-------
i
I
TABLE IH-3
MASS TRANSFER COEFFICIENTS
Individual
Non-Aerated:
1.1 x 10
3.12 (1.024)
Aerated:
J (Prn) (1.024)9-2" „ H0»j /Di>H0 0.5
Floating Immiscible Layer:
kG - 1.1 x 10"4 U'78 D --OJ
sc
Overall
N'on-Aeratad:
e
ror a dilute aqueous solution at 1 ataosphera,
-^- - -I - I .
£Q£ k, ' fc (3.47 H) wnera H = Henry's Law
* ^ Constant (ata-£r3/ib-nol)
Aeratad:
A
(K ) -£
^oa7T A
c A ' ^--'-T. i
Convective Zone
vhera K - 3.47H
111-37
-------
TA3LZ IH-3 Continued
Turbulent Zone
1 ] + i
K(k_) vhere
Floating Immiscible Layer:
K-, - P k_/P_
Source: Arthur D. Little, Inc.
-------
1.3 Emission Reduction and Efficiencies of Controls
The reduction in emission rates is defined by:
- X,*,
and assumed e° be
Al -
A2'
wo
(Xoal
V
. .•* Cost-Effectiveness of Controls
----
In-situ:
A
constant = vR (S/yr)
-------
wnera y - cost per pound raduction
7 " A ($/lb-reduced)
R
Post-treatment:
A - F -I- pR ($/yr)
whera F - cose of collection system per year
P - cost per pound of post-treatment system
y - A - F 4- p ($/lb-reduced)
R R
In terms of throughput (T) and efficiency (E) :
In-situ:
A - yET ($/yr)
7 « A/ET (5/lb-reduced)
Pos t-treatmant :
A - ? + pET ($/yr)
7 - F T- p ($/lb-raduced)
ET
Pratreatment costs var*/
volatiles removed
r P°URd °£
dn- C«™-f°ir ?reCraaPerit: we-a- obtained from Sniv
1Q8A)
=or post-treatment by carbon absorption arc
from E?A (1932). "
2. Parameters
-e- • ,
.era ootaz.naa
the
d 3 ordars "
111-40
-------
/Inyl Chloride
lathyleue Cli
I'r 1 ch 1 orue thy 1 eno
i-Xylene
It-'thyl Ethyl K^tone
el ijicliloroetliylone
Lliyl benzene
-Butyl Alcohol
roiuobeiizcnu
irbon Tturachlorldo
Alcohol
'erage
west
TABLE 11 f-/»
TYIMCAI. VALUES FOR WASTE PARAMETERS
Liquid
Liquid Henry's Law Molecular Olffuaivity
Gas
J^15l£iL V|«ic<>sit)r Conun.nt
of oxygen In water ut 18"0
urce: Arthur D. I. It tie, Inc.
(^ || (,) . 0.5y x
(Ib/ft )
56.8
82.8
91.6
54.9
50.6
53.7
50.3
101.3
54.1
54.1
50.6
93. J
99.5
69.0
49.3
49.3
66.33
101.3
49. J
(lb/ft-at:c) (dtui-ft /
lli-iuol )
1361.42
3 xlO 129.79
3.9x10 145.75
4.4x10 U8.09
3.9xlfl"A
-4
4.2x10 83.29
2.8x10"'' o.70
6.0x10 132.94
4.0x10"'' J05.71
4.5x10'''
2.0xl()"3
a.oxio"4
6.5x10"'' 368.38
5.4xlO~'' 5«j 26
a.ixio"'1
0.4
6.05x10"^
2.0xlO~3
2.8x10"''
62.5
84.93
131.5
78 11
100.2
106.16
72.1
165.83
92.1
106.17
74.12
157 02
153.8
112 56
46.07
58.08
100.08
165.83
46.07
In Water Viscosity
(ft /hr) (Ib/ft-sec)
6.23x10
6.23x10
-5
~5
3.02X10
'5
3.5X10
1.9X10'
6.05X10
4.37X10'
'5
'5
3.77xlO
6.05X20
1.91X10
~5
"5
'5
Gas
IHtlust-
vity
(ft2/hr>
0.29
0.26
0.27
0.26
0.24
0.24
0.38
0.28
0.38
0.24
Schmidt Gas
Number Density
Ob/ft3)
0.17
0.24
0.37
1.71 0.22
0.28
0.29
0.20
0.46
1.86 0.26
0.29
1.88
1.71 0.44
2.13 0.43
2.13 0.31
1.30
1.82 0.30
2.13 0.44
1.30 0.17
A II
g-mol
6263
7572
8315
10254
9904
8150
9241
9369
9309
10158
8272
10098
9674
7642
8872
10254
6263
Vapor
• ressure
(utm)
3.5(25°C)
0.46(20°C)
0.079(20°C)
0.1(20°C)
0.0079(20°C)
0.102(20°C)
O.Ola(20°C)
0.029(20°C)
0.092(20°C)
0.043(20°C)
0.15(25"C)
0.016(25°C)
-------
The impoundment sizes chosen are shown in Table III-5. The
values for site and impoundment parameters are shown in Table ITI-6
Small impoundments are usually not aerated, and so the impoundment at
the tenth percentile is considered to be a non-aerated' imuoundmer.t
only.
3. Mass Transfer Coefficients and Emissions
TT_ /Th* average, high, and low values for waste parameters from Table
IIi-4 were substituted into the relationship for Individual mass
transfer coefficients. It was found, that individual mass transfer
efficients did not vary greatly with changes in values of wasta
characteristics (within only about one order of magnitude). Since the
primary intarest is ralative emissions under different control
situations, the average values for the waste characteristics given in
Xclu Ifi XI X"*» v7-3 -r"a I* & ~i*3 *•** j — .TJ _ _ if.. . * M . .. .. _ °
coefficients.
T,t,, TTT , -, — —- -=•-"-= *-.ia.i..3.<-i-st_3w_c5 given in.
Table III-4 wera used to define "typical" individual mass crarsfe-
nfe
The calculatad individual mass transfer coefficiants for non-
aerated Impoundments, aerated impoundments, and impoundments w-th a
floating immiscible layer are shown in Table III-7. These values may
be used ror most wastes with errors within one order of magnitude.
Overall mass transfer coefficients and emissions, for X, - 1, are
shown in Table III-8 and III-9 respectively for a range of Henry's Law
Constant and vapor pressure- In non-aerated impoundments with H much
less than around O.L atn-ft /Ib-mol, the waste volatilizes slowly at a
rate dependent on H. The gas-phase resistance dominatas over the
liqu.c- pnase (i.e. gas-phase controlled). For H much greater than
0.1 atm-rt /lo-nol, tne volatilization is liquid-phase controll-d and
reaches a maximum of k, for wastes with very high E. From ~afaie
L.J.-4, very few chemicals have low values for Henry's Lav Constant.
The ^values tor acetone and methyl ethyl katona ara around 0 5
atm-rt /la-owl.. 3-3romo-l-?ropanol and dialdrin ara verv non-volaf1-
compounds wish Eanry's Law Constant around SxlO"-1 at— f tVb—
-------
TABLE III-5
SURFACE IMPOUNDMENT SIZES
(Full Capacity) (757, Capacity)
Surface
Pereantile Capacity Area Depth Volume Surface Area Deoth
(ft3) (ft2) (ft) (ft3) (ft2) (ft)
_ 1,340 600 5 1,005 432 4
50% 73,260 2xl04 9 54,945 16,635 7.6
§ 90% 4xl05 3xl05 15 3xl06 259,112 12
i
g Source: Arthur D. Little, Inc.
111-43
-------
TABLE III-6
SITS AND IMPOUNDMENT PARAMETER VALUES
Site
Wind Speed, U ft/hr 52,800
Wind Speed at Surface, UQ - 0.035 x U ft/sec 0.513
Ambient Temperature, 9 aC 25
Impoundment
(At 75%-capacity)
Effactiva pool diameter, D ft
p
Effective deoth, H ft
o
Number of aerators
Diameter of aerator, D ft
Impeller rotational speed, u rad/sec.
Power to imaellar, ? ho
r *
Oxygen transfer rating of aerator,
J lb-02/hr-h?
Efficiency of power conversion, n
Oxygen transfer convection factor, a
Turbulent surface araa to turbulenc volume
Percentile of Impoundments
10Z 502
24.77 145.54
4 7.6
6
1.97
126
15.4
3
.73
.325
.09
90%
574.33
12
6
6
126
100
3
.73
.325
.0555
ratio a ft "
Volume affactad by aerators, V ft3 - 3,119 39,710
per aerator
Effective surface area of turbulent zone, - 1,704.0 13,236.0
Aj ft" (x number of aerators)
Effective surface area of convection zone,* - 14931.2 245376
'Assuming that surface impoundment is operating at 752 capacity.
Source: Arthur 0. Little, Inc.
tII-44
-------
TABLE III-7
"TYPICAL" INDIVIDUAL k VALUES FOR SURFACE IMPOUNDMENTS
WITHOUT CONTROLS
Non-Aerated
10%
50%
90%
1
I
Ib-mol/ft -hr 0.254
lb-mol/ft"-hr 0.654
0.205
0.379
0.177
0.257
1
I
I
Aerated
k Ib-!nol/ft2-hr
1- Ib-aol/ft-hr
0.42
703.53
1.78
531.37
Floating lamiscible Lavar
9
k lb-moi/ft~-hr 0.254
0.205
0.177
Source: Arthur D. Little, Inc.
-------
TAUl.li 111-8
2
102
Vapor Pressure
(Atmosphere)
''
7X10
7xlO~3
7xlO~2
0.7
7
Henry's Law Constant
(atiw-ft /Ib-moJ)
Non-Aururuil
50%
90%
Aerated
50%
90%
Floating Immiscible Layer
10%
50%
1.75x10"
1.44x10
-4
1.75xlO~3 1.44xlO~3
1.75x10
0.175
1.747
~2
1.44x10
0.144
1.438
~2
90%
1.24x10
1.24x10
1.24x10
0.124
1.236
-4
~2
It.
V '
JL'.
fc
ii:
10 J
I0~2
O.I
1
10
100
1000
10000
8.65x10"'
8.55xlO~3
7.65xlO~2
0.3726
0.6080
0.6490
0.6534
0.6539
7.11x10 ''
7.00xlO~J
6.00xlO~2
0.2474
0.3598
0.3770
0.378H
0.3789
6.11x10"^
5.99xlO~3
4.95xlO~2
0.1811
0.2467
0.2560
0.2569
0.2570
7.87x10"
8.96x10"
7.76x10 J
6.09xlO~2
0.3702
1.777
12.64
48.80
68.97
8.83x10
7.85x10
0.4840
3.086
15.54
27.37
29.65
-------
TAI1LE Ifl-'J
NJiJ''K< W ^^^ 1 / lir )'
Non-Aerated
Aerated
50%
90%
50%
Vapor Pressure
(Aim)
-4
-2
7x10
7x20
7x10
0.7
7
90%
Floating Immiscible Layer
10% 50% 90%
0.084
0.844
8.435
84.35
842.05
2.392
23.921
239.214
2392.14
23921.418
32.03
3.203x10
3.203x10'
3.203x10,
3.203x10'
2
Henry'u Law Constant
(atm-ft /ll
IO-2
10
0.1
1
10
100
1000
1 0000
0.4169
4.1211
36.8730
179.5932
293.0560
312.8180
314.94
315.18
11 .8276
116.4464
998.1 120
4115.5485
5985.3450
6271.4704
6301 .41
6303.08
158.3174
1552.0809
12826.044
46925.18
63922.93
66332.67
66565.87
66591 .78
13.0919
129.09
1146.17
6158.35
29560.75
210268.93
811797.76
1147329.74
232.164
2287.96
20340.29
125410.21
799619.63
4026600.48
7091895.44
7682670.80
Uaing (X( -X*)
Source: Arthur I). Uttle, Tin:.
I
ti
-------
impoundments, all the controlling parameters are aerator relate
except for ambient temperature and Henry's Law Constant. Th
temperature however, cannot be changed by in-situ control withou
impairing the effectiveness of the aeration treatment. Henry's La
Constant in this case can only be decreased by pretreatment and/or b'
limitation and exclusion of volatile wastes. The alternative 1
collection and post-treatment of emissions. For the impoundment witi
a floating immiscible layer, the vapor pressure of the volatile
component in the layer and wind speed directly affect K . Thi
effective pool diameter inversely affects X Vapor pressure* can b<
reduced by pretreatment and/or by exclusion* and" limitation, or b^
decreasing the temperature of the impoundment surface. For ver]
non-volatile waste (H « 0.1 ata-fcj/lb-mol, decreasing tht
temperature would reduce K for non-aerazed impoundments, but most
chemicals have H greater tnan 0.1 atm-ftJ/lb-mol. In summary, the
controllable parameters for each type of emission controls is shown ir
Table 111-10.
The Henry's Law Constant decreases with decreasing temperature.
At any temperature, the Henry's Law Constant of a compound is the
ratio of the partial pressure (P) and the solubility of "the compound
at that temperature. The solubility could increase or decrease with
temperature, but the sensitivity of solubility to temperature is not
as large as that of vapor pressure to temperature which are related by
the Clausius-Clapeyron equation:
d In P AH
v
d T A Z RTZ
where: £Z - 1 for ideal gas (vapor)
AH^ - heat of vaporisation, (cal/aol)
? • vapor pressure (ata)
5. - gas constant, (cal/mol-'S)
T - temperature, (3I<)
Neglecting the change of H with temperature, the simplest
solution to the above relationship Is:
In ? - A - 3/T
where A and 3 are constants;
dHv AH
3 * ITzSi * -=p (for ideal gases)
111-48
-------
' TABLE III-10
CONTROLLABLE PARAMETERS TO REDUCE EMISSION RATES
FOR CATEGORIES OF EMISSION CONTROLS
Q' - KoaA (XL - X*>
Parameter
Proportionality Effective on Impoundment Type
Pretreatment
Mol fraction of diffusing direct
component, X.
Design
Effective depth, H
Effective pool diameter, D
Wind Speed, U and U P
(by increasing freeooard)
Surface area, A
Operating
Temperature, 3
Wind speed, U and U
(by increasing frieboard)
Surface area, A
In- Situ
Temperature, 5
Wind speed, U and U
Effective pool diameter, D
Surface area, A
H
U
-.85
o -.11
p. 78
.67
(1.024)
9-20
U
U
.78
.67
A
(1.024)
3-20
u -78
.67
•A
aerated, non-aerated, float.
immiscible layer
non-aerated
float, immiscible layer,non-aerated
float, immiscible layer,non-aerated
non-aerated
non-aerated, float, immiscible
layer
non-aerated
float, immiscible layer, 'aeraced
float, immiscible layer, non-aeratad
non-aerated
non-aerated, float, immiscible
layer
non-aerated
float, immiscible layer, aeracad
float, immiscible layer, non-aeratad
non-aerated
float, immiscible layer, non-aeratad
non-aeratad, float, immiscible
layer
Sourca: Arthur D. Little, Inc.
111-49
-------
In ?l - In ?2 -
Using an average
P
8872 cal/g-mol and R = 1.9872 cal/mol-'K
T,-T,
(T in °K)
exp [4465 (T-^)/ (T^
Neglecting the sensitivity of solubility vith temoeratu-e
aenrv's Law Constant at TI is related to Henry's Law Constant acT^
esp [4465 (T
(T in °K)
VTV* ^"5 "S «laciansrii?3 of controllable parameters ^tamDaratur^
^nd .peed ana geometry^ to emissions, the reductions in amissiot- a-d
"L ;!:C1"S °r ChanSing an7 °f Che ?«»»«•« -era calc^'at^
Geometry changes vere made by keeping capacitv cor.st=n- ^
'!;r^rr:SS °: Ches.a, Ch,an?ss OQ "issicn raductions from non-aerat-'
and -ioauing:xamisci.ola-layer impoundments ara shcvn in F'*ur-s ^?-"
^1^ anc :__-; cor che 5Cch percantila impoundmanc. "= ---- '
The figures above shov efficiencies wichour ra^acins them to -.»•
controls. Using tht medians for Henri's Law Constan- and
""
s aw onsan-
pressure (100 atm-flb-mol and 0.07 «» r^«ece?"?T)" as-ors
reauctions and efficiencies were derived for 'each "7 the ^st-u
controls as described belov. The emissions r"duct?ons an"
emciencies are shown in Table III-U.
Rafts
The efficiency of rafrs is approximately eoual to the pe-
area covered. Vhite Styrofoam rafts 4 s 8 faec, 0.5 and f
thick vera chosen. It vas assumed thac 90 3ercant of the
surrace area or an impoundment is covered by rafts at anv time
of
-------
20
17.5
15
Float, limn. Luyor, 0.07 ami. v.|».
Non Acruiud. 100 iiliu (i3/IU inol
Source: Arthur D. Little, Inc., 1984
23 22
Temperature (deg. C)
FIGURE 1113 EFFECT OF TEMPERATURE ON EMISSIONS
(tiOih I'ERCENTILE SIZE IMPOUNDMENT)
21
20
-------
Efficiency %
'--^•'•^
-------
80 __
60 _
-------
TAHLE III-11
EMISSIONS M-mi
CONTROLS
Iri-Sttu Control a
Non-Aerated:
Uafla
Harr leva
Floating Spheres
Floating Immiscible Layer:
Ituftb
Harr lei a
Floating Spheres
*
Uciluct Ions
(lb/yr)
10% 50% 90%
2.468xlOU
3.0l7xlO;
1.207x10°
2.468x10
6.655x10
8.l34xl05
6
9 r -,o/ IA10
4.948x10 5.234x10
6.048xI08 6.397x10°
2.419x10° 2.559xlOl°
4.948x10° 5.234x10
I.887xl08 2.529x10°
2.307xl07 3.089xlOa
9.228xl07 1.2 36x10°
I.887xl08 2.527x10°
Efficiencies
(%)
10% 50%
90 . 90
11 11
44 44
90 90
90 90
11 11
44 44
90 90
90%
90
11
44
90
90
11
44
90
'(•! 1
-"• t
* ll,, I „(. llemy's Law Constant - 100 alm-f t3/ Ih-mol , vapor pressure
molecular weight = 100.08. X -X - I
' '•)!!
Source: Arlhur 1). I.I tt le. Inc. ; ;l'i
0.07 atm,
-------
of the area will be exposed due to difficulty of cutting the Scvrofoam
to fit the exact shape of the impoundment. The percent reduction will
be assumed as 90 percent. Additional reduction may result from any
effects on lowering wind reiocity over the remaining open surface that
are induced by the raft system.
Barriers
The reduction of wind speed over an impoundment is dependent on
the height:, length of grid ratio (H/L). Using flat Styrofoam
(expanded polystyrene) barriers 1x4 inch in a 8 x 8 feet grid (i.e.,
H/L = 1 inch/8 feet - 1.042 x 10 ), Crow and Manges (1967) obtained
11 percent evaporation reductions in test ponds containing water. It
is likely that the efficiency of a barrier also varies with the wind
speed above the influence of the barriers. An 11 percent reduction
was assumed for both non-aerated and floating-immiscible-layer
impoundments.
The Crow and Manges studies were carried out on water reservoirs
where diffusion is controlled in the gas phase. The relative
effectiveness of barriers on liquid phase controlled impoundments
would depend on the difference in dependence on wind velocity in the
trjo regimes.. The exponents on the wind velocity term in the t"o
relationships used in this study are not very different (0.78 in the
gas film, Mackay and Matsuga; 0.67 in the liquid film, Owens/Hwan?).
To the extent that these relationships are valid, barriers for
impoundments should behave similarly to water reservoirs.
Shades
The efficiency of a shade in reducing emissions from an
impoundment is proportional to the percent shade of the material used,
i.e., the amount of sunlight shaded out. Woven "black" polypropylene
usad in horticulture is chosen as the material for the shade. IT. pan
tests, 42 percent shade black, woven polystyrene mesh reduced
evaporation of water by 44 percent (Crow and >fanges, 1967* . The
reduction is due both to wind speed and temperature reduction. Ar
efficiency of 44 percent was assumed for non-aerated and
floating-iraiiscibla-layer impoundments.
Floating Spheres
The efficiency of floating spheres is approximately equal to the
percent area covered. On a fully covered surface, the covered area is
91 percent. According to vendor literature (Capricorn Chemicals'*,
efficiencies over 38 percent have been obtained experimentally for
open tanks. An efficiency of 90 percent was assumed.
-------
>Vp->-£»x;-'i-~i'"1*~f-i. "-..^"••X-•-'**= ,.i'-*-'>*~- -S —f'- "-t^" "..-.---> " -•-'_:-* '" - X:. ' -t-"1-'- <~ '-*.- •* " ''' ' ^'•'7--^-' y •J-"-^-•-•'•v •• -f'~ •*'••-*- ^.^—" :^J*.r:.-'. J^ ---^rgj^r^^a^aa^^ajSa
Vf-.--Jt7^:-;,>•-.-? 4—. : ^--"...--. - ,^ _ :_^ ;-Y^;r .-1. ,.-.-"-r^^^;i^Jk^rlS^:^-^zi^^^^"'^"'^''^'''''r^'''*"*"
^v-^'JU^'vl^.-^rfjCr-vU^^'^'^^-'^- ' ^*~- ^ ^J-'^J—«- -'
?ost Treatment
The rate of emissions is affected by the collection system since
Che collection system protects the impoundment from the environment.
Emissions are drawn out of the system by fans tnrougn a vent to be
post—treated.
efficiency of 95 percent and afterburning at 98 percent.
5. Costs
Pre treatment
Pr-t-earaenc costs taken from Spivey et al (198M «ere in the
o-der o~* Tl 00 ?er oound of volatiles removed from a wastastream
%WO/W. Cost's for pretraatment depend «- «»taStr.ao prop.rc,-s
rr-atmen- trrpe, system design and size. .he cosu va^ae cnosar
presented Ihe Jnge of most pre-treat,ent technologies wxth,n a
factor of 2.
In-situ Controls
"
TTT_"I xhe rationale used in obtaining material, instaj.-at.sr
ooiracicn/xaiacacaaca costs for each technology i5 dascnoeu ^^
Rafts
TWO thicknesses, 0.5 and 1.0 inch of ^,:panded
ve-> chosen for the costing or rarts.
lation costs are expected to be re.
is si-^e, involving little labor in cloating the
n«alcton s s-e,
"
ss rr^st.
1-inch thick 'Scvrofoam panels ara used.
-------
TAIJUS 11 r-12
UNIT MATEKTA1. COSTS FOIl SUUFACE IMPOUNDMENT EMISSION REDUCTION 1N-SITU TECHNOLOGIES
(Dollars per Square Foot, Summer 1984 Dollars)
EPS
Sheets
Size
4' x 8' x 1/2"
4' x 8' x 1"
EPS(1) Strips (8'x 8' grids)
Size
4" x 8' x 1"
4" x 8' x 2"
8" x 8' x 1"
8" x 8' x 2"
12" x 8' x 1"
12" x 8' x 2"
10th Percentile
0.08
0.13
50th Percentile
($/ft2)
0.06
0.12
90th Percentile
($/ft2)
0.05
0.10
0.04
0.08
0.08
0.17
0.13
0.25
0.04
0.08
0.08
0.15
0.12
0.23
0.03
0.06
0.05
0.11
0.08
0.17
Shade Cloth
(2)
Percent Shade
21%
57%
92%"
0.07
0.11
0.20
0.07
0.10
0.18
0.07
0.09
0.17
(1) Expanded polystyrene
(2) Woven "black" polypropylene
-------
TAIll.E 111-12 Continued
(Doll art, per Square Foot. Summer 1984 Dollara)
Spherea
Polypropylene
Diameter 1 3/A Inchea
Diameter 6 inchea
High Denslcy Polyethylene
Diameter 1 3/4 inches
10th Percent-He
7.55
50th Percentlle
(I/ft2)
6.75
90th Perccntile
6.55
U.69
5.05
7.50
4.65
7.50
6.75
Snurcea: Hcllabl e Pluatlcu, NewatU, N.I. 1JBA
X. S. Smith Company, Kalonlown. N.I. 1 ->»"
Capricorn i:liemU-ulu Corporal ion, Secaucua. N.I, J
-------
In-Sltu
ANNnAL
TAHI.E 111-13
V'OR SUIU-'AEH TMPOUNDMKNT CONTROLS. $/YR (Summer 1984 Dollars)
Kafts
Barrlers
Shades
Floating Spheres
I'oat-Treatment
Collection
**
jOth Percent lie
38.56 - 62.66
19.28
53.02
514.00 - 682.00
50th Percentlle
998.11 - 1996.22
665.41
1663.52
13672.00 - 20305.00
24000
90th Percent lie
12955.60 - 25911.20
7773.36
23320.08
196087.00 - 316270.00
250000
I
»':f
*' J
u- •
ii
ViJi
I
i
Installation, 0 and M, and other costs not Included.
Treatment costs are variable costs depending on the amount of
emissions treated. These costs are discussed In the text. The
coats shown here Include basic structures and installation.
f:':
B ..'
Source; Arthur n. Little, Inc.
j
I
-------
TAHl.E
UK I .AT I VJl J MSTAI ^XJU
OF IN-STTU CONTUOI.S
I
Installation
50%
90%
Operation/Maintenance
10Z
50%
90%
Uaftu
0.5-1 inch Styrofoam
Low
Lou
Low
Lou
Lou
Lou
Itarrlera
a1 x 8' grJda of Styrofoam
atrJps
Shadea
Black woven polypropylene
Medium
High
.
Hlgli
High
High
Lou
Lou
Lou
Low
Lou
Low
I'olypropylene/IIDPK
Lou
Lou
Lou
Lou
Lou
Low
Source: Arthur D. Little, Inc.
-------
Barriers
A 8 x 8 feet grid made of Styrofoam strips 4" x 8' x 1" was
chosen for the costing of barriers. The barriers may be 4 inches or 1
inch high. These barriers are expected to last a year. Barriers are
expected to entail relatively high installation costs because the
Styrofoam strips have to be constructed into a grid formation and
installed en the impoundment surface. For small impoundments, the
grid is small and consists of relatively few strips. The design and
installation of the grid may be relatively easy. For. large
impoundments, the design and installation of the grid may have to be
sub-contracted and will be expensive. Operation and maintenance costs
are expected to be low under normal conditions. However, strong winds
may effectively destroy a grid. Heavy snow may also damage the grid.
The volume of Styrofoam generated that have to be disposed is lower
than in the case of rafts but is another element of the costs in the
use of wind barriers. - —
Shades
Black woven polypropylene shade cloth used in horticulture is
chosen as the shade material. There is not much difference in price
within a small variation of shade value so the cost of a 57 percent
shade value is used for that of a 47 percent shade value of the same
material. The installation costs of shades are expected to be
relatively high. For small impoundments, the shade may be stretched a
few inches over the impoundment and secured at the edge. Shade cloth
is sold in pieces and pieces need to be sealed together to obtain a
large enough piece to cover impoundments. Larger impoundments may
require the use of floats spread out over the surface of the
impoundment to prevent the shade from dropping below the impoundment
surface. In horticultural use, the shade cloth is used for- the 3
summer months and lasts between 7-9 years. For year around use over a
surface impoundment, the lifetime is estimated to be between 1-2
years. Operation and maintenance costs are expected to be low under
normal conditions. However, strong winds and heavy snow may damage
the shade or cause the shade to drop below the surface. The volume of
shade cloth that needs to be disposed of at the end of its useful life
is smaller than in the cases of rafts or barriers.
Spheres
Polypropylene spheres of diameters 1-3/4 inches and 6 inches are
used to provide a range of costs for spheres. The polypropylene
spheres are cheaper than the high density polyethylene (HDPE) spheres
for the same size spheres and are available up to 6 inches in
diameter. HDPE spheres are available in only one size (1-3/4 inches
diameter) . Installation costs of spheres ara expected to be
relatively very low. Depending on the chemical(s) present in the
impoundment, spheres are expected to last a relatively long period of
use. An estimated lifetime of 10 years was used to annuaiiza costs at
10 percent per year. Operation and maintenance costs are expected to
-------
be ve-y low, or zero. The volume of spheres that need to be disposed
of per year and at the end of its useful life is much smaller than
Sytrofoam barriers or rafts.
Post-Treatment
Costs for oost-treatment consists of the costs for the collection
svstem and the' treatment. The collection system cost is a fixed
an^a! cost for the design size as shown in Table «^- tt" «£
was estimated by Air Structures International, Inc. (Tappan, NY) .or
^o air structures covering 17,000 square feet and 260,000 square feet
corresponding to the 50th percentile impoundment and the 90tn
pe"entile impoundment respectively. The 10th percentile impoundment
was too small for the installation of an air structure. The a .
structure for the 50th percentile impoundment was I/O feet ,l°ng. 100
feet wide and 36 feet high made of translucent rabnc wita a cable
system ard anchors for support. It has an exit door and an entrance
door a "10^ BTU heating system, a 24,000 W lighting system ana a
vehicle air lock system. The 90th percer.tile impoundment .«
structure vas 260 feet wide, 1,000 feet long, and /5 ieet high, made
;ra±r^^
1 wers3.* Th°e Bating sys'tem was a 12.5 * L0ff BTU *«- ^.'J"
lighting ar.d the vehicle air lock system were not estimate because
these varied greatly depending on the requirements. Installation
costs we~e estimated to be between 31-2 per square root, wnich
includes foundations. For this analysis, installation «s estimated
to be SL.50 per square foot. The costs snown do not Delude
maintenance (which is low) and energy costs. Costs ror the co.lec ion
system are shown in Table III-I5 with costs annualizec at 10 pe.ce..t
in LO years.
-eat-e*"- costs are variable costs dependent en the total
ns Veated. To estimate the treatment cost per pouna or
ons removed, a 10,000 cubic feet per minuta wastestrean
a'-ning 50 oom trichloroethylene was chosen as a raprasencate
through 'the post-treatment systam. Tb. emissions tr.r
system would be around 10,000 pounds of ICa per year. _ An-uai
^stalled capital costs for both carbon adsorption anc ar.a.su. .
Gere at least one order of magnitude lower than annual operating cos.,
198"). Total installed costs for carbon adsorption was a3/,00u
ed to an annual operating cost of 3870,000. Total instaliec
'or afterburning was 3230,000 and annual operating cost was
costs
S45'and sVo "respectively (SlOO.OOC/Mg
ar-e-ou—e-s ara'also less expensive than non-catalytic systems. If
these 4o "roes of post-treatment systems are included, the treatment
costs for post-traaLent would be between 35-10 per pound TCE ramovea
(311,000-22,GOO/MS).
-------
TABLE III-15
CAPITAL COSTS FOR COLLECTION SYSTEM
FOR POST TREATMENT (Summer 1984 Dollars)
50th Percantila 90th Percentila
Structure 70000 985000
Heating 24500 175000
Lighting 15000 Not estimated
Air lock vehicle 15000 - 24000 Not estimated
Installation 25500 390QQQ
Total " 150000 "IbUUOOO
Annualized * 24000 ' 250000
(10%, 10 years)
Source: Air -Structures International, Inc. Tappan, NY, 1984
111-63
-------
6. Cost-Effectiveness of Controls
Table 111-16 expresses the cost-effectiveness of in-situ controls
in terms of the cost per percent of reductions per square foot of
impoundment. Figure III-6 illustrates these values on a graph that
compares the cost-effectiveness with impoundment size. Each sat of
points represent the effectiveness for the 10th, 50th, and 90th
percentile impoundments. The figures show some slight economies of
scale. Of the in-situ controls, rafts appear to be the most cost-
effective. Shades are more cost-effective than barriers in terms of
the pounds of emissions reduced. Floating spheres are the least
cost-effective of the in-situ controls. When installation and
operation/maintenance costs are included, the relative
cost-effectiveness ranking of in-situ controls will not change,
because rafts have low relative installation and operation and
maintenance costs. Shades and barriers have higher values for these
costs but the material costs for spheres ara so much higher that the
relative cost-effectiveness of spheres is still expectad to be the
lowest.
Figurss III-7 and III-S show the hyperbolic functions relating
cost per pound of emissions reduced or ramoved to the throughput of """""
volatiles per year and the total pounds of volatilas ramoved per year ""_
respectively. 'The horizontal curves represent the pretraatment cost
per pound of volattiles ramoved. There are some economics of scale for '-/. ^A^
pretraatment, but these have been neglected. Each of the hyperbolic -"- - ^—
curves are at a constant annual cost of in-situ controls. The curves ;
for post- treatment are not shown because collection and treatment
costs for post-treatment ara very high and are over in the top right '=
hand corner of the figure. For the most part, the post-craacment
curves do not appear within Che rang a of Che other ccr.trol.5.
Figura III-7 incorporates the efficiency of each control
technology by considering the throughput of volatilas. On the bottom
left of the figure whara the horizontal linas represer.tir.s
pretraacment ara below and to cha left of the curves, ?ratreatment is I
more case-effective. Whara the horizontal curves ara abova cha ;
hyperbolic curves, the in-situ controls ara more case-erfactive. As
aay be seen, pratraattient is mora cost-effective for small svstams, ~-
i.e. low emissions reduced and low throughputs. In a medium siza :
impoundment, at pretraatment costs of S2.00 per pound removed ^
($4,£00/Mg) or less, throughputs of less than 1,000 Ib per year would l
favor pratraatmant. At higher throughputs of volatilas', in-situ 2
controls ara more cost-effectiva. In terms of throughput, rafts ara ,i
still the most cost-effective of the in-situ controls and spheres ara ^
the least. Shades when compared in tarms of throughput' ara more S
cost-sffactive than barriers. This same .comparison of effectiveness 5
applies to small and large impoundments as well. Unless pratraacment f
costs for a wastastraam ara extremely low (much less than $0.50 per J
Ib), in-situ controls ara generally more ccst—affactive of all the I
controls. J.
fS-
-------
; -t^ f~:' • i rv-i"* -•
TABLE 111-16
COMPARATIVE COST-EFFECTIVE^
FOR IN-SITU EMISSIONS CONT^nTg
Rafts
Barriers
Shades
Floating Spheres
Z Reduction
per ft2 ($/ft2)
8.9 - 14.4
36.4
25.0
118 - 157
(xlO"4)
6.7 - 13.3
36.4
22.7
91.3 - 136
5.6 - 11.1
27.3
20.5
84.1 - 136
ara annualized for ,Dhea at
of installation, 0 and M and othJr
the relative cost-ef?actlvenes^ rc
see text.) ^-tiveness ranking
S' C°SCs
year3' The inclusion
aX?eC=ad C° ch«Se
r each technology. (pie=se
Source: Arthur D. Little, Inc.
-------
Rafts Barriers Shades
Controls
Spneres
'Only material costs are used. Installation
0 and M, and other costs are not included.
SURFACS .MPOUNDMENT CONTROLS'
lii—OO
-------
n
H
M
Post-Treatment, p = $45/lb
Carbon Adsorption
Post-Treatment, p « $16/lb
Post-Treatment, p • $5/ll>
Adsorplion wild ReQeneration
Pretreatment $2/11
0
Pretreatment
10
Source: Arthur I). UiLlu, Inc., 1984
FIGURE III 7
™ SURFACE .MPOUNDMENT CONTROLS VERSUS THROUGHPUT
-------
I
I
111 rtnlucutl (removud) per
Sonrct-: Artliui- I). I.I I Lie, liu:., 1'JH/t
FIGURE III 0 COST EFFECTIVENESS OF SURFACE IMPOUNDMENT CONTROLS
VERSUS REDUCTION
-------
Figure III-8 shows the cost-effectiveness picture for various
annual costs and a wide range of pounds of volatiles reduced or
removed per year. Each of the hyperbolic curves represents an annual
cost. As an example, for an in-situ system that costs $1,500 annually
and if pretreatment is $1.00 per Ib ($2,200/Mg), a removal rate or
reduction of emissions of greater than 1,500 Ib per year would favor
the in-situ control. If pretreatment cost was increased to $2.00 per
pound ($4,400/Mg), a rate of greater than about 800 Ib per year
reduced (removed) would favor the in-situ control costing $1,500 per
year. The $17,000 annual cost curve which corresponds to using
spheres in a 50th percentile situation illustrates the point.
Floating spheres in this impoundment would be more cost-effective than
pretreatment if the emissions reductions achieved was more than 17,000
Ib per year and pretreatment was $1.00 or more per pound ($2,200/Mg)
of volatiles removed.
E. Summary
In-situ controls are generally experimental and in many cases are
taken from some other different kind of applications. For example,
rafts were experimentally studied in reservoirs as evaporation
controls. Spheres are more directly transferable than the other
in-situ controls, since they are used in emissions control from
treatment tanks. On the whole, data on in-situ controls are very
poor. There also appears to be limits on the use of some in-situ
controls on large impoundments.
In any in-situ control, there is some point at which it becomes
more cost-effective than pretreatment. This tradeoff point is very
sensitive to pretrsatment costs. For a small change in pre-treatment
cost, the trade-off point will shift relatively far to the left (with
greater pratreataent cost) or to the right (with smaller pretraatment
cost). Estimates of emissions from uncontrolled surface impoundments
are of the order of 300,000 metric tons per year (GCA, 1982). This
reference also estimates that thera are about 2,000 operating
impoundments. On the average, then, emissions ara about ^00 metric
tons per year per impoundment. At this rata, in-situ treatment should
be considerably more cost effective than pretreatment.
Post-craatment, including collection and treatment is the most
expansive control technique. The curves for post-traatment would fall
above and to the right of the in-situ controls in Figures III-7 and
IIT-3. If the only concern is the rate of reduction of emissions,
post-treatment would never be cost-affective. However, if thera is
concern about the absolute level of removal, the tradeoff to be
considered is between pretraatment and post-traatment. Post-treatment
is more expensive than pretreatment for each pound of volatiles
removed primarily because very dilute mixtures in. a gaseous medium ara
treated. For example, for carbon adsorption assuming no regeneration,
the cost per pound (not including collection) post-treatad is $45. A
regenerative system would cost around $5 compared with a regenerative
carbon adsorption pretraatment of around $1 per pound. If, however,
-------
-CTJ.^4&;£4S^
the waste cannot be pretreated, post-treatrient may be the only way to
remove volatiles even though the cost is between. $10 - 50 per pound,
excluding collection coses. If there is a market to encourage
recovery following post-treatment, this alternative may become less
expensive. Also, the post-treatment alternative may be more
attractive if, as in the Upjohn case, the volatiles can be replaced in
a treatment impoundment.
If the design objectives offer any flexibility, there may be
opportunities to reduce emissions by altering the1 design of an
impoundment. Operating procedures also present possibilities in
emissions reduction.
F. References
Air Structures International, Inc. Tappan, NT. July 1984. Personal
Communications.
Bartholic, J.F., J.R. Runkles, and S.B. Stenmark. 1967. Effects of a
Monolayer on Reservoir Temperature and Evaporation. Water Resources
Research, 3:173-179.
Beraett, U.K., L.A. Halper, N.C. Jarvis, and T.M. Thomas. 1970.
Effect of Adsorbed Monomolecular Films on the Evaporation of Volatile
Organic Liquids. Industrial and Engineering Chemistry Fundamentals,
9:150-156.
Breton, H. et al, 1983. Assessment of Air Emissions from Hazardous
Waste Treatment, Storage, and Disposal Facilities (TSDF's)
Preliminary National Emissions Estimates — Draft Final Report - GCA
Corporation for the USEPA. GCA Resort No. GCA-TR-33-70-G fAu*ust
1983). " *
Capricorn Chemicals Corporation. Secaucus, NJ. June 1984. Personal
Communications.
Cluff, C.3., 1967. Rafts: New Wav to Control Evaporation. Crops and
Soils >!agazine, 20:7-9.
Crow, F.R. and H.L. Manges, 1967. Comparison of Chemical and
Non-Chemical Techniques for Suppressing Evaporation from Small
Reservoirs. American Society of Agricultural Engineers, Transactions,
10:172-174.
Crow, F.R., 1973. Increasing Water Supplies by Suppression cf
Reservoir Evaporation. OWRR A-I04-OKLA. Oklahoma Water Resources
Institute, Stillwater, OK.
Shrenfeld, J. and J. Bass. 1983. Handbook for Evaluating Remedial
Action Technology Plans. SPA-6CO/2-33-076. U.S. Environmental
Protection Agency, Cincinnati, OH.
-------
' ~
Federal Register. May 19, 1980. Vol. 45, No. 98, D. 33075
'
;' - ;~r •••<••«
for Che D.S. Environmental Protection A/» 'a"/- Re'orc- ?reparad
Washington, D.C. "election Agency, Ofrice of Solid Wasta,
Und Oi
facilities.
s, Presented at 1984
I»«l»« of Chemical Engineer'^
^
Coerflclent5 for Surface
, =££? ', ,
' on
Enginearing,. 51:434-439.
Journal of Chenical
ta« tavers.
. 8. P
argacon Press
AIr
Pollacion
r»cin. University of Arnsaayet
tics. ;:e,ar,, „. ;une IM4.
v /*• o TT- •
Vloci;'FrS--m> '"' ' G
Missions." ,e?rint
,er Coe.icie
i e, If"""'
Air Pollution Control Techr-'
Triangle Institute, •.M^'.
— Cental Protection Agancy, rai.-
- " -«-««=•.«« as an
*- Je3e"=h
' "" B-S-
rocengs
*«er V**. Chicago, Illinois L7
Cheaical Corporation,"
Personal Conmunicanions.
Confa«a"
n r
' Connecticut. April 1984.
-------
U.S. Department of Health, Education, and Welfare. 1970. Control
Techniques for Hydrocarbon and Organic Solvent Emissions irom
Stationary Sources. National Air Pollution Control Administration
Publication No. A2-68. .U.S. Department of Health, Education, and
Welfare, Public Health Service, Environmental Health Services,
National Air Pollution Control Administration, Washington, DC.
U.S. Environmental Protection Agency. 1978. Control Technologies for
Volatile Organic Emissions from Stationary Sources. EPA-450/2-78-022.
U.S. Environmental Protection Agency. 1980. Lining of Waste
Impoundment and Disposal Facilities. SW-870. Office of Water and
Waste Management, Washington, DC.
U.S. Environmental Protection Agency. June 1982. Handbook for
Remedial Action at Waste Disposal Sites. EPA-625/6-82-006. Office or
Emergency and Remedial Response, Washington, DC.
U.S. Environmental Protection Agency. July 1982. Draft RC3A Guidance
Document Surface Impoundments Liner Systems, Final Cover, and
Freeboard Control.
U S. Environmental Protection Agency. September 1982. Closure of
Hazardous Waste Surface Impoundments. SW-873. Office of Solid Waste
and Emergency Response, Washington, DC.
"W.L. Gore and Associates, Inc. Nevark, DE. June 198*. Personal
Communications.
X.S. Smith Co. Eatontown, MJ. June 198*. Personal Communications.
-------
IV. CONTROLS FOR TANKS
A. Tank Description
1. Definition
means a stationary device, designed to contain an
accumulation of hazardous waste which is constructed primarily of
non-earthen materials (e.g., wood, concrete, steel, plastic) which
provide structural support (Federal Register, May 19, 1980).
2. Types, Construction and Uses
The types and construction of hazardous waste tanks are similar
to those used for the storage of petroleum liquids. The types of
tanks are: open tanks, fixed roof tanks, floating roof tanks,
variable vapor storage tanks, and pressure tanks. The minimum
accepted standard for storage of petroleum liquids is the fixed roof
tank. In the hazardous waste area, open tanks are still in use.
Since detailed descriptions of tanks may be found in several readily
available sources (U.S. EPA, 1977; U.S. EPA, 1978; U.S. EPA, 1980;
American Petroleum Institute, 1962; 196^; 1980), we will only describe
them briefly here.
Open Tanks are essentially tanks without a roof. Concrete-lined
basins are by definition considered tanks (Federal Register, May 19,
1980). They are examples of open tanks.
Fixed Roof Tanks have a fixed roof equipped with some type of
vent.
Floating Roof Tanks consist of tanks with a roof that is frae co
float on the surfaces of the stored- waste. External floating"roofs
are exposed en the surface. Internal floating roofs are covered by a
fixed roof which protects the roof from the weather.
Variable Vapor Storage Tanks work by storing expanding vapors
emporarily in a gas holder. Venting occurs or.lv when the holder
capacity is exceed. During periods when vapors are contracting, the
stored vapors are transferred back to the storage tanks.
Pressure Tanks can withstand higher pressure variations befor»
incurring emission losses.
Tank material, configuration and auxiliary equipment must
correspond to and be compatible with the stored waste. " Materials of 11,1.1
construction include carbon steel, stainless steel, corrosion Jf
resistant alloys, aluminum, concrete, or fiberglass reinforced ' l'
plastics. Tanks vary widely in configuration, fabrication techniques
materials and operating conditions. Small tanks (between 1,300 to
-1,000 gallons) nay be shop-fabricated. Larger tanks ar=
rield-erectad (Corripio et al, 1982).
-------
. tothoe .
tte uses of tanks are very simlai w tt o£ uasces. Besides
except that tanks «. «« «7otto treatLr.t by biodegradation,
nentraUzatiofoxidation, anons *any other uses.
3 . Operation
operations of "
^ operations of -*"" ddld"^? «U S2(
treatment tanks, reaSents ««7 be ^ 'Each tank has a specified
•£ SS.'Lp'SSS^'S^* - » - — al"ldy
contained in the tat*.
of
,
treatment. The influent could be ^
Lsta could be added from ^"^f^^^'cank per year is called
T^e total volume or wasta processed thro S ^^ by tha
the throughput per year. , Tht ^ £ tiEes per year vastas
c ed *.
turnover rate.
, A of their lifetime, or when operations have ceased,
At the end of tiieir *•->•*— '
tanks are disassembled ana disposed o..
3. Emission Sou~^ and y.odels_
!. General Description of Factors Affecting Emissions
^ssicns to the atmosphere occur when the
or its contents withdrawn and aiso wai-e .n- -an. -
i c-» i •.•-flCJ on is dependent on tn«
rata of_jw*a"*70^."tVa"ts" and the surrounding
-
those affectir.g wasta volati^at on ^n ^ a i=?ouadmenc but
r^eatad hera. in open c«.c - J^^id surfaca due so che higher
vith a very low w-nd speed £ -jj^^ of wks . Please rarer
s for a =ore detailed description.
H«d roof tank emission losses are due to:
(breathing losses), and
17-2
-------
o vapor displacement due to filling and emptying (working
losses).
Floating roof tank emission losses are due to:
o losses due to imperfect fit of the seal and losses through
the gap between the flexible seal and the inner wall
(standing losses), and
o losses due to the vaporization of the wet tank as the roof
decends when the tank is being emptied (withdrawal losses).
2. Emission Models
The relationships describing emissions from tanks are described
in GCA (1983). For comparison, the base uncontrolled case will
consist of two different uses of open tanks; storage and aerated
treatment. Each of the different roofs (fixed roof and floating roof)
will be considered as a control alternative. The relationships for
the latter type are empirical. The models for emission losses from
open tanks are the same as those describing surface impoundments.
Table IV-1 summarizes these relationships.
The definition of each of the parameters in these relationships
is shown in Table IV-2.
3. Parameters That Control Emissions
The rate of emissions from an open tank depends on the overall
mass transfer coefficient, the exposed area, and the concentration or
mole fraction in the waste. These are the same factors that determine
the rate from surface impoundments and are not repeated here.
C. Potential Controls
1. Summary of Applicable Controls
The categories of potential controls are similar to those used in
surface impoundments: pretreatment, design and operating practices,
in-situ controls and post-treatment. Each control will be described
under these approaches in terms of their mode of action, expected
effectiveness and related costs. Only those approaches not already
covered in surface impoundments will be discussed in detail.
2. Pretreatment
Pretreatment basically removes the volatile components of a waste
before it is put into a tank. A detailed discussion is given in the
Surface Impoundments chanter.
17-3
-------
TA3LZ IV-L
RELATIONSHIPS DESCRIBING EMISSION LOSSES IN TANKS
OPEN STORAGE; Please see Surface Impoundments, Non-Aerated
AERATED; Please see Surface Impoundments, Aerated
FIXED ROOF TANK:
Losses » Q. » L, + L
xi a w
Breathing; L - 2.26 x 10~2 K . P °-68 D L-73 H °'51 AT °'5° ? CK lb/vr
'
Working: L - 7.56 x 10"4 M P K» K Q Ib/y
W *i C
FLOATING ROOF TANK:
Losses = Q. = L •*•• L
i s v
Standing: L = K V^ ?* D '1 K E Ib/rr
S3 c r
Withdrawal: L - (0.943) Q CT WT Ib/yr
w i. u
D
Source: American Petroleum Institute
1
-------
PARAMETER
TABLE IV-2
PARAMETERS FOR TANK EMISSION RELATIONSHIP?
DEFINITION
Waste;
M Molecular weight
P True vapor pressure at bulk liquid
Kc Product factor
P (also Vapor pressure function
environment)
CL (also Shell clingage factor
tank)
WL
Tank;
D
H
N
Average organic liquid density
Tank diameter
Average vapor space height
Point factor
Adjustment for small diameter tanks
Turnover factor
Seal factor
Seal related wind speed component
Secondary seal factor
Average throughput
Effective depth
Exposed surface area
Site (Environmental);
v Average wind speed
AT
8
Average ambient diurnal temperature change
Average ambient temperature
(P/PA)
UNITS
Ib/lb-mol
psia
bbl/1000 ft2
lb/gallon
feet
feet
bbl/vr
rear"
mph
[1 + (I-?/?.)0'5]2
A
where ?A =. average atmospheric pressure = 14.7 Psi
psia
IV-5
-------
•VL."--^ if - ~^aJf 7^_t:- J. - ^_£~-?v jLj*. ' ^- r%*j-~ •-- ^A-T^
^•fc"** -.-.•-•.»— , ^r-,-^ci^','"_^ST*_T-»^K--A.—-ariari V
3. Design and Operating Practices
For a tank with fixed capacity and throughput, design
considerations to control air emissions include surface area
minimization and inflow/outflow pipe locations. The choice of a fixed
roof tank, external or internal roof tanks, and other types of tanks
are also viable design alternatives. An operational change that could
decrease emissions is the temperature of the influent. These
practices are discussed in Surface Impoundments.
4. In-Situ Controls
Technologies applied at a tank can be used to change one or more
of the parameters that affect emission rates from the surface of an
open tank. The in-situ controls described below are: fixed roof,
floating roof, rafts, and floating spheres.
4.1 Fixed Roofs
It is commonly accepted that fixed roofs over open tanks reduce
emissions. Fixed roofs with a pressure/vacuum vent only release
vapors when the internal pressure is exceeded. Fixed roofs are
generally dome-shaped, and they are either welded or bolted onto the
top of the tank wall.
Considerations in designing a fixed roof for an open tank
include:
o The pressure vacuum settings of the breather valve in a tank
is determined by the structural strength of the tank for
safety, and the maintenance of a vapor concentration below
the lower explosive limit.
o As shown in the equations above, the choice of paint on a
tank is an effective means of reducing emissions, although
the factor is more important for the fixed-roof tank than
the floating roof tank. A highly reflective paint reduces
the temperature of the tank and the liquid stcred in the
tank.
o Xoof material must be compatible with waste components.
Another kind of roof which may or may not be fixed is the
aluminum dome. Information for this technology was obtained from
Temcor in Torrance, California (1983^. The material used in the
construction of aluminum domes ara aluminum alloys. The dome is
formed using aluminum struts to form a triangular space truss. Tnis
is then covered with triangular panels. The dome does not require any
columns for vertical support. Individual domes can be constructed
alongside tanks and lifted into place. Hundreds of aluminum domes
.have been installed all over the country. Aluminum domes have been
used to cover petroleum storage tanks, bulk storage areas, wastewatar
-------
lffri"nir -r^r.t.,... ,,r-i- , ^m*g^aLttiieL^-:.v^vs*ErSS^
treatment tanks, wacar and ocher liquid storage tanks. In wastewate-
treatment, for example, hydrogen sulfide or other gases from treatment
can be collected and treated. The dome also provides insulation to
increase process efficiency.
Each aluminum done is designed for the purpose at hand. An
important consideration in its use as a storage/treatment tank cover
is the structural strength of the tank wall because it is the main
support for the dome. The waste in the tank has to be compatible with
aluminum.
Vapor losses due to wind venturi action are eliminated because
there are no seals used as in the case of a floating roof. There ar=
no floating roof weather problems. The aluminum dome is maintenance
free (according to Temcor) and aluminum is very resistant to
corrosion. Since there are no columns necessary in the design of an
aluminum dome, there are few appurtenances. According to Temcor, the
cost of an aluminum dome is competitive with a stsel cover. Expensive
downtime is eliminated because individual domes can be constructed
separately and then lifted into place.
4.2 Floating Roofs
An excellent description of floating roofs and the cvpes of seals
available with floating roofs is given in U.S. EPA (1930). There are
basically two kinds of floating roofs, external and internal floating
roors. Internal floating roofs are again divided into two tvpes-
contact where the roof floats on the liquid surface and non-contact
wnen the roor is supported on pontoons several inches above the licuid
5TT1"*" 3 f+ a T-
race.
_ rloating roofs are by far the most commonly used method of
hyarocaraon loss control in the petroleum industry. Thev a—
generally considered inherently effective in reducing emission losses!"
^
— __..^ wu*^Ml *JJ«W4_t * W 3 3C ^3 •
raauctions of around 95 percent over fixed roofs
(U.S.^PA, L976). In the internal floating roof, the fixed roof -s
ventaa to _allow surficient air into the tank to maintain a vancr
concentration below the lower explosive limit. All internal floating
roors are designed to be retrofitted into existing fixed roof tanks!
Seals for floating roots are normally sold separately from the roof
ana are not necessarily dependent on the roof design (U.S. EPA, 1976).
According to Jonker et al (1977), the tyoe of seals used is
important in determining emission losses from tanks. Maintenance of
seals was also found to be important in reducing emissions. Secondarv
seals were determined to be effective in reducing emissions in this
study. Gaps between tank walls and seals of greater than 1/3 inches
were also found to be unavoidable for the vast majority of tanks. As
expected, these authors concluded that the amount of liquid exposed to
a gap, the access of wind through the gap and to the vaoor above the
liquid, and the length of path for the vapors to reach the ataosche-o
were important parameters in controlling air emissions.
at
-------
Runchal (L978) used a cyclone fanes on the tank top to modify the
aerodynamics above the roof of an external floating roof. He found
significant reductions in the pressure diffarancas on the two sides of
the roof. Substantial impact on windflow was therafora achieved by
the fence and wind-induced emissions were also probably reduced
significantly as a result although emissions were not measured.^
Significant reductions were also obtained when the floating roof
operated at a greater depth from the top of the tank (greater
freeboard). These tests show the importance of the wind speed and
flow in determining emissions from external floating roofs and are
considerations in the design of a floating roof tank.
Other considerations include:
o Stability of the floating roof under stresses of water and
snow. A pan floater is lass stable than a pontoon roof (Air
Pollution' Control Association, 1971). A covered floating
roof does not have this problem.
o Insulation of the roof can reduce temperatures in the tank.
In a floating roof tank, a double-deck roof is not only mora
stable but has insulating qualities as well (Air Pollution
Control Association, 1971).
o Roof material and seals oust be compatible with waste
components.
o Modifications to the tank may be necessary. Tank wall
deformations and obstructions may have to be corrected so
that seals will conform to the wall.
4.3 Rafts
Please see discussion in Surfaca Impoundments.
4.4 Floating Spheres
Please see discussion in Surfaca Impoundments.
5. Post-Treatment
As discussed in post-treatment in surface impoundments,
collection and post-treatment requires collection of emissions by
means of a cover and a vent, and traatment units(s) at the vent. In
the case of tanks, the collection system may consist of a fixed roor
or an aluminum dome with a vent, and post-treatment with a variety of
treatment tachnologias. Descriptions of two approaches, carbon
adsorption and afterburners ara given in the chapter or. Surface
Impoundments.
-------
A post-traatment systam has been installed at a facility owned by
Waste Conversion in Hatfield, Pennsylvania. This facility treats
wastes including acids, caustics, sewer sludges, coolants, food
processing wastes in about 25 tanks. All of these are hooked up to
scrubbers. The first scrubber was installed 4 years ago, and there
have been numerous additions since. The post-treatment system
includes carbon adsorption (sent to another company for regeneration),
wet scrubbers with sodium hypochlorita and "caustic soda, and
precipitators. In this facility, there is some in-situ control as
well, in the addition of activated carbon to treatment solutions
themselves to adsorb volatiles before emission. The whole system is
large, e.g., the carbon adsorption consists of 5 carbon drums 12 faet
in diameter and 9 feet high each. The primary purpose of all the
controls is the reduction of odors. Otherwise, 'the operators of this
facility believe that they do meet point source air standards with
controls. So far, the system costs around $500,000 (Waste Conversion,
Personal Communication, July, 1984).
D. Effectiveness of Tank Controls
1. Methodology
1.1 Selection of Parameter Values
To evaluate the eff activeness of controls in reducing emissions
from tanks, waste, tank and site (environmental) parameters necessary
for quantifying emissions were defined. These parameters were shown
in Table IV-2. Parameters required to calculate emissions from open
tanks were the sane as those used in surface impoundments exc=p«- for
wind speed at the surface of the liquid. This was varied because
etriciancies from the baseline of using controls are very sensitive to
the surfaca wind speed.
From various sources of data, GCA (1983) compiled typical ranges
or^values for input parameters used in relationships for" calculating
emission losses from tanks.
One tank size was chosen from these data as a representative
tank. Other average or representative values were chosen for a7!
parameters within reasonable expectations of tank design and
operation. Some economies of scale are expected for larger' sizas.
The general cost-effectiveness relationships developed below for the
single representative case are axpected to hold for larger sizes.
1.2 Calculation of Mass Transfer Coefficients and Emissions
The storage tank was selected to represent the tanks in use
Treatment tanks were not considered as different because technologies
to control emissions would be similarly effective in treatment and
storage tanks, unless the treatment tank was aerated in which case
Boating roots, rafts and floating spheras would not be viable as
-------
control technologies. However, for each technology that is applicable
to both types of tanks, the relative efficiencies and cost-
effectiveness would be equivalent. It was also assumed that emissions
were liquid-phase controlled.
The relationships for calculating mass transfer coefficients and
emissions losses were shown in Table IV- I. Total emissions from open
tanks were calculated as in surface impoundments. The floating roof
tank chosen for comparison is the external floating roof tank.
Emissions using rafts and spheres were calculated as 10 percent of
baseline plus losses due to clingage during withdrawal using L for
floating roof tanks. w
1.3 Emission Reduction and Efficiencies of Controls
The open tank was used as the basis of comparison for all the
control technologies, i.e., it was considered the tank without
controls.
The reduction in emission rates is defined by:
a - qt - Q2
where the subscripts I and 2 refer to tanks without controls and with
controls respectively.
The efficiency (E) is defined by:
E - 100 (Q - Q
The reduction in emission ratas depends on the baseline select ad
in terms of surfaca wind speed in the open tank. The efficiencies cf
controls ara extremely sensitive to surfaca wind speed. Curves cf
efficiencies of the controls with varying surfaca wind speeds will be
shown.
L.£ Cost-Ef f activanass of Controls
The in-situ controls for emissions raductions wera compared using
the cost of each percant of Deduction efficiency per square faet of
surfaca area ($/percant-ft~) . Carves were developed to shew
cost-affactiveness with varying surfaca wind speed based on the
relationships in Table IV- 1. Pratraatment, in-situ controls, and
post-treatment wera compared by considering the curves of cost per
pound removed (reduced) versus pounds per year removed (reduced) .
Similar curves were ganeratad for cost per pound removed (raducac"5
versus throughput in pounds per year. As in the discussion an surface
impoundments the curves ara:
-------
,*»,,,*-
7 = £ (?/lb-reducad)
y - A/ET ($/lb-reduced)
Post-Treatment y = 1 + p ($/ib-reduced)
F
7 = 2T~" "*" p C?/lb-ramoved )
whera: A - annual cost of in-situ control ($/year)
R » reductions (removal) (Ib/year)
E » efficiency of control
T » throughput (Ib/year)
F - cost of collection per year ($/vear)
p - cost per pound of post-traatment ($/lb)
dlffAWe f.comPared in-situ, post-treatment and pretreatment using
situ costsPwea-ereoaC3er C°-S ^ Caken.from Spiv«y at al (1984). In!
Post-treatment costs were obtained from EPA (1982).
2. Parameters
.^ ^ ^\*"r^^2£^^ r?r
™;3f iaf £'£%rzxz- wrs-s^._
o be usea in the floating roof and that thev we^e i-
aooa condition. The waste parameter (?) was choser as 1
representative value for wastes storad in tanks.
3. Emissions
Emissions were calculated using a mole fraction of 1 ^r the
volatile components in the impoundment. Emissions from one^ tanks
che U^i
4. Emissions Reduction and Efficiencies
In-Situ
Emissions reductions and efficiencies of each of the *n-s'tu
'-±J:!^^Tabfar7-4- Curves of efficiencies of ^
—,_ ^T^ ^ anr? -^"* ^ *• *• v
fixed roofs. External floating roofs^
, are much more efficient than fixed roofs
s
ts and spheres become less efficient than fixed r
-------
Tank:
TASLZ IV- 3
PARAMETER VALUES FOR TANKS**
PARAMETER VALUE
UNITS
100.08 Ib/lb-aol
2.5 psia
Kc 1.0
? 0.0466
CL °-3 bbl/1000 ft2
WL 9 lb /gallon
D 45.75
H 10 faac
1.3
c i.o
Kj 0.6
5S °'7
H 0.4
E? 0.75
Q 8.2 x 10 bbi/year
Ho 30
A 1643.9
Site (Environmental) :
7 10
iT 15 «7
9 25 «C
**
Assume tank is 40 feet call capacity s 11,700 bbl, and turnovers
per year - 70. Primary and secondary seals, both the good condition
Source: Arthur D. Little, Inc.
rv-12
.1
---a
-
-------
TABLE IV-4
I2**§J»!LJ^ICIKIICTESOF CONTROLS
Surface Wind
Speed
(l'0/ft/aec)
2 x 10~5
10-*
2 x I0~/l
10
"2
Fit
**
j£l!ii£lioiisOl)/y r ) *
El'R
***
Rafts/
Spheres
FR
Rafts/
Spheres
16,107
86,431
779,609
2,490,508
12,025.586
72,603
142,656
508,440
8 36. 105
2,547.004
12.082,082
61,032
124,080
453.286
748,184
2,287,993
10,869,563
13.6
45.8
81.5
.88.4
96.1
99.2
61.3
75.6
91.7
94.8
98.2
99.6
51.5
65.8
81.8
84.8
88.2
89.6
I
K
>
*
**
***
unit ,nole fraction of volatile covenant
FR - Fixed Roof
EFR - External Floating Roof
Source: Arthur D. Little. jm:.
-------
100
90
30
70
SO
5 50
'3
40
30
20
10"
10"
10'°
Surface Wind Speed, UQ ft /sec
FR » Fixed Roof
EFR a Extsrnal Floating Roof
Source: Arthur D. Litels, Inc., 1934
10'
FIGURE IV-1 EFFICIENCIES OF IN-SJTU CONTROLS FOR TANKS
-------
•»&tk:£l^'f,S-^^r^^T'' ^ ,-" - '- fi'"
t.
through the po«-tr.«ment unit
»* fician=7 of
«« <« ^arisen:
Iha
and the
carbon
an
5. Costs
j?r e treatment
In-Situ Controls
b?
the differance in a new tank wlch a
According to the vendor, Se S«a
ithin the saae magnitude of a" or
by taking the difference!
Installation costs wer<=>
-he cost for aluminum domes
spneras have verv low Insta
-re not included" in chrj
-or rarts and spheres vere not included.
ra,..R°70f3 hfve a lccS lifetime Cover 25
ra.ts last 1 year and that
« «
n
Per
"cfs, Che loca£ion
derived ^ Caki"S
W±thouc a roof'
Iv vould be
as the figures
years)
u
««•
*S ^ «of3.
and float^^
, TheSe ««'
Disposal costs
as3UEe^ =^at
»
-------
TABLE IV-5
Tanks
1
Open top with vind girder
With column supported cone roof
With double deck external floating
roof incl. primary and secondary
seals
Total
95,000
115,000
215,000
la-Situ
Column supported cone roof
Aluoinua dome^
Double deck external floating
roof incl. priaary and
secondary seals
Rafts
Bloating spheras
Collection
C«xcl. treataent)
1. For t.
and
20,000
16,000 - 25,000
120,000
130 - 210
10,300 - 14,300
Annualizad
3,200
2,600 - 3,900
19,000
13C - 210
1,700 - 2,300
16,000-25,000 2,600 - 3,900
17-16
-------
c aftarb»~
6.
P°ur.d, rasoec-
of
r -
°P*ratad in
appea"
'affec«ve, bai
ng
of
Figuras IV-
catlk
'Pectivelv. r
constant *•*-,
costs.
-3icu c
ontrols and for ^
es are ac a
ae levels of
T7-3
n
•j-c c-t"ia boct
om la;-
-
.
""«=«=»« cost
-srractiva,
and fi:c
hyperbolic
S^ i.72^. "^"iS1^ SS?
S %^^S?5^ ^ȣ^ rs?
wt^-^-^^«2-t5£^:
, ,:
Sfl
I III I
-------
TABLK TV-6
COST-KFPKCTIVENKSS FOR TANK IN-SITU CONTROLS
3
Surface Wind Speed
(ft/uec)
10
2 x 10
—5
-5
Hf<
2 x
10
10
r3
-2
Cout-Kffectlvenean
Column Supported Aluminum
Cone Uoof
I'.. 2
4.2
2. 4
2.2
2.0
2.0
Double Deck Ext.
Dome
II.
3.
2.
1.
1.
1.
7 -
5 -
0 -
8 -
7 -
6 -
17.
5.
2.
2.
2.
2.
5
2
9
7
5
A
Floating Uoof
18.
15.
12.
12.
11.
11.
9
3
6
2
8
6
Rafts S
0.2 - 0.3 2.
0.1 - 0.2 1.
0.1 - 0.2 1.
0.1-0.2 • 1.
0.1 1.
0.1 l.
Iphei
0 -
6 -
2 _
2 -
2 -
2 -
refi
2.
2.
1.
1.
1.
1.
1
7
1
7
6
6
5
Multiply
Source: Arthur I). Little, Inc.
-------
O
c
30
m
O
O
TO
J>
3)
J>
m
o
O
tn
m
Tl
-ii
rn
O
m
2
m
in
(A
O
•n
o
O
2
00
O
Tl
O
JO
CO
t/J
o
C
n
n
n>
it
Cost-
. $ per P
00
m -n
x1 -
o
oil
oo
r*
H-
rt
ft
(U
M
M
n
*
^8
6" **•
01
f-\
3
id
OJ
0
o
-*»
^
3-
o
i.
3
Q.
M
t)
A
a
ID
n
O
CJ
"'"• /•'-
j f!''-i>
! i' "V'
I [•:• ^;
j I-.1;/..
I )?.- •
I rrV
-------
o
I
i
Puil Trudlmenl. (> » j46/lt»
iUui|iii
-------
A). ._
(iO
/ E
F - 3000. p = $4S/U,
Adsorption
F - 3000.,, - $5/11,
R«uwwrailon
K
"
I
$
r-
f.vv:
. .
I'';
I:?-
••-*
•S.'s
-------
•' i n'M «fri frf^'Hi'if''~^^i~'-'^'^sgj3SSzi^.
If the price of post-treatment can be reduced, it may become more
iii^n^r*1 f"°acins r°°fs « *ro«gh£cV",7
around 10 Ib/yr (e.g., if post-treatment costs $5/lb ($11,000/MO
vxth . caroou regeneration). Under low ost-trea*
-treatmet costs
than fi.el
r0nf,In ChS a.na^sis' the "fluencies and the cost-effectiveness of
roofs are prooafaly underestimated with respect to spheres and rafts
Fixed roots are likely to be very comparable to using spheres'
of the iow cosc °£ ' "
Figure IV-4 shows the cost-effectiveness versus the pounds oe-
year recuced or removed per year. Each of the hyperbolic cu4es
represents au annual cost. la-aim controls «» favored co
precreatnent as the pounds per year is increased. If "« TTn-si"
orn!lnLflaS f TUal CrC °f S3'000/^ (corresponding to fixed roo7
or alumiaua dome), a reduction rate of 3,000 Ibs/yr is the trade-o°-
point at which the in-situ control becomes more «s".£f.ct" ?
pr.treaea.nt at the cost of $l/lb ($2,200/Hg). If pr.tr.IU.lt
vas increased to $2.00 per pound (S4>400/Xg)f a rate of
E. Summarv
Roofs are well-used, proven emission control technologies -om
deJ-'i^ra^Sv^teen1"' • F£°aCia* s?heras> »d to a much leaser
industry for emissions control. Pretreatment ^and^oo^t-^"3
ao «. easily a
t~e case or tanks. :,asCe Conversion in Hatfield, ?\," is a ,«od
esanpie wnere post-treatment has been used effec-'^e'V "
ssicns from treatment tanks. As an example o'? a"
ao.e procuct Calgon Corporation offers 7..Morb, a t
Ventsorb is a 55-gallon dn
specifically developed Co be used at
process applications. Each unit co_ «w.«u ^jj-ao^ a
and^h"7 P°Sed °f aftar asa§a- Tha ^ics can also be taken
a"-. C e "rbon re?lacsd- Replacement carbon costs around $300 " o
am.. (Calgon Corporation, Personal Communication, September 1984)'.
Certain technologies may be applicable in storage tanks but -
in treatment tanks. Floating roofs are general!, not aon
Post-treatment are applicable to
-------
*Ssiisj£iuii_
r° a similar wav -fn •
8" M Ser °U"
or in s
vaste before
without a large V«
-------
F. References
Air Pollution Control Association, 1971. Control of Atmospheric
Emissions from Petroleum Storage Tanks. Journal of the Air Pollution
Control Association, 21:260-268.
American Petroleum Institute, 1952. Evaporation Loss from Fixed Roof
Tanks. Bulletin 2518. American Petroleum Institute, Evaporation Loss
Committee, Washington, DC.
American Petroleum Institute, 1964. Use of Variable-Vapor-Space
Systems to Reduce Evaporation Loss. Bulletin 2520. American
Petroleum Institnta, Evaporation Loss Committee, Washington, DC.
American Petroleum Institute, 1980. Evaporation Loss from External
Floating Roof Tanks. Bulletin 25L7 (Revised). American Petroleum
Institute, Evaporation Loss Committee, Washington, DC.
Calgon Corporation, Pittsburgh, PA. September 1984. Personal
Communications.
Chicago Bridge and Iron Company, Boston, MA. July 1984. Personal
Communications.
Corripio, A.3., K.S. Chrien, and L.3. Evans, 1982. Estimate Costs of
Heat Exchangers and Storage Tanks via Correlations. Chemical
Engineering, 89(2): 125-127.
Federal Register, May 19, 1980. Vol. 45, MO. 98, p. 33075.
GCA, 1983. Evaluation and Selection of Models for Estimating Air
Emissions from Hazardous Waste Treatment, Storaze and Disposal
Facilities. GCA-T3.-32-33-G. Revised Draft Final Report. Prepared
for the U.S. Environmental Protection Agency, Office of Solid Vases,
Washington, DC.
Jonker, ?.£., C.3, Scott, and W.J. Porter, 1977. Pollution
Regulations from Floating-Roof Tank-Seal Study. Oil and Gas Journal,
75 (24):72-75.
Runchal, A.K., 1978. Hydrocarbon. Vapor Emissions from Floating Roof
Tanks and the Role of Aerodynamic Modifications. Journal of the Air
Pollution Control Association, 28(5): 498-501.
Spivey, J.J., C.C. Allen, D.A. Gcasn, J.P. Wood, and R.L. Stailings.
1984. Preliminary Assessment of Hazardous Waste Pratreatment as an
Air Pollution Control Technique. Draft Final Report. Research
Triangle Institute, Research Triangle Park, NC. " For the U.S.
Environmental Protection Agency, IZRL, Cincinnati, OH.
IV-2 4
-------
Temcor, Torranoe. CA. , October !983. Personal Co,«uni=ations .
rlr '. "«« " *'•«-. ^
Tanks. E?A-i50/3-76-036 Hydr°';a'bo.n Missions from Petroleum Storage
KesearchTriangUPark.se. E^iron«eatal Protection Agency,
r Ed
Protection Agency, ^search Triange Park uc B'S-
"
•-USr^-S; 198C°- .B""» B^»i»» '».
EPA-450/3-30-034a. n.S Enliror J / i ^, " PraP°sal Standards.
Triangle Park, 8tc. E^"on«ental Protection Agency, Research
Emergency and Remedial .2-^- <****•
Conversion, HatfieZd, PA, July 1984.
-------
I. LANDFILL.'?
A* Landfill
techniques is required by
practices to isolate che
UndfiU facility contains "r.e
-
T -«•• •»
,,A varia <" control
" wlr " Sood o»erating
« «vironM«. A typical*
«-„„
U,Uids. Containers
regular patterns. Bulk solids
and are distributed over che
equipment. Bulk liquids are »ed lth
being placed in the landfiH. IJca,
are ^dled essentially ^ the
" bulk
generally in
'h. Undlill
"" °f "'"-moving
soUdf"" '
soil
soil cover generally consists of fron 6 ?0
or other aggregates capable of b«in? , " rf
suosequent !ayers flifts) of »Ltes and
at "n
large operations.
ChaC day'
°f 3oi1' fl? «>".
. ' cre
m"=a as several acras at a fav
t ent
Che land surface foiloving c7osu°8
~
S°me M"s to
use
in
the
-------
B* Session Sources and Models
I « General
n
.r
ily (or te^orarv) cove-
permeate che final" (per^anVut)
landfill. The rata of emi7/£m
the for* in which the ^^T
operating practices at the facility.
; fr°° ac
T the arsa wich «*
aT* ? ^/^ COnP°u^s «c
Cl°Sed Secci°°s of the
be
tight so that no essins
integrity at soce lats- dat- then
utltiaately penneate through' the
through the cover into the ?r Vo^
diffuse to the surface and into t
generally quite low as aar'
solid surface and exhibit
-
aaoiene conditions and
bui:< solids,
MW"d C° bi
onca^e"s lose
C3nsc^^==s can
""* and ^SSra.
" ** *«& 3olids
v ^ racas
b'C°M abs°rfaed On
carried out by adding liquids dife"c*' TV
operating face and then olac'n* ^ the
possible to have pools of l^id nr-J
good practice *ould avoid th"s '
vould be siailar to those « »
organic layer or a land Cr«".*
applicacion of vastas.
be avoided for nmar
tica, etc., ic wifl not
- h °?fraCl0ns
^ bul.
-------
'&iig&ti£^^&&&t3tt:
KH^jav«iw«'«^mX¥TH*VfiSfXK
•;: ^\T£^t^itsfeslSs
the
„
atmosphere in su, Or in may a
2« Hoission Models
onlv
-
Covers
—usion through covers
where:
Q
A
D ..
volatilization raca nb/h
area of cover (V) a
effactive diffusivitv (f 2;
I!
-------
Tor the top cover, the concentration in the atmosphere can
generally be neglected relative to the concentration below the cover.
Effective diffusivity expresses the diffusive behavior of a single
compound through the pores of the cover for soils or through the
fabric of a synthetic cover. Of several equations available for
soil-type covers, Parser's (1978) equation appears most appropriate in
terns of the objectives of this analysis. It is relatively simple but
indicates how diffusion relates to soil properties. Parser's equation
is:
7
where: D . * diffusivity of compound in air (ft~/hr)
£ » porosity of air-filled pores
t * total porosity
Further, porosity can be related to the density to which the soil
has been compacted as:
where: 3 » soil bulk, density (lb/ft3
9 = . particle density (Ib/ft )
If the soil is completely dry, then total porosity and air-filled
porosity are the same and the effective diffusity becomes -he norsal
diffusivity in air. If the soil is wet, part of the pore volume
becomes filled by vatar. In this case, the air-filled porosity
becomes:
where:
-------
ADC
m
m
where: A - area of cover (ft2)
Dm " Permeation rate of a given diff using. compound
through synthetic cover material (ft /hrj
C - concentration of diffusing vapor at the top
or the landfill (Ib/ft )
Cm * thickness of synthetic cover (ft)
j-.
where: c = vapor concentration (Ib/ft3)
< ** empirical constant
x - mass of volatile compound absorbed oer unit
mass of soil
a » empirical constant
where:
vapor pressure of pure component (atm)
molecular weight of diffusing' component
(Ib/lo-mol)
gas law constant (0.73 ata-ft3/lb-mol-°F)
temperature (aR)
T = temperature
Y - activity coefficient
x - mole fraction
-------
i _
II
For dilute solutions, Henry's Law can be used as an alternate
iorm. In all of these relationships, vapor concentration increases
with increasing temperature, all other factors being equal.
Bulk liquids
The mix of free liquids and solidifying or bulking agents can be
represented by the models developed for land treatment. In land
treatment, also called land-farming, oily wastes are deposited en and
tilled into soil surraces. The rate of emission displays a complex
time-varying relationship reflecting depletion of" the volatile
materials near the surface (Thibodeaux as reported in Hwan» 1982)
The characteristic time for land treatment" cycles is qu'it- Ion-
relative to the period during which mixed liquids are exposed at the
working face of a landfill. At landfills, bulk liquids are mixed v* eh
solidirying materials such as kiln dust, prior to deposition in the
landfill. Pooled tree liquids may be present, but onlv for short
periods. The bulked liquids, in the solidified matrix, mav be exoosed
to the atmosphere for periods ranging from hours to several days."
In this situation, it is reasonable to assume that losses occur
at the exposed surface through diffusion from free lisu'd in the po-as
or the bulking agent. In this case, the mass flow equations s-
to:
Ak C*
oa
where: A » area of exposed face (fc2)
• T:Cjja * overall mass transfer coefficient (ft/hr)
C - equilibrium concentrations above free i-'
(To/ft )
For purs or mixed organic compounds, the overall coe---'"-'»~- -3
generally gaa-fila ccntrolled and follows a law siailar'To" chose
discussed in the surface impoundment chapter. The coefficient deoe-ds
generally en wind speed, seme characteristic dimension of the expose-
surface, and diffusiviry in air.
Bulk solids
liquid rarfaca.
-------
-. '-. >' - =J»i. .'- -
3. Controlling parameters
Covers
as the vater tableevel)
leachate collection
factors
3nd lin"
to
™r"s 'Is a VT stro°s *s«i«"7
-owermg the internal temperature of ^»
volatile emissions. Diffusivity of
selection of the basic cover
content. For synthetic covers,
and memo ranee thickness.
Working faces
mass transfer coefficients as -
practical. ~" '
Since
means of
-^ would reduce
m°difi2d b^
and moiscure
of
-Id reduce
- bulk liauid is
cc^ld be added.
-2_ac facilities
s" case, is not
c- Controls
1- Introduction
There i
compared to
the _ same for all "cr«aKaenc and
Design and operating pracf'c=>s mav ,-a^ ' . 5 -i«ariixs.
without interfering Jith aormal 0™it "ont" ,em±SS10ns "nsiderablv
covers including vents is ^^d^thm^a8Wn 3f P««umeni:
£3;~;is:=^^in::?^ss
includes t-,0 distinc, cypas of'conJoiT' P°SC ' CraaC—- Broaches,
**
^ «sts are
landfill,.
-------
-JM-.. r^JF^ j^r^f ^U^ -W ~*1 r-^^r^-rrT*^'^
-------
froa being filled. Table 7-1 shovs a ranking of a variety evr>es of
soils according to several different functions («* igygf ri?
c'^^^r/110;' ^^ very hish =^---/97^;rtun:teDi:;
correspona to clays and miXes of clays and other soils
. ^.r^r^T^r
curves shoOT ccrr.spoad to the So-c7iled standard enaction '
-
iS., falaved- " » «"-: "«a« of about 13 It./cibic ^oc ::1 -
"^a="°" «" « '"
.ff active diffusiv-y by f
-------
TAHJ.IJ V-l
HANK-lNf; OP USC.S SOIL TYHI-S ACCOHDTNC TO I'ERPOttMANCIi OK COVKR FUNCTION
- *""» *«•- ''^'"'«-.-^"U^^^^^^
U»ll KiuJtJ »mvo|M, Kl.vtl u.m.1 t f K f .. „
• ImuivM. litilu o,- „., nuft *• K t U r
I'ourly ni.i,l.,J gr.ivuU. _(uvvl- ' f r t „
• Hill! KlUlmeu. |||| III U| „„ 'BK t |T j.
f I nil*
Silly .muni*, (riivul- vi,,,j .id
A! m in p.
i;i;
su
SI'
Sll
si:
HI.
ml H| mttH
Wu|| ui.i.l.-.l ua.iJ.,
.un.lo. lln U in nu
1'iiiiily uruilfil .1111. In
u.xiilN. 1 In In (,r ,,u
rluytiy «UM«|MV NUIIIJ
UllllllM aill^L 1 l.tla*
y i.
HI'Hvully j;
1 Inuu
, «l»vclly l
1 limn
• III •IklllM.U |i-f
i; F
F
f e
!•' G
r F
r. f
i-l.iyfy fliiu nuiiili4t ^i I'luyiiw
Ulllu Ullll Hll|)j|UI I. ll^
«.'!. liliiiKiinli: ••!.,>• ,i| |,,u 4., Bej|u
(.Li.,! li:lly. (ilnvtlly Ll.iy.,.
u.iii.ly i-luya, .Illy t|jy,j, |,.ai,
i:l.iyu
i l.tyu ul |,iu |,I«.| Idly
Ml lil»iB.tnlc ulllu. nli.-ni-v»im ui
n.il In, i-ljj| Ic villa
t'll lii.iiK.iuli: tl.iy. ul |,|K|, ^
|>l.iul Ully. (.I cl*yu r I K F r F F
• ft Hi d ,1111 c il.iy. „) i»..,||.,« !„ (,,„(, r
|ll.l:illl.l|y. U1|1.,.,U .Hill " - - F F
ft l'«.il uuJ oiliur hiulily .ii,;,i,,l,: ,.
ttUlIu ~"~U--
H«yY•-r=-.,,c.:iiJ,l,-i -irvii,.u.ii FV7,i,; ,.%^,r
Source: Kl'A, 1«J'/«J.
1
$
k
-------
"""'"'''''* >'']>"^'i f-i v'.i'.-ouj; "
3 a
Source: Arthur D. Licrle, Inc., 1
.cm
-CQQ1
•3 .4
rracnon Water {w/o,.j
«'
V., RELATIVE O.FFUS1VITY.NSO.L COVERS
-------
rjK»-#)*>* *>*!••*?";
TABLE V-2
RELATIVE DIFFUSIVIT?1 AS A FUNCTION OF SOU PQRQSTI
Water
Coatant(w)
Total Porosity (s )
Relative
Water Fraction
0.3
0.4
0.5
0.6
0.7
0.8
(1
6
11
13
25
31
37
43.
•b/fO
0
.24
.5
.7
.0
.6
.4
.7
(w/P )
0
0
0
0
0
o,
' 0,
w
0
.1
.2
.3
.4
.5
.6
.7
.20
.052
.005
0
-
-
.29
.11
.029
.0029
0
-
.40
.19
.072
.019
.0019
0
^
.51
.23
.14
.052
.014
.0012
0
"~
.62
.37
.20
.096
.037
.0096
.00095
0
.74
.48
.28
.16
.073
.023
.0072
.0007:
1.
D ..
err
D .
air
(e) 10/3
and £
v
Source: Arthur D. Little,
Inc.
-------
130
SO
3 '° '3 20 2S
MOISTURE CONTENT, PERCENT OF DRY a
IGHT
FIGURE V-2 EXAHPLE STANDARD COMPACTION
FOR VARIOUS SOIL TYPES
Source: U.S. Envi^encal Proceed Agency, 1979
-------
decreases demonstrates the need to prevent drying out. Very large
relative increases in diffusivity occur as the moisture content begins
to fall much below the optimum point.
3.3 Final or Permanent Covers
When a working cell at a hazardous waste landfill has been filled
up to its capacity, that portion of the landfill is closed. Closing
involves the" installation of a cover or cap over the top of the
collected wastes to serve many purposes. These include the prevention
of infiltration of surface water, the reduction of gaseous emissions,
general site security, and others. The current regulations for
landfills focus on the problem of grcundwater protection and emphasize
infiltration control and leachata collection as a means to achieve
this objective. Fortunately, from an emissions point of view, this
objective also serves as an implicit gaseous emissions control.
Covers that are effective in reducing water infiltration are also
effective in reducing emissions. Both gas and liquid permeability of
permeat:
always be some residual level of emissions even when a synthetic
membrane cover has been installed. -- —
The installation of covers does not eliminate the generation cf_-
gases. Gas generation continues through the volatilization of organic"
wastes and in some settings through the generation of methane as a
product of anaerobic degradation. These gases will gradually build up
in the landfill and may, if sufficient pressure is generated, damage
the cover. At the same tine because of the increased pressure, the
gases will tend to diffuse laterally out of the landfill and
ultimately to the surface. Some sort of vent system is of tan
installed in conjunction with the cover in order to prevent either or
these two situations from arising.
The discussion above on temporary covers describes the basic
behavior of soils relative to permeability. In designing and
installing a permanent cover, thera is considerably more flexibility
than is possible in temporary covers. The economics permit a much
wider choice of materials and complexity of design. In particular,
layered designs are becoming quite commonplace. The designer can
incorporate favorable trafficability, water impermeability and gas
barrier properties are using different materials rather than suffering
the trade-offs intrinsic in the use of a single material. Figure 7-3
(EPA, 1979) illustrates the concept of layering. In even more complex
systems, synthetic membranes may be added in addition to the various
soil lavers.
7-14
-------
:::::::::::::::::::::: LOAM (FOR VEGETATION) :J:!ji|J:J::;H:jH::::
CLAY (BARRIER)
oooooooooooooooooo**--- ----^ii^ix7^;?r5"^°icaoooooaoo?c"oTo"oo"oP
OOOOOOOOOOOOOOOOOO ^-3Aiyt?\ ,****. — — TOOCOOOOOOOOOOOOOO
oooooooooooooooooo GRAVEL (GAS CHANNEL) 100000000000000000
OOOOOOOOOOOOOOOOOOww M OOOOOOOOOOOOOOOOO
CLAY (BARRI SR)
1
j SILT (FILTER)
!
1
I!
!
FIGURE V-3 TYPICAL LAY25ED COVER SYSTEMS
Source: U.S. Environmental Protection Agency, 1979
-------
The gas channel shown in the figure ±s installed for use with
some sort of vent system to control lateral gas migration. Several
technologies can be used:
o Trench vents. Trench vents are narrow trenches backfilled
with sand, gravel and/or stone. They are often lined on one
side and can be open to the atmosphere or capped with clay
and fitted with laterals and riser pipes vented to the
atmosphere. They can also be connected to a negative
pressure fan for forced withdrawal.
o Vertical barriers. Vertical barriers include slurry walls,
grout curtains, and synthetic liners.
o Forced wells. Forced wells for lateral migration control
are identical to those for vertical control, except that
they are placed around the perimeter of the sits and spaced
such that all gas is drawn to the wells before crossing the
site boundary.
o Injection trenches and wells. These are similar to forced
induction trenches and wells, except that a blower is used
to force air into the systen. This creates a pressure
gradient in the landfill, causing gas to flow away from the
system, and thereby preventing lateral migration across the
boundary.
In installations where the principal purpose of the gas control
system is to pravent damage to the cover, the vapors released directly
into the atmosphere. For emission control purposes, some sort or
treatment would be added.
4. In-3itu Controls
Sone of the controls considered are classed as ir.-situ controls.
5. Post-Treatment
Post-crsarment involves the collection of gaseous emissions from
the landfill and treatment of those emissions to remove or destroy the
volatile organic components. Such systems consist of the collection
means and the treatment means. Combinations of external covers and
treatment techniques such as carbon adsorption or incineration have
been discussed above in the chapter on Surface Impoundments. This
approach can be used on landfill operations in essentially the same
manner as that for surface impoundments. As previously discussed, air
inflated structures can be installed over closad or operating landfil"
sections covering the typical range of sizes from a fraction of "an
acre to as much as 5 or 6 acres. These types of structures can
include complicated vehicle air locks to permit access during the
operating phase. "**"
T* • £.
v-J.3
-------
The air introduced Co
conventional systems escapes bv n
in this application be exhausted
to the treatment system.
from the surface of the
e zn
arter passing through the treatment ^stel
rh
' < in
Che aacari^' *°uld
& '""* °f VentS ««i«cced
V3p°r raleasad
C°
as weu as
of a cover at che fflcos f P^ffipa reaS°n for the
Louisiana, is to keep precipitation out A 7 in LivinS^°n,
approach with comparable peSoSnc- vould f alteraative control
connected directly to gas ven"ts^ns^lT . • t • * Craat:aenc
exiting through the covlr. ForLd vents 1U?/ ^
drxving mechanism for introducing JsasJCa^ ^ C° pr°Vide
for achieving high collaccion ™ «° « tr.at»ent unit and
Effectiveness
!• Introduction
and
Rightly diffarent from that Ucd
landfills there is ™ ./1, 7
reference casef E^erT Wf'n Tas
emission rate through^ the covers
orders of magnitude. Therefore
reduction are arbitrary and [ daVand
reterence. Cost-effectiveness ^ t
cost per pound of emissionTr4oved
ace
the effectiveness
-chodology is
impoundments.
"
° C°V" but Che
°V8r Several
°U
on the choice
"' eMa±«d °n Cha
2-
Effectiveness
2.1 Covers
of
of
.
means to examine the effectiveness of
equation described above h7v«b..,,
relative effectiveness of di^ "
and Figure 7-4 present data
covers of different total
are expressed in te-ms of
ffnlt emissions are th? pounds
per pound Per cubic foot of
Diffusivit Wa8 assumed to be G
°n rhe ?
a
tv at
=°
SCa=S' Tabla 7-
C°mbinacioas of soil
WaCer co^ents.
12~*«*
Cnn, , aaisslons P«r square foot
? 1011 ^ Che b°tt0n sida'
-dfill operations
and
-------
TABLE 7-3
UNIT EMISSIONS1*2 THROUGH 12-INCH SOIL COVERS
FOR SOILS OF DIFFERENT DRY POROSITY
Unic Emission (ft/hr)
7. Water'
0
5
10
15
20
25
Z Moisture at Zero
Porosit^
Dry Porosity (Bulk density)4
0.3(113)
.056
.016
.0020
.0000032
-
-
15.3
0.4(101)
.083
.039
.015
.0036
.00033
-
24.7
0,5(84)
.111
.069
.039
.020
.0084
.0027
37.1
0.6(57)
.142
.10
.073
.050
.032
.020
55.3
Cnits are
Ib / Ib or ft/hr;
a-3
rt -cir
0
AC
2. Diffusivity in air - 0.23 ftVhr; t = 1 ft;
3. Percent of dry veighc
4. Bulk density (lb/ft3) in she-parentheses, based on
density * 2.7
Source: Arthur D. Little, Inc.
T7-TS
-------
a .07
.001
.0001
Source: Arthur D. Liet^ Tnc
| , — *" J .ki-iV. • ,
10
'5 20
i Water (% of dry weignt)
FiGURE V-4 UNIT
A LANDFILL
-------
proportional to cover thickness. For a 5 inch cover, the data shown
in Che table and figure should be multiplied by 2. Conversely, for a
24-inch cover, these data should be divided by 2.
rn -LiSpir% 7~t Sh°.7 Che ««-«« sensitivity of emissions to
conditions in the soil. For a given soil type compacted to a given
porosity, the emission rate can vary over several orders of magnitude
depending on the percent of water. In the steeper part of the curves,
a change in only a few percentage points in water content can make a
substantial change in emission rates.
The reduction in emissions along any one of the curves in Figure
V-4 is due to the displacement of air filled voids in the soil bv
water. At some point, the pores will become completely Billed v< -h
water and the emissions will become essentially zero. ' The moistur-
content corresponding to pore saturation is indicated at the bottom of
Table V-3. Under saturated conditions, organic compounds can diffuse
througn the water in the pores. The rate of this process is very slow
compared^to the rate through air and has been assumed to be
The extreme sensitivity to conditions illustrated in the cu—es
indicates the critical significance of choice of cover mater-'al
compaction practices, and moisture control in achieving high levels' of
emissions control when using soil covers. In most cases, the choice
or daily cover materials is made on economic grounds with the result
that materials excavated from the site or available from nearbv
sources are generally used. It may be fortuitous that these mat — ^'s
have properties desirable from an emissions control point of view * T*
not, the properties can be altered to provide lower poros—v ar~d
cugner moisture retaining properties by arising in relaeivelv 'soa**T
amounts of clay or clay materials. ~ *"
Hoistura control is perhaps the most important -'ac— -'n
emissions reduction. Hut little attention is gene-a^v — *»-- ~-\
moisture control. Cover ratarials are often piled u= unco-e-°--' Ta T_
inactive portion of the sita. The moistura content, unde- ".--"s
practice, depends on the recent weather patterns. To oi-m~~a
emissions, daily cover materials should be as w«t as possible ra-Iciv^
to the maintenance of mechanical properties appropriate to workab^li-v
and structural integrity. --L-L-<
Soil, synthetic membrane, or combinations of the two can be used
for_ permanent covers. As is the case for soil materials, there are
r"l availac.a ror vapor permeation through synthetic mamfar-nes
or t..e type anc conriguration used as covers or liners. Table 7-4
presents data recently reported on permeation rates for a var-'^-r 0-
;J?ar";al? \°r S2vVaral differeac "Sanic chemicals. The data shown in
this taole have been converted into the same units used to dist>iav the
soil cover characteristics above. Permeation ratas f-hraizh" aU
polymeric materials is highly dependent on the chemical nature"of eh-
duzusinz compounc. Polar compounds such as acetone genial'y be^ava
-------
TABLE V-4
Xylene
Acetone
Chloroform
TEFLON1 - 4 MTT.S
0.011
0.00028
0.0071
Xylene
Acetone
Chloroform
0.000008
0.00063
0.0027
Units are
rt -hr
-------
quite dirrerently from hydrocarbons such as xylene or chlorinated
hydrocarbons such as chloroform. In the 30 mil polyethylene membrane
the permeation rate of xylene is about 50 times that of acetone, but
in a 4 mil Teflon membrane, the ratio is reversed. Acetone passes
througr. the Teflon membrane at about 100 times more raoidlv than
rylene, but Terlon remains more effective in absolute terms.'
It is important to note that the magnitude of these
permeabilities fall within the range obtainable with soi^ covers
Four points have been indicated on the Figure 7-4 above to represent
typical temporary and permanent soil cover conditions and 2 membranes.
Points A and B respectively are located at points corresponding to
conditions that might be expected in a temporary soil cover and at a
permanent cover. Point C and D represent the permeability of a
neoprene and a higher performance material such as Teflon
respectively. The synthetic materials which are often characterized
as impermeaole are in theory of the same order of effectiveness as
properly designed and maintained soil covers. And, if water content
is maintained at the saturation point, soil covers can theor-tica^y
reduce emissions essentially to zero (neglecting liquid phase
diffusion), a level unattainable with the polymeric materials commonlv
used in today's practice.
Composite membranes including a layer of Mylar, a uolyester
polymeric material, can achieve vapor permeation rates that are
efrectively unmeasurafale. These materials have been used in
developmental applications in food containers and in suec-'al
protective fabrics. (Personal communication, A. Schwope). Laminates
in forms suitable for field application as permanent cover mat*-als
are presently unavailable.
As components of permanent covers, synthetic memb-*nes ha**e
several advantages relative to soils. Once' insta^d, -he"- i-e"uJ-»
little maintenance to maintain their efficacy. Performance over 'Non-
periods or time is, however, uncertain. The materials may deface an'
It Cms occurs, would have to be replaced. In practice, c-ac;ci-^ and
nonhomogeneicies in the materials could si-if icantlv raeac-' cb«
er.ectiveness relative to the design values. Small fissu—s <*. a
cover would act as conduits for the vapors generated within a ~ar»-
area of the landfill in the vicinity of the crack. Car-ul
maintenance or _the cover including vegetation to prevent erosion, and
installation or sprinklers to maintain moisture content at uniform
Bevels wiil reduce the probability of the formation of cracks. The
roots of plants must be prevented from penetrating the gas barrier.
Maintaining appropriate moisture levels is, however, inconsistent
with groundwatar protection objectives at a landfill. Downward
infiltration of water and prevention of leachata fo-mat-'on is a
primary objective for covers from this point of view. Combinations of
a soil cover and membrane can be designed to achieve both sets o-
oojectives.
-------
finite emission rate Tables
7ear through an acre of surface
systems depicted as points A B
Emissions are given for a '
landfill. The table ind/cates
in plica. considerable loss of
occur. Volatile solvents such as
as
vapor pressures of the order of 100
conditions. Such comnounds if nrp.l , P
could be emitted in Grange of 'several met
of quite low permeability' X^S?-
suitable cover material (E^A 197?^, %
order of magnitude greater!
W±11 exhibic
^ancit7 of emissions oer
to the four cover
Figura V~L afa°ve.
V*P" concenc^tions in the
""* h±Sh Performance covers
0?r°rb *™SS
&
per million at ambient
«*il«t.d form
«"idered a
emissio*s of about an
organics at present.
of cover systems
of the
of volatile
2.2 Post -Treatment
leve l eu
ultimately entering the atmosphere
permeability, emissions w^ll conrn,
all the materials in the landfill h
For very effective covers t?ett
hundreds of years. Post-tr a Lent
"tlt* of missions
is SOme finica
ataosPhe^ oncll
into che atmosphere.
atmosphere, abov^ the landfall
discussed above, the syst^ e"
systems employing extarra' s
configuration plus adsor^t" on
control means can be use" The
collection system. The treatment
efficient asca
-landfil- or from Che
vapors and
C"CU" =he Sasas- 2i=^«
°r °Cher =aseous
o primari^ °* the
ion can achieve high levels of
.
.«
induction
sicuaclon.. I
crunches) and Injection
limited, tn. integrity
.ff.cei
"
° e;-va many
ars , <^l»ding lin.d
oo<1' but:
-------
TABLE V-5
ANNUAL EMISSIONS
Emissions (Ib/year-aeral
Vapor Concentration
(ppnrv)
10
50
100
500
1000
5000
10000
50000
100000
Daily Cover
A
42
210
420
2100
4200
21000
42000
210000
420000
Final
Cover
B
1.0
5.3
10.5
53
105
530
1050
5300
10500
Neoprene
Caa
C
10.5
53
105
530
1050
5300
10500
53000
105000
Laminate
Can
D
0.1
.53
1.05
5.3
10.5
53
105
530
1050
Notas:
I. A, 3, C, D refer t
o points on Figure 7-i
Source: Arthur D. Little, Inc.
-------
the tlo^^ Sh-ld -tend Co bedrock
s^^^^^t
control strategy ° * lad««i«» wells may be the
3. Costs
3.1 Pretreataient
were used. Pretreat^ent CO8Cs take^ f ^ *"**« n^ents
the range of $1.00 per po^d ^QQQ^J9^7 ee al" C1984) are in
incomxng waste stream. Cost of other con? ? W3Ste rem°Ved "°° «n
of pre-trwtMnt costs to reflect va-fr *? C°mpared Co a "nge
P-pert.es, treatment type, s±z^d^~ «. strj,
3.2 Design and Operating Practice
Installed cover system
• 1979). Membrane cover ^ayer^1™3^/ ara shown in Table V-6.
s. Costs depend on aiany site suacf^!. * timeS as exP«nsive
De Onnei J«—_j •, -^ -s-^'-c SpSCinp rar-f-/^-^^ m»_ . . _
ticular sica
'
ra ma_
passes were performed v^ - acaxeve higher comnaction -- exr-I
3.3 In-Situ Controls
3-4 Post-Traataent
-------
TA3L2 V-5
ESTIMATED UNIT COSTS FOR SOi-E COVER LAYERS
Layer Trae and ^^v—ss -nstallad Cosl
• —~" ^s dollars/'.-c2
Loose soil (2 ft)
Compacted soil (2 ft)
0. /O
Cement concrete (li -'r.)
9.00
Asphalt ccr.cra-a (I in.) _ .. _ _
2.jO-3.pO
Soil-csnant (T in.) , _^
i.jO
Soil-asrhalt
1. 50
Polyethylene nenbrane (10 ail)r l Q0_, ..
Polyviayl chlorida ae-brane (20 ail) 1.^0-2.00
Cilcrinatad ?ol"a-ir/lana =anbrana (20-20 ail) . , KO_- ^
Hi'palon aecbrane (20 ail) _ _p
ZTecprane aeabraae ^
Zthylene prop'/lsr.a rubber aeabrana -_-.-,
2.TG-J.>u
3u-yl rubber asabraa- ^ » -
2.iQ-3.30
Paring asphal- (2 in.) 1.20-1.-?
Sprayed asphal- nanbrana (lA in.) and soil ccvar
P.einfcrcad asphal- aeabraae (ICO ail) and scil cover 1.50-2.00
2e=tcni-3 layer (2 i«.) . ,
-.-"••j
~ Hot rasczsiandad becaus
Sourca: U.S. Eavironmaatal Protacriou Agancy, 1979
V-2S
-------
TABLE V-7
0.4 Acre
Air-Supported System
Pipe Vents
Compacted Soil Cover
20-JtLl Hypalou Cover
6 Acre
c»tta
$150,000
80,000
2,000
6,500
AnnualizecP
$24,000
12,000
500
1,500
Cauital
$1,600,000 .
403,000
28,000
96,000
Annualiz
$250,000
60,000
5,000
15,000
Nota: 1.
2.
3.
Treatment costs must be added to the f±surM 3hown. •
Cost in 1982 dollars.
and typical O&M costs
Source: Arthur D. Little, Inc.
-------
Costs for a post-treatment system based on collection by Beans of
vents coupled to carbon adsorption or incineration are also shown in
Table 7-7. The costs ara based on a pipe vent system. Pipe vents
include the blowers required to drive a control system. Passive
trench vent systems might be used in situations where cover protection
is the only function of the gas control. Pipe vents appear better
suited for post-treatment applications. The costs presented do not
include the cover.
4. Cost-Effectiveness
As noted in the introductory paragraph to this section, de-
finitions of an uncontrolled, reference landfill is rather arbitrary
since covers are required by regulations, but vary widely in per-
formance. Thus, it is not meaningful to compare cover performance Co
other operating controls on the basis of pounds of volatiles removed.
Notwithstanding that analytic problem, operating practices
involving covers may be extremely cost-affective, that is, providing
significant emissions reduction for little incremental cost. The
earlier discussion describing emission rata as a function of cover
properties indicates that several orders of magnitude or more
improvement in performance may be attainable with careful practice.
The costs to achieve this performance can be quite low. Moisture
control of daily cover and grain size modifications by adding soil
conditioners, clays, etc., ara not expensive relative to the basic
operating costs at a landfill. Under these circumstances, the
cost-effectiveness would be high, compared to pratreatment, for
example, expressed as pounds of volatile reduction per dollar. Even
the added cost of heavier earth-moving equipment to achieve dansar
compaction should not change the cost-effectiveness very much.
The use of permeability reducing techniques for permanent covers
should be similarly ccst-effactiva comparad to conventional design
approaches. Lew vapor permeability soil and synthetic membrane covers
do not raprasant significant incremental costs. Design requirements
for covers ara established currantly by regulations designed to raduca
or prevent surfaca watar infiltration. Incremental costs to maximize
gas control performance ara small.
Combination covers appear most effective. Although permeability
in soil covers can, in theory, be reduced to zero, it would be
extremely difficult to achieve perfect performanca in practice.
Imperfections in soil covers, particularly in large cells, ara mora or
less inevitable. Maintaining high moistura content runs counter to
control of watar infiltration. Adding a synthetic membrane could
offset these practical difficulties without significant incremental
costs. The cover would prevent watar infiltration from penetrating
into the closed call, and would act as a seal to inhibit permeation
through cracks in the soil layer.
7-23
-------
Even as performance approaches the theoretical Unit, the-e are
two Actors which suggest the potential applications of" alternative
controls. rirst, as noted, practical performance mav not reach
theoretical levels. There are no data currently available to estate
the departure from theoretical performance. Second, covers only
retard the loss or materials from the landfill. Little decav occurl
in hazaraous vaste landfills so that, with any finite permeabilitv
wastes wzll continue to enter the atmosphere. The applications"of
pre- or post-treatment can remove volatiles permanently. "
ehev !r f K costs are less than post-treatment for landfills as
they are for other kinds of disposal facilities. Thus, unless there
is some technical reason that pretreatment would not be practical
post-treatment would not be the cost-effective choice. Pretreatment
s are expected to be less than five dollars per oound of waste
removed (1-2 dollars/per pound have been used in comparison, above)?
Post-treatment costs are expected to exceed about five dollars per
pound removed plus the costs of the collector (cover or vent system"
Thus, pretreatment would always be preferred. Covers serve more than
one purpose; keeping out rain as well as keeping in volatiles. If the
covf,"11 ?,e all°Catad to SOTeral Proses, post-treatment, using
covers, would appear mora cost-effective. - - °
E. Summary
Cover design and maintenance present the most cost-effac^ve and
InS?!!* ^ °r emissi°n "Auction Potential of all the controls.
In theory, emissions can be reduced to essentially zero bv maintain*
the nores ot a «urf 1 rmra-,- f,,tT ~* „ .. . • UittiUl-<:1-u-n-s
4,
|
j organic vapors.
Combination cover systems with both soil layers and
lnf^-4^'^ Va^ 'f*h ?«fo»«« 1—13 'for both vapor' a
water inf.ltratxon control. Combinations can offse- ,-ac-'-l
limitations in soil covers due to cracks and inhomcgeneities. " " ~~^~
Very little data are available that characterize currant sracfce
at operating landfills or at closed, previouslv active sites The""
is, even in this situation, a reasonable ejection chat oast and
current practices are poor with respect to vaoor control, and 'so eh"-
scale nC1S" °P?°rtrait^ Co "du« '»Por 'emissions on a Stional
11fflir the potential for emissions, but nay have
f^^1^1011- C1 ChS hiShl? v«i*bl. wastes that are nlaced i"
landfills. Much or the wastes may come from widely disused sma^
generators. These conditions limit the practicality 'of Dret~4acmSt~~
-------
Post-treatment systems have not been used at landfills, but the
recent installation of an air inflated structure at a landfill in
Louisiana indicates that this approach can be applied. The critical
element in a post-treatment system is the collectors means. Treatment
technology is proven but expensive. The covering structure includes
air locks to permit vehicle access and prevents rainfall from falling
on the site.
F. References
EPA, 1979, Design and Construction of Covers for Solid Waste Landfills
(Prepared by R.J. Lutton, et al.). S. Report No. EPA-600/2-79-165.
Farmer, W.J. at al., 1978, Land Disposal of Hazardous Pastes:
Controlling Vapor Movement in Soils, in Proceedings of 4ch Annual EPA
Research Symposium. EPA Report No. EPA-60019-78-015.
Haxo, H. et al., 1984, Permeability of Polymeric Membrane Lining
Materials, Proceedings, International Conference on Gecmembranes,
Denver, CO.
Hwang, S.T., 1982, Toxic Emissions from Land Disposal Facilities.
Envir. Progr., Vol. 1, No. 1 (Feb. 1982).
Schwope, A., July 1984, Arthur D. Little, Inc., Cambridge, MA.
Personal Communications.
Spivey, J.J., C.C. Allen, D.A. Green, J.P. Wood, and R.L. Stailings,
1984. Preliminary Assessment of Eazardous .Waste Pretraatment as an
Air Pollution Control Technique. Draft Final Report. Research
Triangle Institute, Research Triangle Park, NC. " For the U.S.
Environmental Protaction Agency, IF.RL, Cincinnati, OH.
Weiser, H.3., 1949, Colloid Chamistr-r, John Wiley and Sons, New York.
V-30
-------
VI. LAND TREATMENT FACILITIES
A. Description
(Spivey ec al
.
approximately 12 acres
™
« each
= "
The wastes aay be anoiiad to the soil *m--a,-a -•
-'aues -^a ^t,^,-,- '" - i. soix aur^ace xr.
'ch.^^^
aost Import
rT. The four «jor
-------
o Overland Flow - wastewatar is caused to flow over relatively
Impermeable soil with a slope from about 2 to 82. This
technique is used for treating contaminated run-off or
wastewatar errluents from industrial processes.
Following the application of wastes to the soil, the wastes inav
be incorporated into the top layer of soil by standard cultivation
techniques. The soil may be tilled several times following a single
application of wasta before the next application. Typically, the
wastes are tilled into the top 4 to 8 inches (10 to 20 cm) of soil.
_ In some settings the sita is revegetatad. In this case, the
surraca is not tilled after each application. This technique is
commonly used to treat dilute wastes which can be anolied bv soray
application. ""
3. Emission Sources and Models
1. General
Emissions to the atmosphere at a land treatment facility ar^se
from two primary sources. The first is pools of liquid wastes which
form a,ter application on the surface. These pools remain until the
liquids see? into the underlying soils or are incorporated bv t«U'-*
Volatilization directly into the atmosphere can occur as long 7s "the
liquid wastes are exposed at the surface.
The second source is wastes which have been incorporated into the
soil. Volatile constituents in the wastes can ent=-"tbe int—st-'c««
ana eventually diffuse to the soil surface. At the sur^ce "the
emissions ais into the atmosphere and are swept away from the site.
2. Emission Models
2.1 Surfaca Emissions
Emissions from a surfaca layer of liquids behave in the sa-e
general manner as emissions from a floating layer of organic compounds
on a sur.ace impoundment. For pure or highly concentrated organic
mixes, the tollowing equation describes the emission rate:
Ak C
S
where Q - emission rata (Ib/hr)
A » surfaca- area (ft*")
kg * aass c=snsfar coefficient (ft/hr)
71-2
-------
vapor concancracions of diffusing., component
in equilibrium with liquid, ib/ft
and k
g
k RT
where
mass transfer coefficient (lb-mol/ft2 hr)
gas constant (ata-ftJ/lb-mol - °R)
temperature (°R)
total pressure (atm)
approprUt
•"« Wllcitlon of
"' Xt "
™ 5
2.2 Emissions from Incorporated Wastes
species, is:
he ith contaminant
Q - AD ..
err
where: 0
C ) X
flux race (Ib/ft2-hr)
Deff
of air filled pore space
air
air * aolfcular diffusivity of i in air
(tt /hr)
-------
t
A
total porosity
tortuosity factor (T s 4)
depth of surface injection (ft)
time after application Chr)
surface area of application (ft )
depth of penetration of plow slice (ft)
initial mass of component i (Ib)
concentration cz i on gas side o
interface (lb/ftJ)
This model is appropriate once the waste has been incorporated
into the soil. It assumes:
o The soil column is isothermal
o No capilliary action
o No adsorption on soil particles
o No biochemical degradation
This rather complex equation becomes much simpler under two
separate assumptions. The first assumption is that the waste is
placed on the surface and immediately tilled. In this case, h equals
zero. This equation, rearranged in terms of emissions per unit area
is:
wnere:
f
G D .. (H ,„'
2 err o/A
Deff/
2 h t
P
2t D .. h
err o
J
YMO/A'
As long as the assumption of no biodegradation is valid, i.e.,
for a short time following applications, the Thibodeau-Hwang equation
indicates that emissions would decrease proportional to the square
root of time expired after application. Once biodegradation becomes
important, so that vapor concentration, Cg, decreases wiih time, the
relationship becomes sore complex. Emission rate would decrease more
rapidly than the inverse square root form indicates. The esact form
deuends on the aature of the behavior of concentration with time.
•
-------
SSSSakfca^^^^tg^^^'SJ^ngSS^ i-
,r * si?Plif?i:iS ^sumption is that the wastes are injected
at a depth equal to the depth of penetration of the ?low or
C ho «" Che equation 'becomes
JL
A
Similarly in this case, the emission rate would remain constant
the rariCtr HChea, W°Uld ^"^ ^"^ C° £he functional "orm of
the relationship between concentrations and time.
3. Controlling Parameters
3.1 Liquid Pools
a liaidnnnl pa"meter thac "n *• controlled as long as
Jj,qrt V °VS Present' To m^i°i" volatile emission, the time
that the liquid are exposed should be kept as short as possible.
3.2 Incorporated Wastes
m™h^miS/i0nS' °nCa ChS WaStaS have been incorporated, depend on a
number of parameters. In all cases, emissions depend in different
For th0^ °raS °U the C0nceac^tion of the component in th. ££?
For the case vnera wastes are injected at the same deoth as the olow
cut the initial emissions depends additionally only on the ef-ec-ive
diffusivity and depth of injection. The deener the injection ch^
lower vouxa be the emission rate. The rate defends direct on
errective diriusivity. Diffusivity in the form devoid bv
Thioodeaux and reported by Hwang (1982) is related to the oorositv of
or fandf-- ^ C°r"°si="k fac="' ^rosity as in the case of covers
on eif ?endS °n Cha dSgras =° Which ch« sci- is compacted and
controllaole parameter for land treatment.
rfM^F°r- Surfa? in^ecc:Lons' tlie initial emission rate defends on the
depth or the plow cut, waste application rate, and time (.nt'StW)
S arfaCriVe < concentration (implicit' function
ly with the square root of time
In this configuration the rate depends
rather chan che *
inve^selv r
-------
The total emissions for a fixed area over a period of cine, say a
year, depend on the number of applications. A given quantity of waste
can be applied as fewer and larger portions or more and smaller
portions. The total emissions over the period will depend on Che
number of applications. The forn of the exact dependence requires
that the rate equations above be integrated. The integration cannot
be carried out analytically, without an explicit form of the
relationship between concentrations and time, which depends on the
nature of the biodegradacion process and on its coupling to the
diffusive mechanism. This relationship is complex and poorly
understood at present.
The equations were integrated for several possible forms for Cg
as a function of time to determine the general shape of the dependency
on application rate. The results indicate chat cotal emissions
increase with increasing frequency of applications; thus, to control
emissions for a fixed quantity of wastes applied over an intended
period, the maximum quantity consistent vith the bicdegradative
behavior should be applied each time.
C. Controls
1. Introduction
Emissions from land treatment can be reduced by removal of
volatile components of wastes prior to application. Pretreatment will
have the same effectiveness for this type of facility as those
discussed previously. Post-treatment techniques involving collection
systems in conjunction with a treatment process can also be applied.
The equations indicate chat the rate of emission is quits sensitive to
a number of che operating design parameters. There ara, as a resulc,
several control methods chat involve design and operating practises.
There ara no available control approaches considered as in-situ
methods for this type of facility.
2. Pretreatment
Pratraat^aent may not be appropriate or effective for land
treatment. If the biodegradation processes chat occur in the soil
produce volatile compounds from the breakdown of heavier molecules,
then pretreatment will not be so effective. Pretreatment may be more
an alternative to land treatment not an adjunct, since both are
designed to handle the same kind of organics.
3. Operating Practices
Volatile emission rate can be controlled through the means by
which the wastes are injected and by adjusting the amount applied per
unit area per pass. Subsurface injection is considerably more
effective in controlling emissions than is surfaca injection
immediately followed by tilling. Wastes should be injected at che
-------
maximum depth consistent with the parameters determine the waste
degradation rates Typical common depths of application range from 4
to 8 incnes (10-20 cm) below the soil surface hooding and Shipp,
19/9). A variety of types of equipment have been developed for
subsurface injection (EPA, 1983, Overcash and Pal, 1979). In some of
these Devices, the waste is simultaneously injected below the surface
and mixed into the top 6 to 10 inches (15 to 25 cm) of soil. The
initial injection may be followed closely by a second pass with 'a.
cultivator to distribute the waste uniformly across the treatment
area. Monographs discussing land treatment recommend subsurface
injection for wastes with volatile components and odorous
constituents. Subsurface injection minimizes exposure of the
operators during application.
Emission rate is a weak function of the application rate per unit
area. For economic reasons, land treatment facility operators apply
^J^^ WSfCe Per Un±t area "Distent "it* the degradation
capabilities and carrying or assimilative capacity of the soils In
practice, application rates often exceed' values recommended in
conventional Design and guidance sources. Emissions increase when the
design capacity is overloaded because degradation will be impeded and
the volatile materials remain in the soil for longer periods* of time.
Typical application rates range from about one-half a pound per square
foot to aoout three times that rate. (EPA, 1983)
th "JTi? ^l11^ S0il P°rosi^ is Probably not controllable but
on ri -- t0 PreV6nt excassive drying. If the soil becomes
too dry the errective diffusivity can increase by several orders of
Sf1^';- C K" ^^ discussio* of l««ills for 'the particulars of
the relationship between diffusivity and soil porosity) So'l
moisture content should be maintained at the maximum level consistent
w..h the parameters controlling degradation in order to keen
atmospneric emissions to a minimum. ?
-unu.0i Ove.
T7T-7
-------
D. Effectiveness
1. Introduction
The effectiveness of controls at land treatment focusses on
tilling practices. Prettraatment and post-traatment perform essen-
tially the sane as described in the preceding sections. Emissions are
referred to surface applications as the uncontrolled case.
2. Emissions Reduction and Effectiveness
Figure VI-1 indicates the percent of volatiles applied in land
treatment thac would be lost to the atmosphere through volatilization.
These curves are based on the equations developed above. The emission
loss relationships and the data generated using them assume no
biological degradation. This assumption is obviously unrealistic.
The main function of land treatment for organic compounds is to
provide degradation. The actual emissions and percentage lost to the
atmosphere will be less than that depicted herein for this reason.
Nevertheless, the equations and the data are useful in describing the
relative effectiveness of a variety of alternate controls. The
results shown in Figure VI-1 are consistent vith data taken in the
fiald. (Hinear et al., 1981). As reported in this reference, oil
wastas spread and tilled into soil resulted in losses of 0.62 and 27,
in tvo separate field tests (Francke and. Clarke, 197£, and Suntech,
undated). In another'tast reported in this sane reference, 11* of the
wastas from an API separator were lost to the atmosphere (Suntech,
undated). In this last test the wastes were spread on the surface but
not tilled into the soil. Vapor concentration over the types of
wastes treatad wera not raported. Based on the types of hydrocarbons
generally prasent in the wastes treatad, the vapor concentration can
be estimated. A value of around 1,000 pom appears reasonable.
The same kind of data ara shown in a somewhat different format in
Table VI-1. la this table the quantity of volatile lasses per acra
per year is shown for compounds of incraasir.g vapor pressure.
Comparison of the columns for surfaca injection versus chose for
subsurface injection illustrate the reduction that is theoretically
possible. Figure VI-2 illustrates the raduction efficiency diractly.
The potential reductions shown in Tabla VI-1 and Figure VI-2 may noc
be achieved in practice, if the rate of biodegradation is reduced
sufficiently by subsurface injection. Stated alternatively, if the
rate of degradation is slowed down, then there is more time and more
unreactad materials available for volatilization. The efficiency
depends on the relative volatility of the constituent. Efficiency for
low volatility compounds is quite high exceeding 902 for constituents
with vapor concentrations below about 1,000 ppo. The efficiency falls
off for the more volatile compounds. For reference, the vapor
concentration in equilibrium with benzene at normal temperatures is
about 100,000 ppm. The corresponding equilibrium concentration for
sylane is about 10,000 ppm. The overall effectiveness will depend on
the particular -?!•? of comnounds in the waste..
VI-3
-------
r »
too
1
100
Vapor Concimlrutlon Ippmv)
1.000
Source: Arthur 1). Uttle, Inc., J9»/,
FIGURE VI-1 ARGENT OF VOLATILES LOST TO ATMOSPHERE
10.000
-------
TABLE VI-l
ANNUAL LQSSZS FROM I ACRE OF LAND TREATMENT1
Injection (h*) and Plow Depth (h )
s p
Equilibrium
Vapor Concentration
(PPMV)3
10
50
100
500
1000
5000
10000
50000
100000
h
h - 4"
P
4.8
10.7
15.2
34
43
107
152
2872
2872
- 0
3"
3.4
7.6
10.7
24
34
76'
107
246
2S72
h
4"
.1
.2
.4
2
4
20
40
200
TO-?2
- h
P
8"
.05
.1
.2
1
2
10
20
100
200
Notes:
Units ara aetric tons per year; 2S7 aetric tons applied per year
2
Complete (LOOS) loss
^ Parts per ailiion by voiuae
Source: Arthur D. Little, Inc.
VI-10
-------
MOID;
12Cyi.lus/Yr
Application lldlo
100
1,000
Vapor Concuriiiiilion (p|>mv)
10,000
J 1 Mill.]
100.000
Source: Arthur 1). Uttlc, Inc., l'J«4
F.GURE VI-2 REOUCT.ON EFFICIENCY FOR SUBSURFACE INJECTION RELATIVE TO SURFACE INJECTION
-------
3. Costs
3.1 Pretreatment
PretTeatmen' c°scs «a "snmed, as above to be of the order of
$1-2 per pound ($2,200-$4,400/Mg) of wastes recovered.
3.2 Operating Practices
The more effective subsurface injection technique is oulv
incrementally more expensive than surface application. The addition
« nSfr CJ °? equlpme:15 Co a tank crx:ck spreader adds about 7% (about
'° I C?/?e CfSC °r Che syacaa ^ercash and Pal, 1979). The labor
cost should be about the same for either applications technique.
_ application rates according, to the Thibodeau-c
up, woulc reduce emissions. This control would be costly as
the land required to treat a given quantity of waste would inc-ase
proportional to the decrease in application rate. The added "cost
depends on the cost of land.
3.3 Post-Treatment
Post-treatment using an air-supported cover in combination with
ca.faon adsorption or incineration costs the same as these systems
described in the previous chapters.
4. Cost Effectiveness
Based on the model used herein, subsurface inject"'on is ^e m0st
cost-errective emission control for land treatment facilities
^resucted ernciency or reduction ranges from about 20-40% for h^hi-
volatile components to better than 95% for low vanor p« ssu-'=>
constituents. The cost-effective curves, if plotted on the same t-^e
or rigure usec in the discussion of surface impoundments and -anks
would ^raij. below pretreatment at about 100 pounds per year, a fj
-------
_ In such a case, post-treatment using air-inflated structures plus
incineration or adsorption would be the choice. If adsorption is
used, the recovered wastes can be reapplied. In this mode, per-
formance would be similar to that of the system described earlier
where recovered wastes are reinjected in the aerated imooundoent over
which the cover is installed.
E. References
(Prepared by K.W. Brown and
Francke, E.G. and F.E. Clark, Disposal of Oil waste bv Mi
110"' R±dSe Nati°nal Laboratory, Report No. VC-ll/Y-1934.
Hwang, S.T., 1982, Toxic Emissions from Land Disposal Fac^'ties
Envir. Progr.. Vol. 1, No. 1, (Feb. 1982). '
Minear, R.A. et al., 1981, Atmospheric Hydrocarbon Emissions from La-d
Treatment of Refiners on ffaggM. Am.^.M
Washington, D.C. Report No. DCN 81-219-060-06.
° an reataent or
Science Polishers, Inc., Ann Arbor,
' aiid R'L- ^tailings,
P.. Assassmenc of Hazardous Waste Pretraatment as an
PoLLucion Control T^±^T. Drart Final Report. - Research
.r.angle institute, Research Triangle Park, NC. For the U.S. Envl
ironmentax Protection Agency, IERL, Cincinnati, OH.
iry of Results from Toledo, Ohio. Re^ae-r
Tests, Suntech Environmental Group, Marcus Hookj ?A? undacad;
Vooding, H.S. and R.F. Shipp, 1979. Agricultural Use and Disposal of
Septic Tank Sludge. In Pennsylvania Znrormation and recommendat-ons
tor tarmers, septage haulers, municipal officials and ragulatorv
agencies. Pennsylvania State University Coop. Ext. Serv. Spec. Circ'.
-------
TECHNICAL REPORT DATA
(Please read Instructions on the rtvenc before completing)
1. REPORT NO. 2.
EPA-450/3-84-017
A. TITLE AND SUBTITLE
Evaluation of Emission Controls for Hazardous Waste
Treatment, Storage, and Disposal Facilities
7. AUTHOR(S)
John R. Ehrenfeld and Joo Hooi Ong
9. PERFORMING ORGANIZATION NAME AND AOCHESS
Arthur 0. Little, Inc.
Acorn Park
Cambridge, Massachusetts 02140
12 SPONSORING AGENCY NAME AND ADDRESS
U.S. Environmental Protection Agency
Office of Air Quality Planning and Standards
Emission Standards and Engineering Division
Research Triangle Park, North Carolina 27711
3. RECIPIENT'S ACCESSION NO.
S. REPORT OATE
November 1984
6. PERFORMING ORGANIZATION CODE
3. PERFORMING ORGANIZATION 3S?ORT NO.
10. PROGRAM ELEMENT NC. ,
11. CONTRACT, GRANT NO.
68-01-6160
13. TYPE OF REPORT AND PERIOD COVE^EC
14. SPONSORING AGENCY COCE
EPA/200/004
15. SUPPLEMENTARY NOTES
IS. A3STHAC1
The purpose of this report is to evaluate controls for volatile
emissions arising from the treatment, storage, and disposal of hazardous
wastes. For each principal type of hazardous waste management facility,
sources of atmospheric emissions are described and controls representing
different approaches, are examined and compared. The evaluation is based
on actual data and on theoretical models where data are lacking or where
the control technologies have been borrowed from other types of applica-
tions or are novel concepts. The information developed in preparing this
report is intended to support the analysis of the regulation and control
of these volatile emissions.
KEY WOROS AND DOCUMENT ANALYSIS
DESCRIPTORS
Ib.lOENTlFIERS/OPSN ENDED TERMS C. COSATI hlflu
Air Pollution
Pollution Control
Hazardous Waste TSDF
Volatile Organic Compounds (VOC)
Air Pollution Control
18. DISTRIBUTION STATEMENT ,. ,,^-^c
Release unlimited, Available rrom NnS
5285 Port Royal Road. Springfield, VA
22161
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EPA Form 2I2Q-1 (R*r. 4-77) PREVIOUS EDITION i i O sso LSTI
19. ScC'w'H
UNCLASSIFIED
164
20 SEC'JRIT^ CLASS {Tins
UNCLASSIFIED
12. PRICE
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