CN2201978Y - High-efficiency liquid distributor - Google Patents
High-efficiency liquid distributor Download PDFInfo
- Publication number
- CN2201978Y CN2201978Y CN 92206562 CN92206562U CN2201978Y CN 2201978 Y CN2201978 Y CN 2201978Y CN 92206562 CN92206562 CN 92206562 CN 92206562 U CN92206562 U CN 92206562U CN 2201978 Y CN2201978 Y CN 2201978Y
- Authority
- CN
- China
- Prior art keywords
- liquid distributor
- distributing slot
- groove
- liquid
- millimeter
- 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.)
- Expired - Fee Related
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Abstract
The utility model provides a high-efficiency liquid distributor, comprising a foam separator, a first stage distributing groove, and a second distributing groove. A stainless steel mesh is arranged on a lower liquid outlet of the groove to filter impurity to prevent the fluid bore from being blocked and caused the inhomogeneous distribution, as a result, the defect and the insufficiency of the prior art are solved, wherein, the anti-foam groove, the first stage distributing groove, and the second stage distributing groove are characterized in that the resistance of staining and blocking is strong, the separating rate of the free section is high, and the high-efficiency liquid distributor is suite for a distillation column for pressure reducing operation, particularly a distillation column for dry type pressure reducing operation. The high-efficiency liquid distributor overcomes the problem that entrainment is produced by the secondary gasification in the column. The utility model has the advantages that the product quality can be improved, the collection efficiency can be increased and the pressure can be decreased to achieve the purpose of saving energy.
Description
The utility model relates to a kind of liquid distribution trough of oil product vacuum distillation tower.
Liquid distribution trough is the crucial intraware of packed tower, and the quality of liquid initial distribution in tower directly affects the operating efficiency of packed tower.The at present domestic liquid distribution trough that is used in the oil product destilling tower can be divided into disc type, nozzle formula, calandria etc., do not satisfy the specification requirement of oil product distillation to a certain extent, especially dry type decompression technology, no matter fuel type or lubricated oil type vacuum distillation tower, it is many that it extracts side line out, packed height little (being generally 1.5-2.5 rice), liquid spraying density is little, and the performance of filler is difficult to performance.Show that the filler pressure drop is big in process of production, the energy consumption height easily produces entrainment, and the product degree of overlapping is big, and is of poor quality, and yield is low, and is of poor benefits.Recycle product is carried with pump, and when filling in pipeline, because of disturbance is big, especially decompression operation easily produces a large amount of foams, will influence the normal drainage of distributor cell wall liquid flow hole.
The purpose of this utility model is to provide a kind of efficient liquid distributor, and it is made of foam separator, I and II distributing slot, thereby overcomes the shortcomings and deficiencies of above-mentioned prior art.
The utility model has designed unique foam separator, in the lower liquid exit of its groove stainless steel filtering net is set, and to filter out impurities, prevents that liquid flow hole is blocked, and causes skewness.
The liquid flow hole that is opened in secondary distributing slot side as sediment space, prevents that liquid stream is blocked apart from bottom land 40-100 millimeter.For making liquid spraying point uniform regularly, in the one-level distributing slot, also be provided with two row's catheters, have liquid flow hole in the pipe.The spray design of counting satisfied efficient structured packing 250Y to spray o'clock greater than 300 o'clock/m
2Specification requirement.Owing to flow in the air-flow shunting, reduce pressure and fall, prevent the generation of local liquid flooding.Liquid flow hole is opened at cell wall, and groove is programmable narrow, make distributor free cross-section branch rate greater than the 62%(high efficiency packing require＞50%), satisfied the specification requirement of dry vacuum distillation to liquid distribution trough.
The secondary distributing slot is offered two discharge opeing discharge orifices (on arrange φ 8-12 millimeter, following row φ 2-4 millimeter), has increased operating flexibility, has satisfied the bigger variation for the treatment of capacity, and the design of catheter has guaranteed the drop accurate placement that the cell wall liquid flow hole is discharged, and evenly distributes.
For guaranteeing the influence of groove internal cause liquid level drop to distributing and being caused, design is limited in liquid flow velocity in the groove within 0.2 meter per second.
Hanging beam of the present utility model makes catheter shorten to the distance of draining plate between the tower packing end face, makes the catheter dripping drops avoid the interference of the high velocity air of rising in the tower, guarantees the drop accurate placement, is evenly distributed.In these characteristics also can make filler and distributor in addition part is packed tower into from same manhole, reduce the height of tower, open manhole less, simplified structure, in same installing space, adopt hanging beam can increase the distributor upper space, make the interior uprising gas of tower have enough spaces evenly to be distributed, improve filler efficient.
Fig. 1. the axial cutaway view of packed tower
Fig. 2. the Liquid Distribution in Packed Columns vertical view
Describe the utility model in detail below in conjunction with accompanying drawing: such as Fig. 1,2, the packed tower inwall is fixed with bearing 9,10, one-level distributing slot 2 is connected with bearing 9, and its both sides connect respectively several secondary distributing slots 3, and secondary distributing slot 3 is hung and is fixed on the bearing 10 by hanger 11,12 respectively. The top of I and II distributing slot is provided with foam breaking groove 1, and the below is provided with draining plate 8. I and II distributing slot sidewall is respectively equipped with catheter 6,7, and has upper and lower liquid hole 4,5 on the distribution cell wall in catheter. Draining plate 8 for the annular screen that is obliquely installed at packed tower axis angle at 45 °. One side of foam breaking groove 1 is provided with filter screen 13.
One-level is connected with flange with the secondary distributing slot, and hanger, bearing are equipped with adjusting bolt, and in order to fixing secondary distributing slot, prior being regulates to guarantee the distributor installation level by bolt.
Liquid distribution trough described in the utility model is compared with nozzle type, has and does not stop up, and does not produce the characteristics of entrainment because of secondary vaporizing.
Draining plate and tower axle structure angle at 45 °, behind each catheter whereabouts liquid contact draining plate face, because action of gravitation, on the plate face, can form a parabolic isometric line segment, the slave plate face falls, certainly distribution uniform filling therewith cooperates, and realizes the distribution from point to face, improves the overall efficiency of filler.
The utlity model has good assembling, but outer pre-assembled the checking on the quality of tower body. Its skewness rate is surveyed in cold mould experiment, through adjusting, generally can guarantee to distribute and all spend requirement. Liquid distribution trough structure and its resultant effect of characteristics of installing are the suitableeest oil product vacuum tower, especially the distillation procedure of dry type decompression.
Embodiment: in withdrawing fluid enters foam breaking groove 1, flow into one-level distributing slot 2 behind filter screen 13 foam removal filter residues, liquid enters secondary distributing slot 3 through distributing once more.The I and II distributing slot is communicated with.The liquid liquid hole on catheter again makes liquid segmentation cloth, and liquid falls from catheter 6,7, and accurate, well-regulated dropping on the draining plate 8 makes liquid become the line distribution by point.
Claims (4)
1, a kind of efficient liquid distributor, comprise that I and II distributing slot, draining plate constitute, it is characterized in that: one-level distributing slot 2 both sides connect secondary distributing slot 3 respectively, I and II distributing slot sidewall is respectively equipped with catheter 6,7, and has upper and lower liquid hole 4,5 on the distribution cell wall in catheter; I and II intake chute top is provided with foam breaking groove 1, and the below is provided with draining plate 8.
2, efficient liquid distributor according to claim 1 is characterized in that: secondary distributing slot 3 is hung and is fixed on the bearing 10 by hanger 11,12, can regulate distributing slot by the adjusting bolt of hanger.
3, efficient liquid distributor according to claim 1 is characterized in that: draining plate 8 is the annular screen that tiltedly is provided with packed tower axis angle lapping at 45.
4, efficient liquid distributor according to claim 1 is characterized in that: following discharge opeing discharge orifice is apart from bottom land 40-100 millimeter, and following discharge opeing discharge orifice directly is the 8-12 millimeter, and last discharge opeing discharge orifice directly is the 2-4 millimeter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 92206562 CN2201978Y (en) | 1992-04-13 | 1992-04-13 | High-efficiency liquid distributor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 92206562 CN2201978Y (en) | 1992-04-13 | 1992-04-13 | High-efficiency liquid distributor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2201978Y true CN2201978Y (en) | 1995-06-28 |
Family
ID=33762009
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 92206562 Expired - Fee Related CN2201978Y (en) | 1992-04-13 | 1992-04-13 | High-efficiency liquid distributor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2201978Y (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101785932A (en) * | 2010-03-15 | 2010-07-28 | 无锡市雪浪化工填料有限公司 | Multi-pipe type liquid collection redistributor |
| CN103830928A (en) * | 2012-11-28 | 2014-06-04 | 上海宝钢化工有限公司 | Online adjustment device and method for tear hole of distillation tower |
| CN104225948A (en) * | 2013-06-18 | 2014-12-24 | 中国石化工程建设有限公司 | Online cleaning device and online cleaning method for trench type liquid distributor |
| CN106753508A (en) * | 2017-03-22 | 2017-05-31 | 中国石油大学(华东) | It is a kind of to be classified separate deep vacuum distillation tower |
| CN111214842A (en) * | 2020-02-19 | 2020-06-02 | 宁波巨化化工科技有限公司 | Process and device for removing light components in by-product sulfuric acid |
-
1992
- 1992-04-13 CN CN 92206562 patent/CN2201978Y/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101785932A (en) * | 2010-03-15 | 2010-07-28 | 无锡市雪浪化工填料有限公司 | Multi-pipe type liquid collection redistributor |
| CN103830928A (en) * | 2012-11-28 | 2014-06-04 | 上海宝钢化工有限公司 | Online adjustment device and method for tear hole of distillation tower |
| CN103830928B (en) * | 2012-11-28 | 2016-03-02 | 上海宝钢化工有限公司 | The on-line control device and method of destilling tower drain hole |
| CN104225948A (en) * | 2013-06-18 | 2014-12-24 | 中国石化工程建设有限公司 | Online cleaning device and online cleaning method for trench type liquid distributor |
| CN104225948B (en) * | 2013-06-18 | 2016-04-13 | 中国石化工程建设有限公司 | A kind of on-line cleaning device and method of tank type liquid distributor |
| CN106753508A (en) * | 2017-03-22 | 2017-05-31 | 中国石油大学(华东) | It is a kind of to be classified separate deep vacuum distillation tower |
| CN106753508B (en) * | 2017-03-22 | 2023-12-19 | 中国石油大学(华东) | Pressure-reducing deep drawing tower for fractionation |
| CN111214842A (en) * | 2020-02-19 | 2020-06-02 | 宁波巨化化工科技有限公司 | Process and device for removing light components in by-product sulfuric acid |
| CN111214842B (en) * | 2020-02-19 | 2021-09-24 | 宁波巨化化工科技有限公司 | Process and device for removing light components in by-product sulfuric acid |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |