28][41].
Figure 1.
Electron photos of nano- and microsilica at different magnifications [41]. ( a
) ×15,000; (
b
) ×50,000.
Table 3.
Data from X-ray spectral analysis of the main elements contained in cyclone dust [41].
Microsilica, depicted in
Figure 1, is a powdery substance composed of ultrafine spherical particles
[41]. It emerges as a by-product during the gas purification process in technological furnaces utilized for producing silicon-containing alloys (such as metallic silicon, ferrosilicon, silicomanganese, and ferrosilicochrome).
Table 3 illustrates the X-ray spectral analysis, presenting the primary elements found in the cyclone dust
[28,41][
The primary components within the initial cyclone dust were nano- and micro-sized SiO
2 spheres, as depicted in
Figure 1.
Figure 1a displays micro- and nanospheres of SiO
2 magnified 15,000 times, whereas
Figure 1b, magnified at 50,000 times, exhibits a micro-sized sphere enveloped with nano-sized SiO
2 spheres.
Figure 2 illustrates the differential and indirect particle distribution by dust size within the cyclones at the Bratsk Ferroalloy Plant.
Figure 2. The differential and integral distribution of particles by dust size from the cyclones of the Bratsk Ferroalloy Plant is shown in the graph (Distribution mode is 0.29 μm)
[41].
Protopopov, E.V. et al.
[39] present a diagram depicting the silicon monoxide formation balance during silicon production (
Figure 3). When a charge containing silicon is melted, silica undergoes sublimation to create silicon monoxide, which then condenses within the colder, upper layers of the charge. A portion of the silicon monoxide is carried by the gas flow to the furnace surface, where it oxidizes to silicon dioxide and is captured by gas cleaning devices
[40,41][40][41].
Figure 3.
Formation of silicon monoxide in furnaces during silicon production [39].
About 10% of the total gas content consists of primary dust, characterized by low dispersion. This dust can be efficiently eliminated from traditional dry and wet cleaning systems due to its granulometric composition. However, the remaining 90% of the dust comprises highly dispersed particles, primarily 2 μm in size. The formation of microsilica is thought to result from the processes outlined in
Figure 3, according to the authors of
[39]:
-
Interaction between silicon monoxide and carbon monoxide in a gas furnace at temperatures ranging from 1400 to 1800 K leads to the formation of microsilica.
-
In the low-temperature zones of the furnace, where the gas phase temperature and the equilibrium concentration of SiO sharply decrease, silicon monoxide disproportionation may occur.
-
The very high cooling rates of the gas phase could potentially lead to the direct condensation of silicon monoxide.
Information from
[39] details the characteristics and volume of dust accumulated at the gas treatment units (GTU) of JSC Kremniy. The silica phase composition encompasses β-cristobalite, α-quartz, iron oxides, silicates, spinel FeO∙Al
2O
3, calcium, phosphorus, magnesium, manganese, titanium oxides, free carbon, and silicon. These dust particles, residues from silicon and ferrosilicon production, share common traits as silicon vapor condensates (silicon monoxide). The microsilica particles predominantly exhibit a spherical shape with an average diameter of 0.1–0.2 μm. They are amorphous and contain a high SiO
2 content, ranging from 84% to 98%. Challenges concerning storage and transportation have been documented
[40,41,42,43,44][40][41][42][43][44].
Figure 4 provides microphotographs of microsilica from various enterprises.
Figure 4. Microphotographs of silicon hose dust surface from the Kamensk-Uralsky branch of OJSC SUAL have been taken, showcasing (
a) the top view, (
b) the appearance at higher magnification, and (
c) surface detailing, with a determination of the diameters of spherical particles of silicon dioxide. Images of the surface of silicon dust after wet cleaning by JSC Kremniy
[39]: (
d) viewed from above, (
e) a closer look at the surface at higher magnification, and (
f) a detailed view at 50,000 times magnification, showing spherical particles of silicon dioxide on the surface.
[41].
Aligned with the Si-O-C diagram and based on process conditions and the condensed phase composition, the furnace bath can be classified into three distinct zones: low, medium, and high temperature
[40,41,42,43,44,45][40][41][42][43][44][45]. These zones exhibit variations in temperature conditions, condensed phase composition, and, most significantly, the inherent processes involved.
The low-temperature zone, existing under conditions of thermal equilibrium, maintains a temperature not exceeding 1500 °C. The condensed phases in this zone are dictated by the initial charge’s composition and the associated processes.
Moving to the medium temperature zone, this area lacks carbon but features the presence of only silica and silicon carbide in its condensed phases.
The high-temperature zone, surpassing 1817 °C, delineates a space where silicon remains stable solely at elevated temperatures exceeding 1817 °C and at a high concentration of SiO(g). Here, the destruction of silicon carbide and the production of silicon may lead to substantial SiO(g) losses. These losses are mitigated by removing them from the high-temperature zone of the furnace bath, resulting in the predominance of silicon dioxide—a primary component of process dust removed from the furnace along with process gases. This promising raw material is sourced from waste dust in the cyclones within the emission purification system used during catalytic silicon production.
Preliminary research indicates that silicon-containing dust comprises 80%–95.28% SiO
2 [39,40,41,42,43][39][40][41][42][43]. The dust consists of spherical particles, ranging from nano-disperse particles up to 100 nm, which have a tendency to aggregate. The study of this waste is essential for extracting silicon dioxide, silicon carbide, and carbon
[40,41][40][41].
Gas purification dust from silicon production is actively used in construction. However, cyclone dust is unsuitable for this application due to its high carbon content, which violates regulatory documents
[47,48,49][47][48][49]. Conversely, microsilica obtained by trapping furnace gases exhibits a minimal bulk density, ranging from 130 to 430 kg/m
3. Challenges in utilizing and storing this product have led to its application in a more convenient, compressed form (with a density of 480–720 kg/m
3) or as an aqueous suspension with a solid content of 50 wt% (with a density of 1320–1440 kg/m
3). The compressed product is produced by passing air through silos containing microsilica over several hours, causing the fusion of clusters into larger aggregates, ranging from 10 to several 100 microns in size (
Figure 5).
Figure 5.
Particles of compacted microsilica (electron microscopic image in secondary electrons) [41]. ( a
) ×33,000; (
b
) ×27,000.
The electric furnace generates soot collected from various collection systems, including baghouses. Instead of disposing of it in slurry fields, this soot is sold as an additive (AS)
[41]. One of the significant advantages of using silica fume is its suitability as a mineral admixture in concrete
[49]. Essentially, silica consists of amorphous (non-crystalline) silicon dioxide (SiO
2). Currently, concrete failure when incorporating microsilica arises from corrosion, leading to increased expenses due to sea salt or icing. Therefore, it is crucial to ensure the end product’s resistance to sulphate, thereby fulfilling a primary objective.
The consensus recognizes that utilizing compressed microsilica necessitates longer and more intense mixing to disperse agglomerates. Despite the technological advancement of microsilica suspensions, they cannot be stored under subzero temperatures and require redispersion after prolonged storage. In the UK, the use of compressed microsilica holds paramount practical importance, while in European countries, both suspended forms and compressed microsilica are commonly employed.
4. History of the Use of Micro and Nanosilica as a Cement Additive
In 1950, the Fiskaa plant in Kristiansand, Norway, installed the first experimental filters for capturing microsilica
[50]. Two years later, initial tests were conducted using MS as an additive to Portland cement concrete, coinciding with the first publication on its concrete application.
The commercial sales of microsilica in concrete plants commenced around 1971. In 1974, engineers from the Fiskaa plant (later forming the Elkem organization) significantly redesigned the industrial bag filter. The increased use of microsilica in concrete led to compliance with silica fume standards in cement in Norway between 1976 and 1978, slightly later in concrete. The utilization of MS in Bluetooth and Iceland began in 1981. By 1990, microsilica had gained global recognition as a concrete additive, proving its capability to enhance final product properties. Considerable attention was directed towards ensuring reliability and extended service life.
By the year 2000, international standards for the use of Microsilica additives (MS) in concrete technologies became available and were commonly applied in industrial production across most countries. High-strength concrete incorporating MS was used in the construction of significant infrastructure projects, including high-rise buildings in Chicago, the Channel Tunnel, the Northumberland Strait Bridge in Washington, and offshore drilling platforms in the North Sea. In Russia, MS-based construction projects were undertaken, albeit with a delay of several decades. These projects in Russia encompass transport tunnels on Kutuzovsky, Leninsky, and Nakhimovsky prospects, a bridge on Bratislavskaya, an overpass on Oleniy Valkikh, and gravity-type oil platform streets for the Sakhalin-2 project. As previously noted, MS is a byproduct derived from silicon production, processed in electric furnaces
[28,39[28][39][40],
40], with required raw materials including quartz, coal, or wood chips.
5. History of the Use of Micro and Nanosilica as a Cement Additive in Russia
Russia has implemented a standard
[49] for an active mineral additive of technogenic origin exhibiting high pozzolanic activity, known as condensed microsilica (hereinafter referred to as microsilica). This is designed to specifically regulate the properties of concrete, mortar, and dry building mixtures, which are made with binders primarily based on Portland cement clinker (
Table 4). Microsilica is categorized in Russian documents like “MK” into three types, each identified as follows:
Table 4.
Quality indicators of microsilica [49].