Soil contamination and remediation Bioremediation Biodegradation technologies in-situ / ex-situ Bioremediation Utilization of microorganisms to destroy or immobilize the contamination Dominantly these organisms are used: • Bacteria (aerobic and anaerobic) • Fungi History of bioremediation 1972 First commercial project: oil pipeline leak Sun Oil, Ambler, Pennsylvania, USA 80. focus on the bacterial research (bioengineering), expected goals were not reached ....... until today return to natural microorganisms, research focuses in their best utilization Mechanisms of bioremediation Microorganisms destroy organic contaminants in process of metabolism or cometabolism Organic compounds supply: carbon – construction of live cells electrons – source of energy Cells catalyze oxidation of organic compounds (of electron donors). Extra electrons from organic matter must be used by electron acceptors. Electron acceptors Aerobic conditions: oxygen Anaerobic conditions (see natural attenuation): nitrates manganese iron sulphates Microorganisms need basic nutrients such as nitrogen or phosphorus as well Oxygen is elec. acceptor Decrease of the energy gain during electron transfer Redox potential (V) (at pH=7) Anaerobic (alternative elec. acceptors) Area of electron acceptors efficiency Aerobic Population of bacteria Growth is very steep where “food” is present – source of carbon. Population doubles each 45 minutes. Clean soils contain 100 to 1000 aerobic bacteria per gram of soil. Population grows to 105 where source of carbon is not depleted. Suitable conditions for bioremediation • • • • Sufficiently large bacteria population Presence of electron acceptors Presence of nutrients (nitrogen and phosphorus) Chemicals not toxic for bacteria (NAPL free phase is often toxic) • Sufficient source of carbon for bacterial growth (contradicting remediation limits for toxicants) degradability Relative capability of biodegradation Simple hydrocarbons degradability decreases with growth of molar weight Aromatic hydrocarbons Alcohols, esters Nitrobenzenes and ether Chlorinated hydrocarbons degradability falls with increasing chlorine substitutions – highly chlorinated compounds (e.g. PCB) and chlorinated solvents can not be degraded easily Pesticides Bioremediation technologies EX-SITU Composting suitable for oil hydrocarbons Slurry phase bioremediation aqueous slurry combines soil, sediment, or sludge with water and other additives - mixed with microorganisms, later dewatered and disposed Biopiling ex-situ – managed biodegradation in heaps (industrial composting) suitable for oil hydrocarbons up to 50000 ppm Landfarming application of the organic matter and consequent irrigation and tillage Managed slurry phase bioremediation soil is decontaminated in the form of slurry within bioreactors or lagoons Zdroj: US ARMY ENVIRONMENTAL CENTER, http://aec.army.mil/usaec/technology/ Composting composting – degradation by microorganisms at raised temperature • Typically 55 – 65°C • Heat is produced by microorganisms • Decrease of bulk density and supply of organic carbon – straw, alfa-alfa, manure, wood chips • Spreading into long rows • Rows are regularly turned over and mixed • Monitoring of pH, temperature and contaminant concentration Composting in rows http://www.rrskw.com/compost_turners.htm Ex-situ managed bioremediation – Biopiling • Soil is mixed with additives and placed onto suitable site • Ventilation device is installed during piling • Pile is 6 m high (max), covered with PE foil Monitoring device air pump pipe perforated pipe Ex-situ managed bioremediation – Biopiling Biopiling – optimal conditions Factor Soil moisture Optimal value 25-85% of saturated Oxygen content >0.2 mg/L dissolved O2 >10% air filled pores REDOX potential Eh > 50 mV Nutrients Temperature C:N:P = 120:10:1 (ratio of molar amounts) 15-45°C pH 5.5 – 8.5 Bioremediation technologies IN-SITU Enriching in situ vadose zone Biostimulation – addition of nutrients into soil environment Bioventing Addition of oxygen to ventilate soil Biosparging Aeration of saturated zone Enriching saturated zone support of bacterial growth and cometabolic processes, addition of alternative electron acceptors Bioremediation IN-SITU Steps of project preparation 1) Field survey • Is contamination under control, does it grow? 2) Laboratory tests • • • • • • • • Amount of bacteria Speed of bacterial activity Bacterial adaptation Concentration of inorganic carbon Concentration of electron acceptors Side products of anaerobic activity Creation of semiproducts of metabolic processes Ration of non-degradable and degradable compounds Bioremediation IN-SITU Steps of project preparation (cont.) 3) Semiroutine experiment in-situ • Stimulation of bacterial growth in the frame of the part of contaminated area • Measurement of consumption of electron acceptor • Monitoring of non-biodegradable tracer compound 4) Modeling • Modeling of abiotic weight loss of contaminant (dissolution, transport, volatilization) 5) Performing the remediation? Bioventing Adding of oxygen (electron acceptor) in unsaturated zone by pressing in or vacuum extracting out of air. Applicable mostly for oil product degradation (also used for PAH). Compared with air sparging – venting uses by far smaller amounts of air. Compressor Air injection Monitoring Contaminant Bioventing Area of bioventing efficiency for chosen hydrocarbons Approximate time for biodegradation Time of landfarming (days) Time of composting (days) Time of compost.+ vacuum aeration (days) Benzene 80-105 60-70 50-58 Toluene 55-79 30-40 20-28 Ethyl-benzene 20-29 22-28 20-26 Xylene 180-206 70-78 60-68 - 184-230 130-184 Total oil hydrocarbons VIRARAGHAVAN, T.; MIHIAL, D.; THOMSON, R.B. A MORTIN M.D.: Bioremediation of a petroleum contaminated site - a feasibility analysis. <http://ce.ecn.purdue.edu/~alleman/w3-piwc/papers/virara.html> Saturated zone enrichment Applicable for oil products (and chlorinated hydrocarbons in limited cases) Saturated zone enrichment Technology of enrichment infiltration by boreholes infiltration by ditches infiltration by irrigation Chemical compouds (carbon source) suitable for enrichment acetate, ethanol, lactate, vegetable oil Enrichment of the groundwater by electron acceptors oxygen, hydrogen peroxide, methane, nitrate Bioremediation – case studies Brown Wood Preserving Superfund Site (Live Oak, Florida (USA) contaminants: PAH (benzo(a)pyrene, benzo(a)anthracene, chrysene, benzo(b)fluorantene) concentration prior to remediation: 100-208 mg/kg soil amount: 6200 m3 technology: land farming concentration after remediation: 23 – 92 mg/kg time of remediation: 18 months (1989-1990) costs: $ 565 400, approx $90 / m3 More at: http://www.clu-in.org/products/costperf/LNDTREAT/Brown.htm Bioremediation – case studies French Limited Superfund Site (Crosby, Texas, USA) contaminants: benzo(a)pyrene, VC, benzene concentration prior to remediation: 400-5000 mg/kg soil amount: 300 000 tons technology: managed slurry phase bioremediation concentration after remediation : 7 – 43 mg/kg costs: $ 49 000 000 More at: http://www.clu-in.org/products/costperf/BIOREM/French.htm References M. Kubal, J. Burkhard, M. Březina, VŠCHT, Praha 2002, http://www.vscht.cz/uchop/CDmartin/8-nejcasteji/3-2.html VIRARAGHAVAN, T.; MIHIAL, D.; THOMSON, R.B. A MORTIN M.D.: Bioremediation of a petroleum - contaminated site - a feasibility analysis. <http://ce.ecn.purdue.edu/~alleman/w3-piwc/papers/virara.html> Norris et al. Handbook of Bioremediation, Lewis publishers, 1994 MIT Open courseware Civil and Environmental Engineering » Waste Containment and Remediation Technology, Spring 2004 http://ocw.mit.edu/OcwWeb/Civil-andEnvironmental-Engineering/1-34Spring2004/LectureNotes/index.htm
© Copyright 2026 Paperzz