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Biochemical landfill leachate treatment process

A landfill leachate and treatment process technology, which is applied in the field of biochemical landfill leachate treatment process, can solve the problems of single electrolyte in the electrolysis method, the effluent cannot meet the discharge standard, and the treatment efficiency of the ozone oxidation method is limited.

Pending Publication Date: 2019-10-22
章俭
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Among them, the common technologies for removing ammonia nitrogen are deammonization tower, nitrification and denitrification deammonization biofilm, and electrolysis. The metabolism of microbial flora is greatly affected by changes in water quality, which in turn affects the treatment efficiency. However, the electrolysis method is limited in scope of use because of its single electrolyte and high energy consumption for electrolysis.
[0004] The common technical methods for deep oxidation to remove COD include the Fenton method and the ozone oxidation method. The Fenton method needs to be carried out in a strong acid environment, which requires high equipment materials, and at the same time produces more physical and chemical sludge, and the treatment cost is higher. ; and because of its limited treatment efficiency and relatively high energy consumption, the use of the ozone oxidation method is also subject to certain restrictions.
[0005] Biochemical treatment after proper pretreatment is also one of the landfill leachate treatment methods, but the traditional activated sludge microbial agent may have insufficient impact resistance or low metabolic efficiency, resulting in post-treatment The effluent does not meet the new discharge standards

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0044] A biochemical landfill leachate treatment process in this embodiment comprises the following steps:

[0045] (1) Pass the landfill leachate with a COD concentration of 20000mg / L, an ammonia nitrogen concentration of 2100mg / L, and a B / C of 0.15 into the pH adjustment tank. Filtration in a canister to remove most of the solid particles;

[0046] (2) Pass the landfill leachate after filtering into the coagulation tank, add polyaluminium chloride (final concentration is 0.1%) in the coagulation tank, mix, and treat insoluble matter (partial COD material and most of macromolecule insoluble After the precipitation, the effluent of the coagulation tank is passed into the electrolytic cell;

[0047] (3) In the electrolyzer, under 3V voltage, utilize titanium alloy electrode and composite electrolyte to carry out electrolysis reaction 30min to the effluent of coagulation tank;

[0048] The composite electrolyte includes industrial sodium chloride, sodium hydroxide, sodium hypo...

Embodiment 2

[0054] A biochemical landfill leachate treatment process, comprising the following steps:

[0055] (1) Pass the landfill leachate with a COD concentration of 11000mg / L, an ammonia nitrogen concentration of 2300mg / L, and a B / C of 0.3 into the pH adjustment tank, adjust the pH of the landfill leachate to 9, and then pass it into the fine water filled with fillers. Filtration in a canister to remove most of the solid particles;

[0056] (2) Pass the filtered landfill leachate into the coagulation tank, add polyaluminum chloride (0.2% final concentration) in the coagulation tank, mix well, and wait for the insoluble matter (partial COD material and most macromolecule insoluble matter) ) after precipitation, the coagulation pool effluent is passed into the electrolytic cell;

[0057] (3) In the electrolyzer, under 4V voltage, utilize titanium alloy electrode and composite electrolyte to carry out electrolysis reaction 25min to coagulation pool effluent;

[0058] The composite ele...

Embodiment 3

[0062] A biochemical landfill leachate treatment process in this embodiment comprises the following steps:

[0063] (1) Pass the landfill leachate with a COD concentration of 5000mg / L, an ammonia nitrogen concentration of 1500mg / L, and a B / C of 0.1 into the pH adjustment tank. Filtration in a canister to remove most of the solid particles;

[0064] (2) Pass the filtered landfill leachate into the coagulation tank, add polyaluminum chloride (0.05% final concentration) in the coagulation tank, mix evenly, and make the insolubles (partial COD substances and most of the macromolecular insolubles) )precipitation;

[0065] (3) Add a catalyst to the effluent of the coagulation tank, and use a dissolved air pump to send the ozone and the effluent of the coagulation tank mixed with the catalyst into the catalytic ozonation reaction tank at the same time. The mass ratio of ozone to the effluent of the coagulation tank is 13.82g: 1t ; Under the irradiation of ultraviolet light, the eff...

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PUM

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Abstract

The invention discloses a biochemical landfill leachate treatment process, which comprises: adjusting the pH value of landfill leachate with an ammonia nitrogen concentration of more than 2000 mg / L and B / C of less than 0.2 to 8-9, and filtering; precipitating the filtered landfill leachate in a coagulation pool; carrying out electrolysis treatment on the effluent of the coagulation pool for 20-30min in an electrolysis tank with a voltage of 3-5 V by using a titanium alloy electrode and a composite electrolyte, wherein the composite electrolyte comprises sodium hydroxide and hydrochloric acidfor adjusting the pH value of the effluent of the coagulation pool to 6-9, sodium chloride for adjusting the TDS value of the effluent of the coagulation pool to more than or equal to 6000 mg / L, and sodium hypochlorite for adjusting the redox potential of the effluent of the coagulation pool to more than -300 mV; and sequentially carrying out catalytic ozone oxidation treatment and biochemical treatment on the effluent of the electrolysis tank. According to the present invention, with the process, by adjusting the TDS value and the redox potential, the direct oxidation effect and the indirectoxidation effect in the electrolysis reaction are optimally balanced so as to obtain the optimal ammonia nitrogen and COD removal effect at low energy consumption.

Description

technical field [0001] The invention belongs to the technical field of wastewater treatment, and in particular relates to a biochemical landfill leachate treatment process. Background technique [0002] Landfill leachate refers to the moisture contained in the garbage itself in the landfill, the rain and snow water and other moisture entering the landfill, deducting the saturated water holding capacity of the garbage and the covering soil, and passing through the garbage layer and the covering soil. A high concentration of organic wastewater. Its characteristics are: complex water quality components, high COD and BOD concentrations, high ammonia nitrogen concentration, and many types of organic matter; based on the above characteristics, the treatment of landfill leachate needs to combine various technical means to meet the requirements of the new discharge standards. [0003] Among them, the common technologies for removing ammonia nitrogen are deammonization tower, nitrif...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/14C02F101/20C02F101/16C02F101/30
CPCC02F1/001C02F1/46104C02F1/5245C02F1/5281C02F1/66C02F1/725C02F1/78C02F3/1215C02F9/00C02F2001/46133C02F2101/16C02F2101/20C02F2101/30C02F2203/006C02F2209/08C02F2209/14C02F2301/08
Inventor 万法磊阮竹成马晓磊许剑飞许翔宇
Owner 章俭
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