Method and system for biological nitrogen and phosphorus removal of sewage

A technology for denitrification and dephosphorization and biological sewage treatment, which is applied in the field of biological denitrification and dephosphorization of sewage, and can solve the problems such as difficulty in achieving high standard discharge in sewage treatment plants, limited capacity for deep denitrification and dephosphorization, and unstable denitrification and dephosphorization process. , to achieve the effect of reducing aeration energy consumption, wide range of water quality, convenient operation and maintenance

Active Publication Date: 2022-03-22
TONGJI UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This kind of traditional biological treatment technology is mature and easy to operate, but it often faces the problem of unstable denitrification and phosphorus removal process and limited deep nitrogen and phosphorus removal capacity
In particular, my country's sewage treatment plants often face low COD in sewage. Since the denitrification process needs to consume carbon sources, when the carbon source in sewage is insufficient, the addition of carbon source not only increases the treatment cost, but also may bring the risk of excessive COD in the effluent.
Therefore, as nitrogen and phosphorus discharge standards become increasingly stringent, it becomes increasingly difficult for sewage treatment plants to achieve high standards of discharge

Method used

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  • Method and system for biological nitrogen and phosphorus removal of sewage

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Effect test

Embodiment 1

[0160] The system of the sewage biological denitrification and dephosphorization used in the embodiment is as figure 1 As shown, follow the steps below:

[0161] (1) The sewage flow is pretreated sequentially through the interception device 1001 and the sand settling device 1002, and the initial total nitrogen and total phosphorus concentrations of the sewage are measured. The total nitrogen concentration is 40 mg / L, and the total phosphorus concentration is 10 mg / L; wherein, the interception device 1001 is a grid, and the sand settling device 1002 is a swirling flow sand settling device;

[0162] (2) The pretreated sewage flows through the anaerobic device 1, the anoxic device 2, the aerobic device 3, the aerobic device 4 and the membrane-based biofilm device 6 for anaerobic treatment, anoxic treatment, and aerobic treatment in sequence. , anaerobic treatment and membrane-based biological treatment; in anaerobic treatment, the oxidation-reduction potential is -120mV, and the...

Embodiment 2

[0167] The system of the sewage biological denitrification and dephosphorization used in the embodiment is as figure 1 As shown, follow the steps below:

[0168] (1) The sewage flow is pretreated sequentially through the interception device 1001 and the sand settling device 1002, and the initial total nitrogen concentration of the measured sewage is 41 mg / L, and the total phosphorus concentration is 10 mg / L; wherein, the interception device 1001 is a grid, and the sand settling The device 1002 is a cyclone sand settling device;

[0169] (2) The pretreated sewage flows through the anaerobic device 1, the anoxic device 2, the aerobic device 3, the aerobic device 4 and the membrane-based biofilm device 6 for anaerobic treatment, anoxic treatment, and aerobic treatment in sequence. , anaerobic treatment and membrane-based biological treatment; in anaerobic treatment, the redox potential is -100mV, and the hydraulic retention time is 1h; in anoxic treatment, the dissolved oxygen c...

Embodiment 3

[0174] The system of the sewage biological denitrification and dephosphorization used in the embodiment is as figure 1 As shown, follow the steps below:

[0175] (1) The sewage flow is pretreated sequentially through the interception device 1001 and the sand settling device 1002, and the initial total nitrogen concentration of the measured sewage is 42 mg / L, and the total phosphorus concentration is 11 mg / L; wherein, the interception device 1001 is a grid, and the sand settling The device 1002 is a cyclone sand settling device;

[0176] (2) The pretreated sewage flows through the anaerobic device 1, the anoxic device 2, the aerobic device 3, the aerobic device 4 and the membrane-based biofilm device 6 for anaerobic treatment, anoxic treatment, and aerobic treatment in sequence. , anaerobic treatment and membrane-based biological treatment; in anaerobic treatment, the oxidation-reduction potential is -150mV, and the hydraulic retention time is 1.5h; in anoxic treatment, the di...

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Abstract

The invention relates to the field of water treatment, in particular to a method and system for biological denitrification and dephosphorization of sewage. The method comprises the following steps: 1) performing anaerobic treatment on the water body to be treated; 2) performing anoxic treatment on the water body obtained from the anaerobic treatment; 3) performing aerobic treatment on the water body obtained from the anoxic treatment; The water body is subjected to anaerobic treatment; 5) Part of the supernatant of the water body obtained from the oxygen elimination treatment is returned to step 2) for anoxic treatment; 6) Part of the supernatant of the water body obtained from the oxygen elimination treatment is subjected to membrane-based biological treatment; 7) Precipitate the mud-water mixture in the lower layer of the water obtained from the aerobic treatment; 8) return part of the water obtained from the membrane-based biological treatment to step 1) for anaerobic treatment; 9) return part of the water obtained from the membrane-based biological treatment to step 3 ) for aerobic treatment. The invention has good removal effect of total nitrogen and total phosphorus pollutants, simple and convenient operation, low energy consumption, and stable and up-to-standard discharge.

Description

technical field [0001] The invention relates to the field of water treatment, in particular to a method and system for biological denitrification and dephosphorization of sewage. Background technique [0002] With the rapid development of my country's economy, the problem of water pollution is becoming more and more serious. In 2018, the total amount of sewage generated in my country reached 70.8 billion tons, of which domestic sewage accounted for 74.4%, becoming the main source of sewage. Domestic sewage is often rich in nitrogen and phosphorus pollutants. In 2015, the total discharge of ammonia nitrogen in my country's urban domestic sewage reached 1.341 million tons, accounting for 60% of the total discharge of all types of sewage. Therefore, the problem of nitrogen and phosphorus removal is still a major challenge for my country's sewage treatment industry. Therefore, efficient removal of nitrogen and phosphorus from sewage is still a major challenge for my country's...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F3/30C02F101/16C02F101/10
CPCC02F3/308C02F3/30C02F2101/105C02F2101/16
Inventor 郑雄杨澜陈银广吴瑒武婧
Owner TONGJI UNIV
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