Document ID: EPA-HQ-OAR-2003-0048-0143
Agency: epa
Document Type: Supporting & Related Material
Title: 
Posted Date: 2004-02-26T05:00Z

Date:
November
26,
2003
Subject:
Selection
of
HAPs
for
Compliance
Options
in
the
Final
Plywood
and
Composite
Wood
Products
Rule
EPA
Contract
No.
68­
D­
1­
079;
EPA
Work
Assignment
No.
2­
12
RTI
Project
No.
08550.002.012
From:
Katie
Hanks
Kristin
Parrish
To:
Mary
Tom
Kissell,
ESD/
WCPG
(
C439­
03)
U.
S.
Environmental
Protection
Agency
Research
Triangle
Park,
NC
27711
I.
Introduction
Several
hazardous
air
pollutants
(
HAP)
may
be
emitted
from
plywood
and
composite
wood
products
(
PCWP)
process
units.
The
proposed
national
emission
standards
for
hazardous
air
pollutants
(
NESHAP)
for
the
PCWP
industry
contained
production­
based
compliance
options
(
PBCO)
and
emissions
averaging
compliance
options
based
on
measurement
of
six
predominant
HAP
(
acetaldehyde,
acrolein,
formaldehyde,
methanol,
phenol,
and
formaldehyde).
The
proposed
NESHAP
also
contained
add­
on
control
device
compliance
options
based
on
measurement
of
two
HAP
(
formaldehyde
or
methanol)
or
total
hydrocarbon
(
THC).
The
purpose
of
this
memo
is
to
document
identification
of
the
predominant
HAP
used
as
the
basis
for
the
PBCO
and
emissions
averaging
compliance
options
(
Section
II)
and
to
discuss
selection
of
HAP
for
the
add­
on
control
device
compliance
options
(
Section
III).

II.
Identification
of
Predominant
HAP
Sources
of
emissions
test
data
used
in
developing
the
NESHAP
for
the
PCWP
industry
included
nearly
100
emission
test
reports
collected
through
EPA's
MACT
survey,
data
from
EPA's
Compilation
of
Air
Pollutant
Emission
Factors,
Volume
I:
Stationary
Point
and
Area
Sources
(
commonly
referred
to
as
AP­
42),
and
extensive
data
from
the
industry­
sponsored
test
program
performed
by
the
National
Council
of
the
Paper
Industry
for
Air
and
Stream
Improvement
(
NCASI).
Most
of
the
speciated
HAP
emissions
test
data
used
to
develop
the
PCWP
NESHAP
came
from
the
NCASI
test
program.
Attachment
1
explains
more
about
which
HAP
were
tested
in
the
NCASI
test
program
and
an
in
an
earlier
EPA
test
program.
2
Table
1
lists
nationwide
baseline
emission
estimates
for
all
of
the
HAP
detected
at
least
once
in
the
compilation
of
HAP
emissions
data
used
in
development
of
the
PCWP
NESHAP.
The
nationwide
baseline
emission
estimates
presented
in
Table
1
are
sorted
in
descending
order
by
mass.
These
estimates
were
developed
using
the
methodology
described
in
a
separate
memorandum.
1
The
PCWP
product
sectors
and
the
number
of
process
units
that
had
detectable
emissions
of
each
HAP
are
also
included
in
Table
1.

Thriteen
HAP
had
nationwide
baseline
emissions
estimates
greater
than
10
tons
per
year
(
tpy),
and
7
HAP
had
nationwide
baseline
emissions
estimates
greater
than
100
tpy.
The
percentage
of
uncontrolled
process
unit
emission
test
runs
in
the
emission
factor
data
base
that
were
below
detection
limit
is
presented
in
Table
2
for
each
of
these
13
HAP.
2
More
then
90
percent
of
the
emission
test
runs
were
non­
detect
for
four
of
the
13
HAP.
The
high
percentage
of
non­
detect
test
runs
indicates
that
emissions
of
these
HAP
occur
infrequently.

The
goal
of
this
analysis
is
to
determine
if
a
subset
of
HAP
could
be
used
to
demonstrate
compliance
with
the
PCWP
rule.
For
a
compliance
demonstration
based
on
a
subset
of
HAP
to
be
feasible,
it
must
ensure
that
MACT
is
achieved
and
reduce
the
cost
of
compliance.
The
subset
of
HAP
used
for
compliance
demonstration
could
be
based
on
the
predominant
HAP
emitted
by
the
PCWP
industry.
The
predominant
HAP
would
be
those
emitted
in
detectable
quantities
and
with
high
mass
relative
to
other
PCWP
HAP.
The
predominant
HAP
would
also
be
emitted
from
many
PCWP
process
units.
Thus,
the
following
criteria
were
used
to
identify
the
predominant
HAP
from
the
PCWP
industry:
(
1)
HAP
with
nationwide
baseline
emissions
greater
than
100
tpy,
(
2)
HAP
emitted
in
the
greatest
mass
by
most
PCWP
sectors
and
process
units,
and
(
3)
HAP
with
less
than
90
percent
of
their
uncontrolled
emissions
test
runs
being
non­
detect.
Based
on
the
information
in
Tables
1
and
2,
the
HAP
that
meet
these
criteria
are
methanol,
formaldehyde,
acetaldehyde,
phenol,
acrolein,
and
propionaldehyde.
Together
these
six
HAP
represent
96
percent
of
the
mass
of
total
HAP
emissions
estimated
for
the
PCWP
industry.
These
six
HAP
are
found
in
emissions
from
nearly
all
PCWP
sectors
(
except
for
hardwood
plywood,
which
is
a
sector
that
contains
no
major
sources)
and
many
process
units.
A
single
test
method
can
be
used
to
test
for
all
six
HAP
simultaneously.
These
six
HAP
were
defined
as
"
total
HAP"
in
the
proposed
PCWP
rule.

The
compliance
demonstration
for
the
PBCO
and
emissions
averaging
compliance
options
are
based
on
the
sum
of
the
six
predominant
HAP.
The
emissions
averaging
provisions
involve
use
of
add­
on
air
pollution
control
devices
(
APCD).
As
discussed
in
section
III
below,
data
indicate
that
when
emissions
of
the
six
predominant
HAP
(
particularly
formaldehyde
and
methanol
because
they
are
most
often
emitted
in
detectable
amounts)
are
controlled
using
a
MACT
control
device,
the
other
organic
HAP
emitted
by
the
PCWP
industry
are
also
reduced
significantly.
Review
of
the
emission
factors
used
to
develop
the
emissions
estimates
for
the
PCWP
source
category
indicates
that
uncontrolled
emissions
of
HAP
(
other
than
the
six
HAP)
are
always
lower
than
emissions
of
the
six
HAP
for
every
process
unit
with
MACT
control
requirements.
Thus,
process
units
meeting
the
PBCO
based
on
total
HAP
also
would
have
low
emissions
of
other
HAP.
3
III.
Relationship
Between
HAP
Selected
for
Add­
on
APCD
Compliance
Options
The
PCWP
rule
contains
compliance
options
for
APCD
in
terms
of
percent
reduction
and
APCD
outlet
concentration
for
formaldehyde,
methanol,
and
THC.
The
rationale
for
selecting
these
HAP
for
the
add­
on
APCD
compliance
options
is
explained
in
a
separate
memorandum
and
is
further
explained
below.
5
Prior
to
proposal
of
the
PCWP
rule,
it
was
noted
that
the
complete
set
of
control
efficiency
data
showed
that
many
HAP
were
emitted
at
levels
near
or
below
the
detection
limit
at
the
inlet
of
the
control
device,
which
rendered
them
useless
for
determining
control
device
performance.
Attachment
3a
presents
the
available
data
used
in
control
efficiency
calculations
for
speciated
HAP
emissions
for
14
regenerative
thermal
oxidizers
(
RTO),
two
regenerative
catalytic
oxidizers
(
RCO),
and
two
biofilters.
The
shaded
control
efficiencies
in
Attachment
3a
indicate
pollutants
that
were
removed
from
the
control
efficiency
analysis.
The
control
efficiencies
for
these
pollutants
were
not
meaningful
because
either
all
of
the
inlet
and
outlet
test
runs
were
below
detection
limit,
or
at
least
two
of
the
inlet
test
runs
were
non­
detects.
Table
3
summarizes
the
number
of
data
sets
from
which
control
efficiency
calculations
for
each
HAP
were
removed
because
of
non­
detect
measurements.
As
shown
in
Table
3,
formaldehyde,
methanol,
and
THC
were
the
only
pollutants
with
control
efficiency
calculations
that
were
unaffected
by
non­
detect
measurements
in
the
APCD
inlet.
Acetaldehyde,
phenol,
and
propionaldehyde
were
affected
by
inlet
non­
detects,
but
were
detected
more
frequently
at
the
APCD
inlet
than
the
other
pollutants.
Nevertheless,
enough
of
the
acetaldehyde,
acrolein,
and
propionaldehyde
control
efficiency
calculations
were
affected
by
inlet
non­
detects
that
it
seemed
unreasonable
to
use
these
HAP
as
the
basis
for
a
control
efficiency
limit
given
that
a
control
device
that
reduces
formaldehyde,
methanol,
or
THC
would
also
reduce
these
HAP
(
when
detectable).

Attachment
3b
presents
the
available
control
efficiency
data
after
removal
of
the
shaded
pollutant
control
efficiencies.
The
APCD
performance
evaluation
focused
on
THC,
methanol,
and
formaldehyde.
These
three
pollutants
were
selected
because
they
were:
(
1)
consistently
measured
in
detectable
quantities
at
the
inlet
of
the
control
devices,
(
2)
the
most
prevalent
pollutants
emitted
across
the
various
types
of
process
units,
and
(
3)
the
most
frequently
tested
pollutants
(
thus,
more
data
were
available
for
these
three
pollutants).
Although
THC
is
not
a
HAP,
THC
can
be
a
good
indicator
of
the
performance
of
the
control
device,
and
it
is
frequently
used
as
a
surrogate
for
volatile
organic
compounds
(
VOC).
When
possible,
methane
was
subtracted
from
the
THC
emission
measurements
to
more
closely
represent
VOC.
The
data
presented
in
Attachment
3b
show
that
when
the
THC,
methanol,
and/
or
formaldehyde
control
efficiency
is
high
(
e.
g.,
90
percent),
the
control
efficiency
for
other
HAP
is
also
significant.
The
other
HAP
are
not
always
reduced
by
90
percent
because
they
are
present
in
the
APCD
inlet
at
a
lower
concentration
(
e.
g.,
usually
less
than
1
ppm
and
almost
always
less
than
10
ppm).
Compounds
present
in
relatively
low
quantities
in
the
uncontrolled
emission
stream
generally
(
but
not
always)
are
associated
with
lower
control
efficiencies.
Additional
information
and
discussion
of
control
device
efficiency
is
presented
in
a
separate
memorandum.
3
4
Based
on
the
available
data,
it
appears
that
a
reduction
in
one
predominant
HAP
or
THC
correlates
with
a
reduction
in
other
HAP
if
the
other
HAP
is
present
in
detectable
quantities
and
at
sufficient
concentration.
Thus,
the
data
indicate
that
the
mechanisms
in
RTO,
RCO,
and
biofilter
control
devices
that
reduce
emissions
of
formaldehyde
and
methanol
are
also
likely
to
reduce
emissions
of
the
remaining
HAP.
Although
biofilters
do
not
reduce
THC
to
the
same
degree
as
RTO
and
RCO
(
because
less
water­
soluble
non­
HAP
components
of
THC,
such
as
pinenes,
are
not
as
easily
destroyed
in
biofilters),
they
achieve
high
reductions
in
formaldehyde
and
methanol.
It
follows
that
any
biofilter
that
achieves
a
high
reduction
in
THC
would
also
achieve
a
high
reduction
in
formaldehyde,
methanol,
or
other
HAP.

In
addition,
an
analysis
of
the
physical
properties
of
the
organic
HAP
emitted
from
PCWP
processes
indicates
that
nearly
all
of
the
HAP
would
be
combusted
at
normal
thermal
oxidizer
operating
temperatures.
Attachment
4
summarizes
the
ignition
temperatures
for
the
various
HAP.
All
of
the
HAP
(
except
carbon
tetrachloride
and
chloroform
which
have
only
been
shown
to
be
emitted
in
minute
amounts
from
one
type
of
process
unit)
are
flammable
with
ignition
temperatures
ranging
from
194oF
to
1319oF.
The
lowest
thermal
oxidizer
combustion
chamber
temperature
reported
in
response
to
the
MACT
survey
is
1425oF.
4
Thus,
based
on
physical
properties
alone,
it
is
expected
that
a
thermal
oxidizer
that
significantly
reduces
methanol
and/
or
formaldehyde
would
also
reduce
the
other
HAP
emitted
from
the
PCWP
industry.

The
available
emissions
data
do
not
reveal
any
process
variables
that
could
be
manipulated
(
without
altering
the
product)
to
achieve
a
quantifiable
reduction
in
emissions.
Furthermore,
nothing
in
the
data
suggests
that
process
variables
could
be
manipulated
in
a
way
that
would
alter
the
relationship
between
formaldehyde
and
methanol
reduction
and
reduction
of
other
HAP.
For
example,
switching
from
urea­
formaldehyde
resin
to
phenol­
formaldehyde
resin
may
change
emissions;
however,
these
resins
are
not
interchangeable
because
the
product
would
also
change.
Urea­
formaldehyde
resins
are
pale
and
are
used
for
interior,
decorative
products
where
the
resin
must
not
show
through
the
products
finish
(
e.
g.,
cabinets,
furniture);
phenol­
formaldehyde
resins
are
dark
brown
and
water­
proof
and
are
used
in
exterior
applications
(
e.
g.
sheathing,
roofing).
Emissions
data
were
revisited
with
respect
to
other
process
variables
that
could
potentially
be
manipulated
without
altering
the
product
including
dryer
firing
method,
fuel
type,
and
in
some
cases
wood
type.
However,
the
variability
in
the
available
emissions
data
is
such
that
there
is
no
apparent
correlation
between
these
process
variables
and
emissions
of
formaldehyde
and
methanol.
5
Less
data
in
the
detectable
range
is
available
for
HAP
other
than
formaldehyde
and
methanol;
therefore,
if
process
variables
cannot
be
shown
to
affect
emissions
of
formaldehyde
and
methanol,
then
it
is
reasonable
to
conclude
no
such
affects
would
be
shown
for
other
less
common
HAP.

IV.
References:

1.
Memorandum
from
K.
Hanks
and
D.
Bullock,
MRI,
to
M.
Kissell,
EPA/
ESD.
June
9,
2000.
Baseline
Emission
Estimates
for
the
Plywood
and
Composite
Wood
Products
Industry.
5
2.
Memorandum
from
D.
Bullock,
K.
Hanks,
and
B.
Nicholson,
MRI
to
M.
Kissell,
EPA/
ESD.
April
28,
1999.
Summary
of
Responses
to
the
1998
EPA
Information
Collection
Request
(
MACT
Survey)
­­
General
Survey.

3.
Memorandum
from
R.
Nicholson,
MRI,
to
M.
Kissell,
EPA/
ESD.
May
26,
2000.
Control
Device
Efficiency
Data
for
Add­
on
Control
Devices
at
PCWP
Plants.

4.
Memorandum
from
D.
Bullock
and
K.
Hanks,
MRI,
to
M.
Kissell,
WCPG/
ESD/
EPA.
Documentation
of
Emission
Factor
Development
for
the
Plywood
and
Composite
Wood
Products
Manufacturing
NESHAP.
April
27,
2000.

5.
Memorandum
from
K.
Parrish
and
K.
Hanks,
RTI
to
M.
Kissell,
EPA/
ESD.
Review
of
Correlations
Between
Process
Variables
and
Emissions
for
the
Plywood
and
Composite
Wood
Products
Industry.
November
26,
2003.
6
Table
1.
Summary
of
Nationwide
Baseline
HAP
Emissions,
Product
Sectors,
and
Process
Units
For
Which
Each
HAP
Detected
HAP
Nationwide
baseline
emissions
(
tpy)
PCWP
sectors
with
HAP
detecteda
No.
of
PCWP
process
units
Methanol
12,000
all
32
Formaldehyde
3,400
all
29
Acetaldehyde
1,500
all
27
Phenol
690
all
20
Acrolein
330
all
but
HPW
17
Propionaldehyde
270
all
but
HPW
13
MIBK
170
all
but
EWP
15
Xylenes
(
includes
m,
pxylene
and
o­
xylene)
80
PB,
HB,
OSB,
SPW
9
Toluene
67
all
but
HPW
13
MEK
63
all
but
HPW
16
Benzene
44
all
but
HPW
13
Cumene
27
PB,
FB,
OSB
7
Styrene
10
all
but
HPW
and
FB
10
MDI
8.8
OSB,
EWP
2
Methylene
chloride
4.8
PB
3
Other
HAPb
1.6
PB
1b
Cresols
(
includes
m,
pcresol
and
o­
cresol)
1.0
HB
1
Chloromethane
0.23
PB,
HB
2
Ethyl
benzene
0.15
PB,
HB
3
Chloroethane
0.025
HB
1
Total
19,000
8
sectors
37
listed
in
Attachment
2c
a
The
eight
PCWP
product
sectors
include
medium
density
fiberboard
(
MDF),
particleboard
(
PB),
hardboard
(
HB),
fiberboard
(
FB),
oriented
strandboard
(
OSB),
softwood
plywood
(
SPW),
hardwood
plywood
(
HPW),
and
engineered
wood
products
(
EWP).
b
"
Other
HAP"
includes
1,1,1­
Trichloroethane,
4­
Methyl­
2­
pentanone,
Acetophenone,
Biphenyl,
Bis­(
2­
ethylhexyl
phthalate),
Bromomethane,
Carbon
disulfide,
Carbon
tetrachloride,
Chloroform,
Chloromethane,
Di­
n­
butyl
phthalate,
Ethyl
benzene,
Hydroquinone,
and
n­
Hexane.
With
the
exception
of
chloroform,
all
of
the
"
other
HAP"
were
detected
in
two
tests
of
two
dry
rotary
dryers
(
EPA
M0010
and
M0030
tests).
Cholroform
was
detected
in
one
green
rotary
dryer
test
(
M0030).
In
addition,
1,1,1­
Trichloroethane
was
detected
in
a
M0030
test
of
a
particleboard
veneer
press.
7
c
Attachment
2
lists
the
types
of
process
units
for
which
emissions
were
estimated
according
to
the
methodology
in
the
baseline
emissions
memo
and
provides
a
breakout
of
HAP
detected
for
each
process
unit
type.
8
Table
2.
Percentage
of
Uncontrolled
Process
Unit
Emission
Test
Runs
Below
Detection
Limit
for
13
HAP
with
Nationwide
Baseline
Emissions
of
10
Tons
per
Year
or
Greater
HAP
Nationwide
baseline
emissions
(
tpy)
Percent
of
uncontrolled
process
unit
test
runs
in
emission
factor
data
base
that
were
below
detection
limita
Methanol
12,000
14%

Formaldehyde
3,400
16%

Acetaldehyde
1,500
46%

Phenol
690
73%

Acrolein
330
77%

Propionaldehyde
270
85%

MIBK
170
93%

Xylenes
(
includes
m,
pxylene
and
o­
xylene)
80
91%

Toluene
67
85%

MEK
63
88%

Benzene
44
87%

Cumene
27
96%

Styrene
10
96%

aReference
2
9
Table
3.
Number
of
Instances
When
a
Pollutant
Was
Removed
from
the
Speciated
HAP
Control
Efficiency
Data
Set
Due
to
Inlet
Non­
detect
Measurementsa
HAP
RTO
(
14
data
sets)
RCO
(
2
data
sets)
Biofilter
(
2
data
sets)
acetaldehyde
2
0
1
acrolein
9
1
2
benzene
11
1
2
cumeneb
12b
1b
2b
formaldehyde
0
0
0
m,
p­
xylene
11
1
2
methanol
0
0
0
methyl
ethyl
ketone
12
1
2
methyl
isobutyl
ketone
11
2
2
methylene
chlorideb
4b
NAb
1b
o­
xyleneb
8b
1b
1b
phenol
10
0
1
propionaldehyde
9
1
2
styrene
13
1
2
THC
as
carbon
0
0
0
toluene
10
1
2
aHAP
were
removed
from
the
control
efficiency
analysis
if:
(
1)
all
APCD
inlet
and
outlet
test
runs
were
below
detection
limit,
or
(
2)
at
least
two
of
the
APCD
inlet
test
runs
were
below
detection
limit.
bData
not
available
in
all
data
sets
for
this
HAP.
However,
every
data
set
containing
this
HAP
was
removed
from
the
control
efficiency
analysis
because
of
non­
detects
in
the
inlet.
ATTACHMENT
1
NCASI
Testing
Program
The
HAP
included
in
the
NCASI
test
program
are
listed
in
Table
1.
Five
of
these
HAP
were
not
detected
at
any
of
the
emission
sources
tested.
1
Prior
to
the
NCASI
testing
program,
efforts
were
made
to
characterize
the
HAP
emitted
from
PCWP
processes.
A
comprehensive
sampling
effort
was
conducted
by
EPA
in
1992/
1993
where
HAP
data
were
obtained
from
testing
at
four
mills
using
three
measurement
methods:
(
1)
Method
0011
for
aldehydes
and
ketones,
(
2)
Method
0010
for
semi­
volatile
organic
compounds,
and
(
3)
Method
0030
for
volatile
organic
compounds.
Theoretically,
these
three
methods
combined
could
be
expected
to
detect
nearly
all
of
the
organic
HAP
present
in
source
emissions
(
if
present
at
concentrations
greater
than
the
method
detection
limits).
The
results
from
this
sampling
effort
were
incorporated
into
EPA's
AP­
42
data,
which
were
used
in
development
of
the
PCWP
NESHAP.
The
results
from
EPA's
HAP
speciation
effort
and
others
were
considered
when
planning
the
NCASI
sampling
program
in
1996/
1997.
Time
constraints
made
it
impractical
for
NCASI
to
sample
for
all
188
HAP.
Also,
because
the
budget
for
the
sampling
effort
was
set
at
$
1.5
to
2
million,
increasing
the
number
of
HAP
sampled
would
increase
testing
costs
and
decrease
the
number
of
processes
and
mills
that
could
be
sampled.
Therefore,
the
NCASI
sampling
effort
focused
on
those
HAP
expected
to
account
for
the
overwhelming
majority
of
the
HAP
emitted
by
PCWP
plants.
2,3
Table
1.
HAP
Analytes
Included
in
the
NCASI
MACT
Sampling
Program
acetaldehyde
methyl
ethyl
ketone
acrolein
methyl
isobutyl
ketone
benzene
methylene
chloride
bromomethanea
phenol
chloroethanea
propionaldehyde
chloroethenea
styrene
cumene
toluene
a,
2­
dichloroethanea
a,
2,4­
trichlorobenzenea
formaldehyde
m,
p­
xylene
methanol
o­
xylene
aThe
data
for
these
compounds
were
not
extracted
from
the
NCASI
data
base
because
emissions
of
these
HAP
were
below
the
method
detection
limit
for
all
test
runs
on
all
sources
tested.

1.
Memorandum
from
D.
Bullock,
K.
Hanks,
and
B.
Nicholson,
MRI
to
M.
Kissell,
EPA/
ESD.
April
28,
1999.
Summary
of
Responses
to
the
1998
EPA
Information
Collection
Request
(
MACT
Survey)
­­
General
Survey.

2.
Volatile
Organic
Compound
Emissions
From
Wood
Products
Manufacturing
Facilities,
Part
VII
­
Test
Methods,
Quality
Assurance,
Quality
Control
Procedures
and
Data
Analysis
Protocol,
Technical
Bulletin
No.
774,
National
Council
of
the
Paper
Industry
for
Air
and
Stream
Improvement,
Inc.,
Research
Triangle
Park,
NC,
1999.

3.
Letter
from
J.
Cooper,
American
Forest
&
Paper
Association
to
B.
Jordan,
EPA/
ESD.
December
23,
1996.
Discussion
of
HAP
to
be
included
in
the
NCASI
sampling
program.
ATTACHMENT
2
HAP
Potentially
Emitted
from
Each
Process
Unit
Type
Attachment
2.
Breakout
of
HAP
Emitted
from
Different
Process
Unit
Typesa
Process
unit
type
Acetaldehyde
Acrolein
Benzene
Chloroethane
Chloromethane
Cumene
Ethylbenzene
Formaldehyde
m,
pcresol
o­
cresol
MDI
MEK
Methanol
Primary
tube
dryers
X
X
X
X
X
X
X
Secondary
Tube
Dryers
X
X
X
X
Conveyor
Dryers
X
X
X
X
X
X
X
Rotary
strand
dryers
X
X
X
X
X
X
X
Conveyor
strand
dryers
X
X
X
X
X
X
X
Dry
rotary
particle
dryers
X
X
X
X
X
X
X
X
X
Paddle­
type
particle
dryers
X
X
X
X
X
X
X
Green
rotary
particle
dryers
X
X
X
X
X
X
X
Hardboard
ovens
X
X
X
X
X
Hardboard
humidifiers
X
X
X
X
X
X
X
X
X
X
Fiberboard
mat
dryer
(
bagasse)

Fiberboard
mat
dryers
(
wood)

Press
preheat
ovens
X
X
X
X
Veneer
redryers
Softwood
veneer
dryers
X
X
X
X
X
X
Hardwood
veneer
dryers
X
X
X
Particleboard
press
molds
Extruders
X
X
X
X
X
X
Engineered
wood
products
presses
X
X
X
X
Plywood
presses
X
X
X
X
Reconstituted
wood
products
presses
X
X
X
X
X
X
X
Reconstituted
wood
products
board
coolers
X
X
X
X
X
X
Pressurized
refiners
X
X
X
X
X
Atmospheric
refiners
X
X
X
X
X
X
Blenders
X
X
Formers
X
X
X
X
Sanders
X
X
X
Saws
X
X
X
Fiber
washers
X
X
X
Chippers
X
X
X
Log
vats
­
SPW
X
X
Bin
Baghouses
­
OSB
X
X
Combined
dust
baghouse
­
HPW
X
Radio
Frequency
Veneer
Dryer
­
SPW
X
X
X
Curing
Ovens
­
I­
J
X
X
Dust
collection
­
I­
J
X
Refiners/
Hammermills/
Flakers
­
PB
X
Count
of
process
units
(
37
total)
27
17
13
1
2
7
3
29
1
1
2
16
32
a
­
The
process
unit
types
listed
are
those
for
which
baseline
emissions
were
estimates.
Different
sets
of
emission
factors
were
used
to
estimate
baseline
emissions
for
the
same
type
of
equipment
used
to
make
different
products
(
e.
g.,
hardboard
tube
dryers
and
MDF
tube
dryers).
An
"
X"
appears
in
the
table
above
if
any
one
of
the
sets
of
emission
factors
included
the
HAP.
Process
unit
type
Methylene
Chloride
MIBK
Phenol
Propionaldehyde
Styrene
Toluene
m,
p­
xylene
o­
xylene
Primary
tube
dryers
X
X
X
X
X
X
X
1,1,1­
Trichloroethane
Secondary
Tube
Dryers
X
X
4­
Methyl­
2­
pentanone
Conveyor
Dryers
X
X
X
X
X
Acetophenone
Rotary
strand
dryers
X
X
X
X
X
X
Biphenyl
Conveyor
strand
dryers
X
X
X
X
X
X
Bis­(
2­
ethylhexyl
phthalate)

Dry
rotary
particle
dryers
X
X
X
X
X
X
X
<­­
Other
HAP:
Bromomethane
Paddle­
type
particle
dryers
X
X
X
X
X
X
X
Carbon
Disulfide
Green
rotary
particle
dryers
X
X
X
X
X
X
X
X
<­­
Other
HAP:
Carbon
tetrachloride
Hardboard
ovens
X
X
X
Chloroform
Di­
N­
butyl
phthalate
Hardboard
humidifiers
X
X
X
X
X
Hydroquinone
Fiberboard
mat
dryer
(
bagasse)
n­
Hexane
Fiberboard
mat
dryers
(
wood)

Press
preheat
ovens
X
Veneer
redryers
Softwood
veneer
dryers
X
X
X
X
X
X
X
Hardwood
veneer
dryers
X
X
Particleboard
press
molds
Extruders
X
X
Engineered
wood
products
presses
X
Plywood
presses
X
X
Reconstituted
wood
products
presses
X
X
X
X
X
X
Reconstituted
wood
products
board
coolers
X
X
Pressurized
refiners
X
X
X
X
Atmospheric
refiners
X
X
Blenders
Formers
X
Sanders
X
X
Saws
X
Fiber
washers
Chippers
X
Log
vats
­
SPW
Bin
Baghouses
­
OSB
Combined
dust
baghouse
­
HPW
Radio
Frequency
Veneer
Dryer
­
SPW
Curing
Ovens
­
I­
J
Dust
collection
­
I­
J
Refiners/
Hammermills/
Flakers
­
PB
Count
of
process
units
(
37
total)
3
15
20
13
10
13
9
7
ATTACHMENT
3
Attachment
3a:
Speciated
HAP
Control
Efficiency
Data
Attachment
3b:
Culled
HAP
Control
Efficiency
Data
ATTACHMENT
3a
Speciated
HAP
Control
Efficiency
Data
Page
1
of
7
Unit
Test
No.
of
No.
of
Pre­
Test
Inlet1,
Inlet1,
Inlet2,
Inlet2,
Total
inlet,
Outlet,
Outlet,
Cont.
effic.,

code
date
Product
runs
runs
BDL
treatmen
t
APCD
Pollutant
method
Units
ppm
lb/
unit
ppm
lb/
unit
lb/
unit
ppm
lb/
unit
%
Comment
B1
PB
batch
press
10/
23/
1997
PB
3
3
NONE
RTO
acetaldehyde
NICM
lb/
hr
0.2093
0.05501
0.05501
0.25654
0.073
­
33.4
all
inlet
and
outlet
runs
BDL
B1
PB
batch
press
10/
23/
1997
PB
3
3
NONE
RTO
acrolein
NICM
lb/
hr
0.14654
0.049014
0.04901
0.17634
0.064
­
31.0
all
inlet
and
outlet
runs
BDL
B1
PB
batch
press
10/
23/
1997
PB
3
3
NONE
RTO
benzene
NICM
lb/
hr
0.0403
0.018783
0.01878
0.0406
0.021
­
9.7
all
inlet
and
outlet
runs
BDL
B1
PB
batch
press
10/
23/
1997
PB
3
3
NONE
RTO
cumene
NICM
lb/
hr
0.80595
0.578026
0.57803
0.81196
0.634
­
9.7
all
inlet
and
outlet
runs
BDL
B1
PB
batch
press
10/
23/
1997
PB
3
3
NONE
RTO
formaldehyde
NICM
lb/
hr
43.2413
7.777488
7.77749
0.09376
0.018
99.8
all
outlet
runs
BDL
B1
PB
batch
press
10/
23/
1997
PB
3
3
NONE
RTO
m,
p­
xylene
NICM
lb/
hr
0.0403
0.025528
0.02553
0.0406
0.028
­
9.7
all
inlet
and
outlet
runs
BDL
B1
PB
batch
press
10/
23/
1997
PB
3
3
NONE
RTO
methanol
NICM
lb/
hr
108.6
20.75225
20.7523
0.33786
0.07
99.7
all
outlet
runs
BDL
B1
PB
batch
press
10/
23/
1997
PB
3
3
NONE
RTO
methyl
ethyl
ketone
NICM
lb/
hr
0.14355
0.061755
0.06175
0.17253
0.081
­
30.8
all
inlet
and
outlet
runs
BDL
B1
PB
batch
press
10/
23/
1997
PB
3
3
NONE
RTO
methyl
isobutyl
ketone
NICM
lb/
hr
0.56457
0.338532
0.33853
0.11658
0.076
77.6
all
outlet
runs
BDL
B1
PB
batch
press
10/
23/
1997
PB
3
3
NONE
RTO
methylene
chloride
NICM
lb/
hr
0.0403
0.020425
0.02042
0.0406
0.022
­
9.7
all
inlet
and
outlet
runs
BDL
B1
PB
batch
press
10/
23/
1997
PB
3
3
NONE
RTO
o­
xylene
NICM
lb/
hr
0.0403
0.025528
0.02553
0.0406
0.028
­
9.7
all
inlet
and
outlet
runs
BDL
B1
PB
batch
press
10/
23/
1997
PB
3
2
NONE
RTO
phenol
NICM
lb/
hr
0.24719
0.138655
0.13865
0.29568
0.18
­
29.6
2
inlet
and
2
outlet
runs
BDL
B1
PB
batch
press
10/
23/
1997
PB
3
3
NONE
RTO
propionaldehyde
NICM
lb/
hr
0.15993
0.055422
0.05542
0.19346
0.073
­
31.6
all
inlet
and
outlet
runs
BDL
B1
PB
batch
press
10/
23/
1997
PB
3
3
NONE
RTO
styrene
NICM
lb/
hr
0.0403
0.025047
0.02505
0.0406
0.027
­
9.7
all
inlet
and
outlet
runs
BDL
B1
PB
batch
press
10/
23/
1997
PB
3
0
NONE
RTO
THC
as
carbon
M25A
lb/
hr
555.985
39.84825
39.8483
4.9284
0.383
99.0
CH4
not
subtracted
(
not
measured)

B1
PB
batch
press
10/
23/
1997
PB
3
3
NONE
RTO
toluene
NICM
lb/
hr
0.0403
0.022159
0.02216
0.0406
0.024
­
9.7
all
inlet
and
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
WESP
RTO
acetaldehyde
NICM
lb/
hr
1.24594
0.471457
0.47146
0.18018
0.069
85.3
all
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
WESP
RTO
acrolein
NICM
lb/
hr
0.11986
0.057732
0.05773
0.11811
0.058
­
0.1
all
inlet
and
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
2
WESP
RTO
benzene
NICM
lb/
hr
0.03743
0.024773
0.02477
0.03914
0.027
­
9.1
2
inlet
runs
and
1
outlet
run
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
WESP
RTO
cumene
NICM
lb/
hr
0.74566
0.772714
0.77271
0.7667
0.803
­
3.9
all
inlet
and
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
2
WESP
RTO
formaldehyde
NICM
lb/
hr
1.06017
0.275196
0.2752
0.10622
0.028
89.8
2
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
1
WESP
RTO
m,
p­
xylene
NICM
lb/
hr
0.06568
0.059258
0.05926
0.03914
0.037
38.0
1
inlet
and
1
outlet
run
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
2
WESP
RTO
methanol
NICM
lb/
hr
4.47411
1.235988
1.23599
0.35166
0.099
92.0
2
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
WESP
RTO
methyl
ethyl
ketone
NICM
lb/
hr
0.11719
0.072593
0.07259
0.11516
0.072
0.2
all
inlet
and
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
WESP
RTO
methyl
isobutyl
ketone
NICM
lb/
hr
0.07807
0.067057
0.06706
0.07185
0.063
6.3
all
inlet
and
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
2
WESP
RTO
methylene
chloride
NICM
lb/
hr
0.03743
0.026939
0.02694
0.03914
0.029
­
9.1
2
inlet
runs
and
1
outlet
run
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
2
WESP
RTO
o­
xylene
NICM
lb/
hr
0.03743
0.03367
0.03367
0.03914
0.037
­
9.1
2
inlet
runs
and
1
outlet
run
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
WESP
RTO
phenol
NICM
lb/
hr
0.14744
0.119303
0.1193
0.14865
0.122
­
2.3
all
inlet
and
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
WESP
RTO
propionaldehyde
NICM
lb/
hr
0.13182
0.065806
0.06581
0.13136
0.067
­
1.2
all
inlet
and
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
2
WESP
RTO
styrene
NICM
lb/
hr
0.03743
0.033035
0.03304
0.03914
0.036
­
9.1
2
inlet
runs
and
1
outlet
run
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
0
WESP
RTO
THC
as
carbon
M25A
lb/
hr
488.493
50.41784
50.4178
6.43446
0.673
98.7
CH4
subtracted
from
inlet
&
outlet
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
1
WESP
RTO
toluene
NICM
lb/
hr
0.08247
0.064641
0.06464
0.03914
0.032
50.7
1
inlet
and
1
outlet
run
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
NONE
WESP/
RTO
acetaldehyde
NICM
lb/
hr
1.20706
0.36108
0.36108
0.18018
0.069
80.8
3
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
NONE
WESP/
RTO
acrolein
NICM
lb/
hr
0.14465
0.054953
0.05495
0.11811
0.058
­
5.1
all
inlet
and
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
NONE
WESP/
RTO
benzene
NICM
lb/
hr
0.03865
0.020468
0.02047
0.03914
0.027
­
32.0
3
inlet
and
1
outlet
run
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
NONE
WESP/
RTO
cumene
NICM
lb/
hr
0.77308
0.629907
0.62991
0.7667
0.803
­
27.4
all
inlet
and
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
2
NONE
WESP/
RTO
formaldehyde
NICM
lb/
hr
0.99953
0.202858
0.20286
0.10622
0.028
86.2
2
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
2
NONE
WESP/
RTO
m,
p­
xylene
NICM
lb/
hr
0.05223
0.037675
0.03768
0.03914
0.037
2.5
2
inlet
and
1
outlet
run
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
2
NONE
WESP/
RTO
methanol
NICM
lb/
hr
3.97445
0.859329
0.85933
0.35166
0.099
88.5
2
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
NONE
WESP/
RTO
methyl
ethyl
ketone
NICM
lb/
hr
0.14168
0.069222
0.06922
0.11516
0.072
­
4.7
all
inlet
and
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
NONE
WESP/
RTO
methyl
isobutyl
ketone
NICM
lb/
hr
0.09798
0.066509
0.06651
0.07185
0.063
5.5
all
inlet
and
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
NONE
WESP/
RTO
methylene
chloride
NICM
lb/
hr
0.03865
0.022258
0.02226
0.03914
0.029
­
32.0
all
inlet
and
1
outlet
run
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
NONE
WESP/
RTO
o­
xylene
NICM
lb/
hr
0.03865
0.027819
0.02782
0.03914
0.037
­
32.0
3
inlet
and
1
outlet
run
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
NONE
WESP/
RTO
phenol
NICM
lb/
hr
0.17546
0.111897
0.1119
0.14865
0.122
­
9.1
all
inlet
and
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
NONE
WESP/
RTO
propionaldehyde
NICM
lb/
hr
0.15802
0.062193
0.06219
0.13136
0.067
­
7.0
all
inlet
and
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
NONE
WESP/
RTO
styrene
NICM
lb/
hr
0.03865
0.027295
0.02729
0.03914
0.036
­
32.0
3
inlet
and
1
outlet
run
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
0
NONE
WESP/
RTO
THC
as
carbon
M25A
lb/
hr
488.493
50.41784
50.4178
6.43446
0.673
98.7
CH4
subtracted
from
inlet
&
outlet
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
2
NONE
WESP/
RTO
toluene
NICM
lb/
hr
0.06121
0.038357
0.03836
0.03914
0.032
16.9
2
inlet
and
1
outlet
run
BDL
Page
2
of
7
Unit
Test
No.
of
No.
of
Pre­
Test
Inlet1,
Inlet1,
Inlet2,
Inlet2,
Total
inlet,
Outlet,
Outlet,
Cont.
effic.,

code
date
Product
runs
runs
BDL
treatmen
t
APCD
Pollutant
method
Units
ppm
lb/
unit
ppm
lb/
unit
lb/
unit
ppm
lb/
unit
%
Comment
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
3
NONE
RTO
acetaldehyde
NICM
lb/
hr
11.7403
2.61133
2.61133
0.20281
0.051
98.0
all
outlet
runs
BDL
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
3
NONE
RTO
acrolein
NICM
lb/
hr
3.3895
0.95692
0.95692
0.14201
0.046
95.2
all
outlet
runs
BDL
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
3
NONE
RTO
benzene
NICM
lb/
hr
0.03541
0.013988
0.01399
0.03911
0.018
­
25.6
all
inlet
and
outlet
runs
BDL
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
3
NONE
RTO
cumene
NICM
lb/
hr
0.7082
0.430467
0.43047
0.78221
0.541
­
25.6
all
inlet
and
outlet
runs
BDL
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
2
NONE
RTO
formaldehyde
NICM
lb/
hr
4.39499
0.661082
0.66108
0.11196
0.019
97.1
2
outlet
runs
BDL
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
3
NONE
RTO
m,
p­
xylene
NICM
lb/
hr
0.03541
0.019011
0.01901
0.03911
0.024
­
25.6
all
inlet
and
outlet
runs
BDL
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
3
NONE
RTO
methanol
NICM
lb/
hr
9.34398
1.520261
1.52026
0.26445
0.049
96.8
all
outlet
runs
BDL
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
3
NONE
RTO
methyl
ethyl
ketone
NICM
lb/
hr
0.1339
0.04891
0.04891
0.13912
0.058
­
18.1
all
inlet
and
outlet
runs
BDL
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
3
NONE
RTO
methyl
isobutyl
ketone
NICM
lb/
hr
0.09213
0.046735
0.04674
0.09671
0.056
­
19.4
all
inlet
and
outlet
runs
BDL
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
3
NONE
RTO
o­
xylene
NICM
lb/
hr
0.03541
0.019011
0.01901
0.03911
0.024
­
25.6
all
inlet
and
outlet
runs
BDL
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
2
NONE
RTO
phenol
NICM
lb/
hr
0.1662
0.07925
0.07925
0.23959
0.131
­
64.8
all
inlet
runs
BDL;
2
outlet
runs
BDL
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
3
NONE
RTO
propionaldehyde
NICM
lb/
hr
11.7729
3.431402
3.4314
0.15499
0.052
98.5
all
outlet
runs
BDL
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
3
NONE
RTO
styrene
NICM
lb/
hr
0.03541
0.018653
0.01865
0.03911
0.023
­
25.6
all
inlet
and
outlet
runs
BDL
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
0
NONE
RTO
THC
as
carbon
M25A
lb/
hr
352.185
21.41545
21.4155
4.67233
0.32
98.5
CH4
not
subtracted
(
not
measured)

F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
3
NONE
RTO
toluene
NICM
lb/
hr
0.03541
0.016502
0.0165
0.03911
0.021
­
25.6
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press,
No.
2
5/
5/
1998
OSB
3
3
NONE
RTO
acetaldehyde
NICM
lb/
hr
0.43672
0.184293
0.18429
0.2078
0.098
46.7
1
inlet
and
3
outlet
runs
BDL
B1
OSB
hot
press,
No.
2
5/
5/
1998
OSB
3
3
NONE
RTO
acrolein
NICM
lb/
hr
0.14098
0.075816
0.07582
0.14541
0.087
­
15.4
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press,
No.
2
5/
5/
1998
OSB
3
3
NONE
RTO
benzene
NICM
lb/
hr
0.03887
0.029122
0.02912
0.0398
0.033
­
14.5
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press,
No.
2
5/
5/
1998
OSB
3
3
NONE
RTO
cumene
NICM
lb/
hr
0.77733
0.896218
0.89622
0.79608
1.026
­
14.5
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press,
No.
2
5/
5/
1998
OSB
3
0
NONE
RTO
formaldehyde
NICM
lb/
hr
5.62712
1.62473
1.62473
0.54175
0.175
89.2
B1
OSB
hot
press,
No.
2
5/
5/
1998
OSB
3
3
NONE
RTO
m,
p­
xylene
NICM
lb/
hr
0.03887
0.03958
0.03958
0.0398
0.045
­
14.5
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press,
No.
2
5/
5/
1998
OSB
3
1
NONE
RTO
methanol
NICM
lb/
hr
17.7308
5.441179
5.44118
0.83214
0.285
94.8
1
outlet
run
BDL
B1
OSB
hot
press,
No.
2
5/
5/
1998
OSB
3
3
NONE
RTO
methyl
ethyl
ketone
NICM
lb/
hr
0.13811
0.095524
0.09552
0.14244
0.11
­
15.3
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press,
No.
2
5/
5/
1998
OSB
3
3
NONE
RTO
methyl
isobutyl
ketone
NICM
lb/
hr
0.09602
0.092258
0.09226
0.09891
0.106
­
15.2
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press,
No.
2
5/
5/
1998
OSB
3
2
NONE
RTO
phenol
NICM
lb/
hr
0.89745
0.810979
0.81098
0.3779
0.383
52.7
2
outlet
runs
BDL
B1
OSB
hot
press,
No.
2
5/
5/
1998
OSB
3
3
NONE
RTO
propionaldehyde
NICM
lb/
hr
0.15385
0.085721
0.08572
0.15872
0.099
­
15.4
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press,
No.
2
5/
5/
1998
OSB
3
3
NONE
RTO
styrene
NICM
lb/
hr
0.03887
0.038834
0.03883
0.0398
0.044
­
14.5
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press,
No.
2
5/
5/
1998
OSB
3
0
NONE
RTO
THC
as
carbon
M25A
lb/
hr
51.3821
5.913199
5.9132
3.306
0.426
92.8
CH4
not
subtracted
(
not
measured)
B1
OSB
hot
press,
No.
2
5/
5/
1998
OSB
3
3
NONE
RTO
toluene
NICM
lb/
hr
0.03887
0.034357
0.03436
0.0398
0.039
­
14.5
all
inlet
and
outlet
runs
BDL
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
0
WESP
RTO
acetaldehyde
NICM
lb/
hr
33.5545
12.18942
12.1894
5.18795
2.211
81.9
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
0
WESP
RTO
acrolein
NICM
lb/
hr
8.47441
3.90733
3.90733
1.13352
0.614
84.3
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
0
WESP
RTO
benzene
NICM
lb/
hr
0.58265
0.376021
0.37602
0.23681
0.179
52.4
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
3
WESP
RTO
cumene
NICM
lb/
hr
0.76617
0.762083
0.76208
0.77639
0.903
­
18.6
all
inlet
and
outlet
runs
BDL
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
0
WESP
RTO
formaldehyde
NICM
lb/
hr
45.2337
11.22791
11.2279
13.1172
3.815
66.0
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
3
WESP
RTO
m,
p­
xylene
NICM
lb/
hr
0.03831
0.033656
0.03366
0.03882
0.04
­
18.6
all
inlet
and
outlet
runs
BDL
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
0
WESP
RTO
methanol
NICM
lb/
hr
24.0545
6.372851
6.37285
4.57033
1.416
77.8
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
3
WESP
RTO
methyl
ethyl
ketone
NICM
lb/
hr
0.23546
0.139938
0.13994
0.13925
0.097
30.5
1
inlet
and
3
outlet
runs
BDL
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
3
WESP
RTO
methyl
isobutyl
ketone
NICM
lb/
hr
0.09341
0.077429
0.07743
0.09665
0.094
­
21.0
all
inlet
and
outlet
runs
BDL
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
0
WESP
RTO
phenol
NICM
lb/
hr
0.68283
0.534002
0.534
0.40188
0.366
31.5
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
1
WESP
RTO
propionaldehyde
NICM
lb/
hr
1.41241
0.676412
0.67641
0.26402
0.148
78.1
1
outlet
run
BDL
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
3
WESP
RTO
styrene
NICM
lb/
hr
0.07777
0.066835
0.06683
0.03882
0.039
41.4
1
inlet
and
3
outlet
runs
BDL
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
0
WESP
RTO
THC
as
carbon
M25A
lb/
hr
390.034
38.56629
38.5663
57.191
6.628
82.8
CH4
not
subtracted
(
not
measured)

R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
3
WESP
RTO
toluene
NICM
lb/
hr
0.33005
0.25076
0.25076
0.03882
0.035
86.2
3
outlet
runs
BDL
Page
3
of
7
Unit
Test
No.
of
No.
of
Pre­
Test
Inlet1,
Inlet1,
Inlet2,
Inlet2,
Total
inlet,
Outlet,
Outlet,
Cont.
effic.,

code
date
Product
runs
runs
BDL
treatmen
t
APCD
Pollutant
method
Units
ppm
lb/
unit
ppm
lb/
unit
lb/
unit
ppm
lb/
unit
%
Comment
B1
OSB
hot
press
1/
18/
1998
OSB
3
3
NONE
RTO
acetaldehyde
NICM
lb/
hr
0.69324
0.64712
0.64712
0.19776
0.166
74.3
nat.
gas
injection
mode;
1
inlet
and
3
outlet
runs
B1
OSB
hot
press
1/
18/
1998
OSB
3
3
NONE
RTO
acrolein
NICM
lb/
hr
0.1579
0.18575
0.18575
0.13871
0.149
20.0
nat.
gas
injection
mode;
all
inlet
and
outlet
runs
B1
OSB
hot
press
1/
18/
1998
OSB
3
3
NONE
RTO
benzene
NICM
lb/
hr
0.03853
0.063176
0.06318
0.03877
0.058
8.4
nat.
gas
injection
mode;
all
inlet
and
outlet
runs
B1
OSB
hot
press
1/
18/
1998
OSB
3
3
NONE
RTO
cumene
NICM
lb/
hr
0.77064
1.944221
1.94422
0.77534
1.78
8.4
nat.
gas
injection
mode;
all
inlet
and
outlet
runs
B1
OSB
hot
press
1/
18/
1998
OSB
3
2
NONE
RTO
formaldehyde
NICM
lb/
hr
3.44725
2.168481
2.16848
0.18984
0.11
94.9
nat.
gas
injection
mode;
2
outlet
runs
BDL
B1
OSB
hot
press
1/
18/
1998
OSB
3
3
NONE
RTO
m,
p­
xylene
NICM
lb/
hr
0.03853
0.085863
0.08586
0.03877
0.079
8.4
nat.
gas
injection
mode;
all
inlet
and
outlet
runs
B1
OSB
hot
press
1/
18/
1998
OSB
3
3
NONE
RTO
methanol
NICM
lb/
hr
25.4525
17.03734
17.0373
0.25763
0.157
99.1
nat.
gas
injection
mode;
3
outlet
runs
BDL
B1
OSB
hot
press
1/
18/
1998
OSB
3
3
NONE
RTO
methyl
ethyl
ketone
NICM
lb/
hr
0.15455
0.233826
0.23383
0.1359
0.187
20.0
nat.
gas
injection
mode;
all
inlet
and
outlet
runs
B1
OSB
hot
press
1/
18/
1998
OSB
3
3
NONE
RTO
methyl
isobutyl
ketone
NICM
lb/
hr
0.10534
0.221419
0.22142
0.09471
0.181
18.2
nat.
gas
injection
mode;
all
inlet
and
outlet
runs
B1
OSB
hot
press
1/
18/
1998
OSB
3
2
NONE
RTO
phenol
NICM
lb/
hr
0.50408
0.993354
0.99335
0.22458
0.404
59.3
nat
gas
injection
mode;
2
outlet
runs
BDL
B1
OSB
hot
press
1/
18/
1998
OSB
3
3
NONE
RTO
propionaldehyde
NICM
lb/
hr
0.17295
0.210786
0.21079
0.15131
0.168
20.4
nat.
gas
injection
mode;
all
inlet
and
outlet
runs
B1
OSB
hot
press
1/
18/
1998
OSB
3
3
NONE
RTO
styrene
NICM
lb/
hr
0.03853
0.084246
0.08425
0.03877
0.077
8.4
nat.
gas
injection
mode;
all
inlet
and
outlet
runs
B1
OSB
hot
press
1/
18/
1998
OSB
3
3
NONE
RTO
THC
as
carbon
M25A
lb/
hr
255.324
64.32727
64.3273
0.5
0.115
99.8
nat.
gas
injection
mode;
all
outlet
runs
BDL;
CH
subtracted
(
not
measured)

B1
OSB
hot
press
1/
18/
1998
OSB
3
3
NONE
RTO
toluene
NICM
lb/
hr
0.03853
0.074532
0.07453
0.03877
0.068
8.4
nat.
gas
injection
mode;
all
inlet
and
outlet
runs
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
acetaldehyde
NICM
lb/
hr
4.63534
4.093543
4.09354
0.19402
0.239
94.2
nat.
gas
injection
mode;
all
outlet
runs
BDL
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
acrolein
NICM
lb/
hr
2.53329
2.845826
2.84583
0.13626
0.214
92.5
nat.
gas
injection
mode;
all
outlet
runs
BDL
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
benzene
NICM
lb/
hr
0.15845
0.247967
0.24797
0.03848
0.084
66.0
nat.
gas
injection
mode;
all
outlet
runs
BDL
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
cumene
NICM
lb/
hr
0.74323
1.789863
1.78986
0.76964
2.592
­
44.8
nat.
gas
injection
mode;
all
inlet
and
outlet
runs
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
4
WESP
RTO
formaldehyde
NICM
lb/
hr
19.0781
11.49902
11.499
0.13634
0.114
99.0
nat.
gas
injection
mode;
4
outlet
runs
BDL
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
m,
p­
xylene
NICM
lb/
hr
0.15135
0.321979
0.32198
0.03848
0.114
64.4
nat.
gas
injection
mode;
all
outlet
runs
BDL
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
methanol
NICM
lb/
hr
6.85387
4.399032
4.39903
0.25259
0.226
94.9
nat.
gas
injection
mode;
all
outlet
runs
BDL
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
methyl
ethyl
ketone
NICM
lb/
hr
0.25732
0.371997
0.372
0.13351
0.27
27.5
nat.
gas
injection
mode;
1
inlet
and
all
outlet
run
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
methyl
isobutyl
ketone
NICM
lb/
hr
0.24273
0.487206
0.48721
0.09321
0.262
46.3
nat.
gas
injection
mode;
all
outlet
runs
BDL
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
2
WESP
RTO
phenol
NICM
lb/
hr
0.29702
0.559844
0.55984
0.40066
1.055
­
88.4
nat.
gas
injection
mode;
2
inlet
runs
and
1
outlet
BDL
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
propionaldehyde
NICM
lb/
hr
0.32756
0.381538
0.38154
0.14858
0.242
36.6
nat.
gas
injection
mode;
1
inlet
and
all
outlet
run
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
styrene
NICM
lb/
hr
0.03716
0.077557
0.07756
0.03848
0.112
­
44.8
nat.
gas
injection
mode;
all
inlet
and
outlet
runs
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
0
WESP
RTO
THC
as
carbon
M25A
lb/
hr
1190
286.0403
286.04
43.8125
14.74
94.8
nat.
gas
injection
mode;
CH4
subtracted
from
in
outlet
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
toluene
NICM
lb/
hr
0.31279
0.57752
0.57752
0.03848
0.099
82.8
nat.
gas
injection
mode;
all
outlet
runs
BDL
Page
4
of
7
Unit
Test
No.
of
No.
of
Pre­
Test
Inlet1,
Inlet1,
Inlet2,
Inlet2,
Total
inlet,
Outlet,
Outlet,
Cont.
effic.,

code
date
Product
runs
runs
BDL
treatmen
t
APCD
Pollutant
method
Units
ppm
lb/
unit
ppm
lb/
unit
lb/
unit
ppm
lb/
unit
%
Comment
T1
HB
tempering
oven
6/
26/
1998
HB
3
3
NONE
RTO
acetaldehyde
NICM
lb/
hr
31.7964
2.57904
2.57904
0.2011
0.022
99.2
all
outlet
runs
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
3
NONE
RTO
acrolein
NICM
lb/
hr
7.78131
0.803204
0.8032
0.14073
0.019
97.6
all
outlet
runs
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
3
NONE
RTO
benzene
NICM
lb/
hr
0.0393
0.005652
0.00565
0.03855
0.007
­
31.4
all
inlet
and
outlet
runs
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
3
NONE
RTO
cumene
NICM
lb/
hr
0.78605
0.17395
0.17395
0.77091
0.229
­
31.4
all
inlet
and
outlet
runs
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
3
NONE
RTO
formaldehyde
NICM
lb/
hr
2.62
0.145166
0.14517
0.06714
0.005
96.6
all
outlet
runs
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
3
NONE
RTO
m,
p­
xylene
NICM
lb/
hr
0.0393
0.007682
0.00768
0.03855
0.01
­
31.4
all
inlet
and
outlet
runs
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
2
NONE
RTO
methanol
NICM
lb/
hr
8.45039
0.497676
0.49768
0.38103
0.03
94.0
2
outlet
runs
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
3
NONE
RTO
methyl
ethyl
ketone
NICM
lb/
hr
0.19283
0.025866
0.02587
0.13786
0.025
5.2
2
inlet
runs
and
3
outlet
runs
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
3
NONE
RTO
methyl
isobutyl
ketone
NICM
lb/
hr
0.84149
0.155454
0.15545
0.09574
0.024
84.8
all
outlet
runs
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
3
NONE
RTO
o­
xylene
NICM
lb/
hr
0.0393
0.007682
0.00768
0.03855
0.01
­
31.4
all
inlet
and
outlet
runs
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
1
NONE
RTO
phenol
NICM
lb/
hr
0.36623
0.06332
0.06332
0.28817
0.067
­
5.8
1
outlet
run
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
3
NONE
RTO
propionaldehyde
NICM
lb/
hr
31.5247
3.372796
3.3728
0.15361
0.022
99.3
all
outlet
runs
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
3
NONE
RTO
styrene
NICM
lb/
hr
0.0393
0.007538
0.00754
0.03855
0.01
­
31.4
all
inlet
and
outlet
runs
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
3
NONE
RTO
THC
as
carbon
M25A
lb/
hr
763.837
16.87325
16.8733
0.5
0.015
99.9
all
outlet
runs
BDL;
CH4
subtracted
from
inlet
b
outlet
(
all
outlet
THC
=
CH4)

T1
HB
tempering
oven
6/
26/
1998
HB
3
3
NONE
RTO
toluene
NICM
lb/
hr
0.0393
0.006668
0.00667
0.03855
0.009
­
31.4
all
inlet
and
outlet
runs
BDL
M1
Dryer/
continuous
press
1/
13/
1998
MDF
3
3
RBP
RTO
acetaldehyde
NICM
lb/
hr
0.62819
0.369673
0.19796
0.04315
0.41282
0.20345
0.164
60.3
all
press
and
outlet
runs
BDL
M1
Dryer/
continuous
press
1/
13/
1998
MDF
3
3
RBP
RTO
acrolein
NICM
lb/
hr
0.13111
0.098053
0.139683
0.03875
0.1368
0.14249
0.146
­
6.7
all
inlet
and
outlet
runs
BDL
M1
Dryer/
continuous
press
1/
13/
1998
MDF
3
3
RBP
RTO
benzene
NICM
lb/
hr
0.03899
0.040623
0.041043
0.01587
0.05649
0.0393
0.056
0.7
all
inlet
and
outlet
runs
BDL
M1
Dryer/
continuous
press
1/
13/
1998
MDF
3
3
RBP
RTO
cumene
NICM
lb/
hr
0.77974
1.25015
0.820867
0.48836
1.73851
0.78599
1.727
0.7
all
inlet
and
outlet
runs
BDL
M1
Dryer/
continuous
press
1/
13/
1998
MDF
3
2
RBP
RTO
formaldehyde
NICM
lb/
hr
16.2976
6.553666
7.692813
1.14699
7.70065
0.18413
0.101
98.7
2
outlet
runs
BDL
M1
Dryer/
continuous
press
1/
13/
1998
MDF
3
3
RBP
RTO
m,
p­
xylene
NICM
lb/
hr
0.03899
0.055211
0.041043
0.02157
0.07678
0.0393
0.076
0.7
all
inlet
and
outlet
runs
BDL
M1
Dryer/
continuous
press
1/
13/
1998
MDF
3
3
RBP
RTO
methanol
NICM
lb/
hr
28.6029
12.25112
8.896868
1.40955
13.6607
0.26527
0.155
98.9
all
outlet
runs
BDL
M1
Dryer/
continuous
press
1/
13/
1998
MDF
3
3
RBP
RTO
methyl
ethyl
ketone
NICM
lb/
hr
0.12852
0.123619
0.136913
0.04885
0.17247
0.13959
0.184
­
6.7
all
inlet
and
outlet
runs
BDL
M1
Dryer/
continuous
press
1/
13/
1998
MDF
3
3
RBP
RTO
methyl
isobutyl
ketone
NICM
lb/
hr
0.09055
0.120988
0.144952
0.0719
0.19288
0.09706
0.178
7.9
all
dryer
and
outlet
runs
BDL;
2
press
runs
BDL
M1
Dryer/
continuous
press
1/
13/
1998
MDF
3
3
RBP
RTO
methylene
chloride
NICM
lb/
hr
0.03899
0.044175
0.041043
0.01726
0.06143
0.0393
0.061
0.7
all
inlet
and
outlet
runs
BDL
M1
Dryer/
continuous
press
1/
13/
1998
MDF
3
3
RBP
RTO
o­
xylene
NICM
lb/
hr
0.03899
0.055211
0.041043
0.02157
0.07678
0.0393
0.076
0.7
all
inlet
and
outlet
runs
BDL
M1
Dryer/
continuous
press
1/
13/
1998
MDF
3
2
RBP
RTO
phenol
NICM
lb/
hr
0.27929
0.348447
0.228859
0.10608
0.45453
0.25696
0.441
3.1
2
press
and
outlet
runs
BDL;
1
dryer
run
BDL
M1
Dryer/
continuous
press
1/
13/
1998
MDF
3
3
RBP
RTO
propionaldehyde
NICM
lb/
hr
0.14273
0.110586
0.152121
0.04372
0.15431
0.1555
0.165
­
7.0
all
inlet
and
outlet
runs
BDL
M1
Dryer/
continuous
press
1/
13/
1998
MDF
3
3
RBP
RTO
styrene
NICM
lb/
hr
0.03899
0.054171
0.041043
0.02116
0.07533
0.0393
0.075
0.7
all
inlet
and
outlet
runs
BDL
M1
Dryer/
continuous
press
1/
13/
1998
MDF
2
0
RBP
RTO
THC
as
carbon
M25A
lb/
hr
201.149
32.22919
20.33499
1.2081
33.4373
9.58696
2.085
93.8
CH4
not
subtracted
(
not
measured)

M1
Dryer/
continuous
press
1/
13/
1998
MDF
3
3
RBP
RTO
toluene
NICM
lb/
hr
0.03899
0.047925
0.041043
0.01872
0.06665
0.0393
0.066
0.7
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press
4/
3/
1998
OSB
3
3
NONE
RTO
acetaldehyde
NICM
lb/
hr
0.46774
0.246413
0.24641
0.20974
0.152
38.1
2
inlet
and
3
outlet
runs
BDL;
nat.
gas
injection
B1
OSB
hot
press
4/
3/
1998
OSB
3
3
NONE
RTO
acrolein
NICM
lb/
hr
0.13883
0.097305
0.09731
0.14691
0.136
­
39.7
all
inlet
and
outlet
runs
BDL;
nat.
gas
injection
m
B1
OSB
hot
press
4/
3/
1998
OSB
3
3
NONE
RTO
benzene
NICM
lb/
hr
0.04043
0.039426
0.03943
0.04055
0.052
­
32.6
all
inlet
and
outlet
runs
BDL;
nat.
gas
injection
m
B1
OSB
hot
press
4/
3/
1998
OSB
3
3
NONE
RTO
cumene
NICM
lb/
hr
0.80863
1.213313
1.21331
0.81109
1.609
­
32.6
all
inlet
and
outlet
runs
BDL;
nat.
gas
injection
m
B1
OSB
hot
press
4/
3/
1998
OSB
3
3
NONE
RTO
formaldehyde
NICM
lb/
hr
2.42042
0.892949
0.89295
0.07391
0.037
95.9
all
outlet
runs
BDL;
nat.
gas
injection
mode
B1
OSB
hot
press
4/
3/
1998
OSB
3
3
NONE
RTO
m,
p­
xylene
NICM
lb/
hr
0.04043
0.053584
0.05358
0.04055
0.071
­
32.6
all
inlet
and
outlet
runs
BDL;
nat.
gas
injection
m
B1
OSB
hot
press
4/
3/
1998
OSB
3
3
NONE
RTO
methanol
NICM
lb/
hr
19.6742
7.913139
7.91314
0.27345
0.144
98.2
all
outlet
runs
BDL;
nat.
gas
injection
mode
B1
OSB
hot
press
4/
3/
1998
OSB
3
3
NONE
RTO
methyl
ethyl
ketone
NICM
lb/
hr
0.13607
0.122654
0.12265
0.14392
0.171
­
39.6
all
inlet
and
outlet
runs
BDL;
nat.
gas
injection
m
B1
OSB
hot
press
4/
3/
1998
OSB
3
3
NONE
RTO
methyl
isobutyl
ketone
NICM
lb/
hr
0.09551
0.119565
0.11956
0.10008
0.165
­
38.4
all
inlet
and
outlet
runs
BDL;
nat.
gas
injection
m
B1
OSB
hot
press
4/
3/
1998
OSB
3
3
NONE
RTO
phenol
NICM
lb/
hr
0.16743
0.197022
0.19702
0.17782
0.276
­
40.2
all
inlet
and
outlet
runs
BDL;
nat.
gas
injection
m
B1
OSB
hot
press
4/
3/
1998
OSB
3
3
NONE
RTO
propionaldehyde
NICM
lb/
hr
0.15124
0.109826
0.10983
0.16032
0.154
­
39.9
all
inlet
and
outlet
runs
BDL;
nat.
gas
injection
m
B1
OSB
hot
press
4/
3/
1998
OSB
3
3
NONE
RTO
styrene
NICM
lb/
hr
0.04043
0.052575
0.05257
0.04055
0.07
­
32.6
all
inlet
and
outlet
runs
BDL;
nat.
gas
injection
m
B1
OSB
hot
press
4/
3/
1998
OSB
3
0
NONE
RTO
THC
as
carbon
M25A
lb/
hr
218.748
32.65834
32.6583
4.36404
0.864
97.4
CH4
not
subtracted
(
not
measured);
nat.
gas
inj
mode
B1
OSB
hot
press
4/
3/
1998
OSB
3
3
NONE
RTO
toluene
NICM
lb/
hr
0.04043
0.046513
0.04651
0.04055
0.062
­
32.6
all
inlet
and
outlet
runs
BDL;
nat.
gas
injection
m
Page
5
of
7
Unit
Test
No.
of
No.
of
Pre­
Test
Inlet1,
Inlet1,
Inlet2,
Inlet2,
Total
inlet,
Outlet,
Outlet,
Cont.
effic.,

code
date
Product
runs
runs
BDL
treatmen
t
APCD
Pollutant
method
Units
ppm
lb/
unit
ppm
lb/
unit
lb/
unit
ppm
lb/
unit
%
Comment
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
0
NONE
RTO
acetaldehyde
NICM
lb/
hr
6.49437
5.302698
5.3027
0.7489
0.628
88.2
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
6
NONE
RTO
acrolein
NICM
lb/
hr
3.24896
3.376787
3.37679
0.18193
0.195
94.2
all
outlet
runs
BDL;
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
6
NONE
RTO
benzene
NICM
lb/
hr
0.27958
0.404575
0.40457
0.05044
0.075
81.4
all
outlet
runs
BDL;
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
6
NONE
RTO
cumene
NICM
lb/
hr
0.97392
2.164732
2.16473
1.00871
2.318
­
7.1
all
inlet
and
outlet
runs
BDL;
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
1
NONE
RTO
formaldehyde
NICM
lb/
hr
22.9191
12.75396
12.754
2.12947
1.268
90.1
1
outlet
run
BDL;
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
6
NONE
RTO
m,
p­
xylene
NICM
lb/
hr
0.20745
0.408414
0.40841
0.05044
0.102
74.9
all
outlet
runs
BDL;
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
2
NONE
RTO
methanol
NICM
lb/
hr
8.5945
5.094153
5.09415
0.71303
0.434
91.5
2
outlet
runs
BDL;
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
6
NONE
RTO
methyl
ethyl
ketone
NICM
lb/
hr
0.1862
0.248517
0.24852
0.17824
0.246
1.2
all
inlet
and
outlet
runs
BDL;
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
6
NONE
RTO
methyl
isobutyl
ketone
NICM
lb/
hr
0.12788
0.237069
0.23707
0.12404
0.237
­
0.2
all
inlet
and
outlet
runs
BDL;
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
5
NONE
RTO
phenol
NICM
lb/
hr
0.2313
0.40297
0.40297
0.34227
0.62
­
53.9
all
inlet
and
5
outlet
runs
BDL;
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
6
NONE
RTO
propionaldehyde
NICM
lb/
hr
0.51269
0.552495
0.5525
0.19851
0.22
60.1
1
inlet
and
all
outlet
runs
BDL;
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
6
NONE
RTO
styrene
NICM
lb/
hr
0.0487
0.093801
0.0938
0.05044
0.1
­
7.1
all
inlet
and
outlet
runs
BDL;
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
4
0
NONE
RTO
THC
as
carbon
M25A
lb/
hr
766.275
169.8813
169.881
29.3996
6.933
95.9
CH4
not
subtracted
(
not
measured);
burner
mod
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
6
NONE
RTO
toluene
NICM
lb/
hr
0.41571
0.710179
0.71018
0.05044
0.089
87.5
all
outlet
runs
BDL;
burner
mode
V1
Dryer
1,2,3,4
heated
zones
11/
17/
1997
SPW
3
2
NONE
RTO
acetaldehyde
NICM
lb/
hr
1.22305
0.376651
0.37665
0.26785
0.09
76.0
2
outlet
runs
BDL
V1
Dryer
1,2,3,4
heated
zones
11/
17/
1997
SPW
3
3
NONE
RTO
acrolein
NICM
lb/
hr
0.13418
0.053946
0.05395
0.13302
0.058
­
7.1
2
inlet
and
3
outlet
runs
BDL
V1
Dryer
1,2,3,4
heated
zones
11/
17/
1997
SPW
3
3
NONE
RTO
benzene
NICM
lb/
hr
0.03802
0.020804
0.0208
0.03575
0.022
­
4.1
all
inlet
and
outlet
runs
BDL
V1
Dryer
1,2,3,4
heated
zones
11/
17/
1997
SPW
3
2
NONE
RTO
formaldehyde
NICM
lb/
hr
4.38435
0.910997
0.911
0.12438
0.029
96.8
2
outlet
runs
BDL
V1
Dryer
1,2,3,4
heated
zones
11/
17/
1997
SPW
3
3
NONE
RTO
m,
p­
xylene
NICM
lb/
hr
0.03802
0.028275
0.02827
0.03575
0.029
­
4.1
all
inlet
and
outlet
runs
BDL
V1
Dryer
1,2,3,4
heated
zones
11/
17/
1997
SPW
3
2
NONE
RTO
methanol
NICM
lb/
hr
5.50852
1.233799
1.2338
0.40357
0.101
91.8
2
outlet
runs
BDL
V1
Dryer
1,2,3,4
heated
zones
11/
17/
1997
SPW
3
3
NONE
RTO
methyl
ethyl
ketone
(
MEK)
NICM
lb/
hr
0.12812
0.064735
0.06474
0.13029
0.073
­
12.4
all
inlet
and
outlet
runs
BDL
V1
Dryer
1,2,3,4
heated
zones
11/
17/
1997
SPW
3
3
NONE
RTO
methyl
isobutyl
ketone
NICM
lb/
hr
0.08991
0.063102
0.0631
0.0902
0.07
­
10.9
all
inlet
and
outlet
runs
BDL
V1
Dryer
1,2,3,4
heated
zones
11/
17/
1997
SPW
3
3
NONE
RTO
o­
xylene
NICM
lb/
hr
0.03802
0.028275
0.02827
0.03575
0.029
­
4.1
all
inlet
and
outlet
runs
BDL
V1
Dryer
1,2,3,4
heated
zones
11/
17/
1997
SPW
3
2
NONE
RTO
phenol
NICM
lb/
hr
0.21899
0.142386
0.14239
0.235
0.172
­
21.1
2
inlet
and
2
outlet
runs
BDL
V1
Dryer
1,2,3,4
heated
zones
11/
17/
1997
SPW
3
3
NONE
RTO
propionaldehyde
NICM
lb/
hr
0.14241
0.057966
0.05797
0.14529
0.065
­
12.8
all
inlet
and
outlet
runs
BDL
V1
Dryer
1,2,3,4
heated
zones
11/
17/
1997
SPW
3
3
NONE
RTO
styrene
NICM
lb/
hr
0.03802
0.027742
0.02774
0.03575
0.029
­
4.1
all
inlet
and
outlet
runs
BDL
V1
Dryer
1,2,3,4
heated
zones
11/
17/
1997
SPW
3
3
NONE
RTO
toluene
NICM
lb/
hr
0.03802
0.024543
0.02454
0.03575
0.026
­
4.1
all
inlet
and
outlet
runs
BDL
V1
Dryer
1,2,3,4
heated
zones
11/
17/
1997
SPW
3
0
NONE
RTO
THC
as
carbon
M25A
lb/
hr
1814.16
151.151
151.151
87.112
8.1
94.6
CH4
subtracted
from
inlet
and
outlet
V1
Dryer
No.
1,2,3
heated
zones
12/
9/
1997
SPW
3
0
NONE
RTO
acetaldehyde
NICM
lb/
hr
5.78019
0.868799
0.8688
0.6621
0.107
87.7
V1
Dryer
No.
1,2,3
heated
zones
12/
9/
1997
SPW
3
3
NONE
RTO
acrolein
NICM
lb/
hr
0.13616
0.026373
0.02637
0.13198
0.027
­
2.4
all
inlet
and
outlet
runs
BDL
V1
Dryer
No.
1,2,3
heated
zones
12/
9/
1997
SPW
3
3
NONE
RTO
benzene
NICM
lb/
hr
0.03741
0.010085
0.01008
0.08223
0.024
­
134.4
3
inlet
and
2
outlet
runs
BDL
V1
Dryer
No.
1,2,3
heated
zones
12/
9/
1997
SPW
3
0
NONE
RTO
formaldehyde
NICM
lb/
hr
4.52957
0.47006
0.47006
2.11837
0.231
50.8
V1
Dryer
No.
1,2,3
heated
zones
12/
9/
1997
SPW
3
3
NONE
RTO
m,
p­
xylene
NICM
lb/
hr
0.03741
0.013706
0.01371
0.03861
0.015
­
9.2
all
inlet
and
outlet
runs
BDL
V1
Dryer
No.
1,2,3
heated
zones
12/
9/
1997
SPW
3
0
NONE
RTO
methanol
NICM
lb/
hr
21.7145
2.366071
2.36607
1.17621
0.138
94.2
V1
Dryer
No.
1,2,3
heated
zones
12/
9/
1997
SPW
3
3
NONE
RTO
methyl
ethyl
ketone
(
MEK)
NICM
lb/
hr
0.13339
0.033228
0.03323
0.12936
0.034
­
2.5
all
inlet
and
outlet
runs
BDL
V1
Dryer
No.
1,2,3
heated
zones
12/
9/
1997
SPW
3
3
NONE
RTO
methyl
isobutyl
ketone
NICM
lb/
hr
0.09268
0.032067
0.03207
0.09087
0.033
­
3.6
all
inlet
and
outlet
runs
BDL
V1
Dryer
No.
1,2,3
heated
zones
12/
9/
1997
SPW
3
3
NONE
RTO
o­
xylene
NICM
lb/
hr
0.03741
0.013706
0.01371
0.03861
0.015
­
9.2
all
inlet
and
outlet
runs
BDL
V1
Dryer
No.
1,2,3
heated
zones
12/
9/
1997
SPW
3
2
NONE
RTO
phenol
NICM
lb/
hr
0.27001
0.085685
0.08569
1.05467
0.36
­
319.9
2
inlet
and
1
outlet
run
BDL
V1
Dryer
No.
1,2,3
heated
zones
12/
9/
1997
SPW
3
3
NONE
RTO
propionaldehyde
NICM
lb/
hr
0.14861
0.029823
0.02982
0.14376
0.03
­
2.2
all
inlet
and
outlet
runs
BDL
V1
Dryer
No.
1,2,3
heated
zones
12/
9/
1997
SPW
3
3
NONE
RTO
styrene
NICM
lb/
hr
0.03741
0.013448
0.01345
0.03861
0.015
­
9.2
all
inlet
and
outlet
runs
BDL
V1
Dryer
No.
1,2,3
heated
zones
12/
9/
1997
SPW
3
3
NONE
RTO
toluene
NICM
lb/
hr
0.03741
0.011898
0.0119
0.03861
0.013
­
9.2
all
inlet
and
outlet
runs
BDL
V1
Dryer
No.
1,2,3
heated
zones
12/
9/
1997
SPW
3
0
NONE
RTO
THC
as
carbon
M25A
lb/
hr
5090.2
213.0387
213.039
130.063
5.693
97.3
not
corrected
for
CH4
(
corrected
value
is
98%)
Page
6
of
7
Unit
Test
No.
of
No.
of
Pre­
Test
Inlet1,
Inlet1,
Inlet2,
Inlet2,
Total
inlet,
Outlet,
Outlet,
Cont.
effic.,

code
date
Product
runs
runs
BDL
treatmen
t
APCD
Pollutant
method
Units
ppm
lb/
unit
ppm
lb/
unit
lb/
unit
ppm
lb/
unit
%
Comment
B1
OSB
hot
press,
No.
1
5/
6/
1998
OSB
3
3
NONE
RCO
acetaldehyde
NICM
lb/
hr
0.80617
0.33195
0.33195
0.20453
0.094
71.7
1
inlet
and
3
outlet
runs
BDL
B1
OSB
hot
press,
No.
1
5/
6/
1998
OSB
3
3
NONE
RCO
acrolein
NICM
lb/
hr
0.14746
0.077131
0.07713
0.14342
0.084
­
8.5
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press,
No.
1
5/
6/
1998
OSB
3
3
NONE
RCO
benzene
NICM
lb/
hr
0.04183
0.030486
0.03049
0.03999
0.033
­
6.7
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press,
No.
1
5/
6/
1998
OSB
3
3
NONE
RCO
cumene
NICM
lb/
hr
0.83664
0.938189
0.93819
0.79985
1.001
­
6.7
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press,
No.
1
5/
6/
1998
OSB
3
0
NONE
RCO
formaldehyde
NICM
lb/
hr
3.54315
0.992828
0.99283
2.59282
0.81
18.4
B1
OSB
hot
press,
No.
1
5/
6/
1998
OSB
3
3
NONE
RCO
m,
p­
xylene
NICM
lb/
hr
0.04183
0.041434
0.04143
0.03999
0.044
­
6.7
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press,
No.
1
5/
6/
1998
OSB
3
0
NONE
RCO
methanol
NICM
lb/
hr
13.3222
3.977665
3.97767
3.9016
1.299
67.4
B1
OSB
hot
press,
No.
1
5/
6/
1998
OSB
3
3
NONE
RCO
methyl
ethyl
ketone
NICM
lb/
hr
0.14449
0.097204
0.0972
0.14052
0.105
­
8.5
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press,
No.
1
5/
6/
1998
OSB
3
3
NONE
RCO
methyl
isobutyl
ketone
NICM
lb/
hr
0.10095
0.094343
0.09434
0.09788
0.102
­
8.2
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press,
No.
1
5/
6/
1998
OSB
3
2
NONE
RCO
phenol
NICM
lb/
hr
0.75926
0.666977
0.66698
0.23541
0.23
65.5
2
outlet
runs
BDL
B1
OSB
hot
press,
No.
1
5/
6/
1998
OSB
3
3
NONE
RCO
propionaldehyde
NICM
lb/
hr
0.16078
0.087128
0.08713
0.15646
0.095
­
8.6
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press,
No.
1
5/
6/
1998
OSB
3
3
NONE
RCO
styrene
NICM
lb/
hr
0.04183
0.040653
0.04065
0.03999
0.043
­
6.7
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press,
No.
1
5/
6/
1998
OSB
3
0
NONE
RCO
THC
as
carbon
M25A
lb/
hr
43.5641
4.87725
4.87725
14.679
1.833
62.4
CH4
not
subtracted
(
not
measured)

B1
OSB
hot
press,
No.
1
5/
6/
1998
OSB
3
3
NONE
RCO
toluene
NICM
lb/
hr
0.04183
0.035966
0.03597
0.03999
0.038
­
6.7
all
inlet
and
outlet
runs
BDL
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
0
NONE
RCO
acetaldehyde
NICM
lb/
hr
15.4492
2.305014
2.30501
8.57686
1.653
28.3
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
3
NONE
RCO
acrolein
NICM
lb/
hr
0.92452
0.172285
0.17229
0.14518
0.036
79.4
all
outlet
runs
BDL
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
3
NONE
RCO
benzene
NICM
lb/
hr
0.36511
0.096476
0.09648
0.04194
0.014
85.2
all
outlet
runs
BDL
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
0
NONE
RCO
formaldehyde
NICM
lb/
hr
20.8234
2.114501
2.1145
7.88849
1.035
51.0
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
3
NONE
RCO
m,
p­
xylene
NICM
lb/
hr
0.29721
0.107072
0.10707
0.04194
0.019
81.8
all
outlet
runs
BDL
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
0
NONE
RCO
methanol
NICM
lb/
hr
9.26046
0.982028
0.98203
0.93658
0.131
86.7
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
3
NONE
RCO
methyl
ethyl
ketone
(
MEK)
NICM
lb/
hr
0.29858
0.074157
0.07416
0.14228
0.045
39.6
1
inlet
and
3
outlet
runs
BDL
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
3
NONE
RCO
methyl
isobutyl
ketone
NICM
lb/
hr
0.14057
0.048371
0.04837
0.09972
0.044
9.8
2
inlet
and
3
outlet
runs
BDL
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
3
NONE
RCO
o­
xylene
NICM
lb/
hr
0.04287
0.015418
0.01542
0.04194
0.019
­
26.1
all
inlet
and
outlet
runs
BDL
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
0
NONE
RCO
phenol
NICM
lb/
hr
0.65176
0.20954
0.20954
0.35714
0.147
29.9
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
3
NONE
RCO
propionaldehyde
NICM
lb/
hr
0.30244
0.05876
0.05876
0.15819
0.04
31.7
1
inlet
and
3
outlet
runs
BDL
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
3
NONE
RCO
styrene
NICM
lb/
hr
0.14344
0.050678
0.05068
0.04194
0.019
62.3
3
outlet
runs
BDL
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
3
NONE
RCO
toluene
NICM
lb/
hr
0.49295
0.153765
0.15377
0.04194
0.017
89.0
3
outlet
runs
BDL
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
0
NONE
RCO
THC
as
carbon
M25A
lb/
hr
1831.21
74.82071
74.8207
152.855
8.009
89.3
not
corrected
for
CH4
(
corrected
value
is
92%)
Page
7
of
7
Unit
Test
No.
of
No.
of
Pre­
Test
Inlet1,
Inlet1,
Inlet2,
Inlet2,
Total
inlet,
Outlet,
Outlet,
Cont.
effic.,

code
date
Product
runs
runs
BDL
treatmen
t
APCD
Pollutant
method
Units
ppm
lb/
unit
ppm
lb/
unit
lb/
unit
ppm
lb/
unit
%
Comment
B1
OSB
hot
press
6/
9/
1998
OSB
3
3
NONE
BIO
acetaldehyde
NICM
lb/
hr
0.66465
0.285666
0.28567
0.20392
0.098
65.7
1
inlet
and
3
outlet
runs
BDL
B1
OSB
hot
press
6/
9/
1998
OSB
3
3
NONE
BIO
acrolein
NICM
lb/
hr
0.1491
0.08189
0.08189
0.14304
0.088
­
6.9
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press
6/
9/
1998
OSB
3
3
NONE
BIO
benzene
NICM
lb/
hr
0.04264
0.03263
0.03263
0.03998
0.034
­
4.4
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press
6/
9/
1998
OSB
3
3
NONE
BIO
cumene
NICM
lb/
hr
0.85287
1.004158
1.00416
0.79965
1.049
­
4.4
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press
6/
9/
1998
OSB
3
3
NONE
BIO
formaldehyde
NICM
lb/
hr
2.90441
0.856085
0.85609
0.07461
0.024
97.1
all
outlet
runs
BDL
B1
OSB
hot
press
6/
9/
1998
OSB
3
3
NONE
BIO
m,
p­
xylene
NICM
lb/
hr
0.04264
0.044347
0.04435
0.03998
0.046
­
4.4
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press
6/
9/
1998
OSB
3
0
NONE
BIO
methanol
NICM
lb/
hr
90.2856
28.29377
28.2938
17.532
6.086
78.5
B1
OSB
hot
press
6/
9/
1998
OSB
3
3
NONE
BIO
methyl
ethyl
ketone
NICM
lb/
hr
0.14611
0.103208
0.10321
0.14014
0.11
­
6.9
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press
6/
9/
1998
OSB
3
3
NONE
BIO
methyl
isobutyl
ketone
NICM
lb/
hr
0.10223
0.100312
0.10031
0.09766
0.107
­
6.4
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press
6/
9/
1998
OSB
3
3
NONE
BIO
phenol
NICM
lb/
hr
4.38731
4.04789
4.04789
0.17299
0.178
95.6
all
outlet
runs
BDL
B1
OSB
hot
press
6/
9/
1998
OSB
3
3
NONE
BIO
propionaldehyde
NICM
lb/
hr
0.16252
0.092479
0.09248
0.15603
0.099
­
7.0
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press
6/
9/
1998
OSB
3
3
NONE
BIO
styrene
NICM
lb/
hr
0.04264
0.043512
0.04351
0.03998
0.045
­
4.4
all
inlet
and
outlet
runs
BDL
B1
OSB
hot
press
6/
9/
1998
OSB
3
0
NONE
BIO
THC
as
carbon
M25A
lb/
hr
128.928
15.15461
15.1546
23.0166
3.014
80.1
CH4
not
subtracted
(
not
measured)

B1
OSB
hot
press
6/
9/
1998
OSB
3
3
NONE
BIO
toluene
NICM
lb/
hr
0.04264
0.038495
0.03849
0.03998
0.04
­
4.4
all
inlet
and
outlet
runs
BDL
C1
PB
press
and
cooler
4/
29/
1997
PB
6
4
NONE
BIO
acetaldehyde
NICM
lb/
hr
0.44445
0.303803
0.3038
0.33811
0.267
12.1
2
inlet
and
4
outlet
runs
BDL
C1
PB
press
and
cooler
4/
29/
1997
PB
6
6
NONE
BIO
acrolein
NICM
lb/
hr
0.18108
0.160815
0.16082
0.13842
0.14
12.8
4
inlet
and
all
outlet
runs
BDL
C1
PB
press
and
cooler
4/
29/
1997
PB
6
6
NONE
BIO
benzene
NICM
lb/
hr
0.09785
0.122633
0.12263
0.02539
0.036
70.8
5
inlet
and
all
outlet
runs
BDL
C1
PB
press
and
cooler
4/
29/
1997
PB
3
3
NONE
BIO
cumene
NICM
lb/
hr
0.50783
0.93177
0.93177
0.50783
1.084
­
16.4
all
inlet
and
outlet
runs
BDL
C1
PB
press
and
cooler
4/
29/
1997
PB
6
3
NONE
BIO
formaldehyde
NICM
lb/
hr
13.4303
6.247704
6.2477
0.21742
0.117
98.1
3
outlet
runs
BDL
C1
PB
press
and
cooler
4/
29/
1997
PB
6
6
NONE
BIO
m,
p­
xylene
NICM
lb/
hr
0.02539
0.042088
0.04209
0.02539
0.049
­
15.5
all
inlet
and
outlet
runs
BDL
C1
PB
press
and
cooler
4/
29/
1997
PB
6
5
NONE
BIO
methanol
NICM
lb/
hr
18.8447
9.310108
9.31011
0.31992
0.185
98.0
5
outlet
runs
BDL
C1
PB
press
and
cooler
4/
29/
1997
PB
6
5
NONE
BIO
methyl
ethyl
ketone
NICM
lb/
hr
0.13854
0.157198
0.1572
0.15756
0.205
­
30.3
5
inlet
and
5
outlet
runs
BDL
C1
PB
press
and
cooler
4/
29/
1997
PB
6
5
NONE
BIO
methyl
isobutyl
ketone
NICM
lb/
hr
0.13261
0.211218
0.21122
0.1208
0.218
­
3.1
5
inlet
and
4
outlet
runs
BDL
C1
PB
press
and
cooler
4/
29/
1997
PB
6
6
NONE
BIO
methylene
chloride
NICM
lb/
hr
0.02539
0.033675
0.03367
0.02539
0.039
­
15.5
all
inlet
and
outlet
runs
BDL
C1
PB
press
and
cooler
4/
29/
1997
PB
6
6
NONE
BIO
o­
xylene
NICM
lb/
hr
0.02539
0.042088
0.04209
0.02539
0.049
­
15.5
all
inlet
and
outlet
runs
BDL
C1
PB
press
and
cooler
4/
29/
1997
PB
6
6
NONE
BIO
phenol
NICM
lb/
hr
0.13452
0.19759
0.19759
0.15857
0.269
­
36.3
all
inlet
and
outlet
runs
BDL
C1
PB
press
and
cooler
4/
29/
1997
PB
6
6
NONE
BIO
propionaldehyde
NICM
lb/
hr
0.13169
0.119599
0.1196
0.15267
0.16
­
33.9
all
inlet
and
outlet
runs
BDL
C1
PB
press
and
cooler
4/
29/
1997
PB
6
6
NONE
BIO
styrene
NICM
lb/
hr
0.02539
0.041295
0.04129
0.02539
0.048
­
15.5
all
inlet
and
outlet
runs
BDL
C1
PB
press
and
cooler
4/
29/
1997
PB
3
0
NONE
BIO
THC
as
carbon
M25A
lb/
hr
116.757
21.30187
21.3019
27.4422
5.824
72.7
C1
PB
press
and
cooler
4/
29/
1997
PB
6
6
NONE
BIO
toluene
NICM
lb/
hr
0.02539
0.036533
0.03653
0.02539
0.042
­
15.5
all
inlet
and
outlet
runs
BDL
Note:
Shaded
control
efficiencies
are
not
meaningful
because
either
all
inlet
and
outlet
runs
are
non­
detect,
or
at
least
2
inlet
runs
were
non­
detect.
ATTACHMENT
3b
Culled
HAP
Control
Efficiency
Data
Page
1
of
3
Unit
Test
No.
of
No.
of
Pre­
Test
Inlet1,
Inlet1,
Inlet2,
Inlet2,
Total
inlet,
Outlet,
Outlet,
Cont.
effic.,

code
date
Product
runs
runs
BDL
treatmen
t
APCD
Pollutant
method
Units
ppm
lb/
unit
ppm
lb/
unit
lb/
unit
ppm
lb/
unit
%
Comment
B1
PB
batch
press
10/
23/
1997
PB
3
3
NONE
RTO
formaldehyde
NICM
lb/
hr
43.2413
7.777488
7.77749
0.09376
0.018
99.8
all
outlet
runs
BDL
B1
PB
batch
press
10/
23/
1997
PB
3
3
NONE
RTO
methanol
NICM
lb/
hr
108.6
20.75225
20.7523
0.33786
0.07
99.7
all
outlet
runs
BDL
B1
PB
batch
press
10/
23/
1997
PB
3
3
NONE
RTO
methyl
isobutyl
ketone
NICM
lb/
hr
0.56457
0.338532
0.33853
0.11658
0.076
77.6
all
outlet
runs
BDL
B1
PB
batch
press
10/
23/
1997
PB
3
0
NONE
RTO
THC
as
carbon
M25A
lb/
hr
555.985
39.84825
39.8483
4.9284
0.383
99.0
CH4
not
subtracted
(
not
measured)

R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
WESP
RTO
acetaldehyde
NICM
lb/
hr
1.24594
0.471457
0.47146
0.18018
0.069
85.3
all
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
2
WESP
RTO
formaldehyde
NICM
lb/
hr
1.06017
0.275196
0.2752
0.10622
0.028
89.8
2
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
1
WESP
RTO
m,
p­
xylene
NICM
lb/
hr
0.06568
0.059258
0.05926
0.03914
0.037
38.0
1
inlet
and
1
outlet
run
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
2
WESP
RTO
methanol
NICM
lb/
hr
4.47411
1.235988
1.23599
0.35166
0.099
92.0
2
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
0
WESP
RTO
THC
as
carbon
M25A
lb/
hr
488.493
50.41784
50.4178
6.43446
0.673
98.7
CH4
subtracted
from
inlet
&
outlet
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
1
WESP
RTO
toluene
NICM
lb/
hr
0.08247
0.064641
0.06464
0.03914
0.032
50.7
1
inlet
and
1
outlet
run
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
3
NONE
WESP/
RTO
acetaldehyde
NICM
lb/
hr
1.20706
0.36108
0.36108
0.18018
0.069
80.8
3
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
2
NONE
WESP/
RTO
formaldehyde
NICM
lb/
hr
0.99953
0.202858
0.20286
0.10622
0.028
86.2
2
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
2
NONE
WESP/
RTO
methanol
NICM
lb/
hr
3.97445
0.859329
0.85933
0.35166
0.099
88.5
2
outlet
runs
BDL
R1
PB
rotary
pre­
dryer
6/
3/
1998
PB
3
0
NONE
WESP/
RTO
THC
as
carbon
M25A
lb/
hr
488.493
50.41784
50.4178
6.43446
0.673
98.7
CH4
subtracted
from
inlet
&
outlet
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
3
NONE
RTO
acetaldehyde
NICM
lb/
hr
11.7403
2.61133
2.61133
0.20281
0.051
98.0
all
outlet
runs
BDL
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
3
NONE
RTO
acrolein
NICM
lb/
hr
3.3895
0.95692
0.95692
0.14201
0.046
95.2
all
outlet
runs
BDL
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
2
NONE
RTO
formaldehyde
NICM
lb/
hr
4.39499
0.661082
0.66108
0.11196
0.019
97.1
2
outlet
runs
BDL
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
3
NONE
RTO
methanol
NICM
lb/
hr
9.34398
1.520261
1.52026
0.26445
0.049
96.8
all
outlet
runs
BDL
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
3
NONE
RTO
propionaldehyde
NICM
lb/
hr
11.7729
3.431402
3.4314
0.15499
0.052
98.5
all
outlet
runs
BDL
F1
FB
dryer
and
HB
press
preheater
10/
30/
1997
FB
3
0
NONE
RTO
THC
as
carbon
M25A
lb/
hr
352.185
21.41545
21.4155
4.67233
0.32
98.5
CH4
not
subtracted
(
not
measured)

B1
OSB
hot
press,
No.
2
5/
5/
1998
OSB
3
3
NONE
RTO
acetaldehyde
NICM
lb/
hr
0.43672
0.184293
0.18429
0.2078
0.098
46.7
1
inlet
and
3
outlet
runs
BDL
B1
OSB
hot
press,
No.
2
5/
5/
1998
OSB
3
0
NONE
RTO
formaldehyde
NICM
lb/
hr
5.62712
1.62473
1.62473
0.54175
0.175
89.2
B1
OSB
hot
press,
No.
2
5/
5/
1998
OSB
3
1
NONE
RTO
methanol
NICM
lb/
hr
17.7308
5.441179
5.44118
0.83214
0.285
94.8
1
outlet
run
BDL
B1
OSB
hot
press,
No.
2
5/
5/
1998
OSB
3
2
NONE
RTO
phenol
NICM
lb/
hr
0.89745
0.810979
0.81098
0.3779
0.383
52.7
2
outlet
runs
BDL
B1
OSB
hot
press,
No.
2
5/
5/
1998
OSB
3
0
NONE
RTO
THC
as
carbon
M25A
lb/
hr
51.3821
5.913199
5.9132
3.306
0.426
92.8
CH4
not
subtracted
(
not
measured)

R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
0
WESP
RTO
acetaldehyde
NICM
lb/
hr
33.5545
12.18942
12.1894
5.18795
2.211
81.9
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
0
WESP
RTO
acrolein
NICM
lb/
hr
8.47441
3.90733
3.90733
1.13352
0.614
84.3
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
0
WESP
RTO
benzene
NICM
lb/
hr
0.58265
0.376021
0.37602
0.23681
0.179
52.4
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
0
WESP
RTO
formaldehyde
NICM
lb/
hr
45.2337
11.22791
11.2279
13.1172
3.815
66.0
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
0
WESP
RTO
methanol
NICM
lb/
hr
24.0545
6.372851
6.37285
4.57033
1.416
77.8
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
3
WESP
RTO
methyl
ethyl
ketone
NICM
lb/
hr
0.23546
0.139938
0.13994
0.13925
0.097
30.5
1
inlet
and
3
outlet
runs
BDL
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
0
WESP
RTO
phenol
NICM
lb/
hr
0.68283
0.534002
0.534
0.40188
0.366
31.5
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
1
WESP
RTO
propionaldehyde
NICM
lb/
hr
1.41241
0.676412
0.67641
0.26402
0.148
78.1
1
outlet
run
BDL
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
3
WESP
RTO
styrene
NICM
lb/
hr
0.07777
0.066835
0.06683
0.03882
0.039
41.4
1
inlet
and
3
outlet
runs
BDL
R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
0
WESP
RTO
THC
as
carbon
M25A
lb/
hr
390.034
38.56629
38.5663
57.191
6.628
82.8
CH4
not
subtracted
(
not
measured)

R1
OSB
rotary
dryers
(
2)
5/
7/
1998
OSB
3
3
WESP
RTO
toluene
NICM
lb/
hr
0.33005
0.25076
0.25076
0.03882
0.035
86.2
3
outlet
runs
BDL
B1
OSB
hot
press
1/
18/
1998
OSB
3
3
NONE
RTO
acetaldehyde
NICM
lb/
hr
0.69324
0.64712
0.64712
0.19776
0.166
74.3
nat.
gas
injection
mode;
1
inlet
and
3
outlet
runs
BD
B1
OSB
hot
press
1/
18/
1998
OSB
3
2
NONE
RTO
formaldehyde
NICM
lb/
hr
3.44725
2.168481
2.16848
0.18984
0.11
94.9
nat.
gas
injection
mode;
2
outlet
runs
BDL
B1
OSB
hot
press
1/
18/
1998
OSB
3
3
NONE
RTO
methanol
NICM
lb/
hr
25.4525
17.03734
17.0373
0.25763
0.157
99.1
nat.
gas
injection
mode;
3
outlet
runs
BDL
B1
OSB
hot
press
1/
18/
1998
OSB
3
2
NONE
RTO
phenol
NICM
lb/
hr
0.50408
0.993354
0.99335
0.22458
0.404
59.3
nat
gas
injection
mode;
2
outlet
runs
BDL
B1
OSB
hot
press
1/
18/
1998
OSB
3
3
NONE
RTO
THC
as
carbon
M25A
lb/
hr
255.324
64.32727
64.3273
0.5
0.115
99.8
nat.
gas
injection
mode;
all
outlet
runs
BDL;
CH4
no
subtracted
(
not
measured)
Page
2
of
3
Unit
Test
No.
of
No.
of
Pre­
Test
Inlet1,
Inlet1,
Inlet2,
Inlet2,
Total
inlet,
Outlet,
Outlet,
Cont.
effic.,

code
date
Product
runs
runs
BDL
treatment
APCD
Pollutant
method
Units
ppm
lb/
unit
ppm
lb/
unit
lb/
unit
ppm
lb/
unit
%
Comment
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
acetaldehyde
NICM
lb/
hr
4.63534
4.093543
4.09354
0.19402
0.239
94.2
nat.
gas
injection
mode;
all
outlet
runs
BDL
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
acrolein
NICM
lb/
hr
2.53329
2.845826
2.84583
0.13626
0.214
92.5
nat.
gas
injection
mode;
all
outlet
runs
BDL
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
benzene
NICM
lb/
hr
0.15845
0.247967
0.24797
0.03848
0.084
66.0
nat.
gas
injection
mode;
all
outlet
runs
BDL
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
4
WESP
RTO
formaldehyde
NICM
lb/
hr
19.0781
11.49902
11.499
0.13634
0.114
99.0
nat.
gas
injection
mode;
4
outlet
runs
BDL
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
m,
p­
xylene
NICM
lb/
hr
0.15135
0.321979
0.32198
0.03848
0.114
64.4
nat.
gas
injection
mode;
all
outlet
runs
BDL
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
methanol
NICM
lb/
hr
6.85387
4.399032
4.39903
0.25259
0.226
94.9
nat.
gas
injection
mode;
all
outlet
runs
BDL
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
methyl
ethyl
ketone
NICM
lb/
hr
0.25732
0.371997
0.372
0.13351
0.27
27.5
nat.
gas
injection
mode;
1
inlet
and
all
outlet
runs
BD
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
methyl
isobutyl
ketone
NICM
lb/
hr
0.24273
0.487206
0.48721
0.09321
0.262
46.3
nat.
gas
injection
mode;
all
outlet
runs
BDL
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
propionaldehyde
NICM
lb/
hr
0.32756
0.381538
0.38154
0.14858
0.242
36.6
nat.
gas
injection
mode;
1
inlet
and
all
outlet
runs
BD
R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
0
WESP
RTO
THC
as
carbon
M25A
lb/
hr
1190
286.0403
286.04
43.8125
14.74
94.8
nat.
gas
injection
mode;
CH4
subtracted
from
inlet
&

R2
OSB
rotary
dryers
(
5)
1/
15/
1998
OSB
6
6
WESP
RTO
toluene
NICM
lb/
hr
0.31279
0.57752
0.57752
0.03848
0.099
82.8
nat.
gas
injection
mode;
all
outlet
runs
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
3
NONE
RTO
acetaldehyde
NICM
lb/
hr
31.7964
2.57904
2.57904
0.2011
0.022
99.2
all
outlet
runs
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
3
NONE
RTO
acrolein
NICM
lb/
hr
7.78131
0.803204
0.8032
0.14073
0.019
97.6
all
outlet
runs
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
3
NONE
RTO
formaldehyde
NICM
lb/
hr
2.62
0.145166
0.14517
0.06714
0.005
96.6
all
outlet
runs
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
2
NONE
RTO
methanol
NICM
lb/
hr
8.45039
0.497676
0.49768
0.38103
0.03
94.0
2
outlet
runs
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
3
NONE
RTO
methyl
isobutyl
ketone
NICM
lb/
hr
0.84149
0.155454
0.15545
0.09574
0.024
84.8
all
outlet
runs
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
1
NONE
RTO
phenol
NICM
lb/
hr
0.36623
0.06332
0.06332
0.28817
0.067
­
5.8
1
outlet
run
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
3
NONE
RTO
propionaldehyde
NICM
lb/
hr
31.5247
3.372796
3.3728
0.15361
0.022
99.3
all
outlet
runs
BDL
T1
HB
tempering
oven
6/
26/
1998
HB
3
3
NONE
RTO
THC
as
carbon
M25A
lb/
hr
763.837
16.87325
16.8733
0.5
0.015
99.9
all
outlet
runs
BDL;
CH4
subtracted
from
inlet
but
no
(
all
outlet
THC
=
CH4)

M1
Dryer/
continuous
press
1/
13/
1998
MDF
3
3
RBP
RTO
acetaldehyde
NICM
lb/
hr
0.62819
0.369673
0.19796
0.04315
0.41282
0.20345
0.164
60.3
all
press
and
outlet
runs
BDL
M1
Dryer/
continuous
press
1/
13/
1998
MDF
3
2
RBP
RTO
formaldehyde
NICM
lb/
hr
16.2976
6.553666
7.692813
1.14699
7.70065
0.18413
0.101
98.7
2
outlet
runs
BDL
M1
Dryer/
continuous
press
1/
13/
1998
MDF
3
3
RBP
RTO
methanol
NICM
lb/
hr
28.6029
12.25112
8.896868
1.40955
13.6607
0.26527
0.155
98.9
all
outlet
runs
BDL
M1
Dryer/
continuous
press
1/
13/
1998
MDF
2
0
RBP
RTO
THC
as
carbon
M25A
lb/
hr
201.149
32.22919
20.33499
1.2081
33.4373
9.58696
2.085
93.8
CH4
not
subtracted
(
not
measured)

B1
OSB
hot
press
4/
3/
1998
OSB
3
3
NONE
RTO
formaldehyde
NICM
lb/
hr
2.42042
0.892949
0.89295
0.07391
0.037
95.9
all
outlet
runs
BDL;
nat.
gas
injection
mode
B1
OSB
hot
press
4/
3/
1998
OSB
3
3
NONE
RTO
methanol
NICM
lb/
hr
19.6742
7.913139
7.91314
0.27345
0.144
98.2
all
outlet
runs
BDL;
nat.
gas
injection
mode
B1
OSB
hot
press
4/
3/
1998
OSB
3
0
NONE
RTO
THC
as
carbon
M25A
lb/
hr
218.748
32.65834
32.6583
4.36404
0.864
97.4
CH4
not
subtracted
(
not
measured);
nat.
gas
injectio
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
0
NONE
RTO
acetaldehyde
NICM
lb/
hr
6.49437
5.302698
5.3027
0.7489
0.628
88.2
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
6
NONE
RTO
acrolein
NICM
lb/
hr
3.24896
3.376787
3.37679
0.18193
0.195
94.2
all
outlet
runs
BDL;
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
6
NONE
RTO
benzene
NICM
lb/
hr
0.27958
0.404575
0.40457
0.05044
0.075
81.4
all
outlet
runs
BDL;
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
1
NONE
RTO
formaldehyde
NICM
lb/
hr
22.9191
12.75396
12.754
2.12947
1.268
90.1
1
outlet
run
BDL;
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
6
NONE
RTO
m,
p­
xylene
NICM
lb/
hr
0.20745
0.408414
0.40841
0.05044
0.102
74.9
all
outlet
runs
BDL;
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
2
NONE
RTO
methanol
NICM
lb/
hr
8.5945
5.094153
5.09415
0.71303
0.434
91.5
2
outlet
runs
BDL;
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
6
NONE
RTO
propionaldehyde
NICM
lb/
hr
0.51269
0.552495
0.5525
0.19851
0.22
60.1
1
inlet
and
all
outlet
runs
BDL;
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
4
0
NONE
RTO
THC
as
carbon
M25A
lb/
hr
766.275
169.8813
169.881
29.3996
6.933
95.9
CH4
not
subtracted
(
not
measured);
burner
mode
R2
OSB
rotary
dryer
(
5)
4/
1/
1998
OSB
6
6
NONE
RTO
toluene
NICM
lb/
hr
0.41571
0.710179
0.71018
0.05044
0.089
87.5
all
outlet
runs
BDL;
burner
mode
V1
Dryer
1,2,3,4
heated
zones
11/
17/
1997
SPW
3
2
NONE
RTO
acetaldehyde
NICM
lb/
hr
1.22305
0.376651
0.37665
0.26785
0.09
76.0
2
outlet
runs
BDL
V1
Dryer
1,2,3,4
heated
zones
11/
17/
1997
SPW
3
2
NONE
RTO
formaldehyde
NICM
lb/
hr
4.38435
0.910997
0.911
0.12438
0.029
96.8
2
outlet
runs
BDL
V1
Dryer
1,2,3,4
heated
zones
11/
17/
1997
SPW
3
2
NONE
RTO
methanol
NICM
lb/
hr
5.50852
1.233799
1.2338
0.40357
0.101
91.8
2
outlet
runs
BDL
V1
Dryer
1,2,3,4
heated
zones
11/
17/
1997
SPW
3
0
NONE
RTO
THC
as
carbon
M25A
lb/
hr
1814.16
151.151
151.151
87.112
8.1
94.6
CH4
subtracted
from
inlet
and
outlet
V1
Dryer
No.
1,2,3
heated
zones
12/
9/
1997
SPW
3
0
NONE
RTO
acetaldehyde
NICM
lb/
hr
5.78019
0.868799
0.8688
0.6621
0.107
87.7
V1
Dryer
No.
1,2,3
heated
zones
12/
9/
1997
SPW
3
0
NONE
RTO
formaldehyde
NICM
lb/
hr
4.52957
0.47006
0.47006
2.11837
0.231
50.8
V1
Dryer
No.
1,2,3
heated
zones
12/
9/
1997
SPW
3
0
NONE
RTO
methanol
NICM
lb/
hr
21.7145
2.366071
2.36607
1.17621
0.138
94.2
V1
Dryer
No.
1,2,3
heated
zones
12/
9/
1997
SPW
3
0
NONE
RTO
THC
as
carbon
M25A
lb/
hr
5090.2
213.0387
213.039
130.063
5.693
97.3
not
corrected
for
CH4
(
corrected
value
is
98%)
Page
3
of
3
Unit
Test
No.
of
No.
of
Pre­
Test
Inlet1,
Inlet1,
Inlet2,
Inlet2,
Total
inlet,
Outlet,
Outlet,
Cont.
effic.,

code
date
Product
runs
runs
BDL
treatmen
t
APCD
Pollutant
method
Units
ppm
lb/
unit
ppm
lb/
unit
lb/
unit
ppm
lb/
unit
%
Comment
B1
OSB
hot
press,
No.
1
5/
6/
1998
OSB
3
3
NONE
RCO
acetaldehyde
NICM
lb/
hr
0.80617
0.33195
0.33195
0.20453
0.094
71.7
1
inlet
and
3
outlet
runs
BDL
B1
OSB
hot
press,
No.
1
5/
6/
1998
OSB
3
0
NONE
RCO
formaldehyde
NICM
lb/
hr
3.54315
0.992828
0.99283
2.59282
0.81
18.4
B1
OSB
hot
press,
No.
1
5/
6/
1998
OSB
3
0
NONE
RCO
methanol
NICM
lb/
hr
13.3222
3.977665
3.97767
3.9016
1.299
67.4
B1
OSB
hot
press,
No.
1
5/
6/
1998
OSB
3
2
NONE
RCO
phenol
NICM
lb/
hr
0.75926
0.666977
0.66698
0.23541
0.23
65.5
2
outlet
runs
BDL
B1
OSB
hot
press,
No.
1
5/
6/
1998
OSB
3
0
NONE
RCO
THC
as
carbon
M25A
lb/
hr
43.5641
4.87725
4.87725
14.679
1.833
62.4
CH4
not
subtracted
(
not
measured)

V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
0
NONE
RCO
acetaldehyde
NICM
lb/
hr
15.4492
2.305014
2.30501
8.57686
1.653
28.3
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
3
NONE
RCO
acrolein
NICM
lb/
hr
0.92452
0.172285
0.17229
0.14518
0.036
79.4
all
outlet
runs
BDL
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
3
NONE
RCO
benzene
NICM
lb/
hr
0.36511
0.096476
0.09648
0.04194
0.014
85.2
all
outlet
runs
BDL
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
0
NONE
RCO
formaldehyde
NICM
lb/
hr
20.8234
2.114501
2.1145
7.88849
1.035
51.0
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
3
NONE
RCO
m,
p­
xylene
NICM
lb/
hr
0.29721
0.107072
0.10707
0.04194
0.019
81.8
all
outlet
runs
BDL
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
0
NONE
RCO
methanol
NICM
lb/
hr
9.26046
0.982028
0.98203
0.93658
0.131
86.7
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
3
NONE
RCO
methyl
ethyl
ketone
(
MEK)
NICM
lb/
hr
0.29858
0.074157
0.07416
0.14228
0.045
39.6
1
inlet
and
3
outlet
runs
BDL
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
0
NONE
RCO
phenol
NICM
lb/
hr
0.65176
0.20954
0.20954
0.35714
0.147
29.9
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
3
NONE
RCO
propionaldehyde
NICM
lb/
hr
0.30244
0.05876
0.05876
0.15819
0.04
31.7
1
inlet
and
3
outlet
runs
BDL
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
3
NONE
RCO
styrene
NICM
lb/
hr
0.14344
0.050678
0.05068
0.04194
0.019
62.3
3
outlet
runs
BDL
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
3
NONE
RCO
toluene
NICM
lb/
hr
0.49295
0.153765
0.15377
0.04194
0.017
89.0
3
outlet
runs
BDL
V1
Dryer
No.
1
and
2
heated
zones
7/
15/
1998
SPW
3
0
NONE
RCO
THC
as
carbon
M25A
lb/
hr
1831.21
74.82071
74.8207
152.855
8.009
89.3
not
corrected
for
CH4
(
corrected
value
is
92%)

B1
OSB
hot
press
6/
9/
1998
OSB
3
3
NONE
BIO
acetaldehyde
NICM
lb/
hr
0.66465
0.285666
0.28567
0.20392
0.098
65.7
1
inlet
and
3
outlet
runs
BDL
B1
OSB
hot
press
6/
9/
1998
OSB
3
3
NONE
BIO
formaldehyde
NICM
lb/
hr
2.90441
0.856085
0.85609
0.07461
0.024
97.1
all
outlet
runs
BDL
B1
OSB
hot
press
6/
9/
1998
OSB
3
0
NONE
BIO
methanol
NICM
lb/
hr
90.2856
28.29377
28.2938
17.532
6.086
78.5
B1
OSB
hot
press
6/
9/
1998
OSB
3
3
NONE
BIO
phenol
NICM
lb/
hr
4.38731
4.04789
4.04789
0.17299
0.178
95.6
all
outlet
runs
BDL
B1
OSB
hot
press
6/
9/
1998
OSB
3
0
NONE
BIO
THC
as
carbon
M25A
lb/
hr
128.928
15.15461
15.1546
23.0166
3.014
80.1
CH4
not
subtracted
(
not
measured)

C1
PB
press
and
cooler
4/
29/
1997
PB
6
3
NONE
BIO
formaldehyde
NICM
lb/
hr
13.4303
6.247704
6.2477
0.21742
0.117
98.1
3
outlet
runs
BDL
C1
PB
press
and
cooler
4/
29/
1997
PB
6
5
NONE
BIO
methanol
NICM
lb/
hr
18.8447
9.310108
9.31011
0.31992
0.185
98.0
5
outlet
runs
BDL
C1
PB
press
and
cooler
4/
29/
1997
PB
3
0
NONE
BIO
THC
as
carbon
M25A
lb/
hr
116.757
21.30187
21.3019
27.4422
5.824
72.7
ATTACHMENT
4
Physical
Properties
of
Organic
HAP
Physical
Properties
of
Organic
HAP
Organic
HAP
Melting
Point,
°
C
(
°
F)
Boiling
Point,

°
C
(
°
F)
Autoignition
(
A)

or
Ignition
(
I)

Temp,
°
C
(
°
F)
a
Lower
Flammable/

Explosive
Limit,

%
b
Upper
Flammable/

Explosive
Limit,

%
b
Acetaldehyde
­
123.6
(­
190.5)
20.5
(
68.9)
185
(
365)
(
A)
4
(
E)
57
(
v/
v)
­
66
(
E)

Acetophenone
20.5
(
68.9)
202.3
(
396.1)
571
(
1060)
(
A)

Acrolein
­
87.9
(­
126.2)
52.5
(
126.5)
234
(
453)
(
A)
2.8
(
v/
v,
E)
31
(
v/
v,
E)

Benzene
5.5
(
41.9)
80.1
(
176.2)
530
(
986)
(
A)
1.2
(
v/
v,
E)
8.0
(
v/
v,
E)

Biphenyl
70
(
158)
254.7
(
490.5)
540
(
1004)
(
A)
0.6
(
v/
v,
E,
at
111

C)
5.8
(
v/
v,
E,
at
166

C)

Bis­(
2­
ethylhexyl)
phthalate
­
50
(­
58)
385
(
545)
350
(
662)
(
A)

Carbon
disulfide
­
110.2
(­
166.4)
46.3
(
115.3)
100
(
212)
(
I)

90
(
194)
(
A)
1.1
(
v/
v,
E)
50
(
v/
v,
E)

Carbon
tetrachloride
­
22.8
(­
9.0)
76.8
(
170.2)
Nonflammable
Chloroform
­
63.6
(
82.5)
61.2
(
142.2)
Nonflammable
m­
Cresol
11.2
(
52.2)
202.4
(
396.32)
626
(
1159)
(
A)
1.1
(
v/
v,
E)
?
(
v/
v,
E)

o­
Cresol
30.4
(
86.7)
191.2
(
376.16)
599
(
1110)
(
A)
1.4
(
v/
v,
E)
?
(
v/
v,
E)

p­
Cresol
35.5
(
95.9)
201.9
(
395.4)
559
(
1038)
(
A)
1.1
(
v/
v,
E,
at
150

C
?
(
v/
v,
E)

Cumene
­
96.9
(­
142.4)
152.5
(
306.5)
420
(
788)
(
A)
0.9
(
v/
v,
E)
6.5
(
v/
v,
E)

Dibutylphthalate
(
di­
n­
butyl
phthalate)
­
35
(­
31)
340
(
644)
402
(
756)
0.5
(
v/
v,
E,
at
235

C)
~
2.5
(
v/
v,
E)

Ethyl
benzene
­
94.7
(­
138.5)
136.2
(
277.2)
432
(
810)
1.0
(
v/
v,
E)
6.7
(
v/
v,
E)
Organic
HAP
Melting
Point,
°
C
(
°
F)
Boiling
Point,

°
C
(
°
F)
Autoignition
(
A)

or
Ignition
(
I)

Temp,
°
C
(
°
F)
a
Lower
Flammable/

Explosive
Limit,

%
b
Upper
Flammable/

Explosive
Limit,

%
b
Ethyl
chloride
(
Chloroethane)
­
138.7
(­
217.7)
12.8
(
55.0)
519
(
966)
(
A)
3.6
(
v/
v,
E)
14.8
(
v/
v,
E)

Formaldehyde
­
92
(­
134)
­
20
(­
4)
430
(
806)
(
A)
7
(
v/
v,
E)
73
(
v/
v,
E)

n­
Hexane
­
95.6
(­
140.1)
68.9
(
156.0)
225
(
437)
(
A)
1.1
(
v/
v,
E)
7.5
(
v/
v,
E)

Hydroquinone
170.4
(
338.7)
285.5
(
545.9)
515
(
959)
(
A)

Methanol
­
97.9
(­
144.2)
64.7
(
148.5)
470
(
878)
(
I)

(
725­
867)
(
A)
5.5
­
6.0
(
v/
v,
E)
36.5
­
44
(
v/
v,
E)

Methyl
bromide
(
Bromomethane)
­
93.3
(­
135.9)
4.0
(
39)
537
(
999)
(
A)
10
(
v/
v,
E)
16
(
v/
v,
E)

Methyl
chloride
(
Chloromethane)
­
97.5
(­
143.5)
­
23.9
(­
11.0)
632
(
1170)
(
A)
8.1
(
v/
v,
E)
17.3
(
v/
v,
E)

Methyl
ethyl
ketone
­
86.3
(­
123.3)
78.9
(
174.0)
510
(
950)
(
A)
1.9
(
v/
v,
E)
11.3
(
v/
v,
E)

Methyl
isobutyl
ketone
(
MIBK)

(
4­
methyl­
2­
pentanone)
­
84.7
(­
120.5)
117.5
(
243.5)
460
(
860)
(
A)
1.4
(
v/
v,
E)
7.5
(
v/
v,
E)

Methylene
chloride
­
95.9
(­
140.6)
40.1
(
104.2)
556
(
1033)
(
A)
12
(
v/
v,
E)
25
(
v/
v,
E)

Methylene
diphenyl
diisocyanate
(
MDI)
(
Methylene
bisphenyl
isocyanate)
37
(
99)
314
(
597)

(
at
100
kPa)
240
(
464)
(
A)

Phenol
41.5
(
106.7)
182
(
360)
715
(
1319)
1.36
(
v/
v,
E)
10
(
v/
v,
E)

Propionaldehyde
­
81
(­
114)
49.3
(
120.7)
207
(
405)
(
A)
2.6
(
v/
v,
E)
17.0
(
v/
v,
E)

Styrene
­
30.8
(­
23.4)
145.5
(
293.9)
490
(
914)
(
A)
0.9
(
v/
v,
E)
6.8
(
v/
v,
E)

Toluene
­
95
(­
139)
110.7
(
231.3)
480
(
896)
(
A)
1.3
(
v/
v,
E)
6.9
(
v/
v,
E)

1,1,1­
Trichloroethane
­
301.3
(­
510.3)
74.1
(
165.4)
537
(
999)
(
A)
8
(
v/
v,
E)
16
(
v/
v,
E)
Organic
HAP
Melting
Point,
°
C
(
°
F)
Boiling
Point,

°
C
(
°
F)
Autoignition
(
A)

or
Ignition
(
I)

Temp,
°
C
(
°
F)
a
Lower
Flammable/

Explosive
Limit,

%
b
Upper
Flammable/

Explosive
Limit,

%
b
m­
Xylene
­
47.6
(­
53.7)
139.2
(
282.6)
527
(
981)
(
A)
1.1
(
v/
v,
E)
7.0
(
v/
v,
E)

o­
Xylene
­
25.1
(­
13.2)
144.2
(
291.6)
463
(
865)
(
A)
0.9
(
v/
v,
E)
6.7
(
v/
v,
E)

p­
Xylene
13.3
(
55.9)
138.1
(
280.6)
528
(
982)
(
A)
1.1
(
v/
v,
E)
7.0
(
v/
v,
E)

a
The
autoignition
temperature
is
the
lower
limit
of
the
ignition
temperature
and
is
a
constant,
regardless
of
conditions.
The
ignition
temperature
varies
depending
on
fuel­
to­
air
ratio,
total
pressure
inside
the
reactor
(
or
APCD),
reactor
(
or
APCD)
geometry,
etc.

b
The
upper
flammability
limit
(
UFL)
and
the
lower
flammability
limit
(
LFL)
are
the
concentrations
of
a
pure
substance
in
air
for
which
the
mixture
is
capable
of
ignition.
If
the
concentration
of
a
compound
in
air
is
above
the
UFL
or
below
the
LFL,
the
mixture
will
not
ignite,
even
if
exposed
to
a
spark
or
flame.

References:

Melting
and
Boiling
points
Budavari,
S.,
ed.
The
Merck
Index.
Eleventh
Edition.
Rahway,
New
Jersey:
Merck
&
Co.,
Inc,
1989.

Felder,
R.
M.
and
R.
W.
Rousseau.
Elementary
Principles
of
Chemical
Processes.
Third
Edition.
New
York:
John
Wiley
&
Sons,
Inc.,
2000.

Perry,
R.
H.,
ed.
Perry's
Chemical
Engineers'
Handbook.
Sixth
Edition.
New
York:
McGraw­
Hill
Book
Company,
1984.

Autoignition
temperatures,
Flammability
limits
Budavari,
S.,
ed.
The
Merck
Index.
Eleventh
Edition.
Rahway,
New
Jersey:
Merck
&
Co.,
Inc,
1989.

Howard
Hughes
Medical
Institute
Laboratory
Chemical
Safety
Summaries.
Reprinted
with
permission
from
Prudent
Practices
in
the
Laboratory:
Handling
and
Disposal
of
Chemicals.
Copyright
1995
by
the
National
Academy
of
Sciences.
Courtesy
of
the
National
Academy
Press,
Washington,
D.
C.

http://
www.
hhmi.
org/
research/
labsafe/
lcss/

International
Programme
on
Chemical
Safety
(
IPCS)
International
Chemical
Safety
Cards
(
ICSCs).

http://
www.
inchem.
org/
pages/
icsc.
html