CN102631995A - Continuous centrifugal separating device for materials - Google Patents
Continuous centrifugal separating device for materials Download PDFInfo
- Publication number
- CN102631995A CN102631995A CN2012101362424A CN201210136242A CN102631995A CN 102631995 A CN102631995 A CN 102631995A CN 2012101362424 A CN2012101362424 A CN 2012101362424A CN 201210136242 A CN201210136242 A CN 201210136242A CN 102631995 A CN102631995 A CN 102631995A
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- Prior art keywords
- basin body
- dynamic
- continuous centrifugal
- packing
- separation
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- 239000000463 material Substances 0.000 title claims abstract description 50
- 238000000926 separation method Methods 0.000 claims abstract description 76
- 238000007789 sealing Methods 0.000 claims abstract description 29
- 230000003068 static effect Effects 0.000 claims abstract description 29
- 238000012856 packing Methods 0.000 claims description 37
- 239000007963 capsule composition Substances 0.000 claims description 5
- 230000008676 import Effects 0.000 claims description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 3
- 239000000741 silica gel Substances 0.000 claims description 3
- 229910002027 silica gel Inorganic materials 0.000 claims description 3
- 238000001035 drying Methods 0.000 abstract description 12
- 239000002002 slurry Substances 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 235000016709 nutrition Nutrition 0.000 abstract description 2
- 230000004071 biological effect Effects 0.000 abstract 1
- 238000007599 discharging Methods 0.000 abstract 1
- 239000004615 ingredient Substances 0.000 abstract 1
- 239000007788 liquid Substances 0.000 description 13
- 239000007787 solid Substances 0.000 description 9
- 238000005119 centrifugation Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 230000007246 mechanism Effects 0.000 description 4
- 238000009825 accumulation Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000011344 liquid material Substances 0.000 description 2
- 238000007790 scraping Methods 0.000 description 2
- 239000011343 solid material Substances 0.000 description 2
- 206010017389 Frotteurism Diseases 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 235000015203 fruit juice Nutrition 0.000 description 1
- 235000012055 fruits and vegetables Nutrition 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000002372 labelling Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000000050 nutritive effect Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000000306 recurrent effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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Abstract
The invention discloses a continuous centrifugal separating device for materials. The continuous centrifugal separating device comprises a static separating basin body, a dynamic separating basin body and a dynamic sealing device, wherein the dynamic separating basin body is coaxially arranged in the static separating basin body; the opening ends of both basin bodies are matched with the dynamic sealing device in a sealing way; a feeding end is matched with a delivering device; and a discharging tube is arranged at the bottom of the rear end of the static separating basin body. A horizontal structure is adopted by the continuous centrifugal separating device for materials and a material dispersing device is used together, so that the materials are centrifugally separated after being fully dispersed and the separated materials are synchronously discharged. The continuous centrifugal separating device for materials is compact in structure, is stable and reliable in operation and is especially suitable for the online continuous centrifugal separation of slurry materials. The continuous centrifugal separating device for materials can be matched with a vacuum device for realizing the separation and drying under a negative pressure state; the separation and drying can be continuously completed at one time; the production cost is greatly reduced; the storage for the biological activity of material nutritional ingredients is boosted; and the quality of biological products is improved.
Description
Technical field
The invention belongs to the separation technical field of drying, be specifically related to a kind of compact conformation, stable and reliable operation is particularly suitable for the material continuous centrifugal separation device that biological products are processed.
Background technology
In the processing of the production process, particularly modern biological product that separate, drying is chemical technology field necessity, separation is indispensable operation with drying.Centrifugation is one of isolation technics commonly used, and the separating effect effect is single centrifugal force, and separative efficiency is low, and especially to the thick slurry material of thickness, the centrifugal separation equipment of prior art is the separating effect that is difficult to reach desirable.Common drying mode all needs heating mostly, and superheated is damaged the active ingredient of biological products, does not hope to take place.In the fruit and vegetable food deep processing, need separate and drying such as the processing fruit drink, fruit juice slurry viscosity is than higher; Dehydration is difficulty relatively, and still moisture content is higher after the centrifugation, has brought bigger difficulty for follow-up drying; Conventional drying needs heating, causes loss of nutritive components.And not only separate, drying belongs to two discontinuous operations, and separates with drying each operation itself and can not accomplish continuously, greatly reduces production efficiency.For this reason, developing a kind of material continuous centrifugal separation device of working continuously can realized, is very favorable to the deep processing of biological products.
Summary of the invention
The object of the present invention is to provide a kind of compact conformation, stable and reliable operation material continuous centrifugal separation device.
The objective of the invention is to realize like this; Comprise static separation basin body, Dynamic Separation basin body, dynamic sealing means; Described Dynamic Separation basin body is coaxial to be arranged in the static separation basin body, and the two openend and dynamic sealing means are sealed and matched, and feed end cooperates with feeding device; Bottom, described static separation basin body rear end is provided with discharge nozzle.
The present invention adopts horizontal type structure, cooperates the dispersal device of material, centrifugalizes after material is fully disperseed again.Liquid material after the separation gets into the feed liquid separation bin, and flows out from the static separation basin bottom, and solid material is derived through the gravitational equilibrium bleeder valve automatically, has realized the slurry Dynamic Separation under the continuously defeated material state, self-emptying.Compact conformation of the present invention, working stability is reliable, is particularly suitable for thick slurry material on-line continuous centrifugation.Can be supporting with vacuum plant, realize separating under the negative pressure state dry; Separating drying can one-time continuous accomplish, and reduces production costs greatly, helps preserving the biologically active of material nutritional labeling, improves the biological products quality.
Description of drawings
Fig. 1 is an overall structure sketch map of the present invention;
Fig. 2 is the right view of Fig. 1;
Among the figure: 1-static separation basin body, 2-Dynamic Separation basin body, 3-dynamic seal (packing) door, 4-spoiler, 5-flow-guiding channel; 6-material diversion seat, 7-fixed pressure ring, 8-dynamic seal (packing) ring, 9-static sealing ring, 10-gravitational equilibrium bleeder valve; The 11-pedestal, 12-feed liquid separation bin, 13-filter screen, 14-observation window, 15-discharge nozzle; The 16-mechanical seal ring, the dynamic basin body base of 17-, the static basin body base of 18-, 19-dispersal device, 20-door lock mechanism.
The specific embodiment
Below in conjunction with accompanying drawing the present invention is further described, but never in any form the present invention is limited, any conversion based on training centre of the present invention is done all falls into protection scope of the present invention.
As shown in Figure 1; The present invention includes static separation basin body 1, Dynamic Separation basin body 2, dynamic sealing means; Described Dynamic Separation basin body 2 coaxial being arranged in the static separation basin body 1, the two openend and dynamic sealing means are sealed and matched, and feed end cooperates with feeding device; Bottom, described static separation basin body 1 rear end is provided with discharge nozzle 15.
As preferred implementation:
Described dynamic sealing means comprises dynamic seal (packing) door 3, dynamic seal (packing) assembly and static sealing assembly; Described dynamic seal (packing) assembly is for to be fixed in the dynamic seal (packing) ring 8 on the dynamic seal (packing) door 3 through fixed pressure ring 7, and dynamic seal (packing) ring 8 is corresponding to Dynamic Separation basin body 2; Described static sealing assembly is the static sealing ring 9 that is arranged on the dynamic seal (packing) door 3, and static sealing ring 9 is corresponding to static separation basin body 1.
Described dynamic seal (packing) ring 8 is a capsule formula sealing ring, and the import or export of blister cavities is communicated with the circulatory system of working media.
The present invention has adopted the dynamic seal (packing) ring 8 of capsule formula structure, and this sealing ring is generally heat-proof silica gel and processes, and the cross section is " Ω " shape, is fixed on the dynamic seal (packing) door 3 through two limits of fixed pressure ring 7 with " Ω ", and tube chamber is provided with the import and the outlet of working media.Owing to be dynamic seal (packing); Dynamic Separation basin body 2 with expand after dynamic seal (packing) ring 8 be in rotation, Frotteurism at a high speed, therefore, the working media of importing should be can heat conduction medium; And should be recurrent state, so just can at any time frictional heat be taken away.What working media was the most frequently used is water, can make different selections according to the hygienic requirements of different field with the cooling needs.The working media entrance point of blister cavities connects circulating pump, and the port of export is provided with flow valve, and two ends cooperate makes the cavity of dynamic seal (packing) ring 8 receive compression swelling, realizes the dynamic seal (packing) with Dynamic Separation basin body 2.Have only between Dynamic Separation basin body 2 and the dynamic seal (packing) door 3 to seal reliably, Dynamic Separation basin body 2 inner chambers and feed liquid separation bin 12 are only separate space, otherwise can't realize reliable Separation of Solid and Liquid.And after the dynamic seal (packing), guarantee that the negative pressure operating mode is better, can improve the operating efficiency of equipment.The arc top of dynamic seal (packing) ring 8 " Ω " structure is for structure thicker, and is more wear-resisting like this.
Described static sealing ring 9 is rubber or silica gel.
On the described dynamic seal (packing) door 3 observation window 14 is set, in the described observation window 14 illuminating lamp is set.
The center of described dynamic seal (packing) door 3 is provided with material diversion seat 6, and material diversion seat 6 tops are provided with spoiler 4, and the flow-guiding channel 5 of the dried material in the ABC of wall of vertical perforation and extension is set in the spoiler 4 below material diversion seats 6; The port of export of described flow-guiding channel 5 is provided with gravitational equilibrium bleeder valve 10, and the two is rotatably assorted through central pin shaft.
After the Separation of Solid and Liquid, liquid partly gets into feed liquid separation bin 12, and solid portion is deposited on the filter screen 13 in the Dynamic Separation basin body 2, and progressively increases; Rotation along with Dynamic Separation basin body 2; After the solid portion accumulation reaches the height of spoiler 4; Fallen into the flow-guiding channel 5 in the material diversion seat 6 by scraping, form at gravitational equilibrium bleeder valve 10 places and pile up, after accumulating amount surpasses gravitational equilibrium bleeder valve 10 balance limits, overturn; Gu shape is partly discharged, gravitational equilibrium bleeder valve 10 automatically resets afterwards.This is provided with and can makes solid portion and liquid part discharge centrifugal separation equipment synchronously, realizes working continuously.
Described spoiler 4 tilts 0 ~ 10 ° to Dynamic Separation basin body 2 direction of rotation.
Described material diversion seat 6 outsides are the tower taper, and its cone-apex angle is 120 ~ 150 °.
Snapping dispersal device 19 on the dynamic basin body base 17 in the described Dynamic Separation basin body 2 is provided with pod apertures on the outer cover of described dispersal device 19.Dispersal device is set is and broken up when making material get into Dynamic Separation basin body 2, especially for sticky material, it is very big for follow-up centrifugation influence to break up operation.
Described Dynamic Separation basin body 2 comprises basin body and the filter screen 13 that is arranged in the basin body.This setting makes Dynamic Separation basin body 2 replaceable filter screens 13, has improved practicality of the present invention, promptly can change the filter screen 13 in different apertures as required.
Fig. 2 shows Facad structure of the present invention, and its dynamic seal (packing) door 3 is laterally opened hinge arrangement, and a side is provided with door lock mechanism 20, and described door lock mechanism 20 is a bearing pin pintle hook lock structure.
The operation principle of the present invention and the course of work:
The present invention adopts horizontal type structure, cooperates the dispersal device 19 of material, centrifugalizes after material is fully disperseed again.Liquid material after the separation gets into feed liquid separation bin 12, and flows out from static separation basin body 2 bottoms, and solid material is derived through gravitational equilibrium bleeder valve 10 automatically, has realized the slurry Dynamic Separation under the continuously defeated material state, self-emptying.
Use when of the present invention, close dynamic seal (packing) door 3 earlier, through door lock mechanism 20 lockings; Static sealing ring 9 compresses under the pressure effect of dynamic seal (packing) door 3, realizes static sealing.Upper level mass transport electric motor starting starts the working media circulating pump of dynamic seal (packing) ring 8 after 5 seconds; Import working media in the capsule formula sealing ring; Capsule formula sealing ring expands; Realize dynamic seal (packing) ring 8 and 2 dynamic seal (packing)s of Dynamic Separation basin body, Dynamic Separation basin body 2 becomes independently environment with feed liquid separation bin 12 like this.At this moment material gets in the Dynamic Separation basin body 2, through dispersal device 19 time, is disperseed, and the material after the dispersion is under action of centrifugal force, and the liquid part gets into feed liquid separation bin 12 fast through filter screen 13, is derived by discharge nozzle 15; Solid portion is deposited on Dynamic Separation basin body 2 inwalls and rotation thereupon; When solid portion is stacked into the height of spoiler 4; Fallen into flow-guiding channel 5 by scraping, pile up at gravitational equilibrium bleeder valve 10 places, when accumulation reach a certain amount of after gravitational equilibrium bleeder valve 10 overturn; Solid portion is derived, and gravitational equilibrium bleeder valve 10 resets afterwards.By above-mentioned course of work operation, material is by high efficiency separation, and solid and liquid part are discharged synchronously.
Claims (10)
1. material continuous centrifugal separation device; It is characterized in that: comprise static separation basin body (1), Dynamic Separation basin body (2), dynamic sealing means; Described Dynamic Separation basin body (2) is coaxial to be arranged in the static separation basin body (1); The two openend and dynamic sealing means are sealed and matched, and feed end cooperates with feeding device; Bottom, described static separation basin body (1) rear end is provided with discharge nozzle (15).
2. material continuous centrifugal separation device according to claim 1; It is characterized in that: described dynamic sealing means comprises dynamic seal (packing) door (3), dynamic seal (packing) assembly and static sealing assembly; Described dynamic seal (packing) assembly is for to be fixed in the dynamic seal (packing) ring (8) on the dynamic seal (packing) door (3) through fixed pressure ring (7), and dynamic seal (packing) ring (8) is corresponding to Dynamic Separation basin body (2); Described static sealing assembly is for to be arranged at the static sealing ring (9) on the dynamic seal (packing) door (3), and static sealing ring (9) is corresponding to static separation basin body (1).
3. material continuous centrifugal separation device according to claim 2 is characterized in that: described dynamic seal (packing) ring (8) is a capsule formula sealing ring, and the import or export of blister cavities is communicated with the circulatory system of working media.
4. material continuous centrifugal separation device according to claim 2 is characterized in that: described static sealing ring (9) is rubber or silica gel.
5. material continuous centrifugal separation device according to claim 2 is characterized in that: observation window (14) is set on the described dynamic seal (packing) door (3), and described observation window is provided with illuminating lamp in (14).
6. according to claim 2 or 5 described material continuous centrifugal separation devices; It is characterized in that: the center of described dynamic seal (packing) door (3) is provided with material diversion seat (6); Material diversion seat (6) top is provided with spoiler (4), and the flow-guiding channel (5) of the dried material in the ABC of wall of vertical perforation and extension is set in spoiler (4) the below material diversion seat (6); The port of export of described flow-guiding channel (5) is provided with gravitational equilibrium bleeder valve (9), and the two is rotatably assorted through central pin shaft.
7. material continuous centrifugal separation device according to claim 6 is characterized in that: described spoiler (4) tilts 0 ~ 10 ° to Dynamic Separation basin body (2) direction of rotation.
8. material continuous centrifugal separation device according to claim 6 is characterized in that: described material diversion seat (6) outside is the tower taper, and its cone-apex angle is 120 ~ 150 °.
9. material continuous centrifugal separation device according to claim 1 and 2; It is characterized in that: the dynamic basin body base (17) in the described Dynamic Separation basin body (2) is gone up snapping dispersal device (19), on the outer cover of described dispersal device (19) pod apertures is set.
10. material continuous centrifugal separation device according to claim 1 and 2 is characterized in that: described Dynamic Separation basin body (2) comprises basin body and the filter screen (13) that is arranged in the basin body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201210136242 CN102631995B (en) | 2012-05-04 | 2012-05-04 | Continuous centrifugal separating device for materials |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201210136242 CN102631995B (en) | 2012-05-04 | 2012-05-04 | Continuous centrifugal separating device for materials |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102631995A true CN102631995A (en) | 2012-08-15 |
| CN102631995B CN102631995B (en) | 2013-10-02 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201210136242 Active CN102631995B (en) | 2012-05-04 | 2012-05-04 | Continuous centrifugal separating device for materials |
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| Country | Link |
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| CN (1) | CN102631995B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105032628A (en) * | 2015-07-07 | 2015-11-11 | 蚌埠市兴利离心机制造有限公司 | Centrifuge capable of avoiding feeding vibration |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2050041U (en) * | 1988-12-04 | 1989-12-27 | 杨大有 | Methyl pentose continuous centrifuger |
| CN2157195Y (en) * | 1992-10-23 | 1994-02-23 | 农业部种子项目办公室 | Centrifugal for removing linters of cotton seeds with diluted sulfuric acid |
| US5403260A (en) * | 1993-06-04 | 1995-04-04 | Hutchinson-Hayes International | Automatic frequency controlled motor backdrive |
| CN2275660Y (en) * | 1996-09-25 | 1998-03-04 | 青岛四洲锅炉设备有限公司 | Air-bag sealing ring |
| CN200946962Y (en) * | 2006-07-21 | 2007-09-12 | 唐山雷克选煤科技有限公司 | Horizontal vibration-unloading centrifugal dehydration machine |
-
2012
- 2012-05-04 CN CN 201210136242 patent/CN102631995B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2050041U (en) * | 1988-12-04 | 1989-12-27 | 杨大有 | Methyl pentose continuous centrifuger |
| CN2157195Y (en) * | 1992-10-23 | 1994-02-23 | 农业部种子项目办公室 | Centrifugal for removing linters of cotton seeds with diluted sulfuric acid |
| US5403260A (en) * | 1993-06-04 | 1995-04-04 | Hutchinson-Hayes International | Automatic frequency controlled motor backdrive |
| CN2275660Y (en) * | 1996-09-25 | 1998-03-04 | 青岛四洲锅炉设备有限公司 | Air-bag sealing ring |
| CN200946962Y (en) * | 2006-07-21 | 2007-09-12 | 唐山雷克选煤科技有限公司 | Horizontal vibration-unloading centrifugal dehydration machine |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105032628A (en) * | 2015-07-07 | 2015-11-11 | 蚌埠市兴利离心机制造有限公司 | Centrifuge capable of avoiding feeding vibration |
| CN105032628B (en) * | 2015-07-07 | 2017-08-25 | 蚌埠市兴利离心机制造有限公司 | A kind of centrifuge for avoiding charging from vibrating |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102631995B (en) | 2013-10-02 |
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Address after: 675000 green food processing garden, Chuxiong economic and Technological Development Zone, Chuxiong Yi Autonomous Prefecture, Yunnan Applicant after: YUNNAN MOER GARDEN BIOLOGICAL SCIENCE & TECHNOLOGY DEVELOPMENT Co.,Ltd. Address before: 675000 green food processing garden, Chuxiong economic and Technological Development Zone, Chuxiong Yi Autonomous Prefecture, Yunnan Applicant before: Yunnan Conrights Biotechnology Development Co.,Ltd. |
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Denomination of invention: Continuous centrifugal separating device for materials Effective date of registration: 20170807 Granted publication date: 20131002 Pledgee: Yunnan modern agriculture and Forestry Investment Co.,Ltd. Pledgor: YUNNAN MOER GARDEN BIOLOGICAL SCIENCE & TECHNOLOGY DEVELOPMENT Co.,Ltd. Registration number: 2017990000714 |
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Date of cancellation: 20190225 Granted publication date: 20131002 Pledgee: Yunnan modern agriculture and Forestry Investment Co.,Ltd. Pledgor: YUNNAN MOER GARDEN BIOLOGICAL SCIENCE & TECHNOLOGY DEVELOPMENT Co.,Ltd. Registration number: 2017990000714 |
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Denomination of invention: Continuous centrifugal separating device for materials Effective date of registration: 20190225 Granted publication date: 20131002 Pledgee: Yunnan modern agriculture and Forestry Investment Co.,Ltd. Pledgor: YUNNAN MOER GARDEN BIOLOGICAL SCIENCE & TECHNOLOGY DEVELOPMENT Co.,Ltd. Registration number: 2019990000128 |
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Date of cancellation: 20220808 Granted publication date: 20131002 Pledgee: Yunnan modern agriculture and Forestry Investment Co.,Ltd. Pledgor: YUNNAN MOER GARDEN BIOLOGICAL SCIENCE & TECHNOLOGY DEVELOPMENT Co.,Ltd. Registration number: 2019990000128 |
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Denomination of invention: A device for continuous centrifugal separation of materials Effective date of registration: 20221115 Granted publication date: 20131002 Pledgee: Yunnan modern agriculture and Forestry Investment Co.,Ltd. Pledgor: YUNNAN MOER GARDEN BIOLOGICAL SCIENCE & TECHNOLOGY DEVELOPMENT Co.,Ltd. Registration number: Y2022990000797 |