Abstract

Silicon dioxide nanoparticles, also known as silica nanoparticles or nanosilica, are the basis for a great deal of biomedical and catalytic research due to their stability, low toxicity and ability to be functionalized with a range of molecules and polymers. A novel synthesis route is based on CO2 absorption/sequestration in an autoclave by forsterite (Mg2SiO4), which is part of the mineral group of olivines. Therefore, it is a feasible and safe method to bind carbon dioxide in carbonate compounds such as magnesite forming at the same time as the spherical particles of silica. Indifference to traditional methods of synthesis of nanosilica such as sol gel, ultrasonic spray pyrolysis method and hydrothermal synthesis using some acids and alkaline solutions, this synthesis method takes place in water solution at 175 °C and above 100 bar. Our first experiments have studied the influence of some additives such as sodium bicarbonate, oxalic acid and ascorbic acid, solid/liquid ratio and particle size on the carbonation efficiency, without any consideration of formed silica. This paper focuses on a carbonation mechanism for synthesis of nanosilica under high pressure and high temperature in an autoclave, its morphological characteristics and important parameters for silica precipitation such as pH-value and rotating speed.

Highlights

  • As a result of the high nickel production costs associated with traditional pyrometallurgical techniques and the depletion of high-grade sulfide ores, renewed interest has developed concern on the production of nickel and cobalt by high pressure acid leaching (PAL) of nickel laterites

  • The results showed that the synthesis temperature of 500 ◦ C provided the smallest size of silica nanoparticle, about 106 nm

  • Synthesis of nanosilica was studied via carbonation of olivine using size fraction between 20 and 63 μm with solid/liquid ratios of 1:10 at 175 ◦ C and partial pressure of CO2 more than 100 bar in an autoclave in the presence of additives such as sodium bicarbonate, oxalic and ascorbic acid

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Summary

Introduction

As a result of the high nickel production costs associated with traditional pyrometallurgical techniques and the depletion of high-grade sulfide ores, renewed interest has developed concern on the production of nickel and cobalt by high pressure acid leaching (PAL) of nickel laterites. More than one third of the world’s nickel is nowadays produced from laterite ores [1,2]. Laterites account for two thirds of the world’s nickel resources. It is likely that increasing amounts of nickel will be produced from laterites. The laterite ore consists of fresh saprolite such as K0.4 (Si3.0 Al1.0 )4.0 (Al2.0 Mg0.3 )2.33 O10 (OH) and nontronite such as Na0,3 (Fe3+ ) (Si,Al) O10 (OH)2 ·nH2 O. These silicate ores represent the various layers in the laterite bedrock. This continues to a nontronite rich zone.

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