CN205730456U - A kind of shell and tube continuous liquid-liquid countercurrent extraction equipment - Google Patents
A kind of shell and tube continuous liquid-liquid countercurrent extraction equipment Download PDFInfo
- Publication number
- CN205730456U CN205730456U CN201620441155.3U CN201620441155U CN205730456U CN 205730456 U CN205730456 U CN 205730456U CN 201620441155 U CN201620441155 U CN 201620441155U CN 205730456 U CN205730456 U CN 205730456U
- Authority
- CN
- China
- Prior art keywords
- phase solvent
- tubulation
- extraction column
- heavy phase
- light phase
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000000605 extraction Methods 0.000 title claims abstract description 59
- 239000007788 liquid Substances 0.000 title claims abstract description 11
- 239000002904 solvent Substances 0.000 claims abstract description 83
- 238000007599 discharging Methods 0.000 claims abstract description 14
- 239000000945 filler Substances 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 abstract description 6
- 238000000926 separation method Methods 0.000 abstract description 3
- 238000000638 solvent extraction Methods 0.000 description 4
- 238000010276 construction Methods 0.000 description 2
- 238000000622 liquid--liquid extraction Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000009854 hydrometallurgy Methods 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000010977 unit operation Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Extraction Or Liquid Replacement (AREA)
Abstract
The utility model discloses a kind of shell and tube continuous liquid-liquid countercurrent extraction equipment, including extraction column 9, the light phase solvent feed mouth 1 being arranged over being connected with light phase solvent tubulation 6 of extraction column 9, lower section is provided with the heavy phase solvent feed mouth 2 being connected with heavy phase solvent tubulation 5, top is provided with the light phase solvent discharging opening 3 being connected with light phase solvent collecting region 7, and bottom is provided with the heavy phase solvent discharging opening 4 being connected with heavy phase solvent collecting region 8;Light phase solvent tubulation 6 and heavy phase solvent tubulation 5 are all longitudinally positioned at extraction column 9, and its port not being connected with charging aperture is respectively close to bottom and the top of extraction column 9.This utility model is simple and reasonable, easy and simple to handle, it is possible to ensures that light, weight two-phase solvent is fully contacted in extraction column, improves mass transfer separation efficiency, it is easy to obtain highly purified target compound product.
Description
Technical field
This utility model relates to a kind of shell and tube continuous liquid-liquid countercurrent extraction equipment, and the liquid-liquid extraction being mainly used in the fields such as hydrometallurgy, chemical industry, medicine, food, waste water process separates, belongs to field of chemical equipment.
Background technology
Liquid-liquid extraction is to utilize the difference of material partition coefficient in the two-phase solvent of immiscible (or slightly soluble) to realize the unit operation that mixture separates.Needing two kinds of density differences in extracting operation, the solution of immiscible (or slightly soluble) separates after being sufficiently mixed again, to reach to separate or purify the purpose of target compound.The most conventional extraction equipment extraction efficiency is low, it is difficult to realize continuous extraction operation, it is therefore necessary to provide a kind of easy to operate, it is possible to realize the countercurrent extraction equipment of continuous extraction.
Utility model content
The purpose of this utility model is to provide a kind of simple in construction to overcome above deficiency, with extraction efficiency intensifier, the shell and tube continuous liquid-liquid countercurrent extraction equipment that is capable of continuous countercurrent extraction.This utility model simple in construction, easy and simple to handle, it is adaptable to industrialized production.
A kind of shell and tube continuous liquid-liquid countercurrent extraction equipment, including extraction column, it is characterized in that the light phase solvent feed mouth being arranged over being connected of described extraction column with light phase solvent tubulation, lower section is provided with the heavy phase solvent feed mouth being connected with heavy phase solvent tubulation, top is provided with the light phase solvent discharging opening being connected with light phase solvent collecting region, and bottom is provided with the heavy phase solvent discharging opening being connected with heavy phase solvent collecting region;Described light phase solvent tubulation and heavy phase solvent tubulation are the most longitudinally positioned at described extraction column, and its port not being connected with charging aperture is respectively close to bottom and the top of described extraction column.
Described light phase solvent tubulation and heavy phase solvent tubulation are several and are spaced in described extraction column.
Described extraction column can be high according to the different post footpath of separation requirement different designs and post, can add filler, arranges liquid re-distributor and increase its extraction efficiency in extraction column.
Described light phase solvent feed mouth, in upper end, arrives bottom extraction column by light phase solvent tubulation, the most naturally rises, the light phase light phase solvent discharging opening discharge from upper end;Heavy phase solvent feed mouth, in lower end, arrives extraction column top by heavy phase solvent tubulation, the most naturally declines, and heavy phase is discharged from bottom heavy phase solvent discharging opening;By this design, thus light in realizing extraction column, weight two phase countercurrent flow extraction process and add strong solvent in mixing radially, improve extraction efficiency.
In described extraction column, spaced multiple light, heavy phase solvent tubulations improve two-phase solvent in distribution radially and mixing, it is achieved light, weight is biphase carries out counter-current extraction around tubulation, it is to avoid the short circuit of solvent and mix uneven problem, improve extraction efficiency.
This utility model realizes counter-current extraction by tubulation in extraction column, makes all can keep between light, the weight two-phase solvent of same level position in whole extraction column certain target compound concentration difference.
In equipment described in the utility model, target compound can dissolve with light phase, uses heavy phase solvent extraction;Heavy phase can also be dissolved in, use light phase solvent extraction.
This utility model compared with prior art has the advantage that simple and reasonable, easy and simple to handle, it is possible to ensures that light, weight two-phase solvent is fully contacted in extraction column, improves mass transfer separation efficiency, it is easy to obtain highly purified target compound product.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure: 1 is light phase solvent feed mouth;2 attach most importance to phase solvent charging aperture;3 is light phase solvent discharging opening;4 attach most importance to phase solvent discharging opening;5 attach most importance to phase solvent tubulation;6 is light phase solvent tubulation;7 is light phase solvent collecting region;8 attach most importance to phase solvent collecting region;9 is extraction column.
Detailed description of the invention
As shown in Figure 1, a kind of shell and tube continuous liquid-liquid countercurrent extraction equipment, including extraction column 9, the light phase solvent feed mouth 1 being arranged over being connected with light phase solvent tubulation 6 of extraction column 9, lower section is provided with the heavy phase solvent feed mouth 2 being connected with heavy phase solvent tubulation 5, top is provided with the light phase solvent discharging opening 3 being connected with light phase solvent collecting region 7, and bottom is provided with the heavy phase solvent discharging opening 4 being connected with heavy phase solvent collecting region 8;Light phase solvent tubulation 6 and heavy phase solvent tubulation 5 are all longitudinally positioned at extraction column 9, and its port not being connected with charging aperture is respectively close to bottom and the top of extraction column 9.
Light phase solvent tubulation 6 and heavy phase solvent tubulation 5 are several and are spaced in extraction column 9.
During use, light phase solvent is after light phase solvent feed mouth 1 pumps into, being entered in extraction column 9 from extraction column bottom by light phase solvent tubulation 6, naturally rise and contact with the heavy phase solvent flowed down from top and start to extract, after light phase solvent collecting region, top 7 is collected, from top, light phase solvent discharging opening 3 flows out;And heavy phase solvent is after heavy phase solvent feed mouth 2 pumps into, enter in extraction column 9 by heavy phase solvent tubulation 5 from extraction column top, naturally the light phase solvent declined and rise with bottom contacts and extracts, flow out from bottom heavy phase solvent discharging opening 4 after heavy phase solvent collecting region, bottom 8 is collected, thus complete whole counter-current extraction process.During extracting operation, target compound can be dissolved in gently, in a phase solvent in heavy phase, use another phase solvent to extract, pump into biphase liquid by lasting and collect the two-phase solvent after extracting on extraction column top and bottom respectively, it is possible to achieve continuous countercurrent extracting operation.
Claims (4)
1. a shell and tube continuous liquid-liquid countercurrent extraction equipment, including extraction column (9), it is characterized in that the light phase solvent feed mouth (1) being arranged over being connected of described extraction column (9) with light phase solvent tubulation (6), lower section is provided with heavy phase solvent feed mouth (2) being connected with heavy phase solvent tubulation (5), top is provided with the light phase solvent discharging opening (3) being connected with light phase solvent collecting region (7), and bottom is provided with heavy phase solvent discharging opening (4) being connected with heavy phase solvent collecting region (8);Described light phase solvent tubulation (6) and heavy phase solvent tubulation (5) are all longitudinally positioned at described extraction column (9), and its port not being connected with charging aperture is respectively close to bottom and the top of described extraction column (9).
2. equipment as claimed in claim 1, it is characterised in that described light phase solvent tubulation (6) and heavy phase solvent tubulation (5) are several and are spaced in described extraction column (9).
3. equipment as claimed in claim 1, it is characterised in that add filler in described extraction column (9).
4. equipment as claimed in claim 1, it is characterised in that described extraction column (9) arranges liquid re-distributor.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620441155.3U CN205730456U (en) | 2016-05-16 | 2016-05-16 | A kind of shell and tube continuous liquid-liquid countercurrent extraction equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620441155.3U CN205730456U (en) | 2016-05-16 | 2016-05-16 | A kind of shell and tube continuous liquid-liquid countercurrent extraction equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
CN205730456U true CN205730456U (en) | 2016-11-30 |
Family
ID=57366186
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201620441155.3U Expired - Fee Related CN205730456U (en) | 2016-05-16 | 2016-05-16 | A kind of shell and tube continuous liquid-liquid countercurrent extraction equipment |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN205730456U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107478770A (en) * | 2017-06-19 | 2017-12-15 | 中国原子能科学研究院 | A kind of extraction/strip kinetics research device based on rising single drop technique |
-
2016
- 2016-05-16 CN CN201620441155.3U patent/CN205730456U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107478770A (en) * | 2017-06-19 | 2017-12-15 | 中国原子能科学研究院 | A kind of extraction/strip kinetics research device based on rising single drop technique |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105263595B (en) | Solvent extraction precipitator device | |
CN205152183U (en) | Volatile oil extraction separation device | |
CN202131345U (en) | Extracting trough for extracting copper from circuit board leaching solution | |
CN202387248U (en) | Novel box type extraction tank for industrial application | |
CN205730456U (en) | A kind of shell and tube continuous liquid-liquid countercurrent extraction equipment | |
CN203281070U (en) | Full-automatic high-efficiency low-emulsification liquid-liquid extraction device | |
CN208340174U (en) | A kind of centrifugal continuous liquid-liquid counterflow extraction device | |
CN103120863B (en) | Liquid-liquid extraction mixer-settler and extraction method and application thereof | |
CN206308326U (en) | A kind of preparation facilities of Rosa Damascana | |
CN101066120B (en) | Efficient continuous spicy material eliminating process in capsanthin production | |
CN202207478U (en) | Solid-liquid separator of mixer-settler for extraction | |
CN209276482U (en) | A kind of volatile oil extracting system | |
CN103845924B (en) | Parallel flow falling film extraction process and equipment | |
CN201454161U (en) | Oil-water separation system | |
CN202555010U (en) | Oil-water separator for extracting essential oil | |
CN204656072U (en) | A kind of oily water separating equipment | |
CN203291552U (en) | Traditional Chinese medicine extraction tank | |
CN203154320U (en) | Multifunctional device for extracting, separating and refining traditional Chinese medicine | |
CN109395428A (en) | Extraction and separation device and system and extraction and separation method thereof | |
CN206746042U (en) | One kind stream wall type liquid-liquid extraction glass device | |
CN202136993U (en) | Self-stirring distillation reactor | |
CN205839085U (en) | A kind of rare earth extraction knot screen | |
CN203677998U (en) | Countercurrent extraction production line | |
CN204656073U (en) | A kind of automatic oil water separation device | |
CN204582602U (en) | Circulation extraction concentration in oral liquid process process |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161130 |