A compound drinking water defluoridation process

A drinking water and process technology, applied in the direction of water pollutants, multi-stage water treatment, water/sewage treatment, etc., can solve the problems of short running time of equipment, less practical application, secondary pollution, etc., to ensure the turbidity of effluent water , Extensive practicability, good effect

Active Publication Date: 2017-01-11
JIANGSU YONGGUAN WATER & WASTERWATER EQUIP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The current defluoridation methods include membrane filtration, coagulation and adsorption filtration. Membrane filtration is mainly reverse osmosis and electrodialysis. Because the membrane method consumes a lot of electricity, has high operating costs and produces a large amount of waste water, it is basically not suitable for drinking water removal. Fluorine; the coagulation method is rarely used in practice due to unstable effluent quality; the adsorption filtration method has a large attenuation of fluoride removal performance and secondary pollution during the regeneration process, so many equipment are discarded after a short running time, resulting in a lot of waste

Method used

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  • A compound drinking water defluoridation process
  • A compound drinking water defluoridation process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0017] Embodiment 1, if the fluorine content of raw water is 3.16mg / L, the treatment process is as follows:

[0018] (1) Add 220ppm of composite hydroxyaluminum phosphorous ash defluoridation agent in the water inlet;

[0019] (2) The coagulation reaction occurs in a coagulation column with a diameter of 200mm and a height of 3.5m, and a fan-shaped static settling area accounting for 1 / 5 of the area and a height of 80mm is isolated on the side of the coagulation column for drainage. For mud, adjust the amount of mud discharge through the cut-off valve, so that the height of the floc is kept at 1.5m, and the rising flow rate of the coagulation column is 4m / hour;

[0020] (4) The effluent of the coagulation column flows through the spherical hydroxyapatite adsorption filter column with a diameter of 200mm and a height of 1.5m for filtration. The height of the spherical hydroxyapatite filter layer is 0.5m and the filtration rate is 4m / hour ;

[0021] (5) Backwash the spherical ...

Embodiment 2

[0023] Embodiment 2, if the fluorine content of raw water is 2.3mg / L, the treatment process is as follows:

[0024] (1) Add 150ppm of composite hydroxyaluminum phosphorous ash defluoridation agent in the water inlet pipe;

[0025] (2) Introduce the coagulation reaction in a coagulation column with a diameter of 200mm and a height of 3.5m, and use a partition to isolate a fan-shaped static settling area accounting for about 1 / 5 of the area and a height of 80mm on the side of the coagulation column. For mud discharge, adjust the amount of mud discharge through the stop valve so that the height of the floc is kept at 1.5m, and the rising flow rate of the coagulation column is 5m / hour;

[0026] (4) The effluent of the coagulation column flows through a spherical hydroxyapatite adsorption filter column with a diameter of 200mm and a height of 1.5m. The height of the spherical hydroxyapatite filter layer is 0.5m, and the filtration rate is 5m / hour;

[0027] (5) Backwash the spheric...

Embodiment 3

[0029] Embodiment 3, if the fluorine content of the raw water is 1.6 mg / L, the treatment process is as follows:

[0030] (1) Add 60ppm of composite hydroxyaluminum phosphorous ash defluoridation agent in the water inlet;

[0031] (2) Introduce the coagulation reaction in a coagulation column with a diameter of 200mm and a height of 3.5m, and use a partition to isolate a fan-shaped static settling area accounting for about 1 / 5 of the area and a height of 80mm on the side of the coagulation column. For mud discharge, adjust the amount of mud discharge with the stop valve so that the height of the floc is kept at 1.5m, and the rising flow rate of the coagulation column is 6m / hour;

[0032] (4) The effluent of the coagulation column flows through a spherical hydroxyapatite adsorption filter column with a diameter of 200mm and a height of 1.5m. The height of the spherical hydroxyapatite filter layer is 0.5m, and the filtration rate is 6m / hour;

[0033] (5) Backwash the spherical h...

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Abstract

The invention discloses a complex drinking water fluorine removing process. According to the complex drinking water fluorine removing process, a fluorine removing method that the addition of an aluminum-base hydroxyapatite fluorine removing agent for coagulation and the adoption of spherical hydroxyapatite for filtration are combined is adopted. A continuous sludge discharging and coagulating column is adopted in the process of coagulating by using the aluminum-base hydroxyapatite fluorine removing agent, and the continuous sludge discharging and coagulating column is internally provided with a static precipitating zone, wherein the area of the static precipitating zone is 1 / 4-1 / 10 of the total area of the continuous sludge discharging and coagulating column. The precipitated flocculate can be discharged continuously through the static precipitating zone so that the height of a flocculate layer in the continuous sludge discharging and coagulating column can be kept to be 1-2 meters and the fluorine removing capability of the aluminum-base hydroxyapatite fluorine removing agent can be fully exerted. The clarified low-turbidity water is fed into a filtering column of spherical hydroxyapatite, so that the concentration of fluorine in the drinking water can be further reduced and the drinking water can reach the drinking-water health standards of the state. By adopting the complex drinking water fluorine removing process disclosed by the invention, a long-term stable fluoride removing effect can be achieved.

Description

technical field [0001] The invention relates to a fluoride removal process, in particular to a compound drinking water fluoride removal process suitable for high fluorine-containing raw water treatment. Background technique [0002] my country's drinking water hygiene standard (GB5749-2006) stipulates that the fluorine content in drinking water should not exceed 1.0mg / L. Fluorosis caused by drinking high-fluoride water is an endemic disease worldwide. In mild cases, it can cause dental fluorosis, and in severe cases, it can cause skeletal fluorosis, resulting in osteoporosis, bone deformation, and even paralysis and loss of working ability. China is one of the countries with the most severe fluorosis in the world. Except for Shanghai, it spreads all over the country, mainly in rural and pastoral areas with relatively backward economy. At present, the population of sick villages due to high fluoride water poisoning is as high as 80 million. Drinking water Fluorine removal is...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F9/04
CPCC02F1/281C02F1/5236C02F9/00C02F2101/14C02F2301/08
Inventor 刘泽山张宝军
Owner JIANGSU YONGGUAN WATER & WASTERWATER EQUIP CO LTD
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