KR200410605Y1 - Apparatus for producing energy and manufacturing fertilizer by using excretions, waste water and slurry - Google Patents

Abstract

The present invention relates to an energy production and organic fertilizer production apparatus using livestock manure and waste water and slurry, foreign matter removal device for removing foreign matter from raw materials put into the input tank; A fermentation apparatus for fermenting the raw material by receiving the raw material from the foreign matter removing device and receiving high-temperature clean air and heat; A slurry drying and conveying apparatus for receiving the fermented raw material from the fermentation apparatus to dry by heat and remove harmful components; A heating device which receives the MFG gas, oxygen and auxiliary fuel supplied from the fermentation device and burns the same to generate heat; An MFG capture tank installed between the fermentation device and the heating device to collect MFG gas generated in the fermentation device; A boiler device installed at a rear end of the heating device to generate steam; A heat exchanger which receives waste heat from the boiler and exchanges heat with clean external air, thereby supplying clean air of high temperature to the fermentation apparatus; And it characterized in that it comprises a sorter for sorting foreign matter from the raw material transferred from the slurry drying and conveying device.

Livestock manure, fertilizer, energy, fermenter, heat exchanger, heating, boiler, gas

Description

APPARATUS FOR PRODUCING ENERGY AND MANUFACTURING FERTILIZER BY USING EXCRETIONS, WASTE WATER AND SLURRY}

1 is a view schematically showing an energy production and organic fertilizer production apparatus using livestock manure and wastewater and slurry according to the present invention;

2 is a view showing in detail the fermentation apparatus in the apparatus of Figure 1;

3 shows in detail the heating device in the device of FIG. 1;

4 is a view showing in detail the slurry drying and conveying apparatus in the apparatus of FIG.

5 shows in detail the cooling device in the device of FIG. 1; And

6 is a view schematically showing a sorting device and a packaging device therethrough in the apparatus of FIG.

<Description of the symbols for the main parts of the drawings>

10: foreign matter removal device 20: fermentation device

30: slurry drying and conveying device 40: heating device

50: boiler device 55: steam storage tank

60: heat exchanger 61: main body

63: outside air inlet 65: heat exchanger tube

70: sorter 80: MFG collection tank

90: oxygen generator 100: steam turbine

The present invention relates to an apparatus for producing energy and organic fertilizer using livestock manure and wastewater and slurry, and more particularly, by applying livestock manure, wastewater and slurry to fermenter and indirectly supplying heat, Applying LNG or LPG mixed with pure oxygen to MFG (Methane Fermentation Gas) to operate the heating device and boiler to produce steam, and to drive the steam turbine with the produced steam to produce electricity and fermentation The present invention relates to a livestock manure producing organic fertilizer by high-speed drying the raw material using heat, and an energy production and organic fertilizer manufacturing apparatus using wastewater and slurry.

In general, in the case of manure, the application of waste lacquer-G becomes a fully fertilized liquid fertilizer after about two months of fermentation due to microorganisms, and can be used as manure. Because it contains a lot of time, fermentation takes about three months.

In the case of large-scale livestock farms, the expenditure on environmental treatment costs exceeds 40% among these livestock farming sources, and the environmental cost burden is gradually increasing. Waste water is stored and then fermented or transported to other places. The concrete tank is waterproof when the concrete structure is tightly constructed, but the livestock manure is so corrosive that it is quickly corroded and cracked. This easily occurs and is difficult to repair in case of cracks. If the wastewater flows underground through this crack, it is not easy to find, and if the wastewater leaks, it is almost impossible to contaminate and restore the land.

In addition, water pollution refers to a condition in which polluted water flows beyond natural purification capacity and is artificially unsuitable for use. These main pollutants can be classified as domestic sewage, industrial wastewater, and agricultural wastewater. Among them, industrial wastewater is operated by installing pollution reduction facilities in accordance with the provisions of the Water Quality Preservation Act.In domestic sewage, sewage is generated through sewage treatment facilities or by other means in public waters such as rivers and sea areas. It is discharged.

However, livestock wastewater has been growing with economic growth and the demand for livestock is increasing, so the countermeasures against livestock wastewater are not sufficient, and related organizations are struggling to deal with these wastewaters.

Since the livestock wastewater has a larger pollution load than the wastewater generation, untreated discharge can lead to deterioration of the water quality of the stream and eutrophication of the lake, which not only contaminates water supply or agricultural water, but also causes odors and pests to hinder the environment. ．

Sewage slurries also suffer from difficulties. Therefore, in order to minimize these pollutants, the government has invested enormously every year by establishing comprehensive water supply measures.

However, in case of livestock wastewater treatment plant, it is considered that there is a limit in treating them with industrial litter of livestock farms. In order to overcome these limitations and activate environmentally-friendly organic farming, these manures are fermented at high speed and used for organic farming. On the other hand, I would like to suggest a way to make energy.

In order to solve the above problems, the object of the present invention is to remove environmental pollution, ferment them with raw materials, obtain MFG, convert it into energy, return it to resources, and produce organic fertilizers to raise farm incomes. It is to provide an energy production and organic fertilizer manufacturing apparatus using.

In order to achieve the above object, the energy production and organic fertilizer production apparatus using livestock manure and waste water and slurry according to the present invention, the foreign material removal device for removing foreign matter from the raw materials put into the loading tank; A fermentation apparatus for fermenting the raw material by receiving the raw material from the foreign matter removing device and receiving high-temperature clean air and heat; A slurry drying and conveying apparatus for receiving the fermented raw material from the fermentation apparatus to dry by heat and remove harmful components; A heating device which receives the MFG gas, oxygen and auxiliary fuel supplied from the fermentation device and burns the same to generate heat; An MFG capture tank installed between the fermentation device and the heating device to collect MFG gas generated from the fermentation device; A boiler device installed at a rear end of the heating device to generate steam; A heat exchanger which receives waste heat from the boiler and exchanges heat with clean external air, thereby supplying clean air of high temperature to the fermentation apparatus; And it characterized in that it comprises a sorter for sorting foreign matter from the raw material transferred from the slurry drying and conveying device.

The fermentation apparatus, a plurality of fermentation tank for fermenting the raw material; Fermentation tank heating chamber integrally installed on the outer wall and bottom of each fermentation tank to supply heat to the raw material; And a plurality of fermentation stirrer tubes installed inside each fermenter to supply hot clean air from the heat exchanger to the respective fermenters, and having a plurality of air injection nozzles. do.

The plurality of fermenters sequentially include a first fermentation tank, a second fermentation tank, and a third fermentation tank, characterized in that the fermentation tanks are connected by passing through the fermentation tank and the fermentation tank at an appropriate height.

A waste heat supply pipe connected to the heat exchanger is connected to a front end of the fermenter heating chamber, and a waste heat suction blower and a waste heat discharge pipe are connected to a rear end thereof.

The heating device has a closed structure and includes a plurality of burners, the plurality of burners in front of the plurality of burners connected to the MFG collection tank, the oxygen generator and the auxiliary fuel supply unit, and the rear end thereof is in communication with the boiler device. It is characterized by.

The MFG collection tank is connected to the MFG transfer pipe communicating with the closed upper wall of the fermentation tank, one side of the MFG transfer pipe is installed with an MFG suction blower for sucking the MFG gas, the MFG collection tank It is characterized by comprising a supply pump.

The slurry drying and conveying apparatus is to be installed across the heating device in the transverse direction,

A raw material inlet is installed at one side and a raw material outlet is installed at the other side; A screw conveyor installed to transfer raw materials into the hollow cylindrical wall; In order to transfer the heat from the heating device to the slurry drying and conveying device, it is installed surrounded by the outer periphery of the cylindrical wall, the upper portion is a heating medium integrally formed with a plurality of gas discharge nozzles in communication with the cylindrical wall; And a humidity control device installed inside one side of the slurry drying and transporting device to control the speed of the slurry drying and transporting device according to the appropriate humidity of the raw material.

In order to supply raw materials to the slurry drying and conveying apparatus, a slurry conveying pump and a slurry supply pipe are connected between the raw material inlet and the fermentation tank, and the raw material outlet is connected to the separator.

The boiler device, characterized in that for further storing the steam generated from the steam storage tank further installed on one side thereof.

In order to produce electricity by receiving steam, it characterized in that it further comprises a steam turbine connected to the steam storage tank.

The heat exchanger includes a main body and a plurality of heat exchange tubes installed inside the main body;

The main body is connected to the waste heat supply pipe, the upper one side is connected to the boiler apparatus, and a plurality of heat exchange tubes are connected to the upper one side thereof, and the plurality of heat exchange tubes are wound around the inside of the main body and connected to the upper other side of the main body. The other side of the main body is connected to a waste heat supply pipe for supplying waste heat to the fermenter heating chamber, the lower part of the main body is formed with an external air inlet, the other side of the main body is characterized in that the high temperature clean air supply pipe is connected to do.

In order to remove the various harmful components contained in the raw material, it is characterized in that the excipient input device is further installed at the inlet of the slurry drying and transfer device so that the excipient can be added to the raw material.

Hereinafter, with reference to the accompanying drawings will be described in detail for the energy production and organic fertilizer production apparatus according to the present invention. The purpose and features of the present invention will become more apparent from the accompanying drawings and the description of the detailed and preferred embodiments of the present invention described below. In addition, it is to be noted that the same to similar parts in the drawings are described with the same to similar reference numerals for convenience of description and understanding.

1 is a view schematically showing an energy production and organic fertilizer production apparatus using livestock manure and wastewater and slurry according to the present invention.

Prior to the description, in the present invention, since the livestock wastewater, wastewater and slurry are used as raw materials, the following will be referred to as raw materials.

As shown in Figure 1, the apparatus according to the present invention, largely remove foreign substances 10, fermentation device 20, slurry drying and conveying device 30, heating device 40, boiler device 50, heat exchange Group 60 and sorter 70.

In addition, an MFG collection tank 80 for collecting the MFG gas generated in the fermentation device 20 is provided between the fermentation device 20 and the heating device 40, to increase the combustion efficiency of the MFG and low air ratio An oxygen generator 90 for supplying oxygen to further obtain a high temperature temperature is installed at the front end of the heating device 20, and the steam turbine 100 receives electricity from the boiler device 50 and generates electricity. It is installed at the rear end of the boiler apparatus 50.

The debris removal device 10 is for removing debris from the raw material introduced into the loading tank 11 to obtain energy and organic fertilizer. The debris removal device 10 generally has a structure such as a rotating roller and a mesh as known in the art.

As shown in Figure 1 and 2, the raw material passed through the foreign material removing device 10 is transferred to the fermentation device (20). The fermentation apparatus 20 includes a first fermentation tank 230, a second fermentation tank 240 and a third fermentation tank 250. Between the first fermentation tank 230, the second fermentation tank 240 and the third fermentation tank 250, a separating wall 215 is mounted, respectively, the separation wall 215 is extended from the top wall to the bottom to It only extends to a certain height.

Fermentation tank heating chamber 220 for supplying heat to ferment the raw material at high speed is installed on the outer wall and bottom of each fermenter. The fermenter heating chamber 220 receives high temperature heat from the heat exchanger 60, and the high temperature heat thus supplied is released after supplying heat to the fermenters while circulating the outer wall and the bottom of each fermenter. In addition, each of the first fermentation tank 230, the second fermentation tank 240 and the third fermentation tank 250, the first fermentation stirring tube 223, the second fermentation stirring tube 224 and the third fermentation stirring tube 225 are respectively installed, it is possible to supply high temperature clean air from the heat exchanger 60 to the respective fermenters. The first fermentation stirrer tube 223, the second fermentation stirrer tube 224, and the third fermentation stirrer tube 225 are integrated into the clean air supply pipe 222 and connected to the heat exchanger 60, and the clean air. One side of the supply pipe 222 is provided with a turbo blower 227 for supplying high-temperature clean air.

Each of the fermentation stirring tubes 223, 224, and 225 inserted into the fermentation tanks 230, 240, and 250, respectively, is provided with a plurality of air injection nozzles 253, By supplying clean air, raw material stirring and fermentation can be promoted.

Such high temperature clean air or heat supply can accelerate the fermentation of livestock manure or slurry, thereby greatly shortening the fermentation period.

The production of the fermentation tank, fermentation stirrer tube and clean air supply pipe is used as a material (SUS316L) resistant to corrosion by salt or water in order to prevent the outflow of raw materials due to corrosion.

In addition, the raw materials inside the fermentation tank to connect the respective fermentation tanks in order to proceed to the first fermentation tank 230, the second fermentation tank 240 and the third fermentation tank 250, and penetrates between the fermentation tank and the fermentation tank at an appropriate height. When the raw material is completely filled in the first fermentation tank 230, the raw material is passed to the second fermentation tank 240, and when the raw material is completely filled in the second fermentation tank 240, it is naturally pushed and transferred to the third fermentation tank 250. Be sure to The flow path of the raw material is shown in FIG. 2.

A waste heat supply pipe 238 connected to the heat exchanger 60 is connected to a front end of the fermenter heating chamber 220, and a waste heat suction blower 242 and a waste heat discharge pipe 244 are connected to a rear end thereof. The waste heat supply pipe 238 supplies waste heat from the heat exchanger 60 to the fermentation tank heating chamber 220, and the waste heat suction blower 242 induces the intake of waste heat for fermentation and at the same time discharged after fermentation. It is supplied to the air pollution prevention facility, treated with clean gas, and discharged to the atmosphere.

The heating device 40 is supplied with MFG gas from the MFG collection tank 80 and oxygen from the oxygen generator 90 is heated through a burner. In this case, the MFG collection tank 80 is connected to the MFG transfer pipe 261 connected in communication with the closed upper wall of the third fermentation tank 250, the MFG gas is sucked to one side of the MFG transfer pipe 261 For this purpose, an MFG suction blower 263 is provided. In addition, an MFG supply pump 265 is provided at the top of the MFG collection tank 80 to supply the collected MFG to the burner by the heating device 40.

The reason for supplying oxygen to the burner of the heating device 40 is to increase the combustion efficiency of the MFG gas and to obtain a high temperature at a low air ratio.

As shown in FIG. 3, the heating device 40 has a plurality of burners 270 as a sealed structure. In addition, the front end of the heating device 40 is connected to the MFG capture tank 80, the oxygen generator 90 and the auxiliary fuel supply unit 276, the rear end is in communication with the boiler device (50).

Subsequently, in order to effectively burn the combustion instability, which is a drawback of the MFG, the city gas (LNG) or LPG gas may be mixed and supplied when the MFG gas is supplied to the burners 270 provided in the heating device 40. have.

As shown in Figures 1 and 4, the slurry drying and conveying device 30 is installed across the heating device 40 in the transverse direction. The slurry drying and conveying apparatus 30 simultaneously performs a drying step of removing moisture of fermented raw materials and a conveying step of raw materials, thereby producing raw materials of organic fertilizer.

The slurry drying and conveying device 30 is provided with a horizontal cylindrical hollow wall 311, a screw conveyor 313 for transferring the raw material in the hollow cylindrical wall 311 is provided. The raw material inlet 320 is integrally formed at the upper end of the cylindrical wall 311 in the front direction of the traveling direction, and the raw material outlet 330 is integrally formed at the lower part of the rear end of the cylindrical wall 311. In addition, the outer circumferential portion of the cylindrical wall 311 is surrounded by a heat medium 340 for transferring heat from the heating device 40 to the slurry drying and conveying device 30. On the upper side of the heat medium 340, a plurality of gas discharge nozzles 345 communicating with the cylindrical wall 311 are integrally formed.

In addition, the humidity control device 315 is attached to one side of the slurry drying and conveying device 30, it is possible to adjust the speed of the slurry drying and conveying device 30 in accordance with the appropriate humidity of the raw material.

The heat medium 340 is adopted to have a constant heat by receiving heat generated from the heating device 40, the material of the heat medium 340 is made of a high strength refractory containing chromium and nickel. The cylindrical wall 311 of the slurry drying and transfer device 30 embedded in the heat medium 340 is made of stainless steel (SUS310), etc., which is resistant to heat and corrosion, and has an internal screw conveyor 313. Made of stainless steel (SUS310), a material resistant to heat and corrosion.

In order to protect the raw material components in the fermented state, a screw conveyor 313 inside the sealed slurry drying and conveying device 30 is provided, and the raw material conveyed by the screw conveyor 313 is accompanied by moisture. Gas is included. The moisture contained in the raw material is removed by heat, and the gas is discharged into the heating device 40 by the plurality of gas discharge nozzles 345. The material of the plurality of gas discharge nozzles 345 is also made of a material (SUS310) resistant to heat and corrosion.

Some of the plurality of burners 270 is ignited or turned off automatically by the control of the humidity control device 315 for checking the humidity of the raw material conveyed by the slurry drying and conveying device 30, finally, the heating device ( 40) The temperature inside can be adjusted.

Here, the heat medium 340 indirectly transfers heat to the slurry drying and conveying device 30, and moisture and gas of the raw material transferred to the slurry drying and conveying device 30 by the heat are expanded by thermal expansion. It is injected through the gas discharge nozzle 315. The gas and moisture discharged in this way are burned in the heating furnace 10, and the gas and moisture are converted into energy as the gas and moisture are burned, and thus meet the energized heat of the MFG gas to produce a greater amount of heat.

In addition, a slurry transfer pump 286 and a slurry supply pipe 287 are connected between the raw material inlet 320 and the third fermentation tank 250 to supply raw materials to the slurry drying and conveying apparatus 30. The raw material outlet 330 is connected to the sorter 70 through a separate line.

In addition, in order to remove various harmful components contained in the raw material, the excipient input device 390 is connected to the inlet of the slurry drying and transfer device 30 so that the excipient can be added to the raw material.

In the above, the raw material dried in the slurry drying and conveying device 30 is discharged to the raw material outlet 330 of the slurry drying and conveying device (30). The raw material discharged through the raw material outlet 330 of the slurry drying and conveying device 30 is packaged after the foreign matter contained in the raw material is removed from the separator 70.

In addition, a boiler device 50 is provided at the rear end of the heating device 40, and the boiler device 50 is operated with the heat obtained from the heating device 40. The upper one side of the boiler device 50 is connected to the steam storage tank 55 to receive steam from the boiler device 50 to send steam to the steam turbine 100 to produce electricity. The steam turbine 100 is generally known in the art and will not be described in detail.

In addition, as shown in FIG. 5, the heat exchanger 60 includes a main body 61 and a plurality of heat exchange tubes 65 installed therein. The main body 61 is connected to the waste heat supply pipe 371, the upper one side is in communication with the boiler apparatus 50, and a plurality of heat exchange tubes 65 are connected to the upper one side thereof, the plurality of heat exchange tubes 65 Is wound around the inside of the main body 61 and connected to the upper other side of the main body 61. The other side of the upper portion of the main body 61 is connected to the waste heat supply pipe 238 for supplying waste heat to the fermenter heating chamber 220. In addition, an outer air inlet 63 is formed at the lower portion of the main body 61 to allow external clean air to flow into the main body 61. In addition, the main body 61 is connected to the high-temperature clean air supply pipe 222, it is possible to supply high-temperature clean air to each of the fermentation tanks 230, 240, 250.

Referring to the operation of the heat exchanger 60, the heat exchange between the high-temperature waste heat flowing through the plurality of heat exchange tubes 65 and the external air introduced into the body 61, the high-temperature clean external air is the first fermentation tank 230, the second fermentation tank 240 and the third fermentation tank 250 are injected at high pressure, and waste heat of high temperature is supplied to the fermentation tank heating chamber 220 through the waste heat supply pipe 238.

6 is a view schematically showing the flow of the organic fertilizer prepared according to the present invention is packaged through the sorter.

Hereinafter, energy production and organic fertilizer manufacturing process using livestock manure and wastewater and slurry according to the present invention will be described in detail.

Remove foreign substances from livestock manure and raw materials consisting of waste water and slurry.

Raw materials from which foreign substances have been removed are first fermented into the first fermentation tank 230. The raw material fermented first in the first fermentation tank 230 is naturally transferred to the second fermentation tank 240 for secondary fermentation. The raw material fermented in the second fermentation tank 240 secondary to the third fermentation tank 250 is naturally fermented to the third.

At this time, in the fermentation process, waste heat is supplied through the fermenter heating chamber 220 in order to accelerate the fermentation process by receiving heat from the fermentation tank side walls and the bottom. In addition, high temperature clean air is supplied into each fermenter to promote raw material stirring and fermentation.

The MFG gas generated from the third fermentation tank 250 is stored in the MFG collection tank 80, and the MFG gas is supplied to the heating device 40.

In order to effectively burn the combustion instability, which is a drawback of the MFG gas, oxygen is supplied or auxiliary fuel such as city gas or LPG gas is supplied.

The collected MFG, oxygen and auxiliary fuel to operate the heating device 40, the boiler device 50 and the steam turbine 100 to generate energy.

The fermented raw material is dried by passing through a heating device 40 to produce an organic fertilizer.

In order to supply the heat required for the fermentation process, the heat exchanger 60 undergoes a heat exchange process for making clean air at a high temperature.

Gas used in the present invention will be referred to as MFG (Methane Fermentation Gas) for convenience. The MFG is described in detail as follows.

MFG (Methane Fermentation Gas) is a kind of biogas produced by anaerobic digestion of organic waste or biomass in principle. The composition of MFG is CH _It is composed of CO ₂ , O ₂ , N _2, etc., and it is a low-calorific fuel with sufficient utilization value of about 3,000 ~ 6,000㎉ / N㎥. The use of these MFGs is not sufficiently efficient yet, and the collected MFGs are often burned or left uncleaned. There are three ways to effectively utilize MFGs. In this case, it is only used as a fuel. In this case, combustion stability is poor and the use range is limited. Therefore, there is a limit to effectively using a large amount of MFG. Second, the proper mixing of existing city gas (LNG) with MFG is used. In this case, the amount of heat generated by the mixed fuel is lower than that of the city gas, but it can greatly improve the combustion instability, which is a drawback of the MFG. Such a MFG mixed fuel can be useful for large plants, power plants, and district heating and cooling. This is the case when LPG is mixed with MFG. In this case, since the calorific value per volume of LPG is about twice as high as CH ₄ , the main component of the city gas, the mixed fuel may be supplied to the gas line in accordance with the compatibility with the city gas (Wobbe Index: WI = 13A). It can also be used as a city gas alternative fuel at a city gas level (WI = 10A). Table 1 below is a gas composition table.

MFG (average) 100% LPG 100% LNG 100% MFG 70% + LPG 30% (10A) MFG 50% + LPG50% (13A) MFG 50% + LNG 50% MFG 30% + LNG 70%   Furtherance CH ₄ 54.5 0.0 89.78 38.15 27.25 72.14 79.20 C ₂ H ₆ 0.0 0.0 7.48 0.00 0.00 3.74 5.24 C ₃ H ₈ 0.0 100.0 2.02 30.00 50.00 1.01 1.41 C ₄ H ₁₀ 0.0 0.0 0.70 0.00 0.00 0.35 0.49 CO ₂ 37.5 0.0 0.00 26.25 18.75 18.75 11.25 N ₂ 7.0 0.0 0.02 4.90 3.50 3.51 2.11 O ₂ 1.0 0.0 0.00 0.70 0.50 0.50 0.30 High calorific value (HHV: ㎉ / ㎥) 5215.0 23969.7 10598.4 10860.3 14605.8 7920.2 8901.6 Weber index high calorific value / specific gravity (㎉ / ㎥) 5338.7 19389.8 13434.0 10232.4 13109.0 8920.5 10582.0 Theoretical Volume Performance 5.14 23.80 10.49 10.74 14.47 7.82 8.89 Specific gravity (air = 1.0) 0.9542 1.5286 0.6224 1.1265 1.2414 0.7883 0.7220 Chemical equilibrium temperature (K) 2115.7 2290.9 2254.2 2229.2 2257.7 2205.8 2228.2

According to the present invention, there is an effect of eliminating environmental pollution, fermenting them with raw materials, obtaining MFG, converting it into energy, returning it to resources, and producing organic fertilizers to increase farm income.

Claims (12)

A debris removal device 10 for removing debris from the raw material introduced into the loading tank 11; A fermentation device 20 for receiving a raw material from the foreign substance removing device 10 and fermenting the raw material by receiving high-temperature clean air and heat; A slurry drying and conveying device 30 for receiving the fermented raw material from the fermentation device 20 to dry by heat and to remove harmful components; A heating device 40 generating heat by receiving MFG gas and oxygen and auxiliary fuel supplied from the fermentation device 20 and burning them; An MFG capture tank 80 installed between the fermentation device 20 and the heating device 40 to collect MFG gas generated in the fermentation device 20; A boiler device 50 installed at a rear end of the heating device 40 to generate steam; A heat exchanger 60 receiving waste heat from the boiler device 50 to heat exchange with clean external air, thereby supplying clean air of high temperature to the fermentation device 20; And Energy production and organic fertilizer production apparatus using livestock manure and wastewater and slurry, characterized in that it comprises a separator (70) for sorting foreign matter from the raw material transferred from the slurry drying and conveying device (30). The method of claim 1, The fermentation device 20, A plurality of fermenters 230, 240, 250 for fermenting the raw materials; Fermentation tank heating chamber 220 is integrally installed on the outer wall and bottom of each fermentation tank to supply heat to the raw material; And In order to supply high-temperature clean air from the heat exchanger 60 to the respective fermenters, the fermenters 230, 240, 250 are installed inside the fermenters 230, 240, and a plurality of air injection nozzles 253. Energy production and organic fertilizer production apparatus using livestock manure and wastewater and slurry comprising a plurality of fermentation stirrer tube (223), (224), (225); The method of claim 2, The plurality of fermenters sequentially include a first fermentation tank 230, a second fermentation tank 240 and a third fermentation tank 250, the fermentation tank is characterized in that the connection between the fermentation tank and the fermentation tank to pass through at an appropriate height. Livestock manure and energy production and organic fertilizer production equipment using wastewater and slurry. The method of claim 2, A waste heat supply pipe 238 connected to the heat exchanger 60 is connected to a front end of the fermenter heating chamber 220, and a waste heat suction blower 242 and a waste heat discharge pipe 244 are connected to a rear end thereof. Livestock manure and energy production and organic fertilizer production equipment using wastewater and slurry. The method of claim 1, The heating device 40 is a sealed structure, It is provided with a plurality of burners 270, the plurality of burners 270 of the front end is connected to the MFG capture tank 80, oxygen generator 90 and auxiliary fuel supply 276, the rear end of the boiler Energy production and organic fertilizer production apparatus using livestock manure and waste water and slurry characterized in that it is in communication with the device (50). The method of claim 2, The MFG collection tank 80 is connected to the MFG transfer pipe 261 communicated with the closed upper wall of the fermentation tank 250, the MFG suction blower for sucking the MFG gas on one side of the MFG transfer pipe 261 263 is installed, the production of organic fertilizer and organic fertilizer using livestock manure and waste water and slurry, characterized in that the MFG collection tank 80 is provided with an MFG supply pump (265). The method of claim 1, The slurry drying and conveying device 30 is installed across the heating device 40 in the transverse direction, A raw material inlet 320 is installed at one side and a raw material outlet 330 is installed at the other side, and a hollow cylindrical wall 311 which is horizontally long; A screw conveyor (313) installed to transfer raw materials into the hollow cylindrical wall (311); In order to transfer heat from the heating device 40 to the slurry drying and conveying device 30, it is installed surrounded by the outer peripheral portion of the cylindrical wall 311, the upper side of the plurality of communication with the cylindrical wall 311 A heat medium 340 in which a gas discharge nozzle 345 is integrally formed; And To control the speed of the slurry drying and transporting device 30 according to the appropriate humidity of the raw material, the humidity control device 315 installed inside one side of the slurry drying and transporting device 30; Energy production and organic fertilizer production equipment using livestock manure, wastewater and slurry. The method of claim 7, wherein In order to supply the raw material to the slurry drying and conveying apparatus 30, a slurry transfer pump 286 and a slurry supply pipe 287 are connected between the raw material inlet 320 and the fermentation tank 250, and the raw material outlet 330 ) Is an energy production and organic fertilizer production apparatus using livestock manure and wastewater and slurry, characterized in that connected to the sorter (70). The method of claim 1, The boiler device 50, in order to store the steam generated therefrom, further comprising a steam storage tank 55 on the upper side of the livestock manure and waste water and slurry production apparatus using organic fertilizer production apparatus . The method of claim 9, Energy production and organic fertilizer production apparatus using livestock manure and waste water and slurry, characterized in that it further comprises a steam turbine (100) connected to the steam storage tank (55) in order to produce electricity by receiving steam. The method of claim 1, The heat exchanger (60) includes a main body (61) and a plurality of heat exchange tubes (65) installed inside the main body (61); The main body 61 is connected to the waste heat supply pipe 371, the upper one side is in communication with the boiler device 50, a plurality of heat exchange tubes 65 are connected to the upper one side, the plurality of heat exchange tubes 65 Winding around the inside of the main body 61 is connected to the other side of the upper portion of the main body 61, the other side of the main body 61 is connected to the waste heat supply pipe 238 for supplying waste heat to the fermenter heating chamber 220 The lower part of the main body 61, the external air inlet 63 is formed, the other side of the main body 61, the livestock waste and waste water and slurry characterized in that the high-temperature clean air supply pipe 222 is connected Used energy production and organic fertilizer manufacturing equipment. The method according to claim 1 or 7, In order to remove various harmful ingredients contained in the raw material, livestock manure, characterized in that the excipient injector 390 is further installed at the inlet of the slurry drying and transfer device 30 to add the excipient to the raw material and Energy production and organic fertilizer production equipment using waste water and slurry.

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