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An anaerobic-ao-sacr combined deep denitrification system and process for high ammonia nitrogen sewage

A deep denitrification, high ammonia nitrogen technology, applied in aerobic and anaerobic process treatment, aerobic process treatment, anaerobic digestion treatment and other directions, can solve the problem of increasing operating costs, low denitrification rate, and difficult denitrification rate Reaching 90% and other problems, achieving the effect of low upgrade cost and reduced process cost

Active Publication Date: 2020-06-30
SHANDONG JIANZHU UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the A / O process has an independent anoxic zone for denitrification, the denitrification rate is faster, but because it belongs to pre-denitrification, the denitrification rate is not high. To improve the denitrification efficiency, the internal circulation must be increased. In addition, the internal circulating liquid comes from the aeration tank and contains a certain amount of DO, which makes it difficult to maintain an ideal anoxic state in the anoxic zone, which affects the denitrification effect, and the denitrification rate is difficult to reach 90%.

Method used

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  • An anaerobic-ao-sacr combined deep denitrification system and process for high ammonia nitrogen sewage
  • An anaerobic-ao-sacr combined deep denitrification system and process for high ammonia nitrogen sewage
  • An anaerobic-ao-sacr combined deep denitrification system and process for high ammonia nitrogen sewage

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Embodiment 1

[0034] Example 1: An anaerobic-AO-SACR combined deep denitrification system for high ammonia nitrogen sewage

[0035] Such as figure 1 As shown, an anaerobic-AO-SACR combined high-ammonia-nitrogen sewage deep denitrification system includes a regulating tank, anaerobic reactor, AO reactor, sedimentation tank, intermediate pool and SACR reactor connected in sequence through pipelines; The outlet end of the adjustment pool is connected to the inlet end of the intermediate pool through a pipeline, and a water pump for regulating the flow is arranged on the pipeline; the intermediate pool is provided with water quality detection equipment; the SACR reactor is provided with a pH detector, a DO Detector, ORP detector, aeration equipment and agitator; also includes PLC controller, said PLC controller communicates with water quality testing equipment, PH detector, DO detector, ORP detector, aeration equipment and agitator respectively connect.

[0036] In this embodiment, the anaero...

Embodiment 2

[0039] Example 2: An anaerobic-AO-SACR combined deep denitrification process for high ammonia nitrogen sewage

[0040] 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 anoxic zone of the AO reactor=(high ammonia nitrogen sewage total nitrogen concentration value / 50 * 3 * per hour Sewage production value) m 3 , the volume of the aerobic zone = (total nitrogen concentration value of high ammonia nitrogen sewage / 50×12×hourly sewage production value) m 3 ;SACR volume = (total nitrogen concentration value of high ammonia nitrogen sewage / 50×20×hourly sewage production value) m 3 ; The unit of total nitrogen concentration in high ammonia nitrogen sewage is mg / L, and the unit of sewage production per hour is m 3 .

[0041] An anaerobic-AO-SACR combined high ammonia nitrogen sewage deep denitrification process, comprising the following steps:

[0042] (1) High ammonia nitrogen sewage enters the ...

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Abstract

The invention provides an anaerobic-AO-SACR combined high ammonia nitrogen sewage deep denitrification system and process. The high ammonia nitrogen sewage first enters the anaerobic reactor, removes most of the organic matter in the sewage, and enters the AO reactor after the water is discharged. The pre-denitrification denitrification is carried out in the oxygen zone, and the remaining organic matter is removed and the nitrification of ammonia nitrogen is carried out in the aerobic zone. After the water is released, it enters the intermediate pool. At the same time, through the control of water quality testing equipment and PLC controller, some raw water is introduced into the intermediate pool to adjust The carbon-to-nitrogen ratio of the sewage, and then, the effluent enters the SACR reactor, using the characteristics of denitrifying bacteria, and through the regulation of the SACR reactor through the PH / DO / ORP detector and the PLC controller, the sewage is accurately pre-denitrified ‑Nitrification‑Endogenous denitrification, thereby deep denitrification, at the same time, no external carbon source is required, the process cost is low, and, for the sewage treatment facilities that have been built using the AO process, it can be implemented only by adding intermediate water tanks and SACR reactors The process of the technical proposal has low upgrading and transformation costs.

Description

technical field [0001] The invention relates to the technical field of sewage treatment, in particular to an anaerobic-AO-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, saving energy a...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F9/14C02F101/16
CPCC02F3/30C02F3/28C02F3/02C02F2101/16C02F2001/007C02F2209/06C02F2209/22C02F2209/005C02F2209/04C02F3/302C02F3/006C02F3/2846C02F2209/44
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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