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
|
Aeration, deaeration,
neutralization with alkalines, liming & neutralizing amines.
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pH
|
Hydrogen ion concentration defined
as pH = log (1/H+1)
|
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.
|
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)
|
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
|
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
|
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
|
Dedicated and thanks to Greenko group CEO &; MD Shri Chalamalasetty Sir and Shri Mahesh Koli SIr, AM Green Ammonia (India) management Shri Gautam Reddy, Shri GVS ANAND, Shri K.Pradeep Mahadev, Shri VIJAY KUMAR (Site Incharge), Shri G.B.Rao, Shri PVSN Raju, Dr. V. Sunny John, Shri V. Parmekar ,Smt .Vani Tulsi,Shri B. B.K Uma Maheswar Rao, Shri T. Govind Babu, Shri P. Rajachand, Shri B.V Rao, Shri. LVV RAO ,Shri P.Srinivaslu Promotion- EHSQL-by Dr. A.N.GIRI- 28 Lakhs Viewed Thanks to NFCL.
Friday 11 March 2016
BOILER FEEDWATER REQUIREMENTS
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