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Challenge the future Delft University of Technology Investigating subsurface iron and arsenic removal: Anoxic column experiments to explore efficiency parameters Graduation Harmen van der Laan | 18 September 2009
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Challenge the future Delft University of Technology Investigating subsurface iron and arsenic removal: Anoxic column experiments to explore efficiency.

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Page 1: Challenge the future Delft University of Technology Investigating subsurface iron and arsenic removal: Anoxic column experiments to explore efficiency.

Challenge the future

DelftUniversity ofTechnology

Investigating subsurface iron and arsenic removal: Anoxic column experiments to explore efficiency parametersGraduation Harmen van der Laan | 18 September 2009

Page 2: Challenge the future Delft University of Technology Investigating subsurface iron and arsenic removal: Anoxic column experiments to explore efficiency.

2

Contents

i. Introductioni. Arsenic problem

ii. Subsurface iron and arsenic removal

iii. Problem description and objectives

iv. Research setup

v. Experimental procedure

ii. Theoretical backgroundiii. Results and discussioniv. Conclusions and recommendations

Page 3: Challenge the future Delft University of Technology Investigating subsurface iron and arsenic removal: Anoxic column experiments to explore efficiency.

3

Arsenic contamination in drinking water

Arsenic problem Naturally in ground water Chronic exposure: higher

rates of lung, bladder and skin tumors

Big social impact (ostracism) WHO guideline: < 10 μg/L

Bangladesh 30 million people are exposed

to concentrations > 50 μg/L Rural areas: no centralized

systems (10 million tube wells)

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Subsurface iron and arsenic removal

Ground water level

Ground water with Fe(II) and As

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Subsurface iron and arsenic removal : injection phase

Ground water level

O2 front

Injected water front

Ground water with Fe(II) and As

Injection water without oxygen

Injection water with oxygen

Page 6: Challenge the future Delft University of Technology Investigating subsurface iron and arsenic removal: Anoxic column experiments to explore efficiency.

6

Subsurface iron and arsenic removal: abstraction phase

Ground water level

Ground water with Fe(II) and As

Injection water without oxygen

Oxidation zone withfreshly formed ferric oxides

iron oxidewith adsorbed Fe(II) and As

Page 7: Challenge the future Delft University of Technology Investigating subsurface iron and arsenic removal: Anoxic column experiments to explore efficiency.

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Subsurface iron and arsenic removal: efficiency ratio

Volume [m3]

Iron c

once

ntr

ati

on [

mg/L

]

4

2

0

VinjectionV

VVi

Efficiency ratio Typically increasing over successive cycles

Page 8: Challenge the future Delft University of Technology Investigating subsurface iron and arsenic removal: Anoxic column experiments to explore efficiency.

8

Problem description and objective

Problem description There is a lack of insight in (i) the dominant mechanisms responsible for the (increasing) sorption of iron and arsenic(ii) operational factors how to optimize the removal efficiency

The objective of this study To obtain reliable experimental data to investigate the parameters affecting the removal efficiency

The primary goal is to gain a better understanding of the dominant sorption mechanisms and the increasing efficiency, in order to optimize the operation of this technology in the field.

Page 9: Challenge the future Delft University of Technology Investigating subsurface iron and arsenic removal: Anoxic column experiments to explore efficiency.

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Research setupAnoxic column experiments to simulate several injection/abstraction

cycles in Bangladesh

Experimental setup 4 columns diameter 36mm, height 308mm

2 types of soil material Virgin Sand 0.6-1.2mm Aquifer Sand 0.12-2.5mm Fe: 2.7 and 2.5 mg/g . As: 2 and 0.5 µg/g

‘average Bangladesh’ Synthetic Ground Water 4 mg/L Fe2+ 200µg/L As(III) pH 6.9 buffers: 5mM NaHCO3 1.64mM NaCl

Ionic Strength 2·10-2

Four experiments, 10 injection/abstraction cycles

Experiment I: Investigation increasing capacity over successive cycles (cycle 1 – 5)

Experiment II: Influence pH: 6.5, 6.9 and 7.5 (cycle 6 – 8)

Experiment III: Influence injection volume (cycle 9)

Experiment IV: Influence increase ionic strength (0.1M NaNO3) (cycle 10)

Monitoring Fe, As, pH, Eh, Conductivity and Oxygen

Page 10: Challenge the future Delft University of Technology Investigating subsurface iron and arsenic removal: Anoxic column experiments to explore efficiency.

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Experimental procedure: the story of one data point

How does one data point at the graph come into existence? What is ‘the story of one ‘data point’

A short movie shows the experimental procedure

Page 11: Challenge the future Delft University of Technology Investigating subsurface iron and arsenic removal: Anoxic column experiments to explore efficiency.

11Met dank aan: Samuël (cameraman) en Ruben (camera én microfoon)

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12

Contents

i. Introductionii. Theoretical background

iii. Results and discussioniv. Conclusions and recommendations

Page 13: Challenge the future Delft University of Technology Investigating subsurface iron and arsenic removal: Anoxic column experiments to explore efficiency.

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Adsorption is influenced by: Surface charge Chemical affinity

Adsorption capacity of a material: Number of sites (sites/nm2) Surface area (m2/g)

Furthermore, Competing ions Inner/outer-sphere complexation

Fe2+ and As(III) form inner-sphere complexes; their adsorption is fairly insensitive to ionic strength changes

Theoretical background

Fe2+

OH OFe

+

H+

OH OH

OH

OH

Sand grain surface

M2+

M2+ M2+

M2+

M2+

Example: adsorption Fe2+

Iron: Fe2+ and Fe3+

Arsenic: As(III) and As(V)Arsenite

Arsenate

Page 14: Challenge the future Delft University of Technology Investigating subsurface iron and arsenic removal: Anoxic column experiments to explore efficiency.

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Contentsi. Introductionii. Theoretical backgroundiii. Results and discussion

i. Experiment I : Influence successive cycles

a. High adsorption capacities

b. Increasing retardation As

c. Stable retardation Fe2+

ii. Experiment IV: Effect of ionic strength

iii. General discussion

iv. Conclusions and recommendations

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Results experiment I: successive cycles

Expectation, based on other experiments and literature:Retardation factor between 5 and 20, slightly increasing

Page 16: Challenge the future Delft University of Technology Investigating subsurface iron and arsenic removal: Anoxic column experiments to explore efficiency.

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Results experiment I: successive cycles

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Results experiment I: successive cycles

Three main findingsa. High adsorption capacities (in absolute

values)b. Increasing adsorption As(III)c. Stable adsorption Fe2+

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High adsorption capacities

Sand grain surface

Fe2+

OH OFe

+

H+

OH OH

OH

OH

OH OH

OH

OH

OH OH

OH

OHOH OH

OH

OH

OH OH

OH

OH

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High adsorption capacitiesHypothesized mechanism

Ion exchange mechanism

Ion exchange capacity determined by a.o. clay particles, in Cation Exchange Capacity (CEC).

Surprisingly, a low CEC value can result in a high retardation!

2 meq/kg Retardation factor 30! (normal sandy aquifer is 10 meq/kg)

Yet, ion exchange in virgin sand?!

Fe2+

Na

+

OH

Na

+

Sand grain surface

Na

+

Na

+

Na

+

Fe2+

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Contentsi. Introductionii. Theoretical backgroundiii. Results and discussion

i. Experiment I : Influence successive

cycles

a. High adsorption capacities

b. Increasing retardation As

c. Stable retardation Fe2+

ii. Experiment IV: Effect of ionic strength

iii. General discussion

iv. Conclusions and recommendations

Page 21: Challenge the future Delft University of Technology Investigating subsurface iron and arsenic removal: Anoxic column experiments to explore efficiency.

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Retardation As(III) increasing

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Stable Fe2+ capacity

Non-increasing capacity Fe2+

Very remarkable! Increase iron content, thus in adsorption sites yet no increase in adsorption

In accordance with other studies and experiments

Ion exchange provides explanation: Exchange Capacity remains constant.

Fe2+

Na

+Na

+

Na

+

Na

+

Fe2+

Fe2+

Na

+Na

+

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Contentsi. Introductionii. Theoretical backgroundiii. Results and discussion

i. Experiment I : Influence successive cycles

a. High adsorption capacities

b. Increasing retardation As

c. Stable retardation Fe2+

ii. Experiment IV: Effect of ionic strength

iii. General discussion

iv. Conclusions and recommendations

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Effect of the ionic strength (0.1M NaNO3)

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Effect of the ionic strength (0.1M NaNO3)

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Effect of the ionic strength (0.1M NaNO3)

Main finding Adsorption As(III) is increasing with increasing ionic strength, while Ferrous iron adsorption is decreasing

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Decrease Fe2+ with high ionic strength

Decrease Fe2+ -70% (average)

Ionic strength influenced adsorption iron? Remember: Inner-sphere complexes,

thus rather insensitive for ionic strength!

The ion exchange mechanism provides a clear explanation.

High Na+ concentration (0.1M vs. 7 mM) results in shift exchanger composition (98% Na+ / 2% Fe2+ vs. 37% Na+ / 63% Fe2+)

Fe2+

Na

+

Na

+Na

+

Sand grain surface

Na

+

Na

+

Na

+

Fe2+

Na

+

Na

+Na

+

Na

+Na

+

Na

+

Na

+

Na

+Na

+

Na

+

Na

+

Na

+

Na

+

Na

+

Na

+

Na

+Na

+

Na

+

Na

+

Na

+

Na

+

Na

+

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Increase As(III) with high ionic strength

Increase As(III) 8 – 43 in one cycle (438%)

Other studies: increasing adsorption with increasing ionic strength. But, there with negative surface charge. Here, As(III) is uncharged and positive charge.

Hypothesis : ionic strength causes surface charge of zeroSurface charge and potential becomes 0 (“point-of-zero-charge”) thus no electrostatic repulsionwhich favors adsorption of the uncharged As(III)

Compare: experiment I: 10 – 50 in 5 cycles

As(III)0

++0 0

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Contentsi. Introductionii. Theoretical backgroundiii. Results and discussion

i. Experiment I : Influence successive cycles

a. High adsorption capacities

b. Increasing retardation As

c. Stable retardation Fe2+

ii. Experiment IV: Effect of ionic strength

iii. General discussion

iv. Conclusions and recommendations

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General discussion

Ion Exchange mechanism

Pro’sNot possible to describe with surface sites theoryStable retardation Fe2+

Decrease Fe2+ adsorption with high ionic strength

Results in adsorption capacity similar to other studies

Con’s / remaining questionsExchange capacity (virgin) sand?!Why no increase adsorption for ferrous iron?Why not all Fe2+

accessible for adsorption?

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Contentsi. Introductionii. Theoretical backgroundiii. Results and discussion

iv. Conclusions and recommendationsi. Iron removal mechanism

ii. Arsenic removal mechanism

iii. (Practical) implications

iv. Recommendations

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Conclusions sorption mechanism of iron

I. High capacity!Much more as ‘theoretically’ possible

II. No increasing efficiency with increasing amount iron oxide.

III. Surprisingly, the ion exchange mechanism played a dominant role

Disclaimer: under laboratory circumstances

Fe2

+

Na

+

OH

Na

+

Sand grain surface

Na

+

Na

+

Na

+

Fe2

+

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Conclusions sorption mechanism of arsenic

I. High capacity!Much more sites accessible as expected

II. The efficiency is increasing (by iron oxides)1 day injection = 1 month 50% arsenic removal!

III. Higher ionic strength, higher efficiencyHypothesis: surface charge becomes zero

Disclaimer: under laboratory circumstances

As(III)0

++0 0

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(Practical) implications

I. Measure ionic strength and ‘point-of-zero-charge’ for site selectionWhere to apply subsurface arsenic removal

II. Honestly, more research is required for more practical implications

III. Biggest implication for future research

if ion exchange mechanism is true, it has a large influence on interpretation results

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Recommendations

I. More column experimentsvarying water quality, sand materials, experiment run times

II. Verify the ion exchange mechanismMeasure Cation exchange capacity, apply cation free injection water, more sampling

III. Focus on soil chemistrydetailed surface analyses: charge, potential, surface area (BET), X-ray diffraction

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General conclusion

Subsurface treatment has a large potential for iron and arsenic removal.

Study results illustrate the theoretical possibilities under ideal circumstances

More research is required to optimize the operational efficiency in the field

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Thank you for your attention

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DE FILIPPIJNENGretha (tropen)verpleegkundigeGezondsheidstraining in communities (niet in kliniek)

Harmen drinkwater ingenieurFaciliteren bij implementatie drinkwatersysteem in dorp

Lokaal team, Filippijnse NGOFebruari 2010 - 1 tot 1.5 jaarWonen in plattelandsdorp‘onbetaald’ – op basis van giftenAvontuur, concrete vraag, drive vanuit God

Nieuwsgierig? Harmenengretha.wordpress.com

www.watervoorfilippijnen.nl