CN206372638U - Tail gas comprehensive recovery device - Google Patents
Tail gas comprehensive recovery device Download PDFInfo
- Publication number
- CN206372638U CN206372638U CN201621472171.5U CN201621472171U CN206372638U CN 206372638 U CN206372638 U CN 206372638U CN 201621472171 U CN201621472171 U CN 201621472171U CN 206372638 U CN206372638 U CN 206372638U
- Authority
- CN
- China
- Prior art keywords
- recovery
- spray column
- water
- tail gas
- watering mechanism
- 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
Landscapes
- Gas Separation By Absorption (AREA)
- Treating Waste Gases (AREA)
Abstract
Tail gas comprehensive recovery device, it mainly includes a recovery spray column for being built-in with filler, the bottom of the recovery spray column is provided with inlet exhaust gas, top is provided with offgas outlet, described recovery spray column inner chamber is disposed with least three layers packing layer from the bottom up, and the watering mechanism of external connection is at least provided with above the packing layer of the superiors；The bottom for reclaiming spray column is provided with recovery water out, and the recovery water out connects external recovery pond by pipeline；A steam-water separator is connected at the top of the recovery spray column, phoenix machine is drawn in the top of the steam-water separator by an exhaust port through blast pipe connection；Described recovery pond is circumscribed with two-way reuse water pipe, connects watering mechanism through a feeding spraying pump all the way, constitutes a reuse water loop, another road is directly connected to reuse wetting system；Described inlet exhaust gas is connected to a condenser constituted using shell-and-tube exchanger；It has structure composition rationally, easy to use and reliable, the features such as reducing pollution.
Description
Technical field
The utility model relates to a kind of tail gas comprehensive recovery device, in particular for powdery sodium benzoate production process
In tail gas comprehensive recovery device, belong to tail gas comprehensive reutilization technical field.
Background technology
Powdery sodium benzoate production process is：With sodium hydroxide neutralization reaction occurs in aqueous for benzoic acid, generates benzene
Sodium formate solution, PhCOONa solution is dried into roller chip dryer and cut after activated carbon filtering adsorbing contaminant
Piece, the sodium benzoate after section is crushed by pulverizer produces standard compliant powdery sodium benzoate product.
In powdery sodium benzoate production process, roller chip dryer can produce substantial amounts of water and steam in the drying process
Also dust generation is had in vapour, crushing process thereafter, the tail gas that this two parts is produced is powdery sodium benzoate production process tail
The constituent of gas.For above-mentioned tail gas, traditional processing method is that the dust for producing crushing process passes through sack cleaner
The common discharge after water dust scrubber is handled of vapor produced after processing with section, although being arranged after being handled by this kind of mode
Put tail gas and reach discharging standards, but sodium benzoate is soluble in water, and a small amount of benzene first is still contained in the water vapour of discharge
Sour sodium powder dirt, is discharged in air not only to air born pollution, but also waste resource.
The content of the invention
The purpose of this utility model is to overcome the shortcomings of that prior art is present, and provides a kind of structure composition rationally, makes
With convenient and reliable, pollution can not only be reduced, raw material is saved, and has reclaimed water vapour, substantially, operating efficiency is improved energy-saving effect
Be used for powdery sodium benzoate production process in tail gas comprehensive recovery device.
The purpose of this utility model is completed by following technical solution, a kind of tail gas comprehensive recovery device, and it leads
To include a recovery spray column for being built-in with filler, the bottom of the recovery spray column is provided with inlet exhaust gas, and top is provided with tail
Gas is exported, and described recovery spray column inner chamber is disposed with least three layers packing layer, at least filling out in the superiors from the bottom up
The watering mechanism of external connection is provided with above the bed of material；The bottom for reclaiming spray column is provided with recovery water out, the recovery water out
External recovery pond is connected by pipeline；A steam-water separator is connected at the top of the recovery spray column, the steam-water separation
The top of device phoenix machine is drawn through blast pipe connection by an exhaust port.
As preferred：Described recovery pond is circumscribed with two-way reuse water pipe, connects Water spray through a feeding spraying pump all the way
Mechanism, constitutes a reuse water loop, another road is directly connected to reuse wetting system；Described inlet exhaust gas is connected to one and uses shell
The condenser that formula heat exchanger is constituted, tail gas is by connecting described inlet exhaust gas after the condenser, and the condenser is cold
But described watering mechanism is attempted by by stop valve with water.
As preferred：Described watering mechanism is arranged on above every layer of packing layer, and is being reclaimed outside spray column and connect
All the way afterwards by interface external connection, the top offgas outlet for reclaiming spray column is connected to the carbonated drink point that a kidney ellipsoid cylinder is constituted by pipe
From device, cone tip part bullet directed downwardly is provided with the centre of the steam-water separator and connect under bullet, led by sector
The air deflector of flow composition.
The utility model belongs to improvements over the prior art, and it has structure composition rationally, easy to use and reliable, can not only
Pollution is reduced, raw material is saved, and has reclaimed water vapour, energy-saving effect is obvious, the features such as operating efficiency is improved.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Embodiment
The utility model is described in detail below in conjunction with accompanying drawing：Shown in Fig. 1, a kind of tail described in the utility model
Gas comprehensive recovery device, it mainly includes a recovery spray column for being built-in with filler, and the bottom of the recovery spray column 6 is provided with tail
Gas import 11, top is provided with offgas outlet 12, and the described inner chamber of recovery spray column 6 is disposed with least three layers from the bottom up
Packing layer 10, is at least provided with the watering mechanism 9 of external connection in the top of packing layer 10 of the superiors；Reclaim the bottom of spray column 6
Recovery water out 8 is provided with, the recovery water out 8 connects external recovery pond 2 by pipeline；The recovery spray column 6
Top is connected to a steam-water separator 13, and the top of the steam-water separator 13 is drawn by an exhaust port through the connection of blast pipe 5
Phoenix machine 4.
Shown in figure, described recovery pond is circumscribed with two-way reuse water pipe, connects Water spray through a feeding spraying pump 3 all the way
Mechanism 9, constitutes a reuse water loop, another road is directly connected to reuse wetting system；Described inlet exhaust gas 11 is connected to a use
The condenser 1 that shell-and-tube exchanger is constituted, the tail gas inlet exhaust gas 11 described by being connected after the condenser 1, and it is described cold
The cooling water of condenser 1 is attempted by described watering mechanism 9 by stop valve 14.
Watering mechanism 9 described in the utility model is arranged on above every layer of packing layer 10, and is being reclaimed outside spray column 6
And connect all the way afterwards by the external connection of interface 7, the top offgas outlet 12 for reclaiming spray column 6 is connected to kidney ellipsoid cylinder composition by pipe
Steam-water separator, cone tip part bullet 15 directed downwardly is provided with the centre of the steam-water separator and is connect under bullet 15
, the air deflector 16 being made up of fan-shaped flow deflector.
The beneficial effects of the utility model are：The utility model passes through the tail gas that powdery sodium benzoate production process is produced
After recovery tower processing, almost dry-steam is discharged, and has been prevented the discharge of sodium benzoate dust, has been saved production cost, is reclaimed
Distilled water, has saved resource.
Claims (3)
1. tail gas comprehensive recovery device, it mainly includes a recovery spray column for being built-in with filler, the recovery spray column（6）Bottom
Portion is provided with inlet exhaust gas（11）, top is provided with offgas outlet（12）, it is characterised in that described recovery spray column（6）Inner chamber
At least three layers packing layer are disposed with from the bottom up（10）, the packing layer at least in the superiors（10）Top is provided with external connection
Watering mechanism（9）；Reclaim spray column（6）Bottom be provided with recovery water out（8）, the recovery water out（8）Pass through pipeline
The external recovery pond of connection（2）；The recovery spray column（6）Top be connected to a steam-water separator（13）, the carbonated drink point
From device（13）Top by an exhaust port through blast pipe（5）Phoenix machine is drawn in connection（4）.
2. tail gas comprehensive recovery device according to claim 1, it is characterised in that described recovery pond（2）It is circumscribed with two
Road reuse water pipe, all the way through a feeding spraying pump（3）Connect watering mechanism（9）, a reuse water-flow circuit is constituted, another road is straight
Water equipment is taken back in succession；Described inlet exhaust gas（11）It is connected to a condenser constituted using shell-and-tube exchanger（1）,
Tail gas passes through the condenser（1）Described inlet exhaust gas is connected afterwards（11）, and the condenser（1）Cooling water pass through cut-off
Valve（14）It is attempted by described watering mechanism（9）.
3. tail gas comprehensive recovery device according to claim 1 or 2, it is characterised in that described watering mechanism（9）Peace
Mounted in every layer of packing layer（10）Above, and reclaiming spray column（6）It is outer and connect all the way afterwards by interface（7）External connection, reclaims spray
Drench tower（6）Top offgas outlet（12）The steam-water separator that one kidney ellipsoid cylinder is constituted is connected to by pipe（13）, in the carbonated drink
Separator（13）Centre be provided with cone tip part bullet directed downwardly（15）With in bullet（15）Under connect, by fan-shaped water conservancy diversion
The air deflector of piece composition（16）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621472171.5U CN206372638U (en) | 2016-12-30 | 2016-12-30 | Tail gas comprehensive recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621472171.5U CN206372638U (en) | 2016-12-30 | 2016-12-30 | Tail gas comprehensive recovery device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206372638U true CN206372638U (en) | 2017-08-04 |
Family
ID=59408036
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621472171.5U Expired - Fee Related CN206372638U (en) | 2016-12-30 | 2016-12-30 | Tail gas comprehensive recovery device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206372638U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106512615A (en) * | 2016-12-30 | 2017-03-22 | 德清崎辉机械科技有限公司 | Comprehensive recovery device for tail gas |
-
2016
- 2016-12-30 CN CN201621472171.5U patent/CN206372638U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106512615A (en) * | 2016-12-30 | 2017-03-22 | 德清崎辉机械科技有限公司 | Comprehensive recovery device for tail gas |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101423214A (en) | Method for catching carbon dioxide in generating plant flue gas by ammonia process and equipment thereof | |
| CN208104264U (en) | Triethylamine dried recovered device in a kind of glyphosate production process | |
| CN209416096U (en) | A kind of dry tail gas spray equipment | |
| CN206463697U (en) | One kind circulation high-pressure spraying pond | |
| CN106178846B (en) | The exhaust system of ECH organic tail gas is reduced in epoxy resin production | |
| CN206372638U (en) | Tail gas comprehensive recovery device | |
| CN104941355A (en) | Comprehensive recovery tower for tail gas in sodium benzoate production process | |
| CN101792447B (en) | Device for preparing urotropine by using gas phase method | |
| CN206168203U (en) | Dichloromethane waste gas treatment system who contains sulphur | |
| CN206660898U (en) | One kind improves hydrogen chloride as by product of chlorinated paraffin production absorptivity and purifier | |
| CN102688663A (en) | Method and device for recycling steam in coal drying waste wet gas | |
| CN208878261U (en) | A kind of furfural exhaust gas recycling and processing device | |
| CN103613107A (en) | Biogas slurry deamination and ammonia recovery method | |
| CN106512615A (en) | Comprehensive recovery device for tail gas | |
| CN103801173B (en) | The processing method of NOx waste gas in a kind of copper zinc catalyst preparation technology | |
| CN102911704A (en) | Method for comprehensive oil gas recovery | |
| CN101708409B (en) | Comprehensive recover tower and process of granule sodium benzoate tail gas | |
| CN206817447U (en) | The dead steam recovery system of sulfuric acid apparatus | |
| CN201952381U (en) | Mirabilite collection device for formic acid production by using sodium formate method | |
| CN207871852U (en) | A kind of heat recovery and nmp solvent retracting device of the exhaust of lithium battery coating machine | |
| CN207645819U (en) | A kind of silica powder drying and nitrogen gas recovering apparatus | |
| CN219128738U (en) | Solid dust absorbing device | |
| CN205386346U (en) | Dry sprayer with concentration tower | |
| CN103214050A (en) | Device and method of separating and recycling hydrochloric acid pickling waste liquid ferric salt and hydrochloric acid | |
| CN213942594U (en) | Glucose acid calcium process tail gas absorption system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20170804 Termination date: 20171230 |