CN217051822U - Concentration equipment for concentration and dealcoholization in wastewater by membrane method - Google Patents
Concentration equipment for concentration and dealcoholization in wastewater by membrane method Download PDFInfo
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- CN217051822U CN217051822U CN202220804794.7U CN202220804794U CN217051822U CN 217051822 U CN217051822 U CN 217051822U CN 202220804794 U CN202220804794 U CN 202220804794U CN 217051822 U CN217051822 U CN 217051822U
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Abstract
The utility model discloses a concentrating equipment for wastewater concentration and dealcoholization by membrane method, which firstly filters the substances in the wastewater through a first filter ring group, a second filter ring group and a third filter ring group, improves the concentrating and dealcoholization effect, and simultaneously can regularly open a second regulating valve to replace the filter substances in the first filter ring group, the second filter ring group and the third filter ring group, thereby avoiding the problem that the filter substances influence the filter effect after long-term use, secondly, the first temporary storage cavity, the second temporary storage cavity and the third temporary storage cavity can be beneficial to the temporary storage of the wastewater respectively and the storage of the dealcoholization impurities, and is beneficial to the cleaning and replacement of the dealcoholization impurities in the first temporary storage cavity, the second temporary storage cavity and the third temporary storage cavity, finally, a flow velocity sensor can also detect the liquid flow velocity in the first temporary storage cavity, the second temporary storage cavity and the third temporary storage cavity, thereby being beneficial to the analysis of the blockage condition of the filter substances by judging the flow velocity by workers, so that the filter material is replaced periodically.
Description
Technical Field
The utility model relates to an ultrafiltration technical field especially relates to a be arranged in waste water concentration dealcoholize embrane method concentrator.
Background
Along with the development of social economy, the living standard of people is gradually improved, the environmental protection consciousness is gradually strengthened, in recent years, China pays attention to the environmental protection problem, the strength is increased to control the environmental protection problem brought by the economic development, particularly the problem of water resource treatment, water is the root of the survival of people, the discharge of waste water is the main problem disturbing the water resource, and the filtration of waste water is the important link of water treatment.
According to the above, the conventional device for filtering and treating wastewater at present has the advantages of simple structure, and many defects and shortcomings, specifically as follows;
1. the filtering effect is poor, multiple effective ultrafiltration can not be realized, and the wastewater treatment effect is influenced.
2. After the membrane method is used for filtering wastewater for a long time, the attached impurity accumulation is not easy to clean and the filter medium is not easy to replace, so that the service life and the cost are influenced.
3. The flow velocity detection to sewage can not be realized, and the blockage condition can not be judged according to the flow velocity by the working personnel.
Therefore, in view of the above drawbacks, it is necessary to design a concentrating device for wastewater concentration and dealcoholization membrane process.
SUMMERY OF THE UTILITY MODEL
The utility model discloses the technical problem that will solve lies in: provides a concentrating device for wastewater concentration and dealcoholization membrane method, which solves the problems of the background art.
In order to solve the technical problem, the technical scheme of the utility model is that: a concentrating device for concentrating and dealcoholizing wastewater by a membrane method comprises a fixed seat, an outer cover, a suction pump, a first filtering ring set, a second filtering ring set, a third filtering ring set, a first temporary storage cavity, a second temporary storage cavity, a third temporary storage cavity, a flow rate sensor, a first regulating valve and a second regulating valve, wherein the outer cover is fixedly arranged at the top of the fixed seat, the outer cover and the fixed seat are integrally formed, the suction pump is fixedly arranged in the middle of the rear end of the outer cover and is welded with the outer cover, the first filtering ring set is fixedly arranged at the inner middle end of the outer cover and is welded with the outer cover, the second filtering ring set is arranged at the outer side of the first filtering ring set and is welded with the outer cover, the third filtering ring set is arranged at the outer side of the second filtering ring set and is welded with the outer cover, the first temporary storage cavity is positioned between the first filter ring group and the second filter ring group, the first temporary storage cavity is an annular cavity, the second temporary storage cavity is positioned between the second filter ring group and the third filter ring group, the second temporary storage cavity is an annular cavity, the third temporary storage cavity is positioned between the third filter ring group and the outer wall of the outer housing cover, the third temporary storage cavity is an annular cavity, the number of the flow rate sensors is a plurality of pieces, the flow rate sensors are fixedly arranged at the inner front end of the outer housing cover from left to right respectively, the flow rate sensors are connected with the outer housing cover by hot melting, the flow rate sensors are respectively positioned in the first temporary storage cavity, the second temporary storage cavity and the third temporary storage cavity, the number of the first regulating valves is a plurality of pieces, the first regulating valves are fixedly arranged at the inner front end of the outer housing cover from top to bottom, the first regulating valves are connected with the outer housing cover by hot melting, just first governing valve be located first chamber, the second chamber and the third chamber of keeping in respectively, second governing valve quantity be a plurality of, the second governing valve from last to setting firmly in the inside front end of outer housing cover down, second governing valve and outer housing cover adopt the hot melt to be connected, just the second governing valve be located first filter ring group, second filter ring group and third filter ring group respectively and organize insidely.
Furthermore, the top end in the outer shell cover is fixedly provided with an inlet pipe, and the inlet pipe is connected with the outer shell cover in a welding mode.
Furthermore, the first filtering ring group, the second filtering ring group and the third filtering ring group are all internally provided with filtering material storage cavities, and the filtering material storage cavities are annular cavities.
Furthermore, the flow rate display is still set firmly at the flow rate sensor front end, flow rate display and flow rate sensor adopt electric connection, just flow rate display and outer clamshell adopt hot melt to be connected.
Compared with the prior art, the concentrating equipment for the wastewater concentration dealcoholization membrane method has the following advantages;
1. at first, through first filtration ring group, second filtration ring group and third filtration ring group, can filter the material in the waste water, improve concentrated dealcoholize effect, also can regularly through opening the second governing valve simultaneously, change the filter material of first filtration ring group, second filtration ring group and third filtration ring group inside, avoid filter material to influence the problem of filter effect after long-term the use.
2. Its first chamber of keeping in, second chamber and the third chamber of keeping in of inferior can do benefit to waste water and temporarily deposit respectively, also is convenient for deposit dealcoholize impurity, does benefit to the follow-up dealcoholize impurity of keeping in chamber inside first chamber, the second chamber of keeping in and the third chamber of keeping in and clears up the change.
3. Finally, the flow velocity sensor can also detect the flow velocity of liquid in the first temporary storage cavity, the second temporary storage cavity and the third temporary storage cavity, so that the blockage condition of filtering materials can be analyzed by workers by judging the flow velocity, and the filtering materials can be replaced regularly.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the embodiments or the technical solutions in the prior art will be briefly described below, and it is obvious that the drawings in the following description are some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without creative efforts.
FIG. 1 is a front view of a concentrating apparatus for concentrating and dealcoholizing wastewater by a membrane method;
FIG. 2 is a top view of a concentrating apparatus for concentrating and dealcoholizing wastewater by a membrane method;
FIG. 3 is a sectional view taken along the direction A of a concentrating apparatus for concentrating and dealcoholizing wastewater by a membrane method;
FIG. 4 is a perspective view of a concentrating apparatus for concentrating and dealcoholizing wastewater by a membrane method, shown in FIG. 1;
FIG. 5 is a perspective view of a concentrating apparatus for wastewater concentration and dealcoholization by a membrane process, shown in FIG. 2.
Fixing base 1, shell cover 2, suction pump 3, first filter ring group 4, second filter ring group 5, third filter ring group 6, first chamber 7 of keeping in, second chamber 8, third chamber 9 of keeping in, flow sensor 10, first governing valve 11, second governing valve 12, admission pipe 201, the filter material deposits chamber 401, flow rate display 1001.
The following detailed description will be further described in conjunction with the above-described drawings.
Detailed Description
In the following description, numerous specific details are set forth in order to provide a thorough understanding of the concepts underlying the described embodiments, however, it will be apparent to those skilled in the art that the described embodiments may be practiced without some or all of these specific details, and in other cases well-known process steps have not been described in detail.
In the description of the present invention, it is to be understood that the terms "upper", "lower", "front", "rear", "left", "right", "top", "bottom", "inner", "outer", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplicity of description, and do not indicate or imply that the device or element being referred to must have a specific orientation, be constructed and operated in a specific orientation, and thus, should not be construed as limiting the present invention.
As shown in fig. 1, fig. 2, fig. 3, fig. 4, and fig. 5, a concentrating apparatus for wastewater concentration dealcoholization membrane process comprises a fixing base 1, a housing cover 2, a suction pump 3, a first filter ring group 4, a second filter ring group 5, a third filter ring group 6, a first temporary storage chamber 7, a second temporary storage chamber 8, a third temporary storage chamber 9, a flow rate sensor 10, a first regulating valve 11, and a second regulating valve 12, wherein the housing cover 2 is fixedly arranged on the top of the fixing base 1, the housing cover 2 and the fixing base 1 are integrally formed, the suction pump 3 is fixedly arranged in the middle of the rear end of the housing cover 2, the suction pump 3 is connected with the housing cover 2 by welding, the first filter ring group 4 is fixedly arranged in the middle of the housing cover 2, the first filter ring group 4 is connected with the housing cover 2 by welding, the second filter ring group 5 is arranged outside the first filter ring group 4, the second filter ring group 5 and the outer casing cover 2 are connected by welding, the third filter ring group 6 is positioned outside the second filter ring group 5, the third filter ring group 6 and the outer casing cover 2 are connected by welding, the first temporary storage chamber 7 is positioned between the first filter ring group 4 and the second filter ring group 5, the first temporary storage chamber 7 is an annular cavity, the second temporary storage chamber 8 is positioned between the second filter ring group 5 and the third filter ring group 6, the second temporary storage chamber 8 is an annular cavity, the third temporary storage chamber 9 is positioned between the third filter ring group 6 and the outer wall of the outer casing cover 2, the third temporary storage chamber 6 is an annular cavity, the flow rate sensors 10 are a plurality of pieces, the flow rate sensors 10 are respectively fixed at the inner front end of the outer casing cover 2 from left to right, the flow rate sensors 10 are connected with the outer casing cover 2 by hot melting, the flow rate sensors 10 are respectively located inside the first temporary storage cavity 7, the second temporary storage cavity 8 and the third temporary storage cavity 9, the number of the first regulating valves 11 is a plurality of pieces, the first regulating valves 11 are fixedly arranged at the front ends inside the outer housing 2 from top to bottom, the first regulating valves 11 are connected with the outer housing 2 in a hot melting mode, the first regulating valves 11 are respectively located inside the first temporary storage cavity 7, the second temporary storage cavity 8 and the third temporary storage cavity 9, the number of the second regulating valves 12 is a plurality of pieces, the second regulating valves 12 are fixedly arranged at the front ends inside the outer housing 2 from top to bottom, the second regulating valves 12 are connected with the outer housing 2 in a hot melting mode, and the second regulating valves 12 are respectively located inside the first filter ring group 4, the second filter ring group 5 and the third filter ring group 6;
the concentration equipment for the wastewater concentration dealcoholization membrane method has the following functions;
A. the suction pump 3 can generate negative pressure suction after being started, so that external sewage can conveniently enter the shell cover 2 and sequentially passes through the first filtering ring group 4, the second filtering ring group 5 and the third filtering ring group 6 to be discharged, and because the surfaces of the first filtering ring group 4, the second filtering ring group 5 and the third filtering ring group 6 are provided with a plurality of micropores, filtering substances such as active carbon are filled in the first filtering ring group 4, the second filtering ring group 5 and the third filtering ring group 6, so that the substances in the wastewater can be filtered, and the concentration and dealcoholization effect is improved, meanwhile, a worker can also regularly open the second regulating valve 12, suck the filtering substances in the first filtering ring group 4, the second filtering ring group 5 and the third filtering ring group 6, and then refill new filtering substances, so that the problem that the filtering effect is influenced after the filtering substances are used for a long time is solved;
B. the first temporary storage cavity 7, the second temporary storage cavity 8 and the third temporary storage cavity 9 can be used for facilitating temporary storage of wastewater respectively, facilitating that the wastewater sequentially passes through the first filter ring group 4, the second filter ring group 5 and the third filter ring group 6, improving the filtering effect and simultaneously facilitating storage of dealcoholized impurities, and facilitating suction cleaning of the dealcoholized impurities in the first temporary storage cavity 7, the second temporary storage cavity 8 and the third temporary storage cavity 9 after a follow-up worker opens the first regulating valve 11;
C. the flow velocity sensor 10 can also detect the flow velocity of the liquid in the first temporary storage cavity 7, the second temporary storage cavity 8 and the third temporary storage cavity 9, so that the blocking condition of the filtering material can be analyzed by workers by judging the flow velocity, and the filtering material can be replaced regularly;
an inlet pipe 201 is fixedly arranged at the top end inside the outer shell cover 2, and the inlet pipe 201 is connected with the outer shell cover 2 in a welding manner;
it should be noted that the inlet pipe 201 can be butted with a waste water drainage pipeline in the prior art, so that waste water can flow into the outer housing cover 2 from the inlet pipe 201;
the first filtering ring group 4, the second filtering ring group 5 and the third filtering ring group 6 are all internally provided with filtering substance storage cavities 401, and the filtering substance storage cavities 401 are annular cavities;
it should be noted that the filtering material storage cavity 401 can be filled with filtering materials, such as activated carbon particles, so as to facilitate subsequent filtering treatment of the circulating medium;
a flow rate display 1001 is fixedly arranged at the front end of the flow rate sensor 10, the flow rate display 1001 is electrically connected with the flow rate sensor 10, and the flow rate display 1001 is connected with the outer shell cover 2 in a hot melting way;
it should be noted that flow rate display 1001 can receive and display the fluid speeds detected by a plurality of flow rate sensors 10, so as to facilitate the operator to grasp and analyze.
Claims (4)
1. The utility model provides a be used for concentrated dealcoholize embrane method concentrator in waste water, its characterized in that includes fixing base, dustcoat, suction pump, first filtration ring group, second filtration ring group, third filtration ring group, first chamber of keeping in, second chamber of keeping in, third chamber of keeping in, velocity of flow sensor, first governing valve, second governing valve, the dustcoat set firmly in the fixing base top, dustcoat and fixing base integrated into one piece, the suction pump set firmly in dustcoat rear end middle part, suction pump and dustcoat adopt welded connection, first filtration ring group set firmly in the inside middle-end of dustcoat, first filtration ring group and dustcoat adopt welded connection, second filtration ring group be located the first filtration ring group outside, second filtration ring group and dustcoat adopt welded connection, third filtration ring group be located the second filtration ring group outside, the third filtering ring group and the outer cover are connected by welding, the first temporary storage cavity is positioned between the first filtering ring group and the second filtering ring group, the first temporary storage cavity is an annular cavity, the second temporary storage cavity is positioned between the second filtering ring group and the third filtering ring group, the second temporary storage cavity is an annular cavity, the third temporary storage cavity is positioned between the outer walls of the third filtering ring group and the outer cover, the third temporary storage cavity is an annular cavity, the quantity of the flow rate sensors is a plurality of pieces, the flow rate sensors are fixedly arranged at the front end inside the outer cover from left to right respectively, the flow rate sensors and the outer cover are connected by hot melting, the flow rate sensors are respectively positioned inside the first temporary storage cavity, the second temporary storage cavity and the third temporary storage cavity, the quantity of the first regulating valves is a plurality of pieces, the first regulating valves are fixedly arranged at the front end inside the outer cover from top to bottom, first governing valve and outer covering adopt the hot melt to be connected, just first governing valve be located first chamber, the second chamber and the third chamber of keeping in respectively, second governing valve quantity be a plurality of, the second governing valve from last to setting firmly in the inside front end of outer covering down, second governing valve and outer covering adopt the hot melt to be connected, just the second governing valve be located first filtration ring group, second filtration ring group and third filtration ring group respectively inside.
2. The concentration equipment for the concentration and dealcoholization of the wastewater by the membrane method as claimed in claim 1, wherein an inlet pipe is fixedly arranged at the top end inside the outer casing, and the inlet pipe is connected with the outer casing by welding.
3. The concentration equipment for wastewater concentration and dealcoholization membrane method according to claim 1, wherein the first filtering ring group, the second filtering ring group and the third filtering ring group are all provided with filtering material storage cavities inside, and the filtering material storage cavities are annular cavities.
4. The concentration equipment for the concentration and dealcoholization membrane method in wastewater as claimed in claim 1, wherein a flow rate display is fixedly arranged at the front end of the flow rate sensor, the flow rate display is electrically connected with the flow rate sensor, and the flow rate display is connected with the outer housing cover by hot melting.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220804794.7U CN217051822U (en) | 2022-04-08 | 2022-04-08 | Concentration equipment for concentration and dealcoholization in wastewater by membrane method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220804794.7U CN217051822U (en) | 2022-04-08 | 2022-04-08 | Concentration equipment for concentration and dealcoholization in wastewater by membrane method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217051822U true CN217051822U (en) | 2022-07-26 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202220804794.7U Active CN217051822U (en) | 2022-04-08 | 2022-04-08 | Concentration equipment for concentration and dealcoholization in wastewater by membrane method |
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| Country | Link |
|---|---|
| CN (1) | CN217051822U (en) |
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- 2022-04-08 CN CN202220804794.7U patent/CN217051822U/en active Active
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