Mastodon Power plant and calculations: Boiler
Showing posts with label Boiler. Show all posts
Showing posts with label Boiler. Show all posts

Top-14 reasons for Boiler Tubes failure

 

        What are the potential reasons for Boiler Tube failure??

Following are the direct causes for Boiler tubes or pressure parts failure.

1-Operation of the Boiler at higher pressure:

Boiler pressure parts are designed to operate at particular pressure for continuous operation. If they are being operated at higher pressure than recommended, leads to failure of pressure parts may be at welding joints or even at plain surfaces.

Boiler pressure parts lose their strength as they become older and older.

As per IBR-7, Boiler operating pressure should be reduced by 5% after 25 years of operation. That is A boiler operating at 109 kg/cm2 pressure should be operated at 103.55 kg/cm2 after 25 years.

Boiler operating pressure reduction chart

Age of the Boiler (From the date of first use in years

25

35

45

50

60

70

80

90

100

% of reduction in working pressure

5

10

15

20

30

40

50

60

70

 

2-Operation of the Boiler at higher temperature:

Operation of the Boilers at Higher temperatures can cause metallurgical weakening of the tubes, leading to deformation, cracking, or rupture. Continuous exposure to high temperatures causes creep, where the metal elongates and loses strength over time.

Rapid or excessive temperature variations cause thermal expansion and contraction, leading to cracks. Operation of the Boilers at higher temperature can also increase internal scaling.

3-Pressure parts or tubes internal scaling:














Poor quality of DM water can lead to internal scaling, this internal scaling of tubes results into poor heat transfer subsequently overheating and tube failure.

Calcium, Magnesium & silica present in water if not treated well can form hard scales on pressure parts internal surfaces.

Operation of the High Boiler at lower pH (< 8) for long time eventually leads filure of pressure parts.

In sugar-based cogeneration plants, there is the chance of entering sugar traces in process return condensate. Due to this, pH of feed water drops ( up to 6) quickly and result into tube failures.

Operation of the high-pressure Boiler at pH around 5 to 6 results into tubes failure in just 3 to 5 hours.

4-Over heating of tubes:

Over heating of pressure parts due to wrongly set burners, air and internal scaling, poor water circulation & soot build up leads into tubes failure.

5-Erosion of tubes:































Erosion of pressure parts is mainly due to high flue gas velocity, bed materials in case of AFBC & CFBC boilers and even due to high velocity of steam and water.

So, ensuring right flue gas velocity at various locations of the Boiler is Vital to take care of erosion of pressure parts.

In case of AFBC & CFBC Boilers, bed coils (Evaporator & Super heaters) and water wall tubes erode due to bubbling beds.

Wrongly designed economiser, evaporators tubes and super heaters coils may suffer from erosion due to high velocity of water and steam. Usually, steam/ water velocity increases due to under sized tubes/coil or operation of the Boiler at over load.

Velocity of the fluid increases as the size of the tubes decreases.

Velocity (m/sec) = Flow (m3/sec) / Area (m2)

Based on above relation, velocity of the fluid increases as the Area of the tubes/pressure parts decreases and Flow increases.

Read>>>Boiler interview questions & Answers

6-Fatigue Failure:

Repeated thermal and mechanical stress due to frequent start up and shutdown cycles, frequent load variation leads to thermal shocks & failure of pressure parts.

7-Chemical cleaning of The Boilers internals:

Excessive use of chemicals especially acids during Boiler chemicals cleaning leads to Pressure parts failure during operation.

8-Stress & corrosion cracking:

Tubes fail due to corrosion, corrosion is mainly due to low pH, dissolved oxygen and other impurities in water which lead to pitting and weakening of the tubes. If Boilers are being operated in such conditions pressure parts go into failure.

9-Poor welding joints:

If welding joints quality is poor i.e if No standard welding procedure was followed during installation stages the joints fails upon small variation load or during abnormal operations.

Joints fail in following cases;

1-Poor welding techniques followed

Read>>>>> What is the significance of post weld and Pre-weld heat treatments (PWHTs)?

2-Poor skill of welder

3-Selecting wrong electrodes etc

4-Wet atmospheric condition

10-Poor operations:

What are the poor operation methods which lead to failure of pressure parts>>>>>??

Boiler pressure parts failure largely depends on Boiler operation skills of the operators.

Pressure parts may fail in following poor operation techniques

1-Not following Boiler start up procedures

2- Not following Boiler shut down procedures

3-Quick start-up of the Boiler, not following the Boiler start up curve

4-Not operating the vents & drains as per requirement or SOP

5-Sudden load variation

6-Operating the Boiler by ‘Bypassing the Boiler protections & Interlocks’.

7-Not providing minimum circulation steam to Boiler during start-ups, shut downs or even in case of ab normal operations.

Not knowing the function of ‘start up vent’ is the main reason for super heater coils failure during Boiler shut downs or low load operations.

Start up vent is used to provide minimum required flow to the Boilers during start-ups, which helps in cooling the super heater coils during No load operations

8-Operating the Boiler on low drum levels or not taking the quick shut downs if there is no water flow into the Boiler.

9-Wrong operation of attemperator. Sudden opening and closing of attemperator valves lead to thermal shocks in super heaters.

10-Operating the Boiler at higher drum levels. Operating the boiler at higher drum levels leads to carryover of wet steam or water into super heaters, which leads to thermal shock & tubes failure.

11-Giving water wall bottom headers blow down at high steam rate: This leads the starvation of water wall tubes.

12-Wrongly set safety valves & higher blow down percentage of safety valves:

In a Boiler, if drum safety valves pop up frequently before popping up of super heater safety valves, then it leads to the starvation of super heater coils and even failure.

12-Hydrogen damage:








Reaction between steel and water at high temperatures produces atomic hydrogen, which diffuses into the metal & leads to embrittlement and cracking, resulting in a fish mouth rupture.

13-Un even thermal expansion of pressure parts:

















Indian Boiler Regulations Book-

Un even of thermal expansion of Boiler tubes due to not following Boiler start up curves & start-up/Shut down procedures or restriction to thermal expansion lead to cracks or failure of joints of pressure parts.

 

Read>>>Why does the thermal expansion occur in Boilers??

14-Metallurgical defects:

Poor quality of metals used for manufacturing of Boiler pressure parts lead to failure of pressure parts during operation.

What are the main reasons for Boiler tubes ‘fish mouth’ opening??
























Fish mouth openings are catastrophic failures in Boilers, It’s a type of rupture where the tube bursts open, resembling a fish's mouth. This failure is highly dangerous and usually indicates severe operational or maintenance issues. The main reasons for a fish mouth opening in boiler tubes are:

Following are the major reasons for Boiler tubes ‘fish mouth’ opening.

1-Short term over heating: Occurs due to localized overheating when tubes are exposed to direct flame or high temperatures without sufficient cooling

2-Internal scaling

3-Operation of the Boiler with low water level

4-Starvation of super heater coils & water wall tubes

5-Hydrogen damage

6-Erosion of pressure parts, mostly in case of AFBC & CFBC Boilers.

7-Operation of the Boiler at higher pressure & Temperature than recommended.

8-Over heating.


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Formulae for Boiler calculations


 












Boiler

1-Boiler efficiency direct method

Boiler efficiency = (Mass of steam flow X Steam enthalpy-Feed water flow at economizer inlet X Enthalpy-Attemperator water flow X Enthalpy) / (GCV of fuel X Fuel consumption)

2-Boiler efficiency by indirect method

Boiler efficiency = 100-Various losses

3-Theoretical air requirement for combustion

Theoretical air Thair = ((11.6 X C% + (34.8 X (H2-O2/8)) + (4.35 X %S))/100

Where C = % of carbon in fuel

H2 = % of Hydrogen present in fuel

S = % of sulphur present in fuel

4-Excess air requirement for combustion

%EA = O2% / (21-O2%)

Where O2 = % of oxygen present in flue gas

5-Mass of actual air supplied

AAS = (1 + EA / 100) X Theoretical air

6-Mass of flue gas

Mfg = Mass of Air + 1

6-Mass of dry flue gas

Mfg = Mass of Co2 in flue gas + Mass of Nitrogen in fuel + Mass of Nitrogen in combustion air + Mass of oxygen in flue gas + Mass of So2 in flue gas

Mfg =(Carbon % in fuel X Molecular weight of CO2 / Mol.weight of Carbon) + N2 in fuel + (Mass of actual air supplied X % of N2 in air i.e 77/100) + ((Mass of actual air – Mass of theoretical air) X 23/100) + S2 in fuel X Mol.weight of SO2 / Mol.weight of sulphur)

7-% of heat loss in dry flue gas

Heat loss = Mfg X Cp X (Tf-Ta) X 100 / GCV of fuel

Where,

Mfg = Mass of flue gas

Cp = Specific heat of flue gas in kacl/kg

Tf = Temperature of flue gas

Ta = Ambient air temperature

9-% of heat loss due to moisture in fuel

Heat loss = M X (584 + Cp X (Tf-Ta))  X 100 /  GCV of fuel

Where,

M = Moisture in fuel

Cp = Specific heat of flue gas in kcal/kg

10-% of heat loss due to moisture in air

Heat loss = AAS X humidity X Cp X (Tf-Ta) X 100/ (GCV of fuel)

Where,

AAS = Actual air supplied for combustion

Cp = Specific heat of flue gas in kcal/kg

Tf = Temperature of flue gas

Ta = Ambient air temperature

11-% of Boiler water blow down

Blow down % = (Feed water TDS X % of makeup water) X 100 / (Maximum permissible TDS in Boiler water –Feed water TDS)

12-Steam velocity in line

Velocity of steam in pipe line,V = Steam flow in m3/sec / Area of pipe line (A)

Steam flow in m3/sec = (Steam flow in kg/hr / Density of steam X 3600)

Area of pipe, A = Pi X D2 / 4

Where D is pipe internal diameter

13-Condensate flash steam calculation

Flash steam % = (H1-H2) X 100 / Hfg)

Where, H1 = Sensible heat at high pressure condensate in kcal/kg

H2 = Sensible heat of steam at low pressure in kcal/kg

Hfg = Latent heat of flash steam

14-Calculation of amount of heat required to raise the water temperature

Heat required in kcal=Mw X Cp X (T2-T1)

Where, Mw = Mass of water

Cp = Specific heat of water in kcal/kg (1 kcal/kg)

T1 = Initial temperature of water in deg C

T2 = Final temperature of water in deg C

15-Calculation of heat required to raise air temperature

Heat required in kcal=Mair X Cp X (T2-T1)

Where, Mw = Mass of water

Cp = Specific heat of flue gas in kcal/kg (0.24 kcal/kg)

T1 = Initial temperature of air in deg C

T2 = Final temperature of air in deg C

16-Surface heat loss calculation

S = (10 + (Ts-Ta) / 20) X (Ts-Ta) X A

S = Surface heat loss in kcal/hr m2

Ts= Hot surface temperature in deg C

Ta = Ambient air temperature in deg C

17-Dryness fraction of steam

X = Mass of dry steam / (Mass of dry steam + Mass of water suspension in mixture)

18-Heat content in wet steam

h = hf + xhfg

h= Heat content in saturated steam

x = Dryness factor of steam

Hfg =Enthalpy of evaporation

19-Heat content in dry saturated steam

h = hf + hfg

h= Heat content in saturated steam

Hfg =Enthalpy of evaporation

20-Heat content in superheated  steam

h = hf + hfg + Cps (Tsup - Ts)

h= Heat content in super heated steam

hfg =Enthalpy of evaporation

Cps = Specific heat of super heated steam

Tsup= Superheated steam temperature in deg C

Ts = Saturated temperature of steam in deg C

21-Calculation of Equivalent evaporation

Me = Ms X (h-hf) / hfg

Ms = Mass of steam

h = Steam enthalpy

hf= Feed water enthalpy

22-Factor of evaporation

Fe = (h-hf) / 539

23-Ash (Total) generation calculation

Ash generation in TPH = Fuel consumption per hour X % of ash in fuel / 100

24-Fly ash generation calculation

Fly ash generation in TPH = Fuel consumption per hour X % of ash in fuel X 80% / 100

25-Bottom  ash generation calculation

Bottom ash generation in TPH = Fuel consumption per hour X % of ash in fuel X 20% / 100

26-Calculation of ash generation in ESP

Ash generation in ESP in TPH = Fuel consumption per hour X % of ash in fuel X 80% X 80% / 100

27-Boiler safety valve blow down calculation

Blow down % = (Set pressure - Re seat pressure) X 100 / Set pressure

28-Calculation of attemperator water flow

Attemperator water flow  in TPH= Steam flow in TPH X (h1-h2) / (h2-h3)

h1 = Enthalpy of steam before desuper heating in kcal/kg

29-Economiser efficiency calculation

ηEco. = (Economiser outlet feed water temperature-Economizer inlet feed water temperature )  X 100 / (Economizer inlet flue gas temperature - Economizer inlet feed water temperature)

30-APH efficiency calculation

APH air side efficiency

ηAPHa = (Air outlet temp-Air inlet temp)) X 100 / (Flue gas inlet temperature -Air inlet temperature)

APH gas side efficiency

ηAPHg = (Flue gas inlet temp.-Flue gas outlet temp) X 100 / (Flue gas inlet temperature -Air inlet temperature )

31-Calculation of steam cost

Steam cost per ton = Steam enthalpy  in kcal/kg X Fuel price per ton/ (Boiler efficiency % X GCV of fuel used in kcal/kg)

32-Travelling grate Boiler heating surface calculation

Boiler heating surface (Appx) = Boiler capacity in kg/hr / 18

33-AFBC Boiler heating surface calculation

Boiler heating surface (Appx) = Boiler capacity in kg/hr / 22

34-Travelling grate slop fired Boiler heating surface calculation

Boiler heating surface (Appx) = Boiler capacity in kg/hr / 12

35-AFBC  slop fired Boiler (Low pressure up to 10 kg/cm2 WP) heating surface calculation

Boiler heating surface (Appx) = Boiler capacity in kg/hr / 8.2

36-Calculation of draught produced in Chimney

Hw = 353 X H (1/Ta – 1/Tg (Ma+ 1)/Ma)

H = Chimney height in meters

Ta = Atmospheric temperature in K

Tg = Flue gas temperature in K

Ma = Mass of air & Mass of flue gas = Ma+1

 

Also given as;

 P = 176.5 X H / Ta

Hw = Chimney height in meters

Ta = Absolute atmospheric temperature in Kelvin

Hw = Draught in mmwc

37-Calculation of mass of flue gas flowing through chimney

Mg (kg/sec)= Density of gas (kg/m3) X Area of Chimney (m2) X Velocity of flue gas in Chimney (m/sec)

38-How to calculate the quantity of De-aerator venting steam?

De-aerator vent rate = 10.98 X Absolute pressure in deaerator X (D X D) Diameter of venting line orifice….Kg/hr

Note: Pressure in PSI

Diameter in inches

Or.

Steam venting flow = 24.24 X P(absolute pressure in PSI) X D X D (Size orifice in inch)........Lbs/hr


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