CN209759400U - natural gas purification and impurity removal mechanism - Google Patents
natural gas purification and impurity removal mechanism Download PDFInfo
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- CN209759400U CN209759400U CN201920270091.9U CN201920270091U CN209759400U CN 209759400 U CN209759400 U CN 209759400U CN 201920270091 U CN201920270091 U CN 201920270091U CN 209759400 U CN209759400 U CN 209759400U
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Abstract
The utility model discloses a natural gas purification and impurity removal mechanism, which comprises a coarse purification component, a humidification component and a desulfurizer; the thick purification subassembly is arranged in purifying the filtration with the large granule impurity in the natural gas, thick purification subassembly and humidification subassembly intercommunication, the humidification subassembly includes first box, the water tank, nozzle and fan, the cavity has in the first box, the water tank sets up the one side at first box, the nozzle is connected with the water tank, the nozzle is used for spouting into the first box with the vapor state with the water in the water tank in, the fan setting is just to the nozzle in one side of nozzle and the fan sector, the desulfurizer is connected with the humidification subassembly, the desulfurizer is used for carrying out desulfurization treatment to the natural gas through the humidification. The utility model discloses a coarse filter subassembly carries out filtration treatment with the large granule impurity in the natural gas, makes the natural gas mix with vapor through the humidification subassembly afterwards, and desulfurization efficiency is higher when desulfurization treatment with vapor mixed natural gas, and vapor can promote the reaction efficiency of the desulfurization catalyst in the disconnector.
Description
Technical Field
The utility model belongs to the technical field of the natural gas treatment, concretely relates to natural gas purifies edulcoration mechanism.
Background
Natural gas is trapped in underground porous rock formations, including oil field gas, gas field gas, coal bed gas, mud volcanic gas, biogenic gas, and the like, and a small amount of natural gas is also released from the coal bed. It is a high-quality fuel and chemical raw material.
the natural gas is mainly used as fuel, can be used for producing carbon black, chemicals and liquefied petroleum gas, and the propane and butane produced by the natural gas are important raw materials of modern industry. Natural gas is composed mainly of gaseous low molecular hydrocarbons mixed with non-hydrocarbon gases.
The natural gas collected from underground contains many impurities and sulfide harmful substances, and the natural gas without being filtered and purified has low combustion efficiency and produces sulfide harmful to the environment.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide a: the utility model provides a natural gas purifies edulcoration mechanism to solve current natural gas filter equipment desulfurization effect not ideal, the filter effect is coarse, remains the problem of impurity easily.
in order to realize the purpose, the utility model discloses a technical scheme be: the natural gas purification and impurity removal mechanism comprises a rough purification component, a humidification component and a desulfurizer; the coarse purification component is used for purifying and filtering large-particle impurities in natural gas, the coarse purification component is communicated with the humidification component, the humidification component comprises a first box body, a water tank, a nozzle and a fan, a cavity is formed in the first box body, the water tank is arranged on one side of the first box body, the nozzle is connected with the water tank, the nozzle is used for spraying water in the water tank into the first box body in a steam state, the fan is arranged on one side of the nozzle, the sector of the fan is right opposite to the nozzle, the desulfurizer is connected with the humidification component, and the desulfurizer is used for conducting desulfurization treatment on the humidified natural gas.
Further, thick purification unit spare includes second box, left baffle and right baffle, the second box be provided with be used for making the natural gas get into the air inlet with be used for with the gas outlet of humidification subassembly intercommunication, left side baffle and right baffle are in crisscross setting from top to bottom in the second box, first end and second end have in the second box, the one end of left side baffle with first end connection, the other end of left side baffle to second end extend and left baffle with second end has the clearance, the one end of right side baffle with second end connection, the other end of right side baffle to first end extend and right baffle with first end has the clearance, press from both sides between left side baffle and the right baffle and be equipped with the active carbon unit check.
Further, have water storage chamber and steam chamber in the water tank, the water storage chamber through first heater with the steam chamber intercommunication, the steam chamber with the nozzle passes through the force pump intercommunication.
Furthermore, a second heater is arranged in the first box body, and the second heater is used for increasing the temperature in the first box body.
Further, the fan has a plurality ofly, and is a plurality of the fan is in the first box sets up from top to bottom in succession, the nozzle also has a plurality ofly, and is a plurality of the nozzle one-to-one is a plurality of the fan.
Further, the desulfurizer is connected with dry subassembly, dry subassembly includes third box, condensation plate and drying plate, the third box with the desulfurizer intercommunication, the condensation plate sets up in the third box, the surface of condensation plate is provided with the through-hole that makes the natural gas pass through, the condensation plate is hollow structure and condensation plate and is connected with the vortex tube, the drying plate also sets up in the third box and be provided with the drier in the drying plate.
Since the technical scheme is used, the beneficial effects of the utility model are that:
The utility model discloses a coarse filter subassembly carries out filtration treatment with the large granule impurity in the natural gas, makes the natural gas mix with vapor through the humidification subassembly afterwards, and desulfurization efficiency is higher when desulfurization treatment with vapor mixed natural gas, and vapor can promote the reaction efficiency of the desulfurization catalyst in the disconnector, the utility model discloses can carry out abundant desulfurization treatment with the natural gas, prevent to remain in the natural gas and contain the sulphur thing and generate the sulphide polluted environment in the burning.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings that are required to be used in the embodiments will be briefly described below, it should be understood that the following drawings only illustrate some embodiments of the present invention, and therefore should not be considered as limiting the scope, and for those skilled in the art, other related drawings can be obtained according to the drawings without inventive efforts.
FIG. 1 is a schematic view of the present invention;
Fig. 2 is a schematic view of the water tank of the present invention.
Reference numerals: 1-coarse purification component, 110-second box body, 120-left baffle plate, 130-right baffle plate, 140-air inlet, 150-air outlet, 160-active carbon unit cell, 2-humidification component, 210-first box body, 220-water tank, 221-water storage cavity, 222-steam cavity, 223-first heater, 224-pressure pump, 230-nozzle, 240-fan, 250-second heater, 3-desulfurizer, 4-drying component, 410-third box body, 420-condensing plate, 430-drying plate and 5-vortex tube.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are some, but not all, embodiments of the present invention. The components of embodiments of the present invention, as generally described and illustrated in the figures herein, may be arranged and designed in a wide variety of different configurations.
Thus, the following detailed description of the embodiments of the present invention, presented in the accompanying drawings, is not intended to limit the scope of the invention, as claimed, but is merely representative of selected embodiments of the invention. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts belong to the protection scope of the present invention.
It should be noted that: like reference numbers and letters refer to like items in the following figures, and thus, once an item is defined in one figure, it need not be further defined and explained in subsequent figures.
In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", and the like indicate the position or positional relationship based on the position or positional relationship shown in the drawings, or the position or positional relationship which is usually placed when the product of the present invention is used, and are only for convenience of description and simplification of the description, but do not indicate or imply that the device or element referred to must have a specific position, be constructed and operated in a specific orientation, and thus, should not be construed as limiting the present invention.
The terms "first," "second," "third," and the like are used solely to distinguish one from another and are not to be construed as indicating or implying relative importance.
The terms "parallel", "perpendicular", etc. do not require that the components be absolutely parallel or perpendicular, but may be slightly inclined. For example, "parallel" merely means that the directions are more parallel relative to "perpendicular," and does not mean that the structures are necessarily perfectly parallel, but may be slightly tilted.
The terms "horizontal", "vertical", "overhang" and the like do not imply that the components are required to be absolutely horizontal or overhang, but may be slightly inclined. For example, "horizontal" merely means that the direction is more horizontal than "vertical" and does not mean that the structure must be perfectly horizontal, but may be slightly inclined.
Furthermore, the terms "substantially", and the like are intended to indicate that the relative terms are not necessarily strictly required, but may have some deviation. For example: "substantially equal" does not mean absolute equality, but it is difficult to achieve absolute equality in actual production and operation, and some deviation generally exists. Thus, in addition to absolute equality, "substantially equal" also includes the above-described case where there is some deviation. In this case, unless otherwise specified, terms such as "substantially", and the like are used in a similar manner to those described above.
In the description of the present invention, it should also be noted that, unless otherwise explicitly specified or limited, the terms "disposed," "mounted," "connected," and "connected" are to be construed broadly, e.g., as meaning either a fixed connection, a removable connection, or an integral connection; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.
The utility model provides a natural gas purification and impurity removal mechanism, as shown in figure 1, comprising a coarse purification component 1, a humidification component 2 and a desulfurizer 3; the collected natural gas for purification and filtration contains a large amount of impurities, such as large-particle impurities, such as paraffin, the rough purification assembly 1 is used for purifying and filtering the large-particle impurities in the natural gas, the rough purification assembly 1 is communicated with the humidification assembly 2, the humidification assembly 2 comprises a first box 210, a water tank 220, a nozzle 230 and a fan 240, a cavity is formed in the first box 210, the water tank 220 is arranged on one side of the first box 210, the nozzle 230 is connected with the water tank 220, the nozzle 230 is used for spraying water in the water tank 220 into the first box 210 in a water vapor state, the fan 240 is arranged on one side of the nozzle 230, a fan face of the fan 240 faces the nozzle 230, the natural gas filtered by the rough purification assembly 1 does not contain large-particle impurities, such as paraffin, and the natural gas is sucked to one side of the fan 240 by the fan 240 after entering the first box 210, meanwhile, the steam sprayed in through the nozzle 230 is sucked to one side of the fan 240 by the fan 240, the natural gas and the steam are blown to one side of the fan 240 continuously, the natural gas and the steam can be fully mixed at one side of the fan 240, the desulfurizer 3 is connected with the humidifying assembly 2, the desulfurizer 3 is used for performing desulfurization treatment on the humidified natural gas, and the steam can improve the catalytic efficiency of the catalyst when the natural gas mixed with the steam is subjected to desulfurization treatment.
Preferably, the rough purification assembly 1 includes a second box 110, a left partition 120 and a right partition 130, the second box 110 is provided with an air inlet 140 for natural gas to enter and an air outlet 150 for communicating with the humidification assembly 2, the left partition 120 and the right partition 130 are staggered from top to bottom in the second box 110, the second box 110 has a first end and a second end, one end of the left partition 120 is connected to the first end, the other end of the left partition 120 extends towards the second end with a gap between the left partition 120 and the second end, one end of the right partition 130 is connected to the second end, the other end of the right partition 130 extends towards the first end with a gap between the right partition 130 and the first end, the left partition 120 and the right partition 130 form a labyrinth passage in the second box 110, the activated carbon unit cell 160 is clamped between the adjacent left partition plate 120 and the right partition plate 130, activated carbon is arranged in the activated carbon unit cell 160 and used for absorbing large-particle impurities in natural gas, and the path of the natural gas passing through the second box body 110 is farther due to the labyrinth passage, so that the natural gas is more sufficiently filtered.
Preferably, the water tank 220 has a water storage cavity 221 and a steam cavity 222 therein, the water storage cavity 221 is communicated with the steam cavity 222 through a first heater 223, the steam cavity 222 is communicated with the nozzle 230 through a pressure pump 224, water is stored in the water storage cavity 221, the first heater 223 can heat the water in the water storage cavity 221 into steam and discharge the steam into the steam cavity 222, the pressure pump 224 can pump the steam in the steam cavity 222 into the nozzle 230 and spray the steam into the first tank 210, and an electromagnetic valve can be disposed between the water storage cavity 221 and the first heater 223 for controlling the amount of the generated steam.
Preferably, a second heater 250 is disposed in the first tank 210, and the second heater 250 is used for raising the temperature in the first tank 210, and after the water vapor is sprayed into the first tank 210 from the nozzle 230, if the temperature in the first tank 210 is low, the water vapor is liquefied into small water drops when it is cooled, so that the water vapor can be kept in a steam state by preheating the interior of the first tank 210 by the second heater 250.
Preferably, there are a plurality of the fans 240, the fans 240 are continuously arranged in the first box 210 from top to bottom, the nozzles 230 are also a plurality of, the nozzles 230 are one-to-one corresponding to the fans 240, and the fans 240 are arranged to improve the mixing efficiency of the water vapor and the natural gas.
Preferably, the desulfurizer 3 is connected with a drying assembly 4, the drying assembly 4 comprises a third box 410, a condensing plate 420 and a drying plate 430, the third box 410 is communicated with the desulfurizer 3, the natural gas desulfurized by the desulfurizer 3 is mixed with water vapor, so that water is necessarily remained in the natural gas, the water may still exist in the form of water vapor or exist in the form of liquid mist, the condensing plate 420 is arranged in the third box 410, a through hole for passing the natural gas is arranged on the surface of the condensing plate 420, the condensing plate 420 is of a hollow structure, the condensing plate 420 is connected with a vortex tube 5, the vortex tube 5 can output cold air, the vortex tube 5 is communicated with the condensing plate 420 and can input the cold air into the inside of the condensing plate 420, so as to reduce the temperature of the condensing plate 420, when the natural gas passes through the condensing plate 420, the water vapor in the natural gas can be cooled and liquefied into water by contacting with the condensing plate 420, therefore, the separation of water vapor is realized, the drying plate 430 is also arranged in the third box body 410, the drying agent is arranged in the drying plate 430, and the natural gas passing through the condensing plate 420 may be mixed with foggy liquid water, so that the natural gas can absorb the foggy liquefied water after passing through the drying plate 430, thereby realizing the effect of drying the natural gas.
The utility model discloses a theory of operation:
The utility model discloses a coarse filter subassembly carries out filtration treatment with the large granule impurity in the natural gas, makes the natural gas mix with vapor through the humidification subassembly afterwards, and desulfurization efficiency is higher when desulfurization treatment with vapor mixed natural gas, and vapor can promote the reaction efficiency of the desulfurization catalyst in the disconnector, the utility model discloses can carry out abundant desulfurization treatment with the natural gas, prevent to remain in the natural gas and contain the sulphur thing and generate the sulphide polluted environment in the burning.
Claims (6)
1. The utility model provides a natural gas purifies edulcoration mechanism which characterized in that: comprises a coarse purification component, a humidification component and a desulfurizer; the coarse purification component is used for purifying and filtering large-particle impurities in natural gas, the coarse purification component is communicated with the humidification component, the humidification component comprises a first box body, a water tank, a nozzle and a fan, a cavity is formed in the first box body, the water tank is arranged on one side of the first box body, the nozzle is connected with the water tank, the nozzle is used for spraying water in the water tank into the first box body in a steam state, the fan is arranged on one side of the nozzle, the sector of the fan is right opposite to the nozzle, the desulfurizer is connected with the humidification component, and the desulfurizer is used for conducting desulfurization treatment on the humidified natural gas.
2. The natural gas purification and impurity removal mechanism according to claim 1, wherein: the thick purification unit spare includes second box, left baffle and right baffle, the second box be provided with be used for making the natural gas get into the air inlet and be used for with the gas outlet of humidification subassembly intercommunication, left side baffle and right baffle are in crisscross setting from top to bottom in the second box, first end and second end have in the second box, the one end of left side baffle with first end connection, the other end of left side baffle to second end extend and left baffle with second end has the clearance, the one end of right baffle with second end connection, the other end of right baffle to first end extend and right baffle with first end has the clearance, press from both sides between left side baffle and the right baffle and be equipped with the active carbon unit check.
3. The natural gas purification and impurity removal mechanism according to claim 1, wherein: the water storage device is characterized in that a water storage cavity and a steam cavity are arranged in the water tank, the water storage cavity is communicated with the steam cavity through a first heater, and the steam cavity is communicated with the nozzle through a pressure pump.
4. The natural gas purification and impurity removal mechanism according to claim 1, wherein: and a second heater is arranged in the first box body and used for increasing the temperature in the first box body.
5. The natural gas purification and impurity removal mechanism according to claim 1, wherein: the fan has a plurality ofly, and is a plurality of the fan is in from top to bottom sets up in succession in the first box, the nozzle also has a plurality ofly, and is a plurality of the nozzle one-to-one is a plurality of the fan.
6. The natural gas purification and impurity removal mechanism according to claim 1, wherein: the desulfurizer is connected with dry subassembly, dry subassembly includes third box, condensation plate and drying plate, the third box with the desulfurizer intercommunication, the condensation plate sets up in the third box, the surface of condensation plate is provided with the through-hole that makes the natural gas pass through, the condensation plate is hollow structure and condensation plate and is connected with the vortex tube, the drying plate also sets up in the third box and be provided with the drier in the drying plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920270091.9U CN209759400U (en) | 2019-03-04 | 2019-03-04 | natural gas purification and impurity removal mechanism |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920270091.9U CN209759400U (en) | 2019-03-04 | 2019-03-04 | natural gas purification and impurity removal mechanism |
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| CN209759400U true CN209759400U (en) | 2019-12-10 |
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| CN201920270091.9U Active CN209759400U (en) | 2019-03-04 | 2019-03-04 | natural gas purification and impurity removal mechanism |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115477966A (en) * | 2022-07-18 | 2022-12-16 | 四川绵竹川润化工有限公司 | Method for removing organic sulfur in natural gas |
| CN115554842A (en) * | 2022-09-28 | 2023-01-03 | 安徽医科大学 | Air quality detection purifier |
| CN116272199A (en) * | 2023-02-27 | 2023-06-23 | 北京建筑大学 | Multilayer treatment type atmosphere treatment equipment based on environmental treatment |
-
2019
- 2019-03-04 CN CN201920270091.9U patent/CN209759400U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115477966A (en) * | 2022-07-18 | 2022-12-16 | 四川绵竹川润化工有限公司 | Method for removing organic sulfur in natural gas |
| CN115554842A (en) * | 2022-09-28 | 2023-01-03 | 安徽医科大学 | Air quality detection purifier |
| CN116272199A (en) * | 2023-02-27 | 2023-06-23 | 北京建筑大学 | Multilayer treatment type atmosphere treatment equipment based on environmental treatment |
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