CN203428944U - Nitrification wastewater concentration device - Google Patents
Nitrification wastewater concentration device Download PDFInfo
- Publication number
- CN203428944U CN203428944U CN201320511926.8U CN201320511926U CN203428944U CN 203428944 U CN203428944 U CN 203428944U CN 201320511926 U CN201320511926 U CN 201320511926U CN 203428944 U CN203428944 U CN 203428944U
- Authority
- CN
- China
- Prior art keywords
- concentrated solution
- pipeline
- condenser
- outlet
- waste water
- 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
Images
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The utility model discloses a nitrification wastewater concentration device, wherein a nitrification wastewater inlet, a secondary vapor outlet and a concentrated solution outlet are formed in a rotary scraping plate evaporator (1), the concentrated solution outlet in the bottom of the rotary scraping plate evaporator (1) is connected to a feed opening of a concentrated solution buffering tank (2) through a pipeline, a discharge opening in the bottom of the concentrated solution buffering tank (2) is connected to the inlet of a pneumatic diaphragm pump (3) through a pipeline, the outlet of the pneumatic diaphragm pump (3) is connected to the feed opening of a concentrated solution storage tank (4) through a pipeline, the secondary vapor outlet in the upper part of the rotary scraping plate evaporator (1) is connected to a feed opening of a condenser (5) through a pipeline, the discharge opening of the condenser (5) is connected to a condensate water tank (6) through a pipeline, vacuum interfaces are formed in the concentrated solution buffering tank (2) and the condenser (5) for connecting vacuum to form the nitrification wastewater concentration device on the whole. Since the rotary scraping plate evaporator is adopted by the nitrification wastewater concentration device disclosed by the utility model, blockage is avoided, the evaporation efficiency is high and the production safety is good.
Description
Technical field
The utility model relates to wastewater treatment equipment, is specifically related to a kind of nitration waste water concentrating unit.
Background technology
Nitro-compound can produce nitration waste water in process of production, wherein contains a certain amount of nitropheneol, nitrobenzene and salt, and nitropheneol, nitrobenzene belong to difficult for biological degradation compound.Thereby our company adopts and first waste water circulation is applied mechanically, then the treatment process of evaporation concentration, organism and water are recycled, reduce the discharge of pollutent, protection of the environment.Owing to containing a certain amount of nitropheneol, nitrobenzene and salt in nitration waste water, conventionally the tube still heater vaporizer adopting, in evaporating concentration process, the easy crystallization of organism and salt results in blockage, vaporization efficiency is low, and nitropheneol is wherein flammable and explosive substance, and concentration process exists certain potential safety hazard.
Summary of the invention
The purpose of this utility model is: a kind of nitration waste water concentrating unit is provided, and this apparatus structure is simple, avoids stopping up, and vaporization efficiency is high.
Technical solution of the present utility model is: this nitration waste water concentrating unit comprises rotating scraper evaporator, concentrated solution surge tank, pneumatic diaphragm pump, concentrated solution basin, condenser and condensate tank, rotating scraper evaporator is provided with nitration waste water import, secondary steam outlet and concentrated solution outlet, the concentrated solution outlet of rotating scraper evaporator bottom is connected with concentrated solution surge tank opening for feed by pipeline, concentrated solution surge tank bottom discharge mouth is connected with pneumatic diaphragm pump inlet by pipeline, pneumatic diaphragm pump discharge is connected with concentrated solution basin opening for feed by pipeline, the secondary steam outlet on rotating scraper evaporator top is connected with the opening for feed of condenser by pipeline, condenser discharge port is connected with condensate tank by pipeline, concentrated solution surge tank with on condenser, be equipped with vacuum interface and be connected vacuum, whole formation nitration waste water concentrating unit.
The utility model adopts rotating scraper evaporator, and waste water enters rotating scraper evaporator, first through cloth tray, distributes, by blade, swept and scrape again, coating filmform in heat conductive wall, rete is subject to thermal evaporation, avoid stopping up, vaporization efficiency is shell and tube evaporator 4 times, improved the security of producing.
Accompanying drawing explanation
Fig. 1 is structural principle schema of the present utility model.
In figure: 1 rotating scraper evaporator, 2 concentrated solution surge tanks, 3 surge pumps, 4 concentrated solution basins, 5 condensers, 6 condensate tanks.
Embodiment
As shown in Figure 1, this nitration waste water concentrating unit comprises rotating scraper evaporator 1, concentrated solution surge tank 2, pneumatic diaphragm pump 3, concentrated solution basin 4, condenser 5 and condensate tank 6, rotating scraper evaporator 1 is provided with nitration waste water import, secondary steam outlet and concentrated solution outlet, the concentrated solution outlet of rotating scraper evaporator 1 bottom is connected with concentrated solution surge tank 2 opening for feeds by pipeline, concentrated solution surge tank 2 bottom discharge mouths are connected with pneumatic diaphragm pump 3 imports by pipeline, pneumatic diaphragm pump 3 outlets are connected with concentrated solution basin 4 opening for feeds by pipeline, the secondary steam outlet on rotating scraper evaporator 1 top is connected with the opening for feed of condenser 5 by pipeline, condenser 5 discharge ports are connected with condensate tank 6 by pipeline, concentrated solution surge tank 2 with on condenser 5, be equipped with vacuum interface and be connected vacuum, whole formation nitration waste water concentrating unit.
During production, nitration waste water enters rotating scraper evaporator 1 by pipeline and under vacuum state, carries out evaporation concentration, the secondary steam that evaporation obtains enters condenser 5 and carries out condensation, condensed water enters condensate tank 6 and stores recycling, the concentrated solution that evaporation obtains enters concentrated solution surge tank 2, through pneumatic diaphragm pump 3, squeeze into concentrated solution basin 4 again and store, finally go burning disposal.
Claims (1)
1. nitration waste water concentrating unit, it is characterized in that: this nitration waste water concentrating unit comprises rotating scraper evaporator (1), concentrated solution surge tank (2), pneumatic diaphragm pump (3), concentrated solution basin (4), condenser (5) and condensate tank (6), rotating scraper evaporator (1) is provided with nitration waste water import, secondary steam outlet and concentrated solution outlet, the concentrated solution outlet of rotating scraper evaporator (1) bottom is connected with concentrated solution surge tank (2) opening for feed by pipeline, concentrated solution surge tank (2) bottom discharge mouth is connected with pneumatic diaphragm pump (3) import by pipeline, pneumatic diaphragm pump (3) outlet is connected with concentrated solution basin (4) opening for feed by pipeline, the secondary steam outlet on rotating scraper evaporator (1) top is connected with the opening for feed of condenser (5) by pipeline, condenser (5) discharge port is connected with condensate tank (6) by pipeline, concentrated solution surge tank (2) with on condenser (5), be equipped with vacuum interface and be connected vacuum, whole formation nitration waste water concentrating unit.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320511926.8U CN203428944U (en) | 2013-08-21 | 2013-08-21 | Nitrification wastewater concentration device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320511926.8U CN203428944U (en) | 2013-08-21 | 2013-08-21 | Nitrification wastewater concentration device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN203428944U true CN203428944U (en) | 2014-02-12 |
Family
ID=50057995
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201320511926.8U Expired - Fee Related CN203428944U (en) | 2013-08-21 | 2013-08-21 | Nitrification wastewater concentration device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN203428944U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111689541A (en) * | 2020-07-17 | 2020-09-22 | 四川北方红光特种化工有限公司 | Safe concentration process and concentration system for nitrophenol sodium salt wastewater |
-
2013
- 2013-08-21 CN CN201320511926.8U patent/CN203428944U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111689541A (en) * | 2020-07-17 | 2020-09-22 | 四川北方红光特种化工有限公司 | Safe concentration process and concentration system for nitrophenol sodium salt wastewater |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104860462A (en) | Equipment and application method of microwave purification treatment for heavy metal ion containing wastewater | |
WO2017107020A1 (en) | Household solar seawater desalination apparatus | |
CN101759590A (en) | DMF recycling method | |
CN205216222U (en) | Concentrated system of MVR centrifugation thin film evaporation | |
CN203428944U (en) | Nitrification wastewater concentration device | |
CN204174031U (en) | The treatment unit of refuse leachate reverse osmosis dope | |
CN104418723B (en) | The recovery method of trade effluent dilute formic acid and device | |
CN204675941U (en) | A kind of equipment of microwave purifying process heavy metal ion-containing waste water | |
CN202844614U (en) | Desalting flash tank containing easily soluble monovalent salt ethylene glycol | |
CN205367778U (en) | Membrane distillation plant | |
CN107601740A (en) | A kind of graphene prepares raffinate harmless treatment and method | |
CN204417424U (en) | Super-viscous oil SAGD cyclic preheat liquid treating system | |
CN204147564U (en) | A kind of equipment utilizing solar energy concentrated vitriol zinc solution | |
CN207511867U (en) | A kind of telescopic bubbling humidification desalination plant | |
CN106186483A (en) | High chlorine high salt liquid waste treatment system | |
CN206580586U (en) | A kind of sea water desalinating unit | |
CN105692739A (en) | System for treating wastewater containing salt and method using system to treat wastewater containing salt | |
CN206355613U (en) | One kind weaving terylene finishing agent production falling film evaporator | |
CN215995629U (en) | Glycerol evaporative condenser heat utilization device | |
CN203653281U (en) | Salt-containing sewage treatment device | |
CN204803163U (en) | High salt liquid water disposal system of high chlorine | |
CN104418396A (en) | Seawater desalination or sewage purification device | |
CN104150547B (en) | Full phase transformation distillation seawater desalinating device | |
CN220393365U (en) | Evaporator with low-boiling-point substance pretreatment device | |
CN212040317U (en) | High-efficient system of recycling of piece alkali device secondary condensate |
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: 20140212 Termination date: 20190821 |