CN206837724U - A kind of flue gas of refuse burning processing system - Google Patents
A kind of flue gas of refuse burning processing system Download PDFInfo
- Publication number
- CN206837724U CN206837724U CN201720095778.4U CN201720095778U CN206837724U CN 206837724 U CN206837724 U CN 206837724U CN 201720095778 U CN201720095778 U CN 201720095778U CN 206837724 U CN206837724 U CN 206837724U
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- China
- Prior art keywords
- water washing
- pipeline
- flue gas
- processing system
- washing tank
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 37
- 239000003546 flue gas Substances 0.000 title claims abstract description 37
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 86
- 238000005406 washing Methods 0.000 claims abstract description 59
- 239000007789 gas Substances 0.000 claims abstract description 30
- 238000004062 sedimentation Methods 0.000 claims abstract description 22
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 13
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 13
- 239000007921 spray Substances 0.000 claims description 32
- 230000003204 osmotic effect Effects 0.000 claims description 20
- 239000003610 charcoal Substances 0.000 claims description 17
- 239000004576 sand Substances 0.000 claims description 17
- 230000008595 infiltration Effects 0.000 claims description 9
- 238000001764 infiltration Methods 0.000 claims description 9
- 238000009434 installation Methods 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 4
- 238000001914 filtration Methods 0.000 abstract description 8
- 238000004140 cleaning Methods 0.000 abstract description 6
- 239000000779 smoke Substances 0.000 abstract description 4
- 238000000889 atomisation Methods 0.000 abstract description 3
- 238000010276 construction Methods 0.000 abstract description 3
- 238000000034 method Methods 0.000 abstract description 3
- 238000004056 waste incineration Methods 0.000 abstract description 3
- 238000010327 methods by industry Methods 0.000 abstract description 2
- 230000008569 process Effects 0.000 abstract description 2
- 239000010865 sewage Substances 0.000 description 9
- 239000010813 municipal solid waste Substances 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000001052 transient effect Effects 0.000 description 3
- 238000009264 composting Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000009738 saturating Methods 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 230000001360 synchronised effect Effects 0.000 description 2
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
Abstract
The utility model discloses a kind of flue gas of refuse burning processing system, including water washing device, liquefying plant and filter；Described water washing device is connected by pipeline A with liquefying plant；Described liquefying plant is connected by pipeline B with filter；Described water washing device includes inlet manifold, sedimentation basin, water washing tank and sprinkler part；Described liquefying plant includes gas pipeline, drive device, the hydraulic turbine and cistern；Described filter includes housing, active carbon layer and gas outlet；Described inlet manifold（101）, pipeline A, gas pipeline and pipeline B be sequentially connected.The utility model includes water washing device, liquefying plant and filter, dense smoke caused by burning can be carried out to water washing cleaning, high-pressure atomization and filtering emission process one by one, simple in construction, process engineering is reasonable, effectively overcomes the smoke pollution problem of waste incineration.
Description
Technical field
The utility model belongs to Purificatory Technology field, is related to a kind of flue gas of refuse burning processing system
System.
Background technology
With expanding economy, the yield of house refuse also increases constantly.Domestic rubbish disposal mode at present, it is main
There are three kinds of sanitary landfills, During High-Temperature Composting and burn sintering energy methods.Because sanitary landfills and During High-Temperature Composting two ways can produce
More serious problem of environmental pollution, thus burn sintering energy processing mode is the direction of urban garbage disposal.But burn
House refuse is harmful into after high temperature incineration in caused flue gas containing a large amount of dioxin, heavy metal, HCl etc. during system can be handled
Point, it is therefore necessary to qualified discharge after handling flue gas.With carrying forward vigorously for national energy-saving emission reduction policy, discarded object is arranged
The standard put requires more and more stricter, and the advance of flue-gas cleaning devices, reliability, security, applicability it is also proposed more
High requirement.
And current fume treatment auxiliary is usually present the problems such as complicated, cost is high, clean-up effect is poor, it is unfavorable for
Flue gas of refuse burning treatment technology be widely popularized and it is long-term use of.
The content of the invention
The utility model is for overcome the deficiencies in the prior art, there is provided the washing of one kind collection, atomization and filtering emission are one
Body, purification efficiency is high, practical flue gas of refuse burning processing system.
To achieve these goals, the technical solution of the utility model is as follows：
A kind of flue gas of refuse burning processing system, including water washing device, liquefying plant and filter；Described washing dress
Put and be connected by pipeline A with liquefying plant；Described liquefying plant is connected by pipeline B with filter；
Described water washing device includes inlet manifold, sedimentation basin, water washing tank and sprinkler part；The top of described water washing tank
It is connected with inlet manifold；Described water washing tank is installed in sedimentation basin；Described sprinkler part include spray house steward, shower and
Spray thrower；A pair of showers are provided with described water washing tank, shower is longitudinally mounted in water washing tank；Described shower is in parallel
To spray house steward；Spray thrower it has been uniformly provided with described shower, the spray thrower on a pair of showers in water washing tank is handed over
Mistake installation；
Described liquefying plant includes gas pipeline, drive device, the hydraulic turbine and cistern；Described drive device and water
Turbine connects；The described hydraulic turbine is fixed in cistern by bearing；Described gas pipeline is connected with the hydraulic turbine；
Described filter includes housing, active carbon layer and gas outlet；The outlet of described gas pipeline and housing
Top connects；Described active carbon layer is located at housing central section, and gap be present with housing bottom；Described gas outlet is located at housing
Top；
Described inlet manifold, pipeline A, gas pipeline and pipeline B is sequentially connected.
The flue gas of refuse burning processing system also includes purifier；Described purifier includes multistage infiltration pond, oozes
Press cascade arrangement in saturating pond；Described sedimentation basin is provided with water outlet A, the water outlet A connection of first order osmotic cell and sedimentation basin；
Described osmotic cell includes pond body, permeation unit and water outlet B；Described permeation unit by dividing plate, sand layer of charcoal and pond body side
Wall surrounds；Described dividing plate is arranged in pond body；The thickness of described sand layer of charcoal is less than the height of dividing plate；The bottom of described dividing plate
Portion is concordant with the bottom of sand layer of charcoal, exists with pond body bottom and is spaced；The side wall of described osmotic cell is provided with delivery port.
Preferably, above-described water washing tank has-group；Described water washing tank is staggered installed in precipitation by front and back position
In pond.Water washing tank arranges in " product " font or " V " type, reduces floor space,
Preferably, the above-described hydraulic turbine includes circular housing, blade and drive shaft；Described blade is distributed on driving
On axle；The lower section of described circular housing is provided with breach；The bottom of described circular housing/-/place immerse cistern liquid level
Lower section；Described drive shaft is connected with drive device.
Preferably, the above-described hydraulic turbine is provided with 3-4 groups.
As a further improvement, the flue gas of refuse burning processing system also includes also including the circulatory system；Described circulation
System includes circulating pump and circulation pipe；Described circulating pump is arranged on the top of osmotic cell；The water inlet pipe peace of described circulating pump
Above sand layer of charcoal, the outlet pipe of circulating pump and one end of circulation pipe connect；The other end of described circulation pipe is total with spray
Pipe connects.
Preferably, above-described circulating pump is arranged on the top of afterbody osmotic cell.
Preferably, the height of above-described active carbon layer is the 2/3-3/4 of body height.Gas filtration is complete, realizes
Non-pollution discharge.
Preferably, above-described spray thrower is spiral spray thrower.
Operation principle of the present utility model：Caused flue gas is passed through after inlet manifold enters water washing tank after waste incineration,
In the presence of spray thrower on shower, the sediment in flue gas is settled down in sedimentation basin completely；Flue gas after cleaning passes through
Pipeline A is entered in liquefaction system, and drive device impeller machine is synchronized with the movement, and turbine drives the water in cistern to revolve at a high speed
Turn, the increase of pressure in turbine, into turbine flue gas in the presence of high-pressure cold water transient liquefaction, the mist eventually formed
Gas enters filter by pipeline B, is discharged after active carbon layer by filtering；Sewage in sedimentation basin passes through in osmotic cell
Infiltration layer by layer, in the presence of sand layer of charcoal, sewage is purified, and can be recycled in water washing tank and be recycled.
The utility model has the advantage that and had the beneficial effect that：
1st, the utility model includes water washing device, liquefying plant and filter, can be by dense smoke caused by burning one by one
Water washing cleaning, high-pressure atomization and filtering emission process are carried out, simple in construction, process engineering is reasonable, effectively overcomes rubbish
The smoke pollution problem that rubbish burns.
2nd, of the present utility model to install a pair of showers in each water washing tank, the spray thrower on a pair of showers is staggeredly pacified
Dress, the spray at no dead angle is realized, so as to fully be washed to entering the flue gas in water washing tank, ensure that the washing cooling of flue gas is net
Change effect.
3rd, multigroup water washing tank of the present utility model is staggered installation of by front and back position, is arranged in " product " font or " V " type, is reduced
Floor space, improve the practicality of device.
4th, the utility model devises liquefying plant, in the presence of the hydraulic turbine drives liquid at high speed to rotate, improves water wheels
Pressure in machine, flue gas encounter high-pressure cold water transient liquefaction, reduce the final discharge of gas, while have reached further water
The purpose of flue gas is washed, strengthens the purification function to flue gas.
5th, the outer casing bottom of the hydraulic turbine of the present utility model is provided with breach, and top is connected with gas pipeline, works as axis of rotation
When, blade drives water to rotate at a high speed, forms high pressure in shell, and the gas in gas pipeline runs into cold water in hyperbaric environment
Rapid liquefaction afterwards, reduces the discharge of gas, design science is reasonable, simple in construction, has very strong practicality.
6th, the utility model is provided with multistage infiltration pond, using the principle of underground water, the sewage to settling acquisition in sedimentation basin
Permeation filtration step by step is carried out, the water after purification is finally obtained, reduces the discharge of sewage.
7th, the utility model in the water circulation after permeation filtration to water washing tank, will realize the repetition profit of water by circulation pipe
With efficent use of resources.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Fig. 2 is partial schematic diagram at the A in Fig. 1.
Fig. 3 is the schematic top plan view of the water washing device of embodiment 3.
Accompanying drawing identifies：
101- inlet manifold, 102- spray house stewards, 103- water washing tanks, 104- water outlet As, 105- sedimentation basins, 106- sprays
Pipe, 107- spray throwers；
2- pipelines A；
301- gas pipelines, the 302- hydraulic turbines, 303- cisterns, 304- blades, 305- drive shafts, 306- circular housings,
307- drive devices；
4- pipelines B；
501- housings, 502- active carbon layers, 503- gas outlets；
601- circulation pipes, 602- circulating pumps；
701- osmotic cells, 702- pond bodies, 703- dividing plates, 704- sand layer of charcoal；705- water outlet Bs.
Embodiment
The utility model is described further below in conjunction with the accompanying drawings.
Embodiment 1：
A kind of flue gas of refuse burning processing system, including water washing device, liquefying plant and filter；Described washing dress
Put and be connected by pipeline A2 with liquefying plant；Described liquefying plant is connected by pipeline B4 with filter.
Described water washing device includes inlet manifold 101, sedimentation basin 105, water washing tank 103 and sprinkler part；Described water
The top of cleaning of evaporator 103 is connected with inlet manifold 101；Provided with 4-8 groups water washing tank 103, water washing tank 103 is in staggeredly by front and back position
Chinese character pin-shaped arrangement is arranged in sedimentation basin 105；Described sprinkler part includes spray house steward 102, shower 106 and spray thrower
107；A pair of showers 106 are provided with described water washing tank 103, shower 106 is longitudinally mounted in water washing tank 103；Described
Shower 106 is connected in parallel on spray house steward 102；Spray thrower 107, water washing tank 103 have been uniformly provided with described shower 106
Spray thrower 107 on interior a pair of showers 106 is staggered installation of；Described spray thrower 107 is spiral spray thrower 107.
Described liquefying plant includes gas pipeline 301, drive device 307, the hydraulic turbine 302 and cistern 303；Described
Drive device 307 is connected with the hydraulic turbine 302；The described hydraulic turbine 302 is fixed in cistern 303 by bearing, provided with 3 groups of water
Turbine 302；Described gas pipeline 301 is connected with the hydraulic turbine 302.
The described hydraulic turbine 302 includes circular housing 306, blade 304 and drive shaft 305；Described blade 304 is distributed on
In drive shaft 305；The lower section of described circular housing 306 is provided with breach；The 1/4-1/3 of the bottom of described circular housing 306
Place is immersed below the liquid level of cistern 303；Described drive shaft 305 is connected with drive device 307.
Described filter includes housing 501, active carbon layer 502 and gas outlet 503；Described gas pipeline 301
Outlet is connected with the top of housing 501；Described active carbon layer 502 exists located at the middle part of housing 501, and with the bottom of housing 501
Gap；The height of active carbon layer 502 is the 2/3-3/4 of the height of housing 501；Described gas outlet 503 is upper located at housing 501
Side.
Described inlet manifold 101, pipeline A2, gas pipeline 301 and pipeline B4 is sequentially connected.
Caused flue gas is passed through after inlet manifold 101 enters water washing tank 103 after waste incineration, on shower 106
In the presence of spiral spray thrower 107, the sediment in flue gas is settled down in sedimentation basin 105 completely；Flue gas after cleaning passes through
Pipeline A2 is entered in liquefaction system, and the impeller machine 302 of drive device 307 is synchronized with the movement, and turbine 302 drives cistern
Water in 303 rotates at a high speed, the pressure increase in turbine 302, into turbine 302 flue gas high-pressure cold water effect
Lower transient liquefaction, the fog eventually formed enter filter by pipeline B4, are arranged after active carbon layer 502 by filtering
Go out.Sewage in sedimentation basin is by the infiltration layer by layer in osmotic cell, and in the presence of sand layer of charcoal, sewage is purified, and can be with
It is recycled in water washing tank and is recycled.
Embodiment 2：
The embodiment difference from Example 1 is：
Water washing device is provided with 6 groups of water washing tanks 103, and water washing tank 103 is staggeredly arranged on precipitation by front and back position in V-shape arrangement
In pond 105, liquefying plant is provided with 4 groups of hydraulic turbines.The flue gas of refuse burning processing system also includes purifier；Described is net
Makeup is put presses cascade arrangement including multistage infiltration pond 701, osmotic cell 701；Described sedimentation basin 105 is provided with delivery port
A104, first order osmotic cell 701 are connected with the water outlet A 104 of sedimentation basin 105；Described osmotic cell 701 includes pond body 702, oozed
Saturating unit and water outlet B 705；Described permeation unit is surrounded by the side wall of dividing plate 703, sand layer of charcoal 704 and pond body 702；It is described
Dividing plate 703 be arranged in pond body 702；The thickness of described sand layer of charcoal 704 is less than the height of dividing plate 703；Described dividing plate
703 bottom is concordant with the bottom of sand layer of charcoal 704, exists with the bottom of pond body 702 and is spaced；In the side wall of described osmotic cell 701
Provided with delivery port.Sewage in sedimentation basin 105 is dirty in the presence of sand layer of charcoal 704 by the infiltration layer by layer in osmotic cell 701
Water warfare is recycled.
Embodiment 3：
The embodiment difference from Example 2 is：
Water washing device is provided with 8 groups of water washing tanks 103, and it is heavy that water washing tank 103 is staggeredly arranged on by front and back position in Chinese character pin-shaped arrangement
In shallow lake pond 105.The flue gas of refuse burning processing system also includes the circulatory system；The described circulatory system includes the He of circulating pump 602
Circulation pipe 601；Described circulating pump 602 is arranged on the top of afterbody osmotic cell 701；The water inlet of described circulating pump 602
Pipe is arranged on the top of sand layer of charcoal 704, and the outlet pipe of circulating pump 602 is connected with one end of circulation pipe 601；Described circulation pipe 601
The other end with spray house steward 102 be connected.Sewage in sedimentation basin 105 is by the infiltration layer by layer in osmotic cell 701, in sand layer of charcoal
In the presence of 704, sewage is purified, and the water after purification can be recycled in water washing tank 103 by circulation pipe 601 and be circulated
Utilize.
Claims (9)
- A kind of 1. flue gas of refuse burning processing system, it is characterised in that：Including water washing device, liquefying plant and filter；Institute The water washing device stated passes through pipeline A（2）It is connected with liquefying plant；Described liquefying plant passes through pipeline B（4）Connect with filter Connect；Described water washing device includes inlet manifold（101）, sedimentation basin（105）, water washing tank（103）And sprinkler part；Described Water washing tank（103）Top and inlet manifold（101）Connection；Described water washing tank（103）It is installed on sedimentation basin（105）In；Institute The sprinkler part stated includes spray house steward（102）, shower（106）And spray thrower（107）；Described water washing tank（103）Inside set There are a pair of showers（106）, shower（106）It is longitudinally mounted to water washing tank（103）It is interior；Described shower（106）It is connected in parallel to Spray house steward（102）On；Described shower（106）On be uniformly provided with spray thrower（107）, water washing tank（103）A pair of interior sprays Shower pipe（106）On spray thrower（107）It is staggered installation of；Described liquefying plant includes gas pipeline（301）, drive device（307）, the hydraulic turbine（302）And cistern（303）；Institute The drive device stated（307）With the hydraulic turbine（302）Connection；The described hydraulic turbine（302）Cistern is fixed on by bearing（303） In；Described gas pipeline（301）With the hydraulic turbine（302）Connection；Described filter includes housing（501）, active carbon layer（502）And gas outlet（503）；Described gas pipeline （301）Outlet and housing（501）Top connection；Described active carbon layer（502）Located at housing（501）Middle part, and and shell Body（501）Gap be present in bottom；Described gas outlet（503）Located at housing（501）Top；Described inlet manifold（101）, pipeline A（2）, gas pipeline（301）With pipeline B（4）It is sequentially connected.
- A kind of 2. flue gas of refuse burning processing system according to claim 1, it is characterised in that：Also include purifier； Described purifier includes multistage infiltration pond（701）, osmotic cell（701）By cascade arrangement；Described sedimentation basin（105）On Provided with water outlet A（104）, first order osmotic cell（701）With sedimentation basin（105）Water outlet A（104）Connection；Described infiltration Pond（701）Including pond body（702）, permeation unit and water outlet B（705）；Described permeation unit is by dividing plate（703）, sand layer of charcoal （704）And pond body（702）Side wall surround；Described dividing plate（703）It is arranged at pond body（702）It is interior；Described sand layer of charcoal（704） Thickness be less than dividing plate（703）Height；Described dividing plate（703）Bottom and sand layer of charcoal（704）Bottom it is concordant, with pond body （702）Interval be present in bottom；Described osmotic cell（701）Side wall be provided with delivery port.
- A kind of 3. flue gas of refuse burning processing system according to claim 1, it is characterised in that：Described water washing tank （103）There are 4-8 groups；Described water washing tank（103）It is staggered by front and back position installed in sedimentation basin（105）It is interior.
- A kind of 4. flue gas of refuse burning processing system according to claim 1, it is characterised in that：The described hydraulic turbine （302）Including circular housing（306）, blade（304）And drive shaft（305）；Described blade（304）It is distributed on drive shaft （305）On；Described circular housing（306）Lower section be provided with breach；Described circular housing（306）Bottom 1/4-1/3 Cistern is immersed at place（303）Liquid level below；Described drive shaft（305）With drive device（307）Connection.
- A kind of 5. flue gas of refuse burning processing system according to claim 1, it is characterised in that：The described hydraulic turbine （302）Provided with 3-4 groups.
- A kind of 6. flue gas of refuse burning processing system according to claim 2, it is characterised in that：Also include the circulatory system； The described circulatory system includes circulating pump（602）And circulation pipe（601）；Described circulating pump（602）Installed in osmotic cell（701） Top；Described circulating pump（602）Water inlet pipe be arranged on sand layer of charcoal（704）Top, circulating pump（602）Outlet pipe with following Endless tube（601）One end connection；Described circulation pipe（601）The other end with spray house steward（102）Connection.
- A kind of 7. flue gas of refuse burning processing system according to claim 6, it is characterised in that：Described circulating pump （602）Installed in afterbody osmotic cell（701）Top.
- A kind of 8. flue gas of refuse burning processing system according to claim 1, it is characterised in that：Described active carbon layer （502）Height be housing（501）The 2/3-3/4 of height.
- A kind of 9. flue gas of refuse burning processing system according to claim 1, it is characterised in that：Described spray thrower （107）For spiral spray thrower（107）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720095778.4U CN206837724U (en) | 2017-01-25 | 2017-01-25 | A kind of flue gas of refuse burning processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720095778.4U CN206837724U (en) | 2017-01-25 | 2017-01-25 | A kind of flue gas of refuse burning processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206837724U true CN206837724U (en) | 2018-01-05 |
Family
ID=60789436
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720095778.4U Expired - Fee Related CN206837724U (en) | 2017-01-25 | 2017-01-25 | A kind of flue gas of refuse burning processing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206837724U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106731354A (en) * | 2017-01-25 | 2017-05-31 | 朱肖州 | A kind of flue gas of refuse burning processing system |
-
2017
- 2017-01-25 CN CN201720095778.4U patent/CN206837724U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106731354A (en) * | 2017-01-25 | 2017-05-31 | 朱肖州 | A kind of flue gas of refuse burning processing system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190625 Address after: 530700 No. 68 Wuliqiao Street, Anyang Town, Duan Yao Autonomous County, Hechi City, Guangxi Zhuang Autonomous Region Patentee after: Duan Tongda Environmental Equipment Manufacturing Plant (General Partnership) Address before: No. 36 Yinghui Community Bridge Road, Anyang Town, Duan Yao Autonomous County, Hechi City, Guangxi Zhuang Autonomous Region, 530700 Patentee before: Zhu Xiaozhou |
|
| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180105 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |