JP4018409B2 - Manure processing equipment - Google Patents

Description

[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a manure processing apparatus.
[0002]
[Prior art]
In recent years, issues related to environmental conservation have been highlighted, and serious discussions have been held on how to create an environment that can satisfy each other while maintaining a state in which people's living environments are not destroyed in order to coexist with humans and animals. It has come to be. At that time, attention has been given to the treatment of livestock excreta as well as human excreta.
[0003]
In general, when manure from cattle, pigs, other livestock, etc. is processed, the solid matter is removed from the excreted excreta and then stored in a large tank and aerated to reduce the smell of manure. In addition, oxidative fermentation treatment is carried out by promoting the self-decomposition of microorganisms, processed into a desired aerated manure treatment solution, and this is used as a fertilizer.
[0004]
[Problems to be solved by the invention]
However, in such a conventional method, when a high-viscosity manure liquid is put into the tank to perform the aeration process, the manure liquid remains at the bottom of the tank without being aerated because the viscosity is high, and as a result, The efficiency of the oxidative fermentation process is deteriorated by promoting the self-decomposition of microorganisms, and it takes time to process it into a desired aeration-processed manure fluid.
Furthermore, in the conventional system, although the aeration treatment is performed on the manure fluid, it is difficult to process the manure fluid into an aeration treatment liquid having predetermined characteristics such as a desired pH value and BOD (Biological oxygen demand) value. Even if the desired aeration treatment liquid is obtained, it is difficult to store the aeration treatment liquid in a state having predetermined characteristics.
[0005]
The present invention has been made in order to solve such problems, and an object of the present invention is to obtain an aeration-processed manure fluid having predetermined characteristics by performing an aeration process on manure fluid more efficiently than before. An object of the present invention is to provide an excrement processing apparatus capable of performing the above-described process.
[0006]
[Means for Solving the Problems]
In order to solve this problem, an excrement disposal apparatus according to the present invention includes at least one aeration treatment tank for aeration treatment of excrement fluid, an air supply means for supplying air for aeration treatment to the aeration treatment tank, and an aeration A parameter value measurement unit that is disposed inside the treatment tank and that measures the aeration treatment state and a control unit that controls the aeration treatment state of the aeration treatment tank, the control unit was obtained by the parameter value measurement unit Based on the measured value, the air supply means is driven so that the parameter value of the aeration treatment tank becomes a desired value, and the aeration treatment state of the aeration treatment tank is controlled. According to this manure processing apparatus, the manure fluid is aerated until the parameter value of the aeration treatment tank reaches a desired value.
[0007]
In the manure processing apparatus, the aeration treatment tank may be composed of first and second aeration treatment tanks. According to this manure processing apparatus, the manure fluid is aerated in the two aeration tanks.
[0008]
In the manure processing apparatus, the parameter value may be at least one selected from pH value, BOD value, COD value, electrical conductivity, temperature and pressure. According to this manure processing apparatus, the manure fluid is subjected to an aeration process based on the pH value, BOD value, COD value, electrical conductivity, temperature and pressure.
[0009]
In the manure processing apparatus, the aeration processing tank may have a sending means for sending the manure fluid in the aeration processing tank to the subsequent stage. According to this manure processing apparatus, the manure fluid that has been subjected to the aeration process until the desired parameter value is obtained in the aeration processing tank is sent to the subsequent stage by the sending means.
[0010]
In the manure processing apparatus, the control unit performs the aeration process until the manure fluid in the aeration treatment tank reaches a predetermined pH value, BOD value, COD value, or electrical conductivity, and thereafter the manure fluid in the aeration treatment tank. The aeration processing state of the aeration processing tank may be controlled so that a predetermined amount is output to the subsequent stage by the sending means. According to this manure processing apparatus, the manure fluid that has been subjected to the aeration process until the predetermined pH value, BOD value, COD value, or electrical conductivity is reached is output to the subsequent stage by the delivery means in a fixed amount.
[0011]
In the excreta treatment apparatus, the control unit may stop each of the air supply means when each of the aeration treatment tanks reaches a predetermined pressure. According to this manure processing apparatus, when the pressure inside the aeration processing tank reaches a predetermined value, the air supply means stops.
[0012]
The feces and urine treatment apparatus further includes a memory for recording a reference value corresponding to the parameter value to be measured, and based on the measurement value obtained by the parameter value measurement unit and the reference value recorded in the memory, The aeration state may be controlled. According to this manure treatment apparatus, the aeration state of the aeration treatment tank is controlled by comparing the reference value recorded in advance in the memory with the measurement value measured by the parameter value measurement unit.
[0013]
In the manure processing apparatus, the control unit may perform control based on a difference between the reference value and the measurement value. According to this manure processing apparatus, the aeration processing state of the aeration processing tank is controlled by the difference between the reference value recorded in the memory and the measured value measured by the parameter value measuring unit.
Further, the control unit may correct the reference value based on the measurement value obtained by the parameter value measurement unit, and control based on the corrected value.
[0014]
In the manure processing apparatus, the control unit may correct the reference value based on an average value of a plurality of measurement values obtained by the parameter value measurement unit. According to this manure processing apparatus, the reference value recorded in the memory is averaged from a plurality of measured values measured by the parameter value measuring unit, and is corrected based on the average value.
[0015]
In the manure processing apparatus, the manure processing apparatus further includes input means for inputting manure fluid into the aeration treatment tank, and the input means outputs a predetermined amount of manure fluid from the aeration treatment tank by the output means, and then the aeration treatment tank. The same amount of excrement fluid may be input from the input means. According to this manure processing apparatus, when a predetermined amount of manure fluid that has been aerated until the parameter value of the aeration treatment tank reaches a desired value is output to the subsequent stage by the sending means, the same amount as the amount sent to the subsequent stage The excrement fluid is input by the input means.
[0016]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.
A feces and urine treatment apparatus to which the present invention shown in FIGS. 1 to 6 is applied includes a first aeration treatment tank 1 that performs aeration treatment of excrement fluid, and a second aeration process tank 1 that is disposed at a subsequent stage of the first aeration treatment tank 1. An aeration treatment tank 2, a first aging tank 3 for storing manure fluid aerated in the above-described aeration treatment tanks 1 and 2 in a state having predetermined characteristics, and a stage subsequent to the first aging tank 3 are disposed. The second aging tank 4, the pre-reservoir tank 5 for supplying the manure fluid separated from the excrement into solid and liquid and supplying the manure fluid to the first aeration treatment tank 1, and the aeration process from the second aging tank 4 An external storage tank 6 for storing the liquid, a drain tank 7 for storing the sediment in the lower part of the aeration processing tanks 1 and 2 described above, a controller 8 for controlling the operation of each part of the entire processing tank, and a control device 9 It consists of and.
In this embodiment, two aeration treatment tanks are provided. However, the number of aeration treatment tanks is not limited to two, and may be freely changed, for example, one.
[0017]
The first aeration treatment tank 1 will be specifically described with reference to FIG. 2. A box 10 that defines the outer shape of the first aeration treatment tank 1 is a rectangular parallelepiped as a whole, and the inside is circulated with the aeration treatment unit 1 a by the partition wall 11. It is partitioned into part 1b. Above the aeration processing unit 1a, a manure fluid diffusion unit 12, output devices 13 and 14, and a defoaming water tank 25 for storing defoamed manure fluid (antifoam water) are provided. A shower 15 that outputs feces and urine fluid is disposed above the inside of the aeration processing unit 1a and the circulation unit 1b, and an aerator 16 that mixes and discharges the manure fluid and air below the inside of the aeration processing unit 1a. An air supply device 17 that is directly supplied into the excreta fluid in the aeration treatment unit 1a and further promotes the aeration treatment is disposed. The sediment at the bottom of the aeration treatment tank 1 is placed in the circulation unit 1b at the bottom of the aeration treatment tank 1. A moving mixer 18 is disposed. Below the inside of the circulation unit 1b provided alongside the aeration processing unit 1a, the pump 19 for sending the manure fluid moved from the aeration processing unit 1a to the manure fluid diffusing unit 12, and the manure fluid moved from the aeration processing unit 2a A drain pipe for discharging the precipitates in the lower part of the first aeration treatment tank 1 to the outside of the first aeration treatment tank 1 and the pump 20 that is sent to the shower 15 and the defoaming water tank 25 or the shower 37 of the second aeration treatment tank 2 described later 21 is disposed, and a pipe 22 for connecting the excrement fluid between the first aeration treatment tank 1 and the second aeration treatment tank 2 is connected to the lower side wall of the circulation part 2b. A heating pipe 23 is disposed on the outer periphery of the bottom of the box 10, and the exposed outer surface of the box 10 is covered with a heat insulating material 24. A pressure sensor 202 is provided on the upper portion of the box body 10, and a pH sensor 201, a temperature sensor 203, and a level sensor 204 that are suspended from the upper portion of the box body 10 are disposed inside the box body 10.
[0018]
In the excrement fluid diffusing unit 12, a diffusion plate 12c is suspended from the upper part of the aeration processing unit 1a by a shaft 12e, and this shaft 12e is attached to a motor 12d.
As well shown in FIGS. 1 and 2, the pipe 12 a led from the inside of the box 10 to the outside of the box 10 in the vicinity of the excrement fluid diffusion portion 12 circulates in the first aeration treatment tank 1 through the valve 114. It is connected to a pipe 19b of a pump 19 disposed in the part 1b. Thereby, in the first aeration treatment tank 1, the excrement fluid guided from the aeration treatment unit 1 a to the circulation unit 1 b is guided again from the excrement fluid diffusion unit 12 to the aeration treatment unit 1 a, and the inside of the first aeration treatment tank 1 is passed through. Circulating and continuous aeration treatment is performed.
The pipe 12a is also connected to a second aeration treatment tank 2, a pre-storage tank 5, and a drain tank 7, which will be described later, via valves 111, 112, 113, and 114.
[0019]
The lead-in pipe 12b is connected to the pipe 12a described above, and a diffusing plate 12c in which the excrement fluid sent from the pipe 12a is suspended downward from a plurality of holes provided in the lower end of the excrement fluid diffusion part 12. Is released towards
The diffusion plate 12c shown here is composed of two large and small disks. When the diffusion plate 12c is rotated by the motor 12d, the excrement fluid colliding with the diffusion plate 12c is blown in the circumferential direction by the centrifugal force of the diffusion plate 12c, and aeration processing is performed. It is effectively diffused into the part 1a.
[0020]
In the present embodiment shown in FIG. 2, the lead-in pipe 12c is provided in the excrement fluid diffusion part 12, but the lead-in pipe 12c may not be provided. You may make it drop the manure fluid sent from the pipe 12a directly into the diffusion plate 12c from the upper part of the aeration processing part 1a. Further, a guide or the like may be provided so that the excrement fluid collides with the diffusion plate 12c with certainty.
[0021]
As shown in FIG. 2, the shower 15 is connected to the pump 20 via a valve 115, and outputs manure fluid delivered from the pump 20 to the inside of the aeration processing unit 1a and the circulation unit 1b from a plurality of nozzles 15a. As a result, the manure fluid at the bottom of the first aeration treatment tank 1 is output from the upper side of the first aeration treatment tank 1 from the shower 15, thereby increasing the contact area with the air and effectively performing the aeration treatment. become.
The shower 15 has a pipe 15b connected to the defoaming water tank 25 through a valve 116, and the manure fluid in the first aeration treatment tank 1 is selectively transferred to the defoaming water tank 25 by this pipe 15b. Is output.
[0022]
As shown in FIG. 2, the aerator 16 is disposed near the center below the aeration processing unit 1 a, and an air introduction pipe 16 a is led out from the aerator 16 to the outside of the box 10. The aerator 16 mixes manure fluid in the vicinity of the aerator 16 and air taken in from the air introduction pipe 16a according to an instruction from the controller 8, and releases the mixture into the manure fluid.
[0023]
The air supply device 17 has a cylindrical shape, and an air supply port 17a is formed at an end disposed near the lower part of the aeration processing unit 1a, and air is discharged from the air supply port 17a into the manure fluid. The One end of the air supply device 17 is led out of the box 10 and is connected to an air supply port 105 of the control device 9 described later. Air indicated by ▼ is supplied. In this way, by providing the air supply device 17 in addition to the aerator 16 in the first aeration treatment tank 1, air is sufficiently supplied to the excrement fluid in the aeration treatment unit 1a, and the excrement fluid is effectively Aerated.
[0024]
As shown in FIGS. 1 and 2, the pump 19 including the pump unit 19 a and the pipe 19 b is connected to the pipe 12 a of the excrement fluid diffusing unit 12 via the valve 114 and is sent from the pump 19. The excrement fluid to be discharged is discharged from the excrement fluid diffusion unit 12 to the aeration processing unit 1a. As a result, the excreta fluid circulates through the aeration processing unit 1a and the circulation unit 1b and is continuously subjected to the aeration process.
[0025]
The pump 19 is connected to the pipe 53 of the first aging tank 3 through valves 114, 112, and 134, and sends manure fluid in the first aeration treatment tank 1 to the first aging tank 3. Realize sending means. Thus, the maintenance of the 1st aeration treatment tank 1 becomes easy by sending the excrement fluid inside the 1st aeration treatment tank 1 to the 1st aging tank 3.
[0026]
As shown in FIGS. 1 and 2, the pump 20 composed of the pump unit 20a and the pipe 20b has the pipe 20b connected to the shower 15 via the valve 115, and the excrement fluid delivered from the pump 20 is The water is discharged from the shower 15 to the defoaming water tank 25 through the aeration processing unit 1 a, the circulation unit 1 b and the valve 116. As a result, the excreta fluid circulates through the aeration processing unit 1a and the circulation unit 1b and is continuously subjected to the aeration process.
The pump 20 can select whether or not to send manure fluid to the antifoam water tank 25 by a valve 116 provided in the shower 15.
The pipe 20b is connected to a pipe 47 of the second aeration treatment tank 2 to be described later via a valve 117, and can send manure fluid sent from the pump 20 to the second aeration treatment tank 2. Thereby, the pump 20 implement | achieves a delivery means and an input means. Thus, the excreta fluid is sent from the first aeration treatment tank 1 to the second aeration treatment tank 2 and subjected to the aeration process step by step.
[0027]
In addition, the pump 19b is arrange | positioned upwards in the circulation part 1b from the pump 20b. As described above, the pumps 19b and 20b are arranged at different heights in the circulation unit 1b, so that feces and urine fluids having different degrees of aeration can be selectively circulated inside the first aeration tank. it can.
[0028]
As shown in FIGS. 1 and 2, the drain pipe 21 is led out of the box 10 from below the circulating portion 1 b and connected to the drain tank 7 via a valve 135 and a pump 98. The sediment deposited on the bottom of the circulating unit 1b is sent to the drain tank 7 through the drain pipe 21. Thereby, the sediment at the bottom of the first aeration treatment tank 1 is sent out to the outside of the first aeration treatment tank 1, and the first aeration treatment tank 1 performs the aeration treatment only on the excreta fluid, and the efficiency of the aeration treatment is improved. improves.
[0029]
As shown in FIGS. 1 and 2, the pipe 22 has one end on the side wall of the box body 10 below the circulating portion 1b and the other end on the box below the circulating portion 2b of the second aeration treatment tank 2 described later. It is connected to the side wall of the body 31 via a valve 119, and moves manure fluid in the first aeration treatment tank and the second aeration treatment tank indicated by reference numeral (2) in FIG.
When the valve 119 is opened when the amount of manure fluid in the first aeration treatment tank 1 is less than the amount of manure fluid in the second aeration treatment tank 2, the manure fluid is transferred from the second aeration treatment tank 2 to the first aeration treatment tank 1. Is sent out. In this way, by adjusting the amount of the excrement fluid in the first aeration treatment tank 1 and the second aeration treatment tank 2 by the pipe 22, it is possible to stabilize the aeration treatment efficiency of the excrement fluid.
The pipe 22 can also send manure fluid in the first aeration treatment tank 1 to the second aeration treatment tank 2.
[0030]
As shown in FIGS. 1 and 2, the heating pipe 23 is disposed on the bottom of the box 10 along the side wall of the bottom of the box 10, and both ends of the heating pipe 23 and the fluid output port 106 of the control device 9 and the fluid are described later. It is connected to the input port 107. The heated fluid output from the fluid output port 106 indicated by reference numeral 6 in FIGS. 1 and 2 passes through the inside of the heating pipe 23 and passes through the inside of the heating pipe 23 indicated by reference numeral 7 in FIGS. The fluid that has flown is output to the fluid input port 107. Thus, the heating pipe 23 heats the inside of the first aeration treatment tank by circulating the heated fluid sent from the control device 9 inside the heating pipe 23.
[0031]
The output devices 13 and 14 are provided with cylindrical envelopes 13b and 14b above the cylindrical guide portions 13a and 14a having tapered ends whose upper ends are narrowed toward the opening, and the envelopes 13b and 14b include Defoaming members 13c and 14c for defoaming bubbles generated by the aeration process are provided. Outlet portions 13d and 14d and gas output portions 13e and 14e are provided on the side walls of the envelopes 13b and 14b, and are connected to pipes 13g and 14g, respectively. Gas exhaust ports 13f and 14f are provided at one end of the pipes 13g and 14g, and the other end is connected to a defoaming water tank 36 of the second aeration treatment tank 2 described later. At least one gas exhaust pipe 13h, 14h is provided above the envelopes 13b, 14b.
[0032]
A large amount of bubbles generated by aeration processing in the aeration processing unit 1a are guided to the cylindrical guide portions 13a and 14a, and the bubbles rising in the cylindrical guide portions 13a and 14a are conical defoaming members 13c. , 14c liquefied and liquefied feces and urine fluid (antifoam water) is dropped onto the outlet portions 13d and 14d, and sent out from the pipes 13g and 14g to the antifoam water tank 25 described later.
The gas exhaust ports 13f and 14f have a cylindrical shape and are connected to the upper ends of the pipes 13g and 14g. By providing the gas exhaust ports 13f and 14f, the excreta fluid liquefied by the defoaming portions 13c and 14c is efficiently output from the pipes 13g and 14g.
Each component of the output devices 13 and 14 mentioned above is comprised from a well-known material.
[0033]
As well shown in FIG. 1 and FIG. 2, the defoamed manure fluid (foamed water) sent out from the pipes 13g and 14g of the output devices 13 and 14 of the first aeration treatment tank 1 consists of a known tank. It is guided to the defoaming water tank 25. The manure fluid guided to the defoaming water tank 25 is supplied from the pipe 25a provided at one end to the bottom of the defoaming water tank 25 or from the pipe 25c connected to the pump 25b. To be released. Thus, the excreta fluid circulates inside the aeration processing unit 1a without hindering the promotion of the aeration processing performed in the first aeration processing tank 1, and is continuously subjected to the aeration processing.
[0034]
The pipe 25a and the pipe 25c may have one end connected to the aerator 16. With such a configuration, the excreta fluid delivered from the pipe 25a and the pipe 25c is mixed with air by the aerator 16, and the aeration process is performed more efficiently.
When a larger amount of defoaming water than the predetermined amount of the defoaming water tank 25 is sent to the defoaming water tank 25, the excess defoaming water indicated by reference numeral (4) in FIG. From the pipe 25d connected to the side wall of the first aging tank 3.
A gas exhaust pipe 25e is provided above the defoaming water tank 25, and the gas generated in the defoaming water tank 25 by the gas exhaust pipe 25e is released to the outside of the defoaming water tank 25.
[0035]
The pH sensor 201 is a known pH sensor and is suspended in the excrement fluid from the upper part of the box 10 as shown in FIG. 2, measures the pH value of the excrement fluid, and outputs the measured value to the controller 8. . In addition, if the position where the pH sensor 201 is disposed is a place where the pH value of the excreta fluid can be measured, it can be freely changed at any position inside the first aeration treatment tank 1.
[0036]
The pressure sensor 202 is a known pressure sensor, and is provided on the top of the box 10 as shown in FIG. 2, measures the pressure inside the box 10, and outputs the measured value to the controller 8. It should be noted that the position where the pressure sensor 202 is disposed can be appropriately changed to any position in the first aeration treatment tank 1 as long as the pressure inside the first aeration treatment tank 1 can be measured.
[0037]
The temperature sensor 203 is a known temperature sensor such as a thermometer, and is suspended in the excrement fluid from the upper part of the box 10 as shown in FIG. 2. The temperature of the excrement fluid is measured, and the measured value is the controller 8. Output to. In addition, if the position which arrange | positions the temperature sensor 203 is a place which can measure the temperature of the excrement fluid in the 1st aeration processing tank 1, it can change freely at any position in the 1st aeration processing tank 1. Can do.
[0038]
The level sensor 204 is a known level sensor, and is suspended in the excrement fluid from the upper part of the box 10 as shown in FIG. 2. The level sensor 204 measures the amount of excrement in the box 10 and the measured value is the controller 8. Output to. In addition, if the position where the level sensor 204 is arrange | positioned is a place which can measure the quantity of the excrement fluid in the 1st aeration processing tank 1, it can be changed suitably freely.
[0039]
Each of the above-described parts is made of a known material.
[0040]
Next, the second aeration treatment tank 2 will be described. Note that the second aeration treatment tank 2 has substantially the same configuration as the first aeration treatment tank 1, and the same components are given the same names, and description thereof is omitted as appropriate.
The pipe 33a of the excrement fluid diffusing unit 33 is connected to a pump 86 of the pre-reservoir tank 5 to be described later via a valve 113, and the excrement fluid introduced into the pre-reservoir tank 5 is selectively supplied to the second aeration treatment tank. Led to 2.
[0041]
As described above, the end of the pipe 47 is connected to the pump 20 of the first aeration treatment tank 1, and the excrement fluid subjected to the aeration treatment in the first aeration treatment tank 1 is sent to the second aeration treatment tank 2. To do. The open end of the pipe 47 is disposed in the vicinity of the aerator 38 at the bottom of the aeration processing unit 2 a via the valve 137, and the excreta fluid sent from the first aeration processing tank 1 is supplied to the aerator 38. Output near. Thereby, the excrement fluid sent from the 1st aeration processing tank 1 is taken in into the aerator 38, and the aeration process is performed also in the 2nd aeration processing tank 2.
The pipe 47 is also connected to the excrement fluid diffusion part 33 through a valve 138. As a result, the excrement fluid sent out from the first aeration treatment tank 1 is released from the excrement fluid diffusion part 33 of the second aeration treatment tank 2 into the second aeration treatment tank 2, and subsequently to the first aeration treatment tank 1. In the second aeration treatment tank 2, aeration processing is performed in stages.
The manure fluid output from the pipe 47 is selectively output to the inside of the second aeration treatment tank 2 by the valves 138 and 139.
[0042]
When more defoaming water is sent to the defoaming water tank 36 than the predetermined amount of the defoaming water tank 36, the excess defoaming water is added to the side wall of the defoaming water tank 36 and the first aeration treatment tank 1 described above. Is sent to the first aging tank 3 from a pipe 36d connected to the pipe 25d of the defoaming water tank 25.
[0043]
As shown in FIG. 1, the pump 41 composed of the pump part 41 a and the pipe 41 b is connected to the shower 37 via the valve 120, and the excrement fluid sent from the pump 41 is sent from the shower 37. The defoamed water tank 36 is discharged through the second aeration treatment tank 2 and the valve 139. As a result, the excreta fluid circulates in the second aeration tank 2 and is continuously subjected to the aeration process.
The pump 41 can select whether or not to send manure fluid to the defoamed water tank 36 by a valve 139 provided in the shower 37.
The pipe 41 b is connected to a pipe 53 connected to a first aging tank 3 to be described later via a valve 121, and the excrement fluid sent from the pump 41 is guided to the first aging tank 3. Thereby, the pump 41 implement | achieves a delivery means.
[0044]
As shown in FIG. 1, the pump 42 composed of the pump unit 42 a and the pipe 42 b is configured such that the pipe 42 b is connected to the pipe 33 a of the manure fluid diffusing unit 33 via the valve 118, and manure discharged from the pump 42. The fluid is discharged from the excreta fluid diffusing unit 33 to the aeration processing unit 2a. As a result, the excreta fluid circulates through the aeration processing unit 2a and the circulation unit 2b and is continuously subjected to the aeration process.
Further, the pipe 42b is connected to the pipe 12a of the excrement fluid diffusing unit 12 of the first aeration treatment tank 1 via valves 118, 113, 134, 112, and the excrement fluid sent from the pump 42 is selected selectively. To the first aeration treatment tank 1. Thereby, the pump 42 implement | achieves an input means.
The pump 42 is disposed below the pump 41.
[0045]
As described above, one end of the pipe 22 connecting the circulation part 1b of the first aeration treatment tank 1 and the circulation part of the second aeration treatment tank 2 is connected to the lower side wall of the circulation part 2b of the box 31. Yes. This pipe 22 opens the valve 119 when the excrement fluid in the first aeration treatment tank 1 is less than the excrement fluid in the second aeration treatment tank 2 to select the excrement fluid in the second aeration treatment tank 2. The first aeration treatment tank 1 is sent out.
[0046]
Next, the first aging tank 3 will be described. As shown in FIG. 3, the box 51 is divided into an aging part 3 a and an aging part 3 b by a partition wall 52. A pipe 53 is disposed above the inside of the aging unit 3a, and the pipe 36d of the defoaming water tank 36 of the second aeration treatment tank 2 described above is connected to the lower side wall of the aging unit 3a. Pumps 54 and 55 are installed at the bottoms of the aging unit 3a and the aging unit 3b, and showers 56 and 57 connected to the pumps 54 and 55 are disposed above the inside of the aging units 3a and 3b. The pipe 58 connected to the pump 54 is led out inside the aging unit 3b, and the pipe 59 connected to the pump 55 is led out to the outside of the first aging tank 3. Further, in both the aging units 3a and 3b, an air supply device 60 is disposed below the inside, and a heating pipe 61 is provided at the bottom. In the aging units 3a and 3b, pH sensors 221 and 222, temperature sensors 223 and 224, and level sensors 225 and 226 suspended from the upper part of the box 51 in the excrement fluid are disposed. Further, the outside of the box 51 is covered with a heat insulating material 62.
[0047]
A pipe 36d is connected to the lower side wall of the aging part 3a of the box 51. The pipe 36d exceeds a predetermined amount of the defoaming water tank 36 indicated by reference numeral 4 in FIGS. The defoamed manure fluid (antifoam water) is sent out.
[0048]
One end of the pipe 53 is disposed above the aging unit 3 a, and the other end is led out of the box 51 and connected to the pipe 41 b of the pump 41 of the second aeration tank 2. As described above, the excrement fluid (aeration treatment liquid) subjected to the aeration process sent from the pump 41 of the second aeration treatment tank 2 is sent to the aging tank 3 a via the pipe 53.
[0049]
As shown in FIG. 1 and FIG. 3, the pump 54 composed of the pump unit 54 a and the pipe 54 b has the pipe 54 b connected to the shower 56 via the valve 122, and an aeration treatment liquid sent from the pump 54. Is discharged from the shower 56. As a result, the aeration treatment liquid is stored inside the aging unit 3a in a state of circulating through the aging unit 3a and having predetermined characteristics.
The pipe 54 b is connected to the pipe 58 via the valve 123, and the aeration treatment liquid stored in the aging unit 3 a is sent to the aging unit 3 b separated by the partition wall 52 by the pump 54.
[0050]
The pump 55 has the same configuration as the above-described pump 54, the pipe 55b is connected to the shower 57 via the valve 124, and the aeration treatment liquid sent to the aging unit 3b by the pipe 58 is the same as the pump 55. The aging part 3b is circulated by the shower 57 and stored in the aging part 3b in a state having predetermined characteristics.
The pipe 55b is connected to a pipe 59 connected to the second aging tank 4 via a valve 125, and the aeration treatment liquid stored in the aging unit 3b is sent to the second aging tank 4 by the pump 55. Is done.
[0051]
The air supply device 60 has a plurality of air supply ports 60 a formed on the surface thereof, and is disposed below the box 51. One end of the air supply device 60 is led out to the outside of the box body 61 and connected to an air supply port 105 of the control device 9 which will be described later. The air supply port 105 is denoted by reference numeral 5 in FIGS. The indicated air is supplied. When the air supply device 60 supplies air into the aeration treatment liquid, the aeration treatment liquid is stored in the first aging tank 3 while maintaining predetermined characteristics.
[0052]
Both ends of the heating pipe 61 stretched around the bottom of the box 51 are connected to a fluid output port 106 and a fluid input port 107 of the control device 9 described later. The heated fluid output from the fluid output port 106 indicated by reference numeral 6 in FIGS. 1 and 3 passes through the inside of the heating pipe 61, and passes through the heating pipe 61 indicated by reference numeral 7 in FIGS. 1 and 3. The fluid that has passed through is output to the fluid input port 107. Thus, the heating pipe 61 heats the inside of the first aeration treatment tank by circulating the heated fluid delivered from the control device 9.
[0053]
PH sensors 221, 222, temperature sensors 223, 224, and level sensors 225, 226 are disposed in each of the aging units 3a, 3b, and the values measured by each are output to the controller 8. In addition, if the position which arrange | positions pH sensor 221,222, temperature sensor 223,224 and level sensor 225,226 is a place which can measure the pH value, temperature, and quantity of the excrement fluid in the 1st aging tank 3, It can be set freely as appropriate.
[0054]
Each of the above-described parts is made of a known material.
[0055]
Next, the second aging tank 4 will be described. The second aging tank 4 has the same configuration as that of the first aging tank 3 described above, and the same names are used for those having the same functions, and therefore description thereof will be omitted as appropriate.
[0056]
One end of the pipe 59 is connected to the upper part of the aging tank 4a, and the other end is led out of the box 65, and is connected to the pipe 55b of the pump 55 of the first aging tank 3 through the valve 125. Has been. The aeration treatment liquid stored in the aging unit 3 b of the first aging tank 3 is sent to the aging tank 4 a via the pipe 59.
[0057]
One end of the pump 69 is led out of the box 51 as shown in FIG. 1, and is connected to a pipe 85 led out from the pre-storage tank 5 and a pipe 91 led out from the external storage tank 6 described later. Has been. The aeration treatment liquid stored in the aging unit 4 b is sent to the pre-storage tank 5 or the external storage tank 6.
All the elements constituting the second aging tank are made of known materials.
[0058]
The first aging tank 3 and the second aging tank 4 described above use an air supply device to supply the aeration treatment liquid that has been subjected to the aeration treatment in the first aeration treatment tank 1 and the second aeration treatment tank 2 to have predetermined characteristics. By supplying air and performing an aeration process in an auxiliary manner, it is stored in a state having predetermined characteristics.
[0059]
Next, the front storage tank 5 will be described. As shown in FIG. 4, the box body 81 is partitioned by the partition wall 82 so that the excrement fluid can move through the respective front reservoirs 5a and 5b. An inlet 83 is installed at the top of the front reservoir 5a, a mixer 84 is installed at the bottom of the front reservoir 5a, a pipe 85 is disposed above the front reservoir 5b, and a pump 86 is disposed at the bottom of the front reservoir 5b. A heating pipe 87 is disposed at the bottom of the front reservoirs 5a and 5b. Inside the box 81, a pH sensor 241, a temperature sensor 242, and a level sensor 243 are disposed. Further, the outside of the box 81 is covered with a heat insulating material 88.
[0060]
The partition wall 82 has a plate shape, and partitions the box 81 into the front storage portions 5a and 5b. The partition wall 82 has a plurality of holes so that the excrement fluid can move between the front reservoirs 5a and 5b.
[0061]
The input port 83 is formed in the upper part of the front storage part 5 a, and the manure fluid separated from the liquid is supplied into the front storage tank 5.
The mixer 84 is installed in the pre-reservoir 5a and agitates the manure fluid in the pre-reservoir 5. One end of the pipe 85 is connected to the upper portion of the front reservoir 5b, and the other end is led out of the box 81 as shown in FIG. 1, and is connected to the second through the valves 128, 130, and 131. The pipe 69 b of the pump 69 of the aging tank 4 and the pipe 92 b of the pump 92 of the external storage tank 6 described later are connected via valves 131 and 133. Thereby, the aeration processing liquid stored in the aging part 4 b of the second aging tank 4 is selectively sent to the front storage tank 5. Further, the aeration treatment liquid stored in the external storage tank 6 is also selectively sent to the front storage tank 5.
[0062]
The pump 86 is composed of a pump part 86a and a pipe 86b. One end of the pipe 86b is connected to the pump part 86a, and the other end is led out of the box 81 as shown in FIG. It is connected to the pipe 12 a of the first aeration treatment tank 1 via valves 112 and 134. Thereby, the manure fluid thrown into the front storage tank 5 is sent to the first aeration treatment tank 1.
[0063]
The heating pipe 87 has the same configuration as the heating pipes 61 and 75 described above. The excrement fluid in the front storage tank 5 can be heated by the heating pipe 87.
[0064]
Inside the box 81, a pH sensor 241, a temperature sensor 242, and a level sensor 243 that are suspended from the upper part of the box 81 are arranged, and the values measured by each are output to the controller 8. The position where the pH sensor 241, the temperature sensor 242, and the level sensor 243 are disposed can be freely changed as long as it is a place where the pH value, temperature, and volume of the excrement fluid in the front storage tank 5 can be measured. it can.
[0065]
The partition wall 82, the charging port 83, the mixer 84, the pipe 85, the pump 86, the heating pipe 87, and the heat insulating material 88 described above are made of known materials.
[0066]
Next, the external storage tank 6 will be described. The external storage tank 6 is composed of a known tank 90, and a pipe 91 is disposed in the upper part thereof, and a pump 92 is disposed in the lower part thereof.
As shown in FIG. 1, the pipe 91 is connected to the pipe 69 a of the second aging tank 4 and stores the aeration treatment liquid sent from the pump 69.
Further, the pump 92 including the pump portion 92a and the pipe 92b is connected to the pipe 69a and the pipe 85 as shown in FIG. As a result, the aeration treatment liquid stored in the external storage tank 6 is selectively delivered to the second aging tank 4 or the pre-storage tank 5.
[0067]
Next, the drain tank 7 will be described. As shown in FIG. 1, the drain tank 7 is composed of a known tank 95, and a pipe 96 connected to a pump 98 is disposed above the tank 95. A pump portion 97a and a pipe 97b are disposed above the tank 95. A pump 97 is provided. Each element constituting the drain tank 7 is made of a known material.
[0068]
The pipe 96 is connected to the drain pipe 21 of the first aeration treatment tank 1 and the drain pipe 43 of the second aeration treatment tank 2 via valves 135 and 136 and a pump 98, and the first aeration treatment tank 1 and the second aeration treatment tank 1. Precipitate retained at the bottom of the aeration treatment tank 2 is sent to the tank 97 by the pump 98.
[0069]
The pipe 97 b is led out of the drain tank 7 and is connected to the pipe 12 a of the first aeration treatment tank 1 through the valve 111. As a result, the supernatant fluid component stored in the tank 95 is sent to the first aeration treatment tank 1 and subjected to the aeration process.
[0070]
Next, the controller 8 will be described. As shown in FIG. 1, the controller 8 includes motors 12d, 33d, aerators 16, 38, mixers 18, 40, pumps 19, 20, 41, 42, 54, 55, 68, 69, 86, 92, 97, valves. 111 to 141 are electrically connected to pH sensors 201, 211, 221, 222, 231, 232, pressure sensors 202, 212, temperature sensors 203, 213, 223, 224, 233, 234, 242 Each control is performed based on this.
The controller 8 also controls the compressor 101, the tank 102, and the boiler 103.
The controller 8 and the valves 111 to 141 are made of known materials.
[0071]
The configuration of the controller 8 is shown in FIG. The controller 8 is electrically connected to a control unit 8a that controls the operation of the entire controller 8 and a memory 8b that stores programs and data related to the operation of the control unit 8a in advance and stores each data received by the I / F 8c. I / F 8c that receives signals from pH sensors, pressure sensors, temperature sensors, and level sensors, and detects operation inputs from operators, and sends and receives signals to and from motors, aerators, mixers, pumps, valves, etc. The operation unit 8d that outputs to the control unit 8a and the display unit 8e that outputs the operating state of the excrement disposal apparatus and the like.
[0072]
Based on a program stored in the memory 8b in advance, the control unit 8a refers to data received by the I / F 8c from each sensor such as a pH sensor, a pressure sensor, a temperature sensor, and a level sensor, and a motor, an aerator, The entire manure processing apparatus is controlled by transmitting / receiving signals to / from an air supply apparatus, a mixer, a pump, a valve, and the like.
The memory 8b stores in advance data such as a program for the control unit 8a to control the entire manure processing apparatus and reference values of each sensor, and data received from the pH sensor, pressure sensor, temperature sensor, and level sensor, A history such as the operating status of the excrement disposal apparatus is stored.
The I / F 8c transmits and receives signals to and from electrically connected motors, aerators, mixers, pumps, valves, and the like based on instructions from the control unit 8a, and also includes pH sensors, pressure sensors, temperature sensors, and level sensors. The data such as the measured values measured by the respective sensors are received.
The operation unit 8d includes a keyboard, a mouse, a touch panel, buttons, and the like, detects an operation input by the operator, and outputs it to the control unit 8a.
The display unit 8e is composed of a screen display device such as a CRT display, and displays the operating status of the feces and urine processing device, information on each processing tank, and the like.
[0073]
By having the above-described configuration, the controller 8 can control all the operations related to the aeration process of the excrement fluid performed in the aeration processing apparatus of the present invention.
[0074]
Next, the control device 9 will be described. As shown in FIG. 1, the control device 9 includes a compressor 101, a tank 102, a boiler 103, an air supply port 105, a fluid output port 106, and a fluid input port 107. The control device 9 performs the operation of the excrement disposal apparatus of the present invention and the control associated therewith based on the instruction of the controller 8.
The compressor 101, the tank 102, and the boiler 103 are made of known materials.
The boiler 103 may be configured by an electric water heater.
[0075]
The air supply port 105 is connected to the air supply devices 17, 39, 60, and 74, and supplies air indicated by reference numeral 5 in FIGS. 1 to 4 from the compressor 101 based on instructions from the controller 8.
The fluid output port 106 is connected to one end of the heating pipes 23, 45, 61, 75, and 87. Each of the fluid output ports 106 is designated by reference numeral 6 in FIGS. Output fluid such as heated water and antifreeze. The fluid input port 107 is connected to one end of the heating pipes 23, 45, 61, 75, and 87, and based on instructions from the controller 8, a fluid output indicated by reference numeral 7 in FIGS. Fluid such as water or antifreeze liquid output from the port 106 is collected.
[0076]
Next, a method for controlling the aeration treatment tank of the excrement disposal apparatus of the present invention will be described with reference to FIGS.
The excreta fluid introduced into the pre-reservoir 5 is sent to the first aeration tank 1. In the first aeration treatment tank 1, the aeration process is performed by a method as shown in the flowchart of FIG. In the present embodiment, description will be made using the pressure inside the aeration treatment tank and the pH value of the excrement fluid inside the aeration treatment tank as parameters for controlling the aeration treatment in the aeration treatment tank.
[0077]
First, the controller 8 detects whether or not there is a predetermined amount of fecal fluid in the first aeration treatment tank 1 by the level sensor 204 (step S1). When the excrement fluid in the first aeration treatment tank 1 is less than the predetermined amount (step S1: NO), the controller 8 drives the pump 86 of the pre-reservoir 5 and the valves 111, 112, 113, 114, By adjusting 134, 140, 141, the excrement fluid in the front storage tank 5 is supplied to the first aeration treatment tank 1 (step S7).
When the excrement fluid in the first aeration treatment tank 1 satisfies a predetermined amount (step S1: YES), the controller 8 drives the aerator 16 and the air supply device 17 that realize the air supply means (step S2). Aeration treatment is performed on the excreta fluid.
[0078]
If the pressure inside the aeration treatment tank becomes too high due to the air output from the air supply means and the gas generated by the oxidative fermentation of microorganisms, the aeration treatment tank may rupture, which is dangerous. If air is not sufficiently supplied into the excrement fluid by the air supply means, the oxidation fermentation process of microorganisms in the excrement fluid is not promoted, and the aeration process cannot be sufficiently performed on the excrement fluid.
Therefore, the controller 8a determines that the pressure (P) in the first aeration treatment tank 1 is within a predetermined range (P ₀₂ <P <P ₀₁ ), and the pH value of the excreta fluid in the first aeration treatment tank 1 is predetermined. Each part of the first aeration treatment tank 1 is controlled so as to continue the aeration process until the value (S1) is exceeded.
That is, when the pressure inside the first aeration treatment tank 1 exceeds P ₀₁ (the upper limit value of the pressure) (step S3: NO), the control unit 8a is too high in the first aeration treatment tank 1. The aerator 16 and the air supply device 17 are stopped (step S8) to prevent the internal pressure of the first aeration treatment tank 1 from rising further. In addition, when the pressure inside the first aeration tank 1 is lower than P ₀₂ (the lower limit value of pressure) (step S4: NO), the controller 8 has sufficiently performed the oxidative fermentation treatment of microorganisms in the excrement fluid. Therefore, when the aerator 16 and the air supply device 17 are stopped, the aerator 16 and the air supply device 17 are driven. When the aerator 16 and the air supply device 17 are driven, the aeration is continued. The lator 16 and the air supply device 17 are driven (step S9).
Reference values such as P ₀₁ , P ₀₂ and S1 are recorded in the memory 8b.
[0079]
The control unit 8a refers to the pH sensor 201 in the state where the pressure inside the first aeration treatment tank 1 is within a predetermined range (step S3, 4: YES), and the pH of the excrement fluid inside the first aeration treatment tank 1 The aeration process is performed until the value reaches a predetermined value (step S5: NO). When the pH value of the excreta fluid in the first aeration treatment tank 1 reaches a predetermined value (step S5: YES), the control unit 8a drives the pump 20 and adjusts the valves 115 and 117. The excrement fluid in the first aeration treatment tank 1 that has been subjected to the aeration process until a predetermined pH value is delivered to the second aeration treatment tank by a predetermined amount.
In addition, after confirming that the pH sensor 201 has measured that the pH value of the excreta fluid in the first aeration treatment tank 1 has reached a predetermined value for a predetermined number of times or for a predetermined time, It is also possible to send manure fluid to the aeration treatment tank 2.
[0080]
The excrement fluid sent to the second aeration treatment tank 2 is subjected to an aeration process until reaching a predetermined pH value by a control method similar to that described above by the control unit 8a. Then, the manure fluid that has been subjected to the aeration process in the second aeration treatment tank 2 until reaching a predetermined pH value is sent to the first aging tank 3 in a fixed amount.
[0081]
In addition, the parameter used for controlling the aeration process in the aeration process tank can also use the temperature of the excreta fluid in the aeration process tank instead of the pressure described above. In this case, an air supply means such as an aerator and an air supply device and a heating device such as a heating pipe are controlled so that the temperature inside the aeration treatment tank falls within a predetermined range (for example, about 50 to 53 ° C.). For example, the temperature is set so that the aeration process is performed within the predetermined range (T ₀₂ <T <T ₀₁ ) until the pH value of the excreta fluid reaches a predetermined value (S1). Is higher than the upper limit value (T ₀₁ ), the air supply means is stopped, and when the temperature is lower than the lower limit value (T ₀₂ ), the air supply means and the heating device are driven in the cold. In this way, it is possible to control the aeration processing in the aeration processing tank.
[0082]
Further, the parameters used for controlling the aeration treatment in the aeration treatment tank can be used in combination with the pressure, temperature and pH values described above. In this case, heating of the air supply means such as the aerator and the air supply device and the heating pipe so that the pressure and temperature inside the aeration tank are within the predetermined range until the pH value of the excreta fluid reaches the predetermined value. The device may be controlled. As for a specific method, the case where pressure is used for the above-described parameter and the case where temperature is used may be combined, and the description thereof will be omitted.
[0083]
Moreover, in this Embodiment, the parameter used for controlling the aeration process in an aeration processing tank can also use a BOD value instead of the pH value mentioned above. This BOD (Biochemical Oxygen Demand / Biochemical Oxygen Demand) value represents the amount of oxygen consumed because organic pollutants in water are biochemically oxidized by aerobic microorganisms in water. In this case, a sensor for detecting the BOD value is provided inside the aeration treatment tank, and the aeration unit is configured so that the pressure or temperature in the aeration treatment tank or the pressure and temperature are within a predetermined range until the BOD value reaches a predetermined value. What is necessary is just to make it control air supply means, such as an air supply apparatus, and heating apparatuses, such as a heating pipe. As for a specific method, the predetermined pH value in step S5 in FIG. 6 may be replaced with a predetermined BOD value, and detailed description thereof will be omitted.
[0084]
In the present embodiment, as a parameter used for controlling the aeration process in the aeration tank, a COD value can be used instead of the pH value described above. This COD (Chemical Oxygen Demand / Chemical Oxygen Demand) value represents the amount of oxygen consumed when organic pollutants are mainly treated with oxidizing substances in water. In this case, a sensor for detecting the COD value is provided inside the aeration treatment tank, and the aeration unit is configured so that the pressure or temperature inside the aeration treatment tank or the pressure and temperature are within a predetermined range until the COD value reaches a predetermined value. What is necessary is just to make it control air supply means, such as an air supply apparatus, and heating apparatuses, such as a heating pipe. As for a specific method, the predetermined pH value in step S5 in FIG. 6 may be replaced with a predetermined COD value, and thus detailed description thereof is omitted.
[0085]
Moreover, in this Embodiment, the electrical conductivity can also be used for the parameter used for controlling the aeration process in an aeration processing tank instead of the pH value mentioned above. This electrical conductivity represents the turbidity of impurities in the excreta fluid. In this case, a sensor for detecting the electrical conductivity of manure fluid is provided inside the aeration treatment tank, and the pressure or temperature inside the aeration treatment tank or the pressure and temperature are within a predetermined range until the electrical conductivity reaches a predetermined value. What is necessary is just to control heating apparatuses, such as an air supply means, such as an aerator and an air supply apparatus, and a heating pipe so that it may be settled. As for a specific method, the predetermined pH value in step S5 in FIG. 6 may be replaced with a predetermined electric conductivity, and thus detailed description thereof is omitted.
[0086]
In addition, the control unit 8a includes a measurement value obtained by a parameter value measurement unit such as a pH sensor, a pressure sensor, a temperature sensor, a BOD value sensor, a COD value sensor, and an electrical conductivity sensor, and a reference recorded in the memory 8b. It is also possible to compare the values and calculate a difference, and to control the aeration tank based on this difference. The controller 8a can smoothly control the aeration processing in the aeration processing tank by adjusting the amount of air supplied by the air supply means according to the degree of difference.
[0087]
In the memory 8b, a plurality of reference values corresponding to the measurement values obtained by the parameter value measurement unit such as a pH sensor, a pressure sensor, a temperature sensor, a BOD value sensor, a COD value sensor, and an electrical conductivity sensor are recorded. The control unit 8a multiplies the measurement value obtained by the parameter value measurement unit such as a pH sensor, pressure sensor, temperature sensor, BOD value sensor, COD value sensor, and electrical conductivity sensor by a reference value. It is also possible to perform correction based on this corrected value. As a result, the manure processing apparatus according to the present embodiment adjusts the amount of air supplied by the air supply means, the driving time, etc. according to the state of the manure fluid in the aeration treatment tank, and the manure fluid in all states It is possible to effectively perform the aeration process.
[0088]
Further, the reference values recorded in the memory 8b are different from each other at the time obtained by each parameter value measuring unit such as a pH sensor, a pressure sensor, a temperature sensor, a BOD value sensor, a COD value sensor, and an electrical conductivity sensor. Correction can be made based on an average value of a plurality of measured values. The measurement value measured by the parameter value measurement unit depends on the characteristics of the manure fluid and the state of the aeration treatment in the aeration treatment tank, depending on the measurement time, that is, the state of the manure fluid near the sensor of the parameter value measurement unit at the time of measurement. May be different. Therefore, the control unit 8a calculates an average value of the measurement values at different time points, and controls the air supply unit and the like based on the average value. The memory 8b records measurement values at different times measured by the parameter value measurement unit, and the control unit 8a corrects the reference value based on the measurement values recorded at different times at the memory 8b. .
Thereby, the excrement processing device of the present invention can perform the stable aeration processing to the whole excrement fluid.
[0089]
Further, the shower 15 outputs the excrement fluid at the bottom of the first aeration treatment tank 1 from above the liquid level of the first aeration treatment tank 1 and brings it into contact with air, thereby promoting oxidation fermentation of the excrement fluid. Similarly to the lator 16 and the air supply device 17, it can be driven as an air supply means. As a result, the excreta fluid is effectively aerated. Needless to say, in the second aeration treatment tank 2, the shower can be driven as air supply means.
[0090]
Next, the operation of the manure processing apparatus of the present invention will be described.
Manure excreted by livestock is separated into a solid component and a liquid component by a commonly used solid-liquid separator. Next, the liquid component (feces and urine fluid) is introduced into the front reservoir 5 a inside the box 48 from the inlet 83 provided in the upper part of the front reservoir 5. The pH value of the excrement fluid put into the pre-reservoir 5 is about 5.0 to 7.0.
[0091]
Since the excrement fluid put into the pre-reservoir 5a has just been separated into solid and liquid, the residual solid matter is mixed in the excrement fluid and has high viscosity. Therefore, the manure fluid charged into the front reservoir 5 a is agitated by the mixer 84. If it does in this way, the liquid component and residual solid-liquid thing in manure fluid will be stirred, and viscosity will become low, and the subsequent aeration process will be performed effectively.
Further, since the partition wall 82 has the hole 82a, the excrement fluid passes through the hole 82a when being stirred by the mixer 84, and is effective by moving between the front storage part 5a and the front storage part 5b. To be stirred.
[0092]
As described above, the excrement fluid introduced into the pre-storage tank 5 and stirred by the mixer 84 is sent to the excrement fluid diffusion part 12 of the first aeration treatment tank 1 by the pump 86 via the pipe 86b and the pipe 12a. Is done.
[0093]
The excrement fluid delivered from the pre-reservoir 5 passes through the inside of the intake pipe 12b from the pipe 12a of the excrement fluid diffusion part 12, and is discharged from the lower end part of the intake pipe 12b toward the diffusion plate 12c. The excrement fluid colliding with the diffusion plate 12c rotated by the motor 12d is effectively diffused inside the aeration processing unit 1a. Thereby, it can prevent that the excrement fluid discharged | emitted in the inside of the 1st aeration processing tank 1 accumulates in one place, and the entire excrement fluid is effectively aerated.
[0094]
The excrement fluid diffused into the aeration processing unit 1a by the excrement fluid diffusion unit 12 is stored in the bottom of the aeration processing unit 1a, and the aeration unit 16 performs the aeration process. At this time, air is supplementarily supplied into the excrement fluid by the air supply device 17, thereby improving the efficiency of the aeration process of the excrement fluid.
[0095]
When an aeration process is performed on the excrement fluid, the excrement fluid generates a large amount of bubbles. The bubbles pass through the cylindrical guide portions 13a and 14a of the output devices 13 and 14 to reach the defoaming portions 13c and 14c, and are defoamed by the defoaming portions 13c and 14c to become liquid, and the outlet portions 13d and 14d It passes through the pipes 13g and 14g and is output to the defoaming water tank 25.
[0096]
The excreta fluid sent from the pipes 13g and 14g to the defoaming water tank 25 is aerated from the pipe 25a provided at one end to the bottom of the defoaming water tank 25 or from the pipe 25c connected to the pump 25b. It discharges | emits to the process part 1a bottom part, and an aeration process is performed in the aeration process part 1a.
Foam generated by the aeration processing of the excrement fluid in the aeration processing unit 1 a is output to the defoaming water tank 25 by the output devices 13 and 14. Thereby, the excreta fluid in the aeration processing unit 1a circulates in the aeration processing unit 1a and is continuously subjected to aeration processing.
In addition, when more excrement fluid than the predetermined amount of the defoaming water tank 25 is sent to the defoaming water tank 25, the excessive excrement fluid is supplied from the pipe 25d connected to the side wall of the antifoaming water tank 25 to the first. It is sent to the aging tank 3.
[0097]
The excrement fluid accumulated at the bottom of the aeration processing unit 1a passes through the gap formed by the lower end of the partition wall 11 and the box 10 by the mixer 18 and enters the circulation unit 1b. The excrement fluid that has entered the circulation part 1b passes through the pipe 19b by the pump 19 through the pipe 12a, is sent again to the excrement fluid diffusion part 12, and is diffused inside the aeration processing part 1a. Thereby, the whole excrement fluid is effectively aerated.
The excrement fluid that has entered the circulation section 1b is sent to the shower 15 via the pipe 20b by the pump 20, discharged into the aeration processing section 1a, and circulated in the first aeration processing tank 1 to perform the aeration process. Applied.
[0098]
The excrement fluid in the first aeration treatment tank 1 is aerated by the method described above until the pH value becomes about 7.5 to 8.5, and then passes through the pipe 20b and the pipe 47 by the pump 20. Then, it is guided to the bottom of the aeration treatment unit 2 a of the second aeration treatment tank 2 or the excrement fluid diffusion unit 33.
[0099]
In addition, the excrement fluid in the 1st aeration processing tank 1 passes along the pipe 53 via the pipe 19b and the pipe 86b by the pump 19 as needed, and is sent to the 1st maturing tank 3. By doing in this way, it becomes possible to perform the aeration process of the double amount of feces and urine fluids in both the first aeration treatment tank 1 and the second aeration treatment tank 2. Further, since the excrement fluid in the first aeration treatment tank 1 can be sent to the first aging tank 3 without going through the second aeration treatment tank, the inside of the second aeration treatment tank 2 is emptied. Maintenance can be done.
[0100]
The deposits accumulated at the bottom of the aeration processing unit 1a are sent to the drain tank 7 through the drain pipe 21.
Further, the supernatant fluid component stored in the drain tank 7 is sent to the first aeration tank 1 by the pump 97 and subjected to the aeration process.
The excrement fluid discharged to the aeration processing unit 2a of the second aeration processing tank 2 by the pump 20 is subjected to the same aeration process as that of the first aeration processing tank 1.
Of the excrement fluid that has entered the output unit 2b through the gap formed by the lower end of the partition wall 32 and the box 31, the excrement fluid below the output unit 2b is sent to the excrement fluid diffusion unit 33 by the pump 42. It is diffused from the fluid diffusion part 33 into the aeration treatment part 2a or sent to the excrement fluid diffusion part 12 of the first aeration treatment tank 1, and circulates through the first aeration treatment tank 1 and the second aeration treatment tank 2 continuously. An aeration process is performed. Thereby, the aeration process liquid which has a predetermined characteristic can be obtained.
[0102]
Of the excrement fluid that has entered the output unit 2 b through the gap formed by the lower end of the partition wall 32 and the box 31, the excrement fluid close to the liquid level of the output unit 2 b is sent to the shower 37 by the pump 41. It is discharged into the second aeration treatment tank 2 and circulates in the second aeration treatment tank 2 to effectively perform the aeration process.
When the pH value becomes about 8.3 to 8.5, the excrement fluid in the second aeration treatment tank 2 is sent from the pipe 53 to the aging part 3a of the first aging tank 3 via the pipe 41b by the pump 41. The
[0103]
In addition, the excrement processing apparatus of this invention can send the excrement fluid of the 2nd aeration processing tank 2 to the 1st aeration processing tank 1 with the pipe 22 as needed. Thereby, the manure processing apparatus of the present invention can always secure the manure fluid to be processed in the aeration treatment tank even when the amount of manure fluid to be introduced is small, and can prevent the bacteria in the manure fluid from being killed.
[0104]
When the aeration treatment is performed in the first aeration treatment tank 1 and the second aeration treatment tank 2, heat is released when the microorganisms undergo oxidative fermentation, and the temperature of the excreta fluid at that time becomes about 50 to 53 ° C. When aeration processing is performed under cold conditions, the excrement fluid can be effectively aerated by heating the inside of the aeration tank with the heating pipes 23 and 45 in order to promote oxidative fermentation of microorganisms.
[0105]
The aeration treatment liquid sent to the first aging tank 3 via the pipe 41b and the pipe 53 by the pump 41 and the aeration treatment liquid sent from the defoaming water tanks 25 and 36 by the pipes 25d and 36d to the aging unit 3a. Stored. The aeration treatment liquid stored in the aging unit 3a is supplied with air by the air supply device 60 as necessary, so that the bacteria in the aeration treatment liquid are prevented from being killed and predetermined characteristics of the aeration treatment liquid, that is, predetermined It can be maintained in a state having a pH value of. Further, the aeration treatment liquid stored in the aging unit 3a can be circulated in the aging unit 3a by being discharged from the shower 56 to the aging unit 3a by the pump 54 as necessary. This also prevents the bacteria in the aeration treatment liquid from being killed and can maintain the predetermined characteristics of the aeration treatment liquid.
[0106]
The aeration treatment liquid stored in the aging unit 3 a for a predetermined period is sent to the aging unit 3 b by the pump 54. The aeration treatment liquid sent to the aging unit 3b is stored in the aging unit 3b in a state having predetermined characteristics like the aging unit 3a, and is sent to the aging unit 4a of the second aging tank. Similarly, the aging units 4a and 4b are also stored in the same manner as the aging unit 3a, and finally the aeration treatment liquid is output from the aging unit 4b to the external storage tank 6 in a state having predetermined characteristics, as liquid fertilizer. Used for cultivation of cultivated crops.
Further, the aeration treatment liquid is sent to the pre-reservoir 5 by the pump 69 as necessary. As a result, the pre-reservoir 5 can always secure the excrement fluid even when the amount of the excrement fluid input is small, and can prevent the bacteria in the excrement fluid from being killed.
[0107]
In the present embodiment, for example, when manure processing is performed on 100 milking cows, the milking cow discharges 60 kg of manure per head (breakdown is 40 kg of shit and 20 kg of urine), and this manure is separated into solid and liquid. When solid-liquid separation is performed by the apparatus, 50 kg of manure fluid is obtained per milking cow, and therefore 5 t (5 m ³ ) of manure fluid is discharged per day for 100 milking cows. In this case, when the capacities of the first aeration treatment tank 1 and the second aeration treatment tank 2 are set to 15 m ³ , and the capacities of the first aging tank 3, the second aging tank 4 and the pre-storage tank 5 are set to 10 m ³ , The manure processing apparatus transfers the manure fluid to the next stage processing apparatus by 5 m ³ per day, and as a result, the aeration process of the manure fluid for one day is completed in a short period of about 6 days.
As described above, when the manure fluid is first introduced into the pre-reservoir 5 and after 6 days, when 5 m ³ of manure fluid is introduced into the pre-reservoir 5 every day, 5 m ³ of the aeration treatment liquid is added to the second aging tank every day. 4, the aeration process of the excrement fluid can be continuously performed.
[0108]
Next, a modification of the first aeration treatment tank 1 is shown in FIG. Elements equivalent to those in the first aeration treatment tank 1 shown in FIG. 5 are denoted by the same reference numerals and names, and description thereof will be omitted as appropriate.
The first aeration treatment tank 1 shown in FIG. 5 is not provided with the defoaming water tank 25 provided in the first aeration treatment tank 1 shown in FIG. The pipes 13g and 14g of the defoaming devices 13 and 14 are connected to the shower 15 via the valves 12145 and 147 via the pipe 12a and the valves 144 and 146 of the excrement fluid diffusing unit 12. As a result, the defoamed water output from the defoaming devices 13 and 14 is diffused from the excrement fluid diffusing unit 12 or the shower 15 into the aeration processing unit 1a. Even with such a configuration, the excrement disposal apparatus of the present invention can efficiently perform the aeration process on the excrement fluid.
[0109]
In FIG. 5, the aerator 16 is provided with a pipe 16b. The pipe 16b is connected to the pipe 86b of the front storage tank 5. With this configuration, the excreta fluid stored in the pre-reservoir 5 indicated by reference numeral (1) is sent to the aerator 16 and is effectively agitated by the aerator 16. In addition, the 1st aeration processing tank 1 shown in FIG. 2 can also be set as the same structure.
[0110]
The defoamed water output from the defoaming devices 13 and 14 is not only output to its own aeration treatment tank, but also output to other tanks such as the diffusion section 33 or the shower 37 of the second aeration treatment tank 2. You can also
Moreover, the defoaming water output from the defoaming apparatuses 13 and 14 can be dropped directly into the tank from the upper part of the tank without using a diffusion part or a shower. This can be performed in the same manner when defoaming water is output to another processing tank.
[0111]
In the excreta treatment apparatus of the present invention, each of the first aeration treatment tank 1, the second aeration treatment tank 2, the first aging tank 3, the second aging tank 4, and the pre-storage tank 5 is constituted by a stainless steel unit structure. . As a result, each unit is made in advance in the factory, and at the installation site, it is only necessary to install the unit and connect the units, and the construction period can be significantly shortened compared to the conventional method.
[0112]
In the present embodiment, the first aeration treatment tank 1, the second aeration treatment tank 2, the first aging tank 3, the second aging tank 4, the pre-storage tank 5, the external storage tank 6, the drain tank 7, the controller 8 and the control. Although composed of the apparatus 9, the number and capacity of the treatment tanks, the order of the aeration process of the excrement treatment and the layout of each tank are not limited to this, and the number of heads, the installation location, etc. can be freely modified as necessary, Can be changed.
[0113]
In the present embodiment, the pressure and the pH value are described as parameters for controlling the aeration treatment tank. However, the parameters for controlling the aeration treatment tank are not limited thereto, and for example, the temperature, the BOD value, the COD value, and the The electrical conductivity can be freely changed as necessary. In addition, pressure, pH value, temperature, BOD value, COD value, electrical conductivity, and the like can be used in appropriate combinations as parameters for controlling the aeration treatment tank. These can be realized by providing a sensor that detects the temperature, BOD value, COD value, and electrical conductivity electrically connected to the controller 8 inside the aeration treatment tank.
Thereby, the aeration process excrement fluid which has a more detailed characteristic can be obtained.
[0114]
【The invention's effect】
As is clear from the above description, according to the present invention, the first and second aeration treatment tanks for aeration treatment of manure fluid and the air for aeration treatment in the first and second aeration treatment tanks, respectively. The first and second air supply means to be supplied, the parameter value measuring unit for measuring the aeration process state of each of the first and second aeration process tanks, and the aeration process state of the first and second aeration process tanks are controlled. A control unit, and the control unit controls the air supply means so that the parameter values of the first and second aeration tanks are respectively desired values based on the measured values obtained by the parameter value measuring unit. By driving and controlling the aeration processing state of the first and second aeration processing tanks, it is possible to perform the aeration processing on manure fluid more efficiently than before and obtain an aeration processing manure fluid having a predetermined characteristic.
[Brief description of the drawings]
FIG. 1 is a schematic view of a manure processing apparatus of the present invention.
FIG. 2 is a cross-sectional view taken along the line II-II in FIG.
FIG. 3 is a cross-sectional view taken along line III-III in FIG.
4 is a cross-sectional view taken along the line IV-IV in FIG.
FIG. 5 is a view showing a modification of the first aeration treatment tank 1;
6 is a block diagram showing a configuration of a controller 8. FIG.
FIG. 7 is a flowchart showing a control method of the controller 8;
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 ... 1st aeration processing tank, 1a ... Aeration processing part, 1b ... Circulation part, 2 ... 2nd aeration processing tank, 2a ... Aeration processing part, 2b ... Circulation part, 3 ... 1st aging tank, 3a, 3b ... Aging Parts 4, second aging tank 4 a, 4 b aging section, 5 pre-storage tank, 5 a, 5 b front storage section, 6 external drain tank, 7 drain tank, 8 controller, 8 a controller, 8b ... Memory, 8c ... I / F, 8d ... Operation part, 8e ... Display part, 9 ... Control device, 101 ... Compressor, 102 ... Tank, 103 ... Boiler, 105 ... Air supply port, 106 ... Fluid output port, 107 ... fluid input port, 111-141 ... valve, 201, 211, 221, 222, 231, 232, 241 ... pH sensor, 202, 212 ... pressure sensor, 203, 213, 223, 224, 233, 234, 242 ... temperature Sensors 204, 2 4,225,226,235,236,243 ... level sensor.

Claims (11)

At least one aeration tank for aeration of manure fluid;
An air supply means for supplying air for aeration treatment to the aeration treatment tank;
A parameter value measuring unit arranged inside the aeration treatment tank and measuring the aeration treatment state;
A control unit for controlling the aeration treatment state of the aeration treatment tank ;
At least one defoaming portion disposed at an upper portion of the aeration treatment tank;
Defoaming water supply means for supplying the defoaming water generated from the defoaming part to the aeration treatment tank itself,
Heating means for heating the aeration treatment tank ,
The control unit drives the air supply unit based on the measurement value obtained by the parameter value measurement unit so that the parameter value of the aeration treatment tank becomes a desired value, and the aeration treatment state of the aeration treatment tank A feces and urine treatment apparatus characterized by controlling In the manure processing apparatus of Claim 1,
The aeration treatment tank is composed of first and second aeration treatment tanks, and the sewage treatment apparatus is characterized in that In the manure processing apparatus of Claim 1,
The parameter value is at least one selected from pH value, BOD value, COD value, electrical conductivity, temperature and pressure. In the excrement processing device according to each of claims 1 to 3,
The aeration processing tank has a sending means for sending manure fluid in the aeration processing tank to a subsequent stage. In the excrement processing device according to claim 4,
The controller performs the aeration process until the excrement fluid in the aeration process tank reaches a predetermined pH value, BOD value, COD value, or electrical conductivity, and thereafter, the excrement fluid in the aeration process tank is sent out. A feces and urine treatment apparatus, wherein the aeration treatment state of the aeration treatment tank is controlled so that a fixed amount is output to a subsequent stage by means. In the excrement processing device according to claim 1 or 4,
The control unit stops each of the air supply means when each of the aeration treatment tanks reaches a predetermined pressure. In the manure processing apparatus of Claim 1,
Furthermore, it has a memory that records the reference value corresponding to the parameter value to be measured,
A feces and urine treatment apparatus, wherein the aeration treatment state of the aeration treatment tank is controlled based on a measurement value obtained by the parameter value measurement unit and a reference value recorded in the memory. In the excrement processing device according to claim 7,
The control unit controls based on a difference between the reference value and the measured value. In the excrement processing device according to claim 7,
The control unit corrects the reference value based on the measured value measured by the parameter value measuring unit, and controls based on the corrected value. In the excrement processing device according to claim 9,
The control unit controls the reference value based on an average value of a plurality of measurement values obtained by the parameter value measurement unit. In the excrement processing device according to claim 5,
Furthermore, an input means for inputting manure fluid into the aeration tank is provided,
The input means inputs a same amount of manure fluid from the input means to the aeration tank after a predetermined amount of manure fluid is output from the aeration tank by the output means. .

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