Jf. Demmink et Aacm. Beenackers, GAS DESULFURIZATION WITH FERRIC CHELATES OF EDTA AND HEDTA - NEW MODEL FOR THE OXIDATIVE ABSORPTION OF HYDROGEN-SULFIDE, Industrial & engineering chemistry research, 37(4), 1998, pp. 1444-1453
The experimental data of Wubs and Beenackers (AIChE J. 1994, 40 (3), 4
33-444) on the oxidative absorption of H2S into aqueous solutions of f
erric chelates of ethylenediaminetetraacetic acid (EDTA) and hydroxyet
hylethylenediaminetriacetic acid (HEDTA) were reinterpreted using a ne
w penetration model for mass transfer parallel to chemical reaction. D
ifferent from the discussion by Wubs and Beenackers (1994), which was
based on general, approximate models for the reactive absorption of ga
ses into liquids, it now appears that the diffusivity of ferric chelat
es of EDTA and HEDTA are in good agreement with the values determined
from the reactive absorption of molecular oxygen into aqueous solution
s of ferrous EDTA and HEDTA (Wubs and Beenackers, Ind. Eng. Chem. Res.
1993, 32, 2580-2594). Also, it now appears that the data from Wubs and
Beenackers (1994) are compatible with ferric chelate complex equilibr
ium constants, reported elsewhere (for instance, Martell and Smith, Cr
itical Stability Constants, 1982). Reinterpretation of the absorption
data from Wubs and Beenackers (1994) resulted in the following kinetic
rate constants (T = 293 K, C-Fe(III) = 78 mol/m(3) and 2 less than or
equal to pH less than or equal to 9): EDTA, monohydroxylated complex,
250 less than or equal to k(1,1) less than or equal to 300 m(3)/(mol
s); HEDTA, monohydroxylated complex, 1.4 less than or equal to k(1,1)
less than or equal to 1.6 m(3)/(mol s); HEDTA, dihydroxylated complex,
550 less than or equal to k(1,1) less than or equal to 650 m(3)/(mol
s); for the reaction rate expressed by -R-H2S = k(1,1)C(H2S)C(Fe(III))
.