CN211284022U - Integrated equipment for treating refractory wastewater - Google Patents
Integrated equipment for treating refractory wastewater Download PDFInfo
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- CN211284022U CN211284022U CN201922071658.2U CN201922071658U CN211284022U CN 211284022 U CN211284022 U CN 211284022U CN 201922071658 U CN201922071658 U CN 201922071658U CN 211284022 U CN211284022 U CN 211284022U
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Abstract
The utility model belongs to the technical field of wastewater treatment equipment, in particular to an integrated device for treating refractory wastewater, which comprises a dosing reaction component, an aeration tank, a sedimentation tank, a releaser, a raw water tank, a middle water tank, an electrooxidation clean water tank and an outer shell, wherein the dosing reaction component comprises a sodium hydroxide dosing tank, a sodium sulfate dosing tank and a polyacrylamide dosing tank, and the sodium hydroxide dosing tank, the sodium sulfate dosing tank and the polyacrylamide dosing tank are respectively provided with a first stirrer; can be through a series of purifications to waste water, discharge the waste water after purifying into the electrooxidation clear water pond again, then come to carry out the electrolysis to getting into wherein water through electrooxidation clear water pond, it can discharge through the evacuation pipe to decompose into oxygen and hydrogen to the water, the impurity people that the waste water electrolysis after the purification produced can clear up through the blow off pipe, then concentrate the transportation and purify the place to the specialty and handle, can reduce the volume in pollution sources, the people's of being convenient for transportation.
Description
Technical Field
The utility model belongs to the technical field of waste water treatment equipment, concretely relates to handle difficult degradation waste water integration equipment.
Background
With the continuous development of modern industry, a large amount of organic compounds are widely used in human production and life, and various waste waters containing organic pollutants difficult to biodegrade are increasing. The waste water generally has the characteristics of high pollutant concentration, high toxicity and poor biodegradability, causes serious pollution to water environment and directly threatens the health of human beings.
The existing wastewater treatment method can not completely purify water, industrial wastewater can also contain some pollution sources after purification, the discharged wastewater which is not completely purified can cause external environment to be polluted to a certain extent, people are required to transport the wastewater to a professional purification site for purification, but the larger volume of the wastewater pollution source can be unfavorable for people to transport the wastewater.
Disclosure of Invention
An object of the utility model is to provide a handle difficult degradation waste water integration equipment to solve the problem that proposes in the above-mentioned background art.
In order to achieve the above object, the utility model provides a following technical scheme: an integrated device for treating refractory wastewater comprises a dosing reaction component, an aeration tank, a sedimentation tank, a releaser, a raw water tank, an intermediate water tank, an electrooxidation clean water tank and an outer shell, wherein the dosing reaction component comprises a sodium hydroxide dosing tank, a sodium sulfate dosing tank and a polyacrylamide dosing tank, the sodium hydroxide dosing tank, the sodium sulfate dosing tank and the polyacrylamide dosing tank are respectively provided with a first stirrer, the first stirrer is electrically connected with an external power supply, an aeration pipe is arranged inside the aeration tank, the input end of the aeration tank is connected with a water inlet pipe, the water inlet pipe is provided with a sodium hydroxide dosing pump, the water inlet pipe is provided with a sodium sulfate dosing pump, the water inlet pipe is fixedly connected with a mixer, the output end of the water inlet pipe is connected with the input end of the aeration tank, the input end of the air blower is connected with an air blower, and the air blower is electrically connected with the external, the input end of the sedimentation water tank is connected with the output end of the aeration tank, the sedimentation water tank is provided with a conductivity electrode, the conductivity electrode is electrically connected with an external power supply, the sedimentation water tank is provided with a PH electrode, the PH electrode is electrically connected with the external power supply, the sedimentation water tank is provided with a polyacrylamide dosing pump, the input end of the polyacrylamide dosing pump is connected with the polyacrylamide dosing tank, the output end of the polyacrylamide dosing pump is connected with the sedimentation water tank, the polyacrylamide dosing pump is electrically connected with the external power supply, the sedimentation water tank is fixedly connected with a second stirring machine, the second stirring machine is electrically connected with the external power supply, the output end of the releaser is connected with the first input end of the dissolved air tank, the second input end of the dissolved air tank is connected with the output end of an air compressor, and the air compressor is electrically connected, the utility model discloses a device for producing waste water, including dissolved gas jar, sediment pond, electric oxidation clean water pond, dissolving gas jar, sediment pond, electric oxidation clean water pond, outer shell body top fixedly connected with weather enclosure, dissolve gas jar output with the first input of middle pond is connected, sediment pond output with the former pond input is connected, the former pond output with middle pond second input is connected, middle pond output is connected with sand rate ware input, sand rate ware output with the electric oxidation clean water pond input is connected, be equipped with electric catalytic oxidation equipment on the electric oxidation clean water pond, electric catalytic oxidation equipment and external power source electric connection, fixedly connected with blow off pipe on the electric oxidation clean water pond, fixedly connected with evacuation pipe on the electric oxidation clean water pond.
Preferably, the dosing reaction assembly, the aeration tank, the sedimentation water tank, the releaser, the raw water tank, the intermediate water tank and the electro-oxidation clean water tank are connected through pipelines.
Preferably, the input end of the sodium hydroxide dosing pump is connected with the sodium hydroxide dosing tank, the output end of the sodium hydroxide dosing pump is connected with the water inlet pipe, and the sodium hydroxide dosing pump is electrically connected with an external power supply.
Preferably, the sodium sulfate dosing pump input end with the sodium sulfate dosing tank is connected, the sodium sulfate dosing pump output end with advance water piping connection, the sodium sulfate dosing pump with external power source electric connection.
Preferably, the outer shell is hinged with an access door through a rotating shaft.
Preferably, a plurality of symmetrically distributed observation windows are arranged on the outer shell.
Compared with the prior art, the beneficial effects of the utility model are that:
when using this device, can be through a series of purifications to waste water, discharge the waste water after purifying into the electrooxidation clear water pond again, then come to carry out the electrolysis to getting into wherein water through the electrooxidation clear water pond, decompose into oxygen and hydrogen to the water and can discharge through the evacuation pipe, the impurity people that the waste water electrolysis after purifying produced can clear up through the blow off pipe, then concentrate the transportation to professional purification place and handle, can reduce the volume of pollution sources, be convenient for people's transportation.
Drawings
The accompanying drawings are included to provide a further understanding of the invention, and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention, and together with the description serve to explain the invention and not to limit the invention. In the drawings:
fig. 1 is a schematic structural view of the present invention;
fig. 2 is a schematic structural view of the outer shell of the present invention;
fig. 3 is a schematic structural diagram of the middle dosing reaction assembly, the aeration tank and the sedimentation tank of the present invention.
In the figure: 1. a dosing reaction assembly; 11. a sodium hydroxide dosing tank; 12. a sodium sulfate dosing tank; 13. a polyacrylamide dosing tank; 14. a first mixer; 2. an aeration tank; 21. an aeration pipe; 22. a water inlet pipe; 221. a sodium hydroxide dosing pump; 222. a sodium sulfate dosing pump; 223. a mixer; 23. a blower; 3. a sedimentation water tank; 31. a conductivity electrode; 32. a PH electrode; 33. a polyacrylamide dosing pump; 34. a second mixer; 4. a releaser; 41. a dissolved air tank; 42. an air compressor; 5. a raw water pool; 6. a middle water tank; 61. a sand rate device; 7. an electro-oxidation clean water tank; 71. an electrocatalytic oxidation device; 72. a blow-off pipe; 73. emptying the pipe; 8. an outer housing; 81. a rain-proof shed; 82. a rotating shaft; 83. an access door; 84. and (4) an observation window.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1-3, the present invention provides the following technical solutions: an integrated device for treating refractory wastewater comprises a dosing reaction component 1, an aeration tank 2, a precipitation tank 3, a releaser 4, a raw water tank 5, an intermediate water tank 6, an electrooxidation clean water tank 7 and an outer shell 8, wherein the dosing reaction component 1 comprises a sodium hydroxide dosing tank 11, a sodium sulfate dosing tank 12 and a polyacrylamide dosing tank 13, the sodium hydroxide dosing tank 11, the sodium sulfate dosing tank 12 and the polyacrylamide dosing tank 13 are respectively provided with a first stirrer 14, the first stirrer 14 is electrically connected with an external power supply, an aeration pipe 21 is arranged inside the aeration tank 2, the input end of the aeration tank 2 is connected with a water inlet pipe 22, the water inlet pipe 22 is provided with a sodium hydroxide dosing pump 221, the model of the sodium hydroxide dosing pump 221 is FP65-50-150-4KW, the water inlet pipe 22 is provided with a sodium sulfate dosing pump 222, the model of the sodium sulfate dosing pump 222 is FP65-50-150-4KW, the mixer 223 is fixedly connected on the water inlet pipe 22, the output end of the water inlet pipe 22 is connected with the input end of the aeration tank 2, the input end of the aeration pipe 21 is connected with the blower 23, the blower 23 is electrically connected with an external power supply, the input end of the sedimentation tank 3 is connected with the output end of the aeration tank 2, the sedimentation tank 3 is provided with the conductivity electrode 31, the conductivity electrode 31 is electrically connected with the external power supply, the sedimentation tank 3 is provided with the PH electrode 32, the PH electrode 32 is electrically connected with the external power supply, the sedimentation tank 3 is provided with the polyacrylamide dosing pump 33, the input end of the polyacrylamide dosing pump 33 is connected with the polyacrylamide dosing tank 13, the output end of the polyacrylamide dosing pump 33 is connected with the sedimentation tank 3, the model of the polyacrylamide dosing pump 33 is FP65-50-150-4KW, the polyacrylamide dosing pump 33 is electrically connected with the external power supply, second mixer 34 and external power source electric connection, the 4 output of releaser is connected with the first input of dissolved gas jar 41, dissolved gas jar 41 second input is connected with air compressor machine 42 output, air compressor machine 42 and external power source electric connection, dissolved gas jar 41 output is connected with the first input of middle pond 6, 3 outputs in sedimentation pond are connected with former pond 5 inputs, 5 outputs in former pond are connected with middle pond 6 second inputs, 6 outputs in middle pond are connected with sand rate ware 61 input, sand rate ware 61 output is connected with the input of electrooxidation clean water pond 7, be equipped with electrocatalytic oxidation equipment 71 on electrooxidation clean water pond 7, electrocatalytic oxidation equipment 71 and external power source electric connection, fixedly connected with blow off pipe 72 on electrooxidation clean water pond 7, fixedly connected with evacuation pipe 73 on electrooxidation clean water pond 7, outer shell 8 top fixedly connected with weather enclosure 81.
In this embodiment: the dosing reaction component 1 comprises a sodium hydroxide dosing tank 11, a sodium sulfate dosing tank 12 and a polyacrylamide dosing tank 13, wherein the sodium hydroxide dosing tank 11, the sodium sulfate dosing tank 12 and the polyacrylamide dosing tank 13 are respectively provided with a first stirrer 14, the first stirrer 14 is electrically connected with an external power supply, medicaments can be added into the sodium hydroxide dosing tank 11, the sodium sulfate dosing tank 12 and the polyacrylamide dosing tank 13, then the medicaments are uniformly stirred by the first stirrer 14, an aeration pipe 21 is arranged inside an aeration tank 2, the input end of the aeration tank 2 is connected with a water inlet pipe 22, a sodium hydroxide dosing pump 221 is arranged on the water inlet pipe 22, a sodium sulfate dosing pump 222 is arranged on the water inlet pipe 22, a mixer 223 is fixedly connected on the water inlet pipe 22, the output end of the water inlet pipe 22 is connected with the input end of the aeration tank 2, the input end of the aeration pipe 21 is connected with a blower 23, and the blower 23 is electrically connected with the external power, when wastewater enters the aeration tank 2 through the water inlet pipe 22, the sodium hydroxide dosing pump 221 on the water inlet pipe 22 can convey the adjusted medicament in the sodium hydroxide dosing tank 11 to the water inlet pipe 22, the sodium sulfate dosing pump 222 can convey the adjusted medicament in the sodium sulfate dosing tank 12 to the water inlet pipe 22, thereby purifying the wastewater in the water inlet pipe 22, then two medicaments can be mixed with the wastewater through the mixer 223 and then enter the aeration tank 2, the blower 23 is started to aerate the wastewater in the aeration tank 2 through the aeration pipe 21, so that the wastewater and the medicament are fully mixed together, the input end of the sedimentation tank 3 is connected with the output end of the aeration tank 2, the sedimentation tank 3 is provided with the conductivity electrode 31, the conductivity electrode 31 is electrically connected with an external power supply, the sedimentation tank 3 is provided with the PH electrode 32, and the PH electrode 32 is electrically connected with the external power supply, a polyacrylamide dosing pump 33 is arranged on the sedimentation water tank 3, the input end of the polyacrylamide dosing pump 33 is connected with the polyacrylamide dosing tank 13, the output end of the polyacrylamide dosing pump 33 is connected with the sedimentation water tank 3, the polyacrylamide dosing pump 33 is electrically connected with an external power supply, the sedimentation water tank 3 is fixedly connected with a second stirrer 34, the second stirrer 34 is electrically connected with the external power supply, water in the aeration tank 2 can enter the sedimentation water tank 3, the wastewater in the sedimentation water tank 3 can be purified by electrifying the conductivity electrode 31 and the PH electrode 32 at the moment, then the medicament in the polyacrylamide dosing tank 13 is conveyed to the inside of the sedimentation water tank by the polyacrylamide dosing pump 33, then the second stirrer 34 is started, sludge and impurities in the wastewater are adsorbed by polyacrylamide, the output end of the releaser 4 is connected with the first input end of the dissolved gas tank 41, the second input end of the dissolved air tank 41 is connected with the output end of the air compressor 42, the air compressor 42 is electrically connected with an external power supply, the output end of the dissolved air tank 41 is connected with the first input end of the intermediate water pool 6, the output end of the sedimentation water pool 3 is connected with the input end of the raw water pool 5, the output end of the raw water pool 5 is connected with the second input end of the intermediate water pool 6, the output end of the intermediate water pool 6 is connected with the input end of the sand ratio device 61, the output end of the sand ratio device 61 is connected with the input end of the electrooxidation clean water pool 7, the electrooxidation clean water pool 7 is provided with the electrocatalytic oxidation device 71, the electrocatalytic oxidation device 71 is electrically connected with the external power supply, the sewage discharge pipe 72 is fixedly connected with the electrooxidation clean water pool 7, the emptying pipe 73 is fixedly connected with the electrooxidation clean water pool 7, the purified waste water, decompose into oxygen and hydrogen to the water and can discharge through evacuation pipe 73, the impurity people that the waste water electrolysis after the purification produced can clear up through blow off pipe 72, then concentrate and transport to the specialty and purify the place and handle, can reduce the volume in pollution sources, the transportation of the people of being convenient for, 8 top fixedly connected with weather enclosure 81 of shell body can prevent through weather enclosure 81 that outside rainwater from entering into the inside of device.
Specifically, the dosing reaction assembly 1, the aeration tank 2, the sedimentation water tank 3, the releaser 4, the raw water tank 5, the intermediate water tank 6 and the electro-oxidation clean water tank 7 are connected through pipelines; the sealed connection between the devices is facilitated by the tubing.
Specifically, the input end of the sodium hydroxide dosing pump 221 is connected with the sodium hydroxide dosing tank 11, the output end of the sodium hydroxide dosing pump 221 is connected with the water inlet pipe 22, and the sodium hydroxide dosing pump 221 is electrically connected with an external power supply; the agent in the sodium hydroxide dosing tank 11 can be transported to the inside of the water inlet pipe 22 by the sodium hydroxide dosing pump 221.
Specifically, the input end of the sodium sulfate dosing pump 222 is connected with the sodium sulfate dosing tank 12, the output end of the sodium sulfate dosing pump 222 is connected with the water inlet pipe 22, and the sodium sulfate dosing pump 222 is electrically connected with an external power supply; the sodium sulfate dosing pump 222 can feed the chemical in the sodium sulfate dosing tank 12 to the inside of the water inlet pipe 22.
Specifically, the outer shell 8 is hinged with an access door 83 through a rotating shaft 82; maintenance and repair of the devices inside the outer case 8 can be performed through the access door 83.
Specifically, the outer shell 8 is provided with a plurality of symmetrically distributed observation windows 84; the observation window 84 is convenient for people to observe the inside of the outer shell 8 at any time.
The utility model discloses a theory of operation and use flow: when wastewater enters the aeration tank 2 through the water inlet pipe 22, the sodium hydroxide dosing pump 221 on the water inlet pipe 22 can convey the adjusted medicament in the sodium hydroxide dosing tank 11 to the water inlet pipe 22, the sodium sulfate dosing pump 222 can convey the adjusted medicament in the sodium sulfate dosing tank 12 to the water inlet pipe 22, so that wastewater in the water inlet pipe 22 is purified, then two medicaments can be mixed with the wastewater through the mixer 223 and then enter the aeration tank 2, the blower 23 is started to aerate the wastewater in the aeration tank 2 through the aeration pipe 21, so that the wastewater and the medicament are fully mixed together, the water in the aeration tank 2 can enter the sedimentation tank 3, at the moment, the conductivity electrode 31 and the pH electrode 32 are electrified to purify the wastewater in the sedimentation tank 3, and then the polyacrylamide dosing pump 33 is used, carry the inside of sedimentation pond to the inside medicament of polyacrylamide dosing tank 13, reopen second mixer 34, adsorb silt and impurity in the waste water through polyacrylamide, waste water after the purification can be discharged in the clean water basin 7 of electrooxidation, then come to electrolyze entering wherein water through the electrocatalytic oxidation equipment 71 on the clean water basin 7 of electrooxidation, it can be discharged through exhaust pipe 73 to decompose into oxygen and hydrogen to the water, the impurity people that the waste water electrolysis after the purification produced can clear up through blow off pipe 72, then concentrate the transportation to the specialty and purify the place and handle, can reduce the volume of pollution sources, be convenient for people's transportation.
Finally, it should be noted that: although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications may be made to the embodiments described in the foregoing embodiments, or equivalents may be substituted for elements thereof. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (6)
1. The utility model provides a handle difficult degradation waste water integration equipment, its characterized in that, including adding medicine reaction unit (1), aeration tank (2), sedimentation tank (3), releaser (4), former pond (5), middle pond (6), electrooxidation clean water pond (7) and shell body (8), add medicine reaction unit (1) including sodium hydroxide with medicine pond (11), sodium sulfate with medicine pond (12) and polyacrylamide with medicine pond (13), all be equipped with first mixer (14) on sodium hydroxide with medicine pond (11), sodium sulfate with medicine pond (12) and the polyacrylamide with medicine pond (13), first mixer (14) and external power source electric connection, aeration tank (2) inside is equipped with aeration pipe (21), aeration tank (2) input is connected with inlet tube (22), be equipped with sodium hydroxide with medicine pump (221) on inlet tube (22), a sodium sulfate dosing pump (222) is arranged on the water inlet pipe (22), a mixer (223) is fixedly connected to the water inlet pipe (22), the output end of the water inlet pipe (22) is connected with the input end of the aeration tank (2), the input end of the aeration pipe (21) is connected with a blower (23), and the blower (23) is electrically connected with an external power supply;
the input end of the sedimentation water tank (3) is connected with the output end of the aeration tank (2), the sedimentation water tank (3) is provided with a conductivity electrode (31), the conductivity electrode (31) is electrically connected with an external power supply, a PH electrode (32) is arranged on the sedimentation water tank (3), the PH electrode (32) is electrically connected with an external power supply, a polyacrylamide dosing pump (33) is arranged on the sedimentation water tank (3), the input end of the polyacrylamide dosing pump (33) is connected with the polyacrylamide dosing tank (13), the output end of the polyacrylamide dosing pump (33) is connected with the sedimentation water tank (3), the polyacrylamide dosing pump (33) is electrically connected with an external power supply, the sedimentation water tank (3) is fixedly connected with a second stirrer (34), and the second stirrer (34) is electrically connected with the external power supply;
the output end of the releaser (4) is connected with the first input end of the dissolved air tank (41), the second input end of the dissolved air tank (41) is connected with the output end of the air compressor (42), the air compressor (42) is electrically connected with an external power supply, and the output end of the dissolved air tank (41) is connected with the first input end of the intermediate water pool (6);
the output end of the sedimentation water tank (3) is connected with the input end of the raw water tank (5), the output end of the raw water tank (5) is connected with the second input end of the intermediate water tank (6), the output end of the intermediate water tank (6) is connected with the input end of the sand rate device (61), the output end of the sand rate device (61) is connected with the input end of the electrooxidation clean water tank (7), an electrocatalytic oxidation device (71) is arranged on the electrooxidation clean water tank (7), the electrocatalytic oxidation device (71) is electrically connected with an external power supply, a drain pipe (72) is fixedly connected to the electrooxidation clean water tank (7), and an emptying pipe (73) is fixedly connected to the electrooxidation clean water tank (7);
the top of the outer shell (8) is fixedly connected with a rainproof shed (81).
2. The integrated equipment for treating refractory wastewater according to claim 1, characterized in that: the chemical feeding reaction assembly (1), the aeration tank (2), the sedimentation water tank (3), the releaser (4), the raw water tank (5), the intermediate water tank (6) and the electro-oxidation clean water tank (7) are connected through pipelines.
3. The integrated equipment for treating refractory wastewater according to claim 1, characterized in that: the sodium hydroxide dosing pump (221) input end with sodium hydroxide dosing pool (11) is connected, sodium hydroxide dosing pump (221) output end with inlet tube (22) is connected, sodium hydroxide dosing pump (221) and external power source electric connection.
4. The integrated equipment for treating refractory wastewater according to claim 1, characterized in that: the sodium sulfate dosing pump (222) input with sodium sulfate dosing tank (12) are connected, sodium sulfate dosing pump (222) output with inlet tube (22) are connected, sodium sulfate dosing pump (222) and external power source electric connection.
5. The integrated equipment for treating refractory wastewater according to claim 1, characterized in that: the outer shell (8) is hinged with an access door (83) through a rotating shaft (82).
6. The integrated equipment for treating refractory wastewater according to claim 1, characterized in that: the outer shell (8) is provided with a plurality of symmetrically distributed observation windows (84).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922071658.2U CN211284022U (en) | 2019-11-27 | 2019-11-27 | Integrated equipment for treating refractory wastewater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922071658.2U CN211284022U (en) | 2019-11-27 | 2019-11-27 | Integrated equipment for treating refractory wastewater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211284022U true CN211284022U (en) | 2020-08-18 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201922071658.2U Active CN211284022U (en) | 2019-11-27 | 2019-11-27 | Integrated equipment for treating refractory wastewater |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN211284022U (en) |
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2019
- 2019-11-27 CN CN201922071658.2U patent/CN211284022U/en active Active
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Address after: 518118 4F, Building A, Phase II Jiahongwan Garden, Pingshan Street, Pingshan New District, Shenzhen City, Guangdong Province Patentee after: Jingzhu environmental protection (Shenzhen) Co.,Ltd. Address before: 518118 4F, Building A, Phase II Jiahongwan Garden, Pingshan Street, Pingshan New District, Shenzhen City, Guangdong Province Patentee before: Huihe Environmental Protection (Shenzhen) Co.,Ltd. |