1. “Flue gas Desulphurization” A real challenge for Thermal Power plants by
A R Mallick

2. Insight What is Flue gas Desulfurisation?
Urgency of FGD system Implementation.
Different Reagents for Desulfurisation.
Available Techniques for FGD.

3. Key Focus areas of Thermal Power Plant
Heat Rate
Auxiliary Power Consumption
Plant Load Factor (PLF)
Water Consumption
Best Practices
Safety
Availability

4. New challenge for Thermal Power Plants -Flue gas Desulfurisation-

5. Flue-gas desulfurization (FGD) is a process to remove SOx from exhaust flue gas using an alkaline reagent.

6. Sulfur oxides (SOx) is a group of gas
Sulfur oxides (SOx) is a group of gas. Among them Sulfur Dioxide (SO2) is important. Other gases in the group are much less common in the atmosphere . 95% of the SOx emitted from combustion of fossil fuel is sulfur dioxide (SO2).

7. Sulfur oxides (SOx) are compounds of sulfur and oxygen molecules.
Thermal power plants burning high-sulfur coal or Oil are generally the main sources of SOX emissions worldwide.
Depending on wind, temperature, humidity, and topography, sulfur dioxide can concentrate close to ground level.

8. High concentrations of sulfur dioxide (SO₂) can result in breathing problems reduced lung function, increased incidence of respiratory symptoms and diseases, irritation of the eyes, nose, and throat, and premature mortality.
Sulfur dioxide is the major contributor for acid rain, which acidifies soils, lakes and streams, accelerates corrosion of buildings and monuments, and reduces visibility.

9. Why it is urgent?

10. Changes in SO2 loading over India and China between 2005 and 2016.
(By OMI instrument on the Aura satellite(NASA), expressed in Dobson Units (1 DU = 2.69 × 1016 molecules cm−2).

11. To monitor SO2 emission, NASA,s Aura satellite captures data by Ozone Monitoring Instrument (OMI).
The data shows India’s SO2 emission is in raising trend. It has doubled in between 2005 to 2014.
That of china is in decline trend from China’s first major effort to reduce sulfur dioxide emissions began in 2007 in anticipation of the 2008 Beijing Olympics. Ambitious plan for reduction of emission started at China from China’s SO2 emissions have fallen 75% since 2007.
India’s emissions have increased 50% in the same period.
This forces India to implement stringent Emission Norms.

12. New emission standard for SOx, NOx was notified by the Ministry of Environment, Forests & Climate Change (MOEFCC) in December 2015.
MOEFCC had set a deadline of 7 December 2017 for the coal power sector to meet these standards.
Most companies have not even started initial work. The industry is asking for some more years to implement these standards.
This Stringent norms are also imposed at other countries across the world.
Thermal power generation process will become more complex to meet stricter emission norms in future.

13. Stringent emission norms is set for Thermal power plants in Environment (Protection) Amendment Rules, 2015 to control SOX emission.
Units installed before 31st December, 2003
Units installed after 1st January,2003, up to 31st December, 2016
Units to be installed from 1st January, 2017
600 mg/Nm3 (Units Smaller than 500MW
200 mg/Nm3 (for units larger than 500MW)
100 mg/Nm3

15. Reagent Used
By-Product
Limestone(CaCO3)- Calcium Carbonate
Gypsum(CaSO4)- Calcium Sulfate
Lime (CaO) / Hydrated Lime(Ca(OH)2)
Calcium Sulfite (CaSO3) and Sulfate((CaSO4)
Ammonia (NH3)
Ammonium Sulfate ((NH4)2SO4 )
Soda Ash (Na2CO3) – Sodium Carbonate / Caustic Soda (NaOH) –Sodium Hydroxide
Sodium Bisulfite (NaHSO3)
Sea Water
None

17. SO2 content in exhaust gases Emission requirements
Selection of the FGD technique depends upon
Type of boiler
Size of the Boiler
SO2 content in exhaust gases
Emission requirements
Cost and availability of reagents
Utilization and disposal of by‐products

18. Available Options Dry Flue Gas Desulphurization System
Semi‐Dry Flue Gas Desulphurization System
Available Options
Wet Flue Gas Desulphurization System

19. Dry Flue Gas Desulphurization System
Dry injection Process

20. Semi‐Dry Flue Gas Desulphurization System
Spray drying Process
Flash Absorption Process

21. Wet Flue Gas Desulphurization System
Limestone scrubbing Process
Sodium scrubbing Process
Ammonia scrubbing Process
Seawater scrubbing Process

22. Dry Sorbent Injection Process
Sorbent injection system is a low cost method of SOX control.
Calcium and Sodium-based reagents are used as Sorbent.
Sorbent is stored and injected dry.
This technique is suitable where space availability is limited.
The Sorbent can be injected into furnace and different locations in flue gas path (before and after Air heater).
In furnace sorbent injection, dry sorbent is injected into the upper part of the furnace.

23. Dry Sorbent Injection

24. Performance of SOX reduction depends upon
Particle size- Finner particles results better performance
Residence time in flue gas
Uniform mixing
Temperature at injection point- Higher temperature gives better result, Minimum temperature should be 275 OF.
Injection location.

25. Chemical Reaction CaCO3 + HEAT → CaO + CO2 CaO+SO2→CaSO3
CaSO3 + ½O2→ CaSO4 (Gypsum)
Sodium carbonate (Soda Ash- Na2CO3) can also be used as Sorbent.
 Na2CO3 + SO2 → Na2SO3 + CO2

26. SO2 Recovery during Combustion
In AFBC and CFBC Boilers, controlled Mixing of Sorbent with fuel is done to control SOX
4% to 8% of lime stone is mixed with coal depending upon purity of lime and sulphur percentage in fuel.

29. Semi‐Dry System - Spray Drying Process
Lime is used as absorbent in this process.
This process is also known as Lime-spray drying (LSD) process. Atomized lime slurry is sprayed inside an absorber chamber to the flue gas stream. Water in the spray droplets evaporates.
Lime reacts with SO2 and form calcium sulfate (CaSO4).
The desulfurized flue gas, along with reaction products passed through a bag filter. Dry solid waste product, i.e-CaSO3, CaSO4 and unreacted lime is collected at bag filter.
A portion of this solids collected is recycled and mixed with fresh lime slurry to maintain required level of alkalinity in the feed slurry.
The clean gas is discharged to atmosphere through stack.

30. SO2 + CaO → CaSO3
CaSO3 + ½O2 → CaSO4 (Gypsum)

32. SO2 in the flue gas reacts with semi solid mixture of lime.
Semi‐Dry System - Flash Absorption Process
SO2 in the flue gas reacts with semi solid mixture of lime.
The reaction by-product consist of unreacted lime, CaCO3, and CaSO4.
The by-product collected is recycled along with the fresh lime slurry into the reactor.
No effluent water is generated as the product is collected in dry form.

34. Wet FGD System - Limestone Scrubbing Process
Preferred technology for Flue gas desulphurisation in larger capacity power plants.
System is usually located after electrostatic precipitator or bag-house.
To get maximum gas–liquid surface area and residence time, various wet scrubber designs like- Spray towers, venturis, plate towers, and packed beds are used.
Flue gas normally flows counter currently with respect to the reagent spray.
Slurry of limestone is sprayed on to the incoming flue gas in a scrubber tower.
Sulphur dioxide in the gas reacts with lime and form calcium sulphite (CaSO3). Oxidation air is bubbled through the slurry to convert CaSO3 (calcium sulphite) to CaSO4 (calcium sulphate).

36. Wet FGD System - Sodium Scrubbing Process
Caustic soda (Sodium Hydroxide, NaOH,) or Soda Ash (Na2CO3) is used as scrubbing agent.
SO2 present in Flue gas is brought in contact with NaOH / Na2CO3 in a tower.
SO2 reacts with of NaOH / Na2CO3 and form Sodium Sulfite (Na2SO3) or Sodium Bisulfite (NaHSO3) which is continuously removed from the bottom of the tower.

37. 2NaOH +SO2 → Na2SO3+H2O
Na2SO3+SO2 +H2O →2NaHSO3
Na2CO3+2SO2 +H2O →2NaHSO3 +CO2

39. Ammonia is used as scrubbing agent.
Wet FGD System - Ammonia Scrubbing Process
Ammonia is used as scrubbing agent.
Does not generate any liquid waste. Ammonium sulfate fertilizer is produced as by-product.
Ammonia is sprayed through multiple levels of spray nozzles in an absorber.
SO2 present in flue gas reacts with ammonia, and produces ammonium sulphate (NH4)2SO4.
The by‐product can generate substantial revenue.

40. 2NH3+SO2 H2O → (NH4)2SO3 (ammonium sulphite)
(NH4)2SO3+ ½ O2 → (NH4)2SO4 (ammonium sulphate)

41. Wet FGD System - Sea Water Scrubbing Process
Can be used at power plants located near sea.
Normal seawater is used as a scrubbing medium by utilizing the alkalinity present in seawater.
Seawater is suitable for absorption of SO2 for two main reasons:
The hot flue gas flow through the absorber in an upward direction.
The sea water is sprayed over the flue gas. The absorbed SO2 is transformed into sulfate ions, a natural constituent of seawater.
The reacted seawater flows by gravity to Oxidation chamber, where water is aerated and mixed again with additional sea water. The mixture is then returned to the sea.