CN2372035Y - Solid-liquid separator - Google Patents
Solid-liquid separator Download PDFInfo
- Publication number
- CN2372035Y CN2372035Y CN 99222638 CN99222638U CN2372035Y CN 2372035 Y CN2372035 Y CN 2372035Y CN 99222638 CN99222638 CN 99222638 CN 99222638 U CN99222638 U CN 99222638U CN 2372035 Y CN2372035 Y CN 2372035Y
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- solid
- outer tube
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- liquid
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Abstract
The utility model discloses a solid-liquid separator. The utility model adopts the principle of cyclone separation. Solid-liquid mixtures are filled into the solid-liquid separator from a tangent line of a solid-liquid inlet connecting pipe 1 which is arranged at the outer side of the upper part of a housing 4, are separated by an inclined hole 11 and a square hole 12 which are arranged on an outer pipe 2 arranged in the housing 4, and are guided by a guide seat 7; thus, the liquid flows out from a water outlet pipe 3 and the solid is exhausted from a solid outlet connecting pipe 10. The utility model has the characteristics of high efficiency, low cost, convenient maintenance, etc.
Description
The utility model belongs to the Separation of Solid and Liquid field.
The application of solid-liquid separator is very extensive, as: sewage disposal, sea, river separate automatically, and cooling circulating water metallurgical, the power plant is used and is handled, Water Treatment, the recovery of metallic nickel, chromium, iron, copper, zinc etc., colliery water treatment or the like.Mainly there is the shortcoming of the following aspects in current solid-liquid separator: 1, current solid-liquid separating equipment great majority are to separate with the internals of motor driven rotary, internals have the various forms Filter column again, if any ceramic mould, winding-type, the molten type of fiber bag etc., complex structure, rotatable parts are many, and the parts that therefore often rotate stop because of inner foreign material block, maintenance process is miscellaneous, tear open again, look into again, can't conclude immediately that fault is for where; 2, current solid-liquid separator needs backwash, promptly filter a period of time need backwash deslagging, increased back purge system like this and caused complex structure, back purge system makes the close solid that is contained in the mesh recoil again and washes off because of filter mesh is fine and closely woven, causes isolated by filtration efficient to reduce; 3, current solid-liquid separator is added its additional zero parts and is cost an arm and a leg because of motor and back purge system are arranged, thereby the cost height; 4, current solid-liquid separator all needs standby one to cause the stopping production accident to two to prevent fatal parking; 5, current solid-liquid separator is restricted because of the medium different application, and is strong as the seawater deep-etching, and stainless steel all can't be anticorrosion in seawater, thereby is difficult to use qualified internals material.
The purpose of this utility model promptly provides a kind of solid-liquid separator, and it is without motor and back purge system, designs simplification, and the efficient height, price is low, and is easy to maintenance.
For reaching this purpose, the technical solution of the utility model is as follows: a kind of solid-liquid separator, it is characterized in that: shell 4 upper outside are connected with solid-liquid inlet connection 1, be provided with outer tube 2 in the shell 4, be provided with outlet pipe 3 in the outer tube 2,45 ° of inclined holes 11 and square hole 12 are arranged on the outer tube 2, one end of end socket 5 is connected with the gap location and the lower edge of square hole 12, the other end of end socket 5 is connected with shell 4, outer tube 2 feeds and reclaims chamber 13, reclaim in the chamber 13 and be provided with guide holder 7, three back-up block 8 support guide seats 7 that become 120 degree angles reclaim chamber 13 and communicate with solid outlet adapter 10, and outer tube 2 and 13 of chambers of recovery are connected to blast pipe 6, reclaim chamber 13 by end socket 9 sealings, 3 of shell 4 and outlet pipes are connected by last lower flange 14.
After adopting such scheme,, therefore saved the time of installing with maintenance because the utility model has been cancelled rotational components; Do not establish back purge system because of the utility model again, so do not need expensive spare part, and the utility model do not have when using and gets stuck, thus also with regard to do not need spare unit, total cost to equal same disposal ability existing separator 60%, price is low; In addition, the utility model efficient height, separating effect is obvious:
Contrast great in 7.0 gram per centimeters
3The solid particle separating effect reach 99.99% (diameter is greater than 80 μ m), as copper foam, steel foam, iron powder, lead powder foam etc.
Contrast great in 2.8 gram per centimeters
3The solid particle separating effect reach (diameter is greater than 80 μ m) more than 95%, as lime stone, the thin foam of glass etc.
Contrast great in 1.5 gram per centimeters
3The solid particle separating effect reach (diameter is greater than 80 μ m) more than 75%, as aluminium foam, concrete etc.
For little also can the separating of particle, if adopt double separating effect also fine.
For good greater than the particle separation effect spy of 80 μ m.
Below in conjunction with accompanying drawing the utility model is described in detail.
Fig. 1 is a structure chart of the present utility model.
Fig. 2 is a vertical view of the present utility model.
Fig. 3 is an outer tube expanded view of the present utility model.
Principle of the present utility model is different with liquid specific gravity according to solid in the solidliquid mixture, its acceleration of gravity and centrifugal force are different, thereby adopt the method for cyclonic separation, give mixture with initial velocity, the tangential direction charging, be allowed to condition in the device with fixing direction cyclonic separation, after the centrifugation, Separation of Solid and Liquid, the guiding of passing through artificial guide holder again leaves solid in the device bottom, flow out from outlet pipe after the fluid separation applications, the solid that has separated can be discharged in bottom of device, takes different whereabouts by solid kind difference, reclaims in this way and uses or refuse eliminating etc. again.
As Fig. 1, Fig. 2, shown in Figure 3, shell 4 upper outside of the present utility model are connected with solid-liquid inlet connection 1, be provided with outer tube 2 in the shell 4, be provided with outlet pipe 3 in the outer tube 2,45 ° of inclined holes 11 and square hole 12 are arranged on the outer tube 2, one end of end socket 5 is connected with the gap location and the lower edge of square hole 12, the other end of end socket 5 is connected with shell 4, outer tube 2 feeds and reclaims chamber 13, reclaim in the chamber 13 and be provided with guide holder 7, three back-up block 8 support guide seats 7 that become 120 degree angles, reclaim chamber 13 and communicate with solid outlet adapter 10, outer tube 2 and 13 of chambers of recovery are connected to blast pipe 6, reclaim chamber 13 by end socket 9 sealings, 3 of shell 4 and outlet pipes are connected by last lower flange 14, take over 1 and solid outlet during 3 of outlet pipes and solid-liquid are gone into and take over 10 and all be connected with flange.
The utility model middle external tube 2 tops are higher than solid-liquid inlet connection 1, solidliquid mixture enters 2 of shell 4 and outer tubes with certain initial velocity from solid-liquid inlet connection 1, and do centrifugal and gravitational motion betwixt, because solid is different with liquid specific gravity, its acceleration of gravity and centrifugal force are also different, again and 45 ° of inclined holes 11 on the outer tube 2 are penetrating outer tube 2 walls, 12 of square holes on the outer tube 2 penetrate outer tube 2 outer walls, outer tube 2 is a hollow extremely down from square hole 12 places, so liquid flows down from the space that inclined hole 11 enters 3 of outer tube 2 and outlet pipes, deposition of solid in space that end socket 5 and outer tube 2 and shell 4 are formed and in square hole 12 enters outer tube 2 walls sedimentation go into to reclaim chamber 13, the guide holder 7 that reclaims in the chamber 13 can make liquid upwards return sooner, to avoid that the solid of sedimentation is stirred impact, thereby outside guide holder 7 and outlet pipe 3 under the effect of pump, liquid is discharged from outlet pipe 3, reclaims the gap sedimentation of the solid self-supporting piece 8 of sedimentation in the chamber 13 and enters solid outlet and take over 10 discharges.Have vapour lock and gas in the utility model and disturb and influence cyclonic separation when the solid-liquid mixed feeding, so be provided with blast pipe 6, the gas in the blast pipe 6 can be discharged with liquid or antifouling hole.
The utility model can be according to the solid particle difference, promptly according to solid proportion difference and flow velocity difference, and internal components such as the inclined hole 11 of design different size and square hole 12.According to China's standardization series, the utility model adopts different series in the hope of wider application.
Pressure series: 0.1 0.25 0.6 1.0 1.6 2.5 4.0 6.4 (units MPa)
Specification series: DN50 80 100 150 200 250 300
350 400 450 500 600 800 100
1200?1400?1800?2000
Flow series: 235 10 20 50 100 ... 2000t/hr
Material selection of the present utility model is wide.
Through on probation, effect of the present utility model is obvious, and solid particle proportion is at 15g/cm
3Above all can disposablely separate.
Claims (1)
- A kind of solid-liquid separator, it is characterized in that: shell [4] upper outside is connected with solid-liquid inlet connection [1], be provided with outer tube [2] in the shell [4], be provided with outlet pipe [3] in the outer tube [2], 45 ° of inclined holes [11] and square hole [12] are arranged on the outer tube [2], one end of end socket [5] is connected with the gap location and the lower edge of square hole [12], the other end of end socket [5] is connected with shell [4], outer tube [2] feeds and reclaims chamber [13], reclaim in the chamber [13] and be provided with guide holder [7], three back-up block [8] support guide seats [7] that become 120 degree angles, reclaiming chamber [13] communicates with solid outlet adapter [10], outer tube [2] and reclaim between chamber [13] and be connected to blast pipe [6] reclaims chamber [13] by end socket [9] sealing, is connected by last lower flange [14] between shell [4] and outlet pipe [3].
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 99222638 CN2372035Y (en) | 1999-01-22 | 1999-01-22 | Solid-liquid separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 99222638 CN2372035Y (en) | 1999-01-22 | 1999-01-22 | Solid-liquid separator |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2372035Y true CN2372035Y (en) | 2000-04-05 |
Family
ID=34012989
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 99222638 Expired - Fee Related CN2372035Y (en) | 1999-01-22 | 1999-01-22 | Solid-liquid separator |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2372035Y (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101455909A (en) * | 2008-12-17 | 2009-06-17 | 济宁金百特工程机械有限公司 | Dregs and liquor separation device |
CN103241853A (en) * | 2013-05-24 | 2013-08-14 | 南京慧城水处理设备有限公司 | Field water source purifying equipment and method |
CN105026008A (en) * | 2013-02-05 | 2015-11-04 | 克劳德·拉瓦尔公司 | Centrifugal separation with extended post |
-
1999
- 1999-01-22 CN CN 99222638 patent/CN2372035Y/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101455909A (en) * | 2008-12-17 | 2009-06-17 | 济宁金百特工程机械有限公司 | Dregs and liquor separation device |
CN105026008A (en) * | 2013-02-05 | 2015-11-04 | 克劳德·拉瓦尔公司 | Centrifugal separation with extended post |
CN103241853A (en) * | 2013-05-24 | 2013-08-14 | 南京慧城水处理设备有限公司 | Field water source purifying equipment and method |
CN103241853B (en) * | 2013-05-24 | 2014-10-08 | 南京慧城水处理设备有限公司 | Field water source purifying equipment and method |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |