US4424197A
Expired / Lapsed
US
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Gas desulfurization
Assignee: United States Gypsum Co
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Filing: 1982-09-29
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Granted: 1984-01-03
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Expires: 2002-09-29
Abstract
Abstract A process for adsorbing sulfur dioxide from a gas comprising contacting a gas containing SO 2 , such as a flue gas, with about stoichiometric amounts of a specially prepared calcium oxide so that substantially all of the sulfur dioxide content is reacted throughout the calcium oxide particle to form a calcium sulfate reaction product. The useful calcium oxide particles comprise a highly voided skeletal structure of very large surface area and large pore volume with numerous macro pores. Such particles are obtained by flash calcining sand-size grains of calcium carbonate, such as aragonite, calcite or dolomite.
Inventors
- 👤 Byron E. Powell
- 👤 Virendar S. Bakhshi
- 👤 Donald A. Randolph
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 18:49
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/50; B01D53/508; C; C01; C01F; C01F11/00; C01F11/46; C01F11/464; C01P; C01P2004/00; C01P2004/01; C01P2006/00; C01P2006/10; C01P2006/12; C01P2006/14; C01P2006/16
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
111 words
A process for decontaminating a SO 2 containing gas wherein such gas also containing oxygen is contacted at a temperature between about 500° C. and 1000° C. with calcium oxide particles; such particles being in a highly voided skeletal structure containing numerous macro pores in the walls of large pores such that the pores of the particles have a total pore volume to weight ratio of at least about 0.4 cubic centimeters per gram and total pore surface area to weight ratio of at least about 0.5 square meters per gram measured by mercury porosimetry; and reacting SO 2 throughout the calcium oxide particle to form a calcium sulfate reaction product.
Claim 2
Dependent Claim
111 words
A process for decontaminating a SO 2 containing gas wherein such gas also containing oxygen is contacted at a temperature between about 500° C. and 1000° C. with calcium oxide particles; such particles being in a highly voided skeletal structure containing numerous macro pores in the walls of large pores such that the pores of the particles have a total pore volume to weight ratio of at least about 0.4 cubic centimeters per gram and total pore surface area to weight ratio of at least about 0.5 square meters per gram measured by mercury porosimetry; and reacting SO 2 throughout the calcium oxide particle to form a calcium sulfate reaction product.
Claim 3
Dependent Claim
43 words
The process of claim 1 in which the skeletal calcium oxide has a median pore diameter as determined by total surface area of less than 2 micrometers and a median pore diameter as determined by total pore volume of greater than 0.8 micrometers.
Claim 4
Dependent Claim
46 words
The process of claim 1 in which the skeletal calcium oxide has a total pore volume to weight of at least about 0.5 cubic centimeters per gram and at least 40% of the cumulative pore volume comprises pores having a diameter between 0.3 and 0.8 micrometers.
Claim 5
Dependent Claim
45 words
The process of claim 1 in which the bulk density of the calcium oxide particles is less than 1 gram per cubic centimeter and the skeletal density, of the bulk density adjusted for pore volume measured at 4000 psia mercury, is greater than 2.6 g/cc.
Claim 6
Dependent Claim
15 words
The process of claim 1 in which the temperature is about 800° to 850° C.
Claim 7
Dependent Claim
46 words
The process of claim 1 wherein the flue gas contains about 0.01 to 3% SO 2 and the flue gas is circulated through a bed of said calcium oxide in a manner to expose about 1 mole of CaO for each mole of SO 2 .
Claim 8
Dependent Claim
21 words
The process of claim 6 wherein such contacting is continued until all of the calcium oxide is converted into calcium sulfate.
Claim 9
Dependent Claim
161 words
A process for continuously decontaminating SO 2 containing flue gas derived from burning fossil fuels comprising: continuously passing such flue gas in about stoichiometric proportions through a bed of calcium oxide particles, at a temperature between 750° and 860° C.; such CaO particles being in the form of a highly voided skeletal structure of bulk density less than 1 gram per cc and such that the particles have a total pore volume of at least about 0.5 cubic centimeters per gram, total surface area of at least 2 square meters per gram, median pore diameter by area of less than 2 micrometers, median pore diameter by volume greater than 0.8 micrometers and apparent skeletal density of at least about 2.7 so that substantially all of the SO 2 content is reacted throughout the CaO particle forming a CaSO 4 reaction product; continuously venting SO 2 free gaseous flow of flue gas; and periodically replenishing the fluidized bed with such CaO particles.
Claim 10
Dependent Claim
161 words
A process for continuously decontaminating SO 2 containing flue gas derived from burning fossil fuels comprising: continuously passing such flue gas in about stoichiometric proportions through a bed of calcium oxide particles, at a temperature between 750° and 860° C.; such CaO particles being in the form of a highly voided skeletal structure of bulk density less than 1 gram per cc and such that the particles have a total pore volume of at least about 0.5 cubic centimeters per gram, total surface area of at least 2 square meters per gram, median pore diameter by area of less than 2 micrometers, median pore diameter by volume greater than 0.8 micrometers and apparent skeletal density of at least about 2.7 so that substantially all of the SO 2 content is reacted throughout the CaO particle forming a CaSO 4 reaction product; continuously venting SO 2 free gaseous flow of flue gas; and periodically replenishing the fluidized bed with such CaO particles.
References Cited (Backward Citations)
US3718453A
Cited
US3781408A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
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| 3.5 Years (Year 4) | 1987-01-02 | 1987-07-04 | 1988-01-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-01-02 | 1991-07-04 | 1992-01-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-01-02 | 1995-07-04 | 1996-01-03 | $7700.00 | Window Closed / Lapsed |