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https://doi.org/10.37815/rte.v34n4.928

Artículos originales=

 

Diseño de un biodigestor de excretas animales en la comunidad El Calvario, parroqu= ia Veracruz, cantón Pastaza, Ecuador

D= esign of a Biodigester of animal excreta in the El Calvario Community, Veracruz Parish, Pastaza Canton, Ecuador

 

Miguel Ángel Enr= íquez1 https://orcid.org/0000-0002-8937-9664

 

1Universidad Esta= tal Amazónica, Puyo, Ecuador

menriquez@uea.edu.ec

 

Enviado:         2022/04/29

Aceptado:       2022/12/01

Publicado:      2022/12/30                         

Resumen

La cantidad de excretas que se producen en la comunidad El Calvario están expuestas al medio ambiente y su descomposición produce gases, lo que= de alguna manera contribuye al calentamiento global. Se ha propuesto la construcción de biodigestores para mitigar el impacto de la degradación de = los residuos y evitar la filtración de estos componentes a las aguas subterráne= as. Esto luego es consumido por la comunidad y causa enfermedades gastrointestinales. Para el diseño de biofermentadores, inductivo y analíti= co se han utilizado documentos pre-elaborados para obtener las fórmulas, diseñ= os, dimensiones y materiales idóneos empleados en la implementación de la construcción de biodigestores tubulares. Además de los métodos, se apoya en= la investigación documental descriptiva. El número de cerdos en un municipio permite determinar la carga fecal diaria. Esto significa que la mezcla que = se alimenta diariamente al biofermentador es de 532,15 kg/día con un tiempo de residencia de 29 días rango. Durante este período, las bacterias que descomponen los residuos producen 9,73 m³ de biogás por día, así como la cantidad de líquidos y sólidos que se obtienen de este proceso.

 

= Palabras clave: biodigestor, excretas, fermentación, biofertilizantes, biogás.

 

Abstract

Sumario: Introducc= ión, Materiales y Métodos, Resultados y Discusión y Conclusiones.

 

Como citar: Enríquez,= M. A. (2022). Diseño de un biodigestor de excretas animales en la comunidad = El Calvario, parroquia Veracruz, cantón Pastaza, Ecuador. Revista Tecnológica - Espol, 34(4), 28-43. http://www.rte.espol.edu.ec/index.php/tecnologica/article/view/9= 28

The amount of excreta produced= in the El Calvario community is exposed to the environment. Its decomposition produces gases, which in some way contributes to global warming. The construction of biodigesters has been proposed to mitigate the impact of wa= ste degradation and prevent the filtration of these components into the groundw= ater. Groundwater is consumed by the community and causes gastrointestinal diseas= es. Inductive and analytical pre-elaborated documents have been used in the des= ign of biofermenters to obtain suitable formulas, designs, dimensions, and materials for the construction of tubular biodigesters. In addition, a descriptive documentary research method is employed. The number of pigs in a municipality allows us to determine the daily fecal load. Therefore, the mixture fed daily to the biofermenter is 532.15 kg/day with a residence tim= e of 29 days range. During this period, the bacteria that decompose the waste produce 9.73 m³ of biogas per day, besides the amount of liquids and solids that result from this process.

 

Keywords: <= span class=3DSpellE>biodi= gester, excreta, fermentation, biofertilizers, biogas.=

 

Introducción

La descomposición de la materia orgánica en animales y plantas produce gases e= n el ambiente (Cabrera, 2011). Según Rodríguez y Urbina (2012), los biorreactores pueden reducir el impacto negativo del estiércol animal, que genera contaminación significativa en el medio y contribuye al calentamiento globa= l a través de la liberación de gases como el metano (CH4) y el dióxi= do de carbono (CO2) procedente de la fermentación de celulosa y almidón. Kaiser et al. (2002) propusieron que la digestión anaerobia es una= de las soluciones de tratamiento de residuos orgánicos que posibilita el uso d= e la biomasa como fuente de energía renovable. Los compuestos de alta energía resultantes se pueden utilizar para generar calor o electricidad. Terashima et al. (2009) sugieren que la digestión anaeróbica es una técnica popular para estabilizar y reducir el exceso de l= odos biológicos después del tratamiento de aguas residuales. El aprovechamiento = de residuos orgánicos en la región amazónica permite obtener productos que mej= oran la calidad de vida de las comunidades Enríquez, Escobar y Guamán (2022). Se= gún Bond y Templeton (2011) argumentan que las trituradoras domésticas se consideran una tecnología limpia y respetuosa co= n el medio ambiente que ayuda a las comunidades rurales a satisfacer sus necesid= ades energéticas para iluminación, cocina y electricidad, mejorando así las condiciones de vida. Barrett (2015) señala que el diseño y construcción de biorreactores en comunidades, organizaciones, instituciones y áreas rurales brindan un mecanismo para reducir los impactos ambientales de los combustib= les fósiles derivados del petróleo crudo. Heiz Cabr= era (2014) sostiene que “Los biorreactores son una alternativa ambiental muy valiosa porque reducen la deforestación al no utilizar leña para la cocción= de alimentos”, Moeller (2013) argumenta que los biorreactores se pueden utilizar cómodamente en el hogar porque ofrecen muc= has posibilidades y son una energía alternativa amigable con el medio ambiente.=

 

Red= uce la carga contaminante del proceso de vertido con una reducción de materia orgá= nica del 60 al 80%, dependiendo del tiempo de retención, y ofrece una serie de beneficios. Toda la energía ahora proviene de fuentes fósiles, lo que incrementa las emisiones de gases de efecto invernadero y contribuye al calentamiento global y al cambio climático. Estas emisiones pueden mitigarse mediante el uso de combustibles fósiles y fuentes de energía renovables (Ri= vas et al., 2012). La energía de biomasa tiene un potencial de 2.635 a 3.771 (<= span class=3DSpellE>pJ) año-1, donde el potencial del biogás es (35-305 PJ año-1) en residuos domésticos y (148-190 PJ año-1) en residuos ganaderos, p= ero el potencial de esta es energía subutilizada (Alemán et al., 2014). Una alternativa de energía limpia en la cría de animales es el biogás producido= a partir de desechos orgánicos utilizando biorreactores, que ofrecen energía = más barata, ingresos adicionales para los agricultores y oportunidades laborale= s, haciendo, energía descentralizada y protección del medio ambiente, reducien= do las emisiones de gases de efecto invernadero (Rivas et al., 2011). El uso de fuentes de energía más limpias debe ser la clave para reducir la contaminac= ión en Ecuador (Enríquez, 2020).

 

El objetivo del estudio es diseñar un biodigestor de excretas animales en la comunidad El Calvario, parroquia Veracruz, Provincia de Pastaza. Para lo cu= al se genera la siguiente interrogante ¿El diseño del biodigestor ayudará a la comunidad en la reducción de la contaminación ambiental?

 

Materiales y Mét= odos

El estudio se realizó= en la comunidad el Calvario parroquia Veracruz, cantón Pastaza, esta se encuen= tra localizada en las coordenadas: 18M (172674.68 m E; 9833075.43 m S), y tiene una superficie de 181.3 km2 (GADMP, 2020).

 

Tipos= de Investigación=

Documental

Se basa en una revisión bibliográfica para encontrar respuestas concretas de estudios generados con anterioridad Baena (2014), utilizándole como una fuente primaria de información con la ayuda de otros textos.

 

Descriptiva<= /span>

Tamayo (2006) trata de comprender situaciones comunes a través de la descripción detallada de actividades, objetos, proce= sos y personas. La investigación consiste en describir las características bási= cas de conjuntos homogéneos de fenómenos utilizando criterios sistemáticos para definir el comportamiento de los fenómenos en estudio (Sabino, 2014). Por e= ste motivo, el estudio permitió obtener datos sobre el número de cerdos necesar= ios para el diseño del biorreactor, así como para determinar el tamaño y peso necesarios.

 

Mét= odos de Investigación

Identific= ación del sector

En la comunidad El Calvario residen familias= que se dedican a la crianza de cerdos, y al no contar con el manejo de desechos= se plantea el uso de biodigestores en la zona.

 

Levantami= ento de información

En la zona de estudio se identificó 11 famil= ias que crían cerdos, a los que se aplicó una ficha de tenencia de esta especie porcina y en la que se detalla parámetros como la edad, número de especies = y la proyección trimestral.

 

Análisis = de la información

Los parámetros para el diseño del biodigesto= r se enfocan al número de cerdos identificados mediante la ficha de tenencia, y = que mediante el autor Braun (2013), proyecta la cantidad aproximada de generación de excretas de cada t= ipo.

 

Selección= y diseño del biodigestor

El biodigestor que se utiliza es de tipo tub= ular debido a que presenta características de manejo para los pobladores de la comunidad. Los materiales empleados en la fabricación del equipo son de fác= il acceso y económicos, así como sus mantenimientos.<= /p>

 

Se identificó 177.05 kg de excretas, a parti= r de este peso se calcula el volumen de producción para los cálculos del biodigestor.

 

Ind= uctivo

Trata de observar, investigar y conocer las mismas o similares características, a partir de las cuales redactar la solicitud o ley en tal sentido. Como lo expresó Abreu (2014), es “un razonamiento de abajo hacia arriba que fluye de lo particular o individual a lo general, y la suposición inductiva es la reflexión centrada en el objetivo”.

 

Ana= lítico

Ruiz (2006) descubrió que el método analítico es un método investigat= ivo que descompone un todo, descomponiéndolo en partes o elementos para observa= r causas, naturaleza y efectos.

 

Pob= lación de estudio

Tal como lo enfatizan Arias et al. (2016) es un conjunto definido, limitado y disponible de casos que formarán parte de una muestra selecciona= da que deberá cumplir con los criterios existentes. Cuando se habla de poblaci= ón, es importante recordar que se refiere no solo a una persona sino también a cualquier cosa que se pueda contar, por ejemplo, animales, muestras biológi= cas, registros. El método de inclusión según Arias et al. (2016) son todas las c= aracterísticas particulares que debe tener un sujeto u objeto de estudio para que sea part= e de la investigación. En este caso lo conformaran las 11 familias de la comunid= ad El Calvario mismas, que se dedican a la crianza de animales porcinos.

 

Resultados y Discusión

En la comunidad El Calvario existen 11 productores de cerdos, los cuales habitan en la zona central de la comunidad con una distancia promedio de 500 metros entre viviendas lo que permi= te el acopio de las excretas, con base en este antecedente la Tabla = 1 tiene resultados de la tenencia de ganado porcino en el sector en el= año 2021. Y esta levantada por trimestres con una media poblacional de 117 espe= cies que generan un promedio de excretas de 177.05 kg/día.

 

Tabla 1=

Ten= encia promedio de ganado porcino en el sector El Calvario

Media Tri= mestral

Meses

Lechones<= o:p>

Madres

Reproduct= ores

Engorde

Total

enero- marzo

65

6

4

40

114<= /o:p>

abril- junio

66

8

4

39

117<= /o:p>

julio- septiembre

67

9

5

37

118<= /o:p>

octubre- diciembre

69

10

5

36

120<= /o:p>

Media

67

8

5

38

117<= /o:p>

Nota. La tabla presenta valores promedios (medi= a) de todo el año, en cuatrimestres.

 

Con los datos obtenidos de tenencia de ganado se procederá a investig= ar la cantidad de estiércol que genera cada tipo de cerdo, lo cual se determin= a en la Tabla 2.

 

 

 

 

 

Tabla 2=

Pro= ducción de excretas según el tipo de cerdo

Etapa

Estiércol kg/día

Estiércol – orina kg/día

Volumen en l/día

Volumen m3/animal/mes<= /span>

25-100 kg

2.3

4.9

7.0

0.25

Hembra

3.6

18.0

16.0

0.48

H. lactación

6.4

6.0

27.0

0.81

Semental

3.0

6.95

9.0

0.28

Lechón

0.35

0.95

1.4

0.05

Promedio

2.35

5.8

8.6

0.27

Nota. Tomado de Bra= un (2013).

 

Con los datos obtenidos de tenencia de ganado porcino se procede a identificar la cantidad de estiércol que se genera por cada cerdo en las diferentes etapas de su desarrollo según se detalla en la  REF _Ref121230459 \h Tabla = 3.

 

Tabla 3=

Pro= ducción de excretas según el tipo de cerdo

Etapa

Estiércol kg/= díaa

Media de tipo= s de cerdos

Producción de kg/día

25-100 kg

2.3

38

87.4

H. lactación

6.4

8

51.2

Semental

3.0

5

15

Lechón

0.35

67

23.45

TOTAL

 

 

177.05 kg/día

Nota: Adaptación de aBraun (2013) para la estimación de excretas porcinas.

 

Con respecto a estos precursores, se ha propuesto desarrollar un biorreactor tubular tipo “salchicha”, cuyas propiedades simples y económicas permiten su uso generalizado en zonas rurales. Es un material flexible, de fácil manejo= y que se puede adquirir en cualquier tienda de materiales de construcción (Bá= ez y Benítez, 2015). El equipo suele colocarse directamente sobre el suelo, en lugares donde la temperatura es más baja por lo que la gente hace agujeros = para aislar y reducir el tiempo de espera que puede ser muy largo. En condiciones normales, la producción de biogás debería comenzar 3 semanas después de la = primera alimentación (Torre y Ruiz, 2008).

 

 

Can= tidad de la mezcla

Es fundamental conocer el volumen acuoso presente en la mezcla que permitirá que la degradación se realice sin inconvenientes, tomando en cuen= ta la relación agua + solidos según se detalla en la Tabla = 4.

 

Tabla 4=

Relación estiércol agua según tipo animal

Porciones de Agua

Bovino

Fresco

1:1

Seco

1:2

Porcino

1:2

Aves

1:1

Equino

1:2

Desechos humanos

1:1

Desechos vegetales

1:0,5-2

= Nota. = García (2016).<= /p>

 

A base de la Tabla 4, se procede a utilizar una relación 1:2. Entonces se ocupará los datos de la tabla 6 que expresa la cantidad de estiércol, misma= que será sustituida en la Ec (1), los datos que se obtuvieron para los 177.05 kg/día de estiércol se aumentan 354.1 kg/día de = agua dando un resultado de 532.15 kg/día de la mezcla que se deben cargar en el biodigestor.

 

Cm: Cantidad de= la mezcla

 

. (1)

 

 

Tie= mpo de retención

Seg= ún Toala (2013) afirma que el tiempo de retención está relacionado con el periodo que tardan los microorganismos en degradar la materia orgánica y obtener un producto. Cáceres (2011) sugirió que las bacterias deben tener un periodo razonable de descomposición de la materia orgánica, si no se cumplen las variables de temperatura y humedad, la tasa = de crecimiento y descomposición de las bacterias será subóptima, como se muest= ra en la Tabla = 5 08D0C9EA79F9BACE118C8200AA004BA90B02000000080000000E0000005F005200= 650066003100320031003200340036003200370038000000 . <= o:p>

 

 

 

Tabla 5=

Tab= la de tiempo de retención

Región característica

Temperatura

Tiempo de retención hidráulico

Trópico<= /span>

30 °C

30 días

Valle

20 °C

40 días

Altiplano

10 °C

60 días

Nota<= /i>. Parámetros ambientales establecidos por Herrero (2008).

 

A base de la información de la  REF _Ref121246278 \h = Tabla = 5 se hizo una interpolación para poder determina= r el tiempo de retención (tr), tomando en cuenta que= la comunidad el calvario tiene una temperatura promedio anual de 30 °c, por lo cual se reemplazará el número de días correspondiente a dicha temperatura en la ecuación 2.

 

Ec. (2)

=

 

Vol= umen líquido

Según Herrero (2008), “El volumen de líquido que provoca la biodegradación será el resultado de multiplicar la carga diaria = de la mezcla por el tiempo de retención”. Los biorreactores tubulares estarán sujetos a una carga diaria de sustancias introducidas para su biodegradación por el tiempo considerado en función de la temperatura y ubicación del dispositivo.

 

Dónde:

 

VL: Volumen de la fracción líquido.<= /span>

TR: Tiempo de retención en días.

Cd: Carga diaria en Kg/día

(Barzallo, 2018)=

 

<= span style=3D'font-size:12.0pt;font-family:"Times New Roman",serif;mso-fareast= -font-family: "Arial MT";mso-ansi-language:ES-EC;mso-fareast-language:ES-TRAD;mso-bidi-= language: AR-SA'>

. (3)

 <= /p>

Vol= umen del gas

El interior del biodigestor se encuentra compue= sto por un 75% de sólidos y líquidos (mezcla de excretas con agua), al estar sometido a un proceso anaeróbico (en ausencia de oxígeno), los gases que sa= len de esta descomposición representan el 25% restante del interior del Biodigestor, dando como resultado que el volumen de Gas es igual a un tercio del volumen del líquido (Herrero, 2008).<= span style=3D'mso-bookmark:_Toc38966068'>

Donde:

 

Vg: Volumen que ocupa la fase gaseosa<= /span>

0.25: Porcentaje que ocupa la parte gaseosa

0.75: Porcentaje que ocupa la parte líquida

VL: Volumen líquido

(Herrero, 2015)

 

Ec. (4)

 

Vol= umen total de biodigestor

Para este cálculo se puede realizar la aplicaci= ón de la ecuación:

 

VT: Vo= lumen total

VL: vo= lumen del liquido

Vg: volumen del gas

(B= arzallo, 2018)<= /span>

 

Ec. (5)

=

=

 <= /p>

Pro= ducción de Biogás por día

Para conocer la cantidad total de energía se de= be tomar en cuenta los valores la Tabla = 6.

 

Tabla 6=

Pro= ducción de Biogás

Tipo de estiércol=

Producción de Gas/kg de Estiércol

Ganado Vacuno=

22 – 40

Cerdos=

40 – 60

Aves de corra= l

65,5 – 115

Humano=

20 – 28

Nota. Tomada de Moreta (2013).

 

Para este estudio se tomará en cuenta la produc= ción de biogás en ganado porcino, generando un intervalo de 40 a 60 kg, tomando = en cuenta un valor promedio de 50 kg para el cálculo, donde:=

 

Pb: producción de biogás

Pb: Producción de biogás

1kg/día=3D50L

 

Ec. (6)

 

Mar= gen de seguridad

El margen de seguridad presenta fluctuaciones repentinas en la producción de biogás. Se debe tener en cuenta un rango del 5-10% como muestra la ecuación 7. Y este producto resultante está compuesto= por diferentes niveles de nutrientes, los cuales están identificados en la Tabla = 7 con sus respectivos porcentajes.

 

Pbseg: Producción de biogás con margen de seguridad =

Pb: Producción de biogás

Margen de seguridad: 10% (0.1)

 

Ec. (7)

 

Tabla 7=

Ran= go de niveles de nutrientes en diversos residuos de origen animal y vegetal<= /span>

Materia Prima<= /o:p>

C (%)

N (%)

P2O5(%)

K2O (%)<= o:p>

CaO (%)

MgO (%)<= /sup>

Excretas

Bovino

17,4 – 40,6

0,3 – 2,0

0,1 – 1,5

0,10

0,35

0,13

Porcino

17,4 - 46,0

1,1 – 2,5

0,4 – 4,6

0,30

0,09

0,10

Caprino

35,0 – 50,0

1,0 – 2,0

0,2 – 1,5

2,30

 

 

Equino

35,0 - 52,0

0,3 – 0,8

0,4 – 1,6

0,35

0,15

0,12

Ovino

35,0 – 46,0

0,3 – 0,6

0,3 – 1,0

0,15

0,33

 

Conejos

23,0 - 35,0

1,0 – 1,9

0,9 – 1,8

2,10

0,45

0,15

Aves

28,0 – 35,0

1,4 – 2,0

2,0 – 2,8

1,40

0,80

0,48

Patos<= /span>

29,0 - 41,0

0,6 – 0,8

1,0 – 1,5

0,40

0,80

 

Pavos

17,4 – 41,0

0,6 – 0,8

0,5 - 0,8

1,10

0,80

 

Humanas

2,5

0,8 – 1,0

0,5

0,30

 

 

Nota. Tomada del Manual de Biogás (2011).

En la Tabla 7 se presenta los diferentes niveles de nutrientes con sus respectivos porcentajes, hay que t= omar en cuenta que el cálculo de la capacidad instalada del dispositivo se basa = en un análisis de la cantidad diaria de estiércol generada a partir de las excretas porcinas que se producen en la zona.  Brown (2013) identifica que existe una cantidad variable de estiérco= l, producidos según el tipo de cerdo (nacimiento, engorde, hembra, lactante o verraco). Se generan 177,05 kg/día de estiércol. En rel= ación a esos datos se identifica la cantidad de agua requerida en el estié= rcol producido, García (2016) sugiere una relación 1:2 para cerdos, es decir, la cantidad de agua equivalente a cada 1 kg de estiércol, 2 kg. se utilizará a= gua, por lo que se cargarán 532,15 kg/día de la mezcla en el biorreactor. La car= ga debe mantenerse durante un periodo determinado, este tiempo de retención dependerá de la ubicación y la temperatura donde se encuentre el biorreacto= r.

 

La comunidad El Calvario está ubicada en una zona tropical de la región amazónica de Ecuado= r, para lo cual Herrero (2008) sugirió un período de retención de 30 días para= que las bacterias degraden la materia orgánica. Este valor se sustituye en la ecuación (2), que genera como resultado un tiempo de retención del estiércol comunitario de 29 días. Tras obtener el valor del tiempo de retención se determinará el volumen del líquido biodegradable. Barzallo (2018) en su est= udio utiliza una ecuación que al cambiar el valor nos da el volumen del líquido = como 15.40 m3, similar a Herrero (2015). En la ecuación 4 se obtiene 5,13 m= 3 de gas. Barzallo (2018) expresa en la ecuación 5 que ayudará a determinar el volumen total del biorreactor, el resultado es 21 m³, para determinar la producción de biogás por día se tendrá en cuenta la Tabla de Moreta (2013),= en cerdo El rango de la producción de biogás es de 40 a 60 kg, con la sustituc= ión en la ecuación (6) dando un valor promedio de 50 kg, correspondiente a un rendimiento de 8,85 m³. Este valor debe corresponder al margen de seguridad, donde Liliana (2018) da con la ecuación (7) que será una capacidad diaria d= el biorreactor de 9,73 m³/día, tomando la química componente de este elemento = del manual de biogás. (2011) encontraron: carbono (3,08 m³/día), N (0,17 m³/día= ), P2O5 (0,24 m³/día), K2O (0,029 m³/día), CaO (0,= 0087 m³/día), MgO (0,0097 m³/día).

 

Pro= ducción de Bioabono por día. <= /p>

Según Herrero (2008) en el proceso de la fermentación se perdió una fracción de sólidos totales.= El estiércol fresco tiene entorno a un 17% de sólidos totales. El rango puede variar de 13 a 20%. Los sólidos totales representan el peso del estiércol u= na vez seco y, por tanto, es la carga real de materia sólida que se estará introduciendo en el biodigestor.

 

=

 

Pro= ducción de biol

Según Herrero (2019= el diseño del biodigestor tubular va relacionado a la gravedad, por= lo cual si es cargado con estiércol más agua por la entrada se tendrá la misma cantidad de biol por la salida.

 

Dis= eño del biodigestor

De acuerdo a los datos obtenidos se determinó que el volumen es de 21m³, por lo cual se va a utili= zar un rollo de 2.5 m de ancho que se encuentra disponible en el mercado como lo muestra la Tabla = 8.

Tabla 8=

Lon= gitudes mínima, máxima y óptima de biodigestores tubulares según circunferencias

Circunferencia =

(m) a

2<= /span>

1

0.32

0.64

3.2

1.02

6.4

2.05

4.8

1.54

3<= /span>

1.5

0.48

0.95

4.8

3.47

9.5

6.87

7.2

5.21

4<= /span>

2

0.64

1.27

6.4

8.23

12.7

16.34

9.5

12.22

*= 5

2.5

0.80

1.59

8.0

16.08<= /span>

15.9

31.96<= /span>

11.9

23.92

6<= /span>

3

0.95

1.91

9.5

26.9

19.1

54.15

14.3

40.54

7<= /span>

3.5

1.11

2.23

11.1

42.96

22.3

86.31

16.7

64.64

8<= /span>

4

1.27

2.55

12.7

64.35

25.5

129.21

19.1

96.78

9<= /span>

4.5

1.43

2.86

14.3

91.86

28.6

183.73

21.5

138.12

10=

5

1.59

3.18

15.9

126.28

31.8

252.56

23.9

189.82

14=

7

2.23

4.46

22.3

348.38

44.6

696.77

33.4

521.80

Nota. Tomado de Herrero (2019).=

*Valores tomados de la tabla para el diseño de = un biodigestor.

 

Figura 1

Vista Lateral del Biodigestor Tubular

 

 

 

 

 

Figura 2

Vis= ta Frontal del Biodigestor Tubular

 

 

Figura 3

Vis= ta Posterior del Biodigestor Tubular

 

Mat= eriales

En la Tabla = 9 se determina los componentes que se van a utilizar para la construcción del biodigestor en la comunidad El Calvario.

 

Tabla 9=

Mat= eriales empleados para la implementación de un biodigestor tipo salchicha

Componente

Comentario

Cantidad

Zanja

Sacos

Para darle una forma adecuada a la zanja en lugares donde el suelo = no lo permita.

Los necesarios

Plásticos viejos, lonas o sacos.

Se puede formar una “sabana” para que sirva como protección para el= biodigestor.

Los necesarios

Biodigestor

Manga tubular

 

Si utilizara una geomembrana de polietil= eno de 500 micrones.

Se soldará de forma tubular. La longitud= de la manga=3D (longitud de la zanja +1m+profundidad de la zanja)=

Longitud de la manga=3D 22,3m=

Tubería de PVC de entrada

 

Se va trabaja= r con una tubería de 6” ya que el contenido va hacer estiércol.

1.5 metros de largo con 80 cm en el inte= rior del biodigestor.

 

Tubería de desagüe de PVC

Se va trabajar con una tubería de 6” ya que el contenid= o va hacer estiércol, esto permitirá un mejor amarre con el plástico tubular.<= o:p>

Tubería de= 3 metros de largo con 80 cm en el interior del biodigestor para la descarga= de biol; y una tubería de 2 metros para descargar el <= span class=3DSpellE>bioabono o desechos sólidos.

Liga de cámara de neumático (también llamada boya o tubo).

Esta se puede obtener de tubos usados, se debe cortar tiras continu= as de 5cm de ancho.

Dos cámaras de aro 14 o 16, o también de 30 a 40 m de liga del neumático ya cortada

Adaptador de tanque en PVC o polipropileno (también llamado flange, pasamuros o brida).

Normalmente se trabaja en 1/2" o 3/4", en este caso ocuparemos la de 3/4".

1<= /span>

Tubería de agua

Normalmente se trabaja en 1/2" o 3/4", se utilizará una de 3/4". Puede ser de PVC, de polietileno o manguera. Se usará para conectar la salida de biogás a la válvula de alivio.

3 metros=

Accesorios PVC

Se puede usar de rosca o pega en PVC, o con uniones Flex para mangu= era.

Los que haga falta para unir el adaptador de tanque con la Tee de la válvula de alivio

Cuerda

Una cuerda plástica mínimo de 1/4".

2.5 veces en metros la longitud del biodigestor

Teflón

Se recomienda usar teflón en la rosca del adaptador de tanque.=

1<= /span>

Válvula de alivio

Elemento que encuentre la conducción de biogás al salir del biodigestor.

Se requiere al menos de una Tee, una pi= eza de tubería de 30 cm, una botella de 2 litros de refresco vacía, y una llave = de paso plástica.

Conducción del biogás<= o:p>

Tubería de agua

Normalmente se trabaja en 1/2" o 3/4", en este caso se va= a ocupar 3/4". Puede ser tubería rígida de PVC.

Tantos metros como haga falta para llevar el biogás desde el biodigestor al punto de consumo

Llaves de bola

Normalmente se trabaja en 1/2" o 3/4", en este caso se va= a ocupar 3/4".

Mínimo 2=

Tee

Normalmente se trabaja en 1/2" o 3/4", en este caso se va= a ocupar 3/4".

Mínimo 1=

Codo

Normalmente se trabaja en 1/2" o 3/4", en este caso se va= a ocupar 3/4".

Mínimo 1=

Codo Unión universal

Normalmente se trabaja en 1/2" o 3/4", en este caso se va= a ocupar 3/4".

Mínimo 1=

Unión univers= al

Normalmente se trabaja en 1/2" o 3/4", en este caso se va= a ocupar 3/4".

Mínimo 1=

Teflón

Se recomienda usar teflón (10 vueltas) en toda conexión de roscada.=

1 o 2, dependiendo de los accesorios de rosca que se usen.

Cocina

Se puede adaptar cualquier cocina de gas considerando disminuir la mezcla con aire y ensanchando el conducto del chiclé o quitándolo.

Se recomienda dos hornillas o quemadores.<= /p>

 

Conclusiones

El valor de excretas parte de un levantamiento de información generado en la comunidad El Calvario donde se identifica un promedio de 117 especies que generan 532.15 kg/día, ocupando un volumen de 21m³, el cual genera 9.73m³/d= ía de biogás (405.42 l/h) con una composición de Carbono<= span lang=3DES style=3D'mso-fareast-font-family:"Arial MT";mso-ansi-language:ES; mso-fareast-language:EN-US'> (3.08m³/día), N(0.17m³/día), P2O5(0.24m³/día), K2O(0.029m³/día), CaO (0.0087m³/día) y MgO (0.0097m³/día)<= span style=3D'mso-fareast-font-family:"Arial MT";mso-bidi-font-family:"Arial MT"; color:black;mso-fareast-language:EN-US'>; además de 146.95 kg/día = de bioabono útil para la agricultura del sector. El biog= ás presenta gran versatilidad de usos, como es la cocción de alimentos (consume por hora 300 l/h.), la generación de electricidad mediante generadores especiales que utilizan = el gas, además para uso en la calefacción de vivienda o edificios.<= /span>

 

El = diseño del biodigestor es una alternativa eficaz para reducir las emisiones de met= ano al ambiente creando una cultura de gestión de residuos, como es la producci= ón de biol y del bioabono. Ambas son alternativas orgánicas que permite aumentar el rendimiento produc= tivo y mejorar la calidad de los productos mediante la reducción de plagas y enfermedades presente en los cultivos de la zona.

 

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6

Miguel Ángel Enríquez

5

Diseño de un biodigestor = de excretas animales en la comunidad El Calvario, parroquia Veracruz, cant= ón Pastaza, Ecuador

 

Escuela Superior Politécn= ica del Litoral, ESPOL

 

Revista Tecnológica Espol= – RTE Vol. 34, N° 4 (Diciembre, 2022) / e-ISSN 1390-3659

 

Escuela Superior Politécn= ica del Litoral, ESPOL

 

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