CN106731024B - A kind of device of gas in removal liquid - Google Patents
A kind of device of gas in removal liquid Download PDFInfo
- Publication number
- CN106731024B CN106731024B CN201611198015.9A CN201611198015A CN106731024B CN 106731024 B CN106731024 B CN 106731024B CN 201611198015 A CN201611198015 A CN 201611198015A CN 106731024 B CN106731024 B CN 106731024B
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- Prior art keywords
- storage device
- cylinder
- medium storage
- medium
- gas
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/0042—Degasification of liquids modifying the liquid flow
- B01D19/0052—Degasification of liquids modifying the liquid flow in rotating vessels, vessels containing movable parts or in which centrifugal movement is caused
Abstract
The invention discloses a kind of devices of the gas in removal liquid, include at least: medium storage device, pipeline and extractor fan；The inlet end of the extractor fan is penetrated through by the first port of the pipeline and the medium storage device and is connected；The inlet end of the extractor fan is located at the top of the first port of the medium storage device.The present invention makes gas-liquid separation by pressure difference to generate pressure difference by extractor fan exhausting from the pipeline for be connected to medium storage device.Specifically, under same pressure difference, the upward resultant force as suffered by gas is larger, and the density and viscosity ratio liquid of gas are small, therefore it moves upwards very fast, it is thus possible to be separated from liquid, to improve the measurement accuracy of flow and the computational accuracy of separative efficiency.
Description
Technical field
The present invention relates to a kind of devices of the gas in the technical field of separator more particularly to removal liquid.
Background technique
Promote inevitably to be doped into one in solid-liquor separation experiment carrying out solid-liquor separation, Liquid liquid Separation and aerating
Quantitative gas, this can be affected to the flow for exporting liquid after measurement separation, to influence the calculating of separative efficiency.Cause
This, the gas adulterated in liquid after removal separation has the computational accuracy of the measurement accuracy and separative efficiency that improve flow very big
Help, have very big directive significance for industrial applicability.
Summary of the invention
The present invention solves by providing a kind of device for removing the gas in liquid and not can be removed separation in the prior art
The technical issues of gas adulterated in liquid afterwards, realizes the skill of the computational accuracy of the measurement accuracy and separative efficiency that improve flow
Art effect.
The present invention provides a kind of devices of the gas in removal liquid, include at least: medium storage device, pipeline and pumping
Wind apparatus；The inlet end of the extractor fan is penetrated through by the first port of the pipeline and the medium storage device and is connected；
The inlet end of the extractor fan is located at the top of the first port of the medium storage device.
Further, the pipeline is vertically arranged.
Further, the first port of the medium storage device is to collapse structure.
Further, the extractor fan includes at least: blower and frequency conversion equipment；The air inlet of the pipeline and the blower
End perforation connection；The signal output end communication connection of the signal input part of the blower and the frequency conversion equipment.
Further, it also includes at least: cyclone separator；The medium output end of the cyclone separator is deposited with the medium
The medium input terminal of storage device penetrates through connection.
Further, the cyclone separator includes at least: swirl cylinder, cylinder, feed pipe, overflow pipe and with drainage trough
Cone；The lower part of the swirl cylinder is arranged in the cylinder；Through-hole is arranged at the lower part of the cylinder；Jie of the overflow pipe
Matter input terminal is passed through the top of the swirl cylinder；The medium output end and the medium of the medium storage device of the overflow pipe are defeated
Enter end perforation connection；The feed pipe is passed through the swirl cylinder with the direction tangent with the swirl cylinder；It is described with drainage trough
Cone is arranged in the swirl cylinder.
Further, the cyclone separator also includes at least: threaded rod；The first end of the threaded rod is fixed on described
On overflow pipe, the second end of the threaded rod is connected through a screw thread with the cone.
Further, there is drainage trough in the inner wall of the swirl cylinder and/or the cylinder.
Further, there is wear-resistant ceramic layer in the inner wall of the swirl cylinder and/or the cylinder.
Further, it also includes at least: flowmeter；The medium output of the medium storage device is arranged in the flowmeter
End.
One or more technical solution provided in the present invention, has at least the following technical effects or advantages:
By extractor fan, exhausting is made to generate pressure difference by pressure difference from the pipeline for be connected to medium storage device
Gas-liquid separation.Specifically, under same pressure difference, the upward resultant force as suffered by gas is larger, and the density of gas
It is small with viscosity ratio liquid, therefore move upwards very fast, it is thus possible to it is separated from liquid, to improve the survey of flow
The computational accuracy of accuracy of measurement and separative efficiency.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the device of the gas in removal liquid provided in an embodiment of the present invention；
Wherein, 1- medium storage device, 2- pipeline, 3- peep hole, 4- blower, 5- frequency conversion equipment, 6- cyclone separator, 7-
Flowmeter.
Specific embodiment
By providing a kind of device for removing the gas in liquid, solving can not go the embodiment of the present invention in the prior art
The technical issues of except the gas adulterated in liquid after separation, realizes the calculating essence of the measurement accuracy and separative efficiency that improve flow
The technical effect of degree.
Technical solution in the embodiment of the present invention is in order to solve the above technical problems, general thought is as follows:
By extractor fan, exhausting is made to generate pressure difference by pressure difference from the pipeline for be connected to medium storage device
Gas-liquid separation.Specifically, under same pressure difference, the upward resultant force as suffered by gas is larger, and the density of gas
It is small with viscosity ratio liquid, therefore move upwards very fast, it is thus possible to it is separated from liquid, to improve the survey of flow
The computational accuracy of accuracy of measurement and separative efficiency.
Above-mentioned technical proposal in order to better understand, in conjunction with appended figures and specific embodiments to upper
Technical solution is stated to be described in detail.
Referring to Fig. 1, the device of the gas in removal liquid provided in an embodiment of the present invention is included at least: media storage dress
Set 1, pipeline 2 and extractor fan；The inlet end of extractor fan is penetrated through by the first port of pipeline 2 and medium storage device 1 to be connected
It connects；The inlet end of extractor fan is located at the top of the first port of medium storage device 1.
Wherein, the first port of pipeline 2 and medium storage device 1 passes through flanged joint.
Specifically, pipeline 2 is vertically arranged, i.e., the inlet end of extractor fan is located at the first port of medium storage device 1
Surface.
The structure of medium storage device 1 is illustrated, the first port of medium storage device 1 is to collapse structure.
The structure of extractor fan is illustrated, extractor fan includes at least: blower 4 and frequency conversion equipment 5；Pipeline 2 and wind
The inlet end of machine 4 penetrates through connection；The signal input part of blower 4 and the signal output end communication connection of frequency conversion equipment 5.
The structure of the embodiment of the present invention is illustrated, is also included at least: cyclone separator 6；The medium of cyclone separator 6
The medium input terminal of output end and medium storage device 1, which penetrates through, to be connected.
The structure of cyclone separator 6 is illustrated, cyclone separator 6 includes at least: swirl cylinder, cylinder, feed pipe,
Overflow pipe and cone with drainage trough；The lower part of swirl cylinder is arranged in cylinder；Through-hole is arranged at the lower part of cylinder；Jie of overflow pipe
Matter input terminal is passed through the top of swirl cylinder；The medium output end of overflow pipe and the medium input terminal of medium storage device 1 penetrate through and connect
It connects；Feed pipe is passed through swirl cylinder with the direction tangent with swirl cylinder；Cone with drainage trough is arranged in swirl cylinder.
In the present embodiment, the top of swirl cylinder and end cap are passed through into flanged joint；Overflow pipe is fixed in end cap
The heart, and it is passed through swirl cylinder.The middle part of swirl cylinder is arranged in feed pipe.
The structure of cyclone separator 6 is further described, cyclone separator 6 also includes at least: threaded rod；Threaded rod
First end be fixed on overflow pipe, second end and the cone of threaded rod are connected through a screw thread.
In the present embodiment, there is drainage trough in the inner wall of swirl cylinder and/or cylinder.
In order to extend the service life of cyclone separator 6, there is wear-resistant ceramic layer in the inner wall of swirl cylinder and/or cylinder.
In the present embodiment, swirl cylinder is cylindrical structure, and cylinder is conical structure, and the cone with drainage trough is circle
Cone, and the diameter of cone between diameter of the diameter to swirl cylinder of overflow pipe determines according to actual conditions.
The structure of the embodiment of the present invention is further described, is also included at least: flowmeter 7；The setting of flowmeter 7 is being situated between
The medium output end of matter storage device 1.
It is the working principle of the embodiment of the present invention below:
Gas-liquid mixture after separation reaches flow velocity after medium storage device 1 after the outlet of cyclone separator 6 outflow
Slow down, the revolving speed of blower 4 is adjusted by frequency conversion equipment 5, blower 4 is in certain revolving speed extraction conduit 2 and medium storage device 1
Gas form certain pressure difference.Since pressure acts on, liquids and gases are acted on by upward power and are moved upwards.When gas-liquid is mixed
Object is closed when rising to certain altitude, downward gravity and resistance and upward force balance and no longer move upwards.But gas
Body is since density and viscosity very little, upward active force are always more than its gravity and resistance, and therefore, gas can move all the way up
Finally excluded by blower 4.After reaching balance inside device, gas can ceaselessly be extracted always pipeline 2 and liquid not by shadow
It rings, to remove the gas in liquid, and then keeps the flowing of liquid more steady, the measured value of flowmeter 7 is more accurate.Here
It should be noted that the revolving speed of blower 4 can be adjusted by frequency conversion equipment 5 to control pressure difference, to control according to actual flow
Separate the speed of gas.
There is also the need to explanation, several transparent peep holes 3 can be designed, on pipeline 2 in order to control liquid
Face height.
[technical effect]
1, by extractor fan, exhausting to generate pressure difference passes through pressure from the pipeline 2 for be connected to medium storage device 1
Official post gas-liquid separation.Specifically, under same pressure difference, the upward resultant force as suffered by gas is larger, and gas
Density and viscosity ratio liquid are small, therefore move upwards very fast, it is thus possible to separate from liquid, to improve flow
Measurement accuracy and separative efficiency computational accuracy.
2, the first port of medium storage device 1 is to collapse structure, can slow down the flow velocity of liquid, to be more conducive to
The separation of gas.
3, it is adjusted by revolving speed of the frequency conversion equipment 5 to blower 4, so as to control pressure difference, and then controls gas point
From speed.
4, by the use to threaded rod, the adjustment of the position to the cone with drainage trough according to actual needs is realized,
To improve the separating effect of cyclone separator 6.
In addition, the embodiment of the present invention also has the advantages that structure is simply and easy to maintain.
Although preferred embodiments of the present invention have been described, it is created once a person skilled in the art knows basic
Property concept, then additional changes and modifications may be made to these embodiments.So it includes excellent that the following claims are intended to be interpreted as
It selects embodiment and falls into all change and modification of the scope of the invention.
Obviously, various changes and modifications can be made to the invention without departing from essence of the invention by those skilled in the art
Mind and range.In this way, if these modifications and changes of the present invention belongs to the range of the claims in the present invention and its equivalent technologies
Within, then the present invention is also intended to include these modifications and variations.
Claims (9)
1. a kind of device of the gas in removal liquid, which is characterized in that include at least: medium storage device, pipeline and exhausting
Device；The inlet end of the extractor fan is penetrated through by the first port of the pipeline and the medium storage device and is connected；Institute
State extractor fan inlet end be located at the medium storage device first port top；The first of the medium storage device
Port is to collapse structure, slows down the flow velocity of liquid.
2. device as described in claim 1, which is characterized in that the pipeline is vertically arranged.
3. device as described in claim 1, which is characterized in that the extractor fan includes at least: blower and frequency conversion equipment；Institute
The inlet end perforation for stating pipeline and the blower connects；The signal of the signal input part of the blower and the frequency conversion equipment exports
End communication connection.
4. device as described in claim 1, which is characterized in that also include at least: cyclone separator；The cyclone separator
The medium input terminal of medium output end and the medium storage device, which penetrates through, to be connected.
5. device as claimed in claim 4, which is characterized in that the cyclone separator includes at least: swirl cylinder, cylinder,
Feed pipe, overflow pipe and the cone with drainage trough；The lower part of the swirl cylinder is arranged in the cylinder；Under the cylinder
There is through-hole in portion；The medium input terminal of the overflow pipe is passed through the top of the swirl cylinder；The medium output end of the overflow pipe with
The medium input terminal of the medium storage device penetrates through connection；The feed pipe is passed through institute with the direction tangent with the swirl cylinder
State swirl cylinder；The cone with drainage trough is arranged in the swirl cylinder.
6. device as claimed in claim 5, which is characterized in that the cyclone separator also includes at least: threaded rod；The spiral shell
The first end of rasp bar is fixed on the overflow pipe, and the second end of the threaded rod is connected through a screw thread with the cone.
7. device as claimed in claim 6, which is characterized in that have in the inner wall of the swirl cylinder and/or the cylinder and draw
Chute.
8. device as claimed in claim 5, which is characterized in that have in the inner wall of the swirl cylinder and/or the cylinder resistance to
Grind ceramic layer.
9. such as device of any of claims 1-8, which is characterized in that also include at least: flowmeter；The flowmeter
The medium output end of the medium storage device is set.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611198015.9A CN106731024B (en) | 2016-12-22 | 2016-12-22 | A kind of device of gas in removal liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611198015.9A CN106731024B (en) | 2016-12-22 | 2016-12-22 | A kind of device of gas in removal liquid |
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| Publication Number | Publication Date |
|---|---|
| CN106731024A CN106731024A (en) | 2017-05-31 |
| CN106731024B true CN106731024B (en) | 2019-05-28 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201611198015.9A Active CN106731024B (en) | 2016-12-22 | 2016-12-22 | A kind of device of gas in removal liquid |
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Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN114478344B (en) * | 2022-04-01 | 2024-03-22 | 史秦博苑 | Caprolactam high-efficiency gasification separation process and system |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1870947A (en) * | 1930-11-07 | 1932-08-09 | A Neher Van | Dust collector |
| CN1470461A (en) * | 2003-06-23 | 2004-01-28 | 华东理工大学 | Oil-containing sewage floatation cyclone coupling separation method |
| JP2010247132A (en) * | 2009-04-13 | 2010-11-04 | Kinichi Takahashi | Apparatus for treating forced foaming-type organic liquid mixture and treatment method |
| CN104259014A (en) * | 2014-09-05 | 2015-01-07 | 吉首大学 | Rotor cyclone two-stage tandem type mineral flotation and defoaming device |
| CN205569835U (en) * | 2016-05-04 | 2016-09-14 | 邯钢集团衡水薄板有限责任公司 | Fire fighting equipment of cold -reduced sheet cleaner |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8741101B2 (en) * | 2012-07-13 | 2014-06-03 | Heartland Technology Partners Llc | Liquid concentrator |
-
2016
- 2016-12-22 CN CN201611198015.9A patent/CN106731024B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1870947A (en) * | 1930-11-07 | 1932-08-09 | A Neher Van | Dust collector |
| CN1470461A (en) * | 2003-06-23 | 2004-01-28 | 华东理工大学 | Oil-containing sewage floatation cyclone coupling separation method |
| JP2010247132A (en) * | 2009-04-13 | 2010-11-04 | Kinichi Takahashi | Apparatus for treating forced foaming-type organic liquid mixture and treatment method |
| CN104259014A (en) * | 2014-09-05 | 2015-01-07 | 吉首大学 | Rotor cyclone two-stage tandem type mineral flotation and defoaming device |
| CN205569835U (en) * | 2016-05-04 | 2016-09-14 | 邯钢集团衡水薄板有限责任公司 | Fire fighting equipment of cold -reduced sheet cleaner |
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| CN106731024A (en) | 2017-05-31 |
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Effective date of registration: 20210120 Address after: 221342 the government of Zhenxing East Road Town, four Town, Pizhou City, Xuzhou, Jiangsu, has passed. Patentee after: Jiangsu big block of wood ginkgo biological Science and Technology Ltd. Address before: 430205 No. 1, Liu Fang Avenue, Jiangxia District, Wuhan, Hubei. Patentee before: WUHAN INSTITUTE OF TECHNOLOGY |
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Effective date of registration: 20230628 Address after: 273 Wujin East Avenue, Luoyang Town, Wujin District, Changzhou City, Jiangsu Province, 213000 Patentee after: Changzhou Kechen Yongxin Precision Machinery Co.,Ltd. Address before: 221342 the government of Zhenxing East Road Town, four Town, Pizhou City, Xuzhou, Jiangsu, has passed. Patentee before: Jiangsu big block of wood ginkgo biological Science and Technology Ltd. |