CN2928215Y - Gas-liquid distributor - Google Patents
Gas-liquid distributor Download PDFInfo
- Publication number
- CN2928215Y CN2928215Y CN 200620084866 CN200620084866U CN2928215Y CN 2928215 Y CN2928215 Y CN 2928215Y CN 200620084866 CN200620084866 CN 200620084866 CN 200620084866 U CN200620084866 U CN 200620084866U CN 2928215 Y CN2928215 Y CN 2928215Y
- Authority
- CN
- China
- Prior art keywords
- gas
- distributor
- liquid
- hydrogen sulfide
- seal pot
- 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
Links
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- Gas Separation By Absorption (AREA)
Abstract
The utility model discloses a gas-liquid distributor comprising a gas distributor, a liquid distributor, a liquid disk, an overflow plate, and a gas rising tube, characterized in that the gas rising tube is equipped in the gas distributor. When passing through the liquid disk connected with the gas distributor, the gas in the pipe passes through the liquid flowing via the liquid distributor, thereby realizing multi-staged hydrogen sulfide removal, overcoming the drawbacks existed in the traditional packed tower hydrogen sulfide removal technology, and achieving an exact desulfuration effect. The utility model is low in energy consumption and operation cost, simple in manufacture, easy for maintenance, and can be widely applied in technical domain of chemistry-used hydrogen sulfide removing device manufacturing.
Description
Technical field
The utility model relates to the machinery manufacturing technology field that removes of chemical gases hydrogen sulfide, especially a kind of gas-liquid distributor.
Background technology
Existing chemical industry desulfurizing tower mostly is packed tower, promptly at the inner filling of tower two sections or three sections fillers, various chemical gases contact the pernicious gas hydrogen sulfide that removes in the chemical gases through packing layers with alkali lye under the sprinkle of top, in use, because gas-liquid contact time is long, the gas-liquid contact is inhomogeneous, causes carbon dioxide to produce serious the interference to removing hydrogen sulfide, cause desulfurized effect poor, the content of hydrogen sulfide is many at 15mg/m in the gas after removing
3More than, seriously restrict stability and safety, the low consumption operation of Chemical Manufacture, and stifled easily tower, overhaul time-consuming.
Summary of the invention
The purpose of this utility model is to remove the drawback that the hydrogen sulfide technological facilities exists at above-mentioned tradition, and provides a kind of gas-liquid contact evenly that time of contact is short, and desulfurized effect is definite, low power consuming, and operating cost is low, not stifled tower, gas-liquid distributor easy to maintenance.
For realizing above-mentioned technical purpose, the utility model has been taked following technical scheme: a kind of gas-liquid distributor, mainly by riser, gas distributor, liquid distribution trough, overflow plate, seal pot constitutes, it is characterized in that: riser is located in the gas distributor of cylinder or polygonal cylinder, seal pot is installed in the gas distributor lower end, liquid distribution trough is connected with seal pot, overflow plate is installed in a side of gas distributor, junction at riser and seal pot, be provided with a plurality of circular holes, the side of gas distributor is provided with a plurality of pores, gas distributor, seal pot, liquid distribution trough, overflow plate all is fixed on the bracing frame.When riser rises up into gas distributor, contact with the alkali lye in being flowing in seal pot, sulphur body hydrogen in the gas is removed in gas-liquid distributor, and back gas enters lower floor's gas-liquid distributor through overflow plate again and carries out identical secondary gas filtration, realizes the absorbing and removing once more of hydrogen sulfide.
Owing to take technique scheme, the utility model is compared with the tower technology that removes hydrogen sulfide of traditional filler, and it is effective to have a hydrogen sulfide stripping, and operating cost is low, low energy consumption, stifled tower, significantly technological merit such as easy to maintenance.The equipment manufacturing technology field that can be widely used in hydrogen sulfide stripping in the chemical industry.
Description of drawings
Fig. 1 is the utility model overall structure schematic diagram
Fig. 2 is that the utility model A is to topology view
1 liquid cloth device, 2 gas distributors, 3 overflow plates, 4 seal pots, 5 supports, 6 riseies, 7 holes, 8 circular ports among the figure
The specific embodiment
It is shown in Figure 2 to press Fig. 1, riser 6 is located in the gas distributor 2, seal pot 4 is installed in the lower end of gas distributor 2, liquid distribution trough 1 is connected with seal pot 4, overflow plate 3 is installed in a side of air distributor 2, be provided with a plurality of circular holes 8 in riser 6 and seal pot 4 junctions, the side of gas distributor is provided with a plurality of pores 7.Gas distributor 2, seal pot 4, liquid distribution trough 1, overflow plate 3 are installed on the bracing frame 5.
Claims (2)
1, a kind of gas-liquid distributor, form by riser (6), gas distributor (2), liquid distribution trough (1), overflow plate (3), seal pot (4), support (5), it is characterized in that: described riser (6) is located in the gas distributor (2), seal pot (4) is installed in the lower end of gas distributor (2), liquid distribution trough (1) is connected with seal pot (4), and overflow plate (3) is installed in a side of gas-liquid distributor (2); Described air distributor (2), seal pot (4), liquid distribution trough (1), overflow plate (3) are installed on the bracing frame (5).
2, according to the described a kind of gas-liquid distributor of claim 1, it is characterized in that: described junction at riser (6) and seal pot (4) is provided with a plurality of circular holes (8); One side of described gas distributor (2) is provided with a plurality of pores (7); Described gas distributor (2) is cylinder or polygonal cylinder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620084866 CN2928215Y (en) | 2006-05-24 | 2006-05-24 | Gas-liquid distributor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620084866 CN2928215Y (en) | 2006-05-24 | 2006-05-24 | Gas-liquid distributor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2928215Y true CN2928215Y (en) | 2007-08-01 |
Family
ID=38306608
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620084866 Expired - Fee Related CN2928215Y (en) | 2006-05-24 | 2006-05-24 | Gas-liquid distributor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2928215Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105983321A (en) * | 2015-01-31 | 2016-10-05 | 中国石油化工股份有限公司 | Ammonia neutralization device and method |
| CN106215668A (en) * | 2016-09-27 | 2016-12-14 | 长春东狮科贸实业有限公司 | A kind of desulfurizing tower |
-
2006
- 2006-05-24 CN CN 200620084866 patent/CN2928215Y/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105983321A (en) * | 2015-01-31 | 2016-10-05 | 中国石油化工股份有限公司 | Ammonia neutralization device and method |
| CN105983321B (en) * | 2015-01-31 | 2018-04-06 | 中国石油化工股份有限公司 | In ammonia and device and neutralization method |
| CN106215668A (en) * | 2016-09-27 | 2016-12-14 | 长春东狮科贸实业有限公司 | A kind of desulfurizing tower |
| CN106215668B (en) * | 2016-09-27 | 2018-10-30 | 长春东狮科贸实业有限公司 | A kind of desulfurizing tower |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070801 |