CN213192875U - High-efficient multichannel spiral-flow type gas-liquid separation - Google Patents
High-efficient multichannel spiral-flow type gas-liquid separation Download PDFInfo
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- CN213192875U CN213192875U CN202022017824.3U CN202022017824U CN213192875U CN 213192875 U CN213192875 U CN 213192875U CN 202022017824 U CN202022017824 U CN 202022017824U CN 213192875 U CN213192875 U CN 213192875U
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- 239000007788 liquid Substances 0.000 title claims abstract description 65
- 238000000926 separation method Methods 0.000 title claims abstract description 19
- 238000005192 partition Methods 0.000 claims abstract description 12
- 230000007306 turnover Effects 0.000 claims description 19
- 239000007791 liquid phase Substances 0.000 abstract description 22
- 239000000463 material Substances 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 5
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 239000007789 gas Substances 0.000 description 28
- 239000000126 substance Substances 0.000 description 18
- 239000002912 waste gas Substances 0.000 description 9
- 239000010963 304 stainless steel Substances 0.000 description 2
- 229910000589 SAE 304 stainless steel Inorganic materials 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
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Abstract
The utility model relates to a high-efficient multichannel spiral-flow type gas-liquid separation device belongs to exhaust-gas treatment equipment technical field. The technical scheme is as follows: the space between the outer cylinder (3) and the inner cylinder (301) of the device is divided into an upper space and a lower space by the partition plate (304), the gas inlet (6) is communicated with the lower space (11), the gas outlet (2) is communicated with the upper space (10), and the upper space (10) is communicated with the lower space (11) up and down through the inner cylinder (301); the number of the spiral guide vanes is more than two, and the lower part space (11) between the outer cylinder (3) and the inner cylinder (301) of the device is divided into more than two spiral downward channels. The utility model discloses can improve the separation effect of liquid phase material in the gas greatly, realize the high-efficient recycle of valuable liquid phase material, this device takes up an area of for a short time, noiselessness, the energy consumption is extremely low.
Description
Technical Field
The utility model relates to a high-efficient multichannel spiral-flow type gas-liquid separation device belongs to exhaust-gas treatment equipment technical field.
Background
The waste gas often contains other liquid phase substances, and many liquid phase substances have high recycling value. Therefore, the device capable of efficiently separating the liquid phase substances in the gas can meet the recycling of the valuable liquid phase substances. At present, the cyclone gas-liquid separation device in the prior art has the following problems: the single central channel makes the gas distribute unevenly in the device, which is easy to produce vortex and can not achieve good gas-liquid separation effect.
Disclosure of Invention
The utility model aims at providing a high-efficient multichannel spiral-flow type gas-liquid separation device, multichannel design make behind the gaseous admission device evenly distributed to every passageway, and the gas in the passageway can not influence each other, can not produce the vortex, has improved the separation effect of liquid phase material in the gas greatly, has solved the above-mentioned problem that exists effectively among the background art.
The technical scheme of the utility model is that: an efficient multi-channel spiral-flow type gas-liquid separation device comprises a gas outlet, an equipment outer cylinder, a supporting plate, a magnetic turnover liquid level meter, a gas inlet, a liquid outlet, a liquid discharge pipe, an electromagnetic valve, an inner cylinder, a wire mesh demister, a demister supporting plate, a partition plate and spiral guide vanes; the device outer cylinder and the inner cylinder are concentrically arranged, and the inner cylinder is arranged inside the device outer cylinder; the gas outlet and the gas inlet are respectively arranged at two sides of the upper part of the outer cylinder body of the equipment; the supporting plate is arranged at the lower part of the outer cylinder of the equipment, and the magnetic turnover liquid level meter is arranged at the lower part of the supporting plate; the liquid outlet is arranged at the bottom of the outer cylinder of the equipment; the liquid discharge pipe is connected with the liquid outlet and is provided with an electromagnetic valve; a demister support plate is arranged at the upper part of the inner cylinder body, and the wire mesh demister is arranged on the demister support plate; the device comprises an outer device barrel, an inner barrel, a partition plate, a gas inlet, a gas outlet, an upper part space, a lower part space, a gas inlet, a gas outlet and a gas inlet, wherein the outer device barrel is connected with the inner barrel through the partition plate; the spiral guide vane is arranged between the outer cylinder and the inner cylinder of the device, and the upper surface of the spiral guide vane is lower than the gas inlet; the spiral guide vanes are arranged on the outer wall of the inner cylinder body and are not contacted with the outer cylinder body of the equipment, the number of the spiral guide vanes is more than two, and the lower part of the space between the outer cylinder body of the equipment and the inner cylinder body is divided into more than two spiral downward channels.
And a wire mesh demister is arranged at the top of the inner cylinder.
And the top of the outer cylinder body of the equipment is provided with an access hole.
The material of the outer cylinder body and the inner cylinder body of the equipment is 304 stainless steel.
The magnetic turnover liquid level meter controls the electromagnetic valve to be opened when the liquid level is high and to be closed when the liquid level is low.
The magnetic turnover liquid level meter is arranged at the lower part of the supporting plate, and the electromagnetic valve is arranged at the lower part of the liquid discharge pipe. The magnetic turnover liquid level meter, the electromagnetic valve, the wire mesh demister and the like are all common equipment known in the field and are sold in the market.
The device separates gas-phase substances from liquid-phase substances by utilizing the centrifugal action in the physics principle. The electric equipment in the device is only a magnetic turnover liquid level meter and an electromagnetic valve, and the energy consumption is extremely low.
The utility model has the advantages that: the lower space between the inner cylinder and the outer cylinder is uniformly divided into more than two channels by more than two spiral guide vanes; the multichannel makes the air current distribution more even, has increased the area of contact, adhesion, the condensation of liquid phase material and equipment, makes the liquid phase material in the waste gas separate out more easily. The design of multiple channels greatly improves the gas-liquid separation rate and solves the problem of poor effect of the gas-liquid separation device. The equipment is highly integrated, the floor area is small, the electric equipment only comprises a magnetic turnover liquid level meter and an electromagnetic valve, and the energy consumption is extremely low.
Drawings
Fig. 1 is a cross-sectional view of the present invention;
FIG. 2 is an external view of the present invention;
fig. 3 is a cross-sectional view of the inner cylinder of the present invention;
in the figure: the device comprises a manhole 1, a gas outlet 2, an outer equipment barrel 3, a supporting plate 4, a magnetic turnover liquid level meter 5, a gas inlet 6, a liquid outlet 7, a liquid discharge pipe 8, an electromagnetic valve 9, an upper part space 10, a lower part space 11, an inner barrel 301, a wire mesh demister 302, a demister supporting plate 303, a partition plate 304 and a spiral guide vane 305.
Detailed Description
The technical solution of the present invention will be further described in detail with reference to the accompanying drawings and examples.
A high-efficiency multi-channel cyclone gas-liquid separation device comprises a gas outlet 2, an equipment outer cylinder 3, a supporting plate 4, a magnetic turnover liquid level meter 5, a gas inlet 6, a liquid outlet 7, a liquid discharge pipe 8, an electromagnetic valve 9, an inner cylinder 301, a wire mesh demister 302, a demister supporting plate 303, a partition plate 304 and a spiral guide vane 305; the equipment outer cylinder 3 and the inner cylinder 301 are concentrically arranged, and the inner cylinder 301 is arranged inside the equipment outer cylinder 3; the gas outlet 2 and the gas inlet 6 are respectively arranged at two sides of the upper part of the outer cylinder 3 of the device; the supporting plate 4 is arranged at the lower part of the outer cylinder 3 of the equipment, and the magnetic turnover liquid level meter 5 is arranged at the lower part of the supporting plate 4; the liquid outlet 7 is arranged at the bottom of the outer cylinder 3 of the device; the liquid discharge pipe 8 is connected with the liquid outlet 7, and the electromagnetic valve 9 is arranged on the liquid discharge pipe 8; a demister supporting plate 303 is arranged at the upper part of the inner cylinder 301, and the wire mesh demister 302 is arranged on the demister supporting plate 303; the device outer cylinder 3 is connected with the inner cylinder 301 through a partition plate 304, the partition plate 304 divides the space between the device outer cylinder 3 and the inner cylinder 301 into an upper space and a lower space, the gas inlet 6 is communicated with the lower space 11, the gas outlet 2 is communicated with the upper space 10, and the upper space 10 is communicated with the lower space 11 up and down through the inner cylinder 301; the spiral guide vane 305 is arranged between the outer cylinder 3 and the inner cylinder 301 of the device, and the upper surface of the spiral guide vane 305 is lower than the gas inlet 6; the spiral guide vanes are arranged on the outer wall of the inner cylinder body 301 and do not contact with the outer cylinder body 3 of the equipment, the number of the spiral guide vanes is more than two, and the lower part space 11 between the outer cylinder body 3 of the equipment and the inner cylinder body 301 is divided into more than two spiral downward channels.
A wire mesh demister 302 is installed at the top of the inner cylinder 301.
And the top of the outer cylinder body 3 of the equipment is provided with an access hole 1.
The outer cylinder 3 and the inner cylinder 301 of the device are made of 304 stainless steel.
The magnetic turnover liquid level meter 5 controls the electromagnetic valve 9 to be opened at a high liquid level and closed at a low liquid level.
The magnetic turnover liquid level meter is arranged at the lower part of the supporting plate, and the electromagnetic valve is arranged at the lower part of the liquid discharge pipe. The magnetic turnover liquid level meter 5, the electromagnetic valve 9, the wire mesh demister 302 and the like are all common equipment known in the field and are sold in the market.
The device separates gas-phase substances from liquid-phase substances by utilizing the centrifugal action in the physics principle. The electric equipment in the device is only a magnetic turnover liquid level meter and an electromagnetic valve, and the energy consumption is extremely low.
In practical application, waste gas to be treated enters the device through the gas inlet 6, enters the lower part space 11 between the inner cylinder 301 and the outer cylinder 3 under the guiding action of the partition plate 304, and spirally moves around the inner cylinder 301 to the bottom of the inner cylinder 301 under the guiding action of the spiral guide vane 305, and in the process, the waste gas containing liquid-phase substances throws the liquid-phase substances onto the inner wall of the outer cylinder 3 under the action of centrifugal force, so that the liquid-phase substances are in contact with the inner wall of the outer cylinder 3, attached to and condensed into liquid-drop flow to the bottom of the device; the multi-channel design ensures that the waste gas is distributed more uniformly, the waste gas is contacted with the inner wall of the outer cylinder 3 more fully, and the adhesion and condensation effects of liquid phase substances are better; liquid phase substances flow to the bottom of the device and are accumulated, and the bottom of the device is provided with a magnetic turnover liquid level meter 5 and an electromagnetic valve 9; when liquid phase substances are accumulated to a high liquid level, the magnetic turnover liquid level meter 5 transmits a signal to the electromagnetic valve 9, so that the electromagnetic valve 9 is opened and the liquid phase substances are discharged through the liquid discharge pipe 8, when the liquid phase substances are discharged to a low liquid level, the magnetic turnover liquid level meter 5 transmits a signal to the electromagnetic valve 9, so that the electromagnetic valve 9 is closed, and liquid discharge is stopped; the waste gas flows to the lower part of the inner cylinder 301 through the spiral guide vane 305 and then moves upwards along the inner part of the inner cylinder 301, the fog drops in the waste gas are removed for the second time through the wire mesh demister 302, and the waste gas enters the upper part space 10 and is finally discharged through the gas outlet 2 or enters the next stage of treatment equipment.
The number of the spiral guide vanes 305 of the device is the number of channels; the angle and the number of the spiral guide vanes 305 can be adjusted according to different medium types and the content of the liquid phase substances, so as to achieve the purpose of removing the corresponding liquid phase substances.
The lower part of the device is provided with a supporting plate 4, the height of the bracket can be adjusted according to actual conditions of different sites, and the installation is convenient.
The utility model relates to a high-efficient multichannel spiral-flow type gas-liquid separation device has realized the high-efficient separation of liquid phase material in the gas, is the innovation equipment among the exhaust-gas treatment.
Claims (4)
1. The utility model provides a high-efficient multichannel spiral-flow type gas-liquid separation device which characterized in that: the device comprises a gas outlet (2), an equipment outer cylinder (3), a supporting plate (4), a magnetic turnover liquid level meter (5), a gas inlet (6), a liquid outlet (7), a liquid discharge pipe (8), an electromagnetic valve (9), an inner cylinder (301), a wire mesh demister (302), a demister supporting plate (303), a partition plate (304) and a spiral guide vane (305); the equipment outer cylinder (3) and the inner cylinder (301) are concentrically arranged, and the inner cylinder (301) is arranged inside the equipment outer cylinder (3); the gas outlet (2) and the gas inlet (6) are respectively arranged at two sides of the upper part of the outer cylinder body (3) of the device; the supporting plate (4) is arranged at the lower part of the outer cylinder body (3) of the equipment, and the magnetic turnover liquid level meter (5) is arranged at the lower part of the supporting plate (4); the liquid outlet (7) is arranged at the bottom of the outer cylinder (3) of the device; the liquid discharge pipe (8) is connected with the liquid outlet (7), and the electromagnetic valve (9) is arranged on the liquid discharge pipe (8); a demister supporting plate (303) is arranged at the upper part of the inner cylinder (301), and the wire mesh demister (302) is arranged on the demister supporting plate (303); the device is characterized in that the device outer cylinder (3) is connected with the inner cylinder (301) through a partition plate (304), the partition plate (304) divides the space between the device outer cylinder (3) and the inner cylinder (301) into an upper space and a lower space, the gas inlet (6) is communicated with the lower space (11), the gas outlet (2) is communicated with the upper space (10), and the upper space (10) is communicated with the lower space (11) up and down through the inner cylinder (301); the spiral guide vane (305) is arranged between the outer cylinder (3) and the inner cylinder (301) of the device, and the upper surface of the spiral guide vane (305) is lower than the gas inlet (6); the spiral guide vane is installed on the outer wall of the inner cylinder body (301) and does not contact with the outer cylinder body (3) of the equipment, the number of the spiral guide vane is more than two, and a lower part space (11) between the outer cylinder body (3) of the equipment and the inner cylinder body (301) is separated into more than two downward spiral channels.
2. A high efficiency multi-channel cyclonic gas-liquid separation apparatus as claimed in claim 1, wherein: and a wire mesh demister (302) is arranged at the top of the inner cylinder (301).
3. A high efficiency multi-channel cyclonic gas-liquid separation apparatus as claimed in claim 1 or 2, wherein: and an access hole (1) is formed in the top of the outer cylinder body (3) of the equipment.
4. A high efficiency multi-channel cyclonic gas-liquid separation apparatus as claimed in claim 1 or 2, wherein: the electromagnetic valve (9) is arranged at the lower part of the liquid discharge pipe (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022017824.3U CN213192875U (en) | 2020-09-16 | 2020-09-16 | High-efficient multichannel spiral-flow type gas-liquid separation |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022017824.3U CN213192875U (en) | 2020-09-16 | 2020-09-16 | High-efficient multichannel spiral-flow type gas-liquid separation |
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| CN213192875U true CN213192875U (en) | 2021-05-14 |
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| CN202022017824.3U Active CN213192875U (en) | 2020-09-16 | 2020-09-16 | High-efficient multichannel spiral-flow type gas-liquid separation |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113856337A (en) * | 2021-11-03 | 2021-12-31 | 沧州万润环保设备有限公司 | Cyclone dehydration dust collector and dust-containing water vapor dehydration dust removal system |
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2020
- 2020-09-16 CN CN202022017824.3U patent/CN213192875U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113856337A (en) * | 2021-11-03 | 2021-12-31 | 沧州万润环保设备有限公司 | Cyclone dehydration dust collector and dust-containing water vapor dehydration dust removal system |
| CN113856337B (en) * | 2021-11-03 | 2024-07-12 | 沧州万润环保设备有限公司 | Rotational flow dehydration dust remover and dust-containing water vapor dehydration dust removal system |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: A high-efficiency multi-channel cyclone gas-liquid separation device Effective date of registration: 20220901 Granted publication date: 20210514 Pledgee: Bank of China Limited by Share Ltd. Tangshan City Jianshe Road branch Pledgor: HEBEI GREEN-DREAM ENVIRONMENTAL SCIENCE& TECHNOLOGY CO.,LTD. Registration number: Y2022990000589 |
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| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20231017 Granted publication date: 20210514 Pledgee: Bank of China Limited by Share Ltd. Tangshan City Jianshe Road branch Pledgor: HEBEI GREEN-DREAM ENVIRONMENTAL SCIENCE& TECHNOLOGY CO.,LTD. Registration number: Y2022990000589 |