﻿116 
  

  

  SANTA 
  MARIA 
  OIL 
  DISTRICT, 
  CALIFORNIA. 
  

   Chemical 
  analyses 
  of 
  California 
  petroleum 
  — 
  Continued. 
  

  

  

  Plash. 
  

  

  Viscosity. 
  

  

  Sulphur. 
  

  

  Calorific 
  

   value 
  of 
  

  

  dry 
  

   samples.** 
  

  

  Calorific 
  

  

  values 
  

  

  per 
  

   cubic 
  

   centi- 
  

   meter. 
  

  

  "3 
  

  

  ' 
  Atl5°C. 
  (about 
  60° 
  F.). 
  

  

  At 
  85° 
  C. 
  (185° 
  F.). 
  

  

  3 
  

   o 
  

   6 
  

  

  Seconds. 
  

  

  i 
  

  

  Seconds 
  

  

  divided 
  by 
  

  

  ■27 
  \ 
  or 
  water 
  =1. 
  

  

  Seconds. 
  

  

  Seconds 
  

  

  divided 
  

  

  by 
  27J 
  or 
  

  

  water 
  =1. 
  

  

  1 
  

   2 
  

   3 
  

   4 
  

   5 
  

   6 
  

  

  o 
  

  

  Below 
  15 
  

   15 
  

  

  Below 
  15 
  

   21 
  

  

  Above 
  70 
  

  

  Above 
  70 
  

  

  Above 
  70 
  

   32 
  

   26 
  

   Below 
  IS 
  

   Below 
  15 
  

   Below 
  15 
  

   Below 
  15 
  

   Below 
  15 
  

   Below 
  15 
  

   Below 
  15 
  

  

  1,060 
  

   47f 
  

   90 
  

   Over 
  1,800 
  

   Over 
  1,800 
  

   Over 
  1,800 
  

   Over 
  1, 
  800 
  

   1,100 
  

   393 
  

   264 
  

   611 
  

   162* 
  

   56 
  

   28J 
  

   454 
  

   38J 
  

  

  38.40 
  

  

  1.72 
  

  

  3. 
  27 
  

  

  Over 
  65. 
  00 
  

  

  Over 
  65. 
  00 
  

  

  Over 
  65. 
  00 
  

  

  Over 
  65. 
  00 
  

  

  39.85 
  

  

  14.24 
  

  

  9.56 
  

  

  2.23 
  

  

  5.91 
  

  

  2.03 
  

  

  1.03 
  

  

  1.66 
  

  

  1.40 
  

  

  77J 
  

   29jj 
  

  

  m 
  

  

  227 
  

   108 
  

   410 
  

   78 
  

   54 
  

   43 
  

   41J 
  

   341 
  

   37 
  

   32£ 
  

   25£ 
  

  

  31* 
  

   292 
  

  

  2.81 
  

   1.07 
  

   1.36 
  

   8.23 
  

   3.91 
  

   14.86 
  

   2.83 
  

   1.96 
  

   1.56 
  

   1.50 
  

   1.24 
  

   1.34 
  

   1.18 
  

   .99 
  

   1.13 
  

   1.07 
  

  

  Per 
  cent. 
  

  

  2.08 
  

  

  .60 
  

  

  1.56 
  

  

  4.43 
  

   .44 
  

  

  10,369 
  

  

  10, 
  825 
  

   10, 
  543 
  

   10,258 
  

  

  10, 
  348 
  

  

  9,907 
  

   9.203 
  

   9,364 
  

   9,822 
  

   10,001 
  

  

  7 
  

   8 
  

   9 
  

  

  .85 
  

  

  .77 
  

  

  10, 
  437 
  

   10, 
  402 
  

  

  0,976 
  

   9,804 
  

  

  10 
  

   11 
  

  

  .94 
  

  

  10,581 
  

  

  9, 
  678 
  

  

  12 
  

   13 
  

   14 
  

   15 
  

  

  .48 
  

   .38 
  

   .06 
  

  

  10,647 
  

   10, 
  739 
  

   10, 
  598 
  

  

  9,384 
  

   9,321 
  

   9,040 
  

  

  16 
  

  

  .28 
  

  

  11,141 
  

  

  9,322 
  

  

  CO 
  

  

  Distillation. 
  

  

  "3 
  

  

  Percentage. 
  

  

  a 
  

   o 
  

  

  Water. 
  

  

  Up 
  to 
  

   100° 
  C. 
  

  

  100°-150° 
  

   C. 
  

  

  150°-200° 
  

   C. 
  

  

  200°-250° 
  

   C. 
  

  

  250°-300° 
  

   C. 
  

  

  300° 
  C. 
  to 
  

   asphalt. 
  

  

  As- 
  

   phalt. 
  

  

  Loss 
  or 
  

  

  o 
  

  

  A. 
  

  

  B. 
  

  

  gain. 
  

  

  1 
  

  

  None. 
  

   None. 
  

   None. 
  

  

  7 
  

  

  .7 
  

   None. 
  

  

  .8 
  

   None. 
  

   None. 
  

   None. 
  

   None. 
  

   None. 
  

   None. 
  

   None. 
  

   None. 
  

   None. 
  

  

  0.9 
  

  

  8.6 
  

  

  8.2 
  

  

  1.3 
  

  

  

  

  

  

  

  

  

  

  

  

  4.2 
  

  

  9.3 
  

  

  4 
  

   10.4 
  

  

  5.5 
  

   15.3 
  

   10.5 
  

  

  6 
  

   16 
  

   17.7 
  

  

  3.9 
  

  

  

  

  

  

  

  

  4.2 
  

  

  4.2 
  

   13.9 
  

   16.5 
  

   14.1 
  

   13.8 
  

   30.6 
  

   15 
  

   20.4 
  

  

  10.5 
  

  

  12 
  

  

  12.1 
  

  

  5.5 
  

  

  1 
  

  

  

  

  

  

  8.9 
  

  

  9.6 
  

  

  8.9 
  

   11.8 
  

  

  9.1 
  

   10.5 
  

   21.5 
  

  

  9.5 
  

   13.8 
  

  

  9.3 
  

   13.4 
  

   9.4 
  

   7.7 
  

   10 
  

   

  

  7.6 
  

  

  8.7 
  

  

  14 
  

  

  9.7 
  

  

  7.7 
  

  

  9.3 
  

  

  10.3 
  

  

  25.4 
  

  

  9.9 
  

  

  13 
  

  

  11 
  

   10.8 
  

  

  9.1 
  

   18.3 
  

   17.4 
  

   22.5 
  

   13.9 
  

   20.2 
  

   14.7 
  

   18.3 
  

  

  9.1 
  

   10.1 
  

   17.5 
  

  

  8.1 
  

  

  9.9 
  

   11.1 
  

  

  39.5 
  

   23 
  

  

  29.7 
  

   34.3 
  

   45.5 
  

   37.5 
  

   40 
  

  

  27.5 
  

   23 
  

   24.2 
  

   31.8 
  

   43 
  

  

  20.8 
  

   5 
  

   28 
  

   16.9 
  

  

  

  22 
  

  

  8 
  

  

  12 
  

  

  20.6 
  

  

  23.5 
  

  

  31.1 
  

  

  21.8 
  

  

  22.5 
  

  

  15.7 
  

  

  13.3 
  

  

  13 
  

  

  9.8 
  

  

  9.1 
  

  

  4.1 
  

  

  10.6 
  

  

  6.8 
  

  

  -0.8 
  

  

  2 
  

   3 
  

  

  7.4 
  

  

  - 
  .8 
  

   -1.8 
  

  

  4 
  

  

  

  -1.4 
  

  

  5 
  

  

  

  -1.9 
  

  

  6 
  

   7 
  

   8 
  

   9 
  

   10 
  

   11 
  

  

  6.9 
  

   14.5 
  

  

  7.5 
  

   16.8 
  

  

  5 
  

  

  _2 
  

   -1.4 
  

  

  - 
  .5 
  

   -2 
  

   -2.5 
  

  

  - 
  .8 
  

  

  12 
  

  

  

  — 
  .6 
  

  

  13 
  

   14 
  

  

  7.3 
  

  

  - 
  .3 
  

  

  + 
  .2 
  

  

  15 
  

  

  

  -1.8 
  

  

  16 
  

  

  6.8 
  

  

  - 
  .7 
  

  

  .2 
  

  

  '3 
  

  

  

  Distillation. 
  

  

  

  

  

  T. 
  

   - 
  

  

  Gravity 
  of 
  preceding 
  fractions 
  at 
  15° 
  C. 
  (about 
  60° 
  F.) 
  . 
  

  

  as 
  

  

  c 
  

  

  Up 
  to 
  100° 
  C. 
  

  

  100°-150° 
  C. 
  

  

  150°-200° 
  C. 
  

  

  200°~250°C. 
  

  

  250°-300° 
  C. 
  

  

  300° 
  C. 
  to 
  

  

  asphalt. 
  

  

  o 
  

  

  A. 
  

  

  B. 
  

  

  1 
  

  

  

  0. 
  7596 
  

   . 
  7683 
  

   . 
  7617 
  

   .7737 
  

  

  0.8087 
  

   .8028 
  

   .8132 
  

   .7906 
  

  

  0. 
  8538 
  

   .8354 
  

   .8583 
  

   .8316 
  

   .8516 
  

  

  0.8875 
  

   .8574 
  

   .8899 
  

   .8613 
  

   .8840 
  

   . 
  8901 
  

   .8849 
  

   .8976 
  

   .8991 
  

   .8937 
  

   .8901 
  

   .8547 
  

   .8774 
  

   .9227 
  

   .8624 
  

   .8606 
  

  

  0.9167 
  

   .8788 
  

   .9085 
  

   .8992 
  

   .9347 
  

   .8997 
  

   .9021 
  

   .8982 
  

   .9210 
  

   .8955 
  

   .9154 
  

   .8778 
  

   .8866 
  

   .9374 
  

   .8875 
  

   .8870 
  

  

  

  2 
  

   3 
  

   4 
  

  

  0.7185 
  

   .7123 
  

  

  0.8822 
  

  

  5 
  

  

  

  

  6 
  

  

  

  

  

  .8938 
  

  

  7 
  

  

  

  

  

  .8625 
  

   .8427 
  

   . 
  8672 
  

   .8597 
  

   .8613 
  

   .8388 
  

   .8382 
  

   .8919 
  

   .8321 
  

   .8359 
  

  

  .9053 
  

  

  8 
  

  

  

  . 
  7760 
  

   .7756 
  

   .7701 
  

   . 
  7724 
  

   .7736 
  

   .7630 
  

   .8074 
  

   .7639 
  

   .7659 
  

  

  .8235 
  

   .8313 
  

   .8172 
  

   N 
  . 
  8202 
  

   .8111 
  

   .8041 
  

   .8396 
  

   .8015 
  

   .8040 
  

  

  .8985 
  

  

  9 
  

  

  

  .9166 
  

  

  10 
  

   11 
  

  

  .7252 
  

   . 
  722s 
  

   .7250 
  

   . 
  6906 
  

   . 
  7395 
  

   .7002 
  

   .7472 
  

  

  .9062 
  

  

  12 
  

   13 
  

   14 
  

  

  15 
  

  

  . 
  9062 
  

  

  16 
  

  

  .8720 
  

  

  a 
  To 
  convert 
  calories 
  into 
  British 
  thermal 
  units, 
  multiply 
  by 
  1.8. 
  

  

  