Use of ArsenXnp, a hybrid anion exchanger, for arsenic removal in remote villages in the Indian subcontinent

https://doi.org/10.1016/j.reactfunctpolym.2007.07.047Get rights and content

Abstract

Many of the arsenic removal units operating in remote villages of West Bengal, India now use a hybrid anion exchanger (HAIX) which are essentially spherical anion exchange resin beads containing dispersed nanoparticles of hydrated ferric oxide (HFO). HAIX, now commercially available as ArsenXnp, offers a very high selectivity for sorption of oxyanions of arsenic due to the Donnan membrane effect. The sorption columns used in the field for removal of arsenic are either single column or split-column design. The sorption columns allow flow of atmospheric oxygen, thereby promoting oxidation of dissolved Fe(II) species of arsenic-contaminated raw water to insoluble Fe(III) oxides or HFO particulates. Apart from the usual role played by the sorbents like ArsenXnp or activated alumina towards arsenic removal, HFO particulates also aid in the treatment process. Each unit is attached to a hand-pump driven well and capable of providing arsenic-safe water to three hundred (300) households or approximately one thousand villagers. No chemical addition, pH adjustment or electricity is required to run these units. On average, every unit runs for more than 20,000 bed volumes before a breakthrough of 50 μg/L of arsenic, the maximum contaminant level in drinking water in India, is reached. In addition to arsenic removal, significant iron removal is also achieved throughout the run. Upon exhaustion, the media is withdrawn and taken to a central regeneration facility where 2% NaCl and 2% NaOH solution are used for regeneration. Subsequently, the regenerated resin is reloaded into the well-head sorption column. Following regeneration, the spent solutions, containing high arsenic concentration, are transformed into solids residuals and contained in a way to avoid any significant arsenic leaching. Laboratory investigations confirmed that the regenerated ArsenXnp is amenable to reuse for multiple cycles without any significant loss in capacity.

Introduction

Arsenic present in drinking water drawn from underground sources is the cause of wide-spread arsenic poisoning affecting nearly 100 million people living in Bangladesh and West Bengal, a neighboring Indian state [1], [2], [3], [4]. While the maximum contaminant level (MCL) of arsenic in drinking water is 50 μg/L [5], [6] in India, arsenic concentrations in this region well exceed the MCL. Health effects related to arsenic ingestion through drinking water take a long time before becoming fatal and life-threatening [7]. Average annual precipitation in this geographic location is significantly high, often exceeding 1500 mm/year. But poor sanitation practices which prevail in this area have contaminated surface waters leading to a potential risk of water borne diseases if used as drinking water without appropriate treatment. On the other hand, relative abundance and ease of finding bacteriologically safe groundwater sources promoted the wide-spread use of wells with hand pumps as drinking water sources. There remain thousands of villages where arsenic-laced ground water is the only viable source of drinking water.

Several treatment technologies and equipment have been developed for removal of arsenic from water. It is well known that hydrated oxides of polyvalent metals like Fe(III), Al(III), Ti(IV) and Zr(IV) exhibit ligand sorption properties by forming inner-sphere complexes [8], [9], [10], [11], [12], [13]. A non-regenerable adsorption media, granulated ferric hydroxide (GFH) has been widely used in many places including West Bengal, India [14]. It has also been reported that the above-mentioned metal oxides, when dispersed within a polymeric host material, offer tunable behaviors for sorption of a wide variety of anionic ligands and transition metal cations [15], [16], [17], [18]. One such hybrid sorbent, produced by dispersing hydrated ferric oxide (HFO) nanoparticles inside a polymeric anion exchanger host material, exhibits high affinity for removal of arsenic from natural waters due to the Donnan membrane effect exerted by the host material [18], [19], [20]. The hybrid anion exchanger (HAIX) is now commercially available as ArsenXnp from SolmeteX Co. in Northborough, MA and Purolite Co. in Philadelphia, PA; however, no endorsement is implied. Earlier investigations showed that the chelating polymers with nitrogen donor atoms, when loaded with copper(II), are very selective to inorganic arsenic species and also are reusable [21], [22], [23]. However, high price of the parent chelating polymer was a major obstacle toward wider applications related to water and wastewater treatment.

Since 1997, Bengal Engineering and Science University, Howrah, India and Lehigh University, USA have collaborated to develop a sustainable solution to combat the arsenic problem in West Bengal, India. Under this initiative, about 160 well-head arsenic removal systems have been installed. These units are community based and serve about 250–300 families; additionally, the units require no electricity, chemical addition or pH adjustments. The adsorbent media used commonly is activated alumina. Characteristics and performance of these units have been previously reported [24]. Since 2004, ArsenXnp media, along with activated alumina has been utilized in the units. The primary objective of this article is to present the performance of ArsenXnp for arsenic removal over a long period of run in the field, regenerability of the media, and elucidation of arsenic removal mechanism and containment strategies of arsenic removed.

Section snippets

Well-head treatment units

The main component of the well-head treatment unit is an adsorption column (diameter 35 cm, height 2 m), which is a gravity-fed system operating in downflow mode. Apart from the adsorption column, there is a coarse-sand filter to contain the backwash waste water from the column, which contains arsenic-laden precipitates of ferric hydroxide or hydrated ferric oxide (HFO). The adsorption column mounted on top of a hand-pump driven well is a stainless steel (SS304) cylindrical tank with two distinct

Isotherms for activated alumina and ArsenXnp

Fig. 6, Fig. 7 show the As(III) and As(V) adsorption isotherms onto ArsenXnp and activated alumina, respectively. It may be noted that As(III) and As(V) isotherms for ArsenXnp are comparable, but activated alumina prefers As(V) well over As(III).

Performance of the single and split-column unit

Fig. 8 shows performance of a single-column unit containing ArsenXnp located at Nabarun Sangha, Kankpul, Ashoknagar in North 24 Parganas district of West Bengal. For an average inlet concentration of 85 μg/L, the unit ran for almost 29,000 bed volumes

Arsenic removal: design of well-head units and role of dissolved iron

The uppermost part of the unit ensures near-complete oxidation of dissolved iron to hydrated ferric hydroxide or HFO by oxygen as shown below:4Fe2++O2+10H2O4Fe(OH)3(s)+8H+(ΔGReac0=18kJ/mole)The standard state free energy change for the above reaction is highly negative implying that the forward reaction is thermodynamically favorable. Hydrogen ions generated by the precipitation reaction are neutralized instantaneously by alkalinity (HCO3-) present in groundwater. As a result, no significant

Conclusions

ArsenXnp is the first polymer-based commercially available arsenic-selective sorbent. The field performances of well-head arsenic removal units using ArsenXnp demonstrate that such units can effectively produce arsenic-safe water for more than 20,000 bed volumes. The units do not require any chemical addition or electricity. These community based units are run and maintained by the villagers. At the end of each run, the exhausted sorbent is regenerated at a central regeneration facility; after

Acknowledgements

Partial financial assistance from private donors like Hilton Foundation and Rotary International through Water For People is acknowledged. Also, the authors would like to thank SolmeteX, Inc. for providing ArsenXnp for the units installed in the villages. The authors like to thank Mr. Alok Pal, Mr. Dilip Ghosh and Mr. Morshed Alam for their assistance in field and laboratory work.

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