Formation of Hydrocarbons from the Reduction of Aqueous CO 2 by Zero-Valent Iron LESLIE I. HARDY † AND ROBERT W. GILLHAM* Waterloo Centre for Groundwater Research, University of Waterloo, Waterloo, Ontario, N2L 3G1 Canada The reduction of aqueous CO 2 by zero-valent iron was studied in batch and column experiments. Ten hydrocarbons up to C5 were identified as products of the reduction process and were shown to have Anderson-Schulz-Flory (ASF)product distributions. A direct consequence of the ASF product distribution is that a significant mass of hydrophobic hydrocarbons may remain sorbed to the iron surface. Based on a reaction mechanism proposed for the electrore- duction of aqueous CO 2 with nickel electrodes, iron acts as both a reactant by corroding to supply electrons and as a catalyst by promoting the formation and growth of hydrocarbon chains. Water is also a reactant in the system. When iron is used to enhance the dechlorination of chlorinated organic compounds, the slow desorption of the hydrocarbon products may become the rate-limiting step in the reaction. Introduction Chlorinated hydrocarbons, primarily used as industrial solvents and dry cleaning fluids, are widespread and persistent groundwater contaminants. The most common method used to treat thiscontamination involvespumping contaminated water to the surface for treatment;however, complete removalofthe contaminantsfrom the subsurface is rarelyachieved,and the treatment usuallyonlytransfers the contamination to another medium (1). A possible alternative to pump and treat is the containment of the contamination with in situ barriers usingreactive media to degrade the contaminants present in the groundwater (2). Zero-valent iron has recently been shown to rapidly dechlorinate a wide range of chlorinated hydrocarbons in laboratory batch and column experiments (3-6) and has been successfully used to dechlorinate trichloroethylene and perchloroethylene in a field demonstration ofa reactive barrier system (7, 8). Zero-valent iron is a very promising reactive medium due to its effectiveness, low cost, and ability to degrade contaminants over wide concentration ranges;however,the reaction mechanism remains elusive. Studiesto date have confirmed that the reaction isreductive, abiotic, and heterogeneous. While it has been proposed that the reduction proceeds bydirect electron transfer from the iron surface to the chlorinated organic, the possibility that adsorbed hydrogen from the reduction of water is involved in a catalytic reaction on the iron surface has not been eliminated (6). Abiotic dechlorination of chlorinated hydrocarbons in aqueous solution has received relatively little attention compared to biological systems. Abiotic studies include homogeneous reactions with water (9-11) or reactions mediated bytransition metalcomplexessuch asporphyrins (12-15). Heterogeneous dechlorination reactions in aque- ous solution have been studied for mineral-water systems (16-19), as has electrolysis with platinum electrodes (20). Hydrodechlorination usinga proprietarypalladium catalyst and hydrogen gas has also been reported (21). While some of these reactions are relatively rapid, notably those with the palladium catalyst, abiotic dechlorination generally proceeds too slowlyto be a usefulremediation technology. Iron-enhanced dechlorination proceeds at rates compa- rable to those reported for the palladium catalyst, and it hasthe verysignificant advantage that an engineered system is not required to supply another reactant. This study is based on the results of preliminary design studies for a large-scale field installation ofan in situ reactive barrier. In those tests, it was found that dissolved C1-C5 hydrocarbonswere present in a controlcolumn containing iron and water. Because no organic constituents were present in the influent solution, the source of the hydro- carbonswasunknown. Thisresultissimilarto observations reported by Senzaki and Kumagi (22), who attributed the presence of the hydrocarbons to the transformation of unidentified organics in the source water. The purpose of this study was to identify reaction products and the reaction pathway of iron and aqueous solution systems. It is shown that C1-C5 hydrocarbons are formed bythe reduction ofaqueous CO 2 byzero-valent iron and that the products have an Anderson -Schulz- Flory(ASF)distribution. ASFproduct distributionsare well known in Fischer -Tropsch synthesis where long-chain hydrocarbonsareproduced bycontactingCOand H 2 gases with a heterogeneous catalyst such as iron or nickel (23). A conceptual model is presented which postulates that alkenes and alkanes are formed on the iron surface and that alkenescan be re-incorporated into longer hydrocarbon chains. This conceptual model is used to show that a deviation from an ideal ASF distribution is expected for long-chain hydrocarbons and that significant carbon mass mayremain sorbed to the iron surface. Based on a reaction mechanism proposed for the electroreduction of aqueous CO 2 ,iron in this system acts as both a reactant,bycorroding to supply electrons, and as a catalyst, by promoting the formation ofhydrocarbons. Water is also a reactant in this system. Experimental Section Tests were conducted with various iron and aqueous solution combinations to evaluate the effects of different materials on the hydrocarbons detected in solution. Selected batches ofiron were pretreated with H 2 to increase the concentration of hydrogen in the iron. This pretreat- ment was undertaken to determine if adsorbed hydrogen *Corresponding author. † Present address: Morrow Environmental Consultants, 8658 Commerce Court, Burnaby, BC, V5A 4N6 Canada. Environ. Sci. Technol. 1996, 30, 57-65 0013-936X/96/0930-0057$12.00/0  1995 American Chemical Society VOL. 30, NO. 1, 1996 / ENVIRONMENTAL SCIENCE & TECHNOLOGY 9 57