CN217235281U - Ground light hydrocarbon gasification tank capable of opposite point-to-point gas supply - Google Patents
Ground light hydrocarbon gasification tank capable of opposite point-to-point gas supply Download PDFInfo
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- CN217235281U CN217235281U CN202220934783.0U CN202220934783U CN217235281U CN 217235281 U CN217235281 U CN 217235281U CN 202220934783 U CN202220934783 U CN 202220934783U CN 217235281 U CN217235281 U CN 217235281U
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- gasification tank
- pipe
- heat pipe
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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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/32—Hydrogen storage
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Abstract
The utility model discloses a but ground light hydrocarbon gasification jar of subtend counter point air feed, include: the gasification tank, the air blowing bag, the air outlet pipe, the liquid level meter and the like; the gasification tank is a horizontal hollow tank body, a closed vertical transparent pipe body is arranged on one side of the gasification tank to form a liquid level meter, four or more groups of lower-opening semi-closed tank bodies are arranged at the top of the gasification tank to form air blowing bags, the tops of the air blowing bags are subjected to round top treatment, openings at the lower parts of the air blowing bags are communicated with the inside of the gasification tank, and each air blowing bag is provided with a pipeline connector to form an air outlet pipe; the lower part of the heating gasification tank is provided with a heater for heating the internal space of the gasification tank; the utility model has the advantages that: the maintenance and the removal are convenient and fast, the maintenance difficulty is low, the potential safety hazard is reduced, and the cost is saved.
Description
Technical Field
The utility model relates to the technical field of energy, in particular to an overground light hydrocarbon gasification tank capable of supplying gas to opposite points.
Background
Most of the existing light hydrocarbon gasification tanks are pre-buried underground, which is inconvenient for maintenance and later removal, the later maintenance and installation cost is too high, the pre-buried light hydrocarbon gasification tanks usually adopt a large main air outlet pipe for external air supply, so in the common technology, a plurality of gas appliances work simultaneously, when multi-point gas transmission is needed, two processing modes are generally provided, one mode is to cut and weld the gas distribution pipe on the large main air outlet pipe, the gas distribution pipe is connected with the gas appliances for air supply, thus the gas supply is more uniform, but the upper space of the large main air outlet pipe is limited, when the points of gas supply are more, the excessive welding pipelines can influence the strength of the pipe body on the large main air outlet pipe, the risk of gas leakage can be caused, the hidden danger of gas explosion is larger, and the other mode is to fixedly weld the gas distribution pipes with fixed quantity on the main air outlet pipe, then weld the branch gas pipelines on the gas distribution pipe, the branch gas pipelines are connected with the gas appliances, can guarantee the body intensity on the big main outlet duct like this, but can lead to the pipeline on the light hydrocarbon gasification jar to be complicated complicatedly, the influence is overhauld, the pipeline laying cost has been increased, and because welded bronchus pipeline quantity is different on every bronchus, so the gas flow that shares because the difference of the interior gas flux of certain time in every bronchus also has very big change, the direct gas output that can lead to every bronchus pipeline is inconsistent, the air feed is inhomogeneous, influence the work efficiency of bronchus line connection gas appliances.
Therefore, the prior art needs a safe and reliable light hydrocarbon gasification tank which can be conveniently maintained and moved, saves manpower and installation cost, saves pipeline laying cost, can supply gas point to point, and can supply a large amount of gas to special gas equipment when necessary.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide a ground light hydrocarbon gasification tank capable of supplying gas to opposite counter points so as to solve the problems mentioned in the background technology.
In order to achieve the above object, the utility model provides a following technical scheme:
an overground light hydrocarbon gasification tank capable of supplying gas to counter-point, comprising: the device comprises a gasification tank, an air blowing bag, an air outlet pipe, a liquid level meter, a heater, a parallel pipe, a support, a bubble generator, an air inlet pipe, a temperature meter port, a pressure meter port, an oil inlet and an oil outlet; the gasification tank is a horizontal hollow tank body, a closed vertical transparent pipe body is arranged on one side of the gasification tank to form a liquid level meter, the upper part and the lower part of the liquid level meter are respectively provided with a pipe body forming balance pipe and a communicating pipe, the balance pipe and the communicating pipe connect the liquid level meter with the gasification tank to lead the inside of the liquid level meter to be communicated with the inside of the gasification tank, the top of the gasification tank is provided with four groups or more than four groups of lower-opening semi-closed tank bodies to form an air blowing bag, the upper part of the air blowing bag is dome-treated, an opening at the lower part of the air blowing bag is communicated with the inside of the gasification tank, and each air blowing bag is provided with a pipeline connector to form an air outlet pipe; the heater is arranged at the lower part of the heating gasification tank and used for heating the internal space of the gasification tank, and comprises a heat pipe built-in channel which is a transverse cylindrical channel arranged below the gasification tank.
Preferably, the heater comprises a sealing head, a heat pipe built-in channel, a heat pipe support and a heat pipe, the heat pipe is a transverse U-shaped pipeline, the heat pipe is built in the gasification tank through the heat pipe built-in channel in a mode that two interfaces face outwards, the gasification tank is provided with the heat pipe support of a steel frame structure, the heat pipe is fixed in the gasification tank through the heat pipe support, the sealing head of a metal cover body structure seals the heat pipe between the heat pipe built-in channel and the heat pipe, and the two interfaces of the heat pipe extend out of the sealing head.
Preferably, the connection parts between the sealing head and the heat pipe built-in channel and between the sealing head and the heat pipe are provided with high-temperature-resistant rubber ring seals, so that no gas or fluid leaks between the sealing head and the heat pipe built-in channel and between the sealing head and the heat pipe.
Preferably, the top end of the gasification tank is provided with two pipelines which are respectively a temperature gauge and a pressure gauge, the temperature gauge is arranged in the temperature gauge for measuring the temperature value in the gasification tank, and the pressure gauge is arranged in the pressure gauge for measuring the pressure value in the gasification tank.
Preferably, the top end of the gasification tank is provided with two pipelines which are respectively an oil inlet and an oil outlet, the oil inlet is used for injecting light hydrocarbon liquid, the oil outlet is used for discharging the light hydrocarbon liquid, the oil inlet and the oil outlet are provided with valves for controlling the on-off of the oil inlet and the oil outlet, and the lower end of the oil outlet is extended to the bottom of the gasification tank.
Preferably, the top of vaporizer is equipped with pipeline structure's intake pipe, and the intake pipe below extends to inside the vaporizer and is connected with a bubble generator in the bottom in the vaporizer.
Preferably, at least four groups of supports are arranged at the bottom outside the gasification tank to support the gasification tank in a balanced manner.
Preferably, the parallel pipe is a metal pipe body, and two or more groups of connectors for connecting the air outlet pipes are arranged on the parallel pipe.
Compared with the prior art, the beneficial effects of the utility model are that:
the maintenance and the removal are more convenient, the maintenance difficulty is low, and the installation cost is greatly reduced: through the establishment of the support: can utilize the support directly to place the gasifier subaerial, compare in the light hydrocarbon vaporization jar of pre-buried formula, it is more convenient to overhaul, and the later stage is removed also more conveniently, and the later stage maintenance degree of difficulty is low and installation cost reduces by a wide margin.
Prolonging the service life of the liquid level meter: because the level gauge is connected with the gasification jar below adoption communicating pipe, according to the U-shaped pipe principle, can appear in the level gauge with the highly unanimous liquid level of gasification jar light hydrocarbon liquid level, the compensating pipe is used for balancing the atmospheric pressure at level gauge and gasification jar top, further ensures that level gauge, gasification jar light hydrocarbon liquid level height are equal, because the level gauge is external, so the level gauge is in static protection state (the tympanic bulla does not get into the level gauge), prolongs the life of level gauge.
Potential safety hazards are reduced, the complex pipeline is reduced, and the pipeline cost is saved: when gas appliances need to be to the point gas transmission, can adopt the pipeline to directly link outlet duct and gas appliances on the drum kit, directly carry out the air feed by the drum kit to every gas appliances, the intensity pressure of main outlet duct has been alleviateed with traditional technique to the relative ratio, the potential safety hazard has been reduced, and each gas appliances air feed is even, and simultaneously, weld the gas-distributing pipe on main trachea for traditional technique, weld the bronchus pipeline again on the gas-distributing pipe, bronchus tube coupling gas appliances's technique, the complicated pipeline of mistake has been reduced, the pipeline cost is saved.
Fourthly, the air supply quantity of the single equipment can be flexibly combined and adjusted: when certain special gas appliances need to use a large amount of gas, the parallel pipes can be adopted to connect two or more than two gas blowing bags through the gas outlet pipes, and then the gas appliances are connected through the parallel pipes, so that the equipment needing a large amount of gas can obtain larger gas flux, and then larger gas consumption is obtained.
Drawings
Fig. 1 is a schematic diagram of the internal structure of an above-ground light hydrocarbon gasification tank capable of supplying gas to opposite points.
Fig. 2 is a schematic side view of an above-ground light hydrocarbon gasification tank capable of opposite point gas supply.
Fig. 3 is a schematic view of a connection structure of the overground parallel pipes capable of supplying air to the opposite points.
In the figure: 1. a gasification tank; 2. an air blowing bag; 3. an air outlet pipe; 4. a liquid level meter; 5. a heater; 6. connecting tubes in parallel; 7. a support; 8. a bubble generator; 9. an air inlet pipe; 10. a thermometer port; 11. a pressure gauge port; 12. an oil inlet; 13. an oil outlet; 41. a balance tube; 42. a communicating pipe; 51. a sealing head; 52. a channel is arranged in the heat pipe; 53. a heat pipe support; 54. a heat pipe.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments; based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts all belong to the protection scope of the present invention.
Referring to fig. 1 to 3, in an embodiment of the present invention, an above-ground light hydrocarbon gasification tank capable of supplying gas to a counter point includes: the device comprises a gasification tank 1, an air blowing bag 2, an air outlet pipe 3, a liquid level meter 4, a heater 5, a parallel pipe 6, a support 7, a bubble generator 8, an air inlet pipe 9, a temperature gauge port 10, a pressure gauge port 11, an oil inlet 12 and an oil outlet 13; the gasification tank 1 is a horizontal hollow tank body, a sealed vertical transparent pipe body is arranged on one side of the gasification tank 1 to form a liquid level meter 4, a pipe body forming balance pipe 41 and a communicating pipe 42 are respectively arranged on the upper part and the lower part of the liquid level meter 4, the balance pipe 41 and the communicating pipe 42 connect the liquid level meter 4 with the gasification tank 1 to enable the interior of the liquid level meter 4 to be communicated with the interior of the gasification tank 1, four groups or more than four groups of lower opening semi-closed tank bodies are arranged on the top of the gasification tank 1 to form an air blowing bag 2, the upper part of the air blowing bag 2 is processed in a round top shape, an opening on the lower part of the air blowing bag 2 is communicated with the interior of the gasification tank 1, and a pipeline connector is arranged on each air blowing bag 2 to form an air outlet pipe 3; the lower part of the heating gasification tank 1 is provided with a heater 5 for heating the internal space of the gasification tank 1, the heater 5 comprises a heat pipe built-in channel 52, and the heat pipe built-in channel 52 is a transverse cylindrical channel arranged below the gasification tank 1.
The heater 5 comprises a sealing head 51, a heat pipe built-in channel 52, a heat pipe support 53 and a heat pipe 54, wherein the heat pipe 54 is a transverse U-shaped pipeline, the heat pipe 54 is built in the gasification tank 1 through the heat pipe built-in channel 52 in a mode that two interfaces face outwards, the gasification tank 1 is provided with the heat pipe support 53 in a steel frame structure, the heat pipe 54 is fixed in the gasification tank 1 through the heat pipe support 53, the sealing head 51 in a metal cover body structure is used for sealing between the heat pipe built-in channel 52 and the heat pipe 54, and the two interfaces of the heat pipe 54 extend out of the sealing head 51.
The connection parts between the sealing head 51 and the heat pipe built-in channel 52 and between the sealing head 51 and the heat pipe 54 are provided with high-temperature resistant rubber ring seals, so that no gas or fluid is leaked between the sealing head 51 and the heat pipe built-in channel 52 and between the sealing head 51 and the heat pipe 54.
The top of the gasification tank 1 is provided with two pipelines which are respectively a temperature gauge port 10 and a pressure gauge port 11, a temperature gauge is arranged in the temperature gauge port 10 and used for measuring the temperature value in the gasification tank 1, and a pressure gauge is arranged in the pressure gauge port 11 and used for measuring the pressure value in the gasification tank 1.
The top end of the gasification tank 1 is provided with two pipelines which are respectively an oil inlet 12 and an oil outlet 13, the oil inlet 12 is used for injecting light hydrocarbon liquid, the oil outlet 13 is used for discharging the light hydrocarbon liquid, the oil inlet 12 and the oil outlet 13 are provided with valves for controlling the on-off of the oil inlet 12 and the oil outlet 13, and the lower end of the oil outlet 13 is extended to the bottom of the gasification tank 1.
The top of gasifier 1 is equipped with pipeline structure's intake pipe 9, and intake pipe 9 below extends to gasifier 1 inside and the bottom in gasifier 1 is connected with a bubble generator 8.
At least four groups of supports 7 are arranged at the bottom outside the gasification tank 1 to support the gasification tank 1 in a balanced manner.
The parallel pipe 6 is a metal pipe body, and is provided with more than two groups of interfaces for connecting the air outlet pipes 3.
The utility model discloses a theory of operation is:
when the device is used, the gasification tank 1 is placed on the ground by using the support 7, compared with a pre-embedded light hydrocarbon gasification tank, the device is more convenient to overhaul and move in the later period, the later maintenance difficulty is low, and the installation cost is greatly reduced, quantitative light hydrocarbon liquid is injected into the gasification tank 1 by using the oil inlet 12, valves on the oil inlet 12 and the oil outlet 13 are closed, because the liquid level meter 4 is connected with the lower part of the gasification tank 1 by using the communicating pipe 42, the liquid level in the liquid level meter 4 is consistent with the light hydrocarbon liquid level of the gasification tank 1 according to the principle of a U-shaped pipe, the balancing pipe 41 is used for balancing the air pressure at the top of the liquid level meter 4 and the gasification tank 1, the liquid level of the liquid level meter 4 and the light hydrocarbon liquid level of the gasification tank 1 are further guaranteed to be equal, and a heat source (generally hot water or hot oil) is conveyed into the heat pipe 5 by using one end interface of the overheating pipe 5 to heat the heat pipe 5 to heat the light hydrocarbon liquid in the gasification tank 1, the heat source for heating the light hydrocarbon liquid after being cooled is discharged from the interface at the other end of the heat pipe 5, and the circulation heating of the light hydrocarbon liquid is realized by repeating the steps; then the input air gets into from intake pipe 9 in the liquid light hydrocarbon bubble generator 8 bubbles in the liquid light hydrocarbon, forms a large amount of small-size bubbles, and the small-size bubble rises and floats out the liquid level, because there is heater 5 heat supply, the light hydrocarbon gasification that the bubble surface carried, and the small-size bubble is broken simultaneously, and wherein the air of parcel mixes with the light hydrocarbon of gasification and forms light hydrocarbon gas mixture and reach drum gas package 2 after the small-size bubble is broken.
When gas appliances need to carry out opposite-direction point gas transmission, the gas outlet pipe 3 on the gas blowing bag 2 and the gas appliances can be directly connected by adopting a pipeline, each gas appliance is directly supplied with gas by the gas blowing bag 2, the strength pressure of a main gas outlet pipe is reduced compared with the prior art, potential safety hazards are reduced, gas supplies of all the gas appliances are even, meanwhile, gas distributing pipes are welded on the main gas pipes, gas distributing pipes are welded on the gas distributing pipes, and the gas appliances are connected with the gas distributing pipes, so that complicated pipelines are reduced, and the pipeline cost is saved.
When certain special gas appliances need to use a large amount of gas, can adopt parallel pipe 6 to connect two and more than two air drum package 2 through outlet duct 3, and gas appliances are connected to rethread parallel pipe 6, and the equipment that needs a large amount of gas just so can obtain great gas flux, and then obtains great gas consumption, compares in traditional valve control formula's gas distribution equipment, and the gas is used more in a flexible way in combination, has saved the valve and has used, has saved a large amount of pipeline valve costs (bubble generator 8 does the utility model discloses a direct application omits its concrete structure for the commonly used technique in this field admittedly.
In the description of the present invention, it is to be understood that the terms "center", "longitudinal", "lateral", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", and the like, indicate orientations or positional relationships based on those shown in the drawings, and are only for convenience of description and simplicity of description, and do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore, should not be construed as limiting the present invention; furthermore, the terms "first", "second", etc. are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated; thus, a feature defined as "first," "second," etc. may explicitly or implicitly include one or more of that feature.
In the description of the present invention, "a plurality" means two or more unless otherwise specified.
In the description of the present invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements.
It will be evident to those skilled in the art that the invention is not limited to the details of the foregoing illustrative embodiments, and that the present invention may be embodied in other specific forms without departing from the spirit or essential attributes thereof; the present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein; any reference sign in a claim should not be construed as limiting the claim concerned.
Furthermore, it should be understood that although the present specification describes embodiments, not every embodiment includes only a single embodiment, and such description is for clarity purposes only, and it is to be understood that all embodiments may be combined as appropriate by one of ordinary skill in the art to form other embodiments as will be apparent to those of skill in the art from the description herein.
Claims (8)
1. An overground light hydrocarbon gasification tank capable of supplying gas to counter-point, comprising: the device comprises a gasification tank (1), an air blowing bag (2), an air outlet pipe (3), a liquid level meter (4), a heater (5), a parallel pipe (6), a support (7), a bubble generator (8), an air inlet pipe (9), a thermometer port (10), a pressure gauge port (11), an oil inlet (12) and an oil outlet (13); the method is characterized in that: the gasification tank (1) is a horizontal hollow tank body, a sealed vertical transparent pipe body is arranged on one side of the gasification tank (1) to form a liquid level meter (4), the upper part and the lower part of the liquid level meter (4) are respectively provided with a pipe body to form a balance pipe (41) and a communicating pipe (42), the balance pipe (41) and the communicating pipe (42) are used for connecting the liquid level meter (4) with the gasification tank (1) so that the interior of the liquid level meter (4) is communicated with the interior of the gasification tank (1), four groups or more than four groups of lower opening semi-closed tank bodies are arranged on the top of the gasification tank (1) to form air blowing bags (2), the upper parts of the air blowing bags (2) are subjected to dome treatment, openings on the lower parts of the air blowing bags (2) are communicated with the interior of the gasification tank (1), and each air blowing bag (2) is provided with a pipeline interface to form an air outlet pipe (3); the heater (5) used for heating the inner space of the gasification tank (1) is arranged at the lower part of the heating gasification tank (1), the heater (5) comprises a heat pipe built-in channel (52), and the heat pipe built-in channel (52) is a transverse cylindrical channel arranged below the gasification tank (1).
2. The above-ground light hydrocarbon gasification tank capable of being supplied with gas to counter-points according to claim 1, wherein: the heater (5) comprises a sealing head (51), a heat pipe built-in channel (52), a heat pipe support (53) and a heat pipe (54), wherein the heat pipe (54) is a transverse U-shaped pipeline, the heat pipe (54) is built in the gasification tank (1) through the heat pipe built-in channel (52) in a mode that two interfaces face outwards, the gasification tank (1) is provided with the heat pipe support (53) with a steel frame structure, the heat pipe (54) is fixed in the gasification tank (1) through the heat pipe support (53), the sealing head (51) with a metal cover body structure is sealed between the heat pipe built-in channel (52) and the heat pipe (54), and the two interfaces of the heat pipe (54) extend out of the sealing head (51).
3. The above-ground light hydrocarbon gasification tank capable of being supplied with gas to counter-points according to claim 1, wherein: high-temperature-resistant rubber ring seals are arranged at connecting parts between the sealing head (51) and the heat pipe built-in channel (52) and between the sealing head (51) and the heat pipe (54), so that no gas or fluid leaks between the sealing head (51) and the heat pipe built-in channel (52) and between the sealing head (51) and the heat pipe (54).
4. The above-ground light hydrocarbon gasification tank capable of being supplied with gas to counter-points according to claim 1, wherein: the top end of the gasification tank (1) is provided with two pipelines which are respectively a temperature gauge port (10) and a pressure gauge port (11), wherein a temperature gauge is arranged in the temperature gauge port (10), and a pressure gauge is arranged in the pressure gauge port (11).
5. The above-ground light hydrocarbon gasification tank capable of being supplied with gas to counter-points according to claim 1, wherein: the top end of the gasification tank (1) is provided with two pipelines which are respectively an oil inlet (12) and an oil outlet (13), the oil outlet (13) is provided with a valve for controlling the on-off of the oil inlet (12) and the oil outlet (13), and the lower end of the oil outlet (13) is extended to the bottom of the gasification tank (1).
6. The above-ground light hydrocarbon gasification tank capable of being supplied with gas to counter-points according to claim 1, wherein: the top of vaporizer (1) is equipped with pipeline structure's intake pipe (9), and intake pipe (9) below extends to vaporizer (1) inside and the bottom in vaporizer (1) is connected with a bubble generator (8).
7. The above-ground light hydrocarbon gasification tank capable of being supplied with gas to counter-points according to claim 1, wherein: the bottom outside the gasification tank (1) is provided with at least four groups of supports (7) for supporting the gasification tank (1) in a balanced manner.
8. The above-ground light hydrocarbon gasification tank capable of being supplied with gas to counter-points according to claim 1, wherein: the parallel pipe (6) is a metal pipe body, and is provided with more than two groups of connectors for connecting the air outlet pipes (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220934783.0U CN217235281U (en) | 2022-04-21 | 2022-04-21 | Ground light hydrocarbon gasification tank capable of opposite point-to-point gas supply |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220934783.0U CN217235281U (en) | 2022-04-21 | 2022-04-21 | Ground light hydrocarbon gasification tank capable of opposite point-to-point gas supply |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217235281U true CN217235281U (en) | 2022-08-19 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202220934783.0U Active CN217235281U (en) | 2022-04-21 | 2022-04-21 | Ground light hydrocarbon gasification tank capable of opposite point-to-point gas supply |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN217235281U (en) |
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2022
- 2022-04-21 CN CN202220934783.0U patent/CN217235281U/en active Active
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