WO2006056620A1 - Purinox, machine for purine treatment and industrial processes - Google Patents

Purinox, machine for purine treatment and industrial processes Download PDF

Info

Publication number
WO2006056620A1
WO2006056620A1 PCT/ES2004/000505 ES2004000505W WO2006056620A1 WO 2006056620 A1 WO2006056620 A1 WO 2006056620A1 ES 2004000505 W ES2004000505 W ES 2004000505W WO 2006056620 A1 WO2006056620 A1 WO 2006056620A1
Authority
WO
WIPO (PCT)
Prior art keywords
liquid
solid
machine
separator
filter
Prior art date
Application number
PCT/ES2004/000505
Other languages
Spanish (es)
French (fr)
Inventor
Tomás CAVERO MECINAS
Pedro Cavero Mecinas
Emilio Cavero Mecinas
Original Assignee
Polinox-Galicia, S.A.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Polinox-Galicia, S.A. filed Critical Polinox-Galicia, S.A.
Priority to PCT/ES2004/000505 priority Critical patent/WO2006056620A1/en
Priority to PCT/ES2005/000291 priority patent/WO2006053914A1/en
Publication of WO2006056620A1 publication Critical patent/WO2006056620A1/en

Links

Classifications

    • 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
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01CPLANTING; SOWING; FERTILISING
    • A01C3/00Treating manure; Manuring
    • 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
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/441Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
    • 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
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/442Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by nanofiltration
    • 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
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/444Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
    • 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
    • C02F2103/20Nature of the water, waste water, sewage or sludge to be treated from animal husbandry
    • 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
    • C02F2103/32Nature of the water, waste water, sewage or sludge to be treated from the food or foodstuff industry, e.g. brewery waste waters
    • C02F2103/322Nature of the water, waste water, sewage or sludge to be treated from the food or foodstuff industry, e.g. brewery waste waters from vegetable oil production, e.g. olive oil production
    • 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
    • C02F2103/32Nature of the water, waste water, sewage or sludge to be treated from the food or foodstuff industry, e.g. brewery waste waters
    • C02F2103/325Nature of the water, waste water, sewage or sludge to be treated from the food or foodstuff industry, e.g. brewery waste waters from processes relating to the production of wine products
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage

Definitions

  • the machine in its first phase uses a pump submerged in the slurry pit that pumps the slurry to the solids separator, object of patent claim and the indicated characteristics, within which a separation of the solid from the liquid is carried out by means of a hydraulic process based on compressing the slurry inside the separator so that it expels all the water it contains; being able to obtain a solid product with the necessary degree of humidity so that it serves as fertilizer for the field.
  • Said separator presents an improvement to make the separation of beef slurries, as well as with the pig slurry and different industrial processes.
  • a pressure liquid solid separator that consists of an external housing that houses the separator unit inside, which in turn serves as a collection of the separated liquids and on which the hydraulic systems are mounted and solids outlet.
  • the internal solid and liquid separator consists of a filter mesh whose hole diameter increases or decreases depending on the product that we are going to separate, and has a special oval design for the easy expulsion of liquid without getting stuck.
  • the entire system is built entirely in stainless steel, and whose size will be larger or smaller depending on the amount of product to be purified per hour.
  • the liquid obtained from said separation the machine subjects it to a cascade microfiltration.
  • Said microfiltration is carried out in the filter unit composed of reactors, object of patent claim, made of stainless steel, whose construction consists of a cylindrical housing with two pointed caps fastened by means of easy-to-open popcorn; inside it houses two rings that in turn support the filter mesh made of sintered stainless steel, on which liquid is sent under pressure at one end; cleaning vanes clean the filter surface through an axis driven by a hydraulic or electric motor that turns round; at the same time, said shaft has other vanes that drive the solid that is being lodged in the solids outlet hopper towards the opposite side of the filter.
  • the filter By the continuous cleaning that the cleaning vanes exert on the filter surface, the filter is prevented from being clogged and that it remains always clean since the solids that remain inside are thrown outside by the outlet hopper automatically, so Said filter unit has unlimited filtration capacity, being able to operate both manually and automatically, and the size of which can vary depending on the amount of liquid to be filtered.
  • the micron mesh In the thickest phase of filtering, the micron mesh is used as the first filter
  • i SUBSTITUTE SHEET (RULE 26) that best suits this thickness, from which the liquid is subjected to a smaller and smaller micrometer filter, being able to reach in its final phase until a miera.
  • the passage of liquid from one reactor to another can be carried out with very large differences of micrometer, being able to pass a filtered product at 1000 microns, to another reactor where it would be filtered directly at 100 microns.
  • the filter never gets clogged since the solids that remain inside are thrown by a hopper automatically. In said process virtually all the solid matter in suspension is eliminated; as well as the different chemical and bacteriological components that they contain and are dissolved in the liquid once separated are minimized.
  • the liquid passes through a cyclone separator of suspended particles.
  • the suspended cyclone particle separator cleans the liquid; said liquid enters tangentially in the upper part of the cyclone and is concentrated below in the inner wall of the cyclone as a result of the rotating movement clockwise.
  • the particles are subjected to an agglomeration process, which causes them to decant towards the bottom, where the drainage point is.
  • the clean liquid is brought back up in a rotating vortex opposite the drain, the liquid comes out through the central upper outlet.
  • the cyclone separator has no moving parts and operates automatically.
  • the liquid then passes to the liquid residence tank where it is for an estimated time of 24 hours and is subjected to an ozone-based purification generated by the machine itself in an oxygen to ozone transformer, which it is injected into the liquid in the precise amount by a dosing pump and an ejector, which removes all organic matter and contaminants in a total way, leaving a harmless, odorless and colorless liquid with a total clearance and a level of COD and BOD that complies with current legislation in Europe for discharge at public flow.
  • an ozone-based purification generated by the machine itself in an oxygen to ozone transformer, which it is injected into the liquid in the precise amount by a dosing pump and an ejector, which removes all organic matter and contaminants in a total way, leaving a harmless, odorless and colorless liquid with a total clearance and a level of COD and BOD that complies with current legislation in Europe for discharge at public flow.
  • This final third phase admits variants such as liquid purification by biological purification, through a biological reactor; another variant that could be presented is through ultraviolet rays; Another variant is the biochemical, biological and chemical half purification consisting of a mixture of chemical products with biological products, all of them would also comply with current legislation on discharge at public flow.
  • the purification machine in its operation of both purification and self-cleaning, does so in total automatic mode and not manual; is programmed through a computer (PLC),
  • SUBSTITUTE SHEET (RULE 26) which tells the machine when there is purin to purify, when there is not and if it has to stop as well as periodic washing, so that the hand of man does not intervene if it is not necessary, or in any case, you can choose for doing the operation manually.
  • the entire electrical system is mounted with its protection systems according to current regulations.
  • the inventors of the present application have had to design and manufacture both the machine, as well as the solid separator, as well as the filter unit composed of the microfuction reactors since in the national or international market there is no machine that makes a total separation of solids and liquid purification by mechanical means.
  • Figure 2 shows the solid separator, with all its elements: 01- Hydraulic thrust cylinder, this cylinder compresses the product to be treated inside the filter,
  • 03- Separator filter consists of a cylinder with open slots that, depending on the product to be purified, are larger or smaller and have a special design so that they do not close when the product is compressed inside it.
  • 04- Pushing tongue consists of an 8mm round disk. thick and with a diameter similar to that of the filter, it is attached to the thrust cylinder and drags the entire product to the opening cylinder.
  • Peephole consists of an opening made in the housing that collects liquids and allows us to look inside the separator.
  • 06- Pressure tab and opening of solids consists of a disc that can be made of stainless or Teflon with 20mm. of thickness finished in cone, on which all the product to be separated is compressed and that once expelled the liquid opens automatically and allows to expel the solid.
  • N ° 24- Cleaning ball to expand the water inside the filter for periodic cleaning of the same
  • N ° 26- Housing circular or square, with two closing and opening lids at its ends and solid ejection hopper and which in turn serves as support and housing for the entire filtration unit.
  • Figure 5 shows the cyclone particle separator

Abstract

The invention relates to a machine that is used for the treatment of purines mainly from pigs and cattle, as well as for certain industrial processes. The inventive machine is installed in situ without requiring any construction work. The treatment process consists in first separating the solid from the liquid using a solid separator and liquid-separating filter units. The resulting liquid is purified of all suspended particles using a cyclone particle separator and of contaminants using a system for the treatment of organic matter by means of ozone injection. The level of contamination in both the solid and the liquid is kept to a minimum, such that the solid can be used as fertiliser and the liquid can be recycled or dumped. The treatment process is performed automatically in situ at a reasonable cost. According to the invention, the entire treatment phase, from obtaining the waste to producing the treated end product, is performed in a single machine.

Description

Descripción de la invención: El funcionamiento principal de la máquina se hace a través del sistema hidráulico, un generador de energía hidráulica, de esta manera con un solo motor eléctrico de baja potencia obtenemos los movimientos necesarios para su funcionamiento. Description of the invention: The main operation of the machine is done through the hydraulic system, a hydraulic power generator, in this way with a single low power electric motor we obtain the necessary movements for its operation.
La máquina en su primera fase se sirve de una bomba sumergida en la fosa del purín que bombea el purín al separador de sólidos, objeto de reivindicación de patente y de las características indicadas, dentro del cual se efectúa una separación del sólido del líquido mediante un proceso hidráulico basado en comprimir el purín dentro del separador de forma que expulsa todo el agua que contiene; pudiendo obtener un producto sólido con el grado de humedad necesario para que sirva como abono para el campo. Dicho separador presenta una mejora para hacer la separación de los purines de vacuno, así como con el purín de cerdo y de diferentes procesos industriales. Sus principales características consisten en un separador de sólido de líquido por presión que consta de una carcasa externa que aloja en su interior a la unidad separadora, que a su vez nos sirve como recogida de los líquidos separados y sobre la cual van montados los sistemas hidráulicos y salida de sólidos. El separador interno de sólidos y líquido consiste en una malla filtrante cuyo diámetro de agujero aumenta o disminuye dependiendo del producto que vayamos a separar, y tiene un diseño especial ovalado para la fácil expulsión de líquido sin que se atasque. Todo el sistema está construido en su totalidad en acero inoxidable, y cuyo tamaño será mayor o menor dependiendo de la cantidad de producto a depurar por hora. En una segunda fase, el líquido que se obtiene de dicha separación, la máquina lo somete a una microfiltración en cascada. Dicha microfiltración se realiza en la unidad filtrante compuesta por reactores, objeto de reivindicación de patente, fabricada en acero inoxidable, cuya construcción consiste en una carcasa cilindrica con dos tapas en punta sujetas mediante palomillas de fácil apertura; en su interior aloja dos arillos que a su vez sustentan la malla filtrante construida en acero inoxidable sinterizado, sobre la cual se le manda líquido a presión por un extremo; unas paletas limpiadoras limpian la superficie filtrante a través de un eje movido por un motor hidráulico o eléctrico que gira en redondo; a su vez dicho eje tiene otras paletas que impulsan hacia la parte contraria del filtro el sólido que a su vez se va alojando en la tolva de salida de sólidos. Por la continua limpieza que ejercen las paletas limpiadoras sobre la superficie filtrante se evita que el filtro se cólmate y que permanezca siempre limpio ya que los sólidos que quedan en el interior son arrojados al exterior por la tolva de salida de forma automática, por lo cual dicha unidad filtrante tiene una capacidad de filtración ilimitada, pudiendo funcionar tanto en manual como en automático, y cuyo tamaño puede variar dependiendo de la cantidad de líquido a filtrar. En la fase más gruesa de filtrado se usa como primer filtro la malla de micrajeThe machine in its first phase uses a pump submerged in the slurry pit that pumps the slurry to the solids separator, object of patent claim and the indicated characteristics, within which a separation of the solid from the liquid is carried out by means of a hydraulic process based on compressing the slurry inside the separator so that it expels all the water it contains; being able to obtain a solid product with the necessary degree of humidity so that it serves as fertilizer for the field. Said separator presents an improvement to make the separation of beef slurries, as well as with the pig slurry and different industrial processes. Its main features consist of a pressure liquid solid separator that consists of an external housing that houses the separator unit inside, which in turn serves as a collection of the separated liquids and on which the hydraulic systems are mounted and solids outlet. The internal solid and liquid separator consists of a filter mesh whose hole diameter increases or decreases depending on the product that we are going to separate, and has a special oval design for the easy expulsion of liquid without getting stuck. The entire system is built entirely in stainless steel, and whose size will be larger or smaller depending on the amount of product to be purified per hour. In a second phase, the liquid obtained from said separation, the machine subjects it to a cascade microfiltration. Said microfiltration is carried out in the filter unit composed of reactors, object of patent claim, made of stainless steel, whose construction consists of a cylindrical housing with two pointed caps fastened by means of easy-to-open popcorn; inside it houses two rings that in turn support the filter mesh made of sintered stainless steel, on which liquid is sent under pressure at one end; cleaning vanes clean the filter surface through an axis driven by a hydraulic or electric motor that turns round; at the same time, said shaft has other vanes that drive the solid that is being lodged in the solids outlet hopper towards the opposite side of the filter. By the continuous cleaning that the cleaning vanes exert on the filter surface, the filter is prevented from being clogged and that it remains always clean since the solids that remain inside are thrown outside by the outlet hopper automatically, so Said filter unit has unlimited filtration capacity, being able to operate both manually and automatically, and the size of which can vary depending on the amount of liquid to be filtered. In the thickest phase of filtering, the micron mesh is used as the first filter
i HOJA DE SUSTITUCIÓN (REGLA 26) que mejor se adapte a dicho grosor, a partir del cual se va sometiendo el líquido a un filtro de micraje cada vez más pequeño, pudiendo llegar en su fase final hasta una miera. El paso de líquido de un reactor a otro puede realizarse con unas diferencias de micraje muy grandes, pudiendo pasar un producto filtrado a 1000 mieras, a otro reactor donde se filtraría directamente a 100 mieras. El filtro no se colmata nunca ya que los sólidos que quedan en su interior son arrojados por una tolva de manera automática. En dicho proceso se elimina prácticamente la totalidad de materia sólida en suspensión; así como también se ven disminuidos hasta la mínima expresión los diferentes componentes químicos y bacteriológicos que contienen y están disueltos en el líquido una vez separado. En una tercera fase, el líquido pasa por un separador ciclónico de partículas en suspensión. El separador ciclónico de partículas en suspensión limpia el líquido; dicho líquido entra tangencialmente en la parte superior del ciclón y se concentra por abajo en la pared interna del ciclón como consecuencia del movimiento giratorio en el sentido de las agujas del reloj. Cuando el liquido alcanza la zona más estrecha, las partículas son sometidas a un proceso de aglomeración, lo que hace que decanten hacia la parte inferior, donde está el punto de drenaje. El líquido limpio es llevado de nuevo hacia arriba en un vórtice rotativo opuesto al drenaje, el líquido sale fuera a través de la toma de salida superior central. El separador ciclónico no tiene ninguna parte móvil y opera automáticamente. Se consigue así que tras la entrada de líquido con una cantidad ínfima de partículas en suspensión, se eliminen estas y se produce la salida del líquido libre de partículas sólidas en suspensión, pero con una gran carga de materia orgánica y otros contaminantes como Nitrógeno, Potasio y la DQO y DBO, el líquido pasa entonces al tanque de residencia de líquidos donde está durante un tiempo estimado de 24 horas y se le somete a una depuración a base de ozono generado por la propia máquina en un transformador de oxígeno a ozono, que es inyectado al liquido en la cantidad precisa por una bomba dosificadora y un eyector, que elimina toda la materia orgánica y contaminantes de una forma total, quedando un líquido inocuo, sin olor e incoloro con una depuración total y un nivel de DQO y DBO que cumple la legislación vigente en Europa para vertido a caudal público.i SUBSTITUTE SHEET (RULE 26) that best suits this thickness, from which the liquid is subjected to a smaller and smaller micrometer filter, being able to reach in its final phase until a miera. The passage of liquid from one reactor to another can be carried out with very large differences of micrometer, being able to pass a filtered product at 1000 microns, to another reactor where it would be filtered directly at 100 microns. The filter never gets clogged since the solids that remain inside are thrown by a hopper automatically. In said process virtually all the solid matter in suspension is eliminated; as well as the different chemical and bacteriological components that they contain and are dissolved in the liquid once separated are minimized. In a third phase, the liquid passes through a cyclone separator of suspended particles. The suspended cyclone particle separator cleans the liquid; said liquid enters tangentially in the upper part of the cyclone and is concentrated below in the inner wall of the cyclone as a result of the rotating movement clockwise. When the liquid reaches the narrowest area, the particles are subjected to an agglomeration process, which causes them to decant towards the bottom, where the drainage point is. The clean liquid is brought back up in a rotating vortex opposite the drain, the liquid comes out through the central upper outlet. The cyclone separator has no moving parts and operates automatically. It is thus achieved that after the entry of liquid with a very small amount of suspended particles, these are eliminated and the liquid free from solid particles in suspension is produced, but with a large load of organic matter and other contaminants such as Nitrogen, Potassium and the COD and BOD, the liquid then passes to the liquid residence tank where it is for an estimated time of 24 hours and is subjected to an ozone-based purification generated by the machine itself in an oxygen to ozone transformer, which it is injected into the liquid in the precise amount by a dosing pump and an ejector, which removes all organic matter and contaminants in a total way, leaving a harmless, odorless and colorless liquid with a total clearance and a level of COD and BOD that complies with current legislation in Europe for discharge at public flow.
Esta fase tercera final admite variantes como son la depuración del liquido por depuración biológica, a través de un reactor biológico; otra variante que se podría presentar es a través de rayos ultravioleta; otra variante es la depuración bioquímica, mitad biológica y mitad química que consiste en una mezcla de productos químicos con productos biológicos, todas ellas igualmente cumplirían la legislación vigente de vertido a caudal público.This final third phase admits variants such as liquid purification by biological purification, through a biological reactor; another variant that could be presented is through ultraviolet rays; Another variant is the biochemical, biological and chemical half purification consisting of a mixture of chemical products with biological products, all of them would also comply with current legislation on discharge at public flow.
La máquina depuradora en su funcionamiento tanto de depuración como de autolimpieza, lo hace en modo automático total y no manual; está programada a través de un ordenador ( PLC),The purification machine in its operation of both purification and self-cleaning, does so in total automatic mode and not manual; is programmed through a computer (PLC),
22
HOJA DE SUSTITUCIÓN (REGLA 26) el cual le dice a la máquina cuándo hay purín que depurar, cuándo no lo hay y si tiene que parar así como los lavados periódicos, de manera que no interviene la mano del hombre si no es necesario, o en todo caso, se puede optar por hacer el funcionamiento de forma manual. Todo el sistema eléctrico está montado con sus sistemas de protección según la normativa vigente. Los inventores de la presente solicitud han tenido que diseñar y fabricar tanto la máquina, como el separador sólidos, así como la unidad filtrante compuesta por los reactores de microfütración puesto que en el mercado nacional ni internacional no existe ninguna máquina que haga una separación total de sólidos y depuración de líquidos por medios mecánicos. Descripción de los dibujos: Para complementar la descripción que se está realizando y con objeto de ayudar a una mejor comprensión de las características del invento, se acompaña a la presente memoria descriptiva, como parte integrante de la misma, un juego de dibujos en donde con carácter ilustrativo y no limitativo donde se representa la máquina en su totalidad con todos sus componentes: La figura 1 muestra la máquina en su totalidad con todos sus componentes:SUBSTITUTE SHEET (RULE 26) which tells the machine when there is purin to purify, when there is not and if it has to stop as well as periodic washing, so that the hand of man does not intervene if it is not necessary, or in any case, you can choose for doing the operation manually. The entire electrical system is mounted with its protection systems according to current regulations. The inventors of the present application have had to design and manufacture both the machine, as well as the solid separator, as well as the filter unit composed of the microfuction reactors since in the national or international market there is no machine that makes a total separation of solids and liquid purification by mechanical means. Description of the drawings: To complement the description that is being made and in order to help a better understanding of the characteristics of the invention, a set of drawings is attached as an integral part thereof, with Illustrative and non-limiting character where the machine is represented in its entirety with all its components: Figure 1 shows the machine in its entirety with all its components:
01 Fosa de purín; 02 Bomba sumergida de aspiración de purín; 03 Sonda de nivel; 04 manguera de trasvase de purín; 05 Entrada de purín; 06 separador de sólidos (FIG.02) separador de líquido de sólido por presión; 07 Bolas de limpieza, se utilizan cuando el separador necesita un lavado interno con arranque y tiempo de lavado automático; 08 Salida líquidos; 09 Circuito de entrada de líquidos; 10 entrada del líquido una vez separado del sólido; 11 conducción desde recipiente receptor de purín líquido a sistema de filtración; 12 bombas de entrada a reactores microfiltrantes; 13 Unidad filtrante (FIG.04); 14 Conducción desde recipiente receptor de líquido a segundo microfiltro; 15 Entrada de líquido microfiltrado a segundo recipiente; 16 Entrada de líquido microfiltrado a tercer recipiente; 17 Conducción desde recipiente receptor de líquido a tercer microfiltro; 18 Central hidráulica (FIG.03); 19 Conexiones de movimiento para el circuito; 20 Manómetro de presión; 21 Cuadro eléctrico; 22 Compresor y sistema de tratamiento de aire; 23 Ozonizador; 24 Bomba dosificadora de ozono; 25 Inyector de mezcla de ozono; 26 Tanque de residencia de líquidos, dosificación de ozono y depuración de materia orgánica; 27 Salida decantación de líquidos totalmente depurados; 28 Bomba de limpieza del separador de sólidos; 29 Salida de limpieza del tanque; 30 Salida sólidos; 31 Separador ciclónico de partículas en suspensión; 32 Entrada líquido con partículas en suspensión; 33 Salida líquido libre de partículas en suspensión.01 slurry pit; 02 Submerged slurry pump; 03 level probe; 04 slurry transfer hose; 05 Manure inlet; 06 solids separator (FIG. 02) solid pressure liquid separator; 07 Cleaning balls are used when the separator needs an internal wash with start-up and automatic wash time; 08 Liquid outlet; 09 Liquid inlet circuit; 10 liquid inlet once separated from the solid; 11 conduction from liquid slurry receiving vessel to filtration system; 12 input pumps to microfiltrating reactors; 13 Filter unit (FIG. 04); 14 Conduction from liquid receiving container to second microfilter; 15 Microfiltered liquid inlet to second container; 16 Microfiltered liquid inlet to third container; 17 Conduction from liquid receiving container to third microfilter; 18 Hydraulic power plant (FIG. 03); 19 Motion connections for the circuit; 20 Pressure gauge; 21 Electrical panel; 22 Compressor and air treatment system; 23 Ozonator; 24 Ozone dosing pump; 25 Ozone Blend Injector; 26 Liquid residence tank, ozone dosing and purification of organic matter; 27 Decanting out of fully purified liquids; 28 Solids separator cleaning pump; 29 Tank cleaning outlet; 30 solid output; 31 Cyclonic suspension of suspended particles; 32 Liquid inlet with suspended particles; 33 Liquid outlet free of suspended particles.
La figura 2 muestra el separador de sólidos, con todos sus elementos: 01- Cilindro hidráulico de empuje, este cilindro nos comprime el producto a depurar que hay dentro del filtro,Figure 2 shows the solid separator, with all its elements: 01- Hydraulic thrust cylinder, this cylinder compresses the product to be treated inside the filter,
3 HOJA DE SUSTITUCIÓN (REGLA 26) expulsando el líquido a través de las ranuras y comprimiendo el sólido contra la compuerta de cierre. Regulándole la presión podemos obtener un sólido separado con mayor o menor grado de humedad.3 SUBSTITUTE SHEET (RULE 26) expelling the liquid through the slots and compressing the solid against the closing gate. By regulating the pressure we can obtain a separate solid with a greater or lesser degree of humidity.
02- Bolas de limpieza, se utilizan cuando el separador necesita de un lavado interno; su arranque y tiempo de lavado se hace automáticamente.02- Cleaning balls, are used when the separator needs an internal wash; Its startup and washing time is done automatically.
03- Filtro separador, consiste en un cilindro con unas ranuras abiertas que dependiendo del producto a depurar son más grandes o más pequeñas y tienen un diseño especial para que no se cierren cuando se comprime el producto dentro de ella.03- Separator filter, consists of a cylinder with open slots that, depending on the product to be purified, are larger or smaller and have a special design so that they do not close when the product is compressed inside it.
04- Lengüeta de empuje, consiste en un disco redondo de 8mm. de espesor y con un diámetro similar al del filtro, va unido al cilindro de empuje y arrastra todo el producto hasta el cilindro de apertura.04- Pushing tongue, consists of an 8mm round disk. thick and with a diameter similar to that of the filter, it is attached to the thrust cylinder and drags the entire product to the opening cylinder.
05- Mirilla, consiste en una abertura efectuada en la carcasa que recoge los líquidos y que nos permite mirar en el interior del separador.05- Peephole, consists of an opening made in the housing that collects liquids and allows us to look inside the separator.
06- Lengüeta de presión y apertura de sólidos, consiste en un disco que puede ser de inoxidable o de teflón con 20mm. de espesor terminado en cono, sobre el cual se comprime todo el producto a separar y que una vez expulsado el líquido abre automáticamente y deja expulsar el sólido.06- Pressure tab and opening of solids, consists of a disc that can be made of stainless or Teflon with 20mm. of thickness finished in cone, on which all the product to be separated is compressed and that once expelled the liquid opens automatically and allows to expel the solid.
07- Cilindro hidráulico de presión y apertura para la expulsión de los sólidos una vez separado del líquido. 08- Tapa07- Hydraulic cylinder of pressure and opening for the expulsion of solids once separated from the liquid. 08- Cover
09- Carcasa, dentro de la cual se aloja el filtro separador y a su vez recoge los líquidos separados.09- Housing, in which the separator filter is housed and in turn collects the separated liquids.
10- Salida de sólidos10- Solids output
11- Cilindro hidráulico y válvula de apertura y cierre de entrada de purín en el separador. 12- Soporte de amarre del cilindro hidráulico.11- Hydraulic cylinder and valve for opening and closing slurry inlet in the separator. 12- Hydraulic cylinder mooring support.
13- Salida de líquidos.13- Liquid outlet.
14- Soportes de sujección del separador La figura 3 muestra la central hidráulica:14- Support brackets of the separator Figure 3 shows the hydraulic power plant:
N015- Conexiones de los circuitos hidráulicos del separador y filtraje. N°16- Manómetro indicador de presión.N 0 15- Connections of the hydraulic circuits of the separator and filtration. N ° 16- Pressure gauge pressure gauge.
N017- Motor.N 0 17- Motor.
N018- Electroválvulas de puesta en marcha y paro del circuito hidráulico del separador N019- Placa base, donde se montan todos los elementos de seguridad interna y de conexión para los diferentes circuitosN 0 18- Start and stop solenoid valves of the hydraulic circuit of the separator N 0 19- Base plate, where all internal safety and connection elements for the different circuits are mounted
4 HOJA DE SUSTITUCIÓN (REGLA 26) N°20- Válvulas de seguridad y de presión interna4 SUBSTITUTE SHEET (RULE 26) N ° 20- Safety and internal pressure valves
N°21- Bomba de presiónN ° 21- Pressure pump
N°22- Filtro de aceite.N ° 22- Oil filter.
N°23- Depósito recipiente de aceite. La figura 4 muestra la unidad filtrante:N ° 23- Oil container tank. Figure 4 shows the filter unit:
N°24- Bola de limpieza, para expandir el agua dentro del filtro para las limpiezas periódicas del mismoN ° 24- Cleaning ball, to expand the water inside the filter for periodic cleaning of the same
N°25- Entrada de líquido sin filtrarN ° 25- Unfiltered liquid inlet
N°26- Carcasa, de forma circular o cuadrada, con dos tapas de cierre y apertura en sus extremos y tolva de expulsión de sólidos y que a su vez sirve como soporte y alojamiento a toda la unidad de filtración.N ° 26- Housing, circular or square, with two closing and opening lids at its ends and solid ejection hopper and which in turn serves as support and housing for the entire filtration unit.
N°27- Compuertas desmontablesN ° 27- Detachable gates
N°28- Muelles de presión de sujección de malla filtranteN ° 28- Filter mesh clamping pressure springs
N°29- Arillos sujección filtros N°30- Filtro de acero inoxidable sinterizado intercambiable según el micraje del producto a depurar.N ° 29- Filter clamping rings N ° 30- Interchangeable sintered stainless steel filter according to the micraje of the product to be cleaned.
N°31- Salida de líquidos microfiltrados.N ° 31- Output of microfiltered liquids.
N°32- Cilindro hidráulico o motor eléctrico para abrir y cerrar el sistema de apertura y expulsión de sólidos N°33- Tolva, salida de sólidosN ° 32- Hydraulic cylinder or electric motor to open and close the opening and expulsion system of solids N ° 33- Hopper, solids outlet
N°34- Sistema de apertura y expulsión de sólidosN ° 34- Solid opening and ejection system
N°35- Paletas limpiadoras de la superficie filtranteN ° 35- Filter surface cleaning paddles
N°36- Muelle de presión de paletas limpiadorasN ° 36- Pressure spring of cleaning vanes
N°37- Paletas de expulsión de sólidos, expulsan hacia la parte trasera del filtro todos los sólidos que no pasan a través del filtro para su posterior salida por la tolva de descarga.N ° 37- Solids ejection vanes, expel all solids that do not pass through the filter to their rear exit through the discharge hopper.
N°38- Motor hidráulico o eléctrico que pone en movimiento todo el sistema de limpieza y expulsión de sólidos del filtroN ° 38- Hydraulic or electric motor that sets the entire filter solids and ejection system in motion
N°39- Eje motrizN ° 39- Drive shaft
N°40- Palomillas de apriete La figura 5, muestra el separador ciclónico de partículas:N ° 40- Clamping knobs Figure 5 shows the cyclone particle separator:
N°41.- Entrada de líquido con partículas en suspensiónN ° 41.- Liquid inlet with suspended particles
N°42.- Salida de partículas previamente en suspensiónN ° 42.- Exit of particles previously suspended
N°43. -Salida de líquido libre de partículas en suspensiónNo. 43 -Plug-free liquid exit in suspension
55
HOJA DE SUSTITUCIÓN (REGLA 26) SUBSTITUTE SHEET (RULE 26)

Claims

REIVINDICACIONES
1 . PURINOX, máquina para depuración de purines y procesos industriales, que realiza in situ el tratamiento de depuración total del purín o desecho desde que se genera hasta que se convierte en sólido y líquido aprovechables, en la que una fosa (1) dotada de una bomba de aspiración (2) y sonda de nivel (3) almacena el purín o desecho industrial, para ser trasvasado por una manguera de trasvase de purín (4), a un tanque o separador de sólidos (6) donde se separa el líquido del sólido por presión, y caracterizada por incorporar dicho separador de sólidos (6) consistente de una carcasa externa y un separador interno de malla filtrante de diseño especial ovalado que facilita la expulsión del líquido sin que se atasque, y dotada de unas bolas de limpieza (7) que se usan cuando la unidad separadora necesita un lavado.one . PURINOX, machine for purification of slurries and industrial processes, which performs in situ the treatment of total purification of the slurry or waste from when it is generated until it becomes solid and usable liquid, in which a pit (1) equipped with a pump suction (2) and level probe (3) stores the slurry or industrial waste, to be transferred by a slurry transfer hose (4), to a tank or solids separator (6) where the liquid is separated from the solid by pressure, and characterized by incorporating said solids separator (6) consisting of an external casing and an internal oval filter separator of special oval design that facilitates the expulsion of the liquid without clogging, and equipped with cleaning balls (7 ) that are used when the separator unit needs a wash.
2. PURINOX, máquina para depuración de purines y procesos industriales, conforme a la reivindicación Ia y caracterizada por incorporar unidades filtrantes o sistema de filtración de líquidos (13), que emplea como filtro mallas filtrantes sobre las cuales se proyecta el líquido a presión por un extremo, que es limpiado por unas paletas limpiadoras movidas por un eje que es movido por un motor hidráulico o eléctrico que gira en redondo y a su vez dicho eje tiene otras paletas que impulsan hacia la parte contraria del filtro el sólido que se va alojando en la tolva de salida de sólidos. La continua limpieza que ejercen las paletas limpiadoras evita que el filtro se cólmate y que los sólidos que quedan en el interior sean arrojados al exterior por la tolva de salida de forma automática.2. PURINOX, machine for purification of slurry and industrial processes, according to claim I a and characterized by incorporating filter units or liquid filtration system (13), which uses as filter filters meshes on which the liquid under pressure is projected at one end, which is cleaned by cleaning vanes moved by an axis that is moved by a hydraulic or electric motor that rotates round and in turn said axis has other vanes that propel the solid that lodges towards the opposite part of the filter in the solids outlet hopper. The continuous cleaning exerted by the cleaning vanes prevents the filter from being clogged and that the solids that remain inside are thrown outside by the outlet hopper automatically.
3. PURINOX, máquina para depuración de purines y procesos industriales, conforme a la reivindicación Ia caracterizada por el empleo de una central hidráulica (18) como generador de energía hidráulica, de esta manera con un solo motor eléctrico de baja potencia obtenemos los movimientos necesarios para el funcionamiento de toda la máquina. 3. PuriNOx machine purifying purines and industrial processes, according to claim I characterized by the use of a hydraulic system (18) as hydraulic power, thus with a single electric motor low power movements obtain necessary for the operation of the entire machine.
4. PURINOX, máquina para depuración de purines y procesos industriales, conforme a la reivindicación Ia caracterizada por incorporar un separador ciclónico de partículas en suspensión que no tiene ninguna parte móvil y opera automáticamente (31) con el fin de limpiar el líquido que entra tangencialmente en la parte superior del ciclón y se concentra por abajo en la pared interna del ciclón como consecuencia del movimiento giratorio en el sentido de las agujas del reloj, al alcanzar el líquido la zona más estrecha, las partículas son sometidas a un proceso de aglomeración, haciendo que decanten hacia la parte inferior, donde está el punto de drenaje; así el líquido limpio es llevado de nuevo hacia arriba en un vórtice rotativo opuesto al drenaje, y sale fuera a través de la toma de salida superior central. Se consigue así que tras la entrada de líquido con una cantidad ínfima de partículas en suspensión, se eliminen estas y se produce la salida del líquido libre de partículas sólidas en suspensión.4. PuriNOx machine purifying purines and industrial processes, according to claim I characterized by incorporating a cyclonic separating particulate matter that has no moving parts and automatically operates (31) in order to clean the liquid entering tangentially at the top of the cyclone and concentrated below on the inner wall of the cyclone as a result of the rotating movement clockwise, when the liquid reaches the narrowest area, the particles are subjected to an agglomeration process , causing them to decant towards the bottom, where the drain point is; thus the clean liquid is brought back upwards in a rotating vortex opposite to the drain, and exits out through the central upper outlet. It is thus achieved that after the entry of liquid with a very small amount of suspended particles, these are eliminated and the liquid free of solid particles in suspension is produced.
6 HOJA DE SUSTITUCIÓN (REGLA 26) 6 SUBSTITUTE SHEET (RULE 26)
5. PURINOX, máquina para depuración de purines y procesos industriales, conforme a la reivindicación Ia caracterizada por que incorpora un sistema de depuración del liquido residual obtenido de la separación liquido y sólido, produciéndose la depuración por la inyección de ozono a través de un eyector (25) dosificado por una bomba dosificadora (24) al líquido residual que está depositado en un tanque de residencia de liquidos (26) siendo el resultado final un líquido inocuo, sin olor e incoloro.5. PuriNOx machine purifying manure and industrial processes, according to claim I to characterized by incorporating a cleaning system the residual liquid obtained from the solid and liquid separation, producing purification by ozone injection through a ejector (25) dosed by a metering pump (24) to the residual liquid that is deposited in a liquid residence tank (26), the final result being a harmless, odorless and colorless liquid.
77
HOJA DE SUSTITUCIÓN (REGLA 26) SUBSTITUTE SHEET (RULE 26)
PCT/ES2004/000505 2004-11-15 2004-11-15 Purinox, machine for purine treatment and industrial processes WO2006056620A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
PCT/ES2004/000505 WO2006056620A1 (en) 2004-11-15 2004-11-15 Purinox, machine for purine treatment and industrial processes
PCT/ES2005/000291 WO2006053914A1 (en) 2004-11-15 2005-05-23 Cavero 2005, machine for purine treatment and industrial processes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/ES2004/000505 WO2006056620A1 (en) 2004-11-15 2004-11-15 Purinox, machine for purine treatment and industrial processes

Publications (1)

Publication Number Publication Date
WO2006056620A1 true WO2006056620A1 (en) 2006-06-01

Family

ID=36406848

Family Applications (2)

Application Number Title Priority Date Filing Date
PCT/ES2004/000505 WO2006056620A1 (en) 2004-11-15 2004-11-15 Purinox, machine for purine treatment and industrial processes
PCT/ES2005/000291 WO2006053914A1 (en) 2004-11-15 2005-05-23 Cavero 2005, machine for purine treatment and industrial processes

Family Applications After (1)

Application Number Title Priority Date Filing Date
PCT/ES2005/000291 WO2006053914A1 (en) 2004-11-15 2005-05-23 Cavero 2005, machine for purine treatment and industrial processes

Country Status (1)

Country Link
WO (2) WO2006056620A1 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20170022522A1 (en) * 2015-07-20 2017-01-26 Anaergia Inc. Production of biogas from organic materials
US9868964B2 (en) 2015-02-06 2018-01-16 Anaergia Inc. Solid waste treatment with conversion to gas and anaerobic digestion
US11123778B2 (en) 2016-03-18 2021-09-21 Anaergia Inc. Solid waste processing with pyrolysis of cellulosic waste
US11286507B2 (en) 2013-07-11 2022-03-29 Anaergia Inc. Anaerobic digestion and pyrolysis system

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ITVE20130033A1 (en) * 2013-07-02 2015-01-03 Della Toffola Spa MACHINE PERFECTED FOR PRESSING FRUIT OR SIMILAR PRODUCTS AND METHOD FOR CLEANING YOUR DRAINAGE CHANNELS.
ITBA20150013A1 (en) * 2015-02-17 2016-08-17 Paparusso Antonio "PLANT FOR THE TREATMENT OF VEGETATION WATER AND RELATED PROCESS"

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2147103A1 (en) * 1997-11-04 2000-08-16 Tratamiento De Depuracion De P Installation for the purification of liquid manures and the like
US20020121475A1 (en) * 2001-03-05 2002-09-05 Degarmo Richard Method and appratus for processing wet material
US6802984B1 (en) * 1999-02-19 2004-10-12 Zentox Corporation Poultry processing water recovery and re-use process

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2147103A1 (en) * 1997-11-04 2000-08-16 Tratamiento De Depuracion De P Installation for the purification of liquid manures and the like
US6802984B1 (en) * 1999-02-19 2004-10-12 Zentox Corporation Poultry processing water recovery and re-use process
US20020121475A1 (en) * 2001-03-05 2002-09-05 Degarmo Richard Method and appratus for processing wet material

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11286507B2 (en) 2013-07-11 2022-03-29 Anaergia Inc. Anaerobic digestion and pyrolysis system
US9868964B2 (en) 2015-02-06 2018-01-16 Anaergia Inc. Solid waste treatment with conversion to gas and anaerobic digestion
US20170022522A1 (en) * 2015-07-20 2017-01-26 Anaergia Inc. Production of biogas from organic materials
US9879285B2 (en) * 2015-07-20 2018-01-30 Anaergia Inc. Production of biogas from organic materials
US11123778B2 (en) 2016-03-18 2021-09-21 Anaergia Inc. Solid waste processing with pyrolysis of cellulosic waste

Also Published As

Publication number Publication date
WO2006053914A1 (en) 2006-05-26

Similar Documents

Publication Publication Date Title
CA2512935C (en) Sanitization system and system components
WO2006053914A1 (en) Cavero 2005, machine for purine treatment and industrial processes
JPH10504997A (en) Gas treatment / floating reactor with device for separating solids from liquids
JP3859074B2 (en) Purification device
CN201436055U (en) Portable purifier
CN206502621U (en) A kind of sewage treatment tower
CN209411959U (en) A kind of municipal administration sanitary sewage tertiary treatment device
CN100475726C (en) Water filter
CN203048715U (en) Precise filter with rotational-flow de-sanding device
KR100824310B1 (en) Filtration system
CN208292761U (en) A kind of easy-to-dismount sewage filter device
CN202688137U (en) Integrated multifunctional water making machine
CN206457305U (en) A kind of BAF and its washed-out sand mechanism
CN104478145A (en) Precision filter with rotational flow sand removal function and manufacturing method thereof
CN108373221A (en) A kind of purifier for sanitary wastewater processing
CN109956595A (en) A kind of energy saving water purifier based on ion exchange technique
CN212315809U (en) Water passing type ultraviolet filter for separating fishpond excrement
CN214299675U (en) Take leading high-efficient filterable industrial wastewater treatment equipment
CN208135983U (en) A kind of sewage purifier
CN217868370U (en) Purification device for efficiently filtering and purifying liquid fluid
KR20010054690A (en) An water purifier using ozone
CN212425692U (en) Reverse osmosis fresh water treatment device with flushing function
CN208857081U (en) A kind of pharmacy wastewater treatment system
CN208327569U (en) A kind of new type sewage purifier
CN209685469U (en) A kind of efficient purification of waste water filter device

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BW BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NA NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): GM KE LS MW MZ NA SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LU MC NL PL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG

121 Ep: the epo has been informed by wipo that ep was designated in this application
NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 04798232

Country of ref document: EP

Kind code of ref document: A1