Table showing heat loss from bare black steel pipes
Note: The conditions applying to this table are.
- Horizontal pipes
- Ambient Air at 20 deg. C
- Emissivity value used = 0,9
- Ambient Ambient air Velocity = 0 m/s
- Pipe contents temperature as shown
Pipe OD |
Heat Loss from black steel bare pipe (W /m - W/m2 from flat ) |
Pipe Temperature ( Deg. C) |
50 |
100 |
150 |
200 |
250 |
300 |
350 |
400 |
450 |
500 |
550 |
600 |
650 |
700 |
17,2 |
23 |
78 |
150 |
241 |
353 |
491 |
658 |
859 |
1099 |
1384 |
1720 |
2113 |
2571 |
3100 |
21,3 |
27 |
93 |
180 |
290 |
427 |
594 |
798 |
1043 |
1337 |
1687 |
2099 |
2583 |
3146 |
3798 |
26,9 |
33 |
114 |
221 |
356 |
525 |
732 |
985 |
1291 |
1658 |
2095 |
2611 |
3217 |
3923 |
4742 |
33,7 |
41 |
139 |
269 |
435 |
641 |
897 |
1209 |
1588 |
2042 |
2585 |
3226 |
3979 |
4859 |
5878 |
42,4 |
50 |
169 |
329 |
532 |
788 |
1104 |
1491 |
1961 |
2527 |
3203 |
4004 |
4945 |
6045 |
7320 |
48,3 |
56 |
190 |
369 |
598 |
885 |
1242 |
1679 |
2212 |
2853 |
3619 |
4527 |
5595 |
6843 |
8292 |
60,3 |
68 |
230 |
448 |
728 |
1081 |
1519 |
2058 |
2715 |
3508 |
4456 |
5582 |
6908 |
8458 |
10258 |
76,1 |
83 |
283 |
551 |
896 |
1333 |
1878 |
2550 |
3370 |
4360 |
5548 |
6958 |
8621 |
10566 |
12827 |
88,9 |
95 |
324 |
632 |
1031 |
1535 |
2165 |
2943 |
3894 |
5044 |
6424 |
8064 |
9998 |
12263 |
14897 |
101,6 |
107 |
365 |
712 |
1162 |
1733 |
2447 |
3330 |
4410 |
5718 |
7287 |
9155 |
11358 |
13940 |
16942 |
114,3 |
119 |
405 |
791 |
1292 |
1929 |
2726 |
3714 |
4922 |
6387 |
8147 |
10241 |
12713 |
15609 |
18979 |
139,7 |
142 |
484 |
947 |
1549 |
2316 |
3279 |
4474 |
5939 |
7716 |
9853 |
12399 |
15406 |
18932 |
23036 |
168,3 |
167 |
571 |
1119 |
1833 |
2746 |
3894 |
5321 |
7072 |
9200 |
11760 |
14812 |
18420 |
22653 |
27582 |
219,1 |
212 |
722 |
1419 |
2330 |
3498 |
4971 |
6806 |
9063 |
11809 |
15117 |
19065 |
23736 |
29220 |
35609 |
273,0 |
258 |
880 |
1731 |
2848 |
4283 |
6098 |
8362 |
11152 |
14550 |
18647 |
24221 |
30135 |
37067 |
45134 |
323,9 |
301 |
1027 |
2021 |
3331 |
5016 |
7151 |
10254 |
13667 |
17813 |
22798 |
28737 |
35754 |
43978 |
53549 |
Flat |
285 |
1212 |
2405 |
3949 |
5897 |
8317 |
11286 |
14890 |
19226 |
24396 |
30515 |
37700 |
46081 |
55794 |
Table showing heat loss from insulated pipes (100 deg.C and 200 deg C contents temp)
Note: The conditions applying to this table are.
- Horizontal pipes
- Ambient Air at 20 deg. C
- Emissivity value used = 0,05
- Ambient air Velocity = 0 m/s
- Pipe Contents temp as shown
The basis used for determining the insulation thickness is to minimise heat loss
on a sound economic basis.
|
Pipe contents temperature = 100 Deg.C |
|
Pipe contents temperature = 200 Deg.C |
Pipe OD |
Insulation Thickness (mm) |
Heat Loss |
Insulation Thickness (mm) |
Heat Loss |
|
k=0,02 |
k=0,03 |
k=0,04 |
k=0,05 |
k=0,06 |
(W/m) |
k=0,03 |
k=0,04 |
k=0,05 |
k=0,06 |
k=0,07 |
(W/m) |
17,2 |
11 |
22 |
40 |
72 |
125 |
10,4 |
20 |
36 |
63 |
106 |
176 |
24,8 |
21,3 |
12 |
24 |
44 |
76 |
128 |
11,1 |
22 |
40 |
67 |
109 |
176 |
26,5 |
26,9 |
14 |
27 |
47 |
78 |
128 |
12,1 |
25 |
43 |
71 |
113 |
176 |
28,6 |
33,7 |
15 |
29 |
50 |
80 |
128 |
13,2 |
28 |
47 |
76 |
118 |
179 |
30,8 |
42,4 |
17 |
32 |
53 |
83 |
128 |
14,5 |
32 |
52 |
81 |
123 |
183 |
33,3 |
48,3 |
18 |
33 |
55 |
85 |
129 |
15,3 |
34 |
55 |
84 |
126 |
185 |
34,9 |
60,3 |
20 |
36 |
58 |
88 |
130 |
16,8 |
37 |
60 |
90 |
132 |
189 |
37,9 |
76,1 |
23 |
39 |
62 |
92 |
131 |
18,7 |
41 |
64 |
95 |
136 |
191 |
41,8 |
88,9 |
24 |
42 |
65 |
94 |
133 |
20,1 |
44 |
68 |
100 |
141 |
195 |
44,5 |
101,6 |
26 |
45 |
67 |
96 |
134 |
21,5 |
47 |
71 |
103 |
144 |
197 |
47,2 |
114,3 |
27 |
48 |
69 |
98 |
136 |
22,8 |
49 |
74 |
106 |
147 |
198 |
49,9 |
139,7 |
29 |
49 |
72 |
101 |
137 |
25,4 |
53 |
79 |
111 |
152 |
202 |
54,8 |
168,3 |
31 |
52 |
77 |
107 |
143 |
27,8 |
57 |
85 |
118 |
159 |
209 |
59,6 |
219,1 |
34 |
56 |
81 |
110 |
145 |
32,5 |
63 |
92 |
126 |
167 |
216 |
68,1 |
244,5 |
35 |
57 |
82 |
112 |
146 |
34,8 |
65 |
94 |
129 |
169 |
217 |
72,6 |
273,0 |
37 |
59 |
85 |
114 |
149 |
37,1 |
68 |
98 |
133 |
174 |
222 |
76,6 |
323,9 |
38 |
61 |
87 |
117 |
150 |
41,5 |
71 |
102 |
138 |
179 |
226 |
84,5 |
355,6 |
39 |
62 |
89 |
118 |
151 |
44,2 |
73 |
105 |
141 |
181 |
228 |
89,4 |
406,4 |
41 |
65 |
91 |
121 |
153 |
48,2 |
76 |
107 |
143 |
183 |
229 |
97,5 |
457,0 |
42 |
66 |
92 |
122 |
154 |
52,5 |
78 |
110 |
146 |
186 |
233 |
105,3 |
508,0 |
43 |
68 |
95 |
124 |
157 |
56,2 |
80 |
113 |
149 |
189 |
237 |
112,3 |
610 + |
49 |
77 |
107 |
141 |
177 |
59,4 |
89 |
125 |
167 |
211 |
260 |
120,6 |
Note: The heat transfer for the 610mm pipe can be used with reasonable accuracy for horizontal plates
with the same surface areas as the mean area of the insulated pipes = L.π (D2 - D1) /ln(D2/D1)
Table showing heat loss from insulated pipes (300 deg.C and 400 deg C contents temp.)
Note: The conditions applying to this table are.
- Horizontal pipes
- Ambient Air at 20 deg. C
- Emissivity value used = 0,05
- Ambient air Velocity = 0 m/s
- Pipe Contents temp as shown
The basis used for determining the insulation thickness is to minimise heat loss
on a sound economic basis.
|
Pipe contents temperature = 300 Deg.C |
|
Pipe contents temperature = 400 Deg.C |
Pipe OD |
Insulation Thickness (mm) |
Heat Loss |
Insulation Thickness (mm) |
Heat Loss |
|
k=0,03 |
k=0,04 |
k=0,05 |
k=0,06 |
k=0,07 |
(W/m) |
k= 0,04 |
k= 0,05 |
k= 0,06 |
k= 0,07 |
k= 0,08 |
(W/m) |
17,2 |
23 |
43 |
75 |
129 |
218 |
36,5 |
33 |
56 |
92 |
148 |
236 |
55,3 |
21,3 |
26 |
46 |
79 |
132 |
218 |
38,9 |
36 |
60 |
96 |
151 |
238 |
58,9 |
26,9 |
29 |
51 |
84 |
137 |
218 |
41,8 |
41 |
65 |
96 |
151 |
238 |
63,0 |
33,7 |
32 |
55 |
90 |
141 |
219 |
45,0 |
45 |
71 |
108 |
163 |
241 |
67,6 |
42,4 |
36 |
60 |
96 |
148 |
223 |
48,5 |
51 |
78 |
118 |
173 |
251 |
72,2 |
48,3 |
39 |
64 |
100 |
152 |
227 |
50,6 |
54 |
83 |
123 |
179 |
256 |
75,1 |
60,3 |
43 |
70 |
108 |
161 |
235 |
54,5 |
60 |
91 |
133 |
189 |
267 |
80,5 |
76,1 |
48 |
76 |
114 |
167 |
237 |
59,7 |
66 |
98 |
140 |
196 |
270 |
87,8 |
88,9 |
51 |
80 |
119 |
171 |
241 |
63,5 |
70 |
103 |
145 |
201 |
273 |
93.,4 |
101,6 |
53 |
83 |
122 |
173 |
240 |
67,5 |
74 |
107 |
150 |
204 |
274 |
98,7 |
114,3 |
56 |
87 |
126 |
177 |
242 |
71,1 |
77 |
111 |
153 |
207 |
276 |
120,9 |
139,7 |
61 |
93 |
134 |
185 |
250 |
77,3 |
84 |
119 |
163 |
217 |
285 |
112,5 |
168,3 |
67 |
100 |
142 |
194 |
259 |
83,6 |
92 |
128 |
174 |
229 |
297 |
120,9 |
219,1 |
73 |
108 |
151 |
202 |
264 |
95,4 |
100 |
139 |
185 |
240 |
308 |
136,9 |
244,5 |
76 |
112 |
154 |
206 |
267 |
101,1 |
105 |
144 |
191 |
246 |
315 |
143,9 |
273,0 |
80 |
116 |
160 |
212 |
273 |
106,5 |
109 |
149 |
196 |
251 |
319 |
152,1 |
323,9 |
84 |
121 |
165 |
216 |
275 |
117,5 |
114 |
154 |
200 |
257 |
321 |
167,6 |
355,6 |
85 |
123 |
166 |
217 |
277 |
117,5 |
117 |
158 |
204 |
262 |
325 |
175,8 |
406,4 |
89 |
127 |
170 |
220 |
280 |
135,2 |
121 |
162 |
211 |
266 |
327 |
190,5 |
457,0 |
92 |
131 |
175 |
226 |
286 |
144,5 |
126 |
170 |
218 |
272 |
333 |
203,1 |
508,0 |
94 |
134 |
181 |
230 |
287 |
154,9 |
130 |
173 |
222 |
275 |
336 |
216,7 |
610 + |
100 |
147 |
195 |
249 |
308 |
168,0 |
141 |
186 |
236 |
292 |
354 |
237,2 |
Note: The heat transfer for the 610mm pipe can be used with reasonable accuracy for horizontal plates
with the same surface areas as the mean area of the insulated pipes = L.π (D2 - D1) /ln(D2/D1)
Table showing heat loss from insulated pipes (500 deg.C and 600 deg C)
Note: The conditions applying to this table are.
- Horizontal pipes
- Ambient Air at 20 deg. C
- Emissivity value used = 0,05
- Ambient air Velocity = 0 m/s
- Pipe Contents temp as shown
The basis used for determining the insulation thickness is to minimise heat loss
on a sound economic basis.
|
Pipe contents temperature = 500 Deg.C |
|
Pipe contents temperature = 600 Deg.C |
Pipe OD |
Insulation Thickness (mm) |
Heat Loss |
Insulation Thickness (mm) |
Heat Loss |
|
k= 0,05 |
k= 0,06 |
k= 0,07 |
k= 0,08 |
k= 0,09 |
(W/m) |
k= 0,06 |
k= 0,07 |
k= 0,08 |
k= 0,09 |
k= 0,10 |
(W/m) |
17,2 |
43 |
69 |
107 |
165 |
252 |
77,2 |
42 |
62 |
90 |
130 |
186 |
112,1 |
21,3 |
48 |
74 |
113 |
170 |
253 |
81,9 |
47 |
67 |
96 |
136 |
191 |
118,7 |
26,9 |
53 |
81 |
121 |
178 |
260 |
87,2 |
52 |
74 |
104 |
144 |
199 |
126,4 |
33,7 |
59 |
88 |
128 |
185 |
265 |
93,1 |
57 |
79 |
110 |
149 |
202 |
135,8 |
42,4 |
65 |
95 |
136 |
193 |
270 |
100,0 |
65 |
90 |
123 |
164 |
220 |
143,3 |
48,3 |
69 |
100 |
142 |
199 |
276 |
103,9 |
70 |
95 |
129 |
172 |
228 |
148,6 |
60,3 |
77 |
110 |
154 |
213 |
290 |
110,8 |
78 |
101 |
141 |
186 |
242 |
158,3 |
76,1 |
84 |
118 |
163 |
220 |
295 |
120,5 |
85 |
113 |
150 |
194 |
250 |
172,0 |
88,9 |
90 |
125 |
170 |
228 |
301 |
127,3 |
91 |
121 |
158 |
203 |
258 |
181,4 |
101,6 |
94 |
130 |
179 |
235 |
305 |
141,2 |
97 |
127 |
164 |
210 |
265 |
190,2 |
114,3 |
98 |
134 |
179 |
235 |
305 |
141,2 |
101 |
132 |
170 |
215 |
270 |
199,2 |
139,7 |
107 |
144 |
191 |
248 |
317 |
152,0 |
111 |
143 |
182 |
228 |
283 |
214,2 |
168,3 |
116 |
155 |
203 |
260 |
334 |
163,2 |
121 |
155 |
195 |
243 |
302 |
229,1 |
219,1 |
127 |
168 |
216 |
276 |
345 |
183,6 |
134 |
170 |
211 |
263 |
320 |
255,7 |
244,5 |
133 |
174 |
223 |
284 |
353 |
192,4 |
139 |
176 |
221 |
270 |
327 |
268,2 |
273,0 |
138 |
181 |
228 |
292 |
361 |
202,1 |
146 |
184 |
230 |
280 |
338 |
280,4 |
323,9 |
144 |
189 |
239 |
297 |
364 |
221,6 |
154 |
193 |
237 |
287 |
343 |
306,9 |
355,6 |
149 |
194 |
244 |
302 |
368 |
232,6 |
160 |
200 |
244 |
294 |
351 |
320,4 |
406,4 |
154 |
200 |
251 |
308 |
373 |
250,2 |
165 |
204 |
248 |
297 |
352 |
347,0 |
457,0 |
161 |
206 |
256 |
313 |
376 |
267,6 |
172 |
213 |
258 |
308 |
363 |
366,7 |
508,0 |
165 |
210 |
261 |
317 |
380 |
284,7 |
178 |
220 |
265 |
315 |
370 |
387,9 |
610 + ** |
180 |
228 |
281 |
340 |
405 |
308,6 |
195 |
239 |
287 |
340 |
397 |
418,6 |
Note: The heat transfer for the 610mm pipe can be used with reasonable accuracy for horizontal plates
with the same surface areas as the mean area of the insulated pipes = L.π (D2 - D1) /ln(D2/D1)
Table showing heat loss from insulated pipes (700 deg C contents temp)
Note: The conditions applying to this table are.
- Horizontal pipes
- Ambient Air at 20 deg. C
- Emissivity value used = 0,05
- Ambient air Velocity = 0 m/s
- Pipe Contents temp as shown
The basis used for determining the insulation thickness is to minimise heat loss
on a sound economic basis.
|
Pipe contents Pipe contents temperature = 700 Deg.C |
Pipe OD |
Insulation Thickness (mm) |
Heat Loss |
|
k= 0,07 |
k= 0,08 |
k= 0,09 |
k= 0,10 |
k= 0,11 |
(W/m) |
17,2 |
52 |
73 |
103 |
145 |
202 |
141,1 |
21,3 |
56 |
79 |
110 |
152 |
209 |
149,1 |
26,9 |
63 |
87 |
119 |
162 |
218 |
158,3 |
33,7 |
68 |
93 |
125 |
167 |
221 |
169,9 |
42,4 |
78 |
105 |
139 |
184 |
240 |
179,2 |
48,3 |
83 |
111 |
146 |
191 |
248 |
185,9 |
60,3 |
93 |
123 |
160 |
206 |
265 |
197,4 |
76,1 |
102 |
132 |
170 |
216 |
273 |
213,8 |
88,9 |
109 |
140 |
179 |
226 |
283 |
224,9 |
101,6 |
115 |
147 |
186 |
233 |
290 |
235,9 |
114,3 |
119 |
152 |
191 |
238 |
300 |
247,0 |
139,7 |
131 |
165 |
206 |
254 |
315 |
264,6 |
168,3 |
143 |
179 |
221 |
274 |
333 |
282,0 |
219,1 |
158 |
195 |
242 |
293 |
352 |
314,0 |
244,5 |
164 |
204 |
250 |
302 |
361 |
328,6 |
273,0 |
169 |
214 |
260 |
312 |
371 |
343,9 |
323,9 |
182 |
223 |
268 |
320 |
377 |
375,0 |
355,6 |
186 |
227 |
272 |
323 |
380 |
394,6 |
406,4 |
194 |
236 |
281 |
333 |
389 |
421,5 |
457,0 |
203 |
245 |
292 |
343 |
400 |
445,7 |
508,0 |
210 |
253 |
300 |
351 |
408 |
470,5 |
610 + |
230 |
275 |
325 |
380 |
439 |
506,1 |
|