COAL - Clpdigital.org
COAL - Clpdigital.org
COAL - Clpdigital.org
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48<br />
larly careful to use the full cylindrical contents<br />
of the fan as the volumetric efficiency will be abnormally<br />
high on account of not using the full<br />
cylindrical contents. All fans at low or no resistance<br />
will put-out cent per cent, of their displacement<br />
volume every minute, or every revolution<br />
when run at proper speed, but in Guibal fans<br />
proper and their many modified forms the diminution<br />
of out-put is an inverse ratio somewhat<br />
greater than the increase in the water gauge or<br />
lesistance.<br />
THE MECHANICAL EFFICIENCY<br />
of the fan is obtained by carefully ascertaining the<br />
power developed by the engine driving it, on the<br />
one hand, and the power given out by the fan in<br />
delivering air in the mine and overcoming resistance<br />
on the other hand. The proportion these<br />
two powers bear to one another is the mechanical<br />
efficiency. Thus it is we have a plant in which<br />
the engine developed 20 horse power and the fan<br />
it drives gives 60,000 cubic feet of air per minute;<br />
at one and 3-10 inch water gauge, this will give<br />
a mechanical efficiency of 62.35. The indicated<br />
horsepower of the engine is generally used in the<br />
calculations of the fan's duty and gives results<br />
against the fan by the amount of power used to<br />
overcome the resistance of the engine itself, and<br />
in the best constructed fans by the additional<br />
power lost in transmission.<br />
"One very important point in obtaining the<br />
manometrical efficiency of the fan, is the placing<br />
and reading of the water gauge and the notation of<br />
other necessary observations at a point not less<br />
than 20 feet from the inlet, if an exhaust fan and<br />
whether an exhaust or blowing fan it should be so<br />
placed that the pipe leading to the gauge be out<br />
of the flow of the air, and not within the influence<br />
of an eddy. Many eminent German authorities<br />
place the gauge pipe in a recess and place over its<br />
mouth several thicknesses of flannel in order to<br />
obtain the true statistical gauge. Long pipes<br />
and pipes of small diameter leading from fan drift<br />
to gauges placed in offices or at distant points are<br />
not to be recommended as friction or leakage may<br />
render them unreliable. Under no condition<br />
should a water gauge be placed upon the fan case.<br />
A difference of as much as 400 per cent, has been<br />
noted from this cause: the gauge showing higher<br />
reading the nearer it is placed to the center. This<br />
remark applies more particularly to single inlet<br />
fans."<br />
The manometrical efficiency of fans is found by<br />
the gauge obtained in a preceding formula divided<br />
into the gauge read, thus, by calculation a 10"<br />
water gauge is obtained, and we note a difference<br />
of 6 inches in the legs of the water gauge, then<br />
the result obtained would show a manometrical<br />
efficiency of 60 6-10 per cent.; manometrical ef<br />
THE <strong>COAL</strong> TRADE BULLETIN.<br />
ficiency is high in many fans which are low in mechanical<br />
efficiency and still lower in volumetric<br />
efficiency.<br />
The practical application of the law and formula<br />
enumerated above is to enable us to intelligently<br />
select a fan for the duty to be performed, to blow<br />
equal quantities through equal areas in equal<br />
times. The pressure varies inversely as the<br />
fourth powers of the diameters of the orifices, and<br />
to prove the statement, let the quantity be 150,000<br />
cubic feet of air per minute, and let the pressure<br />
for an orifice 10 feet in diameter be 3 inches of<br />
water gauge, then the pressure per square foot<br />
required to blow the same volume of air per minute<br />
through an orifice 5 feet in diameter is equal<br />
to the fourth power multiplied by three inches of<br />
water gauge, equaling 448 inches water gauge.<br />
To obtain the best results from the ventilating<br />
fan the depression necessary for the entry of the<br />
air should, if possible, not exceed one pound per<br />
square foot; hence the velocity should<br />
NOT EXCEED 18 FEET PER SECOND.<br />
for by formula where V equals velocity and P equals<br />
pressure, the square root of the pressure multiplied<br />
by 18 equals the velocity in feet per second;<br />
then by using quantity the port of entry may be<br />
found by the following formula.<br />
Where Q equals quantity and D equals diameter<br />
of the port of entry, .0343 a factor proven by experiments,<br />
we have the following equation:<br />
.0343 multiplied by the square root of the quantity<br />
equals D. or in other words, the square root of the<br />
quantity multiplied by .0343 equals the diameter of<br />
the port of entry.<br />
Then by the square of the volume obtained and<br />
the resistance by which it is obtained, we are enabled<br />
to calculate the dimensions of the fan we<br />
want and what speed we must drive it to obtain<br />
a desired larger volume. For the benefit of the<br />
practical members present who have not had the<br />
opportunities of an education, we will go through<br />
the steps required to determine tip speed and<br />
increased quantities. Suppose we have a fan<br />
producing 72,000 cubic feet of air per minute at<br />
1.75 inch water gauge, and we want to increase<br />
that volume to 200,000 cubic feet per minute. Our<br />
first step would be to find the water gauge due to<br />
the increased volume. This may be found by the<br />
square of the quantities and we find that if it required<br />
1.75 inch water gauge to produce 72,000<br />
cubic feet per minute, it will require<br />
200<br />
2x1.75=13.5<br />
72<br />
water gauge to produce 200,000 cubic feet per minute,<br />
all other conditions remaining the same. In<br />
our next formula we will show how to find the tip<br />
speed from the water gauge. By an equation we