CN205151894U - Degree of depth denitrogenation V type filtering pond - Google Patents
Degree of depth denitrogenation V type filtering pond Download PDFInfo
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- CN205151894U CN205151894U CN201520614102.2U CN201520614102U CN205151894U CN 205151894 U CN205151894 U CN 205151894U CN 201520614102 U CN201520614102 U CN 201520614102U CN 205151894 U CN205151894 U CN 205151894U
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- back flushing
- pipe
- inlet pipe
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- 238000001914 filtration Methods 0.000 title claims abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 92
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 46
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 26
- 239000000463 material Substances 0.000 claims abstract description 23
- 238000011010 flushing procedure Methods 0.000 claims description 38
- 239000000706 filtrate Substances 0.000 claims description 24
- 239000002351 wastewater Substances 0.000 claims description 20
- 238000011001 backwashing Methods 0.000 claims description 18
- 239000006004 Quartz sand Substances 0.000 claims description 9
- 229910052799 carbon Inorganic materials 0.000 claims description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 8
- 239000002245 particle Substances 0.000 claims description 8
- 239000000919 ceramic Substances 0.000 claims description 6
- 239000004927 clay Substances 0.000 claims description 6
- 239000007789 gas Substances 0.000 claims description 5
- 239000000701 coagulant Substances 0.000 claims description 4
- 230000000630 rising effect Effects 0.000 claims description 4
- 239000000178 monomer Substances 0.000 claims description 3
- 239000002657 fibrous material Substances 0.000 claims description 2
- 239000004033 plastic Substances 0.000 claims description 2
- 229920003023 plastic Polymers 0.000 claims description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 abstract description 8
- 239000011574 phosphorus Substances 0.000 abstract description 8
- 229910052698 phosphorus Inorganic materials 0.000 abstract description 8
- 238000012423 maintenance Methods 0.000 abstract description 2
- 239000007787 solid Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 26
- 239000000126 substance Substances 0.000 description 23
- 244000005700 microbiome Species 0.000 description 10
- 241000894006 Bacteria Species 0.000 description 7
- 230000001105 regulatory effect Effects 0.000 description 7
- 239000010865 sewage Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 5
- 238000010926 purge Methods 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000000717 retained effect Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 238000009287 sand filtration Methods 0.000 description 2
- 230000035939 shock Effects 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 description 1
- YUWBVKYVJWNVLE-UHFFFAOYSA-N [N].[P] Chemical compound [N].[P] YUWBVKYVJWNVLE-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 210000003850 cellular structure Anatomy 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000035800 maturation Effects 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 150000003016 phosphoric acids Chemical class 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000001632 sodium acetate Substances 0.000 description 1
- 235000017281 sodium acetate Nutrition 0.000 description 1
- 238000010408 sweeping Methods 0.000 description 1
Abstract
The utility model discloses a degree of depth denitrogenation V type filtering pond comprises V type inlet channel, anti - flushed drainage tank, filtering pond body, back flush intake pipe, back flush inlet tube and outlet pipe, and the inlet channel lies in the top in filtering pond, packs the filter material in the filtering pond, and filtering pond underfill has the supporting layer and installs the filter plate filter, and backwash air hose, backwash inlet tube, outlet pipe lie in the bottom in filtering pond, the utility model has the advantages of the hydraulic load is big, area is little, nitrogen and phosphorus removal is effectual, the suspended solid get rid of effectual, going out water quality of water, good and the operation maintenance is simple.
Description
Technical field
The utility model relates to sewage treatment area, particularly a kind of be applicable to advanced treatment of wastewater simultaneous denitrification, dephosphorization and remove the V-type biological filter of suspended substance.
Background technology
Typical sewage quality generally comprises organism, nitrogen, phosphorus and suspended substance.Along with the raising day by day of environmental protection codes and standards, by process Water circulation or before entering environment water, effectively must remove the nitrogen in water body, phosphorus and suspended substance, especially the process water Nitrogen-and Phosphorus-containing for avoiding entering environment water is too high causes body eutrophication, is strictly limited nitrogen and phosphorus content in sewage disposal emission standard.
In removal suspended substance and phosphorus, V-type filter tank has good treatment effect.V-type filter tank is a kind of sand filtration filtration process, developed by French Degremont S.A, in 1994 in french application patent (
v-type filter tank), and be used widely in feedwater and advanced treatment of wastewater, to the phosphorus in water body and suspended substance, there is good treatment effect.There is good SS filter effect in V-type filter tank, technology maturation, but cannot be directly used in the removal of total nitrogen particularly nitric nitrogen.
In denitrogenation,
dN denitrification filter pool is the heavy filter material biological filter developed by French Degremont S.A, has obtained industry at home and has generally approved, has that floor space is little, denitrifying load is high, the technical characteristic of strong shock resistance.
dN denitrification filter pool shows excellence in denitrogenation, but the concentration of water outlet phosphorus and suspended substance is higher, more want the region of strict (as TP<0.5mg/L, SS<5mg/L) in sewage drainage standard, then cannot be effectively satisfied.
Utility model content
The technical problems to be solved in the utility model overcomes the deficiencies in the prior art, in conjunction with V-type filter tank and
the technical characterstic of DN denitrification filter pool, by improving the existing design in V-type filter tank, providing a kind of simultaneous denitrification, dephosphorization and removing the lower to stream V-type biological filter of suspended substance, hydraulic load is large, floor space is little, effluent quality is good advantage that it has.
In order to solve the problems of the technologies described above, the utility model provides following technical scheme:
A kind of advanced nitrogen V-type filter tank, comprise V-type water inlet and distribute canal, multiple biological filter unit, rising pipe and back flushing inlet pipe, back flushing water inlet pipe, backwashing wastewater pipe, described water inlet distributes canal and is connected with biofilter unit top; Described biofilter unit inside is provided with the biological filter bed of material, fine filtering layer, supporting layer and filter plate from top to bottom successively, and described filter plate is evenly equipped with filter; It is characterized in that: the biological filter unit in the same area adopts positioned opposite side by side, between relative biological filter unit, form the central piping lane passage of sensible each monomer leading portion; Passage is divided into upper and lower two isolated parts, and top is divided into back flushing drainage tray, and bottom is divided into backwash gas water dispenser groove, is provided with backwashing wastewater pipe in back flushing drainage tray, is provided with back flushing inlet pipe, back flushing water inlet pipe and rising pipe in back flushing air-water distribution tray.
Further, top, described filter tank is provided with carbon source and supplies pipe for pipe and coagulating agent.
Further, described filtrate is haydite, shale, plastics or the Fiber Materials that clay is fired.
Further, described filtrate adopts heavy clay ceramic grain filter, and filtrate diameter adopts 1 ~ 5mm, and the height of filter material layer is 1.5 ~ 2.5m.
Further, fine filtering layer is the quartz sand filter media that biological filter material layer bottom is placed, and the particle diameter of upper strata biofilter material is greater than the particle diameter of lower quartz sand, but density is contrary.
Further, back flushing water inlet pipe is connected with water distributing area bottom filter tank with inlet pipe, carries out water distribution and distribution by filter; Air water distribution chamber is positioned at the below of filter plate, symmetrical distribution; Backwash gas water dispenser slot in the middle of air water distribution chamber, and is communicated with by air water dispensing orifice with air water distribution chamber; Back flushing drainage tray is positioned at above back flushing air-water distribution tray, and is communicated with by back-flushing drainage weir with biological filter.
The beneficial effects of the utility model:
1, process filtering velocity high, hydraulic load is large, and floor space is little;
2, by regulating operating parameter and backwash cycle, different water quality and quantities can be adapted to, strong shock resistance;
4, denitrification effect is good, and water outlet total nitrogen can lower than 3mg/L;
5, phosphor-removing effect is good, and water outlet total phosphorus can lower than 0.3mg/L;
6, suspended substance removal is respond well, and water outlet SS can lower than 5mg/L;
7, backwashing water consumption, energy consumption is low, has the advantages that to save water and energy.
Accompanying drawing explanation
Fig. 1 filter tank normal filtration schematic diagram
Fig. 2 filter back washing schematic diagram
11-ceramic aggregate biological filtrate; 12-quartz sand filter media; 13-gravel supporting layer; 14-filter; 20-V type is intake and is swept wash water canal; 21-carbon source; 22-coagulating agent; 23-goes out water regulating valve; 30-back flushing water inlet pipe; 31-back flushing inlet pipe; 32-air cushion layer; 33-backwashing wastewater pipe.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described in detail, should be appreciated that content described herein is only for instruction and explanation of the utility model, and be not used in restriction the utility model.
The utility model is a kind of Downward-flow biofilter, is applied to sewage disposal.More specifically, the utility model a kind ofly relies on the lower to streaming system of gravity filtration, and use a kind of heavy filter material, filter bed is all immersed in water, reaches the function of effective denitrogenation, dephosphorization and removal suspended substance simultaneously.This biological filtering tank process can be regarded as advanced treatment, after being used in sewage second-level process.
Fig. 1, embodiment illustrated in fig. 2 in, a monomer V-type biological filter forms by with lower member: a Rectangular Water Trough, V-type water inlet and sweep wash water canal and be positioned at tank two side roof part, and former water accesses thus.Backwashing wastewater slot is in the middle of filter tank, and be provided with backwashing wastewater pipe 33, backwashing wastewater is discharged thus.Have that the microorganism of function of biological purification is attached in a large number to be combined on filtrate 11 and 12.Supporting layer is overall filter plate 13 times, and the filter 14 be mounted thereon can ensure that biological filter water and air distributing is even, and filter plate and upper filter thereof have good sealing property, are backwash gas water dispenser room under filter plate.Be back flushing air-water distribution tray under backwashing wastewater groove, go out water regulating valve 23 after back flushing water inlet pipe 30, back flushing inlet pipe 31 and filter and access thus.Process water is discharged by going out water regulating valve 23, and backwashing wastewater is discharged after drainage weir to backwashing wastewater pipe 33.
The waste water that bacteria filter system reception etc. are to be treated, being intake by V-type and sweeping wash water canal 20 is entered, and has processed rear water outlet and has passed through water regulating valve 23 and discharge.Use a kind of ceramic aggregate biological filtrate 11 of high-specific surface area in this system, contribute to attachment and the growth of microorganism.High-specific surface area filtrate, as
the BIOLITETM clay filtering material that DN denitrification filter pool uses, can be used.The distinctive cellular structure of BIOLITETM clay filtering material contributes to the attachment of microorganism, and filtrate diameter range is 1mm ~ 5mm, the height of filter material layer is 1.5 ~ 2.5m.
The ceramic aggregate biological filtrate 11 of high-specific surface area can be lived away from home a large amount of microorganism, (adds carbon source 21), remove the nitric nitrogen (NO3-N and NO2-N) in water inlet, and retain into the suspended substance in water under suitable environment; Simultaneously under the help of coagulating agent 22, assist to remove the phosphoric acid salt (PO4-P) in water inlet and suspended substance.
Except ceramic aggregate biological filter material layer 11, this bacteria filter system also can place quartz sand filter media 12 in filter material layer 11 bottom simultaneously, plays further secondary filter; Quartz sand filter media bottom is gravel supporting layer 13, is used for supporting filter material layer 12 and 11, and prevents filtrate 12 or 11 from blocking filter 14.Gravel supporting layer 13 can be made up of the gravel of different gradation.More specifically, the size of this graded gravel is between 8mm ~ 40mm.
The particle diameter of upper strata biofilter material 11 is greater than the particle diameter of lower quartz sand 12, but density is contrary, is conducive to like this playing respective advantage, and top filtrate 11 particle diameter is comparatively large, based on biological denitrificaion, and retains oarse-grained suspended substance.Bottom filtrate 12 particle diameter is less, mainly rises and retains fine suspension further, obtains better effluent quality.Upper strata biofilter material and lower floor's quartz sand filter media Size Matching, all can reach certain rate of expansion and partial fluidised state when back flushing, and back flushing terminates rear recovery layering clearly 11 and 12.
Water inlet (for Sewage Plant secondary clarifier effluent) enters from the top of bacteria filter system, after flowing through filter material layer 11,12 and gravel bed 13, then through filter 14, finally goes out water regulating valve 23 from bottom treatment and discharges.
Water level in filtration procedure in filter tank, by water outlet governor valve control, adopts RegulazurIII master mode, can make filtration water level substantially constant, so both can ensure stable effluent quality, the consumption of can substantially not intake again drop thus minimizing carbon source.
In order to allow microorganism better be attached on filtrate 11 effectively to remove the nitric nitrogen in water inlet, need additional carbon 21 in most cases.Different types of carbon source all can be used, as methyl alcohol, ethanol, acetic acid or sodium acetate.In operational process, microbes utilizes the nitric nitrogen in intaking as electron acceptor(EA), consumes additional carbon simultaneously.Owing to maintaining specific denitrification environment in bacteria filter system, on filtrate 11, the microbes of attachment consumes into the nitric nitrogen in water, thus the DO of process water outlet is generally lower than 0.5mg/L.Additional carbon 21 can as electron donor, and facilitate the removal of nitric nitrogen, final nitric nitrogen can be discharged with the form of N2.
In bacteria filter system operational process, first the suspended substance in water inlet can be retained by filtrate absorption.As time goes on, suspended substance can be accumulated in system, causes head loss, and filter bed penetrates even, causes process water outlet concentration of suspension to worsen, thus must remove the suspended substance retained in time.Correspondingly, bacteria filter system contains the removal of back flushing water inlet in order to assist suspended substance.
Backwashing water upwards by filter bed by back flushing water inlet pipe 30, can be caused filter bed expansion to a certain degree and present fluidized state, and this expansion and fluidized state can allow the suspended substance wash-out that is trapped going out.The waste water that back flushing produces will be discharged by backwashing wastewater pipe 33.
But the suspended substance that independent water backwash is difficult to be retained by filtrate is fully rinsed well, in conjunction with air purge, must be introduced by back flushing inlet pipe 31.First back flushing air inlet can form air cushion layer 32 under filter plate, is more upwards flowed into by filter uniformly distributing, and the backwash air of larger flow velocity can increase the turbulivity in filter bed, discharges the suspended substance be trapped, and is peeled off by the microorganism that filtrate adheres to.By regular back flushing, the suspended substance can removed excessive microorganism He be trapped, ensures that the normal table of system runs.
V-type biological filter still keeps V-type groove to intake when backwash, the surface intake by former water is like this assisted to sweep to wash and backwash in filtrate can be accelerated to be drained by backwashing wastewater pipe 33 rapidly to the microbial film of the water surface and suspended substance, substantially reduces the backwash time and has saved the water yield.The wedge shape buffering effluent weir at backwashing wastewater canal top, effectively can avoid filterins media run-off.
For the backwash procedure of biological filter, following requirement must be met: after (1) backwash, filter bed entirety must eliminate the suspended substance and excessive microorganism that retain; (2) microorganism that simultaneously must keep enough runs for subsequent technique: can not cause filtrate loss (as run material) in (3) backwash process; (4) water consumption and energy consumption must minimize; (5) backwash procedure must be automatic start-up and operation.
Correspondingly, standard backwash procedure has been developed for meeting the demand, can be optimized according to operating experience and revise simultaneously in actual moving process.Backwash procedure can start automatically according to working time or the head loss preset.
The key step of backwash procedure is as follows: (1) reduces liquid level to reduce discharge of wastewater; (2) air purge prepares (form air cushion layer 32 and loosen filter bed); (3) air purge; (4) air water combines flushing; (5) be vented; (6) wash; (7) rinsed.For back flushing water generally from process water outlet clean water basin.Simultaneously for ensureing the continuous operation to streaming system under this, must periodic operation driving nitrogen program, also namely removing in denitrification process by backwashing water the nitrogen bubble be accumulated in filter bed, this contributes to the smooth running extending filtration cycle and guarantee system.Driving nitrogen program is by stopping water inlet in filtration procedure, but continues to filter (go out water regulating valve 23 and be still in opened condition), and water level decreasing to close to after filter material surface, utilizes back flushing to intake removal nitrogen, and such used time is very short also discharges without waste water.
Described automatic backflushing washing procedure and drive nitrogen program and ensure that the simple and reliable of bacteria filter system operation and maintenance.
This biological filtering tank process can provide following advantage: the circular heavy filter material of (1) individual layer, for attached growth of microorganisms and retain suspended substance; (2) high-specific surface area filtrate, to guarantee attached microbial abundant amount, is different from other type filtrate (as sand filtration) of same volume, thus ensure that higher pollutants removal rate; (3) air purge of upward flow is adopted during backwash; (4) according to the automatic backflushing washing procedure of embody rule demand optimization.
Last it is noted that the foregoing is only explanation of the present utility model, be not limited to the utility model, although be described in detail the utility model, for a person skilled in the art, it still can be modified to aforementioned described technical scheme, or carries out equivalent replacement to wherein portion of techniques feature.All within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (6)
1. an advanced nitrogen V-type filter tank, comprise V-type water inlet and distribute canal, multiple biological filter unit, rising pipe and back flushing inlet pipe, back flushing water inlet pipe, backwashing wastewater pipe, described water inlet distributes canal and is connected with biofilter unit top; Described biofilter unit inside is provided with the biological filter bed of material, fine filtering layer, supporting layer and filter plate from top to bottom successively, and described filter plate is evenly equipped with filter; It is characterized in that: the biological filter unit in the same area adopts positioned opposite side by side, between relative biological filter unit, form the central piping lane passage of sensible each monomer leading portion; Passage is divided into upper and lower two isolated parts, and top is divided into back flushing drainage tray, and bottom is divided into backwash gas water dispenser groove, is provided with backwashing wastewater pipe in back flushing drainage tray, is provided with back flushing inlet pipe, back flushing water inlet pipe and rising pipe in back flushing air-water distribution tray.
2. advanced nitrogen V-type filter tank according to claim 1, is characterized in that: top, described filter tank is provided with carbon source and supplies pipe for pipe and coagulating agent.
3. advanced nitrogen V-type filter tank according to claim 1, is characterized in that: described filtrate is haydite, shale, plastics or the Fiber Materials that clay is fired.
4. advanced nitrogen V-type filter tank according to claim 3, is characterized in that: described filtrate adopts heavy clay ceramic grain filter, and filtrate diameter adopts 1 ~ 5mm, and the height of filter material layer is 1.5 ~ 2.5m.
5. advanced nitrogen V-type filter tank according to claim 1, is characterized in that: fine filtering layer is the quartz sand filter media that biological filter material layer bottom is placed, and the particle diameter of upper strata biofilter material is greater than the particle diameter of lower quartz sand, but density is contrary.
6. advanced nitrogen V-type filter tank according to claim 1, is characterized in that: back flushing water inlet pipe is connected with water distributing area bottom filter tank with inlet pipe, carries out water distribution and distribution by filter; Air water distribution chamber is positioned at the below of filter plate, symmetrical distribution; Backwash gas water dispenser slot in the middle of air water distribution chamber, and is communicated with by air water dispensing orifice with air water distribution chamber; Back flushing drainage tray is positioned at above back flushing air-water distribution tray, and is communicated with by back-flushing drainage weir with biological filter.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520614102.2U CN205151894U (en) | 2015-08-14 | 2015-08-14 | Degree of depth denitrogenation V type filtering pond |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520614102.2U CN205151894U (en) | 2015-08-14 | 2015-08-14 | Degree of depth denitrogenation V type filtering pond |
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| CN205151894U true CN205151894U (en) | 2016-04-13 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105060476A (en) * | 2015-08-14 | 2015-11-18 | 得利满水处理系统(北京)有限公司 | V-shaped filter tank for deep denitrogenation |
| CN106673105A (en) * | 2016-12-16 | 2017-05-17 | 华南农业大学 | Nitrogen and phosphorus removal composite filler based on shale and agricultural waste, and preparation method and application thereof |
| CN111115990A (en) * | 2020-03-13 | 2020-05-08 | 广东正诚环境科技有限公司 | Denitrification filter tank system |
-
2015
- 2015-08-14 CN CN201520614102.2U patent/CN205151894U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105060476A (en) * | 2015-08-14 | 2015-11-18 | 得利满水处理系统(北京)有限公司 | V-shaped filter tank for deep denitrogenation |
| CN106673105A (en) * | 2016-12-16 | 2017-05-17 | 华南农业大学 | Nitrogen and phosphorus removal composite filler based on shale and agricultural waste, and preparation method and application thereof |
| CN106673105B (en) * | 2016-12-16 | 2019-06-28 | 华南农业大学 | A kind of denitrogenation dephosphorizing synthetic filling and the preparation method and application thereof based on mud shale and agricultural wastes |
| CN111115990A (en) * | 2020-03-13 | 2020-05-08 | 广东正诚环境科技有限公司 | Denitrification filter tank system |
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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. Country or region after: China 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. Country or region before: China Address after: 100026 31 / F, Taikang financial building, building 1, courtyard 38, East Third Ring Road North, Chaoyang District, Beijing Patentee after: Suez Water Treatment Co,.Ltd. Country or region after: China Address before: Room 430, Huatong Building, No. 19, Chegongzhuang West Road, Haidian District, Beijing Patentee before: DEGREMONT WATER TREATMENT SYSTEM (BEIJING) CO.,LTD. Country or region before: China |