CN212504177U - Collect whirlwind separation and honeycomb filter sediment in water treatment facilities of an organic whole - Google Patents
Collect whirlwind separation and honeycomb filter sediment in water treatment facilities of an organic whole Download PDFInfo
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- CN212504177U CN212504177U CN202021472461.6U CN202021472461U CN212504177U CN 212504177 U CN212504177 U CN 212504177U CN 202021472461 U CN202021472461 U CN 202021472461U CN 212504177 U CN212504177 U CN 212504177U
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Abstract
The utility model provides a water treatment device integrating cyclone separation and honeycomb filtration and sedimentation, which comprises a cylinder body, a water inlet pipe and a water outlet pipe, wherein the cylinder body comprises an upper cylinder body and a lower cylinder body which are communicated up and down, the upper cylinder body is cylindrical, the interior of the upper cylinder body is divided into an outer cavity and an inner cavity which are arranged in a nested manner by concentric circles, and the inner cavity is fixedly connected with the outer cavity by a plurality of welding connecting pieces; a honeycomb filter element is arranged in the inner cavity, and the lower barrel body is a conical sedimentation cavity; the upper end of the water inlet pipe is connected to the upper left section of the cylinder and is tangentially communicated with the mixing and stirring cavity, and the lower end of the water inlet pipe is communicated with an external sewage source through a water pump; the static mixer is arranged in the water inlet pipe, two liquid medicine storage boxes are respectively communicated with the water inlet pipe through pipelines, and connecting ports of the two liquid medicine storage boxes and the water inlet pipe are respectively positioned at two sides of the static mixer; the upper end of the drain pipe is vertically connected with the upper right section of the cylinder body and is communicated with the precipitation filter cavity. The utility model discloses simple structure collects cyclone and honeycomb filter sediment in an organic whole, and it is good to deposit the filter effect.
Description
Technical Field
The utility model belongs to the technical field of water treatment, concretely relates to collect cyclone and honeycomb filter sediment in water treatment facilities of an organic whole.
Background
The water treatment mode comprises physical treatment and chemical treatment. The mode of human being's water treatment has been quite a lot of years history, and the physical method includes utilizing the different filter media of various aperture sizes, utilizes absorption or separation mode, gets rid of the impurity in aquatic outside, and the more important person in the absorption mode is for adsorbing with active carbon, and separation method is to pass through the filter media with water, lets the impurity of bigger volume can't pass through, and then obtains comparatively clean water. In addition, the physical methods also include precipitation methods, which are obtained by floating impurities with a smaller specific gravity on the water surface or precipitating impurities with a larger specific gravity below the water surface. The chemical method is to convert the impurities in water into substances which are less harmful to human bodies by various chemicals or concentrate the impurities, and the longest historical chemical treatment method can be that alum is added into water, and after the impurities in the water are collected, the volume is increased, and then the impurities can be removed by a filtration method.
Traditional precipitation device relies on gravity to subside, and settling velocity is slow, and is in addition through filling liquid medicine for sewage and liquid medicine reaction, the formation of accelerateing the sediment, through agitating unit, stir, mixing speed is slow, mixes inhomogeneously, and settling efficiency is low.
Disclosure of Invention
To the weak point among the prior art, the utility model provides a collect whirlwind separation and honeycomb filter sediment in water treatment facilities of an organic whole.
In order to achieve the above purpose, the utility model discloses technical scheme as follows:
a water treatment device integrating cyclone separation and honeycomb filtration and precipitation comprises a cylinder, a water inlet pipe and a water discharge pipe, wherein the cylinder comprises an upper cylinder and a lower cylinder which are communicated up and down, the upper cylinder is cylindrical, the interior of the upper cylinder is divided into an outer cavity and an inner cavity which are arranged in a nested manner in concentric circles, and the inner cavity is fixedly connected with the outer cavity through a plurality of welding connecting pieces; the outer cavity is a mixing and stirring cavity, the inner cavity is a precipitation filter cavity, a honeycomb filter element made of FPR materials is additionally arranged in the precipitation filter cavity, the lower barrel is a conical precipitation cavity, and the bottom of the precipitation cavity is connected with a sludge discharge pipe;
the upper end of the water inlet pipe is connected to the upper left section of the barrel and is tangentially communicated with the mixing and stirring cavity, and the lower end of the water inlet pipe is communicated with an external sewage source through a water pump; a static mixer is arranged in the water inlet pipe; the two liquid medicine storage tanks are respectively communicated with the water inlet pipe through pipelines, and the connecting ports of the two liquid medicine storage tanks and the water inlet pipe are respectively positioned at two sides of the static mixer;
when sewage enters the mixing and stirring cavity from the tangentially communicated water inlet pipe, the liquid medicine is filled through the water inlet pipe and is mixed with the sewage, a vortex is formed in the mixing and stirring cavity, the sewage and the liquid medicine are quickly and uniformly mixed and reacted, and impurities are quickly condensed; the speed of the vortex is gradually reduced after the vortex is downwards rotated into the precipitation cavity, and impurities are precipitated under the action of gravity; the water after the primary treatment can be further filtered again through the precipitation filter cavity;
the upper end of the drain pipe is vertically connected with the upper right section of the cylinder body and is communicated with the precipitation filter cavity.
Further, the lower end of the drain pipe is communicated with a drain storage tank.
Further, still include the base, the barrel outside evenly is equipped with four support arms, and four support arms correspond the installation with the support column of base respectively.
Furthermore, a control box and a test bench are arranged on the outer side of the barrel, the test bench is located above the control box, and an escalator and a safety protection cage which fall on the ground are arranged on one side of the test bench.
Furthermore, the sludge discharge pipe adopts a polyvinyl chloride pipe, the polyvinyl chloride pipe is provided with a valve controlled by a control box, and the sludge discharge time is automatically controlled according to a set program.
Further, the control box comprises two water level floating switches which respectively control the two liquid medicine storage tanks.
Has the advantages that: the utility model has the advantages that the mixing and stirring cavity and the sedimentation and filtration cavity which are nested inside and outside the upper layer, the sedimentation cavity which is conical at the lower layer and the tangentially communicated water inlet pipe are used for generating downward vortex when sewage and liquid medicine enter the mixing and stirring cavity, and the sewage and the liquid medicine are quickly and uniformly mixed and reacted under the action of centrifugal force, so that the reaction is sufficient, and impurities are quickly condensed; the speed of the sewage eddy flow entering the settling chamber is gradually reduced, and impurities are settled under the action of gravity; the speed of sewage vortex reduces gradually, and the vortex contacts the sloping bottom plate of precipitation chamber and moves upwards behind, and the sewage after will subsiding lets in the further filtration in filter material chamber, has better sediment filter effect.
Drawings
Fig. 1 is a schematic structural view of the present invention;
FIG. 2 is a partial left view of FIG. 1;
FIG. 3 is a cross-sectional view A-A;
FIG. 4 is a cross-sectional view B-B;
FIG. 5 is a schematic view of the structure of the inspection station, the escalator and the safety cage
Fig. 6 is a partial top schematic view of a dual barrel configuration according to an exemplary embodiment.
FIG. 7 is a schematic top view of a portion of a three barrel configuration according to an exemplary embodiment.
In the figure, 1-a cylinder, 2-a water inlet pipe, 3-a water discharge pipe, 4-a liquid medicine storage box, 5-a water discharge storage box, 6-a base, 7-a control box, 8-a test bench, 9-a staircase and 10-a water pump;
11-an upper cylinder body, 12-a lower cylinder body, 13-a mixing and stirring cavity, 14-a precipitation filter cavity, 15-a honeycomb filter element, 16-a precipitation cavity, 17-a sludge discharge pipe, 18-a support arm, 19-a liquid return port and 20-a welding connecting piece;
21-static mixer, 22-liquid medicine pump and 23-safety protection cage.
Detailed Description
The present invention is described below with reference to specific examples. It will be understood by those skilled in the art that these examples are for illustrative purposes only and are not intended to limit the scope of the present invention in any way.
A water treatment device integrating cyclone separation and honeycomb filtration and sedimentation, as shown in figures 1 to 5, comprises a cylinder body 1, a water inlet pipe 2, a drain pipe 3, a liquid medicine storage tank 4, a drain storage tank 5 and a base 6,
the barrel 1 comprises an upper barrel 11 and a lower barrel 12 which are communicated up and down, the upper barrel 11 is cylindrical, the interior of the upper barrel is divided into an outer cavity and an inner cavity which are nested in concentric circles, and the inner cavity is fixedly connected with the outer cavity through an upper group of welding connecting pieces 20 and a lower group of welding connecting pieces 20 which are eight in total; the outer cavity is a mixing and stirring cavity 13, the inner cavity is a precipitation filter cavity 14, a honeycomb filter element 15 made of FPR materials is additionally arranged in the precipitation filter cavity 14, the lower barrel 12 is a conical precipitation cavity 16, and the bottom of the precipitation cavity 16 is connected with a sludge discharge pipe 17;
four supporting arms 18 are uniformly arranged on the outer side of the barrel 1, and the four supporting arms 18 are respectively and correspondingly installed with supporting columns of the base 6 through bolts;
the upper end of the water inlet pipe 2 is connected to the upper left section of the barrel 1 and is tangentially communicated with the mixing and stirring cavity 13, and the lower end of the water inlet pipe 2 is communicated with an external sewage source through a water pump 10 and a water pump suction hose; a static mixer 21 is arranged in the water inlet pipe 2;
the liquid medicine storage tank 4 is divided into a liquid medicine storage tank 4a and a liquid medicine storage tank 4b, the liquid medicine storage tank 4a and the liquid medicine storage tank 4b are respectively communicated with the water inlet pipe 2 through pipelines, a connection port C1 of the liquid medicine storage tank 4a and the water inlet pipe 2 is close to the input end of the static mixer 21, and a connection port C2 of the liquid medicine storage tank 4b and the water inlet pipe 2 is close to the output end of the static mixer 21;
when sewage enters the mixing and stirring cavity 13 from the tangentially communicated water inlet pipe 2, the liquid medicine is injected through the water inlet pipe 2 and is mixed with the sewage, and a vortex is formed under the bidirectional action of the arc inner wall of the mixing and stirring cavity 13 and the arc outer wall of the precipitation and filtration cavity 14, so that the sewage and the liquid medicine are quickly and uniformly mixed and reacted, and impurities are quickly condensed; the speed of the vortex is gradually reduced after the vortex rotates downwards and enters the sedimentation cavity 16, and impurities are precipitated under the action of gravity; the water after the primary treatment can be further filtered again through the sedimentation filter chamber 14;
the upper end of the drain pipe 3 is vertically connected with the upper right section of the cylinder 1 and is communicated with the precipitation filter cavity 14, and the lower end of the drain pipe 3 is communicated with the drain storage tank 5;
a control box 7 and a test platform 8 are arranged on the outer side of the barrel 1, the test platform 8 is positioned above the control box 7, and an escalator 9 and a safety protection cage 23 which fall on the ground are arranged on one side of the test platform 8;
the control tank 7 includes a water level float switch D1 controlling the liquid medicine storage tank 4a and a water level float switch D2 controlling the liquid medicine storage tank 4 b.
In one embodiment, the sludge discharge pipe 17 is a polyvinyl chloride pipe.
The utility model discloses a theory of operation:
(1) starting the water pump 10, enabling sewage to flow into the water inlet pipe 2, simultaneously starting the liquid medicine pumps 22 of the liquid medicine storage tank 4a and the liquid medicine storage tank 4b, respectively and sequentially filling liquid medicine into the water inlet pipe 2, and mixing the liquid medicine and the sewage through the static mixer 21;
(2) when sewage and liquid medicine enter the mixing and stirring cavity 13 from the tangentially communicated water inlet pipe 2, a vortex is formed under the bidirectional action of the arc inner wall of the mixing and stirring cavity 13 and the arc outer wall of the precipitation and filtration cavity 14, so that the sewage and the liquid medicine are quickly and uniformly mixed and reacted, and impurities are quickly condensed;
(3) the speed of the vortex is gradually reduced after the vortex rotates downwards and enters the sedimentation cavity 16, and impurities are precipitated under the action of gravity; sludge can be removed by opening a valve of the sludge discharge pipe 17, and the valve is controlled by the control box 7 to automatically control the sludge discharge time according to a set program;
(4) the speed of the sewage vortex is gradually reduced, after the vortex contacts the inclined bottom plate of the sedimentation chamber 16, the vortex moves upwards to the sedimentation filter chamber 14 through the liquid return port 19 at the bottom of the sedimentation filter chamber 14, the honeycomb filter element 15 in the sedimentation filter chamber 14 filters a small amount of impurities which are splashed, and the sewage passing through the sedimentation filter chamber 14 is discharged from the drain pipe 3 and flows into the drainage storage tank 5.
In the specific embodiment, the cylinder is not limited to a single cylinder structure, and may be a double cylinder structure or a multi-cylinder structure having two or more cylinders. As shown in fig. 6, the double-cylinder structure has two inlet branch pipes 2a and 2b of one inlet pipe 2 tangentially communicated with the cylinder 1a and the cylinder 1b, respectively, and the cylinder 1a and the cylinder 1b are provided with respective drain pipes 3a and 3b, respectively. In the three-tube structure shown in fig. 7, three inlet branch pipes 2a, 2b, 2c of one inlet pipe 2 are tangentially communicated with the tube body 1a, the tube body 1b, and the tube body 1c, respectively, and the tube body 1a, the tube body 1b, and the tube body 1c are provided with respective drain pipes 3a, 3b, 3c, respectively.
Claims (8)
1. The utility model provides a collect cyclone and honeycomb filter sediment in water treatment facilities of an organic whole which characterized in that: comprises a cylinder body, a water inlet pipe and a water outlet pipe,
the cylinder comprises an upper cylinder and a lower cylinder which are communicated up and down, the upper cylinder is cylindrical, the interior of the upper cylinder is divided into an outer cavity and an inner cavity which are arranged in a nested manner by concentric circles, and the inner cavity is fixedly connected with the outer cavity through a plurality of welding connecting pieces; the outer cavity is a mixing and stirring cavity, the inner cavity is a precipitation filter cavity, a honeycomb filter element is additionally arranged in the precipitation filter cavity, the lower barrel is a conical precipitation cavity, and the bottom of the precipitation cavity is connected with a sludge discharge pipe;
the upper end of the water inlet pipe is connected to the upper left section of the barrel and is tangentially communicated with the mixing and stirring cavity, and the lower end of the water inlet pipe is communicated with an external sewage source through a water pump; the two liquid medicine storage tanks are respectively communicated with the water inlet pipe through pipelines, and the connecting ports of the two liquid medicine storage tanks and the water inlet pipe are respectively positioned at two sides of the static mixer;
when sewage enters the mixing and stirring cavity from the tangentially communicated water inlet pipe, the liquid medicine is filled through the water inlet pipe and is mixed with the sewage, a vortex is formed in the mixing and stirring cavity, the sewage and the liquid medicine are quickly and uniformly mixed and reacted, and impurities are quickly condensed; the speed of the vortex is gradually reduced after the vortex is downwards rotated into the precipitation cavity, and impurities are precipitated under the action of gravity; the water after the primary treatment can be further filtered again through the precipitation filter cavity;
the upper end of the drain pipe is vertically connected with the upper right section of the cylinder body and is communicated with the precipitation filter cavity.
2. The water treatment device integrating cyclone separation and honeycomb filtration precipitation as claimed in claim 1, wherein: the lower end of the drain pipe is communicated with a drain storage tank.
3. The water treatment device integrating cyclone separation and honeycomb filtration precipitation as claimed in claim 1, wherein: the cylinder body is characterized by further comprising a base, wherein four supporting arms are uniformly arranged on the outer side of the cylinder body and are respectively installed corresponding to supporting columns of the base.
4. The water treatment device integrating cyclone separation and honeycomb filtration precipitation as claimed in claim 1, wherein: the outer side of the barrel is provided with a control box and a test bench, the test bench is positioned above the control box, and one side of the test bench is provided with an escalator and a safety protection cage which fall on the ground.
5. The water treatment device integrating cyclone separation and honeycomb filtration precipitation as claimed in claim 1, wherein: the sludge discharge pipe adopts a polyvinyl chloride pipe, the polyvinyl chloride pipe is provided with a valve controlled by a control box, and the sludge discharge time is automatically controlled according to a set program.
6. The water treatment device integrating cyclone separation and honeycomb filtration precipitation as claimed in claim 1, wherein: the honeycomb filter core is made of FPR materials.
7. The water treatment device integrating cyclone separation and honeycomb filtration precipitation as claimed in claim 4, wherein: the control box comprises two water level floating switches which respectively control the two liquid medicine storage boxes.
8. The water treatment device integrating cyclone separation and honeycomb filtration precipitation as claimed in claim 1, wherein: the cylinder body can also adopt a double-cylinder structure or a three-cylinder structure, the double-cylinder structure is respectively tangentially communicated with the two cylinder bodies through two water inlet branch pipes of one water inlet pipe, and the two cylinder bodies are respectively provided with respective water discharge pipes; the three-cylinder structure is tangentially communicated with the three cylinders through three water inlet branch pipes of one water inlet pipe, and the three cylinders are provided with respective water discharge pipes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021472461.6U CN212504177U (en) | 2020-07-23 | 2020-07-23 | Collect whirlwind separation and honeycomb filter sediment in water treatment facilities of an organic whole |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021472461.6U CN212504177U (en) | 2020-07-23 | 2020-07-23 | Collect whirlwind separation and honeycomb filter sediment in water treatment facilities of an organic whole |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN212504177U true CN212504177U (en) | 2021-02-09 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202021472461.6U Active CN212504177U (en) | 2020-07-23 | 2020-07-23 | Collect whirlwind separation and honeycomb filter sediment in water treatment facilities of an organic whole |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN212504177U (en) |
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- 2020-07-23 CN CN202021472461.6U patent/CN212504177U/en active Active
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