CN1251053A - Method for exchanging materials between two liquid phases - Google Patents
Method for exchanging materials between two liquid phases Download PDFInfo
- Publication number
- CN1251053A CN1251053A CN98803533A CN98803533A CN1251053A CN 1251053 A CN1251053 A CN 1251053A CN 98803533 A CN98803533 A CN 98803533A CN 98803533 A CN98803533 A CN 98803533A CN 1251053 A CN1251053 A CN 1251053A
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- CN
- China
- Prior art keywords
- exchange media
- room
- chamber
- exchange
- extraction 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.)
- Pending
Links
- 238000000034 method Methods 0.000 title claims abstract description 44
- 239000007791 liquid phase Substances 0.000 title claims abstract description 16
- 239000000463 material Substances 0.000 title claims abstract description 16
- 239000012071 phase Substances 0.000 claims abstract description 37
- 238000000605 extraction Methods 0.000 claims abstract description 27
- 238000010521 absorption reaction Methods 0.000 claims abstract description 19
- 239000007788 liquid Substances 0.000 claims abstract description 7
- 230000002411 adverse Effects 0.000 claims description 5
- 230000004087 circulation Effects 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- TVEXGJYMHHTVKP-UHFFFAOYSA-N 6-oxabicyclo[3.2.1]oct-3-en-7-one Chemical compound C1C2C(=O)OC1C=CC2 TVEXGJYMHHTVKP-UHFFFAOYSA-N 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000009854 hydrometallurgy Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J47/00—Ion-exchange processes in general; Apparatus therefor
- B01J47/10—Ion-exchange processes in general; Apparatus therefor with moving ion-exchange material; with ion-exchange material in suspension or in fluidised-bed form
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/04—Solvent extraction of solutions which are liquid
- B01D11/0426—Counter-current multistage extraction towers in a vertical or sloping position
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/04—Solvent extraction of solutions which are liquid
- B01D11/0488—Flow sheets
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Extraction Or Liquid Replacement (AREA)
Abstract
The invention relates to a method for exchanging materials between two liquid phases in two interconnected contact chambers by means of an exchange medium which is brought into contact with the liquid extraction phase in the first chamber and the liquid absorption phase in the second chamber. The material which is to be separated is transferred from the extraction phase to the absorption phase by the exchange medium. The inventive method is characterized in that the exchange medium is divided up by means of a distribution device into the extraction and absorption phases which fill the chambers.
Description
The present invention relates to two kinds of mass exchange methods between liquid phase, this method is undertaken by one-step method or a series of classification step that runs through continuously by means of exchange media.Each classification step comprises two contact connected to one another chambers.Extraction phase contacts with exchange media in first Room, and the exchange media that carries extraction phase contacts with absorption in second Room.From extraction phase, isolate material in this way and transfer in the absorption mutually.
In chemistry, hydrometallurgy, microorganism and other industrial department, use this mass exchange method, be used for separating, concentrating and purifying substances.
The one step exchange process of carrying out between two kinds of liquid phases by means of exchange media is known, and this method has been used the system of two chambers.A kind of liquid phase exchange media has all been filled in two chambers, and exchange media forms continuous phase.Feed decentralized photo in each chamber, this decentralized photo does not dissolve in exchange media, but feeds in the exchange media as a kind of drop.Thereby material is transferred to the exchange media from decentralized photo (extraction phase) in a chamber.This exchange media is imported in another chamber.Import another kind of decentralized photo (absorption phase) through exchange media in this chamber, material is transferred in the absorption mutually from exchange media.For example at " theoretical foundation of Chemical Technology " magazine, (Moskau) 1984, B.18; The 6th phase, this method is disclosed in the 736-738 page or leaf.
The separative efficiency of a disclosed step material exchange processes is still waiting to improve.A kind of improving one's methods is to expand to multistep processes.
By Russ P application number 95117738 and 95117767 known a kind of multistep material exchange processes that on October 19th, 95 proposed, this method is being carried out in a series of classification step that run through each other between two kinds of liquid phases by means of a kind of exchange media.In this case, each classification step comprises two contact connected to one another chambers.Exchange media has been filled in these chambers.Extraction phase that disperses, be insoluble to continuous exchange media or absorption are passed through these chambers with drop group's form.Exchange media successively with first Room in extraction phase and the absorption in second Room contact.At this moment the material that need separate is transferred in second Room by first Room, is transferred in the absorption mutually by extraction phase.In order to improve mass exchange, a plurality of this classification step that run through each other are set.This method is called extraction-extract again combined techniques.Exchange media is an extractant.
The application potential of this known multistep material exchange processes and separative efficiency also are still waiting exploitation, for example expand to gas-liquid exchange or solid-liquid exchange.
The objective of the invention is to develop improving one's methods of a kind of known substance exchange process with other using value.In order to improve the separative efficiency of the mass exchange between two kinds of liquid phases, this method comprises the process of carrying out by means of exchange media and the cohesive process of absorption, absorption and desorb in different states of matters.
The objective of the invention is to realize by following form, extraction phase is contained in first Room of a step, and will absorbs in second Room that is contained in a step mutually according to above-mentioned one-step method and multistep processes.Exchange material with exchange media, at first exchange media is assigned in the chamber that extraction phase is housed, then be assigned to one and be equipped with in the chamber that absorbs phase.
Exchange media circulates between first and second Room in same step at every turn.
Another kind method is that exchange media also can circulate in a plurality of or whole classification step, is transported in first Room of next step by second Room of a step.
Extraction phase is with absorb mutually can be with following current or adverse current form by a series of classification step.
Be method of the present invention astoundingly by improve between each step chamber or between a plurality of classification step chamber the circulation rate of exchange media can improve separative efficiency.
Describe the present invention in detail by means of embodiment and accompanying drawing below.Wherein:
Fig. 1 is the process chart of the classification step that runs through continuously, comprise exchange media in step circulation and liquid phase through the adverse current route of all classification step.
Fig. 2 is the process chart of the classification step that runs through continuously, comprise exchange media in step circulation and liquid phase through the following current route of all classification step.
Fig. 3 is the process chart of the classification step that runs through continuously, comprise exchange media through in steps circulation and the adverse current route of the classified step of liquid phase.
Fig. 4 is the process chart of the classification step that runs through continuously, comprise exchange media through in steps circulation and liquid phase through the following current route of this step.
In the method for Fig. 1 and Fig. 3, first Room and second Room that constitute classification step are set in the housing separately.
In the method for Fig. 2 and Fig. 4, first Room and second Room that constitute classification step are placed in the housing superimposedly, and classification step is overlapping in a housing.
In all technological operations, corresponding liquid phase all is equipped with in the contact chamber of classification step.In first Room 1 extraction phase is housed, in second Room 2 the absorption phase is housed.Then exchange media between the chamber in classification step (Fig. 1 to 2) or circulate by a series of classification step (Fig. 3 to Fig. 4).Like this by exchange media is assigned to chamber 1 and chamber 2 mutually in, contact fully between making exchange media and extraction phase or absorbing mutually.Exchange media distribution in each phase is to carry out with the form of drop, bubble, particle, Fig. 2 schematic diagram for example, but also can injection stream and the form of film carry out Fig. 4 schematic diagram for example.Exchange media can be liquid, gas or solid.
Extraction phase through pipeline 3 be transported to first classification step chamber 1 in, discharge from last classification step through pipeline 4.Absorb through pipeline 5 and carry, discharge through pipeline 6.The pipeline 7 one-level one-levels ground of extraction phase through connecting is carried, and carries and absorb through connecting line 8 one-level one-levels ground.Pipeline 9 circulations of exchange media through connecting.
Exchange media is indoor mobile in contact, is undertaken by gravity from the top or the bottom outflow of chamber.Exist very big difference mutually and between the exchange media at extraction phase and absorption.According to this big difference, exchange media is collection chamber 1 and the bottom (Fig. 1,4) of chamber 2 or the top (Fig. 2,3) of chamber 1 and chamber 2 in being assigned to corresponding liquid phase the time, forms phase boundary 10.Exchange media in the contact chamber 1 and 2 is assigned in the liquid phase through distributor 11.Physical characteristic according to exchange media realizes various distribution, for example carries out with the form of drop, bubble, particle or injection stream and plume.
The material that needs to separate is transferred in the exchange media by extraction phase in chamber 1, is transferred in the absorption mutually by exchange media in chamber 2.The material of flowing through in the extraction phase of chamber 1 by this method reduces, and the material in the absorption mutually of the chamber 2 of flowing through increases.
Extraction phase passes through classification step with following current (Fig. 2,4) or adverse current (Fig. 1,3) form mutually each other with absorbing.The following current route implements simple industrial.But when the material that need to separate as quick as thought with absorb mutually or during its contained component reaction, they can only arrive a maximal efficiency.
In mass exchange method of the present invention, extraction phase forms continuous phase with absorbing in contacting the chamber, fill most of space of chamber.Make thus two kinds in the indoor time of staying length than known method, exchange media further fills up the chamber.The longer time of staying is favourable, because can carry out the mass exchange of longer time, makes exchange more abundant thus.If mass exchange is accompanied by chemical transformation, so this method is particularly important, and chemical transformation can not disappear as quick as thought.
Claims (6)
1. the mass exchange method between two kinds of liquid phases, carry out in two contact connected to one another chambers (1) and (2) by means of exchange media, exchange media is contacted in second Room (2) with liquid the absorption in first Room (1) contact with liquid extraction phase, the material that need to separate is transferred in the absorption mutually by extraction phase by exchange media, it is characterized in that: exchange media is assigned to by distributor (11) in the extraction phase that is contained in respectively in chamber (1) and chamber (2) and the absorption mutually.
2. according to the method for claim 1, it is characterized in that: a plurality of classification step run through continuously, are made of two chambers connected to one another respectively.
3. according to the method for claim 1 or 2, it is characterized in that: exchange media circulates between first Room and second Room in rapid same relating at every turn.
4. according to the method for claim 2, it is characterized in that: exchange media circulates through a plurality of or whole classification step, and they are transported in first Room of next step by second Room of a step.
5. according to each method of claim 2 to 4, it is characterized in that: extraction phase and the form with following current of absorbing are by multistage step.
6. according to each method of claim 2 to 4, it is characterized in that: extraction phase with absorb with the adverse current form by multistage step.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| RU97105096 | 1997-04-02 | ||
| RU97105096/25A RU97105096A (en) | 1997-04-02 | METHOD OF STAGE MASS TRANSFER BETWEEN TWO LIQUID PHASES |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1251053A true CN1251053A (en) | 2000-04-19 |
Family
ID=20191435
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN98803533A Pending CN1251053A (en) | 1997-04-02 | 1998-03-27 | Method for exchanging materials between two liquid phases |
Country Status (5)
| Country | Link |
|---|---|
| EP (1) | EP0971778A1 (en) |
| JP (1) | JP2001517148A (en) |
| CN (1) | CN1251053A (en) |
| CA (1) | CA2285361A1 (en) |
| WO (1) | WO1998043718A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102847339A (en) * | 2012-09-07 | 2013-01-02 | 福州大学 | Gas phase extraction and enrichment method for liquid phase volatile material, and system thereof |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AUPP790898A0 (en) | 1998-12-23 | 1999-01-28 | Life Therapeutics Limited | Renal dialysis |
| AUPP790698A0 (en) | 1998-12-23 | 1999-01-28 | Life Therapeutics Limited | Separation of microorganisms |
| AUPP971399A0 (en) * | 1999-04-12 | 1999-05-06 | Life Therapeutics Limited | Separation of plasma components |
| US7077942B1 (en) | 1999-12-23 | 2006-07-18 | Gradipore Limited | Removal of biological contaminants |
| AUPQ691400A0 (en) | 2000-04-14 | 2000-05-11 | Life Therapeutics Limited | Separation of micromolecules |
| ATE449200T1 (en) | 2000-04-18 | 2009-12-15 | Gradipore Ltd | SEPARATION AND TREATMENT OF SAMPLES BY ELECTROPHORESIS |
| AUPQ697300A0 (en) | 2000-04-18 | 2000-05-11 | Life Therapeutics Limited | Separation apparatus |
| US6923896B2 (en) | 2000-09-22 | 2005-08-02 | The Texas A&M University System | Electrophoresis apparatus and method |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2573415B1 (en) * | 1984-11-16 | 1986-12-12 | Pechiney Uranium | PROCESS FOR RECOVERY IN THE FORM OF TETRAVALENT FLUORIDE OF URANIUM EXTRACTED FROM PHOSPHATE SOLUTIONS |
| FR2680980A1 (en) * | 1991-09-09 | 1993-03-12 | Commissariat Energie Atomique | PROCESS FOR TREATING A SOLUTION CONTAINING ACETIC ACID IN THE PRESENCE OF HALOGENES |
| FR2707416B1 (en) * | 1993-07-08 | 1995-08-18 | Cogema | Process and installation for decontamination of radioactive nitric effluents containing strontium and sodium. |
-
1998
- 1998-03-27 WO PCT/EP1998/001811 patent/WO1998043718A1/en not_active Application Discontinuation
- 1998-03-27 CA CA002285361A patent/CA2285361A1/en not_active Abandoned
- 1998-03-27 EP EP98924084A patent/EP0971778A1/en not_active Withdrawn
- 1998-03-27 JP JP54114698A patent/JP2001517148A/en active Pending
- 1998-03-27 CN CN98803533A patent/CN1251053A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102847339A (en) * | 2012-09-07 | 2013-01-02 | 福州大学 | Gas phase extraction and enrichment method for liquid phase volatile material, and system thereof |
| CN102847339B (en) * | 2012-09-07 | 2014-11-05 | 福州大学 | Gas phase extraction and enrichment method for liquid phase volatile material, and system thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| WO1998043718A1 (en) | 1998-10-08 |
| EP0971778A1 (en) | 2000-01-19 |
| JP2001517148A (en) | 2001-10-02 |
| CA2285361A1 (en) | 1998-10-08 |
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