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<article article-type="research-article" dtd-version="3.0" xml:lang="en" xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink">
	<front>
		<journal-meta>
			<journal-id journal-id-type="publisher-id">MC</journal-id>
			<journal-title-group>
				<journal-title>Materiales de Construcci&#x00F3;n</journal-title>
			</journal-title-group>
			<issn pub-type="epub">0465-2746</issn>
			<publisher>
				<publisher-name>Consejo Superior de Investigaciones Cientificas</publisher-name>
			</publisher>
		</journal-meta>
		<article-meta>
			<article-id pub-id-type="publisher-id">MC201348-e046</article-id>
			<article-id pub-id-type="doi">10.3989/mc.2015.00814</article-id>
			<article-categories>
				<subj-group subj-group-type="heading">
					<subject>Articles</subject>
				</subj-group>
			</article-categories>
			<title-group>
				<article-title>Synthesis of geopolymer from spent FCC: Effect of SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> and Na<sub>2</sub>O/SiO<sub>2</sub> molar ratios</article-title>
				<trans-title-group xml:lang="es">
					<trans-title>Sintesis de geopolimero basado en un catalizador gastado de craqueo catalitico (FCC): Efecto de las relaciones molares SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> y Na<sub>2</sub>O/SiO<sub>2</sub></trans-title>
				</trans-title-group>
				<alt-title alt-title-type="running-head">Synthesis of geopolymer from spent FCC: Effect of SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> and Na<sub>2</sub>O/SiO<sub>2</sub> molar ratios</alt-title>
			</title-group>
			<contrib-group>
				<contrib contrib-type="author">
					<name>
						<surname>Trochez</surname>
						<given-names>J.J.</given-names>
					</name>
					<xref ref-type="aff" rid="AF0001">a</xref>
				</contrib>
				<contrib contrib-type="author" corresp="yes">
					<name>
						<surname>Mej&#x00ED;a de Guti&#x00E9;rrez</surname>
						<given-names>R.</given-names>
					</name>
					<xref ref-type="aff" rid="AF0001">a</xref>
					<xref ref-type="corresp" rid="cor1">&#x002A;</xref>
				</contrib>
				<contrib contrib-type="author">
					<name>
						<surname>Rivera</surname>
						<given-names>J.</given-names>
					</name>
					<xref ref-type="aff" rid="AF0001">a</xref>
				</contrib>
				<contrib contrib-type="author">
					<name>
						<surname>Bernal</surname>
						<given-names>S.A.</given-names>
					</name>
					<xref ref-type="aff" rid="AF0002">b</xref>
				</contrib>
			</contrib-group>
			<aff id="AF0001">
				<label>a</label>Universidad del Valle, (Cali, Colombia)</aff>
			<aff id="AF0002">
				<label>b</label>University of Sheffield, (Sheffield, United Kingdom)</aff>
			<author-notes>
				<corresp id="cor1"><label>&#x002A;</label><email xlink:href="ruby.mejia@correounivalle.edu.co">ruby.mejia@correounivalle.edu.co</email>
				</corresp>
			</author-notes>
			<pub-date pub-type="epub">
				<day>31</day>
				<month>03</month>
				<year>2015</year>
			</pub-date>
			<pub-date pub-type="collection">
				<year>2015</year>
			</pub-date>
			<volume>65</volume>
			<issue>317</issue>
			<elocation-id content-type="doi">10.3989/mc.2015.00814</elocation-id>
			<history>
				<date date-type="received">
					<day>25</day>
					<month>01</month>
					<year>2014</year>
				</date>
				<date date-type="accepted">
					<day>08</day>
					<month>07</month>
					<year>2014</year>
				</date>
				<date date-type="Available on line">
					<day>02</day>
					<month>02</month>
					<year>2015</year>
				</date>
			</history>
			<permissions>
				<copyright-statement>&#x00A9; 2015 CSIC</copyright-statement>
				<copyright-year>2015</copyright-year>
				<license license-type="open-access" xlink:href="http://creativecommons.org/licenses/by-nc/3.0/">
					<license-p>This is an open-access article distributed under the terms of the Creative Commons Attribution-Non Commercial (by-nc) Spain 3.0 License.</license-p>
				</license>
			</permissions>
			<abstract>
				<title>ABSTRACT</title>
				<p>This paper assesses the feasibility of using a spent fluid catalytic cracking catalyst (SFCC) as precursor for the production of geopolymers. The mechanical and structural characterization of alkali-activated SFCC binders formulated with different overall (activator + solid precursor) SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> and Na<sub>2</sub>O/SiO<sub>2</sub> molar ratios are reported. Formation of an aluminosilicate &#x2018;geopolymer&#x2019; gel is observed under all conditions of activation used, along with formation of zeolites. Increased SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> induces the formation of geopolymers with reduced mechanical strength, for all the Na<sub>2</sub>O/SiO<sub>2</sub> ratios assessed, which is associated with excess silicate species supplied by the activator. This is least significant at increased alkalinity conditions (higher Na<sub>2</sub>O/SiO<sub>2</sub> ratios), as larger extents of reaction of the spent catalyst are achieved. SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> and Na<sub>2</sub>O/SiO<sub>2</sub> ratios of 2.4 and 0.25, respectively, promote the highest compressive strength (67 MPa). This study elucidates the great potential of using SFCC as precursor to produce sustainable ceramic-like materials via alkali-activation.</p>
				</abstract>
				<trans-abstract xml:lang="es">
				<title>RESUMEN</title>
				<p><italic>Sintesis de geopolimero basado en un catalizador gastado de craqueo catalitico (FCC): Efecto de las relaciones molares SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> y Na<sub>2</sub>O/SiO<sub>2</sub></italic>. Este art&#x00ED;culo estudia la factibilidad de usar un catalizador gastado del proceso de craqueo (SFCC) para la producci&#x00F3;n de geopol&#x00ED;meros. Se eval&#x00FA;an las caracter&#x00ED;sticas mec&#x00E1;nicas y estructurales de los geopol&#x00ED;meros producidos con diferentes relaciones molares (activador + precursor solido) de SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> y Na<sub>2</sub>O/SiO<sub>2</sub>. La formaci&#x00F3;n de un gel geopolim&#x00E9;rico de tipo aluminosilicato se observa a las diferentes condiciones evaluadas, as&#x00ED; como la formaci&#x00F3;n de zeolitas. Un incremento en la relaci&#x00F3;n SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> genera geopol&#x00ED;meros de baja resistencia mec&#x00E1;nica, a las diferentes relaciones molares Na<sub>2</sub>O/SiO<sub>2</sub> evaluadas, como consecuencia del exceso de especies silicato provenientes del activador. Este efecto es menos significativo al incrementar las condiciones de alcalinidad (mayores relaciones Na<sub>2</sub>O/SiO<sub>2</sub>), ya que un mayor grado de reacci&#x00F3;n del catalizador gastado es alcanzado. Las relaciones SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> y Na<sub>2</sub>O/SiO<sub>2</sub> de 2.4 and 0.25, respectivamente, promueven la mayor Resistencia a la compresi&#x00F3;n (67 MPa). Este estudio muestra el gran potencial de uso del SFCC como precursor en materiales cer&#x00E1;micos obtenidos por activaci&#x00F3;n alcalina.</p>
			</trans-abstract>
			<kwd-group xml:lang="en">
			<title>KEYWORDS</title>
				<kwd>Spent fluid catalytic cracking catalyst</kwd>
				<kwd>Alkali-activation</kwd>
				<kwd>Geopolymers</kwd>
				<kwd>Structural characterization</kwd>
				</kwd-group>
				<kwd-group xml:lang="es">
				<title>PALABRAS CLAVE</title>
				<kwd>Catalizador gastado de craqueo catal&#x00ED;tico</kwd>
				<kwd>Activaci&#x00F3;n alcalina</kwd>
				<kwd>Geopolimeros</kwd>
				<kwd>Caracterizaci&#x00F3;n estructural</kwd>
			</kwd-group>
		</article-meta>
	</front>
	<body>
		<sec id="S0001" sec-type="intro">
			<title>1. INTRODUCTION</title>
			<p>The catalyst used in fluid catalytic cracking (FCC) in the petrochemical industry is an aluminosilicate with a zeolitic structure, often on an alumina or silica-alumina support. The FCC process is conducted to obtain higher-octane gasoline through the breaking of the long chains of hydrocarbon molecules. When the FCC catalyst loses its catalytic properties (becoming &#x2018;spent&#x2019;), it is replaced, and the deactivated catalyst residue is discarded and treated as an inert waste (<xref ref-type="bibr" rid="CIT0001">1</xref>).</p>
			<p>In the search for ways to utilize this waste, the application of SFCC as an alternative supplementary cementitious material for the production of blended cements has been explored (<xref ref-type="bibr" rid="CIT0002">2</xref>, <xref ref-type="bibr" rid="CIT0003">3</xref>). The pozzolanic activity of SFCC from different sources has been demonstrated, and the production of high performance Portland cement&#x2013;based mortars and concretes has been achieved (<xref ref-type="bibr" rid="CIT0001">1</xref>). Despite these evident good results, the availability of this by-product worldwide is relatively low, at around 800000 tons per year (<xref ref-type="bibr" rid="CIT0004">4</xref>), and therefore, it has not been considered a commercially attractive alternative as a supplementary cementitious material in the global context. In Colombia, there is an estimated production 12400 tons/year of spent FCC, which is currently disposed in landfill. However, considering that SFCC can contain heavy metals, cementation of this waste is a viable alternative for its stabilization, rather than landfilling, which is the current disposal route in most parts of the world.</p>
			<p>In the past decades great attention has been given to alternative cementitious materials known as &#x2018;geopolymers&#x2019;, which are binders produced through the chemical reaction between an aluminosilicate precursor and an alkaline activator. The main precursors used in geopolymers production are metakaolin (<xref ref-type="bibr" rid="CIT0005">5</xref>) and industrial by-products from coal fired power generation, particularly fly ash (<xref ref-type="bibr" rid="CIT0006">6</xref>&#x2013;<xref ref-type="bibr" rid="CIT0009">9</xref>). However, it has been proven that geopolymers can be produced from other aluminosilicate precursors, such as volcanic ashes (<xref ref-type="bibr" rid="CIT0010">10</xref>, <xref ref-type="bibr" rid="CIT0011">11</xref>) and natural minerals (<xref ref-type="bibr" rid="CIT0012">12</xref>, <xref ref-type="bibr" rid="CIT0013">13</xref>), whose composition is rich in silica and alumina present in energetic (usually disordered) solid phases. These precursors are easily dissolved in an alkaline media, promoting the subsequent polycondensation of the Al and Si species to form a hardened product (<xref ref-type="bibr" rid="CIT0005">5</xref>).</p>
			<p>The widespread interest in geopolymers for different industrial applications has motivated the assessment of low cost precursors such as SFCC in geopolymer production. Preliminary work activating SFCC catalysts to form geopolymers (<xref ref-type="bibr" rid="CIT0014">14</xref>, <xref ref-type="bibr" rid="CIT0015">15</xref>) showed good mechanical strength in the activated SFCC specimens. This was attributed to the dissolution of the zeolite phases in the spent catalyst, promoting the formation of a crosslinked aluminosilicate type gel (<xref ref-type="bibr" rid="CIT0015">15</xref>). The high reactivity of SFCC, along with its chemical composition rich in Al and Si, makes it a suitable precursor for production of geopolymers; however, there is not yet a good understanding of the mechanism of reaction of these materials, or detailed identification of the factors controlling their microstructural evolution. Also, it is expected that SFCC catalysts from different sources will have different compositions and structures, making necessary the assessment of different formulation conditions for each source of materials, to produce binders with good performance and to generate useful information by comparison of the performance of residues from different sources worldwide.</p>
			<p>This study evaluates the feasibility of producing geopolymer materials based on a Colombian SFCC. The effect of formulation conditions, specifically overall Na<sub>2</sub>O/SiO<sub>2</sub> and SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> molar ratios, in the microstructure and compressive strength of these materials is assessed. Detailed structural analysis of the activated SFCC catalyst is conducted using X-ray diffraction (XRD), Fourier transform infrared spectroscopy (FTIR), <sup>29</sup>Si and <sup>27</sup>Al MAS nuclear magnetic resonance spectroscopy, and scanning electron microscopy (SEM).</p>
		</sec>
		<sec id="S0002">
			<title>2. EXPERIMENTAL PROGRAM</title>
			<sec id="S20003">
				<title>2.1. Materials</title>
				<p>A spent fluid catalytic cracking catalyst (SFCC) from a Colombian petroleum company is used as the geopolymer precursor in this study. Before chemical activation, the SFCC was milled for 5 hours, using a ball mill. The resulting powder had specific gravity of 2630 kg/m<sup>3</sup> and a mean diameter D (<xref ref-type="bibr" rid="CIT0004">4</xref>, <xref ref-type="bibr" rid="CIT0003">3</xref>) of 16.8 &#x00B5;m. The particle size distribution, determined by laser diffraction using a Mastersizer 200 of Malvern, was: 10% below 2.46 &#x00B5;m (D10), 50% below 13.25 &#x00B5;m (D50) and 90% below 37.44 &#x00B5;m (D90). Its chemical composition, determined by X-Ray Fluorescence (XRF) using a Philips MagixPro PW&#x2013;2440 spectrometer fitted with a rhodium tube, is shown in <xref ref-type="table" rid="T0001">Table 1</xref>.
</p>
				<table-wrap id="T0001">
					<label>Table 1</label>
					<caption>
						<p>Chemical composition of the SFCC. LOI is loss on ignition at 1000 &#x00B0;C</p>
					</caption>
					<table frame="hsides" rules="groups">
						<thead>
							<tr>
								<th align="left">Component</th>
								<th align="center">mass %</th>
							</tr>
						</thead>
						<tbody>
							<tr>
								<td align="left">SiO<sub>2</sub>
								</td>
								<td align="center">48.09</td>
							</tr>
							<tr>
								<td align="left">Al<sub>2</sub>O<sub>3</sub>
								</td>
								<td align="center">41.57</td>
							</tr>
							<tr>
								<td align="left">Fe<sub>2</sub>O<sub>3</sub>
								</td>
								<td align="center">0.91</td>
							</tr>
							<tr>
								<td align="left">CaO</td>
								<td align="center">0.22</td>
							</tr>
							<tr>
								<td align="left">MgO</td>
								<td align="center">0.13</td>
							</tr>
							<tr>
								<td align="left">K<sub>2</sub>O</td>
								<td align="center">0.09</td>
							</tr>
							<tr>
								<td align="left">TiO<sub>2</sub>
								</td>
								<td align="center">0.85</td>
							</tr>
							<tr>
								<td align="left">LOI</td>
								<td align="center">2.19</td>
							</tr>
						</tbody>
					</table>
				</table-wrap>
				<p>The X-ray diffractogram of the SFCC (<xref ref-type="fig" rid="F0001">Fig. 1</xref>) shows that this material contains an amorphous component, as well as the crystalline zeolite phases faujasite (Na<sub>2</sub>Al<sub>2</sub>Si<sub>10</sub>O<sub>24</sub>&#x00B7;<italic>n</italic>H<sub>2</sub>O, Powder Diffraction File (PDF) # 012-0228) and analcime (NaAl<sub>2</sub>Si<sub>2</sub>O<sub>6</sub>&#x00B7;H<sub>2</sub>O, PDF # 003-0740), along with the aluminosilicate minerals andalusite (Al<sub>2</sub>SiO<sub>5</sub>, PDF # 039-0376), mullite (2Al<sub>2</sub>O<sub>3</sub>&#x00B7;SiO<sub>2</sub>, PDF # 089-2645), sillimanite (Al<sub>2</sub>O<sub>3&#x00B7;</sub>SiO<sub>2</sub>, PDF # 089-0888), kyanite (Al<sub>2</sub>SiO<sub>5</sub>, PDF #00-011-046) and quartz (SiO<sub>2</sub>, PDF # 046-1045).</p>
				<p>The alkali activator used was a commercial sodium silicate solution with 29.1 wt.% SiO<sub>2</sub> and 10.2 wt.% Na<sub>2</sub>O and 60.0 wt.% H<sub>2</sub>O, and solid analytical grade NaOH pellets. This was dissolved in the mix water and allowed to cool until reaching room temperature prior to preparation of the specimens. All the activating solutions reach a pH higher than 14.</p>
			</sec>
			<sec id="S20004">
				<title>2.2. Sample preparation and tests conducted</title>
				<p>For the preparation of the geopolymer specimens, the alkaline activator was formulated to obtain overall (activator + solid precursor) SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> molar ratios of 2.0, 2.2, 2.4, 2.6, 2.8 and 3.0, and overall Na<sub>2</sub>O/SiO<sub>2</sub> molar ratios of 0.20, 0.25 and 0.30. The amount of water in the alkali activator was adjusted to achieve a total H<sub>2</sub>O/Na<sub>2</sub>O ratio of 11 in all samples (<xref ref-type="table" rid="T0002">Table 2</xref>). The fresh pastes were mixed for 12 minutes using a Hobart mixer, poured into cylindrical molds, and vibrated for 5 minutes to reach a homogeneous distribution in the mold and remove entrained air. Samples were kept in sealed molds at ambient temperature (25&#x00B1;5 &#x00B0;C) for 24 hours, then demolded and stored in a high humidity container (relative humidity &#x003E;90%), also at ambient temperature, for 7 days.
</p>
				<table-wrap id="T0002">
					<label>Table 2</label>
					<caption>
						<p>Chemical Composition of geopolymer systems (total H<sub>2</sub>O/Na<sub>2</sub>O molar ratio of 11)</p>
					</caption>
					<table frame="hsides" rules="groups">
						<thead>
							<tr>
								<th align="left" colspan="3">Mix Composition (Total Molar Ratio)</th>
								<th align="center">Alkaline activator Solution</th>
							</tr>
							<tr>
								<th align="center" colspan="3"><hr/></th>
								<th align="center" colspan="1"><hr/></th>
							</tr>
							<tr>
								<th align="left">SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub>
								</th>
								<th align="center">Na<sub>2</sub>O/SiO<sub>2</sub>
								</th>
								<th align="center">Na<sub>2</sub>O/Al<sub>2</sub>O<sub>3</sub>
								</th>
								<th align="center">Ms = SiO<sub>2</sub>/Na<sub>2</sub>O (molar ratio)</th>
							</tr>
						</thead>
						<tbody>
							<tr>
								<td align="left">2.0</td>
								<td align="center"/>
								<td align="center">0.40</td>
								<td align="center">0.08</td>
							</tr>
							<tr>
								<td align="left">2.2</td>
								<td align="center"/>
								<td align="center">0.44</td>
								<td align="center">0.53</td>
							</tr>
							<tr>
								<td align="left">2.4</td>
								<td align="center">0.20</td>
								<td align="center">0.48</td>
								<td align="center">0.90</td>
							</tr>
							<tr>
								<td align="left">2.6</td>
								<td align="center"/>
								<td align="center">0.52</td>
								<td align="center">1.22</td>
							</tr>
							<tr>
								<td align="left">2.8</td>
								<td align="center"/>
								<td align="center">0.56</td>
								<td align="center">1.49</td>
							</tr>
							<tr>
								<td align="left">3.0</td>
								<td align="center"/>
								<td align="center">0.60</td>
								<td align="center">1.72</td>
							</tr>
							<tr>
								<td align="left">2.0</td>
								<td align="center"/>
								<td align="center">0.50</td>
								<td align="center">0.07</td>
							</tr>
							<tr>
								<td align="left">2.2</td>
								<td align="center"/>
								<td align="center">0.55</td>
								<td align="center">0.42</td>
							</tr>
							<tr>
								<td align="left">2.4</td>
								<td align="center"/>
								<td align="center">0.60</td>
								<td align="center">0.72</td>
							</tr>
							<tr>
								<td align="left">2.6</td>
								<td align="center">0.25</td>
								<td align="center">0.65</td>
								<td align="center">0.97</td>
							</tr>
							<tr>
								<td align="left">2.8</td>
								<td align="center"/>
								<td align="center">0.70</td>
								<td align="center">1.19</td>
							</tr>
							<tr>
								<td align="left">3.0</td>
								<td align="center"/>
								<td align="center">0.75</td>
								<td align="center">1.38</td>
							</tr>
							<tr>
								<td align="left">2.0</td>
								<td align="center"/>
								<td align="center">0.60</td>
								<td align="center">0.06</td>
							</tr>
							<tr>
								<td align="left">2.2</td>
								<td align="center"/>
								<td align="center">0.66</td>
								<td align="center">0.35</td>
							</tr>
							<tr>
								<td align="left">2.4</td>
								<td align="center"/>
								<td align="center">0.72</td>
								<td align="center">0.60</td>
							</tr>
							<tr>
								<td align="left">2.6</td>
								<td align="center">0.30</td>
								<td align="center">0.78</td>
								<td align="center">0.81</td>
							</tr>
							<tr>
								<td align="left">2.8</td>
								<td align="center"/>
								<td align="center">0.84</td>
								<td align="center">0.99</td>
							</tr>
							<tr>
								<td align="left">3.0</td>
								<td align="center"/>
								<td align="center">0.90</td>
								<td align="center">1.15</td>
							</tr>
						</tbody>
					</table>
				</table-wrap>
				<p>The compressive strength was assessed for cylindrical paste samples of 30 mm (diameter) &#x00D7; 60 mm (height), using a universal testing instrument (Instron) at a displacement rate of 1 mm/min. Sample ends were flattened and made parallel using coarse sandpaper before testing. Each reported value corresponds to the average of 5 measurements. Powdered pastes were analyzed through:</p>
				<list list-type="bullet">
					<list-item>
						<p>X-ray diffraction (XRD), using a Bruker D8 Advance instrument with Cu K&#x3B1; radiation and a nickel filter. The tests were conducted with a step size of 0.020&#x00B0;, for 2&#x3B8; values between 3&#x00B0; and 60&#x00B0;.</p>
					</list-item>
					<list-item>
						<p>Fourier transform infrared (FTIR) spectroscopy, with a PerkinElmer Spectrum 100 instrument. The KBr pellet technique was used to prepare the samples, which were scanned from 4000 to 400 cm<sup>&#x2212;1</sup>.</p>
					</list-item>
					<list-item>
						<p>Solid-state <sup>29</sup>Si and <sup>27</sup>Al magic angle spinning nuclear magnetic resonance (MAS NMR). The analysis of the SFCC was carried out with a Bruker 400 Ultrashield Avance II 400 spectrometer (9.4 T) using a MAS NMR probe for 5 mm rotors and a spinning speed of 5.0 kHz. <sup>29</sup>Si MAS NMR spectra were acquired using a resonance frequency of 79.5 MHz, a pulse width of 5 &#x03BC;s and a relaxation delay of 5 s and 4000 scans. <sup>27</sup>Al MAS NMR experiments were conducted at 104.23 MHz, with a pulse width of 5 &#x03BC;s, a relaxation delay of 0.25 s, and 2048 scans. MAS NMR spectra of the alkali activated specimens were obtained on a Varian Direct Drive VNMRS-600 spectrometer (14.1 T) using a MAS NMR probe for 4 mm o.d. zirconia rotors and a spinning speed of 10.0 kHz. <sup>29</sup>Si MAS NMR spectra were acquired using a pulse width of 4 &#x03BC;s and a relaxation delay of 20 s, and more than 3600 scans. <sup>27</sup>Al MAS NMR experiments were conducted at 156.3 MHz on the same instrument, with a pulse width of 0.5 &#x03BC;s, a relaxation delay of 2 s, and 1024 scans. All <sup>29</sup>Si and <sup>27</sup>Al chemical shifts are referenced to external samples of tetramethylsilane (TMS) and a 1.0 M aqueous solution of AlCl<sub>3</sub>&#x00B7;6H<sub>2</sub>O, respectively.</p>
					</list-item>
					<list-item>
						<p>Scanning electron microscopy (SEM), conducted in a JEOL JSM-6490LV high vacuum microscope (3&#x00D7;10<sup>&#x2212;6</sup> torr) at an acceleration voltage of 20 keV, using carbon coated unpolished specimens.</p>
					</list-item>
				</list>
				<fig id="F0001">
					<label>Figure 1</label>
					<caption>
						<p>Diffractogram of the unreacted spent FCC catalyst. An: andalusite, Am: analcime, F: faujasite, K: kyanite, M: mullite, Q: quartz, S: sillimanite.</p>
					</caption>
					<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="MC201348-e046-g001.tif"/>
				</fig>
			</sec>
		</sec>
		<sec id="S0005" sec-type="results|discussion">
			<title>3. RESULTS AND DISCUSSION</title>
			<sec id="S20006">
				<title>3.1. Compressive strength</title>
				<p>The formulation of the specimens has a marked effect on strength. The highest mechanical strengths are obtained (<xref ref-type="fig" rid="F0002">Fig. 2</xref>) in samples formulated with a Na<sub>2</sub>O/SiO<sub>2</sub> ratio of 0.25 and a SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> ratio of 2.4, reporting values of up to 67 MPa. In activated SFCC pastes formulated with a low Na<sub>2</sub>O/SiO<sub>2</sub> ratio (0.20), a significant decrease in the mechanical strength is identified at higher SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> ratios beyond the optimum. This effect is least pronounced at higher Na<sub>2</sub>O/SiO<sub>2</sub> ratio (0.30), where activated spent catalyst samples formulated with SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> ratios between 2.4 and 3.0 do not show significant changes in the compressive strength as a function of the formulation conditions. Specimens formulated with a Na<sub>2</sub>O/SiO<sub>2</sub> molar ratio of 0.20 and SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> of 2.0 and 2.2 were not tested due to the low degree of compaction achieved in these specimens.</p>
				<fig id="F0002">
					<label>Figure 2</label>
					<caption>
						<p>7-day compressive strengths of alkali-activated SFCC specimens.</p>
					</caption>
					<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="MC201348-e046-g002.tif"/>
				</fig>
				<p>These results are comparable with the strengths of metakaolin-based geopolymers with the same curing duration and similar formulation conditions, including the reduction in strength at high SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> ratios (<xref ref-type="bibr" rid="CIT0016">16</xref>). This strength reduction is associated with the excess of silicates in the system supplied by the activator, as the extent of polymerization of the silica is high and its rate of reaction is slower than is required for optimal strength development (<xref ref-type="bibr" rid="CIT0017">17</xref>). However, in the formulations with higher Na<sub>2</sub>O/SiO<sub>2</sub> ratios, it is expected that the increased alkalinity promote a higher extent of dissolution of the spent catalysts, and therefore higher availability of Al-rich species, which are able to react with the additional silicate species that the activator can supply at higher SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> ratios.</p>
			</sec>
			<sec id="S20007">
				<title>3.2. X-ray diffraction</title>
				<p>The X-ray diffractograms of the activated spent FCC pastes formulated with Na<sub>2</sub>O/SiO<sub>2</sub> molar ratios of 0.20, 0.25 and 0.30 are shown in <xref ref-type="fig" rid="F0003">Fig. 3</xref>. All of the activated SFCC pastes show (<xref ref-type="fig" rid="F0003">Figs. 3A</xref>, <xref ref-type="fig" rid="F0003">3B</xref> and <xref ref-type="fig" rid="F0003">3C</xref>) an amorphous hump between 2&#x3B8; values of 25&#x00B0; and 35&#x00B0;, attributed to the formation of an aluminosilicate type gel similar to those typically observed in metakaolin-based geopolymers (<xref ref-type="bibr" rid="CIT0018">18</xref>). Mullite, sillimanite, kyanite and quartz, previously identified in the unreacted SFCC (<xref ref-type="fig" rid="F0001">Fig. 1</xref>), are also observed in the alkali-activated pastes, suggesting that these phases are not participating in the activation reaction to any notable extent. This is consistent with the observations in fly ash based geopolymers, where mullite and quartz are also identified as unreactive compounds (<xref ref-type="bibr" rid="CIT0019">19</xref>), and the results of Rodr&#x00ED;guez et al. (<xref ref-type="bibr" rid="CIT0015">15</xref>) in alkali-activated specimens based on a Spanish SFCC material.</p>
				<p>In samples formulated with an Na<sub>2</sub>O/SiO<sub>2</sub> ratio of 0.20 (<xref ref-type="fig" rid="F0003">Fig. 3A</xref>), the intensities of the peaks assigned to faujasite and analcime are significantly reduced upon activation, when compared with the unreacted SFCC, along with the formation of zeolite Na-A (Na<sub>12</sub>Al<sub>12</sub>Si<sub>12</sub>O<sub>48</sub>&#x00B7;<italic>x</italic>H<sub>2</sub>O, PDF # 039-0221), which has been identified as a reaction product in geopolymer materials based on metakaolin (<xref ref-type="bibr" rid="CIT0020">20</xref>). The formation of multiple zeolite phases embedded in the geopolymer gel has been reported in several studies (<xref ref-type="bibr" rid="CIT0018">18</xref>), and our findings are consistent with these results. The formation of ussingite (Na<sub>2</sub>AlSi<sub>3</sub>O<sub>8</sub>(OH), PDF # 028-1037), which is a higher-silica secondary mineral often formed along with sodalite, is also observed under the activation conditions assessed.</p>
				<fig id="F0003">
					<label>Figure 3</label>
					<caption>
						<p>Diffractograms of activated SFCC pastes formulated with a Na<sub>2</sub>O/SiO<sub>2</sub> ratio of (A) 0.20, (B) 0.25 and (C) 0.30. An: analcime, F: faujasite, U: ussingite, ZA: zeolite Na-A, Q: quartz, M: mullite, S: sillimanite and Ky: kyanite.</p>
					</caption>
					<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="MC201348-e046-g003.tif"/>
				</fig>
				<p>Upon increasing the Na<sub>2</sub>O/SiO<sub>2</sub> molar ratio to 0.25 (<xref ref-type="fig" rid="F0003">Fig. 3B</xref>), ussingite and zeolite Na-A are identified at the different SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> ratios assessed. The intensity of the peaks assigned to faujasite is reduced upon activation. A similar trend is observed in the XRD patterns for the specimens formulated with the highest Na<sub>2</sub>O/SiO<sub>2</sub> ratio (0.30) (<xref ref-type="fig" rid="F0003">Fig. 3C</xref>), where faujasite reflections are no longer observed. Considering this, and the fact that these samples have a more intense amorphous hump than specimens formulated with lower Na<sub>2</sub>O/SiO<sub>2</sub> ratios, it is likely that faujasite is acting as a source of Al and Si species in the system, promoting the formation of an amorphous aluminosilicate type product. The excess hydroxide ion concentration, associated with higher Na<sub>2</sub>O/SiO<sub>2</sub> ratios, is likely to influence the aluminosilicate gel precipitation at very early stages of reaction (<xref ref-type="bibr" rid="CIT0021">21</xref>), promoting increased solubility, which affects the precipitation and the subsequent geopolymerization reactions. This is according with the results of compressive strength development presented in section 3.1.</p>
			</sec>
			<sec id="S20008">
				<title>3.3. Fourier transform infrared spectroscopy (FTIR)</title>
				<p>The spectrum of unreacted SFCC (<xref ref-type="fig" rid="F0004">Fig. 4</xref>) shows bands at 912 cm<sup>&#x2212;1</sup> corresponding to the OH deformation vibration (<xref ref-type="bibr" rid="CIT0022">22</xref>), and the signals at 834, 612 and 526 cm<sup>&#x2212;1</sup> attributed to asymmetric, double 6-ring, and bending vibration modes of the aluminosilicate framework in dealuminated faujasite (<xref ref-type="bibr" rid="CIT0023">23</xref>). The band at 560 cm<sup>&#x2212;1</sup> is assigned to the octahedral aluminum present in mullite, kyanite and sillimanite, as identified by XRD (<xref ref-type="fig" rid="F0001">Fig. 1</xref>), and the band at 460 cm<sup>&#x2212;1</sup> corresponds to the symmetric bending modes of the Si-O-Si bonds (<xref ref-type="bibr" rid="CIT0024">24</xref>).</p>
				<fig id="F0004">
					<label>Figure 4</label>
					<caption>
						<p>FTIR spectra of SFCC precursor, and activated pastes formulated with SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> (S/A) ratios as marked, at Na<sub>2</sub>O/SiO<sub>2</sub> ratios of (A) 0.20, (B) 0.25, (C) 0.30.</p>
					</caption>
					<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="MC201348-e046-g004.tif"/>
				</fig>
				<p>All alkali-activated pastes display a main band between 1200 cm<sup>&#x2212;1</sup> and 800 cm<sup>&#x2212;1</sup> corresponding to the asymmetric stretching vibration mode of the Si-O-T linkage (where T may be Si or Al) (<xref ref-type="bibr" rid="CIT0025">25</xref>). It is observed that this band shifts towards lower wavenumbers (&#x223C;1011 cm<sup>&#x2212;1</sup>) upon activation of the anhydrous SFCC precursor (1080 cm<sup>&#x2212;1</sup>). This displacement suggests a structural change of the SFCC upon partial dissolution in the alkaline environment, and the subsequent formation of an aluminosilicate type gel.</p>
				<p>The activation process also leads to a reduction in the intensities of the bands observed in the SFCC precursor at 460 cm<sup>&#x2212;1</sup>, 526 cm<sup>&#x2212;1</sup> and 617 cm<sup>&#x2212;1</sup>, associated with the dissolution of the zeolite phases, consistent with the XRD results (<xref ref-type="fig" rid="F0003">Fig. 3</xref>). It is likely that the highly alkaline environment promotes the dissolution of the SFCC initially through the breaking of Al-O bonds, considering that this type of bonds has a lower energy (&#x223C;60 kcal/mol) than Si-O bonds (&#x223C;80 kcal/mol) (<xref ref-type="bibr" rid="CIT0026">26</xref>).</p>
				<p>Bands at 1630 cm<sup>&#x2212;1</sup> and 3450 cm<sup>&#x2212;1</sup> in the activated pastes are attributed to bending (H&#x2013;O&#x2013;H) and stretching vibrations (&#x2013;OH) of water in the hydrated products, respectively (<xref ref-type="bibr" rid="CIT0027">27</xref>). The higher intensity of these bands in the alkali activated pastes, compared with the SFCC precursor, is consistent with more adsorbed water groups (&#x2261;Si-OH &#x2026; H<sub>2</sub>O and &#x2261;Al-OH &#x2026; H<sub>2</sub>O) in the aluminosilicate gel (<xref ref-type="bibr" rid="CIT0028">28</xref>).</p>
				<p>In samples with an Na<sub>2</sub>O/SiO<sub>2</sub> molar ratio of 0.20, a lower SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> ratio promotes shifting of the T-O-T band towards lower wavenumbers (1017 cm<sup>&#x2212;1</sup> for SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub>=2.4), suggesting the incorporation of higher contents of Al within the gel, compared with the samples activated with higher SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> ratio that show slight variations in the T-O-T band position (1022 cm<sup>&#x2212;1</sup> for SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub>=3.0). These results are consistent with the formation of a more Si-rich gel in the samples formulated with the highest SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> ratio. This is in agreement with the shifting of the band at 725 cm<sup>&#x2212;1</sup> towards higher wavenumbers at increased SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> ratios, as a consequence of the more Si-rich environment in the gel. The Si-O-T band is observed to be narrower and significantly more intense for the samples with SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> ratios of 2.4 and 2.6, because of the higher extent of dissolution of the SFCC, contributing more silicate and aluminate species for geopolymer gel formation. Similar trends are observed in specimens formulated with higher Na<sub>2</sub>O/SiO<sub>2</sub> ratios (0.25 and 0.30).</p>
				<p>At higher alkalinity conditions, associated with higher Na<sub>2</sub>O/SiO<sub>2</sub> ratios, the alkali content favors the initial dissolution of the aluminosilicate precursor and its consequent reaction to form the geopolymer product. This leads to the shifting of the main T-O-T band towards lower wavenumbers as identified in the activated specimens when compared with the unreacted SFCC. Conversely, at low alkalinity conditions a higher proportion of unreacted precursor is identified, as the T-O-T band of the SFCC does not exhibit variations in the activated samples.</p>
			</sec>
			<sec id="S20009">
				<title>3.4. <sup>29</sup>Si and <sup>27</sup>Al MAS NMR spectroscopy</title>
				<p>
					<xref ref-type="fig" rid="F0005">Figure 5</xref> shows the <sup>27</sup>Al MAS spectrum of the unreacted SFCC, with broad bands in the regions assigned to octahedrally (Al(VI)) (&#x2013;10 to 30 ppm), tetrahedrally (Al(IV)) (50 to 80 ppm), and minor pentahedrally (Al(V)) (30 to 50 ppm) coordinated Al environments. The intense peak in the 10 ppm region is mainly attributed to the octahedral aluminum species present in kyanite and sillimanite phases (<xref ref-type="bibr" rid="CIT0029">29</xref>), and extra-framework Al(VI) species in the dealuminated zeolites identified through XRD (<xref ref-type="fig" rid="F0001">Fig. 1</xref>). The resonance near 60 ppm is assigned to the tetrahedrally coordinated Al in the zeolites present in the SFCC (<xref ref-type="bibr" rid="CIT0030">30</xref>). The intensity at 45 ppm is ascribed to a less ordered framework where Al atoms are present in imperfectly crystalline zeolites. The FCC catalyst suffers hydrothermal dealumination through its use in the catalytic cracking process where up to 90% of the tetrahedrally-coordinated Al in the zeolite framework is removed, and consequently the bonds involving Al are replaced by hydroxyl groups linked to silicon (<xref ref-type="bibr" rid="CIT0031">31</xref>).</p>
				<fig id="F0005">
					<label>Figure 5</label>
					<caption>
						<p>
							<sup>27</sup>Al MAS NMR spectrum of the unreacted SFCC.</p>
					</caption>
					<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="MC201348-e046-g005.tif"/>
				</fig>
				<p>The <sup>29</sup>Si MAS spectrum of the unreacted SFCC (<xref ref-type="fig" rid="F0006">Fig. 6</xref>) shows a dominant resonance near &#x2013;105 ppm, attributed to the Q<sup>4</sup>(0Al) sites of the highly dealuminated faujasite resulting from the different stages in the cracker unit (<xref ref-type="bibr" rid="CIT0032">32</xref>), and also a contribution from quartz (&#x2013;107 ppm) as identified via XRD (<xref ref-type="fig" rid="F0001">Fig. 1</xref>). The asymmetry of this band suggests that it overlaps with a wide range of resonances from different Si-containing phases identified in the SFCC, and therefore cannot be attributed to a single phase.</p>
				<fig id="F0006">
					<label>Figure 6</label>
					<caption>
						<p>
							<sup>29</sup>Si MAS NMR spectrum of the unreacted SFCC.</p>
					</caption>
					<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="MC201348-e046-g006.tif"/>
				</fig>
				<p>The <sup>27</sup>Al MAS spectra of selected SFCC-based geopolymers (<xref ref-type="fig" rid="F0007">Fig. 7</xref>) show changes in the line shape compared with unreacted SFCC (<xref ref-type="fig" rid="F0005">Fig. 5</xref>). The Al(V) resonance observed between 30 and 50 ppm (<xref ref-type="fig" rid="F0007">Fig. 7</xref>) in the unreacted precursor completely disappears upon activation, consistent with the high reactivity of Al(V) sites. In alkali activation of aluminosilicates, it has been shown that Al(V) and Al(VI) are converted to tetrahedral sites (Al(IV)) with an associated alkali cation to maintain electroneutrality (<xref ref-type="bibr" rid="CIT0033">33</xref>).</p>
				<fig id="F0007">
					<label>Figure 7</label>
					<caption>
						<p>
							<sup>27</sup>Al MAS NMR spectra of SFCC geopolymers formulated with a SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> ratio of 2.4, as a function of Na<sub>2</sub>O/SiO<sub>2</sub> (N/S) ratio as marked.</p>
					</caption>
					<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="MC201348-e046-g007.tif"/>
				</fig>
				<p>A significant reduction of the Al(VI) band is identified in the activated SFCC, when compared with the unreacted SFCC, along with a significant increase in the intensity in the Al(IV) region of the spectra. The reduction in the intensity of the bands in the Al(VI) region is attributed to the dissolution of the dealuminated zeolite, leading to the formation of a highly crosslinked disordered aluminosilicate &#x2018;geopolymer&#x2019; gel, as identified by FTIR.</p>
				<p>Although the <sup>27</sup>Al MAS NMR spectra of the activated SFCC specimens are dominated by the resonance associated with Al(IV), a small resonance centered between 2 and 3 ppm is also observed in the spectra. This resonance corresponds to small amounts of Al(VI) from the residual mullite phase (<xref ref-type="bibr" rid="CIT0034">34</xref>), identified in the XRD after the activation (<xref ref-type="fig" rid="F0003">Fig. 3</xref>). The amount of Al(IV) increases as the alkali content (Na<sub>2</sub>O/SiO<sub>2</sub> ratio) increases from 0.20 to 0.30, in good agreement with the formation of a larger amount of aluminosilicate type gel, as observed via FTIR, and in good agreement with the decrease in intensity of the Al(VI) band remaining from unreacted material.</p>
				<p>The peak at &#x2013;105 ppm in the <sup>29</sup>Si MAS NMR spectrum of the unreacted SFCC (<xref ref-type="fig" rid="F0008">Fig. 8</xref>) is no longer identified in the geopolymer specimens, consistent with the dissolution of faujasite upon activation as observed via XRD (<xref ref-type="fig" rid="F0003">Fig. 3</xref>). The <sup>29</sup>Si MAS NMR spectra of the alkali activated SFCC binders (<xref ref-type="fig" rid="F0008">Fig. 8</xref>) show a broad band centered at &#x2013;91 ppm assigned to Q<sup>4</sup>(3Al) sites, consistent with the incorporation of Al in the geopolymer gel. The spectrum of activated SFCC is within the region assigned to Q<sup>4</sup>(4Al), Q<sup>4</sup>(3Al), Q<sup>4</sup>(2Al) and Q<sup>4</sup>(1Al) sites, overlapping with the sites in the residual unreacted precursor, which means that it is difficult to identify particular sites from the unreacted spent catalyst and the newly forming phases.</p>
				<fig id="F0008">
					<label>Figure 8</label>
					<caption>
						<p>
							<sup>29</sup>Si MAS NMR spectra of SFCC geopolymers formulated with a SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> ratio of 2.4, as function of the Na<sub>2</sub>O/SiO<sub>2</sub> (N/S) ratio.</p>
					</caption>
					<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="MC201348-e046-g008.tif"/>
				</fig>
				<p>Low alkali content (Na<sub>2</sub>O/SiO<sub>2</sub> of 0.20) promotes the broadening of the <sup>29</sup>Si MAS NMR spectrum, along with a low intensity shoulder between &#x2013;98 ppm and &#x2013;120 ppm, corresponding to the Q<sup>4</sup> sites of faujasite from the spent catalyst that are not completely consumed during the geopolymerisation process. Increasing the alkali content (higher Na<sub>2</sub>O/SiO<sub>2</sub>), the intensity of this shoulder is significantly reduced, confirming a higher extent of dissolution of faujasite from the SFCC at higher alkali content in the systems, as observed in the XRD results (<xref ref-type="fig" rid="F0003">Fig. 3</xref>). The main band also becomes slightly narrowed and more intense when the Na<sub>2</sub>O/SiO<sub>2</sub> ratio is increased from 0.20 to 0.30, indicating a higher degree of ordering of the gel formed, in good agreement with the <sup>27</sup>Al NMR results (<xref ref-type="fig" rid="F0007">Fig. 7</xref>).</p>
			</sec>
			<sec id="S20010">
				<title>3.5. Scanning electron microscopy</title>
				<p>
					<xref ref-type="fig" rid="F0009">Figure 9</xref> shows evident differences in the density, surface smoothness, and proportion of unreacted particles in activated SFCC as a function of formulation conditions, as a more homogeneous and dense microstructure is identified in specimens with increased SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> ratio. The visibly low densities exhibited by samples formulated with SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> of 2.0 and 2.2 are consistent with their low compressive strengths (<xref ref-type="fig" rid="F0002">Fig. 2</xref>), this can be associated with a low degree of reaction of the SFCC under these activation conditions. Although the highest mechanical strength is obtained in samples formulated with a SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> ratio of 2.4, its microstructure (<xref ref-type="fig" rid="F0009">Fig. 9C</xref>) is not as dense as in specimens formulated with a SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> ratio of 2.6 (<xref ref-type="fig" rid="F0009">Fig. 9D</xref>). This suggests that the materials might be more brittle at these activation conditions. Samples formulated with an SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> ratio greater than 2.6 (<xref ref-type="fig" rid="F0009">Figs. 9E</xref>, <xref ref-type="fig" rid="F0009">F</xref>) show large cracks associated with severe shrinkage, which can lead to the reduced mechanical strength observed at these activation conditions.</p>
				<fig id="F0009">
					<label>Figure 9</label>
					<caption>
						<p>SEM images of geopolymers formulated with an Na<sub>2</sub>O/SiO<sub>2</sub> molar ratio of 0.25, and SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> molar ratios of (A) 2.0 (B) 2.2 (C) 2.4 (D) 2.6, (E) 2.8 and (F) 3.0.</p>
					</caption>
					<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="MC201348-e046-g009.tif"/>
				</fig>
			</sec>
		</sec>
		<sec id="S0011" sec-type="conclusions">
			<title>4. CONCLUSIONS</title>
			<p>Geopolymers can be successfully produced from spent fluid catalytic cracking catalyst, which is available in high volumes in some parts of the world. Structural studies show that the alkali-activated SFCC pastes consist of an amorphous phase corresponding to an aluminosilicate &#x2018;geopolymer&#x2019; type gel, along with different types of zeolites, depending on the contents of silicates and alkalis available in the systems. The mechanical strength of the activated SFCC is strongly influenced by the formulation conditions, where optimal overall SiO<sub>2</sub>/Al<sub>2</sub>O<sub>3</sub> and Na<sub>2</sub>O/SiO<sub>2</sub> ratios of 2.4 and 0.25, respectively, promoting a compressive strength of up to 67 MPa. Insufficient alkali content in the formulated geopolymers retards the initial dissolution of the zeolite phases present in the SFCC, and consequently a higher proportion of unreacted precursor is identified in the samples activated with an Na<sub>2</sub>O/SiO<sub>2</sub> molar ratio of 0.20. These results elucidate that alkali-activation of SFCC is a viable method for managing and valorizing this industrial waste, with great potential for the production of ceramic-like materials with good mechanical performance.</p>
		</sec>
	</body>
	<back>
	<ack>
			<title>ACKNOWLEDGMENTS</title>
			<p>This study was sponsored by the <italic>Universidad del Valle</italic> (Colombia), the Center of Excellence of Novel Materials (CENM) and <italic>Colciencias</italic>. The authors would like to thank Drs. John Gehman and Rackel San Nicolas (U. Melbourne) for NMR data acquisition, and Prof. John L. Provis (U. Sheffield) for valuable discussions.</p>
		</ack>
		<ref-list>
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							<given-names>E.</given-names>
						</name>
					</person-group>
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