US4478810A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of treating final products from flue gas desulfurization
Assignee: Hitachi Zosen Inova Steinmueller GmbH
•
Filing: 1982-08-31
•
Granted: 1984-10-23
•
Expires: 2002-08-31
Abstract
Abstract A method of treating final products from a flue gas desulfurization. The flue gas desulfurization is carried out by the absorption of sulfur oxide in a spray dryer with a suspension which contains lime, or in a reactor with a dry, fine-grained, absorbent which contains lime. Prior to desulfurization, the fly ash carried along by the flue gas which is to be desulfurized is separated entirely, partially, or not at all from the flue gas, and the final products from the flue gas desulfurization, prior to any further treatment thereof, amount to 1-99% by weight, preferably 1-70% by weight, of fly ash, and 1-99% by weight, preferably 30-99% by weight, of the sum of the desulfurization products, preferably calcium sulfite hemihydrate, and/or calcium sulfite, and/or calcium sulfate dyhydrate, and/or calcium sulfate hemihydrate, and/or calcium sulfate, as well as residue of the absorbent. The reduction of the amount of calcium sulfite is implemented by a dry oxidation with air.
Inventors
- 👤 Wolfgang Bloss
- 👤 Ulrich Mohn
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-02 20:18
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/508; B01D53/501
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
211 words
A method of treating products resulting from a flue gas desulfurization, said method of treating being effective externally of a combustion chamber and for producing an industrially usable calcium sulfate anhydrite construction material comprising in combination the steps of: at least partially separating out fly ash from the flue gas which is to be desulfurized; thereupon carrying out desulfurization of flue gas by absorption of sulfur oxide with a lime-containing absorbent to produce products which, prior to any further treatment thereof, contain at least some calcium sulfite therewith, and in particular contain 1-70% by weight fly ash, and 30-99% by weight of the sum of the desulfurization products and residue of said absorbent; said desulfurization products including at least one of the group consisting of calcium sulfite hemihydrate, calcium sulfite, calcium sulfate dyhydrate, calcium sulfate hemihydrate, and calcium sulfate; thereafter effecting a reduction of the amount of calcium sulfite by means of a dry oxidation with air of said products to obtain a difficult to dissolve calcium sulfate anhydrite employable for the construction industry; carrying out said oxidation only at temperatures in a range between 400° C. and 600° C.; and at least partially meeting the energy requirement necessary for said oxidation by supplying hot flue gases to the dry oxidation.
Claim 2
Independent Claim
211 words
A method of treating products resulting from a flue gas desulfurization, said method of treating being effective externally of a combustion chamber and for producing an industrially usable calcium sulfate anhydrite construction material comprising in combination the steps of: at least partially separating out fly ash from the flue gas which is to be desulfurized; thereupon carrying out desulfurization of flue gas by absorption of sulfur oxide with a lime-containing absorbent to produce products which, prior to any further treatment thereof, contain at least some calcium sulfite therewith, and in particular contain 1-70% by weight fly ash, and 30-99% by weight of the sum of the desulfurization products and residue of said absorbent; said desulfurization products including at least one of the group consisting of calcium sulfite hemihydrate, calcium sulfite, calcium sulfate dyhydrate, calcium sulfate hemihydrate, and calcium sulfate; thereafter effecting a reduction of the amount of calcium sulfite by means of a dry oxidation with air of said products to obtain a difficult to dissolve calcium sulfate anhydrite employable for the construction industry; carrying out said oxidation only at temperatures in a range between 400° C. and 600° C.; and at least partially meeting the energy requirement necessary for said oxidation by supplying hot flue gases to the dry oxidation.
Claim 3
Independent Claim
210 words
A method of treating products resulting from a flue gas desulfurization, said method of treating being effective externally of a combustion chamber and for producing an industrially usable calcium sulfate anhydrite construction material comprising in combination the steps of: at least partially separating out fly ash from the flue gas which is to be desulfurized; thereupon carrying out desulfurization of flue gas by absorption of sulfur oxide with a lime-containing absorbent to produce products which, prior to any further treatment thereof, contain at least some calcium sulfite therewith, and in particular contain 1-70% by weight fly ash, and 30-99% by weight of the sum of the desulfurization products and residue of said absorbent; said desulfurization products including at least one of the group consisting of calcium sulfite hemihydrate, calcium sulfite, calcium sulfate dyhydrate, calcium sulfate hemihydrate, and calcium sulfate; thereafter effecting a reduction of the amount of calcium sulfite by means of a dry oxidation with air of said products to obtain a difficult to dissolve calcium sulfate anhydrite employable for the construction industry; carrying out said oxidation only at temperatures in a range between 400° C. and 600° C.; and at least partially meeting the energy requirement necessary for said oxidation by supplying combustion air to the dry oxidation.
Claim 4
Independent Claim
210 words
A method of treating products resulting from a flue gas desulfurization, said method of treating being effective externally of a combustion chamber and for producing an industrially usable calcium sulfate anhydrite construction material comprising in combination the steps of: at least partially separating out fly ash from the flue gas which is to be desulfurized; thereupon carrying out desulfurization of flue gas by absorption of sulfur oxide with a lime-containing absorbent to produce products which, prior to any further treatment thereof, contain at least some calcium sulfite therewith, and in particular contain 1-70% by weight fly ash, and 30-99% by weight of the sum of the desulfurization products and residue of said absorbent; said desulfurization products including at least one of the group consisting of calcium sulfite hemihydrate, calcium sulfite, calcium sulfate dyhydrate, calcium sulfate hemihydrate, and calcium sulfate; thereafter effecting a reduction of the amount of calcium sulfite by means of a dry oxidation with air of said products to obtain a difficult to dissolve calcium sulfate anhydrite employable for the construction industry; carrying out said oxidation only at temperatures in a range between 400° C. and 600° C.; and at least partially meeting the energy requirement necessary for said oxidation by supplying combustion air to the dry oxidation.
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) | 1987-10-23 | 1988-04-23 | 1988-10-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-10-23 | 1992-04-23 | 1992-10-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-10-23 | 1996-04-23 | 1996-10-23 | $7700.00 | Window Closed / Lapsed |