2016
DOI: 10.1016/j.jct.2015.12.030
|View full text |Cite
|
Sign up to set email alerts
|

Volumetric and transport properties of binary liquid mixtures of sulfolane with aniline, N,N-dimethylaniline and N,N-diethylaniline at different temperatures and atmospheric pressure

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1

Citation Types

0
3
0

Year Published

2016
2016
2024
2024

Publication Types

Select...
6

Relationship

0
6

Authors

Journals

citations
Cited by 17 publications
(3 citation statements)
references
References 19 publications
0
3
0
Order By: Relevance
“…This event causes more holes with appropriate sizes to be created for more and better placement of the components of the mixture and thus; V E m ; decreases. So, these results show that packing [46] 0.67430 0.669 [50] 298.15 0.86235 0.86433 [47] 0.62345 0.6299 [47] 0.8625 [48] 303.15 0.85932 0.86454 [49] 0.59754 0.5981 [47] 0.85995 [47] 0.5976 [49] 308.15 0.85341 0.85361 [14] 0.55840 0.558 [14] 313.15 0.85108 0.85114 [47] 0.53660 0.537 [47] 0.85976 [49] 0.5369 [49] Aniline 293.15 1.02186 1.0217 [51] 4.40530 4.407 [51] 1.021747 [52] 4.404 [52] 298.15 1.01757 1.0174 [51] 3.69330 3.737 [51] 1.017404 [52] 3.773 [52] 303.15 1.01323 1.0130 [51] 3.17430 3.197 [51] 1.013152 [52] 3.190 [52] 308.15 1.00889 1.0087 [53] 2.77950 2.800 [53] 1.0088 [54] 313.15 1.00454 1.0044 [53] 2.42160 2.420 [53] 1.0045 [54] 2.400 [54] Standard uncertainties, u, are: uðTÞ ¼ 0:01K; uðPÞ ¼ 0:01kPa, and the expanded uncertainties, U c in densities, U c ð1Þ ¼ �1:2kg � m À 3 and in viscosities, U c ðhÞ ¼ 3 � 10 À 2 (0.95 level of confidence). Table 3.…”
Section: Densitiesmentioning
confidence: 99%
“…This event causes more holes with appropriate sizes to be created for more and better placement of the components of the mixture and thus; V E m ; decreases. So, these results show that packing [46] 0.67430 0.669 [50] 298.15 0.86235 0.86433 [47] 0.62345 0.6299 [47] 0.8625 [48] 303.15 0.85932 0.86454 [49] 0.59754 0.5981 [47] 0.85995 [47] 0.5976 [49] 308.15 0.85341 0.85361 [14] 0.55840 0.558 [14] 313.15 0.85108 0.85114 [47] 0.53660 0.537 [47] 0.85976 [49] 0.5369 [49] Aniline 293.15 1.02186 1.0217 [51] 4.40530 4.407 [51] 1.021747 [52] 4.404 [52] 298.15 1.01757 1.0174 [51] 3.69330 3.737 [51] 1.017404 [52] 3.773 [52] 303.15 1.01323 1.0130 [51] 3.17430 3.197 [51] 1.013152 [52] 3.190 [52] 308.15 1.00889 1.0087 [53] 2.77950 2.800 [53] 1.0088 [54] 313.15 1.00454 1.0044 [53] 2.42160 2.420 [53] 1.0045 [54] 2.400 [54] Standard uncertainties, u, are: uðTÞ ¼ 0:01K; uðPÞ ¼ 0:01kPa, and the expanded uncertainties, U c in densities, U c ð1Þ ¼ �1:2kg � m À 3 and in viscosities, U c ðhÞ ¼ 3 � 10 À 2 (0.95 level of confidence). Table 3.…”
Section: Densitiesmentioning
confidence: 99%
“…[1][2][3][4][5] The knowledge and understanding thermodynamic and transport properties comprising liquid mixtures has been used to resolve numerous challenges encountered in industrial processes, this also includes heat and mass transfer, fluid flow, and energy transformations. [6][7][8][9] The study of intermolecular interactions is one of the most interesting areas, and therefore, the application of experimental data and theoretical models are used to investigate the behavior of liquid mixtures. This work represents several transport and thermophysical properties of binary mixtures comprising (2-Benzylaminoethanol + Methanol, Ethanol, 1-Propanol, or 2-Propanol) at different temperatures as to investigate the nature and extent of intermolecular interactions occurring between the binary systems.…”
Section: Introductionmentioning
confidence: 99%
“…The collected thermophysical data can be employed in the optimization and design of a desulfurization/CO 2 -capture process utilizing the studied solutions. Furthermore, this data can also be utilized for the theoretical model extension as well as in solving many difficult engineering problems such as fluid flow, heat and mass transfer, and energy transformations. …”
Section: Introductionmentioning
confidence: 99%