| Literature DB >> 24563561 |
Magdalena Tyczyńska1, Małgorzata Jóźwiak1.
Abstract
The density of 15-crown-5 ether (15C5) solutions in the mixtures of N,N-dimethylformamide (DMF) and water (H2O) was measured within the temperature range 293.15-308.15 K using an Anton Paar oscillatory U-tube densimeter. The results were used to calculate the apparent molar volumes (VΦ ) of 15C5 in the mixtures of DMF + H2O over the whole concentration range. Using the apparent molar volumes and Redlich and Mayer equation, the standard partial molar volumes of 15-crown-5 were calculated at infinite dilution ([Formula: see text]). The limiting apparent molar expansibilities (α) were also calculated. The data are discussed from the point of view of the effect of concentration changes on interactions in solution.Entities:
Keywords: 15-Crown-5; Density; Hydrophobic hydration; N,N-Dimethylformamide–water mixture; Partial molar volume
Year: 2014 PMID: 24563561 PMCID: PMC3925500 DOI: 10.1007/s10953-014-0138-7
Source DB: PubMed Journal: J Solution Chem ISSN: 0095-9782 Impact factor: 1.677
Experimental density of N,N-dimethylformamide and literature data
| Substance |
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|---|---|---|---|---|
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| DMF | 0.948737 | 0.943971 | 0.939196 | 0.934420 |
| 0.94939a | 0.94460a | 0.93983a | 0.93505a | |
| 0.95045b | 0.94559b | 0.94069b | 0.93561b | |
| 0.948051c | 0.942915c | 0.938876c | 0.933964c | |
| 0.94917d | 0.944e | 0.9386h | 0.9344h | |
| 0.94381f | ||||
| 0.94403g | ||||
aBerna-García et al. [25]
bMarchetti et al. [26]
cSharlin et al. [27]
dTôrres et al. [28]
eBakshi et al. [29]
fBendová et al. [30]
gTong-Chun et al. [31]
hAkhtar et al. [32]
Experimental densities, ρ, of 15-crown-5 in the DMF + H2O mixtures at temperatures T = (293.15, 298.15, 303.15 and 308.15) K
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|---|---|---|---|---|---|
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| 0.00 | 0 | 0.948737 | 0.943971 | 0.939196 | 0.934420 |
| 0.02548 | 0.949612 | 0.944847 | 0.940074 | 0.935300 | |
| 0.05941 | 0.950756 | 0.945992 | 0.941221 | 0.936447 | |
| 0.08622 | 0.951640 | 0.946877 | 0.942114 | 0.937343 | |
| 0.11692 | 0.952642 | 0.947884 | 0.943125 | 0.938359 | |
| 0.13341 | 0.953166 | 0.948402 | 0.943644 | 0.938876 | |
| 0.17510 | 0.954477 | 0.949715 | 0.944959 | 0.940197 | |
| 0.20937 | 0.955535 | 0.950789 | 0.946034 | 0.941275 | |
| 0.24408 | 0.956576 | 0.951832 | 0.947081 | 0.942326 | |
| 0.10 | 0 | 0.953731 | 0.948879 | 0.944216 | 0.939439 |
| 0.03367 | 0.954840 | 0.949990 | 0.945328 | 0.940554 | |
| 0.06351 | 0.955807 | 0.950958 | 0.946296 | 0.941523 | |
| 0.09159 | 0.956705 | 0.951856 | 0.947199 | 0.942428 | |
| 0.12396 | 0.957723 | 0.952879 | 0.948218 | 0.943453 | |
| 0.15189 | 0.958575 | 0.953736 | 0.949088 | 0.944310 | |
| 0.18502 | 0.959590 | 0.954751 | 0.950095 | 0.945334 | |
| 0.20868 | 0.960304 | 0.955451 | 0.950810 | 0.946049 | |
| 0.25199 | 0.961562 | 0.956728 | 0.952086 | 0.947332 | |
| 0.20 | 0 | 0.959310 | 0.954573 | 0.949823 | 0.945045 |
| 0.04255 | 0.960655 | 0.955919 | 0.951171 | 0.946398 | |
| 0.07195 | 0.961569 | 0.956833 | 0.952086 | 0.947314 | |
| 0.09842 | 0.962382 | 0.957646 | 0.952903 | 0.948136 | |
| 0.12857 | 0.963288 | 0.958561 | 0.953820 | 0.949060 | |
| 0.15401 | 0.964054 | 0.959321 | 0.954584 | 0.949819 | |
| 0.18505 | 0.964960 | 0.960245 | 0.955506 | 0.950752 | |
| 0.21101 | 0.965727 | 0.961002 | 0.956267 | 0.951517 | |
| 0.25734 | 0.967045 | 0.962328 | 0.957596 | 0.952839 | |
| 0.30 | 0 | 0.965705 | 0.960992 | 0.956253 | 0.951493 |
| 0.02471 | 0.966441 | 0.961730 | 0.956994 | 0.952236 | |
| 0.05485 | 0.967328 | 0.962619 | 0.957884 | 0.953130 | |
| 0.08073 | 0.968082 | 0.963374 | 0.958637 | 0.953883 | |
| 0.10921 | 0.968901 | 0.964195 | 0.959466 | 0.954715 | |
| 0.13379 | 0.969599 | 0.964897 | 0.960160 | 0.955410 | |
| 0.16111 | 0.970369 | 0.965665 | 0.960939 | 0.956192 | |
| 0.17732 | 0.970821 | 0.966119 | 0.961394 | 0.956647 | |
| 0.21842 | 0.971953 | 0.967254 | 0.962534 | 0.957787 | |
| 0.40 | 0 | 0.972987 | 0.968296 | 0.963577 | 0.958796 |
| 0.02690 | 0.973758 | 0.969067 | 0.964349 | 0.959571 | |
| 0.05893 | 0.974663 | 0.969974 | 0.965259 | 0.960484 | |
| 0.07837 | 0.975204 | 0.970517 | 0.965806 | 0.961031 | |
| 0.11204 | 0.976138 | 0.971452 | 0.966740 | 0.961967 | |
| 0.13346 | 0.976713 | 0.972038 | 0.967327 | 0.962556 | |
| 0.16708 | 0.977630 | 0.972948 | 0.968239 | 0.963471 | |
| 0.19964 | 0.978498 | 0.973818 | 0.969110 | 0.964344 | |
| 0.23028 | 0.979305 | 0.974627 | 0.969920 | 0.965157 | |
| 0.50 | 0 | 0.980849 | 0.976200 | 0.971517 | 0.966802 |
| 0.02234 | 0.981473 | 0.976823 | 0.972141 | 0.967426 | |
| 0.05427 | 0.982354 | 0.977704 | 0.973025 | 0.968309 | |
| 0.07937 | 0.983037 | 0.978387 | 0.973710 | 0.968992 | |
| 0.10775 | 0.983803 | 0.979151 | 0.974479 | 0.969758 | |
| 0.12484 | 0.984258 | 0.979608 | 0.974936 | 0.970217 | |
| 0.16227 | 0.985245 | 0.980597 | 0.975928 | 0.971207 | |
| 0.19826 | 0.986181 | 0.981530 | 0.976867 | 0.972146 | |
| 0.22877 | 0.986960 | 0.982314 | 0.977652 | 0.972930 | |
| 0.60 | 0 | 0.988582 | 0.984016 | 0.979419 | 0.974785 |
| 0.02030 | 0.989155 | 0.984587 | 0.979990 | 0.975354 | |
| 0.03362 | 0.989529 | 0.984960 | 0.980362 | 0.975726 | |
| 0.06490 | 0.990396 | 0.985826 | 0.981225 | 0.976588 | |
| 0.09303 | 0.991169 | 0.986597 | 0.981997 | 0.977360 | |
| 0.12367 | 0.992000 | 0.987427 | 0.982827 | 0.978187 | |
| 0.15369 | 0.992802 | 0.988226 | 0.983625 | 0.978984 | |
| 0.18395 | 0.993600 | 0.989023 | 0.984420 | 0.979780 | |
| 0.25543 | 0.995445 | 0.990865 | 0.986260 | 0.981619 | |
| 0.70 | 0 | 0.995521 | 0.991167 | 0.986768 | 0.982319 |
| 0.03136 | 0.996464 | 0.992101 | 0.987695 | 0.983239 | |
| 0.06435 | 0.997443 | 0.993070 | 0.988659 | 0.984194 | |
| 0.09125 | 0.998224 | 0.993844 | 0.989431 | 0.984956 | |
| 0.11435 | 0.998893 | 0.994508 | 0.990088 | 0.985616 | |
| 0.15157 | 0.999956 | 0.995565 | 0.991137 | 0.986646 | |
| 0.18098 | 1.000785 | 0.996387 | 0.991953 | 0.987424 | |
| 0.20196 | 1.001369 | 0.996967 | 0.992529 | 0.988026 | |
| 0.23981 | 1.002417 | 0.998008 | 0.993562 | 0.989070 | |
| 0.80 | 0 | 0.999822 | 0.995938 | 0.991999 | 0.987998 |
| 0.03182 | 1.000884 | 0.996986 | 0.993035 | 0.989021 | |
| 0.06761 | 1.002061 | 0.998150 | 0.994180 | 0.990158 | |
| 0.10137 | 1.003158 | 0.999234 | 0.995264 | 0.991212 | |
| 0.13026 | 1.004090 | 1.000146 | 0.996151 | 0.992096 | |
| 0.15750 | 1.004958 | 1.001001 | 0.996994 | 0.992930 | |
| 0.19474 | 1.006118 | 1.002143 | 0.998121 | 0.994039 | |
| 0.20937 | 1.006572 | 1.002591 | 0.998563 | 0.994478 | |
| 0.26742 | 1.008344 | 1.004339 | 1.000287 | 0.996181 | |
| 0.90 | 0 | 0.999747 | 0.996896 | 0.993931 | 0.990857 |
| 0.02425 | 1.000667 | 0.997792 | 0.994803 | 0.991718 | |
| 0.06077 | 1.002037 | 0.999125 | 0.996102 | 0.993000 | |
| 0.10132 | 1.003533 | 1.000583 | 0.997525 | 0.994401 | |
| 0.11740 | 1.004122 | 1.001160 | 0.998083 | 0.994952 | |
| 0.13681 | 1.004826 | 1.001846 | 0.998748 | 0.995613 | |
| 0.17294 | 1.006122 | 1.003106 | 0.999979 | 0.996827 | |
| 0.20232 | 1.007166 | 1.004121 | 1.000967 | 0.997804 | |
| 0.23732 | 1.008391 | 1.005317 | 1.002131 | 0.998952 | |
| 0.92 | 0 | 0.999213 | 0.996655 | 0.993967 | 0.991148 |
| 0.03136 | 1.000408 | 0.997816 | 0.995106 | 0.992268 | |
| 0.06265 | 1.001589 | 0.998962 | 0.996231 | 0.993374 | |
| 0.09774 | 1.002895 | 1.000233 | 0.997477 | 0.994599 | |
| 0.12799 | 1.004011 | 1.001315 | 0.998539 | 0.995644 | |
| 0.15895 | 1.005139 | 1.002411 | 0.999614 | 0.996700 | |
| 0.19205 | 1.006334 | 1.003571 | 1.000751 | 0.997819 | |
| 0.21136 | 1.007023 | 1.004239 | 1.001408 | 0.998464 | |
| 0.26014 | 1.008749 | 1.005912 | 1.003051 | 1.000078 | |
| 0.94 | 0 | 0.998613 | 0.996383 | 0.993997 | 0.991465 |
| 0.03717 | 1.000020 | 0.997759 | 0.995345 | 0.992788 | |
| 0.06953 | 1.001232 | 0.998944 | 0.996502 | 0.993923 | |
| 0.09583 | 1.002213 | 0.999904 | 0.997433 | 0.994832 | |
| 0.13217 | 1.003545 | 1.001207 | 0.998721 | 0.996094 | |
| 0.16474 | 1.004731 | 1.002368 | 0.999851 | 0.997212 | |
| 0.20262 | 1.006084 | 1.003694 | 1.001159 | 0.998491 | |
| 0.22400 | 1.006831 | 1.004423 | 1.001871 | 0.999187 | |
| 0.27371 | 1.008583 | 1.006135 | 1.003547 | 1.000829 | |
| 0.96 | 0 | 0.998064 | 0.996186 | 0.994128 | 0.991899 |
| 0.02961 | 0.999179 | 0.997277 | 0.995195 | 0.992944 | |
| 0.06577 | 1.000529 | 0.998597 | 0.996484 | 0.994206 | |
| 0.09853 | 1.001742 | 0.999775 | 0.997638 | 0.995337 | |
| 0.12369 | 1.002660 | 1.000674 | 0.998517 | 0.996199 | |
| 0.15178 | 1.003682 | 1.001671 | 0.999488 | 0.997147 | |
| 0.18196 | 1.004770 | 1.002731 | 1.000525 | 0.998162 | |
| 0.21265 | 1.005857 | 1.003794 | 1.001564 | 0.999177 | |
| 0.25315 | 1.007279 | 1.005182 | 1.002920 | 1.000502 | |
| 0.98 | 0 | 0.997773 | 0.996269 | 0.994553 | 0.992644 |
| 0.02909 | 0.998855 | 0.997327 | 0.995588 | 0.993659 | |
| 0.06203 | 1.000069 | 0.998512 | 0.996751 | 0.994798 | |
| 0.09171 | 1.001153 | 0.999570 | 0.997786 | 0.995811 | |
| 0.12209 | 1.002250 | 1.000647 | 0.998833 | 0.996846 | |
| 0.15501 | 1.003428 | 1.001796 | 0.999969 | 0.997943 | |
| 0.18354 | 1.004440 | 1.002784 | 1.000930 | 0.998902 | |
| 0.20860 | 1.005323 | 1.003649 | 1.001774 | 0.999726 | |
| 0.24953 | 1.006746 | 1.005039 | 1.003135 | 1.001057 | |
| 1.00 | 0 | 0.998199 | 0.997043 | 0.995649 | 0.994041 |
| 0.02470 | 0.999077 | 0.997898 | 0.996488 | 0.994859 | |
| 0.06100 | 1.000348 | 0.999145 | 0.997711 | 0.996065 | |
| 0.09177 | 1.001429 | 1.000189 | 0.998745 | 0.997078 | |
| 0.11536 | 1.002244 | 1.000985 | 0.999524 | 0.997845 | |
| 0.13029 | 1.002753 | 1.001488 | 1.000020 | 0.998329 | |
| 0.17530 | 1.004282 | 1.002977 | 1.001491 | 0.999777 | |
| 0.20216 | 1.005193 | 1.003866 | 1.002358 | 1.000628 | |
| 0.23731 | 1.006360 | 1.005023 | 1.003489 | 1.001745 | |
x 2 is the mole fraction of water in the mixture
Coefficient b V of Eq. 2
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| 0.00 | 4.71 ± 0.10 | 4.48 ± 0.24 | 4.46 ± 0.22 | 4.32 ± 0.30 |
| 0.10 | 2.99 ± 0.18 | 3.04 ± 0.14 | 2.69 ± 0.13 | 2.71 ± 0.18 |
| 0.20 | 1.81 ± 0.15 | 1.43 ± 0.07 | 1.30 ± 0.07 | 1.34 ± 0.22 |
| 0.30 | 0.76 ± 0.03 | 0.82 ± 0.04 | 0.88 ± 0.23 | 1.06 ± 0.24 |
| 0.40 | 0.79 ± 0.18 | 0.56 ± 0.04 | 0.61 ± 0.09 | 0.75 ± 0.06 |
| 0.50 | 0.80 ± 0.05 | 0.59 ± 0.04 | 0.35 ± 0.08 | 0.47 ± 0.05 |
| 0.60 | 0.64 ± 0.06 | 0.52 ± 0.09 | 0.57 ± 0.11 | 0.36 ± 0.12 |
| 0.70 | 0.91 ± 0.14 | 0.62 ± 0.16 | 0.68 ± 0.10 | 0.85 ± 0.51 |
| 0.80 | 0.42 ± 0.12 | 0.68 ± 0.10 | 0.96 ± 0.28 | 1.06 ± 0.13 |
| 0.90 | 0.51 ± 0.04 | 0.41 ± 0.09 | 0.34 ± 0.08 | 0.27 ± 0.04 |
| 0.92 | −0.25 ± 0.04 | −0.17 ± 0.02 | −0.19 ± 0.02 | −0.19 ± 0.02 |
| 0.94 | −0.42 ± 0.18 | −0.51 ± 0.20 | −0.72 ± 0.19 | −0.68 ± 0.25 |
| 0.96 | −0.97 ± 0.15 | −0.60 ± 0.08 | −0.55 ± 0.03 | −0.38 ± 0.08 |
| 0.98 | −0.90 ± 0.04 | −0.96 ± 0.06 | −0.86 ± 0.12 | −0.92 ± 0.12 |
| 1.00 | −1.71 ± 0.29 | −1.65 ± 0.15 | −1.59 ± 0.14 | −1.44 ± 0.10 |
± is the standard deviation
Partial molar volume of 15-crown-5, , in the DMF + H2O mixtures
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| 0.00 | 193.72 ± 0.01 | 194.49 ± 0.04 | 195.16 ± 0.03 | 195.90 ± 0.04 |
| 0.10 | 194.39 ± 0.03 | 195.13 ± 0.02 | 195.90 ± 0.20 | 196.63 ± 0.09 |
| 0.20 | 194.90 ± 0.02 | 195.70 ± 0.01 | 196.45 ± 0.01 | 197.13 ± 0.04 |
| 0.30 | 195.97 ± 0.01 | 196.70 ± 0.01 | 197.42 ± 0.03 | 198.14 ± 0.03 |
| 0.40 | 195.96 ± 0.03 | 196.73 ± 0.01 | 197.47 ± 0.01 | 198.19 ± 0.01 |
| 0.50 | 195.39 ± 0.01 | 196.23 ± 0.01 | 196.97 ± 0.01 | 197.80 ± 0.01 |
| 0.60 | 193.79 ± 0.01 | 194.64 ± 0.01 | 195.44 ± 0.01 | 196.31 ± 0.02 |
| 0.70 | 190.72 ± 0.02 | 191.74 ± 0.02 | 192.65 ± 0.02 | 193.64 ± 0.08 |
| 0.80 | 186.70 ± 0.20 | 187.71 ± 0.02 | 188.71 ± 0.04 | 189.75 ± 0.02 |
| 0.90 | 182.18 ± 0.01 | 183.59 ± 0.01 | 185.02 ± 0.01 | 185.96 ± 0.01 |
| 0.92 | 182.05 ± 0.01 | 183.51 ± 0.01 | 184.62 ± 0.01 | 185.66 ± 0.01 |
| 0.94 | 182.33 ± 0.03 | 183.50 ± 0.03 | 184.68 ± 0.03 | 185.76 ± 0.04 |
| 0.96 | 182.67 ± 0.02 | 183.78 ± 0.01 | 184.91 ± 0.01 | 185.99 ± 0.01 |
| 0.98 | 183.21 ± 0.01 | 184.29 ± 0.01 | 185.30 ± 0.02 | 186.31 ± 0.02 |
| 1.00 | 185.02 ± 0.04 | 186.02 ± 0.02 186.4a 186.2b 186.06c 186.46d | 186.79 ± 0.02 | 187.59 ± 0.01 |
x 2 is the mole fraction of water in the mixture
± is the standard deviation
aDagade et al. [20]
bBernal et al. [39]
cHøiland [40]
dZielenkiewicz et al. [41]
Fig. 1Standard partial molar volume () of 15-crown-5 (full symbol) and urea [21] (open symbol) in the DMF + H2O mixtures for various temperatures: filled square 293.15 K, filled circle 298.15 K, filled triangle 303.15 K, filled tilled triangle 308.15 K as a function of the mole fraction of water
Fig. 2Standard solvation enthalpy (Δsolv H°) (see the text) of: filled circle, 15-crown-5; and filled square, urea in the solvent mixture (DMF + H2O) at 298.15 K as a function of the mole fraction of water
Limiting apparent molar expansibilities of 15C5 in the DMF + H2O mixtures
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|---|---|---|
| 0.00 | 0.144 ± 0.003 | 0.99936 |
| 0.10 | 0.150 ± 0.001 | 0.99990 |
| 0.20 | 0.149 ± 0.003 | 0.99870 |
| 0.30 | 0.145 ± 0.001 | 0.99998 |
| 0.40 | 0.149 ± 0.002 | 0.99978 |
| 0.50 | 0.159 ± 0.003 | 0.99942 |
| 0.60 | 0.167 ± 0.002 | 0.99976 |
| 0.70 | 0.193 ± 0.003 | 0.99956 |
| 0.80 | 0.203 ± 0.001 | 0.99994 |
| 0.90 | 0.255 ± 0.017 | 0.99170 |
| 0.92 | 0.239 ± 0.014 | 0.99331 |
| 0.94 | 0.229 ± 0.003 | 0.99960 |
| 0.96 | 0.222 ± 0.001 | 0.99992 |
| 0.98 | 0.206 ± 0.002 | 0.99972 |
| 1.00 | 0.170 ± 0.007 0.18a | 0.99628 |
x 2 is the mole fraction of water in the mixture
± is the standard deviation
R is the regression coefficient
aBernal et al. [57]
Fig. 3Limiting apparent molar expansibilities of filled circle, 15-crown-5, and filled square, urea in the solvent mixture (DMF + H2O)