CN111517614A - Superconducting dry-wet separator - Google Patents
Superconducting dry-wet separator Download PDFInfo
- Publication number
- CN111517614A CN111517614A CN202010465677.8A CN202010465677A CN111517614A CN 111517614 A CN111517614 A CN 111517614A CN 202010465677 A CN202010465677 A CN 202010465677A CN 111517614 A CN111517614 A CN 111517614A
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- Prior art keywords
- pipe
- cylinder
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- stainless steel
- recovery
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- 238000000926 separation method Methods 0.000 claims abstract description 52
- 229910001220 stainless steel Inorganic materials 0.000 claims abstract description 46
- 239000010935 stainless steel Substances 0.000 claims abstract description 46
- 238000011084 recovery Methods 0.000 claims abstract description 42
- 238000010438 heat treatment Methods 0.000 claims abstract description 30
- 239000007788 liquid Substances 0.000 claims abstract description 10
- 239000007789 gas Substances 0.000 claims description 37
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 34
- 244000144972 livestock Species 0.000 claims description 15
- 244000144977 poultry Species 0.000 claims description 14
- 210000003608 fece Anatomy 0.000 claims description 12
- 239000010871 livestock manure Substances 0.000 claims description 12
- 239000010865 sewage Substances 0.000 claims description 10
- 239000002893 slag Substances 0.000 claims description 8
- 239000010802 sludge Substances 0.000 claims description 7
- 239000000126 substance Substances 0.000 claims description 7
- 239000010806 kitchen waste Substances 0.000 claims description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 8
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 238000009395 breeding Methods 0.000 description 3
- 230000001488 breeding effect Effects 0.000 description 3
- 238000002309 gasification Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/13—Treatment of sludge; Devices therefor by de-watering, drying or thickening by heating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Treatment Of Sludge (AREA)
Abstract
The invention discloses a superconducting dry-wet separator, which comprises a stainless steel separation cylinder, a superconducting pipe, a compressor, a vacuum cylinder, a recovery cylinder, a buoy, a feeding pipe, a gas conduction pipe and a recovery pipe; the feeding pipe is communicated with the stainless steel separation cylinder, the superconducting pipe is arranged in the inner cavity of the stainless steel separation cylinder, superconducting liquid is arranged in the superconducting pipe, a heating chamber is formed at the bottom of the stainless steel separation cylinder, the heating chamber is communicated with the compressor, and hot gas is provided for the heating chamber by the compressor; the stainless steel separation cylinder is communicated with the vacuum cylinder through a gas conduction pipe, the gas conduction pipe is provided with an electromagnetic valve A, an atomized cold gas pipe of the compressor is communicated with the vacuum cylinder, the vacuum cylinder is communicated with the recovery cylinder through a recovery pipe, and the recovery pipe is provided with an electromagnetic valve C and a vacuum pump; the inside of the recovery cylinder is provided with a buoy, and the end part of the recovery pipe extends into the buoy. The device has simple structure and high operation efficiency, and realizes the dry-wet separation rapidly through superconducting heating.
Description
Technical Field
The invention relates to the field related to separation of sludge, livestock and poultry manure and kitchen waste, in particular to a superconductive dry-wet separator.
Background
At present, the separation and treatment of sludge, livestock and poultry manure and kitchen waste are necessary, and if the sludge, the livestock and poultry manure and the kitchen waste are not treated properly, the environment is polluted, and resources are wasted. The method is particularly suitable for livestock and poultry manure, and with the development of the modern livestock and poultry breeding industry and the rise of industrial intensive breeding, the material requirements of people are enriched, but the flooding of livestock and poultry sewage is also brought, and the pollution to water sources, air and environment is caused. The existing breeding excrement treatment machine has a complex structure and is difficult to quickly and effectively separate the raw excrement sewage or sludge of the livestock excrement.
Disclosure of Invention
Accordingly, to address the above-described deficiencies, the present invention provides a superconducting wet and dry separator. The device has simple structure and high operation efficiency, and realizes the dry-wet separation rapidly through superconducting heating.
The invention is realized by constructing a superconducting dry-wet separator, which is characterized in that; comprises a stainless steel separation cylinder, a superconducting pipe, a compressor, a vacuum cylinder, a recovery cylinder, a buoy, a feeding pipe, a gas conduction pipe and a recovery pipe; the feeding pipe is communicated with the stainless steel separation cylinder, the superconducting pipe is arranged in the inner cavity of the stainless steel separation cylinder, superconducting liquid is arranged in the superconducting pipe, a heating chamber is formed at the bottom of the stainless steel separation cylinder, the heating chamber is communicated with the compressor, and hot gas is provided for the heating chamber by the compressor; the stainless steel separation cylinder is communicated with the vacuum cylinder through a gas conduction pipe, the gas conduction pipe is provided with an electromagnetic valve A, an atomized cold gas pipe of the compressor is communicated with the vacuum cylinder, the vacuum cylinder is communicated with the recovery cylinder through a recovery pipe, and the recovery pipe is provided with an electromagnetic valve C and a vacuum pump; the inside of the recovery cylinder is provided with a buoy, and the end part of the recovery pipe extends into the buoy.
The superconducting dry-wet separator is characterized in that; the feeding pipe is provided with a sewage inlet valve.
The superconducting dry-wet separator is characterized in that; the superconducting pipes are in multiple groups and are vertically arranged in the stainless steel separating cylinder respectively.
The superconducting dry-wet separator is characterized in that; the bottom of the vacuum cylinder is provided with a drain pipe, and the drain pipe is provided with an electromagnetic valve B and a water pump.
The superconducting dry-wet separator is characterized in that; the bottom of the side surface of the stainless steel separation barrel is provided with a slag outlet door.
The superconducting dry-wet separator is characterized in that; a water level gauge is arranged on the side surface of the vacuum cylinder.
The superconducting dry-wet separator is characterized in that; the operation is as follows; opening a sewage inlet valve, and conveying substances to be separated into the stainless steel separation cylinder through a feed pipe; starting a compressor to work, on one hand, heating the heating chamber by the compressor to heat the superconducting pipe, uniformly heating the inner cavity of the stainless steel separation cylinder by the superconducting pipe, and keeping the temperature in the stainless steel separation cylinder within the range of 30-60 ℃ to realize gasification and separation of substances to be separated; then the electromagnetic valve A is opened, the separated mixed gas enters the vacuum cylinder through the gas conduction pipe, and meanwhile, the compressor inputs atomized cold air into the vacuum cylinder through the atomized cold air pipe to cool the water vapor in the mixed gas which is just transmitted into the liquid water; and opening the electromagnetic valve C and the vacuum pump, and enabling other gases in the vacuum cylinder to enter the floating cylinder through the recovery pipe to be recovered.
The superconducting dry-wet separator is characterized in that; the substances to be separated are sludge, livestock and poultry manure and kitchen waste.
The invention has the following advantages: the present invention provides a superconducting wet-dry separator by improvement, as shown in fig. 1; comprises a stainless steel separation cylinder, a superconducting pipe, a compressor, a vacuum cylinder, a recovery cylinder, a buoy, a feeding pipe, a gas conduction pipe and a recovery pipe; the feeding pipe is communicated with the stainless steel separation cylinder, the superconducting pipe is arranged in the inner cavity of the stainless steel separation cylinder, superconducting liquid is arranged in the superconducting pipe, a heating chamber is formed at the bottom of the stainless steel separation cylinder, the heating chamber is communicated with the compressor, and hot gas is provided for the heating chamber by the compressor; the stainless steel separation cylinder is communicated with the vacuum cylinder through a gas conduction pipe, the gas conduction pipe is provided with an electromagnetic valve A, an atomized cold gas pipe of the compressor is communicated with the vacuum cylinder, the vacuum cylinder is communicated with the recovery cylinder through a recovery pipe, and the recovery pipe is provided with an electromagnetic valve C and a vacuum pump; the inside of the recovery cylinder is provided with a buoy, and the end part of the recovery pipe extends into the buoy. Opening a sewage inlet valve, and conveying the livestock and poultry manure into the stainless steel separation through a feed pipe; starting a compressor to work, on one hand, heating the heating chamber by the compressor to heat the superconducting pipe, and heating the inner cavity of the stainless steel separation cylinder after the superconducting pipe is uniformly heated to keep the temperature in the stainless steel separation cylinder within the range of 30-60 ℃ so as to realize gasification separation of livestock and poultry manure; then the electromagnetic valve A is opened, the separated mixed gas (nitrogen, methane and water vapor) enters the vacuum cylinder through the gas conduction pipe, and meanwhile, the compressor inputs atomized cold air into the vacuum cylinder through the atomized cold air pipe to cool the water vapor in the mixed gas which is just transmitted into the vacuum cylinder into liquid water; and opening the electromagnetic valve C and the vacuum pump, and enabling nitrogen and methane gas in the vacuum cylinder to enter the buoy through the recovery pipe to be recovered. After the treatment is finished, opening a slag outlet door, and removing slag in the stainless steel separation cylinder; the water level condition in the vacuum cylinder can be observed through the water level meter, and when the water level is high, the electromagnetic valve B and the water suction pump can be opened to discharge water through the water discharge pipe. The device has simple structure and high operation efficiency, and realizes the dry-wet separation rapidly through superconducting heating.
Drawings
Fig. 1 is a schematic view of the overall structure of the present invention.
Wherein: the device comprises a stainless steel separation cylinder 1, a superconducting pipe 2, a compressor 3, a vacuum cylinder 4, a recovery cylinder 5, a buoy 6, a feeding pipe 7, a gas conduction pipe 8, a recovery pipe 9, a sewage inlet valve 10, superconducting liquid 11, a heating chamber 12, an electromagnetic valve A13, an atomized cold air pipe 14, a drain pipe 15, an electromagnetic valve B16, a water suction pump 17, an electromagnetic valve C18, a vacuum pump 19, a slag outlet door 20, a water level gauge 21 and a cooler 22.
Detailed Description
The present invention will be described in detail with reference to fig. 1, and the technical solutions in the embodiments of the present invention will be clearly and completely described, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
The present invention provides a superconducting wet-dry separator by improvement, as shown in fig. 1; comprises a stainless steel separation cylinder 1, a superconducting pipe 2, a compressor 3, a vacuum cylinder 4, a recovery cylinder 5, a buoy 6, a feeding pipe 7, a gas conduction pipe 8 and a recovery pipe 9; the feeding pipe 7 is communicated with the stainless steel separation cylinder 1, the superconducting pipe 2 is arranged in the inner cavity of the stainless steel separation cylinder 1, superconducting liquid 11 is arranged in the superconducting pipe 2, a heating chamber 12 is formed at the bottom of the stainless steel separation cylinder 1, the heating chamber 12 is communicated with the compressor 3, and hot gas is provided for heating by the compressor 3; the stainless steel separation cylinder 1 is communicated with the vacuum cylinder 4 through a gas conduction pipe 8, the gas conduction pipe 8 is provided with an electromagnetic valve A13, an atomized cold gas pipe 14 of the compressor 3 is communicated with the vacuum cylinder 4, the vacuum cylinder 4 is communicated with the recovery cylinder 5 through a recovery pipe 9, and the recovery pipe 9 is provided with an electromagnetic valve C18 and a vacuum pump 19; the recovery cylinder 5 has a float 6 inside, and the end of the recovery pipe 9 extends into the float 6.
In practice, the feeding pipe 7 is provided with a sewage inlet valve 10.
During implementation, the superconducting pipes 2 are arranged in multiple groups and are vertically arranged in the stainless steel separation cylinder 1 respectively.
In the implementation, the bottom of the vacuum cylinder 4 is provided with a water discharge pipe 15, and the water discharge pipe 15 is provided with an electromagnetic valve B16 and a water suction pump 17.
In practice, the bottom of the side surface of the stainless steel separation barrel 1 is provided with a slag outlet door 20.
In practice, a water level gauge 21 is provided on the side surface of the vacuum cylinder 4.
The superconducting dry-wet separator can be used for separating and treating substances such as sludge, livestock and poultry manure, kitchen waste and the like; now, the principle of the method is described by taking the livestock and poultry manure as an example;
opening a sewage inlet valve 10, and conveying the livestock and poultry manure into the stainless steel separation 1 through a feed pipe 7; starting the compressor 3 to work, on one hand, heating the heating chamber 12 by the compressor 3 to heat the superconducting pipe 2, and after the superconducting pipe 2 is uniformly heated, heating the inner cavity of the stainless steel separation cylinder 1 to keep the temperature in the stainless steel separation cylinder 1 within the range of 30-60 ℃ so as to gasify and separate the livestock and poultry manure; then the electromagnetic valve A13 is opened, the separated mixed gas (nitrogen, methane, water vapor) enters the vacuum cylinder 4 through the gas conduction pipe 8, meanwhile, the compressor 3 inputs atomized cold air into the vacuum cylinder 4 through the atomized cold air pipe 14, the fog in the vacuum cylinder is cooled by the cooler 22 to become water state, namely, the water vapor in the mixed gas which is just transmitted is cooled to become liquid water; and opening the electromagnetic valve C18 and the vacuum pump 19, and enabling the nitrogen and methane gas in the vacuum cylinder 4 to enter the float 6 through the recovery pipe 9 to realize recovery. After the treatment is finished, opening a slag outlet door 20 to remove slag in the stainless steel separation cylinder 1; the water level inside the vacuum cylinder 4 can be observed by the water level gauge 21, and when the water level is high, the electromagnetic valve B16 and the water pump 17 can be opened to discharge water through the water discharge pipe 15. The device has simple structure and high operation efficiency, and realizes the dry-wet separation rapidly through superconducting heating.
The previous description of the disclosed embodiments is provided to enable any person skilled in the art to make or use the present invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the generic principles defined herein may be applied to other embodiments without departing from the spirit or scope of the invention. Thus, the present invention is not intended to be limited to the embodiments shown herein but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.
Claims (8)
1. A superconducting wet-dry separator, characterized in that; comprises a stainless steel separation cylinder (1), a superconducting pipe (2), a compressor (3), a vacuum cylinder (4), a recovery cylinder (5), a buoy (6), a feeding pipe (7), a gas conduction pipe (8) and a recovery pipe (9); the feeding pipe (7) is communicated with the stainless steel separation cylinder (1), the superconducting pipe (2) is arranged in the inner cavity of the stainless steel separation cylinder (1), superconducting liquid (11) is arranged in the superconducting pipe (2), a heating chamber (12) is formed at the bottom of the stainless steel separation cylinder (1), the heating chamber (12) is communicated with the compressor (3), and hot gas is provided for heating by the compressor (3); the stainless steel separation cylinder (1) is communicated with the vacuum cylinder (4) through a gas conduction pipe (8), the gas conduction pipe (8) is provided with an electromagnetic valve A (13), an atomized cold gas pipe (14) of the compressor (3) is communicated with the vacuum cylinder (4), the vacuum cylinder (4) is communicated with the recovery cylinder (5) through a recovery pipe (9), and the recovery pipe (9) is provided with an electromagnetic valve C (18) and a vacuum pump (19); the interior of the recovery cylinder (5) is provided with a buoy (6), and the end part of the recovery pipe (9) extends into the buoy (6).
2. The superconducting wet-dry separator according to claim 1, wherein; a sewage inlet valve (10) is arranged on the feeding pipe (7).
3. The superconducting wet-dry separator according to claim 1, wherein; the superconducting pipes (2) are in a plurality of groups and are vertically arranged in the stainless steel separating cylinder (1) respectively.
4. The superconducting wet-dry separator according to claim 1, wherein; the bottom of the vacuum cylinder (4) is provided with a drain pipe (15), and the drain pipe (15) is provided with an electromagnetic valve B (16) and a water pump (17).
5. The superconducting wet-dry separator according to claim 1, wherein; a slag outlet door (20) is arranged at the bottom of the side surface of the stainless steel separation barrel (1).
6. The superconducting wet-dry separator according to claim 1, wherein; a water level gauge (21) is arranged on the side surface of the vacuum cylinder (4).
7. The superconducting wet-dry separator according to claim 1, wherein; the operation is as follows; opening a sewage inlet valve (10), and conveying substances to be separated into the stainless steel separation cylinder (1) through a feed pipe (7); starting the compressor (3) to work, on one hand, the compressor (3) heats the heating chamber (12) to heat the superconducting pipe (2), the superconducting pipe (2) is heated uniformly to heat the inner cavity of the stainless steel separation cylinder (1), the temperature in the stainless steel separation cylinder (1) is kept within the range of 30-60 ℃, and the substances to be separated are gasified and separated; then the electromagnetic valve A (13) is opened, the separated mixed gas enters the vacuum cylinder (4) through the gas conduction pipe (8), and meanwhile, atomized cold air is input into the vacuum cylinder (4) through the atomized cold air pipe (14) by the compressor (3) to cool the water vapor in the mixed gas which is just transmitted into liquid water; and opening the electromagnetic valve C (18) and the vacuum pump (19), and enabling other gases in the vacuum cylinder (4) to enter the buoy (6) through the recovery pipe (9) to be recovered.
8. The superconducting wet-dry separator according to claim 7, wherein; the substances to be separated are sludge, livestock and poultry manure and kitchen waste.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010465677.8A CN111517614A (en) | 2020-05-28 | 2020-05-28 | Superconducting dry-wet separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010465677.8A CN111517614A (en) | 2020-05-28 | 2020-05-28 | Superconducting dry-wet separator |
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| Publication Number | Publication Date |
|---|---|
| CN111517614A true CN111517614A (en) | 2020-08-11 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202010465677.8A Pending CN111517614A (en) | 2020-05-28 | 2020-05-28 | Superconducting dry-wet separator |
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN200944672Y (en) * | 2006-09-05 | 2007-09-05 | 匡平 | Vacuum superconductor heating equipment |
| CN101671104A (en) * | 2008-09-12 | 2010-03-17 | 王文准 | Vacuum boiling sludge dewatering and drying method and system |
| CN105910481A (en) * | 2016-06-20 | 2016-08-31 | 张琦 | Super heat conducting tube and superconductive radiator |
| CN208182828U (en) * | 2018-02-05 | 2018-12-04 | 山东派宁环保科技有限公司 | A kind of sludge dehydrating and drying all-in-one machine based on function of mechanical steam recompression machine MVR |
| CN212451140U (en) * | 2020-05-28 | 2021-02-02 | 杨缤 | Superconducting dry-wet separator |
-
2020
- 2020-05-28 CN CN202010465677.8A patent/CN111517614A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN200944672Y (en) * | 2006-09-05 | 2007-09-05 | 匡平 | Vacuum superconductor heating equipment |
| CN101671104A (en) * | 2008-09-12 | 2010-03-17 | 王文准 | Vacuum boiling sludge dewatering and drying method and system |
| CN105910481A (en) * | 2016-06-20 | 2016-08-31 | 张琦 | Super heat conducting tube and superconductive radiator |
| CN208182828U (en) * | 2018-02-05 | 2018-12-04 | 山东派宁环保科技有限公司 | A kind of sludge dehydrating and drying all-in-one machine based on function of mechanical steam recompression machine MVR |
| CN212451140U (en) * | 2020-05-28 | 2021-02-02 | 杨缤 | Superconducting dry-wet separator |
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