SYSTEM AND METHOD FOR COMPREHENSIVE TREATMENT OF CULTIVATION POLLUTION IN SCALABLE PIG FARM

Abstract

A system for comprehensive treatment of cultivation pollution in a scalable pig farm includes a source separation pigsty, a pigsty flushing water treatment system, a solid-liquid separation system, a solid high-temperature aerobic fermentation system, a liquid high-temperature aerobic fermentation system, an odor and flue gas treatment system, a boiler system and a test and control system. The source separation pigsty is designed into a pigsty that separates feces and urine from rainwater, pigsty flushing water and residual drinking water. The sludge pump pumps the feces and urine to the solid-liquid separation device. Solids separated by the solid-liquid separation device are conveyed to the solid high-temperature aerobic fermentation system, and liquid separated by the solid-liquid separation device is conveyed to the liquid high-temperature aerobic fermentation system. The boiler system includes a boiler, a circulating pump, a hot water pipeline and a water return pipeline.

Claims

1. A system for comprehensive treatment of cultivation pollution in a scalable pig farm comprising a source separation pigsty a pigsty flushing water treatment system, a solid-liquid separation system, a solid high-temperature aerobic fermentation system, a liquid high-temperature aerobic fermentation system, an odor and flue gas treatment system, a boiler system and a test and control system, wherein the source separation pigsty is designed into a pigsty that separates feces and urine from rainwater, pigsty flushing water and residual drinking water; the rainwater and the residual drinking water are discharged into an outdoor drainage ditch; the feces and urine are conveyed to a feces collection pit of the solid-liquid separation system; the pigsty flushing water is discharged into a pigsty flushing water pit of the pigsty flushing water treatment system; the solid-liquid separation system is composed of a sludge pump installed at a bottom of the feces collection pit, a solid-liquid separation device and conveying equipment; the sludge pump pumps the feces and urine to the solid-liquid separation device; solids separated by the solid-liquid separation device are conveyed to a feed port of the solid high-temperature aerobic fermentation system, and liquid separated by the solid-liquid separation device is conveyed to a liquid inlet of the liquid high-temperature aerobic fermentation system; fermentation odor exhaust ports of the solid high-temperature aerobic fermentation system and the liquid high-temperature aerobic fermentation system and a flue gas exhaust port of the boiler system are connected with the odor and flue gas treatment system through pipelines; the boiler system comprises a boiler, a circulating pump, a hot water pipeline and a water return pipeline; the hot water pipeline of the boiler is connected with a heat exchange jacket or coil pipe of the solid high-temperature aerobic fermentation system and a jacket or coil pipe of the liquid high-temperature aerobic fermentation system; the circulating pump is installed in the water return pipeline; all sensors of the test and control system are disposed in the above systems to detect all key parameters; and the rest and control system controls connection of the above systems.

2. The system according to claim 1, wherein the pigsty flushing water treatment system is composed of the pigsty flushing water pit, an ABR (anaerobic baffled reactor) and a plurality of parallel-connected SBRs (sequencing batch reactors); a water overflow port is formed in an upper part of the pigsty flushing water pit; a large grating and a small grating are respectively installed on a water inlet outer side and a water outlet inner side of the pigsty flushing water pit; the water outlet side of the overflow port is connected with a water inlet of the ABR through an overflow pipe, a water outlet of the ABR is connected with water inlets of the parallel-connected SBRs through pipelines respectively; an electromagnetic valve is installed in front of the water inlet of each SBR; the water outlet of each SBR is connected to an ecological wetland through a pipeline; and settled sludge in the pigsty flushing water pit, in the ABR and in the SBRs are conveyed to a feed port of the solid high-temperature aerobic fermentation reactor and then are mixed with feces for fermentation to prepare a solid organic fertilizer

3. The system according to claim 1, wherein the solid high-temperature aerobic fermentation system comprises 1 to X solid high-temper a true aerobic fermentation reactors; X is more than or equal to 1, each solid high-temperature aerobic fermentation reactor is composed of an inclined horizontal drum, a teed side sealing cover labyrinth sealing device, a discharge side sealing cover labyrinth sealing device; a power supporting wheel group, a stirring and anti-sticking device and an integrated base; a water jacket is arranged outside the horizontal drum; a feed side is higher than a discharge side; the horizontal drum, a feed side sealing cover, a discharge side sealing cover and the labyrinth sealing devices on both sides form a closed fermentation space; a feed hole and an exhaust hole are formed in an upper part of the feed side scaling cover; an air inlet hole is formed in an upper part of the discharge side sealing cover; a discharge hole is formed in a lower part of the discharge side sealing cover; a discharge gate is installed on a discharge hole; the stirring and anti-sticking device is positioned in the horizontal drum which is disposed on the power supporting wheel group; and the power supporting wheel group, the feed side sealing cover and the discharge side sealing cover are fixed to the inclined integrated base to form a whole.

4. The system according to claim 3, wherein a structure and principle of the feed side sealing cover labyrinth sealing device are completely the same as those of the discharge side sealing cover labyrinth sealing device, and each of the structures is that two or more concentric cylindrical hoods having unequal diameters are perpendicularly welded and fixed to an inner side of the sealing cover, and the cylindrical hoods are consistent in height; correspondingly, a radial lining ring is welded and fixed to an inner wall of the drum at an end part of the horizontal drum; periphery of the lining ring is hermetically welded and fixed with the inner wall of the drum; one, two or more concentric cylindrical bodies having unequal diameters are perpendicularly welded on the lining ring, and the concentric cylindrical bodies are consistent in height, moreover, the height of each of the concentric cylindrical bodies is equal to that of each of the concentric cylindrical hoods on the sealing cover; and the concentric cylindrical hoods on the inner sides of the sealing covers and the concentric cylindrical bodies on the lining ring at the end part of the horizontal drum are alternately sheathed and sealed in a labyrinth manner.

5. The system according to claim 4, wherein according to a length of the horizontal drum, the stirring and anti-sticking device is composed of one or more cage-shaped structures; when the horizontal drum is relatively short, the stirring and anti-sticking device is composed of only one cage-shaped structure; when the horizontal drum is relatively long, the stirring and anti-sticking device is composed of a plurality of cage-shaped structures; each of the cage-shaped structures is composed of two coaxial supporting plates and a plurality of shoveling plates; the supporting plates are circular rings, and both ends of each of the plurality of shoveling plates are respectively connected and fixed with the two coaxial supporting plates; correspondingly, contact blocks are disposed on the inner wall of the horizontal drum; the plurality of shoveling plates are parallel to axes of the cage-shaped structures, or the plurality of shoveling plates and the axes of the cage-shaped structures form inclined angles, or the plurality of shoveling plates are of spiral curve shapes; and when the horizontal drum rotates, the contact blocks on the inner wall drive the stirring and anti-sticking device to rotate.

6. The system according to claim 1, wherein the liquid high-temperature aerobic fermentation system is composed of 1 to N liquid high-temperature aerobic fermentation reactors; N is more than or equal to 1; each liquid high-temperature aerobic fermentation reactor mainly comprises a top cover, a tank body, a lifting device and a hanging basket; a feed port is formed in the top cover, and a discharge port is formed in a bottom of the tank body; a heat exchange coil is arranged in the tank and is connected with an external hot water pipeline through a water inlet flange and a water outlet flange which are installed on the tank body; an aeration device is also arranged in the tank and is connected with an aeration pipeline and a fan through an air inlet flange installed on the tank body; an exhaust port flange is also installed on the top cover of the tank body to exhaust aeration waste gas; the discharge port is connected to a biogas generating pit through a pipeline; the aeration device is connected to an external fan through an air inlet pipeline; the lifting device is used for lifting and transferring the top cover component and the hanging basket, the hanging basket is composed of a hanging basket main body, a hanging basket door and a lock catch; the hanging basket door is laterally opened from one side and is used for allowing putting dead livestock or placentas into the hanging basket; steel meshes are welded at an upper part, a bottom and a side wall of the hanging basket main body; and the hanging basket carries the dead livestock and the placentas and puts the dead livestock and the placentas into the feces and urine fermentation liquid for fermentation.

7. The system according to claim 1, wherein the odor and flue gas treatment system comprises an odor heat exchange condenser, a flue gas heat exchange condenser, a biological deionization filtering tower, an induced draft fan, a temperature sensor, a three-way electric regulation valve and an electromagnetic valve; each heat exchange condenser comprises an upper end cover, a tank body and a lower end cover which are connected and fixed in sequence; an upper end of the upper end cover is provided with an odor inlet flange; an odor collection pipeline is connected and fixed with the odor inlet flange, a lower part of the side wall of the tank body is provided with a fresh air inlet flange, and a upper part is provided with a hot air exhaust flange; an upper pipe plate is installed at an upper part of the tank body and a lower pipe plate is installed at a lower part of the tank body, a plurality of holes are uniformly formed in the upper and the lower pipe plates; a heat exchange pipe passes through corresponding holes of the upper pipe plate and the lower pipe plate to connect the upper pipe plate with the lower pipe plate; both ends of the heat exchange pipe are respectively fixed to the upper and the lower pipe plates, so that a closed cavity is formed among the ripper and the lower pipe plates, an outer side of the heat exchange pipe and an outer wall of the tank body and is communicated with outside through the fresh air inlet flange and the hot air exhaust flange; a plurality of pull rods are uniformly fixed to the lower pipe plate; a plurality of partition plates are uniformly arranged in a space between the fresh air inlet flange and the hot air exhaust flange in the tank body; the partition plates are fixed to the pull rods; an inner cavity of the heat exchange pipe is communicated with the upper end cover and the lower end cover: a U-shaped pipe is arranged at a bottom of a lower cover plate; an odor exhaust flange is arranged on a side wall of the lower end cover; a volume of the lower end cover of each heat exchange condenser is greater than or equal to that of the upper end cover; each partition plate is of a trimmed circular structure and has a diameter equal to an inner diameter of the tank body; the partition plates are uniformly distributed in the tank body in a disordered manner along an axial direction; and the partition plates are fixed to the pull rods, so that fresh air flows in a Z-shaped manner.

8. The system according to claim 7, wherein the odor and flue gas treatment system is configured to realize the following treatment systems: (1) an odor treatment system of the solid high-temperature aerobic fermentation system, wherein the exhaust port of the solid high-temperature aerobic fermentation reactor is connected with a heat exchange air inlet of the odor heat exchange condenser A; a heat exchange exhaust port of the odor heat exchange condenser A is connected with an input end of the induced draft fan; an electromagnetic valve and a bypass branch are arranged on an air inlet pipeline of the odor heat exchange condenser A; the bypass branch of the odor heat exchange condenser A is provided with an electromagnetic valve; an output end of the induced draft fan is connected with an air inlet of the biological deodorization filtering tower, and a temperature sensor is installed on a main-path air inlet pipeline of the biological deodorization filtering tower; a biological deodorization filler is arranged in the biological deodorization filtering tower; the air inlet of the odor heat exchange condenser A is connected with atmosphere, and an air output port connected to an air inlet of the solid high-temperature aerobic fermentation reactor through a pipeline; and (2) an odor treatment system of the high-temperature aerobic fermentation system and a flue gas treatment system of the boiler system, wherein a flue gas exhaust port of the boiler is connected with one air inlet input end of a three-way electric regulation valve, and the other air inlet input end of the three-way electric regulation valve is connected with atmosphere; an output end of the three-way electric regulation valve is connected with an input end of an aeration fan; an output end of the aeration fan is connected with an air inlet flange of the liquid high-temperature aerobic fermentation reactor; an exhaust flange of the liquid high-temperature aerobic fermentation reactor is connected with a heat exchange air inlet of an odor heat exchange condenser B; a heat exchange exhaust port of the odor heat exchange condenser B is connected with the input end of the induced draft fan; an electromagnetic valve and a bypass branch are arranged on an air inlet pipeline of the odor heat exchange condenser B; a bypass branch of the odor heat exchange condenser B is provided with an electromagnetic valve; the output end of the induced draft fan is connected with an air inlet of a biological deodorization filtering tower, and a temperature sensor is installed on a main-path air inlet pipeline of the biological deodorization filtering tower; a biological deodorization filler is arranged in the biological deodorization filtering tower; an air inlet of the odor heat exchange condenser B is connected with the atmosphere, and an air output port is connected to an air inlet of the boiler through a pipeline.

9. The system according to claim 7, wherein when the boiler is used for incinerating objects, such as garbage and dead pigs which, block the aeration heads easily, the odor and flue gas treatment system adopts the following connection modes that: (1) in an odor treatment system of the solid high-temperature aerobic fermentation system, the exhaust, port of the solid high-temperature aerobic fermentation reactor is connected with a heat exchange air inlet of an odor heat exchange condenser A; a heat exchange exhaust port of the odor heat exchange condenser A is connected with an input end of the induced draft fan; an electromagnetic valve and a bypass branch are arranged on an air inlet pipeline of the odor heat exchange condenser A; the bypass branch of the odor heat exchange condenser A is provided with the electromagnetic valve; an output end of the induced draft fan is connected with an air inlet of a biological deodorization filtering tower, and a temperature sensor is installed on a main-path air inlet pipeline of the biological deodorization filtering tower; a biological deodorization filler is arranged in the biological deodorization filtering tower, the air inlet of the odor heat exchange condenser A is connected with atmosphere, and an air output port is connected to an air inlet of the solid high-temperature aerobic fermentation reactor through a pipeline; (2) in an odor treatment system of the liquid high-temperature aerobic fermentation system, an exhaust flange of a liquid high-temperature aerobic fermentation reactor is connected with a heat exchange air inlet of an odor heat exchange condenser C; a heat exchange exhaust port of the odor heat exchange condenser C is connected with the input end of the induced draft fan; an electromagnetic valve and a bypass branch are arranged on an air inlet pipeline of the odor heat exchange condenser C; the bypass branch of the odor heat exchange condenser C is provided with, the electromagnetic valve; the output end of the induced draft fan is connected with the air inlet of the biological deodorization filtering tower, and the temperature sensor is installed on the main-path air inlet pipeline of the biological deodorization filtering tower; the biological deodorization filler is arranged in the biological deodorization filtering tower; the air inlet of the odor heat exchange condenser C is connected with atmosphere; an air output port is connected to an air inlet of an aeration fan through a pipeline; and an air outlet of the aeration fan is connected with an air inlet of the liquid high-temperature aerobic fermentation reactor; and (3) in a flue gas treatment system of the boiler system, a flue gas exhaust port of the boiler is connected with a heat exchange air inlet of the flue gas heat exchange condenser; a heat exchange exhaust port of the flue gas heat exchange condenser is connected wish the input end of the induced draft fan; the output end of the induced draft fan is connected with the air inlet of the biological deodorization filtering tower; the biological deodorization filler is arranged in the biological deodorization filtering tower; the air inlet of the fine gas heat exchange condenser is connected with atmosphere; and an air output port is connected to an air inlet of the boiler through a pipeline.

10. The system according to claim 1, wherein the boiler system mainly comprises the boiler, the circulating pump, a pressure water tank, a three-way electric regulation valve and an electromagnetic valve, a water outlet pipeline of the boiler is connected to an input end of the three-way electric regulation valve; two output ends of the three-way electric regulation valve are respectively connected with water inlet flanges of parallel-connected liquid high-temperature aerobic fermentation reactors and parallel-connected solid high-temperature aerobic fermentation reactors through the water outlet pipeline; water outlet pipelines of the liquid high-temperature aerobic fermentation reactors and the solid high-temperature aerobic fermentation reactors are connected with the electromagnetic valve, a water outlet of the electromagnetic valve is connected with the water return pipeline of the boiler; temperature sensors me respectively arranged on the water outlet pipeline and the water return pipeline of the boiler; and the circulating pump is further installed on the water return pipeline to allow circulating water to form a loop.

11. The system according to claim 1, wherein the test and control system comprises a sensor, a controller and a data gateway which are installed in system equipment; the controller acquires key data of all aspects of the system equipment through the sensor and coordinately controls all parts of the system equipment according to the acquired data, the controller further communicates with the data gateway; and the controller sends the key data to a cloud or remote server through the data gateway for later inquiry and management.

12. A method for comprehensive treatment of system according to claim 1, comprising that: (I) a source separation pigsty separates rainwater from sewage, separates drinking water from sewage and separates feces and urine from pigsty flushing water; rainwater and residual drinking water of pigs are discharged to an external ditch; pigsty flushing water is conveyed into a pigsty flushing water pit; feces and urine are conveyed into a feces collection pit; (II) when a liquid level of the pigsty flushing water in the pigsty flushing water pit reaches an overflow port, the pigsty flushing water is filtered through gratings; filtrate flows into ABRs (anaerobic baffled reactors) through an overflow pipeline; a test and control system controls to turn on or turn off electromagnetic valves in front of SBRs (sequencing batch reactors) to allow liquid treated by the ABRs to respectively flow into different SBRs, and the SBRs are aerated intermittently according to an SBR technique to realize an aerobic-anaerobic technological process; before a complete SBR technique cycle is completed, the control system turns off the electromagnetic valve in front of the reactor and turns on the electromagnetic valve in front of a next SBR; when the SBRs complete the complete SBR treatment technique, a water pump pumps supernatant into an ecological wetland for discharging; sludge in the pigsty flushing water pit, the ABRs and the SBRs are regularly conveyed to a feed port of a solid high-temperature aerobic fermentation reactor and mixed with feces for fermentation to prepare a solid organic fertilizer; (III) the feces and urine of piglets in a suckling period and a nursing period are conveyed into a liquid high-temperature aerobic fermentation reactor, namely a solid part separated by a solid-liquid separation device from the feces and urine of fattening pigs, boars and sows is conveyed into the solid high-temperature aerobic fermentation reactor, and a liquid part separated through solid-liquid separation is conveyed into the liquid high-temperature aerobic fermentation reactor; (IV) auxiliary materials and high-temperature aerobic bacteria are conveyed into the solid high-temperature aerobic fermentation reactor through conveying equipment; during feeding, the test and control system starts all power driving devices at the same time to allow all power supporting wheel groups to rotate at the same nine to drive a horizontal drum of the solid high-temperature aerobic fermentation reactor to rotate forwards; by action of a spiral stirring and anti-sticking device in the solid high-temperature aerobic fermentation reactor, fermentation raw materials are conveyed to a discharge side, and organic waste is shoveled up and dropped down so that organic waste is fully stirred and mixed with oxygen, thereby enlarging a contact area of fermentation raw materials and the oxygen; (V) dead pigs and placentas are put into a hanging basket through a forklift truck or other sets of transferring equipment; a lifting device lifts the hanging basket into the liquid high-temperature aerobic fermentation reactor to immerse the whole hanging basket into the liquid, and at the same time, a proper amount of a composite microbial fermentation agent is inoculated into the liquid high-temperature aerobic fermentation reactor for high-temperature aerobic fermentation; if certain pig farms are qualified for treating the dead pigs and the placentas in an incineration way or other sanitary ways, the hanging basket is omitted; (VI) a circulating pump and a boiler are started in sequence; hot water enters a jack of the solid high-temperature aerobic fermentation reactor and a heat exchange coil of the liquid high-temperature aerobic fermentation reactor to respectively heat solids in the solid high-temperature aerobic fermentation reactor and liquid in the liquid high-temperature aerobic fermentation reactor. (VII) a boiler system and an odor and flue gas treatment system are started at the same time, and the odor and fine gas treatment system is configured to realize the following methods: (1) an odor treatment method of a solid high-temperature aerobic fermentation system odor exhausted by the solid high-temperature aerobic fermentation reactor through an exhaust port is cooled by an odor heat exchange condenses A, then is absorbed and converted through a biological deodorization filtering tower and is discharged after meeting a standard; hot air subjected to heat exchange through the odor heat exchange condenser A enters the solid high-temperature aerobic fermentation reactor through an air inlet of the solid high-temperature aerobic fermentation reactor to provide fresh hot air for the solid high-temperature aerobic fermentation reactor; and (2) an odor treatment method of a high-temperature aerobic fermentation system and a flue gas treatment method of the boiler system: an aeration fan adjusts an opening of a three-way electric regulation valve according to air oxygen demand of a material in the liquid high-temperature aerobic fermentation reactor to aerate the liquid high-temperature aerobic fermentation reactor, so that air input ends of a hearth of the boiler and the three-way electric regulation valve are in negative pressure states all the time, and flue gas generated by the boiler and partial fresh air are mixed through the three-way electric regulation valve and enter the liquid high-temperature aerobic fermentation reactor for aeration; odor exhausted by the liquid high-temperature aerobic fermentation reactor through the exhaust port is cooled by an odor heat exchange condenser B, then is absorbed and converted through the biological deodorization filtering tower and is discharged after reaching the standard; and hot air subjected to hear exchange of the odor heat exchange condenser B enters the hearth of the boiler to provide fresh hot air for the boiler; (VIII) when the boiler is used for incinerating objects, such as garbage and dead pigs which block the aeration heads easily, the odor and flue gas treatment system is configured to realize the following methods. (1) an odor treatment method of the solid high-temperature aerobic fermentation system, the odor exhausted by the solid high-temperature aerobic fermentation reactor through the exhaust port is cooled by the odor heat exchange condenser A, then is absorbed and converted through the biological deodorization filtering tower and is discharged after reaching the standard; hot air subjected to heat exchange through the odor heat exchange condenser A enters the solid high-temperature aerobic fermentation reactor through the air inlet of the solid high-temperature aerobic fermentation reactor to provide fresh hot air for the solid high-temperature aerobic fermentation reactor; (2) an odor treatment method of the liquid high-temperature aerobic fermentation system: the odor exhausted by the liquid high-temperature aerobic fermentation reactor through the exhaust port is cooled by the odor heat exchange condenser C, then is absorbed and converted through the biological deodorization filtering tower and is discharged after reaching the standard; hot air subjected to heat exchange of the odor heat exchange condenser C is blasted into the liquid high-temperature aerobic fermentation reactor through the aeration fan to provide fresh hot air for the liquid high-temperature aerobic fermentation reactor; and (3) flue gas exhausted by the boiler is cooled by the flue gas heat exchange condenser, then is absorbed and converted through the biological deodorization filtering tower and is discharged after reaching the standard; and cold air is heated by the flue gas heat exchange condenser and then enters the hearth of the hot water boiler to provide fresh hot air for the hot water boiler; (IX) when detecting that the odor temperature detected by a temperature sensor installed on a main-path air inlet pipeline of the biological deodorization filtering tower is more than 40 C., the test and control system turns on the electromagnetic valves on the air inlet pipelines of the odor heat exchange condensers A, B and C and turns off the electromagnetic valves of the bypass branches to allow the odor entering the biological deodorization filtering tower to be cooled by the odor heat exchange condensers A, B and C at first; when detecting that odor temperature detected by the temperature sensor installed on the main-path air inlet pipeline of the biological deodorization filtering tower is less than 15 C., the test and control system turns off the electromagnetic valves on the air inlet pipelines of the odor heat exchange condensers A, B and C and turns on the electromagnetic valves of the bypass branches to forbid the odor to enter the odor heat exchange condensers A, B and C for cooling, so that the biological deodorization filtering tower works in a temperature range between 15 C. and 40 C., so as to guarantee the deodorization effect and prevent dormancy and death of microorganisms in the biological deodorization filtering tower; (X) when hot odor and cold air are subjected to heat exchange in the odor heat exchange condensers A, B and C, and hot flue gas and cold air are subjected to heat exchange in the flue gas heat exchange condenser, produced condensed water is discharged by the odor heat exchange condensers A, B and C and the flue gas heat exchange condenser and then is drained to an external ditch through a pipeline; (XI) in an aerobic fermentation reaction process, the test and control system controls a power driving device of the solid high-temperature aerobic fermentation reactor to operate in a periodic intermittent operation manner of backward rotation-stop-backward rotation-stop . . . according to a detected temperature of the fermentation raw material or a set time; during rotation of a drum, under driving of contact blocks welded on an inner wall of a horizontal drum, shoveling plates of a stirring and anti-sticking device drive materials at an inner bottom of the horizontal drum to move upwards along an inner wall of the drum, and materials are separated from the shoveling plates and thrown away and fall back to the bottom of the horizontal drum under gravity action, so as to achieve stirring and air contact effects; by action of spiral shoveling plates in the solid high-temperature aerobic fermentation reactor, a backward rotating drum shovels up the materials and conveys the fermentation raw materials to a feed side, so that the fermentation materials are not compacted on a discharge side sealing cover; because cage-shaped structures of the stirring and anti-sticking device collide with different contact blocks in the drum and rotate under the driving of the contact blocks, the cage-shaped structures and the inner wall of the drum slide relatively, so that the fermentation raw materials are not adhered to the inner wall of the drum of the solid high-temperature aerobic fermentation reactor, and energy consumption caused by stirring and heat conduction is minimized; (XII) solids in the solid high-temperature aerobic fermentation reactor are continuously fermented at 60 C. or higher for more than 24 hours to complete the whole high-temperature aerobic fermentation process to prepare the solid organic fertilizer; the test and control system controls to turn off electromagnetic valves at front ends of the power driving device and a water inlet pipeline of the water jacket and controls to turn on a discharge gate at the same time; then the test and control system controls the power driving device to continuously rotate forwards to discharge part of old fermentation materials to a next working procedure for treatment through external conveying equipment; (XIII) the material in the liquid high-temperature aerobic fermentation reactor is continuously fermented at 60 C. or higher for more than 3 days to complete the whole high-temperature aerobic fermentation process; if carcasses of dead pigs and placentas are not placed, the feces and urine are continuously fermented at 60 C. or higher for 24 hours to complete high-temperature harmless treatment; further, a discharge port of the liquid high-temperature aerobic fermentation reactor is provided with a heat preservation anaerobic fermentation reactor (a biogas generating pit), hot fermentation liquid subjected to the high-temperature aerobic fermentation is immediately conveyed to the heat preservation anaerobic fermentation reactor subjected to heat preservation treatment through a pipeline for high-temperature or medium-temperature anaerobic fermentation: the fermentation liquid is continuously anaerobically fermented at 35-60 C. for 15 to 20 days to complete the anaerobic fermentation process; after being diluted, secondary fermentation liquid is directly applied for agriculture, and produced biogas is applied to the boiler system or power generation; residues produced by the dead pigs are rotten, and hairs and bone residues are conveyed to a furnace for incineration, ash produced by incineration is conveyed to the solid high-temperature aerobic fermentation reactor and is mixed with solid feces for fermentation, so as to prepare a solid organic fertilizer; (XIV) the test and control system is used for monitoring and acquiring key data of all aspects of the system for comprehensive treatment and coordinately controlling all constituents of the system for comprehensive treatment according to the acquired data; (1) in the high-temperature aerobic fermentation reaction process, the test and control system automatically controls the opening of a circulating water three-way electric regulation valve according to the temperatures of the materials in the high-temperature aerobic fermentation reactors, so that the temperatures of the fermentation materials are stabilized at a set temperature all the time: when the temperature of the material in the high-temperature aerobic fermentation reactor of a first fermentation object is less than the set value, the opening of the three-way electric regulation valve in this loop is 100%, and the openings of the loops of other high-temperature aerobic fermentation reactors are 0; when the temperature of the material of the first fermentation object is close to the set value, the test and control system controls to turn on the electromagnetic valve in the loop of the second high-temperature aerobic fermentation reactor, and the three-way electric regulation valve performs PID regulation to allow the hot circulating water part to flow through the second high-temperature aerobic fermentation reactor, so that the second high-temperature aerobic fermentation reactor is heated under the condition of stabilizing the temperature of the material of the first high-temperature aerobic fermentation reactor at the set value; because the aerobic fermentation process is a heat release process, with the fermentation, the temperatures of the materials in the high-temperature aerobic fermentation reactors continuously rise up; when the temperature of the material in the high-temperature aerobic fermentation reactor of the first fermentation object is greater than the set value, the test and control system slows down or shuts off the heating of the boiler, under the action of the circulating pump, the circulating water of the high-temperature aerobic fermentation reactors of the first fermentation object and the second fermentation object is mixed, resulting in that the temperature of the material in the high-temperature aerobic fermentation reactor of the first fermentation object is reduced, and the temperature of the material in the high-temperature aerobic fermentation reactor of the second fermentation object is increased; the three-way electric legislation valve and the electromagnetic valve are coordinately controlled by the test and control system to convey fermentation reaction heat of the previous high-temperature aerobic fermentation reactor and heat generated by heating of the boiler to the second or Mth solid high-temperature aerobic fermentation reactor or the Nth liquid high-temperature aerobic fermentation reactor, so that the temperatures of the materials in the high-temperature aerobic fermentation reactors may be stabilized at the set value, and the heat energy generated by the fermentation reaction may be recycled; and (2) the test and control system uploads the key data in a data region in the test and control system to a cloud or remote server for storage and backup through communication with a data gateway, so that all data of a treatment process evidence chain are stored for later inquiry and service staff of a remote head office can find out faults and alarm of equipment operation by virtue of the cloud data and handle with the faults and alarm in time; and the data stored in the cloud are also favorable for completion and upgrading of the treatment system.

13. The method according to claim 12, wherein the odor and flue gas treatment system is configured to realize the following methods: (1) an odor treatment method of the solid high-temperature aerobic fermentation system: odor exhausted by the solid high-temperature aerobic fermentation reactor through an exhaust port is cooled by an odor heat exchange condenser A, then is absorbed and converted through a biological deodorization filtering tower and is discharged after reaching the standard; hot air subjected to heat exchange through the odor heat exchange condenser A enters the solid high-temperature aerobic fermentation reactor through an air inlet of the solid high-temperature aerobic fermentation reactor to provide fresh hot air for the solid high-temperature aerobic fermentation reactor; and (2) an odor treatment method of a high-temperature aerobic fermentation system and a flue gas treatment method of the boiler system; an aeration fan adjusts the opening of a three-way electric regulation valve according to an oxygen demand of a material in the liquid high-temperature aerobic fermentation reactor to aerate the liquid high-temperature aerobic fermentation reactor, so that the air input ends of a hearth of the boiler and the three-way electric regulation valve are in negative pressure states all the time, and flue gas generated by the boiler and partial fresh air are mixed through the three-way electric regulation valve and enter the liquid high-temperature aerobic fermentation reactor; odor exhausted by the liquid high-temperature aerobic fermentation reactor through the exhaust port is cooled by an odor heat exchange condenser B, then is absorbed and converted through the biological deodorization filtering tower and is discharged after reaching the standard; and hot air subjected to heat exchange of the odor heat exchange condenser B enters the hearth of the boiler to provide fresh hot air for the boiler.

14. The method according to claim 12, wherein the odor and flue gas treatment system is configured to realize the following methods: (1) an odor treatment method of the solid high-temperature aerobic fermentation system: the odor exhausted by the solid high-temperature aerobic fermentation reactor through the exhaust port is cooled by the odor heat exchange condenser A, then is absorbed and converted through the biological deodorization filtering tower and is discharged after reaching the standard; hot air subjected to heat exchange through the odor heat exchange condenser A enters the solid high-temperature aerobic fermentation reactor through the air inlet of the solid high-temperature aerobic fermentation reactor to provide fresh hot air for the solid high-temperature aerobic fermentation reactor; (2) an odor treatment method of the liquid high-temperature aerobic fermentation system: odor exhausted by the liquid high-temperature aerobic fermentation reactor through the exhaust port is cooled by the odor heat exchange condenser C, then is absorbed and converted through the biological deodorization filtering tower and is discharged after reaching the standard; hot air subjected to heat exchange of the odor heat exchange condenser C is blasted into the liquid high-temperature aerobic fermentation reactor through the aeration fan to provide fresh hot air for the liquid high-temperature aerobic fermentation reactor; and (3) flue gas exhausted by the boiler is cooled by the flue gas heat exchange condenser, then is absorbed and converted through the biological deodorization filtering tower and is discharged after reaching the standard; and cold air is heated by the flue gas heat exchange condenser and then enters the hearth of the hot water boiler to provide fresh hot air for the hot water boiler.

Description

DESCRIPTION OF THE DRAWINGS

[0089] FIG. 1 is a schematic diagram of a system for comprehensive treatment of cultivation pollution in a scalable pig farm;

[0090] FIG. 2 is a structural schematic diagram of a pollutant source separation pigsty;

[0091] FIG. 3 is a sectional diagram along line A-A of FIG. 2;

[0092] FIG. 4 is a schematic diagram of a pigsty flushing water treatment system;

[0093] FIG. 5 is a schematic diagram of an overall structure of a solid high-temperature aerobic fermentation reactor.

[0094] FIG. 6 is a schematic diagram of a specific structure of a solid high-temperature aerobic fermentation reactor.

[0095] FIG. 7 is a structural schematic diagram of a side surface of a power supporting wheel group;

[0096] FIG. 8 is a structural schematic diagram of a cross section of a power supporting wheel group;

[0097] FIG. 9 is a schematic diagram of a cage-shaped structure with parallel shoveling plates;

[0098] FIG. 10 is a schematic diagram of a cage-shaped structure with inclined shoveling plates;

[0099] FIG. 11 is a structural diagram of Embodiment 1 of a sealing device;

[0100] FIG. 12 is an enlarged view of portion A in FIG. 11;

[0101] FIG. 13 is a structural schematic diagram of Embodiment 2 of a sealing device;

[0102] FIG. 14 is an enlarged view of portion C in FIG. 13;

[0103] FIG. 15 is a structural schematic diagram of a stop wheel;

[0104] FIG. 16 is a structural schematic diagram of a liquid high-temperature aerobic fermentation reactor.

[0105] FIG. 17 is a structural schematic diagram of a top cover component of a liquid high-temperature aerobic fermentation reactor;

[0106] FIG. 18 is a structural schematic diagram of a hanging basket;

[0107] FIG. 19 is a schematic diagram of Embodiment 1 of an odor and flue gas treatment system;

[0108] FIG. 20 is a schematic diagram of Embodiment 2 of an odor and line gas treatment system;

[0109] FIG. 21 is a schematic diagram of Embodiment 3 of an odor and flue gas treatment system;

[0110] FIG. 22 is a schematic diagram of Embodiment 4 of an odor and flue gas treatment system;

[0111] FIG. 23 is a schematic diagram of Embodiment 5 of an odor and flue gas treatment system;

[0112] FIG. 24 is a structural schematic diagram of a heat exchange condenser;

[0113] FIG. 25 is a schematic diagram of a boiler system;

[0114] FIG. 26 is a the temperature/time table of main pathogenic microorganisms carried by feces and urine of pigs and dead pigs; and

[0115] FIG. 27 is a report for analysis for a liquid organic fertilizer.

[0116] Numbering in FIG. 1: 201source separation pigsty; 202pigsty flushing water treatment system, 203feces collection pit; 204biogas generating pit; 205solid-liquid separation system; 206liquid high-temperature aerobic fermentation system; 207solid high-temperature aerobic fermentation system; 208boiler system; 209odor and flue gas treatment system; 210test and control system; 211cloud or remote server.

[0117] Numbering in FIG. 2 and FIG. 3: 101external drainage ditch; 102slatted floor; 103longitudinal beam; 104cross beam; 105V-shaped slope; 106feces cleaning ditch; 107driving device; 108feces scraper; 108Alimiting clip, 108Bscraper blade; 109feces scraping control system; 110driving rope; 111position sensor and mounting seat; 112sludge pump; 203feces collection pit;

[0118] Numbering in FIG. 4: 301pigsty flushing water pit; 302ABR; 303ASBR; 303BSBR; 303XSBR; 304ecological wetland; 305Aelectromagnetic valve; 305Belectromagnetic valve; 305Xelectromagnetic valve.

[0119] Numbering in FIG. 5: 701power supporting wheel group; 801feed side sealing cover; 808feed side sealing device; 809cage-shaped structure; 814horizontal drum; 815discharge side sealing device; 822discharge side sealing cover; 823integrated base;

[0120] Numbering in FIG. 6, FIG. 11 and FIG. 13: 801feed side sealing cover; 802material temperature sensor; 803feed side water jacket rotating joint; 804solid high-temperature aerobic fermentation reactor water outlet flange; 805feed side water jacket extraction pipe; 806solid high-temperature aerobic fermentation reactor exhaust hole; 807solid in high-temperature aerobic fermentation reactor feed hole; 808feed side sealing device; 809stirring and anti-sticking device; 810feed side rolling ring; 811water jacket; 812heat preservation layer: 813discharge side rolling ring; 814horizontal drum; 815discharge side sealing device; 816solid high-temperature aerobic fermentation reactor air inlet hole; 817discharge side water jacket extraction pipe; 818solid high-temperature aerobic fermentation reactor water inlet flange; 819discharge side water jacket rotating joint; 820discharge gate; 821solid high-temperature aerobic fermentation reactor discharge hole, 822discharge side sealing cover; 823integrated base; 824concrete foundation;

[0121] Numbering in FIG. 7: 903Asupporting wheel; 903Bsupporting wheel; 904Ashaft coupler; 904Bshaft coupler; 905Amotor; 905Bmotor; 906Aspeed reducer; 906Bspeed reducer;

[0122] Numbering in FIG. 8: 1001contact block; 903Csupporting wheel:

[0123] Numbering in FIG. 9: 1101parallel shoveling plate left side cage-shaped structure; 1102parallel shoveling plate middle side cage-shaped structure; 1103parallel, shoveling plate right side cage-shaped structure; 1104parallel shoveling plate middle side cage-shaped structure left supporting plate; 1105parallel shoveling plate middle side cage-shaped structure right supporting plate; 1106parallel shoveling plate

[0124] Numbering in FIG. 10: 1201inclined shoveling plate left side cage-shaped structure; 1202inclined shoveling plate middle side cage-shaped structure; 1203inclined shoveling plate right side cage-shaped structure; 1204inclined shoveling plate middle side cage-shaped structure left supporting plate; 1205inclined shoveling plate; 1206inclined shoveling plate middle side cage-shaped structure right supporting plate;

[0125] Numbering in FIG. 12: 1801sealing cover outer hood; 1802sealing cover inner hood A; 1803drum ring hood A; 1804drum lining ring;

[0126] Numbering in FIG. 14: 1805sealing cover inner hood B; 1806drum ring hood B

[0127] Numbering in FIG. 15: 1301stop wheel;

[0128] Numbering in FIG. 16: 1401top cover; 1402tankbody; 1403supporting vertical column; 1404top cover component: 1405lifting device; 1406escalator; 1407liquid drainage port; 1408liquid drainage valve;

[0129] Numbering in FIG. 17: 1501lifting ring; 1502top cover; 1503sealing door: 1504bracket; 1505heat exchange coil water outlet flange; 1506heat exchange coil water inlet flange; 1507safety valve; 1508feed flange; 1509exhaust flange; 1510air inlet flange; 1511heat exchange coil; 1512aeration device; 1513vertical frame; 1514connecting plate; 1515aeration head;

[0130] Numbering in FIG. 18: 1001hanging basket main body; 1602hanging basket door; 1603lock catch; 1604dead pig

[0131] Numbering in FIG. 19: Aodor heat exchange condenser; 402Ainduced draft fan; 403Abiological deodorization filtering tower; 405Aelectromagnetic valve; 405Belectromagnetic valve; 406Atemperature sensor;

[0132] Numbering in FIG. 20: Bodor heat exchange condenser; 402Binduced draft fan; 403Bbiological deodorization filtering tower; 404aeration fan; 405Celectromagnetic valve; 405Delectromagnetic valve; 406Btemperature sensor; 407three-way electric regulation valve;

[0133] Numbering in FIG. 21: Aodor heat exchange condenser; 402induced draft fan; 403Abiological deodorization filtering tower; 405Aelectromagnetic valve; 405Belectromagnetic valve; 406Atemperature sensor;

[0134] Numbering in FIG. 22: Codor heat exchange condenser; 602Binduced draft fan; 403Bbiological deionization filtering tower; 404aeration fan; 405Celectromagnetic valve; 405Delectromagnetic valve; 406B-temperature sensor

[0135] Numbering in FIG. 23: 601flue gas heat exchange condenser; 602induced draft fan; 403Bbiological deodorization filtering tower; Aodor heat exchange condenser; 402Ainduced draft fan; 403Abiological deodorization filtering tower 405Aelectromagnetic valve; 405Belectromagnetic valve; 406Atemperature sensor

[0136] Numbering in FIG. 24: 1701upper end cover; 1702upper pipe plate; 1703heat exchange pipe; 1704partition plate; 1705pull rod; 1706fresh air inlet flange; 1707lower end cover; 1708odor exhaust flange; 1709odor inlet flange; 1710hot air exhaust flange; 1711tank body; 1712lower pipe plate; 1713U-shaped pipe;

[0137] Numbering in FIG. 25: 206Aliquid high-temperature aerobic fermentation reactor, 206Bliquid high-temperature aerobic fermentation reactor; 206Nliquid high-temperature aerobic fermentation reactor; 207Asolid high-temperature aerobic fermentation reactor; 207Bsolid high-temperature aerobic fermentation reactor; 207Msolid high-temperature aerobic fermentation reactor; 501pressure water tank; 502boiler water inlet valve; 503boiler water inlet pipeline; 504water supplementing valve; 505water supplementing pipe; 506three-way electric regulation valve; 507Atemperature sensor; 507Btemperature sensor; 508boiler water return pipeline; 509exhaust valve; 510pressure gauge; 511boiler water outlet pipeline; 512boiler; 513circulation pump

DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS

[0138] A comprehensive treatment system disclosed by the present disclosure is shown in FIG. 1, and mainly includes a source separation pigsty 201, a pigsty flushing water treatment system 202, a solid-liquid separation system 205, a liquid high-temperature aerobic fermentation system 206, a solid high-temperature aerobic fermentation system 207, a boiler system 208, an odor and flue gas treatment system 209 and a test and control system 210. The source separation pigsty 201 separates feces and urine from rainwater, pigsty flushing water and residual drinking water the rainwater and the residual drinking water are discharged into an external drainage ditch 101. The feces and urine are conveyed to a feces collection pit 203 of the solid-liquid separation system 205. The pigsty flushing water are discharged into a pigsty flushing water pit 301 of the pigsty flushing water treatment system 202. The solid-liquid separation system 205 is composed of a sludge pump installed at the bottom of the feces collection pit, a solid-liquid separation device and conveying equipment. The sludge pump pumps the feces and urine to the solid-liquid separation device. Solids separated by the solid-liquid separation device are convened to a feed port of the solid high-temperature aerobic fermentation system 207, and liquid separated by the solid-liquid separation device is conveyed to a feed port of the liquid high-temperature aerobic fermentation system 206. The liquid drainage port of tire high-temperature aerobic fermentation system 206 is connected with the liquid inlet of the biotas generating pit 204 through the conveying equipment and a pipeline. Fermentation odor generated by the solid high-temperature aerobic fermentation system 207 and the liquid high-temperature aerobic fermentation system 206 and flue gas generated by the boiler system 208 are conveyed to the odor and flue gas treatment system 209. The boiler system 208 conveys hot water to a heat exchange jacket or coil of the solid high-temperature aerobic fermentation system 207 and a jacket or coil of the liquid high-temperature aerobic fermentation system 206 through hot water pipelines so as to provide heat, and under the driving of a circulating pump 513, the hot water returns into a boiler 512 through a water return pipeline to complete the cycle. The test and control system 210 arranges sensors into all the systems to detect respective key parameters and coordinately controls the above systems.

[0139] The pollutant source separation pigsty involved in the present disclosure is shown in FIG. 2 and FIG. 3, and includes rainwater and sewage separation and drinking water and sewage separation, and separation and collection of feces and urine from pigsty flushing water. The drinking water and sewage separation is mainly composed of an autodrinker for pigs, a U-shaped water collection cavity, a drainage pipeline and an external drainage ditch. The U-shaped water collection cavity is arranged under a water faucet of the autodrinker for pigs. The drainage port in the bottom of the U-shaped water collection cavity is connected with the drainage pipeline. The water outlet of the drainage pipeline is connected with the external drainage ditch. The separation and collection of the feces and urine of pigs from the pigsty flushing water is mainly composed of a pigsty slatted floor 102, V-shaped slopes 10, a feces cleaning ditch 106, a feces scraping system and a feces collection pit 203. The V-shaped slopes 105 and the feces cleaning ditch 106 are arranged below the pigsty slatted floor 102. The V-shaped slopes 105 are positioned on both sides of the feces cleaning ditch 106. A feces scraper 108 is arranged in the feces cleaning ditch 106. A feces scraping system involved in the present disclosure is shown in FIG. 1, and mainly includes a driving device 107, a driving rope 110, the feces scraper 108, sensors 111 and a feces scraping control system 109. A limiting clip 108 A and a scraper blade 108B are arranged on the feces scraper 108. The driving device 107 is connected with the feces scraper 108 through the driving rope 110. The sensors 111 are arranged at both ends of the feces cleaning ditch 106. The driving device 107 drives the feces scraper 108 through the driving rope 110 to move back and forth from the highest end to the lowest end along the bottom surface of the feces cleaning ditch 106. When the feces scraper 108 moves towards one side of the feces collection pit 203, the limiting clip 108A clamps the scraper blade 108B, and the scraper blade 108B drives the feces and urine to move forwards to finally collect the feces and urine into the feces collection pit 203. When the sensors 111 detect that the feces scraper 108 arrives at both ends of the feces cleaning ditch 106, the feces scraping control system 109 controls the feces scraping driving device 107 to stop the operation and then to operate oppositely after delay time. When the feces scraper 108 operates oppositely the restriction of the limiting clip 108A is released, and the scraper blade 108B is shoveled up by the driving rope 110, but the feces and urine may not move backwards.

[0140] The structural schematic diagram of the pigsty flushing water treatment system involved in the present disclosure is shown in FIG. 4, and is mainly composed of a pigsty flushing water pit 301, an ABR (anaerobic baffled reactor) 302, a plurality of SBRs (sequencing batch reactors) (303A, 303B and . . . 303X). an ecological wetland 304 and a plurality of electromagnetic valves (305A, 305B and . . . 305X). Large and small gratings are arranged on the outer side of the water inlet and the inner side of the water overflow port of the pigsty flushing water pit 301. The water outlet outer side of the water overflow port of the pigsty flushing water pit is connected with the water inlet of the ABR 302 through a water outlet pipeline. The water outlet of the ABR 302 is connected to the water inlets of the parallel-connected SBRs (303A, 303B and . . . 303X) respectively through pipelines. An electromagnetic valve (305A, 305B and . . . 305X) is installed on the water inlet pipeline of each SBR (303A, 303B and . . . 303X). and the water outlets of the SBRs (303A, 303B and . . . 303X) are connected with the water inlet of the ecological wetland 304. When the source separation pigsty 201 is flushed, the pigsty flushing water enters the pigsty flushing water pit 301 through the coarse grating and flows to the ABR 302 through the fine grating and the overflow pipe. The pigsty flushing water is subjected to sludge settling and anaerobic fermentation of the ABR 302, and then fermentation liquid enters the first SBR 303A. After the liquid level of the first SBR 303A reaches its designed liquid level, the test and control system 210 controls the electromagnetic valve 305A in front of the SBR 303A to turn off the electromagnetic valve 305A in front of the first SBR 303A and tarn on the electromagnetic valve 305B of the second SBR 303B, so as to allow the liquid levels of all the SBRs to reach the designed liquid levels. The test and control system 210 realizes an aerobic-anaerobic alternating technical process on all the SBRs (303A, 303B and . . . 303X) according to an SBR technique by controlling intermittent aeration. After the SBRs (303A, 303B and . . . 303X) complete a complete SBR treatment technique, supernatant is conveyed to the ecological wetland 304 through the conveying equipment and then discharged.

[0141] The structural schematic diagram, of the solid high-temperature aerobic fermentation reactor is shown in FIG. 5 and FIG. 6. The solid high-temperature aerobic fermentation reactor is composed of an inclined horizontal drum 814, a feed side sealing cover 801, a sealing device 808, a discharge side sealing cover 822, a sealing device 815, a power supporting wheel group 701, a stirring and anti-sticking device 809 and an integrated base 823. The feed side is higher than the discharge side. The horizontal drum 814, the feed side sealing cover 801, the discharge side searing cover 822 and the sealing devices (808 and 815) on both sides form a closed fermentation space. A feed hole 807 and an exhaust hole 806 are formed in the upper part of the feed side sealing cover 801. An air inlet hole 816 is formed in the upper part of the discharge side sealing cover 822. A discharge hose 821 is formed in the lower part of the discharge side sealing cover 822. A discharge gate 820 is installed on the discharge hole. A temperature sensor 802 is arranged at the lower part of the feed side sealing cover 801. A temperature probe of the temperature sensor 802 extends into the horizontal drum 814.

[0142] A water jacket 811 is welded outside the horizontal drum 814, and is divided into several parts by a feed side rolling ring 810 and a discharge side rolling ring 813 on the horizontal drum 814. The water jacket 811 is connected into a whole through a water jacket connection pipe. The water jacket 811 is connected with a solid high-temperature aerobic fermentation reactor water inlet flange 818 by a feed side water jacket extraction pipe 805 through a feed side water jacket rotating joint 803 arranged in the center of the feed side sealing cover 801. The water jacket 811 is connected with a solid high-temperature aerobic fermentation reactor water outlet flange 804 by a discharge side water jacket extraction pipe 817 through a discharge side water jacket rotating joint 819 arranged in the center of the discharge side sealing cover 822. The water inlet flange 818 and the water outlet flange 804 of the solid high-temperature aerobic fermentation reactor are connected with a water outlet pipeline 511 of the boiler system 208 to form a circulating loop. A heat preservation layer 812 is arranged outside the water jacket 811, so that radiation waste of heat energy may be reduced.

[0143] The stirring and anti-sticking device 809 is positioned in the horizontal drum 814. The horizontal drum 814 is arranged on the power supporting wheel group 701. The power supporting wheel group 701, the feed side sealing cover 801 and the discharge side sealing cover 822 are fixed to the inclined integrated base 823 to form a whole. The integrated base 823 is fixed to an inclined concrete foundation 824 through second pouring; the basic plane of the concrete foundation 824 and the gradient of a horizontal plane form an adjustable included angle of 0-5 degrees. The conveying speed of fermentation raw materials to the discharge end may be adjusted by adjusting the included angle.

[0144] The structural schematic diagram of the side surface and the structural schematic diagram of the cross section of the power supporting wheel group 701 are shown in FIG. 7 and FIG. 8. The power supporting wheel group 701 is composed of two groups of supporting wheels and power driving devices thereof and the like. Power driving adopts four-wheel driving. In FIG. 6 of the structural schematic diagram of the side surface, the structure of the first power driving device is that; a motor 905A, a speed reducer 906A and a shaft coupler 904A are connected with the supporting wheel 903A in sequence and are in connection transmission in sequence. The structure of the second power driving device is that: a motor 905B, a speed reducer 906B and a shaft coupler 904B are connected with the supporting wheel 903B in sequence and are in connection transmission in sequence. In this way, each supporting wheel is a driving wheel. The two groups of supporting wheels are in linear contact with the rolling ring 901 of the horizontal drum 814. The power supporting wheel group is controlled to coordinately drive the horizontal, drum 814 to rotate.

[0145] The structural schematic diagram of a contact block is shown in FIG. 8. A general shovel plate structure is not disposed on the inner wall of the horizontal drum 814. On the inner wall, a plurality of contact blocks 1001 are uniformly fixed relative to gap positions of cage-shaped structures 809 of the stirring and anti-sticking device. When the horizontal drum 814 rotates, the contact blocks 1001 on the inner wall drive a parallel shoveling plate left side cage-shaped structure 1101, a parallel shoveling plate middle side cage-shaped structure 1102 and a parallel shoveling plate right side cage-shaped structure 1103 to rotate at the same time. Because shoveling plates 1106 of the cage-shaped structures have certain widths, the three cage-shaped structures (1101, 1102 and 1103) drive materials at the bottom of the horizontal drum 814 to move upwards. Under the gravity action, the materials are separated from the shoveling plates and thrown away, and fall to the bottom of the horizontal drum 814, so as to achieve material throwing and stirring effects. Because the outer diameters of the parallel shoveling plate left, side cage-shaped structure 1101, the parallel shoveling plate middle side cage-shaped structure 1102 and the parallel shoveling plate right side cage-shaped structure 1103 are less than the inner diameter of the horizontal drum 814, gaps are also reserved between the contact blocks 1001 and the three cage-shaped structures (1101, 1102 and 1103). When the horizontal drum 814 rotates, the three cage-shaped structures (1101, 1102 and 1103) and the horizontal drum 814 generate relative movement. By virtue of collision and scratching between left supporting plates and right supporting plates of the three cage-shaped structures (1101, 1102 and 1103) as well as between the shoveling plates and the inner wall of the horizontal drum 814, the materials possibly adhered on the inner surface of a drum body of the horizontal drum 314 may be cleaned, so as to achieve an effect of preventing the materials in the horizontal drum 814 from being adhered on the inner wall of the horizontal drum 814.

[0146] The stirring and anti-sticking system 809 is composed of one or more than one cage-shaped structure. According to a state whether the axes of the cage-shaped structures are parallel to the shoveling plates, the cage-shaped structures are divided into parallel shoveling plate cage-shaped structures and inclined shoveling plate cage-shaped structures. The schematic diagram of the parallel shoveling plate cage-shaped structure is shown in FIG. 9. The stirring and anti-sticking system is composed of the parallel shoveling plate left side cage-shaped structure 1101, the parallel shoveling plate middle side cage-shaped structure 1102 and the parallel shoveling plate right side cage-shaped structure 1103. Each cage-shaped structure is composed of a left supporting plate, a right supporting plate and a plurality of shoveling plates. The left and the right supporting plates are circular rings and are coaxial. The plurality of shoveling plates are arranged between the supporting plates. As shown in FIG. 11, the parallel shoveling plate middle side cage-shaped structure 1102 is composed of a parallel shoveling plate middle side cage-shaped structure left supporting plate 1104, a parallel shoveling plate middle side cage-shaped structure right supporting plate 1105 and a plurality of shoveling plates 1106. The left supporting plate 1104 and the right supporting plate 1105 are coaxial, and a plurality of parallel shoveling plates 1106 are arranged between the left supporting plate 1104 and the right supporting plate 1105 The shoveling plates 1106 are parallel to the axis of the horizontal drum 814.

[0147] The schematic diagram of the inclined shoveling plate cage-shaped structure is shown in FIG. 10. The stirring and anti-sticking system 809 is composed of an inclined shoveling plate left side cage-shaped structure 1201, an inclined shoveling plate middle side cage-shaped structure 1202 and an inclined shoveling plate right side cage-shaped structure 1203. Each cage-shaped structure is composed of a left supporting plate, a right supporting plate and a plurality of inclined shoveling plates. The left and right supporting plates are circular rings and are coaxial. The plurality of inclined shoveling plates are disposed between the supporting plates. The inclined shoveling plates are inclined to their axes at certain angles. The inclined shoveling plate middle side cage-shaped structure 1202 is composed of a left supporting plate 1204, a right supporting plate 1205 and a plurality of inclined shoveling plates 1206. When the horizontal chum 902 rotates, the contact blocks 1001 on the inner wall drive the inclined shoveling plate left side cage-shaped structure 1201, the inclined shoveling plate middle side cage-shaped structure 1202 and the inclined shoveling plate right side cage-shaped structure 1203 to rotate at the same time. Because the shoveling plates 1206 of the cage-shaped structures have certain widths, the three cage-shaped structures (1201, 1202 and 1203) drive materials at the bottom of the horizontal drum 814 to move upwards. Under the gravity action, the materials are separated from the shoveling plates and thrown away, and fall to the bottom of the horizontal drum 814. When the materials are thrown away, the shoveling plates of the three cage-shaped structures (1201, 1202 and 1203) form certain angles to their axes, and a forward thrust is generated while the materials are thrown away to allow the materials to move from the feed side to the discharge side, so as to achieve material throwing, stirring and guiding effects.

[0148] The structural schematic diagram of the labyrinth sealing device involved in the present disclosure is shown in FIG. 11 and FIG. 12. The structure of the sealing device is sealed in a labyrinth manner. Sealing between the drum 814 and the teed side sealing cover 801 and sealing between the drum 814 and the discharge side sealing cover 822 are labyrinth sealing. The labyrinth sealing is realized on the inner sides of the two sealing covers (the feed side sealing cover 801 and the discharge side sealing cover 822). As shown in FIG. 10, an outer hood 1801 and an inner hood 1802 which are coaxial with each other are perpendicularly welded on the inner side of the discharge side sealing cover 822. Correspondingly, coaxial lining rings 1804 are welded in parts, positioned on both sides, of the drum 814. The perpendicular lining rings 1804 are welded with coaxial ring hoods 1803, each of which has an outer diameter less than the inner diameter of the drum 814. The inner diameter of the sealing cover outer hood 1801 is greater than the outer diameter of the drum 814. The inner diameter of the sealing cover inner hood 1802 is greater than the outer diameter of the ring hood 1803. The outer diameter of the sealing cover inner hood 1802 is less than the inner diameter of the drum 814. The depth of the sealing cover inner hood 1802 is equal to that of the ring hood 1803. The labyrinth sealing effect is guaranteed by gaps between the inner sides of the sealing covers (the feed side sealing cover 801 and the discharge side sealing cover 822) and the end surfaces of the drum 814. If the gaps between the inner sides of the sealing covers (the feed side sealing cover 801 and the discharge side sealing cover 822) and the end surfaces of the drum 814 are smaller, fewer materials are leaked, so that the positions of the end covers (the feed side sealing cover 801 and the discharge side sealing cover 822) on both sides are adjusted to allow the drum 814 to rotate flexibly, so as to achieve a sealing effect of least leakage.

[0149] Further, the number of labyrinths is increased to lengthen the labyrinths and reduce the leakage. As shown in FIG. 13 and FIG. 14, an outer hood 1801, an inner hood A1802 and an inner hood B1805 which are coaxial are perpendicularly welded on the inner side of the discharge side sealing cover 822. Correspondingly, coaxial lining rings 1804 are welded in pans, positioned on both sides, of the drum 814. The perpendicular lining rings 1804 are welded with a ring hood A1803 and a ring hood B1806 coaxial with each other and having an outer diameter less than the inner diameter of the drum 814. The inner diameter of the sealing cover outer hood 1801 is greater than the outer diameter of the drum 814. The inner diameter of the sealing cover inner hood A1802 is greater than the outer diameter of the ring hood A1803. The outer diameter of the sealing cover inner hood A1802 is less than the inner diameter of the drum 814. The inner diameter of the sealing cover inner hood B1805 is greater than the outer diameter of the ring hood B1803. The inner diameter of the ring hood A1802 is greater than the outer diameter of the sealing cover inner hood B1805. The depth of the sealing cover inner hood A1802 is equal to those of the sealing cover inner hood B1805, the ring cover A1803 and the ring cover B1806, that is, the four hoods have the consistent depths. The labyrinth sealing effect is guaranteed by gaps between the inner sides of the sealing covers (the feed side sealing cover 801 and the discharge side sealing cover 822) and the end surfaces of the drum 814. If the gaps between the inner sides of the sealing covers (the feed side sealing cover 801 and the discharge side sealing cover 822) and the end surfaces of the drum 814 are smaller, fewer materials are leaked, so that the positions of the end covers (the feed side sealing cover 801 and the discharge side sealing cover 822) on both sides ate adjusted to allow the drum 814 to rotate flexibly, so as to achieve a sealing effect of least leakage.

[0150] The structural schematic diagram of a stop wheel is shown in FIG. 15. The stop wheel 1301 is connected to the integrated base 823 in a bolting manner. A waist-shaped hole groove is formed in a stop wheel seat. The stop wheel 1301 is adjusted through the waist-shaped hole groove so that the stop wheel 1301 comes into contact with the side line of the discharge side rolling ring 813. The stop wheel 1301 keeps off an axial component force of the horizontal drum 814, so as to prevent the horizontal drum 814 from moving along the axis.

[0151] The liquid high-temperature aerobic fermentation reactor is of a vertical type structure. As shown in FIG. 16, each liquid high-temperature aerobic fermentation reactor 1407 mainly includes a tank body 1402, a supporting vertical column 1403, a top cover component 1404, a lifting device 1405, a hanging basket and the like. The structural diagram of the top cove component 1404 of the liquid high-temperature aerobic fermentation reactor is shown in FIG. 14. The fop cover component 1404 mainly includes a lifting ring 1501, a top cover 1502, a sealing door 1503, a heat exchange coil water outlet flange 1505, a heat exchange coil water inlet flange 1506, a safety valve 1507, a feed flange 1505, an exhaust flange 1509. an air inlet flange 1510, a heat exchange coil 1511 and an aeration device 1512. The lifting ring 1501 is fixed to the top cover 1502 and is used for lifting the top cover component 1404. The feed flange 1508, the water inlet flange 1506, the water outlet flange 1505, the aeration device 1512, the air inlet flange 1510 and the exhaust flange 1509 are fixed to the top cover 1502. The heat exchange coil 1511 is fixed to the lower side of the top cover 1502 through a connecting plate 1514 and a vertical frame 1513 and is immersed in the fermentation liquid. The top cover 1502 is supported by the supporting vertical column 1403 and fixed at the upper part of the liquid high-temperature aerobic fermentation reactor 1407 to form a closed space together with the tank body 1402. A liquid drainage port 1407 is formed in the bottom of the tank body 1402. The liquid drainage port 1407 is connected to the biomass generating pit 212 through a pipeline. A liquid drainage valve 1408 is arranged on a liquid drainage pipeline. The aeration device 1512 is connected to an external aeration fan through an air inlet pipeline. A plurality of aeration heads 1515 are uniformly arranged on an aeration pipeline.

[0152] The structure of the hanging basket is shown in FIG. 18. The hanging basket is a tool used for accommodating dead pigs 1604 and placentas, and is mainly composed of a hanging basket main body 1601, a hanging basket door 1602, a lock catch 1603 and the like.

[0153] The schematic diagram of the odor and flue gas system involved in the present disclosure is shown in FIG. 19 FIG. 20, FIG. 21, FIG. 22 and FIG. 23. The odor and flue gas treatment system mainly includes odor heat exchange condensers (A, B and C), induced draft fans (402A and 402B), biological deodorization filtering towers (403A and 403B), an aeration fan 404, an electromagnetic valve 405, a three-way electromagnetic valve 407, a flue gas heat exchange condenser 601 and an induced draft fan 602. The schematic diagram of the odor treatment system of the solid high-temperature aerobic fermentation system is shown in FIG. 19. The exhaust port of the solid high-temperature aerobic fermentation reactor 207 is connected with the heat exchange an inlet of the odor heat exchange condenser A. The heat exchange exhaust port of the odor heat exchange condenser A is connected with the input end of the induced draft fan 402A. The electromagnetic valve 405A and a bypass branch are arranged on the air inlet pipeline of the odor heat exchange condenses A. The bypass branch of the odor heat exchange condenser A is provided with the electromagnetic valve 405B. The output end of the induced draft foil 402A is connected with an air inlet of the biological deodorization filtering tower 403A, and a temperature sensor 406A is installed on a main-path air inlet pipeline of the biological deionization filtering towel 403A. A biological deodorization filler is arranged in the biological deodorization filtering tower 403A. Odor exhausted by the solid high-temperature aerobic fermentation reactor 307 is cooled by the odor heat exchange condenser A, then is absorbed and converted through the biological deodorization filtering tower 403A and is discharged after reaching the standard. The air inlet of the odor heat exchange condenser A is connected with the atmosphere, and the air output port is connected to the air inlet of the solid high-temperature aerobic fermentation reactor 207 through a pipeline. Cold air is heated by the odor heat exchange condenser A to provide fresh hot air for the solid high-temperature aerobic fermentation reactor 207.

[0154] The odor treatment system of the liquid high-temperature aerobic fermentation system and the flue gas treatment system of the boiler system are as shown in FIG. 20. The flue gas exhaust port of the hot water boiler 512 is connected with one air inlet input end of the three-way electric regulation valve 407, and the other air inlet input end of the three-way electric regulation valve 407 is connected with the atmosphere. The output end of the three-way electric legislation valve 407 is connected with the input end of an aeration fan 404. The output end of the aeration fan 404 is connected with the air inlet flange of the liquid high-temperature aerobic fermentation reactor 206. The exhaust flange of the liquid high-temperature aerobic fermentation reactor 206 is connected with a heat exchange an inlet of the odor heat exchange condenser B. A heat exchange exhaust port of the odor heat exchange condenser B is connected with the input end of the induced draft fan 402B. An electromagnetic valve 405C and a bypass branch are arranged on an air inlet pipeline of the odor heat exchange condenser B. The bypass branch of the odor heat exchange condenser B is provided with an electromagnetic valve 405D. The output end of the induced draft fan 402B is connected with an air inlet of the biological deodorization filtering tower 403B, and a temperature sensor 406B is installed on a main-path air inlet pipeline of the biological deodorization filtering tower 403B. A biological deodorization filler is arranged in the biological deodorization filtering tower 403B. The aeration fan 404 adjusts the opening of the three-way electric regulation valve 407 according to an oxygen demand of a material in the liquid high-temperature aerobic fermentation reactor 206 to aerate the liquid high-temperature aerobic fermentation reactor 206, so that the an input ends of a hearth of the hot water boiler 512 and the three-way electric regulation valve 407 are in negative pressure states all the time, and flue gas generated by the hot water boiler 512 and partial fresh air are mixed through the three-way electric regulation valve 407 and enter the liquid high-temperature aerobic fermentation reactor 206. Odor exhausted by the liquid high-temperature aerobic fermentation reactor 206 is cooled by the odor heat exchange condenser B, then is absorbed and converted through the biological deodorization filtering tower 403B and is discharged after reaching the standard. The air inlet of the odor heat exchange condenser B is connected with the atmosphere, and the air output port is connected to the air inlet of an air blower of the hot water boiler 512. Cold air is heated by the odor heat exchange condenser B to provide fresh hot air for the hot water boiler 512.

[0155] When the boiler is used for incinerating objects, such as garbage and dead pigs, which block the aeration heads easily, the odor and flue gas treatment system is shown in FIG. 21, FIG. 22 and FIG. 23. The schematic diagram of the odor treatment system of the solid high-temperature aerobic fermentation system is shown in FIG. 17-1. The exhaust port of the solid high-temperature aerobic fermentation reactor 207 is connected with the heat exchange air inlet of the odor heat exchange condenser A. The heat exchange exhaust port of the odor heat exchange condenser A is connected with the input end of the induced draft fan 402A. The electromagnetic valve 405A and a bypass branch are arranged on the air inlet pipeline of the odor heat exchange condenser A. The bypass branch of the odor heat exchange condenser A is provided with the electromagnetic valve 405B. The output end of the induced draft fan 402A is connected with an air inlet of the biological deodorization filtering tower 403A, and a temperature sensor 406A is installed on a main-path air inlet pipeline of the biological deodorization filtering tower 403A. A biological deodorization filler is arranged in the biological deodorization filtering rower 403A. Odor exhausted by the solid high-temperature aerobic fermentation reactor 207 is cooled by the odor heat exchange condenser A, then is absorbed and converted through the biological, deodorization filtering tower 403A and is discharged after reaching the standard. The air inlet of the odor heat exchange condenser A is connected with the atmosphere, and the air output port is connected to the air inlet of the solid high-temperature aerobic, fermentation reactor 207 through a pipeline. Cold air is heated by the odor heat exchange condenser A to provide fresh hot air for the solid high-temperature aerobic fermentation reactor 207.

[0156] The schematic diagram of the odor treatment system of the liquid high-temperature aerobic fermentation system is shown in FIG. 22. The exhaust flange of the liquid high-temperature aerobic fermentation reactor 206 is connected with a heat exchange air inlet of the odor heat exchange condenser C. A heat exchange exhaust port of the odor heat exchange condenser C is connected with the input end of the induced draft fair 402B. An electromagnetic valve 405C and a bypass branch are arranged on an air inlet pipeline of the odor heat exchange condenser C. The bypass branch of the odor heat exchange condenser C is provided with an electromagnetic valve 405D. The output end of the induced draft fan 402B is connected with an air inlet of the biological deodorization filtering tower 403B, and a temperature sensor 406B is installed on a main-path air inlet pipeline of the biological deodorization filtering tower 403B. A biological deodorization filler is arranged in the biological deodorization filtering tower 403B. Odor exhausted by the liquid high-temperature aerobic fermentation reactor 206 is cooled by the odor heat exchange condenser C, then is absorbed and converted through the biological deodorization filtering tower 403B and is discharged after reaching the standard. The air inlet of the odor heat exchange condenser C is connected with the atmosphere, and the air output port is connected to the air inlet of the aeration fan 404. The air outlet of the aeration fan 404 is connected with the air inlet of the liquid high-temperature aerobic fermentation reactor 206. Cold air is heated by the odor heat exchange condenser C and then blown into the liquid high-temperature aerobic fermentation reactor 206 through the aeration fan 404 to provide fresh hot air for the liquid high-temperature aerobic fermentation reactor 206.

[0157] The schematic diagram of the flue gas treatment system of the boiler system is shown in FIG. 23. The flue gas exhaust port of the boiler 512 is connected with the heat exchange air inlet of the flue gas heat exchange condenser 601. The heat exchange exhaust port of the flue gas heat exchange condenser 601 is connected with the input end of the induced draft fan 602. The output end of the induced draft fan 602 is connected with the air inlet of the biological deodorization filtering tower 403C. A biological deodorization filler is arranged in the biological deodorization filtering tower 403C. Flue gas exhausted by the hot water boiler 512 is cooled by the Hue gas heat exchange condenser 601, then is absorbed and converted through the biological deodorization filtering tower 403C and is discharged after reaching the standard. The air inlet of the flue gas heat exchange condenser 601 is connected with the atmosphere, and the air output port is connected to the air inlet of the air blower of the hot water boiler 512 through the pipeline. Cold air is heated by the flue gas heat exchange condenser 601 and then blown into the hearth of the hot water boiler 512 through the air blower of the hot water boiler 512 to provide fresh hot air for the hot water boiler 512.

[0158] The structure schematic diagram of the heat exchange condenser involved in the present disclosure is shown in FIG. 24, the heat exchange condenser includes an upper end cover 1701, a tank body 1711 and a lower end cover 1707 winch are connected and fixed in sequence. The upper end of the upper end cover 1701 has an odor inlet flange 1709. An odor collection pipeline is connected and fixed with the odor inlet flange 1709. The lower part of the side wall of the tank body 1711 is provided with a fresh air inlet flange 1706, and the upper part is provided with a hot air exhaust flange 1710. An upper pipe plate 1702 is installed at the upper part of the tank body 1711, and a lower pipe plate 1712 is installed at the lower part of the tank body 1711. A plurality of holes are uniformly formed in the upper pipe plate 1702 and the lower pipe plate 1712. A heat exchange pipe 1703 passes through the corresponding holes of the upper pipe plate 1702 and the lower pipe plate 1712 to connect the upper pipe plate 1702 with the lower pipe plate 1712. Both ends of the heat exchange pipe 1703 are respectively welded on the upper pipe plate 1702 and the lower pipe plate 1712, so that, a closed cavity is formed among the upper pipe plate 1702, the lower pipe plate 1712, the outer side of the heat exchange pipe 1703 and the outer wall of the tank body 1711 and is communicated with the outside through the fresh air inlet flange 1706 and the hot air exhaust flange 1710. A plurality of pull rods 1705 are uniformly fixed to the lower pipe plate. A plurality of partition plates 1704 are uniformly arranged in a space between the fresh air inlet flange 1706 and the hot air exhaust flange 1710 in the tank body. The partition plates 1704 are fixed to the pull rods 1705. An inner cavity of the heat exchange pipe is communicated with the upper end cover 1701 and the lower end cover 1707. A U-shaped pipe 1713 is arranged at the bottom of a lower cover plate 1707.

[0159] The schematic diagram of the boiler system is shown in FIG. 25. The liquid high-temperature aerobic fermentation system 206 includes a liquid high-temperature aerobic fermentation reactor 206A. a liquid high-temperature aerobic fermentation reactor 206B and a liquid high-temperature aerobic fermentation reactor 206N, that is, includes totally N liquid high-temperature aerobic fermentation reactors (N1). The solid high-temperature aerobic fermentation system 207 includes a solid high-temperature aerobic fermentation, reactor 207A, a solid high-temperature aerobic fermentation reactor 207B and a solid high-temperature aerobic fermentation reactor 207M, that is, includes totally M solid high-temperature aerobic fermentation reactors (M1). A water inlet pipeline 503 of the boiler 512 is connected with the water outlet of a pressure water tank 501. A water inlet valve 502 is arranged on the water inlet pipeline 503. The water inlet of the pressure water tank 501 is connected with a water supplementing pipe 505. A water supplementing valve 501 is arranged on the water supplementing pipe 505. A water outlet pipeline 511 of the boiler 512 is connected to the input end of a three-way electric regulation valve 506. The two output ends of the three-way electric regulation valve 506 are respectively connected with the water inlet flanges of the plurality of liquid high-temperature aerobic fermentation reactors (206A, 206B and . . . 206N) and the water inlets of the solid high-temperature aerobic fermentation reactors (207A, 207R and . . . 207N) through the water outlet pipeline 511. The water outlet flange of each liquid high-temperature aerobic reactor 206 and the water outlet of each solid high-temperature aerobic fermentation reactor 207 are connected with a water return pipeline 508 of the boiler 512. Electromagnetic valves 507 are arranged on the water outlet pipelines of each liquid high-temperature aerobic reactor 206 and each solid high-temperature aerobic fermentation reactor 207. A temperature sensor is installed on the water outlet pipeline 511 of the boiler 512. A temperature sensor 507B, a circulating pump 513, an exhaust valve 509 and a pressure gauge 510 are also arranged on the water return pipeline 508 of the boiler 512.

Implementation Mode I:

[0160] (1). The pigsty keeps off rainwater, and the rainwater is drained through the external drainage ditch 101 in time, thereby realizing rainwater and sewage separation. When pigs drink water, water leaking from the autodrinker for pigs and lips fall, into the U-shaped water collection cavity and then is drained into the external drainage ditch 101 through the water drainage pipeline in time, thereby realizing dunking water and sewage separation. Daily excrements (including feces and urine) of the pigs leak from the slatted floors 102 and fall onto the Y-shaped slope 105 or fall into the feces cleaning ditch 106. The feces and urine which fall onto the V-shaped slope 105 naturally slide into the feces cleaning ditch 106 under the gravity action. The feces scraping system is started regularly every day. The driving device 107 drives the feces scraper 108 through the driving rope 110 to move back and forth from the highest end to the lowest end along the bottom surface of the feces cleaning ditch 106. When the feces scraper 108 moves towards the feces collection pit 203, the limiting clip 108A clamps the scraper blade, and the scraper blade 108B drives the feces and urine to move forwards to finally collect the feces and urine into the feces collection pit 203. When the feces scraper 108 moves towards the other side of the feces collection pit 203, the restriction of the limiting clip 108A is released, and the scraper blade 108B is shoveled up by the driving rope 110, but the feces and urine may not move backwards. When the sensors 111 detect that the feces scraper 108 arrives at both ends of the feces cleaning ditch 106, the feces scraping control system 109 controls the feces scraping driving device 107 to stop the operation and then to operate oppositely after delay time. When there are pigs being slaughtered, the feces scraping system is started firstly to clean the feces and urine falling onto the Y-shaped slope 105 or falling into the feces cleaning ditch 106, and then the water is controlled to flush the pigsty. During pigsty flushing, the feces scraping system stops the operation, and the pigsty flushing water flows into the feces cleaning ditch 106 through the slatted floor 102 and finally flows into the pigsty flushing water pit 301.

[0161] (2) When the source separation pigsty 201 is flushed, the pigsty flushing water enters the pigsty flushing water pit 301 through the coarse grating and flows to the ABR 302 through the fine grating and the overflow pipe. The pigsty flushing water is subjected to sludge settling and anaerobic fermentation of the ABR 302, and then fermentation liquid enters the first SBR 303A. After the liquid level of the first SBR 303A reaches its designed liquid level, the test and control system 210 controls the electromagnetic valve 305A in front of the SBR 303 A to turn off the electromagnetic valve 305A in front of the first SBR 303A and turn on the electromagnetic valve 305B of the second SBR 303B, so as to allow the liquid levels of all the SBRs to reach the designed liquid levels respectively. The test and control system 210 realizes an aerobic-anaerobic alternating technical process on all SBRs (303A, 303B and 303X) according to an SBR technique by controlling intermittent aeration. After the SBRs (303A, 303B and . . . 303X) complete a complete SBR treatment technique, supernatant is conveyed to the ecological wetland 304 through the conveying equipment and then discharged. Filter residues produced by impurity removal through the gratings of the pigsty flushing water pit 301 and sludge produced by the ABR 302 and the SBRs 303 are conveyed into the solid high-temperature aerobic fermentation reactor 207 and are mixed with the feces for high-temperature aerobic fermentation treatment to prepare a solid organic fertilizer

[0162] (3). The feces and urine in a piglet pigsty are conveyed into the liquid high-temperature aerobic fermentation reactor 206 through the conveying equipment. A liquid part separated through the solid-liquid separation device 205 is conveyed into the liquid high-temperature aerobic fermentation reactor 206 through a conveying device, and a separated solid part is conveyed into the solid high-temperature aerobic fermentation reactor 207 through the conveying device.

[0163] (4) Auxiliary materials and high-temperature aerobic bacteria are conveyed into the solid high-temperature aerobic fermentation reactor 207 through conveying equipment. During feeding, the test and control system 210 starts all the power driving devices at the same time to allow all the power supporting wheel groups 701 to rotate at the same time to drive the horizontal drum 814 of the solid high-temperature aerobic fermentation reactor 207 to rotate forwards. By virtue of the action of the spiral stirring and anti-sticking device 809 in the solid high-temperature aerobic fermentation reactor 207, fermentation raw materials are conveyed to the discharge side, and organic wastes are shoveled up and fall down so as to be fully stirred and mixed with oxygen, thereby enlarging the contact area of the fermentation raw materials and the oxygen.

[0164] (5). The dead pigs and the placentas 1604 are put into the hanging basket through a forklift truck or other sets of transferring equipment. The lifting device 1405 lifts the hanging basket into the liquid high-temperature aerobic fermentation reactor 206 to immerse the whole hanging basket into the liquid, and at the same time, a proper amount of a composite microbial fermentation agent is inoculated into the liquid high-temperature aerobic fermentation reactor 206.

[0165] (6). The circulating pump 513 and the boiler 512 are started in sequence. Hot water enters the heat exchange coil of the liquid high-temperature aerobic fermentation reactor 206 and the jack of the solid high-temperature aerobic fermentation reactor 207 to respectively heat the materials in the liquid high-temperature aerobic fermentation reactor 206 and the solid high-temperature aerobic fermentation reactor 207. The boiler system 208 and the odor and flue gas treatment system 209 are started at the same time. Odor exhausted by the solid high-temperature aerobic fermentation reactor 207 is cooled by the odor heat exchange condenser A, then is conveyed to the biological deodorization. filtering tower 403A through the induced draft fan 402A for absorption and conversion and is discharged into the atmosphere through the exhaust port of the biological deodorization filtering tower 403A after reaching the standard. Hot air heated by the odor heat exchange condenser A is introduced into the solid high-temperature aerobic fermentation reactor 207 through the induced draft fan 402A to heat and supply oxygen to the material in the solid high-temperature aerobic fermentation reactor 207. The aeration fan 404 adjusts the opening of the three-way electric regulation valve 407 according to an oxygen demand of the material in the liquid high-temperature aerobic fermentation reactor 206 to aerate the liquid high-temperature aerobic fermentation reactor 206, so that the air input ends of the hearth of the boiler 512 and the three-way electric regulation valve 407 are in negative pressure states all the time, and flue gas generated by the boiler 512 and partial fresh air are mixed through the three-way electric regulation valve 407 and enter the liquid high-temperature aerobic fermentation reactor 206 tor aeration of the feces and urine liquid. Odor exhausted by the liquid high-temperature aerobic fermentation reactor 206 is cooled by the odor heat exchange condenser B, then is conveyed to the biological deodorization filtering tower 403B through the induced draft fan 402B for absorption and conversion and is discharged to the atmosphere through the exhaust port of the biological deodorization filtering tower 403B after reaching the standard. Hot air heated by the odor heat exchange condenser B is introduced into the hot water boiler 512 through the air blower of the hot water boiler 512 to provide fresh hot air for the hot water boiler 512. Condensed water produced by heat exchange between hot odor and cold air is drained into a natural ditch through the U-shaped pipes 1713 of the odor heat exchange condensers A and B.

[0166] (7) When detecting that the odor temperature detected by the temperature sensors (406A and 406B) installed on the main-path air inlet pipelines of the biological deodorization filtering towers (403A and 403B) is more than 40 C., the test and control system 210 turns on the electromagnetic valves (405A and 405C) on the air inlet pipelines of the odor heat exchange condensers (A and B) and turns off the electromagnetic valves (405B and 405D) of the bypass branches to allow the odor entering the deodorization filtering tower (403A and 403B) to be cooled by the odor heat exchange condensers (A and B). When detecting that the odor temperature defected by the temperature sensors ( 406A. and 406B) installed on the main-path air inlet pipelines of the biological deodorization filtering towers (403A and 403B) is less than 15 C. the test and control system 210 turns off the electromagnetic valves (405A and 405C) on the air inlet pipelines of the odor heat exchange condensers (A and B) and turns on the electromagnetic valves (405B and 405D) of the bypass branches to forbid the odor to enter the odor heat exchange condensers (A and B) for cooling, so that the biological deodorization filtering towers (403A and 403B) work in a temperature range between 15 C. and 40 C. so as to guarantee the deodorization effect and prevent dormancy or death of microorganisms in the biological deodorization filtering towers (403A and 403B).

[0167] (8) In an aerobic fermentation reaction process, the test and control system 210 controls the power driving device of the solid high-temperature aerobic fermentation reactor 207 to operate in a periodic intermittent operation manner of backward rotation-stop-backward rotation-stop . . . according to a detected temperature of the fermentation raw material or a set time. During rotating of the drum 814, under the driving of the contact blocks 1001, the shoveling plates of the stirring and anti-sticking device drive 809 drive the materials at the bottom of the horizontal drum 814 to move upwards along the inner wall of the drum 814, and the materials are separated from the shoveling plates and thrown away and fall back to the bottom of the horizontal drum 814 under the gravity action, so as to achieve stirring and air contact effects. By virtue of the action of the spiral shoveling plates in the solid high-temperature aerobic fermentation reactor 207, the backward rotating drum shovels up the materials and conveys the fermentation raw materials to the feed side, so that the fermentation materials may not compact the discharge side sealing cover 822. Because the cage-shaped structures of the stirring and anti-sticking device 809 collide with different contact blocks 1001 in the drum 814 and rotate under the driving of the contact blocks 1001, the cage-shaped structures and the inner wall of the drum 814 may slide relatively, so that the fermentation raw materials may not be adhered to the inner wall of the drum 814 of the solid high-temperature aerobic fermentation reactor 207, and the energy consumption caused by stirring and heat conduction is reduced to the minimum.

[0168] (9). The solid materials in the solid high-temperature aerobic fermentation reactor 207 are continuously fermented at more than 60 C. for more than 24 hours to complete the whole high-temperature aerobic fermentation process to prepare the solid organic fertilizer. The test and control system 210 controls to turn off the electromagnetic valves 507 at the front ends of the power supporting wheel group 701 of the solid high-temperature aerobic fermentation reactor 207 and the water inlet pipeline of the water jacket 811 and controls to bun on the discharge gate 820 at the same time. Then the test and control system 210 controls the power supporting wheel group 701 to continuously rotate forwards to discharge part of old fermented materials to the next working procedure for treatment through external conveying equipment.

[0169] (10). The material in the liquid high-temperature aerobic fermentation reactor 206 is continuously fermented at 60 C. or higher for more than 3 days to complete the whole high-temperature aerobic fermentation process. Hot fermentation liquid subjected to the high-temperature aerobic fermentation is immediately conveyed to the biogas generating pit 204 subjected to heat presentation treatment through a pipeline for high-temperature or medium-temperature anaerobic fermentation. The fermentation liquid is continuously anaerobically fermented at 35-60 C. for 15 to 20 days to complete the anaerobic fermentation process. After being diluted secondary fermentation liquid may be directly applied lot agriculture, and produced biogas may be applied to the boiler system 208 or power generation. Residues produced by the dead pigs 1604 are rotten, and hairs and bone residues are conveyed to the boiler 512 for incineration. Ash produced by incineration is conveyed to the solid high-temperature aerobic fermentation reactor 207 and is mixed with solid feces for fermentation, so as to prepare the solid organic fertilizer.

[0170] (11). The test and control system 210 is used for monitoring and acquiring key data of all aspects of the comprehensive treatment system and coordinately controlling all constituents of the comprehensive treatment system according to the acquired data:

[0171] {circumflex over (1)} in the high-temperature aerobic fermentation reaction process, the test and control system 210 automatically controls the opening of a circulating water three-way electric regulation valve 506 according to the temperatures of the materials in the high-temperature aerobic fermentation reactors (the liquid high-temperature aerobic fermentation reactor 206 and the solid high-temperature aerobic fermentation reactor 207), so that the temperatures of the fermentation materials are stabilized at a set temperature all the time when the temperature of the material in the high-temperature aerobic fermentation reactor (the liquid high-temperature aerobic fermentation reactor 206 or the solid high-temperature aerobic fermentation reactor 207) of a first fermentation object is less than the set value, the opening of the three-way electric regulation valve 506 in tins loop is 100%, and the openings in the loops of other high-temperature aerobic fermentation reactors (the liquid high-temperature aerobic fermentation reactor 207) or the solid high-temperature aerobic fermentation reactor 207) are 0; when the temperature of the material of the high-temperature aerobic fermentation reactor (the liquid high-temperature aerobic fermentation reactor 206 or the solid high-temperature aerobic fermentation reactor 207) of the first fermentation object is close to the set value, the test and control system 210 controls to turn on the electromagnetic valve in the loop of the second high-temperature aerobic fermentation reactor (the liquid high-temperature aerobic fermentation reactor 206 or the solid high-temperature aerobic fermentation reactor 207), and the three-way electric regulation valve 506 performs PID regulation to allow part of the hot circulating water to flow through the second high-temperature aerobic fermentation reactor, so that the second high-temperature aerobic fermentation reactor is heated under the condition of stabilizing the temperature of the material of the first high-temperature aerobic fermentation reactor at the set value, because the aerobic fermentation process is a heat release process, with the fermentation, the temperature of the material in the high-temperature aerobic fermentation reactor (the liquid high-temperature aerobic fermentation reactor 206 or the solid high-temperature aerobic fermentation reactor 207) continuously use up; when the temperature of the material in the high-temperature aerobic fermentation reactor of the first fermentation object is greater than the set value, the test and control system 210 slows down oi shuts off the heating of the boiler 512; under the action of the circulating pump 513, the circulating water is mixed with circulating water of the high-temperature aerobic fermentation reactors of the first fermentation object and the second fermentation object, resulting in that the temperature of the material in the high-temperature aerobic fermentation reactor of the first fermentation object is reduced, and the temperature of the material in the high-temperature aerobic fermentation reactor of the second fermentation object is increased; the three-way electric regulation valve 506 and the electromagnetic valve 507 are coordinately controlled by the test and control system 210 to convey fermentation reaction heat of the previous high-temperature aerobic fermentation reactor and heat generated by heating of the boiler to the second or Mth solid high-temperature aerobic fermentation reactor (207A, 207B and . . . 207M) or the Nth liquid high-temperature aerobic fermentation reactor (206A, 206B and . . . 206N), so that the temperatures of the materials in the high-temperature aerobic fermentation reactors (the liquid high-temperature aerobic fermentation reactor 206 or the solid high-temperature aerobic fermentation reactor 207) may be stabilized at the set value, and the heat energy generated by the fermentation reaction may be recycled; and

[0172] {circumflex over (2)} the test and control system 210 uploads the key data in a data region in the test and control system 210 to a cloud or remote server 211 for storage and backup through communication with a data gateway, so that all data of a treatment process evidence chain are stored for later inquiry, and service staff of a remote head office can find out faults and alarm of equipment operation by virtue of the data of the cloud and handle with the faults and alarm in time; and the data stored in the cloud are also favorable for completion and upgrading of the treatment system.

Implementation Mode II:

[0173] (1). The pigsty keeps off rainwater and the rainwater is drained through the external drainage ditch 101 in time, thereby realizing rainwater and sewage separation When pigs drink water, water leaking from the autodrinker for pigs and lips fall into the U-shaped water collection cavity and then is drained into the external drainage ditch 101 through the water drainage pipeline in time, thereby realizing drinking water and sewage separation Daily excrements (including feces and urine) of the pigs leak from the slatted floors 102 and fall onto the V-shaped slope 105 or fall into the feces cleaning ditch 106. The feces and urine which fall onto the V-shaped slope 105 naturally slide into the feces cleaning ditch 106 under the gravity action. The feces scraping system is started regularly every day. The driving device 107 drives the feces scraper 108 through the driving rope 110 to move back and forth from the highest end to the lowest end along the bottom surface of the feces cleaning ditch 106. When the feces scraper 108 moves towards the feces collection pit 203, the limiting clip 108A clamps the scraper blade, and the scraper blade 108B drives the feces and urine to move forwards to finally collect the feces and urine into the feces collection pit 203. When the feces scraper 108 moves towards the other side of the feces collection pit 203, the restriction of the limiting clip 108A is released, and the scraper blade 108B is shoveled up by the driving rope 110, but the feces and urine may not move backwards. When the sensors 111 detect that the feces scraper 108 arrives at both ends of the feces cleaning ditch 106, the feces scraping control system 109 controls the feces scraping driving device 107 to stop the operation and then to operate oppositely after delay time. When there are pigs being slaughtered, the feces scraping system is started firstly to clean the feces and urine falling onto the V-shaped slope 105 or falling into the feces cleaning ditch 106, and then the water is controlled to flush the pigsty. During pigsty flushing the feces scraping system stops the operation, and the pigsty flushing water flows into the feces cleaning ditch 106 through the slatted floor 102 and finally flows into the pigsty flushing water pit 301.

[0174] (2) When the source separation pigsty 201 is flushed, the pigsty flushing water enters the pigsty flushing water pit 301 through the coarse grating and flows to the ABR 302 through the fine grating and the overflow pipe. The pigsty flushing water is subjected to sludge settling and anaerobic fermentation of the ABR 302, and then fermentation liquid enters the first SBR 303A. After the liquid level of the first SBR 303A reaches its designed liquid level, the test and control system 210 controls the electromagnetic valve 305A in front of the SBR 303A to turn off the electromagnetic valve 305A in front of the first SBR 303A and turn on the electromagnetic valve 305B of the second SBR 303B, so as to allow the liquid levels of all the SBRs to reach the designed liquid levels respectively. The test and control system 210 realizes an aerobic-anaerobic alternating technical process on all SBRs (303A, 303B and . . . 303X) according to an SBR technique by controlling intermittent aeration. After the SBRs (303A, 303B and . . . 303X) complete a complete SBR treatment technique, supernatant is conveyed to the ecological wetland 304 through the conveying equipment and then discharged. Filter residues produced by impurity removal through the gratings of the pigsty flushing water pit 301 and sludge produced by the ABR 302 and the SBRs 303 are conveyed into the solid high-temperature aerobic fermentation reactor 207 and are mixed with the feces for high-temperature aerobic fermentation treatment to prepare a solid organic fertilizer.

[0175] (3). The feces and urine in a piglet pigsty are conveyed into the liquid high-temperature aerobic fermentation reactor 206 through the conveying equipment. A liquid part separated through the solid-liquid separation device 205 is conveyed into the liquid high-temperature aerobic fermentation reactor 200 through a conveying device, and a separated solid part is conveyed into the solid high-temperature aerobic fermentation reactor 207 through the conveying device.

[0176] (4) Auxiliary materials and high-temperature aerobic bacteria are conveyed into the solid high-temperature aerobic fermentation reactor 207 through conveying equipment. During feeding, the test and control system 210 starts all the power driving devices at the same time to allow all the power supposing wheel groups 701 to rotate at the same time to drive the horizontal drum 814 of the solid high-temperature aerobic fermentation reactor 207 to rotate forwards. By virtue of the action of the spiral stirring and anti-sticking device 809 in the solid high-temperature aerobic fermentation reactor 207, fermentation raw materials are conveyed to the discharge side, and organic wastes are shoveled up and fall down so as to be fully stirred and mixed with oxygen, thereby enlarging the contact area of the fermentation raw materials and the oxygen.

[0177] (5). The dead pigs 1604 are conveyed into the combustion hearth of the boiler 512 through a forklift truck or other sets of transferring equipment. At the same time, a proper amount of a composite microbial fermentation agent is inoculated into the liquid high-temperature aerobic fermentation reactor 206.

[0178] (6). The circulating pump 513 and the boiler 512 are started in sequence. Hot water enters the heat exchange coil of the liquid high-temperature aerobic fermentation reactor 206 and the jack of the solid high-temperature aerobic fermentation reactor 207 to respectively heat the materials in the liquid high-temperature aerobic fermentation reactor 206 and the solid high-temperature aerobic fermentation reactor 207. The boiler system 208 and the odor and flue gas treatment system 209 are started at the same time. Odor exhausted by the solid high-temperature aerobic fermentation reactor 207 is cooled by the odor heat exchange condenser A, then is conveyed to the biological deodorization filtering tower 403A through the induced draft fan 402A for absorption and conversion and is discharged into the atmosphere through the exhaust port of the biological deodorization filtering tower 403A after reaching the standard. Hot air heated by the odor heat exchange condenser A is introduced into the solid high-temperature aerobic fermentation reactor 207 through the induced draft fan 402A to heat and supply oxygen to the material in the solid high-temperature aerobic fermentation reactor 207. Odor exhausted by the liquid high-temperature aerobic fermentation reactor 206 is cooled by the odor heat exchange condenser C, then is conveyed to the biological deodorization filtering tower 403B through the induced draft fan 402B for absorption and conversion and is discharged to the atmosphere through the exhaust port of the biological deodorization filtering tower 403B after reaching the standard. Hot air heated by the odor heat exchange condenser C is blown and pressurized by the aeration fan 404 and conveyed into the liquid high-temperature aerobic fermentation reactor 206. The feces and urine liquid is heated and aerated. Flue gas generated by the hot water boiler 512 is subjected to heat exchange and is cooled by the flue gas heat exchange condenser 601, is introduced into the biological deodorization filtering tower 403C through the induced draft fan 602 for absorption and conversion and is discharged to the atmosphere through the exhaust port of the biological deodorization filtering tower 403C after reaching the standard. Hot air heated by the flue gas heat exchange condenser 601 is blasted into the hearth of the hot water boiler 512 through the an blower of the hot water boiler 512 to provide fresh not air for the combustion of the hot water boiler 512. Condensed water produced by heat exchange between the odor heat exchange condensers A and C and the flue gas heat exchange condenser 601 is drained into a natural ditch through the U-shaped pipes 1713 of the odor heat exchange condensers A and C and the flue gas heat exchange condenser 601.

[0179] (7) When detecting that the odor temperature detected by the temperature sensors (406A and 406B) installed on the main-path air inlet pipelines of the biological deodorization filtering towers (403A and 403B) is more than 40 C., the test and control system 210 turns on the electromagnetic valves (405A and 405C) on the air inlet pipelines of the odor heat exchange condensers and turns off the electromagnetic valves (405B and 405D) of the bypass branches to allow the odor entering the deodorization filtering tower (403A and 403B) to be cooled by the odor heat exchange condensers (A, B and C). When detecting that the odor temperature detected by the temperature sensors (406A and 406B) installed on the main-path air inlet pipelines of the biological deodorization filtering towers (403A and 403B) is less than 15 C., the test and control system 210 turns off the electromagnetic valves (405A and 405C) on the air inlet pipelines of the odor heat exchange condensers (A, B and C) and turns on the electromagnetic valves (405B and 405D) of the bypass branches to forbid the odor to enter the odor heat exchange condensers (A, B and C) for cooling, so that the biological deodorization filtering towers (403A and 403B) work in a temperature range between 15 C. and 40 C., so as to guarantee the deodorization effect and prevent dormancy or death of microorganisms in the biological deodorization filtering towers (403A and 403B).

[0180] (8) In an aerobic fermentation reaction process, the test and control system 210 controls the power driving device of the solid high-temperature aerobic fermentation reactor 207 to operate in a periodic intermittent operation manner of backward rotation-stop-backward rotation-stop . . . according to a detected temperature of the fermentation raw material or a set time. During rotating of the drum 814, under the driving of the contact blocks 1001, the shoveling plates of the stirring and anti-sticking device drive 809 drive the materials at the bottom of the horizontal drum 814 to move upwards along the inner wall of the drum 814. and the materials are separated from the shoveling plates and thrown away and fall back to the bottom of the horizontal drum 814 under the gravity action, so as to achieve stirring and air contact effects. By virtue of the action of the spiral, shoveling plates in the solid high-temperature aerobic fermentation reactor 207, the backward rotating drum shovels up the materials and conveys the fermentation raw materials to the feed side, so that the fermentation materials may not compact the discharge side sealing cover 822. Because the cage-shaped structures of the stilling and anti-sticking device 809 collide with different contact blocks 1001 in the drum 814 and rotate under the driving of the contact blocks 1001, the cage-shaped structures and the inner wall of the drum 814 may slide relatively, so that the fermentation raw materials may not be adhered to the inner wall of the drum 814 of the solid high-temperature aerobic fermentation reactor 207, and the energy consumption caused by stirring and heat conduction is reduced to the minimum.

[0181] (9). The solid materials in the solid high-temperature aerobic fermentation reactor 207 are continuously fermented at more than 60 C. for more than 24 hours to complete the whole high-temperature aerobic fermentation process to prepare the solid organic fertilizer The test and control system 210 controls to turn off the electromagnetic valves 507 at the front ends of the power supporting wheel group 701 of the solid high-temperature aerobic fermentation reactor 207 and the water inlet pipeline of the water jacket 811 and controls to turn on the discharge gate 820 at the same time. Then the test and control system 210 controls the power supporting wheel group 701 to continuously rotate forwards to discharge part of old fermented materials to the next working procedure for treatment through external conveying equipment.

[0182] (10). The material in the liquid high-temperature aerobic fermentation reactor 206 is continuously fermented at 60 C. or higher tor more than 3 days to complete the whole high-temperature aerobic fermentation process. Hot fermentation liquid subjected to the high-temperature aerobic fermentation is immediately conveyed to the biogas generating pit 204 subjected to heat preservation treatment through a pipeline for high-temperature or medium-temperature anaerobic fermentation. The fermentation liquid is continuously anaerobically fermented at 35-60 C. for 15 to 20 days to complete the anaerobic fermentation process. After being diluted, secondary fermentation liquid may be directly applied for agriculture, and produced biogas may be applied to the boiler system 208 or power generation.

[0183] (11). The test and control system 210 is used for monitoring and acquiring key data of all aspects of the comprehensive treatment system and coordinately controlling all constituents of the comprehensive treatment system according to the acquired data:

[0184] {circumflex over (1)} in the high-temperature aerobic fermentation reaction process, the test and control system 210 automatically controls the opening of a circulating water three-way electric regulation valve 506 according to the temperatures of the materials in the high-temperature aerobic fermentation reactors (the liquid high-temperature aerobic fermentation reactor 206 and the solid high-temperature aerobic fermentation reactor 207), so that the temperatures of the fermentation materials are stabilized at a set temperature all the time: when the temperature of the material in the high-temperature aerobic fermentation reactor (the liquid high-temperature aerobic fermentation reactor 200 or the solid high-temperature aerobic fermentation reactor 207) of a first fermentation object is less than the set value, the opening of the three-way electric regulation valve 506 in this loop is 100%, and the openings in the loops of other high-temperature aerobic fermentation reactors (the liquid high-temperature aerobic fermentation reactor 206 or the solid high-temperature aerobic fermentation reactor 207) are 0; when the temperature of the material of the high-temperature aerobic fermentation reactor (the liquid high-temperature aerobic fermentation reactor 206 or the solid high-temperature aerobic fermentation reactor 207) of the first fermentation object is close to the set value, the test and control system 210 controls to turn on the electromagnetic valve in the loop of the second high-temperature aerobic fermentation reactor (the liquid high-temperature aerobic fermentation reactor 206 or the solid high-temperature aerobic fermentation reactor 207), and the three-way electric regulation valve 506 performs PID regulation to allow part of the hot circulating water to flow through the second high-temperature aerobic fermentation reactor, so that the second high-temperature aerobic fermentation reactor is heated under the condition of stabilizing the temperature of the material of the first high-temperature aerobic fermentation reactor at the set value; because the aerobic fermentation process is a heat release process, with the fermentation, the temperature of the material in the high-temperature aerobic fermentation reactor (the liquid high-temperature aerobic fermentation reactor 206 or the solid high-temperature aerobic fermentation reactor 207) continuously rise up- when the temperature of the material in the high-temperature aerobic fermentation reactor of the first fermentation object is greater than the set value, the test and control system 210 slows down or shuts off the heating of the boiler 512; under the action of the circulating pump 51 the circulating water is mixed with circulating water of the high-temperature aerobic fermentation reactor s of the first fermentation object and the second fermentation object, resulting in that the temperature of the material in the high-temperature aerobic fermentation reactor of the first fermentation object is reduced, and the temperature of the material in the high-temperature aerobic fermentation reactor of the second fermentation object is increased; the three-way electric regulation valve 506 and the electromagnetic valve 507 are coordinately controlled by the test and control system 210 to convey fermentation reaction heat of the previous high-temperature aerobic fermentation reactor and heat generated by heating of the boiler to the second or Mth solid high-temperature aerobic fermentation reactor (207A, 207B and . . . 207M) or file Nth liquid high-temperature aerobic fermentation reactor (206A, 206B and . . . 206N), so that the temperatures of the materials in the high-temperature aerobic fermentation reactors (the liquid high-temperature aerobic fermentation reactor 206 or the solid high-temperature aerobic fermentation reactor 207) may be stabilized at the set value, and the heat energy generated by the fermentation reaction may be recycled; and

[0185] {circumflex over (2)} the test and control system 210 uploads the key data in a data region in the test and control system 210 to a cloud or remote server 211 for storage and backup through communication with a data gateway, so that all data of a treatment process evidence chain are stored for later inquiry, and service staff of a remote head office can find out faults and alarm of equipment operation by virtue of the data of the cloud and handle with the faults and alarm in time and the data stored in the cloud are also favorable for completion and upgrading of the treatment system

Implementation Mode III:

[0186] (1). The pigsty keeps off rainwater, and the rainwater is drained through the external drainage ditch 101 in time, thereby realizing rainwater and sewage separation. When pigs drink water, water leaking from the autodrinker for pigs and lips fall into the U-shaped water collection cavity and then is drained into the external drainage ditch 101 through the water drainage pipeline in time, thereby realizing drinking water and sewage separation. Daily excrements (including feces and urine) of the pigs leak from the slatted floors 102 and fall onto the Y-shaped slope 105 or fall into the feces cleaning ditch 106. The feces and urine which fall onto the V-shaped slope 108 naturally slide into the feces cleaning ditch 106 under the gravity action. The feces scraping system is started regularly every day. The driving device 107 drives the feces scraper 108 through the driving rope 110 to move back and forth from the highest end to the lowest end along the bottom surface of the feces cleaning ditch 106. When the feces scraper 108 moves towards the feces collection pit 203, the limiting clip 108A clamps the scraper blade, and the scraper blade 108B drives the feces and urine to move forwards to finally collect the feces and urine into the feces collection pit 203. When the feces scraper 108 moves towards the other side of the feces collection pit 203, the restriction of the limiting clip 108A is released, and the scraper blade 108B is shoveled up by the driving rope 110, but the feces and urine may not move backwards. When the sensors 111 detect that the feces scraper 108 arrives at both ends of the feces cleaning ditch 106, the feces scraping control system 109 controls the feces scraping driving device 107 to stop the operation and then to operate oppositely after delay time. When there are pigs being slaughtered, the feces scraping control system 109 is started firstly to clean the feces and urine falling onto the V-shaped slope 105 or falling into the feces cleaning ditch 106, and then the water is controlled to flush the pigsty. During pigsty flushing, the feces scraping control system 109 stops the operation, and the pigsty flushing water flows into the feces cleaning ditch 106 through the slatted floor 102 and finally flows into the pigsty flushing water pit 301.

[0187] (2) When the source separation pigsty 201 is flushed, the pigsty flushing water enters the pigsty flushing water pit 301 through the coarse grating and flows to the ABR 302 through the fine grating and the overflow pipe. The pigsty flushing water is subjected to sludge settling and anaerobic fermentation of the ABR 302, and then fermentation liquid enters the first SBR 303A. After the liquid level of the first SBR 303A reaches its designed liquid level, the test and control system 210 controls the electromagnetic valve 305 A in front of the SBR 303A to turn off the electromagnetic valve 305A in front of the first SBR 303A and turn on the electromagnetic valve 305B of the second SBR 303B, so as to allow the liquid levels of all the SBRs to reach the designed liquid levels respectively. The test and control system 210 realizes an aerobic-anaerobic alternating technical process on all SBRs (303A, 303B and . . . 303X) according to an SBR technique by controlling intermittent aeration. After the SBRs (303A, 303B and . . . 303X) complete a complete SBR treatment technique, supernatant is conveyed to the ecological wetland 304 through the conveying equipment and then discharged. Filter residues produced by impurity removal through the gratings of the pigsty flushing water pit 301 and sludge produced by the ABR 302 and the SBRs 303 are conveyed into the solid high-temperature aerobic fermentation reactor 207 and are mixed with the feces for high-temperature aerobic fermentation treatment to prepare a solid organic fertilizer.

[0188] (3). The feces and urine in a piglet pigsty are conveyed into the liquid high-temperature aerobic fermentation reactor 206 through the sludge pump 112 and a connection pipeline thereof. A liquid part separated through the solid-liquid separation device 205 is conveyed into the liquid high-temperature aerobic fermentation reactor 206 through a conveying device, and a separated solid part is conveyed into the solid high-temperature aerobic fermentation reactor 207 through the conveying device.

[0189] (4) Auxiliary materials and high-temperature aerobic bacteria are conveyed into the solid high-temperature aerobic fermentation reactor 207 through conveying equipment. During feeding, the test and control system 210 starts all the power driving devices at the same tune to allow all the power supporting wheel groups 701 to rotate at the same time to drive the horizontal drum 814 of the solid high-temperature aerobic fermentation reactor 207 to rotate forwards. By virtue of the action of the spiral stirring and anti-sticking device 809 in the solid high-temperature aerobic fermentation reactor 207, fermentation raw materials are conveyed to the discharge side, and organic wastes are shoveled up and fall down so as to be fully stirred and mixed with oxygen, whereby enlarging the contact area of the fermentation raw materials and the oxygen.

[0190] (5). The dead pigs 1604 are conveyed into the combustion hearth of the boiler 512 through a forklift truck or other sets of transferring equipment. At the same time, a proper amount of a composite microbial fermentation agent is inoculated into the liquid high-temperature aerobic fermentation reactor 206.

[0191] (6). The circulating pump 513 and the boiler 512 are started in sequence Hot water enters the heat exchange coil of the liquid high-temperature aerobic fermentation reactor 206 and the jack of the solid high-temperature aerobic fermentation reactor 207 to respectively heat the materials in the liquid high-temperature aerobic fermentation reactor 206 and the solid high-temperature aerobic fermentation reactor 207. The boiler system 208 and the odor and flue gas treatment system 209 are started at the same time. Odor exhausted by the solid high-temperature aerobic fermentation reactor 207 is cooled by the odor heat exchange condenser A, then is conveyed to the biological deodorization filtering tower 403A through the induced draft fan 402A for absorption and conversion and is discharged into the atmosphere through the exhaust port of the biological deodorization filtering tower 403A after reaching the standard. Hot air heated by the odor heat exchange condenser A is introduced into the solid high-temperature aerobic fermentation reactor 207 through the induced draft fan 402A to heat and supply oxygen to the material in the solid high-temperature aerobic fermentation reactor 207. Odor exhausted by the liquid high-temperature aerobic fermentation reactor 206 is cooled by the odor heat exchange condenser C, then is conveyed to the biological deodorization filtering tower 403B through the induced draft fan 402B for absorption and conversion and is discharged to the atmosphere through the exhaust port of the biological deodorization filtering tower 403B after reaching the standard. Hot air heated by the odor heat exchange condenser C is blown and pressurized by the aeration fan 404 and conveyed into the liquid high-temperature aerobic fermentation reactor 206. The feces and urine liquid is heated and aerated. Flue gas generated b the hot water boiler 512 is subjected to heat exchange and is cooled by the flue gas heat exchange condenser 601, is introduced into the biological deodorization filtering tower 403C through the induced, draft fan 602 for absorption and conversion and is discharged to the atmosphere through the exhaust port of the biological deodorization filtering tower 403C after reaching the standard. Hot air heated by the flue gas heat exchange condenser 601 is blasted into the hearth of the hot water boiler 512 through the air blower of the hot water boiler 512 to provide fresh hot air for the combustion of the hot water boiler 512. Condensed water produced by heat exchange between the odor hear exchange condensers A and C and the flue gas heat exchange condenser 601 is drained into a natural ditch through the U-shaped pipes 1713 of the odor heat exchange condensers A and C and the flue gas heat exchange condenser 601.

[0192] (7) When detecting that the odor temperature detected by the temperature sensors (406A and 406B) installed on the main-path air inlet pipelines of the biological deodorization filtering towers (403A and 403B) is more than 40 C., the test and control system 210 turns on the electromagnetic valves (405A and 405C) on the air inlet pipelines of the odor heat exchange condensers and turns off the electromagnetic valves (405B and 405D) of the bypass branches to allow the odor entering the deodorization filtering tower (403A and 403B) to be cooled by the odor heat exchange condensers A and C. When detecting that the odor temperature detected by the temperature sensors (406A and 406B) installed on the main-path air inlet pipelines of the biological deodorization filtering towers (403A and 403B) is less than 15 C. the test and control system 210 turns off the electromagnetic valves (405A and 405C) on the air inlet pipelines of the odor heat exchange condensers A and C and turns on the electromagnetic valves (405B and 405D) of the bypass branches to forbid the odor to enter the odor heat exchange condensers A and C for cooling, so that the biological deodorization filtering towers (403A and 403B) work in a temperature range between 15 C. and 40 C., so as to guarantee the deodorization effect and prevent dormancy or death of microorganisms in the biological deodorization filtering towers (403A and 403B).

[0193] (8) In an aerobic fermentation reaction process, the test and control system 210 controls the power driving device of the solid high-temperature aerobic fermentation reactor 207 to operate in a periodic intermittent operation manner of backward rotation-stop-backward rotation-stop . . . according to a detected temperature of the fermentation raw material or a set time. During rotating of the drum 814, under the driving of the contact blocks 1001, the shoveling plates of the stirring and anti-sticking device drive 809 drive the materials at the bottom of the horizontal drum 814 to move upwards along the inner wall of the drum 814, and the materials are separated from the shoveling plates and thrown away and fall back to the bottom of the horizontal drum 814 under the gravity action, so as to achieve stirring and air contact effects. By virtue of the action of the spiral shoveling plates in the solid high-temperature aerobic fermentation reactor 207, the backward rotating drum shovels up the materials and conveys the fermentation raw materials to the feed side, so that the fermentation materials may not compact the discharge side sealing cover 822. Because the cage-shaped structures of the stirring and anti-sticking device 809 collide with different contact blocks 1001 in the drum 814 and rotate under the driving of the contact blocks 1001, the cage-shaped structures and the inner wall of the drum 814 may slide relatively, so that the fermentation raw materials may not be adhered to the inner wall of the drum 814 of the solid high-temperature aerobic fermentation reactor 207, and the energy consumption caused by stirring and heat conduction is reduced to the minimum.

[0194] (9). The solid materials in the solid high-temperature aerobic fermentation reactor 207 are continuously fermented at more than 60 C. for more than 24 hours to complete the whole high-temperature aerobic fermentation process to prepare the solid organic fertilizer. The test and control system 210 controls to turn off the electromagnetic valves 507 at the front ends of the power supporting wheel group 701 of the solid high-temperature aerobic fermentation reactor 207 and the water inlet pipeline of the water jacket 811 and controls to turn on the discharge gate 820 at the same time. Then the test and control system 210 controls the power supporting wheel group 701 to continuously rotate forwards to discharge part of old fermented materials to the next working procedure for treatment through external conveying equipment.

[0195] (10). The material in the liquid high-temperature aerobic fermentation reactor 206 is continuously fermented at 60 C. or higher for more than 3 days to complete the whole high-temperature aerobic fermentation process. After being diluted, the fermentation liquid may be directly applied for agriculture.

[0196] (11). The test and control system 210 is used for monitoring and acquiring key data of all aspects of the comprehensive treatment system and coordinately controlling all constituents of the comprehensive treatment system according to the acquired data:

[0197] {circumflex over (1)} in the high-temperature aerobic fermentation reaction process, the test and control system 210 automatically controls the opening of a circulating water three-way electric regulation valve 506 according to the temperatures of the materials in the high-temperature aerobic fermentation reactors (the liquid high-temperature aerobic fermentation reactor 206 and the solid high-temperature aerobic fermentation reactor 207), so that the temperatures of the fermentation materials are stabilized at a set temperature all the time: when the temperature of the material in the high-temperature aerobic fermentation reactor (the liquid high-temperature aerobic fermentation reactor 206 or the solid high-temperature aerobic fermentation reactor 207) of a first fermentation object is less than the set value, the opening of the three-way electric regulation valve 506 in this loop is 100% and the openings in the loops of other high-temperature aerobic fermentation reactors (the liquid high-temperature aerobic fermentation reactor 206 or the solid high-temperature aerobic fermentation reactor 207) are 0; when the temperature of the material of the high-temperature aerobic fermentation reactor (the liquid high-temperature aerobic fermentation reactor 200 or the solid high-temperature aerobic fermentation reactor 207) of the first fermentation object is close to the set value, the test and control system 210 controls to turn on the electromagnetic valve in the loop of the second high-temperature aerobic fermentation reactor (the liquid high-temperature aerobic fermentation reactor 206 or the solid high-temperature aerobic fermentation reactor 207), and the three-way electric regulation valve 506 performs PID regulation to allow part of the hot circulating water to flow through the second high-temperature aerobic fermentation reactor, so that the second high-temperature aerobic fermentation reactor is heated under the condition of stabilizing the temperature of the material of the first high-temperature aerobic fermentation reactor at the set value; because the aerobic fermentation process is a heat release process, with the fermentation, the temperature of the material in the high-temperature aerobic fermentation reactor (the liquid high-temperature aerobic fermentation reactor 206 or the solid high-temperature aerobic fermentation reactor 207) continuously rise up; when the temperature of the material in the high-temperature aerobic fermentation reactor of the first fermentation object is greater than the set value, the test and control system 210 slows down or shuts off the heating of the boiler 512, under the action of the circulating pump 513, the circulating water is mixed with circulating water of the high-temperature aerobic fermentation reactors of the first fermentation object and the second fermentation object, resulting in that the temperature of the material in the high-temperature aerobic fermentation reactor of the first fermentation object is reduced, and the temperature of the material in the high-temperature aerobic fermentation reactor of the second fermentation object is increased; the three-way electric regulation valve 506 and the electromagnetic valve 507 are coordinately controlled by the test and control system 210 to convey fermentation reaction heat of the previous high-temperature aerobic fermentation reactor and heat generated by heating of the boiler to the second or Mth solid high-temperature aerobic fermentation reactor (207A, 207B and . . . 207M) or the Nth liquid high-temperature aerobic fermentation reactor (206A, 206B and . . . 206N), so that the temperatures of the materials in the high-temperature aerobic fermentation reactors (the liquid high-temperature aerobic fermentation reactor 206 or the solid high-temperature aerobic fermentation reactor 207) may be stabilized at the set value, and the heat energy generated by the fermentation reaction may be recycled; and

[0198] {circumflex over (2)} the test and control system 210 uploads the key data in a data region in the test and control system 210 to a cloud or remote server 211 for storage and backup through communication with a data gateway, so that all data of a treatment process evidence chain are stored for later inquiry, and service staff of a remote head office can find out faults and alarm of equipment operation by virtue of the data of the cloud 211 and handle with the faults and alarm in time; and the data stored in the cloud 211 are also favorable for completion and upgrading of the treatment system.