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<article article-type="research-article" dtd-version="1.0" specific-use="sps-1.6" 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">dyna</journal-id>
			<journal-title-group>
				<journal-title>DYNA</journal-title>
				<abbrev-journal-title abbrev-type="publisher">Dyna rev.fac.nac.minas</abbrev-journal-title>
			</journal-title-group>
			<issn pub-type="ppub">0012-7353</issn>
			<publisher>
				<publisher-name>Universidad Nacional de Colombia</publisher-name>
			</publisher>
		</journal-meta>
		<article-meta>
			<article-id pub-id-type="doi">10.15446/dyna.v85n204.67589</article-id>
			<article-categories>
				<subj-group subj-group-type="heading">
					<subject>Artículos</subject>
				</subj-group>
			</article-categories>
			<title-group>
				<article-title>Analysis of pressure and pressure derivative interference tests under linear and spherical flow conditions</article-title>
				<trans-title-group xml:lang="es">
					<trans-title>Análisis de presión y derivada de presión en pruebas de interferencia en condiciones de flujos lineal y esférico</trans-title>
				</trans-title-group>
			</title-group>
			<contrib-group>
				<contrib contrib-type="author">
					<name>
						<surname>Escobar-Macualo</surname>
						<given-names>Freddy Humberto</given-names>
					</name>
					<xref ref-type="aff" rid="aff1"><sup>a</sup></xref>
				</contrib>
				<contrib contrib-type="author">
					<name>
						<surname>Rojas-Borrego</surname>
						<given-names>Esteban</given-names>
					</name>
					<xref ref-type="aff" rid="aff1"><sup>a</sup></xref>
				</contrib>
				<contrib contrib-type="author">
					<name>
						<surname>Alarcón-Olaya</surname>
						<given-names>Neila Tatiana</given-names>
					</name>
					<xref ref-type="aff" rid="aff1"><sup>a</sup></xref>
				</contrib>
				<aff id="aff1">
					<label>a</label>
					<institution content-type="original"> Grupo de Investigación GIPE de la Facultad de Ingeniería, Universidad Surcolombiana, Neiva, Colombia. fescobar@usco.edu.co, rojasborrego@gmail.com, ntalarcon123@gmail.com </institution>
					<institution content-type="normalized">Universidad Surcolombiana</institution>
					<institution content-type="orgdiv1">Facultad de Ingeniería</institution>
					<institution content-type="orgname">Universidad Surcolombiana</institution>
					<addr-line>
						<named-content content-type="city">Neiva</named-content>
					</addr-line>
					<country country="CO">Colombia</country>
					<email>fescobar@usco.edu.co</email>
					<email>rojasborrego@gmail.com</email>
					<email>ntalarcon123@gmail.com</email>
				</aff>
			</contrib-group>
			<pub-date pub-type="epub-ppub">
				<season>Jan-Mar</season>
				<year>2018</year>
			</pub-date>
			<volume>85</volume>
			<issue>204</issue>
			<fpage>44</fpage>
			<lpage>52</lpage>
			<history>
				<date date-type="received">
					<day>08</day>
					<month>09</month>
					<year>2017</year>
				</date>
				<date date-type="rev-recd">
					<day>30</day>
					<month>10</month>
					<year>2017</year>
				</date>
				<date date-type="accepted">
					<day>11</day>
					<month>11</month>
					<year>2017</year>
				</date>
			</history>
			<permissions>
				<license license-type="open-access" xlink:href="http://creativecommons.org/licenses/by-nc-nd/4.0/" xml:lang="en">
					<license-p>This is an open-access article distributed under the terms of the Creative Commons Attribution License</license-p>
				</license>
			</permissions>
			<abstract>
				<title>Abstract</title>
				<p>Often, interpretation of interference tests is performed for systems acting under radial flow regimen conditions by means of conventional straight-line method, type-curve matching and <italic>TDS</italic> technique. For linear and spherical flow cases, the interpretation of interference tests is performed by the conventional analysis and type-curve matching. These procedures do not allow verification of the estimated parameters; therefore, this paper presents the formulation of a more practical, useful and accurate methodology which is achieved based upon the determination of characteristic features found on the pressure and pressure derivative versus time log-log plot with the purpose of developing analytical expressions for the interpretation of interference tests under spherical and linear flow conditions. These equations were successfully verified by their application on synthetic tests.</p>
			</abstract>
			<trans-abstract xml:lang="es">
				<title>Resumen</title>
				<p>Normalmente, la interpretación de las pruebas de interferencia se realiza en sistemas que actúan bajo condiciones de régimen flujo radial utilizando análisis convencional de la línea recta, curvas tipo y técnica <italic>TDS</italic>. Para los casos de flujos lineal y esférico, la interpretación de pruebas de interferencia se realiza mediante el método convencional y el ajuste con curvas tipo. Estos procedimientos no permiten verificación de los parámetros estimados, y por ello en este trabajo se presenta una formulación de una metodología más práctica, útil y práctica mediante el uso de rasgos características en el gráfico logarítmico de la presión y derivada de presión contra tiempo, que permitan desarrollar expresiones analíticas directas usadas para la caracterización del yacimiento en pruebas interferencia en condiciones de flujos esférico y lineal. Estas ecuaciones se verificaron satisfactoriamente mediante a su aplicación a pruebas sintéticas. </p>
			</trans-abstract>
			<kwd-group xml:lang="en">
				<title>Keywords:</title>
				<kwd>interference testing</kwd>
				<kwd>linear flow</kwd>
				<kwd>spherical flow</kwd>
				<kwd>steady state</kwd>
				<kwd>pseudosteady state</kwd>
			</kwd-group>
			<kwd-group xml:lang="es">
				<title>Palabras clave:</title>
				<kwd>pruebas de interferencia</kwd>
				<kwd>flujo lineal</kwd>
				<kwd>flujo esférico</kwd>
				<kwd>estado estable</kwd>
				<kwd>estado pseudoestable</kwd>
			</kwd-group>
			<counts>
				<fig-count count="12"/>
				<table-count count="4"/>
				<equation-count count="49"/>
				<ref-count count="19"/>
				<page-count count="9"/>
			</counts>
		</article-meta>
	</front>
	<body>
		<sec sec-type="intro">
			<title>1. Introducción</title>
			<p>Normally, the methods used for interference tests interpretation are type-curve matching and the conventional straight-line method. In the study by [<xref ref-type="bibr" rid="B11">11</xref>] on water flow in aquifers and its influence on water-producing wells, he took the first steps in developing a graphical analysis method that intermediate the field data and the theoretical data for radial regime, which is known as type-curve matching method. Later [<xref ref-type="bibr" rid="B2">2</xref>,<xref ref-type="bibr" rid="B12">12</xref>,<xref ref-type="bibr" rid="B15">15</xref>,<xref ref-type="bibr" rid="B18">18</xref>], among others, improved this form of analysis for interference tests by involving either conventional analysis or the pressure derivative function. Type-curve matching is not only tedious but highly inaccurate with a slight data point reading variation.</p>
			<p>The first application of the pressure derivative in interference tests was done by [<xref ref-type="bibr" rid="B18">18</xref>]. This method did not have much impact at first because it made use of the arithmetic derivative and secondly the noise introduced to the pressure data by external sources increased with the derivative and before the 90s there was not many studies with the estimate of the pressure derivative function. A subsequent analysis was performed by [<xref ref-type="bibr" rid="B5">5</xref>], taking as reference the work done by [<xref ref-type="bibr" rid="B18">18</xref>] for two-rate testing.</p>
			<p>[<xref ref-type="bibr" rid="B13">13</xref>] presented the analytical models for radial, linear and spherical flow regimes and used type-curve matching and regression analysis for the interpretation of interference tests. In addition to presenting the analytical interference solution for radial flow regime, [<xref ref-type="bibr" rid="B13">13</xref>] also presented the solutions for linear and spherical flow regimes. The first one occurs in elongated deposits caused by channeling or faulting and the second one in very thick formations. [<xref ref-type="bibr" rid="B17">17</xref>] followed the philosophy of the <italic>TDS</italic> Technique, [<xref ref-type="bibr" rid="B19">19</xref>], for interference testing using the intersection between pressure and pressure derivative. Later, these recently mentioned works were applied by [<xref ref-type="bibr" rid="B7">7</xref>] to determine heterogeneities from interference testing. <italic>TDS</italic> Technique has many applications, just to name a few of them, [<xref ref-type="bibr" rid="B6">6</xref>] and [<xref ref-type="bibr" rid="B8">8</xref>] extended this methodology for interpreting pressure tests in elongated systems, and [<xref ref-type="bibr" rid="B14">14</xref>] developed the <italic>TDS</italic> for heavy oil obeying power-law behavior. Much more applications of the <italic>TDS</italic> Technique were compiled by [<xref ref-type="bibr" rid="B9">9</xref>]. </p>
			<p>Formulating a more practical interpretation methodology for interpretation of interference tests under linear and spherical conditions is the purpose of this paper. For this, the starting points are the linear and spherical solutions presented by [<xref ref-type="bibr" rid="B13">13</xref>] so the behavior of pressure and the pressure derivative curves are generated, and, from observations at characteristic points analytical expressions are developed to allow interpreting interference tests in a simple, practical and accurate way. Additionally, based on the work of [<xref ref-type="bibr" rid="B3">3</xref>,<xref ref-type="bibr" rid="B10">10</xref>], the presence of either pseudosteady-state or steady-state periods was used to develop expressions for the determination of the well drainage area when the duration of the test allows it. The expressions developed were verified satisfactorily with their application to synthetic tests.</p>
		</sec>
		<sec>
			<title>2. Mathematical model</title>
			<p>For the development of the TDS Technique, [<xref ref-type="bibr" rid="B19">19</xref>], in interference tests where either linear or spherical conditions are presented, it is necessary to understand the pressure and pressure derivative behavior in each system with the purpose of finding special features or straight lines which allow obtaining mathematical expressions for reservoir characterization.</p>
			<sec>
				<title>2.1. Lineal flow regime model</title>
				<p>[<xref ref-type="bibr" rid="B16">16</xref>] presented the solution for the pressure distribution in linear systems. This solution was considered for the case of a well producing a constant flow and infinite system. In addition, for an interference test, it was assumed that only half of the active well flow rate is perceived in the observer well. The pressure drop for the described condition is:</p>
				<p>
					<disp-formula id="e1">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e1.jpg"/>
					</disp-formula>
				</p>
				<p>And the pressure derivative is given by:</p>
				<p>
					<disp-formula id="e2">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e2.jpg"/>
					</disp-formula>
				</p>
				<p>The dimensionless parameters are given as:</p>
				<p>
					<disp-formula id="e3">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e3.jpg"/>
					</disp-formula>
				</p>
				<p>
					<disp-formula id="e4">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e4.jpg"/>
					</disp-formula>
				</p>
				<p>
					<disp-formula id="e5">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e5.jpg"/>
					</disp-formula>
				</p>
				<p>
					<xref ref-type="disp-formula" rid="e1">Eqs. (1)</xref> and <xref ref-type="disp-formula" rid="e2">(2)</xref> allowed generating several pressure and pressure curves as given in <xref ref-type="fig" rid="f1">Fig. 1</xref> using data from <xref ref-type="table" rid="t1">Table 1</xref>. As either the reservoir width, <italic>b</italic>, or the distance between the wells, <italic>L</italic>, or the reservoir thickness, <italic>h</italic>, varies so do the pressure and pressure derivative curves; therefore, a unique behavior was obtained after multiplying both dimensionless pressure and pressure derivative and dimensionless time values by certain parameters as shown in <xref ref-type="fig" rid="f2">Fig. 2</xref>. Notice in <xref ref-type="disp-formula" rid="e3">Eq. (3)</xref> that the squared wellbore radius can be changed by drainage area obtained the dimensionless time based on area, <sub>
 <sup>
 <italic>tDA</italic>
</sup> 
</sub> .</p>
				<p>
					<fig id="f1">
						<label>Figure 1</label>
						<caption>
							<title>Dimensionless pressure and pressure derivative behavior for interference tests under linear flow conditions</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-204-00044-gf1.jpg"/>
						<attrib><bold>Source:</bold> The authors</attrib>
					</fig>
				</p>
				<p>
					<table-wrap id="t1">
						<label>Table 1</label>
						<caption>
							<title>Input data for generating data in <xref ref-type="fig" rid="f1">Figure 1</xref>.</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-204-00044-gt1.jpg"/>
						<table-wrap-foot>
							<fn id="TFN1">
								<p><bold>Source:</bold> The authors</p>
							</fn>
						</table-wrap-foot>
					</table-wrap>
				</p>
				<p>
					<fig id="f2">
						<label>Figure 2</label>
						<caption>
							<title>Unified pressure derivative behavior interference tests under linear flow conditions</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-204-00044-gf2.jpg"/>
						<attrib><bold>Source:</bold> The authors</attrib>
					</fig>
				</p>
				<p>From the unified behavior observed in <xref ref-type="fig" rid="f2">Fig. 2</xref>, a unique intersection point with coordinates 270869.0956, 0.1006 is found:</p>
				<p>
					<disp-formula id="e6">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e6.jpg"/>
					</disp-formula>
				</p>
				<p>After replacing the dimensionless time and the definition of dimensionless length, <sub>
 <sup>
 <italic>xD</italic>
</sup> 
</sub> =<italic>x</italic>/<italic>L</italic>, in <xref ref-type="disp-formula" rid="e6">Eq. (6)</xref>, an expression to find porosity was obtained:</p>
				<p>
					<disp-formula id="e7">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e7.jpg"/>
					</disp-formula>
				</p>
				<p>The abscise value was:</p>
				<p>
					<disp-formula id="e8">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e8.jpg"/>
					</disp-formula>
				</p>
				<p>From which permeability is solved for once <xref ref-type="disp-formula" rid="e4">Eq. (4)</xref> and <sub>
 <sup>
 <italic>xD</italic>
</sup> 
</sub> , are replaced in the above expression:</p>
				<p>
					<disp-formula id="e9">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e9.jpg"/>
					</disp-formula>
				</p>
				<p>Since the pressure and pressure derivative values are the same, <xref ref-type="disp-formula" rid="e9">Eq. (9)</xref> can also use the pressure derivative value, instead.</p>
				<p>The governing equation for the unique linear flow regime was obtained by regression analysis to be: </p>
				<p>
					<disp-formula id="e10">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e10.jpg"/>
					</disp-formula>
				</p>
				<p>Replacing the dimensionless parameters in <xref ref-type="disp-formula" rid="e10">Eq. (10)</xref> is possible to obtain an expression to find permeability using an arbitrary point during linear flow regime:</p>
				<p>
					<disp-formula id="e11">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e11.jpg"/>
					</disp-formula>
				</p>
				<p>Because of the noise introduced to the pressure readings from external sources, it is recommended to read the pressure derivative value during linear flow at a time, <italic>t</italic> = 1 hr, to obtain a more representative reading value, then, Equation (11) becomes:</p>
				<p>
					<disp-formula id="e12">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e12.jpg"/>
					</disp-formula>
				</p>
				<p>The dimensionless pressure governing was found by integration of <xref ref-type="disp-formula" rid="e11">Eq. (10)</xref>; therefore:</p>
				<p>
					<disp-formula id="e13">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e13.jpg"/>
					</disp-formula>
				</p>
				<p>Dividing <xref ref-type="disp-formula" rid="e13">Eq. (13)</xref> by <xref ref-type="disp-formula" rid="e10">Eq. (10)</xref>, and solving for the linear skin factor and replacing the dimensionless quantities, it yields:</p>
				<p>
					<disp-formula id="e14">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e14.jpg"/>
					</disp-formula>
				</p>
			</sec>
			<sec>
				<title>2.2. Spherical flow regime model</title>
				<p>The governing pressure drop equation for a well producing a constant flow was given by [<xref ref-type="bibr" rid="B4">4</xref>] when spherical flow is developed in a reservoir is given by:</p>
				<p>
					<disp-formula id="e15">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e15.jpg"/>
					</disp-formula>
				</p>
				<p>Its pressure derivative is then:</p>
				<p>
					<disp-formula id="e16">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e16.jpg"/>
					</disp-formula>
				</p>
				<p>As for the former case, pressure and pressure derivative curves were generated, for this case with data from <xref ref-type="table" rid="t2">Table 2</xref>, considering the variation of wellbore radius, <sub>
 <sup>
 <italic>rw</italic>
</sup> 
</sub> , reservoir thickness, <italic>h</italic>, and distance between wells, <italic>r</italic>. Such curves are reported in <xref ref-type="fig" rid="f3">Fig. 3</xref>.</p>
				<p>
					<table-wrap id="t2">
						<label>Table 2</label>
						<caption>
							<title>Input data for generating data in <xref ref-type="fig" rid="f3">Figure 3</xref>.</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-204-00044-gt2.jpg"/>
						<table-wrap-foot>
							<fn id="TFN2">
								<p><bold>Source:</bold> The authors</p>
							</fn>
						</table-wrap-foot>
					</table-wrap>
				</p>
				<p>
					<fig id="f3">
						<label>Figure 3</label>
						<caption>
							<title>Dimensionless pressure and pressure derivative behavior for interference tests under spherical flow conditions</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-204-00044-gf3.jpg"/>
						<attrib><bold>Source:</bold> The authors</attrib>
					</fig>
				</p>
				<p>It was also necessary to unify the pressure derivative curves to obtain a universal behavior. It was performed by multiplying both dimensionless pressure, pressure derivative and time for certain factors as shown in <xref ref-type="fig" rid="f4">Fig. 4</xref>. </p>
				<p>
					<fig id="f4">
						<label>Figure 4</label>
						<caption>
							<title>Unified pressure derivative behavior interference tests under spherical flow conditions</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-204-00044-gf4.jpg"/>
						<attrib><bold>Source:</bold> The authors</attrib>
					</fig>
				</p>
				<p>From the unified behavior observed in <xref ref-type="fig" rid="f4">Fig. 4</xref> a unique intersection point with coordinates 0.029163, 0.17513 is found. Therefore<bold>,</bold> </p>
				<p>
					<disp-formula id="e17">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e17.jpg"/>
					</disp-formula>
				</p>
				<p>From which porosity is obtained once the dimensionless quantities are used:</p>
				<p>
					<disp-formula id="e18">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e18.jpg"/>
					</disp-formula>
				</p>
				<p>and;</p>
				<p>
					<disp-formula id="e19">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e19.jpg"/>
					</disp-formula>
				</p>
				<p>After replacing <xref ref-type="disp-formula" rid="e4">Eq. (4)</xref>, the definition of dimensionless radius and solving for the formation permeability, it yields.</p>
				<p>
					<disp-formula id="e20">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e20.jpg"/>
					</disp-formula>
				</p>
				<p>Since the pressure and pressure derivative values are the same, <xref ref-type="disp-formula" rid="e20">Eq. (20)</xref> can use the pressure derivative value, instead.</p>
				<p>The governing universal equation for spherical flow was obtained by linear regression to be:</p>
				<p>
					<disp-formula id="e21">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e21.jpg"/>
					</disp-formula>
				</p>
				<p>Replacing the dimensionless parameters in <xref ref-type="disp-formula" rid="e21">Eq. (21)</xref>, it is possible to obtain an expression to find permeability using an arbitrary point during linear flow regime:</p>
				<p>
					<disp-formula id="e22">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e22.jpg"/>
					</disp-formula>
				</p>
				<p>As for the linear case, because of the noise, it is recommended to apply <xref ref-type="disp-formula" rid="e22">Eq. (22)</xref> at the time of 1 hr. </p>
				<p>The dimensionless pressure governing equation was obtained by integration of <xref ref-type="disp-formula" rid="e25">Eq. (25)</xref>, to be:</p>
				<p>
					<disp-formula id="e23">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e23.jpg"/>
					</disp-formula>
				</p>
				<p>Dividing <xref ref-type="disp-formula" rid="e23">Eq. (23)</xref> by <xref ref-type="disp-formula" rid="e21">Eq. (21)</xref>, replacing the dimensionless quantities and solving for the spherical skin factor will result:</p>
				<p>
					<disp-formula id="e24">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e24.jpg"/>
					</disp-formula>
				</p>
			</sec>
			<sec>
				<title>2.3. Late time behavior</title>
				<p>The basis for interference in bounded systems were given by [<xref ref-type="bibr" rid="B3">3</xref>]. The application of the pressure derivative for limited reservoirs was presented by [<xref ref-type="bibr" rid="B10">10</xref>]. This means that it is feasible to develop either pseudosteady-state or steady-state periods during an interference test. As observed in <xref ref-type="fig" rid="f5">Fig. 5</xref>, once spherical flow regime vanishes pseudosteady-state period obeys the following governing pressure derivative equation:</p>
				<p>
					<disp-formula id="e25">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e25.jpg"/>
					</disp-formula>
				</p>
				<p>Replacing the dimensionless quantities and solving for the drainage area, it results:</p>
				<p>
					<disp-formula id="e26">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e26.jpg"/>
					</disp-formula>
				</p>
				<p>As shown in <xref ref-type="fig" rid="f6">Fig. 6</xref> the pressure derivative governing equation is given by:</p>
				<p>
					<disp-formula id="e27">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e27.jpg"/>
					</disp-formula>
				</p>
				<p>As for the spherical flow case, after replacing the dimensionless time based on area, the resulting area equation was:</p>
				<p>
					<disp-formula id="e28">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e28.jpg"/>
					</disp-formula>
				</p>
				<p>
					<fig id="f5">
						<label>Figure 5</label>
						<caption>
							<title>Dimensionless pressure behavior versus dimensionless time based on area for spherical flow interference in closed systems</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-204-00044-gf5.jpg"/>
						<attrib><bold>Source:</bold> The authors</attrib>
					</fig>
				</p>
				<p>
					<fig id="f6">
						<label>Figure 6</label>
						<caption>
							<title>Dimensionless pressure behavior versus dimensionless time based on area for linear flow interference in closed systems</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-204-00044-gf6.jpg"/>
						<attrib><bold>Source:</bold> The authors</attrib>
					</fig>
				</p>
				<p>On the other hand, for constant-pressure bounded systems, <xref ref-type="fig" rid="f7">Figs. 7</xref> and <xref ref-type="fig" rid="f8">8</xref>, the late-time governing pressure derivative equations for linear and spherical flow regimes, respectively are given by:</p>
				<p>
					<disp-formula id="e29">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e29.jpg"/>
					</disp-formula>
				</p>
				<p>Replacing the dimensionless quantities and solving for the drainage area results in:</p>
				<p>
					<disp-formula id="e30">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e30.jpg"/>
					</disp-formula>
				</p>
				<p>As shown in <xref ref-type="fig" rid="f8">Fig. 8</xref> the pressure derivative governing equation is given by:</p>
				<p>
					<disp-formula id="e31">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e31.jpg"/>
					</disp-formula>
				</p>
				<p>Replacing the dimensionless quantities and solving for the drainage area, it results:</p>
				<p>
					<disp-formula id="e32">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e32.jpg"/>
					</disp-formula>
				</p>
				<p>
					<fig id="f7">
						<label>Figure 7</label>
						<caption>
							<title>Dimensionless pressure behavior versus dimensionless time based on area for spherical flow interference in constant-pressure systems</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-204-00044-gf7.jpg"/>
						<attrib><bold>Source:</bold> The authors</attrib>
					</fig>
				</p>
				<p>
					<fig id="f8">
						<label>Figure 8</label>
						<caption>
							<title>Dimensionless pressure behavior versus dimensionless time based on area for linear flow interference in constant-pressure systems</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-204-00044-gf8.jpg"/>
						<attrib><bold>Source:</bold> The authors</attrib>
					</fig>
				</p>
				<p>Because of the noise, it is recommended to apply <xref ref-type="disp-formula" rid="e28">Eqs. (28)</xref>, <xref ref-type="disp-formula" rid="e30">(30)</xref> and <xref ref-type="disp-formula" rid="e32">(32)</xref> at time of 1 hr. </p>
				<p>The spherical system can be readily converted to hemispherical system. As seen in <xref ref-type="disp-formula" rid="e15">Eq. (15)</xref>, the constant <sub>
 <sup>
 <italic>(sp</italic>
</sup> 
</sub> has the value of 70.6. For hemispherical flow conditions this constant is multiplied by two, taking the value of 141.2, so do the constants in the related equations. Apart from this, appendix A presents the gas flow equations for linear and spherical flow conditions.</p>
			</sec>
		</sec>
		<sec>
			<title>3. Examples</title>
			<p>Two synthetic examples were generated to validate the porosity and permeability equations and two other tests were synthetically created two verify the equations of area. <xref ref-type="table" rid="t3">Table 3</xref> contains the input data for the examples. </p>
			<p>
				<table-wrap id="t3">
					<label>Table 3</label>
					<caption>
						<title>Input data for the examples</title>
					</caption>
					<graphic xlink:href="0012-7353-dyna-85-204-00044-gt3.jpg"/>
					<table-wrap-foot>
						<fn id="TFN3">
							<p><bold>Source:</bold> The authors</p>
						</fn>
					</table-wrap-foot>
				</table-wrap>
			</p>
			<sec>
				<title>3.1. Example 1 (Linear)</title>
				<p>The simulated data provided in <xref ref-type="fig" rid="f9">Fig. 9</xref> was generated with data from <xref ref-type="table" rid="t3">Table 3</xref>, from where the following information was read:</p>
				<p>
					<inline-graphic xlink:href="0012-7353-dyna-85-204-00044-i044.jpg"/>
				</p>
				<p>
					<fig id="f9">
						<label>Figure 9</label>
						<caption>
							<title>Log-log of pressure and pressure derivative versus time for example 1 (linear case)</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-204-00044-gf9.jpg"/>
						<attrib><bold>Source:</bold> The authors</attrib>
					</fig>
				</p>
				<p>Then, permeability was estimated with <xref ref-type="disp-formula" rid="e9">Eqs. (9)</xref> and <xref ref-type="disp-formula" rid="e11">(11)</xref> and porosity with <xref ref-type="disp-formula" rid="e7">Eq. (7)</xref>. Results are reported in <xref ref-type="table" rid="t4">Table 4</xref>.</p>
				<p>
					<table-wrap id="t4">
						<label>Table 4</label>
						<caption>
							<title>Results for worked examples</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-204-00044-gt4.jpg"/>
						<table-wrap-foot>
							<fn id="TFN4">
								<p><bold>Source:</bold> The authors</p>
							</fn>
						</table-wrap-foot>
					</table-wrap>
				</p>
			</sec>
			<sec>
				<title>3.2. Example 2 (spherical)</title>
				<p>
					<xref ref-type="fig" rid="f10">Fig. 10</xref> presents the pressure and pressure derivative data for a synthetic test under spherical flow interference conditions which used input data from <xref ref-type="table" rid="t3">Table 3</xref>. The following information was read from such plot:</p>
				<p>
					<fig id="f10">
						<label>Figure 10</label>
						<caption>
							<title>Log-log of pressure and pressure derivative versus time for example 2 (spherical case)</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-204-00044-gf10.jpg"/>
						<attrib><bold>Source:</bold> The authors</attrib>
					</fig>
				</p>
				<p>
					<inline-graphic xlink:href="0012-7353-dyna-85-204-00044-i048.jpg"/>
				</p>
				<p>Permeability was estimated using <xref ref-type="disp-formula" rid="e20">Eqs. (20)</xref> and <xref ref-type="disp-formula" rid="e22">(22)</xref>. Porosity was found with <xref ref-type="disp-formula" rid="e18">Eq. (18)</xref>. Results are also reported in <xref ref-type="table" rid="t4">Table 4</xref>.</p>
			</sec>
			<sec>
				<title>3.3. Example 3 (spherical case)</title>
				<p>A long pressure test was also simulated with input data from <xref ref-type="table" rid="t3">Table 3</xref>. The pressure and pressure derivative for this example is reported in <xref ref-type="fig" rid="f11">Fig. 11</xref> from where the following characteristic point was read:</p>
				<p>
					<inline-graphic xlink:href="0012-7353-dyna-85-204-00044-i049.jpg"/>
				</p>
				<p>Drainage area was estimated with <xref ref-type="disp-formula" rid="e30">Eq. (30)</xref> -reading at <italic>t</italic> = 1 hr- and reported in <xref ref-type="table" rid="t4">Table 4</xref>.</p>
				<p>
					<fig id="f11">
						<label>Figure 11</label>
						<caption>
							<title>Log-log of pressure and pressure derivative versus time for example 3 (spherical case)</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-204-00044-gf11.jpg"/>
						<attrib><bold>Source:</bold> The authors</attrib>
					</fig>
				</p>
			</sec>
			<sec>
				<title>3.4. Example 4 (linear case)</title>
				<p>The pressure and pressure derivative versus time data reported in <xref ref-type="fig" rid="f12">Fig. 12</xref> was also obtained using data from <xref ref-type="table" rid="t3">Table 3</xref>. The following datum was read from this figure.</p>
				<p>
					<inline-graphic xlink:href="0012-7353-dyna-85-204-00044-i051.jpg"/>
				</p>
				<p>Drainage area was estimated with <xref ref-type="disp-formula" rid="e28">Eq. (28)</xref> -reading at <italic>t</italic> = 1 hr- and also reported in <xref ref-type="table" rid="t4">Table 4</xref>.</p>
				<p>
					<fig id="f12">
						<label>Figure 12</label>
						<caption>
							<title>Log-log of pressure and pressure derivative versus time for example 4 (linear case)</title>
						</caption>
						<graphic xlink:href="0012-7353-dyna-85-204-00044-gf12.jpg"/>
						<attrib><bold>Source:</bold> The authors</attrib>
					</fig>
				</p>
			</sec>
		</sec>
		<sec sec-type="conclusions">
			<title>4. Conclusions</title>
			<p>
				<list list-type="order">
					<list-item>
						<p>The intersection point, a characteristic one-half slope (for linear flow) and negative one-half slope (for spherical) flow, a late time unit-slope line (pseudosteady state) and a late time negative unit-slope line (steady state) are identified and set as characteristic features on the pressure and pressure derivative versus time log-log plot which allow developing expressions for reservoir characterization.</p>
					</list-item>
					<list-item>
						<p><italic>TDS</italic> Technique is applied to interference testing under linear and spherical flow regime conditions. A unique point of intersection - found for each case - is used to find expressions to find reservoir permeability and porosity. Also, the permeability value is verified by another expression that uses an arbitrary point read on each flow regime (linear or spherical). There are also developed equations to estimate the drainage area in both dealt flow regimes for close or constant-pressure boundary systems. The Equations are successfully verified on synthetic cases.</p>
					</list-item>
				</list>
			</p>
			<p><bold>Nomenclature</bold></p>
			<p>
				<inline-graphic xlink:href="0012-7353-dyna-85-204-00044-i053.jpg"/>
			</p>
			<p><bold>Suffixes</bold></p>
			<p>
				<inline-graphic xlink:href="0012-7353-dyna-85-204-00044-i054.jpg"/>
			</p>
			<p><bold>Greek</bold></p>
			<p>
				<inline-graphic xlink:href="0012-7353-dyna-85-204-00044-i055.jpg"/>
			</p>
		</sec>
	</body>
	<back>
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		<fn-group>
			<fn fn-type="other" id="fn1">
				<label>How to cite:</label>
				<p> Escobar-Macualo, F.H., Rojas-Borrego, E. and Alarcón-Olaya, N.T., Analysis of pressure and pressure derivative interference tests under linear and spherical flow conditions. DYNA, 85(204), pp. 44-52, March, 2018.</p>
			</fn>
		</fn-group>
		<app-group>
			<app id="app1">
				<label>Appendix A. Gas flow Equations</label>
				<p>[<xref ref-type="bibr" rid="B1">1</xref>] introduced the pseudotime function to account for the time dependence of both gas viscosity and total system compressibility:</p>
				<p>
					<disp-formula id="e33">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e33.jpg"/>
					</disp-formula>
				</p>
				<p>This function is better defined as a pressure function given in hr psi/cp: </p>
				<p>
					<disp-formula id="e34">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e34.jpg"/>
					</disp-formula>
				</p>
				<p>Now, <italic>μ</italic> and <sub>
 <sup>
 <italic>ct</italic>
</sup> 
</sub> are pressure dependent properties. Rewriting <xref ref-type="disp-formula" rid="e3">Eq. (3)</xref> can be rewritten as:</p>
				<p>
					<disp-formula id="e35">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e35.jpg"/>
					</disp-formula>
				</p>
				<p>Including the pseudotime function, <sub>
 <sup>
 <italic>ta</italic>
</sup> 
</sub> (<italic>P</italic>), in <xref ref-type="disp-formula" rid="e35">Eq. (A.3)</xref>, the dimensionless pseudotime is given by: </p>
				<p>
					<disp-formula id="e36">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e36.jpg"/>
					</disp-formula>
				</p>
				<p>Multiplying and, then, dividing by (<sub>
 <sup>
 <italic>μct</italic>
</sup> 
</sub> )<sub>
 <italic>i</italic>
</sub> a similar equation to the general dimensionless time expression; </p>
				<p>
					<disp-formula id="e37">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e37.jpg"/>
					</disp-formula>
				</p>
				<p>The dimensionless pseudopressure and pseudopressure derivative are defined by: </p>
				<p>
					<disp-formula id="e38">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e38.jpg"/>
					</disp-formula>
				</p>
				<p>
					<disp-formula id="e39">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e39.jpg"/>
					</disp-formula>
				</p>
				<p>For gas linear flow regime interference, Eqs. (7), (9) and (12) become: </p>
				<p>
					<disp-formula id="e40">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e40.jpg"/>
					</disp-formula>
				</p>
				<p>
					<disp-formula id="e41">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e41.jpg"/>
					</disp-formula>
				</p>
				<p>
					<disp-formula id="e42">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e42.jpg"/>
					</disp-formula>
				</p>
				<p>For spherical gas flow regime interference, Eqs. (18), (20) and (22) become: </p>
				<p>
					<disp-formula id="e43">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e43.jpg"/>
					</disp-formula>
				</p>
				<p>
					<disp-formula id="e44">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e44.jpg"/>
					</disp-formula>
				</p>
				<p>
					<disp-formula id="e45">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e45.jpg"/>
					</disp-formula>
				</p>
				<p>For late time behavior, Eqs. (26), (28), (30), and (32) become: </p>
				<p>
					<disp-formula id="e46">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e46.jpg"/>
					</disp-formula>
				</p>
				<p>
					<disp-formula id="e47">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e47.jpg"/>
					</disp-formula>
				</p>
				<p>
					<disp-formula id="e48">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e48.jpg"/>
					</disp-formula>
				</p>
				<p>
					<disp-formula id="e49">
						<graphic xlink:href="0012-7353-dyna-85-204-00044-e49.jpg"/>
					</disp-formula>
				</p>
			</app>
		</app-group>
	</back>
</article>