Date:
December
18,
2003
Subject:
Production­
Based
Compliance
Options
for
the
Final
Plywood
and
Composite
Wood
Products
NESHAP
EPA
Contract
No.
68­
D­
1­
079;
EPA
Work
Assignment
No.
2­
12
RTI
Project
No.
08550.002.012
From:
Katie
Hanks
To:
Mary
Tom
Kissell,
ESD/
WCPG
(
C439­
03)
U.
S.
Environmental
Protection
Agency
Research
Triangle
Park,
NC
27711
I.
Introduction
National
emission
standards
for
hazardous
air
pollutants
(
NESHAP)
were
proposed
for
the
plywood
and
composite
wood
products
(
PCWP)
industry
on
January
9,
2003.1
The
proposed
NESHAP
contained
a
production­
based
compliance
option
(
PBCO)
(
formerly
referred
to
as
production­
based
emission
limits).
The
PBCO
was
developed
for
process
units
that
use
pollution
prevention
or
are
otherwise
inherently
low­
emitting.
The
PBCO
consists
of
separate
emission
limits
for
specific
process
units
types.
The
PBCO
limits
are
in
terms
of
mass
per
unit
production
such
as
pounds
per
oven
dried
ton
(
lb/
ODT)
or
pounds
per
thousand
square
feet
(
lb/
MSF),
of
"
total
HAP."
"
Total
HAP"
is
defined
in
the
PCWP
NESHAP
as
the
total
emissions
of
the
following
six
HAP:
acetaldehyde,
acrolein,
formaldehyde,
methanol,
phenol,
and
propionaldehyde.
The
methodology
used
to
develop
the
proposed
PBCO
is
presented
in
a
separate
memorandum.
2
This
memorandum
discusses
the
changes
made
to
the
PBCO
limits
in
response
to
the
public
comments,
including
changes
in
how
non­
detect
measurements
are
treated
(
discussed
in
Section
II)
and
changes
to
the
PBCO
limits
due
to
revised
distinctions
among
process
units
(
discussed
in
Section
III).
The
final
PBCO
limits
are
presented
in
Section
IV.

II.
Treatment
of
Non­
Detect
Measurements
The
commenters
stated
that
most
of
the
PBCO
limit
could
be
consumed
by
using
one­
half
of
the
method
detection
limit
(
MDL)
for
non­
detect
measurements,
as
required
by
the
proposed
rule.
They
suggested
excluding
non­
detect
measurements
from
the
PBCO
limit
calculation
instead
of
using
one­
half
of
the
MDL.
In
response
to
these
comments,
an
analysis
was
conducted
to
determine
the
validity
of
the
commenters'
concerns
(
see
Attachment
A).
Based
on
the
analysis
2
included
in
Attachment
A,
we
agree
that
most
of
the
PBCO
limit
would
be
reached
by
using
onehalf
of
the
MDL
for
non­
detect
measurements.
Therefore,
we
changed
the
rule:
(
1)
to
exclude
non­
detect
measurements
from
the
PBCO
limit
calculations
when
all
test
runs
are
non­
detect,
and
(
2)
to
ensure
that
the
development
of
the
PBCO
limits
is
consistent
with
excluding
non­
detect
measurements
by
recalculating
the
limits
using
zero
for
non­
detect
measurements
when
all
test
runs
were
non­
detect.

III.
Changes
in
Process
Unit
Distinctions
1.
Primary
and
secondary
tube
dryers
In
the
proposed
PCWP
NESHAP,
single­
stage
and
multi­
stage
tube
dryers
were
treated
as
one
process
unit,
"
tube
dryers."
Commenters
requested
that
stages
in
multistage
tube
dryers
be
considered
separate
tube
dryers
so
that
different
compliance
options
can
be
used
for
various
dryer
stages.
Single­
stage
tube
dryers
include
only
a
primary
tube
dryer.
Multi­
stage
tube
drying
systems
incorporate
two
stages
in
series,
a
primary
tube
dryer
and
a
secondary
tube
dryer,
which
are
separated
by
an
emission
point
(
e.
g.,
a
cyclonic
collector).
Each
stage
of
a
multi­
stage
tube
dryer
functions
as
an
individual
dryer,
and
the
existing
source
MACT
floor
for
both
primary
tube
dryer
and
secondary
tube
dryers
is
the
same
(
e.
g.,
incineration­
based
control).
To
allow
for
more
flexibility
in
application
of
pollution
prevention
or
controls
to
the
different
stages
of
tube
dryers,
the
final
PCWP
rule
defines
the
stages
of
multi­
stage
tube
dryers
separately
in
definitions
of
"
primary
tube
dryer"
and
"
secondary
tube
dryer."
Primary
tube
dryers
include
single­
stage
tube
dryers
and
the
first
stage
of
multi­
stage
tube
dryers.
Secondary
tube
dryers
include
the
second
stage
of
multi­
stage
tube
dryers.
3
In
the
final
PCWP
rule,
both
primary
and
secondary
tube
dryers
are
required
to
apply
MACT
controls
and
each
will
have
a
separate
PBCO
limit.

2.
Conveyor
strand
dryers
One
definition
of
"
strand
dryers"
was
included
in
the
proposed
PCWP
rule
because,
at
proposal,
MACT
for
both
rotary
and
conveyor
strand
dryers
was
the
same
(
i.
e,
MACT
was
represented
by
incineration­
based
control
of
100
percent
of
the
exhaust
from
both
types
of
dryers).
One
commenter
recommended
that
conveyor
strand
dryers
be
exempt
from
control
requirements
in
the
final
rule
because
they
are
low­
emitting
dryers.
Conveyor
strand
dryers
have
three
zones,
each
with
its
own
heat
and
exhaust
flow.
Following
proposal,
the
MACT
floor
for
conveyor
strand
dryers
was
revised
to
require
control
of
exhaust
from
zone
1
for
existing
dryers
and
zones
1
and
2
for
new
dryers.
3
No
conveyor
strand
dryer
emissions
data
are
available
for
all
six
of
the
HAP
that
comprise
"
total
HAP."
Therefore,
a
PBCO
limit
cannot
be
developed
for
conveyor
strand
dryers.

IV.
PBCO
Limits
for
the
Final
PCWP
NESHAP
The
same
approach
used
to
establish
the
PBCO
limits
for
the
proposed
PCWP
NESHAP
was
used
to
establish
the
limits
for
the
final
NESHAP
(
except
that
non­
detect
measurements
were
3
treated
as
zero
for
the
final
analysis).
The
available
"
total
HAP"
test
data
were
grouped
according
to
the
process
unit
groups
with
controlled
MACT
floors.
The
highest
"
total
HAP"
test
value
was
identified
for
each
process
unit
group,
and
the
PBCO
limit
for
the
process
unit
group
was
established
by
multiplying
the
highest
test
value
by
0.1
to
reflect
a
90­
percent
reduction
from
the
highest
test.
Attachment
B
presents
the
data
set
used
to
establish
the
PBCO
limits
for
each
process
unit
group.
The
"
total
HAP"
summations
presented
in
Attachment
B
were
developed
using
zero
when
all
test
runs
were
below
the
MDL.
Table
1
summarizes
the
PBCO
limits
recommended
for
the
final
PCWP
NESHAP.
The
differences
in
the
proposed
and
final
PBCO
limits
are:
(
1)
a
secondary
tube
dryer
PBCO
limit
has
been
added,
and
(
2)
the
reconstituted
wood
product
board
cooler
PBCO
limit
decreased
from
0.015
to
0.014
lb/
MSF
3/
4"
due
to
use
of
zero
when
all
test
runs
were
below
the
MDL.

TABLE
1.
PBCO
LIMITS
FOR
FINAL
PCWP
NESHAP
Equipmenta
PBCO
limit
units
PBCO
limit
Primary
tube
dryers
lb/
ODT
0.26
Secondary
tube
dryers
lb/
ODT
0.010
Rotary
strand
dryers
lb/
ODT
0.18
Green
wood
particle
rotary
dryers
lb/
ODT
0.058
Softwood
veneer
dryer
heated
zones
lb/
MSF
3/
8"
0.022
Hardboard
ovens
lb/
MSF
1/
8"
0.022
Reconstituted
wood
product
presses
lb/
MSF
3/
4"
0.30
Pressurized
refiners
lb/
ODT
0.039
Press
predryers
(
new
only)
lb/
MSF
1/
2"
0.037
Reconstituted
wood
product
board
coolers
(
new
only)
lb/
MSF
3/
4"
0.014
Fiberboard
mat
dryer
heated
zones
(
new
only)
lb/
MSF
1/
2"
0.022
a
Applies
to
new
and
existing
equipment
unless
otherwise
noted.
b
There
is
no
PBCO
limit
for
conveyor
strand
dryers.
References:

1.
U.
S.
Environmental
Protection
Agency.
National
Emission
Standards
for
Hazardous
Air
Pollutants:
Plywood
and
Composite
Wood
Products;
Proposed
Rule.
68
FR1276.
Washington,
DC.
U.
S.
Government
Printing
Office.
January
9,
2003.

2.
Memorandum
from
K.
Hanks,
MRI,
to
M.
Kissell,
EPA/
ESD.
June
2,
2000.
Development
of
Production­
Based
Emission
Limits
for
Plywood
and
Composite
Wood
Products
Process
Units
3.
Memorandum
from
K.
Hanks,
B.
Nicholson,
and
K.
Parrish,
RTI,
to
M.
Kissell,
EPA/
ESD.
December
15,
2003.
Determination
of
MACT
floors
and
MACT
for
the
Final
Plywood
and
Composite
Wood
Products
Industry
NESHAP.
Attachment
A
Analysis
of
Portion
of
Proposed
PBCO
Limit
Consumed
if
One­
Half
of
the
Method
Detection
Limit
Is
Used
for
Non­
detect
Measurements
Portion
of
Proposed
PBCO
Limit
Consumed
if
One­
Half
of
the
Method
Detection
Limit
Is
Used
for
Non­
detect
Measurements
Tables
A1
and
A2
present
an
analysis
of
the
portion
of
the
proposed
PBCO
limit
consumed
if
one­
half
of
the
method
detection
limit
(
MDL)
is
used
for
non­
detect
measurements.
Table
A1
contains
typical
process
parameters
for
each
type
of
process
units
with
a
proposed
PBCO
limit.
The
upper
end
of
the
typical
MDL
range
for
the
test
methods
most
likely
to
be
used
to
demonstrate
compliance
with
the
PBCO
(
i.
e.,
the
NCASI
Impinger/
cannister
method
(
NCASI
Method
IM/
CAN/
WP­
99.01)
or
EPA
Method
320
(
Appendix
A
to
40
CFR
part
63)
is
1
part
per
million
(
ppm).
The
process
parameters
in
Table
A1
were
combined
with
one­
half
of
1
ppm
(
i.
e.,
0.5
ppm)
to
calculate
the
percentage
of
the
PBCO
limit
that
would
be
consumed
if
all
of
the
six
HAP
were
not
detected
and
one­
half
of
MDL
was
used
to
calculate
"
total
HAP."

Table
A2
presents
the
calculations
of
the
percent
of
the
PBCO
limit
consumed
by
nondetect
measurements.
For
five
process
units,
use
of
one­
half
the
MDL
for
all
six
HAP
consumed
all
of
the
PBCO
limit.
Because
formaldehyde,
methanol,
and
acetaldehyde
are
the
most
commonly
detected
HAP
from
PCWP
process
units,
these
pollutants
were
eliminated
from
the
analysis.
However,
using
one­
half
of
the
MDL
for
acrolein,
phenol,
and
propionaldehyde
still
resulted
in
consumption
of
the
entire
PBCO
limit
for
five
process
units.
Based
on
the
analysis
presented
in
Tables
A1
and
A2,
it
appears
to
be
reasonable
to
allow
facilities
to
assume
zero
for
non­
detect
measurements
when
determining
compliance
with
the
PBCO,
provided
that
the
MDL
is
not
set
at
an
unreasonably
high
level
such
that
pollutants
cannot
be
detected.
TABLE
A1.
TYPICAL
PROCESS
PARAMETERS
FOR
PROCESS
UNITS
WITH
PROPOSED
PBCO
Process
Unit
Proposed
PBCO
limit
PBCO
limit
units
Typical
annual
throughput*
Throughput
Units
Typical
hourly
throughput
Typical
flow
(
dscfm)

Presses
0.3
lb/
MSF
3/
4
100,000
MSF
3/
4
12.5
75,000
Strand
Dryers
0.18
lb/
ODT
65,000
ODT
8.1
32,478
Softwood
Veneer
Dryers
0.022
lb/
MSF
3/
8
71,000
MSF
3/
8
8.9
12,062
Tube
Dryers
0.26
lb/
ODT
87,000
ODT
10.9
79,173
Green
Rotary
Dryers
0.058
lb/
ODT
70,000
ODT
8.8
35,731
Fiberboard
Mat
Dryer
0.022
lb/
MSF
1/
2
165,000
MSF
1/
2
20.6
49,389
Hardboard
Ovens
0.022
lb/
MSF
1/
8
163,000
MSF
1/
8
20.4
4,742
Press
Pre­
dryers
0.037
lb/
MSF
1/
2
40,750
MSF
1/
2
5.1
21,812
Pressurized
Refiners
0.039
lb/
ODT
87,000
ODT
10.9
1,000
Board
Coolers
0.015
lb/
MSF
3/
4
100,000
MSF
3/
4
12.5
60,000
TABLE
A2.
PERCENTAGE
OF
PBCO
LIMIT
CONSUMED
BY
USING
ONE­
HALF
OF
THE
MDL
FOR
NON­
DETECT
TEST
RUNS
Process
unit
PBCO
units
HAP
emissionsa
(
lb
/
unit
throughput)
Percent
of
PBCO
limit
consumed
by
½
­
MDL
calculation
if
all
6
HAP
are
non­
detectb
Percent
of
PBCO
limit
consumed
by
½
­
MDL
calculation
if
only
acrolein,
propionaldehyde,
and
phenol
are
non­
detectb
Acrolein
Acetaldehyde
Formaldehyde
Methanol
Propionaldehyde
Phenol
Presses
lb/
MSF
3/
4
0.0262
0.0206
0.0140
0.0149
0.0271
0.0439
49%
32%

Strand
Dryers
lb/
ODT
0.0174
0.0137
0.0093
0.0100
0.0181
0.0293
54%
36%

Softwood
Veneer
Dryers
lb/
MSF
3/
8
0.0059
0.0047
0.0032
0.0034
0.0061
0.0099
151%
100%

Tube
Dryers
lb/
ODT
0.0317
0.0249
0.0170
0.0181
0.0329
0.0533
68%
45%

Green
Rotary
Dryers
lb/
ODT
0.0178
0.0140
0.0095
0.0102
0.0184
0.0299
172%
114%

Fiberboard
Mat
Dryer
lb/
MSF
1/
2
0.0104
0.0082
0.0056
0.0060
0.0108
0.0175
266%
176%

Hareboard
Ovens
lb/
MSF
1/
8
0.0010
0.0008
0.0005
0.0006
0.0011
0.0017
26%
17%

Press
Pre­
dryers
lb/
MSF
1/
2
0.0187
0.0147
0.0100
0.0107
0.0193
0.0313
283%
187%

Pressurized
Refiners
lb/
ODT
0.0004
0.0003
0.0002
0.0002
0.0004
0.0007
6%
4%

Board
Coolers
lb/
MSF
3/
4
0.0209
0.0164
0.0112
0.0120
0.0217
0.0351
782%
518%

a
The
emissions
of
each
HAP
(
X)
was
calculated
as
follows:

lbx/
throughput
=
(
ppmx)
/
(
106)
x
(
lb
X/
lbmol
X)
x
(
dscfm)
x
(
60
min/
hr)
/
(
385.3
ft3/
lbmol
ideal
gas
at
528oR)
/
hourly
throughput
b
The
percent
of
the
PBCO
consumed
is
the
sum
of
the
emissions
of
each
pollutant
divided
by
the
proposed
PBCO
limit.
Attachment
B
Summary
of
Total
HAP
Test
Averages
Used
to
Develop
PBCO
Limits
Summary
of
Total
HAP
Test
Averages
Used
to
Develop
PBCO
Limits
Uncontrolled
emissions
tests
including
all
six
of
the
HAP
that
comprise
"
total
HAP"
were
used
in
developing
the
PBCO.
In
summing
emissions
of
the
six
HAP,
zero
was
used
for
pollutants
with
non­
detects
for
all
emission
test
runs.
Emissions
tests
for
process
units
with
control
devices
that
alter
HAP
emissions
(
e.
g.,
RTO,
RCO,
WESP,
etc)
were
not
used
in
development
of
the
PBCO
limits.
The
PBCO
limits
were
developed
based
on
a
90­
percent
reduction
from
the
highest
uncontrolled
emission
test
result.
Table
B1
presents
the
"
total
HAP"
test
data
used
to
develop
the
PBCO
limits.
Table
B2
presents
the
"
total
HAP"
data
that
were
not
used
in
developing
the
PBCO
limits,
and
the
reason
that
data
were
not
used
(
generally
because
the
data
represented
controlled
emissions).
TABLE
B1.
TOTAL
HAP
EMISSION
TESTS
USED
TO
DEVELOP
THE
PBCO
Process
Unit
(
count)
MRI
code
Unit
code
Test
date
Product
Total
HAP
test
average
Units
Highest
test
average
(
H)
Emission
limit
(=
H
x
0.1)

Reconstituted
Wood
Product
Press
(
17)
234­
1PB2
HB
press
6/
25/
98
HB
2.1
lb/
MSF
3/
4"

072­
1PB1
HB
press
(
high
resin/
high
wax)
5/
14/
98
HB
1.7
lb/
MSF
3/
4"

072­
1PB1
HB
press
(
high
resin/
low
wax)
5/
13/
98
HB
3.0
lb/
MSF
3/
4"

072­
1PB1
HB
press
(
low
resin/
low
wax)
5/
12/
98
HB
2.1
lb/
MSF
3/
4"

053­
2PB1
HB
press
10/
29/
97
HB
1.1
lb/
MSF
3/
4"

404­
1PT2
Continuous
press
and
BC
1/
13/
98
MDF
0.59
lb/
MSF
3/
4"

100­
1PB4
Hot
press
8/
25/
97
MDF
1.2
lb/
MSF
3/
4"

142­
1PB2
Hot
press
3/
12/
98
MDF
0.76
lb/
MSF
3/
4"

118­
1PB2
OSB
hot
press
6/
9/
98
OSB
1.2
lb/
MSF
3/
4"

083­
1PB2
OSB
hot
press,
No.
1
5/
6/
98
OSB
0.36
lb/
MSF
3/
4"

083­
2PB2
OSB
hot
press,
No.
2
5/
5/
98
OSB
0.56
lb/
MSF
3/
4"

145­
1PB2
OSB
hot
press
1/
18/
98
OSB
1.1
lb/
MSF
3/
4"

410­
1PB2
OSB
hot
press
4/
3/
98
OSB
0.57
lb/
MSF
3/
4"

010­
1PB2
PB
hot
press
10/
23/
97
PB
1.3
lb/
MSF
3/
4"

039­
1PB1
PB
hot
press
6/
5/
98
PB
0.51
lb/
MSF
3/
4"

156­
1PB2
PB
hot
press
9/
19/
97
PB
0.47
lb/
MSF
3/
4"

183­
1PXX
PB
hot
press
4/
29/
97
PB
0.89
lb/
MSF
3/
4"
3.0
0.30
Hardboard
oven
(
1)
234­
1OT2
HB
tempering
oven
6/
26/
98
HB
0.22
lb/
MSF
1/
8"
0.22
0.022
Fiberboard
mat
dryer
(
heated
zones)
(
4)
053­
2DF3
HB
dryer
10/
30/
97
HB
0.22
lb/
MSF
1/
2"

062­
1DF1
FB
dryer
(
hushboard)
6/
24/
97
FB
0.03
lb/
MSF
1/
2"

062­
1DF1
FB
dryer
(
high
density
roofing)
6/
25/
97
FB
0.029
lb/
MSF
1/
2"

062­
1DF1
FB
dryer
(
structural
sheathing)
6/
27/
97
FB
0.057
lb/
MSF
1/
2"
0.22
0.022
Board
coolers
(
3)
142­
1CW1
No.
1
Press
Board
cooler
vent
3/
12/
98
MDF
0.027
lb/
MSF
3/
4"

156­
1CS1
PB
cooler
&
kicker
9/
18/
97
PB
0.059
lb/
MSF
3/
4"

183­
1CW4
PB
primary
cooler
4/
29/
97
PB
0.14
lb/
MSF
3/
4"
0.14
0.014
Pressurized
refiner
(
1)
072­
3RP1
HB
pressurized
digester/
refiner
5/
11/
98
HB
0.39
lb/
ODT
0.39
0.039
Press
predryer
(
1)
053­
PPH
HB
press
preheater
10/
30/
97
HB
0.37
lb/
MSF
1/
2"
0.37
0.037
TABLE
B1,
CONTINUED
Process
Unit
(
count)
MRI
code
Unit
code
Test
date
Product
Total
HAP
test
average
Units
Highest
test
average
(
H)
Emission
limit
(=
H
x
0.1)

Softwood
veneer
dryer
(
heated
zones)
(
11)
194­
1DV2
Dryer
No.
1
heated
zones
11/
12/
97
SPW
0.18
lb/
MSF
3/
8"

194­
XDV2
Dryer
No.
1
and
2
heated
zones
7/
15/
98
SPW
0.22
lb/
MSF
3/
8"

112­
XDV2
Dryer
No.
2
and
3
heated
zones
7/
29/
97
SPW
0.057
lb/
MSF
3/
8"

112­
XDV2
Dryer
No.
2
and
3
heated
zones
8/
1/
97
SPW
0.17
lb/
MSF
3/
8"

115­
XDV2
Dryer
1,
2,
3
heated
zones
7/
24/
97
SPW
0.17
lb/
MSF
3/
8"

155­
XDV2
Dryer
1,2,3
heated
zones
9/
17/
97
SPW
0.059
lb/
MSF
3/
8"

165­
XDV2
Dryer
1,2,3,4
heated
zones
11/
17/
97
SPW
0.058
lb/
MSF
3/
8"

170­
XDV2
Dryer
No.
1,2,3
heated
zones
12/
9/
97
SPW
0.066
lb/
MSF
3/
8"

188­
XDV2
Dryer
No.
1,2,3,4
heated
zones
5/
19/
98
SPW
0.030
lb/
MSF
3/
8"

188­
XDV2
Dryer
No.
1,2,3,4
heated
zones
5/
20/
98
SPW
0.12
lb/
MSF
3/
8"

194­
2DV2
Dryer
No.
2
heated
zones
11/
12/
97
SPW
0.067
lb/
MSF
3/
8"
0.22
0.022
Rotary
strand
dryers
(
4)
145­
3DR4
OSB
rotary
dryer
No.
3
1/
17/
98
OSB
0.4
lb/
ODT
145­
4DR4
OSB
rotary
dryer
No.
4
1/
17/
98
OSB
0.51
lb/
ODT
410­
XDR3
OSB
rotary
dryers
(
5)
4/
1/
98
OSB
0.65
lb/
ODT
083­
XDR2
OSB
rotary
dryers
(
2)
5/
7/
98
OSB
1.8
lb/
ODT
1.8
0.18
Green
furnish
rotary
dryers
(
5)
039­
1DR3
PB
final
rotary
dryer
6/
4/
98
PB
0.39
lb/
ODT
156­
2DR2
PB
rotary
dryer
(
2)
9/
22/
97
PB
0.22
lb/
ODT
039­
6DR3
PB
rotary
predryer
6/
3/
98
PB
0.027
lb/
ODT
183­
3DR2
PB
rotary
dryer
(
face)
5/
1/
97
PB
0.58
lb/
ODT
156­
1DR2
PB
rotary
dryer
(
2)
9/
22/
1997
PB
0.24
lb/
ODT
0.58
0.058
Primary
tube
dryers
(
8)
100­
2DT2
Core
tube
dryer
(
inlet
prior
to
quench)
8/
23/
97
MDF
0.87
lb/
ODT
142­
2DT2
No.
2
Tube
dryer
(
Scrubber
inlet)
3/
9/
98
MDF
1.2
lb/
ODT
100­
1DT2
Face
tube
dryer
(
Wet
Scrubber
Inlet,
before
quench)
8/
24/
97
MDF
1.9
lb/
ODT
132­
2DT2
Face
primary
tube
dryer
(
Sum
of
2
cyclone
outlets)
2/
4/
98
MDF
1.9
lb/
ODT
132­
4DT2
Core
primary
tube
dryer
(
Sum
of
2
cyclone
outlets)
2/
5/
98
MDF
2.4
lb/
ODT
404­
1DT2
Tube
dryer
(
Product
cyclone
outlet)
1/
13/
98
MDF
2.5
lb/
ODT
109
D­
T1
1/
17/
95
HB
2.6
lb/
ODT
234­
XDT4
HB
1st
stage
tube
dryers
6/
22/
98
HB
1.5
lb/
ODT
2.6
0.26
TABLE
B1,
CONTINUED
Process
Unit
(
count)
MRI
code
Unit
code
Test
date
Product
Total
HAP
test
average
Units
Highest
test
average
(
H)
Emission
limit
(=
H
x
0.1)

Secondary
tube
dryers
(
4)
132­
XDT1
Face
secondary
tube
dryer
(
Baghouse
Outlet)
2/
4/
98
MDF
0.027
lb/
ODT
132­
YDT1
Core
secondary
tube
dryer
(
Baghouse
Outlet)
2/
5/
98
MDF
0.051
lb/
ODT
234­
3DT2
HB
2nd
stage
tube
dryer
#
3
6/
24/
98
HB
0.091
lb/
ODT
234­
4DT2
HB
2nd
stage
tube
dryer
#
4
6/
24/
98
HB
0.098
lb/
ODT
0.098
0.010
TABLE
B2.
TOTAL
HAP
EMISSION
TESTS
NOT
USED
FOR
PBCO
LIMIT
DEVELOPMENT
Process
Unit
MRI
code
Unit
code
Test
date
Product
MACT
Control
Total
HAP
test
average
Units
Reason
not
used
for
PBCO
development
Reconstituted
wood
product
press
234­
1PB1
HB
press
6/
25/
98
HB
0.96
lb/
MSF
3/
4"
After
wet
controls
118­
1PB1
OSB
hot
press
6/
9/
98
OSB
BIO
0.23
lb/
MSF
3/
4"
After
MACT
control
device
083­
1PB1
OSB
hot
press,
No.
1
5/
6/
98
OSB
RCO
0.14
lb/
MSF
3/
4"
After
MACT
control
device
083­
2PB1
OSB
hot
press,
No.
2
5/
5/
98
OSB
RTO
0.059
lb/
MSF
3/
4"
After
MACT
control
device
145­
1PB1
OSB
hot
press
1/
18/
98
OSB
RTO
0.027
lb/
MSF
3/
4"
After
MACT
control
device
410­
1PB1
OSB
hot
press
4/
3/
98
OSB
RTO
0
lb/
MSF
3/
4"
After
MACT
control
device
039­
1PB2
PB
hot
press
6/
5/
98
PB
0.64
lb/
MSF
3/
4"
After
WESP
010­
1PB1
PB
hot
press
10/
23/
97
PB
RTO
0.0082
lb/
MSF
3/
4"
After
MACT
control
device
Hardboard
oven
234­
1OT1
HB
tempering
oven
6/
26/
98
HB
RTO
0.0029
lb/
MSF
1/
8"
After
MACT
control
device
Softwood
veneer
dryer
(
heated
zones)
194­
XDV1
Dryer
No.
1
and
2
heated
zones
7/
15/
98
SPW
RCO
0.11
lb/
MSF
3/
8"
After
MACT
control
device
112­
2DV6
Dryer
No.
2
heated
zones
7/
29/
97
SPW
0.054
lb/
MSF
3/
8"
Only
1
section
of
dryer
112­
2DV6
Dryer
No.
2
heated
zones
8/
1/
97
SPW
0.062
lb/
MSF
3/
8"
Only
1
section
of
dryer
112­
XDV1
Dryer
No.
2
and
3
heated
zones
7/
29/
97
SPW
0.028
lb/
MSF
3/
8"
After
WESP
112­
XDV1
Dryer
No.
2
and
3
heated
zones
8/
1/
97
SPW
0.04
lb/
MSF
3/
8"
After
WESP
115­
XDV1
Dryer
1,
2,
3
heated
zones
7/
24/
97
SPW
0.14
lb/
MSF
3/
8"
After
ESP
155­
XDV1
Dryer
1,2,3
heated
zones
9/
17/
97
SPW
0.056
lb/
MSF
3/
8"
After
EFB
170­
2DV3
Dryer
No.
2
heated
zones
12/
9/
97
SPW
0.046
lb/
MSF
3/
8"
Only
1
of
3
dryers
170­
3DV3
Dryer
No.
3
heated
zones
12/
9/
97
SPW
0.083
lb/
MSF
3/
8"
Only
1
of
3
dryers
188­
XDV1
Dryer
No.
1,2,3,4
heated
zones
5/
19/
98
SPW
0.043
lb/
MSF
3/
8"
After
WESP
188­
XDV1
Dryer
No.
1,2,3,4
heated
zones
5/
20/
98
SPW
0.12
lb/
MSF
3/
8"
After
WESP
165­
XDV1
Dryer
1,2,3,4
heated
zones
11/
17/
97
SPW
RTO
0.0084
lb/
MSF
3/
8"
After
MACT
control
device
170­
XDV1
Dryer
No.
1,2,3
heated
zones
12/
9/
97
SPW
RTO
0.014
lb/
MSF
3/
8"
After
MACT
control
device
Rotary
strand
dryers
145­
3DR3
OSB
rotary
dryer
No.
3
1/
17/
98
OSB
0.41
lb/
ODT
After
WESP
145­
4DR3
OSB
rotary
dryer
No.
4
1/
17/
98
OSB
0.58
lb/
ODT
After
WESP
145­
XDR3
OSB
rotary
dryers
(
5)
1/
15/
98
OSB
0.63
lb/
ODT
After
WESP
145­
XDR2
OSB
rotary
dryers
(
5)
1/
15/
98
OSB
RTO
0.031
lb/
ODT
After
MACT
control
device
410­
XDR2
OSB
rotary
dryers
(
5)
4/
1/
98
OSB
RTO
0.071
lb/
ODT
After
MACT
control
device
083­
XDR1
OSB
rotary
dryers
(
2)
5/
7/
98
OSB
RTO
0.44
lb/
ODT
After
MACT
control
device
TABLE
B2,
CONTINUED
Process
Unit
MRI
code
Unit
code
Test
date
Product
MACT
Control
Total
HAP
test
average
Units
Reason
not
used
for
PBCO
development
Green
furnish
rotary
dryers
039­
1DR2
PB
final
rotary
dryer
6/
4/
98
PB
0.46
lb/
ODT
After
WESP
039­
XDR1
PB
final
rotary
dryers
(
5)
6/
4/
98
PB
0.39
lb/
ODT
After
WESP
156­
XDR1
PB
rotary
dryer
(
2)
9/
22/
97
PB
0.14
lb/
ODT
After
wet
scrubber
039­
6DR2
PB
rotary
predryer
6/
3/
98
PB
0.037
lb/
ODT
After
WESP
039­
6DR1
PB
rotary
predryer
6/
3/
98
PB
RTO
0.0025
lb/
ODT
After
MACT
control
device
Primary
tube
dryers
100­
2DT1
Core
tube
dryer
(
scrubber
outlet)
8/
23/
97
MDF
0.78
lb/
ODT
After
wet
scrubber
142­
2DT1
No.
2
Tube
dryer
(
Scrubber
outlet)
3/
9/
98
MDF
0.75
lb/
ODT
After
scrubber
100­
1DT1
Face
tube
dryer
(
Wet
Scrubber
Outlet)
8/
24/
97
MDF
1
lb/
ODT
After
wet
scrubbed
234­
XDT3
HB
1st
stage
tube
dryers
6/
22/
98
HB
1.4
lb/
ODT
After
Ducon
scrubber
