CN2038028U - Helical discharge sedimentation-type centrifuge - Google Patents
Helical discharge sedimentation-type centrifuge Download PDFInfo
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- CN2038028U CN2038028U CN 88220437 CN88220437U CN2038028U CN 2038028 U CN2038028 U CN 2038028U CN 88220437 CN88220437 CN 88220437 CN 88220437 U CN88220437 U CN 88220437U CN 2038028 U CN2038028 U CN 2038028U
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- rotary drum
- liquid
- discharge sedimentation
- liquid phase
- centrifuge
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Abstract
The utility model discloses a helical discharge sedimentation-type centrifuge, and relates to a centrifuge with a helical rotary drum. The helical discharge sedimentation-type centrifuge is that the big end cover of the column-conical rotary drum is provided with double-layer liquid outlets. One layer is provided with overflow liquid outlets with large outlet diameter, and the other layer is provided with throttling liquid outlets which control liquid flow amount and are filled with liquid. The helical discharge sedimentation-type centrifuge can effectively separate three-phase mixture of light liquid-heavy liquid-solid, and can also effectively separate suspension liquid whose grain diameters are widespread into three kinds of material flow. The utility model has the advantages of simple structure, convenient manufacture.
Description
The present invention relates to centrifuge, specially refer to the centrifuge of rotary rotating cylinder.
Spiral discharge sedimentation centrifuge is a kind of good to material adaptability, the continuous centrifuge that range of application is wider.The LW-450 type horizontal spiral discharge sedimentation centrifuge that Shanghai chemical produces discloses the structure of this type.It is by the rotary drum belt pulley, the differential belt pulley, differential mechanism, charge pipe, casing with two kinds of material outlet pipelines is contained in the rotary drum that has mud hole of two parts ┈ outsides of circling round on the base bearing and the inner auger conveyor with spiral blade with one heart and constitutes.Rotary drum is by the big end cap that has spout hole, and little end cap and cylinder ┈ conical rotor drum cylindrical shell constitute.Motor drives rotary drum belt pulley and differential belt pulley by V belt, utilizes differential mechanism to make rotary drum and auger conveyor do to rotate in the same way, but has speed discrepancy between them, and revolutional slip is 0.2-3%.Suspension adds in the rotary drum from charge pipe continuously, under the centrifugal action of drum rotating, form a ring-shaped pool in the rotary drum, solids are formed sediment to the drum inner wall face and are got rid of sediment outlet into casing by the afterbody that the blade on the auger conveyor is pushed to rotary drum from mud hole by centrifugal sedimentation.The spout hole that is provided with on the big end cap of rotary drum can be derived clarified solution and enter the clear liquid outlet of casing, thereby reaches the purpose of separate out suspended liquid.When needs separate the suspension of some particle diameter distribution wide (from several microns to tens microns even several millimeters), not only bulky grain to be formed sediment, and will some particular requirement liquid be divided into " weight " liquid phase and concentrated " gently " liquid phase two parts of fine grained that coarse granule is concentrated, here " weight " and " gently " is not that the difference of specific gravity of liquid itself causes, but because the different caused apparent specific gravities of liquid endoparticle thickness degree (or claiming apparent specific gravity (gd)) difference is caused.Generally speaking, when adopting spiral discharge sedimentation centrifuge to operate, centrifuge is rotated at a high speed, separating factor is greater than 3000G, " gently " liquid phase and " weight " liquid phase could there be one " layering " significantly, " gently " liquid phase is overflowed from spout hole, and " weight " liquid phase is discharged from slag-drip opening with oarse-grained sediment.This lock out operation need consume more energy.When " weight " liquid phase of separating needs further to handle, be the higher underflow of water capacity often, cause the difficulty in the transportation because of what separate; Just can handle but also its further dilution will be removed the bulky grain sediment that is mingled in wherein.
The objective of the invention is to avoid above-mentioned weak point of the prior art and provide a kind of energy consumption lower, the novel centrifugal machine that can the suspension that particle diameter distribution is wider be separated into satisfactory " gently " liquid phase ┈ " weight " liquid phase ┈ sediment simple in structure.
Purpose of the present invention can realize by following technical measures: by the rotary drum belt pulley, and differential belt pulley, casing, charge pipe has in the spiral discharge sedimentation centrifuge that the rotary drum of mud hole and auger conveyor constitute, and rotary drum is by big end cap, little end cap, cylinder ┈ conical rotor drum cylindrical shell is formed.On big end cap, double-deck outage is set.That is to say: the radial direction along big end cap is provided with the bigger draining overflow hole in one or more apertures near rotating shaft, for concentrated " gently " liquid phase overflow discharge opeing of fine grained; And the throttling outage of the less control flow in one or more apertures is set between spout hole and big end cap edge, and " weight " liquid phase that coarse granule is concentrated is full of throttle orifice and discharge opeing, and its flow is subjected to the limited aperture of throttling outage.The pore size in these two kinds of holes and " gently ", " weight " liquid phase flow are relevant.Bernoulli's equation in the available stream mechanics is tried to achieve.
Motor drives rotary drum and the equidirectional rotation of auger conveyor by two belt pulleys, and their revolutional slip is 0.2-3%.When the wider suspension of particle diameter distribution entered rotary drum continuously from charge pipe after, because the centrifugal action of rotary drum, suspension was divided into three layers very soon.The bulky grain sediment nestles up drum inner wall, and auger conveyor constantly rotation constantly scrapes and discharge rotary drum with sediment, discharges from the pipeline of slagging tap of casing." weight " liquid phase that coarse granule is concentrated is between drum inner wall and " gently " liquid phase, and " weight " liquid phase is full of the throttling outage and also constantly enters casing from throttle orifice, limited aperture flow, from the coarse granule suspension pipeline of casing, discharge." gently " liquid phase that fine grained is concentrated occupies the innermost layer of the interior liquid pool of rotary drum, and overflow from draining overflow hole and going out is discharged from the fine grained suspension pipeline of casing.Reached the purpose of suspension three phase separation.
Sometimes in order to prevent that " gently " liquid phase and " weight " liquid phase from mixing, annular baffle is set in the inboard of end cap greatly.
The present invention also can be used to handle the three-phase mixture of the different light liquid ┈ heavy-fluid ┈ solid phase of proportion.Also be applicable to the vertical helical discharging sedimentation centrifuge.
Compared with prior art utilize the present invention to handle the wide suspension of particle diameter distribution, do not need very high separating factor, test shows that separating factor is that 2500G just can be separated into the bulky grain sediment with this suspension effectively, " gently " liquid phase three parts that " weight " liquid phase that coarse granule is concentrated and fine grained are concentrated.And " weight " liquid phase does not form underflow, convenient transportation when further handling.Structure of the present invention is also simpler, and is easy to make.
Below in conjunction with accompanying drawing embodiments of the invention are described
Fig. 1 is the front view of spiral discharge sedimentation centrifuge of the present invention
Fig. 2 is the big end cap part enlarged drawing of present embodiment
Spiral discharge sedimentation centrifuge is by differential belt pulley (1), rotary drum belt pulley (2), and differential mechanism (3), bearing (4), casing (5), auger conveyor (6), rotary drum (7), charge pipe (8) constitutes.Rotary drum (7) is installed on a pair of base bearing (4) with one heart with auger conveyor (6).Rotary drum (7) is then by big end cap (9), and little end cap (10) and rotary drum body (11) are formed.
A certain suspension contains the sediment of 2-4 millimeter, the big or small uneven grain of 2-30 micron.This suspension is sent in the rotary drum (7) continuously by charge pipe (8).Motor is by differential belt pulley (1), and rotary drum belt pulley (2) drives rotary drum (7) and the equidirectional rotation of auger conveyor (6), and to make the revolutional slip of rotary drum (7) and auger conveyor (6) by differential mechanism (3) be 0.2-3%.
On the radial direction of big end cap (9), draining overflow hole (12) is set near the internal layer ┈ rotating shaft, the aperture is the 40-50 millimeter, and communicates with apocenosis passage (13).Between the edge of outer ┈ draining overflow hole (12) and big end cap (9) throttling outage (14) is set, the aperture is the 5-6 millimeter, and communicates with apocenosis passage (15).
Enter the suspension behind the rotary drum (7), because the effect of the rotary centrifugal force of rotary drum (7).The bulky grain sediment of 2-4 millimeter is near the inwall of rotary drum (7), and by auger conveyor (6) it constantly scraped, and entered the sediment outlet (17) of casing (5) by the scum hole (16) of rotary drum (7)." gently " liquid phase that the fine grained of 1-4 micron is concentrated occupies the innermost layer of the interior liquid pool of rotary drum (7), and process discharge outage (12) and apocenosis passage (13) overflow enter the fine grained suspension outlet (18) of casing (5)." weight " liquid phase that the coarse granule of 4-30 micron is concentrated is between the inwall and " gently " liquid phase of rotary drum (7), and be full of throttling outage (14), its flow is subjected to the limited aperture of throttling outage (14), and " weight " liquid phase enters the coarse granule suspension outlet (19) of casing (5) through apocenosis passage (15) and throttling outage (14) throttling.So far, above-mentioned suspension is separated into the fine grained suspension of 1-4 micron; The coarse granule suspended phase of 4-30 micron and the bulky grain sediment of 1-4 millimeter have reached the purpose of separating.
Claims (1)
- Spiral discharge sedimentation centrifuge, has differential belt pulley (1), rotary drum belt pulley (2), differential mechanism (3), bearing (4), casing (5), auger conveyor (6), rotary drum (7) and charge pipe (8) is characterized in that, on big end cap (9), be provided with one or more holes, also be provided with one or more holes as the throttling discharge opeing of controlling flow as the overflow discharge opeing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 88220437 CN2038028U (en) | 1988-12-06 | 1988-12-06 | Helical discharge sedimentation-type centrifuge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 88220437 CN2038028U (en) | 1988-12-06 | 1988-12-06 | Helical discharge sedimentation-type centrifuge |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2038028U true CN2038028U (en) | 1989-05-24 |
Family
ID=4852666
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 88220437 Withdrawn CN2038028U (en) | 1988-12-06 | 1988-12-06 | Helical discharge sedimentation-type centrifuge |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2038028U (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100393423C (en) * | 2003-04-22 | 2008-06-11 | 维斯科特尔姆股份公司 | Centrifuge comprising hydraulic differential speed determination |
| CN102292160A (en) * | 2008-12-30 | 2011-12-21 | 阿尔法拉瓦尔股份有限公司 | A decanter centrifuge with a slide valve body |
| CN101980789B (en) * | 2008-03-28 | 2012-06-20 | 安德里兹分离有限公司 | Screen bowl centrifuge |
| CN102941165A (en) * | 2012-11-26 | 2013-02-27 | 浙江天宇环保设备有限公司 | Primary solid-phase outlet device of centrifugal solid-liquid separators |
| CN102941162A (en) * | 2012-11-26 | 2013-02-27 | 浙江天宇环保设备有限公司 | Centrifugal solid-liquid separator |
| CN102271819B (en) * | 2008-12-30 | 2013-10-16 | 阿尔法拉瓦尔股份有限公司 | A decanter centrifuge and a decanter centrifuge discharge port member |
| CN103586142A (en) * | 2013-11-15 | 2014-02-19 | 上海普锐通实业有限公司 | Horizontal type spiral sedimentation three-phase separation centrifugal machine |
| CN117861875A (en) * | 2024-03-12 | 2024-04-12 | 菏泽学院 | Centrifugal equipment is used in preparation of plant growth regulator |
-
1988
- 1988-12-06 CN CN 88220437 patent/CN2038028U/en not_active Withdrawn
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100393423C (en) * | 2003-04-22 | 2008-06-11 | 维斯科特尔姆股份公司 | Centrifuge comprising hydraulic differential speed determination |
| CN101980789B (en) * | 2008-03-28 | 2012-06-20 | 安德里兹分离有限公司 | Screen bowl centrifuge |
| CN102292160A (en) * | 2008-12-30 | 2011-12-21 | 阿尔法拉瓦尔股份有限公司 | A decanter centrifuge with a slide valve body |
| CN102271819B (en) * | 2008-12-30 | 2013-10-16 | 阿尔法拉瓦尔股份有限公司 | A decanter centrifuge and a decanter centrifuge discharge port member |
| CN102292160B (en) * | 2008-12-30 | 2013-10-30 | 阿尔法拉瓦尔股份有限公司 | Decanter centrifuge with slide valve body |
| CN102941165A (en) * | 2012-11-26 | 2013-02-27 | 浙江天宇环保设备有限公司 | Primary solid-phase outlet device of centrifugal solid-liquid separators |
| CN102941162A (en) * | 2012-11-26 | 2013-02-27 | 浙江天宇环保设备有限公司 | Centrifugal solid-liquid separator |
| CN102941162B (en) * | 2012-11-26 | 2015-04-22 | 浙江天宇环保设备有限公司 | Centrifugal solid-liquid separator |
| CN102941165B (en) * | 2012-11-26 | 2015-06-17 | 浙江天宇环保设备有限公司 | Primary solid-phase outlet device of centrifugal solid-liquid separators |
| CN103586142A (en) * | 2013-11-15 | 2014-02-19 | 上海普锐通实业有限公司 | Horizontal type spiral sedimentation three-phase separation centrifugal machine |
| CN117861875A (en) * | 2024-03-12 | 2024-04-12 | 菏泽学院 | Centrifugal equipment is used in preparation of plant growth regulator |
| CN117861875B (en) * | 2024-03-12 | 2024-05-17 | 菏泽学院 | Centrifugal equipment is used in preparation of plant growth regulator |
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| C06 | Publication | ||
| PB01 | Publication | ||
| 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 |