CN106391332A - Rotational flow two-stage separation tube for high flow-rate liquid with deposited impurities - Google Patents
Rotational flow two-stage separation tube for high flow-rate liquid with deposited impurities Download PDFInfo
- Publication number
- CN106391332A CN106391332A CN201611129674.7A CN201611129674A CN106391332A CN 106391332 A CN106391332 A CN 106391332A CN 201611129674 A CN201611129674 A CN 201611129674A CN 106391332 A CN106391332 A CN 106391332A
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- section
- eddy flow
- diameter
- expanding
- flow section
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B5/00—Other centrifuges
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B7/00—Elements of centrifuges
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Abstract
The invention discloses a rotational flow two-stage separation tube for high flow-rate liquid with deposited impurities. The rotational flow two-stage separation tube is composed of an expanding rotational flow section and a double-layer separation section. The expanding rotational flow section is a conical tube body, and the inner wall of the expanding rotational flow section tube body is provided with a plurality of centrifugal rotational flow blades used for guiding the liquid flowing through to be in the radial direction for outward centrifugal rotation. The double-layer separation section is a double-layer tube body with an annular cavity formed inside. Outer layer high-concentration liquid guided by the centrifugal rotational flow blades is directly led into a middle layer tube body of the double-layer separation section to be conveyed, and a tube cavity of an inner tube body conveys low-concentration liquid under the centrifugal effect.
Description
Technical field
The present invention relates to body, carry depositing contaminants liquid cyclone the second-order separation pipe particularly to a kind of for high flow rate.
Background technology
Liquid delivery tube body currently for hyper tape depositing contaminants is common monolayer body, and pipe only serves conveying
Act on, this body is easy to occur deposition to block, in the event of obstruction because disposal costs are higher, and then can only select to change
Body, very wastes.
Content of the invention
The present invention is directed to above-mentioned technical problem, proposes a kind of liquid that can effectively prevent hyper tape depositing contaminants and conveys generation
Block, be provided simultaneously with centrifugation impurity ability carries depositing contaminants liquid cyclone the second-order separation pipe for high flow rate.
For reaching object above, it is achieved through the following technical solutions：
Carry depositing contaminants liquid cyclone the second-order separation pipe for high flow rate, by expanding eddy flow section and double layer separation section group
Become；
The taper body that expanding eddy flow section is become larger from arrival end to port of export diameter, and expanding eddy flow section inboard wall of tube body
It is provided with several for the centrifugal cyclone blade that guiding fluid is radially outward centrifugal rotation will be flowed through；
Double layer separation section is the internal double-deck pipe structure with ring cavity is to be divided into outside large-diameter pipe body and internal small diameter tube
Body；
Outside large-diameter pipe body is connected with the port of export of expanding eddy flow section, and the diameter of outside large-diameter pipe body and expanding eddy flow section
Port of export diameter identical；
The radial height of centrifugal cyclone blade is less than or equal to clearance distance between outside large-diameter pipe body and internal path body；
Internal path body arrival end is inserted into inside the tube chamber of expanding eddy flow section exit position；
Further, internal path body arrival end is provided with the taper undergauge conduit that diameter is gradually reduced；
Wherein, towards expanding eddy flow section, this structure function is that auxiliary is produced by eddy flow to taper undergauge conduit miner diameter end
The guiding fluid doing impurity concentration of centrifugal force enters in the tube chamber between outside large-diameter pipe body and internal path body.
Using the present invention of technique scheme, the liquid of the hyper tape depositing contaminants path entrance by expanding eddy flow section
End input, realizes reducing flow velocity in the presence of expanding, promotes liquid to be formed simultaneously under the guide effect of centrifugal cyclone blade
Radially outer centrifugal cyclone is so being greater than water due to depositing contaminants density itself and then deposit under the influence of centrifugal force
Impurity in the outer layer of liquid flow, thus can be importing directly into the outside large-diameter pipe body of double layer separation section and internal path body it
Between tube chamber, more clean liquid flows directly into the inner chamber of internal path body, and then realizes separating effect, so manages whole
The outlet section on road can targetedly process high concentration liquid and low-concentration liquid, and on the premise of centrifugation, due to liquid
Body generally eddy flow flows into without depositing.
Described above is only the general introduction of technical solution of the present invention, in order to better understand the technological means of the present invention,
And can be practiced according to the content of description, and in order to allow the above and other objects, features and advantages of the present invention can
Become apparent, below especially exemplified by preferred embodiment, and coordinate accompanying drawing, describe in detail as follows.
Brief description
The present invention totally 3 width accompanying drawing, wherein：
Fig. 1 is the overall structure diagram of the present invention.
Fig. 2 is the A-A of Fig. 1 to cross section view.
Fig. 3 is centrifugal cyclone blade construction schematic diagram.
In figure：1st, expanding eddy flow section, 1.1, centrifugal cyclone blade, 2, double layer separation section, 2.1, outside large-diameter pipe body, 2.2,
Internal path body, 2.3, taper undergauge conduit.
Specific embodiment
One kind as shown in Figure 1, Figure 2 and Figure 3 is used for high flow rate and carries depositing contaminants liquid cyclone the second-order separation pipe, by expanding
Footpath eddy flow section 1 and double layer separation section 2 form；
In the taper body that expanding eddy flow section 1 is become larger from arrival end to port of export diameter, and expanding eddy flow section 1 body
Wall is provided with several for flowing through the centrifugal cyclone blade 1.1 that guiding fluid is radially outward centrifugal rotation；
Double layer separation section 2 is the internal double-deck pipe structure with ring cavity is to be divided into outside large-diameter pipe body 2.1 and inside little
Footpath body 2.2；
Outside large-diameter pipe body 2.1 is connected with the port of export of expanding eddy flow section 1, and the diameter of outside large-diameter pipe body 2.1 and expansion
The port of export diameter of footpath eddy flow section 1 is identical；
The radial height of centrifugal cyclone blade 1.1 is less than or equal between outside large-diameter pipe body 2.1 and internal path body 2.2
Clearance distance；
Internal path body 2.2 arrival end is inserted into inside expanding eddy flow section 1 exit position tube chamber；
Further, internal path body 2.2 arrival end is provided with the taper undergauge conduit 2.3 that diameter is gradually reduced；
Wherein, towards expanding eddy flow section 1, this structure function is that auxiliary passes through eddy flow to taper undergauge conduit 2.3 miner diameter end
The guiding fluid doing impurity concentration producing centrifugal force enters the pipe between outside large-diameter pipe body 2.1 and internal path body 2.2
Intracavity.
Using the present invention of technique scheme, the liquid of hyper tape depositing contaminants is entered by the path of expanding eddy flow section 1
The input of mouth end, realizes reducing flow velocity in the presence of expanding, promotes liquid simultaneously under the guide effect of centrifugal cyclone blade 1.1
Form radially outer centrifugal cyclone, so due to depositing contaminants density itself be greater than water so that under the influence of centrifugal force
The outside large-diameter pipe body 2.1 that depositing contaminants in the outer layer of liquid flow, can thus be importing directly into double layer separation section 2 is little with inside
Tube chamber between footpath body 2.2, more clean liquid flows directly into the inner chamber of internal path body 2.2, and then realizes separating effect
Really, so high concentration liquid and low-concentration liquid can targetedly be processed in the outlet section of whole pipeline, and in centrifugation
On the premise of, because liquid generally eddy flow flows into without depositing.
The above, be only presently preferred embodiments of the present invention, not the present invention is made with any pro forma restriction, though
So the present invention is disclosed above with preferred embodiment, but is not limited to the present invention, any is familiar with this professional technology people
Member, in the range of without departing from technical solution of the present invention, a little change or is modified to when the technology contents of available the disclosure above are made
The Equivalent embodiments of equivalent variations, as long as being the content without departing from technical solution of the present invention, according to the technical spirit pair of the present invention
Any simple modification made for any of the above embodiments, equivalent variations and modification, all still fall within the range of technical solution of the present invention.
Claims (2)
1. be used for high flow rate carry depositing contaminants liquid cyclone the second-order separation pipe it is characterised in that by expanding eddy flow section (1) and pair
Layer segregation section (2) composition；
The taper body that described expanding eddy flow section (1) is become larger from arrival end to port of export diameter, and expanding eddy flow section (1) pipe
Internal wall is provided with several for flowing through centrifugal cyclone blade (1.1) that guiding fluid is radially outward centrifugal rotation；
Described double layer separation section (2) is the internal double-deck pipe structure with ring cavity for being divided into outside large-diameter pipe body (2.1) and interior
Portion's path body (2.2)；
Described outside large-diameter pipe body (2.1) is connected with the port of export of expanding eddy flow section (1), and outside large-diameter pipe body (2.1) is straight
Footpath is identical with the port of export diameter of expanding eddy flow section (1)；
The radial height of described centrifugal cyclone blade (1.1) is less than or equal to outside large-diameter pipe body (2.1) and internal path body
(2.2) clearance distance between；
Described internal path body (2.2) arrival end is inserted into inside the tube chamber of expanding eddy flow section (1) exit position.
2. according to claim 1 for high flow rate carry depositing contaminants liquid cyclone the second-order separation pipe it is characterised in that：
Described internal path body (2.2) arrival end is provided with taper undergauge conduit (2.3) that diameter is gradually reduced；
Wherein, taper undergauge conduit (2.3) miner diameter end is towards expanding eddy flow section (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611129674.7A CN106391332B (en) | 2016-12-09 | 2016-12-09 | The eddy flow the second-order separation pipe of depositing contaminants liquid is carried for high flow rate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611129674.7A CN106391332B (en) | 2016-12-09 | 2016-12-09 | The eddy flow the second-order separation pipe of depositing contaminants liquid is carried for high flow rate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106391332A true CN106391332A (en) | 2017-02-15 |
| CN106391332B CN106391332B (en) | 2018-09-25 |
Family
ID=58085350
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611129674.7A Active CN106391332B (en) | 2016-12-09 | 2016-12-09 | The eddy flow the second-order separation pipe of depositing contaminants liquid is carried for high flow rate |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106391332B (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2510169Y (en) * | 2001-09-25 | 2002-09-11 | 黄云生 | Water centrifugal spiral dust collecting apparatus |
| CN2717526Y (en) * | 2004-07-21 | 2005-08-17 | 上海第二医科大学附属第九人民医院 | Conic sandwich centrifugal machine |
| CN101642725A (en) * | 2008-07-16 | 2010-02-10 | 奥索临床诊断有限公司 | Use of fluid aspiration/dispensing tip as a microcentrifuge tube |
| US20100044287A1 (en) * | 2007-02-21 | 2010-02-25 | Holger Blum | Hydro cyclone device and hydro cyclone installation |
| CN203841701U (en) * | 2014-01-26 | 2014-09-24 | 武汉美达康科技有限公司 | Disposable peripheral micro blood collecting separator |
-
2016
- 2016-12-09 CN CN201611129674.7A patent/CN106391332B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2510169Y (en) * | 2001-09-25 | 2002-09-11 | 黄云生 | Water centrifugal spiral dust collecting apparatus |
| CN2717526Y (en) * | 2004-07-21 | 2005-08-17 | 上海第二医科大学附属第九人民医院 | Conic sandwich centrifugal machine |
| US20100044287A1 (en) * | 2007-02-21 | 2010-02-25 | Holger Blum | Hydro cyclone device and hydro cyclone installation |
| CN101642725A (en) * | 2008-07-16 | 2010-02-10 | 奥索临床诊断有限公司 | Use of fluid aspiration/dispensing tip as a microcentrifuge tube |
| CN203841701U (en) * | 2014-01-26 | 2014-09-24 | 武汉美达康科技有限公司 | Disposable peripheral micro blood collecting separator |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106391332B (en) | 2018-09-25 |
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