Document ID: EPA-HQ-RCRA-2002-0031-0038
Agency: epa
Document Type: Supporting & Related Material
Title: 
Posted Date: 2004-01-14T05:00Z

Appendix
U
Example
Cost
Calculation:
1999
Off­
site
Disposal
of
Emission
Control
Dust
(
K061)
Shifting
to
On­
site
Metals
Recovery
(
2001
$)
Pre­
Rule
Cost
CalculationPost­
Rule
Cost
Calculation
Cost
Inputs
Total
Quantity
of
Hazardous
Waste
Generated32,000
tons
hazardous
waste/
yrTotal
Quantity
of
Hazardous
Waste
Generated(
32,000
tons
hazardous
waste/
yr)
­
(
32,000
tons
recovered
waste/
yr)+
(
32,000
tons
recovered
waste/
yr*
0.32
fraction
as
residuals
*
0.95
fraction
characteristically
hazardous)
=
9,728
tons
hazardous
waste/
yr
(
recovered
waste
quantity
no
longer
hazardous
by
definition)
Generator
StatusIf
(
tons
hazardous
waste/
yr
>
13.2
tons/
yr)
then
LQGGenerator
StatusIf
(
tons
hazardous
waste/
yr
>
13.2
tons/
yr)
then
LQG
Quantity
of
Waste
Recovered
On
Site0
tons
recovered
waste/
yrQuantity
of
Waste
Recovered
On
Site32,000
tons
recovered
waste/
yr
Quantity
of
Waste
Disposed
Off
Site
(
Hazardous
Landfill)
32,000
tons
disposed
waste/
yrQuantity
of
Waste
Disposed
Off
Site
(
Hazardous
Landfill)
0
tons
disposed
waste/
yr
Estimated
Residual
Quantity*
32%
of
recovered
waste
quantity
will
be
residual
(
0.32)
*
(
0
tons
recovered
waste/
yr)
=
0
tons
residual/
yrEstimated
Residual
Quantity32%
of
recovered
waste
quantity
will
be
residual
(
0.32)
*
(
32,000
tons
recovered
waste/
yr)
=
10,240
tons
residual/
yr
Estimated
Hazardous
Residual
Quantity*
95%
residual
is
characteristically
hazardous;
(
0.95)
*
(
0
tons
residual/
yr)
=
0
tons
hazardous
residual/
yrEstimated
Hazardous
Residual
Quantity95%
residual
is
characteristically
hazardous;
(
0.95)
*
(
10,240
tons
residual/
yr)
=
9,728
tons
hazardous
residual/
yr
Estimated
Nonhazardous
Residual
Quantity*
5%
residual
is
nonhazardous;
(
0.05)
*
(
0
tons
residual/
yr)
=
0
tons
nonhazardous
residual/
yrEstimated
Non­
hazardous
Residual
Quantity5%
residual
is
nonhazardous;
(
0.05)
*
(
10,240
tons
residual/
yr)
=
512
tons
nonhazardous
residual/
yr
Estimated
Recovered
Product
Quantity15%
of
recovered
waste
quantity
will
be
recovered
metal
product
(
0.15)
*
(
0
tons
recovered
waste)
=
0
tons
recovered
metalEstimated
Recovered
Product
Quantity15%
of
recovered
waste
quantity
will
be
recovered
metal
product
(
0.15)
*
(
32,000
tons
recovered
waste)
=
4,800
tons
recovered
metal
Number
of
Off­
site
Hazardous
Waste
Residual
Shipments
per
Year*
0
hazardous
waste
shipments
per
yearNumber
of
Off­
site
Hazardous
Waste
Residual
Shipments
per
YearGiven
LQG
and
>
200
miles
then
maximum
of
(
4
shipments
or
9,728
tons
recovery
wastes/
18
ton
truck)
=
540.4
hazardous
waste
shipments
per
year
Number
of
Off
Site
Disposal
Shipments
per
Year
(
Hazardous
Landfill)
Given
LQG
and
>
200
miles
then
maximum
of
(
4
shipments
or
32,000
tons
disposal
wastes/
18
ton
truck)
=
1,777.8
disposal
shipments
per
yearNumber
of
Off
Site
Disposal
Shipments
per
Year
(
Hazardous
Landfill)
0
disposal
shipments
per
year
Number
of
Off­
site
Nonhazardous
Waste
Residual
Shipments
per
Year*(
0
tons
nonhazardous
residual/
18
tons
per
truck)
=
0
nonhazardous
waste
shipments
per
yearNumber
of
Off­
site
Non­
Hazardous
Waste
Residual
Shipments
per
Year(
512
tons
nonhazardous
residual/
18
tons
per
truck)
=
28.4
nonhazardous
waste
shipments
per
year
Distance
to
Nearest
Off­
site
Hazardous
Waste
Landfill338
milesDistance
to
Nearest
Off­
site
Hazardous
Waste
Landfill338
miles
Distance
to
Nearest
Off­
site
Non­
hazardous
Waste
Landfill50
milesDistance
to
Nearest
Off­
site
Non­
hazardous
Waste
Landfill50
miles
Location
of
GeneratorOregonLocation
of
GeneratorOregon
Cost
Calculations
(
costs
are
positive
and
revenues
are
negative)
On­
site
Metal
Recovery
Cost$
1,933.5
*
(
0
tons
recovered
waste/
yr)^
0.78
+
$
6,744.4
*
(
0
tons
recovered
waste/
yr)^
0.59
+
$
23,685
=
$
0/
yrOn­
site
Metal
Recovery
Cost$
1,933.5
*
(
32,000
tons
recovered
waste/
yr)^
0.78
+
$
6,744.4
*
(
32,000
tons
recovered
waste/
yr)^
0.59
+
$
23,685
=
$
9,407,401/
yr
Off­
site
Waste
Disposal
(
Hazardous
Waste
Landfill)
Given
full
truck
loads
(
greater
than
60%
full):
($
153.42/
ton)
*
(
32,000
tons
waste
per
yr)=
$
4,909,440/
yrOff­
site
Waste
Disposal
(
Hazardous
Waste
Landfill)
($
153.42/
ton)
*
(
0
tons
waste
per
yr)=
$
0/
yr
Residual
Off­
site
Hazardous
Landfill
Costmaximum(
($
320/
ton)
*
(
0
tons
waste
per
yr)
or
($
2,246/
load)
*
(
0
Hazardous
Waste
Shipments)
)=
$
0/
yrResidual
Off­
site
Hazardous
Landfill
Costmaximum(
($
320/
ton)
*
(
9,728
tons
waste
per
yr)
or
($
2,246/
load)
*
(
540.4
Hazardous
Waste
Shipments)
)=
$
3,112,960/
yr
Residual
Off­
site
Non­
hazardous
Landfill
Cost($
111/
ton)
*
(
0
tons
non­
hazardous
residual
per
yr)
=
$
0/
yrResidual
Off­
site
Non­
hazardous
Landfill
Cost($
111/
ton)
*
(
512
tons
non­
hazardous
residual
per
yr)
=
$
56,832/
yr
Waste
Characterization
Testing
Cost($
1,532/
load)
*
(
1,777.8
Hazardous
Loads
+
0
Non­
Hazardous
Load)
=
$
2,723,590/
yrWaste
Characterization
Testing
Cost($
1,532/
load)
*
(
540.4
Hazardous
Loads
+
28.4
Non­
Hazardous
Load)
=
$
871,402/
yr
Manifesting
Costs($
236/
shipment)
*
(
1,777.8
shipments/
yr)
=
$
419,561/
yr
Manifesting
Costs($
236/
shipment)
*
(
540.4
hazardous
shipments/
yr
)+
($
89/
shipment)
*
(
28.4
shipments/
yr)
=
$
130,062/
yr
Loading
Costs($
2.57/
ton)
*
(
32,000
tons
recovered
waste)
=
$
82,240/
yrLoading
Costs($
2.57/
ton)
*
(
10,240
tons
residual)
=
$
26,317/
yr
Residual
Waste
Transportation
Costs($
3.73/
mile)*(
0
hazardous
waste
shipments/
yr)*(
338
miles
to
hazardous
landfill/
hazardous
waste
shipment)
+
($
2.16/
mile)*(
0
nonhazardous
waste
shipments/
yr)*(
50
miles
to
nonhazardous
Landfill/
nonhazardous
waste
shipment)
=
$
0/
yrResidual
Waste
Transportation
Costs($
3.73/
mile)*(
540.4
hazardous
waste
shipments/
yr)*(
338
miles
to
hazardous
landfill/
hazardous
waste
shipment)
+
($
2.16/
mile)*(
28.4
nonhazardous
waste
shipments/
yr)*(
50
miles
to
nonhazardous
Landfill/
nonhazardous
waste
shipment)
=
$
684,371/
yr
Disposal
Waste
Transportation
Cost($
3.73/
mile)*(
1,777.8
hazardous
waste
shipments/
yr)*(
338
miles
to
hazardous
landfill/
hazardous
waste
shipment)
=
$
2,241,343/
yrDisposal
Waste
Transportation
Cost($
3.73/
mile)*(
0
hazardous
waste
shipments/
yr)*(
338
miles
to
hazardous
landfill/
hazardous
waste
shipment)
=
$
0/
yr
Salvage
(
Recovered
Product)
Value($
643/
ton
metal)
*
(
0
tons
recovered
metal/
yr)
=
$
0/
yrSalvage
(
Recovered
Product)
Value($
643/
ton
metal)
*
(
4,800
recovered
metal/
yr)
=
$
3,086,400/
yr
Hazardous
Material
Training
CostGiven
LQG
then
$
9,794/
yrHazardous
Material
Training
CostGiven
LQG
then
$
9,794/
yr
Manifest
Training
CostGiven
LQG
then
$
1,828/
yrManifest
Training
CostGiven
LQG
then
$
1,828/
yr
Biennial
Report/
General
Administrative
Duties
CostGiven
LQG
then
$
2,430/
yrBiennial
Report/
General
Administrative
Duties
CostGiven
LQG
then
$
2,430/
yr
Contingency
Planning
CostGiven
LQG
then
$
2,796Contingency
Planning
CostGiven
LQG
then
$
2,796
Initial
Waste
Characterization
Cost$
6,160Initial
Waste
Characterization
Cost$
6,160
Exclusion
Filing
Fee
(
One
time
Expenditure)$
0Exclusion
Filing
Fee
(
One
time
Expenditure)$
639
State
Facility
Tax/
FeeGiven
Oregon
and
LQG
then:
$
525
activity
verification
fee/
yrState
Facility
Tax/
FeeGiven
Oregon
and
LQG
then:
$
525
activity
verification
fee/
yr
State
Generation
Tax/
FeeGiven
Oregon
then:
($
45
generation
fee/
ton)
*
(
32,000
tons
disposed
waste/
yr)
=
$
1,440,000/
yrState
Generation
Tax/
FeeGiven
Oregon
then:
($
45
generation
fee/
ton)
*
(
9,728
tons
residual/
yr)
=
$
437,360/
yr
Total$
11,839,707/
yr$
11,664,477/
yr
Incremental
Costs­$
175,230/
yr
*
Residual
costs
are
included
in
the
cost
for
off­
site
commercial
treatment
and
disposal
Appendix
V
Example
Cost
Calculation:
1999
Off­
site
Disposal
of
Spent
Aluminum
Potliner
(
K088)
shifting
to
On­
site
Sodium
Fluoride
Recovery
(
2001
$)
Pre­
Rule
Cost
CalculationPost­
Rule
Cost
Calculation
Cost
Inputs
Total
Quantity
of
Hazardous
Waste
Generated360
tons
hazardous
waste/
yrTotal
Quantity
of
Hazardous
Waste
Generated(
360
tons
hazardous
waste/
yr)
­
(
360
tons
recovered
waste/
yr)+
(
360
tons
recovered
waste/
yr*
0.32
fraction
as
residuals
*
0
fraction
characteristically
hazardous)
=
0
tons
hazardous
waste/
yr
(
recovered
waste
quantity
no
longer
hazardous
by
definition)
Generator
StatusIf
(
tons
hazardous
waste/
yr
>
13.2
tons/
yr)
then
LQGGenerator
StatusIf
(
1.3
tons/
yr
>
tons
hazardous
waste/
yr)
then
CESQG
(
Not
a
Generator)
Quantity
of
Waste
Recovered
On
Site0
tons
recovered
waste/
yrQuantity
of
Waste
Recovered
On
Site360
tons
recovered
waste/
yr
Quantity
of
Waste
Disposed
Off
Site360
tons
recovered
waste/
yrQuantity
of
Waste
Disposed
Off
Site0
tons
recovered
waste/
yr
Estimated
Residual
Quantity*
33%
of
recovered
waste
quantity
will
be
residual
(
0)
*
(
0
tons
recovered
waste/
yr)
=
0
tons
residual/
yrEstimated
Residual
Quantity32%
of
recovered
waste
quantity
will
be
residual
(
0.32)
*
(
360
tons
recovered
waste/
yr)
=
119
tons
residual/
yr
Estimated
Hazardous
Residual
Quantity*
100%
residual
is
Listed
hazardous;
(
1.00)
*
(
0
tons
residual/
yr)
=
0
tons
hazardous
residual/
yrEstimated
Hazardous
Residual
Quantity0%
residual
is
characteristically
hazardous;
(
0)
*
(
119
tons
residual/
yr)
=
0
tons
hazardous
residual/
yr
Estimated
Nonhazardous
Residual
Quantity*
0%
residual
is
nonhazardous;
(
0)
*
(
0
tons
residual/
yr)
=
0
tons
nonhazardous
residual/
yrEstimated
Non­
hazardous
Residual
Quantity100%
residual
is
nonhazardous;
(
1.0)
*
(
119
tons
residual/
yr)
=
119
tons
nonhazardous
residual/
yr
Estimated
Recovered
Product
Quantity2%
of
recovered
waste
quantity
will
be
recovered
sodium
fluoride
product
(
0.02)
*
(
0
tons
recovered
waste)
=
0
tons
recovered
sodium
fluorideEstimated
Recovered
Product
Quantity2%
of
recovered
waste
quantity
will
be
recovered
sodium
fluoride
product
(
0.02)
*
(
360
tons
recovered
waste)
=
7.2
tons
recovered
sodium
fluoride
Number
of
Off­
site
Hazardous
Waste
Residual
Shipments
per
Year*
0
hazardous
waste
shipments
per
yearNumber
of
Off­
site
Hazardous
Waste
Residual
Shipments
per
Year0
hazardous
waste
shipments
per
year
Number
of
Off
Site
Disposal
Shipments
per
YearGiven
LQG
and
>
200
miles
then
maximum
of
(
4
shipments
or
360
tons
recovery
wastes/
18
ton
truck)
=
20
recovery
shipments
per
yearNumber
of
Off
Site
Recovery
Shipments
per
Year0
recovery
shipments
per
year
Number
of
Off­
site
Nonhazardous
Waste
Residual
Shipments
per
Year*(
0
tons
nonhazardous
residual/
18
tons
per
truck)
=
0
nonhazardous
waste
shipments
per
yearNumber
of
Off­
site
Non­
Hazardous
Waste
Residual
Shipments
per
Year(
119
tons
nonhazardous
residual/
18
tons
per
truck)
=
6.6
nonhazardous
waste
shipments
per
year
Distance
to
Nearest
Off­
site
Hazardous
Waste
Incineration
Facility1000
milesDistance
to
Nearest
Off­
site
Hazardous
Waste
Incineration
Facility1000
miles
Distance
to
Nearest
Off­
site
Non­
hazardous
Waste
Landfill50
milesDistance
to
Nearest
Off­
site
Non­
hazardous
Waste
Landfill50
miles
Location
of
GeneratorOregonLocation
of
GeneratorOregon
Cost
Calculations
(
costs
are
positive
and
revenues
are
negative)
On­
site
Sodium
Fluoride
Recovery
Cost($
465/
ton)
*
(
0
tons
recovered
waste/
yr)^
0.9
+
($
4,136/
ton)
*
(
0
tons
recovered
waste/
yr)^
0.6
$
53,603
=
$
0/
yrOn­
site
Sodium
Fluoride
Recovery
Cost($
465/
ton)
*
(
360
tons
recovered
waste/
yr)^
0.9
+
($
4,136/
ton)
*
(
360
tons
recovered
waste/
yr)^
0.6
$
53,603
=
$
287,898/
yr
Off­
site
Incineration
Cost($
551.5/
ton)
*
(
360
tons
incinerated
waste/
yr)
=
$
198,551/
yrOff­
site
Incineration
Cost
Given
small
loads
(
less
than
60%
of
a
full
18
ton
load):
($
170/
ton
+
$
25.50/
ton
surcharge)
*
(
0
tons
incinerated
waste/
yr)
=
$
0/
yr
Residual
Off­
site
Hazardous
Landfill
Cost
($
320/
ton)
*
(
0
tons
hazardous
residual
per
yr)
=
$
0/
yrResidual
Off­
site
Hazardous
Landfill
Cost
($
320/
ton)
*
(
0
tons
hazardous
residual
per
yr)
=
$
0/
yr
Residual
Off­
site
Non­
hazardous
Landfill
Cost($
111/
ton)
*
(
0
tons
non­
hazardous
residual
per
yr)
=
$
0/
yrResidual
Off­
site
Non­
hazardous
Landfill
Cost($
111/
ton)
*
(
119
tons
non­
hazardous
residual
per
yr)
=
$
13,209/
yr
Waste
Characterization
Testing
Cost($
1,410/
load)
*
(
20
Hazardous
Loads
+
0
Non­
Hazardous
Load)
=
$
28,200/
yrWaste
Characterization
Testing
Cost($
1,410/
load)
*
(
0
Hazardous
Loads
+
6.6
Non­
Hazardous
Load)
=
$
9,306/
yr
Manifesting
Costs($
236/
shipment)
*
(
20
shipments/
yr)
=
$
4,720/
yr
Manifesting
Costs($
89/
shipment)
*
(
6.6
shipments/
yr)
=
$
587/
yr
Loading
Costs($
2.57/
ton)
*
(
360
tons
recovered
waste)
=
$
925/
yrLoading
Costs($
2.57/
ton)
*
(
119
tons
residual)
=
$
306/
yr
Residual
Waste
Transportation
Costs($
3.73/
mile)*(
0
hazardous
waste
shipments/
yr)*(
1,000
miles
to
hazardous
incineration/
hazardous
waste
shipment)
+
($
2.16/
mile)*(
0
nonhazardous
waste
shipments/
yr)*(
50
miles
to
nonhazardous
landfill/
nonhazardous
waste
shipment)
=
$
0/
yrTransportation
Costs($
3.73/
mile)*(
0
hazardous
waste
shipments/
yr)*(
1,000
miles
to
hazardous
incineration/
hazardous
waste
shipment)
+
($
2.16/
mile)*(
6.6
nonhazardous
waste
shipments/
yr)*(
50
miles
to
nonhazardous
landfill/
nonhazardous
waste
shipment)
=
$
713/
yr
Disposed
Waste
Transportation
Cost($
3.73/
mile)
*
(
20
hazardous
waste
shipments/
yr)*(
1,000
miles
to
hazardous
incineration/
hazardous
waste
shipment)
=
$
74,600/
yrDisposed
Waste
Transportation
Cost($
3.73/
mile)
*
(
0
hazardous
waste
shipments/
yr)*(
1,000
miles
to
hazardous
incineration/
hazardous
waste
shipment)
=
$
0/
yr
Salvage
(
Recovered
Product)
Value($
1,240/
ton
sodium
fluoride)
*
(
0
tons
recovered
acid/
yr)
=
$
0/
yrSalvage
(
Recovered
Product)
Value($
1,240/
ton
sodium
fluoride)
*
(
7.2
tons
recovered
acid/
yr)
=
$
8,928/
yr
Hazardous
Material
Training
CostGiven
LQG
then
$
9,794/
yrHazardous
Material
Training
CostGiven
Not
a
Generator
then
$
0/
yr
Manifest
Training
CostGiven
LQG
then
$
1,828/
yrManifest
Training
CostGiven
Not
a
Generator
then
$
0/
yr
Biennial
Report/
General
Administrative
Duties
CostGiven
LQG
then
$
2,430/
yrBiennial
Report/
General
Administrative
Duties
CostGiven
Not
a
Generator
then
$
0/
yr
Contingency
Planning
CostGiven
LQG
then
$
2,796Contingency
Planning
CostGiven
Not
a
Generator
then
$
0
Initial
Waste
Characterization
Cost$
6,160Initial
Waste
Characterization
Cost$
6,160
Exclusion
Filing
Fee
(
One
time
Expenditure)$
0Exclusion
Filing
Fee
(
One
time
Expenditure)$
639
State
Facility
Tax/
FeeGiven
Oregon
and
LQG
then:
$
525
activity
verification
fee/
yrState
Facility
Tax/
FeeGiven
Oregon
and
Not
a
Generator
then:
$
0
activity
verification
fee/
yr
State
Generation
Tax/
FeeGiven
Oregon
then:
($
45
generation
fee/
ton)*(
360
tons
recovered
waste/
yr)
=
$
16,200/
yrState
Generation
Tax/
FeeGiven
Oregon
then:
($
45
generation
fee/
ton)*(
0
tons
residual/
yr)
=
$
0/
yr
Total$
346,728/
yr$
308,842/
yr
Incremental
Costs­
$
37,887/
yr
*
Residual
costs
are
included
in
the
costs
for
off­
site
commercial
incineration.
Appendix
W
Methodology
for
Estimating
Residual
Generation
and
Management
This
appendix
presents
the
methodology
used
regarding
metal,
solvent,
and
acid
recovery
residual
generation
and
disposal.

Using
1999
BRS
data,
facilities
reporting
waste
management
with
system
types
M013,
M021,
and
M031
were
reviewed.
Due
to
the
limited
number
of
facilities
reporting
wastes
managed
with
system
types
M013
and
M031,
all
such
facilities
were
reviewed.
Facilities
reporting
management
by
system
type
M021
were
divided
into
5
groups,
approximately
equal
in
number,
based
on
the
mass
of
waste
managed
by
system
type
M021.
Six
facilities
were
selected
from
each
group.
The
groups
were
divided
as
follows:
less
than
1.1
tons
managed,
1.1
to
5
tons
managed,
5
to
13.5
tons
managed,
13.5
to
55
tons
managed,
and
greater
than
55
tons
managed.
The
tables
below
present
the
data
results.

The
following
assumptions
were
made
regarding
the
recovery
processes:

°
Reclamation
systems
for
acid
and
solvents
are
closed
loop.
That
is
no
losses
from
spillage
or
waste
are
assumed.
This
is
a
simplification
of
the
actual
process
as
many
processes
may
include
settlement
tanks
or
other
open­
air
sections
that
may
allow
evaporation
or
spillage.

°
All
ineffective
products
are
removed
with
the
process
residuals.
An
effectiveness
factor
or
assay
value
is
included
to
estimate
the
"
purity"
of
the
recovered
solvent,
acid,
or
metal.

°
Mass
is
assumed
to
be
balanced
in
the
acid
and
solvent
recovery
process.
No
additives
or
precipitants
are
assumed
into
the
process,
or
the
change
in
product/
residual
mass
in
comparison
to
the
total
mass
is
minor.
The
recovery
of
metals
process,
68
percent
of
the
waste
stream
mass
is
assumed
to
contain
the
product
metals
and
components
that
are
volatilized
(
e.
g.,
water
vapor).
Twenty
(
20)
percent
of
the
waste
stream
is
assumed
recovered
as
metals
in
higher
quality
wastes
and
five
percent
in
lower
quality
wastes.
Thirty­
two
(
32)
percent
is
assumed
to
be
residual
waste.
The
mass
recovery
of
products
is
discussed
further
below.

Metals
Recovery
Statistics
No.
Data
Points7
Range0.42
to
84
percent
Average32
percent
Standard
Deviation33.92
percent
DPRA
reviewed
a
total
of
19
facilities
reporting
wastes
managed
by
M013
in
the
1999
BRS.
One
additional
facility,
for
a
total
of
seven
facilities,
was
able
to
be
used
in
a
percent
residual
assumption.
Residual
waste
streams
could
not
be
identified
in
the
remaining
facilities.
The
management
system
type
reported
for
the
residuals
identified
from
M013
system
processes
are
M061,
M111,
M112,
M119,
and
M132.
Five
of
seven
waste
generating
facilities
managed
the
M013
residuals
by
stabilization
(
M111,
M112,
and
M119).
The
likely
final
deposition
of
the
stabilized
wastes
are
in
a
RCRA
Subtitle
C
hazardous
waste
landfill.

Solvent
Recovery
Statistics
No.
Data
Points23
Range0.46
to
140
percent
Average33
percent
Standard
Deviation32.13
percent
Residuals
generated
by
M021
system
processes
were
reported
managed
by
the
following
system
types;
M042,
M051,
M061,
and
M081.
An
total
of
28
facilities
were
reviewed,
of
which
5
facility
residual
waste
streams
could
not
be
identified.
Fuel
blending
(
M061)
was
reported
by
17
of
22
facilities
for
management
of
M021
residuals.
An
additional
three
facilities
managed
M021
residuals
by
other
co­
burning
or
incineration
systems
(
M042
and
M051).

Acid
Recovery
Statistics
No.
Data
Points18
Range0
to
105
percent
Average26
percent
Standard
Deviation31.92
percent
Residuals
generated
by
M031
system
processes
were
assumed
to
be
similar
in
form
to
the
spent
acid
waste
stream.
That
is,
the
contaminants
(
generally
metals)
were
concentrated
in
a
smaller
portion
of
the
waste
stream
for
management.
The
disposal
quantities
of
these
residuals
were
identified
by
their
description
and
management
system
type.
An
total
of
23
facilities
were
reviewed,
of
which
5
facility
residual
waste
streams
could
not
be
identified.
Residuals
were
reported
managed
by
M039,
M042,
M043,
M051,
M077,
M104,
M109,
M121,
M134,
M136.
Chemical
precipitation
(
M077)
was
reported
by
seven
of
eighteen
facilities
for
management
of
M031
residuals.
One
additional
facility
reported
management
by
neutralization
only
(
M121),
which
is
similar
to
chemical
precipitation.

The
analysis
should
use
the
average
residual
generation
values
listed
above.
Metal
recovery
residuals
will
be
managed
by
stabilization
and
Subtitle
C
landfill.
Solvent
residuals
are
managed
by
energy
recovery.
Acid
recovery
residuals
are
managed
by
chemical
precipitation.
Cost
assumptions
for
management
of
acid
recovery
residuals
will
include
stabilization
and
landfill
disposal
of
precipitates,
and
sewer
discharge
of
neutralized
wastewater.
Appendix
X
Analysis
of
Metals
Containing
and
Organic
Liquid
Disposal
Quantities
This
appendix
presents
the
review
of
selected
metals
containing
liquids
and
organic
liquids
waste
streams
to
determine
the
potential
for
or
quantity
of
mis­
categorized
disposed
waste
streams.
Disposed
wastes
streams
1999
BRS
data
was
reviewed
for
the
final
disposition
in
the
case
of
metals
containing
liquids
and
the
description
in
the
case
of
organic
liquids.
Metals
containing
liquids
may
be
classified
as
disposed
based
on
the
reported
1999
Biennial
Report
management
methods,
but
the
waste
may
be
managed
further
and
metals
content
recovered.
The
final
disposal/
management
method
may
not
be
reflected
in
the
reporting
by
the
disposing
facility.
For
example,
metals
containing
liquids
reported
managed
by
chemical
precipitation
(
M077)
may
be
disposed
in
a
landfill
or
shipped
to
a
high
temperature
metals
recovery
facility.
In
which
case,
the
waste
streams
should
be
classified
as
recovered
off­
site
outside
the
same
NAICs.
For
organic
liquid
wastes
disposed,
the
facility
may
recover
solvents
on
site
and
produce
a
waste
stream
with
a
similar
form
as
spent
solvents.
The
screening
process
for
the
1999
BRS
data
did
not
differentiate
between
solvent
recovery
residuals
and
spent
solvents.
A
review
of
the
wastes
descriptions
was
conducted
to
determine
if
the
organic
liquid
wastestreams
were
the
result
of
onsite
recovery
and
should
be
excluded
from
the
analysis.
Examples
of
wastes
that
should
be
removed
from
the
analysis
include
still
bottoms,
distillation
fractions,
column
bottoms.
Other
wastes
streams
with
descriptions
indicating
a
recovery
process
was
employed
were
also
flagged
to
be
removed.

DPRA
reviewed
a
total
of
10
metals
containing
liquids
generating
facilities,
representing
$
1.9
million
of
a
total
of
$
2.9
million
in
incremental
cost
savings
without
taxes
(
66
percent).
Three
facilities
were
identified
that
generate
3,621.5
tons
of
metals
containing
liquid
waste
streams
with
which
the
metals
are
ultimately
recovered.
The
recovery
facilities
represent
a
total
of
$
0.56
million
of
the
incremental
costs
savings
without
taxes,
29
percent
of
the
reviewed
facilities
and
19
percent
of
the
total
incremental
cost
savings
without
taxes.

DPRA
reviewed
a
total
of
35
organic
liquids
generating
facilities,
representing
$
87.9
million
of
a
total
of
$
174.4
million
in
incremental
cost
savings
without
taxes
(
50
percent).
Eight
facilities
were
identified
that
generate
10,610
tons
of
organic
liquid
waste
streams
of
which
the
description
indicates
them
to
be
solvent
recovery
residuals.
These
facilities
represent
a
total
of
$
23.9
million
of
the
incremental
costs
savings
without
taxes,
27
percent
of
the
reviewed
facilities
and
14
percent
of
the
total
incremental
cost
savings
without
taxes.
The
waste
streams
identified
represent
only
a
portion
of
the
organic
liquids
generated
at
seven
of
the
eight
facilities;
therefore,
the
identified
wastes
streams
account
for
less
than
the
facility
totals
of
$
23.9
million
incremental
costs
savings
without
taxes.
DPRA
estimates
the
waste
streams
represent
53
percent
of
the
eight
facilities
incremental
cost
savings
without
taxes
($
46.6
million).
Metals
Containing
Liquids
Generating
Facilities
Reviewed
for
Potential
Metal
Recovery
Ultimate
Disposal
Generator
EPA
ID
Total
Offsite
Shipped
Quantity
(
tons)
Offsite
Shipped
Quantity
(
tons)
Management
Method
Receiver
EPA
ID
Receiver
Name
(

Secondary
Receiver
Name)
Management
Method
for
Precipitated
Sludges
Conclusions
NYD002241982
1773.4
169.9
Stabilization
(
M077)
PAD010154045
Envirite
of
Pennsylvania
Inc.
Stabilization/
chemical
fixation
(
M111)
Stabilization/
chemical
fixation
­
likely
landfilled
1603.5
Chemical
precipitation
in
combination
with
biological
treatment
(
M091)
NJD002385730
Dupont
Chambers
Works
(
Unable
to
find
related
waste
stream)

ILD984774513
1233.1
1233.1
Chemical
precipitation
(
M077)
ILD062480850

TXR000000034
Phibro­
Tech
Inc

ECS
Refining
Texas
LLC
No
1999
Biennial
Report
data
for
TXR000000034
WID000711077
1315.2
1315.2
Stabilization/
chemical
fixation
(
M111)
IND093219012
Heritage
Environmental
Svc
­
Indy
Landfill
(
M132)
Landfilled
MND980680540
1514.5
1514.5
Chemical
precipitation/
other
aqueous
inorganic
treatment
(
M077/
M078)
MND981098478
US
Filter
Recovery
Services
Inc
High
temperature
metals
recovery
(
M011)

Remove
facility
from
off­
site
disposal
scenario
to
off­
site
recovery
scenario.

AZD980818330
1105.3
1105.3
Chemical
oxidation
followed
by
chemical
precipitation
(
M074)
CAD008488025
Phibro­
Tech
Inc
Other
metals
recovery
for
reuse
(
M014)
Remove
facility
from
offsite
disposal
scenario
to
off­
site
recovery
scenario.

NOTE:
WR­
form
says
M014,
not
M074
ILD067464875
1332.9
1288.6
Chemical
precipitation
(
M077)
ILD000666206

(
onsite
M112)

MID000724831
Envirite
of
Illinois
Inc.
Stabilization/
chemical
fixation
(
M111)
Stabilization/
chemical
fixation
­
likely
landfilled
­
NOTE:
GM­
form
says
M112,
not
M077
33.3
Transfer
facility
storage
(
M141)
ILD980502744
Safety­
Kleen
Corp
(
Unable
to
find
related
waste
stream)

11.0
Chemical
precipitation
(
M077)
ILD062480850

TXR000000034
Phibro­
Tech
Inc

ECS
Refining
Texas
LLC
No
1999
Biennial
Report
data
for
TXR000000034
ILD984809905
760.9
760.9
Chemical
precipitation
(
M077)
ILD000666206

(
onsite
M112)

MID000724831
Envirite
of
Illinois
Inc.
Stabilization/
chemical
fixation
(
M111)
Stabilization/
chemical
fixation
­
likely
landfilled
­
NOTE:
GM­
form
says
M112,
not
M077
ILD155126030
687.3
687.3
Chemical
precipitation
(
M077)
ILD000666206

(
onsite
M112)

MID000724831
Envirite
of
Illinois
Inc.
Stabilization/
chemical
fixation
(
M111)
Stabilization/
chemical
fixation
­
likely
landfilled
­
NOTE:
GM­
form
says
M112,
not
M077
MND001037639
1001.8
1001.5
Chemical
precipitation/
other
aqueous
inorganic
treatment
(
M077/
M078)
MND981098478
US
Filter
Recovery
Services
Inc
High
temperature
metals
recovery
(
M011)

Remove
facility
from
off­
site
disposal
scenario
to
off­
site
recovery
scenario.

0.2
Chemical
precipitation
(
M077)
MND980996805

MND981098478
Enviro­
Chem
Inc

US
Filter
Recovery
Services
Inc
High
temperature
metals
recovery
(
M011)
Remove
facility
from
off­
site
disposal
scenario
to
off­
site
recovery
scenario.

ILD984844134
601.3
601.3
Chemical
precipitation
(
M077)
ILD000666206

(
onsite
M112)

MID000724831
Envirite
of
Illinois
Inc.
Stabilization/
chemical
fixation
(
M111)
Stabilization/
chemical
fixation
­
likely
landfilled
­
NOTE:
GM­
form
says
M112,
not
M077
Organic
Liquids
Generating
Facilities
Reviewed
for
Potential
to
be
Solvent
Recovery
Residuals
Generator
EPA
ID
Total
Offsite
Shipped
Quantity
(
tons)
Offsite
Shipped
Quantity
(
tons)
Waste
Description
Other
Info
Conclusions
NJD002146504
3,760.6
0.1
WASTE
PETROLEUM
NAPTHA,
COMBUSTIBLE
LIQUID,
FROM
PARTS
DEGREASING
3,760.5
FLAMMABLE
LIQUID
FROM
PRODUCTION
OR
SUNSCREENS
WID000808824
3,676.5
3,657.5
(
no
waste
description)
F005,
A34,
B203
19.0
(
no
waste
description)
F005,
A37,
B203
WIR000046276
3,263.2
14.8
(
no
waste
description)
F003,
A09,
B203
3,248.4
(
no
waste
description)
D001,
A09,
B203
0.1
(
no
waste
description)
D038,
A59,
B203
0.1
(
no
waste
description)
D006,
A19,
B203
0.2
(
no
waste
description)
U122,
A58,
B219
TXD980626014
3,224.0
1,711.7
STYRENE
WASTE
OIL.
THIS
WASTE
CONSISTS
OF
BENZENE,
TOLUENE,

534.8
SPENT
XYLENE.
THE
WASTE
IS
A
SPENT
XYLENE
SOLVENT.
IT
IS
A
1.8
FLAMMABLE
ORGANIC
LIQUIDS.
THE
WASTE
CONSISTS
OF
ORGANIC
LI
5.7
PAINT
WASTE,
LIQUID
954.2
NON­
AQUEOUS
LIQUID,
TYPICALLY
AS
FOLLOWSHEPTANE
ISOMERS
48%,

2.2
ANTIOXIDANT.
THE
WASTE
IS
A
CLEAR
LIGHT
YELLOW
LIQUID
WITH
13.6
PARTS
WASHER
SOLVENT
IAD005272398
2,830.7
17.2
DUPONT
WASTE
CODE
=
WFW­
1
OBSOLETE
NON­
SALEABLE
PAINT
AND
PA
INT
RELATED
MATERIAL,
ORGANIC
LIQUID,
FUELS
BLENDING
FOR
CEM
ENT
KILN
1,737.0
DUPONT
WASTE
CODE
=
WOM­
0;
MIXED
WASTE
PAINT
AND
PAINT
RELAT
ED
MATERIALS,
ORGANIC
LIQUIDS,
TFE
STILL
BOTTOMS,
FUELS
FOR
CEMENT
KILN
AND
INCINERATION
Already
a
distillation
by­
product
1,076.6
DUPONT
WASTE
CODE
=
WOM­
16;
OCPSF
PROCESS
WASTEWATER,
RESIN
WATER
OF
REACTION,
LOW
SOLIDS
LIQUID,
SHIPPED
OFF­
SITE
FOR
BIOLOGICAL
WATER
TREATMENT
WVD004325353
3,228.7
3,188.2
IGNITABLE,
LISTED
WASTE
SOLVENTS
FROM
PROCESS
EQUIPMENT
CLEA
NUP;
CONTAINS
TOLUENE,
METHANOL,
ISOPROPANOL,
ETHANOL
AND
SO
LVENT
140.
0.1
IGNITABLE
OFF­
SPEC
RAW
MATERIAL,
ISOPROPYL
ALCOHOL.

1.6
IGNITABLE
OFF­
SPEC
ORGANOFUNCTIONAL
SILANE
PRODUCT.

2.9
IGNITABLE,
SILOXANE
DISTILLATION/
STRIPPING
WASTE
FROM
PRODUC
T
MANUFACTURING.
Already
a
distillation
by­
product
8.1
CORROSIVE
OFF­
SPEC
RAW
MATERIAL,
POLYOXYALKYLENE
BUTYL
EHTER
PHOSPHATE.

0.7
IGNITABLE,
SILOXANE
DISTILLATION/
STRIPPING
RESIDUE
FROM
PROD
UCT
MANUFACTURING
CONTAINING
ETHANOL.
Already
a
distillation
by­
product
0.8
IGNITABLE
WASTE
FROM
PROCESS
EQUIPMENT
CLEANUP
WITH
ETHANOL.

0.1
IGNITABLE,
LISTED
OFF­
SPEC
RAW
MATERIAL,
METHYLENE
CHLORIDE.

0.2
LISTED
OFF­
SPEC
RAW
MATERIAL,
TETRAHYDROFURAN.

0.2
IGNITABLE,
LISTED
WASTE
SOLVENTS
FROM
PROCESS
EQUIPMENT
CLEA
NUP
CONTAINING
TOLUENE
AND
METHANOL.

0.4
IGNITABLE
OFF­
SPEC
RAW
MATERIAL,
DICYCLOPENTADIENE.
1.2
IGNITABLE,
SILOXANE
DISTILLATION/
STRIPPING
RESIDUE
FROM
PROD
UCT
MANUFACTURING.
Already
a
distillation
by­
product
1.3
IGNITABLE
OFF­
SPEC
RAW
MATERIAL,
ETHYLENE
GLYCOL.

2.6
IGNITABLE,
LISTED
PAINT
SOLVENTS
FROM
MAINTENANCE
OPERATIONS
.

20.3
IGNITABLE,
LISTED
WASTE
SOLVENTS
AND
OFF­
SPEC
SURFACTANTS.

NJD981080401
2,682.7
2,682.7
DISTILLATION
FRACTIONS
&
STILL
BOTTOMS
AND
SOLVENTS
USED
Already
a
distillation
by­
product
TXD000461533
2,944.3
13.3
PAINT
RELATED
WASTE
CONSISTS
OF
PAINT,
PAINT
THINNER,
PAINT
597.0
ORGANIC
ACID
RESIDUES
GENERATED
DURING
PRODUCTION
OF
ORGANIC
70.7
SPENT
ACETONE/
MSO
WASTE
GENERATED
AT
OLEFINS
UNIT
FROM
ACETY
982.1
VINYL
ACETATE
POLYMER
IS
VISCOUS
ORGANIC
LIQUID
MATERIAL
RES
928.3
"
A"
DRIPOLENE
IS
STILL
BOTTOMS
GENERATED
AS
PART
OF
OLEFINS
Already
a
distillation
by­
product
6.4
SPENT
SOLVENTS,
HALOGENATED
&
NON­
HALOGENATED
ORGANIC
CHEMIC
0.2
METHANOL
SYNOSOL
WATER
RESULTING
FROM
MIXTURE
OF
METHANOL,
S
346.2
MIXED
VARNISH
WASTE
IS
VISCOUS
LIQUID
ORGANIC
MATERIAL
RESUL
ARD052528809
2,876.3
19.2
TANK
CLEANOUT,
ONE
TIME.
(
15)
FLAMMABLE.
CONTAINS
TOLUENE.
(
13292)

0.7
MIXED
LAB
WASTES.
(
LAB)
FLAMMABLE,
TOXIC.
CONTAINS
ACETONE,
METHANOL.
(
12654)

1.8
MIXED
LAB
WASTES.
(
LAB)
FLAMMABLE,
TOXIC.
CONTAINS
ACETONE,
BENZENE.
(
9433)

5.0
MIXED
LAB
WASTES.
(
LAB)
FLAMMABLE,
TOXIC.
CONTAINS
ACETONE,
DICHLOROMETHANE.
(
9276)

695.5
SPENT
DISTILLATION
CHASER
FLUID,
WASTE
OIL.
(
DE)
FLAMMABLE.
(
CP1374)
Already
a
distillation
by­
product
0.6
DISTILLATION
COLUMN
BOTTOMS
AND
OVERHEADS.
(
AD)
FLAMMABLE.
(
9345)
Already
a
distillation
by­
product
2,145.1
DISTILLATION
BY
PRODUCT
FROM
PRODUCTION.
(
AD
­
PCO)
FLAMMAB
LE.
(
9710­
06333)
Already
a
distillation
by­
product
1.7
PAINT
WASTE.
(
MAINT)
TOXIC,
FLAMMABLE.
CONTAINS
TOLUENE,
XYL
ENE.
(
9278)

6.6
TANK
CLEANOUT,
ONE
TIME.
(
AD)
FLAMMABLE.
CONTAINS
ADMA.
(
137
72)

TXD008092793
2,451.1
2,404.5
MISCELLANEOUS
ORGANIC
LIQUIDS
46.6
HAZARDOUS
NON­
HALOGENATED
SOLVENTS
PRD090036021
2,589.0
60.7
AQUEOUS
PHASE
FROM
PHARMACEUTICAL
MANUFACTURING
PROCESS.

1,968.6
IGNITABLE
SPENT
SOLVENT
MIXTURE
FROM
PHARMACEUTICAL
MANUFACT
URING
PROCESS;
MIXTURE
OF
TOLUENE,
ACETONE,
ETHYL
ACETATE,
M
ETHYLENE
CHLORIDE,

METHANOL,
XYLENE,
METHYL
ISOBUTYL
KETONE
5.8
DISCARDED
SPENT
HALOGENATED
&
NON­
HALOGENATED
SOLVENTS
535.5
IGNITABLE
SPENT
SOLVENT
MIXTURE
FROM
PHARMACEUTICAL
PROCESS;
ACETONE,
METHANOL,
ETHYL
ACETATE
AND
METHYLENE
CHLORIDE.

14.2
DISCARDED
FLAMMABLE
WASTE
FROM
PHARMACEUTICAL
MANUFACTURINGP
ROCESS
4.2
OFF
SPEC
DISCARDED
INTERMEDIATE
ORGANIC
LIQUIDS
OHD076796887
2,766.8
155.1
DRUM
LIQUIDS
FROM
RESIN
MANUFACTURING
0.1
2K
CLEARCOAT
AND
KILLED
ISOCYANATE
WASTE
0.2
AGED
RAW
MATERIAL:
DIMETHYLETHANOLAMINE
5.3
AGED
RAW
MATERIAL:
PHENOTIC
RESIN
SOLUTION
20.8
CLEANING
SOLVENT
BLEND
USED
IN
RESIN
MANUFACTURING
19.7
OFF­
SPEC
WATERBASED
RESIN
2.4
WASTE
MONOMER
MIX
FROM
LABORATORY
TESTING
293.3
OFF­
SPEC
SOLVENT
BASED
RESINS
70.9
WASTE
TOLUENE
AND
METHYL
CARBANATE
SOLUTION
2,198.7
FLAMMABLE
LIQUID
DISTILLATE
FROM
RESIN
MANUFACTURING
Already
a
distillation
by­
product
0.4
KARL
FISCHER
REAGENT
FROM
LABORATORY
TESTING
VAD000019828
2,236.6
PAINT
MANUFACTURER
HAZARDOUS
WASTE
SOLVENT
NJD002191211
2,283.3
15.9
METHYLENE
CHLORIDE
0.2
WASTE
SOLVENTS
2,267.2
BULK
SOLVENTS
BUILDING
30
IAD045372836
2,432.7
1,047.9
BENZENE­
CONTAINING
PYROLYSIS
OIL
FROM
ETHYLENE
PRODUCTION:
MIXTURE
OF
ORGANIC
COMPONENTS.

1,354.5
IGNITABLE
SPENT
SOLVENT
AND
CO­
MONOMER
FROM
LOW
DENSITY
POLYETHYLENE
PRODUCTION:
MIXTURE
OF
MINERAL
SPIRITS
AND
VINYL
ACETATE.

28.0
IGNITABLE
SPENT
SOLVENT
AND
CO­
MONOMER
FROM
LOW
DENSITY
POLYETHYLENE
PRODUCTION:
MIXTURE
OF
MINERAL
SPIRITS
AND
METHYL
ACRYLATE.

0.2
IGNITABLE
SPENT
SOLVENT
FROM
OPERATIONAL
CLEANOUT:
MIXTURE
OF
ALIPHATIC
HYDROCARBONS.

0.2
IGNITABLE
SPENT
SOLVENTS
FROM
QUALITY
CONTROL
LABORATORY
OPERATIONS:
MIXTURE
OF
SOLVENTS,
WITH
MAIN
COMPONENTS
BEING
CYCLOHEXANE
AND
TETRACHLOROETHENE.

1.2
WASTE
PAINT
MATERIALS
AND
MIXTURE
OF
VARIOUS
OIL­
BASED
PAINTS.

0.7
IGNITABLE
SPENT
SOLVENTS
FROM
QUALITY
CONTROL
LABORATORY
OPERATIONS:
MIXTURE
OF
SOLVENTS,
WITH
MAIN
COMPONENTS
BEING
CYCLOHEXANE
AND
TETRACHLOROETHENE.

TXD008090011
2,212.8
2,212.0
BY­
PRODUCT
ORGANICS
FROM
MERCAPTAN
MANUFACTURING.
TOWER
BOT
0.8
WASTE
PAINT
THINNER
AND
PAINT
COLLECTED
IN
55
GALLON
DRUMS
TXR000025809
2,670.4
0.4
PAINT
THINNER
OR
PETROLEUM
DISTILLATES
Already
a
distillation
by­
product
26.6
POLYETHYLENE
AND
POLYVINYLACETATE
WAX
IN
VINYL
ACETATE
FRO
2,319.1
RECOVERED
ORGANICS
­
SPENT
CONTAMINATED
LUBRICATING
OILS,
MI
11.8
SPENT
PARTS
WASHER
SOLVENT
29.5
HEAVY
AROMATIC
HYDROCARBONS
(
ETHYLENE
TARS)

15.2
POLYETHYLENE
ADDITIVE
SLURRY
(
AMINES,
ANTIOXIDENTS
&
AMIDE
4.4
WASTE
PAINT
RELATED
RESIDUES,
EXCESS
PAINT
AND
APPLICATOR
17.7
SPENT
CYCLOHEXANE
WASH
SOLUTION
197.0
SPENT
METHANOL
USED
IN
CLEANING
PROCESS
VESSELS
21.9
RECOVERED,
SPENT
ORGANIC
PEROXIDE
IN
MINERAL
SPIRITS
2.5
OLD/
CONTAMINATED
FUEL
0.2
USED
N­
PROPANOL
PUMP
SEAL
FLUIDS
24.2
SPENT
LABORATORY
SOLVENT
WITH
ANALYTICAL
RESIDUES
MOD985791995
2,158.5
1,437.9
IGNITABLE
SPENT
SOLVENT
FROM
PHARMACEUTICAL
MFG
PROCESS
­
MI
XTURE
OF
METHANOL
AND
TOLUENE
485.6
SPENT
SOLVENT
FROM
PHARMACEUTICAL
MFG
PROCESS
SOLUTION
OF
ME
THYLENE
CHLORIDE
AND
WATER
WITH
ACETONE
234.9
IGNITABLE
SPENT
SOLVENT
FROM
PHARMACEUTICAL
MFG.
PROCESS­
TOL
UENE
KYD082390394
2,002.0
459.5
IGNITABLE,
BARIUM,
CHROMIUM,
LEAD
1,542.5
IGNITABLE,
LEAD,
BARIUM,
MEK,
TOLUENE
MAD980912323
2,947.1
1,111.0
TOXIC
IGNITABLE
SOLVENT
(
ACETONE,
TOLUENE,
BUTANOL,
XYLENE)
GENERATED
FROM
ORGANIC
CHEMICAL
FILTERING
PROCESSING
AND
EQUIPMENT
CLEANING.
3.6
DISTILLATION
STILLBOTTOMS
AND
SPENT
SOLVENT.
CONTAINS
METHYLENE
CHLORIDE
AND
ANILINE.
Already
a
distillation
by­
product
566.1
TOXIC
IGNITABLE
AQUEOUS
SOLUTION
CONTAINS
(
ACETONE,
TOLUENE,
BUTANOL,
METHANOL,
CHLOROBENZENE)
GENERATED
FROM
SITE
AIR
ABATEMENT
EQUIPMENT,

WASTEWATER
CONTROL
EQUIPMENT,
PRODUCT
FILTERING
AND
EQUIPMENT
CLEANOUTS.

783.5
TOXIC
IGNITABLE
AQUEOUS
SOLUTION
CONTAINS
(
ACETONE,
TOLUENE,
BUTANOL,
METHYLENE
CHLORIDE,
METHANOL)
GENERATED
FROM
SITE
AIR
ABATEMENT
EQUIPMENT,
WASTEWATER
CONTROL
EQUIPMENT,
PRODUCT
FILTERING
AND
EQUIPMENT
CLEANOUTS.

48.9
IGNITABLE
SOLVENT
SOLUTION,
BUTANOL
CONTAMINATED
WITH
ETHYL
ACETATE.

150.1
IGNITABLE
AQUEOUS
SOLUTION,
CONTAINS
ISOPROPANOL
GENERATED
FROM
PRODUCT
FILTERING.

20.0
WASTE
SOLVENTS
FROM
DRYER
CONDENSATE
AND
CAPTURED
VENT
OVERHEADS.(
BUTANOL,
ACETONE,
ISOPROPANOL,
CYCLOHEXANE)
GENERATED
FROM
ORGANIC
CHEMICAL
DRYING.
8.7
SPENT
INPROCESS
SOLVENT
WASTE,
(
METHANOL,
TOLUENE,
XYLENE,
ISOPROPANOL,
ETHYL
ACETATE)
GENERATED
FROM
ORGANIC
CHEMICAL
MANUFACTURE.

0.5
WASTE
METHYLENE
CHLORIDE
AND
ISOPROPANOL.
GENERATED
FROM
ORGANIC
CHEMICAL
MANUFACTURING.

0.8
LABORATORY
SOLVENT
WASTE.
GENERATED
IN
QUALITY
AND
RESEARCH
LABORTORIES.

9.4
WASTE
SOLVENTS
FROM
CONTAMINATED
REACTION.
(
BUTANOL,
ETHYL
ACETATE)
GENERATED
WHEN
INPROCESS
REACTION
BECAME
CONTAMINATED
WITH
ETHYL
ACETATE.
0.8
SPENT
IGNITABLE,
CORROSIVE
SOLVENT
USED
IN
VESSEL
CLEANING
(
ACETONE,
HYDROCHLORIC
ACID)
GENERATED
FROM
PROCESS
VESSEL
CLEANING.

0.3
IGNITABLE,
TOXIC
AND
CORROSIVE
CLEANOUT
SOLUTION,
(
ACETONE,
METHYLENE
CHLORIDE,
HYDROCHLORIC
ACID).
GENERATED
FROM
VESSEL
CLEANING.

18.6
SPENT
TOXIC
SOLVENT,
(
METHYLENE
CHLORIDE).
SENT
OFFSITE
FOR
RECOVERY.
GENERATED
FROM
ORGANIC
CHEMICAL
MANUFACTURE.

42.5
DISTILLATION
STILLBOTTOMS
AND
SPENT
SOLVENT.
CONTAINS
ISOPROPANOL
OR
CYCLOHEXANE.
GENERATED
FROM
ONSITE
SOLVENT
RECOVERY.
Already
a
distillation
by­
product
2.4
IGNITABLE
WASTE
OIL,
CONTAMINATED
WITH
CYCLOHEXANE.
GENERATED
FROM
OIL
CHANGES
ON
VACCUM
PUMPS.

1.0
INPROCESS
SOLVENT
SAMPLE
STREAMS
CONTAINING,
METHANOL,
TOLUENE,
ACETONE
OR
ACETIC
ACID.
GENERATED
FROM
SAMPLING
ORGANIC
CHEMICAL
REACTIONS.

6.0
SPENT
SOLVENTS
GENERATED
FROM
PROCESS
CLEANOUTS.
(
METHANOL,
ISOPROPANOL,
BUTANOL)

99.7
DISTILLATION
STILLBOTTOMS
AND
SPENT
SOLVENT.
CONTAINS
METHYLENE
CHLORIDE
AND
PYRIDINE.
Already
a
distillation
by­
product
2.7
SPENT
PROCESS
SOLVENT
(
PROPIONIC
ACID)
GENERATED
IN
ORGANIC
CHEMICAL
MANUFACTURE.

0.2
SPENT
PROCESS
SOLVENT,
(
PROPIONIC
ACID,
M­
CRESOL)
GENERATED
IN
ORGANIC
CHEMICAL
MANUFACTURE.

13.1
SPENT
IGNITABLE,
CORROSIVE,
TOXIC
LIQUID
GENERATED
FROM
DISTILLATION
OF
SOLVENTS
FROM
ORGANIC
CHEMICAL
MANUFACTURING.
CONTAINS
CHLOROBENZENE
AND
HYDROCHLORIC
ACID.
Already
a
distillation
by­
product
57.5
SPENT
IGNITABLE,
TOXIC,
CORROSIVE
LIQUID.
GENERATED
FROM
THE
DISTILLATION
OF
SOLVENTS
IN
ORGANIC
CHEMICAL
MANUFACTURING.
CONTAINS
CHLOROBENZENE,
METHANOL
AND
HYDROCHLORIC
ACID.
Already
a
distillation
by­
product
PAD042259374
1,842.2
1,841.9
WASTE
FLAMMABLE
LIQUID,
HEPTANE/
TOLUENE
SOLUTION
SEPARATED
F
ROM
CAUSTIC
WASH
0.2
WASTE
COMBUSTIBLE
LIQUID,
PETROLEUM
NAPHTHA
USED
AS
A
PARTS
CLEANER
IN
MAINTENANCE
SHOP
TXD980867345
1,804.0
7.1
RESIN
WASTE
­
OFF­
GRADE
NON­
SALABLE
RESIN
USED
IN
FUEL
SUPPL
61.5
MIXED
SOLVENTS
FROM
PROCESS
AID
OF
REACTIONS
­
10,000
GAL.
T
1,735.4
AQUEOUS/
SOLVENT
SOLUTION
­
CHEMICALS/
WASTEWATER
FROM
REACTIO
PAD003008943
1,741.4
9.3
INKS,
DYES,
ALCOHOLS
AND
ADHESIVES
FROM
CONSUMER
HEALTHCARE
PRODUCTS
AND
PHARMAUCEUTICALS
PACKAGING
OPERATIONS
0.8
MIXTURE
CONTAINING
PETROLEUM
NAPHTHA
USED
IN
MACHINERY
PARTS
WASHER
1,695.0
OFF­
SPEC
PRODUCTION
WASTE
CONTAINING
FLAMABLE
LIQUIDS
33.5
ALCOHOLS
MIXTURES
USED
IN
THE
PRODUCTION
OF
CONSUMER
HEALTHC
ARE
PRODUCTS
AND
PHARMACEUTICALS
2.9
OUT­
DATED
OR
EXPIRED
FLAVORINGS
USED
IN
THE
PRODUCTION
OF
CO
NSUMER
HEALTHCARE
PRODUCTS
PRD090346909
1,618.1
IGNITABLE
SPENT
SOLVENT
FROM
THE
PRODUCTION
OF
PHARMACEUTICA
LS
PRODUCT.

LAD003913183
1,491.5
WASTE
FLAMMABLE
LIQUIDS
(
ETHANOL/
PROPANOL)

OHD004282976
1,558.9
1,153.9
WASTE
FLAMMABLE
LIQUID
­
SPENT
SOLVENT
136.3
WASTE
GELLED
ALKYD
RESIN
CONTAINING
NAPHTHA
268.8
WASTE
OFF
SPECIFICATION
SOLVENT
BORNE
PAINT
TXD096037932
1,596.0
956.0
MIXED
ORGANIC
LIQUIDS
WITH
140
F.

637.6
WASTE
ISOBUTANOL
AND
DIOL
0.6
FURFURAL
WASTE
1.8
ISOBUTYRALDEHYDE
WASTE
TXD980625966
1,510.0
1,494.8
RED
OIL
AND
RED
OIL
POLYMER
WITH
HAN
15.1
METHANOL/
PROPANOL
MIXTURE
0.1
DIMETHYL
SULFIDE
GAD075876623
1,569.7
0.0
SPENT
SOLVENT
FROM
QUALITY
CONTROL
TESTING
(
CONTAINS
PYRIDIN
E
AND
DICHLOROMETHANE),
IGNITABLE
AND
TOXIC
6.1
ORGANIC
DEFECTIVE
PAINT,
IGNITABLE,
TOXIC
FOR
METALS
AND
MEK
388.7
DEFECTIVE
SOLVENT
BASED
PAINT
AND
SPENT
SOLVENT
(
IGNITABLE
A
ND
TOXIC­
CONTAINS
METALS
AND
SOLVENT)

1.6
EPOXY
PRIMER,
IGNITABLE
1,173.3
SPENT
SOLVENT
FROM
CLEANING
PAINT
PRODUCTION
EQUIPMENT,
IGNI
TABLE
AND
TOXIC
TXD008088833
1,574.2
0.7
MIXED
LIQUID
LABORATORY
WASTE
FROMTECHNICAL
LABORATORY
ACTIV
37.9
POLYMER
BLOWDOWN
CONAINING
SOLVENT.
INITIAL
GENERATION
1996
1,497.1
SPENT
NON­
HALOGENATED
SOLVENT
FROM
LOW
DENSITY
POLYETHYLENE
0.2
HALOGENATED
LABORATORY
SOLVENT
FROM
QUALITY
CONTROL
LABORATO
0.4
QUALITY
CONTROL
LABORATORY
WASTE.
FIRST
GENERATED
1980.

1.7
PILOT
PLANT
WASTE
SOLVENT
GENERATED
DURING
POLYETHYLENE
5.0
PLANT
DEGREASER,
HAZARDOUS
LIQUID.
MAINTENANCE
PARTS
WASHER
1.3
PAINT
THINNER,
CHLOROBENZENE.

0.5
SP
SOLVENT/
MONOMER/
AND
ADDITIVES
29.4
SPECIALTY
POLYMER
WASTE
INACTIVE
CATALYST.
GENERATED
DURING
0.1
POLYARD,
HAZARDOUS,
LIQUID,
RESIDUE
FROM
LOW
DENSITY
POLYETH
TXD008088247
1,550.6
31.2
BCHLOR
WASH
WATER
18.7
DIOL
WASTE
FROM
THE
MANUFACTURE
AND
PURIFICATION
OF
DIOL
PRO
919.2
DBE
REACTOR
BOTTOMS
/
MANUFACTURE
OF
DIBASIC
ESTERS
562.4
REACTOR
WASH
SOLUTION
/
PROCESS
EQUIPMENT
CLEANING
/
FEB.
19
0.2
OTHER
ORGANIC
LIQUIDS
0.2
LIQUID
WASTE
FROM
THE
MANUFACTURE
OF
SIMA.

0.7
BENZYL
CHLORIDE
WASTES
18.0
AQUEOUS
REACTOR
WASH
SOLUTION
CAD070635669
1,266.5
FLAMMABLE
SPENT
SOLVENT
FROM
THE
MANUFACTURING
OF
BULK
PHARMACEUTICALS
WHICH
INCLUDE
A
MIXTURE
OF
TOLUENE,
METHANOL
ISOPROPYL
ALCOHOL,
ETHYL
ACETATE
AND
ETHANOL
LAD098168206
1,259.0
HEAVY
ENDS/
OFF­
SPEC
PRODUCT
FROM
PRODUCTION
OF
ETHYLENE
DICH
LORIDE
BY
"
DIRECT
CHLORINATION"
PROCESS,
EDC,
1,1,2­
TRICHLOR
OETHYLENE,

BIS­
2
CHLOROETHYL
ETHER
TXD065096273
1,677.9
24.6
OFF
SPECIFICATION
BUTYL
ACRYLATE
0.1
LIGHT
ENDS
FROM
BUTYL
METHACRYLATE/
ISO­
BUTYL
METHACRYLATE
PR
1.9
IMMERSION
SOLVENT
USED
IN
SAFETY
KLEEN
PARTS
WASHERS
3.0
PAINT/
THINNER
MIXTURES.
GENERATED
FROM
PAINTING
AND
MAINTEN
865.5
81R
RESIDUE.
MANUFACTURING
WASTE
FROM
THE
PRODUCTION
OF
81R
49.0
METHYL
METHACRYLATE,
OFF
SPEC
PRODUCT.

455.5
B­
3
LIGHT
ENDS.
MANUFACTURING
BYPRODUCT
OF
MMA
AND
MAA
PROD
11.7
OFF
SPEC
METHACRYLIC
ACID
PRODUCT
17.1
METHYL
METHACRYLATE
TANK
WASHINGS
AND
DISCHARGES.
FROM
CRUD
0.0
SAFETY
KLEEN
SOLVENT,
USED
IN
DEGREASING
OPERATIONS
AND
PART
226.0
BMA
BLEED
STRIPPER
BOTTOMS.
MANUFACTURING
WASTE
FROM
THE
PR
23.3
ACETIC
ACID,
COPRODUCT
OF
ACRYLIC
ACID
PRODUCTION.
DISCARDE
WVD005005483
1,823.8
385.3
IGNITABLE
MATERIAL
FROM
UNIT
PRODUCTION
(
PVA/
IPA
STREAM)

0.2
DISCARDED
RAW
MATERIAL
CYCLOHEXANONE.

440.6
IGNITABLE
RESIDUES
CONTAINING
CHROMIUM
FROM
UNIT
PRODUCTION
(
CBM
RESIDUES).

1.8
MISCELLANEOUS
IGNITABLE
ORGANIC
MATERIALS
FROM
PLANT
LABORAT
ORY.

6.2
PAINT
WASTE
CONTAINING
VARIOUS
SOLVENTS.

368.9
IGNITABLE
MATERIAL
FROM
PRODUCTION
(
PVA
RESIDUES).

2.1
MISCELLANEOUS
IGNITABLE
OUT­
OF­
DATE
PRODUCTS.

49.1
IGNITABLE
RESIDUES
FROM
PRODUCTION
OF
DIENE
299
CONTAINING
A
LCOHOLS.

414.1
IGNITABLE
RESIDUES
CONTAINING
BENZENE
FROM
UNIT
PRODUCTION
(
MVA
RESIDUES).

18.4
IGNITABLE
MATERIAL
FROM
UNIT
PRODUCTION
(
PVA
LA­
1
WASTE).

42.6
IGNITABLE
RESIDUES
CONTAINING
BENZENE
AND
METHYL
ETHYL
KETO
NE
FROM
UNIT
PRODUCTION
(
ACETONE
RECOVERY).

55.0
FLAMMABLE
WASTE
FROM
OVERHEAD
STRIP;
MIXTURE
CONTAINS
ISOPRO
PANOL
AND
VINYL
ETHYL
ETHER.

39.6
IGNITABLE
RESIDUES
CONTAINING
BENZENE
AND
METHYL
ETHYL
KETON
E
FROM
UNIT
PRODUCTION
(
MVA
RESIDUES).