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).

1.63836 4 0.40959

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.

1.63836 3 0.54612

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.

1.31447 3 0.43816

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,

1.63836 4 0.40959

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.

1.31447 2 0.65724

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.

1.33630 3 0.44543

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.

1.63836 3 0.54612

18 Mariana Teodorescu, Alexandru Barhala, Dana Dragoescu, Daniela Gheorghe, Isothermal Vapor_Liquid Equilibria for Nitromethane and Nitroethane + 1,3-Dichloropropane Binary Systems at

1.53774 4 0.38444

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.

1.33630 3 0.44543

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.

1.63836 3 0.54612

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.

1.53774 3 0.51258

Total

SN

i i

i

ns

1

10.69103

Ns=21 50910021

691031011

..ns

N,NmaxS

sN

i i

i

refsmed

2.Verificarea indeplinirii standardului Cmed ≥ 5; criteriu indeplinit: Cmed = 5.55 Numarul publicatiei care citeaza

Referinta bibliografica a publicatiei k care citeaza

sk

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,

Extension of the PPR78 model (predictive 1978, Peng-Robinson EOS with temperature-dependent kij calculated through a group-contribution method) to systems containing naphtenic compounds, Fluid Phase Equilibria 243/1-2 (2006) 9-28.

1.63836

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

Studies of viscosities and excess molar volumes of the binary mixtures of 1-heptanol + 1,2-dichloroethane, + 1,1,1-

1.53774

4

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.

2.38623

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.

1.33630

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

0.69237

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

1.20665

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

R. in “Isothermal vapor-liquid equilibrium data for the binary propane-2-one plus chloroalkanes mixtures at temperatures from 298.15 K to 313.15 K”, Fluid Phase Equilibria 157/1 (1999) 41-51.

1.63836

5

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.

1.63836

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.

1.63836

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.

1.63836

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.

1.63836

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.

1.63836

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.

1.53774

14 Bernatová, S., Aim, K., Wichterle, I., in Isothermal vapour-liquid equilibrium with chemical reaction in the quaternary water + methanol + acetic acid + methyl acetate

1.63836

6

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.

1.53774

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.

1.63836

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-

MH, Livingstone-DJ, Application of QSPR to mixtures, Journal of Chemical Information and Modeling, 46/5 (2006) 2043-2055.

2.38623

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. 18 Sanz M. T., Calvo B., Beltran S.,

Cabezas J. L., in “Vapor-liquid equilibria at (33.33, 66.66, and 101.33) kPa and densities at 298.15 K for the system methanol plus methyl lactate”, J. Chem. Eng. Data 47/4 (2002) 1003-1006.

1.53774

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.

1.53774

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.

1.53774

21 Toikka, A., Toikka, M., in Phase transitions and azeotropic properties of acetic acid-n-

1.63836

7

propanol-water-n-propyl acetate system, Fluid Phase Equilibria 250 (1-2) (2006), pp. 93-98.

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.

1.63836

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.

0.70755

24 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.

1.53774

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,

1.63836

26 Toikka, A., Toikka, M. in Solubility and critical phenomena in reactive liquid-liquid systems, Pure and Applied Chemistry 2009, 81 (9), pp. 1591-1602

2.35329

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.

1.53774

28 de Jong MC, Zondervan E, Dimian AC, et al, Entrainer selection for the synthesis of fatty acid esters by Entrainer-based Reactive Distillation, CHEMICAL ENGINEERING RESEARCH &

1.51887

8

DESIGN, 2010, 88(1A), 34-44. 29 Jan Pavlíček, Grozdana Bogdanić,

Ivan Wichterle in Vapour–liquid and chemical equilibria in the ethyl ethanoate + ethanol + propyl ethanoate + propanol system accompanied with transesterification reaction, Fluid Phase Equilibria, 2012, 328, pp. 61-68.

1.63836

30 Toikka, M., Toikka, A. Peculiarities of phase diagrams of reactive liquid-liquid systems. Pure and Applied Chemistry 85 (1) (2013), 277-288.

2.35329

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. 31 Laursen T., Rasmussen P.,

Andersen S. J., in “VLE and VLLE measurements of dimethyl ether containing systems”, J. Chem. Eng. Data 47/2 (2002) 198-202.

1.53774

32 Garcia Sancez F., Eliosa Jimenes G., Silva Oliver G., Vazquez Roman R., in “Vapor-liquid equilibria of nitrogen hydrocarbon systems using PC-SAFT equation of state”, Fluid Phase Equilibria 217/2 (2004) 241-253.

1.63836

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.

1.63836

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.

1.63836

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.

1.63836

36 Liang X., Tan H., Fu Z., Chou 2.30968

9

S.Y., Air bubble formation and dissolution in dispensing nanoimprint lithography, Nanotechnology 18/2 (2007), art. no. 025303.

37 Wu-JT, Yin-JG, Vapor-pressure measurements of dimethyl ether from (213 to 393) K, Journal of Chemical and Engineering Data 53 (2008) 2247-2249.

1.53774

38 Dirk-Faitakis, C.B., An, W., Lin, T.-B., Chuang, K.T. in Catalytic distillation for simultaneous hydrolysis of methyl acetate and etherification of methanol, Chemical Engineering and Processing: Process Intensification 2009, 48 (5), pp. 1080-1087

1.73899

39 Ralf Dohrn, Stephanie Peper, José M.S. Fonseca, High-pressure fluid-phase equilibria: Experimental methods and systems investigated (2000–2004), Fluid Phase Equilibria 288 (2010) 1–54.

1.63836

40 Wu, J., Zhou, Y., Lemmon, E.W. in An Equation of State for the Thermodynamic Properties of Dimethyl Ether, Journal of Physical and Chemical Reference Data 2011, 40 (2), art. no. 023104

5.90419

41 Kongmeng Ye, Hannsjörg Freund, Kai Sundmacher in Modelling (vapour + liquid) and (vapour + liquid + liquid) equilibria of {water (H2O) + methanol (MeOH) + dimethyl ether (DME) + carbon dioxide (CO2)} quaternary system using the Peng–Robinson EoS with Wong–Sandler mixing rule, The Journal of Chemical Thermodynamics, 2011, 43, pp. 2002-2014.

1.33630

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.

0.50314

43 Anton A. Kiss, David J.-P. C. Suszwalak in Innovative dimethyl

1.87736

10

ether synthesis in a reactive dividing-wall column, Computers & Chemical Engineering, 2012, 38, pp. 74-81.

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.

0.50314

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.

1.31447

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. 46 Di Nicola, G., Giuliani, G.,

Polonara, F., Stryjek, R., in Solid-liquid equilibria for the CO2 + R125 and N2O + R125 systems: A new apparatus, Journal of Chemical and Engineering Data 51 (6) (2006), pp. 2209-2214.

1.53774

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.

1.91195

48 Caco-AI, Varanda-F, deMelo-MJP, Dias-AMA, Dohrn-R, Marrucho-IM, Solubility of antibiotics in different solvents. Part II. Non-hydrochloride forms of tetracycline and ciprofloxacin, Industrial & Engineering Chemistry Research, 47/21 (2008) 8083-8089

1.91195

49 Gomes, P.B., Mata, V.G., Rodrigues, A.E. in Experimental validation of perfumery ternary diagram® methodology, , AIChE Journal 2008, 54 (1), pp. 310-320

2.22327

50 Acree, W., Chickos, J.S. in Phase 5.90419

11

Transition Enthalpy Measurements of Organic and Organometallic Compounds. Sublimation, Vaporization and Fusion Enthalpies From 1880 to 2010, Journal of Physical and Chemical Reference Data 2010, 39 (4), art. no. 043101

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.

1.53774

52 Cuevas, J., Llovell, F., Galindo, A., Vesovic, V., Segura, H., Pérez-Correa, J.R. in Solid-liquid equilibrium using the SAFT-VR equation of state: Solubility of naphthalene and acetic acid in binary mixtures and calculation of phase diagrams, Fluid Phase Equilibria 2011, 306 (1), pp. 137-147

1.63836

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. 53 Quinones Cisneros-SE, Garcia-J,

Fernandez-J, Monsalvo-MA, Phase and viscosity behavior of refrigerant-lubricant mixtures, International Journal of Refrigeration -Revue Internationale du Froid 28/5 (2005) 714-724.

1.75417

54 Fandino-O, Garcia-J, Comunas-MJP, Lopez-ER, Fernandez-J, P-rho-T measurements and equation-of-state (eos) predictions of ester lubricants up to 45 MPa, Industrial and Engineering Chemistry Research 45/3 (2006) 1172-1182.

1.91195

55 Marchi, P., Scalabrin, G., Ihmels, E.C., Richon, D., A fundamental equation of state for the (R134a + triethylene glycol dimethyl ether) mixture, AIChE Journal 53/5 (2007) 1349-1361.

2.22327

56 Lugo-L, Comunas-MJP, Lopez-ER, Fernandez-J, Volumetric

0.54829

12

properties of 1-iodoperfluorohexane plus n-octane binary system at several temperatures - experimental data and eos prediction, Journal of Thermal Analysis and Calorimetry 87/1 (2007) 179-187.

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.

1.63836

58 Youbi-Idrissi, M., Bonjour, J., The effect of oil in refrigeration: Current research issues and critical review of thermodynamic aspects, International Journal of Refrigeration 2008, 31 (2), pp. 165-179

1.75417

59 Segovia-JJ, Fandino-O, Lopez-ER, Lugo-L, Martin-MC, Fernandez-J, Automated densimetric system measurements and uncertainties for compressed fluids, Journal of Chemical Thermodynamics, 41 (2009) 632-638.

1.33630

60 Ren, W., Scurto, A.M. in Phase equilibria of imidazolium ionic liquids and the refrigerant gas, 1,1,1,2-tetrafluoroethane (R-134a), Fluid Phase Equilibria 2009, 286 (1), pp. 1-7

1.63836

61 Ren W, Sensenich B, Scurto AM, High-pressure phase equilibria of {carbon dioxide (CO2) + n-alkyl-imidazolium bis(trifluoromethylsulfonyl)amide} ionic liquids, JOURNAL OF CHEMICAL THERMODYNAMICS, 2010, 42, 305-311

1.33630

62 Polishuk, I., Generalization of SAFT + Cubic equation of state for predicting and correlating thermodynamic properties of heavy organic substances, Journal of Supercritical Fluids, 2012, 67, pp. 94-107.

2.16667

13

63 Freitas, A.C.D., Cunico, L.P., Aznar, M., Guirardello, R. Modeling vapor liquid equilibrium of ionic liquids + gas binary systems at high pressure with cubic equations of state. Brazilian Journal of Chemical Engineering 30 (1), (2013), 63-73.

0.70755

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. 64 Valtz, A., Coquelet, C., Richon,

D., in Volumetric properties of the monoethanolamine-methanol mixture at atmospheric pressure from 283.15 to 353.15 K, Thermochimica Acta 428 (1-2) (2005), pp. 185-191.

1.20665

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.

1.20665

66 Zafarani-Moattar, M.T., Tohidifar, N., in Vapor-liquid equilibria, density, and speed of sound for the system poly(ethylene glycol) 400 + methanol at different temperatures, Journal of Chemical and Engineering Data 51 (5) (2006) , pp. 1769-1774.

1.53774

67 Valtz, A., Coquelet, C., Nikitine, C., Richon, D., in Volumetric properties of the water + ethylenediamine mixture at atmospheric pressure from 288.15 to 353.15 K, Thermochimica Acta 443 (2) (2006), pp. 251-255.

1.20665

68 Hsieh, Chi-Jui; Chen, Ji-Miao; Li, Meng-Hui, Dielectric constants of aqueous diisopropanolamine, diethanolamine, N-methyldiethanolamine, triethanolamine, and 2-amino-2-methyl-1-propanol solutions, JOURNAL OF CHEMICAL AND ENGINEERING DATA, 52 (2007) 619-623.

1.53774

14

69 Montanes, Fernando; Olano, Agustin; Ibanez, Elena; et al., Modeling solubilities of sugars in alcohols based on original experimental data, AIChE J, 53 (2007) 2411-2418.

2.22327

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.

1.53774

71 Zafarani-Moattar, Mohammed Taghi; Tohidifar, Nastaran, Vapor-liquid equilibria, density, speed of sound, and viscosity for the system poly(ethylene glycol) 400+ethanol at different temperatures, JOURNAL OF CHEMICAL AND ENGINEERING DATA, 53 (2008) 785-793.

1.53774

72 I.M. Abdulagatov, J.T. Safarov, F.Sh. Aliyev, M.A. Talibov, A.N. Shahverdiyev, E.P. Hassel, Experimental densities and derived thermodynamic properties of liquid propan-1-ol at temperatures from 298 to 423K and at pressures up to 40MPa, Fluid Phase Equilibria 268 (2008) 21–33.

1.63836

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

0.52129

74 Gat, S., Brauner, N., Ullmann, A. in Heat transfer enhancement via liquid-liquid phase separation, International Journal of Heat and Mass Transfer 2009, 52 (5-6), pp. 1385-1399

2.26707

75 Wang, Ying; Lian, Hong-Lei; Luo, Ting-Liang; et al., Densities and Viscosities of (1,6-Hexanediamine

1.53774

15

plus Ethanol) and (1,6-Hexanediamine plus Ethanol plus Water) Mixtures at T = (303.15 to 328.15) K, JOURNAL OF CHEMICAL AND ENGINEERING DATA, 54 (2009) 1158-1162.

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.

1.53774

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.

1.53774

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

1.53774

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

1.33630

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

1.33630

16

Thermodynamics, 2011, 43, pp. 1824-1843.

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.

0.69237

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.

1.33630

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.

1.46282

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

1.95448

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.

1.20665

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.

1.53774

87 Piazza L., Span R., An equation of state for methanol including the association term of SAFT, Fluid

1.63836

17

Phase Equilibria 2013, 349, 12-24. 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. 88 Acree, W., Chickos, J.S. Phase

Transition Enthalpy Measurements of Organic and Organometallic Compounds. Sublimation, Vaporization and Fusion Enthalpies From 1880 to 2010 K Journal of Physical and Chemical Reference Data 39 (4), art. no. 043101 (2010)

5.90419

Barhala A., Dragoescu D., Teodorescu M., Wichterle I, Isothermal (vapour + liquid) equilibria in the binary mixtures (1,2-dichloroethane and 1,1,1-trichloroethane with cyclopentanone) within the temperature range (298.15 to 313.15) K, The Journal of Chemical Thermodynamics, 38/5 (2006) 617-623. 89 Sprunger-LM, Gibbs-J, Acree-

WE, Abraham-MH, Correlation and prediction of partition-coefficients for solute transfer to 1,2-dichloroethane from both water and from the gas-phase, Fluid Phase Equilibria 273 (2008) 78-86.

1.63836

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.

1.63836

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

0.91317

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-

WE, Abraham-MH, Leo-AJ, Hoekman-D, Correlation and prediction of solute transfer to chloroalkanes from both water and

1.63836

18

the gas-phase, Fluid Phase Equilibria, 281 (2009) 144-162.

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.

0.69237

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-

WE, Abraham-MH, Correlation and prediction of partition-coefficients for solute transfer to 1,2-dichloroethane from both water and from the gas-phase, Fluid Phase Equilibria 273 (2008) 78-86.

1.63836

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,

L., Stryjek, R. in Solubility of carbon dioxide in pentaerythritol tetrabutyrate (PEC4) and comparison with other linear chained pentaerythritol tetraalkyl esters, International Journal of Thermophysics 2009, 30 (4), pp. 1144-1154

0.68597

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

1.33630

97 Bobbo, S., Fedele, L., Pernechele, F., Scattolini, M., Stryjek, R. in Solubility measurements and correlation of carbon dioxide in pentaerythritol tetra-2-methylhexanoate. Comparison with other pentaerythritol esters, Fluid Phase Equilibria 2010, 290 (1-2), pp. 115-120

1.63836

19

98 Fandiño, O., López, E.R., Lugo, L., Fernández, J. in Compressed liquid densities of two dipentaerythritol esters, Fluid Phase Equilibria 2010, 296 (1), pp. 30-36

1.63836

99 Paredes, X., Pensado, A.S., Comuñas, M.J.P., Fernández, J. in Experimental dynamic viscosities of dipentaerythritol ester lubricants at high pressure, Journal of Chemical and Engineering Data 2010, 55 (9), pp. 3216-3223

1.53774

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

2.16667

101 Fandiño, O., López, E.R., Lugo, L., Fernández, J. in Solubilities of carbon dioxide in a dipentaerythritol ester and in a polyether, Journal of Chemical and Engineering Data 2010, 55 (12), pp. 5483-5488

1.53774

102 Fonseca, J.M.S., Dohrn, R., Peper, S. in High-pressure fluid-phase equilibria: Experimental methods and systems investigated (2005-2008), Fluid Phase Equilibria 2011, 300 (1-2), pp. 1-69

1.63836

103 García, J., Abou Naccoul, R., Fernández, J., Razzouk, A., Mokbel, I. in Vapor-pressure measurements and modeling of dipentaerythritol ester lubricants, Industrial and Engineering Chemistry Research 2011, 50 (8), pp. 4231-4237

1.91195

104 Fandiño, O., Lugo, L., Segovia, J.J., López, E.R., Comuñas, M.J.P., Fernández, J. in High pressure densities of carbon dioxide + dipentaerythritol hexaheptanoate: New experimental setup and volumetric behavior, Journal of Supercritical Fluids 2011, 58 (2), pp. 189-197.

2.16667

105 Regueira, T., Fandiño, O., Lugo, L., López, E.R., Fernández, J., in

2.16667

20

Carbon dioxide solubility in reference and vegetable lubricants developed for two stroke engines, Journal of Supercritical Fluids, 2012, 68, pp. 123 - 130

106 Almantariotis, D., Fandiño, O., Coxam, J.-Y., Costa Gomes, M.F., Direct measurement of the heat of solution and solubility of carbon dioxide in 1-hexyl-3-methylimidazolium bis[trifluoromethylsulfonyl]amide and 1-octyl-3-methylimidazolium bis[trifluoromethylsulfonyl]amide, International Journal of Greenhouse Gas Control, 2012, 10, pp. 329-340.

2.46247

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

1.63836

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

1.53774

109 Zhao, Xiaolei; Zhang, Yuejun, Bacteria-removing and Bactericidal Efficiencies of PDADMAC Composite Coagulants in Enhanced Coagulation Treatment, CLEAN-SOIL AIR WATER, 2013, 41(1),

0.77223

21

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.

1.20665

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

NC = 18 (numarul lucrarilor

proprii citate scrise cu

bold)

5552018

111 .,max

Cmed

3.Verificarea indeplinirii standardului P ≥ 12; criteriu indeplinit P = 24.23941. Numarul publicatiei

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:

i

i

ps

P = 24.23941