STACK SIZES FOR OIL FUEL

ADAPTED FROM C. R. WEYMOUTH'S TABLE (TRANS.

A. S. M. E. VOL. 34)

+----------------------------------------------------+

|+--------+-----------------------------------------+|

|| | Height in Feet Above Boiler Room Floor ||

||Diameter+------+------+------+-----+--------------+|

|| Inches | 80 | 90 | 100 | 120 | 140 | 160 ||

|+--------+------+------+------+------+------+------+|

|| 33 | 161 | 206 | 233 | 270 | 306 | 315 ||

|| 36 | 208 | 253 | 295 | 331 | 363 | 387 ||

|| 39 | 251 | 303 | 343 | 399 | 488 | 467 ||

|| 42 | 295 | 359 | 403 | 474 | 521 | 557 ||

|| 48 | 399 | 486 | 551 | 645 | 713 | 760 ||

|| 54 | 519 | 634 | 720 | 847 | 933 | 1000 ||

|| 60 | 657 | 800 | 913 | 1073 | 1193 | 1280 ||

|| 66 | 813 | 993 | 1133 | 1333 | 1480 | 1593 ||

|| 72 | 980 | 1206 | 1373 | 1620 | 1807 | 1940 ||

|| 84 | 1373 | 1587 | 1933 | 2293 | 2560 | 2767 ||

|| 96 | 1833 | 2260 | 2587 | 3087 | 3453 | 3740 ||

|| 108 | 2367 | 2920 | 3347 | 4000 | 4483 | 4867 ||

|| 120 | 3060 | 3660 | 4207 | 5040 | 5660 | 6160 ||

|+--------+------+------+------+------+------+------+|

+----------------------------------------------------+

Figures represent nominal rated horse power. Sizes as given good for 50

per cent overloads.

Based on centrally located stacks, short direct flues and ordinary

operating efficiencies.

Table 56 gives the sizes of stacks, and horse power which they will

serve for oil fuel. This table is, in modified form, one calculated by

Mr. C. R. Weymouth after an exhaustive study of data pertaining to the

subject, and will ordinarily give satisfactory results.

Stacks for Blast Furnace Gas Work--For boilers burning blast furnace

gas, as in the case of oil-fired boilers, stack sizes as suited for coal

firing will have to be modified. The diameter of stacks for this work

should be approximately the same as for coal-fired boilers. The volume

of gases would be slightly greater than from a coal fire and would

decrease the draft with a given stack, but such a decrease due to volume

is about offset by an increase due to somewhat higher temperatures in

the case of the blast furnace gases.

Records show that with this class of fuel 175 per cent of the rated

capacity of a boiler can be developed with a draft at the boiler damper

of from 0.75 inch to 1.0 inch, and it is well to limit the height of

stacks to one which will give this draft as a maximum. A stack of proper

diameter, 130 feet high above the ground, will produce such a draft and

this height should ordinarily not be exceeded. Until recently the

question of economy in boilers fired with blast furnace gas has not been

considered, but, aside from the economical standpoint, excessive draft

should be guarded against in order to lower the upkeep cost.

Stacks should be made of sufficient height to produce a draft that will

develop the maximum capacity required, and this draft decreased

proportionately for loads under the maximum by damper regulation. The

amount of gas fed to a boiler for any given rating is a fixed quantity

and if a draft in excess of that required for that particular rate of

operation is supplied, economy is decreased and the wear and tear on the

setting is materially increased. Excess air which is drawn in, either

through or around the gas burners by an excessive draft, will decrease

economy, as in any other class of work. Again, as in oil-fired practice,

it is essential on the other hand that a suction be maintained within

all parts of the setting, in this case not only to provide against

setting deterioration but to protect the operators from leakage of gas

which is disagreeable and may be dangerous. Aside from the intensity of

the draft, a poor mixture of the gas and air or a "laneing" action may

lead to secondary combustion with the possibility of dangerous

explosions within the setting, may cause a pulsating action within the

setting, may increase the exit temperatures to a point where there is

danger of burning out damper boxes, and, in general, is hard on the

setting. It is highly essential, therefore, that the furnace be properly

constructed to meet the draft which will be available.

Stacks for Wood-fired Boilers--For boilers using wood as fuel, there is

but little data upon which to base stack sizes. The loss of draft

through the bed of fuel will vary over limits even wider than in the

case of coal, for in this class of fuel the moisture may run from

practically 0.0 per cent to over 60 per cent, and the methods of

handling and firing are radically different for the different classes of

wood (see chapter on Wood-burning Furnaces). As economy is ordinarily of

little importance, high stack temperatures may be expected, and often

unavoidably large quantities of excess air are supplied due to the

method of firing. In general, it may be stated that for this class of

fuel the diameter of stacks should be at least as great as for coal-fired

boilers, while the height may be slightly decreased. It is far the best

plan in designing a stack for boilers using wood fuel to consider each

individual set of conditions that exist, rather than try to follow any

general rule.

One factor not to be overlooked in stacks for wood burning is their

location. The fine particles of this fuel are often carried unconsumed

through the boiler, and where the stack is not on top of the boiler,

these particles may accumulate in the base of the stack below the point

at which the flue enters. Where there is any air leakage through the

base of such a stack, this fuel may become ignited and the stack burned.

Where there is a possibility of such action taking place, it is well to

line the stack with fire brick for a portion of its height.

Draft Gauges--The ordinary form of draft gauge, Fig. 35, which consists

of a U-tube, containing water, lacks sensitiveness in measuring such

slight pressure differences as usually exist, and for that reason gauges

which multiply the draft indications are more convenient and are much

used.

[Illustration: Fig. 35. U-tube Draft Gauge]

[Illustration: Fig. 36. Barrus Draft Gauge]

An instrument which has given excellent results is one introduced by Mr.

G. H. Barrus, which multiplies the ordinary indications as many times as

desired. This is illustrated in Fig. 36, and consists of a U-tube made

of one-half inch glass, surmounted by two larger tubes, or chambers,

each having a diameter of 2½ inches. Two different liquids which will

not mix, and which are of different color, are used, usually alcohol

colored red and a certain grade of lubricating oil. The movement of the

line of demarcation is proportional to the difference in the areas of

the chambers and the U-tube connecting them. The instrument is

calibrated by comparison with the ordinary U-tube gauge.

In the Ellison form of gauge the lower portion of the ordinary U-tube

has been replaced by a tube slightly inclined to the horizontal, as

shown in Fig. 37. By this arrangement any vertical motion in the

right-hand upright tube causes a very much greater travel of the liquid

in the inclined tube, thus permitting extremely small variation in the

intensity of the draft to be read with facility.

[Illustration: Fig. 37. Ellison Draft Gauge]

The gauge is first leveled by means of the small level attached to it,

both legs being open to the atmosphere. The liquid is then adjusted

until its meniscus rests at the zero point on the left. The right-hand

leg is then connected to the source of draft by means of a piece of

rubber tubing. Under these circumstances, a rise of level of one inch in

the right-hand vertical tube causes the meniscus in the inclined tube to

pass from the point 0 to 1.0. The scale is divided into tenths of an

inch, and the sub-divisions are hundredths of an inch.

The makers furnish a non-drying oil for the liquid, usually a 300

degrees test refined petroleum.

A very convenient form of the ordinary U-tube gauge is known as the

Peabody gauge, and it is shown in Fig. 38. This is a small modified

U-tube with a sliding scale between the two legs of the U and with

connections such that either a draft suction or a draft pressure may be

taken. The tops of the sliding pieces extending across the tubes are

placed at the bottom of the meniscus and accurate readings in hundredths

of an inch are obtained by a vernier.

[Illustration: Fig. 38. Peabody Draft Gauge]

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