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Diseño de un proceso de producción de ácido cítrico por simulación computacional.<= o:p>

 

Design of a process of production of citrus acid by computational simulation

=  

= María Augusta Guadalupe Alcoser. [1= ], Mabel Mariela Parada Rivera. [2= ], Linda Mariuxi Flores Fiallos. [3= ] & Paúl Marcelo Manobanda Pinto. [4= ]

 

Recibido: 18-10-2019 / Revisado: 15-1= 1-2019 /Aceptado: 04-12-2019/ Publicado: 05-01-2020

 Abstract.   =                               DOI: https://doi.org/10.32/cienciadigital= .v3i1.947

 

The design of a citric acid production process from fermentation with Aspergillus Niger by computer simulation, was carried out with the use of SuperPro Designer software, the design parameters were established based on previous studies, which were entered into the calculation platform, subsequently the results obtained in= the design were analyzed technically and economically, which allowed to determi= ne an amount of citric acid production of 6 914. 69 ton / year, when using FOB prices (Free on board) you have an investment total of $ 31,460,000 together with a NPV (net present value) of $ 165,000 and an IRR (internal rate of return) of 8.05%, indicating that the project can be carried out and is profitable in a time of retribution 8 years old The process consists of two stages: fermentation and isolation, which must be carried out under the operating conditions (T =3D 25ºC and P =3D 1 atmosphere in most operations)= and the optimal fermentation conditions for Aspergillus niger<= /span> (T =3D 35ºC, pH =3D 5.8 and P =3D 1 atmosphere) that are suitable to obtain= a quality product that can be offered in the national and international market. Final= ly, it is proven that the use of software allows technical studies to be develo= ped without the need to resort to long periods of time with experimental labora= tory tests, that is, it saves us: time, pre-design costs and errors.

 

Keywords: Chemical Engineering / Industrial Processes / Simulation/ Fermentation/ Operation parameters

Resumen.

El diseño de un proceso de producción de ácido cítrico a partir de la fermenta= ción con Aspergillus Niger por simulación computacional, se realizó con el uso del software SuperPro Designer, los pa= rámetros de diseño se establecieron en base a estudios previos, mismos que se ingres= aron a la plataforma de cálculo, posteriormente los resultados obtenidos en el diseño se analizaron técnica y económicamente, lo que permitió determinar u= na cantidad de producción de ácido cítrico de 6 914. 69 ton/año, al usar preci= os FOB (Free on board)= se tiene una inversión total de $ 31 460 000 junto a un VAN (Valor actual neto= ) de $165 000 y un TIR (Tasa interna de retorno) del 8.05%, lo que indica que el proyecto se puede llevar a cabo y resulta rentable en un tiempo de retribuc= ión de 8 años. El proceso consta de dos etapas: fermentación y aislamiento, que deben realizarse bajo las condiciones de operación (T=3D 25ºC y P=3D 1 atmósfera en la mayoría de las operaciones) y las condiciones óptimas de fermentación para el Aspergillus niger (T=3D 35ºC, pH=3D 5.8 y P=3D 1 atmósfera) que son adecuadas  para  obtener un producto de calidad que pueda ofertarse en el mercado nacional como internacional.  Finalmente, se comprueba que el uso de software permite desarrollar estudios técnicos sin la necesidad de recurrir a largos período= s de tiempo con análisis experimentales en laboratorio, es decir, nos ahorra: tiempo, costos de pre-diseño y errores.

Palabras claves: Ingeniería Química/ Procesos Industriales/ Simulación / Fermentación/ Parámetros de operación

Introducción.

El ácido cítrico (ácido 2-hidroxi-1, 2, 3-propanotricarboxílico), es un ácido orgánico que se encuentra de forma natural en las frutas, como el limón y la naranja. Pero puede sintetizarse en laboratorio a partir de microorganismos= . Se aisló por primera vez a partir del zumo de limón mezclado con cal y disolvi= endo el precipitado con ácido sulfúrico (Sánchez , Ortiz, & Betancourt, 2004= ).

Según Kumar & Jain (2008), en su investigación: “Solid s= tate fermentation studies of citric acid production”, alrededor del 99% de la producción mundial de ácido cítrico se da por procesos microbianos. Se comercializa co= mo un ácido anhidro o monohidratado, se espera una producción anual de 1.5 millones de toneladas de las cuales el 70% se utiliza en la industria de alimentos y bebidas como acidificante o antioxidante para preservar o mejor= ar los sabores y aromas de jugos de frutas, helados y mermeladas. 20% se usa, = en la industria farmacéutica como antioxidante para conservar las vitaminas, efervescentes, correctores de pH. El 10% restante se utiliza en la industria química como un agente de formación de espuma para el ablandamiento y el tratamiento de los textiles. En la metalurgia, se usa para el abrillantado y eliminación del óxido en metales como el cobre y aleaciones como el latón. = El ácido cítrico también se utiliza en la industria de los detergentes como un sustituto de fosfato, debido al menor efecto eutrófico. En Ecuador no se pr= oduce ácido cítrico a nivel industrial, este se exporta desde Alemania, Estados Unidos, China, Uruguay y otros países lo cual eleva el costo de importación= , es por esto el desarrollo de un proyecto técnico-investigativo mediante el uso= de un software que permita evaluar y diseñar un proceso de producción industri= al de ácido cítrico a partir del hongo Aspergillus Niger. El elaborar una planta a escala pilo= to, implica costos e incluso el difícil acceso a materiales de tamaño reducido,= si el proceso es complejo dificulta la determinación de los parámetros bajo los cuales se debe operar para obtener una eficiencia alta, así las evaluacione= s de un proceso con el uso de simulaciones nos evitan estos gastos económicos y = de tiempo con la finalidad de optimizar el proceso.

Metodología

a) Ingeniera Conceptual del Proceso

 La investigación se desarrolló en forma ordenada y sistemática, iniciando con = la revisión de fuentes bibliográficas específicas al tema, como libros, artícu= los científicos, páginas web, para definir conceptos, teorías, condiciones y variables de proceso. La simulación del proceso de producción de ácido cítr= ico con el uso de Aspergillus Niger, se desarrolla con el software SuperPro Designer; que es= un programa computacional para realizar la simulación de procesos en estado estacionario. La simulación permite predecir la operación de un proceso cua= ndo se han alcanzado condiciones de estacionalidad, esto facilita el estudio de= la sensibilidad del sistema frente a cambios en los distintos parámetros y variables de operación (Designer, 2019).

Para iniciar la simulación de un proceso en el software, se siguen los pasos que= se indican a continuación en la Figur= a 1:

Figura 1: Modalidad de trabajo para un proceso = en el simulador

            Realizado por: Autores, 2019

b) Proceso de diseño y simulación

 El proceso de diseño y simulación de un proceso de producción sigue los pasos = que se indican a continuación. En primer lugar, se inicia con la generació= n de ideas sobre el proceso a diseñarse, en este caso la producción de ácido cít= rico por medio de fermentación, donde realiza la ingeniería conceptual del proce= so, se indican las etapas, además de procesos y operaciones necesarias para cum= plir con el objetivo propuesto. Una vez que se ha definido la ingeniería concept= ual, se procede a realizar la planificación estratégica del proceso de diseño y posterior simulación. En segundo lugar, se desarrolla el proceso de acuerdo= a la ingeniería conceptual y se evalúa las alternativas, para seleccionar la = más viable. Posterior a esto, se diseñan las facilidades y se realizan los ajus= tes al proceso, esto en primer lugar se lo puede realizar por medio de simulación, esto nos dará como resultado la ingeniería de detalle. Finalmente, se proce= de a optimizar el proceso, analizar los tiempos de los ciclos y se puede program= ar la producción a llevarse a cabo en la planta diseñada.

Diagrama General del Proceso de Producción de Ácido Cítrico

En la Figura 2, se indica el diag= rama de flujo del proceso. El diseño del proceso se realiza para obtener 6 914 toneladas métricas de ácido cítrico por año en forma cristalina, que es utilizado  por la industria para preservar los alimentos y bebidas, así como mejorar su sabor

Figura 2: Diagrama del proceso de producción de ácido cítrico

Fuente: SuperPro Designer®<= o:p>

 La fuente de carbono que se utiliza para la fermentación es la melaza, la cual= se diluye con agua hasta un 50% de azucares fermentables (V-101). El material particulado suspendido se remueve por medio de filtración (PFF-101). Los io= nes metálicos, particularmente el ión de hierro, son subsecuentemente removidos por una columna cromatográfica de intercambio ió= nico (C-101) y la solución de materia prima purificada se esteriliza con calor e= n un pasteurizador (ST-101). Los nutrientes tal como zinc, fuentes de amonio, potasio, fósforo, magnesio y cobre, son disueltos en agua (V-104) y esterilizado al calor (ST-101).

Después de la esterilización, los nutrientes y la fuente de carbono se transfieren = a un fermentador (FR-101). La fermentación ocurre de acuerdo a la siguiente estequiometría de masa:

Reacción 1

 El tiempo de fermentación es de 5 días a una temperatura constante de 35 °C, c= on un pH de 5.8 hasta tener un rendimiento de reacción de 99%. El aire necesar= io para mantener las condiciones aerobias de la fermentación se realiza por me= dio de un compresor (G-101). El agua de enfriamiento remueve el calor producido= por el proceso exotérmico y mantiene la temperatura constante.

Para satisfacer la demanda de producción, la fermentación es llevada a cabo por 7 fermentadores que operan en modo alternado. Además, la planta opera todo el= día y un lote de fermentación se inicia y otro se finaliza diariamente. Cada fermentador tiene un volumen de 150 m3. Una vez completada la fermentación, el caldo se descarga dentro de un tanque de retención (V-105)= , el cual actúa como un tanque de regulación buffer entre el lote que ingresa y = la sección de salida.

Para el aislamiento de ácido cítrico, es decir, obtener este compuesto de forma pura, su purificación inicia con la remoción de la biomasa por un filtro al vacío rotatorio (RVF-101). Este líquido clarificado de la fermentación subsecuentemente fluye dentro de un reactor agitado (V-106) donde es añadido aproximadamente 1 parte de cal hidratada, Ca (OH)2, por 2 partes= de licor esto lentamente añadida para formar el precipitado de citrato de calc= io. El citrato de calcio es entonces separado por medio de un segundo filtro rotatorio al vacío (RVF-102) y el filtrado libre de citrato (Desecho Acuoso= -1) es enviado a un tanque de colección de desechos.

La torta de citrato de calcio se envía a otro reactor agitado (V-107), donde se añade  ácido sulfúrico para formar un precipitado de sulfato de calcio (yeso). Un tercer filtro (RVF-103) remueve el precipitado de yeso y una solución de ácido cítrico impuro. Es importante cuidar el control del pH y = la temperatura en la precipitación para maximizar el rendimiento de ácido cítr= ico. La solución resultante es concentrada y cristalizada en un cristalizador continuo (CR-101).

 c) Descripción del proceso de producción de ácido cítrico

Como se observa en la Figura 3, el proceso industrial de producción del ácido cítrico se divide en dos seccion= es: fermentación y aislamiento. En la primera se encuentran todos los procesos necesarios para llevar a cabo la obtención del ácido cítrico a partir de la fermentación de la melaza utilizando Aspergillus Niger. La segunda sección del proceso, corresponde a todas las operaciones necesarias, para obtener el ácido cítri= co puro en forma cristalina.

Figura 3: Secciones del proceso de producción de ácido cítrico

Realizado por:= Autores, 2019

 

Sección de Fermentación

 Para la obtenc= ión del ácido cítrico mediante fermentación con Aspergillus Niger se utiliza como materia prima la mela= za, que es la fuente de carbono.

La melaza es diluida, para proceder a remover los sólidos suspendidos, además = de eliminar los iones metálicos, especialmente el hierro, y finalmente esterilizarla mediante pasteurización con el fin de eliminar todos los microorganismos que pueda producir otro tipo de compuesto no deseado en la fermentación. Se añade a la melaza sustancias que mejoraran el proceso de fermentación y vuelve a ser esterilizada antes de realizarse la fermentación respectiva.

Una vez preparada la mezcla de melaza y aditivos se procede a realizar la fermentación en condiciones aeróbicas mediante inóculo de Aspergillus Niger hasta obtener el producto final y almacenarlo, para que posteriormente este producto sea dirigido hacia la sección de aislamiento.

 Sección de Aislamiento=

En el producto final de la fermentación se procede a eliminar la biomasa, dando como resultado un producto totalmente líquido y sin sólidos. En este produc= to se elimina los sub productos y aditivos residuales del proceso de fermentac= ión mediante precipitación, obteniéndose finalmente una corriente líquida de ác= ido cítrico que por procesos de cristalización y secado se consigue el producto final: ácido cítrico en forma cristalina.

 d) Requerimiento de materias primas

 Como materias primas se requiere: agua, melaza, sulfato de amonio, nutrientes, nitrógeno, hidróxido de sodio, hidróxido de calcio, nitrógeno, oxígeno, cal y ácido sulfúrico. Mientras que como productos se tiene: biomasa, cristales de ácido cítrico, citrato de calcio, dióxido de carbono, yeso, impurezas,=

 e) Datos Generales del Proceso para el c= álculo

Los cálculos de diseño requieren de los datos generales del proceso de producci= ón de ácido cítrico, estos datos son referentes a como se opera la planta de producción y el tiempo de operación de la misma como se muestra en la tabla 1.

Tabla 1: Datos generales del proceso

Tiempo de Operación Anua= l

47.90

semana

Tasa de Referencia de Un= idad de Producción

6 914 691.48

kg MP

Tamaño del lote

21 081.38

kg MP

Tiempo de preparación de ingredientes del lote

199.18

h

Tiempo del ciclo de prep= aración de ingredientes

24.00

h

Número de lotes por año<= /span>

328.00

 

 

*MP: Flujo total de la corriente “Producto final”

Realizado por:= Autores, 2019

MP corresponde al Flujo Total de la Corriente 'Producto Final', el tiempo de operación anual, se encuentra dado en número de semanas y su cálculo se efe= ctúa de acuerdo al tiempo de operación de la planta, cabe mencionar que, la plan= ta opera continuamente y las operaciones son una mezcla de procesos por lote, semicontinuos o continuos.

f) Requisitos de partida de materia prima por sección

En los requisitos de materia prima se presenta la sección de producción con la respectiva materia prima de partida como es la glucosa en el caso de la fermentación y como producto activo al ácido cítrico en fase acuosa. Mientr= as que, la sección de aislamiento tiene como materia prima de partida el ácido cítrico producido en la sección de fermentación y como producto activo el á= cido cítrico en forma de cristales.

 

Tabla 2: Requisitos de partida de ma= teria prima por sección

Sección

Material de Partida

Producto Activo

Rendimiento Másico

Masa

(%)

Bruta

 

Rendimiento

 

(%)

Sección de Fermentación<= /span>

Glucosa

Ácido Cítrico

84.53

84.53

Sección de Aislamiento

Ácido Cítrico

Cristales de Ácido Cítri= co

92.25

92.25

 

Realizado por:= Autores, 2019

La cantidad necesaria (kg/kg), representa el mínimo requerido para que los procesos de producción se ejecuten de forma eficiente. El rendimiento molar, rendimiento másico y rendimiento de masa bruta, corresponde al porcentaje de transformación de materia prima a producto activo mediante los procesos de producción, como se indican los valores en la tabla 2.

g)  Total de materias primas<= span lang=3DES-EC style=3D'font-size:12.0pt;line-height:115%;font-family:"Times = New Roman",serif'>

 En un proceso = de producción es importante conocer las cantidades que se utilizan de materia prima que interviene en el proceso de producción, para poder planificar el stock de las mismas.

            Tabla 3: Total de  materias pri= mas

Material

kg/año

kg/lote

Agua

56 701 804

172 871.354

Melaza

17 646 400

53 800.000

Sulfato de Amonio=

277 580

846.281

Nutrientes

1 894 077

5 774.626

Nitrógeno

49 204

150.013

NaOH (1 M)

2 617 888

7 981.366

Aire

123 178 744

375 544.952

Cal  (33%)

13 659 737

41 645.539

H2SO4 (10% w/w)

57 628 992

175 698.145

TOTAL

273 654 427

834 312.276

 

Realizado por:= Autores, 2019

 En la tabla 3, se presenta los kilogramos necesarios de cada materia prima por año, lote y cantidad de producto final.

 h) Balance general de masa del p= roceso de producción de ácido cítrico

En el balance general de compuestos se presentan las sustancias químicas, impurezas y nutrientes intervienen en todo el proceso de producción.

La melaza en este balance se encuentra representada como glucosa e impurezas, también se presencia un componente NFS, el cual es Nitrógeno, Fósforo y Azu= fre que se utiliza para efectuar la fermentación.

 

i) Condiciones y variables óptimas de operación

      =    Identificación de los equipos utiliza= dos en el diseño

A continuación en la tabla 4= , se presentan los equipos utilizados en el proceso de producción de ácido cítri= co, con sus características generales y el modo de operación, como: por lotes o= batch, continuos y semicontinuos.

Tabla 4: Equipos utilizados en el di= seño

Diagrama

Descripción

 

Tanque de mezcla<= /b>

Este proceso forma parte  de un sistema y permite realizar  mezclas o almacenamien= to de líquidos  que requieren ser agitados.

 

Filtro de Placa y Marco<= /span>

Este proceso se utiliza = en la industria química, alimentos e industrias ambientales, presenta la filtración y formación de la torta por la remoción de  los sólidos suspendidos desde una lechada.

 

Cromatografía de adsorci= ón de lecho empacado

Este proceso se refiere a cualquier tipo de cromatografía de adsorción, tal como  intercambio iónico, afinidad, HIC, fases  reversas, etc., donde se encuentra una columna de lecho empacado.

 

Pasteurización

Este proceso representa = un pasteurizador y calcula la inactivación de microorganismos y cinética de = degradación  de componentes alimenticios.

 

Fermentador por lote

Operación que representa= la secuencia de operación en un fermentador, las operaciones típicas pero no necesariamente incluyen reacciones de fermentación como estequiometria o = cinética.

 

Almacenamiento de Lote en Tanque de Fondo plano

Este equipo permite almacenar productos  líquidos, por lo que un sin número de procesos = lo utilizan.

 

Filtro Rotario al Vacío<= /span>

Este diagrama representa= la filtración con

generación de torta de f= orma continua obteniendo altos rendimientos.

 

Neutralización

Este equipo representa la neutralización de un compuesto ácido o básico: Pudiendo especificarse cualquier número de reacciones por estequiometría.

 

Cristalizador Continuo

Equipo utilizado para la evaporación de una capa fina de producto, provocando la  cristalizac= ión de los compuestos de interés.

Secador Rotatorio=

Equipo que maneja una gr= an eficiencia y se utiliza en la industria química y de alimentos. El proces= o de secado puede darse directamente con uso de una  corriente de gas caliente o indirectamente mediante la utilización de vapor en una chaquet= a.

Fuente: SuperPro Designer®<= o:p>

      =    Diseño y simulación del proceso de producción de ácido cítrico

 Para el diseño y simulación se selecciona el tipo de proceso, en este caso los fermentadores tienen una operación por lotes, mientras que, el cristalizador opera de forma contínua. Luego se debe ingresar= todas las sustancias que intervienen en el proceso: materia prima y productos, ad= emás de registrar las mezclas.

Posterior a esto, se realiza el diagrama del proceso junto a la secuencia de operacio= nes para cada equipo. Seguido se procede a revisar los parámetros de los equipo= s, el costo de los mismos, las características mecánicas, los aditivos, el rendimiento y si existieran comentarios.

Resultados

Para la modelación se toman como referencia datos de estudios previos para abast= ecer la necesidad de ácido cítrico para el Ecuador, se plantean cantidades grand= es de materia prima, por tanto, se obtiene una gran producción de ácido cítric= o; como se muestra en la tabla 5.

 

Tabla 5: Datos modelo= de simulación

 

Melaza

Agua

Cristales de ácido cítri= co

kg/lote

kg/lote

kg/lote

53 800

42 000

21 081.38

 

Realizado por:= Autores, 2019

 En la tabla 5, se muestran los principales valores que se obtienen en la simulación del modelo para la producción de ácido cítrico. Se muestran cantidades de materia prima, producción total de ácido cítrico, total de residuos y el resumen de costos para el análisis económico.

Tabla 6: Datos técnicos y económicos= de los cuatro modelos simulados

 

Datos

Melaza (kg/año)

17 646 400

Agua (kg/año)=

56 701 804

Total de materias primas (kg/año)

273 654 427

Tasa de producción Ac. Cítrico (kg/año)

6 914 691.48

Tasa de producción de Ac. Cítrico (ton/año)

6 914

Costos FOB de equipos ($= )

7 018 000

Inversión total de capit= al ($)

31 460 000

Margen bruto (%)<= /b>

16.09

Retorno sobre la inversi= ón (%)

11.28

Tiempo de retribución (a= ños)

8.86

TIR (%)

8.05

VAN (8%)     

165 000

 

Realizado por: Autores, 2019

 En base a la Tabla 6, se define q= ue el modelo de simulación es óptimo para la producción de ácido cítrico por vía = de fermentación con el uso de Aspergil= lus niger, este modelo es viable desde el punto de vi= sta técnico y económico,  se tiene una producción acorde a las necesidades= del mercado, la inversión es menor y la ganancia es en un tiempo aproximado de 8 años.

·      =    Estimación de costos de las operaciones del proyecto

 

Base de costos.

Los resultados de los costos presentados en esta sección se encuentran en base a costos del año 2012, en función al año de los costos encontrados en bibliografía y proveedores de equipos. Además, los costos se encuentran expresados en dólares y en precios FOB  (Free On<= /span> Board).

Resumen de costos

En este apartado se presenta el resumen de costos de toda la planta de producc= ión de ácido cítrico, para lo cual cada ítem tiene un valor y se encuentra expresado en sus unidades respectivamente.

  Tabla 7: Resumen de costos

Inversión Total de Capit= al

31 460 000

$

Costo de Operación

31 460 000

$/año

Costo neto de Operación<= /span>

11 605 000

$/año

Ingresos

13 829 000

$/año

Tasa de Costo Base Anual=

6 914 691

kg MP/año

Costo unitario de Produc= ción

1.68

$/kg MP

Costo neto de Producción Unitaria

1.68

$/kg MP

Ingresos de Producción Unitaria

2.00

$/kg MP

Margen Bruto

16.09

%

Retorno sobre la inversi= ón

11.28

%

Tiempo de retribución

8.86

Años

TIR (Después de Impuesto= s)

8.05

%

VAN (con 8.0% Intereses)=

165 000

$

 

Realizado por:= Autores, 2019

En la Tabla 7, el flujo total de = la corriente de producto final está representado por MP, mientras que el TIR corresponde a la Tasa Interna de Retorno que se refiere a la rentabilidad q= ue genera un proyecto determinado cuando sus flujos de caja son periódicos. El= VAN es el valor actual neto, que es el cálculo a valor presente, el dinero que = una inversión generará en el futuro.

 Discusión de resultados

Se realizó un modelo de simulación para la producción de ácido cítrico por fermentación con el uso de Aspergil= lus Níger, en el que se ingresan cantidades de materia prima, tamaño de equipos, lo que permite obtener los costos de producción y la inversión tot= al de la planta.

El diseño del proceso de producción consta de dos secciones, la sección de fermentación en donde se utiliza como materia prima la melaza como fuente de carbono (53 800 kg/lote) para esta etapa. A continuación en un tanque de me= zcla se diluye la melaza (42 000 kg/lote), con el fin de remover los sólidos suspendidos (Filtro) y eliminar los iones metálicos (columna de intercambio iónico), es necesario pasteurizar con el fin de matar los microorganismos no deseados y evitar la formación de otros compuestos. Al fermentador ingresa también una mezcla de sulfato de amonio y nutrientes (nitrógeno, fósforo y azufre), con el fin de mejorar el producto para la siguiente sección. Con e= sta mezcla que se prepara y los aditivos se realiza la fermentación en condicio= nes aeróbicas mediante inóculo de Asper= gillus Niger, bajo un pH de 5.8 y una temperatura = de 35◦C durante cinco días,  hasta obtener el producto final, almacenarlo y dirigirlo hacia la siguiente sección: la de asilamiento.=

En la sección de aislamiento se elimina la biomasa, subproductos y aditivos residuales (Filtro al vacío rotatorio), obteniendo un producto líquido libr= e de sólidos (ácido cítrico), que por cristalización y secado se obtiene el ácido cítrico en forma cristalina (21 081.38 kg/lote).

Según Rivada (2008), en su estudio planta industrial = de producción de ácido cítrico a partir de melazas de remolacha la mejor cepa = que permite el crecimiento de Aspergill= us Niger es la ATTC 11414, en un pH ácido de 5.8 y u= na temperatura de 30◦C, en la investigación los fermentadores operan a 35◦C durante cinco días con el fin de producir la cantidad ideal de á= cido cítrico.

El simulador SuperPro Designe= r según Cara, Gómez&Martínez en su estudio “Aplicación de SuperPro De= signer en el análisis de sensibilidad en instalaciones para la producción de biocombustibles y bioproductos”, menciona que é= sta plataforma presenta una herramienta de análisis de costes y emisiones lo qu= e la hace muy versátil para su utilización en diferentes asignaturas relacionadas con los procesos fermentativos, ambientales, energías renovables y de producción química; este estudio evidencia la gran utilidad que proporciona= el simulador al permitir diseñar el proceso de producción de ácido cítrico por fermentación con el uso del hongo A= spergillus Niger.

La inversión total de la planta para el modelo es de $ 31 460 000, el Van (Val= or neto actual) que es de $ 165 000, el TIR (Tasa interna de retorno) de 8.05%= en un tiempo de retribución del capital de 8 años. Según Mete (2014), en su estudio “Valor actual neto y tasa de retorno: su utilidad como herramientas para el análisis y evaluación de proyectos de inversión”, manifiesta que el= VAN y el TIR son imprescindibles para garantizar un correcto análisis financiero con el fin de asegurar la estabilidad y proyección futura de las organizaciones, en este caso los valores del VAN y TIR al ser positivos, indican que la inversión en el proyecto es rentable, debido a que se recupe= ra el capital y existe ganancia en un tiempo estimado.

Al no existir estudios previos similares a esta investigación basada en una simulación, no se establecen comparaciones.

El impacto ambiental que produce el proceso no representa un daño considerable para el medio ambiente, se tiene 141 959 226 kg/año de residuos líquidos, orgánicos, acuosos y emisiones; los residuos provenientes de aguas de lavado son los que se encuentran en mayor cantidad (103 190 859 kg/año), por esta = razón se debe tratar los residuos previo a su descarga o buscar una alternativa p= ara usarlos y de esta manera disminuir la contaminación leve que provocan, el c= osto total para el tratamiento de residuos es de $ 629 648, que se incluyen en la inversión total.

Conclusiones.

·      =    El diseño del proceso de producción de ácido cítrico por fermentación con el u= so de Aspergillus Níger consta de = dos secciones: fermentación y aislamiento. La sección de fermentación cuenta con trece operaciones entre filtración, mezcla, intercambio iónico y fermentaci= ón en sí; La sección de asilamiento tiene diez operaciones entre filtración al vacío, mezcla, cristalización y secado. La cepa  de Aspergillus Níger que más se utiliza para la producción de ácido cítrico a nivel industrial es la ATTC 11414.

·      =    La simulación del proceso de producción de ácido cítrico indica que es viable, acorde al análisis económico; se asemeja más a un proyecto real que a nivel técnico y económico se podría llevar a cabo.

·      =    Para que el proceso de producción de ácido cítrico se realice de manera adecuada= se debe controlar las condiciones y variables de operación; para la sección de= fermentación, las variables a tener en cuenta son: temperatura constante para la mayoría = de operaciones de 25◦C y a 1 atmósfera de presión. La fermentación del h= ongo (Aspergillus N= iger), se da a un pH de 5.8; a una temperatura óptima de 35◦C, durante cinco días; se recomienda usar 7 fermentadores para evitar cuellos de botella y lograr que el proceso sea continuo. Para la sección de aislamiento, la temperatura opera entre un rango más elevado respecto al anterior (25-110◦C), y la presión es de 1 atmósfera.

·      =    La inversión total de capital para el modelo óptimo es de $ 31 460 000; los índices de rentabilidad que se determinan son: la tasa interna de retorno (= TIR) que refleja un valor de 8.05%, el Valor Actual Neto es de $165 000; en un tiempo de retribución de 8 años, estos valores indican que el proyecto es rentable y es factible invertir.

 

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PARA CITAR EL ARTÍCULO INDEXADO.=

 

 <= /span>

Gua= dalupe Alcoser, M. A., Parada Rivera, M. M., Flores Fi= allos, L. M., & Manobanda Pinto, P. M. (2020). Dis= eño de un proceso de producción de ácido cítrico por simulación computacional. = Ciencia Digital, 4(1), 54-71. https://doi.org/= 10.33262/cienciadigital.v4i1.1063

 

 



 

 

 

El artículo que se publica es de exclusiva responsabilidad de los autores y no necesariamente reflejan el pensamiento de la Revi= sta Ciencia Digital.

 

El artículo queda en propiedad de la revista y, por tanto, su publicación parc= ial y/o total en otro medio tiene que ser autorizado por el director de la Revista Ciencia Digital.

 

 

 

 



[1] Escuela Superior Politécnica de Chimborazo, Chimborazo, Ecuador, maria.guadalupe@espoch.edu.= ec

[2= ] Escuela Superior Politécnica de Chimborazo, Chimborazo, Ecuador, <= span lang=3DES-EC style=3D'font-size:10.0pt;line-height:115%;font-family:"Times = New Roman",serif'>mparada@espoch.edu.ec

[3] Escuela Superior Politécnica de Chimborazo, Chimborazo, Ecuador, linda.flores@espoc= h.edu.ec

[4] Universidad Estatal Amazónica , Chimborazo, Ecuador, pmanobanda@uea.edu.ec

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                                                 =                               Vol. 4, N°1, p. 54-72, enero - marzo, 20 20

 Educación e igual= dad de género    =                                                                                =                               Página 6

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