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HEAT & MASS BALANCE
ANALYSIS
IN CEMENT INDUSTRY
BY :-NITIN ASNANI
CEA-28964(BEE-Certified Energy Auditor)
EX-Jaypee/UTCL/CII -12 yrs exp
Energy & Mass Balance Concept
• Define System Boundary
• Define Basis-Ex-kg per kg clinker, kg per kg gases mol
• After identifying system boundary, evaluate the following parameters
are as below:-
➢Identify Input streams
➢Identify Output streams
➢Identify the accumulation & formation inside the process .
System Boundary Concept
OVERALL MASS BALANCE CONCEPT
CASE STUDY-XYZ PLANT
CASE STUDY-XYZ PLANT
IMPORTANT FORMULAE'S
METHDOLOGY
Cooler Fan Efficiency Calculation
PHASE DENSITY CONCEPT
CONVEYING AIR CALCULATIONS-Blower
CONVEYING AIR CALCULATIONS-Blowers
KILN FEED, Water Spray, Moisture from fuel
Total Inputs in SYSTEM Boundary-PYRO
OUTPUT STREAMS ACROSS SYSTEM Boundary
Cooler vent losses
Cooler VENT Calculations
COOLER VENT SHEET
COOLER Balance with INPUT Cooling Air
How to find cooler null point?
How to find cooler null point?
Preheater GAS Flow sheet
TOTAL OUTPUT ACROSS SYSTEM
BOUNDARY
OVERALL CONCLUSION-Mass Balance Study
IMPORTANT KEY POINTS
Specific preheater
Norms:-
1.30 -1.50(NM3/kg
Clinker)
Cooler Norms
Input Cooling Air -
1.75 -1.80 Nm3/kg
Clinker
Cooler Vent Air-1-
1.05 N m3/kg clinker
Preheater Fan
efficiency>80%
False air Across
Preheater<8%
False Air across
Cooler ESP without
WHRS <7%
False Air Across
Cooler ESP With
WHRS <10%
Specific power of
cooler fans-3 -4.0
kWh/ton clinker
Specific power of
preheater fan
without WHRS-3-5
kWh/per ton clinker
Specific power of
Preheater Fan With
WHRS-4-7 kWh/ton
Clinker
Cooler vent fan
without WHRS-0.3 -
0.5 kWh/per ton
Clinker
Cooler Vent Fan with
WHRS-0.7 -1.0
kWh/ton clinker
Radiation losses
Input sensible heats
System Boundary
Kiln feed
Fuel
Input
cooling air
Primary
air & coal
conveying
air
Preheater gas
losses
Cooler vent gas
losses
Return dust heat
losses
Heat losses
through Clinker
Heat from fuel
INPUT SENSIBLE HEAT
1) Sensible heat from cooling air
= Input air(kg/clinker) x specific heat x (temperature difference)
= 2.36 x 0.237 x(32-0)
= 17.87 kcal/kg clinker………………………………….1
Temperature difference= Ambient Temp-Reference Temperature
2) Sensible heat from kiln feed
= kiln feed x specific heat x( kiln feed temp-0)
= 1.6 x 0.213 x(75-0)
= 25.60 kcal/kg clinker………………………..…...2
3) Sensible heat from Primary Air
= Primary air(kg air/kg clinker) x Specific heat x (Primary air temp-reference temp)
= 0.049 x 0.237 x(32-0)
= 0.37 kcal/kg clinker……………………………………3………………..3
Kiln Feed & Fuel moisture
Total Input Heat
OUTPUT HEAT
OUTPUT HEAT
Energy Losses due to convection & Radiation
Energy Losses due to convection & Radiation
Kiln and TAD radiation Losses Sheet
Preheater Radiation losses Sheet
Cooler Radiation Losses Sheet
INPUT HEAT
OUTPUT HEAT
Overall Heat Balance Conclusion
IMPORTANT KEY POINTS
Best Values -6
Stage Preheater-
675 Kcal/kg
Clinker
5 Stage-690
kcal/kg clinker
Cooler losses-110-
120 kcal/kg clinker
Cooler Efficiency
with WHRS-65%&
Without-70%
Preheater outlet
Temperature-240-
250 Degree C
Radiation Losses-
5-8%
Top cyclone
efficiency-97.5%
Max AFR
Utilization-30% by
weight
Pressure drop
across 6 stage
preheater-350-450
mmwg
By increasing input
sensible heat, the
energy losses will
be reduced
AQC Boiler
60-70% Power in
WHRS
Specific power of
Preheater Fan
With WHRS-4-7
kWh/ton Clinker
Retention time in
New calciner-5sec
-10 sec
Coal phase
density-3-4 kg
coal/kg air
Numerical Questions
By minimizing the leakages and certain modifications across the preheater
system the plant gets the benefit in terms of overall specific heat
consumption by 20 kcal/kg clinker
NCV of Coal- 6300 kcal/kg coal
Clinker production :-5500 TPD; Grinding Cost of Fine Coal- Rs 15000 per
tonne
Present Specific heat consumption:-750 kcal/kg clinker
Calculate the following:-
a) Present coal consumption per day
b) Coal consumption with improved thermal efficiency & also calculate
saving in Rs per day?
Future
modules…………
Subscribe my Channel for more
videos………………………..
KNOWLEDGE IS POWER OF TODAY,
SMALL EFFORTS BRING CHANGES IN
THE SOCIETY..
KEEP Subscribing…..!!
KEEP Watching……..!!
Link for subscribing the channel-
http://www.youtube.com/@nitinasn
ani08
•FAN AUDIT
•APPLICATION OF FAN CURVE
•CASE STUDIES…
•BAG FILTER DESIGN….
•CALCINER DESIGN
•ENERGY AUDIT METHDOLOGY IN
CEMENT PLANT…
•WHRS OPTIMIZATION & AUDIT & many
more…..

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Heat & Mass Balance PPT in cement industry version 2.0.pdf

  • 1. HEAT & MASS BALANCE ANALYSIS IN CEMENT INDUSTRY BY :-NITIN ASNANI CEA-28964(BEE-Certified Energy Auditor) EX-Jaypee/UTCL/CII -12 yrs exp
  • 2. Energy & Mass Balance Concept • Define System Boundary • Define Basis-Ex-kg per kg clinker, kg per kg gases mol • After identifying system boundary, evaluate the following parameters are as below:- ➢Identify Input streams ➢Identify Output streams ➢Identify the accumulation & formation inside the process .
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  • 12. Cooler Fan Efficiency Calculation
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  • 18. KILN FEED, Water Spray, Moisture from fuel
  • 19. Total Inputs in SYSTEM Boundary-PYRO
  • 20. OUTPUT STREAMS ACROSS SYSTEM Boundary
  • 24. COOLER Balance with INPUT Cooling Air
  • 25. How to find cooler null point?
  • 26. How to find cooler null point?
  • 28. TOTAL OUTPUT ACROSS SYSTEM BOUNDARY
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  • 31. IMPORTANT KEY POINTS Specific preheater Norms:- 1.30 -1.50(NM3/kg Clinker) Cooler Norms Input Cooling Air - 1.75 -1.80 Nm3/kg Clinker Cooler Vent Air-1- 1.05 N m3/kg clinker Preheater Fan efficiency>80% False air Across Preheater<8% False Air across Cooler ESP without WHRS <7% False Air Across Cooler ESP With WHRS <10% Specific power of cooler fans-3 -4.0 kWh/ton clinker Specific power of preheater fan without WHRS-3-5 kWh/per ton clinker Specific power of Preheater Fan With WHRS-4-7 kWh/ton Clinker Cooler vent fan without WHRS-0.3 - 0.5 kWh/per ton Clinker Cooler Vent Fan with WHRS-0.7 -1.0 kWh/ton clinker
  • 32. Radiation losses Input sensible heats System Boundary Kiln feed Fuel Input cooling air Primary air & coal conveying air Preheater gas losses Cooler vent gas losses Return dust heat losses Heat losses through Clinker Heat from fuel
  • 33. INPUT SENSIBLE HEAT 1) Sensible heat from cooling air = Input air(kg/clinker) x specific heat x (temperature difference) = 2.36 x 0.237 x(32-0) = 17.87 kcal/kg clinker………………………………….1 Temperature difference= Ambient Temp-Reference Temperature 2) Sensible heat from kiln feed = kiln feed x specific heat x( kiln feed temp-0) = 1.6 x 0.213 x(75-0) = 25.60 kcal/kg clinker………………………..…...2 3) Sensible heat from Primary Air = Primary air(kg air/kg clinker) x Specific heat x (Primary air temp-reference temp) = 0.049 x 0.237 x(32-0) = 0.37 kcal/kg clinker……………………………………3………………..3
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  • 35. Kiln Feed & Fuel moisture
  • 39. Energy Losses due to convection & Radiation
  • 40. Energy Losses due to convection & Radiation
  • 41. Kiln and TAD radiation Losses Sheet
  • 46. Overall Heat Balance Conclusion
  • 47. IMPORTANT KEY POINTS Best Values -6 Stage Preheater- 675 Kcal/kg Clinker 5 Stage-690 kcal/kg clinker Cooler losses-110- 120 kcal/kg clinker Cooler Efficiency with WHRS-65%& Without-70% Preheater outlet Temperature-240- 250 Degree C Radiation Losses- 5-8% Top cyclone efficiency-97.5% Max AFR Utilization-30% by weight Pressure drop across 6 stage preheater-350-450 mmwg By increasing input sensible heat, the energy losses will be reduced AQC Boiler 60-70% Power in WHRS Specific power of Preheater Fan With WHRS-4-7 kWh/ton Clinker Retention time in New calciner-5sec -10 sec Coal phase density-3-4 kg coal/kg air
  • 48. Numerical Questions By minimizing the leakages and certain modifications across the preheater system the plant gets the benefit in terms of overall specific heat consumption by 20 kcal/kg clinker NCV of Coal- 6300 kcal/kg coal Clinker production :-5500 TPD; Grinding Cost of Fine Coal- Rs 15000 per tonne Present Specific heat consumption:-750 kcal/kg clinker Calculate the following:- a) Present coal consumption per day b) Coal consumption with improved thermal efficiency & also calculate saving in Rs per day?
  • 49. Future modules………… Subscribe my Channel for more videos……………………….. KNOWLEDGE IS POWER OF TODAY, SMALL EFFORTS BRING CHANGES IN THE SOCIETY.. KEEP Subscribing…..!! KEEP Watching……..!! Link for subscribing the channel- http://www.youtube.com/@nitinasn ani08 •FAN AUDIT •APPLICATION OF FAN CURVE •CASE STUDIES… •BAG FILTER DESIGN…. •CALCINER DESIGN •ENERGY AUDIT METHDOLOGY IN CEMENT PLANT… •WHRS OPTIMIZATION & AUDIT & many more…..