CN202961962U - Multistage continuous-countercurrent extraction and separation system - Google Patents
Multistage continuous-countercurrent extraction and separation system Download PDFInfo
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- CN202961962U CN202961962U CN 201220655337 CN201220655337U CN202961962U CN 202961962 U CN202961962 U CN 202961962U CN 201220655337 CN201220655337 CN 201220655337 CN 201220655337 U CN201220655337 U CN 201220655337U CN 202961962 U CN202961962 U CN 202961962U
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- liquid separator
- extraction
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Abstract
The utility model provides a multistage continuous-countercurrent extraction and separation system. According to the technical scheme, the multistage continuous-countercurrent extraction and separation system comprises at least two extraction and separation devices, wherein each extraction and separation device is composed of a pipeline type extractor and a slag-liquid separator; the discharge hole of the slag-liquid separator of the high-stage extraction and separation device is connected with the feeding hole of the pipeline type extractor of the low-stage extraction and separation device which is adjacent to the high-stage extraction and separation device; the separated-liquid outlet of the slag-liquid separator of the low-stage extraction and separation device is communicated with the feeding hole of the pipeline type extractor of the high-stage extraction and separation device through a pipe and a separated-liquid delivery pump; the separated-liquid outlet of the slag-liquid separator of the first-stage extraction and separation device is communicated with a finished-product tank through a pipe and a separated-liquid delivery pump; the feeding hole of the pipeline type extractor of the first-stage extraction and separation device is a raw-material inlet; the feeding hole of the pipeline type extractor of the last-stage extraction and separation device is communicated with a solvent tank through a pipe and a solvent pump; and the discharge hole of the slag-liquid separator of the last-stage extraction and separation device is used for discharging slag.
Description
Technical field:
The utility model relates to a kind of equipment that uses liquid medium that solid material is extracted, especially a kind of employing multistage subsection formula is extracted and is separated, and realizes that a kind of multiple stage continuous adverse current of Continuous Countercurrent Extraction extracts piece-rate system.
Background technology:
in the prior art, the technical scheme that approaches the most with the application is the Continuous Countercurrent Extraction machine in use, this Continuous Countercurrent Extraction machine is to be made of the more piece extraction tube, the inner spiral propeller that is equipped with, material is under the effect of spiral propeller, be transported to the other end from an end of extraction tube, and extract solvent with the direction opposite with mass transport, flow to the other end from an end, form counter-flow extraction, be widely used in the extraction of various plant materials, if but raw material unit weight and extract the proportion of solvent when close, both are difficult to separate, just can't realize reverse propulsion, carry, one is to realize counter-flow extraction in extraction tube, the 2nd, the material operation is not smooth, form and stop up, the 3rd, extract can be taken a large amount of slag charges out of, be difficult to process.Above-mentioned these reasons cause equipment normally to move, and actual extracting treating capacity and designed capacity differ greatly simultaneously, greatly reduce the cost performance of equipment, and this is the existing weak point of prior art.
The utility model content:
Technical problem to be solved in the utility model, be exactly for the existing deficiency of prior art, and provide a kind of multiple stage continuous adverse current to extract the technical scheme of piece-rate system, this scheme adopts a plurality of extraction separator unit that are comprised of duct type extractor and dreg-liquid separator, utilizes the extract that respectively extracts separator output to be defeated by upper level extraction separator and realizes counter-flow extraction.
This programme is achieved by the following technical measures:
the multiple stage continuous adverse current of first technical scheme extracts piece-rate system, include the extraction separator that is formed by duct type extractor and dreg-liquid separator, extraction tube discharging opening on the duct type extractor of this extraction separator is connected with the dreg-liquid separator charging aperture of dreg-liquid separator, the characteristics of this programme are that described extraction separator has two at least, the dreg-liquid separator discharging opening that upper level extracts the separator dreg-liquid separator is connected with the charging aperture that adjacent next stage extracts separator duct type extractor, the discharge channel that next stage extracts the separator dreg-liquid separator is communicated with the charging aperture that adjacent upper level extracts separator duct type extractor by pipeline and parting liquid delivery pump, the charging aperture that raw material extracts separator duct type extractor from the first order enters, the charging aperture that the fresh extractor solvent extracts separator duct type extractor from final stage enters, the discharge channel that finished fluid extracts the separator dreg-liquid separator from the first order is discharged, and the dreg-liquid separator discharging opening that slag charge extracts the separator dreg-liquid separator from final stage is discharged.The concrete characteristics of this programme also have, described duct type extractor has the duct type extraction tube, in the duct type extraction tube, spiral propeller is arranged, be connected with driving mechanism with this spiral propeller, an end at described duct type extraction tube has charging aperture, at the other end, output mechanism and extraction tube discharging opening is arranged.Described dreg-liquid separator has a casing, the sieve aperture guipure is arranged in this casing, in described casing bottom, the parting liquid feeder is arranged, in the bottom of described parting liquid feeder, discharge channel is arranged, an end at described casing has the dreg-liquid separator charging aperture, and the other end has the dreg-liquid separator discharging opening.Described duct type extraction tube outer wall can assemble ultrasonic transducer.
The multiple stage continuous adverse current of second technical scheme extracts piece-rate system, include the extraction separator that is formed by duct type extractor and dreg-liquid separator, extraction tube discharging opening on the duct type extractor of this extraction separator is connected with the dreg-liquid separator charging aperture of dreg-liquid separator, the characteristics of this programme are that described extraction separator has two at least, and the dreg-liquid separator discharging opening that upper level extracts the separator dreg-liquid separator is connected with the charging aperture that adjacent next stage extracts separator duct type extractor; The rinsing mixture export that extracts the separator dreg-liquid separator at the same level is communicated with by the charging aperture on the duct type extractor of pipeline and rinsing mixed liquor infusion pump and extraction separator at the same level; The discharge channel that next stage extracts the separator dreg-liquid separator is communicated with the rinsing liquid import that adjacent upper level extracts the separator dreg-liquid separator by pipeline and parting liquid delivery pump; The charging aperture that raw material extracts separator duct type extractor from the first order enters, the rinsing liquid import that the fresh extractor solvent extracts the separator dreg-liquid separator from final stage enters, the discharge channel that finished fluid extracts the separator dreg-liquid separator from the first order is discharged, and the dreg-liquid separator discharging opening that slag charge extracts the separator dreg-liquid separator from final stage is discharged.The concrete characteristics of this programme also have, described duct type extractor has the duct type extraction tube, in the duct type extraction tube, spiral propeller is arranged, be connected with driving mechanism with this spiral propeller, an end at described duct type extraction tube has charging aperture, at the other end, output mechanism and extraction tube discharging opening is arranged.Described dreg-liquid separator has a casing, the sieve aperture guipure is arranged in this casing, in described casing bottom, the parting liquid feeder is arranged, in the bottom of described parting liquid feeder, discharge channel is arranged, on the sieve aperture guipure above described parting liquid feeder, the parting liquid compression roller is arranged; Rinsing mixed liquor feeder is arranged in the middle and lower part of described casing, the rinsing mixture export is arranged at the bottom at this rinsing mixed liquor feeder, on the casing above described rinsing mixed liquor feeder, the rinsing liquid import is arranged, on the sieve aperture guipure above described rinsing mixed liquor feeder, rinsing mixed liquor compression roller is arranged, an end at described casing has the dreg-liquid separator charging aperture, and the other end has the dreg-liquid separator discharging opening.Described duct type extraction tube outer wall can assemble ultrasonic transducer.
The beneficial effect of this programme can be learnt according to the narration to such scheme, due in this scheme, extract solvent and material and be conveying in the same way in the duct type extraction tube, solvent and material can not occur extracting and oppositely carry the clogging that causes in the duct type extraction tube, duct type extraction tube volume obtains the utilization of maximal efficiency, and extracted amount significantly improves.The slag of discharging from the duct type extraction tube separates at dreg-liquid separator with liquid, and the slag of separation enters the next stage separating extraction device and extracts, and the parting liquid of separation enters the upper level separating extraction device, forms counter-flow extraction.This shows, the utility model compared with prior art has substantive distinguishing features and progress, and the beneficial effect of its enforcement is also apparent.
Description of drawings:
Fig. 1 is the structural representation of first technical scheme specific embodiment of the utility model.
Fig. 2 is the structural representation of second technical scheme specific embodiment of the utility model.
in figure, 1 is driving mechanism, 2 is the extraction tube charging aperture, 3 is spiral propeller, 4 is the duct type extraction tube, 5 is output mechanism, 6 is the extraction tube discharging opening, 7 is the dreg-liquid separator charging aperture, 8 is the sieve aperture guipure, 9 is the dreg-liquid separator discharging opening, 10 is the parting liquid feeder, 11 is discharge channel, 12 is the parting liquid infusion pump, 13 is finished pot, 14 is the solvent tank, 15 is the solvent pump, 16 is the parting liquid compression roller, 17 is the rinsing liquid import, 18 are rinsing mixed liquor compression roller, 19 are rinsing mixed liquor feeder, 20 are the rinsing mixture export, 21 are rinsing mixed liquor infusion pump.
The specific embodiment:
For clearly demonstrating the technical characterstic of this programme, below by two specific embodiment, and in conjunction with its accompanying drawing, this programme is set forth.
Fig. 1 is the accompanying drawing of first technical scheme specific embodiment, can find out by accompanying drawing 1, the multiple stage continuous adverse current of this programme extracts piece-rate system by the extraction separator that is comprised of duct type extractor and dreg-liquid separator, and the extraction tube discharging opening 6 on the duct type extractor of this extraction separator is connected with the dreg-liquid separator charging aperture 7 of dreg-liquid separator.Described duct type extractor has duct type extraction tube 4, spiral propeller 3 is arranged in duct type extraction tube 4, be connected with driving mechanism 1 with this spiral propeller 3, an end at described duct type extraction tube 4 has extraction tube charging aperture 2, at the other end, output mechanism 5 and extraction tube discharging opening 6 are arranged, described duct type extraction tube also can adopt ultrasonic extraction tube.Described dreg-liquid separator has a casing, sieve aperture guipure 8 is arranged in this casing, in described casing bottom, parting liquid feeder 10 is arranged, in the bottom of described parting liquid feeder 10, discharge channel 11 is arranged, an end at described casing has dreg-liquid separator charging aperture 7, the other end has dreg-liquid separator discharging opening 9, and certain described dreg-liquid separator also can adopt the dreg-liquid separator of other known structure, also can mix use.The described extraction separator of this programme has two at least, and this specific embodiment has six extraction separators.The dreg-liquid separator discharging opening 9 that upper level extracts the separator dreg-liquid separator is connected with the extraction tube charging aperture 2 that adjacent next stage extracts separator duct type extractor, and the discharge channel 11 that next stage extracts the separator dreg-liquid separator is communicated with extraction tube charging aperture 2 or the feed end that adjacent upper level extracts separator duct type extractor by pipeline and parting liquid delivery pump 12.The discharge channel 11 that the first order is extracted the separator dreg-liquid separator is communicated with finished pot 13 by pipeline and parting liquid delivery pump 12, and the charging aperture 2 that the first order is extracted separator duct type extractor is the feed(raw material)inlet.The charging aperture 2 of the 6th grade of extraction separator duct type extractor is communicated with solvent tank 14 by pipeline and solvent pump 15, and the dreg-liquid separator discharging opening row 9 of the 6th grade of extraction separator dreg-liquid separator goes out slag charge.
Fig. 2 is the accompanying drawing of second technical scheme specific embodiment, can find out by accompanying drawing 2, the multiple stage continuous adverse current of this programme extracts piece-rate system by the extraction separator that is comprised of duct type extractor and dreg-liquid separator, and the extraction tube discharging opening 6 on the duct type extractor of this extraction separator is connected with the dreg-liquid separator charging aperture 7 of dreg-liquid separator.Described duct type extractor has duct type extraction tube 4, spiral propeller 3 is arranged in duct type extraction tube 4, be connected with driving mechanism 1 with this spiral propeller 3, at an end of described duct type extraction tube 4, extraction tube charging aperture 2 arranged, at the other end, output mechanism 5 and extraction tube discharging opening 6 are arranged.Described dreg-liquid separator has a casing, sieve aperture guipure 8 is arranged in this casing, in described casing bottom, parting liquid feeder 10 is arranged, in the bottom of described parting liquid feeder 10, discharge channel 11 is arranged, on the sieve aperture guipure 8 above described parting liquid feeder 10, parting liquid compression roller 16 is arranged; Rinsing mixed liquor feeder 19 is arranged in the middle and lower part of described casing, rinsing mixture export 20 is arranged at the bottom at this rinsing mixed liquor feeder 19, on the casing above described rinsing mixed liquor feeder 19, rinsing liquid import 17 is arranged, on the sieve aperture guipure 8 above described rinsing mixed liquor feeder 19, rinsing mixed liquor compression roller 18 is arranged, an end at described casing has dreg-liquid separator charging aperture 7, and the other end has dreg-liquid separator discharging opening 9.The described extraction separator of this programme has two at least, and this specific embodiment has four extraction separators.The dreg-liquid separator discharging opening 9 that upper level extracts the separator dreg-liquid separator is connected with the extraction tube charging aperture 2 that adjacent next stage extracts separator duct type extractor.The rinsing mixture export 20 that extracts the separator dreg-liquid separator at the same level is communicated with by extraction tube charging aperture 2 or the feed end on the duct type extractor of pipeline and rinsing mixed liquor infusion pump 21 and extraction separator at the same level.The discharge channel 11 that next stage extracts the separator dreg-liquid separator is communicated with the rinsing liquid import 17 that adjacent upper level extracts the separator dreg-liquid separator by pipeline and parting liquid delivery pump 12.The discharge channel 11 that the first order is extracted the separator dreg-liquid separator is communicated with finished pot 13 by pipeline and parting liquid delivery pump 12, and the charging aperture 2 that the first order is extracted separator duct type extractor is the feed(raw material)inlet.The rinsing liquid import 17 that the fourth stage extracts the separator dreg-liquid separator is communicated with solvent tank 14 by pipeline and solvent pump 15, and the fourth stage extracts the dreg-liquid separator discharging opening 9 of separator dreg-liquid separator and discharges slag charge.
Claims (6)
1. a multiple stage continuous adverse current extracts piece-rate system, include the extraction separator that is formed by duct type extractor and dreg-liquid separator, extraction tube discharging opening on the duct type extractor of this extraction separator is connected with the dreg-liquid separator charging aperture of dreg-liquid separator, it is characterized in that: described extraction separator has two at least, the dreg-liquid separator discharging opening that upper level extracts the separator dreg-liquid separator is connected with the charging aperture that adjacent next stage extracts separator duct type extractor, the discharge channel that next stage extracts the separator dreg-liquid separator is communicated with the charging aperture that adjacent upper level extracts separator duct type extractor by pipeline and parting liquid delivery pump, the charging aperture that the first order is extracted separator duct type extractor enters raw material, the charging aperture that final stage is extracted separator duct type extractor enters the fresh extractor solvent, the first order is extracted the discharge channel of separator dreg-liquid separator and is discharged finished fluid, and final stage is extracted the dreg-liquid separator discharging opening of separator dreg-liquid separator and discharged slag charge.
2. extraction piece-rate system according to claim 1, it is characterized in that: described dreg-liquid separator has a casing, the sieve aperture guipure is arranged in this casing, in described casing bottom, the parting liquid feeder is arranged, discharge channel is arranged at the bottom at described parting liquid feeder, an end at described casing has the dreg-liquid separator charging aperture, and the other end has the dreg-liquid separator discharging opening.
3. a multiple stage continuous adverse current extracts piece-rate system, include the extraction separator that is formed by duct type extractor and dreg-liquid separator, extraction tube discharging opening on the duct type extractor of this extraction separator is connected with the dreg-liquid separator charging aperture of dreg-liquid separator, it is characterized in that: described extraction separator has two at least, and the dreg-liquid separator discharging opening that upper level extracts the separator dreg-liquid separator is connected with the charging aperture that adjacent next stage extracts separator duct type extractor; The rinsing mixture export that extracts the separator dreg-liquid separator at the same level is communicated with by the charging aperture on the duct type extractor of pipeline and rinsing mixed liquor infusion pump and extraction separator at the same level; The discharge channel that next stage extracts the separator dreg-liquid separator is communicated with the rinsing liquid import that adjacent upper level extracts the separator dreg-liquid separator by pipeline and parting liquid delivery pump; The charging aperture that the first order is extracted separator duct type extractor enters raw material, the rinsing liquid import that final stage is extracted the separator dreg-liquid separator enters the fresh extractor solvent, the first order is extracted the discharge channel of separator dreg-liquid separator and is discharged finished fluid, and final stage is extracted the dreg-liquid separator discharging opening of separator dreg-liquid separator and discharged slag charge.
4. according to claim 1 or 3 described extraction piece-rate systems, it is characterized in that: described duct type extractor has the duct type extraction tube, in the duct type extraction tube, spiral propeller is arranged, be connected with driving mechanism with this spiral propeller, an end at described duct type extraction tube has charging aperture, at the other end, output mechanism and extraction tube discharging opening is arranged.
5. extraction piece-rate system according to claim 3, it is characterized in that: described dreg-liquid separator has a casing, the sieve aperture guipure is arranged in this casing, in described casing bottom, the parting liquid feeder is arranged, discharge channel is arranged at the bottom at described parting liquid feeder, on the sieve aperture guipure above described parting liquid feeder, the parting liquid compression roller is arranged; Rinsing mixed liquor feeder is arranged in the middle and lower part of described casing, the rinsing mixture export is arranged at the bottom at this rinsing mixed liquor feeder, on the casing above described rinsing mixed liquor feeder, the rinsing liquid import is arranged, on the sieve aperture guipure above described rinsing mixed liquor feeder, rinsing mixed liquor compression roller is arranged, an end at described casing has the dreg-liquid separator charging aperture, and the other end has the dreg-liquid separator discharging opening.
6. according to claim 1 or 3 described extraction piece-rate systems, is characterized in that: can assemble ultrasonic transducer outside described duct type extraction tube, tube wall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220655337 CN202961962U (en) | 2012-11-23 | 2012-11-23 | Multistage continuous-countercurrent extraction and separation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220655337 CN202961962U (en) | 2012-11-23 | 2012-11-23 | Multistage continuous-countercurrent extraction and separation system |
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| CN202961962U true CN202961962U (en) | 2013-06-05 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN 201220655337 Withdrawn - After Issue CN202961962U (en) | 2012-11-23 | 2012-11-23 | Multistage continuous-countercurrent extraction and separation system |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102974126A (en) * | 2012-11-23 | 2013-03-20 | 白中明 | Multistage continuous countercurrent extraction and separation system |
| CN103691148A (en) * | 2013-12-20 | 2014-04-02 | 济宁金百特生物机械有限公司 | Continuous countercurrent extraction production line |
| US10031989B2 (en) | 2014-11-18 | 2018-07-24 | Globalfoundries Inc. | Integrated circuit performance modeling using a connectivity-based condensed resistance model for a conductive structure in an integrated circuit |
-
2012
- 2012-11-23 CN CN 201220655337 patent/CN202961962U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102974126A (en) * | 2012-11-23 | 2013-03-20 | 白中明 | Multistage continuous countercurrent extraction and separation system |
| CN103691148A (en) * | 2013-12-20 | 2014-04-02 | 济宁金百特生物机械有限公司 | Continuous countercurrent extraction production line |
| CN103691148B (en) * | 2013-12-20 | 2015-12-16 | 济宁金百特生物机械有限公司 | A kind of Continuous Countercurrent Extraction production line |
| US10031989B2 (en) | 2014-11-18 | 2018-07-24 | Globalfoundries Inc. | Integrated circuit performance modeling using a connectivity-based condensed resistance model for a conductive structure in an integrated circuit |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20130605 Effective date of abandoning: 20150422 |