WO2020183305A1 - Process for obtaining food products from coffee pulp - Google Patents
Process for obtaining food products from coffee pulp Download PDFInfo
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- WO2020183305A1 WO2020183305A1 PCT/IB2020/051927 IB2020051927W WO2020183305A1 WO 2020183305 A1 WO2020183305 A1 WO 2020183305A1 IB 2020051927 W IB2020051927 W IB 2020051927W WO 2020183305 A1 WO2020183305 A1 WO 2020183305A1
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- coffee
- pulp
- coffee pulp
- ground
- dry
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Classifications
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
- A23F5/00—Coffee; Coffee substitutes; Preparations thereof
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
- A23F5/00—Coffee; Coffee substitutes; Preparations thereof
- A23F5/02—Treating green coffee; Preparations produced thereby
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
- A23F5/00—Coffee; Coffee substitutes; Preparations thereof
- A23F5/04—Methods of roasting coffee
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
- A23F5/00—Coffee; Coffee substitutes; Preparations thereof
- A23F5/08—Methods of grinding coffee
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
- A23F5/00—Coffee; Coffee substitutes; Preparations thereof
- A23F5/10—Treating roasted coffee; Preparations produced thereby
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L19/00—Products from fruits or vegetables; Preparation or treatment thereof
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
- A23L33/10—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
- A23L33/105—Plant extracts, their artificial duplicates or their derivatives
Definitions
- the present invention is directed to a process for obtaining food products that comprises mixing coffee with coffee pulp.
- food products are obtained in the form of a powder for reconstitution or an infusion drink.
- patent US7833560 refers to a caffeinated drink comprising an extract derived from coffee husk, coffee pulp and coffee cherry and the method for producing it.
- the process for obtaining the caffeinated beverage comprises obtaining a by-product of coffee production (eg coffee husk, coffee pulp and coffee cherry); preparing a mixture of water and the coffee by-products to produce a mixture composed of a liquid portion and a solid portion; separating the liquid portion from the solid portion to produce a liquid extract; concentrate the liquid extract to produce a concentrated extract and between mixing the concentrated extract with additional components to get the caffeinated drink.
- a by-product of coffee production eg coffee husk, coffee pulp and coffee cherry
- preparing a mixture of water and the coffee by-products to produce a mixture composed of a liquid portion and a solid portion
- separating the liquid portion from the solid portion to produce a liquid extract
- concentrate the liquid extract to produce a concentrated extract and between mixing the concentrated extract with additional components to get the caffeinated drink
- the mixing of water and coffee by-products is carried out at temperatures between 65 to 80 ° C and may include an additional stage to reduce the size and increase the surface area of the solids and improve the efficient extraction of the desired substances from the by-products.
- this grinding is preferably carried out wet for a period between 15 to 30 minutes.
- patent US7807205 describes a process for producing beverages such as teas, juices and carbonated drinks from a coffee cherry extract.
- the process to obtain the extract from coffee cherry begins with the collection of coffee cherries; dry for a period between 0 to 48 hours until the percentage of water is not higher than 20% (w / w) in the coffee cherries; extract with an aqueous solvent in a ratio of 5: 1 to 20: 1 solvent / coffee cherry at a temperature of 82 to 100 ° C for a period of 30 minutes to 2 hours; filter or centrifuge to separate solids and liquids and obtain the liquid extract that can be further evaporated to obtain the solid extract of coffee cherry.
- the process contemplates an additional grinding stage to improve the contact area before extraction so that particles between 0.1 to 5 mm are obtained.
- the present invention refers to a process for obtaining food products from coffee pulp that comprises mixing coffee with coffee pulp, wherein the coffee is selected from green coffee, roasted coffee and ground coffee; and the coffee pulp is selected from dry coffee pulp, roasted coffee pulp and ground coffee pulp.
- the coffee pulp is dry ground coffee pulp or ground coffee pulp; if the selected coffee is roasted coffee, the coffee pulp is roasted coffee pulp; and the mixture obtained is subjected to a grinding step; and if the selected coffee is green coffee, the coffee pulp is dry pulp of coffee; and the mixture obtained is subjected to a roasting stage and subsequently to a grinding stage.
- food products are obtained characterized by a luminosity between 10 to 35 L *; humidity up to 10%, pH between 5 to 7 and a caffeine content between 0.1 to 5% w / w.
- FIG. 1 Flow chart of the process to obtain food products from green coffee and dry coffee pulp.
- FIG.2 Flow chart of the process to obtain food products from roasted coffee and roasted coffee pulp.
- FIG. 3 Flow chart of the process to obtain food products from ground coffee and ground coffee pulp.
- FIG. 4 Flow diagram of the process to obtain food products from ground coffee and dry ground coffee pulp.
- the present invention corresponds to a process to obtain food products from coffee pulp that comprises mixing coffee between 99% and 1% with coffee pulp between 1% and 99%, where the coffee is selected from green coffee , roast coffee and roast and ground coffee; and the coffee pulp is selected from dry coffee pulp, dry ground coffee pulp, roasted coffee pulp and ground coffee pulp.
- the term "coffee” refers to the seed that is extracted from the fruits of the coffee plant (coffee cherry) as a result of the wet milling process and the term “coffee pulp” is refers to a fibrous material or husk that is generated during the processing of coffee.
- the coffee pulp is dry coffee pulp; and the mixture obtained is subjected to a roasting stage that is carried out by means of heat by convection, conduction or radiation at temperatures between 130 to 250 ° C for a period between 2 to 30 minutes in a roaster selected from drum type roasters, perforated drum, continuous, centrifugal, bed fluidized, among others and subsequently to a grinding stage to an average particle size between 20 to 5000 microns, 50 to 4500 microns, 200 to 3500 microns, 400 to 3000 microns, 600 to 2500 microns, 800 to 1500 microns and 900 to 1000 microns in a mill selected from: mass type mill, disc mill, centrifugal mill, among others.
- a roasting stage that is carried out by means of heat by convection, conduction or radiation at temperatures between 130 to 250 ° C for a period between 2 to 30 minutes in a roaster selected from drum type roasters, perforated drum, continuous, centrifugal, bed fluidized, among others and subsequently to
- green coffee refers to the seed extracted from the fruits of the coffee plant after the wet beneficiation process that has not been roasted or ground. Green coffee is found in the mixture in a concentration between 1% to 99%, 10% to 90%, 20% to 80%, 30% to 70%, 40% to 60% and 50% to 55%.
- dry coffee pulp refers to the mucilaginous fibrous material that dries to a moisture content between 4% to 12%. The dry coffee pulp is found in the mixture in a concentration between 1% to 99%, 10% to 90%, 20% to 80%, 30% to 70%, 40% to 60% and 50% to 55%.
- the coffee pulp is roasted coffee pulp; and the mixture obtained is subjected to a grinding stage to an average particle size between 20 to 5000 microns, 50 to 4500 microns, 200 to 3500 microns, 400 to 3000 microns, 600 to 2500 microns, 800 to 1500 microns and 900 to 1000 microns in a mill selected from: mass type mill, disc mill, centrifugal mill, among others.
- roast coffee refers to the seed extracted from the fruits of the coffee plant after the wet beneficiation process that is roasted by means of heat by convection, conduction or radiation at temperatures between 130 to 250 ° C for a period between 2 to 30 minutes in a roaster selected from drum, perforated drum, continuous, centrifugal, fluidized bed roasters, among others.
- Roasted coffee is found in the mixture in a concentration between 1% to 99%, 10% to 90%, 20% to 80%, 30% to 70%, 40% to 60% and 50% to 55%.
- roasted coffee pulp refers to the dry pulp that is subjected to a roasting stage by means of heat by convection, conduction or radiation at temperatures between 130 to 250 ° C for a period between 2 to 30 minutes. in a roaster selected from drum, perforated drum, continuous, centrifugal, fluidized bed roasters, among others.
- the roasted coffee pulp in the mixture is in a concentration between 1% to 99%, 10% to 90%, 20% to 80%, 30% to 70%, 40% to 60% and 50% to 55%.
- the coffee pulp is dry ground coffee pulp or ground coffee pulp.
- ground coffee refers to roasted coffee that is ground to an average particle size between 20 to 5000 microns, 50 to 4500 microns, 200 to 3500 microns, 400 to 3000 microns, 600 to 2500 microns, 800 to 1500 microns and 900 to 1000 microns in a mill selected from: mass type mill, disk mill, centrifugal mill, among others.
- the ground coffee is found in the mixture in a concentration between 1% to 99%, 10% to 90%, 20% to 80%, 30% to 70%, 40% to 60% and 50% to 55%.
- dry ground coffee pulp refers to dry coffee pulp with a humidity percentage between 4% to 12% that is ground to an average particle size between 20 to 5000 microns, 50 to 4500 microns. , 200 to 3,500 microns, 400 to 3,000 microns, 600 to 2,500 microns, 800 to 1,500 microns and 900 to 1,000 microns in a mill selected from: mass type mill, disk mill, centrifugal mill, among others.
- the dry ground coffee pulp is found in the mixture in a concentration between 1% to 99%, 10% to 90%, 20% to 80%, 30% to 70%, 40% to 60% and 50% to 55%. .
- ground coffee pulp refers to roasted coffee pulp that is ground to an average particle size between 20 to 5000 microns, 50 to 4500 microns, 200 to 3500 microns, 400 to 3000 microns, 600 to 2500 microns, 800 to 1500 microns and 900 to 1000 microns in a mill selected from: mass type mill, disk mill, centrifugal mill, among others.
- the ground coffee pulp is found in the mixture in a concentration between 1% to 99%, 10% to 90%, 20% to 80%, 30% to 70%, 40% to 60% and 50% to 55%.
- food products are obtained in the form of powder to reconstitute or infusion drink characterized by a luminosity between 10 to 35 L *; humidity up to 10%, pH between 5 to 7 and a caffeine content between 0.1 to 5% w / w.
- Example 1 Process to obtain food products from green coffee and
- Table 2 shows the characteristics of the two products obtained with the process described in Example 1.
- Example 2 Process to obtain food products from roasted coffee and roasted coffee pulp
- 160kg of decaffeinated roasted coffee were weighed characterized by a dry base caffeine content of 0.11% and a moisture percentage of 11.08%, which had previously been subjected to a roasting stage in a plate centrifugal roaster operated on a curve. 200 ° C to 202 ° C for 10 minutes (Product DI).
- 160Kg of dry coffee pulp with a humidity percentage of 10.5% were weighed and added to a perforated drum type roaster operated at a temperature curve of 130 ° C to 178 ° C for a period of 8 minutes, to Obtain a roasted coffee pulp that was discharged on a cooling sieve until it reached a temperature of 30 ° C (Product D2).
- the products Ei and Fi were prepared, in which the amounts of coffee and roasting conditions were varied, as shown in table 3.
- the products E2 were prepared and F2 in which proportions of coffee pulp and roasting conditions were varied, as shown in table 4. From which the products E and F. were obtained.
- Table 5 shows the characteristics of the two products obtained with the process described in Example 2.
- Example 3 Process to obtain food products from ground coffee and ground coffee pulp
- the food product obtained was characterized by an average particle size of 300 mhi. a humidity percentage of 4.7%, a luminosity value of 16 L * and a caffeine content on a dry basis 0.93% (Product G).
- Table 8 shows the characteristics of the products obtained with the process described in Example 3.
- Example 4 Process to obtain food products from ground coffee and dry ground coffee pulp
- the food product obtained was characterized by an average particle size of 380 pm, a humidity percentage of 4.7%, a luminosity value of 23 L * and a caffeine content on a dry basis 1.07% (Product J) .
- the product Ki was prepared, in which the proportions of coffee, roasting and grinding conditions were varied, as shown in table 9.
- the product K2 was prepared, in which were varied proportions of coffee pulp and grinding conditions, as shown in table 10. From which the product K was obtained.
- Table 11 shows the characteristics of the products obtained with the process described in Example 4.
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Abstract
The invention provides a process for obtaining food products in the form of a powder to be reconstituted or an infused beverage, which comprises mixing coffee with coffee pulp, wherein the coffee is selected from green coffee, roasted coffee and ground coffee, and the coffee pulp is selected from dry coffee pulp, dry ground coffee pulp, roasted coffee pulp and ground coffee pulp. In particular, in the process of the invention, if the selected coffee is ground coffee, the coffee pulp is dry ground coffee pulp or ground coffee pulp; if the selected coffee is roasted coffee, the coffee pulp is roasted coffee pulp, and the obtained mixture is subjected to a step of grinding; and if the selected coffee is green coffee, the coffee pulp is dry coffee pulp, and the obtained mixture is subjected to a step of roasting and subsequently a step of grinding.
Description
PROCESO PARA OBTENER PRODUCTOS ALIMENTICIOS A PARTIR DE PROCESS TO OBTAIN FOOD PRODUCTS FROM
PULPA DE CAFÉ COFFEE PULP
CAMPO DE LA INVENCIÓN La presente invención está dirigida a un proceso para obtener productos alimenticios que comprende mezclar café con pulpa de café. Con el proceso de la invención se obtienen productos alimenticios en forma de polvo para reconstituir o bebida de infusión. FIELD OF THE INVENTION The present invention is directed to a process for obtaining food products that comprises mixing coffee with coffee pulp. With the process of the invention, food products are obtained in the form of a powder for reconstitution or an infusion drink.
DESCRIPCIÓN DEL ESTADO DE LA TÉCNICA Durante las diferentes etapas del cultivo de planta de café, se genera materiales como las hojas y ramas que en la renovación se quedan aportando materia orgánica al suelo, los tallos que generalmente son usados como leña o madera, la pulpa y mucílago producidos en el proceso de beneficio; la cascarilla generada en la etapa de trilla, y la borra o ripio generadas en la preparación de la bebida a partir del grano tostado y molido. Todo este material vegetal, si no se maneja y dispone de forma apropiada, se convierten en una fuente de contaminación. Particularmente, la pulpa de café es el residuo resultante más abundante y por caracterizarse por un alto contenido de materia orgánica normalmente es utilizado como abono para mejorar las condiciones químicas y físicas del suelo. Sin embargo, se estudian nuevas formas de aprovechar este material orgánico con fines nutricionales en productos alimenticios, fermentando la pulpa de café para obtener vinos o tratando la pulpa de café para obtener bebidas con cafeína. DESCRIPTION OF THE STATE OF THE TECHNIQUE During the different stages of coffee plant cultivation, materials such as leaves and branches are generated that in the renewal are left contributing organic matter to the soil, the stems that are generally used as firewood or wood, the pulp and mucilage produced in the beneficiation process; the husk generated in the threshing stage, and the waste or gravel generated in the preparation of the drink from the roasted and ground grain. All this plant material, if not handled and disposed of properly, becomes a source of contamination. In particular, coffee pulp is the most abundant resulting residue and because it is characterized by a high content of organic matter, it is normally used as fertilizer to improve the chemical and physical conditions of the soil. However, new ways of taking advantage of this organic material for nutritional purposes in food products are being studied, fermenting the coffee pulp to obtain wines or treating the coffee pulp to obtain caffeinated beverages.
Por ejemplo, la patente US7833560 se refiere a una bebida con cafeína que comprende un extracto que se deriva de cascara de café, pulpa de café y cereza de café y el método para producirlo. El proceso para obtener la bebida con cafeína comprende obtener un subproducto de la producción del café (p.e. cáscara de café, pulpa de café y cereza de café); preparar una mezcla de agua y con los subproductos de café para producir una mezcla compuesta de una porción líquida y una porción sólida; separar la porción líquida de la porción sólida para producir un extracto líquido; concentrar el extracto líquido para producir un extracto concentrado y entre mezclar el extracto concentrado con
componentes adicionales para obtener la bebida con cafeína. Particularmente la mezcla de agua y los subproductos de café se realiza a temperaturas entre 65 a 80°C y puede incluir una etapa adicional para reducir el tamaño y aumentar el área superficial de los sólidos y mejorar la extracción eficiente de las sustancias deseadas de los subproductos de café, esta molienda es preferiblemente realizada en húmedo por un periodo entre 15 a 30 minutos. For example, patent US7833560 refers to a caffeinated drink comprising an extract derived from coffee husk, coffee pulp and coffee cherry and the method for producing it. The process for obtaining the caffeinated beverage comprises obtaining a by-product of coffee production (eg coffee husk, coffee pulp and coffee cherry); preparing a mixture of water and the coffee by-products to produce a mixture composed of a liquid portion and a solid portion; separating the liquid portion from the solid portion to produce a liquid extract; concentrate the liquid extract to produce a concentrated extract and between mixing the concentrated extract with additional components to get the caffeinated drink. In particular the mixing of water and coffee by-products is carried out at temperatures between 65 to 80 ° C and may include an additional stage to reduce the size and increase the surface area of the solids and improve the efficient extraction of the desired substances from the by-products. of coffee, this grinding is preferably carried out wet for a period between 15 to 30 minutes.
Adicionalmente, la patente US7807205 describe un proceso para producir bebidas como té, jugos y bebidas carbonatadas a partir de un extracto de cereza de café. El proceso para obtener el extracto a partir de cereza de café inicia con la recolección de cerezas de café; secar por un periodo entre 0 a 48 horas hasta que el porcentaje de agua no sea superior al 20% (p/p) en las cerezas de café; extraer con un solvente acuosos en una relación 5: 1 a 20: 1 de solvente/cereza de café a una temperatura de 82 a 100°C por un periodo de 30 minutos a 2 horas; filtrar o centrifugar para separar sólidos y líquidos y obtener el extracto líquido que puede adicionalmente evaporarse para obtener el extracto solido de cereza de café. El proceso contempla una etapa adicional de molienda para mejorar el área de contacto antes de la extracción de manera que se obtienen partículas entre 0,1 a 5 mm. Additionally, patent US7807205 describes a process for producing beverages such as teas, juices and carbonated drinks from a coffee cherry extract. The process to obtain the extract from coffee cherry begins with the collection of coffee cherries; dry for a period between 0 to 48 hours until the percentage of water is not higher than 20% (w / w) in the coffee cherries; extract with an aqueous solvent in a ratio of 5: 1 to 20: 1 solvent / coffee cherry at a temperature of 82 to 100 ° C for a period of 30 minutes to 2 hours; filter or centrifuge to separate solids and liquids and obtain the liquid extract that can be further evaporated to obtain the solid extract of coffee cherry. The process contemplates an additional grinding stage to improve the contact area before extraction so that particles between 0.1 to 5 mm are obtained.
En los procesos empleados usualmente para aprovechar este material orgánico con fines nutricionales en productos alimenticios comprenden una extracción con agua caliente, que posteriormente se mezcla con aditivos y saborizantes para obtener el producto alimenticio. En la presente invención, se describe un proceso para obtener productos alimenticios en forma de polvo para reconstituir o bebida de infusión a partir de pulpa de café que comprende mezclar café con pulpa de café. In the processes usually used to take advantage of this organic material for nutritional purposes in food products, they comprise an extraction with hot water, which is subsequently mixed with additives and flavorings to obtain the food product. In the present invention, a process for obtaining food products in powder form for reconstitution or infusion beverage from coffee pulp is described which comprises mixing coffee with coffee pulp.
BREVE DESCRIPCIÓN DE LA INVENCIÓN La presente invención se refiere un proceso para obtener productos alimenticios a partir de pulpa de café que comprende mezclar café con pulpa de café, en donde el café se selecciona de café verde, café tostado y café molido; y la pulpa de café se selecciona de pulpa seca de café, pulpa de café tostada y pulpa de café molida. Particularmente, en el proceso de la presente invención si el café seleccionado es café molido, la pulpa de café es pulpa seca de café molida o pulpa de café molida; si el café seleccionado es café tostado, la pulpa de café es pulpa de café tostada; y la mezcla obtenida se somete a una etapa de molido; y si el café seleccionado es café verde, la pulpa de café es pulpa seca de
café; y la mezcla obtenida se somete a una etapa de tostado y posteriormente a una etapa de molido. Con el proceso de la invención se obtienen productos alimenticios caracterizados por una luminosidad entre 10 a 35 L*; humedad hasta 10%, pH entre 5 a 7 y un contenido de cafeína entre 0, 1. a 5%p/p. BRIEF DESCRIPTION OF THE INVENTION The present invention refers to a process for obtaining food products from coffee pulp that comprises mixing coffee with coffee pulp, wherein the coffee is selected from green coffee, roasted coffee and ground coffee; and the coffee pulp is selected from dry coffee pulp, roasted coffee pulp and ground coffee pulp. Particularly, in the process of the present invention, if the selected coffee is ground coffee, the coffee pulp is dry ground coffee pulp or ground coffee pulp; if the selected coffee is roasted coffee, the coffee pulp is roasted coffee pulp; and the mixture obtained is subjected to a grinding step; and if the selected coffee is green coffee, the coffee pulp is dry pulp of coffee; and the mixture obtained is subjected to a roasting stage and subsequently to a grinding stage. With the process of the invention, food products are obtained characterized by a luminosity between 10 to 35 L *; humidity up to 10%, pH between 5 to 7 and a caffeine content between 0.1 to 5% w / w.
BREVE DESCRIPCIÓN DE LAS FIGURAS BRIEF DESCRIPTION OF THE FIGURES
FIG. 1 Diagrama de flujo del proceso para obtener productos alimenticios a partir de café verde y pulpa seca de café. FIG.2 Diagrama de flujo del proceso para obtener productos alimenticios a partir a partir de café tostado y pulpa de café tostada. FIG. 1 Flow chart of the process to obtain food products from green coffee and dry coffee pulp. FIG.2 Flow chart of the process to obtain food products from roasted coffee and roasted coffee pulp.
FIG. 3 Diagrama de flujo del proceso para obtener productos alimenticios a partir de café molido y pulpa de café molida. FIG. 3 Flow chart of the process to obtain food products from ground coffee and ground coffee pulp.
FIG. 4 Diagrama de flujo del proceso para obtener productos alimenticios a partir de café molido y pulpa seca de café molida. FIG. 4 Flow diagram of the process to obtain food products from ground coffee and dry ground coffee pulp.
DESCRIPCIÓN DETALLADA La presente invención corresponde a un proceso para obtener productos alimenticios a partir de pulpa de café que comprende mezclar café entre 99% y 1% con pulpa de café entre 1% y 99%., en donde el café se selecciona de café verde, café tostado y café tostado y molido; y la pulpa de café se selecciona de pulpa seca de café, pulpa seca de café molida, pulpa de café tostada y pulpa de café molida. Para efectos de la presente invención, el término“café” se refiere a la semilla que se extrae de los frutos de la planta de café (cereza de café) como resultado del proceso de beneficio en húmedo y el término“ pulpa de café” se refiere a un material fibroso o cascará que se genera durante el procesamiento del café. DETAILED DESCRIPTION The present invention corresponds to a process to obtain food products from coffee pulp that comprises mixing coffee between 99% and 1% with coffee pulp between 1% and 99%, where the coffee is selected from green coffee , roast coffee and roast and ground coffee; and the coffee pulp is selected from dry coffee pulp, dry ground coffee pulp, roasted coffee pulp and ground coffee pulp. For the purposes of the present invention, the term "coffee" refers to the seed that is extracted from the fruits of the coffee plant (coffee cherry) as a result of the wet milling process and the term "coffee pulp" is refers to a fibrous material or husk that is generated during the processing of coffee.
Específicamente, en el proceso de la presente invención si el café seleccionado es café verde, la pulpa de café es pulpa seca de café; y la mezcla obtenida se somete a una etapa de tostado que se realiza mediante calor por convección, conducción o radiación a temperaturas entre 130 a 250 °C por un periodo entre 2 a 30 minutos en un tostador seleccionado de tostadores tipo tambor, tambor perforado, continuo, centrífugo, lecho
fluidizado, entre otros y posteriormente a una etapa de molido hasta un tamaño de partícula promedio entre 20 a 5000 mieras, 50 a 4500 mieras, 200 a 3500 mieras, 400 a 3000 mieras, 600 a 2500 mieras, 800 a 1500 mieras y 900 a 1000 mieras en un molino seleccionado de: molino tipo masas, molino de discos, molino centrífugo, entre otros. Specifically, in the process of the present invention, if the selected coffee is green coffee, the coffee pulp is dry coffee pulp; and the mixture obtained is subjected to a roasting stage that is carried out by means of heat by convection, conduction or radiation at temperatures between 130 to 250 ° C for a period between 2 to 30 minutes in a roaster selected from drum type roasters, perforated drum, continuous, centrifugal, bed fluidized, among others and subsequently to a grinding stage to an average particle size between 20 to 5000 microns, 50 to 4500 microns, 200 to 3500 microns, 400 to 3000 microns, 600 to 2500 microns, 800 to 1500 microns and 900 to 1000 microns in a mill selected from: mass type mill, disc mill, centrifugal mill, among others.
Para efectos de la presente invención, el término “café verde” se refiere a la semilla extraída de los frutos de la planta de café después del proceso de beneficio en húmedo que no ha sido ni tostado ni molido. El café verde se encuentra en la mezcla en una concentración entre 1% a 99%, 10% a 90%, 20% a 80%, 30% a 70%, 40% a 60% y 50% a 55%. Por otro lado, el término “pulpa seca de café” se refiere al material fibroso mucilaginoso que se seca hasta un porcentaje de humedad entre 4% a 12%. La pulpa seca de café se encuentra en la mezcla en una concentración entre 1% a 99%, 10% a 90%, 20% a 80%, 30% a 70%, 40% a 60% y 50% a 55% For the purposes of the present invention, the term "green coffee" refers to the seed extracted from the fruits of the coffee plant after the wet beneficiation process that has not been roasted or ground. Green coffee is found in the mixture in a concentration between 1% to 99%, 10% to 90%, 20% to 80%, 30% to 70%, 40% to 60% and 50% to 55%. On the other hand, the term "dry coffee pulp" refers to the mucilaginous fibrous material that dries to a moisture content between 4% to 12%. The dry coffee pulp is found in the mixture in a concentration between 1% to 99%, 10% to 90%, 20% to 80%, 30% to 70%, 40% to 60% and 50% to 55%.
Particularmente, en el proceso de la presente invención si el café seleccionado es café tostado, la pulpa de café es pulpa de café tostada; y la mezcla obtenida se somete a una etapa de molido hasta un tamaño de partícula promedio entre 20 a 5000 mieras, 50 a 4500 mieras, 200 a 3500 mieras, 400 a 3000 mieras, 600 a 2500 mieras, 800 a 1500 mieras y 900 a 1000 mieras en un molino seleccionado de: molino tipo masas, molino de discos, molino centrífugo, entre otros. Particularly, in the process of the present invention, if the selected coffee is roasted coffee, the coffee pulp is roasted coffee pulp; and the mixture obtained is subjected to a grinding stage to an average particle size between 20 to 5000 microns, 50 to 4500 microns, 200 to 3500 microns, 400 to 3000 microns, 600 to 2500 microns, 800 to 1500 microns and 900 to 1000 microns in a mill selected from: mass type mill, disc mill, centrifugal mill, among others.
Para efectos de la presente invención, el término“ café tostado” se refiere a la semilla extraída de los frutos de la planta de café después del proceso de beneficio en húmedo que se tuesta mediante calor por convección, conducción o radiación a temperaturas entre 130 a 250 °C por un periodo entre 2 a 30 minutos en un tostador seleccionado de tostadores tipo tambor, tambor perforado, continuo, centrífugo, lecho fluidizado, entre otros. El café tostado se encuentra en la mezcla en una concentración entre 1% a 99%, 10% a 90%, 20% a 80%, 30% a 70%, 40% a 60% y 50% a 55%. For the purposes of the present invention, the term "roasted coffee" refers to the seed extracted from the fruits of the coffee plant after the wet beneficiation process that is roasted by means of heat by convection, conduction or radiation at temperatures between 130 to 250 ° C for a period between 2 to 30 minutes in a roaster selected from drum, perforated drum, continuous, centrifugal, fluidized bed roasters, among others. Roasted coffee is found in the mixture in a concentration between 1% to 99%, 10% to 90%, 20% to 80%, 30% to 70%, 40% to 60% and 50% to 55%.
Por otro lado, el término“ pulpa de café tostada” se refiere a la pulpa seca que se somete a una etapa de tostado mediante calor por convección, conducción o radiación a temperaturas entre 130 a 250 °C por un periodo entre 2 a 30 minutos en un tostador seleccionado de tostadores tipo tambor, tambor perforado, continuo, centrífugo, lecho fluidizado, entre otros. La pulpa de café tostada en la mezcla se encuentra en una
concentración entre 1% a 99%, 10% a 90%, 20% a 80%, 30% a 70%, 40% a 60% y 50% a 55%. On the other hand, the term "roasted coffee pulp" refers to the dry pulp that is subjected to a roasting stage by means of heat by convection, conduction or radiation at temperatures between 130 to 250 ° C for a period between 2 to 30 minutes. in a roaster selected from drum, perforated drum, continuous, centrifugal, fluidized bed roasters, among others. The roasted coffee pulp in the mixture is in a concentration between 1% to 99%, 10% to 90%, 20% to 80%, 30% to 70%, 40% to 60% and 50% to 55%.
Específicamente, en el proceso de la presente invención si el café seleccionado es café molido, la pulpa de café es pulpa seca de café molida o pulpa de café molida. Para efectos de la presente invención, el término“café molido” se refiere al café tostado que es molido hasta un tamaño de partícula promedio entre 20 a 5000 mieras, 50 a 4500 mieras, 200 a 3500 mieras, 400 a 3000 mieras, 600 a 2500 mieras, 800 a 1500 mieras y 900 a 1000 mieras en un molino seleccionado de: molino tipo masas, molino de discos, molino centrífugo, entre otros. El café molido se encuentra en la mezcla en una concentración entre 1% a 99%, 10% a 90%, 20% a 80%, 30% a 70%, 40% a 60% y 50% a 55%. Specifically, in the process of the present invention if the selected coffee is ground coffee, the coffee pulp is dry ground coffee pulp or ground coffee pulp. For purposes of the present invention, the term "ground coffee" refers to roasted coffee that is ground to an average particle size between 20 to 5000 microns, 50 to 4500 microns, 200 to 3500 microns, 400 to 3000 microns, 600 to 2500 microns, 800 to 1500 microns and 900 to 1000 microns in a mill selected from: mass type mill, disk mill, centrifugal mill, among others. The ground coffee is found in the mixture in a concentration between 1% to 99%, 10% to 90%, 20% to 80%, 30% to 70%, 40% to 60% and 50% to 55%.
Por otro lado, el término“ pulpa seca de café molida” se refiere a pulpa seca de café con un porcentaje de humedad entre 4% a 12% que es molida hasta un tamaño de partícula promedio entre 20 a 5000 mieras, 50 a 4500 mieras, 200 a 3500 mieras, 400 a 3000 mieras, 600 a 2500 mieras, 800 a 1500 mieras y 900 a 1000 mieras en un molino seleccionado de: molino tipo masas, molino de discos, molino centrífugo, entre otros. La pulpa seca de café molida se encuentra en la mezcla en una concentración entre 1% a 99%, 10% a 90%, 20% a 80%, 30% a 70%, 40% a 60% y 50% a 55%. On the other hand, the term "dry ground coffee pulp" refers to dry coffee pulp with a humidity percentage between 4% to 12% that is ground to an average particle size between 20 to 5000 microns, 50 to 4500 microns. , 200 to 3,500 microns, 400 to 3,000 microns, 600 to 2,500 microns, 800 to 1,500 microns and 900 to 1,000 microns in a mill selected from: mass type mill, disk mill, centrifugal mill, among others. The dry ground coffee pulp is found in the mixture in a concentration between 1% to 99%, 10% to 90%, 20% to 80%, 30% to 70%, 40% to 60% and 50% to 55%. .
Por otra parte, el término“pulpa de café molida” se refiere a la pulpa de café tostada que es molida hasta un tamaño de partícula promedio entre 20 a 5000 mieras, 50 a 4500 mieras, 200 a 3500 mieras, 400 a 3000 mieras, 600 a 2500 mieras, 800 a 1500 mieras y 900 a 1000 mieras en un molino seleccionado de: molino tipo masas, molino de discos, molino centrífugo, entre otros. La pulpa de café molida se encuentra en la mezcla en una concentración entre 1% a 99%, 10% a 90%, 20% a 80%, 30% a 70%, 40% a 60% y 50% a 55%. On the other hand, the term “ground coffee pulp” refers to roasted coffee pulp that is ground to an average particle size between 20 to 5000 microns, 50 to 4500 microns, 200 to 3500 microns, 400 to 3000 microns, 600 to 2500 microns, 800 to 1500 microns and 900 to 1000 microns in a mill selected from: mass type mill, disk mill, centrifugal mill, among others. The ground coffee pulp is found in the mixture in a concentration between 1% to 99%, 10% to 90%, 20% to 80%, 30% to 70%, 40% to 60% and 50% to 55%.
Con el proceso de la presente invención se obtienen productos alimenticios en forma de polvo para reconstituir o bebida de infusión caracterizados por una luminosidad entre 10 a 35 L*; humedad hasta 10%, pH entre 5 a 7 y un contenido de cafeína entre 0,1 a 5%p/p. With the process of the present invention, food products are obtained in the form of powder to reconstitute or infusion drink characterized by a luminosity between 10 to 35 L *; humidity up to 10%, pH between 5 to 7 and a caffeine content between 0.1 to 5% w / w.
La presente invención será presentada en detalle a través de los siguientes ejemplos, los cuales son suministrados solamente con propósitos ilustrativos y no con el objetivo de limitar su alcance.
EJEMPLOS The present invention will be presented in detail through the following examples, which are provided for illustrative purposes only and not with the aim of limiting its scope. EXAMPLES
Ejemplo 1. Proceso para obtener productos alimenticios a partir de café verde y Example 1. Process to obtain food products from green coffee and
pulpa seca de café dried coffee pulp
Se mezclaron 120 kg de café verde con un porcentaje de humedad de 11,32% humedad y 80 Kg de pulpa seca de café con un porcentaje de humedad de 10,64% y la mezcla obtenida se alimentó a un tostador tipo tambor perforado operado en una curva de temperatura de 180°C hasta 200°C por un periodo de 12 minutos. El producto obtenido de la etapa de tostado, se llevó a un molino de discos hasta obtener un producto alimenticio en forma de polvo para reconstituir o bebida de infusión (Producto A). A partir de café verde y pulpa seca de café, y siguiendo el mismo procedimiento descrito anteriormente (FIG. 1), se prepararon los productos B y C, variando las proporciones de café verde y pulpa seca de café, las condiciones de tiempo y temperatura en la etapa de tostar, como se muestra en la Tabla 1. 120 kg of green coffee with a humidity percentage of 11.32% humidity and 80 Kg of dry coffee pulp with a humidity percentage of 10.64% were mixed and the mixture obtained was fed to a perforated drum type roaster operated in a temperature curve from 180 ° C to 200 ° C for a period of 12 minutes. The product obtained from the roasting stage was taken to a disk mill to obtain a food product in powder form to reconstitute or infusion drink (Product A). From green coffee and dry coffee pulp, and following the same procedure described above (FIG. 1), products B and C were prepared, varying the proportions of green coffee and dry coffee pulp, the conditions of time and temperature. in the roasting stage, as shown in Table 1.
Tabla 1. Table 1.
En la Tabla 2 se muestran las características de los dos productos obtenidos con el proceso descrito en el Ejemplo 1. Table 2 shows the characteristics of the two products obtained with the process described in Example 1.
Tabla 2. Table 2.
Ejemplo 2. Proceso para obtener productos alimenticios a partir de café tostado y pulpa de café tostada Example 2. Process to obtain food products from roasted coffee and roasted coffee pulp
Se pesaron 160kg de café tostado descafeinado caracterizado por un contenido de cafeína base seca de 0,11% y porcentaje de humedad de 11,08%, que previamente se había sometido a una etapa de tostado en un tostador centrífugo de platón operado en una curva de temperatura de 200°C a 202°C durante 10 minutos (Producto DI). Paralelamente se pesaron 160Kg de pulpa seca de café con un porcentaje de humedad de 10,5% y se adicionaron a un tostador tipo tambor perforado operado en una curva de temperatura de 130°C hasta 178°C por un periodo de 8 minutos, para obtener una pulpa de café tostada que se descargó en una criba de enfriamiento hasta que alcanzo una temperatura de 30°C (Producto D2). 160kg of decaffeinated roasted coffee were weighed characterized by a dry base caffeine content of 0.11% and a moisture percentage of 11.08%, which had previously been subjected to a roasting stage in a plate centrifugal roaster operated on a curve. 200 ° C to 202 ° C for 10 minutes (Product DI). At the same time, 160Kg of dry coffee pulp with a humidity percentage of 10.5% were weighed and added to a perforated drum type roaster operated at a temperature curve of 130 ° C to 178 ° C for a period of 8 minutes, to Obtain a roasted coffee pulp that was discharged on a cooling sieve until it reached a temperature of 30 ° C (Product D2).
Posteriormente, se mezclaron lOOKg pulpa de café tostada junto con 100kg de café tostado en un mezclador de cintas durante 5 minutos. Seguidamente, la mezcla obtenida se llevó a un molino tipo masas hasta obtener un producto alimenticio caracterizado por un tamaño de partícula promedio de 450pm, un valor de luminosidad de 19,69 L*, un porcentaje de humedad de 4,5% y un contenido de cafeína en base seca 0,45% (Producto D). Subsequently, LOOKg roasted coffee pulp was mixed together with 100kg of roasted coffee in a ribbon mixer for 5 minutes. Next, the mixture obtained was taken to a mass type mill until obtaining a food product characterized by an average particle size of 450pm, a luminosity value of 19.69 L *, a humidity percentage of 4.5% and a content 0.45% dry caffeine (Product D).
Siguiendo el mismo procedimiento descrito anteriormente (FIG. 2), se prepararon los productos Ei y Fi, en los cuales se variaron las cantidades de café y condiciones de tostión, como se muestra en la tabla 3. De igual forma se prepararon los productos E2 y F2 en los cuales se variaron proporciones de pulpa de café y condiciones de tostión, como se muestra en la tabla 4. A partir de los cuales se obtuvieron los productos E y F. Following the same procedure described above (FIG. 2), the products Ei and Fi were prepared, in which the amounts of coffee and roasting conditions were varied, as shown in table 3. In the same way, the products E2 were prepared and F2 in which proportions of coffee pulp and roasting conditions were varied, as shown in table 4. From which the products E and F. were obtained.
Tabla 4. Table 4.
En la Tabla 5 se muestran las características de los dos productos obtenidos con el proceso descrito en el Ejemplo 2. Table 5 shows the characteristics of the two products obtained with the process described in Example 2.
Tabla 5. Table 5.
Ejemplo 3. Proceso para obtener productos alimenticios a partir de café molido y pulpa de café molida Example 3. Process to obtain food products from ground coffee and ground coffee pulp
Se pesaron 200Kg de café verde con un porcentaje de humedad de 10,99% y se adicionaron a un tostador tipo tambor operado en una temperatura hasta 203 °C por un periodo de 11 minutos. El café tostado obtenido se llevó a un molino de discos hasta obtener un café molido (Producto Gi) con un tamaño de partícula de 350 mih . Paralelamente, 250Kg de pulpa seca de café con un porcentaje de humedad de 9,78% y se adicionaron a un tostador tipo tambor perforado operado a una curva de temperatura entre 150°C a 191°C por un periodo de 6 minutos, para obtener una pulpa de café tostada, que se llevó a un molino de masas hasta obtener pulpa de café molida con tamaño de partícula de 220 pm (Producto G2). 200Kg of green coffee with a humidity percentage of 10.99% were weighed and added to a drum type roaster operated at a temperature up to 203 ° C for a period of 11 minutes. The roasted coffee obtained was taken to a disk mill until obtaining ground coffee (Product Gi) with a particle size of 350 mih. In parallel, 250Kg of dry coffee pulp with a humidity percentage of 9.78% and were added to a perforated drum type roaster operated at a temperature curve between 150 ° C to 191 ° C for a period of 6 minutes, to obtain a roasted coffee pulp, which was taken to a mass mill to obtain ground coffee pulp with a particle size of 220 pm (Product G 2 ).
Finalmente, se mezclaron 75kg de café molido y 25kg de pulpa de café molida en un mezclador tipo cintas durante 3 minutos para obtener el producto alimenticio. El producto alimenticio obtenido se caracterizó por un tamaño de partícula promedio de 300 mhi. un porcentaje de humedad de 4,7%, un valor de luminosidad de 16 L*y un contenido de cafeína en base seca 0,93% (Producto G). Finally, 75kg of ground coffee and 25kg of ground coffee pulp were mixed in a belt type mixer for 3 minutes to obtain the food product. The food product obtained was characterized by an average particle size of 300 mhi. a humidity percentage of 4.7%, a luminosity value of 16 L * and a caffeine content on a dry basis 0.93% (Product G).
Siguiendo el mismo procedimiento descrito anteriormente (FIG. 3), se prepararon los productos Hi y Ii, en los cuales se variaron proporciones de café, condiciones de tostión y molienda, como se muestra en la tabla 6. De igual forma se prepararon los productos Eh y h en los cuales se variaron proporciones de pulpa de café, condiciones de tostión y molienda, como se muestra en la tabla 7. A partir de los cuales se obtuvieron los productos H y E Following the same procedure described above (FIG. 3), the Hi and Ii products were prepared, in which the proportions of coffee, roasting and grinding conditions were varied, as shown in table 6. In the same way, the products were prepared. Eh and h in which proportions of coffee pulp, roasting and grinding conditions were varied, as shown in table 7. From which products H and E were obtained
Tabla 6. Table 6.
Tabla 7. Table 7.
En la Tabla 8 se muestran las características de los productos obtenidos con el proceso descrito en el Ejemplo 3. Table 8 shows the characteristics of the products obtained with the process described in Example 3.
Tabla 8. Table 8.
Ejemplo 4. Proceso para obtener productos alimenticios a partir de café molido y pulpa seca de café molida Example 4. Process to obtain food products from ground coffee and dry ground coffee pulp
Se pesaron 400Kg de café verde con un porcentaje de humedad de 11,38% y se adicionaron a un tostador tipo centrífugo operado en una temperatura entre 180 a 210°C por un periodo de 12 minutos. El café tostado obtenido se llevó a un molino tipo masas hasta obtener un café molido (Producto Ji) con un tamaño de partícula de 450 mih . Paralelamente, 150Kg de pulpa seca de café con un porcentaje de humedad del 5% se llevaron a un molino de discos hasta obtener pulpa seca de café molida con tamaño de partícula de 320 pm (Producto J2). Finalmente, se mezclaron 170kg de café molido y 30kg de pulpa seca de café molida en un mezclador tipo cintas durante 4 minutos para obtener el producto alimenticio. El producto alimenticio obtenido se caracterizó por un tamaño de partícula promedio de 380 pm, un porcentaje de humedad de 4,7%, un valor de luminosidad de 23 L*y un contenido de cafeína en base seca 1,07% (Producto J). Siguiendo el mismo procedimiento descrito anteriormente (FIG. 4), se preparó el producto Ki, en el cual se variaron proporciones de café, condiciones de tostión y molienda, como se muestra en la tabla 9. De igual forma preparó el producto K2, en el cuales se variaron proporciones de pulpa de café y condiciones de molienda, como se muestra en la tabla 10. A partir de los cuales se obtuvo el producto K. 400Kg of green coffee with a humidity percentage of 11.38% were weighed and added to a centrifugal type roaster operated at a temperature between 180 to 210 ° C for a period of 12 minutes. The roasted coffee obtained was taken to a mass-type mill until obtaining ground coffee (Product Ji) with a particle size of 450 mih. At the same time, 150Kg of dry coffee pulp with a humidity percentage of 5% were taken to a disk mill to obtain dry ground coffee pulp with a particle size of 320 pm (Product J2). Finally, 170kg of ground coffee and 30kg of dry ground coffee pulp were mixed in a belt mixer for 4 minutes to obtain the food product. The food product obtained was characterized by an average particle size of 380 pm, a humidity percentage of 4.7%, a luminosity value of 23 L * and a caffeine content on a dry basis 1.07% (Product J) . Following the same procedure described above (FIG. 4), the product Ki was prepared, in which the proportions of coffee, roasting and grinding conditions were varied, as shown in table 9. In the same way, the product K2 was prepared, in which were varied proportions of coffee pulp and grinding conditions, as shown in table 10. From which the product K was obtained.
Tabla 9 Table 9
En la Tabla 11 se muestran las características de los productos obtenidos con el proceso descrito en el Ejemplo 4. Table 11 shows the characteristics of the products obtained with the process described in Example 4.
Tabla 11. Table 11.
Claims
1. Un proceso para obtener productos alimenticios a partir de pulpa de café que comprende mezclar café con pulpa de café; A process for obtaining food products from coffee pulp comprising mixing coffee with coffee pulp;
en donde: where:
el café se selecciona de café verde, café tostado y café molido; y coffee is selected from green coffee, roasted coffee, and ground coffee; and
la pulpa de café se selecciona de pulpa seca de café, pulpa seca de café molida, pulpa de café tostada y pulpa de café molida; the coffee pulp is selected from dry coffee pulp, dry ground coffee pulp, roasted coffee pulp and ground coffee pulp;
y en donde: and where:
si el café seleccionado es café molido, la pulpa de café es pulpa seca de café molida o pulpa de café molida; if the selected coffee is ground coffee, the coffee pulp is dry ground coffee pulp or ground coffee pulp;
si el café seleccionado es café tostado, la pulpa de café es pulpa de café tostada; y la mezcla obtenida se somete a una etapa de molido; if the selected coffee is roasted coffee, the coffee pulp is roasted coffee pulp; and the mixture obtained is subjected to a grinding step;
si el café seleccionado es café verde, la pulpa de café es pulpa seca de café; y la mezcla obtenida se somete a una etapa de tostado y posteriormente a una etapa de molido. if the selected coffee is green coffee, the coffee pulp is dry coffee pulp; and the mixture obtained is subjected to a roasting stage and subsequently to a grinding stage.
2. El proceso de acuerdo con la Reivindicación 1, en donde la mezcla contiene pulpa de café entre 1% y 99% y café entre 99% y 1%. 2. The process according to Claim 1, wherein the mixture contains coffee pulp between 1% and 99% and coffee between 99% and 1%.
3. El proceso de acuerdo a la Reivindicación 1, en donde con la etapa de molido se reduce el tamaño de partícula entre 20 a 5000 mieras. 3. The process according to Claim 1, wherein with the grinding step the particle size is reduced between 20 to 5000 microns.
4. El proceso de acuerdo con la Reivindicación 1, en donde la etapa de molido se realiza en una máquina seleccionada de molino de masas, molino de discos, molino martillo, molino de bolas y centrífugo, entre otros. 4. The process according to Claim 1, wherein the milling step is carried out in a machine selected from a mass mill, a disk mill, a hammer mill, a ball mill and a centrifuge, among others.
5. El proceso de acuerdo con la Reivindicación 1, en donde la etapa de tostado es mediante calor por convección, conducción o radiación. 5. The process according to Claim 1, wherein the roasting step is by convection, conduction or radiation heat.
6. El proceso de acuerdo con la Reivindicación 1, en donde la etapa de tostado se realiza a temperaturas entre 130 a 250 °C por un periodo entre 2 a 30 minutos
6. The process according to Claim 1, wherein the roasting step is carried out at temperatures between 130 to 250 ° C for a period between 2 to 30 minutes.
7. El proceso de acuerdo con la Reivindicación 1, en donde la etapa de tostado se realiza en una maquina seleccionada de tostadores tipo tambor, tambor perforado, continuo, centrífugo, lecho fluidizado, entre otros. 7. The process according to Claim 1, wherein the roasting step is carried out in a machine selected from drum type roasters, perforated drum, continuous, centrifugal, fluidized bed, among others.
8. El proceso de acuerdo con la Reivindicación 1, en donde el producto alimenticio obtenido se caracteriza por una luminosidad entre 10 a 35 L*; humedad hasta 10%, pH entre 5 a 7 y un contenido de cafeína entre 0,1 a 5%p/p. 8. The process according to Claim 1, wherein the obtained food product is characterized by a luminosity between 10 to 35 L *; humidity up to 10%, pH between 5 to 7 and a caffeine content between 0.1 to 5% w / w.
9. El proceso de acuerdo con la Reivindicación 1 a 8, en donde el producto alimenticio obtenido está en forma de polvo para reconstituir o bebida de infusión.
The process according to Claim 1 to 8, wherein the food product obtained is in the form of a powder for reconstitution or infusion drink.
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WO2024112706A3 (en) * | 2022-11-23 | 2024-07-18 | Smith Anderson Ventures Llc | Coffee cascara food product |
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WO2005072535A1 (en) * | 2004-01-28 | 2005-08-11 | Gilvaria Oy | Coffee composition and method of making the same |
WO2015013199A1 (en) * | 2013-07-23 | 2015-01-29 | Edward Hirschberg | Coffee fruit products and processing |
JP2017006094A (en) * | 2015-06-26 | 2017-01-12 | 株式会社珈琲研究所 | Roasted coffee beans rich in chlorogenic acid amount, and process for preparing the same |
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WO2005072535A1 (en) * | 2004-01-28 | 2005-08-11 | Gilvaria Oy | Coffee composition and method of making the same |
WO2015013199A1 (en) * | 2013-07-23 | 2015-01-29 | Edward Hirschberg | Coffee fruit products and processing |
JP2017006094A (en) * | 2015-06-26 | 2017-01-12 | 株式会社珈琲研究所 | Roasted coffee beans rich in chlorogenic acid amount, and process for preparing the same |
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WO2024112706A3 (en) * | 2022-11-23 | 2024-07-18 | Smith Anderson Ventures Llc | Coffee cascara food product |
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