CN202237362U - Continuous extracting device - Google Patents

Continuous extracting device Download PDF

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Publication number
CN202237362U
CN202237362U CN2011203082452U CN201120308245U CN202237362U CN 202237362 U CN202237362 U CN 202237362U CN 2011203082452 U CN2011203082452 U CN 2011203082452U CN 201120308245 U CN201120308245 U CN 201120308245U CN 202237362 U CN202237362 U CN 202237362U
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CN
China
Prior art keywords
extracting
kettle
outlet
liquid
extractant
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.)
Withdrawn - After Issue
Application number
CN2011203082452U
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Chinese (zh)
Inventor
陈文阳
陈文飞
李康
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CHANGZHOU HUAREN CHEMICAL Co Ltd
Original Assignee
CHANGZHOU HUAREN CHEMICAL Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by CHANGZHOU HUAREN CHEMICAL Co Ltd filed Critical CHANGZHOU HUAREN CHEMICAL Co Ltd
Priority to CN2011203082452U priority Critical patent/CN202237362U/en
Application granted granted Critical
Publication of CN202237362U publication Critical patent/CN202237362U/en
Anticipated expiration legal-status Critical
Withdrawn - After Issue legal-status Critical Current

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Abstract

The utility model discloses a continuous extracting device, which comprises an extracting kettle and a distilling kettle. The extracting kettle is provided with a material inlet, an extracting liquid outlet and an extracting agent liquid returning port; the distilling kettle is provided with an extracting liquid inlet, a solute outlet and an extracting agent steam outlet; the extracting liquid outlet of the extracting kettle is connected with the extracting liquid inlet of the distilling kettle through an extracting liquid pipe; the extracting agent steam outlet of the distilling kettle is connected with the extracting agent liquid returning port of the extracting kettle through an extracting agent pipe; and the ratio of a distance H2 between the extracting liquid outlet and a liquid level in the extracting kettle to a distance H1 between the extracting liquid outlet and the extracting liquid inlet is equal to the density ratio of a high-density extracting agent and the low-density original solvent. By using the device provided by the utility model, the whole extracting process can be guaranteed to be carried out continuously, and the manual operation is not needed. Furthermore, due to the design, the height of the whole extracting device can be decreased, and the requirements on a work site are not high.

Description

A kind of continuous extraction apparatus
Technical field
The utility model relates to a kind of chemical engineering unit operation equipment, is specifically related to a kind of continuous extraction apparatus.
Background technology
At present a lot of extraction equipments all need manually-operated, and can't carry out continuous extraction, greatly reduce extraction efficiency like this.The height of whole extraction equipment is very high in addition, has relatively high expectations for the production place.
The utility model content
The purpose of the utility model is to address the above problem, and provides a kind of and need not manually-operated, to the less demanding continuous extraction apparatus in production place.
The technical scheme that realizes the utility model purpose is: a kind of continuous extraction apparatus comprises extraction kettle and distillation still; Said extraction kettle is provided with charging aperture, extract outlet and extractant liquid return hole; Said distillation still is provided with extract import, solute outlet and extractant and steams mouth; The extract outlet of said extraction kettle is connected with the extract import of said distillation still through liquid extraction pipe; The extractant of said distillation still steams mouth and is connected with the extractant liquid return hole of said extraction kettle through the extractant pipe; The ratio of the distance H 1 between the distance H 2 between the liquid level in outlet of said extract and the extraction kettle and outlet of said extract and the said extract import equals the density ratio of high density extractant and the former solvent of low-density.
The extractant liquid return hole of said extraction kettle is provided with cooling sprayer.
The good effect that the utlity model has: the device of the utility model makes the ratio of the distance between the extract import of extract outlet and distillation still of extract outlet and distance between the liquid level in the extraction kettle and extraction kettle of extraction kettle equal the density ratio of the lower former solvent of the higher extractant of density and density; Make that like this pressure of extraction kettle and distillation still is identical; Thereby guarantee that whole extraction process can carry out continuously, and need not manually-operated.And this design can be so that the height of whole extraction equipment be minimized, and is less demanding to the production place.
Description of drawings
Fig. 1 is the structural representation of the continuous extraction apparatus of the utility model.
Mark in the above-mentioned accompanying drawing is following:
Extraction kettle 1, charging aperture 11, extract outlet 12, extractant liquid return hole 13,
Distillation still 2, extract import 21, solute outlet 22, extractant steam mouth 23,
Liquid extraction pipe 3, extractant pipe 4, cooling sprayer 5.
The specific embodiment
See Fig. 1, the continuous extraction apparatus of present embodiment comprises extraction kettle 1 and distillation still 2.
Extraction kettle 1 is provided with charging aperture 11, extract outlet 12 and extractant liquid return hole 13.Distillation still 2 is provided with extract import 21, solute outlet 22 and extractant and steams mouth 23.
The extract outlet 12 of extraction kettle 1 is connected with the extract import 21 of distillation still 2 through liquid extraction pipe 3.The extractant of distillation still 2 steams mouth 23 and is connected with the extractant liquid return hole 13 of extraction kettle 1 through extractant pipe 4.
The ratio of the distance H 1 between the extract outlet 12 of distance H 2 between the liquid level in outlet 12 of the extract of extraction kettle 1 and the extraction kettle 1 and extraction kettle 1 and the extract import 21 of distillation still 2 equals the density ratio of high density extractant and the former solvent of low-density.
The extractant liquid return hole 13 of extraction kettle 1 is provided with cooling sprayer 5.
Adopt method that the continuous extraction apparatus of present embodiment carries out continuous extraction (is example with the bromine in the chloroform extraction water) as follows:
1. chloroform (extractant) and brominated water (feed liquid) are together joined the extraction kettle 1 from charging aperture 11; Make bromine and layering in the chloroform extraction water, the ratio of the distance H 1 between distance H 2 between the liquid level of chloroform that is added and brominated water and the extract outlet 12 and extract import 21 and the extraction kettle outlet 12 equals the density ratio of chloroform and water.
2. the brominated chloroform (extract) of lower floor is discharged from extract outlet 12, and feed the distillation still 2 from extract import 21 through liquid extraction pipe 3.Keeping simultaneously joins brominated water the extraction kettle 1 from charging aperture 11, and remains the density ratio that ratio that distance H 2 and extract import 21 and extraction kettle between liquid level in the extraction kettle 1 (water and a small amount of undischarged brominated chloroform by being positioned at the upper strata after initiate brominated water, the extraction are formed) and the extract outlet 12 export the distance H 1 between 12 equals chloroform and water.
3. the brominated chloroform in the distillation still 2 is distilled; The chloroform that distills out is steamed mouthful 23 discharges from extractant; And feed cooling sprayers 5 from extractant liquid return hole 13 through extractant pipe 4, after supercooling, get back in the extraction kettle 1 recycling through spray equipment.This process remains the density ratio that ratio that distance H 2 and extract import 21 and extraction kettle between liquid level in the extraction kettle 1 (chloroform by being positioned at water, a small amount of undischarged brominated chloroform on upper strata after initiate brominated water, the extraction and getting back to extraction kettle 1 is formed) and the extract outlet 12 export the distance H 1 between 12 equals chloroform and water.The bromine that obtains after the distillation is then discharged from solute outlet 22.

Claims (2)

1. a continuous extraction apparatus is characterized in that: comprise extraction kettle (1) and distillation still (2); Said extraction kettle (1) is provided with charging aperture (11), extract outlet (12) and extractant liquid return hole (13); Said distillation still (2) is provided with extract import (21), solute outlet (22) and extractant and steams mouthful (23); The extract outlet (12) of said extraction kettle (1) is connected with the extract import (21) of said distillation still (2) through liquid extraction pipe (3); The extractant of said distillation still (2) steams mouthful (23) and is connected with the extractant liquid return hole (13) of said extraction kettle (1) through extractant pipe (4);
The ratio that distance H 2 between the liquid level in said extract outlet (12) and the extraction kettle (1) and said extract export the distance H 1 between (12) and the said extract import (21) equals the density ratio of high density extractant and the former solvent of low-density.
2. continuous extraction apparatus according to claim 1 is characterized in that: the extractant liquid return hole (13) of said extraction kettle (1) is provided with cooling sprayer (5).
CN2011203082452U 2011-08-23 2011-08-23 Continuous extracting device Withdrawn - After Issue CN202237362U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011203082452U CN202237362U (en) 2011-08-23 2011-08-23 Continuous extracting device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011203082452U CN202237362U (en) 2011-08-23 2011-08-23 Continuous extracting device

Publications (1)

Publication Number Publication Date
CN202237362U true CN202237362U (en) 2012-05-30

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011203082452U Withdrawn - After Issue CN202237362U (en) 2011-08-23 2011-08-23 Continuous extracting device

Country Status (1)

Country Link
CN (1) CN202237362U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102380229A (en) * 2011-08-23 2012-03-21 常州市华人化工有限公司 Continuous extraction device and continuous extraction method adopting same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102380229A (en) * 2011-08-23 2012-03-21 常州市华人化工有限公司 Continuous extraction device and continuous extraction method adopting same

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C14 Grant of patent or utility model
GR01 Patent grant
AV01 Patent right actively abandoned

Granted publication date: 20120530

Effective date of abandoning: 20131002

RGAV Abandon patent right to avoid regrant