Document v62NOmmB2Zx451zZXL3BQ5zv9
One Flash Tank Is Recommended for System
Since doiler pressure in CH't plant it only l^S psig, he is right in saying one flash tank and one heat exchanger is the most economical heat-sover sys tem lor his plant The system proposed for him was undoubtedly designed (or o high-pressure plant
Sketch above shows a system that I believe will suit his needs best Piping used should be larger than lor a highpressure system, in order to get oil Rash steam possible from blowdown
woter. About $0% ol heal in blowdown woter will be extracted from flashed steam while most ol remaining heat will be given up to feedwater makeup through'heat exchanger.
Flashed steam may be piped to heater steam inlet, os shown, or it may be used for process or plant besting if present exhaust steam fills demand for healing* feedwater. Leave exact piping sizes to the design engineer.
Arthur Belton Montreal, Canada
One Tank and UquItMo-LIquId Heat Exchanger
Uss or one flash tank and a liquid-loliquid heal exchanger is most eco nomical in CU't case. As makeup and blowdown are approximately the same, feedwater will be heated to 202.4 F provided blowdown is cooled to o tem perature ol 222.4 F.
Less heot-transler surlace will be re quired to heal feedwater to 202.4 F il blowdown inlet is at 3 psig rather than atmospheric pressure. Incidentally, liquid-to-Hquid heat transfer requires less area than iteam-to-liquid, and vol ume handled is far less than il the blowdown is noi allowed to flash. Actu ally, il sufficient hcat-exehonger area is provided in either case, fuel saving will be the same.
II flash tank No. 2 is eliminated, care must be taken to prevent blowdown
liquid at 3 psig from flashing at entry
to heat exchanger. It will not if friction
loss through exchanger is over 3 pi.
Pressure can be maintained in exchan
ger by throttling or by Installing a short
riser in outlet. Outlet pressure can be
less than 3 p* as blowdown has been
cooled at this point.
Assuming a boiler efficiency of 75%
and coal at 14,000 Rlu per lb, actual
savings are easily worked out. Flashed
steam to the deaerator saves 6) tons of
coal per year. Cooling blowdown from
flash tank No. 1 to 80 F (whether flash
tank No. 2 is used or not) saves 49 tons
of coal per year. As a matter ol in
terest, latent heat in steam flashed from
No. 2 tank amounts to only 3.6 tons ol
coal per year.
W L Covan
Ontario, Canada
Outlines Economic Study
DtronE CH ean state positively cost of extra flash lank is unwamh' he must analyze the problem thas Determine enthalpy of water I steam-to-Uquid heat exchanger ordinary heat-balance methods sod culate efficiency of both exchu^t Then find enthalpy of water liquid-to-iiquid heat exchanger wb flash tank No. 2 it omitted. Differea' between these two values givesi satoas! of heat that must be added1 elsewhsr in cycle. Multiplying this result monetary value ol one Btu in (eedwst and number ol operating days s y< yields the extra annual eost of single-flash-tank system.
Extra annual eost is then eom| with annual cost ol second flssb taking into account amount ol w depreciation, maintenance. This " parison quickly shows the most di
able economic system. Addition ol second flash tank
exchanger increases heat-lraoslei lace and efficiency ol blowdown if CH will find extent and eftekaey, heat-transfer surface dependent oa oua factors, some ol which are: over-all coefficient ol heat transmit (2) cost of a Btu (3) length ol t
the surface is used during 1 Analyzing the blowdown systemi pletely and plotting the results* ^ loins a curve like the above. TW** greater saving as heot-transler s (
ihcreasea up to o certain P0 creasing surlace beyond this P creases saving. Above method e*0 termine system closest to ms**0
Ing. Tyler C Hicks Next York, N-
116 (7151
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