| | | | | | | 13.22 | 12.18 | 1.0547 | 11.80 | 10.49 | 62.9 | 1.0513 | 13.27 | 12.23 | 1.0549 | 11.85 | 10.53 | 63.1 | 1.0515 | 13.32 | 12.28 | 1.0551 | 11.90 | 10.58 | 63.3 | 1.0517 | 13.38 | 12.33 | 1.0554 | 11.95 | 10.63 | 63.5 | 1.0519 | 13.44 | 12.38 | 1.0556 | 12.00 | 10.67 | 63.7 | 1.0521 | ----------+----------+--------+----------+----------+---------+--------+ TABLE 5.—_Tomato Pulp and Filtered Liquor_—Continued ======================================================================== Whole pulp | Filtrate from pulp | ------------------------------+---------------------+---------+--------+ Solids by drying | | Solids by drying |Immersion| | ---------------------+ +---------------------+refract- | | _In vacuo_| At |Specific|_In vacuo_| At | ometer |Specific| at 70° C.| atmo- |gravity | at 70° C.| atmo- |reading | gravity| | spheric | at | | spheric | at | at | | pressure | 20° C. | | pressure |17.5° C. | 20° C.| | 100° C.| | | 100° C | | | ----------+----------+--------+----------+----------+---------+--------+ _Per cent_|_Per cent_| |_Per cent_|_Per cent_| | | 13.50 | 12.44 | 1.0558 | 12.05 | 10.71 | 64.0 | 1.0523 | 13.55 | 12.49 | 1.0560 | 12.10 | 10.75 | 64.2 | 1.0525 | 13.60 | 12.54 | 1.0562 | 12.15 | 10.80 | 64.4 | 1.0527 | 13.66 | 12.59 | 1.0565 | 12.20 | 10.84 | 64.6 | 1.0529 | 13.72 | 12.64 | 1.0567 | 12.25 | 10.89 | 64.8 | 1.0531 | | | | | | | | 13.78 | 12.70 | 1.0569 | 12.30 | 10.94 | 65.0 | 1.0533 | 13.83 | 12.75 | 1.0572 | 12.35 | 10.98 | 65.2 | 1.0535 | 13.89 | 12.80 | 1.0574 | 12.40 | 11.02 | 65.4 | 1.0537 | 13.95 | 12.85 | 1.0576 | 12.45 | 11.07 | 65.6 | 1.0539 | 14.01 | 12.90 | 1.0579 | 12.50 | 11.11 | 65.8 | 1.0541 | -----------------------------------------------------------------------+ The per cent of solids in the filtered liquor obtained by drying _in_ _vacuo_, multiplied by 1.12, gives the per cent of solids in the original pulp obtained by drying _in vacuo_. This relationship is shown in Table 2, in the column headed “Ratio of pulp solids to filtrate solids,” and also in Table 5.