CN206045484U - Liquid separating appts with ball float level meters - Google Patents
Liquid separating appts with ball float level meters Download PDFInfo
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- CN206045484U CN206045484U CN201620845373.3U CN201620845373U CN206045484U CN 206045484 U CN206045484 U CN 206045484U CN 201620845373 U CN201620845373 U CN 201620845373U CN 206045484 U CN206045484 U CN 206045484U
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- push rod
- travel switch
- outlet valve
- regenerator
- ball float
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Abstract
The utility model discloses a kind of liquid separating appts with ball float level meters, including regenerator, the regenerator is provided with the first electromagnetism outlet valve and the second electromagnetism outlet valve, ball float level meters are provided with regenerator, the ball float level meters are connected with control device, and the control device controls the switch of the first electromagnetism outlet valve and the second electromagnetism outlet valve.This utility model is used for the Liquid level that the split-phase of two kinds of liquid phases is layered, and in making same container, two kinds of layering liquid phases are smoothly detached discharge.
Description
Technical field
This utility model is related to field of chemical equipment, and in particular to a kind of liquid separating appts with ball float level meters.
Background technology
In Chemical Manufacture, such as phosphoric acid production technique, the back extraction acid and tributyl phosphate mixture after back extraction, Jing pressures
After filter filter pressing, its liquid phase enters subsequent production, but because containing impurity in back extraction acid, makes subsequent production not up to standard.Traditional
It is that the liquid phase after filter pressing is entered into regenerator in technique, and is mixed with the kerosene in regenerator, and oscillating screen plate (realizes two
Plant even in liquid phase mixing), Jing after the suction ester of kerosene and washing, the tributyl phosphate in back extraction acid is separated, its organic facies
Realize that split-phase is layered with two kinds of liquid phases of water phase, but how to realize the discharge of two layering liquid phasesTraditional mode is to adopt
The mode of overflow, i.e.,：Water from tower bottom discharge, organic faciess such as top of tower overflow and go out.But how to learn the overflow of top institute
What is gone out must be organic faciess, and bottom discharge be exactly water phaseAnd the mode of this kind of overflow, can also enter again in overflow
Material, then carry out consecutive productionAnswer is negative.Therefore control mixed and disorderly, it is impossible to realize large-scale industrial production, make
Low into purification efficiency, recovery utilization rate is low.
Utility model content
The purpose of this utility model is to provide a kind of liquid separating appts with ball float level meters, dividing for two kinds of liquid phases
The Liquid level being mutually layered, in making same container, two kinds of layering liquid phases are smoothly detached discharge.
In order to achieve the above object, this utility model adopts the following technical scheme that a kind of liquid with ball float level meters divides
From device, including regenerator, which it is critical only that：The regenerator is provided with the first electromagnetism outlet valve and the outlet of the second electromagnetism
Valve, is provided with ball float level meters in regenerator, and the ball float level meters are connected with control device, the control device control the
The switch of one electromagnetism outlet valve and the second electromagnetism outlet valve.
In Chemical Manufacture, detached liquefied mixture is needed to enter regenerator, by extractant is added in regenerator,
Organic faciess in mixture are layered with water phase split-phase, organic faciess are lighter due to density, float on top, and water is due to density
It is heavier to be deposited on lower section, and the first electromagnetism outlet valve is arranged at the bottom of regenerator, the water phase larger for discharging density, second
Electromagnetism outlet valve is arranged at regenerator side surface upper part, the organic faciess lighter for discharging density, and ball float level meters have for detection
Interface location between machine phase and water phase, judges the number of two kinds of liquid of organic faciess and water phase according to the height of interface location, and
Detection signal is passed to into control device, control device controls the switch of the first electromagnetism outlet valve and the second electromagnetism outlet valve, from
And excessive organic faciess or water phase are discharged, realize that organic faciess are separated from the water and persistently automatically control.
The position of the first electromagnetism outlet valve and the second electromagnetism outlet valve arranges and belongs to conventional setting.
Water needs the larger liquid of detached density in mutually referring to liquefied mixture, organic faciess are needed in referring to liquefied mixture point
From the less liquid of density.
The ball float level meters are provided with hollow float, and the hollow float is fixed with transfer bar mechanism, and the transfer bar mechanism is defeated
Go out and give control device control signal.
The ball float level meters simple structure, it is easy to manufacture.It is not easy to occur demagnetization and the problems such as magnetic weakens, only leans on
The buoyancy of hollow float promotes transfer bar mechanism, hollow float to apply trigger to control device by transfer bar mechanism.
The transfer bar mechanism includes the first push rod, one end connection hollow float of first push rod, the first push rod it is another
One end is fixed with the second push rod after stretching out the top via of regenerator, and the first push rod is slidably matched with the top via of regenerator,
Second push rod is vertically arranged with the first push rod, and connected first push rod in one end of the second push rod, the other end apply to touch to control device
Signal.
Preferably, hollow float and the first push rod are PPR materials or engineering plastics.
The setting is easy to control device is arranged at outside regenerator, it is to avoid it is rotten that control device is reproduced the mixed liquor in tower
Erosion.
The control device includes the first travel switch, the second travel switch, and first the first electromagnetism of stroke on-off control goes out
The switch of mouth valve, the second travel switch control the switch of the second electromagnetism outlet valve；
First travel switch is located at the upward stroke limit point of the other end of the second push rod；
Second travel switch is located at the downward stroke limit point of the other end of the second push rod；
The other end of the second push rod controls the first travel switch, the switch of the second travel switch.
First stroke on-off control the first electromagnetism outlet valve break-make power supply, so as to control the switch of the first electromagnetism outlet valve；
Second travel switch controls the second electromagnetism outlet valve break-make power supply, so as to the switch of the second electromagnetism outlet valve of control.
The control device is simple and practical, when the water in regenerator it is mutually excessive, when organic faciess are very few, on hollow float
Floating, the second push rod promotes the first travel switch, first the first electromagnetism of stroke on-off control outlet valve to open, and releases excessive water
Phase, when in regenerator, organic faciess are excessive, when water is mutually very few, hollow float declines, the second push rod the second travel switch of promotion, and second
Travel switch controls the second electromagnetism outlet valve and opens, and releases excessive organic faciess.
The other end of first push rod is also fixed with hopper, and counterweight is housed in the hopper, and the counterweight is sand.
As density of the organic faciess with water phase is often varied from, by increasing and decreasing appropriate counterweight in hopper, can adjust
The position of hollow float, makes the testing result of ball float level meters more accurate.
Institute's regenerator is fixed with traveller, and first travel switch is fixed with the first sliding sleeve, and second travel switch is solid
The second sliding sleeve is connected with, first sliding sleeve, the second sliding sleeve are slidably located on traveller, and first sliding sleeve, the second sliding sleeve are equal
Holding screw is radially arranged, holding screw is fixed on the first sliding sleeve, the second sliding sleeve on traveller.
The setting is easy to arrange the first travel switch, the starting threshold value of the second travel switch, the first travel switch, second
Travel switch is separated by nearer, and it is less to start threshold value, and contrary to start threshold value bigger；It is pre- that the meaning refers to that the position of ball float level meters exceedes
During the interface location certain value for first setting, the first travel switch, the second travel switch just start.
Scale is provided with first push rod.
The scale is easy to operator to be adjusted at any time for indicating position height of the hollow float in regenerator.
First push rod, hollow float are provided with polytetrafluorethylecoatings coatings.
Polytetrafluorethylecoatings coatings are used for the first push rod, the pH protective of hollow float.
Remarkable result：This utility model provides a kind of liquid separating appts with ball float level meters, for two kinds of liquid phases
The Liquid level of split-phase layering, in making same container, two kinds of layering liquid phases are smoothly detached discharge.
Description of the drawings
Fig. 1 is structural representation of the present utility model.
Specific embodiment
This utility model is described in further detail with specific embodiment below in conjunction with the accompanying drawings.
As shown in figure 1, this utility model provides a kind of liquid separating appts with ball float level meters, including regenerator 1,
The regenerator 1 is provided with the first electromagnetism outlet valve 2 and the second electromagnetism outlet valve 3, in regenerator 1 is provided with ball float interface
Meter 4, the ball float level meters 4 are connected with control device, and the control device controls the first electromagnetism outlet valve 2 and the second electromagnetism
The switch of outlet valve 3.
In Chemical Manufacture, need detached liquefied mixture to enter regenerator 1, extracted by adding in regenerator 1
Agent, the organic faciess in liquefied mixture and water phase split-phase are layered, and organic faciess are lighter due to density, float on top, and water phase
Lower section is deposited on as density is heavier, and the first electromagnetism outlet valve 2 is arranged at the bottom of regenerator 1, it is larger for discharging density
Water phase, the second electromagnetism outlet valve 3 is arranged at 1 side surface upper part of regenerator, the organic faciess lighter for discharging density, ball float interface
Meter 4 is used to detect interface location between organic faciess and water phase, judges two kinds of organic faciess and water phase according to the height of interface location
Liquid number, and detection signal is passed to into control device, control device is controlled the first electromagnetism outlet valve 2 and is gone out with the second electromagnetism
The switch of mouth valve 3, so as to discharge excessive organic faciess or water phase, realizes that organic faciess are separated from the water and persistently automatically controls.
The position of the first electromagnetism outlet valve 2 and the second electromagnetism outlet valve 3 arranges and belongs to conventional setting.
The ball float level meters 4 are provided with hollow float 41, and the hollow float 41 is fixed with transfer bar mechanism 42, hollow floating
Ball 41 applies trigger to control device by transfer bar mechanism 42.
The top of regenerator 1 is additionally provided with mixed liquor import 9 and extractant import 8.
Mixed liquor import 9 is used to be put into liquefied mixture, and extractant import 8 is used to be put into extractant.
Key equipment of the present utility model is ball float level meters 4, and it includes a hollow float 41 and transfer bar mechanism 42,
The average weight of ball float level meters 4, enables hollow float 41 to swim on organic faciess and the interface of water phase.
The transfer bar mechanism 42 includes the first push rod 42a, and one end of the first push rod 42a connects hollow float 41, the
The other end of one push rod 42a is fixed with the second push rod 42b after stretching out the top via of regenerator 1, the first push rod 42a slides and wears
In the top via of regenerator 1, the second push rod 42b is vertically arranged with the first push rod 42a, and one end of the second push rod 42b is connected the
One push rod 42a, the other end apply trigger to control device.
Preferably, hollow float 41 and the first push rod 42a are PPR materials.
The control device includes the first travel switch 6, the second travel switch 5, and the first travel switch 6 controls the first electromagnetism
The switch of outlet valve 2, the second travel switch 5 control the switch of the second electromagnetism outlet valve 3；
Upward stroke limit point of first travel switch 6 positioned at the other end of the second push rod 42b；
Downward stroke limit point of second travel switch 5 positioned at the other end of the second push rod 42b；
The other end of the second push rod 42b promotes the first travel switch 6, the second stroke to open as hollow float 41 moves up and down
Close 5 switch.
First travel switch 6 controls 2 break-make power supply of the first electromagnetism outlet valve, so as to control opening for the first electromagnetism outlet valve 2
Close；Second travel switch 5 controls 3 break-make power supply of the second electromagnetism outlet valve, so as to the switch of the second electromagnetism outlet valve 3 of control,
Circuit diagram is omited.
The other end of the first push rod 42a is also fixed with hopper 43, and counterweight is housed in the hopper 43, and the counterweight is sand.
Institute's regenerator 1 is fixed with traveller 11, and first travel switch 6 is fixed with the first sliding sleeve 61, second stroke
Switch 5 is fixed with the second sliding sleeve 51, and first sliding sleeve 61, the second sliding sleeve 51 are slidably located on traveller 11, and described first
Sliding sleeve 61, the second sliding sleeve 51 have been radially arranged holding screw 7, and the first sliding sleeve 61, the second sliding sleeve 51 are fixed on by holding screw 7
On traveller 11.
Scale is provided with the first push rod 42a.
The first push rod 42a, hollow float 41 are provided with polytetrafluorethylecoatings coatings.
Density p according to organic faciess and water phase carries out accurate calculating, makes ball float level meters 4, and ball float level meters make
After good, it be put in regenerator 1 and tested, according to the sand in the actual float position increase and decrease hopper 43 of hollow float 41, makes sky
Separating interface of the flighty and impatient ball 41 in two kinds of liquid phases；And regulate first travel switch 6 and the second travel switch 5 of control device
Position, when the position of ball float level meters 4 exceedes interface location certain value set in advance, the first travel switch 6, the second stroke
Switch 5 just starts.
The control device is simple and practical, when the water in regenerator 1 it is mutually excessive, when organic faciess are very few, hollow float
41 float, and the second push rod 42b promotes the first travel switch 6, the first travel switch 6 to control the first electromagnetism outlet valve 2 and open, release
Excessive water phase, when in regenerator 1, organic faciess are excessive, when water is mutually very few, hollow float 41 declines, and the second push rod 42b promotes the
Two travel switches 5, the second travel switch 5 control the second electromagnetism outlet valve 3 and open, and release excessive organic faciess.
Water needs the larger liquid of detached density in mutually referring to liquefied mixture, organic faciess are needed in referring to liquefied mixture point
From the less liquid of density.
Advantage of the present utility model：
1st, realize that the detached precision of liquid split-phase is automatically controlled in regenerator, it is simple to operate, it is easy to control.
2nd, the segregation apparatuss belong to production line balance, it is possible to achieve industrialized production.
In sum, this utility model provides a kind of liquid separating appts with ball float level meters, for two kinds of liquid phases
The Liquid level of split-phase layering, in making same container, two kinds of layering liquid phases are smoothly detached discharge.
Claims (5)
1. a kind of liquid separating appts with ball float level meters, including regenerator (1), it is characterised in that：The regenerator (1) sets
The first electromagnetism outlet valve (2) and the second electromagnetism outlet valve (3) are equipped with, and ball float level meters (4) are provided with regenerator (1),
The ball float level meters (4) are connected with control device, and the control device controls the first electromagnetism outlet valve (2) and the second electromagnetism
The switch of outlet valve (3)；
The ball float level meters (4) are provided with hollow float (41), and the hollow float (41) is fixed with transfer bar mechanism (42), empty
Flighty and impatient ball (41) applies trigger to control device by transfer bar mechanism (42)；
The transfer bar mechanism (42) includes the first push rod (42a), one end connection hollow float of first push rod (42a)
(41), the other end of the first push rod (42a) is fixed with the second push rod (42b) after stretching out the top via of regenerator (1), and first pushes away
Bar (42a) is slidably matched with the top via of regenerator (1), and the second push rod (42b) is vertically arranged with the first push rod (42a), the
Connected first push rod (42a) in one end of two push rods (42b), the other end apply trigger to control device；
The control device includes the first travel switch (6), the second travel switch (5), and the first travel switch (6) control first is electric
The switch of magnetic outlet valve (2), the second travel switch (5) control the switch of the second electromagnetism outlet valve (3)；
Upward stroke limit point of first travel switch (6) positioned at the other end of the second push rod (42b)；
Downward stroke limit point of second travel switch (5) positioned at the other end of the second push rod (42b)；
The other end of the second push rod (42b) controls the first travel switch (6), the switch of the second travel switch (5).
2. liquid separating appts with ball float level meters according to claim 1, it is characterised in that：First push rod
(42a) the other end is also fixed with hopper (43), and counterweight is housed in the hopper (43), and the counterweight is sand.
3. liquid separating appts with ball float level meters according to claim 1, it is characterised in that：Institute's regenerator (1) is solid
Traveller (11) is connected with, first travel switch (6) is fixed with the first sliding sleeve (61), and second travel switch (5) is fixed with
Second sliding sleeve (51), first sliding sleeve (61), the second sliding sleeve (51) are slidably located on traveller (11), first sliding sleeve
(61), the second sliding sleeve (51) has been radially arranged holding screw (7), and holding screw (7) is by the first sliding sleeve (61), the second sliding sleeve
(51) it is fixed on traveller (11).
4. liquid separating appts with ball float level meters according to claim 1, it is characterised in that：First push rod
(42a) scale is provided with.
5. liquid separating appts with ball float level meters according to claim 1, it is characterised in that：First push rod
(42a), hollow float (41) is provided with polytetrafluorethylecoatings coatings.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620845373.3U CN206045484U (en) | 2016-08-05 | 2016-08-05 | Liquid separating appts with ball float level meters |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620845373.3U CN206045484U (en) | 2016-08-05 | 2016-08-05 | Liquid separating appts with ball float level meters |
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| Publication Number | Publication Date |
|---|---|
| CN206045484U true CN206045484U (en) | 2017-03-29 |
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ID=58380276
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620845373.3U Active CN206045484U (en) | 2016-08-05 | 2016-08-05 | Liquid separating appts with ball float level meters |
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| Country | Link |
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| CN (1) | CN206045484U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109126206A (en) * | 2018-09-29 | 2019-01-04 | 任少虎 | A kind of mixing liquid separation method and device |
| CN109179703A (en) * | 2018-08-31 | 2019-01-11 | 嘉兴汇昌塑业有限公司 | A kind of oil-water separation tank can be avoided line clogging |
| CN112010382A (en) * | 2020-09-08 | 2020-12-01 | 绍兴市九鑫环保有限公司 | Phosphorus-containing waste acid extraction device and extraction method thereof |
-
2016
- 2016-08-05 CN CN201620845373.3U patent/CN206045484U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109179703A (en) * | 2018-08-31 | 2019-01-11 | 嘉兴汇昌塑业有限公司 | A kind of oil-water separation tank can be avoided line clogging |
| CN109126206A (en) * | 2018-09-29 | 2019-01-04 | 任少虎 | A kind of mixing liquid separation method and device |
| CN112010382A (en) * | 2020-09-08 | 2020-12-01 | 绍兴市九鑫环保有限公司 | Phosphorus-containing waste acid extraction device and extraction method thereof |
| CN112010382B (en) * | 2020-09-08 | 2021-09-21 | 绍兴市九鑫环保有限公司 | Phosphorus-containing waste acid extraction device and extraction method thereof |
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