FIN-DS-2 (7/98) Data Catalog - Trane

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Performance Adjustment Factors Table PAF-1 — Hot Water Pressure Drop (Expressed in Feet of Water) Cabinet Water Flow Cabinet Length Depth GPM 26 (660) 32 (813) 38 (965) 44 (1118) 50 (1270) 56 (1422) 62 (1575) 68 (1727) .25 .031 .033 .035 .037 .039 .041 .043 .045 4 .5 .115 .124 .129 .136 .143 .150 .157 .164 (102) 1.0 .452 .469 .493 .517 .541 .565 .589 .613 2.0 1.68 1.76 1.85 1.93 2.05 2.10 2.19 2.28 .5 .050 .053 .056 .059 .063 .066 .069 .072 6 1.0 .200 .212 .224 .235 .247 .258 .267 .276 (152) 2.0 .798 .823 .848 .883 .933 .982 1.031 1.08 3.0 1.75 1.84 1.93 2.01 2.10 2.18 2.24 2.3 4.0 2.85 3.09 3.23 3.36 3.49 3.62 3.75 3.88 .5 .033 .035 .037 .039 .041 .043 .045 .049 8 1.0 .123 .130 .137 .144 .151 .158 .165 .172 (203) 2.0 .465 .493 .521 .549 .569 .589 .609 .629 3.0 1.05 1.10 1.15 1.20 1.25 1.30 1.35 1.40 4.0 1.84 1.92 2.00 2.09 2.17 2.26 2.35 2.44 5.0 2.88 3.00 3.12 3.25 3.37 3.50 3.63 3.76 Table PAF-2 — Steam Ratings at Pressures Above One Pound Gauge Steam Pressure Gauge 5 10 15 25 50 60 Factor 1.123 1.254 1.364 1.56 1.93 2.05 Btu Per Sq. Ft. — Factor x 240 270 301 328 374 464 492 Note: Service above 60 psig (413 kPa) steam or 307 F (153 C) not recommended for standard element construction. Table PAF-3 — Heating Effect Enclosure Height 14 (356) 16 18 20 24 26 30 32 36 (914) Unit & Under (406) (457) (508) (610) (660) (762) (813) & Over Wall Hung Sloping Top 7.5 6.5 4.5 3.5 1 1 0 0 0 Wall Hung Front Outlet 15 13 9 7 3 2 0 0 0 Floor Standing Sloping Top 7.5 7.5 7.5 6.5 4.5 3.5 1.5 1 0 Floor Standing Front Outlet 15 15 15 13 9 7 3 2 0 Top Outlet Extruded Grille 0 0 0 0 0 0 0 0 0 Table PAF-4 — Reduction in Ratings with Standard Inlet Grilles (In Percent) Enclosure Height 14 & 16 18 & 20 24 & 26 30 & 32 36 & 38 Depth (356 & 406) (457 & 508) (610 & 660) (762 & 813) (914 & 965) 4 (102) & 6 (152) 3% 5% 2% 4% 6% 8 (203) 6% 8% 4% 6% 9% Table PAF-5 — Btu per Sq. Ft. EDR Conversion Factors Average Water Temp. In Convectors 160 170 180 190 200 210 215 220 5 F Drop Forced Cir. 131 150 167 189 208 228 237 247 10 F Drop Forced Cir. 125 143 161 180 198 216 226 235 20 F Drop Forced Cir. 105 123 142 160 179 198 208 217 30 F Drop Gravity Cir. Notes: 104 121 137 153 169 185 193 201 1. One EDR = 240 Btu @ 215 F Steam, 1 Psi 2. One MBh = 1000 Btu 3. Dimensions shown in ( ) are in millimeters. Metric Conversions 1 Psi = 6.895 kPa (Kilo Pascals) at 65 F Air (18.3 C Air) Sq. Ft. EDR at 1 Psi (6.895 kPa) at 65 F Air (18.3 C) Air x 240 BTU = Total BTU’s (Watts) 1 BTU/HR. = 0.2931 Watts 1 Foot = 0.3048 Meters - 1 Meter = 3.2808 Feet 1 BTU/HR/FT = 0.9616 Watts/Meter 10.7639 Sq. Feet = 1 Square Meter 1 Lbs = 0.4536 Kg (Kilograms) 1 Inch = 25.4 mm (Millimeters) 8
Chart PD-1 — Gallons Per Minute of Hot Water Required Chart PD-1 can be used to determine the approximate gpm required for the desired MBh with various water temperature drops. The example shown below may also be used to determine gpm. Example 18.1 MBh 10 F temperature drop 0.206 Factor from formula 18.1 x .206 = 3.73 GPM GPM = BTU *500 x Water Temperature Drop Performance Data *The weight of a U.S. gallon of water at 60 F is 8.33 pounds. At a flow rate of 1 U.S. gpm, the weight of the water circulated through the system in one hour is 1.0 x 8.33 multiplied by 60 minutes = 500 pounds. Chart PD-2 may be used to approximate the gpm required for various MBh and temperature drops. Table PD-1 — Correction Factors for Non-Standard Average Water Temperatures Average Entering Air Temperature Water Temp. 45 F 50 F 55 F 60 F 65 F 70 F 75 F 80 F 85 F (F) (C) 7 C 10 C 13 C 16 C 18 C 21 C 24 C 27 C 29 C 170 77 .82 .77 .72 .67 .61 .57 .53 .48 .44 180 82 .91 .86 .81 .75 .69 .65 .61 .56 .52 190 88 1.00 .94 .89 .84 .78 .73 .69 .64 .60 200 93 1.09 1.03 .97 .92 .86 .81 .77 .72 .68 210 99 1.18 1.12 1.06 1.01 .95 .90 .85 .80 .76 220 104 1.27 1.21 1.15 1.09 1.05 .98 .93 .88 .84 230 110 1.37 1.30 1.24 1.19 1.14 1.08 1.03 .98 .93 240 116 1.47 1.41 1.35 1.29 1.25 1.17 1.12 1.07 1.02 250 121 1.57 1.50 1.44 1.38 1.32 1.26 1.20 1.15 1.10 260 127 1.67 1.60 1.52 1.46 1.40 1.34 1.29 1.24 1.20 270 132 1.78 1.70 1.62 1.56 1.50 1.44 1.39 1.34 1.29 280 138 1.88 1.80 1.72 1.66 1.60 1.54 1.48 1.43 1.38 290 143 1.98 1.90 1.82 1.75 1.69 1.63 1.58 1.52 1.48 300 Notes: 149 2.08 2.00 1.92 1.85 1.79 1.73 1.67 1.62 1.57 To determine capacity of non-standard conditions, apply the correction factor to convector capacities at 215 F steam ratings (6.895 kPa steam). 1 MBh equals 1000 Btu. 1 EDR – (215 F steam) equals 240 Btu. 9 Chart PD-2 — Gallons Per Minute for Various MBh and Temperature Drops Table PD-2 — Factors Used to Convert 1 PSI Steam Ratings to Hot Water Ratings at Temperatures Indicated Average Water Temperature Correction (F) (C) Factor 100 F 38 C 0.15 110 F 43 C 0.20 120 F 49 C 0.26 130 F 54 C 0.33 140 F 60 C 0.40 150 F 66 C 0.45 155 F 68 C 0.49 160 F 71 C 0.53 165 F 74 C 0.57 170 F 77 C 0.61 175 F 79 C 0.65 180 F 82 C 0.69 185 F 85 C 0.73 190 F 88 C 0.78 195 F 91 C 0.82 200 F 93 C 0.86 205 F 96 C 0.91 210 F 99 C 0.95 215 F 102 C 1.00 220 F 104 C 1.05 225 F 107 C 1.09 230 F 110 C 1.14 235 F 113 C 1.20 240 F 116 C 1.25 Note: To determine capacity at non-standard conditions, multiply the corresponding factor above by the EDR steam rating found on pages 10-11.
Page 1 and 2: Architectural Radiation Convectors
Page 3 and 4: Panel Construction Features The fro
Page 5 and 6: Floor standing recessed unit. Featu
Page 7: Selection Procedure Hot Water Syste
Page 11 and 12: Performance Data Convector Steam Ra
Page 13 and 14: Performance Data 13 Hot Water Model
Page 19 and 20: Performance Data 19 Model W, FK, FG
Page 21 and 22: Performance Data 21 Model AK, AG*,
Page 23 and 24: Performance Data 23 Model AK, AG*,
Page 25 and 26: Table DD-4 — Minimum Unit Height
Page 27 and 28: General The contractor shall furnis

FIN-DS-2 (7/98) Data Catalog - Trane

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