CN204490671U - The vertical gas-liquid two-phase gravitational separator of geothermal deep well well head - Google Patents
The vertical gas-liquid two-phase gravitational separator of geothermal deep well well head Download PDFInfo
- Publication number
- CN204490671U CN204490671U CN201520123254.2U CN201520123254U CN204490671U CN 204490671 U CN204490671 U CN 204490671U CN 201520123254 U CN201520123254 U CN 201520123254U CN 204490671 U CN204490671 U CN 204490671U
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- China
- Prior art keywords
- liquid
- tank body
- steam
- pipe
- separator
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- 239000007788 liquid Substances 0.000 title claims abstract description 38
- 239000012530 fluid Substances 0.000 claims abstract description 19
- 230000008676 import Effects 0.000 claims description 10
- 239000003595 mist Substances 0.000 claims description 4
- 238000000926 separation method Methods 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 4
- 239000002245 particle Substances 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 230000000087 stabilizing effect Effects 0.000 abstract description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 230000004888 barrier function Effects 0.000 description 1
- 235000014171 carbonated beverage Nutrition 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/10—Geothermal energy
Abstract
The utility model relates to the vertical gas-liquid two-phase gravitational separator of a kind of geothermal deep well well head, its technical scheme is: the side of tank body is provided with liquid-inlet pipe, the opposite side of tank body is provided with drain pipe, tank body is provided with escape pipe, blow-off pipe, liquid level display and safety valve, liquid level display connecting fluid level controller, the top of tank body is provided with tensimeter, tensimeter Bonding pressure sensor, described escape pipe is provided with pressure controlled valve, described liquid-inlet pipe connects the rare solution device of steam of disengagement chamber inside by initial separator, the bottom of the rare solution device of steam is provided with eddy flow wing plate, the bottom of liquid collecting cavity is provided with horizontal baffle, the beneficial effects of the utility model are: this equipment have utilize submersible pump do work be supplied to heat-exchange equipment, voltage stabilizing afterflow, the disposable separation of steam except effect of the medium sand class particle that anhydrates, property safe and reliable to operation, its cost is low, and floor space is little, is easy to remove dirt in cylindrical shell, be convenient to realize blowdown and liquid automatic control, be suitable for processing the air containing fluid compared with large discharge.
Description
Technical field
The utility model relates to a kind of steam and is separated desanding device, the particularly vertical gas-liquid two-phase gravitational separator of a kind of geothermal deep well well head.
Background technology
Geothermal energy resources are clean environment firendly, renewable energy source, are stored in deeper subsurface, because underground mine distribution is in variation, thus can contain various material such as inflammable gas, sand in underground water; Under mechanical action, hot water easily forms steam simultaneously.The separate discharge of inflammable gas or application are related to the safe utilization of geothermal energy resources, and steam mixing also causes the low of heat transfer effect.Current, the steam trap on market is arranged on the discharge end of heat-exchange system more, and reason is the afterflow problem that user cannot solve water lift water pump.If be that is contained in well head, the submersible pump of water lift is directly supplied to machine room and just cannot realizes, and can only increase secondary pressurized systems pumps again, namely increase running cost, be not thus used.Steam separator is arranged on the discharge end of heat-exchange system, just causes the actual state that inflammable gas leaks at machine room, forms major safety risks, the work of interchanger that also made water vapor get involved, causes heat exchanger efficiency low.
Summary of the invention
The purpose of this utility model is exactly in view of the foregoing defects the prior art has, provides a kind of geothermal deep well well head vertical gas-liquid two-phase gravitational separator.
Its technical scheme is: comprise tank body, liquid-inlet pipe, initial separator, escape pipe, blow-off pipe, liquid level display, safety valve, fluid level controller, tensimeter, pressure transmitter, control valve, pressure controlled valve, drain pipe, the rare solution device of steam, eddy flow wing plate, horizontal baffle, the side of tank body is provided with liquid-inlet pipe, and the opposite side of tank body is provided with drain pipe, and the top of tank body is provided with escape pipe, and the bottom of tank body connects blow-off pipe, and the inside of tank body is divided into disengagement chamber, liquid collecting cavity, air collecting chamber, tank body is provided with liquid level display and safety valve, liquid level display connecting fluid level controller, the top of tank body is provided with tensimeter, tensimeter Bonding pressure sensor, one end of described fluid level controller connects drain pipe by control valve, one end Bonding pressure sensor of fluid level controller, described escape pipe is provided with pressure controlled valve, described liquid-inlet pipe connects the rare solution device of steam of disengagement chamber inside by initial separator, the bottom of the rare solution device of steam is provided with eddy flow wing plate, and the bottom of liquid collecting cavity is provided with horizontal baffle.
The rare solution device of above-mentioned steam is pyramidal structure, and the inside of the rare solution device of steam is provided with three grades of ladders.
Above-mentioned air collecting chamber is provided with collection mist plate.
Above-mentioned initial separator comprises import, outlet, spiral flow deflector, thrust-augmenting nozzle, and thrust-augmenting nozzle two ends are provided with import and outlet, and the import of thrust-augmenting nozzle and outlet are tangential inlet structure, and the inside of thrust-augmenting nozzle is provided with spiral flow deflector.
The beneficial effects of the utility model are: this equipment have utilize submersible pump do work be supplied to heat-exchange equipment, voltage stabilizing afterflow, the disposable separation of steam except effect of the medium sand class particle that anhydrates, property safe and reliable to operation, its cost is low, and floor space is little, is easy to remove dirt in cylindrical shell, be convenient to realize blowdown and liquid automatic control, be suitable for processing the air containing fluid compared with large discharge.
Accompanying drawing explanation
Accompanying drawing 1 is structural representation of the present utility model;
Accompanying drawing 2 is structural representations of initial separator;
In upper figure: the rare solution device 14 of tank body 1, liquid-inlet pipe 2, initial separator 3, escape pipe 4, blow-off pipe 5, liquid level display 6, safety valve 7, fluid level controller 8, tensimeter 9, pressure transmitter 10, control valve 11, pressure controlled valve 12, drain pipe 13, steam, eddy flow wing plate 15, horizontal baffle 16, collection mist plate 17; Disengagement chamber 1.1, liquid collecting cavity 1.2, air collecting chamber 1.3, import 3.1, outlet 3.2, spiral flow deflector 3.3, thrust-augmenting nozzle 3.4.
Embodiment
1-2 by reference to the accompanying drawings, the utility model will be further described:
The utility model comprises tank body 1, liquid-inlet pipe 2, initial separator 3, escape pipe 4, blow-off pipe 5, liquid level display 6, safety valve 7, fluid level controller 8, tensimeter 9, pressure transmitter 10, control valve 11, pressure controlled valve 12, drain pipe 13, the rare solution device 14 of steam, eddy flow wing plate 15, horizontal baffle 16, the side of tank body 1 is provided with liquid-inlet pipe 2, and the opposite side of tank body 1 is provided with drain pipe 13, and the top of tank body 1 is provided with escape pipe 4, and the bottom of tank body 1 connects blow-off pipe 5, and the inside of tank body 1 is divided into disengagement chamber 1.1, liquid collecting cavity 1.2, air collecting chamber 1.3, tank body 1 is provided with liquid level display 6 and safety valve 7, liquid level display 6 connecting fluid level controller 8, the top of tank body 1 is provided with tensimeter 9, tensimeter 9 Bonding pressure sensor 10, one end of described fluid level controller 8 connects drain pipe 13 by control valve 11, one end Bonding pressure sensor 10 of fluid level controller 8, described escape pipe 4 is provided with pressure controlled valve 12, described liquid-inlet pipe 2 connects the rare solution device 14 of steam of disengagement chamber 1.1 inside by initial separator 3, the bottom of the rare solution device 14 of steam is provided with eddy flow wing plate 15, and the bottom of liquid collecting cavity 1.2 is provided with horizontal baffle 16, cylinder internal gas pressure value monitored by pressure transmitter 10, when cylindrical shell internal gas pressure reaches certain value and liquid level reaches certain value, pressure controlled valve 12 is opened and is discharged air-flow, and adjust the control valve at the mouth of a river, when being less than set(ting)value, the control valve of pressure controlled valve 12 and drain pipe 13 stops action, and gas-liquid separation proceeds Circulation, horizontal baffle 16 produces gas swirl in order to prevent during discharge opeing, and in leakage fluid dram, side arranges horizontal baffle 16 barrier gas vortex.
Wherein, the rare solution device 14 of steam is pyramidal structure, and the inside of the rare solution device 14 of steam is provided with three grades of ladders.
Wherein, air collecting chamber 1.3 is provided with collection mist plate 17, before near gas flow outlet, for trapping the comparatively small droplets (10 ~ 100 μm) that settling section fails to separate, fine droplet collides at this, condense, and is finally combined into larger drop and sinks down into liquid collecting cavity 1.2.
In addition, initial separator 3 comprises import 3.1, outlet 3.2, spiral flow deflector 3.3, thrust-augmenting nozzle 3.4, thrust-augmenting nozzle 3.4 two ends are provided with import 3.1 and outlet 3.2, import 3.1 and the outlet 3.2 of thrust-augmenting nozzle 3.4 are tangential inlet structure, the inside of thrust-augmenting nozzle 3.4 is provided with spiral flow deflector 3.3, and the current tangent line gangway mode of thrust-augmenting nozzle can improve the effect of primary separation.
Principle of work: be injected in after the hot water that the submersible pump in geothermal well extracts enters tank body by water-in on steam rare solution device and realize being separated step by step by the pyramidal structure of the rare solution device 14 of steam and three grades of ladders, makes steam nature sharp separation.By Liquid level, the volume of tank body 1 air collecting chamber 1.3 is remained unchanged in tank, namely accomplish the space invariance that aqueous vapor is separated, make equipment be in the working order of carbonated drink separation all the time.Gaseous emission uses normally closed two-way electronic valve to control, and setting pressure table, safety valve, make equipment work pressure and system working pressure equalization.For in the tank body of guarantee gas-water separation, spatial stability is constant, equipment is provided with fluid level controller 8, and is provided with liquid level display 6.When liquid level is critical, liquid level display 6 can intuitively show, and fluid level controller 8 works, and drain pipe 13 sluices simultaneously.The sand class particle contained in water after the rare solution of steam directly sinks to tank body 1 bottom discharge along eddy flow wing plate 15, and the water after steam separation, desanding is supplied to heat exchange machine room by water outlet.
Claims (4)
1. the vertical gas-liquid two-phase gravitational separator of geothermal deep well well head, is characterized in that: comprise tank body (1), liquid-inlet pipe (2), initial separator (3), escape pipe (4), blow-off pipe (5), liquid level display (6), safety valve (7), fluid level controller (8), tensimeter (9), pressure transmitter (10), control valve (11), pressure controlled valve (12), drain pipe (13), the rare solution device (14) of steam, eddy flow wing plate (15), horizontal baffle (16), the side of tank body (1) is provided with liquid-inlet pipe (2), and the opposite side of tank body (1) is provided with drain pipe (13), and the top of tank body (1) is provided with escape pipe (4), the bottom of tank body (1) connects blow-off pipe (5), and the inside of tank body (1) is divided into disengagement chamber (1.1), liquid collecting cavity (1.2), air collecting chamber (1.3), tank body (1) is provided with liquid level display (6) and safety valve (7), liquid level display (6) connecting fluid level controller (8), the top of tank body (1) is provided with tensimeter (9), tensimeter (9) Bonding pressure sensor (10), one end of described fluid level controller (8) connects drain pipe (13) by control valve (11), one end Bonding pressure sensor (10) of fluid level controller (8), described escape pipe (4) is provided with pressure controlled valve (12), described liquid-inlet pipe (2) connects the inner rare solution device (14) of steam of disengagement chamber (1.1) by initial separator (3), the bottom of the rare solution device (14) of steam is provided with eddy flow wing plate (15), and the bottom of liquid collecting cavity (1.2) is provided with horizontal baffle (16).
2. the vertical gas-liquid two-phase gravitational separator of geothermal deep well well head according to claim 1, is characterized in that: the rare solution device (14) of described steam is pyramidal structure, and the inside of the rare solution device (14) of steam is provided with three grades of ladders.
3. the vertical gas-liquid two-phase gravitational separator of geothermal deep well well head according to claim 1, is characterized in that: described air collecting chamber (1.3) is provided with collection mist plate (17).
4. the vertical gas-liquid two-phase gravitational separator of geothermal deep well well head according to claim 1, it is characterized in that: described initial separator (3) comprises import (3.1), outlet (3.2), spiral flow deflector (3.3), thrust-augmenting nozzle (3.4), thrust-augmenting nozzle (3.4) two ends are provided with import (3.1) and outlet (3.2), import (3.1) and the outlet (3.2) of thrust-augmenting nozzle (3.4) are tangential inlet structure, and the inside of thrust-augmenting nozzle (3.4) is provided with spiral flow deflector (3.3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520123254.2U CN204490671U (en) | 2015-03-03 | 2015-03-03 | The vertical gas-liquid two-phase gravitational separator of geothermal deep well well head |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520123254.2U CN204490671U (en) | 2015-03-03 | 2015-03-03 | The vertical gas-liquid two-phase gravitational separator of geothermal deep well well head |
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| Publication Number | Publication Date |
|---|---|
| CN204490671U true CN204490671U (en) | 2015-07-22 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520123254.2U Active CN204490671U (en) | 2015-03-03 | 2015-03-03 | The vertical gas-liquid two-phase gravitational separator of geothermal deep well well head |
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| CN (1) | CN204490671U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106178882A (en) * | 2016-09-09 | 2016-12-07 | 成都九十度工业产品设计有限公司 | Ozone and the liquid collector of waste gas mixing reactor |
-
2015
- 2015-03-03 CN CN201520123254.2U patent/CN204490671U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106178882A (en) * | 2016-09-09 | 2016-12-07 | 成都九十度工业产品设计有限公司 | Ozone and the liquid collector of waste gas mixing reactor |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170613 Address after: 257100, north of the Yellow River Road, Dongying District, Shandong City, Dongying Province, west of route five Patentee after: DONGYING MINGHUI NEW ENERGY TECHNOLOGY Co.,Ltd. Address before: 257000, A, Vientiane square, Tianmu Mountain Road, Dongying District, Dongying, Shandong Patentee before: SHANDONG MING MING GEOTHERMAL ENERGY DEVELOPMENT CO.,LTD. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20231108 Address after: 257000 Dongying Technology Enterprise Accelerator E2-4-076, north of Huanghe Road and west of Guihua Fifth Road, Dongying District, Dongying City, Shandong Province Patentee after: Shandong Mingbang Power Technology Co.,Ltd. Address before: 257100 north of Huanghe Road and west of Guihua fifth road, Dongying District, Dongying City, Shandong Province Patentee before: DONGYING MINGHUI NEW ENERGY TECHNOLOGY Co.,Ltd. |
|
| 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: Vertical gas-liquid two-phase gravity separator for geothermal deep well wellhead Effective date of registration: 20231117 Granted publication date: 20150722 Pledgee: Dongying laishang village bank Limited by Share Ltd. Development Zone sub branch Pledgor: Shandong Mingbang Power Technology Co.,Ltd. Registration number: Y2023980066261 |