Feasibility of Na-based thermochemical cycles for the capture of CO2 from air—Thermodynamic and thermogravimetric analyses

https://pure.rug.nl/ws/files/14527911/2001ChemEngSciCents.pdf

Gas absorption in an agitated gas-liquid-liquid system

Interfacial area and volumetric mass transfer coefficient in a bubble reactor at elevated pressures

https://pure.rug.nl/ws/files/14491513/2005_Chem.-Eng.-Sci._Cents-A.H.G.pdf

Validation of the Danckwerts-plot technique by simultaneous chemical absorption of CO2 and physical desorption of O2

The kinematic viscosities of aqueous solutions of NaH2PO4, Na2HPO4, Na3PO4, KH2PO4, K2HPO4, and K3PO4, and of their pH-buffering ternary systems, were measured at various concentrations and at temperatures between 293.1 K and 323.1 K. Those of the single-solute solutions were correlated with concentration and temperature, and those of the ternary system with temperature, with deviations less than 1.2% and 0.5%, respectively.

Viscosity of Binary and Ternary Aqueous Systems of NaH2PO4, Na2HPO4, Na3PO4, KH2PO4, K2HPO4, and K3PO4

Validation of the gas-lift bubble column, a new laboratory device, has been achieved by studying the chemical absorption of carbon dioxide into carbonate/bicarbonate solutions. This reaction has been conducted over a range of temperatures extending from 293.2 K to 343.2 K, and using the hypochlorite ion as a catalyst, with corresponding NaClO molarities ranging from zero to 0.2 M. The Danckwerts model was used.The surface renewal rate s , the liquid-side mass-transfer coefficient k L and the rate constant K 2 wer determined. During the hydrodynamic study, the gas-liquid exchange area was evaluated by a photographic method.

Validation of the gas-lift capillary bubble column as a simulation device for a reactor by the study of CO2 absorption in Na2CO3/NaHCO3 solutions

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Validation of the gas-lift capillary bubble column as a simulation device for a reactor by the study of CO2 absorption in Na2CO3/NaHCO3 solutions