CN206033472U - Trichloroisocyanuric acid waste water processing system - Google Patents
Trichloroisocyanuric acid waste water processing system Download PDFInfo
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- CN206033472U CN206033472U CN201620938497.6U CN201620938497U CN206033472U CN 206033472 U CN206033472 U CN 206033472U CN 201620938497 U CN201620938497 U CN 201620938497U CN 206033472 U CN206033472 U CN 206033472U
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Abstract
The utility model discloses a trichloroisocyanuric acid waste water processing system, it includes that the analytic tower of waste water storage tank, heat exchanger, delivery pump, acidification, hydrochloric acid storage tank, vacuum pump, chlorine buffer tank, chlorination cauldron, analytic waste water storage tank, sodium bisulfite storage tank, cyanuric acid generate water line in jar, alkali lye storage tank, filter press, cyanuric acid recovery jar, filter -pressing liquid storage tank, membrane filter, resin adsorption tower, evaporated crystallizer, salt storage tank and the condensation. The moving guiding mechanism in the utility model is advantageous in that, the utility model discloses processing system scientific and reasonable thoroughly solves the exhaust pollution air scheduling problem of unable discharge to reach standard, production behind the trichloroisocyanuric acid waste water treatment to water, salt, gas to after handling carry out recycle, have reduced the formation cost, have improved production utilization ratio of material.
Description
Technical field：
This utility model is related to the processing system of industrial production wastewater, and more particularly to a kind of sym-closene produces waste water
Processing system.
Background technology：
The production method of sym-closene mainly generates cyanuric acid trisodium using liquid caustic soda method, i.e. cyanuric acid and liquid caustic soda
Salt, then the method that chlorine generates sym-closene is passed through, but a large amount of waste water can be produced in this production process, contain in waste water
The recovery value of substantial amounts of Sodium Chloride and sym-closene, wherein Sodium Chloride is low, and sym-closene compound is containing triazine
The heterocycle compound of ring structure, it is difficult to degradation treatment；At present, sym-closene production is produced centrifuge mother liquor and washings
Typically processed using dechlorination Deng waste water, there is waste water after process and be changed into haline water residual fraction sym-closene, cause place
Waste water after reason still cannot qualified discharge, while during storage, waste water can discharge part chlorine and cause asking for air pollution
Topic, the waste water for ultimately resulting in sym-closene production generation are difficult, and the raw materials for production in waste water cannot be recycled, and cause
The waste of raw materials for production.
Utility model content：
The purpose of this utility model is to provide a kind of sym-closene that improves to produce waste water dechlorination efficiency, wastewater treatment
Sym-closene production wastewater treatment system in hgher efficiency.
The purpose of this utility model is implemented by following technical scheme：Sym-closene production wastewater treatment system, its bag
Include wastewater storage tank, heat exchanger, delivery pump, acid adding Analytic Tower, hydrochloric acid tank, vacuum pump, Chlorine Buffer Vessel, chlorination tank, parsing useless
Water storage tank, sodium sulfite storage tank, cyanuric acid generate the tank, alkali liquor storage tank, filter press, cyanuric acid recycling can, pressing filtering liquid storage
Tank, film filter, resin adsorption tower, crystallizing evaporator, salt storage tank and condensation middle water line,
The outlet of the wastewater storage tank is connected with the waterwater entrance of the heat exchanger, the wastewater outlet of the heat exchanger and institute
State the entrance connection of delivery pump, the inlet communication of the outlet of the delivery pump and the acid adding Analytic Tower, the acid adding Analytic Tower
Acid solution import and the hydrochloric acid tank outlet, the chlorine gas outlet of the acid adding Analytic Tower and the import of the vacuum pump
Connection, the outlet of the vacuum pump connected with the Chlorine Buffer Vessel air inlet, the gas outlet of the Chlorine Buffer Vessel with it is described
The air inlet connection of chlorination tank；The wastewater outlet of the acid adding Analytic Tower and the inlet communication for parsing wastewater storage tank, it is described
Parsing wastewater storage tank reagent entry port and the sodium sulfite storage tank outlet, the outlet of the parsing wastewater storage tank with
The inlet communication of the cyanuric acid generate the tank；The reagent entry port of the cyanuric acid generate the tank is connected with the outlet of the alkali liquor storage tank
It is logical, the outlet of the cyanuric acid generate the tank and the inlet communication of the filter press；The solid outlet of the filter press
With the cyanuric acid recycling can inlet communication, the import of the liquid outlet of the filter press and the filter pressing liquid storage tank connects
It is logical, the outlet of the filter pressing liquid storage tank and the inlet communication of the film filter；The outlet of the film filter and the resin
The inlet communication of adsorption tower, the concentrated water outlet of the film filter and the inlet communication of the filter press；The resin is inhaled
The inlet communication of the outlet of attached tower and the crystallizing evaporator, the solid outlet of the crystallizing evaporator are entered with the salt storage tank
Mouth connection, the liquid outlet of the crystallizing evaporator are connected with the condensation middle water line.
Further, gel type resin is filled with the resin adsorption tower.
Further, the crystallizing evaporator is mechanical steam recompression crystallizing evaporator or Multi-effect evaporation crystallizer.
Advantage of the present utility model：1st, this utility model processing system is scientific and reasonable, thoroughly solves sym-closene
After wastewater treatment cannot qualified discharge, produce exhaust emission air the problems such as, and the water after process, salt, gas are reclaimed
Utilize, reduce manufacturing cost, improve raw materials for production utilization rate；2nd, the waste water that will be produced in sym-closene production process
Jing after heat exchanger heating deliver to, can make its acid adding dechlorination reaction carry out it is more thorough；
3rd, the chlorine that acid adding dechlorination in acid adding Analytic Tower is produced is pumped to chlorination tank using vacuum pump, one can be to make acid adding Analytic Tower
It is more thorough that interior acid adding dechlorination reaction is carried out, and two is to process the chlorine recycling that waste water is produced, and has saved production original
Material, reduces the waste of raw materials for production.
Description of the drawings：
Fig. 1 is this utility model Waste Water Treatment schematic diagram.
Wastewater storage tank 1, heat exchanger 2, delivery pump 3, acid adding Analytic Tower 4, hydrochloric acid tank 5, vacuum pump 6, Chlorine Buffer Vessel 7,
Chlorination tank 8, parses wastewater storage tank 9, sodium sulfite storage tank 10, cyanuric acid generate the tank 11, alkali liquor storage tank 12, filter press
13, cyanuric acid recycling can 14, filter pressing liquid storage tank 15, film filter 16, resin adsorption tower 17, crystallizing evaporator 18, salt storage tank 19,
Condensation middle water line 20.
Specific embodiment：
Embodiment 1：
As shown in figure 1, sym-closene production wastewater treatment system, which includes wastewater storage tank 1, heat exchanger 2, delivery pump
3, acid adding Analytic Tower 4, hydrochloric acid tank 5, vacuum pump 6, Chlorine Buffer Vessel 7, chlorination tank 8 parse wastewater storage tank 9, sodium sulfite
Storage tank 10, cyanuric acid generate the tank 11, alkali liquor storage tank 12, filter press 13, cyanuric acid recycling can 14, filter pressing liquid storage tank 15, film
Filter 16, resin adsorption tower 17, crystallizing evaporator 18, salt storage tank 19 and condensation middle water line 20, fill out in resin adsorption tower 17
Equipped with gel type resin, crystallizing evaporator 18 is mechanical steam recompression crystallizer or Multi-effect evaporation crystallizer；
The outlet of wastewater storage tank 1 is connected with the waterwater entrance of heat exchanger 2, heat exchanger 2 will can flow out from wastewater storage tank 1 three
Symclosene generate waste water heating, can make its acid adding dechlorination reaction carry out it is more thorough；The wastewater outlet of heat exchanger 2 with it is defeated
Send the entrance of pump 3 to connect, the outlet of delivery pump 3 and the inlet communication of acid adding Analytic Tower 4, the acid solution import of acid adding Analytic Tower 4 with
The outlet of hydrochloric acid tank 5, the chlorine gas outlet of acid adding Analytic Tower 4 and the inlet communication of vacuum pump 6, the outlet of vacuum pump 6 with
7 air inlet of Chlorine Buffer Vessel is connected, and the use of vacuum pump 6 one can be to carry out the acid adding dechlorination reaction in acid adding Analytic Tower 4
More thoroughly, two is can will to process the chlorine recycling that waste water is produced, and has saved raw materials for production, has reduced the wave of raw materials for production
Take；The gas outlet of Chlorine Buffer Vessel 7 is connected with the air inlet of chlorination tank 8；The wastewater outlet of acid adding Analytic Tower 4 and parsing waste water storage
The inlet communication of tank 9, parses the reagent entry port of wastewater storage tank 9 and the outlet of sodium sulfite storage tank 10, parsing waste water storage
The outlet of tank 9 and the inlet communication of cyanuric acid generate the tank 11；The reagent entry port of cyanuric acid generate the tank 11 is gone out with alkali liquor storage tank 12
Mouth connection, the outlet of cyanuric acid generate the tank 11 and the inlet communication of filter press 13；The solid outlet of filter press 13 with
14 inlet communication of cyanuric acid recycling can, the liquid outlet of filter press 13 and the inlet communication of filter pressing liquid storage tank 15, pressing filtering liquid
The outlet of storage tank 15 and the inlet communication of film filter 16；The outlet of film filter 16 and the inlet communication of resin adsorption tower 17,
The concentrated water outlet of film filter 16 and the inlet communication of filter press 13；The outlet of resin adsorption tower 17 and crystallizing evaporator 18
Inlet communication, the solid outlet of crystallizing evaporator 18 and the inlet communication of salt storage tank 19, the liquid outlet of crystallizing evaporator 18
Connect with condensation middle water line 20.
The present embodiment is scientific and reasonable, it is simple effectively, thoroughly solve after sym-closene wastewater treatment cannot qualified discharge,
The problems such as exhaust emission air of generation, and the water after process, salt, gas are recycled, manufacturing cost is reduced, is improved
Raw materials for production utilization rates.
Preferred embodiment of the present utility model is these are only, it is not to limit this utility model, all in this practicality
Within new spirit and principle, any modification, equivalent substitution and improvements made etc. should be included in guarantor of the present utility model
Within the scope of shield.
Claims (3)
1. sym-closene production wastewater treatment system, it is characterised in that it include wastewater storage tank, heat exchanger, delivery pump, plus
Sour Analytic Tower, hydrochloric acid tank, vacuum pump, Chlorine Buffer Vessel, chlorination tank, parsing wastewater storage tank, sodium sulfite storage tank, cyanuric acid
Generate the tank, alkali liquor storage tank, filter press, cyanuric acid recycling can, filter pressing liquid storage tank, film filter, resin adsorption tower, evaporation knot
Brilliant device, salt storage tank and condensation middle water line,
The outlet of the wastewater storage tank is connected with the waterwater entrance of the heat exchanger, and the wastewater outlet of the heat exchanger is defeated with described
The entrance of pump is sent to connect, the inlet communication of the outlet of the delivery pump and the acid adding Analytic Tower, the acid of the acid adding Analytic Tower
The outlet of liquid import and the hydrochloric acid tank, the import of the chlorine gas outlet and the vacuum pump of the acid adding Analytic Tower connect
Logical, the outlet of the vacuum pump is connected with the Chlorine Buffer Vessel air inlet, the gas outlet of the Chlorine Buffer Vessel and the chlorine
Change the air inlet connection of kettle；The wastewater outlet of the acid adding Analytic Tower and the inlet communication for parsing wastewater storage tank, the solution
The reagent entry port of analysis wastewater storage tank and the outlet of the sodium sulfite storage tank, the outlet of the parsing wastewater storage tank and institute
State the inlet communication of cyanuric acid generate the tank；The reagent entry port of the cyanuric acid generate the tank and the outlet of the alkali liquor storage tank,
The outlet of the cyanuric acid generate the tank and the inlet communication of the filter press；The solid outlet of the filter press and institute
State cyanuric acid recycling can inlet communication, the inlet communication of the liquid outlet of the filter press and the filter pressing liquid storage tank, institute
State the outlet of filter pressing liquid storage tank and the inlet communication of the film filter；The outlet of the film filter and the resin adsorption tower
Inlet communication, the film filter concentrated water outlet and the filter press inlet communication；The resin adsorption tower
The inlet communication with the crystallizing evaporator is exported, the solid outlet of the crystallizing evaporator is connected with the import of the salt storage tank
Logical, the liquid outlet of the crystallizing evaporator is connected with the condensation middle water line.
2. sym-closene production wastewater treatment system according to claim 1, it is characterised in that the resin absorption
Gel type resin is filled with tower.
3. sym-closene production wastewater treatment system according to claim 1, it is characterised in that the evaporative crystallization
Device is mechanical steam recompression crystallizing evaporator or Multi-effect evaporation crystallizer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620938497.6U CN206033472U (en) | 2016-08-24 | 2016-08-24 | Trichloroisocyanuric acid waste water processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620938497.6U CN206033472U (en) | 2016-08-24 | 2016-08-24 | Trichloroisocyanuric acid waste water processing system |
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| Publication Number | Publication Date |
|---|---|
| CN206033472U true CN206033472U (en) | 2017-03-22 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201620938497.6U Active CN206033472U (en) | 2016-08-24 | 2016-08-24 | Trichloroisocyanuric acid waste water processing system |
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| CN (1) | CN206033472U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106467341A (en) * | 2016-08-24 | 2017-03-01 | 内蒙古兰太实业股份有限公司 | Sym-closene production wastewater treatment system and method |
-
2016
- 2016-08-24 CN CN201620938497.6U patent/CN206033472U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106467341A (en) * | 2016-08-24 | 2017-03-01 | 内蒙古兰太实业股份有限公司 | Sym-closene production wastewater treatment system and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 750336 Helan District, Alashan Economic Development Zone, Alashan League, Inner Mongolia Autonomous Region Patentee after: China Salt Inner Mongolia Chemical Co.,Ltd. Address before: 750336 Room 8415, Salt Science and Technology Building, Ustin Economic Development Zone, Alxa League, Inner Mongolia Autonomous Region (Inner Mongolia Lantai Industrial Co., Ltd.) Patentee before: INNER MONGOLIA LANTAI INDUSTRIAL Co.,Ltd. |
|
| CP03 | Change of name, title or address | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20221202 Address after: 750336 south of Ulanbuhe street, Alxa Economic Development Zone, Alxa League, Inner Mongolia Autonomous Region (WuSitai town) Patentee after: INNER MONGOLIA LANTAI SODIUM INDUSTRY Co.,Ltd. Patentee after: China Salt Inner Mongolia Chemical Co.,Ltd. Address before: 750336 Helan District, Alashan Economic Development Zone, Alashan League, Inner Mongolia Autonomous Region Patentee before: China Salt Inner Mongolia Chemical Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 750336 south of Ulanbuhe street, Alxa Economic Development Zone, Alxa League, Inner Mongolia Autonomous Region (WuSitai town) Patentee after: China Salt Inner Mongolia Chemical sodium Industry Co.,Ltd. Patentee after: China Salt Inner Mongolia Chemical Co.,Ltd. Address before: 750336 south of Ulanbuhe street, Alxa Economic Development Zone, Alxa League, Inner Mongolia Autonomous Region (WuSitai town) Patentee before: INNER MONGOLIA LANTAI SODIUM INDUSTRY Co.,Ltd. Patentee before: China Salt Inner Mongolia Chemical Co.,Ltd. |
|
| CP01 | Change in the name or title of a patent holder |