Activation of calcium oxide as a sorbent

• US 4,226,839 A
• Filed: 07/21/1978
• Issued: 10/07/1980
• Est. Priority Date: 07/21/1978
• Status: Expired due to Term

• Current Assignee: United States Environmental Protection Agency
• Original Assignee: United States Environmental Protection Agency
• Inventors: Keairns, Dale L., O'Neill, Eoin P.
• Primary Examiner(s): Langel, Wayne A.
• Application Number:
  US05/926,925
• Time in Patent Office: 809 Days
• Field of Search: 423/175, 423/177, 423/635, 423/637, 432/24
• US Class Current: 423/177
• CPC Class Codes: B01D 53/02 by adsorption, e.g. preparative gas chromatography solid sorbent compositions B01J20/00, preparation of inorganic compounds or elements C01
• CPC Class Codes: B01J 20/041 Oxides or hydroxides
• CPC Class Codes: B01J 20/3078 Thermal treatment, e.g. calcining or pyrolizing
• CPC Class Codes: C01F 11/06 of carbonates
• CPC Class Codes: C01F 11/464 Sulfates of Ca from gases containing sulfur oxides

Abstract

The sorbent capacity of calcium oxide with respect to sulfur dioxide is increased by calcining limestone or dolomite in an atmosphere where the partial pressure of carbon dioxide is greater than 40 percent of the equilibrium partial pressure of carbon dioxide over calcium carbonate at the reaction temperature. Where dolomite is the starting material, it may be calcined in a two-step heating process in which the atmosphere during the first heating stage contains carbon dioxide and the temperature is maintained in the dissociation range of magnesium carbonate (M_g CO₃); the atmosphere of the second heating stage also contains carbon dioxide, but the temperature is maintained in the calcium carbonate (CaCO₃) dissociation range. Calcium oxide so produced in such an atmosphere of carbon dioxide sufficient to delay calcination is found to have relatively large mouthed pores capable of sorbing increased amounts of sulfur.

Claims

1. A method for producing calcium oxide of increased sorbent capacity with respect to sulfur dioxide which comprises:

heating stones of particle size 400-1000 microns containing calcium carbonate, at about 900°

C. for a time sufficient to effect decomposition of the CaCO₃ to CaO, in a calcination delaying atmosphere containing carbon dioxide where the partial pressure of the carbon dioxide is greater than 40 percent and up to 85 percent the equilibrium partial pressure of carbon dioxide over calcium carbonate at the reaction temperature, to cause a back pressure of CO₂ sufficient to convert initially formed fine pores of CaO to coalesce into larger pores.

2. The method of claim 1 where the stones are limestones.

3. A method in accordance with claim 1, wherein calcination is carried out for 40 minutes to 4 hours.

4. A method in accordance with claim 1 wherein calcination is carried out for 80 minutes to 2 hours.

5. A method in accordance with claim 1 further comprising the subsequent step of recovering the calcium oxide thus produced.

6. A method of producing calcium oxide of increased sorbent capacity with respect to sulfur dioxide from stones of 400-2000 microns particle size containing calcium carbonate and magnesium carbonate, which comprises:

a. heating said stones at 700°

up to 900°

C. in an atmosphere in which the partial pressure of carbon dioxide is greater than the equilibrium partial pressure of CO₂ over CaCO₃ at the reaction temperature to calcine the magnesium fraction of the stones; and

,

b. additionally heating said stones in an atmosphere containing an amount sufficient of carbon dioxide to delay calcination and for a time sufficient to cause sufficient CO₂ back pressure to produce large mouthed pores, at a temperature greater than that in step (a) in the range 900°

-950°

C. for a time sufficient to effect decomposition of the CaCO₃ to CaO, the CO₂ partial pressure being greater than 40% but not exceeding 85% of the equilibrium partial pressure of CO₂ over CaCO₃ at the reaction temperature.

7. The method of claim 6 where step (a) is performed until substantially all of the magnesium fraction is calcined and step (b) is performed until substantially all of the calcium fraction is calcined.

8. The method of claim 6 where the temperature in step (a) is in the dissociation temperature range of magnesium carbonate in dolomite and the temperature in step (b) is in the dissociation temperature range of calcium carbonate.

9. The method of claim 6 where the partial pressure of carbon dioxide in step (a) is about 1 atmosphere and in step (b) is about 1/2 atmosphere.

10. A method in accordance with claim 6 wherein step (b) is carried out for about 1 hour.