VB997® soil Used
for Soil Bioremediation Guadalupe Oil field The principal land use at TB9 from 1946 to March 1944 was the production of oil and natural gas. The production company first acquired a 49 percent interest in the field in 1951 and purchased the remaining 51 percent in June 1953. Peak oil production of approximately 4,500 barrels per day occurred in the 1980s from 215 potential oil wells. Oil production ceased April 1994. The Crude oil produced at TB9 was extremely viscous. To enhance the production and transportation of the heavy crude oil, a refined petroleum product referred to as diluent was introduced at the site. The composition of the diluent was similar to that of a mixture of kerosene and diesel oil, and was derived from the distillation of crude oil. Over the years, diluent was inadvertently released from the pipelines and storage tanks and is now present in soils and groundwater at the site. Climate Topography Geology The dune sand is underlain by Late Quaternary alluvium, which Worts (1951) divided into two members: an upper fine-grained member “Upper Alluvium” and a lower course-grained member “Lower Alluvium.” The Upper Alluvium ranges from approximately 60 to 120 feet thick, and consists of interbeded sand and silt, with some clay. The Lower Alluvium consists of gravel and sand with sparse lenses of silt. Its thickness is similar to the Upper Alluvium. Applicability of Biological Land Treatment The primary reactions created during bioremediation are oxidation-reduction reactions that yield free energy that microorganisms can then use for cell growth and reproduction. Because these catalyzed oxidation-reduction reactions are dependent on the presence of microorganisms and the enzymes that they produce, environmental control is necessary for enzyme production and the desired reactions. The chemical and physical parameters of the environment must be controlled in order to stimulate the growth of indigenous (native) microbes in the soil to enhance the degradation of target contaminant compounds. Biological degradation of petroleum hydrocarbons is a naturally occurring process. Complete destruction or mineralization of petroleum hydrocarbons ultimately results in the production of carbon dioxide, water, and microbial biomass. However, the rate of this reaction is highly dependent on a variety of factors, including the specific compound structure and its bioavailability to the microbes; the availability of oxygen, nutrients, moisture, and pH; and the nature of the soil or other matrix in which the petroleum resides. Certain compounds can be biologically degraded over a very short time (hours), whereas other compounds such as asphaltenes are slow to degrade. The availability of oxygen has a significant effect on petroleum degradation. Studies have shown that the greatest rate of hydrocarbon degradation occurs when oxygen is used as the terminal electron acceptor (Atlas and Bartha, 1993; Schneider and Billingsley, 1990; Riser-Roberts, 1998). During biodegradation, microorganisms transfer electrons from donors to acceptors. This results in the oxidation of the electron donor and reduction of the electron acceptor. This oxidation-reduction reaction yields free energy that the microorganisms can use for cell maintenance and reproduction. In addition to oxygen, microorganisms require relatively large amounts of nutrients such as nitrogen and phosphorous for cell growth and reproduction and the appropriate pH, moisture content, and the temperature range to enhance hydrocarbon biodegradation rates. Solid-phase biological treatment processes are designed to remove constraints that slow degradation rates, such as limited oxygen and nutrient concentrations, to bring about rapid rates of degradation. Application Methodology
*Contractor was able to maintain only 6-8 percent moisture content throughout project. Guadalupe, California Remediation Project
Using VB997®
Guadalupe, California Remediation Project
Using VB997®
Overview Sampling Locations and Methods The cell was divided into quarter sections. From each quarter, five (5) approx.1 liter samples were taken from the vertical midpoint of the cell and homogenized to produce one composite batch for semi-volatile 8015 analysis and PCBs.
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