CN221513556U - Vapour-liquid separation recovery unit - Google Patents
Vapour-liquid separation recovery unit Download PDFInfo
- Publication number
- CN221513556U CN221513556U CN202323474773.7U CN202323474773U CN221513556U CN 221513556 U CN221513556 U CN 221513556U CN 202323474773 U CN202323474773 U CN 202323474773U CN 221513556 U CN221513556 U CN 221513556U
- Authority
- CN
- China
- Prior art keywords
- tank
- vapor
- pipe
- water
- recovery
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 88
- 238000011084 recovery Methods 0.000 title claims abstract description 72
- 238000000926 separation method Methods 0.000 title claims abstract description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 80
- 238000010438 heat treatment Methods 0.000 claims abstract description 46
- 238000009434 installation Methods 0.000 claims abstract description 14
- 230000000149 penetrating effect Effects 0.000 claims description 2
- 239000008234 soft water Substances 0.000 abstract description 13
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 7
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 7
- 238000004140 cleaning Methods 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 4
- 238000004064 recycling Methods 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 2
- 230000003020 moisturizing effect Effects 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000004781 supercooling Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model provides a vapor-liquid separation and recovery device, and belongs to the technical field of vapor-liquid separation and recovery devices. The utility model relates to a vapor-liquid separation recovery device, which comprises a liquid heating tank and an installation tank, wherein the installation tank is arranged on the right side of the liquid heating tank, a vapor condensing pipe, a vapor-liquid separator, a condensate pipe, a recovery tank, a temperature sensor monitor and a heating plate are mutually matched, firstly, high-temperature and high-pressure vapor output by the liquid heating tank enters the vapor condensing pipe and exchanges heat with low-temperature polluted nitrogen, the condensate water and low-temperature low-pressure steam are formed, the condensate water enters the vapor-liquid separator through the vapor condensing pipe, the condensate water is discharged from the outlet of the condensate pipe, the steam passes through the fixed pipe and then is introduced into soft water in the recovery tank to preheat the soft water, and when the temperature sensor detects that the steam cannot heat the soft water to the corresponding temperature, the heating plate is controlled to heat, so that the water and the vapor can be utilized, and the recovery rate is improved.
Description
Technical Field
The utility model relates to the field of vapor-liquid separation and recovery devices, in particular to a vapor-liquid separation and recovery device.
Background
The vapor-liquid separation and recovery device is a device for treating liquid pollutants in exhaust gas, and is generally composed of a separator, a recovery device and a treatment system, wherein firstly, the exhaust gas enters the device through the separator, the separator separates liquid pollutant and gas in the waste gas by using a physical principle, the separated liquid pollutant is collected into a recovery device and can be reused after being treated, and the gas part is purified by a treatment system so as to reach the emission standard.
In the specific vapor-liquid separation recovery, the vapor is usually directly discharged or is recycled to a low-pressure vapor pipe network, the recovery efficiency is too low, a large amount of water sources and energy consumption are wasted, but in daily life, water is needed for cleaning objects, the direct water cleaning can cause the waste of water resources, the water and the vapor cannot be utilized, and the vapor is recycled, so that the use of the vapor is inconvenient for operators.
Disclosure of utility model
In order to overcome the above disadvantages, the present utility model provides a vapor-liquid separation recovery device that overcomes the above technical problems or at least partially solves the above problems.
The utility model is realized in the following way:
The utility model provides a vapor-liquid separation and recovery device, which comprises a liquid heating tank and a mounting tank, wherein the mounting tank is arranged on the right side of the liquid heating tank,
The gas-liquid separation mechanism comprises a mounting pipe, wherein the mounting pipe is arranged between the liquid heating tank and the mounting tank, one end of the mounting pipe is provided with a gas condensing pipe, one end of the gas condensing pipe is provided with a gas-liquid separator, one side of the gas-liquid separator is provided with a fixing pipe, one end of the fixing pipe is provided with a recovery tank, and the inside of the recovery tank is provided with a heating plate;
The circulating mechanism comprises a circulating pump, the circulating pump is arranged at the top of the recovery tank, a temperature sensor is arranged in the recovery tank, and a water level controller is arranged on one side of the recovery tank.
In a preferred embodiment, the vapor condensation pipe is disposed inside the installation tank, and the recovery tank is disposed above the installation tank.
In a preferred scheme, a condensate pipe is arranged at the bottom of the vapor-liquid separator, and a valve is arranged on the surface of the condensate pipe.
In a preferred scheme, the top of the recovery tank is provided with a mounting pipe in a penetrating way, and the mounting pipe is arranged on one side of the circulating pump.
In a preferred embodiment, a delivery pipe is provided on one side of the circulation pump, and one end of the delivery pipe is inserted into the liquid heating tank.
In a preferred scheme, the rear part of the installation tank is provided with a water tank, and the top of the water tank is provided with a water pump.
In a preferred scheme, the top of water pump is provided with the water pipe, the one end of water pipe sets up in the inside of collection box.
In a preferred embodiment, the bottoms of the mounting tank and the liquid heating tank are each provided with a support leg, and the fixing tube is disposed above the vapor condensing tube.
The utility model provides a vapor-liquid separation and recovery device, which has the beneficial effects that:
1. Through the mutually supporting of liquid heating jar, vapor condenser pipe, vapour liquid separator, the condensate pipe, the recovery tank, temperature sensor prison and hot plate, at first get into the vapor condenser pipe with the high temperature high pressure steam of liquid heating jar output and with low temperature dirty nitrogen gas heat exchange back, form comdenstion water and low temperature low pressure steam, get into in the vapour liquid separator through the vapor condenser pipe, the comdenstion water is got rid of from the condensate pipe export, the steam passes through the fixed pipe then lets in the soft water of recovery tank inside, preheat for the soft water, realize the recovery of steam, when temperature sensor detects that the heat energy that the steam contained can not heat soft water to corresponding temperature, temperature sensor control hot plate heats, thereby can utilize water and vapor, promote the rate of recovery.
2. Through the mutually supporting of circulating pump, liquid heating jar, water level controller, recovery tank and water pump to when the operator needs to circulate, the operator can not lead to steam output unstable through the water input liquid heating jar that the supercooling was put into to the circulating pump, and water level controller monitors the inside water yield of recovery tank, and the control water pump is taken out from the water tank is inside not enough, and carries out the moisturizing, and the circulating pump carries the water that the recovery tank top has reached preheating temperature to liquid heating jar and carries out continuous output high temperature high pressure steam, thereby can circulate and utilize vapor.
Drawings
For a clearer description of the technical solutions of the embodiments of the present utility model, the drawings that are needed in the embodiments will be briefly described below, it being understood that the following drawings only illustrate some examples of the present utility model and should not be considered as limiting the scope, and other related drawings may be obtained according to these drawings without inventive effort for a person skilled in the art;
FIG. 1 is an overall perspective view provided by an embodiment of the present utility model;
FIG. 2 is a schematic view of the internal structure of a sectional mounting can according to an embodiment of the present utility model;
FIG. 3 is a schematic view of the internal structure of a sectional recycling bin according to an embodiment of the present utility model;
FIG. 4 is a schematic view of a rear structure of a mounting tank according to an embodiment of the present utility model;
in the figure: 1. a vapor-liquid separation mechanism; 11. a liquid heating tank; 12. installing a pipe; 13. a mounting tank; 14. a vapor condensing tube; 15. a vapor-liquid separator; 16. a condensate pipe; 17. a fixed tube; 18. a recovery box; 19. a heating plate; 2. a circulation mechanism; 21. a circulation pump; 22. assembling a tube; 23. a delivery tube; 24. a water level controller; 25. a temperature sensor; 26. a water tank; 27. and (3) a water pump.
Detailed Description
For the purpose of making the objects, technical solutions and advantages of the embodiments of the present utility model more apparent, the technical solutions of the embodiments of the present utility model will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present utility model, and it is apparent that the described embodiments are some embodiments of the present utility model, but not all embodiments. All other embodiments, based on the embodiments of the utility model, which are apparent to those of ordinary skill in the art without inventive faculty, are intended to be within the scope of the utility model.
Examples
Referring to fig. 1-4, the present utility model provides a technical solution: the vapor-liquid separation and recovery device comprises a vapor-liquid separation mechanism 1, a circulation mechanism 2, a liquid heating tank 11 and a mounting tank 13, wherein the vapor-liquid separation mechanism 1 is a mechanism capable of separating and recovering vapor, the circulation mechanism 2 is a mechanism capable of recycling vapor, the mounting tank 13 is arranged on the right side of the liquid heating tank 11, the vapor-liquid separation mechanism 1 comprises a mounting pipe 12, the mounting pipe 12 is arranged between the liquid heating tank 11 and the mounting tank 13, one end of the mounting pipe 12 is provided with a vapor condensing pipe 14, one end of the vapor condensing pipe 14 is provided with a vapor-liquid separator 15, one side of the vapor-liquid separator 15 is provided with a fixing pipe 17, one end of the fixing pipe 17 is provided with a recovery tank 18, the inside of the recovery tank 18 is provided with a heating plate 19, the circulation mechanism 2 comprises a circulation pump 21, the circulation pump 21 is arranged at the top of the recovery tank 18, the inside of the recovery tank 18 is provided with a temperature sensor 25, one side of the recovery tank 18 is provided with a water level controller 24, through the mutual matching of the liquid heating tank 11, the vapor condensing pipe 14, the vapor-liquid separator 15, the condensate pipe 16, the recovery tank 18, the temperature sensor monitor 25 and the heating plate 19, when an operator needs to separate and recover the vapor from the liquid, firstly, the high-temperature and high-pressure vapor output by the liquid heating tank 11 can enter the vapor condensing pipe 14 to exchange heat with the low-temperature polluted nitrogen to form condensed water and low-temperature and low-pressure vapor, the condensed water enters the vapor-liquid separator 15 through the vapor condensing pipe 14 and is discharged from the outlet of the condensate pipe 16 for daily life use, the vapor passes through the fixed pipe 17 and then is introduced into the soft water in the recovery tank 18 to preheat the soft water, thereby realizing the recovery of the vapor, when the temperature sensor 25 detects that the heat energy contained in the vapor can not heat the soft water to the corresponding temperature, the temperature sensor 25 controls the heating plate 19 to heat, so that water resources can not be wasted, water and water vapor can be utilized, and recovery rate is improved.
Referring to fig. 1 to 4, in a preferred embodiment, a gas condensing pipe 14 is provided inside a mounting tank 13, a recovery tank 18 is provided above the mounting tank 13, a condensate pipe 16 is provided at the bottom of a gas-liquid separator 15, a valve is provided on the surface of the condensate pipe 16, the condensate pipe 16 can be controlled by providing the valve, a packing pipe 22 is inserted into the top of the recovery tank 18, and the packing pipe 22 is provided at one side of a circulation pump 21.
Referring to fig. 1 to 4, in a preferred embodiment, a transfer pipe 23 is provided at one side of a circulation pump 21, one end of the transfer pipe 23 is inserted into the liquid heating tank 11, a water tank 26 is provided at the rear of the installation tank 13, a water pump 27 is provided at the top of the water tank 26, a water pipe is provided at the top of the water pump 27, one end of the water pipe is provided in the recovery tank 18, support legs are provided at the bottoms of the installation tank 13 and the liquid heating tank 11, stability of the installation tank 13 and the liquid heating tank 11 is improved by providing the support legs, a fixing pipe 17 is provided above the vapor condensing pipe 14, and when an operator needs to circulate, the circulation pump 21, the liquid heating tank 11, a water level controller 24, the recovery tank 18 and the water pump 27 are mutually matched, so that the operator can input water into the liquid heating tank 11 through the circulation pump 21 without causing unstable vapor output, the water level controller 24 monitors the water amount in the recovery tank 18, the water pump 27 is controlled to be drawn out from the inside the water tank 26 and make up water, the circulation pump 21 continuously heats the water at the top of the tank 18 to a preheated temperature, and the high-pressure vapor can be circulated by the high-pressure vapor output.
Specifically, the working process or working principle of the vapor-liquid separation and recovery device is as follows: in particular to vapor-liquid separation and recovery, the vapor is usually directly discharged or recovered to a low-pressure vapor pipe network, the recovery efficiency is too low, a great amount of water source and energy consumption are wasted, but in daily life, water is needed for cleaning objects, the direct water is used for cleaning, water resource waste is caused, water and vapor cannot be utilized, and the vapor is recycled, so that the vapor-liquid separation and recovery is inconvenient for operators, therefore, the technical scheme can solve the problems, when the operators need to separate and recover the vapor-liquid, firstly, the high-temperature and high-pressure vapor output by the liquid heating tank 11 can enter the vapor condensing pipe 14 to exchange heat with low-temperature polluted nitrogen to form condensed water and low-temperature low-pressure vapor, the condensed water enters the vapor-liquid separator 15 through the vapor condensing pipe 14, and the condensed water is discharged from the outlet of the condensate pipe 16 for daily life, the steam is preheated by the soft water which is led into the recovery tank 18 through the fixed pipe 17, so that the recovery of the steam is realized, when the temperature sensor 25 detects that the heat energy contained in the steam can not heat the soft water to the corresponding temperature, the temperature sensor 25 controls the heating plate 19 to heat, so that the waste of water resources can be avoided, water and steam can be utilized, the recovery rate is improved, when an operator needs to circulate, the operator can input supercooled water into the liquid heating tank 11 through the circulating pump 21, unstable steam output can not be caused, the water level controller 24 monitors the water quantity in the recovery tank 18, the water pump 27 is controlled to pump out from the water tank 26 when the water quantity is insufficient, the water is supplemented, the circulating pump 21 conveys the water which has reached the preheating temperature at the top of the recovery tank 18 to the liquid heating tank 11 for continuously outputting high-temperature and high-pressure steam, the whole process is through recycling bin 18 with low temperature low pressure vapor recovery, and the heat is used for heating the soft water to liquid heating jar 11 moisturizing, reduces the heating energy consumption, can keep the inside stable output steam of liquid heating jar 11 moreover, can not lead to temperature difference pressure too big, and steam gets into recycling bin 18 and belongs to soft water recovery and recycles, saves the heating energy consumption moreover, and the comdenstion water can daily use to save water resource, all flows end so far.
It should be noted that, the vapor-liquid separator 15, the heating plate 19, the circulating pump 21, the water level controller 24, the temperature sensor 25 and the water pump 27 are all electrically connected with an external power source and are devices or apparatuses existing in the prior art, or are devices or apparatuses that can be implemented in the prior art, and the power supply, the specific composition and the principle thereof are clear to those skilled in the art, so that detailed descriptions thereof are omitted.
Claims (8)
1. The vapor-liquid separation and recovery device comprises a liquid heating tank (11) and a mounting tank (13), wherein the mounting tank (13) is arranged on the right side of the liquid heating tank (11),
The gas-liquid separation mechanism (1), gas-liquid separation mechanism (1) includes installation pipe (12), installation pipe (12) set up between liquid heating jar (11) and installation jar (13), the one end of installation pipe (12) is provided with vapor condensing tube (14), the one end of vapor condensing tube (14) is provided with vapour-liquid separator (15), one side of vapour-liquid separator (15) is provided with fixed pipe (17), the one end of fixed pipe (17) is provided with recovery tank (18), the inside of recovery tank (18) is provided with hot plate (19);
Circulation mechanism (2), circulation mechanism (2) include circulating pump (21), circulating pump (21) set up in the top of collection box (18), the inside of collection box (18) is provided with temperature sensor (25), one side of collection box (18) is provided with water level controller (24).
2. A vapour-liquid separation recovery device according to claim 1, characterized in that the vapour condensing duct (14) is arranged inside the mounting tank (13), and the recovery tank (18) is arranged above the mounting tank (13).
3. A vapour-liquid separation recovery device according to claim 2, characterized in that the bottom of the vapour-liquid separator (15) is provided with a condensate pipe (16), the surface of the condensate pipe (16) being provided with a valve.
4. A vapour-liquid separation recovery device according to claim 3, characterized in that the top of the recovery tank (18) is provided with a mounting tube (22) in a penetrating way, the mounting tube (22) being arranged on one side of the circulation pump (21).
5. The vapor-liquid separation and recovery device according to claim 4, wherein a delivery pipe (23) is provided on one side of the circulation pump (21), and one end of the delivery pipe (23) is inserted into the liquid heating tank (11).
6. The vapor-liquid separation and recovery device according to claim 5, wherein a water tank (26) is provided at the rear of the installation tank (13), and a water pump (27) is provided at the top of the water tank (26).
7. The vapor-liquid separation and recovery device according to claim 6, wherein a water pipe is provided at the top of the water pump (27), and one end of the water pipe is provided inside the recovery tank (18).
8. The vapor-liquid separation and recovery device according to claim 7, wherein the bottoms of the installation tank (13) and the liquid heating tank (11) are respectively provided with supporting legs, and the fixing pipe (17) is arranged above the vapor condensing pipe (14).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202323474773.7U CN221513556U (en) | 2023-12-20 | 2023-12-20 | Vapour-liquid separation recovery unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202323474773.7U CN221513556U (en) | 2023-12-20 | 2023-12-20 | Vapour-liquid separation recovery unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN221513556U true CN221513556U (en) | 2024-08-13 |
Family
ID=92204835
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202323474773.7U Active CN221513556U (en) | 2023-12-20 | 2023-12-20 | Vapour-liquid separation recovery unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN221513556U (en) |
-
2023
- 2023-12-20 CN CN202323474773.7U patent/CN221513556U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103910399B (en) | Rubbish leachate treatment system | |
| CN102219273B (en) | Solar and thermocompression vapor-compression distillation type water purifying device | |
| CN206156788U (en) | Miniature sea water desalination device based on waste heat utilization | |
| CN201373623Y (en) | Combined secondary steam heat energy recovery device for conventional phase change heat exchanger of steam jet heat pump | |
| CN106766342B (en) | System for recovering ammonia steam waste heat at top of ammonia still tower by using lithium bromide absorption heat pump | |
| CN109095535B (en) | Sewage evaporation concentration device and operation method thereof | |
| CN103830921A (en) | System and technology for evaporation concentration of extraction water | |
| CN102329035B (en) | Fresh water collecting and supplying system | |
| CN201373694Y (en) | Combined secondary steam heat energy recovery device for heat pipe phase change heat exchanger of steam jet heat pump | |
| CN108251144B (en) | Process and system for realizing final dehydration of tar by recycling waste heat of heat pump unit | |
| CN221513556U (en) | Vapour-liquid separation recovery unit | |
| JP4139597B2 (en) | Desalination equipment | |
| CN210656809U (en) | Tar negative pressure dewatering system | |
| CN110306969B (en) | Oil-water separation and wastewater evaporation concentration heat pump system device of oil field oil extraction gathering and transportation station | |
| CN204173942U (en) | Rubbish leachate treatment system | |
| CN201373695Y (en) | Combined secondary steam heat energy recovery device for heat pipe phase change heat exchanger of combined heat pump | |
| CN218089250U (en) | Concentrated solution processing apparatus based on water source heat pump | |
| CN104986819A (en) | Photovoltaic solar waste heat evaporation process free of energy consumption | |
| CN2839249Y (en) | Energy-saving distilled water machine | |
| CN207113295U (en) | A kind of oilfield sewage waste heat recovery utilization system | |
| CN215250668U (en) | Negative pressure debenzolization device | |
| CN105423623A (en) | Sewage heating heat pump capable of replacing large-sized heating boiler | |
| CN215523230U (en) | Steam condensate recovery device | |
| CN215905885U (en) | Full-quantification landfill leachate treatment device | |
| CN203736879U (en) | Extracted water evaporating and concentrating system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |