CN205011498U - Phosphorus containing sewage purifier - Google Patents
Phosphorus containing sewage purifier Download PDFInfo
- Publication number
- CN205011498U CN205011498U CN201520479172.1U CN201520479172U CN205011498U CN 205011498 U CN205011498 U CN 205011498U CN 201520479172 U CN201520479172 U CN 201520479172U CN 205011498 U CN205011498 U CN 205011498U
- Authority
- CN
- China
- Prior art keywords
- waste water
- water container
- phosphorus
- reaction zone
- containing wastewater
- 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.)
- Expired - Fee Related
Links
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 title claims abstract description 33
- 229910052698 phosphorus Inorganic materials 0.000 title claims abstract description 31
- 239000011574 phosphorus Substances 0.000 title claims abstract description 31
- 239000010865 sewage Substances 0.000 title abstract description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 46
- 238000006243 chemical reaction Methods 0.000 claims abstract description 36
- 239000002351 wastewater Substances 0.000 claims description 75
- 239000010802 sludge Substances 0.000 claims description 30
- 238000007670 refining Methods 0.000 claims description 15
- 239000000126 substance Substances 0.000 claims description 11
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 7
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 7
- 239000003795 chemical substances by application Substances 0.000 claims description 7
- 239000004571 lime Substances 0.000 claims description 7
- 239000008267 milk Substances 0.000 claims description 7
- 210000004080 milk Anatomy 0.000 claims description 7
- 235000013336 milk Nutrition 0.000 claims description 7
- 239000000523 sample Substances 0.000 claims description 7
- 238000005189 flocculation Methods 0.000 claims description 6
- 230000016615 flocculation Effects 0.000 claims description 6
- 210000001364 upper extremity Anatomy 0.000 claims description 6
- 238000007689 inspection Methods 0.000 claims description 4
- 230000000630 rising effect Effects 0.000 claims description 4
- 230000000694 effects Effects 0.000 abstract description 11
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 abstract description 10
- 239000002244 precipitate Substances 0.000 abstract description 6
- 239000003814 drug Substances 0.000 abstract description 4
- 238000000034 method Methods 0.000 description 11
- 238000004062 sedimentation Methods 0.000 description 7
- 230000008569 process Effects 0.000 description 5
- 238000001179 sorption measurement Methods 0.000 description 4
- 230000031018 biological processes and functions Effects 0.000 description 3
- 239000000701 coagulant Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 2
- 229920000388 Polyphosphate Polymers 0.000 description 2
- 229920000037 Polyproline Polymers 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 238000000909 electrodialysis Methods 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000001205 polyphosphate Substances 0.000 description 2
- 235000011176 polyphosphates Nutrition 0.000 description 2
- 238000001223 reverse osmosis Methods 0.000 description 2
- 239000005422 algal bloom Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000008570 general process Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 150000003016 phosphoric acids Chemical class 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 230000002000 scavenging effect Effects 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Removal Of Specific Substances (AREA)
Abstract
The utility model discloses a phosphorus containing sewage purifier, including the sewage container, be equipped with the mud fill in this sewage container, the macrostoma end that this mud was fought up, top edge that this mud was fought with the interior wall connection of sewage container is below this mud is fought the sewage container forms the reaction zone, above this mud is fought the sewage container forms the settling zone, the reaction zone is connected with the inlet tube, reaction zone and settling zone pass through the pipeline intercommunication. Adopt the utility model discloses a phosphorus containing sewage purifier's the effect that is showing is, mud is fought to cut apart the sewage container and is formed reaction zone and settling zone, sewage in the reaction zone with throw the medicament reaction that adds, produce phosphorous precipitate, the settling zone is delivered to through pipeline with sewage more together to phosphorous precipitate, phosphorous precipitate deposits to be detached in mud is fought, reaction zone and settling zone separate each other, eliminate influencing each other between two steps, and dirty treatment of water purifying effect is good.
Description
Technical field
The utility model relates to a kind of effluent treatment plant, is specifically related to a kind of phosphorus-containing wastewater refining plant.
Background technology
Phosphor in sewage element exceeds standard, and can accelerate the eutrophication of water body, and this phenomenon is comparatively serious in China, all brings great harm to industry, water industry, agricultural and tourism.The nutrient concentrations such as nitrogen, phosphorus raises, and being the reason of algal bloom, is again wherein key factor with phosphorus.Therefore, how effectively to reduce the concentration of phosphor in sewage, to decontamination, protection of the environment, tool is of great significance.Therefore, country has made strict regulation to the content of total phosphorus in the sewage of discharge after process, mostly all requires that the content of total phosphorus in sewage can not more than 0.5mg/l.
At present, domestic and international sewage dephosphorization technology mainly contains biological process, the large class of chemical method two.Biological process is as A/O, A
2/ O, UCT technique, main being applicable to, processes lower concentration and organic phosphorus-containing wastewater; Chemical method and physico-chemical processes mainly contain the techniques such as coagulant sedimentation, ion exchange adsorption, electrodialysis, reverse osmosis, and main being applicable to processes inorganic states phosphorus-containing wastewater.
Biological process is generally only applicable to the phosphorus-containing wastewater of lower concentration, and as required, total phosphorous is less than below 10mg/l.Its cutting mechanisms is polyP bacteria excessive adsorption, is then reached the object of dephosphorization by mud discharging.Owing to easily discharging after polyP bacteria excessive adsorption, sludge dewatering also can make total phosphorus again enter water body, thus causes the pollution again of total phosphorus, and the method treatment effect is unstable again.
And conventional coagulant sedimentation is not very good to the removal effect of high-concentration phosphorus-containing wastewater yet, after general process, total phosphorus is also at about 1mg/l, reduces often effect further unstable.And the technology investments such as ion exchange adsorption, electrodialysis, reverse osmosis are high, operational management requires high, if the bad processing power causing fouling membrane generally not easily to recover film of pre-treatment, loss is very large, therefore generally seldom adopts.
In various phosphorus-containing wastewater, be maximum with the phosphorized waste water intractability produced in metal phosphorizing process, because its phosphoric acid salt quantity discharged is large, and contain the inorganic salts such as the zine ion of higher concentration, also have the pollutent such as petroleum-type and suspended substance in addition.According to feature and the phosphatization drainage situation of phosphorized waste water, the emphasis determining such wastewater treatment removes PO
4 3-, petroleum-type and Zn
2+deng.At present, when using coagulant sedimentation Removal of Phosphorus in Wastewater, after waste water is mixed with precipitation agent and flocculation agent in reaction tank, Direct precipitation is separated, and effect is bad.
Utility model content
For solving above technical problem, the utility model provides a kind of phosphorus-containing wastewater refining plant.
Technical scheme is as follows:
A kind of phosphorus-containing wastewater refining plant, its key is: comprise waste water container, sludge bucket is provided with in this waste water container, the big opening end of this sludge bucket upward, the upper limb of this sludge bucket is connected with the inwall of described waste water container, the described waste water container forming reactions district below this sludge bucket, and the described waste water container above this sludge bucket forms settling region, described reaction zone is connected with water inlet pipe, and described reaction zone is communicated with by transport pipe with settling region.
The unusual effect of above technical scheme is adopted to be, waste water container is split forming reactions district and settling region by sludge bucket, sewage in reaction zone and the medicament reaction added, produce phosphorous throw out, phosphorous throw out delivers to settling region by transport pipe again together with sewage, and phosphorous precipitate removes in sludge bucket; Upper strata clear water effluent sewerage container, compact construction is reasonable.
The cross section of above-mentioned waste water container inwall is rounded, and the connection end of described water inlet pipe and described reaction zone is near the upper limb of described sludge bucket, and the tube core line of the connection end of described water inlet pipe overlaps with the tangent line of the described waste water container of rounded section.Adopt above technical scheme, because sludge bucket is up big and down small, make the reaction zone below sludge bucket up-small and down-big, sewage tangentially enters on top, reaction zone, under turning in the waste water container inward turning that cross section is rounded, sewage is in the downward mistake of rotation becomes, and sewage and medicament react the tiny throw out generated and mutually collide, and pass through the bridging effect of flocculation agent, make fine suspension generate the thick suspended substance being easy to precipitation; Sewage is during in rotation, downward mistake becomes, and from large to small, velocity slope is descending successively decreases its flow velocity in reaction zone, is conducive to the formation of floc sedimentation.
Above-mentioned water inlet pipe is provided with line mixer, this line mixer is connected to lime milk dosing pipe and flocculation agent chemical feed pipe.Adopt above technical scheme, lime milk dosing pipe and flocculation agent chemical feed pipe directly can mix with waste water in the water inlet process of waste water, can add at any time according to quantity, convenient control.
The lower end of above-mentioned transport pipe and the bottom of described reaction zone are connected, and the upper end of described transport pipe and the top of described settling region are connected, and are connected with water distributor after described settling region is stretched in the upper end of described transport pipe.Adopt above technical scheme, the thick suspended substance of formation and floc sedimentation etc. are assembled in the bottom of reaction zone, then deliver to settling region by transport pipe together with waste water, and after the water distribution uniformity of water distributor, precipitate in sludge bucket, upper liquid is scavenging solution.
Above-mentioned water inlet pipe is provided with pH meter probe, and this pH meter probe is between described lime milk dosing pipe and the connection end of described water inlet pipe.Adopt above technical scheme, the pH of pH meter probe on-line measurement waste water.
The described waste water container that above-mentioned settling region is corresponding is provided with inspection manhole.Adopt above technical scheme, inspection manhole facilitates maintainer to come in and go out.
The lower surface of above-mentioned sludge bucket is connected with the bottom surface of described waste water container.Adopt above technical scheme, the outer wall of sewage around sludge bucket in reaction zone steadily rotates, and forms the effective of thick suspended substance and floc sedimentation.
Above-mentioned waste water container is two, two described waste water containers are up and down just to setting, wherein the described waste water container of below is one section of treater, the described waste water container of top is two sections of treaters, the top of the settling region of described one section of treater is provided with header, the tube wall of this header is provided with sieve aperture, and the water inlet pipe of this header and described two sections of treaters is connected.
Adopt above technical scheme, because the zine ion contained in sewage can affect treatment effect, therefore technique needs first to dezincify, dephosphorization again, two waste water container series connection use simultaneously, one section of treater dezincifies, and interference is discharged in two sections of treater dephosphorization, improve treatment effect, waste water can be processed continuously, efficiently.The header on top, one section of treater settling region is intake to the water inlet pipe of two sections of treaters, and the sieve aperture on header plays the effect of filtering thick suspended substance and floc sedimentation.
The top of the described water distributor of above-mentioned two sections of treaters is provided with filtrating area, and the inwall of the described waste water container above this filtrating area is provided with ring-type water leg, and the inner side of this ring-type water leg is provided with skimming plate, and this ring-type water leg is connected with rising pipe.Adopt above technical scheme, settling region upper liquid is filtered by filtrating area, then by spilling into ring-type water leg after skimming plate, is discharged by rising pipe.
Beneficial effect: adopt phosphorus-containing wastewater refining plant of the present utility model, waste water container is split forming reactions district and settling region by sludge bucket, sewage in reaction zone and the medicament reaction added, produce phosphorous throw out, phosphorous throw out delivers to settling region by transport pipe again together with sewage, and phosphorous precipitate removes in sludge bucket; Reaction zone and settling region are spaced from each other, and eliminate influencing each other between two steps, and the treatment and purification of sewage is effective.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Embodiment
Below in conjunction with embodiment and accompanying drawing, the utility model is described in further detail.
As shown in Figure 1, a kind of phosphorus-containing wastewater refining plant, comprise waste water container 1, the cross section of this waste water container 1 inwall is rounded, sludge bucket 3 is provided with in this waste water container 1, the big opening end of this sludge bucket 3 upward, the upper limb of this sludge bucket 3 is connected with the inwall of described waste water container 1, the lower surface of described sludge bucket 3 is connected with the bottom surface of described waste water container 1, described waste water container 1 forming reactions district 1a below this sludge bucket 3, described waste water container 1 above this sludge bucket 3 forms settling region 1b, described reaction zone 1a is connected with water inlet pipe 5, the connection end of this water inlet pipe 5 and described reaction zone 1a is near the upper limb of described sludge bucket 3, the tube core line of the connection end of described water inlet pipe 5 overlaps with the tangent line of the described waste water container 1 of rounded section.
Described reaction zone 1a is communicated with by transport pipe 7 with settling region 1b, the lower end of this transport pipe 7 and the bottom of described reaction zone 1a are connected, the upper end of described transport pipe 7 and the top of described settling region 1b are connected, be connected with water distributor 8 after described settling region 1b is stretched in the upper end of described transport pipe 7, the described waste water container 1 that described settling region 1b is corresponding is provided with inspection manhole.
Described water inlet pipe 5 is provided with line mixer 6, this line mixer 6 is connected to lime milk dosing pipe 2 and flocculation agent chemical feed pipe 4, described water inlet pipe 5 is provided with pH meter probe x, and this pH meter probe x is between described lime milk dosing pipe 2 and the connection end of described water inlet pipe 5.
Described waste water container 1 is two, two described waste water containers about 1 are just to setting, wherein the described waste water container 1 of below is one section of treater, the described waste water container 1 of top is two sections of treaters, the top of the settling region 1b of described one section of treater is provided with header 9, the tube wall of this header 9 is provided with sieve aperture, and this header 9 is connected with the water inlet pipe 5 of described two sections of treaters.
The top of the described water distributor 8 of described two sections of treaters is provided with filtrating area 11, the inwall of the described waste water container 1 above this filtrating area 11 is provided with ring-type water leg 12, this ring-type water leg 12 is connected with rising pipe 13, and the inner side of this ring-type water leg 12 is provided with skimming plate 10.
Finally it should be noted that; foregoing description is only preferred embodiment of the present utility model; those of ordinary skill in the art is under enlightenment of the present utility model; under the prerequisite without prejudice to the utility model aim and claim; can make like multiple types and representing, such conversion all falls within protection domain of the present utility model.
Claims (9)
1. a phosphorus-containing wastewater refining plant, it is characterized in that: comprise waste water container (1), sludge bucket (3) is provided with in this waste water container (1), the big opening end of this sludge bucket (3) upward, the upper limb of this sludge bucket (3) is connected with the inwall of described waste water container (1), described waste water container (1) the forming reactions district (1a) of this sludge bucket (3) below, the described waste water container (1) of this sludge bucket (3) top forms settling region (1b), described reaction zone (1a) is connected with water inlet pipe (5), described reaction zone (1a) is communicated with by transport pipe (7) with settling region (1b).
2. phosphorus-containing wastewater refining plant according to claim 1, it is characterized in that: the cross section of described waste water container (1) inwall is rounded, the upper limb of connection end near described sludge bucket (3) of described water inlet pipe (5) and described reaction zone (1a), the tube core line of the connection end of described water inlet pipe (5) overlaps with the tangent line of the described waste water container (1) of rounded section.
3. phosphorus-containing wastewater refining plant according to claim 1 and 2, it is characterized in that: on described water inlet pipe (5), be provided with line mixer (6), this line mixer (6) is connected to lime milk dosing pipe (2) and flocculation agent chemical feed pipe (4).
4. phosphorus-containing wastewater refining plant according to claim 1, it is characterized in that: the lower end of described transport pipe (7) and the bottom of described reaction zone (1a) are connected, the upper end of described transport pipe (7) and the top of described settling region (1b) are connected, and are connected with water distributor (8) after described settling region (1b) is stretched in the upper end of described transport pipe (7).
5. phosphorus-containing wastewater refining plant according to claim 3, it is characterized in that: on described water inlet pipe (5), be provided with pH meter probe (x), this pH meter probe (x) is positioned between the connection end of described lime milk dosing pipe (2) and described water inlet pipe (5).
6. phosphorus-containing wastewater refining plant according to claim 1, is characterized in that: on the described waste water container (1) that described settling region (1b) is corresponding, be provided with inspection manhole.
7. the phosphorus-containing wastewater refining plant according to claim 1,2,4 or 6, is characterized in that: the lower surface of described sludge bucket (3) is connected with the bottom surface of described waste water container (1).
8. phosphorus-containing wastewater refining plant according to claim 4, it is characterized in that: described waste water container (1) is two, two described waste water containers (1) are up and down just to setting, wherein the described waste water container (1) of below is one section of treater, the described waste water container (1) of top is two sections of treaters, the top of the settling region (1b) of described one section of treater is provided with header (9), the tube wall of this header (9) is provided with sieve aperture, and this header (9) is connected with the water inlet pipe (5) of described two sections of treaters.
9. phosphorus-containing wastewater refining plant according to claim 8, it is characterized in that: the top of the described water distributor (8) of described two sections of treaters is provided with filtrating area (11), the inwall of the described waste water container (1) of top, this filtrating area (11) is provided with ring-type water leg (12), this ring-type water leg (12) is connected with rising pipe (13), and the inner side of this ring-type water leg (12) is provided with skimming plate (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520479172.1U CN205011498U (en) | 2015-07-06 | 2015-07-06 | Phosphorus containing sewage purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520479172.1U CN205011498U (en) | 2015-07-06 | 2015-07-06 | Phosphorus containing sewage purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205011498U true CN205011498U (en) | 2016-02-03 |
Family
ID=55210112
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520479172.1U Expired - Fee Related CN205011498U (en) | 2015-07-06 | 2015-07-06 | Phosphorus containing sewage purifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205011498U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104973716A (en) * | 2015-07-06 | 2015-10-14 | 重庆泰克环保工程设备有限公司 | Phosphorus-containing sewage purification device |
-
2015
- 2015-07-06 CN CN201520479172.1U patent/CN205011498U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104973716A (en) * | 2015-07-06 | 2015-10-14 | 重庆泰克环保工程设备有限公司 | Phosphorus-containing sewage purification device |
| CN104973716B (en) * | 2015-07-06 | 2017-12-05 | 重庆泰克环保科技股份有限公司 | A kind of phosphorus-containing wastewater purifier |
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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 |
Granted publication date: 20160203 |