CN210656834U - Wellhead gas source purifier - Google Patents
Wellhead gas source purifier Download PDFInfo
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- CN210656834U CN210656834U CN201921393815.5U CN201921393815U CN210656834U CN 210656834 U CN210656834 U CN 210656834U CN 201921393815 U CN201921393815 U CN 201921393815U CN 210656834 U CN210656834 U CN 210656834U
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- desulfurization
- dust removal
- dehydration
- pipe
- gas
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Abstract
The utility model relates to a well head air supply clarifier. The technical scheme is as follows: including air supply import, whirl dehydration pipe, desulfurization dust removal pipe, purification gas export and bottom plate seat, wherein, whirl dehydration pipe and desulfurization dust removal pipe are installed on the bottom plate seat, the latter half of whirl dehydration pipe is equipped with the air supply import, and the top of whirl dehydration pipe is equipped with the purification gas export, and the inner chamber of whirl dehydration pipe is equipped with the condensation cap, the downside of whirl dehydration pipe is connected to the desulfurization air inlet of two or more desulfurization dust removal pipes through the dehydration gas export, and desulfurization dust removal pipe inner chamber is equipped with telescopic filter screen, the top of desulfurization dust removal pipe is connected to the purification gas storage chamber at the top of whirl dehydration pipe through the desulfurization gas outlet to discharge through the purification gas export. The beneficial effects are that: the utility model discloses collect desulfurization, dehumidification, dust removal as an organic whole, it is multiple functional, small, simple structure, easily installation has realized sleeve pipe natural gas desulfurization, dehydration, dust removal purification on oil field individual well.
Description
Technical Field
The utility model relates to a special device and a method for oil field desulfurization, dehydration and purification, in particular to a wellhead air source purifier.
Background
At present, the fuel for heating the heating furnace or the oil storage tank at the well site of the oil field is mostly oil well casing natural gas (i.e. unprocessed natural moisture), contains a small amount of water vapor and trace hydrogen sulfide (H)2S), generating sulfur dioxide after hydrogen sulfide is combusted, and corroding a flue chimney; the water content of the natural gas can cause incomplete combustion, increase the blackness of smoke dust, and cause the environmental protection not to reach the standard, thereby influencing the health of people. The natural moisture of the sleeve is uniformly and intensively treated and then used, no matter a pipe network is laid or transported, the investment is not small, and the environmental protection requirement is not moderate. In addition, the existing desulfurization equipment has large volume, adopts the standard of a pressure vessel for design and management, and is troublesome to install, annual check and manage; due to the objective conditions of the well site, the method is difficult to realize in practice in consideration of economy.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a well head air source clarifier that is suitable for and uses on the single well, and is small to the above-mentioned defect that prior art exists, both can give the natural gas desulfurization, again can dry the dehydration.
The utility model provides a well head air supply clarifier, its technical scheme is: comprises an air source inlet (1), one or more rotational flow dehydration tubes (2), two or more desulfurization and dust removal tubes (6), a purified gas outlet (10) and a base plate seat (11), wherein the rotational flow dehydration tubes (2) and the desulfurization and dust removal tubes (6) are arranged on the base plate seat (11), the lower half part of the rotational flow dehydration tubes (2) is provided with the air source inlet (1), the top part of the rotational flow dehydration tubes (2) is provided with the purified gas outlet (10), the inner cavity of the rotational flow dehydration tubes (2) is provided with a water condensation cap, the lower side of the rotational flow dehydration tubes (2) is connected to the desulfurization air inlets (5) of the two or more desulfurization and dust removal tubes (6) through a dehydration gas outlet (4), the inner cavity of the desulfurization and dust removal tubes (6) is provided with a sleeve type filter screen, the top parts of the desulfurization and dust removal tubes (6) are connected to the purified gas storage cavity at the top parts of the rotational flow dehydration tubes, and is discharged through a purge gas outlet (10).
Preferably, the rotational flow dehydration tube (2) comprises a tube body (2.1), a dehydration gas guide tube (2.2), a purified gas storage cavity (2.3), a blocking plate (2.4), a water condensation cap (2.5), a partition plate (2.6) and a seal head (2.7), wherein the blocking plate (2.4) is arranged at the bottom of the tube body (2.1), the seal head (2.7) is arranged at the top of the tube body, the partition plate (2.6) is arranged below the seal head (2.7), a purified gas storage cavity (2.3) is formed between the partition plate (2.6) and the seal head (2.7), and a purified gas inlet (9) and a purified gas outlet (10) are arranged at the outer side of the purified gas storage cavity (2.3); a dehydrated air conduit (2.2) and a plurality of condensed water caps (2.5) are arranged below the clapboard (2.6), and a first sewage discharge port (3) is arranged at the lower side of the pipe body (2.1).
Preferably, the dehydrated gas conduit (2.2) is arranged in the inner cavity of the pipe body (2.1), is positioned below the partition plate (2.6), passes through the centers of the plurality of water condensation caps (2.5), and the bottom of the dehydrated gas conduit (2.2) is communicated with the desulfurization and dust removal pipe (6) through the dehydrated gas outlet (4).
Preferably, the dehydrated gas conduit (2.2) is arranged outside the pipe body (2.1), the upper end of the dehydrated gas conduit (2.2) is connected to the lower position of the partition plate (2.6) in the pipe body (2.1), and the lower end of the dehydrated gas conduit (2.2) is communicated with the desulfurization and dust removal pipe (6).
Preferably, the desulfurization and dust removal pipe (6) comprises a desulfurization and dust removal pipe body (6.1), a sleeve type filter screen (6.2), a transverse bracket (6.3), a second blocking plate (6.4), a second partition plate (6.5), a charging hole (6.6) and a discharge hole (6.8), the top of the desulfurization dust removal pipe body (6.1) is connected with a charging hole flange blind plate (13), a second partition plate (6.5) is arranged below the charging hole flange blind plate (13), a charging hole (6.6) is arranged at the lower side of the second partition plate (6.5), a sleeve type filter screen (6.2) and a cross bracket (6.3) are arranged in the inner cavity at the lower side of the desulfurization dust removal pipe body (6.1), the sleeve type filter screen (6.2) is arranged on the upper surface of the cross bracket (6.3), a desulfurization air inlet (5) is arranged below the transverse support (6.3), a second sewage draining outlet (14) and a second blocking plate (6.4) are arranged below the desulfurization air inlet (5), and a discharge outlet (6.8) is arranged at the outer side of the sleeve type filter screen (6.2).
Preferably, the top of the desulfurization and dust removal pipe (6) is connected to a purified gas inlet (9) at the top of the rotational flow dehydration pipe (2) through a desulfurization gas outlet (7).
Preferably, the rotational flow dehydration pipe (2) is one, the desulfurization and dust removal pipes (6) are in multiple groups, and the multiple groups of desulfurization and dust removal pipes (6) are in vertical layout.
Preferably, the rotational flow dehydration pipe (2) is one, the desulfurization and dust removal pipes (6) are in multiple groups, and the multiple groups of desulfurization and dust removal pipes (6) are in horizontal layout.
Preferably, the rotational flow dehydration pipe (2) is one, the desulfurization and dust removal pipes (6) are in a plurality of groups, and the desulfurization and dust removal pipes (6) are in a circular vertical layout.
The utility model provides a method for using of well head air supply clarifier, including following process:
the natural gas of the well mouth sleeve enters the rotational flow dehydration pipe (2) through the internal cutting of the gas source inlet (1) and rises in a spiral shape, and the water in the natural gas is attached to the inner wall of the pipe under the action of centrifugal force and is condensed into water drops which flow to the bottom of the pipe; meanwhile, the ascending natural gas collides with a water condensation cap (2.5) to further separate out floating free water, and the floating free water is condensed into water drops to sink to the bottom of the pipe; condensed water at the bottom of the pipe can be discharged through the first sewage outlet (3) periodically; the dehydrated natural gas which rises to the top downwards leaves the cyclone dehydration pipe (2) from a dehydrated gas outlet through a dehydrated gas guide pipe (2.2), and then enters the bottom of the desulfurization dust removal pipe (6) through a desulfurization gas inlet (5); the natural gas continues upwards in the desulfurization dust removal pipe, and through telescopic filter screen (6.2), the hydrogen sulfide composition in the natural gas reacts with the desulfurization agent in telescopic filter screen (6.2), and the natural gas after desulfurization finally leaves from desulfurization gas outlet (4), and top purification gas storage chamber (2.3) in getting into whirl dehydration pipe (2) shell through series connection valve (8), purification gas import (9), and the rethread purification gas export (10) is defeated outward and is used.
The utility model has the advantages that: the utility model integrates the functions of desulfurization, dehumidification and dust removal, has complete functions, small volume, simple structure and easy installation, and realizes the desulfurization, dehydration and dust removal purification of sleeve natural gas on a single well of an oil field; the equipment is safe and stable due to the tubular structure (DN is less than or equal to 150mm) and miniaturization, and does not need registration and annual inspection during installation and use; in addition, because the equipment is modularized, the number (power size) can be increased or decreased freely according to needs, and the layout can be combined freely according to needs; because of the tubular structure, the flow path is small, the natural gas can fully contact with the desulfurizer without dead angles, the utilization rate is high, the desulfurization is thorough, and the fine desulfurization level (H) can be achieved2S﹤10PPm）。
Drawings
FIG. 1 is a schematic structural diagram of the present invention;
fig. 2 is a top view of the present invention;
FIG. 3 is a schematic structural view of a cyclone dewatering tube;
FIG. 4 is a top view of the spin-drying tube;
FIG. 5 is another schematic diagram of the structure of the spin-drying tube;
FIG. 6 is a schematic structural view of a desulfurization dust removal pipe;
FIG. 7 is another schematic diagram of the desulfurization dust removal pipe;
fig. 8 is a schematic horizontal structure diagram of embodiment 3 of the present invention;
fig. 9 is a schematic view of embodiment 3 of the present invention from direction a;
fig. 10 is a schematic view of embodiment 3 of the present invention in the direction of B;
fig. 11 is a top view of a circular layout of embodiment 4 of the present invention;
fig. 12 is a top view of a square layout of embodiment 5 of the present invention;
in the upper diagram: an air source inlet 1, a rotational flow dehydration pipe 2, a first sewage discharge port 3, a dehydrated gas outlet 4, a desulfurization air inlet 5, a desulfurization dust removal pipe 6, a desulfurization air outlet 7, a series valve 8, a purified gas inlet 9, a purified gas outlet 10, a bottom plate seat 11, a pressure measuring port 12, a charging port flange blind plate 13, a second sewage discharge port 14, a dehydrated gas manifold 15 and a purified gas manifold 16,
the device comprises a pipe body 2.1, a dehydrated gas guide pipe 2.2, a purified gas storage cavity 2.3, a blocking plate 2.4, a water condensation cap 2.5, a partition plate 2.6 and a seal head 2.7, and further comprises a desulfurization and dust removal pipe body 6.1, a sleeve type filter screen 6.2, a cross bracket 6.3, a second blocking plate 6.4, a second partition plate 6.5, a charging hole 6.6, a second seal head 6.7 and a discharge hole 6.8.
Detailed Description
The preferred embodiments of the present invention will be described in conjunction with the accompanying drawings, and it will be understood that they are presented herein only to illustrate and explain the present invention, and not to limit the present invention.
Referring to the attached drawings 3-4, the rotational flow dehydration tube 2 comprises a tube body 2.1, a dehydration gas guide tube 2.2, a purified gas storage cavity 2.3, a blocking plate 2.4, a water condensation cap 2.5, a partition plate 2.6 and an end enclosure 2.7, wherein the blocking plate 2.4 is arranged at the bottom of the tube body 2.1, the end enclosure 2.7 is arranged at the top of the tube body, the partition plate 2.6 is arranged below the end enclosure 2.7, so that the purified gas storage cavity 2.3 is formed between the partition plate 2.6 and the end enclosure 2.7, and a purified gas inlet 9 and a purified gas outlet 10 are arranged outside the purified gas storage cavity 2.3; a dehydrated air conduit 2.2 and a plurality of water condensation caps 2.5 are arranged below the clapboard 2.6, and a first sewage discharge port 3 is arranged at the lower side of the pipe body 2.1.
Wherein, congeal the water cap and can adopt umbrella-type structure, in addition, whirl dehydration pipe 2 can also realize in step that wet flue gas desulfurization is supplementary (specifically to the intraductal injection liquid desulfurizer of whirl dehydration, just so can realize wet flue gas desulfurization when the dehydration), like this, this scheme can cooperate subsequent dry process desulfurization dust removal pipe to realize going on simultaneously dry and wet flue gas desulfurization, makes desulfurization effect better.
Wherein, dehydration gas pipe 2.2 installs the inner chamber at pipe body 2.1, is located the below of baffle 2.6, and passes a plurality of water condensation caps 2.5's center, and dehydration gas pipe 2.2's bottom communicates desulfurization dust removal pipe 6 through dehydration gas outlet 4, from the user's angle, exposes an air supply import and purified gas export, does not have too many pipelines, during the use, and is simple and clear, is difficult to the working error that appears.
Referring to the attached drawing 6, the desulfurization and dust removal pipe 6 comprises a desulfurization and dust removal pipe body 6.1, a sleeve type filter screen 6.2, a cross support 6.3, a second blocking plate 6.4, a second partition plate 6.5, a charging hole 6.6 and a discharge hole 6.8, the top of the desulfurization and dust removal pipe body 6.1 is connected with a charging hole flange blind plate 13, the second partition plate 6.5 is arranged below the charging hole flange blind plate 13, the charging hole 6.6 is arranged below the second partition plate 6.5, the sleeve type filter screen 6.2 and the cross support 6.3 are arranged in an inner cavity at the lower side of the desulfurization and dust removal pipe body 6.1, the sleeve type filter screen 6.2 is arranged on the upper surface of the cross support 6.3, a desulfurization air inlet 5 is arranged below the cross support 6.3, a second sewage discharge outlet 14 and the second blocking plate 6.4 are arranged below the desulfurization air inlet 5, and the discharge hole 6.8 is arranged at the.
Preferably, the top of the desulfurization dust removal pipe 6 is connected to a purified gas inlet 9 at the top of the cyclone dehydration pipe 2 through a desulfurization gas outlet 7.
The utility model provides a method for using of well head air supply clarifier, including following process:
the natural gas of the well head sleeve enters the rotational flow dehydration pipe 2 through the internal cutting of the gas source inlet 1 and rises spirally, and the water in the natural gas is attached to the inner wall of the pipe under the action of centrifugal force and is condensed into water drops which sink to the bottom of the pipe; meanwhile, the rising natural gas collides with the water condensation cap 2.5, and further the floating free water is separated out and condensed into water drops to sink to the bottom of the pipe; condensed water at the bottom of the pipe can be discharged through the first sewage outlet 3 periodically; the dehydrated natural gas which rises to the top downwards leaves the rotational flow dehydration pipe 2 from the dehydrated gas outlet through the dehydrated gas guide pipe 2.2 and then enters the bottom of the desulfurization dust removal pipe 6 through the desulfurization gas inlet 5; the natural gas continues upwards in the desulfurization dust removal pipe, the natural gas passes through the sleeve type filter screen 6.2, hydrogen sulfide in the natural gas reacts with the desulfurization agent in the sleeve type filter screen 6.2, the desulfurized natural gas finally leaves from the desulfurization gas outlet 4, enters the top purified gas storage cavity 2.3 in the shell of the rotational flow dehydration pipe 2 through the serial valve 8 and the purified gas inlet 9, and is output and applied through the purified gas outlet 10.
the dehydration gas conduit 2.2 can also be arranged at the outer side of the pipe body 2.1, the upper end of the dehydration gas conduit 2.2 is connected at the lower position of the clapboard 2.6 in the pipe body 2.1, the lower end of the dehydration gas conduit 2.2 is communicated with the desulfurization dust removal pipe 6, but the structure is that the whole device is slightly messy, one more exposed pipeline is arranged, the structure is simpler than that of the embodiment 1, from the viewpoint of the user, the device is exposed with an air source inlet and a purified gas outlet, and the dehydration gas conduit 2.2 is also arranged, but from the whole function, the two are the same, and the field requirement can be met.
the utility model discloses a whirl dehydration pipe 2 adopts one, and for vertical structure, desulfurization dust removal pipe 6 adopts many, and many desulfurization dust removal pipe 6 adopts horizontal overall arrangement to through the 15 intercommunication one ends of dehydration manifold, the other end is through purifying 16 intercommunications of gas manifolds.
Referring to the attached drawings 8-10, the cyclone dewatering pipe 2 adopts one, the desulfurization dust removal pipe 6 adopts 8 as an example, and the concrete structure is as follows:
the bottom of the rotational flow dehydration pipe 2 is arranged on the bottom plate seat 11, and the desulfurization and dust removal pipes 6 are arranged in a group in pairs and are horizontally arranged in sequence, so that four desulfurization and dust removal pipes 6 are respectively arranged on two sides of the rotational flow dehydration pipe 2; the latter half of whirl dehydration pipe 2 is equipped with air supply import 1, and the top of whirl dehydration pipe 2 is equipped with purification gas export 10, and the inner chamber of whirl dehydration pipe 2 is equipped with the condensation cap, the downside of whirl dehydration pipe 2 is connected to horizontal desulfurization dust removal pipe 6 of placing through dehydration gas export 4 to be connected to the one end of each desulfurization dust removal pipe 6 through dehydration gas manifold 15, 6 inner chambers of each desulfurization dust removal pipe are equipped with telescopic filter screen, and eight desulfurization dust removal pipes 6 are connected to the purification gas storage chamber at the top of whirl dehydration pipe 2 through desulfurization gas outlet 7 and purification gas manifold 16, and discharge through purification gas export 10.
Of course, it should be noted that a plurality of cyclone dewatering pipes 2, or 4, 6, 10 desulfurization and dust removal pipes 6 may be used according to the needs of the site, and the specific number is not limited, and it is emphasized in this embodiment that the installation of the desulfurization and dust removal pipes 6 may be designed to be a horizontal structure.
the utility model discloses a whirl dehydration pipe 2 adopts one, adopts vertical structure, and desulfurization dust removal pipe 6 adopts many, and many desulfurization dust removal pipe 6 adopts vertical structure, and whirl dehydration pipe 2 and desulfurization dust removal pipe 6 constitute circular overall arrangement, and use whirl dehydration pipe 2 as the centre of a circle.
Referring to fig. 11, the desulfurization dust removal pipe 6 adopts six, surrounds the whirl dehydration pipe 2 and constitutes circular overall arrangement, also the utility model discloses can be applied to the deformation of a structure on scene.
the utility model discloses a whirl dehydration pipe 2 adopts 2, adopts vertical structure, and desulfurization dust removal pipe 6 adopts many, and many desulfurization dust removal pipe 6 adopts vertical structure, and whirl dehydration pipe 2 and desulfurization dust removal pipe 6 constitute square overall arrangement.
Referring to fig. 12, the desulfurization dust removal pipe 6 adopts ten, surrounds the whirl dehydration pipe 2 and constitutes square overall arrangement, and through the manifold intercommunication, also be the utility model discloses can be applied to the deformation of a structure on scene.
In a word, the utility model provides a "well head air supply clarifier" be desulfurization, dehydration, take off the trinity sled piece structure of dirt, both can give the natural gas desulfurization, can dry dehydration dust removal again. Complete functions, small volume, simple structure and easy installation.
The wellhead gas source purifier is of a tubular structure (DN is less than or equal to 150mm), and can be of a vertical structure or a horizontal structure. The number and height of the desulfurization pipes and the dehydration pipes can be set at will according to the needs, and the layout mode can be combined at will according to the needs. The layout mode can be circular and even distribution, and can also be square and parallel and even distribution;
the desulfurization dust removal pipe is parallel connection structure each other, and the desulfurization dust removal pipe and the rotational flow dehydration pipe are connected structure each other. Therefore, the desulfurization dust removal pipes can be used separately and sequentially, after the first group of desulfurization dust removal pipes are used until the first group of desulfurization dust removal pipes completely lose effectiveness, the second group of desulfurization dust removal pipes are started to be used, and the rest can be done by analogy until the first group of desulfurization dust removal pipes are used up.
Because of the tubular structure, the flow path is small, the natural gas can fully contact with the desulfurizer without dead angles, the utilization rate is high, the desulfurization is thorough, and the fine desulfurization level (H2S less than 10 PPm) can be achieved.
Because of the tubular structure (DN is less than or equal to 150mm), the device is installed and used according to normal pressure equipment without annual record inspection without safety accessories.
The cyclone dewatering pipe component adopts a cyclone centrifugal and impact coagulation type combination technology, and the dewatering is clean and efficient.
Dry desulfurization, which adopts an internal sleeve type filter screen, and the desulfurizer is safe and convenient to replace (or an external flange enters and exits a material exchange port); the device can also realize dry-wet desulphurization, and has better effect.
The end openings of the desulfurization pipe and the dehydration pipe can be plugged by a seal head, a flange blind plate or a welding blind plate according to the requirement.
The utility model can also be used for other working conditions, such as methane desulfurization and dehydration.
The above description is only a preferred embodiment of the present invention, and any person skilled in the art may modify the present invention or modify it into an equivalent technical solution by using the technical solutions described above. Therefore, any simple modifications or equivalent replacements made according to the technical solution of the present invention belong to the scope of the claimed invention as far as possible.
Claims (9)
1. A wellhead gas source purifier is characterized in that: comprises an air source inlet (1), one or more rotational flow dehydration tubes (2), two or more desulfurization and dust removal tubes (6), a purified gas outlet (10) and a base plate seat (11), wherein the rotational flow dehydration tubes (2) and the desulfurization and dust removal tubes (6) are arranged on the base plate seat (11), the lower half part of the rotational flow dehydration tubes (2) is provided with the air source inlet (1), the top part of the rotational flow dehydration tubes (2) is provided with the purified gas outlet (10), the inner cavity of the rotational flow dehydration tubes (2) is provided with a water condensation cap, the lower side of the rotational flow dehydration tubes (2) is connected to the desulfurization air inlets (5) of the two or more desulfurization and dust removal tubes (6) through a dehydration gas outlet (4), the inner cavity of the desulfurization and dust removal tubes (6) is provided with a sleeve type filter screen, the top parts of the desulfurization and dust removal tubes (6) are connected to the purified gas storage cavity at the top parts of the rotational flow dehydration tubes, and is discharged through a purge gas outlet (10).
2. A wellhead gas source cleaner as claimed in claim 1, wherein: the cyclone dehydration tube (2) comprises a tube body (2.1), a dehydration gas guide tube (2.2), a purified gas storage cavity (2.3), a blocking plate (2.4), a condensation cap (2.5), a partition plate (2.6) and a seal head (2.7), wherein the blocking plate (2.4) is arranged at the bottom of the tube body (2.1), the seal head (2.7) is arranged at the top of the tube body, the partition plate (2.6) is arranged below the seal head (2.7), a purified gas storage cavity (2.3) is formed between the partition plate (2.6) and the seal head (2.7), and a purified gas inlet (9) and a purified gas outlet (10) are arranged at the outer side of the purified gas storage cavity (2.3); a dehydrated air conduit (2.2) and a plurality of condensed water caps (2.5) are arranged below the clapboard (2.6), and a first sewage discharge port (3) is arranged at the lower side of the pipe body (2.1).
3. A wellhead gas source cleaner as claimed in claim 2, wherein: the dehydration gas conduit (2.2) is arranged in the inner cavity of the pipe body (2.1), is positioned below the partition plate (2.6) and penetrates through the centers of the plurality of water condensation caps (2.5), and the bottom of the dehydration gas conduit (2.2) is communicated with the desulfurization dust removal pipe (6) through the dehydration gas outlet (4).
4. A wellhead gas source cleaner as claimed in claim 2, wherein: the dehydration gas conduit (2.2) is arranged at the outer side of the pipe body (2.1), the upper end of the dehydration gas conduit (2.2) is connected at the lower position of the partition plate (2.6) in the pipe body (2.1), and the lower end of the dehydration gas conduit (2.2) is communicated with the desulfurization dust removal pipe (6).
5. A wellhead gas source cleaner as claimed in claim 2, wherein: the desulfurization and dust removal pipe (6) comprises a desulfurization and dust removal pipe body (6.1), a sleeve type filter screen (6.2), a cross bracket (6.3), a second blocking plate (6.4), a second partition plate (6.5), a charging hole (6.6) and a discharge hole (6.8), the top of the desulfurization dust removal pipe body (6.1) is connected with a charging hole flange blind plate (13), a second partition plate (6.5) is arranged below the charging hole flange blind plate (13), a charging hole (6.6) is arranged at the lower side of the second partition plate (6.5), a sleeve type filter screen (6.2) and a cross bracket (6.3) are arranged in the inner cavity at the lower side of the desulfurization dust removal pipe body (6.1), the sleeve type filter screen (6.2) is arranged on the upper surface of the cross bracket (6.3), a desulfurization air inlet (5) is arranged below the transverse support (6.3), a second sewage draining outlet (14) and a second blocking plate (6.4) are arranged below the desulfurization air inlet (5), and a discharge outlet (6.8) is arranged at the outer side of the sleeve type filter screen (6.2).
6. A wellhead gas source cleaner as claimed in claim 5, wherein: the top of the desulfurization dust removal pipe (6) is connected to a purified gas inlet (9) at the top of the rotational flow dehydration pipe (2) through a desulfurization gas outlet (7).
7. A wellhead gas source cleaner as claimed in claim 1, wherein: the cyclone dewatering pipe (2) is one, the desulfurization and dust removal pipes (6) are in multiple groups, and the multiple groups of desulfurization and dust removal pipes (6) are in vertical layout.
8. A wellhead gas source cleaner as claimed in claim 1, wherein: the cyclone dewatering pipe (2) is one, the desulfurization and dust removal pipes (6) are in multiple groups, and the multiple groups of desulfurization and dust removal pipes (6) are in horizontal layout.
9. A wellhead gas source cleaner as claimed in claim 1, wherein: the cyclone dewatering pipe (2) is one, the desulfurization and dust removal pipes (6) are in multiple groups, and the multiple groups of desulfurization and dust removal pipes (6) are in circular vertical layout.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921393815.5U CN210656834U (en) | 2019-08-26 | 2019-08-26 | Wellhead gas source purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921393815.5U CN210656834U (en) | 2019-08-26 | 2019-08-26 | Wellhead gas source purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210656834U true CN210656834U (en) | 2020-06-02 |
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ID=70837082
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921393815.5U Expired - Fee Related CN210656834U (en) | 2019-08-26 | 2019-08-26 | Wellhead gas source purifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210656834U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110540881A (en) * | 2019-08-26 | 2019-12-06 | 刘凯 | Wellhead gas source purifier and method |
-
2019
- 2019-08-26 CN CN201921393815.5U patent/CN210656834U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110540881A (en) * | 2019-08-26 | 2019-12-06 | 刘凯 | Wellhead gas source purifier and method |
| CN110540881B (en) * | 2019-08-26 | 2024-01-09 | 东营市瑞兽节能设备有限公司 | Wellhead air source purifier and method |
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