Wet type flue gas desulfurization apparatus and operation method of the same

Patent metadata

Field	Value
Publication number	US-10322370-B2
Application number	US-201715845591-A
Country	US
Kind code	B2
Filing date	Dec 18, 2017
Priority date	Mar 27, 2015
Publication date	Jun 18, 2019
Grant date	Jun 18, 2019

Abstract

Provided is an absorber that removes sulfur oxide in a flue gas with an absorbent, an absorbent storing unit that stores the absorbent that has absorbed the sulfur oxide, an oxidation-reduction potential meter that measures an oxidation-reduction potential of the absorbent in the absorbent storing unit, a reducing additive supplying unit that supplies a sulfur oxoacid reducing additive into the absorbent storing unit, and a control device that controls the reducing additive supplying unit based on a measured value of the oxidation-reduction potential of the absorbent measured with the oxidation-reduction potential meter, wherein the reducing additive supplying unit supplies the sulfur oxoacid reducing additive when the measured value of the oxidation-reduction potential has exceeded an upper limit of an appropriate range of the oxidation-reduction potential.

First claim

The invention claimed is:

1. A wet type flue gas desulfurization apparatus comprising:
an absorber that removes sulfur oxide in a flue gas with an absorbent;
an absorbent storing unit that stores the absorbent that has absorbed the sulfur oxide;
an oxidation-reduction potential meter that measures an oxidation-reduction potential of the absorbent in the absorbent storing unit;
a reducing additive supplying unit that supplies a sulfur oxoacid reducing additive into the absorbent storing unit; and
a control device that controls the reducing additive supplying unit based on a measured value of the oxidation-reduction potential of the absorbent measured with the oxidation-reduction potential meter.

2. The wet type flue gas desulfurization apparatus according to claim 1 , wherein the valence of the sulfur oxoacid reducing additive is two to four.

3. The wet type flue gas desulfurization apparatus according to claim 1 , wherein the sulfur oxoacid reducing additive is at least one of sodium thiosulfate, sodium metabisulfite, and sodium dithionite.

4. The wet type flue gas desulfurization apparatus according to claim 1 , comprising:
a flue gas duct that is connected to the absorber and discharges a purified gas that has passed through the absorber; and
a mercury meter that is provided in the flue gas duct and measures the concentration of mercury in the purified gas discharged from the absorber,
wherein the reducing additive supplying unit supplies the sulfur oxoacid reducing additive when a value of the mercury meter exceeds a predetermined threshold value.

5. The wet type flue gas desulfurization apparatus according to claim 1 , further comprising an oxidizing additive supplying unit that supplies an oxidizing additive into the absorbent storing unit,
wherein the control device controls the oxidizing additive supplying unit to supply the oxidizing additive into the absorbent storing unit when the measured value of the absorbent measured with the oxidation-reduction potential meter is lower than 50 mV as a result of supplying the sulfur oxoacid reducing additive.

6. An operation method of a wet type flue gas desulfurization apparatus, comprising:
measuring an oxidation-reduction potential of an absorbent with an oxidation-reduction potential meter; and
adjusting the oxidation-reduction potential to be within an appropriate range by supplying a sulfur oxoacid reducing additive based on the oxidation-reduction potential of the absorbent measured with the oxidation-reduction potential meter.

7. The operation method of a wet type flue gas desulfurization apparatus according to claim 6 , wherein the valence of the sulfur oxoacid reducing additive is two to four.

8. The operation method of a wet type flue gas desulfurization apparatus according to claim 6 , wherein the sulfur oxoacid reducing additive is at least one of sodium thiosulfate, sodium metabisulfite, and sodium dithionite.

9. The operation method of a wet type flue gas desulfurization apparatus according to claim 6 , wherein the appropriate range of the oxidation-reduction potential is 50 mV to 200 mV.

10. The operation method of a wet type flue gas desulfurization apparatus according to claim 6 , wherein when the concentration of mercury in a purified gas discharged from an absorber is measured and the concentration exceeds a predetermined threshold value as a result of the mercury measurement, the sulfur oxoacid reducing additive is supplied to decrease the concentration of mercury to the predetermined threshold value or lower.

11. The operation method of a wet type flue gas desulfurization apparatus according to claim 6 , wherein when a measured value of the oxidation-reduction potential of the absorbent is lower than 50 mV as a result of supplying the sulfur oxoacid reducing additive, an oxidizing additive is supplied.

12. The operation method of a wet type flue gas desulfurization apparatus according to claim 7 , wherein the sulfur oxoacid reducing additive is at least one of sodium thiosulfate, sodium metabisulfite, and sodium dithionite.

13. The operation method of a wet type flue gas desulfurization apparatus according to claim 7 , wherein the appropriate range of the oxidation-reduction potential is 50 mV to 200 mV.

14. The operation method of a wet type flue gas desulfurization apparatus according to claim 7 , wherein when the concentration of mercury in a purified gas discharged from an absorber is measured and the concentration exceeds a predetermined threshold value as a result of the mercury measurement, the sulfur oxoacid reducing additive is supplied to decrease the concentration of mercury to the predetermined threshold value or lower.

15. The operation method of a wet type flue gas desulfurization apparatus according to claim 7 , wherein when a measured value of the oxidation-reduction potential of the absorbent is lower than 50 mV as a result of supplying the sulfur oxoacid reducing additive, an oxidizing additive is supplied.

16. The operation method of a wet type flue gas desulfurization apparatus according to claim 8 , wherein the appropriate range of the oxidation-reduction potential is 50 mV to 200 mV.

17. The operation method of a wet type flue gas desulfurization apparatus according to claim 8 , wherein when the concentration of mercury in a purified gas discharged from an absorber is measured and the concentration exceeds a predetermined threshold value as a result of the mercury measurement, the sulfur oxoacid reducing additive is supplied to decrease the concentration of mercury to the predetermined threshold value or lower.

18. The operation method of a wet type flue gas desulfurization apparatus according to claim 8 , wherein when a measured value of the oxidation-reduction potential of the absorbent is lower than 50 mV as a result of supplying the sulfur oxoacid reducing additive, an oxidizing additive is supplied.

19. The operation method of a wet type flue gas desulfurization apparatus according to claim 9 , wherein when the concentration of mercury in a purified gas discharged from an absorber is measured and the concentration exceeds a predetermined threshold value as a result of the mercury measurement, the sulfur oxoacid reducing additive is supplied to decrease the concentration of mercury to the predetermined threshold value or lower.

20. The operation method of a wet type flue gas desulfurization apparatus according to claim 9 , wherein when a measured value of the oxidation-reduction potential of the absorbent is lower than 50 mV as a result of supplying the sulfur oxoacid reducing additive, an oxidizing additive is supplied.

Assignees

• Mitsubishi Hitachi Power Sys

Inventors

• Honjo Shintaro
• Inaba Norikazu
• Okamoto Takuya
• Hashimoto Jun
• Kamiyama Naoyuki

Classifications

• B01D2258/0283

  Flue gases · CPC title

• B01D2251/606

  Carbonates · CPC title

• B01D53/80

  Semi-solid phase processes, i.e. by using slurries · CPC title

• B01D53/508

  by treating the gases with solids · CPC title

• B01D53/505 Primary

  in a spray drying process · CPC title