CN1063089A

CN1063089A - The fluorinated water treatment process

Info

Publication number: CN1063089A
Application number: CN 91100227
Authority: CN
Inventors: 马志毅; 吴炳耀; 周凤鸣; 邢权; 杨文敏
Original assignee: SHANXI MEDICAL COLLEGE; TAIYUAN POLYTECHNIC UNIVERSITY
Current assignee: SHANXI MEDICAL COLLEGE; TAIYUAN POLYTECHNIC UNIVERSITY
Priority date: 1991-01-12
Filing date: 1991-01-12
Publication date: 1992-07-29
Anticipated expiration: 2006-01-12
Also published as: CN1025954C

Abstract

A kind of treatment process of fluorinated water, its adopts the method for fixed bed flyash absorption can make high-fluorine drinking water reach the following sanitary standard for drinking water of fluorine-containing 1mg/l, adopts slurry attitude bed absorption method can make the trade effluent of the fluorine-containing 700-1000mg/l of phosphate fertilizer plant reach the following emission standard of fluorine-containing 20mg/l.Fluorine-containing ash can be used as the preparation building block or brick can not cause secondary pollution, thereby reaches the purpose of the treatment of wastes with processes of wastes against one another.This method and existing lime precipitation mutually specific investment only be its 22%, cost only be its 69%.

Description

The fluorinated water treatment process

The invention belongs to a kind of technology of absorption method treating water, be specifically related to a kind of treatment process of fluorinated water.

The long-term drinking fluoro-containing concentration surpasses the water of 1.5mg/l, can cause fluorosis, and it mainly shows is dental fluorosis and skeletal fluorosis.According to the regulation of China's " drinking water sanitary standard ", the amount of fluoride must be below 1.0mg/l in the Drinking Water.Some geographic tap water, fluorine content is too high, must be through just drinkable after handling.The method of drinking water defluorination is a lot, as coagulant sedimentation, absorption method, ion exchange method, electroosmose process, electrolytic process and cold method etc., and these methods or take medicine or expense electricity or equipment complexity, thereby, the processing costs height, initial cost is big.

If contain fluorine, can pollute rivers, underground water in the trade effluent, also can work the mischief at last people and ecotope.The defluorination method of trade effluent has calcium salt precipitation method, absorption method, calcium superphosphate ion exchange method and reverse osmosis method.Using maximum is calcium precipitation method, promptly uses this method as the processing of Taiyuan phosphate fertilizer plant fluoride waste.Its principle is to add lime (Cao) in water, and Ca and F generate CaF ₂Be precipitated out.Adopt this method, labor condition extreme differences such as lime fragmentation, cost height (cost of handling waste water per ton is up to 1.4 yuan), waste residue (CaF ₂) be difficult to utilize, cause secondary environmental pollution.

The objective of the invention is to develop the fluoride waste treatment process of a kind of economical and effective, the treatment of wastes with processes of wastes against one another, comprehensive utilization.

Major technique feature of the present invention is to be sorbent material with flyash, adopts slurry attitude bed or fixed bed to adsorb, and after the solid-liquid separation, water up to standard is standby, and fluorine-containing ash is used to fire building brick or makes other building block.

Technical process of the present invention is described as follows in conjunction with the embodiments:

Embodiment 1

The processing of high fluorine area Drinking Water.Fluorine-containing 12-22.5mg/L in the water before handling.The adsorption column that the rigid polyvinyl chloride of employing internal diameter 65mm is made, the supporting layer of bottom is brown skin and cobble, height overall 100mm, flyash is adorned on its top No. 4, and height overall is 2m, and gross weight is 4kg, and water flows through from top to bottom, and filtering velocity is 0.9-1.2m/h.Operate under normal pressure, the room temperature.

The size-grade distribution of above-mentioned sorbent material (flyash) sees Table 1

Table 1

Sieve mesh＜below 20 20～40～60～80～100～120～140-200

％ 10.5 28.3 27.1 8.2 9.4 8.2 4.0 7.4

As shown in Table 1, about 66% particle is below 40 orders, and this particle that shows this flyash is thicker.Its physical properties and component see Table No. 4 ashes in 2.

Table 2

Grey type No. 4 No. 5

Proportion (d ²⁰ ₂₀) 1.878 2.230

Unit weight g/cm ³0.567 0.618

Loss on ignition % 33.32 19.23

Specific surface m ²/ g 73 ± 1.0 11.5 ± 1.0

Iodine number mg/g 49.65 87.91

W % 0.74 0.4

C % 31.84 18.33

CL % 0.074 0.047

SiO ₂% 8.92 40.54

Al ₂O ₃% 5.64 25.24

Fe ₂O ₃% 0.80 9.40

CaO % 0.45 3.68

MgO % 0.12 0.33

TiO ₂% 0.27 0.94

As ppm 0.3 0.8

F ppm 60 130

Cr ppm 10.6 56.6

Cd ppm 1.8 8.1

Hg ppm 0.38 0.24

Pb ppm 8.8 32.2

In process with the aforesaid method treating water, per hour carry out a water quality analysis, the result shows, all be lower than the requirement of drinking water standard 1mg/L in 9 hours with interior water outlet fluorine content, other indexs are: turbidity is reduced to 1.2 degree by 25 degree, chlorion is reduced to 10mg/L by 13.08mg/L, and COD reduces to 1.68mg/l by 1.45mg/l.It is neutral that pH value keeps, and the flyash fluoride removing quantity is the 12.8-44mg/kg(ash), the stripping quantity of metals such as Cr, Pb and Hg all is no more than the scope of permission in the water.

Embodiment 2

The waste water that produces during Taiyuan phosphate fertilizer plant produces, average fluorine content is about 700-1000mg/L, and pH value is 2-3.After adopting the absorption of slurry attitude bed, make Ash Water Separator with the standing sedimentation method, fluorine-containing below 20mg/L after handling, reach emission standard.Ash behind the absorption fluorine is distinguished fusion in ratio and lime, cement, the pitch of 25-50%, thereby makes lime building block, cement block or asphalt block, is fired into brick with the clay fusion.30 days immersion result of above-mentioned building block and brick shows that the leaching yield of fluorine only has 0.01-1.67%, only otherwise these building blocks or brick are used for the ground of exterior wall or many water, generally can not cause secondary pollution because of the stripping of fluorine.

Water/the gray scale of slurry attitude bed is 7-10, stirs 30-130 minute, and rotating speed is about 500rpm, the about 3-5W/m of power level ³, normal temperature and pressure is operation down, is sorbent material with No. 5 flyash, and its physical properties and composition see Table 2.Size-grade distribution is as shown in table 3.

Table 3

Sieve mesh＜20 20～40～60～80～100～120～140～

% 0.2 0.4 1.1 1.2 4.8 22.3 18.8 1.3

Sieve mesh 160～180～＜200

% 28.8 0.5 22.2

This shows that No. 5 grey particle diameter is thinner, 50% more than 160 orders, wherein account for 22% more than 200 orders.

The specific embodiments and the result thereof of slurry attitude bed are as follows:

With volume is that pack into fluorine-containing 700-1000mg/L, pH value of 23 liters plastic barrel is 10 liters of 2 waste water, adds No. 5 grey 1kg, continuously stirring, and the fluoro-containing concentration in 1 hour sampling analysis water is measured pH value.Its result is that PH increases to 6-7 by 2 in several minutes, stabilize to neutrality and no longer change.Fluorine content is 40mg/L after 1 hour in the water, is 30mg/L after 1.5 hours, and 3.0 hours is 20mg/L, is 15mg/L after 6 hours.

The investment estimation that adopts slurry attitude bed to handle phosphate fertilizer plant's waste water shows that its capital cost only is 22% of at present general lime precipitation, and 0.98 yuan of/ton water of processing cost average out to only is 69% of lime precipitation.

In sum, the tap water that adopts the flyash ADSORPTION IN A FIXED BED to contain high fluorine can make it reach the following drinking water standard of fluorine-containing 1mg/L.Adopt slurry attitude bed absorption flyash to adsorb fluorine-containing trade effluent, can make waste water reach the following emission standard of 20mg/L, PH becomes neutrality by alkalescence, and the content of other pollutents also descends to some extent, the flyash of absorption fluorine can be used as material of construction, reaches the purpose of the treatment of wastes with processes of wastes against one another.

Claims

1, a kind of fluorinated water treatment process is characterized in that with flyash being sorbent material, adopts slurry attitude bed or fixed bed to adsorb, and after the solid-liquid separation, water up to standard is standby, and fluorine-containing ash is used to fire building brick or makes building block.

2, treatment process as claimed in claim 1 is characterized in that described fluorinated water is a high-fluorine drinking water, and employing flyash is sorbent material, and ADSORPTION IN A FIXED BED, filtering velocity are 0.9-1.2m/h.

3, fluorinated water treatment process as claimed in claim 1 is characterized in that described fluorinated water is the trade effluent of fluorine-containing 700-1000mg/L, is sorbent material with flyash, adopt the absorption of slurry attitude bed, churning time is 30-180 minute, the about 500rpm of stirring velocity, power level 3-5W/m ³, water/gray scale is 7-10, and normal temperature and pressure is operation down, and by gravity settling separation, discharged wastewater met the national standard, fluoropolymer powder coal ash are made building block with ratio and lime, cement or the pitch fusion of 25-50%, or mix with clay and to burn till building brick.