Document ym4epnVvKbZyOrL3mXpZJMw6E
698_____ 'Chapter 40 '
______ -
1945 Guide'
'Controlling Air Velocities '
Exact determinations of hood control velocities are not available, but it is safe to assume that for most dusty operations velocities should not be less than 200 fpm at the point of origin; Recommended air velocities through hood openings for various processes are given in Table 5. For granite dust generated by pneumatic devices, velocities from 150 to 200 fpm, depending on the type of hood used, are recommended as sufficient for safe control6. Considering the character of the industry, air velocities of this order may be extended to similar dusty operations. The method for approximately determining these velocities in terms of the velocity at the hood opening is given in Equation 3.
No set rule can be given regarding the shape of a hood for a particular operation, but it is well to remember that its essential function is to create an adequate velocity distribution. The fact that the zone of greatest
Table 4. ' Branch Pipe Sizes for Grinding and Buffing Hoods
Type of Wheel
Grinding
Disc Grinding Buffing, Polishing and
Scratch Brushing
Wheel Size Diameter, In.
Max.
9 9 18 18 24 24 30 30 36
20 '20 30
8 8 16 16 24 24 30
Maximum
Width In.
i 3 4 5 6
Area Sq In..
30 175 300 500 700
300
2 50 3 150 4 300 6 600
Branch Pipe Minimum Diameter.
In.
3 4 5 '6 7
4 5
Zii 4 5 6
effectiveness does not extend laterally from the edges of the opening may frequently be utilized in estimating the size of hood required. Where complete enclosure, of a dusty operation is contemplated, it is desirable to leave enough free space to equal the area of the connecting duct. Hoods for grinding, polishing and buffing should fit closely, but at the same time should provide an easy means for changing the wheels. It is advisable to design these hoods with a removable hopper at the base to capture the heavy dust and articles dropped by the operator. Such provisions are of assistance in keeping the ducts clear. Air volumes used to control many dust discharges may often be reduced by effective baffling or partial enclosure of an operation. This procedure is strongly urged where dusts are directed beyond the zone of influence of the hood.
Axial Velocity Formula for Hoods
When the normal flow of air into a hood is unobstructed, Equation 3 may be used to determine the air velocity at any point along the axis6:
Control of the Silicosis Hazard in the Hard Rock Industries. I. A Laboratory Study of the Design of Dust Control Systems for Use with Pneumatic Granite Cutting Tools, by Theodore Hatch. Philip Drinker and Sarah P. Choate. (Journal qf Industrial Bytime, Vol. XII. No. 3, March. 1930).
The Control of Industrial Dust, by J. M. DallaValle (Mechanical Enginecrint, VoL 65, No. 10, October.
Industrial Exhaust Systems
699
V
0.1 Q x* + 0,1 A
where V = velocity at point, feet per minute. Q = volume of air handled, cubic feet per minute.
. x = distance along axis, feet. * A = area of opening, square feet.
(3)
Velocity Contours
It is possible by use of a specially constructed Pitot tube7 to map contours of equal velocity in any axial plane located in the field of in fluence. It has been found that the positions of these contours for any hood can be expressed as percentages of the velocity at the hood opening and are purely functions of the shape of the hood8.
Further, the velocity contours are identical for similar hood shapes when the hoods are reduced to the same basis of comparison. These facts are applicable to all hood problems so that when the velocity contour
Table 5. Recommended Air Velocities Through Openings in Hoods Enclosing Operations or Located Over Zones of Generation of Dusts, Fumes, Vapors and Gases Released in Certain Manufacturing Processes
Condition of Generation of Contaminant
Released without noticeable movement................ ... ....
Minimum Air Velocity. FPM
50-100
Released with low velocity 100-200
Active generation...........J Released with great force....
200-500 500-2000
Process
Evaporation of vapors, . exhaust from
pickling,, washing, degreasing,' plating,
welding, etc.
.
Paint spraying in booth; inspection, sort
ing, weighing, packaging, low speed
. conveyor transfer points, rotating mix
tures, barrel filling.
Foundry shakeout, high speed conveyor
transfer points, crushers, screens.
Grinding, tumbling mills, abrasive dean-,
ing.
distribution is known, the air flow required can be determined. Fig. 1 shows the contour distribution in two axial planes perpendicular to the sides of a rectangular hood with a side ratio of one-half. The distribu tion shown is identical for all openings with a similar side ratio provided the mapping is as shown in the figure. The contours, of course, are expressed as percentages of the velocity at the opening.
Low Velocity Systems
On multiple installations of the same operation it is often possible to institute a great saving in power cost by designing an exhaust system using low velocities in the main ducts. Such a system for use in grinding and shaping porcelain has been described. In these operations, the. separate machines are grouped around a central plenum chamber and exhausted by means of a low pressure fan connected to the plenum. In this, case a power saving of over 90 per cent was obtained; A similar design technique1 has been described for use in ventilating plating tanks.
'Studies in the Design of Local Exhaust Hoods, by J. M. DallaValle and Theodore Hatch (A.SM.&.
Transactions, VoL 54, 1932).
Velocity Characteristics of Hoods under Suction, by J. M. DallaValle (A.S.H.V.E. Transactions, Vol. 38.1932, p. 387).
Low Velocity Exhaust Systems, by Theodore Hatch (.Heating and Ventilating, October, 1940, p. 27).
"Tank Ventilating Power Costs Cut by Low Velocity Systems, by William B. Harris (Heating and
Ventilating, July, 1942, p. 42).
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