CN204644009U - Kitchen waste water treatment system, device - Google Patents
Kitchen waste water treatment system, device Download PDFInfo
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- CN204644009U CN204644009U CN201520267683.7U CN201520267683U CN204644009U CN 204644009 U CN204644009 U CN 204644009U CN 201520267683 U CN201520267683 U CN 201520267683U CN 204644009 U CN204644009 U CN 204644009U
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- kitchen waste
- waste water
- breakdown
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- 239000010806 kitchen waste Substances 0.000 title claims abstract description 53
- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 155
- 230000015556 catabolic process Effects 0.000 claims abstract description 40
- 239000000839 emulsion Substances 0.000 claims abstract description 36
- 230000003647 oxidation Effects 0.000 claims abstract description 33
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 33
- 239000007788 liquid Substances 0.000 claims abstract description 14
- 238000000926 separation method Methods 0.000 claims abstract description 7
- 238000004945 emulsification Methods 0.000 claims abstract description 6
- 238000012545 processing Methods 0.000 claims abstract description 6
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical group [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 44
- 230000018044 dehydration Effects 0.000 claims description 5
- 238000006297 dehydration reaction Methods 0.000 claims description 5
- 239000002893 slag Substances 0.000 claims description 5
- 238000011001 backwashing Methods 0.000 claims description 3
- 238000000354 decomposition reaction Methods 0.000 claims description 3
- 230000007246 mechanism Effects 0.000 claims description 3
- 230000009467 reduction Effects 0.000 claims description 3
- 238000009833 condensation Methods 0.000 claims description 2
- 230000005494 condensation Effects 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 18
- 239000007764 o/w emulsion Substances 0.000 abstract description 9
- 230000008569 process Effects 0.000 abstract description 8
- 238000005516 engineering process Methods 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 239000003921 oil Substances 0.000 description 28
- 239000002351 wastewater Substances 0.000 description 7
- 239000002245 particle Substances 0.000 description 6
- 239000010802 sludge Substances 0.000 description 5
- 239000002699 waste material Substances 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000006385 ozonation reaction Methods 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 238000001311 chemical methods and process Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000006722 reduction reaction Methods 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000003513 alkali Substances 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000003020 moisturizing effect Effects 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- 238000006479 redox reaction Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 240000007049 Juglans regia Species 0.000 description 1
- 235000009496 Juglans regia Nutrition 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000008346 aqueous phase Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004581 coalescence Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 235000011194 food seasoning agent Nutrition 0.000 description 1
- 238000007429 general method Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000010773 plant oil Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000012163 sequencing technique Methods 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 235000020234 walnut Nutrition 0.000 description 1
- 238000003809 water extraction Methods 0.000 description 1
- 239000002569 water oil cream Substances 0.000 description 1
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model relates to environmental technology field, disclose a kind of kitchen waste water treatment system, comprise breakdown of emulsion unit, molten gas separating unit, oxidation unit, exhaust unit and control unit, kitchen waste water is after described breakdown of emulsion unit carries out breakdown of emulsion process, after described molten gas separating unit carries out solid-liquid or Liquid liquid Separation, be oxidized the organism in described kitchen waste water through described oxidation unit, by described exhaust unit, water outlet up to standard discharged.The invention also discloses kitchen waster water processing apparatus, solve oil in water emulsion and dissolving oil in kitchen waste water treating processes and remove difficult problem.
Description
Technical field
The utility model relates to environmental technology field, particularly relates to a kind of kitchen waste water treatment system, device.
Background technology
Kitchen waste water is high density pollution source, complicated component, and organic content is high, mainly contains the protein etc. of foodstuff fibre, starch, fat, animal-plant oil, all kinds of seasoning matter, washing composition.
The forms such as the oil in kitchen waste water general above oil slick, dispersed oil, oil in water emulsion, dissolving oil, oil-containing solids exist.
(1) upper oil slick, the oil content that particle diameter is greater than 30 μm, accounts for 50% ~ 60% at kitchen waste water oily(waste)water.Because particle is comparatively large, can comparatively fast float after leaving standstill, wafing with the oil film of external phase floats on the surface.
(2) dispersed oil, particle diameter, between the oil content of 1 ~ 30 μm, accounts for 35% ~ 45% at kitchen waste water oily(waste)water.Small oil droplet suspended dispersed is in aqueous phase.Dispersed oil is unstable, coalescence can become larger oil droplet and floats to the water surface, also may diminish further, change into oil in water emulsion.
(3) oil in water emulsion, the oil content that particle diameter is less than 1 μm, accounts for 3% ~ 5% at kitchen waste water oily(waste)water.Imperceptible oil droplet with water in oil fine particulate form suspended dispersed in water.
(4) dissolving oil, is scattered in water body with molecularity or chemical mode, and oil content and water form homogeneous system, and highly stable, very difficult general method is removed.0.5% ~ 1.5% is accounted at kitchen waste water oily(waste)water.
(5) oil-solids, in water body, oil droplet sticks to oil-solids that the surface of solid suspension material is formed.2% ~ 6.5% is accounted at kitchen waste water oily(waste)water.
The major technique of current oily water separation has the large class of Physical (mainly the method such as gravity, filtration) and physico-chemical processes two.To deoil method as by deoil method, walnut shell filter of oil trap, it is better that these class methods remove oil slick effect, but bad for the effect removing dissolving oil and oil in water emulsion.
In addition, the mud produced in system treating processes is also the most important thing of this project, existing water extracter is mainly centrifugal drier or plate and frame water extracter, its principle of work is respectively centrifugal principle and pressurization principle, but these two kinds of water extracter power consumptions are large, are not suitable for the dehydration of oiliness mud and take up an area large; Centrifugal drier energy consumption is high and noise large, and plate and frame water extracter is difficult to realize automatically running continuously.
Utility model content
The purpose of this utility model is to solve the problem, and provides a kind of kitchen waste water treatment system, device, realizes the removal to vegetable and animals oils in kitchen waste water.
The technical scheme that the utility model is taked is:
A kind of kitchen waste water treatment system, it is characterized in that, comprise breakdown of emulsion unit, molten gas separating unit, oxidation unit, exhaust unit and control unit, kitchen waste water is after described breakdown of emulsion unit carries out breakdown of emulsion process, after described molten gas separating unit carries out solid-liquid or Liquid liquid Separation, be oxidized the organism in described kitchen waste water through described oxidation unit, by described exhaust unit, water outlet up to standard discharged.
Further, described breakdown of emulsion unit is mixed condensation type breakdown of emulsion unit.
Further, described oxidation unit is ozone oxidation unit, described ozone oxidation unit comprises ozone generating unit and tail gas resolving cell, and described ozone generating unit provides ozone for described ozone oxidation unit, and the tail gas after reduction is carried out decompositions discharge by described tail gas resolving cell.
Further, described kitchen waste water is sent to described breakdown of emulsion unit after being collected by former water header, and described kitchen waste water is stored to intermediate water tank after described breakdown of emulsion unit and molten gas separating unit, delivers to described oxidation unit by intermediate water tank.
Further, described former water header and intermediate water tank are equipped with liquidometer, described breakdown of emulsion unit realizes start and stop according to the water level of described former water header, described oxidation unit realizes start and stop according to the water level of described intermediate water tank, arrange in stirrer, well heater, air-dissolving apparatus, slag scraper in described breakdown of emulsion unit and molten gas separating unit one or more, described oxidation unit comprises backwashing mechanism.
Further, described mud is discharged after folded spiral shell water extracter dehydration.
A kind of kitchen waster water processing apparatus, above-mentioned kitchen waste water treatment system is installed, it is characterized in that, comprise support, the former water header that pipeline pipe fitting connects is arranged through in described support, ozone filter tank, intermediate water tank and molten medicine-chest, folded spiral shell water extracter is installed in described support, described ozone filter tank arranges ozonizer and tail gas splitter, the water-in of breakdown of emulsion unit is arranged on the side lower end of described support, the discharge outlet of described tail gas splitter is arranged at the top of described support, at the side in described foul smell filter tank, ozone filter tank water outlet and ozone filter tank backwash water outlet are set.
Further, volume pump is set above described molten medicine-chest, middle water pump is set below described breakdown of emulsion unit and molten gas separating unit, in described support, also housing is installed.
The beneficial effects of the utility model are:
(1) solve oil in water emulsion and dissolving oil in kitchen waste water treating processes and remove difficult problem;
(2) utilize physico-chemical process, system integrates the function such as oils, COD, SS, stink removed in waste water;
(3) oxygenerator, ozonizer and centralized Control cabinet are designed to one, formation processing device;
(4) treatment unit makes full use of locus, and floor space is little, and device layout is compact.
Accompanying drawing explanation
Accompanying drawing 1 is working-flow figure of the present utility model;
Accompanying drawing 2 is front views of the utility model treatment unit;
Accompanying drawing 3 is side-views of the utility model treatment unit;
Accompanying drawing 4 is vertical views of the utility model treatment unit.
Label in accompanying drawing is:
1. kitchen waste water; 2. breakdown of emulsion reactor;
3. molten gas separating device; 4. mud room;
5. sludge pump; 6. water extracter;
7. intermediate water tank; 8. middle water pump;
9. ozonation aerated filter tank; 10. oxygenerator;
11. ozonizers; 12. tail gas decomposers;
21. supports; 22. pipeline pipe fittings;
24. ozone filter tanks; 25. intermediate water tanks;
26. molten medicine-chests; 27. folded spiral shell water extracters;
28. water-ins; 29. sewage draining exits;
30. discharge outlets; 31. water outlets;
32. backwash water outlets; 33. volume pumps;
34. middle water pumps; 36. housings.
Embodiment
Elaborate below in conjunction with the embodiment of accompanying drawing to the utility model kitchen waste water treatment system, device.
In five kinds of oil of kitchen waste water, intractability is large, containing certain amount and directly to affect effluent quality be oil in water emulsion.Use due to washing composition makes the oil in kitchen waste water be emulsification shape, and general oily water separating equipment is difficult to carry out oily water separation, oil in water emulsion must be carried out breakdown of emulsion process.
Kitchen waste water treatment system of the present utility model, comprise breakdown of emulsion unit, molten gas separating unit, oxidation unit, exhaust unit and control unit, kitchen waste water carries out after breakdown of emulsion process through breakdown of emulsion unit, water-gas-particle three-phase mixed system is formed through molten gas separating unit, after particle adhesion bubble, form apparent density be less than the flco of water and float to the water surface, form scum layer to be struck off, thus after realizing the process of solid-liquid or Liquid liquid Separation, through oxidation unit oxidation kitchen waste water organism, by exhaust unit, water outlet up to standard is discharged.
By scheme comparison, the reaction of employing breakdown of emulsion and molten gas are separated the oil-water separation method as kitchen waste water.Consider that, containing dissolving oil and organism in waste water, particularly containing organism, the waste water after discharge easily produces stink.The treatment unit of current employing is comprise biochemical treatment mostly, and biochemical processing method is subject to the restriction of many conditions: cannot carry out intermittent operation, and the impact of temperature and environment is comparatively large to result fluctuation ratio, and floor space is large, use, overhaul extremely inconvenient.
Oxidation unit elects ozone oxidation unit as, and ozone oxidation unit comprises ozone generating unit and tail gas resolving cell, and ozone generating unit provides ozone for ozone oxidation unit, and the tail gas after reduction is carried out decompositions discharge by tail gas resolving cell.
Chemical method redox reaction is adopted to reduce organic concentration in waste water.Fully mixing to make ozone and waste water and organism participation redox reaction as much as possible, must increase and cutting a body in ozone and water contact process, this section of body absorption property is strong and play the effect of catalyzer.Select high-efficient purification filtrate, to improve the ability of ozone oxidation for this reason.
Kitchen waste water is sent to breakdown of emulsion unit after being collected by former water header, and kitchen waste water is stored to intermediate water tank after breakdown of emulsion unit and molten gas separating unit, delivers to oxidation unit by intermediate water tank.Former water header and intermediate water tank are equipped with liquidometer, breakdown of emulsion unit realizes start and stop according to the water level of former water header, oxidation unit realizes start and stop according to the water level of intermediate water tank, arrange in stirrer, well heater, air-dissolving apparatus, slag scraper in breakdown of emulsion unit and molten gas separating unit one or more, oxidation unit comprises backwashing mechanism.
The mud oil-containing that native system produces, sludge quantity are little, and its sludge dewatering adopts folded spiral shell dehydration technique.
See accompanying drawing 1, as an implementing procedure of the present utility model, kitchen waste water 1 is sent to after breakdown of emulsion reactor 2 carries out breakdown of emulsion reaction by kitchen waste water treatment system, deliver to molten gas separating device 3, after mud is delivered to mud room 4 by molten gas separating device 3, after being dehydrated by sludge pump 5 dozens to water extracter 6, mud is transported outward.And the kitchen waste water that molten gas separating device is separated is stored in intermediate water tank 7, through middle water pump 8 injection of ozone aerating filter 9, sewage through be oxidized qualified after discharge, ozonation aerated filter tank 9 provides ozone by oxygenerator 10, ozonizer 11, ozone after reduction reaction, by tail gas decomposer 12 decompose up to standard after be vented by ventilator trunk.
The device of application kitchen waste water treatment system, comprise support 21, the ozone filter tank 24 of pipeline pipe fitting 22 connection, intermediate water tank 25 and molten medicine-chest 26 is arranged through in support 21, folded spiral shell water extracter 27 is installed in support 21, ozone filter tank 24 arranges ozonizer and tail gas splitter, the water-in 28 of breakdown of emulsion reactor 2 and system sewage draining exit 29 be arranged on the side lower end of support, the discharge outlet 30 of tail gas splitter is arranged at the top of support 21, arranges ozone filter tank water outlet 31 and ozone filter tank backwash water outlet 32 at the side in ozone filter tank 24.Volume pump 33 is set above molten medicine-chest 26, breakdown of emulsion reactor 2 and molten gas separating device 3 is set above middle water pump 34, in support, housing 36 is also installed.
This device plug and play, can run in gap, and can effectively deodorizing, conveniently moving.
Be described in detail system of the present utility model and device below, key to work step of the present utility model is as follows:
(1) integrated kitchen waster water processing apparatus whole system (except sludge dewatering system) is run by former water header Liquid level, and low-water level is out of service, and median water level brings into operation.When intermediate water tank water level attains to a high place, former water lift pump also will quit work.
(2) when former water extraction rises pump startup, first order reaction stirrer, second order reaction stirrer, electrically heated, air dissolving system, emulsion splitter volume pump, alkali volume pump, all corresponding startup of PAM volume pump.Wherein electric heater unit controls by temperature transmitter, and alkali volume pump is by PH instrument control system.Slag scraper gap is run.Scum chamber is to time high-order simultaneously, and slag scraper also quits work.
(3), when intermediate water tank water level reaches meta, water pump in the middle of starting, ozonation system and ozone filter tank system are started working simultaneously.When intermediate water tank water level reaches low level, quit work.
(4) in the operational process of ozone filter tank, filter tank water level rises gradually, and when reaching a certain position, ozone filter tank system and ozonation system quit work and enter backwash state.Middle water pump (variable frequency control) starts to enter water backwash, and also carry out gas backwash during backwash, after backwash for some time, ozone filter tank system enters normal operating condition.In water backwash process, intermediate water tank can moisturizing at any time (tap water), to meet the backwash water yield.Above-mentioned functions is automatic mode.
(5), when scum chamber water level reaches a middle high position, folded spiral shell machine system starts, PAM volume pump is also started working simultaneously.Mud volume reaches certainweight or scum chamber water level and reaches after low level or the molten medicine-chest liquid level of PAM reach low level, folded spiral shell machine system stalls.
(6) when molten medicine-chest water level reaches low level, corresponding volume pump quits work, and corresponding chemical feeding points system also will quit work simultaneously.When molten medicine-chest water level reaches low level, automatic water supplement, to specified location, is reminded and is manually offerd medicine, and after moisturizing puts in place, corresponding stirring system starts, and after stirring for some time, stirring system stops automatically, recovers medicine charging function.
(7) system blowdown is designed to operating in a key mode.According to technique needs, blowdown is provided with sequencing.
(8) native system is except artificial dispensing and the outward transport of dry mud, and other are automatic control.
According to above-mentioned step, sum up kitchen waste water process method step as follows:
(1) kitchen waste water is injected into former water header, and when control unit detects that former water header median water level height is median water level, startup breakdown of emulsion unit can cross the oil in water emulsion in physico-chemical processes removal kitchen waste water;
(2) kitchen waste water is separated by molten gas separating unit, and delivered to by isolated mud and discharge after folded spiral shell water extracter dehydration, the storage of waste water separated is to intermediate water tank;
(3), when control unit detects that intermediate water tank median water level height reaches median water level, start ozone oxidation unit, become water up to standard to discharge wastewater oxidation by middle water pump.
The above is only preferred implementation of the present utility model; it should be pointed out that for those skilled in the art, under the prerequisite not departing from the utility model principle; can also make some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.
Claims (8)
1. a kitchen waste water treatment system, it is characterized in that: comprise breakdown of emulsion unit, molten gas separating unit, oxidation unit, exhaust unit and control unit, kitchen waste water is after described breakdown of emulsion unit carries out breakdown of emulsion process, after described molten gas separating unit carries out solid-liquid or Liquid liquid Separation, be oxidized the organism in described kitchen waste water through described oxidation unit, by described exhaust unit, water outlet up to standard discharged.
2. kitchen waste water treatment system according to claim 1, is characterized in that: described breakdown of emulsion unit is mixed condensation type breakdown of emulsion unit.
3. kitchen waste water treatment system according to claim 1, it is characterized in that: described oxidation unit is ozone oxidation unit, described ozone oxidation unit comprises ozone generating unit and tail gas resolving cell, described ozone generating unit provides ozone for described ozone oxidation unit, and the tail gas after reduction is carried out decompositions discharge by described tail gas resolving cell.
4. kitchen waste water treatment system according to any one of claim 1 to 3, it is characterized in that: described kitchen waste water is sent to described breakdown of emulsion unit after being collected by former water header, described kitchen waste water is stored to intermediate water tank after described breakdown of emulsion unit and molten gas separating unit, delivers to described oxidation unit by intermediate water tank.
5. kitchen waste water treatment system according to claim 4, it is characterized in that: described former water header and intermediate water tank are equipped with liquidometer, described breakdown of emulsion unit realizes start and stop according to the water level of described former water header, described oxidation unit realizes start and stop according to the water level of described intermediate water tank, arrange in stirrer, well heater, air-dissolving apparatus, slag scraper in described breakdown of emulsion unit and molten gas separating unit one or more, described oxidation unit comprises backwashing mechanism.
6. kitchen waste water treatment system according to claim 4, is characterized in that: the mud that described kitchen waste water treatment system produces is discharged after folded spiral shell water extracter dehydration.
7. a kitchen waster water processing apparatus, kitchen waste water treatment system according to any one of claim 1 to 6 is installed, it is characterized in that: comprise support, the former water header that pipeline pipe fitting connects is arranged through in described support, ozone filter tank, intermediate water tank and molten medicine-chest, described support is installed folded spiral shell water extracter, on side, described ozone filter tank, ozonizer and tail gas splitter are set, the water-in of breakdown of emulsion unit is arranged on the side lower end of described support, the discharge outlet of described tail gas splitter is arranged at the top of described support, at the side in described ozone filter tank, ozone filter tank water outlet and ozone filter tank backwash water outlet are set.
8. kitchen waster water processing apparatus according to claim 7, is characterized in that: above described molten medicine-chest, arrange volume pump, arranges middle water pump, in described support, also install housing below described breakdown of emulsion unit and molten gas separating unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520267683.7U CN204644009U (en) | 2015-04-28 | 2015-04-28 | Kitchen waste water treatment system, device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520267683.7U CN204644009U (en) | 2015-04-28 | 2015-04-28 | Kitchen waste water treatment system, device |
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| Publication Number | Publication Date |
|---|---|
| CN204644009U true CN204644009U (en) | 2015-09-16 |
Family
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520267683.7U Active CN204644009U (en) | 2015-04-28 | 2015-04-28 | Kitchen waste water treatment system, device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204644009U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104803517A (en) * | 2015-04-28 | 2015-07-29 | 吴冠生 | Kitchen wastewater treatment system, device and method |
| CN107619101A (en) * | 2017-10-26 | 2018-01-23 | 杨晓艳 | A kind of device and technique that sewage drainage is further handled using tide |
-
2015
- 2015-04-28 CN CN201520267683.7U patent/CN204644009U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104803517A (en) * | 2015-04-28 | 2015-07-29 | 吴冠生 | Kitchen wastewater treatment system, device and method |
| CN107619101A (en) * | 2017-10-26 | 2018-01-23 | 杨晓艳 | A kind of device and technique that sewage drainage is further handled using tide |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information |
Inventor after: Wu Guansheng Inventor after: Ding Mingqi Inventor before: Wu Guansheng Inventor before: Zhang Zhengbao Inventor before: Ding Mingqi |
|
| CB03 | Change of inventor or designer information | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20231204 Address after: Room 201, No. 14, Lane 198, Jingjiang Road, Jing'an District, Shanghai, 200040 Patentee after: Wu Guansheng Patentee after: Ding Mingqi Address before: Room 201, No. 14, Lane 198, Jingjiang Road, Zhabei District, Shanghai, 200070 Patentee before: Wu Guansheng Patentee before: Zhang Zhengbao Patentee before: Ding Mingqi |
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| TR01 | Transfer of patent right |