CN204824446U - Low organic matter waste water degree of depth processing system - Google Patents
Low organic matter waste water degree of depth processing system Download PDFInfo
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- CN204824446U CN204824446U CN201520502519.XU CN201520502519U CN204824446U CN 204824446 U CN204824446 U CN 204824446U CN 201520502519 U CN201520502519 U CN 201520502519U CN 204824446 U CN204824446 U CN 204824446U
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- 239000002351 wastewater Substances 0.000 title claims abstract description 43
- 239000005416 organic matter Substances 0.000 title abstract 2
- 238000006243 chemical reaction Methods 0.000 claims abstract description 30
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 27
- 238000001914 filtration Methods 0.000 claims abstract description 17
- 238000004140 cleaning Methods 0.000 claims abstract description 11
- 239000010802 sludge Substances 0.000 claims description 17
- GEHJYWRUCIMESM-UHFFFAOYSA-L Sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 claims description 10
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 8
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L MgCl2 Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 claims description 8
- 235000015450 Tilia cordata Nutrition 0.000 claims description 8
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 8
- 239000003513 alkali Substances 0.000 claims description 8
- 239000004571 lime Substances 0.000 claims description 8
- 229920002401 polyacrylamide Polymers 0.000 claims description 8
- 239000006228 supernatant Substances 0.000 claims description 7
- 239000007788 liquid Substances 0.000 claims description 6
- 235000010265 sodium sulphite Nutrition 0.000 claims description 5
- BAUYGSIQEAFULO-UHFFFAOYSA-L Iron(II) sulfate Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 claims description 4
- 229940045641 Monobasic Sodium Phosphate Drugs 0.000 claims description 4
- 206010042602 Supraventricular extrasystoles Diseases 0.000 claims description 4
- 239000011790 ferrous sulphate Substances 0.000 claims description 4
- 235000003891 ferrous sulphate Nutrition 0.000 claims description 4
- 229910000359 iron(II) sulfate Inorganic materials 0.000 claims description 4
- 229910001629 magnesium chloride Inorganic materials 0.000 claims description 4
- 238000003825 pressing Methods 0.000 claims description 4
- SUKJFIGYRHOWBL-UHFFFAOYSA-N Sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 claims description 3
- 235000012970 cakes Nutrition 0.000 claims description 3
- PMZURENOXWZQFD-UHFFFAOYSA-L na2so4 Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims description 3
- 238000000746 purification Methods 0.000 claims description 3
- 229910052938 sodium sulfate Inorganic materials 0.000 claims description 3
- 235000011152 sodium sulphate Nutrition 0.000 claims description 3
- 238000001556 precipitation Methods 0.000 abstract description 8
- 238000007599 discharging Methods 0.000 abstract 2
- 238000009434 installation Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 12
- WQYVRQLZKVEZGA-UHFFFAOYSA-N Hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- CVTZKFWZDBJAHE-UHFFFAOYSA-N [N].N Chemical compound [N].N CVTZKFWZDBJAHE-UHFFFAOYSA-N 0.000 description 2
- 230000001112 coagulant Effects 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000000903 blocking Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000000994 depressed Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 239000008239 natural water Substances 0.000 description 1
- 230000001264 neutralization Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 150000003016 phosphoric acids Chemical class 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- 238000007634 remodeling Methods 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002562 thickening agent Substances 0.000 description 1
- 150000003568 thioethers Chemical class 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Abstract
The utility model discloses a low organic matter waste water degree of depth processing system, waste water is washd in the processing that it can be high -efficient reliable. The utility model discloses in, the workshop is washd waste water and is carried to the waste water equalizing basin through the wastewater collection pipe, intercommunication installation riser on the waste water equalizing basin, the distal end of riser stretches into to the first order reaction pond, first order reaction pond and pipe chute precipitation tank intercommunication, the other end and the second order reaction pond intercommunication of pipe chute precipitation tank, tip and another pipe chute precipitation tank intercommunication in second order reaction pond, the delivery port intercommunication of another pipe chute precipitation tank has pH readjustment pond and middle pond, and middle pond is through filtering the pipeline and filtering the adsorption tower intercommunication, the delivery port that filters the adsorption tower passes through the clean water pipe way and feeds through to the retrieval and utilization pond, retrieval and utilization pond and discharging pool intercommunication, the last discharge to reach standard pipe of installing of discharging pool, first order reaction pond and second order reaction pond are inside to be equallyd divide for four check, the tank bottom of pipe chute precipitation tank is connected with the blowdown subassembly through discharge pipeline.
Description
Technical field
The utility model relates to a kind of production wastewater treatment system, specifically for the cleaning factory effluent in workshop, and the process of the workshop Cleaning Wastewater of eyeglass enterprise especially processed.
Background technology
Find in our practice of construction process that some enterprises produce a certain amount of polishing Cleaning Wastewater in process of production, especially to prepare enterprise the most common for glasses; The pollutents such as CODCr, SS, PH, colourity are mainly contained in its waste water.If such waste water does not process, directly enter natural water body, the dissolved oxygen in waste water can be consumed in a large number, fall end water transparency, cause the water quality of receiving water body to be turned black smelly; Simultaneously a large amount of suspended substance meeting blocking pipe etc.; Havoc water ecological setting;
Traditional treatment system can not the process of high efficient and reliable, and the water after process also cannot reuse and reliable qualified discharge.
Utility model content
Technical problem to be solved in the utility model is for above-mentioned deficiency of the prior art, a kind of low organism factory effluent advanced treatment system is provided, it can the process Cleaning Wastewater of high efficient and reliable, whole system continuity is good, floor space is little, and the water after process can reuse and qualified discharge.
The utility model solves the technical scheme that its technical problem adopts: low organism factory effluent advanced treatment system, and for the treatment of workshop Cleaning Wastewater, described workshop Cleaning Wastewater is delivered to wastewater equalization pond by wastewater collection pipe; Described wastewater equalization pond is communicated with and installs riser tube, riser tube is provided with lift pump, and the far-end of riser tube stretches to first order reaction pond;
Described first order reaction pond is communicated with tube settling groove, and the other end of tube settling groove is communicated with second order reaction pond, and the end in second order reaction pond is communicated with another tube settling groove; The water outlet of another tube settling groove described is communicated with pH and adjusts back pond, and the water outlet that pH adjusts back pond is communicated with intermediate pool, and intermediate pool is communicated with Filtration Adsorption tower by filter pipeline, and filter pipeline is provided with filtration pump; The water outlet of described Filtration Adsorption tower is communicated to reuse pool by clear water pipeline, and described reuse pool is communicated with discharge pond, and described discharge pond is provided with qualified discharge pipe;
Inside, described first order reaction pond is divided into four lattice, is communicated with dosing pipe and grug feeding jar in each lattice; Be followed successively by adding alkali or adding lime tank of the first lattice along grug feeding jar described in purification of waste water direction, the second lattice add sodium sulphite tank, the 3rd lattice add ferrous sulfate tank and the 4th lattice add PAM tank;
Inside, described second order reaction pond is divided into four lattice equally, and each lattice is all communicated with dosing pipe and grug feeding jar; First lattice are communicated with and add alkali tank, add magnesium chloride tank and add SODIUM PHOSPHATE, MONOBASIC tank; Second lattice are communicated with and add lime tank, and the 3rd lattice are communicated with and add PAC tank, and the 4th lattice are communicated with and add PAM tank;
The bottom land of described tube settling groove is vertebral body structure, and the bottom of two tube settling grooves is connected with blowdown assembly by blow-off line, and described blow-off line is provided with residual sea water pump.
As a kind of preferred implementation of the present utility model, described blowdown assembly comprises the sludge concentration tank be communicated with blow-off line, the bottom of sludge concentration tank is communicated with mud pipeline, and mud pipeline is provided with sludge pump, and the far-end of mud pipeline stretches to the opening for feed of pressure filter; The mud cake that pressure filter is discharged is transported by mud transporter; The pressing filtering liquid of pressure filter is back to wastewater equalization pond by return line; The supernatant liquor of described sludge concentration tank is back to wastewater equalization pond by supernatant liquor pipeline.
As a kind of preferred implementation of the present utility model, described pH adjusts back pond and is communicated with dosing pipe and grug feeding jar, and described grug feeding jar is for adding sodium sulfate tank; Described intermediate pool is communicated with dosing pipe and grug feeding jar, and described grug feeding jar is for adding clorox tank.
As a kind of preferred implementation of the present utility model, described reuse pool is also communicated with reuse pipeline.
The utility model compared with prior art has the following advantages:
The utility model by the wastewater collection in workshop to comprehensive wastewater equalizing tank, comprehensive wastewater rises to reaction tank by lift pump, alkali or lime adjustment pH value is added at the first lattice, second lattice add sodium sulphite, heavy metal is made to generate sulfide precipitation, 3rd lattice add ferrous sulfate, neutralize unnecessary sodium sulphite and carry out coagulating, 4th lattice add PAM and carry out flocculation reaction, small particulate matter is made to form larger sail flower-shaped, be convenient to precipitation, reacted water outlet carries out solid-liquid separation from flowing to tube settler, supernatant liquor enters second order reaction pond, alkali is added at these pond first lattice, magnesium chloride, ammonia nitrogen in SODIUM PHOSPHATE, MONOBASIC and waste water reacts, second lattice feeding lime, remove phosphoric acid salt, 3rd lattice add PAC and carry out coagulating, 4th lattice add PAM and carry out flocculation reaction, small particulate matter is made to form larger sail flower-shaped, be convenient to precipitation, reacted water outlet carries out solid-liquid separation from flowing to tube settler, pond is adjusted back again through PH, by adding sulfuric acid readjustment PH to neutral, enter intermediate pool again, in this pond by dropping into hypochlorite oxidation agent, oxidize away organism and the ammonia nitrogen of part, be filtered absorption again, water outlet flows automatically to reuse tank and returns and or discharge outlet qualified discharge.Whole technological process continuity is good, and efficiency is high, and treatment effect is reliable and stable.
The utility model is also by the reliable blowdown of blowdown assembly, specifically right, and we are by regularly draining into sludge thickener by settling tank base sludge, and mud is depressed into plate and frame(type)filter press by sludge pump and is cured process.Pressing filtering liquid is back to water collecting basin and again processes, and the mud of solidification can transfer to the process of industrial waste treatment station.
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of embodiment of the present utility model;
Fig. 2 is the structural representation of a kind of embodiment of blowdown assembly of the present utility model.
Description of reference numerals:
1-wastewater collection pipe, 2-wastewater equalization pond, 3-lift pump, 4-first order reaction pond, 5-tube settling groove, 6-second order reaction pond, 7-PH adjusts back pond, 8-intermediate pool, 9-filtration pump, 10-Filtration Adsorption tower, 11-reuse pool, 12-discharges pond, 13-grug feeding jar, 14-residual sea water pump, 15-blow-off pipe, 16-sludge concentration tank, 17-sludge pump, 18-pressure filter, 19-mud transporter.
Embodiment
Below in conjunction with drawings and Examples, the utility model embodiment is described:
Fig. 1 and Fig. 2 shows a kind of concrete structure of the present utility model, and as shown in the figure, the utility model low organism factory effluent advanced treatment system, for the treatment of workshop Cleaning Wastewater; Described workshop Cleaning Wastewater is delivered to wastewater equalization pond 2 by wastewater collection pipe 1; Described wastewater equalization pond is communicated with and installs riser tube, riser tube is provided with lift pump 3, the far-end of riser tube stretches to first order reaction pond 4;
As shown in the figure, described first order reaction pond is communicated with tube settling groove 5, and the other end of tube settling groove is communicated with second order reaction pond 6, and the end in second order reaction pond is communicated with another tube settling groove 5; The water outlet of another tube settling groove described is communicated with pH and adjusts back the water outlet connection intermediate pool 8 that pond is adjusted back in pond 7, pH, and intermediate pool is communicated with Filtration Adsorption tower 10 by filter pipeline, filter pipeline is provided with filtration pump 9; The water outlet of described Filtration Adsorption tower is communicated to reuse pool 11 by clear water pipeline, and described reuse pool is communicated with discharge pond 12, and described discharge pond is provided with qualified discharge pipe;
As shown in the figure, inside, described first order reaction pond is divided into four lattice, is communicated with dosing pipe and grug feeding jar 13 in each lattice; Be followed successively by adding alkali or adding lime tank of the first lattice along grug feeding jar described in purification of waste water direction, the second lattice add sodium sulphite tank, the 3rd lattice add ferrous sulfate tank and the 4th lattice add PAM tank;
As shown in the figure, inside, described second order reaction pond is divided into four lattice equally, and each lattice is all communicated with dosing pipe and grug feeding jar; First lattice are communicated with and add alkali tank, add magnesium chloride tank and add SODIUM PHOSPHATE, MONOBASIC tank; Second lattice are communicated with and add lime tank, and the 3rd lattice are communicated with and add PAC tank, and the 4th lattice are communicated with and add PAM tank;
As shown in the figure, the bottom land of described tube settling groove is vertebral body structure, and the bottom of two tube settling grooves is connected with blowdown assembly by blow-off line 15, described blow-off line is provided with residual sea water pump 14.
Preferably, as shown in the figure, described blowdown assembly comprises the sludge concentration tank 16 be communicated with blow-off line, and the bottom of sludge concentration tank is communicated with mud pipeline, mud pipeline is provided with sludge pump 17, and the far-end of mud pipeline stretches to the opening for feed of pressure filter 18; The mud cake that pressure filter is discharged is transported by mud transporter 19; The pressing filtering liquid of pressure filter is back to wastewater equalization pond by return line; The supernatant liquor of described sludge concentration tank is back to wastewater equalization pond by supernatant liquor pipeline.
Preferably, as shown in the figure, described pH adjusts back pond and is communicated with dosing pipe and grug feeding jar, and described grug feeding jar is for adding sodium sulfate tank; Described intermediate pool is communicated with dosing pipe and grug feeding jar, and described grug feeding jar is for adding clorox tank.
Preferably, as shown in the figure, described reuse pool is also communicated with reuse pipeline.
By reference to the accompanying drawings the utility model preferred implementation is explained in detail above, but the utility model is not limited to above-mentioned embodiment, in the ken that those of ordinary skill in the art possess, can also make a variety of changes under the prerequisite not departing from the utility model aim.
Do not depart from design of the present utility model and scope can make many other and change and remodeling.Should be appreciated that the utility model is not limited to specific embodiment, scope of the present utility model is defined by the following claims.
Claims (4)
1. low organism factory effluent advanced treatment system, for the treatment of workshop Cleaning Wastewater, is characterized in that: described workshop Cleaning Wastewater is delivered to wastewater equalization pond by wastewater collection pipe; Described wastewater equalization pond is communicated with and installs riser tube, riser tube is provided with lift pump, and the far-end of riser tube stretches to first order reaction pond;
Described first order reaction pond is communicated with tube settling groove, and the other end of tube settling groove is communicated with second order reaction pond, and the end in second order reaction pond is communicated with another tube settling groove; The water outlet of another tube settling groove described is communicated with pH and adjusts back pond, and the water outlet that pH adjusts back pond is communicated with intermediate pool, and intermediate pool is communicated with Filtration Adsorption tower by filter pipeline, and filter pipeline is provided with filtration pump; The water outlet of described Filtration Adsorption tower is communicated to reuse pool by clear water pipeline, and described reuse pool is communicated with discharge pond, and described discharge pond is provided with qualified discharge pipe;
Inside, described first order reaction pond is divided into four lattice, is communicated with dosing pipe and grug feeding jar in each lattice; Be followed successively by adding alkali or adding lime tank of the first lattice along grug feeding jar described in purification of waste water direction, the second lattice add sodium sulphite tank, the 3rd lattice add ferrous sulfate tank and the 4th lattice add PAM tank;
Inside, described second order reaction pond is divided into four lattice equally, and each lattice is all communicated with dosing pipe and grug feeding jar; First lattice are communicated with and add alkali tank, add magnesium chloride tank and add SODIUM PHOSPHATE, MONOBASIC tank; Second lattice are communicated with and add lime tank, and the 3rd lattice are communicated with and add PAC tank, and the 4th lattice are communicated with and add PAM tank;
The bottom land of described tube settling groove is vertebral body structure, and the bottom of two tube settling grooves is connected with blowdown assembly by blow-off line, and described blow-off line is provided with residual sea water pump.
2. low organism factory effluent advanced treatment system as claimed in claim 1, it is characterized in that: described blowdown assembly comprises the sludge concentration tank be communicated with blow-off line, the bottom of sludge concentration tank is communicated with mud pipeline, mud pipeline is provided with sludge pump, and the far-end of mud pipeline stretches to the opening for feed of pressure filter; The mud cake that pressure filter is discharged is transported by mud transporter; The pressing filtering liquid of pressure filter is back to wastewater equalization pond by return line; The supernatant liquor of described sludge concentration tank is back to wastewater equalization pond by supernatant liquor pipeline.
3. low organism factory effluent advanced treatment system as claimed in claim 1 or 2, is characterized in that: described pH adjusts back pond and is communicated with dosing pipe and grug feeding jar, and described grug feeding jar is for adding sodium sulfate tank; Described intermediate pool is communicated with dosing pipe and grug feeding jar, and described grug feeding jar is for adding clorox tank.
4. low organism factory effluent advanced treatment system as claimed in claim 1, is characterized in that: described reuse pool is also communicated with reuse pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520502519.XU CN204824446U (en) | 2015-07-07 | 2015-07-07 | Low organic matter waste water degree of depth processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520502519.XU CN204824446U (en) | 2015-07-07 | 2015-07-07 | Low organic matter waste water degree of depth processing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204824446U true CN204824446U (en) | 2015-12-02 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520502519.XU Expired - Fee Related CN204824446U (en) | 2015-07-07 | 2015-07-07 | Low organic matter waste water degree of depth processing system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204824446U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108059272A (en) * | 2017-12-14 | 2018-05-22 | 佛山市中环环境检测中心 | A kind of leaded vanadium effluent treatment plant |
-
2015
- 2015-07-07 CN CN201520502519.XU patent/CN204824446U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108059272A (en) * | 2017-12-14 | 2018-05-22 | 佛山市中环环境检测中心 | A kind of leaded vanadium effluent treatment plant |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151202 Termination date: 20200707 |