Standard Tables for Volume and Specific Gravity Correction for Creosote, Creosote-Coal Tar Solution and Coal Tar

SCOPE
1.1 These tables have been prepared by the National Institute of Standards and Technology to meet a demand from the wood preserving industry for convenient tables for reducing creosote volumes to the basis of 100°F (38°C) and for reducing specific gravity observations to the same temperature. Tables 1 and 2 give in parallel columns corrections factors for creosote and for mixtures of creosote and coal tar (up to 50% tar) designated as solution, and for coal tar. They are based on density determinations made on a selected range of domestic coke-oven tars.  
1.2 Table 2 shows the volume occupied at 100°F (38°C) by a quantity of oil occupying a unit volume at the indicated temperature; for example, 1 gal of creosote measured at 120°F (49°C) will have a volume of 0.9921 gal at 100°F (38°C); thus, if the volume of creosote at 120°F (49°C) equals 10000 gal, then the volume at 100°F (38°C) equals 10000 times 0.9921 or 9921 gal.  
1.3 Table 2 gives corrections for observed specific gravity which are simply made by adding them to the observed values for temperatures above 100°F (38°C) and subtracting them for temperatures below 100°F (38°C).  
1.4 This standard does not purport to address all of the safety problems, if any, associated with its use. It is the responsibility of whoever uses this standard to consult and establish appropriate safety and health practices and determine the applicability of regulatory limitations prior to use.>

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NOTICE: This standard has either been superseded and replaced by a new version or withdrawn.
Contact ASTM International (www.astm.org) for the latest information
Designation: D 347 – 97
Standard Tables for
Volume and Specific Gravity Correction for Creosote,
,
1 2
Creosote-Coal Tar Solution and Coal Tar
This standard is issued under the fixed designation D 347; the number immediately following the designation indicates the year of
original adoption or, in the case of revision, the year of last revision. A number in parentheses indicates the year of last reapproval. A
superscript epsilon (e) indicates an editorial change since the last revision or reapproval.
1. Scope 1.2 Table 2 shows the volume occupied at 100°F (38°C) by
a quantity of oil occupying a unit volume at the indicated
1.1 These tables have been prepared by the National Insti-
temperature; for example, 1 gal of creosote measured at 120°F
tute of Standards and Technology to meet a demand from the
(49°C) will have a volume of 0.9921 gal at 100°F (38°C); thus,
wood preserving industry for convenient tables for reducing
if the volume of creosote at 120°F (49°C) equals 10 000 gal,
creosote volumes to the basis of 100°F (38°C) and for reducing
then the volume at 100°F (38°C) equals 10 000 times 0.9921 or
specific gravity observations to the same temperature. Table 1
9921 gal.
and Table 2 give in parallel columns corrections factors for
1.3 Table 2 gives corrections for observed specific gravity
creosote and for mixtures of creosote and coal tar (up to 50 %
which are simply made by adding them to the observed values
tar) designated as solution, and for coal tar. They are based on
for temperatures above 100°F (38°C) and subtracting them for
density determinations made on a selected range of domestic
temperatures below 100°F (38°C).
coke-oven tars.
1.4 This standard does not purport to address all of the
safety concerns, if any, associated with its use. It is the
These tables are under the jurisdiction of ASTM Committee D07 on Wood and responsibility of the user of this standard to establish appro-
are the direct responsibility of Subcommittee D07.06 on Treatments for Wood
priate safety and health practices and determine the applica-
Products.
bility of regulatory limitations prior to use.
Current edition approved Oct. 10, 1997. Published February 1998. Originally
e1
published as D 347 – 32 T. Last previous edition D 347 – 33 (1992) .
2. Keywords
These tables have been adopted as standard by the American Wood Preservers’
Association and by the American Railway Engineering Association; they are the
2.1 coal tar; creosote; specific gravity; volume
outcome of a Joint Conference Committee representing these associations and the
American Society for Testing and Materials.
Copyright © ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959, United States.
D347–97
TABLE 1 Volume Correction Table for Creosote, Creosote-Coal Tar Solution (up to 50 % Tar), and Coal Tar (Coke-Oven Tars)
The observed volume is to be multiplied by the factor corresponding to the observed temperature.
Volume at 100°F Occu- Volume at 100°F Occu- Volume at 100°F Occu-
pied by Unit Volume at pied by Unit Volume at pied by Unit Volume at
Observed Observed Observed
Indicated Temperature Indicated Temperature Indicated Temperature
Temper- Temper- Temper-
ature, °F ature,° F ature,° F
Creo- Solu- Coal Creo- Solu- Coal Creo- Solu- Coal
sote tion Tar sote tion Tar sote tion Tar
220 0.9526 0.9542 0.9594 180 0.9684 0.9696 0.9732 140 0.9742 0.9850 0.9867
219 0.9530 0.9546 0.9597 179 0.9687 0.9700 0.9735 139 0.9846 0.9853 0.9870
218 0.9534 0.9550 0.9600 178 0.9691 0.9704 0.9739 138 0.9850 0.9857 0.9874
217 0.9538 0.9554 0.9604 177 0.9695 0.9708 0.9742 137 0.9853 0.9861 0.9877
216 0.9542 0.9557 0.9607 176 0.9699 0.9712 0.9745 136 0.9857 0.9865 0.9880
215 0.9546 0.9561 0.9611 175 0.9703 0.9715 0.9749 135 0.9861 0.9868 0.9884
214 0.9550 0.9565 0.9614 174 0.9707 0.9719 0.9752 134 0.9865 0.9872 0.9887
213 0.9554 0.9569 0.9618 173 0.9711 0.9723 0.9756 133 0.9869 0.9876 0.9890
212 0.9558 0.9573 0.9621 172 0.9715 0.9727 0.9759 132 0.9873 0.9880 0.9894
211 0.9561 0.9577 0.9625 171 0.9719 0.9731 0.9762 131 0.9877 0.9884 0.9897
210 0.9565 0.9581 0.9628 170 0.9723 0.9735 0.9766 130 0.9881 0.9887 0.9900
209 0.9569 0.9584 0.9632 169 0.9727 0.9738 0.9769 129 0.9885 0.9891 0.9904
208 0.9573 0.9588 0.9635 168 0.9731 0.9742 0.9772 128 0.9889 0.9895 0.9907
207 0.9577 0.9592 0.9639 167 0.9735 0.9746 0.9776 127 0.9893 0.9899 0.9910
206 0.9581 0.9596 0.9642 166 0.9739 0.9750 0.9779 126 0.9897 0.9902 0.9914
205 0.9585 0.9600 0.9646 165 0.9743 0.9754 0.9783 125 0.9901 0.9906 0.9917
204 0.9589 0.9604 0.9649 164 0.9747 0.9758 0.9786 124 0.9905 0.9910 0.9920
203 0.9593 0.9608 0.9652 163 0.9751 0.9762 0.9789 123 0.9909 0.9914 0.9924
202 0.9597 0.9611 0.9656 162 0.9754 0.9765 0.9793 122 0.9913 0.9917 0.9927
201 0.9601 0.9615 0.9659 161 0.9758 0.9769 0.9796 121 0.9917 0.9921 0.9930
200 0.9605 0.9619 0.9663 160 0.9762 0.9773 0.9800 120 0.9921 0.9925 0.9934
199 0.9609 0.9623 0.9666 159 0.9766 0.9777 0.9803 119 0.9925 0.9929 0.9937
198 0.9612 0.9627 0.9670 158 0.9770 0.9781 0.9806 118 0.9929 0.9932 0.9940
197 0.9616 0.9631 0.9673 157 0.9774 0.9785 0.9810 117 0.9932 0.9936 0.9944
196 0.9620 0.9634 0.9677 156 0.9778 0.9788 0.9813 116 0.9936 0.9940 0.9947
195 0.9624 0.9638 0.9680 155 0.9782 0.9792 0.9816 115 0.9940 0.9944 0.9950
194 0.9628 0.9642 0.9684 154 0.9786 0.9796 0.9820 114 0.9944 0.9948 0.9954
193 0.9632 0.9646 0.9687 153 0.9790 0.9800 0.9823 113 0.9948 0.9951 0.9957
192 0.9636 0.9650 0.9690 152 0.9794 0.9804 0.9827 112 0.9952 0.9955 0.9960
191 0.9640 0.9654 0.9694 151 0.9789 0.9808 0.9830 111 0.9956 0.9959 0.9964
190 0.9644 0.9658 0.9697 150 0.9802 0.9811 0.9833 110 0.9960 0.9962 0.9967
189 0.9648 0.9662 0.9701 149 0.9806 0.9815 0.9837 109 0.9964 0.9966 0.9970
188 0.9652 0.9665 0.9704 148 0.9810 0.9819 0.9840 108 0.9968 0.9970 0.9974
187 0.9656 0.9669 0.9708 147 0.9814 0.9823 0.9844 107 0.9972 0.9974 0.9977
186 0.9660 0.9673 0.9711 146 0.9818 0.9827 0.9847 106 0.9976 0.9978 0.9980
185 0.9664 0.9677 0.9714 145 0.9822 0.9830 0.9850 105 0.9980 0.9981 0.9983
184 0.9668 0.9681 0.9718 144 0.9826 0.9834 0.9854 104 0.9984 0.9985 0.9987
183 0.9672 0.9685 0.9721 143 0.9830 0.9838 0.9857 103 0.9988 0.9989 0.9990
182 0.9676 0.9688 0.9725 142 0.9834 0.9842 0.9860 102 0.9992 0.9992 0.9993
181 0.9680 0.9692 0.9728 141 0.9838 0.9846 0.9864 101 0.9996 0.9996 0.9997
100 1.0000 1.0000 1.0000
A
The portion of the table below should not be used unless the oil is entirely free from crystals
Volume at 100°F Occu- Volume at 100°F Occu- Volume at 100° Occu-
pied by Unit Volume at pied by Unit Volume at pied by Unit Volume at
Observed Observed Observed
Indicated Temperature Indicated Temperature Indicated Temperature
Temper- Temper- Temper-
ature, °F ature,° F ature,° F
Creo- Solu- Coal Creo- Solu- Coal Creo- Solu- Coal
sote tion Tar sote tion Tar sote tion Tar
99 1.0004 1.0004 1.0003 84 1.0063 1.0062 1.0053 69 1.0122 1.0116 1.0103
98 1.0008 1.0008 1.0007 83 1.0067 1.0066 1.0056 68 1.0126 1.0120 1.0106
97 1.0012 1.0011 1.0010 82 1.0071 1.0070 1.0060 67 1.0130 1.0124 1.0109
96 1.0016 1.0015 1.0013 81 1.0075 1.0074 1.0063 66 1.0134 1.0127 1.0112
95 1.0020 1.0019 1.0017 80 1.0079 1.0078 1.0066 65 1.0138 1.0131 1.0116
94 1.0024 1.0022 1.0020 79 1.0083 1.0079 1.0070 64 1.0142 1.0135 1.0119
93 1.0028 1.0026 1.0023 78 1.0087 1.0082 1.0073 63 1.0146 1.0138 1.0122
D347–97
TABLE 1 Continued
A
The portion of the table below should not be used unless the oil is entirely free from crystals
Volume at 100°F Occu- Volum
...

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