1
1
Steam Enhanced Remediation
In Fractured Rock
(and a little about the other sites)
Gorm Heron, Scientist/Engineer
Hank Sowers, CEO/Chief Operator
Dacre Bush, Geologist/Program Manager
Gregg Crisp, Site manager
SteamTech Environmental Services
Bakersfield, CA
2
2
Creosote DNAPL to +140 ft depth
Alluvial sands and gravels with clays
Both LNAPL and DNAPL
Approaching MCLs in 2002
Craig Eaker, SCE
160,000 gallons removed from subsurface
In-situ destruction significant
UC Berkeley � LLNL - SCE
Visalia Pole Yard
7
7
Florida site! Full-scale clean-up with performance guarantee
! Steam enhanced remediation and electrical heating
! Tight pneumatic and hydraulic control
! Stimulated oxidation reactions for reduction of TPH concentrations in oily areas
! Detailed subsurface monitoring (temperature and electrical resistance tomography)
8
8
Extraction well with Hawthorn electrode
(EE)
Clay
Sand
Area A steam injection well with Hawthorn electrode (SE)
Perimeter steam injection wells (SI) Steam
Electrode
Electrode
Deep electrode
(DE)
Well types
9
9
Preliminary results, Edwards AFB
Acknowledgments to:
� Stephen Watts, Edwards AFB project manager
� Dave Leeson, AFCEE
� Scott Palmer, Earth Tech project manager
� Gregg Crisp, site manager and operator
� Layi Oyelowo, Edwards AFB
Results are preliminary, conclusions have not been published or confirmed by the above persons
11
11
Objectives/questions�Will SER be effective for removal of VOCs from fractured rock atEdwards AFB?
�How is the DNAPL mobilized and extracted?
�What are the ultimate VOC cleanup levels that can be expected atEdwards AFB using SER?
�How rapidly will the steam heat Site 61 at Edwards AFB?
�How should steam injection and extraction well-fields be designed for optimum performance at Edwards AFB?
�What is the optimal steam injection and extraction strategy for DNAPL in fractured rock at Edwards AFB?
�How long will the site stay hot after completion of the steaming?
14
14
Vertical distribution of contaminants before operations: PID readings on cores
0
200
400
600
800
1,000
1,200
1,400
1,600
1,800
2,000
0 5 10 15 20 25 30 35Depth below grade (ft)
PID
read
ing
(ppm
)B13 B14
16
16
Injection well
design
0
10
20
60
50
40
30
High-temperature grout (9 ft)
High-temperature grout (5 ft)
High-temperature grout (5 ft)
Coarse sand/gravel (9 ft)
Fine sand (3 ft)
#1/20 Fine sand (3 ft)
Fine sand (2 ft)
Fine sand (2 ft)
Coarse sand/gravel (13 ft)
Coarse sand/gravel (11 ft)
Wea
ther
ed z
one
(app
roxi
mat
ely
35 ft
)Fr
esh
bedr
ock
43
34
23
12
9
52
45
65
26
31
50
#1/20 Fine sand (3 ft)
Deep injection screen (58 to 60 ft)
Middle injection screen (38 to 40 ft)
Top injection screen (18 to 20 ft)
Dep
th b
elow
gra
de (f
t)
Note: Thermocouples were attached at 5 ft intervals from 5 ft below grade to 45 ft below grade, and at 49 ft, 52 ft, 55 ft and 60 ft.
19
19
Strategy
Vacuum test: Vapor capture radius ~ 80 ft
Initially steam injection deep only, extraction shallow
Air co-injection
Extract 25 to 50 % more than injected
Monitor carefully and adjust strategy
20
20
VEA-5
VEA-4
VEA-3 VEA-1
VEA-2
EW-1
EW-3
EW-2
EW-4
TMA-A
TMA-D
TMA-C
TMA-B
IW-1
Subsurface monitoring network
23
23
20
30
40
50
60
70
80
90
100
0 10 20 30 40 50 60 70
Tem
pera
ture
(OC
)
6/2
6/9
6/10
6/11
6/12
6/14
6/17
Depth below grade (ft)
Thermocouple data
24
24
20
30
40
50
60
70
80
90
100
0 10 20 30 40 50 60 70
Tem
pera
ture
(OC
)
6/2
6/9
6/10
6/11
6/12
6/14
6/17
6/20
6/21
6/22
Depth below grade (ft)
25
25
20
30
40
50
60
70
80
90
100
0 10 20 30 40 50 60 70
Tem
pera
ture
(OC
)
6/2
6/9
6/10
6/11
6/12
6/14
6/17
6/20
6/21
6/22
6/23
6/28
Depth below grade (ft)
26
26
Water balance
0
20,000
40,000
60,000
80,000
100,000
120,000
5/20 5/23 5/26 5/29 6/1 6/4 6/7 6/10 6/13 6/16 6/19 6/22 6/25 6/28 7/1 7/4 7/7 7/10 7/13 7/16 7/19
Tota
l vol
ume
(gal
lons
)
Total pumped from EW's
Total steam injected (as water)
Net extraction
27
27
Energy balance
0
50
100
150
200
250
300
350
400
5/20 5/23 5/26 5/29 6/1 6/4 6/7 6/10 6/13 6/16 6/19 6/22 6/25 6/28 7/1 7/4 7/7 7/10 7/13 7/16 7/19
Cum
ulat
ive
ener
gy c
onte
nt (m
illio
n B
TU)
Energy injected as steam
Energy extracted as condensate
Energy in pumped water
Energy in extacted vapors
Total energy extracted
Energy stored in formation
Energy balance
28
28
Vapor flow rate and PID readings
648
0
200
400
600
800
1,000
1,200
1,400
1,600
5/20 5/23 5/26 5/29 6/1 6/4 6/7 6/10 6/13 6/16 6/19 6/22 6/25 6/28 7/1 7/4 7/7 7/10 7/13 7/16 7/19
Mas
s of
TC
E re
mov
ed in
vap
or (l
bs)
0
1,000
2,000
3,000
4,000
5,000
6,000
7,000
8,000
PID
read
ing
at V
-1 (p
pmv)
lbs
ppmv
29
29
Headspace PID screenings on grab water samples
0
500
1,000
1,500
2,000
2,500
3,000
3,500
5/20 5/23 5/26 5/29 6/1 6/4 6/7 6/10 6/13 6/16 6/19 6/22 6/25 6/28 7/1 7/4 7/7 7/10 7/13 7/16 7/19
PID
hea
dspa
ce re
adin
g (p
pmv)
L-1
EW-1
EW-2
EW-3
EW-4
Headspace PID data
31
31
Results� Successful treatability study - great data
� Steam heated site partially, and accelerated mass removal
� More than 700 lbs of VOCs removed
� NAPL recovered where no NAPL was expected
� Air injection promising for opening fractures to steam flow, and potentially for reducing risk of NAPL condensation
� ERT apparently valuable at Edwards: Heated zones showed large changes in electrical resistivity
� Very uneven steam distribution: Increased focus on temperature monitoring, also in extraction wells