• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
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  • 优先权
    • 专利摘要:
    Procedure for the recovery of effluents from the agri-food industry and livestock manure, and plant to carry out said procedure, comprising: an initial stage of separation of the solid part of the effluent from the liquid part by means of a grinder (2) 1000 microns; a stage of pre-treatment of the liquid part obtained in the initial stage, to separate the matter that carries said liquid in suspension by means of, at least, one compactor (11) with filter (27) of up to 240 microns; and a stage of chemical treatment of the liquid product obtained in the pre-treatment stage by adding components such as surfactants, coagulant, polyamide and ozone, which contemplates a double recirculation (24, 24') of the product that creates currents galvanic. (Machine-translation by Google Translate, not legally binding)
    公开号:ES2845275A1
    申请号:ES202030058
    申请日:2020-01-24
    公开日:2021-07-26
    发明作者:Munoz Antonio Cuenca
    申请人:Munoz Antonio Cuenca；
    IPC主号:
    专利说明:

    [0002] PROCEDURE FOR THE RECOVERY OF EFFLUENTS FROM THE AGRI-FOOD INDUSTRY AND LIVESTOCK DEJECTIONS, AND PLANT
    [0004] OBJECT OF THE INVENTION
    [0006] The invention, as expressed in the wording of the present specification, refers to a procedure for the recovery of effluents from the agri-food industry and livestock manure, and to a plant to carry out said procedure, providing advantages and characteristics, which are described in detail below, which represent an improvement of the current state of the art.
    [0008] More specifically, the object of the invention focuses on a process and an effluent recovery plant, which can consist of both agri-food waste and livestock waste or slurry, which, essentially, is based on separating the solid part in suspension from the part liquid by means of a grinder and carry out a treatment of the liquid part obtained which, in turn, comprises a first treatment or pre-treatment with two compactors, which are specifically designed with an auger provided with lining or rubber on its edge and a cover that works under pressure, and that can reach the lower limit of 240 microns, with which it is possible to separate about 90% of the suspended matter carried by the effluent, completing the procedure with a subsequent chemical treatment, which is developed in a treatment tank in which surfactants, coagulant, polyamide and ozone are added, and whose quantity and order of application varies depending on the n of the type of product to be treated. Furthermore, said chemical treatment contemplates a double recirculation of the product in the chemical treatment tank, which creates galvanic currents that, due to their negative charges, accelerate or favor the precipitation of inorganic matter.
    [0010] FIELD OF APPLICATION OF THE INVENTION
    [0012] The field of application of the present invention is framed within the sector of the industry dedicated to the treatment of waste, focusing particularly on the field of organic waste from the agri-food industry, as well as from livestock farms.
    [0013] BACKGROUND OF THE INVENTION
    [0015] As a reference to the current state of the art, it should be noted that the essential objective of the procedure for the recovery of effluents proposed by the present invention is to provide an improvement of the "Treatment process for slurry and plant to carry out said process" described in document ES 2712 324 B2, owned by the applicant himself.
    [0017] Specifically, said process essentially comprises: separating the solid part from the liquid part in a compactor separator, after which, with the liquid part, a centrifugal pre-treatment is carried out in a centrifugal machine and an ozone injection treatment itself and subsequent incorporation of coagulant and pH regulator. In parallel, the solid part separated at the beginning is mixed with that obtained in the centrifuge and fermented in a digester.
    [0019] This process and the plant to carry it out, although it satisfactorily fulfills the objective for which it is intended, has aspects that can be improved, the improvement of said aspects being the objective of the present invention. Specifically, the essential objective of the improved procedure is to replace the centrifuge, and the entire process that is developed in it to improve the performance of the plant by using instead of compactors specifically designed to provide said improvement and ensure a separation of up to 90% of the matter in suspension in the effluent product before submitting it to chemical treatment.
    [0021] EXPLANATION OF THE INVENTION
    [0023] The procedure for the recovery of effluents from the agri-food industry and livestock manure, and the plant to carry out said procedure that the invention proposes allow to satisfactorily achieve the aforementioned objectives, being the characterizing details that make it possible and that it They are conveniently set out in the final claims that accompany the present description.
    [0025] The process and the plant that the invention proposes, as indicated above, applicable both for effluvia of agri-food waste and waste livestock or slurry, essentially, is based on separating the solid part in suspension from the liquid part by means of a grinder of up to 1000 microns and carry out a treatment of the liquid part obtained which, in turn, comprises, firstly, a first treatment or mechanical pre-treatment carried out with at least one, preferably two compactors, which are specifically designed differently from the currently known conventional compactors, with an auger provided with lining or rubber on its edge and a lid that works under pressure, and that can reach the lower limit of 240 microns, with which it is possible to separate about 90% of the suspended matter carried by the effluent, completing the procedure then with a chemical treatment of the liquid product obtained, which is developed, at the less, in a treatment tank in which surfactants, coagulant, polyamide and ozone are added, and whose quantity and order of application v It would vary depending on the type of product to be treated.
    [0027] More specifically, the compacting machine that comprises the plant of the invention incorporates, sewn, glued or injected along the entire end part or edge of the helical wing of the worm, a rubber or piece of lining that causes it to have friction with the filter attached to said auger, at least in the first section of the machine, so that, with the appropriate pressure, it drags the suspended matter greater than the size of the filter.
    [0029] In addition, the lid of this compactor, instead of being a lid in a door format, has a homogeneous pressure outlet, aided by tensioners. More specifically, said tensioners act as a retainer that, with small weights, allow the liquid outflow to be canceled and only when the solid matter exerts a pressure greater than that exerted by the tensioner weights does it open and go outside in very acceptable drying conditions, for subsequent treatment and without producing leachate. In addition, the cover has a rubber seal that makes it fit perfectly with the mouth of the compactor.
    [0031] With all this, the procedure makes it possible to separate, depending on the type of slurry, of the order of 90% of the matter in suspension.
    [0033] As said, the method also comprises a chemical treatment that takes place in a treatment tank. For this, and depending on the product to be treated, the components that are added vary in the quantities and the order of application. Said components are: surfactants or surfactants, coagulant, polyamide and ozone.
    [0035] In any case, the procedure also contemplates that said chemical treatment has double recirculation of the product in the chemical treatment tank, which creates galvanic currents that, due to their negative charges, accelerate or favor the precipitation of inorganic matter. For example, the denitrification process.
    [0037] In short, the process of the present invention is based, in a manner known according to the patent mentioned in the previous section, on:
    [0039] - an initial stage of separation of the solid part of the effluent from the liquid part by means of mechanical elements,
    [0040] - a stage of pre-treatment of the liquid part obtained in the initial stage, also by means of mechanical elements, to separate the matter that carries said liquid in suspension, and
    [0041] - a stage of chemical treatment of the liquid product obtained in the pre-treatment stage by adding components such as surfactants, coagulant, polyamide and ozone.
    [0043] And, based on this, the procedure is distinguished, essentially, in that:
    [0045] - the initial stage of separation of the solid part of the effluent from the liquid part is carried out by means of a 1000 micron grinder,
    [0046] - the pre-treatment stage of the liquid part obtained in the initial stage to separate the matter that carries said liquid in suspension, is carried out by means of, at least, one compactor with a filter of up to 240 microns, and
    [0047] - the stage of chemical treatment based on adding surfactants or surfactants, coagulant, polyamide and ozone, contemplates a double recirculation of the product that creates galvanic currents.
    [0049] The set of actions of separating the solid matter and subsequent treatment of the liquid matter makes the process improve in the reduction of nitrogenous, phosphate, potassium and pathogenic elements, so that the liquid part is deodorized, sanitized and therefore suitable. for irrigation.
    [0051] In the event that better results are desired, sand filters or nano filtrations can optionally be used.
    [0052] To complement the description that is being made and in order to help a better understanding of the characteristics of the invention, the present specification is accompanied, as an integral part thereof, by a set of drawings in which, for illustrative purposes and non-limiting, the following has been represented:
    [0054] Figure number 1.- Shows a schematic representation of an example of the plant to carry out the effluent recovery procedure that is the object of the invention, showing the main parts and elements that it comprises.
    [0056] Figure number 2.- Shows a schematic representation of an example of the separation pre-treatment part by compactors of the plant, according to the invention.
    [0058] Figure number 3.- Shows a schematic representation of an example of the chemical treatment part of the plant, according to the invention.
    [0060] Figures 4, 5 and 6.- They show respective schematic views, in sectioned side elevation, and front and rear elevation, of an embodiment of the compactor that comprises the plant of the invention, showing its general configuration and main parts.
    [0062] Figure number 7.- Shows a schematic elevation view of the inside of the product outlet cover that the compactor of the plant shown in Figures 4 to 6 has.
    [0064] And figure number 8.- Shows a schematic sectional elevation view of the conical body that the compactor has at its entrance to the auger.
    [0066] PREFERRED EMBODIMENT OF THE INVENTION
    [0068] In view of the aforementioned figures, an example of a non-limiting embodiment of the plant to carry out the process of the invention can be observed, which comprises what is indicated and described in detail below, according to the numbering adopted according to the following list:
    [0070] 1 floor
    [0071] grinder
    [0072] first bomb
    [0073] casket
    [0074] agitator
    [0075] butterfly valve
    [0076] sprayer
    [0077] return conduction
    [0078] first deposit
    [0079] level sensor
    [0080] compactor
    [0081] second pump
    [0082] second deposit
    [0083] third bomb
    [0084] third tank, chemical treatment dispensers
    [0085] ozone machine
    [0086] sand filter
    [0087] Valve of three paths
    [0088] fourth tank, of treated water
    [0089] fourth bomb
    [0090] nanofiltration / osmosis system Instant Mix Reactor
    [0091] - 24 'recirculation pipes circuits - 25' fifth and sixth casing turbine pumps
    [0092] endless
    [0093] filter
    [0094] motor
    [0095] axis
    [0096] pulley
    [0097] stop piece, rubber or lining
    [0098] top
    [0099] tensioners
    [0100] Council
    [0101] conical body
    [0102] Thus, as can be seen in said figures, the plant (1) in question essentially comprises a 1000 micron grinder (2) which, fed with product to be treated by a first pump (3) that drives it from a sump ( 4) or pit with agitators (5) as well as water through a butterfly valve (6) or solenoid valve and sprinkler (7), preferably water from the system itself through a return line (8) that communicates With the treated water tank (20) described later, although it can also be tap water, it serves to carry out the first stage of the procedure consisting of separating the liquid part from the solid part.
    [0104] Then, after a first tank (9) to which the liquid part of the product arrives from the grinder (2), and which like the rest of the tanks in the plant has a level sensor (10), the existence of of, at least one compactor (11), with auger (27) and filter (28) of different micron sizes, reaching the lower limit of 240 microns, although the plant (1) preferably has two compactors (11) arranged in line, in any case connected, in turn, through respective butterfly valves (6) and sprinkler (7), with the aforementioned water return conduit (8), in which the pre-treatment of the said liquid part and to which it is driven through a second pump (12).
    [0106] After the compactor (s) (11), another conduit communicates with a second tank (13) where the liquid product arrives and from which, by means of a third pump (14), the corresponding conduit is sent to, at least, a third tank (15) for chemical treatment in which, through corresponding dispensers (16), surfactants or surfactants, coagulant, polyamide and ozone are added, by means of a specific machine (17) for this.
    [0108] Optionally, after said chemical treatment tank (15), the plant (1) comprises a sand filter (18) for greater filtering of the product.
    [0110] In any case, by means of a distribution pipe with a three-way valve (19), the liquid is distributed to a fourth tank (20) of treated water provided in the plant (1), from which said treated water can be used directly and / or make it arrive, through the aforementioned return line (8) and with the help of, at least, a fourth pump (21), preferably two, depending on the existing distance, to the beginning of the plant (1 ) in the sprinklers (7) of the grinder (2) and the compactors (11). In addition, said treated water tank (20), optionally, has a nanofiltration and / or osmosis system (22) and an Instant Mixing Reactor (23) to keep the treated water in the best conditions possible conditions.
    [0112] As can be seen in Figure 1, the chemical treatment tank (15) of the plant comprises two recirculation conduit circuits (referenced respectively as 24 and 24 ') in which, through respective fifth and sixth turbine pumps ( 25, 25 '), the product recirculates before being directed to the next element of the plant, creating galvanic currents whose negative charges accelerate or favor the precipitation of inorganic matter. In the preferred embodiment, the recirculation line of a first circuit (24) incorporates an outlet branch with a three-way valve (19) to divert the treated liquid to the next station of the plant (1) and, also so Preferably, a second circuit (24 ') includes the ozone injection machine (17).
    [0114] Considering said figure 1, the plant (1) of the invention preferably comprises two tanks (15) for chemical treatment to which the product arrives from the previous tank (13) through a bifurcated pipeline with a three-way valve. (19), there being also, in the outlet branch of said tanks (15) another conduit that gathers again, through another three-way valve (19), the product of both tanks (15) in the same conduit that carries the treated liquid to the next station of the plant (1).
    [0116] Looking at Figure 3, it can be seen how, preferably, the plant comprises three dispensers (16) which, through corresponding pipes, respectively incorporate coagulant, polymer and foaming agent into the chemical treatment tank (15). In addition, it also optionally contemplates the inclusion of another dispenser (16), of soda in this case, in one of the two recirculation conduit circuits (24), while the other circuit (24 ') incorporates the injection machine of ozone (17). Likewise, in said figure 3 it is also observed how, optionally, a bicarbonate dispenser (16) is included in the outlet conduit that, after a three-way valve (19), allows the product to be taken to the sand filters (18 ). In addition, the installation foresees that the product coming from the tank (13) in which it accumulates after the compactor (11) and from which it is taken to the treatment tank (15), driven by the corresponding turbine engine (14), also can previously pass through said sand filters (18) by means of the interposition of another three-way valve (19).
    [0118] In short, the plant (1) of the present invention, being one of those which, in a known way, comprises a set of liquid circulation pipes with different pumps (3,12,14,21,25) to circulate the product to be treated from a pit (4) or pit in which said product is located, first to mechanical means (2, 11) for separating the solid part and liquid of the product, then to a tank (15) for chemical treatment, with dispensers (16) that incorporate different components to it, and finally to a tank (20) of treated water, it is essentially distinguished in that, said mechanical means (2 , 11) comprise the 100 micron grinder (2), and the, at least one, compactor (11) with auger (27) and filter (28) of up to less than 240 microns, with which it is possible to separate, depending on the type of product, of the order of 90% of the matter in suspension.
    [0120] On the other hand, taking into account Figures 4 to 8, it is observed how said compactor (11) or compactors (11) of the plant (1) consists, in a known way, of a machine that comprises a casing (26) in the form of a The tube inside which houses an endless screw (27) and a filter (28) that encompasses at least a portion thereof, so that the product, as it passes through it and is pushed by the helical wing of the endless screw (27) It is filtered through said filter (28) in its most liquid portion, while the solids are pushed towards the outlet of the tubular casing (26). The worm (27) is driven by a motor (29) that is coupled to its shaft (30) through a pulley transmission (31).
    [0122] And, based on said configuration, this compactor (11) is distinguished, essentially, in that it incorporates, sewn, glued or injected along the entire end part or edge of the helical wing of the worm (27), a stop piece ( 32) made of rubber or lining that causes it to recede with the filter wall (28).
    [0124] In addition, at the exit of the compactor (11) the existence of a cover (33) is contemplated that incorporates some tensioners (34), appreciable in figure 6, which make it work by pressure, so that the solid matter only comes out when it exerts a pressure greater than that exerted by the tensioners (34). In addition, the cover (33), as seen in figure 7, has internally a rubber gasket (35) that makes it fit perfectly with the outlet mouth of the compactor (11).
    [0126] Likewise, as can be seen in figure 8, the compactor (11) has a conical body (36) that allows the auger (27) to fit perfectly and the movement of said auger (27) to be homogeneous on its axis (30) .
    [0128] Sufficiently described the nature of the present invention, as well as the manner of To put it into practice, it is not considered necessary to make its explanation more extensive so that any expert in the field understands its scope and the advantages derived from it, stating that, within its essentiality, it may be put into practice in other ways implementation that differ in detail from that indicated by way of example, and to which the protection sought will also be achieved as long as its fundamental principle is not altered, changed or modified.
    权利要求:
    Claims (1)
    [0001]
    r e iv in d ic a tio n s
    1. - PROCEDURE FOR THE RECOVERY OF EFFLUENTS FROM THE AGRI-FOOD INDUSTRY AND LIVESTOCK DEJECTIONS, comprising: an initial stage of separation of the solid part of the effluent from the liquid part by means of mechanical elements; a stage of pre-treatment of the liquid part obtained in the initial stage, also by means of mechanical elements, to separate the matter that carries said liquid in suspension; and a stage of chemical treatment of the liquid product obtained in the pre-treatment stage by adding components such as surfactants, coagulant, polyamide and ozone, is characterized in that the initial stage of separation of the solid part of the effluent of the liquid part is carried out by means of a 1000 micron grinder (2); in which the stage of pre-treatment of the liquid part obtained in the initial stage to separate the matter that carries said liquid in suspension, is carried out by means of, at least, one compactor (11) with filter (27) of up to 240 microns; and in which the chemical treatment stage contemplates a double recirculation (24, 24 ') of the product that creates galvanic currents.
    2. - PLANT TO CARRY OUT A PROCEDURE, according to that described in claim 1 which, comprising a set of liquid circulation pipes with different pumps (3,12,14,21,25) to circulate the product to be treated from a manhole (4) or pit in which it is located, to a chemical treatment tank (15), with dispensers (16) that incorporate different components to it, and to a treated water tank (20), it is characterized by comprising a 100 micron grinder (2), fed with product to be treated from the casket (4), and, after a first deposit (9) where the liquid part of product arrives from the grinder (2), at least one compactor (11) with auger (27) and filter (28) down to less than 240 microns.
    4. - PLANT TO CARRY OUT A PROCEDURE, according to claim 3, characterized in that it comprises two compactors (11) arranged in line.
    5. - PLANT TO CARRY OUT A PROCEDURE, according to claim 3 or 4, characterized in that the chemical treatment tank (15) comprises two circuits of recirculation pipes (24, 24 ') in which the product recirculates creating galvanic currents .
    6. - PLANT TO CARRY OUT A PROCEDURE, according to claim 4 or 5, characterized in that it comprises two tanks (15) for chemical treatment.
    7. - PLANT TO CARRY OUT A PROCEDURE, according to any of claims 3 to 6, characterized in that it comprises three dispensers (16) that incorporate coagulant, polymer and foaming agent to the chemical treatment tank (15).
    8. - PLANT TO CARRY OUT A PROCEDURE, according to claim 5, characterized in that it comprises a soda dispenser (16) in one of the two recirculation conduit circuits (24).
    9. - PLANT TO CARRY OUT A PROCEDURE, according to any of claims 3 to 6, characterized in that it comprises a bicarbonate dispenser (16) in a conduit that leads to sand filters (18).
    10. - PLANT TO CARRY OUT A PROCEDURE, according to any of claims 3 to 9, characterized in that the compactor (11) incorporates, sewn, glued or injected along the entire end part or edge of the helical wing of the worm (27), a stop piece (32) made of rubber or lining that causes it to rub against the filter (28).
    11. - PLANT TO CARRY OUT A PROCEDURE, according to claim 10, characterized in that the compactor (11) has a cover (33) that incorporates tensioners (34) that make it work by pressure.
    12. - PLANT TO CARRY OUT A PROCEDURE, according to claim 11, characterized in that the cover (33) has a rubber gasket (35) that makes it fit perfectly with the outlet of the compactor (11).
    13. - PLANT TO CARRY OUT A PROCEDURE, according to any of claims 10 to 12, characterized in that the compactor (11) has a conical body (36) in which the auger (27) fits perfectly, causing the movement of said worm (27) is homogeneous about its axis (30).
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    同族专利:
    公开号 | 公开日
    ES2845275B2|2022-02-14|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    ES2153739A1|1998-07-10|2001-03-01|Riera Molist Ricardo|Purines separation consists of ozone based oxidation, and neutralization of the separated liquid, for simplified distillation|
    ES2198219A1|2002-07-05|2004-01-16|Netporc Xxi S L|Purification of purines consists of mechanical separation of solids, for oxidation neutralization, and distillation and filtration|
    ES2712324A1|2017-11-09|2019-05-10|Munoz Antonio Cuenca|PROCESS OF TREATMENT OF PURINES AND PLANT TO CARRY OUT SUCH PROCESS |
    法律状态:
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    优先权:
    申请号 | 申请日 | 专利标题
    ES202030058A|ES2845275B2|2020-01-24|2020-01-24|PROCEDURE FOR THE RECOVERY OF EFFLUENTS FROM THE AGRI-FOOD INDUSTRY AND LIVESTOCK DEJECTIONS, AND PLANT TO CARRY OUT SAID PROCEDURE|ES202030058A| ES2845275B2|2020-01-24|2020-01-24|PROCEDURE FOR THE RECOVERY OF EFFLUENTS FROM THE AGRI-FOOD INDUSTRY AND LIVESTOCK DEJECTIONS, AND PLANT TO CARRY OUT SAID PROCEDURE|
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