05.06.2013 Views

PNNL-13501 - Pacific Northwest National Laboratory

PNNL-13501 - Pacific Northwest National Laboratory

PNNL-13501 - Pacific Northwest National Laboratory

SHOW MORE
SHOW LESS

You also want an ePaper? Increase the reach of your titles

YUMPU automatically turns print PDFs into web optimized ePapers that Google loves.

Summary and Conclusions<br />

Over the past few years the <strong>Laboratory</strong> has made great<br />

strides in advancing the use of In Situ Redox<br />

Manipulation technology for the transformation/<br />

degradation of redox-sensitive contaminants such as<br />

chromate and trichloroethylene. The technology involves<br />

the injection of a dithionite solution that transforms<br />

(structural) Fe(III) to Fe(II), thus establishing a reductive<br />

Fe(II) barrier in the flow path of the plume. Large-scale<br />

field implementation of the In Situ Redox Manipulation<br />

technology is now under way at Hanford for chromate<br />

remediation. Given the large magnitude of the operation,<br />

it is critical to evaluate the performance and costeffectiveness<br />

of any proposed design for the barrier. The<br />

main components of the cost model are the drilling costs,<br />

the cost of reagents, the cost of waste disposal, and the<br />

labor costs. The key design variables are the number of<br />

wells, their flow rate, and the number of regenerations of<br />

the barrier. The design variables affect the total cost in<br />

different ways. Increasing the number of wells will<br />

decrease the total amount of dithionite required and will<br />

generate less waste. A smaller barrier width will decrease<br />

the loss and wastage of reductive capacity, but will<br />

increase the costs related to more frequent regeneration.<br />

We developed a code for optimal selection of key design<br />

parameters that would yield a robust design and also<br />

minimize the total cost of the remediation effort. The cost<br />

model is driven by the process model consisting of two<br />

parts: 1) the creation of the barrier by injecting the<br />

reducing agent, and 2) the reoxidation of the barrier by<br />

the contaminant (and also oxygen if aerobic) in the<br />

invading groundwater. We also considered the loss of<br />

reducing capacity that can occur due to rainfall events and<br />

due to the diffusion of oxygen from the atmosphere. The<br />

solution to the reoxidation submodel was combined with<br />

the known solution to the reduction submodel to develop<br />

an analytic objective function (cost of the operation) in<br />

terms of the key decision variables (assuming a<br />

homogeneous system). We developed an engineering<br />

design tool to obtain optimal design parameters and also<br />

their sensitivity to uncertainties in the physiochemical<br />

description of the problem.<br />

Publication<br />

Chilakapati A, MD Williams, SB Yabusaki, CR Cole, and<br />

JE Szecsody. 2000. “Optimal design of an in situ Fe(II)<br />

barrier: Transport limited reoxidation.” Environmental<br />

Science and Technology (submitted).<br />

Earth System Science 199

Hooray! Your file is uploaded and ready to be published.

Saved successfully!

Ooh no, something went wrong!