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Depuración de aguas servidas. Estudio de caso en San Isidro de Patulú= .=

Treatment of Wastewater: A Case Study in San Isidro de Patulú.

= ¹	Alex Xavier Frías Torres	https://orcid.org/0000-0002-7433-819X
	Magister en Sistem= as de Gestión Ambiental, Universidad Técnica de Ambato, Ambato, Ecuador. ax.frias@uta.edu.ec
= ²	Danny Germán Muyul= ema Muyulema	https://orcid.org/0009-0006-7113-0752
	Magister en Estructuras Metálicas, Uni= versidad Técnica de Ambato, Ambato, Ecuador. dg.muyulema@uta.edu.ec
= ³	Galo Wilfrido Núńez Aldás	https://orcid.org/0000-0001-7087-1213
	Magister en Docenc= ia y Currículo para la Educación Superior, Universidad Técnica de Ambato, Amba= to, Ecuador. gw.nunez@uta.edu.ec
= ⁴	Edgar Patricio Chu= sin Vega	https://orcid.org/0009-0008-3258-9987
	Estudiante, Univer= sidad Técnica de Ambato, Ambato, Ecuador. echusin5781@uta.edu.ec

	Artículo de Investigación Científica y Tecnológica Enviado: 14/11/2024 Revisado: 18/12/2024 Aceptado: 15/01/2025 Publicado: 17/02/2025 DOI: https://doi.org/10.33262/ap.v7i1.1.580 <= /o:p>
<= span lang=3DEN-US style=3D'font-size:8.0pt;line-height:115%;font-family:"Times= New Roman",serif; mso-fareast-font-family:"Times New Roman";color:blue;mso-ansi-language:EN= -US'>
&= nbsp; Cítese: <= /b>		Frías Torres, A. X., Muyulema Muyulema, D. G., Núńez Aldás, G. W., & Chusin Vega, E. P. (2025). Depuración de aguas servidas. Estudio de caso en San Isidro de Patulú. AlfaPublicaciones, 7(1.1), 30–48. https://doi.org/10.33262/= ap.v7i1.1.580
		ALFA PUBLICACIONES, es una revista multidisciplinar= , trimestral, que se publicará en soporte electrónico tiene como misión contribu= ir a la formación de profesionales competentes con visión humaníst= ica y crítica que sean capaces de exponer sus resultados investigativos y científicos en la misma medida que se promueva mediante su intervención cambios positivos en la sociedad. https://alfapublicaciones.com La revista es editada por la Editorial Ciencia Digital (Editorial de prestigio registrada en la Cámara Ecuatoriana de Libro con No de Afiliación 663) www.celibro.org.ec
		Esta revista está protegida ba= jo una licencia Creative Commons Attribution Non Commercial No Derivatives 4= .0 International. Copia de la licencia: http://creativecommons.org/licenses/by-nc-sa/4.0/ <= span style=3D'font-size:8.0pt;line-height:115%;font-family:"Times New Roman",s= erif; mso-fareast-font-family:"Times New Roman"'>
Palabras claves: Planta de Tratamiento de Aguas Residuales (PTAR), Santa Rosa, San Francisco, límites permisibles, río Gu= ano.		Resumen: El presente estudio tiene como objetivo el diseńo de una Planta de Tratamiento de Agu= as Residuales (PTAR) para las comunidades Santa Rosa y San Francisco de la parroquia San Isidro de Patulú, con el fin de reducir la carga contaminan= te de las aguas residuales y garantizar su cumplimiento con los límites máxi= mos permisibles establecidos por la normativa vigente. Se realizó una caracterización del agua residual en la que se identificaron parámetros físico-químicos clave, destacándose la Demanda Química de Oxígeno (DQO), = la Demanda Bioquímica de Oxígeno (DBO5) y el Nitrógeno Total como principales contaminantes que exceden los límites normativos. Con base en estos resultados, se diseńó una línea de tratamiento eficiente que permite una reducción significativa de los contaminantes presentes en el agua residua= l. La evaluación de la eficiencia del tratamiento implementado demostró que = los valores de DQO, DBO5 y Nitrógeno Total fueron reducidos a niveles dentro = de los límites permisibles, permitiendo que el agua tratada pueda ser descar= gada al río Guano. Se diseńó una Planta de Tratamiento de Aguas Residuales (PT= AR) que incluye procesos de cribado, seguidos de dos tanques de sedimentación= , un filtro anaeróbico de flujo ascendente (FAFA) y un lecho de secado para la gestión de los lodos, garantizando que la descarga final cumpla con los requisitos ambientales establecidos. Este estudio proporciona una base técnica y científica para la implementación de una PTAR funcional y efici= ente en la zona de estudio, contribuyendo a la mitigación del impacto ambiental generado por las aguas residuales y promoviendo el uso sostenible de los recursos hídricos.
Keywords: Wastewater Treatment Plant (WWTP), Santa Rosa, San Francisco, permissible limits, Guano River.	&= nbsp;	Abstract This study aims to design a Wastewater Treatment Plant (WWTP) for the communities of Santa Rosa and S= an Francisco in the parish of San Isidro de Patulú, with the purpose of redu= cing the pollutant load of the wastewater and ensuring compliance with the max= imum permissible limits established by current regulations. A characterization= of the wastewater was conducted, identifying key physico-chemical parameters, with Chemical Oxygen Demand (COD), Biochemical Oxygen Demand (BOD5), and Total Nitrogen standing out as the main pollutants exceeding regulatory limits. Based on these results, an efficient treatment line was designed, allowing for a significant reduction of the pollutants present in the wastewater. The evaluation of the treatment efficiency demonstrated that = COD, BOD5, and Total Nitrogen values were reduced to levels within permissible limits, allowing the treated water to be discharged into the Guano River.= A Wastewater Treatment Plant (WWTP) was designed, which includes screening processes, followed by two sedimentation tanks, an upflow anaerobic filter (UAFF), and a drying bed for sludge management, ensuring that the final discharge meets the established environmental requirements. This study provides a technical and scientific basis for the implementation of a functional and efficient WWTP in the study area, contributing to the mitigation of the environmental impact generated by wastewater and promot= ing the sustainable use of water resources.

1. Introducción<= /b>

En = la parroquia de San Isidro de Patulú, comunidades como la de Santa Rosa y San francisco enfrentan importantes desafíos relacionados con la provisión de servicios básicos de saneamiento. Según datos del Instituto Nacional de Estadísticas y Censos (Terán & Cand= o, 2023) pr= esentan una baja cobertura del alcantarillado alcanzando solo el 23,9% de viviendas. En relación con los residuos líquidos, según el Gobierno Autónomo Descentraliz= ado Parroquial de San Isidro de Patulú (GAD Parroquial = de San Isidro de Patulú, 2020) plantea que en tres de los seis cantones implementan procesos de tratamiento de aguas residuales, contando con un total de nueve plantas de tratamiento convencionales y cuatro plantas que utilizan digestión anaeróbi= ca.

En función de ADDIN ZOTERO_I= TEM CSL_CITATION {"citationID":"oUN0psQ2","properties":{"= formattedCitation":"(Botturi et\\uc0\\u160{}al., 2021)","plainCitation":"(Botturi et al., 2021)","noteIndex":0},"citationItems":[{"id&q= uot;:127,"uris":["http://zotero.org/users/16204466/items/2VT= FHG89"],"itemData":{"id":127,"type":&quo= t;article-journal","abstract":"Combined sewer overflows (CSOs) are of major environmental concern for impacted surf= ace waterbodies. In the last decades, major storm events have become increasing= ly regular in some areas, and meteorological scenarios predict a further rise = in their frequency. Consequently, control and treatment of CSOs with respect to best practice examples, innovative treatment solutions, and management of s= ewer systems are an inevitable necessity. As a result, the number of publications concerning quality, quantity, and type of treatments has recently increased. This review therefore aims to provide a critical overview on the effects, control, and treatment of CSOs in terms of impact on the environment and pu= blic health, strict measures addressed by regulations, and the various treatment alternatives including natural and compact treatments. Drawing together the previous studies, an innovative treatment and control guideline are also proposed for the better management practices.","container-title":"Critical Reviews in Environmental Science and Technology","DOI":"10.1080/10643389.2020.1757957",= "ISSN":"1064-3389","issue":"15",&qu= ot;note":"publisher: Taylor & Francis\n_eprint: https://doi.org/10.1080/10643389.2020.175795= 7","page":"1585-1618","source":"Tay= lor and Francis+NEJM","title":"Combined sewer overflows: A critical review on best practice and innovative solutions to mitigate impac= ts on environment and human health","title-short":"Combined sewer overflows","volume":"51","author":= [{"family":"Botturi","given":""},{&= quot;family":"Ozbayram","given":"E. Gozde"},{"family":"Tondera","given":&quo= t;Katharina"},{"family":"Gilbert","given"= ;:"Nathalie I."},{"family":"Rouault","given":"P= ascale"},{"family":"Caradot","given":&qu= ot;Nicolas"},{"family":"Gutierrez","given&quo= t;:"Oriol"},{"family":"Daneshgar","given= ":"Saba"},{"family":"Frison","given= ":"Nicola"},{"family":"Akyol","give= n":"Çağrı"},{"family":"Foglia"= ,"given":"Alessia"},{"family":"Eusebi&qu= ot;,"given":"Anna Laura"},{"family":"Fatone","given":"= ;Francesco"}],"issued":{"date-parts":[["2021&= quot;]]}}}],"schema":"https://github.com/citation-style-lang= uage/schema/raw/master/csl-citation.json"} (Botturi et = al., 2021) la disponibilidad de servicios básicos, como el alcantarillado sanit= ario y el tratamiento de aguas residuales mediante plantas de tratamiento, constituye un indicador clave para evaluar la calidad de vida, la salud púb= lica y la sostenibilidad ambiental.

Además, seg= ún la Organización Mundial de la Salud (OMS, 2024= ) a nivel global, el 44% de las aguas residuales de origen doméstico fueron descargadas sin haber recib= ido un tratamiento adecuado para garantizar su seguridad y según estimaciones, aproximadamente una décima parte de la población global ingiere productos cultivados con el uso de aguas residuales. Este estudio es pertinente debid= o a la creciente preocupación por la contaminación hídrica y sus efectos en la salud humana y el ecosistema. La falta de tratamiento de aguas residuales en las comunidades de Santa Rosa y San Francisco no solo representa un riesgo sanitario, sino que también limita el desarrollo socioeconómico de la zona. Implementar una solución técnica y sostenible es fundamental para cumplir c= on los Objetivos de Desarrollo Sostenible (Naciones Unidas, 2023) particularmente el ODS = 6, que busca garantizar la disponibilidad de agua limpia y saneamiento para to= dos.

El problema científico central de esta investigación radica en la falta de datos específicos sobre= la composición y carga contaminante de las aguas residuales en las comunidades= de Santa Rosa y San Francisco, debido a que no existe alcantarillado sanitario= lo que dificulta el diseńo de sistemas de tratamiento eficientes y adaptados a= sus necesidades. Este estudio busca generar información técnica en base a la caracterización del afluente de la Planta de Tratamiento= de Aguas Residuales (PTAR) San Isidro 1 que permitió seleccionar y dimensionar tecnologías adecuadas para el tratamiento de aguas residuales en contextos rurales. La caracterización de las aguas residuales también forma parte impo= rtante de la selección de las tecnologías seleccionadas puesto que influyen sobre = los sistemas de saneamiento optimizando su diseńo y seguridad (Morales Corozo &= amp; Loor Vergara, 2023). Esta caracterización conste del tipo de efluentes de la concentración promedio de contaminantes = en las aguas sabiendo que las altas cargas orgánicas requieren de proceso biológicos intensivos para su tratamiento. Esta evaluación se realiza por parámetros químicos como la demanda bioquímica de oxígeno (DBO), la demanda química de oxígeno (DQO) y de los sólidos suspendidos totales (STT), ya que esto permite que los tanques de sedimentación, reactores biológicas y filtr= os sean dimensionados adecuadamente (Hur et al., 2010). <= o:p>

De acuerdo con ADDIN ZOTERO_I= TEM CSL_CITATION {"citationID":"9uVqd5Jg","properties":{"= formattedCitation":"(Osorio Rivera et\\uc0\\u160{}al., 2021)","plainCitation":"(Oso= rio Rivera et al., 2021)","noteIndex":0},"citationItems":[{"id&q= uot;:131,"uris":["http://zotero.org/users/16204466/items/UR2= Z6RAY"],"itemData":{"id":131,"type":&quo= t;article-journal","abstract":"Las aguas residuales domésticas conocidas también con el nombre de aguas servid= as, son aquellas que tienen origen en las actividades de la rutina diaria del s= er humano, las descargas son a través de sistemas de alcantarillado o de vertimientos directos sobre el ambiente. La composición de las aguas residu= ales domésticas es muy variada y manifiesta características fisicoquímicas y biológicas muy alteradas, las cuales en tal estado no son aptas para el con= sumo humano, es por ello que hace falta un especial tratamiento, dentro de los principales constituyentes que se pueden encontrar dentro de estas tenemos a los sólidos suspendidos totales, compuestos orgánicos biodegradables, const= ituyentes inorgánicos disueltos, metales pesados, nutrientes, y polutantes orgánicos prioritarios. La caracterización de las aguas residuales domésticas se basa= en determinar el olor, color, temperatura, densidad, turbiedad, sólidos totale= s, nitratos, sulfatos, cromo, hierro, cloruros, calcio, zinc, y el pH.","container-title":"Polo del Conocimiento: Revista científico - profesional","ISSN":"2550-682X","issue":= "3","language":"spa","note":"p= ublisher: Coni\nsection: Polo del Conocimiento: Revista científico - profesional","page":"228-245","source":&= quot;dialnet.unirioja.es","title":"La calidad de las aguas residuales domésticas","volume":"6","author":[{&quo= t;family":"Osorio Rivera","given":"Miguel A."},{"family":"Carrillo Barahona","given":"Willian Estuardo"},{"famil= y":"Negrete Costales","given":"José Hernán"},{"family":"Loor Lalvay","given":"Xavier Antonio"},{"family":"Riera Guachichullca","given":"Erick Javier"}],"issu= ed":{"date-parts":[["2021"]]}}}],"schema"= ;:"https://github.com/citation-style-language/schema/raw/master/csl-ci= tation.json"} (Osorio Rivera et al., 2021) en el ámbito del tratamiento de aguas residuales, se han realizado investigaciones enfocadas en evaluar la calidad de estas aguas mediante su caracterización, considerando parámetros físicos, químicos y biológicos. Es= tos estudios buscan determinar el tipo de tratamiento más adecuado en función d= e la concentración de dichos parámetros, tomando en cuenta que estas característ= icas pueden presentar variaciones significativas.

En Ecuador, (Mena et al., 2017) desarrollaron un prototipo de laboratorio donde replicaron las condiciones del agua residual en su estado original. Su propósito fue diseń= ar una PTAR para un caudal de 55.21 litros por día, enfatizando la posibilidad= de reutilizar el agua tratada en el riego de áreas verdes. A partir de su estu= dio, concluyeron que el sistema de lodos activados es el más eficiente para este proceso.

Este estudio se enfoca e= n el diseńo de una planta de tratamiento de aguas residuales para un caudal de 4= .97 l/s destinada a las comunidades de Santa Rosa y San Francisco, en el cantón Gua= no, provincia de Chimborazo. La iniciativa busca abordar la problemática del ma= nejo inadecuado de aguas residuales en la zona, con el fin de mitigar los impact= os ambientales y sanitarios. Además, se pretende promover la reutilización del agua tratada en actividades como la agricultura, optimizando los recursos hídricos y fomentando prácticas sostenibles que beneficien a la población l= ocal y su entorno.

2.&n= bsp; Metodología

Este estudio se enmarca en una investigación de tipo aplicada o práctica, c= uyo propósito es generar soluciones concretas para mejorar la calidad de vida de las comunidades de Santa Rosa y San Francisco, en el cantón Guano, provinci= a de Chimborazo, mediante el diseńo de una planta de tratamiento de aguas residuales.

Desde el punto de vista metodológico, la investigación adopta un enfoque cuantitativo, ya que se basa en la medición numérica de los pa= rámetros físico, químicos y microbiológico de las aguas residuales, tales como la demanda bioquímica de oxígeno (DBO), la demanda química de oxígeno (DQO) y = los sólidos suspendidos totales (SST). Estos parámetros permiten caracterizar l= as aguas residuales y fundamentar el diseńo de la planta de tratamiento, asegu= rando que los resultados sean precisos, confiables y replicables.

La investigación combina dos fuentes principales de datos: documental y de campo. En la fase documental, se real= izó una revisión exhaustiva de literatura científica, normativas ambientales y = estudios previos relacionados con el tratamiento de aguas residuales en contextos rurales. Esta revisión permitió identificar las tecnologías más adecuadas y= los estándares de calidad aplicables. Se llevó a cabo la recolección directa de muestras de aguas residuales cercanas a las comunidades de estudio, así com= o la observación y registro de las condiciones actuales de saneamiento.

Para ello, según el Instituto Ecuatoriano de Normalización (INEN, 2013) se recolectó = una muestra compuesta del agua residual. Esta muestra se obtuvo tomando varias submuestras durante un período de 6 horas, con intervalos de 1 hora, las cu= ales se almacenaron en un envase de vidrio de 1 litro, un envase de plástico de 1 litro y dos envases de plástico adicionales destinados al análisis bacteriológico. Posteriormente, las muestras fueron transportadas al laboratorio LABCESTTA en la ciudad de Riobamba para su caracterización. Esta norma específica que las muestras deben estar debidamente identificadas con información como la fecha de recolección, el tipo de agua, el lugar de recolección y el nombre del recolector. Además, para las muestras destinada= s a la determinación de parámetros físicos y químicos, se requiere que los enva= ses se llenen completamente, evitando la presencia de aire, mientras que, para = el análisis bacteriológico, debe dejarse un espacio de aire en el envase. Finalmente, las muestras se transportaron en un cooler con ice packs para mantener las condiciones adecuadas hasta su llegada al laboratorio.

Estas actividades se realizaron con el fin de obtener datos reales y representati= vos de la situación local, en base a la tabla 9 del Texto Unificado de Legislac= ión Secundaria del Ministerio del Ambiente (Asamblea Nacional Constituyente del Ecuador, 2015) permitieron establecer la línea de tratamiento necesaria para lograr que la calidad del efluente cumpla con los límites de descarga a un cuerpo de agua dulce.=

La población de estudio está conformada por las aguas residuales domésticas generad= as en San Isidro de Patulú, ubicada a 2 km de las comunidades de estudio debido a= la inexistencia de alcantarillado en el sector. El criterio de selección esta acorde a la similitud de las características económicas, sociales y geográf= icas identificadas entre las comunidades mencionadas. Los criterios de inclusión consideran muestras de agua provenientes de viviendas conect= adas al sistema de alcantarillado y que no hayan sido tratadas previamente. Estos criterios aseguran que los datos obtenidos sean representativos de la problemática específica de las comunidades.

Es importante seńalar que la selección del caudal de diseńo es un aspecto crítico en el dimensionamiento de una Planta de Tratamiento de Aguas Residuales (PTAR), ya que determina la capacidad operativa del sistema y garantiza su eficiencia a lo largo del tiempo. En el caso de las comunidade= s de Santa Rosa y San Francisco, en el cantón Guano, provincia de Chimborazo, el caudal de diseńo fue de 4.96 l/s obtenido luego del diseńo de la red de alcantarillado sanitario.

El diseńo de la planta de tratamiento de aguas residuales se realizó siguiendo= los lineamientos técnicos establecidos por la Secretaría del agua (Secreta= ría del Agua, 2012) en la "N= orma para estudio y diseńo de sistemas de agua potable y disposición de aguas residuales para poblaciones mayores a 1000 habitantes".

Para el dimensionamiento de las unidades de tratamiento, se adoptaron metodologí= as reconocidas a nivel internacional. En particular, según la (Comisión Nacional del Agua, 2016b) se diseńó el cribado y el sedimentador primario. Luego, en base a la (Comisión Nacional del Agua, 2016a) se usaron los criterios para el filtro anaerobio de flujo ascendente (FAFA), garantizando eficiencia en la remoción de sólidos y materia orgánica.<= /p>
Asimismo, se diseńó el lecho de secado de lodos fundamentándose en las especificacion= es técnicas descritas en la "Guía para el diseńo de tanques sépticos, tan= ques Imhoff y lagunas de estabilización" de acuerdo con la Organización Panamericana de la Salud (OPS, 2005= ). Esta referen= cia proporciona criterios específicos para el manejo y disposición final de los lodos generados en el proceso de tratamiento, asegurando una gestión adecua= da y sostenible.

En cuanto a los aspectos éticos, este estudio contó con la autorización d= el Gobierno Autónomo Descentralizado del cantón Guano. Se obtuvo el consentimiento informado de los representantes de las comunida= des de Santa Rosa y San Francisco, quienes fueron informados detalladamente sob= re los objetivos, procedimientos y beneficios de la investigación. Además, se garantizó la confidencialidad de los datos y el respeto a los derechos de l= as comunidades involucradas, asegurando que la investigación se realice bajo l= os más altos estándares éticos.

En resumen, esta metodología combina enfoques cuantitativos, técnicas de campo= y revisión documental para diseńar una planta de tratamiento de aguas residua= les que responda a las necesidades específicas de las comunidades estudiadas. L= os resultados obtenidos no solo contribuirán al mejoramiento de las condicione= s de vida en la región, sino que también servirán como base para futuras investi= gaciones en el campo del saneamiento ambiental.

3. Resultados

La caracterización del agua residual tomada de la Planta de Tratamiento de Agu= as Residuales (PTAR) San Isidro 1 proporciona datos fundamentales para el dise= ńo del sistema de tratamiento, permitiendo evaluar la calidad del afluente y su impacto en el medio ambiente. Se identificaron parámetros que cumplen con l= os límites normativos, lo que sugiere estabilidad en ciertos componentes y una adecuada capacidad de autodepuración en algunos aspectos del agua residual.= No obstante, se evidenció que ciertos indicadores asociados a la carga orgánic= a y al contenido nitrogenado superan los valores permitidos, como se muestra en= la Tabla 1, lo que resalta la necesidad de aplicar procesos específicos de tratamiento para su reducción. Esto implica la implementación de tecnologías que optimicen la remoción de contaminantes y garanticen la calidad del efluente final, asegurando su viabilidad para un posible reúso o su disposición en cuerpos hídricos sin comprometer el equilibrio ecológico.

Tab= la 1

Caracterización del agua residual de la PTAR San Isidro I

Determinaciones=	Unidad	Resultados<= /p>	Límite máximo permisible	Condición
pH		7.69=	6-9<= /span>	CUMPLE
DQO<= /span>	mg/l=	212<= /span>	200<= /span>	NO CUMPLE<= /o:p>
DBO5=	mg/l=	102<= /span>	100<= /span>	NO CUMPLE<= /o:p>
Sólidos suspend= idos	mg/l=	45	130<= /span>	CUMPLE
Nitrógeno Total=	mg/l=	52.12	50	NO CUMPLE<= /o:p>
Tensoactivos	mg/l=	0.45=	0.5<= /span>	CUMPLE
Aceites y Grasa= s	mg/l=	19.90	30	CUMPLE
Sólidos totales=	mg/l=	856<= /span>	1600=	CUMPLE
Cloruros	mg/l=	<10	1000=	CUMPLE
Fluoruros<= /o:p>	mg/l=	0.82=	5	CUMPLE

Fuente: Tomado de Laboratorio LABCESSTA (2024).

Considerando lo expuesto anteriormente, la propuesta de tratamiento contempla una serie = de etapas que incluyen un proceso de cribado, la incorporación de dos tanques = de sedimentación, un filtro anaeróbico de flujo ascendente (FAFA) y un lecho de secado diseńado para el manejo adecuado de los lodos, como se observa en la= Figura 1. <= /p>

Fig= ura <= span style=3D'font-size:12.0pt;line-height:115%;font-family:"Times New Roman",se= rif; color:windowtext;font-style:normal'>1

Propuesta de la Planta de Tratamiento de Aguas Residuales

Fuente: Elaboración propia.=

Como parte del pretratamiento, se diseńó una criba con el propósi= to de evitar obstrucciones en las etapas posteriores causadas por sólidos grue= sos y materiales fibrosos. El canal de aproximación se dimensionó con= una velocidad de 0.44 m/s, valor que se encuentra dentro del rango recomendado.= Al asumir un ancho de canal de 0.30 m, se determinó un tirante de 0.14 m y se adoptó un borde libre de 0.50 m. Para la reja de cribado, se seleccion= aron barras rectangulares de 9 mm de espesor, espaciadas a 25 mm, lo que resultó= en un total de 9 barras dispuestas con una inclinación de 45°, como se muestra= en la Tabla 2.

De acuerdo con la (Comisión Nacional del Agua, 2016b) el diseńo de cribado con limpieza manual presenta varias ventajas en el tratamiento de a= guas residuales. En primer lugar, es una opción de bajo costo en términos de inversión inicial y mantenimiento, ya que no requiere sistemas automatizados complejos. Además, permite una mayor flexibilidad en la operación, ya que l= os operadores pueden ajustar la frecuencia de limpieza según las condiciones específicas del flujo y la cantidad de sólidos presentes, lo que garantiza = una mayor eficiencia en la remoción de materiales gruesos. Este tipo de diseńo también facilita la inspección directa y la identificación de posibles problemas en el sistema de cribado, permitiendo intervenciones rápidas y oportunas. Finalmente, la limpieza manual reduce la posibilidad de obstrucciones o fallos mecánicos que podrían ocurrir en sistemas automatiza= dos, lo que aumenta la confiabilidad del proceso.

Tab= la 2

Resultados del diseńo del cribado

Parámetro de diseńo	Valores
Ancho del canal	0.3 m
β	2.42 (Barra rectangular)<= /span>
Espesor de la barra	9 mm
Separación entre barras	25 mm
Velocidad en las barras	0.44 m/s
Ángulo de inclinación de las barras<= o:p>	45 °
Coeficiente de rugosidad del canal	0.013 (Hormigón)
Eficiencia de las barras<= /span>	73.53 %
Área útil del canal	0.0314 m²
Área del canal	0.0428 m²
Tirante máximo del canal<= /span>	0.1426 m
Radio hidráulico del canal	0.0731 m
Pendiente del canal	0.11 %

Tab= la 2

Resultados del diseńo del cribado (continuación)

Parámetro de diseńo	Valores
Velocidad del canal	0.44 m/s = (Cumple 0.4 m/s a 0.75 m/s)
Número de barras	9
Pérdida de energía en la rejilla	0.01835 m
Pérdida de carga total en la rejilla=	0.008041 m
Velocidad de las rejas con 50% de obstrucción	1.2 m/s
Pérdida de carga total con 50% de obstrucción	0.07864 m
Borde Libre	0.50 m
Altura útil de la reja	0.64 m
Altura asumida	0.7 m
Longitud de la reja	1 m
Proyección horizontal de la reja	0.7 m

Fuente: Elaboración propia.

En el tratamiento primario, cuyo objetivo es la remoción de sólidos sedimentables, tanto orgánicos como inorgánicos, se optó por un sedimentador primario. Se diseńaron dos tanques sedimentadores, cuyo cálculo hidráulico se basó en una carga superficial de 40 mł/m˛/día. Esto permitió establecer un ancho de 1.6 m y, considerando una relación largo-an= cho de 3, se determinó una longitud de 4.8 m. El volumen total del sedimentador= es de 11.52 mł. Además, se verificó que el tiempo de retención hidráulica de 1= .29 horas se encuentra dentro de los rangos permisibles. Con una eficiencia de remoción del 30% para la DBO₅ y del 50% para los sólidos suspendidos,= se proyecta que el afluente tendrá concentraciones de 71.40 mg/l y 22.50 mg/l, respectivamente, como se muestra en la Tabla 3.

En el sedimentador primario, la relación entre la velocidad de arrastre de 0.2= 27 m/s y la velocidad horizontal a flujo máximo de 0.00393 m/s es fundamental = para optimizar el proceso de sedimentación y garantizar una eficiente remoción de sólidos suspendidos. La velocidad de arrastre, que se refiere a la velocida= d a la cual el agua fluye a través del sedimentador, influye directamente en la capacidad del sistema para movilizar los sólidos hacia el fondo del tanque, facilitando su posterior remoción. En contraste, la velocidad horizontal a flujo máximo es la velocidad del agua en la dirección del flujo principal d= el sedimentador, y su valor relativamente bajo asegura un tiempo adecuado de sedimentación para los sólidos, evitando la re-suspensión de los mismos. La combinación de estas dos velocidades garantiza un balance adecuado entre la= eficiencia de la remoción de sólidos y la minimización de la re-suspensión, lo que res= ulta en un desempeńo óptimo del sedimentador primario en el tratamiento de aguas residuales.

Tab= la 3

Resultados del diseńo del sedimentador primario

Parámetro de diseńo	Valores
Número de sedimentadores<= /span>	2
Carga superficial<= /p>	40 m³/m²/d
Diámetro de la partícula<= /span>	0.2 mm
Densidad relativa de la partícula	2.65
Factor de fricción=	0.02
Pendiente fondo del sedimentador	10%
Pendiente canal de limpieza	5%
Área del sedimentador	5.36 m²
Ancho	1.34 m
Ancho asumido	1.6 m
Longitud calculada=	4.8 m
Volumen del sedimentador<= /span>	11.52 m³
Comprobación del tiempo de retención=	1.55 h (Cumple rango 1.5 h a 2.5 = h)
Velocidad de arrastre	0.227 m/s (Cumple < 1.5 m/s)
Velocidad horizontal a flujo máximo<= o:p>	0.00393 m/s (Cumple Va>V_L=)
Comprobación relación S	3 (Cumple rango de 3-10)=
Comprobación relación D	3.2 (Cumple <30)
Borde libre	0.50 m
Altura natas	0.10 m
Remoción de DBO5 y SS
Velocidad de paso en orificios<= /o:p>	0.15= m/s (Cumple rango de 0.1-0.2 m/s)
Área total de orificios	0.01= 66 m²
Diámetro asumido de orificios	0.05= m
Área del orificio<= /p>	0.00= 196 m²
Número de orificios calculada	8.43=
Número de orificios adoptada	9
Altura de pantalla para los orificio= s	1.8 = m

Fuente: Elaboración propia.

Para el tratamiento secundario, se propuso la implementación de un filtro anaeró= bico de flujo ascendente (FAFA), una tecnología que se caracteriza por su alta eficiencia en la remoción de materia orgánica, su capacidad para adaptarse a variaciones en los caudales de entrada y su bajo costo operativo. En su dis= eńo, se asumió una carga hidráulica de 10 mł/m˛/día, lo que permitió calcular un diámetro de 5.25 metros para el sistema. Al considerar una carga orgánica de 0.40 kg DBO/mł/día, se determinó un volumen de tratamiento necesario de 38.= 29 mł, como se muestra en la Tabla 4. Además, con un lecho filtrante compuesto por grava y una altura de 1.80 metros, se obtuvo un volumen total para el filtro de 47.62 mł, lo que excede ligeramente el volumen requerido.= El tiempo de retención hidráulica dentro del tanque es de 5.33 horas, lo que se encuentra dentro del rango recomendado para este tipo de procesos, y se log= ró una eficiencia en la remoción de materia orgánica del 62.31%. Este sistema,= por su bajo costo y capacidad de adaptación, representa una opción viable para = el tratamiento eficiente de aguas residuales en diferentes contextos operativo= s.

Tab= la 4

Resultados del diseńo del FAFA

Parámetro de diseńo

Valores

Carga hidráulica

10 m³/m²/d

Carga orgánica volumétrica

0.40 kg DBO5 m³/d

Área del filtro

21.44 m²

Diámetro del filtro

5.22 m

Diámetro del filtro asumido

5.25 m

Volumen del lecho filtrante

38.29 m³

Altura del medio filtrante

1.79 m

Altura asumida del medio filtrante

1.8 m

Altura del falso fondo del filtro

0.30 m

Altura del bloque de HS <= /span>

0.10 m

Borde libre

0.50 m

Volumen real del filtro

47.62 m³ (Mayor a 104.= 39 m³)

Carga orgánica volumétrica calculada=

0.32 kg DBO5 m³/d (Cum= ple rango entre 0.15 a 0.5)

Tiempo de retención calculado

5.33 h (Cumple rango entre 5 y 10= h)

Eficiencia de remoción

62.31 %

Concentración del DBO5 en el efluent= e

26.91 mg/l

Fuente: Elaboración propia.

Finalmente, para la deshidratación de lodos estabilizados, se seleccionó la opción más económica, el lecho de secado de lodos. Se calculó la carga= de sólidos en función del contenido de sólidos en el agua residual, asumiendo = una densidad de lodos de 1.03 kg/l y un período de secado de 55 días. Esto resu= ltó en un volumen de lodos a extraer de 12.24 mł. Considerando una profundidad = de aplicación de 25 cm y dos divisiones, el área unitaria por lecho es de 24.48 m˛, por lo que se adoptó un ancho de 4 m y una longitud de 6.6 m. Además, s= egún (Tilley et al., 2014) la capacidad = de eliminación de nitrógeno es reducida, alcanzando generalmente un máximo del= 15% en relación con el nitrógeno total, en este caso se consideró el 10%, como = se muestra en la Tabla 5.

De acuerdo con (Alzate Lina, 202= 1) el diseńo de lecho de secado de lodos ofrece varias ventajas económicas significativas e= n el tratamiento de aguas residuales. En primer lugar, este sistema reduce los costos operativos asociados con el tratamiento de lodos al aprovechar la energía solar para el proceso de secado, disminuyendo la necesidad de energ= ía eléctrica o combustibles fósiles, lo que contribuye a la sostenibilidad económica a largo plazo. Además, el lecho de secado de lodos reduce el volu= men y el peso de los lodos, lo que facilita su manejo y disposición final, resultando en menores costos de transporte y disposición en vertederos.

Tab= la 5

Resultados del diseńo del lecho de secados de lodo= s

Parámetro de diseńo

Ecuación

Gravedad específica

1.03 kg/l

Contenido de sólidos

8%

Profundidad de aplicación=

25 c= m

Periodo de aplicación

5 h<= o:p>

Periodo de secado<= /p>

55 d= ías

Periodo de remoción de lodo seco

14 d= ías

Periodo de preparación y mantenimien= to

2 dí= as

Ancho del lecho

4 m<= o:p>

Carga de sólidos

9.65 kg/d

Masa de sólidos

18.34 kg/d

Volumen diario de lodos digeridos

222.56 l/d

Volumen de lodos a extraer

12.24 m³

Área del lecho de secado<= /span>

48.96 m²

Número de divisiones

2

Área unitaria por lecho

24.48 m²

Tab= la 5

Resultados del diseńo= del lecho de secados de lodos (continuación)

Parámetro de diseńo

Ecuación

Longitud del lecho=

6.12 m

Longitud de lecho asumido=

6.6 m

Fuente: Elaboración propia.

En la Tabla 6, se observa los resultados obtenidos, evidenciando la efectividad de la línea de tratamiento implement= ada en la PTAR. Los datos reflejan una disminución considerable en la concentra= ción de los contaminantes presentes en el agua residual, lo que indica que el proceso de depuración cumple con los estándares establecidos para su posible reutilización o descarga segura en el medio ambiente.

Tab= la 6

Resultados del afluente y efluente

Determinaciones=

Unidad

Resultados=

Agua residual tratada

Límite máximo permisible

Condición<= /o:p>

DQO<= /span>

mg/l=

212<= /span>

79.90

200<= /span>

CUMPLE

DBO5=

mg/l=

102<= /span>

26.91

100<= /span>

CUMPLE

Nitrógeno Total=

mg/l=

52.12

46.91

50

CUMPLE

Fuente: Elaboración propia.

4.      Conclusiones

·      =    Se desarrolló un diseńo optimizado par= a la planta de tratamiento de aguas residuales, integrando un proceso de pretratamiento a través de un sistema de cribado. A continuación, se establ= eció un tratamiento primario compuesto por dos unidades de sedimentación. En la = fase secundaria, se aplicó un f= iltro anaeróbico de flujo ascendente (FAFA) como método de depuración biológica, concluyendo con un lecho de secado de lodos que contribuye a la eficiencia en la eliminación de contaminantes y el adecuado tratamiento del agua residual.

·      =    En el presente estudio los resultados = de la caracterización del agua residual provenientes de las comunidades estudi= adas evidencian una alta carga contaminante, con parámetros críticos como 212 mg= /l de DQO y 102 mg/l de DBO5, con una reducción del 62.31% y 73.62%, respectivamente. Además, el Nitrógeno Total se espera una remoción del 10%.= El diseńo implementado ha demostrado una significativa reducción en la concentración de estos contaminantes en el efluente, logrando cumplir con l= os límites máximos permisibles establecidos por la normativa ambiental, lo que indica = la efectividad del sistema de tratamiento propuesto.

·      =    La investigación ha permitido identifi= car y seleccionar tecnologías adecuadas para el tratamiento de aguas residuales= en contextos rurales, basándose en metodologías reconocidas internacionalmente= y en directrices de la Comisión Nacional del Agua (CONAGUA) y la Secretaría Nacional del Agua (SENAGUA). Este enfoque no solo optimiza el proceso de tratamiento, sino que también adapta la infraestructura a las realidades específicas de las comunidades, mejorando así su viabilidad y sostenibilida= d.

·      =    De esta forma, los resultados obtenidos abren la puerta a futuras investigaciones sobre el tratamiento de aguas residuales en contextos rurales, sugiriendo la necesidad de estudios adicionales que evalúen la operación a largo plazo de la Planta Tratamiento= de Aguas Residuales (PTAR), así como el impacto social y ambiental de su implementación. Además, se recomienda la exploración de innovaciones en tecnologías de tratamiento que puedan mejorar aún más la eficiencia y sostenibilidad de estos sistemas. Asimismo, se recomienda la capacitación de personal local en el manejo y operación de dichas unidades de tratamientos = para asegurar su sostenibilidad en el tiempo.

·      =    Los resultados obtenidos sugieren la necesidad de investigar más a fondo el desempeńo a largo plazo del sistema = de tratamiento, así como su impacto social y ambiental en las comunidades beneficiadas. Se recomienda llevar a cabo estudios adicionales que evalúen = la efectividad de diferentes tecnologías de tratamiento en función de las variaciones estacionales de la calidad del agua.

5.&n= bsp;     Conflicto de intereses

Los autores declaran que no existe conflicto de intereses en relación con el artículo presentado.

6.&n= bsp;     Declaración de contribución de los autores

Todos autores contribuyeron significativamente en la elaboración del artículo.

7.&n= bsp;     Costos de financiamiento

La presente investigación fue financiada en su totalidad con fondos propios de= los autores.

<= span style=3D'font-size:12.0pt;line-height:107%;font-family:"Times New Roman",se= rif; mso-fareast-font-family:"Times New Roman";color:#767171;mso-themecolor:back= ground2; mso-themeshade:128'>8.      Referencias bibliográficas

= Alzate Lina. (2021). Evaluación del dimensionamiento de los lechos de secado en diferentes Plantas de Tratamien= to de Aguas Residuales del Oriente Antioqueńo. Universidad de Antioquia. h= ttps://bibliotecadigital.udea.edu.co/bitstream/10495/21603/5/AlzateLina_202= 1_DimensionamientoLechosSecado.pdf

= Botturi, A., Ozbayram, E. G., Tondera, K., Gilbert, N. I., Rouault, P., Caradot, N., Gutierrez, O., Daneshgar, S., Frison, N., Akyol, Ç., Foglia, A., Eusebi, A.= L., & Fatone, F. (2021). Combined sewer overflows: A critical review on best practice and innovative solutions to mitigate impacts on environment and human health. <= i>Critical Reviews in Environmental Science and Technology, 51(15), 1585–1618. https://doi.org/10.1080/10643389.2020.1757957

= Comisión Nacional del Agua. (2016a). = Manual de Agua Potable, Alcantarillado y Saneamiento: Diseńo de Plantas de Tratami= ento de Aguas Residuales Municipales: Filtros Anaeróbicos y Filtros Ascendentes.= Comisión Nacional del Agua. https://sswm.info/sites/default/files/reference_attachments/CONAGUA%202015.= %20Manual%20Filtros%20anaerobios%20de%20flujo%20ascendente.pdf

= Comisión Nacional del Agua. (2016b). Manual de Agua Potable, Alcantarillado y Saneamiento: Diseńo de Plan= tas de Tratamiento de Aguas Residuales Municipales: Pretratamiento Primario y Tratamiento Primario. Comisión Nacional del Agua.<= span style=3D'mso-bookmark:ref4'> https://sswm.info/sites/default/files/reference_attachments/CONAGUA%202015.= %20Manual%20%20Pretratamiento%20y%20Tratamiento%20primario..pdf<= /span>

= Morales Corozo, J. P., & Loor Vergara , K. (2023). Diseńo de biofiltro para eliminación de contaminantes de aguas residuales de la comunidad Ballagán, Ecuador: Design of a filter for the elimination of pollutants from wastewat= er in the Ballagan community, Ecuador. Revista Científica Ecociencia, <= i>10(2), 92–106. https://doi.org/10.21855/ecociencia.102.801

= GAD Parroquial de San Isidro de Patulú. (2020). Plan de Desarrollo y Ordenamiento Territorial 2020-2023. GAD Parroquial de San Isidro de Pat= ulú https://gpsanisidro.gob.ec/media/gpsanisidro/rendicion_archivos/PDYOT20= 23.pdf

= Hur, J., Lee, B.-M., Lee, T.-H., & Park, D.-H. (2010). Estimation of Biological Oxygen Demand and Chemical Oxygen Demand f= or Combined Sewer Systems Using Synchronous Fluorescence Spectra. <= /span>Sensors, 10(4), 2460–2471. https://www.mdpi.com/1424-8220= /10/4/2460

Terán, C., & Cando, C. (2024). Estadística de Información Ambiental Económi= ca en Gobiernos Autónomos Descentralizados Municipales – Gestión de Agua Potab= le y Saneamiento 2023. INEC. https://www.ecuadorencifras.gob.ec/documentos/w= eb-inec/Encuestas_Ambientales/Municipios/2023/Agua_potable_alcantarillado/D= ocumento_Metodologico_APA_2023_ACT2.pdf

= INEN. (2013). Agua. Calidad del agua. Muestreo. Manejo y conservasión de muest= ras. INEN. https://www.insistec.ec/images/insistec/02-cliente/07-descargas/NTE%2= 0INEN%202169%20-%20AGUA.%20%20CALIDAD%20DEL%20AGUA.%20%20MUESTREO.%20%20MAN= EJO%20Y%20CONSERVACI%C3%93N%20DE%20MUESTRAS.pdf

= Mena, M. E. C., Guadalupe, C. S. A., Vallejo, M. V. P., Córdova, G. B. M., Bernal= , C. M. V., Suárez, J. G. B., & Mena, A. P. C. (2017). Diseńo De Una Planta = De Tratamiento De Aguas Residuales Para Su Reutilización En Riego En Áreas Ver= des. European Scientific Journal, 13(18), 94. https://doi.org/10.19044/esj.2017.v13n18p94

= Naciones Unidas. (2023). Objetivo 6: Garantizar la disponibilidad de agua y su gestión sostenible y el saneamiento para todos:= Agua y saneamiento. Naciones Unidas. https://www.un.org/sustainabledevelopment/es/water-and-sanitation/

= OMS. (2024). Saneamiento. Organización Mundial de la Salud. https://www.who.int/es/news-room/fact-sheets/detail/sanitation

= OPS. (2005). Guía Para El Diseńo De Tanques Sépticos, Tanques Imhoff Y Lagunas De Estabilización. Organización Panamericana de la Salud. https://sswm.info/sites/default/files/reference_= attachments/OPS%202005.%20Gu%C3%ADa%20para%20el%20dise%C3%B1o%20de%20tanque= s%20s%C3%A9pticos.pdf

= Osorio-Rivera, M. A., Carrillo-Barahona, W. E., Negrete-Costales, J. H., Loor-Lalvay, X. A= ., & Riera-Guachichullca, E. J. (2021). La calidad de las aguas residuales domésticas. Polo del Conocimiento: Revista científico - profesional, 6(3), 228–245. https://dialnet.unirioja.es/servlet/articulo?codigo=3D792690= 5

Secretaría del Agua. (2012). Norma de Diseńo para Sistemas de Abastecimiento de Agua Potable, Disposición de Excretas y Residuos Líquidos en el Área Rural. Secretaría del Agua. https://inmobiliariadja.wordpress.com/wp-content/uploads/2016/09/norma-co-1= 0-7-602-area-rural.pdf

= Tilley, E., Ulrich, L., Lüthi, C., Reymond, P., Schertenleib, R. &= Zurbrügg, C. (2014). Compe= ndio de sistemas y tecnologías de saneamiento. Swiss Federal Institute of Aquatic Science and Technology (Eawag). https://sswm.info/sites/default/files/refer= ence_attachments/TILLEY%20et%20al%202018.%20Compendio%20de%20sistemas%20y%2= 0tecnolog%C3%ADas%20de%20saneamiento.pdf

Asamblea Nacional Constituyente del Ecuador. (20= 15). Ministerio del Ambiente. Decreto Legislativo 387 (4 noviembre 2015), Registro Oficial 3. https://www.gob.ec/si= tes/default/files/regulations/2018-09/Documento_Registro-Oficial-No-387-04-= noviembre-2015.pdf

<= /span>

El artículo que se publica es de exclusiva responsabilidad de los autores y no necesariamente reflejan el pensamiento = de la Revista Alfa Publicaciones.

3Dedito=

El artíc= ulo queda en propiedad de la revista y, por tanto, su publicación parcial y/o t= otal en otro medio tiene que ser autorizado por el director de la Revista Alfa Publicaciones.<= /o:p>

&nb= sp;

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Parámetro de diseńo	Valores
Carga hidráulica	10 m³/m²/d
Carga orgánica volumétrica	0.40 kg DBO5 m³/d
Área del filtro	21.44 m²
Diámetro del filtro	5.22 m
Diámetro del filtro asumido	5.25 m
Volumen del lecho filtrante	38.29 m³
Altura del medio filtrante	1.79 m
Altura asumida del medio filtrante	1.8 m
Altura del falso fondo del filtro	0.30 m
Altura del bloque de HS <= /span>	0.10 m
Borde libre	0.50 m
Volumen real del filtro	47.62 m³ (Mayor a 104.= 39 m³)
Carga orgánica volumétrica calculada=	0.32 kg DBO5 m³/d (Cum= ple rango entre 0.15 a 0.5)
Tiempo de retención calculado	5.33 h (Cumple rango entre 5 y 10= h)
Eficiencia de remoción	62.31 %
Concentración del DBO5 en el efluent= e	26.91 mg/l

Parámetro de diseńo	Ecuación
Gravedad específica	1.03 kg/l
Contenido de sólidos	8%
Profundidad de aplicación=	25 c= m
Periodo de aplicación	5 h<= o:p>
Periodo de secado<= /p>	55 d= ías
Periodo de remoción de lodo seco	14 d= ías
Periodo de preparación y mantenimien= to	2 dí= as
Ancho del lecho	4 m<= o:p>
Carga de sólidos	9.65 kg/d
Masa de sólidos	18.34 kg/d
Volumen diario de lodos digeridos	222.56 l/d
Volumen de lodos a extraer	12.24 m³
Área del lecho de secado<= /span>	48.96 m²
Número de divisiones	2
Área unitaria por lecho	24.48 m²

Parámetro de diseńo	Ecuación
Longitud del lecho=	6.12 m
Longitud de lecho asumido=	6.6 m

Determinaciones=	Unidad	Resultados=	Agua residual tratada	Límite máximo permisible	Condición<= /o:p>
DQO<= /span>	mg/l=	212<= /span>	79.90	200<= /span>	CUMPLE
DBO5=	mg/l=	102<= /span>	26.91	100<= /span>	CUMPLE
Nitrógeno Total=	mg/l=	52.12	46.91	50	CUMPLE