CN112592014A - Dirty conversion utilization apparatus of pig raising excrement with do wet separation function - Google Patents
Dirty conversion utilization apparatus of pig raising excrement with do wet separation function Download PDFInfo
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- CN112592014A CN112592014A CN202011146923.XA CN202011146923A CN112592014A CN 112592014 A CN112592014 A CN 112592014A CN 202011146923 A CN202011146923 A CN 202011146923A CN 112592014 A CN112592014 A CN 112592014A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/02—Biological treatment
- C02F11/04—Anaerobic treatment; Production of methane by such processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C21/00—Disintegrating plant with or without drying of the material
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/18—Treatment of sludge; Devices therefor by thermal conditioning
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/06—Sludge reduction, e.g. by lysis
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- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
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Abstract
The invention discloses a pig raising manure conversion and utilization device with a dry-wet separation function, which comprises a processing device, a dehydration device, a dry material box, a fermentation tank, a cyclone separator, a crushing device, a second spiral feeding machine, a first spiral feeding machine, an annular guide rail and an electric trolley base, wherein the processing device is arranged on the processing device; the pig raising excrement conversion and utilization device with the dry-wet separation function can realize accurate temperature regulation and control in the anaerobic fermentation tank, effectively accelerate the anaerobic fermentation speed, kill pathogenic bacteria in pig manure through high temperature, grind organic matters containing a large amount of cellulose, lignin and other refractory components in the pig manure into powder, further effectively increase the effect of the anaerobic fermentation of the pig manure, preliminarily separate moisture in the pig manure through the pretreatment device, effectively break the agglomerated pig manure, and effectively dehydrate the pig manure through the dehydration device.
Description
Technical Field
The invention relates to the technical field of cultivation waste treatment, in particular to a pig raising excrement conversion and utilization device with a dry-wet separation function.
Background
With the continuous development of economy and society in China, the living standard is rapidly improved, the demand of residents on meat and egg foods is rapidly increased, the domestic livestock and poultry breeding industry is in a rapid development trend and tends to be stable, the pork yield reaches 5299 million tons and accounts for 45.5 percent of the world total amount, and the livestock and poultry breeding industry gradually becomes the most active growth point and the main supporting industry in agricultural economy in China. However, with the improvement of the intensification degree of the farm, the farm is separated from the planting industry, a large amount of excrement is not consumed, the breeding wastewater is discharged out of order, and the like, which is the reason for the large discharge amount of phosphorus in the breeding industry in China and is one of the sources of non-point source pollution of agriculture in China.
With the development of pig raising scale in China, the manure discharge of pig farms is one of the largest pollution industries in China, and although pig raising wastes have more environmental risks, the pig raising wastes are carriers of nutrients and energy and are special agricultural resources, so that the pig raising wastes distributed in small and medium-sized pig farms in rural fields are used for irrigating farmlands for a long time in large quantities, the physical and chemical properties of soil are easily deteriorated, the air permeability and the water permeability of the soil are reduced, and steep growth, lodging, late maturity or immature maturity, yield reduction and even large-area rotting of crops are caused. Improper treatment of pig raising wastes is also prone to breeding mosquitoes and flies, spreading pathogens and further harming human and livestock health. In addition, ammonia, hydrogen sulfide and mercaptan substances in the pig raising waste are main sources of odor pollution, so that the air quality is influenced, and the health of people and livestock is also endangered. Therefore, the problem that the pig raising waste is treated by adopting a reasonable technical means becomes an urgent need to be solved in the existing pig raising industry. In the prior art, three methods are commonly used for treating pig raising wastes: aerobic composting, anaerobic fermentation and thermochemical treatment.
Thermochemical treatment methods include hydrothermal, wet oxidation, incineration, gasification, thermal cracking, and the like. Thermochemical treatment techniques have several common advantages: 1. the range of the solid waste which can be treated is wide, and the solid waste can be treated in a dry or wet manner, has single or complex components, and can be treated in a municipal or agricultural manner; 2. the added value of the product is high, the application is wide, and the resource utilization is realized; 3. belongs to a harmless and quantitative reduction technology, can effectively kill pathogenic bacteria, degrade organic pollutants, reduce the volume of waste and reduce the landfill pressure of urban land. The thermochemical treatment technology is generally only suitable for municipal refuse treatment, and has the disadvantages of high cost, complex treatment procedure, high energy consumption and difficult popularization when being used for treating the excrement of the live pigs.
An aerobic composting method, namely a waste stabilizing and humification process for realizing the aerobic degradation of organic matters and killing pathogenic bacteria at high temperature by microorganisms by artificially controlling the conditions of carbon-nitrogen ratio, water content, pH value, temperature, ventilation quantity and the like of materials of easily degradable organic wastes. In the aspect of treating the pig raising wastes, the pig raising wastes have certain market with the advantages of simple operation, low treatment cost, thorough decomposition of organic matters, good deodorization and sterilization effects, product fertilizer application and the like. However, in the specific operation process, because the type of the feed used by the farmers in the process of feeding the live pigs is not used, the composition of the excrement of the live pigs is different, meanwhile, in the specific implementation process of the aerobic composting method, the difference in the aspects of the control mode and the like can greatly affect the flora of microorganisms, the quality of the compost products and the surrounding environment of the plant area, and the aerobic composting technology still has the problems of serious greenhouse gas emission, difficult treatment of percolate, uneven quality of the compost products, heavy metal pollution risk in the subsequent application and the like. The aerobic composting method has complicated steps, long period in the specific implementation process and high cost of required equipment, so the aerobic composting method is not widely applied in the actual production process.
The anaerobic fermentation method is one of the traditional ways for realizing resource utilization of organic wastes. The technology can effectively convert organic matters into methane and carbon dioxide to burn and generate electricity mainly through assimilation of anaerobic bacteria. Therefore, the method is already in the farming era, and the technology is widely applied. However, the existing anaerobic fermentation has the following problems: firstly, three processes of low-temperature fermentation, medium-temperature fermentation and high-temperature fermentation are generally needed in the process of fermenting the pig manure, and the existing anaerobic fermentation tank cannot realize accurate temperature regulation and control. The method is widely applied to the treatment of the live pig manure through wet anaerobic fermentation and medium-high temperature anaerobic fermentation. The PH value required by anaerobic fermentation is generally 6.5-7.5 from the viewpoint of ensuring the methane production; from the viewpoint of stabilization of organic matter, the retention time is generally 20 to 30 days. However, the pig manure contains a large amount of organic matters containing refractory components such as wood fibers and the like, so that the effect of anaerobic fermentation of the pig manure is reduced; in addition, the conventional anaerobic fermentation of the pig manure is limited by the fermentation temperature, so that a large amount of pathogenic bacteria are remained in the pig manure.
Disclosure of Invention
The invention aims to overcome the defects in the prior art, and provides a pig raising excrement conversion and utilization device with a dry-wet separation function, which can realize accurate temperature regulation and control in an anaerobic fermentation tank, effectively accelerate the speed of anaerobic fermentation, kill pathogenic bacteria in pig manure through high temperature, and grind a large amount of organic matters containing cellulose, lignin and other refractory components in pig manure into powder, thereby effectively increasing the effect of the pig manure anaerobic fermentation and effectively solving the problems in the background art.
The invention is realized by the following technical scheme:
a pig raising excrement conversion and utilization device with a dry-wet separation function comprises a processing device, a dehydration device, a dry material box, a fermentation tank, a cyclone separator, a crushing device, a second spiral feeding machine, a first spiral feeding machine, an annular guide rail and an electric trolley base; the treatment device comprises a rectangular box body, a discharge port is arranged on the lower side of the right end of the outer side surface of the rectangular box body, a feed port of the first spiral feeding machine is connected with the discharge port, the dehydration device comprises a cylindrical outer shell, a second motor and a second cylindrical flow guide cover, the upper end of the outer side surface of the second cylindrical flow guide cover is connected with the discharge port of the first spiral feeding machine through a first feeding nozzle, the cylindrical outer shell is rotatably connected with a cylindrical inner shell through bearings arranged at the left end and the right end of the inner side surface of the cylindrical outer shell, a material pushing screw rod and a water discharge hole are arranged on the inner side surface of the cylindrical inner shell, the left end of the inner side surface of the cylindrical inner shell is rotatably connected with the right end of the outer side surface of the second cylindrical flow guide cover through a sealing bearing, a liquid discharge pipe is arranged in the middle of the lower end of the outer, the material pushing screw penetrates through the inner side surface of the first cylindrical flow guide cover, the drying box comprises a cylindrical storage bin, the upper end of the outer side surface of the cylindrical storage bin is connected with the tail end of the first cylindrical flow guide cover, a third motor is installed on the outer side surface of the cylindrical storage bin, an output shaft of the third motor is connected with the right end surface of the material pushing screw through a coupler, a spherical storage bin is arranged on the lower end surface of the cylindrical storage bin, the crushing device comprises a pulverizer, a feed inlet of a second spiral feeding machine is connected with the lower end of the outer side surface of the spherical storage bin, a discharge outlet of the second spiral feeding machine is connected with a feed inlet of the crushing device, an air pump is arranged on the outer side surface of the pulverizer, a crushed material discharge port is arranged on the lower side of the right end of the outer side surface of the pulverizer, the second spiral feeding machine comprises a conical barrel body, the conical barrel body is fixedly connected with a storage, the up end of cone links to each other through the air inlet of first honeycomb duct with the air pump, and the gas outlet of air pump links to each other with the lateral surface right-hand member upside of milling machine, the fermentation cylinder includes the cylindricality reactor.
Furthermore, two first motors which are arranged in a bilateral symmetry mode are arranged at the left end and the right end of the front side face of the rectangular box body, triangular baffles are arranged at the center of the bottom of the inner side face of the rectangular box body and at the left end and the right end of the inner side face of the rectangular box body, the rectangular box body is rotatably connected with two material stirring rotating shafts through bearings arranged at the left end and the right end of the middle part of the inner side face of the rectangular box body, a material fork is arranged on the outer side face of each material stirring rotating shaft, the front end face of each material stirring rotating shaft is connected with an output shaft of each first motor, an upper cover plate is arranged on the upper surface of the rectangular box; the setting of triangle-shaped baffle can be effectively to carry out the initial gross separation to the moisture that contains in the live pig excrement and urine, can break up the live pig excrement and urine of conglobation through the material fork.
Furthermore, the cavity on the inner side surface of the cylindrical inner shell is gradually enlarged from left to right, and the solid-liquid separation is facilitated by the arrangement of the gradually-changed inner cavity.
Further, first belt pulley is installed to the output shaft of second motor, and the left end face of cylindricality interior casing passes the left surface setting of cylindricality shell body, and the left end face of cylindricality interior casing has cup jointed the second belt pulley, and the second belt pulley passes through the belt and links to each other with first belt pulley.
Furthermore, the lower end of the outer side surface of the storage tank is provided with a dry material outlet, a third electric control valve is installed on the dry material outlet, and the outer side surface of the storage tank is provided with a fourth support frame.
Furthermore, a filter screen is arranged at the upper end of the inner side surface of the conical barrel, a high-pressure pump is arranged at the upper end of the outer side surface of the conical barrel, an air outlet of the high-pressure pump is connected with the upper end surface of the conical barrel, an air inlet of the high-pressure pump is connected with the first flow guide pipe through a flushing pipe, and a second electric control valve is mounted on the flushing pipe.
Furthermore, the cylindrical reactor is composed of an outer heat-insulating layer and an inner heat-conducting layer, a heating cavity is arranged between the outer heat-insulating layer and the inner heat-conducting layer, heat-conducting oil and an electric heating wire are arranged inside the heating cavity, and the heat-conducting oil is convenient to uniformly heat.
Furthermore, the outer side surface of the cylindrical reactor is provided with a fifth support frame, the bottom of the cylindrical reactor is provided with a discharge pipe, and a discharge pipe valve is arranged on the discharge pipe.
Further, the upper end of the inner side surface of the cylindrical reactor is provided with a pressure sensor and a temperature sensor, the cylindrical reactor is provided with a stirring shaft in the middle of the inner side surface thereof through the arrangement, the outer side surface of the stirring shaft is provided with a stirring screw, the upper end surface of the cylindrical reactor is provided with an upper end cover, the middle of the upper surface of the upper end cover is provided with a stirring motor, the output shaft of the stirring motor is connected with the upper end surface of the stirring shaft through a coupler, the upper surface of the upper end cover is provided with a conical feeding nozzle, a liquid feeding pipe and an exhaust pipe, and the conical feeding nozzle.
Further, the fermentation cylinder is installed on the upper surface of electronic dolly base, and electronic dolly base installation is on ring rail, and twelve are no less than to the quantity of electronic dolly base, and the electronic dolly base evenly distributed of no less than twelve is at ring rail's upper surface, the setting of a plurality of fermentation cylinders for the dirty processing of live pig excrement can carry out in succession.
Compared with the prior art, the invention has the following beneficial effects:
1. the pig raising excrement conversion and utilization device with the dry-wet separation function can realize accurate temperature regulation and control in the anaerobic fermentation tank, effectively accelerate the anaerobic fermentation speed, kill pathogenic bacteria in the live pig excrement at high temperature, and grind a large amount of organic matters containing cellulose, lignin and other refractory components in the live pig excrement into powder, thereby effectively increasing the effect of the live pig excrement anaerobic fermentation.
2. Moisture in the pig manure can be preliminarily separated through the pretreatment device, the agglomerated pig manure can be effectively scattered, the pig manure can be effectively dehydrated through the dehydration device, and the arrangement of the triangular baffle plate can effectively prevent the pig manure from being accumulated at the dead angle inside the rectangular box body.
3. Can grind the coarse fiber in the raw pig manure after the dehydration into the powder through the milling machine, can wash the filter screen through the high-pressure pump, can prevent effectively that the filter screen from taking place to block up, can carry out heat treatment to the fermentation cylinder through electric heating wire, the setting of conduction oil has made things convenient for the thermally equivalent.
Drawings
FIG. 1 is a schematic front view of the present invention;
FIG. 2 is a schematic structural view of the present invention;
FIG. 3 is a schematic view of the pretreatment apparatus;
FIG. 4 is a cross-sectional view of a pretreatment device;
FIG. 5 is a schematic view of a dewatering device;
FIG. 6 is a schematic view of a crushing and feeding device;
FIG. 7 is a schematic view of a fermenter configuration;
FIG. 8 is a front view of the fermenter.
In the figure: 1 pretreatment device, 2 dehydration device, 3 dry box, 4 fermentation tank, 5 cyclone separator, 6 crushing device, 7 second spiral feeder, 8 first spiral feeder, 9 annular guide rail, 10 electric trolley base, 11 feeding pipe, 12 rectangular box, 13 discharging port, 14 triangular baffle, 15 fork, 16 stirring rotating shaft, 17 water pumping pipe, 18 feeding nozzle, 19 water pumping port, 20 lifting lug, 21 upper cover plate, 22 first motor, 23 first feeding nozzle, 24 pushing screw, 25 second motor, 26 first belt pulley, 27 liquid discharging pipe, 28 first support, 29 second support, 30 spherical storage bin, 31 third motor, 32 cylindrical storage bin, 33 first cylindrical flow guide cover, 34 cylindrical outer shell, 35 cylindrical inner shell, 36 second belt pulley, 37 second cylindrical flow guide cover, 38 flour mill, 39 air pump, 40 first flow guide pipe, 41 second valve, 41 second flow guide pipe, 38 first flow guide pipe, 40 second flow guide pipe, 41 second valve, 9 second spiral feeder, 9 annular guide rail, 10 electric trolley base, 11 feeding pipe, 12 rectangular box, 13 discharging port, 14 triangular baffle, 42 flushing pipes, 43 high-pressure pumps, 44 conical cylinders, 45 third support frames, 46 material storage tanks, 47 third electric control valves, 48 fourth support frames, 49 second guide pipes, 50 crushed aggregate discharge openings, 51 stirring screws, 52 air pressure sensors, 53 stirring shafts, 54 temperature sensors, 55 electric heating wires, 56 cylindrical reactors, 57 fifth support frames, 58 fifth electric control valves, 59 conical feeding nozzles, 60 stirring motors, 61 liquid adding pipes, 62 air discharging pipes, 63 upper end covers and 64 discharging pipes.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
As shown in fig. 1 and 2, a pig raising excrement conversion and utilization device with dry-wet separation function comprises a processing device 1, a dewatering device 2, a dry material box 3, a fermentation tank 4, a cyclone separator 5, a crushing device 6, a second spiral feeding machine 7, a first spiral feeding machine 8, an annular guide rail 9 and an electric trolley base 10, wherein the fermentation tank 4 is installed on the upper surface of the electric trolley base 10, the electric trolley base 10 is installed on the annular guide rail 9, the number of the electric trolley base 10 is not less than twelve, and the electric trolley base 10 with not less than twelve is uniformly distributed on the upper surface of the annular guide rail 9.
As shown in fig. 3 and 4, the processing device 1 includes a rectangular box 12, a discharge port 13 is provided at the lower side of the right end of the outer side of the rectangular box 12, a feed port of a first spiral feeder 8 is connected with the discharge port 13, two first motors 22 are provided at the left and right ends of the front side of the rectangular box 12, two triangular baffles 14 are provided at the center and left and right ends of the bottom of the inner side of the rectangular box 12, two material stirring shafts 16 are rotatably connected to the rectangular box 12 through bearings provided at the left and right ends of the middle portion of the inner side thereof, a material fork 15 is provided at the outer side of the material stirring shaft 16, the front end surface of the material stirring shaft 16 is connected with the output shaft of the first motor 22, an upper cover plate 21 is provided on the upper surface of the rectangular box 12, a feed pipe 11, a water pumping port 19 and a lifting lug 20 are provided on the upper surface of the, moisture in the pig manure can be preliminarily separated through the pretreatment device, the agglomerated pig manure can be effectively scattered, the pig manure can be effectively dehydrated through the dehydration device, and the triangular baffle plate 14 can be used for effectively preventing the pig manure from being accumulated at the dead angle inside the rectangular box body 12.
As shown in fig. 5, the dewatering device 2 includes a cylindrical outer housing 34, a second motor 25 and a second cylindrical air guide sleeve 37, the upper end of the outer side surface of the second cylindrical air guide sleeve 37 is connected with the discharge port of the first spiral feeder 8 through a first feeding nozzle 23, the cylindrical outer housing 34 is rotatably connected with a cylindrical inner housing 35 through bearings arranged at the left and right ends of the inner side surface thereof, the cavity of the inner side surface of the cylindrical inner housing 35 gradually becomes larger from left to right, the inner side surface of the cylindrical inner housing 35 is provided with a pushing screw 24 and a drain hole, the left end of the inner side surface of the cylindrical inner housing 35 is rotatably connected with the right end of the outer side surface of the second cylindrical air guide sleeve 37 through a sealing bearing, the left end surface of the pushing screw 24 is rotatably connected with the left end of the inner side surface of the second cylindrical air guide sleeve 37 through a bearing, the middle part of the lower, the pushing screw 24 is arranged by penetrating through the inner side surface of the first cylindrical air guide sleeve 33, the first cylindrical air guide sleeve 33 is fixed on the ground by a first support frame 28, the second cylindrical air guide sleeve 37 is arranged on the ground by a positioning support, the first belt pulley 26 is arranged on the output shaft of the second motor 25, the left end surface of the cylindrical inner shell 35 is arranged by penetrating through the left side surface of the cylindrical outer shell 34, the left end surface of the cylindrical inner shell 35 is sleeved with a second belt pulley 36, the second belt pulley 36 is connected with the first belt pulley 26 by a belt, the drying box 3 comprises a cylindrical storage bin 32, the upper end of the outer side surface of the cylindrical storage bin 32 is connected with the tail end of the first cylindrical air guide sleeve 33, the outer side surface of the cylindrical storage bin 32 is provided with a third motor 31, the output shaft of the third motor 31 is connected with the right end surface of the pushing screw 24 by a, the lower end surface of the cylindrical storage bin 32 is provided with a spherical storage bin 30.
As shown in fig. 6, the crushing device 6 comprises a flour mill 38, coarse fibers in dehydrated pig manure can be ground into powder by the flour mill 38, a feed inlet of the second spiral feeder 7 is connected with the lower end of the outer side of the spherical storage bin 30, a discharge outlet of the second spiral feeder 7 is connected with a feed inlet of the crushing device 6, an air pump 39 is arranged on the outer side of the flour mill 38, a crushed material discharge outlet 50 is arranged on the lower side of the right end of the outer side of the flour mill 38, the second spiral feeder 7 comprises a conical cylinder 44, the conical cylinder 44 is fixedly connected with a storage tank 46 through a third support frame 45, a dry material outlet is arranged on the lower end of the outer side of the storage tank 46, a third electric control valve 47 is arranged on the dry material outlet, a fourth support frame 48 is arranged on the outer side of the storage tank 46, the upper end of the outer side of the conical cylinder 44 is connected with the crushed material discharge outlet 50 through a second guide pipe 49, the upper end of the conical cylinder 44 is, the air outlet of the air pump 39 is connected with the upper side of the right end of the outer side face of the flour mill 38, a filter screen is arranged at the upper end of the inner side face of the conical barrel 44, a high-pressure pump 43 is arranged at the upper end of the outer side face of the conical barrel 44, the air outlet of the high-pressure pump 43 is connected with the upper end face of the conical barrel 44, the air inlet of the high-pressure pump 43 is connected with the first flow guide pipe 40 through a flushing pipe 42, a second electric control valve 41 is installed on the flushing pipe 42, the filter screen can be flushed through the high-pressure.
As shown in fig. 7 and 8, the fermentation tank 4 comprises a cylindrical reactor 56, the cylindrical reactor 56 comprises an outer heat-insulating layer and an inner heat-conducting layer, a heating cavity is arranged between the outer heat-insulating layer and the inner heat-conducting layer, heat-conducting oil and an electric heating wire 55 are arranged inside the heating cavity, the fermentation tank can be heated by the electric heating wire 55, the heat-conducting oil is conveniently arranged for uniform heating, a fifth support frame 57 is arranged on the outer side surface of the cylindrical reactor 56, a discharge pipe 64 is arranged at the bottom of the cylindrical reactor 56, a discharge pipe valve is arranged on the discharge pipe 64, an air pressure sensor 52 and a temperature sensor 54 are arranged at the upper end of the inner side surface of the cylindrical reactor 56, a stirring shaft 53 is arranged in the middle of the inner side surface of the cylindrical reactor 56, a stirring screw 51 is arranged on the outer side surface of the stirring shaft 53, an upper end cover, agitator motor 60's output shaft passes through the shaft coupling and links to each other with the up end of (mixing) shaft 53, the upper surface of upper end cover 63 is equipped with toper feed nozzle 59, liquid feeding pipe 61 and blast pipe 62, install fifth electrically controlled valve 58 on the toper feed nozzle 59, this dirty conversion utilization equipment of pig raising excrement that has dry and wet separation function, can realize accurate temperature regulation and control in the anaerobic fermentation jar, anaerobic fermentation's speed has effectively been accelerated, and can kill the pathogenic bacterium in the pig excrement and urine through high temperature, can be with a large amount of celluloses that contain in the pig excrement and urine, the organic matter of difficult degradation compositions such as lignin grinds into the powder, thereby can effectively increase pig excrement and urine anaerobic fermentation's effect.
When in use: switching on an external power supply, feeding the raw pig manure and sewage in a pig house into the rectangular box body 12 through the feeding nozzle 18 and the feeding pipe 11, driving the material fork 15 to rotate by the first motor 22, pulling the solid pig manure to the position near the discharging port 13 by the material fork 15, scattering the pig manure in blocks by the material fork 15, pumping the sewage in the rectangular box body 12 out through the water pumping pipe 17, conveying the sewage into external deodorization and sterilization equipment for deodorization and sterilization, using the sewage after deodorization and sterilization for planting water-cultured vegetables, conveying the solid pig manure containing a large amount of moisture into the cylindrical inner shell 35 through the first spiral feeding machine 8, driving the cylindrical inner shell 35 to rotate at high speed through the belt transmission system by the second motor 25 to dehydrate the pig manure, discharging the sewage generated by dehydration into the external deodorization and sterilization equipment through the discharging pipe 27 for deodorization and sterilization, using the sewage after deodorization and sterilization for planting the water-cultured vegetables, the dehydrated pig manure is conveyed into the spherical storage bin 30 through the pushing screw 24, the pig manure in the spherical storage bin 30 is conveyed into the pulverizer 38 through the second spiral feeding machine 7, the pig manure is thoroughly pulverized by the pulverizer 38, the pulverized pig manure is pumped into the conical cylinder 44 through the cyclone separator, finally enters the interior of the cylindrical reactor 56 through the third electric control valve 47 and the conical feeding nozzle 59, water and additives can be added into the interior of the cylindrical reactor 56 through the liquid adding pipe 61, the materials in the cylindrical reactor 56 can be heated through the electric heating wire before anaerobic fermentation, germs in the high-temperature heating process, in the anaerobic fermentation process, the mixture in the cylindrical reactor 56 is stirred by the stirring device, after the stirring is completed, the interior of the cylindrical reactor 56 is vacuumized through the exhaust pipe 62, or nitrogen gas is injected into the interior of the column reactor 56.
It is to be noted that, in the embodiment, the input ends of the second spiral feeder 7, the first spiral feeder 8, the electric trolley base 10, the first motor 22, the second motor 25, the third motor 31, the pulverizer 38, the air pump 39, the second electric control valve 41, the high-pressure pump 43, the third electric control valve 47, the air pressure sensor 52, the temperature sensor 54, the electric heating wire 55, the fifth electric control valve 58 and the stirring motor 60 are all electrically connected to the output shaft of the external control switch set, the core chip of the external control switch set 12 is a PLC single chip, specifically, the model is siemens S7-200, the second spiral feeder 7, the first spiral feeder 8, the electric trolley base 10, the first motor 22, the second motor 25, the third motor 31, the pulverizer 38, the air pump 39, the second electric control valve 41, the high-pressure pump 43, the third electric control valve 47, the electric heating wire 55, the electric heating wire 41, the electric trolley base 10, the electric heating wire 55, the fifth electric control valve 58 and the stirring motor 60 can be freely configured according to practical application scenes, and the external control switch group controls the second spiral feeding machine 7, the first spiral feeding machine 8, the electric trolley base 10, the first motor 22, the second motor 25, the third motor 31, the flour mill 38, the air pump 39, the second electric control valve 41, the high-pressure pump 43, the third electric control valve 47, the air pressure sensor 52, the temperature sensor 54, the electric heating wire 55, the fifth electric control valve 58 and the stirring motor 60 to work by adopting a method commonly used in the prior art.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (10)
1. The utility model provides a dirty conversion of pig raising excrement utilizes device with dry wet separation function which characterized in that: comprises a processing device (1), a dewatering device (2), a dry material box (3), a fermentation tank (4), a cyclone separator (5), a crushing device (6), a second spiral feeding machine (7), a first spiral feeding machine (8), an annular guide rail (9) and an electric trolley base (10); the treatment device (1) comprises a rectangular box body (12), a discharge hole (13) is formed in the lower side of the right end of the outer side face of the rectangular box body (12), a feed inlet of the first spiral feeding machine (8) is connected with the discharge hole (13), the dehydration device (2) comprises a cylindrical outer shell (34), a second motor (25) and a second cylindrical flow guide cover (37), the upper end of the outer side face of the second cylindrical flow guide cover (37) is connected with the discharge hole of the first spiral feeding machine (8) through a first feeding nozzle (23), the cylindrical outer shell (34) is rotatably connected with a cylindrical inner shell (35) through bearings arranged at the left end and the right end of the inner side face of the cylindrical outer shell (37), a material pushing screw (24) and a water discharge hole are formed in the inner side face of the cylindrical inner shell (35), and the left end of the inner side face of the cylindrical inner, the left end face of a material pushing screw rod (24) is rotatably connected with the left end of the inner side face of a second cylindrical flow guide cover (37) through a bearing, a liquid discharge pipe (27) is arranged in the middle of the lower end face of the outer side face of a cylindrical outer shell (34), a cylindrical inner shell (35) is rotatably connected with a first cylindrical flow guide cover (33) through a bearing arranged at the right end of the inner side face of the cylindrical inner shell, the material pushing screw rod (24) penetrates through the inner side face of the first cylindrical flow guide cover (33) to be arranged, a dry box (3) comprises a cylindrical storage bin (32), the upper end of the outer side face of the cylindrical storage bin (32) is connected with the tail end of the first cylindrical flow guide cover (33), a third motor (31) is installed on the outer side face of the cylindrical storage bin (32), an output shaft of the third motor (31) is connected with the right end face of the material pushing screw rod (24) through a coupler, the feed inlet of the second spiral feeding machine (7) is connected with the lower end of the outer side surface of the spherical storage bin (30), the discharge outlet of the second spiral feeding machine (7) is connected with the feed inlet of the crushing device (6), an air pump (39) is arranged on the outer side surface of the flour mill (38), a crushed material discharge opening (50) is arranged on the lower side of the right end of the outer side surface of the flour mill (38), second spiral material loading machine (7) are including cone shell (44), and cone shell (44) are through third support frame (45) fixedly connected with stock chest (46), and the lateral surface upper end of cone shell (44) links to each other with crushed aggregates escape orifice (50) through second honeycomb duct (49), and the up end of cone shell (44) links to each other through the air inlet of first honeycomb duct (40) with air pump (39), and the gas outlet of air pump (39) links to each other with the lateral surface right-hand member upside of milling machine (38), fermentation cylinder (4) are including cylindricality reactor (56).
2. The device for converting and utilizing the feces of the pig raising with the dry-wet separation function according to claim 1, wherein: both ends are equipped with first motor (22) that two bilateral symmetry set up about the leading flank of rectangle box (12), medial surface bottom central authorities of rectangle box (12) all are equipped with triangle-shaped baffle (14) with controlling both ends, rectangle box (12) are connected with two through setting up bearing rotation at its inboard middle part left and right sides both ends and dial material pivot (16), the lateral surface of dialling material pivot (16) is provided with material fork (15), the preceding terminal surface of dialling material pivot (16) links to each other with the output shaft of first motor (22), the last surface mounting of rectangle box (12) has upper cover plate (21), the upper surface of upper cover plate (21) is provided with inlet pipe (11), draw water mouth (19) and lug (20), feed nozzle (18) are installed to the end of inlet pipe (11), draw water mouth (19) department and be provided with drinking-water pipe (17).
3. The device for converting and utilizing the feces of the pig raising with the dry-wet separation function according to claim 1, wherein: the cavity of the inner side surface of the cylindrical inner shell (35) is gradually enlarged from left to right.
4. The device for converting and utilizing the feces of the pig raising with the dry-wet separation function according to claim 1, wherein: first belt pulley (26) is installed to the output shaft of second motor (25), and the left end face that cylindricality shell body (34) was passed to the left surface setting of cylindricality interior casing (35), and second belt pulley (36) have been cup jointed to the left end face of cylindricality interior casing (35), and second belt pulley (36) pass through the belt and link to each other with first belt pulley (26).
5. The device for converting and utilizing the feces of the pig raising with the dry-wet separation function according to claim 1, wherein: the lower end of the outer side face of the storage tank (46) is provided with a dry material outlet, a third electric control valve (47) is installed on the dry material outlet, and the outer side face of the storage tank (46) is provided with a fourth support frame (48).
6. The device for converting and utilizing the feces of the pig raising with the dry-wet separation function according to claim 1, wherein: the upper end of the inner side surface of the conical cylinder body (44) is provided with a filter screen, the upper end of the outer side surface of the conical cylinder body (44) is provided with a high-pressure pump (43), an air outlet of the high-pressure pump (43) is connected with the upper end surface of the conical cylinder body (44), an air inlet of the high-pressure pump (43) is connected with the first flow guide pipe (40) through a flushing pipe (42), and the flushing pipe (42) is provided with a second electric control valve (41).
7. The device for converting and utilizing the feces of the pig raising with the dry-wet separation function according to claim 1, wherein: the column reactor (56) is composed of an outer heat-insulating layer and an inner heat-conducting layer, a heating cavity is arranged between the outer heat-insulating layer and the inner heat-conducting layer, and heat-conducting oil and an electric heating wire (55) are arranged inside the heating cavity.
8. The device for converting and utilizing the feces of the pig raising with the dry-wet separation function according to claim 1, wherein: the outer side surface of the cylindrical reactor (56) is provided with a fifth support frame (57), the bottom of the cylindrical reactor (56) is provided with a discharge pipe (64), and a discharge pipe valve is arranged on the discharge pipe (64).
9. The device for converting and utilizing the feces of the pig raising with the dry-wet separation function according to claim 1, wherein: the pneumatic control stirring device is characterized in that an air pressure sensor (52) and a temperature sensor (54) are arranged at the upper end of the inner side face of the cylindrical reactor (56), a stirring shaft (53) is arranged in the middle of the inner side face of the cylindrical reactor (56) through the arrangement, a stirring screw (51) is installed on the outer side face of the stirring shaft (53), an upper end cover (63) is arranged on the upper end face of the cylindrical reactor (56), a stirring motor (60) is arranged in the middle of the upper surface of the upper end cover (63), an output shaft of the stirring motor (60) is connected with the upper end face of the stirring shaft (53) through a coupler, a conical feeding nozzle (59), a liquid feeding pipe (61) and an exhaust pipe (62) are arranged on the upper surface of the upper end.
10. The device for converting and utilizing the feces of the pig raising with the dry-wet separation function according to claim 1, wherein: the fermentation tank (4) is arranged on the upper surface of the electric trolley base (10), the electric trolley base (10) is arranged on the annular guide rail (9), the number of the electric trolley bases (10) is not less than twelve, and the electric trolley bases (10) which are not less than twelve are uniformly distributed on the upper surface of the annular guide rail (9).
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115626750A (en) * | 2022-12-21 | 2023-01-20 | 湖南大略环保科技有限公司 | High solid content is treatment device for aquaculture waste water |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20050000906A1 (en) * | 2002-04-09 | 2005-01-06 | Jean-Francois Blais | Methods and apparatus for treating animal manure |
CN201165520Y (en) * | 2008-01-12 | 2008-12-17 | 宝林 | Heating heat insulation anaerobic fermentator |
EP2135938A1 (en) * | 2008-06-20 | 2009-12-23 | Sergio Trabattoni | Anaerobic fermentation process and plant |
CN104710091A (en) * | 2015-04-03 | 2015-06-17 | 周玲娣 | Pretreatment method before milk cow manure anaerobic fermentation |
CN206970434U (en) * | 2017-06-13 | 2018-02-06 | 西北民族大学 | A kind of sludge multistage anaerobic fermentation vat |
CN208980562U (en) * | 2018-10-15 | 2019-06-14 | 遂宁市安居区长华养殖专业合作社 | A kind of swine excrement separating dry space from moist space device |
CN209210795U (en) * | 2018-10-31 | 2019-08-06 | 河南未来再生能源股份有限公司 | A kind of anaerobic ferment devices |
CN210764552U (en) * | 2019-07-05 | 2020-06-16 | 安徽力孚建筑工程有限公司 | Anaerobic generator with automatic stirring function |
-
2020
- 2020-10-23 CN CN202011146923.XA patent/CN112592014B/en active Active
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20050000906A1 (en) * | 2002-04-09 | 2005-01-06 | Jean-Francois Blais | Methods and apparatus for treating animal manure |
CN201165520Y (en) * | 2008-01-12 | 2008-12-17 | 宝林 | Heating heat insulation anaerobic fermentator |
EP2135938A1 (en) * | 2008-06-20 | 2009-12-23 | Sergio Trabattoni | Anaerobic fermentation process and plant |
CN104710091A (en) * | 2015-04-03 | 2015-06-17 | 周玲娣 | Pretreatment method before milk cow manure anaerobic fermentation |
CN206970434U (en) * | 2017-06-13 | 2018-02-06 | 西北民族大学 | A kind of sludge multistage anaerobic fermentation vat |
CN208980562U (en) * | 2018-10-15 | 2019-06-14 | 遂宁市安居区长华养殖专业合作社 | A kind of swine excrement separating dry space from moist space device |
CN209210795U (en) * | 2018-10-31 | 2019-08-06 | 河南未来再生能源股份有限公司 | A kind of anaerobic ferment devices |
CN210764552U (en) * | 2019-07-05 | 2020-06-16 | 安徽力孚建筑工程有限公司 | Anaerobic generator with automatic stirring function |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN115626750A (en) * | 2022-12-21 | 2023-01-20 | 湖南大略环保科技有限公司 | High solid content is treatment device for aquaculture waste water |
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