CN217473116U - Gas-liquid separation ring - Google Patents
Gas-liquid separation ring Download PDFInfo
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- CN217473116U CN217473116U CN202123101829.5U CN202123101829U CN217473116U CN 217473116 U CN217473116 U CN 217473116U CN 202123101829 U CN202123101829 U CN 202123101829U CN 217473116 U CN217473116 U CN 217473116U
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- 239000007788 liquid Substances 0.000 title claims abstract description 143
- 238000000926 separation method Methods 0.000 title claims abstract description 100
- 238000003860 storage Methods 0.000 claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 58
- 238000001035 drying Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 59
- 230000005484 gravity Effects 0.000 description 11
- 238000007599 discharging Methods 0.000 description 9
- 238000004458 analytical method Methods 0.000 description 5
- 238000004220 aggregation Methods 0.000 description 3
- 230000002776 aggregation Effects 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 238000005034 decoration Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 238000012824 chemical production Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000002274 desiccant Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000004868 gas analysis Methods 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000001151 other effect Effects 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000003209 petroleum derivative Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
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Abstract
A gas-liquid separation ring relates to the technical field of high-humidity gas-liquid separation and comprises an air inlet pipeline, an air outlet pipeline, a separation ring and a liquid guide assembly, wherein water-containing gas enters the separation ring from the air inlet pipeline to perform gas-liquid separation, first gas-liquid separation is realized in the air inlet pipeline, water vapor enters the separation ring and is condensed into liquid water to be collected to the bottom of the separation ring, second gas-liquid separation is performed, the liquid water flows into a liquid storage tank through a liquid discharge pipeline to realize drying and dewatering of the separation ring, the water-containing gas finally performs third gas-liquid separation from the air outlet pipeline, finally leaves the separation ring to enter an instrument of the next step, and a worker judges whether a gas sample after gas-liquid separation meets the standard by observing the indication of a humidity measuring instrument arranged outside the air outlet pipeline, so as to determine whether secondary gas-liquid separation is needed; to summarize, the utility model has simple structure, convenient operation and low cost, and can be widely applied to gas-liquid separation in the industrial field.
Description
Technical Field
The utility model relates to a high wet gas-liquid separation technical field, concretely relates to gas-liquid separation ring.
Background
In chemical production, such as the field of petroleum products or the field of coal products, when the sample gas in an extraction process pipeline is subjected to component analysis, when the water content of the sample gas is high and cannot meet the requirement of sample analysis of a gas analysis instrument, water vapor in the sample gas needs to be separated, but because the compression ratio of liquid is small, if the liquid is absorbed into the gas sample, the analysis instrument cannot accurately perform component analysis on the gas in the sample, and the redundant liquid in the gas sample easily causes irreversible damage to the analysis instrument, so that the service life of the instrument is shortened.
The existing related gas-liquid separation technology generally adopts a cyclone separation mode, a wire mesh mist trapping mode and a fiber aggregation separation mode, wherein the cyclone separation mode utilizes the centrifugal force of gas-liquid rotational flow to enable liquid with high density to continuously collide the barrel wall of a cyclone separator to realize separation, the wire mesh mist trapping mode utilizes liquid drops to collide a wire mesh to form interception so as to realize separation, and the fiber aggregation mode utilizes the adsorption, collision, aggregation and other effects of fibers on tiny liquid drops to realize separation.
In view of the above-mentioned related technologies, the inventors of the present invention have considered that the conventional gas-liquid separation methods are all disadvantageous in that the separation methods are complicated and costly.
SUMMERY OF THE UTILITY MODEL
To the not enough that prior art exists, the utility model aims to provide a transportation equipment for packing of digital product, concrete scheme is as follows:
the gas-liquid separation ring comprises a separation ring body, the separation ring body is in a closed ring shape, two parts of the separation ring body are respectively communicated with an air inlet pipeline and an air outlet pipeline, a liquid guide assembly is further arranged at the other part of the separation ring body, and the liquid guide assembly is arranged below the air inlet pipeline and the air outlet pipeline.
Further optimally, the separating ring comprises a first U-shaped pipe, a second U-shaped pipe and a straight pipe, the first U-shaped pipe, the second U-shaped pipe and the straight pipe are communicated end to end through a tee joint, an air inlet pipeline is arranged at a joint of the first U-shaped pipe and the straight pipe, an air outlet pipeline is arranged at a joint of the second U-shaped pipe and the straight pipe, the separating ring is placed in the vertical direction, the tee joint at the joint of the first U-shaped pipe and the second U-shaped pipe is located at the lower part of the vertical direction of the separating ring, and the straight pipe is located at the tee joint at the joint of the first U-shaped pipe and the tee joint at the joint of the straight pipe and the second U-shaped pipe.
Further optimally, the air inlet pipeline is vertical direction setting, just the air inlet setting of air inlet pipeline is at the lower extreme of air inlet pipeline, the gas outlet of air inlet pipeline pass through the decurrent port of three way connection with the connection can be dismantled in the split ring realization, the air outlet pipeline is vertical direction setting, just the gas outlet setting of air outlet pipeline is in the upper end of air outlet pipeline, the air inlet of air outlet pipeline pass through the ascending port of three way connection with the connection can be dismantled in the split ring realization.
Further optimally, the liquid guiding assembly comprises a liquid discharging pipeline and a liquid storage tank, and the liquid discharging pipeline is arranged at a joint where the first U-shaped pipe and the second U-shaped pipe are communicated.
Further optimally, the liquid drainage pipeline is arranged in the vertical direction, and a liquid inlet of the liquid drainage pipeline is arranged at the upper end of the liquid drainage pipeline.
Further optimally, a humidity measuring instrument is communicated with the outside of the gas outlet pipeline and used for displaying the humidity of the gas sample passing through the gas-liquid separation ring
Further optimally, the liquid discharge pipeline is arranged in the liquid storage tank, and the liquid discharge pipeline is arranged in the liquid storage tank in a suspended mode.
Compared with the prior art, the beneficial effects of the utility model are as follows:
(1) the water-containing gas firstly enters the gas inlet pipeline, flowing water-vapor mixture contacts the gas inlet pipeline with lower temperature and is condensed into liquid water which flows out along the gas inlet pipeline, first gas-liquid separation is realized, after the water-containing gas continuously enters the separation ring through the gas inlet pipeline, when the water-containing gas flows in the separation ring, part of the water-vapor is condensed into liquid water which is attached to the inner wall of the pipeline of the separation ring, the liquid water gradually converges downwards to the bottom of the separation ring under the action of gravity, second gas-liquid separation is realized, the arrangement of the separation ring can effectively prevent water vapor from uprushing up, the water blocking effect is realized, meanwhile, the buffering effect is realized on the water-containing gas continuously input from the device, when a drier gas sample passing through the separation ring is discharged out of the device through the gas outlet pipeline arranged at the other position of the separation ring, under the cooling and gravity effects of the inner wall of the gas outlet pipeline, the water vapor is also condensed into liquid water which flows downwards into the separation ring, gas-liquid separation in the third step is realized, and the water content of discharged gas is reduced; in summary, the gas containing water sequentially enters the gas inlet pipeline, the separating ring and the gas outlet pipeline, three times of gas-liquid separation are carried out in the contact process of the gas containing water and the inner wall of the pipeline and under the action of gravity, the gas containing water is finally changed into drier gas to be discharged out of the gas-liquid separating ring, the operation is simple, and the cost is relatively low;
(2) the three-way joint is arranged, so that the pipelines at all sections of the separating ring are connected end to form a closed loop, the sealing performance of equipment is ensured, and meanwhile, an air inlet pipeline, an air outlet pipeline and a liquid guide assembly are conveniently connected into the separating ring;
(3) the air inlet pipeline is arranged in a vertical state, the air inlet of the air inlet pipeline is arranged at the lower end, when air flows into the vertical air inlet pipeline, water vapor of the part, contacting the inner wall of the air inlet pipeline, of the water-containing air is condensed into liquid water and flows downwards from the air inlet of the air inlet pipeline under the action of gravity to be discharged out of the gas separation ring, primary gas-liquid separation is realized, meanwhile, the air outlet pipeline is arranged in a vertical state, the air inlet of the air outlet pipeline is arranged at the lower end, and when the water-containing air passes through the air outlet pipeline, the water vapor is also condensed into liquid water and flows downwards into the separation ring under the action of cooling and gravity of the inner wall of the pipeline, so that the working efficiency of the device is improved;
(4) by arranging the liquid drainage pipeline and the liquid storage tank, liquid water collected at the bottom of the separation ring is downwards drained out of the liquid storage tank in the gas-liquid separation ring in time through the vertically arranged liquid drainage pipeline under the action of gravity, so that the interior of the separation ring is always in a drier state, the separation efficiency is improved, and the liquid storage tank is used for preventing the drained liquid water from splashing everywhere;
(5) the humidity measuring instrument is arranged at the gas outlet pipeline and used for displaying the humidity of the gas-liquid separated sample so as to judge whether the sample meets the standard or not, and a worker judges whether the gas-liquid separation work needs to be carried out again or not according to the data;
(6) through hanging the setting in the liquid storage pot of fluid-discharge line, can prevent effectively that the device from suck liquid backward when suspending to prevent effectively that liquid from to the pollution and the erosion of device.
Drawings
Fig. 1 is an overall schematic diagram of an embodiment of the present invention.
Reference numerals: 1. a separating ring; 11. a first U-shaped pipe; 12. a second U-shaped tube; 13. a straight line pipe; 2. an air intake line; 3. a gas outlet pipeline; 4. a liquid guiding component; 41. a drainage line; 42. a liquid storage tank; 5. a humidity measuring instrument; 6. a gasket; 7. a three-way joint.
Detailed Description
The present invention will be described in further detail with reference to the following examples and drawings, but the embodiments of the present invention are not limited thereto.
As shown in figure 1, a gas-liquid separation ring comprises a separation ring 1, the separation ring 1 is used for realizing gas-liquid separation of water-containing gas and preventing water vapor from uprushing, the separation ring 1 is wholly in a closed ring shape, the separation ring 1 is divided into three sections, namely a first U-shaped pipe 11, a second U-shaped pipe 12 and a straight pipe 13, the three sections of pipes are communicated with each other in a head position through a tee joint 7 (the tee joint of the utility model adopts a T-shaped tee joint, the protruding end of the tee joint is in the vertical direction of the tee joint), the interfaces of the tee joint 7 connected between every two three sections of pipes are in the horizontal direction, the vertical directions of the tee joints 7 at two positions of the separation ring 1 are respectively communicated with an air inlet pipeline 2 and an air outlet pipeline 3, and the vertical direction of the tee joint 7 at the other position of the separation ring 1 is also provided with a liquid guide component 4, the gas inlet pipeline 2 and the gas outlet pipeline 3 are used for circulating gas, and the liquid guide component 4 is used for guiding out liquid in the device.
For the circulation of convenient gas, air inlet pipeline 2 all is vertical direction setting with giving vent to anger pipeline 3 to, considering that gas density is less, air inlet pipeline 2 and the air inlet setting of giving vent to anger pipeline 3 are at air inlet pipeline 2/the lower extreme that gives vent to anger pipeline 3.
After the water-containing gas enters the gas inlet pipeline 2, because the temperature of the inner wall of the pipeline is lower, part of water vapor is condensed into liquid water to be attached to the pipe wall, because of the action of gravity, the liquid water flows out of the device along the gas inlet pipeline 2 to realize the first gas-liquid separation, after the water-containing gas enters the separating ring 1 through the gas inlet pipeline 2, when the water flows in the separating ring 1, part of the water vapor is condensed into liquid water to be attached to the inner wall of the pipeline of the separating ring 1, the liquid water gradually converges to the bottom of the separating ring 1 under the action of gravity to realize the second gas-liquid separation, when a drier gas sample passing through the separating ring 1 is discharged out of the device through the gas outlet pipeline 3 vertically arranged at one side of the upper end of the separating ring 1, under the cooling and gravity action of the inner wall of the pipeline, the water vapor is also condensed into liquid water to be downward discharged into the separating ring 1 to realize the third gas-liquid separation, and the third gas-liquid separation is carried out, the moisture in the gas is sufficiently removed.
Because the gas-liquid separation efficiency in the separation ring 1 is easily reduced by the liquid water stored in the separation ring 1, the arranged liquid guiding assembly 4 is used for discharging the liquid water in the separation ring 1 out of the device, the liquid guiding assembly 4 comprises a liquid discharging pipeline 41 and a liquid storage tank 42, the liquid discharging pipeline 41 is arranged in the liquid storage tank 42, the liquid discharging pipeline 41 is detachably connected with the separation ring 1 through a vertical port of a three-way joint 7, a certain height difference exists between the liquid discharging pipeline 41 and the gas inlet pipeline 2 and the gas outlet pipeline 3, the liquid water in the separation ring 1 flows into the liquid storage tank 42 along the liquid discharging pipeline 41 under the action of gravity, in order to prevent liquid from flowing back or the liquid in the liquid storage tank 42 from polluting the separation ring 1, the liquid discharging pipeline 41 is arranged in the liquid storage tank 42 in a suspended mode and is not contacted with the liquid in the liquid storage tank 42, and the liquid storage tank 42 can also effectively prevent the discharged liquid water from scattering everywhere.
In order to prevent the leakage loss of the water-containing gas in the device, the three-way joint 7 and the separating ring 1 as well as the interfaces of the air inlet pipeline 2, the air outlet pipeline 3 and the liquid discharge pipeline 41 are provided with sealing gaskets 6, and drying agents are arranged inside the three-way joint 7 and used for improving the gas-liquid separation efficiency.
In order to judge whether gas-liquid separation ring combustion gas accords with the sample standard, the utility model discloses still be provided with moisture meter 5 in 3 outside intercommunications of gas outlet pipe way, whether the staff judges sample gas can get into analytical instrument or get into separating ring 1 again and carry out gas-liquid separation work according to moisture meter 5's registration.
The working process of the utility model is as follows:
after water-containing gas enters the vertical gas inlet pipeline 2, part of water vapor is condensed into liquid water to flow back along the inner wall to realize first gas-liquid separation, after the gas enters the separation ring 1, the water vapor which is not completely removed contacts the inner wall of the annular pipeline to be condensed into liquid water attached to the pipe wall, the accumulated liquid on the pipe wall is collected to the bottom of the pipeline under the action of gravity, the accumulated liquid at the bottom of the pipeline continuously flows downwards into the liquid storage tank 42 through the liquid discharge pipeline 41 to realize second gas-liquid separation, the water-containing gas is changed into drier gas after the gas-liquid separation is finished to enter the gas outlet pipeline 3, when the flowing gas flows in the upward gas outlet pipeline 3, the water which is not completely removed is condensed into liquid water again to flow back to the inside of the separation ring 1 to realize final gas-liquid separation, and a worker judges whether the sample is qualified or not by observing the humidity measuring instrument 5 which is externally connected with the gas outlet pipeline 3.
It is above only the utility model discloses a preferred embodiment, the utility model discloses a scope of protection does not only confine above-mentioned embodiment, the all belongs to the utility model discloses a technical scheme under the thinking all belongs to the utility model discloses a scope of protection. It should be noted that, for those skilled in the art, various modifications and decorations can be made without departing from the principle of the present invention, and such modifications and decorations should also be regarded as the protection scope of the present invention.
Claims (7)
1. The gas-liquid separation ring is characterized by comprising a separation ring (1), wherein the separation ring (1) is in a closed ring shape, two parts of the separation ring (1) are respectively communicated with an air inlet pipeline (2) and an air outlet pipeline (3), a liquid guide assembly (4) is further arranged at the other part of the separation ring (1), and the liquid guide assembly (4) is arranged below the air inlet pipeline (2) and the air outlet pipeline (3).
2. The gas-liquid separation ring according to claim 1, wherein the separation ring (1) comprises a first U-shaped pipe (11), a second U-shaped pipe (12) and a straight pipe (13), the first U-shaped pipe (11), the second U-shaped pipe (12) and the straight pipe (13) are communicated end to end through a tee joint (7), the air inlet pipeline (2) is arranged at a joint of the first U-shaped pipe (11) and the straight pipe (13), the air outlet pipeline (3) is arranged at a joint of the second U-shaped pipe (12) and the straight pipe (13), the separation ring (1) is placed in a vertical direction, the tee joint (7) at the joint of the first U-shaped pipe (11) and the second U-shaped pipe (12) is located at the lower part of the separation ring (1) in the vertical direction, and the tee joint (7) at the joint of the straight pipe (13) and the first U-shaped pipe (11) are arranged in the vertical direction, And a tee joint (7) at the interface of the straight pipe (13) and the second U-shaped pipe (12) is positioned at the upper part of the separation ring (1) in the vertical direction.
3. The gas-liquid separation ring as claimed in claim 2, wherein the gas inlet pipeline (2) is arranged in a vertical direction, the gas inlet of the gas inlet pipeline (2) is arranged at the lower end of the gas inlet pipeline (2), the gas outlet of the gas inlet pipeline (2) is detachably connected with the separation ring (1) through a downward port of the tee joint (7), the gas outlet pipeline (3) is arranged in a vertical direction, the gas outlet of the gas outlet pipeline (3) is arranged at the upper end of the gas outlet pipeline (3), and the gas inlet of the gas outlet pipeline (3) is detachably connected with the separation ring (1) through an upward port of the tee joint (7).
4. The gas-liquid separation ring according to claim 2, wherein the liquid guiding assembly (4) comprises a liquid draining pipe (41) and a liquid storage tank (42), and the liquid draining pipe (41) is arranged at the joint where the first U-shaped pipe (11) and the second U-shaped pipe (12) are communicated.
5. The gas-liquid separation ring according to claim 4, wherein the liquid discharge pipe (41) is vertically disposed, and a liquid inlet of the liquid discharge pipe (41) is disposed at an upper end of the liquid discharge pipe (41).
6. The gas-liquid separation ring as recited in claim 1, wherein a humidity measuring instrument (5) is communicated with the outside of the gas outlet pipeline (3), and the humidity measuring instrument (5) is used for displaying the humidity of the gas sample after passing through the gas-liquid separation ring.
7. The gas-liquid separation ring according to claim 4, wherein the liquid discharge pipe (41) is placed in the reservoir (42), and the liquid discharge pipe (41) is suspended in the reservoir (42).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123101829.5U CN217473116U (en) | 2021-12-06 | 2021-12-06 | Gas-liquid separation ring |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123101829.5U CN217473116U (en) | 2021-12-06 | 2021-12-06 | Gas-liquid separation ring |
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| Publication Number | Publication Date |
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| CN217473116U true CN217473116U (en) | 2022-09-23 |
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| CN202123101829.5U Active CN217473116U (en) | 2021-12-06 | 2021-12-06 | Gas-liquid separation ring |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117045230A (en) * | 2023-09-11 | 2023-11-14 | 复旦大学附属中山医院 | A collection device for assisting monitoring breathe end carbon dioxide |
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2021
- 2021-12-06 CN CN202123101829.5U patent/CN217473116U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117045230A (en) * | 2023-09-11 | 2023-11-14 | 复旦大学附属中山医院 | A collection device for assisting monitoring breathe end carbon dioxide |
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