HOME > ǰҰ >
 
ȸġ Ư,


1. Ϸ(,Ÿ̾,,ǰ,øƮ,, )

2. Ұ( )

3. 뱤,ȭ,(,ȭ)

ȿ

1. ô뿡 ȿ(3~5%)

2. Co2 Gas (ź ȯ汸)

3. ʱ ں ȸ (1)

4. ű, 忡 밡

 
ǰ
  ߽ ()
   ȰϿ ȭ ȯ شȭ Ű ý
   ̿Ͽ ȿ âϴ ģȯ ý
"E-NOVO" ǰ
ǰ
ġ ,
 
м SHEET

 

S/N
DESCRIPTION
UNITS
BOILER 1
BOILEER 2
EXAMPLE
1
BOILER DETAILS
1.1
DESIGN CAPACITY
Kg/h
Ton/h
Lbs/h
10 Ton/h
1.2
OPERATING CAPACITY
%
70
1.3
WORKING PRESSURE
Barg
15
1.4
1.5
WORKING DURATION
Hrs/day
Days/yr
24
360
2
FUEL CONSUMPTION
2.1
TYPE OF FUEL USED(DIESEL/FUEL OIL/
NATURAL GAS/PALM SHELL/EFB
Naturl Gas
2.2
SULPHUR CONTENT
%
2.3
MOISTURE CONTENT OF FUEL
%
2.4
DAILY FUEL CONSUMPTION
L/day
Sm/day
15,000Sm/day
2.5
PRICE OF FUEL
'/L
\500/Sm
2.6
GROSS CALORIFIC VALUE OF FUEL
MJ/Kg
MJ/Sm
39.9 MJ/Sm
3
BOILER FEEDWATER
3.1
TEMPERATURE OF WATER INTO
FEEDWATER STORAGE TANK
0c
30
3.2
TEMPERATURE OF BOILER FEEDWATER
WITH CONDENSATE RECOVERY ONIY
(WITHOUT PREHEATING)
0c
50
3.3
TEMPERATURE OF BOILER FEEDWATER
WITH CONDENSATE RECOVERY AND
PRE-HEATING
0c
3.4
TEMPERATURE OF BOILER FEEDWATER
AFTER DE-AERATOR
0c
103
4
AIR INLET TEMPERATURE
0c
30
AIR FLOWRATE
Nm/
5
FLUE GAS
5.1
FLUE GAS DISCHARGE TEMPERATURE
0c
250
5.2
FLUE GAS COMPOSITION,IF ANY
CO
%
-
SO
%
-
No
%
-
O
%
-
6
OTHERS
6.1
METHOD DO DE-AERATION
THERMAL DE-AERATOR
Y / N
Y / N
/ N
VACUUM DE-AERATOR
Y / N
Y / N
y / N
CHEMICAL
Y / N
Y / N
/ N
6.2
ANY EXISTING ECONOMIZER/HEAT
EXCHANGER?
Y / N
Y / N
y /
EXISTING CONDITION OF ECONOMISER
(G-GOOD,F-FAIR,P-POOR)
G / F / P
G / F / P
G / F / P
6.3
ANY EXISTING AIR PRE-HEATER?
Y / N
Y / N
y /
EXISTING CONDITION OF AIR PRE-HEATER
(G-GOOD,F-FAIR,P-POOR)
G / F / P
G / F / P
G / F / P
 
*Nm is the amount of fuel st 0c whereas Sm is the amount of fuel at 15c
 
 
 
Untitled Document