CN206121208U - But chemical industry strip tower of automatically regulated liquid level - Google Patents
But chemical industry strip tower of automatically regulated liquid level Download PDFInfo
- Publication number
- CN206121208U CN206121208U CN201621046077.3U CN201621046077U CN206121208U CN 206121208 U CN206121208 U CN 206121208U CN 201621046077 U CN201621046077 U CN 201621046077U CN 206121208 U CN206121208 U CN 206121208U
- Authority
- CN
- China
- Prior art keywords
- liquid
- tower
- chemical industry
- pipe
- tower body
- 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.)
- Active
Links
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a but chemical industry strip tower of automatically regulated liquid level, it includes tower body (1) he tagai (19), from last set gradually under to desicator (15) in the tower body, spray film separator (14), liquid distributor (12), ripple packing layer (5), air distributor (6) and porous regular packing layer (7), be provided with feed liquor pipe (2) between spray film separator and the liquid distributor, feed liquor guan yuzhu liquid pipe (18) links to each other, main liquid pipe is gone up the interval and is provided with a plurality of branch liquid pipes (13), last be provided with ring channel (3) of liquid distributor, be provided with out liquid hole (17) in the ring channel and between the ring channel, be provided with between ripple filler and the liquid distributor magnetic level gauge (4). Its adjusts the flow of waste water in the tower that gets into from the feed liquor pipe, and the low problem of bringing when high both can remain suitable throughput throughout when having avoided the manual control flow, can ensure product stable quality again.
Description
Technical field
The utility model is related to belong to field of chemical equipment, and in particular to chemical industry stripper.
Background technology
Too low into the wastewater flow in tower in chemical industry stripper, liquid distribution is uneven in possible tower, it is possible to exceed
The disposal ability of tower, affects ammonia removal efficiency；First generation ammonia nitrogen reclaimer is adjusted using the aperture of manual adjustment water pump return valve
The flow of section water inlet, but supply voltage is fluctuation, causes flow of inlet water not stop change, needs artificial constantly amendment, and group
Conjunction tank liquor position fluctuating range is very big, and the quality stability to producing product brings fluctuation.The fluctuation of flow of inlet water simultaneously is easily made
When flowing out stripping tower bottom portion's discharge nozzle into liquid, turbulent flow can be formed in tube hub, make respectively to mix and flow out in tower body, to tower body
In bringing many problems such as gas suction pump on liquid level, pump is set to form vacuum；Cause some impurities in liquid to flow out, affect finished product
Quality.
Utility model content
According to the deficiencies in the prior art, the utility model makes liquid distribution more equal and can automatically adjust liquid level there is provided one kind
Stripping chemical tower.
The technical scheme that the technical problems to be solved in the utility model is adopted is：The chemical industry for automatically adjusting liquid level
Stripper includes being disposed with drier, spray film separator, liquid distribution from top to bottom in tower body and Ta Gai, the tower body
Device, corrugated filler layer, gas distributor and porous structured filling material layer, are provided between the spray film separator and liquid distribution trough
Feed tube, feed tube is connected with main hydraulic pipe, and some separating tubes are arranged at intervals with main hydraulic pipe, and the separating tube is from tower wall in
The heart is stepped distribution, and on the liquid distribution trough cannelure is provided with, and liquid is provided with out and cannelure between in cannelure
Hole, between the ripple packing and liquid distribution trough magnetic double level gauge is provided with.
The utility model one is to change liquid distribution trough structure in existing chemical industry stripper, liquid is distributed in tower
Obtain evenly, liquid level is more dispersed tiny, can be fully contacted with gas, so as to can further improve Srteam Stripping effect, while in tower
Magnetic double level gauge is provided with level tank, flow of the waste water in tower entered from feed tube can be reasonably adjusted, it is to avoid
Low brought problem when high during artificial control flow, can both remain suitable disposal ability, and product quality is can ensure that again
It is stable, improve treatment effect.
The utility model uses PID arithmetic device, and it is that bottom of towe is given up automatically adjust stripper to calculate output analog signal
Water takes the frequency of the frequency converter of water pump away, so as to control flow of inlet water, automatically adjusts the flat horizontal stroke of dynamic of chemical tower liquid level, occurs
Liquid level can not report to the police in setting range, and autostop, will not bring potential safety hazard, without setting special messenger's nurse, reduce manpower
Cost.
Description of the drawings
Fig. 1 is main cross section structure diagram of the present utility model,
Fig. 2 is the A-A cross section structure diagrams of Fig. 1.
In figure, 1, tower body 2, feed tube 3, cannelure 4, magnetic double level gauge 5, corrugated filler layer 6, gas point
Cloth device 7, porous structured filling material layer 8, tower tray 9, liquid outlet 10, hot air intake 11, grid orifice plate 12, liquid distribution trough
13rd, separating tube 14, spray film separator 15, drier 16, escaping pipe 17, fluid hole 18, main hydraulic pipe 19, Ta Gai.
Specific embodiment
In fig. 1 and 2, the chemical industry stripper for automatically adjusting liquid level includes tower body 1 and Ta Gai 19, the tower lid
On be provided with escaping pipe 16, tower body bottom is provided with liquid outlet 9, and tower body bottom is provided with hot air intake 10, in the tower body
Drier 15, spray film separator 14, liquid distribution trough 12, corrugated filler layer 5, gas distributor 6 are disposed with from top to bottom
With porous structured filling material layer 7, porous structured filling material layer is supported on tower tray 8, and tower tray is higher than hot air intake 10, liquid distribution trough
It is arranged on grid orifice plate 11, grid orifice plate is fixed on tower body on inwall, between the spray film separator and liquid distribution trough
Feed tube 2 is provided with, feed tube is connected with main hydraulic pipe 18, and six roots of sensation separating tube 13 is arranged at intervals with main hydraulic pipe（May also be other
Many, depending on tower inner chamber size）, three separating tubes are stepped distribution from tower wall to center, and six roots of sensation separating tube exists
It is symmetrical on tower face, cannelure 3 is provided with the liquid distribution trough, it is arranged at intervals with and cannelure between in cannelure
Fluid hole 17, fluid hole pore size is 5-10 millimeters, and the fluid hole gross area is the 1/5-1/3 of tower lumenal cross-section product, goes out liquid
Hole is preferably in taper hole shape, up-small and down-big, and magnetic double level gauge 4 is provided between the ripple packing and liquid distribution trough.
Embodiment of above is only unrestricted to illustrate the technical solution of the utility model, although with reference to specific embodiment
The utility model has been described in detail, it will be understood by those within the art that, can be to skill of the present utility model
Art scheme is modified or equivalent, and without deviating from the spirit and scope of technical solutions of the utility model, it all should cover
In protective scope of the claims of the present utility model.
Claims (2)
1. the chemical industry stripper of liquid level can be automatically adjusted, and it includes tower body（1）With tower lid（19）, in the tower body from top to bottom according to
It is secondary to be provided with drier（15）, spray film separator（14）, liquid distribution trough（12）, corrugated filler layer（5）, gas distributor（6）
With porous structured filling material layer（7）, it is characterized in that：Feed tube is provided between the spray film separator and liquid distribution trough（2）, enter
Liquid pipe and main hydraulic pipe（18）It is connected, some separating tubes is arranged at intervals with main hydraulic pipe（13）, the separating tube is from tower wall in
The heart is stepped distribution, and on the liquid distribution trough cannelure is provided with（3）, it is provided with out and cannelure between in cannelure
Fluid apertures（17）, between the corrugated filler layer and liquid distribution trough magnetic double level gauge is provided with（4）.
2. the chemical industry stripper for automatically adjusting liquid level according to claim 1, is characterized in that：The fluid hole（17）Hole
Footpath size is 5-10 millimeters, and the fluid hole gross area is the 1/5-1/3 of tower lumenal cross-section product.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621046077.3U CN206121208U (en) | 2016-09-09 | 2016-09-09 | But chemical industry strip tower of automatically regulated liquid level |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621046077.3U CN206121208U (en) | 2016-09-09 | 2016-09-09 | But chemical industry strip tower of automatically regulated liquid level |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206121208U true CN206121208U (en) | 2017-04-26 |
Family
ID=58570519
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621046077.3U Active CN206121208U (en) | 2016-09-09 | 2016-09-09 | But chemical industry strip tower of automatically regulated liquid level |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206121208U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114130053A (en) * | 2021-09-06 | 2022-03-04 | 中轻化工绍兴有限公司 | High-efficient neutralization steam stripping device of no gel zone class high concentration sulfonated product |
-
2016
- 2016-09-09 CN CN201621046077.3U patent/CN206121208U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114130053A (en) * | 2021-09-06 | 2022-03-04 | 中轻化工绍兴有限公司 | High-efficient neutralization steam stripping device of no gel zone class high concentration sulfonated product |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204718480U (en) | A kind of cooling tower water distribution system and cooling tower | |
| CN206121208U (en) | But chemical industry strip tower of automatically regulated liquid level | |
| CN110526395A (en) | Eddy flow anaerobic reactor for waste water treatment system | |
| CN206576127U (en) | A kind of intelligent pestsides synthesis spray appliance with node spraying function | |
| CN206126939U (en) | Modular gas distribution device | |
| CN112359942A (en) | Water separator device capable of accurately adjusting flow and adjusting method | |
| CN104058502B (en) | One all presses Turbulent Flow Type water distributor | |
| CN217593874U (en) | Strip tower for overflow weir | |
| CN207903983U (en) | Reducing optimizes UASB reactors | |
| CN215403340U (en) | Anaerobic reactor of marsh gas inner loop | |
| CN209726910U (en) | A kind of variable-flow crossflow cooling tower watering device | |
| CN103304024B (en) | Easy membrane formation type circulating bio-contact oxidation integrated reactor | |
| CN208287975U (en) | Catalyst reactor with counterflow-preventing | |
| CN108373246B (en) | Domestic sewage treatment equipment | |
| CN204874510U (en) | Biogas fermentation tank ejection of compact overflow arrangement | |
| CN210656244U (en) | Integrated high-efficiency energy-saving vacuum deaerator | |
| CN217564269U (en) | Full-automatic vertical circulation crop planting equipment | |
| CN203403096U (en) | Biological reaction pot | |
| CN203959918U (en) | A kind of Turbulent Flow Type water distributor of all pressing | |
| CN203683204U (en) | Carrier attachment type circular culture apparatus of heterotrophic nitrification and aerobic denitrification bacteria | |
| CN212864298U (en) | High-efficiency energy-saving aeration device for sewage treatment equipment | |
| CN216093030U (en) | Avoid spray column of bias current | |
| CN210030166U (en) | Improved generation domestic sewage anaerobic treatment device | |
| CN213824660U (en) | Structure for uniformly guiding gas out of filling type particle material treatment equipment | |
| CN209997605U (en) | gas-liquid two-phase flow jet reactor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |