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HOME > ǰҰ > |
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뵵
1. Ϸ(,Ÿ̾,,ǰ,øƮ,, )
2. Ұ( )
3. 뱤,ȭ,(,ȭ)
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ȿ
1. ô뿡 ȿ(3~5%)
2. Co2 Gas (ź ȯ汸)
3. ʱ ں ȸ (1)
4. ű, 忡 밡
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߽ ()
ȰϿ ȭ ȯ شȭ Ű ý
̿Ͽ ȿ âϴ ģȯ ý |
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| м SHEET |  |
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S/N |
DESCRIPTION |
UNITS |
BOILER 1 |
BOILEER 2 |
EXAMPLE |
1 |
BOILER DETAILS |
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1.1 |
DESIGN CAPACITY |
Kg/h
Ton/h
Lbs/h |
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10 Ton/h |
1.2 |
OPERATING CAPACITY |
% |
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70 |
1.3 |
WORKING PRESSURE |
Barg |
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15 |
1.4
1.5
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WORKING DURATION |
Hrs/day
Days/yr |
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24
360 |
2 |
FUEL CONSUMPTION |
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2.1 |
TYPE OF FUEL USED(DIESEL/FUEL OIL/
NATURAL GAS/PALM SHELL/EFB
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Naturl Gas
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2.2 |
SULPHUR CONTENT |
% |
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2.3 |
MOISTURE CONTENT OF FUEL |
% |
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2.4 |
DAILY FUEL CONSUMPTION |
L/day
Sm/day |
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15,000Sm/day |
2.5 |
PRICE OF FUEL |
'/L |
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\500/Sm |
2.6 |
GROSS CALORIFIC VALUE OF FUEL |
MJ/Kg
MJ/Sm |
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39.9 MJ/Sm |
3 |
BOILER FEEDWATER |
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3.1 |
TEMPERATURE OF WATER INTO
FEEDWATER STORAGE TANK |
0c |
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30 |
3.2 |
TEMPERATURE OF BOILER FEEDWATER
WITH CONDENSATE RECOVERY ONIY
(WITHOUT PREHEATING) |
0c |
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50 |
3.3 |
TEMPERATURE OF BOILER FEEDWATER
WITH CONDENSATE RECOVERY AND
PRE-HEATING |
0c |
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3.4 |
TEMPERATURE OF BOILER FEEDWATER
AFTER DE-AERATOR |
0c |
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103 |
4 |
AIR INLET TEMPERATURE |
0c |
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30 |
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AIR FLOWRATE |
Nm/ |
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5 |
FLUE GAS |
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5.1 |
FLUE GAS DISCHARGE TEMPERATURE |
0c |
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250 |
5.2 |
FLUE GAS COMPOSITION,IF ANY |
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CO |
% |
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- |
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SO |
% |
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- |
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No |
% |
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- |
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O |
% |
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- |
6 |
OTHERS |
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6.1 |
METHOD DO DE-AERATION |
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THERMAL DE-AERATOR |
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Y / N |
Y / N |
/ N |
VACUUM DE-AERATOR |
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Y / N |
Y / N |
y / N |
CHEMICAL |
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Y / N |
Y / N |
/ N |
6.2 |
ANY EXISTING ECONOMIZER/HEAT
EXCHANGER? |
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Y / N |
Y / N |
y /
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EXISTING CONDITION OF ECONOMISER
(G-GOOD,F-FAIR,P-POOR) |
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G / F / P |
G / F / P |
G / F / P |
6.3 |
ANY EXISTING AIR PRE-HEATER? |
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Y / N |
Y / N |
y / |
EXISTING CONDITION OF AIR PRE-HEATER
(G-GOOD,F-FAIR,P-POOR) |
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G / F / P |
G / F / P |
G / F / P |
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*Nm is the amount of fuel st 0c whereas Sm is the amount of fuel at 15c |
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