Sorbent composition for an electrostatic precipitator

Patent metadata

Field	Value
Publication number	US-10874975-B2
Application number	US-201816032152-A
Country	US
Kind code	B2
Filing date	Jul 11, 2018
Priority date	Jul 11, 2018
Publication date	Dec 29, 2020
Grant date	Dec 29, 2020

Abstract

A powdery calcium-magnesium compound used as a sorbent composition in flue gas treatment, compatible with electrostatic precipitators. The calcium magnesium compound is doped with calcium nitrate or nitric acid to reduce the electrical resistivity of the particles, increasing their collection efficiency.

First claim

What is claimed is:

1. A powdery calcium-magnesium compound comprising at least a calcium-magnesium hydroxide content greater or equal to 80 weight %, with respect to the total weight of the powdery calcium-magnesium compound characterized in that it presents a resistivity at 300° C. (572° F.) (R300) lower than 1E11(1×10 11 ) Ohms·cm and higher than 1E7(1×10 7 ) Ohms·cm; and
wherein the powdery calcium-magnesium compound is doped with calcium nitrate at an amount greater than or equal to 0.05 weight % and lower or equal to 5 weight % with respect to the total weight of the powdery calcium-magnesium compound.

2. A powdery calcium-magnesium compound, according to claim 1 , further comprising a sodium based additive in an amount up to 3.5 weight % with respect to the total weight of the powdery calcium-magnesium compound, expressed as sodium equivalent.

3. A powdery calcium-magnesium compound according to claim 1 , presenting a BET specific surface area by nitrogen adsorption of at least 20 m 2 /g.

4. A powdery calcium-magnesium compound according to claim 1 , presenting a BJH pore volume for pores having a diameter lower or equal to 1000 Å by nitrogen desorption of at least 0.1 cm 3 /g.

5. A sorbent composition for a flue gas treatment installation including an electrostatic precipitator, the sorbent composition comprising a powdery calcium-magnesium compound having at least a calcium-magnesium hydroxide content greater or equal to 80 weight %, with respect to the total weight of the powdery calcium-magnesium compound characterized in that it presents a resistivity at 300° C. (572° F.) (R300) lower than 1E11(1×10 11 ) Ohms·cm and higher than 1E7(1×10 7 ) Ohms·cm;
wherein said powdery calcium-magnesium compound is doped with calcium nitrate and wherein said calcium nitrate is present at an amount greater than or equal to 0.05 weight % and lower or equal to 5 weight % with respect to the total weight of the powdery calcium-magnesium compound.

6. A sorbent composition according to claim 5 further comprising an additive selected from the group consisting of activated charcoal, lignite coke, halloysite, sepiolite, clays, bentonite, kaolin, vermiculite, fire clay, aerated cement dust, perlite, expanded clay, lime sandstone dust, trass dust, Yali rock dust, trass lime, fuller's earth, cement, calcium aluminate, sodium aluminate, calcium sulphide, organic sulphide, calcium sulfate, open-hearth coke, lignite dust, fly ash, and water glass.

7. A sorbent composition according to claim 5 , comprising a sodium based additive in an amount up to 3.5 weight % with respect to the total weight of the powdery sorbent composition and expressed as sodium equivalent.

8. A sorbent composition according to claim 5 , wherein said calcium-magnesium compound is hydrated lime.

9. A process for manufacturing a sorbent composition for a flue gas treatment installation including an electrostatic precipitator, the process comprising the steps of
a) providing a powdery calcium-magnesium compound to a reactor, the powdery calcium-magnesium compound comprising at least a calcium-magnesium hydroxide content greater or equal to 80 weight %, with respect to the total weight of the powdery calcium-magnesium compound characterized in that it presents a resistivity at 300° C. (572° F.) (R300) lower than 1E11(1×10 11 ) Ohms·cm and higher than 1E7(1×10 7 ) Ohms·cm; and
b) adding an additive selected from the group consisting of calcium nitrate and nitric acid and combinations thereof in an amount calculated to obtain between 0.1 weight % and 5 weight % of calcium nitrate in weight of dry sorbent composition.

10. A process according to claim 9 , wherein said calcium-magnesium compound comprises a calcium-magnesium hydroxide content greater or equal to 80 weight %, with respect to the total weight of the dry calcium-magnesium compound.

11. A process according to claim 9 , wherein said step of providing a calcium-magnesium compound to a reactor comprises a step of providing a quicklime to said reactor, slaking said quicklime with a predetermined amount of water to obtain said calcium-magnesium compound comprising at least a calcium hydroxide content greater or equal to 80 weight %, with respect to the total weight of the dry calcium-magnesium compound with a predetermined amount of moisture.

12. A process for manufacturing a sorbent composition according to claim 9 , characterized in that it comprises a step of adding a sodium based additive in an amount calculated to obtain up to 3.5% of sodium equivalent in weight of the dry sorbent composition.

13. A process for manufacturing a sorbent composition according to claim 11 , characterized in that said step of slaking is performed in conditions such as to obtain hydrated time with a BET specific surface area measured by nitrogen adsorption of at least 20 m 2 /g.

14. A process for manufacturing a sorbent composition according to claim 11 characterized in that said step of slaking is performed in conditions such as to obtain hydrated lime with a BJH pore volume for pores having a diameter lower or equal to 1000 Å measured by nitrogen desorption of at least 0.1 cm 3 /g.

15. A process for manufacturing a sorbent composition according to claim 9 , characterized in that it further comprises a step of adding an additional additive selected from the group consisting of activated charcoal, lignite coke, halloysite, sepiolite, clays, bentonite, kaolin, vermiculite, fire clay, aerated cement dust, perlite, expanded clay, lime sandstone dust, trass dust, Yali rock dust, trass lime, fuller's earth, cement, calcium aluminate, sodium aluminate, calcium sulphide, an organic sulphide, calcium sulfate, open-hearth coke, lignite dust, fly ash, and water glass.

16. A flue gas treatment process using an installation comprising an injection zone arranged upstream of an electrostatic precipitator, characterized in that it comprises a step of injecting in said injection zone a sorbent composition comprising a powdery calcium-magnesium compound having, at least a calcium-magnesium hydroxide content greater or equal to 80 weight %, with respect to the total weight of the powdery calcium-magnesium compound characterized in that it presents a resistivity at 300° C. (572° F.) (R300) lower than 1E11(1×10 11 ) Ohms·cm and higher than 1E7(1×10 7 ) Ohms·cm and wherein said powdery calcium-magnesium compound is doped with calcium nitrate, said calcium nitrate being present at an amount greater than or equal to 0.05 weight % and lower or equal to 5 weight % with respect to the total weight of the powdery calcium-magnesium compound.

17. A flue gas treatment process according to claim 16 , wherein said sorbent composition is injected in said injection zone wherein said flue gas has a temperature greater than or equal to 180° C. (356° F.).

18. A flue gas treatment process according to claim 16 , wherein said sorbent composition is injected as a dry powder in a dry sorbent injection system or injected as an atomized slurry in a spray dryer absorber system.

Assignees

• Lhoist Rech Et Developpement Sa

Inventors

• Foo Rodney
• Lyons David
• Saratovsky Ian

Classifications

• B01D2253/11

  Clays · CPC title

• B01D53/508 Primary

  by treating the gases with solids · CPC title

• B01D53/83

  with moving reactants · CPC title

• B03C3/013

  Conditioning by chemical additives, e.g. with SO3 · CPC title

• B01D53/10 Primary

  with dispersed adsorbents · CPC title