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654
CHAPTER 28
1956 Guide
Table 1. Heat Losses from Horizontal Babe Steel Pipes
Expressed in Btu per (hour) (linear foot) (Fahrenheit degree difference between the pipe and surrounding still air at 70 F)
---------------------- r \ r
Hot Water
? '
Steam
f 120 f : - 150 F ' - 180 F
210 F
227.1 F.: 299.7 F (5 psig) (50 psig)
Nominal Pipe She ,
' '(Inches)
i ,. r
Temperature Difference--F Deo
337.9 F (100 psig)
H H l 1H r
.2 2H 3 3*4
r. 4 . . .
5 6 8 10 12
SO 80
0.455 0.555 0.084 0.847 0.958
0.495 0.605 : 0.743 : 0.619 1.041
:
1.180
. 1.400 1.680 :
1.900 2.118
1.281 1.532
1.825 2.064
2.302
2.580 3.036 - 3.880 4.760 '
5.590
2.804 3.294
.4.215 5.180 6.070
110
0.546 0.666 0.819 1.014 1.148
1.412 1.683 2.010 2.221 2.534
3.084 3.626 4.638 5.680 6.670
140
157.1
227.7
0.584 0.715 0.877 1.086 1.230
1.512 1.796 2.153 2.433 2.717
3.303 3.886 4.960 6.090 7.145
0.612
0.748 0.919
1.138
: 1.288 '
0.706
0.866 1.065 1.324 1.492
4.578 .1.883
2.260 2.552
2.850
<
1.840 2.190
2.630 2.974
3.320
3.470 4.074
5.210 6.410 '
7.500
4.050 4.765 . 6.100 7.490
8.800
267.9
0.760 0.933 . 1.147 1.425 1.633
1.987 2.363 2.840 3.215 3.590
4.385 5.160 6.610 8.116 9.530
\ Table 2. Heat Loss fbom Horizontal Tarnished Copper Pipe1
Expressed in Btuper (hour) (linear foot) (Fahrenheit degree difference between the pipe ana surrounding still air at 70 F)
Nominal Pip* Sib, (Inches)
Hot Wateb (Type K Copper Tube)
120 F
150 F
180 F
210 F
Steam (Standard Pip Bias Pipe)
227.1 F ` (5 psig)
297.7 F (50 psig)
337.9 F (100 psig)
Temperature Difference--F Dbg
50
80
no.
140
157.1
.227.7.
267.9
H H
\
Hi
m
0.250 0.340
0.440 0.500
0.580
,
6.287
0.381 0.475 0.559
0.656
0.300 0.409
0.509 0.618 0.710
0.321 0.429 0.536
0.622 0.750
0.433 0.533 0.636 . 0.764 . 0.904
-
0.500 0.543
0.746 0.878
1.053
0.530
0.654 0.803 0.934 1.120
2
2h
3 3*4 4
0.730
0.880 1.040
1.180 1.460
01..802050
1.175 1.350
1.500
0.890 1.091 1.272
1.454
1.635
0.957
1.143 1.343
1.535 1.715
1.101
1.305 1.560
1.750 1.941
1.273
1.490 1.800 .
2.020 2.240
1.364
1.605 1.940 2.170
2.430
4*4
5 6
8
. 1.600 1.840 2.400
i.kii
2.125 2.685
L980 2.270
2.910
2.071 2.430
3.110
2.131 2.387
2.740 3.310
2.465 2.770 3.210 4.050
2.650 2.990 3.440
4.370
Table 3. External Surface per Linear Foot of Pipe
Nominal Pipe Size (Inches)
H * 1 1H
Subface Abea (So Ft)
0.22 0.275 0.344 0.435 0.498
Nominal Pipe She (Inches)
2 2H 3 3*4 4
Surface Abba (Sq Ft)
0.622 0.753 0.917 1.047 1.178
Nominal Pipe Sibe (Inches)
5 6 8. 10 12
Subpace Abba (SqFt)
1.4sT 1.734 2.257 2.817 3.338
Pipe and Industrial Insulation
655
Table 4. External Surface per Linear Foot of Copper Tubing Outside diameter J^j in. greater than nominal size
Tubs Size (Inches)
H H 1 1 *4 m
Surface Abba (Sq Ft)
0.164 0.229 0.295 0.360 0.426
Tube Sue (Inches)
2 m 3 3*4 4
Subface Area (Sq Ft)
0.556 - 0.687
0.818 0.949 1.080
Tube Size (Inches)
.5g. 8
' Surface Area (Sq Ft)
1.342, ' 1.604
2.128
perature difference of 169.4 F is found to be 1.624 Btu per (hr) (linear ft) (Fdeg). The total annual heat loss from the entire line = 1.624 X 169.4 X' 165 (linear ft) X 4000 (hr) = 181,600 Mb. (Mb = 1000 Btu.)
Example S: Coal costing $11.50 per ton and having a calorific value of 13,000 Btu per pound is being burned in the furnace supplying steam to the pipe line given iri the previous example. If the system is operating at an overall efficiency of 55 percent, determine the monetary value of the annual heat loss from the line.
Solution: The cost of heat per 1000 Mb supplied to the system = 1,000,000 X 11.5 (dollars) -f- [13,000 (Btu) X 2000 0b) X 0.55 (efficiency)] = $0,804. The total cost of heat lost per year = 0.804 X 181.6 (thousand Mb) = $146.00.
INDUSTRIAL AND PIPE INSULATIONS
Insulating materials are made of various substances and are supplied in a number of different forms. Preformed insulations are made in the form of blocks for flat surfaces, segmental pieces for small cylindrical vessels and large pipes, and sectional insulation for smaller pipes. Preformed pipe insulation is regularly supplied in sectional form up to about 12-inch pipe size. Certain types up to 20-inch pipe size are available in sectional form. Sections are either split in half longitudinally Or . cut through on one side and scored on the inner surface of the other to facilitate applica tion to the pipe. Blanket insulations are used to insulate flat or curved surfaces or large pipes. Pipe fittings and bends are commonly insulated with portions of standard preformed insulations,; or, , when irregular in contour, with blankets or plastic insulating cements.
Insulation is secured to pipes, flat surfaces, and large vessels in a variety of ways depending on the contour of the surface and the form of the'in-
Table 5. Area of Flanged Fittings, Square Feet*
Nominal Pipe She (Inches)
Flanged Coupling
90 Deg Ell
Standard
Extra Heavy
Standard
Extra Heavy
Long Radius Ell
Standard
Extra Heavy
Tee `
Standard
Extra Heavy
Cboss
Standard
Extra Heavy
1 0.320 0.438 0.795 1.015 0.892 1.0S3 1;235 1.575 1.622 .2.07
IK
0.383 0.510 0.957 1.098 1.084 1.340 1.481 1.925 1.943
2.53
i*a
0.477 0.727 1.174 1.332 1.337 1.874 1.815 2.68
2.38
,3.54
0.672 0.848, 1.65
2.01
1.84
2.16
2.54
3.09
3.32 . 4.06
2*4 0.841 1.107 2.09 2.57 2.32 2.76 3.21 4.05 4.19 6.17
3
3*4 4
0.945 1.122
1.344
1.484 1.644
1.914
2.38
2.98 3.53
3.49
3.96 4.64
2.68 3.28 3.96
3.74 4.28 4.99
3.66 -
4.48 5.41
5.33 4.77 6.04 5.83 . 7.07 7.03
6.95 ,7.89-
9.24
4*4 5
1.474 2.04 3.95 5.02 4.43 5.46 6.07 7.72 7.87 10.07 1.622 2.18 4.44 5.47 5.00 6.02 6.81 8.52 8.82 10.97
6 8
1.82 2.78 2.41 3.77
5.13 6.98
6.99 9.76.
5.99 8.56
7.76 11.09
7.84 10.55
10.64 14.74
10.08 13.44
13.75 18.97
3.43 5.20 10.18 13.58 12.35 15.60 15.41 20.41 19.58
26.26
4.41 6.71 13.08 17.73 16.35 18.76 19.67 26.65 24.87
34.11
* Including areas of accompanying flanges bolted to the fitting.