Wet flue gas desulfurization apparatus and operation method for wet flue gas desulfurization apparatus

Patent metadata

Field	Value
Publication number	US-10646820-B2
Application number	US-201615745794-A
Country	US
Kind code	B2
Filing date	Jul 15, 2016
Priority date	Jul 23, 2015
Publication date	May 12, 2020
Grant date	May 12, 2020

Abstract

Flue gas generated when fuel is subjected to combustion by a combustor such as a boiler is supplied, and a sulfur oxide is reduced or removed from the supplied flue gas. A desulfurization apparatus 10 A includes an absorber 11 , a gas introduction unit 13 a , an absorbent jetting unit 15 , a plurality of water flow oxidation devices 20 , an absorbent supplying unit 25 , a demister 30 , a gas discharging unit 13 b , and a control device 40 that varies the number of water flow oxidation devices 20 that jet absorbent 14 and air 21 based on a rate of the sulfur compound in the absorbent 14 within an absorbent storage tank 11 A.

First claim

The invention claimed is:

1. A wet flue gas desulfurization apparatus comprising:
an absorber that includes an absorbent storage tank for storing absorbent and a flue gas passage through which flue gas discharged from a combustor passes, the absorber being configured to bring the flue gas into contact with the absorbent to cause the absorbent to absorb a sulfur oxide included in the flue gas;
a gas introduction unit that is arranged on an upper side wall of the absorber, and that is configured to introduce the flue gas into the absorber;
an absorbent jetting unit that is arranged in the flue gas passage, and that is configured to jet the absorbent into a space of the absorber;
an absorbent circulation line that is configured to supply the absorbent to the absorbent jetting unit from the absorbent storage tank;
a plurality of water flow oxidation devices that are configured to jet part of the absorbent branched and introduced from the absorbent circulation line into an inside of the absorbent storage tank together with air; and
a control device that is configured to execute for adjusting any one or both of a jetting amount of the absorbent jetted from the water flow oxidation devices and a supply amount of the air supplied to the water flow oxidation devices based on any one or both of a concentration of a sulfur compound included in the flue gas and a concentration of a sulfur compound in the absorbent within the absorbent storage tank,
wherein the control device is configured to execute any one or both of control for varying the number of operating water flow oxidation devices and control for varying a circulation amount of the absorbent circulated into the water flow oxidation devices, and
the control device is configured to execute control for varying an amount of the air supplied to the water flow oxidation devices with a valve, and
wherein the control device is configured to execute control for reducing the number of the operating water flow oxidation devices when any one or both of a concentration of a sulfur compound included in the flue gas and a concentration of a sulfur compound in the absorbent within the absorbent storage tank are lower than a predetermined threshold set in advance.

2. The wet flue gas desulfurization apparatus according to claim 1 , wherein
the absorbent circulation line includes a plurality of circulation pumps, and
when the concentration of the sulfur compound included in the flue gas or the concentration of the sulfur compound in the absorbent within the absorbent storage tank is lower than the predetermined threshold set in advance, the control device is configured to execute control for stopping operations of some of the circulation pumps to reduce the circulation amount of the absorbent.

3. The wet flue gas desulfurization apparatus according to claim 1 , comprising:
a plurality of air supply lines that are configured to supply air to the respective water flow oxidation devices; and
valves that are arranged in the respective air supply lines and are configured to adjust the supply amount of the air, wherein
when the concentration of the sulfur compound included in the flue gas or the concentration of the sulfur compound in the absorbent within the absorbent storage tank is lower than the predetermined threshold set in advance, the control device is configured to execute control for closing some of the valves or adjusting a degree of opening of the valves to reduce the amount of the air supplied to the water flow oxidation device.

4. The wet flue gas desulfurization apparatus according to claim 1 , wherein the water flow oxidation device comprises:
a connection part connected to an absorbent branch line that branches part of the absorbent from the absorbent circulation line;
a liquid supply passage that communicates with the connection part and includes a flow channel narrow part formed inside that is narrower than the liquid supply passage; and
an air supply passage having an opening in a downstream area of the flow channel narrow part within the liquid supply passage.

5. The wet flue gas desulfurization apparatus according to claim 1 , wherein, in reducing the number of the operating water flow oxidation devices, the control device is configured to stop the operations of any of the water flow oxidation devices at intervals of every predetermined number in an arrangement direction of the water flow oxidation devices.

6. The wet flue gas desulfurization apparatus according claim 1 , comprising:
an oxidation-reduction potential meter that is configured to measure oxidation reduction potential within the absorbent storage tank, wherein
the control device is configured to obtain the concentration of the sulfur compound in the absorbent within the absorbent storage tank based on a measured value of the oxidation-reduction potential measured with the oxidation-reduction potential meter.

7. The wet flue gas desulfurization apparatus according to claim 1 , wherein the control device is configured to execute for adjusting any one or both of the jetting amount of the absorbent jetted from the water flow oxidation devices and the supply amount of the air supplied to the water flow oxidation devices based on at least one of values of a boiler load, inlet SO 2 concentration, outlet SO 2 concentration, and a desulfurization ratio, and the concentration of the sulfur compound in the absorbent within the absorbent storage tank.

8. The wet flue gas desulfurization apparatus according to claim 1 , comprising:
a stirring device within the absorbent storage tank, wherein
the stirring device is started/stopped by the control device.

9. The wet flue gas desulfurization apparatus according claim 1 , comprising:
a blower that supplies the air to the water flow oxidation device, wherein,
when the concentration of the sulfur compound included in the flue gas or the concentration of the sulfur compound in the absorbent is higher than the threshold, the control device is configured to increase the supply amount of the air supplied from the blower to the water flow oxidation device.

10. The wet flue gas desulfurization apparatus according to claim 1 , comprising:
a blower that is configured to supply the air to the water flow oxidation device, wherein,
in adjusting the supply amount of the air supplied to the water flow oxidation devices, when the concentration of the sulfur compound included in the flue gas or the concentration of the sulfur compound in the absorbent is lower than a threshold, the control device is configured to execute control for reducing the supply amount of the air supplied from the blower to the water flow oxidation devices.

Assignees

• Mitsubishi Hitachi Power Sys

Inventors

• Kagawa Seiji
• Kamiyama Naoyuki
• Yoshimoto Takashi
• Ushiku Tetsu
• Sugita Satoru

Classifications

• B01D2258/0283

  Flue gases · CPC title

• B01D53/80

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

• B01D53/504

  characterised by a specific device · CPC title

• B01D53/14

  by absorption · CPC title

• B01D53/50

  Sulfur oxides (B01D53/60 takes precedence) · CPC title