CN206872617U - A kind of pharmacy wastewater treatment system - Google Patents
A kind of pharmacy wastewater treatment system Download PDFInfo
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- CN206872617U CN206872617U CN201720434381.3U CN201720434381U CN206872617U CN 206872617 U CN206872617 U CN 206872617U CN 201720434381 U CN201720434381 U CN 201720434381U CN 206872617 U CN206872617 U CN 206872617U
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- sedimentation basin
- wastewater treatment
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Abstract
The utility model discloses a kind of pharmacy wastewater treatment system, belong to waste water system technical field, the pharmacy wastewater treatment system includes wastewater collection pond, the first sedimentation basin, catalysis oxidation pond, biochemistry pool, regulating reservoir, UASB anaerobic ponds, preaeration tank, the second sedimentation basin, Aerobic Pond, multilayer dielectricity filtering ponds, detection cell, reuse pool.Pharmacy wastewater treatment system architecture simple and compact of the present utility model, floor space is small, stable performance, and Pharmaceutical Wastewater Treatment cost is low, can effectively reduce small-sized pharmacy corporation and steal effluent phenomenon, the waste water for handling up to standard is directly entered environment, avoids polluting environment.
Description
【Technical field】
The utility model belongs to waste water system technical field, more particularly to a kind of pharmacy wastewater treatment system.
【Background technology】
With the development of China's medical industry, pharmacy waste water has been increasingly becoming one of important pollution sources.Pharmaceutical industry category
In fine chemistry industry, its feature is exactly that production of raw medicine is wide in variety, and production process is more, and utilization rate of raw materials is low.For these reasons,
Pharmaceuticals industry waste water generally has complicated component, and organic pollutant category is more, and salt content is high, NH3-N, the characteristics such as colourity is deep, than
Other treatment of Organic Wastewater are more difficult.Because pharmaceuticals industry environmental protection is more late than pharmaceuticals industry starting, and pollution administration can not
Direct economic benefit is brought to enterprise, pharmaceutical wastewater treatment process also lags behind pharmaceutical technology.Simultaneously because pharmacy waste water is answered
Miscellaneous changeable characteristic, also there is problems and weak point for present handling process.So many pharmacy waste waters are difficult at present
Remained high with processing, or processing cost, therefore the phenomenon of effluent steathily more or less be present in some small-sized pharmacy corporations,
To it not handle or handle below standard waste water and be directly entered environment, serious harm will be caused to environment.
【Utility model content】
The utility model provides a kind of pharmacy wastewater treatment system, is difficult to handle to solve existing existing pharmacy waste water,
Or processing cost remains high, some small-sized pharmacy corporations steal effluent, and it is straight not handle or handle below standard waste water
Tap into environment, the problems such as causing to seriously endanger to environment, pharmacy wastewater treatment system architecture simple and compact of the present utility model,
Floor space is small, stable performance, and Pharmaceutical Wastewater Treatment cost is low, can effectively reduce small-sized pharmacy corporation and steal effluent phenomenon,
The waste water for handling up to standard is directly entered environment, avoids polluting environment.
To solve above technical problem, the utility model provides following technical scheme：
A kind of pharmacy wastewater treatment system, including wastewater collection pond, the first sedimentation basin, catalysis oxidation pond, biochemistry pool, regulation
Pond, UASB anaerobic ponds, preaeration tank, the second sedimentation basin, Aerobic Pond, multilayer dielectricity filtering ponds, detection cell, reuse pool, it is special
Sign is：The wastewater collection pond side is connected by pipeline with first sedimentation basin；The first sedimentation basin opposite side leads to
Piping is connected with the catalysis oxidation pond；Catalysis oxidation pond opposite side is connected by pipeline with the biochemistry pool；It is described
Biochemistry pool opposite side is connected by pipeline with the regulating reservoir；The regulating reservoir opposite side passes through pipeline and the UASB anaerobic ponds
It is connected；The UASB anaerobic ponds opposite side is connected by pipeline with the preaeration tank；The preaeration tank opposite side passes through pipe
Road is connected with second sedimentation basin；The second sedimentation basin opposite side is connected by pipeline with the Aerobic Pond；It is described aerobic
Pond opposite side is connected by pipeline with the multilayer dielectricity filtering ponds；The multilayer dielectricity filtering ponds opposite side passes through pipeline and institute
Detection cell is stated to be connected；The detection cell opposite side is connected by pipeline with the reuse pool.
Further, the wastewater collection pond is provided with wastewater collection pond water inlet pipe, and grid are provided with the wastewater collection pond
Net, the grid gap length of the aperture plate is 0.04-0.1cm.
Further, separation filter plate is provided with first sedimentation basin；Temperature device, institute are provided with first sedimentation basin
State temperature device and maintain temperature at 23-30 DEG C.
Further, dephosphorization apparatus and nitrogen removing device are provided with the biochemistry pool；The biochemistry pool is provided with biochemistry pool air inlet
Pipe, aeration tube, observation panel, the biochemistry pool air inlet pipe are located on the biochemistry pool, and the aeration tube is located at the biochemistry pool bottom
Portion, the observation panel are located at the top of the biochemistry pool.
Further, the bottom of the preaeration tank is equipped with the discharge pipe being connected with external air blower, for passing through connection
Pipeline receives the waste water that anoxic pond is overflowed and completes preaeration.
Further, the bottom in the Aerobic Pond pond is equipped with the discharge pipe being connected with external air blower, for passing through connection
Pipeline receives the waste water that first sedimentation basin overflows and carries out Aerobic Process for Treatment.
Further, the reuse pool is provided with reuse pool outlet pipe.
The utility model has following effects：
(1) pharmacy wastewater treatment system excellent wastewater treatment effect of the present utility model, the water of discharge do not cause dirt to environment
Dye, efficiently solves the reluctant problem of existing pharmacy waste water；
(2) pharmacy wastewater treatment system architecture simple and compact of the present utility model, floor space is small, stable performance, making
Cost is low, is advantageous to promote the use of；
(3) pharmacy wastewater treatment system Pharmaceutical Wastewater Treatment cost of the present utility model is low, can effectively reduce small-sized system
Effluent phenomenon is stolen by medicine enterprise, and the waste water for handling up to standard is directly entered into environment, avoids polluting environment.
【Brief description of the drawings】
Fig. 1 is the utility model pharmacy wastewater treatment system structure diagram,
In figure, 1 is wastewater collection pond, and 1-1 is wastewater collection pond water inlet pipe, and 2 be the first sedimentation basin, and 3 be catalysis oxidation pond,
4 be biochemistry pool, and 41 be biochemistry pool air inlet pipe, and 42 be aeration tube, and 43 be observation panel, and 5 be regulating reservoir, and 6 be UASB anaerobic ponds, and 7 are
Preaeration tank, 8 be the second sedimentation basin, and 9 be Aerobic Pond, and 10 be multilayer dielectricity filtering ponds, and 11 be detection cell, and 12 be reuse pool,
121 be reuse pool outlet pipe.
【Embodiment】
The utility model content is described in detail with reference to such as Fig. 1.
Embodiment 1
A kind of pharmacy wastewater treatment system, including wastewater collection pond 1, the first sedimentation basin 2, catalysis oxidation pond 3, biochemistry pool 4,
Regulating reservoir 5, UASB anaerobic ponds 6, preaeration tank 7, the second sedimentation basin 8, Aerobic Pond 9, multilayer dielectricity filtering ponds 10, detection cell 11,
Reuse pool 12, the side of wastewater collection pond 1 is connected by pipeline with first sedimentation basin 2, in the wastewater collection pond 1
Provided with wastewater collection pond water inlet pipe 1-1, aperture plate is provided with the wastewater collection pond 1, the grid gap length of the aperture plate is
0.04cm；The opposite side of first sedimentation basin 2 is connected by pipeline with the catalysis oxidation pond 3, is set in first sedimentation basin 2
There is separation filter plate；Temperature device is provided with first sedimentation basin 2, the temperature device maintains temperature at 28 DEG C；The catalysis
The opposite side of oxidation pond 3 is connected by pipeline with the biochemistry pool 4, and dephosphorization apparatus and nitrogen removing device are provided with the biochemistry pool 4；Institute
State biochemistry pool 4 and be located at the biochemistry provided with biochemistry pool air inlet pipe 41, aeration tube 42, observation panel 43, the biochemistry pool air inlet pipe 41
On pond 4, the aeration tube 42 is located at the bottom of biochemistry pool 4, and the observation panel 43 is located at the top of biochemistry pool 4；The life
Change the opposite side of pond 4 by pipeline with the regulating reservoir 5 to be connected；The opposite side of regulating reservoir 5 passes through pipeline and the UASB anaerobism
Pond 6 is connected；The opposite side of UASB anaerobic ponds 6 is connected by pipeline with the preaeration tank 7, the bottom of the preaeration tank 7
The discharge pipe being connected with external air blower is equipped with, for receiving the waste water of anoxic pond spilling by connecting line and completing pre-exposure
Gas；The opposite side of preaeration tank 7 is connected by pipeline with second sedimentation basin 8；The opposite side of second sedimentation basin 8 passes through
Pipeline is connected with the Aerobic Pond 9, and the bottom in the pond of Aerobic Pond 9 is equipped with the discharge pipe being connected with external air blower, for leading to
Cross connecting line and receive the waste water progress Aerobic Process for Treatment that first sedimentation basin overflows；The opposite side of Aerobic Pond 9 passes through pipeline
It is connected with the multilayer dielectricity filtering ponds 10；The opposite side of multilayer dielectricity filtering ponds 10 passes through pipeline and the phase of detection cell 11
Even；The opposite side of detection cell 11 is connected by pipeline with the reuse pool 12, and the reuse pool 12 is provided with recycle-water
Pond outlet pipe 121.
Embodiment 2
A kind of pharmacy wastewater treatment system, including wastewater collection pond 1, the first sedimentation basin 2, catalysis oxidation pond 3, biochemistry pool 4,
Regulating reservoir 5, UASB anaerobic ponds 6, preaeration tank 7, the second sedimentation basin 8, Aerobic Pond 9, multilayer dielectricity filtering ponds 10, detection cell 11,
Reuse pool 12, the side of wastewater collection pond 1 is connected by pipeline with first sedimentation basin 2, in the wastewater collection pond 1
Provided with wastewater collection pond water inlet pipe 1-1, aperture plate is provided with the wastewater collection pond 1, the grid gap length of the aperture plate is
0.1cm；The opposite side of first sedimentation basin 2 is connected by pipeline with the catalysis oxidation pond 3, is set in first sedimentation basin 2
There is separation filter plate；Temperature device is provided with first sedimentation basin 2, the temperature device maintains temperature at 23 DEG C；The catalysis
The opposite side of oxidation pond 3 is connected by pipeline with the biochemistry pool 4, and dephosphorization apparatus and nitrogen removing device are provided with the biochemistry pool 4；Institute
State biochemistry pool 4 and be located at the biochemistry provided with biochemistry pool air inlet pipe 41, aeration tube 42, observation panel 43, the biochemistry pool air inlet pipe 41
On pond 4, the aeration tube 42 is located at the bottom of biochemistry pool 4, and the observation panel 43 is located at the top of biochemistry pool 4；The life
Change the opposite side of pond 4 by pipeline with the regulating reservoir 5 to be connected；The opposite side of regulating reservoir 5 passes through pipeline and the UASB anaerobism
Pond 6 is connected；The opposite side of UASB anaerobic ponds 6 is connected by pipeline with the preaeration tank 7, the bottom of the preaeration tank 7
The discharge pipe being connected with external air blower is equipped with, for receiving the waste water of anoxic pond spilling by connecting line and completing pre-exposure
Gas；The opposite side of preaeration tank 7 is connected by pipeline with second sedimentation basin 8；The opposite side of second sedimentation basin 8 passes through
Pipeline is connected with the Aerobic Pond 9, and the bottom in the pond of Aerobic Pond 9 is equipped with the discharge pipe being connected with external air blower, for leading to
Cross connecting line and receive the waste water progress Aerobic Process for Treatment that first sedimentation basin overflows；The opposite side of Aerobic Pond 9 passes through pipeline
It is connected with the multilayer dielectricity filtering ponds 10；The opposite side of multilayer dielectricity filtering ponds 10 passes through pipeline and the phase of detection cell 11
Even；The opposite side of detection cell 11 is connected by pipeline with the reuse pool 12, and the reuse pool 12 is provided with recycle-water
Pond outlet pipe 121.
Embodiment 3
A kind of pharmacy wastewater treatment system, including wastewater collection pond 1, the first sedimentation basin 2, catalysis oxidation pond 3, biochemistry pool 4,
Regulating reservoir 5, UASB anaerobic ponds 6, preaeration tank 7, the second sedimentation basin 8, Aerobic Pond 9, multilayer dielectricity filtering ponds 10, detection cell 11,
Reuse pool 12, the side of wastewater collection pond 1 is connected by pipeline with first sedimentation basin 2, in the wastewater collection pond 1
Provided with wastewater collection pond water inlet pipe 1-1, aperture plate is provided with the wastewater collection pond 1, the grid gap length of the aperture plate is
0.06cm；The opposite side of first sedimentation basin 2 is connected by pipeline with the catalysis oxidation pond 3, is set in first sedimentation basin 2
There is separation filter plate；Temperature device is provided with first sedimentation basin 2, the temperature device maintains temperature at 30 DEG C；The catalysis
The opposite side of oxidation pond 3 is connected by pipeline with the biochemistry pool 4, and dephosphorization apparatus and nitrogen removing device are provided with the biochemistry pool 4；Institute
State biochemistry pool 4 and be located at the biochemistry provided with biochemistry pool air inlet pipe 41, aeration tube 42, observation panel 43, the biochemistry pool air inlet pipe 41
On pond 4, the aeration tube 42 is located at the bottom of biochemistry pool 4, and the observation panel 43 is located at the top of biochemistry pool 4；The life
Change the opposite side of pond 4 by pipeline with the regulating reservoir 5 to be connected；The opposite side of regulating reservoir 5 passes through pipeline and the UASB anaerobism
Pond 6 is connected；The opposite side of UASB anaerobic ponds 6 is connected by pipeline with the preaeration tank 7, the bottom of the preaeration tank 7
The discharge pipe being connected with external air blower is equipped with, for receiving the waste water of anoxic pond spilling by connecting line and completing pre-exposure
Gas；The opposite side of preaeration tank 7 is connected by pipeline with second sedimentation basin 8；The opposite side of second sedimentation basin 8 passes through
Pipeline is connected with the Aerobic Pond 9, and the bottom in the pond of Aerobic Pond 9 is equipped with the discharge pipe being connected with external air blower, for leading to
Cross connecting line and receive the waste water progress Aerobic Process for Treatment that first sedimentation basin overflows；The opposite side of Aerobic Pond 9 passes through pipeline
It is connected with the multilayer dielectricity filtering ponds 10；The opposite side of multilayer dielectricity filtering ponds 10 passes through pipeline and the phase of detection cell 11
Even；The opposite side of detection cell 11 is connected by pipeline with the reuse pool 12, and the reuse pool 12 is provided with recycle-water
Pond outlet pipe 121.
Embodiment 4
A kind of pharmacy wastewater treatment system, including wastewater collection pond 1, the first sedimentation basin 2, catalysis oxidation pond 3, biochemistry pool 4,
Regulating reservoir 5, UASB anaerobic ponds 6, preaeration tank 7, the second sedimentation basin 8, Aerobic Pond 9, multilayer dielectricity filtering ponds 10, detection cell 11,
Reuse pool 12, the side of wastewater collection pond 1 is connected by pipeline with first sedimentation basin 2, in the wastewater collection pond 1
Provided with wastewater collection pond water inlet pipe 1-1, aperture plate is provided with the wastewater collection pond 1, the grid gap length of the aperture plate is
0.05cm；The opposite side of first sedimentation basin 2 is connected by pipeline with the catalysis oxidation pond 3, is set in first sedimentation basin 2
There is separation filter plate；Temperature device is provided with first sedimentation basin 2, the temperature device maintains temperature at 25 DEG C；The catalysis
The opposite side of oxidation pond 3 is connected by pipeline with the biochemistry pool 4, and dephosphorization apparatus and nitrogen removing device are provided with the biochemistry pool 4；Institute
State biochemistry pool 4 and be located at the biochemistry provided with biochemistry pool air inlet pipe 41, aeration tube 42, observation panel 43, the biochemistry pool air inlet pipe 41
On pond 4, the aeration tube 42 is located at the bottom of biochemistry pool 4, and the observation panel 43 is located at the top of biochemistry pool 4；The life
Change the opposite side of pond 4 by pipeline with the regulating reservoir 5 to be connected；The opposite side of regulating reservoir 5 passes through pipeline and the UASB anaerobism
Pond 6 is connected；The opposite side of UASB anaerobic ponds 6 is connected by pipeline with the preaeration tank 7, the bottom of the preaeration tank 7
The discharge pipe being connected with external air blower is equipped with, for receiving the waste water of anoxic pond spilling by connecting line and completing pre-exposure
Gas；The opposite side of preaeration tank 7 is connected by pipeline with second sedimentation basin 8；The opposite side of second sedimentation basin 8 passes through
Pipeline is connected with the Aerobic Pond 9, and the bottom in the pond of Aerobic Pond 9 is equipped with the discharge pipe being connected with external air blower, for leading to
Cross connecting line and receive the waste water progress Aerobic Process for Treatment that first sedimentation basin overflows；The opposite side of Aerobic Pond 9 passes through pipeline
It is connected with the multilayer dielectricity filtering ponds 10；The opposite side of multilayer dielectricity filtering ponds 10 passes through pipeline and the phase of detection cell 11
Even；The opposite side of detection cell 11 is connected by pipeline with the reuse pool 12, and the reuse pool 12 is provided with recycle-water
Pond outlet pipe 121.
Embodiment 5
A kind of pharmacy wastewater treatment system, including wastewater collection pond 1, the first sedimentation basin 2, catalysis oxidation pond 3, biochemistry pool 4,
Regulating reservoir 5, UASB anaerobic ponds 6, preaeration tank 7, the second sedimentation basin 8, Aerobic Pond 9, multilayer dielectricity filtering ponds 10, detection cell 11,
Reuse pool 12, the side of wastewater collection pond 1 is connected by pipeline with first sedimentation basin 2, in the wastewater collection pond 1
Provided with wastewater collection pond water inlet pipe 1-1, aperture plate is provided with the wastewater collection pond 1, the grid gap length of the aperture plate is
0.08cm；The opposite side of first sedimentation basin 2 is connected by pipeline with the catalysis oxidation pond 3, is set in first sedimentation basin 2
There is separation filter plate；Temperature device is provided with first sedimentation basin 2, the temperature device maintains temperature at 28 DEG C；The catalysis
The opposite side of oxidation pond 3 is connected by pipeline with the biochemistry pool 4, and dephosphorization apparatus and nitrogen removing device are provided with the biochemistry pool 4；Institute
State biochemistry pool 4 and be located at the biochemistry provided with biochemistry pool air inlet pipe 41, aeration tube 42, observation panel 43, the biochemistry pool air inlet pipe 41
On pond 4, the aeration tube 42 is located at the bottom of biochemistry pool 4, and the observation panel 43 is located at the top of biochemistry pool 4；The life
Change the opposite side of pond 4 by pipeline with the regulating reservoir 5 to be connected；The opposite side of regulating reservoir 5 passes through pipeline and the UASB anaerobism
Pond 6 is connected；The opposite side of UASB anaerobic ponds 6 is connected by pipeline with the preaeration tank 7, the bottom of the preaeration tank 7
The discharge pipe being connected with external air blower is equipped with, for receiving the waste water of anoxic pond spilling by connecting line and completing pre-exposure
Gas；The opposite side of preaeration tank 7 is connected by pipeline with second sedimentation basin 8；The opposite side of second sedimentation basin 8 passes through
Pipeline is connected with the Aerobic Pond 9, and the bottom in the pond of Aerobic Pond 9 is equipped with the discharge pipe being connected with external air blower, for leading to
Cross connecting line and receive the waste water progress Aerobic Process for Treatment that first sedimentation basin overflows；The opposite side of Aerobic Pond 9 passes through pipeline
It is connected with the multilayer dielectricity filtering ponds 10；The opposite side of multilayer dielectricity filtering ponds 10 passes through pipeline and the phase of detection cell 11
Even；The opposite side of detection cell 11 is connected by pipeline with the reuse pool 12, and the reuse pool 12 is provided with recycle-water
Pond outlet pipe 121.
Above content is to combine specific preferred embodiment further detailed description of the utility model, it is impossible to
Assert that specific implementation of the present utility model is confined to these explanations.For the ordinary skill of the utility model art
For personnel, without departing from the concept of the premise utility, some simple deduction or replace can also be made, should all be regarded
To belong to the scope of patent protection that the utility model is determined by the claims submitted.
Claims (7)
1. a kind of pharmacy wastewater treatment system, including wastewater collection pond (1), the first sedimentation basin (2), catalysis oxidation pond (3), biochemistry
Pond (4), regulating reservoir (5), UASB anaerobic ponds (6), preaeration tank (7), the second sedimentation basin (8), Aerobic Pond (9), multilayer dielectricity mistake
Filter tank (10), detection cell (11), reuse pool (12), it is characterised in that：Wastewater collection pond (1) side passes through pipeline and institute
The first sedimentation basin (2) is stated to be connected；First sedimentation basin (2) opposite side is connected by pipeline with the catalysis oxidation pond (3)；Institute
Catalysis oxidation pond (3) opposite side is stated by pipeline with the biochemistry pool (4) to be connected；Biochemistry pool (4) opposite side passes through pipeline
It is connected with the regulating reservoir (5)；Regulating reservoir (5) opposite side is connected by pipeline with the UASB anaerobic ponds (6)；It is described
UASB anaerobic ponds (6) opposite side is connected by pipeline with the preaeration tank (7)；Preaeration tank (7) opposite side passes through pipe
Road is connected with second sedimentation basin (8)；Second sedimentation basin (8) opposite side is connected by pipeline with the Aerobic Pond (9)；
Aerobic Pond (9) opposite side is connected by pipeline with the multilayer dielectricity filtering ponds (10)；The multilayer dielectricity filtering ponds
(10) opposite side is connected by pipeline with the detection cell (11)；Detection cell (11) opposite side passes through pipeline and the reuse
Pond (12) is connected.
2. pharmacy wastewater treatment system according to claim 1, it is characterised in that：The wastewater collection pond (1) is provided with
Wastewater collection pond water inlet pipe (1-1), the wastewater collection pond (1) is interior to be provided with aperture plate, and the grid gap length of the aperture plate is
0.04-0.1cm。
3. pharmacy wastewater treatment system according to claim 1, it is characterised in that：It is provided with first sedimentation basin (2)
Separate filter plate；Temperature device is provided with first sedimentation basin (2), the temperature device maintains temperature at 23-30 DEG C.
4. pharmacy wastewater treatment system according to claim 1, it is characterised in that：Dephosphorization is provided with the biochemistry pool (4)
Device and nitrogen removing device；The biochemistry pool (4) is provided with biochemistry pool air inlet pipe (41), aeration tube (42), observation panel (43), the life
Change pond air inlet pipe (41) to be located on the biochemistry pool (4), the aeration tube (42) is located at the biochemistry pool (4) bottom, the sight
Cha Kou (43) is located at the top of the biochemistry pool (4).
5. pharmacy wastewater treatment system according to claim 1, it is characterised in that：Put the bottom of the preaeration tank (7)
There is the discharge pipe being connected with external air blower, for receiving the waste water of anoxic pond spilling by connecting line and completing preaeration.
6. pharmacy wastewater treatment system according to claim 1, it is characterised in that：Put the bottom in Aerobic Pond (9) pond
There is the discharge pipe being connected with external air blower, the waste water for receiving the first sedimentation basin spilling by connecting line enters to act charitably
Oxygen processing.
7. pharmacy wastewater treatment system according to claim 1, it is characterised in that：The reuse pool (12) is provided with back
Millpond outlet pipe (121).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720434381.3U CN206872617U (en) | 2017-04-24 | 2017-04-24 | A kind of pharmacy wastewater treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720434381.3U CN206872617U (en) | 2017-04-24 | 2017-04-24 | A kind of pharmacy wastewater treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206872617U true CN206872617U (en) | 2018-01-12 |
Family
ID=61343159
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720434381.3U Expired - Fee Related CN206872617U (en) | 2017-04-24 | 2017-04-24 | A kind of pharmacy wastewater treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206872617U (en) |
-
2017
- 2017-04-24 CN CN201720434381.3U patent/CN206872617U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180112 Termination date: 20210424 |