CN101402008A - Pressure feed liquid separation apparatus - Google Patents
Pressure feed liquid separation apparatus Download PDFInfo
- Publication number
- CN101402008A CN101402008A CNA2008102259481A CN200810225948A CN101402008A CN 101402008 A CN101402008 A CN 101402008A CN A2008102259481 A CNA2008102259481 A CN A2008102259481A CN 200810225948 A CN200810225948 A CN 200810225948A CN 101402008 A CN101402008 A CN 101402008A
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- filter core
- liquid separation
- pressure feed
- feed liquid
- separation apparatus
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- Apparatuses For Bulk Treatment Of Fruits And Vegetables And Apparatuses For Preparing Feeds (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention discloses a pressure feed liquid separation device, which belongs to a solid-liquid separation pretreatment device. The pressure feed liquid separation device adopts a technical proposal that the pressure feed liquid separation device comprises a filter core 1, and a liquid outlet 7 and a drive unit 6 which are fixedly connected with the filter core 1 and rotate on a coaxial line, wherein a cylindrical shell 2 which is provided with a feed opening 9 and a discharge opening 10 is hermetically connected with an end cover 4 through an end face to form a separator shell; the shaft diameter of the liquid outlet of the filter core 1 and an inner hole of the end cover 4 of the separator shell form rotary coupling through a bearing 5, wherein the shaft diameter and the inner hole are limited to perform axial displacement; a rotary seal 3 is arranged on the filter core 1 to form moving seal between the filter core 1 and the cylindrical shell 2; and a scraper 8 is arranged on the cylindrical shell 2 along the axial line; and relative sliding between the scraper 8 and the outer surface of the filter core 1 is maintained. The pressure feed liquid separation device is applied to pre-separation of partial liquid during the process of conveying solid-liquid mixture, so as to lighten the load of a last-stage solid-liquid separation device and improve the production efficiency.
Description
Technical field
The present invention relates to a kind of pressure feed liquid separation apparatus, belong to the Separation of Solid and Liquid pre-processing device; Its operation principle is: in the solidliquid mixture material course of conveying under pressure during the micropore filter element outer surface by rotation partially liq pass micropore and enter in normal pressure (or negative pressure) filter core and be discharged from, finish the separation of partially liq, rest materials by continuing to be transported to juice extractor behind the separator, is finished the final Separation of Solid and Liquid of predetermined crushing juice rate under pressure by juice extractor.
Technical background
A kind of large-scale production mode of China's agricultural byproducts place of production processing is that fruits and vegetables concentrate clear juice production; the main production process is: fruit immersion, conveying, selection, spray Cleaning for High Capacity, lifting, fragmentation, enzyme processing, squeezing, desanding, come unstuck, ultrafiltration, evaporation and concentration, pasteurization, sterile filling; product is that 65 ° of above fruits and vegetables of Bx concentrate clear juice; can preserve 1 year down by normal temperature; and intrinsic nutrition of raw material and local flavor have been kept; not containing any additives or anticorrisive agent, is natural green food.Squeezing is the solid-liquid separation technique critical process in the production process, fruits and vegetables are finished Separation of Solid and Liquid through the solidliquid mixture material after the crusher in crushing by cartridge type juice extractor squeezing process on the production line, the material treating capacity of juice extractor has determined the productivity ratio of whole production line, therefore in the course of conveying of solidliquid mixture material before entering juice extractor after the fragmentation the free juice of part is carried out pre-separation on the production line and will alleviate juice extractor squeezing load, enhance productivity.
Summary of the invention
The objective of the invention is to provide a kind of pressure feed liquid separation apparatus, is applied to the partially liq pre-separation in the solidliquid mixture material course of conveying, so that alleviate back level solid-liquid separating equipment load, enhances productivity.
Comprise in order to reach the technical scheme that purpose of the present invention takes: the liquid outlet 7 and the drive unit 6 of filter core 1 and coaxial line rotation that is connected with it, the cartridge type housing 2 that is provided with charging aperture 9 and discharging opening 10 is by end face and the end cap 4 formation separator shell that is tightly connected, the liquid outlet diameter of axle of filter core 1 is limited the rotation-coupled of axial displacement by the bearing 5 and the endoporus formation of separator shell end cap 4, rotatory sealing 3 is installed in the movable sealing that forms on the filter core 1 between filter core 1 and the cartridge type housing 2, scraper plate 8 is installed in the relative slip that keeps on the cartridge type housing 2 with filter core 1 outer surface along axis, constitutes pressure rotating liquid separator (as Fig. 1).Power drives filter core 1 by drive unit 6 and rotates in separator shell, the solidliquid mixture material that is broken is moved, is discharged by discharging opening 10 by the passage that charging aperture 9 is gone into, formed along the outer surface and cartridge type housing 2 inner surfaces of filter core 1 under pressure, the micropore that material partially liq by pressure feed liquid separation apparatus the time passes filter core 1 enters in the filter core and is discharged from by liquid outlet 7, scraper plate 8 can be removed the material attached to the filter core outer surface, and rotatory sealing 3 can prevent that material unloads in the course of conveying outward.
In the above-mentioned pressure feed liquid separation apparatus, can be by changing the material outlet resistance, the pre-separation amount of control solidliquid mixture material liquid the time by pressure feed liquid separation apparatus.
In the above-mentioned pressure feed liquid separation apparatus, forward separating feed mouth 9, discharging opening 10 can exchange, and change reverse separating feed mouth 10, discharging opening 9 into, as shown in Figure 2.
In the above-mentioned pressure feed liquid separation apparatus, scraper plate 8 can be set to 1,2 or 3 according to filter core diameter d and material characteristic.
In the above-mentioned pressure feed liquid separation apparatus, the separating area of filter core 1 determines that by filter core diameter d, length L stripe shape hole (as F among Fig. 1) along the circumferential direction is set on the filter core, and it is the feed separation parameter that stripe shape pore width δ is called filter core micropore aperture; By changing filter core diameter d, rotation speed n, defeated material gap c and material and same material different conveying capacity and the liquid pre-separation amount of filter core micropore aperture δ to adapt to different qualities.
Description of drawings
Fig. 1 is the pressure feed liquid separation apparatus fundamental diagram.
Fig. 2 changes input and output material direction fundamental diagram for pressure feed liquid separation apparatus.
Fig. 3 is pressure feed liquid separation apparatus fundamental diagram on the Separation of Solid and Liquid production line.
Specific embodiments
With reference to the accompanying drawings embodiments of the invention are described below.
Pressure feed liquid separation apparatus fundamental diagram shown in Figure 1, the solidliquid mixture material that has been broken is moved, is discharged the back by discharging opening 10 and continued to carry by the passage that charging aperture 9 is gone into, formed along the outer surface and housing 2 inner surfaces of filter core 1 under pressure, the material micropore that partially liq passes filter core 1 during by pressure feed liquid separation apparatus in the pressure course of conveying enters in the filter core and is discharged from by liquid outlet 7, finishes the pre-separation of partially liq from be transferred material; Because outer power rotates in separator shell by drive unit 6 driving filter cores 1 separately, the relative slip of outer surface of scraper plate 8 and filter core, can remove material attached to the filter core outer surface, be beneficial to fluid separation applications and prevent to stop up filter core, rotatory sealing 3 is to the sealing of the circumferential pressure between filter core 1 and the cartridge type housing 2, can prevent that material unloads in the course of conveying outward.By changing filter core diameter d, length L, rotation speed n, defeated material gap c and material and the same material different conveying capacity of filter core micropore aperture δ, can control the pre-separation amount of solidliquid mixture material liquid the time by pressure feed liquid separation apparatus by changing the material outlet resistance to adapt to different qualities.
Pressure feed liquid separation apparatus shown in Figure 3 is fundamental diagram on the Separation of Solid and Liquid production line, the solidliquid mixture material is built pressure by screw pump B after fruit or the vegetables process disintegrating machine A fragmentation, be delivered to the charging aperture 9 of pressure feed liquid separation apparatus C, in the solidliquid mixture material course of conveying under pressure during filter core 1 outer surface by rotation partially liq pass micropore and enter in normal pressure (or negative pressure) filter core and be discharged from, finish the pre-separation of partially liq, rest materials is continued on to juice extractor D by separator discharging opening 10 backs under pressure, is finished the final Separation of Solid and Liquid of predetermined crushing juice rate by juice extractor.Partially liq had been alleviated the live load of juice extractor by pre-separation when the solidliquid mixture material passed through pressure feed liquid separation apparatus in course of conveying, had improved productivity ratio.
Claims (4)
1, pressure feed liquid separation apparatus comprises: the liquid outlet 7 and the drive unit 6 of filter core 1 and coaxial line rotation that is connected with it, it is characterized in that, the cartridge type housing 2 that is provided with charging aperture 9 and discharging opening 10 is by end face and the end cap 4 formation separator shell that is tightly connected, the liquid outlet diameter of axle of filter core 1 is limited the rotation-coupled of axial displacement by the bearing 5 and the endoporus formation of separator shell end cap 4, rotatory sealing 3 is installed in the movable sealing that forms on the filter core 1 between filter core 1 and the cartridge type housing 2, scraper plate 8 is installed in the relative slip that keeps on the cartridge type housing 2 with filter core 1 outer surface along axis, the solidliquid mixture material that is broken is gone into by charging aperture 9 under pressure, move along the outer surface of filter core 1 and the passage of cartridge type housing 2 inner surfaces formation, discharged by discharging opening 10, the micropore that material partially liq by pressure feed liquid separation apparatus the time passes filter core 1 enters in the filter core and is discharged from by liquid outlet 7.
2, pressure feed liquid separation apparatus according to claim 1 is characterized in that, can be by changing the material outlet resistance, the pre-separation amount of control solidliquid mixture material liquid by pressure feed liquid separation apparatus the time.
3, pressure feed liquid separation apparatus according to claim 1 is characterized in that, forward separating feed mouth 9, discharging opening 10 can exchange, and changes reverse separating feed mouth 10, discharging opening 9 into.
4, pressure feed liquid separation apparatus according to claim 1 is characterized in that, scraper plate 8 can be set to 1,2 or 3 according to filter core diameter d and material characteristic.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008102259481A CN101402008B (en) | 2008-11-07 | 2008-11-07 | Pressure feed liquid separation apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008102259481A CN101402008B (en) | 2008-11-07 | 2008-11-07 | Pressure feed liquid separation apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101402008A true CN101402008A (en) | 2009-04-08 |
| CN101402008B CN101402008B (en) | 2012-05-23 |
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ID=40536256
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2008102259481A Expired - Fee Related CN101402008B (en) | 2008-11-07 | 2008-11-07 | Pressure feed liquid separation apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101402008B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111228874A (en) * | 2020-03-25 | 2020-06-05 | 深圳市怡盛源净水产业有限公司 | Water purifier convenient to it is clean |
-
2008
- 2008-11-07 CN CN2008102259481A patent/CN101402008B/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111228874A (en) * | 2020-03-25 | 2020-06-05 | 深圳市怡盛源净水产业有限公司 | Water purifier convenient to it is clean |
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| Publication number | Publication date |
|---|---|
| CN101402008B (en) | 2012-05-23 |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120523 Termination date: 20131107 |