TEMPERATURE-VOLUME CORRECTIONS FOR ASPHALTIC MATERIALS (CUSTOMARY UNITS)
LEGEND: t = Observed Temperature in Degrees Fahrenheit
M = Multiplier for Correcting Oil Volumes to the Basis of 60°F
t M |
t M |
t M |
t M |
t M |
0 1.0241 |
50 1.0040 |
100 0.9842 |
150 0.9647 |
200 0.9456 |
1 1.0237 |
51 1.0036 |
101 0.9838 |
151 0.9643 |
201 0.9452 |
2 1.0233 |
52 1.0032 |
102 0.9834 |
152 0.9639 |
202 0.9448 |
3 1.0229 |
53 1.0028 |
103 0.9830 |
153 0.9635 |
203 0.9444 |
4 1.0225 |
54 1.0024 |
104 0.9826 |
154 0.9632 |
204 0.9441 |
5 1.0221 |
55 1.0020 |
105 0.9822 |
155 0.9628 |
205 0.9437 |
6 1.0217 |
56 1.0016 |
106 0.9818 |
156 0.9624 |
206 0.9433 |
7 1.0213 |
57 1.0012 |
107 0.9814 |
157 0.9620 |
207 0.9429 |
8 1.0209 |
58 1.0008 |
108 0.9810 |
158 0.9616 |
208 0.9425 |
9 1.0205 |
59 1.0004 |
109 0.9806 |
159 0.9612 |
209 0.9422 |
10 1.0201 |
60 1.0000 |
110 0.9803 |
160 0.9609 |
210 0.9418 |
11 1.0197 |
61 0.9996 |
111 0.9799 |
161 0.9605 |
211 0.9414 |
12 1.0193 |
62 0.9992 |
112 0.9795 |
162 0.9601 |
212 0.9410 |
13 1.0189 |
63 0.9988 |
113 0.9791 |
163 0.9597 |
213 0.9407 |
14 1.0185 |
64 0.9984 |
114 0.9787 |
164 0.9593 |
214 0.9403 |
15 1.0181 |
65 0.9980 |
115 0.9783 |
165 0.9589 |
215 0.9399 |
16 1.0177 |
66 0.9976 |
116 0.9779 |
166 0.9585 |
216 0.9395 |
17 1.0172 |
67 0.9972 |
117 0.9775 |
167 0.9582 |
217 0.9391 |
18 1.0168 |
68 0.9968 |
118 0.9771 |
168 0.9578 |
218 0.9388 |
19 1.0164 |
69 0.9964 |
119 0.9767 |
169 0.9574 |
219 0.9384 |
20 1.0160 |
70 0.9960 |
120 0.9763 |
170 0.9570 |
220 0.9380 |
21 1.0156 |
71 0.9956 |
121 0.9760 |
171 0.9566 |
221 0.9376 |
22 1.0152 |
72 0.9952 |
122 0.9756 |
172 0.9562 |
222 0.9373 |
23 1.0148 |
73 0.9948 |
123 0.9752 |
173 0.9559 |
223 0.9369 |
24 1.0144 |
74 0.9944 |
124 0.9748 |
174 0.9555 |
224 0.9365 |
25 1.0140 |
75 0.9940 |
125 0.9744 |
175 0.9551 |
225 0.9361 |
26 1.0136 |
76 0.9936 |
126 0.9740 |
176 0.9547 |
226 0.9358 |
27 1.0132 |
77 0.9932 |
127 0.9736 |
177 0.9543 |
227 0.9354 |
28 1.0128 |
78 0.9929 |
128 0.9732 |
178 0.9539 |
228 0.9350 |
29 1.0124 |
79 0.9925 |
129 0.9728 |
179 0.9536 |
229 0.9346 |
30 1.0120 |
80 0.9921 |
130 0.9725 |
180 0.9532 |
230 0.9343 |
31 1.0116 |
81 0.9917 |
131 0.9721 |
181 0.9528 |
231 0.9339 |
32 1.0112 |
82 0.9913 |
132 0.9717 |
182 0.9524 |
232 0.9335 |
33 1.0108 |
83 0.9909 |
133 0.9713 |
183 0.9520 |
233 0.9331 |
34 1.0104 |
84 0.9905 |
134 0.9709 |
184 0.9517 |
234 0.9328 |
35 1.0100 |
85 0.9901 |
135 0.9705 |
185 0.9513 |
235 0.9324 |
36 1.0096 |
86 0.9897 |
136 0.9701 |
186 0.9509 |
236 0.9320 |
37 1.0092 |
87 0.9893 |
137 0.9697 |
187 0.9505 |
237 0.9316 |
38 1.0088 |
88 0.9889 |
138 0.9693 |
188 0.9501 |
238 0.9313 |
39 1.0084 |
89 0.9885 |
139 0.9690 |
189 0.9498 |
239 0.9309 |
40 1.0080 |
90 0.9881 |
140 0.9686 |
190 0.9494 |
240 0.9305 |
41 1.0076 |
91 0.9877 |
141 0.9682 |
191 0.9490 |
241 0.9301 |
42 1.0072 |
92 0.9873 |
142 0.9678 |
192 0.9486 |
242 0.9298 |
43 1.0068 |
93 0.9869 |
143 0.9674 |
193 0.9482 |
243 0.9294 |
44 1.0064 |
94 0.9865 |
144 0.9670 |
194 0.9478 |
244 0.9290 |
45 1.0060 |
95 0.9861 |
145 0.9666 |
195 0.9475 |
245 0.9286 |
46 1.0056 |
96 0.9857 |
146 0.9662 |
196 0.9471 |
246 0.9283 |
47 1.0052 |
97 0.9854 |
147 0.9659 |
197 0.9467 |
247 0.9279 |
48 1.0048 |
98 0.9850 |
148 0.9655 |
198 0.9463 |
248 0.9275 |
49 1.0044 |
99 0.9846 |
149 0.9651 |
199 0.9460 |
249 0.9272 |
TEMPERATURE-VOLUME CORRECTIONS FOR ASPHALTIC MATERIALS (CUSTOMARY UNITS)
LEGEND: t = Observed Temperature in Degrees Fahrenheit
M = Multiplier for Correcting Oil Volumes to the Basis of 60°F
t M |
t M |
t M |
t M |
t M |
250 0.9268 |
300 0.9083 |
350 0.8902 |
400 0.8724 |
450 0.8550 |
251 0.9264 |
301 0.9080 |
351 0.8899 |
401 0.8721 |
451 0.8547 |
252 0.9260 |
302 0.9076 |
352 0.8895 |
402 0.8717 |
452 0.8543 |
253 0.9257 |
303 0.9072 |
353 0.8891 |
403 0.8714 |
453 0.8540 |
254 0.9253 |
304 0.9069 |
354 0.8888 |
404 0.8710 |
454 0.8536 |
255 0.9249 |
305 0.9065 |
355 0.8884 |
405 0.8707 |
455 0.8533 |
256 0.9245 |
306 0.9061 |
356 0.8881 |
406 0.8703 |
456 0.8529 |
257 0.9242 |
307 0.9058 |
357 0.8877 |
407 0.8700 |
457 0.8526 |
258 0.9238 |
308 0.9054 |
358 0.8873 |
408 0.8696 |
458 0.8522 |
259 0.9234 |
309 0.9050 |
359 0.8870 |
409 0.8693 |
459 0.8519 |
260 0.9231 |
310 0.9047 |
360 0.8866 |
410 0.8689 |
460 0.8516 |
261 0.9227 |
311 0.9043 |
361 0.8863 |
411 0.8686 |
461 0.8512 |
262 0.9223 |
312 0.9039 |
362 0.8859 |
412 0.8682 |
462 0.8509 |
263 0.9219 |
313 0.9036 |
363 0.8856 |
413 0.8679 |
463 0.8505 |
264 0.9216 |
314 0.9032 |
364 0.8852 |
414 0.8675 |
464 0.8502 |
265 0.9212 |
315 0.9029 |
365 0.8848 |
415 0.8672 |
465 0.8498 |
266 0.9208 |
316 0.9025 |
366 0.8845 |
416 0.8668 |
466 0.8495 |
267 0.9205 |
317 0.9021 |
367 0.8841 |
417 0.8665 |
467 0.8492 |
268 0.9201 |
318 0.9018 |
368 0.8838 |
418 0.8661 |
468 0.8488 |
269 0.9197 |
319 0.9014 |
369 0.8834 |
419 0.8658 |
469 0.8485 |
270 0.9194 |
320 0.9010 |
370 0.8831 |
420 0.8654 |
470 0.8481 |
271 0.9190 |
321 0.9007 |
371 0.8827 |
421 0.8651 |
471 0.8478 |
272 0.9186 |
322 0.9003 |
372 0.8824 |
422 0.8647 |
472 0.8474 |
273 0.9182 |
323 0.9000 |
373 0.8820 |
423 0.8644 |
473 0.8471 |
274 0.9179 |
324 0.8996 |
374 0.8816 |
424 0.8640 |
474 0.8468 |
275 0.9175 |
325 0.8992 |
375 0.8813 |
425 0.8637 |
475 0.8464 |
276 0.9171 |
326 0.8989 |
376 0.8809 |
426 0.8633 |
476 0.8461 |
277 0.9168 |
327 0.8985 |
377 0.8806 |
427 0.8630 |
477 0.8457 |
278 0.9164 |
328 0.8981 |
378 0.8802 |
428 0.8626 |
478 0.8454 |
279 0.9160 |
329 0.8978 |
379 0.8799 |
429 0.8623 |
479 0.8450 |
280 0.9157 |
330 0.8974 |
380 0.8795 |
430 0.8619 |
480 0.8447 |
281 0.9153 |
331 0.8971 |
381 0.8792 |
431 0.8616 |
481 0.8444 |
282 0.9149 |
332 0.8967 |
382 0.8788 |
432 0.8612 |
482 0.8440 |
283 0.9146 |
333 0.8963 |
383 0.8784 |
433 0.8609 |
483 0.8437 |
284 0.9142 |
334 0.8960 |
384 0.8781 |
434 0.8605 |
484 0.8433 |
285 0.9138 |
335 0.8956 |
385 0.8777 |
435 0.8602 |
485 0.8430 |
286 0.9135 |
336 0.8953 |
386 0.8774 |
436 0.8599 |
486 0.8427 |
287 0.9131 |
337 0.8949 |
387 0.8770 |
437 0.8595 |
487 0.8423 |
288 0.9127 |
338 0.8945 |
388 0.8767 |
438 0.8592 |
488 0.8420 |
289 0.9124 |
339 0.8942 |
389 0.8763 |
439 0.8588 |
489 0.8416 |
290 0.9120 |
340 0.8938 |
390 0.8760 |
440 0.8585 |
490 0.8413 |
291 0.9116 |
341 0.8934 |
391 0.8756 |
441 0.8581 |
491 0.8410 |
292 0.9113 |
342 0.8931 |
392 0.8753 |
442 0.8578 |
492 0.8406 |
293 0.9109 |
343 0.8927 |
393 0.8749 |
443 0.8574 |
493 0.8403 |
294 0.9105 |
344 0.8924 |
394 0.8746 |
444 0.8571 |
494 0.8399 |
295 0.9102 |
345 0.8920 |
395 0.8742 |
445 0.8567 |
495 0.8396 |
296 0.9098 |
346 0.8916 |
396 0.8738 |
446 0.8564 |
496 0.8393 |
297 0.9094 |
347 0.8913 |
397 0.8735 |
447 0.8560 |
497 0.8389 |
298 0.9091 |
348 0.8909 |
398 0.8731 |
448 0.8557 |
498 0.8386 |
299 0.9087 |
349 0.8906 |
399 0.8728 |
449 0.8553 |
499 0.8382 |
The following formula is used to create the values in the table above. This formula is used in the HMA Plant Report software: