CN219300505U - Bubbling vaporizer - Google Patents
Bubbling vaporizer Download PDFInfo
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- CN219300505U CN219300505U CN202222664350.0U CN202222664350U CN219300505U CN 219300505 U CN219300505 U CN 219300505U CN 202222664350 U CN202222664350 U CN 202222664350U CN 219300505 U CN219300505 U CN 219300505U
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- air
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- pipe
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- light hydrocarbon
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Abstract
The utility model discloses a bubbling vaporizer for producing mixed air light hydrocarbon fuel gas by taking liquid light hydrocarbon as a raw material, which comprises a vertical cylindrical tank body, an air inlet pipe, a fuel gas outlet pipe, an oil inlet pipe, an oil outlet pipe assembly and a thermocouple thermometer assembly which are fixedly arranged on the vertical cylindrical tank body, wherein a disc-shaped air disc with a plurality of through holes distributed on the lower part of the cylindrical tank body is fixedly arranged on the lower part of the cylindrical tank body, a terminal pipe orifice of the air inlet pipe is arranged below the air disc, a plurality of strip-shaped guide plates are uniformly distributed on the lower part of the air disc along the radial direction of the air disc and in the direction perpendicular to the air disc, and a disc-shaped guide plate is fixedly arranged below the guide plates. The bubbling vaporizer has simple structure, and can improve the gasification rate of liquid light hydrocarbon and the heat value of mixed light hydrocarbon gas.
Description
Technical Field
The utility model relates to a vaporizer, in particular to a bubbling vaporizer for producing mixed air light hydrocarbon fuel gas by taking liquid light hydrocarbon as a raw material.
Background
The mixed air light hydrocarbon gas is used as a novel gas source for various gas heating facilities of urban residents and industrial enterprises. The liquid light hydrocarbon vaporizer is key equipment in a mixed air light hydrocarbon gas making device, chinese patent grant publication No. CN201047489Y, grant publication No. 2008, 4 months and 16 days, and the utility model is named: the application discloses a bubbling vaporizer, which has the defect that when the diameter of a tank body of the bubbling vaporizer reaches or exceeds 1.2 meters, the gasification rate of liquid light hydrocarbon and the heat value of the prepared air-mixed light hydrocarbon gas are reduced.
Disclosure of Invention
In order to overcome the defects of the prior art, the utility model provides the bubbling vaporizer which has a simple structure and can improve the gasification rate of liquid light hydrocarbon and the calorific value of the prepared mixed air light hydrocarbon fuel gas.
The technical scheme adopted for solving the technical problems is as follows: the utility model provides a bubble vaporizer, includes a vertical cylindrical jar body and air intake pipe, gas outlet pipe, advance oil pipe, play oil pipe subassembly and a thermocouple thermometer subassembly that set firmly on it, encircles the periphery of the cylindrical jar body and has set firmly a hot water sleeve pipe, hot water sleeve pipe's lower extreme and upper end have set firmly inlet tube and outlet pipe respectively, the disk-shaped air dish that distributes numerous through-holes has set firmly to the lower part in the cylindrical jar body, and the below of air dish is arranged in to the terminal mouth of pipe of air intake pipe, evenly distributed has a plurality of rectangular guide plate along its radial and with the perpendicular direction of air dish below the air dish, set firmly a discoid guide plate below the guide plate.
The number of the strip-shaped guide plates is 8, and the diameter of the disc-shaped guide plate is 0.9 times of that of the disc-shaped air plate.
The beneficial effects of the utility model are as follows: when the diameter of the cylindrical tank body of the bubbling vaporizer is 1.2-2 meters, the liquid light hydrocarbon gasification rate of the bubbling vaporizer still can reach 95-100%, and the heat value of the prepared mixed air light hydrocarbon fuel gas can reach 6000kcal/m 3 ～8000kcal/m 3 And the structure is simple.
Drawings
The utility model will be further described with reference to the drawings and examples.
Fig. 1 is a front view of the present utility model.
Fig. 2 is a sectional view A-A in fig. 1.
In the figure, a carburetor 1, a fuel gas outlet pipe 2, an air inlet pipe 3, an oil inlet pipe 4, a thermocouple thermometer assembly 5, a tank 6, a water outlet pipe 7, an air disk 8, a guide plate 9, a guide plate 10, a guide plate 11, a water inlet pipe 12, a hot water sleeve pipe 13 and an oil outlet pipe assembly.
Detailed Description
Examples: in fig. 1 and 2, the main body of the bubbling vaporizer 1 is a steel vertical cylindrical tank 6, on which a gas outlet pipe 2, an air inlet pipe 3, an oil inlet pipe 4 and an oil outlet pipe assembly 13 made of steel pipes are welded respectively, a steel cylindrical hot water sleeve 12 with two closed ends is welded around the cylindrical periphery of the tank 6, a separate closed space is formed between the hot water sleeve 12 and the two cylindrical barrels of the tank 6, a water inlet pipe 11 and a water outlet pipe 7 made of steel pipes are welded respectively at the lower end and the upper end of the hot water sleeve 12, a thermocouple thermometer assembly 5 is welded at the top end of the tank 6, a disc-shaped air disk 8 made of steel plates and provided with a plurality of through holes is welded at the lower part of the tank 6, the end pipe orifice of the air inlet pipe 3 is arranged below the air disk 8, strip-shaped guide plates 9 made of 8 are welded on the lower surface of the air disk 8 along the radial direction of the air disk 8, the number of the guide plates 9 is determined according to the diameter of the air disk 8, the number of the guide plates is more than the number of the guide plates 9, and the number of the guide plates 9 is 10, and the number of the guide plates is more than the number of the guide plates 9 is 10, and the number of the guide plates are welded in the diameter of the guide plates is 10.
When the bubbling vaporizer 1 works, the lower part in the tank body 6 is filled with liquid light hydrocarbon, compressed air is sprayed downwards from the tail end pipe orifice positioned below the air disk 8 through the air inlet pipe 3 in the form of air bubbles and then is blocked by the guide disk 10, the original vertical downward advancing direction is forced to be changed, the center of the guide disk 10 flows to the inner wall direction of the tank body 6 along the radial direction of the guide disk 10, a part of the air bubbles reach the inner wall of the tank body 6 and then upwards pass through the through holes in the air disk 8 to enter the liquid light hydrocarbon above the air disk 8, the liquid light hydrocarbon continuously floats until the liquid light hydrocarbon is separated from the liquid light hydrocarbon liquid level in the tank body 6, and then the mixed air light hydrocarbon gas is formed to flow to a user gas pipeline through the gas outlet pipe 2, and the guide disk 9 has the function of uniformly distributing the air bubbles below the air disk 8 along all directions of the whole circumference of the air disk 8. When the bubbling vaporizer 1 works, liquid light hydrocarbon stored in a raw material tank of the air-fuel light hydrocarbon gas production device enters the tank body 6 through the oil inlet pipe 4 to supplement the liquid light hydrocarbon consumed in the gasification process, and when the liquid level of the liquid light hydrocarbon in the tank body 6 exceeds the horizontal pipe section of the oil outlet pipe assembly 13, the redundant liquid light hydrocarbon automatically flows out of the tank through the horizontal pipe section of the oil outlet pipe assembly 13. The gasification process of the liquid light hydrocarbon in the tank body 6 is an endothermic process, so that a certain amount of heat is required to be input into the vaporizer 1 in the process, the working temperature of the vaporizer 1 is set to be 18 ℃ at the lowest temperature and 22 ℃ at the highest temperature, when the working temperature is lower than 18 ℃, the thermocouple thermometer assembly 5 sends a signal to a control system in the mixed light hydrocarbon gas production device, hot water in the mixed light hydrocarbon gas production device enters an independent closed space formed between the hot water sleeve 12 and the cylindrical cylinder body of the tank body 6 through the water inlet pipe 11 and flows out through the water outlet pipe 7 to form a continuous hot water circulation state, the heat is transmitted inwards through the outer wall of the cylinder body of the tank body 6 to enable the working temperature of the vaporizer 1 to be continuously increased, when the working temperature is increased to 22 ℃, the thermocouple assembly 5 sends a signal to the control system in the mixed light hydrocarbon gas production device, the working temperature of the vaporizer 1 is stopped from being continuously increased along with the operation of the vaporizer 1, when the working temperature of the vaporizer 1 is continuously reduced to 18 ℃, and when the working temperature of the thermocouple assembly is increased to be controlled again in the mixed light hydrocarbon production device, and the working temperature of the vaporizer 1 is continuously increased to be in the state between the two cylindrical cylinders, and the vaporizer 1 is repeatedly kept at the working temperature of the mixed light hydrocarbon production device and the vaporizer 1.
Claims (3)
1. The utility model provides a bubble vaporizer, includes a vertical cylindrical jar body and air intake pipe, gas outlet pipe, advance oil pipe, play oil pipe subassembly and a thermocouple thermometer subassembly that set firmly on it, encircles the periphery of the cylindrical jar body and has set firmly a hot water sleeve pipe, hot water sleeve pipe's lower extreme and upper end have set firmly inlet tube and outlet pipe respectively, the disk-shaped air dish that distributes numerous through-holes has set firmly to the lower part in the cylindrical jar body, and the below of air dish is arranged in to the terminal mouth of pipe of air intake pipe, characterized by: the air disk is characterized in that a plurality of strip-shaped guide plates are uniformly distributed below the air disk along the radial direction of the air disk and in the direction perpendicular to the air disk, and a disk-shaped guide disk is fixedly arranged below the guide plates.
2. The bubbling vaporizer of claim 1, wherein: the number of the strip-shaped guide plates is 8.
3. The bubbling vaporizer of claim 1, wherein: the diameter of the disc-shaped guide disc is 0.9 times of that of the disc-shaped air disc.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222664350.0U CN219300505U (en) | 2022-09-28 | 2022-09-28 | Bubbling vaporizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222664350.0U CN219300505U (en) | 2022-09-28 | 2022-09-28 | Bubbling vaporizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219300505U true CN219300505U (en) | 2023-07-04 |
Family
ID=86981996
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202222664350.0U Active CN219300505U (en) | 2022-09-28 | 2022-09-28 | Bubbling vaporizer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219300505U (en) |
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2022
- 2022-09-28 CN CN202222664350.0U patent/CN219300505U/en active Active
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