Zobrazeno 1 - 7
of 7
pro vyhledávání: '"Ruiqi Qiao"'
Autor:
Rongxing Ma, Xiaokang Gao, Yangyang Jin, Xiaolong Wang, Ruifeng Li, Ruiqi Qiao, Xinliang Wang, Dayong Liu, Zhitao Xie, Limin Wang, Jingyu Zhang, Weiguo Xu, Yongcheng Hu
Publikováno v:
Frontiers in Medicine, Vol 11 (2024)
BackgroundDecellularized allograft tendons are highly regarded for their accessibility and the reduced risk of immune rejection, making them a promising choice for grafting due to their favorable characteristics. However, effectively integrating reco
Externí odkaz:
https://doaj.org/article/5a3c358a5ebb4f19b3874daa5c1386a9
Publikováno v:
Fluid Phase Equilibria. 472:212-217
Isobaric vapor - liquid equilibrium (VLE) data for the binary system of ethanol + dimethyl carbonate (DMC) and the ternary systems of ethanol + DMC + 1-hexyl-3-methylimidazolium bis[(trifluoromethyl) sulfonyl] imide ([HMIM][NTf2]) and ethanol + DMC +
Publikováno v:
Fluid Phase Equilibria. 466:14-18
A modified Othmer still was used to measure the vapor–liquid equilibrium data for the ternary system chloroform + methanol + 1,3-dimethylimidazolium dimethylphosphate ([MMIM]+[DMP]−) at 101.3 kPa. The measured data were correlated with the NRTL m
Publikováno v:
Fluid Phase Equilibria. 466:1-6
Publikováno v:
Journal of Molecular Liquids. 243:699-705
Isobaric vapor-liquid equilibrium data for the ternary systems of dichloromethane (DCM) + methanol + ionic liquids (ILs) were measured at a constant pressure of 101.3 kPa using a modified Othmer and they were also amended and correlated using the NRT
Autor:
Yudong Liu, Chunjiang Li, Xiaolin Song, Qunsheng Li, Hongjian Tang, Kun Zhang, Ruiqi Qiao, Zhuo Li
Publikováno v:
Fluid Phase Equilibria. 427:90-96
Isobaric vapor-liquid equilibrium data for the ternary systems of methanol + methyl ethyl ketone (MEK) + 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ([BMIM][NTf 2 ]) and methanol + MEK + 1-hexyl-3-methylimidazolium bis(trifluorometh
Publikováno v:
Separation and Purification Technology. 238:116487
The separation of acetonitrile-water mixtures is a challenging and significant task due to the presence of azeotrope, for which three separation alternatives are proposed, including an energy-efficient extractive distillation strategy (ED), an pressu