using predictive uncertainty analysis to optimise tracer test design and data acquisition
TRANSCRIPT
Accepted Manuscript
Using predictive uncertainty analysis to optimise tracer test design and dataacquisition
Ilka Wallis, Catherine Moore, Vincent Post, Leif Wolf, Evelien Martens,Henning Prommer
PII: S0022-1694(14)00335-7DOI: http://dx.doi.org/10.1016/j.jhydrol.2014.04.061Reference: HYDROL 19592
To appear in: Journal of Hydrology
Received Date: 26 November 2013Revised Date: 18 March 2014Accepted Date: 24 April 2014
Please cite this article as: Wallis, I., Moore, C., Post, V., Wolf, L., Martens, E., Prommer, H., Using predictiveuncertainty analysis to optimise tracer test design and data acquisition, Journal of Hydrology (2014), doi: http://dx.doi.org/10.1016/j.jhydrol.2014.04.061
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Using predictive uncertainty analysis to optimise tracer 1
test design and data acquisition 2
3
Ilka Wallis* 1,2
, Catherine Moore3,4
, Vincent Post1,2
,Leif Wolf5, Evelien Martens
6 and Henning 4
Prommer2,6,7
5
6
1School of the Environment, Flinders University, Adelaide, GPO Box 2100, SA 5001, 7
Australia 8
2National Centre for Groundwater Research and Training, Flinders University, Adelaide, GPO 9
Box 2100, SA 5001, Australia 10
3CSIRO Land and Water, Dutton Park QLD 4102, Australia 11
4Institute of Environmental Science and Research Ltd, Porirua 5240, New Zealand
12
5 Karlsruhe Institute of Technology, Kaiserstr. 12, 76131 Karlsruhe, Germany 13
6CSIRO Land and Water, Private Bag No. 5, Wembley WA 6913, Australia 14
7School of Earth and Environment, University of Western Australia, Crawley, 6009 15
16
*corresponding author; email: [email protected]; Tel: +61 8 8201 2020; Fax +61 8 17
8201 3567 18
Submitted to Journal of Hydrology 19
20
21
22
ABSTRACT 23
Tracer injection tests are regularly-used tools to identify and characterise flow and transport 24
mechanisms in aquifers. Examples of practical applications are manifold and include, among 25
others, managed aquifer recharge schemes, aquifer thermal energy storage systems and, 26
increasingly important, the disposal of produced water from oil and shale gas wells. The 27
hydrogeological and geochemical data collected during the injection tests are often employed to 28
assess the potential impacts of injection on receptors such as drinking water wells and regularly 29
serve as a basis for the development of conceptual and numerical models that underpin the 30
prediction of potential impacts. 31
As all field tracer injection tests impose substantial logistical and financial efforts, it is crucial to 32
develop a solid a-priori understanding of the value of the various monitoring data to select 33
monitoring strategies which provide the greatest return on investment. 34
In this study, we demonstrate the ability of linear predictive uncertainty analysis (i.e. “data 35
worth analysis”) to quantify the usefulness of different tracer types (bromide, temperature, 36
methane and chloride as examples) and head measurements in the context of a field-scale aquifer 37
injection trial of coal seam gas (CSG) co-produced water. Data worth was evaluated in terms of 38
tracer type, in terms of tracer test design (e.g., injection rate, duration of test and the applied 39
measurement frequency) and monitoring disposition to increase the reliability of injection impact 40
assessments. This was followed by an uncertainty targeted Pareto analysis, which allowed the 41
interdependencies of cost and predictive reliability for alternative monitoring campaigns to be 42
compared directly. 43
For the evaluated injection test, the data worth analysis assessed bromide as superior to head 44
data and all other tracers during early sampling times. However, with time, chloride became a 45
more suitable tracer to constrain simulations of physical transport processes, followed by 46
methane. Temperature data was assessed as the least informative of the solute tracers. However, 47
taking costs of data acquisition into account, it could be shown that temperature data when used 48
in conjunction with other tracers was a valuable and cost-effective marker species due to 49
temperatures low cost to worth ratio. In contrast, the high costs of acquisition of methane data 50
compared to its muted worth, highlighted methanes unfavourable return on investment. Areas of 51
optimal monitoring bore position as well as optimal numbers of bores for the investigated 52
injection site were also established. 53
The proposed tracer test optimisation is done through the application of common use 54
groundwater flow and transport models in conjunction with publicly available tools for 55
predictive uncertainty analysis to provide modelers and practitioners with a powerful yet 56
efficient and cost effective tool which is generally applicable and easily transferrable from the 57
present study to many applications beyond the case study of injection of treated CSG produced 58
water. 59
Keywords: experimental design, tracer tests, coal seam gas, data worth, linear predictive 60
uncertainty analysis, optimisation, Pareto analysis 61
1. Introduction 62
63
Tracer injection tests are regularly-used tools to identify and characterise flow and transport 64
mechanisms in aquifers. Such tests can be used to derive subsurface hydraulic properties, and to 65
investigate the transport behaviour of both non-reactive and reactive solutes in groundwater. 66
Examples of practical applications are manifold and include, among others, managed aquifer 67
recharge schemes (e.g. Culkin et al., 2008, Descourvieres et al., 2010, Wallis et al., 2011), 68
aquifer thermal energy storage systems (e.g., Zuurbier et al. 2013), the storage of CO2 emissions 69
in deep aquifers (e.g. Michael et al., 2010) and, increasingly important, the disposal of treated 70
coals seam gas (CSG) production water or produced water from oil and shale gas wells into deep 71
aquifers (NWC, 2011; U.S. Dep. of the Interior, 2011). The hydrogeological and geochemical 72
data collected during the injection tests often serve as a basis for the development and 73
parameterisation of conceptual and numerical models that are subsequently used to predict the 74
larger-scale and longer-term hydraulic and water quality impacts of operational injection, storage 75
and abstraction schemes. 76
77
All field tracer injection tests impose substantial logistical and financial efforts. This is 78
particularly so within the context of injection of CSG-produced water, given the often 79
considerable depth of the targeted aquifers, in many cases exceeding 1 km. A significant number 80
of sampling events is often not only required during injection, especially under dynamically 81
changing flow conditions, but also in the post-injection monitoring phase, to capture long-term 82
geochemical changes. Monitoring may include continuous recording of various data types using 83
cost-effective down-hole sensors, for example for temperature, pressure or electrical conductivity 84
data (Ma et al., 2012). However, data acquisition for most chemical constituents to date still 85
relies on more costly laboratory analysis of water samples. To minimise efforts and costs, 86
sampling strategies that can most efficiently identify and characterise the transport mechanisms 87
and geochemical processes in the targeted aquifers within the given budget and access 88
constraints need to be chosen. A robust a priori understanding of the costs and the value (i.e., 89
data worth) of the available data types will allow (i) optimisation of the trial design (e.g., types of 90
tracers amended, concentrations of amended tracers, duration of amendment); (ii) optimisation of 91
monitoring strategies (e.g., type and frequency of the collected data); and (iii) reduction of the 92
uncertainty of model predictions, and thus maximise the predictive power of models simulating 93
long-term impacts during and after operational injection. The proposed methodology requires to 94
set up a numerical groundwater model already ahead of the trial. 95
96
Within the context of water resources modelling, the assessment of “data worth” involves 97
quantification of the utility of observation data in reducing the uncertainty of model predictions 98
of future environmental behaviour (e.g., first or mean contaminant arrival time, magnitude of 99
plume spreading) which underpin management decisions. The value of a data type or an 100
observation location is greater, the more it enhances the certainty with which the model is able to 101
predict such environmental behaviour. By comparing the difference in predictive uncertainty 102
with or without such data, the value of potential observations is assessed. Predictive uncertainty 103
is typically computed using global optimisation methods, such as Monte Carlo simulations (e.g.. 104
James and Gorelick, 1994, Parker et al., 2010), Fu and Gómez-Hernández, 2008). Monte Carlo 105
techniques often pose a considerable computational burden, as they consist of performing a large 106
number of forward model runs based on a random selection from model parameter distributions. 107
Their application therefore remains restricted mostly to groundwater models of limited run-time. 108
In order to assess data worth within the context of field-scale, multi-species non-reactive as well 109
as reactive transport problems, where model run times and the number of adjustable parameters 110
can be high, a computationally more efficient approach is desirable. A methodology which is 111
applicable to field-scale problems was initially presented by Moore and Doherty (2005) and later 112
extended by Christensen and Doherty (2008). This analysis is based on linear predictive 113
uncertainty analysis formulated for distributed parameter models and is incorporated as the 114
freely-available prediction uncertainty tools PREDUNC and PREDVAR into the PEST suite 115
(Doherty, 2010a, b) (Figure 1). The approach derives estimates of simulated prediction 116
uncertainty based on direct propagation of uncertainties originating from incomplete knowledge 117
of model parameters. Computational efficiency is gained by assuming that the system response is 118
sufficiently linear over the range of evaluated parameters to establish relative contributions to 119
uncertainty. This allows the calculation of predictive uncertainty to be made rapidly, so that it 120
can be repeated for many alternative monitoring strategies (potential monitoring sites, potential 121
observation data types and sampling times). 122
123
The methodology has been successfully applied to several synthetic numerical groundwater 124
model problems. Moore (2005), for example, investigated the worth of spatially distributed head 125
and hydraulic conductivity measurements with respect to the reliability of contaminant transport 126
predictions. Dausman et al (2010) investigated the relative worth of salinity and temperature 127
observations for predictions of the location of a theoretical salt water–fresh water interface, while 128
Fienen et. al (2010) used prediction uncertainty analysis to explore its use in a hypothetical 129
water-level monitoring network design by analysing the worth of head measurements for 130
drawdown and flux predictions. A recent example of the practical application of data worth to a 131
field-scale problem was presented by Engelhardt et al. (2013), where the suitability of the 132
artificial sweetener acesulfame as conservative tracer for sewage related fluxes and its value in 133
constraining simulated water and mass-fluxes was investigated. Nevertheless, a wider range of 134
studies which demonstrate the robustness of this methodology to field-scale problems in 135
hydrogeologically and geochemically heterogeneous porous media is still lacking, and moreover, 136
its use in conjunction with minimising the actual cost of data acquisition has also not been 137
demonstrated. This allows for the evaluation of a monitoring strategy subject to both cost and 138
rigour constraints and is of particular importance in the water resources context, where 139
monitoring is typically a significant effort and often under public scrutiny. 140
141
In this study, we demonstrate the ability of linear predictive uncertainty analysis (hereafter 142
simply referred to as “data worth analysis”) to quantify the usefulness of different tracer types 143
and head measurements in the context of a field-scale aquifer injection trial of CSG co-produced 144
water. Data worth is evaluated in terms of the degree to which chemical concentrations, 145
temperature and head data increase the reliability of injection impact assessments, employing the 146
metrics of dilution and time of travel. The relative merits of different tracer test designs are 147
explored. These differ in terms of where and when tracer concentrations are collected, the 148
injection rate and duration of the test, the tracer concentration to ambient concentration ratios 149
(signal to noise ratios) and the applied measurement frequency. We then formulate the trade-off 150
between the established relative value of tracer data on the one hand and the costs of its 151
acquisition on the other hand (Figure 1) to select monitoring strategies which provide the greatest 152
return for investment. 153
154
2. Data worth methodology 155
The uncertainty analysis theory underpinning the methodology of data worth is briefly 156
summarised here to provide the theoretical background for this work. Various particular aspects 157
are presented in more detail elsewhere (Moore and Doherty, 2005, Christensen and Doherty, 158
2008, Dausman et al., 2010, Fienen et al., 2010, Moore et al. 2011, Engelhardt et al., 2013). 159
160
A vector p can be partitioned into two subvectors p1 and p2. In the hydrogeological context 161
considered in this paper such a vector could comprise hydraulic parameters such as porosity and 162
hydraulic conductivity for distributed points in space. If p is comprised of multi-Gaussian 163
random variables with a covariance matrix C(p), then C(p) be partitioned on the same p1, p2 164
basis, e.g., (C(p1p1) or C11, C(p1p2) or C12, C(p2p1) or C21, and C(p2p2) or C22) . If elements of 165
p2 become known (e.g. field tests of hydraulic conductivity or porosity are undertaken), then 166
C’11, the covariance matrix of p1 conditional on knowing p2 is calculated as (Koch, 1987): 167
C’11 = C11-C21C-1
22C21 (1) 168
This formula can be used to characterise the reduction in uncertainty of model parameters, and 169
the predictions which depend on them, that is achieved by adding data that contains information 170
pertinent to model parameters, including the special case where a parameter value becomes 171
perfectly known, and its covariance becomes zero. 172
173
Now let a (m×1) vector p contain the values of parameters used by a model. Let the action of a 174
(linear) model on these parameters p be represented by the matrix X. Unless the parameter 175
values encapsulated in the vector p are accurately known at all places within a model domain, 176
they must be described in probabilistic terms. Therefore, let the covariance matrix of p be 177
denoted as C(p). Further, let the vector h represent observations of system state comprising the 178
model calibration set and allow for these observations to be contaminated by measurement noise 179
ɛ, such that: 180
h = Xp+ɛ (2) 181
Let s (a scalar) designate a prediction made by the model; let the sensitivities of this prediction to 182
model parameters be represented by the vector y. Then s is calculable using the relationship: 183
s = ytp (3) 184
Combining (2) with (3) leads to: 185
���� = ��� 0
� ���� (4) 186
From the propagation of error formula we can calculate: 187
C ���� = �y� 0
� ��(�) 00 �(�)� �� �
0 � = ����(�)� ���(�)��(�)� �(�)� + �(�)� (5) 188
Where C(p) is the covariance of innate parameter variability, and I is the identity matrix. In 189
Christensen and Doherty (2008) equation (1) and (5) are combined. This is shown to be a 190
Bayesean formulation of linear predictive uncertainty in Fienen et al (2010) and Dausman et al. 191
(2010). The Bayesean approach abandons the notion of a calibrated model, and instead a suite of 192
model outputs are used to describe the possible predictions, as encapsulated by equation (6): 193
ơ2
s= ytC(p)y - y
tC(p)X
t[XC(p)X
t + C(ε)]
-1 XC(p)y (6) 194
In this work this formulation is used to evaluate the worth of different tracer test designs. It is 195
important to note the assumption of model linearity encapsulated in equation 6. The implication 196
of this being that calculated predictive errors should be considered in a relative rather than 197
absolute magnitude sense where models exhibit non-linear behavior. However because data 198
worth analysis is explicitly a relative comparison between alternatives, rather than a calculation 199
that obtains absolute values, the use of equation 6 in this context is considered appropriate. In 200
addition, where compared quantities may be affected by an erroneous assumption of model 201
linearity, relativity of the compared alternatives may nevertheless be preserved (Doherty et. al. 202
2010). Equation 6 also assumes independence between parameter and error covariance terms, but 203
correlation between these terms can exist when the model is under determined. However, given 204
the relative rather than absolute nature of this assessment, the omission of these correlation terms 205
is considered acceptable. 206
207
The cost effectiveness of different tracer test design options were explored within a Pareto 208
optimisation framework (Pareto, 1906; Stadler, 1979). The Pareto front is the locus of points 209
along which it is not possible to lower one objective function without increasing another, and 210
was first demonstrated in a predictive uncertainty context by Moore et al. (2010). The framework 211
was applied in two dimensions whereby one objective function was defined in terms of the 212
uncertainty of a prediction as calculated using equation (6), and the second objective function 213
was defined in terms of the cost of the tracer test analyses. The Pareto optimisation framework is 214
available through the PEST software suite (Doherty, 2010a,b) and the major components of this 215
optimisation methodology are summarised in the flow chart depicted below (Figure 1). 216
217
218
219
220
221
222
223
224
225
226
227
228
229
230
231
232
233
234
235
236
237
238
239
240
* Predictions are predictions of interest for the problem at hand. The optimisation goal for this study is the reduction of 241
uncertainty of (i) transport time predictions and (ii) concentration dilution predictions. Both are key characteristics for assessing 242
the impact of the re-injection of treated CSG operational water on aquifer geochemistry. 243
Figure 1: Flow chart of employed optimisation methodology. 244
245
3. Application of data worth methodology 246
3.1 Case study 247
Analysis of trade-off in
costs vs. reliability
Numerical Model relating
prediction* to parameter inputs
Measurement data types and
disposition to explore Calculated sensitivities of
prediction to parameters
Parameter probability
distribution
Observation data worth: Calculated reduction in
prediction uncertainty with additional
observation data
Parameter worth: Calculated reduction in
prediction uncertainty with increased
parameter knowledge
PEST SUITE
PREDUNC / PREDVAR
PARETO ANALYIS
The case study that provided the motivation for the present data worth analysis is a deepwell 248
injection site located in northern Queensland, Australia, where a large-scale injection program 249
for treated CSG production water (permeate water) is proposed. Here, the operator of the site is 250
investigating the suitability of the local aquifer for re-injection of reverse osmosis (RO) treated 251
water. The target aquifer is the Precipice Sandstone aquifer of the Surat Basin (Elliott, 1989; 252
QWC, 2012), which, at the site, extends from approximately 420m below ground level (mbgl) to 253
515mbgl (Figure 2). The aquifer is comprised of fine- to coarse-grained sandstones with 254
interbedded siltstones and mudstones representing a generally upward-fining, fluvial sedimentary 255
sequence. The main injection horizon is the coarse-grained lower 60 m of the formation, termed 256
the Braided Stream Formation which is of high primary and secondary porosity, and which is 257
characterised by high permeability and rapid, preferential flow through fractures. The Precipice 258
Sandstone is separated from overlying and underlying aquifers by thick sequences of mainly silt- 259
and mudstones (QWC, 2012). 260
261
The groundwater in the target aquifer prior to the start of injection is anoxic, as indicated by high 262
methane and Fe2+ concentrations, and the absence of appreciable concentrations of oxygen, 263
nitrate or sulphate (Table 1). The injectate is reverse osmosis treated CSG water (RO permeate), 264
and further treated by membrane removal of dissolved gases and UV sterilisation. The resulting 265
water is oxic water with a low mineralisation. A summary of average RO permeate chemistry is 266
given in Table 1. 267
268
A range of potentially suitable tracers were considered that included, on one hand groundwater 269
constituents that already prevail in the ambient groundwater and, on the other hand, added or 270
‘amendment’ tracers. Potential monitoring of these proposed tracers aims to (i) document the 271
spreading of the RO permeate within the target aquifer and (ii) to subsequently use this 272
information to establish quantitative models (Table 1). The range of potentially suitable ambient 273
tracers included methane, which prevails at high concentration in the ambient groundwater but is 274
absent in the oxic injectant (Table 1), therefore acting as a “negative” tracer. Differences in 275
chloride concentration between the injectate and the groundwater are relatively low (Table 1) 276
and chloride was therefore regarded as a potentially less suitable tracer with respect to its value 277
for constraining physical transport processes. However, chloride is widely used in field tracer 278
tests elsewhere because of its conservative behaviour (i.e., non-reactive) and hence was included 279
in the current data worth analysis for comparison. Potassium bromide (KBr) was identified as 280
suitable amendment for the injectate. Under the conditions considered here, bromide has proven 281
to behave conservatively in the subsurface and not to react with the aquifer matrix or other 282
solutes (Davis et al., 1980). For the purposes of this study, KBr was assumed to be dosed into the 283
injectate at concentrations of 0.25 mg/l, i.e., several times that of the background (0.06 mg/l) for 284
7 days at the start of the injection trial before switching back to the original RO water 285
composition without KBr amendment (Table 1). Finally we also included temperature in the data 286
worth analysis. Temperature is increasingly recognised as a valuable, cost-effective 287
environmental tracer in groundwater studies (e.g. Anderson, 2005). Where the difference 288
between the injectate and the ambient groundwater temperature was sufficiently large, 289
temperature was also shown to be a suitable tracer in managed recharge applications (e.g., 290
Prommer and Stuyfzand, 2005, Greskowiak et al., 2006). At our study site, injectate 291
temperatures were expected to vary with surface temperatures. Besides solute and heat tracers, 292
hydraulic heads were assumed to be monitored on a continuous basis and therefore included in 293
this way for the data worth analysis. 294
Table 1 Ambient and injectate water chemistry (Source: Origin Energy Resources LTD) 296
Analyte Units RO Permeate Precipice Sandstone
water at Injection Site Min Max Median
Temperature °C Variable depending on ambient
temperature 37
Electrical Conductivity µS/cm 98 201 130 230
Redox potential mV - - - -220
pH
6.86 7.92 7.35 6.4
Total Dissolved Solids mg/L 44 88 58 113
Bromide mg/L 0.07 0.14 0.1 0.06
Carbonate Alkalinity mg/L BD* 0.4 BD* <1
Bicarbonate Alkalinity mg/L 15 21 19 <1
Total Alkalinity mg/L 12 18 16 <1
Sulphate mg/L BD* BD* BD* 4
Chloride mg/L 20 46 26 13
Calcium mg/L BD* 7.7 0.1 4
Magnesium mg/L BD* 1.9 BD* <1
Sodium mg/L 17 27 23 35.5
Potassium mg/L 0.1 0.6 0.3 2
Iron mg/L BD* 0.075 0.036 4.02
Methane µg/L BD* BD* BD* 11950
* BD: Below detection limit 297
298
3.2 Model description 299
3.2.1 Conceptual model and numerical model setup 300
As the natural groundwater flow velocities are with gradients of less than 0.01 very small at the 301
injection site compared to those induced by the re-injection operation, radial-symmetric flow and 302
transport conditions were assumed. Flow and solute transport were therefore simulated using a 303
2D quasi-radial flow and transport model that represents a radial-symmetric 3D domain, using a 304
previously developed and tested approach (Greskowiak et al., 2005, Wallis et al., 2012). This 305
allows for savings in model run times of one to two orders of magnitude (Wallis et al. 2012) and 306
allows the calculation of predictive uncertainty to be made rapidly. The finite-difference model 307
MODFLOW (Harbaugh, 2005) was used for the flow simulations while solute and heat transport 308
were simulated with the multi-species transport simulator MT3DMS (Zheng and Wang, 1999, 309
Langevin et al. 2009; Ma et al. 2012, Engelhardt et al. 2013). The model has a radial extent of 310
515m with grid cell-sizes increasing from 1 m near the injection well to 15m at the outer model 311
fringes, where a constant head boundary was implemented. The total simulation period was set to 312
100 days, whereby the amended RO permeate was injected during the first 7 days. The model 313
simulation period was divided into 5 stress periods, which varied in length between 2 and 78 314
days to represent the variability of injection rates and KBr amendment in the injection water. The 315
resulting flow and transport model represents the expected major flow and concentration pattern 316
created by the injection well and served as the base case scenario for the subsequent data worth 317
and network design analysis (Figure 3). 318
319
3.2.2 Model parameterisation 320
The geological sequence of the Precipice Sandstone Formation was separated into 9 model layers 321
with four distinct conductivity zones that were defined on the basis of the lithological profile 322
obtained from core logging as well as the geophysical down-the-hole surveys and the test pump 323
program conducted by the operator (Table 2 and Figure 2). The analysis of the collected core 324
material showed fracturing within the main injection horizon, i.e., the Braided Stream Formation 325
(BSF, model layer 8). Therefore a dual domain mass-transfer approach was implemented for this 326
layer (Feehley et al., 2000; Liu et al., 2007). This approach allows mimicking the characteristic 327
transport behavior that is created where highly permeable portions of the aquifer, including 328
fractures, exchange mass with stagnant or slow-flowing zones (Haggerty, 2001). Likely flow and 329
transport model parameter values and the lower and upper limits excepted for these parameters 330
were estimated based on published reports on the aquifers in this region (Radke, 2012) (Table 2). 331
In the case of the heat transport parameters, estimated values were based on literature data and 332
actual measured, site-specific, lab-determined thermal conductivity and heat capacity values by 333
the operator. Vertical and horizontal hydraulic conductivities and porosity were defined in the 334
model using the pilot points method (de Marsily et al., 1984, Doherty 2003) to introduce 335
parameter heterogeneity. Thereby, mean parameter values (Table 2) were uniformly assigned to 336
a total of 117 pilot points (one point placed into every 5th model cell) and then spatially 337
interpolated to all active model cells using kriging. The spatial variability was thereby assumed 338
to be log-normally distributed and characterized through a variogram with a range of 250m, sill 339
of 0.2 and a nugget of zero. The use of distributed pilot point parameters mitigates contamination 340
of the data worth analysis from the structural error associated with parameter lumping, as they 341
introduce minimal assumptions about the geometry and lumping of the hydraulic-conductivity 342
and porosity field (e.g. Moore 2005, and Doherty and Welter, 2010, and Fienen et al. 2010). In 343
total the model is comprised of 244 model parameters (Table 2). Figure 2 illustrates the 344
simulated tracer concentration and heat distribution patterns within the BSF created by the 345
injection well computed using the mean hydraulic properties as listed in Table 2. 346
347
Table 2: Model parameterization 348
Parameter
Model
layer Units
Distributio
n Mean
Lower
limit
Upper
limit
PEST
parameter
group
Storage coefficient L1-9 - uniform 1.00E-05 1.00E-06 1.00E-04 stor
Kh1) - varying log of kh by 3*sd0.22) L8 [m/d] pilot points 100 4.56 2196 kh
kh1) - varying log of kh by 3*sd0.22) L1, 3, 9 [m/d] pilot points 1.00E-04 4.56E-06 0.0022 kh
kh1) - varying log of kh by 3*sd0.22) L2, L5 [m/d] pilot points 0.1 0.0046 2.2 kh
kh1) - varying log of kh by 3*sd0.22) L4 [m/d] pilot points 10 0.46 219.6 kh
n1 - porosity – mobile domain L1-7, 9 - pilot points 0.1 0.05 0.3 por
n2 - porosity (BSF3)) – mobile domain L8 - pilot points 0.01 0.005 0.1 por
n3 - porosity (BSF3)) - immobile domain
L8 - Uniform 0.04 0.01 0.1 por
n3 - porosity - immobile domain
L1-7, 9 - Uniform 0.0001 not allowed to vary n.a.
m - mass transfer rate L8 [1/d] uniform 1.00E-04 1.00E-05 1.00E-03 mass
Dispersivity L1-9 [m] uniform 1 0.5 2 disp
Therm. Diffusivity L1-7, 9 [m2/d] uniform 0.0452 0.014 0.14 thermdif
Therm. diff. (BSF3)) L8 [m2/d] uniform 0.0941 0.028 0.28 thermdif
Thermal kd L1-9 [m3/kg] uniform 0.0002 0.00015 0.00022 thermkd
Bulk density (BSF3)) L8 [kg/m3] uniform 2660 1900 2900 thermbd
Bulk density L1-7, 9 [kg/m3] uniform 2520 1800 2800 thermbd
349 1) kh = kv 350 2) The parameter standard deviation descriptions for the hydraulic parameters are calculated in the log 351
domain, i.e. parameter standard deviation (sd) = 0.2( log domain) times 3 352 3) BSF = Braided Stream Formation 353
354
3.3 Optimisation of tracer test design and data acquisition 355
3.3.1 Optimisation goal 356
The data worth methodology is based on the premise that a measure of the worth of different 357
monitoring designs is its ability to reduce the uncertainty of key model predictions of future 358
environmental behaviour (Figure 1). The calculated uncertainty is thereby specific to the 359
required prediction type and is quantified by the standard deviation. The latter depends on the 360
uncertainty of the estimated hydrogeologic parameters (Table 2) and the ability of the selected 361
tracer data to constrain these parameters. The optimisation goal for this study is the reduction of 362
uncertainty of (i) transport time predictions and (ii) concentration dilution. Both are key 363
characteristics for assessing the impact of the re-injection of treated CSG operational water on 364
aquifer geochemistry. Our assessment of the predictions is composed of the time of solute 365
breakthrough within the BSF at 24m, 50m, 78m, 106m, 125m, 155m and 175m radial distance 366
from the injection well (Figure 2) and of the corresponding dilution. Unlimited observation 367
locations can be added as appropriate to reflect locations of actual risk receptors. The relative 368
worth of an observation location or tracer type is then ranked against others based on their ability 369
to reduce the uncertainty of these predictions at the selected locations depicted in Figure 2. 370
371
3.3.2 Monitoring network and data types 372
A base case observation network was established to explore optimal monitoring strategies. 373
Bromide, chloride and methane concentration as well as head and temperature data observations 374
were simulated at varying distances from the injection well (Figure 2). Tracer observations were 375
thereby placed in every 5th model cell into layers 1, 3, 5, 7, 8 and 9, providing a total of 78 376
potential observation locations for each tracer (Figure 2). This complete observation suite served 377
as the base case observation set (Table 3). 378
379
For all observation values a level of systematic uncertainty was assumed, which reflects the 380
measurement errors of the collected data as well as the level of observed background variability 381
in concentration, head and temperature data. It also includes model structural noise induced 382
through model artefacts e.g. discretisation, or alternatively the numerical dispersion or the 383
chosen advection scheme. The estimate of this measurement noise for each observation type was 384
based on the approximate accuracy expected for the respective laboratory methods (e.g., analysis 385
of bromide concentrations through ion-chromatography) in conjunction with the expected 386
magnitude of errors induced during field sampling. Background variability of each data type was 387
available from the injection site. The combination of measurement and structural noise of 388
observation data was considered in the data worth analysis by assigning weighting factors equal 389
to the inverse of the total observation uncertainty (which combines measurement and model 390
structural error). Based on the above, the observation values were assumed to have a systematic 391
uncertainty expressed as a standard deviation equal to 5% (temperature data), 10% (head 392
observations), 15% (chloride and bromide concentrations) and 20% (methane concentrations) of 393
measured values. 394
395
396
Figure 2 Cross-section through radial model grid, showing position of the 9 model layers and 65 model 397
cells in radial direction. Also shown are 78 potential observation locations (blue circle) and spreading 398
prediction locations (red square) and the lithological and natural gamma log profile of the injection bore. 399
400
3.3.3 Alternative monitoring configurations 401
A number of additional, alternative monitoring configurations where then defined and compared 402
with the base case network (see Table 3) and included: (i) different monitoring network designs 403
based on different numbers and locations of observation bores, and different monitoring 404
frequencies, and (ii) different injection test configuration based on changes to the ratio between 405
concentration of injectant to ambient solutes, and to the applied injection rate. These different 406
scenarios thereby target the optimum combination of the spatial disposition of monitoring wells, 407
the temporal disposition of measurements made at these wells, and the signal to noise disposition 408
of the tracer tests, where optimum is defined in terms of ability to reduce predictive uncertainty. 409
410
Table 3: Model scenarios 411
Scenario Tracer Sampling Injection Br [mg/l] Duration Scenario
frequenc
y
Rate Injectant Amendment type
Base case All tracers daily 500/1000 m3/d 0.25 1 week 78 observation bores
Scenario 1-4 All tracers daily 500/1000 m3/d 0.25 1 week Nr of obs. Bores
1): 1, 2, 3, 5
Scenario 5-9 All tracers2)
variable 500/1000 m3/d 0.25 1 week Sampling frequency
2): 2, 7, 14, 21, 30
Scenario 10-12 All tracers daily 500/1000 m3/d 0.25 1 week Timing of sampling: 1, 2, 3
3)
Scenario 13 Br daily 500/1000 m3/d 0.15 1 week Amendment of injectant conc.
Scenario 14 Br daily 500/1000 m3/d 0.20 1 week Amendment of injectant conc.
Scenario 15 Br daily 500/1000 m3/d 0.50 1 week Amendment of injectant conc.
Scenario 16-17 Br weekly 500/1000 m3/d 0.25 variable Duration of amendment: 2; 12 days
Scenario 18 All tracers daily 1000/2000 m3/d 0.25 1 week Injection rate doubled
Scenario 19 All tracers daily 250/500 m
3/d 0.25 1 week Injection rate halved
Scenario 20 Cl
daily 500/1000 m3/d 0.25 1 week
3)Cl permeate conc. = 11.5 mg/l
Scenario 21 Cl
daily 500/1000 m3/d 0.25 1 week
3)Cl permeate conc. = 15 mg/l
Scenario 22 Cl
daily 500/1000 m3/d 0.25 1 week
3)Cl permeate conc. = 20 mg/l
Scenario 23-24 Cl daily 500/1000 m3/d 0.25 1 week Cl noise = St. Dev. 10%, 20%, 40%
1) Nr. of observation bores - 1: 124m; 2: 98m and 195m; 3: 67.5m and 145m and 267.5m; 5: 67.5m and 98m and 412
145m and 195m and 267.5m radial distance in BSF 413
2) Sampling frequency: 2=every second day; 7 = weekly; 14 = 2-weekly; 21= three-weekly and 30=monthly 414
3) Timing of sampling: daily sampling during (1) first month of trial; (2) second month and (3) third month of trial 415
4) Chloride background conc. = 11 mg/l, i.e. signal to noise ratio = 11.5/11 (Scenario 17), 15/11 (Scenario 18), 416
20/11 (Scenario 19) and 28/11 (base case). 417
418
4. RESULTS 419
4.1 Base case solute migration 420
The solution migration behaviour of the base case flow and transport model is illustrated in the 421
breakthrough curves in Figure 3. Chloride and methane display conservative breakthrough 422
behaviour. Bromide concentrations peak in the base case during the first 7 days, i.e., the phase 423
during which tracer amendment at the start of the trial still persisted. In the following 424
concentrations dilute during aquifer passage until at the end of the trial the Br peak has 425
dissipated. Compared to the migration rate of the concentration fronts of bromide, chloride and 426
methane the temperature signal is retarded. 427
428
429
Figure 3 Simulated solute concentrations and temperatures with time within the Braided Stream Formation aquifer 430
(model layer 8). 431
432
4.2 Improved parameter knowledge to reduce predictive uncertainty 433
The first analysis performed on the base case was undertaken to provide insights into the relative 434
significance of direct hydrogeological parameter knowledge in terms of constraining the 435
uncertainty of the chosen solute spreading predictions. The goal of this analysis was to identify 436
those parameters for which increased knowledge would provide the largest reduction in 437
uncertainty of dilution and travel time predictions. The worth of increased parameter knowledge 438
was assessed in two stages. Firstly the uncertainty of a prediction was calculated, assuming all 439
model parameters were known to a level of certainty commensurate with that described in Table 440
2. Then, sequentially, parameters were assumed to be perfectly known at each pilot point 441
location (i.e. “freezing” a parameter to a value and assuming no uncertainty). The extent to 442
which a direct parameter measurement would be able to reduce the uncertainty of a prediction 443
was then quantified from equation 1, and then normalised by the sum of all parameter 444
contributions to uncertainty, to provide a range from 0 to 1. This relative worth of different 445
parameter types is summarised in Figure 4 for a travel time prediction in close proximity to the 446
injection well (24m), then at 78m, as well as at a distant prediction location (175m). 447
448
For both the dilution and travel time predictions, porosity was identified as the parameter of 449
greatest significance for making reliable predictions. This is a credible result and reflects the fact 450
that within the context of injection schemes, where background flow is often negligible, 451
groundwater flow velocities are injection rate driven, regardless of the hydraulic conductivity. 452
Aquifer porosities govern the conservative transport velocities and control how far a solute will 453
migrate. Thus, conductivity measurements obtained, e.g., through discharge tests, would be of 454
limited usefulness to reduce predictive uncertainties, while measurements of porosity would be 455
most informative. However, for injection schemes in which the background flow represents a 456
more important component of the overall groundwater flow hydraulic conductivities would 457
acquire greater significance. 458
459
Dilution predictions are similarly sensitive to porosity and to the mass exchange rate at locations 460
in close proximity to the injection well, where injection has resulted in concentration contrasts 461
between matrix and fracture networks. With distance the relative worth of hydraulic conductivity 462
data increases as the solute spreads out beyond the BSF into over- and underlying aquifer 463
formations and as the background flow field gains in importance but the worth of conductivity 464
data remains well below that of porosity. Other parameters make minimal contributions to 465
predictive uncertainty reduction. 466
467
468
469
470
471
Figure 4: Summary of relative reduction in dilution prediction uncertainty at 24m, 78m and 175 m radial distance 472
from the injection well through enhanced knowledge of various hydraulic parameters. 473
474
4.3 Regions of greatest data worth and ranking of different data types 475
The purpose of the second analysis that was undertaken for the base case was to identify optimal 476
tracer test measurement locations and assess the relative usefulness of different data types, when 477
making predictions of the spreading of CSG permeate. Starting from a baseline, which assumes 478
no observation data (i.e., no pre-existing monitoring network) individual observation data types 479
were sequentially added at the 78 potential observation locations and the subsequent reduction in 480
predictive uncertainty calculated. Thus, the worth of each individual potential observation 481
location and data type was established, independently of any other potential observations. 482
483
Data worth was thereby calculated as the normalised decrease in predictive uncertainty variance 484
according to: 485
������ = !"#$%#&'#( )*++!,-,&.( (7) 486
487
488
where ������ is the normalised decrease of prediction uncertainty variance for a given 489
observation; �/01�0230� is the decrease in prediction uncertainty variance incurred through 490
addition of a given observation to the calibration data set; and ����24� is the total predictive 491
uncertainty variance for a given data type. 492
493
494
495
496
497 Figure 5 The spatial distribution of data worth (equation 8) within the 2nd week and 8th week of injection, for all 498 tracer observations with respect to the solute dilution prediction at 106m from the injection well. 499 500 501
4.3.1 Regions of greatest data worth 502
In Figure 5, the contours of predictive uncertainty decrease achieved through addition of 503
individual observation types and locations are depicted for monitoring data at 2 and 8 weeks 504
after injection. These contours indicate that the general area where added observations will 505
provide maximum information are coincident with the high hydraulic conductivity region of the 506
model (Braided Stream Formation) where most of the injectant is moving, and where there is the 507
greatest concentration change (i.e., the greatest signal to noise ratio), thus most informative are 508
observations ahead of the plume, before full breakthrough of the injectant (Figure 3 and 5). 509
Comparing data worth at three selected times (Figure 5) illustrates the transient nature of “best 510
monitoring location”, which is related to the changing signal to noise ratio between the plume 511
and surrounding groundwater that occurs as the plume migrates from the tracer injection point. 512
Therefore observations close to the injection point (<50m) are most informative at the start of the 513
trial, but lose information content soon thereafter as groundwater rapidly attains the 514
concentrations of the injectant. With time the region of greatest data worth moves outwards into 515
the aquifer. However, because groundwater velocities decrease rapidly away from the injection 516
point due to the radial expansion in aquifer volume, the outward movement of the plume slows 517
successively. This region of data worth can be related to the solute front position (here defined as 518
the location in the aquifer where C/Co = 0.5) which moves proportional to √6789 in a radial 519
velocity field. For example the simulated methane data shows solute breakthrough (C/Co=0.5) 520
to occur at a distance of about 200 metres 60 days into the injection trial (Figure 3), but if instead 521
an observation well is located at three times that distance (600m), the time to breakthrough is 522
extended to about 1.5 years. At the same time dilution reduces concentration contrasts and 523
diminishes predictive information contained in these more distant observations. This 524
combination creates the down gradient limits to the regions of data worth depicted in Figure 5. If 525
data worth is integrated at each location for all tracer types and over the entire duration of the 526
injection trial, i.e. over 100 days, the optimal observation locations lie within radial distances 527
between 50m and 250m from the injection bore. 528
4.3.2 Tracer data worth 529
Under base case conditions, bromide is the superior tracer at earlier times: bromide provides the 530
lowest predictive uncertainty standard deviation (up to +/- 5 days during the first month of the 531
trial, Figure 7) compared to other tracers and it does so over a larger area compared to other 532
tracers (Figure 5).. However as Br amendment ceases, the Br concentration diminishes as the 533
solute plume spreads throughout the aquifer, thus decreasing the information content of Br 534
measurements as the injection trial progresses (Figure 5 and 7). At later times after injection, 535
chloride emerges as the tracer of greatest data worth, ahead of bromide, methane and 536
temperature. This same trend applies to predictions being made at increasing distances from the 537
injection well: the further the distance for which predictions are made, the more favourable 538
chloride becomes compared to Br (Figure 7). 539
540
For predictive locations close to the injection point, temperature data are of similar worth as 541
solute tracers (Figure 5 and 7). The usefulness of temperature data however decreases the further 542
away predictions are required in relation to the injection point and predictive uncertainty 543
standard deviations increase rapidly (Figure 7). Temperatures diminished usefulness with 544
increasing distance from the injection well is due to the velocity of the thermal front being less 545
than the pore water velocity as heat is exchanged between the injectant and the aquifer (e.g. 546
Brookfield et al., 2009), i.e., the temperature signal is strongly retarded compared to the solute 547
tracer concentration fronts and the contrast in temperature between CSG permeate and ambient 548
water becomes increasingly attenuated with travel distance. 549
550
The monitoring of head data provides no significant improvement in the reliability of solute 551
spreading predictions: groundwater heads provide minimal information content for predicting 552
solute spreading, as head observations provide no information on porosities, the main parameter 553
controlling solute spreading (results not shown). This confirms the previous finding on the 554
superiority of porosity data in predicting solute spreading and is a distinguishing feature under 555
injection-driven flow conditions. In contrast, under natural flow conditions, or for injection tests 556
which do not override the background flow, head data can be expected to be of more 557
significance. 558
559
4.4 Alternative monitoring designs 560
561
A selection of alternative feasible monitoring network configurations were evaluated and 562
compared to the base case (Table 3) in terms of their ability to reduce the uncertainty of travel 563
time and dilution predictions. The alternatives included: (i) reduced numbers of available 564
observation bores (scenarios 1-4, Table 3); (ii) reduced sampling frequencies (scenario 5-9, 565
Table 3); (iii) modified injectate to ambient concentration ratios and amendment durations 566
(scenario 10-15; 18-24, Table 3) and (iv) altered injection rates (scenario 16-17, Table 3). 567
568
4.4.1 Number of observation locations and measurement frequency 569
The accuracy of solute spreading predictions depends on the number of available observation 570
bores and the frequency at which these bores are sampled. In order to compare various 571
monitoring strategies and quantify their ability to improve the predictions of the spreading of the 572
injected CSG produced water, it was first assumed that observation data was available for all 573
tracers, at a daily sampling frequency, for all potential observation locations (i.e., 78 bores) (base 574
case scenario, Table 3). This results in a very small post calibration uncertainty standard 575
variation, which was compared with the uncertainties calculated for progressively coarser 576
sampling frequencies, for each individual tracer (scenarios 5 to 9, Table 3). 577
578
The impact of measurement frequency is shown in Figure 6a and depicts the contours of the 579
standard deviation of travel time error for all tracers and combinations of measurement 580
frequency, versus the distance at which a prediction of travel time is sought. As expected, with a 581
coarsening sampling frequency, the uncertainty increases. If all monitoring observations are 582
available, e.g., at 78 observation locations, the calculated standard deviation of predictions of 583
travel time is less than 1 day within a radial distance of about 100 meters, assuming all tracers 584
are sampled at least every three days. When sampling frequency is reduced to once per week, 585
such accuracy can only be achieved up to a radial distance of about 40 metres, reduced further to 586
about 20 meters if a monthly sampling regime was adopted. 587
588
The analysis of the influence of the total number of available bores on predictive accuracies 589
(Figure 6b, scenarios 1-4) indicated that data from a single optimally located observation bore, 590
sampled daily for all tracers within the region of greatest data worth, achieves a reduction of 591
uncertainty of almost two orders of magnitude. This can be compared with two optimally located 592
observation wells, sampled daily for all tracers, which achieves a further halving of predictive 593
uncertainty compared to the case of a single bore. Thereafter, additional observation wells 594
provide diminishing returns in terms of the rate of decrease in predictive error. The addition of a 595
third, fourth and fifth bore within the area of greatest data worth, i.e., between 50m to 250m 596
radial distance, leads to only minor reductions in uncertainty. This analysis indicates that two 597
appropriately located observation bores provide the greatest reduction in uncertainty; with any 598
further addition of monitoring bores incurring disproportionally low reductions in uncertainty in 599
this relatively homogeneous radial flow case. 600
601
602
603
604 Figure 6 Predictive uncertainty standard deviation of peak solute breakthrough [days] as a function of a) frequency 605 of sampling events and radial distance from the injection well (based on 78 observation bores) and b) number of 606 available observation bores for a prediction at 106m. Location of observation bores and integrated data worth over 607 the duration of the injection trial (i.e. 100 days) is also shown. Sampling frequencies: (1) = daily, (2)= every second 608 day … (30)= monthly sampling. 609
610
611
4.4.2 Ratio of injection concentration to ambient concentration 612
A number of numerical experiments were undertaken where the signal (injection concentration) 613
to noise (ambient conditions) ratio of tracers was increased via increasing amendment 614
concentrations and duration and/or reducing the measurement error, for instance through more 615
accurate sampling techniques (noise term in eq. 2) (scenario 10-15; 18-24, Table 3). To allow 616
comparisons between different tracer types, the difference between injection and ambient tracer 617
concentration was normalised by the standard error of tracer measurement (assuming standard 618
contrast to noise normalisation formulae). 619
620
The impact of the different amplitudes of the four tracer signals on predictive uncertainty is 621
plotted in Figure 7 based on scenarios 10 to 15. Prediction uncertainty is described in terms of 622
the standard deviation of error of the solute breakthrough time (in units of days) as a function of 623
increasing distance to the injection well and time of sampling. The figure clearly demonstrates 624
that bromide, as the amended tracer, is of greatest use for shorter-term predictions in closer 625
proximity to the injection well. The bromide amendment of 0.25mg/l (base case) yields a signal-626
to-noise ratio that is twice that of chloride during amendment, which again is twice that of 627
methane and temperature. However, after amendment ceases and as time progresses, the 628
amplitude of the Br signal diminishes and chloride becomes the more suitable tracer to constrain 629
physical transport processes. In contrast to bromide, temperature data gains in utility as time 630
progresses as heat successively propagates into the aquifer. However, due to its strong 631
attenuation compared to solute tracers, and despite its very low measurement error, the ability of 632
temperature data to inform CSG permeate spreading remains well below that of the solute 633
tracers. 634
635
The superiority of bromide as a tracer in this context can be further enhanced by increasing the 636
amendment concentration and/or amendment duration (results not shown). The minimum 637
amendment concentration required for Br to remain superior to chloride and other tracers at early 638
times in the injection trial was found to be 0.15mg/l (as depicted in Figure 7). Methane and 639
chloride maintain a constant signal to noise ratio at the injection site with the normalised ratio for 640
methane thereby being half that of chloride. This, together with a higher measurement error 641
makes methane the least reliable of the three solute tracers to predict solute spreading in this case 642
study. 643
644
645 Figure 7: Contoured predictive uncertainty standard deviation of peak solute breakthrough [days] as a function of 646 radial distance from the injection well and time of sampling. Contours are based on a potential observation network 647 consisting of 5 bores located within the area of greatest data worth (50 – 250m in BSF). (Time of sampling: daily 648 sampling during first month (1), second month (2) and during last month (3) of trial). 649 650
651
4.4.3 Injection rate 652
Under injection-driven groundwater flow schemes, the injection rate affects the tracer signal to 653
noise ratio, and hence the accuracy of dilution predictions. This relationship is depicted in Figure 654
8, where the injection rate is progressively increased. Within distances up to about 50 m from the 655
injection well, predictive accuracy is high, irrespective of the selected injection rate. However, 656
with increasing distance, larger injection rates reduce uncertainty. The result can be explained by 657
the increased number of observation bores with significant concentration increases that occur 658
with larger injection rates and the greater injected mass under higher injection rates, which in 659
turn, reduces the predictive uncertainty variance of the model (Figure 8). 660
661
Increasing injection rates also impact the relative worth of temperature data. At low injection 662
rates, there is a reduction in induced flow velocities, which increases the time available for 663
thermal energy uptake by the aquifer as the plume spreads into the BSF and over- and underlying 664
aquifer layers, resulting in a lowered signal to noise ratio and diminished usefulness of 665
temperature data relative to solute tracers. 666
667
Figure 8: Contoured predictive uncertainty standard deviation of peak solute breakthrough [days] as a function of 668 radial distance from the injection well and injection rate. Contours are based on the potential observation network of 669 78 bores under a daily sampling regime monitoring all tracers. 670 671 672
5. Cost analysis 673
Given the vast differences in costs of acquisition of different tracer and marker species, there is a 674
need to establish which monitoring strategy potentially provides the greatest return for 675
investment for implementation at the injection site. To incorporate cost into our analysis we 676
employ a methodology where cost effectiveness is defined in terms of both the reduction in the 677
uncertainty of a prediction achieved by various analyses, and their cost. This allows for the 678
evaluation of an optimal monitoring strategy subject to both cost and predictive accuracy. Costs 679
of sampling was based on representative laboratory charges, which are $44AUD /sample for 680
bromide; $82.5AUD/sample for methane and $10.5AUD/sample for chloride, while temperature 681
data is gathered using a temperature sensor with an integrated datalogger. One-off costs for these 682
dataloggers were distributed over the duration of the injection trial leading to approximate costs 683
for temperature data of approximately $1AUD$/sample. Sampling frequencies of bores were 684
altered repeatedly (range: daily to monthly monitoring), and independently for all tracers. The 685
resulting costs of each sampling strategy, and its ability to predict spreading behaviour was then 686
collated for each combination. 687
688
Pareto front based on all tracers 689
Figure 9a shows the Pareto fronts defined between two objective functions: (i) monitoring costs 690
and (ii) predictive accuracy for three solute breakthrough predictions (viz. travel time at 691
distances of 78m, 125m and 155m). The Pareto front characterises the front for which it is 692
impossible to further lower costs and improve accuracy simultaneously. One end of the Pareto 693
front establishes the most accurate, but also most expensive sampling campaign (daily sampling 694
of all tracers), while at the other end of the Pareto front the accuracy is minimised (monthly 695
sampling of all tracers), and the cost of the sampling campaign is low. Between these two 696
endpoints, neither costs nor predictive uncertainty can be lowered further, without raising the 697
other. Because the uncertainty is a function of the distance at which prediction of solute 698
spreading is sought, this analysis provides the Pareto front points for predictions of travel time at 699
three distances; at 78m, 125m and 155m from the injection well and on the basis of an 700
observation network consisting of 5 bores located within the area of greatest data worth (50 – 701
250m in BSF). (Figure 9a). 702
703
Tracer specific Pareto fronts 704
Based on this Pareto analysis, the outcomes of different monitoring designs can firstly be 705
compared separately and their merits in regards to predictive accuracy versus costs evaluated. 706
Figure 9b depicts the results for a single travel time prediction at a distance of 125m from the 707
injection well. The strongly diverging returns for investment of the different tracers are clearly 708
visible (Figure 9b). If analysing chloride only, the monitoring costs would be relatively low 709
overall with moderate predictive accuracy (i.e., standard deviation (sd) of 6 days or +/- 25% of 710
predicted peak solute arrival time under a daily monitoring regime). If instead only methane was 711
being analysed daily the predictive accuracy decreases, while monitoring costs would rise 8-fold. 712
This highlights the unfavourable return for investment of the methane tracer in this case study, 713
due to methanes' very high cost of acquisition but muted worth compared to other available 714
tracers. Temperature data measurements, when sampled in isolation, were also not adequate to 715
significantly constrain solute spreading predictions. While monitoring costs are low, the 716
reduction in uncertainty of predictions is the least of all tracers, confirming previous findings 717
(section 4). Monitoring Br data yields the most accurate predictions at the site (uncertainty sd= 718
2.4 days under daily monitoring). However, this decrease in uncertainty is penalised by a 4-fold 719
increase in monitoring costs compared to the “chloride-only” sample regime (Figure 9b). 720
721
Pareto analysis of combination of all tracers and all measurement frequencies 722
Closer examination of the Pareto analysis outputs revealed the influence of variable sampling 723
frequencies on predictive uncertainty and costs as the Pareto front is traversed (Figure 10a,b). 724
The analysis showed that it is possible to lower costs for very little increase in uncertainty, by 725
reducing the sampling frequency of methane, the most expensive tracer considered in this study 726
(Figure 10a). As lower costs are sought, it is most effective to reduce the frequency of methane 727
sampling, followed by bromide. In fact, removing methane altogether, while other tracers 728
continue to be monitored on a daily basis, increases predictive uncertainty only very marginally, 729
while costs decrease considerably. For instance, the predictive uncertainty standard deviation of 730
solute breakthrough at 125m increases only from 1.8 days (daily sampling of all tracers) to 1.9 731
days, if methane is omitted from the monitoring regime, however, overall monitoring costs 732
reduce by more than half. 733
734
In addition, Figure 10a and b indicate that when using a combination of tracers with variable 735
sampling frequencies it is possible to lower the predictive uncertainty for a very modest change 736
in costs. This is achieved through a combination of a high sampling frequency of temperature 737
data, the least costly tracer in this study, in conjunction with a solute tracer of greater information 738
content, such as chloride and or bromide. 739
740
A distinct point of diminishing returns can be established along the Pareto front, where lowering 741
the uncertainty incurs disproportional increases in costs. For a solute spreading prediction at 742
125m radial distance, predictive accuracies can be lowered over 15-fold from sd = 109 days 743
(monthly sampling of all tracers) to sd=7 days for an approximate two-fold increase in costs 744
(Figure 9b). However, a further halving of the uncertainty to 1.8 days (daily sampling of all 745
tracers) incurs a 10-fold rise in monitoring costs. This analysis suggest, that a sampling campaign 746
selected in proximity to the point of diminishing returns, such as daily sampling of temperature 747
data, weekly sampling of chloride and bromide data, while disregarding methane data entirely 748
would provide a monitoring strategy with a favourable return for investment at the injection site. 749
Such a sampling regime would result in costs of 56 AUS$/sample event or in total costs of 750
laboratory analysis charges of about 4500 AUS$ for a three month sampling campaign. 751
752 753 Figure 9 (a) Pareto front defining trade‐off between monitoring costs and accuracy for three peak breakthrough 754 predictions; (b): Pareto front defining trade‐off between monitoring costs and accuracy of peak breakthrough 755 prediction at 125m distance from injection well if single tracers are monitored. Each point on the Pareto front is 756 characterised by a unique combination of independent sampling frequencies (range: daily to monthly sampling 757 events) for Cl, Br, CH4 and temperature. Sampling frequencies: (1) = daily, (2)= every second day … (30)= monthly 758 sampling. 759 760 761 762
Figure 10 Changes in sampling frequency of Br, Cl, CH4 and temp. versus a) costs and b) predictive uncertainty as 763 the Pareto front for the peak prediction at 125m is traversed (Figure 9b) (only sub-set of points along the Pareto 764 front are shown for clarity). Frequencies: (1) = daily, (2)= every second day … (30)= monthly sampling. 765
766
6. Summary and Conclusions 767
This paper develops an approach for a model based tracer test optimisation methodology and 768
illustrates its practical application to an example where the factors that determine cost effective 769
test design and monitoring data acquisition were explored. The methodology employs a linear 770
predictive analysis theory from Moore and Doherty (2005) and Christensen and Doherty (2008), 771
with an uncertainty targeted Pareto methodology (Moore et al. 2010). 772
The constraints used by the optimisation method were the reduction in the uncertainty of 773
predictions of solute spreading as defined in terms of travel time and dilution. Based on the 774
numerical representation, we analysed different solute tracers, temperature and hydraulic heads 775
in terms of their utility to inform solute transport behaviour versus the cost of their acquisition. 776
The establishment of regions of greatest data worth and data worth ranking was followed by an 777
uncertainty targeted Pareto analysis, which was used to identify a monitoring regime, which 778
provided the best return on investment as defined in terms of cost and reliability. The Pareto 779
analysis allowed the interdependencies of cost, predictive reliability, and various monitoring 780
campaigns to be compared directly, thereby informing decisions of which monitoring regime 781
provides the greatest return for investment. 782
783
For the investigated injection scheme, porosity was identified as the parameter of greatest 784
significance for making reliable predictions above all other hydraulic parameters. This finding is 785
representative for injection schemes, which override ambient groundwater flow and were flow 786
velocities are injection rate driven, regardless of the hydraulic conductivity. Consequently, 787
conductivity data was found to make minimal contributions to predictive uncertainty reduction. 788
For the same reasons, monitoring of head data was found to provide no significant improvement 789
in the reliability of solute spreading predictions as hydraulic heads are not informing on 790
porosities, the main parameter controlling solute spreading under injection-driven radial flow 791
conditions. Under natural flow conditions, or for injection tests which do not override the 792
background flow, conductivity measurements and head data can be expected to be of more 793
significance. 794
Bromide was assessed as superior to head data and all other tracers during early sampling times 795
in the injection trial. However, once bromide amendment ceased, chloride became a more 796
suitable tracer to constrain simulations of physical transport processes, followed by methane. 797
Temperature data was assessed as the least informative of the solute tracers. With heat transport 798
being retarded due to the heat exchange between the injectant and the aquifer, the ability of 799
temperature records to describe solute spreading was diminished and decreased with growing 800
distance from the injection well. However, taking costs of data acquisition into account, it could 801
be shown that temperature data when used in conjunction with other tracers was a valuable and 802
cost-effective marker species due to temperatures low cost to worth ratio. In contrast, the high 803
costs of acquisition of methane data compared to its muted worth, highlighted methanes 804
unfavourable return on investment. The best return on investment at the injection site was shown 805
to be a combination of daily (high-frequency) temperature measurements, complimented by 806
weekly Br and Cl sampling, while omitting methane data entirely; these measurements being 807
obtained at two observation locations within the area of greatest data worth, i.e., at radial 808
distances between 50m and 250m from the injection bore. Any further addition of monitoring 809
bores achieved only small additional reductions in uncertainty in this relatively homogeneous 810
radial flow field. 811
812
This demonstration of tracer test design and monitoring disposition based on the extent to which 813
a data type reduces the predictive error variance provides modelers and practitioners with a 814
powerful yet efficient and cost effective decision making tool for field tracer test design. 815
Uncertainty of solute transport predictions can be estimated for a range of ‘what–if’ scenarios, 816
allowing efficient comparisons between different monitoring regimes: a given observation 817
location may be considered in the light of other observations; a specific tracer type can be 818
evaluated based on its utility in the light of other available tracers and marker species; sampling 819
frequencies can be selected based on the number of observation bores to be drilled and the 820
distance at which solute predictions are thought. Combining this with an analysis of data 821
acquisition costs allows rigorous comparisons to be made between different monitoring regimes 822
and the return on investment these provide. Efficiency is gained via a model linearity assumption 823
in the problem formulation, which allows the calculation to be made sufficiently rapidly, so that 824
it can be repeated at many alternative proposed monitoring sites, times and under different tracer 825
calibration constraints. The software for such analyses is in the public domain (Doherty, 2010a 826
and b). These are particularly important benefits in the context of tracer injection schemes in 827
deep aquifers, where monitoring reflects typically a significant financial burden. 828
829
Through the application of common use groundwater flow and transport models in conjunction 830
with publicly available tools for predictive uncertainty analysis the proposed tracer test 831
optimisation methodology is generally applicable and easily transferrable from the present study 832
to many applications beyond the case study of injection of treated CSG co-produced water. 833
Many practical water resources problems would benefit equally from a-priori knowledge of the 834
relative worth of different hydrogeological data types and monitoring locations to infer solute 835
transport behavior, especially in settings where target aquifers are deep and drilling and/or 836
monitoring costs high, as e.g. in the case of CO2 underground storage or disposal of produced 837
water from oil and shale gas wells. Potential other applications for such “data worth” analysis 838
include tracer injection experiments focusing on point source contamination, push-pull tests, in-839
situ iron removal operations aquifer storage and recovery (ASR) systems, aquifer thermal energy 840
storage (ATES) systems and in-situ bioremediation operations. 841
842
Acknowledgement 843
We gratefully acknowledge the contributions to this manuscript by Ryan Morris, Origin Energy 844
through provision of data, site information and hydrogeological expertise. We also thank 845
Sreekanth Janardhanan and Adam Siade from CSIRO for their reviews of earlier versions of the 846
manuscript. 847
848
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Figure3
Figure4
Figure6
Figure7
Figure8
Figure9
Figure10
Highlights 992
-we investigate a field-scale injection trial of coal seam gas co-produced water 993
-we use numerical simulations to establish impact of injection 994
- we analyse the worth of field data to maximise reliability of impact assessment 995
-we use “data worth analysis” to optimise monitoring for the site 996
-we establish monitoring strategy which provides greatest return on investment 997
998
999