CN205152030U - Mud decrement combination processing system - Google Patents
Mud decrement combination processing system Download PDFInfo
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- CN205152030U CN205152030U CN201520827909.4U CN201520827909U CN205152030U CN 205152030 U CN205152030 U CN 205152030U CN 201520827909 U CN201520827909 U CN 201520827909U CN 205152030 U CN205152030 U CN 205152030U
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- 238000012545 processing Methods 0.000 title claims abstract description 10
- 238000001914 filtration Methods 0.000 claims abstract description 34
- 230000018044 dehydration Effects 0.000 claims abstract description 28
- 238000006297 dehydration reaction Methods 0.000 claims abstract description 28
- 238000001816 cooling Methods 0.000 claims abstract description 27
- 238000003860 storage Methods 0.000 claims abstract description 16
- 238000003825 pressing Methods 0.000 claims abstract description 15
- 239000000463 material Substances 0.000 claims abstract description 3
- 238000001035 drying Methods 0.000 claims description 36
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 30
- 238000002156 mixing Methods 0.000 claims description 29
- 239000003570 air Substances 0.000 claims description 23
- 239000003814 drug Substances 0.000 claims description 16
- 239000007787 solid Substances 0.000 claims description 13
- 238000007599 discharging Methods 0.000 claims description 11
- 239000000701 coagulant Substances 0.000 claims description 9
- 238000011084 recovery Methods 0.000 claims description 9
- 239000002131 composite material Substances 0.000 claims description 8
- 239000004744 fabric Substances 0.000 claims description 7
- 239000010801 sewage sludge Substances 0.000 claims description 7
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 claims description 6
- 229920000620 organic polymer Polymers 0.000 claims description 6
- 239000002351 wastewater Substances 0.000 claims description 6
- 238000011144 upstream manufacturing Methods 0.000 claims description 4
- 230000015572 biosynthetic process Effects 0.000 claims description 3
- 238000004332 deodorization Methods 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- 238000012546 transfer Methods 0.000 claims description 3
- 239000012080 ambient air Substances 0.000 claims description 2
- 238000009833 condensation Methods 0.000 claims description 2
- 230000005494 condensation Effects 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 14
- 230000008878 coupling Effects 0.000 abstract 2
- 238000010168 coupling process Methods 0.000 abstract 2
- 238000005859 coupling reaction Methods 0.000 abstract 2
- 239000010802 sludge Substances 0.000 description 14
- 239000012065 filter cake Substances 0.000 description 12
- 238000005516 engineering process Methods 0.000 description 8
- 230000008569 process Effects 0.000 description 6
- 230000009471 action Effects 0.000 description 5
- 102100028902 Hermansky-Pudlak syndrome 1 protein Human genes 0.000 description 4
- 101000838926 Homo sapiens Hermansky-Pudlak syndrome 1 protein Proteins 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000005189 flocculation Methods 0.000 description 4
- 230000016615 flocculation Effects 0.000 description 4
- 239000008187 granular material Substances 0.000 description 4
- 230000008092 positive effect Effects 0.000 description 4
- 238000012549 training Methods 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 230000009467 reduction Effects 0.000 description 3
- 238000005336 cracking Methods 0.000 description 2
- 230000001877 deodorizing effect Effects 0.000 description 2
- 239000002274 desiccant Substances 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000003311 flocculating effect Effects 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 238000013467 fragmentation Methods 0.000 description 1
- 238000006062 fragmentation reaction Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
Abstract
The utility model discloses a mud decrement combination processing system, including mud storage pool, dehydration filter pressing device, middle hopper dredger, mud make -up machine and the belt mummification machine of storing up, dehydration filter pressing device includes a piston cylinder and a rotatory reciprocating motion's piston, sets up a set of flexibility in the piston cylinder and filters the carrier, filters carrier connection piston and pull by the piston, filters carrier inside and has the guiding gutter, belt mummification machines have dry section and cooling space, and the dry section passes through dry fan of tube coupling and air heater, inserts the dry section again and forms the dry air return circuit, and a tube coupling cooling blower and a material cooler are passed through to the cooling space, insert the cooling space again and form the cooling air return circuit, joint operation through piston and filtration carrier makes mud fully filtered on the whole, and the moisture content of mud is dropped to below 70%, chooses eco -power low temperature belt mummification technique for use to reduce the heat rate cost of mummification by a wide margin.
Description
Technical field
The utility model relates to the Reduction Technology field of mud, specifically a kind of novel sludge high-drying dewatering system.
Background technology
Sludge reduction is the primary goal of specific resistance to filtration, and existing sludge reduction technology mainly comprises mechanical dehydration, mummification, burns, cracking etc.General treatment scheme is, first relies on the decrement that mechanical dehydration is preliminary, then by the sufficient decrement of mummification, finally as required with burning or cracking decrement thoroughly.In whole treatment scheme, mummification is very important middle-chain, is also the link that generation is concentrated in heat energy consumption.Traditional mechanical dehydration technology mainly comprises belt press filtration, centrifugation and filter press, if adopt press filtration mode to dewater, the subject matter existed is the filter cake formed on filtering interface is fixing in filtration procedure, therefore filter cake inside presents the structure of layering, Partial filtration the closer to filtering interface is more abundant, water ratio is lower, Partial filtration more away from filtering interface is more limited, water ratio is higher, generally speaking, filter insufficient, water ratio is higher, reduced training is more limited, as shown in Figure 1.
Be limited by traditional mechanical dehydration technology mud extraction water ratio higher (about 80%), decrement effect more limited, the consumption of heat energy of mummification is generally excessive: by the sludge drying of water ratio 80% to water ratio 10%, mummification 1 ton of dry solids needs evaporated water to be 3.889 tons, and the hear rate of often evaporating the conventional desiccation machine needs of 1 ton of water is generally 900kWh ~ 1100kWh, the hear rate therefore corresponding to mummification 1 ton of dry solids will reach 3500 ~ 4000kWh; Simultaneously because moisture percentage in sewage sludge is higher, cause molding effect poor, the low temperature belt-type drying technology of economical thermal source can be utilized to be difficult to be suitable for, the anhydration system that thermal source unit cost is higher can only be selected, cause the working cost of mummification too high like this, be difficult to promote on a large scale, thus mud can not get fully or decrement thoroughly, the target of specific resistance to filtration is difficult to realize.
Now research and develop a kind of novel high level cadre dehydration and low temperature belt-type drying mud decrement combined system and technique, object is strengthened the reduced training of mechanical dehydration by its novel high level cadre's dehydration technique, reduced the water ratio of mud further, hear rate needed for mummification is reduced, be conducive to selecting Eco-power low temperature belt-type drying technology simultaneously, thus significantly reduce the hear rate cost of mummification, make the working cost of mummification drop to the level of economical rationality, mud is realized fully or decrement thoroughly.
Utility model content
The purpose of this utility model overcomes the limited defect causing mummification running cost too high of traditional sludge mechanical dehydration technology reduced training, a kind of novel high level cadre is provided to dewater and low temperature dewatered sludge decrement combinatorial process system and method, the heat energy consumption of the reduced training of mechanical dehydration, the water ratio reducing mud further, minimizing mummification is strengthened by its novel high level cadre's dehydration technique, again by selecting Eco-power low temperature drying technique, reduce the unit cost of thermal source, thus make the working cost of sludge drying be reduced to economical rationality level.
To achieve these goals, the technical solution of the utility model is:
A kind of mud decrement composite processing system, is characterized in that, comprises sewage sludge storage pond, dehydration filter-pressing device, middle storage hopper dredger, mud forming machine and belt-type drying machine; Sewage sludge storage pond is passed through to connect dehydration filter-pressing device into mud pipe, entering on mud pipe to be furnished with the first mixing tank and the second mixing tank, second mixing tank is positioned at the first mixing tank downstream, and the first medicine storing pot is connected to the first mixing tank, and the second medicine storing pot is connected to the second mixing tank; Dehydration filter-pressing device comprises the piston of a piston cylinder and a rotary reciprocating motion, arranges one group of flexible filter carrier in piston cylinder, and filtration supports connects piston and draws by piston, and filtration supports inside has diversion trench; The outlet of dehydration filter-pressing device connects middle storage hopper dredger, after filter-press dehydration, mud enters middle storage hopper dredger, belt-type drying machine is assigned to after mud forming machine, belt-type drying facility have drying zone and cooling zone, drying zone connects drying air fan and airheater by pipeline, access drying zone again and form dry air loop, cooling zone connects cooling blower and a material water cooler by pipeline, then accesses formation cooling air loop, cooling zone; Isolated by rotary valve between drying zone and cooling zone, inside, drying zone is provided with arid zones, and inside, cooling zone is provided with cooling zone.
Further, the first medicine storing pot is connected to the first mixing tank by the first volume pump, and the second medicine storing pot is connected to the second mixing tank by the second volume pump, is also furnished with into dredge pump in the first mixing tank upstream entering mud pipe; Deposit molysite coagulant aids in first medicine storing pot, deposit organic polymer coargulator in the second medicine storing pot, mud mixes in the first mixing tank with molysite coagulant aids, and mud mixes in the second mixing tank with organic polymer coargulator; First mixing tank is line mixer, and the second mixing tank adopts motorized agitator to carry out Forced Mixing.
Further, enter on mud pipe and be provided with solids concn meter and under meter, the first volume pump and the second volume pump adjust added amount of chemical by solids concn meter and flow meter signal; Enter the transfer movement of dredge pump by dehydration filter-pressing device synchronization control.
Further, filtration supports is made up of one group of coated filter cloth of flexible filter core; The piston cylinder of dehydration filter-pressing device can be opened and rotate, and carries out discharging by the piston cylinder opened, rotate.
Further, belt-type drying machine also connects exhaust fan by pipeline, exhaust fan outlet connects gas-gas heat recovery exchanger, and the entrance of heat recovery exchanger introduces ambient air, accesses the upstream of drying air fan after heat recovery exchanger carries out preheating by heat exchange; Outer air-discharging access subcooler after heat recovery exchanger, then enter deodorization unit, the condensation waste water produced in subcooler enters wastewater collection pond.
By the teamwork of piston and filtration supports, filtration supports repeats the process that filter cake is formed, filter cake disintegrates, formed, disintegrates, and mud is fully filtered on the whole, and the water ratio of mud is down to less than 70%.By the sludge drying of water ratio 70% to water ratio 10%, mummification 1 ton of dry solids needs evaporated water to be 2.222 tons, and often evaporate 1 ton of hear rate stated low temperature desiccation machine and need waterborne and be generally 900kWh, therefore corresponding to the hear rate of mummification 1 ton of dry solids is 2000kWh; Illustrate that this case can energy efficient more than 40%, and economic low-grade heat source can be adopted, realize running cost and significantly reduce.
Accompanying drawing explanation
The structural representation of Fig. 1 filter cake interior laminate layer
Fig. 2 System's composition
Embodiment
Be further described below in conjunction with accompanying drawing 2 pairs of the utility model, 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.
Composite processing system formation as described below, in the T1 of sewage sludge storage pond, the mud of water ratio about 95% ~ 97% enters dredge pump P1 to reciprocating piston pressure filter HPS1 charging by positive displacement.Molysite coagulant aids is from medicine storing pot T2 by adding volume pump P2 to entering mud pipe filling coagulant aids, and mud mixes in line mixer M1 with coagulant aids.Organic polymer coargulator is from medicine storing pot T3 by adding volume pump P3 to entering mud pipe filling flocculation agent, and chemical feeding points is positioned at M1 downstream, mud and flocculation agent Forced Mixing in motorized agitator M2.P2 and P3 is by the solids concn meter on sludge pipe and flow meter signal adjustment medicament optimum dosage, and polyreaction is carried out with top condition, and the mud that flocculation reaction occurs enters in water extracter.The operation of P1 controls by HPS1.
HPS1 comprise one can open, the piston of rotating piston cylinder and one rotary reciprocating motion all the time, the filtration supports that one group of coated filter cloth of flexible filter core is formed is set in cylinder, draws by piston.During piston positive action, mud in cylinder is exerted pressure, draws filtration supports simultaneously and reverse and bend, " rubbing " effect is produced to mud, the moisture leached in mud is discharged outside cylinder through the diversion trench of filter cloth carrier inside after filtration, and solid is trapped within filter cloth surface and forms filter cake; During piston reverses direction action, mud decompress(ion) in cylinder, filtration supports stretches by natural resiliency and piston traction, simultaneously under negative pressure state, the diversion trench of air carrier inside after filtration sucks, acting in conjunction makes it disintegrate in the filter cake of filter cloth surface, treat piston again positive action form filter cake at filter cloth surface.Filtration stage comprises the reciprocation action of several times piston, and ensure fully being filtered of the mud globality in cylinder, water ratio drops to less than 70%.The operation of charging and press filtration all completes, without foul smell diffusion problem in the filtering jar closed.The negative pressure that the foul smell produced during discharging is formed in storage hopper dredger B1 by deodorizing blower fan F4 is discharged in a organized way after pipeline is sent to deodoration system purification.
First sludge high-drying dewatering process in the utility model adds a small amount of molysite coagulant aids and organic polymer coargulator successively in the mud of water ratio about 95% ~ 97%, the dosage of flocculation agent and coagulant aids adjusts according to sewage sludge solid flux to obtain best flocculating effect, mud and medicament fully mix rear polymerization reaction take place, in reciprocating piston filter pressing dehydrator, then realize the solid-liquid separation of mud.
Water extracter HPS1 operation by batch-mode operation, about 2 ~ 3 hours work period, comprise charging 0.5 ~ 1 hour, press filtration 1 ~ 1.5 hour, discharging 5 ~ 10 minutes.Charging is interval, comprises the reciprocation action of piston several times, only when piston reverses direction action, starts charging; When piston positive action, charging stops, and carries out pre-press filtration to mud.The press filtration stage comprises the reciprocation action of piston several times, repeats following process: filter cake → decompress(ion) of exerting pressure → formed → filter cake disintegrates.During discharging, cylinder body is opened, piston positive action, impels mud cake to be discharged into storage hopper dredger B1 by deadweight and keeps in.What rely on filtration supports rubs effect, and the mud after dehydration presents loose kenel, without the need to fragmentation.
By the teamwork of piston and filtration supports, filtration supports repeats the process that filter cake is formed, filter cake disintegrates, formed, disintegrates, and mud is fully filtered on the whole, and the water ratio of mud is down to less than 70%.Water extracter ensures except discharging, and charging and press filtration are all carried out in enclosed space, without foul smell diffusion problem.The foul smell produced during discharging is discharged in a organized way in the negative pressure formed in storage hopper dredger by deodorizing blower fan after pipeline is sent to deodoration system purification.
Mud after filter-press dehydration presents loose kenel, automatically be discharged into storage hopper dredger by deadweight to keep in, mud forming machine CP1 is delivered to by shaftless screw P4 from bin bottom, be assigned to the arid zones of belt-type drying machine LBT1 on after cutting into the strip of length 3 ~ 5cm or particulate state wherein, mud granule is with in arid zones traveling process, contact with the hot air flow perpendicular to arid zones, dry out gradually and obtain drying.Because the time of mud granule and air flow contacts is adjustable, the water ratio of dewatered sludge can adjust between 10% ~ 30%.Mud granule after mummification transfers to cooling zone subsequently, is isolated between the drying zone at arid zones place and the cooling zone at cooling zone place by rotary valve, guarantees that drying zone forms stable negative pressure.Dewatered sludge contacts with flow of cooled air and lowers the temperature on cooling zone, and the temperature of final desiccation machine exit dewatered sludge is down to 40 DEG C ~ 50 DEG C.Mud granule after mummification is sent into feed bin and is deposited.
Desiccant air is recycled by special fan F1, a part of wet air is discharged by exhaust fan F2 in desiccation machine outlet, extract equivalent fresh air as a supplement from environment simultaneously, the wet air of discharge and fresh air heat-shift in heat recovery exchanger HX1 of suction, fresh air is preheated, and this heat recuperation link can make anhydration system hear rate saving roughly 10%.Fresh air after preheating enters desiccant air loop, and air was heated up by airheater HX3 before being admitted to desiccation machine, and heating medium is hot water or the thermal oil of 90 ~ 95 DEG C.Outer air-discharging continues cooling by subcooler HX2, discharges in a organized way, become waste water and enter wastewater collection pond after the water vapor that outer air-discharging is taken out of condenses in HX2 after then entering deodorization unit OCU1 purification.The air of cooling is recycled by special fan F3, and air is lowered the temperature by pellet cooler HX4.HX2 and HX4 all adopts water coolant as heat-eliminating medium.
By the sludge drying of water ratio 70% to water ratio 10%, mummification 1 ton of dry solids needs evaporated water to be 2.222 tons, and often evaporate 1 ton of hear rate stated low temperature desiccation machine and need waterborne and be generally 900kWh, therefore corresponding to the hear rate of mummification 1 ton of dry solids is 2000kWh; Illustrate that this case can energy efficient more than 40%, and economic low-grade heat source can be adopted, realize running cost and significantly reduce.
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 (5)
1. a mud decrement composite processing system, is characterized in that, comprises sewage sludge storage pond, dehydration filter-pressing device, middle storage hopper dredger, mud forming machine and belt-type drying machine; Sewage sludge storage pond is passed through to connect dehydration filter-pressing device into mud pipe, entering on mud pipe to be furnished with the first mixing tank and the second mixing tank, second mixing tank is positioned at the first mixing tank downstream, and the first medicine storing pot is connected to the first mixing tank, and the second medicine storing pot is connected to the second mixing tank; Dehydration filter-pressing device comprises the piston of a piston cylinder and a rotary reciprocating motion, arranges one group of flexible filter carrier in piston cylinder, and filtration supports connects piston and draws by piston, and filtration supports inside has diversion trench; The outlet of dehydration filter-pressing device connects middle storage hopper dredger, after filter-press dehydration, mud enters middle storage hopper dredger, belt-type drying machine is assigned to after mud forming machine, belt-type drying facility have drying zone and cooling zone, drying zone connects drying air fan and airheater by pipeline, access drying zone again and form dry air loop, cooling zone connects cooling blower and a material water cooler by pipeline, then accesses formation cooling air loop, cooling zone; Isolated by rotary valve between drying zone and cooling zone, inside, drying zone is provided with arid zones, and inside, cooling zone is provided with cooling zone.
2. mud decrement composite processing system according to claim 1, it is characterized in that, first medicine storing pot is connected to the first mixing tank by the first volume pump, and the second medicine storing pot is connected to the second mixing tank by the second volume pump, is also furnished with into dredge pump in the first mixing tank upstream entering mud pipe; Deposit molysite coagulant aids in first medicine storing pot, deposit organic polymer coargulator in the second medicine storing pot, mud mixes in the first mixing tank with molysite coagulant aids, and mud mixes in the second mixing tank with organic polymer coargulator; First mixing tank is line mixer, and the second mixing tank adopts motorized agitator to carry out Forced Mixing.
3. mud decrement composite processing system according to claim 2, is characterized in that, enters on mud pipe and is provided with solids concn meter and under meter, and the first volume pump and the second volume pump adjust added amount of chemical by solids concn meter and flow meter signal; Enter the transfer movement of dredge pump by dehydration filter-pressing device synchronization control.
4. mud decrement composite processing system according to claim 1, is characterized in that, filtration supports is made up of one group of coated filter cloth of flexible filter core; The piston cylinder of dehydration filter-pressing device can be opened and rotate, and carries out discharging by the piston cylinder opened, rotate.
5. mud decrement composite processing system according to claim 1, it is characterized in that, belt-type drying machine also connects exhaust fan by pipeline, exhaust fan outlet connects gas-gas heat recovery exchanger, the entrance of heat recovery exchanger introduces ambient air, accesses the upstream of drying air fan after heat recovery exchanger carries out preheating by heat exchange; Outer air-discharging access subcooler after heat recovery exchanger, then enter deodorization unit, the condensation waste water produced in subcooler enters wastewater collection pond.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520827909.4U CN205152030U (en) | 2015-10-22 | 2015-10-22 | Mud decrement combination processing system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520827909.4U CN205152030U (en) | 2015-10-22 | 2015-10-22 | Mud decrement combination processing system |
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| CN205152030U true CN205152030U (en) | 2016-04-13 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105174683A (en) * | 2015-10-22 | 2015-12-23 | 得利满水处理系统(北京)有限公司 | Sludge reduction combined treatment system and method |
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- 2015-10-22 CN CN201520827909.4U patent/CN205152030U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105174683A (en) * | 2015-10-22 | 2015-12-23 | 得利满水处理系统(北京)有限公司 | Sludge reduction combined treatment system and method |
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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 |
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