CN216426975U - Integrated sewage treatment equipment - Google Patents
Integrated sewage treatment equipment Download PDFInfo
- Publication number
- CN216426975U CN216426975U CN202122604480.0U CN202122604480U CN216426975U CN 216426975 U CN216426975 U CN 216426975U CN 202122604480 U CN202122604480 U CN 202122604480U CN 216426975 U CN216426975 U CN 216426975U
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- Prior art keywords
- treatment area
- water
- ozone
- box
- laminar flow
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- 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.)
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- 238000011282 treatment Methods 0.000 title claims abstract description 79
- 239000010865 sewage Substances 0.000 title claims abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 71
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 37
- 238000000926 separation method Methods 0.000 claims abstract description 15
- 238000009792 diffusion process Methods 0.000 claims abstract description 14
- 239000007788 liquid Substances 0.000 claims abstract description 14
- 239000011941 photocatalyst Substances 0.000 claims abstract description 8
- 230000010354 integration Effects 0.000 claims abstract description 5
- 238000005273 aeration Methods 0.000 claims description 3
- 239000002893 slag Substances 0.000 claims 2
- 238000004065 wastewater treatment Methods 0.000 claims 1
- 241000894006 Bacteria Species 0.000 abstract description 6
- 241000195493 Cryptophyta Species 0.000 abstract description 6
- 241000700605 Viruses Species 0.000 abstract description 6
- 238000001914 filtration Methods 0.000 abstract description 6
- 230000007613 environmental effect Effects 0.000 abstract description 4
- 230000005611 electricity Effects 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 11
- 239000002957 persistent organic pollutant Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- CVOFKRWYWCSDMA-UHFFFAOYSA-N 2-chloro-n-(2,6-diethylphenyl)-n-(methoxymethyl)acetamide;2,6-dinitro-n,n-dipropyl-4-(trifluoromethyl)aniline Chemical compound CCC1=CC=CC(CC)=C1N(COC)C(=O)CCl.CCCN(CCC)C1=C([N+]([O-])=O)C=C(C(F)(F)F)C=C1[N+]([O-])=O CVOFKRWYWCSDMA-UHFFFAOYSA-N 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000004332 deodorization Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000010977 unit operation Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Images
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- Treatment Of Water By Oxidation Or Reduction (AREA)
- Physical Water Treatments (AREA)
Abstract
The utility model relates to the technical field of environmental protection, in particular to sewage treatment integration equipment. The power distribution box comprises a box body, be equipped with treatment area and lower treatment area in the box, go up the treatment area top and seted up the water inlet, upward be equipped with solid-liquid separation equipment in the treatment area, go up treatment area and pass through water conservancy diversion mouth intercommunication with lower treatment area, be equipped with a plurality of laminar flows board from last level down in the lower treatment area, be equipped with ozone diffusion equipment between the diapire of the laminar flow board of below and box, the backward flow mouth has been seted up to the last lateral wall of lower treatment area, the delivery port has been seted up to the lower lateral wall of lower treatment area, through water pipeline intercommunication between backward flow mouth and the delivery port, the top of box is equipped with ozone concentration sensor, be equipped with water quality sensor in the box, ozone concentration sensor, ozone diffusion equipment, water quality sensor all is connected with the controller electricity. Compared with the prior art, the utility model discloses filtration efficiency is high, utilizes ozone, ultraviolet ray, photocatalyst etc. to thoroughly exterminate bacterium, virus and the algae of aquatic, can extensively use widely.
Description
Technical Field
The utility model relates to the technical field of environmental protection, in particular to sewage treatment integration equipment.
Background
With the increasing serious problem of water pollution, organic pollutants in water have obvious toxic action on human bodies and organisms, and the elimination of the organic pollutants in water has become an important subject in the field of environmental protection. The solid-liquid separation is an important unit operation for sewage treatment, is an important component of heterogeneous separation, and has high and low technical level, and the quality of the solid-liquid separation directly influences the possibility of realizing industrial scale production, the advancement and reliability of the process, the product quality, the energy consumption, the environmental protection and other economic and social benefits. The existing solid-liquid separation equipment is generally divided into two categories, one category is that sewage is directly poured into a separation device to be kept stand and filtered, although the cost is saved, the filtering efficiency is low, and the filter screen needs to be cleaned manually at regular intervals, which is inconvenient, the second category is that solid matters in the sewage are crushed firstly and then filtered, but various components in waste materials are more, the sewage is polluted again after being crushed, the subsequent filtering force needs to be increased, the sewage can reach the discharge standard, and the cost is increased; ozone has strong oxidation performance, can be automatically decomposed in water in a short time, has no secondary pollution, and is an ideal green oxidation water treatment agent which is already utilized in the aspects of drinking water, industrial wastewater and domestic sewage treatment, sterilization and disinfection, deodorization, peculiar smell removal and the like. However, if ozone is used alone to mineralize the pollutants which are difficult to be biodegraded into carbon dioxide and water, the ozone dosage is large, the required cost is too high, the economy is poor, and the ozone cannot be applied to large scale in practical engineering.
SUMMERY OF THE UTILITY MODEL
To the deficiency of the background art, the utility model provides a sewage treatment integrated equipment.
The utility model adopts the technical scheme as follows: sewage treatment integration equipment, the key lies in: the improved water treatment device comprises a box body, be equipped with treatment area and lower treatment area in the box, go up the treatment area top and seted up the water inlet, upward be equipped with solid-liquid separation equipment in the treatment area, go up the treatment area with the treatment area passes through water conservancy diversion mouth intercommunication down, be equipped with a plurality of laminar flow boards from last to the level down in the treatment area down, the below laminar flow board with be equipped with ozone diffusion equipment between the diapire of box, the backward flow mouth has been seted up to the last lateral wall in treatment area down, the delivery port has been seted up to the lower lateral wall in treatment area down, through water pipeline intercommunication between backward flow mouth and the delivery port, the top in treatment area is equipped with ozone concentration sensor down, be equipped with water quality sensor in the box, ozone concentration sensor, ozone diffusion equipment, water quality sensor all are connected with the controller electricity. The effect of the proposal is that the solid-liquid separation device in the upper treatment area is used for separating the sewage from solid impurities, thereby achieving the filtering effect, removing the solid in the sewage and achieving the primary sewage filtering effect; the ozone diffusion device in the lower treatment area thoroughly kills bacteria, viruses and algae in water and oxidizes and decomposes the bacteria, viruses and algae together with other organic pollutants, so that the bacteria, viruses and algae cannot be accumulated in the water purifier, the water purifier keeps clean while purifying water, the treatment time of the water body is prolonged in a water backflow mode, and the ozone addition amount is controlled by the linkage of the ozone backflow and the ozone concentration sensor and the ozone diffusion device.
Preferably, the ozone diffusion device includes driving motor, driving motor's base pass through the support with box fixed connection, driving motor's the vertical downwardly extending of output shaft is connected with the air guide and is responsible for, be connected with a plurality of air guide branch pipes on the air guide is responsible for, the aeration hole has been seted up on the air guide branch pipe, the lower extreme that the air guide was responsible for is worn out the box is connected with rotary joint, rotary joint is connected with ozone generator. The effect of this scheme is that driving motor drive air guide main pipe rotates to make the ozone in the leading-in device distribute more evenly in the water.
Preferably, the solid-liquid separation device is including the pivot of horizontal setting, be equipped with helical blade in the pivot, helical blade's outer edge with go up the contact of disposal area inner wall, the one end of pivot is worn out the box is connected with the motor, the water inlet with the water conservancy diversion mouth is close to the motor sets up, go up the disposal area and seted up the slagging scorification mouth, the slagging scorification mouth is close to the other end setting of pivot. The effect of this scheme is that under helical blade's promotion, solid impurity is constantly discharged from the slagging-off mouth, and liquid flows in gradually from the clearance between helical blade and the last treatment zone to flow into lower treatment zone through the guiding opening, reach solid-liquid separation purpose.
Preferably, the diversion port is provided with a filter screen. The effect of this solution is to avoid filter residues entering the lower treatment zone.
Preferably, the water outlet and the water inlet are respectively arranged close to the uppermost laminar flow plate and the lowermost laminar flow plate.
Preferably, a plurality of laminar flow plates are arranged in a staggered mode. The effect of this scheme is that can prolong the contact time of water and laminar flow board, improves water purification efficiency.
Preferably, the water pipeline comprises a water outlet pipe, the water outlet pipe is provided with an electromagnetic valve, the electromagnetic valve is connected with a return pipe, and the water inlet end of the return pipe is connected with the return port. The effect of this scheme is that can be according to the quality of water condition, control water body backward flow and the situation of intaking.
Preferably, the return pipe is provided with a circulating pump. The effect of this scheme is can accelerate the flow of water.
Preferably, the surface of each laminar flow plate is coated with a photocatalyst, and an ultraviolet lamp is arranged between every two adjacent laminar flow plates. The scheme has the effects that bacteria, viruses and algae in water are thoroughly killed by ultraviolet rays, photocatalyst and the like, and are oxidized and decomposed together with other organic pollutants, so that the treatment effect of pollutants difficult to degrade is improved.
Has the advantages that: compared with the prior art, the utility model provides a sewage treatment integration equipment, rational in infrastructure, convenient to use, filtration efficiency is high, utilizes bacterium, virus and the algae of ozone, ultraviolet ray, photocatalyst etc. to the aquatic thoroughly to exterminate, and through the continuous backward flow of water flow, the photocatalyst on the laminar flow board contacts to strengthened the mass transfer process, can non-maintaining use for a long time, and the investment is little, has good economic value and social, can extensively use widely.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
Detailed Description
In order to make the technical solution of the present invention better understood by those skilled in the art, the present invention will be described in detail with reference to the accompanying drawings and the detailed description.
Example 1
As shown in fig. 1, the integrated sewage treatment equipment comprises a box body 1, wherein an upper treatment area a and a lower treatment area b are arranged in the box body 1, a water inlet 7 is arranged at the top of the upper treatment area a, a solid-liquid separation device 10 is arranged in the upper treatment area a, the upper treatment area a is communicated with the lower treatment area b through a flow guide port 11, a filter screen is arranged at the flow guide port 11, a plurality of laminar flow plates 2 are horizontally arranged in the lower treatment area b from top to bottom, an ozone diffusion device 3 is arranged between the lowermost laminar flow plate 2 and the bottom wall of the box body 1, a return port 4 is arranged on the upper side wall of the lower treatment area b, a water outlet 5 is arranged on the lower side wall of the lower treatment area b, the return port 4 is communicated with the water outlet 5 through a water return pipeline 6, an ozone concentration sensor 9 is arranged at the top of the lower treatment area b, and a water quality sensor 8 is arranged in the box body 1, the surface of the laminar flow plate 2 is coated with a photocatalyst, an ultraviolet lamp 14 is arranged between the adjacent laminar flow plates 2, and the ozone concentration sensor 9, the ozone diffusion device 3, the water quality sensor 8 and the water quality sensor 8 are all electrically connected with the controller.
Example 2
As shown in fig. 1, the integrated sewage treatment equipment comprises a tank 1, wherein an upper treatment area a and a lower treatment area b are arranged in the tank 1, a water inlet 7 is arranged at the top of the upper treatment area a, a solid-liquid separation device 10 is arranged in the upper treatment area a, the upper treatment area a is communicated with the lower treatment area b through a flow guide port 11, the flow guide port 11 is provided with a filter screen, a plurality of laminar flow plates 2 are horizontally arranged in the lower treatment area b from top to bottom, the laminar flow plates 2 are arranged in a staggered manner, an ozone diffusion device 3 is arranged between the lowermost laminar flow plate 2 and the bottom wall of the tank 1, a backflow port 4 is arranged on the upper side wall of the lower treatment area b, a water outlet 5 is arranged on the lower side wall of the lower treatment area b, the backflow port 4 and the water outlet 5 are respectively close to the uppermost laminar flow plate 2 and the lowermost laminar flow plate 2, the backflow port 4 and the water outlet 5 are communicated through a water pipeline 6, the top of the lower treatment area b is provided with an ozone concentration sensor 9, a water quality sensor 8 is arranged in the box body 1, the surface of each laminar flow plate 2 is coated with a photocatalyst, and an ultraviolet lamp 14 is arranged between every two adjacent laminar flow plates 2;
the ozone diffusion device 3 comprises a driving motor 31, a base of the driving motor 31 is fixedly connected with the box body 1 through a support 32, an output shaft of the driving motor 31 vertically extends downwards to be connected with an air guide main pipe 33, the air guide main pipe 33 is connected with a plurality of air guide branch pipes 34, the air guide branch pipes 34 are provided with aeration holes 35, the lower end of the air guide main pipe 33 penetrates out of the box body 1 to be connected with a rotary joint 36, and the rotary joint 36 is connected with an ozone generator 37; the solid-liquid separation device 10 comprises a rotating shaft 101 which is transversely arranged, a helical blade 102 is arranged on the rotating shaft 101, one end of the rotating shaft 101 penetrates out of the box body 1 and is connected with a motor 103, the water inlet 7 and the flow guide port 11 are arranged close to the motor 103, the upper treatment area a is provided with a deslagging port 12, and the deslagging port 12 is arranged close to the other end of the rotating shaft 101; the water pipeline 6 comprises a water outlet pipe 63, the water outlet pipe 63 is provided with an electromagnetic valve 62, the electromagnetic valve 62 is connected with a return pipe 64, the water inlet end of the return pipe 64 is connected with the return port 4, and the return pipe 64 is provided with a circulating pump 13; the ozone concentration sensor 9, the circulating pump 13, the driving motor 31, the water quality sensor 8 and the water quality sensor 8 are all electrically connected with the controller.
Finally, it should be noted that the above description is only a preferred embodiment of the present invention, and that those skilled in the art can make various similar representations without departing from the spirit and scope of the present invention.
Claims (9)
1. Sewage treatment integration equipment, its characterized in that: comprises a box body (1), an upper treatment area (a) and a lower treatment area (b) are arranged in the box body (1), a water inlet (7) is formed in the top of the upper treatment area (a), a solid-liquid separation device (10) is arranged in the upper treatment area (a), the upper treatment area (a) is communicated with the lower treatment area (b) through a flow guide port (11), a plurality of laminar flow plates (2) are horizontally arranged in the lower treatment area (b) from top to bottom, an ozone diffusion device (3) is arranged between the lowermost laminar flow plate (2) and the bottom wall of the box body (1), a backflow port (4) is formed in the upper side wall of the lower treatment area (b), a water outlet (5) is formed in the lower side wall of the lower treatment area (b), the backflow port (4) is communicated with the water outlet (5) through a water pipeline (6), and an ozone concentration sensor (9) is arranged at the top of the lower treatment area (b), a water quality sensor (8) is arranged in the box body (1), and the ozone concentration sensor (9), the ozone diffusion device (3) and the water quality sensor (8) are all electrically connected with the controller.
2. The integrated sewage treatment apparatus of claim 1, wherein: ozone diffusion equipment (3) include driving motor (31), the base of driving motor (31) pass through support (32) with box (1) fixed connection, the output shaft of driving motor (31) is vertical to be stretched out downwards and is connected with the air guide and be responsible for (33), the air guide is responsible for and is connected with a plurality of air guide branch pipes (34) on (33), aeration hole (35) have been seted up on air guide branch pipe (34), the air guide is responsible for the lower extreme of (33) and is worn out box (1) is connected with rotary joint (36), rotary joint (36) are connected with ozone generator (37).
3. The integrated sewage treatment apparatus of claim 1, wherein: solid-liquid separation equipment (10) is including horizontal pivot (101) that sets up, be equipped with helical blade (102) on pivot (101), the one end of pivot (101) is worn out box (1) is connected with motor (103), water inlet (7) with water conservancy diversion mouth (11) are close to motor (103) set up, go up treatment area (a) and seted up slag removal mouth (12), slag removal mouth (12) are close to the other end setting of pivot (101).
4. The integrated sewage treatment apparatus of claim 3, wherein: the diversion port (11) is provided with a filter screen.
5. The integrated sewage treatment apparatus of claim 1, wherein: the backflow port (4) and the water outlet (5) are respectively close to the laminar flow plate (2) at the top and the laminar flow plate (2) at the bottom.
6. The integrated sewage treatment apparatus of claim 1, wherein: the laminar flow plates (2) are arranged in a staggered mode.
7. The integrated sewage treatment apparatus of claim 1, wherein: the water pipeline (6) comprises a water outlet pipe (63), an electromagnetic valve (62) is installed on the water outlet pipe (63), the electromagnetic valve (62) is connected with a return pipe (64), and the water inlet end of the return pipe (64) is connected with the return port (4).
8. The integrated wastewater treatment apparatus according to claim 7, wherein: the return pipe (64) is provided with a circulating pump (13).
9. The integrated sewage treatment apparatus of claim 5, wherein: the surface of each laminar flow plate (2) is coated with a photocatalyst, and an ultraviolet lamp (14) is arranged between every two adjacent laminar flow plates (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122604480.0U CN216426975U (en) | 2021-10-28 | 2021-10-28 | Integrated sewage treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122604480.0U CN216426975U (en) | 2021-10-28 | 2021-10-28 | Integrated sewage treatment equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216426975U true CN216426975U (en) | 2022-05-03 |
Family
ID=81332118
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202122604480.0U Expired - Fee Related CN216426975U (en) | 2021-10-28 | 2021-10-28 | Integrated sewage treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN216426975U (en) |
-
2021
- 2021-10-28 CN CN202122604480.0U patent/CN216426975U/en not_active Expired - Fee Related
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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: 20220503 |