TY - JOUR
T1 - Simple mechanistic models for inhibition of a dissolution reaction
AU - Ganor, Jiwchar
AU - Lasaga, Antonio C.
N1 - Funding Information:
This research was supported by grant No. 94-00089 from the United States-Israel Binational Science Foundation (BSF), Jerusalem, Israel. The initiation of this study was motivated by many discussions with E. H. Oelkers and J. Schott during the last few years and by the experimental studies of them and their group at Toulouse. We wish to express our gratitude to J. M. Soler, I. N. MacInnis and A. Lttge for fruitful discussions and to A. Avital, G. Ronen, and E. Roet for technical assistance.
PY - 1998/4/1
Y1 - 1998/4/1
N2 - In this paper we examine the effect of inhibition on mineral dissolution rate. We postulate a reaction mechanism that involves catalysis and inhibition. The reaction mechanism consists of fast adsorption of a catalyst and/or an inhibitor on the mineral surface, followed by a slow hydrolysis step. The rate of the hydrolysis, which is the rate-determining step, demands on the adsorbed surface species. Therefore, the rate law includes the adsorption isotherms of the catalyst and the inhibitor. Two endmember mechanisms are analyzed. In the first mechanism the catalyst and the inhibitor compete with each other; ie, they have a full mutual (negative) dependence; while in the second mechanism we assume that the adsorption of the catalyst and the inhibitor are absolutely independent on each other. A third general mechanism describes the whole range between the two endmember mechanisms. In this model, the degree of dependence of the catalyst adsoption on the inhibitor adsorption varies from 1 to 0, ie, from complete competition to full independence, respectively. The models are applied to three case studies of kaolinite, albite and K-feldspar dissolution.
AB - In this paper we examine the effect of inhibition on mineral dissolution rate. We postulate a reaction mechanism that involves catalysis and inhibition. The reaction mechanism consists of fast adsorption of a catalyst and/or an inhibitor on the mineral surface, followed by a slow hydrolysis step. The rate of the hydrolysis, which is the rate-determining step, demands on the adsorbed surface species. Therefore, the rate law includes the adsorption isotherms of the catalyst and the inhibitor. Two endmember mechanisms are analyzed. In the first mechanism the catalyst and the inhibitor compete with each other; ie, they have a full mutual (negative) dependence; while in the second mechanism we assume that the adsorption of the catalyst and the inhibitor are absolutely independent on each other. A third general mechanism describes the whole range between the two endmember mechanisms. In this model, the degree of dependence of the catalyst adsoption on the inhibitor adsorption varies from 1 to 0, ie, from complete competition to full independence, respectively. The models are applied to three case studies of kaolinite, albite and K-feldspar dissolution.
UR - http://www.scopus.com/inward/record.url?scp=0031712695&partnerID=8YFLogxK
U2 - 10.1016/S0016-7037(98)00036-2
DO - 10.1016/S0016-7037(98)00036-2
M3 - Article
AN - SCOPUS:0031712695
SN - 0016-7037
VL - 62
SP - 1295
EP - 1306
JO - Geochimica et Cosmochimica Acta
JF - Geochimica et Cosmochimica Acta
IS - 8
ER -