The standard description of HF acidizing chemistry clearly demonstrates pri
mary and secondary reaction of HF with alumino-silicates.(1-6) Field experi
ence has taught our industry that possible precipitation during the seconda
ry reaction can adversely affect treatment success,(7,8) especially in form
ations with high K-feldspar content(9) or temperatures above 300 degreesF.
Recent work has also been reported on the existence of a third, or tertiary
reaction of HF with alumino-silicates.(10)
In this paper determination of the rate law and kinetics for the primary re
action of HF on sand, clay, and feldspar over a broad temperature range is
reported. The rate law for the primary reaction of HF with sand had no HCl
dependence and was second order in HF concentration. The rate law for the p
rimary reaction of HF with clay and feldspar was assumed to also have no HC
l dependence and was adequately described by a first order in HF concentrat
ion. In addition, a mass transfer equation for reactive fluids flowing thro
ugh porous sandstone media is proposed. These findings were made possible b
y recently applied experimental techniques including F-19 nuclear magnetic
resonance (NMR) (10) fractional pore-volume flow experiments,(11) and an sp
ectroscopy, accurate knowledge of the HF stoichiometry.(12) Laboratory find
ings have been verified through detailed analyses of flowback samples from
field treatments.(13)