CN201433127Y - Crystallized phosphorus removing reactor - Google Patents
Crystallized phosphorus removing reactor Download PDFInfo
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- CN201433127Y CN201433127Y CN2009201201159U CN200920120115U CN201433127Y CN 201433127 Y CN201433127 Y CN 201433127Y CN 2009201201159 U CN2009201201159 U CN 2009201201159U CN 200920120115 U CN200920120115 U CN 200920120115U CN 201433127 Y CN201433127 Y CN 201433127Y
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- reaction zone
- crystallizing
- zone
- reactor
- water outlet
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- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 title abstract description 13
- 229910052698 phosphorus Inorganic materials 0.000 title abstract description 12
- 239000011574 phosphorus Substances 0.000 title abstract description 12
- 238000006243 chemical reaction Methods 0.000 claims abstract description 32
- 238000005273 aeration Methods 0.000 claims abstract description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 21
- 230000000630 rising effect Effects 0.000 claims abstract description 7
- 239000004744 fabric Substances 0.000 claims description 15
- 230000008676 import Effects 0.000 claims description 7
- 230000001174 ascending effect Effects 0.000 claims description 4
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 11
- 238000002425 crystallisation Methods 0.000 abstract description 6
- 230000008025 crystallization Effects 0.000 abstract description 5
- 239000003814 drug Substances 0.000 abstract description 5
- 239000007788 liquid Substances 0.000 abstract description 5
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 abstract description 5
- 230000009286 beneficial effect Effects 0.000 abstract description 4
- 239000013078 crystal Substances 0.000 abstract description 4
- 238000004062 sedimentation Methods 0.000 abstract description 4
- 238000000926 separation method Methods 0.000 abstract description 4
- 239000001506 calcium phosphate Substances 0.000 abstract description 2
- 229910000389 calcium phosphate Inorganic materials 0.000 abstract description 2
- 235000011010 calcium phosphates Nutrition 0.000 abstract description 2
- 239000012530 fluid Substances 0.000 abstract description 2
- 238000004064 recycling Methods 0.000 abstract description 2
- 238000007599 discharging Methods 0.000 abstract 1
- 239000002351 wastewater Substances 0.000 description 12
- 238000011160 research Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000006004 Quartz sand Substances 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 238000009388 chemical precipitation Methods 0.000 description 2
- 238000003795 desorption Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 102000004160 Phosphoric Monoester Hydrolases Human genes 0.000 description 1
- 108090000608 Phosphoric Monoester Hydrolases Proteins 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- CKMXBZGNNVIXHC-UHFFFAOYSA-L ammonium magnesium phosphate hexahydrate Chemical compound [NH4+].O.O.O.O.O.O.[Mg+2].[O-]P([O-])([O-])=O CKMXBZGNNVIXHC-UHFFFAOYSA-L 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000012295 chemical reaction liquid Substances 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 230000006911 nucleation Effects 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 150000003016 phosphoric acids Chemical class 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 239000010801 sewage sludge Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 229910052567 struvite Inorganic materials 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
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Abstract
The utility model discloses a crystallized phosphorus removing reactor. A crystallized phosphorus removing reactor main body is provided with a water distribution zone, a reaction zone and a sedimentation zone from bottom to top. The water distribution zone is provided with a dreg removing pipe, a water inlet pipe, a flow rising column disc type distributor and an aeration device. The aeration device is composed by the combination of an aeration pipe and an aeration head. A carrier inlet and a medicine inlet pipe are arranged at the lower part of the reaction zone. A first flow return pipe anda second flow return pipe are arranged at the upper and lower middle parts of the reaction zone. The sedimentation zone is provided with a water outlet weir, a water outlet pipe and a discharging opening. A saw-tooth type overflow weir is arranged at the upper part of the water outlet weir, two parallel baffles are arranged at the side face of the water outlet weir, and an inclined plate is arranged at the bottom part of the water outlet weir. The functions of the reactor is clear; the water distribution zone is provided with the flow rising column disc type distributor, which can effectivelyavoid short flowing of fluid; the reaction zone is provided with a carrier, which can intensify the crystallization of calcium phosphate; by adopting the running method of continuous charging and interval aeration, the reactor can prevent blockage of the carrier and is beneficial for the desorbing and recycling of crystals on the carrier; the sedimentation zone is provided with the saw-tooth baffle water outlet weir, so that the water outlet is uniform; as the inclined plate is arranged, solid-liquid separation is good.
Description
Technical field
The utility model relates to reactor, relates in particular to a kind of crystallizing-dephosphorizing reactor.
Background technology
China's water pollution problems is very serious, and in main lake, the eutrophic lake that nitrogen and phosphorus pollution caused accounts for more than 50%, and the financial loss that annual " wawter bloom " and " red tide " causes is up to more than 10,000,000,000 yuan.Phosphorus-containing wastewater is increasing on the one hand, and the environmental pollution and the ecological damage that cause constantly aggravate; Phosphorus is a kind of valuable source on the other hand, only enough human the uses about 100 years of the phosphorus reserves of verifying in the world.Research waste water reclaiming dephosphorization technique is eliminated the plain pollution of phosphorus in waste water, recycles phosphor resource simultaneously, has become pressing for of social development.
Chemical precipitation dephosphorization method is a kind of important waste water dephosphorization technology.The practical discovery, traditional chemical precipitation dephosphorization method have slow, the shortcomings such as solid-liquid separation is poor, moisture percentage in sewage sludge height, sludge dewatering treatment complexity of sedimentation speed.The biological phosphate-eliminating method is one of focus of the research of wastewater treatment in recent years.Studies show that pair waste water composition requirement height (C: N: P=100: could satisfy the demand of functional microorganism at 5: 1), operation stability are also arranged the biological phosphate-eliminating method and handiness is relatively poor, excess sludge is handled and dispose problem such as difficulty.Chemicrystallization dephosphorization method mainly contains MAP (struvite) crystallizing-dephosphorizing method and HAP (calcium phosphate) crystallizing-dephosphorizing method, and these class methods can be removed phosphorus, can reclaim phosphorus again, has therefore obtained the favor of academia and industrial community.
Reactor is the key of chemicrystallization dephosphorization process.At present, research reports such as external existing DHV crystallization reactor (DHVCrystalactor TM Pelletiser), CSIR fluidized-bed crystallization post (CSIR Fluiclised bed CrystallsationColumn) and Kurita fixed bed crystallization post (Kurita Fixed Bed Crystallisation Column), domestic then rarely seen correlative study report.Stable, the phosphoric acid salt organic efficiency height of crystallizing-dephosphorizing reactor novel structure, operation condition that the utility model is related is applicable to various treatment of Phosphorus Containing Waste Water.
Summary of the invention
The utility model purpose is to overcome the deficiencies in the prior art, and a kind of crystallizing-dephosphorizing reactor is provided.
The crystallizing-dephosphorizing reactor body is provided with cloth pool, reaction zone and settling region from top to bottom, the cloth pool is provided with scum pipe, water inlet pipe, up-flow post disc type sparger, aerating apparatus, aerating apparatus is combined by aeration tube, aeration head, the reaction zone bottom is provided with carrier import, drug-feeding tube, upper and lower first return line, second return line of being provided with at reaction zone middle part, the settling region is provided with effluent weir, rising pipe, discharge port, effluent weir top is provided with the prionodont overflow weir, the effluent weir side is provided with two parallel baffles, and the effluent weir bottom is provided with swash plate.
Described reactor body adopts circular plexi-glass tubular to make.The volume ratio of cloth pool, reaction zone and settling region is 1: 2～3: 0.8～1.Up-flow post disc type sparger is made up of perforation plate and distribution post, perforation plate diameter 100～200mm, have 4～9 circular holes on the plate, one is positioned at the positive center of perforation plate, other is uniformly distributed on the circumference of diameter 50～150mm, the distribution post of internal diameter 15～25mm, height 30～50mm is installed in the hole, distribution post lower ending opening, upper end closed, the aperture of Φ 2～5mm is evenly offered in the side, up-flow post disc type sparger is fixed between cloth pool and the reaction zone, is 100～150mm from the height of reactor bottom.First return line, second return line end are back taper.Two parallel baffle spacings are 20～40mm, and bottom swash plate width is 20～40mm, and swash plate becomes 25～35 ° with sea line.Effluent weir is separated into ascending zone, flooded zonevvv by water (flow) direction with the settling region and falls the stream district.
The beneficial effect that the utility model compared with prior art has: 1) reactor is divided into cloth pool, three unit of reaction zone and settling region from bottom to top, and it is less to influence each other, and each element diameter equates, compact construction, take up an area of and lack, adopt flange to connect between the unit, be convenient to demolition and maintenance; 2) the cloth pool is provided with up-flow post disc type sparger, can make uniform gas-liquid distribution, effectively avoids the short stream of fluid, can play the effect of supporting the reactor carrier again; 3) reaction zone is provided with carrier (as gac, quartz sand etc.), utilizes the carrier surface characteristic, can form local supersaturated solution at carrier surface, is beneficial to the crystallization of calcium and phosphatase reaction formation calcium phosphate salt and separates out; 4) reactor adopts " continuously feeding-intermittent aeration " mode to move, and continuously feeding can realize the continuous processing to phosphorus-containing wastewater, and intermittent aeration adopts " aeration-stop aeration-aeration " cyclical operation, can improve wastewater pH, reinforcing mass transfer prevents that filler from stopping up, and makes the crystal desorption; 5) the settling region effluent weir adopts the sawtooth baffle plate, can guarantee that the settling region fluidised form is even, adopts swash plate can guarantee the good solid-liquid separation.
Description of drawings
Fig. 1 is the crystallizing-dephosphorizing reactor structural representation;
Fig. 2 is the current distribution plan of settling region in the crystallizing-dephosphorizing reactor;
Fig. 3 is a crystallizing-dephosphorizing reactor structure A-A sectional view;
Fig. 4 is a crystallizing-dephosphorizing reactor structure B-B sectional view;
Among the figure: scum pipe 1, water inlet pipe 2, up-flow post disc type sparger 3, distribution post 4, drug-feeding tube 5, reaction zone first return line 6, flange 7, discharge port 8, rising pipe 9, sawtooth overflow weir 10, parallel baffle 11, swash plate 12, cylinder 13, reaction zone second return line 14, carrier import 15, aeration head 16, aeration tube 17, base 18.
Embodiment
As shown in Figure 1, the crystallizing-dephosphorizing reactor body is provided with cloth pool I from top to bottom, reaction zone II and settling region III, cloth pool I is provided with scum pipe 1, water inlet pipe 2, up-flow post disc type sparger 3, aerating apparatus, aerating apparatus is by aeration tube 17, aeration head 16 combines, reaction zone II bottom is provided with carrier import 15, drug-feeding tube 5, on the reaction zone II middle part, have first return line 6, second return line 14, settling region III is provided with effluent weir, rising pipe 9, discharge port 8, effluent weir top is provided with prionodont overflow weir 10, the effluent weir side is provided with two parallel baffles 11, and the effluent weir bottom is provided with swash plate 12.
Described reactor body adopts circular plexi-glass tubular to make.The volume ratio of cloth pool I, reaction zone II and settling region III is 1: 2～3: 0.8～1.First return line 6, second return line, 14 ends are back taper, and it is uniform and stable not only to help refluxing, and are beneficial to the short-and-medium flow phenomenon of minimizing reaction zone.
As shown in Figure 2, effluent weir is separated into ascending zone, flooded zonevvv by water (flow) direction with settling region III and falls the stream district.
As shown in Figure 3, two parallel baffles, 11 spacings are 20～40mm, and swash plate 10 width in bottom are 20～40mm, and swash plate 10 becomes 25～35 ° with sea line.
As shown in Figure 4, up-flow post disc type sparger 3 is made up of perforation plate and distribution post, perforation plate diameter 100～200mm, have 4～9 circular holes on the plate, one is positioned at the positive center of perforation plate, other is uniformly distributed on the circumference of diameter 50～150mm, the distribution post 4 of internal diameter 15～25mm, height 30～50mm is installed in the hole, distribution post 4 lower ending openings, upper end closed, the aperture of Φ 2～5mm is evenly offered in the side, and up-flow post disc type sparger 3 is fixed between cloth pool I and the reaction zone II, is 100～150mm from the height of reactor bottom.
Crystallizing-dephosphorizing reactor can be made of PVC plate and steel plate.In the actual motion, at first in reaction zone, fill carrier by carrier import 15, be filled to distribution post 4 height with big particle diameter rubble or glass sphere earlier, recharge the carrier that particle diameter is 0.9mm～1.25mm (as gac or quartz sand), packing height is to reaction zone 2/3.Pump into waste water and the medicament of phosphorous 30mg/L then in reactor, medicine component is 180mg/LCaCl
2Solution is with 2mol/LNaOH and 2mol/LHCl conditioned reaction liquid pH.
Reactor adopts the operation scheme of " continuously feeding-intermittent aeration ".Waste water imports cloth pool I by water inlet pipe 2, and medicament imports reaction zone II by drug-feeding tube 5, and air is introduced from reactor bottom by aeration tube 17, and waste water and air enter reaction zone through up-flow post disc type sparger.Under the aeration effect, waste water and medicament thorough mixing in the reaction zone are at reaction zone generation chemical reaction.Stop aeration behind the aeration 1h, the crystal of generation is in carrier surface nucleation, growth.Reactor operation aeration again after 4 hours, the calcium phosphate salt crystal desorption that carrier surface is formed enters flooded zonevvv through the overflow weir of ascending zone, enters and falls the stream district, utilizes the density difference of calcium phosphate salt and water, makes it realize the solid, liquid separation falling the stream district.Water outlet is discharged from rising pipe 9, and crystalline product is discharged from discharge port 8, carries out recycling.
Claims (7)
1. crystallizing-dephosphorizing reactor, it is characterized in that: reactor body is provided with cloth pool (I) from top to bottom, reaction zone (II) and settling region (III), cloth pool (I) is provided with scum pipe (1), water inlet pipe (2), up-flow post disc type sparger (3), aerating apparatus, aerating apparatus is by aeration tube (17), aeration head (16) combines, reaction zone (II) bottom is provided with carrier import (15), drug-feeding tube (5), on reaction zone (II) middle part, have first return line (6), second return line (14), (III) is provided with effluent weir in the settling region, rising pipe (9), discharge port (8), effluent weir top is provided with prionodont overflow weir (10), the effluent weir side is provided with two parallel baffles (11), and the effluent weir bottom is provided with swash plate (12).
2. a kind of crystallizing-dephosphorizing reactor according to claim 1 is characterized in that: described reactor body adopts circular plexi-glass tubular to make.
3. a kind of crystallizing-dephosphorizing reactor according to claim 1 is characterized in that: the volume ratio of described cloth pool (I), reaction zone (II) and settling region (III) is 1: 2～3: 0.8～1.
4. a kind of crystallizing-dephosphorizing reactor according to claim 1, it is characterized in that: described up-flow post disc type sparger (3) is made up of perforation plate and distribution post, perforation plate diameter 100～200mm, have 4～9 circular holes on the plate, one is positioned at the positive center of perforation plate, other is uniformly distributed on the circumference of diameter 50～150mm, internal diameter 15～25mm is installed in the hole, the distribution post (4) of height 30～50mm, distribution post (4) lower ending opening, upper end closed, the aperture of Φ 2～5mm is evenly offered in the side, and up-flow post disc type sparger (3) is fixed between cloth pool (I) and the reaction zone (II), is 100～150mm from the height of reactor bottom.
5. a kind of crystallizing-dephosphorizing reactor according to claim 1 is characterized in that: described first return line (6), second return line (14) end are back taper.
6. a kind of crystallizing-dephosphorizing reactor according to claim 1 is characterized in that: described two parallel baffles (11) spacing is 20～40mm, and bottom swash plate (11) width is 20～40mm, and swash plate (11) becomes 25～35 ° with sea line.
7. a kind of crystallizing-dephosphorizing reactor according to claim 1 is characterized in that: described effluent weir is separated into ascending zone, flooded zonevvv by water (flow) direction with settling region (III) and falls the stream district.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009201201159U CN201433127Y (en) | 2009-05-18 | 2009-05-18 | Crystallized phosphorus removing reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009201201159U CN201433127Y (en) | 2009-05-18 | 2009-05-18 | Crystallized phosphorus removing reactor |
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| Publication Number | Publication Date |
|---|---|
| CN201433127Y true CN201433127Y (en) | 2010-03-31 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009201201159U Expired - Lifetime CN201433127Y (en) | 2009-05-18 | 2009-05-18 | Crystallized phosphorus removing reactor |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101555057B (en) * | 2009-05-18 | 2010-12-08 | 浙江大学 | Crystallizing-dephosphorizing reactor |
| CN104843902A (en) * | 2015-05-15 | 2015-08-19 | 浙江大学 | Integrated biological vector dephosphorizing reactor |
| CN108715477A (en) * | 2018-08-22 | 2018-10-30 | 山东太平洋环保股份有限公司 | The reaction unit and method of nitrogen P elements in a kind of removal sewage |
| CN110885124A (en) * | 2019-12-02 | 2020-03-17 | 怀化恒一颜料化学有限公司 | Equipment for treating quinacridone production wastewater |
-
2009
- 2009-05-18 CN CN2009201201159U patent/CN201433127Y/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101555057B (en) * | 2009-05-18 | 2010-12-08 | 浙江大学 | Crystallizing-dephosphorizing reactor |
| CN104843902A (en) * | 2015-05-15 | 2015-08-19 | 浙江大学 | Integrated biological vector dephosphorizing reactor |
| CN108715477A (en) * | 2018-08-22 | 2018-10-30 | 山东太平洋环保股份有限公司 | The reaction unit and method of nitrogen P elements in a kind of removal sewage |
| CN108715477B (en) * | 2018-08-22 | 2023-06-02 | 山东太平洋环保股份有限公司 | Reaction device and method for removing nitrogen and phosphorus elements in sewage |
| CN110885124A (en) * | 2019-12-02 | 2020-03-17 | 怀化恒一颜料化学有限公司 | Equipment for treating quinacridone production wastewater |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20100331 Effective date of abandoning: 20090518 |