CN206483293U - Vapour liquid separator with condensation function - Google Patents
Vapour liquid separator with condensation function Download PDFInfo
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- CN206483293U CN206483293U CN201720080601.7U CN201720080601U CN206483293U CN 206483293 U CN206483293 U CN 206483293U CN 201720080601 U CN201720080601 U CN 201720080601U CN 206483293 U CN206483293 U CN 206483293U
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- tank
- condenser
- cavity
- tank body
- liquid separator
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Abstract
The utility model discloses a kind of vapour liquid separator with condensation function, its drip irrigation device is, including tank body, air inlet pipe is provided with the top of tank body, tank base sets discharging tube, it is provided with the middle part of tank body for tank interior cavity to be divided into two-part condenser up and down, condenser is internally provided with cavity, many are provided with condenser through cavity and the interior two-part siphunculus up and down of connection tank body, provided with the cooling medium with siphunculus wall contacts in cavity, the escape pipe below condenser is provided with tank wall.One vapour liquid separator can complete condensation, the function of vapor-liquid separation, and two functions can be integrated in an entirety.
Description
Technical field
The utility model is related to vapor-liquid separation field, more particularly to a kind of vapour liquid separator with condensation function.
Background technology
In Chemical Manufacture, during some liquid reactions, substantial amounts of gas can be produced.Pyroreaction meeting in reactor
The material that can be evaporated entrainment of some in the gas of generation is allowed, it is necessary to be reclaimed to evaporation material.It is existing to reclaim behaviour
Make, as shown in figure 1, being typically that the steam that reaction is generated passes through a piece cooler 51, the steam of high temperature is in piece cooler 51
Interior cooling, and then material can be because the reduction of temperature becomes liquid again.Then entered out of piece cooler 51 in vapor-liquid separation tank 52,
The material of liquid can deposit in vapor-liquid separation tank 52, and then gas can go out from the gas outlet of vapor-liquid separation tank 52, sink
The material accumulated can be back in reactor again by pipeline, and then realizes the material recycle being evaporated.
But wherein need to use 52 two parts of piece cooler 51 and vapor-liquid separation tank, it is necessary to pacify both respectively
Dress is produced respectively, and cost is higher, easily leakage.
Utility model content
In view of the deficienciess of the prior art, the purpose of this utility model is to provide a kind of vapour-liquid with condensation function
Separator, integrates condensation, vapor-liquid separation function.
Above-mentioned technical purpose of the present utility model technical scheme is that：One kind is with condensation function
Vapour liquid separator, including tank body is provided with air inlet pipe at the top of the tank body, the tank base sets discharging tube, the tank
It is provided with the middle part of body for tank interior cavity to be divided into two-part condenser up and down, the condenser is internally provided with sky
Many are provided with chamber, the condenser to be provided with cavity and the interior two-part siphunculus up and down of connection tank body, the cavity
With the cooling medium of siphunculus wall contacts, the escape pipe below condenser is provided with the tank wall.
By above-mentioned technical proposal, air-flow is entered at the top of tank body by air inlet pipe, then is entered by the siphunculus in condenser
Below to tank body, the heat absorbed on siphunculus that the cooling medium in condenser cavity can continue so passes through the gas of siphunculus
Cooling down can be just obtained, after gas temperature reduction, its internal material can be condensed into liquid, finally drop onto tank body
Bottom is deposited.The liquid of bottom deposit can be discharged by the discharging tube of bottom, and other gases are below condenser
Escape pipe discharge.Such a vapour liquid separator can complete condensation, the function of vapor-liquid separation, and two functions can be integrated in
In one entirety.
The utility model is further arranged to：The water inlet entered for cooling medium, cooling are provided with the condenser
But the delivery port that medium flows out, the water inlet is close to cavity bottom, and the delivery port is close to cavity top.
By above-mentioned technical proposal, the water inlet of lower section can allow current up progressively full under having after after cavity
Come up, then the delivery port water outlet from top, so allow in cavity and remain the full state of liquid, and cooling medium can
Stable circulation, flow speed stability, to cooling more abundant of siphunculus.
The utility model is further arranged to：The tank body includes upper tank and lower tank, the condenser top surface and bottom surface point
Do not connected in upper tank, lower tank flange.
By above-mentioned technical proposal, whole tank body is divided into upper tank, lower tank two parts, can be separated with condenser three
Processing, has saved processing cost.Using condenser as centre, it is connected by flange with upper tank, lower tank, allows attachment structure more steady
It is fixed, meanwhile, it is also convenient for the maintenance subsequently taken apart.
The utility model is further arranged to：The siphunculus is made up of carborundum.
By above-mentioned technical proposal, carborundum is high due to stable chemical performance, thermal conductivity factor, applies on condenser, one
Aspect can bear to separate the corrosivity that the gas/liquid of the high corrosions such as bromine carrys out equipment belt, on the other hand can be quickly by gas
Heat be transferred on cooling medium, the effect of cooling can be reached when passing the gas through siphunculus.
The utility model is further arranged to：The siphunculus is straight tube or bend pipe.
By above-mentioned technical proposal, straight tube and bend pipe can passing through for steady air current, straight tube can improve condenser
Interior space availability ratio, is adapted to the densely arranged of multi-pipeline, and bend pipe can improve walking of the unit length downstream in pipeline
Distance, extension air-flow is passing through interior process time.
The utility model is further arranged to：The upper tank is with being inserted with the thermometer for displays temperature on lower tank.
By above-mentioned technical proposal, the design of thermometer can get information about the situation of tank interior, be easy to operator
According to temperature conditions to operation is adjusted.
The utility model is further arranged to：Shutoff valve is provided with the tie point of the discharging tube and tank body.
By above-mentioned technical proposal, shutoff valve can control the output of liquid in tank body, meet the liquid turnover in tank body
Balance.
Brief description of the drawings
Fig. 1 is the material recycle mode described in background technology；
Fig. 2 is the structure chart of embodiment.
Reference：1st, tank body；11st, upper tank；12nd, lower tank；13rd, air inlet pipe；14th, discharging tube；15th, escape pipe；2nd, condense
Device；21st, cavity；22nd, siphunculus；23rd, water inlet；24th, delivery port；3rd, thermometer；4th, shutoff valve；51st, piece cooler；52nd, vapour-liquid point
From tank.
Embodiment
The utility model is described in further detail below in conjunction with accompanying drawing.
As shown in Fig. 2 a kind of vapour liquid separator with condensation function, including tank body 1,1 point of tank body is upper tank 11 with
Tank 12, is provided with a condenser 2 between upper tank 11 and lower tank 12.The top of condenser 2 is fixed with upper tank 11 by flange to be connected
Connect, the bottom of condenser 2 is fixedly connected with lower tank 12 also by flange.Upper tank 11 can be set with the lower inwall of tank 12 erosion-resisting
Anti-corrosion layer.Condenser 2 splits tank body 1, and the top of upper tank 11 is provided with air inlet pipe 13, and gas enters from upper tank 11, passes through
Enter lower tank 12 after condenser 2.
Condenser 2 is internally provided with cavity 21, and siphunculus 22, siphunculus are provided through between the top surface of condenser 2 and bottom surface
22 pass through inside cavity 21 and the upper tank 11 of connection and lower tank 12, siphunculus 22 for use by gas.The quantity of siphunculus 22 it is more and
It is uniformly distributed in condenser 2, the mounting hole installed for siphunculus 22 is set on condenser 2, siphunculus 22 can be designed as straight tube and also may be used
Think bend pipe.Wherein, siphunculus 22 is made up of carbofrax material, naturally it is also possible to be other high-termal conductivity, corrosion resistant material systems
Into.
The water inlet 23 and delivery port 24 connected with cavity 21 is provided with condenser 2, water inlet 23 is close to the bottom of cavity 21
Portion, and delivery port 24 is close to the top of cavity 21.Extraneous cooling medium can enter cavity 21 from water inlet 23, be gradually filled with
Gone out after cavity 21 from delivery port 24, cooling medium can be chilled brine etc..When cooling medium is full of whole cavity 21
When, the wall contacts of cooling medium and siphunculus 22, the heat for absorbing the internal gas of siphunculus 22.
It is provided with escape pipe 15 on lower tank 12, the tie point of escape pipe 15 and lower tank 12 is located at lower tank 12 close to condenser 2
Position, for being discharged by the gas after condenser 2, while being additionally provided with expansion joint on escape pipe 15, alleviate because of temperature difference
Pipeline deformation is produced with mechanical oscillation.
The bottom of lower tank 12 is provided with discharging tube 14, and the end of discharging tube 14 may be provided in air inlet pipe 13, by condenser 2
Solid accumulation after condensation flows into air inlet pipe 13 after lower tank 12, by discharging tube 14 and is eventually returned in reactor.Discharge opeing
Shutoff valve 4 is provided with pipe 14, discharging tube 14 can be adjusted by adjusting shutoff valve 4 and go out liquid status.
Meanwhile, upper tank 11 is with being inserted with the thermometer 3 for displays temperature on lower tank 12, the one end of thermometer 3 is inserted into
In tank body 1, the temperature in detectable reactor.The numerical value end of thermometer 3 is located at outside tank body 1, is easy to the specific number of people's observation
Value.
During production and processing, the past cavity 21 that the water inlet 23 of condenser 2 is lasting is passed through cooling medium, reactor
The high-temperature gas inside reflected is entered in upper tank 11 from air inlet pipe 13, then enters lower tank by cooling by gathering
In 12.During by passing through siphunculus 22, material cooling is in a liquid state and is deposited on the lower bottom of tank 12, and other gases are from outlet
Pipe 15 is discharged.Being deposited on the material of bottom can be entered in air inlet pipe 13 by discharging tube 14, be then refluxed for reactor.
Described above is only exemplary embodiment of the present utility model, not for limitation protection model of the present utility model
Enclose, protection domain of the present utility model is determined by appended claim.
Claims (7)
1. a kind of vapour liquid separator with condensation function, it is characterized in that：Including tank body (1), it is provided with the top of the tank body (1)
Air inlet pipe (13), tank body (1) bottom sets and is provided with the middle part of discharging tube (14), the tank body (1) for by tank body (1)
Portion's cavity is divided into two-part condenser (2) up and down, and the condenser (2) is internally provided with cavity (21), the condenser
(2) many are provided with cavity (21) and the interior two-part siphunculus (22) up and down of connection tank body (1), the cavity (21)
Provided with the cooling medium with siphunculus (22) wall contacts, going out below condenser (2) is provided with the wall of tank body (1) side
Tracheae (15).
2. the vapour liquid separator according to claim 1 with condensation function, it is characterized in that：Set on the condenser (2)
The water inlet (23) entered for cooling medium, the delivery port (24) gone out for cooling medium stream are equipped with, the water inlet (23) is close
Cavity (21) bottom, the delivery port (24) is at the top of cavity (21).
3. the vapour liquid separator according to claim 1 with condensation function, it is characterized in that：The tank body (1) includes upper
Tank (11) and lower tank (12), condenser (2) top surface are connected with bottom surface respectively at upper tank (11), lower tank (12) flange.
4. the vapour liquid separator according to claim 1 with condensation function, it is characterized in that：The siphunculus (22) is by being carbonized
Silicon is made.
5. the vapour liquid separator according to claim 1 with condensation function, it is characterized in that：The siphunculus (22) is straight tube
Or bend pipe.
6. the vapour liquid separator according to claim 3 with condensation function, it is characterized in that：The upper tank (11) and lower tank
(12) thermometer (3) for displays temperature is inserted with.
7. the vapour liquid separator according to claim 1 with condensation function, it is characterized in that：The discharging tube (14) and tank
Shutoff valve (4) is provided with the tie point of body (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720080601.7U CN206483293U (en) | 2017-01-22 | 2017-01-22 | Vapour liquid separator with condensation function |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720080601.7U CN206483293U (en) | 2017-01-22 | 2017-01-22 | Vapour liquid separator with condensation function |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206483293U true CN206483293U (en) | 2017-09-12 |
Family
ID=59766104
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720080601.7U Active CN206483293U (en) | 2017-01-22 | 2017-01-22 | Vapour liquid separator with condensation function |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206483293U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110393935A (en) * | 2019-07-04 | 2019-11-01 | 昌和化学新材料(江苏）有限公司 | A kind of condenser for a benzene distillation |
-
2017
- 2017-01-22 CN CN201720080601.7U patent/CN206483293U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110393935A (en) * | 2019-07-04 | 2019-11-01 | 昌和化学新材料(江苏）有限公司 | A kind of condenser for a benzene distillation |
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