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Obtención de queso mozzarella, mediante el diseńo = de un proceso industrial, en la provincia de Chimborazo, cantón Colta

Obtaining mozzarella cheese, through the design of an industrial process, in the prov= ince of Chimborazo, city Colta

= ¹

Danielita Fernanda Borja Mayorga<= /o:p>

https://orcid.org/000= 0-0002-8438-064X

=

Escuela Superior Politécnica del Chimborazo (ESPOCH), Faculty of Chemical Engineering, Riobamba, Ecuador

dborja@espoch.edu.ec <= /span>

= ²

Marco Raul Chuiza Rojas

https://orcid.org/000= 0-0003-1908-8033

Escuela Superior Politécnica del Chimborazo (ESPOCH), Faculty of Chemical Engineering, Riobamba, Ecuador <= /span>

m.c= huiza@espoch.edu.ec

= ³

Mónica Lilian Andrade Avalos

https://orcid.org/000= 0-0001-5736-5607

Escuela Superior Politécnica del Chimborazo (ESPOCH), Faculty of Chemical Engineering, Riobamba, Ecuador

moandrade@espoch.edu.ec=

&nb= sp;

Artículo de Investigación Científica y Tecnológica

Enviado: 08/0= 4/2022

Revisado: 22/= 05/2022

Aceptado: 27/= 05/2022

Publicado:24/= 06/2022

DOI: https://doi.org/10.33262/= ap.v4i2.2.228

&nb= sp;

Cítese:

Borja Mayorga, D. F., Chuiza Rojas, M. R., & Andrade Avalos , M. L. (2022). Obtención de qu= eso mozzarella, mediante el diseńo de un proceso industrial, en la provincia = de Chimborazo, cantón Colta. AlfaPublicaciones, 4(2.2), 146–169. https://doi.org/10.33262/= ap.v4i2.2.228

ALFA PUBLICACIONES, e<= span style=3D'font-size:8.0pt;line-height:115%;font-family:"Times New Roman",s= erif; mso-fareast-font-family:Calibri;mso-ansi-language:ES-EC;mso-fareast-langu= age: EN-US'>s una revista multidisciplinar, trimestral, que se publicar= á en soporte electrónico tiene como misión contribuir a la   formación de profesionales competentes con visión humanística y crítica q= ue sean capaces de exponer sus resultados investigativos y científicos en la misma medida que se promueva mediante su intervención cambios positivos e= n 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 Afiliaci= ón 663) www.celibro.org.ec

Esta revista = está protegida bajo una licencia Creative Commons Attribution Non Commercial No Derivatives 4.0 International. Copia de la licencia: http://creativecommons.org/licenses/by-nc-nd/4.0/

Palabras clav= es:

leche, queso mozzarella, diseńo, proceso, industria láctea.

Resumen

Introducción. La industrialización de un proceso permite obtener un producto en menor tiempo y se asegura la calidad de este con lo establecido en la norma NTE INEN 82: Queso mozzarella. Requisitos. Objetivo. Diseńar un proceso industrial para la obtención de queso mozzarella en la planta procesadora “SIERRALAC” perteneciente a la Corporación de Organizaciones Campesinas e Indígenas de las Huaconas y Culluctus (COCIH), en la Provincia de Chimborazo, Cantón Colta. Metodología. <= span style=3D'mso-bidi-font-style:italic'>Se inició con la caracterización de la materia prima, mediante análisis fisicoquímicos y microbiológicos basados en la NTE INEN 0009: 2012. Leche cruda. Requisito= s. NTE INEN 9:2012. Además, se realizó pruebas para identificar las variable= s de operación para la elaboración de queso mozzarella a nivel de laboratorio arrojando los siguientes resultados: temperatura de pasteurización a 65 °C durante 30 minutos, temperatura de enfriamiento a 40 °C, tiempo de acidificación de 2-3 horas, pH ideal entre 5,2-5,4 para la etapa de hilad= o, temperatura de hilado a 65 °C y tiempo de salado de 3 horas. Para cumplir= con los requerimientos de la microempresa se empleó el método de fermentación enzimática debido a su alto rendimiento y calidad del producto. Resulta= dos. En b= ase a los valores de las variables de operación se realiza el diseńo de los equ= ipos a escala industrial, cuyos equipos son: una marmita con un sistema de agitación, un tanque de hilado, una lira y una mesa de moldeo para una capacidad de procesamiento de 500 litros de leche. Conclusión. La validación del diseńo de ingeniería se efectuó mediante la caracterización físico, bromatológico, y microbiológico de queso mozzarel= la de acuerdo con la norma NTE INEN 82: Queso mozzarella. Requisitos, cuyos resultados cumplen con los parámetros de calidad siendo apto para su cons= umo. Mediante un estudio de análisis financiero se verificó que el proyecto es viable, para garantizar la inocuidad del producto se recomienda aplicar b= uenas prácticas de manufactura.

Keywords: milk, mozzar= ella cheese, design, process, dairy industry.

Abstrac= t

Introduction. The industrialization of a process allows a pro= duct to be obtained in less time and its quality is ensured with the provision= s of the NTE INEN 82 standard: Mozzarella cheese. Requirements. Objectives. Design an industrial process to obtain mozzarella cheese in the "SIERRALAC" processi= ng plant belonging to the Corporation of Peasant and Indigenous Organization= s of Huaconas and Culluctus (COCIH), in the Province of Chimborazo, city Colta= . Methodology. It began with the characterization of the raw material, through physical-chemical and microbiological analyzes based on the NTE INEN 0009: 2012. Raw milk. Requirements. NTE INEN 9:2012. In addition, tests were carried out to identify the operating variables for the production of mozzarella cheese = at the laboratory level, yielding the following results: pasteurization temperature at 65 °C for 30 minutes, cooling temperature at 40 °C, acidif= ication time of 2- 3 hours, ideal pH between 5.2-5.4 for the spinning stage, spin= ning temperature at 65 °C and salting time of 3 hours. To meet the requirement= s of the microenterprise, the enzymatic fermentation method was used due to its high yield and product quality. = Results. Based on the values of the operating variables, the design = of the equipment is conducted on an industrial scale, whose equipment is: a = pot with a stirring system, a spinning tank, a lyre, and a molding table for a processing capacity of 500 liters of milk. Conclusion. The validation of the engineering design was conducted through the physical, bromatological, and microbiological characterization of mozzarella cheese according to the NTE INEN 82 standa= rd: Mozzarella cheese. Requirements, whose results meet the quality parameters being suitable for consumption. Through a financial analysis study, it was verified that the project is viable, to guarantee the safety of the produ= ct, it is recommended to apply good manufacturing practices.

<= span lang=3DEN-US style=3D'font-family:"Times New Roman",serif;mso-ansi-language= :EN-US'>

Introducción

A nivel mundial, nacional y local la producción de leche se ha incrementado paulatinamente, constituyéndose en uno de los sectores más importantes referente a la generación de empleo en el sector agrícola y en = la economía de los países (Ruíz, 2017).

La producción lechera en el Ecuador constituye una actividad product= iva sustancial por razones de orden económico y nutricional. Según estudios estadísticos realizados por el Ministerio de Agricultura, Ganadería, Acuicultura y Pesca (MAGAP), indica que existen más de 600.000 personas que dependen directamente de la producción de leche y varía en cada zona de acu= erdo con la disponibilidad que tengan en su medio y los requerimientos de cada población, siendo un ingreso relativamente seguro y creciente en los último= s días para los pequeńos productores (Cuichan, 2006).

Dentro de la industria láctea una de las tecnologías más relevantes = que se ha desarrollado es la elaboración de quesos, aprovechando todos los nutrientes que presentan la leche y así obtener quesos que presenten características nutritivas y un sabor muy exquisito como es el queso mozzar= ella (Quinzo, 2015). El queso mozzarella tiene su origen en Italia, desde allí se difundió por el resto del mundo, es un queso de pasta hilada de masa acidificada, antiguamente elaborado con leche de búfala, debido a que es es= caso conseguir la leche de búfala hoy en día es reemplazado con leche de vaca y ocupa un gran puesto en el mercado de la pizzería y de la industria quesera (Sémper, 2016). Los elementos nutricionales que aporta este producto son: proteínas, grasas, vitaminas y minerales tales como; calcio, hierro y fósfo= ro, permitiendo así el buen funcionamiento del organismo (Toro, 2011).

Los beneficios nutricionales que brinda este tipo de queso es que, al ser un alimento rico en fósforo, ayuda a mantener los huesos y dientes sanos así también una piel equilibrada, mayor resistencia física y contribuye a mejorar las funciones biológicas del cerebro. Además, por poseer un alto contenido de calcio es esencial para los huesos y consumo durante el embara= zo (Sémper, 2016).

La quesera recepta alrededor de 1000 litros de leche diario, de los cuales 400 se procesan para la elaboración de queso fresco de 500 y 1000 gr= amos con el fin de brindar a los consumidores un producto de calidad y que conse= rve su valor nutritivo, esto permite solventar la economía de la organización p= ara mejorar la calidad de vida de la zona en la cual habitan, además la cantidad restante de leche entregan a otras industrias lácteas; con el fin de contri= buir en la mejora continua de la corporación se ha visto la necesidad de obtener queso mozzarella, mediante el diseńo de un proceso industrial, el cual perm= ite ayudar a que la empresa siga creciendo y buscando nuevos mercados.

La salud alimentaria exige que los productos de consumo masivo sean aptos para el consumo humano tanto en las características bromatológicas, microbiológicas y organolépticas basadas en la NTE INEN 0082: Queso Mozzare= lla. Requisitos, es por ello la importancia de realizar un estudio de la calidad microbiológica del queso mozzarella, debiéndose conocer la calidad microbiológica de los productos que elabora esta empresa para garantizar la salud de los consumidores (Servicio Ecuatoriano de Normalización [INEN], 20= 11).

Por tanto, es significativo emprender acciones al respecto, como por ejemplo al proponer una alternativa de producción, que ofrezca a los pequeń= os productores la elaboración de un producto de calidad y con un buen rendimie= nto, pudiéndose convertir los mismos en la generación de economía propia para el sector.

Metodología

Leche

La leche = es un líquido secretado por las glándulas mamarias de las hembras de los mamíferos, obtenida por el ordeńo completo de una o más vacas bien alimenta= das y en buen estado de salud, caracterizado por poseer alto valor nutricional (Alais,1985, pp.4-5; Revilla, 1985, p.11).

Tabla 1

Composición de la leche = de varios mamíferos

Especie

% Agua

% Grasa

% Proteína

Vaca

87

3.8

3.35

Humana (mujer)

87

3.8

2.30

Cabra

86

4.8

4.30

Oveja

83

5.3

6.30

Yegua

90

0.6

2.10

Burra

91

1.2

1.50

Búfala

82

8.0

4.0

Coneja

70

10.5

15.5

Llama

86

3.2

3.9

                               Fuete: Revilla (1985)

Para llevar a c= abo el presente proyecto se sustentó en métodos, como: Inductivo, Deductivo y Experimental, para obtener los valores de las variables de operación y poder diseńar un proceso de obtención de queso mozzarella.

Para realizar la caracterización de la leche cruda, el muestreo resalta un punto importante, puesto que de ello dependen los resultados de la calidad de la materia prim= a. De acuerdo con las normas descritas a continuación:

NTE INEN 0004: 1984. Le= che y productos lácteos. Muestreo (Servicio Ecuatoriano de Normalización [INEN], 1984).

·&nb= sp;        Instructivo para “Toma de muestras de lec= he cruda” (Instructivo INT/CL/010), publicado por el Laboratorio de Control de Calidad de Leche Agrocalidad

La caracterización de la leche se basó en la NTE INEN 0009:2012. Leche cruda. Requisitos (Servicio Ecuatoriano de Normalización [INEN], 2012).

Determinación de grasa, sólidos no grasos, proteína, densidad, temperatura, lactosa, conductividad, pH

Los respectivos análisis se determinaron mediante la ayuda de un equipo denomin= ado Ekomilk Ultra, es un analizador de leche robusto, confiable y de parámetros múltiples que proporciona resultados de análisis rápidos, este no requiere = de reactivos, emite resultados precisos en tan solo 2 min aproximadamente. A continuación, en la tabla 2 se tabulan los resultados (Agrocalidad, 2017).

Tabla 2

Parámetros que analiza el equipo Ekomilk Ultra=

Parámetros

Rango

Precisión

Unidad

Grasa

0,5 - 12=

0,1

%<= /span>

Solidos no grasos

6 - 12

0,2 %

%<= /span>

Densidad

1,0260 – 1,03= 30

0,00005<= /o:p>

Proteína

2 - 6

0,2<= /span>

%<= /span>

Temperatura

0 - 50

0,1<= /span>

Lactosa

0,5 – 7<= /o:p>

0,2<= /span>

%<= /span>

Conductividad

2 - 20

1 %<= /span>

<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; position:relative;top:4.0pt;mso-text-raise:-4.0pt;mso-ansi-language:ES; mso-fareast-language:ES;mso-bidi-language:AR-SA'> (18°= C)

pH

0,00 - 14

0,02=

-<= /span>

Nota: Manual Ekomilk Ultra 2015 Fuente: Agrocalidad (2017)

Resultado de la caracterización de la mate= ria prima

Los resultados = de los análisis fisicoquímicos de la leche cruda, se muestra en la tabla 3, la mayoría de los parámetros se encuentran dentro de los requerimientos.<= /o:p>

Tabla 3

Análisis fisicoquímico de la leche cruda de la microempresa de lácte= os “SIERRALAC”

Parámetros

Método de ensayo/Norma=

Unidad

Resultado

Valor Limite permisible

Mínimo

Máximo

Grasa

PEE/CL/002

Método de referencia (AOAC 972.16)

(g/100ml)

3,95

3,0

-

Proteína

PEE/CL002

Método de referencia (AOAC 972.16)

(g/100ml)

3,32

2,9

-

Solidos total= es

PEE/CL/002

Método de referencia (AOAC 972.16)

(g/100ml)

12,59

11,2

-

Solidos no gr= asos

PEE/CL/002

Método de referencia (AOAC 972.16)

(g/100ml)

8,65

8,2

-

Punto crioscó= pico (°C)

PEE/CL/013

(g/100ml)

-0,5735

-0,536

-0,512

Agua ańadida<= o:p>

PEE/CL/013

%

0,00

-

-

Acidez <= /o:p>

PEE/CL/012

(g/100ml)

0,17

0,13

0,17

Grupo de antibióticos 1 ( -LACT-SULF-TETRA)

PEE/CL/010

Establecido e= n el CODEX CAC/MRL2

(pos/neg)

Negativo

Negativo

-

Cloruros=

PEE/CL/014

(pos/neg)

Negativo

Negativo

-

Neutralizante= s

PEE/CL/005

(pos/neg)

Negativo

Negativo

-

Peróxidos

PEE/CL/008

(pos/neg)

Negativo

Negativo

-

Nota: Laboratorio de Control de Calidad de Lec= he. Fuente: Agrocalidad (2017)

Se determina que dos parámetros se encuentran con valores críticos, = como la acidez con un valor de 0,17 (g/100ml) encontrándose en el límite máximo, esto es debido a la presencia de carga microbiana y punto crioscópico con un valor de -0,5735 (g/100ml), esta variación suele presentarse debido al aume= nto de la acidez, sin embargo, la leche puede ser procesada ya que para este ti= po de queso mozzarella.

Tabla 4

Análisis de la densidad relativa de leche cruda

Parámetros

Método de ensayo/Norma

Unidad

Resultado

Valor Limite permisible

Mínimo

Máximo

Densidad rela= tiva A 20 °C

Método del lactodensímetro/NTE INEN 11

-<= /span>

1,029

1,028

1,032

Nota: Laboratorio de Bromatología y Bioquímica de la Facultad de Ciencias. ESPOCH.

Fuente: Agrocalidad (2017)

De acuerdo con la tabla 3, se indica que la densidad relativa se encuentra dentro del límite establecido por la norma INEN 09. Leche cruda. Requisitos.

Tabla 5

Análisis de pH en leche cruda<= /p>

Parámetros

Método de ensayo/Norma

Unidad

Resultado

Valor Limite permisible

Mínimo

Máximo

pH=

Medición dire= cta utilizando el equipo Ekomilk.

-<= /span>

6,62

6,5

6,8

Nota: Laborato= rio de la Planta de Lácteos Tunshi-ESPOCH. Fuente: = Agrocalidad (2017)

Tabla 6

Análisis microbiológicos de la leche cruda

Parámetros

Método de ensayo/Norma

Unidad

Resultado

Límite máximo=

Recuento de células somáticas

PEE/CL/001

(x1000/ml)

276

7,0*10^5<=
/sup>

Contaje total= de bacterias

PEE/CL/003

(x1000/ml)

19136

-<= /span>

Nota: Laboratorio de control de calidad de leche. Fuente: Agrocalidad (2017)

La cantidad de células somáticas es mínima y está dentro del límite, mientras que el conta= je total de bacterias se encuentra con una cantidad crítica, esta alteración s= uele presentarse por falta de higiene durante el ordeńo y transporte, pero dicha anomalía se contrarresta en la etapa de pasteurización.

Ensayos a escala de laboratorio para la elaboración de queso mozzarella

El queso mozzarella es un queso de pasta hilada, blando, de color ligeramente blanco amarillento y de sabor suave. Obtenido de leche pasteurizada o cruda, mediante la adición de fermentos lácticos, al conseguir una adecuada acidez= de la cuajada y el proceso de hilado; es un ingrediente óptimo en la pizzería,= sánduches, ensaladas y platos calientes (Toro, 2011, p.30).

Requerimientos de materia prima e insumos, materiales y equipos

Una= vez determinado que la leche cumple con los parámetros establecidos por la norm= a, se procede a la elaboración de queso mozzarella, en este caso, se llevó a c= abo mediante fermentación enzimática por su buen rendimiento.

Tabla 7

Materia prima e Insumos

Materia prima

Insumos

Leche cruda

Cuajo líquido=

Fermento láct= ico TCC-20 (Streptococcus Thermophilus y Lactobacillus Helveticus<= /span>

Cloruro de ca= lcio

Cloruro de so= dio

Fuente: Agrocalidad (2= 017), elaborado por Guailla

Tabla 8

Materiales y equipos necesarios para la elaboración de queso mozzare= lla

Materiales

Equipos

Reactivos

Pipeta <= /o:p>

Espátula

Vidrio reloj =

Varilla de agitación

Malla

Moldes <= /o:p>

Lienzos<= /o:p>

Recipientes (jarras, baldes, ollas)

Cucharones

Cuchillo=

Vasos de precipitación de 250 y 500 ml

Fundas plásti= cas (específico para quesos)

Equipo de protección personal (guantes, mascarilla, botas, cofia)=

Tanque de recepción

Caldero =

Marmita =

Liras horizon= tal y vertical

Tanque de hil= ado y amasado

Mesa quesera =

Prensadora

Cocina indust= rial

pH-metro

Termómetro industrial

Balanza analí= tica

Selladora

Cámara de refrigeración

Agua destilada

Fuente: Agrocalidad (2= 017), elaborado por Guailla

Descripción del proceso a nivel de laboratorio

El proceso consiste en seguir una secuencia de pasos hasta la obtenc= ión del producto final, para ello es importante el control de las variables, co= mo temperatura, pH, tiempo de acidificación, etc. Previamente para empezar es necesario realizar la dosificación adecuada tanto de materia prima como de = los insumos requeridos, a continuación, en la tabla 8:

Tabla 9

Formulación de ensayos para la elaboración de queso mozzarella<= /o:p>

Materia prima e insumos

Dosis

Unidad

Leche

10

L

Fermento láctico TCC- 20

0,16

g

Cloruro de calcio

3

g

Cuajo líquido

1

ml

Fuente: Agrocalidad (2017), elaborado por<= span style=3D'font-size:10.0pt;line-height:200%;font-family:"Times New Roman",se= rif; mso-ansi-language:ES-EC'> Guailla

Resultados y Discusión<= /b>

Una vez obtenido el producto a escala de laboratorio de identifica las variable= s de operación del proceso.

Tabla 10

Variables y Parámetros = del proceso

Variables

Tipos de variables

Concepto

Método de medición

Etapa durante el proceso

Parámetro

Temperatura

Independiente=

Cantidad de calor o frío de los cuerpos.=

Termómetro

Pasteurización

65 °C

Enfriamiento

40 °C

Acidificación

40 °C

Hilado

65 °C

Salado

10-15 °C

Tiempo

Dependiente

Duración de las etapas del proceso.

Cronómetro

Pasteurización

30 min

Enfriamiento

5-10 min

Acidificación

2-3 horas

Salado

3 horas

pH

Dependiente

Nivel de acidez o basicidad de una soluc= ión acuosa.

Potenciómetro

Acidificación

5,2 – 5,4

Cantidad de fermento láctico, cloruro de calcio, cuajo y cloruro de sodio

Dependiente

Aditivos que brindan características pro= pias al queso mozzarella.

Balanza

Estandarización

Fermento láct= ico 1%

Cloruro de ca= lcio 21%

Cuajo 7%=

Cloruro de sodio 1%

Fuente: Agrocalidad (2017), elaborado por<= span style=3D'font-size:10.0pt;line-height:115%;font-family:"Times New Roman",se= rif; mso-ansi-language:ES-EC'> Guailla

Curva de acidificación

Permite determi= nar la variación del pH de la cuajada en función del tiempo, a fin de conseguir= un valor que varíe entre 5,2 - 5,4 ideal para el hilado (Antezana, 2015).

Figura 1

Curva de acidificación de queso mozzarella mediante fermentación enzimática<= span style=3D'font-size:12.0pt;line-height:115%;font-family:"Times New Roman",se= rif; mso-fareast-font-family:Calibri;mso-ansi-language:ES-EC;mso-fareast-languag= e: EN-US'>

Fuente: Agrocalidad (2017), elaborado por Guailla

Balance de materia y energía

El proceso de elaboración de queso mozzarella a nivel de laboratorio permitió tomar datos experimentales, a fin de realizar los cálculos de balance de masa y energía, que servirá como sustento para el diseńo respectivo a escala industrial (Oviedo & Rodríguez, 2013).

Balance de masa

El balance de m= asa en el proceso de elaboración de queso mozzarella permite determinar el rendimiento de cada una de las etapas, tomando como base la masa que entra y sale de la misma. El volumen de leche destinado para la elaboración de queso mozzarella es de 500 L.

=

Figura 2

Balance general de masa para = la elaboración de queso mozzarella<= /p>
Fuente: Agrocalidad (2017), elaborado por Guailla

Para determinar el rendimiento global del proceso de elaboración de queso mozzarella, se divide la cantidad de queso mozzarella y la cantidad de masa= de alimentación el mismo arroja un resultado del 11%

Balance de energíaEl balance de energía se establece según la primera ley de la termodinámica, el cual permite determi= nar las cantidades de energía que se intercambian y acumulan dentro del sistema, para realizar estos cálculos de consideran los mecanismos de transferencia = de calor (McCabe et al., 1998), y contemplando todos los equipos que contiene = el proceso se determinó que el balance global de transferencia para la Marmita= es 3,839 KJ/Kg °C, en la Caldera 0,16 KW/m²°C, y en el pasteurizador 0,22 KW/m²°C.

Resultados del dimensionamiento de equipos

Se consideran varias ecuaciones para realizar el dimensionamiento de los equipos (Geankoplis, 19= 98), arrojando los siguientes resultados:

Tabla 11

Dimensiones de la marmita

Descripción

Simbología

Valor

Unidad

Medidas de la marmita

Volumen de diseńo

<= !--[if gte msEquation 12]>VDM=

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,075

<= !--[if gte msEquation 12]>m3<= ![if !msEquation]>

Volumen total del tanque

<= !--[if gte msEquation 12]>VTM=

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,575

<= !--[if gte msEquation 12]>m3<= ![if !msEquation]>

Diámetro del tanque

<= !--[if gte msEquation 12]>Dt<= /m:oMath> <= /p>

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,90

<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'> <= /p>

Radio interno del tanque

<= !--[if gte msEquation 12]>ri<= ![if !msEquation]>

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,45

<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'>

Altura del tanque

<= !--[if gte msEquation 12]>h<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'>

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,90

<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'>

Diámetro de la chaqueta

<= !--[if gte msEquation 12]> <= /p>

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,09

<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'> <= /p>

Material Acero Inoxidable AISI

<= !--[if gte msEquation 12]>- <= /p>

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>304

<= !--[if gte msEquation 12]>- <= /p>

<= span style=3D'font-size:10.0pt;line-height:115%;mso-fareast-font-family:"Times= New Roman"; mso-fareast-theme-font:minor-fareast;mso-bidi-font-family:"Times New Roma= n"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>Sistema de agitació= n

Longitud de brazo del agitador

<= !--[if gte msEquation 12]>LB<= ![if !msEquation]> <= /p>

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,45

<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'> <= /p>

Espesor del agitador <= /p>

<= !--[if gte msEquation 12]>Ea<= /m:oMath> <= /p>

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,045

<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'> <= /p>

Diámetro del agitador =

<= !--[if gte msEquation 12]>∅a<= /m:oMath> <= /p>

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,675

<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'> <= /p>

Distancia entre el fondo del tanque y la paleta

<= !--[if gte msEquation 12]>E <= /p>

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,45

<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'> <= /p>

Altura de la paleta

<= !--[if gte msEquation 12]>Ap<= /m:oMath> <= /p>

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,09

<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'> <= /p>

Distancia entre rejillas

<= !--[if gte msEquation 12]> <= /p>

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,075

<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'> <= /p>

Numero de paletas

<= !--[if gte msEquation 12]>Np<= /m:oMath> <= /p>

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>6=

<= !--[if gte msEquation 12]>- <= /p>

Velocidad rotacional <= /p>

<= !--[if gte msEquation 12]>N <= /p>

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>1=

<= !--[if gte msEquation 12]>rps <= /p>

Potencia

<= !--[if gte msEquation 12]>P <= /p>

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>1=

<= !--[if gte msEquation 12]>Hp <= /p>

Fuente: Agrocalidad (2017), elaborado por<= span style=3D'font-size:10.0pt;line-height:200%;font-family:"Times New Roman",se= rif; mso-ansi-language:ES-EC'> Guailla

Tabla 12

Dimensiones de lira

Descripción

Simbología

Valor

Unidad

L= ongitud del brazo de lira

<= !--[if gte msEquation 12]>LBL= <= /p>

<= span style=3D'mso-bidi-font-family:"Times New Roman";mso-fareast-language:ES-E= C; mso-bidi-font-weight:bold'>0,65

<= !--[if gte msEquation 12]>m <= /p>

E= spesor de lira

<= !--[if gte msEquation 12]>EL<= /m:oMath> <= /p>

<= span style=3D'mso-bidi-font-family:"Times New Roman";mso-fareast-language:ES-E= C; mso-bidi-font-weight:bold'>0,065

<= !--[if gte msEquation 12]>m <= /p>

L= ongitud de lira

<= !--[if gte msEquation 12]>LL<= /m:oMath> <= /p>

<= span style=3D'mso-bidi-font-family:"Times New Roman";mso-fareast-language:ES-E= C; mso-bidi-font-weight:bold'>0,30

<= !--[if gte msEquation 12]>m <= /p>

A= lto de la paleta de lira

<= !--[if gte msEquation 12]>ApL= <= /p>

<= span style=3D'mso-bidi-font-family:"Times New Roman";mso-fareast-language:ES-E= C; mso-bidi-font-weight:bold'>0,13

<= !--[if gte msEquation 12]>m <= /p>

A= ltura total de lira

<= !--[if gte msEquation 12]>ATL= <= /p>

<= span style=3D'mso-bidi-font-family:"Times New Roman";mso-fareast-language:ES-E= C; mso-bidi-font-weight:bold'>0,78

<= !--[if gte msEquation 12]>m <= /p>

D= istancia entre el fondo del tanque y la lira

<= !--[if gte msEquation 12]>x<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'>

<= span style=3D'mso-bidi-font-family:"Times New Roman";mso-fareast-language:ES-E= C; mso-bidi-font-weight:bold'>0,12

<= !--[if gte msEquation 12]>m

D= istancia entre hilo e hilo

<= !--[if gte msEquation 12]>xV<= ![if !msEquation]>

<= span style=3D'mso-bidi-font-family:"Times New Roman";mso-fareast-language:ES-E= C; mso-bidi-font-weight:bold'>0,03

<= !--[if gte msEquation 12]>m

Fuente: Agrocalidad (2017), elaborado por<= span style=3D'font-size:10.0pt;line-height:115%;font-family:"Times New Roman",se= rif; mso-ansi-language:ES-EC'> Guailla

Tabla 13

Dimensiones del tanque de hil= ado

Descripción=

Simbología<= /span>

Valor

Unidad

Volumen de diseńo de hiladora

0,0225

Volumen total de hiladora

0,1725

Diámetro interno del tanque

0,60

Radio del tanque de hiladora

0,30

Altura del tanque de hiladora

0,60

Fuente: Agrocalidad (2017), elaborado por<= span style=3D'font-size:10.0pt;line-height:200%;font-family:"Times New Roman",se= rif; mso-ansi-language:ES-EC'> Guailla

Tabla 14

Dimensiones de mesa de moldeo<= /i>

Descripción

Simbología

Valor

Unidad

Longitud de mesa

<= !--[if gte msEquation 12]>Lm<= ![if !msEquation]>

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>1,50

<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'>

Ancho de mesa

<= !--[if gte msEquation 12]>am<= ![if !msEquation]>

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,75

<= !--[if gte msEquation 12]>m

Altura de mesa

<= !--[if gte msEquation 12]>Am<= ![if !msEquation]>

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,80

<= !--[if gte msEquation 12]>m

Volumen de mesa

<= !--[if gte msEquation 12]>Vm<= ![if !msEquation]>

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,90

<= !--[if gte msEquation 12]>m3<= ![if !msEquation]>

Fuente: Agrocalidad (2017), elaborado por Guailla
= El proceso de producción de elaboración de q= ueso mozzarella propuesto para la microempresa “SIERRALAC” es considerado como un tipo de producción batch, puesto que la leche solo se recepta una vez al dí= a y por ser una nueva línea de producción para la planta.

Materia prima, aditivos e insumos=

Para la elaboración de queso mozzarella a nivel industrial es necesario el requerimiento de los siguient= es aditivos, materia prima e insumos para procesar 500 litros de leche diarios= .

Tabla= 15

Mater= ia prima, aditivos e insumos

Materia prima

Leche cruda=

Cantidad

Unidad

Aditivos

Cloruro de calcio=

150<= /p>

g

Fermento lácticoTCC-20 (bacterias thermophilus)

8

g

Cuajo líquido

50

mL

Cloruro de sodio<= /o:p>

23%<= /p>

-

Insumos

Fundas plásticas<= /o:p>

110<= /p>

Unidades

Fuente: Agrocalidad (2017), elaborado por Guailla

Figura 3

                        Diagrama del proc= eso de elaboración de queso mozzarella

Fuente: Agrocalidad (2017), elaborado por Guailla

Descripción del diagrama del proceso de elaboración de queso mozzarella

·&nb= sp;        Recepción de materia prima

La leche cruda es receptada en un tanque de acero inoxidable, el cual presenta un filtro (lienzo) a fin de que queden retenid= as las impurezas y partículas adheridas a la leche.

·&nb= sp;        Control de calidad

Mediante pruebas de calidad permite determinar si = la leche cumple con los estándares de calidad y si es apta para ser procesada, garantizando la inocuidad de la leche y posteriormente del producto final.<= o:p>

·&nb= sp;        Pasteurización

Etapa que mediante la adición de calor permite destruir los microorganismos patógenos y perjudiciales presentes en la lech= e, así, asegurando la higiene durante el proceso. Para efectuar dicha etapa, la leche sufre un tratamiento lento a una temperatura de 65 °C durante un tiem= po de 30 minutos, dicha temperatura es considerada adecuada ya que se mantiene= las propiedades nutricionales del producto sin modificación alguna.<= /span>

·&nb= sp;        Enfriamiento

La leche pasteurizada es enfriada, mediante la ayu= da de una corriente de agua fría hasta conseguir una temperatura que oscila en= tre 38-40 °C

·&nb= sp;        Inoculación

Consiste en adicionar la cantidad exacta de fermen= to láctico TCC-20 que es un medio de cultivo de bacterias streptococcus thermophilus, específico para queso mozzarella. La temperatura óptima de esta etapa es de 38-40 °C, puesto que es la adecuada = para que las bacterias se desarrollen de una manera adecuada. Para mantener una mezcla homogénea se empleará el agitador respectivo.

·&nb= sp;        Adición de cloruro de calcio

Para que la cuajada adquiera mayor firmeza mecánic= a se agrega cloruro de calcio, debido que durante la pasteurización se efectúa un proceso normal de precipitación de calcio.

·&nb= sp;        Coagulación

Proceso en el que se produce la formación de un ge= l por la acción del cuajo, dado que tiene la capacidad de coagular las proteínas = que se encuentran en la leche. Para que se forme la cuajada debe permanecer en reposo durante 40 minutos.

·&nb= sp;        Primer corte y agitación

El objetivo del corte es convertir la masa de cuaj= ada formada en fragmentos pequeńos, permitiendo así la eliminación del suero, el tamańo de los granos incide en el tipo de queso que se desea elaborar. Para ello se utilizan liras horizontal y vertical para obtener trozos de 3-4 cm aproximadamente, después se debe realizar un batido lento sin romper los tr= ozos de cuajada durante 10 minutos con el fin de conseguir que los granos de cua= jada estén consistentes.

·&nb= sp;        Desuerado parcial

Consiste en eliminar las 2/3 partes del suero, par= a el cual se usan mallas para evitar eliminar granos de cuajada.

·&nb= sp;        Acidificación

Proceso en el que los granos de la cuajada alcanza= n un pH óptimo para la etapa de hilado, para ello la temperatura debe mantenerse= de 38-40 °C durante un tiempo de 2-3 horas, tiempo necesario para que el pH alcance un valor de 5,2 a 5,4. Para llevar un control de pH adecuado es necesario la ayuda de un potenciómetro, en el que el pH se mide cada 15 min= utos hasta lograr llegar a dichos valores.

Previamente al hilado se realiza la prueba de hila= do, se verifica colocando un pequeńo trozo de cuajada en agua caliente (60-65 °= C) y observar que se estire, una vez comprobado será ideal para la siguiente eta= pa; caso que se puede aplicar al no disponer de un equipo Potenciométrico.

·&nb= sp;        Desuerado total y corte

Con la ayuda de mallas el suero se elimina por completo. Una vez eliminado el suero por completo se procede a cortar la ma= sa de cuajada en fragmentos de 8-10 cm aproximados.

·&nb= sp;        Hilado y amasado

Proceso térmico que consiste en someter los trozos= de cuajada en agua o suero caliente (60-65 °C) durante 2 min y luego se estira= e introduce en agua caliente hasta el moldeo con el objeto de que adquiera brillo, plasticidad y capacidad de formar hebras.

·&nb= sp;        Moldeado y Prensado

La masa hilada se debe colocar en moldes y mediant= e la ayuda de una prensa mecánica logrando adquirir un producto con mayor compactación y firmeza.

·&nb= sp;        Enfriado

El queso debe ser enfriado a temperatura de 5-10 °C durante 15-25 minutos, debido que si entra directamente produce un queso deformado, salmuera caliente y mayor concentración de sal en el queso, sali= da de agua y grasa del queso para la salmuera y la salmuera está más expuesta = al deterioro.

·&nb= sp;        Salazón

Para que el queso adquiera el sabor característico= se sumerge en salmuera a una concentración del 23% durante 6-8 horas.

·&nb= sp;        Empacado

Colocar los quesos en fundas plásticas para que posteriormente sean comercializados.

·&nb= sp;        Almacenado

Para conservar y prolongar el tiempo de vida el producto final se somete a un cuarto o cámaras de refrigeración (4°C).=

Figura 4

Queso mozzarella

Fuente: Agrocalidad (2017), elaborado por<= span style=3D'font-size:10.0pt;line-height:115%;font-family:"Times New Roman",se= rif; mso-ansi-language:ES-EC'> Guailla
Una v= ez elaborado el producto y a fin de validar el diseńo se realizó la caracterización del queso mozzarella establecido por la norma NTE INEN 0082:2011. Queso mozzarella. Requisitos.

Tabla 16

Análisis físico de queso mozzarella

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-bidi-font-weight:bold'>Parámetro

<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-bidi-font-weight:bold'>Características

Color

Blanco

Olor

Característico

Aspecto

Normal, libre de material extrańo

Fuente: Agrocalidad (2017), elaborado por<= span style=3D'font-size:10.0pt;line-height:115%;font-family:"Times New Roman",se= rif; mso-ansi-language:ES-EC'> Guailla

Tabla 17

Análisis bromatológico de queso mozzarella<= /o:p>

Parámetro =

Mé= todo

Re= sultado

Un= idad

Li= mite permisible

Mí= n.

Má= x.

Humedad

NTE INEN 63

39= ,21

%<= o:p>

-<= o:p>

60=

Grasa

NTE INEN 64

46= ,32

%<= o:p>

45=

-<= o:p>

Nota= : Laboratorio de Servicios Analíticos, Químicos y Microbiológicos en Aguas.

Tabla 18

Análisis microbiológico de queso mozzarella=

Parámetros<= /span>

Método

Resultado

Escherichia Coli UFC/g

Siembra en masa

Ausencia

Stafilococus Aureus UFC/g

Siembra en masa

Ausencia

Enterobacteraceas UFC/g

Siembra en masa

40

Salmonella en 25 g

Reveal 2.0 NEOGEN

Ausencia

Listeria en 25 g

Reveal 2.0 NEOGEN

Ausencia

Nota: La= boratorio de Servicios Analíticos, Químicos y Microbiológicos en Aguas

Conforme a los resultados conseguidos de los análisis, el queso mozzarella elaborado= a escala piloto cumple con los requisitos establecidos por la norma NTE INEN 0082: 2011.Queso Mozzarella. Requisitos, de manera que el diseńo para esta nueva línea de producción en la microempresa es factible para su implementación.

Tabla 19

Equipos requeridos para la producción de queso mozzarella

Equipo

Descripción

Características

Marmita

Material de acero inoxidable 304, posee una cami= sa o chaqueta por donde circulará el vapor para llevar a cabo la pasteurizació= n, además contendrá un agitador tipo rejilla de paletas planas inclinadas con ángulo de inclinación de 45 °C permitiendo que la transferencia de calor = se dé por todo el fluido logrando así que la mezcla sea homogénea, 1 válvula= de salida y bridas para fijar el equipo en el piso.

Volumen =3D 575 L

Altura =3D 0,90 m

Diámetro =3D 0,90 m

Área =3D 3,43 =

Espesor del agitador =3D 0,044 m

Diámetro del agitador =3D 0,66 m

Altura de las paletas =3D 0,09 m

Potencia del motor =3D 1 Hp

Tabla 19

Equipos requeridos para la producción de queso mozzarella (continuación)

Eq= uipo

De= scripción

Ca= racterísticas

Lira vertical

Material de acero inoxidable 304, en el que el número de hilos depende del tipo de queso a elaborar y por lo tanto el co= rte es diferente.

Longitud del brazo de la lira =3D0,65 m

Espesor de la lira =3D 0,065 m

Alto de la paleta de la lira =3D 0,13 m

Altura total de la lira =3D 0,78 m<= /span>

Tanque de hilado

Material acero inoxidable 304.

Forma cilíndrica.

Volumen total del tanque =3D 172.5 L.

Diámetro interno del tanque =3D 0,60 m.

Radio del tanque =3D 0,30 m.=

Altura del tanque =3D 0, 60 m.

Área =3D 1

Mesa de moldeo

Material de acero inoxidable 304, específicame= nte dimensionado para el moldeo.

Longitud =3D 1,50 m

Ancho =3D 0,75 m

Altura =3D 0,80 m

Volumen =3D 0,90 m

Fuente: Agrocalidad (2017), elaborado por Guailla
De un volumen de 500 L de producción se obti= ene 55 kg de queso mozzarella, para que el producto salga al mercado se propuso= una presentación de 500 gramos, mismos que son empacados en fundas de plástico respectivo.

El estudio financiero del presente proyecto permite determinar la viabilidad de este, en el que los costos de los equipos, materiales, materia prima, aditi= vos se han considerado los costos del mercado.

Conforme a los resultados del estudio financiero se obtiene que los indicadores financieros más importantes son el TIR (Tasa Interna de Retorno con un valo= r de $ 5866,20 y el VAN (Valor Actual N= eto) con el 87%, el proyecto es económicamente viable debido a que el TIR es mayor que la tasa de rendimien= to del mercado, el proyecto es aceptable puesto que el VAN es mayor que cero y= la relación costo beneficio será de $ 1,09 por cada dólar que se invierte y el período de recuperación de lo invertido será de 0,96 ańos.

Conclusiones

·      =    La caracterización de la leche cruda se realizó mediante análisis fisicoquímico y microbiológico en base a la NTE INEN 0009: Leche cruda. Requisitos, donde se determinó que los parámetros más importan= tes para este proceso fueron densidad 1,029 (ug/l) y acidez 0,17 (g/100ml).

·      =    Mediante pruebas realizadas a escala piloto se obt= uvo queso mozzarella con un rendimiento del 11 %, durante el proceso se identif= icó las variables más relevantes siendo estas las siguientes: temperatura de pasteurización a 65 °C, tiempo de acidificación de 2-3 horas, temperatura p= ara la acidificación de 40 °C, pH de hilado que varía entre 5,2-5,4, la tempera= tura de hilado de 65 °C y tiempo de salado de 4-6 horas.

·      =    En base a los datos obtenidos a nivel de laborator= io se realizó el diseńo de ingeniería para procesar 500 litros de leche, en ba= se a cálculos técnicos, dimensionamiento, tipo de material y presupuesto se dise= ńó los siguientes equipos: marmita, sistema de agitación, lira vertical, tanqu= e de hilado y mesa de moldeo para la obtención de queso mozzarella a escala industrial, además el material de los equipos es de acero inoxidable AISI 3= 04 por tratarse de un alimento.

·&nb= sp;        Por medio de la caracterización del queso mozzarel= la se validó el diseńo obteniendo los siguientes valores: humedad 39% y grasa (falta) y mediante el análisis microbiológico el producto presenta ausencia= de escherichia coli, stafilococus aureus, salmonella, listeria y enterobactera= ceas con 40 UFC/g, está dentro de rango.

Referencias Bibliográficas

Agrocalidad. (2017). Instructivo para toma de muestras de l= eche cruda. http://www.agrocalidad.gob.ec/wp-content/uploads/2015/09/intructivo-para-to= ma-de-muestras-de-leche-cruda-19-01-2017.pdf.

Alais, C. (1985). Ciencia de la leche: Principios de téc= nica lechera. [ed.] Manuel Company. Barcelona-Espańa: Reverté, S. A., 4-5.

Antezana Vázquez C. (2015)= . Efecto de la hidrólisis enzimática de = la lactosa en el perfil de textura de queso fresco normal y bajo en grasa.= [Tesis de grado, Universidad Nacional Agraria La Molina Perú] Archivo digital.           http://repositorio.lamolina.ed= u.pe/bitstream/handle/UNALM/1789/Q04_A558_T%20BAN%20UNALM.pdf?sequence=3D1&= amp;isAllowed=3Dy.

Cuichan R, (2006). Diseńo de un plan de análisis de pelig= ros y puntos críticos para el control para queso mozzarella en la empresa la hola= ndesa. http= ://dspace.espoch.edu.ec/bitstream/123456789/885/1/27T075.pdf

Geankoplis Christie, J. (1998). Procesos de Transporte y Operaciones Unitarias. (3.^a ed.). https://fenomenosdetransporte.files.wordpress.com/2008/05/geankopolis= .pdf

McCabe, Warren, L., Smith, Julian C., & Harriott, P. (1998). Operaciones Unitarias en Ingeniería Química. (7.^a ed.). Editorial McGraw-Hill. http://librodigital.sangregorio.edu.ec/librosu= sgp/14698.pdf

Servicio Ecuatoriano de Normalización [INEN]. (1984). Norma Técnica Ecuatoriana 4, Leche y productos lácteos. Muestreo. Requisitos. https://www.no= rmalizacion.gob.ec/buzon/normas/4-1.pdf.

Servicio Ecuatoriano de Normalización [INEN]. (2012). Norma Técnica Ecuatoriana 9, Leche cruda. Requisitos. https://ia601905.us.archive.org/26/items/ec.nte.0009.2008/e= c.nte.0009.2008.pdf.

Servicio Ecuatoriano de Normalización [INEN]. (2011). Norma Técnica Ecuatoriana 82, Queso Mozzar= ella. Requisitos. https://www.normalizacion.gob.ec/buzon/normas/82.pdf.

Oviedo Carrillo, M. & = Rodríguez Mejía, V. (2013). Diseńo y construc= ción de un sistema para la producción de queso ricota a partir lacto suero de la Planta de Lácteos ESPOCH. [Tesis de grado, Escuela Superior Politécnica= de Chimborazo] http://dspace.espoch.edu.ec/handle/123456789/3202

Quinzo, O. (2015). Diseńo e implementación de un manual de buenas prácticas de manufactura bpm, para la empresa láctea alpen swiss s.a= . http://dspace.espoch.edu.ec/bitstream/12= 3456789/6080/1/27T0316.pdf.

Revilla, A. (1985). Tecnología de la leche. México: He= rrero Hermanos, Alais, C. (pp. 11). https://r= edi.uta.edu.ec/bitstream/123456789/3963/1/P.AL237.pdf

Ruíz, G. (2017). Evaluación de queso mozzarella elabora= do con leche de tres especies zootécnicas. http://dspace.espoch.edu.ec/bitstream/123456789/7087/1/17T1460.pdf.

Sémper, B. (2016). “Diseńo y construcción de un prototipo= de amasadora e hiladora semi automática para queso mozzarella en la empresa riolac". http://dspace.espoch.edu.ec/bitstream/123456789/5793/1/27T0306.pdf.

Toro, P. (2011). Elabor= ación de queso mozzarella (utilizando leche de bovino) a partir de cuatro tipos de leche acidulada con un cultivo termófilo (streptococcus thermophilus), ácid= o cítrico, ácido láctico y suero ácido, utilizando 2 tipos de coagulación. [Tesis = de grado, Universidad Técnica de Cotopaxi] http://repositorio.utc.edu.ec/handl= e/27000/863.

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

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;

=

&nb= sp;

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= ISSN: 2773-7330

= Vol. 4 No. 2.2. pp. 146 – 169. junio 2022

www= .alfapublicaciones.com

= =

Indagación Página 146 | 1

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= ¹	Danielita Fernanda Borja Mayorga<= /o:p>	https://orcid.org/000= 0-0002-8438-064X
=	Escuela Superior Politécnica del Chimborazo (ESPOCH), Faculty of Chemical Engineering, Riobamba, Ecuador dborja@espoch.edu.ec <= /span>
= ²	Marco Raul Chuiza Rojas	https://orcid.org/000= 0-0003-1908-8033
	Escuela Superior Politécnica del Chimborazo (ESPOCH), Faculty of Chemical Engineering, Riobamba, Ecuador <= /span> m.c= huiza@espoch.edu.ec
= ³	Mónica Lilian Andrade Avalos	https://orcid.org/000= 0-0001-5736-5607
	Escuela Superior Politécnica del Chimborazo (ESPOCH), Faculty of Chemical Engineering, Riobamba, Ecuador moandrade@espoch.edu.ec=

&nb= sp;	Artículo de Investigación Científica y Tecnológica Enviado: 08/0= 4/2022 Revisado: 22/= 05/2022 Aceptado: 27/= 05/2022 Publicado:24/= 06/2022 DOI: https://doi.org/10.33262/= ap.v4i2.2.228
&nb= sp;
Cítese:		Borja Mayorga, D. F., Chuiza Rojas, M. R., & Andrade Avalos , M. L. (2022). Obtención de qu= eso mozzarella, mediante el diseńo de un proceso industrial, en la provincia = de Chimborazo, cantón Colta. AlfaPublicaciones, 4(2.2), 146–169. https://doi.org/10.33262/= ap.v4i2.2.228
		*ALFA PUBLICACIONES,* e<= span style=3D'font-size:8.0pt;line-height:115%;font-family:"Times New Roman",s= erif; mso-fareast-font-family:Calibri;mso-ansi-language:ES-EC;mso-fareast-langu= age: EN-US'>s una revista multidisciplinar, trimestral, que se publicar= á en soporte electrónico tiene como misión contribuir a la formación de profesionales competentes con visión humanística y crítica q= ue sean capaces de exponer sus resultados investigativos y científicos en la misma medida que se promueva mediante su intervención cambios positivos e= n 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 Afiliaci= ón 663) www.celibro.org.ec
		Esta revista = está protegida bajo una licencia Creative Commons Attribution Non Commercial No Derivatives 4.0 International. Copia de la licencia: http://creativecommons.org/licenses/by-nc-nd/4.0/
Palabras clav= es: leche, queso mozzarella, diseńo, proceso, industria láctea.		Resumen Introducción. La industrialización de un proceso permite obtener un producto en menor tiempo y se asegura la calidad de este con lo establecido en la norma NTE INEN 82: Queso mozzarella. Requisitos. Objetivo. Diseńar un proceso industrial para la obtención de queso mozzarella en la planta procesadora “SIERRALAC” perteneciente a la Corporación de Organizaciones Campesinas e Indígenas de las Huaconas y Culluctus (COCIH), en la Provincia de Chimborazo, Cantón Colta. Metodología. <= span style=3D'mso-bidi-font-style:italic'>Se inició con la caracterización de la materia prima, mediante análisis fisicoquímicos y microbiológicos basados en la NTE INEN 0009: 2012. Leche cruda. Requisito= s. NTE INEN 9:2012. Además, se realizó pruebas para identificar las variable= s de operación para la elaboración de queso mozzarella a nivel de laboratorio arrojando los siguientes resultados: temperatura de pasteurización a 65 °C durante 30 minutos, temperatura de enfriamiento a 40 °C, tiempo de acidificación de 2-3 horas, pH ideal entre 5,2-5,4 para la etapa de hilad= o, temperatura de hilado a 65 °C y tiempo de salado de 3 horas. Para cumplir= con los requerimientos de la microempresa se empleó el método de fermentación enzimática debido a su alto rendimiento y calidad del producto. Resulta= dos. En b= ase a los valores de las variables de operación se realiza el diseńo de los equ= ipos a escala industrial, cuyos equipos son: una marmita con un sistema de agitación, un tanque de hilado, una lira y una mesa de moldeo para una capacidad de procesamiento de 500 litros de leche. Conclusión. La validación del diseńo de ingeniería se efectuó mediante la caracterización físico, bromatológico, y microbiológico de queso mozzarel= la de acuerdo con la norma NTE INEN 82: Queso mozzarella. Requisitos, cuyos resultados cumplen con los parámetros de calidad siendo apto para su cons= umo. Mediante un estudio de análisis financiero se verificó que el proyecto es viable, para garantizar la inocuidad del producto se recomienda aplicar b= uenas prácticas de manufactura.
Keywords: milk, mozzar= ella cheese, design, process, dairy industry.		Abstrac= t Introduction. The industrialization of a process allows a pro= duct to be obtained in less time and its quality is ensured with the provision= s of the NTE INEN 82 standard: Mozzarella cheese. Requirements. Objectives. Design an industrial process to obtain mozzarella cheese in the "SIERRALAC" processi= ng plant belonging to the Corporation of Peasant and Indigenous Organization= s of Huaconas and Culluctus (COCIH), in the Province of Chimborazo, city Colta= . Methodology. It began with the characterization of the raw material, through physical-chemical and microbiological analyzes based on the NTE INEN 0009: 2012. Raw milk. Requirements. NTE INEN 9:2012. In addition, tests were carried out to identify the operating variables for the production of mozzarella cheese = at the laboratory level, yielding the following results: pasteurization temperature at 65 °C for 30 minutes, cooling temperature at 40 °C, acidif= ication time of 2- 3 hours, ideal pH between 5.2-5.4 for the spinning stage, spin= ning temperature at 65 °C and salting time of 3 hours. To meet the requirement= s of the microenterprise, the enzymatic fermentation method was used due to its high yield and product quality. = Results. Based on the values of the operating variables, the design = of the equipment is conducted on an industrial scale, whose equipment is: a = pot with a stirring system, a spinning tank, a lyre, and a molding table for a processing capacity of 500 liters of milk. Conclusion. The validation of the engineering design was conducted through the physical, bromatological, and microbiological characterization of mozzarella cheese according to the NTE INEN 82 standa= rd: Mozzarella cheese. Requirements, whose results meet the quality parameters being suitable for consumption. Through a financial analysis study, it was verified that the project is viable, to guarantee the safety of the produ= ct, it is recommended to apply good manufacturing practices.

Especie	% Agua	% Grasa	% Proteína
Vaca	87	3.8	3.35
Humana (mujer)	87	3.8	2.30
Cabra	86	4.8	4.30
Oveja	83	5.3	6.30
Yegua	90	0.6	2.10
Burra	91	1.2	1.50
Búfala	82	8.0	4.0
Coneja	70	10.5	15.5
Llama	86	3.2	3.9

Parámetros	Rango	Precisión	Unidad
Grasa	0,5 - 12=	0,1	%<= /span>
Solidos no grasos	6 - 12	0,2 %	%<= /span>
Densidad	1,0260 – 1,03= 30	0,00005<= /o:p>
Proteína	2 - 6	0,2<= /span>	%<= /span>
Temperatura	0 - 50	0,1<= /span>
Lactosa	0,5 – 7<= /o:p>	0,2<= /span>	%<= /span>
Conductividad	2 - 20	1 %<= /span>	<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; position:relative;top:4.0pt;mso-text-raise:-4.0pt;mso-ansi-language:ES; mso-fareast-language:ES;mso-bidi-language:AR-SA'> (18°= C)
pH	0,00 - 14	0,02=	-<= /span>

Parámetros	Método de ensayo/Norma=	Unidad	Resultado	Valor Limite permisible
Mínimo	Máximo
Grasa	PEE/CL/002 Método de referencia (AOAC 972.16)	(g/100ml)	3,95	3,0	-
Proteína	PEE/CL002 Método de referencia (AOAC 972.16)	(g/100ml)	3,32	2,9	-
Solidos total= es	PEE/CL/002 Método de referencia (AOAC 972.16)	(g/100ml)	12,59	11,2	-
Solidos no gr= asos	PEE/CL/002 Método de referencia (AOAC 972.16)	(g/100ml)	8,65	8,2	-
Punto crioscó= pico (°C)	PEE/CL/013	(g/100ml)	-0,5735	-0,536	-0,512
Agua ańadida<= o:p>	PEE/CL/013	%	0,00	-	-
Acidez <= /o:p>	PEE/CL/012	(g/100ml)	0,17	0,13	0,17
Grupo de antibióticos 1 ( -LACT-SULF-TETRA)	PEE/CL/010 Establecido e= n el CODEX CAC/MRL2	(pos/neg)	Negativo	Negativo	-
Cloruros=	PEE/CL/014	(pos/neg)	Negativo	Negativo	-
Neutralizante= s	PEE/CL/005	(pos/neg)	Negativo	Negativo	-
Peróxidos	PEE/CL/008	(pos/neg)	Negativo	Negativo	-

Parámetros	Método de ensayo/Norma	Unidad	Resultado	Valor Limite permisible
Mínimo	Máximo
Densidad rela= tiva A 20 °C	Método del lactodensímetro/NTE INEN 11	-<= /span>	1,029	1,028	1,032

Materia prima e insumos	Dosis	Unidad
Leche	10	L
Fermento láctico TCC- 20	0,16	g
Cloruro de calcio	3	g
Cuajo líquido	1	ml

Variables	Tipos de variables	Concepto	Método de medición	Etapa durante el proceso	Parámetro
Temperatura	Independiente=	Cantidad de calor o frío de los cuerpos.=	Termómetro	Pasteurización	65 °C
Enfriamiento	40 °C
Acidificación	40 °C
Hilado	65 °C
Salado	10-15 °C
Tiempo	Dependiente	Duración de las etapas del proceso.	Cronómetro	Pasteurización	30 min
Enfriamiento	5-10 min
Acidificación	2-3 horas
Salado	3 horas
pH	Dependiente	Nivel de acidez o basicidad de una soluc= ión acuosa.	Potenciómetro	Acidificación	5,2 – 5,4
Cantidad de fermento láctico, cloruro de calcio, cuajo y cloruro de sodio	Dependiente	Aditivos que brindan características pro= pias al queso mozzarella.	Balanza	Estandarización	Fermento láct= ico 1% Cloruro de ca= lcio 21% Cuajo 7%= Cloruro de sodio 1%

Descripción	Simbología	Valor	Unidad
Medidas de la marmita
Volumen de diseńo	<= !--[if gte msEquation 12]>VDM=	<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,075	<= !--[if gte msEquation 12]>m3<= ![if !msEquation]>
Volumen total del tanque	<= !--[if gte msEquation 12]>VTM=	<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,575	<= !--[if gte msEquation 12]>m3<= ![if !msEquation]>
Diámetro del tanque	<= !--[if gte msEquation 12]>Dt<= /m:oMath> <= /p>	<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,90	<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'> <= /p>
Radio interno del tanque	<= !--[if gte msEquation 12]>ri<= ![if !msEquation]>	<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,45	<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'>
Altura del tanque	<= !--[if gte msEquation 12]>h<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'>	<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,90	<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'>
Diámetro de la chaqueta	<= !--[if gte msEquation 12]> <= /p>	<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,09	<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'> <= /p>
Material Acero Inoxidable AISI	<= !--[if gte msEquation 12]>- <= /p>	<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>304	<= !--[if gte msEquation 12]>- <= /p>
<= span style=3D'font-size:10.0pt;line-height:115%;mso-fareast-font-family:"Times= New Roman"; mso-fareast-theme-font:minor-fareast;mso-bidi-font-family:"Times New Roma= n"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>Sistema de agitació= n
Longitud de brazo del agitador	<= !--[if gte msEquation 12]>LB<= ![if !msEquation]> <= /p>	<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,45	<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'> <= /p>
Espesor del agitador <= /p>	<= !--[if gte msEquation 12]>Ea<= /m:oMath> <= /p>	<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,045	<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'> <= /p>
Diámetro del agitador =	<= !--[if gte msEquation 12]>∅a<= /m:oMath> <= /p>	<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,675	<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'> <= /p>
Distancia entre el fondo del tanque y la paleta	<= !--[if gte msEquation 12]>E <= /p>	<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,45	<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'> <= /p>
Altura de la paleta	<= !--[if gte msEquation 12]>Ap<= /m:oMath> <= /p>	<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,09	<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'> <= /p>
Distancia entre rejillas	<= !--[if gte msEquation 12]> <= /p>	<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>0,075	<= !--[if gte msEquation 12]>m<= span lang=3DES style=3D'font-size:11.0pt;line-height:115%;font-family:"Calibri= ",sans-serif; mso-ascii-theme-font:minor-latin;mso-fareast-font-family:"Times New Roman= "; mso-fareast-theme-font:minor-fareast;mso-hansi-theme-font:minor-latin; mso-bidi-font-family:"Times New Roman";mso-bidi-theme-font:minor-bidi; mso-ansi-language:ES;mso-fareast-language:ES;mso-bidi-language:AR-SA'> <= /p>
Numero de paletas	<= !--[if gte msEquation 12]>Np<= /m:oMath> <= /p>	<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>6=	<= !--[if gte msEquation 12]>- <= /p>
Velocidad rotacional <= /p>	<= !--[if gte msEquation 12]>N <= /p>	<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>1=	<= !--[if gte msEquation 12]>rps <= /p>
Potencia	<= !--[if gte msEquation 12]>P <= /p>	<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-fareast-language:ES-EC;mso-bidi-font-weight:bold'>1=	<= !--[if gte msEquation 12]>Hp <= /p>

Descripción=	Simbología<= /span>	Valor	Unidad
Volumen de diseńo de hiladora		0,0225
Volumen total de hiladora		0,1725
Diámetro interno del tanque		0,60
Radio del tanque de hiladora		0,30
Altura del tanque de hiladora		0,60

Materia prima	Leche cruda=	Cantidad	Unidad
Aditivos	Cloruro de calcio=	150<= /p>	g
Fermento lácticoTCC-20 (bacterias thermophilus)	8	g
Cuajo líquido	50	mL
Cloruro de sodio<= /o:p>	23%<= /p>	-
Insumos	Fundas plásticas<= /o:p>	110<= /p>	Unidades

	<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-bidi-font-weight:bold'>Parámetro	<= span style=3D'font-size:10.0pt;line-height:115%;mso-bidi-font-family:"Times Ne= w Roman"; mso-bidi-font-weight:bold'>Características
Color	Blanco
Olor	Característico
Aspecto	Normal, libre de material extrańo

Parámetro =	Mé= todo	Re= sultado	Un= idad	Li= mite permisible
Mí= n.	Má= x.
Humedad	NTE INEN 63	39= ,21	%<= o:p>	-<= o:p>	60=
Grasa	NTE INEN 64	46= ,32	%<= o:p>	45=	-<= o:p>

Parámetros<= /span>	Método	Resultado
Escherichia Coli UFC/g	Siembra en masa	Ausencia
Stafilococus Aureus UFC/g	Siembra en masa	Ausencia
Enterobacteraceas UFC/g	Siembra en masa	40
Salmonella en 25 g	Reveal 2.0 NEOGEN	Ausencia
Listeria en 25 g	Reveal 2.0 NEOGEN	Ausencia

Eq= uipo	De= scripción	Ca= racterísticas
Lira vertical	Material de acero inoxidable 304, en el que el número de hilos depende del tipo de queso a elaborar y por lo tanto el co= rte es diferente.	Longitud del brazo de la lira =3D0,65 m Espesor de la lira =3D 0,065 m Alto de la paleta de la lira =3D 0,13 m Altura total de la lira =3D 0,78 m<= /span>
Tanque de hilado	Material acero inoxidable 304. Forma cilíndrica.	Volumen total del tanque =3D 172.5 L. Diámetro interno del tanque =3D 0,60 m. Radio del tanque =3D 0,30 m.= Altura del tanque =3D 0, 60 m. Área =3D 1
Mesa de moldeo	Material de acero inoxidable 304, específicame= nte dimensionado para el moldeo.	Longitud =3D 1,50 m Ancho =3D 0,75 m Altura =3D 0,80 m Volumen =3D 0,90 m