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Uso del Kikuyo (Pennisetum Clandestinum L), residu= o de la poda de áreas verdes para la obtención de ácido piroleńoso con fines agr= opecuarios

 

Use of Kikuyo (Pennisetum Clandestinum L), residue from the pruning of green areas for obtaining pyroligneous acid for agricultural purposes

Diego Burbano Salas[1]<= i>Recibido: 15-07-2019 / Revisado: 25-07-2019 /Aceptado: 20-08-2019/ Publicado: 10-09-2= 019

 

Abstract                     DOI: https://doi.org/10.33262/cienciadigital.v= 3i3.4..884

The large volumes of biomass generated in the maintenance of green areas are considered a focal point for the production = of organic waste. In the present work, it is proposed to obtain piroleńoso acid from the precursor Pennisetum Clandestinum L (kikuyo), a very common waste product of pruning and gardening; Describes the thermochemical process for = the validation of the technology for the production of the product and utilizab= le by-products (coal and tar) and the evaluation of the macro elements and the structural components of the substance by means of the Fourier Transform Infrared Spectrometry (FTIR) method. (Fourier transform infrared spectrosco= py), by a direct comparison, it is shown that its properties are similar to the product from Bamboo (Phyllostachys pubescense f) which has characteristics = that can increase root growth in vegetables, in farm animals improves the digestibility of Nutrients and reduces harmful intestinal coliforms. The results obtained describe a yield of between 20 and 30% for the gases with a maximum delivered energy that oscillates between 150 and 1000 kcal.<= span lang=3DEN-US style=3D'font-size:12.0pt;line-height:115%;font-family:"Times = New Roman",serif; mso-ansi-language:EN-US'>

Keywords: Pyroligneous acid, biocarbon, pyrolysis, organic waste.

 

= Resumen

Los grandes volúmenes de biomasa generados en el mantenimiento de áreas verdes se los considera un punto focal de producción de desechos orgánicos. En el presente trabajo, se propone la obtención del ácido piroleńoso a partir del precurso= r Pennisetum Clandestinum L (kikuyo), residuo muy común producto de las podas y de adecentamiento de jardines; se describe todo el proceso termoquímico de validación de la tecnología para o= btención del producto y subproductos aprovechables (carbón, alquitrán)  y la evaluación de los macro elementos y= los componentes estructurales de la sustancia mediante el método de Espectrometría Infrarroja con Transformada de Fourier (FTIR del in= glés Fourier transform infrared spectroscopy<= span lang=3DES-EC style=3D'font-size:12.0pt;line-height:115%;font-family:"Times = New Roman",serif; color:black;mso-ansi-language:ES-EC;mso-bidi-font-weight:bold'>), por una comparativa directa, se demuestra que sus propiedades son similares al prod= ucto proveniente del Bambú (Phyllostachys pubescens f) el cual posee características que pueden incrementar el crecimiento radicular en vegetales, en animales de granja mejora la digestibilidad de los nutrientes y reduce los coliformes intestinales perjudiciales. Los resultados obtenidos describen un rendimiento de entre 2= 0 y 30 % para los gases con una energía máxima entregada que oscila entre 150 y 1000 kcal.  

Palabras clave: Ácido piroleńoso, biocarbón, pirolisis, Residuos orgánicos.

Introducción

La crisis mundial con respecto a la contaminación y a la degradación del suelo crece a tasas alarmantes, sobre todo porque las soluciones a estos problemas tienen que ver con actividades antropogénicas que utilizan indiscriminadame= nte los recursos y generan una cantidad de residuos de todo tipo. Los procesos térmicos a partir de la biomasa son motivo de investigación e implementació= n de sistemas en varios lugares del mundo científico, pero sobre todo es una necesidad del creciente desarrollo. (Jun, 2006). = Ecuador cuenta con una gran cantidad de residuos de biomasa provenientes principalm= ente de procesos de industrias de alimentos, que están siendo aprovechadas principalmente en la generación alternativa de energía, sin embargo, las tecnologías que se aplican no son lo suficientemente eficientes para compet= ir con las fuentes tradicionales, deteniendo el crecimiento de este tipo de incitativas, por consiguiente, aumentando la cantidad de residuos. = (Aguilera, 2006).= La sustancia obtenida es un subprod= ucto del pirólisis conocido como vinagre de madera, es generalmente marrón oscuro, viscoso y compuesto por una mezcla muy compleja de hidrocarburos oxigenados= . Es útil para el mejoramiento del suelo, la actividad de las semillas, la germi= nación y especialmente en la actividad biológica de los ataques de hongos y termit= as. (Choi, 2009).=

 

La composición y rendimiento de vinagre de madera dependen de las condiciones del proceso y de las composiciones de la biomasa usada. Se han realizado extensos estudios sobre las composiciones químicas y las aplicaciones basadas en materiales de partida con roble, sakura, té ver= de, bambú, eucalipto, planta de manglar y residuos de agricultura. (CharMarker, 2009). Sin embargo, = no ha habido ninguna investigación sistemática en el análisis químico avanzado del vinagre de Pennisetum Clandestinum L (kikuyo). El objetivo de la presente investigación es la caracterización de ácido piroleńoso obtenido a partir de este producto de la poda, con fines de su posible utilización agropecuaria, para lo cual se describe el proceso de producción y se realiza la caracterización de los principios activos del producto obtenido.    

 

 

Materiales y Métod= os

 <= /h2>

Ubicación

El área seleccionada para la obtención de residuos de kikuyo fue la Escuela Su= perior Politecnica de Chimborazo (ESPOCH), en la parte externa de la institución s= e ha adecuado un lugar como botadero de material vegetativo producto de la poda y mantenimiento de las áreas verdes.

 

Recolección de la = materia prima

El proceso de recolección y separación de agentes inorgánicos como fundas y envolturas no reviste mayor dificultad y estos residuos se depositaron en la basura inorgánica común. El área de descarga a cielo abierto mencionada se encuentra aledańa al almacenamiento de agua potable que abastece al sector = y a la institución, detectándose procesos de descomposición, presencia de vecto= res y contaminación visual.

 

Toma y procesamiento de la muestr= a

 

Se tomó una muestra de 42 kg de P. clandestinum L, del lugar seleccionado el cual se sometió al proceso de= pirólisis a una temperatura entre los 200°C – 800°C. (Burnett= e, An Introduction to Wood Vinager, 2013). Para la caracterización de la materia prima se tomaron daos bibliográficos. En la T= abla 1 se encuentra representada las fracciones de proteína cruda de kikuyo, tan= to en su parte de fracción soluble, fracción potencialmente degradable y fracc= ión no degradable, dando a conocer las características proteicas que posee la biomasa utilizada, un 62% es degradable un 31.2% fracción soluble y un 12.7% constituye una parte no degradable. (Hagner, 2013).

 <= /span>

Tabla 1:Fracciones de la proteína = cruda de muestras de Pennisetum Clandestinum= L

 

Fracciones de la PC

 

a

b

C

Promedio

31.2

62.5

12.7

Máximo

42.9

72.2

19.5

Mínimo

18.9

44.9

7.07

D. E.

5.21

8.50

4.66

C. V., %

16.7

13.6

36.7

             = a = =3D fracción soluble; b =3D fracción potencialmente degradable; c =3D fracción = no

             degradable; D.= E.=3D Desviación Estándar; C.V =3D coeficiente de variación.

 

En el método in situ, la fracción&nb= sp;a corresponde a la fracción proteica que rápidamente desaparece (NRC 2001). En promedio, = el 31.2% de la PC del pasto kikuyo está representado por la fracción a=  con una variación que oscila entre el 18.9 y el 42.9 % (Hagner, 2013)

 

Metodología de producción<= /o:p>

 

Para la extracción, se utilizó un reactor de lecho fijo a escala pilo= to, herméticamente cerrado para asegurar condiciones de reacción anaeróbicas, el equipo así dispuesto (figura 3) fue utilizado en el proceso de pirólisis ob= teniendo varios productos de oxidación, las emisiones de la pirólisis son recogidas = por un sistema de destilación con agua de refrigeración a 10°C; al finalizar el= proceso de destilación el líquido es el ácido piroleńoso. (Ikeshima, 1999)

 

Caracterización del producto ob= tenido

 

De la revisión bibliográfica= se presume que dentro del ácido existen más de 200 tipos de componentes químic= os involucrados y estos incluyen principalmente ácidos orgánicos, fenólicos, alcanos, compuestos de alcohol y éster. (Ikeshima, 1999)= .  En la evaluación de los macroelementos y componentes estructurales se ha utilizad= o la metodología de espectrometría infrarroja por transformadas de Fourier (FTIR= ). Cuando la radiación IR se hace pasar a través de una muestra, parte de la radiació= n es absorbida y parte pasa a través de la muestra. La seńal resultante en el de= tector es un espectro que representa una 'huella digital' molecular de la muestra.= La utilidad de la espectroscopia de infrarrojo surge debido a que diferentes estructuras químicas (moléculas) producen diferentes huellas espectrales. El FTIR utiliza interferómetria para grabar información sobre un material colo= cado en el haz IR. La transformada de Fourier otorga resultados en los espectros= que los analistas pueden utilizar para identificar o cuantificar el material. <= /span>(Bradley, 2002= )

 

Resultados y Discusión

 

Proceso de obtención propuesto<= /b>

&= nbsp;

El áci= do piroleńoso es un líquido que se obtiene de la destilación seca de material vegetativo previamente deshidratado, está integrado por un 70 a 90 % de hum= edad y muchos compuestos orgánicos, entre ellos el ácido acético y el alcohol metilico, en el proceso se obtiene una serie de subproductos aprovechables = como son el biocarbón y el alquitrán.

&= nbsp;

La figura 1 muestra, el proceso que se realiza par= a la obtención del ácido piroleńoso, la energía solar interviene en el proceso de secado, como producto de esto se ocasiona emisiones de calor residual, resi= duos forestales, como la leńa que es el pilar para el incremento de la  temperatura en la pirólisis, se emiten = gases de combustión además de ácidos, fenoles, alcanos que ingresan al proceso de destilación, durante este proceso se genera, alquitrán vegetal, destilado y como residuo final de la pirólisis de la biomasa, se obtiene biocarbón y ce= niza producto de la quema de los residuos forestales.

 

 

Figura 1: Diagrama de proceso de obtención de ácido piroleńoso.

 

 

Partiendo de aproximadamente 70 Kg de biomasa en= la cual el 60% corresponde a la materia prima analizada y reconociendo que el porcentaje de humedad del proceso es relativamente bajo, se recupera aproxi= madamente medio litro de destilado que principalmente contiene ácido acético, como subproductos se obtienen 17 kg de biocarbón y 95 ml de alquitrán, estimando= un rendimiento = de entre 20 y 30 % para los gases con una energía máxima entregada que oscila entre 150 y 1000 kcal.  =

 

 

 

 

Figura 2.<= span style=3D'font-size:12.0pt;line-height:115%;font-family:"Times New Roman",se= rif'> Balance de materia de residuos procesados para la obtención de ácido piroleńoso.

La figura 3 presenta la transformación del desec= ho por medio de un proceso termoquímico. Los gases obtenidos se someten a proc= esos de condensación simple. Las temperaturas del proceso oscilan entre 300, 450= y 600 °C. Los resultados fundamentales que se obtienen son: Rendimiento a car= bón oscila entre 25 y 35 %, Rendimiento a gas oscilan entre 21 y 29 %, Rendimie= nto a alquitrán entre 5 y 9 %.

 

 

Figura 3. Sistema de destilación de humos producto de la pirólisis.

 

La Figura 4 muestra el análisis de la muestra de destilado realizado en un espectrofotómetro infrarrojo utilizando la metodología (FTIR), se realizó u= na dilución de 15 ml de destilado en 200 ml de agua des ionizada, se observan bandas que reflejan su composición, los compuestos orgánicos se clasificaro= n en ácidos carboxílicos, fenoles, cetonas y aldehídos que es lo que hace presumibles gases fundamentales como: H2, CO, CH4, CO= 2, C2H4, C2H6, C2H= 2, entre otros.

 

 

=  <= /p>

= Fuente: (Laboratorio de Química Analítica, ESPOCH et al., 2017)

Figura 4. Análisis en el Espectro IR del “condensado de kikuyo” con longitud de onda.=

 

Tabla 2Composición química e interpretación de resultad= os del condensado. Análisis en el Espectro IR (Laboratorio de Química Analítica, ESPOCH, 2017).

Longitud de onda. cm-1=

Rango de longitud de onda. = cm-1

Grupo y clase

Compuestos presentes

3304.43

3400-3300

 -OO-H En hidroperóxidos

Alcohol

2919.9

2990-2850

–CH3 y –CH2 en compuestos alifáticos<= /span>

Grupos alifáticos

2361.41

2410-2280

-PH en fosfinas

Nitrilo

1637.27

1640-1580

NH3+ en aminoácidos

Aminoácidos

1236.15

1240-1070

C-O-C en éter

Éter

1090.55

1100-1000

Si-O-Si en siloxanos

Compuestos de organosilicio y fósforo=

616.45

645-615

Naftaleno

Compuestos halogenados

 

Fuente: Spectra–Structure Correl= ations in the Mid- and Far-infrared. H.F. Shurvell. Queen’s University, Kingston, Ontario, Canada.

 

Discusión

La investigación confirma la aplicación de una eficiente tecnología desarrolla= da para la obtención de vinagre de bambú, por la Facultad de Ciencia y Tecnolo= gía de Materiales de la Universidad Forestal de Beijing (china) y que ha sido adaptada a nuestro medio potenciando el uso de residuos orgánicos disponibl= es y accesibles, en este contexto, por su naturaleza y origen, contribuye a la gestión de impactos ambientales negativos significativos del medio y con posteriores investigaciones, una potencial contribución con el ambiente, reduciendo la utilización de productos químicos como fertilizantes que a la= rgo plazo, inhiben los ciclos biológicos de los suelos para su regeneración natural.  Con los análisis realizad= os al producto, es posible relacionarlo con el denominado vinagre de bambú, cuyos componentes identificados fueron del 70,65% en base al área del pico de espectros, en la que los componentes acéticos ocuparon el 42,32%, con el ác= ido acético como componente principal, los componentes fenólicos del 23,22% con fenol, guaiacol y su syringol como componentes principales, Componentes neu= tros del 5,11% con furfural y ciclopentanona. (Jun, 2006), El vinagre de bambú, actualmente es utilizado para potenciar el crecimiento radicular, con los porcentajes que  se menciona. El análisis que arroja el FTIR, son similares al vinagre de bambú, se puede asumir, que el vinagre proveniente de P. clandestinum L, podría ser usado con éxito para crecimiento radicular e= ntre otras aplicaciones agropecuarias que serían probadas con futuras investigaciones.

 

Una posible valoración económica de los residuos orgánicos producto de diferent= es actividades de poda no han sido de interés de los sistemas económicos por tratarse de material desechado, es necesario incluir a este proceso en el m= arco de la economía, su inserción a la actividad económica como materia primaria para su reutilización se vería determinada por la posible utilidad agropecu= aria de los subproductos como reemplazo de géneros comerciales que cumplen las mismas funciones pero reduciendo los riesgos ambientales por su naturaleza orgánica. (Aguilera, 2006).

 

Conclusiones

 

ˇ      =      Como subproducto de la pirolisis de la materia orgánica se obtiene el biocarbón, en una cantidad de 17 kg de una biomasa inicial de 42 kg, es decir, con 40 % de rendimiento, el cual debido= a sus características físicas es propicio para sistemas de secuestro de CO2.

ˇ      =       El análisis FTIR del destilado obtenido del proceso realizado evidencia la presencia de compuestos orgánicos como: ácidos carboxílicos, fenoles, cetonas y aldehídos con lo que se confirma la similitud con los productos obtenidos de procesos realizados para el bambú.

ˇ      =      El proceso de destilación no operó al = 100 % de su capacidad debido a errores sistemáticos y aleatorios por lo que se obtuvo 500 ml de ácido piroleńoso, la optimización de sistema aumenta la posibilidad de obtener mayores volúmenes de ácido piroleńoso.

ˇ      =      La eficiencia del proceso = depende especialmente de la cantidad de ácido acético obtenido, pues es el principio activo más utilizado, se determina que el rendimiento varía mucho con la cl= ase y mezcla de residuos utilizados en el proceso, a más de la eficiencia de condensación.

ˇ      =      Si el kikuyo cuenta con un elevado promedio de fracción soluble de proteína cruda (Tabla 1), no es pos= ible que exista cantidades de proteína en el condensado obtenido, sin embargo, al existir concentraciones de fracciones no degradables permite suponer que ex= ista también en el proceso de destilado, se considera también la composición ini= cial en base seca para determinar la eficiencia del producto aplicado en el suel= o.

ˇ      =       La acentuada crisis económica, la cultura productiva, la dependencia de los productores de la fertilización química, los bajos niveles productivos y el deterioro constan= te de los suelos evidencia la importancia del uso de esta tecnología como una alternativa productiva de bajo costo y con énfasis agroecológico.

Agradecimientos<= /o:p>

A los seńores estudia= ntes Alex Escobar, Byron Cajamarca, Félix Vaca y Diego Carrillo de la carrera de Ingeniería en Biotecnología Ambiental de la Escuela Superior Politécnica de= Chimborazo, que fueron parte fundamental de la presente investigación.

 

 

Referencias Bi= bliográficas

Aguilera, U. (2006). El valor económico del medio ambiente. Obtenido de:

 http://www.revistaecosistemas.net/artí= culo

Br= adley, M. (2002). Logotipo de Thermo Fisher Scientific. Obtenido de Fundamentos de FTIR: https://www.thermofisher.com/ec/en/home/industrial/spectroscopy-elemental= -isotope-analysis/spectroscopy-elemental-isotope-analysis-learning-center/m= olecular-spectroscopy-information/ftir-information/ftir-basics.html

Burnette, R. (2013). An Introduction to Wood Vinager= . Obtenido de c.ymcdn.com: https://c.ymcdn.com/sites/echocommunity.site-ym.com/resource/collection/D= 9D576A1-771A-4D95-A889-4FBD9E75D03D/TN_77_An_Introduction_to_Wood_Vinegar.p= df

CharMarker. (2009). Producing Pyrolysis Liquids and = wood vinegar from biomass. Obtenido de www.esenergy.com.au: http://www.esenergy.com.au/wp-content/uploads/2016/0= 3/CharMaker-MPP-Pyrolysis-liquids-production.pdf

Choi, J. Y. (2009). Effect of Wood Vinegar on the Performance, Nutrient Digestibility and Intestinal Microflora in Weanling Pigs. Asian-Aust. J. Anim. Sci., 8.

Hagner, M. (2013). Potential of the slow pyrolysis products ISBN 978-952-10-9169-8 . Ob= tenido de helda.helsinki.fi: https://helda.helsinki.fi/bitstream/handle/10138/40305/hagner_dissertatio= n.pdf

Ikeshima, Y. (1999). Method of Producing and Using Bamb= oo Charcoal and Bamboo Vinegar. Nosan Gyoson Bunka Kyokai, 23.

Jun, M. (2006). Preliminary study of application effect= of bamboo vinegar on vegetable growth. Stud. China, 5.

 

 

 

 

 

 

 

 

 

 

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[1] Facultad de Ciencias, Escuela de Ciencias Químicas, Escuela Superior politécnica de Chimborazo, Riobamba, Ecuador. E-mail: dburbano@es= poch.edu.ec

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                                                 =                                                                      ISSN: 2602-8085

                        =                                                                            =     Vol. 3, N°3.4, p. 354-36= 4, septiembre, 2019

 

Desarrollo & Crecimien= to (Volumen Especial)PAGE= 342

 

 

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