KR200283099Y1 - Apparatus for eradication of starchy - Google Patents

Abstract

The present invention is to separate the liquid separated in the solid-liquid separator of the manure four independent aeration tank, the aeration motor, the aeration circulation tube and the arc organ, and aeration formed in the four independent aeration tank, the wave formed on the outside of the four independent aeration tank It is a device for removing starch by a pressurized flotation starch remover consisting of aeration and three pressurization.

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 dehydrator and The present invention relates to an oxidative-injured pressurized starch removing device including a stirring means, an air supply means, a bubble removing means, 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, not only is it incurred a considerable cost and difficulty in processing, but also organic matter in the livestock manure is decomposed. 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. The high speed fermentation method utilized as a raw material of the is 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 a manure treatment of biological concept to a physicochemical treatment, the patent application No. 99- filed on May 12, 1999 of the present invention or filed No. 17038 Design of the method and apparatus for treating livestock manure, and Patent No. 306228 Name of the invention; the most basic solid-liquid separator in the purification of livestock manure and domestic wastewater, Utility Model Application Nos. 20-2001-0023605 and 20 The name of the invention; Urine fermentation mist sprayer, Patent Application No. 10-2001-306224 Oxidation floater is improved, after separating sludge and urine by solid-liquid separation and high-speed dehydrator, aeration in an independent aeration tank used as a mixing and stirring device After the degassing, the depressurized starch remover and the three pressurizers were used, and the water and microorganisms contained in the bubbles were refined and evaporated using the defoaming means. It is a technical task of the present invention to provide an apparatus for removing oxidized starch that can process livestock manure in a short time by allowing a series of processes to be performed continuously and automatically and to reuse 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

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

1st aeration tank (1-1), 2nd aeration tank (1-2), 3rd aeration tank (1-3), 4th aeration tank (1-4), transfer motors (2,2-1,2-2,2) -3), sensor (3), conveying pipe (4), aeration device (5), aeration circulation pipe (6), arc engine (7), starch moving pipe (9), circulation hole (10), deaerator (11) ), The pressure booster 14 ', the first pressure booster 14'-1, the second pressure booster 14'-2, the third pressure booster 14'-3, the pressure float induction pipe (14-1), pressurized injury cross pipe (14-2), pressurized injury cross pipe (14-3), pressurized injury double pipe (14-4), cover (14-5), starch drain pipe (15), drain pipe (Drain) (16), aeration motor suction pipe (17), aeration belt connection (46.46`), aeration shaft (47), aeration impeller (48), air injection pipe (49), suction port (50), bushing (51) (51)), broo (52), discharge pipe (54, 54`), scoop belt upper connector (25), spool belt bottom connector (26), spooling shaft (27), spooler secondary impeller ( 27 '), spooler primary impeller (28), bearing (29), motor fixture (30),, aeration cylinder (31), manure solids separation and high speed dehydrator (100), vibrator (101), vibration plate Clean 102, hydraulic sprayer 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, Pressurized Injury Starch Remover (400 ')

The present invention for achieving the above object is the invention patent (patent 0306228 livestock manure treatment method and apparatus) of 1999 developed by the oxidized sludge to remove only a small amount of starch through a blister, 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.

The present invention transfers the liquid separated from the solid-liquid separator of manure to the four independent aeration tanks in which the aeration motor, the aeration circulation tube and the arc engine are formed, and then aeration treatment. It is a device for removing starch by the configured pressurized floating starch remover.

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 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 pressurized floater of the present invention, and FIG. , The first aeration tank (1-1), the second aeration tank (1-2), the third aeration tank (1-3), the fourth aeration tank (1-4), the transfer motors (2,2-1,2-2, 2-3), sensor (3), feed pipe (4), aeration device (5), aeration circulation pipe (6), arc engine (7), starch transfer pipe (9), circulation hole (10), deaerator ( 11), the pressure booster 14 ', the first pressure booster 14'-1, the second pressure booster 14'-2, the third pressure booster 14'-3, and the pressure injury induction Pipe (14-1), pressure injury cross pipe (14-2), pressure injury cross pipe (14-3), pressure injury double pipe (14-4), cover (14-5), starch drainage pipe (15), Drainpipe (16), Aeration Aerator suction pipe (17), aeration belt connection (46.46`), aeration shaft (47), aeration impeller (48), air injection pipe (49), suction port (50), bushing (51, 51 '), brower ( 52), discharge pipes (54, 54`), the top of the wrapper belt connector (25), the bottom of the wrapper belt connector (26), the packer shaft (27), the packer secondary impeller (27 '), the packer primary Impeller (28), bearing (29), motor fixture (30), aeration cylinder (31), manure solids 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 height 106, discharge water pipe 107, screw-type high-speed dehydrator 108, raw water pipe 109, manure injection pipe 110, gas Generation screw motor 111, high 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, vibrating rubber plate 123, blade 124, outer mesh 125, sludge outlet 126, pressurized wound starch remover 400 ' Can.

Looking at the structure, as shown in Figure 1, the manure discharged from the barn is a manure solid-liquid separation and high-speed dehydrator 100 for separating the solid and liquid flowing in the collection tank filled with water initially, and the manure solid-liquid separation and A transfer motor 2 for transferring the separated liquid formed under the high speed dehydrator 100 to the first aeration tank 1-1 through a transfer pipe 4, and on the side surfaces of the first aeration tank 1-1. The second aeration tank (1-2) and the third aeration tank (1-2), which are formed in sequence, transfer the liquid processed by the transfer motors (2-1, 2-2, 2-3) and are connected to the starch pipe (7) at the top ( 1-3) and the fourth aeration tank (1-4) and the pressurized wound starch remover (400 '),

Inside the first aeration tank (1-1) is connected to the neighboring aeration tank penetrating the upper one side and the starch transfer pipe (9) for moving the aerated starch, and in the lower portion of the first aeration tank (1-1) A drain pipe (drain) 16 formed to discharge the manure liquid, if necessary, an aeration device 5 formed at the outer lower portion of the first aeration tank 1-1 to aerated the manure liquid introduced thereto, and the first It is installed inside the aeration tank 1-1, connected to the aeration device 5, and the intake pipe 17 and the circulation pipe 6 for circulating the aerated liquid, and the circulation pipe 6 and It is formed in the lower part of the said first aeration tank 1-1 and the arc pipe 7 connected to the upper part of the inside of the 1st aeration tank 1-1 which supplies air to the aeration apparatus 5, The 1st A drain pipe (drain) 16 for discharging the internal liquid of the aeration tank 1-1 and a circulation port 10 for discharging the aeration treatment liquid formed and treated on one side of the first aeration tank 1-1. Is connected to the circulation port 10, is formed on the outer side of the first aeration tank (1-1) to transfer the aerated process liquid to the neighboring second aeration tank (1-2) transfer motor ( 2-1), the second aeration tank (1-2) for aeration of the first aerated liquid transferred by the transfer motor (2-1), and the upper portion of the second aeration tank (1-2) The starch pipe (9) extending from the upper portion of the first aeration tank (1-1) is connected to the branch is connected, the second aeration tank (1-2) is the same component as the first aeration tank (1-1), The transfer motor 2 is composed of a device, structure and form, connected to the circulation port 10 formed on one side of the second aeration tank (1-2), and formed on the outside of the second aeration tank (1-2). The aeration treatment liquid is supplied by -2) and the third aeration tank (1-3) and the third aeration tank (1-3) formed on the other side of the second aeration tank (1-2) are connected to the first aeration tank (1--1). 1) and the same parts, devices and structures as the second aeration tank (1-2) And a circulation port 10 formed at one side of the third aeration tank 1-3, and connected to the transfer motor 2-3 formed outside the third aeration tank 1-3. The aeration treatment liquid is supplied by the fourth aeration tank 1-4 and the third aeration tank 1-3 formed on the other side of the third aeration tank 1-3, and the first aeration tank 1-1, the third aeration tank 1-3. It is composed of the same parts, apparatus, structure and form as the two aeration tanks 1-2 and the third aeration tank 1-3.

It is formed on the outer side of the fourth aeration tank (1-4), the pressurized wound starch remover (400 ') and the pressurized wound starch remover (400') connected to the starch transfer pipe (9) is formed in the upper debris ( 11), and the three first pressurizing portion 14'-1, the second pressurizing portion 14'-2, and the third pressurizing portion 14'-3 formed in the lower portion are pressurized floating induction pipes ( 14-1) is formed, and is formed in the upper portion of each of the pressurizing unit and the breaker 11 for crushing the foam of the manure liquid introduced, and is formed in the lower portion of the breaker 11 Starch for draining the manure solution finally processed by the three first pressurizer 14'-1, the second pressurizer 14'-2, and the third pressurizer 14'-3 having a cylindrical shape. A drain pipe 15 and one of the starch drain pipes 15 are connected to a drain pipe (drain) 16 formed at a lower portion of the fourth aeration tank 1-4, and the other branch is branched to form the first aeration tank. Tooth injected to (1-1) It relates to an oxidative injury pressurized starch removal device, characterized in that it is connected to the pipe (4) and configured to process again.

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 in the connection between the motor and the dehydrator, 125 ) 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 embedded in 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 is a pressurized floatation starch remover, which includes a starch moving tube 9 for moving the aerated starch, three independent first pressurizing portions 14'-1 connected to the starch moving tube 9, and a second pressurization. A deformer 11 formed on the floating unit 14'-2 and the third pressurizing unit 14'-3 and the pressurized injured starch remover 400 'to crush bubbles of the manure liquid introduced thereto. And three pressurizing portions 14 'formed at a lower portion of the breaker 11 and configured as a double cylinder tube, a first pressurizing portion 14'-1, and a second pressurizing portion 14'-2. ), And a pressurized floatation starch remover, characterized in that it is composed of a starch drain pipe 15 for draining the manure solution finally processed in the third pressure booster 14'-3.

FIG. 7 shows the three pressurizing floaters, which includes a starch moving tube 9 conveyed from an aeration tank, a pressurized flotation induction pipe 14-1 connected to the starch moving tube 9, and the pressurized flotation induction pipe 14 A breaker 11 formed at an upper portion of -1) and the pressurized floatation induction pipe 14-1 are connected to the lower portion and branched into three places, and each branched pressurized floatation induction pipe 14-1 is lowered. Three independent first pressure booster 14'-1, second pressure booster 14'-2, and third pressure booster 14'-3 having the same structure and parts as that of

The first pressurizing part 14'-1, the second pressurizing part 14'-2, and the third pressurizing part 14'-3 are connected to the pressurizing flotation induction pipe 14-1. Floating cross pipe (14-2), the lower portion of the pressure injury cross pipe (14-2) extending to the lower portion of the pressure injury cross pipe (14-3) formed so that the open portion, and the pressure injury cross pipe (14-) 2) is formed in a double to surround the pressurized floating double tube (14-4), the cover 14-5 and the cover (14-5) formed on the outside of the pressurized floating double tube (14-4) It is a pressurizing portion consisting of a starch drainage pipe 15 formed on the lower side of the.

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.

Oxidation injury pressurized starch removal 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 powder is discharged through the solid (min) outlet 13 and used as compost feed,

The urine is moved to the first aeration tank 1-1 through the transfer pipe 4 by the transfer motor 2 formed below the manure solids separation and high speed dehydrator 100, and aerated by the aeration device 5. The air is circulated by the arc pipe 7 extending to the upper part of the first aeration tank 1-1, and the BOD and SS concentrations at this time are aerated at less than 15,000 when the raw water is 80,000. Then, the first aeration tank 1- 1) is transferred to the second aeration tank (1-2) using a transfer motor (2-1) connected to the circulation port 10 formed on one side, the second aeration tank (1-2) is the first aeration tank ( The second aeration tank (1-2) is composed of the same components, apparatus, structure, and form as 1-1), and the BOD and SS concentrations in the second aeration tank (1-2) are less than 15,000 to 5,000. Transfer to the third aeration tank (1-3) by the transfer motor (2-2) formed on the outside of the third aeration tank (1-3), the first and second aeration tank (1-1,1-2) Consists of identical parts, devices, structures and forms The urine is aerated at 80% fermentation state, and then the transfer motor formed outside the third aeration tank (1-3) connected to the circulation port (10) formed on one side of the third aeration tank (1-3). 2-3, the aeration treatment liquid is supplied to the fourth aeration tank 1-4, and the fourth aeration tank 1-4 is the first aeration tank 1-1, the second aeration tank 1-2 and the third aeration tank 1-4. A starch transfer tube composed of the same parts, apparatus, structure, and form as the aeration tank (1-3) and formed on the upper part of each aeration tank (1-1,1-2,1-3,1-4). (9) is transferred to the pressurized wound starch remover 400 'formed on the outside of the fourth aeration tank 1-4, and is provided by the depacking machine 11 installed on the pressurized wound starch remover 400'. As the foam is removed, three first pressurizers 14'-1 and a second pressurizer 14'-2 installed at the lower portion of the starch and unremoved foams are pressurized starch remover 400 '. , The double cylinder tube (14-3, 14-4, 14-5) flows into the lower portion of the third pressing portion 14'-3 Later by a bubble is completely removed while realizing the starch removal rate 90% or more, to remove the starch through a removal pipe (15). (BOD and SS concentration rate at this time maintains 100-200.)

If it is not treated by accident, the untreated starch can be recovered to the transfer pipe 4 through a recovery pipe connected to the starch removal pipe 15 to be reprocessed, and formed at the bottom of each treatment tank. It is possible to drain directly through the drain pipe (drain) 16, and urine fluid to each treatment tank through the circulation port 10 formed in the lower portion of each aeration tank (1-1,1-2,1-3,1-4). It can be circulated.

The urine treated in each treatment tank can be discharged at 20 PPM that meets the effluent standard.

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. The liquid fermentation dehydration storage tank, (113) is a passage to transfer to the gas removal storage tank, using the space of 3㎡ to minimize the level of ammonia, phosphorus or methane mixed with the manure, Solid-liquid fermentation gas generating screw 104 is installed in the dehydration reservoir 112 and to the manure injection through the injector pressure by the gas generating screw motor 111 to rotate the screw separates the methane gas generant mixture to urinary

When moving to the aging tank (6) to remove the odor and methane gas in the preliminary fermentation tank, the gas ejection pipe and the fan 105 is separated by the gas generated in the secondary storage tank 113 and the gas generating screw (104) When the gas is discharged to the outside, the manure sludge filtered from the vibrating screen 102 is introduced through the manure inlet 121 of the high speed dehydrator 108 of FIG. It is operated by hitting with a rotation of 3600 RPM per minute using a high-speed rotating shaft and heating it to have evaporation and fermentation effect, and is easily decomposed easily by the eight blades 124 installed in the motor and the high speed dehydrator 8. After that, the dewatered wastewater is discharged through the external network 125 and the suspend net 127 and at the same time, the fermented sludge is discharged through the fermentation sludge outlet 126,

After the gas is stored in the gas removal storage tank 113 and discharged through the gas discharge pipe and the fan 105,

In the operation method of the aeration device 5, the aeration device 5 is installed in the lower portion of each treatment tank (W, X, Y, Z) as shown in Figure 1, the aeration device as shown in Figure 5 When the motor embedded in the upper portion of the (5) starts to operate, the aeration shaft 17 connected to the aeration device belt connector 16, 16` and the aeration impeller 18 installed below the aeration shaft 17 rotate. To start. 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 the 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, when the aerated starch liquor flows into the pressurized floatation induction pipe 14-1 through the starch transfer pipe 9, a deformer formed on the upper portion of the pressurized floatation induction pipe 14-1 ( 11) and the breaker 11 is connected to the breaker belt connector 25 and 27 of the motor as shown in FIG. 8 by a belt, and an impeller 27` is formed at the lower end of the shaft. Impellers 28 are respectively installed in the middle part, and the impellers 27` and 28 connected to the trapping machine shaft and the packer shaft by the rotation of the motor rotate together while evaporating the fine particles of the crushed liquid. When the bubble starts to rise in the center by the rotation of the chime impeller 28, the bubble is broken by the breaker second chime 27 (27 ') to change into a starch liquid, and the pressure floating induction pipe 14 formed at the bottom as shown in FIG. -3) the first three independent first connected to the lower portion of the pressure floating induction pipe (14-1) While moving to the floating flotation cross pipe 14-2 of the floating unit 14'-1, the second pressurizing unit 14'-2, and the third pressurizing unit 14'-3, respectively (at this time, some starch Starch (urine fluid) flowing from the moving tube (9) may be included), in the enlarged portion formed in the middle portion of the pressure injury cross pipe (14-2) is not eliminated as bubbles are collected, the starch liquid is removed After continuing to move downward to pass through the pressure floating cross pipe bottom 14-3 to reach the open pressure floating double pipe 14-4, the untreated bubble is raised again, the pressure floating double pipe 14-4. The starch liquor is collected and removed at an upper portion of the upper portion of the pressurized double tube (14-4) through the lower portion of the pressurized double tube (14-4) is transferred to the cover (14-5) formed in the cover 14-5 It is a pressurizing portion configured to drain to the starch drainage pipe 15 formed on one side of the).

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 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, The process can be maintained and the series of processes are carried out continuously and automatically by using a mechanical device, which doubles the processing performance, and the aeration device allows the manure, microorganisms and air to be mixed smoothly, defoamed and then pressurized It is economical and eco-friendly to remove starch as injured and process starch of odorless manure.

Claims (4)

In the oxidized injury pressurized starch removal device, the manure discharged from the barn is a manure solids separation and high speed dehydrator (100) for separating solids and liquids introduced from a collection tank filled with water at first, and the manure solids separation and high speed dehydrator (100) The transfer motor 2 for transferring the separated and formed liquid to the first aeration tank (1-1) through the transfer pipe (4), and sequentially formed on the side of the first aeration tank (1-1) The second aeration tank (1-2), the third aeration tank (1--1), which transfers the liquid processed by the transfer motors (2-1, 2-2, 2-3), and is connected to the starch pipe (7) at the top. 3) and the fourth aeration tank (1-4) and pressurized wound starch remover (400 '), The pressurized injured starch remover 400 ′ includes a deformer 11 formed at an upper portion thereof, a first pressurizing portion 14'-1 formed at a lower portion thereof, a second pressurizing portion 14'-2 formed at a lower portion thereof, and a third pressing portion. The floating machine 14'-3 is connected to the pressure floating induction pipe 14-1, and the first pressure booster 14'-1, the second pressure booster 14'-2, A deformer 11 formed at an upper portion of the third pressurizing portion 14'-3 and crushing the bubbles of the manure liquid introduced thereto, and formed at a lower portion of the deformer 11 and formed of a double cylinder type A starch drain pipe 15 for draining the manure solution finally processed by the first pressurizing unit 14'-1, the second pressurizing unit 14'-2, and the third pressurizing unit 14'-3; One of the starch drain pipes 15 is connected to a drain pipe (drain) 16 formed at the bottom of the fourth aeration tank 1-4, and the other is branched to the first aeration tank 1-1. It is characterized in that it is connected to the feed pipe (4) is injected is configured to process again Oxidation injury pressure starch removal unit. The method of claim 1, wherein the first aeration tank (1-1) is connected to a neighboring aeration tank penetrating the upper one side and the starch moving tube (9) for moving the aerated starch, and the first aeration tank (1-) A drain pipe (drain) 16 formed at the lower part of 1) to discharge the manure liquid, if necessary, and an aeration apparatus 5 formed at the outer lower part of the first aeration tank 1-1 to aerated the manure liquid introduced thereto. And an intake pipe 17 and a circulation pipe 6 installed in the first aeration tank 1-1 and connected to the aeration device 5 to circulate the aerated liquid, and the circulation. It is formed in the lower part of the first aeration tank (1-1) and the arc engine (7) connected to the inner upper portion of the first aeration tank (1-1) for supplying air to the pipe (6) and the aeration device (5) A drain pipe (drain) 16 for discharging the internal liquid of the first aeration tank 1-1 and the aeration treatment liquid formed and treated on one side of the first aeration tank 1-1, The second aeration tank (1-2) connected to the circulation port (10) and the circulation port (10) and adjacent to the aeration liquid formed on another side of the first aeration tank (1-1) and aerated A second aeration tank (1-2) for aeration of the transfer motor (2-1), the first aerated liquid transported by the transfer motor (2-1), and the second aeration tank for transfer to The upper part of the (1-2) is connected to the starch pipe (9) extending and branched from the upper portion of the first aeration tank (1-1), the second aeration tank (1-2) is the first aeration tank ( It is composed of the same parts, apparatus, structure and form as 1-1), and is connected to the circulation port 10 formed at one side of the second aeration tank 1-2, and the second aeration tank 1-2. The third aeration tank (1-3) and the third aeration tank (1-3), which are supplied to the aeration treatment liquid by the transfer motor (2-2) formed outside of the second aeration tank (1-2), and formed on another side of the second aeration tank (1-2). ) Is the same as the first aeration tank (1-1) and the second aeration tank (1-2) It is composed of a component, a device, a structure and a shape, and is connected to the circulation port 10 formed on one side of the third aeration tank (1-3), the transfer motor formed on the outside of the third aeration tank (1-3) ( The aeration treatment liquid is supplied by 2-3, and the fourth aeration tank 1-4 and the third aeration tank 1-3 formed on another side of the third aeration tank 1-3 have a first aeration tank 1. -1), the second aeration tank (1-2) and the third aeration tank (1-3) and the same parts, devices, structures and forms, and is formed outside the fourth aeration tank (1-4) , Pressurized floating starch remover (400 ') connected to the starch moving tube (9) characterized in that the oxidized injury pressurized starch removing device. The method of claim 1, wherein the pressurized floating starch remover (400 ') is a starch moving tube (9) for moving the aerated starch, and the three first pressure booster (14' -1) connected to the starch moving tube (9) And a second pressurizing unit 14'-2, a third pressurizing unit 14'-3, and a wave formed at the upper portion of the pressurized injured starch remover 400 'to crush the bubbles of the manure liquid introduced into the wave. Aeration 11, and three pressurizing portion (14 ') formed in the lower portion of the breaker (11) consisting of a double cylinder tube, the first pressing portion (14' -1), the second pressing portion ( 14'-2), the oxidized injury pressurized starch removing apparatus, characterized in that it is composed of a starch drain pipe (15) for draining the manure solution finally processed in the third pressure booster (14'-3). The method according to claim 1 or 3, wherein the three pressing portion, that is, the first pressing portion 14'-1, the second pressing portion 14'-2 and the third pressing portion 14'-3 ) Is composed of the same parts, apparatus, structure and form, the starch transfer pipe (9) conveyed in the aeration tank, the pressurized flotation induction pipe (14-1) connected to the starch transfer pipe (9), and the pressurized flotation induction pipe The breaker 11 formed in the upper part of 14-1, and it is branched into three places connected to the said pressure floating induction pipe 14-1 in the lower part, and each branched pressure floating induction pipe 14-1. It is composed of three independent first pressure booster 14'-1, second pressure booster 14'-2 and third pressure booster 14'-3 having the same structure and parts formed at the bottom of the There is, Each pressurizing part of each of the first pressurizing part 14'-1, the second pressurizing part 14'-2, and the third pressurizing part 14'-3 is the pressurizing part induction pipe 14 -1) the pressurized injury cross pipe (14-2) connected to the, and the pressurized injury cross pipe (14-3) formed to extend to the lower portion of the pressurized injury cross pipe (14-2) to open the upper portion, and the pressurized It is formed in a double to surround the floating cross pipe (14-2) and the pressurized floating double pipe (14-4) of the lower portion, the cover (14-5) formed on the outside of the pressure floating double pipe (14-4) and the Oxidation injury pressurized starch removing apparatus, characterized in that consisting of a starch drain pipe 15 formed on one side of the lower portion of the cover (14-5).