Determining Moisture Loads or Latent Loads
Recommended Design Outside Moisture Level | Latent Heat Dissipated by Adult Occupants | Vapor Pressures of Water Miscellaneous Moisture Loads | Regain of Hygroscopic Materials
Moisture load can come from many sources, which provide the data needed to calculate the total latent load on any air conditioning or drying system. The total latent load equals the sum of applicable individual loads.
Outside design level: Bry-Air Dehumidifier performance characteristics are expressed in terms of specific humidity or grains per pound of air. To determine the outside design moisture level, use the standard design dry-bulb and wet-bulb conditions because this value measures the design total heat (wet-bulb) occurring with the highest practical dry-bulb. The design moisture level will exist when a lower dry-bulb occurs with the design wetbulb. This condition represents the same total heat, but a higher specific humidity. The table below lists the recommended design specific humidity for various design wet-bulb temperatures. Use the standard accepted design wet-bulb for your locality.
Example: If the accepted design level for your city is 95°db (dry-bulb temperature) and 76°wb (wet-bulb temperature), this condition equals 104 grs/lb. But there will be many days when 76°wb will occur at a lower dry-bulb temperature. From the table below, the proper design specific humidity for comfort would be 115 grs/lb; for industrial work it would be 125 grs/lb. Figures below assume that these levels will be reached or exceeded on 30% of summer days for comfort work and 10% of days for process work.
Ventilation latent load: Determine the latent load equivalent to the outside air by subtracting the indoor or maintained specific humidity from the outdoor specific humidity and multiplying that amount by the pounds of outside air brought into the system.
EXAMPLE: If 1,000 cfm ventilation air is at 125 grs/lb. design and the design inside condition is 70 grs/lb., what is the ventilation latent load?
1000 x (125 - 70) = 3930 gr/min or 235,800 gr/hr. 14
The average density of air is given as 14 cu. ft. per pound of air and is used regardless of the actual density at design conditions.
Recommended Design Outside Moisture Level
Design Outside Wet Bulb |
Design Specific Humidity |
| Comfort Work |
Process Work |
| F |
(grs/lb) |
(grs/lb) |
| 81° |
139 |
149 |
| 80° |
130 |
143 |
| 79° |
125 |
139 |
| 78° |
120 |
134 |
| 77° |
118 |
130 |
| 76° |
115 |
125 |
| 75° |
112 |
121 |
| 74° |
108 |
117 |
| 73° |
105 |
113 |
| 72° |
100 |
109 |
| 71° |
95 |
106 |
| 70° |
90 |
102 |
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Latent Heat Dissipated by Adult Occupants
Dry Bulb Temperature |
Occupants At Rest |
Occupants Doing Light Physical Exertion * |
Occupant Doing Heavy Physical Exertion ** |
| F |
(grs/hr) |
(grs/hr) |
(grs/hr) |
| 60° |
400 |
1300 |
1960 |
| 65° |
530 |
1630 |
2400 |
| 70° |
670 |
2060 |
2920 |
| 75° |
900 |
2540 |
3450 |
| 80° |
1180 |
3040 |
3950 |
| 85° |
1525 |
3550 |
4450 |
| 90° |
1870 |
4000 |
5000 |
* Examples - Waiters, dinner dancing, light factory assembly work **Examples - Factory machine operator, continuous dancing
Evaporation from a wetted surface: Determine the amount of moisture evaporation from a pan, tank or other wetted surface into a space using the following calculations: Where: Gr. = moisture evaporated in grs/hr. Vel = air velocity in F.P.M. VL = vapor pressure equivalent to temperature of surface water - inches of mercury. VA = vapor pressure equivalent to dew point temperature of air over surface - inches of mercury.
| If air is moving across surface: |
Gr. = 650 x ( 1 + |
Vel 230 |
) x (VL- VA) x (sq ft of surface) |
| If air is impacting surface: |
Gr. = 1350 x ( 1 + |
Vel 250 |
) x (VL- VA) x (sq ft of surface) |
Vapor Pressures of Water
Temperature Degrees F |
Vapor Pressure Inches Mercury |
Temperature Degrees F |
Vapor Pressure Inches Mercury |
Temperature Degrees F |
Vapor Pressure Inches Mercury |
| 30 |
0.1663 |
65 |
0.6222 |
100 |
1.933 |
| 35 |
0.2035 |
70 |
0.7392 |
110 |
2.60 |
| 40 |
0.2478 |
75 |
0.8750 |
120 |
3.45 |
| 45 |
0.3004 |
80 |
1.032 |
130 |
4.53 |
| 50 |
0.3626 |
85 |
1.213 |
140 |
5.88 |
| 55 |
0.4359 |
90 |
1.422 |
150 |
7.57 |
| 60 |
0.5218 |
95 |
1.660 |
160 |
9.65 |
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Miscellaneous Moisture Loads
Description: Food (Per meal) Steam Table (per sq It top) Coffee Urn, 3 gal. steam or electric Coffee Urn, 3 gal. gas Coffee Urn, 5 gal. steam or electric Coffee Urn, 5 gal. gas Hair Dryer, electric, per helmet Hair Dryer, gas, per helmet Unvented gas burners (nat. or mfg. gas) per 1000 Btu. input |
Load Grs/Hr: 200 2,000 10,000 15,000 17,000 26,000 2,700 4,000 650
|
Moisture permeation. This is discussed in detail in Part Four beginning on page 8. Moisture loads in the table above represent unvented appliances. Although personal judgment is used to determine vent or hood efficiency, the hood efficiency should never be higher than 50%.
Drying hygroscopic materials. The calculations shown above apply only to evaporation of free water from a surface. When hygroscopic materials are in the first stages of drying-when the surface is actually wet¬then the above relationship may exist. But after surface drying is complete, further drying will occur at a rate that depends on the rate of diffusion within the material; the rate varies with the degree of dryness within the material and is based on expected structural changes that occur during the drying process.
Establish the drying rate of hygroscopic materials in order to establish the hourly moisture load. Unfortunately these rates must be determined experimentally in each situation.
Usually, the desired outcome with hygroscopic drying is to improve drying rate or degree of dryness in the final product within an existing set up or with the addition of a dehumidifier. In doing so, the desired drying period is generally included with the total weight of material to be handled.
| Average drying rate |
= |
Wt. of material entering minus Wt. of material leaving Drying time (hrs) |
One caution here: the drying period cannot be arbitrarily assumed; it must be realistic. For example, if dry air circulates in a dehumidifier and cannot dry a material to totally dry within 2 hours, and then 2 hours will be neither a possible nor a realistic desired drying time.
Storage of hygroscopic materials. When hygroscopic materials enter a dry storage space, even for a short time, they contribute a moisture load that must be absorbed by the dehumidifier. The table below lists the moisture holding capacity of various materials in equilibrium with air at the relative humidities shown. The percentages compare the moisture to the substance's totally dry weight.
If the incoming material has unknown moisture content, assume that it is in equilibrium with 60% RHair. In winter, the materials will likely come into a room in equilibrium with 90% RHair. However, in winter most other sources of rh are lower, so the summer figure (60%) can be used all year, unless the product loads makes up most of the entire total and the permeation load is minor by comparison.
Regain of Hygroscopic Materials
Moisture Content Expressed in Percent of Dry Weight of the Substance at Various Relative Humidities - Temperature, 75°F.
| Classification |
Material |
Description |
Relative Humidity - Per Cent |
Authority |
| 10 |
20 |
30 |
40 |
50 |
60 |
70 |
80 |
90 |
Natural Textile Fibers |
Cotton |
Sea island - roving |
2.5 |
3.7 |
4.6 |
5.5 |
6.6 |
7.9 |
9.5 |
11.5 |
14.1 |
Hartshorne |
| Cotton |
American - cloth |
2.6 |
3.7 |
4.4 |
5.2 |
5.9 |
6.8 |
8.1 |
10.0 |
14.3 |
Schloesing |
| Cotton |
Absorbent |
4.8 |
9.0 |
12.5 |
15.7 |
18.5 |
20.8 |
22.8 |
24.3 |
25.8 |
Fuwa |
| Wool |
Australian merino-skein |
4.7 |
7.0 |
8.9 |
10.8 |
12.8 |
14.9 |
17.2 |
19.9 |
23.4 |
Hartshorne |
| Silk |
Raw chevennes - skein |
3.2 |
5.5 |
6.9 |
8.0 |
8.9 |
10.2 |
11.9 |
14.3 |
18.8 |
Schloesing |
| Linen |
Table cloth |
1.9 |
2.9 |
3.6 |
4.3 |
5.1 |
6.1 |
7.0 |
8.4 |
10.2 |
Atkinson |
| Linen |
Dry spun - yarn |
3.6 |
5.4 |
6.5 |
7.3 |
8.1 |
8.9 |
9.8 |
11.2 |
13.8 |
Sommer |
| Jute |
Avg. of severalgrades |
3.1 |
5.2 |
6.9 |
8.5 |
10.2 |
12.2 |
14.4 |
17.1 |
20.2 |
Storch |
| Hemp |
Manila & sisal - rope |
2.7 |
4.7 |
6.0 |
7.2 |
8.5 |
9.9 |
11.6 |
13.6 |
15.7 |
Fuwa |
| Rayon |
Viscous Nitrocellulose Cupramonium |
Average skein |
4.0 |
5.7 |
6.8 |
7.9 |
9.2 |
10.8 |
12.4 |
14.2 |
16.0 |
Robertson |
Cellulose Acetate |
Fiber |
0.8 |
1.1 |
1.4 |
1.9 |
2.4 |
3.0 |
3.6 |
4.3 |
5.3 |
Robertson |
| Paper |
M.F.Newsprint |
Wood pulp - 24% ash |
2.1 |
3.2 |
4.0 |
4.7 |
5.3 |
6.1 |
7.2 |
8.7 |
10.6 |
U.S.B. of S. |
| H.M.FWriting |
Wood pulp - 3% ash |
3.0 |
4.2 |
5.2 |
6.2 |
7.2 |
8.3 |
9.9 |
11.9 |
14.2 |
U.S.B. of S. |
| White Bond |
Rag -1% ash |
2.4 |
3.7 |
4.7 |
5.5 |
6.5 |
7.5 |
8.8 |
10.8 |
13.2 |
U.S.B. of S. |
| Com. Ledger |
75% rag - 1% ash |
3.2 |
4.2 |
5.0 |
5.6 |
6.2 |
6.9 |
8.1 |
10.3 |
13.9 |
U.S.B. of S. |
| Kraft Wrapping |
Coniferous |
3.2 |
4.6 |
5.7 |
6.6 |
7.6 |
8.9 |
10.5 |
12.6 |
14.9 |
U.S.B. of S. |
Misc. Organic Materials |
Leather |
Sole oak - tanned |
5.0 |
8.5 |
11.2 |
13.6 |
16.0 |
18.3 |
20.6 |
24.0 |
29.2 |
Phelps |
| Catgut |
Racquet strings |
4.6 |
7.2 |
8.6 |
10.2 |
12.0 |
14.3 |
17.3 |
19.8 |
21.7 |
Fuwa |
| Glue |
Hide |
3.4 |
4.8 |
5.8 |
6.6 |
7.6 |
9.0 |
10.7 |
11.8 |
12.5 |
Fuwa |
| Rubber |
Solid Tire |
0.11 |
0.21 |
0.32 |
0.44 |
0.54 |
0.66 |
0.76 |
0.88 |
0.99 |
Fuwa |
| Wood |
Timber (average) |
3.0 |
4.4 |
5.9 |
7.6 |
9.3 |
11.3 |
14.0 |
17.5 |
22.0 |
Forest P.Lab. |
| Soap |
White |
1.9 |
3.8 |
5.7 |
7.6 |
10.0 |
12.9 |
16.1 |
19.8 |
23.8 |
Fuwa |
| Tobacco |
Cigarette |
5.4 |
8.6 |
11.0 |
13.3 |
16.0 |
19.5 |
25.0 |
33.5 |
50.0 |
Ford |
Food- stuffs |
White Bread |
|
0.5 |
1.7 |
3.1 |
4.5 |
6.2 |
8.5 |
11.1 |
14.5 |
19.0 |
Atkinson |
| Crackers |
|
2.1 |
2.8 |
3.3 |
3.9 |
5.0 |
6.5 |
8.3 |
10.9 |
14.9 |
Atkinson |
| Macaroni |
|
5.1 |
7.4 |
8.8 |
10.2 |
11.7 |
13.7 |
16.2 |
19.0 |
22.1 |
Atkinson |
| Flour |
|
2.6 |
4.1 |
5.3 |
6.5 |
8.0 |
9.9 |
12.4 |
15.4 |
19.1 |
Bailey |
| Starch |
|
2.2 |
3.8 |
5.2 |
6.4 |
7.4 |
8.3 |
9.2 |
10.6 |
12.7 |
Atkinson |
| Gelatin |
|
0.7 |
1.6 |
2.8 |
3.8 |
4.9 |
6.1 |
7.6 |
9.3 |
11.4 |
Atkinson |
Misc. Inorganic Materials |
Asbestos Fiber |
Finely divided |
0.16 |
0.24 |
0.26 |
0.32 |
0.41 |
0.51 |
0.62 |
073 |
0.84 |
Fuwa |
| Silica Gel |
|
5.7 |
9.8 |
12.7 |
15.2 |
17.2 |
18.8 |
20.2 |
21.5 |
22.6 |
Fuwa |
| Domestic Coke |
|
0.20 |
0.40 |
0.61 |
0.81 |
1.03 |
1.24 |
1.46 |
1.67 |
1.89 |
Selvig |
Activated Charcoal |
Steam activated |
7.1 |
14.3 |
22.8 |
26.2 |
128.3 |
29.2 |
30.0 |
31.1 |
32.7 |
Fuwa |
| Sulfuric Acid |
H2SO4 |
33.0 |
41.0 |
47.5 |
52.5 |
57.0 |
61.5 |
67.0 |
73.5 |
82.5 |
Mason |
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