CN104437333B - A kind of high efficiency separation packed tower - Google Patents
A kind of high efficiency separation packed tower Download PDFInfo
- Publication number
- CN104437333B CN104437333B CN201410766244.0A CN201410766244A CN104437333B CN 104437333 B CN104437333 B CN 104437333B CN 201410766244 A CN201410766244 A CN 201410766244A CN 104437333 B CN104437333 B CN 104437333B
- Authority
- CN
- China
- Prior art keywords
- cell body
- passage
- tower
- window
- packing layer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/32—Packing elements in the form of grids or built-up elements for forming a unit or module inside the apparatus for mass or heat transfer
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/32—Packing elements in the form of grids or built-up elements for forming a unit or module inside the apparatus for mass or heat transfer
- B01J19/325—Attachment devices therefor, e.g. hooks, consoles, brackets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00002—Chemical plants
- B01J2219/00018—Construction aspects
- B01J2219/0002—Plants assembled from modules joined together
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00164—Controlling or regulating processes controlling the flow
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/24—Stationary reactors without moving elements inside
- B01J2219/2401—Reactors comprising multiple separate flow channels
- B01J2219/2402—Monolithic-type reactors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/24—Stationary reactors without moving elements inside
- B01J2219/2401—Reactors comprising multiple separate flow channels
- B01J2219/2402—Monolithic-type reactors
- B01J2219/2423—Separation means, e.g. membrane inside the reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
- B01J2219/33—Details relating to the packing elements in general
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
- B01J2219/332—Details relating to the flow of the phases
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention discloses a kind of high efficiency separation packed tower, including tower body and skirt, liquid distribution trough, the first packing layer, liquid header, liquid distribution trough, the second packing layer it is sequentially installed with from top to bottom in described tower body, tower body upper end is provided with steam (vapor) outlet, skirt is installed on bottom tower body, reboiler is installed bottom tower body, tower body is provided with steam inlet tube and feed pipe.The present invention can greatly improve the contact between liquid phase, and air resistance is little, and operation pressure drop is low, compact conformation, and mass-and heat-transfer efficiency is high, uniform gas-liquid distribution, improves separation efficiency.
Description
[technical field]
The present invention relates to the technical field of packed tower, the technical field of a kind of high efficiency separation packed tower.
[background technology]
Packed tower is the one of tower.The filler of suitably height is filled, to increase between two kinds of fluids in tower
Contact surface.Such as when being applied to GAS ABSORPTION, liquid is entered by distributor by the top of tower, along filler
Surface declines.Gas is then sailed against the current by filler hole by the bottom of tower, with liquid close contact and mutual
Effect.Structure is relatively simple, overhauls more convenient.Be widely used in GAS ABSORPTION, distill, the operation such as extraction.
Tower internals is the ingredient of packed tower, and it collectively forms a complete packed tower with filler and tower body.Institute
The effect of some tower internals is provided to make gas-liquid better contact with in tower, in order to play the maximum of packed tower
Production capacity and maximal efficiency, liquid distribution trough belong to filler in a kind of tower internals, therefore liquid distribution
The quality of separator directly affects playing and the performance of whole packed tower of carrier performance.
Packing ring focuses primarily in packed tower, as the mass transfer apparatus of contact member between gas-liquid two-phase, it is adaptable to
At the separation of various gases, absorption, desorption device, synthesis ammonia decarburization, desulphurization system, ethylbenzene separation, toluene
Separate.Common metal packing ring and common fillers ring are big because of weight, window impeller structure and the machine of ring body structurc
Tool intensity is low, yielding during stacking, easily forms dead angle in tower, and space is discontinuous, causes fluid resistance
Bigger flux is relatively low, easily causes gas-liquid channel, causes flux to reduce, and pressure drop raises, and separation efficiency reduces.
Structured packing is that one is arranged by uniform geometric figure in tower, the filler neatly piled up.Owing to having
Specific surface area is big, pressure drop is little, fluid divides uniformly, mass-and heat-transfer efficiency advantages of higher, has therefore obtained extensively
Application.Develop the earliest is metal structured packing, and that the most in succession develops has plastic regular packing material, pottery
Structured packing and carbon fibre regular filler.Orifice plate filler is the one in structured packing, existing orifice plate filler
Using single-side holed structure, the through-hole aperture that orifice plate is processed to form is relatively big, and the mechanical strength of orifice plate is relatively low,
Two through-hole apertures using hydraulic pressure to be processed to form are too small, and convection effects is poor, and pressure drop is big, and fluid distrbution is uneven,
Have a strong impact on separating effect.
[summary of the invention]
The purpose of the present invention solves the problems of the prior art exactly, proposes a kind of high efficiency separation packed tower, liquid
Body distributor has bigger mass transfer, the effective surface area of heat transfer, and liquid distribution is uniform, it is possible to change greatly
Contact between kind liquid phase, air resistance is little, and operation pressure drop is low, and compact conformation takes up space in tower
Little, thus improve the efficiency of tower, random packing ring quality is relatively light, and window impeller structure and outer ring body structure have relatively
High mechanical strength, is not easily formed dead angle during stacking, space is continuous, and fluid resistance relatively small throughput is higher, subtracts
Few gas-liquid channel, it is possible to effectively reduce pressure drop, separation efficiency improves, and it is strong that filler orifice plate has good machinery
Degree, and convection effects is good, mass-and heat-transfer efficiency is high, uniform gas-liquid distribution, improves separation efficiency.
For achieving the above object, the present invention proposes a kind of high efficiency separation packed tower, including tower body and skirt,
Liquid distribution trough, the first packing layer, liquid header, liquid it is sequentially installed with from top to bottom in described tower body
Distributor, the second packing layer, tower body upper end is provided with steam (vapor) outlet, and skirt is installed on bottom tower body, tower body
Bottom is provided with reboiler, and tower body is provided with steam inlet tube and feed pipe, and described liquid distribution trough includes
Chassis, distributing disc and inverted draw cut composition, described distributing disc is installed on chassis, chassis has some first and leads to
Pore, is connected with chassis bottom described distributing disc, distributing disc the most successively by the first cell body, second
Cell body, the 3rd cell body, the 4th cell body, the 3rd cell body, the second cell body and the first cell body composition, in distributing disc
The heart is provided with the 5th cell body, and the first cell body, the second cell body, the 3rd cell body, the 4th cell body are connected by the 5th cell body
Logical, described inverted draw cut is installed on distributing disc by some springs, inverted draw cut has some forms, in distributing disc
Being provided with cross bar, described cross bar is provided with some first arc flow deflectors and some second arc flow deflectors, institute
Stating the first packing layer to be made up of the stacking of random packing ring, random packing ring includes that outer ring body structure, inner ring body are tied
Structure, some window structures and some window impeller structures, described window structure is opened in outer ring body structure, forms
Being provided with the first web plate in structure, one end of window impeller structure is connected with window structure, another of window impeller structure
End be connected with inner ring body structure, described inner ring body structure is provided with some deflectors, if window impeller structure by
Dry arc-shaped leaf bar forms, and is provided with the second web plate, described second packing layer between two adjacent arc-shaped leaf bars
Put by stuffing hole sheetpile and form, filler orifice plate include by the first inclined-plane, the second inclined-plane, the first passage,
Two passages and the filler orifice plate of convection holes composition, if described first inclined-plane and the second inclined-plane are disposed adjacent formation
Dry boss structure and groove structure, described first passage and the second passage distribute alternately on filler orifice plate,
Second passage is offered, the first passage and the in the rectangular centre that every 4 the first passages are formed
The first turnup structure and the second turnup structure being stamped and formed out, the first turnup structure it is respectively equipped with on two passages
In opposite direction with the second turnup structure.
As preferably, between described first packing layer and liquid header, bracing frame, steam inlet tube are installed
It is installed on the bottom of the second packing layer, between steam inlet tube and the second packing layer, bracing frame is installed, second
Packing layer upper end is provided with hold-down grid, and feed pipe is installed between the first packing layer and the second packing layer.
As preferably, the length of described first cell body is less than the length of the second cell body, and the length of the second cell body is little
In the length of the 3rd cell body, the length of the 3rd cell body is less than the length of the 4th cell body, described the first adjacent groove
Install between body and the second cell body, between the second cell body and the 3rd cell body, between the 3rd cell body and the 4th cell body
There is bracing piece.
As preferably, the bottom of described inverted draw cut offers the second passage, and the edge of inverted draw cut is provided with groove knot
Structure, inverted draw cut both sides are provided with spring retainer ring, and spring one end is connected with spring retainer ring, the spring other end with
Distributing disc is connected, and number of springs is 6～8, described cross bar be respectively arranged in the first cell body, the second cell body,
In 3rd cell body and the 4th cell body, the first arc flow deflector and the second arc flow deflector are respectively symmetrically and are arranged at horizontal stroke
The both sides of bar, the bending direction of the first arc flow deflector and the second arc flow deflector is contrary.
As preferably, a diameter of the 10～90mm of described outer ring body structure, the inwall of outer ring body structure offers
Some guiding gutters, are distributed 2～3 guiding gutters between adjacent two window impeller structures, described window impeller structure is curved
The outwards arc at ring body structurc center, window impeller structure passes through bracing piece with outer near one end of outer ring body structure
Ring body structurc is connected, and described deflector is installed on the inner side of inner ring body structure, in deflector tilts to be installed on
On ring body structurc, the quantity of deflector is 6～8 pieces, and some deflector circular array are distributed, described window leaf
Structure is made up of 2～4 arc-shaped leaf bars.
As preferably, described boss structure is provided with the first plane, and groove structure is provided with the second plane, vertical
On direction, adjacent two have convection holes, on described first passage between boss structure and groove structure
First turnup structure flips up, and the second turnup structure on the second passage is turned over downwards.
As preferably, described first passage and the second passage are respectively equipped with 2 first turnup structures and 2
Sheet the second turnup structure, the first passage and the second passage are in-line through hole.
As preferably, described first passage and the second passage are respectively equipped with 4 first flange knots
Structure and 4 second turnup structures, the first passage and the second passage are cross-shaped through hole.
Beneficial effects of the present invention: the liquid distribution trough in the present invention have bigger mass transfer, heat transfer effective
Surface area, liquid distribution is uniform, it is possible to improve the contact between liquid phase greatly, and air resistance is little, behaviour
Make pressure drop low, compact conformation, take up space in tower little, thus improve the efficiency of tower, random packing ring matter
Amount is relatively light, and window impeller structure and outer ring body structure have higher mechanical strength, are not easily formed dead angle during stacking,
Space is continuous, and fluid resistance relatively small throughput is higher, reduces gas-liquid channel, it is possible to effectively reduce pressure drop, separates
Efficiency improves, and filler orifice plate has good mechanical strength, and convection effects is good, and mass-and heat-transfer efficiency is high,
Uniform gas-liquid distribution, improves separation efficiency.
Inventive feature and advantage will combine accompanying drawing by embodiment and be described in detail.
[accompanying drawing explanation]
Fig. 1 is the main TV structure figure of the present invention a kind of high efficiency separation packed tower；
Fig. 2 is the main TV structure figure of random packing ring of the present invention；
Fig. 3 is the plan structure figure of random packing ring of the present invention；
Fig. 4 is the structural representation of window impeller structure of the present invention；
Fig. 5 is the top view of fluid present invention distributor；
Fig. 6 is the structural representation of inverted draw cut of the present invention；
Fig. 7 is the main TV structure figure of filler orifice plate of the present invention；
Fig. 8 is the present invention the first passage and the distribution schematic diagram of the second passage；
Fig. 9 is the structure chart of the present invention the first passage；
Figure 10 is the structure chart of the present invention the second passage.
[detailed description of the invention]
Refering to Fig. 1 to Figure 10, one high efficiency separation packed tower of the present invention, including tower body 1 and skirt 11, institute
Be sequentially installed with from top to bottom in stating tower body 1 liquid distribution trough the 2, first packing layer 3, liquid header 12,
Liquid distribution trough the 2, second packing layer 4, tower body 1 upper end is provided with steam (vapor) outlet 13, and skirt 11 is installed on
Bottom tower body 1, reboiler 14 is installed bottom tower body 1, tower body 1 is provided with steam inlet tube 15 and enters
Material pipe 16, described liquid distribution trough 2 includes that chassis 21, distributing disc 22 and inverted draw cut 23 form, described distribution
Dish 22 is installed on chassis 21, and chassis 21 has some first passages 211, described distributing disc 22 end
Portion is connected with chassis 21, distributing disc 22 the most successively by first cell body the 221, second cell body 222,
3rd cell body the 223, the 4th cell body the 224, the 3rd cell body the 223, second cell body 222 and the first cell body 221 groups
Becoming, distributing disc 22 center is provided with the 5th cell body 225, and the 5th cell body 225 is by first cell body the 221, second groove
Body the 222, the 3rd cell body the 223, the 4th cell body 224 is connected, and described inverted draw cut 23 is pacified by some springs 24
It is loaded on distributing disc 22, inverted draw cut 23 has some forms 231, cross bar 25 is installed in distributing disc 22,
Described cross bar 25 is provided with some first arc flow deflectors 251 and some second arc flow deflectors 252, described
First packing layer 3 is stacked by random packing ring and is formed, and random packing ring includes outer ring body structure 31, inner ring body
Structure 32, some window structures 33 and some window impeller structures 34, described window structure 33 is opened in outer ring body
In structure 31, being provided with the first web plate 331 in window structure 33, one end of window impeller structure 34 is tied with forms
Structure 33 is connected, and the other end of window impeller structure 34 is connected with inner ring body structure 32, described inner ring body structure
Being provided with some deflectors 321 on 32, window impeller structure 34 is made up of some arc-shaped leaf bars 341, and two adjacent
Arc-shaped leaf bar 341 between the second web plate 342 is installed, described second packing layer 4 is put group by stuffing hole sheetpile
Becoming, filler orifice plate includes by the 41, second inclined-plane, the first inclined-plane the 42, first passage the 43, second passage
44 and convection holes 45 composition filler orifice plate, described first inclined-plane 41 and the second inclined-plane 42 are disposed adjacent formation
Some boss structures 46 and groove structure 47, described first passage 43 and the second passage 44 distribute alternately
On filler orifice plate, the rectangular centre of every 4 the first passage shapes 43 one-tenth offers second passage
44, the first passage 43 and the second passage 44 are respectively equipped with the first turnup structure 431 being stamped and formed out
In opposite direction with the second turnup structure 441, the first turnup structure 431 and the second turnup structure 441.
Between described first packing layer 3 and liquid header 12, bracing frame 17, steam inlet tube 15 are installed
It is installed on the bottom of the second packing layer 4, between steam inlet tube 15 and the second packing layer 4, bracing frame is installed
17, the second packing layer 4 upper end is provided with hold-down grid 18, and feed pipe 16 is installed on the first packing layer 3 and
Between two packing layers 4, the length of described first cell body 221 is less than the length of the second cell body 222, the second groove
The length of body 222 is less than the 4th cell body 224 less than the length of the 3rd cell body 223, the length of the 3rd cell body 223
Length, described between adjacent the first cell body 221 and the second cell body 222, the second cell body 222 and the 3rd
Bracing piece 26, described inverted draw cut are installed between cell body 223, between the 3rd cell body 223 and the 4th cell body 224
The bottom of 23 offers the second passage 232, and the edge of inverted draw cut 23 is provided with insection structure 233, inverted draw cut 23
Both sides are provided with spring retainer ring 234, and spring 24 one end is connected with spring retainer ring 234, spring 24 another
End is connected with distributing disc 22, and spring 24 quantity is 6～8, and described cross bar 25 is respectively arranged in first
In cell body the 221, second cell body the 222, the 3rd cell body 223 and the 4th cell body 224, the first arc flow deflector 251
The both sides being arranged at cross bar 25, the first arc flow deflector 251 He it is respectively symmetrically with the second arc flow deflector 252
The bending direction of the second arc flow deflector 252 is contrary.
A diameter of the 10～90mm of described outer ring body structure 31, the inwall of outer ring body structure 31 offers some
Guiding gutter 311, is distributed 2～3 guiding gutters 311 between adjacent two window impeller structures 34, described window leaf is tied
Structure 34 is the arc bending towards outer ring body structure 31 center, and window impeller structure 34 is near outer ring body structure 31
One end is connected with outer ring body structure 31 by bracing piece 343, and described deflector 321 is installed on inner ring body knot
The inner side of structure 32, deflector 321 tilt be installed in inner ring body structure 32, the quantity of deflector 321 be 6～
8 pieces, some deflector 321 circular array are distributed, and described window impeller structure 34 is by 2～4 arc-shaped leaf bars
341 compositions.
Described boss structure 46 is provided with the first plane 461, and groove structure 47 is provided with the second plane 471,
Convection holes 48 is had between adjacent two boss structures 46 and groove structure 47 on longitudinal direction, described first
The first turnup structure 431 on passage 43 flips up, the second turnup structure on the second passage 44
441 are turned over downwards, and described first passage 43 and the second passage 44 are respectively equipped with 2 first flange knots
Structure 431 and 2 second turnup structures 441, the first passage 43 and the second passage 44 are in-line through hole,
It is respectively equipped with 4 first turnup structures 431 and 4 on described first passage 43 and the second passage 44
Sheet the second turnup structure 441, the first passage 43 and the second passage 44 are cross-shaped through hole.
Work process of the present invention:
In the course of the work, liquid distribution trough in the course of the work, divides one high efficiency separation packed tower of the present invention
Cloth dish 22 is the most successively by first cell body the 221, second cell body the 222, the 3rd cell body the 223, the 4th cell body
224, the 3rd cell body the 223, second cell body 222 and the first cell body 221 form, and distributing disc 22 center is provided with
Five cell bodies 225, the 5th cell body 225 by first cell body the 221, second cell body 222, the 3rd cell body 223,
Four cell bodies 224 are connected, and cross bar 25 is provided with some first arc flow deflectors 251 and some second arcs are led
Flow 252, distributing disc 22 has bigger mass transfer, the effective surface area of heat transfer, and liquid distribution is uniform, energy
Enough improvement greatly has the first passage 211 on the contact between liquid phase, chassis 21 and inverted draw cut 23
With the second passage 232, and inverted draw cut 23 is connected with distributing disc 22 by spring 24, and air resistance is little,
Operation pressure drop is low, and compact conformation takes up space in tower little, thus improves the efficiency of tower.
On random packing ring, one end of window impeller structure 34 is connected with window structure 33, window impeller structure 34 another
One end is connected with inner ring body structure 32, lighter weight, and window impeller structure 34 is near the one of outer ring body structure 31
End is connected with outer ring body structure 31 by bracing piece 343, and window impeller structure 34 and outer ring body structure 31 have
Higher mechanical strength, is not easily formed dead angle during stacking, space is continuous, if being provided with in inner ring body structure 32
Dry deflector 321, is provided with the second web plate 342 between two adjacent arc-shaped leaf bars 341, and fluid resistance is relatively
Small throughput is higher, reduces gas-liquid channel, it is possible to effectively reduce pressure drop, and separation efficiency improves.
By processing the first passage 43 and the second passage 44 distributed alternately on filler orifice plate, first leads to
Pore 43 and the second passage 44 use the processing mode of punching press to be formed, the first passage 43 and the second ventilation
Hole 44 is got through the most completely, and the first passage 43 and the second passage 44 are respectively equipped be stamped and formed out
One turnup structure 431 and the second turnup structure 441, the first turnup structure 431 and the second turnup structure 441
In opposite direction so that filler orifice plate has good mechanical strength, and convection effects is good, mass-and heat-transfer efficiency
Height, uniform gas-liquid distribution, improves separation efficiency.
Above-described embodiment is the description of the invention, is not limitation of the invention, any simple to the present invention
Scheme after conversion belongs to protection scope of the present invention.
Claims (6)
1. a high efficiency separation packed tower, it is characterised in that: include tower body (1) and skirt (11), described tower body
(1) liquid distribution trough (2), the first packing layer (3), liquid header it are sequentially installed with in from top to bottom
(12), liquid distribution trough (2), the second packing layer (4), tower body (1) upper end is provided with steam (vapor) outlet
(13), skirt (11) is installed on tower body (1) bottom, and tower body (1) bottom is provided with reboiler (14),
Steam inlet tube (15) and feed pipe (16), described liquid distribution trough (2) are installed on tower body (1)
Forming including chassis (21), distributing disc (22) and inverted draw cut (23), described distributing disc (22) is installed on
On chassis (21), chassis (21) have some first passages (211), described distributing disc (22)
Bottom be connected with chassis (21), distributing disc (22) the most successively by the first cell body (221),
Second cell body (222), the 3rd cell body (223), the 4th cell body (224), the 3rd cell body (223),
Two cell bodies (222) and the first cell body (221) composition, distributing disc (22) center is provided with the 5th cell body (225),
5th cell body (225) by the first cell body (221), the second cell body (222), the 3rd cell body (223),
Four cell bodies (224) are connected, and described inverted draw cut (23) is installed on distributing disc (22) by some springs (24)
On, inverted draw cut (23) has some forms (231), cross bar (25) is installed in distributing disc (22),
Described cross bar (25) is provided with some first arc flow deflectors (251) and some second arc flow deflectors
(252), described first packing layer (3) is stacked by random packing ring and is formed, and random packing ring includes outer shroud
Body structure (31), inner ring body structure (32), some window structures (33) and some window impeller structures (34),
Described window structure (33) is opened in outer ring body structure (31), and window structure is provided with in (33)
First web plate (331), one end of window impeller structure (34) is connected with window structure (33), and window leaf is tied
The other end of structure (34) is connected with inner ring body structure (32), the upper peace of described inner ring body structure (32)
Equipped with some deflectors (321), window impeller structure (34) is made up of some arc-shaped leaf bars (341), two
Second web plate (342), described second packing layer (4) are installed between adjacent arc-shaped leaf bar (341)
Put by stuffing hole sheetpile and form, filler orifice plate include by the first inclined-plane (41), the second inclined-plane (42),
The filler orifice plate that one passage (43), the second passage (44) and convection holes (45) form, described
One inclined-plane (41) and the second inclined-plane (42) are disposed adjacent the some boss structures of formation (46) and groove knot
Structure (47), described first passage (43) and the second passage (44) distribute alternately on filler orifice plate,
Second passage (44) is offered in the rectangular centre that every 4 the first passages (43) are formed, the
The first turnup structure (431) being stamped and formed out it is respectively equipped with on one passage (43) and the second passage (44)
With the second turnup structure (441), the first turnup structure (431) and the side of the second turnup structure (441)
To on the contrary；Between described first packing layer (3) and liquid header (12), bracing frame (17) is installed,
Steam inlet tube (15) is installed on the bottom of the second packing layer (4), steam inlet tube (15) and second
Being provided with bracing frame (17) between packing layer (4), the second packing layer (4) upper end is provided with hold-down grid
(18), feed pipe (16) is installed between the first packing layer (3) and the second packing layer (4)；Described
The length of the first cell body (221) is less than the length of the second cell body (222), the length of the second cell body (222)
Degree is less than the 4th cell body (224) less than the length of the 3rd cell body (223), the length of the 3rd cell body (223)
Length, between described adjacent the first cell body (221) and the second cell body (222), the second cell body (222)
And the 3rd between cell body (223), be provided with between the 3rd cell body (223) and the 4th cell body (224) and add
Strong bar (26).
2. a kind of high efficiency separation packed tower as claimed in claim 1, it is characterised in that: described inverted draw cut (23)
Bottom offers the second passage (232), and the edge of inverted draw cut (23) is provided with insection structure (233),
Inverted draw cut (23) both sides are provided with spring retainer ring (234), spring (24) one end and spring retainer ring (234)
Being connected, spring (24) other end is connected with distributing disc (22), and spring (24) quantity is 6～8
Root, described cross bar (25) is respectively arranged in the first cell body (221), the second cell body (222), the 3rd groove
In body (223) and the 4th cell body (224), the first arc flow deflector (251) and the second arc flow deflector
(252) it is respectively symmetrically and is arranged at the both sides of cross bar (25), the first arc flow deflector (251) and second
The bending direction of arc flow deflector (252) is contrary.
3. a kind of high efficiency separation packed tower as claimed in claim 1, it is characterised in that: described outer ring body structure (31)
A diameter of 10～90mm, the inwall of outer ring body structure (31) offers some guiding gutters (311), phase
2～3 guiding gutters (311), described window impeller structure (34) are distributed between adjacent two window impeller structures (34)
For bending towards the arc at outer ring body structure (31) center, window impeller structure (34) is near outer ring body structure (31)
One end be connected with outer ring body structure (31) by bracing piece (343), described deflector (321)
Being installed on the inner side of inner ring body structure (32), deflector (321) tilts to be installed on inner ring body structure (32)
On, the quantity of deflector (321) is 6～8 pieces, and some deflectors (321) circular array is distributed,
Described window impeller structure (34) is made up of 2～4 arc-shaped leaf bars (341).
4. a kind of high efficiency separation packed tower as claimed in claim 1, it is characterised in that: described boss structure (46)
Being provided with the first plane (461), groove structure (47) is provided with the second plane (471), longitudinal direction
A convection holes (48) is had between upper adjacent two boss structures (46) and groove structure (47), described
The first turnup structure (431) on one passage (43) flips up, on the second passage (44)
Second turnup structure (441) is turned over downwards.
5. a kind of high efficiency separation packed tower as claimed in claim 1, it is characterised in that: described first passage (43)
Be respectively equipped with on the second passage (44) 2 first turnup structures (431) and 2 second flange knot
Structure (441), the first passage (43) and the second passage (44) are in-line through hole.
6. a kind of high efficiency separation packed tower as claimed in claim 1, it is characterised in that: described first ventilation
4 first turnup structures (431) and 4 it are respectively equipped with on hole (43) and the second passage (44)
Two turnup structures (441), the first passage (43) and the second passage (44) are cross-shaped through hole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410766244.0A CN104437333B (en) | 2014-12-12 | 2014-12-12 | A kind of high efficiency separation packed tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410766244.0A CN104437333B (en) | 2014-12-12 | 2014-12-12 | A kind of high efficiency separation packed tower |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104437333A CN104437333A (en) | 2015-03-25 |
| CN104437333B true CN104437333B (en) | 2016-08-24 |
Family
ID=52884543
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410766244.0A Active CN104437333B (en) | 2014-12-12 | 2014-12-12 | A kind of high efficiency separation packed tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104437333B (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4774033A (en) * | 1987-03-17 | 1988-09-27 | Energair Research And Development | Gas liquid tower structure |
| US5942164A (en) * | 1997-08-06 | 1999-08-24 | The United States Of America As Represented By The United States Department Of Energy | Combined heat and mass transfer device for improving separation process |
| JP2008119635A (en) * | 2006-11-14 | 2008-05-29 | Tadayoshi Nagaoka | Liquid distributor of gas-liquid contact apparatus for performing mass transfer and the like |
| CN202777878U (en) * | 2012-06-18 | 2013-03-13 | 天津大学 | Microbubble integral mass transfer tower tray |
| CN103041762A (en) * | 2012-12-21 | 2013-04-17 | 泰州职业技术学院 | Grid plate tower |
| CN204395967U (en) * | 2014-12-12 | 2015-06-17 | 海盐新世纪石化设备有限公司 | A kind of new and effective separating filler tower |
-
2014
- 2014-12-12 CN CN201410766244.0A patent/CN104437333B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4774033A (en) * | 1987-03-17 | 1988-09-27 | Energair Research And Development | Gas liquid tower structure |
| US5942164A (en) * | 1997-08-06 | 1999-08-24 | The United States Of America As Represented By The United States Department Of Energy | Combined heat and mass transfer device for improving separation process |
| JP2008119635A (en) * | 2006-11-14 | 2008-05-29 | Tadayoshi Nagaoka | Liquid distributor of gas-liquid contact apparatus for performing mass transfer and the like |
| CN202777878U (en) * | 2012-06-18 | 2013-03-13 | 天津大学 | Microbubble integral mass transfer tower tray |
| CN103041762A (en) * | 2012-12-21 | 2013-04-17 | 泰州职业技术学院 | Grid plate tower |
| CN204395967U (en) * | 2014-12-12 | 2015-06-17 | 海盐新世纪石化设备有限公司 | A kind of new and effective separating filler tower |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104437333A (en) | 2015-03-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105457454B (en) | Separate and recover monoblock type absorption tower and the method for carrying organic amine salt in flue gas secretly | |
| CN101269314B (en) | Screen aperture reticular lamina corrugated filler tablet and regular packing | |
| CN206867858U (en) | A kind of steam-water separator device suitable for steam | |
| CN205145954U (en) | Extensive flue gas CO2 entrapment reactor | |
| CN204364924U (en) | Liquid sieve-plate tower falls in dispersion | |
| CN204395967U (en) | A kind of new and effective separating filler tower | |
| CN104524801B (en) | A kind of dispersion descending liquid sieve-plate tower | |
| CN104437333B (en) | A kind of high efficiency separation packed tower | |
| CN205796637U (en) | The Despumation device that a kind of gas-liquid separator is built-in | |
| CN107126820A (en) | The wire mesh demister of multiple foam removal | |
| CN201066254Y (en) | Reinforced multiple waveform water collector | |
| CN204543610U (en) | Vortex filament shape is from uniform regular packed tower | |
| CN207041947U (en) | A kind of catalytic distillation module | |
| CN201304261Y (en) | Porous three-dimensional gas-liquid contact element | |
| CN204865860U (en) | Pottery regular packing | |
| CN105258453B (en) | A kind of method that lighter hydrocarbons and hydrogen are reclaimed in the tail gas from petrochemical plant | |
| CN205386396U (en) | Integral absorption tower of smuggleing organic amine salts secretly in flue gas is retrieved in separation | |
| CN203155232U (en) | Difference-peak wire mesh corrugated packing | |
| CN201632186U (en) | Steam separating device | |
| CN205627966U (en) | Novel ring square saddle bulk packing | |
| CN204563881U (en) | A kind of high-concentration formaldehyde absorption tower | |
| CN111013178B (en) | Stepped liquid circulation bubble tower and method for dispersing gas | |
| CN204395976U (en) | A kind of liquid distribution trough | |
| CN102600788A (en) | Multi-stage spray reaction tower | |
| CN102688658A (en) | Novel drying and absorption tower |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 314300, Zhejiang, Haiyan County, Jiaxing province Haiyan Economic Development Zone, new step, Feng Nong junction Patentee after: Jiaxing Wushi Engineering Co.,Ltd. Address before: 314300, Zhejiang, Haiyan County, Jiaxing province Haiyan Economic Development Zone, new step, Feng Nong junction Patentee before: HAIYAN NEW CENTURY PETROCHEMICAL EQUIPMENT Co.,Ltd. |
|
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 314300 Nongfeng road crossing, Baibu New District, Haiyan Economic Development Zone, Haiyan County, Jiaxing City, Zhejiang Province Patentee after: Maestro Technology Co.,Ltd. Address before: 314300 Nongfeng road crossing, Baibu New District, Haiyan Economic Development Zone, Haiyan County, Jiaxing City, Zhejiang Province Patentee before: Jiaxing Wushi Engineering Co.,Ltd. |
|
| CP01 | Change in the name or title of a patent holder |