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A Remediation System for Groundwater Contaminated by Ammonia Nitrogen-Inorganic Phosphorus

A technology for complex pollution and restoration systems, applied in the treatment of polluted groundwater/leachate, water pollutants, and multi-stage treatment of water/sewage, etc., can solve the problems of increasing the cost of water treatment per ton, threats to human health, death, etc. Achieve the effect of reducing the frequency of gas flushing and operation and maintenance costs, avoiding premature saturation failure, and reducing the load of influent water

Active Publication Date: 2020-08-04
CHINESE ACAD OF ENVIRONMENTAL PLANNING
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Ammonia nitrogen and inorganic phosphorus in groundwater will cause a rapid decrease in the concentration of dissolved oxygen in the water, causing eutrophication, causing obvious toxicity and even death to aquatic organisms, and changing the chemical conditions of groundwater and microbial colony structure; at the same time, it will increase the number of water purification plants. The amount of disinfectant not only increases the cost per ton of water treatment, but also produces a large number of carcinogenic, teratogenic and mutagenic disinfection by-products, which pose a serious threat to human health
[0003] In domestic sewage and industrial wastewater treatment, A 2 O method, SBR method, oxidation ditch method and other traditional biological methods have been widely studied and widely used in the simultaneous removal of ammonia nitrogen and inorganic phosphorus, but the effect of simultaneous removal of ammonia nitrogen and inorganic phosphorus still needs to be improved

Method used

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  • A Remediation System for Groundwater Contaminated by Ammonia Nitrogen-Inorganic Phosphorus
  • A Remediation System for Groundwater Contaminated by Ammonia Nitrogen-Inorganic Phosphorus
  • A Remediation System for Groundwater Contaminated by Ammonia Nitrogen-Inorganic Phosphorus

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preparation example Construction

[0072] The preparation method of the above-mentioned composite adsorption material includes: crushing zeolite, bentonite and coal cinder to 200-500 mesh respectively; weighing the crushed raw materials according to the above weight ratio and stirring and mixing; putting the mixture into a granulator to make 2 ~4mm particles; drying at 50-60°C for 5-10 hours; roasting at 500-700°C for 3-4 hours.

[0073] Further, the length:width:height ratio of the anaerobic pool is 1~3:1~1.5:4~5;

[0074] The length: width: height ratio of the anoxic pool is 1~3:1~1.5:4~5;

[0075] The length: width: height ratio of the aerobic pool is 1~3:1~1.5:4~5;

[0076] The length: width: height ratio of the sedimentation tank is 1~3:1~1.5:4~5;

[0077] The length:width:height ratio of the adsorption pool is 1~3:1~1.5:4~5.

[0078] Each pool body is in the shape of a cuboid, which can be a glass reinforced plastic structure, a concrete structure or a steel structure.

[0079] Further, it also includes...

Embodiment 1

[0107] This embodiment provides a repair system for ammonia nitrogen-inorganic phosphorus compound polluted groundwater, such as figure 1 As shown, it is composed of anaerobic pond 1, anoxic pond 2, aerobic pond 3, sedimentation pond 4 and adsorption pond 5, anaerobic pond 1, anoxic pond 2, aerobic pond 3, sedimentation pond 4 and adsorption pond 5 The hydraulic retention time ratio is 1:1:1:1:1, and the volume ratio is 1:1:1:1:1; each pool is in the form of a cuboid, with a glass fiber reinforced plastic structure, and the length h1 of the first diversion area is the same as the The ratio of the length H1 of the anaerobic tank is 5:20; the ratio of the length h2 of the second diversion zone to the length H2 of the anoxic tank is 5:20; the length h3 of the third diversion zone is compared to the length h3 of the anoxic tank The ratio of the length H3 of the aerobic tank is 5:20; the ratio of the length h4 of the fourth diversion zone to the length H4 of the sedimentation tank ...

Embodiment 2

[0115] This embodiment provides a repair system for ammonia nitrogen-inorganic phosphorus compound polluted groundwater, such as figure 1 As shown, it is composed of anaerobic pond 1, anoxic pond 2, aerobic pond 3, sedimentation pond 4 and adsorption pond 5, anaerobic pond 1, anoxic pond 2, aerobic pond 3, sedimentation pond 4 and adsorption pond 5 The hydraulic retention time ratio is 1:1:1:1:1, and the volume ratio is 1:1:1:1:1. Each pool body is a rectangular parallelepiped and has a glass fiber reinforced plastic structure. The ratio of the length h1 of the first diversion area to the length H1 of the anaerobic pool is 6:20; The ratio of the length H2 of the third diversion zone is 6:20; the ratio of the length h3 of the third diversion zone to the length H3 of the aerobic tank is 6:20; the length h4 of the fourth diversion zone and the length of the sedimentation tank The ratio of the length H4 is 6:20; the ratio of the length h5 of the fifth diversion area to the length...

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Abstract

The invention discloses a repair system of ammonia nitrogen-inorganic phosphorus composite polluted underground water. The repair system comprises an anaerobic tank, an anoxic tank, an aerobic tank, asedimentation tank and an adsorption tank which are sequentially arranged, wherein the hydraulic retention time ratio of the tanks is (1-2):(1-2):(1-2):(1-2):(1-2), and the volume ratio is (1-2):(1-2):(1-2):(1-2):(1-2). A filling frame is arranged in the anaerobic tank, and the filling frame is filled with a mixture of sawdust and scrap iron, wherein the mixture of the sawdust and the scrap ironaccounts for 10-15% of the effective volume of the anaerobic tank. According to the repair system, the removal rate of NH4<+>-N reaches 98.2-99.6%, the total nitrogen (TN) removal rate reaches 74.2-94.1%, the total phosphorus (TP) removal rate reaches 95.2-98.6%, the concentration of NH4<+>-N is less than 0.5 mg / L, the concentration of TP is less than 0.5 mg / L, and the defect of difficulty in reducing the phosphorus concentration of outflow water to 0.5 mg / L is solved.

Description

technical field [0001] The invention belongs to the field of water treatment, and in particular relates to a repair system for ammonia nitrogen-inorganic phosphorus compound polluted groundwater. Background technique [0002] Worldwide, the extensive application of chemical fertilizers, the return of human and livestock manure and urine, unreasonable sewage irrigation, the wanton discharge of industrial wastewater and domestic sewage, the lateral recharge of polluted river water, the exploitation or over-exploitation of groundwater, and garbage seepage The infiltration of the filtrate has caused the groundwater to be generally polluted by ammonia nitrogen and inorganic phosphorus, and its pollution has become a worldwide environmental and health problem. According to reports, countries such as China, the United States, Germany, India, Australia, the United Kingdom, and South Korea have found high concentrations of ammonia nitrogen and inorganic phosphorus in groundwater. For...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F9/14C02F101/10C02F101/16C02F103/06
CPCC02F1/28C02F1/52C02F3/02C02F3/2806C02F3/286C02F9/00C02F2101/105C02F2101/16C02F2103/06
Inventor 黄国鑫王夏晖朱文会季国华田梓何俊卢然宋志晓
Owner CHINESE ACAD OF ENVIRONMENTAL PLANNING
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