CN1395976A - Tower plate with defrosting guide structure and no back mix - Google Patents
Tower plate with defrosting guide structure and no back mix Download PDFInfo
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- CN1395976A CN1395976A CN 02128873 CN02128873A CN1395976A CN 1395976 A CN1395976 A CN 1395976A CN 02128873 CN02128873 CN 02128873 CN 02128873 A CN02128873 A CN 02128873A CN 1395976 A CN1395976 A CN 1395976A
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Abstract
A tower plate with defog and current-guide structure and non-getting mixed is composed of tower plate, parallel-flow jet mass-transfer unit consisting of parallel rectangular bodies and partitions to form many sub-units, and defog unit with liquid collector. Its advantages are high efficiency increased by 15%, high processing power increased by 1/4, low pressure drop decreased by 1/3, and non-getting mixed of liquid phase due to reduced gas phase.
Description
Affiliated technical field
The present invention relates to the gas-liquid mass transfer (contact) equipment in the Chemical Engineering, be a kind of band demist guide structure and no back mix column plate specifically, its characteristics for it be by column plate, and stream spray mass transfer unit group and demisting unit group etc. and constitute, the cuboid parallel with the liquid flow path direction constitutes and flows the main body of injection mass transfer unit, each cuboid and stream spray and can add some dividing plates in the mass transfer unit and be divided into several little and streams and spray the mass transfer unit body, the demisting unit group is provided with collecting tank, collect demisting unit and capture the liquid that gets off, it is imported downspout along column plate liquid flow path direction.
Background technology
The plate column of counter current contacting and packed tower are the gas-liquid mass transfer (contact) equipments that extensively adopts at present, and separative efficiency is higher, but disposal ability is limited.Though and the disposal ability of the packed tower unit cross-sectional area of stream contact is very big, its efficient can only reach a mass transfer theory level at most, therefore uses to be very limited.
Chinese patent (ZL 96 1 10153.9) has proposed a kind of parallel jet compounding tower, utilize common adverse current column plate gravity to fall liquid and the local extract of gas, realize the local gas and liquid flowing operation under the overall counter-current operation condition of gas-liquid, thereby realized high flux, high efficiency.Adjacent and the stream of this column plate sprays mass transfer unit " to blowing " phenomenon can take place, and helps strengthening mass transfer under underload, but under high load capacity, big entrainment situation can occur.Be raising parallel jet compounding tower disposal ability, then can address the above problem if between adjacent tray, increase by a cover demister, but structure be too complicated that it is interior than large space to take tower, and investment is very high.And this demister that simply adds, though can reduce entrainment, demister captures the liquid that gets off and falls back again on the column plate, causes backmixing of liquid phase, does not give full play to column efficiency.In addition, the parallel jet compounding tower column plate is circle or square opening, column plate air guide, drain structure lack or effect not remarkable, cause that local resistance is bigger than normal, plate pressure drop is higher.
In addition, the parallel jet compounding tower plate adopts unidirectional or multidirectional open-celled structure, though help the even distribution of liquid layer on the column plate, has also caused the back-mixing of localized liquid simultaneously, is unfavorable for giving full play to plate efficiency.
Summary of the invention
The present invention aims to provide a kind of band demist guide structure and no back mix column plate.The present invention can overcome the deficiencies in the prior art, can effectively eliminate liquid dispersion on the column plate, reduce the liquid phase that gas phase causes and carry secretly and back-mixing, improves plate efficiency and disposal ability and significantly reduces plate pressure drop.The present invention can be used for the gas-liquid mass transfer (contact) equipment in the chemical process, can realize the multistage cocurrent cooling operation of packed tower in this tower, improves production capacity and separative efficiency greatly.
The present invention mainly includes tower body, column plate, downspout, collecting tank, baffle plate, dividing plate, perforate, also stream sprays mass transfer unit group and demisting unit group formation, the cuboid parallel with the liquid flow path direction constitutes and flows the main body of injection mass transfer unit, the demisting unit group is provided with collecting tank, collect demisting unit and capture the liquid that gets off, it is imported downspout along column plate liquid flow path direction.
Each cuboid of the present invention and stream spray and can add some dividing plates in the mass transfer unit and be divided into several little and streams and spray the mass transfer unit body, make that liquid becomes piston flow on the column plate, avoid the generation of liquid dispersion phenomenon on the column plate, can improve plate efficiency more than 15%.
The present invention can effectively eliminate the parallel jet compounding tower plate and produce entrainment greatly owing to adjacent and stream spray mass transfer unit " to blowing " under high gas speed, and demisting unit is provided with collecting tank, collect demisting unit and capture the liquid that gets off, it is imported downspout along column plate liquid flow path direction.This band demist guide structure and no back mix column plate has reduced that liquid phase is carried secretly and back-mixing, has improved plate efficiency, and the more common parallel jet compounding tower plate of disposal ability improves more than 1/4.And flow-guiding structure is adopted in the column plate perforate, significantly reduces plate pressure drop, and the more common parallel jet compounding tower plate of plate pressure drop reduces more than 1/3.Band demist guide structure and no back mix column plate provided by the invention can be used for the gas-liquid mass transfer (contact) equipment in the chemical process, can realize the multistage cocurrent cooling operation of packed tower in this tower, improves production capacity and separative efficiency greatly,
Band demist guide structure and no back mix column plate provided by the invention is very suitable for normal pressure to occasions such as pressurizing absorption, rectifying, heat exchange.
Description of drawings
Fig. 1 is common parallel jet compounding tower figure.
Fig. 2 is that common parallel jet compounding tower plate and stream spray mass transfer unit and perforate layout viewing.
Fig. 3 is band demist guide structure and no back mix column plate figure.
Fig. 4 is a band demist guide structure and no back mix column plate perforate layout viewing one.
Fig. 5 is a band demist guide structure and no back mix column plate perforate layout viewing two.
Fig. 6 is a band demist guide structure and no back mix column plate perforate layout viewing three.
Fig. 7 is entrainment figure under the common parallel jet compounding tower plate hight gas speed.
Fig. 8～Figure 11 is different types band demist guide structure and no back mix column plate demist mechanism figure.
Figure 12 is the drain structure chart of various structural shapes.
Figure 13 is demisting unit and collecting tank integral structure figure.
Figure 14 is the demisting unit figure of different structure type.
Figure 15 is the flow-guiding structure perforate pattern figure of different structure.
Figure 16 is that a kind of band demist guide structure and no back mix column plate of typical structure is connected and fixed pattern figure.
Figure 17 is column plate, fixed head, also stream injection mass transfer unit is connected and fixed pattern figure.
Figure 18 is that column plate, fixed head are connected and fixed pattern figure.
The specific embodiment
Specific embodiments of the present invention are described in detail as follows with reference to accompanying drawing:
As shown in Figure 3, band demist guide structure and no back mix column plate provided by the invention, mainly comprise tower body 1, downspout 2, and stream spray mass transfer unit 3, column plate 4, demisting unit 5, collecting tank 6, baffle plate 7, extract pipe 8, dividing plate 9 and perforate 10 etc. and partly constitute.
Though comparing with common valve plate, parallel jet compounding tower plate as shown in Figure 1 has higher efficient and disposal ability, but unidirectional or multidirectional perforate is adopted in its column plate perforate, and stream injection mass transfer unit adopts circle or square structure more, perforate is arranged as shown in Figure 2, triangularity or parallelogram are arranged on column plate, this staggered perforate is with all directions of the guiding fluid column plate of extract pipe lifting, though help liquid on the uniform distribution column plate, but also destroyed column plate self liquid flowing state simultaneously, cause backmixing of liquid phase, reduce plate efficiency and disposal ability.
As shown in Figure 3, band demist guide structure and no back mix column plate provided by the invention, adopt the cuboid parallel to constitute and flow the main body of injection mass transfer unit 3 with the liquid flow path direction, each cuboid and stream spray and can add some dividing plates 9 in the mass transfer unit 3 and be divided into several little and streams and spray the mass transfer unit body, make that liquid becomes piston flow on the column plate, avoided the generation of liquid dispersion phenomenon on the column plate, can effectively improve plate efficiency and reach more than 10%.
As shown in Figure 4, band demist guide structure and no back mix column plate provided by the invention, parallel, linearly aligned perforate 10 structures can be adopted, the perforate 10 of rectangle, circle, rhombus, square, ellipse, various how much patterns such as trapezoidal can be adopted with the liquid flow path direction.
As shown in Figure 5, the adjacent apertures parallel with the liquid flow path direction 10 can be merged into the bar shaped open-celled structure.
As shown in Figure 6, can also utilize two slits between the column plate to constitute the perforate 10 of column plate.
" to blowing " phenomenon under high operating gas velocity, can take place owing to adjacent and stream spray mass transfer unit in parallel jet compounding tower plate as shown in Figure 1, big entrainment situation (as shown in Figure 7) can occur.
As shown in Figure 8, owing to entrainment adjacent and that stream injection mass transfer unit " to blowing " causes is captured by the demisting unit 5 of column plate provided by the invention, and assemble on demisting unit 5, formation bulky grain drop flows in the collecting tank 6 along demisting unit 5.Because an end of collecting tank 6 is provided with baffle plate 7, makes liquid to enter downspout 2 along column plate liquid flow path direction, avoid being caused backmixing of liquid phase, the reduction plate efficiency by the liquid that demisting unit the captures column plate that falls back.Because demisting unit 5 this demist effects, the disposal ability that can improve the parallel jet compounding tower plate reaches more than 1/4, because the minimizing of entrainment under the high gas speed, and the reducing of backmixing of liquid phase, plate efficiency can improve more than 15%.
As Fig. 3, shown in Figure 8, demisting unit 5 of the present invention can be positioned at and flow the top of spraying mass transfer unit 3, it can be made of the silk screen of all size, the expanded metals of all size, the sieve plate of all size, the deflection plate of all size, the eddy flow plate of all size, or the combination of above-mentioned various structures, its quantity can be 0～20 layer.
As Fig. 9, shown in Figure 10, demisting unit 5 of the present invention also can be made up of above-mentioned various structures equally in the bottom of column plate 4, or their combination.
Fig. 9 can adopt the high band iron of 10～160mm as baffle plate for adopting the Defrosting structure of baffle forms, in the drop importing collecting tank 6 under will removing.
Figure 10 can adopt above-mentioned various structure to form for adopting the Defrosting structure of flap form, and the drop under it removes is directed to the bottom of flap, imports in the collecting tank 6.
Figure 11 is for adopting the demisting unit of a separate unit structural shape, and it is also between stream injection mass transfer unit 3 and the column plate 4.
As shown in figure 12, collecting tank 6 of the present invention can be an absolute construction; Or as shown in figure 13, with the demisting unit combining structure, according to concrete application scenario, demisting unit can organically be integrated with collecting tank; Also can be as shown in Figure 8, collecting tank 6 is and flows a part of spraying mass transfer unit 3 that promptly also stream sprays the cover plate of mass transfer unit 3.The structural shape of collecting tank 6 can be various forms such as trapezoidal, square, V font, circle or ellipse.
As Figure 13, shown in Figure 14, demisting unit 5 can be the circular arc corrugated board structures, also can adopt flap shape structure or level board structure.
Column plate perforate 10 of the present invention can be adopted common perforate pattern, and as circle, square, rectangle, ellipse, rhombus, perforate pattern such as trapezoidal, perforate can be common punching structure, also can be the open-celled structure of band lead angle.But above-mentioned perforate pattern causes local resistance bigger than normal, the more high defective of plate pressure drop because air guide, drain structure shortage or effect are not remarkable.As shown in figure 15, band demist guide structure and no back mix column plate of the present invention can adopt the flow-guiding structure open-cellular form, and flow-guiding structure can be circular arc (as shown in Figure 8), hypotenuse shape or flanging shape structural shapes such as (as shown in figure 15).This flow-guiding structure open-cellular form is compared with common perforate pattern, and it can significantly reduce the gas access resistance, reduces plate pressure drop and reaches more than 1/3.
Adopt Fig. 5, bar shaped open-celled structure shown in Figure 6, can effectively improve open ratio of plate, improve the column plate disposal ability more than 30%.
Figure 16, Figure 17, Figure 18 provide a kind of band demist guide structure and no back mix tower plate structure sketch of typical structure.Column plate provided by the invention can adopt the adjacent tray combinational gap to constitute the perforate of column plate, adopt limiting plate adjustment and fixedly perforate size, connection between the column plate can be by adopting bolt to be connected with also flowing the injection mass transfer unit, and column plate integral body is removable structure, is convenient to piecemeal and assembles and overhaul.
Band demist guide structure and no back mix column plate provided by the invention can except that also flowing the perforate of injection mass transfer unit correspondence position, can also be offered sieve aperture, the pilot hole of all size, the float valve of all size of perhaps arranging according to concrete operating mode and needs on column plate.
Below by concrete Application Example the present invention is made an explanation, but for illustrative purposes only rather than the restriction the present invention.
Application Example:
In φ 1200 experiment towers, under the normal pressure, adopt air, water thing to carry out cold mould experiment, Ta Nei establishes 2 layers of common single overflow parallel jet compounding tower plate and 2 layers of single overflow band demist guide structure and no back mix column plate have carried out the contrast experiment.
Common single overflow parallel jet compounding tower plate structure parameter is as follows:
Single overflow band demist guide structure and no back mix tower plate structure parameter is as follows:
Regulate the gas-liquid flow, the maintenance fluid flow is 60m
3/ h measure the plate pressure drop under the different gas phase loads of two kinds of column plates, and the maximum of two kinds of column plates allows the void tower F factor.
The contrast experiment one, and fluid flow is 60m
3/ h, the following two kinds of plate pressure drops contrast of identical empty tower gas velocity:
The contrast experiment two, and fluid flow is 60m
3/ h, two kinds of maximum void tower F factors that allow of column plate:
| The column plate pattern | Plate pressure drop, mmH 2O |
| Common single overflow parallel jet compounding tower plate | ????106 |
| Single overflow band demist guide structure and no back mix column plate | ????78 |
| The column plate pattern | The maximum void tower F factor that allows |
| Common single overflow parallel jet compounding tower plate | ????2.8 |
| Single overflow band demist guide structure and no back mix column plate | ????3.6 |
By above-mentioned contrast experiment as can be seen, under the identical operations working condition, band demist guide structure and no back mix column plate is compared with common parallel jet compounding tower plate, and plate pressure drop has reduced:
(106-78)/78×100％＝35.9％
Under the identical operations working condition, band demist guide structure and no back mix column plate is compared with common parallel jet compounding tower plate, and the column plate disposal ability has improved:
(3.6-2.8)/2.8×100％＝28.5％
Can reach a conclusion thus, band demist guide structure and no back mix column plate is compared with common parallel jet compounding tower plate, has the advantage that pressure drop is low, treating capacity is big, is the good mass transfer of a kind of application prospect, heat transfer member.
Claims (10)
1, a kind of band demist guide structure and no back mix column plate, it is characterized in that it mainly includes tower body, column plate, downspout, collecting tank, baffle plate, dividing plate, perforate, also stream sprays mass transfer unit group and demisting unit group formation, the cuboid parallel with the liquid flow path direction constitutes and flows the main body of injection mass transfer unit, the demisting unit group is provided with collecting tank, collect demisting unit and capture the liquid that gets off, it is imported downspout along column plate liquid flow path direction.
2,, it is characterized in that to add in said and the stream injection mass transfer unit some dividing plates and be divided into several little also stream injection mass transfer unit bodies according to the said band demist of claim 1 guide structure and no back mix column plate.
3, according to the said band demist of claim 1 guide structure and no back mix column plate, it is characterized in that said demisting unit can be positioned at and flow injection mass transfer unit top, also can be in column plate bottom, or separate unit and stream spray between mass transfer unit and the column plate.
4, according to the said band demist of claim 1 guide structure and no back mix column plate, it is characterized in that said demisting unit can be made of silk screen, expanded metals, sieve plate, deflection plate, baffle plate or eddy flow plate etc., or the combination of above-mentioned various structures.
5, according to the said band demist of claim 1 guide structure and no back mix column plate, it is characterized in that said collecting tank can be an absolute construction, or with the demisting unit combining structure, or also flow a part of spraying mass transfer unit, also collecting tank and demisting unit organically can be integrated.
6, according to the said band demist of claim 1 guide structure and no back mix column plate, it is characterized in that said column plate perforate can adopt common perforate pattern, also can adopt the flow-guiding structure open-cellular form.
7,, it is characterized in that said flow-guiding structure can be circular arc, hypotenuse shape or flanging shape structural shape according to the said band demist of claim 6 guide structure and no back mix column plate.
8, according to the said band demist of claim 1 guide structure and no back mix column plate, it is characterized in that said column plate is except that also flowing the perforate of injection mass transfer unit correspondence position, can also on column plate, offer sieve aperture, the pilot hole of all size, the float valve of all size of perhaps arranging.
9,, it is characterized in that said column plate perforate can adopt two combinational gaps between the column plate to constitute according to the said band demist of claim 1 guide structure and no back mix column plate.
10,, it is characterized in that the connection between one deck column plate can connect by the mass transfer unit assembling according to the said band demist of claim 1 guide structure and no back mix column plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021288739A CN1179773C (en) | 2002-08-19 | 2002-08-19 | Tower plate with defrosting guide structure and no back mix |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB021288739A CN1179773C (en) | 2002-08-19 | 2002-08-19 | Tower plate with defrosting guide structure and no back mix |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1395976A true CN1395976A (en) | 2003-02-12 |
| CN1179773C CN1179773C (en) | 2004-12-15 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB021288739A Expired - Fee Related CN1179773C (en) | 2002-08-19 | 2002-08-19 | Tower plate with defrosting guide structure and no back mix |
Country Status (1)
| Country | Link |
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| CN (1) | CN1179773C (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100428976C (en) * | 2005-12-06 | 2008-10-29 | 中国石油天然气集团公司 | Vapour-liquid mass transfering method without amplifying effect |
| CN101507883B (en) * | 2009-02-23 | 2010-12-29 | 天津市创举科技有限公司 | Film spray no-back mixing column plate |
| CN105194951A (en) * | 2015-10-29 | 2015-12-30 | 徐州天正活性炭厂 | Activated carbon production tail gas purification device and purification method |
| CN107158733A (en) * | 2017-06-06 | 2017-09-15 | 淮阴工学院 | A kind of acetic acid rectifying column of good separating effect |
| WO2018094562A1 (en) * | 2016-11-22 | 2018-05-31 | 南通苏通分离工程科技有限公司 | Downcomer corrugated wire mesh defoaming device |
| CN111989144A (en) * | 2018-03-29 | 2020-11-24 | 环球油品有限责任公司 | Vapor-liquid contacting apparatus and method employing offset contacting modules |
| CN114828977A (en) * | 2019-12-17 | 2022-07-29 | 英力士乙酰英国有限公司 | Separation method and apparatus |
-
2002
- 2002-08-19 CN CNB021288739A patent/CN1179773C/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100428976C (en) * | 2005-12-06 | 2008-10-29 | 中国石油天然气集团公司 | Vapour-liquid mass transfering method without amplifying effect |
| CN101507883B (en) * | 2009-02-23 | 2010-12-29 | 天津市创举科技有限公司 | Film spray no-back mixing column plate |
| CN105194951A (en) * | 2015-10-29 | 2015-12-30 | 徐州天正活性炭厂 | Activated carbon production tail gas purification device and purification method |
| WO2018094562A1 (en) * | 2016-11-22 | 2018-05-31 | 南通苏通分离工程科技有限公司 | Downcomer corrugated wire mesh defoaming device |
| CN107158733A (en) * | 2017-06-06 | 2017-09-15 | 淮阴工学院 | A kind of acetic acid rectifying column of good separating effect |
| CN107158733B (en) * | 2017-06-06 | 2019-11-08 | 淮阴工学院 | A kind of acetic acid rectifying column of good separating effect |
| CN111989144A (en) * | 2018-03-29 | 2020-11-24 | 环球油品有限责任公司 | Vapor-liquid contacting apparatus and method employing offset contacting modules |
| CN114828977A (en) * | 2019-12-17 | 2022-07-29 | 英力士乙酰英国有限公司 | Separation method and apparatus |
| CN114828977B (en) * | 2019-12-17 | 2024-05-07 | 英力士乙酰英国有限公司 | Separation method and apparatus |
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| Publication number | Publication date |
|---|---|
| CN1179773C (en) | 2004-12-15 |
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Granted publication date: 20041215 |