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Start and control method for partial nitrosation

A control method and nitrification technology, applied in chemical instruments and methods, anaerobic digestion treatment, biological water/sewage treatment, etc., can solve the problem of difficult maintenance of sludge concentration in the system, unstable effluent nitrogen ratio, and difficulty in continuous flow operation and other problems, to achieve the effects of low energy consumption of aeration and fluidization, long-term stable operation, and adjustable volume load

Active Publication Date: 2018-04-06
苏州诺津环保科技有限公司
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Problems solved by technology

[0030] In order to solve the problems in the prior art that the nitrosation process is difficult to operate continuously, the ratio of effluent nitrogen is unstable, the long-term operation is easy to convert to the whole process of nitrification, and the sludge concentration in the system is difficult to maintain, etc., the present invention proposes a partial nitrosation start-up and Control method, which has the advantages of continuous operation, stable treatment effect, long-term operation stability, precise control of effluent nitrogen ratio, convenient management and maintenance, etc.

Method used

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Embodiment 1

[0060] The reactor tank capacity is 10m 3 , using a specific surface area of ​​700m 2 / m 3 Suspended carrier, the specific gravity of the suspended carrier before hanging on the film is 0.965, and the void ratio is >95%; the reactor is not equipped with sludge return, and the concentration of suspended sludge in the reactor is always <0.5g / L during the continuous flow operation; the influent is domestic sewage After decarbonization, the influent BOD is 10±3mg / L, TN is 55±6mg / L, ammonia nitrogen is 50±5mg / L, BOD:TN<0.2, influent SS<20mg / L, water temperature is 15±5mg / L 3℃;

[0061] 1) The nitrification is started, and the suspension carrier is filled for 4m 3 , the filling rate is 40%, the DO is controlled at 4-5mg / L, the activated sludge of the sewage plant is inoculated at 4g / L, and each cycle runs for 10h. After precipitation, the supernatant is discharged, and the reactor is emptied after 10 cycles of operation. Sludge, start continuous water inflow and aeration, initia...

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Abstract

The invention discloses a start and control method for partial nitrosation, belongs to the field of sewage treatment and solves the problems that start is not easy, the nitrite accumulation effect isunstable and the like in the conventional nitrosation process. The method comprises the steps as follows: nitration start, intermittent aeration start, nitrite accumulation rate control, ammonia oxidation rate control, stable operation control of nitrosation and the like. The final ammonia nitrogen oxidation rate is stabilized at 55%-60%, nitrite accumulation rate is stabilized to be higher than or equal to 92%, the ammonia nitrogen removal surface load is higher than or equal to 0.60 gN / (m<2>.d), and requirements of subsequent anaerobic ammonia oxidation for nitrogen are met. The partial nitrosation effect is stable, the ammonia nitrogen oxidation load is high, the occupied area is saved, operation is simple, and running is reliable; compared with the traditional process, the method can realize selection and elimination of microorganisms and prevent long-term operation instability; the oxygen utilization rate is high, and aeration fluidization energy consumption is low.

Description

technical field [0001] The invention belongs to the field of sewage treatment, and particularly relates to a method for starting and controlling partial nitrosation. Background technique [0002] Anaerobic Ammonium Oxidation (Anaerobic Ammonium Oxidation, referred to as ANAMMOX), is based on NO 2 - -N is the electron acceptor, CO 2 As an inorganic carbon source, under anaerobic conditions, the NH 4 + -N is oxidized to N 2 biological process. Compared with the traditional nitrification-denitrification process, the ANAMMOX process has the advantages of saving 50% of the aeration amount and 100% of the organic carbon source. [0003] Since the anaerobic ammonia oxidation process requires ammonia nitrogen and nitrite nitrogen in a ratio of 1:1.31 as substrates, a pretreatment process is required to partially oxidize ammonia nitrogen to nitrite nitrogen without generating nitrate nitrogen, that is, partial nitrosation Process, also known as nitrosation process, short-range...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F3/28
CPCC02F3/286
Inventor 王金龙董子为其他发明人请求不公开姓名
Owner 苏州诺津环保科技有限公司
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