Method of improving the Hg-removing capability of a flue gas cleaning process

• US 5,435,980 A
• Filed: 11/04/1991
• Issued: 07/25/1995
• Est. Priority Date: 11/04/1991
• Status: Expired due to Term

• Current Assignee: NIRO A/S (GEA Group AG)
• Original Assignee: NIRO A/S (GEA Group AG)
• Inventors: Felsvang, Karsten S., Nielsen, Kirsten K., Ove, B. Christiansen
• Primary Examiner(s): Langel, Wayne
• Assistant Examiner(s): Vanoy, Timothy C.
• Application Number:
  US07/787,433
• Time in Patent Office: 1,359 Days
• Field of Search: 423/210, 423/463, 423/239.1, 423/240 S, 423/244.08
• US Class Current: 423/210
• CPC Class Codes: B01D 53/10 with dispersed adsorbents
• CPC Class Codes: B01D 53/64 Heavy metals or compounds thereof, e.g. mercury

Abstract

A method is disclosed of improving the Hg removing capability of flue gas purification processes for coal-fired power plant flue gases using spray drying absorption systems. By adjusting the chloride content of the flue gas or the absorbent a permanent high Hg removal is achieved.

Claims

1. In a flue gas cleaning process for elemental Hg vapor containing flue gas having a temperature of 110°

-170°

C. and resulting from the combustion of coal having a chloride content insufficient to convert the elemental Hg vapor into HgCl₂, in which process an aqueous suspension of a basic absorbent in a drying chamber of a drying-absorption zone comprising a dryer chamber and a particle collector as well as a duct connecting them, is atomized to fine droplets into the hot flue gas, evaporating the water of said droplets to form dry fine basic absorbent particles and in which a part of noxious components of the gas including sulphur oxides, hydrogen halides and nitrogen oxides and mercury, is simultaneously sorbed by the basic absorbent particles, whereupon the flue gas with entrained dry fine basic absorbent particles is passed to the particle collector wherein contact between the particles and the flue gas causes a further sorption of noxious compounds, wherein the improvement comprises;

the step of increasing the amount of chloride supplied to the drying-absorption zone to a quantity sufficient to convert elemental Hg to HgCl₂ to improve the Hg sequestering effect of the droplets.

2. The method of claim 1, wherein powdery activated carbon is dispersed into the flue gas at a location upstream of the particle collector.

3. The method of claim 1, wherein the increase of the amount of chloride in the drying absorption zone is accomplished by incorporating an alkaline metal or alkaline earth metal salt or a solution thereof in the aqueous suspension of basic absorbent.

4. The method of claim 1, wherein the increase of the amount of chloride in the drying-absorption zone is accomplished by increasing the chloride concentration in the flue gas by one or both of the following measures (a) adding a chloride or chlorine containing material to the coal before or during the combustion thereof, and (b) injecting gaseous HCl into the flue gas upstream of or into the drying-absorption zone.

5. The method of claim 2, wherein the activated carbon is used in an amount of 1-100 mg/Nm³ flue gas.

6. The process of claim 2, wherein 90-99% of the Hg content of the flue gas is removed by increasing the chloride content of the gas supplied to the drying-absorption zone to 20-150 ppm and by dispersing activated carbon into the flue gas in an amount of 1-100 mg/Nm³.

7. The method of claim 1, including the steps of determining the Hg content of the flue gas leaving the particle collector and increasing the amount of chloride supplied to the drying-absorption zone in response to an increase in the Hg content determined in the flue gas leaving the particle collector.

8. The method of claim 1, including the steps of determining the chloride content of the flue gas entering the drying-absorption zone and adjusting the amount of chloride supplied to the drying-absorption zone in response to an increase or decrease of the chloride content in the flue gas entering the drying-absorption zone.

9. The method of claim 8, wherein said chloride content is established by gas analysis and/or by calculations based on chloride analysis of the coal.

10. In a process of removing noxious components including sulphur dioxide and mercury from hot flue gases originating from the combustion of coal, the chloride content of said coal being such that normal combustion thereof in a boiler forms a flue gas having a chloride content, calculated as Cl^-, less than 150 ppm by weight, in which process an aqueous basic absorbent suspension having a chloride content, calculated as Cl^-, less than 0.1 percent by weight based on dry solids, is atomized to fine droplets which are contacted with the hot flue gas in the drying chamber of a drying-absorption zone comprising a drying chamber and a particle collector and a duct connecting them, the water of said droplets evaporating leaving dry fine particles, and a part of the noxious components of the gas is simultaneously sorbed by the droplets and the fine particles, whereupon the flue gas with entrained dry fine particles is passed to the particle collector wherein contact between the particles and the flue gas causes a further sorption of noxious compounds, the improvement of increasing the amount of chloride in the drying-absorption zone to a mercury absorption improving quantity by increasing the chloride content of the flue gas before it reaches said zone or by adding sodium chloride or calcium chloride to the aqueous suspension or by applying both these measures.

11. The process of claim 10, wherein powdery activated carbon is dispersed into the flue gas at a location upstream of the particle collector.

12. The process of claim 10, wherein gaseous hydrogen chloride is added to the flue gas upstream of or into the drying-absorption zone to obtain a total chloride concentration in the flue gas of at least 1 ppm per weight.

13. The process of claim 10, wherein the step of increasing the chloride content of the flue gas is performed by adding a chloride or chlorine containing material to the coal before or during combustion thereof in an amount sufficient to obtain a total chloride concentration in the flue gas of at least 1 ppm by weight.

14. The process of claims 12 or 13 wherein a total chloride concentration in the flue gas of 20-120 ppm is obtained.

15. The process of claim 10, wherein activated carbon and gaseous HCl are injected together upstream of or into the drying-absorption zone.

16. The process of claim 10, wherein the desired increase of the amount of chloride in the drying-absorption zone is provided by adding sodium or calcium chloride to the absorbent suspension.

17. A process for removing noxious components including sulphur dioxide and elementary Hg vapor from a hot flue gas originating from the combustion of coal having a chloride content insufficient to convert the elementary Hg vapor into HgCl2 in which process an aqueous suspension of a basic absorbent in a drying chamber of a drying-absorption zone comprising a drying chamber and a particle collector as well as a duct connecting them, is atomized to fine droplets into the hot flue gas, whereby the water of said droplets evaporates leaving dry fine particles and simultaneously a part of the noxious components of the gas including sulphur oxides, hydrogen halides, nitrogen oxides and mercury, are sorbed by the droplets and the fine particles, whereupon the flue gas with entrained dry particles is passed to a particle collector wherein contact between the particles and the flue gas causes a further sorption of noxious components, comprising the steps of:

(a) determining the chloride content of the flue gas upstream of the drying-absorption zone, and

(b) based on the thus determined chloride content, adding a chloride containing material to at least one of the flue gas, the coal and the aqueous suspension to increase the amount of chloride supplied to the drying-absorption zone sufficient to convert the Hg into HgCl2 and thereby improve the Hg removing capability of the process.

18. The process of claim 17, wherein powdery activated carbon is dispersed into the flue gas at a location upstream of the particle separator.

19. The process of claim 17, wherein the chloride content of the flue gas upstream of the drying-absorption zone is established by gas analysis.

20. The process of claim 17, wherein the chloride content of the flue gas upstream of the drying-absorption zone is established by calculation based on the chloride content of the coal.