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Anaerobic-oxidation ditch-SACR combined deep denitrification system and process for sewage with high ammonia nitrogen content

A deep denitrification and oxidation ditch technology, applied in aerobic and anaerobic process treatment, aerobic process treatment, anaerobic digestion treatment and other directions, can solve the problem of limited effect of nitrogen removal, volume and dissolved oxygen concentration difficult to accurately control and other problems, to achieve the effect of low upgrading and transformation cost and reducing process cost

Active Publication Date: 2020-01-17
SHANDONG JIANZHU UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The traditional oxidation ditch process mainly uses the inhomogeneity of dissolved oxygen distribution in the ditch, and through reasonable design, it can generate alternate cycles of aerobic zone and anoxic zone in the ditch, so as to achieve the purpose of denitrification. Its biggest advantage is The removal of organic matter and total nitrogen can be achieved in the same ditch without the need for an external carbon source, but the disadvantages are also obvious. It is difficult to accurately control the respective volumes and dissolved oxygen concentrations of the aerobic zone and the anoxic zone in the same ditch. Therefore, the effect on nitrogen removal is limited

Method used

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  • Anaerobic-oxidation ditch-SACR combined deep denitrification system and process for sewage with high ammonia nitrogen content
  • Anaerobic-oxidation ditch-SACR combined deep denitrification system and process for sewage with high ammonia nitrogen content
  • Anaerobic-oxidation ditch-SACR combined deep denitrification system and process for sewage with high ammonia nitrogen content

Examples

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Embodiment 1

[0031] Example 1: An anaerobic-oxidation ditch-SACR combined deep denitrification system for high ammonia nitrogen sewage

[0032] Such as figure 1 As shown, an anaerobic-oxidation ditch-SACR combined deep denitrification system for high-ammonia nitrogen sewage, including a regulating tank, anaerobic reactor, oxidation ditch reactor, sedimentation tank, intermediate tank and SACR reaction connected in sequence through pipelines device; the outlet end of the regulating pool is connected with the inlet end of the intermediate pool through a pipeline; the pipeline is provided with a water pump for regulating the flow rate; the intermediate pool is provided with water quality detection equipment; the SACR reactor is provided with a pH detection device Instrument, DO detector, ORP detector, aeration equipment and agitator; also includes PLC controller, the PLC controller is respectively connected with water quality testing equipment, PH detector, DO detector, ORP detector, aeration...

Embodiment 2

[0036] Example 2: An anaerobic-oxidation ditch-SACR combined deep denitrification process for high-ammonia nitrogen sewage

[0037] The technology in this embodiment is based on the system in embodiment 1, and the anaerobic reactor is a UASB reactor; the volume of the oxidation ditch reactor=(high ammonia nitrogen sewage raw water total nitrogen concentration value / 50 * 30 * sewage per hour output value) m3; the unit of total nitrogen concentration in high ammonia nitrogen sewage raw water is mg / L, and the unit of sewage output per hour is m 3 ;SACR volume = (total nitrogen concentration value of high ammonia nitrogen sewage raw water / 50×20×hourly sewage production value) m 3 ; The unit of total nitrogen concentration in high ammonia nitrogen sewage raw water is mg / L, and the unit of sewage output per hour is m 3 .

[0038] An anaerobic-oxidation ditch-SACR combined high ammonia nitrogen sewage deep denitrification process, comprising the following steps:

[0039] (1) High ...

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Abstract

The invention provides an anaerobic-oxidation ditch-SACR combined type deep denitrification system and process for sewage with high ammonia nitrogen content. According to the process, high-ammonia-nitrogen sewage firstly enters an anaerobic reactor for removal of most of organic matters; the effluent of the anaerobic reactor enters an oxidation ditch reactor for removal of biochemical organic matters, ammonia nitrogen and a part of total nitrogen in the sewage in the oxidation ditch; the effluent of the oxidation ditch reactor enters an intermediate water tank; under the control of water quality detection equipment and a PLC, a part of raw water is introduced into the intermediate water tank to adjust the carbon-nitrogen ratio of the sewage; and then the effluent enters an SACR reactor. Byutilizing the characteristics of denitrifying bacteria and by regulating and controlling the SACR reactor via a PH / DO / ORP detector and the PLC, the sewage is accurately subjected to pre-denitrification / nitrification / endogenous denitrification, so deep denitrification is realized; meanwhile, an external carbon source is not needed, and the treatment cost of the process is low; and for a built sewage treatment facility adopting an oxidation ditch process, the process with the above technical scheme can be implemented only by additionally arranging the intermediate water tank and the SACR reactor, so upgrading and reconstruction cost is low.

Description

technical field [0001] The invention relates to the technical field of sewage treatment, in particular to an anaerobic-oxidation ditch-SACR combined deep denitrification system and process for high ammonia nitrogen sewage. Background technique [0002] At present, with the strengthening of environmental protection awareness, the strengthening of environmental pollution control and the development of environmental protection technology, water pollution has been relatively effectively controlled initially. However, the standard discharge of high-ammonia-nitrogen wastewater common in industrial production is still an urgent problem. The problem. High ammonia nitrogen wastewater mainly comes from chemical fertilizer, petrochemical, aquaculture, garbage treatment and other industries. In terms of high ammonia nitrogen wastewater treatment, it is not only necessary to pursue the technical indicators of efficient denitrification, but also to consider reducing energy consumption, sa...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/14C02F101/16
CPCC02F3/02C02F3/28C02F3/30C02F3/302C02F2001/007C02F2101/16C02F2209/005C02F2209/04C02F2209/06C02F2209/22
Inventor 王凯武道吉谭凤训罗从伟成小翔李宏业田宇
Owner SHANDONG JIANZHU UNIV
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