CN206823220U - A kind of novel extraction actual training device - Google Patents
A kind of novel extraction actual training device Download PDFInfo
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- CN206823220U CN206823220U CN201621297813.2U CN201621297813U CN206823220U CN 206823220 U CN206823220 U CN 206823220U CN 201621297813 U CN201621297813 U CN 201621297813U CN 206823220 U CN206823220 U CN 206823220U
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Abstract
It the utility model is related to a kind of novel extraction actual training device, including by heavy phase liquid storage tank, extraction phase storage tank, light phase liquid storage tank, raffinate phase storage tank, raffinate phase separation tank, compressed air surge tank, extraction tower, heavy phase pump, light phase pump group into circulation line, be additionally provided with circulation line at least one in following disturbance point：Gas pulse frequency disturbance point is provided between the extraction tower and compressed air surge tank；Gas pulse flow rate disturbance point is provided between the extraction tower and compressed air surge tank；Extraction phase concentration perturbation point is provided between the extraction tower and heavy phase liquid storage tank；Also include spiral heat exchange tube, the spiral heat exchange tube is sheathed on heavy phase liquid storage tank periphery.The utility model is provided with spiral heat exchange tube and heat-exchanging water tank, and spiral heat exchange tube is sheathed on heavy phase liquid storage tank periphery, can carry out uniform heat exchange with heavy-phase liquid in heavy phase liquid storage tank, while vibrator can increase liquid turbulence in heavy phase liquid storage tank, be heated evenly it.
Description
Technical field
The utility model belongs to Chemical Manufacture analogue means field, more particularly to a kind of novel extraction actual training device.
Background technology
Traditional extraction experiments device is by heavy-phase liquid storage tank, extraction phase storage tank, light phase storage tank, raffinate phase storage tank, raffinate point
Phase tank, extraction tower, compressed air surge tank, pump etc. form, and are used for the students such as student, Plant personnel experiment or orientation.
Its shortcoming is：Although student can favorably accomplish experiment, it is only capable of being familiar with flow principle and the effect of extraction experiments device, and
Manipulative ability, operative skill cannot improve, to practice in factory also without actual cognition；Equally, factory new employee is entering factory
When, often only in a short time, the equipment of normal operation and production process are familiar with by technical staff's guidance, to actual production
In the failure being likely encountered and the method fixed a breakdown be still to know nothing.Because operating personnel lack hands-on, also just lack
Weary analysis failure, the ability fixed a breakdown, therefore once break down, production safety and the quality of product will be influenceed.For solution
Certainly this problem, my the patent CN200620027109.5 of company personnel's application disclose extraction actual training device, including by heavy phase
Liquid storage tank, extraction phase storage tank, light phase storage tank, raffinate phase storage tank, raffinate phase separation tank, extraction tower, compressed air surge tank, pump institute group
Into circulation line, be additionally provided with least one in following disturbance point：The extraction tower and the compressed air surge tank it
Between be provided with gas pulse frequency disturbance point；Gas pulse stream is provided between the extraction tower and the compressed air surge tank
Measure disturbance point；Boundary position disturbance point is provided between the extraction tower and the extraction phase separation tank；The extraction tower and institute
State and be provided with extraction phase concentration perturbation point between heavy phase tank；Described quench remaining is connected with the first pipe between phase storage tank and the light phase pump
Road, the input concentration disturbance point of phase liquid is provided between the light phase storage tank and first pipeline；In the heavy phase liquid storage tank
Thermal perturbation point is provided with, however, the utility model also Shortcomings, the temperature that one side thermal perturbation point has improves not clear
It is aobvious, and heated the shortcomings that uneven because local heating often occurs, the height that heavy-phase liquid is fallen in another aspect extraction tower
Also extraction efficiency can be influenceed, and this disturbance point is not referred in conventional patent, therefore, based on these problems, there is provided Yi Zhongneng
Quick and uniformly rise heavy-phase liquid temperature, while the extraction actual training device for increasing disturbance point in extraction tower has important reality
Meaning.
Utility model content
The purpose of this utility model is overcome the deficiencies in the prior art, there is provided a kind of novel extraction actual training device, this reality
Be provided with spiral heat exchange tube and heat-exchanging water tank with new, the water in heat-exchanging water tank under agitating paddle and electric heater collective effect
Even heating, spiral heat exchange tube are sheathed on heavy phase liquid storage tank periphery, can carry out uniform heat exchange with heavy-phase liquid in heavy phase liquid storage tank, together
When vibrator can increase liquid turbulence in heavy phase liquid storage tank, be heated evenly it so that heavy-phase liquid tank temperature is obviously improved, and is added
It is hot uniform.
The utility model solves its technical problem and takes following technical scheme to realize：
A kind of novel extraction actual training device, including stored up by heavy phase liquid storage tank, extraction phase storage tank, light phase liquid storage tank, raffinate phase
Tank, raffinate phase separation tank, compressed air surge tank, extraction tower, heavy phase pump, light phase pump group into circulation line, in circulation line
It is additionally provided with least one in following disturbance point：Gas pulse frequency is provided between the extraction tower and compressed air surge tank
Rate disturbance point；Gas pulse flow rate disturbance point is provided between the extraction tower and compressed air surge tank；The extraction tower with
Extraction phase concentration perturbation point is provided between heavy phase liquid storage tank；Set light phase dense between the light phase liquid storage tank and the light phase pump
Spend disturbance point；Raffinate phase concentration perturbation point is set between the raffinate phase storage tank and the raffinate phase separation tank；The extraction tower with
Boundary position disturbance point is set between the raffinate phase separation tank；Also include spiral heat exchange tube, the spiral heat exchange pipe sleeve
Located at heavy phase liquid storage tank periphery, the input of the spiral heat exchange tube is connected by inlet channel with heat-exchanging water tank, the spiral shell
The output end of rotation shape heat exchanger tube is connected by outlet conduit with heat-exchanging water tank, and the inlet channel is provided with water pump, the heavy phase
Be provided with vibrator on the outside of liquid storage tank, the extraction tower is interior to be placed with the first distributor, the second distributor, the 3rd under upper successively
Distributor, first distributor, the second distributor, the 3rd distributor pass through the first pipeline, second pipe, the 3rd pipeline respectively
It is affixed with heavy-phase liquid conveyance conduit；
The inlet channel is provided with heavy-phase liquid thermal perturbation point, and the heavy-phase liquid thermal perturbation point is the first regulation electromagnetism
Valve is in parallel with the second electromagnetic valve for adjusting to be formed, and first electromagnetic valve for adjusting is on inlet channel, the second regulation electromagnetism
Valve is on branch's inlet channel；
Electric heater is provided with the heat-exchanging water tank, the heat-exchanging water tank central upper portion position is provided with motor, the motor
Output end be connected with the agitating paddle in the heat-exchanging water tank；
Also include heavy-phase liquid distributed disturbance point, the heavy-phase liquid distributed disturbance point is the 3rd electromagnetic valve for adjusting, the 4th regulation
Magnetic valve, the 5th electromagnetic valve for adjusting are in parallel to be formed, the 3rd electromagnetic valve for adjusting, the 4th electromagnetic valve for adjusting, the 5th regulation electromagnetism
Valve is respectively arranged in the first pipeline, second pipe, on the 3rd pipeline.
Further, one end of the gas pulse flow rate disturbance point passes through pipeline and the gas pulse frequency disturbance point
Connection, its other end are connected by pipeline with the compressed air surge tank.
Further, the gas pulse frequency disturbance point, gas pulse flow rate disturbance point, extraction phase concentration perturbation point,
Light phase concentration perturbation point, raffinate phase concentration perturbation point, boundary position disturbance point are respectively that stop valve and normally open solenoid valve are in parallel
Form.
Further, in the circulation line, be provided with each contact or branch road magnetic valve, ball valve or pressure gauge,
Or thermometer or liquid level gauge or flowmeter or flow indicator or sample tap.
The advantages of the utility model and good effect are：
1. the utility model is provided with spiral heat exchange tube and heat-exchanging water tank, the water in heat-exchanging water tank is in agitating paddle and electrical heating
Uniformly heated under device collective effect, spiral heat exchange tube is sheathed on heavy phase liquid storage tank periphery, can be with heavy-phase liquid in heavy phase liquid storage tank
Uniform heat exchange is carried out, while vibrator can increase liquid turbulence in heavy phase liquid storage tank, be heated evenly it so that heavy phase liquid storage tank
Temperature is obviously improved, homogeneous heating.
2. the utility model sets up heavy-phase liquid distributed disturbance point, the first distribution is placed with successively under upper in extraction tower
Device, the second distributor, the 3rd distributor, can change the height that heavy-phase liquid is fallen in extraction tower, further simulate in actual production
The failure being likely encountered.
Brief description of the drawings
The technical solution of the utility model is described in further detail below with reference to drawings and examples, still
It should be known that these accompanying drawings only design for task of explanation, therefore not as the restriction of the scope of the utility model.In addition,
Unless otherwise indicated, these accompanying drawings are meant only to conceptually illustrate structure construction described herein, without to carry out to scale
Draw.
Fig. 1 is the utility model structure diagram；
Fig. 2 is I regions enlarged diagram in Fig. 1；
Fig. 3 is off valve and is connected in parallel schematic diagram with normally open solenoid valve.
In figure：1. heavy phase liquid storage tank, 2. extraction phase storage tanks, 3. light phase liquid storage tanks, 4. raffinate phase storage tanks, 5. raffinate split-phases
Tank, 6. compressed air surge tanks, 7. extraction towers, 8. heavy phase pumps, 9. light phase pumps, 10. spiral heat exchange tubes, 11. inlet channels,
12. heat-exchanging water tank, 13. outlet conduits, 14. water pumps, 15. vibrators, 16. first distributors, 17. second distributors, 18.
Three distributors, 19. first pipelines, 20. second pipes, 21. the 3rd pipelines, 22. heavy-phase liquid conveyance conduits, 23. first regulation electricity
Magnet valve, 24. second electromagnetic valve for adjusting, 25. branch's inlet channels, 26. electric heaters, 27. motors, 28. agitating paddles, 29. the 3rd
Electromagnetic valve for adjusting, 30. the 4th electromagnetic valve for adjusting, 31. the 5th electromagnetic valve for adjusting, 32. stop valves, 33. normally open solenoid valves, A. gas phases
Pulse frequency disturbance point, B. gas pulses flow rate disturbance point, C. extraction phases concentration perturbation point, D. light phases concentration perturbation point, E. extractions
Remaining phase concentration disturbance point, F. boundaries position disturbance point, H. heavy-phase liquids thermal perturbation point, G. heavy-phase liquids distributed disturbance point, PI.
Pressure gauge, TI. thermometers, LI. liquid level gauges, FV. flowmeters, FI. flow indicators, AI. sample taps.
Embodiment
Firstly, it is necessary to explanation, will illustrate concrete structure of the present utility model, feature by way of example below
With advantage etc., but all descriptions are intended merely to what is illustrated, and should not be construed as forming the utility model and appoint
What is limited.In addition, any single technical characteristic for being described by or implying in each embodiment mentioned by this paper, or it is shown
Or implicit any single technical characteristic in the drawings, still can continue between these technical characteristics (or its equivalent) into
Row any combination is deleted, so as to obtain the more other embodiments of the present utility model that may do not referred to directly herein.
In addition, for the sake of simplifying drawing, same or like technical characteristic may be indicated only at one in the same figure.
It will be understood that when it is said that part ' attach ' into another part, it can be directly connected to another part or
There may be intermediate member.On the contrary, when it is said that part " being directly connected to " is arrived into another part, then it represents that in the absence of pars intermedia
Part.
Fig. 1 is the utility model structure diagram, and Fig. 2 is I regions enlarged diagram in Fig. 1, Fig. 3 be off valve with it is normally opened
Magnetic valve is connected in parallel schematic diagram.Fig. 1, Fig. 2 and Fig. 3 are just combined below to illustrate the utility model.
As Figure 1-3, a kind of novel extraction actual training device, including by heavy phase liquid storage tank 1, extraction phase storage tank 2, light-phase liquid
What storage tank 3, raffinate phase storage tank 4, raffinate phase separation tank 5, compressed air surge tank 6, extraction tower 7, heavy phase pump 8, light phase pump 9 formed follows
Endless tube road, it is additionally provided with circulation line at least one in following disturbance point：The extraction tower 7 and compressed air surge tank
Gas pulse frequency disturbance point A is provided between 6；Gas pulse is provided between the extraction tower 7 and compressed air surge tank 6
Flow rate disturbance point B；Extraction phase concentration perturbation point C is provided between the extraction tower 7 and heavy phase liquid storage tank 1；The light-phase liquid storage
Light phase concentration perturbation point D is set between tank 3 and the light phase pump 9；Between the raffinate phase storage tank 4 and the raffinate phase separation tank 5
Raffinate phase concentration perturbation point E is set；Boundary position disturbance point F is set between the extraction tower 7 and the raffinate phase separation tank 5；
Also include spiral heat exchange tube 10, the spiral heat exchange tube 10 is sheathed on the periphery of heavy phase liquid storage tank 1, the spiral heat exchange tube
10 input is connected by inlet channel 11 with heat-exchanging water tank 12, and the output end of the spiral heat exchange tube 10 passes through outlet pipe
Road 13 is connected with heat-exchanging water tank 12, and the inlet channel 11 is provided with water pump 14, and the outside of heavy phase liquid storage tank 1 is provided with vibration
Device 15, the first distributor 16, the second distributor 17, the 3rd distributor 18, institute are placed with successively under upper in the extraction tower 7
The first distributor 16, the second distributor 17, the 3rd distributor 18 is stated to manage by the first pipeline 19, second pipe the 20, the 3rd respectively
Road 21 and heavy-phase liquid conveyance conduit 22 are affixed；The inlet channel is provided with heavy-phase liquid thermal perturbation point H, the heavy-phase liquid temperature
Disturbance point H is the first electromagnetic valve for adjusting 23 and 24 composition in parallel of the second electromagnetic valve for adjusting, and first electromagnetic valve for adjusting 23 is located at
On inlet channel 11, second electromagnetic valve for adjusting 24 is on branch's inlet channel 25；Electricity is provided with the heat-exchanging water tank 12
Heater 26, the central upper portion position of heat-exchanging water tank 12 are provided with motor 27, and the output end of the motor 27 is with being located at heat-exchanging water
Agitating paddle 28 in case 12 is connected；It is the 3rd regulation also to include heavy-phase liquid distributed disturbance point G, the heavy-phase liquid distributed disturbance point G
Magnetic valve 29, the 4th electromagnetic valve for adjusting 30, the 5th electromagnetic valve for adjusting 31 are in parallel to be formed, the 3rd electromagnetic valve for adjusting the 29, the 4th
Electromagnetic valve for adjusting 30, the 5th electromagnetic valve for adjusting 31 are respectively arranged in the first pipeline 19, second pipe 20, on the 3rd pipeline 21.
One end of the gas pulse flow rate disturbance point B is connected by pipeline with the gas pulse frequency disturbance point A, its
The other end is connected by pipeline with the compressed air surge tank 6.
The gas pulse frequency disturbance point A, gas pulse flow rate disturbance point B, extraction phase concentration perturbation point C, light phase are dense
Degree disturbance point D, raffinate phase concentration perturbation point E, boundary position disturbance point F are respectively that stop valve 32 and normally open solenoid valve 33 are in parallel
Form.
In the circulation line, magnetic valve, ball valve or pressure gauge PI or temperature are provided with each contact or branch road
Count TI or liquid level gauge LI or flowmeter FV or flow indicator FI or sample tap AI.
Operation principle：Heavy-phase liquid is injected from heavy phase liquid storage tank 1 through heavy phase pump 8 from the top of extraction tower 7, and light-phase liquid is stored up by light phase
Tank 3 is injected through light phase pump 9 from the bottom of towe of extraction tower 7, and light, weight two-phase in counter current contacting, is pressed in extraction tower 7 in contact process
Pulse of compressed air mode in contracting air cushioning tank 6 is injected in extraction tower 7, and light-phase liquid is risen and eliminates emulsification, extraction phase
Be discharged into by the bottom of towe of extraction tower 7 in extraction phase storage tank 2, raffinate phase is discharged into raffinate phase separation tank 5 by the tower top of extraction tower 7, raffinate phase by
The top of raffinate phase separation tank 5 is discharged into raffinate phase storage tank 4, can be re-used, and the greasy dirt isolated is arranged by the bottom of raffinate phase separation tank 5
Go out, complete extraction process.
In the utility model, inlet channel is provided with heavy-phase liquid thermal perturbation point H, and heavy-phase liquid thermal perturbation point H is first
24 composition in parallel of electromagnetic valve for adjusting 23 and the second electromagnetic valve for adjusting, heavy phase liquid storage tank 1 are arranged with spiral heat exchange tube 10, spiral outside
The input of shape heat exchanger tube 10 is connected by inlet channel 11 with heat-exchanging water tank 12, and the output end of spiral heat exchange tube 10 is by going out
Waterpipe 13 is connected with heat-exchanging water tank 12, and opening electric heater 26, motor 27, the water of heat-exchanging water tank 12 is heated properly, just
Often in experiment, the first electromagnetic valve for adjusting 23, water pump 14, vibrator 15 are opened, the liquid in heavy phase liquid storage tank 1 is made by uniform heat exchange
Temperature rise is obtained, vibrator 15 can increase liquid turbulence, be heated evenly it, when the first electromagnetic valve for adjusting 23 of closing, heavy-phase liquid
Heavy-phase liquid temperature in storage tank is reduced, and stable procedure parameter is destroyed, and now can open the second electromagnetic valve for adjusting by adjusting
24, hot water is entered spiral heat exchange tube 10 via branch's inlet channel 25, system is recovered stable again.
Heavy-phase liquid distributed disturbance point G is by the 3rd electromagnetic valve for adjusting 29, the 4th electromagnetic valve for adjusting 30, the 5th electromagnetic valve for adjusting 31
Parallel connection is formed, and in normal experiment, opens the 3rd electromagnetic valve for adjusting 29 so that heavy-phase liquid is entered by the first distributor 16 to be extracted
In tower 7, when closing the 3rd electromagnetic valve for adjusting 29, the procedure parameter stablized in extraction tower 7 is destroyed, and can now open the 4th regulation
The electromagnetic valve for adjusting 31 of magnetic valve 30 or the 5th so that heavy-phase liquid enters extraction tower 7 by the second distributor 17, the 3rd distributor 18
It is interior, system is recovered stable again.
Gas pulse frequency disturbance point A is provided between extraction tower 7 and compressed air surge tank 6 to disturb with gas pulse flow
Dynamic point B, gas pulse frequency disturbance point A are stop valve 32 and the composition in parallel of normally open solenoid valve 33, are connected by pipeline, voltage supply
Strength source is by the way that for controlling the gas pulse frequency injected in extraction tower 7, gas pulse flow rate disturbance point B is stop valve 32
With the composition in parallel of normally open solenoid valve 33, gas pulse flow rate disturbance point B one end passes through pipeline and gas pulse frequency disturbance point A
Connection, its other end is connected with compressed air surge tank 6, connected by pipeline, for pressure gas source by control gas phase arteries and veins
Swash of wave amount.Gas pulse frequency disturbance point A is used for controlling gas pulse frequency to change, i.e.,：In normal experiment, normally open solenoid valve
33 be opening, and pressure gas source is entered in extraction tower 7 by pipeline and is used for the emulsification for eliminating light-phase liquid, when the normally opened electricity of change
The open frequency of magnet valve 33, the flow of pressure gas source are changed, and stable parameter is destroyed, and being mainly reflected in can not be complete
The emulsification of light-phase liquid is eliminated, influences experiment effect.Now trouble point can be found in gas pulse frequency disturbance point A by observation
Place, so as to solve failure, can allow pressure gas source to pass through from bypass, system is recovered steady again by adjusting the aperture of stop valve 32
It is fixed.Gas pulse flow rate disturbance point B is used for controlling gas pulse changes in flow rate, i.e.,：In normal experiment, normally open solenoid valve 33 is
Opening, pressure gas source are entered in extraction tower 7 by pipeline and are used for the emulsification for eliminating light-phase liquid, when change normally open solenoid valve 33
Open frequency, the flow of pressure gas source changed, and stable parameter is destroyed, and light phase can not be completely eliminated by being mainly reflected in
The emulsification of liquid, experiment effect is influenceed, now trouble point can be found at gas pulse flow rate disturbance point B by observation, so as to solve
Certainly failure, pressure gas source can be allowed to pass through from bypass, system is recovered stable again by adjusting the aperture of stop valve 32.
Extraction phase concentration perturbation point C is provided between extraction tower 7 and heavy phase liquid storage tank 1, extraction phase concentration perturbation point C is to cut
Only valve 32 and the composition in parallel of normally open solenoid valve 33, are connected by pipeline, for heavy-phase liquid by being injected for controlling in extraction tower 7
Heavy phase flow quantity, i.e.,：In normal experiment, normally open solenoid valve 33 is opening, and heavy-phase liquid enters extraction tower by pipeline
In 7, when closing normally open solenoid valve 33, so as to cause extraction phase concentration to change, stable parameter is destroyed, and is mainly reflected in
The interfacial level of extraction tower 7 will constantly rise, and heavy-phase liquid may be made to be entered by raffinate phase outlet in raffinate phase separation tank 5, influence to test
Effect, heavy-phase liquid can now be allowed to pass through from bypass, system is recovered stable again by adjusting the aperture of stop valve 32.
It is stop valve 32 that light phase concentration perturbation point D, light phase concentration perturbation point D are set between light phase liquid storage tank 3 and light phase pump 9
With the composition in parallel of normally open solenoid valve 33, connected by pipeline, passed through for light-phase liquid, for controlling the light phase injected in extraction tower 7
Flow quantity, i.e.,：In normal experiment, normally open solenoid valve 33 is opening, and light-phase liquid is entered in extraction tower 7 by pipeline, when
Normally open solenoid valve 33 is closed, so as to cause light-phase liquid concentration to change, stable parameter is destroyed, and is mainly reflected in extraction phase
And raffinate phase concentration changes therewith, experiment effect is influenceed, now trouble point can be found in light phase liquid storage tank 3 by observation
Place, so as to solve failure, light-phase liquid can be allowed to pass through from bypass, system is recovered stable again by adjusting the aperture of stop valve 32.
Setting raffinate phase concentration perturbation point E, raffinate phase concentration perturbation point E are between raffinate phase storage tank 4 and raffinate phase separation tank 5
Stop valve 32 and the composition in parallel of normally open solenoid valve 33, are connected by pipeline, for raffinate phase liquid by injecting raffinate phase for controlling
Raffinate phase flow quantity in storage tank, i.e.,：In normal experiment, normally open solenoid valve 33 is opening, and raffinate phase liquid passes through pipeline
Into in raffinate phase storage tank 4, when closing normally open solenoid valve 33, so as to cause light-phase liquid concentration to change, stable parameter quilt
Destroy, be mainly reflected in extraction phase and raffinate phase concentration changes therewith, influence experiment effect, can now be found by observation
Trouble point is at raffinate phase liquid storage tank 4, so as to solve failure, can allow raffinate phase liquid from bypass by adjusting the aperture of stop valve 32
By making system recover stable again.
Boundary position disturbance point F is provided between extraction tower 7 and raffinate phase separation tank 5, boundary position disturbance point F is to cut
Only valve 32 and the composition in parallel of normally open solenoid valve 33, are connected by pipeline, passed through for raffinate phase liquid, light in extraction tower 7 for controlling
Phase and the high and low position at heavy phase interface, i.e.,：In normal experiment, normally open solenoid valve 33 is opening, and raffinate phase liquid passes through pipe
Road enters in raffinate phase separation tank 5, when closing normally open solenoid valve 33, so as to cause raffinate phase liquid not flow out, and stable parameter quilt
Destroy, influence experiment effect.Now trouble point can be found at extraction tower 7 by observation, so as to solve failure, adjustment can be passed through
The aperture of stop valve 32, allows raffinate phase liquid to pass through from bypass, system is recovered stable again.
The utility model is described in detail above example, but the content is only of the present utility model preferably real
Apply example, it is impossible to be considered as being used to limit practical range of the present utility model.All equalizations made according to present utility model application scope
Change and improvement etc., all should still be belonged within patent covering scope of the present utility model.
Claims (4)
1. a kind of novel extraction actual training device, including by heavy phase liquid storage tank, extraction phase storage tank, light phase liquid storage tank, raffinate phase storage tank,
Raffinate phase separation tank, compressed air surge tank, extraction tower, heavy phase pump, light phase pump group into circulation line, also set in circulation line
It is equipped with least one in following disturbance point：Gas pulse frequency is provided between the extraction tower and compressed air surge tank to disturb
Dynamic point, gas pulse flow rate disturbance point, the extraction tower and heavy phase are provided between the extraction tower and compressed air surge tank
Extraction phase concentration perturbation point is provided between liquid storage tank, sets light phase concentration to disturb between the light phase liquid storage tank and the light phase pump
Dynamic point, between the raffinate phase storage tank and the raffinate phase separation tank set raffinate phase concentration perturbation point, the extraction tower with it is described
Boundary position disturbance point is set between raffinate phase separation tank, it is characterised in that：
Also include spiral heat exchange tube, the spiral heat exchange tube is sheathed on heavy phase liquid storage tank periphery, the spiral heat exchange tube
Input be connected by inlet channel with heat-exchanging water tank, the output end of the spiral heat exchange tube passes through outlet conduit and heat exchange
Water tank is connected, and the inlet channel is provided with water pump, and vibrator is provided with the outside of the heavy phase liquid storage tank, and the extraction tower is interior from upper
Under be placed with the first distributor, the second distributor, the 3rd distributor, first distributor, the second distributor, the 3rd successively
Distributor is affixed by the first pipeline, second pipe, the 3rd pipeline and heavy-phase liquid conveyance conduit respectively；
The inlet channel is provided with heavy-phase liquid thermal perturbation point, the heavy-phase liquid thermal perturbation point be the first electromagnetic valve for adjusting with
Second electromagnetic valve for adjusting is in parallel to be formed, and on inlet channel, second electromagnetic valve for adjusting is set first electromagnetic valve for adjusting
In on branch's inlet channel；
Be provided with electric heater in the heat-exchanging water tank, the heat-exchanging water tank central upper portion position is provided with motor, the motor it is defeated
Go out end with the agitating paddle in heat-exchanging water tank to be connected；
Also include heavy-phase liquid distributed disturbance point, the heavy-phase liquid distributed disturbance point is the 3rd electromagnetic valve for adjusting, the 4th regulation electromagnetism
Valve, the 5th electromagnetic valve for adjusting are in parallel to be formed, the 3rd electromagnetic valve for adjusting, the 4th electromagnetic valve for adjusting, the 5th electromagnetic valve for adjusting point
The first pipeline, second pipe are not installed on, on the 3rd pipeline.
A kind of 2. novel extraction actual training device according to claim 1, it is characterised in that：The gas pulse flow rate disturbance
One end of point is connected by pipeline with the gas pulse frequency disturbance point, and its other end is delayed by pipeline and the compressed air
Rush tank connection.
A kind of 3. novel extraction actual training device according to claim 1, it is characterised in that：The gas pulse frequency disturbance
Point, gas pulse flow rate disturbance point, extraction phase concentration perturbation point, light phase concentration perturbation point, raffinate phase concentration perturbation point, boundary
Position disturbance point is respectively stop valve and normally open solenoid valve composition in parallel.
A kind of 4. novel extraction actual training device according to claim 1, it is characterised in that：In the circulation line, each
Magnetic valve, ball valve or pressure gauge or thermometer or liquid level gauge or flowmeter are provided with individual contact or branch road or flow shows
Show device or sample tap.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621297813.2U CN206823220U (en) | 2016-11-30 | 2016-11-30 | A kind of novel extraction actual training device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621297813.2U CN206823220U (en) | 2016-11-30 | 2016-11-30 | A kind of novel extraction actual training device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206823220U true CN206823220U (en) | 2018-01-02 |
Family
ID=60779944
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621297813.2U Active CN206823220U (en) | 2016-11-30 | 2016-11-30 | A kind of novel extraction actual training device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206823220U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112957768A (en) * | 2021-02-18 | 2021-06-15 | 哈尔滨工程大学 | Novel automatic baffle plate pulse extraction column system for experiments |
| CN115337666A (en) * | 2022-05-30 | 2022-11-15 | 烟台理工学院 | Centrifugal extraction system |
-
2016
- 2016-11-30 CN CN201621297813.2U patent/CN206823220U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112957768A (en) * | 2021-02-18 | 2021-06-15 | 哈尔滨工程大学 | Novel automatic baffle plate pulse extraction column system for experiments |
| CN115337666A (en) * | 2022-05-30 | 2022-11-15 | 烟台理工学院 | Centrifugal extraction system |
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