CN204996242U - Water conservancy diversion baffle and horizontal deareator thereof - Google Patents
Water conservancy diversion baffle and horizontal deareator thereof Download PDFInfo
- Publication number
- CN204996242U CN204996242U CN201520760335.3U CN201520760335U CN204996242U CN 204996242 U CN204996242 U CN 204996242U CN 201520760335 U CN201520760335 U CN 201520760335U CN 204996242 U CN204996242 U CN 204996242U
- Authority
- CN
- China
- Prior art keywords
- blocking
- flow apron
- flow
- conservancy diversion
- water conservancy
- Prior art date
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract 11
- 239000007788 liquid Substances 0.000 claims abstract description 23
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 18
- 239000010959 steel Substances 0.000 claims abstract description 18
- 239000007787 solid Substances 0.000 claims abstract description 11
- 230000005514 two-phase flow Effects 0.000 claims abstract description 11
- 239000007791 liquid phase Substances 0.000 claims abstract description 10
- 241000681094 Zingel asper Species 0.000 claims description 38
- 230000000903 blocking Effects 0.000 claims description 31
- 239000007792 gaseous phase Substances 0.000 claims description 10
- 238000010521 absorption reaction Methods 0.000 claims description 4
- 238000000926 separation method Methods 0.000 abstract description 5
- 238000005259 measurement Methods 0.000 abstract 1
- 238000005191 phase separation Methods 0.000 abstract 1
- 239000011901 water Substances 0.000 description 11
- 239000007789 gases Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 239000012071 phases Substances 0.000 description 1
- 230000001340 slower Effects 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
Abstract
The utility model discloses a water conservancy diversion baffle and horizontal deareator thereof. Be provided with the water conservancy diversion baffle in the horizontal deareator, the striking district for left rectification district and right side is separated with horizontal deareator to the water conservancy diversion baffle, the import of air water two -phase flow is distinguished with the striking and is connected, the gas exports setting is in rectification district upper end, and the liquid phase export sets up distinguishes the lower extreme in the rectification, the rectification district still is provided with the overflow mouth, the level gauge is connected to rectification district left end, supreme separation section and the water conservancy diversion section down of including is in proper order down followed to the water conservancy diversion baffle, the separation section is solid steel plate structure, the steel plate structure of water conservancy diversion section for being provided with a plurality of through -holes down. The utility model discloses flow field inequality in the gas -liquid two -phase separation technology system can effectively be solved to the water conservancy diversion baffle of application, and the liquid level is undulant great, and liquid level measurement is inaccurate, and the liquid drop is easily along with gaseous spill scheduling problem.
Description
Technical field
The utility model relates to circulating water system, refers to a kind of flow apron and horizontal pneumatic separator thereof especially.
Background technology
At engineering field, moisture trap is often designed to the vertical tank body of single admission.The problems such as it is large that the type moisture trap exists floor space, and separating effect is not good, and liquid is easily gone out, and tank level fluctuation is large.Inner at knockout drum, part moisture trap does not arrange baffle plate, or arranges baffle plate and be also only simple geometry entity and be placed near separator gaseous phase outlet.But the setting of this baffle plate result in the further increase of flow resistance, the disturbance of tank flow field aggravates, and level gauging is forbidden, and gas-water separation carries effect limited extent, and liquid still cannot be avoided to go out phenomenon.
Utility model content
The purpose of this utility model is the horizontal pneumatic separator flow apron overcoming the disturbance of horizontal pneumatic separator flow field, level gauging is forbidden and provided.
The utility model realizes by following technical scheme:
Flow apron, comprises lower blocking section and diversion section successively; Described lower blocking section is solid steel plate structure, and described diversion section is the steel plate structure being provided with some through holes.
Described lower blocking section top is provided with the horizontal wave absorption plate extended to described impingement region.
Described lower blocking section right side is provided with damping ripple struction.
Flow apron above described diversion section is also provided with blocking section, and described upper blocking section is solid steel plate structure.
Described diversion section is provided with array of circular apertures or square hole array or shutter grid structure.
With the horizontal pneumatic separator of flow apron, comprise horizontal pneumatic separator, described horizontal pneumatic separator comprises air-water two phase flow import, gaseous phase outlet, liquid-phase outlet, overfall and liquid level gauge.
Be provided with flow apron in described horizontal pneumatic separator, described horizontal pneumatic separator is divided into the commutating zone in left side and the impingement region on right side by described flow apron; Described air-water two phase flow import is connected with described impingement region; Described gaseous phase outlet is arranged on described commutating zone upper end, and described liquid-phase outlet is arranged on described commutating zone lower end; Described commutating zone is also provided with overfall; Described commutating zone left end connects described liquid level gauge;
Described flow apron comprises lower blocking section and diversion section from bottom to up successively; Described lower blocking section is solid steel plate structure, and described diversion section is the steel plate structure being provided with some through holes.
It is uneven that the flow apron that the utility model uses effectively can solve gas-liquid two-phase separating technology system flow field, liquid fluctuating is larger, level gauging is forbidden, drop is easily with problems such as gas spill: after biphase gas and liquid flow is compiled in impingement region, gas-water separation upper back gas flows into commutating zone by diversion section, liquid after being separated is then by bottom and the commutating zone UNICOM of blocking section, thus keep impingement region consistent with commutating zone liquid level, while strengthening gas-liquid separation, farthest less drop spills, and maintains the stable of liquid level and improve certainty of measurement.
Accompanying drawing explanation
Fig. 1 is horizontal pneumatic separator schematic cross-section.
Fig. 2 is flow apron front view and side view (circular hole).
Fig. 3 is flow apron front view and side view (square groove).
Fig. 4 is flow apron front view and side view (louver grid-type).
In figure: horizontal pneumatic separator 0; Flow apron 1; Horizontal wave absorption plate 11; Upper blocking section 12; Lower blocking section 13; Diversion section 14; Air-water two phase flow import 2; Impingement region 3; Commutating zone 4; Gaseous phase outlet 5; Liquid-phase outlet 6; Overfall 7; Liquid level gauge 8.
Detailed description of the invention
Below in conjunction with drawings and Examples, the utility model is described in further detail, but this embodiment should not be construed restriction of the present utility model, only for example, simultaneously by illustrating that advantage of the present utility model will become clearly and easy understand.
As shown in drawings, horizontal pneumatic separator flow apron, comprises horizontal pneumatic separator 0, and horizontal pneumatic separator 0 comprises air-water two phase flow import 2, gaseous phase outlet 5, liquid-phase outlet 6, overfall 7 and liquid level gauge 8.
Be provided with flow apron 1 in horizontal pneumatic separator 0, horizontal pneumatic separator 0 is divided into the commutating zone 4 in left side and the impingement region 3 on right side by flow apron 1; Air-water two phase flow import 2 is connected with impingement region 3; Air-water two phase flow import 2 is provided with corner structure, reduces the impact in impingement region 3.Gaseous phase outlet 5 is arranged on commutating zone 4 upper end, and liquid-phase outlet 6 is arranged on commutating zone 4 lower end; Commutating zone 4 is also provided with overfall 7; Commutating zone 4 left end connects liquid level gauge 8;
Flow apron 1 comprises lower blocking section 13 and diversion section 14 from bottom to up successively; Lower blocking section 13 is solid steel plate structure, and diversion section 14 is for being provided with the steel plate structure of some through holes.
Lower blocking section 13 top is provided with the horizontal wave absorption plate 11 extended to impingement region 3, stops energized fluid to enter commutating zone 4 by diversion section 14.In horizontal pneumatic separator 0, liquid level is in lower blocking section 13 scope.
Lower blocking section 13 right side is provided with damping ripple struction, slows down the vibration of impingement region 3.
Flow apron 1 above diversion section 14 is also provided with blocking section 15, and upper blocking section 15 is solid steel plate structure, arranges blocking section 15 and stops high energy steam group to enter commutating zone 4.
Diversion section 14 is provided with array of circular apertures or square hole array or shutter grid structure.
With the horizontal pneumatic separator of flow apron, comprise horizontal pneumatic separator 0, described horizontal pneumatic separator 0 comprises air-water two phase flow import 2, gaseous phase outlet 5, liquid-phase outlet 6, overfall 7 and liquid level gauge 8.
Be provided with flow apron 1 in horizontal pneumatic separator 0, horizontal pneumatic separator 0 is divided into the commutating zone 4 in left side and the impingement region 3 on right side by flow apron 1; Air-water two phase flow import 2 is connected with impingement region 3; Gaseous phase outlet 5 is arranged on commutating zone 4 upper end, and liquid-phase outlet 6 is arranged on commutating zone 4 lower end; Commutating zone 4 is also provided with overfall 7; Commutating zone 4 left end connects liquid level gauge 8;
Flow apron 1 comprises lower blocking section 13 and diversion section 14 from bottom to up successively; Lower blocking section 13 is solid steel plate structure, and diversion section 14 is for being provided with the steel plate structure of some through holes.
It should be noted that: to those of ordinary skill in the art, can also make some changes or distortion to the utility model under the prerequisite not changing the utility model principle, this belongs to protection domain of the present utility model equally.
Claims (8)
1. flow apron, is characterized in that: comprise flow apron (1), and described flow apron (1) comprises lower blocking section (13) and diversion section (14) from bottom to up successively; Described lower blocking section (13) is solid steel plate structure, and described diversion section (14) is for being provided with the steel plate structure of some through holes.
2. flow apron according to claim 1, is characterized in that: described lower blocking section (13) top is provided with the horizontal wave absorption plate (11) extended to described impingement region (3).
3. flow apron according to claim 1 and 2, is characterized in that: described lower blocking section (13) right side is provided with damping ripple struction.
4. flow apron according to claim 1, it is characterized in that: the flow apron (1) of described diversion section (14) top is also provided with blocking section (12), and described upper blocking section (12) is solid steel plate structure.
5. flow apron according to claim 3, it is characterized in that: the flow apron (1) of described diversion section (14) top is also provided with blocking section (12), and described upper blocking section (12) is solid steel plate structure.
6. flow apron according to claim 5, is characterized in that: described diversion section (14) is provided with array of circular apertures or square hole array or shutter grid structure.
7. flow apron according to claim 1, is characterized in that: described diversion section (14) is provided with array of circular apertures or square hole array or shutter grid structure.
8. be with the horizontal pneumatic separator of flow apron, comprise horizontal pneumatic separator (0), described horizontal pneumatic separator (0) comprises air-water two phase flow import (2), gaseous phase outlet (5), liquid-phase outlet (6), overfall (7) and liquid level gauge (8), it is characterized in that:
Be provided with flow apron (1) in described horizontal pneumatic separator (0), described horizontal pneumatic separator (0) is divided into the commutating zone (4) in left side and the impingement region (3) on right side by described flow apron (1); Described air-water two phase flow import (2) is connected with described impingement region (3); Described gaseous phase outlet (5) is arranged on described commutating zone (4) upper end, and described liquid-phase outlet (6) is arranged on described commutating zone (4) lower end; Described commutating zone (4) is also provided with overfall (7); Described commutating zone (4) left end connects described liquid level gauge (8);
Described flow apron (1) comprises lower blocking section (13) and diversion section (14) from bottom to up successively; Described lower blocking section (13) is solid steel plate structure, and described diversion section (14) is for being provided with the steel plate structure of some through holes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520760335.3U CN204996242U (en) | 2015-09-28 | 2015-09-28 | Water conservancy diversion baffle and horizontal deareator thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520760335.3U CN204996242U (en) | 2015-09-28 | 2015-09-28 | Water conservancy diversion baffle and horizontal deareator thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204996242U true CN204996242U (en) | 2016-01-27 |
Family
ID=55153148
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520760335.3U CN204996242U (en) | 2015-09-28 | 2015-09-28 | Water conservancy diversion baffle and horizontal deareator thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204996242U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106422531A (en) * | 2016-08-31 | 2017-02-22 | 中国电力工程顾问集团中南电力设计院有限公司 | Horizontal gas-water separator with built-in heat exchanger and gas-water separating method thereof |
| CN107741777A (en) * | 2017-11-02 | 2018-02-27 | 曙光节能技术（北京）股份有限公司 | Cooling system and liquid cooled server for server |
-
2015
- 2015-09-28 CN CN201520760335.3U patent/CN204996242U/en active IP Right Grant
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106422531A (en) * | 2016-08-31 | 2017-02-22 | 中国电力工程顾问集团中南电力设计院有限公司 | Horizontal gas-water separator with built-in heat exchanger and gas-water separating method thereof |
| CN107741777A (en) * | 2017-11-02 | 2018-02-27 | 曙光节能技术（北京）股份有限公司 | Cooling system and liquid cooled server for server |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| C14 | Grant of patent or utility model |