Power plant and calculation site basically includes the detailed study of power plant operation and maintenance, its related all calculations and thumb rules. It also involves detailed troubleshooting guides for operation and maintenance of power plant system/equipments like Boiler, fans, compressors, belt conveyors, ash handling system, ESP, steam turbine, cooling tower, heat exchangers, steam ejectors, condensers WTP. etc.
Heat rate, efficiency
The efficiency of the APH are calculated from two
ways one is from air side other from gas side.
APH gas side efficiency
ηAPHg = (Flue gas inlet temp.Tfi-Flue gas outlet
temp.Tfo) X 100 / (Flue gas inlet temperature tfi-Air inlet temperature Tai)
APH air side efficiency
ηAPHa = (Air outlet temp.Tao-Air inlet temp.Tao)) X
100 / (Flue gas inlet temperature tfi-Air inlet temperature Tai)
Calculate the APH gas
side & air efficiency if its flue gas inlet and out let temperature are 245
deg C and 155 deg C and air inlet and out let temperatures are 32 deg C & 173
deg C respectively.
APH Gas side
efficiency calculation
ηAPHg = (Flue gas inlet temp.Tfi-Flue gas outlet
temp.Tfo) X 100 / (Flue gas inlet temperature tfi-Air inlet temperature Tai)
ηAPHg =(245-155) X 100 / (245-32)
ηAPHg = 42.25%
APH Air side
efficiency calculation
ηAPHa = (Air outlet temp.Tao-Air inlet temp.Tao)) X
100 / (Flue gas inlet temperature tfi-Air inlet temperature Tai)
ηEco. = (Economiser outlet feed water temperature Two-Economiser
inlet feed water temperature Twi) X 100 / (Economiser inlet flue gas
temperature Tfi- Economiser inlet feed water temperature Twi)
Example:
Calculate the economiser effectiveness,
whose feed water inlet & outlet temperatures are 150 Deg C & 220 Deg C
respectively & flue gas inlet & outlet temperatures 385 deg C & 215
deg c respectively.
Desuperheating (or attemperation) is the process of reducing the temperature of super heated steam by injecting water. The injected water absorbs heat from the steam and evaporates completely, bringing the steam temperature closer to saturation or the specified outlet temperature.
Typical applications:
Boiler outlet temperature control
Turbine inlet temperature control
HRSG and WHRB steam temperature regulation
Process steam conditioning
Parameters Required for Calculating Desuperheating Water Flow
To determine the required spray water quantity, you need:
Steam Input Conditions
Inlet steam pressure (P₁)
Inlet steam temperature (T₁)
Steam Output Requirements
Outlet steam pressure (P₂)
Outlet steam temperature (T₂)
Water Conditions
Desuperheating water temperature (Tᵥ)
Desuper heating water flow online calculator
Desuperheating Water Quantity Calculator
Desuperheating Water Quantity Calculator
Calculates spray water required based on inlet & outlet steam pressure/temperature and water temperature.
In power plant, calculation of cost
of steam is very vital in commercial point of view. Following are the
parameters which affect the cost of steam.
1.Steam pressure
2.Steam temperature
3.GCV of fuel
4.Price of fuel
5.And Boiler efficiency
Following gives you the relation among steam cost & above all
parameters & vice versa
Steam cost increases as the
enthalpy or heat content in steam increases and vice versa
Steam cost increases as the
GCV of fuel decreases and vice versa
Steam cost increases as the
fuel price increases & vice versa
Steam cost increases as the
Boiler efficiency decreases & vice versa
Understanding with examples.
1.Calculate the cost of steam per kg,
which is been using for Steam turbine having pressure 121 kg/cm2 &
temperature 550 deg C.The boiler of efficiency 75% uses coal of GCV 4200
kcal/kg to produce this steam.Cosnsider the price of coal is Rs 5000/MT
Enthalpy of steam at above pressure & temperature H = 830.43 kcal/kg
Boiler efficiency ⴖb= 75%
GCV of coal = 4200 kcal/kg
Now, cost of steam = Heat content in steam in kcal/kg X Fuel
price / (GCV of fuel in kcal/kg X Boiler efficiency ⴖb)
=
830.43 X 5000 / (4500 X 0.75)
=
1230.26 rupees / MT of steam or Rs 1.23 / kg of steam
2.Calculate the cost of steam per
kg, which is been using for chemical process plant having pressure 5 kg/cm2
& temperature 180 deg C.The boiler of efficiency 65% uses biomass of GCV
2800 kcal/kg to produce this steam.Cosnsider the price of biomass is Rs 2400/MT
Enthalpy of steam at above pressure & temperature H = 670 kcal/kg
Boiler efficiency ⴖb= 65%
GCV of coal = 2800 kcal/kg
Now, cost of steam = Heat content in steam in kcal/kg X Fuel price /
(GCV of fuel in kcal/kg X Boiler efficiency ⴖb)
=
670 X 2400 / (2800 X 0.65)
=
883.51 rupees / MT of steam or Rs 0.88 / kg of steam
Note: This tool estimates steam energy and cost based on simplified enthalpy equations.
It does not consider feedwater temperature or full steam tables.