CN217716070U - Flash evaporation gas heat exchange device and system - Google Patents
Flash evaporation gas heat exchange device and system Download PDFInfo
- Publication number
- CN217716070U CN217716070U CN202123238334.7U CN202123238334U CN217716070U CN 217716070 U CN217716070 U CN 217716070U CN 202123238334 U CN202123238334 U CN 202123238334U CN 217716070 U CN217716070 U CN 217716070U
- Authority
- CN
- China
- Prior art keywords
- water
- heat exchanger
- inlet
- flash
- communicated
- 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
Images
Abstract
The utility model provides a flash distillation gas heat transfer device and system, this system includes: the heat exchanger is provided with a cold water inlet, a hot water outlet and a flash evaporation gas inlet; the flash evaporation gas inlet is used for being connected with a factory equipment terminal so as to recycle secondary flash evaporation gas to the heat exchanger; at least one group of circulating water pumps, wherein each group of circulating water pumps is provided with a water inlet and a water outlet, the water inlet is communicated with a water source to receive cold water, and the water outlet is communicated with a cold water inlet of the heat exchanger through a water pipe so that the circulating water pumps the cold water into the heat exchanger; the bathroom water tank is provided with a water inlet, the water inlet is communicated and connected with a hot water outlet of the heat exchanger through a communicating pipe so as to receive hot water of the heat exchanger, and a liquid level meter for measuring liquid level is arranged in the bathroom water tank; and the controller is in communication connection with the liquid level meter and the heat exchanger.
Description
Technical Field
The utility model relates to a factory equipment terminal exhaust secondary flash distillation gas, concretely relates to application of secondary flash distillation gas.
Background
Most of the existing domestic factories directly boil water through a boiler for bathroom use. In addition, the phenomenon of "white smoke dragon" in factories still appears endlessly and cannot be solved.
SUMMERY OF THE UTILITY MODEL
The utility model provides a flash distillation gas heat transfer device, the device includes:
the heat exchanger is provided with a cold water inlet, a hot water outlet and a flash evaporation gas inlet; the flash evaporation gas inlet is used for being connected with a factory equipment terminal so as to recycle secondary flash evaporation gas to the heat exchanger;
at least one group of circulating water pumps, wherein each group of circulating water pumps is provided with a water inlet and a water outlet, the water inlet is communicated with a water source to receive cold water, and the water outlet is communicated with a cold water inlet of the heat exchanger through a water pipe so that the circulating water pumps the cold water into the heat exchanger;
the bathroom water tank is provided with a water inlet, the water inlet is communicated and connected with a hot water outlet of the heat exchanger through a communicating pipe so as to receive hot water of the heat exchanger, and a liquid level meter for measuring liquid level is arranged in the bathroom water tank;
and the controller is in communication connection with the liquid level meter and the circulating water pump.
Preferably, the circulating water pumps are provided with a plurality of groups.
Preferably, a temperature meter is arranged inside the heat exchanger.
Preferably, the heat exchanger has an overflow, a condensate outlet and an exhaust.
Further, the utility model also provides a flash distillation gas heat transfer system, this system include mill's equipment terminal and aforementioned the device, mill sets up the terminal and has secondary flash distillation gas discharge port, secondary flash distillation gas discharge port communicates with the flash distillation gas entry of heat exchanger.
Drawings
Fig. 1 is the structure schematic diagram of the flash evaporation gas heat exchange device provided by the utility model.
Detailed Description
Example 1
Referring to fig. 1, the present embodiment provides a flash vapor heat exchange device, which includes a heat exchanger 1, at least one set of circulating water pump 2, a bathroom water tank 3, and a controller 5; the heat exchanger 1 is provided with a cold water inlet 11, a hot water outlet 12 and a flash evaporation gas inlet 100; the flash evaporation gas inlet 100 is used for being connected with a terminal of factory equipment so as to recycle secondary flash evaporation gas to the heat exchanger;
the circulating water pump 2 is provided with a water inlet 21 and a water outlet 22, the water inlet 21 is communicated with a water source to receive cold water, and the water outlet 22 is communicated with the cold water inlet 11 of the heat exchanger 1 through a water pipe 23 to enable the circulating water pump 2 to pump the cold water into the heat exchanger 1;
the bathroom water tank 3 has a water inlet which is connected in communication with the hot water outlet 12 of the heat exchanger 1 through a communication pipe 32 to receive the hot water of the heat exchanger 1; therefore, after cold water enters the heat exchanger, the heat exchanger is provided with a secondary flash steam inlet, the cold water is heated to a certain temperature through the waste heat of the secondary flash steam, and then the cold water is discharged and pushed to the bathroom water tank 3.
A liquid level meter 33 for measuring liquid level is arranged in the bathroom water tank 3; the controller 5 is in communication connection with the liquid level meter 33, and the controller 5 is in communication connection with the circulating water pump 2; this embodiment sets for the water level of bathroom water tank to a definite value, and when the level gauge detected that the water level of water tank was less than the setting value, the heat exchanger will be squeezed hot water into the water tank to guarantee that the water tank can continuously supply hot water.
The device can recycle secondary flash steam discharged from the factory equipment end, and the secondary flash steam is heated by exchange with cold water, and the cold water is heated to a certain temperature and then discharged to a bathroom water tank for bathing of factory staff. In this embodiment, the circulating water pumps 2 are provided in two groups, one for each use; the controller is powered by a power supply 51, cold water is pumped into the heat exchanger through a circulating water pump, and the circulating water pump is operated by the controller after being used.
In the present embodiment, a temperature gauge is provided inside the heat exchanger 1.
In the present embodiment, the heat exchanger 1 has an overflow port 16, a condensed water outlet 13, and an exhaust port 15.
It can be understood that, in order to maintain the water way through and the automatic water adding function of the heat exchanger, the device provided by the embodiment includes, but is not limited to, a stop valve, a check valve, a ball valve, etc., and the efficient and controllable work of the whole system is effectively ensured.
Example 2
This embodiment provides a flash distillation gas heat transfer system, this system includes the plant equipment terminal and the device of embodiment 1, the plant sets up the terminal and has secondary flash distillation gas discharge port, secondary flash distillation gas discharge port communicates with the flash vessel entry of heat exchanger.
The set of system device makes full use of secondary flash steam discharged at ordinary times, and water is heated by waste heat of the secondary flash steam, so that the cost of burning a boiler can be saved, the flash steam can be recovered in a centralized manner, the phenomenon of flash steam discharged to the air is eliminated, and the national environmental protection requirement is also met.
Claims (5)
1. A flash vapor heat exchange device is characterized by comprising:
a heat exchanger (1) having a cold water inlet (11), a hot water outlet (12) and a flash gas inlet (100); the flash evaporation gas inlet (100) is used for being connected with a terminal of plant equipment so as to recover secondary flash evaporation gas to the heat exchanger (1);
at least one group of circulating water pumps (2) provided with a water inlet (21) and a water outlet (22), wherein the water inlet (21) is communicated with a water source to receive cold water, and the water outlet (22) is communicated with a cold water inlet (11) of the heat exchanger (1) through a water pipe (23) so that the circulating water pumps (2) pump the cold water into the heat exchanger (1);
the bathroom water tank (3) is provided with a water inlet, the water inlet is communicated and connected with a hot water outlet (12) of the heat exchanger (1) through a communication pipe (32) to receive hot water of the heat exchanger, and a liquid level meter (33) for measuring liquid level is arranged in the bathroom water tank;
and the controller (5) is in communication connection with the liquid level meter (33), and is in communication connection with the circulating water pump.
2. The flash gas heat exchange device according to claim 1, wherein the circulating water pump is provided with a plurality of groups.
3. The flash gas heat exchange device according to claim 1, wherein a temperature meter is arranged inside the heat exchanger.
4. The flash gas heat exchange apparatus of claim 1, wherein the heat exchanger has an overflow port, a condensate outlet, and a vent.
5. A flash gas heat exchange system, characterized in that the system comprises a plant terminal and the device of any one of claims 1 to 4, wherein the plant terminal is provided with a secondary flash gas discharge port, and the secondary flash gas discharge port is communicated with a flash gas inlet of a heat exchanger.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202123238334.7U CN217716070U (en) | 2021-12-21 | 2021-12-21 | Flash evaporation gas heat exchange device and system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202123238334.7U CN217716070U (en) | 2021-12-21 | 2021-12-21 | Flash evaporation gas heat exchange device and system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN217716070U true CN217716070U (en) | 2022-11-01 |
Family
ID=83774219
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202123238334.7U Active CN217716070U (en) | 2021-12-21 | 2021-12-21 | Flash evaporation gas heat exchange device and system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN217716070U (en) |
-
2021
- 2021-12-21 CN CN202123238334.7U patent/CN217716070U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN204555414U (en) | A kind of degression type steam condensate (SC) reclaiming system | |
CN202644252U (en) | Steam iron remnant steam and residual heat recovery device | |
CN207279602U (en) | A kind of closed type condensate water recovery device | |
CN217716070U (en) | Flash evaporation gas heat exchange device and system | |
CN206073240U (en) | A kind of intelligent natural gas heating system | |
CN105588108A (en) | System for replenishing water to steam boiler by means of steam condensate | |
CN104964483B (en) | A kind of recovery type heat sewage source heat pump system | |
CN208253697U (en) | A kind of geothermal heating operating system of accumulation of heat and multistage terminal user's combined heat | |
CN100552290C (en) | Condensation water recovery system | |
CN207501127U (en) | A kind of boiler blowdown water waste heat and water resource recycling system | |
CN207132324U (en) | Steam power plant's condensation water recovery and use system | |
CN203384963U (en) | Steam return water waste heat recovery device | |
CN210462973U (en) | Boiler blow-off flash evaporation recovery equipment | |
CN210069822U (en) | High-pressure high-temperature condensed water flash evaporation recovery system | |
CN204851350U (en) | Utilize living water heating system of power plant's exhaust steam waste heat | |
CN210887400U (en) | Traditional chinese medicine draws comprehensive utilization system of workshop steam condensate | |
CN211204183U (en) | Energy-saving heat recovery steam heat transfer system | |
CN209459460U (en) | A kind of boiler blow-off residual neat recovering system | |
CN208702473U (en) | Closed-up water back heating system | |
CN207501331U (en) | The air-conditioning system that a kind of steam heat recovery utilizes | |
CN110566921A (en) | Gas boiler waste heat recycling device and method | |
CN212584921U (en) | High-pressure return water recovery system for heat transfer oil heat exchanger | |
CN206386911U (en) | A kind of chemical water heating system | |
CN213453598U (en) | Steam condensate recovery device | |
CN204607617U (en) | A kind of waste water evaporation process system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |