Essentially seven studies were performed. Initially, the formation was sampled by coring the formation during the installation of wells and multilevel samplers. Descriptive logs of the wells cored are available in the database in the table Boring Logs. The core samples were analyzed for a group of chemicals initially believed to be representative of the site and of regulatory concern. The selected chemicals represented several classes of contaminants. Following the installation of the instrumentation, the formation was allowed to re-equilibrate before any additional measurements were made. Ground-water samples were collected under both static and dynamic conditions. Injecting uncontaminated ground water into the formation, simulating a forced gradient flush or water flood, created the dynamic flow conditions. The static samples would be representative of the maximum concentration that would be anticipated in water samples from this location. Ground-water sampling was followed by a pre-remediation tracer study. The pre-remediation tracer study was designed to estimate the mass of NAPL in the formation. Once the pre-remediation tracer study was completed, the remedial technology was implemented and its performance monitored. At the termination of the remedial demonstration, the three characterization steps were repeated in reverse order. A time line for the activities is shown in Table 4.7.0.2. An analysis of this data permits an evaluation of the technology.
Cyclodextrin molecules are helical structures with a hydrophobic interior and a hydrophilic exterior. The objective was to use the characteristic of the molecule to transport the hydrophobic molecules through the formation since the molecule itself moves through the formation as easily as water. Essentially, this is a solubilization process since the cyclodextrin increases the hydrophobic "carrying capacity" of the fluid. The amount of remedial fluid required to achieve a cleanup level is related to the partition coefficient between the cyclodextrin and the individual contaminants and how cyclodextrin preferentially carries the different contaminants.
Table 4.7.0.1 Operating Conditions for the Experiments
| Parameter |
|
||
| Pre-Remediation Tracer | Demonstration | Post-Remediation Tracer | |
| Average Saturated Thickness (m) | ND | ND | ND |
| Average Head Across Cell (m) | ND | ND | ND |
| Average Influent Flow rate (lpm) | ND | ND | ND |
| Average Effluent Flow rate (lpm) | 4.29 | 4.58 | 4.32 |
Table 4.7.0.2 Study Sequence
| Test | Activity | Fluid injected * | Total flux rate (l/m)- volume (l) | Duration |
| Core and install instrumentation | Collect soil samples | None | 3/12/96 - 3/14/96 | |
| Ground-water sampling | Collect water samples | None | 5/27/96 | |
| Pre-remediation tracer | Establish flow field | Water | 4.6 lpm | ? |
| Inject tracer suite 1 | br,eth,pen,hex,dmp,methep | 4.6 lpm | 6/6/96 | |
| Maintain flow field | Water | 4.6 lpm | 6/6/96 - 6/16/96 | |
| Remedial technology | Establish flow field | Water | 4.6 lpm | |
| Inject remedial fluid | 10% cyclodextrin | 4.6 lpm | 7/20/96-7/31/96 | |
| Remove hpcd | Water | 4.6 lpm | 7/31/96 - 8/5/96 | |
| Post-remediation tracer | Establish flow field | Water | simultaneous with above | |
| Inject tracer suite 2 | br,eth,pen,hex,dmp,methep | 4.6 lpm | 8/6/96 - 8/7/96 | |
| Maintain flow field | water | 4.6 lpm | 8/7/96 - 8/13/96 | |
| Ground-water sampling | Collect water samples | None | 8/19/96 | |
| Core | Collect soil samples | None | 9/18/96 - 9/20/96 |
Table 4.7.1.1 Summary of Core Data Based on Boxcar Averaged Results
| Chemical | Pre-Remediation concentration (mg/kg) | Post-Remediation concentration (mg/kg) | Fraction Removed |
| dichlorobenzene | 130 | 27 | 0.79 |
| 1,1,1-trichloroethane | 3.8 | 0.91 | 0.76 |
| toluene | 16 | 4.7 | 0.71 |
| o-xylene | 14 | 4.3 | 0.69 |
| m-xylene | 5 | 1.4 | 0.72 |
| naphthalene | 7.2 | 1.5 | 0.79 |
| trimethylbenzene | 7.9 | 4.0 | 0.49 |
| decane | 68 | 50 | 0.26 |
| undecane | 250 | 170 | 0.32 |
| ethylbenzene | 2.8 | 0.64 | 0.77 |
| trichloroethene | 6.8 | 0.71 | 0.90 |
| benzene | 0.25 | 0.034 | 0.86 |
If one evaluates the performance of cyclodextrin based on fraction of mass removed, the performance does not look like one of the better performers. However, if one evaluates the mass of contaminant removed as a function of the number of pore volumes of remedial fluid used it begins to look like one of the better systems.
| Tracer | Pre-Remediation | Post-Remediation | ||||
| Concentration (mg/l) | Total Mass Injected (g) | Mass Recovered
(g)* |
Concentration (mg/l) | Total Mass Injected (g) | Mass Recovered
(g)* |
|
| Bromide | 292 | 438 | 340 | 304 | 432 | 203 |
| 2,2-dimethyl-3-pentanol | 531 | 796 | 553 | 619 | 879 | 798 |
| hexanol | 983 | 1475 | 871 | 1237 | ||
| pentanol | 1083 | 1624 | 797 | 1132 | ||
| Tracer Volume (l) |
|
1420 | ||||
| Injection Time (min) |
|
313 | ||||
One would anticipate good conservation of mass for bromide. In the pre-remediation study, only 78% of the bromide was recovered. In the post-remediation study, only 47% of the bromide was recovered. When mass conserve is not observed with bromide in a closed system one begins to question the internal consistency of the rest of the data. For this reason, we only discuss the tracer data on a qualitative basis rather than making quantitative conclusions based on the data. The pre-remediation tracer showed relatively uniform flow across the cell and the NAPL saturation estimates are reasonable for the highly contaminated conditions that were observed with the core data. In the post-remediation tracer analysis, two observations can be made. First, the time of travel is significantly less than almost one half the travel time for the pre-remediation study. Second, the apparent NAPL saturation has increased significantly. This suggests that either there was significant biofouling of the formation because of the readily degradable sugar molecule that was used to increase the solubilization, or that a significant portion of the sugar had gelled in the formation reducing the permeability and showing a partition coefficient to the tracers. Even from a qualitative standpoint, significant changes were observed in the aquifer properties and the long-term implications of this change should be investigated before the technique is implemented in a full-scale operation.
Table 4.7.2.2. Summary of Extraction Well 1 Tracer Analysis
| Extraction Well 1 |
|
Post-remediation | |||||
| conservative (bromide) | 2,2-dimethyl
-3-pentanol |
NAPL Saturation | conservative (bromide) | 2,2-dimethyl
-3-pentanol |
NAPL Saturation | ||
| Pulse duration (days) | 0.230 | 0.217 | |||||
| zero moment data | 61.861 | 90.957 | 30.049 | 170.078 | |||
| zero moment extrapolated | 65.408 | 95.691 | 30.269 | 109.569 | |||
| first moment / zero moment data (days) | 1.720 | 2.711 | 0.083 | 0.624 | 2.174 | 0.405 | |
| first moment extrapolated / zero moment (days) | 2.243 | 3.243 | 0.0673 | 0.631 | 2.311 | 0.432 | |
| Convective Dispersive Model | 0.045 | 0.280 | |||||
| dispersivity (m) | 0.275 | 0.339 | 1.870 | 0.255 | |||
| est. initial conc. (mg/l) | 209.725 | 1.405 | 163.943 | 403.675 | |||
| mean time of travel (days) | 1.052 | 281.096 | 0.516 | 1.593 | |||
| Stochastic model | 0.044 | 0.259 | |||||
| variance in travel time | 0.967 | 0.986 | 0.935 | 0.993 | |||
| travel time (days) | 1.098 |
1.454 |
0.546 | 1.596 | |||
| est. initial conc. (mg/l) | 271.997 | 312.126 | 167.455 | 384.059 | |||
Figure 4.7.2.1 Extraction
Well 1 Pre-remediation tracer analysis 2-2,dimethyl-3-pentanol
Figure 4.7.2.1.b Extraction
Well 1 Pre-remediation tracer analysis 2-2,dimethyl-3-pentanol log
Figure 4.7.2.2 Extraction
Well 1 Post-remediation tracer analysis 2,2-dimethyl-3-pentanol
Figure 4.7.2.2.b Extraction
Well 1 Post-remediation tracer analysis 2,2-dimethyl-3-pentanol log
Figure 4.7.2.3 Extraction
Well 1 Post-remediation tracer analysis hexanol
Figure 4.7.2.3.b Extraction
Well 1 Post-remediation tracer analysis hexanol log
Figure 4.7.2.4 Extraction
Well 1 Post-remediation tracer analysis methylheptanol
Figure 4.7.2.4.b Extraction
Well 1 Post-remediation tracer analysis methylheptanol log
Table 4.7.2.3. Summary of Extraction Well 2 Tracer Analysis
| Extraction Well 2 |
|
Post-remediation | |||||
| conservative (bromide) | 2,2-dimethyl
-3-pentanol |
NAPL Saturation | conservative (bromide) | 2,2-dimethyl
-3-pentanol |
NAPL Saturation | ||
| Pulse duration (days) | 0.230 | 0.217 | |||||
| zero moment data | 56.806 | 81.850 | 35.287 | 111.488 | |||
| zero moment extrapolated | 58.790 | 83.420 | 35.461 | 117.341 | |||
| first moment / zero moment data (days) | 1.239 | 2.120 | 0.105 | 0.481 | 2.101 | 0.585 | |
| first moment extrapolated / zero moment (days) | 1.645 | 2.317 | 0.059 | 0.485 | 2.444 | 0.699 | |
| Convective Dispersive Model | 0.089 | 0.251 | |||||
| dispersivity (m) | 1.333 | 0.311 | 9.886 | 0.316 | |||
| est. initial conc. (mg/l) | 251.586 | 289.441 | 278.879 | 430.926 | |||
| mean time of travel (days) | 0.772 | 1.283 | 0.506 | 1.451 | |||
| Stochastic model | 0.104 | 0.247 | |||||
| variance in travel time | 0.997 | 0.937 | 0.984 | 1.00 | |||
| travel time (days) | 0.770 |
1.364 |
0.512 | 1.451 | |||
| est. initial conc. (mg/l) | 270.960 | 379.727 | 236.876 | 430.926 | |||
Figure 4.7.2.5 Extraction
Well 2 Pre-remediation tracer analysis 2,2-dimethyl-3-pentanol
Figure 4.7.2.5.b Extraction
Well 2 Pre-remediation tracer analysis 2,2-dimethyl-3-pentanol log
Figure 4.7.2.6 Extraction
Well 2 Post-remediation tracer analysis 2,2-dimethyl-3-pentanol
Figure 4.7.2.6.b Extraction
Well 2 Post-remediation tracer analysis 2,2-dimethyl-3-pentanol log
Figure 4.7.2.7 Extraction
Well 2 Post-remediation tracer analysis hexanol
Figure 4.7.2.7.b Extraction
Well 2 Post-remediation tracer analysis hexanol log
Figure 4.7.2.8 Extraction
Well 2 Post-remediation tracer analysis methylheptanol
Figure 4.7.2.8.b Extraction
Well 2 Post-remediation tracer analysis methylheptanol log
Table 4.7.2.4. Summary of Extraction Well 3 Tracer Analysis
| Extraction Well 3 |
|
Post-remediation | |||||
| conservative (bromide) | 2,2-dimethyl
-3-pentanol |
NAPL Saturation | conservative (bromide) | 2,2-dimethyl
-3-pentanol |
NAPL Saturation | ||
| Pulse duration (days) | 0.230 | 0.217 | |||||
| zero moment data | 60.487 | 88.141 | 31.785 | 148.193 | |||
| zero moment extrapolated | 61.373 | 89.659 | 31.953 | 158.086 | |||
| first moment / zero moment data (days) | 1.188 | 2.320 | 0.142 | 0.593 | 2.192 | 0.444 | |
| first moment extrapolated / zero moment (days) | 1.278 | 2.487 | 0.140 | 0.599 | 2.622 | 0.555 | |
| Convective Dispersive Model | 0.077 | 0.365 | |||||
| dispersivity (m) | 1.867 | 0.493 | 0.924 | 0.367 | |||
| est. initial conc. (mg/l) | 301.528 | 309.650 | 152.722 | 608.762 | |||
| mean time of travel (days) | 0.978 | 1.536 | 0.445 | 1.654 | |||
| Stochastic model | 0.073 | 0.323 | |||||
| variance in travel time | 0.985 | 1.001 | 0.839 | 1.009 | |||
| travel time (days) | 0.990 | 1.214 | 0.496 | 1.689 | |||
| est. initial conc. (mg/l) | 305.238 | 424.112 | 173.912 | 593.570 | |||
Figure 4.7.2.9 Extraction
Well 3 Pre-remediation tracer analysis 2,2-dimethyl-3-pentanol
Figure 4.7.2.9.b Extraction
Well 3 Pre-remediation tracer analysis 2,2-dimethyl-3-pentanol log
Figure 4.7.2.10 Extraction
Well 3 Post-remediation tracer analysis 2,2-dimethyl-3-pentanol
Figure 4.7.2.10.b Extraction
Well 3 Post-remediation tracer analysis 2,2-dimethyl-3-pentanol log
Figure 4.7.2.11 Extraction
Well 3 Post-remediation tracer analysis hexanol
Figure 4.7.2.11.b Extraction
Well 3 Post-remediation tracer analysis hexanol log
Figure 4.7.2.12 Extraction
Well 3 Post-remediation tracer analysis methylheptanol
Figure 4.7.2.12.b Extraction
Well 3 Post-remediation tracer analysis methylheptanol log
Data appears to be internally reasonably consistent with the core data
with similar removal fractions for 1,2,4-trimethylbenzene,
ethylbenzene,
toluene,
and naphthalene.
It appears from the elution curve of the macromolecule
that the delivery of the remedial fluid was consistent across the cell.
One would anticipate that the analysis would be constant with the core
data. The results for three of the chemicals show strange variability
well to well: undecane,
decane,
and trichloroethene.
The concentration for undecane in well 2 is approximately 10 times the
concentration in the other wells. If well 2 were the correct values
and wells 1 and 3 miss reported by a factor of 10, the data would appear
much more consistent with the core data. Dichlorobenzene
appears to have eluted nearly 100% based on the elution curves while only
50% based on the core data. Either the core data underestimates the
mass removed or the remedial fluid swept a volume greater than the target
zone. Note that in the core
data figure dichlorobenzene there is a significant amount of contaminant
above the target region. The elution curve for o-xylene,
is significantly less than the mass removed based on core analysis.
Since GC/MS performed the core analysis and the elution curves were analyzed
by GC, it is believed that the GC analysis is less reliable and it is likely
the cyclodextrin was masking some of the o-xylene.
Table 4.7.3.1 Summary of Mass Removed in Elution Curve
| Chemical | Initial mass * (g) | Mass extracted (g) | Fraction removed |
| dichlorobenzene |
|
5278 | 0.97 |
| decane |
|
62.4 | 0.01 |
| naphthalene |
|
404 | 0.61 |
| o-xylene |
|
111.95 | 0.01 |
| undecane |
|
296 | 0.01 |
| ethylbenzene |
|
101 | 0.66 |
| toluene |
|
733 | 0.75 |
| trimethylbenzene |
|
203.6 | 0.26 |