CN108310921A - Oval ripple sieve-plate tower - Google Patents
Oval ripple sieve-plate tower Download PDFInfo
- Publication number
- CN108310921A CN108310921A CN201810310201.XA CN201810310201A CN108310921A CN 108310921 A CN108310921 A CN 108310921A CN 201810310201 A CN201810310201 A CN 201810310201A CN 108310921 A CN108310921 A CN 108310921A
- Authority
- CN
- China
- Prior art keywords
- tower
- plate
- tray
- liquid
- sieve
- 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.)
- Pending
Links
- 239000007788 liquid Substances 0.000 claims abstract description 35
- 238000010521 absorption reaction Methods 0.000 claims abstract description 5
- 238000012216 screening Methods 0.000 claims abstract description 4
- 210000005182 tip of the tongue Anatomy 0.000 claims abstract description 4
- 239000011148 porous material Substances 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 229910000831 Steel Inorganic materials 0.000 claims description 3
- 239000010959 steel Substances 0.000 claims description 3
- 230000008676 import Effects 0.000 claims description 2
- 239000000463 material Substances 0.000 claims description 2
- 229920003023 plastic Polymers 0.000 claims description 2
- 239000004033 plastic Substances 0.000 claims description 2
- 239000010865 sewage Substances 0.000 claims description 2
- 229910001220 stainless steel Inorganic materials 0.000 claims description 2
- 239000010935 stainless steel Substances 0.000 claims description 2
- 238000005406 washing Methods 0.000 abstract description 4
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract description 2
- 239000012855 volatile organic compound Substances 0.000 abstract description 2
- 238000003466 welding Methods 0.000 abstract description 2
- 238000010009 beating Methods 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 3
- 239000003595 mist Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
- B01D53/18—Absorbing units; Liquid distributors therefor
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
Oval ripple sieve-plate tower.Technical field：Chemical industry；Environmental protection；Gas is absorbed, washing, is sprayed, VOCs is administered.Oval ripple sieve-plate tower is the New-type plate absorption tower advantageous in high throughput, is made of tower top, tower body and bottom of tower.Master unit is that semiellipse corrugated sieve column plate is by beating porous semiellipse tube welding on the disk of garden, and peak is all that upward being welded in a plane constitutes waveform sieve tray between each semicanal；It is that the retroflect the tip of the tongue of shape goes out at liquid with column plate upwards in parallel that downspout lower part, which sets screening (folding) flowing plate, and boom plate is provided with multiple half circular holes below makes liquid in the outflow of ridge shape；It does not set and holds liquid zone.
Description
Technical field：Chemical industry；Environmental protection；Gas is absorbed, washing, is sprayed, VOCs is administered
Background technology：The gas that absorption tower is widely used in petrochemical industry field of environment protection is absorbed, washing, is sprayed, VOCS processing
In, absorption tower is divided into board-like and two big type of packed tower：Packed tower is chiefly used in handling small gas flow, large-minded required when handling
Tower diameter it is big when, because gas-liquid is unevenly distributed can make column efficiency degradation；In addition packed tower also has that pressure drop is big, gas-liquid folder
With it is serious the defects of.In big tower diameter, plate column is inevitable choice, and the area that the efficiency of tower is contacted with liquid-gas is related, at present
Alternative plate column is few in industry, and column efficiency is not high.This patent is exactly to use two the present inventor just to declare
Patent《Semiellipse sieve pore ripple tray》With《A kind of downspout with aft cover plate》Mist folder is reduced to improve gas liquid interfacial area
One idle work of band, to improve tower working efficiency.Two patented technologies are taken in column plate and downspout, theoretically, every
Effectively 20% or more (increase of plate plane) of contact area increase has manufactured non-perpendicular contact to a certain extent on layer column plate
Mode can also increase column efficiency and play the role of eliminating mist.Cause《Semiellipse corrugated sieve column plate》(the present inventor is applying
Patent) most sieve pores in tower be with column plate plane are that non-vertical direction (not only increases mass-transfer efficiency and also effectively reduces
Entrained liquid).Tower is simple to manufacture, and cost and manufacture difficulty are little.Because every layer of column plate is exactly a liquid distribution trough, thus it is not another
If liquid distribution trough.Therefore the tower no liquid distributor therefore liquid of structure are gone directly bottom of tower by tower top, and reducing has liquid distribution
A part of liquid flow of many places inlet tube of device is short, therefore the washing effect in same amount of liquid significantly improves, and makes in downspout
With《A kind of downspout with aft cover plate》Also the patent that the present inventor is applying.This patent is that the present invention enters tower series
One of new idea.
Invention content ellipse ripple sieve-plate tower is completely new tray absorption columns, it is by tower top, tower body and bottom of tower three parts
Composition, wherein influencing maximum to be the exactly completely new invention place of this army of tower body point on column efficiency.Present disclosure：This hair
Bright 1, it is to use《Semiellipse sieve pore ripple tray》(separately apply) be master unit-be from multiple semiellipse tube wave peaks for having beaten hole to
On be welded into plate face, be equipped with 40% or more hole, about 10% tray area of arc string lacked on tower tray, be downflow weir-be
Welding one is perpendicular to the baffle of tower tray on tower tray string, and baffle top is higher than tower tray plane 40-70mm (being known as liquid holdup) in tower tray
The baffle of lower end is downspout；2, it is the patent for using me and applying《A kind of downspout with aft cover plate》(separate case Shen
Please)-and it is that downspout lower part sets aft cover plate, aft cover plate is that the retroflect the tip of the tongue of shape goes out at liquid with column plate upwards in parallel；In downspout
Boom plate is provided with multiple straight half circular holes below makes liquid be flowed out in ridge shape；3, it does not set and holds the gas-liquid contact that liquid zone not only increases 10%
Area also makes the air-flow for holding liquid zone rising be stopped by aft cover plate and switch to be parallel to tower face with decline liquid stream simultaneously by upwardly direction
Row further lifts prolonged action liquid stream rotation sky and horizontal force time, to promoting gas-liquid contact and impact mist to act on.Tower layer
Height is all mutually 40-70cm with tradition.
Manufacture material：Steel；Stainless steel, plastics, plastimets etc..The scope of application；Tower diameter 0.6-5.5m is (preferably
2-4.5m), normal pressure, room temperature.
Specific implementation mode：Oval ripple sieve-plate tower is that novel absorbent tower is by tower top, tower body, bottom of tower three parts group
At.Tower top is that gas vent is connect with pipe flange (see Fig. 1)；Here is demister；It is that inlet tube leads to Ta Nei simultaneously still further below
It is directly punched in the lower half portion of pipe；Tower body is often to save multilayer column plate staggered, master unit column plate is half ellipse by multiple tower sections
Circle ripple sieve tray (separate case) one is welded on steel pipe on the disk of garden by the semiellipse pipe of the long diameter 89-159mm punched and is equipped with 40-
60% hole；It is to weld one on tower tray string that the area that about 10% tower tray of an arc string vacancy has been lacked on tower tray, which is downflow weir one,
Perpendicular to the baffle of tower tray, baffle top is in tower tray lower end higher than tower tray plane 40-70mm (being known as liquid holdup)《A kind of band screening
The downspout of flowing plate》-- it is that downspout lower part sets aft cover plate, aft cover plate is that the retroflect the tip of the tongue of shape goes out at liquid with column plate upwards in flat
Row；Being provided with multiple straight half circular holes below in descending liquid tube string makes liquid be flowed out in ridge shape；Liquid-bearing pan is not set on tower tray.Bottom of tower (see
Fig. 1) top is connected by flange with tower body, is air inlet pipe under connecting flange, into tower in top to the another side of import tower inner wall,
And it is provided with the hole that area is more than air inlet pipe sectional area in the middle and lower part for entering pipe in tower, hole distribution center should be with tower center phase
Together；It is outlet tube still further below, sewage draining exit is equipped in tower bottommost.Description of the drawings：Because the innovation of this patent is in tower body and tower
Top and bottom of tower do not have excessive emphasize.Fig. 1 is the assembling schematic diagram of round Wave screen plate tower, and wherein tower body is more piece multilayer, there is two
Critical piece is completely new：Column plate is《Semiellipse sieve pore ripple tray》；Downspout is《A kind of downspout with aft cover plate》；Tower
Nothing holds liquid zone on plate；Tower top, bottom of tower are to be formulated conventionally；Fig. 2 is《A kind of downspout with aft cover plate》Middle ligulate rolls over (screening) flowing plate
Schematic diagram；Fig. 3 is《Semiellipse sieve pore ripple tray》Schematic diagram.
Note：In figure by aft cover plate be denoted as baffle plate be in order to another kind《Ligulate sieve pore aft cover plate》It distinguishes.
Claims (4)
1. oval ripple sieve-plate tower：It is completely new tray absorption columns, is made of tower top, tower body and bottom of tower three parts：Wherein tower top-
The flange being connect by gas outlet, demister, inlet tube and liquid distributor and with tower body forms；Bottom of tower -- top passes through flange
It is connected with tower body, is that air inlet pipe (arrives the tower inner wall of the another side of import entering top in tower, and entering in tower under connecting flange
The middle and lower part of pipe is provided with the square hole that total sectional area is more than air inlet pipe sectional area, and the hole center centers Ying Yuta are identical)；In air inlet pipe
The outlet tube that lower part is parallel to air inlet pipe is connected to outside tower；It is equipped with sewage draining exit in tower bottommost；Master unit tower body -- it is more
Tower section often saves that have multilayer column plate plate layer height be 40-70mm, and column plate is welded to upside of ellipse pipe with the sieve pore peak for being equipped with 40-60%
At column plate；About 10% tray area of arc string is downflow weir on tower tray -- it is the gear that one is welded on tower tray string perpendicular to tower tray
Plate, baffle top are higher than tower tray plane 40-70mm, and the baffle in tower tray lower end is downspout -- screening (folding) flowing plate is set in lower part,
Aft cover plate is that the retroflect the tip of the tongue of shape goes out at liquid with column plate upwards in parallel；Being provided with multiple half circular holes below in descending liquid tube string makes liquid
Body is flowed out in ridge shape；It does not set and holds liquid zone.
The patent that 2. column plate according to claim 1, which is the present inventor, to be applied《Semiellipse ripple sieve tray》.
The patent that 3. downspout according to claim 1, which is the present inventor, to be applied《A kind of descending liquid with aft cover plate
Pipe》.
4. manufacture material：Steel；Stainless steel, plastics, plastimets etc.；The scope of application；Tower diameter 0.6-5.5 (preferably 2-
4.5m)m；Normal pressure, room temperature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810310201.XA CN108310921A (en) | 2018-03-29 | 2018-03-29 | Oval ripple sieve-plate tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810310201.XA CN108310921A (en) | 2018-03-29 | 2018-03-29 | Oval ripple sieve-plate tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108310921A true CN108310921A (en) | 2018-07-24 |
Family
ID=62897181
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810310201.XA Pending CN108310921A (en) | 2018-03-29 | 2018-03-29 | Oval ripple sieve-plate tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108310921A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2798127C1 (en) * | 2022-10-28 | 2023-06-15 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Ангарский государственный технический университет" | Rotary column mass transfer apparatus |
Citations (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1039362A (en) * | 1988-06-14 | 1990-02-07 | 尤尼-夫瑞克有限公司 | Vapor/liquid contact column structure |
| CN2186593Y (en) * | 1993-11-11 | 1995-01-04 | 李绍通 | Perforated tray with adjustable overflow |
| CN1181282A (en) * | 1997-07-31 | 1998-05-13 | 南京大学 | Mixed box tower plate |
| TW438616B (en) * | 1997-03-03 | 2001-06-07 | Koch Entpr Inc | Improved apparatus for chemical process tower |
| CN2537446Y (en) * | 2001-04-27 | 2003-02-26 | 北京化工大学 | High efficiency guide sieve plate tower |
| CN1978025A (en) * | 2005-12-05 | 2007-06-13 | 中国石油天然气集团公司 | Three-layer efficient high-speed gas-liquid mass transfer tower board |
| CN101327379A (en) * | 2008-07-14 | 2008-12-24 | 天津市创举化工设备有限公司 | Duct downstream spray tray |
| CN101874933A (en) * | 2009-12-03 | 2010-11-03 | 中国石油天然气集团公司 | A Compound Overflow Weir for Promoting Vapor-Liquid Separation |
| CN201618434U (en) * | 2010-04-02 | 2010-11-03 | 天津市北方博隆塔器技术开发有限公司 | Column internals of a tray column |
| CN203737229U (en) * | 2013-12-13 | 2014-07-30 | 江阴市东发机械设备制造有限公司 | Steel-based composite reaction tower |
| CN204093075U (en) * | 2014-07-31 | 2015-01-14 | 南京德邦金属装备工程股份有限公司 | A kind of tower tray with stephanoporate block-resistant plug sawtooth downflow weir |
| CN104722095A (en) * | 2015-04-12 | 2015-06-24 | 万强 | Liquid-accommodation diversion type drop pipe |
-
2018
- 2018-03-29 CN CN201810310201.XA patent/CN108310921A/en active Pending
Patent Citations (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1039362A (en) * | 1988-06-14 | 1990-02-07 | 尤尼-夫瑞克有限公司 | Vapor/liquid contact column structure |
| CN2186593Y (en) * | 1993-11-11 | 1995-01-04 | 李绍通 | Perforated tray with adjustable overflow |
| TW438616B (en) * | 1997-03-03 | 2001-06-07 | Koch Entpr Inc | Improved apparatus for chemical process tower |
| CN1181282A (en) * | 1997-07-31 | 1998-05-13 | 南京大学 | Mixed box tower plate |
| CN2537446Y (en) * | 2001-04-27 | 2003-02-26 | 北京化工大学 | High efficiency guide sieve plate tower |
| CN1978025A (en) * | 2005-12-05 | 2007-06-13 | 中国石油天然气集团公司 | Three-layer efficient high-speed gas-liquid mass transfer tower board |
| CN101327379A (en) * | 2008-07-14 | 2008-12-24 | 天津市创举化工设备有限公司 | Duct downstream spray tray |
| CN101874933A (en) * | 2009-12-03 | 2010-11-03 | 中国石油天然气集团公司 | A Compound Overflow Weir for Promoting Vapor-Liquid Separation |
| CN201618434U (en) * | 2010-04-02 | 2010-11-03 | 天津市北方博隆塔器技术开发有限公司 | Column internals of a tray column |
| CN203737229U (en) * | 2013-12-13 | 2014-07-30 | 江阴市东发机械设备制造有限公司 | Steel-based composite reaction tower |
| CN204093075U (en) * | 2014-07-31 | 2015-01-14 | 南京德邦金属装备工程股份有限公司 | A kind of tower tray with stephanoporate block-resistant plug sawtooth downflow weir |
| CN104722095A (en) * | 2015-04-12 | 2015-06-24 | 万强 | Liquid-accommodation diversion type drop pipe |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2798127C1 (en) * | 2022-10-28 | 2023-06-15 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Ангарский государственный технический университет" | Rotary column mass transfer apparatus |
| RU2799964C1 (en) * | 2022-11-29 | 2023-07-14 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Ангарский государственный технический университет" | Rotary jet mass transfer apparatus |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CA1107634A (en) | Gas-liquid contacting tray with improved inlet bubbling means | |
| US5554329A (en) | Fractionation tray formed by triangular downcomer modules | |
| AU737526B2 (en) | Co-current contacting separation tray design and methods for using same | |
| US4499035A (en) | Gas-liquid contacting tray with improved inlet bubbling means | |
| US5837105A (en) | Co-current contacting separation tray design and methods for using same | |
| CN104324587B (en) | The board-like bubble tower of fine ga(u)ge screen | |
| CN202921125U (en) | Flue gas purification tower | |
| WO1999019054A1 (en) | Method and apparatus for fluid contact | |
| AU3961397A (en) | Chemical process tower deentrainment assembly | |
| US20050280169A1 (en) | Gas-liquid contact tray with fixed valves for mass transfer | |
| CN202751924U (en) | Flue gas cleaning tower | |
| CN110354523A (en) | A kind of New Type of Tray with more microporous bubble covers | |
| US3231251A (en) | Froth disengagement in gas-liquid contact apparatus | |
| US2847083A (en) | Fractionator design | |
| CN101244373A (en) | Cross current type absorption reaction device | |
| CN108905580B (en) | Wet desulfurization tower provided with ridge type tray | |
| US4775499A (en) | Gas-liquid contacting apparatus | |
| CN108310921A (en) | Oval ripple sieve-plate tower | |
| CN108525471A (en) | The tower made of oval ripple sieve tray | |
| CN108452641A (en) | Ellipse head sieve pore cap plate tower | |
| CN108619863A (en) | The tower made of ellipse head sieve pore cap plate | |
| EP0664157A1 (en) | A high-velocity, high capacity mist eliminator and liquid-gas contacting means | |
| CN202876577U (en) | Flue gas purification tower | |
| CN214764486U (en) | Mesh plate for boiler denitration elution tower and boiler denitration elution tower | |
| CN108310793A (en) | Oval ripple sieve tray destilling tower |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20180724 |
|
| WD01 | Invention patent application deemed withdrawn after publication |