
By M. Frenkel, X. Hong, R.C. Wilhoit, K.R. Hall, K.R. Hall, K.N. Marsh
Info at the densities of natural compounds are crucial for either clinical and business functions. wisdom of densities is necessary in lots of parts, together with custody move of fabrics, product specification, improvement of assorted predictive equipment, and for characterizing compounds and estimating their purity. The densities of alcohols have been amassed from the unique literature released from 1870, to early 1998 and significantly evaluated. The tables comprise the unique literature facts besides their envisioned uncertainties, and the evaluated info, in either numerical shape and as coefficients to equations with chosen statistical info. the quantity additionally comprises the CASR quantity Index and a Chemical identify Index. The integrated CD-ROM permits quickly complete textual content index seek.
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Coefficients of the polynomial expansion equation. 7605 · 10−2 (combined temperature ranges, unweighted). 11090 · 10−3 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 3 −3 − in Fig. 17 14-smi( ) 1) Ref. (Symbol in Fig. 1) 14-smi( ) 14-smi( ) 14-smi( ) 14-smi( ) 14-smi( ) 28-tim/mar( ) 28-tim/mar( ) 28-tim/mar( ) Not included in Fig. 1. cont. 1 Alkanols, C1 - C4 31 ρ ρ Further references: [48-kor/pat].
Coefficients for the polynomial expansion equations. 6459 · 10−1 (combined temperature ranges, unweighted). 07285 · 10−6 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig. 24 1) Ref. (Symbol in Fig. 1) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 63-amb/tow(✕ ) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah1) 64-dan/bah(✕ ) 83-hal/gun(∇) 83-hal/gun(∇) 83-hal/gun(∇) 83-hal/gun(∇) 83-hal/gun(∇) 83-hal/gun(∇) 83-hal/gun(∇) 83-hal/gun(∇) 83-hal/gun(∇) Not included in Fig.
The curves above and below the zero line indicate the calculated error region of the recommended values given in Table 3. The error bars represent the experimental errors. 20 kg·m−3 [63-amb/bro] Table 1. Coefficients for the polynomial expansion equations. 2141 · 10−1 (combined temperature ranges, unweighted). 95139 · 10−7 cont. 1 Alkanols, C1 - C4 Table 2. Experimental values with uncertainties and deviation from calculated values. ρexp − ρcalc Ref. (Symbol ρexp − ρcalc ρexp ± 2σ est ρexp ± 2σ est T T −3 −3 −3 in Fig.