CN1613532A - Vapor-liquid mixed high-efficient mass transferring tray with liquid-phase zoning cross current flow - Google Patents
Vapor-liquid mixed high-efficient mass transferring tray with liquid-phase zoning cross current flow Download PDFInfo
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- CN1613532A CN1613532A CN 200410072053 CN200410072053A CN1613532A CN 1613532 A CN1613532 A CN 1613532A CN 200410072053 CN200410072053 CN 200410072053 CN 200410072053 A CN200410072053 A CN 200410072053A CN 1613532 A CN1613532 A CN 1613532A
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- liquid
- tower tray
- tray
- column plate
- downspout
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
An efficient mass-transfer tower tray for sufficient mixing between steam and liquid features that the tower tray is divided into parallel strip regions with same pitch by the partitions, each strip region has a down-flow spout at its one end and a liquid collecting tray, and adjacent two strip regions have alternatively down-flow spout and liquid collecting tray at same ends. Its advantages are high steam-liquid distribution uniformity and high mass transfer efficiency.
Description
Technical field
The present invention relates to a kind of abundant mixed high-efficient mass transferring tower tray of vapour-liquid of liquid phase subregion cross-flow passes, belong to mass transfer, the heat transfer tower internals structure technology of rectifying, absorption and desorb etc.
Background technology
Vapour-liquid mass equipment mainly is divided into plate column and packed tower two big classes.Because plate column is simple in structure, with low cost, be easy to amplify and possessed the experience of comparative maturity in design and operating aspect, therefore the main equipment on current industrial is still based on plate column.But it is less that its flux ratio is compared in plate column and efficient structured packing, and efficient is also lower.Its general form is for being provided with seal pot and the downspout access way as liquid phase respectively at the column plate two ends, gas phase is entered by the gas phase channel that is certain distribution form on the column plate (sieve aperture, bubble-cap, float valve, spray-hole) and contact the generation effect of mass transmitting with liquid phase.
Find Liquid Flow distribution appreciable impact mass-transfer efficiency by mass transport process under the different condition for imports being carried out analog computation with CFD.As seen from Figure 2, the even more mass-transfer efficiency of vapour-liquid distribution is high more.Because all liquid phase stream is to identical, so the CONCENTRATION DISTRIBUTION trend of liquid phase is to be reduced gradually to outlet by import, so its mass-transfer efficiency also reduces gradually on traditional single downspout column plate.Corresponding with the CONCENTRATION DISTRIBUTION of liquid phase, also there is identical trend in gas phase.Thereby make the import department skewness of gas-liquid,, also can only guarantee high efficiency (as the Case2 among Fig. 2) near the minority column plate of import department even consequently take measures to make the import department of tower to be evenly distributed at upper and lower layer column plate.And for the non-aperture area of larger-diameter tower at close tower wall, because gas phase is less to the perturbation action of liquid phase, the lower stagnant area of mass-transfer efficiency can appear, this also is a lower reason of conventional tower plate efficiency.
Summary of the invention
In order to overcome the lower shortcoming of the especially large-scale column plate mass-transfer efficiency of traditional column plate, the object of the present invention is to provide a kind of abundant mixed high-efficient mass transferring tower tray of vapour-liquid of liquid phase subregion cross-flow passes, this tower tray phase concentrations after keeping gas-liquid by column plate evenly distributes, thereby improves mass-transfer efficiency.
The present invention is realized by following technical proposals, the abundant mixed high-efficient mass transferring tower tray of a kind of vapour-liquid of liquid phase subregion cross-flow passes, it is characterized in that, at sieve tray, on valve plate or the ejection-type column plate, adopt demarcation strip that column plate is divided into the parallel striped interval that spacing equates or do not wait, the end between each slab region is provided with downspout, the other end is provided with seal pot, alternate downspout and the seal pot of being provided with of the same end in two adjacent bar shaped intervals.
Above-mentioned demarcation strip height is 100-200mm;
At least 4 in parallel striped interval on the above-mentioned tower tray, every bar shaped interval width is 200-400mm;
Above-mentioned downspout is circle, rectangle, triangle or D font.
Offer saw shape tooth above the above-mentioned seal pot.
Above-mentioned demarcation strip is welded on the column plate or by screw and is connected on the column plate.
The invention has the beneficial effects as follows, thereby can under the prerequisite that keeps simple this advantage of column plate original structure, make the more even mass-transfer efficiency that significantly improves of vapour-liquid distribution.
Description of drawings
Fig. 1 is a structural representation of the present invention.
Among the figure: 1. seal pot, 2. downspout, 3. exit weir, 4. dividing plate, 5. bolts and nuts.
Fig. 2 is the plate efficiency curve map of 20 sieve-plate towers and the plate efficiency curve map of 20 tower tray towers of the present invention.Among the figure: E
MVBe gas phase Merphree efficient, n is the tower tray sequence number; ■-Casel is the mass-transfer efficiency curve of tower of the present invention; -Case2 is the mass-transfer efficiency curve of sieve-plate tower.
The specific embodiment
Under the situation of tray diameter less than 800mm, adopt that tower tray is whole to be made, after promptly parts such as the gas phase channel on the tower tray, downspout, seal pot and exit weir and demarcation strip are made whole tower tray by scheme between slab region, be directly welded in the tower; Under the situation of tray diameter greater than 800mm, adopt the manufacturing of tower tray piecemeal, the parts such as downspout, seal pot, exit weir, dividing plate that are every slab region manufacture one separately, and then each slab region part that will make welds in tower or is connected to become whole tower tray with bolts and nuts.
The tower tray of the present invention that now with the tray diameter is 2440mm is embodiment, the present invention is described in detail: the gas-liquid bubbling area is divided into 7 intervals on the column plate, the interval width in 5 intervals is 360mm wherein, and both sides arch area interval width is 300mm, dividing plate height 200mm.Seal pot on this tower tray is accepted the dirty liquid phase of last layer tower tray downspout in the tower, so, liquid phase flow direction in each slab region on this tower tray, flow by the direction of seal pot 1 to downspout 2, the liquid phase of whole each slab region of tower tray is to form overall cross-flow passes, and liquid phase is distributed in the less zone like this, make flow with mix more even, and each slab region all has bigger gas phase circulation area, thus effectively eliminate large-scale column plate intrinsic inefficient stagnant area.The subregion cross-flow passes of liquid makes the gas phase of adjacent area mix, and makes the CONCENTRATION DISTRIBUTION of gas between plate very even.Can guarantee that like this import and export condition that whole tower is respectively pulled is in desirable situation, make each plate efficiency all maintain higher level, the bi-component medium that Casel among Fig. 2 has provided with relative volatility 1.25 carries out plate efficiency calculating, and the efficient of tower tray of the present invention improves more than 20% than the efficient of common column plate as can be seen.
Claims (6)
1, the abundant mixed high-efficient mass transferring tower tray of a kind of vapour-liquid of liquid phase subregion cross-flow passes, it is characterized in that: at sieve tray, on valve plate or the ejection-type column plate, adopt demarcation strip that column plate is divided into the parallel striped interval that spacing equates or do not wait, end between each slab region is provided with downspout, the other end is provided with seal pot, alternate downspout and the seal pot of being provided with of the same end in two adjacent bar shaped intervals.
2, by the described tower tray of claim 1, it is characterized in that: the demarcation strip height is 100-200mm.
3, by the described tower tray of claim 1, it is characterized in that: the parallel striped interval is at least 4 on the tower tray, and every bar shaped interval width is 200-400mm.
4, by the described tower tray of claim 1, it is characterized in that: downspout is circle, rectangle, triangle or D font.
5, by the described tower tray of claim 1, it is characterized in that: offer saw shape tooth above the seal pot.
6, by the described tower tray of claim 1, it is characterized in that: demarcation strip is welded on the column plate or by screw and is connected on the column plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200410072053 CN1256162C (en) | 2004-09-22 | 2004-09-22 | Vapor-liquid mixed high-efficient mass transferring tray with liquid-phase zoning cross current flow |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200410072053 CN1256162C (en) | 2004-09-22 | 2004-09-22 | Vapor-liquid mixed high-efficient mass transferring tray with liquid-phase zoning cross current flow |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1613532A true CN1613532A (en) | 2005-05-11 |
| CN1256162C CN1256162C (en) | 2006-05-17 |
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ID=34765187
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200410072053 Expired - Fee Related CN1256162C (en) | 2004-09-22 | 2004-09-22 | Vapor-liquid mixed high-efficient mass transferring tray with liquid-phase zoning cross current flow |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1256162C (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103100351A (en) * | 2011-11-10 | 2013-05-15 | 中国石油化工股份有限公司 | Gas-liquid distribution plate capable of reducing horizontal susceptibility |
| CN103372326A (en) * | 2012-04-18 | 2013-10-30 | Ifp新能源公司 | Partitioned distributor tray for offshore gas/liquid contact column |
| CN103432764A (en) * | 2013-08-05 | 2013-12-11 | 北京泽华化学工程有限公司 | Multi-downcomer tower tray and plate tower provided with multi-downcomer tower tray |
-
2004
- 2004-09-22 CN CN 200410072053 patent/CN1256162C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103100351A (en) * | 2011-11-10 | 2013-05-15 | 中国石油化工股份有限公司 | Gas-liquid distribution plate capable of reducing horizontal susceptibility |
| CN103100351B (en) * | 2011-11-10 | 2015-04-15 | 中国石油化工股份有限公司 | Gas-liquid distribution plate capable of reducing horizontal susceptibility |
| CN103372326A (en) * | 2012-04-18 | 2013-10-30 | Ifp新能源公司 | Partitioned distributor tray for offshore gas/liquid contact column |
| CN103372326B (en) * | 2012-04-18 | 2016-05-11 | Ifp新能源公司 | For the subregion distributor tower tray of marine gas/liquid contact tower |
| CN103432764A (en) * | 2013-08-05 | 2013-12-11 | 北京泽华化学工程有限公司 | Multi-downcomer tower tray and plate tower provided with multi-downcomer tower tray |
| US9919239B2 (en) | 2013-08-05 | 2018-03-20 | Beijing Zehua Chemical Engineering Co., Ltd. | Multiple downcomer tray and tray column comprising the same |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1256162C (en) | 2006-05-17 |
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