CN104399311B - A kind of secondary returning streaming transition joint - Google Patents
A kind of secondary returning streaming transition joint Download PDFInfo
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- CN104399311B CN104399311B CN201410644689.1A CN201410644689A CN104399311B CN 104399311 B CN104399311 B CN 104399311B CN 201410644689 A CN201410644689 A CN 201410644689A CN 104399311 B CN104399311 B CN 104399311B
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- barrel shrond
- drainage
- filter chamber
- shrond
- cyclonic separation
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- 230000007704 transition Effects 0.000 title claims abstract description 14
- 238000000926 separation method Methods 0.000 claims abstract description 35
- 239000012530 fluid Substances 0.000 claims description 24
- 238000010992 reflux Methods 0.000 claims description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 10
- 239000002184 metal Substances 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 238000001179 sorption measurement Methods 0.000 claims description 5
- 230000002093 peripheral effect Effects 0.000 claims description 3
- 239000012535 impurity Substances 0.000 abstract description 21
- 238000001914 filtration Methods 0.000 abstract description 11
- 230000008021 deposition Effects 0.000 abstract description 4
- 230000000903 blocking effect Effects 0.000 abstract description 2
- 239000007788 liquid Substances 0.000 abstract description 2
- 238000009434 installation Methods 0.000 abstract 1
- 239000008187 granular material Substances 0.000 description 10
- 239000010410 layer Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 230000000712 assembly Effects 0.000 description 2
- 238000000429 assembly Methods 0.000 description 2
- 230000001413 cellular effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000037237 body shape Effects 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000000280 densification Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- Cyclones (AREA)
Abstract
The present invention relates to a kind of secondary returning streaming transition joint, including cyclonic separation portion, separated part of confluxing and backflow portion, the main body convection cell that cyclonic separation portion is mainly provided with spiral type eddy flow groove by a setting rotates, the impurity making different quality size separates, subsequently in separated part of confluxing, separation assembly by a flaring mouth, convection cell carries out the separating and filtering of secondary, the impurity of the deposition in separation assembly is back in cyclonic separation portion by liquid stream by backflow portion afterwards, secondary separation and the secondary back of convection cell is realized by an easy structure, effectively prevent impurity from too much causing confluxing the blocking of separated part, the present invention is easy for installation, cheap.
Description
Technical field
The present invention relates to a kind of secondary returning streaming transition joint, be specifically related to a kind of fluid connection that trace impurity and unrelated mixture can be filtered.
Background technology
In the fluid device the highest to water quality requirement; drum, distillator and some chemical industry equipments in such as boiler; not only it is frequently necessary to water is filtered; and these equipment are because bigger operational difference and soda acid change; often produce incrustation scale; especially at pipe joint, being particularly easy to because fouling or foul alluvial block, either impurity still blocks and all can bring certain potential safety hazard to these stress reaction equipment；
So, in the joint of these equipment higher to water quality requirement, needing to arrange some both can have filter effect, ensured certain fluid filter assemblies by property again simultaneously；
Wherein ZL201320354014.4 proposes a kind of filter pipeline joint, and this kind of joint working condition requirement to using can be higher, and this joint realizes the filtration to fluids within pipes by an easy replaceable filter assemblies；Although the granule being relatively large in diameter or lamellar impurity can be filtered by cellular joint; but the flow resistance that cellular flowing hole road brings can be the highest; can seriously reduce the flow of current; this kind of poroid flowing hole road is easy to or flowing hole road internal incrustation excessive because of granule and blocks simultaneously; once block, associated vessel can be caused intrinsic pressure too high, explode; and the bearing capacity of this kind of transition joint is the biggest, it is easy to leak；
ZL201320158107.X discloses the spiral-flow filter of another kind of tank body shape, this structure employing fluid eddy flow is centrifugal carries out filtering flow, flow resistance ratio is relatively low, but the volume ratio of this structure is huger, miniaturization even interface cannot be realized, and the approach axis of this structure convection cell also has certain requirement, so general expenditure ratio is relatively low, cost is the highest, is not suitable for the pipeline configuration to some closenesses are high and filters；
To sum up, there are the following problems for existing filter device for pipes or transition joint:
1, flow resistance is relatively big, and being easily caused pressure vessel cannot row pressure in time；
2, filtration is relatively backward, and the poroid filtration of traditional iris type is affected bigger by profile and the size of impurity in fluid；
3, it is very easy to because fouling and filtration granule block relatively greatly；
4, efficient filtration often volume ratio is huger, it is impossible to realize miniaturization and densification is arranged.
Summary of the invention
The technical problem to be solved in the present invention is: overcomes pipe joint in prior art cannot realize high efficiency and filters and the technical problem of low flow resistance, it is provided that the spiral-flow type transition joint of a kind of miniaturization.
The technical solution adopted for the present invention to solve the technical problems is:
A kind of secondary returning streaming transition joint, including cyclonic separation portion, separated part of confluxing and backflow portion, described cyclonic separation portion and confluxing interconnects between separated part, described backflow portion is arranged on the periphery in cyclonic separation portion, described cyclonic separation portion includes the barrel shrond A of hollow shape, the two ends of described barrel shrond A are provided with flow inlet, drainage port, some eddy flow drainage troughs it are provided with on the internal face of described barrel shrond A, the path of the described eddy flow drainage trough axis relative to barrel shrond A is helically arranged, it is provided with drainage screen in described eddy flow drainage trough, the lateral cross section of described drainage screen is that continuous print is stepped, the ladder vertical plane of described drainage screen is towards the flow inlet of barrel shrond A；
Also being arranged concentrically the rhone of annular in the wall of described barrel shrond A, one end closing, one end open on described rhone axial direction, the opening of described rhone is positioned at around the drainage port A of barrel shrond A；
Described separated part of confluxing includes barrel shrond B main body, the inwall of barrel shrond B is provided with parting surface, barrel shrond B internal cavities was separated into stream chamber and filter chamber by described parting surface, described stream chamber of crossing is positioned in the middle part of barrel shrond B, it is peripheral that described filter chamber was arranged on stream chamber, described filter chamber is semiclosed annular chamber, described filter chamber is towards at the drainage port of barrel shrond A, described parting surface includes separating cylinder and separate mesh, described separation cylinder is truncated cone-shaped, the less one end of described separation drum diameter is towards the drainage port of barrel shrond A, described separation drum diameter less one end bore diameter less than drainage port A；
Described separate mesh is annular, and one end that described separate mesh is bigger with separating drum diameter connects；
Described backflow portion includes that some annular array are at backflow separated part and the reflux line of cyclonic separation portion outer wall, one end of described reflux line connects through the wall of barrel shrond B with filter chamber, and the other end of reflux line connects through the wall of the barrel shrond A at flow inlet with rhone；
The blind end of described filter chamber drainage port side dorsad is provided with one for the water conservancy diversion cambered surface by the guiding fluid reflux line in filter chamber.
As the further innovation of the present invention, the wall of described rhone is coated with activated carbon adsorption layer.
As the further innovation of the present invention, described parting surface provides connection post to be fixed on the internal face of barrel shrond B.
As the further innovation of the present invention, described drainage screen includes bilevel metal filter screen, is additionally provided with fleece in the middle of double layer of metal drainage screen.
Further innovation as the present invention, described barrel shrond A is provided centrally with an eddy flow assembly, described eddy flow assembly includes a spiral spiral board, the central part of described spiral board is provided with a fixing axle, and the two ends of described fixing axle are connected by supporting network is fixing with the inwall of barrel shrond A.
The invention has the beneficial effects as follows:
1, the present invention by a cyclone structure being arranged on inner-walls of duct and be arranged on the stepped drainage screen bottom cyclone structure realize impurity in convection cell efficiently from centrifugal and filter, stair-stepping drainage screen can occur certain deceleration and stop so that be positioned at the fluid with impurity bottom cyclone structure, prevent along laminar flow speed too high, impurity cannot be settled, the present invention or drainage screen excessive because of granule will occur blocking to affect the flow velocity of fluid simultaneously, has higher safety；Shunting section cannot can occur the granule of sedimentation to carry out secondary filter in time by occurring eddy flow centrifugal, often the quality of these granules all ratios are relatively low, adhesive force can be poor, and average diameter is smaller, it is desirable to provide it is filtered by a highdensity drainage screen；So the shunting section of the present invention can separate with convection cell, the fluid of center and marginal position separates according to different runners, under the flow velocity of the flow resistance and fluid itself that do not affect pipe joint itself, carry out the filtration of fluid, shunting section can carry out secondary separation to the relatively small impurities granule through stepped drainage screen simultaneously, ensure the effect filtered, the present invention is in order to prevent the impurity over-deposit in filter chamber simultaneously, the backflow portion of the present invention can be under the liquid stream after shunting drives, the impurity of filter chamber is taken to the cyclonic separation intracavity that filtration contact area is bigger, the rate of flow of fluid of cyclonic separation intracavity is higher simultaneously, impurity will not occur too fast deposition to affect filter quality；
2, the activated carbon adsorption layer on rhone can the interior soluble impurity of convection cell carry out adsorbing and filtering further, improves filter quality；
3, connect post and can improve the stability of parting surface, prevent fluid too high at flow velocity, when impulsive force is excessive, parting surface is caused damage.
4, the drainage screen of eddy flow section of the present invention is sandwich, middle fleece can carry out the most careful filtration with convection cell, and the metal filter screen being positioned at fleece both sides is possible to prevent the granule being relatively large in diameter to damage fleece, drainage screen compared to monolayer, this structured filter effect is more preferable, and intensity and durability are the most more increased.
5, the eddy flow assembly in barrel shrond A of the present invention, can the eddy flow of strengthening fluid further, the centrifugal force of impurity in lifting fluid, promote the effect of impurity centrifugation further.
Accompanying drawing explanation
The present invention is further described with embodiment below in conjunction with the accompanying drawings.
Fig. 1 is that the structure of the present invention is always schemed；
Fig. 2 is the transverse cross-sectional view of eddy flow section of the present invention；
Fig. 3 is the generalized section of eddy flow assembly of the present invention；
Fig. 4 is the schematic diagram of drainage screen of the present invention；
Figure includes: barrel shrond A1, eddy flow drainage trough 2, rhone 3, the opening 4 of rhone, drainage port A5, activated carbon adsorption layer 6, separate mesh 7, separation cylinder 8, barrel shrond B9, filter chamber 10, excessively stream chamber 11, spiral board 12, fixing axle 13, metal filter screen 14, fleece 15, reflux line 16, water conservancy diversion cambered surface 17.
Detailed description of the invention
In conjunction with the accompanying drawings, the present invention is further detailed explanation.These accompanying drawings are the schematic diagram of simplification, and the basic structure of the present invention is described the most in a schematic way, and therefore it only shows the composition relevant with the present invention.
As shown in Figure 1, the present invention is a kind of secondary returning streaming transition joint, including cyclonic separation portion, separated part of confluxing and backflow portion, described cyclonic separation portion and confluxing interconnects between separated part, described backflow portion is arranged on the periphery in cyclonic separation portion, described cyclonic separation portion includes the barrel shrond A1 of hollow shape, the two ends of described barrel shrond A1 are provided with flow inlet, drainage port, six eddy flow drainage troughs 2 it are provided with on the internal face of described barrel shrond A1, the path of described eddy flow drainage trough 2 axis relative to barrel shrond A1 is helically arranged, it is provided with drainage screen in described eddy flow drainage trough 2, the lateral cross section of described drainage screen is that continuous print is stepped, the ladder vertical plane of described drainage screen is towards the flow inlet of barrel shrond；
Also being arranged concentrically the rhone 3 of annular in the wall of described barrel shrond A1, one end closing, one end open on described rhone 3 axial direction, the opening 4 of described rhone 3 is positioned at around the drainage port A5 of barrel shrond A1；
Described separated part of confluxing includes barrel shrond B9 main body, the inwall of barrel shrond B9 is provided with parting surface, barrel shrond B9 internal cavities was separated into stream chamber 11 and filter chamber 10 by described parting surface, described stream chamber 11 of crossing is positioned in the middle part of barrel shrond B9, it is peripheral that described filter chamber 10 was arranged on stream chamber 11, described filter chamber 10 is semiclosed annular chamber, described filter chamber 10 is towards at the drainage port of barrel shrond A1, described parting surface includes separating cylinder 8 and separate mesh 7, described separation cylinder 8 is truncated cone-shaped, the less one end of described separation cylinder 8 diameter is towards the drainage port of barrel shrond A1, described separation cylinder 8 diameter less one end bore diameter less than drainage port A5；
Described separate mesh 7 is annular, and described separate mesh 7 connects with separating one end that cylinder 8 is relatively large in diameter；
Described backflow portion includes that some annular array are at backflow separated part and the reflux line 16 of cyclonic separation portion outer wall, one end of described reflux line 16 connects through the wall of barrel shrond B9 with filter chamber 10, and the other end of reflux line 16 connects through the wall of the barrel shrond A at flow inlet with rhone 3；
The blind end of described filter chamber drainage port side dorsad is provided with one for the water conservancy diversion cambered surface 17 by the guiding fluid reflux line in filter chamber；
It is coated with activated carbon adsorption layer 6 on the wall of described rhone 3；
Described parting surface provides connection post to be fixed on the internal face of barrel shrond B9；
Described drainage screen includes bilevel metal filter screen 14, is additionally provided with fleece 15 in the middle of double layer of metal drainage screen 14；
Described barrel shrond A1 is provided centrally with an eddy flow assembly, described eddy flow assembly includes a spiral spiral board 12, the central part of described spiral board 12 is provided with a fixing axle 13, and the two ends of described fixing axle 13 are connected by supporting network is fixing with the inwall of barrel shrond A1；
nullIt is more that the present invention may be mounted at some impurity、And in the less pipeline of granule，Fluid is after entering into barrel shrond A1，Under the driving of eddy flow assembly and eddy flow drainage trough 2，Rotate，Magazine separates in centrifugal acting on pure fluid，The granule foreign that quality is bigger is blocked on stair-stepping drainage screen，Quality less after entering in barrel shrond B9，Separate via separating cylinder 8，Pure fluid entered directly in stream chamber 11，Then there is secondary filter via separate mesh 7 in the external fluid carrying impurity，Entered back in stream chamber 11,And the impurity particle of deposition is taken out of at the fluid separated by separation cylinder 8 in filter chamber 10，The bigger rhone in space 3 is entered into via reflux line 16，The filter effect of fluid after preventing the impurity in separate mesh 7 from occurring deposition impact to separate.
With the above-mentioned desirable embodiment according to the present invention for enlightenment, by above-mentioned description, relevant staff can carry out various change and amendment completely in the range of without departing from this invention technological thought.The content that the technical scope of this invention is not limited in description, it is necessary to determine its technical scope according to right.
Claims (5)
1. a secondary returning streaming transition joint, it is characterized in that: include cyclonic separation portion, separated part of confluxing and backflow portion, described cyclonic separation portion and confluxing interconnects between separated part, described backflow portion is arranged on the periphery in cyclonic separation portion, described cyclonic separation portion includes the barrel shrond A of hollow shape, the two ends of described barrel shrond A are provided with flow inlet, drainage port, some eddy flow drainage troughs it are provided with on the internal face of described barrel shrond A, the path of the described eddy flow drainage trough axis relative to barrel shrond A is helically arranged, it is provided with drainage screen in described eddy flow drainage trough, the lateral cross section of described drainage screen is that continuous print is stepped, the ladder vertical plane of described drainage screen is towards the flow inlet of barrel shrond A；
Also being arranged concentrically the rhone of annular in the wall of described barrel shrond A, one end closing, one end open on described rhone axial direction, the opening of described rhone is positioned at around the drainage port A of barrel shrond A；
Described separated part of confluxing includes barrel shrond B main body, the inwall of barrel shrond B is provided with parting surface, barrel shrond B internal cavities was separated into stream chamber and filter chamber by described parting surface, described stream chamber of crossing is positioned in the middle part of barrel shrond B, it is peripheral that described filter chamber was arranged on stream chamber, described filter chamber is semiclosed annular chamber, described filter chamber is towards at the drainage port of barrel shrond A, described parting surface includes separating cylinder and separate mesh, described separation cylinder is truncated cone-shaped, the less one end of described separation drum diameter is towards the drainage port of barrel shrond A, described separation drum diameter less one end bore diameter less than drainage port A；
Described separate mesh is annular, and one end that described separate mesh is bigger with separating drum diameter connects；
Described backflow portion includes that some annular array are at backflow separated part and the reflux line of cyclonic separation portion outer wall, one end of described reflux line connects through the wall of barrel shrond B with filter chamber, and the other end of reflux line connects through the wall of the barrel shrond A at flow inlet with rhone；
The blind end of described filter chamber drainage port side dorsad is provided with one for the water conservancy diversion cambered surface by the guiding fluid reflux line in filter chamber.
2. a kind of secondary returning streaming transition joint as claimed in claim 1, is characterized in that: be coated with activated carbon adsorption layer on the wall of described rhone.
3. a kind of secondary returning streaming transition joint as claimed in claim 1, is characterized in that: described parting surface provides connection post to be fixed on the internal face of barrel shrond B.
4. a kind of secondary returning streaming transition joint as claimed in claim 1, is characterized in that: described drainage screen includes bilevel metal filter screen, is additionally provided with fleece in the middle of double layer of metal drainage screen.
5. a kind of secondary returning streaming transition joint as claimed in claim 1, it is characterized in that: described barrel shrond A is provided centrally with an eddy flow assembly, described eddy flow assembly includes a spiral spiral board, the central part of described spiral board is provided with a fixing axle, and the two ends of described fixing axle are connected by supporting network is fixing with the inwall of barrel shrond A.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410644689.1A CN104399311B (en) | 2014-11-14 | 2014-11-14 | A kind of secondary returning streaming transition joint |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410644689.1A CN104399311B (en) | 2014-11-14 | 2014-11-14 | A kind of secondary returning streaming transition joint |
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| Publication Number | Publication Date |
|---|---|
| CN104399311A CN104399311A (en) | 2015-03-11 |
| CN104399311B true CN104399311B (en) | 2016-09-21 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201410644689.1A Active CN104399311B (en) | 2014-11-14 | 2014-11-14 | A kind of secondary returning streaming transition joint |
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Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110652782A (en) * | 2019-10-27 | 2020-01-07 | 葛军 | High-pressure anti-blocking filter joint |
| CN112604364B (en) * | 2020-12-12 | 2022-05-06 | 山东舜业压力容器有限公司 | Composite dirt remover |
| CN112957772B (en) * | 2021-02-04 | 2022-10-18 | 无锡力必特自动化设备有限公司 | Fluid filter and filtering method |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB275695A (en) * | 1926-04-09 | 1927-08-09 | Shell Mex Ltd | Improvements in or relating to filters |
| JP2000167355A (en) * | 1998-12-09 | 2000-06-20 | Tao:Kk | Purifying apparatus |
| CN2832266Y (en) * | 2005-10-11 | 2006-11-01 | 刘光辉 | Spiral type water-purifying filter core |
| CN1919467A (en) * | 2005-08-18 | 2007-02-28 | 筱崎隆 | Oil filter |
| CN102423568A (en) * | 2011-10-25 | 2012-04-25 | 中国北车集团大连机车研究所有限公司 | Centrifugal magnetic filter |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TW558605B (en) * | 2002-02-08 | 2003-10-21 | Mitsubishi Electric Corp | Fuel filter and fuel supply device |
-
2014
- 2014-11-14 CN CN201410644689.1A patent/CN104399311B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB275695A (en) * | 1926-04-09 | 1927-08-09 | Shell Mex Ltd | Improvements in or relating to filters |
| JP2000167355A (en) * | 1998-12-09 | 2000-06-20 | Tao:Kk | Purifying apparatus |
| CN1919467A (en) * | 2005-08-18 | 2007-02-28 | 筱崎隆 | Oil filter |
| CN2832266Y (en) * | 2005-10-11 | 2006-11-01 | 刘光辉 | Spiral type water-purifying filter core |
| CN102423568A (en) * | 2011-10-25 | 2012-04-25 | 中国北车集团大连机车研究所有限公司 | Centrifugal magnetic filter |
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| CN104399311A (en) | 2015-03-11 |
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Effective date of registration: 20160823 Address after: 226600, No. 6 the Yellow Sea Avenue (middle), Haian County Development Zone, Nantong, Jiangsu Applicant after: Jiangsu Sheng Li detection instrument company limited Address before: 266045 Shandong province Qingdao City, Zhengzhou Road No. 43 building 130 room A Applicant before: Qingdao Rubber Valley Intellectual Property Co.,Ltd. |
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