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DSpace at VNU: Investigation of As, Mn and Fe fixation inside the aquifer during groundwater exploitation in the experimental system imitated natural conditions

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The exper-iment was carried out on the column imitated a bore core of anaerobic aquifer with water phase containing FeII, MnII, AsIII concentration of 45.12 mg/L, 14.52 mg/L, 219.4 lg/L,

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O R I G I N A L P A P E R

Investigation of As, Mn and Fe fixation inside the aquifer

during groundwater exploitation in the experimental system

imitated natural conditions

Nguyen Thi Kim Dung•Tran Hong Con•

Bui Duy Cam•Yumei Kang

Received: 21 March 2011 / Accepted: 13 July 2011 / Published online: 9 August 2011

Ó Springer Science+Business Media B.V 2011

Abstract Water-dissolved oxygen was supplied

into anaerobic aquifer , which oxidized Fe(II), Mn(II)

and trivalent arsenic and changed them into

undis-solved solid matter through hydrolysis, precipitation,

co-precipitation and adsorption processes The

exper-iment was carried out on the column imitated a bore

core of anaerobic aquifer with water phase containing

Fe(II), Mn(II), As(III) concentration of 45.12 mg/L,

14.52 mg/L, 219.4 lg/L, respectively and other ions

similarly composition in groundwater After 6 days

of air supply, concentration of iron reduced to

0.38 mg/L, manganese to 0.4 mg/L, arsenic to

9.8 lg/L (equivalent 99.16% of iron, 97.25% of

manganese and 95.53% of arsenic fixed), and for other

ions, the concentration changed almost according to

general principles Ion phosphate and silicate strongly

influenced on arsenic removal but supported iron and

manganese precipitation from water phase Based on the experimental results, new model of groundwater exploitation was proposed

Keywords Arsenic Exploitation  Groundwater manganese Iron fixation

Introduction

In recent years, arsenic contamination in groundwater and drinking water in Vietnam has received consid-erable attention Elevated levels of As were found in groundwater in the upper aquifers in several areas in Red River Delta (Berg et al.2001; Agusa et al.2006, 2009) Residents living in high As-contaminated groundwater area are exposed to As through con-sumption of rice and groundwater, suggesting potential health risk of As exposure (Agusa et al 2009) Symptoms for chronic exposure to As have not yet observed, but the continuous usage of tube wells might cause health effects of the residents Given high degree of exposure to As in a large area of Red River and Mekong River in Vietnam, investigations

on the mechanisms of arsenic releases into ground-water, as well as model for reduction in As in groundwater, are critically important to develop a simple and effective technology for arsenic removal

in groundwater and thus reduce health risk due to elevated and chronic exposure

N T K Dung ( &)

Haiphong Private University, 36 Dan Lap Street,

Le Chan District, Hai Phong, Vietnam

e-mail: dungntk10@gmail.com

T H Con  B D Cam

Hanoi University of Science, Vietnam National

University, 334 Nguyen Trai Street, Thanh Xuan,

Hanoi, Vietnam

Y Kang

Laboratory of Soil Environmental Science, Faculty

of Agriculture, Kochi University, Monobe B200,

Nankoku City, Kochi 783-8502, Japan

DOI 10.1007/s10653-011-9401-7

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In the aquifer, under anaerobic conditions, iron

and manganese exist as divalent species and arsenic

as almost nondissociated trivalent arsenious acid

(Con et al.2002; Nriagu1994; Saha et al 1999) In

order to remove iron from underground water,

tra-ditional technology used aeration technique to

oxi-dize Fe(II) to Fe(III) and then separated it from water

in the form of insoluble Fe(III) For manganese

removal, normally use filtration through sand-coated

MnO2(Chang et al.2010) For groundwater

contam-inated by arsenic, there were many methods and

technologies for arsenic treatment, especially since

‘‘largest poisoning in the World’’ at Bangladesh

revealed in 1993 (Chang et al 2010; Chakraborti

et al.2010) Our recent study has showed that during

and after oxidation of Fe(II) to Fe(III), Fe(III)

immediately hydrolyzed to form almost insoluble

Fe(OH)3 and the iron hydroxide species strongly

adsorbed arsenate anions and partly co-precipitated

with manganese (Dung et al.2009) We investigated

fixation capabilities of iron, manganese and arsenic

on equipment imitated natural conditions of the

aquifer During the fixation of iron, manganese and

arsenic, the expected influencing factors such as

phosphate, silicate, NO3-, NH4?and SO42-

concen-trations were also investigated Experiment result

of this study was applied for fixation of iron,

manganese, arsenic inside aquifer and reduction in

ammonium concentration in exploited water The

underground water exploitation model was

estab-lished based on the idea that underground water after

pumped up was saturated by air oxygen Part of

the oxygen-saturated water was pumped back to

exploited layer to do fixation of iron, arsenic and

manganese, and other part was filtrated to do supply

Experiment

The experimental system was installed as described

in Fig.1 The research column was filled 50-mm

layer of weathering gravel in bottom, next was

600-mm layer of sand mixed with 0.001% of As in

the form of arsenate, 0.01% of Mn in the form of

MnO2and 0.1% of Fe in the form of Fe(OH)3(w/w

percentage) The main components in water phase are

listed in Table 1

Before fixation investigation, the experimental

system (Fig 1) was running with circulation of water

phase and air tightening for 50 days in order to create anaerobic condition in inner system similar to condition in natural aquifer

The investigation started when air was continually supplied to the regulation tank with a rate of 0.5 L/min Samples were taken daily at fixed time from valve (6)

(2)

(1)

(3) (4) (5) (6)

1

9

2

7

6

4

5

10

Fig 1 Schematic diagram of the research system, 1 Column head, 2 Thermoisolation cover, 3 Layer of sand, MnO2, Fe(OH)3, undissolved As(V) and other components, 4 Weath-ering gravel layer, 5 Porous membrane, 6 (1)-(6) Sampling valves, 7 Peristaltic pump, 8 Regulation tank, 9 Thermostat, 10 Air supply device

Table 1 Main composition of water phase (Berg et al 2001 ) Component Concentration (M)

Ca2? 1.0 9 10-3 HCO3- 2.4 9 10-3

NO3- 3.0 9 10-4

SO42- 5.2 9 10-4

PO43- 3.0 9 10-5

Mg 2? 6.0 9 10 -5

Digestible organic matter 1.2 9 10 -3 (glucose)

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at the experimental column, and parameters were

analyzed triplicate by the methods listed in Table2

Results and discussion

Composition of water phase in anaerobic state

The composition and main parameters of water phase

in anaerobic system (after 50 days air absent running)

are analyzed (samples were taken from valve number

(6) at the experimental column and result is shown in

Table3)

The variation in Fe, Mn and As concentrations

under influence of oxygen present

When air oxygen was supplied into system, dissolved

oxygen concentration (DO) increased along with

bubbling time and reached near 8 mg/L after 10 days

(the system changed into almost aerobic condition)

Changing nature of the system from anaerobic to

aerobic caused variation in almost all constituents in

the system (Fig.2)

Together with increasing in DO, ORP of water

phase also increased regularly It was inevitable

In case of arsenic and iron, the variations were

different In the beginning hours of oxygen

supply (about first day), the concentrations of

both elements increased The reason of this

phenomenon could be oxidation by DO yielding

dissolved forms of iron(II) and arsenic(III) from fresh and unstable precipitate species of iron arsenide and sulfide (Dung et al 2010) In the following days, the system was in oxygen-rich condition, iron(II) oxidized into iron(III) This species started to hydrolyzed and precipitated as undissolved Fe(OH)3 That is why iron concen-tration decreased In this condition, arsenite species also slowly oxidized into arsenate in the form of anions hydoarsenate and started to co-precipitate with iron(III) hydroxide or to adsorb onto surface of iron(III) hydroxide particles So total arsenic concentration in the system also decreased (Dung et al.2009) When system was almost in the aerobic condition, the concentra-tions of iron as well as arsenic decreased to meet limited concentrations of 0.50 mg/L and 0.010 lg/L, respectively The results of samples collected from valves 1–5 showed the similar law of elements’ concentration variation and transformation but the time to reach aerobic condition was earlier from valves 1–5

For manganese(II) ion, its concentration was decreased continuously from beginning to the end The reason could be that slow oxidation of Mn(II)

to Mn(IV) by DO in neutral environment formed undissolved MnO2 This process was less influenced

Table 2 Analysis methods APHA, AWWA, WEF ( 1995 )

Parameter Analysis method

As AAS-HVG method

Fe, Mn F-AAS method

NO3-, Cadmium reduction method

Phosphate Stannous chloride method

Silicate Molybdosilicate method

SO42- Methylthymol blue method

NH4? Phenate method

Table 3 Composition of water phase in anaerobic state

Parameters DO

(mg/L)

ROP (mV)

Fe (mg/L)

Mn (mg/L)

As (lg/L)

NO2 -(mg/L)

NH4? (mg/L)

SO4 2-(mg/L)

PO4 3-(mg/L)

SiO3 2-(mg/L) Value 0.8 -45 45.12 1.45 219.4 1.24 48.20 13.76 0.95 2.82

Fig 2 Variation in Fe, Mn, As concentrations, ORP and DO versus air supply time (sampling from valve 6)

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by chemical and physicochemical processes of iron

and arsenic species in the system

The variation in sulfate, phosphate and silicate

concentrations

For investigation of sulfate, phosphate and silicate

variations, samples were taken after interval of 2 days

each other The result for 20-day survey is shown in

Fig.3 There were different variations in

concentra-tions between ions While concentraconcentra-tions of phosphate

and silicate were almost unchanged, concentration

of sulfate increased during survey time However, in

beginning 4 days, the increase rate was low in

com-parison with the following time

Increasing in sulfate ion in the system was result of

oxidation process of sulfide together with arsenide in

the precipitate created before in anaerobic period

The low increasing rate of sulfate concentration in the

system at beginning days could be consequence of

competitive oxidation reactions of iron(II),

arseni-c(III) and other easier oxidation species present in the

system

The variations in NH4?, NO2-, NO3

-concentrations

When system in anaerobic condition, concentration

of nitrate was almost limited to analyze, nitrite was

1.28 mg/L and ammonium was 48.20 mg/L

Supply-ing oxygen from air supplied changed concentration

of all those nitrogen formations Ammonium

con-centration slowly decreased, nitrite concon-centration

decreased to detection limit and nitrate concentration

increased (Fig 4)

Influence of phosphate concentration

For investigation of influence of phosphate concen-tration on immobilization of arsenic, iron and man-ganese, phosphate solution was putted on into the system to meet designed concentration range The samples were collected 8 h each after other, and arsenic, manganese, iron were analyzed

Based on the results presented in Fig 5, we can see that increasing phosphate concentration only lightly influenced on dissolved iron and manganese With concentration of 20 mg/L phosphate, concentration

of total iron dropped from 0.80 to 0.54 mg/L and manganese from 1.38 to 1.12 mg/L The lightly decreasing concentration of iron and manganese could

be the result of precipitation of iron and manganese phosphate in the system For arsenic, this was different Phosphate ion strongly influenced on arsenic immobi-lization With the concentration of phosphate lower than 10 mg/L, the concentration of arsenic was almost uninfluenced; but when phosphate concentration was higher than 10 mg/L, the adsorptive competition

Fig 3 Variations in sulfate, phosphate and silicate

concen-trations

Fig 4 Variations in NH4? , NO2- and NO3- concentrations

Fig 5 Influence of phosphate concentration on fixation of As,

Fe and Mn

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between phosphate and arsenate ions on solid phase

appeared; therefore, concentration of arsenic sharply

increased

Influence of silicate concentration

Investigation of influence of silicate concentration on

immobilization of arsenic, iron and manganese was

implemented similarly as case of phosphate

The result presented in Fig.6showed that soluble

species of iron and manganese in the system were

almost uninfluenced by concentration of silicate But

for arsenate ion, the situation was similar to

phos-phate interaction However, the competitive power was

weaker than phosphate Those expressed by affected

concentration of silicate was higher than phosphate

(15 mg/L vs 10 mg/L), and angular coefficient of line

segment slope in the graph of silicate was less than

phosphate (2.150 vs 5.342) So, in any case, the

presence of phosphate or silicate or both with high

enough concentration raised difficulties for

immobili-zation of arsenic, iron and manganese in oxygen-rich

(aerobic) condition

Proposal model of fixation of As, Fe and Mn

in the aquifer during groundwater exploitation

The aquifer is a water-saturated layer of sand and

gravel Horizontal water flow rate in the aquifer is

normally 10–15 m per day So the aquifer is

under-ground water resource and also can play as a good

water filter Based on our results presented above

together with exploitability of the aquifer, we have

had idea to bring some stages of groundwater

treatment process down to the aquifer These are

aeration, iron precipitation, filtration, arsenic and

manganese treatment stages The oxygenation and sterilization stages are kept on ground The schema of underground water exploitation is described in Fig.7 The production process could be that: Groundwa-ter firstly was pumped up from first tube well to oxygenation basin A portion of oxygen saturation water was pumped back to the aquifer though second tube well Where second well is located in front of first well along to groundwater flow direction Other portion of oxygen-saturated water was used for supply The proportion of supply and fit-back water portions depends on iron concentration in groundwa-ter and oxygen saturation possibility The distance between exploitation and fit-back wells depends on groundwater flow rate and exploitation capacity Based on the result of our study, when iron concentration in water phase C10 mg/L, more than 98% arsenic was remained in solid phase despite total arsenic concentration was up to 0.3 mg/L and the part

of it was oxidized from arsenide formation and dissolved into water phase

Conclusion

Supplying oxygen in the form of dissolved oxygen in water into anaerobic system imitated natural aquifer oxidized almost Fe(II) into Fe(III), partly Mn(II) into Mn(IV) and arsenite into arsenate Hydrolysis of Fe(III) and Mn(IV) helped co-precipitation and adsorption process of arsenate together with iron hydroxide and manganese dioxide The result of these processes reduced concentration of iron, manganese

Fig 6 Influence of silicate concentration

Groundwater current up

O 2 rich current

back

Exploitation well Fit-back well

Treatment system/Oxygenation

Ground water flow direction

Supply water

Oxidation zone

Fig 7 The schema of underground water exploitation

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and arsenic in water phase and retained them among

sand/gravel layer in the system Fixation of the

elements, especially arsenic, influenced by phosphate

and silicate concentrations in water phase However,

ammonia, nitrite, nitrate and sulfate showed almost no

affect Other oxidation processes of sulfide, ammonia

even organic mater increased supplied water quality

Acknowledgments The authors acknowledge the financial

support from the sub-project TRIG A from Hanoi University of

Science and Dr Michael Berg, ESTNV Manager & Scientific

Advisor Department of Water Resources and Drinking Water

to facilitate the implementation process.

References

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Viet, P H., et al (2009) Relationship of urinary arsenic

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Viet, P H., et al (2006) Contamination by arsenic and

other trace elements to humans in Hanoi, Vietnam.

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APHA, AWWA, WEF (1995) Standard methods for the

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Berg, M., Con, T H., et al (2001) Arsenic contamination

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Chakraborti, D., Rahman, M M., Das, B., Murrill, M., Dey, S., Mukherjee, S C., et al (2010) Status of groundwater arsenic contamination in Bangladesh A 14-year study report Water Research, 44, 5789–5802.

Chang, F., Qui, J., Liu, R., Zhao, X., & Lei, P (2010) Practical performance and its efficiency of arsenic removal from groundwater using Fe–Mn binary oxide Journal of Environmental Sciences, 22, 1–6.

Con, H T., Hanh, T N., et al (2002) Investigation of arsenic releasing from solid phase into water in the earth’s crust.

In The proceeding of the 5th international conference on arsenic exposure and health effects, San Diego, CA Dung, N T K., Cam, B D., & Con, T H (2009) Investigation

of influence of basic parameters in groundwater on co-precipitation–adsorption of arsenic, manganese and fresh iron(III) hydroxide Journal of Analytical Science, 14, 40–45 (in Vietnamese).

Dung, N T K., Cam, B D., Con, T H., & Cuong, L M (2010) Investigation and evaluation of factors influencing on arsenic, manganese and iron releasing into groundwater in experimental system imitated natural anearobic conditions Journal of Chemistry, 8, 390–395 (in Vietnamese) Nriagu, J O (1994) Arsenic in environment Part I: Cycling and characterization New York: Wiley.

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