CN220745647U - Chemical oil remover - Google Patents
Chemical oil remover Download PDFInfo
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- CN220745647U CN220745647U CN202322472034.8U CN202322472034U CN220745647U CN 220745647 U CN220745647 U CN 220745647U CN 202322472034 U CN202322472034 U CN 202322472034U CN 220745647 U CN220745647 U CN 220745647U
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- 239000000126 substance Substances 0.000 title claims abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 159
- 238000006243 chemical reaction Methods 0.000 claims abstract description 105
- 239000010802 sludge Substances 0.000 claims abstract description 71
- 238000005189 flocculation Methods 0.000 claims abstract description 59
- 230000016615 flocculation Effects 0.000 claims abstract description 59
- 238000004062 sedimentation Methods 0.000 claims abstract description 44
- 238000009826 distribution Methods 0.000 claims description 30
- 238000011010 flushing procedure Methods 0.000 claims description 23
- 238000003860 storage Methods 0.000 claims description 16
- 238000011282 treatment Methods 0.000 claims description 12
- 238000005238 degreasing Methods 0.000 claims description 9
- 229910000831 Steel Inorganic materials 0.000 claims description 8
- 239000010959 steel Substances 0.000 claims description 8
- 238000011049 filling Methods 0.000 claims description 7
- 238000004891 communication Methods 0.000 claims description 6
- 239000011150 reinforced concrete Substances 0.000 claims description 3
- 239000010865 sewage Substances 0.000 claims description 3
- 239000013527 degreasing agent Substances 0.000 claims description 2
- 239000002245 particle Substances 0.000 abstract description 12
- 239000003814 drug Substances 0.000 abstract description 11
- 230000000694 effects Effects 0.000 abstract description 5
- 230000035484 reaction time Effects 0.000 abstract description 4
- 238000010992 reflux Methods 0.000 abstract description 4
- 230000036632 reaction speed Effects 0.000 abstract description 3
- 238000009825 accumulation Methods 0.000 description 8
- 230000005484 gravity Effects 0.000 description 5
- 229940037003 alum Drugs 0.000 description 4
- 239000000945 filler Substances 0.000 description 4
- 238000007599 discharging Methods 0.000 description 3
- 239000010419 fine particle Substances 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- 239000000701 coagulant Substances 0.000 description 2
- 238000010907 mechanical stirring Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005237 degreasing agent Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 150000002910 rare earth metals Chemical class 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model provides a chemical oil remover, which comprises a body, a water inlet pipe, an oil flocculant dosing pipe, a hydrocyclone reaction chamber, a vortex flocculation reaction chamber, a flow guiding chamber, an inclined plate sedimentation area, an overflow groove and a water collecting tank, wherein the hydrocyclone reaction chamber is arranged in the center of the body; the water inlet pipe is communicated with the hydrocyclone reaction chamber, the vortex flocculation reaction chamber and the diversion chamber are all arranged at the periphery of the hydrocyclone reaction chamber, the top of the inclined plate sedimentation zone is provided with an overflow device, one end of the overflow device is connected with the vortex flocculation reaction chamber, the annular shape between the other end of the overflow device and the inside of the body is an overflow groove, the overflow groove is communicated with a water collecting groove, and the water collecting groove is communicated with a siphon water outlet. By arranging the hydrocyclone reaction chamber and the vortex flocculation reaction chamber, the reaction efficiency and the reaction speed are improved, and the reaction time is shortened. The sludge reflux pipe is added to mix the residual medicament in the sludge with the water in the primary sedimentation tank, and the sludge particles are mutually adsorbed to form large oil sludge particles which are settled at the bottom of the tank, so that the medicament effect is exerted, and the water quality of the discharged water is improved.
Description
Technical Field
The utility model belongs to the technical field of turbid circulating water treatment of steel, and particularly relates to a chemical oil remover.
Background
The conventional treatment mode of the steel turbid circulating water treatment technology is as follows: the treatment of turbid circulating water generally adopts a cyclone sedimentation tank to carry out primary sedimentation, and then a horizontal sedimentation tank, or a chemical oil remover, a rare earth magnetic disk purifying device and a high-efficiency turbid circulating water purifying device are used for carrying out secondary treatment to remove most of suspended matters and oil in water. The three treatments are filtering treatments, further removing suspended solids and colloid of fine particles in water, pressurizing to a cooling tower by a lifting pump after reaching the water standard of circulating water quality, pressurizing the cooled water by a pump for the user to recycle, and repeating.
The existing chemical oil removers have three main problems in operation:
1. after the oil flocculant is added into the water in the mechanical stirring reaction chamber, the oil flocculant and the coagulant added in the prior art are combined together to react, so that large-particle sludge is rapidly coagulated and settled, the sludge accumulation in the mechanical stirring reaction chamber is serious, the phenomenon of sludge upturning occurs, and the normal operation of the stirrer is influenced;
2. due to air resistance, the water outlet of the water collecting tank is unstable, and water accumulation phenomenon occurs frequently;
3. the inverted trapezoid mud storage hopper is easy to produce mud accumulation, and the mud circulation is not smooth, so that the mud discharge pipe is blocked.
Disclosure of Invention
The utility model aims to provide a chemical oil remover, which overcomes the technical problems in the prior art.
Therefore, the technical scheme provided by the utility model is as follows:
a chemical oil remover comprises a body, a water inlet pipe, an oil flocculant dosing pipe, a hydrocyclone reaction chamber, a vortex flocculation reaction chamber, a flow guide chamber, an inclined plate sedimentation area, an overflow groove and a water collecting tank, wherein the hydrocyclone reaction chamber is arranged in the center of the body;
the utility model discloses a sewage treatment device, including water inlet pipe, vortex flocculation reaction chamber, baffle plate sedimentation zone, overflow arrangement and overflow flocculation reaction chamber, the water inlet pipe is connected with the water conservancy diversion reaction chamber, oil flocculant adds the pencil and communicates with the water conservancy diversion reaction chamber, vortex flocculation reaction chamber and water conservancy diversion chamber all locate the water conservancy diversion reaction chamber periphery, the delivery port and the vortex flocculation reaction chamber intercommunication of water conservancy diversion reaction chamber, the baffle plate sedimentation zone is the below and both the intercommunication of vortex flocculation reaction chamber, the swash plate sedimentation zone is the area between body inner wall and vortex flocculation reaction chamber, water conservancy diversion chamber and the water conservancy diversion reaction chamber, the swash plate sedimentation zone top is equipped with overflow arrangement, overflow arrangement one end meets with the vortex flocculation reaction chamber, the overflow arrangement is located between overflow arrangement and the body, the overflow arrangement is annular, overflow arrangement intercommunication water catch bowl, the water catch bowl is located outside the body, the water catch bowl intercommunication has the siphon delivery port has the outlet pipe.
The upper part of the hydrocyclone reaction chamber is cylindrical, the lower part of the hydrocyclone reaction chamber is a round table type mud storage hopper with a large upper part and a small lower part, a plurality of water distribution ports are formed in the upper part of the cylinder, water distribution pipes are arranged between the hydrocyclone reaction chamber and the vortex flocculation reaction chamber, the water distribution pipes are in one-to-one correspondence with the water distribution ports and are communicated with the water distribution ports, water distribution branch pipes are communicated with the water distribution pipes, and the water distribution branch pipes are arranged in the vortex flocculation reaction chamber;
the mud storage hopper is communicated with a mud discharge pipe, the mud discharge pipe is communicated with a mud backflow pipeline and a flushing water pipeline, a mud backflow pipe valve is arranged on the mud backflow pipeline, and a communication point of the flushing water pipeline communicated with the mud discharge pipe is arranged in front of the mud backflow pipe valve.
The upper part of the vortex flocculation reaction chamber is of a square structure, the bottom of the vortex flocculation reaction chamber is of an inverted trapezoid structure, micro-vortex flocculation balls are filled in the vortex flocculation reaction chamber, and a diversion hole is formed in the bottom of the vortex flocculation reaction chamber.
The sedimentation zone comprises a clear water zone, a filling zone and a sludge sedimentation zone which are sequentially arranged from top to bottom, one end of the filling zone is connected with the inner wall of the body, the other end of the filling zone is connected with the diversion zone, a triangular mud baffle is arranged at the center of the bottom of the sludge sedimentation zone, the triangular mud baffle divides the sludge sedimentation zone into two parts, sludge discharge ports are respectively formed in the two parts, and the sludge discharge ports are communicated with a sludge discharge pipe.
The sludge discharge pipe is communicated with a flushing water pipe, a sludge discharge pipe valve is arranged on the sludge discharge pipe, and a communication point of the flushing water pipe and the flushing water pipe is arranged in front of the sludge discharge pipe valve.
The overflow device is a triangular overflow weir or an overflow plate.
The body upper portion is square steel structure, and the lower part is trapezoidal steel structure, body both ends are equipped with the support, and the lower part is equipped with the basis, basis and support are reinforced concrete structure.
The beneficial effects of the utility model are as follows:
according to the chemical oil remover provided by the utility model, the hydraulic cyclone reaction chamber and the vortex flocculation reaction chamber are arranged, so that the reaction of a mechanical stirrer is canceled, the energy is saved, the reaction efficiency and the reaction speed are improved, and the reaction time is shortened. The hydraulic cyclone reaction chamber sludge reflux pipe is added, so that the problem of sludge accumulation in the reaction chamber is solved, the medicament is saved, the medicament remained in the sludge is mixed with the water in the primary sedimentation tank, and large oil sludge particles formed by mutual adsorption are deposited at the bottom of the tank, thereby not only playing the effect of medicament energy, but also improving the water quality of effluent.
The gravity water outlet of the water collecting tank is arranged as a siphon water outlet, and air is effectively blocked from entering the water outlet pipe system by utilizing the siphon principle, so that the problems of water accumulation of the water collecting tank and blockage of the water outlet pipe caused by air resistance generated by the pipe are solved.
According to the chemical degreasing agent, the inverted trapezoid mud storage hopper Shan Geyou is divided into two grids, the triangular mud separating plate is additionally arranged in the middle of the inverted trapezoid mud storage hopper, two mud discharging ports are matched, the flushing water pipe is additionally arranged in front of the mud discharging pipe valve, the Shan Gechu mud volume is reduced, the mud circulation is improved, and the problem of mud discharging pipe blockage is solved. Through setting up the flushing water pipe, conveniently wash mud discharge pipe and mud in the mud discharge pipe, further solve mud discharge pipe jam problem.
Drawings
FIG. 1 is a schematic plan view of an embodiment of the present utility model;
fig. 2 is an elevation view of one embodiment of the present utility model.
In the figure: 1. a body; 2. a water inlet pipe; 3. an oil flocculant adding pipe; 4. a hydrocyclone reaction chamber; 4-1, a water distribution port; 4-2, a mud storage bucket; 4-3, a mud discharge pipe; 4-4, a mud return pipe valve; 4-5, a sludge return pipe; 5. a vortex flocculation reaction chamber; 5-1, micro vortex flocculation balls; 5-2, water distribution pipes; 5-3, a water distribution branch pipe; 6. a diversion chamber; 6-1, a diversion hole; 7. a precipitation zone; 7-1, a supporting frame; 7-2, a filler zone; 7-3, a clear water area; 7-4, a sludge sedimentation zone; 7-5, a sludge discharge outlet; 7-6, a sludge discharge pipe; 7-7, a sludge discharge pipe valve; 8. triangular overflow weir; 9. an overflow trough; 10. a water collection tank; 11. a siphon water outlet; 12. a water outlet pipe; 13. triangular mud-guard; 14. a flushing water pipe; 15. and (5) a manhole.
Detailed Description
Further advantages and effects of the present utility model will become apparent to those skilled in the art from the disclosure of the present specification, by describing the embodiments of the present utility model with specific examples.
The exemplary embodiments of the present utility model will now be described with reference to the accompanying drawings, however, the present utility model may be embodied in many different forms and is not limited to the examples described herein, which are provided to fully and completely disclose the present utility model and fully convey the scope of the utility model to those skilled in the art. The terminology used in the exemplary embodiments illustrated in the accompanying drawings is not intended to be limiting of the utility model. In the drawings, like elements/components are referred to by like reference numerals.
Unless otherwise indicated, terms (including technical and scientific terms) used herein have the same meaning as commonly understood by one of ordinary skill in the art. In addition, it will be understood that terms defined in commonly used dictionaries should be interpreted as having a meaning that is consistent with their meaning in the context of the relevant art and will not be interpreted in an idealized or overly formal sense.
Example 1
The embodiment provides a chemical oil remover, which is shown in figure 1, and comprises a body 1, a water inlet pipe 2, an oil flocculant dosing pipe 3, a hydrocyclone reaction chamber 4, a vortex flocculation reaction chamber 5, a diversion chamber 6, an inclined plate sedimentation area 7, an overflow groove 9 and a water collecting tank 10, wherein the hydrocyclone reaction chamber 4 is arranged in the center of the body 1;
the utility model discloses a sewage treatment device, including water inlet pipe 2, vortex flocculation reaction chamber 5, baffle chamber 6, baffle plate sedimentation zone 7, overflow arrangement and overflow flocculation reaction chamber 5 are connected to oil flocculant adding pipe 3 and water conservancy diversion reaction chamber 4, vortex flocculation reaction chamber 5 and baffle chamber 6 all are located water conservancy diversion reaction chamber 4 periphery, the delivery port and the vortex flocculation reaction chamber 5 intercommunication of water conservancy diversion reaction chamber 4, baffle chamber 6 locates the below of vortex flocculation reaction chamber 5 and both intercommunication, baffle plate sedimentation zone 7 is the region between body 1 inner wall and vortex flocculation reaction chamber 5, baffle chamber 6 and water conservancy diversion reaction chamber 4, baffle plate sedimentation zone 7 top is equipped with overflow arrangement, overflow arrangement one end meets with vortex flocculation reaction chamber 5, overflow launder 9 locates between overflow arrangement and the body 1, overflow launder 9 is annular, overflow launder 9 intercommunication water catch bowl 10, water catch bowl 10 locates outside the body 1, water catch bowl 10 intercommunication has siphon delivery port 11, siphon delivery port 11 intercommunication has outlet pipe 12.
Working principle:
turbid water precipitated in the primary sedimentation tank flows into a hydrocyclone reaction chamber 4 in a tangential direction through a water inlet pipe 2 after being pressurized by a lifting pump, a pipeline mixer is arranged on the water inlet pipe before entering the oil remover, coagulant is added, then oil flocculant is added by an oil flocculant adding pipe 3 for mixing reaction, large particles are formed by rapid agglomeration, and sludge is discharged at regular time after sedimentation. The upper water enters a vortex flocculation reaction chamber 5, fine particles in the water migrate and collide to be coagulated under the action of micro-vortex flocculation balls 5-1 to form alum flocs with large particle size, the alum flocs are suspended in the water, then the water flows into a diversion chamber 6 and is uniformly distributed in an inclined plate sedimentation zone 7, so that flocculent sediments formed in the water are effectively separated, mud is settled after separation, and the mud is discharged through a mud discharge pipe. After reaching a certain amount, the supernatant flows into the overflow groove 9 through the overflow device, is collected into the water collecting groove 10 through the overflow groove 9, and is discharged to the next treatment process through the siphon water outlet 11.
Example 2
On the basis of the embodiment 1, the embodiment provides a chemical degreasing device, as shown in fig. 2, the upper part of the hydrocyclone reaction chamber 4 is cylindrical, the lower part of the hydrocyclone reaction chamber is a round table-shaped mud storage hopper 4-2 with a large upper part and a small lower part, the cylindrical upper part is provided with a plurality of water distribution ports 4-1, water distribution pipes 5-2 are arranged between the hydrocyclone reaction chamber 4 and the vortex flocculation reaction chamber 5, the water distribution pipes 5-2 are in one-to-one correspondence with the water distribution ports 4-1 and are communicated with the water distribution ports 4-1, the water distribution pipes 5-2 are communicated with water distribution branch pipes 5-3, and the water distribution branch pipes 5-3 are arranged in the vortex flocculation reaction chamber 5;
the mud storage hopper 4-2 is communicated with a mud discharge pipe 4-3, the mud discharge pipe 4-3 is communicated with a mud backflow pipeline and a flushing water pipe 14, the mud backflow pipeline is provided with a mud backflow pipe valve 4-4, and a communication point of the flushing water pipe 14 and the mud discharge pipe 4-3 is arranged in front of the mud backflow pipe valve 4-4.
By arranging the flushing water pipe 14, the mud in the mud discharge pipe 4-3 is conveniently cleaned, and the problem of mud discharge pipe blockage is further solved. The sludge reflux pipe 4-5 is added, so that the problem of sludge accumulation in the reaction chamber is solved, the medicament is saved, the medicament remained in the sludge is mixed with the water in the primary sedimentation tank, and large oil sludge particles formed by mutual adsorption are deposited at the bottom of the tank, thereby not only playing the effect of medicament energy, but also improving the water quality of effluent.
Turbid water and an oil flocculant are mixed and reacted, and are rapidly condensed to form large particles, and under the action of centrifugal force and gravity, suspended particles with specific gravity greater than 1 are settled in a truncated cone-shaped mud storage hopper 4-2 and are discharged through a mud discharge pipe 4-3 at regular time. Fine particles which are not suitable for sedimentation enter the vortex flocculation reaction chamber 5 through the water distribution port 4-1, the water distribution pipe 5-2 and the water distribution branch pipe 5-3 to carry out secondary alum blossom and flocculation.
Example 3
On the basis of the embodiment 1, the embodiment provides a chemical degreasing device, as shown in fig. 1 and 2, the upper part of the vortex flocculation reaction chamber 5 is of a square structure, the bottom of the vortex flocculation reaction chamber 5 is of an inverted trapezoid structure, micro-vortex flocculation balls 5-1 are filled in the vortex flocculation reaction chamber 5, and a diversion hole 6-1 is formed in the bottom of the vortex flocculation reaction chamber 5.
Through the action of the micro-vortex flocculation ball 5-1, the tiny particles in the water migrate and collide to agglomerate, so that the reaction efficiency is improved, and the reaction time is shortened. And because the micro-vortex flocculator is a hollow shell, the internal flow velocity is small, a large amount of floccules (alum flowers) with larger particle size are accumulated and suspended in water in the micro-vortex flocculator and flow into the diversion chamber 6 through the diversion holes 6-1.
The diversion chamber 6 is arranged between the vortex reaction chamber and the hydrocyclone reaction chamber 4 and is of a square structure.
Example 4
On the basis of the embodiment 1, the embodiment provides a chemical degreasing device, as shown in fig. 2, the sedimentation zone 7 comprises a clear water zone 7-3, a filler zone 7-2 and a sludge sedimentation zone 7-4 which are sequentially arranged from top to bottom, one end of the filler zone 7-2 is connected with the inner wall of the body 1, the other end of the filler zone is connected with a diversion zone, a triangular mud baffle 13 is arranged at the center of the bottom of the sludge sedimentation zone 7-4, the triangular mud baffle 13 divides the sludge sedimentation zone 7-4 into two parts, sludge discharge ports 7-5 are respectively formed in the two parts, and the sludge discharge ports 7-5 are communicated with a sludge discharge pipe 7-6.
The sedimentation area 7 is provided with an inclined plate or an inclined tube, and the filling area 7-2 is supported by a support frame 7-1 to fill the inclined plate (or the inclined tube). Sludge water formed by condensation after the vortex flocculation reaction is uniformly distributed in the inclined plate sedimentation zone 7 through the diversion chamber 6, and according to the shallow layer theory of inclined plate sedimentation, the water rises to the clear water zone 7-3 along the inclined plate (or inclined pipe), is discharged into the overflow groove 9 through the overflow device to be converged to the water collecting groove 10, and flows into the next treatment process through the siphon water outlet 11 and the water outlet pipe 12. The separated sludge slides downwards to a trapezoid sludge storage hopper 4-2 (a sludge sedimentation zone 7-4) along an inclined plate (or an inclined pipe) under the action of gravity, and is discharged through a sludge discharge port through a sludge discharge pipe. The trapezoid sludge storage hopper 4-2 is provided with a manhole 15, so that the sludge in the storage hopper 4-2 can be conveniently overhauled and cleaned.
Example 5
On the basis of embodiment 4, the embodiment provides a chemical oil remover, the sludge discharge pipe 7-6 is communicated with a flushing water pipe 14, the sludge discharge pipe 7-6 is provided with a sludge discharge pipe valve 7-7, and a communication point between the flushing water pipe 14 and the flushing water pipe 14 is arranged in front of the sludge discharge pipe valve 7-7.
By arranging the flushing water pipe 14, the sludge in the sludge discharge pipe 7-6 is conveniently cleaned, the fluidity of the sludge is improved, the blockage of a sludge pipeline is prevented, the flushing is convenient, and the use is flexible.
Example 6
On the basis of the embodiment 1, the embodiment provides a chemical oil remover, and the overflow device is a triangular overflow weir 8 or an overflow plate.
The upper portion of the body 1 is a square steel structure body, the lower portion is an inverted trapezoid steel structure body, supports are arranged at two ends of the body 1, a foundation is arranged at the lower portion, and the foundation and the supports are of reinforced concrete structures.
In summary, the utility model eliminates the reaction of the mechanical stirrer, saves energy, improves the reaction efficiency and reaction speed and shortens the reaction time by arranging the hydrocyclone reaction chamber 4 and the vortex flocculation reaction chamber 5. The sludge reflux pipe 4-5 is added, so that the problem of sludge accumulation in the reaction chamber is solved, the medicament is saved, the medicament remained in the sludge is mixed with the water in the primary sedimentation tank, and large oil sludge particles formed by mutual adsorption are deposited at the bottom of the tank, thereby not only playing the effect of medicament energy, but also improving the water quality of effluent. The gravity water outlet of the water collecting tank 10 is arranged as a siphon water outlet 11, and the siphon principle is utilized to effectively block air from entering the water outlet pipe 12 system, so that the problems of water accumulation of the water collecting tank 10 and blockage of the water outlet pipe 12 caused by air resistance generated by pipelines are solved. The inverted trapezoid mud storage hopper 4-2 Shan Geyou is divided into two grids, the triangular mud baffle 13 is added in the middle of the inverted trapezoid mud storage hopper, two mud discharge ports are matched, the flushing water pipe 14 is added in front of the mud discharge pipe valve, the Shan Gechu mud volume is reduced, the mud circulation is improved, and the problem of mud discharge pipe blockage is solved. By arranging the flushing water pipe 14, the sludge in the sludge discharge pipe 4-3 and the sludge discharge pipe 7-6 can be conveniently cleaned, and the problem of blockage of the sludge discharge pipe is further solved.
The foregoing examples are merely illustrative of the present utility model and are not intended to limit the scope of the present utility model, and all designs that are the same or similar to the present utility model are within the scope of the present utility model.
Claims (7)
1. A chemical degreaser, characterized in that: the device comprises a body, a water inlet pipe, an oil flocculant dosing pipe, a hydrocyclone reaction chamber, a vortex flocculation reaction chamber, a flow guide chamber, an inclined plate sedimentation area, an overflow groove and a water collecting tank, wherein the hydrocyclone reaction chamber is arranged in the center of the body;
the utility model discloses a sewage treatment device, including water inlet pipe, vortex flocculation reaction chamber, baffle plate sedimentation zone, overflow arrangement and overflow flocculation reaction chamber, the water inlet pipe is connected with the water conservancy diversion reaction chamber, oil flocculant adds the pencil and communicates with the water conservancy diversion reaction chamber, vortex flocculation reaction chamber and water conservancy diversion chamber all locate the water conservancy diversion reaction chamber periphery, the delivery port and the vortex flocculation reaction chamber intercommunication of water conservancy diversion reaction chamber, the baffle plate sedimentation zone is the below and both the intercommunication of vortex flocculation reaction chamber, the swash plate sedimentation zone is the area between body inner wall and vortex flocculation reaction chamber, water conservancy diversion chamber and the water conservancy diversion reaction chamber, the swash plate sedimentation zone top is equipped with overflow arrangement, overflow arrangement one end meets with the vortex flocculation reaction chamber, the overflow arrangement is located between overflow arrangement and the body, the overflow arrangement is annular, overflow arrangement intercommunication water catch bowl, the water catch bowl is located outside the body, the water catch bowl intercommunication has the siphon delivery port has the outlet pipe.
2. A chemical degreasing apparatus according to claim 1, wherein: the upper part of the hydrocyclone reaction chamber is cylindrical, the lower part of the hydrocyclone reaction chamber is a round table type mud storage hopper with a large upper part and a small lower part, a plurality of water distribution ports are formed in the upper part of the cylinder, water distribution pipes are arranged between the hydrocyclone reaction chamber and the vortex flocculation reaction chamber, the water distribution pipes are in one-to-one correspondence with the water distribution ports and are communicated with the water distribution ports, water distribution branch pipes are communicated with the water distribution pipes, and the water distribution branch pipes are arranged in the vortex flocculation reaction chamber;
the mud storage hopper is communicated with a mud discharge pipe, the mud discharge pipe is communicated with a mud backflow pipeline and a flushing water pipeline, a mud backflow pipe valve is arranged on the mud backflow pipeline, and a communication point of the flushing water pipeline communicated with the mud discharge pipe is arranged in front of the mud backflow pipe valve.
3. A chemical degreasing apparatus according to claim 1, wherein: the upper part of the vortex flocculation reaction chamber is of a square structure, the bottom of the vortex flocculation reaction chamber is of an inverted trapezoid structure, micro-vortex flocculation balls are filled in the vortex flocculation reaction chamber, and a diversion hole is formed in the bottom of the vortex flocculation reaction chamber.
4. A chemical degreasing apparatus according to claim 1, wherein: the sedimentation zone comprises a clear water zone, a filling zone and a sludge sedimentation zone which are sequentially arranged from top to bottom, one end of the filling zone is connected with the inner wall of the body, the other end of the filling zone is connected with the diversion zone, a triangular mud baffle is arranged at the center of the bottom of the sludge sedimentation zone, the triangular mud baffle divides the sludge sedimentation zone into two parts, sludge discharge ports are respectively formed in the two parts, and the sludge discharge ports are communicated with a sludge discharge pipe.
5. A chemical degreasing apparatus according to claim 4, wherein: the sludge discharge pipe is communicated with a flushing water pipe, a sludge discharge pipe valve is arranged on the sludge discharge pipe, and a communication point of the flushing water pipe and the flushing water pipe is arranged in front of the sludge discharge pipe valve.
6. A chemical degreasing apparatus according to any of claims 1-5, wherein: the overflow device is a triangular overflow weir or an overflow plate.
7. A chemical degreasing apparatus according to any of claims 1-5, wherein: the body upper portion is square steel structure, and the lower part is trapezoidal steel structure, body both ends are equipped with the support, and the lower part is equipped with the basis, basis and support are reinforced concrete structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322472034.8U CN220745647U (en) | 2023-09-12 | 2023-09-12 | Chemical oil remover |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322472034.8U CN220745647U (en) | 2023-09-12 | 2023-09-12 | Chemical oil remover |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220745647U true CN220745647U (en) | 2024-04-09 |
Family
ID=90555455
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322472034.8U Active CN220745647U (en) | 2023-09-12 | 2023-09-12 | Chemical oil remover |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220745647U (en) |
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2023
- 2023-09-12 CN CN202322472034.8U patent/CN220745647U/en active Active
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