CN220047597U - Horizontal separator for high-efficiency gas-liquid two-phase separation - Google Patents
Horizontal separator for high-efficiency gas-liquid two-phase separation Download PDFInfo
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- CN220047597U CN220047597U CN202321677200.1U CN202321677200U CN220047597U CN 220047597 U CN220047597 U CN 220047597U CN 202321677200 U CN202321677200 U CN 202321677200U CN 220047597 U CN220047597 U CN 220047597U
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- 239000007788 liquid Substances 0.000 title claims abstract description 165
- 238000005191 phase separation Methods 0.000 title claims abstract description 14
- 238000000926 separation method Methods 0.000 claims abstract description 37
- 239000007921 spray Substances 0.000 claims abstract description 34
- 238000001704 evaporation Methods 0.000 claims abstract description 32
- 230000008020 evaporation Effects 0.000 claims abstract description 32
- 230000005484 gravity Effects 0.000 claims abstract description 31
- 238000005507 spraying Methods 0.000 claims abstract description 23
- 238000009827 uniform distribution Methods 0.000 claims abstract description 23
- 238000004062 sedimentation Methods 0.000 claims abstract description 22
- 238000005192 partition Methods 0.000 claims abstract description 21
- 239000003595 mist Substances 0.000 claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 238000005485 electric heating Methods 0.000 claims description 9
- 239000010865 sewage Substances 0.000 claims description 9
- 230000001502 supplementing effect Effects 0.000 claims description 7
- 230000010354 integration Effects 0.000 abstract description 9
- 238000009434 installation Methods 0.000 abstract description 3
- 239000012535 impurity Substances 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 3
- 239000000945 filler Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000003020 moisturizing effect Effects 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Abstract
The utility model discloses a horizontal separator for high-efficiency vapor-liquid two-phase separation, which mainly comprises a spray evaporation area, a gravity sedimentation area, a mist capturing area and a liquid collecting area; the spraying evaporation area is intersected with the gravity sedimentation area and the liquid collecting area respectively and is intersected with the liquid level of the steam uniform distribution partition board (5) and the liquid collecting area; the gravity sedimentation area is intersected with the mist capturing area and the liquid collecting area respectively and is intersected with the liquid level of the liquid remover (6) and the liquid collecting area; the mist capturing area is intersected with the liquid collecting area and is intersected with the liquid level of the liquid collecting area. Compared with the traditional separator, the horizontal separator has higher vapor-liquid two-phase separation efficiency and better separation stability; the vertical height of the horizontal separator is lower, so that the integration compactness of the evaporation system is improved, and the transportation and the high-efficiency integration of the evaporation system are facilitated; the horizontal separator is mainly suitable for special occasions with limited installation height, high system integration requirements and the like.
Description
Technical Field
The utility model belongs to the field of vapor-liquid separation, and particularly relates to a horizontal separator for efficient vapor-liquid two-phase separation.
Background
The gas-liquid separator is a separating device for realizing efficient liquid removal, and mainly comprises a barrel, a cyclone separator, an efficient foam breaking net, a blow-down valve and other main components, wherein a plurality of separating structures are generally adopted, and the separating method comprises the following steps: gravity settling, baffling separation, centrifugal force separation, silk screen separation, ultrafiltration separation, filler separation and the like. From the viewpoint of the requirements of the vapor-liquid separator, it is required that the separator is capable of separating the gas from the liquid as much as possible, and after passing through the vapor-liquid separator, the liquid is the liquid and contains no gas, and the gas is the gas and contains no liquid. In practical cases, the vapor-liquid separator needs to be selected according to different separation requirements. For example, the separation requirement is relatively low, and gravity settling separation is selected; the separation requires generally, common baffle separation (baffle separation) or common centrifugal separation (cyclone separation) are selected; the requirement is high, and filler separation is selected; the requirement is high, and silk screen separation is selected; the requirements are very high, and microporous filtration separation is selected.
CN101396628A provides a horizontal gas-liquid separator, which is characterized in that a plurality of separation units are fixedly distributed in a cavity of a shell through a tube plate, each separation unit is provided with a unit tube shell, and a gas inlet and a gas outlet are arranged on the left side and the right side of the unit tube shell. CN103055608A relates to a novel horizontal gas-liquid separator, which consists of a shell with a sealing structure, a liquid phase outlet pipe, a gas-liquid two-phase inlet pipe, a spiral pipe shell and a liquid collecting cavity. CN 103453512a relates to a steam-water separator housing, which solves the problems that the existing steam-water separator housing, steam-water mixture enters the housing, cannot be primarily purified in the steam-water mixture entering stage, cannot realize the enlargement of the separator, and is inconvenient for the overhaul of the separator. CN103585823 a discloses a one-tank multistage horizontal separator, which comprises a tank body, a tank foot, a graded drip stand pipe, a drip converging pipe and the like, and improves the purity of oxyhydrogen by utilizing the principles of gravity sedimentation separation, centrifugal separation, collision separation and multiple separation. CN105311882a relates to a horizontal oil-gas separator, which is provided with an oil-gas separation section, a primary filter element and a secondary filter element are arranged in the horizontal oil-gas separator, and a plurality of filter holes are formed in the side walls of the primary filter element and the secondary filter element. The horizontal separators of all of the above patents are quite different from the present utility model and are quite distinct.
From the technical and economic point of view, the utility model provides the horizontal type separator for high-efficiency gas-liquid two-phase separation, which is mainly applicable to special occasions with limited installation height, high system integration requirement and the like, not only improves the integration compactness of the evaporation system, but also is more beneficial to transportation and high-efficiency integration of the evaporation system; the horizontal separator has important significance for promoting the development of the current vapor-liquid efficient separation technology.
Disclosure of Invention
First, the technical problem to be solved
The technical problems to be solved by the utility model are as follows: the horizontal separator for high-efficiency vapor-liquid two-phase separation is provided for improving the separation efficiency of vapor-liquid two-phase separation after evaporation, reducing the vertical height of separation and improving the compactness of an evaporation integrated system.
(II) technical scheme
In order to solve the technical problems, the technical scheme of the utility model is as follows: the horizontal separator mainly comprises a spray evaporation area, a gravity sedimentation area, a mist capturing area and a liquid collecting area;
the spraying evaporation area is intersected with the gravity sedimentation area and the liquid collecting area respectively and is intersected with the liquid level of the steam uniform distribution partition board (5) and the liquid collecting area;
the gravity sedimentation area is intersected with the mist capturing area and the liquid collecting area respectively and is intersected with the liquid level of the liquid remover (6) and the liquid collecting area;
the mist capturing area is intersected with the liquid collecting area and is intersected with the liquid level of the liquid collecting area.
Further, the spray evaporation area is mainly positioned at the left side part of the steam uniform distribution partition board (5) and mainly comprises the left side part of the horizontal tank body (1), a steam inlet (2), an electric heater (3), a spray liquid inlet (4), the steam uniform distribution partition board (5), a water supplementing port (9), a water spraying interface (10), a spray liquid interface (11) and a sewage outlet (12);
the spraying evaporation area increases evaporation capacity and reduces impurity content in the steam mainly through spraying measures;
the steam inlet (2) is a short pipe with a 90-degree elbow, the outlet is opposite to the left end socket section of the horizontal tank body (1), and the steam inlet is mainly used for carrying out primary impact separation when the steam to be separated enters the horizontal tank body (1) along with the pipeline, and part of liquid can fall into a liquid collecting area of the part;
the electric heating unit (3) is composed of a plurality of groups of electric heating elements, and the actual requirements of a spraying evaporation area are required to be met;
the spray liquid inlets (4) are composed of a plurality of groups of spray liquid, are uniformly distributed in the upper space of the spray evaporation area, and are required to enable no dead angle to appear in the spray space of the horizontal tank body (1);
the spray liquid interface (11) is provided with two replaceable pipelines.
Further, the gravity sedimentation zone is mainly positioned between the steam uniform distribution partition plate (5) and the liquid remover (6), and mainly comprises the middle part of the horizontal tank body (1), the steam uniform distribution partition plate (5), the liquid remover (6), the liquid level meter (13), the liquid level meter lower interface (14), the liquid level meter upper interface (15), the pressure meter interface (16), the thermometer interface (17), the pressure relief valve interface (18) and the standby interface (19);
the gravity sedimentation zone mainly removes liquid entrained in steam from vapor from the spray evaporation zone in a gravity sedimentation mode;
the steam uniform distribution partition plate (5) is a circular uniform distribution partition plate with holes, which is fixed inside the horizontal tank body (1), and a certain distance of no holes are reserved at the top, as shown in fig. 3, so that steam is prevented from directly passing through the top and then entering the gravity sedimentation zone.
Further, the mist capturing area is mainly positioned at the right side part of the liquid remover (6) and mainly comprises the right side part of the horizontal tank body (1), the liquid remover (6), a steam exhaust baffle (7), a steam exhaust port (8) and a sewage outlet (12);
the liquid remover (6) is a liquid removing device filled with metal separation materials, and can be replaced or used for removing impurities;
the steam exhaust baffle (7) is used for preventing steam from being exhausted after the steam passes through the top of the liquid remover (6), and liquid entrained in the steam can be further removed in a bypass mode.
Further, the liquid collecting area is mainly located at the bottom of the horizontal tank body (1), mainly comprises the bottom of the horizontal tank body (1), an electric heating device (3), a water supplementing port (9), a water spraying port (10), a spraying liquid port (11), a sewage draining port (12) and a liquid level meter lower port (14), and is located at the filling part in fig. 1.
(III) beneficial effects
After the technical scheme is adopted, the utility model has the following beneficial effects:
(1) Compared with the traditional separator, the horizontal separator has higher vapor-liquid two-phase separation efficiency and better separation stability;
(2) The vertical height of the horizontal separator is lower, so that the integration compactness of the evaporation system is improved, and the transportation and the high-efficiency integration of the evaporation system are facilitated;
(3) The horizontal separator is mainly suitable for special occasions with limited installation height, high system integration requirements and the like.
Drawings
In order to more clearly illustrate the embodiments of the utility model or the technical solutions in the prior art, the drawings that are required in the embodiments or the description of the prior art will be briefly described, it being obvious that the drawings in the following description are only some embodiments of the utility model, and that other drawings may be obtained according to these drawings without inventive effort for a person skilled in the art.
Fig. 1 is a horizontal separator for efficient vapor-liquid separation according to the present utility model, and fig. 2 and 3 are complementary illustrations of fig. 1.
The symbols in the figures are respectively as follows:
horizontal jar body (1), steam inlet (2), electrical heating (3), spray liquid import (4), steam equipartition baffle (5), knockout (6), exhaust baffle (7), exhaust mouth (8), moisturizing mouth (9), water spray interface (10), spray liquid interface (11), drain (12), liquid level gauge (13), liquid level gauge lower interface (14), liquid level gauge upper interface (15), manometer interface (16), thermometer interface (17), relief valve interface (18), reserve interface (19).
Detailed Description
In order that the utility model may be more readily understood, a more particular description of the utility model will be rendered by reference to specific embodiments that are illustrated in the appended drawings.
As shown in figure 1, the horizontal separator for high-efficiency vapor-liquid two-phase separation is mainly divided into a spray evaporation area, a gravity sedimentation area, a mist capturing area and a liquid collecting area;
the spraying evaporation area is intersected with the gravity sedimentation area and the liquid collecting area respectively and is intersected with the liquid level of the steam uniform distribution partition board (5) and the liquid collecting area;
the gravity sedimentation area is intersected with the mist capturing area and the liquid collecting area respectively and is intersected with the liquid level of the liquid remover (6) and the liquid collecting area;
the mist capturing area is intersected with the liquid collecting area and is intersected with the liquid level of the liquid collecting area.
Preferably, as shown in fig. 1, the spray evaporation area is mainly located at the left side part of the steam uniform distribution partition board (5), and mainly comprises the left side part of the horizontal tank body (1), a steam inlet (2), an electric heating (3), a spray liquid inlet (4), the steam uniform distribution partition board (5), a water supplementing port (9), a water spraying interface (10), a spray liquid interface (11) and a sewage outlet (12);
the spraying evaporation area increases evaporation capacity and reduces impurity content in the steam mainly through spraying measures;
the steam inlet (2) is a short pipe with a 90-degree elbow, the outlet is opposite to the left end socket section of the horizontal tank body (1), and the steam inlet is mainly used for carrying out primary impact separation when the steam to be separated enters the horizontal tank body (1) along with the pipeline, and part of liquid can fall into a liquid collecting area of the part;
the electric heating unit (3) is composed of a plurality of groups of electric heating elements, and the actual requirements of a spraying evaporation area are required to be met;
the spray liquid inlets (4) are composed of a plurality of groups of spray liquid, are uniformly distributed in the upper space of the spray evaporation area, and are required to enable no dead angle to appear in the spray space of the horizontal tank body (1);
the spray liquid interface (11) is provided with two replaceable pipelines;
the work flow of the spray evaporation area is specifically as follows:
firstly, gas to be separated enters a horizontal tank body (1) along with a pipeline from a gas inlet (2) for primary impact separation, and part of liquid falls into a liquid collecting area of the part; secondly, the steam after primary separation gradually flows to a steam uniform distribution baffle plate (5) along with the horizontal tank body (1) from left to right; thirdly, gas is contacted with a plurality of groups of spray liquid from the top to wash gas, and the spray liquid is continuously recycled; then, the electric heating (3) in the liquid collecting area can continuously heat the spray liquid, so that the spray liquid is vaporized to the greatest extent after spraying to generate vaporization, and the vapor loss generated in the gas washing process is supplemented; finally, the vapor gradually and uniformly flows from the vapor uniform distribution partition plate (5) to the gravity sedimentation area, thereby completing the circulation of the spray evaporation area.
Preferably, as shown in fig. 1, the gravity settling zone is mainly located at a part between the steam uniform distribution partition plate (5) and the liquid remover (6), and mainly comprises a middle part of the horizontal tank body (1), the steam uniform distribution partition plate (5), the liquid remover (6), a liquid level meter (13), a liquid level meter lower interface (14), a liquid level meter upper interface (15), a pressure meter interface (16), a thermometer interface (17), a pressure relief valve interface (18) and a standby interface (19);
the gravity sedimentation zone mainly removes liquid entrained in steam from vapor from the spray evaporation zone in a gravity sedimentation mode;
the steam uniform distribution partition plate (5) is a circular uniform distribution partition plate with holes, which is fixed in the horizontal tank body (1), and a certain distance of no holes are reserved at the top, as shown in fig. 3, so that steam is prevented from directly passing through the top and then entering the gravity sedimentation zone;
the work flow of the gravity settling zone is specifically as follows:
firstly, the steam flowing out of a steam uniform distribution baffle plate (5) gradually flows to a liquid remover (6) along with a horizontal tank body (1) from left to right; secondly, the gas continuously generates gravity sedimentation along with the proceeding of the gas flow direction under the action of gravity during the period; then, after passing through the whole gravity settling zone, the liquid in the vapor has been substantially completely separated; finally, the liquid in the whole gravity settling zone is collected in the liquid collecting zone, so that the whole working cycle is completed.
Preferably, as shown in fig. 1, the mist capturing area is mainly located at the right side part of the liquid remover (6) and mainly comprises the right side part of the horizontal tank body (1), the liquid remover (6), the steam exhaust baffle (7), the steam exhaust port (8) and the sewage outlet (12);
the liquid remover (6) is a liquid removing device filled with metal separation materials, and can be replaced or used for removing impurities;
the steam exhaust baffle (7) is used for preventing steam from being exhausted after the steam passes through the top of the liquid remover (6), and liquid entrained in the steam can be further removed in a bypass mode;
the working flow of the mist capturing area is specifically as follows:
firstly, the gas flowing out of the liquid remover (6) gradually flows to the right end socket of the horizontal tank body (1) from left to right; secondly, after removing residual liquid in the steam, forming a bypass with a steam exhaust baffle (7) and discharging from a steam exhaust port (8); then, the liquid in the whole mist capturing area is collected in the liquid collecting area; finally, excess waste liquid can be discharged from the drain (12), thereby completing the entire work cycle.
Preferably, as shown in fig. 1, the liquid collecting area is mainly located at the bottom of the horizontal tank body (1), and mainly comprises the bottom of the horizontal tank body (1), an electric heater (3), a water supplementing port (9), a water spraying interface (10), a spraying liquid interface (11), a sewage draining outlet (12) and a liquid level meter lower interface (14), and is located at the filling part in fig. 1;
the working flow of the liquid collecting area is specifically as follows:
firstly, the liquid collecting area can collect liquid at the steam inlet (2); secondly, the liquid collecting area can collect liquid in the spraying evaporation area and provide spraying liquid for the whole spraying process; again, the liquid collection zone will collect liquid from the gravity settling zone; then, the liquid collecting area can collect liquid in the mist capturing area; finally, when the liquid in the liquid collecting area is insufficient, the liquid can be timely supplemented from the water supplementing port (9), so that the whole working cycle is completed.
The technical problems, technical solutions and advantageous effects solved by the present utility model have been further described in detail in the above-described embodiments, and it should be understood that the above-described embodiments are only illustrative of the present utility model and are not intended to limit the present utility model, and any modifications, equivalent substitutions, improvements, etc. within the spirit and principle of the present utility model should be included in the scope of protection of the present utility model.
Claims (5)
1. The horizontal separator for high-efficiency vapor-liquid two-phase separation is characterized by mainly comprising a spray evaporation area, a gravity sedimentation area, a mist capturing area and a liquid collecting area; the spraying evaporation area is intersected with the gravity sedimentation area and the liquid collecting area respectively and is intersected with the liquid level of the steam uniform distribution partition board (5) and the liquid collecting area; the gravity sedimentation area is intersected with the mist capturing area and the liquid collecting area respectively and is intersected with the liquid level of the liquid remover (6) and the liquid collecting area; the mist capturing area is intersected with the liquid collecting area and is intersected with the liquid level of the liquid collecting area.
2. The horizontal separator for efficient vapor-liquid two-phase separation according to claim 1, wherein the spray evaporation area is mainly located at the left side part of the vapor uniform distribution partition plate (5), and mainly comprises the left side part of the horizontal tank body (1), a vapor inlet (2), electric heating (3), a spray liquid inlet (4), the vapor uniform distribution partition plate (5), a water supplementing port (9), a water spraying interface (10), a spray liquid interface (11) and a sewage draining outlet (12).
3. The horizontal separator for efficient vapor-liquid two-phase separation according to claim 2, wherein the gravity settling zone is mainly located between the vapor uniform distribution partition plate (5) and the liquid remover (6), and mainly comprises the middle part of the horizontal tank body (1), the vapor uniform distribution partition plate (5), the liquid remover (6), the liquid level meter (13), the liquid level meter lower interface (14), the liquid level meter upper interface (15), the pressure meter interface (16), the thermometer interface (17), the pressure relief valve interface (18) and the standby interface (19).
4. A horizontal separator for efficient vapor-liquid separation according to claim 3, characterized in that the mist capturing zone is mainly located at the right side of the liquid remover (6) and mainly comprises the right side of the horizontal tank (1), the liquid remover (6), a vapor discharge baffle (7), a vapor discharge port (8) and a sewage outlet (12).
5. The horizontal separator for efficient vapor-liquid two-phase separation according to claim 4, wherein the liquid collecting area is mainly located at the bottom of the horizontal tank body (1) and mainly comprises the bottom of the horizontal tank body (1), an electric heating device (3), a water supplementing port (9), a water spraying interface (10), a spraying liquid interface (11), a sewage draining outlet (12) and a liquid level meter lower interface (14).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321677200.1U CN220047597U (en) | 2023-06-29 | 2023-06-29 | Horizontal separator for high-efficiency gas-liquid two-phase separation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321677200.1U CN220047597U (en) | 2023-06-29 | 2023-06-29 | Horizontal separator for high-efficiency gas-liquid two-phase separation |
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| Publication Number | Publication Date |
|---|---|
| CN220047597U true CN220047597U (en) | 2023-11-21 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321677200.1U Active CN220047597U (en) | 2023-06-29 | 2023-06-29 | Horizontal separator for high-efficiency gas-liquid two-phase separation |
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| Country | Link |
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| CN (1) | CN220047597U (en) |
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2023
- 2023-06-29 CN CN202321677200.1U patent/CN220047597U/en active Active
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