WO2015173450A1 - Equipment for breeding insect larvae and auxiliary systems - Google Patents

Equipment for breeding insect larvae and auxiliary systems Download PDF

Info

Publication number
WO2015173450A1
WO2015173450A1 PCT/ES2015/070364 ES2015070364W WO2015173450A1 WO 2015173450 A1 WO2015173450 A1 WO 2015173450A1 ES 2015070364 W ES2015070364 W ES 2015070364W WO 2015173450 A1 WO2015173450 A1 WO 2015173450A1
Authority
WO
WIPO (PCT)
Prior art keywords
reactor
equipment according
solid
equipment
larvae
Prior art date
Application number
PCT/ES2015/070364
Other languages
Spanish (es)
French (fr)
Inventor
Andres Fullana Font
Santos ROJO VELASCO
Paola GOBBI
Alfredo LLECHA GALIÑANES
Agustín LOZANO MORCILLO
Original Assignee
Universidad De Alicante
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 Universidad De Alicante filed Critical Universidad De Alicante
Publication of WO2015173450A1 publication Critical patent/WO2015173450A1/en

Links

Classifications

    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01KANIMAL HUSBANDRY; AVICULTURE; APICULTURE; PISCICULTURE; FISHING; REARING OR BREEDING ANIMALS, NOT OTHERWISE PROVIDED FOR; NEW BREEDS OF ANIMALS
    • A01K67/00Rearing or breeding animals, not otherwise provided for; New or modified breeds of animals
    • A01K67/033Rearing or breeding invertebrates; New breeds of invertebrates

Definitions

  • the present invention relates to an insect larvae breeding equipment, for example dipterans, beetles and, in general, saprophagous insects, by means of hyperbaric conduits, which allows the conversion of organic waste into larval biomass, and that can be used later in human or animal feed or in the generation of compounds with industrial interest.
  • Larvae can feed on organic matter of very diverse nature in large areas of the world.
  • reactors digesters
  • a length / diameter ratio with a value less than 1
  • the use of gaseous streams at atmospheric pressure percolating through conventional means in which the larvae of the dipterans are fed is relatively inefficient, since the air is randomly blurred by the places where it finds less resistance. This fact does not completely solve the problems derived from areas with anaerobiosis, since there will be completely anaerobic areas randomly located in the food substrate that will be naturally avoided by the larvae.
  • the present invention is aimed at solving the technical problems described above, by means of a novel insect larval breeding equipment and, in a second object of the invention, a plurality of auxiliary systems of said equipment.
  • the present invention thus relates to a breeding equipment for insect larvae, preferably saprophages (decomposers of organic substrates), for example dipterans or beetles.
  • This equipment allows the development and collection of insect larvae using reactors composed of pipes that can work in hyperbaric regime.
  • the invention also relates to systems for the provision of the food substrate and for the removal of solids containing waste and the larvae of the reactors of said equipment.
  • the present invention solves the aforementioned problems, its objective being the creation of a breeding equipment for diptera insect larvae as an integral system for the development and growth of organic matter decomposing diptera larvae, including the fattening and biomass collection stages.
  • insects to which the system refers can be, for example, larvae of species of saprophagous dipterans of different families, mainly stratiomides (Stratiomyidae, eg Hermetia lllucens), symphids (Syrphidae, eg Eristalis tenax, Eristalinus aeneus) muscled (Muscidae eg Musca domestica) and caliporides (Calliphoridae, eg Calliphora vicina, Chrysomya megacephala, Lucilia sericata) although it can be applied to larvae of other families of organic matter decomposing dipterans, and also of beetles.
  • the texture of the organic substrate offered as food to the larvae of decomposing insects of organic matter is often a pasty solid that prevents its correct drive by conventional methods. That is why the present invention is aimed at generating a mixing and impulsion of sludge capable of providing a mixture of foods with a correct moisture content, which It allows to be transported inside large pipes.
  • the present invention also includes means for the introduction of neonatal insects or larvae of small dipterans inside the reactors, by means of a drive system.
  • the present invention also solves the problem of the development of larvae in substrates with thicknesses greater than 25 cm. This is possible thanks to the continuous injection of oxygen, which can be introduced into the system maintaining a hyperbaric pressure inside the reactor to optimize the larval digestion process in aerobiosis. Besides maintaining this hyperbaric pressure, it is possible to control the temperature and humidity of the substrate, so that they are adequate to guarantee the growth and fattening of larvae of the diptera.
  • This hyperbaric pressure is maintained by means of control arranged inside the reactor (for example valve systems), allowing a total oxygenation thereof, greatly increasing the survival of the larvae and accelerating their metabolism.
  • the proposed system works in such a way that the substrate introduced into the reactor is assimilated by the larvae of the interior, being able to proceed to the addition of a new food substrate, if required, allowing its mixing with the substrate previously modified by the larval and microbial activity .
  • the system is discontinuous and operates by loads of food. Once the larval development process has been completed, the interior of the reactor and the larvae can be extracted from the system for later use. Breeding equipment of decomposing insect larvae comprises a larval digestion reactor. In addition to the reactor, the equipment includes a feed system, aeration system and a solids extraction system.
  • the solids extraction system preferably operates by air flow, for which it comprises an air delivery system configured to generate an incoming air stream, and preferably introducing it into the base or bottom of the reactor. Once said air drags the solids (debris and larvae), then it takes an outlet pipe from the reactor.
  • the entrained solids can be taken to a tank for subsequent treatment or, directly, to a solid-gas separator, followed by a second separator, in this case solid-solid to separate the larvae from the waste material.
  • the aeration system preferably comprises an aeration duct, located at the base or bottom of the reactor, and is connected to the digestion chamber by means of a diffuser containing a plurality of perforations along the chamber of reactor digestion.
  • the aeration duct can also function as an input of the solids extraction system.
  • the feed system will preferably be a mixer of a stream of water and a stream of nutrients that forms a sludge or paste and an extruder that introduces it into the reactor through a narrowing. In this narrowing, water or neonatal insects can be added in an additional stream.
  • the equipment will comprise a hermetic reactor and a hyperbaric air or oxygen pressure system inside the reactor.
  • This may have a pressure line that connects a pressure vessel or discharge equipment to the reactor, and as an optional safety measure, an internal pressure gauge to the reactor capable of acting on an exhaust or purge valve of the reactor.
  • the pressure gas can be entered through the aeration duct.
  • the invention also relates to a solids extraction system and the feeding system independently, for application to larval breeding equipment of diptera or beetle insects. DESCRIPTION OF THE DRAWINGS
  • Figure 2. Flow chart of the reactor content extraction process. - Figure 3. Scheme of a first embodiment of the reactor, of square section.
  • Figure 6 Flow diagram of a reactor in hyperbaric conditions.
  • Figure 1 shows an embodiment of the feeding system, configured to provide mixing of the different substrates with nutrients for the larvae.
  • the system is connected to a stream of nutrients (1) that contains the different types of nutrients that the larvae need, and a stream of water (2), which helps to obtain the necessary plasticity for the drive of the resulting substrate in form of mud.
  • the two streams enter the mixer (3), where a series of blades that are inserted in an axis remove and mix the different components and nutrients that the larvae need.
  • the turn can be one way, or include several sets of blades with opposite turns.
  • the mixer (3) will be in the form of a hopper, conical, pyramidal or truncated cone or any shape that allows the mixing taking advantage of the existing space.
  • the sludge stream (6) is driven to a narrowing (7), in which the sludge can be directed towards a flexible or fixed line to be introduced into the reactor (8).
  • the additional stream (9) would correspond to an extra stream of water or neonatal insects that can be introduced into the reactor (8) along with the sludge, through the narrowing (7).
  • the reactor (8) may have a cylindrical, hexagonal, square or rectangular profile, due to its ease of modular scaling, or any other, generally having its inscribed diameter less than or equal to its length.
  • Figure 2 describes the solids extraction system inside the reactor (8) where insect larvae are grown. Inside the reactor (8) are the larvae, remains of undigested food substrate and substrate biodegraded by larval and microbial activity.
  • the system is composed of an inlet air stream (10), which enters into an air delivery system (1 1), such as a compressor, from where it is propelled into the reactor (8) by means of the corresponding driving.
  • the elements that are to be evacuated are carried by the current of air that has entered the reactor (8) from the bottom, and they exit through the outlet pipe (12), larger in diameter than the inlet, to the solid-gas separator (13).
  • the air delivery system (1 1) will therefore be strong enough to drag the solids from the reactor (8).
  • solid-gas separator (13) cyclone, filter or expansion chamber, for example
  • the solid stream (14) feeds a solid-solid separation system (15) (screening, flotation, aeration, centrifugation, etc.), which allows the larvae to be separated into a stream of larvae (16) and the rest of solids in the waste stream (17).
  • the solids extraction system can also function as a reactor aeration system (8), simply by driving less inlet air stream (10) in the air discharge system (1 1), so that it is capable of removing the stale air without removing larvae and nutrients.
  • FIG 3 describes a first embodiment of the digestion reactor (8).
  • This reactor (8) preferably comprises a system composed of a rectangular housing (81) into which both the food and the larvae are introduced and their cultivation is carried out.
  • the aeration system contains a diffuser (83), in this case corresponding to a diffuser plate in which there are perforations (84) where the air exits to the internal digestion chamber of the reactor (8).
  • the gas stream enters through a rectangular aeration duct (82), in the lower part of the reactor (8), and exits through the perforations (84) of the diffuser plate, passing through the bed formed by the larvae and the food allowing substrate oxygenation and larval aerobic metabolic activity.
  • the perforations (84) may not be too large to prevent material from falling into the aeration duct (82).
  • FIG 4 describes a second embodiment of the digestion reactor (8), in which the housing (81) is cylindrical.
  • the aeration system contains the diffuser (83), in this case a cylindrical diffuser conduit, in which the perforations (84) are located, where the air inside the digestion chamber leaves.
  • the air enters through a circular aeration duct (82 '), at the bottom of the reactor (8), and exits through the perforations (84) of the diffuser line, passing the air through the bed formed by the larvae and the food.
  • FIG. 5 describes the general scheme of a third embodiment of the reactor (8) whose housing (81) is also cylindrical.
  • the aeration system of this embodiment comprises a blind aeration duct (82 "), that is to say no outlet at its innermost end to the reactor (8), which blows a gaseous stream into the interior of the reactor (8).
  • Aeration (82 ") has a diffuser (83) formed by a face of its outer wall. In the diffuser (83) the perforations (84) will be arranged so that the air can escape.
  • the reactor (8) may be hermetically sealed and connected to an oxygen pressure vessel that maintains a hyperbaric oxygen pressure, which spreads homogeneously in the diet or medium from which the larvae are fed. necessarily through the perforations (84) as will be explained below. Alternatively, it may have a non-hermetic cover (85) at at least one of the ends to facilitate aeration and sampling or control of the reactor contents.
  • Figure 6 describes the general operation of the reactor (8) in hyperbaric conditions of air or oxygen, preferably with a pressure between 1 and 6 bar and can reach 20 bar, depending on the type of larva.
  • the reactor (8) is connected to a hyperbaric pressure system formed by a pressure line (18) plugged into a pressure vessel or delivery equipment (19), which injects the gas into the reactor (8).
  • a control or shut-off valve (20) In the pressure line (18) there is a control or shut-off valve (20), which allows the gas inlet to the reactor (8) to be controlled.
  • a pressure control system formed by a meter (21) acting on an exhaust valve (22) or purge the reactor (8) is introduced if the detected pressure exceeds a predefined value.
  • the pressure gas inlet into the reactor (8) can be through the aeration duct itself (82, 82 ', 82 ") or by an added inlet, preferably also at the bottom of the reactor (8) and covered by the Nutrients and larvae.
  • the gas stream should allow adequate humidity, temperature and oxygen diffusion for the correct survival and development of the larvae, the optimum conditions being known in the state of the art.

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Environmental Sciences (AREA)
  • Animal Behavior & Ethology (AREA)
  • Zoology (AREA)
  • Animal Husbandry (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Processing Of Solid Wastes (AREA)
  • Apparatuses For Bulk Treatment Of Fruits And Vegetables And Apparatuses For Preparing Feeds (AREA)
  • Housing For Livestock And Birds (AREA)
  • Medicines Containing Material From Animals Or Micro-Organisms (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

The invention relates to equipment for breeding insect larvae, comprising a larvae digestion reactor, with a supply system, an aeration system and a solid extraction system. The solid extraction system has an air stream introduced via the base of the reactor, solid-gas and solid-solid separators being arranged behind the reactor. The aeration system comprises an aeration conduit arranged in the lower part of the reactor, connected to the digestion chamber by means of a diffuser with a plurality of perforations along the digestion chamber. The supply system comprises a water and nutrient mixer and an extruder for extruding the sludge formed. The reactor can operate under hyperbaric conditions.

Description

EQUIPO DE CRÍA DE LARVAS DE INSECTOS Y SISTEMAS AUXILIARES  BREEDING EQUIPMENT OF INSECT LARVES AND AUXILIARY SYSTEMS
DESCRIPCIÓN DESCRIPTION
Equipo de cría de larvas de insectos y sistemas auxiliares. Breeding equipment for insect larvae and auxiliary systems.
SECTOR DE LA TÉCNICA La presente invención se refiere a un equipo de cría de larvas de insectos, por ejemplo insectos dípteros, coleópteros y, en general, insectos saprófagos, mediante conducciones en régimen hiperbárico, que permite la conversión de desechos orgánicos en biomasa larvaria, y que puede ser utilizada posteriormente en alimentación humana o animal o en la generación de compuestos con interés industrial. TECHNICAL SECTOR The present invention relates to an insect larvae breeding equipment, for example dipterans, beetles and, in general, saprophagous insects, by means of hyperbaric conduits, which allows the conversion of organic waste into larval biomass, and that can be used later in human or animal feed or in the generation of compounds with industrial interest.
Igualmente se refiere a sistemas auxiliares de alimentación y de extracción de sólidos de desecho. It also refers to auxiliary systems for feeding and extracting waste solids.
ESTADO DE LA TÉCNICA STATE OF THE TECHNIQUE
Existen numerosas ventajas en la utilización de larvas de insectos descomponedores para el procesado de diferentes sustratos orgánicos (p. ej. subproductos agroalimentarios, lodos de depuradoras, residuos ganaderos, hosteleros, urbanos etc.), algunas de dichas ventajas son: There are numerous advantages in the use of decomposing insect larvae for the processing of different organic substrates (eg agri-food by-products, sewage sludge, livestock waste, catering, urban, etc.), some of these advantages are:
1) Las larvas pueden alimentarse de materia orgánica de muy diversa naturaleza en amplias zonas del mundo. 1) Larvae can feed on organic matter of very diverse nature in large areas of the world.
2) Transforman los compuestos orgánicos contenidos en los residuos y subproductos en proteínas, grasas y otros bio-compuestos con interés industrial. 2) They transform the organic compounds contained in the residues and by-products into proteins, fats and other bio-compounds with industrial interest.
3) Su elevado contenido proteico tiene un gran valor nutricional para su utilización en alimentación animal y/o humana. Aunque en el estado de la técnica se han propuesto diversos equipos para el cultivo artificial y producción masiva de larvas de dípteros descomponedores, uno de los principales problemas que presentan es la imposibilidad de su desarrollo en condiciones totalmente anaeróbicas. Las larvas no pueden crecer y alimentarse adecuadamente en espesores de sustrato superiores a 25 centímetros. Es por ello que en algunos equipos conocidos se utilizan bandejas de poca profundidad («10 cm) como dispositivos para el desarrollo de larvas, tal como se aprecia en US20130319334A1 (Larry Newton & Craig Sheppard. "Systems and Methods for Rearing Insect Larvae") o US201 10296756A1 (Mao Zhang. Mini Space Farm, "A Food Regenerative System in the Long-Term Space Mission"). Estos equipos tienen el problema del mal aprovechamiento del espacio, el escalado de su producción y la dificultad del cosechado de las larvas al finalizar la digestión del sustrato. 3) Its high protein content has great nutritional value for use in animal and / or human nutrition. Although in the state of the art various equipment for artificial cultivation and mass production of decomposing diptera larvae have been proposed, one of the The main problems they present are the impossibility of their development in totally anaerobic conditions. Larvae cannot grow and feed properly on substrate thicknesses greater than 25 centimeters. That is why in some known equipment shallow trays ( « 10 cm) are used as devices for the development of larvae, as seen in US20130319334A1 (Larry Newton & Craig Sheppard." Systems and Methods for Rearing Insect Larvae ") or US201 10296756A1 (Mao Zhang. Mini Space Farm, "A Food Regenerative System in the Long-Term Space Mission"). These teams have the problem of poor use of space, the scaling of their production and the difficulty of harvesting the larvae at the end of the digestion of the substrate.
Para la recolección de las larvas, muchos equipos incorporan rampas que permiten la salida natural de las larvas permitiendo el auto cosechado de las mismas. Se cita US20130319334A1 de nuevo y US6579713B2 (Paul Olivier. "Apparatus for bio- conversion of putrescent wastes"). Sin embargo, estos métodos consumen mucho tiempo y no mejoran la producción de biomasa por unidad de superficie. Además las larvas frecuentemente no realizan un desarrollo y crecimiento sincrónico por lo que el auto-cosechado puede durar varios días o semanas. For the collection of the larvae, many teams incorporate ramps that allow the natural exit of the larvae allowing their self-harvesting. US20130319334A1 is cited again and US6579713B2 (Paul Olivier. "Apparatus for bio-conversion of putrescent wastes"). However, these methods are time consuming and do not improve biomass production per unit area. In addition, larvae often do not perform synchronous growth and development, so self-harvesting can last several days or weeks.
Algunos procedimientos incluyen el uso de aire forzado en dispositivos rectangulares o cúbicos (CN102499190A; "Ventilating and stirring type Hermetia illucens bioprocessor". ES2331452B21 FLYSOIL, S.L. "Equipo y proceso para la eliminación de residuos orgánicos mediante larvas de insecto"). No obstante, estos equipos operan de manera continua y en ellos se establecen diferentes gradientes con larvas de edades distintas y múltiples suministro de sustrato. Some procedures include the use of forced air in rectangular or cubic devices (CN102499190A; "Ventilating and stirring type Hermetia illucens bioprocessor". ES2331452B2 1 FLYSOIL, SL "Equipment and process for the elimination of organic waste by insect larvae"). However, these devices operate continuously and they establish different gradients with larvae of different ages and multiple substrate supply.
Por otro lado, el uso de reactores (digestores) con una relación longitud/diámetro con un valor inferior a 1 , conlleva un menor aprovechamiento del espacio, dificulta el suministro del sustrato para el desarrollo larvario, así como la extracción del sustrato modificado por la actividad larvaria y el propio cosechado de las larvas. Además, la utilización de corrientes gaseosas a presión atmosférica percolando a través de medios convencionales en el que se alimentan las larvas de los dípteros es relativamente ineficiente, ya que el aire se difumina aleatoriamente por los lugares donde encuentra menos resistencia. Este hecho no resuelve pues totalmente los problemas derivados de las zonas con anaerobiosis, ya que existirán zonas completamente anaeróbicas localizadas aleatoriamente en el sustrato alimenticio que serán evitadas de forma natural por las larvas. La presente invención está orientada a resolver los problemas técnicos antes descritos, mediante un novedoso equipo de cría de larvas de insectos y, en un segundo objeto de la invención, a una pluralidad de sistemas auxiliares de dicho equipo. On the other hand, the use of reactors (digesters) with a length / diameter ratio with a value less than 1, leads to less space utilization, hinders the supply of the substrate for larval development, as well as the extraction of the substrate modified by the larval activity and the larvae harvested. In addition, the use of gaseous streams at atmospheric pressure percolating through conventional means in which the larvae of the dipterans are fed is relatively inefficient, since the air is randomly blurred by the places where it finds less resistance. This fact does not completely solve the problems derived from areas with anaerobiosis, since there will be completely anaerobic areas randomly located in the food substrate that will be naturally avoided by the larvae. The present invention is aimed at solving the technical problems described above, by means of a novel insect larval breeding equipment and, in a second object of the invention, a plurality of auxiliary systems of said equipment.
BREVE EXPLICACIÓN DE LA INVENCIÓN BRIEF EXPLANATION OF THE INVENTION
La presente invención se refiere, pues, a un equipo de cría de larvas de insectos preferentemente saprófagos (descomponedores de sustratos orgánicos), por ejemplo saprófagos dípteros o coleópteros. Dicho equipo permite el desarrollo y recolección de larvas de insectos utilizando reactores compuestos por conducciones que puede trabajar en régimen hiperbárico. La invención se refiere, asimismo, a sistemas para la provisión del sustrato alimenticio y para la retirada de los sólidos conteniendo los desechos y las larvas de los reactores de dicho equipo. The present invention thus relates to a breeding equipment for insect larvae, preferably saprophages (decomposers of organic substrates), for example dipterans or beetles. This equipment allows the development and collection of insect larvae using reactors composed of pipes that can work in hyperbaric regime. The invention also relates to systems for the provision of the food substrate and for the removal of solids containing waste and the larvae of the reactors of said equipment.
La presente invención solventa los problemas mencionados anteriormente, siendo su objetivo la creación de un equipo de cría de larvas de insectos dípteros como sistema integral de desarrollo y crecimiento de larvas de dípteros descomponedores de materia orgánica, incluyendo las etapas de engorde y recolección de biomasa. The present invention solves the aforementioned problems, its objective being the creation of a breeding equipment for diptera insect larvae as an integral system for the development and growth of organic matter decomposing diptera larvae, including the fattening and biomass collection stages.
Los insectos a los que el sistema hace referencia pueden ser, por ejemplo, larvas de especies de dípteros saprófagos de diferentes familias, principalmente los estratiómidos (Stratiomyidae, ej. Hermetia lllucens), sírfidos (Syrphidae, ej. Eristalis tenax, Eristalinus aeneus) múscidos (Muscidae ej. Musca domestica) y califóridos (Calliphoridae, ej. Calliphora vicina, Chrysomya megacephala, Lucilia sericata) aunque puede ser aplicado a larvas de otras familias de dípteros descomponedores de materia orgánica en general, y también de coleópteros. The insects to which the system refers can be, for example, larvae of species of saprophagous dipterans of different families, mainly stratiomides (Stratiomyidae, eg Hermetia lllucens), symphids (Syrphidae, eg Eristalis tenax, Eristalinus aeneus) muscled (Muscidae eg Musca domestica) and caliporides (Calliphoridae, eg Calliphora vicina, Chrysomya megacephala, Lucilia sericata) although it can be applied to larvae of other families of organic matter decomposing dipterans, and also of beetles.
La textura del sustrato orgánico ofrecido como alimento a las larvas de insectos descomponedores de materia orgánica es frecuentemente un sólido pastoso que impide su correcta impulsión por métodos convencionales. Es por ello que la presente invención está orientada a generar un mezclado e impulsión de lodo capaces de proporcionar una mezcla de alimentos con un contenido de humedad correcto, que permite ser transportado en el interior de conducciones de gran longitud. La presente invención también incluye medios para la introducción de insectos neonatos o larvas de dípteros de pequeño tamaño en el interior de los reactores, mediante un sistema de impulsión. The texture of the organic substrate offered as food to the larvae of decomposing insects of organic matter is often a pasty solid that prevents its correct drive by conventional methods. That is why the present invention is aimed at generating a mixing and impulsion of sludge capable of providing a mixture of foods with a correct moisture content, which It allows to be transported inside large pipes. The present invention also includes means for the introduction of neonatal insects or larvae of small dipterans inside the reactors, by means of a drive system.
También se solventa en la presente invención el problema de extracción de los componentes sólidos procedentes de la digestión larvaria y retenidos en reactores de tipo conducción, en los que su relación longitud/diámetro tiene un valor superior a 1. Esta extracción aprovecha el movimiento de las larvas en el interior del reactor y su efecto de mezclado. La digestión larvaria ocasiona con el tiempo que el sustrato alimenticio se transforme en un sólido con estructura porosa. Es por ello que es posible extraer el contenido del interior del reactor mediante un sistema de arrastre por aire compuesto por un equipo de impulsión de aire, el propio reactor que actúa como conducción y un sistema de separación sólido-gas que permite la recolección de la masa formada por el sustrato sin digerir, sustrato digerido y biomasa larvaria. Al encontrarse esta corriente sólida con un bajo contenido en agua, es posible realizar una separación por cribado de las larvas y el resto de componentes. The problem of extracting solid components from larval digestion and retained in conductors of type reactors, in which their length / diameter ratio has a value greater than 1, is also solved in the present invention. This extraction takes advantage of the movement of the larvae inside the reactor and their mixing effect. Larval digestion causes over time that the food substrate is transformed into a solid with porous structure. That is why it is possible to extract the contents of the interior of the reactor by means of an air entrainment system composed of an air supply unit, the reactor itself that acts as a conduit and a solid-gas separation system that allows the collection of the mass formed by the undigested substrate, digested substrate and larval biomass. When this solid current is found with a low water content, it is possible to perform a separation by screening of the larvae and the other components.
La presente invención resuelve también el problema del desarrollo de larvas en sustratos con espesores mayores de 25 cm. Esto es posible gracias a la inyección de oxígeno de forma continua, pudiendo éste ser introducido al sistema manteniendo una presión hiperbárica en el interior del reactor para optimizar el proceso de digestión larvaria en aerobiosis. Además manteniendo esta presión hiperbárica es posible controlar la temperatura y la humedad del sustrato, para que sean las adecuadas para garantizar el crecimiento y engorde de larvas de los dípteros. The present invention also solves the problem of the development of larvae in substrates with thicknesses greater than 25 cm. This is possible thanks to the continuous injection of oxygen, which can be introduced into the system maintaining a hyperbaric pressure inside the reactor to optimize the larval digestion process in aerobiosis. Besides maintaining this hyperbaric pressure, it is possible to control the temperature and humidity of the substrate, so that they are adequate to guarantee the growth and fattening of larvae of the diptera.
Esta presión hiperbárica se mantiene mediante medios de control dispuestos dentro del reactor (por ejemplo sistemas válvulas), permitiendo una oxigenación total del mismo, aumentando en gran medida la supervivencia de las larvas y acelerando su metabolismo. El sistema propuesto trabaja de forma que el sustrato introducido en el reactor es asimilado por las larvas del interior, pudiendo proceder a la adición de nuevo sustrato alimenticio, si así fuese requerido, permitiendo su mezcla con el sustrato previamente modificado por la actividad larvaria y microbiana. El sistema es discontinuo y opera por cargas de comida. Una vez se ha completado el proceso de desarrollo larvario, el interior del reactor y las larvas pueden ser extraídas del sistema para su posterior utilización. El equipo de cría de larvas de insectos descomponedores comprende un reactor de digestión de las larvas. Además del reactor, el equipo comprende un sistema de alimentación, un sistema de aireación y un sistema de extracción de sólidos. This hyperbaric pressure is maintained by means of control arranged inside the reactor (for example valve systems), allowing a total oxygenation thereof, greatly increasing the survival of the larvae and accelerating their metabolism. The proposed system works in such a way that the substrate introduced into the reactor is assimilated by the larvae of the interior, being able to proceed to the addition of a new food substrate, if required, allowing its mixing with the substrate previously modified by the larval and microbial activity . The system is discontinuous and operates by loads of food. Once the larval development process has been completed, the interior of the reactor and the larvae can be extracted from the system for later use. Breeding equipment of decomposing insect larvae comprises a larval digestion reactor. In addition to the reactor, the equipment includes a feed system, aeration system and a solids extraction system.
El sistema de extracción de sólidos opera preferentemente por corriente de aire, para lo que comprende un sistema de impulsión de aire configurado para generar una corriente de aire de entrada, e introducirla preferentemente en la base o parte inferior del reactor. Una vez dicho aire arrastra los sólidos (desechos y larvas), posteriormente toma una conducción de salida del reactor. Los sólidos arrastrados se pueden llevar a un depósito para su posterior tratamiento o, directamente, a un separador sólido-gas, seguido si acaso de un segundo separador, en este caso sólido-sólido para separar las larvas del material de desecho. En particular, el sistema de aireación comprende preferentemente un conducto de aireación, situado en la base o parte inferior del reactor, y se conecta con la cámara de digestión por medio de un difusor que contiene una pluralidad de perforaciones a lo largo de la cámara de digestión del reactor. El conducto de aireación puede funcionar también como entrada del sistema de extracción de sólidos. The solids extraction system preferably operates by air flow, for which it comprises an air delivery system configured to generate an incoming air stream, and preferably introducing it into the base or bottom of the reactor. Once said air drags the solids (debris and larvae), then it takes an outlet pipe from the reactor. The entrained solids can be taken to a tank for subsequent treatment or, directly, to a solid-gas separator, followed by a second separator, in this case solid-solid to separate the larvae from the waste material. In particular, the aeration system preferably comprises an aeration duct, located at the base or bottom of the reactor, and is connected to the digestion chamber by means of a diffuser containing a plurality of perforations along the chamber of reactor digestion. The aeration duct can also function as an input of the solids extraction system.
El sistema de alimentación será, preferiblemente, un mezclador de una corriente de agua y una corriente de nutrientes que forma un lodo o pasta y una extrusora que lo introduce en el reactor a través de un estrechamiento. En este estrechamiento se pueden añadir agua o insectos neonatos en una corriente adicional. The feed system will preferably be a mixer of a stream of water and a stream of nutrients that forms a sludge or paste and an extruder that introduces it into the reactor through a narrowing. In this narrowing, water or neonatal insects can be added in an additional stream.
Preferentemente, el equipo comprenderá un reactor hermético y un sistema de presión hiperbárica de aire u oxígeno en el interior del reactor. Éste podrá tener una conducción de presión que conecta un recipiente a presión o equipo de impulsión al reactor, y como medida opcional de seguridad, un medidor de la presión interna al reactor capaz de actuar sobre una válvula de escape o purga del reactor. La entrada del gas a presión podrá hacerse por el conducto de aireación. Preferably, the equipment will comprise a hermetic reactor and a hyperbaric air or oxygen pressure system inside the reactor. This may have a pressure line that connects a pressure vessel or discharge equipment to the reactor, and as an optional safety measure, an internal pressure gauge to the reactor capable of acting on an exhaust or purge valve of the reactor. The pressure gas can be entered through the aeration duct.
La invención se refiere, asimismo, a un sistema de extracción de sólidos y el sistema de alimentación de forma independiente, para su aplicación a equipos de cría de larvas de insectos dípteros o coleópteros. DESCRIPCIÓN DE LOS DIBUJOS The invention also relates to a solids extraction system and the feeding system independently, for application to larval breeding equipment of diptera or beetle insects. DESCRIPTION OF THE DRAWINGS
Para una mejor comprensión de la invención, se incluyen las siguientes figuras: - Figura 1. Diagrama de flujo del proceso de llenado del reactor con los nutrientes y neonatos. For a better understanding of the invention, the following figures are included: - Figure 1. Flow chart of the reactor filling process with nutrients and neonates.
Figura 2. Diagrama de flujo del proceso de extracción del contenido del reactor. - Figura 3. Esquema de una primera realización del reactor, de sección cuadrada. Figure 2. Flow chart of the reactor content extraction process. - Figure 3. Scheme of a first embodiment of the reactor, of square section.
Figura 4. Esquema de una segunda realización del reactor, de sección circular. Figure 4. Scheme of a second embodiment of the reactor, of circular section.
Figura 5. Esquema de una tercera realización del reactor, igualmente de sección circular. Figure 5. Scheme of a third embodiment of the reactor, also of circular section.
Figura 6. Diagrama de flujo de un reactor en condiciones hiperbáricas. Figure 6. Flow diagram of a reactor in hyperbaric conditions.
MODOS DE REALIZACIÓN DE LA INVENCIÓN EMBODIMENTS OF THE INVENTION
A continuación se pasa a describir un modo de realización preferente de la invención, como ejemplo ilustrativo y no limitativo de ésta. A preferred embodiment of the invention will now be described, as an illustrative and non-limiting example thereof.
La figura 1 muestra una realización del sistema de alimentación, configurado para proporcionar el mezclado de los diferentes sustratos con nutrientes para las larvas. Preferentemente, el sistema está conectado a una corriente de nutrientes (1) que contiene los diferentes tipos de nutrientes que necesitan las larvas, y una corriente de agua (2), que ayuda a obtener la plasticidad necesaria para la impulsión del sustrato resultante en forma de lodo. Figure 1 shows an embodiment of the feeding system, configured to provide mixing of the different substrates with nutrients for the larvae. Preferably, the system is connected to a stream of nutrients (1) that contains the different types of nutrients that the larvae need, and a stream of water (2), which helps to obtain the necessary plasticity for the drive of the resulting substrate in form of mud.
Las dos corrientes entran en el mezclador (3), donde una serie de palas que están insertadas en un eje remueven y mezclan los diferentes componentes y nutrientes que las larvas necesitan. El giro puede ser en un único sentido, o comprender varios juegos de palas con giros contrarios. El mezclador (3) tendrá forma de tolva, cónica, piramidal o troncocónica o cualquier forma que permita la mezcla aprovechando el espacio existente. Una vez el alimento ha sido mezclado, éste se transporta al exterior, por ejemplo mediante un tornillo sin fin, cuyo primer extremo está dentro del mezclador (3). La corriente de alimento mezclado (4), abandona el mezclador (3) hasta llegar a un segundo tornillo sin fin o extrusora (5) de uno o dos husillos. En la salida de la extrusora (5), se impulsa la corriente de lodo (6) hasta un estrechamiento (7), en el que el lodo puede dirigirse hacia una conducción, flexible o fija, para introducirse en el reactor (8). La corriente adicional (9) correspondería a un corriente extra de agua o insectos neonatos que puede introducirse en el reactor (8) junto con el lodo, a través del estrechamiento (7). The two streams enter the mixer (3), where a series of blades that are inserted in an axis remove and mix the different components and nutrients that the larvae need. The turn can be one way, or include several sets of blades with opposite turns. The mixer (3) will be in the form of a hopper, conical, pyramidal or truncated cone or any shape that allows the mixing taking advantage of the existing space. Once the food has been mixed, it is transported outside, for example by means of an endless screw, whose first end is inside the mixer (3). The mixed feed stream (4) leaves the mixer (3) until it reaches a second worm or extruder (5) with one or two spindles. At the outlet of the extruder (5), the sludge stream (6) is driven to a narrowing (7), in which the sludge can be directed towards a flexible or fixed line to be introduced into the reactor (8). The additional stream (9) would correspond to an extra stream of water or neonatal insects that can be introduced into the reactor (8) along with the sludge, through the narrowing (7).
El reactor (8) puede tener perfil cilindrico, hexagonal, cuadrado o rectangular, por su facilidad de escalado modular, o cualquier otro, siendo generalmente su diámetro inscrito menor o igual que su longitud. The reactor (8) may have a cylindrical, hexagonal, square or rectangular profile, due to its ease of modular scaling, or any other, generally having its inscribed diameter less than or equal to its length.
La figura 2 describe el sistema de extracción de sólidos del interior del reactor (8) donde se cultivan las larvas de insectos. En el interior del reactor (8) se encuentran las larvas, restos de sustrato alimenticio sin digerir y sustrato biodegradado por la actividad larvaria y microbiana. El sistema se compone por una corriente de aire de entrada (10), que entra en el interior de un sistema de impulsión de aire (1 1), como un compresor, de donde se impulsa hacia el reactor (8) por medio de la correspondiente conducción. Los elementos que se quieren evacuar son arrastrados mediante la corriente de aire que ha entrado al reactor (8) por la parte inferior, y salen por la conducción de salida (12), de mayor diámetro que la entrada, hasta el separador sólido-gas (13). El sistema de impulsión de aire (1 1) será por lo tanto lo suficientemente fuerte para arrastrar los sólidos del reactor (8). Figure 2 describes the solids extraction system inside the reactor (8) where insect larvae are grown. Inside the reactor (8) are the larvae, remains of undigested food substrate and substrate biodegraded by larval and microbial activity. The system is composed of an inlet air stream (10), which enters into an air delivery system (1 1), such as a compressor, from where it is propelled into the reactor (8) by means of the corresponding driving. The elements that are to be evacuated are carried by the current of air that has entered the reactor (8) from the bottom, and they exit through the outlet pipe (12), larger in diameter than the inlet, to the solid-gas separator (13). The air delivery system (1 1) will therefore be strong enough to drag the solids from the reactor (8).
En el separador sólido-gas (13) (ciclón, filtro o cámara de expansión, por ejemplo) es posible separar los sólidos del interior del reactor (8) en dos corrientes, una de gas libre de sólidos y otra corriente de sólidos (14) que contiene todos los elementos sólidos del interior del reactor (8). La corriente de sólidos (14) alimenta a un sistema de separación sólido-sólido (15) (cribado, flotación, aireación, centrifugación, etc.), que permite la separación de las larvas en una corriente de larvas (16) y el resto de sólidos en la corriente de desecho (17). El sistema de extracción de sólidos puede funcionar también como sistema de aireación del reactor (8), simplemente impulsando menos la corriente de aire de entrada (10) en el sistema de impulsión de aire (1 1), para que sea capaz de retirar el aire viciado sin remover las larvas y los nutrientes. In the solid-gas separator (13) (cyclone, filter or expansion chamber, for example) it is possible to separate the solids from inside the reactor (8) into two streams, one of gas free of solids and another stream of solids (14 ) which contains all the solid elements inside the reactor (8). The solid stream (14) feeds a solid-solid separation system (15) (screening, flotation, aeration, centrifugation, etc.), which allows the larvae to be separated into a stream of larvae (16) and the rest of solids in the waste stream (17). The solids extraction system can also function as a reactor aeration system (8), simply by driving less inlet air stream (10) in the air discharge system (1 1), so that it is capable of removing the stale air without removing larvae and nutrients.
La figura 3 describe una primera realización del reactor (8) de digestión. Este reactor (8) comprende, preferentemente, un sistema compuesto por una carcasa (81) rectangular en cuyo interior se introducen tanto el alimento como las larvas y se realiza el cultivo de las mismas. El sistema de aireación contiene un difusor (83), en este caso correspondiendo a una placa difusora en la que se encuentran unas perforaciones (84) por donde sale el aire a la cámara de digestión interior del reactor (8). La corriente gaseosa entra por un conducto de aireación (82) rectangular, en la parte inferior del reactor (8), y sale por las perforaciones (84) de la placa difusora, pasando a través del lecho que forman las larvas y el alimento permitiendo la oxigenación del sustrato y la actividad metabólica aeróbica larvaria. Las perforaciones (84) no podrán ser demasiado grandes para evitar la caída de material al interior del conducto de aireación (82). Figure 3 describes a first embodiment of the digestion reactor (8). This reactor (8) preferably comprises a system composed of a rectangular housing (81) into which both the food and the larvae are introduced and their cultivation is carried out. The aeration system contains a diffuser (83), in this case corresponding to a diffuser plate in which there are perforations (84) where the air exits to the internal digestion chamber of the reactor (8). The gas stream enters through a rectangular aeration duct (82), in the lower part of the reactor (8), and exits through the perforations (84) of the diffuser plate, passing through the bed formed by the larvae and the food allowing substrate oxygenation and larval aerobic metabolic activity. The perforations (84) may not be too large to prevent material from falling into the aeration duct (82).
La figura 4 describe una segunda realización del reactor (8) de digestión, en el que la carcasa (81) es cilindrica. El sistema de aireación contiene el difusor (83), en este caso una conducción difusora cilindrica, en la que se encuentran las perforaciones (84), por donde sale el aire al interior de la cámara de digestión. El aire entra por un conducto de aireación (82') circular, en la parte inferior del reactor (8), y sale por las perforaciones (84) de la conducción difusora, pasando el aire a través del lecho que forman las larvas y el alimento. Figure 4 describes a second embodiment of the digestion reactor (8), in which the housing (81) is cylindrical. The aeration system contains the diffuser (83), in this case a cylindrical diffuser conduit, in which the perforations (84) are located, where the air inside the digestion chamber leaves. The air enters through a circular aeration duct (82 '), at the bottom of the reactor (8), and exits through the perforations (84) of the diffuser line, passing the air through the bed formed by the larvae and the food.
La figura 5 describe el esquema general de una tercera realización del reactor (8) cuya carcasa (81) es igualmente cilindrica. El sistema de aireación de esta realización comprende un conducto de aireación (82") ciego, es decir sin salida en su extremo más interior al reactor (8), que insufla una corriente gaseosa en el interior del reactor (8). Este conducto de aireación (82") posee un difusor (83) formado por una cara de su pared exterior. En el difusor (83) se dispondrán las perforaciones (84) para que el aire pueda salir. Figure 5 describes the general scheme of a third embodiment of the reactor (8) whose housing (81) is also cylindrical. The aeration system of this embodiment comprises a blind aeration duct (82 "), that is to say no outlet at its innermost end to the reactor (8), which blows a gaseous stream into the interior of the reactor (8). Aeration (82 ") has a diffuser (83) formed by a face of its outer wall. In the diffuser (83) the perforations (84) will be arranged so that the air can escape.
El reactor (8) podrá estar cerrado herméticamente y conectado a un recipiente a presión de oxigeno que mantiene una presión hiperbárica de oxígeno, el cual se extiende por difusión homogéneamente en la dieta o medio del que se alimentan las larvas no necesariamente a través de las perforaciones (84) como se explicará a continuación. Alternativamente, podrá tener una tapa no hermética (85) en al menos uno de los extremos para facilitar la aireación y la toma de muestras o control del contenido del reactor. The reactor (8) may be hermetically sealed and connected to an oxygen pressure vessel that maintains a hyperbaric oxygen pressure, which spreads homogeneously in the diet or medium from which the larvae are fed. necessarily through the perforations (84) as will be explained below. Alternatively, it may have a non-hermetic cover (85) at at least one of the ends to facilitate aeration and sampling or control of the reactor contents.
La figura 6 describe el funcionamiento general del reactor (8) en condiciones hiperbáricas de aire u oxígeno, preferentemente con una presión entre 1 y 6 bar pudiendo llegar a 20 bar, dependiendo del tipo de larva. El reactor (8), está conectado a un sistema de presión hiperbárica formado por una conducción de presión (18) enchufada a un recipiente a presión o equipo de impulsión (19), que inyecta el gas en el interior del reactor (8). En la conducción de presión (18) hay una válvula de control o de corte (20), que permite controlar la entrada de gas al reactor (8). Igualmente, se introduce un sistema de control de presión formado por un medidor (21) que actúa sobre una válvula de escape (22) o purga del reactor (8) si la presión detectada supera un valor predefinido. La entrada de gas a presión en el reactor (8) puede ser por el propio conducto de aireación (82, 82', 82") o por una entrada añadida, preferentemente también en la parte inferior del reactor (8) y cubierta por los nutrientes y las larvas. Figure 6 describes the general operation of the reactor (8) in hyperbaric conditions of air or oxygen, preferably with a pressure between 1 and 6 bar and can reach 20 bar, depending on the type of larva. The reactor (8), is connected to a hyperbaric pressure system formed by a pressure line (18) plugged into a pressure vessel or delivery equipment (19), which injects the gas into the reactor (8). In the pressure line (18) there is a control or shut-off valve (20), which allows the gas inlet to the reactor (8) to be controlled. Likewise, a pressure control system formed by a meter (21) acting on an exhaust valve (22) or purge the reactor (8) is introduced if the detected pressure exceeds a predefined value. The pressure gas inlet into the reactor (8) can be through the aeration duct itself (82, 82 ', 82 ") or by an added inlet, preferably also at the bottom of the reactor (8) and covered by the Nutrients and larvae.
La corriente gaseosa deberá permitir una humedad, temperatura y difusión de oxígeno adecuadas para la correcta supervivencia y desarrollo de las larvas, siendo las condiciones óptimas conocidas en el estado de la técnica. The gas stream should allow adequate humidity, temperature and oxygen diffusion for the correct survival and development of the larvae, the optimum conditions being known in the state of the art.

Claims

REIVINDICACIONES
1- Equipo de cría de larvas de insectos que comprende un reactor (8) de digestión de las larvas y un sistema de alimentación, estando dicho equipo caracterizado por que comprende un sistema de aireación y un sistema de extracción de sólidos, donde dicho sistema de extracción de sólidos comprende un sistema de impulsión de aire (11) configurado para introducir una corriente de aire de entrada (10) en la parte inferior del reactor (8), y una conducción de salida (12) de aire. 1- Insect larvae breeding equipment comprising a larval digestion reactor (8) and a feeding system, said equipment being characterized in that it comprises an aeration system and a solids extraction system, wherein said system of Solids extraction comprises an air delivery system (11) configured to introduce an inlet air stream (10) into the bottom of the reactor (8), and an air outlet duct (12).
2- Equipo según la reivindicación 1 , donde el sistema de extracción de sólidos comprende además un separador sólido-gas (13) conectado con la conducción de salida (12). 2- Equipment according to claim 1, wherein the solids extraction system further comprises a solid-gas separator (13) connected to the outlet line (12).
3- Equipo según la reivindicación 2, donde el sistema de extracción de sólidos comprende además un separador sólido-sólido (15) que separa las larvas de los materiales sólidos de desecho. 3- Equipment according to claim 2, wherein the solid extraction system further comprises a solid-solid separator (15) that separates the larvae from the solid waste materials.
4- Equipo según cualquiera de las reivindicaciones anteriores, donde el sistema de aireación comprende un conducto de aireación (82, 82', 82") situado en la parte inferior del reactor (8), conectado con la cámara de digestión por medio de un difusor (83) con una pluralidad de perforaciones (84) a lo largo de la cámara de digestión. 4- Equipment according to any of the preceding claims, wherein the aeration system comprises an aeration duct (82, 82 ', 82 ") located at the bottom of the reactor (8), connected to the digestion chamber by means of a diffuser (83) with a plurality of perforations (84) along the digestion chamber.
5- Equipo según la reivindicación 4, donde el conducto de aireación (82, 82, 82") comprende una entrada para la corriente de aire de entrada (10) generada por el sistema de extracción de sólidos. 5- Equipment according to claim 4, wherein the aeration duct (82, 82, 82 ") comprises an inlet for the inlet air stream (10) generated by the solids extraction system.
6- Equipo, según cualquiera de las reivindicaciones anteriores, donde el sistema de aireación es el sistema de extracción de sólidos con el sistema de impulsión de aire (1 1). 6- Equipment according to any of the preceding claims, wherein the aeration system is the solids extraction system with the air delivery system (1 1).
7- Equipo según cualquiera de las reivindicaciones anteriores, donde el sistema de alimentación comprende un mezclador (3) de agua y nutrientes y una extrusora (5) con un estrechamiento (7) previo al reactor (8). 7- Equipment according to any of the preceding claims, wherein the feed system comprises a mixer (3) of water and nutrients and an extruder (5) with a narrowing (7) prior to the reactor (8).
8- Equipo según la reivindicación anterior, donde el mezclador (3) posee forma de tolva. 9- Equipo según cualquiera de las reivindicaciones 7-8, que comprende un tornillo sin fin cuyo primer extremo está dentro del mezclador (3) y un segundo tornillo sin fin o extrusora (5) de uno o dos husillos. 8- Equipment according to the preceding claim, wherein the mixer (3) has a hopper shape. 9. Equipment according to any of claims 7-8, comprising an endless screw whose first end is inside the mixer (3) and a second endless screw or extruder (5) of one or two spindles.
10- Equipo según la reivindicación anterior, donde la salida de la extrusora (5) llega hasta el estrechamiento (7) y donde dicho estrechamiento (7) está conectado a una conducción, flexible o fija, para introducirse en el reactor (8). 10- Equipment according to the preceding claim, where the extruder outlet (5) reaches the narrowing (7) and where said narrowing (7) is connected to a conduit, flexible or fixed, to be introduced into the reactor (8).
1 1- Equipo según cualquiera de las reivindicaciones 7-10, que comprende en el estrechamiento (7) una entrada para una corriente adicional (9) de agua o insectos neonatos. 1 1- Equipment according to any of claims 7-10, comprising in the narrowing (7) an inlet for an additional stream (9) of water or neonatal insects.
12- Equipo según cualquiera de las reivindicaciones anteriores, que comprende además un sistema de presión hiperbárica de aire u oxígeno en el interior del reactor (8) el cual es hermético. 12. Equipment according to any of the preceding claims, further comprising a hyperbaric air or oxygen pressure system inside the reactor (8) which is airtight.
13- Equipo según la reivindicación anterior, donde la presión está comprendida entre 1 y 6 bar, o es igual o inferior a 20 bar. 13. Equipment according to the preceding claim, wherein the pressure is between 1 and 6 bar, or is equal to or less than 20 bar.
14- Equipo según cualquiera de las reivindicaciones 12-13, donde el sistema de presión hiperbárica está formado por una conducción de presión (18) conectada a un recipiente a presión o equipo de impulsión (19) y al reactor (8), y un medidor (21) de la presión interna al reactor (8) conectado a una válvula de escape (22) o purga del reactor (8). 14. Equipment according to any of claims 12-13, wherein the hyperbaric pressure system is formed by a pressure line (18) connected to a pressure vessel or delivery equipment (19) and to the reactor (8), and a internal pressure gauge (21) to the reactor (8) connected to an exhaust valve (22) or reactor purge (8).
15- Equipo según la reivindicación anterior, donde la conducción de presión (18) comprende una entrada al reactor (8) por el sistema de aireación. 15. Equipment according to the preceding claim, wherein the pressure line (18) comprises an inlet to the reactor (8) through the aeration system.
16- Equipo según cualquiera de las reivindicaciones anteriores, donde el reactor (8) tiene perfil cilindrico, hexagonal, cuadrado o rectangular. 16. Equipment according to any of the preceding claims, wherein the reactor (8) has a cylindrical, hexagonal, square or rectangular profile.
17- Equipo según cualquiera de las reivindicaciones anteriores, donde el reactor (8) está cerrado herméticamente. 17. Equipment according to any of the preceding claims, wherein the reactor (8) is sealed.
18- Equipo según cualquiera de las reivindicaciones anteriores, donde el diámetro inscrito del reactor (8) es igual o inferior a su longitud. 19- Sistema de extracción de sólidos, para el equipo de cría de insectos de la reivindicación 1 , caracterizado por que comprende un sistema de impulsión de aire (11) configurado para introducir una corriente de aire de entrada (10) en la parte inferior del reactor (8), y una conducción de salida (12) de aire. 18. Equipment according to any of the preceding claims, wherein the inscribed diameter of the reactor (8) is equal to or less than its length. 19- Solid extraction system, for the insect breeding equipment of claim 1, characterized in that it comprises an air delivery system (11) configured to introduce an inlet air stream (10) in the lower part of the reactor (8), and an outlet duct (12) of air.
20- Sistema según la reivindicación 19, que comprende un separador sólido-gas (13) tras la conducción de salida (12). 20- A system according to claim 19, comprising a solid-gas separator (13) after the exit line (12).
21- Sistema según la reivindicación 20, que comprende además un separador sólido- sólido (15) para separar las larvas de los materiales sólidos de desecho. 21- System according to claim 20, further comprising a solid-solid separator (15) for separating the larvae from solid waste materials.
22- Sistema de alimentación para el equipo de cría de insectos de la reivindicación 1 , caracterizado por que comprende una entrada de una corriente de agua (2) y de una corriente de nutrientes (1) en un mezclador (3), y una extrusora (5) conectada al reactor (8) a través de un estrechamiento (7). 22- Feeding system for the insect breeding equipment of claim 1, characterized in that it comprises an inlet of a stream of water (2) and a stream of nutrients (1) in a mixer (3), and an extruder (5) connected to the reactor (8) through a narrowing (7).
23- Sistema según la reivindicación 22, que comprende una entrada para una corriente adicional (9) de agua o insectos neonatos en el estrechamiento (7). 23- System according to claim 22, comprising an inlet for an additional stream (9) of water or neonatal insects in the narrowing (7).
PCT/ES2015/070364 2014-05-15 2015-05-06 Equipment for breeding insect larvae and auxiliary systems WO2015173450A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
ESP201400396 2014-05-15
ES201400396A ES2551280B2 (en) 2014-05-15 2014-05-15 Breeding equipment for insect larvae and auxiliary systems

Publications (1)

Publication Number Publication Date
WO2015173450A1 true WO2015173450A1 (en) 2015-11-19

Family

ID=54478482

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/ES2015/070364 WO2015173450A1 (en) 2014-05-15 2015-05-06 Equipment for breeding insect larvae and auxiliary systems

Country Status (2)

Country Link
ES (1) ES2551280B2 (en)
WO (1) WO2015173450A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10842138B1 (en) 2017-08-02 2020-11-24 Insecticycle LLC Method, device, and system for use with insect larvae

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5178094A (en) * 1990-05-02 1993-01-12 Crop Genetics International Corporation Method and apparatus for mass producing insects entomopathogens and entomoparasites
GB2436199A (en) * 2006-03-17 2007-09-19 Zoobiotic Ltd Sterile maggot production
WO2010137980A1 (en) * 2009-05-27 2010-12-02 Stichting Wetsus Centre Of Excellence For Sustainable Water Technology Method and device for growing biomass on sludge
WO2010137971A1 (en) * 2009-05-27 2010-12-02 Stichting Wetsus Centre Of Excellence For Sustainable Water Technology System and method for treating an aqueous waste stream
WO2012029041A2 (en) * 2010-09-03 2012-03-08 Francesco Caprio Plant and method for organic waste bioconversion and municipal waste biostabilization
US20120137977A1 (en) * 2010-12-03 2012-06-07 Urban Stream Innovation Inc. Food Production System From Biomass With Heat And Nutrient Recovery
US20120187041A1 (en) * 2011-01-20 2012-07-26 Portland State University Insect-based removal of organic solutes from liquid
US20120214223A1 (en) * 2011-02-21 2012-08-23 Hughes Kenneth D Worm Culture Systems

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5178094A (en) * 1990-05-02 1993-01-12 Crop Genetics International Corporation Method and apparatus for mass producing insects entomopathogens and entomoparasites
GB2436199A (en) * 2006-03-17 2007-09-19 Zoobiotic Ltd Sterile maggot production
WO2010137980A1 (en) * 2009-05-27 2010-12-02 Stichting Wetsus Centre Of Excellence For Sustainable Water Technology Method and device for growing biomass on sludge
WO2010137971A1 (en) * 2009-05-27 2010-12-02 Stichting Wetsus Centre Of Excellence For Sustainable Water Technology System and method for treating an aqueous waste stream
WO2012029041A2 (en) * 2010-09-03 2012-03-08 Francesco Caprio Plant and method for organic waste bioconversion and municipal waste biostabilization
US20120137977A1 (en) * 2010-12-03 2012-06-07 Urban Stream Innovation Inc. Food Production System From Biomass With Heat And Nutrient Recovery
US20120187041A1 (en) * 2011-01-20 2012-07-26 Portland State University Insect-based removal of organic solutes from liquid
US20120214223A1 (en) * 2011-02-21 2012-08-23 Hughes Kenneth D Worm Culture Systems

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10842138B1 (en) 2017-08-02 2020-11-24 Insecticycle LLC Method, device, and system for use with insect larvae

Also Published As

Publication number Publication date
ES2551280B2 (en) 2016-06-22
ES2551280A1 (en) 2015-11-17

Similar Documents

Publication Publication Date Title
Schneider et al. Analysis of nutrient flows in integrated intensive aquaculture systems
Li et al. Bioremediation of fishpond effluent and production of microalgae for an oyster farm in an innovative recirculating integrated multi-trophic aquaculture system
CN104430089A (en) Pollution-free fresh water lobster breeding method
CN104430125B (en) A kind of high-efficiency aquaculture system and method
CN102320712A (en) Chicken manure treatment and reutilization technique
CN102511452B (en) Novel method for artificial mass rearing of Amblyseius orientalis
US9617191B1 (en) Bioreactor system and method
US20130236952A1 (en) System for processing biomass
US20160096761A1 (en) Systems and methods for processing organic compounds
Enache et al. The influence of stocking density on the growth of common carp, Cyprinus carpio, in a recirculating aquaculture system
CN102696922A (en) Intestine protecting compound for sea cucumbers and preparation thereof
CN108713489B (en) Comprehensive intercropping circulating culture system and method for fish and plant symbiosis
US20140305866A1 (en) System for decomposition of organic compounds and method of operation
An et al. Gas production from pig manure fed at different loading rates to polyethylene tubular biodigesters
WO2015173450A1 (en) Equipment for breeding insect larvae and auxiliary systems
CN103351092A (en) Method and equipment for harmlessly treating and utilizing livestock feces on large-scale livestock farm
CN104086066A (en) Economic circulation method of pig industry
SE526875C2 (en) Methods and apparatus for producing biogas from an organic material
CN203923179U (en) The solar energy light-organic of spirulina and fairy shrimp symbiosis culture
CN102499190A (en) Ventilating and stirring type Hermetia illucens bioprocessor
US20140017161A1 (en) Method for production of organic ammonium sulfate using captured nh3 and nh4 produced by aerobic composting
Siikavuopio et al. Comparative growth study of wild-and hatchery-produced Arctic charr (Salvelinus alpinus L.) in a coldwater recirculation system
ES2609101T3 (en) Multiplication procedure of phyto-beneficial microorganisms
CN208402913U (en) A kind of constant-temperature rearing pond
CN205455389U (en) High -efficient recirculating water aquaculture case is supported altogether to fish dish

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 15792005

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 15792005

Country of ref document: EP

Kind code of ref document: A1