| Note: | For a more detailed discussion of fundamentals relating to this subject, see ANSI Z9.2-1960. |
| DIAMETER OR GREATER DIMENSION | |
| (U.S. gauge) |
|
| Up to 8 inches inclusive . . . . . . . . . . . . | No. 24 |
| Over 8 inches to 18 inches inclusive . . . . . . . . . . . . | No. 22 |
| Over 18 inches to 30 inches inclusive . . . . . . . . . . . . | No. 20 |
| Over 30 inches . . . . . . . . . . . . | No. 18 |
| Operating Airflow conditions for object completely inside booth | Crossdraft f.p.m. |
Velocities, f.p.m. |
|
| Design | Range | ||
| Electrostatic and automatic airless operation contained in booth without operator. | Negligible . . . . . . . . . . . . | 50 large booth 100 small booth |
50-75 75-125 |
| Air-operated guns, manual or automatic | Up to 50 . . . . . . . . . . . . | 100
large booth 150 small booth |
75-125 125-175 |
| Air-operated guns, manual or automatic | Up to 100 . . . . . . . . . . . . | 150
large
booth 200 small booth |
125-175 150-250 |
| Notes: |
|
| (1) Attention is invited to the fact that the effectiveness of the spray booth is dependent upon the relationship of the depth of the booth to its height and width. | |
| (2) Crossdrafts can be eliminated through proper design and such design should be sought. Crossdrafts in excess of 100 fpm (feet per minute) should not be permitted. | |
| (3) Excessive air pressures result in loss of both efficiency and material waste in addition to creating a backlash that may carry overspray and fumes into adjacent work areas. | |
| (4) Booths should be designed with velocity shown in the
column headed "Design." However, booths operating with
velocities shown in the column headed "Range" are in
compliance with this standard. |
Dilution volume required per gallon of solvent |
= |
4 (100-LEL) (cubic feet of vapor per gallon) |
|||
| LEL | |||||
| Using toluene as the solvent. (1) LEL of toluene from Table 15, column 2, is 1.4 percent. (2) Cubic feet of vapor per gallon from Table 15, column 1, is 30.4 cubic feet per gallon. (3) Dilution volume required = |
|||||
| 4 (100-1.4) 30.4 | = |
8,564 cubic feet. |
|||
| 1.4 | |||||
| (4) To convert to cubic feet per minute of required ventilation, multiply the dilution volume required per gallon of solvent by
the number of gallons of solvent evaporated per minute. |
| Cubic feet of vapor per gallon of liquid at 70°F. | Lower explosive limit in percent by volume of air at 70°F. | |
| Solvent | ||
| Column 1 | Column 2 | |
| Acetone . . . . . . . . . . . . | 44.0 | 2.6 |
| Amyl Acetate (iso) . . . . . . . . . . . . | 21.6 | 1.01 |
| Amyl Alcohol (n) . . . . . . . . . . . . | 29.6 | 1.2 |
| Amyl Alcohol (iso) . . . . . . . . . . . . | 29.6 | 1.2 |
| Benzene . . . . . . . . . . . . | 36.8 | 1.41 |
| Butyl Acetate (n) . . . . . . . . . . . . | 24.8 | 1.7 |
| Butyl Alcohol (n) . . . . . . . . . . . . | 35.2 | 1.4 |
| Butyl Cellosolve . . . . . . . . . . . . | 24.8 | 1.1 |
| Cellosolve . . . . . . . . . . . . | 33.6 | 1.8 |
| Cellosolve Acetate . . . . . . . . . . . . | 23.2 | 1.7 |
| Cyclohexanone . . . . . . . . . . . . | 31.2 | 1.11 |
| 1,1 Dichloroethylene . . . . . . . . . . . . | 42.4 | 5.6 |
| 1,2 Dichloroethylene . . . . . . . . . . . . | 42.4 | 9.7 |
| Ethyl Acetate . . . . . . . . . . . . | 32.8 | 2.5 |
| Ethyl Alcohol . . . . . . . . . . . . | 55.2 | 4.3 |
| Ethyl Lactate . . . . . . . . . . . . | 28.0 | 1.51 |
| Methyl Acetate . . . . . . . . . . . . | 40.0 | 3.1 |
| Methyl Alcohol . . . . . . . . . . . . | 80.8 | 7.3 |
| Methyl Cellosolve . . . . . . . . . . . . | 40.8 | 2.5 |
| Methyl Ethyl Ketone . . . . . . . . . . . . | 36.0 | 1.8 |
| Methyl n-Propyl Ketone . . . . . . . . . . . . | 30.4 | 1.5 |
| Naphtha (VM&P) (76° Naphtha) . . . . . . . . . . . . |
22.4 |
0.9 |
| Naphtha (100° Flash) Safety Solvent-Stoddard Solvent . . . . . . . . . . . . |
23.2 |
1.1 |
| Propyl Acetate (n) . . . . . . . . . . . . | 27.2 | 2.0 |
| Propyl Acetate (iso) . . . . . . . . . . . . | 28.0 | 1.8 |
| Propyl Alcohol (n) . . . . . . . . . . . . | 44.8 | 2.1 |
| Propyl Alcohol (iso) . . . . . . . . . . . . | 44.0 | 2.0 |
| Toluene . . . . . . . . . . . . | 30.4 | 1.4 |
| Turpentine . . . . . . . . . . . . | 20.8 | 0.8 |
| Xylene (o) . . . . . . . . . . . . | 26.4 | 1.0 |
| 1 | At 212°F. |