Dr. Ing. Teodorescu Mariana – Verificarea indeplinirii standardele minimale in domeniul Chimie cf. Ordin
4478/2011 pentru aprobarea sustinerii tezei de abilitare 1.Verificarea indeplinirii standardului Smed ≥ 0.4; criteriu indeplinit: Smed = 0.5091. Numarul publicatiei
Referinta bibliografica si ni si/ni
1 Teodorescu M., Barhala A., Marchidan D. I., Landauer O., Vapour pressures and excess Gibbs energy of ethylbenzene - cyclooctane binary mixtures. Fluid Phase Equilibria, 126, 127-134 (1996).
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2 Teodorescu M., Linek J., Densities and excess volumes of pentan-3-one + 1,2-dichloroethane, +1,3-dichloropropane, + 1,4-dichlorobutane, + trichloromethane, + 1,1,1-trichloroethane, + 1,1,2,2-tetrachloroethane binary mixtures at 298.15 K. Fluid Phase Equilibria, 146 (1998) 155-160.
1.63836 2 0.81918
3 Teodorescu M., Aim K., Wichterle I., Isothermal vapour-liquid equilibria for pentan-3-one + 1,4-dichlorobutane, + trichloromethane, + 1,1,1-trichloroethane, + 1,1,2,2-tetrachloroethane binary mixtures. Fluid Phase Equilibria, 147 (1998) 215-228.
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4 Teodorescu M., Linek J., Wichterle I., Isothermal vapour-liquid equilibria and densities for the 5-chloropentan-2-one + n-hexane, + toluene, + ethylbenzene binary mixtures. Fluid Phase Equilibria, 149 (1998) 127-138.
1.63836 3 0.54612
5 Teodorescu M., Wagner Z., Wichterle I., Application of the predictive UNIFAC model to the pentan-3-one / chloroalkane and 5-chloro-2-pentanone / hydrocarbon binary systems. Chemical Engineering & Technology, 23 (2000) No. 4, 367-370.
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6 Teodorescu M., Wichterle I., Evaluation of the carbonyl / chlorine interaction parameters in the pentan-3-one + chloroalkane mixtures using the DISQUAC group contribution model. Collection of Czechoslovak Chemical Communications, 65/10 (2000) 1559-1570.
0.68862 2 0.34431
7 Teodorescu M., Aim K., Wichterle I., Isothermal vapor-liquid equilibrium in the quaternary water + isopropanol + acetic acid + isopropyl acetate system with chemical reaction. Journal of Chemical and Engineering Data, 46/2 (2001) 261-266.
1.53774 3 0.51258
8 Teodorescu M., Rasmussen P., High pressure vapor-liquid equilibria in the systems: nitrogen + dimethyl ether, methanol + dimethyl ether, carbon dioxide + dimethyl ether + methanol and nitrogen + dimethyl ether + methanol. Journal of Chemical and Engineering Data, 46/3 (2001) 640-646.
1.53774 2 0.76887
9 Teodorescu M., Wilken M., Wittig R., Gmehling J., Azeotropic and solid-liquid equilibria data for several binary organic systems containing one acetal compound,
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2
Fluid Phase Equilibria 204 (2003) 267-280. 10 Teodorescu M., Wichterle I., Modeling of the Nitrogen
and Carbon Dioxide Solubility in Alternative Fuels at High Pressures Using Soave–Redlich–Kwong Equation of State, Chem. Eng. & Technology, 26/9 (2003) 992-995.
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11 Teodorescu M., Krummen M., Gmehling J., Excess Molar Enthalpies for the Binary Systems of Benzene or Cyclohexane with 1,1-Diethoxyethane at 323.15 K or with 2,2-Dimethoxybutane at 303.15 K and Infinite Dilution Activity Coefficients in 1,1-Diethoxyethane, Journal of Chemical and Engineering Data, 48 (2003) 435-439.
1.53774 3 0.51258
12 Valtz A., Teodorescu M., Wichterle I., Richon D., Liquid densities and excess molar volumes for water + diglycolamine, and water, methanol, ethanol, 1-propanol + triethylene glycol binary systems at atmospheric pressure and temperatures in the range of 283.15 - 363.15 K, Fluid Phase Equilibria, 215 (2004) 129-142.
1.63836 4 0.40959
13 Teodorescu M., Barhala A., Dragoescu D., Isothermal (vapour-liquid) equilibria for the binary (cyclopentanone or cyclohexanone with 1,1,2,2-tetrachloroethane) systems at temperatures of (343.15, 353.15 and 363.15) K, The Journal of Chemical Thermodynamics, 38/11 (2006) 1432-1437.
1.33630 3 0.44543
14 Dana Dragoescu, Mariana Teodorescu and Alexandru Barhala, Isothermal (vapour + liquid) equilibria and excess Gibbs free energies in some binary (cyclopentanone + chloroalkane) mixtures at temperatures from 298.15 K to 318.15 K, The Journal of Chemical Thermodynamics, 39 (2007) 1452-1457.
1.33630 3 0.44543
15 Dana Dragoescu, Alexandru Barhala, Mariana Teodorescu, Vapour pressure and excess Gibbs energy of binary 1, 2-dichloroethane + cyclohexanone, chloroform + cyclopentanone and chloroform + cyclohexanone mixtures at temperatures from 298.15 to 318.15 K, Fluid Phase Equilib. 267 (1) (2008) 70-78.
1.63836 3 0.54612
16 Dana Dragoescu, Alexandru Barhala, Mariana Teodorescu, (Vapour + liquid) equilibria and excess Gibbs energies of (cyclohexanone + 1-chlorobutane and + 1,1,1-trichloroethane) binary mixtures at temperatures from (298.15 K to 318.15) K, The Journal of Chemical Thermodynamics, 41 (2009) 1025-1029.
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17 Mariana Teodorescu, Alexandru Barhala, Dana Dragoescu, Isothermal vapour–liquid equilibria for 1,2-dichloroethane + nitromethane and + nitroethane binary systems at temperatures between 333.15 and 353.15 K, Fluid Phase Equilibria, 292 (2010) 58–63.
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18 Mariana Teodorescu, Alexandru Barhala, Dana Dragoescu, Daniela Gheorghe, Isothermal Vapor_Liquid Equilibria for Nitromethane and Nitroethane + 1,3-Dichloropropane Binary Systems at
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3
Temperatures between (343.15 and 363.15) K, Journal of Chemical and Engineering Data, 56 (2011), 4665–4671.
19 Mariana Teodorescu, Dana Dragoescu, Daniela Gheorghe, Isothermal (vapour + liquid) equilibria for (nitromethane or nitroethane + 1,4-dichlorobutane) binary systems at temperatures between (343.15 and 363.15) K, The Journal of Chemical Thermodynamics, 56 (2013) 32-37.
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20 Dragoescu D., Teodorescu M., Gheorghe D. Isothermal vapour-liquid equilibria and excess Gibbs free energies in some binary nitroalkane + chloroalkane mixtures at temperatures from 298. 15 K to 318. 15 K. Fluid Phase Equilibria, 338 (2013) 16-22.
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21 Gheorghe D., Dragoescu D., Teodorescu M., Volumetric study for the binary nitromethane with chloroalkanes mixtures at Temperatures in the Range (298.15 - 318.15) K, Journal of Chemical and Engineering Data, 58 (2013) 1161-1167.
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2.Verificarea indeplinirii standardului Cmed ≥ 5; criteriu indeplinit: Cmed = 5.55 Numarul publicatiei care citeaza
Referinta bibliografica a publicatiei k care citeaza
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Teodorescu M., Barhala A., Landauer O., Isothermal vapor-liquid equilibrium data for the binary cyclooctane + butylbenzene and n-heptane + cyclooctane at temperatures from 343.15 K to 393.15 K, ELDATA: Int. Electron. J. Phys.-Chem. Data, 2, 169-174 (1996). 1 Vitu-S, Jaubert-JN, Mutelet-F,
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Teodorescu M., Linek J., Densities and excess volumes of pentan-3-one + 1,2-dichloroethane, +1,3-dichloropropane, + 1,4-dichlorobutane, + trichloromethane, + 1,1,1-trichloroethane, + 1,1,2,2-tetrachloroethane binary mixtures at 298.15 K. Fluid Phase Equilibria, 146 (1998) 155-160. 2 Iloukhani, H., Samiey, B., in
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trichloroethane, + 1,1,2,2- tetrachloroethane, + trichloroethylene and tetrachloroethylene at (293.15, 298.15, and 303.15) K for the liquid region and at ambient pressure, Journal of Chemical and Engineering Data 50 (6) (2005), pp. 1911-1916.
3 Ajmani, S., Rogers, S.C., Barley, M.H., Livingstone, D.J., in Application of QSPR to mixtures, Journal of Chemical Information and Modeling 46 (5) (2006), pp. 2043-2055.
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4 Magalhaes-JG, Torres-RB, Volpe-PLO, in Volumetric behavior of binary-mixtures of (trichloromethane + amines) at temperatures between T = (288.15 and 303.15) K at P = 0.1 MPa, Journal of Chemical Thermodynamics, 40 (2008) 1402-1417.
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5 Ali, A., Tariq, M., in Temperature dependence of excess molar volumes, (∂ VE / ∂ T) and deviation in isentropic compresibilities of binary liquid mixtures of benzene with chloroalkanes, Journal of Molecular Liquids 137 (1-3), (2008), 64-73
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6 Tafat-Igoudjilene, O., Daoudi, H., Bey-Larouci, A.H., Aitkaci, A., Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure, Thermochimica Acta, 561, (2013), 63-71
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Teodorescu M., Aim K., Wichterle I., Isothermal vapour-liquid equilibria for pentan-3-one + 1,4-dichlorobutane, + trichloromethane, + 1,1,1-trichloroethane, + 1,1,2,2-tetrachloroethane binary mixtures. Fluid Phase Equilibria, 147 (1998) 215-228. 7 Dragoescu D., Barhala A., Vilcu
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8 Bernatova S., Wichterle I., in “Isothermal vapor-liquid equilibrium in the binary tert-butanol or 2,2,4-trimethylpentane + 1-tert-buthoxy-2-propanol, and in the ternary tert-butanol + 2,2,4-trimethylpentane + 1-tert-butoxy-2-propanol systems”, Fluid Phase Equilibria 189/1-2 (2001) 111-118.
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9 Bernatova S., Wichterle I., in “Isothermal vapor-liquid equilibria in the ternary system tert-buthyl methyl ether + tert-butanol + 2,2,4-trimethylpentane and 3 binary subsystems”, Fluid Phase Equilibria 180/1-2 (2001) 235-245.
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10 Constantinescu D., Wichterle I., in “Isothermal vapor-liquid equilibria and excess molar volumes in the binary ethanol plus methyl propanoate or methyl butanoate systems”, Fluid Phase Equilibria 203/1-2 (2002) 71-82.
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11 Psutka S., Wichterle I., in “Isothermal vapour-liquid equilibria in the binary and ternary systems composed of 2-propanol, diizopropyl eter and 1-methoxy-2-propanol”, Fluid Phase Equilibria 220/2 (2004) 161-165.
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12 Psutka, S., Wichterle, I., in Isothermal vapour-liquid equilibria in the binary and ternary systems composed of 2-propanol, diisopropyl ether and 4-methyl-2-pentanone, Fluid Phase Equilibria 235 (1) (2005), pp. 58-63.
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13 Psutka, S., Wichterle, I., in Vapor-liquid equilibria in the binary and ternary systems composed of 2-methylpentane, 3-methyl-2-butanone and 3-methyl-2-butanol, Journal of Chemical and Engineering Data 50 (4) (2005), pp. 1338-1342.
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14 Bernatová, S., Aim, K., Wichterle, I., in Isothermal vapour-liquid equilibrium with chemical reaction in the quaternary water + methanol + acetic acid + methyl acetate
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system, and in five binary subsystems, Fluid Phase Equilibria 247 (1-2) (2006), pp. 96-101.
15 Svatoslava Bernatov , Karel Aim, and Ivan Wichterle, in Vapor-Liquid and Chemical Equilibria in the Ethanol + Ethanoic Acid System at 348.15 K, J. Chem. Eng. Data, 52 (1) (2007), 20 -23.
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16 Psutka-S, Wichterle-I, Isothermal vapor-liquid-equilibria in the binary and ternary-systems composed of 2-propanol, 3-methyl-2-butanone and 2,2,4-trimethylpentane, Fluid Phase Equilibria, 264 (2008) 55-61.
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Teodorescu M., Linek J., Wichterle I., Isothermal vapour-liquid equilibria and densities for the 5-chloropentan-2-one + n-hexane, + toluene, + ethylbenzene binary mixtures, Fluid Phase Equilibria, 149, 127-138 (1998). 17 Ajmani-S, Rogers-SC, Barley-
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19 Sanz M. T., Beltran S., Calvo B., Cabezas J. L., Coca J., in “Vapor-liquid equilibria of the mixtures involved in the esterification of lactic acid with methanol”, J. Chem. Eng. Data 48/6 (2003) 1446-1452.
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20 Chang, W., Guan, G., Li, X., Yao, H., in Isobaric vapor-liquid equilibria for water + acetic acid + (n-pentyl acetate or isopropyl acetate), Journal of Chemical and Engineering Data 50 (4) (2005), pp. 1129-1133.
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21 Toikka, A., Toikka, M., in Phase transitions and azeotropic properties of acetic acid-n-
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22 Bernatová, S., Aim, K., Wichterle, I. in Isothermal vapour-liquid equilibrium with chemical reaction in the quaternary water + methanol + acetic acid + methyl acetate system, and in five binary subsystems, Fluid Phase Equilibria 247 (1-2) (2006), pp. 96-101.
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23 Mandagarán, B.A., Campanella, E.A., in Correlation of vapor - Liquid equilibrium data for acetic acid -isopropanol -water -isopropyl acetate mixtures, Brazilian Journal of Chemical Engineering 23 (1) (2006), pp. 93-103.
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25 Delgado-P, Sanz-MT, Beltran-S, Isobaric vapor-liquid-equilibria for the quaternary reactive system - ethanol plus water plus ethyl lactate plus lactic-acid at 101.33 kPa, Fluid Phase Equilibria, 255/1 (2007), 17-23,
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27 Zhu ZY, Ma YX, Gao J, Isobaric Vapor-Liquid Equilibria for Binary Systems of Acetic Acid plus Benzene, Chloroacetic Acid plus Benzene, and Dichloroacetic Acid plus Benzene at 101.33 kPa, JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2010, 55 3387-3390.
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33 López, J.A., Trejos, V.M., Cardona, C.A., in Objective functions analysis in the minimization of binary VLE data for asymmetric mixtures at high pressures, Fluid Phase Equilibria 248 (2) (2006), pp. 147-157.
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34 Arturo-SG, Knox-DE, Application of force-field in Gibbs ensemble lattice statistics to model vapor/liquid equilibria, Fluid Phase Equilibria, 252 (2007) 175-188.
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35 Ihmels E.C., Lemmon E.W., Experimental densities, vapor pressures, and critical point, and a fundamental equation of state for dimethyl ether, Fluid Phase Equilibria 260 (2007) 36-48.
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42 Kim, S.A., Yim, J.H., Byun, H.-S., Lim, J.S., Isothermal vapor-liquid equilibria for the binary system of dimethyl ether (CH 3OCH3)+ methanol (CH3OH), Korean Journal of Chemical Engineering, 2011, 28(12), pp. 2324-2328.
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44 Minh, L.Q., Van Duc Long, N., Lee, M. Energy efficiency improvement of dimethyl ether purification process by utilizing dividing wall columns, Korean Journal of Chemical Engineering , 2012, 29 (11) , pp. 1500-1507.
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45 Kiss, A.A., Ignat, R.M. Revamping Dimethyl Ether Separation to a Single-Step Process. Chemical Engineering and Technology, 36 (7,) (2013), 1261-1267.
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47 Varanda, F., Pratas De Melo, M.J., Cac ̧o, A.I., Dohrn, R., Makrydaki, F.A., Voutsas, E., Tassios, D., Marrucho, I.M., in Solubility of antibiotics in different solvents. 1. Hydrochloride forms of tetracycline, moxifloxacin, and ciprofloxacin, Industrial and Engineering Chemistry Research 45 (18) (2006), pp. 6368-6374.
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51 Kim JI, Choi YY, Park SJ, Solid-Liquid Equilibria, Excess Molar Volumes, and Molar Refractivity Deviations for Extractive Solvents of Molybdenum, JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2010, 55, 1179-1185.
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57 Antonio Razzouk, Ilham Mokbel, Josefa Garcia, Josefa Fernandez, Nizar Msakni, Jacques Jose, Vapor pressure measurements in the range 10−5 Pa to 1 Pa of four pentaerythritol esters. Density and vapor–liquid equilibria modeling of ester lubricants, Fluid Phase Equilibria 260 (2007) 248–261.
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65 Coquelet, C., Valtz, A., Courtial, X., Richon, D., in Volumetric properties of the water + 3-(dimethylamino) propylamine (DMAPA) mixture at atmospheric pressure from 283.15 to 353.15 K, Thermochimica Acta 448 (1) (2006), pp. 47-51.
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70 Qun-Sheng Li, Ming-Gao Su, and Shui Wang, Densities and Excess Molar Volumes for Binary Glycerol + 1-Propanol, + 2-Propanol, + 1,2-Propanediol, and + 1,3-Propanediol Mixtures at Different Temperatures, J. Chem. Eng. Data, 2007, 52 (3), pp 1141–1145.
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73 Abdulagatov, I.M., Tekin, A., Safarov, J., Shahverdiyev, A., Hassel, E. in High-pressure densities and derived volumetric properties (excess, apparent and partial molar volumes) of binary mixtures of methanol + [BMIM][PF 6], Journal of Solution Chemistry 2008, 37 (6), pp. 801-833
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75 Wang, Ying; Lian, Hong-Lei; Luo, Ting-Liang; et al., Densities and Viscosities of (1,6-Hexanediamine
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76 Afzal, Waheed; Mohammadi, Amir H.; Richon, Dominique, Volumetric Properties of Mono-, Di-, Tri-, and Polyethylene Glycol Aqueous Solutions from (273.15 to 363.15) K: Experimental Measurements and Correlations, JOURNAL OF CHEMICAL AND ENGINEERING DATA, 54 (2009) 1254-1261.
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77 Zafarani-Moattar MT, Kheyrabi N. in Volumetric, Ultrasonic, and Transport Properties of an Aqueous Solution of Polyethylene Glycol Monomethyl Ether at Different Temperatures, JOURNAL OF CHEMICAL AND ENGINEERING DATA, 55 (2010), pp. 3976-3982.
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78 Liu, J., Zhu, C., Ma, Y. in Densities and viscosities of binary solutions of benzene-1,3-diol + water, ethanol, propan-1-ol, and butan-1-ol at T = (293.15 to 333.15) K, Journal of Chemical and Engineering Data 2011, 56 (5), pp. 2095-2099
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79 Hoga, H.E., Tôrres, R.B., Volumetric and viscometric properties of binary mixtures of {methyl tert-butyl ether (MTBE) + alcohol} at several temperatures and p = 0.1 MPa: Experimental results and application of the ERAS model, Journal of Chemical Thermodynamics 2011, 43 (8), pp. 1104-1134
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80 D.I. Sagdeev, M.G. Fomina, G.Kh. Mukhamedzyanov, I.M. Abdulagatov in Experimental study of the density and viscosity of polyethylene glycols and their mixtures at temperatures from 293 K to 473 K and at atmospheric pressure, The Journal of Chemical
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81 Zhenhua Guo, Jianbin Zhang, Tong Zhang, Chunping Li, Yongfeng Zhang, Jie Bai in Liquid viscosities, excess properties, and viscous flow thermodynamics of triethylene glycol + water mixtures at T = (298.15, 303.15, 308.15, 313.15, and 318.15) K, Journal of Molecular Liquids, 2012, 165, pp. 27-31.
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82 Zafarani-Moattar, M.T., Majdan-Cegincara, R., Effect of temperature on volumetric and transport properties of nanofluids containing ZnO nanoparticles poly(ethylene glycol) and water, Journal of Chemical Thermodynamics, 2012, 54, pp. 55-67.
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83 Zafarani-Moattar, M.T., Majdan-Cegincara, R., Stability, rheological, magnetorheological and volumetric characterizations of polymer based magnetic nanofluids, Colloid and Polymer Science 2013, 291 (8), pp. 1977-1987.
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84 Li, Q., Zhang, J., Li, L., He, Z., Yang, X., Zhang, Y., Guo, Z., Zhang, Q., Solubility properties and spectral investigation of dilute SO2in a triethylene glycol + water + La3+ system. Journal of Physical Chemistry B, 117 (18), (2013) , pp. 5633-5646
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85 Moosavi, M., Motahari, A., Omrani, A., Rostami, A.A. Thermodynamic study on some alkanediol solutions: Measurement and modeling, Thermochimica Acta 561, (2013), 1-13.
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86 Yang, F., Wang, X., Wang, W., Liu, Z. Densities and excess properties of primary amines in alcoholic solutions. Journal of Chemical and Engineering Data 58 (3), (2013), 785-791.
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87 Piazza L., Span R., An equation of state for methanol including the association term of SAFT, Fluid
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90 Faouzia Amireche-Ziar, Ghenima Boukais-Belaribi, Antje Jakob, Ilham Mokbel, Farid Brahim Belaribi, Isothermal vapour–liquid equilibria of binary systems of 1,2-dichloroethane with ethers, Fluid Phase Equilibria 268 (2008) 39–44.
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91 Iloukhani, H., Jafari, M. in Thermodynamic and transport properties for binary and ternary mixtures of 2-methyltetrahydrofuran + chlorobenzene + cyclopentanone at T = 298.15 K, Monatshefte fur Chemie 2011, 142 (10), pp. 1005-1011
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Dana Dragoescu, Mariana Teodorescu and Alexandru Barhala, Isothermal (vapour + liquid) equilibria and excess Gibbs free energies in some binary (cyclopentanone + chloroalkane) mixtures at temperatures from 298.15 K to 318.15 K, The Journal of Chemical Thermodynamics, 39 (2007) 1452-1457. 92 Sprunger-LM, Achi-SS, Acree-
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93 Hossein Iloukhani, Mehdi Fattahi in Correlation of excess molar enthalpies of cyclopentanone (1) + 1-alkanols (C1–C5) (2) by Peng–Robinson–Stryjek–Vera equation of state and ERAS-model, Journal of Molecular Liquids, 2012, 171, pp. 37-42.
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Dana Dragoescu, Alexandru Barhala, Mariana Teodorescu, Vapour pressure and excess Gibbs energy of binary 1, 2-dichloroethane + cyclohexanone, chloroform + cyclopentanone and chloroform + cyclohexanone mixtures at temperatures from 298.15 to 318.15 K, Fluid Phase Equilib. 267 (1) (2008) 70-78. 94 Sprunger-LM, Gibbs-J, Acree-
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Olivia Fandiño, Enriqueta R. López, Luis Lugo, Mariana Teodorescu, Ana M. Mainar, Josefa Fernández, Solubility of carbon dioxide in two pentaerythritol ester oils between 283 and 333 K, Journal of Chemical Engineering and Data 53 (8) (2008) 1854-1861. 95 Pernechele, F., Bobbo, S., Fedele,
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96 Fandiño, O., Lugo, L., Comuñas, M.J.P., López, E.R., Fernández, J. in Temperature and pressure dependences of volumetric properties of two poly(propylene glycol) dimethyl ether lubricants, Journal of Chemical Thermodynamics 2010, 42 (1), pp. 84-89
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100 Fandiño, O., López, E.R., Lugo, L., García, J., Fernández, J. in Solubility of carbon dioxide in pentaerythritol ester oils. New data and modeling using the PC-SAFT model, Journal of Supercritical Fluids 2010, 55 (1), pp. 62-70
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Dragoescu, D., Barhala, A., Teodorescu, M., (Vapour + liquid) equilibria and excess Gibbs free energies of (cyclohexanone + 1-chlorobutane and + 1,1,1-trichloroethane) binary mixtures at temperatures from (298.15 to 318.15) K, Journal of Chemical Thermodynamics 2009, 41 (9), pp. 1025-1029 107 Montaño, D., Gascón, I., Bölts, R.,
Gmehling, J. Lafuente, C., in Isothermal vapour-liquid equilibria and excess enthalpies for the binary mixtures containing an isomeric chlorobutane and diisopropyl ether, Fluid Phase Equilibria 2011, 308 (1-2), pp. 8-14
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Ciocirlan, O., Teodorescu, M., Dragoescu, D., Iulian, O., Barhala, A., Densities and excess molar volumes of the binary mixtures of cyclopentanone with chloroalkanes at T = (288.15, 298.15, 308.15, and 318.15) K, Journal of Chemical and Engineering Data 2010, 55 (9), pp. 3891-3895 108 Bermúdez-Salguero, C., Gracia-
Fadrique, J., Calvo, E., Amigo, A. in Densities, refractive indices, speeds of sound, and surface tensions for dilute aqueous solutions of 2-methyl-1-propanol, cyclopentanone, cyclohexanone, cyclohexanol, and ethyl acetoacetate at 298.15 K, Journal of Chemical and Engineering Data 2011, 56 (10), pp. 3823-3829
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37-42. Ciocirlan, O., Teodorescu, M., Dragoescu, D., Iulian, O., Barhala, A. Densities and excess molar volumes of the binary mixtures of cyclohexanone with chloroalkanes at temperatures between (288.15 and 318.15) K, Journal of Chemical and Engineering Data 55 (2) (2010), 968-973. 110 Tafat-Igoudjilene, O., Daoudi, H.,
Bey-Larouci, A.H., Aitkaci, A. Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure. Thermochimica Acta, 561 (2013), 63-71.
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Dragoescu, D., Barhala, A., Teodorescu, M., Chiscan, D., Isothermal vapour-liquid equilibria in cyclohexanone + dichloroalkane binary mixtures at temperatures from 298.15 to 318.15 K, Journal of the Serbian Chemical Society 2011, 76 (2), pp. 305-315 111 Islam, A.W., Rahman, M.H, in A
review of Barker's activity coefficient method and VLE data reduction, Journal of Chemical Thermodynamics 2012, 44 (1), pp. 31-37.
1.33630
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Referinta bibliografica si pi si / pi
1 Teodorescu M., Barhala A., Marchidan D. I., Landauer O., Vapour pressures and excess Gibbs energy of ethylbenzene - cyclooctane binary mixtures. Fluid Phase Equilibria, 126, 127-134 (1996).
1.63836 1 1.63836
5 Teodorescu M., Linek J., Densities and excess volumes of pentan-3-one + 1,2-dichloroethane, +1,3-dichloropropane, + 1,4-dichlorobutane, + trichloromethane, + 1,1,1-trichloroethane, + 1,1,2,2-tetrachloroethane binary mixtures at 298.15 K. Fluid Phase Equilibria, 146 (1998) 155-160.
1.63836 1 1.63836
6 Teodorescu M., Aim K., Wichterle I., Isothermal vapour-liquid equilibria for pentan-3-one + 1,4-dichlorobutane, + trichloromethane, + 1,1,1-trichloroethane, + 1,1,2,2-tetrachloroethane binary mixtures. Fluid Phase Equilibria, 147 (1998) 215-228.
1.63836 1 1.63836
7 Teodorescu M., Linek J., Wichterle I., Isothermal 1.63836 1 1.63836
22
vapour-liquid equilibria and densities for the 5-chloropentan-2-one + n-hexane, + toluene, + ethylbenzene binary mixtures. Fluid Phase Equilibria, 149 (1998) 127-138.
11 Teodorescu M., Wagner Z., Wichterle I., Application of the predictive UNIFAC model to the pentan-3-one / chloroalkane and 5-chloro-2-pentanone / hydrocarbon binary systems. Chemical Engineering & Technology, 23 (2000) No. 4, 367-370.
1.31447 1 1.31447
12 Teodorescu M., Wichterle I., Evaluation of the carbonyl / chlorine interaction parameters in the pentan-3-one + chloroalkane mixtures using the DISQUAC group contribution model. Collection of Czechoslovak Chemical Communications, 65/10 (2000) 1559-1570.
0.68862 1 0.68862
14 Teodorescu M., Aim K., Wichterle I., Isothermal vapor-liquid equilibrium in the quaternary water + isopropanol + acetic acid + isopropyl acetate system with chemical reaction. Journal of Chemical and Engineering Data, 46/2 (2001) 261-266.
1.53774 1 1.53774
15 Teodorescu M., Rasmussen P., High pressure vapor-liquid equilibria in the systems: nitrogen + dimethyl ether, methanol + dimethyl ether, carbon dioxide + dimethyl ether + methanol and nitrogen + dimethyl ether + methanol. Journal of Chemical and Engineering Data, 46/3 (2001) 640-646.
1.53774 1 1.53774
19 Teodorescu M., Wilken M., Wittig R., Gmehling J., Azeotropic and solid-liquid equilibria data for several binary organic systems containing one acetal compound, Fluid Phase Equilibria 204 (2003) 267-280.
1.63836 1 1.63836
20 Teodorescu M., Wichterle I., Modeling of the Nitrogen and Carbon Dioxide Solubility in Alternative Fuels at High Pressures Using Soave–Redlich–Kwong Equation of State, Chem. Eng. & Technology, 26/9 (2003) 992-995.
1.31447 1 1.31447
21 Teodorescu M., Lugo L., Fernandez J., Modeling of gas solubility data for HFCs – lubricant oil binary systems by means of the SRK equation of state, International Journal of Thermophysics, 24/4 (2003) 1043-1060.
0.68597 1 0.68597
22 Teodorescu M., Krummen M., Gmehling J., Excess Molar Enthalpies for the Binary Systems of Benzene or Cyclohexane with 1,1-Diethoxyethane at 323.15 K or with 2,2-Dimethoxybutane at 303.15 K and Infinite Dilution Activity Coefficients in 1,1-Diethoxyethane, Journal of Chemical and Engineering Data, 48 (2003) 435-439.
1.53774 1 1.53774
26 Teodorescu M., Barhala A., Dragoescu D., Isothermal (vapour-liquid) equilibria for the binary (cyclopentanone or cyclohexanone with 1,1,2,2-tetrachloroethane) systems at temperatures of
1.33630 1 1.33630
23
(343.15, 353.15 and 363.15) K, The Journal of Chemical Thermodynamics, 38/11 (2006) 1432-1437.
27 Mariana Teodorescu, Alexandru Barhala, Dana Dragoescu, Isothermal vapour–liquid equilibria for 1,2-dichloroethane + nitromethane and + nitroethane binary systems at temperatures between 333.15 and 353.15 K, Fluid Phase Equilibria, 292 (2010) 58–63.
1.63836 1 1.63836
29 Mariana Teodorescu, Alexandru Barhala, Dana Dragoescu, Daniela Gheorghe, Isothermal Vapor_Liquid Equilibria for Nitromethane and Nitroethane + 1,3-Dichloropropane Binary Systems at Temperatures between (343.15 and 363.15) K, Journal of Chemical and Engineering Data, 56 (2011), 4665–4671.
1.53774 1 1.53774
30 Mariana Teodorescu, Dana Dragoescu, Daniela Gheorghe, Isothermal (vapour + liquid) equilibria for (nitromethane or nitroethane + 1,4-dichlorobutane) binary systems at temperatures between (343.15 and 363.15) K, The Journal of Chemical thermodynamics, 56 (2013) 32-37.
1.33630 1 1.33630
31 Gheorghe D., Dragoescu D., Teodorescu M., Volumetric study for the binary nitromethane with chloroalkanes mixtures at Temperatures in the Range (298.15 - 318.15) K, Journal of Chemical and Engineering Data, 58 (2013) 1161-1167.
1.53774 3 0.51258
33 Teodorescu M., Secuianu C., Refractive Indexes and Their Deviations Measurement and Correlation for Selected Binary Systems of Various Polarities at 25 0C, Journal of Solution Chemistry, 42(10) (2013) 1912-1934.
0.52129 1 0.52129
34 Teodorescu M., Marongiu B., Maxia S., Piras A., Usula M., Porcedda S., Calorimetric study of the selected nitroalkane + chloroalkane binary systems. Comparison with DISQUAC predictions, Journal of Thermal Analysis and Calorimetry, in press (DOI 10.1007/s10973-013-3408-5).
0.54829 1 0.54829
Total:
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