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 .
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
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?
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