CN204125224U - Nanoscale Iron disposes heavy metal wastewater thereby integrated apparatus - Google Patents
Nanoscale Iron disposes heavy metal wastewater thereby integrated apparatus Download PDFInfo
- Publication number
- CN204125224U CN204125224U CN201420546226.7U CN201420546226U CN204125224U CN 204125224 U CN204125224 U CN 204125224U CN 201420546226 U CN201420546226 U CN 201420546226U CN 204125224 U CN204125224 U CN 204125224U
- Authority
- CN
- China
- Prior art keywords
- reaction zone
- zone
- flocculation
- nanoscale iron
- heavy metal
- 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.)
- Active
Links
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title claims abstract description 72
- 229910052742 iron Inorganic materials 0.000 title claims abstract description 36
- 239000002351 wastewater Substances 0.000 title claims abstract description 31
- 229910001385 heavy metal Inorganic materials 0.000 title claims abstract description 27
- 238000006243 chemical reaction Methods 0.000 claims abstract description 46
- 238000005189 flocculation Methods 0.000 claims abstract description 45
- 230000016615 flocculation Effects 0.000 claims abstract description 45
- 239000000126 substance Substances 0.000 claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 18
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 10
- 230000000630 rising Effects 0.000 claims abstract description 10
- 210000003660 Reticulum Anatomy 0.000 claims description 5
- 230000005484 gravity Effects 0.000 abstract description 4
- 238000003756 stirring Methods 0.000 description 4
- 239000003814 drug Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 239000003292 glue Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 1
- 230000000711 cancerogenic Effects 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000009713 electroplating Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000003311 flocculating Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000003505 mutagenic Effects 0.000 description 1
- 231100000219 mutagenic Toxicity 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Abstract
The utility model provides a kind of Nanoscale Iron to dispose heavy metal wastewater thereby integrated apparatus, and water inlet pipe is connected with the bottom of reaction zone; Nanoscale Iron chemical feed pipe, flocculation agent chemical feed pipe pass into reaction zone I; Reaction zone is provided with agitator; Flocculation zone in the outside of reaction zone, the height higher than flocculation zone of reaction zone height; Settling region is in the outside of flocculation zone; Bucket is arranged on the below of reaction zone, flocculation zone, settling region; Shore pipe is connected with the bottom of bucket; Rising pipe is arranged on the top of device, and is in the top of settling region.Its advantage is overall integration, for concentric(al) circles is arranged, is connected between each concentric(al) circles with support, and the interval waste water of each concentric(al) circles relies on gravity flow, simple structure, reduces reaction compartment.
Description
Technical field
The utility model relates to a kind of heavy metal containing wastewater treatment reaction precipitation integrated apparatus, is particularly useful for Nanoscale Iron medicament reaction precipitation integrated apparatus.
Background technology
Containing plurality of heavy metal in the waste water that smelting and electroplating industry produce, heavy metal contamination has carcinogenic, teratogenesis, mutagenic significant damage to the mankind.Adopt Nanoscale Iron reaction process efficiently can remove heavy metal in waste water, can also recycle rare precious metal.Current employing Nanoscale Iron art breading heavy metal wastewater thereby, long flow path, device is many and complicated, and floor space is large, and energy consumption is high.
Utility model content
The purpose of this utility model aims to provide a kind of facility compact, floor space is little, energy consumption is low simple heavy metal process integrated apparatus, to overcome the existing defects of above-mentioned prior art.
The utility model provides a kind of Nanoscale Iron to dispose heavy metal wastewater thereby integrated apparatus, comprising: water inlet pipe 01, Nanoscale Iron chemical feed pipe 08, flocculation agent chemical feed pipe 10, reaction zone I, flocculation zone II, settling region III, bucket 03, shore pipe 02 and rising pipe 05; Water inlet pipe 01 is connected with the bottom of reaction zone I; Nanoscale Iron chemical feed pipe 08, flocculation agent chemical feed pipe 10 pass into reaction zone I; Reaction zone I is provided with agitator 09; Flocculation zone II in the outside of reaction zone I, reaction zone I height the height higher than flocculation zone II; Settling region III is in the outside of flocculation zone II; Bucket 03 is arranged on the below of reaction zone I, flocculation zone II, settling region III; Shore pipe 02 is connected with the bottom of bucket 03; Rising pipe 05 is arranged on the top of device, and is in the top of settling region III.
Further, the utility model provides a kind of Nanoscale Iron to dispose heavy metal wastewater thereby integrated apparatus, can also have such feature: Nanoscale Iron chemical feed pipe 08 is through to the bottom of reaction zone I.
Further, the utility model provides a kind of Nanoscale Iron to dispose heavy metal wastewater thereby integrated apparatus, can also have such feature: flocculation agent chemical feed pipe 10 leads to the top of reaction zone I.
Further, the utility model provides a kind of Nanoscale Iron to dispose heavy metal wastewater thereby integrated apparatus, can also have such feature: flocculation zone II is provided with efficient micro swirl flocculation ball 07.
Further, the utility model provides a kind of Nanoscale Iron to dispose heavy metal wastewater thereby integrated apparatus, can also have such feature: settling region III is provided with honeycomb inclined-tube 04.
Further, the utility model provides a kind of Nanoscale Iron to dispose heavy metal wastewater thereby integrated apparatus, can also have such feature: reaction zone I, flocculation zone II, settling region III are concentric(al) circles.
Further, the utility model provides a kind of Nanoscale Iron to dispose heavy metal wastewater thereby integrated apparatus, can also have such feature: also comprise water leg 06, set out water pipe 05 front end.
The beneficial effect of utility model
A kind of Nanoscale Iron that the utility model provides disposes heavy metal wastewater thereby integrated apparatus, overall integration, for concentric(al) circles is arranged, the compositions such as the district that responds, flocculation zone, settling region, bucket, be connected with support between each concentric(al) circles, the interval waste water of each concentric(al) circles relies on gravity flow.
Post-type mixer is established in reaction zone, and waste water adds Nanoscale Iron in this region and reacts, and stirrer screw-blade can arrange many groups according to device height.
Efficient micro swirl flocculation ball is dosed in flocculation zone, and efficient micro swirl flocculation ball flocculating effect is good, and flocculation time is very short, strong shock resistance, simple structure, reduces reaction compartment.
Honeycomb inclined-tube is established in settling region, and inclined tube is fixed on support.Device top is clear water zone, and water outlet flows to rising pipe by water leg.Device bottom is bucket, relies on gravity concentration, regular spoil disposal.
Accompanying drawing explanation
Fig. 1 is that Nanoscale Iron of the present utility model disposes heavy metal wastewater thereby integrated apparatus structural representation.
Fig. 2 is the vertical view cutaway drawing of Fig. 1.
Embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is further described.
Nanoscale Iron disposes heavy metal wastewater thereby integrated apparatus, comprising: water inlet pipe 01, Nanoscale Iron chemical feed pipe 08, flocculation agent chemical feed pipe 10, reaction zone I, flocculation zone II, settling region III, bucket 03, shore pipe 02, rising pipe 05 and water leg 06.
Water inlet pipe 01 is connected with the bottom of reaction zone I.Nanoscale Iron chemical feed pipe 08 is through to the bottom of reaction zone I.Flocculation agent chemical feed pipe 10 leads to the top of reaction zone I.
Reaction zone I is provided with vertical stirrer 09.Agitator 09 has stir shaft, agitating vane and stirring motor.Stirring motor drives stir shaft to rotate, and drives agitating vane to rotate.
Flocculation zone II in the outside of reaction zone I, reaction zone I height the height higher than flocculation zone II.Flocculation zone II is provided with efficient micro swirl flocculation ball 07.
Settling region III is in the outside of flocculation zone II.Settling region III is provided with honeycomb inclined-tube 04.Reaction zone I, flocculation zone II, settling region III are concentric structure.
Bucket 03 is arranged on the below of reaction zone I, flocculation zone II, settling region III.
Shore pipe 02 is connected with the bottom of bucket 03.Rising pipe 05 is arranged on the top of device, and is in the top of settling region III.Water leg 06, sets out water pipe 05 front end.
Nanoscale Iron disposes heavy metal wastewater thereby integrated apparatus working process:
Waste water enters bottom reaction zone through water inlet pipe, adds proper amount of nano medicament by Nanoscale Iron chemical feed pipe, and Nanoscale Iron adds pipe through to bottom, with waste water direct reaction, spreads abundant reaction completely through stirrer, to reduce dosing.
After having reacted, top, reaction zone adds flocculation agent by adding pipe, and the waste water outflow after reaction terminates enters flocculation zone, and under the effect of efficient micro swirl flocculation ball, rapid diffusion is also fully collided with water-borne glue body, makes water-borne glue body de-steady fast.
Waste water is from bottom from flowing into settling region, and through honeycomb inclined-tube High-rate sedimentation, top is clear liquid, is arranged outward through rising pipe by water leg; Bottom mud, by bucket gravity concentration, regularly passes through shore pipe spoil disposal.
Claims (7)
1. a Nanoscale Iron disposes heavy metal wastewater thereby integrated apparatus, it is characterized in that, comprising: water inlet pipe (01), Nanoscale Iron chemical feed pipe (08), flocculation agent chemical feed pipe (10), reaction zone (I), flocculation zone (II), settling region (III), bucket (03), shore pipe (02) and rising pipe (05);
Described water inlet pipe (01) is connected with the bottom of described reaction zone (I);
Described Nanoscale Iron chemical feed pipe (08), described flocculation agent chemical feed pipe (10) pass into described reaction zone (I);
Described reaction zone (I) is provided with agitator (09);
Described flocculation zone (II) in the outside of described reaction zone (I), described reaction zone (I) height the height higher than described flocculation zone (II);
Described settling region (III) is in the outside of described flocculation zone (II);
Described bucket (03) is arranged on the below of described reaction zone (I), described flocculation zone (II), described settling region (III);
Described shore pipe (02) is connected with the bottom of described bucket (03);
Described rising pipe (05) is arranged on the top of device, and is in the top of described settling region (III).
2. Nanoscale Iron according to claim 1 disposes heavy metal wastewater thereby integrated apparatus, it is characterized in that:
Wherein, described Nanoscale Iron chemical feed pipe (08) is through to the bottom of described reaction zone (I).
3. Nanoscale Iron according to claim 1 disposes heavy metal wastewater thereby integrated apparatus, it is characterized in that:
Wherein, described flocculation agent chemical feed pipe (10) leads to the top of described reaction zone (I).
4. Nanoscale Iron according to claim 1 disposes heavy metal wastewater thereby integrated apparatus, it is characterized in that:
Wherein, described flocculation zone (II) is provided with efficient micro swirl flocculation ball (07).
5. Nanoscale Iron according to claim 1 disposes heavy metal wastewater thereby integrated apparatus, it is characterized in that:
Described settling region (III) is provided with honeycomb inclined-tube (04).
6. Nanoscale Iron according to claim 5 disposes heavy metal wastewater thereby integrated apparatus, it is characterized in that:
Wherein, described reaction zone (I), described flocculation zone (II), described settling region (III) are concentric structure.
7. Nanoscale Iron as claimed in any of claims 1 to 6 disposes heavy metal wastewater thereby integrated apparatus, it is characterized in that:
Also comprise water leg (06), described rising pipe (05) front end is set.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420546226.7U CN204125224U (en) | 2014-09-22 | 2014-09-22 | Nanoscale Iron disposes heavy metal wastewater thereby integrated apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420546226.7U CN204125224U (en) | 2014-09-22 | 2014-09-22 | Nanoscale Iron disposes heavy metal wastewater thereby integrated apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204125224U true CN204125224U (en) | 2015-01-28 |
Family
ID=52381597
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420546226.7U Active CN204125224U (en) | 2014-09-22 | 2014-09-22 | Nanoscale Iron disposes heavy metal wastewater thereby integrated apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204125224U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109133445A (en) * | 2018-10-10 | 2019-01-04 | 吉林大学 | A kind of integrated reacting system for nanometer micro-electrolysis material |
-
2014
- 2014-09-22 CN CN201420546226.7U patent/CN204125224U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109133445A (en) * | 2018-10-10 | 2019-01-04 | 吉林大学 | A kind of integrated reacting system for nanometer micro-electrolysis material |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203393208U (en) | Ozone oxidation reactor | |
| CN203999104U (en) | From stirring catalysis iron biological carbon and phosphorous removal device | |
| CN204356103U (en) | A kind of counter current contact formula ozone dissolved air flotation device | |
| CN103408211A (en) | Stirrer for sludge anaerobic digester | |
| CN204474452U (en) | A kind of new and effective treating organic waste water by Fenton method deflector type integration apparatus | |
| CN204125224U (en) | Nanoscale Iron disposes heavy metal wastewater thereby integrated apparatus | |
| CN103395909B (en) | Two-stage coagulation air-flotation separation equipment and method | |
| CN207153584U (en) | A kind of industry environmental protection flocculation stirring machine | |
| CN204981327U (en) | Carrier biofilm reactor is removed in circulation | |
| CN204607690U (en) | Activated sludge reaction and equipment for separating liquid from solid | |
| CN202849134U (en) | Chemical dosing device | |
| CN206985926U (en) | A kind of light electrolysis adds photocatalysis equipment | |
| CN207998468U (en) | A kind of high tower dissolved gas floatator | |
| CN103103215B (en) | Gradient circulation stirring method in marsh gas reactor and anaerobic reactor thereof | |
| CN206666280U (en) | A kind of wastewater from chemical industry purifier | |
| CN203545759U (en) | Sedimentation reaction tank for physical water treatment | |
| CN201147649Y (en) | Adjustable low-energy consumption highly-effective water power mix coagulation reactor | |
| CN204939156U (en) | A kind of portable containing cyanogen slurry processing unit | |
| CN203922787U (en) | A kind of efficient air-floating apparatus | |
| CN204369649U (en) | The efficiently heavy stream aerobic reactor of honeycomb fashion | |
| CN201058833Y (en) | Highly-effective steel-making wet dust removal sewage and refining sewage treating apparatus | |
| CN202576027U (en) | High speed air flotation water treatment device | |
| CN203513389U (en) | Chemical oil removal inclined pipe precipitator | |
| CN207024714U (en) | It is a kind of tangentially to enter streaming deep cone thickener system | |
| CN107935088A (en) | A kind of high tower dissolved gas floatator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |