TY - JOUR
T1 - Kinetics of K2FeF5·H2O (s) and CrF3·2H2O (s) crystallization from stainless steel spent pickling baths
AU - Gálvez, José L.
AU - Dufour, Javier
AU - Negro, Carlos
AU - López-Mateos, Federico
PY - 2007/7/18
Y1 - 2007/7/18
N2 - Stainless steel spent pickling bath is a hazardous waste composed mainly of iron, chromium, and nickel nitrates and fluorides and free nitric and hydrofluoric acids. A new process has been developed for the recovery of this waste. The first stage is the crystallization of K2FeF 5·H2O and CrF3·2H2O by adding a mixture of potassium fluoride and hydroxide. Nickel is kept in solution and can be recovered in a further stage. In this work, crystallization of fluorides has been modeled by the population-balance method. Results show that crystal growth rate is linear-dependent with crystal size, while other population phenomena should be taken into account, such as aggregation or breakage. Temperature shows an anomalous influence on the crystals population balance, because of the stability decrease of CrF3, although its solubility increases. Mass transfer modeling of the reaction allows supersaturation calculation. Mass transfer coefficient values at 40, 52.5, and 65°C are 4.1 × 10-6, 1.7 × 10-5, and 2.2 × 10-3 L4.5 mol3.5 μm-2 min-1, respectively. A crystal growth global order of 4.5 has been observed. Moreover, it has been observed that steady-state supersaturation has a direct relationship with initial concentration of precipitating compounds, so a new simplified model has been proposed.
AB - Stainless steel spent pickling bath is a hazardous waste composed mainly of iron, chromium, and nickel nitrates and fluorides and free nitric and hydrofluoric acids. A new process has been developed for the recovery of this waste. The first stage is the crystallization of K2FeF 5·H2O and CrF3·2H2O by adding a mixture of potassium fluoride and hydroxide. Nickel is kept in solution and can be recovered in a further stage. In this work, crystallization of fluorides has been modeled by the population-balance method. Results show that crystal growth rate is linear-dependent with crystal size, while other population phenomena should be taken into account, such as aggregation or breakage. Temperature shows an anomalous influence on the crystals population balance, because of the stability decrease of CrF3, although its solubility increases. Mass transfer modeling of the reaction allows supersaturation calculation. Mass transfer coefficient values at 40, 52.5, and 65°C are 4.1 × 10-6, 1.7 × 10-5, and 2.2 × 10-3 L4.5 mol3.5 μm-2 min-1, respectively. A crystal growth global order of 4.5 has been observed. Moreover, it has been observed that steady-state supersaturation has a direct relationship with initial concentration of precipitating compounds, so a new simplified model has been proposed.
UR - https://www.scopus.com/pages/publications/34547485876
U2 - 10.1021/ie061343u
DO - 10.1021/ie061343u
M3 - Article
AN - SCOPUS:34547485876
SN - 0888-5885
VL - 46
SP - 5221
EP - 5227
JO - Industrial & Engineering Chemistry Research
JF - Industrial & Engineering Chemistry Research
IS - 15
ER -