CN103830931A - Full-automatic extraction-evaporation device - Google Patents
Full-automatic extraction-evaporation device Download PDFInfo
- Publication number
- CN103830931A CN103830931A CN201210495938.6A CN201210495938A CN103830931A CN 103830931 A CN103830931 A CN 103830931A CN 201210495938 A CN201210495938 A CN 201210495938A CN 103830931 A CN103830931 A CN 103830931A
- Authority
- CN
- China
- Prior art keywords
- storage tank
- extractor
- extraction
- pump
- recovery machine
- 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
Images
Landscapes
- Extraction Or Liquid Replacement (AREA)
Abstract
The invention relates to the field of chemical equipment and in particular relates to a full-automatic extraction-evaporation device. The device comprises an extraction tank, a storage tank I, a storage tank II and a solvent recovery machine, wherein the extraction tank is connected with the storage tank I by using a pump I, is connected with the storage tank II by using a pump II and is connected with the solvent recovery machine by using a pump. The device has the beneficial effects that an extraction device is organically combined with an evaporation device through the pump, so that the manual carrying process is removed and the continuous working effect is achieved.
Description
Technical field
The present invention relates to chemical industry equipment field, be specifically related to a kind of automatization abstraction-vaporising device.
Background technology
Extraction (Extraction) refers to utilize the difference of compound solubility or distribution coefficient in the solvent of two kinds immiscible (or slightly solubles), and compound is transferred to another solvent in a kind of solvent.Through repeated multiple times extraction, the method that most compounds is extracted.Extraction claims again solvent extraction or liquid-liquid extraction (to be different from liquid-solid extraction, i.e. leaching), also claim extracting (being common to petroleum refining industry), that the liquid extractant of a kind of use is processed immiscible bi-component or Multi component with it, realizing the mass transfer separation process that component separates, is a kind of unit operations of extensive use.Utilize the similar principle that mixes, extraction has two kinds of modes: liquid-liquid extraction, by certain component in selected separated from solvent liquid mixture, solvent must be immiscible with the mixture liquid being extracted, there is optionally solvability, and the heat endurance that must have and chemical stability, and there are little toxicity and corrosivity.As separated the phenol in coal tar with benzene; With the alkene in organic solvent separation petroleum distillate; Use CCl
4br in extraction water
2.Leaching, is also named leaching, by the component in separated from solvent solid mixture, as the carbohydrate with in water extraction beet; With the soya-bean oil in alcohol leaching soya bean to improve oil yield; Water leaches active ingredient to produce liquid extract " oozing drop " or " leaching " from Chinese medicine.
In current most of Chemical Manufacture technique extraction after be all accompanied by evaporation, so from extraction equipment material handling to evaporation equipment, not only waste time and energy, be also unfavorable for continuous operations.
Summary of the invention
In prior art, extraction equipment and vaporising device can not organically combine, and bring into play the object that it is worked continuously, and the invention provides a kind of full-automatic extraction-vaporising device, have solved the problem that extraction equipment and vaporising device are worked continuously.
The invention provides a kind of full-automatic extraction-vaporising device, described device comprises extractor, storage tank I, storage tank II and solvent recovery machine, extractor is connected by pump I with storage tank I, and extractor is connected by pump II with storage tank II, and extractor is connected with pump with solvent recovery machine.
The connector of the extractor of described device and storage tank I is preferably and is positioned at the top of extractor, is also preferably with the connector of storage tank II the top that is positioned at extractor.
The extractor of described device and storage tank I are preferably and are connected by measuring pump I, and be also preferably and be connected by measuring pump II with storage tank II, be to be shifted by storage tank the liquid of arbitrary volume to extractor by the advantage that measuring pump connects.
The extractor of described device is connected with centrifugal pump with solvent recovery machine, with centrifugal pump connect advantage be the liquid in extractor directly can be transferred to solvent recovery machine to carry out evaporate to dryness, without artificial transfer, reduce cost of labor and time cost, also help continuous operations.
Between the extractor of described device and solvent recovery machine, be connected with 1 triple valve, triple valve effect is to open triple valve by lower mutually emptying while being instantly raffinate phase mutually, then closes triple valve upper phase transfer to solvent recovery machine is carried out to evaporate to dryness.
The invention has the beneficial effects as follows: extraction equipment and vaporising device are organically combined by pump, not only removed a dead lift from, also reached the effect of continuous operations.
Brief description of the drawings
Fig. 1 is full-automatic extraction-vaporising device structural representation of embodiment 1;
Wherein, 1, storage tank I, 2, extractor, 3, storage tank II, 4, solvent recovery machine, 5, measuring pump I, 6, triple valve, 7, centrifugal pump, 8, measuring pump II.
Detailed description of the invention
Following non-limiting example can make the present invention of those of ordinary skill in the art's comprehend, but does not limit the present invention in any way.
A kind of full-automatic extraction-vaporising device, comprise extractor, storage tank I, storage tank II and solvent recovery machine, extractor is connected by measuring pump I with storage tank I, extractor is connected by measuring pump II with storage tank II, extractor is connected with centrifugal pump with solvent recovery machine, the connector of extractor and storage tank I is positioned at the top of extractor, and the connector of extractor and storage tank II is positioned at the top of extractor, is connected with 1 triple valve between extractor and solvent recovery machine.
Claims (7)
1. a full-automatic extraction-vaporising device, it is characterized in that: described device comprises extractor, storage tank I, storage tank II and solvent recovery machine, extractor is connected by pump I with storage tank I, and extractor is connected by pump II with storage tank II, and extractor is connected with pump with solvent recovery machine.
2. method according to claim 1, is characterized in that: the connector of described extractor and storage tank I is positioned at the top of extractor.
3. method according to claim 1, is characterized in that: the connector of described extractor and storage tank II is positioned at the top of extractor.
4. method according to claim 1, is characterized in that: described extractor is connected with storage tank I measuring pump I.
5. method according to claim 1, is characterized in that: described extractor is connected with storage tank II measuring pump II.
6. method according to claim 1, is characterized in that: described extractor is connected with solvent recovery machine centrifugal pump.
7. method according to claim 1, is characterized in that: between described extractor and solvent recovery machine, be connected with 1 triple valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210495938.6A CN103830931A (en) | 2012-11-27 | 2012-11-27 | Full-automatic extraction-evaporation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210495938.6A CN103830931A (en) | 2012-11-27 | 2012-11-27 | Full-automatic extraction-evaporation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103830931A true CN103830931A (en) | 2014-06-04 |
Family
ID=50795018
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210495938.6A Pending CN103830931A (en) | 2012-11-27 | 2012-11-27 | Full-automatic extraction-evaporation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103830931A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20020195329A1 (en) * | 1999-09-06 | 2002-12-26 | Stuart Corr | Apparatus and methods for removing solvent residues |
| US20040016704A1 (en) * | 1999-09-06 | 2004-01-29 | Stuart Corr | Apparatus and method for removing solvent residues |
| CN1775914A (en) * | 2005-11-17 | 2006-05-24 | 中国矿业大学 | Oil coal cinder extracting process and equipment |
| CN1800035A (en) * | 2005-12-21 | 2006-07-12 | 史立皂 | Avermectin-containing waste liquor recovery process |
| CN101172940A (en) * | 2006-11-02 | 2008-05-07 | 中国石油化工股份有限公司 | Extractive agent for recycling acetic acid in dilute acetic acid |
| CN101596373A (en) * | 2009-06-16 | 2009-12-09 | 河南金龙工程技术有限公司 | Liquid rotary type continuous extraction process and device |
-
2012
- 2012-11-27 CN CN201210495938.6A patent/CN103830931A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20020195329A1 (en) * | 1999-09-06 | 2002-12-26 | Stuart Corr | Apparatus and methods for removing solvent residues |
| US20040016704A1 (en) * | 1999-09-06 | 2004-01-29 | Stuart Corr | Apparatus and method for removing solvent residues |
| CN1775914A (en) * | 2005-11-17 | 2006-05-24 | 中国矿业大学 | Oil coal cinder extracting process and equipment |
| CN1800035A (en) * | 2005-12-21 | 2006-07-12 | 史立皂 | Avermectin-containing waste liquor recovery process |
| CN101172940A (en) * | 2006-11-02 | 2008-05-07 | 中国石油化工股份有限公司 | Extractive agent for recycling acetic acid in dilute acetic acid |
| CN101596373A (en) * | 2009-06-16 | 2009-12-09 | 河南金龙工程技术有限公司 | Liquid rotary type continuous extraction process and device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104946303B (en) | A kind of method of phenol mixture in Selective Separation oil | |
| WO2011008924A3 (en) | Recovery of butanol from a mixture of butanol, water and an organic extractant | |
| CN103897009B (en) | A kind of separation method of tall oil | |
| CN102071100A (en) | Method for extracting grease from wet alga mud by using mixed organic solvent | |
| CN105176689A (en) | Method for improving extraction rate of chamomilia essential oil | |
| TW200618850A (en) | Method of separating and recovering phosphoric acid from mixed acid waste liquid containing acetic, nitric and phosphoric acids | |
| WO2011098889A3 (en) | Process for the recovery of oils from a solid matrix | |
| CN103242880A (en) | High-quality impregnant asphalt production process | |
| CN203281070U (en) | Full-automatic high-efficiency low-emulsification liquid-liquid extraction device | |
| CN107416936A (en) | A kind of composite extractant for extracting dihydric phenols material and its production and use | |
| CN104945463A (en) | Extracting method for tea saponin | |
| CN104478785A (en) | Method for enriching indole substances from wash oil of coal tar | |
| CN102319517A (en) | Extraction tank | |
| CN105368473A (en) | Device and process for separating coal tar components | |
| CN103830931A (en) | Full-automatic extraction-evaporation device | |
| CN104707549B (en) | A kind of device and method reclaiming chromatographic grade organic reagent from organic reagent waste liquid | |
| CN205164188U (en) | Continuous extraction device is used to chinese -medicinal material | |
| CN108004016A (en) | A kind of preparation method of the antarctic krill oil of high lecithin content | |
| CN201208517Y (en) | Natural herbals light-oil heavy-oil extraction device | |
| CN211411078U (en) | Continuous extraction instant separation device | |
| CN105164234B (en) | The manufacturing method of ashless coal | |
| CN101029277A (en) | Method for recovering mixed oil by cottonseed protein extracting process | |
| CN107400049A (en) | The separation method of non-solvent component in a kind of ketone benzene binary solvent | |
| CN203281064U (en) | Automatic solid-liquid extraction device | |
| CN202207477U (en) | Extraction tank |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20140604 |