KR200283103Y1 - Apparatus for eradication of starchy - Google Patents

Abstract

The present invention is the first and second and third treatment tank (P, Q, R) formed sequentially on the separated urine storage tank (O) and the separated urine storage tank (O) in the manure solids separation and dehydrator (100) And the aeration machine 11A-1, 11A-2 in the pressure injury treatment tank S formed on the side surface of the third treatment tank R after the treatment by the aeration device and the mist injector formed in each of the treatment tanks. , 11A-3) and the activated carbon layer which is transferred to the filtration apparatus 500 formed on the side of the pressure floatation tank S after being processed by the pressure flotation units 14A-1, 14A-2, and 14A-3. 501 and the sand layer 502, the present invention relates to an oxidized floating pressure starch removal device for processing.

Description

Oxidation injury pressurized starch removal device {Apparatus for eradication of starchy}

The present invention relates to a pressurized starch removal device for oxidative injury of starch (aka sludge), which is a hardly decomposable substance, in detail, in order to treat manure by physical means, solid-liquid separation and high-speed fermentation dehydrator And an oxidative injury pressurized starch removing device including a stirring means, an air supplying means, a bubble removing means, a fog flotation device, and the like so that the treatment process is continuously and automatically performed.

In general, a large amount of manure is inevitably generated in livestock farms, and since the livestock manure contains a lot of water and starch, it is not only causing considerable cost and difficulty in processing, but also decomposing organic matter in the livestock manure. Severe odor was generated and other pathogens grew naturally, which greatly affected hygiene. This is the biggest issue of wastewater treatment and remains a challenge.

The characteristics of starch, the so-called high turbidity, changes in material are changed frequently by temperature and humidity, and various indegradable substances including organic materials, inorganic materials, proteins, and fibers, which are difficult to decompose. It is true that they have felt a great deal of difficulty in their creation.

In addition, sedimentation induced frequent blockages of aeration tanks and browers, resulting in the inability to treat manure.

There are various methods of treating livestock manure, but until now, it has been generally applied without fertilization or fertilization without manure, active sludge treatment methods utilizing water treatment facilities, and high-speed fermentation by adding moisture regulators to compost or compost. High-speed fermentation methods that are used as raw materials are widely applied.

However, when manure is applied as compost without processing, there is a problem of contaminating the surrounding environment as well as groundwater due to the generation of leachate during rainy weather, and the problem of deterioration of crops and soils as heavy metals in livestock manure are fertilized without filtration. Is holding.

In addition, even in the case of activated sludge treatment method, the treatment facility cost and maintenance cost is excessively consumed, which is a problem that is impossible in small and medium farms.

Fast fermentation methods are also difficult to implement in each livestock farm due to high maintenance costs.

In order to solve this problem, recently, a method of reducing weight by a method similar to the present invention or drying using external energy has been proposed.

Since the conventional techniques are based on biological treatment of manure treatment, there is a lack of sufficient air supply for microbial activation or the design of an air supply process that meets the required reduction rate is poor, thus reaching 10 to 30% reduction rate. There is a drawback that it is difficult to reduce the manure because it does not take the unnecessary device and does not smoothly remove the bubbles that are hindered during processing.

In order to solve the above problems, the present invention is to change the manure treatment from biological manure treatment to physicochemical treatment, the patent application No. 99- of May 12, 1999, the invention or filed by the applicant No. 17038 Design of the method and apparatus for treating livestock waste, and Patent No. 306228 Name of the invention; The name of the invention; Urine fermentation mist sprayer, Patent No. 10-2001-306224 Oxidation floater is improved, and after separating sludge and urine by solid-liquid separation and high-speed fermentation dehydrator, aeration and aeration machine used as a mixing / stirring device And evaporate the water and microorganisms contained in the foam by using a bubble removing means, and the method of treating livestock manure is performed continuously and automatically by using a mechanical device. It is a technical task of the present invention to provide an apparatus for removing oxidized injury starch that can be processed in a short time and reuses the treated manure.

Figure 1 is a detailed view of the oxidative injury pressurized starch removal device of the present invention

Figure 2 is a detailed diagram of the manure solids separation and high speed dehydrator of the present invention

Figure 3 is a detailed view of the high speed dehydrator of the present invention

4 is a detailed view of the vibrator of the present invention

5 is a detailed view of the aeration device of the present invention

6 is a detailed view of the pressurized floating starch remover of the present invention

7 is a detailed view of the pressure buoy of the present invention

8 is a detailed view of the breaker of the present invention

9 is a detailed view of the mist float spreader of the present invention

10 is another detailed view of the mist float spreader of the present invention

11 is a detailed view of the filtration device of the present invention

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

Transfer pump (2A), sensor (3), transfer pipe (4), aeration device (5), aeration pump (5-1), aeration circulation pipe (6), arc engine (7), starch transfer pipe (9), Circulation through hole (10), overpass pipe (10-1, 10-2), lower overpass pipe (10-3), breaker (11A-1, 11A-2, 11A-3), fog floater (14) ), Solid outlet (13), pressurizer 14A-1, first pressurizer 14A-1, second pressurizer 14A-2, third pressurizer 14A- 3), the pressure injury induction pipe (14-1), the pressure injury cross pipe (14-2), the lower pressure injury cross pipe (14-3), the pressure injury double pipe (14-4), cover (14-5), Drain pipe (drain) 16, aeration motor suction pipe 17, discharge pipe 18, aeration belt connection port (46.46`), aeration shaft 47, aeration impeller 48, air injection pipe 49, suction port ( 50), bushings (51, 51 '), broo (52), discharge pipes (54, 54'), breaker belt upper connector (25), breaker belt lower connector (26), breaker shaft (27), Aerator 2nd impeller (27 '), Aerator 1st impeller (28), bearing (29), motor stopper (30), aeration cylinder (31), manure solids separation and high speed Dehydrator 100, vibrator 101, diaphragm screen 102, hydraulic injector 103, gas generating screw 104, gas ejection pipe and fan 105, vibration height 106, discharge water pipe 107, Screw-type high speed dehydrator 108, raw water pipe 109, manure injection pipe 110, gas generating screw motor 111, solid-liquid dehydration storage tank 112, gas removal storage tank 113, vibration motor 114, dehydrator Motor 115, Tras 116, Case 117, 121 Inlet, 122 Mechanical Seal, 123 Vibratory Rubber Plate, 124 Blade, 125 Outer Network, 126 Sludge Outlet Motors 201 and 208, bearings 202 and 202 ', lidena 203, wing shaft 204, wing 205, oxygen supply pipe 206, fog float 207, connecting portion 209, inlet ( 210), outlet 211, pressurized floating starch remover 400A, filtration device 500, activated carbon layer 501, sand layer 502 A: bubble moving tube, B: air moving tube, C: bubble and air contact portion, O: separate urine storage tank, P: first treatment tank, Q: second treatment tank, R: third treatment tank, S: pressure injury treatment tank

The present invention for achieving the above object is the invention patent (patent 0306228 livestock waste treatment method and apparatus) of 1999 developed by the person has been to remove only a small amount of starch through a scavenger by oxidizing the sludge, Since then, R & D has been continuously conducted. It has been filed with the commercialization of starch removal device by oxidation method that can be perfected even in the pre-treatment stage and the final treatment of highly difficult wastewater treatment.

According to the present invention, two aeration pumps 5-1 and one transfer pump 2A are installed in the lower part of the first treatment tank P to pass the urine treatment liquid that is overpassed in one side urine storage tank O in parallel. The aeration device 5 is provided and connected to the first aerator 11-A by a starch transfer tube 9 to process the starch, and then the overpass pipe (Q) to the second processing tank (Q). 10-1) is provided, and the aeration device 5 is provided with one aeration pump 5-1 and one transfer pump 2A in parallel in the lower portion of the second processing tank (Q). The upper part is connected to the second breaker 11A-2 by the starch moving tube 7 to process the starch, while the upper part connected to the transfer pump 2A and the conveying pipe is connected to the mist flotation processor 12. After the liquid flows into the processing tank, it is transferred to the third processing tank (R) through the overpass pipe (10-1), and one aeration device (5) is installed in the inner lower portion of the third processing tank (R). And, the upper part is connected to the third breaker (11A-3) by the starch moving tube (9) to treat the starch, the other side of the upper to process the liquid by the mist flotation processor (12), The pressurized floating starch remover 400A built in the pressurized floatation treatment tank E formed at one side of the third processing tank R is a depacking machine 11A-1 and a lower part of the depacking machine 11A-3. Pressurizer 14A-1 connected to the other, other breaker 11A-2, another pressurizer 14A-2 connected to the bottom of the other breaker 11A-2, and another breaker Three independent devices consisting of 11A-3 and a pressurizer 4A-3 connected to the bottom of another breaker 11-3 are configured in parallel to process the final foam and starch, and then the bottom over. Oxidative injury pressure is formed on the side of the pass pipe (10-2), consisting of a discharge pipe (18) which is transported to the filtration device 500 consisting of the activated carbon layer 501 and the sand layer 502, filtered and discharged Min relates to a breaker.

Hereinafter, the present invention will be described in detail with reference to the accompanying drawings.

1 is a detailed view of the oxidative injury pressurized starch removal device of the present invention, Figure 2 is a detailed view of the manure solids separation and high-speed dehydrator of the present invention, Figure 3 is a detailed view of the high speed dehydrator of the present invention, Figure 4 is a detailed view of the vibrator of the present invention FIG. 5 is a detailed view of the aeration device of the present invention, FIG. 6 is a detailed view of the pressurized floatation starch remover of the present invention, FIG. 7 is a detailed view of the pressurization portion of the present invention, and FIG. Is a detailed view of the mist float spreader of the present invention, Figure 10 is another detailed view of the mist float spreader of the present invention, Figure 11 shows a detailed view of the filtration device of the present invention, the transfer pump (2A), the sensor (3), Transfer pipe (4), aeration device (5), aeration pump (5-1), aeration circulation pipe (6), arc engine (7), starch transfer pipe (9), circulation hole (10), overpass pipe (10) -1,10-2), lower overpass pipe (10-3), breaker (11A-1, 11A-2, 11A-3), fog floater (14), solid (outlet) (13), Pressurizing unit 14A-1, first pressing unit 14A-1, second pressing unit 14A -2), the third pressure booster (14A-3), the pressure injury induction pipe (14-1), the pressure injury cross pipe (14-2), the pressure injury cross pipe (14-3), the pressure injury double pipe ( 14-4), cover (14-5), drain pipe (drain) (16), aeration motor suction pipe (17), discharge pipe (18), aerator belt connector (46.46`), aeration shaft (47), aeration impeller ( 48), air inlet pipe (49), suction port (50), bushings (51, 51 '), broo (52), discharge pipes (54, 54'), scoop belt top connector (25), scoop belt Lower connector (26), punching machine shaft (27), punching machine 2nd impeller (27 '), punching machine 1st impeller (28), bearing (29), motor fixture (30),, aeration cylinder (31), manure Solid-liquid separation and high-speed dehydrator (100), vibrator (101), diaphragm screen (102), hydraulic spray (103), gas generating screw (104), gas ejection pipe and fan (105), vibration solid part (106), discharge water pipe 107, screw type high speed dehydrator 108, raw water pipe 109, manure injection pipe 110, gas generating screw motor 111, solid-liquid dehydration storage tank 112, gas removal storage tank 113, vibration motor ( 114), dehydrator Motor 115, Tras 116, Case 117, Inlet 121, Mechanical seal 122, Vibration rubber plate 123, Blade 124, Outer net 125, Sludge outlet 126, Motors 201 and 208, bearings 202 and 202 ', lidena 203, wing shaft 204, wing 205, oxygen supply pipe 206, fog float 207, connecting portion 209, inlet ( 210), outlet 211, pressurized floating starch remover 400A, filtration device 500, activated carbon layer 501, sand layer 502 A: bubble moving tube, B: air moving tube, C: bubble and air contact portion, It can be seen that O: separated urine storage tank, P: first treatment tank, Q: second treatment tank, R: third treatment tank, and S: pressure injury treatment tank.

Looking at the structure, as shown in Figure 1, the manure discharged from the barn is first introduced into the collection tank filled with water to separate the solid and liquid manure liquid separation and high-speed dehydrator 100, and the manure solid liquid separation and It is formed in the lower portion of the high-speed dehydrator 100, the manure liquid storage tank (O) for storing the separated urine solution, and formed on one side of the manure liquid storage tank (O) to the overpass in the manure liquid storage tank (O) first The first treatment tank (P) for processing the manure liquid flowing from the treatment tank (P), and the first aeration tank (P) has two aeration pump (5-1) and one transfer pump (2A) in the lower part inside Is connected to the aeration device 5 and the aeration pump 5 installed in parallel,

An intake pipe 17 and a circulation pipe 6 for sucking and circulating the aerated liquid and a arc pipe connected to the circulation pipe 6 and having air circulated and connected from the inside to the upper portion of the first treatment tank P; (7) and a drain pipe (drain) 16 formed at another side of the lower portion of the first treatment tank P to discharge the internal liquid of the first treatment tank P, if necessary, and the first treatment. An overpass tube 10-1 for overpassing the aeration treatment liquid formed and processed on one side of the middle P of the tank P to the second treatment tank Q, and starch formed on the upper portion of the first treatment tank P. The first aerator 11A-1 of the pressure flotation treatment tank S tank connected by the moving tube 9 and the starch moving tube 9 is formed on another upper side, and one side of the lower aeration device is provided. The fog pump is connected to the transfer pump 2A of (5) with a transfer pipe (4), and the other side is formed by the transfer pipe (4) so that the urine solution treated by the second processing tank (Q) located next to the inlet flows in. It consists of a flotation processor (12),

Second treatment tank (Q) for treating the urine fluid flowed into the first treatment tank (P) by one side of the mist float processor (12) of the first treatment tank (P) and the overpass pipe (10-1). Is

One aeration pump (5-1) and one transfer pump (2A) in the lower portion inside and connected to one side of the aeration device 5, the aeration pump (5) installed in parallel, and sucks the aerated liquid An intake pipe 17 and a circulation pipe 6 to circulate, an arc pipe 7 connected to the circulation pipe 6 and having air circulated and connected from the inside to the upper portion of the second processing tank Q; It is formed on the other side of the lower part of 2 processing tank Q, and the drain pipe (drain) 16 which discharges the internal liquid of 2nd processing tank Q as needed, and the middle of the said 2nd processing tank Q. An overpass pipe 10-2 for overpassing the aeration treatment liquid formed and treated on the upper one side to the third treatment tank R,

It is formed in the upper portion of the second treatment tank (Q), the mist flotation processor 12 for processing the urine fluid introduced into the second treatment tank (P), and formed on one side of another upper portion, and the starch transfer pipe (9) , The second breaker (11A-2) of the pressure flotation treatment tank (S) tank connected by the starch transfer pipe (9) and the transfer pump (2A) formed in the lower portion of the second processing tank (Q) is a transfer pipe (4) is provided so as to be connected to the fog floater 12 of the neighboring third treatment tank (R),

It is formed on one side of the second processing tank (Q), the second by the feed pipe (4) and the overpass pipe (10-2) of one side of the mist flotation processor (12) of the third processing tank (R) The third treatment tank (R) for processing the liquid introduced from the treatment tank (P) is

The third treatment tank (R) is connected to an aeration device (5) installed as one aeration pump (5-1) in the lower part inside, and is connected to one side of the aeration pump (5), and aspirated aeration liquid An intake pipe 17 and a circulation pipe 6 to be connected to the circulation pipe 6, and an air pipe 7 connected to the upper portion from the inside of the third processing tank R to the upper portion, It is formed on the other side of the lower part of the processing tank R, The drain pipe (drain) 16 which discharges the internal liquid of the 3rd processing tank R as needed, and formed in the upper part of the 3rd processing tank R. It is composed of a structure connected to the starch moving tube (9), and the third breaker (11A-1) of the pressure flotation treatment tank (S) tank connected by the starch moving tube (9),

It is formed in one side of the said 3rd processing tank R, and three breakers 11A-1, 11A-2, 11A-3, and the said 3 breakers 11A-1, 11A-2, 11A- 3) the starch remover 400A formed of three sets of pressurization portions 14A-1, 14A-2, 14A-3 formed in the lower portion of the

Three pressurizers 14A-1, second pressurizers 14A-2, and third pressurizers having three breakers 11A-1, 11A-2, and 11A-3 formed on the upper part. Each group 14A-3 is connected to each other by a pair of pressurized floating guide pipes 14-1, and the final treatment is performed in three (14A-1, 14A-2, 14A-3) configured as the double cylinder. Starch drain pipe 15 for discharging the liquid to the pressurized floatation starch processing tank (S), and the lower overpass pipe (10) for transferring the treated liquid to the filtration device 500 installed on one side of the pressurized floatation starch processing tank (S). A filtering device 500 for filtering the treated urine solution introduced from the lower overpass pipe 10-3;

The filtration device 500 is an activated carbon layer 501 and a sand layer 502 are alternately stacked from the top, and formed in the upper portion of the filtration device 500 to discharge pipe 18 for discharging the treated liquid. The present invention relates to an oxidative injury pressurized starch removing apparatus characterized in that the configuration.

2 is a detailed view of the manure solids separation and high-speed dehydrator 100, the manure injection secondary pipe 110 and the raw water pipe 109 and the vibrator 101 and the diaphragm screen 102 is installed, the fermentation of high liquid at the bottom A hydraulic spraying machine 103 connected to the pipe formed of the dehydration storage tank 112 and the 2mm susceptor net 127 is formed, and a gas generating screw is formed at a lower portion thereof, and a gas removal storage tank 113 and a discharge water pipe at the lower portion thereof. 107 is formed, the high-speed fermentation dehydrator 108 and the gas generating motor is formed on the side of the device, the gas discharge pipe and the fan 105 is formed on the other side,

3 is a high-speed fermentation dehydrator 108, the manure inlet 121 and the gas generating screw motor 115, the mechanical seal 122 and eight blades 124 and the outer network 125 installed at the connection between the motor and the dehydrator. ) And susnet 127 and the fermentation sludge outlet 126 is installed, the lower support of the device is composed of a vibration rubber prevention plate 123,

Figure 4 relates to a solid-liquid separation vibrator, it can be seen that the vibrator 101 is equipped with a screen 102 of 0.1 m 2 at the bottom.

FIG. 5 shows the aeration device 5 in detail. The motor is mounted on the aeration device, and the belt is connected to the aeration belt connection parts 46 and 46` of the motor and the aeration shaft 47 by a belt. An aeration impeller 48 installed at the lower portion of the 47 is installed in the aeration cylinder 31, and eight air injection pipes 49 are installed around the aeration shaft 47, and a middle of the aeration cylinder 31 is provided. Inlet 50 is formed in the lower portion, the aeration cylinder 31 can be rotated by the bushing (51, 51`), the heater 52 is installed on the aeration cylinder 31, the aeration cylinder It can be seen that the discharge pipes 54 and 54` are horizontally mounted to the lower part of the 31 and the broa 52 is installed to the upper part of the aeration cylinder 31 from the top of the aeration device 5,

6 shows that the pressurized floatation starch remover 400A is installed in the pressurized floatation treatment tank E, and is formed by a starch transfer tube 9 formed on the upper portion of the first treatment tank P and the starch transfer tube 9. It is installed inside the first breaker 11A-1 of the pressurized flotation treatment tank S and the pressurized floatation treatment tank S to be connected, and the first breaker 11A-1 and the pressurized injury are induced. The first pressurizing unit 14A-1 connected to the bottom by the tube 14A-1, and the upper portion of the second processing tank Q, are formed and formed on the starch transfer tube 9 and the starch transfer tube. The second breaker 14A-2 of the pressure flotation treatment tank S connected by (9),

It is installed in the pressure flotation treatment tank (S), the pressurizing portion (14A-1, 14A-2, 14A-3) are connected in parallel, respectively, the second breaker (14A-2) And a second pressurizing portion 14A-2 connected downward by a pressurizing float induction pipe 14-1,

The third breaker 11A-3 and the third breaker 11A-3 of the pressure floatation treatment tank S group connected by the starch transfer pipe 9 formed on the third treatment tank R. It consists of a third pressure booster (14A-3) of the pressure floating treatment tank (S) tank connected to the lower part of the,

The first pressurizing unit 14A-1, the second pressurizing unit 14A-2 and the third pressurizing unit 14A-3 are each independently and side by side installed, and each of the gig breakers Pressurized floating cross pipe (14-2), which is connected to the lower portion by a pressurized floating guide pipe (14-1) and connected to the pressurized floating guide pipe (14-1), and the pressurized floating cross pipe (14-2). Pressurized injury cross pipe (14-3) formed to extend to the lower portion of the lower portion to open the lower portion, and the pressurized injury double pipe (14-) is formed in a double to surround the pressing injury cross pipe (14-2). 4) and a cover 14-5 formed on the outside of the pressurized double tube 14-4.

8 is a detailed view of the breaker 11, and is connected to the breaker belt connector 25 and the breaker shaft 27 of the motor by a belt, and the breaker secondary to the bottom of the breaker shaft 27. Impeller (27 ') is installed, in the middle of the packer primary impeller (28) is installed, the packer secondary impeller (27) is installed about half less than the packer primary impeller (28) It was. It can be seen that the unexplained sign (29) bearing (30) consists of a motor fixture.

9 and 10 show in detail the mist-spray spreader of the present invention, the bubble flow pipe (A) and the spray device formed on the upper side of the bubble movement pipe (A) and the bubble movement pipe (A) of the bubble flow pipe (A) One side surface, the air moving tube (B) and the air moving device formed on the lower portion of the wing 205 of the spreading device, and the oxygen supply pipe for preventing the vacuum state of the wing 205, and supply oxygen during mist spraying ( 206 and an outlet 211 in which the bubble meets the air at the bubble and the air contacting part C and is blown out and discharged in a fog shape.

The spreading device is formed horizontally on the top of the bubble moving tube (A), the motor 201, the connecting portion 209 connected to the motor 201, the wing shaft 204 connected to the connecting portion 209 and And a wing 205 formed at an end of the wing shaft 204 and a lidena 203 formed outside the wing shaft 204 and surrounding the wing shaft by bearings 202 and 202 '. The air moving device is formed on one side of the bubble moving tube (A), and is operated by a motor (208) to the fan (207), and the air generated by the fan (207) to move the air pipe (B) A configured mist float spreader.

As shown in FIG. 11, the filtration apparatus 500 includes a sand layer 502 formed at a lowermost portion, an activated carbon layer 501 formed on an upper portion of the sand layer 502, and the lamination as described above. And, it is composed of a discharge port 18 formed on the upper part of the filtration device 500, when the liquid is introduced from the lower overpass pipe (10-3) connected to the lower portion of the pressure flotation treatment tank (S), while rising to the top, After passing through the sand layer 502 and the activated carbon layer 501 three times, it is discharged through the outlet 18.

Referring to the operation and use state, the oxidative injury pressurized starch removal treatment method of the present invention, as shown in Figure 1,

First, by separating the manure from the raw water storage tank in the manure solid-liquid separation and high-speed dehydrator 100, the manure is discharged through the solid (min) outlet (13) to use as a compost feed, urine is a manure fluid storage tank (O) Flows into the first treatment tank P as an overpass, and the introduced urine flows in the first treatment tank P in parallel with two aeration pumps 5-1 and one transfer pump 2A in the lower part of the interior. BOD and SS concentration is aerated by less than 15,000 when the raw water is 80,000 by the aeration device (5) installed, and then part of the overpass pipe (10-1) formed on one side of the middle of the first treatment tank (P) It is conveyed to the second processing tank (Q) located on the side through, while the foam is connected to the first breaker (11A-1) of the pressure flotation treatment tank (S) tank to the starch transfer pipe (9) formed on the upper side and pressurized It is processed in the flotation tank (S), and on the other hand, the mist float connected to the transfer pump (2A) of the lower aeration device (5) by the transfer pipe (4) Was transferred to a processor (12), a second treatment tank (Q) is treated in the following,

As described above, in the second treatment tank Q, one aeration pump 5-1 and one transfer pump 2A are disposed in parallel with the treatment liquid introduced from the first treatment tank P. (5) and the fog floater (12) installed on one side of the BOD, SS concentration is treated with a solution treated with less than 15,000 to less than 5,000, and then overpass formed in the middle upper one side of the second treatment tank (Q) The second wave of the pressure flotation treatment tank (S) tank is passed through the processing liquid to the third treatment tank (R) by the pipe (10-1), and the foam or the like is pushed through the starch moving tube (9) formed on another upper side. After transferring to the aeration (11A-2) and processing,

In the third treatment tank R, the treatment liquid transferred from the second treatment tank Q to the aeration device 5 and the fog buoy 12 are installed in one lower aeration pump 5-1. The foam is transferred to the third bubbler 11A-1 of the pressure flotation treatment tank S connected to the starch moving tube 9 formed on the upper portion thereof, and bubbles are completely removed to treat the starch removal rate at 90% or more. , The internal liquid of the third treatment tank (R) is discharged through the drain pipe (drain) 16, and in the pressure flotation treatment tank (S) formed on one side of the third treatment tank (R), three breakers (11A) -1,11A-2,11A-3 and the pressurizing part 14A-1,14A-2,14A-3 formed in the lower part of the three breakers 11A-1,11A-2,11A-3. After treating the bubbles and the like transferred through the starch transfer pipe (9) in each treatment tank (P, Q, R) by the starch remover (400A) formed of three sets of), the final treated liquid is pressurized Lower overpass pipe (1) to the filtration device 500 installed on one side of (S) After passing through 0-1), the liquid to be transported is formed by filtering through the filtration device 500 in which the activated carbon layer 501 and the sand layer 502 are alternately stacked from the bottom to the top to be filtered. Discharge through the discharge pipe (18) for discharging the liquid, if not handled by accident, or if necessary, the first processing tank (S) through the recovery pipe connected to the discharge pipe 18, if necessary ) To be reprocessed and to be directly drained through drain pipes (drain) 16 formed at the bottom of each treatment tank (P, Q, R, S).

The manure solids separation and the high speed dehydrator 100, the high speed dehydrator 108 and the operation method of the vibrator as shown in Figures 2 to 4 in the manure collection tank in the manure solids separation and high speed fermentation dehydrator secondary manure pipe 110 The manure wastewater introduced through) is guided to the place where the vibrator 101 and the diaphragm screen 102 are installed together with the raw water supplied from the raw water pipe 109 and lowered by the vibrating screen by the operation of the vibrator 101. Part of which is transferred to the lower part, by the action of the hydraulic sprayer 103 connected to the pipe formed of the solid-liquid fermentation dehydration storage tank 112 and the 2mm susceptor network 127 was moved by the hydraulic pressure through the movement of the separated manure. High liquid fermentation dehydration storage tank, (113) is a passage to transfer to the gas removal storage tank, by using the space of 3㎡ to minimize the level of ammonia, phosphorus or methane mixed with manure,

The gas generating screw 104 installed in the solid-liquid fermentation dehydration storage tank 112 rotates the manure injected through the hydraulic sprayer by the gas generating screw motor 111 to separate the methane gas product mixed in the urine.

When moving to the aging tank (6) to remove the odor and methane gas in the preliminary fermentation tank, the gas ejection pipe and fan 105 is separated by the gas generated in the secondary storage tank 113 and the gas generating screw 104 To vent the gas to the outside,

When the manure sludge filtered from the vibrating screen 102 is introduced through the manure inlet 121 of the high speed dehydrator 108 of FIG. 6 installed on the sides of the devices, a screw using a high speed rotation shaft is operated by the gas generating screw motor 115. After hitting with a rotation of 3600 RPM per meal and heating, the water has evaporation and fermentation effects, and after being easily decomposed by the eight blades 124 installed in the motor and the high speed dehydrator 8, the dewatered wastewater is Evaporated and discharged at the same time through the external network 125 and the suspend net 127, the fermentation sludge is discharged through the fermentation sludge outlet 126,

After the gas is stored in the gas removal storage tank 113, the gas is discharged through the gas discharge pipe and the fan 105, and the operation method of the aeration device 5 is each treatment tank (W, X, Y, Z). The aeration device 5 is installed in the lower part of the inside as shown in FIG. 1, and when the motor built in the upper part of the aeration device 5 starts to operate as shown in FIG. 5, the aeration device belt connector 16, 16. The aeration shaft 17 connected to `) and the aeration impeller 18 installed at the lower portion of the aeration shaft 17 start to rotate. The aeration impeller 18 is mounted inside the aeration cylinder 31, and eight air injection pipes 19 installed around the aeration shaft 17 are rotated at the top of the air injection pipe 19. Air starts to flow from the broa 22 installed in the.

The inlet 20 is formed at the lower middle of the aeration cylinder 31, and the aeration cylinder 31 is rotated by bushings 21 and 21 ′, and the manure is introduced into the inlet 20 of the aeration cylinder to provide air. The discharge pipe 24 is guided by the discharge pipe 24 horizontally installed under the aeration cylinder 31 while the manure and air are sufficiently stirred by the aeration impeller 18 while contacting the air injected into the injection pipe 19. ) Is rotated and forcedly discharged by pressure into the aeration tank to mix well with the existing liquid.

The upper part of the aeration cylinder 31 may be provided with a heater 32 to adjust the temperature 50 ~ 65 ℃ to facilitate the growth of microorganisms. Normal temperature is 38-40 ℃.

As shown in Fig. 6, the operation state of the floatable starch removing apparatus of the present invention is that the aeration treated starch liquor in each treatment tank (P, Q, R) through the starch transfer pipe (9). 1), it is transferred to each of the breakers (11A-1, 11A-2, 11A-3) formed in the upper portion of the pressurized floating induction pipe (14-1) and the respective breakers (11A-1, 11A-2, 11A-3) are connected to the belt of the breaker belt connector 25 and 27 of the motor as shown in Fig. 8, with an impeller 27` at the lower end of the shaft, Impellers 28 are provided, respectively, and the impellers 27 'and 28 connected to the breaker axis and the breaker axis by the rotation of the motor rotate together while evaporating the fine particles of the crushed liquid. When the bubble starts to rise to the center by the rotation of 28), the bubble is broken by the breaker secondary chimney 27 'and turned into a starch liquid. Three independent first pressure booster 14A-1, second pressure booster 14A-2, and third pressure booster 14A- which are connected to the lower portion through the respective pressure float induction pipes 14-1. While moving to each of the pressure injury cross pipe (14-2) of 3) (hereinafter describes the operation method of one pressure booster and the rest is the same operation method),

Bubbles that have not been removed are collected in the enlarged portion formed in the middle portion of the pressure injury cross pipe (14-2), and the starch solution is continuously moved downward to pass through the pressure injury cross pipe (14-3). After reaching the pressurized floatation double tube 14-4 having an open lower portion, the untreated bubbles are raised again and collected at the upper portion of the pressurized floatation double tube 14-4, and the starch liquid is removed from the pressurized floatation double tube 14-4. 4 is transferred to the cover 14-5 formed on the outside of the pressure floating double tube 14-4 through the lower portion of the pressure floating treatment tank S to the starch drainage pipe 15 formed on one side of the cover 14-5. To drain).

9 and 10, when the mist sprayer operates the motor 201, a connecting portion 209 connected to the motor 201 and a wing 205 formed at an end of a wing shaft connected to the connecting portion 209 are provided. When it starts to rotate, and at the same time by operating the motor 208 and the fan 207 formed on one side of the bubble moving tube (A) to transfer air to the upper through the air moving tube (B),

The air conveyed through the air moving tube (B) acts as an ejector, and bubbles are introduced along the bubble moving tube (A), crashed into the rotating blades (205), and crushed and advanced to the air transferred through the air moving tube (B). It turns into a mist shape and is sprayed.

At this time, the oxygen is supplied by the oxygen supply pipe 206 formed on the upper side of the motor to prevent the instantaneous vacuum is formed on the rear surface of the wing 205 to prevent the vacuum, it is a device for supplying oxygen to the mist sprayed. .

Mechanical performance and treatment comparison table

Aeration

Comparative specification and performance Third party Headquarters Rotation Ratio (R.P.M) 1750 2100 Exit diameter 100 mm 350 ~ 400mm Power consumption 5HP 3.75KW 7HP 5.25KW 3HP 2.25KW Driving time 24 hours Available as required Suction Caliber 100mm Caliber 600mm Oxygen inhalation Discharge suction 40mm Forced suction 120mm Evaporation 60 minutes / 0.9ℓ 60 minutes / 108ℓ Fermentation efficiency 90 days based on 250 TON, 10 TON fresh water 13 days of manure 100% 250 TON Bubble generation costs 100% at 50% fresh water 100% when manure solution is 100% Sludge treatment About 10% 90% Fermentation Light red coffee color Light red coffee color P.P.M measurement ratio 25,000 ~ 40,000 (50% fresh water) 25,000-40,000 Hourly processing 0.9 TON 1.8 TON Fermentation agent added has exist none Average fermentation temperature 20 ℃ ~ 32 ℃ 36 ℃ ~ 40 ℃ Hitachi 50 ℃ ~ 65 ℃ Barn Clean Fee (Gas) none none Storage tank facility Civil engineering standard according to design Existing tank facilities and specifications available Sludge in machinery tanks Remaining none Mechanical use Fermentation (Underwater Motor) Septic Tank (Manufacturing Machine) Facility fee Sludge Tanks / Storage Fermenters 2 Fermenter 2 Install and let Mechanical product standard (underwater motor) Manufactured according to tank capacity Wig effect Yes (after 90 days) none

2. Aerator

Comparative specification and performance Third party Headquarters Motor R.P.M IHP 1750 2HP 1750 Bubble crushing amount limit Infinity 휀 none U. RPM. 1480-1850 Impera RPM 1750 RPM 2100 ~ 2600 Bubble generation ratio control impossible Adjustable Spray Angle (Pulverization) Almost none 2,000 mm upward Crushing remnants Can't Infinity Grinding 60 minutes /0.9TON 60 minutes / 8TON overload has exist none

3. solid-liquid separator

Comparison Species This invention Treatment ability 15TON per day 15TON per day Electric power consumption 7.5㎾ 0.75㎾ Moisture content 20 to 25% 20 to 25% Moving direction screen Stainless steel net 0.5㎡ Phase polyester 0.1㎡ under Screen plate Stainless Steel Arm 4mm Plastic plate 30 mm

4. High speed fermentation dehydrator

Comparison Species This invention Treatment ability 15TON per day 15TON per day Electric power consumption 3㎾ to 5.0㎾ 1.5 ㎾ High speed rotation method Heater method 80% 100% of low temperature method over 60 ° Acid water sawdust none Composting 100% 100%

5. hydraulic injector

Comparison Species This invention Treatment ability Urine 1 day 20TON Urine 1 day 20TON Electricity consumption 850 yen none Method Jet Natural SUS 3㎡ Gas removal rate 40% to 50% 40% to 50%

6. Gas generating screw

Comparison Species This invention Treatment ability Urine 1 day 20TON Urine 1 day 20TON Electric power consumption 0.75㎾ 850 yen Method Circulation jet Blow trommel Gas removal rate 40% to 50% 40% to 50% Squirt road Forced suction 휀 150 W

As described above, the present invention transforms the biological manure treatment from home and abroad into physicochemical treatment, and at the same time, dramatically reduces the national notification of 18,000 won to 2,000-3,000 won per head of manure treatment cost to livestock farms, It is able to maintain the processing, and it is a starch processor by the oxidation injury method installed in the pipeline (5) .It basically uses microorganisms to decompose and reduce 100% livestock manure and process it. The series of processes are carried out continuously and automatically, which doubles the processing performance, smoothly mixes manure, microorganisms and air using the aeration device, and removes air bubbles with a debris to remove odor-free fermented manure liquid. It is effective to reuse for cleaning.

Claims (5)

In the oxidized injury pressurized starch removal device, two aeration pumps (5-1) and one transfer pump to the urine treatment liquid that is overpassed in the separate urine storage tank (O) on the lower side of the first treatment tank (P) ( 2A) is provided with an aeration device 5 installed in parallel, the upper portion is connected to the first aerator 11-A by the starch transfer tube 9 to process the starch, and then the second treatment tank Q ) Through the overpass pipe (10-1), In the lower part of the second processing tank Q, there is provided an aeration device 5 in which one aeration pump 5-1 and one transfer pump 2A are installed in parallel, and in the upper part of the starch pipe 7, The starch is connected to the second breaker (11A-2) to process the starch, and on the other hand, the upper portion connected to the transfer pump (2A) and the transfer pipe is treated with the liquid introduced by the mist floatation processor (12), Transfer to the third processing tank (R) through the overpass pipe (10-1), one aeration device (5) is installed in the inner lower portion of the third processing tank (R), the starch transfer pipe (9) It is connected to the third breaker (11A-3) by to process the starch, the other side of the upper to the liquid treatment by the mist flotation treatment unit 12 at the top, the third treatment tank (R) Pressurized wound starch remover (400A) built in the pressure floatation treatment tank (E) formed on one side is a depressor 11A-1 and a pressurized injury connected to the lower part of the deaerator 11A-3. 14A-1, another breaker 11A-2, another pressurizer 14A-2 connected to the bottom of the other breaker 11A-2, and another breaker 11A-3. And three independent apparatuses composed of pressurizers 4A-3 connected to the lower part of another de-aerator 11-3 are configured in parallel to process the final foam and starch, and then the lower overpass tube 10-. 2) is formed on the side, and the oxidized injury pressurized starch, characterized in that composed of a discharge pipe (18) which is transported to the filtration device 500 consisting of the activated carbon layer 501 and the sand layer 502 and filtered and discharged Removal device. The aeration apparatus (5) of claim 1, wherein the first aeration tank (P) has an aeration device (5) and two aeration pumps (5-1) and one transfer pump (2A) installed in parallel in the lower portion of the inside, and the aeration pump (5). It is connected to one side of the intake pipe 17 and the circulation pipe 6 for sucking and circulating the aerated liquid, and connected to the circulation pipe 6, the air is circulated and the first treatment tank (P) It is formed on the other side of the arc pipe 7 connected from the inside to the upper part, and another side of the lower part of the 1st processing tank P, and the drain pipe (drain) which discharges the internal liquid of the 1st processing tank P as needed. ), An overpass pipe 10-1 for overpassing the aeration treatment liquid formed and treated on the middle upper side of the first treatment tank P to the second treatment tank Q, and the first treatment tank ( Starch transfer tube (9) formed on the upper portion of P), the first breaker (11A-1) of the pressure flotation treatment tank (S) tank connected by the starch transfer tube (9), and is formed on the other one side , One side Connected to the transfer pump (2A) of the lower aeration device (5) by the transfer pipe (4), the other side is the urine fluid treated in the second processing tank (Q) located in the neighborhood with the transfer pipe (4) Oxidation injury pressurized starch removal device, characterized in that consisting of the mist flotation processor (12) formed to be introduced. The second method of treating urine fluid introduced from the first treatment tank P by one side of the mist injury processor 12 of the first treatment tank P and the overpass pipe 10-1. Treatment tank (Q) One aeration pump (5-1) and one transfer pump (2A) in the lower portion inside and connected to one side of the aeration device 5, the aeration pump (5) installed in parallel, and sucks the aerated liquid An intake pipe 17 and a circulation pipe 6 to circulate, an arc pipe 7 connected to the circulation pipe 6 and having air circulated and connected from the inside to the upper portion of the second processing tank Q; It is formed on the other side of the lower part of 2 processing tank Q, and the drain pipe (drain) 16 which discharges the internal liquid of 2nd processing tank Q as needed, and the middle of the said 2nd processing tank Q. An overpass pipe 10-2 for overpassing the aeration treatment liquid formed and treated on the upper one side to the third treatment tank R, It is formed in the upper portion of the second treatment tank (Q), the mist flotation processor 12 for processing the urine fluid introduced into the second treatment tank (P), and formed on one side of another upper portion, and the starch transfer pipe (9) , The second breaker 11A-2 of the pressure flotation treatment tank S connected by the starch moving tube 9, The transfer pump 2A formed at the bottom of the second treatment tank Q is provided to be connected to the mist buoy 12 of the neighboring third treatment tank R by the transfer pipe 4. Oxidation injury pressurized starch removal device. The conveying pipe 4 and the overpass pipe 10-2 of Claim 1 which are formed in the one side of the said 2nd processing tank Q, and are the mist float processing apparatus 12 of the 3rd processing tank R. The third treatment tank (R) for processing the liquid introduced into the second treatment tank (P) by The third treatment tank (R) is connected to an aeration device (5) installed as one aeration pump (5-1) in the lower part inside, and is connected to one side of the aeration pump (5), and aspirated aeration liquid An intake pipe 17 and a circulation pipe 6 to be connected to the circulation pipe 6, and an air pipe 7 connected to the upper portion from the inside of the third processing tank R to the upper portion, It is formed on the other side of the lower part of the processing tank R, The drain pipe (drain) 16 which discharges the internal liquid of the 3rd processing tank R as needed, and formed in the upper part of the 3rd processing tank R. Oxidation injury pressurized starch, characterized in that consisting of a starch transfer pipe (9) and the third breaker (11A-1) of the pressure flotation treatment tank (S) tank connected by the starch transfer pipe (9) Removal device. The starch moving tube (9) of claim 1, wherein the pressurized floating starch remover (400A) is installed in the pressure floating treatment tank (E), and the starch moving tube (9) formed on the upper portion of the first processing tank (P) and the starch moving tube (9). The first breaker 11A-1 of the pressure floatation treatment tank S connected by the said tank is installed in the inside of the said pressure flotation treatment tank S, and pressurized with the said 1st breaker 11A-1. A first pressurizing floater 14A-1 connected downward by the floating induction pipe 14A-1, The second breaker 14A-2 formed in the upper part of the 2nd processing tank Q and formed and connected by the starch moving tube 9 and the said starch moving tube 9 by the pressure flotation processing tank S group. )Wow, It is installed in the pressure flotation treatment tank (S), the pressurizing portion (14A-1, 14A-2, 14A-3) are connected in parallel, respectively, the second breaker (14A-2) And a second pressurizing portion 14A-2 connected downward by a pressurizing float induction pipe 14-1, The third breaker 11A-3 and the third breaker 11A-3 of the pressure floatation treatment tank S group connected by the starch transfer pipe 9 formed on the third treatment tank R. It consists of a third pressure booster (14A-3) of the pressure floatation treatment tank (S) tank connected to the lower portion of the, The first pressurizing unit 14A-1, the second pressurizing unit 14A-2 and the third pressurizing unit 14A-3 are each independently installed side by side, and each of the breakers is Pressurized floating cross pipe (14-2), which is connected to the lower portion by a pressurized floating guide pipe (14-1) and connected to the pressurized floating guide pipe (14-1), and the pressurized floating cross pipe (14-2). Pressurized injury cross pipe (14-3) formed to extend to the lower portion of the lower portion to open the lower portion, and the pressurized injury double pipe (14-) is formed in a double to surround the pressing injury cross pipe (14-2). 4), it is composed of a cover (14-5) formed on the outside of the pressure floating double tube (14-4), The breaker is connected to the breaker belt connector 25 and the breaker shaft 27 of the motor by a belt, and a breaker secondary impeller 27 'is installed below the breaker shaft 27. In the middle, the breaker primary impeller 28 is installed, and the breaker secondary impeller 27 is about 1/2 less than that of the breaker primary impeller 28. Device.