CN211035641U - Organic matter high temperature treatment system - Google Patents
Organic matter high temperature treatment system Download PDFInfo
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- CN211035641U CN211035641U CN201920250727.3U CN201920250727U CN211035641U CN 211035641 U CN211035641 U CN 211035641U CN 201920250727 U CN201920250727 U CN 201920250727U CN 211035641 U CN211035641 U CN 211035641U
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Abstract
The utility model discloses an organic matter high temperature treatment system, a serial communication port, include: the device comprises a sand removing device, an adjusting device, a reaction kettle, a pressure release tower, a heat exchanger, a first guide pipe, a first tank body, a first motor, a stirring paddle, a packing auger and a first discharge pipe, wherein the first motor is fixedly arranged at the upper end of the first tank body; the stirring paddle is vertically arranged, the upper end of the stirring paddle is in driving connection with a driving shaft of the first motor, and the lower end of the stirring paddle is arranged in the first tank body; the packing auger is obliquely arranged, the lower end of the packing auger extends into the first tank body, and the lower end of the packing auger is communicated with the bottom of the first tank body; the second tank body is provided with the circulating pump, and the circulating pump is used for internally circulating the materials in the second tank body, so that the materials in the second tank body are fully contacted with water vapor, hydrolysis of organic matters is accelerated, macromolecular chains of the organic matters are hydrolyzed into micromolecular chains, and the later methane generation rate is accelerated.
Description
Technical Field
The utility model relates to an organic waste handles technical field, concretely relates to organic matter high temperature treatment system.
Background
Organic waste can be fermented to generate biogas for human reuse, most of organic matters in the prior art, such as chicken manure, are directly put into a fermentation tank for fermentation, and the biogas generation rate is low.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to overcome above-mentioned technique not enough, provide an organic matter high temperature treatment system, solve the organic waste among the prior art and directly drop into the fermentation cylinder and ferment, marsh gas produces the lower technical problem of speed.
In order to achieve the above technical purpose, the technical solution of the present invention provides an organic matter high temperature treatment system, which is characterized by comprising: the device comprises a sand removing device, an adjusting device, a reaction kettle, a pressure release tower, a heat exchanger, a first guide pipe, a first tank body, a first motor, a stirring paddle, a packing auger and a first discharge pipe, wherein the first motor is fixedly arranged at the upper end of the first tank body; the stirring paddle is vertically arranged, the upper end of the stirring paddle is in driving connection with a driving shaft of the first motor, and the lower end of the stirring paddle is arranged in the first tank body; the packing auger is obliquely arranged, the lower end of the packing auger extends into the first tank body, the lower end of the packing auger is communicated with the bottom of the first tank body, and the upper end of the packing auger extends to the outside of the first tank body; one end of the first discharge pipe is communicated with the inner cavity of the first tank body, and the other end of the first discharge pipe extends to the outside of the first tank body; the adjusting device comprises a second tank body, a circulating pump, a second feeding pipe and a second discharging pipe, wherein a first inner circulating port communicated with an inner cavity of the second tank body is formed in the middle of the second tank body, and a second inner circulating port communicated with the inner cavity of the second tank body is formed in the lower part of the second tank body; a steam inlet is formed in the area, located between the first inner circulation port and the second inner circulation port, of the second tank body; the feed end of the circulating pump is communicated with the second internal circulation port, and the discharge end of the circulating pump is communicated with the first circulation port; one end of the second feeding pipe is communicated with an inner cavity at the upper part of the second tank body, and the other end of the second feeding pipe is communicated with the first discharging pipe; one end of the second discharge pipe is communicated with the lower inner cavity of the second tank body; the reaction kettle comprises a third tank body, a fourth tank body, a third feeding pipe, a third discharging pipe, a third gas inlet pipe, a third gas exhaust pipe and a third slag discharge pipe, wherein the third tank body is arranged in the fourth tank body, and the upper end of the third tank body is opened; one end of the third slag discharge pipe penetrates through the fourth tank body and is communicated with the lower end of the third tank body; one end of each of the third air inlet pipe and the third material inlet pipe penetrates through the fourth tank body and then is communicated with the lower part of the third tank body, the position where the third air inlet pipe is communicated with the third tank body is higher than the position where the third air inlet pipe is communicated with the third tank body, and the other end of the third material inlet pipe is communicated with the other end of the second material outlet pipe through the first flow guide pipe; one end of the third discharge pipe is communicated with the lower end of the fourth tank body; one end of the third exhaust pipe is communicated with the upper end of the fourth tank body, and the other end of the third exhaust pipe is communicated with a steam inlet on the second tank body; the heat exchanger is arranged on the first conduit; the pressure relief tower comprises a fifth tank body, a fourth feeding pipe, a fourth discharging pipe and a fourth discharging pipe, wherein one end of the fourth feeding pipe is communicated with one side of the middle part of the fifth tank body, and the other end of the fourth feeding pipe is communicated with the third discharging pipe; one end of the fourth discharging pipe is communicated with the other side of the middle part of the fifth tank body, and the other end of the fourth discharging pipe is communicated with the fermentation tank; one end of the fourth exhaust pipe is communicated with the top of the fifth tank body, and the other end of the fourth exhaust pipe is communicated with a steam inlet on the second tank body.
Compared with the prior art, the beneficial effects of the utility model include: the first tank body in the organic matter high-temperature treatment system is used for containing chicken manure pulled from a chicken farm, water needs to be added into the first tank body while the chicken manure is added into the first tank body, the first motor is started at the same time, the first motor drives the stirring paddle to rotate, and the stirring paddle homogenizes the chicken manure in the first tank body; the packing auger is started, sand grains precipitated at the bottom of the first tank body are discharged by the packing auger, the sand grains in the chicken manure are prevented from blocking a pipeline in subsequent fermentation equipment, and two functions of homogenizing and desanding can be realized by one equipment; the second tank body is provided with the circulating pump, and the circulating pump is used for internally circulating the materials in the second tank body, so that the materials in the second tank body are fully contacted with water vapor, the hydrolysis of organic matters is accelerated, macromolecular chains of the organic matters are hydrolyzed into micromolecular chains, and the later methane generation rate is accelerated; the steam entering the second tank from the steam inlet of the second tank comes from the reaction kettle, so that the heat in the reaction kettle is fully utilized, and the waste of a heat source is avoided; the material in the adjusting device enters the reaction kettle through the first conduit to be continuously hydrolyzed and fluidized; the heat exchanger is used for heating the material flowing through the first conduit; after the hydrolysis and fluidization of the material in the reaction kettle are completed, the material enters the pressure release tower through the third discharge pipe to be cooled and decompressed, and then is directly conveyed to the fermentation tank through the fourth discharge pipe to be fermented, and at the moment, high-temperature bacteria are adopted in the fermentation tank to ferment, so that the methane production rate is further increased.
Drawings
Fig. 1 is a schematic view of the three-dimensional structure of the sand removing device of the present invention.
Fig. 2 is a schematic diagram of the planar layout structure of the present invention.
Fig. 3 is a schematic view of the internal structure of the sand removing device of the present invention.
Fig. 4 is a schematic view of the internal structure of the adjusting device of the present invention.
Fig. 5 is a schematic diagram of the internal structure of the reaction kettle of the present invention.
Fig. 6 is a schematic top view of the steam spraying plate of the present invention.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more clearly understood, the present invention is further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
Referring to fig. 1 to 6, the present embodiment provides a high temperature processing system for organic materials, comprising: the device comprises a sand removing device 1, a regulating device 2, a reaction kettle 3, a pressure release tower 4, a heat exchanger 5, a first conduit 6 and a crystallization tower 7.
The sand removing device 1 comprises a first tank body 11, a first motor 12, a stirring paddle 13, an auger 14 and a discharge pipe 15.
The first motor 12 is fixedly arranged at the upper end of the first tank body 11; the stirring paddle 13 is vertically arranged, the upper end of the stirring paddle 13 is in driving connection with the driving shaft of the first motor 11, and the lower end of the stirring paddle 13 is arranged in the first tank 11, in this embodiment, the driving shaft of the first motor 12 is coaxially and fixedly connected with the upper end of the stirring paddle 13, and the driving shaft of the first motor 12 can also be in driving connection with the stirring paddle 12 through a gearbox; the packing auger 14 is obliquely arranged, the lower end of the packing auger 14 extends into the first tank body 11, the lower end of the packing auger 14 is communicated with the bottom of the first tank body 11, and the upper end of the packing auger 14 extends to the outside of the first tank body 11; one end of the first discharge pipe 15 is communicated with the inner cavity of the first tank body 11, and the other end of the first discharge pipe 15 extends to the outside of the first tank body 11; the first tank 11 in the sand removing device 1 is used for containing chicken manure pulled from a chicken farm, water needs to be added into the first tank 11 while the chicken manure is added into the first tank 11, the first motor 11 is started at the same time, the first motor 11 drives the stirring paddle 13 to rotate, and the stirring paddle 13 homogenizes the chicken manure in the first tank 11; start auger 14, auger 14 will the grit that first jar of body 11 bottoms settled is discharged, avoids the grit in the chicken manure to cause the jam to the pipeline in the follow-up fermentation equipment to two functions of homogenate, degritting can be realized to a equipment.
Specifically, the auger 14 comprises a riser 141, a second motor 142, a lifting shaft 143, auger blades 144 and a sand discharge pipe 145, wherein the riser 141 is obliquely arranged, the lower end of the riser 141 extends to the inside of the first tank 11, the lower end of the riser 141 is communicated with the bottom of the first tank 11, the riser 141 is fixedly connected with the first tank 11, and the upper end of the riser 141 extends to the outside of the first tank 11; the second motor 142 is fixedly mounted at the upper end of the lift pipe 141, the lift shaft 143 is coaxially disposed in the lift pipe 141, the lower end of the lift shaft 143 is rotatably connected to the bottom of the first tank 11, and the upper end of the lift shaft 143 is drivingly connected to the driving shaft of the second motor 142, specifically, the driving shaft of the second motor 142 may be directly coaxially and fixedly connected to the upper end of the lift shaft 141, and the driving shaft of the second motor 142 may also be drivingly connected to the lift shaft 143 through a gearbox; the auger blade 144 is arranged in the riser 141, the auger blade 144 is spirally fixed on the outer circumferential surface of the lifting shaft 143, and the outer edge of the auger blade 144 is arranged close to the inner circumferential surface of the riser 141; the sand discharge pipe 145 is vertically arranged, the upper end of the sand discharge pipe 145 is communicated with the inner cavity at the upper end of the riser 141, and the sand discharge pipe 145 is fixedly connected with the riser 141.
In this embodiment, the upper end of the first tank 11 is open, so that a user can add chicken manure and water into the first tank 11 from the upper end of the first tank 11; place in first discharging pipe 15 the one end of first jar of body 11 is located the below of stirring rake 13, and place in first discharging pipe 15 the one end of first jar of body 11 is higher than the lower extreme of auger 14 is arranged, place in first discharging pipe 15 the one end opening of first jar of body 11 is down, thereby avoids the chicken manure jam of whereabouts first discharging pipe 15 to start earlier first motor 12 carries out homogenate, closes after the homogenate is accomplished first motor 12, start second motor 142 carries out the sand discharge.
Preferably, the cross-sectional area of the inner cavity at the lower end of the first tank 11 is gradually reduced from top to bottom, which is beneficial to settling sand particles to the lower end of the lifting pipe 141, thereby facilitating sand discharge.
The adjusting device 2 comprises a second tank body 21, a circulating pump 22, a second feeding pipe 23 and a second discharging pipe 24, a first inner circulation port 21a communicated with an inner cavity of the second tank body 21 is formed in the middle of the second tank body 21, and a second inner circulation port 21b communicated with the inner cavity of the second tank body 21 is formed in the lower portion of the second tank body 21; a steam inlet 21c is formed in the area, located between the first internal circulation port 21a and the second internal circulation port 21b, of the second tank 21; the feed end of the circulating pump 22 is communicated with the second internal circulation port 21b, and the discharge end of the circulating pump 22 is communicated with the first circulation port 21 a; one end of the second feeding pipe 23 is communicated with the upper inner cavity of the second tank body 21; one end of the second discharge pipe 24 is communicated with the lower inner cavity of the second tank 21.
The reaction kettle 3 comprises a third tank 31, a fourth tank 32, a third feeding pipe 33, a third discharging pipe 34, a third feeding pipe 35, a third discharging pipe 36, a third slag discharging pipe 37 and a steam spraying disc 38, wherein the third tank 31 is arranged in the fourth tank 32, and the upper end of the third tank 31 is open; one end of the third slag discharge pipe 37 penetrates through the fourth tank 32 and then is communicated with the lower end of the third tank 31; the third air inlet pipe 35 and the third air inlet pipe 33 have one end penetrating through the fourth tank 32 and then communicating with the lower part of the third tank 31, the position where the third air inlet pipe 33 communicates with the third tank 31 is higher than the position where the third air inlet pipe 35 communicates with the third tank 31, and the other end of the third air inlet pipe 33 communicates with the other end of the second discharge pipe 24 through the first guide pipe 6; one end of the third discharge pipe 34 is communicated with the lower end of the fourth tank 32; one end of the third exhaust pipe 36 is communicated with the upper end of the fourth tank 32, and the other end of the third exhaust pipe 36 is communicated with a steam input port 21c on the second tank 21; the heat exchanger 5 is arranged on the first conduit 6; the steam spray disk 38 is horizontally arranged in the third tank 31, a plurality of air injection holes 38a penetrating through the upper end surface and the lower end surface of the steam spray disk 38 are formed in the steam spray disk 38, the position where the steam spray disk 38 is arranged is higher than the position where the third air inlet pipe 35 is communicated with the third tank 31, and the position where the steam spray disk 38 is arranged is lower than the position where the third air inlet pipe 33 is communicated with the third tank 31.
The pressure relief tower 4 comprises a fifth tank body, a fourth feeding pipe, a fourth discharging pipe and a fourth discharging pipe, wherein one end of the fourth feeding pipe is communicated with one side of the middle part of the fifth tank body, and the other end of the fourth feeding pipe is communicated with the third discharging pipe; one end of the fourth discharging pipe is communicated with the other side of the middle part of the fifth tank body, and the other end of the fourth discharging pipe is communicated with the fermentation tank; one end of the fourth exhaust pipe is communicated with the top of the fifth tank body, and the other end of the fourth exhaust pipe is communicated with a steam input port 21c on the second tank body 21; in the organic matter high-temperature treatment system, the circulating pump 22 is arranged on the second tank 21, and the circulating pump 22 is used for internally circulating the materials in the second tank 21, so that the materials in the second tank 21 are fully contacted with water vapor, the hydrolysis of the organic matters is accelerated, macromolecular chains of the organic matters are hydrolyzed into micromolecular chains, and the later methane generation rate is accelerated; the steam entering the second tank 21 from the steam inlet 21c of the second tank 21 comes from the reaction kettle 3, so that the heat in the reaction kettle 3 is fully utilized, and the waste of a heat source is avoided; the material in the adjusting device 2 enters the reaction kettle 3 through the first conduit 6 to be continuously hydrolyzed and fluidized; the heat exchanger 5 is used for heating the material flowing through the first conduit 6; after the hydrolysis and fluidization of the material in the reaction kettle 3 are completed, the material enters the pressure release tower 4 through the third discharge pipe 34 for cooling and pressure release, and then the material is directly conveyed to the fermentation tank through the fourth discharge pipe for fermentation, and at the moment, the fermentation tank is fermented by high-temperature bacteria, so that the methane production rate is further increased.
In this embodiment, the second tank 21 is provided with three steam input holes 21c, and the second tank 21 is provided with two second discharge pipes 24; the reaction kettles 3, the heat exchanger 5 and the first guide pipes 6 are all provided with two, the uniform ends of the two first guide pipes 6 are communicated with the two second discharge pipes 24 in a one-to-one correspondence manner, and the other ends of the two first guide pipes 6 are communicated with the two reaction kettles 3 in a one-to-one correspondence manner; each first conduit 6 is provided with one heat exchanger 5; the third exhaust pipes 36 on the two reaction kettles 3 are communicated with the two steam input holes 21c on the second tank 31 in a one-to-one correspondence manner; the fourth exhaust pipe is communicated with a third steam input hole 21c on the second tank 21, so that the water vapor in the pressure release tower 4 is also recovered to the regulating device 2; a lift pump 6a is arranged on the first conduit 6; the middle side wall of the second tank body 21 is provided with a temperature adjusting water inlet 21 f.
An ammonia gas recovery port 21d is formed in the upper portion of the second tank 21, a slag discharge port 21e is formed in the lower portion of the second tank 21, and the ammonia gas recovery port 21d is communicated with the crystallization tower 7.
In this embodiment, the third feeding pipe 33, the third discharging pipe 34, the third feeding pipe 35, the third discharging pipe 36 and the third deslagging pipe 37 are all provided with electromagnetic valves, and the positions where the third feeding pipe 33 and the third feeding pipe 35 are communicated with the third tank 31 are all provided with temperature detecting elements and pressure detecting elements; and the third discharge pipe 34, the third exhaust pipe 36 and the fourth tank 32 are respectively provided with a temperature detection element and a pressure detection element at the positions communicated with each other, so that the automatic control and the maintenance are facilitated.
The working principle is as follows: in the organic matter high-temperature treatment system, the circulating pump 22 is arranged on the second tank 21, and the circulating pump 22 is used for internally circulating the materials in the second tank 21, so that the materials in the second tank 21 are fully contacted with water vapor, the hydrolysis of the organic matters is accelerated, macromolecular chains of the organic matters are hydrolyzed into micromolecular chains, and the later methane generation rate is accelerated; the steam entering the second tank 21 from the steam inlet 21c of the second tank 21 comes from the reaction kettle 3, so that the heat in the reaction kettle 3 is fully utilized, and the waste of a heat source is avoided; the material in the adjusting device 2 enters the reaction kettle 3 through the first conduit 6 to be continuously hydrolyzed and fluidized; the heat exchanger 5 is used for heating the material flowing through the first conduit 6; after the hydrolysis and fluidization of the material in the reaction kettle 3 are completed, the material enters the pressure release tower 4 through the third discharge pipe 34 for cooling and pressure release, and then the material is directly conveyed to the fermentation tank through the fourth discharge pipe for fermentation, and at the moment, the fermentation tank is fermented by high-temperature bacteria, so that the methane production rate is further increased.
The above description of the present invention does not limit the scope of the present invention. Any other corresponding changes and modifications made according to the technical idea of the present invention should be included in the scope of the claims of the present invention.
Claims (10)
1. A high temperature treatment system for organic matter, comprising: the device comprises a sand removing device, an adjusting device, a reaction kettle, a pressure release tower, a heat exchanger, a first guide pipe, a first tank body, a first motor, a stirring paddle, a packing auger and a first discharge pipe, wherein the first motor is fixedly arranged at the upper end of the first tank body; the stirring paddle is vertically arranged, the upper end of the stirring paddle is in driving connection with a driving shaft of the first motor, and the lower end of the stirring paddle is arranged in the first tank body; the packing auger is obliquely arranged, the lower end of the packing auger extends into the first tank body, the lower end of the packing auger is communicated with the bottom of the first tank body, and the upper end of the packing auger extends to the outside of the first tank body; one end of the first discharge pipe is communicated with the inner cavity of the first tank body, and the other end of the first discharge pipe extends to the outside of the first tank body; the adjusting device comprises a second tank body, a circulating pump, a second feeding pipe and a second discharging pipe, wherein a first inner circulating port communicated with an inner cavity of the second tank body is formed in the middle of the second tank body, and a second inner circulating port communicated with the inner cavity of the second tank body is formed in the lower part of the second tank body; a steam inlet is formed in the area, located between the first inner circulation port and the second inner circulation port, of the second tank body; the feed end of the circulating pump is communicated with the second internal circulation port, and the discharge end of the circulating pump is communicated with the first internal circulation port; one end of the second feeding pipe is communicated with an inner cavity at the upper part of the second tank body, and the other end of the second feeding pipe is communicated with the first discharging pipe; one end of the second discharge pipe is communicated with the lower inner cavity of the second tank body; the reaction kettle comprises a third tank body, a fourth tank body, a third feeding pipe, a third discharging pipe, a third gas inlet pipe, a third gas exhaust pipe and a third slag discharge pipe, wherein the third tank body is arranged in the fourth tank body, and the upper end of the third tank body is opened; one end of the third slag discharge pipe penetrates through the fourth tank body and is communicated with the lower end of the third tank body; one end of each of the third air inlet pipe and the third material inlet pipe penetrates through the fourth tank body and then is communicated with the lower part of the third tank body, the position where the third material inlet pipe is communicated with the third tank body is higher than the position where the third air inlet pipe is communicated with the third tank body, and the other end of the third material inlet pipe is communicated with the other end of the second material outlet pipe through the first guide pipe; one end of the third discharge pipe is communicated with the lower end of the fourth tank body; one end of the third exhaust pipe is communicated with the upper end of the fourth tank body, and the other end of the third exhaust pipe is communicated with a steam inlet on the second tank body; the heat exchanger is arranged on the first conduit; the pressure relief tower comprises a fifth tank body, a fourth feeding pipe, a fourth discharging pipe and a fourth discharging pipe, wherein one end of the fourth feeding pipe is communicated with one side of the middle part of the fifth tank body, and the other end of the fourth feeding pipe is communicated with the third discharging pipe; one end of the fourth discharging pipe is communicated with the other side of the middle part of the fifth tank body, and the other end of the fourth discharging pipe is communicated with the fermentation tank; one end of the fourth exhaust pipe is communicated with the top of the fifth tank body, and the other end of the fourth exhaust pipe is communicated with a steam inlet on the second tank body.
2. The organic matter high-temperature treatment system according to claim 1, wherein the reaction kettle further comprises a steam spray tray, the steam spray tray is horizontally arranged in the third tank body, a plurality of air injection holes penetrating through the upper end surface and the lower end surface of the steam spray tray are formed in the steam spray tray, the steam spray tray is arranged at a position higher than the position where the third air inlet pipe is communicated with the third tank body, and the position of the steam spray tray is lower than the position where the third air inlet pipe is communicated with the third tank body.
3. The organic matter high-temperature treatment system according to claim 1, wherein the second tank body is provided with three steam input holes, and the second tank body is provided with two second discharge pipes; the reaction kettles, the heat exchanger and the first guide pipes are all provided with two, one end of each of the two first guide pipes is communicated with the two second discharge pipes in a one-to-one correspondence mode, and the other ends of the two first guide pipes are communicated with the two reaction kettles in a one-to-one correspondence mode; each first conduit is provided with one heat exchanger; the third exhaust pipes on the two reaction kettles are communicated with the two steam input holes on the second tank body in a one-to-one correspondence manner; the fourth exhaust pipe is communicated with the third steam input hole on the second tank body.
4. The organic high temperature treatment system of claim 1, wherein a lift pump is disposed on the first conduit.
5. The high temperature treatment system for organic matter according to claim 1, further comprising a crystallization tower; an ammonia gas recovery port is formed in the upper portion of the second tank body, a slag discharge port is formed in the lower portion of the second tank body, and the ammonia gas recovery port is communicated with the crystallization tower.
6. The organic matter high-temperature treatment system according to claim 1, wherein electromagnetic valves are arranged on the third feeding pipe, the third discharging pipe, the third feeding pipe, the third discharging pipe and the third deslagging pipe, and a temperature detection element and a pressure detection element are arranged at positions where the third feeding pipe and the third feeding pipe are communicated with the third tank body; and the third discharge pipe, the third exhaust pipe and the fourth tank body are communicated with each other, and a temperature detection element and a pressure detection element are arranged at the positions of the third discharge pipe, the third exhaust pipe and the fourth tank body.
7. The organic matter high-temperature treatment system according to claim 1, wherein the first discharge pipe is arranged in the first tank body, one end of the first discharge pipe is positioned below the stirring paddle, and one end of the first discharge pipe arranged in the first tank body is higher than the lower end of the packing auger.
8. The organic high temperature treatment system of claim 7, wherein the first discharge pipe is disposed in the first tank with an end opening facing downward.
9. The organic matter high-temperature treatment system according to claim 1, wherein the auger comprises a riser, a second motor, a lifting shaft, auger blades and a sand discharge pipe, the riser is obliquely arranged, the lower end of the riser extends into the first tank body, the lower end of the riser is communicated with the bottom of the first tank body, the riser is fixedly connected with the first tank body, and the upper end of the riser extends to the outside of the first tank body; the second motor is fixedly arranged at the upper end of the lifting pipe, the lifting shaft is coaxially arranged in the lifting pipe, the lower end of the lifting shaft is rotatably connected with the bottom of the first tank body, and the upper end of the lifting shaft is in driving connection with a driving shaft of the second motor; the auger blade is arranged in the riser, the auger blade is spirally fixed on the outer peripheral surface of the lifting shaft, and the outer edge of the auger blade is arranged close to the inner peripheral surface of the riser; the sand discharge pipe is vertically arranged, the upper end of the sand discharge pipe is communicated with the inner cavity at the upper end of the lifting pipe, and the sand discharge pipe is fixedly connected with the lifting pipe.
10. The organic high-temperature treatment system according to claim 1, wherein the upper end of the first tank is open; the cross-sectional area of the inner cavity at the lower end of the first tank body is gradually reduced from top to bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920250727.3U CN211035641U (en) | 2019-02-28 | 2019-02-28 | Organic matter high temperature treatment system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201920250727.3U CN211035641U (en) | 2019-02-28 | 2019-02-28 | Organic matter high temperature treatment system |
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| CN211035641U true CN211035641U (en) | 2020-07-17 |
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| CN201920250727.3U Expired - Fee Related CN211035641U (en) | 2019-02-28 | 2019-02-28 | Organic matter high temperature treatment system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109748476A (en) * | 2019-02-28 | 2019-05-14 | 周嘉豪 | A kind of organic matter high-temperature process system |
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2019
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109748476A (en) * | 2019-02-28 | 2019-05-14 | 周嘉豪 | A kind of organic matter high-temperature process system |
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| TR01 | Transfer of patent right |
Effective date of registration: 20200708 Address after: 430000 No.189, group 4, dongmenhe village, Qingquan Town, Xishui County, Huanggang City, Hubei Province Patentee after: Dihui environmental protection equipment (Hubei) Co.,Ltd. Address before: 430000 Dongmenhe Village, Qingquan Town, Huanggang City, Hubei Province, Group 4, 189 Patentee before: Zhou Jiahao |
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| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20200717 |
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| CF01 | Termination of patent right due to non-payment of annual fee |