*
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342
For
the
reasons
set
out
in
the
preamble,
title
40,
chapter
I,
of
the
Code
of
Federal
Regulations
is
proposed
to
be
amended
as
follows:

PART
63
 
NATIONAL
EMISSION
STANDARDS
FOR
HAZARDOUS
AIR
POLLUTANTS
FOR
SOURCE
CATEGORIES
1.
The
authority
citation
for
part
63
continues
to
read
as
follows:
Authority:
42
U.
S.
C.
7401
et
seq.
2.
The
table
of
contents
of
part
63,
subpart
EEE,
is
amended
by
revising
to
read
as
follows:
Subpart
EEE
 
National
Emission
Standards
for
Hazardous
Air
Pollutants
from
Hazardous
Waste
Combustors
GENERAL
Sec.
63.1200
Who
is
subject
to
these
regulations?
63.1201
Definitions
and
acronyms
used
in
this
subpart.
63.1202
[
Reserved]

EMISSIONS
STANDARDS
AND
OPERATING
LIMITS
FOR
INCINERATORS,
CEMENT
KILNS,
AND
LIGHTWEIGHT
AGGREGATE
KILNS
63.1203
What
are
the
standards
for
hazardous
waste
incinerators?
63.1203A
What
are
the
replacement
standards
for
hazardous
waste
incinerators?
63.1204
What
are
the
standards
for
hazardous
waste
burning
cement
kilns?
63.1204A
What
are
the
replacement
standards
for
hazardous
waste
burning
cement
kilns?
63.1205
What
are
the
standards
for
hazardous
waste
burning
lightweight
aggregate
kilns?
63.1205A
What
are
the
replacement
standards
for
hazardous
waste
burning
lightweight
aggregate
kilns?

MONITORING
AND
COMPLIANCE
PROVISIONS
63.1206
When
and
how
must
you
comply
with
the
standards
and
operating
requirements?
63.1207
What
are
the
performance
testing
requirements?
63.1208
What
are
the
test
methods?
63.1209
What
are
the
monitoring
requirements?

NOTIFICATION,
REPORTING
AND
RECORDKEEPING
63.1210
What
are
the
notification
requirements?
63.1211
What
are
the
recordkeeping
and
reporting
requirements?
63.1212
What
are
the
other
requirements
pertaining
to
the
NIC
and
associated
progress
reports?

OTHER
63.1213
How
can
the
compliance
date
be
extended
to
install
pollution
prevention
or
waste
minimization
controls?
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343
63.1214
Implementation
and
enforcement.
63.1215
What
are
the
alternative
risk­
based
standards
for
hydrogen
chloride
and
chlorine
gas?

EMISSIONS
STANDARDS
AND
OPERATING
LIMITS
FOR
SOLID
FUEL­
FIRED
BOILERS,
LIQUID
FUEL­
FIRED
BOILERS,
AND
HYDROCHLORIC
ACID
PRODUCTION
FURNANCES
63.1216
What
are
the
standards
for
solid
fuel­
fired
boilers?
63.1217
What
are
the
standards
for
liquid
fuel­
fired
boilers?
63.1218
What
are
the
standards
for
hydrochloric
acid
production
furnaces?

TABLE
1
TO
SUBPART
EEE
OF
PART
63
 
GENERAL
PROVISIONS
APPLICABLE
TO
SUBPART
EEE
APPENDIX
A
TO
SUBPART
EEE
 
QUALITY
ASSURANCE
PROCEDURES
FOR
CONTINUOUS
EMISSIONS
MONITORS
USED
FOR
HAZARDOUS
WASTE
COMBUSTORS
3.
Section
63.1200
is
amended
by
revising
the
introductory
text
and
paragraph
(
a)(
2)
to
read
as
follows:
§
63.1200
Who
is
subject
to
these
regulations?
The
provisions
of
this
subpart
apply
to
all
hazardous
waste
combustors:
incinerators
that
burn
hazardous
waste,
cement
kilns
that
burn
hazardous
waste,
lightweight
aggregate
kilns
that
burn
hazardous
waste,
solid
fuel­
fired
boilers
that
burn
hazardous
waste,
liquid
fuel­
fired
boilers
that
burn
hazardous
waste,
and
hydrochloric
acid
production
furnaces
that
burn
hazardous
waste.
Hazardous
waste
combustors
are
also
subject
to
applicable
requirements
under
parts
260­
270
of
this
chapter.
(
a)
*
*
*
(
2)
Both
area
sources
and
major
sources
subject
to
this
subpart,
but
not
previously
subject
to
title
V,
are
immediately
subject
to
the
requirement
to
apply
for
and
obtain
a
title
V
permit
in
all
States,
and
in
areas
covered
by
part
71
of
this
chapter.
*
*
*
*
*

4.
Section
63.201
is
amended
by
revising
the
definition
of
"
New
source",
and
adding
the
definition
of
"
Hydrochloric
acid
production
furnace",
"
Liquid
fuel­
fired
boiler",
and
"
Solid
fuelfired
boiler"
to
paragraph
(
a)
in
alphabetical
order
to
read
as
follows:
§
63.1201
Definitions
and
acronyms
used
in
this
subpart.
(
a)
*
*
*
Hydrochloric
acid
production
furnace
and
HCl
production
furnace
mean
a
halogen
acid
furnace
defined
in
§
260.10
of
this
chapter
that
produces
aqueous
hydrochloric
acid
(
HCl)
product
and
that
burns
hazardous
waste
at
any
time.
*
*
*
*
*
Liquid
fuel­
fired
boiler
and
liquid
boiler
mean
a
boiler
defined
in
§
260.10
of
this
chapter
*
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344
that
does
not
burn
solid
fuels
and
that
burns
hazardous
waste
at
any
time.
Liquid
fuel­
fired
boiler
includes
boilers
that
only
burn
gaseous
fuels.
*
*
*
*
*
New
source
means
any
affected
source
the
construction
or
reconstruction
of
which
is
commenced
after
the
dates
specified
under
§
§
63.1206(
a)(
1)(
i)(
B),
(
a)(
1)(
ii)(
B),
and
(
a)(
2)(
ii).
*
*
*
*
*
Solid
fuel­
fired
boiler
and
solid
boiler
mean
a
boiler
defined
in
§
260.10
of
this
chapter
that
burns
a
solid
fuel
and
that
burns
hazardous
waste
at
any
time.
*
*
*
*
*
5.
Section
63.1203A
is
added
to
read
as
follows:
§
63.1203A
What
are
the
replacement
standards
for
hazardous
waste
incinerators?
(
a)
Emission
limits
for
existing
sources.
You
must
not
discharge
or
cause
combustion
gases
to
be
emitted
into
the
atmosphere
that
contain:
(
1)(
i)
Dioxin
and
furan
in
excess
of
0.28
ng
TEQ/
dscm
corrected
to
7
percent
oxygen
for
incinerators
equipped
with
either
a
waste
heat
boiler
or
dry
air
pollution
control
system;
or
(
ii)
Dioxin
and
furan
in
excess
of
0.40
ng
TEQ/
dscm
corrected
to
7
percent
oxygen
for
sources
not
equipped
with
either
a
waste
heat
boiler
or
dry
air
pollution
control
system;
(
iii)
A
source
equipped
a
wet
air
pollution
control
system
followed
by
a
dry
air
pollution
control
system
is
not
considered
to
be
a
dry
air
pollution
control
system,
and
a
source
equipped
with
a
dry
air
pollution
control
system
followed
a
wet
air
pollution
control
system
is
considered
to
be
a
dry
air
pollution
control
system
for
purposes
of
this
emission
limit;
(
2)
Mercury
in
excess
of
130
ug/
dscm
corrected
to
7
percent
oxygen;
(
3)
Cadmium
and
lead
in
excess
of
59
ug/
dscm,
combined
emissions,
corrected
to
7
percent
oxygen;
(
4)
Arsenic,
beryllium,
and
chromium
in
excess
of
84
ug/
dscm,
combined
emissions,
corrected
to
7
percent
oxygen;
(
5)
For
carbon
monoxide
and
hydrocarbons,
either:
(
i)
Carbon
monoxide
in
excess
of
100
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis
and
corrected
to
7
percent
oxygen.
If
you
elect
to
comply
with
this
carbon
monoxide
standard
rather
than
the
hydrocarbon
standard
under
paragraph
(
a)(
5)(
ii)
of
this
section,
you
must
also
document
that,
during
the
destruction
and
removal
efficiency
(
DRE)
test
runs
or
their
equivalent
as
provided
by
§
63.1206(
b)(
7),
hydrocarbons
do
not
exceed
10
parts
per
million
by
volume
during
those
runs,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
or
(
ii)
Hydrocarbons
in
excess
of
10
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
(
6)
Hydrogen
chloride
and
chlorine
gas
(
total
chlorine)
in
excess
of
1.5
parts
per
million
by
volume,
combined
emissions,
expressed
as
a
chloride
(
Cl(­))
equivalent,
dry
basis
and
corrected
to
7
percent
oxygen;
and
(
7)
Except
as
provided
by
paragraph
(
e)(
2),
particulate
matter
in
excess
of
34
mg/
dscm
*
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345
corrected
to
7
percent
oxygen.
(
b)
Emission
limits
for
new
sources.
You
must
not
discharge
or
cause
combustion
gases
to
be
emitted
into
the
atmosphere
that
contain:
(
1)(
i)
Dioxin
and
furans
in
excess
of
0.11
ng
TEQ/
dscm
corrected
to
7
percent
oxygen
for
incinerators
equipped
with
either
a
waste
heat
boiler
or
dry
air
pollution
control
system;
or
(
ii)
Dioxin
and
furans
in
excess
of
0.20
ng
TEQ/
dscm
corrected
to
7
percent
oxygen
for
sources
not
equipped
with
either
a
waste
heat
boiler
or
dry
air
pollution
control
system;
(
iii)
A
source
equipped
a
wet
air
pollution
control
system
followed
by
a
dry
air
pollution
control
system
is
not
considered
to
be
a
dry
air
pollution
control
system,
and
a
source
equipped
with
a
dry
air
pollution
control
system
followed
a
wet
air
pollution
control
system
is
considered
to
be
a
dry
air
pollution
control
system
for
purposes
of
this
standard;
(
2)
Mercury
in
excess
of
8
ug/
dscm
corrected
to
7
percent
oxygen;
(
3)
Cadmium
and
lead
in
excess
of
6.5
ug/
dscm,
combined
emissions,
corrected
to
7
percent
oxygen;
(
4)
Arsenic,
beryllium,
and
chromium
in
excess
of
8.9
ug/
dscm,
combined
emissions,
corrected
to
7
percent
oxygen;
(
5)
For
carbon
monoxide
and
hydrocarbons,
either:
(
i)
Carbon
monoxide
in
excess
of
100
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis
and
corrected
to
7
percent
oxygen.
If
you
elect
to
comply
with
this
carbon
monoxide
standard
rather
than
the
hydrocarbon
standard
under
paragraph
(
b)(
5)(
ii)
of
this
section,
you
must
also
document
that,
during
the
destruction
and
removal
efficiency
(
DRE)
test
runs
or
their
equivalent
as
provided
by
§
63.1206(
b)(
7),
hydrocarbons
do
not
exceed
10
parts
per
million
by
volume
during
those
runs,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
or
(
ii)
Hydrocarbons
in
excess
of
10
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
(
6)
Hydrogen
chloride
and
chlorine
gas
in
excess
of
0.18
parts
per
million
by
volume,
combined
emissions,
expressed
as
a
chloride
(
Cl(­))
equivalent,
dry
basis
and
corrected
to
7
percent
oxygen;
and
(
7)
Except
as
provided
by
paragraph
(
e)(
3),
particulate
matter
in
excess
of
1.6
mg/
dscm
corrected
to
7
percent
oxygen.
(
c)
Destruction
and
removal
efficiency
(
DRE)
standard.
(
1)
99.99%
DRE.
Except
as
provided
in
paragraph
(
c)(
2)
of
this
section,
you
must
achieve
a
destruction
and
removal
efficiency
(
DRE)
of
99.99%
for
each
principle
organic
hazardous
constituent
(
POHC)
designated
under
paragraph
(
c)(
3)
of
this
section.
You
must
calculate
DRE
for
each
POHC
from
the
following
equation:
DRE
=
[
1
­
(
W
out
/
W
in)]
x
100%
Where:
W
in
=
mass
feedrate
of
one
POHC
in
a
waste
feedstream;
and
W
out
=
mass
emission
rate
of
the
same
POHC
present
in
exhaust
emissions
prior
to
release
to
the
*
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346
atmosphere.
(
2)
99.9999%
DRE.
If
you
burn
the
dioxin­
listed
hazardous
wastes
F020,
F021,
F022,
F023,
F026,
or
F027
(
see
§
261.31
of
this
chapter),
you
must
achieve
a
DRE
of
99.9999%
for
each
POHC
that
you
designate
under
paragraph
(
c)(
3)
of
this
section.
You
must
demonstrate
this
DRE
performance
on
POHCs
that
are
more
difficult
to
incinerate
than
tetra­,
penta­,
and
hexachlorodibenzo­
p­
dioxins
and
dibenzofurans.
You
must
use
the
equation
in
paragraph
(
c)(
1)
of
this
section
to
calculate
DRE
for
each
POHC.
In
addition,
you
must
notify
the
Administrator
of
your
intent
to
incinerate
hazardous
wastes
F020,
F021,
F022,
F023,
F026,
or
F027.
(
3)
Principal
organic
hazardous
constituent
(
POHC).
(
i)
You
must
treat
each
POHC
in
the
waste
feed
that
you
specify
under
paragraph
(
c)(
3)(
ii)
of
this
section
to
the
extent
required
by
paragraphs
(
c)(
1)
and
(
c)(
2)
of
this
section.
(
ii)
You
must
specify
one
or
more
POHCs
from
the
list
of
hazardous
air
pollutants
established
by
42
U.
S.
C.
7412(
b)(
1),
excluding
caprolactam
(
CAS
number
105602)
as
provided
by
§
63.60,
for
each
waste
to
be
burned.
You
must
base
this
specification
on
the
degree
of
difficulty
of
incineration
of
the
organic
constituents
in
the
waste
and
on
their
concentration
or
mass
in
the
waste
feed,
considering
the
results
of
waste
analyses
or
other
data
and
information.
(
d)
Significant
figures.
The
emission
limits
provided
by
paragraphs
(
a)
and
(
b)
of
this
section
are
presented
with
two
significant
figures.
Although
you
must
perform
intermediate
calculations
using
at
least
three
significant
figures,
you
may
round
the
resultant
emission
levels
to
two
significant
figures
to
document
compliance.
(
e)
Alternative
to
the
particulate
matter
standard
for
incinerators.
(
i)
General.
In
lieu
of
complying
with
the
applicable
particulate
matter
standards
of
paragraphs
(
a)(
7)
and
(
b)(
7)
of
this
section,
you
may
elect
to
comply
with
the
following
alternative
metal
emission
control
requirements:
(
ii)
Alternative
metal
emission
control
requirements
for
existing
sources.
(
A)
You
must
not
discharge
or
cause
combustion
gases
to
be
emitted
into
the
atmosphere
that
contain
cadmium,
lead,
and
selenium
in
excess
of
59
ug/
dscm,
combined
emissions,
corrected
to
7
percent
oxygen;
and,
(
B)
You
must
not
discharge
or
cause
combustion
gases
to
be
emitted
into
the
atmosphere
that
contain
antimony,
arsenic,
beryllium,
chromium,
cobalt,
manganese,
and
nickel
in
excess
of
84
ug/
dscm,
combined
emissions,
corrected
to
7
percent
oxygen.
(
iii)
Alternative
metal
emission
control
requirements
for
new
sources.
(
A)
You
must
not
discharge
or
cause
combustion
gases
to
be
emitted
into
the
atmosphere
that
contain
cadmium,
lead,
and
selenium
in
excess
of
6.5/
dscm,
combined
emissions,
corrected
to
7
percent
oxygen;
and,
(
B)
You
must
not
discharge
or
cause
combustion
gases
to
be
emitted
into
the
atmosphere
that
contain
antimony,
arsenic,
beryllium,
chromium,
cobalt,
manganese,
and
nickel
in
excess
of
8.9
ug/
dscm,
combined
emissions,
corrected
to
7
percent
oxygen.
6.
Section
63.1204A
is
added
to
read
as
follows:
§
63.1204A
What
are
the
replacement
standards
for
hazardous
waste
burning
cement
kilns?
(
a)
Emission
limits
for
existing
sources.
You
must
not
discharge
or
cause
combustion
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347
gases
to
be
emitted
into
the
atmosphere
that
contain:
(
1)(
i)
Dioxin
and
furan
in
excess
of
0.20
ng
TEQ/
dscm
corrected
to
7
percent
oxygen;
or
(
ii)
Dioxin
and
furan
in
excess
of
0.40
ng
TEQ/
dscm
corrected
to
7
percent
oxygen
provided
that
the
combustion
gas
temperature
at
the
inlet
to
the
initial
dry
particulate
matter
control
device
is
400
°
F
or
lower
based
on
the
average
of
the
test
run
average
temperatures;
(
2)
Mercury
in
excess
of
64
ug/
dscm
corrected
to
7
percent
oxygen;
(
3)
In
excess
of
4.0
x
10­
4
lbs
combined
emissions
of
cadmium
and
lead
attributable
to
the
hazardous
waste
per
million
British
thermal
unit
heat
input
from
the
hazardous
waste;
(
4)
In
excess
of
1.4
x
10­
5
lbs
combined
emissions
of
arsenic,
beryllium,
and
chromium
attributable
to
the
hazardous
waste
per
million
British
thermal
unit
heat
input
from
the
hazardous
waste;
(
5)
Carbon
monoxide
and
hydrocarbons.
(
i)
For
kilns
equipped
with
a
by­
pass
duct
or
midkiln
gas
sampling
system,
either:
(
A)
Carbon
monoxide
in
the
by­
pass
duct
or
mid­
kiln
gas
sampling
system
in
excess
of
100
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis
and
corrected
to
7
percent
oxygen.
If
you
elect
to
comply
with
this
carbon
monoxide
standard
rather
than
the
hydrocarbon
standard
under
paragraph
(
a)(
5)(
i)(
B)
of
this
section,
you
must
also
document
that,
during
the
destruction
and
removal
efficiency
(
DRE)
test
runs
or
their
equivalent
as
provided
by
§
63.1206(
b)(
7),
hydrocarbons
in
the
by­
pass
duct
or
mid­
kiln
gas
sampling
system
do
not
exceed
10
parts
per
million
by
volume
during
those
runs,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
or
(
B)
Hydrocarbons
in
the
by­
pass
duct
or
midkiln
gas
sampling
system
in
excess
of
10
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
(
ii)
For
kilns
not
equipped
with
a
by­
pass
duct
or
midkiln
gas
sampling
system,
either:
(
A)
Hydrocarbons
in
the
main
stack
in
excess
of
20
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
or
(
B)
Carbon
monoxide
in
the
main
stack
in
excess
of
100
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis
and
corrected
to
7
percent
oxygen.
If
you
elect
to
comply
with
this
carbon
monoxide
standard
rather
than
the
hydrocarbon
standard
under
paragraph
(
a)(
5)(
ii)(
A)
of
this
section,
you
also
must
document
that,
during
the
destruction
and
removal
efficiency
(
DRE)
test
runs
or
their
equivalent
as
provided
by
§
63.1206(
b)(
7),
hydrocarbons
in
the
main
stack
do
not
exceed
20
parts
per
million
by
volume
during
those
runs,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane.
(
6)
Hydrogen
chloride
and
chlorine
gas
in
excess
of
110
parts
per
million
by
volume,
combined
emissions,
expressed
as
a
chloride
(
Cl(­))
equivalent,
dry
basis,
corrected
to
7
percent
oxygen;
and
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(
7)
Particulate
matter
in
excess
of
65
mg/
dscm
corrected
to
7
percent
oxygen.
(
b)
Emission
limits
for
new
sources.
You
must
not
discharge
or
cause
combustion
gases
to
be
emitted
into
the
atmosphere
that
contain:
(
1)(
i)
Dioxin
and
furan
in
excess
of
0.20
ng
TEQ/
dscm
corrected
to
7
percent
oxygen;
or
(
ii)
Dioxin
and
furan
in
excess
of
0.40
ng
TEQ/
dscm
corrected
to
7
percent
oxygen
provided
that
the
combustion
gas
temperature
at
the
inlet
to
the
initial
dry
particulate
matter
control
device
is
400
°
F
or
lower
based
on
the
average
of
the
test
run
average
temperatures;
(
2)
Mercury
in
excess
of
35
ug/
dscm
corrected
to
7
percent
oxygen;
(
3)
In
excess
of
6.2
x
10­
5
lbs
combined
emissions
of
cadmium
and
lead
attributable
to
the
hazardous
waste
per
million
British
thermal
unit
heat
input
from
the
hazardous
waste;
(
4)
In
excess
of
1.4
x
10­
5
lbs
combined
emissions
of
arsenic,
beryllium,
and
chromium
attributable
to
the
hazardous
waste
per
million
British
thermal
unit
heat
input
from
the
hazardous
waste;
(
5)
Carbon
monoxide
and
hydrocarbons.
(
i)
For
kilns
equipped
with
a
by­
pass
duct
or
midkiln
gas
sampling
system,
carbon
monoxide
and
hydrocarbons
emissions
are
limited
in
both
the
bypass
duct
or
midkiln
gas
sampling
system
and
the
main
stack
as
follows:
(
A)
Emissions
in
the
by­
pass
or
midkiln
gas
sampling
system
are
limited
to
either:
(
1)
Carbon
monoxide
in
excess
of
100
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis
and
corrected
to
7
percent
oxygen.
If
you
elect
to
comply
with
this
carbon
monoxide
standard
rather
than
the
hydrocarbon
standard
under
paragraph
(
b)(
5)(
i)(
A)(
2)
of
this
section,
you
also
must
document
that,
during
the
destruction
and
removal
efficiency
(
DRE)
test
runs
or
their
equivalent
as
provided
by
§
63.1206(
b)(
7),
hydrocarbons
do
not
exceed
10
parts
per
million
by
volume
during
those
runs,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
or
(
2)
Hydrocarbons
in
the
by­
pass
duct
or
midkiln
gas
sampling
system
in
excess
of
10
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
and
(
B)
Hydrocarbons
in
the
main
stack
are
limited,
if
construction
of
the
kiln
commenced
after
April
19,
1996
at
a
plant
site
where
a
cement
kiln
(
whether
burning
hazardous
waste
or
not)
did
not
previously
exist,
to
50
parts
per
million
by
volume,
over
a
30­
day
block
average
(
monitored
continuously
with
a
continuous
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane.
(
ii)
For
kilns
not
equipped
with
a
by­
pass
duct
or
midkiln
gas
sampling
system,
hydrocarbons
and
carbon
monoxide
are
limited
in
the
main
stack
to
either:
(
A)
Hydrocarbons
not
exceeding
20
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
or
(
B)(
1)
Carbon
monoxide
not
exceeding
100
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
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349
basis,
corrected
to
7
percent
oxygen;
and
(
2)
Hydrocarbons
not
exceeding
20
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane
at
any
time
during
the
destruction
and
removal
efficiency
(
DRE)
test
runs
or
their
equivalent
as
provided
by
§
63.1206(
b)(
7);
and
(
3)
If
construction
of
the
kiln
commenced
after
April
19,
1996
at
a
plant
site
where
a
cement
kiln
(
whether
burning
hazardous
waste
or
not)
did
not
previously
exist,
hydrocarbons
are
limited
to
50
parts
per
million
by
volume,
over
a
30­
day
block
average
(
monitored
continuously
with
a
continuous
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane.
(
6)
Hydrogen
chloride
and
chlorine
gas
in
excess
of
78
parts
per
million,
combined
emissions,
expressed
as
a
chloride
(
Cl(­))
equivalent,
dry
basis
and
corrected
to
7
percent
oxygen;
and
(
7)
Particulate
matter
in
excess
of
13
mg/
dscm
corrected
to
7
percent
oxygen.
(
c)
Destruction
and
removal
efficiency
(
DRE)
standard.
(
1)
99.99%
DRE.
Except
as
provided
in
paragraph
(
c)(
2)
of
this
section,
you
must
achieve
a
destruction
and
removal
efficiency
(
DRE)
of
99.99%
for
each
principle
organic
hazardous
constituent
(
POHC)
designated
under
paragraph
(
c)(
3)
of
this
section.
You
must
calculate
DRE
for
each
POHC
from
the
following
equation:
DRE
=
[
1
­
(
W
out
/
W
in)]
x
100%
Where:
W
in
=
mass
feedrate
of
one
POHC
in
a
waste
feedstream;
and
W
out
=
mass
emission
rate
of
the
same
POHC
present
in
exhaust
emissions
prior
to
release
to
the
atmosphere.
(
2)
99.9999%
DRE.
If
you
burn
the
dioxin­
listed
hazardous
wastes
F020,
F021,
F022,
F023,
F026,
or
F027
(
see
§
261.31
of
this
chapter),
you
must
achieve
a
DRE
of
99.9999%
for
each
POHC
that
you
designate
under
paragraph
(
c)(
3)
of
this
section.
You
must
demonstrate
this
DRE
performance
on
POHCs
that
are
more
difficult
to
incinerate
than
tetra­,
penta­,
and
hexachlorodibenzo­
p­
dioxins
and
dibenzofurans.
You
must
use
the
equation
in
paragraph
(
c)(
1)
of
this
section
to
calculate
DRE
for
each
POHC.
In
addition,
you
must
notify
the
Administrator
of
your
intent
to
incinerate
hazardous
wastes
F020,
F021,
F022,
F023,
F026,
or
F027.
(
3)
Principal
organic
hazardous
constituent
(
POHC).
(
i)
You
must
treat
each
POHC
in
the
waste
feed
that
you
specify
under
paragraph
(
c)(
3)(
ii)
of
this
section
to
the
extent
required
by
paragraphs
(
c)(
1)
and
(
c)(
2)
of
this
section.
(
ii)
You
must
specify
one
or
more
POHCs
from
the
list
of
hazardous
air
pollutants
established
by
42
U.
S.
C.
7412(
b)(
1),
excluding
caprolactam
(
CAS
number
105602)
as
provided
by
§
63.60,
for
each
waste
to
be
burned.
You
must
base
this
specification
on
the
degree
of
difficulty
of
incineration
of
the
organic
constituents
in
the
waste
and
on
their
concentration
or
mass
in
the
waste
feed,
considering
the
results
of
waste
analyses
or
other
data
and
information.
(
d)
Cement
kilns
with
in­
line
kiln
raw
mills.
The
provisions
of
§
63.1204(
d)
apply.
(
1)
General.
(
i)
You
must
conduct
performance
testing
when
the
raw
mill
is
on­
line
and
when
the
mill
is
off­
line
to
demonstrate
compliance
with
the
emission
standards,
and
you
must
establish
separate
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350
operating
parameter
limits
under
§
63.1209
for
each
mode
of
operation,
except
as
provided
by
paragraph
(
d)(
1)(
iv)
of
this
section.
(
ii)
You
must
document
in
the
operating
record
each
time
you
change
from
one
mode
of
operation
to
the
alternate
mode
and
begin
complying
with
the
operating
parameter
limits
for
that
alternate
mode
of
operation.
(
iii)
You
must
establish
rolling
averages
for
the
operating
parameter
limits
anew
(
i.
e.,
without
considering
previous
recordings)
when
you
begin
complying
with
the
operating
limits
for
the
alternate
mode
of
operation.
(
iv)
If
your
in­
line
kiln
raw
mill
has
dual
stacks,
you
may
assume
that
the
dioxin/
furan
emission
levels
in
the
by­
pass
stack
and
the
operating
parameter
limits
determined
during
performance
testing
of
the
by­
pass
stack
when
the
raw
mill
is
off­
line
are
the
same
as
when
the
mill
is
on­
line.
(
2)
Emissions
averaging.
You
may
comply
with
the
mercury,
semivolatile
metal,
low
volatile
metal,
and
hydrochloric
acid/
chlorine
gas
emission
standards
on
a
time­
weighted
average
basis
under
the
following
procedures:
(
i)
Averaging
methodology.
You
must
calculate
the
time­
weighted
average
emission
concentration
with
the
following
equation:
C
total
=
{
C
mill­
off
x
(
T
mill­
off
/(
T
mill­
off
+
T
mill­
on
))}
+
{
C
mill­
on
x
(
T
mill­
on
/(
T
mill­
off
+
T
mill­
on
))}
Where:
C
total
=
time­
weighted
average
concentration
of
a
regulated
constituent
considering
both
raw
mill
on
time
and
off
time;
C
mill­
off
=
average
performance
test
concentration
of
regulated
constituent
with
the
raw
mill
offline
C
mill­
on
=
average
performance
test
concentration
of
regulated
constituent
with
the
raw
mill
online
T
mill­
off
=
time
when
kiln
gases
are
not
routed
through
the
raw
mill;
and
T
mill­
on
=
time
when
kiln
gases
are
routed
through
the
raw
mill.
(
ii)
Compliance.
(
A)
If
you
use
this
emission
averaging
provision,
you
must
document
in
the
operating
record
compliance
with
the
emission
standards
on
an
annual
basis
by
using
the
equation
provided
by
paragraph
(
d)(
2)
of
this
section.
(
B)
Compliance
is
based
on
one­
year
block
averages
beginning
on
the
day
you
submit
the
initial
notification
of
compliance.
(
iii)
Notification.
(
A)
If
you
elect
to
document
compliance
with
one
or
more
emission
standards
using
this
emission
averaging
provision,
you
must
notify
the
Administrator
in
the
initial
comprehensive
performance
test
plan
submitted
under
§
63.1207(
e).
(
B)
You
must
include
historical
raw
mill
operation
data
in
the
performance
test
plan
to
estimate
future
raw
mill
down­
time
and
document
in
the
performance
test
plan
that
estimated
emissions
and
estimated
raw
mill
down­
time
will
not
result
in
an
exceedance
of
an
emission
standard
on
an
annual
basis.
(
C)
You
must
document
in
the
notification
of
compliance
submitted
under
§
63.1207(
j)
that
an
emission
standard
will
not
be
exceeded
based
on
the
documented
emissions
from
the
performance
test
and
predicted
raw
mill
down­
time.
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351
(
e)
Preheater
or
preheater/
precalciner
kilns
with
dual
stacks.
(
1)
General.
You
must
conduct
performance
testing
on
each
stack
to
demonstrate
compliance
with
the
emission
standards,
and
you
must
establish
operating
parameter
limits
under
§
63.1209
for
each
stack,
except
as
provided
by
paragraph
(
d)(
1)(
iv)
of
this
section
for
dioxin/
furan
emissions
testing
and
operating
parameter
limits
for
the
by­
pass
stack
of
in­
line
raw
mills.
(
2)
Emissions
averaging.
You
may
comply
with
the
mercury,
semivolatile
metal,
low
volatile
metal,
and
hydrochloric
acid/
chlorine
gas
emission
standards
specified
in
this
section
on
a
gas
flowrate­
weighted
average
basis
under
the
following
procedures:
(
i)
Averaging
methodology.
You
must
calculate
the
gas
flowrate­
weighted
average
emission
concentration
using
the
following
equation:
C
tot
=
{
C
main
x
(
Q
main
/(
Q
main
+
Q
bypass))}
+
{
C
bypass
x
(
Q
bypass
/
(
Q
main
+
Q
bypass))}
Where:
C
tot
=
gas
flowrate­
weighted
average
concentration
of
the
regulated
constituent;
C
main
=
average
performance
test
concentration
demonstrated
in
the
main
stack;
C
bypass
=
average
performance
test
concentration
demonstrated
in
the
bypass
stack;
Q
main
=
volumetric
flowrate
of
main
stack
effluent
gas;
and
Q
bypass
=
volumetric
flowrate
of
bypass
effluent
gas.
(
ii)
Compliance.
(
A)
You
must
demonstrate
compliance
with
the
emission
standard(
s)
using
the
emission
concentrations
determined
from
the
performance
tests
and
the
equation
provided
by
paragraph
(
e)(
1)
of
this
section;
and
(
B)
You
must
develop
operating
parameter
limits
for
bypass
stack
and
main
stack
flowrates
that
ensure
the
emission
concentrations
calculated
with
the
equation
in
paragraph
(
e)(
1)
of
this
section
do
not
exceed
the
emission
standards
on
a
12­
hour
rolling
average
basis.
You
must
include
these
flowrate
limits
in
the
Notification
of
Compliance.
(
iii)
Notification.
If
you
elect
to
document
compliance
under
this
emissions
averaging
provision,
you
must:
(
A)
Notify
the
Administrator
in
the
initial
comprehensive
performance
test
plan
submitted
under
§
63.1207(
e).
The
performance
test
plan
must
include,
at
a
minimum,
information
describing
the
flowrate
limits
established
under
paragraph
(
e)(
2)(
ii)(
B)
of
this
section;
and
(
B)
Document
in
the
Notification
of
Compliance
submitted
under
§
63.1207(
j)
the
demonstrated
gas
flowrate­
weighted
average
emissions
that
you
calculate
with
the
equation
provided
by
paragraph
(
e)(
2)
of
this
section.
(
f)
Significant
figures.
The
emission
limits
provided
by
paragraphs
(
a)
and
(
b)
of
this
section
are
presented
with
two
significant
figures.
Although
you
must
perform
intermediate
calculations
using
at
least
three
significant
figures,
you
may
round
the
resultant
emission
levels
to
two
significant
figures
to
document
compliance.
(
g)
[
Reserved].
(
h)
When
you
comply
with
the
particulate
matter
requirements
of
paragraphs
(
a)(
7)
or
(
b)(
7)
of
this
section,
you
are
exempt
from
the
New
Source
Performance
Standard
for
particulate
matter
and
opacity
under
§
60.60
of
this
chapter.
7.
Section
63.1205A
is
added
to
read
as
follows:
§
63.1205A
What
are
the
replacement
standards
for
hazardous
waste
burning
*
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352
lightweight
aggregate
kilns?
(
a)
Emission
limits
for
existing
sources.
You
must
not
discharge
or
cause
combustion
gases
to
be
emitted
into
the
atmosphere
that
contain:
(
1)
Dioxins
and
furans
in
excess
of
0.40
ng
TEQ/
dscm
corrected
to
7
percent
oxygen;
(
2)
Mercury
in
excess
of
67
ug/
dscm
corrected
to
7
percent
oxygen;
(
3)(
i)
In
excess
of
3.1
x
10­
4
lbs
combined
emissions
of
cadmium
and
lead
attributable
to
the
hazardous
waste
per
million
British
thermal
unit
heat
input
from
the
hazardous
waste;
and
(
ii)
Lead
and
cadmium
in
excess
of
250
ug/
dscm,
combined
emissions,
corrected
to
7
percent
oxygen;
(
4)(
ii)
In
excess
of
9.5
x
10­
5
lbs
combined
emissions
of
arsenic,
beryllium,
and
chromium
attributable
to
the
hazardous
waste
per
million
British
thermal
unit
heat
input
from
the
hazardous
waste;
and
(
ii)
Arsenic,
beryllium,
and
chromium
in
excess
of
110
ug/
dscm,
combined
emissions,
corrected
to
7
percent
oxygen;
(
5)
Carbon
monoxide
and
hydrocarbons.
(
i)
Carbon
monoxide
in
excess
of
100
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis
and
corrected
to
7
percent
oxygen.
If
you
elect
to
comply
with
this
carbon
monoxide
standard
rather
than
the
hydrocarbon
standard
under
paragraph
(
a)(
5)(
ii)
of
this
section,
you
also
must
document
that,
during
the
destruction
and
removal
efficiency
(
DRE)
test
runs
or
their
equivalent
as
provided
by
§
63.1206(
b)(
7),
hydrocarbons
do
not
exceed
20
parts
per
million
by
volume
during
those
runs,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
or
(
ii)
Hydrocarbons
in
excess
of
20
parts
per
million
by
volume,
over
an
hourly
rolling
average,
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
(
6)
Hydrogen
chloride
and
chlorine
gas
in
excess
of
150
parts
per
million
by
volume,
combined
emissions,
expressed
as
a
chloride
(
Cl(­))
equivalent,
dry
basis
and
corrected
to
7
percent
oxygen;
and
(
7)
Particulate
matter
in
excess
of
57
mg/
dscm
corrected
to
7
percent
oxygen.
(
b)
Emission
limits
for
new
sources.
You
must
not
discharge
or
cause
combustion
gases
to
be
emitted
into
the
atmosphere
that
contain:
(
1)
Dioxins
and
furans
in
excess
of
0.40
ng
TEQ/
dscm
corrected
to
7
percent
oxygen;
(
2)
Mercury
in
excess
of
67
ug/
dscm
corrected
to
7
percent
oxygen;
(
3)(
i)
In
excess
of
2.4
x
10­
5
lbs
combined
emissions
of
cadmium
and
lead
attributable
to
the
hazardous
waste
per
million
British
thermal
unit
heat
input
from
the
hazardous
waste;
and
(
ii)
Lead
and
cadmium
in
excess
of
43
ug/
dscm,
combined
emissions,
corrected
to
7
percent
oxygen;
(
4)(
i)
In
excess
of
3.2
x
10­
5
lbs
combined
emissions
of
arsenic,
beryllium,
and
chromium
attributable
to
the
hazardous
waste
per
million
British
thermal
unit
heat
input
from
the
hazardous
waste;
and
(
ii)
Arsenic,
beryllium,
and
chromium
in
excess
of
110
ug/
dscm,
combined
emissions,
corrected
to
7
percent
oxygen;
*
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353
(
5)
Carbon
monoxide
and
hydrocarbons.
(
i)
Carbon
monoxide
in
excess
of
100
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis
and
corrected
to
7
percent
oxygen.
If
you
elect
to
comply
with
this
carbon
monoxide
standard
rather
than
the
hydrocarbon
standard
under
paragraph
(
b)(
5)(
ii)
of
this
section,
you
also
must
document
that,
during
the
destruction
and
removal
efficiency
(
DRE)
test
runs
or
their
equivalent
as
provided
by
§
63.1206(
b)(
7),
hydrocarbons
do
not
exceed
20
parts
per
million
by
volume
during
those
runs,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
or
(
ii)
Hydrocarbons
in
excess
of
20
parts
per
million
by
volume,
over
an
hourly
rolling
average,
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
(
6)
Hydrogen
chloride
and
chlorine
gas
in
excess
of
150
parts
per
million
by
volume,
combined
emissions,
expressed
as
a
chloride
(
Cl(­))
equivalent,
dry
basis
and
corrected
to
7
percent
oxygen;
and
(
7)
Particulate
matter
in
excess
of
23
mg/
dscm
corrected
to
7
percent
oxygen.
(
c)
Destruction
and
removal
efficiency
(
DRE)
standard.
(
1)
99.99%
DRE.
Except
as
provided
in
paragraph
(
c)(
2)
of
this
section,
you
must
achieve
a
destruction
and
removal
efficiency
(
DRE)
of
99.99%
for
each
principal
organic
hazardous
constituent
(
POHC)
designated
under
paragraph
(
c)(
3)
of
this
section.
You
must
calculate
DRE
for
each
POHC
from
the
following
equation:
DRE
=
[
1
­
(
W
out
/
W
in)]
x
100%
Where:
W
in
=
mass
feedrate
of
one
POHC
in
a
waste
feedstream;
and
W
out
=
mass
emission
rate
of
the
same
POHC
present
in
exhaust
emissions
prior
to
release
to
the
atmosphere.
(
2)
99.9999%
DRE.
If
you
burn
the
dioxin­
listed
hazardous
wastes
F020,
F021,
F022,
F023,
F026,
or
F027
(
see
§
261.31
of
this
chapter),
you
must
achieve
a
destruction
and
removal
efficiency
(
DRE)
of
99.9999%
for
each
POHC
that
you
designate
under
paragraph
(
c)(
3)
of
this
section.
You
must
demonstrate
this
DRE
performance
on
POHCs
that
are
more
difficult
to
incinerate
than
tetra­,
penta­,
and
hexachlorodibenzo­
dioxins
and
dibenzofurans.
You
must
use
the
equation
in
paragraph
(
c)(
1)
of
this
section
to
calculate
DRE
for
each
POHC.
In
addition,
you
must
notify
the
Administrator
of
your
intent
to
burn
hazardous
wastes
F020,
F021,
F022,
F023,
F026,
or
F027.
(
3)
Principal
organic
hazardous
constituents
(
POHCs).
(
i)
You
must
treat
each
POHC
in
the
waste
feed
that
you
specify
under
paragraph
(
c)(
3)(
ii)
of
this
section
to
the
extent
required
by
paragraphs
(
c)(
1)
and
(
c)(
2)
of
this
section.
(
ii)
You
must
specify
one
or
more
POHCs
from
the
list
of
hazardous
air
pollutants
established
by
42
U.
S.
C.
7412(
b)(
1),
excluding
caprolactam
(
CAS
number
105602)
as
provided
by
§
63.60,
for
each
waste
to
be
burned.
You
must
base
this
specification
on
the
degree
of
difficulty
of
incineration
of
the
organic
constituents
in
the
waste
and
on
their
concentration
or
mass
in
the
waste
feed,
considering
the
results
of
waste
analyses
or
other
data
and
information.
(
d)
Significant
figures.
The
emission
limits
provided
by
paragraphs
(
a)
and
(
b)
of
this
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354
section
are
presented
with
two
significant
figures.
Although
you
must
perform
intermediate
calculations
using
at
least
three
significant
figures,
you
may
round
the
resultant
emission
levels
to
two
significant
figures
to
document
compliance.
8.
Section
63.1206
is
amended
by:
a.
Revising
paragraph
(
a).
b.
Revising
paragraphs
(
b)(
1)(
ii),
(
b)(
6),
(
b)(
7)(
i)(
A),
(
b)(
9)(
i)
introductory
text,
(
b)(
10)(
i)
introductory
text,
(
b)(
11),
(
b)(
13)(
i)
introductory
text,
and
(
b)(
13)(
ii).
c.
Revising
paragraphs
(
c)(
1)(
i)
introductory
text
and
(
c)(
7)(
ii)
introductory
text.
d.
Adding
paragraphs
(
c)(
7)(
ii)(
C)
and
(
c)(
7)(
iii).
The
revisions
and
additions
read
as
follows:
§
63.1206
When
and
how
must
you
comply
with
the
standards
and
operating
requirements?
(
a)
Compliance
dates.
(
1)
Compliance
dates
for
incinerators,
cement
kilns,
and
lightweight
aggregate
kilns
that
burn
hazardous
waste.
(
i)
Compliance
date
for
standards
under
§
§
63.1203,
63.1204,
and
63.1205.
(
A)
Compliance
dates
for
existing
sources.
You
must
comply
with
the
emission
standards
under
§
§
63.1203,
63.1204,
and
63.1205
and
the
other
requirements
of
this
subpart
no
later
than
the
compliance
date,
September
30,
2003,
unless
the
Administrator
grants
you
an
extension
of
time
under
§
63.6(
i)
or
§
63.1213.
(
B)
New
or
reconstructed
sources.
(
1)
If
you
commenced
construction
or
reconstruction
of
your
hazardous
waste
combustor
after
April
19,
1996,
you
must
comply
with
the
emission
standards
under
§
§
63.1203,
63.1204,
and
63.1205
and
the
other
requirements
of
this
subpart
by
the
later
of
September
30,
1999
or
the
date
the
source
starts
operations,
except
as
provided
by
paragraph
(
a)(
1)(
i)(
B)(
2)
of
this
section.
The
costs
of
retrofitting
and
replacement
of
equipment
that
is
installed
specifically
to
comply
with
this
subpart,
between
April
19,
1996
and
a
source's
compliance
date,
are
not
considered
to
be
reconstruction
costs.
(
2)
For
a
standard
under
§
§
63.1203,
63.1204,
and
63.1205
that
is
more
stringent
than
the
standard
proposed
on
April
19,
1996,
you
may
achieve
compliance
no
later
than
September
30,
2003
if
you
comply
with
the
standard
proposed
on
April
19,
1996
after
September
30,
1999.
This
exception
does
not
apply,
however,
to
new
or
reconstructed
area
source
hazardous
waste
combustors
that
become
major
sources
after
September
30,
1999.
As
provided
by
§
63.6(
b)(
7),
such
sources
must
comply
with
the
standards
under
§
§
63.1203,
63.1204,
and
63.1205
at
startup.
(
ii)
Compliance
date
for
standards
under
§
§
63.1203A,
63.1204A,
and
63.1205A.
(
A)
Compliance
dates
for
existing
sources.
You
must
comply
with
the
emission
standards
under
§
§
63.1203A,
63.1204A,
and
63.1205A
and
the
other
requirements
of
this
subpart
no
later
than
the
compliance
date,
[
insert
date
three
years
after
date
of
publication
of
the
final
rule
in
the
Federal
Register],
unless
the
Administrator
grants
you
an
extension
of
time
under
§
63.6(
i)
or
§
63.1213.
(
B)
New
or
reconstructed
sources.
(
1)
If
you
commenced
construction
or
reconstruction
of
your
hazardous
waste
combustor
after
[
insert
date
of
publication
of
the
proposed
rule
in
the
Federal
Register],
you
must
comply
with
the
emission
standards
under
§
§
63.1203A,
63.1204A,
and
63.1205A
and
the
other
requirements
of
this
subpart
by
the
later
of
[
insert
date
of
publication
of
the
final
rule
in
the
Federal
Register]
or
the
date
the
source
starts
operations,
except
as
*
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355
provided
by
paragraph
(
a)(
1)(
ii)(
B)(
2)
of
this
section.
The
costs
of
retrofitting
and
replacement
of
equipment
that
is
installed
specifically
to
comply
with
this
subpart,
between
[
insert
date
of
publication
in
the
Federal
Register]
and
a
source's
compliance
date,
are
not
considered
to
be
reconstruction
costs.
(
2)
For
a
standard
under
§
§
63.1203A,
63.1204A,
and
63.1205A
that
is
more
stringent
than
the
standard
proposed
on
[
insert
date
of
publication
in
the
Federal
Register],
you
may
achieve
compliance
no
later
than
[
insert
date
three
years
after
date
of
publication
of
the
final
rule
in
the
Federal
Register]
if
you
comply
with
the
standard
proposed
on
[
insert
date
of
publication
in
the
Federal
Register]
after
[
insert
date
of
publication
of
the
final
rule
in
the
Federal
Register].
This
exception
does
not
apply,
however,
to
new
or
reconstructed
area
source
hazardous
waste
combustors
that
become
major
sources
after
[
insert
date
three
years
after
date
of
publication
of
the
final
rule
in
the
Federal
Register].
As
provided
by
§
63.6(
b)(
7),
such
sources
must
comply
with
the
standards
under
§
§
63.1203A,
63.1204A
and
63.1205A
at
startup.
(
2)
Compliance
dates
for
solid
fuel­
fired
boilers,
liquid
fuel­
fired
boilers,
and
hydrogen
chloride
production
furnaces
that
burn
hazardous
waste
for
standards
under
§
§
63.1216,
63.1217,
and
63.1218.
(
i)
Compliance
date
for
existing
sources.
You
must
comply
with
the
standards
of
this
subpart
no
later
than
the
compliance
date,
[
insert
date
three
years
after
date
of
publication
of
the
final
rule
in
the
Federal
Register],
unless
the
Administrator
grants
you
an
extension
of
time
under
§
63.6(
i)
or
§
63.1213.
(
ii)
New
or
reconstructed
sources.
(
A)
If
you
commenced
construction
or
reconstruction
of
your
hazardous
waste
combustor
after
[
insert
date
of
publication
of
the
proposed
rule
in
the
Federal
Register],
you
must
comply
with
this
subpart
by
the
later
of
[
insert
date
of
publication
of
the
final
rule
in
the
Federal
Register]
or
the
date
the
source
starts
operations,
except
as
provided
by
paragraph
(
a)(
2)(
ii)(
B)
of
this
section.
The
costs
of
retrofitting
and
replacement
of
equipment
that
is
installed
specifically
to
comply
with
this
subpart,
between
[
insert
date
of
publication
of
the
proposed
rule
in
the
Federal
Register]
and
a
source's
compliance
date,
are
not
considered
to
be
reconstruction
costs.
(
B)
For
a
standard
in
the
subpart
that
is
more
stringent
than
the
standard
proposed
on
[
insert
date
of
publication
of
the
proposed
rule
in
the
Federal
Register],
you
may
achieve
compliance
no
later
than
[
insert
date
three
years
after
date
of
publication
of
the
final
rule
in
the
Federal
Register]
if
you
comply
with
the
standard
proposed
on
[
insert
date
of
publication
of
the
proposed
rule
in
the
Federal
Register]
after
[
insert
date
of
publication
of
the
final
rule
in
the
Federal
Register]
This
exception
does
not
apply,
however,
to
new
or
reconstructed
area
source
hazardous
waste
combustors
that
become
major
sources
after
[
insert
date
three
years
after
date
of
publication
of
the
final
rule
in
the
Federal
Register].
As
provided
by
§
63.6(
b)(
7),
such
sources
must
comply
with
this
subpart
at
startup.
(
3)
Early
compliance.
If
you
choose
to
comply
with
the
emission
standards
of
this
subpart
prior
to
the
dates
specified
in
paragraphs
(
a)(
1)
and
(
a)(
2)
of
this
section,
your
compliance
date
is
the
earlier
of
the
date
you
postmark
the
Notification
of
Compliance
under
§
63.1207(
j)(
1)
or
the
dates
specified
in
paragraphs
(
a)(
1)
and
(
a)(
2)
of
this
section.
(
b)
*
*
*
(
1)
*
*
*
*
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356
(
ii)
When
hazardous
waste
is
not
in
the
combustion
chamber
(
i.
e.,
the
hazardous
waste
feed
to
the
combustor
has
been
cut
off
for
a
period
of
time
not
less
than
the
hazardous
waste
residence
time)
and
you
have
documented
in
the
operating
record
that
you
are
complying
with
all
otherwise
applicable
requirements
and
standards
promulgated
under
authority
of
sections
112
(
e.
g.,
subparts
LLL,
NNNNN,
DDDDD)
or
129
of
the
Clean
Air
Act
in
lieu
of
the
emission
standards
under
§
§
63.1203,
63.1203A,
63.1204,
63.1204A,
63.1205,
63.1205A,
63.1215,
63.1216,
63.1217,
and
63.1218;
the
monitoring
and
compliance
standards
of
this
section
and
§
§
63.1207
through
63.1209,
except
the
modes
of
operation
requirements
of
§
63.1209(
q);
and
the
notification,
reporting,
and
recordkeeping
requirements
of
§
§
63.1210
through
63.1212.
*
*
*
*
*
(
6)
Compliance
with
the
carbon
monoxide
and
hydrocarbon
emission
standards.
This
paragraph
applies
to
sources
that
elect
to
comply
with
the
carbon
monoxide
and
hydrocarbon
emissions
standards
of
this
subpart
by
documenting
continuous
compliance
with
the
carbon
monoxide
standard
using
a
continuous
emissions
monitoring
system
and
documenting
compliance
with
the
hydrocarbon
standard
during
the
destruction
and
removal
efficiency
(
DRE)
performance
test
or
its
equivalent.
*
*
*
*
*
(
7)
*
*
*
(
i)
*
*
*
(
A)
You
must
document
compliance
with
the
Destruction
and
Removal
Efficiency
(
DRE)
standard
under
this
subpart
only
once
provided
that
you
do
not
modify
the
source
after
the
DRE
test
in
a
manner
that
could
affect
the
ability
of
the
source
to
achieve
the
DRE
standard.
*
*
*
*
*
(
9)
*
*
*
(
i)
You
may
petition
the
Administrator
to
recommend
alternative
semivolatile
metal,
low
volatile
metal,
mercury,
or
hydrogen
chloride/
chlorine
gas
emission
standards
under
§
63.1205
if:
*
*
*
*
*
(
10)
*
*
*
(
i)
You
may
petition
the
Administrator
to
recommend
alternative
semivolatile
metal,
low
volatile
metal,
mercury,
or
hydrogen
chloride/
chlorine
gas
emission
standards
under
§
63.1204
if:
*
*
*
*
*
(
11)
Calculation
of
hazardous
waste
residence
time.
You
must
calculate
the
hazardous
waste
residence
time
and
include
the
calculation
in
the
performance
test
plan
under
§
63.1207(
f)
and
the
operating
record.
You
must
also
provide
the
hazardous
waste
residence
time
in
the
Documentation
of
Compliance
under
§
63.1211(
d)
and
the
Notification
of
Compliance
under
§
§
63.1207(
j)
and
63.1210(
d).
*
*
*
*
*
(
13)
*
*
*
(
i)
Cement
kilns
that
feed
hazardous
waste
at
a
location
other
than
the
end
where
products
are
normally
discharged
and
where
fuels
are
normally
fired
must
comply
with
the
carbon
monoxide
and
hydrocarbon
standards
of
this
subpart
as
follows:
*
*
*
*
*
(
ii)
Lightweight
aggregate
kilns
that
feed
hazardous
waste
at
a
location
other
than
the
end
*
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357
where
products
are
normally
discharged
and
where
fuels
are
normally
fired
must
comply
with
the
hydrocarbon
standards
of
this
subpart
as
follows:
(
A)
Existing
sources
must
comply
with
the
20
parts
per
million
by
volume
hydrocarbon
standard
of
this
subpart;
(
B)
New
sources
must
comply
with
the
20
parts
per
million
by
volume
hydrocarbon
standard
of
this
subpart.
*
*
*
*
*
(
c)
*
*
*
(
1)
*
*
*
(
i)
You
must
operate
only
under
the
operating
requirements
specified
in
the
Documentation
of
Compliance
under
§
63.1211(
d)
or
the
Notification
of
Compliance
under
§
§
63.1207(
j)
and
63.1210(
d),
except:
*
*
*
*
*
(
7)
*
*
*
(
ii)
Bag
leak
detection
system
requirements.
If
your
combustor
is
equipped
with
a
baghouse
(
fabric
filter),
you
must
continuously
operate
a
bag
leak
detection
system
that
meets
the
specifications
and
requirements
of
paragraph
(
c)(
7)(
ii)(
A)
of
this
section
and
you
must
comply
with
the
corrective
measures
requirements
of
paragraph
(
c)(
7)(
ii)(
B)
of
this
section.
*
*
*
*
*
(
C)
Excessive
exceedances
notification.
If
you
operate
the
combustor
when
the
detector
response
exceeds
the
alarm
set­
point
more
than
5
percent
of
the
time
during
any
6­
month
block
time
period,
you
must
submit
a
notification
to
the
Administrator
within
5
days
that
describes
the
causes
of
the
exceedances
and
the
revisions
to
the
design,
operation,
or
maintenance
of
the
combustor
or
baghouse
you
are
taking
to
minimize
exceedances.
(
iii)
Particulate
matter
detection
system
requirements
for
electrostatic
precipitators
and
ionizing
wet
scrubbers.
If
your
combustor
is
equipped
with
an
electrostatic
precipitator
or
ionizing
wet
scrubber,
and
you
elect
not
to
establish
under
§
63.1209(
m)(
1)(
iv)
site­
specific
operating
parameter
limits
that
are
linked
to
the
automatic
waste
feed
cutoff
system
under
paragraph
(
c)(
3)
of
this
section,
you
must
continuously
operate
a
particulate
matter
detection
system
that
meets
the
specifications
and
requirements
of
paragraph
(
c)(
7)(
iii)(
A)
of
this
section
and
you
must
comply
with
the
corrective
measures
requirements
of
paragraph
(
c)(
7)(
iii)(
B)
of
this
section.
(
A)
Particulate
matter
detection
system
requirements­­(
1)
The
particulate
matter
detection
system
must
be
certified
by
the
manufacturer
to
be
capable
of
continuously
detecting
and
recording
particulate
matter
emissions
at
the
loadings
you
expect
to
achieve
during
the
comprehensive
performance
test;
(
2)
The
particulate
matter
detector
shall
provide
output
of
relative
or
absolute
particulate
matter
loadings;
(
3)
The
particulate
matter
detection
system
shall
be
equipped
with
an
alarm
system
that
will
sound
an
audible
alarm
when
an
increase
in
relative
or
absolute
particulate
loadings
is
detected
over
the
set­
point
(
4)
You
must
install
and
operate
the
particulate
matter
detection
system
in
a
manner
consistent
with
available
written
guidance
from
the
U.
S.
Environmental
Protection
Agency
or,
in
the
absence
of
such
written
guidance,
the
manufacturer's
written
specifications
and
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358
recommendations
for
installation,
operation,
and
adjustment
of
the
system;
(
5)
You
must
establish
the
alarm
set­
point
as
the
average
detector
response
of
the
test
run
averages
achieved
during
the
comprehensive
performance
test
demonstrating
compliance
with
the
particulate
matter
emission
standard.
You
must
comply
with
the
alarm
set­
point
on
a
6­
hour
rolling
average,
updated
each
hour
with
a
one­
hour
block
average
that
is
the
average
of
the
detector
responses
over
each
15­
minute
block.
(
6)
Where
multiple
detectors
are
required
to
monitor
multiple
control
devices,
the
system's
instrumentation
and
alarm
system
may
be
shared
among
the
detectors.
(
B)
Particulate
matter
detection
system
corrective
measures
requirements.
The
operating
and
maintenance
plan
required
by
paragraph
(
c)(
7)(
i)
of
this
section
must
include
a
corrective
measures
plan
that
specifies
the
procedures
you
will
follow
in
the
case
of
a
particulate
matter
detection
system
alarm.
The
corrective
measures
plan
must
include,
at
a
minimum,
the
procedures
used
to
determine
and
record
the
time
and
cause
of
the
alarm
as
well
as
the
corrective
measures
taken
to
correct
the
control
device
malfunction
or
minimize
emissions
as
specified
below.
Failure
to
initiate
the
corrective
measures
required
by
this
paragraph
is
failure
to
ensure
compliance
with
the
emission
standards
in
this
subpart.
(
1)
You
must
initiate
the
procedures
used
to
determine
the
cause
of
the
alarm
within
30
minutes
of
the
time
the
alarm
first
sounds;
and
(
2)
You
must
alleviate
the
cause
of
the
alarm
by
taking
the
necessary
corrective
measure(
s)
which
may
include
shutting
down
the
combustor.
(
C)
Excessive
exceedances
notification.
If
you
operate
the
combustor
when
the
detector
response
exceeds
the
alarm
set­
point
more
than
5
percent
of
the
time
during
any
6­
month
block
time
period,
you
must
submit
a
notification
to
the
Administrator
within
5
days
that
describes
the
causes
of
the
exceedances
and
the
revisions
to
the
design,
operation,
or
maintenance
of
the
combustor
or
electrostatic
precipitator
or
ionizing
wet
scrubber
you
are
taking
to
minimize
exceedances.
9.
Section
63.1207
is
amended
by:
a.
Revising
paragraph
(
b)(
1).
b.
Revising
paragraph
(
c)(
1).
c.
Revising
paragraphs
(
e)(
2)
and
(
e)(
3)(
iv).
d.
Revising
paragraphs
(
f)(
1)(
ii)(
D
),
(
f)(
1)(
xiii),
and
(
f)(
1)(
xiv).
e.
Revising
paragraphs
(
j)(
1)(
ii)
and
(
j)(
3).
f.
Revising
paragraph
(
l)(
1).
g.
Adding
paragraph
(
b)(
3).
h.
Adding
paragraph
(
c)(
3).
i.
Adding
paragraph
(
f)(
1)(
xv).
The
revisions
and
additions
read
as
follows:
§
63.1207
What
are
the
performance
testing
requirements?
*
*
*
*
*
(
b)
*
*
*
(
1)
Comprehensive
performance
test.
You
must
conduct
comprehensive
performance
tests
to
demonstrate
compliance
with
the
emission
standards
provided
by
the
subpart,
establish
*
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359
limits
for
the
operating
parameters
provided
by
§
63.1209,
and
demonstrate
compliance
with
the
performance
specifications
for
continuous
monitoring
systems.
*
*
*
*
*
(
3)
One­
Time
Dioxin/
Furan
Test
for
Boilers
Not
Subject
to
a
Numerical
Dioxin/
Furan
Standard.
For
boilers
that
are
not
subject
to
a
numerical
dioxin/
furan
emission
standard
under
§
§
63.1216
and
63.1217­­
solid
fuel­
fired
boilers,
and
those
liquid
fuel­
fired
boilers
that
are
not
equipped
with
a
dry
particulate
matter
control
device­­
you
must
conduct
a
one­
time
emission
test
for
dioxin/
furan
under
feed
and
operating
conditions
that
are
most
likely
to
maximize
dioxin/
furan
emissions,
similar
to
a
dioxin/
furan
compliance
test.
(
i)
You
must
conduct
the
dioxin/
furan
emissions
test
no
later
than
the
deadline
for
conducting
the
initial
comprehensive
performance
test.
(
ii)
You
may
use
dioxin/
furan
emissions
data
from
previous
testing
to
meet
this
requirement,
provided
that:
(
A)
The
testing
was
conducted
under
feed
and
operating
conditions
that
are
most
likely
to
maximize
dioxin/
furan
emissions,
similar
to
a
dioxin/
furan
compliance
test;
(
B)
You
have
not
changed
the
design
or
operation
of
the
boiler
in
a
manner
that
could
significantly
affect
stack
gas
dioxin/
furan
emission
concentrations;
and
(
C)
The
data
meet
quality
assurance
objectives
that
may
be
determined
on
a
site­
specific
basis.
(
iii)
You
may
use
dioxin/
furan
emissions
data
from
a
boiler
to
represent
emissions
from
another
on­
site
boiler
in
lieu
of
testing
(
i.
e.,
data
in
lieu
of
testing)
if
the
design
and
operation,
including
fuels
and
hazardous
waste
feed,
of
the
boilers
are
identical.
(
iv)
You
must
include
the
results
of
the
one­
time
dioxin/
furan
emissions
test
with
the
results
of
the
initial
comprehensive
performance
test
in
the
Notification
of
Compliance.
(
v)
You
must
repeat
the
dioxin/
furan
emissions
test
if
you
change
the
design
or
operation
of
the
source
in
a
manner
that
may
increase
dioxin/
furan
emissions.
(
c)
*
*
*(
1)
Test
date.
Except
as
provided
by
paragraphs
(
c)(
2)
and
(
c)(
3)
of
this
section,
you
must
commence
the
initial
comprehensive
performance
test
not
later
than
six
months
after
the
compliance
date.
*
*
*
*
*
(
3)
For
incinerators,
cement
kilns,
and
lightweight
aggregate
kilns,
you
must
commence
the
initial
comprehensive
performance
test
to
demonstrate
compliance
with
the
standards
under
§
§
63.1203A,
63.1204A,
and
63.1205A
not
later
than
12
months
after
the
compliance
date.
*
*
*
*
*
(
e)
*
*
*
(
2)
After
the
Administrator
has
approved
the
site­
specific
test
plan
and
CMS
performance
evaluation
test
plan,
but
no
later
than
60
calendar
days
before
initiation
of
the
test,
you
must
make
the
test
plans
available
to
the
public
for
review.
You
must
issue
a
public
notice
to
all
persons
on
your
facility/
public
mailing
list
(
developed
pursuant
to
40
CFR
§
§
70.7(
h),
71.11(
d)(
3)(
i)(
E)
and
124.10(
c)(
1)(
ix))
announcing
the
approval
of
the
test
plans
and
the
location
where
the
test
plans
are
available
for
review.
The
test
plans
must
be
accessible
to
the
public
for
60
calendar
days,
beginning
on
the
date
that
you
issue
your
public
notice.
The
location
must
be
unrestricted
and
*
OMB
Review
Draft*

360
provide
access
to
the
public
during
reasonable
hours
and
provide
a
means
for
the
public
to
obtain
copies.
The
notification
must
include
the
following
information
at
a
minimum:
(
i)
The
name
and
telephone
number
of
the
source's
contact
person;
(
ii)
The
name
and
telephone
number
of
the
regulatory
agency's
contact
person;
(
iii)
The
location
where
the
approved
test
plans
and
any
necessary
supporting
documentation
can
be
reviewed
and
copied;
(
iv)
The
time
period
for
which
the
test
plans
will
be
available
for
public
review;
and
(
v)
An
expected
time
period
for
commencement
and
completion
of
the
performance
test
and
CMS
performance
evaluation
test.
(
3)
*
*
*
(
iv)
Public
notice.
At
the
same
time
that
you
submit
your
petition
to
the
Administrator,
you
must
notify
the
public
(
e.
g.,
distribute
a
notice
to
the
facility/
public
mailing
list
developed
pursuant
to
40
CFR
§
§
70.7(
h),
71.11(
d)(
3)(
i)(
E)
and
124.10(
c)(
1)(
ix))
of
your
petition
to
waive
a
performance
test.
The
notification
must
include
all
of
the
following
information
at
a
minimum:
(
A)
The
name
and
telephone
number
of
the
source's
contact
person;
(
B)
The
name
and
telephone
number
of
the
regulatory
agency's
contact
person;
(
C)
The
date
the
source
submitted
its
site­
specific
performance
test
plan
and
CMS
performance
evaluation
test
plans;
and
(
D)
The
length
of
time
requested
for
the
waiver.
(
f)
*
*
*
(
1)
*
*
*
(
ii)
*
*
*
(
D)
The
Administrator
may
approve
on
a
case­
by­
case
basis
a
hazardous
waste
feedstream
analysis
for
organic
hazardous
air
pollutants
in
lieu
of
the
analysis
required
under
paragraph
(
f)(
1)(
ii)(
A)
of
this
section
if
the
reduced
analysis
is
sufficient
to
ensure
that
the
POHCs
used
to
demonstrate
compliance
with
the
applicable
DRE
standards
of
this
subpart
continue
to
be
representative
of
the
organic
hazardous
air
pollutants
in
your
hazardous
waste
feedstreams;
*
*
*
*
*
(
xiii)
For
cement
kilns
with
in­
line
raw
mills,
if
you
elect
to
use
the
emissions
averaging
provision
of
this
subpart,
you
must
notify
the
Administrator
of
your
intent
in
the
initial
(
and
subsequent)
comprehensive
performance
test
plan,
and
provide
the
information
required
by
the
emission
averaging
provision;
(
xiv)
For
preheater
or
preheater/
precalciner
cement
kilns
with
dual
stacks,
if
you
elect
to
use
the
emissions
averaging
provision
of
this
subpart,
you
must
notify
the
Administrator
of
your
intent
in
the
initial
(
and
subsequent)
comprehensive
performance
test
plan,
and
provide
the
information
required
by
the
emission
averaging
provision;
(
xv)
If
you
request
to
use
Method
23
for
dioxin/
furan
you
must
provide
the
information
required
under
§
63.1208(
b)(
1)(
i)(
B);
*
*
*
*
*
(
j)
*
*
*
(
1)
*
*
*
(
ii)
Upon
postmark
of
the
Notification
of
Compliance,
you
must
comply
with
all
operating
requirements
specified
in
the
Notification
of
Compliance
in
lieu
of
the
limits
specified
in
the
*
OMB
Review
Draft*

361
Documentation
of
Compliance
required
under
§
63.1211(
d).
*
*
*
*
*
(
3)
See
§
§
63.7(
g),
63.9(
h),
and
63.1210(
d)
for
additional
requirements
pertaining
to
the
Notification
of
Compliance
(
e.
g.,
you
must
include
results
of
performance
tests
in
the
Notification
of
Compliance).
*
*
*
*
*
(
l)
Failure
of
performance
test­­(
1)
Comprehensive
performance
test.
The
provisions
of
this
paragraph
do
not
apply
to
the
initial
comprehensive
performance
test
if
you
conduct
the
test
prior
to
your
compliance
date.
*
*
*
*
*
10.
Section
63.1208
is
amended
by
revising
paragraphs
(
b)(
1)(
i)
and
(
b)(
5)
to
read
as
follows:
§
63.1208
What
are
the
test
methods?
*
*
*
*
*
(
b)
*
*
*
(
1)
*
*
*
(
i)
To
determine
compliance
with
the
emission
standard
for
dioxins
and
furans,
you
must
use:
(
A)
Method
0023A,
Sampling
Method
for
Polychlorinated
Dibenzp­
p­
Dioxins
and
Polychlorinated
Dibenzofurans
emissions
from
Stationary
Sources,
EPA
Publication
SW­
846,
as
incorporated
by
reference
in
paragraph
(
a)
of
this
section;
or
(
B)
Method
23,
provided
in
appendix
A,
part
60
of
this
chapter,
except
that
for
coal­
fired
boilers,
sources
equipped
with
an
activated
carbon
injection
system,
and
other
sources
that
the
Administrator
determines
may
emit
carbonaceous
particulate
matter
that
may
bias
Method
23
results,
you
may
use
Method
23
only
upon
the
Administrator's
approval.
In
determining
whether
to
grant
approval
to
use
Method
23,
the
Administrator
may
consider
factors
including
whether
dioxin/
furan
are
detected
at
levels
substantially
below
the
emission
standard,
and
whether
previous
Method
0023
analyses
detected
low
levels
of
dioxin/
furan
in
the
front
half.
*
*
*
*
*
(
5)
Hydrogen
chloride
and
chlorine
gas­­(
i)
Compliance
with
MACT
standards.
To
determine
compliance
with
the
emission
standard
for
hydrogen
chloride
and
chlorine
gas
(
combined),
you
must
use:
(
A)
Method
26/
26A
as
provided
in
appendix
A,
part
60
of
this
chapter;
or
(
B)
Methods
320
or
321
as
provided
in
appendix
A,
part
60
of
this
chapter,
or
ASTM
D
6735­
01,
Test
Method
for
Measurement
of
Gaseous
Chlorides
and
Fluorides
from
Mineral
Calcining
Exhaust
Sources­­
Impinger
Method
to
measure
emissions
of
hydrogen
chloride,
and
Method
26/
26A
to
measure
emissions
of
chlorine
gas.
(
ii)
Compliance
with
risk­
based
limits
under
§
63.1215.
To
demonstrate
compliance
with
emission
limits
established
under
§
63.1215,
you
must
use
Methods
26/
26A,
320,
or
321,
or
ASTM
D
6735­
01,
Test
Method
for
Measurement
of
Gaseous
Chlorides
and
Fluorides
from
Mineral
Calcining
Exhaust
Sources­­
Impinger
Method,
except:
(
A)
For
cement
kilns
and
sources
equipped
with
a
dry
acid
gas
scrubber,
you
must
use
Methods
320
or
321,
or
ASTM
D
6735­
01
to
measure
hydrogen
chloride,
and
the
back­
half,
*
OMB
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Draft*

362
caustic
impingers
of
Method
26/
26A
to
measure
chlorine
gas;
and
(
B)
For
incinerators,
boilers,
and
lightweight
aggregate
kilns,
you
must
use
Methods
320
or
321,
or
ASTM
D
6735­
01
to
measure
hydrogen
chloride,
and
Method
26/
26A
to
measure
total
chlorine,
and
calculate
chlorine
gas
by
difference
if:
(
1)
The
bromine/
chlorine
ratio
in
feedstreams
is
greater
than
5
percent;
or
(
2)
The
sulfur/
chlorine
ratio
in
feedstreams
is
greater
than
50
percent.
*
*
*
*
*
11.
Section
63.1209
is
amended
by:
a.
Revising
paragraphs
(
a)(
1)(
ii)(
A),
(
a)(
1)(
iv)(
D),
and
(
a)(
1)(
v)(
D).
b.
Revising
paragraph
(
f)(
1).
c.
Revising
paragraph
(
g)(
1).
d.
Revising
paragraphs
(
k)(
1)(
i)
and
(
k)(
2)(
i).
e.
Revising
paragraph
(
l)(
1).
f.
Revising
paragraph
(
m)(
1)(
iv)
introductory
text.
g.
Revising
paragraphs
(
n)
introductory
text
and
(
n)(
2).
h.
Revising
paragraph
(
o)
introductory
text
and
(
o)(
1).
i.
Revisng
paragraph
(
q)(
1)(
ii).
The
revisions
read
as
follows:
§
63.1209
What
are
the
monitoring
requirements?
(
a)
*
*
*
(
1)
*
*
*
(
ii)
*
*
*
(
A)
You
must
maintain
and
operate
each
COMS
in
accordance
with
the
requirements
of
§
63.8(
c)
except
for
the
requirements
under
§
63.8(
c)(
3).
The
requirements
of
§
63.1211(
d)
shall
be
complied
with
instead
of
§
63.8(
c)(
3);
and
*
*
*
*
*
(
iv)
*
*
*
(
D)
To
remain
in
compliance,
all
six­
minute
block
averages
must
not
exceed
the
opacity
standard.
(
v)
*
*
*
(
D)
To
remain
in
compliance,
all
six­
minute
block
averages
must
not
exceed
the
opacity
standard.
*
*
*
*
*
(
f)
*
*
*
(
1)
Section
63.8(
c)(
3).
The
requirements
of
§
63.1211(
d),
that
requires
CMSs
to
be
installed,
calibrated,
and
operational
on
the
compliance
date,
shall
be
complied
with
instead
of
§
63.8(
c)(
3).
*
*
*
*
*
(
g)
*
*
*
(
1)
Requests
to
use
alternatives
to
operating
parameter
monitoring
requirements.
(
i)
You
may
submit
an
application
to
the
Administrator
or
State
with
an
approved
Title
V
program
under
this
paragraph
for
approval
of
alternative
operating
parameter
monitoring
requirements
to
document
compliance
with
the
emission
standards
of
this
subpart.
For
requests
to
use
additional
*
OMB
Review
Draft*

363
CEMS,
however,
you
must
use
paragraph
(
a)(
5)
of
this
section
and
§
63.8(
f).
*
*
*
*
*
(
k)
*
*
*
(
1)
*
*
*
(
i)
For
sources
other
than
a
lightweight
aggregate
kiln,
if
the
combustor
is
equipped
with
an
electrostatic
precipitator,
baghouse
(
fabric
filter),
or
other
dry
emissions
control
device
where
particulate
matter
is
suspended
in
contact
with
combustion
gas,
you
must
establish
a
limit
on
the
maximum
temperature
of
the
gas
at
the
inlet
to
the
device
on
an
hourly
rolling
average.
You
must
establish
the
hourly
rolling
average
limit
as
the
average
of
the
test
run
averages.
*
*
*
*
*
(
2)
*
*
*
(
i)
For
sources
other
than
cement
kilns,
you
must
measure
the
temperature
of
each
combustion
chamber
at
a
location
that
best
represents,
as
practicable,
the
bulk
gas
temperature
in
the
combustion
zone.
You
must
document
the
temperature
measurement
location
in
the
test
plan
you
submit
under
§
§
63.1207(
e)
and
(
f);
*
*
*
*
*
(
l)
Mercury.
*
*
*
(
1)
Feedrate
of
mercury.
(
i)
For
incinerators,
cement
kilns,
and
lightweight
aggregate
kilns,
when
complying
with
the
mercury
emission
standards
under
§
§
63.1203,
63.1204,
and
63.1205,
and
for
solid
fuel­
fired
boilers,
you
must
establish
a
12­
hour
rolling
average
limit
for
the
total
feedrate
of
mercury
in
all
feedstreams
as
the
average
of
the
test
run
averages.
(
ii)
For
incinerators,
cement
kilns,
and
lightweight
aggregate
kilns,
when
complying
with
the
mercury
emission
standards
under
§
§
63.1203A,
63.1204A,
and
63.1205A,
you
must
establish
an
annual
rolling
average
limit
for
the
total
feedrate
of
mercury
in
all
feedstreams
as
follows:
(
A)
You
must
calculate
a
mercury
system
removal
efficiency
for
each
test
run
as
[
1
­
mercury
emission
rate
(
g/
s)
/
mercury
feedrate
(
g/
s)],
and
calculate
the
average
system
removal
efficiency
of
the
test
run
averages,
except
if
your
source
is
not
equipped
with
a
control
system
that
consistently
and
reproducibly
controls
mercury
emissions,
you
must
assume
zero
system
removal
efficiency.
If
emissions
exceed
the
mercury
emission
standard,
it
is
not
a
violation
because
compliance
with
these
mercury
emission
standards,
which
are
derived
from
normal
emissions
data,
is
based
on
compliance
with
the
mercury
feedrate
limit
on
an
annual
rolling
average.
(
B)
You
must
calculate
the
annual
average
mercury
feedrate
limit
as
the
mercury
emission
standard
(
ug/
m3)
divided
by
the
system
removal
efficiency.
The
feedrate
limit
is
expressed
as
an
emission
concentration,
ug
mercury/
m3
of
stack
gas.
(
C)
You
must
comply
with
the
emission
concentration­
based
annual
average
mercury
feedrate
limit
by
measuring
the
mercury
feedrate
(
g/
s)
and
the
stack
gas
flowrate
(
m3/
s)
at
least
once
a
minute
to
calculate
a
60­
minute
average
emission
concentration­
based
feedrate
as
[
mercury
feedrate
(
g/
s)
/
gas
flowrate
(
m3/
s)].
(
D)
You
must
calculate
an
annual
rolling
average
mercury
feedrate
that
is
updated
each
hour.
(
iii)
For
liquid
fuel­
fired
boilers,
you
must
establish
an
annual
rolling
average
hazardous
waste
mercury
thermal
concentration
limit,
as
follows:
*
OMB
Review
Draft*

364
(
A)
You
must
calculate
a
mercury
system
removal
efficiency
for
each
test
run
as
[
1
­
mercury
emission
rate
(
g/
s)
/
mercury
feedrate
(
g/
s)],
and
calculate
the
average
system
removal
efficiency
of
the
test
run
averages,
except
if
your
source
is
not
equipped
with
a
control
system
that
consistently
and
reproducibly
controls
mercury
emissions,
you
must
assume
zero
system
removal
efficiency.
If
emissions
exceed
the
mercury
emission
standard,
it
is
not
a
violation
because
compliance
with
the
mercury
emission
standard,
which
is
derived
from
normal
emissions
data,
is
based
on
compliance
with
the
hazardous
waste
mercury
thermal
concentration
limit
on
an
annual
rolling
average.
(
B)
You
must
calculate
the
annual
average
hazardous
waste
mercury
thermal
concentration
limit
as
the
mercury
emission
standard
(
lb/
MM
Btu)
divided
by
the
system
removal
efficiency.
The
hazardous
waste
thermal
concentration
limit
is
expressed
as:
lb
mercury
in
hazardous
waste
feedstreams
per
million
Btu
of
hazardous
waste.
(
C)
You
must
comply
with
the
annual
average
hazardous
waste
mercury
thermal
concentration
limit
by
measuring
the
feedrate
of
mercury
in
all
hazardous
waste
feedstreams
(
lb/
s)
and
the
hazardous
waste
thermal
feedrate
(
MM
Btu/
s)
at
least
once
a
minute
to
calculate
a
60­
minute
average
thermal
emission
concentration
as
[
hazardous
waste
mercury
feedrate
(
g/
s)
/
hazardous
waste
thermal
feedrate
(
MM
Btu/
s)].
(
D)
You
must
calculate
an
annual
rolling
average
hazardous
waste
mercury
thermal
concentration
that
is
updated
each
hour.
(
iv)
Extrapolation
of
feedrate
levels.
In
lieu
of
establishing
mercury
feedrate
limits
as
specified
in
paragraphs
(
l)(
1)(
i­
iii)
of
this
section,
you
may
request
as
part
of
the
performance
test
plan
under
§
§
63.6(
b)
and
(
c)
and
§
§
63.1207
(
e)
and
(
f)
to
use
the
mercury
feedrates
and
associated
emission
rates
during
the
comprehensive
performance
test
to
extrapolate
to
higher
allowable
feedrate
limits
and
emission
rates.
The
extrapolation
methodology
will
be
reviewed
and
approved,
as
warranted,
by
the
Administrator.
The
review
will
consider
in
particular
whether:
(
A)
Performance
test
metal
feedrates
are
appropriate
(
i.
e.,
whether
feedrates
are
at
least
at
normal
levels;
depending
on
the
heterogeneity
of
the
waste,
whether
some
level
of
spiking
would
be
appropriate;
and
whether
the
physical
form
and
species
of
spiked
material
is
appropriate);
(
B)
Whether
the
extrapolated
feedrates
you
request
are
warranted
considering
historical
metal
feedrate
data;
and
(
C)
Whether
you
have
interpreted
the
performance
test
results
properly
and
the
extrapolation
procedure
is
appropriate
for
your
source.
*
*
*
*
*
(
m)
*
*
*
(
1)
*
*
*
(
iv)
Other
particulate
matter
control
devices.
For
each
particulate
matter
control
device
that
is
not
a
fabric
filter
or
high
energy
wet
scrubber,
or
is
not
an
electrostatic
precipitator
or
ionizing
wet
scrubber
for
which
you
elect
to
monitor
particulate
matter
loadings
under
§
63.1206(
c)(
7)(
iii)
of
this
chapter
for
process
control,
you
must
ensure
that
the
control
device
is
properly
operated
and
maintained
as
required
by
§
63.1206(
c)(
7)
and
by
monitoring
the
operation
of
the
control
device
as
follows:
*
*
*
*
*
*
OMB
Review
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365
(
n)
Semivolatile
metals
and
low
volatile
metals.
*
*
*
*
*
*
*
*
(
2)
Maximum
feedrate
of
semivolatile
and
low
volatile
metals.
(
i)
General.
You
must
establish
feedrate
limits
for
semivolatile
metals
(
cadmium
and
lead)
and
low
volatile
metals
(
arsenic,
beryllium,
and
chromium)
as
follows,
except
as
provided
by
paragraph
(
n)(
2)(
vii)
of
this
section.
(
ii)
For
incinerators,
cement
kilns,
and
lightweight
aggregate
kilns,
when
complying
with
the
emission
standards
under
§
§
63.1203,
63.1203A,
63.1204,
and
63.1205,
and
for
solid
fuelfired
boilers,
you
must
establish
12­
hour
rolling
average
limits
for
the
total
feedrate
of
semivolatile
and
low
volatile
metals
in
all
feedstreams
as
the
average
of
the
test
run
averages
and
as
specified
in
paragraph
(
n)(
2)(
iv)
of
this
section.
(
iii)
For
cement
kilns,
when
complying
with
the
emission
standards
under
§
63.1204A,
you
must
establish
12­
hour
rolling
average
feedrate
limits
for
semivolatile
and
low
volatile
metals
as
the
thermal
concentration
of
semivolatile
metals
or
low
volatile
metals
in
all
hazardous
waste
feedstreams.
You
must
calculate
hazardous
waste
thermal
concentrations
for
semivolatile
metals
and
low
volatile
metals
for
each
run
as
the
total
mass
feedrate
of
semivolatile
metals
or
low
volatile
metals
for
all
hazardous
waste
feedstreams
divided
by
the
total
heat
input
rate
for
all
hazardous
waste
feedstreams.
The
12­
hour
rolling
average
feedrate
limits
for
semivolatile
metals
and
low
volatile
metals
are
the
average
of
the
hazardous
waste
thermal
concentrations
for
the
runs.
(
iv)
Lightweight
aggregate
kilns
under
§
63.1205A.
(
A)
Existing
sources.
When
complying
with
the
emission
standards
under
§
63.1205A,
you
must
establish
semivolatile
metal
and
low
volatile
metal
feedrate
limits
as
12­
hour
rolling
average
feedrate
limits
and
12­
hour
rolling
average
hazardous
waste
thermal
concentrations
as
specified
in
paragraphs
(
n)(
2)(
ii
and
iii).
You
must
comply
with
both
feedrate
limits
for
semivolatile
metals
and
low
volatile
metals.
(
B)
New
sources.
When
complying
with
the
emission
standards
under
§
63.1205A,
you
must
establish
semivolatile
metal
and
low
volatile
metal
feedrate
limits
as
12­
hour
rolling
average
hazardous
waste
thermal
concentrations
as
specified
in
paragraphs
(
n)(
2)(
ii
and
iii).
(
v)
Liquid
fuel­
fired
boilers.
(
A)
For
semivolatile
metals,
you
must
establish
an
annual
rolling
average
hazardous
waste
thermal
concentration
limit,
as
follows:
(
1)
You
must
calculate
a
semivolatile
metals
system
removal
efficiency
for
each
test
run
as
[
1
­
semivolatile
metals
emission
rate
(
g/
s)
/
semivolatile
metals
feedrate
(
g/
s)],
and
calculate
the
average
system
removal
efficiency
of
the
test
run
averages,
except
if
your
source
is
not
equipped
with
a
control
system
that
consistently
and
reproducibly
controls
semivolatile
metals
emissions,
you
must
assume
zero
system
removal
efficiency.
If
emissions
exceed
the
semivolatile
metals
emission
standard,
it
is
not
a
violation
because
compliance
with
the
semivolatile
metals
emission
standard,
which
is
derived
from
normal
emissions
data,
is
based
on
compliance
with
the
semivolatile
metals
hazardous
waste
thermal
concentration
limit
on
an
annual
rolling
average.
(
2)
You
must
calculate
the
annual
average
hazardous
waste
semivolatile
metals
thermal
concentration
limit
as
the
semivolatile
metals
emission
standard
(
lb/
MM
Btu)
divided
by
the
system
removal
efficiency.
The
hazardous
waste
thermal
concentration
limit
is
expressed
as:
lb
semivolatile
metals
in
hazardous
waste
feedstreams
per
million
Btu
of
hazardous
waste.
*
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366
(
3)
You
must
comply
with
the
annual
average
hazardous
waste
semivolatile
metals
thermal
concentration
limit
by
measuring
the
feedrate
of
semivolatile
metals
in
all
hazardous
waste
feedstreams
(
lb/
s)
and
the
hazardous
waste
thermal
feedrate
(
MM
Btu/
s)
at
least
once
a
minute
to
calculate
a
60­
minute
average
thermal
emission
concentration
as
[
hazardous
waste
semivolatile
metals
feedrate
(
g/
s)
/
hazardous
waste
thermal
feedrate
(
MM
Btu/
s)].
(
4)
You
must
calculate
an
annual
rolling
average
hazardous
waste
semivolatile
metals
thermal
concentration
that
is
updated
each
hour.
(
B)
For
low
volatile
metals,
you
must
establish
12­
hour
rolling
average
feedrate
limits
for
chromium
as
the
thermal
concentration
of
chromium
in
all
hazardous
waste
feedstreams.
You
must
calculate
a
hazardous
waste
thermal
concentration
for
chromium
for
each
run
as
the
total
mass
feedrate
of
chromium
for
all
hazardous
waste
feedstreams
divided
by
the
total
heat
input
rate
for
all
hazardous
waste
feedstreams.
The
12­
hour
rolling
average
feedrate
limit
for
chromium
is
the
average
of
the
hazardous
waste
thermal
concentrations
for
the
runs.
(
vi)
LVM
limits
for
pumpable
wastes.
You
must
establish
separate
feedrate
limits
for
low
volatile
metals
in
pumpable
feedstreams
using
the
procedures
prescribed
above
for
total
low
volatile
metals.
Dual
feedrate
limits
for
both
pumpable
and
total
feedstreams
are
not
required,
however,
if
you
base
the
total
feedrate
limit
solely
on
the
feedrate
of
pumpable
feedstreams.
(
vii)
Extrapolation
of
feedrate
levels.
In
lieu
of
establishing
feedrate
limits
as
specified
in
paragraphs
(
l)(
1)(
i­
iii)
of
this
section,
you
may
request
as
part
of
the
performance
test
plan
under
§
§
63.6(
b)
and
(
c)
and
§
§
63.1207
(
e)
and
(
f)
to
use
the
semivolatile
metal
and
low
volatile
metal
feedrates
and
associated
emission
rates
during
the
comprehensive
performance
test
to
extrapolate
to
higher
allowable
feedrate
limits
and
emission
rates.
The
extrapolation
methodology
will
be
reviewed
and
approved,
as
warranted,
by
the
Administrator.
The
review
will
consider
in
particular
whether:
(
A)
Performance
test
metal
feedrates
are
appropriate
(
i.
e.,
whether
feedrates
are
at
least
at
normal
levels;
depending
on
the
heterogeneity
of
the
waste,
whether
some
level
of
spiking
would
be
appropriate;
and
whether
the
physical
form
and
species
of
spiked
material
is
appropriate);
(
B)
Whether
the
extrapolated
feedrates
you
request
are
warranted
considering
historical
metal
feedrate
data;
and
(
C)
Whether
you
have
interpreted
the
performance
test
results
properly
and
the
extrapolation
procedure
is
appropriate
for
your
source.
*
*
*
*
*
(
o)
Hydrogen
chloride
and
chlorine
gas.
*
*
*
(
1)
Feedrate
of
total
chlorine
and
chloride.
(
i)
Incinerators,
cement
kilns,
lightweight
aggregate
kilns,
solid
fuel­
fired
boilers,
and
hydrochloric
acid
production
furnaces.
You
must
establish
12­
hour
rolling
average
limit
for
the
total
feedrate
of
chlorine
(
organic
and
inorganic)
in
all
feedstreams
as
the
average
of
the
test
run
averages.
(
ii)
Liquid
fuel­
fired
boilers.
You
must
establish
a
12­
hour
rolling
average
limit
for
the
feedrate
of
chlorine
(
organic
and
inorganic)
as
the
thermal
concentration
of
chlorine
in
all
hazardous
waste
feedstreams.
You
must
calculate
a
hazardous
waste
thermal
concentration
for
chlorine
for
each
run
as
the
total
mass
feedrate
of
chlorine
for
all
hazardous
waste
feedstreams
divided
by
the
total
heat
input
rate
for
all
hazardous
waste
feedstreams.
The
12­
hour
rolling
*
OMB
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367
average
feedrate
limit
chlorine
is
the
average
of
the
hazardous
waste
thermal
concentrations
for
the
runs.
*
*
*
*
*
(
q)
*
*
*
(
1)
*
*
*
(
ii)
You
must
specify
(
e.
g.,
by
reference)
the
otherwise
applicable
requirements
as
a
mode
of
operation
in
your
Documentation
of
Compliance
under
§
63.1211(
d),
your
Notification
of
Compliance
under
§
63.1207(
j),
and
your
title
V
permit
application.
These
requirements
include
the
otherwise
applicable
requirements
governing
emission
standards,
monitoring
and
compliance,
and
notification,
reporting,
and
recordkeeping.
*
*
*
*
*
12.
Section
63.1210
is
amended
by:
a.
Revising
the
table
in
paragraph
(
a)(
1)
and
the
table
in
paragraph
(
a)(
2).
b.
Redesignating
paragraph
(
b)
as
(
d).
c.
Adding
new
paragraph
(
b).
d.
Adding
new
paragraph
(
c).
The
revisions
and
additions
read
as
follows:
§
63.1210
What
are
the
notification
requirements?
*
*
*
*
*
(
a)
*
*
*
(
1)
*
*
*

Reference
Notification
(
1)
63.9(
b)
Initial
notifications
that
you
are
subject
to
Subpart
EEE
of
this
Part.

(
2)
63.9(
d)
Notification
that
you
are
subject
to
special
compliance
requirements.

(
3)
63.9(
j)
Notification
and
documentation
of
any
change
in
information
already
provided
under
§
63.9.

(
4)
63.1206(
b)(
5)(
i)
Notification
of
changes
in
design,
operation,
or
maintenance.

(
5)
63.1206(
c)(
7)(
ii)(
C)
Notification
of
excessive
bag
leak
detection
system
exceedances.

(
6)
63.1207(
e),
63.9(
e)
63.9(
g)(
1)
and
(
3)
Notification
of
performance
test
and
continuous
monitoring
system
evaluation,
including
the
performance
test
plan
and
CMS
performance
evaluation
plan.
1
*
OMB
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368
(
7)
63.1210(
d),
63.1207(
j),
63.1207(
k),
63.1207(
l),
63.9(
h),
63.10(
d)(
2),
63.10(
e)(
2)
Notification
of
compliance,
including
results
of
performance
tests
and
continuous
monitoring
system
performance
evaluations.

1
You
may
also
be
required
on
a
case­
by­
case
basis
to
submit
a
feedstream
analysis
plan
under
§
63.1209(
c)(
3).

(
2)
*
*
*

Reference
Notification,
Request,
Petition,
or
Application
(
1)
63.9(
i)
You
may
request
an
adjustment
to
time
periods
or
postmark
deadlines
for
submittal
and
review
of
required
information.

(
2)
63.10(
e)(
3)(
ii)
You
may
request
to
reduce
the
frequency
of
excess
emissions
and
CMS
performance
reports.

(
3)
63.10(
f)
You
may
request
to
waive
recordkeeping
or
reporting
requirements.

(
4)
63.1204(
d)(
2)(
iii)
63.1204A(
d)(
2)(
iii)
Notification
that
you
elect
to
comply
with
the
emission
averaging
requirements
for
cement
kilns
with
in­
line
raw
mills.

(
5)
63.1204(
e)(
2)(
iii),
63.1204A(
e)(
2)(
iii)
Notification
that
you
elect
to
comply
with
the
emission
averaging
requirements
for
preheater
or
preheater/
precalciner
kilns
with
dual
stacks.

(
6)
63.1206(
b)(
4),
63.1213,
63.6(
i),
63.9(
c)
You
may
request
an
extension
of
the
compliance
date
for
up
to
one
year.

(
7)
63.1206(
b)(
5)(
i)(
C)
You
may
request
to
burn
hazardous
waste
for
more
than
720
hours
and
for
purposes
other
than
testing
or
pretesting
after
a
making
a
change
in
the
design
or
operation
that
could
affect
compliance
with
emission
standards
and
prior
to
submitting
a
revised
Notification
of
Compliance.

(
8)
63.1206(
b)(
8)(
iii)(
B)
If
you
elect
to
conduct
particulate
matter
CEMS
correlation
testing
and
wish
to
have
federal
particulate
matter
and
opacity
standards
and
associated
operating
limits
waived
during
the
testing,
you
must
notify
the
Administrator
by
submitting
the
correlation
test
plan
for
review
and
approval.

(
9)
63.1206(
b)(
8)(
v)
You
may
request
approval
to
have
the
particulate
matter
and
opacity
standards
and
associated
operating
limits
and
conditions
waived
for
more
than
96
hours
for
a
correlation
test.

(
10)
63.1206(
b)(
9)
Owners
and
operators
of
lightweight
aggregate
kilns
may
request
approval
of
alternative
emission
standards
for
mercury,
semivolatile
metal,
low
volatile
metal,
and
hydrochloric
acid/
chlorine
gas
under
certain
conditions.
*
OMB
Review
Draft*

369
(
11)
63.1206(
b)(
10)
Owners
and
operators
of
cement
kilns
may
request
approval
of
alternative
emission
standards
for
mercury,
semivolatile
metal,
low
volatile
metal,
and
hydrochloric
acid/
chlorine
gas
under
certain
conditions.

(
12)
63.1206(
b)(
14)
Owners
and
operators
of
incinerators
may
elect
to
comply
with
an
alternative
to
the
particulate
matter
standard.

(
13)
63.1206(
b)(
15)
Owners
and
operators
of
cement
and
lightweight
aggregate
kilns
may
request
to
comply
with
the
alternative
to
the
interim
standards
for
mercury.

(
14)
63.1206(
c)(
2)(
ii)(
C)
You
may
request
to
make
changes
to
the
startup,
shutdown,
and
malfunction
plan.

(
15)
63.1206(
c)(
5)(
i)(
C)
You
may
request
an
alternative
means
of
control
to
provide
control
of
combustion
system
leaks.

(
16)
63.1206(
c)(
5)(
i)(
D)
You
may
request
other
techniques
to
prevent
fugitive
emissions
without
use
of
instantaneous
pressure
limits.

(
17)
63.1207(
c)(
2)
You
may
request
to
base
initial
compliance
on
data
in
lieu
of
a
comprehensive
performance
test.

(
18)
63.1207(
d)(
3)
You
may
request
more
than
60
days
to
complete
a
performance
test
if
additional
time
is
needed
for
reasons
beyond
your
control.

(
19)
63.1207(
e)(
3),
63.7(
h)
You
may
request
a
time
extension
if
the
Administrator
fails
to
approve
or
deny
your
test
plan.

(
20)
63.1207(
h)(
2)
You
may
request
to
waive
current
operating
parameter
limits
during
pretesting
for
more
than
720
hours.

(
21)
63.1207(
f)(
1)(
ii)(
D)
You
may
request
a
reduced
hazardous
waste
feedstream
analysis
for
organic
hazardous
air
pollutants
if
the
reduced
analysis
continues
to
be
representative
of
organic
hazardous
air
pollutants
in
your
hazardous
waste
feedstreams.

(
22)
63.1207(
g)(
2)(
v)
You
may
request
to
operate
under
a
wider
operating
range
for
a
parameter
during
confirmatory
performance
testing.

(
23)
63.1207(
i)
You
may
request
up
to
a
one­
year
time
extension
for
conducting
a
performance
test
(
other
than
the
initial
comprehensive
performance
test)
to
consolidate
testing
with
other
state
or
federally­
required
testing.

(
24)
63.1207(
j)(
4)
You
may
request
more
than
90
days
to
submit
a
Notification
of
Compliance
after
completing
a
performance
test
if
additional
time
is
needed
for
reasons
beyond
your
control.

(
25)
63.1207(
l)(
3)
After
failure
of
a
performance
test,
you
may
request
to
burn
hazardous
waste
for
more
than
720
hours
and
for
purposes
other
than
testing
or
pretesting.

(
26)
63.1209(
a)(
5),
63.8(
f)
You
may
request:
(
1)
approval
of
alternative
monitoring
methods
for
compliance
with
standards
that
are
monitored
with
a
CEMS;
and
(
2)
approval
to
use
a
CEMS
in
lieu
of
operating
parameter
limits.
*
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370
(
27)
63.1209(
g)(
1)
You
may
request
approval
of:
(
1)
alternatives
to
operating
parameter
monitoring
requirements,
except
for
standards
that
you
must
monitor
with
a
continuous
emission
monitoring
system
(
CEMS)
and
except
for
requests
to
use
a
CEMS
in
lieu
of
operating
parameter
limits;
or
(
2)
a
waiver
of
an
operating
parameter
limit.

(
28)
63.1209(
l)(
1)
You
may
request
to
extrapolate
mercury
feedrate
limits.

(
29)
63.1209(
n)(
2)
You
may
request
to
extrapolate
semivolatile
and
low
volatile
metal
feedrate
limits.

(
30)
63.1211(
e)
You
may
request
to
use
data
compression
techniques
to
record
data
on
a
less
frequent
basis
than
required
by
§
63.1209.

(
b)
Notification
of
intent
to
comply
(
NIC).
(
1)
You
must
prepare
a
Notification
of
Intent
to
Comply
that
includes
all
of
the
following
information:
(
i)
General
information:
(
A)
The
name
and
address
of
the
owner/
operator
and
the
source;
(
B)
Whether
the
source
is
a
major
or
an
area
source;
(
C)
Waste
minimization
and
emission
control
technique(
s)
being
considered;
(
D)
Emission
monitoring
technique(
s)
you
are
considering;
(
E)
Waste
minimization
and
emission
control
technique(
s)
effectiveness;
(
F)
A
description
of
the
evaluation
criteria
used
or
to
be
used
to
select
waste
minimization
and/
or
emission
control
technique(
s);
and
(
G)
A
general
description
of
how
you
intend
to
comply
with
the
emission
standards
of
this
subpart.
(
ii)
As
applicable
to
each
source,
information
on
key
activities
and
estimated
dates
for
these
activities
that
will
bring
the
source
into
compliance
with
emission
control
requirements
of
this
subpart.
You
must
include
all
of
the
following
key
activities
and
dates
in
your
NIC:
(
A)
The
dates
by
which
you
will
develop
engineering
designs
for
emission
control
systems
or
process
changes
for
emissions;
(
B)
The
date
by
which
you
will
commit
internal
or
external
resources
for
installing
emission
control
systems
or
making
process
changes
for
emission
control,
or
the
date
by
which
you
will
issue
orders
for
the
purchase
of
component
parts
to
accomplish
emission
control
or
process
changes.
(
C)
The
date
by
which
you
will
submit
construction
applications;
(
D)
The
date
by
which
you
will
initiate
on­
site
construction,
installation
of
emission
control
equipment,
or
process
change;
(
E)
The
date
by
which
you
will
complete
on­
site
construction,
installation
of
emission
control
equipment,
or
process
change;
and
(
F)
The
date
by
which
you
will
achieve
final
compliance.
The
individual
dates
and
milestones
listed
in
paragraphs
(
b)(
1)(
ii)(
A)
through
(
F)
of
this
section
as
part
of
the
NIC
are
not
requirements
and
therefore
are
not
enforceable
deadlines;
the
requirements
of
paragraphs
(
b)(
1)(
ii)(
A)
through
(
F)
of
this
section
must
be
included
as
part
of
the
NIC
only
to
inform
the
public
of
your
how
you
intend
to
comply
with
the
emission
standards
of
this
subpart.
*
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371
(
iii)
A
summary
of
the
public
meeting
required
under
paragraph
(
c)
of
this
section;
(
iv)
If
you
intend
to
cease
burning
hazardous
waste
prior
to
or
on
the
compliance
date,
you
must
include
in
your
NIC
a
schedule
of
key
dates
for
the
steps
to
be
taken
to
stop
hazardous
waste
activity
at
your
combustion
unit.
Key
dates
include
the
date
for
submittal
of
RCRA
closure
documents
required
under
subpart
G,
part
264
of
this
chapter.
(
2)
You
must
make
a
draft
of
the
NIC
available
for
public
review
no
later
than
30
days
prior
to
the
public
meeting
required
under
paragraph
(
c)(
1)
of
this
section.
(
3)
You
must
submit
the
final
NIC
to
the
Administrator
no
later
than
one
year
following
the
effective
date
of
the
emission
standards
of
this
subpart.
(
c)
NIC
public
meeting
and
notice.
(
1)
Prior
to
the
submission
of
the
NIC
to
the
permitting
agency,
and
no
later
than
10
months
after
the
effective
date
of
the
emission
standards
of
this
subpart,
you
must
hold
at
least
one
informal
meeting
with
the
public
to
discuss
anticipated
activities
described
in
the
draft
NIC
for
achieving
compliance
with
the
emission
standards
of
this
subpart.
You
must
post
a
sign­
in
sheet
or
otherwise
provide
a
voluntary
opportunity
for
attendees
to
provide
their
names
and
addresses;
(
2)
You
must
submit
a
summary
of
the
meeting,
along
with
the
list
of
attendees
and
their
addresses
developed
under
paragraph
(
b)(
1)
of
this
section,
and
copies
of
any
written
comments
or
materials
submitted
at
the
meeting,
to
the
Administrator
as
part
of
the
final
NIC,
in
accordance
with
paragraph
(
b)(
1)(
iii)
of
this
section;
(
3)
You
must
provide
public
notice
of
the
NIC
meeting
at
least
30
days
prior
to
the
meeting.
You
must
provide
public
notice
in
all
of
the
following
forms:
(
i)
Newspaper
advertisement.
You
must
publish
a
notice
in
a
newspaper
of
general
circulation
in
the
county
or
equivalent
jurisdiction
of
your
facility.
In
addition,
you
must
publish
the
notice
in
newspapers
of
general
circulation
in
adjacent
counties
or
equivalent
jurisdiction
where
such
publication
would
be
necessary
to
inform
the
affected
public.
You
must
publish
the
notice
as
a
display
advertisement.
(
ii)
Visible
and
accessible
sign.
You
must
post
a
notice
on
a
clearly
marked
sign
at
or
near
the
source.
If
you
place
the
sign
on
the
site
of
the
hazardous
waste
combustor,
the
sign
must
be
large
enough
to
be
readable
from
the
nearest
spot
where
the
public
would
pass
by
the
site.
(
iii)
Broadcast
media
announcement.
You
must
broadcast
a
notice
at
least
once
on
at
least
one
local
radio
station
or
television
station.
(
iv)
Notice
to
the
facility
mailing
list.
You
must
provide
a
copy
of
the
notice
to
the
facility
mailing
list
in
accordance
with
§
124.10(
c)(
1)(
ix)
of
this
chapter.
(
4)
You
must
include
all
of
the
following
in
the
notices
required
under
paragraph
(
c)(
3)
of
this
section:
(
i)
The
date,
time,
and
location
of
the
meeting;
(
ii)
A
brief
description
of
the
purpose
of
the
meeting;
(
iii)
A
brief
description
of
the
source
and
proposed
operations,
including
the
address
or
a
map
(
e.
g.,
a
sketched
or
copied
street
map)
of
the
source
location;
(
iv)
A
statement
encouraging
people
to
contact
the
source
at
least
72
hours
before
the
meeting
if
they
need
special
access
to
participate
in
the
meeting;
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372
(
v)
A
statement
describing
how
the
draft
NIC
(
and
final
NIC,
if
requested)
can
be
obtained;
and
(
vi)
The
name,
address,
and
telephone
number
of
a
contact
person
for
the
NIC.
13.
Section
63.1211
is
amended
by:
a.
Revising
the
table
in
paragraph
(
b).
b.
Redesignating
paragraphs
(
c)
and
(
d)
as
(
d)
and
(
e).
c.
Adding
new
paragraph
(
c).
The
revisions
and
additions
read
as
follows:
§
63.1211
What
are
the
recordkeeping
and
reporting
requirements?
*
*
*
*
*
(
b)
*
*
*

Reference
Document,
Data,
or
Information
(
1)
63.1200,
63.10(
b)
and
(
c)
General.
Information
required
to
document
and
maintain
compliance
with
the
regulations
of
Subpart
EEE,
including
data
recorded
by
continuous
monitoring
systems
(
CMS),
and
copies
of
all
notifications,
reports,
plans,
and
other
documents
submitted
to
the
Administrator.

(
2)
63.1204(
d)(
1)(
ii),
63.1204A(
d)(
1)(
ii)
Documentation
of
mode
of
operation
changes
for
cement
kilns
with
in­
line
raw
mills.

(
3)
63.1204(
d)(
2)(
ii),
63.1204A(
d)(
2)(
ii)
Documentation
of
compliance
with
the
emission
averaging
requirements
for
cement
kilns
with
in­
line
raw
mills.

(
4)
63.1204(
e)(
2)(
ii),
63.1204A(
e)(
2)(
ii)
Documentation
of
compliance
with
the
emission
averaging
requirements
for
preheater
or
preheater/
precalciner
kilns
with
dual
stacks.

(
5)
63.1206(
b)(
1)(
ii)
If
you
elect
to
comply
with
all
applicable
requirements
and
standards
promulgated
under
authority
of
the
Clean
Air
Act,
including
Sections
112
and
129,
in
lieu
of
the
requirements
of
Subpart
EEE
when
not
burning
hazardous
waste,
you
must
document
in
the
operating
record
that
you
are
in
compliance
with
those
requirements.

(
6)
63.1206(
b)(
5)(
ii)
Documentation
that
a
change
will
not
adversely
affect
compliance
with
the
emission
standards
or
operating
requirements.

(
7)
63.1206(
b)(
11)
Calculation
of
hazardous
waste
residence
time.

(
8)
63.1206(
c)(
2)
Startup,
shutdown,
and
malfunction
plan.

(
9)
63.1206(
c)(
2)(
v)(
A)
Documentation
of
your
investigation
and
evaluation
of
excessive
exceedances
during
malfunctions.
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373
(
10)
63.1206(
c)(
3)(
v)
Corrective
measures
for
any
automatic
waste
feed
cutoff
that
results
in
an
exceedance
of
an
emission
standard
or
operating
parameter
limit.

(
11)
63.1206(
c)(
3)(
vii)
Documentation
and
results
of
the
automatic
waste
feed
cutoff
operability
testing.

(
12)
63.1206(
c)(
4)(
ii)
Emergency
safety
vent
operating
plan.

(
13)
63.1206(
c)(
4)(
iii)
Corrective
measures
for
any
emergency
safety
vent
opening.

(
14)
63.1206(
c)(
5)(
ii)
Method
used
for
control
of
combustion
system
leaks.

(
15)
63.1206(
c)(
6)
Operator
training
and
certification
program.

(
16)
63.1206(
c)(
7)(
i)(
D)
Operation
and
maintenance
plan.

(
17)
63.1209(
c)(
2)
Feedstream
analysis
plan.

(
18)
63.1209(
k)(
6)(
iii),
63.1209(
k)(
7)(
ii),
63.1209(
k)(
9)(
ii),
63.1209(
o)(
4)(
iii)
Documentation
that
a
substitute
activated
carbon,
dioxin/
furan
formation
reaction
inhibitor,
or
dry
scrubber
sorbent
will
provide
the
same
level
of
control
as
the
original
material.

(
19)
63.1209(
k)(
7)(
i)(
C)
Results
of
carbon
bed
performance
monitoring.

(
20)
63.1209(
q)
Documentation
of
changes
in
modes
of
operation.

(
21)
63.1211(
d)
Documentation
of
compliance.

*
*
*
*
*
(
c)
Compliance
progress
reports
associated
with
the
notification
of
intent
to
comply.
(
1)
General.
Not
later
than
two
years
following
the
effective
date
of
the
emission
standards
of
this
subpart,
you
must
comply
with
the
following,
unless
you
comply
with
paragraph
(
c)(
2)(
ii)
of
this
section:
(
i)
Develop
engineering
design
for
any
physical
modifications
to
the
source
needed
to
comply
with
the
emission
standards
of
this
subpart;
(
ii)
Submit
applicable
construction
applications
to
the
Administrator;
and
(
iii)
Document
an
internal
or
external
commitment
of
resources,
i.
e.,
funds
or
personnel,
to
purchase,
fabricate,
and
install
any
equipment,
devices,
and
ancillary
structures
needed
to
comply
with
the
emission
standards
and
operating
requirements
of
this
subpart.
*
OMB
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374
(
2)
Progress
report.
(
i)
You
must
submit
to
the
Administrator
a
progress
report
not
later
than
two
years
following
the
effective
date
of
the
emission
standards
of
this
subpart,
which
contains
information
documenting
that
you
have
met
the
requirements
of
paragraph
(
c)(
1)
of
this
section
and
updates
the
information
you
previously
provided
in
your
NIC.
This
information
will
be
used
by
the
Administrator
to
determine
if
you
have
made
adequate
progress
towards
compliance
with
the
emission
standards
of
this
subpart.
In
any
evaluation
of
adequate
progress,
the
Administrator
may
consider
any
delays
in
a
source's
progress
caused
by
the
time
required
to
obtain
necessary
permits
(
e.
g.,
operating
and
construction
permits
or
licenses)
from
governmental
regulatory
agencies
when
the
sources
have
submitted
timely
and
complete
permit
applications.
(
ii)
If
you
can
comply
with
the
emission
standards
and
operating
requirements
of
this
subpart,
without
undertaking
any
of
the
activities
described
in
paragraph
(
c)(
1)
of
this
section,
you
must
submit
a
progress
report
documenting
either:
(
A)
That
you,
at
the
time
of
the
progress
report,
are
in
compliance
with
the
emission
standards
and
operating
requirements;
or
(
B)
The
steps
you
will
take
to
comply,
without
undertaking
any
of
the
activities
listed
in
paragraphs
(
c)(
1)(
i)
through
(
c)(
1)(
iii)
of
this
section.
(
3)
Schedule.
(
i)
You
must
include
in
the
progress
report
a
detailed
schedule
that
lists
key
dates
for
all
projects
that
will
bring
the
source
into
compliance
with
the
emission
standards
and
operating
requirements
of
this
subpart
for
the
time
period
between
submission
of
the
progress
report
and
the
compliance
date
of
the
emission
standards
and
operating
requirements
of
this
subpart.
(
ii)
The
schedule
must
contain
anticipated
or
actual
dates
for
all
of
the
following:
(
A)
Bid
and
award
dates,
as
necessary,
for
construction
contracts
and
equipment
supply
contractors;
(
B)
Milestones
such
as
ground
breaking,
completion
of
drawings
and
specifications,
equipment
deliveries,
intermediate
construction
completions,
and
testing;
(
C)
The
dates
on
which
applications
will
be
submitted
for
operating
and
construction
permits
or
licenses;
(
D)
The
dates
by
which
approvals
of
any
operating
and
construction
permits
or
licenses
are
anticipated;
and
(
E)
The
projected
date
by
which
you
expect
to
comply
with
the
emission
standards
and
operating
requirements
of
this
subpart.
(
4)
Sources
that
intend
to
cease
burning
hazardous
waste
prior
to
or
on
the
compliance
date.
(
i)
If
you
indicated
in
your
NIC
your
intent
to
cease
burning
hazardous
waste
and
do
so
prior
to
submitting
a
progress
report,
you
are
exempt
from
the
requirements
of
paragraphs
(
c)(
1)
through
(
c)(
3)
of
this
section.
However,
you
must
submit
and
include
in
your
progress
report
the
date
on
which
you
stopped
burning
hazardous
waste
and
the
date(
s)
you
submitted,
or
plan
to
submit
RCRA
closure
documents.
(
ii)
If
you
signify
in
the
progress
report,
submitted
not
later
than
two
years
following
the
effective
date
of
the
emission
standards
of
this
subpart,
your
intention
to
cease
burning
hazardous
waste,
you
must
stop
burning
hazardous
waste
on
or
before
the
compliance
date
of
the
emission
standards
of
this
subpart.
*
OMB
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Draft*

375
*
*
*
*
*
14.
Section
63.1212
is
added
to
read
as
follows:
§
63.1212
What
are
the
other
requirements
pertaining
to
the
NIC
and
associated
progress
report?
(
a)
Certification
of
intent
to
comply.
(
1)
The
Notice
of
Intent
to
Comply
(
NIC)
and
Progress
Report
must
contain
the
following
certification
signed
and
dated
by
an
authorized
representative
of
the
source:
I
certify
under
penalty
of
law
that
I
have
personally
examined
and
am
familiar
with
the
information
submitted
in
this
document
and
all
attachments
and
that,
based
on
my
inquiry
of
those
individuals
immediately
responsible
for
obtaining
the
information,
I
believe
that
the
information
is
true,
accurate,
and
complete.
I
am
aware
that
there
are
significant
penalties
for
submitting
false
information,
including
the
possibility
of
fine
and
imprisonment.
(
2)
An
authorized
representative
should
be
a
responsible
corporate
officer
(
for
a
corporation),
a
general
partner
(
for
a
partnership),
the
proprietor
(
of
a
sole
proprietorship),
or
a
principal
executive
officer
or
ranking
elected
official
(
for
a
municipality,
State,
Federal,
or
other
public
agency).
(
b)
Sources
that
begin
burning
hazardous
waste
after
the
effective
date
of
the
emission
standards
of
this
subpart.
(
1)
If
you
begin
to
burn
hazardous
waste
after
the
effective
date
of
the
emission
standards
of
this
subpart,
but
prior
to
nine
months
after
the
effective
date
of
the
emission
standards
of
this
subpart,
you
must
comply
with
the
requirements
of
§
§
63.1206(
a)(
2),
63.1210(
b)
and
(
c),
63.1211(
c),
and
paragraph
(
a)
of
this
section,
and
associated
time
frames
for
public
meetings
and
document
submittals.
(
2)
If
you
intend
to
begin
burning
hazardous
waste
more
than
nine
months
after
the
effective
date
of
the
emission
standards
of
this
subpart,
you
must
comply
with
the
requirements
of
§
§
63.1206(
a)(
2),
63.1210(
b)
and
(
c),
63.1211(
c),
and
paragraph
(
a)
of
this
section
prior
to
burning
hazardous
waste.
In
addition:
(
i)
You
must
make
a
draft
NIC
available
to
the
public,
notice
the
public
meeting,
conduct
a
public
meeting,
and
submit
a
final
NIC
prior
to
burning
hazardous
waste;
and
(
ii)
You
must
submit
your
progress
report
at
the
time
you
submit
your
final
NIC.
15.
Section
63.1214
is
amended
by
revising
paragraphs
(
c)(
1),
(
c)(
2),
(
c)(
3),
and
(
c)(
4)
to
read
as
follows:
§
63.1214
Implementation
and
enforcement.
*
*
*
*
*
(
c)
*
*
*
(
1)
Approval
of
alternatives
to
requirements
in
§
§
63.1200,
63.1203,
63.1203A,
63.1204,
63.1204A,
63.1205,
63.1205A,
63.1206(
a),
63.1215,
63.1216,
63.1217,
and
63.1218.
(
2)
Approval
of
major
alternatives
to
test
methods
under
§
§
63.7(
e)(
2)(
ii)
and
(
f),
63.1208(
b),
and
63.1209(
a)(
1),
as
defined
in
§
63.90,
and
as
required
in
this
subpart.
(
3)
Approval
of
major
alternatives
to
monitoring
under
§
§
63.8(
f)
and
63.1209(
a)(
5),
as
defined
in
§
63.90,
and
as
required
in
this
subpart.
(
4)
Approval
of
major
alternatives
to
recordkeeping
and
reporting
under
§
§
63.10(
f)
and
63.1211(
a)
through
(
d),
as
defined
in
§
63.90,
and
as
required
in
this
subpart.
16.
Section
§
63.1215
is
added
to
read
as
follows:
*
OMB
Review
Draft*

376
§
63.1215
What
are
the
alternative
risk­
based
standards
for
hydrogen
chloride
and
chlorine
gas?
[
To
be
added]

17.
Section
63.1216
is
added
to
read
as
follows:
§
63.1216
What
are
the
standards
for
solid
fuel­
fired
boilers
that
burn
hazardous
waste?
(
a)
Emission
limits
for
existing
sources.
You
must
not
discharge
or
cause
combustion
gases
to
be
emitted
into
the
atmosphere
that
contain:
(
1)
For
dioxin
and
furan,
either
carbon
monoxide
or
hydrocarbon
emissions
in
excess
of
the
limits
provided
by
paragraph
(
a)(
5)
of
this
section;
(
2)
Mercury
in
excess
of
10
ug/
dscm
corrected
to
7
percent
oxygen;
(
3)
Except
for
an
area
source
as
defined
in
§
63.2,
cadmium
and
lead
in
excess
of
170
ug/
dscm,
combined
emissions,
corrected
to
7
percent
oxygen;
(
4)
Except
for
an
area
source
as
defined
in
§
63.2,
arsenic,
beryllium,
and
chromium
in
excess
of
210
ug/
dscm,
combined
emissions,
corrected
to
7
percent
oxygen;
(
5)
For
carbon
monoxide
and
hydrocarbons,
either:
(
i)
Carbon
monoxide
in
excess
of
100
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis
and
corrected
to
7
percent
oxygen.
If
you
elect
to
comply
with
this
carbon
monoxide
standard
rather
than
the
hydrocarbon
standard
under
paragraph
(
a)(
5)(
ii)
of
this
section,
you
must
also
document
that,
during
the
destruction
and
removal
efficiency
(
DRE)
test
runs
or
their
equivalent
as
provided
by
§
63.1206(
b)(
7),
hydrocarbons
do
not
exceed
10
parts
per
million
by
volume
during
those
runs,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
or
(
ii)
Hydrocarbons
in
excess
of
10
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
(
6)
Except
for
an
area
source
as
defined
in
§
63.2,
hydrogen
chloride
and
chlorine
gas
in
excess
of
110
parts
per
million
by
volume,
combined
emissions,
expressed
as
a
chloride
(
Cl(­))
equivalent,
dry
basis
and
corrected
to
7
percent
oxygen;
and
(
7)
Except
for
an
area
source
as
defined
in
§
63.2,
particulate
matter
in
excess
of
68
mg/
dscm
corrected
to
7
percent
oxygen.
(
b)
Emission
limits
for
new
sources.
You
must
not
discharge
or
cause
combustion
gases
to
be
emitted
into
the
atmosphere
that
contain:
(
1)
For
dioxin
and
furan,
either
carbon
monoxide
or
hydrocarbon
emissions
in
excess
of
the
limits
provided
by
paragraph
(
b)(
5)
of
this
section;
(
2)
Mercury
in
excess
of
10
ug/
dscm
corrected
to
7
percent
oxygen;
(
3)
Except
for
an
area
source
as
defined
in
§
63.2,
cadmium
and
lead
in
excess
of
170
ug/
dscm,
combined
emissions,
corrected
to
7
percent
oxygen;
(
4)
Except
for
an
area
source
as
defined
in
§
63.2,
arsenic,
beryllium,
and
chromium
in
excess
of
190
ug/
dscm,
combined
emissions,
corrected
to
7
percent
oxygen;
*
OMB
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Draft*

377
(
5)
For
carbon
monoxide
and
hydrocarbons,
either:
(
i)
Carbon
monoxide
in
excess
of
100
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis
and
corrected
to
7
percent
oxygen.
If
you
elect
to
comply
with
this
carbon
monoxide
standard
rather
than
the
hydrocarbon
standard
under
paragraph
(
b)(
5)(
ii)
of
this
section,
you
must
also
document
that,
during
the
destruction
and
removal
efficiency
(
DRE)
test
runs
or
their
equivalent
as
provided
by
§
§
63.1206(
b)(
7),
hydrocarbons
do
not
exceed
10
parts
per
million
by
volume
during
those
runs,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
or
(
ii)
Hydrocarbons
in
excess
of
10
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
(
6)
Except
for
an
area
source
as
defined
in
§
63.2,
hydrogen
chloride
and
chlorine
gas
in
excess
of
73
parts
per
million
by
volume,
combined
emissions,
expressed
as
a
chloride
(
Cl(­))
equivalent,
dry
basis
and
corrected
to
7
percent
oxygen;
and
(
7)
Except
for
an
area
source
as
defined
in
§
63.2,
particulate
matter
in
excess
of
34
mg/
dscm
corrected
to
7
percent
oxygen.
(
c)
Destruction
and
removal
efficiency
(
DRE)
standard.
(
1)
99.99%
DRE.
Except
as
provided
in
paragraph
(
c)(
2)
of
this
section,
you
must
achieve
a
DRE
of
99.99%
for
each
principle
organic
hazardous
constituent
(
POHC)
designated
under
paragraph
(
c)(
3)
of
this
section.
You
must
calculate
DRE
for
each
POHC
from
the
following
equation:
DRE
=
[
1

(
Wout
/
Win)]
X
100%
Where:
Win
=
mass
feedrate
of
one
POHC
in
a
waste
feedstream;
and
Wout
=
mass
emission
rate
of
the
same
POHC
present
in
exhaust
emissions
prior
to
release
to
the
atmosphere.
(
2)
99.9999%
DRE.
If
you
burn
the
dioxin­
listed
hazardous
wastes
F020,
F021,
F022,
F023,
F026,
or
F027
(
see
§
261.31
of
this
chapter),
you
must
achieve
a
DRE
of
99.9999%
for
each
POHC
that
you
designate
under
paragraph
(
c)(
3)
of
this
section.
You
must
demonstrate
this
DRE
performance
on
POHCs
that
are
more
difficult
to
incinerate
than
tetra­,
penta­,
and
hexachlorodibenzo­
p­
dioxins
and
dibenzofurans.
You
must
use
the
equation
in
paragraph
(
c)(
1)
of
this
section
to
calculate
DRE
for
each
POHC.
In
addition,
you
must
notify
the
Administrator
of
your
intent
to
incinerate
hazardous
wastes
F020,
F021,
F022,
F023,
F026,
or
F027.
(
3)
Principal
organic
hazardous
constituents
(
POHCs).
(
i)
You
must
treat
the
POHCs
in
the
waste
feed
that
you
specify
under
paragraph
(
c)(
3)(
ii)
of
this
section
to
the
extent
required
by
paragraphs
(
c)(
1)
and
(
c)(
2)
of
this
section.
(
ii)
You
must
specify
one
or
more
POHCs
from
the
list
of
hazardous
air
pollutants
established
by
42
U.
S.
C.
7412(
b)(
1),
excluding
caprolactam
(
CAS
number
105602)
as
provided
by
§
63.60,
for
each
waste
to
be
burned.
You
must
base
this
specification
on
the
degree
of
difficulty
of
incineration
of
the
organic
constituents
in
the
waste
and
on
their
concentration
or
mass
in
the
waste
feed,
considering
the
results
of
waste
analyses
or
other
data
and
information.
(
d)
Significant
figures.
The
emission
limits
provided
by
paragraphs
(
a)
and
(
b)
of
this
section
are
presented
with
two
significant
figures.
Although
you
must
perform
intermediate
*
OMB
Review
Draft*

378
calculations
using
at
least
three
significant
figures,
you
may
round
the
resultant
emission
levels
to
two
significant
figures
to
document
compliance.
18.
Section
63.1217
is
added
to
read
as
follows:
§
63.1217
What
are
the
standards
for
liquid
fuel­
fired
boilers
that
burn
hazardous
waste?
(
a)
Emission
limits
for
existing
sources.
You
must
not
discharge
or
cause
combustion
gases
to
be
emitted
into
the
atmosphere
that
contain:
(
1)(
i)
Dioxin
and
furan
in
excess
of
0.40
ng
TEQ/
dscm
corrected
to
7
percent
oxygen
for
incinerators
equipped
with
either
a
waste
heat
boiler
or
dry
air
pollution
control
system;
or
(
ii)
Either
carbon
monoxide
or
hydrocarbon
emissions
in
excess
of
the
limits
provided
by
paragraph
(
a)(
5)
of
this
section
for
sources
not
equipped
with
either
a
waste
heat
boiler
or
dry
air
pollution
control
system;
(
iii)
A
source
equipped
a
wet
air
pollution
control
system
followed
by
a
dry
air
pollution
control
system
is
not
considered
to
be
a
dry
air
pollution
control
system,
and
a
source
equipped
with
a
dry
air
pollution
control
system
followed
a
wet
air
pollution
control
system
is
considered
to
be
a
dry
air
pollution
control
system
for
purposes
of
this
emission
limit;
(
2)
Mercury
in
excess
of
3.7
x
10­
6
lbs
mercury
emissions
attributable
to
the
hazardous
waste
per
million
British
thermal
unit
heat
input
from
the
hazardous
waste;
(
3)
Except
for
an
area
source
as
defined
in
§
63.2,
in
excess
of
1.1
x
10­
5
lbs
combined
emissions
of
cadmium
and
lead
attributable
to
the
hazardous
waste
per
million
British
thermal
unit
heat
input
from
the
hazardous
waste;
(
4)
Except
for
an
area
source
as
defined
in
§
63.2,
in
excess
of
1.1
x
10­
4
lbs
chromium
emissions
attributable
to
the
hazardous
waste
per
million
British
thermal
unit
heat
input
from
the
hazardous
waste;
(
5)
For
carbon
monoxide
and
hydrocarbons,
either:
(
i)
Carbon
monoxide
in
excess
of
100
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis
and
corrected
to
7
percent
oxygen.
If
you
elect
to
comply
with
this
carbon
monoxide
standard
rather
than
the
hydrocarbon
standard
under
paragraph
(
a)(
5)(
ii)
of
this
section,
you
must
also
document
that,
during
the
destruction
and
removal
efficiency
(
DRE)
test
runs
or
their
equivalent
as
provided
by
§
63.1206(
b)(
7),
hydrocarbons
do
not
exceed
10
parts
per
million
by
volume
during
those
runs,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
or
(
ii)
Hydrocarbons
in
excess
of
10
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
(
6)
Except
for
an
area
source
as
defined
in
§
63.2,
in
excess
of
2.5
x
10­
2
lbs
combined
emissions
of
hydrogen
chloride
and
chlorine
gas
attributable
to
the
hazardous
waste
per
million
British
thermal
unit
heat
input
from
the
hazardous
waste;
and
(
7)
Except
for
an
area
source
as
defined
in
§
63.2
or
as
provided
by
paragraph
(
e)(
2)
of
this
section,
particulate
matter
in
excess
of
59
mg/
dscm
corrected
to
7
percent
oxygen.
*
OMB
Review
Draft*

379
(
b)
Emission
limits
for
new
sources.
You
must
not
discharge
or
cause
combustion
gases
to
be
emitted
into
the
atmosphere
that
contain:
(
1)(
i)
Dioxin
and
furan
in
excess
of
0.015
ng
TEQ/
dscm
corrected
to
7
percent
oxygen
for
incinerators
equipped
with
either
a
waste
heat
boiler
or
dry
air
pollution
control
system;
or
(
ii)
Either
carbon
monoxide
or
hydrocarbon
emissions
in
excess
of
the
limits
provided
by
paragraph
(
a)(
5)
of
this
section
for
sources
not
equipped
with
either
a
waste
heat
boiler
or
dry
air
pollution
control
system;
(
iii)
A
source
equipped
a
wet
air
pollution
control
system
followed
by
a
dry
air
pollution
control
system
is
not
considered
to
be
a
dry
air
pollution
control
system,
and
a
source
equipped
with
a
dry
air
pollution
control
system
followed
a
wet
air
pollution
control
system
is
considered
to
be
a
dry
air
pollution
control
system
for
purposes
of
this
emission
limit;
(
2)
In
excess
of
3.8
x
10­
7
lbs
mercury
emissions
attributable
to
the
hazardous
waste
per
million
British
thermal
unit
heat
input
from
the
hazardous
waste;
(
3)
Except
for
an
area
source
as
defined
in
§
63.2,
in
excess
of
4.3
x
10­
6
lbs
combined
emissions
of
cadmium
and
lead
attributable
to
the
hazardous
waste
per
million
British
thermal
unit
heat
input
from
the
hazardous
waste;
(
4)
Except
for
an
area
source
as
defined
in
§
63.2,
in
excess
of
3.6
x
10­
5
lbs
chromium
emissions
attributable
to
the
hazardous
waste
per
million
British
thermal
unit
heat
input
from
the
hazardous
waste;
(
5)
For
carbon
monoxide
and
hydrocarbons,
either:
(
i)
Carbon
monoxide
in
excess
of
100
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis
and
corrected
to
7
percent
oxygen.
If
you
elect
to
comply
with
this
carbon
monoxide
standard
rather
than
the
hydrocarbon
standard
under
paragraph
(
a)(
5)(
ii)
of
this
section,
you
must
also
document
that,
during
the
destruction
and
removal
efficiency
(
DRE)
test
runs
or
their
equivalent
as
provided
by
§
63.1206(
b)(
7),
hydrocarbons
do
not
exceed
10
parts
per
million
by
volume
during
those
runs,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
or
(
ii)
Hydrocarbons
in
excess
of
10
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
(
6)
Except
for
an
area
source
as
defined
in
§
63.2,
in
excess
of
7.2
x
10­
4
lbs
combined
emissions
of
hydrogen
chloride
and
chlorine
gas
attributable
to
the
hazardous
waste
per
million
British
thermal
unit
heat
input
from
the
hazardous
waste;
and
(
7)
Except
for
an
area
source
as
defined
in
§
63.2
or
as
provided
in
paragraph
(
e)(
3)
of
this
section,
particulate
matter
in
excess
of
9.8
mg/
dscm
corrected
to
7
percent
oxygen.
(
c)
Destruction
and
removal
efficiency
(
DRE)
standard.
(
1)
99.99%
DRE.
Except
as
provided
in
paragraph
(
c)(
2)
of
this
section,
you
must
achieve
a
DRE
of
99.99%
for
each
principle
organic
hazardous
constituent
(
POHC)
designated
under
paragraph
(
c)(
3)
of
this
section.
You
must
calculate
DRE
for
each
POHC
from
the
following
equation:
DRE
=
[
1

(
Wout
/
Win)]
X
100%
Where:
Win
=
mass
feedrate
of
one
POHC
in
a
waste
feedstream;
and
*
OMB
Review
Draft*

380
Wout
=
mass
emission
rate
of
the
same
POHC
present
in
exhaust
emissions
prior
to
release
to
the
atmosphere.
(
2)
99.9999%
DRE.
If
you
burn
the
dioxin­
listed
hazardous
wastes
F020,
F021,
F022,
F023,
F026,
or
F027
(
see
§
261.31
of
this
chapter),
you
must
achieve
a
DRE
of
99.9999%
for
each
POHC
that
you
designate
under
paragraph
(
c)(
3)
of
this
section.
You
must
demonstrate
this
DRE
performance
on
POHCs
that
are
more
difficult
to
incinerate
than
tetra­,
penta­,
and
hexachlorodibenzo­
p­
dioxins
and
dibenzofurans.
You
must
use
the
equation
in
paragraph
(
c)(
1)
of
this
section
to
calculate
DRE
for
each
POHC.
In
addition,
you
must
notify
the
Administrator
of
your
intent
to
incinerate
hazardous
wastes
F020,
F021,
F022,
F023,
F026,
or
F027.
(
3)
Principal
organic
hazardous
constituents
(
POHCs).
(
i)
You
must
treat
the
POHCs
in
the
waste
feed
that
you
specify
under
paragraph
(
c)(
3)(
ii)
of
this
section
to
the
extent
required
by
paragraphs
(
c)(
1)
and
(
c)(
2)
of
this
section.
(
ii)
You
must
specify
one
or
more
POHCs
from
the
list
of
hazardous
air
pollutants
established
by
42
U.
S.
C.
7412(
b)(
1),
excluding
caprolactam
(
CAS
number
105602)
as
provided
by
§
63.60,
for
each
waste
to
be
burned.
You
must
base
this
specification
on
the
degree
of
difficulty
of
incineration
of
the
organic
constituents
in
the
waste
and
on
their
concentration
or
mass
in
the
waste
feed,
considering
the
results
of
waste
analyses
or
other
data
and
information.
(
d)
Significant
figures.
The
emission
limits
provided
by
paragraphs
(
a)
and
(
b)
of
this
section
are
presented
with
two
significant
figures.
Although
you
must
perform
intermediate
calculations
using
at
least
three
significant
figures,
you
may
round
the
resultant
emission
levels
to
two
significant
figures
to
document
compliance.
(
e)
Alternative
to
the
particulate
matter
standard
for
liquid
fuel­
fired
boilers.
(
1)
General.
In
lieu
of
complying
with
the
applicable
particulate
matter
standards
of
paragraphs
(
a)(
7)
and
(
b)(
7)
of
this
section,
you
may
elect
to
comply
with
the
following
alternative
metal
emission
control
requirements:
(
2)
Alternative
metal
emission
control
requirements
for
existing
sources.
(
i)
You
must
not
discharge
or
cause
combustion
gases
to
be
emitted
into
the
atmosphere
that
contain
in
excess
of
1.1
x
10­
5
lbs
combined
emissions
of
cadmium,
lead,
and
selenium
attributable
to
the
hazardous
waste
per
million
British
thermal
unit
heat
input
from
the
hazardous
waste,
corrected
to
7
percent
oxygen;
and,
(
ii)
You
must
not
discharge
or
cause
combustion
gases
to
be
emitted
into
the
atmosphere
that
contain
in
excess
of
7.7
x
10­
5
lbs
combined
emissions
of
antimony,
arsenic,
beryllium,
chromium,
cobalt,
manganese,
and
nickel
attributable
to
the
hazardous
waste
per
million
British
thermal
unit
heat
input
from
the
hazardous
waste,
corrected
to
7
percent
oxygen.
(
3)
Alternative
metal
emission
control
requirements
for
new
sources.
(
i)
You
must
not
discharge
or
cause
combustion
gases
to
be
emitted
into
the
atmosphere
that
contain
in
excess
of
4.3
x
10­
6
lbs
combined
emissions
of
cadmium,
lead,
and
selenium
attributable
to
the
hazardous
waste
per
million
British
thermal
unit
heat
input
from
the
hazardous
waste,
corrected
to
7
percent
oxygen;
and,
(
ii)
You
must
not
discharge
or
cause
combustion
gases
to
be
emitted
into
the
atmosphere
that
contain
in
excess
of
3.6
x
10­
5
lbs
combined
emissions
of
antimony,
arsenic,
beryllium,
chromium,
cobalt,
manganese,
and
nickel
attributable
to
the
hazardous
waste
per
million
British
*
OMB
Review
Draft*

381
thermal
unit
heat
input
from
the
hazardous
waste,
corrected
to
7
percent
oxygen.
19.
Section
63.1218
is
added
to
read
as
follows:
§
63.1218
What
are
the
standards
for
hydrochloric
acid
production
furnaces
that
burn
hazardous
waste?
(
a)
Emission
limits
for
existing
sources.
You
must
not
discharge
or
cause
combustion
gases
to
be
emitted
into
the
atmosphere
that
contain:
(
1)
Dioxin
and
furan
emissions
in
excess
of
0.40
ng
TEQ/
dscm,
corrected
to
7
percent
oxygen;
(
2)
For
mercury,
hydrogen
chloride
and
chlorine
gas
emissions
in
excess
of
the
levels
provided
by
paragraph
(
a)(
6)
of
this
section;
(
3)
For
lead
and
cadmium,
hydrogen
chloride
and
chlorine
gas
emissions
in
excess
of
the
levels
provided
by
paragraph
(
a)(
6)
of
this
section;
(
4)
For
arsenic,
beryllium,
and
chromium,
hydrogen
chloride
and
chlorine
gas
emissions
in
excess
of
the
levels
provided
by
paragraph
(
a)(
6)
of
this
section;
(
5)
For
carbon
monoxide
and
hydrocarbons,
either:
(
i)
Carbon
monoxide
in
excess
of
100
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis
and
corrected
to
7
percent
oxygen.
If
you
elect
to
comply
with
this
carbon
monoxide
standard
rather
than
the
hydrocarbon
standard
under
paragraph
(
a)(
5)(
ii)
of
this
section,
you
must
also
document
that,
during
the
destruction
and
removal
efficiency
(
DRE)
test
runs
or
their
equivalent
as
provided
by
§
63.1206(
b)(
7),
hydrocarbons
do
not
exceed
10
parts
per
million
by
volume
during
those
runs,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
or
(
ii)
Hydrocarbons
in
excess
of
10
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
(
6)
For
hydrogen
chloride
and
chlorine
gas,
either:
(
i)
Emission
in
excess
of
14
parts
per
million
by
volume,
combined
emissions,
expressed
as
a
chloride
(
Cl(­))
equivalent,
dry
basis
and
corrected
to
7
percent
oxygen;
or
(
ii)
Emissions
greater
than
the
levels
that
would
be
emitted
if
the
source
is
achieving
a
system
removal
efficiency
(
SRE)
of
less
than
99.9927
percent
for
total
chlorine
and
chloride
fed
to
the
combustor.
You
must
calculate
SRE
from
the
following
equation:
SRE
=
[
1

(
Cl
out
/
Cl
in)]
X
100%
Where:
Cl
in
=
mass
feedrate
of
total
chlorine
or
chloride
in
all
feedstreams,
reported
as
chloride;
and
Cl
out
=
mass
emission
rate
of
hydrogen
chloride
and
chlorine
gas,
reported
as
chloride,
in
exhaust
emissions
prior
to
release
to
the
atmosphere.
(
7)
For
particulate
matter,
hydrogen
chloride
and
chlorine
gas
emissions
in
excess
of
the
levels
provided
by
paragraph
(
a)(
6)
of
this
section.
(
b)
Emission
limits
for
new
sources.
You
must
not
discharge
or
cause
combustion
gases
to
be
emitted
into
the
atmosphere
that
contain:
(
1)
Dioxin
and
furan
emissions
in
excess
of
0.40
ng
TEQ/
dscm,
corrected
to
7
percent
oxygen;
*
OMB
Review
Draft*

382
(
2)
For
mercury,
hydrogen
chloride
and
chlorine
gas
emissions
in
excess
of
the
levels
provided
by
paragraph
(
a)(
6)
of
this
section;
(
3)
For
lead
and
cadmium,
hydrogen
chloride
and
chlorine
gas
emissions
in
excess
of
the
levels
provided
by
paragraph
(
a)(
6)
of
this
section;
(
4)
For
arsenic,
beryllium,
and
chromium,
hydrogen
chloride
and
chlorine
gas
emissions
in
excess
of
the
levels
provided
by
paragraph
(
a)(
6)
of
this
section;
(
5)
For
carbon
monoxide
and
hydrocarbons,
either:
(
i)
Carbon
monoxide
in
excess
of
100
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis
and
corrected
to
7
percent
oxygen.
If
you
elect
to
comply
with
this
carbon
monoxide
standard
rather
than
the
hydrocarbon
standard
under
paragraph
(
b)(
5)(
ii)
of
this
section,
you
must
also
document
that,
during
the
destruction
and
removal
efficiency
(
DRE)
test
runs
or
their
equivalent
as
provided
by
§
63.1206(
b)(
7),
hydrocarbons
do
not
exceed
10
parts
per
million
by
volume
during
those
runs,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
or
(
ii)
Hydrocarbons
in
excess
of
10
parts
per
million
by
volume,
over
an
hourly
rolling
average
(
monitored
continuously
with
a
continuous
emissions
monitoring
system),
dry
basis,
corrected
to
7
percent
oxygen,
and
reported
as
propane;
(
6)
For
hydrochloric
acid
and
chlorine
gas,
either:
(
i)
Emission
in
excess
of
1.2
parts
per
million
by
volume,
combined
emissions,
expressed
as
a
chloride
(
Cl(­))
equivalent,
dry
basis
and
corrected
to
7
percent
oxygen;
or
(
ii)
Emissions
greater
than
the
levels
that
would
be
emitted
if
the
source
is
achieving
a
system
removal
efficiency
(
SRE)
of
less
than
99.99937
percent
for
total
chlorine
and
chloride
fed
to
the
combustor.
You
must
calculate
SRE
from
the
following
equation:
SRE
=
[
1

(
Cl
out
/
Cl
in)]
X
100%
Where:
Cl
in
=
mass
feedrate
of
total
chlorine
or
chloride
in
all
feedstreams,
reported
as
chloride;
and
Cl
out
=
mass
emission
rate
of
hydrogen
chloride
and
chlorine
gas,
reported
as
chloride,
in
exhaust
emissions
prior
to
release
to
the
atmosphere.
(
7)
For
particulate
matter,
hydrogen
chloride
and
chlorine
gas
emissions
in
excess
of
the
levels
provided
by
paragraph
(
a)(
6)
of
this
section.
(
c)
Destruction
and
removal
efficiency
(
DRE)
standard.
(
1)
99.99%
DRE.
Except
as
provided
in
paragraph
(
c)(
2)
of
this
section,
you
must
achieve
a
DRE
of
99.99%
for
each
principle
organic
hazardous
constituent
(
POHC)
designated
under
paragraph
(
c)(
3)
of
this
section.
You
must
calculate
DRE
for
each
POHC
from
the
following
equation:
DRE
=
[
1

(
Wout
/
Win)]
X
100%
Where:
Win
=
mass
feedrate
of
one
POHC
in
a
waste
feedstream;
and
Wout
=
mass
emission
rate
of
the
same
POHC
present
in
exhaust
emissions
prior
to
release
to
the
atmosphere.
(
2)
99.9999%
DRE.
If
you
burn
the
dioxin­
listed
hazardous
wastes
F020,
F021,
F022,
F023,
F026,
or
F027
(
see
§
261.31
of
this
chapter),
you
must
achieve
a
DRE
of
99.9999%
for
each
POHC
that
you
designate
under
paragraph
(
c)(
3)
of
this
section.
You
must
demonstrate
this
DRE
performance
on
POHCs
that
are
more
difficult
to
incinerate
than
tetra­,
penta­,
and
*
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383
hexachlorodibenzo­
p­
dioxins
and
dibenzofurans.
You
must
use
the
equation
in
paragraph
(
c)(
1)
of
this
section
to
calculate
DRE
for
each
POHC.
In
addition,
you
must
notify
the
Administrator
of
your
intent
to
incinerate
hazardous
wastes
F020,
F021,
F022,
F023,
F026,
or
F027.
(
3)
Principal
organic
hazardous
constituents
(
POHCs).
(
i)
You
must
treat
the
POHCs
in
the
waste
feed
that
you
specify
under
paragraph
(
c)(
3)(
ii)
of
this
section
to
the
extent
required
by
paragraphs
(
c)(
1)
and
(
c)(
2)
of
this
section.
(
ii)
You
must
specify
one
or
more
POHCs
from
the
list
of
hazardous
air
pollutants
established
by
42
U.
S.
C.
7412(
b)(
1),
excluding
caprolactam
(
CAS
number
105602)
as
provided
by
§
63.60,
for
each
waste
to
be
burned.
You
must
base
this
specification
on
the
degree
of
difficulty
of
incineration
of
the
organic
constituents
in
the
waste
and
on
their
concentration
or
mass
in
the
waste
feed,
considering
the
results
of
waste
analyses
or
other
data
and
information.
(
d)
Significant
figures.
The
emission
limits
provided
by
paragraphs
(
a)
and
(
b)
of
this
section
are
presented
with
two
significant
figures.
Although
you
must
perform
intermediate
calculations
using
at
least
three
significant
figures,
you
may
round
the
resultant
emission
levels
to
two
significant
figures
to
document
compliance.
PART
264
 
STANDARDS
FOR
OWNERS
AND
OPERATORS
OF
HAZARDOUS
WASTE
TREATMENT,
STORAGE,
AND
DISPOSAL
FACILITIES
1.
The
authority
citation
for
part
264
continues
to
read
as
follows:
Authority:
42
U.
S.
C.
6905,
6912(
a),
6924,
6925,
6927,
6928(
h),
and
6974.
2.
Section
264.340
is
amended
by
revising
the
first
sentence
of
paragraph
(
b)(
1)
and
adding
paragraph
(
b)(
5)
to
read
as
follows:
§
264.340
Applicability.
*
*
*
*
*
(
b)
*
*
*
(
1)
Except
as
provided
by
paragraphs
(
b)(
2)
through
(
b)(
5)
of
this
section,
the
standards
of
this
part
no
longer
apply
when
an
owner
or
operator
demonstrates
compliance
with
the
maximum
achievable
control
technology
(
MACT)
requirements
of
part
63,
subpart
EEE,
of
this
chapter
by
conducting
a
comprehensive
performance
test
and
submitting
to
the
Administrator
a
Notification
of
Compliance
under
§
§
63.1207(
j)
and
63.1210(
d)
of
this
chapter
documenting
compliance
with
the
requirements
of
part
63,
subpart
EEE,
of
this
chapter.
*
*
*
*
*
*
*
*
(
5)
The
particulate
matter
standard
of
§
264.343(
c)
remains
in
effect
for
incinerators
that
elect
to
comply
with
the
alternative
to
the
particulate
matter
standard
of
§
63.1203A(
e)
of
this
chapter.
*
*
*
*
*
PART
265
 
INTERIM
STATUS
STANDARDS
FOR
OWNERS
AND
OPERATORS
OF
HAZARDOUS
WASTE
TREATMENT,
STORAGE,
AND
DISPOSAL
FACILITIES
1.
The
authority
citation
for
part
265
continues
to
read
as
follows:
Authority:
42
U.
S.
C.
6905,
6906,
6912,
6922,
6923,
6924,
6925,
6935,
6936,
and
6937.
2.
Section
265.340
is
amended
by
revising
paragraph
(
b)(
1)
to
read
as
follows:
§
265.340
Applicability.
*
*
*
*
*
*
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384
(
b)
*
*
*
(
1)
Except
as
provided
by
paragraphs
(
b)(
2)
and
(
b)(
3)
of
this
section,
the
standards
of
this
part
no
longer
apply
when
an
owner
or
operator
demonstrates
compliance
with
the
maximum
achievable
control
technology
(
MACT)
requirements
of
part
63,
subpart
EEE,
of
this
chapter
by
conducting
a
comprehensive
performance
test
and
submitting
to
the
Administrator
a
Notification
of
Compliance
under
§
§
63.1207(
j)
and
63.1210(
d)
of
this
chapter
documenting
compliance
with
the
requirements
of
part
63,
subpart
EEE,
of
this
chapter.
*
*
*
*
*
PART
266
 
STANDARDS
FOR
THE
MANAGEMENT
OF
SPECIFIC
HAZARDOUS
WASTES
AND
SPECIFIC
TYPES
OF
HAZARDOUS
WASTE
MANAGEMENT
FACILITIES
1.
The
authority
citation
for
part
266
continues
to
read
as
follows:
Authority:
42
U.
S.
C.
1006,
2002(
a),
3001­
3009,
3014,
6905,
6906,
6912,
6921,
6922,
6924­
6927,
6934,
and
6937.
2.
Section
266.100
is
amended
by
revising
the
first
sentence
of
paragraph
(
b)(
1)
and
adding
paragraph
(
b)(
3)
to
read
as
follows:
§
266.100
Applicability.
*
*
*
*
*
(
b)
*
*
*
(
1)
Except
as
provided
by
paragraphs
(
b)(
2)
and
(
b)(
3)
of
this
section,
the
standards
of
this
part
no
longer
apply
when
an
owner
or
operator
demonstrates
compliance
with
the
maximum
achievable
control
technology
(
MACT)
requirements
of
part
63,
subpart
EEE,
of
this
chapter
by
conducting
a
comprehensive
performance
test
and
submitting
to
the
Administrator
a
Notification
of
Compliance
under
§
§
63.1207(
j)
and
63.1210(
d)
of
this
chapter
documenting
compliance
with
the
requirements
of
part
63,
subpart
EEE,
of
this
chapter.
*
*
*
*
*
*
*
*
(
3)
If
you
own
or
operate
a
boiler
or
hydrochloric
acid
furnace
that
is
an
area
source
under
§
63.2
of
this
chapter
and
you
elect
not
to
comply
with
the
emission
standards
under
§
§
63.1216,
63.1217,
and
63.1218
of
this
chapter
for
particulate
matter,
semivolatile
and
low
volatile
metals,
and
total
chlorine,
you
also
remain
subject
to:
(
i)
Section
266.105­­
Standards
to
control
particulate
matter;
(
ii)
Section
266.106­­
Standards
to
control
metals
emissions,
except
for
mercury;
and
(
ii)
Section
266.107­­
Standards
to
control
hydrogen
chloride
and
chlorine
gas.
*
*
*
*
*
PART
270
 
EPA
ADMINISTERED
PERMIT
PROGRAMS:
THE
HAZARDOUS
WASTE
PERMIT
PROGRAM
1.
The
authority
citation
for
part
270
continues
to
read
as
follows:
Authority:
42
U.
S.
C.
6905,
6912,
6924,
6925,
6927,
6939,
and
6974.
2.
Section
270.10
is
amended
by
adding
paragraph
(
l)
to
read
as
follows:
§
270.10
General
application
requirements.
*
*
*
*
*
(
l)
If
the
Director
concludes
that
there
is
reason
to
believe
that
compliance
with
the
standards
in
40
CFR
Parts
63,
Subpart
EEE
alone
may
not
be
protective
of
human
health
or
the
*
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385
environment,
the
Director
shall
require
additional
information
or
assessment(
s)
that
the
Director
determines
are
necessary
to
ensure
protection
of
human
health
and
the
environment.
The
Director
also
may
require
a
permittee
or
an
applicant
to
provide
information
necessary
to
determine
whether
such
an
assessment(
s)
should
be
required.
3.
Section
270.19
is
amended
by
revising
paragraph
(
e)
to
reads
as
follows:
§
270.19
Specific
part
B
information
requirements
for
incinerators.
*
*
*
*
*
(
e)
When
an
owner
or
operator
demonstrates
compliance
with
the
air
emission
standards
and
limitations
in
part
63,
subpart
EEE,
of
this
chapter
(
i.
e.,
by
conducting
a
comprehensive
performance
test
and
submitting
a
Notification
of
Compliance
under
§
§
63.1207(
j)
and
63.1210(
d)
of
this
chapter
documenting
compliance
with
all
applicable
requirements
of
part
63,
subpart
EEE,
of
this
chapter),
the
requirements
of
this
section
do
not
apply,
except
those
provisions
the
Director
determines
are
necessary
to
ensure
compliance
with
§
§
264.345(
a)
and
264.345(
c)
of
this
chapter
if
you
elect
to
comply
with
§
270.235(
a)(
1)(
i)
to
minimize
emissions
of
toxic
compounds
from
startup,
shutdown,
and
malfunction
events.
Nevertheless,
the
Director
may
apply
the
provisions
of
this
section,
on
a
case­
by­
case
basis,
for
purposes
of
information
collection
in
accordance
with
§
§
270.10(
k),
270.10(
l),
270.32(
b)(
2),
and
270.32(
b)(
3)
of
this
chapter.
3.
Section
270.22
is
amended
by
revising
the
introductory
text
to
read
as
follows:
§
270.22
Specific
part
B
information
requirements
for
boilers
and
industrial
furnaces
burning
hazardous
waste
When
an
owner
or
operator
of
a
cement
kiln,
lightweight
aggregate
kiln,
solid
fuel­
fired
boiler,
liquid
fuel­
fired
boiler,
or
hydrochloric
acid
production
furnace
demonstrates
compliance
with
the
air
emission
standards
and
limitations
in
part
63,
subpart
EEE,
of
this
chapter
(
i.
e.,
by
conducting
a
comprehensive
performance
test
and
submitting
a
Notification
of
Compliance
under
§
§
63.1207(
j)
and
63.1210(
d)
of
this
chapter
documenting
compliance
with
all
applicable
requirements
of
part
63,
subpart
EEE,
of
this
chapter),
the
requirements
of
this
section
do
not
apply.
The
requirements
of
this
section
do
apply,
however,
if
the
Director
determines
certain
provisions
are
necessary
to
ensure
compliance
with
§
§
266.102(
e)(
1)
and
266.102(
e)(
2)(
iii)
of
this
chapter
if
you
elect
to
comply
with
§
270.235(
a)(
1)(
i)
to
minimize
emissions
of
toxic
compounds
from
startup,
shutdown,
and
malfunction
events;
or
if
you
are
an
area
source
and
elect
to
comply
with
the
§
§
266.105,
266.106,
and
266.107
standards
and
associated
requirements
for
particulate
matter,
hydrogen
chloride
and
chlorine
gas,
and
non­
mercury
metals;
or
the
Director
determines
certain
provisions
apply,
on
a
case­
by­
case
basis,
for
purposes
of
information
collection
in
accordance
with
§
§
270.10(
k),
270.10(
l),
270.32(
b)(
2),
and
270.32(
b)(
3).
*
*
*
*
*
4.
Section
270.32
is
amended
by
adding
paragraph
(
b)(
3)
to
read
as
follows:
§
270.32
Establishing
permit
conditions.
*
*
*
*
*
(
b)
*
*
*
(
3)
If,
as
the
result
of
an
assessment(
s)
or
other
information,
the
Administrator
or
Director
determines
that
conditions
are
necessary
in
addition
to
those
required
under
40
CFR
Parts
63,
Subpart
EEE,
264
or
266
to
ensure
protection
of
human
health
and
the
environment,
he
shall
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386
include
those
terms
and
conditions
in
a
RCRA
permit
for
a
hazardous
waste
combustion
unit.
*
*
*
*
*
5.
Section
270.42
is
amended
by:
a.
Revising
paragraph
(
j)(
1).
b.
Redesignating
paragraph
(
j)(
2)
as
(
j)(
3).
c.
Adding
new
paragraph
(
j)(
2).
d.
Adding
new
paragraph
(
k);
and
e.
Adding
a
new
entry
10
in
numerical
order
in
section
L
of
Appendix
I.
The
revisions
and
additions
reads
as
follows:
§
270.42
Permit
modification
at
the
request
of
the
permittee.
*
*
*
*
*
(
j)
*
*
*
(
1)
Facility
owners
or
operators
must
have
complied
with
the
Notification
of
Intent
to
Comply
(
NIC)
requirements
of
40
CFR
63.1210
that
were
in
effect
prior
to
October
11,
2000,
(
See
40
CFR
Part
63
Revised
as
of
July
1,
2000)
in
order
to
request
a
permit
modification
under
this
section
for
the
purpose
of
technology
changes
needed
to
meet
the
40
CFR
63.1203,
63.1204,
and
63.1205
standards.
(
2)
Facility
owners
or
operators
must
comply
with
the
Notification
of
Intent
to
Comply
(
NIC)
requirements
of
40
CFR
63.1210(
b)
and
63.1212
before
a
permit
modification
can
be
requested
under
this
section
for
the
purpose
of
technology
changes
needed
to
meet
the
40
CFR
63.1203A,
63.1204A,
63.1205A,
63.1215,
63.1216,
63.1217,
and
63.1218
standards
promulgated
on
[
insert
date
of
publication
of
the
final
rule
in
the
Federal
Register].
*
*
*
*
*
(
k)
Waiver
of
RCRA
permitting
requirements
in
support
of
transition
to
the
part
63
MACT
standards.
(
1)
You
may
request
to
have
specific
RCRA
operating
and
emissions
limits
waived
by
submitting
a
Class
1
permit
modification
request
under
Appendix
I
of
this
section,
section
L(
10).
You
must:
(
i)
Identify
the
specific
RCRA
permit
operating
and
emissions
limits
which
you
are
requesting
to
waive;
(
ii)
Provide
an
explanation
of
why
the
changes
are
necessary
in
order
to
minimize
or
eliminate
conflicts
between
the
RCRA
permit
and
MACT
compliance;
and
(
iii)
Discuss
how
the
revised
provisions
will
be
sufficiently
protective.
(
2)
To
request
this
modification
in
conjunction
with
MACT
performance
testing
where
permit
limits
may
only
be
waived
during
actual
test
events
and
pretesting,
as
defined
under
40
CFR
63.1207(
h)(
2)(
i)
and
(
ii),
for
an
aggregate
time
not
to
exceed
720
hours
of
operation
(
renewable
at
the
discretion
of
the
Administrator)
you
must:
(
i)
Demonstrate
that
your
site­
specific
emissions
test
plan
and
continuous
monitoring
system
performance
evaluation
test
plan
have
been
submitted
and
approved
by
the
Administrator
as
required
in
40
CFR
63.1207(
e),
and
(
ii)
Submit
your
modification
request
upon
approval
of
your
test
plan.
(
3)
The
Director
shall
approve
or
deny
the
request
within
30
days
of
receipt
of
the
request.
The
Director
may,
at
his
or
her
discretion,
extend
this
30
day
deadline
one
time
for
up
to
30
days
*
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387
by
notifying
the
facility
owner
or
operator.
*
*
*
*
*
Appendix
I
to
§
270.42­­
Classification
of
Permit
Modification.

Modifications
Class
*
*
*
*
*
*
*
10.
Changes
to
RCRA
permit
provisions
needed
to
support
transition
to
40
CFR
part
63
(
Subpart
EEE
 
National
Emission
Standards
for
Hazardous
Air
Pollutants
From
Hazardous
Waste
Combustors),
provided
the
procedures
of
§
270.42(
k)
are
followed.
*
*
*
*
*
*
*
\
1\
1
*
*
*
*
*
6.
Section
270.62
is
amended
by
revising
the
introductory
text
to
read
as
follows:
§
270.62
Hazardous
waste
incinerator
permits.
When
an
owner
or
operator
demonstrates
compliance
with
the
air
emission
standards
and
limitations
in
part
63,
subpart
EEE,
of
this
chapter
(
i.
e.,
by
conducting
a
comprehensive
performance
test
and
submitting
a
Notification
of
Compliance
under
§
§
63.1207(
j)
and
63.1210(
d)
of
this
chapter
documenting
compliance
with
all
applicable
requirements
of
part
63,
subpart
EEE,
of
this
chapter),
the
requirements
of
this
section
do
not
apply,
except
those
provisions
the
Director
determines
are
necessary
to
ensure
compliance
with
§
§
264.345(
a)
and
264.345(
c)
of
this
chapter
if
you
elect
to
comply
with
§
270.235(
a)(
1)(
i)
to
minimize
emissions
of
toxic
compounds
from
startup,
shutdown,
and
malfunction
events.
Nevertheless,
the
Director
may
apply
the
provisions
of
this
section,
on
a
case­
by­
case
basis,
for
purposes
of
information
collection
in
accordance
with
§
§
270.10(
k),
270.10(
l),
270.32(
b)(
2),
and
270.32(
b)(
3)
of
this
chapter.
*
*
*
*
*
7.
Section
270.66
is
amended
by
revising
the
introductory
text
to
read
as
follows:
§
270.66
Permits
for
boilers
and
industrial
furnaces
burning
hazardous
waste
When
an
owner
or
operator
of
a
cement
kiln,
lightweight
aggregate
kiln,
solid
fuel­
fired
boiler,
liquid
fuel­
fired
boiler,
or
hydrochloric
acid
production
furnace
demonstrates
compliance
with
the
air
emission
standards
and
limitations
in
part
63,
subpart
EEE,
of
this
chapter
(
i.
e.,
by
conducting
a
comprehensive
performance
test
and
submitting
a
Notification
of
Compliance
under
§
§
63.1207(
j)
and
63.1210(
d)
of
this
chapter
documenting
compliance
with
all
applicable
requirements
of
part
63,
subpart
EEE,
of
this
chapter),
the
requirements
of
this
section
do
not
apply.
The
requirements
of
this
section
do
apply,
however,
if
the
Director
determines
certain
provisions
are
necessary
to
ensure
compliance
with
§
§
266.102(
e)(
1)
and
266.102(
e)(
2)(
iii)
of
this
chapter
if
you
elect
to
comply
with
§
270.235(
a)(
1)(
i)
to
minimize
emissions
of
toxic
compounds
from
startup,
shutdown,
and
malfunction
events;
or
if
you
are
an
area
source
and
elect
to
comply
with
the
§
§
266.105,
266.106,
and
266.107
standards
and
associated
requirements
for
particulate
matter,
hydrogen
chloride
and
chlorine
gas,
and
non­
mercury
metals;
or
the
Director
determines
certain
provisions
apply,
on
a
case­
by­
case
basis,
for
purposes
of
information
collection
in
accordance
with
§
§
270.10(
k),
270.10(
l),
270.32(
b)(
2),
and
270.32(
b)(
3).
*
OMB
Review
Draft*

388
*
*
*
*
*
8.
Section
270.235
is
amended
by:
a.
Revising
paragraphs
(
a)(
1)
and
(
a)(
2).
b.
Revising
paragraphs
(
b)(
1)
and
(
b)(
2).
The
revisions
read
as
follows:
*
*
*
*
*
§
270.235
Options
for
incinerators,
cement
kilns,
lightweight
aggregate
kilns,
solid
fuelfired
boilers,
liquid
fuel­
fired
boilers
and
hydrochloric
acid
production
furnaces
to
minimize
emissions
from
startup,
shutdown,
and
malfunction
events.
(
a)
*
*
*
(
1)
Revisions
to
permit
conditions
after
documenting
compliance
with
MACT.
The
owner
or
operator
of
a
RCRA­
permitted
incinerator,
cement
kiln,
lightweight
aggregate
kiln,
solid
fuel­
fired
boiler,
liquid
fuel­
fired
boiler,
or
hydrochloric
acid
production
furnace
may
request
that
the
Director
address
permit
conditions
that
minimize
emissions
from
startup,
shutdown,
and
malfunction
events
under
any
of
the
following
options
when
requesting
removal
of
permit
conditions
that
are
no
longer
applicable
according
to
§
§
264.340(
b)
and
266.100(
b)
of
this
chapter:
*
*
*
*
*
(
2)
Addressing
permit
conditions
upon
permit
reissuance.
The
owner
or
operator
of
an
incinerator,
cement
kiln,
lightweight
aggregate
kiln,
solid
fuel­
fired
boiler,
liquid
fuel­
fired
boiler,
or
hydrochloric
acid
production
furnace
that
has
conducted
a
comprehensive
performance
test
and
submitted
to
the
Administrator
a
Notification
of
Compliance
documenting
compliance
with
the
standards
of
part
63,
subpart
EEE,
of
this
chapter
may
request
in
the
application
to
reissue
the
permit
for
the
combustion
unit
that
the
Director
control
emissions
from
startup,
shutdown,
and
malfunction
events
under
any
of
the
following
options:
*
*
*
*
*
(
b)
*
*
*
(
1)
Interim
status
operations.
In
compliance
with
§
§
265.340
and
266.100(
b),
the
owner
or
operator
of
an
incinerator,
cement
kiln,
lightweight
aggregate
kiln,
solid
fuel­
fired
boiler,
liquid
fuel­
fired
boiler,
or
hydrochloric
acid
production
furnace
that
is
operating
under
the
interim
status
standards
of
part
265
or
266
of
this
chapter
may
control
emissions
of
toxic
compounds
during
startup,
shutdown,
and
malfunction
events
under
either
of
the
following
options
after
conducting
a
comprehensive
performance
test
and
submitting
to
the
Administrator
a
Notification
of
Compliance
documenting
compliance
with
the
standards
of
part
63,
subpart
EEE,
of
this
chapter.
*
*
*
*
*
(
2)
Operations
under
a
subsequent
RCRA
permit.
When
an
owner
or
operator
of
an
incinerator,
cement
kiln,
lightweight
aggregate
kiln,
solid
fuel­
fired
boiler,
liquid
fuel­
fired
boiler,
or
hydrochloric
acid
production
furnace
that
is
operating
under
the
interim
status
standards
of
parts
265
or
266
of
this
chapter
submits
a
RCRA
permit
application,
the
owner
or
operator
may
request
that
the
Director
control
emissions
from
startup,
shutdown,
and
malfunction
events
under
any
of
the
options
provided
by
paragraphs
(
a)(
2)(
i),
(
a)(
2)(
ii),
or
(
a)(
2)(
iii)
of
this
section.
*
*
*
*
*
*
OMB
Review
Draft*

389
PART
271­­
REQUIREMENTS
FOR
AUTHORIZATION
OF
STATE
HAZARDOUS
WASTE
PROGRAMS
1.
The
authority
citation
for
part
271
continues
to
read
as
follows:
Authority:
42
U.
S.
C.
6905,
6912(
a),
and
6926.
2.
Section
271.1(
j)
is
amended
by
adding
the
following
entries
to
Table
1
in
chronological
order
by
date
of
publication
in
the
Federal
Register,
to
read
as
follows:
§
271.1
Purpose
and
scope.
*
*
*
*
*
(
j)
*
*
*
TABLE
1.
­­
REGULATIONS
IMPLEMENTING
THE
HAZARDOUS
AND
SOLID
WASTE
AMENDMENTS
OF
1984
Promulgation
date
Title
of
Regulation
Federal
Register
reference
Effective
date
*
*
*
*
*
[
Insert
date
of
publication
of
final
rule
in
the
FEDERAL
REGISTER
(
FR)].
Standards
for
Hazardous
Air
Pollutants
for
Hazardous
Waste
Combustors
[
Insert
FR
page
numbers].
[
Insert
date
of
publication
of
final
rule].
