WO2017209590A1 - A plant biomass mixture, phyto-removal product and method for removing toxic components from foodstuffs - Google Patents

A plant biomass mixture, phyto-removal product and method for removing toxic components from foodstuffs Download PDF

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Publication number
WO2017209590A1
WO2017209590A1 PCT/MX2016/000054 MX2016000054W WO2017209590A1 WO 2017209590 A1 WO2017209590 A1 WO 2017209590A1 MX 2016000054 W MX2016000054 W MX 2016000054W WO 2017209590 A1 WO2017209590 A1 WO 2017209590A1
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mixture
phyto
family
food products
fruit
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PCT/MX2016/000054
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Spanish (es)
French (fr)
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Ruth Araceli DE CELIS CARRILLO
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De Celis Carrillo Ruth Araceli
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    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, 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
    • A23L5/00Preparation or treatment of foods or foodstuffs, in general; Food or foodstuffs obtained thereby; Materials therefor
    • A23L5/20Removal of unwanted matter, e.g. deodorisation or detoxification

Definitions

  • the present invention relates to the technical field of Biotechnology and the food industry, because it provides a mixture of plant biomass, a fitoremovedor product, and a method, to remove toxic elements from food, for humans and animals.
  • Wastewater may contain Arsenic, Mercury, Nickel, Lead, Copper, Zinc, Chrome and Aluminum, because they are frequently used in the electronics, automotive, mining, food, pharmaceutical, cosmetics, textiles and leather goods.
  • the methods used to remove metals from wastewater are chemical precipitation, coagulation, solvent extraction, electrolysis, membrane separation, ion exchange and adsorption. Most of these methods used require a large investment, equipment and training to perform them.
  • One of the first objects of the present invention is to provide a mixture of plant biomass to remove toxic elements from food products.
  • the main toxic elements to be removed are: Arsenic (As) which is the element commonly found on the surfaces of food products, Boron (B), Nickel (Ni), Lead (Pb) and pesticide residues.
  • So food products can be mainly agricultural products, but not limited to, grains, seeds, fruits, strawberries, plant tissues, among others.
  • Said mixture of vegetable biomass is made up of a powdered extract of the dried peel of the fruit of a member of the Rosaceae family; and a powdered extract of the seeds of the fruit of a member of the Annonaceae family.
  • the member of the Rosaceae family is of the genus Pyrus; more specifically of the species Pyrus malus; and more preferably of the "Golden Delicious" variety.
  • a variant of the vegetable biomass mixture in question is when the member of the Annonaceae family is of the Annona genus; being more specifically of the species Annona muricata.
  • a preferred embodiment of the vegetable biomass mixture of the present invention is when the particle size of the dried extract of the dried peel of the fruit of the member of the Rosaceae family is 0.15 to 0.20 mm in diameter; and the particle size of the dried extract of dried seeds of the fruit of the member of the family of the Annonaceae, is from 0.20 to 2.50 mm in diameter.
  • Another preferred embodiment of the vegetable biomass mixture in question is that it also comprises a third powdered extract of the dried peel of the fruit of a member of the Solanaceae family; being more specifically of the Lycopersicon genus; preferably of the species Lycopersicon esculentum; and more preferred of the variety "Saladett".
  • Another embodiment of the mixture according to the present invention is when the particle size of the dried extract of the dried peel of the fruit of the Solanaceae family member is 0.05 to 1.50 mm in diameter.
  • a further object of the present invention is to provide a product that we call as a phytoremovedor, to remove, capture, eliminate, etc., the toxic elements found in food products.
  • Said fitoremovedor product is characterized by comprising a mixture of plant biomass, in accordance with the mixtures of plant biomass of the present invention; and a container made of a porous material contains in its interior the mixture of vegetable biomass.
  • Said porous material may be paper, silk, nylon, to name a few examples; where the pores of the material must be of sufficient size to allow a perfect interaction between the components of the mixture of vegetable biomass and the toxic elements that contaminate food products; or put another way, to allow a complete bioadsorption of toxic elements.
  • An example of the container of the vegetable biomass mixture can be a bag, sachet, sack, envelope, bag, etc. It should also be noted that said container of the vegetable biomass mixture must be closed or sealed in some conventional manner and may optionally carry a fastening means, such as a thread, rope, etc., for easy handling during use; as if it were a conventional tea bag.
  • a further embodiment of the phyto-moving product of the preceding claim it can be that said phyto-moving product is in a ratio of 1 part of vegetable biomass mixture to 33.33 parts of food product, to which the toxic elements will be removed.
  • the food products that can be treated with this phyto-stirring product, they can be grains, fruits, strawberries, seeds or any other plant tissue that could be cleaned of its toxic contaminants by means of the present invention.
  • a further object of the present invention is a method for removing toxic elements from food products, by using the phyto-moving product described in this invention, whereby said method comprises the following steps: i) placing the food products in water, in a ratio of 28.56: 71.43;
  • An embodiment of the present method is to leave the phytoremovedor product submerged in water for 2 h, which is when the highest degree of saturation of toxic elements is achieved.
  • One modality of the method in question is to use a ratio, mixture of plant biomass: food product (1: 33.33).
  • a further variant of said method according to the present invention is when a container of the vegetable biomass mixture, made of a porous material, is used. such as paper, silk, nylon, etc .; where the porosity must have a size that allows a perfect interaction between the ingredients of the mixture in question, with the toxic elements.
  • the container can be a bag, sachet, envelope, bag, and the like. It should be noted that said container must be closed or sealed in a conventional manner and may optionally have a fastening means, such as a thread, rope, etc., for easy handling during use; as if it were a conventional tea bag.
  • This example illustrates one of the embodiments of the present invention.
  • Apple, tomato and soursop fruits, firm, ripe, of good quality, clean, free of external damage, chemical agents and pests were used. All the fruits that were used were cultivated and collected in different states of Mexico, considering first, the largest producers of each species of fruit. From the JRosaceae family, yellow apples [Pyrus malus, variety "Golden delicious") were used, obtained from the states of Chihuahua and Durango. The apples obtained the peels and underwent a process of dehydration in a hot air oven at 60 ° C (Waring Pro DHR30 Food Dehydrator), for 10 continuous hours.
  • Soursop [Annona muricata) were used, which were obtained from the states of Colima and Guerrero. From these soursop the seeds were extracted, which were subjected to a cleaning process of pulp residues of the fruit and allowed to dry in the open air at room temperature. Subsequently, the seeds were crushed in a manual grain mill and already crushed they were subjected to dehydration in a hot air oven at 60 ° C (Waring Pro DHR30 Food Dehydrator), for 4 continuous hours. At the end of the drying process, an elementary analysis of the biomass and it was obtained that crushed soursop seeds recorded 4.90% moisture and 1.18% ash. Soursop seed fragments were between 0.2 and 2.5 mm in diameter on average.
  • Treatment 1 2 g of powdered extract of apple peels, in a filter paper envelope.
  • Treatment 2 2 g of powdered extract of tomato peels, in a filter paper envelope.
  • Treatment 3 2g of soursop seed powder extract, in a filter paper envelope.
  • Treatment 4 a mixture of 2 g of powdered extract of tomato peels and 2 g of powdered extract of soursop seeds, in a filter paper envelope.
  • Treatment 5 a mixture of 2 g of apple peel powder extract and 2 g of tomato peel powder extract, in a filter paper envelope.
  • Treatment 6 a mixture of 2 g of apple peel extract powder and 2 g of soursop seed powder extract, in a filter paper envelope.
  • Treatment 7 A mixture of 2 g of powdered extract of apple peels, 2 g of powdered extract of tomato peels and 2 g of powdered extract is soursop seeds, in a filter paper envelope.
  • Adsorption Solutions To test the different treatments described above, it was chosen to prepare an aqueous solution of Arsenic (As) (analytical grade), based on the fact that it is the toxic element mostly found in edible grains, due to contamination of irrigation water and because it is an element that is used in the formulation of many pesticides used in food production. In all our previous analyzes of edible grains, Ace has been present in greater or lesser concentration.
  • Arsenic Arsenic
  • said aqueous solution of As it also contained the following toxic elements: Boron (B), Nickel (Ni), Lead (Pb) and pesticide residues (DDT (0.002 ⁇ g / L) and DDD (0.003 ⁇ g / L), in three of the samples; DDE (0.030 ⁇ g / L) in 6 of the samples and Lindane (0.002 ⁇ g / L) in one sample).
  • the solutions were prepared with double distilled water and all tests were performed in triplicate.
  • the pH of the solutions was between 6 and 8.
  • the bioadsorption capacity was calculated based on the difference between the initial concentration (Co, mg / L) and the final concentration (Ce, mg / L) in each flask, with the following formula:
  • q e is the bioabsorption capacity of metal (mg / g).
  • M is the dry mass of the biosorbent 2 g for each of the powdered extracts of the vegetables.
  • V is the volume of the solution of As in the flask (500 mL) for all tests.
  • the minimum time for bioadsorption of toxic elements was one hour. Triplicate tests of 1, 2, 5, 12 and 24 hours were carried out and it was observed that the tests of greater intervals of time did not exceed the adsorbed concentration at which it was quantified in the first 2 hours. Table 1 shows the results of each of the treatments.
  • Treatment 1 containing powdered extract of exclusively dehydrated apple peels, effectively adsorbed and removed 90.3% of the Ace from the solution, 80% of B, 90% of Pb, but did not remove pesticides, and reached saturation until past 2 hours of interaction.
  • Table 1 Behavior in% of the removal of toxic elements in food, by the different treatments.
  • Treatment 4 which contained the mixture of tomato and soursop powder extracts, removed 92% of As, 97 of Ni and also removed pesticides from the solution; but he did not eliminate Boron, nor Lead; and it was saturated in the first hour.
  • treatment 5 containing the mixture of tomato and apple powder extracts eliminated 94% of As, 90% of B, 99% of Ni, 90% of Pb, but there was no pesticide removal from the solution, and it was saturated in the first hour.
  • treatment 7 that contained the mixture of apple, tomato and soursop powder extracts, eliminated 95% of As, 97% of Boron, 94 of Nickel, 97% of Lead, and also eliminated residues of pesticides of the solution, and it was saturated until after 2 hours.
  • Vegetable the content of an envelope

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  • Health & Medical Sciences (AREA)
  • Nutrition Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Preparation Of Fruits And Vegetables (AREA)
  • Seeds, Soups, And Other Foods (AREA)
  • Storage Of Fruits Or Vegetables (AREA)

Abstract

A plant biomass mixture comprises: a powdered extract from the dehydrated husk of the fruit from a member of the Rosaceae family; and a powdered extract of seeds from the fruit from a member of the Annonaceae family. The mixture also comprises a third powdered extract of husks of the fruit from a member of the Solanaceae family. A product for the phyto-removal of toxic components from foodstuffs comprises: a plant biomass mixture, such as that described in the previous paragraph; and a container, manufactured from a porous material, containing the plant biomass mixture. A method for removing toxic components from foodstuffs comprises the following steps: placing the foodstuffs in water, immersing a phyto-removal product, such as that described in the previous paragraph, in the water containing the foodstuffs; removing the phyto-removal product from the water containing the foodstuffs; and removing the water from the foodstuffs.

Description

MEZCLA DE BIOMASA VEGETAL, PRODUCTO FITORREMOVEDOR Y MÉTODO, PARA. REMOVER ELEMENTOS TÓXICOS DE LOS ALIMENTOS  MIXTURE OF VEGETABLE BIOMASS, FITORREMOVEDOR PRODUCT AND METHOD, FOR. REMOVE TOXIC ELEMENTS FROM FOOD
CAMPO TÉCNICO DE LA INVENCIÓN TECHNICAL FIELD OF THE INVENTION
La presente invención se relaciona con el campo técnico la Biotecnología y la industria alimenticia, debido a que proporciona una mezcla de biomasa vegetal, un producto fitorremovedor, y un método, para remover elementos tóxicos de los alimentos, para humanos y animales. The present invention relates to the technical field of Biotechnology and the food industry, because it provides a mixture of plant biomass, a fitoremovedor product, and a method, to remove toxic elements from food, for humans and animals.
ANTECEDENTES DE LA INVENCIÓN BACKGROUND OF THE INVENTION
En la actualidad, debido a desfavorables prácticas de procesos industriales, agrícolas y otras actividades humanas, numerosas descargas de materia orgánica, iones metálicos, hidrocarburos, pesticidas y colorantes son descargados a cuerpos de agua, que después son utilizados para beber o para irrigar campos de cultivo donde se producen alimentos para consumo humano y animal. At present, due to unfavorable practices of industrial, agricultural and other human activities, numerous discharges of organic matter, metal ions, hydrocarbons, pesticides and dyes are discharged to water bodies, which are then used to drink or irrigate fields of crop where food is produced for human and animal consumption.
Las aguas residuales pueden contener Arsénico, Mercurio, Níquel, Plomo, Cobre, Zinc, Cromo y Aluminio, porque son elementos frecuentemente utilizados en la industria electrónica, automotriz, minería, alimentaria, farmacéutica, cosmética, textil y artículos de piel. Wastewater may contain Arsenic, Mercury, Nickel, Lead, Copper, Zinc, Chrome and Aluminum, because they are frequently used in the electronics, automotive, mining, food, pharmaceutical, cosmetics, textiles and leather goods.
De ahí que el contenido de elementos tóxicos en animales y vegetales para el consumo humano es significativo, debido a que no se pueden metabolizar, sólo se acumulan en el organismo y esto es causa de diversas enfermedades, como cáncer, síndrome metabólico, diabetes mellitus, cirrosis, y otras, además tiene un impacto adverso en el medio ambiente. Hence the content of toxic elements in animals and plants for human consumption is significant, because they cannot be metabolized, they only accumulate in the body and this is the cause of various diseases, such as cancer, metabolic syndrome, diabetes mellitus, cirrhosis, and others, it also has an adverse impact on the environment.
Numerosos alimentos contienen una gran cantidad de elementos tóxicos que con sólo lavarlos o desinfectarlos o cocerlos, no se pueden eliminar, tal es el caso de los metales pesados, metaloides y pesticidas. Numerous foods contain a large amount of toxic elements that cannot be eliminated by simply washing or disinfecting or cooking them, such as heavy metals, metalloids and pesticides.
Los métodos utilizados para remover metales de las aguas residuales son la precipitación química, coagulación, extracción con solventes, electrólisis, separación con membrana, intercambio iónico y adsorción. La mayoría de estos métodos empleados requieren una gran inversión, equipo y capacitación para realizarlos. The methods used to remove metals from wastewater are chemical precipitation, coagulation, solvent extraction, electrolysis, membrane separation, ion exchange and adsorption. Most of these methods used require a large investment, equipment and training to perform them.
Los métodos de fitorremediación convencionales utilizan plantas vivas, fijas a un sustrato sólido del cual se requiere extraer algún contaminante, de tal manera que el vegetal vivo extrae de manera dinámica, por medio de sus mecanismos metabólicos, los elementos que le son útiles para su crecimiento, desarrollo o nutrición, o aquellos que son secuestrados por las raices del vegetal, de manera no selectiva. Como se puede ver la mayoría de las investigaciones están destinadas a la descontaminación de aguas residuales industriales, pero ninguna se enfoca específicamente para descontaminar a productos alimenticios en una forma más simple y sencilla; por ejemplo, Acosta y colaboradores (2012) realizaron una revisión de literatura del uso de diferentes biomasas fúngicas y naturales como alternativas para la remoción de metales pesados en aguas residuales provenientes de diferentes nichos contaminados. Quienes concluyeron que las biomasas analizadas y reportadas en la literatura remueven eficientemente metales pesados y arsénico en solución, por lo que pueden ser utilizada para eliminar los metales presente en sitios contaminados, como aguas residuales industriales (Acosta Rodriguez, I., J. F. Cárdenas González y V. M. Martinez Juárez (2012), ΧΈ1 uso de diferentes biomasas para la eliminación de metales pesados en sitios contaminados", Ide@s CONCYTEG, 7 (85), PP. 911-922. Conventional phytoremediation methods use live plants, fixed to a solid substrate from which some contaminant is required to be extracted, so that the living plant dynamically extracts, through its metabolic mechanisms, the elements that are useful for its growth , development or nutrition, or those that are kidnapped by the roots of the vegetable, non-selectively. As you can see, most of the investigations are aimed at the decontamination of industrial wastewater, but none is specifically focused to decontaminate food products in a simpler and simpler way; For example, Acosta et al. (2012) conducted a literature review of the use of different fungal and natural biomass as alternatives for the removal of heavy metals in wastewater from different contaminated niches. Who concluded that the biomass analyzed and reported in the literature efficiently remove heavy metals and arsenic in solution, so they can be used to remove metals present in contaminated sites, such as industrial wastewater (Acosta Rodriguez, I., JF Cárdenas González and VM Martinez Juárez (2012), Χ Έ1 use of different biomass for the removal of heavy metals in contaminated sites ", Ide @ s CONCYTEG, 7 (85), PP. 911-922.
Por su parte Hernáinz y colaboradores (2008) estudiaron la cinética de biosorción de cromo (VI) usando hueso de aceituna como sólido sorbente, encontrando que el Cr(VI) es en parte retirado por el hueso y en parte reducido a Cr(III) y que, a partir de un tiempo de contacto próximo a 300 minutos, el porcentaje retirado de Cr(VI) y Cr total se mantiene constante, lo que indica que no se produce ninguno de los dos procesos. Asi mismo, la capacidad de eliminación de Cr (VI) que tiene el hueso de aceituna disminuye con el aumento del pH, siendo este descenso mucho más cuando el pH es >2. Para el Cr total los valores de la capacidad de eliminación resultan inferiores a los obtenidos para Cr(VI), lo que pone de manifiesto el efecto de la reducción de Cr(VI) a Cr(III). El efecto de la temperatura en la cinética del proceso muestra que, para Cr(VI), la capacidad de biosorción y la constante cinética aumentan cuando la temperatura se eleva de 25 a 60 °C, permaneciendo ambos parámetros prácticamente constantes cuando la temperatura aumenta hasta 80 °C (Hernáinz F., Calero M. , Martin-Lara M. A. y Tenorio G. (2008), "Cinética de la biosorción de Cr (VI) con hueso de aceituna", AFINIDAD LXV, 538, Noviembre-Diciembre 2008) . Es por ello que en esta invención se desarrolló una mezcla a base de extractos vegetales en polvo (no viable) , para elaborar un producto Fitorremovedor para remover elementos tóxicos de productos alimenticios, mediante un método de adsorción pasivo. On the other hand, Hernáinz et al. (2008) studied the chromium biosorption kinetics (VI) using olive bone as a sorbent solid, finding that Cr (VI) is partly removed by the bone and partly reduced to Cr (III) and that, from a contact time close to 300 minutes, the percentage removed from Cr (VI) and Cr total remains constant, indicating that neither process occurs. Likewise, the elimination capacity of Cr (VI) that the olive bone has decreases with the increase in pH, this decrease being much more when the pH is> 2. For the total Cr, the elimination capacity values are lower than those obtained for Cr (VI), which shows the effect of the reduction of Cr (VI) to Cr (III). The effect of the temperature on the kinetics of the process shows that, for Cr (VI), the biosorption capacity and the kinetic constant increase when the temperature rises from 25 to 60 ° C, both parameters remaining practically constant when the temperature rises to 80 ° C (Hernáinz F., Calero M., Martin-Lara MA and Tenorio G. (2008), "Kinetics of the biosorption of Cr (VI) with olive bone", AFINIDAD LXV, 538, November-December 2008) . That is why in this invention a mixture based on powdered vegetable extracts (non-viable) was developed to produce a Phytoremovedor product to remove toxic elements from food products, using a passive adsorption method.
DESCRIPCION DETALLADA DE LA INVENCIÓN DETAILED DESCRIPTION OF THE INVENTION
Los detalles característicos de la presente invención se muestran claramente en siguiente descripción detallada y del ejemplo que se acompaña, los cuales ilustran algunas de las realizaciones preferentes de esta invención, por lo que no deben ser considerados como una limitante para dicha invención. The characteristic details of the present invention are clearly shown in the following detailed description and the accompanying example, which illustrate some of the preferred embodiments of this invention, and therefore should not be considered as a limitation on said invention.
Uno de los primeros objetos de la presente invención es proporcionar una mezcla de biomasa vegetal para remover elementos tóxicos de los productos alimenticios. Donde los principales elementos tóxicos a remover son: Arsénico (As) que es el elemento comúnmente encontrado en las superficies de productos alimenticios, Boro (B) , Níquel (Ni), Plomo (Pb) y residuos de pesticidas. One of the first objects of the present invention is to provide a mixture of plant biomass to remove toxic elements from food products. Where the main toxic elements to be removed are: Arsenic (As) which is the element commonly found on the surfaces of food products, Boron (B), Nickel (Ni), Lead (Pb) and pesticide residues.
Por lo que los productos alimenticios pueden ser principalmente productos agrícolas, a manera enunciativa y no limitativa, granos, semillas, frutas, frutillas, tejidos vegetales, entre otros. So food products can be mainly agricultural products, but not limited to, grains, seeds, fruits, strawberries, plant tissues, among others.
Dicha mezcla de biomasa vegetal se conforma de, un extracto en polvo de la cáscara deshidratada del fruto de un miembro de la familia de las Rosaceae; y un extracto en polvo de las semillas del fruto de un miembro de la familia de las Annonaceae. Donde una de las modalidades de la mezcla de blomasa vegetal, es que el miembro de la familia de las Rosaceae es del género Pyrus; más específicamente de la especie Pyrus malus; y más preferentemente de la variedad "Golden Delicious". Said mixture of vegetable biomass is made up of a powdered extract of the dried peel of the fruit of a member of the Rosaceae family; and a powdered extract of the seeds of the fruit of a member of the Annonaceae family. Where one of the modalities of the mixture of vegetable blomasa, is that the member of the Rosaceae family is of the genus Pyrus; more specifically of the species Pyrus malus; and more preferably of the "Golden Delicious" variety.
Una variante de la mezcla de biomasa vegetal en cuestión, es cuando el miembro de la familia de las Annonaceae, es del género Annona; siendo más específicamente de la especie Annona muricata. A variant of the vegetable biomass mixture in question is when the member of the Annonaceae family is of the Annona genus; being more specifically of the species Annona muricata.
Una realización preferente de la mezcla de biomasa vegetal, de la presente invención es cuando el tamaño de partícula del extracto en polvo de la cáscara deshidratada del fruto del miembro de la familia de las Rosaceae, es de 0.15 a 0.20 mm de diámetro; y el tamaño de partícula del extracto en polvo de semillas deshidratadas del fruto del miembro de la familia de las Annonaceae, es de 0.20 a 2.50 mm de diámetro. A preferred embodiment of the vegetable biomass mixture of the present invention is when the particle size of the dried extract of the dried peel of the fruit of the member of the Rosaceae family is 0.15 to 0.20 mm in diameter; and the particle size of the dried extract of dried seeds of the fruit of the member of the family of the Annonaceae, is from 0.20 to 2.50 mm in diameter.
Otra modalidad preferente de la mezcla de biomasa vegetal en cuestión, es que comprende además, un tercer extracto en polvo de la cáscara deshidratada del fruto de un miembro de la familia de las Solanaceae; siendo más específicamente del género Lycopersicon; siendo preferentemente de la especie Lycopersicon esculentum; y más preferente de la variedad "Saladett". Another preferred embodiment of the vegetable biomass mixture in question is that it also comprises a third powdered extract of the dried peel of the fruit of a member of the Solanaceae family; being more specifically of the Lycopersicon genus; preferably of the species Lycopersicon esculentum; and more preferred of the variety "Saladett".
Otra realización de la mezcla de acuerdo con la presente invención, es cuando el tamaño de partícula del extracto en polvo de la cáscara deshidratada del fruto del miembro de la familia de las Solanaceae, es de 0.05 a 1.50 mm de diámetro. ün objeto más de la presente invención es la de proporcionar un producto que denominamos como fitorremovedor, para remover, capturar, eliminar, etc., los elementos tóxicos que se encuentran en los productos alimenticios . Dicho producto fitorremovedor se caracteriza por comprender una mezcla de biomasa vegetal, de conformidad con las mezclas de biomasa vegetal de la presente invención; y un contenedor fabricado de un material poroso contiene en su interior a la mezcla de biomasa vegetal. Dicho material poroso puede ser papel, seda, nylon, por citar algunos ejemplos; donde los poros del material, debe ser de un tamaño suficiente para permitir una perfecta interacción entre los componentes de la mezcla de biomasa vegetal y las elementos tóxicos que contaminan a los productos alimenticios; o dicho de otra forma, para permitir un completa bioadsorción de los elementos tóxicos. Un ejemplo del contenedor de la mezcla de biomasa vegetal puede ser una bolsa, bolsita, saco, sobre, talega, etc. Cabe señalar también que dicho contenedor de la mezcla de biomasa vegetal, debe ir cerrado o sellado de alguna manera convencional y puede opcionalmente llevar un medio de sujeción, como un hilo, cuerda, etc., para manipularlo con facilidad durante su uso; como si fuese una bolsita de té convencional. Another embodiment of the mixture according to the present invention is when the particle size of the dried extract of the dried peel of the fruit of the Solanaceae family member is 0.05 to 1.50 mm in diameter. A further object of the present invention is to provide a product that we call as a phytoremovedor, to remove, capture, eliminate, etc., the toxic elements found in food products. Said fitoremovedor product is characterized by comprising a mixture of plant biomass, in accordance with the mixtures of plant biomass of the present invention; and a container made of a porous material contains in its interior the mixture of vegetable biomass. Said porous material may be paper, silk, nylon, to name a few examples; where the pores of the material must be of sufficient size to allow a perfect interaction between the components of the mixture of vegetable biomass and the toxic elements that contaminate food products; or put another way, to allow a complete bioadsorption of toxic elements. An example of the container of the vegetable biomass mixture can be a bag, sachet, sack, envelope, bag, etc. It should also be noted that said container of the vegetable biomass mixture must be closed or sealed in some conventional manner and may optionally carry a fastening means, such as a thread, rope, etc., for easy handling during use; as if it were a conventional tea bag.
Un realización más del producto fitorremovedor de la reivindicación anterior, puede ser que dicho producto fitorremovedor está en una relación de 1 parte de mezcla de biomasa vegetal para 33.33 partes de producto alimenticio, al cual se le removerán los elemento tóxicos. A further embodiment of the phyto-moving product of the preceding claim, it can be that said phyto-moving product is in a ratio of 1 part of vegetable biomass mixture to 33.33 parts of food product, to which the toxic elements will be removed.
Dentro de los productos alimenticios que puede ser tratados con este producto fito-rremovedor, pueden ser granos, frutas, frutillas, semillas o cualquier otro tejido vegetal que pudiera ser limpiado de sus contaminantes tóxicos por medio de la presente invención. Among the food products that can be treated with this phyto-stirring product, they can be grains, fruits, strawberries, seeds or any other plant tissue that could be cleaned of its toxic contaminants by means of the present invention.
Otro objeto más de la presente invención es un método para remover elementos tóxicos de los productos alimenticios, mediante el uso del producto fitorremovedor descrito en esta invención, por lo que dicho método comprende las siguientes etapas: i) colocar los productos alimenticios en agua, en una proporción de 28.56:71.43; A further object of the present invention is a method for removing toxic elements from food products, by using the phyto-moving product described in this invention, whereby said method comprises the following steps: i) placing the food products in water, in a ratio of 28.56: 71.43;
ii) sumergir el producto fitorregulador en el agua que contiene a los productos alimenticios, durante al menos 1 hora, para que se lleve acabo la bioadsorción de los elementos tóxicos;  ii) submerge the phytoregulatory product in the water that contains the food products, for at least 1 hour, so that the bioadsorption of the toxic elements is carried out;
iii) retirar el producto fitorremovedor del agua que contiene a los productos alimenticios; y iv) remover el agua de los productos alimenticios ya tratados .  iii) remove the phytoremovedor product from the water that contains the food products; and iv) remove water from food products already treated.
Una realización del presente método es dejar sumergido el producto fitorremovedor en el agua, durante 2 h, que es cuando se logra el mayor grado de saturación de elementos tóxicos . An embodiment of the present method is to leave the phytoremovedor product submerged in water for 2 h, which is when the highest degree of saturation of toxic elements is achieved.
Una modalidad del método en cuestión, es usar una relación, mezcla de biomasa vegetal :producto alimenticio (1:33.33) . One modality of the method in question is to use a ratio, mixture of plant biomass: food product (1: 33.33).
Una variante más de dicho método según la presente invención, es cuando se utiliza un contenedor de la mezcla de biomasa vegetal, hecho de un material poroso, tales como papel, seda, nylon, etc.; donde la porosidad debe tener un tamaño que permita una perfecta interacción entre los ingredientes de la mezcla en cuestión, con los elementos tóxicos. El contenedor puede ser una bolsa, bolsita, sobre, talega, y similares. Cabe señalar que dicho contender debe ir cerrado o sellado de una manera convencional y puede opcionalmente llevar un medio de sujeción, como un hilo, cuerda, etc., para manipularlo con facilidad durante su uso; como si fuese una bolsita de té convencional . A further variant of said method according to the present invention is when a container of the vegetable biomass mixture, made of a porous material, is used. such as paper, silk, nylon, etc .; where the porosity must have a size that allows a perfect interaction between the ingredients of the mixture in question, with the toxic elements. The container can be a bag, sachet, envelope, bag, and the like. It should be noted that said container must be closed or sealed in a conventional manner and may optionally have a fastening means, such as a thread, rope, etc., for easy handling during use; as if it were a conventional tea bag.
Con este método se pueden tratar productos alimenticios tales como, granos, frutas, frutillas, semillas, entre otros tipos de tejidos vegetales que puedan ser tratados con dicho método. With this method, food products such as grains, fruits, strawberries, seeds, among other types of plant tissues that can be treated with said method can be treated.
Ejemplo único Unique example
Este ejemplo ilustra una de las realizaciones de la presente invención.  This example illustrates one of the embodiments of the present invention.
Materiales materials
Se utilizaron frutos de manzana, jitomate y guanábana, firmes, maduros, de buena calidad, limpios, exentos de daños externos, agentes químicos y de plagas. Todos los frutos que se utilizaron fueron cultivados y recolectados en diferentes estados de México, considerando en primer lugar, los mayores productores de cada especie de fruto. De la familia JRosaceae se utilizaron manzanas amarillas [Pyrus malus, variedad "Golden delicious"), obtenidas de los estados de Chihuahua y Durango. De las manzanas se obtuvieron las cáscaras y se sometieron a un proceso de deshidratación en un horno de aire caliente a 60 °C (Deshidratador de Alimentos Waring Pro DHR30), por 10 horas continuas. Al término del proceso de secado, se realizó un análisis elemental de la biomasa y se obtuvo que las cáscaras de manzana registraron 9.94 % de humedad y 1.19 % de cenizas. Las cáscara de manzana ya deshidratadas fueron fragmentadas hasta obtener un tamaño de corte promedio entre 0.15 y 0.20 mm de diámetro. De la familia Solanáceas se utilizaron jitomates {Lycopersicon esculentum, de la variedad "Saladette") , obtenidos de los estados de Sinaloa y Jalisco. De estos jitomates se obtuvieron las cáscaras, las cuales se sometieron a un proceso de deshidratación en un horno de aire caliente a 60 °C (Deshidratador de Alimentos Waring Pro DHR30) , por 8 horas continuas. Al término del proceso de secado, se realizó un análisis elemental de la biomasa y se obtuvo que las cáscaras de jitomate registraron un 8.18% de humedad y 8.19% de cenizas. Los fragmentos de cáscara de jitomate que se obtuvieron estuvieron entre 0.05 y 1.5 mm de diámetro en promedio. Apple, tomato and soursop fruits, firm, ripe, of good quality, clean, free of external damage, chemical agents and pests were used. All the fruits that were used were cultivated and collected in different states of Mexico, considering first, the largest producers of each species of fruit. From the JRosaceae family, yellow apples [Pyrus malus, variety "Golden delicious") were used, obtained from the states of Chihuahua and Durango. The apples obtained the peels and underwent a process of dehydration in a hot air oven at 60 ° C (Waring Pro DHR30 Food Dehydrator), for 10 continuous hours. At the end of the drying process, an elementary analysis of the biomass was carried out and it was obtained that the apple peels recorded 9.94% of humidity and 1.19% of ashes. Apple peel already dehydrated was fragmented until an average cut size between 0.15 and 0.20 mm in diameter was obtained. Tomatoes (Lycopersicon esculentum, of the variety "Saladette"), obtained from the states of Sinaloa and Jalisco, were used from the Solanaceae family. From these tomatoes the husks were obtained, which were subjected to a dehydration process in a hot air oven at 60 ° C (Waring Pro DHR30 Food Dehydrator), for 8 continuous hours. At the end of the drying process, an elementary analysis of the biomass was carried out and it was obtained that the tomato shells registered 8.18% of humidity and 8.19% of ashes. The tomato shell fragments that were obtained were between 0.05 and 1.5 mm in diameter on average.
De la familia Annonaceae se utilizaron Guanábanas [Annona muricata) , que se obtuvieron de los estados de Colima y Guerrero. De estas guanábanas se extrajeron las semillas, las cuales se sometieron a un proceso de limpieza de residuos de pulpa de la fruta y se dejaron secar al aire libre a temperatura ambiente. Posteriormente, las semillas fueron trituradas en un molino para granos manual y ya trituradas fueron sometidas a deshidratación en un horno de aire caliente a 60 °C (Deshidratador de Alimentos Waring Pro DHR30) , por 4 horas continuas. Al término del proceso de secado, se realizó un análisis elemental de la biomasa y se obtuvo que las semillas trituradas de guanábana registraron 4.90 % de humedad y 1.18 % de cenizas. Los fragmentos de semillas de guanábana estuvieron entre 0.2 y 2.5 mm de diámetro en promedio. From the Annonaceae family, Soursop [Annona muricata) were used, which were obtained from the states of Colima and Guerrero. From these soursop the seeds were extracted, which were subjected to a cleaning process of pulp residues of the fruit and allowed to dry in the open air at room temperature. Subsequently, the seeds were crushed in a manual grain mill and already crushed they were subjected to dehydration in a hot air oven at 60 ° C (Waring Pro DHR30 Food Dehydrator), for 4 continuous hours. At the end of the drying process, an elementary analysis of the biomass and it was obtained that crushed soursop seeds recorded 4.90% moisture and 1.18% ash. Soursop seed fragments were between 0.2 and 2.5 mm in diameter on average.
Tratamientos Treatments
Con la finalidad de conocer las capacidades de absorción de elementos tóxicos, de los extractos en polvo de los frutos de manzana, jitomate y guanábana, antes descritos, se platearon los siguientes tratamientos: In order to know the absorption capacities of toxic elements, of the powdered extracts of apple, tomato and soursop fruits, described above, the following treatments were plated:
Tratamiento 1: 2 g de extracto en polvo de cáscaras de manzana, en un sobre de papel filtro. Treatment 1: 2 g of powdered extract of apple peels, in a filter paper envelope.
Tratamiento 2 : 2 g de extracto en polvo de cáscaras de jitomate, en un sobre de papel filtro. Treatment 2: 2 g of powdered extract of tomato peels, in a filter paper envelope.
Tratamiento 3: 2g de extracto en polvo de semillas de guanábana, en un sobre de papel filtro. Treatment 3: 2g of soursop seed powder extract, in a filter paper envelope.
Tratamiento 4: una mezcla de 2 g de extracto en polvo de cáscaras de jitomate y 2 g de extracto en polvo de semillas de guanábana, en un sobre de papel filtro. Tratamiento 5: una mezcla de 2 g de extracto en polvo de cáscaras de manzana y 2 g de extracto en polvo de cáscaras de jitomate, en un sobre de papel filtro. Tratamiento 6: una mezcla de 2 g de extracto en polvo de cáscaras de manzana y 2 g de extracto en polvo de semillas de guanábana, en un sobre de papel filtro. Tratamiento 7: una mezcla de 2 g de extracto en polvo de cáscaras de manzana, 2 g de extracto en polvo de cáscaras de jitomate y 2 g de extracto en polvo se semillas de guanábana, en un sobre de papel filtro. Treatment 4: a mixture of 2 g of powdered extract of tomato peels and 2 g of powdered extract of soursop seeds, in a filter paper envelope. Treatment 5: a mixture of 2 g of apple peel powder extract and 2 g of tomato peel powder extract, in a filter paper envelope. Treatment 6: a mixture of 2 g of apple peel extract powder and 2 g of soursop seed powder extract, in a filter paper envelope. Treatment 7: A mixture of 2 g of powdered extract of apple peels, 2 g of powdered extract of tomato peels and 2 g of powdered extract is soursop seeds, in a filter paper envelope.
Soluciones para la adsorción Para probar los distintos tratamientos antes descritos, se eligió preparar una solución acuosa de Arsénico (As) (grado analitico) , con base a que es el elemento tóxico mayormente encontrado en los granos comestibles, debido a la contaminación del agua de riego y por ser un elemento que se utiliza en la formulación de muchos pesticidas utilizados en la producción de alimentos. En todos nuestros análisis anteriores de granos comestibles, el As ha estado presente en mayor o en menor concentración. Adsorption Solutions To test the different treatments described above, it was chosen to prepare an aqueous solution of Arsenic (As) (analytical grade), based on the fact that it is the toxic element mostly found in edible grains, due to contamination of irrigation water and because it is an element that is used in the formulation of many pesticides used in food production. In all our previous analyzes of edible grains, Ace has been present in greater or lesser concentration.
En dicha solución acuosa de As, también contenia los siguientes elementos tóxicos: Boro (B) , Níquel (Ni), Plomo (Pb) y residuos de pesticidas (DDT (0.002 μg/L) y DDD (0.003 μg/L) , en tres de las muestras; DDE (0.030μg/L) en 6 de las muestras y Lindane (0.002 μg/L) en una muestra) . In said aqueous solution of As, it also contained the following toxic elements: Boron (B), Nickel (Ni), Lead (Pb) and pesticide residues (DDT (0.002 μg / L) and DDD (0.003 μg / L), in three of the samples; DDE (0.030μg / L) in 6 of the samples and Lindane (0.002 μg / L) in one sample).
Las soluciones fueron preparadas con agua bidestilada y todos los ensayos fueron realizados por triplicado. El pH de las soluciones estuvo entre 6 y 8. The solutions were prepared with double distilled water and all tests were performed in triplicate. The pH of the solutions was between 6 and 8.
El análisis del agua bidestilada simple, de las soluciones con As (a una concentración de 0.12 mg/L) con los otros elementos tóxicos, y de las soluciones resultantes de la bioadsorción fueron realizadas por espectrofotometría de emisión óptica de plasma acoplado inductivamente, gravimetría . The analysis of simple double-distilled water, of the solutions with As (at a concentration of 0.12 mg / L) with the other toxic elements, and of the solutions resulting from bioadsorption were performed by inductively coupled plasma optical emission spectrophotometry, gravimetry.
La capacidad de bioadsorción se calculó con base a la diferencia entre la concentración inicial (Co, mg/L) y la concentración final (Ce, mg/L ) en cada matraz, con la siguiente fórmula:
Figure imgf000013_0001
The bioadsorption capacity was calculated based on the difference between the initial concentration (Co, mg / L) and the final concentration (Ce, mg / L) in each flask, with the following formula:
Figure imgf000013_0001
Donde :  Where :
qe = es la capacidad de bioadsorción de metal (mg/g) . q e = is the bioabsorption capacity of metal (mg / g).
Co = mg/L concentración inicial de la solución. Co = mg / L initial concentration of the solution.
Ce = mg/L concentración final de la solución. Ce = mg / L final concentration of the solution.
M = es la masa seca del biosorbente 2 g para cada uno de los extractos en polvo de los vegetales. M = is the dry mass of the biosorbent 2 g for each of the powdered extracts of the vegetables.
V = es el volumen de la solución de As en el matraz (500 mL) para todos los ensayos. Resultados V = is the volume of the solution of As in the flask (500 mL) for all tests. Results
El tiempo mínimo para la bioadsorción de los elementos tóxicos fue de una hora. Se realizaron ensayos por triplicado de 1, 2, 5, 12 y 24 horas y se observó que los ensayos de intervalos mayores de tiempo, no superaron la concentración adsorbida a la que se cuantificó en las primeras 2 horas. En la Tabla 1 se presentan los resultados de cada uno de los tratamientos . The minimum time for bioadsorption of toxic elements was one hour. Triplicate tests of 1, 2, 5, 12 and 24 hours were carried out and it was observed that the tests of greater intervals of time did not exceed the adsorbed concentration at which it was quantified in the first 2 hours. Table 1 shows the results of each of the treatments.
El tratamiento 1 que contenia extracto en polvo de cáscaras de manzana deshidratadas exclusivamente, adsorbió efectivamente y eliminó el 90.3 % del As de la solución, el 80 % de B, 90 % de Pb, pero no removió pesticidas, y alcanzó su saturación hasta pasadas las 2 hora de interacción. Treatment 1 containing powdered extract of exclusively dehydrated apple peels, effectively adsorbed and removed 90.3% of the Ace from the solution, 80% of B, 90% of Pb, but did not remove pesticides, and reached saturation until past 2 hours of interaction.
El tratamiento 2 que contenía extracto en polvo de cáscaras de jitomate deshidratadas exclusivamente, fue el que adsorbió mas rápidamente y eliminó el 91.2 % del As y el 97 % de Ni, pero no removió B, Pb, ni pesticidas de la solución, pero fue el que se saturó durante la primera hora de interacción. Tabla 1. Comportamiento en % de la remoción de elementos tóxicos en alimentos, por los distintos tratamientos . Treatment 2 containing powdered extract of dried tomato shells exclusively, was the one that adsorbed more rapidly and removed 91.2% of As and 97% of Ni, but did not remove B, Pb, or pesticides from the solution, but it was the one that was saturated during the first hour of interaction. Table 1. Behavior in% of the removal of toxic elements in food, by the different treatments.
Figure imgf000014_0001
Figure imgf000014_0001
Pest = Pesticidas; Si = sí hubo remoción de pestici as; No = no hubo eliminación de pesticidas.  Pest = Pesticides; Yes = yes there was pesticide removal; No = there was no pesticide disposal.
Mientras que el tratamiento 3 que contenia extracto de polvo de semillas trituradas de guanábana deshidratadas exclusivamente, adsorbió y eliminó el 91.5 % del As, 97 % de Ni y sí hubo remoción de pesticidas de la solución, pero no eliminó Boro, ni de Plomo y alcanzó sus saturación hasta pasada las 2 hora de interacción. While treatment 3 containing powdered extract of crushed soursop seeds exclusively dehydrated, adsorbed and removed 91.5% of As, 97% of Ni and yes there was pesticide removal from the solution, but it did not eliminate Boron, or Lead and reached saturation until after 2 hours of interaction.
El tratamiento 4 que contenía la mezcla de los extracto en polvo de jitomate y guanábana, eliminó el 92 % del As, 97 de Ni y también removió los pesticidas de la solución; pero no eliminó Boro, ni Plomo; y se saturó en la primera hora. Treatment 4, which contained the mixture of tomato and soursop powder extracts, removed 92% of As, 97 of Ni and also removed pesticides from the solution; but he did not eliminate Boron, nor Lead; and it was saturated in the first hour.
En cambio, el tratamiento 5 que contenía la mezcla de los extractos en polvo de jitomate y manzana, eliminó el 94 % del As, 90 % de B, 99 % de Ni, 90 % de Pb, pero no hubo eliminación de pesticidas de la solución, y se saturó en la primera hora. El tratamiento 6 que contenia la mezcla de los extractos en polvo de manzana y guanábana, eliminó el 92 % del As, 86 % de B, 94 de Ni, 96 de Pb y eliminó los residuos de pesticidas de la solución, y se saturó en la primera hora. On the other hand, treatment 5 containing the mixture of tomato and apple powder extracts eliminated 94% of As, 90% of B, 99% of Ni, 90% of Pb, but there was no pesticide removal from the solution, and it was saturated in the first hour. Treatment 6, which contained the mixture of apple and soursop powder extracts, removed 92% of As, 86% of B, 94 of Ni, 96 of Pb and removed pesticide residues from the solution, and saturated in the first hour.
Por su parte el tratamiento 7 que contenía la mezcla de los extractos en polvo de manzana, jitomate y guanábana, elimino el 95 % del As, 97 % de Boro, 94 de Níquel, 97 % de Plomo, y también eliminó los residuos de los pesticidas de la solución, y se saturó hasta pasadas las 2 horas. On the other hand, treatment 7 that contained the mixture of apple, tomato and soursop powder extracts, eliminated 95% of As, 97% of Boron, 94 of Nickel, 97% of Lead, and also eliminated residues of pesticides of the solution, and it was saturated until after 2 hours.
Se observó que este todos los tratamientos fueron estables a los cambios de temperatura y variaciones mínimas de pH. Como se puede ver, los tratamientos 6 y 7 fueron los que eliminaron a todos los elementos tóxicos y los residuos de pesticidas, siendo el tratamiento 7 el que mayor porcentaje de bioadsorción presentó. It was noted that this all treatments were stable to temperature changes and minimal pH variations. As can be seen, treatments 6 and 7 were those that eliminated all toxic elements and pesticide residues, with treatment 7 being the highest percentage of bioadsorption.
También se observó que el porcentaje de bioadsorción es directamente proporcional a la biomasa vegetal, una vez que llega a su nivel de saturación ya no adsorbe más, por tanto, en el caso de que la concentración de tóxicos sea muy alta, hay que aumentar el volumen de biomasa para asegurarse de que la remoción de estos elementos tóxicos en los alimentos, sea óptima. It was also observed that the percentage of bioadsorption is directly proportional to plant biomass, once it reaches its saturation level it no longer adsorbs, therefore, in the case that the toxic concentration is very high, the biomass volume to ensure that the removal of these toxic elements in food is optimal.
Con base en los resultados anteriores de las concentraciones de elementos tóxicos encontradas en los granos crudos, se calculó un volumen de 6 g de biomasa vegetal (el contenido de un sobre) para la óptima remoción de elementos tóxicos en 200 g de granos crudos, que deberán remojarse en 500 mL de agua limpia. Based on the previous results of the concentrations of toxic elements found in the raw grains, a volume of 6 g of biomass was calculated Vegetable (the content of an envelope) for the optimal removal of toxic elements in 200 g of raw grains, which should be soaked in 500 mL of clean water.

Claims

REIVINDICACIONES
1. Una mezcla de biomasa vegetal, caracterizada porque comprende : 1. A mixture of plant biomass, characterized in that it comprises:
1) un extracto en polvo de la cáscara deshidratada del fruto de un miembro de la familia de las Rosaceae; y 1) a powdered extract of the dried peel of the fruit of a member of the Rosaceae family; Y
ii) un extracto en polvo de las semillas del fruto de un miembro de la familia de las Annonaceae.  ii) a powdered extract of the seeds of the fruit of a member of the Annonaceae family.
2. La mezcla de la reivindicación anterior, donde el miembro de la familia de las Rosaceae es del género Pyrus. 2. The mixture of the preceding claim, wherein the member of the Rosaceae family is of the genus Pyrus.
3. La mezcla de la reivindicación anterior, donde el miembro del género Pyrus pertenece a la especie Pyrus malus. 3. The mixture of the preceding claim, wherein the member of the genus Pyrus belongs to the species Pyrus malus.
4. La mezcla de la reivindicación precedente, donde el miembro de la especie Pyrus malus es de la variedad "Golden Delicious". 4. The mixture of the preceding claim, wherein the member of the species Pyrus malus is of the "Golden Delicious" variety.
5. La mezcla de conformidad con la reivindicación 1, donde el miembro de la familia de las Annonaceae, es del género Annona. 5. The mixture according to claim 1, wherein the member of the Annonaceae family, is of the genus Annona.
6. La mezcla de la reivindicación anterior, donde el miembro del género Annona es de la especie Annona muricata. 6. The mixture of the preceding claim, wherein the member of the genus Annona is of the species Annona muricata.
7. La mezcla de acuerdo con la reivindicación 1, donde el tamaño de partícula del extracto en polvo de la cáscara deshidratada del fruto del miembro de la familia de las Rosaceae, es de 0.15 a 0.20 mm de diámetro. 8. La mezcla de según la reivindicación 1, donde el tamaño de partícula del extracto en polvo de la semilla deshidratada del fruto del miembro de la familia de las Annonaceae, es de 0.20 a 2.50 mm de diámetro. 9. La mezcla de la reivindicación 1, caracterizada porque comprende además, un extracto en polvo de la cáscara deshidratada del fruto de un miembro de la familia de las Solanaceae. 7. The mixture according to claim 1, wherein the particle size of the shell powder extract dehydrated from the fruit of the member of the Rosaceae family, is 0.15 to 0.20 mm in diameter. 8. The mixture according to claim 1, wherein the particle size of the dried extract of the dried seed of the fruit of the member of the Annonaceae family, is 0.20 to 2.50 mm in diameter. 9. The mixture of claim 1, characterized in that it further comprises a powder extract of the dried peel of the fruit of a member of the Solanaceae family.
10. La mezcla de la reivindicación precedente, donde el miembro de la familia de las Solanaceae es del género10. The mixture of the preceding claim, wherein the member of the Solanaceae family is of the genus
Lycopersicon . Lycopersicon
11. La mezcla acorde a la reivindicación anterior, donde el miembro del género Lycopersicon es de la especie Lycopersicon esculentum. 11. The mixture according to the preceding claim, wherein the member of the genus Lycopersicon is of the species Lycopersicon esculentum.
12. La mezcla de la reivindicación anterior, donde el miembro de la especie Lycopersicon esculentum es de la variedad "Saladett". 12. The mixture of the preceding claim, wherein the member of the species Lycopersicon esculentum is of the "Saladett" variety.
13. La mezcla de acuerdo con la reivindicación 9, donde el tamaño de partícula del extracto en polvo de la cáscara deshidratada del fruto del miembro de la familia de las Solanaceae, es de 0.05 a 1.50 mm de diámetro. 13. The mixture according to claim 9, wherein the particle size of the dried extract of the dried peel of the fruit of the Solanaceae family member is 0.05 to 1.50 mm in diameter.
14. Un producto fitorremovedor de elementos tóxicos de los productos alimenticios, caracterizado porque comprende: i) una mezcla de biomasa vegetal, de conformidad con cualquiera de la reivindicaciones anteriores; y ii) un contenedor fabricado de un material poroso, contiene a la mezcla de biomasa vegetal; donde el tamaño de los poros permiten una completa bioadsorción. 15. El producto fitorremovedor de la reivindicación anterior, donde la relación, mezcla de biomasa vegetal y producto alimenticio, es de 1:33.33. 14. A fitoremovedor product of toxic elements of food products, characterized in that it comprises: i) a mixture of plant biomass, according to any of the preceding claims; and ii) a container made of a porous material, contains the mixture of plant biomass; where the size of the pores allow complete bioadsorption. 15. The phyto-moving product of the preceding claim, wherein the ratio, mixture of vegetable biomass and foodstuff, is 1: 33.33.
16. El producto fitoremovedor según la reivindicación 14, donde el material poroso es papel, seda, y/o nylon. 17. El producto fitorremovedor acorde a la reivindicación anterior, donde el material poroso es papel filtro. 16. The phyto-stirring product according to claim 14, wherein the porous material is paper, silk, and / or nylon. 17. The phyto-moving product according to the preceding claim, wherein the porous material is filter paper.
El producto fitorremovedor de la reivindicación 14, donde el contenedor de la mezcla de biomasa se selecciona del grupo: bolsa, bolsita, sobre y talega. The phyto-moving product of claim 14, wherein the biomass mixture container is selected from the group: bag, sachet, envelope and bag.
19. El producto fitorremovedor tal y como se reclama en la reivindicación 14, caracterizado porque comprende además, un medio de sujeción, como un hilo o cuerda. 19. The phyto-moving product as claimed in claim 14, characterized in that it further comprises a fastening means, such as a thread or rope.
20. El producto fitorremovedor de acuerdo con la reivindicación 14, donde los productos alimenticios a limpiar, son granos, frutas, frutillas, semillas, y/o tejidos vegetales. 20. The phyto-stirring product according to claim 14, wherein the food products to be cleaned are grains, fruits, strawberries, seeds, and / or plant tissues.
21. Un método para remover elementos tóxicos de los productos alimenticios, caracterizado porque comprende: v) colocar los productos alimenticios en agua, en una proporción de 28.56:71.43; 21. A method for removing toxic elements from food products, characterized in that it comprises: v) place food products in water, at a ratio of 28.56: 71.43;
vi) sumergir un producto fitorremovedor, de conformidad con cualquiera de las reivindicaciones 14 a la 18, en el agua que contiene a los productos alimenticios, durante al menos 1 hora, para que se lleve acabo la bioadsorción de los elementos tóxicos;  vi) immersing a phyto-stirring product, according to any one of claims 14 to 18, in the water containing the food products, for at least 1 hour, so that the bio-absorption of the toxic elements is carried out;
vii) retirar el producto fitorremovedor del agua que contiene a los productos alimenticios; y viii) eliminar el agua de los productos alimenticios.  vii) remove the phytoremovedor product from the water containing the food products; and viii) remove water from food products.
22. El método de la reivindicación anterior, donde la relación, mezcla de biomasa vegetal y alimento, es 1:33.33. 22. The method of the preceding claim, wherein the ratio, mixture of plant biomass and food, is 1: 33.33.
23. El método según la reivindicación 21, donde el material poroso es papel, seda y/o nylón. 24. El método acorde a la reivindicación anterior, donde el material poroso es papel filtro. 23. The method according to claim 21, wherein the porous material is paper, silk and / or nylon. 24. The method according to the preceding claim, wherein the porous material is filter paper.
25. El método de la reivindicación 21, donde el contenedor de la mezcla de biomasa se selecciona del grupo: bolsa, bolsita, sobre y talega. 25. The method of claim 21, wherein the biomass mixture container is selected from the group: bag, sachet, envelope and bag.
26. El método tal y como se reclama en la reivindicación 21, caracterizado porque comprende además, un medio de sujeción, como un hilo o cuerda. 26. The method as claimed in claim 21, characterized in that it further comprises a fastening means, such as a thread or rope.
27. El método de acuerdo con la reivindicación 21, donde los productos alimenticios a limpiar son: granos, frutas, frutillas, semillas y/o tejidos vegetales. 27. The method according to claim 21, wherein the food products to be cleaned are: grains, fruits, strawberries, seeds and / or plant tissues.
PCT/MX2016/000054 2016-06-01 2016-06-02 A plant biomass mixture, phyto-removal product and method for removing toxic components from foodstuffs WO2017209590A1 (en)

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