CN204477685U - The recycling residual heat gasification installation of liquid gas - Google Patents
The recycling residual heat gasification installation of liquid gas Download PDFInfo
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- CN204477685U CN204477685U CN201520073289.XU CN201520073289U CN204477685U CN 204477685 U CN204477685 U CN 204477685U CN 201520073289 U CN201520073289 U CN 201520073289U CN 204477685 U CN204477685 U CN 204477685U
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- heat
- heat exchanger
- accumulation
- water tank
- bucket
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Abstract
The utility model discloses a kind of recycling residual heat gasification installation of liquid gas.Comprise heat exchanger, drencher and circulation water channel, described heat exchanger comprises heat exchange water tank and is located at the coil pipe in described heat exchange water tank, the entrance of described heat exchanger coiled pipe is connected to the gas outlet of corresponding accumulation of heat bucket, the peripheral wall surfaces of described heat exchanger coiled pipe is laid with radiating fin, be connected with filter between the gas outlet of described heat exchanger coiled pipe and accumulation of heat bucket, between the entrance of described heat exchange water tank and circulation water channel, be connected with a circulating water pump; The entrance of described drencher is connected respectively by the outlet of the collecting annulus of corresponding control valve and bathroom, solar water heater and described heat exchange water tank.The recycling residual heat gasification installation operating cost of this liquid gas is low, energy-conserving and environment-protective.
Description
Technical field
The utility model relates to a kind of recycling residual heat gasification installation of liquid gas.
Background technique
The electric heating ability of swimming vaporizer structure of existing liquefied petroleum gas is by the cylindrical shell of band insulation, coiler, electric heater, the compositions such as liquid phase connecting tube, liquefied petroleum gas enters vaporizer along liquid-phase tube entrance, the inside serpentine coil soaked in the hot water along it from top to bottom flows, the heat of the outer hot water transmission of absorption tube and gasifying, the liquefied petroleum gas (LPG) of gaseous state is risen by the gas collecting tube of centre, confess after the pressure regulation of gas phase pipe, LPG (liquefied petroleum gas) residual liquid is discharged by gas collecting tube bottom blow-down pipe, but, this vaporizer process structure is complicated, heat absorption area is not enough, vaporization ability is on the low side, when air demand is excessive or exceed the vaporization ability of equipment, vaporizer gaseous phase outlet duct ligation is easily caused to reveal, gas phase pipe is outward with the globule or frosting, thus lose vaporization ability, and only using electricity as thermal source power, energy consumption is large, water energising immersed with liquefied gas tank body is heated simultaneously, dangerous.
And the existing gasification installation utilizing the liquid gas of gas-heating apparatus, because entire system composition structure is unreasonable, and the working efficiency of the heat exchange method of its heat exchanger is not ideal enough.Make the operational effect human world not to the utmost of whole gasification installation.
Model utility content
The utility model object is for prior art Problems existing, provides a kind of recycling residual heat gasification installation of liquid gas.The recycling residual heat gasification installation structure of this liquid gas is simple, operating cost is low, energy-conserving and environment-protective.
The recycling residual heat gasification installation of liquid gas of the present utility model comprises heat exchanger, liquefied gas tank heating chamber, described heat exchanger comprises heat exchange water tank and is located at the coil pipe in described heat exchange water tank, the entrance of described heat exchanger coiled pipe is connected to the gas outlet of corresponding accumulation of heat bucket, the peripheral wall surfaces of described heat exchanger coiled pipe is laid with radiating fin, filter is connected with between the gas outlet of described heat exchanger coiled pipe and accumulation of heat bucket, described liquefied gas tank heating chamber comprises drencher and circulation water channel, a circulating water pump is connected with between the entrance of described heat exchange water tank and circulation water channel, the entrance of described drencher is respectively by the collecting annulus of corresponding control valve and bathroom, solar water heater is connected with the outlet of described heat exchange water tank.
Described accumulation of heat bucket is arranged at the relative both sides of the burner of combustion furnace or boiler, and this accumulation of heat bucket is a truncated cone shape accumulation of heat bucket, is provided with heat-storing sphere in truncated cone shape accumulation of heat bucket.
Described heat exchange water tank, collecting annulus and solar water heater are respectively equipped with temperature transducer, and the described control valve being connected to described sprinkler entrance is solenoid valve, and described solenoid valve is connected with an intelligent controller respectively by signaling line with each temperature transducer.
The recycling residual heat gasification installation of the utility model liquid gas by carrying out the recycle and reuse of multipath intelligent comprehensive to the waste heat of boiler or burner etc., not only energy saving but also safety and environmental protection.System architecture is simple, implementation cost is low, easy to operate, and the heat exchange efficiency of its heat exchanger is high, energy-conservation, safety, environmental protection.Be specially adapted to liquefied gas station distribution.
Accompanying drawing explanation
Fig. 1 is the recycling residual heat gasification installation one example structure schematic diagram of model utility liquid gas.
Embodiment
Now in conjunction with the accompanying drawings and embodiments the utility model is described in detail.As shown in Figure 1, the recycling residual heat gasification installation of the liquid gas of the present embodiment comprises the sprinkler 1 be located at above liquefied gas tank 2, heat exchanger 15, circulating water pump 13 etc., the heat exchanger coiled pipe 6 that heat exchanger comprises heat exchange water tank 5 and is located in heat exchange water tank 5, the periphery wall of heat exchanger coiled pipe 6 is laid with radiating fin 6a.The outlet of heat exchanger coiled pipe 6 can be connected with smoke-ejecting pipe or emptying directly to outside.The exhausting air of the accumulation of heat bucket 9 of the entrance of heat exchanger coiled pipe 6 and boiler or combustion furnace 8 exports and is connected, accumulation of heat bucket 9 is one be arranged at the truncated cone shape of the both sides of the corresponding site of boiler or combustion furnace 8 or the accumulation of heat bucket of pinnacle of a pagoda type, be filled with heat-storing sphere 10 in the accumulation of heat bucket of truncated cone shape or pinnacle of a pagoda type, and the quantity that the heat-storing sphere 10 set by accumulation of heat bucket 9 inner chamber of truncated cone shape or pinnacle of a pagoda type distributes on accumulation of heat bucket 9 cross section reduces gradually from bottom to top.Utilize the exhausting air of accumulation of heat bucket after carrying out heat exchange with boiler or combustion furnace 8 to send into heat exchanger 15 to heat the water in its heat exchange water tank.The heat recovery mode of this heat exchange structure and accumulation of heat bucket thereof has better recycles efficiency.
Between the exhausting air outlet and heat exchanger coiled pipe 6 of accumulation of heat bucket 9, be connected with filter 11, its filter 11 is ceramic packing filter, can avoid heat exchanger coiled pipe system jams, and can improve discharge environment.The bottom of liquefied gas tank 2 is provided with circulation water channel 7, and circulating water pump 13 is connected between the lower entrances of circulation water channel 7 and heat exchange water tank 5.The water collecting annulus 3 of the upper outlet of heat exchange water tank 5, solar water heater 4 and bathroom is connected with the entrance of drencher 1 respectively by corresponding solenoid valve 12, is collected by the spent hot water of collecting annulus 3 pairs of bathrooms.
By arranging the accumulation of heat bucket of said structure in the heat-exchange system of boiler or combustion furnace, the waste heat of heat exchanger to boiler or combustion furnace is made to obtain balanced use.The heating and gasifying of liquefied gas tank is more even, steady.
Solar water heater 4, water-collecting machine 3 and heat exchange water tank 5 are respectively equipped with temperature transducer 14, and each temperature transducer 14 is connected with an intelligent controller input end by signaling line, and the corresponding output terminal of intelligent controller is connected with solenoid valve 12 respectively by signaling line.By intelligent controller according to solar water heater 4, heat exchange water tank 5 or/and the water temperature of collecting annulus 3 is by the water supply of electromagnetic valve to drencher.By circulation water channel 7 drencher 1 sprayed liquefied gas tank 2 pairs of liquefied gas tanks heat after waste water collect after, deliver to heat exchange water tank 5 through circulating water pump 13, recycle.Drencher 1 can be spraying tube.
In another embodiment of the utility model, the output pipeline of its solar water heater, heat exchange water tank and collecting annulus is respectively equipped with the flow transducer being connected to intelligent controller by signaling line, controls the water supply to drencher of solar water heater, water-collecting machine and/or heat exchange water tank respectively by intelligent controller uninterrupted as required.All the other structures of this example etc. can with above-described embodiment roughly the same.
Claims (3)
1. the recycling residual heat gasification installation of a liquid gas, comprise heat exchanger, liquefied gas tank heating chamber, it is characterized in that described heat exchanger comprises heat exchange water tank and is located at the coil pipe in described heat exchange water tank, the entrance of described heat exchanger coiled pipe is connected to the gas outlet of corresponding accumulation of heat bucket, the peripheral wall surfaces of described heat exchanger coiled pipe is laid with radiating fin, filter is connected with between the gas outlet of described heat exchanger coiled pipe and accumulation of heat bucket, described liquefied gas tank heating chamber comprises drencher and circulation water channel, a circulating water pump is connected with between the entrance of described heat exchange water tank and circulation water channel, the entrance of described drencher is respectively by the collecting annulus of corresponding control valve and bathroom, solar water heater is connected with the outlet of described heat exchange water tank.
2. the recycling residual heat gasification installation of liquid gas according to claim 1, it is characterized in that described accumulation of heat bucket is arranged at the relative both sides of the burner of combustion furnace or boiler, this accumulation of heat bucket is a truncated cone shape accumulation of heat bucket, is provided with heat-storing sphere in truncated cone shape accumulation of heat bucket.
3. the recycling residual heat gasification installation of liquid gas according to claim 1, it is characterized in that described heat exchange water tank, collecting annulus and solar water heater are respectively equipped with temperature transducer, the described control valve being connected to described sprinkler entrance is solenoid valve, and described solenoid valve is connected with an intelligent controller respectively by signaling line with each temperature transducer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520073289.XU CN204477685U (en) | 2015-02-02 | 2015-02-02 | The recycling residual heat gasification installation of liquid gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520073289.XU CN204477685U (en) | 2015-02-02 | 2015-02-02 | The recycling residual heat gasification installation of liquid gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204477685U true CN204477685U (en) | 2015-07-15 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520073289.XU Expired - Fee Related CN204477685U (en) | 2015-02-02 | 2015-02-02 | The recycling residual heat gasification installation of liquid gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204477685U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107192132A (en) * | 2016-03-15 | 2017-09-22 | 北京强度环境研究所 | A kind of double thermal source water bath carburetors of afterheat recovery type |
| CN110953431A (en) * | 2019-12-20 | 2020-04-03 | 陕西博睿信息科技有限公司 | A pipeline cooling device for petrochemical plant |
-
2015
- 2015-02-02 CN CN201520073289.XU patent/CN204477685U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107192132A (en) * | 2016-03-15 | 2017-09-22 | 北京强度环境研究所 | A kind of double thermal source water bath carburetors of afterheat recovery type |
| CN110953431A (en) * | 2019-12-20 | 2020-04-03 | 陕西博睿信息科技有限公司 | A pipeline cooling device for petrochemical plant |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150715 Termination date: 20170202 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |