CN1480408A - Up-flow type response operator for anaerobic ammoxidation biomembrane - Google Patents
Up-flow type response operator for anaerobic ammoxidation biomembrane Download PDFInfo
- Publication number
- CN1480408A CN1480408A CNA03141723XA CN03141723A CN1480408A CN 1480408 A CN1480408 A CN 1480408A CN A03141723X A CNA03141723X A CN A03141723XA CN 03141723 A CN03141723 A CN 03141723A CN 1480408 A CN1480408 A CN 1480408A
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- Prior art keywords
- reaction unit
- anaerobic ammonia
- reaction
- unit body
- ammonia oxidation
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- 238000006243 chemical reaction Methods 0.000 claims abstract description 57
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 30
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000000945 filler Substances 0.000 claims abstract description 11
- 230000003647 oxidation Effects 0.000 claims description 14
- 238000007254 oxidation reaction Methods 0.000 claims description 14
- 229910000831 Steel Inorganic materials 0.000 claims description 4
- 230000000630 rising effect Effects 0.000 claims description 4
- 239000010959 steel Substances 0.000 claims description 4
- 239000010802 sludge Substances 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 2
- 239000012528 membrane Substances 0.000 abstract 2
- 230000000903 blocking effect Effects 0.000 abstract 1
- 238000006298 dechlorination reaction Methods 0.000 abstract 1
- 230000001590 oxidative effect Effects 0.000 abstract 1
- 230000000813 microbial effect Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- 241001453382 Nitrosomonadales Species 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
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- Y02W10/12—
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- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
A flowing upward anaerobic ammonia oxidizing reactor with biologic membrane is composed of a cylindrical main body with water inlet tube, gas outlet tube and water outlet tube, the soft filler hung in said main body, and the denitrating biologic membrane for inoculating sludge to start said reaction. Its advantages are not blocking and high dechlorination effect.
Description
Technical field
The present invention relates to a kind of upflow type anaerobic ammonia oxidation biomembrane reaction apparatus, it can be held effectively and stay anaerobic ammonia oxidation microbiological.
Anammox is a kind of with NH
4 +For electron donor, with NO
2 -New biological denitrificaion reaction for electron acceptor(EA) has the excellent development application prospect in the wastewater biological denitrificaion field.But, the anaerobic ammonia oxidizing bacteria poor growth, in the Sludge Bed Anammox reaction unit that adopts at present, mud is easy to run off, and causes reaction unit longer start time, has limited this The Application of Technology.
Summary of the invention
The purpose of this invention is to provide a kind of upflow type anaerobic ammonia oxidation biomembrane reaction apparatus.
It has the reaction unit body, hangs soft-filler in the reaction unit body, and reaction unit body bottom is provided with water inlet pipe, and the reaction unit bodies top is provided with escape pipe, and reaction unit body upper side is provided with rising pipe.
The present invention adopts column or cube-shaped device, and interior extension soft-filler is the startup that seed sludge carries out the Anammox reaction unit with the denitrification biofilm, reaches to accelerate the purpose that the Anammox reaction unit starts.The upflowing water intake mode can make into water thorough mixing, avoids stopping up, and the soft-filler low price can effectively be held and stay microorganism, improves the biomass in the reaction unit.With the denitrification biofilm is that seed sludge can successfully start upflow type anaerobic ammonia oxidation biomembrane reaction apparatus in 3 months, and can obtain the denitrification effect of stability and high efficiency.
Description of drawings
Accompanying drawing is a upflow type anaerobic ammonia oxidation biomembrane reaction apparatus structural representation.
Embodiment
Upflow type anaerobic ammonia oxidation biomembrane reaction apparatus has column or cube-shaped reaction unit body, in the reaction unit body, hang soft-filler 1, reaction unit body bottom is provided with water inlet pipe 2, and the reaction unit bodies top is provided with escape pipe 4, and reaction unit body upper side is provided with rising pipe 3.The reaction unit body adopts steel or Steel Concrete to make up, reaction unit body aspect ratio 5: 1～10: 1, and big volume reaction unit adopts the lattice assembling.Soft-filler upper end is at the water surface below 5～10 centimetres, 15～25 centimetres of following end distance reaction unit bottoms.Reaction unit adopts the upflowing water intake mode, adopts the perforation water distributor to intake from the bottom.Reaction unit adopts denitrification biofilm to carry out the startup of Anammox biomembrane reaction apparatus.The reaction unit body is a column or cube-shaped.
As shown in the figure, reaction unit is cylindric, and interior extension soft-filler forms microbial film with attached microbial.Waste water enters from reaction unit bottom water inlet pipe 2, and after formed Anammox microbial film was handled on the soft-filler 1 in reaction unit, from rising pipe 3 outflows on top, the gases such as nitrogen that reaction unit produces were discharged from the escape pipe 4 at top.Earlier cultivating denitrification biofilm in hanging with the reaction unit of soft-filler during startup, is the startup that seed sludge carries out the Anammox reaction unit subsequently with the denitrification biofilm, can successfully start upflow type anaerobic ammonia oxidation biomembrane reaction apparatus in 3 months.
Claims (6)
1. upflow type anaerobic ammonia oxidation biomembrane reaction apparatus, it is characterized in that: it has the reaction unit body, in the reaction unit body, hang soft-filler (1), reaction unit body bottom is provided with water inlet pipe (2), the reaction unit bodies top is provided with escape pipe (4), and reaction unit body upper side is provided with rising pipe (3).
2. a kind of upflow type anaerobic ammonia oxidation biomembrane reaction apparatus according to claim 1, it is characterized in that: said reaction unit body adopts steel or Steel Concrete to make up, reaction unit body aspect ratio 5: 1～10: 1, big volume reaction unit adopts the lattice assembling.
3. a kind of upflow type anaerobic ammonia oxidation biomembrane reaction apparatus according to claim 1 is characterized in that: said soft-filler upper end is at the water surface below 5～10 centimetres, 15～25 centimetres of following end distance reaction unit bottoms.
4. a kind of upflow type anaerobic ammonia oxidation biomembrane reaction apparatus according to claim 1 is characterized in that: said reaction unit adopts the upflowing water intake mode, adopts the perforation water distributor to intake from the bottom.
5. a kind of upflow type anaerobic ammonia oxidation biomembrane reaction apparatus according to claim 1 is characterized in that: said reaction unit adopts denitrification biofilm to carry out the startup of Anammox biomembrane reaction apparatus.
6. a kind of upflow type anaerobic ammonia oxidation biomembrane reaction apparatus according to claim 1, it is characterized in that: said reaction unit body is a column or cube-shaped.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA03141723XA CN1480408A (en) | 2003-07-18 | 2003-07-18 | Up-flow type response operator for anaerobic ammoxidation biomembrane |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA03141723XA CN1480408A (en) | 2003-07-18 | 2003-07-18 | Up-flow type response operator for anaerobic ammoxidation biomembrane |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1480408A true CN1480408A (en) | 2004-03-10 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNA03141723XA Pending CN1480408A (en) | 2003-07-18 | 2003-07-18 | Up-flow type response operator for anaerobic ammoxidation biomembrane |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1480408A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100526231C (en) * | 2007-01-19 | 2009-08-12 | 华南理工大学 | USAB-biological membrane anaerobic ammoxidation strain denitrogenation method and its apparatus |
| CN101962225A (en) * | 2010-10-28 | 2011-02-02 | 哈尔滨工业大学 | External anaerobic ammonia oxidation membrane bioreactor |
| CN101343116B (en) * | 2008-07-18 | 2011-06-15 | 北京工业大学 | Quick start method for anaerobic ammonia oxidation bioreactor for urban sewage |
| CN1709806B (en) * | 2004-06-18 | 2011-07-06 | 株式会社日立工业设备技术 | Method for operating anaerobic ammonium oxidation vessel and anaerobic ammonium oxidation equipment |
| CN102173533A (en) * | 2011-02-28 | 2011-09-07 | 桂林理工大学 | Efficient anaerobic ammonium oxidation sewage treatment method |
| CN102557356A (en) * | 2012-02-16 | 2012-07-11 | 北京工业大学 | Process and method for denitrification and phosphorus removal of municipal sewage by half shortcut nitrification and anaerobic ammonium oxidation |
| CN103011399A (en) * | 2012-12-18 | 2013-04-03 | 中山大学 | Novel anammox biomembrane reactor and biological denitrifying method thereof |
-
2003
- 2003-07-18 CN CNA03141723XA patent/CN1480408A/en active Pending
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1709806B (en) * | 2004-06-18 | 2011-07-06 | 株式会社日立工业设备技术 | Method for operating anaerobic ammonium oxidation vessel and anaerobic ammonium oxidation equipment |
| CN100526231C (en) * | 2007-01-19 | 2009-08-12 | 华南理工大学 | USAB-biological membrane anaerobic ammoxidation strain denitrogenation method and its apparatus |
| CN101343116B (en) * | 2008-07-18 | 2011-06-15 | 北京工业大学 | Quick start method for anaerobic ammonia oxidation bioreactor for urban sewage |
| CN101962225A (en) * | 2010-10-28 | 2011-02-02 | 哈尔滨工业大学 | External anaerobic ammonia oxidation membrane bioreactor |
| CN101962225B (en) * | 2010-10-28 | 2012-07-25 | 哈尔滨工业大学 | External anaerobic ammonia oxidation membrane bioreactor |
| CN102173533A (en) * | 2011-02-28 | 2011-09-07 | 桂林理工大学 | Efficient anaerobic ammonium oxidation sewage treatment method |
| CN102173533B (en) * | 2011-02-28 | 2012-08-08 | 桂林理工大学 | Efficient anaerobic ammonium oxidation sewage treatment method |
| CN102557356A (en) * | 2012-02-16 | 2012-07-11 | 北京工业大学 | Process and method for denitrification and phosphorus removal of municipal sewage by half shortcut nitrification and anaerobic ammonium oxidation |
| CN103011399A (en) * | 2012-12-18 | 2013-04-03 | 中山大学 | Novel anammox biomembrane reactor and biological denitrifying method thereof |
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| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |