CN216972179U - High-precision treatment system for high-salt organic wastewater - Google Patents
High-precision treatment system for high-salt organic wastewater Download PDFInfo
- Publication number
- CN216972179U CN216972179U CN202121412471.5U CN202121412471U CN216972179U CN 216972179 U CN216972179 U CN 216972179U CN 202121412471 U CN202121412471 U CN 202121412471U CN 216972179 U CN216972179 U CN 216972179U
- Authority
- CN
- China
- Prior art keywords
- gas
- water
- activated carbon
- reaction tower
- inlet
- 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
Images
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The utility model discloses a treatment system for treating high-salinity organic wastewater with high precision, which comprises a water inlet pump, an internal circulating pump, a gas-water mixer and an active carbon adsorption reaction tower, wherein the gas-water mixer is provided with a water inlet and a gas inlet; the side surface of the bottom of the activated carbon adsorption reaction tower is symmetrically provided with a reaction tower inlet and an inner circulating pump inlet, the top of the activated carbon adsorption reaction tower is provided with a reaction tower outlet, the inner circulating pump inlet is connected with an inner circulating pump, the reaction tower inlet is connected with the outlet of a gas-water mixer, and the reaction tower outlet is connected with a gas-liquid separator; the gas-liquid separator is also provided with a gas outlet and a water outlet, the gas outlet of the gas-liquid separator is connected with the buffer tank, and the buffer tank is also connected with an ozone tail gas destructor. Through the combination of the activated carbon and the ozone oxidation process, the COD of the process target is lower than 100 mg/L.
Description
Technical Field
The utility model belongs to the field of organic wastewater treatment, and particularly relates to a treatment system for treating high-salinity organic wastewater with high precision.
Technical Field
On the basis of realizing the whole recovery of water, the zero discharge technology of waste water has become an industrial difficulty and a hotspot in harmlessness and reclamation of mixed salt nowadays. A pre-salt-separating Nanofiltration (NF) system, a bipolar membrane salt electrolysis and acid-Base (BPED) system for salt deep utilization, an evaporation system requiring the salt yield to be higher than 90 percent and the like all put more strict requirements on the COD of the inlet water, although the ozone oxidation process can realize the removal rate of the COD of the inlet water to be 400-600mg/L by treating high-concentration salt water, the COD value of the produced water to be 200-300mg/L is still a main influence factor for preventing the long-period stable operation of the three systems.
In the case of water inlet COD of 200-.
In order to further improve the efficient and stable operation of a salt separation or salt recycling system, a process technology that the COD of inlet water is 200-300mg/L and the COD of outlet water is lower than 100 mg/L or even lower than 50mg/L under the working conditions that the TDS of the high-salt organic wastewater is about 3-6% and the B/C ratio is less than 0.2 is urgently needed.
SUMMERY OF THE UTILITY MODEL
Aiming at the defects of the prior art, the utility model provides a treatment system for treating high-salinity organic wastewater with high precision, which combines activated carbon and ozone oxidation and has the characteristics of high ozone utilization rate, high COD removal efficiency and the like.
A treatment system for treating high-salinity organic wastewater with high precision comprises a water inlet pump, an internal circulating pump, a gas-water mixer and an active carbon adsorption reaction tower, wherein the gas-water mixer is provided with a water inlet and a gas inlet, the water inlet pump and the internal circulating pump are connected with the water inlet of the gas-water mixer through a pipeline, and the gas inlet of the gas-water mixer is connected with an ozone generator and a buffer tank;
a reaction tower inlet and an internal circulating pump inlet are symmetrically arranged on the side surface of the bottom of the activated carbon adsorption reaction tower, a reaction tower outlet is arranged at the top of the activated carbon adsorption reaction tower, the internal circulating pump inlet is connected with the internal circulating pump, the reaction tower inlet is connected with an outlet of a gas-water mixer, and the reaction tower outlet is connected with a gas-liquid separator;
the gas-liquid separator is also provided with a gas outlet and a water outlet, the gas outlet of the gas-liquid separator is connected with the buffer tank, and the buffer tank is also connected with an ozone tail gas destructor.
Preferably, a lower water distribution area, an activated carbon adsorption layer and an upper water distribution area are arranged inside the activated carbon adsorption reaction tower from bottom to top.
Preferably, the upper water distribution area and the lower water distribution area are both filled with distribution devices; the activated carbon adsorption layer is filled with activated carbon. The distribution device enables water to flow uniformly through the cross section of the upper water distribution area or the lower water distribution area.
Preferably, the distribution device is a water baffle, and a plurality of through holes are uniformly distributed on the water baffle.
Preferably, the height-diameter ratio of the activated carbon adsorption reaction tower is 6-10, the design pressure is 0.2MPa, and the working pressure is less than or equal to 0.1 MPa; the height of the activated carbon adsorption layer is more than or equal to 1 meter, and the interval between the activated carbon adsorption layer and the upper water distribution area and the interval between the activated carbon adsorption layer and the lower water distribution area are both more than or equal to 1 meter.
Preferably, the activated carbon is raw coal crushed activated carbon, the specification is 8-30 meshes, and the iodine value is more than 600.
Preferably, the gas-water mixer is any one of a dissolved air pump, a titanium aeration disc, a water ejector and a hydrodynamic cavitation mixer.
Preferably, the gas-liquid separator is a filler gas-liquid separator or a wire mesh gas-liquid separator.
Preferably, the ozone generator is a dielectric barrier discharge type ozone generator.
A treatment method for treating high-salinity organic wastewater with high precision adopts the treatment system to carry out treatment, and specifically comprises the following steps:
(1) the high-salinity organic wastewater and the internal circulating water are pressurized by a water inlet pump and an internal circulating pump respectively, mixed with ozone and backflow gas generated by an ozone generator by a gas-water mixer, and then enter an activated carbon adsorption reaction tower;
(2) the water entering the activated carbon adsorption reaction tower enters the activated carbon adsorption layer through the lower water distribution area, and then is collected by the upper water distribution area and enters the gas-liquid separator;
(3) after gas-water separation in the gas-liquid separator, qualified produced water is discharged from a water outlet of the gas-liquid separator, and gas is sucked by the gas-water mixer, passes through a buffer tank and enters the gas-water mixer;
(4) the constant pressure of the buffer tank is controlled, the constant pressure is not more than 0.1MPa, the overpressure exhaust gas enters the ozone tail gas destructor, and the concentration of ozone discharged by the ozone tail gas destructor is less than 0.1 mg/L.
The utility model has the advantages that:
(1) the utility model adopts the design of internal circulation and gas recovery, ensures that the utilization rate of ozone reaches more than 95 percent and is improved by more than 40 percent compared with the traditional ozone oxidation;
(2) fully-closed automatic operation, safety, environmental protection, stability and reliability
(3) The utility model combines the active carbon and the ozone oxidation process, partially enriches organic matters and ozone through active carbon micropore adsorption, improves mass transfer and reaction effects, and can regenerate the active carbon adsorption position after the organic matters are completely decomposed, carry out the next adsorption and reaction process, and solve the working conditions of about 3-6% of TDS (total dissolved solids) of high-salinity organic wastewater, less than 0.2 of B/C ratio, 300mg/L of COD (chemical oxygen demand) 200 and less than 100 mg/L of COD (chemical oxygen demand), even 50mg/L of process target.
Drawings
FIG. 1 is a schematic structural diagram of a treatment system for treating high-salinity organic wastewater with high precision, provided by the utility model;
wherein, 1, an activated carbon adsorption reaction tower; 2. an activated carbon adsorption layer; 3. a gas-water mixer; 4. a gas-liquid separator; 5. a buffer tank; 6. an ozone generator; 7. an ozone tail gas destructor; 8. a water inlet pump; 9. an internal circulation pump; 10. a lower water distribution area; 11. and an upper water distribution area.
Detailed Description
The utility model can be realized by adopting an ozone tail gas destructor in the prior art.
Example 1
A treatment system for treating high-salinity organic wastewater with high precision comprises a water inlet pump 8, an internal circulation pump 9, a gas-water mixer 3 and an activated carbon adsorption reaction tower 1, wherein the gas-water mixer 3 is provided with a water inlet and an air inlet, the water inlet pump 8 and the internal circulation pump 9 are connected with the water inlet of the gas-water mixer 3 through a pipeline, and the air inlet of the gas-water mixer 3 is connected with an ozone generator 6 and a buffer tank 5;
a reaction tower inlet and an inner circulating pump 9 inlet are symmetrically arranged on the side surface of the bottom of the activated carbon adsorption reaction tower 1, a reaction tower outlet is arranged at the top of the activated carbon adsorption reaction tower, the inner circulating pump inlet is connected with the inner circulating pump 9, the reaction tower inlet is connected with an outlet of the gas-water mixer 3, and the reaction tower outlet is connected with a gas-liquid separator 4;
still be provided with gas outlet and delivery port on the vapour and liquid separator 4, the gas outlet of vapour and liquid separator 4 links to each other with buffer tank 5, still be connected with ozone tail gas destroyer 7 on the buffer tank 5.
Example 2
In addition to the embodiment 1, a lower water distribution region 10, an activated carbon adsorption layer 2 and an upper water distribution region 11 are arranged inside the activated carbon adsorption reaction tower 1 from bottom to top.
Example 3
On the basis of the embodiment 2, the upper water distribution area 11 and the lower water distribution area 10 are both filled with distribution devices; and the activated carbon adsorption layer 2 is filled with activated carbon. The distribution means enables water to flow uniformly through the cross-section of the upper or lower distribution area 11, 10.
The distribution device is a water baffle plate, and a plurality of through holes are uniformly distributed on the water baffle plate.
Example 4
On the basis of the embodiment 3, the height-diameter ratio of the activated carbon adsorption reaction tower 1 is 6-10, the design pressure is 0.2MPa, and the working pressure is less than or equal to 0.1 MPa; the height of the active carbon adsorption layer 2 is more than or equal to 1 meter, and the interval between the active carbon adsorption layer 2 and the upper water distribution area 11 and the interval between the active carbon adsorption layer 2 and the lower water distribution area 10 are more than or equal to 1 meter.
Example 5
On the basis of example 4, the activated carbon is raw coal crushed activated carbon, the specification is 8-30 meshes, and the iodine value is more than 600.
The gas-water mixer 3 is any one of a dissolved air pump, a titanium aeration disc, a water ejector and a hydraulic cavitation mixer.
The gas-liquid separator 4 is a filler gas-liquid separator or a wire mesh gas-liquid separator.
The ozone generator 6 is a dielectric barrier discharge type ozone generator.
Example 6
A treatment method for treating high-salinity organic wastewater with high precision adopts the treatment system of the embodiment 2 to carry out treatment, and specifically comprises the following steps:
(1) the high-salinity organic wastewater and the internal circulating water are pressurized by a water inlet pump 8 and an internal circulating pump 9 respectively, mixed with ozone and backflow gas generated by an ozone generator 6 through a gas-water mixer 3 and then enter an activated carbon adsorption reaction tower 1;
(2) water entering the activated carbon adsorption reaction tower 1 is distributed by the lower water distribution area 10 and enters the activated carbon adsorption layer 2, and then is collected by the upper water distribution area 11 and enters the gas-liquid separator 4; the organic matters and ozone are locally enriched by the adsorption action of the activated carbon micropores, and after the organic matters are completely decomposed, the adsorption sites of the activated carbon are regenerated for the next adsorption and reaction process;
(3) after gas-water separation in the gas-liquid separator 4, qualified produced water is discharged from a water outlet of the gas-liquid separator 4, and gas is sucked by the gas-water mixer 3 and enters the gas-water mixer 3 through the buffer tank 5;
(4) the buffer tank 5 is controlled at constant pressure which is not more than 0.1MPa, the overpressure exhaust gas enters the ozone tail gas destructor 7, and the concentration of ozone discharged by the ozone tail gas destructor 7 is less than 0.1 mg/L.
Example 7
On the basis of the embodiment 6, the upper water distribution area 11 and the lower water distribution area 10 are both filled with distribution devices; the activated carbon adsorption layer 2 is filled with activated carbon; the distribution means enables water to flow uniformly through the cross-section of the upper or lower distribution area 11, 10.
The distribution device is a water baffle plate, and a plurality of through holes are uniformly distributed on the water baffle plate.
The height-diameter ratio of the activated carbon adsorption reaction tower 1 is 6-10, the design pressure is 0.2MPa, and the working pressure is less than or equal to 0.1 MPa; the height of the active carbon adsorption layer 2 is more than or equal to 1 meter, and the interval between the active carbon adsorption layer 2 and the upper water distribution area 11 and the interval between the active carbon adsorption layer 2 and the lower water distribution area 10 are more than or equal to 1 meter.
The activated carbon is raw coal crushed activated carbon, the specification is 8-30 meshes, and the iodine value is more than 600.
The air-water mixer 3 is any one of a dissolved air pump, a titanium aeration disc, a water ejector and a hydraulic cavitation mixer.
The gas-liquid separator 4 is a filler gas-liquid separator or a wire mesh gas-liquid separator.
The ozone generator 6 is a dielectric barrier discharge type ozone generator.
Example 8
On the basis of the embodiment 7, the height-diameter ratio of the activated carbon adsorption reaction tower 1 is 6, the design pressure is 0.2MPa, and the working pressure is less than or equal to 0.1 MPa; the height of the activated carbon adsorption layer 2 is 1 meter, and the interval between the activated carbon adsorption layer 2 and the upper water distribution area 11 and the interval between the activated carbon adsorption layer 2 and the lower water distribution area 10 are both 1 meter;
the adsorption capacity of the activated carbon for oxidizing COD is 0.04gCOD/gc, the adsorption redundancy of the activated carbon is 500 percent times, and the filling volume of the activated carbon is 3.14 m3；
The hydraulic retention time of the empty tower is 0.6h, the hour period number is 1.7 periods/h, and the flow of the water inlet pump 8 is 7.8 m3H, circulation pump flow rate 40 m3The air inlet flow of the ozone generator 6 is 4.2 kg/h;
the reverse osmosis concentrated brine inflow TDS of a certain coal chemical industry terminal zero-emission process is about 5.2 percent, B/C is 0.12, COD is 200ppm, the operation is continuously carried out for 72 hours, the COD of produced water is stably sampled every hour and is 50-80mg/L, the average COD is 64.2mg/L, the expected effect is achieved, and the ozone cost is about 36 yuan/delta CODkg (the oxygen price is 800 yuan/ton).
Therefore, the utility model adopts the design of internal circulation and gas recovery, improves the utilization rate of ozone, strengthens the mass transfer and reaction effects by combining the activated carbon and the ozone oxidation process, can control the operation cost within the range of the traditional ozone oxidation process when being used in a water treatment system with higher requirements on COD, and has better popularization significance.
Claims (9)
1. The utility model provides a high salt organic waste water's processing system is handled to high accuracy, includes intake pump (8), internal circulation pump (9), gas-water mixer (3) and active carbon adsorption reaction tower (1), be provided with water inlet and air inlet on gas-water mixer (3), its characterized in that:
the water inlet pump (8) and the internal circulating pump (9) are connected with a water inlet of the gas-water mixer (3) through a pipeline, and an ozone generator (6) and a buffer tank (5) are connected to a gas inlet of the gas-water mixer (3);
a reaction tower inlet and an internal circulating pump inlet are symmetrically arranged on the side surface of the bottom of the activated carbon adsorption reaction tower (1), a reaction tower outlet is arranged at the top of the activated carbon adsorption reaction tower, the internal circulating pump inlet is connected with an internal circulating pump (9), the reaction tower inlet is connected with an outlet of a gas-water mixer (3), and the reaction tower outlet is connected with a gas-liquid separator (4);
still be provided with gas outlet and delivery port on vapour and liquid separator (4), the gas outlet of vapour and liquid separator (4) links to each other with buffer tank (5), still be connected with ozone tail gas destructor (7) on buffer tank (5).
2. The system for treating high-salinity organic wastewater with high precision according to claim 1, is characterized in that: the interior of the activated carbon adsorption reaction tower (1) is provided with a lower water distribution area (10), an activated carbon adsorption layer (2) and an upper water distribution area (11) from bottom to top.
3. The system for treating high-salinity organic wastewater with high precision according to claim 2, characterized in that: the upper water distribution area (11) and the lower water distribution area (10) are both filled with distribution devices; and the activated carbon adsorption layer (2) is filled with activated carbon.
4. The system for treating high-salinity organic wastewater with high precision according to claim 3, characterized in that: the distribution device is a water baffle plate, and a plurality of through holes are uniformly distributed on the water baffle plate.
5. The system for treating high-salinity organic wastewater with high precision according to claim 3, characterized in that: the height-diameter ratio of the activated carbon adsorption reaction tower (1) is 6-10, the design pressure is 0.2MPa, and the working pressure is less than or equal to 0.1 MPa; the height of the active carbon adsorption layer (2) is more than or equal to 1 meter, and the interval between the active carbon adsorption layer (2) and the upper water distribution area (11) and the interval between the active carbon adsorption layer and the lower water distribution area (10) are both more than or equal to 1 meter.
6. The system for treating high-salinity organic wastewater with high precision according to claim 3, characterized in that: the activated carbon is raw coal crushed activated carbon with the specification of 8-30 meshes.
7. The system for treating high-salinity organic wastewater with high precision according to claim 1, is characterized in that: the gas-water mixer (3) is any one of a dissolved air pump, a titanium aeration disc, a water ejector and a hydraulic cavitation mixer.
8. The system for treating high-salinity organic wastewater with high precision according to claim 1, is characterized in that: the gas-liquid separator (4) is a filler gas-liquid separator or a wire mesh gas-liquid separator.
9. The system for treating high-salinity organic wastewater with high precision according to claim 1, is characterized in that: the ozone generator (6) is a dielectric barrier discharge type ozone generator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121412471.5U CN216972179U (en) | 2021-06-24 | 2021-06-24 | High-precision treatment system for high-salt organic wastewater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121412471.5U CN216972179U (en) | 2021-06-24 | 2021-06-24 | High-precision treatment system for high-salt organic wastewater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216972179U true CN216972179U (en) | 2022-07-15 |
Family
ID=82338352
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202121412471.5U Active CN216972179U (en) | 2021-06-24 | 2021-06-24 | High-precision treatment system for high-salt organic wastewater |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN216972179U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113233653A (en) * | 2021-06-24 | 2021-08-10 | 陕西省石油化工研究设计院 | Treatment system and method for treating high-salinity organic wastewater with high precision |
-
2021
- 2021-06-24 CN CN202121412471.5U patent/CN216972179U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113233653A (en) * | 2021-06-24 | 2021-08-10 | 陕西省石油化工研究设计院 | Treatment system and method for treating high-salinity organic wastewater with high precision |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202766327U (en) | High-efficiency recyclable photocatalysis industrial wastewater treatment device | |
| CN212151749U (en) | High-efficient ozone catalytic oxidation processing apparatus of high salt waste water | |
| CN102276121A (en) | Process and system for treating reverse osmosis concentrated water of cold rolling steel mill | |
| CN201762209U (en) | Integrally combined device for recycling coking wastewater | |
| CN109264845A (en) | A kind of device and method of reverse osmosis concentrated water organic matter and ammonia nitrogen removal simultaneously | |
| CN203833777U (en) | Treatment device for ozone oxidation treatment leachate nanofiltration concentrated solution | |
| CN104355369A (en) | Device for removing nitrate nitrogen in water and application method of device | |
| CN216972179U (en) | High-precision treatment system for high-salt organic wastewater | |
| CN105417843A (en) | Treatment method achieving zero release of leachate in municipal domestic garbage incineration plant | |
| CN102234166A (en) | Three-dimensional electrolytic oxidation and membrane separation integrated industrial waste water recycling process | |
| CN113233653A (en) | Treatment system and method for treating high-salinity organic wastewater with high precision | |
| CN217677209U (en) | Coking wastewater recycling treatment system | |
| CN216236582U (en) | Concentrated water denitrification processing apparatus of MABR reverse osmosis | |
| CN102616991B (en) | Method and equipment for sewage treatment by means of biochemical pressurized dissolved air flotation | |
| CN105565541A (en) | Integrated process and equipment for eutrophic water body control | |
| CN206570116U (en) | A kind of waste water by ozone catalytic oxidizing equipment | |
| CN211170274U (en) | Full-quantitative treatment system for percolate of old refuse landfill | |
| CN211170310U (en) | Old garbage landfill leachate treatment system | |
| CN209128117U (en) | A kind of device of reverse osmosis concentrated water organic matter and ammonia nitrogen removal simultaneously | |
| CN203159385U (en) | Treatment and reuse system for polymerization centrifugation mother liquor | |
| CN204237642U (en) | A kind of special purpose device of Coal Chemical Industry haline water purification process technique | |
| CN210505820U (en) | Dissolved gas catalytic oxidation composite treatment system | |
| CN210140512U (en) | Environment-friendly RO reverse osmosis effluent treatment plant of cycle recycle | |
| CN210133954U (en) | Continuous reactor for treating wet desulphurization wastewater | |
| CN207862069U (en) | A kind of high salinity high rigidity organic concentration waste water treatment system difficult to degrade |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |