Nitrogen and phosphorus removal system and method for treating low-carbon-nitrogen-ratio domestic wastewater by A2O-MBBR (anaerobic-anoxic-oxic-moving bed biofilm reactor) combined chemical process

A low-carbon nitrogen ratio, domestic sewage technology, applied in chemical instruments and methods, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc., can solve problems such as poor denitrification and phosphorus removal, and reduce carbon emissions The competition for the source, the guarantee of anaerobic state, the effect of high removal rate

Inactive Publication Date: 2014-12-24
HARBIN INST OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] The purpose of the present invention is to solve the problem that the denitrification and dephosphorization effect of the existing water purification process for processing low-carbon nitrogen ratio domestic sewage is poor, and to provide A 2 Nitrogen and phosphorus removal system and method for treating domestic sewage with low carbon-to-nitrogen ratio by O-MBBR combined with chemical method

Method used

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  • Nitrogen and phosphorus removal system and method for treating low-carbon-nitrogen-ratio domestic wastewater by A2O-MBBR (anaerobic-anoxic-oxic-moving bed biofilm reactor) combined chemical process
  • Nitrogen and phosphorus removal system and method for treating low-carbon-nitrogen-ratio domestic wastewater by A2O-MBBR (anaerobic-anoxic-oxic-moving bed biofilm reactor) combined chemical process
  • Nitrogen and phosphorus removal system and method for treating low-carbon-nitrogen-ratio domestic wastewater by A2O-MBBR (anaerobic-anoxic-oxic-moving bed biofilm reactor) combined chemical process

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specific Embodiment approach 1

[0033] Specific implementation mode one: this implementation mode A 2 The nitrogen and phosphorus removal system of O-MBBR combined with chemical method to treat domestic sewage with low carbon-to-nitrogen ratio includes A 2 O reactor 2, medium sedimentation tank 3, MBBR reactor 4, chemical phosphorus removal tank 5 and final sedimentation tank 6, where A 2 O reactor 2 is further divided into anaerobic zone a, anoxic zone b and aerobic zone c, anoxic zone b is sandwiched between anaerobic zone a and aerobic zone c, and aerobic zone c is provided with an aerobic zone gas device, regulating pool 1 passes through No. 1 water pipe 11 and A 2 The water inlet of the anaerobic zone a in the O reactor 2 is connected, the water outlet on the top of the anaerobic zone a is connected to the water inlet on the top of the chemical phosphorus removal tank 5 through the second water pipe 12, and the water outlet on the top of the aerobic zone c passes through No. 3 water pipe 13 communicat...

specific Embodiment approach 2

[0036] Specific implementation mode two: the difference between this implementation mode and specific implementation mode one is that in A 2 Stirring devices are installed in the anoxic zone b in the O reactor 2 and in the chemical phosphorus removal tank 5 .

specific Embodiment approach 3

[0037] Embodiment 3: This embodiment differs from Embodiment 1 or Embodiment 2 in that a water inlet pump is provided in the No. 1 water pipe 11 , and a nitrification liquid return pump is provided in the No. 6 water pipe 16 .

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Abstract

The invention discloses a nitrogen and phosphorus removal system and a method for treating low-carbon-nitrogen-ratio domestic wastewater by an A2O-MBBR (anaerobic-anoxic-oxic-moving bed biofilm reactor) combined chemical process, belongs to the field of city wastewater treatment and regeneration, and solves the problem of poor nitrogen and phosphorus removal effect of an existing water purification process for treating the low-carbon-nitrogen-ratio domestic wastewater. The nitrogen and phosphorus removal system comprises an A2O reactor, an intermediate settling pond, an MBBR, a chemical phosphorus removal pond and a final settling pond. According to the method, the MBBR is arranged behind the intermediate settling pond, a nitrifying process is finished, and an inorganic metal salt agent is added into the chemical phosphorus removal pond; all active sludge subjected to standing and settling by the chemical phosphorus removal pond flows back to the A2O reactor, so that the number of phosphorus-accumulating bacteria cannot be reduced; then, electron acceptors are provided for the denitrifying effect and the anoxic phosphorus uptake effect by flowing part of outlet water of the MBBR back to an anoxic zone of the A2O reactor. By the nitrogen and phosphorus removal system, the removal rate of ammonia nitrogen and total phosphorus can reach more than 90%.

Description

technical field [0001] The invention belongs to the field of urban sewage treatment and regeneration, and in particular relates to a treatment system and method for simultaneously and efficiently removing organic matter, nitrogen and phosphorus in domestic sewage with a low carbon-to-nitrogen ratio. Background technique [0002] In recent years, with the rapid development of the economy and the continuous improvement of people's living standards, the dietary structure has changed, causing the nitrogen content in urban domestic sewage to increase sharply, and the phenomenon of low carbon-nitrogen ratio in domestic sewage has appeared, making the nitrogen removal of sewage at the same time Phosphorus removal is more difficult. Coupled with the increasingly stringent national sewage discharge standards, many traditional processes have failed to meet the nitrogen and phosphorus standards in the effluent. It is imminent to find an efficient method for nitrogen and phosphorus remo...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/14
Inventor 李相昆孙豆豆朱昆
Owner HARBIN INST OF TECH
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