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 1.0211 |
50 1.0035 |
100 0.9861 |
150 0.9689 |
200 0.9520 |
1 1.0208 |
51 1.0031 |
101 0.9857 |
151 0.9686 |
201 0.9516 |
2 1.0204 |
52 1.0028 |
102 0.9854 |
152 0.9682 |
202 0.9513 |
3 1.0201 |
53 1.0024 |
103 0.9851 |
153 0.9679 |
203 0.9509 |
4 1.0197 |
54 1.0021 |
104 0.9847 |
154 0.9675 |
204 0.9506 |
5 1.0194 |
55 1.0017 |
105 0.9844 |
155 0.9672 |
205 0.9503 |
6 1.0190 |
56 1.0014 |
106 0.9840 |
156 0.9669 |
206 0.9499 |
7 1.0187 |
57 1.0010 |
107 0.9837 |
157 0.9665 |
207 0.9496 |
8 1.0183 |
58 1.0007 |
108 0.9833 |
158 0.9662 |
208 0.9493 |
9 1.0179 |
59 1.0004 |
109 0.9830 |
159 0.9658 |
209 0.9489 |
10 1.0176 |
60 1.0000 |
110 0.9826 |
160 0.9655 |
210 0.9486 |
11 1.0172 |
61 0.9997 |
111 0.9823 |
161 0.9652 |
211 0.9483 |
12 1.0169 |
62 0.9993 |
112 0.9819 |
162 0.9648 |
212 0.9479 |
13 1.0165 |
63 0.9990 |
113 0.9816 |
163 0.9645 |
213 0.9476 |
14 1.0162 |
64 0.9986 |
114 0.9813 |
164 0.9641 |
214 0.9472 |
15 1.0158 |
65 0.9983 |
115 0.9809 |
165 0.9638 |
215 0.9469 |
16 1.0155 |
66 0.9979 |
116 0.9806 |
166 0.9635 |
216 0.9466 |
17 1.0151 |
67 0.9976 |
117 0.9802 |
167 0.9631 |
217 0.9462 |
18 1.0148 |
68 0.9972 |
118 0.9799 |
168 0.9628 |
218 0.9459 |
19 1.0144 |
69 0.9969 |
119 0.9795 |
169 0.9624 |
219 0.9456 |
20 1.0141 |
70 0.9965 |
120 0.9792 |
170 0.9621 |
220 0.9452 |
21 1.0137 |
71 0.9962 |
121 0.9788 |
171 0.9618 |
221 0.9449 |
22 1.0133 |
72 0.9958 |
122 0.9785 |
172 0.9614 |
222 0.9446 |
23 1.0130 |
73 0.9955 |
123 0.9782 |
173 0.9611 |
223 0.9442 |
24 1.0126 |
74 0.9951 |
124 0.9778 |
174 0.9607 |
224 0.9439 |
25 1.0123 |
75 0.9948 |
125 0.9775 |
175 0.9604 |
225 0.9436 |
26 1.0119 |
76 0.9944 |
126 0.9771 |
176 0.9601 |
226 0.9432 |
27 1.0116 |
77 0.9941 |
127 0.9768 |
177 0.9597 |
227 0.9429 |
28 1.0112 |
78 0.9937 |
128 0.9764 |
178 0.9594 |
228 0.9426 |
29 1.0109 |
79 0.9934 |
129 0.9761 |
179 0.9590 |
229 0.9422 |
30 1.0105 |
80 0.9930 |
130 0.9758 |
180 0.9587 |
230 0.9419 |
31 1.0102 |
81 0.9927 |
131 0.9754 |
181 0.9584 |
231 0.9416 |
32 1.0098 |
82 0.9923 |
132 0.9751 |
182 0.9580 |
232 0.9412 |
33 1.0095 |
83 0.9920 |
133 0.9747 |
183 0.9577 |
233 0.9409 |
34 1.0091 |
84 0.9916 |
134 0.9744 |
184 0.9574 |
234 0.9405 |
35 1.0088 |
85 0.9913 |
135 0.9740 |
185 0.9570 |
235 0.9402 |
36 1.0084 |
86 0.9909 |
136 0.9737 |
186 0.9567 |
236 0.9399 |
37 1.0081 |
87 0.9906 |
137 0.9734 |
187 0.9563 |
237 0.9395 |
38 1.0077 |
88 0.9902 |
138 0.9730 |
188 0.9560 |
238 0.9392 |
39 1.0074 |
89 0.9899 |
139 0.9727 |
189 0.9557 |
239 0.9389 |
40 1.0070 |
90 0.9896 |
140 0.9723 |
190 0.9553 |
240 0.9385 |
41 1.0067 |
91 0.9892 |
141 0.9720 |
191 0.9550 |
241 0.9382 |
42 1.0063 |
92 0.9889 |
142 0.9716 |
192 0.9547 |
242 0.9379 |
43 1.0060 |
93 0.9885 |
143 0.9713 |
193 0.9543 |
243 0.9375 |
44 1.0056 |
94 0.9882 |
144 0.9710 |
194 0.9540 |
244 0.9372 |
45 1.0053 |
95 0.9878 |
145 0.9706 |
195 0.9536 |
245 0.9369 |
46 1.0049 |
96 0.9875 |
146 0.9703 |
196 0.9533 |
246 0.9366 |
47 1.0046 |
97 0.9871 |
147 0.9699 |
197 0.9530 |
247 0.9362 |
48 1.0042 |
98 0.9868 |
148 0.9696 |
198 0.9526 |
248 0.9359 |
49 1.0039 |
99 0.9864 |
149 0.9693 |
199 0.9523 |
249 0.9356 |
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 0.9352 |
300 0.9187 |
350 0.9024 |
400 0.8864 |
450 0.8705 |
251 0.9349 |
301 0.9184 |
351 0.9021 |
401 0.8861 |
451 0.8702 |
252 0.9346 |
302 0.9181 |
352 0.9018 |
402 0.8857 |
452 0.8699 |
253 0.9342 |
303 0.9177 |
353 0.9015 |
403 0.8854 |
453 0.8696 |
254 0.9339 |
304 0.9174 |
354 0.9011 |
404 0.8851 |
454 0.8693 |
255 0.9336 |
305 0.9171 |
355 0.9008 |
405 0.8848 |
455 0.8690 |
256 0.9332 |
306 0.9167 |
356 0.9005 |
406 0.8845 |
456 0.8687 |
257 0.9329 |
307 0.9164 |
357 0.9002 |
407 0.8841 |
457 0.8683 |
258 0.9326 |
308 0.9161 |
358 0.8998 |
408 0.8838 |
458 0.8680 |
259 0.9322 |
309 0.9158 |
359 0.8995 |
409 0.8835 |
459 0.8677 |
260 0.9319 |
310 0.9154 |
360 0.8992 |
410 0.8832 |
460 0.8674 |
261 0.9316 |
311 0.9151 |
361 0.8989 |
411 0.8829 |
461 0.8671 |
262 0.9312 |
312 0.9148 |
362 0.8986 |
412 0.8826 |
462 0.8668 |
263 0.9309 |
313 0.9145 |
363 0.8982 |
413 0.8822 |
463 0.8665 |
264 0.9306 |
314 0.9141 |
364 0.8979 |
414 0.8819 |
464 0.8661 |
265 0.9302 |
315 0.9138 |
365 0.8976 |
415 0.8816 |
465 0.8658 |
266 0.9299 |
316 0.9135 |
366 0.8973 |
416 0.8813 |
466 0.8655 |
267 0.9296 |
317 0.9132 |
367 0.8969 |
417 0.8810 |
467 0.8652 |
268 0.9293 |
318 0.9128 |
368 0.8966 |
418 0.8806 |
468 0.8649 |
269 0.9289 |
319 0.9125 |
369 0.8963 |
419 0.8803 |
469 0.8646 |
270 0.9286 |
320 0.9122 |
370 0.8960 |
420 0.8800 |
470 0.8643 |
271 0.9283 |
321 0.9118 |
371 0.8957 |
421 0.8797 |
471 0.8640 |
272 0.9279 |
322 0.9115 |
372 0.8953 |
422 0.8794 |
472 0.8636 |
273 0.9276 |
323 0.9112 |
373 0.8950 |
423 0.8791 |
473 0.8633 |
274 0.9273 |
324 0.9109 |
374 0.8947 |
424 0.8787 |
474 0.8630 |
275 0.9269 |
325 0.9105 |
375 0.8944 |
425 0.8784 |
475 0.8827 |
276 0.9266 |
326 0.9102 |
376 0.8941 |
426 0.8781 |
476 0.8624 |
277 0.9263 |
327 0.9099 |
377 0.8937 |
427 0.8778 |
477 0.8621 |
278 0.9259 |
328 0.9096 |
378 0.8934 |
428 0.8775 |
478 0.8618 |
279 0.9256 |
329 0.9092 |
379 0.8931 |
429 0.8772 |
479 0.8615 |
280 0.9253 |
330 0.9089 |
380 0.8928 |
430 0.8768 |
480 0.8611 |
281 0.9250 |
331 0.9086 |
381 0.8924 |
431 0.8765 |
481 0.8608 |
282 0.9246 |
332 0.9083 |
382 0.8921 |
432 0.8762 |
482 0.8605 |
283 0.9243 |
333 0.9079 |
383 0.8918 |
433 0.8759 |
483 0.8602 |
284 0.9240 |
334 0.9076 |
384 0.8915 |
434 0.8756 |
484 0.8599 |
285 0.9236 |
335 0.9073 |
385 0.8912 |
435 0.8753 |
485 0.8596 |
286 0.9233 |
336 0.9070 |
386 0.8908 |
436 0.8749 |
486 0.8593 |
287 0.9230 |
337 0.9066 |
387 0.8905 |
437 0.8746 |
487 0.8590 |
288 0.9227 |
338 0.9063 |
388 0.8902 |
438 0.8743 |
488 0.8587 |
289 0.9223 |
339 0.9060 |
389 0.8899 |
439 0.8740 |
489 0.8583 |
290 0.9220 |
340 0.9057 |
390 0.8896 |
440 0.8737 |
490 0.8580 |
291 0.9217 |
341 0.9053 |
391 0.8892 |
441 0.8734 |
491 0.8577 |
292 0.9213 |
342 0.9050 |
392 0.8889 |
442 0.8731 |
492 0.8574 |
293 0.9210 |
343 0.9047 |
393 0.8886 |
443 0.8727 |
493 0.8571 |
294 0.9207 |
344 0.9044 |
394 0.8883 |
444 0.8724 |
494 0.8568 |
295 0.9204 |
345 0.9040 |
395 0.8880 |
445 0.8721 |
495 0.8565 |
296 0.9200 |
346 0.9037 |
396 0.8876 |
446 0.8718 |
496 0.8562 |
297 0.9197 |
347 0.9034 |
397 0.8873 |
447 0.8715 |
497 0.8559 |
298 0.9194 |
348 0.9031 |
398 0.8870 |
448 0.8712 |
498 0.8556 |
299 0.9190 |
349 0.9028 |
399 0.8867 |
449 0.8709 |
499 0.8552 |
The following formula is used to create the values in the table above. This formula is used in the HMA Plant Report software: