CN208465553U - A kind of anti-shake dynamic gas and liquid collecting redistributor - Google Patents

A kind of anti-shake dynamic gas and liquid collecting redistributor Download PDF

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Publication number
CN208465553U
CN208465553U CN201820729625.5U CN201820729625U CN208465553U CN 208465553 U CN208465553 U CN 208465553U CN 201820729625 U CN201820729625 U CN 201820729625U CN 208465553 U CN208465553 U CN 208465553U
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liquid
module
unit
shake dynamic
redistributor
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CN201820729625.5U
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王柱祥
商恩霞
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Tianjin Pioneering Polytron Technologies Inc
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Tianjin Pioneering Polytron Technologies Inc
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Abstract

The utility model discloses a kind of anti-shake dynamic gas and liquid collecting redistributors, are disposed with liquid collecting unit, liquid conductive unit and liquid distribution unit from top to bottom;Liquid collecting unit is made of the interconnection of N number of liquid collection module;Liquid distribution unit is made of the interconnection of N number of liquid distribution module;Liquid conductive unit is made of N number of liquid conductive module and N connecting pipe.Gas-liquid has been divided into three collection, conduction and redistribution processes by this redistributor, liquid collection module, liquid conductive module and liquid distribution module form a complete collection redistribution system, single or multiple such systems form complete anti-shake dynamic gas and liquid collecting redistributor, each collection redistribution system is independent work, it is each responsible for respective region, is not interfere with each other;Even if strong shaking occurs, liquid is also to prevent from playing equally distributed effect because of bias current and wall stream caused by shaking severity in oneself independent region.

Description

A kind of anti-shake dynamic gas and liquid collecting redistributor
Technical field
The utility model relates to operate the internals that gas and liquid collecting redistributes in the case that operating condition is shaken, specially a kind of chemical industry Anti-shake dynamic gas and liquid collecting redistributor on knockout tower of mass transfer.
Background technique
With progress of the epoch, chemical production technical has long-range development, new production technology is to chemical production equipment Requirement it is also higher and higher, especially tower and internals, new technology require the specification of tower increasing (diameter and height), It asks the efficiency of internals higher and higher, while also to guarantee that it can work under complex environment operating condition, such as: land wind load The platform in biggish region or sea, both operating conditions feature having the same are exactly shaken larger.
In land: if tower is relatively high, (the tower equipment height run at present has been more than 60 meters, some even 100 Meter or more), these equipment just will appear apparent shaking, more severe, the rolling at the top of tower of the bigger shaking of wind when meeting strong wind Dynamic amplitude is maximum.Serious bias current and wall stream are formed when shaking in tower, forms liquid blank area, makes gas-liquid contact less than generation is short Road causes the internals efficiency in tower to decline, and liquid distribution is ineffective, influences overall efficiency.
At sea on platform: China coastal seas natural gas resource is abundant, these marine energies abundant, need to utilize in order to obtain Offshore platform is exploited, but needs to transport by processing after the extraction of some energy, such as the natural gas of offshore production, In natural gas other than main component alkane, also contain CO2And H2S impurity, this, which just needs to increase to absorb on platform at sea, sets Standby (such as absorption tower) is to CO2And H2S could be transported after carrying out removing processing.When absorption tower is at sea run, due to marine stormy waves It is bigger, cause offshore production platform shake, serious bias current and wall stream are formed in tower, make gas-liquid contact less than, occur short circuit, Influence desulfurization and decarburization effect.
Structure composition in general absorption tower include a set of slot type gas and liquid collecting distributor and slotted disc type gas and liquid collecting again Distributor, and slotted disc type gas and liquid collecting redistributor is mounted on the bottom of tower.Under this shaking operating condition, slotted disc type gas-liquid is received Collection redistributor has fatal defect.Be primarily due to: when slotted disc type gas and liquid collecting redistributor works, liquid is uniformly to divide Cloth is on slotted disc type gas and liquid collecting redistributor, the overflow hole under conventional design, on slotted disc type gas and liquid collecting redistributor Generally it is higher by supporting plane 50mm, liquid layer when work on slotted disk can be higher by overflow hole certain distance, it is capable of forming pressure in this way, Make liquid that there is power to flow out by overflow hole, only holding liquid level degree, just can guarantee the discharge phase of each overflow hole Together.When biggish shaking occurs in tower, it cannot guarantee the levelness of liquid level on distributor, make the flow between each overflow hole There is deviation, influences to be uniformly distributed.
It can be seen that in the case where shaking, in tower slotted disc type gas and liquid collecting redistributor to the distribution of liquid not It, is the key that reduce overall efficiency.
Utility model content
In view of the deficiencies of the prior art, the technical issues of the utility model intends to solve is to provide a kind of anti-shake dynamic gas-liquid Collect redistributor.
The technical solution that the utility model solves the technical problem is to provide a kind of anti-shake dynamic gas and liquid collecting redistribution Device, it is characterised in that the redistributor is disposed with liquid collecting unit, liquid conductive unit and liquid distribution from top to bottom Unit;
The liquid collecting unit is made of the interconnection of N number of liquid collection module, the cross of the liquid collecting unit of composition Cross sectional shape is identical as the cross-sectional shape of tower;Each liquid collection module includes fluid hole, riser and liquid barrier;Often The contour structures of a liquid collection module are that lowest point is provided with fluid hole to recessed irregular funnel-form;Each liquid M riser is penetrated through in collection module, riser runs through the upper and lower surface of liquid collection module;It is provided with above each riser The liquid barrier of suspension;
The liquid distribution unit is made of the interconnection of N number of liquid distribution module, the cross of the liquid distribution unit of composition Cross sectional shape is identical as the cross-sectional shape of tower;Each liquid distribution module includes supervisor, a fluid inlet pipe With several branch pipes;All branch pipes and supervisor are generally aligned in the same plane and connect with supervisor's square crossing;Supervisor and branch pipe just under Several liquid distributing holes of Fang Kaiyou;Fluid inlet pipe is welded on supervisor;
The liquid conductive unit is made of N number of liquid conductive module and N connecting pipe;Each liquid conductive module Upper end connects a fluid hole, and lower end connects a fluid inlet pipe;In the same plane, two neighboring liquid conductive module it Between a connecting pipe is installed;M, N is positive integer.
Compared with prior art, the utility model beneficial effect is:
(1) gas-liquid has been divided into collection, conduction and has redistributed three processes by this redistributor, liquid collection module, Liquid conductive module and liquid distribution module form a complete collection redistribution system, single or multiple such system groups At complete anti-shake dynamic gas and liquid collecting redistributor, each collection redistribution system is independent work, is each responsible for each From region, do not interfere with each other;Even if strong shaking occurs, liquid is also that will not arbitrarily flow in oneself independent region It is dynamic, guarantee that liquid is distributed in respective region, prevents from playing equally distributed effect because of bias current and wall stream caused by shaking severity Fruit guarantees mass transfer and heat transfer efficiency.
(2) liquid conductive module has certain vertical height, is capable of forming higher liquid level, and high liquid level can make liquid Body rate of outflow with higher when flowing out, this is just avoided that the direction let the liquid out by shaking changes, while can also Enough guarantee that liquid distribution inside modules are hydraulically full.
(3) liquid collection module is similar to an infundibulate (intermediate low surrounding high), after liquid flows into, can prevent liquid because It shakes and trickle collection module, plays the role of liquid uniform collection.
(4) liquid level that connecting pipe can balance between each liquid conductive module is not in apparent deviation, is played The quadratic distribution of liquid phase acts on.
(5) the hydraulically full liquid blank area that can prevent from occurring by shaking of liquid distribution inside modules, most for liquid It is evenly distributed eventually and plays the role of guarantee.
(6) liquid distributing hole, which ensure that, sprays being uniformly distributed for liquid.
Detailed description of the invention
Fig. 1 is a kind of anti-shake embodiment overall structure schematic front view of dynamic gas and liquid collecting redistributor of the utility model;
Fig. 2 is a kind of vertical view of the liquid collecting unit of embodiment of the anti-shake dynamic gas and liquid collecting redistributor of the utility model Schematic diagram;
Fig. 3 is a kind of main view of the liquid collection module of embodiment of the anti-shake dynamic gas and liquid collecting redistributor of the utility model Schematic cross-sectional view;
Fig. 4 is a kind of main view of the liquid conductive unit of the anti-shake dynamic embodiment of gas and liquid collecting redistributor of the utility model Schematic diagram;
Fig. 5 is a kind of vertical view of the liquid conductive unit of the anti-shake dynamic embodiment of gas and liquid collecting redistributor of the utility model Schematic diagram;
Fig. 6 is a kind of vertical view of the liquid distribution unit of the anti-shake dynamic embodiment of gas and liquid collecting redistributor of the utility model Structural schematic diagram;
Fig. 7 is a kind of vertical view of the liquid distribution module of the anti-shake dynamic embodiment of gas and liquid collecting redistributor of the utility model Schematic diagram;
Fig. 8 is a kind of left view of the liquid distribution module of the anti-shake dynamic embodiment of gas and liquid collecting redistributor of the utility model Schematic diagram.(in figure: 1- tower, 2- gas and liquid collecting redistributor, 3- liquid collecting unit, 31- liquid collection module, 32- go out liquid Hole, 33- riser, 34- liquid barrier, 4- liquid conductive unit, 41- liquid conductive module, 42- connecting pipe, 5- liquid distribution Unit, 51- liquid distribution module, 511- supervisor, 512- branch pipe, 513- fluid inlet pipe, 514- liquid distributing hole)
Specific embodiment
Specific embodiment of the utility model is given below.Specific embodiment is only used for being further described originally practical new Type does not limit the protection scope of the claim of this application.
The utility model provides a kind of anti-shake dynamic gas and liquid collecting redistributor (referring to Fig. 1-8, abbreviation redistributor), The gas and liquid collecting redistributor 2 is mounted on the position between the packing section in tower 1, it is characterised in that the redistributor is by upper Liquid collecting unit 3, liquid conductive unit 4 and liquid distribution unit 5 are disposed under;
The liquid collecting unit 3 passes through connector phase by N number of (N >=1, the present embodiment are 4) liquid collection module 31 Connect composition, and the cross-sectional shape of the liquid collecting unit 3 of composition is identical as the cross-sectional shape of tower 1, and (the present embodiment is It is discoid);Each liquid collection module 31 includes fluid hole 32, riser 33 and liquid barrier 34;Each liquid collection module 31 contour structures are that lowest point is provided with fluid hole 32 to recessed irregular funnel-form;Each liquid collection module 31 Interior perforation M (M >=2, the present embodiment are 6) riser 33 not of uniform size, riser 33 is through liquid collection module 31 Upper and lower surface;It is provided with the liquid barrier 34 of suspension above each riser 33, gas phase is from 33 upper end of liquid barrier 34 and riser Gap uniformly through, while guarantee from top and come liquid phase not can enter riser 33;
The liquid distribution unit 5 is located at the lowest level of entire redistributor, by N number of (N >=1, the present embodiment are 4) liquid Body distribution module 51 is connected with each other by connector and is formed, the cross-sectional shape of the liquid distribution unit 5 of composition and the cross of tower 1 Cross sectional shape is identical (the present embodiment is discoid);Each liquid distribution module 51 include 511, liquid phase of supervisor into Mouthful pipe 513 and several (the present embodiment is 5, quantity according to be calculated) branch pipe 512;The length of branch pipe 512 can be identical It can also be different;All branch pipes 512 and supervisor 511 are generally aligned in the same plane and connect with 511 square crossings of supervisor, the present embodiment In, a supervisor 511 and five branch pipes 512 form a quarter circle;Supervisor 511 and branch pipe 512 be Circular Pipe or rectangular tube, The underface of supervisor 511 and branch pipe 512 is provided with several liquid distributing holes 514 (quantity is calculated according to filler model);Supervisor 511 On be welded with fluid inlet pipe 513,513 end of fluid inlet pipe is equipped with flange;
The liquid conductive unit 4 between liquid collecting unit 3 and liquid distribution unit 5, liquid conductive unit 4 by N number of (N >=1, the present embodiment are 4) liquid conductive module 41 and N item (N >=1, the present embodiment are 4) connecting pipe 42 form; The upper end of each liquid conductive module 41 passes through one fluid inlet of flanged joint by one fluid hole 32 of flanged joint, lower end Pipe 513;In the same plane, a connecting pipe 42, connecting pipe 42 are installed between two neighboring liquid conductive module 41 It is not in apparent deviation that the liquid level between each liquid conductive module 41, which can be balanced, and the quadratic distribution for playing liquid phase is made With;The main function of liquid conductive unit 4 is that the liquid phase of the inner collection of liquid collecting unit 3 is transmitted in liquid distribution unit 5. M, N is positive integer;
Quantity, the liquid conductive module 41 of the liquid collection module 31 are identical with the quantity of liquid distribution module 51;Liquid Body collection module 31, liquid conductive module 41 and 51 three of liquid distribution module form a complete receipts by flanged joint Collect redistribution system, entire redistributor is collected redistribution system by several and formed, can be according to tower diameter size and operating environment (shaking degree) adjusts quantity.
The quantity of the liquid distributing hole 514 is calculated according to filler model, because every kind of filler has 514 quantity of liquid distributing hole Requirement.The riser 33 is for gas phase uniformly through riser 33 has certain height, prevents liquid from flowing into, and rises The specification and quantity of tracheae 33 are obtained according to gas phase carry calculation.
In the present embodiment, the diameter of tower 1 is DN1400, is made of four liquid collection modules 31, and corresponding liquid passes Guide module 41 and liquid distribution module 51 are 4.
The working principle and workflow of the anti-shake dynamic gas and liquid collecting redistributor of the utility model are:
In tower 1, self filler section and the liquid phase come are flowed into liquid collecting unit 3 by self gravity, liquid is collected single Each liquid collection module 31 of member 3 is similar to an infundibulate (intermediate low surrounding high), after liquid flows into, can prevent liquid because It shakes and trickle collection module 31, plays the role of liquid uniform collection;The lowest point of each liquid collection module 31 It is connected equipped with fluid hole 32 with liquid conductive module 41, the liquid that liquid collection module 41 is collected passes through liquid conductive module 41 It imported into liquid distribution module 51;The characteristics of liquid conductive module 41 is that have certain vertical height, is capable of forming higher Liquid level, and when high liquid level can be let the liquid out rate of outflow with higher, this is just avoided that lets the liquid out because of shaking Direction changes, while can also ensure that liquid distribution inside modules are hydraulically full.In the same plane, two neighboring liquid A connecting pipe 42 is installed between conduction module 41, connecting pipe 42 can balance between each liquid conductive module 41 Liquid level is not in apparent deviation, plays the role of the quadratic distribution of liquid phase;51 inside of liquid distribution module is hydraulically full can The liquid blank area occurred by shaking is prevented, is finally evenly distributed for liquid and plays the role of guarantee;Liquid distribution module 51 are evenly distributed with a certain number of liquid distributing holes 514 in lowest part, lower part, ensure that and spray being uniformly distributed for liquid;Top and liquid pass Guide module 41 is connected by flange, and triple interaction complements each other.
The utility model does not address place and is suitable for the prior art.

Claims (8)

1. a kind of anti-shake dynamic gas and liquid collecting redistributor, it is characterised in that the redistributor is disposed with liquid from top to bottom Collector unit, liquid conductive unit and liquid distribution unit;
The liquid collecting unit is made of the interconnection of N number of liquid collection module, the cross section of the liquid collecting unit of composition Shape is identical as the cross-sectional shape of tower;Each liquid collection module includes fluid hole, riser and liquid barrier;Each liquid The contour structures of body collection module are that lowest point is provided with fluid hole to recessed irregular funnel-form;Each liquid is collected M riser is penetrated through in module, riser runs through the upper and lower surface of liquid collection module;Suspension is provided with above each riser Liquid barrier;
The liquid distribution unit is made of the interconnection of N number of liquid distribution module, the cross section of the liquid distribution unit of composition Shape is identical as the cross-sectional shape of tower;If each liquid distribution module include one supervisor, a fluid inlet pipe and Dry branch pipe;All branch pipes and supervisor are generally aligned in the same plane and connect with supervisor's square crossing;It is opened immediately below supervisor and branch pipe There are several liquid distributing holes;Fluid inlet pipe is welded on supervisor;
The liquid conductive unit is made of N number of liquid conductive module and N connecting pipe;The upper end of each liquid conductive module A fluid hole is connected, lower end connects a fluid inlet pipe;In the same plane, pacify between two neighboring liquid conductive module Equipped with a connecting pipe;M, N is positive integer.
2. anti-shake dynamic gas and liquid collecting redistributor according to claim 1, it is characterised in that the liquid of composition is collected single The cross-sectional shape of member is discoid.
3. anti-shake dynamic gas and liquid collecting redistributor according to claim 1, it is characterised in that the liquid distribution list of composition The cross-sectional shape of member is discoid.
4. anti-shake dynamic gas and liquid collecting redistributor according to claim 1, it is characterised in that supervisor and branch pipe are oval Pipe or rectangular tube.
5. anti-shake dynamic gas and liquid collecting redistributor according to claim 1, it is characterised in that N >=1;M≥2.
6. anti-shake dynamic gas and liquid collecting redistributor according to claim 1, it is characterised in that the liquid collection module Quantity, liquid conductive module it is identical with the quantity of liquid distribution module.
7. anti-shake dynamic gas and liquid collecting redistributor according to claim 1, it is characterised in that the quantity of the liquid distributing hole It is calculated according to filler model.
8. anti-shake dynamic gas and liquid collecting redistributor according to claim 1, it is characterised in that the riser has anti- Only the height that liquid flows into, the specification and quantity of riser are obtained according to gas phase carry calculation.
CN201820729625.5U 2018-05-16 2018-05-16 A kind of anti-shake dynamic gas and liquid collecting redistributor Active CN208465553U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201820729625.5U CN208465553U (en) 2018-05-16 2018-05-16 A kind of anti-shake dynamic gas and liquid collecting redistributor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201820729625.5U CN208465553U (en) 2018-05-16 2018-05-16 A kind of anti-shake dynamic gas and liquid collecting redistributor

Publications (1)

Publication Number Publication Date
CN208465553U true CN208465553U (en) 2019-02-05

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CN (1) CN208465553U (en)

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