CN107986571A - A kind of processing method of the electroplating wastewater containing antimony - Google Patents
A kind of processing method of the electroplating wastewater containing antimony Download PDFInfo
- Publication number
- CN107986571A CN107986571A CN201711362983.3A CN201711362983A CN107986571A CN 107986571 A CN107986571 A CN 107986571A CN 201711362983 A CN201711362983 A CN 201711362983A CN 107986571 A CN107986571 A CN 107986571A
- Authority
- CN
- China
- Prior art keywords
- chitosan
- water
- brush
- outlet
- antimony
- Prior art date
- 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.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/286—Treatment of water, waste water, or sewage by sorption using natural organic sorbents or derivatives thereof
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/16—Nature of the water, waste water, sewage or sludge to be treated from metallurgical processes, i.e. from the production, refining or treatment of metals, e.g. galvanic wastes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
- C02F2201/007—Modular design
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Sorption (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention discloses a kind of processing method of electroplating wastewater containing antimony, and waste water is successively by sump, coarse rack, primary sedimentation basin, pH value regulating reservoir, chitosan biological catalytic adsorption cleaning system, aeration tank, biological phosphate-eliminating pond, secondary sedimentation tank, water purifying tank processing.The rolling absorption brush that make use of of the invention is attached with chitosan and sargassum thunbergii is selective exposure reaction medium, when the antimony ion in waste water comes into full contact with rolling absorption brush, hydroxyl, carboxyl, amide groups on chitosan and sargassum thunbergii strand can selectivity complex reaction occurs with antimony ion, make the antimony in waste water by sargassum thunbergii efficient absorption, the sargassum thunbergii residue after adsorption reaction is brushed by fixed brush and is allowed to natural subsidence, sludge material is gradually formed, so that the antimony ion in waste water is removed.Meanwhile material used in the system --- chitosan is material of low cost, being readily available with sargassum thunbergii.
Description
Technical field
The present invention relates to a kind of processing method of electroplating wastewater containing antimony, belong to the field of waste water treatment in environmental protection.
Background technology
In recent years, antimony has a wide range of applications in non-ferrous metal industry, and the stibium-containing wastewater of factory's discharge is water body antimony pollution
Primary pollution source.For example the waste water antimony of the industry such as smelting, printing, ceramics, lead-acid battery, fire retardant, ore dressing, washup discharge contains
Measure very high, water pollution is particularly acute.In electroplating industry, sb oxide passes through basic unit's coating material frequently as Ti electrode
Material, with the progress of plating, antimony element can progressively intake in waste water.Substantial amounts of antimony enter it is internal, can to respiratory tract, alimentary canal,
Crawl, lung, liver produces stimulates and destroy, and can induce cancer, huge to human health damage.Therefore, stibium-containing wastewater is effective
Handle very urgent, develop the treatment research of the stibium-containing wastewater of high-efficiency and economic, there is great society, economy and Significance for Environment.
The currently used processing method for removing stibium-containing wastewater has chemical precipitation method, electrolysis, absorption method, ion exchange
Method.(1) chemical precipitation method is by first adding vulcanized sodium into stibium-containing wastewater, being precipitated out antimony, then add polyaluminum sulfate
Iron, generates iron sulfide and iron hydroxide, and the purpose for removing Antimony in Waste Water is reached using their cohesion and co-precipitation.Although
Many advantages, such as being simple and convenient to operate with technique, be economical and practical, but its precipitation slag is difficult to handle, and can cause secondary pollution.
(2) electrolysis is to use platinum group oxide or PbO2Make anode, to destroy cyanide, then by antimony ion pH=11 condition
Lower flocculation, precipitation, filtering are removed antimony, and this method energy consumption is big, therefore fail to obtain generally in the processing of stibium-containing wastewater
Using.(3) absorption method is to utilize porous solid material, antimony+absorption in waste water is removed in solid adsorbent surfaces
A kind of method.This method is applied widely to stibium-containing wastewater, will not cause secondary pollution, but absorption choosing of the adsorbent to antimony ion
Selecting property is not high.(4) although ion-exchange operating procedure is simple, is easy to regenerate, except antimony effect is good.But the method is inhaled by resin
Attached capacity limit, suitable for the low waste water of processing concentration containing antimony, and resin is easy to be poisoned, and processing cost is higher.
The content of the invention
To solve the deficiencies in the prior art, the present invention provides a kind of processing method of electroplating wastewater containing antimony, contain
Antimony electroplating wastewater enters sump by waste line, carries out centralized collection herein and preliminarily stabilised is adjusted, the outlet of sump
Coarse rack is connected by waste line, the major diameter solid matter in industrial wastewater is removed at this, the outlet of coarse rack, which passes through, gives up
Water pipeline connects primary sedimentation basin, and in this insoluble matter in further removing waste water, the outlet of primary sedimentation basin passes through waste water
Pipeline connects pH value regulating reservoir, and the pH value range of pH value regulating reservoir water outlet is about 6.0 ~ 8.0, to meet chitosan-living things catalysis
Adsorption cleaning system enters the requirement of water pH value, and the outlet of pH value regulating reservoir connects chitosan-living things catalysis by waste line and inhales
Attached cleaning system, the sludge material outward transport processing of chitosan-living things catalysis adsorption cleaning system discharge, meanwhile, chitosan-biology
The outlet of catalytic adsorption cleaning system connects aeration tank by waste line, herein by aerobic aeration process, makes in waste water
Various phosphorus containg substances are converted into orthophosphates, and the outlet of aeration tank connects biological phosphate-eliminating pond by waste line, its effect is
The orthophosphates decomposition and inversion in waste water is removed by bioactivity reaction process, the outlet in biological phosphate-eliminating pond passes through waste pipe
Line connects secondary sedimentation tank, all removes the remaining insoluble matter in waste water at this, the outlet of secondary sedimentation tank passes through waste water
Pipeline connects water purifying tank, and the outlet of water purifying tank will be arranged by waste line outside purification water outlet after treatment;Wherein, shell gathers
The pond body of sugar-living things catalysis adsorption cleaning system uses strengthened glass steel material, and pond body left side lower section is equipped with inlet valve and stretches
Contracting mud pusher, right side top are equipped with flowing water Valve, and lower right-hand side is equipped with sludge row's mouth, and pond body top is equipped with light steel bracket, thereon
3 groups of totally 9 atomizers are fixed with, pond body is fixedly arranged in the middle of 3 sets and rolls absorption brush, and often set rolls absorption brush left side and is provided with
1 fixed brush, is bonded with rolling absorption brush;Industrial wastewater after pH value adjusting processing is inhaled by chitosan-living things catalysis
The inlet valve of lower section enters cleaning system on the left of attached cleaning system, and 3 sets in the middle part of pond body roll absorption brush and start up time
Pin rolls, and the chitosan and sargassum thunbergii adhered to thereon comes into full contact with the antimony ion in waste water, passes through chitosan and sargassum thunbergii point
The complex reaction occurred with antimony ion of hydroxyl, carboxyl, acid amides based selective in subchain, makes the antimony in waste water by sargassum thunbergii height
Effect absorption, the sargassum thunbergii residue after adsorption reaction is brushed and be allowed to natural subsidence to bottom of pond portion, gradual shape by fixed brush afterwards
Into sludge material, after promoted by flexible mud pusher, through sludge row's mouth discharge pond body, while brush clean rolling brush through fixed brush
Hair continues to do more than clockwise movement to the water surface, sprays chitosan-sargassum thunbergii mixed liquor again by atomizer, adsorbs rolling
Brush is regenerated, and is entered again through clockwise movement path in water, is started new adsorption reaction process.
Its chitosan-living things catalysis adsorption cleaning system, its pond body dischargeable capacity are 245m3, it rolls absorption brush brush length
3.5m, the long 10cm of bristle, it is 380V, swing circle 180s that it, which drives the operating voltage of motor,.
Its chitosan-living things catalysis adsorption cleaning system, in its chitosan-sargassum thunbergii mixed liquor, chitosan and sargassum thunbergii
Mass concentration be respectively 60.0mg/L and 4.5g/L.
The advantage of the invention is that:
(1)The present invention has broken away from the inherent technology route of the existing electroplating wastewater processing containing antimony, and creative make use of sargassum thunbergii
With selection characterization of adsorption of the chitosan to metal ion, especially antimony ion, pass through the hydroxyl on sargassum thunbergii and chitosan molecule chain
Efficient complex reaction occurs for the antimony ion in base, carboxyl, amide groups and waste water, can have been given play to significantly for stibium-containing wastewater
Adsorption cleaning effect, its antimony ion removal efficiency is up to 99.5%.
(2)Compared with the method for existing processing stibium-containing wastewater, the most preferably applicable pH value range of the system is wider, only needs letter
Single enters water pH value regulating measure, so that it may which easily reach system enters the requirement of water pH value.
(3)Present invention utilizes both not only common but also cheap products of chitosan and sargassum thunbergii, operation is greatly reduced
In Material Cost, be highly suitable for coastal economy and promoted the use of with industrial comparatively developed regions.
(4)Present invention employs chitosan and sargassum thunbergii absorption Antimony in Waste Water ion means, without using it is any have poison
Material is learned, so as to eliminate the risk for introducing pollutant that is new, endangering bigger.
Brief description of the drawings
Fig. 1 is the equipment schematic diagram of the present invention.
In figure:1- sumps, 2- coarse racks, 3- primary sedimentation basins, 4-pH values regulating reservoir, 5- chitosans-living things catalysis are inhaled
Attached cleaning system, 6- aeration tanks, 7- biological phosphate-eliminatings pond, 8- secondary sedimentation tanks, 9- water purifying tanks
Fig. 2 is the schematic diagram of chitosan-living things catalysis adsorption cleaning system.
51- glass reinforced plastics pond body, the light steel brackets of 52-, 53- atomizers, 54- roll absorption brush, 55- fixed brushes, 56-
Inlet valve, 57- flowing water Valves, 58- sludge row mouth, 59- stretch mud pusher.
Embodiment
The processing method of removal heavy metals in industrial wastewater as shown in Figure 1, electroplating wastewater containing antimony are passed through useless by waste water
Water pipeline enters sump 1, carries out centralized collection herein and preliminarily stabilised is adjusted, the outlet of sump 1 is connected by waste line
Coarse rack 2 is connect, the major diameter solid matter in industrial wastewater is removed at this, the outlet of coarse rack 2 connects one by waste line
Secondary sedimentation basin 3, in this insoluble matter in further removing waste water, the outlet 3 of primary sedimentation basin connects pH by waste line
It is worth regulating reservoir 4, waste water is neutralized and carries out the accurate adjusting of pH value, the pH value range of 4 water outlet of pH value regulating reservoir herein
For 6.0 ~ 8.0, to meet that the water pH value that enters of chitosan-living things catalysis adsorption cleaning system 5 requires, the outlet of pH value regulating reservoir 4
Chitosan-living things catalysis adsorption cleaning system 5 is connected by waste line, chitosan-living things catalysis adsorption cleaning system 5 is discharged
Sludge material outward transport processing, meanwhile, the outlet of chitosan-living things catalysis adsorption cleaning system 5 passes through waste line connection and exposes
Gas pond 6, herein by aerobic aeration process, makes the various nitrogen substances in waste water be converted into nitrate nitrogen, aeration tank 6 goes out
Mouthful biological phosphate-eliminating pond 7 is connected by waste line, it is by bioactivity reaction process that it, which is acted on, various is contained make in waste water
Phosphorus substance is converted into orthophosphates, and the outlet in biological phosphate-eliminating pond 7 connects secondary sedimentation tank 8 by waste line, herein will be useless
Remaining insoluble matter in water all removes, and the outlet of secondary sedimentation tank 8 connects water purifying tank 9 by waste line, water purifying tank 9
Outlet will be arranged by waste line outside the purification water outlet after the system is handled;Wherein, chitosan-living things catalysis adsorption cleaning
The pond body 51 of system 5 uses strengthened glass steel material, and pond body dischargeable capacity is 245m3, pond body left side lower section is equipped with inlet valve
56 and flexible mud pusher 59, flowing water Valve 57 be housed above right side, lower right-hand side is equipped with sludge row's mouth 58, and pond body top is equipped with gently
Steel bracket 52, is fixed with 3 groups of totally 9 atomizers 53 thereon, and pond body is fixedly arranged in the middle of 3 sets and rolls absorption brush 54, brushes long 3.5m,
The long 10cm of bristle, it is 380V, swing circle 180s that it, which drives the operating voltage of motor, and often set, which rolls, adsorbs each peace in the left side of brush 54
Equipped with 1 fixed brush 55, it is bonded with rolling absorption brush 54;Waste water after pH value adjusting processing is urged by chitosan-biology
The inlet valve 56 for changing the left side of adsorption cleaning system 5 lower section enters cleaning system, and 3 sets in the middle part of pond body roll absorption brush 54
Start to roll clockwise, the chitosan and sargassum thunbergii adhered to thereon come into full contact with the antimony ion in waste water, by chitosan and
The complex reaction occurred with antimony ion of hydroxyl, carboxyl, acid amides based selective on sargassum thunbergii strand, makes the antimony quilt in waste water
Sargassum thunbergii efficient absorption, the sargassum thunbergii residue after adsorption reaction is brushed and be allowed to natural subsidence to bottom of pond by fixed brush 55 afterwards
Portion, gradually forms sludge material, after promoted by flexible mud pusher 59, discharge pond body through sludge row's mouth 58, meanwhile, through fixed brush 55
Brush clean rolling bristle to continue to do more than clockwise movement to the water surface, chitosan-rat-tail is sprayed by atomizer 53 again
Algae mixed liquor, is regenerated rolling absorption brush 54, enters again through clockwise movement path in water, start new adsorption reaction
Process;The effect of wherein pH value regulating reservoir 4 is will to be adjusted by the pH value of waste water of primary sedimentation to 6.8 ~ 7.2, to meet that shell gathers
Sugar-living things catalysis adsorption cleaning system 5 enters the requirement of water pH value;Wherein, in chitosan-sargassum thunbergii mixed liquor, chitosan and mouse
The mass concentration of tail algae is respectively 60.0mg/L and 4.5g/L.
Electroplating wastewater containing antimony after being handled by the system, its antimony removal efficiency is up to 99.5%.
Claims (1)
1. the processing method of a kind of electroplating wastewater containing antimony, it is characterised in that electroplating wastewater containing antimony is entered by waste line to catchment
Well, carries out centralized collection herein and preliminarily stabilised is adjusted, and the outlet of sump connects coarse rack by waste line, removes herein
Major diameter solid matter in industrial wastewater, the outlet of coarse rack connect primary sedimentation basin by waste line, herein further
The insoluble matter in waste water is removed, the outlet of primary sedimentation basin connects pH value regulating reservoir by waste line, and pH value regulating reservoir goes out
The pH value range of water is about 6.0 ~ 8.0, to meet that the water pH value that enters of chitosan-living things catalysis adsorption cleaning system requires, pH value
The outlet of regulating reservoir connects chitosan-living things catalysis adsorption cleaning system by waste line, and chitosan-living things catalysis absorption is net
The sludge material outward transport processing of change system discharge, meanwhile, the outlet of chitosan-living things catalysis adsorption cleaning system passes through waste pipe
Line connects aeration tank, herein by aerobic aeration process, the various phosphorus containg substances in waste water is converted into orthophosphates, is aerated
The outlet in pond connects biological phosphate-eliminating pond by waste line, and it is by the positive phosphorus in waste water by bioactivity reaction process that it, which is acted on,
Hydrochlorate decomposition and inversion removes, and the outlet in biological phosphate-eliminating pond connects secondary sedimentation tank by waste line, will be surplus in waste water at this
Remaining insoluble matter all removes, and the outlet of secondary sedimentation tank connects water purifying tank by waste line, and the outlet of water purifying tank, which passes through, gives up
Water pipeline will be arranged outside purification water outlet after treatment;Wherein, the pond body of chitosan-living things catalysis adsorption cleaning system is using strong
Change glass steel material, pond body dischargeable capacity is 245m3, lower section is equipped with inlet valve and flexible mud pusher on the left of pond body, on right side
Side is equipped with flowing water Valve, and lower right-hand side is equipped with sludge row's mouth, and pond body top is equipped with light steel bracket, is fixed with 3 groups of totally 9 mists thereon
Change nozzle, pond body is fixedly arranged in the middle of 3 sets and rolls absorption brush, rolls absorption and brush long 3.5m, the long 10cm of bristle, and often set rolls absorption brush
Left side is respectively provided with 1 fixed brush, is bonded with rolling absorption brush;Industrial wastewater after pH value adjusting processing is gathered by shell
The inlet valve of lower section enters cleaning system on the left of sugar-living things catalysis adsorption cleaning system, and 3 sets in the middle part of pond body, which roll, to be inhaled
Attached brush starts to roll clockwise, and the chitosan and sargassum thunbergii adhered to thereon comes into full contact with the antimony ion in waste water, gathered by shell
The complex reaction occurred with antimony ion of sugar and the hydroxyl on sargassum thunbergii strand, carboxyl, acid amides based selective, makes in waste water
Sargassum thunbergii residue after adsorption reaction is brushed and is allowed to natural subsidence to pond by sargassum thunbergii efficient absorption by antimony by fixed brush afterwards
Bottom, gradually forms sludge material, after promoted by flexible mud pusher, through sludge row's mouth discharge pond body, while brush through fixed brush
Clean rolling bristle continues to do more than clockwise movement to the water surface, sprays chitosan-sargassum thunbergii mixing again by atomizer
The mass concentration of liquid, chitosan and sargassum thunbergii is respectively 60.0mg/L and 4.5g/L, is regenerated rolling absorption brush, passes through again
Clockwise movement path enters in water, starts new adsorption reaction process.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711362983.3A CN107986571B (en) | 2016-03-15 | 2016-03-15 | Treatment method of antimony-containing electroplating wastewater |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610145400.0A CN105668933B (en) | 2016-03-15 | 2016-03-15 | A kind of processing method of the electroplating wastewater containing antimony |
CN201711362983.3A CN107986571B (en) | 2016-03-15 | 2016-03-15 | Treatment method of antimony-containing electroplating wastewater |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610145400.0A Division CN105668933B (en) | 2016-03-15 | 2016-03-15 | A kind of processing method of the electroplating wastewater containing antimony |
Publications (2)
Publication Number | Publication Date |
---|---|
CN107986571A true CN107986571A (en) | 2018-05-04 |
CN107986571B CN107986571B (en) | 2020-06-12 |
Family
ID=56310344
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201711362983.3A Active CN107986571B (en) | 2016-03-15 | 2016-03-15 | Treatment method of antimony-containing electroplating wastewater |
CN201610145400.0A Active CN105668933B (en) | 2016-03-15 | 2016-03-15 | A kind of processing method of the electroplating wastewater containing antimony |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610145400.0A Active CN105668933B (en) | 2016-03-15 | 2016-03-15 | A kind of processing method of the electroplating wastewater containing antimony |
Country Status (1)
Country | Link |
---|---|
CN (2) | CN107986571B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108640390B (en) * | 2018-05-31 | 2021-10-22 | 阳谷祥光铜业有限公司 | Treatment method of antimony-containing wastewater |
Citations (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19800610A1 (en) * | 1998-01-12 | 1999-07-15 | Helmar Haug | Cleaning up waste water containing heavy metals, e.g. in electronics or electroplating industries |
CN101186419A (en) * | 2007-12-25 | 2008-05-28 | 赵青海 | Method for treating electroplating mixed wastewater |
CN101302073A (en) * | 2008-06-13 | 2008-11-12 | 吴江市运东邱舍污水处理有限公司 | Advanced treatment process for electroplating sewage |
CN101676224A (en) * | 2008-09-18 | 2010-03-24 | 中国科学院福建物质结构研究所 | Method for treating industrial chromium-containing waste water by bacteria |
CN102115890A (en) * | 2011-01-04 | 2011-07-06 | 华南理工大学 | Total recycling method of PCB (printed circuit board) nitric acid type tin-lead stripping waste liquid |
CN102502996A (en) * | 2011-11-15 | 2012-06-20 | 镇江绿能环保科技有限公司 | Pretreatment technical flow for applying industrial sewage to microalgae aquaculture |
CN102872814A (en) * | 2012-08-28 | 2013-01-16 | 常州大学 | Composite adsorbing material for removing nickel ions in natural water and preparation method thereof |
CN103011464A (en) * | 2012-12-07 | 2013-04-03 | 常州大学 | Treatment method of stibium-containing wastewater |
CN103086569A (en) * | 2013-01-08 | 2013-05-08 | 华南理工大学 | Method for detoxifying, emission-reducing and deeply treating wastewater of electronic electroplating industry |
WO2014021726A1 (en) * | 2012-08-03 | 2014-02-06 | Instytut Biochemii I Biofizyki | A process for purification treatment of waste water with a high content of metals, particularly copper and silver, and a composition for use thereof |
CN103663713A (en) * | 2013-12-20 | 2014-03-26 | 中山大学 | Biological compound treatment agent for sewage and sewage treatment method |
CN104728136A (en) * | 2015-03-23 | 2015-06-24 | 宁波风机有限公司 | Full three-dimensional multi-stage centrifugal blower |
CN104843939A (en) * | 2015-04-30 | 2015-08-19 | 四川海天环保能源有限公司 | Process for adopting metal film to cooperatively treat wastewater capable of reaching Class III in water quality |
CN104898848A (en) * | 2015-06-17 | 2015-09-09 | 苏州艾曼纽自动化科技有限公司 | HUD (head up display) system based on DLP (digital light processing) technology |
KR20160015441A (en) * | 2014-07-30 | 2016-02-15 | 가톨릭관동대학교산학협력단 | Method of Hybridly Treating Acid Mine Drainage with Clay Minerals and Microalgae |
-
2016
- 2016-03-15 CN CN201711362983.3A patent/CN107986571B/en active Active
- 2016-03-15 CN CN201610145400.0A patent/CN105668933B/en active Active
Patent Citations (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19800610A1 (en) * | 1998-01-12 | 1999-07-15 | Helmar Haug | Cleaning up waste water containing heavy metals, e.g. in electronics or electroplating industries |
CN101186419A (en) * | 2007-12-25 | 2008-05-28 | 赵青海 | Method for treating electroplating mixed wastewater |
CN101302073A (en) * | 2008-06-13 | 2008-11-12 | 吴江市运东邱舍污水处理有限公司 | Advanced treatment process for electroplating sewage |
CN101676224A (en) * | 2008-09-18 | 2010-03-24 | 中国科学院福建物质结构研究所 | Method for treating industrial chromium-containing waste water by bacteria |
CN102115890A (en) * | 2011-01-04 | 2011-07-06 | 华南理工大学 | Total recycling method of PCB (printed circuit board) nitric acid type tin-lead stripping waste liquid |
CN102502996A (en) * | 2011-11-15 | 2012-06-20 | 镇江绿能环保科技有限公司 | Pretreatment technical flow for applying industrial sewage to microalgae aquaculture |
WO2014021726A1 (en) * | 2012-08-03 | 2014-02-06 | Instytut Biochemii I Biofizyki | A process for purification treatment of waste water with a high content of metals, particularly copper and silver, and a composition for use thereof |
CN102872814A (en) * | 2012-08-28 | 2013-01-16 | 常州大学 | Composite adsorbing material for removing nickel ions in natural water and preparation method thereof |
CN103011464A (en) * | 2012-12-07 | 2013-04-03 | 常州大学 | Treatment method of stibium-containing wastewater |
CN103086569A (en) * | 2013-01-08 | 2013-05-08 | 华南理工大学 | Method for detoxifying, emission-reducing and deeply treating wastewater of electronic electroplating industry |
CN103663713A (en) * | 2013-12-20 | 2014-03-26 | 中山大学 | Biological compound treatment agent for sewage and sewage treatment method |
KR20160015441A (en) * | 2014-07-30 | 2016-02-15 | 가톨릭관동대학교산학협력단 | Method of Hybridly Treating Acid Mine Drainage with Clay Minerals and Microalgae |
CN104728136A (en) * | 2015-03-23 | 2015-06-24 | 宁波风机有限公司 | Full three-dimensional multi-stage centrifugal blower |
CN104843939A (en) * | 2015-04-30 | 2015-08-19 | 四川海天环保能源有限公司 | Process for adopting metal film to cooperatively treat wastewater capable of reaching Class III in water quality |
CN104898848A (en) * | 2015-06-17 | 2015-09-09 | 苏州艾曼纽自动化科技有限公司 | HUD (head up display) system based on DLP (digital light processing) technology |
Non-Patent Citations (1)
Title |
---|
范彩彩: "鼠尾藻对水体重金属铅、铜、锌、镉的生物吸附效应研究", 《中国优秀硕士学位论文全文数据库工程科技Ⅰ辑 》 * |
Also Published As
Publication number | Publication date |
---|---|
CN107986571B (en) | 2020-06-12 |
CN105668933A (en) | 2016-06-15 |
CN105668933B (en) | 2018-02-06 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101538102A (en) | Ozone-bacteria filter system for advanced treatment of hardly-degradable organic wastewater | |
CN105214465A (en) | The apparatus and method of integration wet process of FGD dedusting | |
CN107754599A (en) | A kind of high/low temperature gaseous recombination desulfurization denitration method | |
CN105601052B (en) | The processing method of lead in a kind of removal electroplating wastewater | |
CN114452799A (en) | Efficient purification washing tower system based on acid-base waste gas treatment and working method thereof | |
CN208115480U (en) | A kind of emission-control equipment of co-oxidation | |
CN205796953U (en) | A kind of biological deodorizing tower | |
CN105601050B (en) | A kind of biofermentation heavy metal precipitation purification method | |
CN105668933B (en) | A kind of processing method of the electroplating wastewater containing antimony | |
CN105668934B (en) | A kind of processing system of the electroplating wastewater containing antimony | |
CN109354328B (en) | A kind of acidic mine waste water processing system | |
CN210332216U (en) | Differential contact countercurrent acid mist spray absorption tower | |
CN207769527U (en) | A kind of device of the ultra-clean processing flue gas of the dust removal integrated wet method of desulphurization denitration | |
CN208626978U (en) | It is a kind of for handling the device of industrial organic exhaust gas | |
CN111484173A (en) | High-efficient clean system of degree of depth of water | |
CN105541056B (en) | A kind of remove the processing method of stannum in PCB industrial wastewater | |
CN215480287U (en) | Utilize sewage purification ware of ultraviolet light and year copper active carbon synergism | |
CN107487961B (en) | Method for removing heavy metals in industrial wastewater | |
CN205760495U (en) | Sewage sedimenting system | |
CN205361042U (en) | High -efficient flue gas desulfurization system | |
CN205055798U (en) | Modular wet -type flue gas desulfurization dust collector | |
CN205055799U (en) | Device that integration wet flue gas desulfurization removed dust | |
CN206570161U (en) | A kind of graphite fluorine-containing waste water processing apparatus | |
CN105541055B (en) | Treatment system for removing tin in PCB industrial wastewater | |
CN208799926U (en) | A kind of energy-efficient diesel-driven generator flue gas cleaner |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
TA01 | Transfer of patent application right |
Effective date of registration: 20200426 Address after: Room 295, Building C, 606 Ningliu Road, Changlu Street, Jiangbei New District, Nanjing City, Jiangsu Province, 210000 Applicant after: Nanjing Boyo Environmental Technology Co., Ltd. Address before: Room 2, unit 155, 401 Ma Ma Street, Shangcheng, 310012, Zhejiang, Hangzhou Applicant before: HANGZHOU QICHENG SCIENCE & TECHNOLOGY Co.,Ltd. |
|
TA01 | Transfer of patent application right | ||
GR01 | Patent grant | ||
GR01 | Patent grant |