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Chapter 45________________________ ,_________ 1945 Guide
the floor above, and down the outside walls. In this way the walls and ceiling become heating panels.
If water is used as the medium, the pipes through which the water circulates--almost always under forced circulation--are placed in the floor, walls, or ceiling in such a manner that as much as possibleof the heat emitted by the pipes will be delivered to the space to be heated.
Table 2. Total Heat Emission by Radiation3
.Bout . Radiation in Btu per square foot per hour
OB emitted to surroundings with a tempera-
Msat rare of absolute aero by bodies at various
Radiant -temperatures and with emissivity factor e'
Tbmpeb-
ATUBB
Dbg F
e
. .1.00
t
,0.95
e 0.90
e
0.80
Bodt OB
Mban Radiant iBMPKE-
Dbg F
Radiation in Btu per square foot per hour,emitted . to surroundings with a temperature of absolute sero bv -bodies at .various temDeratures and with emissivity factor e
ee 1.00 0.95 0.90 0.80
30 35 40. 45 46 47 48 49 50 51 52 53 . 54 55 56 57' 58 59 60 61 62 63 64 65
66 67 68 69 70
. 99.7 103.9 108.0 112.5 113.3 114.3 115:2 116.0 116.9 117.9 118.8 119.8 120.6 121.7 122.6 123.5 124.4 125.3 126.3 127.1 128.2
129.1 130.1 131.0 132.1 133.0 134.0 135.0 136.0
94.7 98.7 102.8 106.9 107.7 108.6 109.5 110.3
111.0
112.0 112.9 113.8 114.6 115.5 116.4 117.4 118.2 119.0 119.9 120.7 121.8 122.6 123.5 124.4 125.5 126.4 127.3 128.3 129.3
89.8 79.7 93.6 83.1 97.2 86.4
101.3 89.0 102.0 90.8 102.9 91.5
103.8 92.3 104.5 92.8 105.3 93.6 .106.4 94.4
106.9 95.1 107.8 95.9
108.6 96.6 109.4 97.3 110.3 98.1 111.3 98.9 112.0 99.6 112.8. 100.3 113.8 101.1 114.4 101.8 115.3 102.6 116.2 103.3 117.1 104.1
117.9 104.8 118.8 105.8 119.7 106.4 120.5 .107.2 121.5 108.0 122.3 108.8
. 71 72 73 74 75 80 85 90
100 110 . 120 130 140 150. 160 170 180 190 200 210 220 250 300 350 400 450 500 550 600
137.0 137.9 138.9 140.2 141.6 147.2 . 152.9 . 158.5 170.3 182.3 195.6 210.9 . 224.1 238.0 252.1 271.6 289.1 307.7 326.5 349.3 373.0 439.5 577.3 743.0 945.8 1181.0 1470.0 1798.0 2181.0
130.1 131.0 132.0 133.1 134.4 140.0 145.2 150.5 ' 161.7 173.2 185.7 200.4 212.9 226.1 239.8 258.0 274.9 292.1 310.2
331.9 354.4 417.6 548.2 705.8 898; 5 1121.0 1396.0 1708.0 2072.0
123.3 109.7 124.0 110.3
124.9 111.0 126.1 112.1 127.4 113.2 132.5 117.9 137.6 122.4 142.7 126.9 153.2 136.2 164.2 146.0
176.1 . 156.5 189.8 168.8 201.8 179.2 214.4 190.5 226.9 201.8 244.5 217.2. 260.1 .231.3 276.9 246.1 293.9 261.3 314.3 279.5 335.7 298.2 395.6 351.6 519.6 461.8 668.6 594.3 850.8 756.5 1063.0 944.0 1323.0 1176.0 1619.0 1439.0
1962.0 1745.0
These'factors are calculated from the formula
/ 0.173 X T*\ * \ 100.000,000 /
where
ffr * total radiation, Btu per (sq ft) (hr) e = emissivity. T = absolute temperature, degrees' Fahrenheit.
Practical limits for surface temperature of heating panels -are given in Table 3.
In this example water will be selected as the medium.
8. Determine the size, length, and location of the pipe coils in the panels.
When hot-water pipes are imbedded in concrete slabs or attached to plastered surfaces, their rate of heat emission varies with many factors. If the pipes are imbedded in dense concrete slabs, it may be assumed that the rate of heat emission of 3'2-in. pipe, spaced 6 in. on centers; %-in. pipe, spaced 9 in. on centers; arid 1-in. pipe spaced 12 in. on centers; per foot of length of pipe and per degree difference between the temperature of the water in. the pipe and that of the air in the space to be heated, is
Panel Heating and Radianl lleatih.fi--.--------,---- '
--------
- --:----------------- 769 -
0.8, 1.0, and 1.2 Btuh, respectively. If the distance between the pipes is increased, the rate of heat emission, per foot of pipe, is also increased; if the distance is doubled, the rate of heat emission is increased about 15 per cent. If the pipes are attached to plastered ceilings, the rate of heat emission is slightly less, probably about 10 per cent less, than when the pipes are imbedded in concrete slabs. The data given regarding heat emission of panels are intended as general guides for the designer. Ad ditional experience and research are needed to develop definite and complete data. However, after a heating panel has been designed and installed, any small error can easily be corrected by modifying the tem perature of the water circulating through the coils.
When the heating pipes are attached to a plastered ceiling, a portion of the heat emitted by the pipes is delivered to the space below the ceiling and a portion to the space above the ceiling. The relative quantities depend on the degree of insulation applied above the heating coils.
When the heating pipes are imbedded in a concrete floor slab a portion
Table 3. Highest Safe Surface Temperatures for Heating Panel
Type of Panel
Plastered Ceiling (Pipes Imbedded)___ _____________________ Plastered Walls (Pipes Imbedded)-_________ 1 ______________ Floor, Any Method........ -............... ................... ................. -...... Floor, Border and Aisles-- ............ ..... 1.......................................... Iron, Hot Water Medium. ......................................................... Iron, Steam Vapor3.______________ __________________ _________ Electrically Heated Panels3--________ ____________ ______ ____
Surface Temperature Deg F
115 120, 90 120 160 180 200
Low surface temperature radiation is recommended regardless of the heating medium employed.
of the heat emitted by the pipes will flow upward into the space to be heated, and the remainder will flow downward into the ground.
When the heating pipes are placed below the concrete floor slab instead '
of being imbedded in the slab, a larger portion of the heat will flow into
the ground, and a smaller portion into the space to be heated.'
'
In the following example it is assumed that the insulation above the pipe coils is such that 90 per cent of the heat emitted by the pipe coils willflow into the room and 10 per cent into the space above.
Since the room is to receive 35,117 Btuh, and since the room is assumed to receive only 90 per cent of the heat emitted by the coils attached to the plastered ceiling, the coils must emit 35,117/0.9 or 39,000 Btuh. If %-in. pipe and a mean water temperature of 140 F are selected, the'heat . emitted, per foot of pipe, will be 0.9 (140 -- 68) or 65 Btuh. The quantity,
of pipe required will therefore be 39,000/65 = 600 lineal feet.
The pipe coils can be arranged in any convenient manner, but should be arranged so that the temperature of the water in the pipe will vary only slightly; otherwise, the temperature distribution over the ceiling will not be uniform. Generally, it is best to arrange the pipes so as to form twopipe reversed-retum systems, as suggested by the two sketches in Fig. 10. By using-33 Funs of %-in. pipe, welded to two \]4. in. mains, sufficient pipe surface is secured; the %-in. pipes will then be spaced about 8)4 in. on centers,- which is satisfactory.
The friction heads of water flowing in pipes and fittings are so well . known that the pipe coils can be designed so that each will receive its