CN210394267U - Gas-liquid separator and thermal cracking equipment - Google Patents
Gas-liquid separator and thermal cracking equipment Download PDFInfo
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- CN210394267U CN210394267U CN201921116838.1U CN201921116838U CN210394267U CN 210394267 U CN210394267 U CN 210394267U CN 201921116838 U CN201921116838 U CN 201921116838U CN 210394267 U CN210394267 U CN 210394267U
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- liquid
- pipeline
- gas
- pyroligneous
- combustible gas
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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Abstract
The utility model relates to an embodiment discloses a vapour and liquid separator, include: the device comprises a U-shaped pipeline, wherein an air inlet is formed in one end of the pipeline, an air outlet is formed in the other end of the pipeline, a switch valve is arranged at the bottom of the pipeline, and liquid which is lower in density than pyroligneous liquor and is not mutually soluble with the pyroligneous liquor is filled in the pipeline. Combustible gas obtained after thermal cracking enters the pipeline from the gas inlet, the gas pressure at the gas inlet is higher than that at the gas outlet, and the combustible gas is forced to pass through the liquid in the pipeline to reach the gas outlet; in the process that combustible gas passes through liquid, fine particle carbon powder is intercepted by liquid, gaseous acid and liquid quench reaction restore into liquid pyroligneous, pyroligneous density is higher than liquid, after the obstructed liquid in the pipeline is stood still, pyroligneous subsides in the liquid bottom and stratifies with liquid, discharge pyroligneous this moment through opening the ooff valve, above-mentioned technical scheme can convenient and fast get rid of fine particle carbon powder and gaseous acid in the combustible gas, the structure is ingenious.
Description
Technical Field
The utility model relates to a refuse treatment technical field, in particular to vapour and liquid separator and thermal cracking equipment.
Background
The biomass energy is a green and clean energy source and is the only renewable carbon source, the biomass thermal cracking technology is an important form for biomass energy utilization, and the biomass energy can be converted into other energy forms such as biomass oil and the like, so that the biomass energy is easy to store and use. With the emergence of the petroleum crisis and the development and utilization of new energy technologies, the biomass thermal cracking technology is receiving more and more attention. Can produce bio-oil, combustible gas and living beings charcoal among the current living beings thermal cracking process, contain fine particle carbon dust and gaseous acid in the combustible gas who obtains after the thermal cracking is accomplished, the current separator structure that is arranged in getting rid of impurity among the combustible gas is complicated, and is with high costs, for this reason the utility model provides a simple structure be used for supplementary separation to purify vapour and liquid separator and thermal cracking equipment.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to solve one of the technical problem that exists among the prior art at least, provide a vapour and liquid separator and thermal cracking equipment, fine particle carbon dust and gaseous acid in the combustible gas of detaching that can be ingenious simultaneously.
According to the utility model discloses a first aspect provides a vapour and liquid separator, include: the wood vinegar liquid mixing device comprises a U-shaped pipeline, wherein an air inlet is formed in one end of the pipeline, an air outlet is formed in the other end of the pipeline, a switch valve is arranged at the bottom of the pipeline, and liquid which is lower in density than wood vinegar liquid and is not mutually soluble with the wood vinegar liquid is filled in the pipeline.
The air outlet is connected with an air extraction compressor.
The end part of the pipeline, which is provided with the air outlet, is higher than the end part of the pipeline, which is provided with the air inlet.
The liquid is set to be pure water.
The pipeline is characterized in that openings are formed in two ends of the pipeline, first flanges are arranged at the openings, the openings are sealed through sealing covers, second flanges are arranged at the joints of the sealing covers and the openings, and the sealing covers are provided with air inlets or air outlets.
Any one of the technical schemes at least has the following beneficial technical effects: combustible gas obtained after thermal cracking enters the pipeline from the gas inlet, the gas pressure at the gas inlet is higher than that at the gas outlet in the process of continuously accumulating the combustible gas, and the combustible gas is forced to pass through liquid in the pipeline to reach the gas outlet; in the process that combustible gas passes through liquid, fine particle carbon powder is intercepted by the liquid, gaseous acid and liquid quench reaction are reduced into liquid pyroligneous, pyroligneous density is higher than liquid, and after liquid is not communicated in the pipeline and stands still, pyroligneous settles at the bottom of the liquid and is layered with the liquid, and the pyroligneous is discharged by opening the switch valve at the moment.
A thermal cracking apparatus comprising said gas-liquid separator.
The technical scheme at least has the following beneficial technical effects: combustible gas obtained after thermal cracking enters the pipeline from the gas inlet, the gas pressure at the gas inlet is higher than that at the gas outlet in the process of continuously accumulating the combustible gas, and the combustible gas is forced to pass through liquid in the pipeline to reach the gas outlet; in the process that combustible gas passes through liquid, fine particle carbon powder is intercepted by liquid, gaseous acid and liquid quench reaction are reduced into liquid pyroligneous, pyroligneous density is higher than liquid, and after liquid is not communicated in the pipeline and is kept stand, pyroligneous settles at the bottom of the liquid and is layered with the liquid, and the pyroligneous is discharged by opening the switch valve at the moment.
Drawings
The present invention will be further described with reference to the accompanying drawings and examples;
fig. 1 is a schematic diagram of an embodiment of the present invention.
Detailed Description
This section will describe in detail the embodiments of the present invention, preferred embodiments of the present invention are shown in the attached drawings, which are used to supplement the description of the text part of the specification with figures, so that one can intuitively and vividly understand each technical feature and the whole technical solution of the present invention, but they cannot be understood as the limitation of the protection scope of the present invention.
In the description of the present invention, it should be understood that the orientation or positional relationship indicated with respect to the orientation description, such as up, down, front, rear, left, right, etc., is based on the orientation or positional relationship shown in the drawings, and is only for convenience of description and simplification of description, and does not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and thus, should not be construed as limiting the present invention.
In the description of the present invention, a plurality of means are one or more, a plurality of means are two or more, and the terms greater than, less than, exceeding, etc. are understood as not including the number, and the terms greater than, less than, within, etc. are understood as including the number. If the first and second are described for the purpose of distinguishing technical features, they are not to be understood as indicating or implying relative importance or implicitly indicating the number of technical features indicated or implicitly indicating the precedence of the technical features indicated.
In the description of the present invention, unless there is an explicit limitation, the words such as setting, installation, connection, etc. should be understood in a broad sense, and those skilled in the art can reasonably determine the specific meanings of the above words in combination with the specific contents of the technical solution.
Referring to fig. 1, a gas-liquid separator includes: be the pipeline 1 of U type, pipeline 1 one end is provided with air inlet 2, and the other end of pipeline 1 is provided with gas outlet 3, and the bottom of pipeline 1 is provided with a ooff valve 4, and the intussuseption of pipeline 1 is filled with density and is less than pyrolkigneous liquid 5 and not with the liquid 6 that pyrolkigneous liquid 5 is mutually soluble, and liquid 6 preferred sets up to the pure water, easily acquires low cost. Combustible gas obtained after thermal cracking enters the pipeline 1 from the gas inlet 2, the gas pressure at the gas inlet 2 is higher than that at the gas outlet 3 in the process of continuously accumulating the combustible gas, and the combustible gas is forced to reach the gas outlet 3 through the liquid 6 in the pipeline 1; in the process that combustible gas passes through liquid 6, the fine particle carbon powder is intercepted by liquid 6, the quenching reaction of gaseous acid and liquid 6 is reduced into liquid pyroligneous 5, the density of pyroligneous 5 is higher than that of liquid 6, after the liquid 6 is not communicated in the pipeline 1 and stands, the pyroligneous 5 is settled at the bottom of the liquid 6 and is layered with the liquid 6, and the pyroligneous 5 is discharged by opening the switch valve 4 at the moment, so that the technical scheme can conveniently and rapidly remove the fine particle carbon powder and the gaseous acid in the combustible gas, and the structure is simple and ingenious.
In some embodiments, as shown in fig. 1, in order to accelerate the passage of the combustible gas through the liquid 6, a suction compressor is connected to the gas outlet 3, by which the gas pressure in the vicinity of the gas outlet 3 is reduced and the pressure difference between the vicinity of the gas outlet 3 and the vicinity of the gas inlet 2 is increased, so that the combustible gas can more easily pass through the liquid 6.
When combustible gas passes through liquid 6, the liquid level near gas outlet 3 can be higher than the liquid level of gas inlet 2, and for this reason preferred, the tip that pipeline 1 was provided with gas outlet 3 is higher than the tip that is provided with gas inlet 2, can save pipeline 1 consumptive material, reduces the shared space of pipeline 1 simultaneously.
As shown in fig. 1, in some embodiments, both ends of the pipeline 1 have openings, a first flange 8 is disposed at the opening, the opening is sealed by a sealing cover 7, a second flange 9 is disposed at a joint of the sealing cover 7 and the opening, an air inlet 2 or an air outlet 3 is disposed on the sealing cover 7, a sealing rubber ring is disposed between the first flange 8 and the second flange 9, the first flange 8 and the second flange 9 are fixed by bolts, the opening is detachably sealed by the sealing cover 7, and the pipeline 1 is convenient to clean and maintain at a later stage.
A thermal cracking apparatus includes a gas-liquid separator. Combustible gas obtained after thermal cracking enters the pipeline 1 from the gas inlet 2, the gas pressure at the gas inlet 2 is higher than that at the gas outlet 3 in the process of continuously accumulating the combustible gas, and the combustible gas is forced to reach the gas outlet 3 through the liquid 6 in the pipeline 1; in the process that combustible gas passes through liquid 6, fine particle carbon powder is intercepted by liquid 6, gaseous acid and liquid 6 quench reaction reduce into liquid pyroligneous 5, pyroligneous 5 is higher than liquid 6 in density, after obstructed liquid 6 is stood in pipeline 1, pyroligneous 5 subsides in liquid 6 bottom and stratifies with liquid 6, discharge pyroligneous 5 through opening ooff valve 4 this moment, it can be seen that above-mentioned technical scheme's thermal cracking equipment can be convenient and fast get rid of fine particle carbon powder and gaseous acid in the combustible gas, simple structure is ingenious.
The embodiments of the present invention have been described in detail with reference to the accompanying drawings, but the present invention is not limited to the above embodiments, and various changes can be made without departing from the spirit of the present invention within the knowledge of those skilled in the art.
Claims (6)
1. A gas-liquid separator, comprising: the wood vinegar liquid mixing device comprises a U-shaped pipeline, wherein an air inlet is formed in one end of the pipeline, an air outlet is formed in the other end of the pipeline, a switch valve is arranged at the bottom of the pipeline, and liquid which is lower in density than wood vinegar liquid and is not mutually soluble with the wood vinegar liquid is filled in the pipeline.
2. A gas-liquid separator according to claim 1 wherein said gas outlet is connected to a suction compressor.
3. A gas-liquid separator according to claim 1 wherein the end of said conduit at which said outlet port is located is higher than the end at which said inlet port is located.
4. A gas-liquid separator as claimed in claim 1 wherein said liquid is provided as purified water.
5. The gas-liquid separator according to claim 1 wherein said conduit has openings at each end, said openings having a first flange, said openings being sealed by a cover, said cover having a second flange at a junction with said openings, said cover having said gas inlet or said gas outlet.
6. A thermal cracking apparatus comprising a gas-liquid separator according to any one of claims 1 to 5.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921116838.1U CN210394267U (en) | 2019-07-16 | 2019-07-16 | Gas-liquid separator and thermal cracking equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921116838.1U CN210394267U (en) | 2019-07-16 | 2019-07-16 | Gas-liquid separator and thermal cracking equipment |
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| Publication Number | Publication Date |
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| CN210394267U true CN210394267U (en) | 2020-04-24 |
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| CN201921116838.1U Active CN210394267U (en) | 2019-07-16 | 2019-07-16 | Gas-liquid separator and thermal cracking equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110373216A (en) * | 2019-07-16 | 2019-10-25 | 中山市至善生物科技有限公司 | A kind of gas-liquid separator and apparatus for thermal cleavage |
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2019
- 2019-07-16 CN CN201921116838.1U patent/CN210394267U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110373216A (en) * | 2019-07-16 | 2019-10-25 | 中山市至善生物科技有限公司 | A kind of gas-liquid separator and apparatus for thermal cleavage |
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