WO2019238993A1 - Milk standardisation device - Google Patents

Milk standardisation device Download PDF

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Publication number
WO2019238993A1
WO2019238993A1 PCT/ES2019/070400 ES2019070400W WO2019238993A1 WO 2019238993 A1 WO2019238993 A1 WO 2019238993A1 ES 2019070400 W ES2019070400 W ES 2019070400W WO 2019238993 A1 WO2019238993 A1 WO 2019238993A1
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WO
WIPO (PCT)
Prior art keywords
milk
light phase
line
hydraulic pump
equipment
Prior art date
Application number
PCT/ES2019/070400
Other languages
Spanish (es)
French (fr)
Inventor
Holger FUNKE
Original Assignee
Seppelec, S.L.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Seppelec, S.L. filed Critical Seppelec, S.L.
Publication of WO2019238993A1 publication Critical patent/WO2019238993A1/en

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Classifications

    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23CDAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
    • A23C9/00Milk preparations; Milk powder or milk powder preparations
    • A23C9/15Reconstituted or recombined milk products containing neither non-milk fat nor non-milk proteins
    • A23C9/1508Dissolving or reconstituting milk powder; Reconstitution of milk concentrate with water; Standardisation of fat content of milk
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01JMANUFACTURE OF DAIRY PRODUCTS
    • A01J11/00Apparatus for treating milk
    • A01J11/10Separating milk from cream
    • GPHYSICS
    • G05CONTROLLING; REGULATING
    • G05DSYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
    • G05D11/00Control of flow ratio
    • G05D11/02Controlling ratio of two or more flows of fluid or fluent material
    • G05D11/13Controlling ratio of two or more flows of fluid or fluent material characterised by the use of electric means
    • G05D11/135Controlling ratio of two or more flows of fluid or fluent material characterised by the use of electric means by sensing at least one property of the mixture
    • G05D11/137Controlling ratio of two or more flows of fluid or fluent material characterised by the use of electric means by sensing at least one property of the mixture by sensing the density of the mixture
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23CDAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
    • A23C2210/00Physical treatment of dairy products
    • A23C2210/25Separating and blending
    • A23C2210/254Cream is separated from milk, one of the fractions is treated and at least part of the cream is remixed with the milk

Definitions

  • the object of the present invention is a novel cream dosing equipment capable of reinjecting in the milk the amount necessary to reach the fat concentration value set in the recipe.
  • the milk production plants consist of a tank of origin, in which milk from livestock farmers is stored, a skimmer placed at the exit of the tank of origin which separates the whole milk into two streams: a main one, called the phase heavy, composed of skim milk and other secondary, called light phase, composed of cream extracted from whole milk, then the standardized equipment of milk is placed, which mixes both streams getting a concentration of cream close to the desired .
  • This equipment on the one hand feeds a cream storage tank and a standardized milk storage tank. After the necessary corrections due to inaccuracy in the dosing of these equipments, the pasteurization and packaging line is fed.
  • the standardization of milk equipment is aimed at dosing cream in milk from the source tank to obtain the desired concentration, which is usually done by means of two or more modulating valves and flow meters that measure the volume of cream to be injected and the volume of milk from the source tank, and regulate the opening and closing of the valves.
  • the present invention advocates a standardization equipment that solves the above drawbacks, is able to work in continuous and batch processes, records and regulates, in real time, the amount of fat or cream contained in standardized milk.
  • the milk standardization equipment which is the object of the present invention, is disposed at the exit of the skimming unit and is fed by the main line that feeds it from the heavy phase and by the secondary line that feeds it from the light phase, and in turn feeds any continuous processing line, sending the remaining cream to the cream storage tank.
  • the milk standardization equipment which is the object of the present invention, comprises:
  • a light or cream phase input line coming from the skimmer unit; • a standardized milk outlet line that is homogeneous milk in its fat content, which feeds the standardized milk processing unit, which usually includes pasteurizers, UHT (for its acronym in Ultra High Temperature or ultra high temperature), and fillers , and which has:
  • a grease meter preferably by spectrophotometry, arranged descending from said static mixer, which uses four optical analysis methods: transmission, dispersion, fluorescence and refraction. Measuring in the wavelength range between 200 nm and 4000 nm;
  • a thermally insulated light phase regulation tank which has two output lines, the first is the mentioned light phase output line and the second is a light phase injection line that connects to the input line of the heavy phase descending from the mass flowmeter and ascending from the hydraulic pump, and having one or more level sensors, one or more maximum level sensors and one or more temperature sensors of the stored light phase ;
  • Figure 1 shows a block diagram of the current state of the art in milk standardization.
  • Figure 2 shows a scheme of a milk production plant that incorporates milk standardization equipment.
  • Figure 3 shows a diagram of the milk standardization equipment.
  • Figure 1 shows a block diagram that represents the current process of standardizing milk, in which milk (b) from livestock farmers is stored, skimmed (C), subsequently standardized (D) and stores the standardized milk (E) and the cream (F), after and after the necessary corrections, cream adjustment (G), due to the inaccuracy in the dosing of these equipments, the pasteurization and packaging line (H) .
  • Figure 2 shows a preferred embodiment of the milk standardization equipment, which is the object of the present description, which is placed at the exit of a skimmer unit (2), which separates the whole milk from the source tank ( 1) in two streams: a main one, called heavy phase, composed of skim milk and a secondary one, called light phase, composed of cream extracted from whole milk, and that feeds a storage tank (3) of the light phase and the standardized milk processing unit (4).
  • a skimmer unit (2) which separates the whole milk from the source tank ( 1) in two streams: a main one, called heavy phase, composed of skim milk and a secondary one, called light phase, composed of cream extracted from whole milk, and that feeds a storage tank (3) of the light phase and the standardized milk processing unit (4).
  • the milk standardization equipment (5) includes:
  • LS1 a standardized milk outlet line (LS1) that feeds the standardized, non-homogenized milk line, continuously and therefore feeds any type of pasteurizer, fillers, etc., and which has:
  • a hydraulic pump (B1) which can be of the booster type, single or double screw, lobular or preferably centrifugal,
  • a static mixer preferably static, although it could be dynamic, placed downwards from said booster pump and which has at least six internal baffles placed in a spiral.
  • a grease meter preferably by spectrophotometry, arranged downwards from said static mixer, which uses four optical analysis methods: transmission, dispersion, fluorescence and refraction. Measuring in the wavelength range between 200 nm and 4000 nm;
  • LS2 light phase output line
  • B3 expedition pump
  • a thermally insulated light phase regulation tank which has two output lines, the first is the mentioned light phase output line (LS2) and the second is a light phase injection line (L1) that it is connected to the heavy phase input line (LE1) downwards from the mass flowmeter (C1) and upwards from the hydraulic pump, and which has one or more level sensors, one or more sensors maximum level and one or more temperature sensors of the stored light phase, which monitor and record the light phase volume and its temperature.
  • the main advantage of the regulation tank is to divide the circuit in two, avoiding any interference in both the operation of the booster pump and the equipment;
  • a dosing pump B2
  • B2 preferably double screw type with a frequency converter, single screw or lobular, arranged in the light phase injection line (L1) ascending from the mass flow meter (C3).
  • a dosing pump B2
  • a frequency inverter and controlled from the computer device (hardware) with the mass measurements and corrections of the grease meter achieves greater accuracy in dosing, since the injection rate does not depend on the pressures and flow rates of the line.
  • a bypass system which may be composed of several valves or preferably a single three-way automatic bypass valve (V), whose common conduit is arranged in the light phase inlet line, whose preferred route is connected to the line for entering the light phase downwards from the mass flowmeter (C1) and upwards from the hydraulic pump, and whose driven path feeds the said light phase regulating tank;
  • V three-way automatic bypass valve
  • the equipment injects the entire light phase out of range into skim milk and recirculates it into the milk tank. origin, which is achieved with the three-way automatic bypass valve.
  • the operating point of the skimming unit is determined by calculations of the fat concentration as a function of the density measured by the first mass flowmeter. Once said operating point is reached, the computer device activates the automatic bypass valve giving way to the light phase to the regulating tank.
  • This regulation tank makes the skimming process independent of the injection process and / or deflection of the excess light phase, avoiding interference between the two.
  • the automatic bypass valve also performs a safety function, since in case of failure of the hydraulic pump and / or grease out of range, the equipment returns to the recirculation position, until the optimum operating parameters are reached.
  • the concentration of fat in the light phase stored in the regulation tank is calculated, adjusting the light phase dosage through the injection line by means of the third mass flow meter.
  • the mixture passes through the static mixer, which homogenizes the heavy phase and light phase mixture before reaching the fat meter, which has a double function: check and record the concentration of fat in the milk and recalibrate the light phase dosage based on the measured results.
  • the equipment has a hydraulic pump capable of isolating the installation downstream from the installation upstream, eliminating any interference in the dosage due to pressure variations.

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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Animal Husbandry (AREA)
  • Environmental Sciences (AREA)
  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Automation & Control Theory (AREA)
  • Chemical & Material Sciences (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Dairy Products (AREA)

Abstract

The invention relates to a standardising devicefor milk, which is a cream-dosing device that can re-inject into milk the amount necessary to achieve a fat concentration value set in a recipe. The device is disposed at the outlet of a skimming unit and is supplied by a main line, which supplies the heavy phase, and by a secondary line, which supplies the light phase and also supplies any continuous processing line, sending the excess cream to a cream storage tank. The device is characterised in that it includes a fat meter (A) and a precise system for measuring (flow meters C1, C2 and C3) and dispensing (pumps B1, B2), as well as hardware and software for signal control and processing.

Description

DESCRIPCIÓN  DESCRIPTION
Equipo de estandarización de leche Milk Standardization Equipment
Objeto de la invención Object of the invention
El objeto de la presente invención es un novedoso equipo de dosificación de nata capaz de reinyectar en la leche la cantidad necesaria para alcanzar el valor de concentración de grasa fijado en la receta. The object of the present invention is a novel cream dosing equipment capable of reinjecting in the milk the amount necessary to reach the fat concentration value set in the recipe.
Antecedentes de la invención Background of the invention
Las plantas de producción de leche constan de un tanque de origen, en el que se almacena la leche procedente de los ganaderos, una desnatadora colocada a la salida de tanque de origen la cual separa la leche entera en dos corrientes: una principal, llamada fase pesada, compuesta por la leche desnatada y otra secundaria, llamada fase ligera, compuesta por la nata extraída de la leche entera, después se coloca el equipo de estandarizado de la leche, el cual mezcla ambas corrientes consiguiendo una concentración de nata cercana a la deseada. Este equipo por un lado alimenta un tanque de almacenamiento de nata y un tanque de almacenamiento de leche estandarizada. Después de las correcciones necesarias debidas a la inexactitud en la dosificación de estos equipos se alimenta la línea de pasteurizado y envasado. The milk production plants consist of a tank of origin, in which milk from livestock farmers is stored, a skimmer placed at the exit of the tank of origin which separates the whole milk into two streams: a main one, called the phase heavy, composed of skim milk and other secondary, called light phase, composed of cream extracted from whole milk, then the standardized equipment of milk is placed, which mixes both streams getting a concentration of cream close to the desired . This equipment on the one hand feeds a cream storage tank and a standardized milk storage tank. After the necessary corrections due to inaccuracy in the dosing of these equipments, the pasteurization and packaging line is fed.
El equipo de estandarización de leche tiene por objetivo la dosificación de nata en la leche procedente del tanque de origen para obtener la concentración deseada, lo que se suele realizar mediante dos o más válvulas modulantes y caudalímetros que miden el volumen de nata a inyectar y el volumen de leche procedente del tanque de origen, y regulan la apertura y cierre de las válvulas. The standardization of milk equipment is aimed at dosing cream in milk from the source tank to obtain the desired concentration, which is usually done by means of two or more modulating valves and flow meters that measure the volume of cream to be injected and the volume of milk from the source tank, and regulate the opening and closing of the valves.
La apertura y cierre de las válvulas modulantes genera interferencias en la unidad desnatadora debidas a las variaciones de presión, lo que ocasiona un funcionamiento errático y variaciones en la concentración de nata en la leche. Además, estos equipos de estandarización requieren de comprobaciones de calidad por parte de los operarios de la planta, restringiendo su utilización en las plantas de cuyo funcionamiento es por lotes. The opening and closing of the modulating valves generates interference in the skimmer unit due to pressure variations, which causes erratic operation and variations in the cream concentration in milk. In addition, these standardization equipment requires quality checks by the plant's operators, restricting its use in plants whose operation is in batches.
Resumiendo, los equipos de estandarización actuales tienen los siguientes inconvenientes: In summary, current standardization equipment has the following disadvantages:
• Necesidad de comprobación de la concentración de grasa o nata en la leche por parte de los operarios. • Need to check the concentration of fat or cream in the milk by the operators.
• Desestabilizan el funcionamiento óptimo de las unidades de desnatado. • They destabilize the optimal functioning of skimming units.
• El alto volumen de merma en la nata durante la puesta en régimen de la planta. • The high volume of shrinkage in the cream during the plant's setting.
La presente invención preconiza un equipo de estandarización que soluciona los anteriores inconvenientes, es capaz de trabajar en procesos continuos y por lotes, registra y regula, en tiempo real la cantidad de grasa o nata contenida en la leche estandarizada. The present invention advocates a standardization equipment that solves the above drawbacks, is able to work in continuous and batch processes, records and regulates, in real time, the amount of fat or cream contained in standardized milk.
Descripción de la invención Description of the invention
El equipo de estandarización de leche, que es el objeto de la presente invención, se dispone a la salida de la unidad de desnatado y es alimentado por la línea principal que lo alimenta de la fase pesada y por la línea secundaria que lo alimenta de la fase ligera, y a su vez alimenta cualquier línea de procesado en continuo, mandando la nata sobrante al tanque de almacenamiento de nata. The milk standardization equipment, which is the object of the present invention, is disposed at the exit of the skimming unit and is fed by the main line that feeds it from the heavy phase and by the secondary line that feeds it from the light phase, and in turn feeds any continuous processing line, sending the remaining cream to the cream storage tank.
El equipo de estandarización de leche, que es el objeto de la presente invención, comprende: The milk standardization equipment, which is the object of the present invention, comprises:
• un bastidor al que se fijan el resto de elementos y dispositivos; • a frame to which the rest of the elements and devices are fixed;
• una línea de entrada de la fase pesada, o leche desnatada, proveniente de la unidad desnatadora;  • a heavy phase input line, or skim milk, from the skimmer unit;
• una línea de entrada de la fase ligera, o nata, proveniente de la unidad desnatadora; • una línea de salida de leche estandarizada es decir leche homogénea en su contenido graso, que alimenta la unidad de procesado de leche estandarizada, que suele englobar pasteurizadores, UHT (por sus siglas en inglés de Ultra High Temperature o temperatura ultraelevada), y llenadoras, y que dispone de: • a light or cream phase input line, coming from the skimmer unit; • a standardized milk outlet line that is homogeneous milk in its fat content, which feeds the standardized milk processing unit, which usually includes pasteurizers, UHT (for its acronym in Ultra High Temperature or ultra high temperature), and fillers , and which has:
— una bomba hidráulica, - a hydraulic pump,
— un mezclador colocado descendentemente desde la citada bomba hidráulica y que dispone en su interior de al menos seis deflectores internos colocados en forma espiral,  - a mixer placed downwards from the said hydraulic pump and which has at least six internal baffles placed in a spiral,
— un medidor de grasa (A), preferentemente por espectrofotometría, dispuesto de forma descendente desde el citado mezclador estático, que utiliza cuatro métodos de análisis ópticos: transmisión, dispersión, fluorescencia y refracción. Midiendo en el rango de longitud de onda entre 200 nm y 4000 nm;  - a grease meter (A), preferably by spectrophotometry, arranged descending from said static mixer, which uses four optical analysis methods: transmission, dispersion, fluorescence and refraction. Measuring in the wavelength range between 200 nm and 4000 nm;
• una línea de salida de fase ligera que alimenta un tanque de almacenamiento de nata, en la que está dispuesta una bomba hidráulica de expedición; • a light phase output line that feeds a cream storage tank, in which a hydraulic dispatch pump is arranged;
• una línea de salida de reinyección a un tanque de origen;  • a reinjection output line to a source tank;
• un primer caudalímetro másico dispuesto en la línea de entrada de la fase pesada;  • a first mass flowmeter disposed in the heavy phase input line;
• un segundo caudalímetro másico dispuesto en la línea de entrada de la fase ligera,  • a second mass flow meter arranged in the light phase input line,
• un tanque de regulación de fase ligera aislado térmicamente, que tiene dos líneas de salida, la primera es la mencionada línea de salida de fase ligera y la segunda es una línea de inyección de fase ligera que se conecta a la línea de entrada de la fase pesada de forma descendente desde el caudalímetro másico y de forma ascendente desde la bomba hidráulica, y que dispone de uno o más sensores de nivel, de uno o más sensores de nivel máximo y de uno o más sensores de temperatura de la fase ligera almacenada;  • a thermally insulated light phase regulation tank, which has two output lines, the first is the mentioned light phase output line and the second is a light phase injection line that connects to the input line of the heavy phase descending from the mass flowmeter and ascending from the hydraulic pump, and having one or more level sensors, one or more maximum level sensors and one or more temperature sensors of the stored light phase ;
• un tercer caudalímetro másico dispuesto en la línea de inyección de fase ligera; • una bomba de dosificación, dispuesta en la línea de inyección de fase ligera de forma ascendente desde el caudalímetro másico; • a third mass flow meter arranged in the light phase injection line; • a dosing pump, arranged in the light phase injection line ascending from the mass flowmeter;
• un sistema de derivación, cuyo conducto común está dispuesto en la línea de entrada de la fase ligera, cuya vía preferente está conectada a la línea de entrada de la fase ligera de forma descendente desde el caudalímetro másico y de forma ascendente desde la bomba hidráulica, y cuya vía accionada alimenta el mencionado tanque de regulación de fase ligera; • a bypass system, whose common conduit is disposed in the light phase input line, whose preferred path is connected to the light phase input line descending from the mass flowmeter and ascending from the hydraulic pump , and whose driven track feeds said light phase regulation tank;
• un dispositivo informático y su correspondiente software que recibe información del primer, segundo y tercer caudalímetros másicos y del medidor de grasa y controla la válvula automática de derivación y el variador de frecuencia de la bomba de dosificación. • a computer device and its corresponding software that receives information from the first, second and third mass flowmeters and the grease meter and controls the automatic bypass valve and the frequency inverter of the dosing pump.
Breve descripción de las figuras Brief description of the figures
La figura 1 muestra un diagrama de bloques del actual estado de la técnica en el estandarizado de leche. Figure 1 shows a block diagram of the current state of the art in milk standardization.
La figura 2 muestra un esquema de una planta de producción de leche que incorpora el equipo de estandarización de leche. Figure 2 shows a scheme of a milk production plant that incorporates milk standardization equipment.
La figura 3 muestra un esquema del equipo de estandarización de leche. Figure 3 shows a diagram of the milk standardization equipment.
Realizaciones
Figure imgf000006_0001
Realizations
Figure imgf000006_0001
La figura 1 muestra un diagrama de bloques que representa el proceso actual de estandarizado de leche, en el cual se almacena la leche (b) procedente de los ganaderos, se procede a su desnatado (C), posteriormente se estandariza (D) y se almacena la leche estandarizada (E) y la nata (F), posteriormente y después de las correcciones necesarias, ajuste de nata (G), debidas a la inexactitud en la dosificación de estos equipos se alimenta la línea de pasteurizado y envasado (H). La figura 2 muestra una realización preferente del equipo de estandarización de leche, que es el objeto de la presente descripción, el cual se coloca a la salida de una unidad desnatadora (2), el cual separa la leche entera procedente del tanque de origen (1) en dos corrientes: una principal, llamada fase pesada, compuesta por la leche desnatada y otra secundaria, llamada fase ligera, compuesta por la nata extraída de la leche entera, y que alimenta un tanque de almacenamiento (3) de la fase ligera y la unidad (4) de procesado de leche estandarizada. Figure 1 shows a block diagram that represents the current process of standardizing milk, in which milk (b) from livestock farmers is stored, skimmed (C), subsequently standardized (D) and stores the standardized milk (E) and the cream (F), after and after the necessary corrections, cream adjustment (G), due to the inaccuracy in the dosing of these equipments, the pasteurization and packaging line (H) . Figure 2 shows a preferred embodiment of the milk standardization equipment, which is the object of the present description, which is placed at the exit of a skimmer unit (2), which separates the whole milk from the source tank ( 1) in two streams: a main one, called heavy phase, composed of skim milk and a secondary one, called light phase, composed of cream extracted from whole milk, and that feeds a storage tank (3) of the light phase and the standardized milk processing unit (4).
El equipo de estandarización de leche (5) comprende: The milk standardization equipment (5) includes:
• un bastidor al que se fijan el resto de elementos y dispositivos; • a frame to which the rest of the elements and devices are fixed;
• una línea de entrada de la fase pesada (LE1), o leche desnatada, proveniente de la unidad desnatadora;  • a heavy phase input line (LE1), or skim milk, from the skimmer unit;
• una línea de entrada de la fase ligera (LE2), o nata, proveniente de la unidad desnatadora;  • a light phase input line (LE2), or cream, from the skimmer unit;
• una línea de salida de leche estandarizada (LS1) que alimenta la línea de leche estandarizada, no homogeneizada, de forma continua y por tanto alimenta cualquier tipo de pasteurizador, llenadoras, etc., y que dispone de:  • a standardized milk outlet line (LS1) that feeds the standardized, non-homogenized milk line, continuously and therefore feeds any type of pasteurizer, fillers, etc., and which has:
— una bomba hidráulica (B1), que puede ser del tipo booster, de simple o de doble tornillo, lobular o preferentemente centrífuga, - a hydraulic pump (B1), which can be of the booster type, single or double screw, lobular or preferably centrifugal,
— un mezclador estático (M), preferentemente estático, aunque pudiera ser dinámico, colocado de forma descendente desde la citada bomba booster y que dispone en su interior de al menos seis deflectores internos colocados en forma espiral. La introducción de un mezclador estático a la salida de la línea de salida de leche estandarizada y homogeneizada, en cuanto a su contenido graso, permite la rápida mezcla de la leche estandarizada, garantizando la correcta homogeneización y eliminando la necesidad de tanques con agitación.  - a static mixer (M), preferably static, although it could be dynamic, placed downwards from said booster pump and which has at least six internal baffles placed in a spiral. The introduction of a static mixer at the exit of the standardized and homogenized milk outlet line, in terms of its fat content, allows the rapid mixing of the standardized milk, guaranteeing the correct homogenization and eliminating the need for tanks with agitation.
— un medidor de grasa (A), preferentemente por espectrofotometría, dispuesto de forma descendente desde el citado mezclador estático, que utiliza cuatro métodos de análisis ópticos: transmisión, dispersión, fluorescencia y refracción. Midiendo en el rango de longitud de onda entre 200 nm y 4000 nm; - a grease meter (A), preferably by spectrophotometry, arranged downwards from said static mixer, which uses four optical analysis methods: transmission, dispersion, fluorescence and refraction. Measuring in the wavelength range between 200 nm and 4000 nm;
• una línea de salida de fase ligera (LS2) que alimenta el tanque de almacenamiento de nata, en la que está dispuesta una bomba (B3) de expedición, preferentemente lobular, aunque pudiera ser de simple o doble tornillo o centrífuga; • a light phase output line (LS2) that feeds the cream storage tank, in which an expedition pump (B3) is arranged, preferably lobular, although it could be single or double screw or centrifugal;
• una línea de salida de inyección (LS3) al tanque de origen;  • an injection outlet line (LS3) to the source tank;
un primer caudalímetro másico (C1) dispuesto en la línea de entrada de la fase pesada;  a first mass flow meter (C1) disposed in the heavy phase input line;
• un segundo caudalímetro másico (C2) dispuesto en la línea de entrada de la fase ligera;  • a second mass flow meter (C2) arranged in the light phase input line;
• un tanque de regulación (T) de fase ligera aislado térmicamente, que tiene dos líneas de salida ,la primera es la mencionada línea de salida de fase ligera (LS2) y la segunda es una línea de inyección (L1) de fase ligera que se conecta a la línea de entrada de la fase pesada (LE1) de forma descendente desde el caudalímetro másico (C1) y de forma ascendente desde la bomba hidráulica, y que dispone de uno o más sensores de nivel, de uno o más sensores de nivel máximo y de uno o más sensores de temperatura de la fase ligera almacenada, los cuales monitorizan y registran el volumen de fase ligera y su temperatura. La principal ventaja del tanque de regulación es dividir el circuito en dos, evitando cualquier interferencia tanto en el funcionamiento de la bomba booster como en el del equipo; • a thermally insulated light phase regulation tank (T), which has two output lines, the first is the mentioned light phase output line (LS2) and the second is a light phase injection line (L1) that it is connected to the heavy phase input line (LE1) downwards from the mass flowmeter (C1) and upwards from the hydraulic pump, and which has one or more level sensors, one or more sensors maximum level and one or more temperature sensors of the stored light phase, which monitor and record the light phase volume and its temperature. The main advantage of the regulation tank is to divide the circuit in two, avoiding any interference in both the operation of the booster pump and the equipment;
• un tercer caudalímetro másico (C3) dispuesto en la línea de inyección (L1) de fase ligera; • a third mass flow meter (C3) arranged in the light phase injection line (L1);
• una bomba (B2) de dosificación, preferentemente de tipo doble tornillo con variador de frecuencia, de simple tornillo o lobular, dispuesta en la línea de inyección (L1) de fase ligera de forma ascendente desde el caudalímetro másico (C3). La dosificación con una bomba equipada con variador de frecuencia y controlada desde el dispositivo informático (hardware) con las medidas de masa y correcciones del medidor de grasa se consigue una mayor precisión en la dosificación, ya que el caudal de inyección no depende de las presiones y caudales de la línea. • un sistema de derivación, pudiendo estar compuesto por varias válvulas o preferiblemente una sola válvula (V) automática de derivación de tres vías, cuyo conducto común está dispuesto en la línea de entrada de la fase ligera, cuya vía preferente está conectada a la línea de entrada de la fase ligera de forma descendente desde el caudalímetro másico (C1) y de forma ascendente desde de la bomba hidráulica, y cuya vía accionada alimenta el mencionado tanque de regulación de fase ligera; • a dosing pump (B2), preferably double screw type with a frequency converter, single screw or lobular, arranged in the light phase injection line (L1) ascending from the mass flow meter (C3). Dosing with a pump equipped with a frequency inverter and controlled from the computer device (hardware) with the mass measurements and corrections of the grease meter achieves greater accuracy in dosing, since the injection rate does not depend on the pressures and flow rates of the line. • a bypass system, which may be composed of several valves or preferably a single three-way automatic bypass valve (V), whose common conduit is arranged in the light phase inlet line, whose preferred route is connected to the line for entering the light phase downwards from the mass flowmeter (C1) and upwards from the hydraulic pump, and whose driven path feeds the said light phase regulating tank;
• un dispositivo informático y su correspondiente software que recibe información del primer, segundo y tercer caudalímetros másicos y del medidor de grasa y controla la válvula automática de derivación y el variador de frecuencia. El mayor avance del equipo es introducir un elemento de control y registro de la cantidad de grasa, este dispositivo informático recalibra el caudal de dosificación de nata en función de los valores de grasa en la mezcla final.  • a computer device and its corresponding software that receives information from the first, second and third mass flowmeters and the grease meter and controls the automatic bypass valve and the frequency inverter. The greatest advance of the equipment is to introduce a control element and record the amount of fat, this computing device recalibrates the cream dosing flow based on the fat values in the final mixture.
Durante la puesta en marcha de la planta de producción de leche, ya que las unidades desnatadoras requieren un cierto periodo de puesta en marcha, el equipo inyecta la totalidad de la fase ligera fuera de rango en la leche desnatada y la recircula en el tanque de origen, lo que se consigue con la válvula automática de derivación de tres vías. During the start-up of the milk production plant, since skimmer units require a certain start-up period, the equipment injects the entire light phase out of range into skim milk and recirculates it into the milk tank. origin, which is achieved with the three-way automatic bypass valve.
El punto de funcionamiento de la unidad de desnatado se determina mediante cálculos de la concentración de grasa en función de la densidad medida por el primer caudalímetro másico. Una vez alcanzado dicho punto de funcionamiento, el dispositivo informático activa la válvula automática de derivación dando paso a la fase ligera al tanque de regulación. Este tanque de regulación independiza el proceso de desnatado del proceso de inyección y/o desvío de la fase ligera sobrante, evitando interferencias entre ambos. La válvula automática de derivación también cumple una función de seguridad, ya que caso de fallo de la bomba hidráulica y/o de grasa fuera de rango, el equipo vuelve a posición de recirculación, hasta alcanzar los parámetros óptimos de funcionamiento. The operating point of the skimming unit is determined by calculations of the fat concentration as a function of the density measured by the first mass flowmeter. Once said operating point is reached, the computer device activates the automatic bypass valve giving way to the light phase to the regulating tank. This regulation tank makes the skimming process independent of the injection process and / or deflection of the excess light phase, avoiding interference between the two. The automatic bypass valve also performs a safety function, since in case of failure of the hydraulic pump and / or grease out of range, the equipment returns to the recirculation position, until the optimum operating parameters are reached.
Una vez terminada la puesta en marcha del equipo, en el funcionamiento en régimen de operación Tanto la nata proveniente de la unidad de desnatado como la leche desnatada son contabilizadas y analizadas por el primer y el segundo caudalímetros másicos y el dispositivo informático registra las concentraciones y caudales de fase pesada y de fase ligera que llegan al equipo. Once the start-up of the equipment is finished, in the operation in operation regime Both the cream coming from the skimmer unit and the skim milk are counted and analyzed by the first and second mass flowmeters and the computing device records the concentrations and flows of heavy phase and light phase that reach the equipment.
Con los datos del segundo caudalímetro másico se calcula la concentración de grasa en la fase ligera almacenada en el tanque de regulación, ajustándose la dosificación de fase ligera a través de la línea de inyección mediante el tercer caudalímetro másico. With the data of the second mass flowmeter, the concentration of fat in the light phase stored in the regulation tank is calculated, adjusting the light phase dosage through the injection line by means of the third mass flow meter.
Una vez realizada la mezcla, ésta pasa por el mezclador estático, el cual homogeneiza la mezcla de fase pesada y de fase ligera antes de llegar al medidor de grasa, el cual tiene una doble función: comprobar y registrar la concentración de grasa en la leche y recalibrar la dosificación de fase ligera en función de los resultados medidos. Once the mixture is done, it passes through the static mixer, which homogenizes the heavy phase and light phase mixture before reaching the fat meter, which has a double function: check and record the concentration of fat in the milk and recalibrate the light phase dosage based on the measured results.
Además, el equipo cuenta con una bomba hidráulica capaz de aislar la instalación aguas abajo de la instalación aguas arriba, eliminando cualquier interferencia en la dosificación debida a variaciones de la presión. In addition, the equipment has a hydraulic pump capable of isolating the installation downstream from the installation upstream, eliminating any interference in the dosage due to pressure variations.

Claims

REIVINDICACIONES
1.- Equipo de estandarización de leche, de aquellos que se disponen entre, por un lado, la unidad de desnatado y, por otro lado, la unidad de procesado de leche estandarizada y el tanque de almacenamiento de nata, caracterizado porque comprende: 1.- Standardization equipment for milk, of those that are disposed between, on the one hand, the skimming unit and, on the other hand, the standardized milk processing unit and the cream storage tank, characterized in that it comprises:
• un bastidor al que se fijan el resto de elementos y dispositivos; • a frame to which the rest of the elements and devices are fixed;
• una línea de entrada de la fase pesada (LE1), o leche desnatada, proveniente de la unidad desnatadora;  • a heavy phase input line (LE1), or skim milk, from the skimmer unit;
• una línea de entrada de la fase ligera (LE2), o nata, proveniente de la unidad desnatadora;  • a light phase input line (LE2), or cream, from the skimmer unit;
• una línea de salida de leche estandarizada (LS1) que alimenta a la unidad de procesado de leche estandarizada que dispone de:  • a standardized milk outlet line (LS1) that feeds the standardized milk processing unit that has:
— una bomba hidráulica (B1), - a hydraulic pump (B1),
— un mezclador (M) dispuesto de forma descendente desde la citada bomba hidráulica (B1) y que dispone en su interior de al menos seis deflectores internos colocados en forma espiral, - a mixer (M) disposed downwardly from said hydraulic pump (B1) and which has at least six internal baffles placed in a spiral,
— un medidor de grasa (A) dispuesto de forma descendente desde el citado mezclador (M); - a grease meter (A) disposed downwardly from said mixer (M);
• una línea de salida de fase ligera (LS2) que alimenta un tanque de almacenamiento de nata, en la que está dispuesta una bomba hidráulica (B3) de expedición pudiendo ser tipo tornillo (simple o doble), centrífuga o preferiblemente lobular. • a light phase output line (LS2) that feeds a cream storage tank, in which an expedition hydraulic pump (B3) is arranged and can be screw type (single or double), centrifugal or preferably lobular.
• una línea de salida de reinyección (LS3) a un tanque de origen;  • a reinjection output line (LS3) to a source tank;
• un primer caudalímetro másico (C1) dispuesto en la línea de entrada de la fase pesada (LE1);  • a first mass flow meter (C1) disposed in the heavy phase input line (LE1);
• un segundo caudalímetro másico (C2) dispuesto en la línea de entrada de la fase ligera (LE2),  • a second mass flowmeter (C2) arranged in the light phase input line (LE2),
• un tanque de regulación (T) de fase ligera aislado térmicamente, que tiene dos líneas de salida, la primera es la mencionada línea de salida de fase ligera (L7=LS2) y la segunda es una línea de inyección (L8) de fase ligera que se conecta a la línea de entrada de la fase pesada (LE1) de forma descendente desde el caudalímetro másico (C1) y de forma ascendente desde la bomba hidráulica (B1), y que dispone de uno o más sensores de nivel, de uno o más sensores de nivel máximo y de uno o más sensores de temperatura de la fase ligera almacenada; • a thermally insulated light phase regulation tank (T), which has two output lines, the first is the mentioned light phase output line (L7 = LS2) and the second is a phase injection line (L8) light which is connected to the heavy phase input line (LE1) downwards from the mass flowmeter (C1) and upwards from the hydraulic pump (B1), and which has one or more level sensors, one or more maximum level sensors and one or more temperature sensors of the stored light phase;
• un tercer caudalímetro másico (C3) dispuesto en la línea de inyección (L8) de fase ligera;  • a third mass flow meter (C3) arranged in the light phase injection line (L8);
• una bomba (B2) de dosificación, dispuesta en la línea de inyección (L8) de fase ligera de forma ascendente desde el caudalímetro másico (C3);  • a dosing pump (B2), arranged in the light phase injection line (L8) ascending from the mass flow meter (C3);
• un sistema de derivación, cuyo conducto común está dispuesto en la línea de entrada de la fase ligera, cuya vía preferente está conectada a la línea de entrada de la fase ligera de forma descendente desde el caudalímetro másico (C1) y de forma ascendente desde la bomba hidráulica (B1), y cuya vía accionada alimenta el mencionado tanque de regulación de fase ligera; • a shunt system, whose common conduit is disposed in the light phase input line, whose preferred path is connected to the light phase input line downward from the mass flowmeter (C1) and upwardly from the hydraulic pump (B1), and whose driven path feeds the said light phase regulating tank;
• un dispositivo informático (hardware) y su correspondiente programa informático (software) que recibe información del primer, segundo y tercer caudalímetros másicos y del medidor de grasa y controla la válvula automática de derivación y el variador de frecuencia de la bomba de dosificación. • a computer device (hardware) and its corresponding computer program (software) that receives information from the first, second and third mass flowmeters and the grease meter and controls the automatic bypass valve and the frequency variator of the dosing pump.
2.- Equipo de estandarización de leche, según reivindicación 1 , caracterizado porque la bomba hidráulica (B1) tiene la función de bomba booster. 2. Milk standardization equipment according to claim 1, characterized in that the hydraulic pump (B1) has the function of a booster pump.
3.- Equipo de estandarización de leche, según reivindicación 1 , caracterizado porque la bomba hidráulica (B1) es una bomba hidráulica centrífuga. 3. Milk standardization equipment according to claim 1, characterized in that the hydraulic pump (B1) is a centrifugal hydraulic pump.
4 - Equipo estandarizador de leche, según cualquiera de las reivindicaciones anteriores, caracterizado porque el mezclador (M) es dinámico. 4 - Standard milk equipment according to any of the preceding claims, characterized in that the mixer (M) is dynamic.
5.- Equipo estandarizador de leche, según cualquiera de las reivindicaciones de la 1 a la 3, caracterizado porque el mezclador (M) es estático. 5. Standard milk equipment, according to any of claims 1 to 3, characterized in that the mixer (M) is static.
6.- Equipo estandarizador de leche, según cualquiera de las reivindicaciones de la 1 a la 5, caracterizado porque la bomba hidráulica de expedición (B3) es del tipo lobular. 6. Standard milk equipment, according to any one of claims 1 to 5, characterized in that the hydraulic expedition pump (B3) is of the lobular type.
7.- Equipo estandarizador de leche, según cualquiera de las reivindicaciones anteriores, caracterizado porque está compuesto por una sola válvula (V) automática de derivación de tres vías. 7. Standard milk equipment, according to any of the preceding claims, characterized in that it is composed of a single automatic three-way bypass valve (V).
8.- Equipo estandarizador de leche, según cualquiera de las reivindicaciones anteriores, caracterizado porque la bomba hidráulica de expedición (B2) es del tipo doble tornillo. 8. Standard milk equipment, according to any of the preceding claims, characterized in that the hydraulic expedition pump (B2) is of the double screw type.
9.- Equipo estandarizador de leche, según cualquiera de las reivindicaciones anteriores, caracterizado porque los medidores de caudal (C1 , C2 y C3) son de tipo másico. 9. Standard milk equipment according to any of the preceding claims, characterized in that the flow meters (C1, C2 and C3) are of the mass type.
10.- Equipo estandarizador de leche, según cualquiera de las reivindicaciones anteriores, caracterizado porque el medidor de grasa (A) realiza la medida por espectrofotometría. 10. Standard milk equipment according to any of the preceding claims, characterized in that the fat meter (A) performs the measurement by spectrophotometry.
PCT/ES2019/070400 2018-06-11 2019-06-10 Milk standardisation device WO2019238993A1 (en)

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3983257A (en) * 1973-05-29 1976-09-28 Alfa-Laval Ab Production of milk with predetermined fat content
US4075355A (en) * 1975-07-04 1978-02-21 Gebruder Ott A.G. Method and apparatus for regulating the fat content of milk
US4074622A (en) * 1975-04-23 1978-02-21 Westfalia Separator Ag Apparatus for the continuous production of standardized milk
EP0427750A1 (en) * 1988-07-21 1991-05-22 Stork Amsterdam Process and device for the production of milk with a predetermined fat content.
US5137738A (en) * 1989-05-16 1992-08-11 Wedgewood Technology, Inc. System and method for controlling butterfat content in standardized milk product using whole product sensor
US5260079A (en) * 1991-11-29 1993-11-09 Westfalia Separator Ag Method of and equipment for controlling the content of fat in milk

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3983257A (en) * 1973-05-29 1976-09-28 Alfa-Laval Ab Production of milk with predetermined fat content
US4074622A (en) * 1975-04-23 1978-02-21 Westfalia Separator Ag Apparatus for the continuous production of standardized milk
US4075355A (en) * 1975-07-04 1978-02-21 Gebruder Ott A.G. Method and apparatus for regulating the fat content of milk
EP0427750A1 (en) * 1988-07-21 1991-05-22 Stork Amsterdam Process and device for the production of milk with a predetermined fat content.
US5137738A (en) * 1989-05-16 1992-08-11 Wedgewood Technology, Inc. System and method for controlling butterfat content in standardized milk product using whole product sensor
US5260079A (en) * 1991-11-29 1993-11-09 Westfalia Separator Ag Method of and equipment for controlling the content of fat in milk

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ES2735078A1 (en) 2019-12-16

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