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EFFECTS OF AQUIFER THERMAL ENERGY STORAGE  (ATES) ON MOBILE CONTAMINANTS IN A GROUNDWATER SYSTEM: A MODEL APPROACH Koen Zuurbier  (KWR, VU, Deltares), Niels Hartog (Deltares),  Johan Valstar (Deltares), Boris van Breukelen (VU), Vincent Post (VU) 26.11.2010, Flinders, Australia
2. Background: ATES and mobile contaminants ,[object Object],[object Object],[object Object],[object Object],[object Object],15 - 20  o C 6 - 8  o C
2. Background: ATES and mobile contaminants ,[object Object],[object Object],[object Object],[object Object],[object Object]
2. Background: ATES and mobile contaminants IF Technology Doublet Summer Winter
2. Background: ATES and mobile contaminants ATES   ≠  Geothermal Energy! Heat & cold demand Heat demand Building = supply+user Building = user
2. Background: ATES and mobile contaminants BTES (Borehole Thermal Energy Storage): Closed loop systems  Horizontal Vertical
2. Background: ATES and mobile contaminants ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],ρ DNAPL  >  ρ water
[object Object],[object Object],2. Background: ATES and mobile contaminants Risks? Conflict Potential benefits? (source: Sanergy.nl)
2. Background: ATES and mobile contaminants ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
2. Background: ATES and mobile contaminants  Aim of my study: What effect does ATES have on existing potential contaminant plumes?  (focus on PCE, source contaminant) ,[object Object],[object Object],[object Object]
2. Background: ATES and mobile contaminants  Aim of my study: What effect does ATES have on existing potential contaminant plumes? ,[object Object],[object Object],[object Object]
2. Background: ATES and mobile contaminants ,[object Object],[object Object],[object Object],Reductive dechlorination VOCl (Wiedemeier, 1999) Source Products following degradation
2.  Background: ATES and mobile contaminants ,[object Object],[object Object],[object Object]
2. Background: ATES and mobile contaminants  ,[object Object],[object Object],How to describe degradation: C i = concentration component i (kg m -3 ) t = time (s) λ 0 = degradation constant 0 e  order (kg m -3  s -1 ) ,[object Object],[object Object],C i = concentration component i (kg m -3 ) t = time (s) λ 0 = degradation constant 1 e  order (s -1 ) C 0 = initial concentration component i (kg m -3 ) Degradation constants ( λ 0 , λ 1 ) vary with redox-conditions and component: Limited degradation of DCE and especially vinylchloride in anoxic environments Larger aquifer volume contaminated = more mass removal!!
2. Background: ATES and mobile contaminants  How to describe degradation: Monod kinetics: combination of 0 th  and 1 st  -order Not modelled (yet) At high C At low C
3. Methods: modelling tools No integral modelling code available Flow:   MODFLOW Transport:   MT3DMS Density/Viscosity  + SEAWAT (V4) Reactions:   PHT3D (V2) (PHREEQC) Plume blending:  Multi-Node-Well Package (MODFLOW) (total discharge    discharge per model layer) (mixing concentrations in well) Compilation
4. Case study ‘Uithof’ ,[object Object],[object Object],[object Object],[object Object],   added (in model only)
4. Case study ‘Uithof’ You are here Temp injection  = 8  o C / 16  o C Temp background  = 10,5  o C  Imbalance:  net 1.2 % to K1
4. Case study ‘Uithof’ You are here Temp injection  = 8  o C / 16  o C Temp background  = 10,5  o C  Imbalance:  net 1.2 % to K1 N.B.: Start installation in last week of November (week 1)
4. Case study ‘Uithof’ 2.8 m 50 m 56 m 41 m Vertical Cross-section 39 m 1760 m 135 m Holocene cover Aquif. 1A Sandy clay Aquif. 1B Aquitard Aquif. 2 DNAPL Holocene cover Aquif. 1A Sandy clay Aquif. 1B Aquitard Aquif. 2
4. Case study ‘Uithof’ Scenario’s Here: degradation using 0 th  –order (1.1*10 -9  mol L -1  d -1 ) ? x x x All factors present S-4 Increasing mass in aquifer, large volume contaminated x x Degradation absent S-3 Initial increase in volume, followed by decrease (increased degr.+blending) x x DNAPL absent S-2 Contaminated plume in +/- original size x Reference:  No DNAPL, no ATES S-1 Predicted effect DNAPL ATES Degr. Characteristics Scenario
5. Results ,[object Object],[object Object],[object Object],Future ATES warm bubble t = 40 yr: Initial plume Conc. requiring remediation (I)
5. Results ,[object Object],[object Object],[object Object],Future ATES warm bubble PCE, base of aquifer 1 t = 40 yr: Initial plume Conc. requiring remediation (I)
5. Results ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
5.  Results ,[object Object],Mainly remaining in aquitard
5.  Results
5.  Results ,[object Object],[object Object],[object Object],S I
t = 19 jaar
5.  Results ,[object Object],[object Object],[object Object]
5.  Results
5.  Results ,[object Object],[object Object],[object Object],[object Object],[object Object],S I
5. Results ,[object Object],[object Object],[object Object],[object Object],[object Object]
5. Results ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
6.  Discussion ,[object Object],[object Object],[object Object],[object Object]
6.  Discussion ,[object Object],[object Object],[object Object],[object Object]
6.  Discussion ,[object Object]
6. Discussion ,[object Object],[object Object],[object Object],[object Object],[object Object]
7. Conclusions ,[object Object],[object Object],[object Object],[object Object],[object Object]

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Flinders University - ATES and contaminated groundwater

  • 1. EFFECTS OF AQUIFER THERMAL ENERGY STORAGE (ATES) ON MOBILE CONTAMINANTS IN A GROUNDWATER SYSTEM: A MODEL APPROACH Koen Zuurbier (KWR, VU, Deltares), Niels Hartog (Deltares), Johan Valstar (Deltares), Boris van Breukelen (VU), Vincent Post (VU) 26.11.2010, Flinders, Australia
  • 2.
  • 3.
  • 4. 2. Background: ATES and mobile contaminants IF Technology Doublet Summer Winter
  • 5. 2. Background: ATES and mobile contaminants ATES ≠ Geothermal Energy! Heat & cold demand Heat demand Building = supply+user Building = user
  • 6. 2. Background: ATES and mobile contaminants BTES (Borehole Thermal Energy Storage): Closed loop systems Horizontal Vertical
  • 7.
  • 8.
  • 9.
  • 10.
  • 11.
  • 12.
  • 13.
  • 14.
  • 15. 2. Background: ATES and mobile contaminants How to describe degradation: Monod kinetics: combination of 0 th and 1 st -order Not modelled (yet) At high C At low C
  • 16. 3. Methods: modelling tools No integral modelling code available Flow: MODFLOW Transport: MT3DMS Density/Viscosity + SEAWAT (V4) Reactions: PHT3D (V2) (PHREEQC) Plume blending: Multi-Node-Well Package (MODFLOW) (total discharge  discharge per model layer) (mixing concentrations in well) Compilation
  • 17.
  • 18. 4. Case study ‘Uithof’ You are here Temp injection = 8 o C / 16 o C Temp background = 10,5 o C Imbalance: net 1.2 % to K1
  • 19. 4. Case study ‘Uithof’ You are here Temp injection = 8 o C / 16 o C Temp background = 10,5 o C Imbalance: net 1.2 % to K1 N.B.: Start installation in last week of November (week 1)
  • 20. 4. Case study ‘Uithof’ 2.8 m 50 m 56 m 41 m Vertical Cross-section 39 m 1760 m 135 m Holocene cover Aquif. 1A Sandy clay Aquif. 1B Aquitard Aquif. 2 DNAPL Holocene cover Aquif. 1A Sandy clay Aquif. 1B Aquitard Aquif. 2
  • 21. 4. Case study ‘Uithof’ Scenario’s Here: degradation using 0 th –order (1.1*10 -9 mol L -1 d -1 ) ? x x x All factors present S-4 Increasing mass in aquifer, large volume contaminated x x Degradation absent S-3 Initial increase in volume, followed by decrease (increased degr.+blending) x x DNAPL absent S-2 Contaminated plume in +/- original size x Reference: No DNAPL, no ATES S-1 Predicted effect DNAPL ATES Degr. Characteristics Scenario
  • 22.
  • 23.
  • 24.
  • 25.
  • 27.
  • 28. t = 19 jaar
  • 29.
  • 31.
  • 32.
  • 33.
  • 34.
  • 35.
  • 36.
  • 37.
  • 38.