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Inactivated sludge-based anaerobic ammonium oxidation rapid enhancement starting method

A technology of anaerobic ammonium oxidation and activated sludge, applied in the field of wastewater biological treatment, can solve the problems of restricting the application of anammox process engineering, reducing the start-up speed of anammox process, and the long start-up period of anammox process , to achieve the effect of shortening the start-up time, stabilizing the removal efficiency and maintaining the removal efficiency

Active Publication Date: 2017-10-17
山东美泉环保科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] However, the growth of anammox bacteria is slow, the generation time is usually as long as 11 days, and the environmental conditions required for survival are very harsh, and the enrichment is extremely difficult, which leads to a long start-up period of the anammox process and restricts the anammox process. The engineering application of the process makes this technology basically in the stage of laboratory theoretical research and less industrial application.
In addition, at present, the enrichment of anammox bacteria generally adopts the form of inoculated activated sludge culture. During the enrichment culture process, the competition of coexisting bacteria hinders the transformation speed of anammox bacteria to dominant bacterial genera, which is very large. Reduced the start-up speed of the anammox process to a certain extent

Method used

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  • Inactivated sludge-based anaerobic ammonium oxidation rapid enhancement starting method
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Examples

Experimental program
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Effect test

Embodiment 1

[0035] A kind of anaerobic ammonium oxidation quick strengthening start-up method based on inactivated sludge, comprises steps as follows:

[0036] (1) Put the activated anaerobic granular sludge under the conditions of pressure 0.13MPa and temperature 120°C for 30 minutes to inactivate with high-pressure steam to obtain inactivated sludge, and then add it to the reaction zone of the upflow anaerobic reactor, At the same time, add active anaerobic ammonium oxidation sludge into the reactor and mix with inactivated sludge evenly. The mass ratio of active anaerobic ammonium oxidation sludge to inactivated sludge is 0.5:1, unit: g / kg. The moisture content of the mixed sludge is greater than or equal to 99wt%. The height range of the upflow anaerobic reactor is 75cm, the inner diameter range is 9cm, the effective volume is 6L, the top is provided with a three-phase separator, and the side wall is provided with sampling at different heights mouth, the bottom is paved with a gravel ...

Embodiment 2

[0051] A kind of anaerobic ammonium oxidation quick strengthening start-up method based on inactivated sludge, same as embodiment 1, the difference is:

[0052] In step (1), the activated aerobic granular sludge was inactivated by high-pressure steam for 30 minutes at a pressure of 0.3 MPa and a temperature of 122° C. to obtain inactivated sludge. Other treatment steps were carried out as in Example 1.

[0053] The upflow anaerobic reactor successfully started the sludge anammox reaction after 60 days of operation.

Embodiment 3

[0055] A kind of anaerobic ammonium oxidation quick strengthening start-up method based on inactivated sludge, same as embodiment 1, the difference is:

[0056] The mass ratio of activated anammox sludge to inactivated sludge in step (1) is: 0.8:1, unit: g / kg, and other treatment steps are carried out as in Example 1. The upflow anaerobic reactor successfully started the sludge anammox reaction after 54 days of operation.

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Abstract

The invention relates to an inactivated sludge-based anaerobic ammonium oxidation rapid enhancement starting method. The method comprises the following steps: feeding deactivated sludge and active anaerobic ammonium oxidation sludge into a reaction area of an upflow type anaerobic reactor and evenly mixing, wherein the mass ratio of the active anaerobic ammonium oxidation sludge to deactivated sludge (unit: g / kg) is (0.5-1.8):1; introducing to-be-treated waste water from the bottom of the upflow type anaerobic reactor by utilizing a peristaltic pump, so that the hydraulic retention time of the to-be-treated waste water in the upflow type anaerobic reactor lasts for 10 to 48 hours; and successfully starting anaerobic ammonium oxidation reaction of sludge after the upflow type anaerobic reactor runs for 40-70 days, thus realizing the high-efficiency removal of nitrogen in sewage. By utilizing the method, the starting time of the anaerobic ammonium oxidation technology can be effectively shortened, and the enrichment speed of anaerobic ammonium oxidation bacteria can be obviously accelerated; the starting time of the upflow type anaerobic reactor can be shortened by 9.3%; and after running for 200 days, the enrichment quantity of anaerobic ammonium oxidation bacteria in the upflow type anaerobic reactor inoculated with deactivated anaerobic granular sludge and active anaerobic ammonium oxidation sludge can be increased by 40.9%.

Description

technical field [0001] The invention relates to a quick and intensified start-up method for anaerobic ammonium oxidation based on inactivated sludge, belonging to the field of wastewater biological treatment. Background technique [0002] The traditional sewage treatment process (nitrification-denitrification process) cannot meet the high-standard sewage denitrification requirements due to high energy consumption, large floor area, low denitrification efficiency, and the need for additional organic carbon sources. The new sewage denitrification process Development and research have become research hotspots in the field of water environment protection in various countries. Anaerobic ammonium oxidation process is a new type of denitrification process that has developed vigorously in recent years. This process means that under anaerobic or anoxic conditions, anammox microorganisms use nitrite nitrogen as an electron acceptor to directly convert ammonia nitrogen into nitrogen g...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F3/28C02F101/16
CPCC02F3/2813C02F2101/16
Inventor 倪寿清王屿
Owner 山东美泉环保科技有限公司
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