Extraction of potassium from K-feldspar via the CaCl2 calcination route
摘要
Abstract
The extraction of potassiumfrom K-feldspar via a calcium chloride calcination route was studied with a focus on the effects of the calcination atmosphere
calcination temperature and time
mass ratio of CaCl
2
to K-feldspar ore and particle size of the K-feldspar ore. The results demonstrated that a competing high-temperature hydrolysis reaction of calcium chloride with moisture in a damp atmosphere occurred concurrently with the conversion reaction of K-feldspar with CaCl
2
thus reducing the amount of potassium extracted. The conversion reaction started at approximately 600 ℃ and accelerated with increasing temperature. When the temperature rose above 900 ℃
the extraction of potassium gradually decreased due to the volatilization of the product
KCl. As much as approximately 41% of the potassium was volatilized in 40 min at 1100 ℃. The mass ratio of CaCl
2
/ K-feldspar ore significantly affected the extraction. At a mass ratio of 1.15 and 900 ℃
the potassium extraction reached 91% in 40 min
while the extractionwas reduced to only 22% at the theoreticalmass ratio of 0.2. Optimal process conditions are as follows: ore particle size of 50-75 μm
tablet forming pressure of 3 MPa
dry nitrogen atmosphere
mass ratio of CaCl
2
/ore 1.15:1
calcination temperature of 900 ℃
and calcination time of 40 min. The XRD analysis revealed that a complex phase transition of the product SiO
2
was also accompanied by the conversion reaction of K-feldspar/CaCl
2
. The SiO
2
product formed at the initial stagewas in the quartz phase at 900 ℃ and was gradually transformed into cristobalite after 30 min.
关键词
Keywords
references
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