CN216604408U - Vertical rotational flow gas-liquid separator for industrial steam recovery - Google Patents
Vertical rotational flow gas-liquid separator for industrial steam recovery Download PDFInfo
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- CN216604408U CN216604408U CN202122751041.2U CN202122751041U CN216604408U CN 216604408 U CN216604408 U CN 216604408U CN 202122751041 U CN202122751041 U CN 202122751041U CN 216604408 U CN216604408 U CN 216604408U
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Abstract
The utility model discloses a vertical rotational flow gas-liquid separator for industrial steam recovery, which comprises a bottom plate, wherein a plurality of welding support legs are welded and installed on the outer wall of the bottom plate, an outer cylinder body is welded and installed on the top of the bottom plate, an air outlet flange is fixedly installed at an air outlet at the top of the outer cylinder body, a first manhole is fixedly installed at the upper part of one side of the outer cylinder body, a liquid discharge port flange is fixedly installed at the lower part of one side of the outer cylinder body, and the water outlet end of the liquid discharge port flange is fixedly installed at the water inlet end of a filtrate pump. This vertical whirl vapour and liquid separator for industry vapor recovery realizes carrying out gas-liquid separation to gas and discharging, and the vapour state water of separation is stored at the stock solution part of outer barrel bottom to draw the emission from the inside of outer barrel through leakage fluid dram flange and filtrate pump, realize recycling the water resource, avoid extravagant, and including the barrel internally mounted hinder the liquid ring, can prevent that liquid water from upwards flowing against the current.
Description
Technical Field
The utility model relates to the field of industrial steam recovery, in particular to a vertical rotational flow gas-liquid separator for industrial steam recovery.
Background
Industry is the social substance production sector for the exploitation, the collection of natural resources and the processing of various raw materials. The industry is a processing and manufacturing industry, and the industry is a product developed by the industry of society and passes through several development stages of handicraft industry and machine industry. Industries are a component of the second industry, which is divided into light and heavy industries. Water vapor is a gaseous form of water. When water reaches its boiling point, it becomes water vapor. At sea level-standard atmospheric pressure, the boiling point of water is 99.974 ℃ or 212 ° F or 373.15 ° K. Water may also evaporate slowly to water vapor when the water is below the boiling point. The gas-liquid separator adopts the principles of centrifugal separation and wire mesh filtration to realize a separation device for removing liquid. It is mainly composed of cylinder, cyclone separator, high-efficiency foam-breaking net and blow-off valve.
In industrial processes and manufacturing, a large amount of water vapor is generated, and the water vapor is in a gas form of water, and in the conventional industrial production, the water vapor is discharged after being used, so that direct waste of water resources is caused, and therefore, a vertical cyclone gas-liquid separator for recovering the water vapor is proposed, which separates the water vapor from the gas and recovers the water resources.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide a vertical cyclone gas-liquid separator for industrial steam recovery, which solves the problems in the background technology.
In order to achieve the purpose, the utility model provides the following technical scheme:
a vertical rotational flow gas-liquid separator for industrial vapor recovery comprises a base plate, wherein a plurality of welding supporting legs are welded on the outer wall of the base plate, an outer barrel is welded on the top of the base plate, an air outlet at the top of the outer barrel is fixedly provided with an air outlet flange, a first manhole is fixedly arranged on the upper portion of one side of the outer barrel, a liquid outlet flange is fixedly arranged on the lower portion of one side of the outer barrel, a water inlet end of a filtrate pump is fixedly arranged on the water outlet end of the liquid outlet flange, a first flange viewing mirror and a second flange viewing mirror are respectively fixedly arranged on one side of the outer barrel and between the first manhole and the liquid outlet flange, a second manhole is fixedly arranged on one side of the outer barrel and between the first flange viewing mirror and the second flange viewing mirror, an air inlet flange is fixedly arranged on the other side of the outer barrel, and a rotational flow sheet is fixedly arranged in the outer barrel, the inner cavity of the spinning disk is fixedly provided with an inner barrel, the spinning disk is sleeved on the outer wall of the inner barrel, a baffle demister is fixedly arranged inside the outer barrel and above the inner barrel, and a spinning track is formed among the inner wall of the outer barrel, the outer wall of the inner barrel and the spinning disk.
As a further scheme of the utility model: the outer wall of interior barrel just is located the top of spinning disk and cup joints and installs the water conservancy diversion swash plate, and the water conservancy diversion swash plate is the tilt state installation, the top of water conservancy diversion swash plate just is located the slope low side and runs through and has seted up back the liquid mouth, the bottom of water conservancy diversion swash plate just is located back the liquid mouth under welded mounting has the honeycomb duct.
As a still further scheme of the utility model: the inside of outer barrel just is located the below welded mounting of interior barrel and hinders and revolve the orifice plate, and hinders the top of revolving the orifice plate and run through and seted up a plurality of holes that hinder and revolve.
As a still further scheme of the utility model: and the inner wall of the inner cylinder body is fixedly provided with a liquid blocking ring.
As a still further scheme of the utility model: the front fixed mounting of outer barrel has the upper portion level gauge flange, the front of outer barrel and the below fixed mounting that is located the upper portion level gauge flange have the lower part level gauge flange, and upper portion level gauge flange is located same vertical straight line with the lower part level gauge flange.
As a still further scheme of the utility model: the baffle plate demister is a detachable PP baffle plate demister.
Compared with the prior art, the utility model has the beneficial effects that:
1. the utility model discloses, gaseous (vapour water, gas mixture) gets into the inside of outer barrel by the air inlet flange, gaseous this moment gets into the whirl track through the spinning disk, because centrifugal force acts on, vapour water in the gas gets rid of the inner wall to outer barrel, through collecting the stock solution part that flows down and hinder the spinning disk below, some vapour water follows gaseous continuation and moves to interior barrel bottom in addition, and upwards get into the inside of interior barrel, realize carrying out gas-liquid separation to gas and discharging again, the liquid storage part of the liquid water of separation bottom the barrel outside stores, and extract the emission from the inside of outer barrel through leakage fluid dram flange and filtrate pump, realize the recovery of water resource and recycle, avoid extravagant, and the liquid ring that hinders of barrel internally mounted including, can prevent liquid water upwards against the current.
2. This practicality, because gaseous whirl is done through the spinning disk, also can the whirl always after leaving the whirl track, can cause the liquid in the below stock solution space to follow and do the whirl like this, owing to hinder the setting of whirl orifice plate, the gaseous whirl can greatly reduced whirl state after hindering the whirl orifice plate of whirl to can make below stock solution space steady.
3. The utility model, the gas enters the demisting space at the top through the inner cylinder, the baffle plate demister which is cheap and detachable is arranged in the space, most of water in the residual gas can be filtered by the gas through the baffle plate demister, finally, the gas leaves the separator through the gas outlet flange, the baffle plate demister is selected to be a detachable PP baffle plate demister, the use effect can be met, the manufacturing cost is also reduced, the worker can directly contact the baffle plate demister through the arranged first manhole, when the baffle plate demister needs to be cleaned, the baffle plate demister can be taken out in blocks through the first manhole, the baffle plate demister is put back after the cleaning is finished, the inclination of the baffle plate demister is simple, the liquid water filtered by the baffle plate demister flows to the flow guide sloping plate under the action of gravity, the water is recycled again through the liquid return port and the liquid storage part below the outer cylinder body by the inclined plate gathering effect.
Drawings
FIG. 1 is a schematic structural view of a vertical cyclone gas-liquid separator for industrial steam recovery;
FIG. 2 is a sectional view of an outer cylinder of a vertical cyclone gas-liquid separator for industrial steam recovery;
FIG. 3 is a sectional view of an inner cylinder in a vertical cyclone gas-liquid separator for industrial steam recovery.
In the figure: the liquid level meter comprises a bottom plate 1, a welding supporting leg 2, a lower liquid level meter flange 3, an outer cylinder 4, an upper liquid level meter flange 5, a gas inlet flange 6, a gas outlet flange 7, a first manhole 8, a first flange sight glass 9, a second manhole 10, a second flange sight glass 11, a liquid discharge port flange 12, a baffle plate demister 13, an inner cylinder 14, a flow guide inclined plate 15, a rotation blocking hole plate 16, a liquid return port 17, a flow guide pipe 18, a liquid blocking ring 19 and a rotation flow sheet 20.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the 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.
Referring to fig. 1-3, the utility model provides a technical scheme, a vertical rotational flow gas-liquid separator for industrial steam recovery, comprising a bottom plate 1, a plurality of welding legs 2 welded on the outer wall of the bottom plate 1, an outer cylinder 4 welded on the top of the bottom plate 1, a gas outlet flange 7 fixed on the gas outlet on the top of the outer cylinder 4, a first manhole 8 fixed on the upper portion of one side of the outer cylinder 4, a liquid outlet flange 12 fixed on the lower portion of one side of the outer cylinder 4, a water inlet end of a filtrate pump fixed on the water outlet end of the liquid outlet flange 12, a first flange viewing mirror 9 and a second flange viewing mirror 11 respectively fixed on one side of the outer cylinder 4 and between the first manhole 8 and the liquid outlet flange 12, a second manhole 10 fixed on one side of the outer cylinder 4 and between the first flange viewing mirror 9 and the second flange viewing mirror 11, a gas inlet flange 6 fixed on the other side of the outer cylinder 4, the inside fixed mounting of outer barrel 4 has spinning disk 20, and barrel 14 in the inner chamber fixed mounting of spinning disk 20, and spinning disk 20 cup joints the outer wall of barrel 14 in, and the top fixed mounting of barrel 14 has baffling board defroster 13 in the inside of outer barrel 4 and being located, forms the whirl track between the inner wall of outer barrel 4, the outer wall of inner barrel 14 and spinning disk 20.
The outer wall of the inner cylinder body 14 and the upper part of the vortex sheet 20 are sleeved with a diversion inclined plate 15, the diversion inclined plate 15 is installed in an inclined state, the top of the diversion inclined plate 15 is located at the inclined low end and runs through the inclined low end, a liquid return opening 17 is formed in the inclined low end, and a diversion pipe 18 is welded and installed under the liquid return opening 17 at the bottom of the diversion inclined plate 15.
The inside of outer barrel 4 just is located the below welding of interior barrel 14 and is installed and hinder and revolve the orifice plate 16, and hinders the top of revolving the orifice plate 16 and run through and seted up a plurality of holes of hindering and revolve.
The inner wall of the inner cylinder 14 is fixedly provided with a liquid blocking ring 19.
The front of outer barrel 4 is fixed with upper portion level gauge flange 5, and the front of outer barrel 4 and the below fixed mounting that is located upper portion level gauge flange 5 have lower part level gauge flange 3, and upper portion level gauge flange 5 is located same vertical straight line with lower part level gauge flange 3.
The baffle plate demister 13 is a detachable PP baffle plate demister.
The working principle of the utility model is as follows:
when the gas-liquid separation and emission device is used, gas-liquid water and a gas mixture enter the inner part of the outer cylinder 4 through the gas inlet flange 6, at the moment, the gas enters a rotational flow track through the rotational flow sheet 20, due to the centrifugal force, the gas-liquid water in the gas is thrown to the inner wall of the outer cylinder 4, and flows downwards after being collected into the liquid storage part below the rotation-resistant hole plate 16, and part of the gas-liquid water continuously moves to the bottom of the inner cylinder 14 along with the gas and upwards enters the inner part of the inner cylinder 14 to realize gas-liquid separation and emission of the gas, and the separated liquid water is stored in the liquid storage part at the bottom of the outer cylinder 4 and is extracted and emitted from the inner part of the outer cylinder 4 through the liquid outlet flange 12 and the filter liquid pump, so that the recycling of water resources is realized, the waste is avoided, and the upward counter flow of the liquid water can be prevented through the liquid-resistant ring 19 arranged in the inner cylinder 14;
because the gas is made into rotational flow through the rotational flow sheet 20, the gas can be always made into rotational flow after leaving the rotational flow orbit, so that the liquid in the liquid storage space below can be made into rotational flow along with the rotational flow, and due to the arrangement of the rotation-resisting pore plate 16, the rotational flow state of the rotational flow gas can be greatly reduced after passing through the rotation-resisting pore plate 16, so that the liquid storage space below can be stable;
the gas enters a demisting space at the top through an inner cylinder 14, a baffle plate demister 13 which is cheap and detachable is arranged in the space, most of moisture in the residual gas can be filtered by the gas through the baffle plate demister 13, the gas finally leaves the separator through a gas outlet flange 7, the baffle plate demister 13 is a detachable PP baffle plate demister, the using effect can be met, the manufacturing cost is also reduced, a worker can directly contact the baffle plate demister 13 through a first manhole 8, when the baffle plate demister 13 needs to be cleaned, the baffle plate demister 13 can be taken out in blocks through the first manhole 8, the baffle plate demister 13 is put back after the cleaning is finished, the inclination of the baffle plate demister 13 is simple, a flow guide sloping plate 15 is additionally arranged below the baffle plate demister 13, and liquid water filtered by the baffle plate demister 13 flows to the flow guide sloping plate 15 under the action of gravity, the water flows into the liquid storage part below the outer cylinder 4 through the liquid return port 17 and the guide pipe 18 under the convergence action of the inclined plate, so that the water resource is recycled again.
Although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that various changes in the embodiments and/or modifications of the utility model can be made, and equivalents and modifications of some features of the utility model can be made without departing from the spirit and scope of the utility model.
Claims (6)
1. The utility model provides a vertical whirl vapour and liquid separator for industrial steam retrieves, includes bottom plate (1), its characterized in that: a plurality of welding support legs (2) are installed on the outer wall of the base plate (1) in a welding mode, an outer barrel (4) is installed on the top of the base plate (1) in a welding mode, an air outlet flange (7) is fixedly installed at the top of the outer barrel (4), a first manhole (8) is fixedly installed on the upper portion of one side of the outer barrel (4), a liquid discharge port flange (12) is fixedly installed on the lower portion of one side of the outer barrel (4), a water inlet end of a liquid filter pump is fixedly installed at a water outlet end of the liquid discharge port flange (12), a first flange viewing mirror (9) and a second flange viewing mirror (11) are respectively and fixedly installed between the first manhole (8) and the liquid discharge port flange (12) on one side of the outer barrel (4), and a second manhole (10) is fixedly installed between the first flange viewing mirror (9) and the second flange viewing mirror (11) on one side of the outer barrel (4), the utility model discloses a cyclone separator, including outer barrel (4), inner chamber fixed mounting has interior barrel (14), and the outer wall of barrel (14) is cup jointed in the inner chamber fixed mounting of whirl piece (20), the inside fixed mounting of outer barrel (4) has interior barrel (14), and whirl piece (20) cup joints the outer wall of barrel (14), the inside of outer barrel (4) and the top fixed mounting that is located interior barrel (14) have baffling board defroster (13), form the whirl track between the inner wall of outer barrel (4), the outer wall of interior barrel (14) and whirl piece (20).
2. The vertical cyclone gas-liquid separator for industrial water vapor recovery according to claim 1, characterized in that: the outer wall of interior barrel (14) and the top that is located spinning disk (20) cup joint and install water conservancy diversion swash plate (15), and water conservancy diversion swash plate (15) are the slope state installation, the top of water conservancy diversion swash plate (15) just is located the slope low side and runs through and has seted up back liquid mouth (17), the bottom of water conservancy diversion swash plate (15) just is located back liquid mouth (17) under welded mounting honeycomb duct (18).
3. The vertical cyclone gas-liquid separator for industrial water vapor recovery according to claim 2, characterized in that: the inside of outer barrel (4) and the below welded installation that is located interior barrel (14) have and hinder orifice plate (16) soon, and hinder the top of orifice plate (16) and run through and seted up a plurality of holes that hinder soon.
4. The vertical cyclone gas-liquid separator for industrial water vapor recovery according to claim 1, characterized in that: and a liquid blocking ring (19) is fixedly arranged on the inner wall of the inner cylinder body (14).
5. The vertical cyclone gas-liquid separator for industrial water vapor recovery according to claim 1, characterized in that: the positive fixed mounting of outer barrel (4) has upper portion level gauge flange (5), the front of outer barrel (4) and the below fixed mounting that is located upper portion level gauge flange (5) have lower part level gauge flange (3), and upper portion level gauge flange (5) are located same vertical straight line with lower part level gauge flange (3).
6. The vertical cyclone gas-liquid separator for industrial water vapor recovery according to claim 1, characterized in that: the baffle plate demister (13) is a detachable PP baffle plate demister.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122751041.2U CN216604408U (en) | 2021-11-11 | 2021-11-11 | Vertical rotational flow gas-liquid separator for industrial steam recovery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122751041.2U CN216604408U (en) | 2021-11-11 | 2021-11-11 | Vertical rotational flow gas-liquid separator for industrial steam recovery |
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| Publication Number | Publication Date |
|---|---|
| CN216604408U true CN216604408U (en) | 2022-05-27 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202122751041.2U Active CN216604408U (en) | 2021-11-11 | 2021-11-11 | Vertical rotational flow gas-liquid separator for industrial steam recovery |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116730547A (en) * | 2023-07-06 | 2023-09-12 | 武汉东碧环保科技有限公司 | Wastewater treatment device and treatment method |
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2021
- 2021-11-11 CN CN202122751041.2U patent/CN216604408U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116730547A (en) * | 2023-07-06 | 2023-09-12 | 武汉东碧环保科技有限公司 | Wastewater treatment device and treatment method |
| CN116730547B (en) * | 2023-07-06 | 2024-01-26 | 武汉东碧环保科技有限公司 | Wastewater treatment device and treatment method |
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