CN107265542A - A kind of water route gas fractionation unit and method - Google Patents

A kind of water route gas fractionation unit and method Download PDF

Info

Publication number
CN107265542A
CN107265542A CN201710713179.9A CN201710713179A CN107265542A CN 107265542 A CN107265542 A CN 107265542A CN 201710713179 A CN201710713179 A CN 201710713179A CN 107265542 A CN107265542 A CN 107265542A
Authority
CN
China
Prior art keywords
grades
water route
water
degassing stages
reducing pipe
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201710713179.9A
Other languages
Chinese (zh)
Other versions
CN107265542B (en
Inventor
郝拴菊
郝立辉
菅晓亮
董叔跃
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hebei Createc Instrument Science & Technology Co Ltd
Original Assignee
Hebei Createc Instrument Science & Technology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hebei Createc Instrument Science & Technology Co Ltd filed Critical Hebei Createc Instrument Science & Technology Co Ltd
Priority to CN201710713179.9A priority Critical patent/CN107265542B/en
Publication of CN107265542A publication Critical patent/CN107265542A/en
Application granted granted Critical
Publication of CN107265542B publication Critical patent/CN107265542B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/20Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N33/00Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
    • G01N33/18Water
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/002Construction details of the apparatus
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00General aspects of water treatment
    • C02F2301/06Pressure conditions
    • C02F2301/063Underpressure, vacuum
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00General aspects of water treatment
    • C02F2301/08Multistage treatments, e.g. repetition of the same process step under different conditions
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/20Controlling water pollution; Waste water treatment

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Biochemistry (AREA)
  • Immunology (AREA)
  • Physics & Mathematics (AREA)
  • Analytical Chemistry (AREA)
  • Food Science & Technology (AREA)
  • General Health & Medical Sciences (AREA)
  • General Physics & Mathematics (AREA)
  • Medicinal Chemistry (AREA)
  • Pathology (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Degasification And Air Bubble Elimination (AREA)

Abstract

The present invention relates to a kind of water route gas fractionation unit, it is communicated on online conveying water route, including the inlet pipeline being connected with the online conveying water route, and simultaneously road is communicated in one-level degassing stages and negative inspiratory pressure mechanism on the inlet pipeline, one-level degassing stages degasification using pipeline reducing injection water;Also include two grades of degassing stages being communicated in the one-level degassing stages downstream, being deaerated using acceleration of gravity, two grades of degassing stages ends offer the outlet pipeline being connected with water quality detecting device, the gas that the negative inspiratory pressure mechanism deviates to two grades of degassing stages carries out negative-pressure adsorption and inputted to the online conveying water route, and the one-level degassing stages are connected with the inter-agency sealing respectively of intersegmental, the described two grades of degassing stages of two grades of degassings and the negative-pressure adsorption.The water route gas fractionation unit of the present invention, by multistage degassing, by the bubble removal in liquid to be detected, and with preferable using effect.

Description

A kind of water route gas fractionation unit and method
Technical field
The present invention relates to liquid-gas separation device technical field in online water route, more particularly to a kind of water route gas separation dress Put.The invention further relates to a kind of method of application water route gas fractionation unit.
Background technology
Water quality monitoring is monitoring and the species, the concentration and variation tendency of each pollutant that determine pollutant in water body, is commented The process of valency water quality condition, its monitoring range is quite varied, including be not contaminated and contaminated natural water (river, river, lake, Sea and underground water) and various industrial water drainages etc., and during online water quality measurement, liquid to be detected can be deposited after circulating by the road There are a large amount of small bubbles, or liquid generally existing itself has a large amount of small bubbles, the presence of its bubble has a strong impact on water The precision of matter measurement.
The content of the invention
For above description, it is an object of the invention to provide a kind of water route gas fractionation unit and method, it is through excessive Level degassing, by the bubble removal in liquid to be detected, and with preferable using effect.
The technical scheme is that be accomplished by the following way:
A kind of water route gas fractionation unit, is communicated on online conveying water route, including be connected with the online conveying water route Logical inlet pipeline, and simultaneously road is communicated in one-level degassing stages and negative inspiratory pressure mechanism on the inlet pipeline, the one-level Degassing stages degasification using pipeline reducing injection water;Also include being communicated in the one-level degassing stages downstream, added using gravity Two grades of degassing stages of speed degassing, two grades of degassing stages ends offer the outlet pipeline being connected with water quality detecting device, The gas that the negative inspiratory pressure mechanism deviates to two grades of degassing stages carries out negative-pressure adsorption and inputted to the online conveying water Lu Shang, the one-level degassing stages and intersegmental, the described two grades of degassing stages of two grades of degassings and the inter-agency difference of the negative-pressure adsorption Sealing connection.
As restriction, the one-level degassing stages include the straight tube that is connected with the inlet pipeline, and with the straight tube The reducing pipe being connected.
As further restriction, the reducing pipe is tapered to be set, and the reducing pipe has relative to the straight tube The angle raised up.
As further limiting, relative to the straight tube, the closing in angle of the reducing pipe is 15 °~30 °.
As further restriction, the seal groove for the current that two grades of degassing stages eject for the undertaking reducing pipe, The seal groove has by the end connectivity part with the reducing pipe to opening up the gradient that outlet pipeline has a down dip.
As further limiting, the gradient that the seal groove has a down dip is 5 °~20 °.
As further limiting, the negative inspiratory pressure mechanism includes simultaneously being communicated in the water inlet pipe in road with the straight tube On road, L-shaped distribution pipeline, and the small reducing pipe connected with the end of the distribution pipeline;It is also described including being communicated in The extension pipeline of small undergauge pipe end, and be communicated in it is described extension line end logical straight tube, the small reducing pipe with it is described The tapered setting of pipeline is extended, and the end of the small reducing pipe and the head end of the extension pipeline enclose composition trunnion, in institute State the suction line for being communicated with and being connected with the seal groove at trunnion, the suction line is connected one with the seal groove End is positioned at the water surface upper strata of the seal groove.
The advantage of the invention is that:
A kind of water route gas fractionation unit of the present invention, by setting one-level degassing stages, the one-level degassing stages profit The degasification with pipeline reducing injection water, by setting two grades of degassing stages, using liquid and bubble density and acceleration of gravity not Together, two grades of degassings are carried out, by setting negative inspiratory pressure mechanism, negative-pressure adsorption can be carried out to the gas of two grades of degassing stages abjections, And three-level degassing is carried out, by above-mentioned multistage degassing, and make degasifying effect good, to lift the precision of water quality monitoring.
Another object of the present invention is to propose a kind of water route gas separating method.
To reach above-mentioned purpose, the technical proposal of the invention is realized in this way:
A kind of water route gas separating method, using water route gas fractionation unit as described above, it comprises the following steps:
A, the water entered via inlet pipeline, flow into reducing pipe from straight tube all the way, enter using from reducing pipe injection water Row one-level deaerates;
B, two grades of degassing stages accept the current ejected in a steps from reducing pipe, in the presence of acceleration of gravity, water Falling speed is fast compared with bubble, carries out two grades of degassings;
C, the water entered via inlet pipeline, negative pressure is flowed into flowing into straight tube another road that simultaneously road is connected all the way in a steps Suction mechanism, negative inspiratory pressure mechanism carries out negative-pressure adsorption to the gas on the water surface upper strata of two grades of degassing stages in b step and bubble, and Carry out three-level degassing.
What the water route gas separating method of the present invention had with above-mentioned water route gas fractionation unit relative to prior art Dominant Facies are same, will not be repeated here.
Brief description of the drawings
Fig. 1 is a kind of structural representation of water route gas fractionation unit described in the embodiment of the present invention one.
Wherein:1- inlet pipelines, 2- one-level degassing stages, 21- straight tubes, 22- reducing pipes, 3- negative inspiratory pressures mechanism, 31- points Flow tube road, the small reducing pipes of 32-, 33- extension pipelines, 34- leads to straight tube, 35- trunnions, 36- suction lines, bis- grades of degassing stages of 4-, 41- Outlet pipeline, 42- seal grooves.
Embodiment
In the description of the invention, it is necessary to explanation, the orientation or position of the instruction such as term " on ", " under ", " interior ", " back of the body " It is, based on orientation shown in the drawings or position relationship, to be for only for ease of the description present invention and simplify description to put relation, rather than Indicate or imply that the device or element of meaning there must be specific orientation, with specific azimuth configuration and operation, therefore can not It is interpreted as limitation of the present invention.In addition, term " first ", " second " be only used for describe purpose, and it is not intended that indicate or Imply relative importance.Describe the present invention in detail below with reference to the accompanying drawings and in conjunction with the embodiments.
Embodiment one
The present embodiment is related to a kind of water route gas fractionation unit, is communicated on online conveying water route, as shown in fig. 1, its Including the inlet pipeline 1 being connected with online conveying water route, and simultaneously road is communicated in the He of one-level degassing stages 2 on inlet pipeline 1 In negative inspiratory pressure mechanism 3, the present embodiment, one-level degassing stages 2 are using reducing injection water and degasification, in addition to are communicated in one-level and take off 2 downstreams of gas section, two grades of degassing stages 4 being deaerated using acceleration of gravity, two grades of ends of degassing stages 4 are offered and water quality detection The outlet pipeline 41 that device is connected, the gas that two grades of degassing stages 4 of negative inspiratory pressure mechanism 3 pair are deviate from carries out negative-pressure adsorption and defeated Enter to online conveying water route, between one-level degassing stages 2 and two grades of degassing stages 4, two grades of degassing stages 4 and the inter-agency difference of negative-pressure adsorption Sealing connection.
By setting one-level degassing stages 2, one-level degassing is carried out using reducing injection water, by setting two grades of degassing stages 4, it is different with bubble density and acceleration of gravity using liquid, and two grades of degassings are carried out, and suction mechanism is pressed by negative set, can be right The gas that two grades of degassing stages 4 are deviate from carries out negative-pressure adsorption, carries out three-level degassing, by multistage degassing, and makes degasifying effect good, with Lift the precision of water quality monitoring.
In the present embodiment, one-level degassing stages 2 include the straight tube 21 being connected with inlet pipeline 1, and are connected with straight tube 21 Logical reducing pipe 22, specifically, being provided with water pump in inlet pipeline 1, the high-pressure water pump in online conveying water route is entered into water In pipeline 1, the present embodiment, straight tube 21 is set perpendicular to inlet pipeline 1, and straight tube 21 is attached in order to the water baffling in current On, and carry out primary degassing.The diameter of straight tube 21 is less than the diameter of inlet pipeline 1, and makes current secondary pressurized, and preferably makes current It is spouting, meanwhile, reducing pipe 22 is tapered to be set, and reducing pipe 22 has the angle raised up relative to straight tube 21, in order to Current are spouting via reducing pipe 22, and carry out one-level degassing, meanwhile, reducing pipe 22 has the angle raised up relative to straight tube 21 Degree, can extend the time that current fall into following seal grooves 42, in the present embodiment, and reducing pipe 22 is connected the pipe of one end with straight tube 21 Footpath is slightly less than the diameter of straight tube 21, in order to be connected with the sealing of straight tube 21, to make pressure effect good, relative to straight tube 21, reducing pipe 22 closing in angle is 15 °~30 °, it is preferred that closing in angle is 15 °~25 °.
In the present embodiment, two grades of degassing stages 4 is accept the seal groove 42 for the current that reducing pipe 22 is ejected, by reducing pipe 22 The current ejected have the angle raised up because of reducing pipe 22, and make water flow jet in the top of seal groove 42, because of water and bubble Density it is different with acceleration of gravity, water is quickly fallen compared with bubble, and carry out two grades degassing, for make two grades of degasifying effects more preferably, Seal groove 42 has by the end connectivity part with reducing pipe 22 to the gradient that outlet pipeline 41 has a down dip is opened up, so that liquid adheres to In on the bottom wall of seal groove 42, and moisture film is formed, to make effect more preferably, the gradient that seal groove 42 has a down dip is 5 °~20 °, it is preferred that The gradient that seal groove 42 has a down dip is 15 °.
In the present embodiment, negative inspiratory pressure mechanism 3 is including simultaneously road is communicated in dividing on inlet pipeline 1, L-shaped with straight tube 21 Flow tube road 31, and the small reducing pipe 32 connected with the end of distribution pipeline 31;Also include being communicated in the small end of reducing pipe 32 Pipeline 33 is extended, and is communicated in the logical straight tube 34 of extension pipeline 33 end, small reducing pipe 32 and extension pipeline 33 are tapered Set, and the end of small reducing pipe 32 and the head end of extension pipeline 33 enclose composition trunnion 35, are communicated with and seal at trunnion 35 The suction line 36 that groove 42 is connected, one end that is connected with seal groove 42 of suction line 36 is located on the water surface of seal groove 42 Layer.In the present embodiment, distribution pipeline 31 is vertically arranged with straight tube 21, the diameter of distribution pipeline 31 and the diameter phase of inlet pipeline 1 Together, the end diameter of small reducing pipe 32 is less than the head end diameter of extension pipeline 33, because injection water speed is very high, then, larynx The surrounding of pipe 311 formation negative pressure makes generation vacuum, and suction line 32 is adsorbed the bubble of the top of seal groove 42, realizes three Level degassing.
The present embodiment, by multistage degassing, by the bubble removal in liquid to be detected, and with preferable using effect.
Embodiment two
The present embodiment is related to a kind of water route gas separating method, the water route gas separation dress in its application such as embodiment one Put, it comprises the following steps:
A, the water entered via inlet pipeline 1, flow into reducing pipe 22 from straight tube 21 all the way, using from the injection water of reducing pipe 22 Stream carries out one-level degassing;
B, two grades of degassing stages 4 accept the current ejected in a steps from reducing pipe 22, and under acceleration of gravity effect, The falling speed of water is fast compared with bubble, carries out two grades of degassings;
C, the water entered via inlet pipeline 1, another road connected with flowing into the tunnel of straight tube 21 1 and road in a steps flow into negative Suction mechanism 3 is pressed, negative inspiratory pressure mechanism 3 carries out negative pressure suction to the bubble on the water surface upper strata of two grades of degassing stages 4 in b step and gas It is attached, and carry out three-level degassing.
In the present embodiment, water is flowed into seal groove 42 under acceleration of gravity effect, can caused after reducing pipe 22 sprays Water forms water film in seal groove, and makes separating effect more preferable.
Better embodiment of the present invention is the foregoing is only, but protection scope of the present invention is not limited thereto, it is any ripe Know those skilled in the art the invention discloses technical scope in, the technique according to the invention design be subject to equivalent substitution or Technical scheme obtained by change, should all be covered by protection scope of the present invention.

Claims (8)

1. a kind of water route gas fractionation unit, is communicated on online conveying water route, it is characterised in that:Including with the online conveying The inlet pipeline that water route is connected, and simultaneously road is communicated in one-level degassing stages and negative inspiratory pressure mechanism on the inlet pipeline, One-level degassing stages degasification using pipeline reducing injection water;Also include being communicated in the one-level degassing stages downstream, profit The two grades of degassing stages deaerated with acceleration of gravity, two grades of degassing stages ends offer going out of being connected with water quality detecting device Water lines, gas that the negative inspiratory pressure mechanism deviates to two grades of degassing stages carry out negative-pressure adsorption and input to it is described On line conveying water route, the one-level degassing stages and intersegmental, the described two grades of degassing stages of two grades of degassings and the negative-pressure adsorption machine Sealing connection respectively between structure.
2. a kind of water route gas fractionation unit according to claim 1, it is characterised in that:The one-level degassing stages include with The straight tube that the inlet pipeline is connected, and the reducing pipe being connected with the straight tube.
3. a kind of water route gas fractionation unit according to claim 2, it is characterised in that:The reducing pipe is tapered to be set Put, and the reducing pipe has the angle raised up relative to the straight tube.
4. a kind of water route gas fractionation unit according to claim 3, it is characterised in that:It is described relative to the straight tube The closing in angle of reducing pipe is 15 °~30 °.
5. a kind of water route gas fractionation unit according to any one of claim 2 to 4, it is characterised in that:Described two grades Degassing stages is accept the seal groove for the current that the reducing pipe is ejected, and the seal groove has by the end with the reducing pipe Connectivity part is to opening up the gradient that is had a down dip at outlet pipeline.
6. a kind of water route gas fractionation unit according to claim 5, it is characterised in that:The gradient that the seal groove has a down dip For 5 °~20 °.
7. a kind of water route gas fractionation unit according to claim 5, it is characterised in that:The negative inspiratory pressure mechanism includes The distribution pipeline of on the inlet pipeline, L-shaped is communicated in the straight tube and road, and is connected with the end of the distribution pipeline Logical small reducing pipe;Also include the extension pipeline for being communicated in the small undergauge pipe end, and be communicated in the extension pipeline end End logical straight tube, the small reducing pipe with it is described extension pipeline it is tapered set, and the end of the small reducing pipe with it is described The head end of extension pipeline encloses composition trunnion, and the suction line being connected with the seal groove is communicated with the trunnion, described The one end that is connected with the seal groove of suction line is located at the water surface upper strata of the seal groove.
8. a kind of water route gas separating method, it is characterised in that water route gas of the application as any one of claim 2 to 7 Body separator, comprises the following steps:
A, the water entered via inlet pipeline, flow into reducing pipe from straight tube all the way, one are carried out using from reducing pipe injection water Level degassing;
B, two grades of degassing stages accept the current ejected in a steps from reducing pipe, in the presence of acceleration of gravity, the whereabouts of water Speed is fast compared with bubble, carries out two grades of degassings;
C, the water entered via inlet pipeline, negative inspiratory pressure is flowed into flowing into straight tube another road that simultaneously road is connected all the way in a steps Mechanism, negative inspiratory pressure mechanism carries out negative-pressure adsorption to the gas on the water surface upper strata of two grades of degassing stages in b step and bubble, and carries out Three-level deaerates.
CN201710713179.9A 2017-08-18 2017-08-18 Waterway gas separation device and method Active CN107265542B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710713179.9A CN107265542B (en) 2017-08-18 2017-08-18 Waterway gas separation device and method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710713179.9A CN107265542B (en) 2017-08-18 2017-08-18 Waterway gas separation device and method

Publications (2)

Publication Number Publication Date
CN107265542A true CN107265542A (en) 2017-10-20
CN107265542B CN107265542B (en) 2023-02-03

Family

ID=60080505

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710713179.9A Active CN107265542B (en) 2017-08-18 2017-08-18 Waterway gas separation device and method

Country Status (1)

Country Link
CN (1) CN107265542B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108543640A (en) * 2018-04-02 2018-09-18 深圳市华星光电技术有限公司 A kind of liquid discharge device

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN85103948A (en) * 1984-05-24 1987-01-14 螺旋体研究有限公司 Reduce the method and apparatus of gas content in the liquid
JP2003080243A (en) * 2001-09-14 2003-03-18 Sanikon:Kk Method and apparatus for removing suspension
TW201200222A (en) * 2005-06-21 2012-01-01 Kaijo Kk Deaeration device and ultrasonic cleaning device using the same
CN203187429U (en) * 2013-02-04 2013-09-11 北京欧力凯科技发展有限责任公司 Vacuum degassing and deaerating plant with spray head
CN103877752A (en) * 2014-04-08 2014-06-25 华东理工大学 Online degassing method and device of pipeline fluid
CN203841088U (en) * 2014-05-04 2014-09-24 石家庄市田牛牧业有限公司 Saturated steam water removal system
CN105194910A (en) * 2015-10-26 2015-12-30 杭州鼎流科技有限公司 Liquid degassing conveying system
CN106861244A (en) * 2017-04-20 2017-06-20 苏州市海崴生物科技有限公司 A kind of gas-liquid separation and the bubble trap of steady rate of flow of fluid
CN207192855U (en) * 2017-08-18 2018-04-06 河北科瑞达仪器科技股份有限公司 A kind of water route gas fractionation unit

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN85103948A (en) * 1984-05-24 1987-01-14 螺旋体研究有限公司 Reduce the method and apparatus of gas content in the liquid
JP2003080243A (en) * 2001-09-14 2003-03-18 Sanikon:Kk Method and apparatus for removing suspension
TW201200222A (en) * 2005-06-21 2012-01-01 Kaijo Kk Deaeration device and ultrasonic cleaning device using the same
CN203187429U (en) * 2013-02-04 2013-09-11 北京欧力凯科技发展有限责任公司 Vacuum degassing and deaerating plant with spray head
CN103877752A (en) * 2014-04-08 2014-06-25 华东理工大学 Online degassing method and device of pipeline fluid
CN203841088U (en) * 2014-05-04 2014-09-24 石家庄市田牛牧业有限公司 Saturated steam water removal system
CN105194910A (en) * 2015-10-26 2015-12-30 杭州鼎流科技有限公司 Liquid degassing conveying system
CN106861244A (en) * 2017-04-20 2017-06-20 苏州市海崴生物科技有限公司 A kind of gas-liquid separation and the bubble trap of steady rate of flow of fluid
CN207192855U (en) * 2017-08-18 2018-04-06 河北科瑞达仪器科技股份有限公司 A kind of water route gas fractionation unit

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108543640A (en) * 2018-04-02 2018-09-18 深圳市华星光电技术有限公司 A kind of liquid discharge device
CN108543640B (en) * 2018-04-02 2020-07-03 深圳市华星光电技术有限公司 Liquid discharge device

Also Published As

Publication number Publication date
CN107265542B (en) 2023-02-03

Similar Documents

Publication Publication Date Title
US9844742B2 (en) Device for liquid degassing
CN101810941B (en) Compound oil-water separation system
JP5258560B2 (en) Integrated deaeration and deaerator
CN103877752B (en) A kind of online degas method of pipeline fluid and device
BR112016019671B1 (en) Submarine multiphase separation system and method for separating oil, water, and solid particles in a multiphase fluid
US7179386B2 (en) Discharging sand from a vessel at elevated pressure
CN102168549B (en) Device and method for measuring output liquid of coal bed methane well
CN103045295B (en) Water removing system for gas-water-containing crude oil and application method of system
CN107265542A (en) A kind of water route gas fractionation unit and method
CN207192855U (en) A kind of water route gas fractionation unit
CN102225221B (en) Degassing device used for hemodialysis equipment
CN219646773U (en) Defoaming equipment for shale gas
US8075770B2 (en) Flotation device
CN208933283U (en) A kind of on-demand automatic filling crude oil removes scale preventative device
CN106433764A (en) Short-process water pre-separation apparatus for oilfield produced fluid
CN206740713U (en) A kind of exhaust apparatus liquid chromatograph
CN202154892U (en) Air removing device for haemodialysis equipment
CN101979118B (en) Multi-branch oil-gas-liquid phase separator
CN105784020A (en) Rectangular needle tube flowmeter
CN201823433U (en) Multiple-branch-pipe gas-liquid phase separator
CN206111115U (en) Coiled tubing underbalance sand washing device
CN210814053U (en) Bubble removing device buffer tank
CN209244787U (en) A kind of natural gas defoaming coalescing devices
CN204699428U (en) A kind of practical packed tower
CN205503416U (en) Pneumatic diaphragm pump of journey is inhaled to height

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant