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1 Kline is associate professor , Department of Wood Science and Forest Products, Virginia Technical and State University, Blacksburg, VA 24061-0503
EXECUTIVE SUMMARY
TABLE OF CONTENTS
LIST OF FIGURESFigure 1.1. Description of the OSB manufacturing processes.
LIST OF TABLES
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| Input Materials |
Co-products Produced
|
Products
|
| Logs PF resin MDI resin Wax |
Bark
Sawdust, dry Panel trimmings Rejected boards |
OSB
|
Delivery of the input materials was by truck, with an average one-way
delivery distance of 89 miles. Delivery distances for PF and MDI
resin and for wax were not determined in this study.
The survey data provided wood input data in either cords or green
weight. Data given in cords was converted to cubic feet (ft3)
of wood by multiplying by 75 ft3/cord (Toennisson and
Hadden, 1993). A final conversion was then made from ft3
to mass (lb) by multiplying by the average weighted densities as
determined by their percentage use as given by the survey, and the
densities for hardwood or softwood species as provided by Toennisson
and Hadden (1993). The average wood density used was 30.9 lb/ft3
oven-dry for the mix of softwood and hardwood logs (see Table 1.2).
Conversion of green log weight to dry wood weight was carried out
using the moisture content assumptions specified in the previous
section.
Table 1.2 Average Density of Wood Species Used to Calculate Mass of Wood from Logs.
| Wood Species |
PercentageUse
in Survey |
Density1
|
|
%
|
lb/ft3
|
|
| Softwood Hardwood Average |
73
27 100 |
29.0
36.0 30.9 |
1 Wood density values are from Toennisson and Hadden (1993).
The input to produce 1.0 thousand square feet (Msf) of OSB 3/8-inch basis includes 49.8 cubic feet (ft3) or 1,540 lb of logs (based on volume and wood densities given in Table 1.2), 42.4 lbs of PF resin, 8.16 lbs MDI resin, and 19.3 lbs of wax . Table 2.1 summarizes all inputs required to produce 1.0 Msf of OSB including electricity and fuel inputs.
Table 2.1 Inputs to Produce
1.0 Msf 3/8-inch Basis of OSB in the Southeast.
| INPUTS | ||
Materials1 |
Units
|
per/MSF
3/8-in basis |
| Round wood 2 |
ft3
|
49.8
|
| Wood Bark Phenol Formaldehyde MDI Resin Wax |
lb
lb lb lb lb |
1540
166 42.4 8.16 19.3 |
Electricity Use |
||
| Electricity |
kWh
|
183
|
Fuel Use |
||
| Wood fuel (produced)3 Natural gas Liquid Propane gas Diesel Fuel Oil |
lb
ft3 gal gal gal |
387
698 1.06 0.018 0.769 |
1 All
materials unless noted, are given as weight oven-dry or as solids
content.
2 Includes volume of only wood (bark excluded)
3 This material includes bark, screening fines, and OSB
trimmings
A complete wood mass balance for woody raw materials used in OSB
production is given in Table 2.2. The difference between the total
wood input and output was 43 lb., and it is this quantity that is
referred to as"unaccounted for wood". The unaccounted
for wood is 2.4% of the total wood input. Only one plant was able
to report the exact amount of bark generated separate from other
wood residues. Based on this report, the percentage of bark generated
on an oven dry weight basis was 10.8 % of the roundwood input at
the plant. This percentage was used to estimate the bark input of
in the mass balance. Most likely the unaccounted for wood of 43
lb. is due to inaccurate/incomplete reporting of bark from the debarking
process or from the wood per cord conversion factor used.
Table 2.2 Wood Mass Balance
for OSB Production from the Southeast Region per 1.0 Msf 3/8-inch
Basis
|
Inputs
|
lb/Msf 3/8-in basis
|
| Round wood (logs) |
17061
|
|
Outputs
|
lb/Msf 3/8-in basis
|
| OSB (wood only) |
12102
|
| Wood waste (to heat) |
387
|
| Bark Sold |
123
|
| Sawdust Sold |
29
|
| Total
Output |
1749
|
| Unaccounted wood |
433
|
1 Includes
weight of both bark and solid wood from Table 2.1.
2 OSB (wood only) based on estimated weight of OSB, 1260
lb, minus weight of resin and wax (50 pounds or 4% by weight basis).
32.4% unaccounted for wood
Energy for the production of OSB comes from electricity, diesel,
liquid propane gas (LPG), natural gas, and wood fuel from bark,
fines and other wood residue. The electricity is used to operate
all the systems described in Section 1.3. Diesel fuel use is assumed
to be by log loaders in the "log handling" process. Forklift
trucks used small amounts of LPG primarily in the "finishing"
process.
The source of fuel used to generate the electricity used in the manufacturing process is very important in determining the type and amount of impact in the LCI analysis. The breakdown of electricity use in the Southeast by fuel source is given in Table 3.1. The source of this data is the U.S. Department of Energy (DOE). In 1998, the dominant form of fuel in the region was coal, representing 49.2% of the total, followed by nuclear at 25.6%, natural gas at 9.6%, petroleum at 3.7% and hydro at 3.4%. In the SimaPro 5 analysis using the FAL database, combusting of coal contributes significant impact values, as does nuclear and petroleum, whereas natural gas contributes relatively less.
Table 3.1. `Electric
Power Industry Generation of Electricity by Primary Energy Sources
and State for the Southeast Region as Defined by the U.S. Department
of Energy (2000).
|
Percentage Share, 19981/
|
|||||||||||||
| Fuel |
AL2
|
AR
|
FL
|
GA
|
KY
|
LA
|
MS
|
NC
|
SC
|
TN
|
TX
|
VA
|
Avg
|
| Source | |||||||||||||
| Coal Petroleum Gas Nuclear Hydro Non utility |
59.5
0.2 2.0 23.9 8.8 5.5 |
50.7
0.3 8.1 28.7 6.8 5.4 |
34.6
21.6 16.7 16.4 0.1 10.6 |
60.6
0.6 1.5 27.2 4.4 5.7 |
95.7
0.1 0.6 0.0 3.6 0.0 |
23.2
0.7 31.6 18.3 0.0 26.2 |
34.1
15.7 16.4 26.7 0.0 7.1 |
56.9
0.2 0.8 31.9 3.4 6.8 |
37.1
0.4 0.5 55.9 2.9 3.3 |
56.4
0.7 0.6 29.0 9.6 3.7 |
37.4
0.0 33.9 10.9 0.4 17.4 |
43.6
3.7 3.0 37.7 0.4 11.6 |
49.2
3.7 9.6 25.6 3.4 8.5 |
1 Source:
Energy Information Administration/State Electric Profiles 2000,
Department of Energy.
http://www.eia.doe.gov/cneaf/electricity/st_profiles/toc.html
2 Abbreviations of Southeastern States
Most of the bark generated during debarking, OSB fines from the screening process, and other waste sources in the plants were combined to use as wood fuel in a direct-fired fuel cell. Wood fuel weight, following industry practice, was given as green weight and assumed to be 50% moisture content on a wet-weight basis. As such, the total wood fuel burned (774 lb.) at 50% moisture content on a wet basis, is equivalent to 387 lb. of oven-dry weight wood fuel. A very small amount of OSB wood waste (trimmings and sawdust) was burned in the boiler. Wood fuel was by far the dominant fuel source at 79.0% of the total energy for heat. In addition to wood fuel for heat generation, natural gas and some fuel oil were also used, representing 18.4% and 2.6%, respectively, of the total heat generation. Table 3.2 provides a breakdown of heat energy use for the boilers by fuel source.
Table 3.2. Southeast
Weighted Data Conversion of Boiler Inputs into Heat Energy for 1.0
Msf 3/8-inch Basis of OSB
| Fuel Type |
Input
|
Heat Energy
BTU |
Allocation
% |
| Wood Fuel (lb) |
387.01/
|
3.29E+062/
|
79.0
|
| Natural Gas (ft3) |
698.0
|
7.68E+053/
|
18.4
|
| Fuel Oil (gal) |
0.769
|
1.08E+054/
|
2.6
|
| Total |
4.17E+06
|
100.0
|
1/ Weight
dry wood fuel oven dry basis (includes bark, screening fines, and
wood waste)
2/ Weight of dry wood multiplied by 8500 BTU/lb
3/ Volume of natural gas multiplied by 1100 Btu/ft3
4/ Volume of fuel oil multiplied by 140,000 BTU/gal
Phenol-formaldehyde (phenolic) resin and/or MDI are the adhesives
used in OSB production. The manufacture of these resins is particularly
energy intensive. The total energy requirement for the production
42.4 lb of phenolic needed for Msf 3/8-inch basis OSB from the Southeast
is 6.99E+05 BTUs. Electricity requirements for phenol-formaldehyde
production per MSF 3/8-inch basis are 27.4 kWh in addition to that
required in the OSB manufacturing process. The phenol-formaldehyde
resin used is comprised of 65% formaldehyde and 35% phenol by weight.
All the material, fuel, and electricity used to produce phenol-formaldehyde
resin are listed in Table 3.3.
The total energy requirement for the production 8.16 lb of MDI needed
for Msf 3/8-inchbasis OSB from the Southeast is 3.18E+05 BTU's.
Electricity requirements for MDI production per Msf 3/8-inch basis
are 6.16 kWh in addition to that required in the OSB manufacturing
process. MDI resin used is comprised of many different materials.
Table 3.4 lists some of the more significant materials along with
fuel use, and electricity used to produce the MDI resin. A complete
listing can be found in Boustead (1999).
Table 3.3: Production
Requirementsfor the 42.4 lb of Phenol-formaldehyde Resin Needed
to Manufacture 1.0 Msf 3/8-inch Basis OSB in the Southeast Region.
1/
| INPUTS | ||
Materials |
Units
|
per MSF 3/8-in basis
|
| Formaldehyde Phenol |
lb
lb |
2.76E+01
1.48E+01 |
Fuel Use |
||
| Heavy Oil Gasoline Natural Gas |
BTU
BTU BTU |
2.59E+04
1.82E+05 4.91E+05 |
Electrical Use |
||
| Electricity |
kWh
|
2.74E+01
|
1/Data
obtained from Material, Energy & Environmental Unit Factor Emissions:
Structural Wood Production, Athena, 1993.
Table 3.4. Production Requirements for the
8.16 lb of MDI Resin Needed to Manufacture 1.0 Msf 3/8-inch Basis
OSB in the Southeast Region. 1/
| INPUTS | ||
Materials2/ |
Units
|
per MSF 3/8-in basis
|
| Crude Oil Gas/Condensate Coal Lignite |
lb
lb lb lb |
4.07E+00
8.95E+00 2.61E+00 8.32E-01 |
Fuel Use |
||
| Heavy Oil Coal Natural Gas |
BTU
BTU BTU |
8.43E+04
3.15E+04 2.02E+05 |
Electrical Use |
||
| Electricity |
kWh
|
6.16E+00
|
1/Data
obtained from I Boustead. Ecoprofiles of chemicals and polymers
1999
2/Partial listing of Materials
Most emissions are generated from the heat generation process used
to supply the dryers and the presses. Since all of the plants surveyed
had direct-fired heating systems for dryers and presses, the emissions
have components of CO, CO2 (fossil), NOx,
SO2, and others. Dryers are used to take the moisture
content of green OSB flakes from about 100% down to about 5% (oven-dry
basis) and have an inlet temperature ranging from 1,100 to 1,300
oF. Hot pressing is done in the OSB manufacturing process
to provide intimate contact between oriented flakes while the phenol-formaldehyde
and/or MDI adhesives cure as a result of temperature in the 360-400oF
range. Emissions are generated from the wood as a result of the
high temperatures in the dryers and presses, and the adhesives also
generate emissions during cure.
In OSB manufacturing, emissions from dryers and hot pressing are
collected and processed through pollution control systems such as
described in Section 1.3. Emissions are monitored through these
pollution control systems. Table 4.1 lists emissions as determined
by surveys of OSB manufacturers.
Table 4.1 Emissions from
Pollution Control Systems of Southeast OSB Manufacturers as Reported
in Surveys
(These are total emissions, no burden or allocation
has been made to co-products).
| Air Emission |
Unit
|
Emissions per MSF 3/8-
in basis1/ |
| CO2 |
lb
|
NR2/
|
| CO |
lb
|
2.49E+00
|
| CH4 |
lb
|
NR
|
| NOx |
lb
|
5.95E-01
|
| SO2 |
lb
|
5.89E-02
|
| VOC |
lb
|
2.18E+00
|
| Particulates |
lb
|
6.13E-01
|
| Phenol |
lb
|
2.42E-02
|
| MDI |
lb
|
1.60E-04
|
Life-cycle inventory results to produce 1.0 Msf 3/8-inch of OSB
in the Southeast is given in Table 5.1 (inputs) and 5.2 (outputs).
Results include all processes within the system boundary defined
in Figure 1.1. These inputs and outputs summarize all those that
were obtained from the surveyed plants. These inputs and outputs
exclude the emissions contributed by the transportation of logs
to the mill or emissions contributed by the production, transportation
and or utilization of resin, wax, fuel, and electricity.
Table 5.1 Life-cycle
Input Inventory Results for Production of 1.0 Msf 3/8-inch Basis
OSB in the Southeast Region. (Results are for OSB production only,
no emissions included for production and delivery of fuel, electricity,
resins or wax).
| INPUTS | ||
Materials1/ |
Units
|
per/Msf
3/8-in basis |
| Round wood2/ |
ft3
|
49.8
|
| Wood Bark |
lb
lb |
1540
166 |
| Phenol Formaldehyde MDI Resin Wax |
lb
lb lb |
42.4
8.16 19.3 |
Electricity Use |
||
| Electricity |
kWh
|
183
|
Fuel Use |
||
| Wood fuel (produced)3/ |
lb
|
387
|
| Natural gas Liquid Propane gas Diesel Fuel Oil |
ft3
gal gal gal |
698
1.06 0.018 0.769 |
Table 5.2 Life-cycle Output Inventory Results
for 1.0 Msf 3/8-inch Basis OSB Production from the Southeast Region.
(Results include OSB production only, no emissions
were included for the production and delivery of electricity, fuels,
resins, and wax).
| OUTPUTS | ||
Material |
Units
|
per/Msf
3/8-in basis |
| Ash |
lb
|
4.22E+00
|
Product |
||
| OSB |
lb
|
1.26E+03
|
Co-products |
||
| Bark Mulch Sawdust Total |
lb
lb lb |
1.23E+02
2.88E+01 1.52E+02 |
Air Emission |
||
| CO2 |
lb
|
NR1/
|
| CO |
lb
|
2.49E+00
|
| CH4 |
lb
|
NR
|
| NOx |
lb
|
5.95E-01
|
| SO2 |
lb
|
5.89E-02
|
| VOC |
lb
|
2.18E+00
|
| Particulates |
lb
|
6.13E-01
|
| Phenol |
lb
|
2.42E-02
|
| MDI |
lb
|
1.60E-04
|
1/ Not reported in survey
Proposed research in the coming year includes expanding the OSB
LCI model into a sub-unit process approach. This model will be useful
in analyzing was to improve production efficiency subject to environmental
impacts. Also the development of an LCI model for Parallel Strand
Lumber will be completed. These models will be used in conjunction
with other LCI models developed in the CORRIM project. A number
of scenarios will be studied to optimize building materials design
to minimize environmental impact. Output of the analyses will be
compared to benchmark data to assess improvements.
APA The Engineered Wood Association (APA). 2001. North America Structural
Panel
Production by Geography 2000. March, 1 p.
Boustead, I. 1999. Ecoprofiles of chemicals and polymers.
Franklin Associates. 1998. Combustion of Wood in Industrial Boilers.
SimaPro5 Life-Cycle
Assessment Software Package, version 36,
2001.
Franklin Associates. 2000. Wood Precombustion. SimaPro5 Life-Cycle
Assessment Software
Package, version 36, 2001.
Franklin Associates. 1998. Natural Gas Combustion in Industrial
Boilers. SimaPro5 Life-Cycle
Assessment Software Package, version 36,
2001.
Franklin Associates. 1998. LPG Precombustion. SimaPro5 Life-Cycle
Assessment Software
Package, version 36, 2001.
Franklin Associates. 1998. Diesel Powered Industrial Equipment.
SimaPro5 Life-Cycle
Assessment Software Package, version 36,
2001.
Franklin Associates. 1998. Electricity from coal. SimaPro5 Life-Cycle
Assessment Software
Package, version 36, 2001.
Franklin Associates. 1998. Electricity from DFO. SimaPro5 Life-Cycle
Assessment Software
Package, version 36, 2001.
Franklin Associates. 1998. Electricity from natural gas. SimaPro5
Life-Cycle Assessment
Software Package, version 36, 2001.
Franklin Associates. 1998. Electricity from uranium. SimaPro5 Life-Cycle
Assessment
Software Package, version 36, 2001.
Franklin Associates. 1998. Electricity from hydropower. SimaPro5
Life-Cycle Assessment
Software Package, version 36, 2001.
PRé Consultants B.V. 2001. SimaPro5 Life-Cycle Assessment
Software Package, version 36.
Plotter 12, 3821 BB Amersfoort, The Netherlands.
http://www.pre.nl/.
The Athena Sustainable Materials Institute (Athena). 1993. Raw
Material Balances, Energy
Profiles and Environmental Unit Factor Estimates:
Structural Wood Products. Forintek
Canada Corp, Ottawa, Canada. March 1993.
Toennisson, R.L. and S.W. Hadden. 1993. Wood Products Engineer's
Handbook. Technical
Note B66, Forest Resources, Tennesse Valley
Authority, Norris, Tennessee. 63 p.
United States Department of Energy (USDOE). 2000. State Electricity
Profiles 2000.
http://www.eia.doe.gov/cneaf/electricity/st_profiles/.
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The CORRIM Home Page is administered through the College of Forest Resources at the University of Washington. CORRIM is a research consortium formed to establish, support, and manage research and education programs relating to renewable industrial materials focused on the environmental impact of the production, use, and disposal of wood and other bio-based materials. The Consortium includes 13 US and Canadian Research Institution members and a number of contributing companies, associations and agencies. This Institution is an equal opportunity provider. For more information please email Bruce Lippke or write toCORRIM, University of Washington BOX 352100 Seattle, WA 98195, (206) 543-0827. |