CN204973148U - Gas -liquid separation tower - Google Patents
Gas -liquid separation tower Download PDFInfo
- Publication number
- CN204973148U CN204973148U CN201520430623.2U CN201520430623U CN204973148U CN 204973148 U CN204973148 U CN 204973148U CN 201520430623 U CN201520430623 U CN 201520430623U CN 204973148 U CN204973148 U CN 204973148U
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- CN
- China
- Prior art keywords
- tower body
- gas
- liquid separation
- intake duct
- tower
- 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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- Gas Separation By Absorption (AREA)
Abstract
The utility model discloses a gas -liquid separation tower, including the tower body, the tower body lower part is equipped with the intake duct, the top of intake duct is equipped with the perforated sieve board, the top of perforated sieve board is equipped with multilayer defogging packing layer, tower body upper portion is equipped with the gas outlet, the tower body bottom is equipped with the valve that drains, the intake duct is for admitting air along tower body inner wall tangential, and air distributor is the horn mouth structure in the tower body, tower body upper portion is equipped with the multilayer shower, is equipped with spiral nozzle on the shower. The utility model discloses an effectively liquid in the separation bubble, and simple process, strong, the easy washing of corrosion resistance, easy maintenance.
Description
Technical field
The utility model relates to field of chemical equipment, is specifically related to a kind of gas-liquid separation tower.
Background technology
Gas-liquid separation tower is that one is applied to water-oil separating, the separator in the places such as dedusting and liquid removal impurity, similar pressure vessel of gas-liquid separation tower, inside is provided with relevant air inlet component and liquid capture component, saturated gas is in cooling or pressure process, part condensated gas cognition is gone into drop and is flowed with gas, time in the container entering sudden enlargement, flow velocity reduces rapidly, in the process that main fluid turns to, the trickle dropping liquid of a part in gas phase sinks, another part enters liquid capture component and to condense further sinking, finally reach the effect of gas-liquid separation.
Chemical enterprise in process of production; usually can discharge a large amount of chemical emission; this type of gas is mostly containing irritant and corrosive substance; as sulfur dioxide, hydrogen sulfide, chlorine, hydrogen fluoride etc.; particularly SO2 emissions are maximum; sulfur dioxide gas directly damages health; corroding metal and building surface; also oxidizable formation acid rain drops to ground; contaminated soil, river, lake; gas-liquid separation device on existing market adopts metal shell mostly, and when processing chemical emission, life cycle is relatively short.
Summary of the invention
The purpose of this utility model is to provide that a kind of technique is simple, corrosion resistance strong, easy cleaning, easy-to-maintain gas-liquid separation tower.
The utility model is achieved through the following technical solutions: a kind of gas-liquid separation tower, comprise tower body, described tower body bottom is provided with air intake duct, the top of described air intake duct is provided with porous sieve plate, the top of described porous sieve plate is provided with multilayer demist packing layer, described tower body top is provided with gas outlet, discharging valve is provided with bottom described tower body, described air intake duct is along tower body inwall tangential admission, in tower body, gas distributor is upper bell-mouth structure of air, described tower body top is provided with Multi-layer sprinkling pipe, and shower is provided with spiral nozzle.
Further, described demist packing layer is three layers.
Further, described tower body adopts glass-reinforced plastic material, wall thickness >=10 millimeter.
Further, the middle part of described tower body is provided with access hole.
The beneficial effects of the utility model are: this utility model can liquid effectively in separation bubble, and technique is simple, corrosion resistance strong, easy cleaning, easily overhaul.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the partial top view of air intake duct and gas distributor.
In the drawings, 1, porous sieve plate; 2, gas outlet; 3, demist packing layer; 4, air intake duct; 5, access hole; 6, discharging valve; 7, tower body 8, gas distributor; 9, shower; 10, spiral nozzle.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail:
A kind of gas-liquid separation tower as depicted in figs. 1 and 2, comprise tower body 7, described tower body 7 bottom is provided with air intake duct 4, the top of described air intake duct 4 is provided with porous sieve plate 1, the top of described porous sieve plate 1 is provided with three layers of demist packing layer 3, described tower body 1 top is provided with gas outlet 2, described tower body inner bottom part is provided with Pagoda-shaped water collector, discharging valve 6 is provided with bottom described tower body 1, described air intake duct 4 is along tower body 1 inwall tangential admission, in tower body 1, gas distributor 8 is upper bell-mouth structure of air, described tower body 1 top is provided with Multi-layer sprinkling pipe 9, shower 9 is provided with spiral nozzle 10, described tower body adopts glass-reinforced plastic material, wall thickness >=10 millimeter, the middle part of described tower body is provided with access hole 5.
The utility model in use, pending gas-liquid is sent to tower body 7 by air intake duct 4, and the partially liq in vapor phase stream sinks rapidly, and residue gas phase flows through porous sieve plate 1 and arrives demist packing layer 3 and to condense further sinking, gas is discharged outside tower through gas outlet 2, thus reaches the object of gas-liquid separation.
The utility model is not limited to above-mentioned embodiment, and every have identical or close technical scheme with the utility model, is protection domain of the present utility model.
Claims (4)
1. a gas-liquid separation tower, it is characterized in that: comprise tower body, described tower body bottom is provided with air intake duct, and the top of described air intake duct is provided with porous sieve plate, and the top of described porous sieve plate is provided with multilayer demist packing layer, described tower body top is provided with gas outlet, be provided with discharging valve bottom described tower body, described air intake duct is along tower body inwall tangential admission, and in tower body, gas distributor is upper bell-mouth structure of air, described tower body top is provided with Multi-layer sprinkling pipe, and shower is provided with spiral nozzle.
2. gas-liquid separation tower according to claim 1, is characterized in that: described demist packing layer is three layers.
3. gas-liquid separation tower according to claim 1, is characterized in that: described tower body adopts glass-reinforced plastic material, wall thickness >=10 millimeter.
4. gas-liquid separation tower according to claim 1, is characterized in that: the middle part of described tower body is provided with access hole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520430623.2U CN204973148U (en) | 2015-06-19 | 2015-06-19 | Gas -liquid separation tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520430623.2U CN204973148U (en) | 2015-06-19 | 2015-06-19 | Gas -liquid separation tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204973148U true CN204973148U (en) | 2016-01-20 |
Family
ID=55107568
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520430623.2U Expired - Fee Related CN204973148U (en) | 2015-06-19 | 2015-06-19 | Gas -liquid separation tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204973148U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105038864A (en) * | 2015-08-04 | 2015-11-11 | 山东理工大学 | Multistage combination type biomass pyrolytic gas condensing tower |
| CN106310721A (en) * | 2015-06-19 | 2017-01-11 | 宜兴市富陶环境保护设备有限公司 | Gas-liquid separation tower |
-
2015
- 2015-06-19 CN CN201520430623.2U patent/CN204973148U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106310721A (en) * | 2015-06-19 | 2017-01-11 | 宜兴市富陶环境保护设备有限公司 | Gas-liquid separation tower |
| CN105038864A (en) * | 2015-08-04 | 2015-11-11 | 山东理工大学 | Multistage combination type biomass pyrolytic gas condensing tower |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160120 Termination date: 20160619 |