POWERPOINT PRESENTATION Gas Clogging During Spreading Basin Recharge Victor Heilweil, Ph.D. Research Hydrologist U.S. Geological Survey West Valley City, Utah Managed Aquifer Recharge Symposium January 25-26, 2011 Irvine, California Symposium Organizers: National Water Research Institute Orange County Water District Water Research Foundation www.nwri-usa.org/rechargesymposium2011.htm
Gas Clogging During Spreading Basin Recharge Victor Heilweil US Geological Survey Kip Solomon University of Utah
Entrapped gases in aquifers From Glass and Nichols, GRL, 1995 Entrapped air is no longer connected to the atmosphere, occurring in the form of small, immobilized, disconnected bubbles (Faybishenko, WRR,1995) Entrapped air and other gases have been documented to occupy 7 to 20 % of otherwise saturated pore spaces (Beckwith and Baird, WRR, 2001; Heilweil et al., GW, 2004)
Sources of gas bubbles Entrapped air: bubbles formed during saturation as the water table rises in response to artificial or natural recharge (Constantz et al., SSSA, 1988; Holocher et al., EST, 2003) Biogenic gas production: CO 2 and CH 4 bubbles formed by respiration and decay of organic material in sediments beneath a spreading basin (Beckwith and Baird, WRR, 2001; Heilweil et al., BGM, 2009) Denitrification: N 2 gas bubbles produced during biodegredation by denitrifying bacteria (Oberdorfer and Peterson, GW, 1985)
Pore-throat clogging reduces permeability Entrapped gas bubbles typically block the largest pore throats, causing increased tortuosity and permeability reduction
Managed Aquifer Recharge at Sand Hollow Spreading basin MAR Navajo Sandstone Aquifer West Pond Experiment Reservoir East 2 km Heilweil et al., USGS Tech Pub 116, 2000
Navajo Formation Well-sorted eolian sandstone Porosity ~ 20 % K sat ~ 0.7 m/d
Pond Experiment, 2000-2001 Heilweil et al., GW, 2004 Goals: Estimate long-term saturated infiltration rates Evaluate permeability reduction caused by trapped gas
Intrinsic permeability doubled during the first four months Increase caused by gas dissolution and 8% reduction in bubble volume with cooler temperatures cooled from 30 to 5 C Intrinsic permeability (cm 2 ) 5.0E-11 4.0E-11 3.0E-11 2.0E-11 1.0E-11 Gas dissolution Jul-00 Oct-00 Jan-01 May-01
Gas-partitioning tracer test Dissolved bromide and helium added to pond Helium is low solubility and partitions to gas phase, causing retardation Transfer from aqueous to gas phase determined by Henry s Law: C aq = H C g If equilibrium transfer, gasfilled porosity calculated from retardation of helium: g = (R-1)/H
Saturated conditions observed in upper 2 m beneath pond Port at 1.5 m beneath pond 22 days Helium substantially retarded at all ports Observed retardation factors of 2 to 12 156 days
Heilweil et al., Groundwater, 2004 CXTFIT Modeling Helium transfer was kinetically limited 7 to 13 % of porosity filled with trapped gas (Heilweil et al., GW, 2004)
Unsaturated laboratory K(θ) results Unsaturated Hydraulic Conductivity (m/d) 1.0E+00 1.0E-01 1.0E-02 1.0E-03 1.0E-04 Sandstone (1.5 m depth) 1.0E-05 10% reduction 1.0E-06 0.00 0.20 0.40 0.60 0.80 1.00 Saturation 10-fold reduction Testing indicates that 10% trapped air in the Navajo Sandstone causes a 10-fold reduction in hydraulic conductivity
Sand Hollow Reservoir completed 2002
Conceptual Model 2002 2004 2006 Vertical Exaggeration 100:1
Sand Hollow Reservoir Recharge (Heilweil and Marston, USGS SIR, 2011) 0.140 Recharge rate (m/d) 0.120 0.100 0.080 0.060 0.040 0.020 Recharge rates much lower than K sat of 0.7 m/d Calibration of MODFLOW model to K sat and hydraulic gradients indicates clogging layer must exist Likely combination of siltation and gas bubbles 0.000 Feb-02 Feb-03 Feb-04 Feb-05 Feb-06 Feb-07 Feb-08 Feb-09 Feb-10
Dissolution of trapped gas bubbles Trapped gas bubbles will dissolve according to Henry s Law Dissolution of gases can occur as quickly as hours or as slow as years (Glass and Nicholl, 1995; Heilweil et al., 2004) Dissolution rate dependent on: Water temperature (more soluble in cooler water) Hydrostatic head (more soluble under higher pressure) Rate of flow by gas bubble (number of pore volumes) Gas solubility (O 2 dissolves more readily than N 2 )
Excess Gas/Air Trapped gas/air dissolved to become excess gas/air (Heaton and Vogel, 1981) Since surface water contains little excess air, it can be used as a tracer of artificial recharge (Clark and Hudson, 2005; Massmann and Sultenfub, J. Hydrol. 2008) Potential tracers of artificial recharge include: Total dissolved gas pressure (TDGP) Dissolved oxygen (DO) Neon excess (Δ Ne) Noble-gas excess air (E a )
Near-field monitoring wells for dissolvedgas sampling
Total Dissolved-Gas Pressure (TDGP) 2,500? DISSOLVED GAS PRESSURE, MM HG 2,000 1,500 1,000 500 0 WD 9 (20 m) WD 11 (50 m) WD 6 (300 m) Atmospheric pressure (680 mm Hg) (Heilweil and Marston, 2011) Jan-01 Jan-02 Jan-03 Jan-04 Jan-05 Jan-06 Jan-07 Jan-08 Jan-09 Jan-10 Conservative tracer Measured with TDGP probe or Diffusion Sampler High pressures (> 3 atmospheres) = large amount of trapped gas
Dissolved Gas Tracer Peaks Site Distance from Reservoir (m) Peak TDGP (mm Hg) Peak DO (mg/l) Peak Neon Excess WD 9 20 >2250 26 250% WD 11 50 >2250 25 320% WD 6 300 1700 22 160% (Heilweil and Marston, 2011)
Noble Gases Bunsen Coefficient ( cc L 1 atm 1 ) 250 200 150 100 50 Kr Ar 0 He Ne 0 5 10 15 20 25 30 35 40 Temperature ( C) Xe Each gas has different solubility If a bubble partially dissolves, dissolved gases will be preferentially enriched in heavier noble gases (Xe, Kr) This fractionation factor (F) can be used to evaluate when trapped gas is dissolved
Calculation of time to dissolve trapped air Assuming: 30 m 3 total volume 30-m rise in water table x 20% porosity = 6 m 3 20% air-filled porosity = 1.2 m 3 trapped air 80% saturated porosity = 4.8 m 3 water Trapped air predominantly N 2 (78% of atmosphere) Increased nitrogen solubility with hydrostatic pressure 45 m 3 of water to dissolve trapped air 9 pore volumes at Q = 0.014 m 3 /d About 9 years to dissolve majority of trapped air 30 m 3 total unit volume Q = 0.014 m 3 /d 24 m 3 aquifer solids 4.8 m 3 water 1.2 m 3 trapped air
Increased recharge rates during 2008-2009 may be due to gas dissolution around edges of reservoir 0.030 0.025 Reservoir filling complete (2006) 0.020 0.015 Final gas dissolution currently occurring? 0.010 0.005 0.000 Jul-03 Jul-04 Jul-05 Jul-06 Jul-07 Jul-08 Jul-09
Same volume of trapped gas would dissolve much faster in more permeable materials Material K sat (m/d) K(θ) (m/d) Q (m 3 /d) Estimated Time (days) Sandstone 0.7 0.12 0.014 3,200 Medium sand 5 1.04 0.125 360 Gravel 50 13.9 1.667 30 Cobbles 250 104 12.5 4
Summary Entrapped gas clogs pore throats and causes significant permeability reduction Effects are more pronounced in finer-grained materials Entrapped gas will eventually dissolve with increased hydrostatic pressure The dissolution process can be monitored with TDGP, DO, and noble gases (neon excess, A e, F) It may take about a decade to dissolve most of the trapped gas beneath Sand Hollow; much less time for recharge facilities located on higher permeability sediments
Acknowledgements We would like to acknowledge our partner in this work, the Washington County Water District. In particular, we appreciate the assistance of Corey Cram and Ron Thompson.
References Beckwith and Baird, 2001, Effect of biogenic gas bubbles on water flow through poorly decomposed blanket peat, Water Resources Research 37 (3): 551-558. Clark and Hudson, 2005, Excess Air: a new tracer for artificially recharged surface water, Proceedings of the 5 th International Symposium on Management of Aquifer Recharge, UNESCO, Berlin: 342-347. Constantz, Herkelrath, and Murphy, 1988, Air encapsulation during infiltration, Soil Science Society of America Journal 52: 10-16. Faybishenko, 1995, Hydraulic behavoir of quasi-saturated soils in the presence of entrapped air: Laboratory experiments, Water Resources Research 31 (10): 2421-2435. Fry, Istok, Semprini, O Reilly, and Buscheck, 1995, Retardation of dissolved oxygen due to a trapped gas phase in porous media, Ground Water 33 (3): 391-398. Glass and Nicholl, 1995,Quantitative visualization of entrapped phase dissolution within a horizontal flowing fracture, Geophysical Research Letters 22 (11), 1413-1416. Heaton and Vogel, 1983, Excess Air in groundwater, Journal of Hydrology 50: 201-216. Heilweil, Freethey, Stolp, Wilkowske, and Wilbert, 2000, Geohydrology and numerical simulation of ground-water flow in the central Virgin River Basin of Iron and Washington Counties, Utah, Utah Dept. of Natural Resources Tech. Pub. 116.
References (cont.) Heilweil and Marston, 2011, Assessment of artificial recharge at Sand Hollow Reservoir, Washington County, Utah, Updated to conditions through 2009, U.S. Geological Survey Scientific Investigations Report 2011-XXXX. Heilweil, Solomon, Perkins, and Ellett, 2004, Gas-partitioning tracer test to quantify trapped gas during recharge, Ground Water 42 (4), 589-600. Holocher, Peeters, Aeschbach-Hertig, Kinzelbach, and Kipfer, 2003, Kinetic model of gas bubble dissolution in groundwater and its implications for the dissolved gas composition, Environmental Science and Technology 37 (7), 1337-1343. Massmann and Sultenfub, 2008, Identification of processes affecting excess air formation during natural bank filtration and managed aquifer recharge, Journal of Hydrology 359: 235-246. Oberdorfer and Peterson, 1985, Waste-Water Injection: Geochemical and biogeochemical clogging processes, Ground Water 23 (6), 753-761.