CN217103199U - Rain sewage treatment system - Google Patents
Rain sewage treatment system Download PDFInfo
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- CN217103199U CN217103199U CN202123103028.2U CN202123103028U CN217103199U CN 217103199 U CN217103199 U CN 217103199U CN 202123103028 U CN202123103028 U CN 202123103028U CN 217103199 U CN217103199 U CN 217103199U
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- liquid level
- sedimentation tank
- signal
- coagulating sedimentation
- sewage
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- 239000010865 sewage Substances 0.000 title claims abstract description 50
- 238000004062 sedimentation Methods 0.000 claims abstract description 159
- 230000001112 coagulating effect Effects 0.000 claims abstract description 88
- 239000007788 liquid Substances 0.000 claims abstract description 66
- 238000012806 monitoring device Methods 0.000 claims abstract description 16
- 230000015271 coagulation Effects 0.000 claims description 93
- 238000005345 coagulation Methods 0.000 claims description 93
- 239000010802 sludge Substances 0.000 claims description 42
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 40
- 238000005189 flocculation Methods 0.000 claims description 17
- 230000016615 flocculation Effects 0.000 claims description 17
- 238000007599 discharging Methods 0.000 claims description 9
- 238000010992 reflux Methods 0.000 claims description 5
- 238000001556 precipitation Methods 0.000 description 29
- 238000004519 manufacturing process Methods 0.000 description 11
- 238000012544 monitoring process Methods 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 239000000470 constituent Substances 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
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Abstract
The utility model relates to a rain sewage treatment system, include: a monitoring device configured to monitor a liquid level and a liquid level variation amount of the storage tank and generate a liquid level signal and a liquid level variation signal; a control device communicatively connected to the monitoring device configured to receive the liquid level signal and the liquid level variation signal from the monitoring device; a coagulating sedimentation tank unit communicatively connected to the control device and communicated with the storage tank to receive the rainwater and sewage from the storage tank, the coagulating sedimentation tank unit including a plurality of coagulating sedimentation tanks, wherein the control device is configured to compare the liquid level signal with a predetermined liquid level threshold value after receiving the liquid level signal and the liquid level variation signal, so that when the liquid level signal is greater than the predetermined liquid level threshold value, an inflow flow peak value is predicted based on the liquid level variation signal, a ratio of the predicted inflow flow peak value to a predetermined design peak value is calculated, and based on the calculated ratio, the number of coagulating sedimentation tanks to be started is obtained, and a start signal is sent to the coagulating sedimentation tank unit.
Description
Technical Field
The utility model relates to a rain sewage treatment system.
Background
With the increase of urban scale, atmospheric pollution and ground pollution are aggravated, and rainwater runoff pollution is increasingly serious. The urban rainwater sewage has the characteristics that (1) rainwater runoff pollution belongs to non-point source pollution and has burst property and non-continuity. (2) The pollutant content in the initial stage rainwater is high, and along with the continuation of runoff, the surface of rainwater runoff is constantly washed, and the pollutant content reduces gradually to relatively stable concentration. (3) The maximum value of the pollutant index of initial rainwater is far higher than that of typical urban domestic sewage, but the composition of the initial rainwater is completely different from that of the typical urban domestic sewage.
At present, the treatment process of domestic sewage is commonly used in the rain sewage treatment, such as a common coagulating sedimentation tank, a conventional high-efficiency sedimentation tank and the like, and a rain sewage treatment system is designed according to a typical urban domestic sewage treatment system. Rain sewage treatment facilities usually face typical problems of rain season and dry season switching, large water inflow amount and water quality fluctuation and the like, and the rain sewage treatment facilities adopt a typical urban domestic sewage treatment process and have the problems of low adaptability, low automation degree and difficulty in meeting the actual treatment requirements of rain sewage.
SUMMERY OF THE UTILITY MODEL
The utility model provides a rain sewage treatment system, include: a monitoring device configured to monitor a liquid level and a liquid level variation amount of the storage tank and generate a liquid level signal and a liquid level variation signal; a control device communicatively connected to the monitoring device configured to receive the liquid level signal and the liquid level variation signal from the monitoring device; and a coagulation sedimentation tank unit communicatively connected to the control device and communicated with the storage tank to receive the rainwater and sewage from the storage tank, the coagulation sedimentation tank unit including a plurality of coagulation sedimentation tanks, wherein the control device is configured to compare the liquid level signal with a predetermined liquid level threshold value after receiving the liquid level signal and the liquid level variation signal, so that when the liquid level signal is greater than the predetermined liquid level threshold value, an inflow flow peak value is predicted based on the liquid level variation signal, a ratio of the predicted inflow flow peak value to a predetermined design peak value is calculated, and based on the calculated ratio, the number of the coagulation sedimentation tanks to be started is obtained, and a start signal is sent to the coagulation sedimentation tank unit to start the number of the coagulation sedimentation tanks.
Advantageously, after calculating the ratio of the peak value of the inflow to the predetermined design peak value, the control device is configured to determine which of a plurality of predetermined ratio ranges the calculated ratio lies within, so as to obtain the number of coagulative precipitation tanks to be started.
Advantageously, the interval lengths of said plurality of predetermined ratio ranges are determined based on the following formula: and L is 1 x 100%/m, wherein L is the interval length, and m is the total number of the coagulation sedimentation tank.
Advantageously, during the start-up of the number of coagulative precipitation tanks, the reject produced water produced by the number of coagulative precipitation tanks is discharged to the remaining un-started coagulative precipitation tanks of the coagulative precipitation unit.
Advantageously, the coagulating sedimentation tank unit comprises: the rainwater and sewage flow into the water inlet channel of the coagulating sedimentation tank unit through the water inlet pipe; each coagulating sedimentation tank of the coagulating sedimentation tank unit is communicated with the return channel through a first automatic gate plate; and the water production channel of each coagulation sedimentation tank of the coagulation sedimentation tank unit is communicated with the main water outlet channel through a second automatic gate plate, wherein during the starting period of the coagulation sedimentation tank, the second automatic gate plate corresponding to the coagulation sedimentation tank is closed, and the first automatic gate plate corresponding to the coagulation sedimentation tank is opened, so that unqualified water produced by the coagulation sedimentation tank flows to the rest coagulation sedimentation tanks of the coagulation sedimentation tank unit through the return channel.
Advantageously, the coagulative precipitation tank unit further comprises a return pump provided at each coagulative precipitation tank, such that during start-up of the coagulative precipitation tank, off-spec produced water is pumped via the return pump to the return canal.
Advantageously, after the start of the number of the coagulation sedimentation tanks is completed, the first automatic gate corresponding to the number of the coagulation sedimentation tanks is closed, and the second automatic gate corresponding to the number of the coagulation sedimentation tanks is opened, so that qualified production water produced by the number of the coagulation sedimentation tanks flows into the production canal.
Advantageously, the control means is further configured to vary the number of coagulative precipitation tanks to be started when the ratio of the predicted influent flow peak to the predetermined design peak is varied to within a different predetermined ratio range.
Advantageously, the control means is configured to also send a start signal to another number of coagulative precipitation tanks when the ratio of the predicted inlet water flow peak to the predetermined design peak increases.
Advantageously, the control device is configured to discharge the sludge resulting from the treatment in the number of coagulation sedimentation tanks to the flocculation zone of each coagulation sedimentation tank of the number of coagulation sedimentation tanks during the start-up of the number of coagulation sedimentation tanks, and to discharge the sludge resulting from the treatment in the number of coagulation sedimentation tanks to the sludge treatment plant after the start-up of the number of coagulation sedimentation tanks is completed.
Advantageously, the coagulating sedimentation tank unit further comprises: and a sludge discharge pipe which is communicated with the sludge discharge port of the settling zone of each coagulation sedimentation tank, the sludge discharge pipe is communicated with the flocculation zone of each coagulation sedimentation tank through a first automatic valve on one hand, and is communicated with the sludge treatment plant through a second automatic valve on the other hand, so that the first automatic valve is opened and the second automatic valve is closed during the starting of the other quantity of coagulation sedimentation tanks, the sludge produced through the treatment of the quantity of coagulation sedimentation tanks is discharged to the flocculation zone of each coagulation sedimentation tank of the other quantity of coagulation sedimentation tanks through the sludge discharge pipe, after the starting of the other quantity of coagulation sedimentation tanks is completed, the first automatic valve is closed and the second automatic valve is opened, and the sludge produced through the treatment of the quantity of coagulation sedimentation tanks is discharged to the sludge treatment plant.
Advantageously, the stormwater treatment system further comprises an emptying unit comprising: the automatic emptying valve is arranged in the settling zone and is used for automatically discharging part of sewage to a sewage pipe network; the sludge reflux pump is arranged in the sedimentation area of each coagulation sedimentation tank and is used for refluxing the residual sewage in the sedimentation area to the flocculation area of each coagulation sedimentation tank; the emptying pump is arranged in the flocculation area of each coagulation sedimentation tank and is used for discharging the residual sewage in the coagulation area and the flocculation area to a sewage pipe network; and the sludge discharge pump is arranged in the settling zone of each coagulating sedimentation tank and is used for discharging the sludge in the settling zone to a sludge treatment plant.
Advantageously, the monitoring device is further configured to monitor a rainfall state and generate a rainfall signal; the liquid level of the catchment canal is monitored, a liquid level signal of the catchment canal is generated, and the catchment canal is used for collecting rain sewage and conveying the rain sewage to the regulation and storage pool.
Advantageously, the control device is further configured to predict the liquid level change amount of the storage tank based on the received rainfall signal and the catchment canal liquid level signal to generate a liquid level change signal.
Drawings
The advantages and objects of the present invention will be better understood from the following detailed description of the preferred embodiments of the invention, taken in conjunction with the accompanying drawings. The drawings are not necessarily to scale, emphasis instead being placed upon illustrating the relationship of the various components. In the drawings:
fig. 1 is a block diagram showing a rain sewage treatment system according to the present invention;
fig. 2 is a schematic view showing a coagulation sedimentation tank unit of the rain sewage treatment system according to the present invention.
Fig. 3 is an enlarged view showing a detail G of fig. 2.
Fig. 4 shows a schematic view of an evacuation cell.
Detailed Description
Various embodiments according to the present invention will be described in detail with reference to the accompanying drawings. Here, it is to be noted that, in the drawings, the same reference numerals are given to constituent parts having substantially the same or similar structures and functions, and repeated description thereof will be omitted. The term "sequentially comprising A, B, etc" merely indicates the order of the included elements A, B, etc. and does not exclude the possibility of including other elements between a and B and/or between B and B.
The drawings in the present specification are schematic views to assist in explaining the concept of the present invention, and schematically show the shapes of the respective portions and the mutual relationships thereof.
Hereinafter, referring to fig. 1 and 2, a preferred embodiment according to the present invention will be described in detail.
Fig. 1 shows a block diagram of a rain sewage treatment system according to the present invention. The rainwater and sewage treatment system includes a monitoring device 1 configured to monitor a liquid level and a liquid level variation amount of a regulation tank, and generate a liquid level signal and a liquid level variation signal. The control device 2 is communicatively connected to the monitoring device and is configured to receive the liquid level signal and the liquid level variation signal from the monitoring device. The coagulation sedimentation tank unit 3 is communicatively connected to the control device, and communicates with the regulation tank to receive the rainwater water from the regulation tank, and includes a plurality of coagulation sedimentation tanks.
In this example, the monitoring device generates a rainfall signal and a catchment canal liquid level signal by monitoring the rainfall state and the liquid level of the catchment canal, respectively, the catchment canal being used to collect rain water and convey the rain water to the storage tank. The control device predicts the liquid level variation of the regulation and storage tank by analyzing the rainfall signal and the water collecting pipe and canal liquid level signal, thereby obtaining the liquid level variation signal. However, it will be appreciated by those skilled in the art that the monitoring device can also directly obtain the liquid change signal by monitoring the amount of change in the liquid level in the storage tank, without monitoring the rainfall state and monitoring the liquid level in the catchment canal.
The control device is configured to compare the liquid level signal to a predetermined liquid level threshold upon receiving the liquid level signal and the liquid level change signal. And under the condition that the liquid level signal is greater than a preset liquid level threshold value, the control device predicts a water inflow peak value based on the liquid level change signal, calculates the ratio of the predicted water inflow peak value to a preset design peak value, calculates the number of the coagulation sedimentation tanks to be started based on the calculated ratio, and sends a starting signal to the coagulation sedimentation tank unit to start the coagulation sedimentation tanks in the number.
Fig. 2 shows an example of a coagulation sedimentation tank unit. In this example, the coagulating sedimentation basin unit comprises 6 coagulating sedimentation basins a-F, and the 6 coagulating sedimentation basins are divided into three groups of 2 coagulating sedimentation basins each. It will be appreciated by those skilled in the art that any number of coagulative precipitation tanks may be included.
As described above, in the case where the liquid level signal is greater than the predetermined liquid level threshold value, the control device predicts the inflow peak value based on the liquid level variation signal, and calculates the ratio of the predicted inflow peak value to the predetermined design peak value. When the calculated ratio is within a certain predetermined ratio range of a plurality of predetermined ratio ranges, the control device obtains the number of the coagulation sedimentation tanks to be started, and sends starting information to the number of the coagulation sedimentation tanks. For example, when the ratio of the predicted inlet water flow peak value to the preset design peak value is between 0 and 33 percent, the control device sends a starting signal to the first group of coagulating sedimentation tanks A and B.
The interval lengths of the plurality of predetermined ratio ranges are determined based on the following formula: and L is 1 x 100%/m, wherein L is the interval length, and m is the total number of the coagulation sedimentation tank. For example, when there are 6 coagulating sedimentation tanks and every 2 coagulating sedimentation tanks are used as a group, the interval length L of the corresponding predetermined ratio range is 2 × 100%/6 — 33% for each group of coagulating sedimentation tanks.
During the start-up of this number of coagulation sedimentation tanks, for example during the start-up of the first set of coagulation sedimentation tanks a and B, the reject produced water produced by the coagulation sedimentation tanks a and B may be discharged to the remaining coagulation sedimentation tanks C-F of the coagulation sedimentation tank unit, preferably to the second set of coagulation sedimentation tanks C and D. After the first group of coagulating sedimentation tanks A and B are started, the coagulating sedimentation tanks A and B are normally operated, and qualified effluent enters a water producing channel.
The control means issues a start signal to the second set of coagulation sedimentation tanks C and D when the calculated ratio is in another one of the predetermined ratio ranges, for example when the calculated ratio is in the range of 34-66%.
Similarly, during start-up of the second set of coagulative precipitation tanks C and D, the off-spec produced water produced by the coagulative precipitation tanks C and D may be discharged to the coagulative precipitation tanks E and F of the coagulative precipitation tank unit. After the second group of coagulating sedimentation tanks C and D are started, the coagulating sedimentation tanks C and D are normally operated, and qualified effluent enters a water producing channel.
The control means sends a start signal to the third set of coagulation sedimentation tanks E and F when the calculated ratio is in a further predetermined ratio range of the plurality of predetermined ratio ranges, for example when the calculated ratio is 67-100%.
During start-up of the third set of coagulative precipitation tanks E and F, the off-spec produced water produced by the coagulative precipitation tanks E and F may be returned to the coagulative precipitation tanks E and F. And after the third group of coagulating sedimentation tanks E and F are started, the coagulating sedimentation tanks E and F are normally operated, and qualified effluent enters a water producing channel.
As shown in fig. 2, the coagulation sedimentation tank unit 3 comprises a water inlet pipe 31, and rain sewage flows into an inlet channel 32 of the coagulation sedimentation tank unit through the water inlet pipe 31; a return channel 33, each coagulation sedimentation tank of the coagulation sedimentation tank unit is communicated with the return channel 33 through a first automatic gate 34; the main water outlet channel 35, the production channel 37 of each coagulation sedimentation tank of the coagulation sedimentation tank unit are communicated with the main water outlet channel 35 through a second automatic gate plate 36. In this example, the first set of coagulative precipitation tanks a and B share a production canal 37, the second set of coagulative precipitation tanks C and D share a production canal 37, and the third set of coagulative precipitation tanks E and F share a production canal 37, but it will be appreciated that each coagulative precipitation tank may have a respective production canal that communicates with the main water outlet canal.
In fig. 2, the return channel 33 and the inlet channel 32 are shown in the same position, but in practice the inlet channel 32 and the return channel 33 are separated from one another, as shown, for example, in fig. 3, which shows an enlarged view of detail G in fig. 2, showing the inlet channel 32 and the return channel 33 separated from one another. Those skilled in the art will appreciate that the location of the inlet channel 32 and return channel 33 is not limited as long as the functions described herein are achieved.
In such a case, during the start-up of the first set of coagulating sedimentation tanks a and B, the second automatic gate plates 36 corresponding to the coagulating sedimentation tanks a and B are closed, while the first automatic gate plates 34 corresponding to the coagulating sedimentation tanks a and B are opened, so that the reject produced water produced by the coagulating sedimentation tanks a and B is flowed to the coagulating sedimentation tanks C and D of the coagulating sedimentation tank unit via the return channel 33 by the return pump (not shown).
After the start-up of the coagulation sedimentation tanks a and B is completed, the first automatic gate plates 34 corresponding to the coagulation sedimentation tanks a and B are closed, and the second automatic gate plates 36 corresponding to the coagulation sedimentation tanks a and B are opened, so that the qualified produced water produced by the coagulation sedimentation tanks a and B flows into the production channel and into the main production channel.
Similarly, the above operations can also be performed during the start-up of the second set of coagulating sedimentation tanks C and D, and are not described in detail herein.
During the start-up of the third set of coagulation sedimentation tanks E and F, the second automatic shutter 36 corresponding to the coagulation sedimentation tanks E and F is closed, and the first automatic shutter 34 corresponding to the coagulation sedimentation tanks E and F is opened, so that the reject produced water produced by the coagulation sedimentation tanks E and F is returned to the coagulation sedimentation tanks E and F via the return channel 33 by a return pump (not shown).
The coagulation sedimentation tank unit further comprises a sludge discharge pipe communicating with a sludge discharge port of the sedimentation zone of each coagulation sedimentation tank, the sludge discharge pipe communicating with the flocculation zone of each coagulation sedimentation tank through a first automatic valve on the one hand and communicating with the sludge treatment plant through a second automatic valve on the other hand, such that during the start-up of another number of coagulation sedimentation tanks, the first automatic valve is opened and the second automatic valve is closed, the sludge produced by the treatment of the number of coagulation sedimentation tanks is discharged to the flocculation zone of each coagulation sedimentation tank of the another number of coagulation sedimentation tanks through the sludge discharge pipe, and after the start-up of the another number of coagulation sedimentation tanks is completed, the first automatic valve is closed and the second automatic valve is opened, and the sludge produced by the treatment of the number of coagulation sedimentation tanks is discharged to the sludge treatment plant.
In this example, after the first set of coagulative precipitation tanks a and B are started and during the second set of coagulative precipitation tanks C and D are started, the first automatic valves corresponding to the second set of coagulative precipitation tanks C and D are opened, and the second automatic valves corresponding to the first set of coagulative precipitation tanks a and B are closed, so that the sludge generated by the first set of coagulative precipitation tanks a and B is discharged to the flocculation zone of the second set of coagulative precipitation tanks through the sludge pump, and the starting speed of the second set of coagulative precipitation tanks is accelerated. After the second group of coagulating sedimentation tanks C and D are started, the first automatic valves corresponding to the second group of coagulating sedimentation tanks C and D are closed, the second automatic valves corresponding to the first group of coagulating sedimentation tanks A and B are opened, and the sludge generated by the first group of coagulating sedimentation tanks A and B is discharged to a sludge treatment plant.
During the start-up of the third set of coagulating sedimentation tanks E and F, the sludge in the first set and the second set of coagulating sedimentation tanks can be discharged to the flocculation zone of the third set of coagulating sedimentation tanks, and the process is as described above and will not be described herein again.
As shown in fig. 4, the rainwater and sewage treatment system further includes an emptying unit 4 provided at the coagulation sedimentation tank unit for preventing the rainwater and sewage in the tank from deteriorating and smelling when the machine is stopped for a long time. The evacuation unit 4 includes: the automatic emptying valve is arranged in the settling zone and is used for automatically discharging part of sewage to a sewage pipe network; a sludge return pump 41 arranged in the sedimentation zone of each coagulation sedimentation tank and used for returning the residual sewage in the sedimentation zone to the flocculation zone of each coagulation sedimentation tank; the emptying pump 42 is arranged in the flocculation area of each coagulation sedimentation tank and is used for discharging the residual sewage in the coagulation area and the flocculation area to a sewage pipe network; and the sludge discharge pump 43 is arranged at the settling zone of each coagulating sedimentation tank and is used for discharging the sludge in the settling zone to a sludge treatment plant.
The coagulating sedimentation tank is one of a coagulating inclined tube sedimentation tank, a high-density sedimentation tank, a sand-adding high-efficiency sedimentation tank and a magnetic coagulating high-efficiency sedimentation tank.
The rain sewage treatment system of the utility model arranges the backflow channel on the coagulating sedimentation tank unit, and accelerates the starting speed of the coagulating sedimentation tank through the unqualified backflow water production; during the starting period, sludge backflow is designed, and the starting speed of the coagulating sedimentation tank is accelerated; the emptying unit after stopping the pool can automatically empty, and the coagulating sedimentation pool unit is emptied by areas. Therefore, automatic starting and stopping can be realized according to the rainfall condition; no unqualified water is discharged in each starting period; the sludge reflux system can be used for realizing quick and automatic starting; automatic emptying after pool stopping can be achieved through the emptying unit.
It should be clear to a person skilled in the art that the above disclosed technical features are not limited to the disclosed combinations with other features, and that other combinations between the technical features can be made by a person skilled in the art according to the purpose of the invention to achieve the object of the invention.
Claims (6)
1. A rain sewage treatment system, comprising:
a monitoring device configured to monitor a liquid level and a liquid level variation amount of the storage tank and generate a liquid level signal and a liquid level variation signal;
a control device communicatively connected to the monitoring device configured to receive the liquid level signal and the liquid level variation signal from the monitoring device;
a coagulating sedimentation tank unit communicatively connected to the control device and communicating with the storage tank to receive the storm sewage from the storage tank, the coagulating sedimentation tank unit including a plurality of coagulating sedimentation tanks,
the rainwater sewage treatment system further comprises an emptying unit, and the emptying unit comprises:
the automatic emptying valve is arranged in the settling zone and is used for automatically discharging part of sewage to a sewage pipe network;
the sludge reflux pump is arranged in the sedimentation area of each coagulation sedimentation tank and is used for refluxing the residual sewage in the sedimentation area to the flocculation area of each coagulation sedimentation tank;
the emptying pump is arranged in the flocculation area of each coagulation sedimentation tank and is used for discharging the residual sewage in the coagulation area and the flocculation area to a sewage pipe network;
and the sludge discharge pump is arranged in the settling zone of each coagulating sedimentation tank and is used for discharging the sludge in the settling zone to a sludge treatment plant.
2. The stormwater treatment system as claimed in claim 1, wherein the coagulating sedimentation tank unit comprises:
the rainwater and sewage flow into the water inlet channel of the coagulating sedimentation tank unit through the water inlet pipe;
each coagulating sedimentation tank of the coagulating sedimentation tank unit is communicated with the return channel through a first automatic gate plate;
and the main water outlet channel, the water producing channel of each coagulating sedimentation tank of the coagulating sedimentation tank unit is communicated with the main water outlet channel through a second automatic gate plate.
3. The stormwater treatment system as claimed in claim 2, wherein the coagulation sedimentation tank unit further comprises a return pump provided at each coagulation sedimentation tank, such that during start-up of the coagulation sedimentation tank, reject produced water is pumped through the return pump to the return channel.
4. The stormwater treatment system as claimed in claim 1, wherein the coagulating sedimentation tank unit further comprises:
a sludge discharge pipe communicated with the sludge discharge port of the settling zone of each coagulation sedimentation tank,
the sludge discharge pipe is communicated with the flocculation area of each coagulation sedimentation tank through a first automatic valve on one hand, and is communicated with a sludge treatment plant through a second automatic valve on the other hand.
5. The stormwater treatment system as claimed in claim 1, wherein the monitoring device is further configured to monitor a rainfall condition and generate a rainfall signal; the liquid level of the catchment canal is monitored, a liquid level signal of the catchment canal is generated, and the catchment canal is used for collecting rain sewage and conveying the rain sewage to the regulation and storage pool.
6. The stormwater treatment system as claimed in claim 5, wherein the control means is further configured to predict an amount of change in the liquid level of the storage tank based on the received rainfall signal and the catchment channel liquid level signal to generate the liquid level change signal.
Priority Applications (1)
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CN202123103028.2U CN217103199U (en) | 2021-12-08 | 2021-12-08 | Rain sewage treatment system |
Applications Claiming Priority (1)
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CN202123103028.2U CN217103199U (en) | 2021-12-08 | 2021-12-08 | Rain sewage treatment system |
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CN217103199U true CN217103199U (en) | 2022-08-02 |
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CN202123103028.2U Active CN217103199U (en) | 2021-12-08 | 2021-12-08 | Rain sewage treatment system |
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2021
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Address after: 3101, 27th Floor, Building 1, Yard 38, East 3rd Ring North Road, Chaoyang District, Beijing, 100026 Patentee after: Suez Environmental Technology (Beijing) Co.,Ltd. Address before: 100026 31 / F, Taikang financial building, building 1, courtyard 38, East Third Ring Road North, Chaoyang District, Beijing Patentee before: Suez Water Treatment Co,.Ltd. |