<?xml version="1.0" encoding="ISO-8859-1"?><article xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance">
<front>
<journal-meta>
<journal-id>2079-3480</journal-id>
<journal-title><![CDATA[Cuban Journal of Agricultural Science]]></journal-title>
<abbrev-journal-title><![CDATA[Cuban J. Agric. Sci.]]></abbrev-journal-title>
<issn>2079-3480</issn>
<publisher>
<publisher-name><![CDATA[Editorial del Instituto de Ciencia Animal]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S2079-34802016000300002</article-id>
<title-group>
<article-title xml:lang="en"><![CDATA[Anaerobic digestion technologies for the treatment of pig wastes]]></article-title>
<article-title xml:lang="es"><![CDATA[Tecnologías de digestión anaerobia para el tratamiento de residuales porcinos]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Pérez-Pérez]]></surname>
<given-names><![CDATA[Tania]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Pereda-Reyes]]></surname>
<given-names><![CDATA[Ileana]]></given-names>
</name>
<xref ref-type="aff" rid="A02"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Oliva-Merencio]]></surname>
<given-names><![CDATA[Deny]]></given-names>
</name>
<xref ref-type="aff" rid="A03"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Zaiat]]></surname>
<given-names><![CDATA[Marcelo]]></given-names>
</name>
<xref ref-type="aff" rid="A04"/>
</contrib>
</contrib-group>
<aff id="A01">
<institution><![CDATA[,Instituto de Ciencia Animal  ]]></institution>
<addr-line><![CDATA[San José de las Lajas Mayabeque]]></addr-line>
</aff>
<aff id="A02">
<institution><![CDATA[,Universidad Tecnológica de La Habana  ]]></institution>
<addr-line><![CDATA[Marianao La Habana]]></addr-line>
</aff>
<aff id="A03">
<institution><![CDATA[,Universidad Tecnológica de La Habana  ]]></institution>
<addr-line><![CDATA[Marianao La Habana]]></addr-line>
</aff>
<aff id="A04">
<institution><![CDATA[,University of São Paulo  ]]></institution>
<addr-line><![CDATA[ ]]></addr-line>
<country>Brazil</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>09</month>
<year>2016</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>09</month>
<year>2016</year>
</pub-date>
<volume>50</volume>
<numero>3</numero>
<fpage>343</fpage>
<lpage>354</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://scielo.sld.cu/scielo.php?script=sci_arttext&amp;pid=S2079-34802016000300002&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.sld.cu/scielo.php?script=sci_abstract&amp;pid=S2079-34802016000300002&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.sld.cu/scielo.php?script=sci_pdf&amp;pid=S2079-34802016000300002&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="en"><p><![CDATA[The growth of pork production in the world favors the excessive generation of manures, so that anaerobic digestion plays an important role as a technology for the treatment of these wastes. The literature shows that in the world, in the last years, the application of high load technologies for the treatment of wastes generated by the pig breeding has increased. In contrast, the anaerobic biodigesters used in Cuban pig breeding currently use high hydraulic retention times and low volumetric organic loads. This involves the use of reactors with high volumes, which lead to huge investments for the treatment of these wastes, which makes these technologies inefficient. It is necessary, from a scientific perspective, to examine the technologies that are used today in the world and to develop researches that allow the fulfillment of the established in the Cuban standards in force on this subject]]></p></abstract>
<abstract abstract-type="short" xml:lang="es"><p><![CDATA[El crecimiento de la producción porcina en el mundo favorece la generación desmedida de estiércoles, por lo que la digestión anaerobia desempeña una función importante como tecnología para el tratamiento de estos residuales. La literatura demuestra que en el mundo, en los últimos años, se ha incrementado la aplicación de tecnologías de alta carga para el tratamiento de los residuos generados por la porcinocultura. Por el contrario, los biodigestores anaerobios empleados en la porcinocultura cubana en la actualidad usan altos tiempos de retención hidráulica y bajas cargas orgánicas volumétricas. Esto implica el uso de reactores con grandes volúmenes, que conllevan a enormes inversiones para el tratamiento de estos residuales, lo que convierte a estas tecnologías en poco eficientes. Es preciso entonces, desde una perspectiva científica, examinar las tecnologías que se utilizan hoy en el mundo y desarrollar investigaciones que permitan el cumplimiento de lo establecido en las normas cubanas vigentes acerca de este tema]]></p></abstract>
<kwd-group>
<kwd lng="en"><![CDATA[anaerobic digesters]]></kwd>
<kwd lng="en"><![CDATA[pig breeding wastes]]></kwd>
<kwd lng="en"><![CDATA[high load technology]]></kwd>
<kwd lng="es"><![CDATA[digestores anaerobios]]></kwd>
<kwd lng="es"><![CDATA[residuos de porcinocultura]]></kwd>
<kwd lng="es"><![CDATA[tecnologías de alta carga]]></kwd>
</kwd-group>
</article-meta>
</front><body><![CDATA[ <p align="right"><font size="2" face="Verdana, Arial, Helvetica, sans-serif"><b>Cuban Journal  of Agricultural Science, 50(3): 343-354, 2016, ISSN: 2079-3480</b></font></p>     <p align="right">&nbsp;</p>     <p align="right"><font size="2" face="Verdana, Arial, Helvetica, sans-serif"><b>REVIEW</b></font></p>     <p align="justify">&nbsp;</p>     <p align="justify"><font size="4" face="Verdana, Arial, Helvetica, sans-serif">  <b>Anaerobic digestion technologies for the treatment of pig wastes</b></font></p>      <p align="justify">&nbsp;</p>     <p align="justify"><font size="3" face="Verdana, Arial, Helvetica, sans-serif">  <b>Tecnologías de digestión anaerobia para el tratamiento de residuales porcinos</b></font></p>      <p align="justify">&nbsp;</p>     <p align="justify">&nbsp;</p>     <p align="justify"><font size="2" face="Verdana, Arial, Helvetica, sans-serif">  <b>Tania Pérez- Pérez,</b><sup><b>I</b></sup> <b> Ileana Pereda- Reyes,</b><sup><b>II</b></sup> <b> Deny Oliva-Merencio,</b><sup><b>III</b></sup> <b> Marcelo Zaiat,</b><sup><b>IV</b></sup>  </font></p>     ]]></body>
<body><![CDATA[<p align="justify"><font size="2" face="Verdana, Arial, Helvetica, sans-serif"><b> </b></font><font size="2" face="Verdana, Arial, Helvetica, sans-serif">    <sup>I</sup>Instituto de Ciencia Animal, Apartado Postal 24, San José de las Lajas, Mayabeque .    <br>   <sup>II</sup>Centro de Ingeniería de Procesos (CIPRO), Universidad Tecnológica de La Habana “José A. Echeverría” (CUJAE).  Marianao, La Habana.     <br>   <sup>III</sup>Centro de Tecnologías Energéticas Renovables (CETER). IUniversidad Tecnológica de La Habana “José A. Echeverría”.  (CUJAE). Marianao, La Habana.    <br>   <sup>IV</sup>Biological Processes Laboratory, Center for Research, Development and Innovation in Environmental Engineering, São Carlos School of Engineering (EESC), University of São Paulo (USP), Brazil. </font></p>     <p align="justify">&nbsp;</p>     <p align="justify">&nbsp;</p> <hr align="JUSTIFY">     <p align="justify"><font size="2" face="Verdana, Arial, Helvetica, sans-serif"><b>ABSTRACT</b></font></p>     <p align="justify"><font size="2" face="Verdana, Arial, Helvetica, sans-serif">The growth of pork production in the world favors the excessive generation of manures, so that anaerobic digestion plays an important role as a technology for the treatment of these wastes. The literature shows that in the world, in the last years, the application of high load technologies for the treatment of wastes generated by the pig breeding has increased. In contrast, the anaerobic biodigesters used in Cuban pig breeding currently use high hydraulic retention times and low volumetric organic loads. This involves the use of reactors with high volumes, which lead to huge investments for the treatment of these wastes, which makes these technologies inefficient. It is necessary, from a scientific perspective, to examine the technologies that are used today in the world and to develop researches that allow the fulfillment of the established in the Cuban standards in force on this subject.</font></p>     <p align="justify"><font size="2" face="Verdana, Arial, Helvetica, sans-serif"><b>Key words:</b> anaerobic digesters, pig breeding wastes, high load technology.</font></p> <hr align="JUSTIFY">     <p align="justify"><font size="2" face="Verdana, Arial, Helvetica, sans-serif"><b>RESUMEN</b></font></p>     ]]></body>
<body><![CDATA[<p align="justify"><font size="2" face="Verdana, Arial, Helvetica, sans-serif">El crecimiento de la producción porcina en el mundo favorece la generación desmedida de estiércoles, por lo que la digestión anaerobia desempeña una función importante como tecnología para el tratamiento de estos residuales. La literatura demuestra que en el mundo, en los últimos años, se ha incrementado la aplicación de tecnologías de alta carga para el tratamiento de los  residuos generados por la porcinocultura. Por el contrario, los biodigestores anaerobios empleados en la porcinocultura cubana en la actualidad usan altos tiempos de retención hidráulica y bajas cargas orgánicas volumétricas. Esto implica el uso de reactores con grandes volúmenes, que conllevan a enormes inversiones para el tratamiento de estos residuales, lo que convierte a estas tecnologías en poco eficientes. Es preciso entonces, desde una perspectiva científica, examinar las tecnologías que se utilizan hoy en el mundo y desarrollar investigaciones que permitan el cumplimiento de lo establecido en las normas cubanas vigentes acerca de este tema.</font></p>     <p align="justify"><font size="2" face="Verdana, Arial, Helvetica, sans-serif"><b>Palabras    clave:</b>    digestores anaerobios, residuos de porcinocultura, tecnologías de alta carga.</font></p> <hr align="JUSTIFY">     <p align="justify">&nbsp;</p>     <p align="justify">&nbsp;</p>     <p align="justify" class="subtitulo" style="margin-bottom:.0001pt;text-align:justify;"><span style="line-height:120%; font-family:'Verdana','sans-serif'; font-size:13.0pt; color:windowtext; "><b>INTRODUCTION</b></span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="line-height:120%; font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">During the last decades, the number of  small pork producers has decreased, while the animal population per farm has  increased (Deng <em>et al.</em> 2014). These conditions have led to a higher  concentration of waste in small areas, which requires urgent development of  easy-to-implement solutions.</span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="line-height:120%; letter-spacing:.2pt; font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Among the  potential solutions for wastes treatment the anaerobic digestion (AD) deserves  special attention due to its efficiency and economic feasibility (Sakar <em>et  al.</em> 2009), as well as its potential for the bioenergy (CH4) production,  reduction of emissions of greenhouse gases and deactivation of pathogens (Mass&eacute; <em>et al.</em> 2011, Abbasi <em>et al.</em> 2012, Franke-Whittle <em>et al.</em> 2014).</span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; "> </span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="line-height:120%; letter-spacing:.1pt; font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">In recent years,  significant progress has been obtained in the world through the evolution of  high-rate anaerobic reactors, which deal with high volumes of wastewater. Due  to their different advantages, the most used include the anaerobic filter (AF),  anaerobic sequential broken reactor (ASBR) and the upflow anaerobic sludge  blanket reactor (UASB). However, in Cuba, today, the most used technologies for  the treatment of pig wastes comprise low-load reactors, which are inefficient  due to their high hydraulic retention times (HRT), which lead to high volumes  of reactors and high costs.</span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; "> </span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">The objective of this study is to make  a review about the anaerobic technologies applied worldwide in the treatment of  pig wastes. It is also intended, to examine the particularities of this theme  in Cuba.</span></p>     <p align="justify" class="MsoNormal" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-align:justify;"><span style="line-height:107%; font-family:'Verdana','sans-serif'; font-size:10.0pt; ">&nbsp;</span></p>     ]]></body>
<body><![CDATA[<p align="justify" class="subtitulo" style="margin-bottom:.0001pt;text-align:justify;"><span style="font-family:'Verdana','sans-serif'; font-size:13.0pt; color:windowtext; "><b>PIG WASTES</b> </span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">The world pig  production has increased more than 3.5 times over the past 40 years. The  tendency is to increase the concentration of animals per farm, even reaching  values of thousands of heads. As the demand of pork meat increases, huge  amounts of waste are generated around the world, which is associated with  increased excreta and wastewater (Lee and Shoda 2008).</span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; "> </span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">In previous decades, pig wastes were  used as fertilizers and soil conditioners in which they were generated.  However, the intensive cattle rearing has caused serious damage to the  environment, including health risks, atmospheric emissions, surface and  groundwater contamination, odor dispersion and soil damage (Mass&eacute; <em>et al.</em> 2004, Lim and Fox 2011). Due to the characteristics these wastes have.</span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Among the  atmospheric emissions, the greenhouse gases (methane and nitrous oxide) are  highlight, which are the result of spontaneous self-purification of wastes. In  turn, the action of manures and slurries in waters and soils is mainly  concentrated, in the dispersion of ammonia and nitrates, due to their potential  effect on the acidification of the environment and water eutrophication  (Benyoucef <em>et al.</em>    2013).</span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; "> </span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Extensive are the studies carried out  in the characterization and treatment of pig wastes, in order to reduce their  negative effects on the environment. Andreadakis (1992) showed that,  approximately,    60.0 % of the total organic matter in the pig wastewater is biodegradable.  Similarly, Deng <em>et al.</em> (2008) reported that pig manure is composed of  readily biodegradable material, and is a good base substrate for biological  processes, such as anaerobic digestion, since it contains buffer capacity and a  wide variety of nutrients (Gonz&aacute;lez-Fern&aacute;ndez and Garc&iacute;a-Encina 2009, Rodr&iacute;guez <em>et al.</em> 2011). These results show that the compounds present in pig  manure contribute to the concentration of biochemical oxygen demand (BOD), the  main indicator of the organic load responsible for the pollutant power of these  wastes.</span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Other indicators  that cause contamination in the wastes from pig facilities, due to their high  concentrations, are suspended solids, chemical oxygen demand (COD), nitrogen,  phosphorus and potassium compounds (Girard <em>et al.</em> 2004, Klomjek 2016)  and gaseous substances such as ammonia, methyl mercaptan and hydrogen sulfide  (Rumsey <em>et al.</em>    2014).</span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; "> </span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">As is showed, pig wastes have great  pollutant power and require an effective treatment before being poured into  receivers. Due to the high concentration of biodegradable compounds present in  these wastes, the anaerobic treatment can be an effective option to contribute  to the environment care.</span></p>     <p align="justify" class="MsoNormal" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-align:justify;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; ">&nbsp;</span></p>     <p align="justify" class="subtitulo" style="margin-bottom:.0001pt;text-align:justify;"><span style="font-family:'Verdana','sans-serif'; font-size:13.0pt; color:windowtext; "><b>ANAEROBIC DIGESTION FOR THE BIOGAS  PRODUCTION</b> </span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">The anaerobic digestion (AD) is the  biological conversion, in the absence of oxygen, that make the facultative and  anaerobic bacteria and methanogenic archaeas, from the synthesis of organic  matter present in solid wastes (domestic and urban), from animals and plants,  and its transformation into methane (CH<sub>4</sub>), carbon dioxide (CO<sub>2</sub>),  ammonia (NH<sub>3</sub>), hydrogen sulfide (H<sub>2</sub>S) and nitrogen (N<sub>2</sub>)  (Batstone and Jensen 2011). This gas mixture is called biogas.</span></p>     ]]></body>
<body><![CDATA[<p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">T<span style="letter-spacing:.1pt; ">he  production of bioenergy from the organic waste, AD is a promising option to  mitigate climate change and is considered a sustainable treatment technology  (Pantaleo <em>et al.</em> 2013). This is because it not only contributes net  production of positive energy, but the produced biogas can substitute fossil  fuels, so it has a positive effect on the reduction of greenhouse gases (Bernet  and B&eacute;line 2009, Shanmugam and Horan 2009, Weiland 2010). The AD also generates  an effluent that can be applied in agricultural fields for the nutrients  recovery, for its properties as fertilizer (Rajagopal <em>et al.</em> 2011). This  biological process, when compared to aerobic processes, offers many significant  advantages, such as low sludge production, lower energy requirements and green  energy recovery (Mass&eacute; <em>et al.</em> 2010, Xia <em>et al.</em> 2012). In AD, 90.0  % of the available energy is transformed into CH4 by direct oxidation, and only  10.0 % of the energy is consumed in the microbial growth, while in the aerobic  process is consumed, approximately, 50.0 %.</span></span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">The initial step  of the Ad process is the hydrolysis of organic matter. In this one, bacteria  and fungi convert macromolecules (proteins, carbohydrates and fats) into amino  acids, sugars and volatile fatty acids (Nielsen <em>et al.</em> 2007, Leis <em>et  al.</em> 2014). In the second stage of the process, called acidogenesis, the  acidogenic bacteria turn sugars, amino acids and fatty acids into organic  acids, alcohols and ketones, acetate, CO</span><sub><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">2</span></sub><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; "> and hydrogen. The acetogenic bacteria transform fatty  acids and alcohols into acetate, H</span><sub><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">2 </span></sub><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">and CO</span><sub><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">2</span></sub><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; "> in the third stage of the process  (acetogenesis). These products are used by methanogenic archaeas to form biogas  in the fourth stage of AD, called methanogenesis (Pereda <em>et al.</em> 2015).  In most of the anaerobic treatments of biodegradable wastes, this last step is  limiting and therefore, it defines the main parameters of monitoring and  control in the process. Methane can be produced by acetotrophic and  hydrogenotrophic methanogens. The changes in the environmental and operational  conditions of the reactor (pH, temperature, hydraulic retention time, substrate  composition) influence on the composition and dynamics of these communities  (Kim <em>et al.</em> 2013, Solli <em>et al.</em> 2014, Yu <em>et al.</em> 2014).</span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; "> </span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">It can be  explained that the AD of pig wastes is important because of its environmental  and energy effect. Due to the rising fossil fuel costs and the need to mitigate  anthropogenic global warming, the biodegradable waste AD is a sustainable  management strategy. The biogas production from several types of raw materials  has proven to be a renewable source of energy that can be produced sustainably  in many countries. Likewise, the generation of an effluent with fertilizing  characteristics, gives this process higher relevance. However, the effective  treatment of wastes should consider the use of appropriate and economically  feasible technologies to comply the environmental standards established in each    country.</span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; "> </span></p>     <p align="justify" class="MsoNormal" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-align:justify;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; ">&nbsp;</span></p>     <p align="justify" class="subtitulo" style="margin-bottom:.0001pt;text-align:justify;"><span style="font-family:'Verdana','sans-serif'; font-size:13.0pt; color:windowtext; "><b>ANAEROBIC DIGESTION TECHNOLOGIES USED  IN THE WORLD FOR PIG WASTES TREATMENT</b> </span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Anaerobic processes are widely used  for pig wastes treatment in reactors of various designs and scales, with the  purpose of stabilizing the organic matter with the consequent production of  energy in methane form (Hwang <em>et al.</em> 2001, Angenent <em>et al.</em>2002,  Ahring 2003). The most studied are AF (Oleszkiewicz 1983, Ng and Chin 1988),  ASBR (Mace and Mata-Alvarez 2002, Mass&eacute; <em>et al.</em> 2003,&nbsp; 2004, Kim <em>et al.</em> 2004, Ga &amp; Ra  2009) and&nbsp; UASB (Lo <em>et al.</em> 1994,  Sanchez <em>et al.</em> 2005, Song <em>et al.</em> 2010). The latter are the most  used on an industrial scale. Other types of high-load technologies, such as  EGSB, have also been considered for the treatment of these wastes, but on a  lower scale (L&oacute;pez-Fern&aacute;ndez <em>et al.</em> 2011, Lee and Han 2012). These  technologies have as main objective to achieve high of elimination  efficiencies, when treating higher volumetric organic loads (VOL) in the lower  reactor volume, which guarantees lower HRT with high retention of active  biomass (SRT).</span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="line-height:120%; letter-spacing:.35pt; font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">The AF is characterized  by being robust systems, with good retention of microorganisms in the medium,  which can work at high VOL and low HRT. Oleszkiewicz (1983) studied the  treatment of pig wastewater with an AF at 23 &deg;C and obtained removal efficiency  of COD of 73.0 % at a VOL of    4.0 kg COD / m<sup>3</sup>d. Ng and Chin (1988), when treating pig wastewater  with an expanded bed anaerobic filter at 30 &deg;C, reported total suspended solids  (TSS) and volatile (VSS) of 93.0 % in a HRT of five days. However, the removal  efficiency of TSS decreased dramatically to 74.0 % when the HRT decreased to  four days. Regardless of its advantages, this configuration is limited to low  values of ascending speed, to avoid the dragging of solids with the effluent.  This does not allow, sometimes, a good biomass-substrate contact and the  efficiency can be affected in some cases.</span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; "> </span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Likewise, the ASBR  is a technology that highlight for its flexibility in operation. Its main  advantages are that the reaction and sedimentation occur in the same unit, and  as a consequence the biomass is in a dynamic state of abundance. These  characteristics make possible that these systems treat solids and liquids  waste, and the operating and maintenance costs be minimal (Islam <em>et al.</em> 2011). There are several experiences with this type of reactor. Mass&eacute; <em>et al.</em> (2003) used an ASBR at laboratory scale to treat pig excreta and they observed  that removal efficiency of COD decreased with decreasing temperature. The  values obtained by these authors were    94.2 &plusmn; 1.1 % at 20 &deg;C, 78.8 &plusmn; 3.0% at 15 &deg;C and 60. 4 &plusmn; 6.4 % at 10 &deg;C. but  Mass&eacute; <em>et al.</em> (2004) in a pilot-scale reactor obtained removal efficiency  of COD of 79.5% at 20 &deg;C. Likewise, Ng (1989), with this same configuration,  but at a 28 &deg;C temperature, obtained removal efficiency of VSS of 89.0 % at a  VOL of 0.4 kg COD / m<sup>3</sup>d. However, when the latter increased, the  efficiency was markedly deteriorated. Similarly, Ndegwa <em>et al.</em> (2008)  studied an ASBR at different temperatures and obtained that the biogas production  remained practically constant at 20 and  35 &deg;C. However, the COD removal slightly decreased from 85.0 to 80.0 % with  increasing temperature.</span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">According to the above results, it can  be inferred that temperature, such as the VOL and the HRT, has a marked influence  on the removal efficiencies of solids and organic matter in the mentioned  configurations. For this reason, Zaiat <em>et al.</em> (2001) recommended  increasing the solids retention time (SRT) to improve the organic matter  removal in ASBR reactors.</span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Many researchers  have reported satisfactory performances in the treatment processes of pig  wastes with high-rate reactors, based on sludge granulation where high biogas  quality is obtained in the range of 70.0-80.0% of the methane content (Mahmoud <em>et  al.</em> 2003, Kim <em>et al.</em> 2004, Najafpour <em>et al.</em> 2006). These  reactors allow the accumulation of high biomass concentrations in granular  sludge form, which results in a process of high efficiency and stability, with  short HRT (McHugh <em>et al.</em> 2003a, 2003b, Najafpour <em>et al.</em>2006).</span></p>     ]]></body>
<body><![CDATA[<p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Deng <em>et al.</em> (2006), when treating pig wastewater in an internal circulation reactor (IC),  obtained elimination efficiencies of COD in the range of 60.0 to 80.0 % with  organic loads of 6.0 to 7.0 kg COD / m<sup>3</sup>d. This effluent was  subsequently treated in a sequential broken reactor and the COD removal  exceeded    95.0 %.</span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; "> </span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">In particular, the  upflow sludge blanket reactor (UASB) has converted anaerobic digestion into a  competitive technology for high organic load wastewater (Torkian <em>et al.</em> 2003, Kim <em>et al.</em> 2004). To achieve the advantages of suspended growth  and adherence growth, Lo <em>et al.</em> (1994) treated pig wastewater in a UASB  reactor, to which a carrier medium was placed in the center of the reactor, in  a temperature range between 22 and 28 &deg;C. These authors obtained removal  efficiency of COD from 95.0 % to VOL of 1.65 kg COD / m<sup>3</sup>d. However,  this efficiency decreased to 57.0 % at a VOL of 3.5 kg/m</span><sup><span style="line-height:120%; letter-spacing:-.2pt; font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">3</span></sup><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">d. Campos <em>et al.</em> (2005), with the  same configuration at 20 h HRT and VOL of 1.42 kg COD/m</span><sup><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">3</span></sup><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">d, obtained removal efficiency of COD of  84.0 %.</span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; "> </span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Pereira-Ram&iacute;rez <em>et al.</em> (2004)  used a UASB reactor with recirculation of effluent and HRT of 12 h for treating  pig wastewater, varying COD/alkalinity relationship. In this study, the  efficiency of COD removal of 85.0% was obtained, for an accessional speed&nbsp; of 0.35 m / h with high VOL (23 kg COD/m<sup><span style="letter-spacing:-.2pt; ">3</span></sup>d), while superior speeds promoted  instability in the functioning of the reactor, and caused a reduction of  organic matter removal, which reached 65.0%.</span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Rodrigues <em>et al.</em> (2010), in a reactor  of 11.5 m<sup>3</sup>, at HRT from  1.7 to 4.1 d, and with VOL between 1.1 and 17.5 kg COD/ m<sup>3</sup>d, obtained COD removal efficiencies  of 92.0 %.</span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Song <em>et al.</em> (2010) studied different hydraulic retention times (7.0, 6.4, 5.0 and 3.5 d) in  a volume of 35 m</span><sup><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">3</span></sup><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">. During the functioning period, efficiencies of COD and  VFA removal were in the range from 74.0 to 78.7% and 89.3 to 96.6%,  respectively. These effluent concentrations constituted an efficient removal of  organic matter and stable functioning. Associated to high removal efficiency,  for different HRT,&nbsp; methane yield values  were 71.0, 83.3, 76.9 and 71.9 %, respectively.</span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Results of the  studies in this configuration show that this technology is suitable for the  treatment of pig wastes. However, S&aacute;nchez <em>et al.</em> (2005) concluded that  the UASB is not suitable for the treatment of pig manure, based on poor yield  for low HRT and high VOL.</span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; "> </span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">As previously  stated, treating these wastes with UASB is effective, due to its ability of  forming a granular sludge with excellent sedimentation characteristics, which  allows to study in a wider range of VOL and lower HRT than in other configurations.</span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; "> </span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Apart from the  different advantages that have made it successful, studies by various authors  (Hickey <em>et al.</em> 1991, McHugh <em>et al.</em> 2004) show that one of the  major disadvantage of UASB reactors are the long starting periods, due to the  time required for the process of anaerobic granulation. Together with this  fact, a good degree of mixture between biological sludge and feeding is not  always achieved, resulting in insufficient mass transfer and appearance of  concentration gradients. For this reason, a modified version of this  configuration is produced, which is called anaerobic reactor of expanded  granular sludge bed (EGSB), which operates at higher accessional speeds by  recirculation of the effluent and is designed with higher height/diameter  ratio, around 20 (Kato <em>et al.</em> 1994, O&rsquo;Reilly and Colleran 2005). High  accessional speed of the liquid applied to these reactors, allows a better hydraulic  agitation of the sludge bed, resulting in a higher expansion of the bed and,  consequently, improves biomass-substrate contact. This may reduce considerably  the volume of dead zones, preferential flows and shortcuts (Nicolella 2000,  Fuentes <em>et al.</em> 2011) and influence positively on the increase of  treatment efficiency (L&oacute;pez and Borzacconi 2011). In recent years, there has  been more focus on EGSB reactors than on UASB reactors, because they endure  higher organic loads, which favor their hydrodynamics (Pu&ntilde;al <em>et al.</em> 2003, Teixeira <em>et al.</em> 2014)</span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">These reactors have been little  studied, compared to UASB. However, due to its many advantages, they are  considered as a technology with broad prospects for high-load wastes. Some  research have used an EGSB reactor for treating effluents from pig breeding,  mainly the studies of L&oacute;pez-Fern&aacute;ndez <em>et al.</em> (2011), Lee and Han (2012).</span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">The first combined  the EGSB reactor with ultrafiltration system and functioning at a HRT of    3.8 d and VOL of 2.76 g COD/Ld, obtained total COD removal efficiency of about  70.0 %. The second authors, using also a combination of reactors, with a batch  reactor after EGSB, obtained COD removal efficiency of 42.5%, with VOL between  2.0 and  6.0 kg COD/m</span><sup><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">3</span></sup><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">d at a HRT of 24 h.</span></p>     ]]></body>
<body><![CDATA[<p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">&nbsp;<span style="letter-spacing:.2pt; ">It is  considered here that previous results do not reflect the actual efficiency of  this technology by the use of one or more units of treatment previous to the  bioreactor, so it is more suitable, for these cases, to refer to efficiency  only in terms of BOD. In these units, biodegradable fraction decreases and  refractal fraction of the waste remains constant, which is demonstrated by the  low efficiencies obtained in terms of removed COD. Due to the high relation of  biodegradability (BOD/COD) of pig waste, which is between 0.3 and 0.8 (Ng 1989,  Villamar <em>et al.</em> 2013, Mofokeng <em>et al.</em> 2016), and high VOL, to  which EGSB reactors are able to function, it should be used as the only  treatment unit. </span></span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Apart from the fact that high load  technologies are more complex in their functioning, they allow to obtain higher  robustness to operate with lower HRT and high VOL, leading to a better  cost-benefit relationship. However, studies on training and development of  granules should be widened, in order to reduce startup time and improve  efficiency of organic load removal with a more appropriate balance of  environmental conditions inside the reactors.</span></p>     <p align="justify" class="MsoNormal" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-align:justify;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; ">&nbsp;</span></p>     <p align="justify" class="subtitulo" style="margin-bottom:.0001pt;text-align:justify;"><span style="font-family:'Verdana','sans-serif'; font-size:13.0pt; color:windowtext; "><b>ANAEROBIC TREATMENTS USED    IN CUBA</b> </span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">For many years,  breeding pig wastes were treated in conventional anaerobic biodigesters.  However, this type of reactor, normally used in the treatment of these  semi-solid wastes, with total solids concentrations around 6.0 %, are not  suitable for the treatment of dilute wastewater, with solids concentrations of  0.1 to 3.0 %, due to the need of very high HRT and consequently, biodigesters  with very high volumes.</span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; "> </span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">One of the most used biodigestors, not  only in Cuba but in the world, is the fixed dome. In our country there are  approximately 400 plants of this type, according to the latest census conducted  by the National Biogas Group (NBG) in 2015. The designs that currently exist  allow adequate treatment of wastewater, up to 500 pigs (Sosa <em>et al.</em> 2014), because as its operation explained, they are located underground and  lead to the movement of important&nbsp;  volumes of soil. The efficiency of the fixed dome technology reduces the  contaminant load between 75.0-90.0 %, depending on the pig waste  characteristics, as well as the efficiency and control of operation of the  biodigester. The effluents treated in fixed dome biodigesters can be arranged  in an oxidation pond and used for crop irrigation, due to their low total  solids percent.</span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">There are also, to a lesser number,  the tubular biodigesters or &quot;Plug Flow&quot;, many of them installed by  researchers and specialists of the Center for the Development of Biogas (CPDB)  from the Institute of Pig Research and, approximately, 120 have been installed  in the Western provinces. In Cuba, these biodigesters are used in farms of up  to 150 pigs, since for their correct functioning and adequate treatment of  wastes , they must have a diameter/length (d/l) of 1/6 relation (Sosa <em>et al.</em> 2014) .</span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">These reactors are not effective for  the treatment of large volumes of wastewater (Oviedo 2011, Guardado 2013). For  this reason, the technology used in Cuba for pig integral centers with a  capacity higher than 500 pigs, is a piston-flow reactor with rigid cover, which  allows the treatment of the generated load up to 2000 heads. These plants are  capable of generating a volume of biogas that supplies the consumption of the  farms where they are installed (D&iacute;az 2012). However, due to the high HRT and  the low loads, large volume reactors are needed, with the consequent low  effectiveness in the treatment of these wastes.</span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">A tendency in  recent years has been the use of covered ponds which use structures and domes  of geomembrane, in which the organic matter oxidation and gas retention occur.  High removal efficiencies of COD are obtained in this technology, ranging from  78.0 to 90.0 %, but at high hydraulic retention times (HRT) with a minimum of  10 d (Blanco <em>et al.</em> 2015). On the other hand, the useful life of the  geomembranes is short, so it is expensive, not only for the large volumes of  ponds, but also for the cost of replacing or maintaining the geomembranes.</span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Although international experiences  show that high-load technologies are more robust and effective from the  environmental and energy point of view, in the design of treatment plants of  pig wastes in Cuban industrial facilities there is no projection of the use of  these technologies.</span></p>     ]]></body>
<body><![CDATA[<p align="justify" class="MsoNormal" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-align:justify;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; ">&nbsp;</span></p>     <p align="justify" class="subtitulo" style="margin-bottom:.0001pt;text-align:justify;"><span style="font-family:'Verdana','sans-serif'; font-size:13.0pt; color:windowtext; "><b>FINAL CONSIDERATIONS</b></span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Taking into  account the characteristics of the pig wastes, the anaerobic digestion  technology allows its degradation with high efficiency. In the world, the UASB  technology is the most used in the anaerobic treatment of these wastes, because  it allows the accumulation of high biomass concentrations in granular sludge  form. This results in a process of high efficiency and stability, in which it  is possible to work at high VOL and lower HRT than in other configurations. Regardless  of this, biomass-substrate contact is still insufficient, which does not favor  the hydrodynamic performance. For these reasons, the international experience  shows that EGSB technology has higher advantages and is promising for the  treatment of high-load wastes.</span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; "> </span></p>     <p align="justify" class="Cuerpodetexto" style="margin-top:5.95pt; text-indent:0cm; margin-bottom: .0001pt;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; ">According to what has been  analyzed so far, the UASB and EGSB configurations have wide potentialities of  use in pig wastes treatment which are generated in facilities on an industrial  scale in Cuba. However, in both cases, studies should be carried out to  establish the most appropriate environmental and operational conditions, in  which higher efficiencies of removal of solids and organic matter were  obtained, allowing the disposal of a higher quality effluent</span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">.</span></p>     <p align="justify" class="MsoNormal" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-align:justify;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; ">&nbsp;</span></p>     <p align="justify" class="subtitulo" style="margin-bottom:.0001pt;text-align:justify;"><span style="font-family:'Verdana','sans-serif'; font-size:13.0pt; color:windowtext; "><b>REFERENCES</b></span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Abbasi,  T., Tauseef, S. M. &amp; Abbasi, S. A. 2012. &ldquo;Anaerobic digestion for global  warming control and energy generation&mdash;An overview&rdquo;. Renewable and Sustainable  Energy Reviews, 16(5): 3228&ndash;3242, ISSN: 1364-0321, DOI:  10.1016/j.rser.2012.02.046.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Ahring,  B.K. 2003. Perspectives for anaerobic digestion. In: Ahring, B.K. (Ed.),  Biomethanation. Springer-Verlag, Heidelberg, Berlin, New York, pp. 3&ndash;7.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Andreadakis,  A. D. 1992. &ldquo;Anaerobic Digestion of Piggery Wastes&rdquo;. Water Science and  Technology, 25(1): 9&ndash;16, ISSN: 0273-1223, 1996-9732.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Angenent,  L.T., Sung, S., Raskin, L. 2002. &ldquo;Methanogenic population dynamics during  startup of a full-scale anaerobic sequencing batch reactor treating swine  waste&rdquo;. Water Research, 36: 4648&ndash;4654.</span></p>     ]]></body>
<body><![CDATA[<p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Batstone,  D. J. &amp; Jensen, P. D. 2011. &ldquo;Anaerobic Processes&rdquo;. In: Treatise on Water  Science, vol. 4, Oxford, U.K.: Academic Press, pp. 615&ndash;639, ISBN:  978-0-444-53199-5, DOI: 10.1016/B978-0-444-53199-5.00097-X, Available:  &lt;<a href="http://linkinghub.elsevier.com/retrieve/pii/B978044453199500097X" target="_blank">http://linkinghub.elsevier.com/retrieve/pii/B978044453199500097X</a>&gt;,  [Consulted: November 10, 2016].</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Bernet,  N. &amp; B&eacute;line, F. 2009. &ldquo;Challenges and innovations on biological treatment  of livestock effluents&rdquo;. </span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Bioresource Technology, 100(22):  5431&ndash;5436, ISSN: 0960-8524, DOI: 10.1016/j.biortech.2009.02.003.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Blanco, D., Su&aacute;rez, J., Jim&eacute;nez, J., Gonz&aacute;lez, F., &Aacute;lvarez, L. M., Cabeza  E. &amp; Verde, J. 2015. Eficiencia del tratamiento de residuales porcinos en  digestores de laguna tapada. Pastos y Forrajes, 38(4): 441-447, ISSN: 2078-8452</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Campos, C. M. M., Damasceno, L. H. S., Mochizuki, E. T. &amp; Botelho, C.  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<body><![CDATA[<p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Franke-Whittle,  I. H., Walter, A., Ebner, C. &amp; Insam, H. 2014. &ldquo;Investigation into the  effect of high concentrations of volatile fatty acids in anaerobic digestion on  methanogenic communities&rdquo;. Waste Management, 34(11): 2080&ndash;2089, ISSN: 0956-053X,  DOI: 10.1016/j.wasman.2014.07.020.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Fuentes,  M., Scenna, N. J. &amp; Aguirre, P. A. 2011. &ldquo;A coupling model for EGSB  bioreactors: Hydrodynamics and anaerobic digestion processes&rdquo;. 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Water Science &amp; Technology, 64(10):  2080&ndash;2088, ISSN: 0273-1223, DOI: 10.2166/wst.2011.697.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">L&oacute;pez-Fern&aacute;ndez,  R., Aristiz&aacute;bal, C. &amp; Irusta, R. 2011. &ldquo;Ultrafiltration as an advanced  tertiary treatment of anaerobically digested swine manure liquid fraction: A  practical and theoretical study&rdquo;. 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<body><![CDATA[<p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Ndegwa,  P.M., Hamilton, D.W., Lalman, J.A. &amp; Cumba, H.J. 2008. &ldquo;Effects of  cycle-frequency and temperature on the performance of anaerobic sequencing  batch reactors (ASBRs) treating swine waste&rdquo;. Bioresource Technology,  99:1972&ndash;1980,</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Ng, W.  J. 1989. &ldquo;A sequencing batch anaerobic reactor for treating piggery  wastewater&rdquo;. Biological Wastes, 28(1): 39&ndash;51, ISSN: 0269-7483, DOI:  10.1016/0269-7483(89)90048-7.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Ng, W.  J. &amp; Chin, K. K. 1988. &ldquo;Treatment of piggery wastewater by expanded-bed  anaerobic filters&rdquo;. Biological Wastes, 26(3): 215&ndash;228, ISSN: 0269-7483, DOI:  10.1016/0269-7483(88)90167-X.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Nicolella,  C. 2000. &ldquo;Wastewater treatment with particulate biofilm reactors&rdquo;. Journal of  Biotechnology, 80(1): 1&ndash;33, ISSN: 0168-1656, DOI: 10.1016/S0168-1656(00)00229-7.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Nielsen,  H., Uellendahl, H. &amp; Ahring, B. 2007. &ldquo;Regulation and optimization of the  biogas process: Propionate as a key parameter&rdquo;. Biomass and Bioenergy,  31(11&ndash;12): 820&ndash;830, ISSN: 0961-9534, DOI: 10.1016/j.biombioe.2007.04.004.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Oleszkiewicz,  J. A. 1983. &ldquo;A comparison of anaerobic treatments of low concentration piggery  wastewaters&rdquo;. Agricultural Wastes, 8(4): 215&ndash;231, ISSN: 0141-4607, DOI:  10.1016/0141-4607(83)90091-4.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">O&rsquo;Reilly,  C. &amp; Colleran, E. 2005. &ldquo;Microbial sulphate reduction during anaerobic digestion:  EGSB process performance and potential for nitrite suppression of SRB  activity&rdquo;. </span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Water Science and Technology, 52(1&ndash;2): 371&ndash;376, ISSN:  0273-1223, 1996-9732.</span></p>     <!-- ref --><p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Oviedo, H. 2011. Biog&aacute;s: experiencias en el municipio Bartolom&eacute; Mas&oacute;.  Bayamo, Cuba: Universidad de Granma.    </span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Pantaleo, A., Gennaro, B. D. &amp; Shah, N. 2013. </span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">&ldquo;Assessment of  optimal size of anaerobic co-digestion plants: An application to cattle farms  in the province of Bari (Italy)&rdquo;. Renewable and Sustainable Energy Reviews, 20:  57&ndash;70, ISSN: 1364-0321, DOI: 10.1016/j.rser.2012.11.068.</span></p>     ]]></body>
<body><![CDATA[<p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Pereda-Reyes, I. Pag&eacute;s-D&iacute;az, J. &amp; S&aacute;rv&aacute;ri-Horv&aacute;th, I. 2015. </span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Biodegradation  and Bioremediation of Polluted Systems - New Advances and Technologies. Chapter  3: Anaerobic Biodegradation of Solid Substrates from Agroindustrial Activities  - Slaughterhouse Wastes and Agrowastes. </span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Pereira-Ram&iacute;rez, O., Quadro, M., Antunes, R. &amp; Koetz, P. 2004.  &ldquo;Influ&ecirc;ncia da recircula&ccedil;&atilde;o e da alcalinidade no desempenho de um reator uasb  no tratamento de efluente de suinocultura&rdquo;. </span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Current Agricultural  Science and Technology, 10(1): 103&ndash;110, ISSN: 2317-2436, DOI:  10.18539/cast.v10i1.664.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Pu&ntilde;al,  A., Brauchi, S., Reyes, J. 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Bioresource  Technology, 102(3): 2185&ndash;2192, ISSN: 0960-8524, DOI:  10.1016/j.biortech.2010.09.112.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Rodrigues, L. S., da Silva, I. J., Zocrato, M. C. de O., Papa, D. N.,  Sperling, M. V. &amp; de Oliveira, P. R. 2010. &ldquo;Avalia&ccedil;&atilde;o de desempenho de  reator UASB no tratamento de &aacute;guas residu&aacute;rias de suinocultura&rdquo;. Revista  Brasileira de Engenharia Agr&iacute;cola e Ambiental, 14(1): 94&ndash;100, ISSN: 1807-1929,  DOI: 10.1590/S1415-43662010000100013.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Rodr&iacute;guez, D. 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Atmospheric Environment, 94: 458&ndash;466, ISSN: 1352-2310, DOI:  10.1016/j.atmosenv.2014.05.041.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Sakar,  S., Yetilmezsoy, K. &amp; Kocak, E. 2009. &ldquo;Anaerobic digestion technology in  poultry and livestock waste treatment - a literature review&rdquo;. Waste Management  &amp; Research, 27(1): 3&ndash;18, ISSN: 0734-242X, DOI: 10.1177/0734242X07079060.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">S&aacute;nchez, E., Borja, R., Travieso, L., Mart&#305;&#769;n, A. &amp; Colmenarejo, M. F.  2005. </span><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">&ldquo;Effect of organic loading rate on the stability, operational  parameters and performance of a secondary upflow anaerobic sludge bed reactor  treating piggery waste&rdquo;. Bioresource Technology, 96(3): 335&ndash;344, ISSN:  0960-8524, DOI: 10.1016/j.biortech.2004.04.003.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Shanmugam,  P. &amp; Horan, N. J. 2009. &ldquo;Optimising the biogas production from leather  fleshing waste by co-digestion with MSW&rdquo;. Bioresource Technology, 100(18):  4117&ndash;4120, ISSN: 0960-8524, DOI: 10.1016/j.biortech.2009.03.052.</span></p>     ]]></body>
<body><![CDATA[<p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Solli,  L., Bergersen, O., S&oslash;rheim, R. &amp; Briseid, T. 2014. &ldquo;Effects of a gradually  increased load of fish waste silage in co-digestion with cow manure on methane  production&rdquo;. Waste Management, 34(8): 1553&ndash;1559, ISSN: 0956-053X, DOI:  10.1016/j.wasman.2014.04.011.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Song,  M., Shin, S. G. &amp; Hwang, S. 2010. &ldquo;Methanogenic population dynamics  assessed by real-time quantitative PCR in sludge granule in upflow anaerobic  sludge blanket treating swine wastewater&rdquo;. Bioresource Technology, 101(1):  S23&ndash;S28, ISSN: 0960-8524, DOI: 10.1016/j.biortech.2009.03.054.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Sosa, R.,  D&iacute;az, Y. M., Cruz, T. &amp; de la Fuente, J. L. 2014. &ldquo;Diversification and  overviews of anaerobic digestion of Cuban pig breeding&rdquo;. Cuban Journal of  Agricultural Science, 48(1): 67&ndash;72, ISSN: 2079-3480.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Teixeira,  C. G., P&eacute;rez, T.P., Pereda, R. I., Oliva, M. D., Zaiat, M. &amp; Hong, K. W.  2014. &ldquo;Mathematical Modeling of the Hydrodynamics of an EGSB Reactor&rdquo;. Journal  of Chemistry and Chemical Engineering, 8(6): 602&ndash;610, ISSN: 1934-7375.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Torkian,  A., Eqbali, A., Hashemian, S.J. 2003. &ldquo;The effect of organic loading rate on  the performance of UASB reactor treating slaughterhouse effluent&rdquo;. Resources  Conservation and Recycling, 40: 1&ndash;11,</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Villamar,  C.A., Rodr&iacute;guez, D.C., L&oacute;pez, D., Pe&ntilde;uela, G. &amp; Vidal, G. 2013. &ldquo;Effect of  the generation and physical&ndash;chemical characterization of swine and dairy cattle  slurries on treatment technologies&rdquo;. Waste Manage Res., 31(8): 820&ndash;828</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Weiland,  P. 2010. &ldquo;Biogas production: current state and perspectives&rdquo;. Applied  Microbiology and Biotechnology, 85(4): 849&ndash;860, ISSN: 0175-7598, 1432-0614,  DOI: 10.1007/s00253-009-2246-7.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; color:windowtext; ">Yu, D.,  Kurola, J. M., L&auml;hde, K., Kym&auml;l&auml;inen, M., Sinkkonen, A. &amp; Romantschuk, M.  2014. &ldquo;Biogas production and methanogenic archaeal community in mesophilic and  thermophilic anaerobic co-digestion processes&rdquo;. Journal of Environmental  Management, 143: 54&ndash;60, ISSN: 0301-4797, DOI: 10.1016/j.jenvman.2014.04.025.</span></p>     <p align="justify" class="referencias" style="margin-top:5.95pt;margin-right:0cm;margin-bottom:.0001pt;margin-left:0cm;text-indent:0cm;"><span style="font-family:'Verdana','sans-serif'; font-size:10.0pt; ">Zaiat, M., Rodrigues, J. A.  D., Ratusznei, S. M., de Camargo, E. F. M. &amp; Borzani, W. 2001. &ldquo;Anaerobic  sequencing batch reactors for wastewater treatment: a developing technology&rdquo;.  Applied Microbiology and Biotechnology, 55(1): 29&ndash;35, ISSN: 0175-7598,  1432-0614, DOI: 10.1007/s002530000475</span><font size="2" face="Verdana, Arial, Helvetica, sans-serif">.</font></p>     <p align="justify">&nbsp;</p>     ]]></body>
<body><![CDATA[<p align="justify">&nbsp;</p>     <p align="justify"><font size="2" face="Verdana, Arial, Helvetica, sans-serif">Received: 19/10/2016    <br>   Accepted: 5/12/2016</font></p>     <p align="justify">&nbsp;</p>     <p align="justify">&nbsp;</p>     <p align="justify"><font size="2" face="Verdana, Arial, Helvetica, sans-serif"><i>Tania Pérez- Pérez,</i> Instituto de Ciencia Animal, Apartado Postal 24, San José de las Lajas, Mayabeque.    Email: <a href="mailto:taniap@ica.co.cu">taniap@ica.co.cu</a></font></p>      ]]></body><back>
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