CN205627486U - Luo dao, coalescence operation filter equipment - Google Patents
Luo dao, coalescence operation filter equipment Download PDFInfo
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- CN205627486U CN205627486U CN201620392728.8U CN201620392728U CN205627486U CN 205627486 U CN205627486 U CN 205627486U CN 201620392728 U CN201620392728 U CN 201620392728U CN 205627486 U CN205627486 U CN 205627486U
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- luo dao
- coalescence
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- defecator
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Abstract
The utility model relates to a luo dao, coalescence operation filter equipment, characterized by: at least, include: fast open -blind board, shell, container low head, fast open -blind board, shell and container low head interface in proper order meet and form sealed container, the container low head is located in on the skirt, cut apart it become container and lower container in the central level of shell by separating the chamber board, upward the container top water is kept flat and has been put the clamp plate, the clamp plate and separate the chamber board between connect a plurality of coalescent filter perpendicularly, have a luo dao in a plurality of coalescent filter peripheries, luodao is from to separating surface distribution on the board of chamber below the clamp plate, luodao's luodao's direction of rotation is levogyration or dextrorotation, luo dao is connected with the shell, the lower container lateral wall have terminal wire mesh mist catcher, natural gas import is in last container lateral wall, natural gas export is in the terminal wire mesh mist catcher of lower container lateral wall in, the drain has outwards been drawn forth to container low head bottom. The device guarantees the absorption tower and gives vent to anger moisturely up to standard, reduces the running cost.
Description
Technical field
This utility model relates to a kind of natural gas filter, particularly a kind of Luo Dao, coalescence operation defecator.
Background technology
The natural gas of extraction from stratum, because of pressure, variations in temperature, have substantial amounts of saturated solution to separate out, these saturated solutions exceeded a certain amount of after, 2,2'-ethylenedioxybis(ethanol). dehydration in downstream is brought the biggest pressure, gas water dew point after 2,2'-ethylenedioxybis(ethanol). being caused to be dehydrated time serious is the most up to standard, directly affects product quality and downstream user uses.At present, the front end of 2,2'-ethylenedioxybis(ethanol). dewatering process flow is provided only with gravity separator, and this gravity separator can only carry out the separation of big drop, it is impossible to deviates from saturated solution.Traditional 2,2'-ethylenedioxybis(ethanol). air inlet flow process: carry out gas and be introduced into gravity separator, enters 2,2'-ethylenedioxybis(ethanol). absorption tower after carrying out simple Gravity Separation, and after 2,2'-ethylenedioxybis(ethanol). absorbs, gas transports to user as outside product gas.Owing in the gas on entrance absorption tower, liquid content is relatively big, in absorption tower, the 2,2'-ethylenedioxybis(ethanol). of circulation can not fully absorb moisture, causes the water dew point in product gas the most up to standard；Give vent to anger aqueous up to standard sometimes for guarantee, it has to strengthen the circulating load of 2,2'-ethylenedioxybis(ethanol). at double, thus cause operating cost to increase.
Summary of the invention
The purpose of this utility model is to provide a kind of Luo Dao, coalescence operation defecator, in order to make the coalescence of natural gas gas-liquid, gravity and end intercept function in one, thus it is aqueous up to standard to ensure to give vent to anger in absorption tower, reduces operating cost.
The purpose of this utility model is achieved in that a kind of Luo Dao, coalescence operation defecator, it is characterized in that: at least include: fast opening blind, shell, container low head；Fast opening blind, shell and container low head interface successively connect to being formed and seal container；Container low head is located on skirt；It is divided into upper container and lower container by separate space plate in shell central horizontal；Upper container top horizontal is placed with pressing plate；Between pressing plate and separate space plate, the multiple Coalescence filter cores of vertical connection, are with Luo Dao, Luo Dao below pressing plate to EDS maps separate space plate outside multiple Coalescence filter cores, and the direction of rotation of the Luo Dao of Luo Dao is left-handed or dextrorotation；Luo Dao is connected with shell；Described lower container side wall has end wire-mesh mist extractor；Imported gas is at described upper container sidewall, and gas outlet is in described lower container side wall end wire-mesh mist extractor；Sewage draining exit is outwards led to bottom container low head.
Described termination, Coalescence filter core bottom uses damascene structures with separate space plate.
There is differential manometer upper interface at upper container sidewall, have differential manometer lower interface at lower container side wall.
Liquid level mouth on liquidometer is had at lower container side wall；Upper container sidewall has gauge port.
Liquid level mouth under liquidometer is outwards drawn bottom described container low head.
Described separate space plate lower end connects the downspout having vertically downward.
Described interval, multiple Coalescence filter cores portion in a reservoir is uniformly distributed concentrically justifies.
Described end wire-mesh mist extractor or horizontally disposed, or be arranged vertically.
Described separate space plate and shell or be welded to connect, or bolt adds and is tightly connected.
Gauge port, drain is had, above the drain of gauge port at upper container sidewall.
The utility model has the advantages that: carry out gas through Imported gas containing saturated solution, entering and be introduced into Luo Dao inside shell epicoele and carry out crude separation, isolated liquid drains into shell cavity of resorption by downspout；Natural gas after Luo Dao separates enters Coalescence filter core, trap a large amount of saturated solution, the big drop formed flows into shell cavity of resorption along the inner tube wall of Coalescence filter core, after Coalescence filter core inner core natural gas via end wire-mesh mist extractor out intercepts, discharged by gas outlet again, enter 2,2'-ethylenedioxybis(ethanol). absorption tower, make the coalescence of natural gas gas-liquid, gravity and end intercept function in one, thus it is aqueous up to standard to ensure to give vent to anger in absorption tower, reduce operating cost.
Accompanying drawing explanation
Below in conjunction with embodiment, the utility model is described in further detail:
Fig. 1 is a kind of eddy flow, coalescence operation filter apparatus configuration sketch.
Fig. 2 is the A-A generalized section of Fig. 1.
In figure, 1, skirt, 2, liquid level mouth under liquidometer, 3, container low head, 4, downspout, 5, liquid level mouth on liquidometer, 6, differential manometer lower interface, 7, separate space plate, 8, differential manometer lower interface, 9, Coalescence filter core, 10, Luo Dao, 11, shell, 12, Imported gas, 13, pressing plate, 14, fast opening blind, 15, gauge port, 16, drain, 17, gas outlet, 18, end wire-mesh mist extractor, 19, sewage draining exit.
Detailed description of the invention
As depicted in figs. 1 and 2, a kind of Luo Dao, coalescence operation defecator: at least include: fast opening blind 14, shell 11, container low head 3；Fast opening blind 14, shell 11 and container low head 3 interface successively connect to being formed and seal container；Container low head 3 is located on skirt 1；It is divided into upper container and lower container by separate space plate 7 in shell 11 central horizontal；Upper container top horizontal is placed with pressing plate 13；Between pressing plate 13 and separate space plate 7, the multiple Coalescence filter cores 9 of vertical connection, are with spiral shell road 10 outside multiple Coalescence filter cores 9, and spiral shell road 10 is to EDS maps separate space plate 7 below pressing plate 13, and the direction of rotation of Luo Dao10Luo Dao is probably left-handed, it is also possible to dextrorotation；Spiral shell road 10 is connected with shell 11；Described lower container side wall has end wire-mesh mist extractor 18；Imported gas 12 is at described upper container sidewall, and gas outlet 17 is in described lower container side wall end wire-mesh mist extractor 18；Sewage draining exit 19 is outwards led to bottom container low head 3.
Termination, Coalescence filter core 9 bottom and separate space plate 7 use damascene structures.
There is differential manometer upper interface 8 at upper container sidewall, have differential manometer lower interface 6 at lower container side wall.
Liquid level mouth 5 on liquidometer is had at lower container side wall.Upper container sidewall has gauge port 15.
Liquid level mouth 2 under liquidometer is outwards drawn bottom described container low head 3.
Described separate space plate 7 lower end connects the downspout 4 having vertically downward.
Described interval, multiple Coalescence filter cores 9 portion in a reservoir is uniformly distributed concentrically justifies.
End wire-mesh mist extractor 18 or horizontally disposed, or be arranged vertically.
Described separate space plate 7 and shell 11 or be welded to connect, or bolt adds and is tightly connected.
Gauge port 15, drain 16 is had, above the drain 16 of gauge port 15 at upper container sidewall.
Separation process of the present utility model is: separation process: carry out gas through Imported gas 12 containing saturated solution, enters and is introduced into spiral shell road 10 inside shell 11 epicoele and carries out crude separation, and isolated liquid drains into shell 11 cavity of resorption by downspout 4；Natural gas after spiral shell road 10 separates enters Coalescence filter core 9, trap a large amount of saturated solution, the big drop formed flows into shell 11 cavity of resorption along the inner tube wall of Coalescence filter core 9, after Coalescence filter core 9 inner core natural gas via end wire-mesh mist extractor 18 out intercepts, discharged by gas outlet 17 again, enter 2,2'-ethylenedioxybis(ethanol). absorption tower.
Parts that the present embodiment describes the most in detail and structure belong to the well-known components of the industry and common structure or conventional means, describe the most one by one.
Claims (10)
1. a Zhong Luo road, coalescence operation defecator, is characterized in that: at least include: fast opening blind (14), shell (11), container low head (3)；Fast opening blind (14), shell (11) and container low head (3) interface successively connect to being formed and seal container；Container low head (3) is located on skirt (1)；It is divided into upper container and lower container by separate space plate (7) in shell (11) central horizontal；Upper container top horizontal is placed with pressing plate (13)；The multiple Coalescence filter cores of vertical connection (9) between pressing plate (13) and separate space plate (7), Luo Dao (10) it is with outside multiple Coalescence filter cores (9), Luo Dao (10) is from pressing plate (13) below to EDS maps separate space plate (7), and the direction of rotation of the Luo Dao of Luo Dao (10) is left-handed or dextrorotation；Luo Dao (10) is connected with shell (11)；Described lower container side wall has end wire-mesh mist extractor (18)；Imported gas (12) is at described upper container sidewall, and gas outlet (17) is in described lower container side wall end wire-mesh mist extractor (18)；Container low head (3) bottom outwards leads to sewage draining exit (19).
A kind of Luo Dao the most according to claim 1, coalescence operation defecator, is characterized in that: described Coalescence filter core (9) termination, bottom uses damascene structures with separate space plate (7).
A kind of Luo Dao the most according to claim 1, coalescence operation defecator, is characterized in that: have differential manometer upper interface (8) at upper container sidewall, have differential manometer lower interface (6) at lower container side wall.
A kind of Luo Dao the most according to claim 1, coalescence operation defecator, is characterized in that: have liquid level mouth (5) on liquidometer at lower container side wall；Upper container sidewall has gauge port (15).
A kind of Luo Dao the most according to claim 1, coalescence operation defecator, is characterized in that: liquid level mouth (2) under liquidometer is outwards drawn in described container low head (3) bottom.
A kind of Luo Dao the most according to claim 1, coalescence operation defecator, is characterized in that: described separate space plate (7) lower end connects the downspout (4) having vertically downward.
A kind of Luo Dao the most according to claim 1, coalescence operation defecator, is characterized in that: described interval, multiple Coalescence filter cores (9) portion in a reservoir is uniformly distributed concentrically justifies.
A kind of Luo Dao the most according to claim 1, coalescence operation defecator, is characterized in that: described end wire-mesh mist extractor (18) or horizontally disposed, or be arranged vertically.
A kind of Luo Dao the most according to claim 1, coalescence operation defecator, is characterized in that: described separate space plate (7) and shell (11) or be welded to connect, or bolt adds and is tightly connected.
A kind of Luo Dao the most according to claim 1, coalescence operation defecator, is characterized in that: have gauge port (15), drain (16) at upper container sidewall, above the drain (16) of gauge port (15).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620392728.8U CN205627486U (en) | 2016-05-04 | 2016-05-04 | Luo dao, coalescence operation filter equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620392728.8U CN205627486U (en) | 2016-05-04 | 2016-05-04 | Luo dao, coalescence operation filter equipment |
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| Publication Number | Publication Date |
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| CN205627486U true CN205627486U (en) | 2016-10-12 |
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| CN201620392728.8U Active CN205627486U (en) | 2016-05-04 | 2016-05-04 | Luo dao, coalescence operation filter equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108144421A (en) * | 2018-02-08 | 2018-06-12 | 江苏优耐特过滤装备有限公司 | Dry gas filter |
-
2016
- 2016-05-04 CN CN201620392728.8U patent/CN205627486U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108144421A (en) * | 2018-02-08 | 2018-06-12 | 江苏优耐特过滤装备有限公司 | Dry gas filter |
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