𝔖 Bobbio Scriptorium
✦   LIBER   ✦

The absorption of CO2 by amine-potash solutions

✍ Scribed by S.S. Laddha; P.V. Dancwerts


Publisher
Elsevier Science
Year
1982
Tongue
English
Weight
236 KB
Volume
37
Category
Article
ISSN
0009-2509

No coin nor oath required. For personal study only.

✦ Synopsis


CO, has been absorbed in a stirred vessel into aqueous solutions of MEA and DEA containing K&O,, KZSOI and Na2S04 at 25" and 11Β°C. While electrolytes in general appear to increase the rate of reaction between CO2 and both MEA and DEA, K*CO, increases the rate of reaction of DEA much more than that of MEA. The addition of K2C03 to solutions of DEA increases the absorption rate, in spite of the decrease in the solubility and diffusivity of CO,. The observations help to explain why DEA is an effective promoter for the absorption and desorption of CO2 by hot. concentrated potash solutions.


πŸ“œ SIMILAR VOLUMES


Desorption of CO2by steam bubbles from a
✍ V.V. Mahajani; P.V. Danckwerts πŸ“‚ Article πŸ“… 1983 πŸ› Elsevier Science 🌐 English βš– 55 KB

## Desorption of CO2 by steam bubbles from amine-prnated potash solutions We have recently described (1) some experiments in which the rate of dasorprion of CO2 per unit eree of interface was measured, using potash solutions with end without the addition of small amounts of alkanolemines. The pres

CO2 absorption in aqueous solutions of h
✍ A.K. Chakraborty; G. Astarita; K.B. Bischoff πŸ“‚ Article πŸ“… 1986 πŸ› Elsevier Science 🌐 English βš– 497 KB

Sterically hindered amines constitute a new class of chemicals which have recently come into industrial use in a variety of gas-treating processes: chemical solvents in both aqueous and nonaqueous solutions. rate promotion additives for the hot carbonate process, and chemical solvents for the select

Absorption of CO2 by NH3 solutions
✍ G.B. De Lancey; K.O. Wu πŸ“‚ Article πŸ“… 1979 πŸ› Elsevier Science 🌐 English βš– 310 KB
CO2 absorption into amine solutions: a n
✍ Srinivas Komati; Akkihebbal K Suresh πŸ“‚ Article πŸ“… 2008 πŸ› Wiley (John Wiley & Sons) 🌐 English βš– 135 KB

## Abstract BACKGROUND: In this paper a novel approach for increasing the mass transfer coefficient in gas/liquid mass transfer is reported and applied to the industrially important system of CO~2~ absorption. The approach makes use of a ferrofluid additive to the liquid phase. To demonstrate this