CN205146475U - Concentrated swirler of screen cloth formula - Google Patents
Concentrated swirler of screen cloth formula Download PDFInfo
- Publication number
- CN205146475U CN205146475U CN201520985361.6U CN201520985361U CN205146475U CN 205146475 U CN205146475 U CN 205146475U CN 201520985361 U CN201520985361 U CN 201520985361U CN 205146475 U CN205146475 U CN 205146475U
- Authority
- CN
- China
- Prior art keywords
- urceolus
- guide cylinder
- discharge pipe
- screen cloth
- splicing
- 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.)
- Expired - Fee Related
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Abstract
The utility model discloses a concentrated swirler of screen cloth formula, including the guide cylinder, connect material urceolus, toper urceolus, overflow mouth, coarse fodder export, pan feeding pipe, manometer, arc screen cloth, carefully expect the discharge pipe, the guide cylinder left end is equipped with the pan feeding pipe that has the manometer, and the guide cylinder top is equipped with an overflow mouth, meet material urceolus and guide cylinder fixed connection, connect and be equipped with the arc screen cloth in the material urceolus, carefully expect the discharge pipe and be connected with connecing the material urceolus, expect carefully that the discharge pipe is equipped with the manometer, the toper urceolus is connected with connecing the material urceolus, and toper urceolus bottom is equipped with coarse fodder export, compare with prior art, the beneficial effects of the utility model are that this is novel to be a concentrated swirler of screen cloth formula, and this treatment of plants volume is big, and the cut size is thin, and it is big to solve the large diameter swirler handling capacity that has the existence now, and the lower limit is low effectively in grades, and it is big that thick ratio is run in the overflow, and the minor diameter descends the limit for height effectively in grades, but the handling capacity is little, and the problem of the high aspect of energy consumption is organized to swirler.
Description
Technical field
The utility model relates to a kind of screening plant, especially a kind of screen mesh type concentrate cyclone.
Background technology
The radial velocity (centrifugal sedimentation speed) of particle equals the ratio that the sinking speed of particle in stationary fluid is multiplied by centrifugal acceleration a and gravity acceleration g; When solid particle is less or its more close to coal slurry water density time, its movement locus and liquid close, the motion of superfine particle in hydrocyclone is almost identical with liquid particle, makes its allocation proportion between underflow and overflow close with liquid.
Existing common cyclone Problems existing is, large diameter cyclone treating capacity is large, but effectively classification lower limit is low, and it is large that thick ratio is run in overflow; And limit for height under the effective classification of minor diameter, but process size, a cluster cyclone energy consumption is high.
Summary of the invention
The purpose of this utility model is to provide a kind of screen mesh type concentrate cyclone, to solve the problem proposed in above-mentioned background technology.
The purpose of this utility model is achieved by following technical proposals: a kind of screen mesh type concentrate cyclone, comprise guide cylinder, splicing urceolus, taper urceolus, overfall, coarse fodder exports, feeding pipe, Pressure gauge, curved screen, fines discharge pipe, described guide cylinder left end is provided with manometric feeding pipe, guide cylinder top is provided with an overfall, described splicing urceolus is fixedly connected with guide cylinder, curved screen is provided with in splicing urceolus, described fines discharge pipe is connected with splicing urceolus, fines discharge pipe is provided with Pressure gauge, described taper urceolus is connected with splicing urceolus, a coarse fodder outlet is provided with bottom taper urceolus.
Further, described coarse fodder outlet, feeding pipe and fines discharge pipe are respectively equipped with by-pass valve control.
Further, described curved screen is fixed in splicing urceolus, the screening wire side of described curved screen and the guide cylinder inwall on top coplanar.
Further, described Pressure gauge is connected with pressure sensor, and pressure sensor described in two is located in feeding pipe and in fines discharge pipe respectively.
Compared with prior art, the beneficial effects of the utility model are these novel a kind of screen mesh type concentrate cyclones, this device processes amount is large, partition size is thin, and the large diameter cyclone treating capacity that can solve existing existence is large, and effective classification lower limit is low, it is large that thick ratio is run in overflow, limit for height under the effective classification of minor diameter, but treating capacity is little, the problem of the aspects such as a cluster cyclone energy consumption height.
Accompanying drawing explanation
Fig. 1 is the utility model whole structure figure;
In figure: 1, guide cylinder, 2, splicing urceolus, 3, taper urceolus, 4, overfall, 5, coarse fodder outlet, 6, feeding pipe, 7, Pressure gauge, 8, curved screen, 9, fines discharge pipe.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the utility model embodiment; technical scheme in the utility model embodiment is clearly and completely described; obviously; described embodiment is only the utility model part embodiment; instead of whole embodiments; based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
As shown in Figure 1, the utility model discloses a kind of screen mesh type concentrate cyclone, comprise guide cylinder 1, splicing urceolus 2, taper urceolus 3, overfall 4, coarse fodder outlet 5, feeding pipe 6, Pressure gauge 7, curved screen 8, fines discharge pipe 9, described guide cylinder 1 left end is provided with the feeding pipe 6 with Pressure gauge 7, guide cylinder 1 top is provided with an overfall 4, described splicing urceolus 2 is fixedly connected with guide cylinder 1, curved screen 8 is provided with in splicing urceolus 2, described fines discharge pipe 9 is connected with splicing urceolus 2, fines discharge pipe 9 is provided with Pressure gauge 7, described taper urceolus 3 is connected with splicing urceolus 2, a coarse fodder outlet 5 is provided with bottom taper urceolus 3, coarse granule in contour stealth and part fine particle arrive the curved screen 8 of limit wall under the influence of centrifugal force, be less than the particle in curved screen 8 aperture through screen cloth, get rid of from the fines discharge pipe 9 of splicing urceolus 2, remaining coarse granule is got rid of from coarse fodder outlet 5 with contour stealth, described coarse fodder outlet 5, feeding pipe 6 and fines discharge pipe 9 are respectively equipped with by-pass valve control, coordinate Pressure gauge 7 to use, and are convenient to control, and reach screening effect and maximize, described curved screen 8 is fixed in splicing urceolus 2, the screening wire side of described curved screen 8 and guide cylinder 1 inwall on top coplanar, described Pressure gauge 7 is connected with pressure sensor, and pressure sensor described in two is located in feeding pipe 6 and in fines discharge pipe 9 respectively.
To those skilled in the art, obvious the utility model is not limited to the details of above-mentioned one exemplary embodiment, and when not deviating from spirit of the present utility model or essential characteristic, can realize the utility model in other specific forms.Therefore, no matter from which point, all should embodiment be regarded as exemplary, and be nonrestrictive, scope of the present utility model is limited by claims instead of above-mentioned explanation, and all changes be therefore intended in the implication of the equivalency by dropping on claim and scope are included in the utility model.Any Reference numeral in claim should be considered as the claim involved by limiting.
In addition, be to be understood that, although this description is described according to embodiment, but not each embodiment only comprises an independently technical scheme, this narrating mode of description is only for clarity sake, those skilled in the art should by description integrally, and the technical scheme in each embodiment also through appropriately combined, can form other embodiments that it will be appreciated by those skilled in the art that.
Claims (4)
1. a screen mesh type concentrate cyclone, comprise guide cylinder (1), splicing urceolus (2), taper urceolus (3), overfall (4), coarse fodder outlet (5), feeding pipe (6), Pressure gauge (7), curved screen (8), fines discharge pipe (9), it is characterized in that: described guide cylinder (1) left end is provided with the feeding pipe (6) with Pressure gauge (7), guide cylinder (1) top is provided with an overfall (4), described splicing urceolus (2) is fixedly connected with guide cylinder (1), curved screen (8) is provided with in splicing urceolus (2), described fines discharge pipe (9) is connected with splicing urceolus (2), fines discharge pipe (9) is provided with Pressure gauge (7), described taper urceolus (3) is connected with splicing urceolus (2), taper urceolus (3) bottom is provided with coarse fodder outlet (5).
2. a kind of screen mesh type concentrate cyclone according to claim 1, is characterized in that: described coarse fodder outlet (5), feeding pipe (6) and fines discharge pipe (9) are respectively equipped with by-pass valve control.
3. a kind of screen mesh type concentrate cyclone according to claim 1, is characterized in that: described curved screen (8) is fixed in splicing urceolus (2), the screening wire side of described curved screen (8) and guide cylinder (1) inwall on top coplanar.
4. a kind of screen mesh type concentrate cyclone according to claim 1, is characterized in that: described Pressure gauge (7) is connected with pressure sensor, and pressure sensor described in two is located in feeding pipe (6) and in fines discharge pipe (9) respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520985361.6U CN205146475U (en) | 2015-12-02 | 2015-12-02 | Concentrated swirler of screen cloth formula |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520985361.6U CN205146475U (en) | 2015-12-02 | 2015-12-02 | Concentrated swirler of screen cloth formula |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205146475U true CN205146475U (en) | 2016-04-13 |
Family
ID=55682217
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520985361.6U Expired - Fee Related CN205146475U (en) | 2015-12-02 | 2015-12-02 | Concentrated swirler of screen cloth formula |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205146475U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106076672A (en) * | 2016-08-12 | 2016-11-09 | 华东理工大学 | Air-flowing type multi-product subparticle sequence clasfficiator |
| CN106269315A (en) * | 2016-08-12 | 2017-01-04 | 华东理工大学 | Inlet particle sequence type cyclone |
| CN110118068A (en) * | 2019-06-01 | 2019-08-13 | 濮阳市中原锐实达石油设备有限公司 | A kind of cleaner and its application method of replaceable drilling well desander desilter |
-
2015
- 2015-12-02 CN CN201520985361.6U patent/CN205146475U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106076672A (en) * | 2016-08-12 | 2016-11-09 | 华东理工大学 | Air-flowing type multi-product subparticle sequence clasfficiator |
| CN106269315A (en) * | 2016-08-12 | 2017-01-04 | 华东理工大学 | Inlet particle sequence type cyclone |
| CN106269315B (en) * | 2016-08-12 | 2019-01-01 | 华东理工大学 | Inlet particle sequence type cyclone |
| CN110118068A (en) * | 2019-06-01 | 2019-08-13 | 濮阳市中原锐实达石油设备有限公司 | A kind of cleaner and its application method of replaceable drilling well desander desilter |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160413 Termination date: 20161202 |