CN208711084U - A kind of novel organic solvent purification recovery device - Google Patents
A kind of novel organic solvent purification recovery device Download PDFInfo
- Publication number
- CN208711084U CN208711084U CN201821407308.8U CN201821407308U CN208711084U CN 208711084 U CN208711084 U CN 208711084U CN 201821407308 U CN201821407308 U CN 201821407308U CN 208711084 U CN208711084 U CN 208711084U
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- distillery
- pedestal
- fixedly installed
- inlet tube
- organic solvent
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Abstract
A kind of novel organic solvent purification recovery device, the utility model relates to chemical equipment technical fields, and distillery is wherein fixedly installed on pedestal, and distillery is tilted to be provided with volatilization plate；Head tank is fixedly installed on pedestal, the bottom of head tank is equipped with inlet tube, and parallel connection is equipped with several capillaries on inlet tube, and the oral area of capillary, which supports, to be located on the high-end upper surface of volatilization plate；Condensation chamber is fixedly installed on pedestal, the upper end of distillery, which is worn, is fixed with gas-guide tube；It utilizes the principle of fluid pressure, and head tank, distillery and condensation chamber height are arranged in a staggered manner, the use of electric appliance is reduced, it reduces equipment and produces pyrophoric probability, stoste is shared on muti-piece volatilization plate and is volatilized, increases its working efficiency by the safety that ensure that equipment.
Description
Technical field
The utility model relates to chemical equipment technical fields, and in particular to a kind of novel organic solvent purification recovery device.
Background technique
Common organic solvent has acetone, alcohol, ethyl acetate, toluene etc., these organic solvents are commonly used in industry and set
In standby cleaning process, the spent organic solvent after participating in work, which can be recycled, to be recycled, and reduces production cost；Organic solvent recycling is normal
Using its volatile feature, by the method for distillation, the impurity in organic solvent is removed, obtains clean recycling having
Solvent；Common organic solvent all have the characteristics that it is inflammable and explosive, when being distilled to recover, it is ensured that reclaimer
Leakproofness and explosion-proof, guarantee the personal safety of operator.
Utility model content
The purpose of this utility model is that in view of the drawbacks of the prior art and insufficient, provide that a kind of structure is simple, design is closed
Reason, novel organic solvent purification recovery device easy to use, utilize fluid pressure principle, by head tank, distillery and
Condensation chamber height is arranged in a staggered manner, and reduces the use of electric appliance, reduces equipment and produces pyrophoric probability, ensure that the safety of equipment
Property, stoste is shared on muti-piece volatilization plate and is volatilized, its working efficiency is increased.
In order to achieve the above purposes, the technical solution adopted by the utility model is:, and it includes pedestal, distillery, volatilization plate, adds
Heated filament is wherein fixedly installed distillery on pedestal, distillery is tilted to be provided with volatilization plate, and several piece volatilization plate is parallel up and down
It is arranged, is fixedly installed heater strip on the lower surface for the plate that volatilizees；Head tank is fixedly installed on pedestal, and the bottom of head tank is high
It is arranged in the top of distillery, the bottom of head tank is equipped with inlet tube, and the other end of inlet tube is threaded through in distillery, and into
Liquid pipe is fixed on the inner sidewall of distillery, and parallel connection is equipped with several capillaries on inlet tube, and the oral area of capillary, which supports, to be set
On the high-end upper surface of volatilization plate；Condensation chamber is fixedly installed on pedestal, and the bottom of condensation chamber is higher than the top of distillery
Setting, the upper end of distillery, which is worn, is fixed with gas-guide tube, and the other end of gas-guide tube wears the side wall lower ends for being fixed on condensation chamber；Institute
The lower end for the distillery stated is fixedly installed waste material box, and holding vessel, and the top of holding vessel are fixedly installed on the pedestal
Bottom lower than condensation chamber is arranged, and the lower end of condensation chamber, which is worn, is fixed with catheter, and the other end of catheter, which is worn, is fixed on storage
It deposits on tank.
Further, the bottom plate of the distillery and pedestal, which are integrally formed, is arranged, and is fixedly installed sliding rail on pedestal, and
Sliding rail is threaded through in distillery, and waste material box is slidably arranged on sliding rail, and waste material box activity after the side wall of distillery plugs
In distillery.
Further, flow control valve has been arranged in series on the inlet tube.
Further, filter chamber is fixedly installed on the pedestal, is fixedly installed strainer in filter chamber, it is described into
It has been arranged in series flow-stop valve in liquid pipe, No.1 pipe has been equipped on the inlet tube of flow-stop valve side, and the other end of No.1 pipe is worn
In the filter chamber of strainer side, No. two pipes are equipped on the inlet tube of the flow-stop valve other side, and the other end of No. two pipes is worn
In the filter chamber of the strainer other side.
Further, the surrounding of the pedestal is fixedly installed Air Filter.
After adopting the above structure, the utility model has the beneficial effect that a kind of novel organic solvent described in the utility model
Purification recovery device utilizes the principle of fluid pressure, and head tank, distillery and condensation chamber height are arranged in a staggered manner, reduced
The use of electric appliance reduces equipment and produces pyrophoric probability, ensure that the safety of equipment, and stoste is shared muti-piece volatilization
It volatilizees on plate, increases its working efficiency, the utility model has structure simple, and rationally, it is excellent that cost of manufacture is low etc. for setting
Point.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor
Under, it is also possible to obtain other drawings based on these drawings.
Fig. 1 is the structural schematic diagram of the utility model.
Fig. 2 is the top view of Fig. 1.
Fig. 3 is filter chamber's the schematic diagram of the section structure in the utility model.
Fig. 4 is the distillery the schematic diagram of the section structure in the utility model.
Description of symbols:
Pedestal 1, distillery 2, volatilization plate 3, heater strip 4, head tank 5, inlet tube 6, capillary 7, condensation chamber 8, gas-guide tube
9, waste material box 10, holding vessel 11, catheter 12, sliding rail 13, flow control valve 14, filter chamber 15, strainer 16, flow-stop valve 17, one
Number pipe 18, No. two pipes 19, Air Filters 20.
Specific embodiment
The utility model will be further described below with reference to the accompanying drawings.
Referring to as Figure 1-Figure 4, present embodiment includes pedestal 1, distillery 2, volatilization plate 3, heater strip 4,
Distillery 2 is welded on middle pedestal 1, distillery 2 is tilted to be provided with volatilization plate 3, and the both sides of volatilization plate 3 are weldingly fixed on
On the inner sidewall of distillery 2, and three blocks of identical about 3 volatilization plates are arranged in parallel, and it is solid to be embedded welding on the lower surface for the plate 3 that volatilizees
Surely there is heater strip 4, heater strip 4 whole to volatilization plate 3 can heat；Riveting is fixed with head tank 5, and head tank 5 on pedestal 1
Bottom be higher than the top of distillery 2 and be arranged, the bottom of head tank 5 is equipped with inlet tube 6, and the other end of inlet tube 6 is threaded through
In distillery 2, and the riveting of 6 snap ring of inlet tube is fixed on the inner sidewall of distillery 2, and the liquid in the head tank 5 of eminence can be certainly
In the dynamic distillery 2 for flowing into lower by inlet tube 6, parallel connection is equipped with three capillaries 7, the oral area of capillary 7 on inlet tube 6
To be located at volatilization the high-end place of plate 3 upper surface on；Riveting is fixed with condensation chamber 8 on pedestal 1, and the bottom of condensation chamber 8 is higher than steaming
The top setting of room 2 is evaporated, the upper end of distillery 2, which is worn, is fixed with gas-guide tube 9, and the other end of gas-guide tube 9, which is worn, is fixed on condensation
The side wall lower ends of room 8；The lower end of the distillery 2, which plugs, is fixed with waste material box 10, and riveting is fixed with storage on the pedestal 1
Tank 11 is deposited, and the top of holding vessel 11 is arranged lower than the bottom of condensation chamber 8, the lower end of condensation chamber 8, which is worn, is fixed with catheter 12,
The other end of catheter 12, which is worn, to be fixed on holding vessel 11.
Further, the bottom plate of the distillery 2 and pedestal 1, which are integrally formed, is arranged, and is welded with sliding rail on pedestal 1
13, and sliding rail 13 is threaded through in distillery 2, waste material box 10 is slidably arranged on sliding rail 13, and waste material box 10 passes through distillery 2
Activity is plugged in distillery 2 after side wall, and waste material box 10 can be extracted out after filling and be replaced.
Further, it has been arranged in series flow control valve 14 on the inlet tube 6, flow control valve 14 can control feed liquor
Flow velocity in pipe 6.
Further, riveting is fixed with filter chamber 15 on the pedestal 1, is welded with strainer vertically in filter chamber 15
16, be arranged in series flow-stop valve 17 on the inlet tube 6, and the setting of flow-stop valve 17 flow control valve 14 and head tank 5 it
Between, flow-stop valve 17 is equipped with No.1 pipe 18 on the inlet tube 6 of 5 side of head tank, and the other end of No.1 pipe 18 is threaded through
In the filter chamber 15 of 16 side of strainer, it is equipped with No. two pipes 19 on the inlet tube 6 of 17 other side of flow-stop valve, and No. two pipes 19 is another
One end is threaded through in the filter chamber 15 of 16 other side of strainer, when the solid impurity in organic solvent to be processed is more, is closed
Flow-stop valve 17 is closed, organic solvent to be processed can be filtered in filter chamber 15.
Further, the surrounding riveting of the pedestal 1 is fixed with Air Filter 20, and Air Filter 20 can block to be generated in production
Spark, guarantee safety.
The working principle of this specific embodiment: being: the volatilization plate 3 in distillery 2 is heated by heater strip 4, to
The organic solvent (hereinafter referred to as stoste) of Recovery Purifying is stored in head tank 5, is controlled in inlet tube 6 by flow control valve 14
Stoste flowing velocity, stoste by inlet tube 6 flow into distillery 2, and by capillary 7 flow to respectively volatilization plate 3 on, high temperature
Volatilization plate 3 to stoste thereon carry out heating make its volatilization, after the gaseous state organic solvent in distillery 2 reaches saturation, because of gas
Buckling enters 8 cooling liquid of condensation chamber automatically by gas-guide tube 9, flows into fluid reservoir eventually by catheter 12 and collects storage；
When solid impurity is more in stoste, flow-stop valve 17 is closed, after being filtered stoste in filter chamber 15, enters back into steaming
Evaporate room 2；Remaining non-volatile high concentration stoste flows into waste material box 10 along volatilization plate 3 in distillery 2, to locate in next step
Reason.
After adopting the above structure, present embodiment is advantageously: it utilizes the principle of fluid pressure, will be former
Batch can, distillery and condensation chamber height are arranged in a staggered manner, and reduce the use of electric appliance, reduce equipment and produce pyrophoric probability, protect
Stoste is shared on muti-piece volatilization plate and is volatilized, increases its working efficiency by the safety for having demonstrate,proved equipment.
The above is merely intended for describing the technical solutions of the present application, but not for limiting the present application, those of ordinary skill in the art couple
The other modifications or equivalent replacement that the technical solution of the utility model is made, without departing from technical solutions of the utility model
Spirit and scope should all cover in the scope of the claims of the utility model.
Claims (5)
1. a kind of novel organic solvent purification recovery device, it is characterised in that: it includes pedestal (1), distillery (2), volatilization plate
(3), heater strip (4) are wherein fixedly installed distillery (2) on pedestal (1), and distillery (2) is tilted to be provided with volatilization plate
(3), and several piece volatilization plate (3) is arranged in parallel up and down, is fixedly installed heater strip (4) on the lower surface of volatilization plate (3)；Pedestal
(1) it is fixedly installed on head tank (5), and the bottom of head tank (5) is higher than the top setting of distillery (2), head tank (5)
Bottom is equipped with inlet tube (6), and the other end of inlet tube (6) is threaded through in distillery (2), and inlet tube (6) is fixed at
On the inner sidewall of distillery (2), parallel connection is equipped with several capillaries (7) on inlet tube (6), and the oral area of capillary (7), which supports, to be located at
It volatilizees on plate (3) high-end upper surface；It is fixedly installed on pedestal (1) condensation chamber (8), and the bottom of condensation chamber (8) is higher than steaming
The top setting of room (2) is evaporated, the upper end of distillery (2), which is worn, to be fixed with gas-guide tube (9), and the other end of gas-guide tube (9) wears solid
It is scheduled on the side wall lower ends of condensation chamber (8)；The lower end of the distillery (2) is fixedly installed waste material box (10), the pedestal
(1) it is fixedly installed on holding vessel (11), and the top of holding vessel (11) is arranged lower than the bottom of condensation chamber (8), condensation chamber (8)
Lower end wear and be fixed with catheter (12), the other end of catheter (12), which is worn, to be fixed on holding vessel (11).
2. a kind of novel organic solvent purification recovery device according to claim 1, it is characterised in that: the distillery
(2) bottom plate and pedestal (1), which is integrally formed, to be arranged, and is fixedly installed sliding rail (13) on pedestal (1), and sliding rail (13) is threaded through steaming
It evaporates in room (2), waste material box (10) is slidably arranged on sliding rail (13), and waste material box (10) is living after the side wall of distillery (2)
It is dynamic to be plugged in distillery (2).
3. a kind of novel organic solvent purification recovery device according to claim 1, it is characterised in that: the inlet tube
(6) flow control valve (14) have been arranged in series on.
4. a kind of novel organic solvent purification recovery device according to claim 1, it is characterised in that: the pedestal
(1) it is fixedly installed filter chamber (15), is fixedly installed strainer (16) in filter chamber (15), the inlet tube is gone here and there on (6) on
Connection is provided with flow-stop valve (17), is equipped with No.1 pipe (18) on the inlet tube (6) of flow-stop valve (17) side, and No.1 pipe (18)
The other end is threaded through in the filter chamber (15) of strainer (16) side, is equipped with two on the inlet tube (6) of flow-stop valve (17) other side
Number pipe (19), and No. two pipe (19) the other ends be threaded through in the filter chamber (15) of strainer (16) other side.
5. a kind of novel organic solvent purification recovery device according to claim 1, it is characterised in that: the pedestal
(1) surrounding is fixedly installed Air Filter (20).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821407308.8U CN208711084U (en) | 2018-08-30 | 2018-08-30 | A kind of novel organic solvent purification recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821407308.8U CN208711084U (en) | 2018-08-30 | 2018-08-30 | A kind of novel organic solvent purification recovery device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208711084U true CN208711084U (en) | 2019-04-09 |
Family
ID=65980243
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821407308.8U Expired - Fee Related CN208711084U (en) | 2018-08-30 | 2018-08-30 | A kind of novel organic solvent purification recovery device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208711084U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111760317A (en) * | 2020-07-14 | 2020-10-13 | 常州海克莱化学有限公司 | Conveying device of vacuum distillation equipment |
-
2018
- 2018-08-30 CN CN201821407308.8U patent/CN208711084U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111760317A (en) * | 2020-07-14 | 2020-10-13 | 常州海克莱化学有限公司 | Conveying device of vacuum distillation equipment |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20190409 Termination date: 20190830 |