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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">MC202011_e215</article-id>
<article-id pub-id-type="doi">10.3989/mc.2020.04219</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Articles</subject>
</subj-group>
</article-categories>
<title-group>
<article-title>Influence of sawdust particle size on fired clay brick properties</article-title>
<trans-title-group xml:lang="es">
<trans-title>Influencia del tama&#x00F1;o de part&#x00ED;cula del serr&#x00ED;n en las propiedades de los ladrillos de arcilla quemada</trans-title>
</trans-title-group>
<alt-title alt-title-type="running-head">Influence of sawdust particle size on fired clay brick properties</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Thalmaier</surname>
<given-names>G.</given-names>
</name>
<xref ref-type="aff" rid="aff0001">a</xref>
<xref ref-type="corresp" rid="cor1">&#x002A;</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Cob&#x00EE;rzan</surname>
<given-names>N.</given-names>
</name>
<xref ref-type="aff" rid="aff0001">a</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Balog</surname>
<given-names>A.-A.</given-names>
</name>
<xref ref-type="aff" rid="aff0001">a</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Constantinescu</surname>
<given-names>H.</given-names>
</name>
<xref ref-type="aff" rid="aff0001">a</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Streza</surname>
<given-names>M.</given-names>
</name>
<xref ref-type="aff" rid="aff0002">b</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Nasui</surname>
<given-names>M.</given-names>
</name>
<xref ref-type="aff" rid="aff0001">a</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Neamtu</surname>
<given-names>B.V.</given-names>
</name>
<xref ref-type="aff" rid="aff0001">a</xref>
</contrib>
</contrib-group>
<aff id="aff0001"><label>a</label>Technical University of Cluj Napoca, Cluj, Romania</aff>
<aff id="aff0002"><label>b</label>National Institute for Research and Development of Isotopic and Molecular Technologies, Cluj-Napoca, Romania</aff>
<author-notes>
<corresp id="cor1"><label>&#x002A;</label><email xlink:href="Gyorgy.Thalmaier@sim.utcluj.ro">Gyorgy.Thalmaier@sim.utcluj.ro</email></corresp>
<fn><p><bold>ORCID ID:</bold> G. Thalmaier (<ext-link ext-link-type="uri" xlink:href="https://orcid.org/0000-0003-2762-6110">https://orcid.org/0000-0003-2762-6110</ext-link>); N. Cob&#x00EE;rzan (<ext-link ext-link-type="uri" xlink:href="https://orcid.org/0000-0002-6904-0436">https://orcid.org/0000-0002-6904-0436</ext-link>); A.-A. Balog (<ext-link ext-link-type="uri" xlink:href="https://orcid.org/0000-0002-3587-6438">https://orcid.org/0000-0002-3587-6438</ext-link>); H. Constantinescu (<ext-link ext-link-type="uri" xlink:href="https://orcid.org/0000-0003-3290-3290">https://orcid.org/0000-0003-3290-3290</ext-link>); M. Streza (<ext-link ext-link-type="uri" xlink:href="https://orcid.org/0000-0002-0030-8625">https://orcid.org/0000-0002-0030-8625</ext-link>); M. N&#x0103;sui (<ext-link ext-link-type="uri" xlink:href="https://orcid.org/0000-0002-4792-2032">https://orcid.org/0000-0002-4792-2032</ext-link>); B.V. Neam&#x021B;u (<ext-link ext-link-type="uri" xlink:href="https://orcid.org/0000-0003-0666-8303">https://orcid.org/0000-0003-0666-8303</ext-link>)</p></fn>
</author-notes>
<pub-date pub-type="epub">
<day>30</day>
<month>06</month>
<year>2020</year>
</pub-date>
<pub-date pub-type="collection">
<year>2020</year>
</pub-date>
<volume>70</volume>
<issue>338</issue>
<elocation-id content-type="doi">10.3989/mc.2020.04219</elocation-id>
<history>
<date date-type="received">
<day>27</day>
<month>03</month>
<year>2019</year>
</date>
<date date-type="accepted">
<day>01</day>
<month>10</month>
<year>2019</year>
</date>
<date date-type="Available on line">
<day>19</day>
<month>03</month>
<year>2020</year>
</date>
</history>
<permissions>
<copyright-statement>&#x00A9; 2020 CSIC</copyright-statement>
<copyright-year>2020</copyright-year>
<license license-type="open-access" xlink:href="https://creativecommons.org/licenses/by/4.0/">
<license-p>This is an open-access article distributed under the terms of the Creative Commons Attribution 4.0 International (CC BY 4.0) License.</license-p>
</license>
</permissions>
<abstract>
<title>ABSTRACT</title>
<p>This study investigates the effect of adding different size fractions of the same pore forming agent (sawdust) on the material&#x2019;s compressive strength and heat transfer. The samples were dry pressed and fired at high temperature inside an oven. Phase transformations were evidenced by a combination of differential thermal analysis, thermogravimetry and mass spectrometry (DTA-TGA-MS) and X-ray diffraction (XRD) techniques, in the temperature range of 24-900 &#x00BA;C. Image analysis (IA) and compression tests were performed to explain the mechanical behaviour of the samples. The thermal conductivity was obtained by using combined photopyroelectric calorimetry (PPE) and lock-in thermography (LIT) techniques. The pressing direction has an impact on the distribution of pores and the heat transfer by conduction.</p>
</abstract>
<trans-abstract xml:lang="es">
<title>RESUMEN</title>
<p><italic>Influencia del tama&#x00F1;o de part&#x00ED;cula del serr&#x00ED;n en las propiedades de los ladrillos de arcilla quemada.</italic> Este estudio investiga el efecto de la adici&#x00F3;n de diferentes fracciones de tama&#x00F1;o del mismo agente de formaci&#x00F3;n de poros (serr&#x00ED;n) sobre la resistencia a la compresi&#x00F3;n y la transferencia de calor del material. Las muestras fueron presionadas, secadas y cocidas a alta temperatura dentro de un horno. Se identificaron transformaciones de fase mediante el empleo de an&#x00E1;lisis t&#x00E9;rmico diferencial, termogravim&#x00E9;trico y espectrometria de masas (DTA-TGA-MS) y t&#x00E9;cnicas de difracci&#x00F3;n de rayos X (XRD) en el intervalo de temperatura de 24-900<sup>0</sup> C. Se realizaron an&#x00E1;lisis de imagen (IA) y ensayos de compresi&#x00F3;n para explicar el comportamiento mec&#x00E1;nico de las muestras. La conductividad t&#x00E9;rmica se obtuvo mediante el uso de t&#x00E9;cnicas combinadas de calorimetr&#x00ED;a fotopiroel&#x00E9;ctrica (PPE) y termografia de bloqueo (LIT). Se concluye que la direcci&#x00F3;n de prensado tiene un impacto sobre la distribuci&#x00F3;n de los poros y la transferencia de calor por conducci&#x00F3;n.</p>
</trans-abstract>
<kwd-group xml:lang="en">
<title>KEYWORDS</title>
<kwd>Brick</kwd>
<kwd>Compressive strength</kwd>
<kwd>Thermal analysis</kwd>
<kwd>Wood</kwd>
<kwd>Pore size distribution</kwd>
</kwd-group>
<kwd-group xml:lang="es">
<title>Palabras clave</title>
<kwd>Ladrillo</kwd>
<kwd>Resistencia a la compresi&#x00F3;n</kwd>
<kwd>An&#x00E1;lisis t&#x00E9;rmico</kwd>
<kwd>Madera</kwd>
<kwd>Distribuci&#x00F3;n de tama&#x00F1;o de poro</kwd>
</kwd-group>
</article-meta>
</front>
<body>
<sec id="sec1" sec-type="intro">
<title>1 . INTRODUCTION</title>
<p>Energy saving in buildings may be achieved by using materials with high thermal performance (<xref ref-type="bibr" rid="cit0001">1</xref>). The easiest way to improve the thermal performance of solid fired-clay bricks is to increase their porosity. It is well known that thermal conductivity and mechanical properties are strongly influenced by void fraction with a direct effect: an increase of the porosity increases thermal performance but decreases mechanical strength. This limits the maximum porosity to levels that ensures a reasonable mechanical strength, for specific application requirements in constructions (<xref ref-type="bibr" rid="cit0002">2</xref>-<xref ref-type="bibr" rid="cit0006">6</xref>). Principal factors which affect the materials values of thermal conductivity and mechanical strength are their microscopic and macroscopic structure (pore volume, size and shape), mineralogical composition and anisotropy (<xref ref-type="bibr" rid="cit0007">7</xref>-<xref ref-type="bibr" rid="cit0012">12</xref>).</p>
<p>For solid clay units the reduction of the thermal conductivity parameter may be obtained by incorporating different waste materials which play the role of pore-forming agents (<xref ref-type="bibr" rid="cit0006">6</xref>, <xref ref-type="bibr" rid="cit0013">13</xref>-<xref ref-type="bibr" rid="cit0018">18</xref>). The well-known pore forming agents&#x2019; materials incorporated up to now into clay matrix by scientific researchers are residual biomass (<xref ref-type="bibr" rid="cit0015">15</xref>, <xref ref-type="bibr" rid="cit0018">18</xref>), paper waste (<xref ref-type="bibr" rid="cit0006">6</xref>, <xref ref-type="bibr" rid="cit0016">16</xref>), vermiculite (<xref ref-type="bibr" rid="cit0019">19</xref>), etc.</p>
<p>An efficient pore forming agent is a building material with high content of organic matter, which has the role to improve the thermal properties of ceramic materials by increasing their porosity. One of the waste materials which can be used as an organic pore forming agent is sawdust. In the clay matrix it plays multiple roles: act as a pore forming agent which burns during the firing, increasing the porosity and reducing the thermal conductivity (<xref ref-type="bibr" rid="cit0012">12</xref>, <xref ref-type="bibr" rid="cit0015">15</xref>) of the final product and save energy in the manufacturing process, due to its high caloric power (15-20,5MJ/kg) (<xref ref-type="bibr" rid="cit0020">20</xref>).</p>
<p>Based on studies performed by other authors, sawdust content into the clay matrix is up to 30% (<xref ref-type="bibr" rid="cit0011">11</xref>, <xref ref-type="bibr" rid="cit0015">15</xref>, <xref ref-type="bibr" rid="cit0021">21</xref>-<xref ref-type="bibr" rid="cit0024">24</xref>), depending by the raw material characteristics.</p>
<p>Depending on the particle size, the sawdust in the firing process will develop in the clay matrix a network of different types of pores (capillary, subcapillary or microcapillary pores). In ceramic specimens these pores are supplementary to those resulted due to the clay&#x2019;s particle arrangement and those resulted during the chemical and mineralogical transformations which appear at different firing temperatures (<xref ref-type="bibr" rid="cit0012">12</xref>).</p>
<p>The study investigates the influence of sawdust particles size on mechanical and thermal properties of solid fired clay bricks, and the anisotropy of porosity and thermal conductivity measured in two directions (parallel and perpendicular to the pressing direction). The aim of the experimental study was to determine the influence of the pore size in improving the thermal properties of fired clay bricks while the mechanical properties are kept in acceptable limits.</p>
</sec>
<sec id="sec2">
<title>2. EXPERIMENTAL PROCEDURES</title>
<sec id="sec2.1">
<title>2.1. Sample preparation</title>
<p>The raw materials used for clay brick samples consists of clays (a mixture of yellow and grey clay, 30:70 ratio) and 15 vol.% sawdust sieved to different size fractions, as follows: &#x003C;0.2mm; 0.315 - 0.4mm; 0.5 - 0.63mm; 0.63 - 0.8mm; 0.8 - 1.2mm. The used percentage of sawdust was determined from preliminary experiments as being the 15 vol. % in order to keep the values of mechanical properties above the admissible value. Approximately 10 vol. % water was added to increase the presability of the mixture. The mixture has a wide size distribution with particle size &#x003C; 6 mm and D<sub>50</sub>~ 2mm, as presented in <xref ref-type="fig" rid="f0001">Figure 1a</xref>. The yellow and gray clays particles size distribution was measured by light scattering on a Fritsch Analysette 22 laser particle size analyser (<xref ref-type="fig" rid="f0001">Figure 1b,c</xref>).</p>
<fig id="f0001">
<label>Figure 1</label>
<caption><p>a) The press-ready mixture&#x2019;s particle size distribution obtained by sieving, the yellow b) and gray c) clays particle size distribution.</p></caption>
<graphic xlink:href="MC202011_e215-g001.tif" xmlns:xlink="http://www.w3.org/1999/xlink"/>
</fig>
<p>Beside the samples containing sawdust particles some control bricks were manufactured without pore forming agent. The samples were pressed at 20MPa in a hardened steel mould, the samples dimensions 15x15x15mm.</p>
<p>The heat cycle used for firing started with a slow heating rate (1.5 &#x00BA;/min) from room temperature to 90 &#x00BA;C and this temperature was maintained for 60 minutes for a thorough drying of the samples. The temperature was further increased at a rate of 5&#x00BA;/min up to 600&#x00BA;C then with 2&#x00BA;/min up to 900 &#x00BA;C where it was maintained for 2h. The cooling curve begins with a decrease (5 &#x00BA;/min) down to 670 &#x00BA;C, and then the cooling rate was decreased to 1.5&#x00BA;/min to avoid the cracking caused by the quartz phase transformation. After 570&#x00BA;C the samples were furnace cooled to room temperature.</p>
<p>The chemical and mineralogical analysis of samples were determined in a previous study (<xref ref-type="bibr" rid="cit0006">6</xref>).</p>
</sec>
<sec id="sec2.2">
<title>2.2. Investigation methods</title>
<sec id="s2b1">
<title>2.2.1. Method used</title>
<p>The phase transformations were evidenced in the 25-900 &#x00BA;C temperature range by a combination of X-ray diffraction (Equinox D3000 diffractometer with Co radiation) and DTA-TGA (10&#x00BA;/min - in air) thermal analysis combined with mass spectrometry.</p>
<p>The water absorption, bulk density and compressive strength were determined as the average values obtained on five cubic specimens 15x15x15mm.</p>
<p>First the samples were dried into an oven at 105&#x00BA;C &#x00B1; 5 &#x00B0;C until a constant mass, and then the water content of the specimens was expressed according to SR EN 772&#x2013;21: 2011 (<xref ref-type="bibr" rid="cit0025">25</xref>), as ratio between the wet and dried mass of the samples.</p>
<p>The bulk density of samples was calculated based on SR EN 772&#x2013;13:2001 (<xref ref-type="bibr" rid="cit0026">26</xref>) by measuring the samples dimensions and dividing the mass by the calculated volume. The material&#x2019;s density was measured by picnometry and used to determine the total porosity of the samples. The pore size distribution was measured by image analysis (on optical images using ImageJ software), the measured areas of the pores were transformed into equivalent diameters considering spherical pores with identical areas.</p>
<p>The total porosity was calculated P = (1- Bulk density/ Solid density) x100, where the solid density was measured in each case by pycnometry.</p>
<p>A Controls Advantest 9 hydraulic press with a load rate of 0.2 MPa/s, and the accuracy of the force recording of 0.01MPa, was used in order to determine the specimens&#x2019; compressive strengths.</p>
<p>The thermal effusivity of the samples was obtained by using the PPE technique in the front configuration (FPPE), while non-contact infrared lock-in thermography technique (LIT) was used to get their thermal diffusivity (<xref ref-type="bibr" rid="cit0027">27</xref>). Knowing the values of the thermal effusivity and thermal diffusivity, the thermal conductivity was calculated according to the following <xref ref-type="disp-formula" rid="eq1">Equation [1</xref>]:</p>
<disp-formula id="eq1">
<alternatives>
<mml:math id="M1">
<mml:mrow>
<mml:mtext>k</mml:mtext>
<mml:mo>=</mml:mo>
<mml:mi>e</mml:mi>
<mml:msup>
<mml:mrow>
<mml:mrow>
<mml:mo>(</mml:mo>
<mml:mi>&#x03B1;</mml:mi>
<mml:mo>)</mml:mo>
</mml:mrow>
</mml:mrow>
<mml:mrow>
<mml:mrow>
<mml:mn>1</mml:mn>
<mml:mo>/</mml:mo>
<mml:mn>2</mml:mn>
</mml:mrow>
</mml:mrow>
</mml:msup>
</mml:mrow>
</mml:math>
<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="MC202011_e215-eq1.tif"/>
</alternatives>
<label>1</label>
</disp-formula>
<p>where &#x03B1; is the thermal diffusivity, <italic>e</italic> is the thermal effusivity and <italic>k</italic> is the thermal conductivity of the investigated sample.</p>
</sec>
<sec id="s2b2">
<title>2.2.2. Theoretical aspects</title>
<p>The temperature variation of a sample exposed to a modulated radiation can be measured with a pyroelectric sensor. In the front detection configuration (FPPE) the sensor is first irradiated, and the investigated sample is placed directly on the pyroelectric sensor. For an optically opaque sensor, the radiation is absorbed on its front electrode and converted into heat. The developed heat propagates through both the sensor and the sample. Due to the thermal gradient between the two electrodes of the sensor, a complex electrical signal is generated. The amplitude and the phase of the signal depends on the thermal parameters of the sample. For a thermally thick sensor and sample, the phase of the PPE signal is given by <xref ref-type="disp-formula" rid="eq2">Equations [2</xref>] and [<xref ref-type="disp-formula" rid="eq3">3</xref>]:</p>
<disp-formula id="eq2">
<alternatives>
<mml:math id="M2">
<mml:mrow>
<mml:mtext>tan</mml:mtext>
<mml:mi>&#x0398;</mml:mi>
<mml:mo>=</mml:mo>
<mml:mfrac>
<mml:mrow>
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<mml:mrow>
<mml:mn>1</mml:mn>
<mml:mo>+</mml:mo>
<mml:msub>
<mml:mi>R</mml:mi>
<mml:mrow>
<mml:mi>m</mml:mi>
<mml:mi>p</mml:mi>
</mml:mrow>
</mml:msub>
</mml:mrow>
<mml:mo>)</mml:mo>
</mml:mrow>
<mml:mtext>exp</mml:mtext>
<mml:mrow>
<mml:mo>(</mml:mo>
<mml:mrow>
<mml:mo>&#x2212;</mml:mo>
<mml:mi>x</mml:mi>
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<mml:mn>1</mml:mn>
<mml:mo>&#x2212;</mml:mo>
<mml:mrow>
<mml:mo>(</mml:mo>
<mml:mrow>
<mml:mn>1</mml:mn>
<mml:mo>+</mml:mo>
<mml:msub>
<mml:mi>R</mml:mi>
<mml:mrow>
<mml:mtext>mp</mml:mtext>
</mml:mrow>
</mml:msub>
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<mml:mo>)</mml:mo>
</mml:mrow>
<mml:mtext>exp</mml:mtext>
<mml:mrow>
<mml:mo>(</mml:mo>
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</mml:mrow>
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</mml:mfrac>
</mml:mrow>
</mml:math>
<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="MC202011_e215-eq2.tif"/>
</alternatives>
<label>2</label>
</disp-formula>
<disp-formula id="eq3">
<alternatives>
<mml:math id="M3">
<mml:mrow>
<mml:mtext>with&#x00A0;</mml:mtext>
<mml:mi>x</mml:mi>
<mml:mo>=</mml:mo>
<mml:msub>
<mml:mi>a</mml:mi>
<mml:mi>p</mml:mi>
</mml:msub>
<mml:msub>
<mml:mi>L</mml:mi>
<mml:mi>p</mml:mi>
</mml:msub>
<mml:mtext>&#x00A0;and&#x00A0;</mml:mtext>
<mml:mfrac>
<mml:mrow>
<mml:msub>
<mml:mi>e</mml:mi>
<mml:mi>m</mml:mi>
</mml:msub>
</mml:mrow>
<mml:mrow>
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<mml:mi>e</mml:mi>
<mml:mi>p</mml:mi>
</mml:msub>
</mml:mrow>
</mml:mfrac>
<mml:mo>=</mml:mo>
<mml:mfrac>
<mml:mrow>
<mml:mn>1</mml:mn>
<mml:mo>+</mml:mo>
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<mml:mi>R</mml:mi>
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<mml:mi>m</mml:mi>
<mml:mi>p</mml:mi>
</mml:mrow>
</mml:msub>
</mml:mrow>
<mml:mrow>
<mml:mn>1</mml:mn>
<mml:mo>+</mml:mo>
<mml:msub>
<mml:mi>R</mml:mi>
<mml:mrow>
<mml:mi>m</mml:mi>
<mml:mi>p</mml:mi>
</mml:mrow>
</mml:msub>
</mml:mrow>
</mml:mfrac>
</mml:mrow>
</mml:math>
<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="MC202011_e215-eq3.tif"/>
</alternatives>
<label>3</label>
</disp-formula>
<p><italic>R<sub>mp</sub></italic> represents the reflection coefficient of the thermal wave at the interface material (m)- sensor (p), <italic>L<sub>p</sub></italic> is the thickness of the sensor, and <italic>a<sub>p</sub></italic> is the reverse of the thermal diffusion length (<italic>a<sub>p</sub> = 1/&#x03BC;</italic>). The thermal diffusion length is &#x03BC; <italic>= (</italic>&#x03B1;<italic>/&#x03C0;f)<sup>1/2</sup>
</italic> with <italic>f</italic> the modulation frequency.</p>
<p>The thermal effusivity of the sample can be measured by performing a frequency scan of the phase of the PPE signal, according to <xref ref-type="disp-formula" rid="eq2">Equations [2</xref>] &#x2013; [<xref ref-type="disp-formula" rid="eq3">3</xref>].</p>
<p>The thermal diffusivity of solid samples by using the lock-in thermography technique can be calculated from the shift of the phase (which is a time delay in the propagation of the thermal wave as compared to a reference signal). The phase shift &#x0394;&#x03D5; has the following expression [<xref ref-type="disp-formula" rid="eq4">4</xref>]:</p>
<disp-formula id="eq4">
<alternatives>
<mml:math id="M4">
<mml:mrow>
<mml:mi>&#x0394;</mml:mi>
<mml:mi>&#x03D5;</mml:mi>
<mml:mo>=</mml:mo>
<mml:msqrt>
<mml:mrow>
<mml:mfrac>
<mml:mrow>
<mml:mi>&#x03C0;</mml:mi>
<mml:mi>f</mml:mi>
</mml:mrow>
<mml:mi>&#x03B1;</mml:mi>
</mml:mfrac>
</mml:mrow>
</mml:msqrt>
<mml:mi>x</mml:mi>
<mml:mo>=</mml:mo>
<mml:mi>a</mml:mi>
<mml:mi>x</mml:mi>
</mml:mrow>
</mml:math>
<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="MC202011_e215-eq4.tif"/>
</alternatives>
<label>4</label>
</disp-formula>
<p>where x is the distance from the punctual heat source, <italic>a = 1/&#x03BC;</italic> is the slope of the phase versus distance plot and <italic>f</italic> is the excitation frequency. At a big distance from the punctual heat source, the thermal wave can be approximated by a plane wave and accordingly, the thermal diffusivity can thus be calculated according to <xref ref-type="disp-formula" rid="eq4">Equation [4</xref>].</p>
</sec>
</sec>
</sec>
<sec id="sec3" sec-type="results|discussion">
<title>3. RESULTS AND DISSCUSIONS</title>
<p>The XRD pattern of the starting mixture (<xref ref-type="fig" rid="f0002">Figure 2</xref>) consists of quartz, kaolinite, calcite, dolomite and some iron oxides. Part of these phases suffer transformations during the firing process.</p>
<fig id="f0002">
<label>Figure 2</label>
<caption><p>X ray diffraction (Q &#x2013;quartz, K- Kaolinite, Fe- iron oxides, C- calcite, D- dolomite, I- illite, S &#x2013;Iron silicon oxide).</p></caption>
<graphic xlink:href="MC202011_e215-g002.tif" xmlns:xlink="http://www.w3.org/1999/xlink"/>
</fig>
<p>Part of the phase transformations that occur during the firing process are associated with heat effects, so these transformations are also monitored by thermal analysis. The DTA-TGA curve is presented in <xref ref-type="fig" rid="f0003">Figure 3</xref>. The water evaporation, the carbonates decomposition and the burning of the added biomass are the main cause of weight loss in brick manufacturing.</p>
<fig id="f0003">
<label>Figure 3</label>
<caption><p>DTA-TGA-MS analysis of the starting mixture: a). DTA-TGA curve, b). CO<sub>2</sub> partial pressure variation.</p></caption>
<graphic xlink:href="MC202011_e215-g003.tif" xmlns:xlink="http://www.w3.org/1999/xlink"/>
</fig>
<p>The first effect visible in the TGA curve is a wide endothermic peak corresponding to the water evaporation. This water evaporation starts at temperatures over 50 &#x00B0;C and is still ongoing up to temperatures around 200 &#x00B0;C. The second effect present is a strong exothermic peak composed of several effects. The major effect is the burning of the sawdust particles in the 270&#x2013;620 &#x00B0;C temperature range. Over this range a smaller endothermic effect is overlapping, the kaolinite- metakaolinite transformation with the release of the OH<sup>-</sup> functional group. Further increasing the temperature, the carbonates&#x2019; decomposition begins. During firing, carbonates act as pore-forming agents and generate crystalline phases, which can enhance mechanical strength (<xref ref-type="bibr" rid="cit0028">28</xref>). The calcium carbonate that begins to decompose as the CO<sub>2</sub> partial pressure indicates, around 700&#x00B0;C and continues up to 860&#x00B0;C. These observations are similar with the findings of other authors on clays (<xref ref-type="bibr" rid="cit0029">29</xref>). No clear evidence of liquid forming was observed in the DTA-TGA analysis.</p>
<p>Samples contains no pore-forming agent except for the naturally occurring carbonates having densities of 1.69g/cm<sup>3</sup> (control sample-CS). By adding sawdust, the other samples had their density reduced by approximately 12-17% and are presented in <xref ref-type="table" rid="t0001">Table 1</xref>. Some scattering of the results was observed but they remained within acceptable limits and were due to the uneven nature of the naturally occurring materials.</p>
<table-wrap id="t0001">
<label>Table 1</label>
<caption><p>The obtained bulk density, water absorption and total porosity.</p></caption>
<table frame="hsides" rules="groups">
<thead>
<tr>
<th align="left">Sample</th>
<th align="center">Sawdust size fraction [mm]</th>
<th align="center">Bulk density [g/cm<sup>3</sup>]</th>
<th align="center">Water absorption [%]</th>
<th align="center">Total porosity [%]</th>
</tr>
</thead>
<tbody>
<tr>
<td align="left">CS</td>
<td align="center">-</td>
<td align="center">1,69</td>
<td align="center">18</td>
<td align="center">25</td>
</tr>
<tr>
<td align="left">M1</td>
<td align="center">&#x003C;0.2</td>
<td align="center">1,45</td>
<td align="center">23.7</td>
<td align="center">36</td>
</tr>
<tr>
<td align="left">M2</td>
<td align="center">0.315 - 0.4</td>
<td align="center">1,39</td>
<td align="center">22.6</td>
<td align="center">39</td>
</tr>
<tr>
<td align="left">M3</td>
<td align="center">0.5 - 0.63</td>
<td align="center">1,40</td>
<td align="center">24.4</td>
<td align="center">38</td>
</tr>
<tr>
<td align="left">M4</td>
<td align="center">0.63 - 0.8</td>
<td align="center">1,38</td>
<td align="center">23.1</td>
<td align="center">40</td>
</tr>
<tr>
<td align="left">M5</td>
<td align="center">0.8 - 1.2</td>
<td align="center">1,38</td>
<td align="center">24.5</td>
<td align="center">37</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>An increase of the total porosity by 11-13% was observed, some of the porosity was lost during the firing shrinkage.</p>
<p>The water absorption properties of bricks are a key factor that affects their durability and describes the open porosity through which water can pass. An important increase (~30%) in the water absorption was obtained by the addition of the sawdust and it is also visible in the total porosity increase. Most of the pores responsible for the water absorption are capillary pores which represent about 23% of the total volume. These pores are generated by two mechanisms: gas releases during the firing representing about 16% (5 % from water and 11 % from calcium carbonate) and 7% from the clay particle arrangement. The difference (up to total porosity) is given by the sawdust particles after burning.</p>
<p>The anisotropic nature of the sawdust particle gives another unusual effect in the samples; the orientation of the pore former in the die&#x2019;s filing direction. This effect was evidenced by measuring the porosity in the transversal and longitudinal direction by image analysis. The results are presented in <xref ref-type="fig" rid="f0004">Figure 4</xref>. Since the porosity is the main factor that affects the compressive strength and the thermal conductivity, it is important to take these variations into account.</p>
<fig id="f0004">
<label>Figure 4</label>
<caption><p>Examples of the variation of the porosity in transversal and longitudinal direction for sample M5 upper row and M2 lower row.</p></caption>
<graphic xlink:href="MC202011_e215-g004.tif" xmlns:xlink="http://www.w3.org/1999/xlink"/>
</fig>
<p>In the fired bricks, the carbonates from the raw materials and the interparticle voids are responsible for generating micrometer sized pores. The large pores generated by the burning of the organic particles create a pore network that can compromise the brick&#x2019;s properties by acting as a weak link. These large pores (millimetre sized), are easily visible by optical microscopy. Using the ImageJ software, the pore size distribution of the different samples was measured on transversal and longitudinal direction for five samples for each sample type. The results are presented in <xref ref-type="fig" rid="f0005">Figure 5</xref>.</p>
<fig id="f0005">
<label>Figure 5</label>
<caption><p>Porosity and pore size distribution obtained by image analysis on samples containing different fractions of sawdust particles.</p></caption>
<graphic xlink:href="MC202011_e215-g005.tif" xmlns:xlink="http://www.w3.org/1999/xlink"/>
</fig>
<p>The measured pore size fraction differs from the used sawdust particle at a first glance but is important to remember that the sawdust particles were separated by sieving, and during this process the particle passes through the mesh on its smallest section, and the image analysis in the used configuration measures all the pore&#x2019;s three dimensions. A gradual decrease of the pore size distribution is observed with the decrease of the used sawdust particles; in each case most of the pores have dimensions less than 0.5 mm. This can be explained by the elongated shape of the pores that varies from 0.3 up to 1 mm. Due to this variation the true dimensions of the pores vary from the calculated equivalent dimension.</p>
<p>Compressive strength on clay mixtures is between 7.9 MPa (M5) and 11.3 MPa (M1) (see <xref ref-type="fig" rid="f0006">Figure 6</xref>). One can observe a wide variation between samples for the same quantity of sawdust. Higher strengths occur in the case of samples M1, M2, which can be explained by the fact that the contact points between the clay particles are stronger and provide a better resistance to samples. As one can observe in <xref ref-type="fig" rid="f0004">Figure 4</xref> a pore network is formed around the clay agglomerates, which tend to act as weak links between them even after firing. This fact explains the reduction of the mechanical properties. The effect of the coarser particles is due to the less bonding bridges between the clay agglomerates, the number of the bonding areas increases as the sawdust particle size decreases.</p>
<fig id="f0006">
<label>Figure 6</label>
<caption><p>Compressive strength of the manufactured samples (a.) and its variation with the mean clay particle size to sawdust ratio (b.).</p></caption>
<graphic xlink:href="MC202011_e215-g006.tif" xmlns:xlink="http://www.w3.org/1999/xlink"/>
</fig>
<p>The thermal diffusivity of the pyroelectric sensor is independent on the thermal behaviour of the investigated sample. In this case, the sensor&#x2019;s thermal diffusivity is &#x03B1; = 1.1 x10<sup>-6</sup> m<sup>2</sup>/s, in good agreement with the literature. This result confirms the fact that the theoretical and the experimental conditions are fulfilled. The obtained results for the investigated samples (M1 - M5) are displayed in <xref ref-type="fig" rid="f0007">Figure 7</xref>. <xref ref-type="fig" rid="f0008">Figure 8</xref> shows the optimization of the fits performed in order to get the thermal effusivity. The correct value of the thermal effusivity minimizes the root mean square (RMS) of the experimental data performed with <xref ref-type="disp-formula" rid="eq1">Equation [1</xref>].</p>
<fig id="f0007">
<label>Figure 7</label>
<caption><p>Normalized FPPE phase as a function of chopping frequency for M5.</p></caption>
<graphic xlink:href="MC202011_e215-g007.tif" xmlns:xlink="http://www.w3.org/1999/xlink"/>
</fig>
<fig id="f0008">
<label>Figure 8</label>
<caption><p>Root mean square deviation of the fit performed with <xref ref-type="disp-formula" rid="eq1">Equation [1</xref>] on the experimental data (PPE phase as a function of chopping frequency), with sample&#x2019;s thermal effusivity as a fit parameter. The minimum of the curve indicates the value of the thermal effusivity.</p></caption>
<graphic xlink:href="MC202011_e215-g008.tif" xmlns:xlink="http://www.w3.org/1999/xlink"/>
</fig>
<p><bold>IR investigations:</bold> The DC amplitude and phase images, together with the corresponding profiles are shown in <xref ref-type="fig" rid="f0009">Figures 9</xref>-<xref ref-type="fig" rid="f0011">11</xref>. The DC and the amplitude images show the dissipation of the heat at the surface of the sample, due to the absorption of the laser. The profiles are quite smooth and thus the emissivity of the investigated surface can be assumed to be constant. The average temperature of the surface has increased from 26 <sup>&#x00B0;</sup>C up to 41 <sup>&#x00B0;</sup>C (see <xref ref-type="fig" rid="f0010">Figure 10</xref>). The profile of the phase image shows that the thermal wave diffuses to the surface of the sample symmetrically with respect to the excitation source (the laser is targeted close to the pixel 170 on the IR images). The thermal wave spreads over a distance of about 1.5 mm around the excitation source. The disturbance of the thermal wave (see the phase profile, around pixel 210) reveals the presence of a small pore located on the surface of the sample M2. The thermal diffusivity of the samples was calculated from phase profiles, according to <xref ref-type="disp-formula" rid="eq4">Equation [4</xref>].</p>
<fig id="f0009">
<label>Figure 9</label>
<caption><p>DC image (left) and the amplitude profile along the marked line (right) for M2.</p></caption>
<graphic xlink:href="MC202011_e215-g009.tif" xmlns:xlink="http://www.w3.org/1999/xlink"/>
</fig>
<fig id="f0010">
<label>Figure 10</label>
<caption><p>Amplitude image (left) and the amplitude profile along the marked line (right) for M2.</p></caption>
<graphic xlink:href="MC202011_e215-g010.tif" xmlns:xlink="http://www.w3.org/1999/xlink"/>
</fig>
<fig id="f0011">
<label>Figure 11</label>
<caption><p>Phase image (left) and the amplitude profile along the marked line (right) for M2.</p></caption>
<graphic xlink:href="MC202011_e215-g011.tif" xmlns:xlink="http://www.w3.org/1999/xlink"/>
</fig>
<p>The obtained results with the associated standard deviations are listed in <xref ref-type="table" rid="t0002">Table 2</xref>. The thermal effusivity was measured for all four transversal sections of a cubic specimen and the average value was calculated. The thermal diffusivity was taken on the same surface, at four different points, and the mean value was calculated.</p>
<table-wrap id="t0002">
<label>Table 2</label>
<caption><p>Thermal conductivities of fired clay bricks in parallel and perpendicular directions.</p></caption>
<table frame="hsides" rules="groups">
<thead>
<tr>
<th align="left">Sample</th>
<th align="center">k&#x22A5;</th>
<th align="center">k<sub>//</sub></th>
<th align="center">(k<sub>//</sub>)/(k&#x22A5;)</th>
</tr>
</thead>
<tbody>
<tr>
<td align="left">M1</td>
<td align="center">0.50&#x00B1;0.05</td>
<td align="center">0.58&#x00B1;0.05</td>
<td align="center">1.16</td>
</tr>
<tr>
<td align="left">M2</td>
<td align="center">0.57&#x00B1;0.06</td>
<td align="center">0.62&#x00B1;0.04</td>
<td align="center">1.08</td>
</tr>
<tr>
<td align="left">M3</td>
<td align="center">0.58&#x00B1;0.06</td>
<td align="center">0.63&#x00B1;0.05</td>
<td align="center">1.06</td>
</tr>
<tr>
<td align="left">M4</td>
<td align="center">0.49&#x00B1;0.05</td>
<td align="center">0.53&#x00B1;0.04</td>
<td align="center">1.08</td>
</tr>
<tr>
<td align="left">M5</td>
<td align="center">0.49&#x00B1;0.04</td>
<td align="center">0.54&#x00B1;0.04</td>
<td align="center">1.1</td>
</tr>
<tr>
<td align="left">CS</td>
<td align="center">0.69&#x00B1;0.04</td>
<td align="center">0.69&#x00B1;0.06</td>
<td align="center">1</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>The thermal conductivity values lie between 0.69W/mK (the control sample) and 0.49W/mK. The thermal conductivity of the samples containing pore-forming agent decreases by 30% compared to the reference sample. At the same time, the samples (M4 and M5) containing the sawdust particles with bigger size (0.6mm&#x00F7;1.2mm) have a slightly lower conductivity (k=0.49 W/mK) compared to M2 and M3 samples (k=0.58W/mK) which contain the same percentage of pore-forming agent with smaller size (0.3mm&#x00F7;0.6mm). May be observed that thermal conductivity coefficient is lower for samples with large particle size of sawdust which are in accordance with other authors observations (<xref ref-type="bibr" rid="cit0012">12</xref>, <xref ref-type="bibr" rid="cit0023">23</xref>).</p>
<p>In the sections perpendicular to the pressing plane (transversal sections) the pore distribution is slightly larger than in the longitudinal direction (parallel with respect to the pressing plane), and the pores are quite elongated. Nevertheless, only a slight anisotropy in the thermal conductivity is revealed, as shown in <xref ref-type="table" rid="t0002">Table 2</xref>. The heat flow is privileged in the parallel direction due to a slightly higher thermal conductivity. Compared to extruded bricks the ratio k<sub>//</sub>/k&#x22A5; &#x2245; 1.1 for conventional bricks is in the range 1.08-1.9 obtained by authors (<xref ref-type="bibr" rid="cit0007">7</xref>,<xref ref-type="bibr" rid="cit0011">11</xref>). Anisotropy of the sample appear due to the pore forming agent and clay layers orientation which affect the thermal and mechanical properties of pressed (<xref ref-type="bibr" rid="cit0010">10</xref>) and extruded clay bricks (<xref ref-type="bibr" rid="cit0007">7</xref>, <xref ref-type="bibr" rid="cit0008">8</xref>, <xref ref-type="bibr" rid="cit0011">11</xref>).</p>
</sec>
<sec id="sec4" sec-type="conclusions">
<title>4. CONCLUSIONS</title>
<p>Room temperature X-ray diffraction shows that the starting crystalline phases are quartz, kaolinite, calcite, dolomite and some iron oxides. High temperature X-ray diffraction combined with the DTA-TGA-MS analysis shows that these phases are subjected to different transformations as follows: quartz suffers a transformation phase around 580&#x00B0;C, followed by the beginning of the dehydration of kaolinite. Around 720&#x00B0;C a sharp rise in the CO<sub>2</sub> partial pressure is observable in the MS curve correlated with a mass loss which corresponds to the calcite decomposition. Further increasing the temperature another peak in the CO<sub>2</sub> partial pressure is observable corresponding to the dolomite&#x2019;s decomposition. In the fired samples the different crystalline phases are present. The silicon dioxide reacts with the aluminum oxide (and forms mullite and illite), incorporating different other cations, some quartz reacts with the iron and forms iron silicon dioxide. A significant quantity of iron oxide remains for the samples to have the specific reddish color.</p>
<p>The optical microscopy shows the formation of a high porosity pore network, significantly reducing the mechanical properties. A difference in the porosity determined by optical microscopy was observed along the length of the scaled down brick due to the anisotropic shape of the sawdust particles.</p>
<p>The pores size distribution measured by image analysis shows a decreasing trend with the decrease of the used sawdust particle size range. Water absorption and total porosity variation with particle size range is in the range of the experimental uncertainties, no clear trend is observable. Since the determining parameter is the porosity not the pore size distribution.</p>
<p>The effect of anisotropy in thermal transport is insignifiant for conventional bricks, compared to ceramic block obtained by extrusion. The thermal conductivity is about 10% smaller in the perpendicular direction than in the longitudinal one. Thus, the laying directions of conventional bricks to the wall geometry is not critical such as the bricks obtained by extrusion.</p>
<p>On the other hand, the compressive strength follows a linear decrease due to the formation of the weak links between the clay particles. By increasing the sawdust particles size, the bigger pores act as more intense crack initiation sites, drastically reducing the samples compressive strength. Compared to the mean particle size of the starting mixture (d<sub>50</sub>=2.1 mm) one can observe that the compressive strength increases with the increase of the clay particle/sawdust particle ratio.</p>
</sec>
</body>
<back>
<ack>
<title>ACKNOWLEDGMENTS</title>
<p>This work was supported by the Romanian National Authority for Scientific Research and Innovation, CNCS/CCCDI &#x2013; UEFISCDI, project number PN-III-P2-2.1-BG-2016-0203, within PNCDI III, contract no. 71BG/2016.</p>
</ack>
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