METHOD FOR CONTROLLING WET FLUE GAS DESULFURIZATION DEVICE, DEVICE FOR CONTROLLING WET FLUE GAS DESULFURIZATION DEVICE, AND REMOTE MONITORING SYSTEM COMPRISING DEVICE FOR CONTROLLING WET FLUE GAS DESULFURIZATION DEVICE

1 . A method for controlling a wet flue gas desulfurization device including:

an absorption tower; and

at least one circulation pump for circulating an absorption liquid in the absorption tower, and

performing desulfurization by bringing the absorption liquid into gas-liquid contact with an exhaust gas generated in a combustion device, in the absorption tower, the method comprising:

a step of constructing a first learning model by machine learning of a relationship between a future sulfur dioxide concentration at an outlet of the absorption tower, and operation data of the combustion device and operation data of the wet flue gas desulfurization device including a circulation flow rate of the absorption liquid;

a step of creating, by using the first learning model, a first relationship table between a circulation flow rate of the absorption liquid at first time and a sulfur dioxide concentration in an effluent gas flowing out of the absorption tower at second time which is time in the future relative to the first time;

a step of deciding, based on the first relationship table, the circulation flow rate of the absorption liquid at the first time, at which the sulfur dioxide concentration in the effluent gas at the second time is not more than a preset set value; and

a step of adjusting an operation condition of the at least one circulation pump based on the decided circulation flow rate, at the first time.

2 . The method for controlling the wet flue gas desulfurization device according to claim 1 ,

wherein the operation data of the wet flue gas desulfurization device including the circulation flow rate of the absorption liquid includes:

a sulfur dioxide concentration in the effluent gas at any time; and

a circulation flow rate of the absorption liquid at time in the past relative to the any time by a time interval obtained by subtracting the first time from the second time.

3 . The method for controlling the wet flue gas desulfurization device according to claim 1 ,

wherein the wet flue gas desulfurization device further includes a gas analyzer for measuring the sulfur dioxide concentration in the effluent gas, and

wherein the method further includes a step of comparing an analysis result by the gas analyzer acquired at the second time with a predictive value of the sulfur dioxide concentration in the effluent gas at the second time.

4 . The method for controlling the wet flue gas desulfurization device according to claim 3 , further comprising:

after creating the first relationship table, a step of reconstructing, based on a difference between the analysis result and the predictive value of the sulfur dioxide concentration in the effluent gas, the first learning model by machine learning of the relationship between the future sulfur dioxide concentration at the outlet of the absorption tower, and the operation data of the combustion device and the operation data of the wet flue gas desulfurization device including the circulation flow rate of the absorption liquid, and creating the first relationship table by using the reconstructed first learning model.

5 . The method for controlling the wet flue gas desulfurization device according to claim 1 ,

wherein the wet flue gas desulfurization device further includes an absorbent slurry supply part for supplying, to the absorption tower, an absorbent slurry which is a slurry of an absorbent included in the absorption liquid, and

wherein the method further includes:

a step of constructing a second learning model by machine learning of a relationship between a future absorbent concentration, and the operation data of the combustion device and the operation data of the wet flue gas desulfurization device including the circulation flow rate of the absorption liquid;

a step of creating, by using the second learning model, a second relationship table between a supply amount of the absorbent slurry to the absorption tower at third time and a concentration of the absorbent in the absorption liquid at fourth time which is time in future relative to the third time;

a step of deciding, based on the second relationship table, the supply amount of the absorbent slurry at the third time, in which the concentration of the absorbent at the fourth time falls within a preset setting range; and

a step of controlling the absorbent slurry supply part based on the decided supply amount of the absorbent slurry, at the third time.

6 . The method for controlling the wet flue gas desulfurization device according to claim 5 ,

wherein the operation data of the wet flue gas desulfurization device including the circulation flow rate of the absorption liquid includes:

a concentration of the absorbent at any time; and

a supply amount of the absorbent slurry at time in the past relative to the any time by a time interval obtained by subtracting the third time from the fourth time.

7 . The method for controlling the wet flue gas desulfurization device according to claim 6 ,

wherein the concentration of the absorbent is calculated with a simulation model by mass balance calculation.

8 . The method for controlling the wet flue gas desulfurization device according to claim 5 ,

wherein an interval from the third time to the fourth time is shorter than an interval from the first time to the second time.

9 . A device for controlling a wet flue gas desulfurization device including:

an absorption tower; and

at least one circulation pump for circulating an absorption liquid in the absorption tower, and

performing desulfurization by bringing the absorption liquid into gas-liquid contact with an exhaust gas generated in a combustion device, in the absorption tower, the device comprising:

a first learning model construction unit for constructing a learning model by machine learning of a relationship between a future sulfur dioxide concentration at an outlet of the absorption tower, and operation data of the combustion device and operation data of the wet flue gas desulfurization device including a circulation flow rate of the absorption liquid;

a first relationship table creation unit for creating, by using the learning model, a first relationship table between a circulation flow rate of the absorption liquid at first time and a sulfur dioxide concentration in an effluent gas flowing out of the absorption tower at second time which is time in the future relative to the first time;

a circulation flow rate decision unit for deciding, based on the first relationship table, the circulation flow rate of the absorption liquid at the first time, at which the sulfur dioxide concentration in the effluent gas at the second time is not more than a preset set value; and

a circulation pump adjustment unit for adjusting an operation condition of the at least one circulation pump based on the decided circulation flow rate, at the first time.

10 . The device for controlling the wet flue gas desulfurization device according to claim 9 ,

wherein the wet flue gas desulfurization device further includes an absorbent slurry supply part for supplying, to the absorption tower, an absorbent slurry which is a slurry of an absorbent included in the absorption liquid, and

wherein the device further includes:

a second learning model construction unit for constructing a second learning model by machine learning of a relationship between a future absorbent concentration, and the operation data of the combustion device and the operation data of the wet flue gas desulfurization device including the circulation flow rate of the absorption liquid;

a second relationship table creation unit for creating, by using the second learning model, a second relationship table between a supply amount of the absorbent slurry to the absorption tower at third time and a concentration of the absorbent in the absorption liquid at fourth time which is time in future relative to the third time;

an absorbent slurry supply amount decision unit for deciding, based on the second relationship table, the supply amount of the absorbent slurry at the third time, in which the concentration of the absorbent at the fourth time falls within a preset setting range; and

an absorbent slurry supply control unit for controlling the absorbent slurry supply part based on the decided supply amount of the absorbent slurry, at the third time.

11 . A remote monitoring system, comprising:

the device for controlling the wet flue gas desulfurization device according to claim 9 ; and

a remote monitoring device electrically connected to the device for controlling the wet flue gas desulfurization device.