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CHEMICAL FEED Tan|| CHARGING INSTRUCTION
SINGLE CHEMICAl-DlSSOLVINO TANK serves a botlery of separate storage tanks. Fig. I and 2. It gives o relatively smoil design, lets you use stainless metals
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layout of a working discharge diuotver in the photo on (ocing poge fils smoothly
I i) design lf^ieo,#l how the 'ow-heod bottom- into the simplified Mow procedure pictured below In Fig. 2
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Various parts moking up bottom-feed discharge dissolver hove stondord dimensions, use stainless steel where needed
Troublefree Chemical Feed SystCHflilts From an Integrated Design
Seemingly simple job of dis solving and feeding chemicals into a boiler-water cycle raises problems all its own. Here's a sure method that's proved fully reliable over a 5-year period in a large-scale central station plant out in California
By R C ALEXANDER Mtehcnlcal tnglnoot
Deportment of Wot*r A Povar Los iagain, Colli.
So MANY POWER PLANTS OCrOIS the water. The newly developed c*1
country use roughly the same chemicals tulfites have greatly accelerat'd;
for water treatment that you'd expeet (ion rates so time and neratioo
some general agreement on what's good are of even greater consequence!
equipment for feeding these chemicals
Sticky Pastes. Certain other f
into the boiler cycle. But actually you'll ' cals, like finely powdered snfy
find anything but agreement. In many disodium phosphate, form sticky,'
instances this seemingly simple process lo-dissotve pastes that require vij
proves a source of operating troubles. mechanical agitation.
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The more Important phases of the
Undesirable Insolubles. IndusU^
chemical.feeding problem fall into three' commercial-grade chemicals ordiaj
divisions: (1) pickup of unwanted out* contain a small percentige of ii
side air (2) handling of sticky. Inter hies that should be screened out lJ
mediary pastes (3) removal of undesir teet chemical feed pumps, check.'
able insolubles in commercial grades of lines, control valves. '
chemicals as supplied.
Each and every one of these
Outside Air. In dissolving a solid soli ties can be solved by proper like sodium sulfite it Is essential to com What's more, the overridingr hheat
plete the solution os quickly as possible of eorrosion to chemical feeder P^1
with.as little air pickup os possible. The also be reduced or controlled enlhf
longer the time, the1 more outside air the design stage. It's olwaye
reaction takes place. Then the chemical ' estlng point for the average
has leu working eopacity to deliver realise sodium sulfite, eonupoWyj where you Want it most--in the feed- to prevent oxidation corrosion
' ENGINEERING 'AND MANAGEMENT SECTION
*lSSi9Wi,.!,Tcre coi roilon of the steel \?WgiJahkx ^JdeiUpproacb to meeting all these
design lor separate etoriJ^fiWjbkfqr the different chemicals
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,0 8 'ingle dissolver. This dissolver design
r[^l*$!7f|uilaUt and hence use stain-
corroalve arena, interconnecting system,
adequate flushing faalone Insures freedom from , J^aUminatlon of later solutions by ^V^of^revlously mixed chemicals.
l^e order of 60 mesh or bailed on the dissolver
prevcnl undesirable In-, Aotild be removable and
the P8ralf o be can
M ne*cie^: Eaperlence iy2v?~pjt,*'*tcei screening, silver-
p^nce* #Ivm best results. VWr * dissolver is to sup-
ply a solution carrying the correct weight of chemicals, completely mixed throughout, with no stratification and us free of contaminants as possible.
Working - System. Illustrations on these pages show a chemical storage and dissolving system in service at the Har bor Steam Plant, Unit No. 2, that has hung up a- completely 'satisfactory 5-yr record. It involves chemical mixing and feedings, and handles sodium hydrox ide, sodium sulfito, dUodium phosphate, strong solutions for boiler and feed water treatment and mixed chemicals for evaporator liquor treatment. Fig. 2 .hows the essentials of the system, its speeiot dissolving funnel and the various
storage-lack manifold piping. .The funnel, Fig. 2, 3, is built above
an annular chamber, which houses four tangent noulea, right, Fig. 3. Water
enters this chamber from the nozzles and gives e vigorous swirling motion to the liquid as the funnet -fills. When this
swirling liquid reaches a suitable height in the funnel, the dry chemical Is added at a high rate. There Is little tendency (or the chemical to agglomerate into a paste since the -hydroulie shear forces break up the chemical. In fact, we've run tests where we've fed as high os S lb of fine powdered anhydrous sodium sulfite, in tpass, and found U completely `dissolved by the'timethe funnel was full.
Once the dissolving Is complete we open the proper tank valve and let the solution drain by gravity from the dis solver into that lank. Then we bring water through the. funnel rinse-ring i<> thoroughly clean all parts of any adher ent solution. This rino water flows out through the grovity feed line Into the
storage tank so. the. pmnifold Is also thoroughly flushed. In addition a drain, Biting to the sower, ties in at (he end of the manifold so the flushing can be cor ded out for the full manifold length when so desired..
ENGINEERING AND MANAGEMENT SECTION