Method for strengthening anaerobic organism phosphorus removal of waste water

An anaerobic biology and wastewater technology, applied in chemical instruments and methods, water pollutants, anaerobic digestion treatment, etc., can solve problems such as complex process, achieve simple process, achieve standard discharge, and obvious phosphorus removal effect Effect

Inactive Publication Date: 2018-06-19
KUNMING UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The existing application CN104828939 A discloses "a method for multi-stage phosphorus removal and production of phosphine from phosphorus-containing organic wastewater". The method includes configuring an anaerobic reactor, a microbial fuel cell, and a microbial electrolytic cell. The two reaction units of oxygen fermentation and microbial electrolytic cell realize multi-stage phosphorus removal to produce phosphine. While improving the efficiency of phosphorus removal, the purity of the produced phosphine is relatively high, but

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0015] Example 1

[0016] Put 1.5L of filtered domestic sewage into a biochemical reactor with an effective volume of 3L, and inoculate the sludge from the anaerobic tank of a municipal sewage treatment plant. The mixed liquid sludge concentration in the reactor is 3120mg / L and the total phosphorus content is 435mg / L; Set up two parallel tests, one of which is administered with exogenous agent Na 2 S 2 O 5 , The dosage is 0.7g / L, and Na is added to the reactor at one time 2 S 2 O 5 Afterwards, stir and mix well, adjust the pH of the mixture to 7.0, pour nitrogen into the reactor to make the dissolved oxygen content in the reactor 0.01mg / L, and then close the reactor; the other group is a blank control, no exogenous agent is added, adjustment The pH value of the mixture reached 7.0. After nitrogen gas was introduced for 3 minutes, the dissolved oxygen content in the reactor was 0.01 mg / L. The reactor was closed; both reactors were placed in a constant temperature water bath at 15°...

Example Embodiment

[0017] Example 2

[0018] Put 1.5L of filtered domestic sewage into a biochemical reactor with an effective volume of 3L, and inoculate the sludge from the anaerobic tank of the municipal sewage treatment plant. The sludge concentration of the mixed liquid in the reactor is 14580mg / L and the total phosphorus content is 2247mg. / L; Set up two parallel tests, one of which is administered with exogenous agent Na 2 S 2 O 5 , The dosage is 1.3g / L, mix well after 2 dosages, adjust the pH value of the mixture to 8.0, and pour nitrogen into the reactor to make the dissolved oxygen content in the reactor 0.05mg / L, in a constant temperature water bath at 25℃ Under the conditions of anaerobic digestion for 120h, the rest of the operation process is the same as in Example 1. The blank control group does not add exogenous agents, and the environmental conditions such as digestion time and temperature are the same as the test group; the total phosphorus removal rate of the blank control group i...

Example Embodiment

[0019] Example 3

[0020] Put 1.5L of filtered domestic sewage into a biochemical reactor with an effective volume of 3L, and inoculate the anaerobic tank sludge of a municipal sewage treatment plant. The mixed liquid sludge concentration in the reactor is 4330mg / L and the total phosphorus content is 648mg / L; Set up two parallel tests, one of which is administered with exogenous agent Na 2 SO 3 , The dosage is 1.5g / L, after one-time dosing, adjust the pH of the mixed solution to 8.0, and add nitrogen to make the dissolved oxygen content in the reactor 0.1mg / L. Oxygen digestion was performed for 100 hours, and the rest of the operation process was the same as in Example 1. The blank control group was not added with exogenous agents, and the environmental conditions such as digestion time and temperature were the same as those of the test group. The total phosphorus removal rate in the blank control group was 0.3%, and the total phosphorus removal rate in the wastewater of the tes...

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Abstract

The invention discloses a method for strengthening anaerobic organism phosphorus removal of waste water. The method comprises the following steps: adding exogenous medicaments such as Na2S2O5 and/or Na2SO3 into phosphorus-containing waste water, mixing uniformly, adjusting the pH value of the waste water to be 6.0 to 8.0, carrying out an anaerobic digestion reaction at the temperature of 15 to 45DEG C, releasing hydrogen phosphide from total phosphorus inside the waste water under the metabolism effect of anaerobic microorganisms so as to be removed from a water body, so that the load of thetotal phosphorus entering an aerobiotic stage in the waste water biochemical treatment system is obviously reduced. The method is simple and practicable, and is obvious in phosphorus removal effect.

Description

technical field [0001] The invention relates to a method for anaerobic biological phosphorus removal of wastewater, in particular to a method for strengthening anaerobic biological phosphorus removal of wastewater by adding exogenous medicaments, and belongs to the technical field of wastewater biological treatment. Background technique [0002] At present, eutrophication has caused serious negative impacts on natural water bodies, such as "algae blooms" in lakes and "red tides" in coastal waters, which occur from time to time and become more severe, which not only endangers agriculture, fishery, tourism and many other industries, but also affects the sanitation of drinking water. and food safety constitute a huge threat. Phosphorus is the main limiting substance that causes eutrophication in water. Only when the concentration of phosphorus in water is high, nitrogen is the limiting substance. It can be seen that the effective removal of phosphorus in wastewater is far more...

Claims

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Application Information

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IPC IPC(8): C02F3/28
CPCC02F1/58C02F1/70C02F3/28C02F2101/105C02F2209/02C02F2209/06
Inventor 刘树根苏福家牛晓君宁平
Owner KUNMING UNIV OF SCI & TECH
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