BOILER FEEDWATER REQUIREMENTS
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Boiler Make-up Water Sources:
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Salinity
Classes
|
Typical
Total Dissolved Solids (TDS), mg/L
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Fresh
Water
|
less
than 1500
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Brackish
(Well or Aquifer) Water
|
1500
to 10000
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Brines
|
greater
than 10,000
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Seawater
|
35000-60000
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Feedwater Impurities:
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1. Dissolved gases such as oxygen
& carbon dioxide, which lead to corrosion.
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2. Dissolved solids which are
usually inorganic salts of calcium & magnesium
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3. Dissolved organics (oil,
organic chemicals) that can foul Heat Transfer areas.
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4. Microbiological &
macrobiological organisms
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5. Particulate matter such as
suspended solids (mud).
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6. Caustic which can cause caustic
embrittlement of steel.
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Scale & Deposit forming
impurities are:
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- Calcium Ions
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- Magnesium ions
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- Silica
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- Phosphates (likely to be
generated by chemical treatment)
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- Iron & Copper
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Water analyses are conventionally
expressed for both cations (+ve charged ions) and anions (-ve charged ions),
in parts per million by weight (ppmw) except for hardness & alkalinity,
which are usually expressed in ppw of calcium carbonate (CaCO3).
These ppmw values can be converted to a common basis such as
milli-equivalents/liter. this permits the summation of oppositely charged
ions such that total cations will equal total anions. Cation & anion
meq/liter can be converted to ppmw CaCO3.
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Total hardness is defined as the
sum of calcium and magnesium ions in ppw of CaCO3. Total
alkalinity is the sum of CO3-2, HCO3-1,
and OH-1 ions in ppw of CaCO3.
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CONSTITUENT
|
CHEMICAL FORMULA
|
DIFFICULTIES CAUSED
|
MEANS OF TREATMENT
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Turbidity
|
None. Usually expressed in Jackson
Turbidity Units
|
Imparts unsightly appearance to
water , deposits in water lines, process equipment, boilers & so on;
interferes with most process uses
|
Coagulation, Settling &
filtration
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Color
|
None
|
Decaying organic material and
metallic ions causing color may cause foaming in boilers; hinders
precipitation methods such as iron removal, hot phosphate softening; can
stain product in process use
|
Coagulation, filtration,
chlori-nation, adsorption by activated carbon
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Hardness
|
Calcium, magnesium, barium, and
strontium salts expressed as CaCO3
|
Chief source of scale in heat
exchange equipment, boilers, pipe lines, and so on; forms curds with soap;
interferes with dyeing
|
Softening, distillation, internal
boiler water treatment, surface active agents, reverse osmosis, electrolytes
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Alkalinity
|
Bicarbonate (CHO3-1),
carbonate (CO3-2) and hydroxyl (OH-1)
expressed as CaCO3)
|
Foaming & carryover of solids
with steam; embrittlement of boiler steel; bicarbonate and carbonate produce
CO3 in steam, a source of corrosion.
|
Lime & lime-soda softening,
acid treatment, hydrogen zeolite softening, demineralization, dealkalization
by anion exchange, distillation, degasifying.
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Free Mineral Acid
|
H2SO4, HCl
etc., expressed as CaCO3 titrated to methyl-orange end-point
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Corrosion
|
Neutralization with alkalies
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Carbon Dioxide
|
CO2
|
Corrosion in water lines &
particularly steam & condensate lines
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Aeration, deaeration,
neutralization with alkalines, liming & neutralizing amines.
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pH
|
Hydrogen ion concentration defined
as pH = log (1/H+1)
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pH varies according to acidic or
alkaline solids in water; most natural waters have a pH of 6.0-8.0
|
pH can be increase by alkalies
& decreased by acids.
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Sulfate
|
SO4-2
|
Adds to solids contents &
increase corrosive character of water.
|
Demineralization, distillation,
reverse osmosis, electrodialysis
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Chloride
|
Cl-1
|
Adds to solids contents &
increase corrosive character of water.
|
Demineralization, distillation,
reverse osmosis, electrodialysis
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Nitrate
|
NO3-1
|
Adds to solids contents, but is
not usually significant industrially; useful for control of boiler metal
embrittlement.
|
Demineralization, distillation,
reverse osmosis, electrodialysis
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Fluoride
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F-1
|
Not usually significant
industrially.
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Adsorption with magnesium
hydroxide, calcium phosphate or bone black; Alum coagulation, reverse
osmosis, electrolytes.
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Silica
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SiO2
|
Scale in boilers & cooling
water systems; insoluble turbine blade deposits due to silica vaporization.
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Hot process removal with magnesium
salts; adsorption by highly basic anion exchange resins, in conjunction with
demineralization, distillation.
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Iron
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Fe+2 (ferrous); Fe+2
(ferric)
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Discolors water on precipitation;
source of deposits in water lines, boilers etc.; interferes with dyeing,
tanning, paper manu-facture.
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Aeration, coagulation &
filtration, lime softening, cation exchange, contact filtration, surface
active agents for iron retention.
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Manganese
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Mn+2
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same as iron
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same as iron
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Oil
|
Expressed as oil or chloroform
extractable material, ppmw
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Scale, sludge & foaming in
boilers; impedes heat exchange; undesirable in most processes.
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Baffle Separators, strainers,
coagulation & filtration, diatomaceous earth filtration.
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Oxygen
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O2
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Corrosion of water lines, heat
exchange equipment, boilers, return lines, etc.
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Deaeration, sodium sulfite,
corrosion inhibitors, hydrazine or suitable substitutes.
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Hydrogen Sulfide
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H2S
|
Cause of "rotten egg"
odor; corrosion.
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Aeration, chlorination, highly
basic anion exchange.
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Ammonia
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NH3
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Corrosion of copper & zinc
alloys by formation of complex soluble ion.
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Cation exchange with hydrogen
zeolite, chlorination, deaeration, mixed-bed demineralization.
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Conductivity
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Expressed as micromhos, specific
conductance
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Conductivity is the result of
ionizable solids in solution; high conductivity can increase the corrosive
characteristics of a water.
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Any process which decreases
dissolved solids content will decrease conductivity; examples are
demineralization, lime softening.
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Dissolved solids
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None
|
"Dissolved Solids" is a
measure of total amount of dissolved matter, determined by evaporation; high
concentrations of dissolved solids are objectionable because of process
interference & as a cause of foaming in boilers.
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Various softening processes such
as lime softening & cation exchange by hydrogen zeolites will reduce
dissolved solids; demineralization; distillation; reverse osmosis;
electrolytes.
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Suspended Solids
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None
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"Suspended Solids" is
the measure of undissolved matter, determined gravimetrically; suspended
solids, plug lines & cause deposits in heat exchange equipment, boilers
etc.
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Subsidence, filtration, usually
preceded by coagulation & settling.
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Total Solids
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None
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"Total Solids" is the
sum of dissolved & suspended solids, determined gravimetrically.
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See "Dissolved Solids"
& "Suspended Solids".
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Blowdown:
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All dissolved & suspended
solids entering a boiler with the feedwater remain in the drums and tubes as
steam is generated. The continual addition of feedwater produces higher &
higher concentration of solids in the boiler water. A point can be reached
beyond which operation is completely unsatisfactory. this situation may be
caused by dissolved solids, silica content or alkalinity. Every boiler has a
limit above which scaling, foaming & carryover occur. In order to keep
boiler water concentrations below this limit, some of the concentrated boiler
water must be removed from the unit as blowdown.
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The intermittent or manual
blowdown is taken from the bottom of the mud drum. This blowdown is mainly
intended to remove any sludge formed in the boiler water. Both suspended
& dissolved are present in the water. These must be removed to prevent
solids from settling & caking on the heat transfer surfaces. the manual
blowdown should be used approximately once per day for a few seconds to
remove suspended solids which may have settled in the mud drum.
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A continuous blowdown system helps
to keep the boiler water within the concentration limits on a
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relatively constant basis.
Removing a small stream of water continuously saves water, chemicals,
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and heat. The heat in the
continuous blowdown water can be recovered in a heat exchange
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system installed in the blowdown
system. The continuous blowdown connection is usually
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located below the low water level
in the steam drum.
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Proper regulation of boiler
blowdown is very important in boiler operation. Too little blowdown
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allows the concentration of
suspended and dissolved solids to become too great, resulting in scale
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formation and carryover of
impurities in the steam. Too much blowdown wastes fuel and
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feedwater. Globe valves with
position indicators allow for accurate control of the blowdown rate.
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Boiler concentration limits to
control corrosion and fouling in the boiler vary as a function of the
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operating pressure. In some cases,
the blowdown from a high pressure boiler may be suitable for
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makeup to a lower pressure boiler.
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Steam that is dirty and wet can
cause deposits in superheaters, turbines, and control valves. A
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good separation of water and steam
must occur inside the boiler steam drum to produce clean and
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dry steam. Most boilers have
effective mechanical separators in the boiler steam drum when the
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water boils smoothly. When boiler
water primes (high level) or foams, however, impurities are
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carried over in the steam. While
water priming and foaming are partly controlled through careful
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operation of the boiler drum level
and chemical injections, respectively, they are highly dependent
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on maintaining proper boiler
blowdown.
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Some blowdown systems have
automated blowdown control based on a continuous conductivity
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measurement of boiler water.
Conductivity is a measure of the dissolved solids in the boiler
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water.
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The blowdown system must safely
dispose of the flashing steam and hot liquid as previously
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discussed.
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Cycles of Concentration:
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A dissolved salt entering the
boiler system will not leave the boiler in the steam. The dissolved
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salt will concentrate in the
boiler water as steam is formed. The dissolved salt concentration can
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be controlled to a given level by
adjusting the blowdown rate. A simple mass balance on the salt
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will demonstrate this principle.
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The mass of salt entering the
boiler is the mass of boiler feed water (BFW) times the
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concentration of the salt. Since
there is no salt in the steam, the mass of salt leaving the boiler is
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the mass of blowdown (BD) times
the concentration of salt in the BD as shown in the figure below.
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The concentration of salt in the
blowdown will be the same as the concentration of salt in the steam
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drum. The cycles of concentration
(CC) is defined by the concentration in the blowdown divided
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by the concentration in the boiler
feedwater which is equal to the BFW rate divided by the
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blowdown rate.
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The percent blowdown is defined as
the blowdown rate divided by the BFW rate times 100. The
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cycles of concentration is the
inverse of the percent blowdown multiplied by 100. The steam
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drum (blowdown) concentration can
readily be controlled by blowdown rate since they are
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directly related.
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X = (FBD / FBFW)
*100
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FBFW*CBFW =
FBD*CBD
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CBFW / CBD =
FBD / FBFW = X / 100
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CC = CBD / CBFW
= 100 / X
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where:
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FBFW = Feedwater
flow, kg/h (lb/h)
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CC = Cycles of concentration, dimensionless
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FBD = Blowdown
flow, kg/h (lb/h)
|
X = % blowdown, percent of boiler feedwater
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FSTM = Steam
flow, kg/h (lb/h)
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CBFW = Solids
concentration in boiler feedwater, ppm
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CBD = Solids
concentration of blowdown (circulating boiler water), ppm
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Deposits are most likely to occur
in the riser tubes. The concentration of dissolved solids will be
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greater in the riser tubes than in
the steam drum because some water has been vaporized. The
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steam drum concentration is
controlled at a level that minimizes deposits in the riser tubes.
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Care should be exercised in use of
% blowdown because some use % blowdown to mean % of
|
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steam and not BFW as defined here.
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Example:
|
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Water is fed into a boiler from a
DM water plant. The chloride specification of this water also controls the
solids specification. The chloride content of the steam drum water must be
≤10 ppm by weight. The boiler feedwater has a chloride content of 0.2 ppm by
weight. The boiler produces 200,000 kg/h of steam. Calculate the BFW &
Blowdown rates.
|
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Calculations:
|
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CBFW =
|
0.2
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CBD =
|
10
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FSTM =
|
200000
|
kg/h
|
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FBD / FBFW =
CBFW / CBD = X /100
|
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FBD / FBFW =
|
0.02
|
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FBD =
|
0.02*FBFW
|
1
|
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FBFW = FSTM
+ FBD
|
2
|
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From 1 & 2
|
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0.98*FBFW = FSTM
=
|
200000
|
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FBFW =
|
204081.6
|
kg/h
|
Boiler Feedwater quantity
|
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FBD =
|
4081.6
|
kg/h
|
Blow down quantity
|
NFCL thankful to beloved SIRS-Shri K.S RAJU, Shri US JHA Chairman, Shri RAHUL RAJU–MD , SHRI RM DESHPANDE, Shri R.RAGHAVAN, Shri GVS ANAND, SHRI VIJAY KUMAR (Site Incharge), Shri G.B.Rao Shri PVSN Raju, Dr. V. Sunny John, Shri KS Gunasekhar , Shri IVSN Raju.Shri MSRKS Prasad, Shri D.Mohanty , Shri Uma Maheswar Rao, Shri T. Govind Babu, Shri. LVV RAO, Shri. DV Reddy, Promotion- EHSQ-Industry by Dr. A.N. GIRI- SPECIAL THANKS TO BELOVED DYNAMIC MD-SHRI RAHUL RAJU SIR-25.3 LAKHS EHSQ Viewed.
Friday 11 March 2016
BOILER FEEDWATER REQUIREMENTS
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