KR200283101Y1 - Apparatus for eradication of starchy - Google Patents

Abstract

The present invention is the present invention is composed of aeration and pressure buoy formed on the outside of the cylindrical device after transferring the liquid separated from the solid-liquid separator of the manure to the cylindrical device formed with four sets of aeration motor, aeration circulation tube and arc organ It is a device for removing starch by pressurized floating starch remover.

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 removal device including an agitating means, an air supply means, a bubble removing means, a mist floatation 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, 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 flotation is improved, after separating sludge and urine by solid-liquid separation and high-speed dehydrator, aeration and aeration machine used as a mixing and stirring device And by evaporating the water and microorganisms contained in the foam by using a bubble removing means, and the method of treating livestock manure by using a mechanical device to continuously and automatically carry out a series of processes. 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

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

Cylindrical device (1), feed motor (2), sensor (3), feed pipe (4), aeration device (5), aeration circulation pipe (6), arc engine (7), inspection port (8), starch transfer pipe ( 9), circulating through-hole (10), breaker (11), pressure buoy (14), pressure injury induction pipe (14-1), pressure injury cross pipe (14-2), pressure injury cross pipe lower (14- 3), pressure floating double pipe (14-4), cover (14-5), starch drain pipe (15), drain pipe (drain) (16), aeration motor suction pipe (17), aeration device belt connector (46.46`), width Axial shaft 47, Aeration impeller 48, Air injection pipe 49, Intake port 50, Bushings 51 and 51 ', Browa 52, Discharge pipes 54 and 54' Connector (25), lower belt end connector (26), puncher shaft (27), packer secondary impeller (27 '), 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, Drainage Pipe 107, Screw Expression 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 1st partition 301, 2nd partition 302, 3rd partition 303, pressurized injured starch remover 400, W: 1 secondary treatment tank, X: secondary treatment tank, Y: tertiary treatment tank, Z 4th treatment tank,

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 the manure to a cylindrical device formed with four sets of aeration motors, aeration circulation pipes and arcs, and then aerations, and then pressurized starch composed of a bubbler and a pressurization device formed outside the cylindrical device. It is a device for removing starch by a 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. , Cylindrical device (1), transfer motor (2), sensor (3), feed pipe (4), aeration device (5), aeration circulation pipe (6), arc engine (7), inspection port (8), starch transfer pipe (9), circulating through hole (10), breaker (11), solid discharge (13), pressurizing floater (14), pressurized float guide pipe (14-1), pressurized floated cross pipe (14-2) ), The lower portion of the pressure injury cross pipe (14-3), the pressure 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 Inlet 50, bushings 51, 51 ', broo 52, discharge pipes 54, 54`, breaker belt upper connector 25, breaker belt lower connector 26, breaker shaft 27 ), Deaerator 2 chime impeller (27 '), deagger 1 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 spraying machine (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), high liquid dehydration storage tank 112, gas removal storage tank 113, vibration motor 114, dehydrator motor (115), tra Switch 116, case 117, inlet 121, mechanical seal 122, vibrating rubber plate 123, blade 124, outer mesh 125, sludge outlet 126, the first partition 301 , Second partition 302, third partition 303, pressurized floating starch remover 400, W: secondary treatment tank, X: secondary treatment tank, Y: tertiary treatment tank, Z: quaternary treatment tank , Indicate It can be seen that.

Looking at the structure, as shown in Figure 1, the manure discharged from the barn is a manure solids separation and high-speed dehydrator (100) and the manure solids separation and separating the solid and liquid flowing in the collection tank filled with water initially A transfer motor 2 formed under the high speed dehydrator 100 to transfer the separated liquid to the cylindrical device 1, a cylindrical device 1 connected to the transfer pipe 4 from the transfer motor 2, and the The first, second and third partitions 301, 302 and 303 formed of three partition walls are formed in the cylindrical device 1 and are divided into the respective treatment tanks W, X, Y and Z. A starch transfer pipe 9 connected to the respective treatment tanks W, X, Y, and Z through the upper one side of the three partitions 301, 302, 303 and moving the aerated starch; and each treatment tank W, X The first, second, and third partitions (301, 302, 303) of Y are formed on one side of the lower portion, and the circulation port (10) for circulating the aerated manure solution and the cylinder Inside the apparatus 1, there are W: primary treatment tanks formed by the first, second, and third partitions 301, 302, 303, X: secondary treatment tanks, Y: tertiary treatment tanks, and Z: quaternary treatment tanks. Four inspection ports 8 formed on the upper part of the processing tanks W, X, Y, and Z, and inside the processing tanks W, X, Y, Z, and the manure, if necessary, A drain pipe (drain) 16 for discharging the liquid, an aeration device 5 for aeration of the manure liquid formed in the lower portion of each of the treatment tanks W, X, Y, and Z, and the aeration device ( 5) connected to the intake pipe 17 and the circulation pipe 6 for circulating the aerated liquid and the upper portion of the cylindrical device 1 for supplying air to the circulation pipe 6 and the aeration device 5; The pressure vessel 7 and the pressure device is formed on the outer side of the cylindrical device 1, the pressurized floatation starch remover 400 connected to the starch transfer pipe 9, and the pressurized floatation starch remover 400 is formed on the wave Aeration 11 and a pressurized flotation formed at the bottom A 14 is connected to the pressure induction induction pipe 14-1, and formed on top of the pressure induction unit 14, the bubbler 11 for crushing the bubbles of the manure liquid introduced, and the wave Starch drain pipe 15 is formed in the lower portion of the aeration 11 and drained the manure solution finally processed in the pressure booster 14 consisting of a double cylinder tube, and one of the starch drain pipe 15 is the third treatment tank It is connected to the drain pipe 16 formed in the lower portion of (Y), and the other side is connected to the feed pipe (4) relates to an oxidized injury pressurized starch removal device, characterized in that configured to be processed 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. The aeration impeller 48 installed at the lower part of the 47 is installed in the aeration cylinder 31, and eight air injection pipes 49 are installed around the aeration shaft 47, and the aeration cylinder 31 is in the middle. 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 floating starch remover, which includes a starch moving tube 9 for moving aerated starches, a pressurizing unit 14 connected to the starch moving tube 9, and an upper portion of the pressing unit 14. Starch for draining the manure solution finally formed in the pressurizer 14 formed in the lower portion of the bubbler 11 and formed in the lower portion of the bubbler 11 and formed to break the foam of the manure liquid introduced and formed It relates to a pressurized floating starch remover, characterized in that consisting of a drain pipe (15).

FIG. 7 shows the pressurizing unit, 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 14-1. A breaker 11 formed at the upper part of the upper part, a pressurized injury cross pipe 14-2 connected to the pressurized injury induction pipe 14-1, and a lower part of the pressurized injury cross pipe 14-2. Pressurized wound cross pipe (14-3) is formed to extend and open the upper portion, and the pressure wound double pipe (14-4) is formed in a double to surround the pressure wound cross pipe (14-2), the lower portion is open; It is a pressurizing floater composed of a cover 14-5 formed on the outside of the pressurized floatation double tube 14-4 and a starch drainage pipe 15 formed on one side of the cover 14-5.

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 treatment tank (W) of the cylindrical device (1) through the conveying pipe (4) by the conveying motor (2) formed under the manure solids separation and high-speed dehydrator (100) aeration device (5) By aeration, the air is circulated by the arc pipe (7) extending to the upper portion of the cylindrical device (1) at this time BOD, SS concentration is less than 15,000 when the raw water 80,000, and then the second treatment tank (X ) Is moved through the starch transfer tube (7), and in the second treatment tank (X), the aeration treatment is performed in the same manner as the first treatment tank (W) to remove the BOD and SS concentration ratios from 15,000 to less than 5,000, The starch transfer tube (7) is transferred to the third treatment tank (Y), and aerated in the same manner as the first and second treatment tanks (W, X), and the urine in the third treatment tank (Y) is 80%. After maintaining the fermentation state of the, through the starch transfer pipe (7) transferred to the fourth processing tank (Z), which is the final processing tank once again the same method as the treatment tank After the last aeration furnace, the starch transfer pipe (7) is transferred to the pressurized flotation starch remover (400) installed on the outside of the cylindrical device (1) by the deburring machine (11) installed on the top of the pressurized wound starch remover (400) As bubbles are removed by the starch, the starch and the bubbles removed are introduced into the lower portion of the pressurization portion 14 installed at the lower portion of the pressurized floating starch remover 400, and the double cylindrical pipes 14-3, 14-4, and 14 The bubble is completely removed by -5) and the starch removal rate is 90% or more, and then the starch removal tube 15 is removed. (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 can be directly drained through the drain pipe (drain) 16, the urine fluid can be circulated to each treatment tank through the circulation port 10 formed in the bottom of the partitions (301, 302, 303) of each treatment tank.

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. 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 discharge pipe and the fan 105 is separated by the gas generated from 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 network 127, the fermentation sludge is discharged through the fermentation sludge outlet 126, and after storing the gas in the gas removal storage 113 and the gas discharge pipe and Discharge through 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 an upper portion 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 is conveyed to the breaker 11 is connected to the belt-belt connector 25 and the breaker shaft 27 of the motor as shown in Figure 8, the lower end of the shaft with an impeller (27`), and 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. -1) through the pressure injury cross pipe (14-2) connected to the lower portion of the pressure injury induction pipe (14-1) While moving (in this case may include starch (urine fluid) introduced from some of the starch moving tube 9), the bubbles not removed in the enlarged portion formed in the middle portion of the pressure injury cross pipe (14-2) is collected After the starch liquid continues to move downward and passes 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 to pressurized injury. The upper part of the double tube 14-4 is collected and removed, and the starch liquid is transferred into the cover 14-5 formed on the outside of the pressurized double tube 14-4 through the lower portion of the pressurized double tube 14-4. To drain into the starch drainage pipe 15 formed on one side of the cover 14-5.

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 (1)

In the pressurized starch removal device for oxidative injury, the transfer motor (2) for separating the manure solids separation and high speed dehydrator (100) and the liquid formed at the lower portion of the manure solids separation and high speed dehydrator (100) to the cylindrical device (2). ), A cylindrical device (1) connected to the transfer pipe (4) from the transfer motor (2), and first, second, and third partitions (301, 302, 303) formed of three partitions to be divided into four equal parts inside the cylindrical device (1). And the first, second and third partitions 301, 302 and 303 through the upper side of each of the first and second partitions 301, 302 and 303, to the respective treatment tanks W, X, Y and Z. Starch transfer pipe (9) which is connected and moves the aerated starch and the first, second and third partitions (301, 302, 303) of the respective treatment tanks (W, X, Y) are formed on one side of the aerated manure W: secondary treatment tank formed by the first, second, third partitions (301, 302, 303) inside the circulation port (10) for circulating the cylindrical device (1), X: secondary treatment tank, Y: tertiary process , Z: the fourth treatment tank, four inspection ports 8 formed on the upper portions of the treatment tanks W, X, Y, and Z to check the inside, and the treatment tanks W, X, Y, A drainage pipe (drain) 16 formed in the lower portion of Z) to discharge the manure liquid, if necessary, and aeration for aerated liquid formed in the inner lower portion of each of the treatment tanks W, X, Y, and Z. Air is supplied to the apparatus 5, the intake pipe 17 and the circulation pipe 6 connected to the aeration device 5 for circulating the aerated liquid, and the circulation pipe 6 and the aeration device 5 The arc engine 7 connected to the upper portion of the cylindrical device 1, and formed on the outer side of the cylindrical device 1, the pressurized floatation starch remover 400 connected to the starch moving tube 9, and the pressurized injury The starch remover 400 is composed of a deformer 11 formed on the upper portion, and a pressurizing portion 14 formed on the lower portion of the starch remover 400 is connected to a pressurizing float induction pipe 14-1. Formed on top Fish starch drainage pipe for crushing the foam of the manure liquid introduced into, and the starch drainage pipe for draining the manure solution finally processed in the pressurizing section (14) formed in the lower portion of the bubbler (11) 15 and one of the starch drain pipes 15 are connected to a drain pipe 16 formed at the lower portion of the third treatment tank Y, and the other branch is connected to the transfer pipe 4. Oxidation injury pressurized starch removal device, characterized in that configured to process again.