CN220012387U - Bentazone waste water treatment system - Google Patents
Bentazone waste water treatment system Download PDFInfo
- Publication number
- CN220012387U CN220012387U CN202321087631.2U CN202321087631U CN220012387U CN 220012387 U CN220012387 U CN 220012387U CN 202321087631 U CN202321087631 U CN 202321087631U CN 220012387 U CN220012387 U CN 220012387U
- Authority
- CN
- China
- Prior art keywords
- tank
- pipe
- bentazone
- adsorption
- filter
- 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
- 239000005476 Bentazone Substances 0.000 title claims abstract description 29
- ZOMSMJKLGFBRBS-UHFFFAOYSA-N bentazone Chemical compound C1=CC=C2NS(=O)(=O)N(C(C)C)C(=O)C2=C1 ZOMSMJKLGFBRBS-UHFFFAOYSA-N 0.000 title claims abstract description 29
- CNBGNNVCVSKAQZ-UHFFFAOYSA-N benzidamine Natural products C12=CC=CC=C2C(OCCCN(C)C)=NN1CC1=CC=CC=C1 CNBGNNVCVSKAQZ-UHFFFAOYSA-N 0.000 title claims abstract description 29
- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 26
- 238000001556 precipitation Methods 0.000 claims abstract description 46
- 239000007788 liquid Substances 0.000 claims abstract description 44
- 238000001179 sorption measurement Methods 0.000 claims abstract description 44
- 230000007246 mechanism Effects 0.000 claims abstract description 25
- 238000003860 storage Methods 0.000 claims abstract description 25
- 238000002156 mixing Methods 0.000 claims abstract description 20
- 230000001105 regulatory effect Effects 0.000 claims abstract description 20
- 238000004519 manufacturing process Methods 0.000 claims abstract description 17
- 239000002699 waste material Substances 0.000 claims abstract description 9
- 238000003756 stirring Methods 0.000 claims description 20
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 14
- 238000004062 sedimentation Methods 0.000 claims description 12
- 239000007921 spray Substances 0.000 claims description 4
- 238000007599 discharging Methods 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 3
- 230000003472 neutralizing effect Effects 0.000 claims description 2
- 239000008394 flocculating agent Substances 0.000 abstract description 18
- 230000000694 effects Effects 0.000 abstract description 12
- 239000000126 substance Substances 0.000 abstract description 12
- 238000011282 treatment Methods 0.000 abstract description 11
- 238000006386 neutralization reaction Methods 0.000 abstract description 5
- 239000002351 wastewater Substances 0.000 description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 239000003814 drug Substances 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- 241000220317 Rosa Species 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- RWZYAGGXGHYGMB-UHFFFAOYSA-N anthranilic acid Chemical compound NC1=CC=CC=C1C(O)=O RWZYAGGXGHYGMB-UHFFFAOYSA-N 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 description 1
- 235000017060 Arachis glabrata Nutrition 0.000 description 1
- 244000105624 Arachis hypogaea Species 0.000 description 1
- 235000010777 Arachis hypogaea Nutrition 0.000 description 1
- 235000018262 Arachis monticola Nutrition 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 244000068988 Glycine max Species 0.000 description 1
- 235000010469 Glycine max Nutrition 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 241000209140 Triticum Species 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000012847 fine chemical Substances 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000002363 herbicidal effect Effects 0.000 description 1
- 239000004009 herbicide Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- 235000020232 peanut Nutrition 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000006277 sulfonation reaction Methods 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model discloses a bentazone production wastewater treatment system, wherein in actual use, quantitative mechanisms are arranged on the right sides of the tops of a settling tank and a PH regulating tank, a mixing mechanism is arranged in the settling tank, the bottom of a settling tube is communicated with the settling tank through the settling tube, one side of the bottom of the settling tank is communicated with a filter tank through a filter tube, the filter tube is positioned above the settling tank, the filter tank is connected with the PH regulating tank through a neutralization tube, one side of the bottom of the PH regulating tank is connected with an adsorption tube, and the other end of the adsorption tube is communicated with the adsorption tank; the top right sides at the precipitation tank and the PH regulating tank are provided with the quantitative mechanism, so that the top plate drives the flocculating agent and the alkaline substance to reach the quantitative pipe from the liquid storage tank, the flocculating agent and the alkaline substance can be accurately added into the precipitation tank and the PH regulating tank, accurate feeding is realized, better treatment effect is achieved, and waste of the flocculating agent and the alkaline substance is reduced.
Description
Technical Field
The utility model relates to the technical field of wastewater treatment, in particular to a bentazone production wastewater treatment system.
Background
Bentazone is an important fine chemical product, is a widely used herbicide, and can be used for crops such as rice, soybean, peanut, wheat and the like. The traditional preparation method of bentazone water aqua comprises the steps of amide synthesis, sulfonation synthesis, closed-loop synthesis, water washing, alkali extraction, water phase acidification, centrifugal (plate frame) discharging and water alkali surfactant addition in a dichloroethane system to prepare the water aqua.
At present, when wastewater generated in the bentazone production process is pretreated, the wastewater cannot be freely controlled when the medicament required by precipitation is added, the efficiency of manual addition is low, the wastewater treatment effect is poor, and the medicament is wasted.
Disclosure of Invention
The utility model aims to provide a bentazone production wastewater treatment system, which solves the problems that when wastewater generated in the bentazone production process is pretreated, the chemical required by precipitation cannot be freely controlled during adding, the efficiency of manual addition is low, the wastewater treatment effect is poor, and the chemical is wasted.
In order to solve the technical problems, the utility model provides a bentazone production wastewater treatment system, which comprises a precipitation tank, a filter tank, a PH regulating tank and an adsorption tank, wherein the right sides of the tops of the precipitation tank and the PH regulating tank are respectively provided with a quantitative mechanism, the tops of the precipitation tank are provided with a waste liquid inlet, a mixing mechanism is arranged in the precipitation tank, the bottom of the precipitation tank is communicated with the precipitation tank through the precipitation tank, one side of the bottom of the precipitation tank is communicated with the filter tank through a filter pipe, the filter pipe is positioned above the precipitation tank, the filter tank is connected with the PH regulating tank through a neutralization pipe, one side of the bottom of the PH regulating tank is connected with the adsorption pipe, and the other end of the adsorption pipe is communicated with the adsorption tank;
the quantitative mechanism comprises a quantitative tube, an electric cylinder and a liquid storage tank, wherein a top plate is connected in the quantitative tube in a sliding manner, the right end of the top plate is fixedly connected with an electric cylinder telescopic shaft, the left end of the quantitative tube is connected with a discharge one-way valve, the bottom end of the quantitative tube is communicated with a liquid suction tube, the bottom end of the liquid suction tube penetrates through the top of the liquid storage tank and extends into the liquid storage tank, and the liquid suction tube is connected with the liquid storage tank in a sealing manner.
In the scheme, the liquid suction pipe is provided with a feeding one-way valve, and the feeding one-way valve is arranged at the upper end of the liquid storage tank.
It is further worth to say that the inboard of precipitation tank top is provided with the annular pipe, the one end of annular pipe with the ration pipe intercommunication sets up, the bottom intercommunication of annular pipe has the shower nozzle.
As a preferred implementation mode, the mixing mechanism comprises a bearing seat embedded in the center position of the top of the precipitation tank, a stirring shaft is fixedly penetrated through an inner ring of the bearing seat, the top of the stirring shaft is connected with a rotating motor, a plurality of stirring rods are clamped at intervals on two sides of the stirring shaft, a plurality of fixing plates are fixedly connected to the tops of the stirring rods, and the fixing plates are fixedly connected with the stirring shaft through screws.
As a preferred implementation mode, the stirring shaft is provided with a slot for being inserted into the stirring rod.
As a preferred embodiment, the device further comprises a grid;
the filter box is internally provided with a filter cavity, a plurality of groups of grids are installed in the filter cavity, and a plurality of groups of grids are provided with intervals.
As a preferred embodiment, a plurality of adsorption layers are arranged on the inner side of the adsorption box, and connecting clamping strips are arranged at two ends of each adsorption layer.
As a preferred embodiment, the adsorption layers are arranged in a rectangular structure, and an activated carbon net is arranged on the inner side of each adsorption layer.
Compared with the prior art, the bentazone production wastewater treatment system provided by the utility model at least comprises the following beneficial effects:
1. the right sides of the tops of the precipitation tank and the PH regulating tank are respectively provided with a quantitative mechanism, so that the top plate drives the flocculating agent and the alkaline substances to reach the quantitative pipe from the liquid storage tank, the flocculating agent and the alkaline substances can be accurately added into the precipitation tank and the PH regulating tank, accurate feeding is realized, a better treatment effect is achieved, and waste of the flocculating agent and the alkaline substances is reduced;
2. the mixing mechanism is arranged in the precipitation tank, so that the flocculant entering the precipitation tank is fully mixed with the wastewater, and the precipitation tank is arranged at the bottom of the precipitation tank, so that the precipitate is collected through the precipitation tank, the wastewater treatment efficiency is improved, and meanwhile, a better treatment effect is achieved;
3. the wastewater is sequentially subjected to precipitation treatment, filtration, neutralization and adsorption treatment, so that a better treatment effect can be achieved.
Drawings
For a clearer description of the technical solutions of the present utility model, the drawings that are required to be used in the embodiments will be briefly described, and it will be obvious to those skilled in the art that other drawings can be obtained from these drawings without making any effort.
FIG. 1 is a schematic diagram of a bentazone production wastewater treatment system provided by the utility model;
FIG. 2 is an enlarged view of FIG. 1 at A;
FIG. 3 is a schematic view of a quantitative mechanism according to the present utility model;
in the figure: 1. a precipitation tank; 10. a waste liquid inlet; 11. a rotating electric machine; 12. a bearing seat; 13. a stirring shaft; 14. a stirring rod; 15. a fixing plate; 16. a screw; 17. a slot; 18. a precipitation tube; 19. a precipitation tank; 100. a filter tube; 2. a filter box; 21. a grid; 200. a neutralization tube; 3. a pH adjusting tank; 300. an adsorption tube; 4. an adsorption box; 41. connecting the clamping strips; 42. an activated carbon net; 5. a dosing mechanism; 51. an electric cylinder; 52. a metering tube; 53. a top plate; 54. a discharge one-way valve; 55. a feed check valve; 56. a pipette; 57. a liquid storage tank; 6. an annular tube; 7. a spray head.
Detailed Description
In order to enable those skilled in the art to better understand the technical solutions of the present utility model, the following description will make clear and complete descriptions of the technical solutions of the embodiments of the present utility model with reference to the accompanying drawings.
The utility model aims to provide a bentazone production wastewater treatment system, which solves the problems that when wastewater generated in the bentazone production process is pretreated, the wastewater cannot be freely controlled when the medicament required by precipitation is added, the efficiency of manual addition is low, the wastewater treatment effect is poor, and the medicament is wasted.
Fig. 1 is a schematic structural view of a bentazone production wastewater treatment system provided by the utility model, fig. 2 is an enlarged view of a position a in fig. 1, and fig. 3 is a schematic structural view of a quantitative mechanism provided by the utility model, see fig. 1 to 3.
The utility model provides a bentazone waste water treatment system, including setting tank 1, rose box 2, PH regulating tank 3 and adsorption tank 4, waste water that bentazone production contracted into and produced loops through setting tank 1, rose box 2, PH regulating tank 3 and adsorption tank 4 handle, in order to can be to setting tank 1 inside accurate adding flocculant, add the material that is used for neutralizing waste water to PH regulating tank 3 in, all be provided with quantitative mechanism 5 on the top right side of setting tank 1 and PH regulating tank 3, in setting tank 1 is added to the flocculant that will quantify through quantitative mechanism 5, the flocculant is the most extensive medicament of application in the sewage treatment at present, flocculation process is indispensable key link in the sewage treatment technology, the person of skill in the art can carry out reasonable selection flocculant according to actual demand. The top of the settling tank 1 is provided with a waste liquid inlet 10, a mixing mechanism is arranged in the settling tank 1, waste water generated by bentazone production is added into the settling tank 1 through the waste liquid inlet 10, and the waste water and the flocculating agent are fully mixed through the mixing mechanism, so that the waste water treatment effect is better. The bottom of the sedimentation tank 1 is communicated with a sedimentation tank 19 through a sedimentation pipe 18, after the wastewater and the flocculating agent are fully mixed, a valve on the sedimentation pipe 18 is opened, so that the wastewater enters the sedimentation tank 19 for standing and sedimentation, and large floccules are subjected to sedimentation collection in the sedimentation tank 19. The bottom one side of the precipitation tank 1 is communicated with the filter tank 2 through the filter pipe 100, the filter pipe 100 is positioned above the precipitation tank 19, water after precipitation in the precipitation tank 1 enters the filter tank 2 through the filter pipe 100, particulate impurities and floccules in the wastewater are filtered through the filter tank 2, the filter tank 2 is connected with the PH adjusting tank 3 through the neutralization pipe 200, alkaline substances are filled in the liquid storage tank 57 on the right side of the top of the PH adjusting tank 3, and since a large amount of anthranilic acid is contained in the bentazone production wastewater, acidic wastewater is common industrial wastewater, alkaline substances are added into the PH adjusting tank 3 through the quantifying mechanism 5, so that the PH value of the wastewater is regulated to be in a reasonable range, the alkaline substances are accurately added through the quantifying mechanism 5, the treatment effect on the wastewater is improved, and waste is prevented. One side of the bottom of the PH adjusting tank 3 is connected with an adsorption pipe 300, the other end of the adsorption pipe 300 is communicated with the adsorption box 4, and after the PH value of wastewater is adjusted to be within a reasonable range, the wastewater enters the adsorption box 4 through the adsorption pipe 300 to be adsorbed.
The quantifying mechanism 5 comprises a quantifying tube 52, an electric cylinder 51 and a liquid storage tank 57, wherein a top plate 53 is slidably connected to the quantifying tube 52, the top plate 53 is used for pushing flocculant in the quantifying tube 52, the right end of the top plate 53 is fixedly connected with a telescopic shaft of the electric cylinder 51, the working principle and structure of the electric cylinder 51 can be seen in the prior art, the left end of the quantifying tube 52 is connected with a discharge one-way valve 54, the bottom end of the quantifying tube 52 is communicated with a liquid suction tube 56, the bottom end of the liquid suction tube 56 penetrates through the top of the liquid storage tank 57 and extends into the liquid storage tank 57, and the liquid suction tube 56 is in sealing connection with the liquid storage tank 57. The electric cylinder 51 is connected with a controller (the controller is not shown in the figure), and in actual operation, a flocculating agent is added into the liquid storage tank 57, the controller controls the electric cylinder 51, and the electric cylinder 51 enables the top plate 53 to drive the flocculating agent to reach the quantitative pipe 52 from the liquid storage tank 57, so that the flocculating agent quantitatively enters the precipitation tank 1. In order to prevent the flocculant from flowing back into the liquid storage tank 57, as a preferred embodiment, a feeding check valve 55 is arranged on the liquid suction pipe 56, the feeding check valve 55 is arranged at the upper end of the liquid storage tank 57, and by arranging a discharging check valve 54 on the quantitative pipe 52, the feeding check valve 55 is arranged on the liquid suction pipe 56, so that the flocculant is prevented from flowing back into the liquid storage tank 57, quantitative addition is further realized, and a better sedimentation effect is achieved.
In order to enable the flocculating agent to be better mixed with the wastewater, preferably, the inner side of the top of the settling tank 1 is provided with an annular pipe 6, the annular pipe 6 is annularly arranged in the inner cavity of the settling tank 1, one end of the annular pipe 6 is communicated with a quantitative pipe 52, the bottom of the annular pipe 6 is communicated with a spray head 7, the flocculating agent in the quantitative pipe 52 enters the annular pipe 6, and then the flocculating agent is sprayed downwards through the spray head 7, so that the contact area between the flocculating agent and the wastewater is increased, and the mixing effect is improved.
In this embodiment, preferably, the mixing mechanism includes the bearing frame 12 of embedding in the central point department in the precipitation tank 1 top, and the inner circle of bearing frame 12 is fixed to run through and is had (mixing) shaft 13, and the top of (mixing) shaft 13 is connected with rotating electrical machines 11, and the equal interval joint in both sides of (mixing) shaft 13 has a plurality of puddlers 14, drives (mixing) shaft 13 and puddler 14 through rotating electrical machines 11 and rotates, intensive mixing flocculant and waste water for waste water obtains purifying treatment. And in order to conveniently dismantle the maintenance to (mixing) shaft 13 and puddler 14, the equal fixedly connected with fixed plate 15 in top of a plurality of puddlers 14, pass through screw 16 fixed connection between fixed plate 15 and the (mixing) shaft 13, preferably, offer on the (mixing) shaft 13 be used for carrying out the slot 17 of pegging graft with puddler 14, the puddler 14 passes through slot 17 and is pegged graft with (mixing) shaft 13, then pass through screw 16, fixed plate 15 and (mixing) shaft 13 fixed connection, make puddler 14 detachable, avoid puddler 14 to produce the fracture after long-term use, thereby need carry out the problem of whole change with it.
In order to improve the filtering effect on the wastewater, the filter box preferably further comprises a plurality of groups of grids 21, a filter cavity is arranged in the filter box 2, the plurality of groups of grids 21 are arranged in the filter cavity, intervals are arranged among the plurality of groups of grids 21, and particles in the wastewater are effectively filtered through the plurality of groups of grids 21.
In this embodiment, preferably, a plurality of adsorption layers are provided on the inner side of the adsorption tank 4, connection clamping strips 41 are provided at two ends of the adsorption layer, and in actual setting, connection grooves for fixing the adsorption layers are provided on the upper and lower inner walls of the adsorption tank 4, and the size of the connection grooves is matched with the size of the connection clamping strips 41, so that the adsorption layers are fixed by clamping the connection clamping strips 41 in the connection grooves. As a preferred embodiment, the adsorption layers are arranged in a rectangular structure, and an activated carbon net 42 is arranged on the inner side of each adsorption layer. The adsorption layer is used for fixing and supporting the activated carbon net 42, and the connection clamping strips 41 at the upper end and the lower end of the adsorption layer are inserted into corresponding connecting grooves to realize the connection fixation of the adsorption layer, and meanwhile, the adsorption layer is conveniently taken out, so that the activated carbon net 42 is conveniently replaced.
According to the bentazone production wastewater treatment system provided by the utility model, in actual use, wastewater generated during bentazone production is added into the precipitation tank 1 through the waste liquid inlet 10, a flocculating agent is added into the liquid storage tank 57, the controller controls the electric cylinder 51, the electric cylinder 51 enables the top plate 53 to drive the flocculating agent to reach the quantitative pipe 52 from the liquid storage tank 57, quantitative entry is carried out in the precipitation tank 1, and then the flocculating agent is sprayed into the cavity of the precipitation tank 1 through the annular pipe 6; simultaneously, a rotating motor 11 is started, the rotating motor 11 drives a stirring shaft 13 and a stirring rod 14 to rotate, after flocculant and wastewater are fully mixed, a valve on a filter pipe 100 is opened, sediment enters a sedimentation tank 19 to be subjected to sedimentation treatment, then the wastewater is introduced into a filter box 2 through the filter pipe 100, and then particles and impurities in the wastewater are effectively filtered through a plurality of groups of grids 21; the filtered wastewater enters the PH adjusting tank 3, alkaline substances are added into the PH adjusting tank 3 through the quantifying mechanism 5, the PH value of the wastewater is adjusted to be within a reasonable range, then the wastewater is adsorbed through the adsorption tank 4, and the activated carbon net 42 can effectively adsorb and filter impurities and harmful bacteria in the water.
Other embodiments of the utility model will be apparent to those skilled in the art from consideration of the specification and practice of the application disclosed herein. This application is intended to cover any variations, uses, or adaptations of the utility model following, in general, the principles of the utility model and including such departures from the present disclosure as come within known or customary practice within the art to which the utility model pertains. It is intended that the specification and examples be considered as exemplary only, with a true scope of the utility model being indicated by the following claims.
It is to be understood that the utility model is not limited to the precise arrangements and instrumentalities shown in the drawings, which have been described above, and that various modifications and changes may be effected without departing from the scope thereof. The embodiments of the present utility model described above do not limit the scope of the present utility model.
Claims (8)
1. A bentazone wastewater treatment system, comprising:
the device comprises a precipitation tank (1), a filter tank (2), a PH regulating tank (3) and an adsorption tank (4), wherein a quantitative mechanism (5) is arranged on the right side of the top of the precipitation tank (1) and the right side of the top of the PH regulating tank (3), a waste liquid inlet (10) is arranged at the top of the precipitation tank (1), a mixing mechanism is arranged in the precipitation tank (1), a precipitation tank (19) is arranged at the bottom of the precipitation tank (1) through a precipitation pipe (18) in a communicating manner, one side of the bottom of the precipitation tank (1) is communicated with the filter tank (2) through a filter pipe (100), the filter pipe (100) is positioned above the precipitation tank (19), the filter tank (2) is connected with the PH regulating tank (3) through a neutralizing pipe (200), an adsorption pipe (300) is connected to one side of the bottom of the PH regulating tank (3), and the other end of the adsorption pipe (300) is communicated with the adsorption tank (4).
The quantitative mechanism (5) comprises a quantitative tube (52), an electric cylinder (51) and a liquid storage tank (57), a top plate (53) is connected in the quantitative tube (52) in a sliding mode, the right end of the top plate (53) is fixedly connected with a telescopic shaft of the electric cylinder (51), the left end of the quantitative tube (52) is connected with a discharging one-way valve (54), a liquid suction tube (56) is arranged at the bottom end of the quantitative tube (52) in a communicating mode, the bottom end of the liquid suction tube (56) penetrates through the top of the liquid storage tank (57) and extends into the liquid storage tank, and the liquid suction tube (56) is connected with the liquid storage tank (57) in a sealing mode.
2. A bentazone waste water treatment system as claimed in claim 1, characterized in that the liquid suction pipe (56) is provided with a feed one-way valve (55), and the feed one-way valve (55) is arranged at the upper end of the liquid storage tank (57).
3. The bentazone wastewater treatment system according to claim 1, characterized in that an annular pipe (6) is arranged on the inner side of the top of the sedimentation tank (1), one end of the annular pipe (6) is communicated with the quantitative pipe (52), and a spray head (7) is communicated with the bottom of the annular pipe (6).
4. The bentazone waste water treatment system according to claim 1, characterized in that the mixing mechanism comprises a bearing seat (12) embedded in the center position of the top of the precipitation tank (1), a stirring shaft (13) is fixedly penetrated through the inner ring of the bearing seat (12), the top of the stirring shaft (13) is connected with a rotating motor (11), a plurality of stirring rods (14) are clamped at intervals on two sides of the stirring shaft (13), a plurality of fixing plates (15) are fixedly connected to the tops of the stirring rods (14), and the fixing plates (15) are fixedly connected with the stirring shaft (13) through screws (16).
5. A bentazone waste water treatment system as claimed in claim 4, wherein the stirring shaft (13) is provided with a slot (17) for plugging with the stirring rod (14).
6. A bentazone production wastewater treatment system as claimed in claim 1, further comprising a grid (21);
the filter box (2) is internally provided with a filter cavity, a plurality of groups of grids (21) are arranged in the filter cavity, and a plurality of groups of grids (21) are provided with intervals.
7. A bentazone waste water treatment system as claimed in claim 1, characterized in that a plurality of adsorption layers are arranged on the inner side of the adsorption box (4), and connecting clamping strips (41) are arranged at two ends of the adsorption layers.
8. A bentazone waste water treatment system as claimed in claim 7, wherein said adsorption layers are rectangular in configuration, and an activated carbon net (42) is provided on the inner side of each of said adsorption layers.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321087631.2U CN220012387U (en) | 2023-05-09 | 2023-05-09 | Bentazone waste water treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321087631.2U CN220012387U (en) | 2023-05-09 | 2023-05-09 | Bentazone waste water treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220012387U true CN220012387U (en) | 2023-11-14 |
Family
ID=88676073
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321087631.2U Active CN220012387U (en) | 2023-05-09 | 2023-05-09 | Bentazone waste water treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220012387U (en) |
-
2023
- 2023-05-09 CN CN202321087631.2U patent/CN220012387U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108619954A (en) | A kind of new multistage stirring sewage-treatment plant | |
| CN108525571A (en) | A kind of dosing agitating device of sewage disposal | |
| CN220012387U (en) | Bentazone waste water treatment system | |
| CN112794426A (en) | Flocculating agent dosing system for water treatment based on two-way multi-parameter online detection | |
| CN219621002U (en) | Domestic sewage integrated treatment equipment | |
| CN210150918U (en) | Weaving workshop humidification system based on weaving waste water | |
| CN210595547U (en) | Iminodiacetic acid waste water processing apparatus | |
| CN111771499A (en) | Wisdom is thing networking liquid manure all-in-one for agricultural | |
| CN116874108A (en) | Tank-type sewage biological deep purification device | |
| CN111068367A (en) | Continuous automatic flocculation and separation process for plant/traditional Chinese medicine extracting solution and water treatment | |
| CN216273480U (en) | Treatment device for aquaculture wastewater | |
| CN215028042U (en) | Integrated recyclable industrial sewage treatment device | |
| CN214360707U (en) | Filter equipment for waste water treatment | |
| CN210764717U (en) | Industrial waste water desulfurization treatment device | |
| CN108203179A (en) | A kind of intelligence fast sewage treatment device | |
| CN207699335U (en) | A kind of intelligence fast sewage treatment device | |
| CN209307168U (en) | A kind of micropolis sewage disposal system | |
| CN209668933U (en) | A kind of sewage dosing circulating treating system | |
| CN112808064A (en) | Novel sludge mixing device | |
| CN215327336U (en) | Sewage treatment equipment | |
| CN109521285A (en) | One kind is based on travelling charge measurement technological system | |
| CN108996704A (en) | Bioflocculation formula purifier device | |
| CN107540188A (en) | A kind of high efficiency spiral sludge dewatering machine | |
| CN219174225U (en) | Movable sewage treatment box body | |
| CN218262027U (en) | Activated clay waste water neutralization pond |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: A wastewater treatment system for the production of Pinus massoniana Granted publication date: 20231114 Pledgee: China Postal Savings Bank Co.,Ltd. Shizuishan Branch Pledgor: Ningxia Lantian Agricultural Development Co.,Ltd. Registration number: Y2024980010645 |