometric ratio of nahcolite to sulfur dioxide of from about 0.9 to about 3.0; thermally crushing said particulate nahcolite to a predominant particle size of from about 0.1 to about 100 microns and a mean particle size of less than 10.8 microns by contacting said particulate nahcolite with said gas stream in said high temperature combustion zone; allowing said thermally crushed nahcolite and said gas stream to remain in contact in said high temperature combustion zone for a time effective to combine at least some of the sulfur dioxide in said gas stream with said thermally crushed nahcolite; and removing said thermally crushed nahcolite with combined sulfur dioxide from said gas stream.
Claim 2
Independent Claim
191 words
A method of removing sulfur dioxide from a gas stream generated by the combustion of a sulfur-containing fuel, comprising: generating a gas stream containing sulfur dioxide by the combustion of a sulfur-containing fuel in a high temperature combustion zone; maintaining said high temperature combustion zone at a temperature of from about 2,000° F. to about 4,000° F. by said combustion; introducing into said gas stream in said high temperature combustion zone an amount of nahcolite sufficient to provide a stoichiometric ratio of nahcolite to sulfur dioxide of from about 0.9 to about 3.0; thermally crushing said particulate nahcolite to a predominant particle size of from about 0.1 to about 100 microns and a mean particle size of less than 10.8 microns by contacting said particulate nahcolite with said gas stream in said high temperature combustion zone; allowing said thermally crushed nahcolite and said gas stream to remain in contact in said high temperature combustion zone for a time effective to combine at least some of the sulfur dioxide in said gas stream with said thermally crushed nahcolite; and removing said thermally crushed nahcolite with combined sulfur dioxide from said gas stream.
Claim 3
Dependent Claim
27 words
The method of claim 1, wherein said thermally crushed nahcolite contacts the gas stream containing sulfur dioxide impurities for a period of up to about ten seconds.
Claim 4
Dependent Claim
18 words
The method of claim 2, wherein the period of contact is from about one to about six seconds.
Claim 5
Dependent Claim
22 words
The method of claim 1, wherein said particulate nahcolite is introduced into the combustion zone by mixing with the combustion zone fuel.
Claim 6
Dependent Claim
22 words
The method of claim 1, wherein said particulate nahcolite is introduced into the combustion zone by mixing with primary or secondary air.
References Cited (Backward Citations)
US3505008A
Cited
US3880629A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-12-12 | 1981-06-13 | 1981-12-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-12-12 | 1985-06-13 | 1985-12-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-12-12 | 1989-06-13 | 1989-12-13 | $7700.00 | Window Closed / Lapsed |