ASTM D206 -36 Abridged Volume Correction Table for Petroleum Oils (Withdrawn 1952)

Approved as
AMERICAN STANDARD
by the AmerIcan Standards ASllOclatlon

A.S.A. NO.: 211.1-1936

AMERICAN PETROLEUM INSTITUTE
STANDARD. A.P.I. No.: 500-36

STANDARD ABRIDGED VOLUME CORRECTION TABLE
FOR PETROLEUM OILS1

A.S.T.M. Designation: D 206 - 36

This table is issued under the fixed designation D 206. the final number in-
dicates the year of original adoption as standard or, in case of revision, the year
of last revision.

ADOPTED, 1925: RE\'ISED, 19H, 1936.

This abridged table has been prepared by the National Bureau of
Standards to meet a demand from the oil industry for a short and
convenient table for reducing oil volumes to the basis of 60 F., when ex-
treme accuracy is not required. It is not intended to replace the
Bureau of Standards Circular No. 410, but rather to supplement it
and especially to replace the various abridged tables heretofore em-
ployed in the oil industry.

The groups, coefficients of expansion, gravity (degrees A.P.I.),
and gravity ranges for the several subdivisions of the present abridged
table follow:

GRAVITY RANGE

COEFFICIENT OF 01' GROUP

EXPANSION AT GRAVITV, (DKGREKS A.P.I.

GROUP NUMBER 60 F. DEGREES A.p.r. AT 60 F.)

O. . .. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .. 0.00035 6 Up to 14.9

1................................... 0.00040 22 15.0 to 34.9

2................................... 0.00050 44 35.0 to 50.9

3 0.00060 58 51.0 to 63.9

4................................... 0.00070 72 64.0 to 78.9

5................................... 0.00080 86 79.0 to 88.9

6................................... 0.00085 91 89.0 to 93.9

7................................... 0.00090 97 94.0 to 100.0

All motor fuel blends of gasoline and benzol shall be considered

as falling in Group 3. In cases of uncertainty regarding the presence

of benzol, a product having a gravity heavier (numerically less) than

51 deg. A.P.I., and a 50 per cent recovery point less than 293 F.

(145 C.) shall be considered as falling in Group 3.

This table shows the volume occupied at 60 F. by a quantity

of oil occupying unit volume at the indicated temperatures.

I Under tho .•tandardizatinn procedure of the Society. this table is under the jurisdiction of tho
A.S.T.M. CommIttee 0-2 on Petroleum Products and Lubricant;.

This abridged table differs from that published in 1934 in three respects: The multipliers for
Group II havo been levised slightly; Group I has been extended from 249 to 499 F.; and GrouPS 4. S
and 6 have been extended from 99 to 124 F.

The multiplien in the Group 0 table in the 1934 standard were taken from the National Bureau
of Standards Miscdlsn.ous Publicalion No. ~·7. With the revision of Circular No. 154 (published as
Circular No. 410) to include data on oils from 0 to 10· A.P.I., it has seemed desirable to employ the
procedure followed in the other groUPS and chOOse the column of multipliers from the unabridged table
which has a base coefficient of expansion ncarest 0.00035, which in the case of Group 0 is the column
corresponding to a gravity of 6" A.P.I.

(988)

A.S.T.M. DESIGNATION: D 206 - 36 989

STANDARD ABRIDGED VOLUME CORRECTION TABLE FOR PETROLEUM OILS

GROUP 0"

IJegend: t = observed temperature in degrees Fahrenheit; M CiI mUltiplier for reducing oil volumes to the basis of 60 F.

t M t M t M t M t M

--- 1. 0211 50.... ..... 1.0035 ----- 0.9862 150 . . . . . . . . 0.9691 200 ........ 0.9523
1.0208 1.0032 0.9858 151. ....... 0.9687 201. .......
O. ...... 51. ........ 1.0028 100 . . . . . . . . 0.9855 152 . . . . . . . . 202 ........ 0.9520
1. ....... 1.020~ 52 ......... 1.0025 101. ....... 0.9852 153 ........ 0.9684 203 ........ 0.9517
2. ....... 53 ......... 1.0021 102 . . . . . . . . 0.9848 154 ........ 0.9680 204 ........ 0.9513
3. ....... 1.0201 54 ......... 103 ........ 0.9510
1.0197 10L ...... 0.9677
4. .......
1.019~ 55 . . . . . . . . . 1.0017 105 ........ 0.9844 155 ........ 0.9674 205 ........ 0.9507
5. ....... 1.0014 106 ........ 0.9841 156 ........ 0.9670 206 ........ O. 950~
1.0190 56 ......... 1.0010 107 . . . . . . . . 0.9837 157 ........ 0.9667 0.9500
6. o • • • • • • 1.0186 57 . . . . . . . . . 1.0007 0.9834 158 ........ 0.9664 207 ........ 0.9497
7........ 1.0183 1. 0003 108 ..... '" 0.9831 159 ........ 0.9660 208 ........ O. 949~
8........ 1. 0179 58 ......... 109 ........ 209 ........
9........ 59 . . . . . . . . .

10 ........ 1. 0176 60 ......... 1. 0000 110 . . . . . . . . 0.9827 160 . . . . . . . . 0.9657 210 ........ 0.9490
11. ....... 1.0172 61 ......... 111. ....... 0.9823 161 ........ 0.9654 211. .......
12 ........ 1. 0168 0.9997 112 ........ 0.9820 162 ........ 0.9650 212 ........ 0.9487
1.0165 62 ......... 0.9993 113 ........ 0.9816 0.9647 0.9484
13 ........ 1.0161 63 ......•.. 114 ........ 0.9813 163 ........ 213 ........
14 ........ 64 ......... 0.9990 164 ........ 0.9643 214 ........ 0.9481
0.9986 0.9477

15 ........ 1.0158 65. . ...... 0.9982 115 ........ 0.9809 165 ........ 0.9640 215 ........ 0.9474
16 ........ 1.0154 66 ......... 0.9979 116 .... ". 09806 166 ........ 0.9637 216 ........ 0.9471

17 . . . . . . . . 1.0151 0.9976 117 ........ 0.9802 167 ........ 0.9633 217 ........ 0.9468
18 ....... 1.0147 67 ...... '" 0.9972 118 ........ 0.9799 168 ........ 0.9630 218 ........ 0.9464
19 . . . . . . . . 1.0144 68 ......... 0.9969 219 ........
69 ......... 119.. ...... 0.9795 169 ........ 0.9627 0.9~61

20 ........ LOW 70 ......... 0.9965 120 ........ 0.9792 170 ........ 0.9623 220 ........ 0.9458
21. .. , .... 1.0137 0.9962 121. ....... 0.9789 171 ........ 221 ........
22 ........ 71 ...... '" 0.9958 122 ........ 0.9785 172 ........ 0.9620 222 ........ 0.9454
23 ........ 1.0134 72 ........ . 0.9955 123 ........ 0.9782 173 ........ 0.9616 223 ........ 0.9451
24 ....... . 73 ......... 124 ........ 0.9779 174 ........ 0.9613 224 ........ 0.9448
1.0130 74 ......... 0.99li2 0.9445
0.9610
1.0126

25 ........ 1.0123 75 ........ . 0.9948 125 ........ 0.9775 175 ........ 0.9606 225 .•.•.... 0.9441
1.0119 76 ......... 0.9944 126 ........ 0.9772 176 ........ 0.9603 226 ........
26 ........ 1.0116 77 ......... 0.9941 127 ........ 0.9768 0.9600 227 ........ 0.9438
27 ........ 1.01l2 78 ......... 0.9938 128 ........ 177. ....... 0.9596 228 ........ 0.9435
28 ........ 1.0109 79 ......... 0.9934 129 ........ 0.9765 178 ........ 229 ........ 0.9432
0.9762 li9 ........ 0.9593 0.9428
29 ........

30 ........ 1.0106 80 ......... 0.9931 130 ........ 0.9758 180 ........ 0.9590 230 ........ 0.9425
31 ........ 1.0102 81 ......... 0.9927 0.9755 181.. ...... 0.9586 231. ....... 0.9422
32 ........ 131 ........ 0.9751 182 ........ 0.9583 232 ........
33 ........ 1.0098 82 ......... 0.9924 132 ........ 0.9748 183 . . . . . . . . 0.9580 233 ........ 0.9419
1.0095 0.9920 133 ........ 0.9745 184 ........ 0.9576
34 ........ 1.0092 83:. .... '" 134.0 ...... 234.. ...... 0.9415
84 ......... 0.9917 0.9412

35 ........ 1.0088 85 ......... 0.9914 135 ........ 0.9741 185 ........ 0.9573 235 ........ 0.9409
36 ........ 1.0084 86 ......... 0.9910 136 . . . . . . . . 0.9738 186 . . . . . . . . 0.9569 236 . . . . . . . . 0.9406
37 ........ 1.0081 87 ......... 0.9907 137 ........ 0.9736 187 ........ 0.9566 237 ........ 0.9402
38 ........ 1.0077 88 ......... 0.9903 138 ........ 0.9731 0.9563 238 ........ 0.9399
39 ........ 89 ......... 0.9900 0.9728 188..... ' .. 0.9559 239 ........ 0.9396
1.0074 139 ........ 189 ........

40 ........ 1.0070 90 ......... 0.9896 140 ........ 0.9724 190 . . . . . . . . 0.9556 240 ........ 0.9392
141. ....... 0.9721 191. ....... 241 ........ 0.9389
41 ........ 1.0067 91. ........ 0.9892 142 ........ 0.9718 192 ........ 0.9553 242 ........ 0.9386
42 ........ 1.0063 92 ......... 0.9889 143 ........ 0.9549 243 ........ 0.9383
43 ........ 1.0059 93 ......... 0.9886 144 ........ 0.9714 193 ........ 244 ........
1.0056 94.. ....... 0.9882 0.9711 19~ ........ 0.9546 0.9380
44 ........ 0.9543

45 ........ 1.0052 95 ......... 0.9879 145 ........ 0.9707 195 ........ 0.9639 245 ........ 0.9376
46 ........ 1.0049 96 ......... 0.9876 146 . . . . . . . . 0.9704 196 ........ 0.9536 0.9373
47 ........ 1.0045 97 ......... 147 ........ 0.9701 197 ........ 246 ........
48 ........ 0.9872 148 ........ 0.9697 . 0.9533 247 ........ 0.9370
49 ....... , 1.0042 98 ......... 0.9869 198 . . . . . . . . 0.9530 248 ........ 0.9367
1.0039 99 ......... 149 ........ 0.9694 199 ........
0.9865 0.9527 249 .....••. 0.9364

• These tables for Group 0 and Group 1 have been adopted as standard by the Society as volume
correction tables for asphaltic products on the joint recommendation of A.S.T.M. Committee D-4
on Road and Paving Materials and Committee D·g an Bituminous Waterproofing and Roofing
Materials.

990 ABRIDGED VOLUME CORRECTION TABLE FOR OILS

STANDARD ABRIDGED VOLUME CORRECTION TABLE FOR PETROLEUM OILS

GROUP 0 a (Continued)

Legend' t = obsenled temperature in dCjlre... Fabreoheit; M = multiplier for reducing oil volumes to tbe basis of 60 F.

t M t M t M t M t M
-------
--- 0.9360 300 .... , ... 0.9201 350 ........ 0.9045 400 ........ 0.8893 450 ........ 0.8744
O. Q357 :101. ....... 0.9198 351 ........ 0.9042 451. .......
250 ....... 0.9354 0.9039 401. ....... 0.8890 452 ........ 0.8741
251. ...... 0.9351 302 ........ 0.9195 352 ........ 0.9036 402 ........ 0.8887 4-53 ........ 0.8738
252 ....... 0.9347 0.9033 403 ........ 0.8884
253 ....... 303 ........ O.U191 353.. ...... 404 ........ 0.8881 454 .. . ..... 0.8735
254 ....... 304 ........ 0.9188 354 ........ 0.8732

255 ....... 0.93H 305 ........ 0.9185 3.~5 ... , .... {U030 405 ....... 0.8878 455 ........ 0.8729
0,9341 306 ........ 406 ....... O. 8~75
256 ....... 0,9338 307 ........ 0.9182 356 ..... .. 0,9027 0.8872 456 .....•.. 0.8726
257 ....... 0,9335 308 ........ 0.9179 407 ....... 457 ........
258 ...... 0.9176 3.17 ........ 0.9024 408 ...... 0.88u9 458 ........ 0.8723
259 ....... 0.9331 309 ........ 0.9173 358 ........ 0.!102\ 409 ........ 0.8866 459 ........ 0.8720
3.19 ....... 0.9017 0.8717

260 ....... 0.9328 310 ........ 0.9169 360 ........ 0.9014 410 ........ 0.8863 460 ........ 0.8714
261. ...... 0.9325 311 ........ 361. ....... 0.9011 0.8860 0.8711
262 ....... 0.9322 0.9\66 411. ....... 0.8857 461. ....... 0.S709
312 ........ 362 ........ 0.900S 412 ........ 0,8854 462 ........
263 ....... 0.n19 313 ........ 0.9163 363 ........ 0.9005 413 ........ 463 ........ 0.8706
264 ...... 0.9315 314 ........ 0.9160 364 ....... 0.9002 0.8851 464 ........ 0.8703

0.9157 414 ........

265 ....... 0.9312 315 ........ 0.9154 365 ........ 0.8999 415 ........ 0.8848 465 ........ 0.8700
266 ....... 0.9309 316 ........ 0,9151 366 ........ 0.8996 416 ........ 0.8845 466 ........ 0.8697
267 ....... 0.9306 317 ........ 367 ....... 0.S9n 0.8842 467 ........
268 ....... 0,9303 0.9148 368 ........ 0,8990 417 ........ 0.8839 0.8694
269 ....... 0,9299 318 ....... ' 0,9145 369 ....... 468 ........ 0.8691
319 ....... ' 0.8987 418 ........ 0.8836 469 ....... , 0.8688
0.9141
419. .......

270 ....... 0.9296 320 . . . . . . . . 0,9138 370 ........ 0.8984 420 ........ 0.8833 470 ........ 0.8685
271 ....... 0.9293 0.9135 0.8981 421. ....... 0.8830 0.8682
2;2 ....... 0.9290 321. ....... 0.9132 371 ........ 0.8978 422 ........ 0.8827 471. ....... 0.8679
273 ....... 0.9287 322 ........ 0.9129 372 ........ 0.8975 423 ........ 08824 472 ........ 0.8676
0.9283 0.9126 373 ........ 0.8972 0.8821
2i4 ....•. 323 ........ 374 ........ 42L. .... 473 ........ 0.8673
324. ...... 474 ........

275 ....... 0.9280 325. ....... 0.9123 3;5 ........ 0.8969 425 .. , . .... 0.8818 475 ........ 0,8671
276 ....... 326. ....... 0.9119 3i6, ....... 0,8965 426 ... . .... 0.8815 476 ........
0.927i 327. ....... 3i7 ........ 427 ........ 0.8812 477 ........ 0.8668
277 ...... ' 0.9274 328 ........ 0.9116 0.8962 428 ........ 478 ........ 0.8665
278 ....... 1l.92il 0.9113 378 .. '" ... 0.895a 429 ....... 0.8809 479 ........
279 ....... 329 ........ 0.9110 379 ........ 0.8956 0.8806 0.8662
0.9267 0.8659

280 ....... 0.9264 330 . . . . . . . . 0.9107 380 . . . . . . . . 0.8953 430 ........ 08803 480 ........ 0.8656
0,9261 331. ....... 0.9104 381 ........ 431. ....... 0.8800 481. .......
281., .... ' 0,9101 382 ....... 0.8950 432 ........ 0.8797 482 ........ 0.8653

282 ....... 0.9258 332 ........ 0.8\147 483 ........ 0.8650
283 .. ..... 0,9098 383 ... '" 433 ........ 0.8794 0.8647
284 .. ..... 0.92'>5 333 ....... 384 .. . ..... 0.89H 484 ..... '"
0,92.12 334.- ..... 0.9095 434 ..... . .. 0.8791 0.8644
0.8941

285 ....... 0.9248 335 ........ 0.9092 385 ........ 0.8938 435 ........ 0.8788 485 ........ 0.8642
286 ....... 0.9245 0.9088 386 ........ 0.8935 436 ........ 0.8785 0.8639
287 ...... , 0.9242 336 ........ 0.9085 387 ........ 0.8932 437 ........ 0.8782 486 ..... '" 0.8636
0.9239 337 ........ 0.9082 438 ........ 0.8779 487 ........
288 ....... 338 ........ 388 ..... '" 0.8929 439 ........ 0.8633
289 ....... 0.n3S 339 ........ 0.9079 389 ........ 0.8926 0.8776 488 ........ 0.8630
489 ........

290 ....... 0.9233 340 . . . . . . . . 0.9076 390 ........ 0.8923 440 ........ 0.8773 490 ........ 0.8627
291. ...... 0.9229 341. ....... 441. ....... 0.8770
292 ....... 0.9226 342 ........ 0.9073 391. ....... 0.8920 491. ....... 0.8624
293 ....... 0.9070 392 ........ 0.8917 442 ........ 0.8767 492 ........ 0.8621
0.9223 343 ........ 0.9067 443 ........ 0.8618
294 ....... 0.9220 3H ........ 393 ........ 0.8914 444 ... ..... 0.8764 493 ........
0.9064 394 ........ 0.8911 0.8762 494 ........ 0.8615

295 ....... 0.9217 345 ........ 0.9061 395 ........ 0.8908 445 ........ 0.87.19 495 ........ 0.8613
296 ....... 0.9214 346 ........ 0.9057 396 ........ 0.8005 446 ........ 0.8756 496 ........ 0.8610
297 ....... 0.9210 347 ........ 0.9054 397 ........ 0.8902 0.8753
0.9207 0.9051 0.8899 447 ........ 0.8,50 497 ........ 0.8607
298 ....... 0.9204 348. ....... 0.9048 398 ........ 0.8896 448 ........ 0.8747 498 ........
299 ....... 0.8604
349 ........ 399 ........ 449 ........ 499 ........ 0.8801

• These tables for Group 0 and Group I have been adopted as standard by the Society as volume
correction tables for asphaltic products on the joint recommendation of A.S.T.M. Committee D.4
on Road and Paving Materials and Committee D-8 on Bituminous Waterproofing and Roofing
Materials.

A.S.T.M. DESIGNATION: D 206 - 36 l)l)l

STANDARD ABRIDGED VOLUME CORRECTION TABLE FOR PETROLEUM OILS

GROUP 1a

Legelld: t ~ aboerved temperature la dellrees Fahrenheit; M - multiplier for reducing oil volum.. to the basi. of 60 F.

I M t M t M I M I M

--- 1.0242 50 ......... 1.0040 100 . . . . . . . . 0.9841 150 ........ 0.9647 200 ........ -0.9-45-7
1.0238 1.0036 101. ....... 0.9837 151. ....... 0.9643 201. .......
0 ........ 1.0234 51 ......... 1.0032 102 ........ 0.9833 152 ...•.•.. 0.9639 202 ........ 0.9453
I. ....... 1.0230 52 ......... 1.0028 103 ........ 0.9830 153 ........ 0.9636 203 ........ 0.9449
1.0226 104 .....•.. 154.. ...... 0.9632 204 ........ 0.9446
2........ 53 ......... 1.0024 0.9826 0.9H2
3........ 54 .........
4 ........

5 ........ 1.0222 55 ......... 1.0020 105 . . . . . . . . 0.9822 155 ........ 0.9628 205.. ...... 0.9438
6........ 1.0218 56 ......... 1.0016 106 . . . . . . . . 0.9818 156 ........ 206 ........
7........ 57 ......... 1.0012 107 ........ 0.9814 157 ........ 0.9624 207 ........ 0.9434
8........ 1.0214 58 ......... 108 ........ 0.9811 158 ........ 0.9620 0.9430
9........ 1.0210 69 ......... 1.0008 109 . . . . . . . . 0.9807 159 ........ 0.9616 208 ........ 0.9427
1.0004 209 ........ 0.9423

1.0206 0.9612

10 ........ 1.0202 60 ......... 1.0000 110 . . . . . . . . 0.9803 160 . . . . . . . . 0.9608 210 ........ 0.9419
11. ....... 1.0198 61. ........ 0.9996 111. ....... 0.9799 161 ........ 0.9604 0.9415
12 ........ 0.9992 112.. ...... 0.9795 162 ........ 0.9601 211 ........ 0.9412
13 ........ 1.0194 62 ......... 0.9988 113 ........ 0.9791 163 ........ 0.9597 212 ........ 0.9408
14 ........ 1.0189 0.9984 114.. ...... 0.9787 164 ........ 213 ........ 0.9405
63 ......... 0.9594 214 ........
1.0185 64 .........

15 ........ 1.0181 6ll ......... 0.9980 1l5........ 0.9783 165 ........ 0.9590 215 .•...... 0.9401
16 ........ 1.0177 0.9976 1l6.. ...... 0.9779 166 ........ 0.9586 216 ........ 0.9397
17 ........ 1.0173 66 ......... 0.9072 117 ........ 0.9775 167 ........ 0.9582 217 ........ 0.9393
18 . . . . . . . . 1.0169 67 ......... 0.9908 1l8........ 0.9771 168 . . . . . . . . 0.9578 218 ........ 0.9390
19 . . . . . . . . 1.0165 68 ......... 0.9964 1l9........ 0.9767 169 ........ 0.9574 219 ........
69 ......... 0.9386

20 ...... " 1.0161 70 ......... 0.9960 120 ........ 0.9763 170 . . . . . . . . 0.9570 220 ........ 0.9382
21. ....... 1.0157 0.9956 121. ....... 0.9759 171. ....... 0.9566 221. ....... 0.9378
22 ........ 1.0153 71 ......... 0.9952 122 . . . . . . . . 0.9755 172 ........ 0.9562 222 ........
I 0148 72 ......... 0.9948 0.9752 173 ........ 0.9559 223 ........ 0.9374
23 ........ 1.0144 0.9944 123 ........ 0.9748 174. ....... 224 ........ 0.9371
24 ........ 73 ......... 0.9555 0.9367
74 ......... 124 ........

25 ........ 1.0140 75 ......... 0.9940 125.. ...... 0.9744 175 ........ 0.9551 225 ........ 0.9363
26 ..••..... 1.0136 76 ......... 0.9936 126 ........ 0.9740 176 . . . . . . . . 0.9547 226 ........ 0.9359
27 ........ I. 0132 0.9932 127 ........ 0.9736 0.9543 227 ........
28 ..••••.. 1.0128 77 ......... 0.9929 128 ........ 0.9732 177 . . . . . . . . 0.9540 228 ........ 0.9356
29 ........ 78 ......... 0.9925 129 ........ 178 ........ 0.9536 229 ........ 0.9352

1.0124 79 ......... 0.9728 179 . • . • . . • . 0.9349

30 ........ 1.0120 80 ......... 0.9921 130 ........ 0.9724 180 . . . . . . . . 0.9532 230 ........ 0.9345
31. ....... 81. ........ 0.9917 131. ....... 0.9720 181. ....... 0.9528 231. ....... 0,9341
32 ........ 1.0116 82 ......... 0.9913 132 . . . . . . . . 0.9716 182 . . . . . . . . 0.9524 232 ........
1.0112 0.9909 133 ...•.•.. 0.9713 183 ........ 0.9521 0.9337
33.. ...... 1.0108 83 ......... 0.9905 134 ........ 184.. ...... 233 ........ 0.9334
34 . . . . . . . . 1.0104 84 ......... 0.9709 0.9517 234 ........ 0.9330

35 ........ 1.0100 86 ......... 0.9901 135 . . . . . . . . 0.9705 185 ........ 0.9513 235 ........ 0.0.126
36 ........ 1.0096 86 ......... 0.9897 136 . • • . . . . . 0.9701 186 ........ 0.9509 236 ........ 0.9322
37 . . . . . . . . 1.0092 87 ......... 0.9893 137 ... 0.9697 187 . . . . . . . . 0.9505 237 ........ 0.9318
38 ........ 1.0088 88 ......... 0.9889 138.... :::: 0.9694 188 ........ 0.9502 238 ........ 0.9315
39 . . . . . . . . 1.0084 89 ......... 0.9885 139 ........ 0.9690 189 ........ 0.9498 239 ........ 0.9311

40 ........ 1.0080 90 ......... 0.9881 140 ........ 0.9686 190 . . . . . . . . 0.9494 240 . . . . . . . . 0.9307
41. ....... 1.0076 91. ........ 0.9877 141 ........ 0.9682 191.. ...... 0.9490 241 ........ 0.9303
42 ........ 1.0072 92 ......... 0.9873 142 . . . . . . . . 0.9678 192 . . . . . . . . 0.9487 242 ........ 0.9300
43 ........ 1.0068 93 ......... 0.9869 143 ........ 0.9675 243 ........ 0.9296
0.9865 144 . . . . . . . . 193 ........ 0.9483 244 ........
44 ........ 1.0064 94 ......... 0.9671 194 ........ 0.9480 0.9293

f5 ........ 1.0060 95 ......... 0.9861 145 . . . . . . . . 0.9667 195 . . . . . . . . 0.9476 245 ........ 0.9289
46 ........ 1.0056 96 ......... 0.9857 146 . . . . . . . . 0.9663 196 ........ 0.9472 0.9285
1.0052 0.9853 147 ........ 0.9659 197 ........ 246 ........ 0.9281
47 ........ 97 ......... 148 . . . . . . . . 0.9653 0.9468 247 . . . . . . . .
48 ... : .... 1.0048 98 ......... 0.984~ If9........ 0.9651 198 ........ 0.9465 0.9278
f9 ........ 1.0044 99 ......... 199 ........ 0.9461 248 ........ 0.9274
0.9845 249 ........

• These tables for Group 0 and Group 1 have been adopted as standard by the Society as volume

correction tables for asphaltic products on the joint recommendation of A.S.T.M. Committee D-4

on Road and Paving Materials and Committee D·8 on Bituminous Waterproofing and Roofing
Materials.

992 ABRIDGED VOLUME CORRECTION TABLE FOR OILS

STANDARD ABRIDGED VOLUME CORRECTION TABLE FOR PETROLEUM OILS

GROUP 1· (Continued)

Legend' t ~ oboerved temperature io degree. Fahrenheit· M - multiplier for reducing oil volumes to tho baai. of 60 F.

t M t M t M t M t M

--- 0.9270 300 ........ 0.9088 350........ 0.8909 400 ........ 0.8734 450 ........ 0.8563
0.P267 301 ........ 0.9084 0.8906 0.8731 451 ........ 0.8560
250 ....... 0.9263 351.. ...... 0.8902 401. ....... 0.8727 0.8557
0.9259 302 . . . . . . . . 0.9081 352 ........ 0.8899 402 ........ 0.8724 452 ........ 0.8553
251 ....... 0.9256 303 ........ 0.9077 353 ........ 0.8895 403 ........ 453 ........ 0.8550
252 ....... 304 ........ 0.9073 354,. ...... 404 ........ 0.8720 454 ........
253 .......
254 .......

255 ....... 0.9252 305 ........ 0.9070 355 ........ 0.8892 405 ........ 0.8717 455 ........ 0.8546
256 ....... 0.9248 306 . . . . . . . . 0.9066 0.8888 406 ........ 0.8714 456 ........ 0.8543
257 ....... 307 ........ 0.9063 356 ........ 0.8884 407 ........ 0.8710 457 ........ 0.8540
0.9245 308 ........ 0.9059 357 ........ 0.8707 0.8536

258 ....... 0.9241 309 ........ 358 ........ 0.8881 408 ........ 0.8703 458 ........ 0.8533
259 ....... 0.9237 0.9055 359 ........ 0.8877 409 ........ 459 ........

260 ....... 0.9234 310 . . . . . . . . 0.9052 360 . . . . . . . . 0.8874 410 ........ 0.8700 460 ........ 0.8530
261.. ..... 0.9230 311 ........ 0.9048 361. ....... 0.8870 411. ....... 0.8696 461. ....... 0.8526
262 ....... 0.9226 312 . . . . . . . . 0.0045 0.8867 412 ........ 0.8693 462 ........ 0.8523
263 ....... 0.9223 0.9041 362 ........ 0.8863 413 ........ 0.8689 463 ........
313 ........ 363 ........ 0.8860 414 ........ 0.8519
264 ....... 0.9219 314 ........ 0.9037 364.. ...... 0.8686 464 ........ 0.8516

265 ....... 0.9215 315 ........ 0.9034 365 ........ 0.8856 415 ........ 0.8683 465 ........ 0.8513
266 ....... 0.9212 0.9030 366 ........ 0.8853 416 ........ 0.8679 466 ........ 0.8509
267 ....... 0.9208 316 ........ 0.9027 367 ........ 0.8849 417 ........ 0.8676 467 ........ 0.8506
317 ........ 0.9023 0.8846 418 ........ 0.8672 468 ........
268 ....... 0.9204 318 . . . . . . . . 368 ........ 419 ........ 469 ........ 0.8503
269 ....... 0.9201 0.9020 369 ........ 0.8842 0.8669 0.8499
319 ........

270 ....... 0.9197 320 . . . . . . . . 0.9016 370 . . . . . . . . 0.8839 420 ........ 0.8665 470 ........ 0.8496
271 ....... 0.9193 321 ........ 0.9012 0.8835 0.8662 471. .......
272 ....... 0.9190 322 ........ 0.9009 371.. ...... 0.8832 421. ....... 0.8659 472 ........ 0.8493
273 ....... 0.9186 323 ........ 0.9005 372 ........ 0.8828 422 ........ 0.8655 473 ........ 0.8489
274.. ..... 0.9182 0.9002 373 ........ 423 ........ 0.8486
324.. ...... 0.8825 0.8652 474 ........ 0.8482
374.. ...... 424 ........

275 ....... 0.9179 325 ........ 0.8998 375 ........ 0.8821 425 ........ 0.8648 475 ........ 0.8479
276 ....... 326 . • • . . • . . 376 ........ 0.8818 0.8645 476 ........ 0.8476
277 ....... 0.9175 327 . . . . . . . . 0.8994 377 ........ 0.8814 426 ........ 0.8641 477 ........ 0.8472
278 ....... 0.9171 328 ........ 0.8991 378 ........ 0.8811 427 ........ 478 ........ 0.8469

279 ....... 0.9168 329 . . . . . . . . 0.8987 0.8807 428 ........ 0.8638 0.8466
0.9164 0.8984 379 ........ 429 ........ 0.8635 479 ......•.

280 ....... 0.9160 330 . . . . . . . . 0.8980 380 ........ 0.8804 430 ........ 0.8731 480 .•.•••.. 0.8462
281. ...... 0.9157 0.8977 381. ....... 0.8800 431. ....... 0.8628 481. ....... 0.8459
282 ....... 0.9153 331. ....... 0.8973 382 ........ 0.8797 432 ........ 0.8624 482 ........ 0.8456
283 ....... 332 ........ 0.8969 383 ........ 0.8793 433 ........ 0.8621 483 ........ 0.8452
0.9149 333 ........ 384 ........ 0.8790 434 ........ 0.8618 484 ........ 0.8449
284.. ..... 0.9146 334.. ...... 0.8966

285 ....... 0.9142 335 ........ 0.8962 385 ........ 0.8786 435 . ....... 0.8614 485 ........ 0.8446
286 ....... 0.9139 336 ........ 0.8959 386 ........ 0.8783 436 ........ 0.8611 486 ........ 0.8442
287 ....... 0.9135 337 ........ 0.8955 0.8779 437 ........ 487 ........ 0.8439
288 ....... 0.9131 338 ........ 0.8952 387 ........ 0.8i76 438 ........ 0.8607 488 ........ 0.8436
289 ....... 0.9128 0.8948 388 ........ 0.8772 439 ........ 0.8604 489 ........ 0.8432
339 ........ 0.8601
389 ........

290 ....... 0.9124 340........ 0.8945 390 . . . . . . . . 0.8769 HO ........ 0.8597 490 ..••.... 0.8429
291. ...... 0.9120 341 ........ 0.8941 391. ....... 0.8766 HI ........ 0.8594 491 ........ 0.8426
292 ....... 0.9117 0.8938 392.. ...... 0.8762 442 ........ 0.8590 492 ........ 0.8422
293 ....... 342 ..... '" 0.8934 393 ........ 443 ........ 0.8587 493 ........ 0.8419
0.9113 343 ........ 0.8930 0.8759 0.8584
294.. ..... 0.9110 394 ........ 0.8755 4H ........ 494 ........ 0.8416
344 ..... '"

295 ....... 0.9106 345 . . . . . . . . 0.8927 395 ........ 0.8752 445 ........ 0.8580 495 ........ 0.8413
296 . . . . . . . 0.9102 346 ........ 0.8923 396 ........ 0.8748 446 ........ 0.8577 496 ........ 0.8409
297 ....... 0.9099 347 ........ 0.8920 397 ........ 0.8745 447 ........ 0.8573 497 ........ 0.8406
0.9095 348 ........ 0.8916 398 ........ 0.8741 448 ........ 0.8570 498 ........ 0.8403

298 ....... 0.9091 349 . . . . . . . . 0.8913 399 ........ 0.8738 449 ........ 0.8567 499 ........ 0.8399
299 .......

• These table. for Group 0 and Group 1 have been adopted as standard by the Society a. volume
correction table. for asphaltic products on the joint recommendation of A.S.T.M. Committee D-4
on Road and Paving Materials and Committee 0-8 on Bituminous Waterproofing and Roofinv
Materials.

A.S.T.M. DESIGNATION: D 206 - 36 993

STANDARD ABRIDGED VOLUME CORRECTION TABLE FOR PETROLEUM OILS

GROUP 2

Legend: t ~ obeerved temperature in degrees Fahrenheit; M - multiplier Cor reducing oil volumes to the basis oC 60 F.

M M - - M M M M
------------- -----
a......... 1.0297 ----- 50 ....... 1.0049 75 ....... 0.9925 100...... 0.0802 125 ...... 0.9677
1.0292 51. ...... 1.0044 76....... 0.9920 101. ..... 0.9797 126 ...... 0.9672
1......... 1.0287 25 ....... 1.0174 52 ....... 1.0039 77 ....... 0.9915 102 ...... 0.0792 127 ...... 0.9667
2......... 1.0283 53 ....... 1.0035 78 ....... 0.9911 103 ...... 0.0786 128 ...... 0.9662
3......... 1.0278 26 ....... 1.0169 54 ....... 1.0030 79 ....... 0.9906 104...... 0.9781 129...... 0.06Q7
4.........
27 ....... 1.0164
28 ....... 1.0159
29 ....... 1.0154

5 ......... 1.0273 30....... 1.0149 55 ....... 1.0025 80 ....... 0.9001 105 ...... 0.0776 130...... 0.9OS2
6......... 1.0268 56 ....... 1.0020 81. ...... 0.9896 106...... 0.9771

7......... 1.0263 31 ....... 1.0144 82 ....... 0.9891 107 ...... 0.9766 131. ..... 0.0647
8......... 1.0258 32....... 1.0139 57 ....... 1.0015 83 ....... 0.9886 108 ...... 0.9762 132 ...... 0.9642
9......... 1.0253 33 ....... 1.0134 58 ....... 1.0010 84 ....... 0.9881 10L .... 0.9757 133 ...... 0.9637
34 ....... 1.0129 59 ....... 1.0005
134 ...... 0.9632

10 ......... 1.0248 35....... 1.0124 60....... 1.0000 85 ....... 0.9876 110...... 0.9752 135 ...... 0.9627
36....... 1.0119 61. ...... 0.9995 86 ....... 0.9871 111. ..... 0.9747 136...... 0.9622
11 ......... 1.0243 37....... 1.0114 62 ....... 0.9990 87 ....... 0.9866 112.. .... 0.9742 137 ...... 0.9617
12 ......... 1.0238 38....... 1.0109 63 ....... 0.9985 88 ....... 0.9861 113.. .... 0.9737 138 ...... 0.9613
13 ......... 1.0233 39....... 1.0104 64 ....... 0.9980 114.. .... 0.9732
89 ....... 0.9856 139 ...... 0.9608
14 ......... 1.0228

15 ......... 1.0223 40 ....... 1.0099 65 ....... 0.9975 90 ....... 0.9851 115.. .... 0.9727 140 ...... 0.9603
16 ......... 1.0218 91. ...... 0.9846 141 ...... 0.9598
17 ......... 1.0213 41 ....... 1.0094 66 ....... 0.9970 92 ....... 0.9841 116.. .... 0.9722 142 ...... 0.9593
18 ......... 1.0208 42 ....... 1.0089 67 ....... 0.9965 93 ....... 0.9836 117...... 0.9717 143 ...... 0.9588
19 ......... 1.0203 43 ....... 1.0084 68 ....... 0.9961 94.. ..... 0.9831 118 ...... 0.9712
44 ....... 1.0079 69 ....... 0.9956 119 ...... 0.9707 144 ...... 0.9583

20 ......... 1.0198 45 ....... 1.0074 70 ....... 0.9951 95 ....... 0.9826 120...... 0.9702 145 ...... 0.9578
21 ......... 1.0193 46 ...•... 1.0069 121 ...... 0.9697
22 ......... 1.0188 47 ....... I. 0064 71. ...... 0.9946 96 ....... 0.9821 122...... 0.9692 146...... 0.9573
23 ......... 1.0184 48 ....... 1.0059 72 ....... 0.9941 97 ....... 0.9816 123 ...... 0.9687
·Z4 ......... 1.0179 49 ....... 1.0054 73 ....... 0.9935 124 ...... 0.9682 147...... 0.9568
74 ....... 0.9930 98 ....... 0.9812 148 ...... 0.9563
99 ....... 0.9807 149 ...... 0.9558

STANDARD ABRIDGED VOLUME CORRECTION TABLE FOR PETROLEUM OILS

GROUP 3

Legend: I - obeerved temperalure in degrees Fahrenheil; M - multiplier Cor reducing oil volumes to Ihe basis oC 60 F.

I M t M I M I M t M

---- 1.0361 25 ......... 1.0211 50 ......... 1.0060 76 •.•.••••. 0.9909 100 . . . . . . . . 0.9757
1.0355 26 ......... 1.0205 61. ........ 1.0054 76 ......... 0.9903 101 ........ 0.9751
0........ 1.0349 27 ......... 1.0199 52 ......... 1.0048 77 ......... 0.9897 102 . . . . . . . . 0.9745
1........ 1.0343 28 ...•..... 1.0193 53 ......... 1.0042 78 ......... 0.9891 103 ........ 0.9738
2........ 1.0337 29 ......... 1.0187 54 ......... 1.0036 79 ......... 0.9885 104 . . . . . . . . 0.9732
3........
4........

5........ 1.0331 30 . . . . . . . . . 1.0181 55 ......... 1.0030 80 ......... 0.9879 105 . . . . . . . . 0.9726
0.9873
6........ 1.0325 31. ........ 1.0175 56 ......... 1.0024 81. ........ 0.9867 106 . . . . . . . . 0.9720
1.0319 32 ......... 1.0169 57 ......... 1.0018 82 ......... 0.9860 107 . . . . . . . . 0.9714
7........ 1.0313 33 ......... 1.0163 58 ......... 1.0012 83 ......... 0.9854 108 ........ 0.9708
8........ 34 . . . . . . . . . 1.0157 59 ......... 1.0006 84 ......... 109 . . . . . . . . 0.9702
9........ 1.0307

10 . . . . • • . . 1.0301 35 . . . . . . . . . 1.0151 60 ......... 1.0000 85 ......... 0.9848 110 . . . . . . . . 0.9696
11 . . . . . . . . 1.0295 36 . . . . . . . . . 1.0145 61. ........ 0.9994 86 ......... 0.9842 0.9690
1.0289 1.0139 62 ......... 0.9988 87 ......... 0.9836 111. ....... 0.9684
12 ........ 1.0283 37 . . . . . . . . . 63 ......... 0.9982 112 ........
13 ........ 1.0277 38 ......... 1.0133 64 ......... 88 ......... 0.9830 0.9678
14 ........ 39 . . . . . . . . . 1.0127 0.9976 89 ......... 0.9824 113 ........ 0.9672
114.. ......

15 ........ 1.0271 40 ......... 1.0121 OS ......... 0.9970 90 ......... 0.9818 115 ........ 0.9666
16 . . . . . . . . 1.0265 41 ......... 1.0115 66 ......... 0.9964 91. ........ 0.9812 116.. ...... 0.9660
1.0259 42 ......... 1.0100 67 ......... 0.9957 0.9806 117 . . . . . . . . 0.9654
17 . . . . . . . . 1.0253 43 ......... 1.0103 68 ......... 0.9051 92 ......... 0.9800 118 . . . . . . . .
18 ........ 1.0247 44 ......... 1.0007 69 ......... 93 ......... 0.9794 n9........ 0.9647
19 . . . . . . . . 0.9945 94 ......... 0.9041

20 ........ 1.0241 45 ......... 1.0001 70 ......... 0.9939 95 ......... 0.9788 120 . . . . . . . . 0.9635
21. ....... 46 . . . . . . . . . 1.0085 71. ........ 0.9933 96 ......... 0.9782 121 ........ 0.9629
22 ........ 1.0235 47 ......... 1.0079 72 ......... 0.9927 97 ......... 0.9776 122 . . . . . . . . 0.9623
23 ........ 1.0229 1.0072 73 ......... 0.9921 9S ......... 0.97G9 123 ........ 0.9617
24 ........ 48 ......... 74 ......... 0.9915 99 ......... 0.9763 124 • • • • • • • . 0.9611
1.0223 49 ......... I.00G6
1.0217

994 ABRIDGED VOLUME CORRECTION TABLE FOR OILS

STANDARD ABRIDGED VOLUME CORRECTIO:-I TABLE FOR PETROLEUM OILS

GROUP 4

Legend: t - observed temperature In degrees Fahrenheit: M - multiplier rar reducing all volumes to the basie or 60 F.

t M t M t M t M t M

--- 1.0419 25. ........ 1.0246 .;0 ...... .. . 1.0070 75 ......... 0.9894 100 . . . . . . . . 0.9716
1.0412 26. ..... 1.0239 1.006:\ 7IL ... . .... 0.9887 Ull ........ 0.9709
0........ 1.0405 27 ......... 1.0232 51 ......... 1.0051) 0.9881l 102 ........ 0.971l2
I. ....... 1.0398 28 ......... 1.0225 52 ........ 1.0049 77 .... . .... 103 ........ 0.9695

1.0391 29 ......... 1.0218 1.00l2 7~ .. . .. . ... 0."R'2 0.9688
2........ 53 .... ..... 09865 104.. ......
3........ 54 . . . . . . . 79 .... ....
4........

5........ 1.0384 30 ......... 1.0211 55 ......... 1.0035 80 ... . ..... 0.9858 lOS ........ 0.9681
6........ 1.0377 31. ........ 1.0204 81. ........ 0.9851 0.96n
7........ 1.0370 32 ......... 1.0197 56 ......... 1.0028 82 ......... 0.9844 106 ........ 0.9666
33 ......... 1.0190 57 ......... 1.0021 0.\1837 107 ........ 0.9fJ59
8........ 1.0364 34.. ....... 1.0183 58 .. ....... 1.0014 8L . ...... 0.9830 lOS ........ 0.9652
9........ 1.0357 1.0007 84.- ....... 109 ........
59. .... .... 0.9823
85. ........ 0.9816
10 . . . . . . . . 1.0350 35 ......... 1.0176 60. ..... ... 1.0000 0.9809 110 ........ 0.9645
1.0169 61. ..... ... 0.9993 8G. . ....... 0.9802 111. ....... 0.9638
11 ........ 1.0343 36..... .... 1.0162 62. ..... .. 0.99SH 0.9795 112.. ...... 0.9631
12 ........ 1.0336 1.0155 87 .. ....... 113.. ......
13 ........ 1.0329 37 .. ....... 1.0148 63. , .... .. 0,9979 88 .. ....... 0.9788 0.9624
0.9972 89. ... .. .. 0.9780 114.. ...... 0.9617
14 ........ 1.0322 38 .... ..... 1.0141 64. ....... 0.9773
39 .. .. ..... 1.0134 90 ... .. . .. 0.0766
15 ........ 1.0315 40 .. .. 1. 0127 65. ...... 0.9965 0.9759 115.. ...... 0.9609
16 . . . . . . . . 1.0120 tit) .•. .... 0.9958 91. ... . ... 116 . . . . . . . . 0.9602
17 . . . . . . . . I.O'~08 41.. ....... 1.0113 67 .. ... .... 0.91151 92 ... '" 0.9752 0.9595
18 ........ 42 .. ...... 6S .... 0.9!J43 0.974S 117 ........
19 . . . . . . . . 1.0301 43. ...... 69. ....... 0.\1936 93 .. .. .... 0.9738 118 ........ 0.9588
44. ....... 94,. . .... 0.9731 119 ........ 0.9581
1.0294 iO ....... .. 0.9929 0.9723
O. !HJ22 95 .. .. . ...
1.0287 71. ..... 0.9\115

72 ....... 0.9908 96 .........
20 ........ 1.0280 45. .. ...... 1.0106 73 ........ 0.9901 97 ......... 120 . . . . . . . . 0.9574
21. ....... 1.0273 46 .. ...... 1.0099 9R.- ....... 121. ....... 0.9567
22 ........ 1.0266 47 ......... 1.0092 74 ....... .. 99.. ....... 122 ........ 0.9560
23. ....... 1.0260 1.0084 123 ........ 0.11552
24.. ...... 1.0253 48 ......... 1.0077 124.. ......
0.9545
49 .........

STANDARD ABRIDGED VOLUME CORRECTION TADLE FOR PETROLEUM OILS

GROUP 5

Legend: ~ ~ aboerved temperature In degrees Fahrenheit: M = multiplier rar reducing all volumes to the basie or 00 F.

t M t M t M t M t M

--- 10476 25 ....... .. 1.0280 50 ........ I.OU80 75 ...... ... 0.9879 100 ........ 0.9676
1.0468 26 ......... 1.0272 51 ........ 100.2 .6 ......... O. U871 101. .......
0........ 1.0460 27 ......... 1. 0264 52 ......... 1.0064 77. . ... O. 081).~ 102 ........ 0.9668
I ........ 1.0453 28 ......... 1.0256 53 ......... 1.0056 0.9854 103 ........ 0.9660
1.0445 29 ......... 1. 0248 54.. ....... 1.0048 78 " ' - 0.9846 104 ........
2........ 79 .. .. .... 0.9652
3........ 30 ......... I. 0240 55. ... 1.0040 0.9643
4........ 31.. ....... 1. 0232 1.0032
32 ......... I. 0224 66 . . . . 10024
5........ 1.0437 33 ......... 1.0216 57 ... 1.0016 80 .. . ...... O. !l838 105 ........ 0.9635
6........ 1.0429 34 ......... 1.0208 58 .... ... 1. 0008 81. .. .. .... 0.9830 106 ........ 0.9627
7........ 1.0421 0.9822 107 ........
8........ 1.0414 35 ......... 1.0200 59.... ..... 1.0000 82 ... - .... 0.U814 108 ........ 0.9619

9........ 1.0406 36 ......... 1.0192 0.9992 0.9806 0.9611
37 ......... 1.0184 60 .... .... 0.9984 8:l.. .. . ... 109 ........
to . . . . . . . . 1.0398 38 ......... 1.0176 0.9976 0.9798 0.9603
10390 39 ......... 1.0168 61. ....... 0.9968 8L .... . .. 0.9700
11 ........ 1.0382 85. ....... 0.9782 110 ........ 0.9592
12 ........ 1.0375 40 ......... 1.0160 62 ...... ... 0.9773
13 ........ 1.0367 41. ........ 1.0152 ~6 .. ....... 0.9765 111. ....... 0.9586
14 ........ 42 ......... 1.0144 63 ........ 112 ........ 0.9578
43 ......... 1.0136 64 ......... 87 .. . ...... 113 ........ 0.9570
44 ......... 1.0128 8R.- . . . . .. Il4.. ...... 0.9562

45 ......... 1.0120 89 .. .....
46 ......... 1.0112
15 ........ 1.0359 47 ......... 1.0104 65 0.9960 90 .. ....... 0.9,.17 Il5.. ...... 0.9554
16 . . . . . . . . 1.0351 48 ......... 1.0096 66 ......... 91 .. ....... 116 ........ 0.9546
17 ........ 1.0343 49.. ....... 1.0088 67 ......... o 9952 92 ......... 0.!l749 Ili.. ...... 0.9538
18 ........ 10335 1lS ......... o !1944 9:1.. ....... 0.9741 118 ........ 0.9529
19 . . . . . . . . 94 ......... 0.9733
1.0327 69 ........ 0.9935 0.9725 119 ........ 0.9521
0.9927

20 ........ 1.0319 70 ...... '" 0.9919 95 ......... 0.9717 120 ........ 0.9513
1.03 II 71. ........ 0.9911 96 ......... 0.9709 121.. ......
21. ....... 1.0303 72 ......... 0.9903 97 ......... 0.9700 122 ........ 0.9505
22 ........ 73 ......... 123 ........ 0.9487
23 ........ 1.0296 0.9895 98 ......... 0.9692 0.9489
1.0288 74 ......... 0.9887 99 ......... 0.9684 124 ........
24 ........ 0.9480

A.S.T.M . DESIGNATION: D 206 - 36 995

STANDARD ABRIDGED VOLUME CORRECTION TABLE FOR PETROLEUM OILS

GROUP 6

tegend: I ~ oooerved lemper.tureln dell..... Fahrenhell; M - mul\ipller for reducIng oil vnlumeolo Ihe baala nf 60 F.

I M t M I M I M I M

--- 1.0501 25 ......... 1.0294 50 ......... 1.0084 75 ......... 0.9873 100 . . . . . . . 0.9659
1.0493 26 ...... .. 1.0286 1.0076 76 ......... 0.9864 0.%50
0 ....... 1. 0484 27 ...... 1.0277 51. ........ 1.0067 77 ......... 0.9856 101.. ...... 0.9642
1. ....... 1.047" 28 ...... 1.0269 52 ......... 1.0059 78 ......... 0.9847 102 ........
2........ 1.0467 29 ..... 1.0200 1.0050 79 ......... 0.9839 103 ........ 0.9633
3..... 53 ......... 104 ........ 0.9625
4........ 54.. .......

5........ 1.0459 30 ........ t .O~52 S5 ..... . ... 1.0042 80 ......... 0.9830 105 ....... 0.9616
6........ 1.0451 31. ....... 1.0244 56 ...... ... 1.0034 81. ....... 0.9821 106 ........ 0.9608
7........ 1.0443 32 ......... 1.0236 57 ..... ... 1.0025 82 ........ 0.9813 107 ........ 0.9599
1.0434 33 ......... 1.0227 58 .... ..... 1.0017 83 . ....... 0.9804 108 ........ 0.9590
8........ 1.0426 34 ......... 1.0219 S9 .. . ... 1.0008 84 ......... 0.9796 109 ........
9........ 0.9582
85 .... ..... 0.9787
10 ........ 1.0418 35 ......... 1.0211 60 .... .... 1.0000 0.9779 110 ........ o .OS73
11 ........ 1.0410 36 ......... 1.(1203 61. .... 0.9992 86 .... . .... 0.9770 111. ....... O. U565
12 ........ 1.0402 37 ........ 02.. ....... 0.9983 87. .. ...... 0.9762
13 ........ 1.0393 38 ......... 1. 0 l!14 0.9975 0.9753 112 ... . .... 0.9550
14. ....... 1.0385 39 ......... 1.0186 1\3 .. ... .. 88 ... . ... .. 0.9548
1.0177 0.9966 113 ........ 0.9539

15. ... .... 1.0377 64 . ..... .. 89 .... . ... 114 ........
1.036\)
16 ....... 1.0360 40 ......... 1.0169 65. . ...... 0.9958 90 ........ 0.9745 115 ........ 0.9530
1.03.>2 1.01liO lill.. .... ... 0.9736 111l . . . . . . . . 0.9522
17. ....... 1.0343 41. ..... ... 1. 0152 67 .... ... .. 0.9949 91. ...... .. 0.9727 0.9513
42 ..... .... 1.014:1 68. ...... .. 0.9!141 0.9710 117 . . . . . . . . 0.0505
18. 1.0135 69 ... ..... 0.9932 92.. ...... 0.9710 118 ........
19. ....... 43. .... .... 0.9924 93 ........ 0.9496
44. ..... ... 1.0126 119.. ......
1.0ll8 94 ..... . ...
45 .. ...... , 1.01l0
20 ........ 1.0335 46 ..... .... 1.0101 70 .... .... 0.9915 95 ......... 0.9702 120 ........ 0.9487
21 ....... . I. 0327 47 ..... .... 1.0093 71 ... ...... 0.9907 96 .... .. . 0.9093 121. ....... 0.9479
1.0319 0.9898 97 ......... 122........ 0.9470
22 ........ 1.0310 48 ......... 'I0~ . • • . • • • • • 0.9890 98 ......... 0.9685
23 ........ 1.0302 49 ..... .... 0.9881 99 ......... 0.9676 123· .. · .... 1 0.0462
24 ........ 73 ......... 0.9068 124 ........ 0.9453
74 .........

STANDARD ABRIDGED VOLUME CORRECTION TABLE FOR PETROLEUM OlI.S

GROUP 7

Leiend: I - oooerved temperature In deg..... Fahrenheit; M - multiplier fnr reducing 011 volumes 10 th. baal. of 60 ~'.

M M M M

0 ............... 1.0531 25 .............. 1.0312 50 .•••.•.••...•. 1.0090 75 .............. 0.9805
I. .............. 1.0522 26 .............. 1.0303 51. ..•.......•.. 1.0081 76 ..............
2............... 1.0513 27 .............. 1.0294 52 .............. 1.0072 77 .............. 0.9856

3............... 1.0505 28 .............. 1.0286 1.0063 78 .............. 0.9847
4............... 1.0496 29 .............. 1.0277 53 .............. 1.0054 79 ..............
54 .............. 0.9838
0.982g

5............... I. 0487 30 . . . . . . . . . . . . . . 1.0268 55 . . . . . . . . . . . . . . 1.0045 80 .............. 0.9820
6............... 1.0478 31. ............. 56 . . . . . . . . . . . . . . 1.0036 0.9811
·1 ......... ...... 1.0UO 32 . . . . . . . . . . . . . . 1.0259 57 .............. 1.0027 81. ............. 0.9802
8............... 1.0461 33 .............. 1.0250 82 .............. 0.9792
1.0453 34 .............. 1.0242 58 .............. 1.0018 83 ..............
9............... 59 .............. 1.0oog 0.9783
1.0233 84 ..............

10 . . . . . . . . . . . . . . . 1.0444 35 .............. 1.0224 60 .............. 1.0000 85 .............. 0.9774
1.0435 36 . . . . . . . . . . . . . . 1.0215 61. ............. 0.9991 86 .............. 0.9765
11 ............... 1.0426 37 . . . . . . . . . . . . . . 0.9982 87 .............. 0.9756
12 ............... 1.0418 38 . . . . . . . . . . . . . . 1.0206 62 .............. 0.9973 88 .............. 0.9747
13 ............... 1.0197 63 .............. 0.g964 0.g738
14 ............... 1.0409 39 . . . . . . . . . . . . . . 1.0188 64 .............. 89 ..............

15 ............... 1.0400 40 .............. 1.0179 65 .............. 0.9955 90 .............. 0.9729
16 ............... 1.0391 41. ............. 1.0170 66 .............. 0.9946 91 ..............
17 ............... 1.0382 42 .............. 1.0161 67 .............. 0.9937 92 .............. 0.9710
18 ............... 1.0374 43 .............. 1.0152 0.9928 g3 .............. 0.9710
10 ............... 1.0305 64 .............. 1.0143 68 .............. 0.901g g4 .............. 0.9701
6g .............. 0.96g2

20 ............... 1.0356 45 .••••••••••••• 1.0134 70 .............. 0.9910 90 .............. 0.9683
21. .............. 1.0347 46 .............. 1.0125 71. ............. 0.9901 0.9674
22 ............... 1.0338 47 .............. 1.0116 72 .............. 0.98g2 96 . . . . . . . . . . . . . . 0.g605

1.0330 48 .............. I. 0108 O.g883 97 ..............
23 ............... 1.0321 49 .............. l.oo9g 73 .............. O.g874 0.9656
24 ............... 74 .............. 98 .............. O.g647
99 ..............

996 ABRIDGED VOLUME CORRECTION TABLE FOR OILS

For purposes of brevity the columns showing observed tempera-
tures in degrees Fahrenheit carry the heading" t." The columns of

multipliers which are actually (volume at 60F.) carry the heading"M."
volume at "t"

NOTE: Exaltlple.-The values given in the table are in the form of multipliers;
'that is, the volume of oil at the indicated temperature and degrees A.P.I. for
each group, multiplied by the corresponding factor in the table, equals the volume
at 60 F. For example, if the degrees A.P.I. of an oil at 60 F. equals 58 (Group 3)
and the volume at 88 F. equals 8000 gal., then the volume at 60 F. equals
8000 X 0.9830 or 7864 gal.