WO2006132519A1 - Composition and method for the treatment of wastewater and sewage water in order to produce drinking water - Google Patents

Composition and method for the treatment of wastewater and sewage water in order to produce drinking water Download PDF

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Publication number
WO2006132519A1
WO2006132519A1 PCT/MX2005/000044 MX2005000044W WO2006132519A1 WO 2006132519 A1 WO2006132519 A1 WO 2006132519A1 MX 2005000044 W MX2005000044 W MX 2005000044W WO 2006132519 A1 WO2006132519 A1 WO 2006132519A1
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Prior art keywords
water
treated
wastewater
sewage
composition
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PCT/MX2005/000044
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Spanish (es)
French (fr)
Inventor
Jaime Raygoza Mora
Cipriano Perez Alvarez
Jaime Mora Flores
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Jaime Raygoza Mora
Cipriano Perez Alvarez
Jaime Mora Flores
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Priority to PCT/MX2005/000044 priority Critical patent/WO2006132519A1/en
Publication of WO2006132519A1 publication Critical patent/WO2006132519A1/en

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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/54Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
    • C02F1/56Macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/727Treatment of water, waste water, or sewage by oxidation using pure oxygen or oxygen rich gas
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/005Black water originating from toilets
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/007Contaminated open waterways, rivers, lakes or ponds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/44Time

Definitions

  • the present invention relates to a formula or composition and process for the treatment of wastewater and sewage, water contaminated with chemicals, microorganisms, suspended particles and heavy metals;
  • This composition and process can be applied in tanks or in the natural channels of rivers or lakes.
  • the proposed formula is a completely novel composition based mainly on calcium, and unlike other formulas for treating wastewater and sewage, with this the transformation of sewage or wastewater into drinking water is achieved.
  • the drinking water that is obtained complies with the
  • Water purification for use in animals and humans More specifically, wastewater or sewage (sewage) containing contaminants can be effectively treated by applying the formula or composition and procedure proposed.
  • Figure 1 Flow chart of the procedure consisting of six stages or steps for the treatment of wastewater or sewage to obtain potable water.
  • the boiling movement due to temperature changes of 10 to 99 degrees Celsius is obtained by the heating that results from contacting the components of the formula with the wastewater or sewage to be treated, and is complemented by heat application by different methods of heating, such as direct flame or solar cells, the boiling impact movement is 250 grams in a test area of Icm2 (one square centimeter).
  • the aqueous mixture is left in a rest period of 3 hours, during this time there is a deconcentration reaction of suspended solids with parameters of 150 to 800 per cubic milligram, obtaining a cleaning by deconcentration of suspended solids of a 80% per cubic milligram.
  • Filtration and oxygenation stages The process that is being presented also consists of a filtration stage and an oxygenation stage, which is important to mention because it is part of the process for obtaining drinking water, but any of the known filtration and oxygenation processes within the state can be used of the technique for the treatment of wastewater and therefore are not a matter of complaint.
  • the sludges that are obtained or that result from the described technique are completely inert residues, free of any bacteria or larvae, which have excellent sedimentation characteristics and with natural properties to be used as fertilizers in farmland, applied in aquaculture or 'as a biological activator for lakes, ponds and the like, without risk of contamination.
  • sludge that results from other wastewater treatments where it is necessary to give a specific treatment to such sludges as the one mentioned in European patent application No. 99946262.5, in our process it is not necessary to give the sludge any special treatment For its destruction, it is more as already mentioned above, this mud is usable as a nutrient in various areas.

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  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Removal Of Specific Substances (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

The invention relates to a composition and method for the treatment of wastewater and sewage water in order to produce drinking water in accordance with drinking water purification standards. The inventive formula is based on completely natural elements, mainly calcium, but can also be based on synthetic elements. The method is novel in that it can be used to purify wastewater or sewage water, i.e. water contaminated with chemical substances, algae, micro-organisms and suspended particles, until said water is drinkable and suitable for human and animal use. In addition, the sludge and sediment obtained during said wastewater and sewage water treatment method is completely inert and free of contamination and, as a result, can be used as a nutrient material or compost in cultivation, sowing or aquaculture, rendering same suitable for use in various different areas of application.

Description

COMPOSICIÓN Y PROCESO PARA TRATAMIENTO DE AGUAS RESIDUALES Y NEGRAS OBTENIENDO AGUA POTABLE.COMPOSITION AND PROCESS FOR TREATMENT OF RESIDUAL AND BLACK WATER OBTAINING DRINKING WATER.
ANTECEDENTESBACKGROUND
En la actualidad se conocen diversos tipos de tratamientos de aguas residuales a base flotación de sólidos, trituración de sólidos, cloración para desconcentrar los sólidos suspendidos, filtración y depuración, los cuales utilizan yoduro y una gama de ácidos, como el muriático, sulfúrico y mezclas de químicos sintéticos, proceso a base de inyección de oxígeno y el proceso anaeróbico, métodos y procesos descritos en FR 2.036.685, FR 2.226.361, FR 2.534.897, Solicitudes de Patentes Europea 9591393.02., 89400156.9., 94916718.9 y E95913932. Todos los procesos antes mencionados y conocidos mundialmente, son tratamientos que dan como resultado la obtención de aguas duras y pesadas, son aguas de segunda, que se destinan exclusivamente al riego de brechas y caminos. Aunado a esto el gran problema de los lodos o sedimentos que resultan de los tratamientos de aguas residuales, que son altamente contaminantes y que aparte se les deben de dar un tratamiento para su destrucción.Currently, various types of wastewater treatments based on solid flotation, crushing of solids, chlorination to deconcentrate suspended solids, filtration and purification, which use iodide and a range of acids, such as muriatic, sulfuric and mixtures are known of synthetic chemicals, oxygen-based process and anaerobic process, methods and processes described in FR 2,036,685, FR 2,226,361, FR 2,534,897, European Patent Applications 9591393.02., 89400156.9., 94916718.9 and E95913932. All the aforementioned processes and known worldwide, are treatments that result in the obtaining of hard and heavy waters, they are second-class waters, which are destined exclusively to the irrigation of gaps and roads. In addition to this, the great problem of sludge or sediment that results from wastewater treatments, which are highly polluting and must be treated separately for their destruction.
CAMPO DE LA INVENCIÓNFIELD OF THE INVENTION
La presente invención se refiere a una formula o Composición y proceso para el tratamiento de aguas residuales y aguas negras, aguas contaminadas con sustancias químicas, microorganismos, partículas suspendidas y metales pesados; ésta composición y proceso se puede aplicar en tanques o en los cauces naturales de los ríos o lagos. La formula que se propone es una composición completamente novedosa a base de principalmente de calcio, y a diferencia de otras fórmulas para tratar aguas residuales y aguas negras, con ésta se logra la transformación de aguas negras o residuales en agua potable. El agua potable que se obtiene cumple con las Normas deThe present invention relates to a formula or composition and process for the treatment of wastewater and sewage, water contaminated with chemicals, microorganisms, suspended particles and heavy metals; This composition and process can be applied in tanks or in the natural channels of rivers or lakes. The proposed formula is a completely novel composition based mainly on calcium, and unlike other formulas for treating wastewater and sewage, with this the transformation of sewage or wastewater into drinking water is achieved. The drinking water that is obtained complies with the
Potabilización de Agua para uso en animales y humanos. Mas específicamente, el agua residual o aguas negras (de cloaca) conteniendo contaminantes puede ser tratada efectivamente mediante la aplicación de fórmula o composición y procedimiento que se propone.Water purification for use in animals and humans. More specifically, wastewater or sewage (sewage) containing contaminants can be effectively treated by applying the formula or composition and procedure proposed.
Componentes naturales de la fórmula (composición):Natural components of the formula (composition):
AL (Aluminio) 0.0043 mg/kgAL (Aluminum) 0.0043 mg / kg
Ba (Bario) 0.0057 mg/kgBa (Barium) 0.0057 mg / kg
B (Boro) 0.0020 mg/kg Cr (Cromo) 0.005 mg/kgB (Boron) 0.0020 mg / kg Cr (Chrome) 0.005 mg / kg
Cd (Cadmio) O.0001 mg/kgCd (Cadmium) O,0001 mg / kg
Ca (Calcio) 43.9372 mg/kgCa (Calcium) 43.9372 mg / kg
Cu (Cobre) 0.007 mg/kgCu (Copper) 0.007 mg / kg
P (Fósforo) 0.3579 mg/kg Fe (Hierro) 0.1687 mg/kgP (Phosphorus) 0.3579 mg / kg Fe (Iron) 0.1687 mg / kg
Mg (Magnesio) 0.4591 mg/kgMg (Magnesium) 0.4591 mg / kg
Ni (Níquel) 0.005 mg/kgNi (Nickel) 0.005 mg / kg
Pb (Plomo) 0.0030 mg/kgPb (Lead) 0.0030 mg / kg
K (Potasio) 0.0958 mg/kg Na (Sodio) 0.0543 mg/kgK (Potassium) 0.0958 mg / kg Na (Sodium) 0.0543 mg / kg
Si (Silicio) 0.0972 mg/kgYes (Silicon) 0.0972 mg / kg
Zn (Zinc) 0.0062 mg/kgZn (Zinc) 0.0062 mg / kg
El procedimiento que se esta proponiendo se presenta en la siguiente descripción y en la figura que a continuación se describe:The procedure that is being proposed is presented in the following description and in the figure described below:
Figura 1: Diagrama de flujo del procedimiento que consta de seis etapas o pasos para el tratamiento de aguas residuales o aguas negras hasta obtener agua potable.Figure 1: Flow chart of the procedure consisting of six stages or steps for the treatment of wastewater or sewage to obtain potable water.
Etapas de Agitación e Incorporación de los elementos de la Fórmula.Stages of Agitation and Incorporation of the elements of the Formula.
En tiempo real y respetando el orden de los elementos contenidos en la fórmula anterior, se van incorporando de uno por uno con un intervalo de 10 minutos de separación en el agua residual o agua negra a tratar con una concentración de sólidos suspendidos de 452 por cada milímetro cúbico, la cual previamente se debe encontrar en un estado de agitación hasta por tres horas por cada 50metro cúbico producido por aspas, propelas, o cualquier otra forma de movimiento mecánico, con un movimiento o velocidad de oleaje de 350 kilogramos de presión de impacto en el área por centímetro 1 cm2 (un centímetro cuadrado).In real time and respecting the order of the elements contained in the previous formula, they are incorporated one by one with an interval of 10 minutes of separation in the wastewater or black water to be treated with a concentration of suspended solids of 452 per cubic millimeter, which must previously be in a state of agitation for up to three hours for every 50 cubic meter produced by blades, propels, or any another form of mechanical movement, with a movement or swell speed of 350 kilograms of impact pressure in the area per 1 cm2 centimeter (one square centimeter).
Etapa de Calentamiento-Ebullición.Heating-Boiling Stage.
El movimiento de ebullición por cambios de temperatura de 10 a 99 grados centígrados se obtiene por el calentamiento que resulta al hacer contacto los componentes de la fórmula con el agua residual o aguas negras a tratar, y se complementa con aplicación de calor por diferentes métodos de calentamiento, como pueden ser flama directa o celdas solares, el movimiento de impacto de ebullición es de 250 gramos en un área de prueba de Icm2 (un centímetro cuadrado).The boiling movement due to temperature changes of 10 to 99 degrees Celsius is obtained by the heating that results from contacting the components of the formula with the wastewater or sewage to be treated, and is complemented by heat application by different methods of heating, such as direct flame or solar cells, the boiling impact movement is 250 grams in a test area of Icm2 (one square centimeter).
Etapa de reposo y desconcentración de sólidos.Resting stage and deconcentration of solids.
La mezcla acuosa se deja en un periodo de reposo de 3 horas, en éste lapso de tiempo se produce una reacción de desconcentración de los sólidos suspendidos con parámetros de 150 a 800 por cada miligramo cúbico, obteniéndose una limpieza por desconcentración de sólidos suspendidos de un 80% por miligramo cúbico.The aqueous mixture is left in a rest period of 3 hours, during this time there is a deconcentration reaction of suspended solids with parameters of 150 to 800 per cubic milligram, obtaining a cleaning by deconcentration of suspended solids of a 80% per cubic milligram.
Los sólidos suspendidos descienden al fondo del tanque o lecho del río, siendo un lodo completamente inerte.Suspended solids descend to the bottom of the tank or riverbed, being a completely inert mud.
Etapas de Filtración y Oxigenación. El proceso que se esta presentando también consta de una etapa de filtración y una de oxigenación, que es importante mencionarla porque es parte del proceso para la obtención del agua potable, pero pueden ser utilizados cualquiera de los procesos de filtración y oxigenación conocidos dentro del estado de la técnica para el tratamiento de aguas residuales y por lo tanto no son materia de reclamo.Filtration and oxygenation stages. The process that is being presented also consists of a filtration stage and an oxygenation stage, which is important to mention because it is part of the process for obtaining drinking water, but any of the known filtration and oxygenation processes within the state can be used of the technique for the treatment of wastewater and therefore are not a matter of complaint.
Los lodos que se obtienen o que resultan por la técnica descrita (fórmula y proceso) son residuos completamente inertes, libres de cualquier bacteria o larva, que tienen excelentes características de sedimentación y con propiedades naturales para ser utilizados como fertilizantes en tierras de cultivo, aplicar en acuacultivos o 'como activador biológico para lagos, estanques y análogos, sin riesgo de contaminación. A diferencia de los lodos que resultan de otros tratamientos de aguas residuales, en donde es necesario darle un tratamiento específico a dichos lodos como el que menciona la solicitud patente europea No. 99946262.5, en nuestro proceso no es necesario dar a los lodos ningún tratamiento especial para su destrucción, es más como ya se menciono anteriormente, éste lodo es utilizable como materia nutriente en diversas áreas.The sludges that are obtained or that result from the described technique (formula and process) are completely inert residues, free of any bacteria or larvae, which have excellent sedimentation characteristics and with natural properties to be used as fertilizers in farmland, applied in aquaculture or 'as a biological activator for lakes, ponds and the like, without risk of contamination. Unlike sludge that results from other wastewater treatments, where it is necessary to give a specific treatment to such sludges as the one mentioned in European patent application No. 99946262.5, in our process it is not necessary to give the sludge any special treatment For its destruction, it is more as already mentioned above, this mud is usable as a nutrient in various areas.
A continuación se transcribe un ejemplo que ilustra el procedimiento, incluido el mejor modo. Este no se debe de interpretar como limitativo sino solamente a manera de ilustración del procedimiento.An example that illustrates the procedure, including the best mode, is transcribed below. This should not be construed as limiting but only as an illustration of the procedure.
Ejemplo 1.Example 1.
Agua tratada del río Lerma.Treated water of the Lerma river.
Se tomaron 30 litros de agua contaminada del río Lerma, se tomo la temperatura que resulto de 21 grados, se midió el PH que resulto de 12.5 y el peso específico de los sólidos fueron 1,150 sólidos por centímetro cúbico, se procedió a dar agitación al agua con un movimiento de tracción mecánica, mientras el agua siga agitándose se van incorporando de uno en uno los elementos de la fórmula que estamos protegiendo con un intervalo de separación de 10 minutos entre ellos, posteriormente se tomo la temperatura y dio como resultado 90 grados centígrados por lo tanto se procedió a aplicar calor a través de flama directa, se volvió a tomar la temperatura y se siguió aplicando calor hasta llegar a los 99 grados centígrados. La mezcla se dejo en reposo, y en los primeros 30 minutos se empezó a ver la desconcentración inicial de los sólidos, se tomo una muestra y se coloco en un matraz con escala de uno a diez del volumen de un litro, ahí se observo la desconcentración de sólidos, si la reacción fue efectiva, los sólidos se desplazan hasta el fondo del tanque, y se obtiene después de tres horas agua limpia libre de sólidos. Posteriormente se realizan las etapas de Filtración y Oxigenación para obtener el agua potable conforme a las reglas de potabilización. 30 liters of contaminated water were taken from the Lerma River, the temperature resulting from 21 degrees was taken, the pH resulting from 12.5 was measured and the specific weight of the solids was 1,150 solids per cubic centimeter, water was stirred With a mechanical traction movement, while the water continues to stir, the elements of the formula that we are protecting are incorporated one by one, with a separation interval of 10 minutes between them, then the temperature was taken and resulted in 90 degrees Celsius therefore, heat was applied through direct flame, the temperature was taken again and heat was applied until it reached 99 degrees Celsius. The mixture was left at rest, and in the first 30 minutes the initial deconcentration of the solids began to be seen, a sample was taken and placed in a flask with a scale of one to ten of the volume of a liter, there was observed solids deconcentration, if the reaction was effective, the solids move to the bottom of the tank, and clean water free of solids is obtained after three hours. Subsequently, the Filtration and Oxygenation stages are carried out to obtain drinking water according to the drinking water rules.

Claims

REIVINDICACIONES
1. Fórmula o Composición para tratamiento de aguas residuales y aguas negras para obtener agua potable a base de los siguientes elementos naturales: AL (Aluminio) 0.0043 mg/kg, Ba (Bario) 0.0057 mg/kg, B (Boro) 0.0020 mg/kg, Cr (Cromo) 0.005 mg/kg, Cd (Cadmio) O.0001 mg/kg, Ca (Calcio) 43.93.72 mg/kg, Cu (Cobre) 0.007 mg/kg, P (Fósforo) 0.3579 mg/kg, Fe (Hierro) 0.1687 mg/kg, Mg (Magnesio) 0.4591 mg/kg, Ni (Níquel) 0.005 mg/kg, Pb (Plomo) 0.0030 mg/kg, K (Potasio) 0.0958 mg/kg, Na (Sodio) 0.0543 mg/kg, Si (Silicio) 0.0972 mg/kg, Zn (Zinc) 0.0062 mg/kg.1. Formula or Composition for wastewater and sewage treatment to obtain drinking water based on the following natural elements: AL (Aluminum) 0.0043 mg / kg, Ba (Barium) 0.0057 mg / kg, B (Boron) 0.0020 mg / kg, Cr (Chrome) 0.005 mg / kg, Cd (Cadmium) O.0001 mg / kg, Ca (Calcium) 43.93.72 mg / kg, Cu (Copper) 0.007 mg / kg, P (Phosphorus) 0.3579 mg / kg , Fe (Iron) 0.1687 mg / kg, Mg (Magnesium) 0.4591 mg / kg, Ni (Nickel) 0.005 mg / kg, Pb (Lead) 0.0030 mg / kg, K (Potassium) 0.0958 mg / kg, Na (Sodium) 0.0543 mg / kg, Si (Silicon) 0.0972 mg / kg, Zn (Zinc) 0.0062 mg / kg.
2. Fórmula o Composición para tratamiento de aguas residuales o aguas negras para obtener agua potable según la reivindicación No. 1, caracterizada, porque también puede elaborarse a base de elementos sintéticos.2. Formula or Composition for treatment of wastewater or sewage to obtain drinking water according to claim No. 1, characterized in that it can also be made from synthetic elements.
3. Procedimiento para tratamiento agua residual o aguas negras para obtener agua potable, incluyendo dicho método los siguientes pasos:3. Procedure for treatment of wastewater or sewage to obtain drinking water, including said method the following steps:
A) Agitación del agua a tratar a través de un movimiento mecánico.A) Stirring of the water to be treated through a mechanical movement.
B) Incorporación de los elementos de la fórmula o composición, al agua a tratar.B) Incorporation of the elements of the formula or composition, to the water to be treated.
C) Calentamiento y ebullición del agua a tratar por la incorporación de la composición y por aplicación de calor.C) Heating and boiling of the water to be treated by the incorporation of the composition and by application of heat.
D) Etapa de reposo y desconcentración de sólidos suspendidos.D) Stage of rest and deconcentration of suspended solids.
E) Filtración del agua a tratada.E) Filtration of treated water.
F) Oxigenación del agua a tratada.F) Oxygenation of treated water.
4. Procedimiento según la reivindicación No. 3, caracterizado por que en la etapa de agitación A), el agua a tratar se agita por tres horas en un parámetro de 50 metros cúbicos, producido por aspas, propelas, o cualquier otra forma de movimiento mecánico.4. Method according to claim No. 3, characterized in that in the stirring stage A), the water to be treated is stirred for three hours in a parameter of 50 cubic meters, produced by blades, propels, or any other form of movement mechanic.
5. Procedimiento según la reivindicación No. 3, caracterizado por que en la etapa B), se van incorporando de uno en uno con un intervalo de 10 minutos de diferencia los elementos naturales siguientes: AL (Aluminio) 0.0043 mg/kg, Ba (Bario) 0.0057 mg/kg, B (Boro) 0.0020, Cr (Cromo) 0.005 mg/kg, Cd (Cadmio) O.0001 mg/kg, Ca (Calcio) 43.9372 mg/kg, Cu (Cobre) 0.007 mg/kg, P (Fósforo) 0.3579 mg/kg, Fe (Hierro) 0.1687 mg/kg, Mg (Magnesio) 0.4591 mg/kg, Ni (Níquel) 0.005 mg/kg, Pb (Plomo) 0.0030 mg/kg, K (Potasio) 0.0958 mg/kg, Na (Sodio) 0.0543 mg/kg, Si (Silicio) 0.0972 mg/kg, Zn (Zinc) 0.0062 mg/kg.5. Method according to claim No. 3, characterized in that in step B), the following natural elements are incorporated one by one with a 10 minute difference interval: AL (Aluminum) 0.0043 mg / kg, Ba ( Barium) 0.0057 mg / kg, B (Boron) 0.0020, Cr (Chrome) 0.005 mg / kg, Cd (Cadmium) O.0001 mg / kg, Ca (Calcium) 43.9372 mg / kg, Cu (Copper) 0.007 mg / kg, P ( Phosphorus) 0.3579 mg / kg, Fe (Iron) 0.1687 mg / kg, Mg (Magnesium) 0.4591 mg / kg, Ni (Nickel) 0.005 mg / kg, Pb (Lead) 0.0030 mg / kg, K (Potassium) 0.0958 mg / kg, Na (Sodium) 0.0543 mg / kg, Si (Silicon) 0.0972 mg / kg, Zn (Zinc) 0.0062 mg / kg.
6. Procedimiento según la reivindicación No. 3, caracterizado porque en la etapa C) al agua a tratar se le aplica calor hasta alcanzar una temperatura 99 grados centígrados, la cual se obtiene por el calentamiento que resulta al hacer contacto los componentes de la fórmula con el agua residual o aguas negras a tratar, y se complementa con aplicación de calor por diferentes métodos de calentamiento, como pueden ser flama directa o celdas solares.6. Method according to claim No. 3, characterized in that in stage C) the water to be treated is applied heat to reach a temperature 99 degrees Celsius, which is obtained by the heating that results when the components of the formula make contact with the wastewater or sewage to be treated, and it is complemented with heat application by different heating methods, such as direct flame or solar cells.
7. Procedimiento según la reivindicación No. 3, caracterizado porque en la etapa D) el agua que se esta tratando se deja en reposo durante un periodo de 3 horas.7. Method according to claim No. 3, characterized in that in step D) the water being treated is left standing for a period of 3 hours.
8. Procedimiento según la reivindicación No. 3, caracterizado porque en la etapa D) se produce una reacción de desconcentración de los sólidos suspendidos con parámetros de 800 a 120 por cada miligramo cúbico, obteniéndose una limpieza por desconcentración de sólidos suspendidos de un 80% por miligramo cúbico.Method according to claim No. 3, characterized in that in stage D) there is a deconcentration reaction of suspended solids with parameters of 800 to 120 per cubic milligram, obtaining a cleaning by deconcentration of suspended solids of 80% per cubic milligram.
9. Procedimiento según la reivindicación No. 3 caracterizado porque durante la etapa de filtración E), se puede agregar hipoclorito de sodio para regular el PH del agua tratada.9. Method according to claim No. 3 characterized in that during the filtration stage E), sodium hypochlorite can be added to regulate the pH of the treated water.
10. Procedimiento según la reivindicación No. 3 en donde es caracterizado porque el agua que se obtiene es de un PH del 7.5 a 8.5.10. Method according to claim No. 3 wherein it is characterized in that the water obtained is from a pH of 7.5 to 8.5.
11. Un lodo o sedimento que es inerte, libre de contaminantes, y utilizable como material nutriente o composta, caracterizado porque es obtenido a través del procedimiento comprendido en las reivindicaciones de la 3 a la 10. 11. A sludge or sediment that is inert, free of contaminants, and usable as a nutrient or compost material, characterized in that it is obtained through the procedure included in claims 3 to 10.
PCT/MX2005/000044 2005-06-09 2005-06-09 Composition and method for the treatment of wastewater and sewage water in order to produce drinking water WO2006132519A1 (en)

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CN102653428A (en) * 2012-04-15 2012-09-05 同济大学 Pretreatment method for separating impurities from water
CN102745834A (en) * 2011-08-02 2012-10-24 深圳城市诺必达节能环保有限公司 Household reclaimed water treatment method and reutilization apparatus
CN103112967A (en) * 2013-02-28 2013-05-22 孟兵川 Oilfield sewage cyclone disturbance treatment method and device
CN104071920A (en) * 2014-08-07 2014-10-01 南通润启时装有限公司 Printing and dyeing wastewater treatment process
CN105399235A (en) * 2015-08-26 2016-03-16 李纳 Domestic drinking water combination treatment method
CN109293089A (en) * 2018-10-29 2019-02-01 甘肃银光聚银化工有限公司 A kind of processing method of TDI production neutral and alkali brine waste

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102745834A (en) * 2011-08-02 2012-10-24 深圳城市诺必达节能环保有限公司 Household reclaimed water treatment method and reutilization apparatus
CN102653428A (en) * 2012-04-15 2012-09-05 同济大学 Pretreatment method for separating impurities from water
CN102653428B (en) * 2012-04-15 2014-01-29 同济大学 Pretreatment method for separating impurities from water
CN103112967A (en) * 2013-02-28 2013-05-22 孟兵川 Oilfield sewage cyclone disturbance treatment method and device
CN104071920A (en) * 2014-08-07 2014-10-01 南通润启时装有限公司 Printing and dyeing wastewater treatment process
CN105399235A (en) * 2015-08-26 2016-03-16 李纳 Domestic drinking water combination treatment method
CN109293089A (en) * 2018-10-29 2019-02-01 甘肃银光聚银化工有限公司 A kind of processing method of TDI production neutral and alkali brine waste

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