Executive Summary
Acronyms
Industry Background
Environmental Issues and
Regulations
Clean Technology Developments
Future Trends
References
TABLES
Table 1:
Key Organizations in the U.S. Pulp and Paper Industry
Table 2: Energy Sources Used by the U.S. Pulp and Paper
Industry
Table 3: Waste Streams Produced and Contaminants of
Concern for Bleached Kraft Pulping
Table 4: Waste Streams Produced and Contaminants of
Concern for Other Pulping Processes
Table 5: TRI Releases for the Pulp and Paper Industry
Table 6: Releases of Selected Air Pollutants
Table 7: Description of Extended Delignification
Processes
Table 8: Description of Alternative Pulping Technologies
1. EXECUTIVE SUMMARY
This report gives a brief overview of the U.S. pulp and paper industry, with
an emphasis on efforts to incorporate pollution prevention and clean
technologies into its manufacturing operations. It is not intended to be a
comprehensive industry guide or study. Rather, this report can be used as
guidance material for those who are seeking general information about the
U.S. pulp and paper industry and its use of technologies and processes that
reduce or prevent pollution.
The United States is the largest consumer of pulp and paper products in the
world. The U.S. pulp and paper industry, which supplies the bulk of this
demand, is larger than the next four largest producers of pulp and paper
outside the United States combined. In 1995 the per capita consumption of
paper in the United States was 331 kilograms. The next closest country in
per capita consumption is Japan, which used 238 kilograms per person.
The U.S. pulp and paper industry is recognized worldwide as a high-quality,
large-volume, low-cost producer that benefits from a large consumer base, a
modern technical infrastructure, an adequate supply of raw materials, and a
highly skilled labor force. It follows, then, that many of the major
technological innovations in the industry, including those in clean
technologies and processes, occur in the United States. The term "clean
technologies" is defined as "manufacturing processes or product
technologies that reduce pollution or waste, energy use, or material use in
comparison to the technologies that they replace."
Key resources used by the industry include the following:
Water. The pulp and paper industry is the largest user (per ton of
product made) of industrial process water in the United States. A typical
modern mill uses 16,000 to 17,000 gallons of water per ton of pulp produced.
This is down from the average of 100,000 gallons per ton that was typical in
the mid-1940s.
Fiber Resources (Furnish). Wood provides the virgin fiber resource or
furnish for virtually all of the papermaking pulp capacity in the
United States. Nonwood fiber sources, common in many parts of the world
(most notably India and China), represent a minuscule percentage of the raw
material used to make pulp in the United States. Secondary (i.e., recycled)
fibers are the next most common fiber source for papermaking in the United
States. About 70% of U.S. mills use some fraction of secondary fibers as
furnish for pulp production, and about 200 facilities rely exclusively on
secondary fibers for furnish.
Energy Use. Chemical pulping processes require on average the
equivalent of more than 170 gallons of oil to produce one ton of pulp.
Chemical pulping, however, generates process residues (i.e., black liquor
from the kraft pulping process) from which process chemicals and energy can
be recovered. In fact, over the past several decades, U.S. industry has come
to rely more on these process wastes for its energy. Sources of fuel used by
the pulp and paper industry include fuels, bark, process residue, and
natural gas. Some mills produce enough process waste to meet all of their
energy needs; in 1994, 57% of U.S. mills were completely energy
self-sufficient in this manner.
Key environmental issues for the U.S. industry include the following:
Water. Primary issues of concern are biochemical oxygen demand (BOD);
chlorinated organic compounds (particularly dioxin), which are often
collectively measured as adsorbable organic halides (AOX); chemical oxygen
demand (COD); total suspended solids (TSS); and aquatic toxicity. Reduction
of water use in the industry is also a concern, although progress has been
made in this area in the past several decades. Elimination of aqueous
effluent from the manufacturing process is a goal of the industry worldwide.
Air. Primary issues of concern are emission of nitrous oxides, sulfur
oxides, and particulate matter. Air emissions from pulp making are typically
highly odorous due to their high sulfur content, which leads the public to
perceive the industry as "dirty."
Chemical Releases. The industry released approximately 218 million
pounds of Toxics Release Inventory (TRI) chemicals to air, water, or land in
1993. This represents less than 4 percent by weight of the total quantity of
chemicals released or transferred by all U.S. manufacturers that year; in
general, releases of chemicals reported by the pulp and paper industry have
been decreasing steadily over time. The top five reported TRI chemicals
released to the environment by the pulp and paper industry are methanol,
hydrochloric acid, sulfuric acid, chloroform, and ammonia.
Bleaching Operations. Chlorine used to bleach pulp leads to the
formation of chlorinated organic compounds in effluent, which have been
linked to adverse health effects in both humans and wildlife. The industry
is undertaking methods to reduce formation of compounds in bleach plant
effluent by using new chemicals and bleaching techniques.
The most significant regulatory topic of interest within the industry is the
so-called Cluster Rule, which was proposed in late 1993 by the U.S.
Environmental Protection Agency (EPA) and is expected to be promulgated in
1997. The Cluster Rule is a first-of-its-kind environmental standard that
will prescribe integrated concentration limits for effluent and air
emissions from pulp and paper mills for a wide variety of environmental
parameters. By and large, industry is awaiting the promulgation of this rule
to make major upgrades to their manufacturing equipment, because the
prescribed limits on effluent and air emissions will likely dictate the type
of technology needed to comply with the limits.
Clean technologies described in this document include the following:
- Elemental chlorine-free (ECF)
bleaching. Use of chlorine dioxide in lieu of elemental chlorine
to bleach pulp.
- Total chlorine-free bleaching.
Use of chemicals not containing chlorine (e.g., oxygen and hydrogen
peroxide) to bleach pulp.
- Extended delignification.
Process modifications to remove additional lignin from pulp to reduce the
use of bleaching chemicals.
- Alternative pulping
technologies. Use of nontraditional chemicals and methods for
pulping that reduce the use of sulfur-containing compounds.
- Use of nonwood fiber sources.
Use of plants that are thought to be more sustainable in the long term
than forest resources.
- Black liquor gasification.
Use of gasification rather than a recovery boiler to recover chemicals
used during pulping.
- Sensors and process control.
Use of advanced techniques to control specific portions of the
manufacturing process to reduce wastes and increase productivity.
- Water use reduction and closed
bleach/ effluent systems. Reduction or total elimination of
effluent from the manufacturing process.
Of these technologies, the ones that the
United States is most readily adopting or most likely to adopt in future
years include ECF bleaching, extended delignification, black liquor
gasification, advanced sensors and process control, and water use reduction
and closed effluent systems. Implementation of the Cluster Rule will act as
a driver for technology implementation. Other trends for the future of the
pulp and paper industry are noted in Agenda 2020, a document that
outlines the research objectives for the United States, as agreed on by
industry representatives and related trade and research organizations with
support from the U.S. Department of Energy (DOE). The issues identified in
this document will require attention and collaborative research among the
industry, its suppliers, other institutions, and the government to ensure
the health of the industry in this time frame. The six topics described in
Agenda 2020 are sustainable forest management, improved environmental
performance, improved energy performance, improved capital effectiveness,
recycling, and advanced sensors and controls. Historically, U.S. investments
are driven by cost-effectiveness, regulatory mandates, and consumer demand
for environmentally benign products. This trend is expected to continue as
the industry moves into the twenty-first century.
ACRONYMS
AET |
Alliance for
Environmental Technology |
AF&PA |
American Forest and Paper Association |
AOX |
adsorbable
organic halides |
BAT |
best
available technology |
BOD |
biochemical
oxygen demand |
CERF |
Civil
Engineering Research Foundation |
COD |
chemical
oxygen demand |
DCS |
distributed
control systems |
DOE |
U.S.
Department of Energy |
ECF |
elemental
chlorine-free |
EPA |
U.S.
Environmental Protection Agency |
MACT |
maximum
achievable control technology |
NCASI |
National
Council for Air and Stream Improvement |
PIMA |
Paper
Industry Manufacturers Association |
TAPPI |
Technical
Association of the Pulp and Paper Industry |
TCF |
total
chlorine-free |
TSS |
total
suspended solids |
US-AEP |
U.S.-Asia
Environmental Partnership |
USAID |
U.S. Agency
for International Development |
USD |
U.S. dollars |
WWW |
World Wide
Web |
2. INDUSTRY
BACKGROUND
2.1 Description and History
The United States is the largest consumer of pulp and paper products in the
world. In fact, the U.S. pulp and paper industry is larger than the next
four largest producers outside the United States of pulp and paper combined.
In 1995 the per capita consumption of paper in the United States was 331
kilograms. The next closest country in per capita consumption is Japan,
which used 238 kilograms per person.
The U.S. pulp and paper industry is recognized worldwide as a high-quality,
large-volume, low-cost producer that benefits from a large consumer base, a
modern technical infrastructure, an adequate supply of raw materials, and a
highly skilled labor force. The current principal competition for this
industry comes from Canada and Scandinavia. Export markets, which are
becoming increasingly important for the economic health of the U.S.
industry, include Canada, Mexico, and Japan.
2.2 Industry Demographics
There are approximately 555 facilities
that manufacture pulp and paper in the United States. Of these facilities,
about half are integrated facilities (i.e., manufacturing both pulp and
paper products), half manufacture only paper products, and about 50 produce
only market pulp. The latest statistics show that the pulp and paper
industry employs about 198,000 people in the United States. In 1991 the pulp
and paper industry, along with the converting industry (those facilities
that make products from paper, such as cartons and envelopes) produced about
US$75 billion in shipments. This represents about 4% of the value of
shipments for the entire U.S. manufacturing sector.
Chemical pulping, specifically the kraft chemical pulping process, is the
dominant pulp-making process used in the United States. It accounted for
about 80% by weight of all U.S.-produced pulp in 1996. Semichemical and
mechanical pulping comprise the remaining percentage of pulping capacity.
Bleaching of chemical pulps is also common in the United States; about half
of pulp tonnage produced in 1993 was bleached in some fashion. Semichemical
and mechanical pulps are difficult and costly to bleach; thus, bleaching is
rare in these instances.
Pulp and paper mills tend to be large and capital intensive. The cost of
building a new, state-of-the-art integrated mill is estimated at US$1
billion. Mills tend to be collocated near forest resources for ease of
transportation of raw materials: the southeast, northwest, northeast, and
north-central portions of the continental United States.
Table 1 provides a brief listing of some of the largest companies and
organizations associated with the U.S. industry. This list is not intended
to be exhaustive, but rather to provide a short overview of industry
players, which include pulp and paper mills, equipment and chemical
suppliers, process design and consulting engineers, professional trade
associations, and research institutions. Small mills tend to work directly
with the supplier community to meet their day-to-day needs for operation and
maintenance of equipment. For large-scale retrofits and redesigns, however,
mills typically work with design and consulting engineers, who in turn work
directly with manufacturers to specify the processes and equipment needed.
Table 1: Key Organizations in the U.S.
Pulp and Paper Industry |
Organization |
Headquarters
|
World Wide Web
Address, if available |
MILLS |
|
|
International Paper
|
Mobile, AL |
www.ipaper.com |
Weyerhaeuser
|
Tacoma, WA |
NA |
Kimberly-Clark
|
Neenah, WI |
www.kimberly-clark.com |
Georgia-Pacific
|
Atlanta, GA |
www.gp.com |
Stone Container
|
Chicago, IL |
www.azird.ord/stone |
Champion International
|
Stamford, CT |
www.championinternational.com |
Mead
|
Dayton, OH |
www.mead.com |
Boise Cascade
|
Boise, ID |
www.bc.com |
Union Camp
|
Wayne, NJ |
www.unioncamp.com |
Jefferson Smurfit
|
St. Louis,
MO |
j-src.com/jsc |
EQUIPMENT
MANUFACTURERS |
|
|
ABB
|
Europe/Windsor, CT |
www.abb.com |
Beloit Corporation
|
Beloit, WI |
www.beloit.com |
Black Clawson
|
Middletown,
OH |
www.blackclawson.com |
Ahlstrom Filtration
|
Chattanooga,
TN |
NA |
Sunds Defibrator
|
Europe/Norcross, GA |
www.sundsdefibrator.com |
CHEMICAL
MANUFACTURERS |
|
|
Air Products and Chemicals
|
Allentown,
PA |
www.airproducts.com |
Ciba-Geigy
|
Summit, NJ |
www.ciba.com |
Dow Chemical
|
Midland, MI |
www.dowchem.com |
3M Company
|
St. Paul, MN |
www.3m.com |
PROCESS
DESIGNERS AND CONSULTANTS |
BE & K Engineering
|
Birmingham,
AL |
www.bek.com |
Babcock and Wilcox
|
Barberton,
OH |
www.babcock.com |
Bechtel
|
Houston, TX |
www.bechtel.com |
Jacobs-Sirrine Engineers
|
Bakersfield,
CA |
NA |
Jaakko Poyry Fluor Daniel
|
Irvine, CA |
www.fluordaniel.com |
Parsons, Inc.
|
Pasadena, CA |
www.parsons.com |
Raytheon/Rust Engineering
|
Lexington,
MA |
www.raytheon.com |
Simons Engineering
|
Vancouver,
BC, Canada |
www.hasimons.com |
Stone & Webster
|
Boston, MA |
www.stonewebster.com |
PROFESSIONAL TRADE ASSOCIATIONS AND RESEARCH INSTITUTES |
Technical Association of the Pulp
and Paper Industry (TAPPI)
|
Atlanta, GA |
www.tappi.org |
Institute for Paper Science and
Technology (IPST)
|
Atltanta, GA |
www.ipst.edu |
National Council for Air and Stream
Improvement (NCASI)
|
Research
Triangle Park, NC |
www.ncasi.org |
Alliance for Environmental
Technology (AET)
|
Washington,
DC |
aet.org |
USDA Forest Products Laboratory
|
Madison, WI |
www.fpl.fs.fed.us |
2.3 Use of Natural Resources
Water
The pulp and paper industry is the largest user
(per ton of product made) of industrial process water in the United States.
A typical modern mill uses 16,000 to 17,000 gallons of water per ton of pulp
produced. This is down from an average of 100,000 gallons per ton, which was
typical in the mid-1940s. Despite this order-of-magnitude improvement,
reduction of water use is still a primary concern of the U.S. industry, and
research to this end has been going on for several decades. A technical
challenge facing the pulp and paper industry worldwide is to close off the
effluent system completely, resulting in no aqueous discharge to the
environment.
Fiber Resources (Furnish)
Wood provides the virgin fiber source or furnish for virtually all of
the papermaking pulp capacity in the United States. Wood is an abundant
natural resource in the United States and can be used to make a diverse
array of paper products varying in use and strength. Nonwood fiber sources,
common in many parts of the world (most notably India and China) represent a
minuscule percentage of the raw material used to make pulp in the United
States.
Secondary (i.e., recycled) fibers are the next most common fiber source for
papermaking in the United States. These may consist of either preconsumer
wastes (e.g., scrap waste from the mill itself) or postconsumer fiber that
is recycled following use. About 40% by weight of paper produced in the
United States is recycled following use; most of this paper comes from
newsprint and corrugated boxes. In fact, worldwide, the recycling rate has
increased as developed countries address the growing problem of solid waste
disposal, of which paper is the largest component by both weight and volume.
About 70% of U.S. mills use some fraction of secondary fibers as furnish for
pulp production, and about 200 of the 550 facilities rely exclusively on
secondary fibers for furnish. These fibers are processed to remove
impurities such as glues and ink.
Energy Use
Pulp and paper manufacturing is an energy-intensive industry. Chemical
pulping processes require on average the equivalent of more than 170 gallons
of oil to produce one ton of pulp. Chemical pulping, however, generates
process residues (i.e., black liquor from the kraft pulping process) from
which process chemicals and energy can be recovered. In fact, in the past
several decades, U.S. industry has come to rely more on these process wastes
for its energy. Table 2 summarizes percentages of energy sources used
by the U.S. pulp and paper industry in the past three decades, in terms of
percentage of total energy used by the industry as a whole. (For instance,
in 1972 residual fuel oil was used to generate 21.2% of the energy used by
the industry.) The estimates show that the proportion of the industry's
energy use derived from fossil fuels has decreased dramatically, whereas
dependence on process wastes has increased. Some mills produce enough
process waste to meet all of their energy needs. In 1994, 57% of U.S. mills
were completely energy self-sufficient in this way.
Semichemical and mechanical pulping processes use less energy than chemical
processes, but they do not generate spent pulping liquors from which energy
can be recovered. Because of this, depending on the size of the
manufacturing operation, use of these processes could result in a net loss
of energy.
Table 2: Energy Sources Used by the
U.S. Pulp and Paper Industry, By Percentages |
Energy Source:Self-Generated |
1972 |
1994 |
Energy
Source:Purchased |
1972 |
1994 |
Spent
pulping liquor |
33.0 |
40.8 |
Residual
fuel oil |
21.2 |
6.0 |
Bark |
4.5 |
6.6 |
Distillate
fuel oil |
1.0 |
0.3 |
Wood
residues |
2.0 |
7.3 |
Natural gas |
21.1 |
16.9 |
Self-generated hydropower |
0.4 |
0.2 |
Purchased
electricity |
4.4 |
6.4 |
Other |
0.4 |
1.0 |
Coal |
10.7 |
12.5 |
|
|
|
Other |
1.3 |
2.0 |
TOTALS |
40.3% |
55.9% |
|
59.7% |
44.1% |
Note: The
percentages for each source represent the fraction of total energy used
by the pulp and paper industry in the year for which data are reported.
Reference: AF&PA, Energy Monitoring System, 1994. |
2.4 Waste Streams of Concern
Production of pulp and paper produces waste streams that must be managed,
recovered, treated, and/or disposed of. Table 3 presents a list of
the waste streams produced and their associated contaminants of concern for
kraft pulping. Table 4 presents a list of waste streams produced by
other pulping processes.
Effluent and air emissions from pulp and paper mills have been a focus of
environmental concerns for the industry. Effluent waste streams include
aqueous discharges from pulping, pulp processing, bleaching, and
papermaking. Because of the large volume of water used in manufacturing,
most mills operate their own primary and secondary wastewater treatment
plants to remove solids and biochemical oxygen demand (BOD) from the
effluent and to treat some fraction of chlorinated organic compounds
(collectively measured as adsorbable organic halides [AOX]) and chemical
oxygen demand (COD) prior to discharge to receiving waters or to a publicly
owned treatment works (POTW). Of particular concern is the formation of
chlorinated compounds in effluent as a result of using elemental chlorine
(Cl2) to bleach pulp. Some chlorinated compounds, particularly
dioxin, have been linked to adverse biological effects on wildlife in
receiving waters, as well as human health risks.
Air emissions result from burning fossil fuels and wood wastes for energy,
from chemical pulping and evaporation of weak black liquor generated by
kraft pulping, and from operation of furnaces in kraft chemical recovery
systems.
Solid wastes produced by the industry include fiber lost during the pulping
process and scrap paper wastes. Because, however, a large portion of fiber
and paper wastes are recovered and recycled, solid wastes are of little
concern compared with effluent and air emissions for the industry.
Spent liquor from nonwood pulping often contains a high silica content,
which presents a challenge in liquor recovery processes. Nonwood pulping
mills that use chemical recovery systems commonly use a similar technology
to that used by wood pulp mills with a modification to remove silica, which
would otherwise form a glass-like residue on the interior of the recovery
furnace evaporators. This concern is not primary in the U.S. industry
because only a small percentage of pulp is made from nonwood fiber sources.
Chemical Releases
Table 5 presents data that summarize the total amount of chemicals
released by the pulp and paper industry over a four-year time frame. Data
from 1992 and 1993 are reported estimates of quantities managed, whereas
data reported for 1994 and 1995 are projections only. The chemicals for
which these data are reported consist of the 316 chemicals that were listed
in 1993 on EPA's Toxics Release Inventory (TRI). Currently, the list of TRI
chemicals has been expanded to more than 600 chemicals, but up-to-date
information on releases of all of these chemicals is not available for the
pulp and paper industry.
Table 5 shows that the industry managed about 2 trillion pounds of
chemical wastes in 1993. Of these wastes, approximately 218 million pounds
were either released to air, water, or land, or shipped off-site for
disposal. Although the pulp and paper industry had the highest TRI chemical
releases per facility of all industries in 1993 (an average of 550,000
pounds), this represents less than 4% by weight of the total quantity of
chemicals released or transferred by all U.S. manufacturers that year.
Releases of chemicals reported by the pulp and paper industry have been
decreasing steadily over time; 1993 statistics show an 8% reduction from
1992 and a 22% reduction since 1988.
The industry releases 87% by weight of its TRI chemicals to air,
approximately 10% to water and POTW; 2% is transferred off-site or disposed
of. This release profile differs from all other TRI-releasing industries,
which average 93% to air, 6% to land, and 1% to water. The difference is
attributable to the water-intensive nature of the pulp and paper
manufacturing process.
The top five reported TRI chemicals released to the environment by the pulp
and paper industry are:
- Methanol
- Hydrochloric acid
- Sulfuric acid
- Chloroform
- Ammonia
Methanol accounts for 50% of all air
releases and 40% of all releases to water.
EPA's Office of Air and Radiation
maintains data on annual releases of several air pollutants for major U.S.
industries. Table 6 summarizes the estimated annual releases of a
suite of common pollutants. The data show that, compared to other
manufacturing sectors, the pulp and paper industry is a primary releaser of
carbon monoxide, nitrogen dioxide, and sulfur dioxide.
Table 3: Waste Streams Produced and
Contaminants of Concern for Bleached Kraft Pulping1 |
Process Sequence |
Waste Stream
Produced |
Contaminants of
Concern |
WATER |
Furnish
preparation and handling |
Water used
in handling, debarking, and chip washing |
total
suspended solids (TSS)biochemical oxygen demand (BOD)color |
Pulping |
Weak black
liquor from digester, liquor spills |
BODreduced
sulfur compounds |
Pulp
processing |
"White
waters" from pulp screening, thickening, and cleaning |
high volume
of waterTSSBOD |
Pulp
bleaching |
Bleach plant
washer filtrates, spills |
chlorinated
organic compounds, including dioxinadsorbable organic halides (AOX)BODcolor |
Wet end
operations |
Water
collected as pulp dries, spills |
TSS |
Chemical
recovery system |
Condensate
from weak black liquor evaporator |
BODreduced
sulfur compounds |
AIR |
Pulping |
Emissions
from digester |
volatile
organic compounds (VOCs) |
Chemical
recovery system |
Emissions
from weak black liquor evaporators |
VOCs |
|
Emissions
from recovery furnace |
fine
particulatestotal reduced sulfur (TRS) compoundsnitrous oxides (NOx) |
Burners for
energy production |
Emissions
from burner |
coarse
particulatesNOxSOx |
|
|
|
1
Note: Although solid wastes are produced during pulp and paper making,
they are not discussed here because they are of secondary importance
from an environmental standpoint for the U.S. industry.
Reference: EPA, Profile of the Pulp and Paper Industry,
EPA/310/R-95/015, September 1995. |
Table 4: Waste Streams Produced and
Contaminants of Concern for Other Pulping Processes1 |
Process Sequence |
Waste Stream
Produced |
Contaminants of
Concern |
Relevant Pulping
Processes |
WATER |
Furnish
preparation and handling |
Water used
in handling, debarking, secondary fiber processing |
TSS
BOD
color |
sulfite
chemical; semi-chemical; mechanical; secondary fiber pulping;
|
Pulping |
Liquor from
digester, liquor spills |
BOD
reduced sulfur compounds |
sulfite
chemical; nonwood pulping |
Pulp
processing |
"White
waters" from pulp screening, thickening, and cleaning |
high volume
of water
TSS
BOD |
sulfite
chemical; nonwood pulping |
Wet end
operations |
Water
collected as pulp dries, spills |
TSS |
sulfite
chemical; semi-chemical; mechanical; secondary fiber pulping; nonwood
pulping
|
Chemical
recovery system |
Condensate
from liquor evaporator |
BOD
reduced sulfur compounds |
sulfite
chemical; nonwood pulping |
AIR |
Pulping |
Emissions
from digester |
VOCs |
sulfite
chemical; nonwood pulping |
Chemical
recovery system |
Emissions
from liquor evaporators |
VOCs |
sulfite
chemical; nonwood pulping |
|
Emissions
from recovery furnace |
fine
particulates
total reduced sulfur (TRS) compounds
NOx
sulfur oxides (SOx) |
sulfite
chemical; nonwood pulping |
Burners for
energy production |
Emissions
from burner |
coarse
particulates
NOx
SOx |
sulfite
chemical; semi-chemical; mechanical; secondary fiber pulping; nonwood
pulping |
1
Although solid wastes are produced during pulp and papermaking, they are
not discussed here because they are of secondary importance from an
environmental standpoint for the U.S. industry.
Reference: EPA, Profile of the Pulp and Paper Industry,
EPA/310/R-95/015, September 1995. |
Table 5: TRI Releases for the Pulp and
Paper Industry |
Year1 |
Quantity of
Production-Related Waste, (millions of pounds) |
Percent of Waste
Managed Onsite |
Percent of Waste
Managed Offsite |
Waste Managed On Site |
Waste Managed Off Site2 |
Percent Recycled |
Percent Energy Recovery |
Percent Treated |
Percent Recycled |
Percent Energy Recovery |
Percent Treated |
1992 |
2,080 |
90 |
10 |
5 |
10 |
74 |
.02 |
.02 |
3 |
1993 |
1,958 |
90 |
9 |
5 |
10 |
74 |
.02 |
.03 |
2 |
1994 |
1,991 |
' |
8 |
5 |
11 |
73 |
.02 |
.03 |
2 |
1995 |
1,949 |
' |
8 |
5 |
11 |
73 |
.02 |
.02 |
2 |
Reference:
EPA, Profile of the Pulp and Paper Industry, EPA/310/R-95/015,
September 1995.
1 Years 1992 and 1993 are reported; years 1994 and 1995 are
estimated.
2 Remaining percentage of wastes managed off site were either
(a) released to the environment through direct discharges to air,
land, and water, and underground injection, or (b) disposed of
off site without treatment. Statistics are not available to quantify
releases to the environment or disposal without treatment. |
Table 6: Releases of Selected Air
Pollutants |
Pollutant |
Tons Released Per
Year |
Rank Among U.S.
Manufacturing Industries |
Carbon
monoxide (CO) |
624,291 |
2 |
Nitrogen
dioxide (NO2) |
394,448 |
1 |
Particulate
matter of diameter of 10 microns or less (PM10) |
35,579 |
5 |
Total
particulates (PT) |
113,571 |
4 |
Sulfur
dioxide (SO2) |
541,002 |
2 |
Volatile
organic compounds (VOCs) |
96,875 |
7 |
Reference:
EPA Office of Air and Radiation, Aerometric Information Retrieval
System (AIRS) data base, May 1995. |
3. ENVIRONMENTAL
ISSUES AND REGULATIONS
The pulp and paper industry is subject to U.S. environmental regulations for
effluent, air emissions, and solid wastes.
Effluent guidelines have been in place for the pulp and paper industry since
1974; updated guidelines were issued in 1977 and 1982. Effluent guidelines
fall under the purview of the Clean Water Act (CWA), which is intended to
restore and maintain the chemical, physical, and biological integrity of the
nation's surface waters. Under the CWA, the National Pollutant Discharge
Elimination System (NPDES) program controls direct discharges of effluent
into navigable waters. Permits for discharge are issued either by EPA or a
state environmental agency and require regular and periodic
characterization, measurement, and monitoring of effluent and its contents.
Many mills in the United States hold NPDES because they discharge large
volumes of effluent to streams and rivers. Parameters often regulated by
NPDES permits in the pulp and paper industry include BOD, COD, chlorinated
organic compounds, temperature, and aquatic toxicity.
The industry is also subject to specific provisions of the Clean Air Act (CAA),
which is designed to protect and enhance the nation's air resources to
protect public health and welfare. The Clean Air Act establishes limits for
air pollutants such as carbon monoxide, nitrous oxides, sulfur oxides, and
particulate matter, all of which are pollutants of concern for the U.S. pulp
and paper industry.
Mills may also generate a number of waste streams that are subject to
regulations of the Resource Conservation and Recovery Act (RCRA), which
outlines requirements for identification, treatment, storage, and disposal
of hazardous wastes.
Cluster Rule: An Integrated Rulemaking
The current and most significant regulatory topic of interest within the
U.S. pulp and paper industry is the so-called "Cluster Rule," which was
proposed in late 1993 by EPA and is expected to be promulgated in 1997. The
Cluster Rule is a first-of-its-kind environmental standard that will
prescribe integrated concentration limits for from pulp and paper mills for
a wide variety of environmental parameters. The rule will apply to most pulp
and paper manufacturers in the United States and will be enforced by EPA
with appropriate participation and coordination with state regulatory
agencies.
The Cluster Rule will call for, although not specifically mandate, adoption
of best available technologies (BAT) for effluent treatment and maximum
achievable control technologies (MACT) for air emissions to control these
waste streams. These technologies are presumably commercially available and
economically feasible for mills to adopt; parameter limits in the rule were
derived with the assumption that mills would use these treatment
technologies.
The Cluster Rule will undoubtedly set environmental standards that other
countries will seek to model in their own regulations and requirements for
their domestic industries. Compliance with the effluent limitations
established in the Cluster Rule will be required of U.S. mills three years
from the date of promulgation. Air emissions limits will be enacted in three
phases.
The time lag between the date the rule was proposed and its predicted
promulgation has been caused in part by industry's response to several of
the tenets of the original draft rule. During that time, the industry
provided EPA with information about its environmental performance and
predicted costs of industry compliance with the rule. In turn, EPA has
revised and refined the language and parameter limits for the Cluster Rule
to respond to the industry's input, as well as input from independent
environmental organizations. Based on industry's current understanding of
EPA's responses, the final Cluster Rule is expected to contain effluent
limitations on the following parameters:
- Total suspended solids (TSS)
- Biochemical oxygen demand (BOD)
- A suite of chlorinated organic
compounds, including a "non-detect" limit for dioxin. Currently, the
detection level for dioxin in aqueous effluent is 10 parts per
quadrillion; in sludges and end products, it is 1 part per trillion.
- Adsorbable organic halides (AOX), a
less costly surrogate measure of a range of chlorinated organic compounds.
Current industry understanding is that the
specific provisions for air emissions in the Cluster Rule are likely to be
superseded by broader and possibly more stringent parameter limits in the
more recently proposed Air Quality Standards under the CAA.
Some tenets of the Cluster Rule are still being debated. For instance,
industry is generally opposed to the use of AOX as a surrogate measure for
several chlorinated organic compounds. The range of compounds measured by
AOX vary widely in degree of toxicity, persistence in the environment, and
potential for bioaccumulation. Industry asserts that most of the AOX
fraction is composed of less chlorinated compounds that exhibit lower to no
toxicity and fewer to no adverse ecological effects when discharged to the
environment, compared to compounds with a higher degree of chlorination.
U.S. mills are waiting until promulgation
of the Cluster Rule to make major upgrades to their manufacturing equipment,
because the prescribed limits on effluent and air emissions will likely
dictate the type of technology needed to comply with the limits. For
instance, to comply with effluent limits, it is likely pulp will have to be
bleached with chemicals other than elemental chlorine (Cl2),
which may require some mills to change or update their bleaching plants.
Recently, a new kraft pulp mill was required to use a catalytic converter to
remove organic compounds in their air emissions to obtain an operating
permit. This requirement is much more stringent than the current scope of
the most recent version of the Cluster Rule and serves as an example of why
industry is waiting to make large-scale capital investments.
4. CLEAN
TECHNOLOGY DEVELOPMENTS
This section provides a brief description of clean technologies and
pollution prevention techniques used by the U.S. pulp and paper industry.
These technologies vary in their acceptance and adoption by industry, which
will also be discussed. "Clean technologies" are defined as
"manufacturing processes or product technologies that reduce pollution or
waste, energy use, or material use in comparison to the technologies that
they replace."
The technologies described in this section are:
- Elemental chlorine-free bleaching
- Total chlorine-free bleaching
- Extended delignification
- Alternative pulping technologies
- Use of nonwood fiber sources
- Black liquor gasification
- Sensors and process control
- Water use reduction and closed
bleach/effluent systems
A Note on Pulp Bleaching and Clean
Technology
Bleaching methods are of considerable importance when discussing clean
technologies for the pulp and paper industry; thus, much of the effort in
clean technology development is intended to minimize the environmental
impacts of this process step. For many decades, the global pulp and paper
industry relied on elemental chlorine (Cl2) as an efficient and
inexpensive pulp-bleaching agent. Scientific evidence suggests, however,
that elemental chlorine reacts with precursors, namely lignin, to form
chlorinated organic compounds (e.g., dioxin) that are believed to be
carcinogenic to humans based on results of laboratory studies with animals.
The presence of these chlorinated compounds has also been linked to adverse
ecological effects on wildlife in receiving waters.
4.1 Elemental Chlorine-Free (ECF) Bleaching
Description. ECF bleaching substitutes chlorine dioxide (ClO2)
for elemental chlorine (Cl2) in the mill's bleach plant. Because
of differences in its chemistry and reaction with lignin, use of chlorine
dioxide in place of elemental chlorine has been demonstrated to improve the
overall environmental performance of the bleaching operation.
Benefits. Studies have shown the following benefits for ECF bleaching
over the use of elemental chlorine:
Effluent concentrations of chlorinated organic compounds were reduced as
much as fivefold to tenfold.
Compounds formed have a lower degree of chlorination than those detected
when using elemental chlorine.
" Concentrations of dioxin in effluent were substantially decreased or
nondetectable.
" Toxicity, adverse ecological effects, degree of persistence in the
environment, and potential for bioaccumulation were lower.
Status of Use in the United States. Production of ECF-bleached pulp
in the United States has increased by nearly 2,000% since 1990, and the use
of ECF bleaching is expected to increase in the United States with
promulgation of the Cluster Rule. At the end of 1995, ECF bleaching
constituted over 30% of the bleached chemical pulp market in the United
States.
4.2 Total Chlorine-Free (TCF) Bleaching
Description. TCF bleaching of pulp uses nonchlorinated chemicals,
such as oxygen (O2), hydrogen peroxide (H2O2),
or ozone (O3), sometimes aided by enzymes. TCF bleaching
processes were developed to reduce or eliminate the formation of chlorinated
compounds in bleach plant effluent.
Benefits. The benefits of using TCF bleaching are similar to those
seen when using ECF bleaching, including:
- Formation of chlorinated compounds in
effluent, including dioxin is reduced or eliminated.
- Toxicity, adverse ecological effects,
degree of persistence in the environment, and potential for
bioaccumulation were lower.
Status of Use in the United States.
The U.S. industry is leaning toward widespread adoption of ECF bleaching
over TCF, for several reasons:
- TCF bleaching has been shown to reduce
pulp yield by as much as 6%, which represents a cost to the industry.
- Some studies show a link between TCF
bleaching and reduction of pulp quality, strength, and brightness.
- The process may decrease the
recyclability of the finished paper because of reduced pulp quality.
- Capital investments are higher for TCF
bleaching than for ECF because concurrent process modifications must be
made in tandem to optimize the process (e.g., equipment for extended
delignification or increase in capacity of recovery boiler).
- There is no current or future
regulatory mandate or perceived domestic demand that will call for the use
of TCF bleaching over any other bleaching process.
4.3 Extended Delignification Processes
Description. Several processes are available to remove residual
lignin (lignin remaining in the pulp following traditional chemical
pulping) from pulp. Table 7 describes the specifics of each process
in more detail.
Benefits. The presence of lignin in most pulps makes them difficult
and costly to bleach. Removal of even an incremental amount of residual
lignin via extended delignification processes can significantly reduce the
volume of bleaching chemicals needed to achieve a target brightness level,
resulting in cost savings for bleaching and treatment of bleach plant
effluent. The challenge of extended delignification is to remove as much
residual lignin as practicable without sacrificing pulp yield.
Status of Use in the United States. Many U.S. mills are awaiting the
promulgation of the Cluster Rule to determine whether implementation of
extended delignification will be necessary to comply with proposed statutory
limits on bleach plant effluent. In general, extended delignification
processes are added when the calculated cost savings and payback period
justify its use in a particular mill. Oxygen delignification appears to be
favored over ozone delignification due to its lower operating costs.
Chemical catalysts to aid delignification are used by only a small number of
mills; use may increase as research to optimize the process progresses.
Table 7: Description of Extended
Delignification Processes |
Process |
Description |
Comments |
Modification
of cook time or temperature |
Either the
cooking time for pulping or the pulping temperature is increased to
provide extended delignification. This process is relatively simple to
control and does not require specialized equipment or chemicals.
|
Extended
cooking generally leads to loss of pulp yield above 95 percent lignin
removal and may result in loss of pulp strength. |
Extended
cook |
The pulping
process is extended by adding cooking liquor to the pulp in stages
rather than as a single "dose." Lignin removal is as high as 97 percent
(a 50 percent increase over pulping alone), which reduces the volume of
bleaching chemicals needed by 35 percent.
|
Extended
cooking increases the solids content of the black liquor, making
additional demands on recovery furnace capacity, which may necessitate
installation of a larger furnace. Capital investment for extended cook
equipment can be substantial. |
Oxygen
Delignification |
A mixture of
elemental oxygen (O2), sodium hydroxide (NaOH), and magnesium
hydroxide (MgOH) is mixed with the pulp following pulping and pumped
into a pressurized reactor to provide up to a 50 percent reduction in
residual lignin. Oxygen can be generated onsite, which is generally less
costly in the long run than off-site purchase. This process increases
the heating value of the black liquor solids, so that a greater amount
of energy can be derived by burning solids in the recovery furnace.
|
The use of
oxygen delignification increases operating costs, but these increases
are offset to some degree by reduced bleaching chemical requirements and
by the increased heating value of the black liquor. Capital costs for
oxygen delignification must take into account the increased heating
value of black liquor solids, as well as the specialized equipment
needed. |
Ozone
delignification |
This process
is similar to oxygen delignification. Ozone (O3) and sulfuric
acid (H2SO4) are mixed with the pulp in a
pressurized reactor prior to pulp washing to provide up to 50 percent
removal of residual lignin. Like oxygen delignification, the process
also increases the solids content of the black liquor, making it
necessary that the recovery furnace handle the additional capacity.
Because ozone is unstable and corrosive, it must be generated on site,
and pH and temperature of the cook as well as pulp washing must be
carefully controlled and monitored. |
Ozone is
less selective in solubilization of lignin than oxygen or kraft pulping
chemicals; thus, this process results in loss of pulp yield and
strength. Generation of ozone is energy intensive, and cooling water is
needed to absorb heat from the strongly exothermic reaction between the
ozone and the pulp. The equipment used for ozone delignification is
similar to that used for oxygen delignification, and capital and
operating costs are similar.
|
Chemical
catalysts for delignification: anthraquinone |
Addition of
anthraquinone to kraft cooking liquor has been shown to provide extended
delignification without reducing pulp quality. Pulp yield can also
increase by as much as 2 percent, which raises the mill's pulp
productivity rate. Pulp treated with anthraquinone can be cooked at a
lower temperature, which decreases energy use requirements. |
The cost of
the addition of anthraquinone to pulping liquor is partially offset by
increased yield, reduced bleach chemical consumption, and reduced costs
of effluent treatment. |
Chemical
catalysts for delignification: polysulfide |
Addition of
polysulfide to the kraft cooking liquor provides many of the same
benefits as anthraquinone, including increase in pulp yield.
|
The heating
value of the black liquor solids is reduced by using this chemical, and
pulp strength also decreases. The process typically requires
installation of oxidation equipment for the white liquor used in kraft
pulping. Addition of polysulfides is a viable option for mills
considering upgrading to an extended cooking process, because the
increased solids loading to the recovery furnace caused by extended
cooking is offset by the decrease in heating value of the black liquor
solids, making it possible to increase delignification of pulp without
having to upgrade liquor recovery. |
Chemical
catalysts for delignification: mix of anthraquinone and polysulfide |
The use of a
mix of anthraquinone and polysulfide in the cooking liquor has been
demonstrated to provide not only extended delignification but also to
increase pulp yield higher than that achieved by either of the two
chemicals used alone. |
The
mechanism responsible for this incremental increase in yield is not
clear; results of testing have been mixed. Dosages and optimal mix
"recipe" have not yet been clearly defined. Research in this area is
ongoing. |
4.4 Alternative Pulping Technologies
Description. Several chemical pulping methods that do not use
conventional cooking chemicals have been developed by industry and research
institutions. Table 8 provides a description of these methods.
Benefits. The primary impetus for this research is to eliminate the
use of sulfur compounds in pulping, which reduces or eliminates air
emissions of sulfur compounds and helps avoid nuisance odors caused by the
presence of sulfur. Some of these processes are also less energy-intensive
than traditional pulping techniques.
Status of Use in the United States. Most of these techniques are
still being researched and are not yet economically feasible or
technologically ready for full-scale implementation. As research continues,
these methods may become more favorable for implementation.
Table 8: Description of Alternative
Pulping Technologies |
Process |
Description |
Comments |
Acetic
acid-based pulping |
Acetic acid
is used to pulp wood chips at pressures typically lower than those used
for traditional kraft pulping. This method produces pulps that are
similar in strength and yield to those made using other chemical pulping
processes. Acid can be recovered from the process via distillation. |
Distillation
is energy-intensive. Also, acid losses through the process, despite
recovery efforts, can be substantial, resulting in costly chemical
purchases. |
Organosolv
pulping |
Organic
chemicals, including alcohol, ethanol, and methanol, are used to pulp
wood. There are several proprietary pulping methods that use these
chemicals. Chemicals can be recovered and reused. |
Because the
chemicals used are volatile, pulping processes must be sealed and
spill-proof because of health risks due to worker exposure. Spills can
also be a fire and explosive hazard. Some pulps made from hardwood are
less strong when pulped with organic chemicals. The process may be most
economical for small-scale mills. |
Biopulping |
Microorganisms such as fungi or xylanases are used to pulp wood (or
nonwood) fibers. Use of microorganisms has been found to maintain pulp
yield and strength and to decrease the energy requirements per unit of
pulp produced. |
The
cost-effectiveness of this process is severely restrained by the slow
rate of delignification achieved, compared to traditional pulping
processes. This technique may be most appropriate for pulping of nonwood
fibers. |
4.5 Use of Nonwood Fiber Sources
Description. Many nonwood
plants and grasses can be used as a fiber source for papermaking. By a wide
margin, the most common nonwood fiber used for papermaking is straw,
followed by bagasse, bamboo, and kenaf. Nonwood fiber can be used in
addition to or in place of wood fiber in papermaking. Each nonwood fiber
source is pulped in a manner specific to its composition. Spent liquor
generated from pulping of nonwood fibers is similar in composition to wood
pulp but often contains a high silica content. Silica must be removed during
liquor recovery because it would form a glassy residue on the interior of
the recovery furnace. Fluidized-bed furnaces may be used to recover liquor
from nonwood pulping in place of a conventional recovery furnace. They are
less costly than conventional recovery furnaces, but less efficient because
their operation requires the use of a greater amount of "external" energy
than a conventional furnace; thus, the tradeoffs in energy consumption and
performance between these two recovery systems must be considered when
making purchasing decisions.
Benefits. Proponents of nonwood-fiber papermaking contend that
nonwood sources are more easily renewable than forests and that nonwood-fiber
manufacturing processes have fewer and less harmful environmental impacts
than those for wood fiber papermaking.
Status of Use in the United States. Research in nonwood fiber pulping
(particularly with kenaf) is ongoing in the United States. Wood and
secondary fiber, however, are expected to remain as the dominant fiber
sources within the U.S. industry because of their abundance and high quality
domestically. The United States thus has relatively limited experience with
processes and technologies for nonwood pulping on a large-scale basis.
4.6 Black Liquor Gasification
Description. Black liquor gasification is being researched as an
alternative technology to a conventional kraft recovery furnace.
Gasification is used to recover the energy and the chemicals in the black
liquor solids generated during kraft pulping. Instead of direct burning of
the solids, the volatile components of the black liquor are gasified. Sodium
is recovered from the black liquor at the gasifier, whereas sulfur is
recovered when the product gas is cleaned using a scrubber. The sodium and
sulfur are then processed to regenerate the kraft pulping chemicals. The
cleaned product gas stream is used to power a turbine or combined-cycle gas
and steam turbine to generate heat and energy for the mill's use.
Gasification systems have on average smaller capacities than traditional
recovery furnaces. The use of multiple gasifiers would probably be required
to match the energy and production needs for larger mills.
Benefits. Proponents of this technology assert that black liquor
gasification used in conjunction with gas turbine cogeneration systems has
the following advantages over traditional recovery furnaces:
- Higher overall energy efficiency
- Lower volume of gas requiring treatment
- Lower emissions (both gaseous and
particulate)
- Higher inherent safety; no explosion
hazard posed by molten smelt, which is present in recovery furnaces
- Higher adaptability to handling
variations in liquor capacity by using multiple gasifiers or by other
process modifications
Proponents also assert that gasification
will become economically competitive with traditional recovery furnaces in
the next few decades.
Status of Use in the United States. It is not yet cost-effective for
U.S. mills to implement full-scale black liquor gasification systems to
recover kraft process chemicals. Research on this technology is ongoing in
both the United States and in Europe, particularly Sweden.
4.7 Improved Sensors and Process Control
Description. Development of improved sensors and controls for pulp
and paper manufacturing processes is a research priority for the industry
worldwide. Of particular interest is control of ECF bleach plant operations.
The challenge for the bleach plant operator is to add the lowest volume of
bleaching chemicals necessary at the right location(s) in the bleaching
tower and between stages to achieve target pulp brightness. To control
bleach plant operations properly, parameters such as pulp brightness,
bleaching chemical concentration, and lignin content of the pulp (i.e.,
kappa number) should be measured both before and after bleaching to assess
the predicted versus actual effectiveness of bleaching, so that the operator
can make adjustments to bleach chemical addition in a timely manner.
Currently, few mills use sensors to measure pulp quality after bleaching;
rather, pulp samples are collected and analyzed in a separate laboratory,
which can take up to two hours to report information back to the operator.
By then, incoming pulp quality may have changed, and adjustments and
corrections based on this information might be inappropriate for new
conditions.
For application in an ECF bleach plant, process controls using "fuzzy logic"
appear to have an advantage over traditional control methods. "Fuzzy" theory
takes both human experiences and traditional controls into account in the
control solution and has proved effective for nonlinear systems in which
measurements and process variables are interdependent. ECF bleaching lends
itself well to "fuzzy" control schemes; results for one ECF bleach plant
showed that variations in pulp quality and brightness were lower for
operations using "fuzzy" controls versus traditional controls.
Benefits. Sensors and controls, if designed and positioned within the
manufacturing process properly, can help improve the environmental and
energy performance of existing and developing technologies used in the
industry, while also maintaining the performance specifications of the
finished product.
Status of Use in the United States. Most pulp and paper mills
currently use distributed control systems (DCS) for controlling operations.
Functions (e.g., opening or closing a valve or starting or stopping of a
motor) can be performed by an operator at a terminal, or controlled by an
algorithm that uses process information, including information from sensors.
Competition among manufacturers of DCS equipment is intense.
Controls employing "fuzzy logic," however,
are still in development for both ECF bleach plants and other industry
operations and there are few large-scale commercial installations at
existing mills.
4.8 Water Use Reduction and Closed
Bleach/Effluent Systems
Description. The global pulp and paper industry is faced with the
challenge of water-use reduction and, ultimately, elimination of effluent
altogether. Such mills are often referred to as "minimum impact mills." This
closed-loop approach is viewed as "next generation" mill technology, as
researchers develop efficient ways to reuse water and steam that are
currently treated and discharged to receiving waters or treatment works. As
a first step in closing the effluent system of a chemical pulp mill, the
industry is attempting to reduce or eliminate discharges from the bleach
plant, which is a primary focus of the environmental concerns for the
industry. Bleach plant effluent may be recovered jointly with black liquor
or in a separate recovery system for evaporation or steam generation.
Although mills will move toward closed-loop systems, material mass balances
still dictate that process residuals such as sludges will require management
and possibly off-site disposal or incineration. Makeup water may need to be
added to the process occasionally to account for evaporation, spills, leaks,
water bound in sludges and residuals, and other losses.
Benefits. Water use reduction or complete elimination of aqueous
discharges from the pulp and paper-manufacturing process would provide
obvious cost savings and environmental benefits. These benefits, however,
would need to be weighed against the costs of redesigning and operating an
effluent-free production process. Costs for new equipment, redesign,
retrofits, and construction would be offset to some degree by reduction or
elimination of wastewater treatment and off-site disposal of other process
wastes, but the degree to which these costs are offset is largely unknown at
this time.
Status of Use in the United States. There are no known totally closed
effluent plants operating in the United States, although a handful are
reportedly operating in Canada and Scandinavia. Research efforts in this
area are expected to be intensive in the next several years. A closed
effluent plant is technologically easier to achieve and more economically
feasible for mills that use mechanical or semichemical pulping methods
rather than chemical pulping. Mills that produce nonchemical pulps will thus
be the primary focus of this research and technology development.
5. FUTURE TRENDS
The U.S. pulp and paper industry has met with related trade organizations,
research institutions, and governmental agencies on an ongoing basis to
discuss the future of the industry from both an economic and environmental
standpoint. One outcome of these continuing collaborations is a document
that outlines a consensus perspective on the desired state of the industry
in 25 years, with an emphasis on technology-related issues, most of which
are environmental in nature. Agenda 2020 was published in November
1994 by the American Forest and Paper Association (AF&PA). The issues
identified in this document will require attention and collaborative
research among the industry, its suppliers, other institutions, and the
government to ensure the health of the industry in this time frame.
Agenda 2020 outlines the research objectives for the United States, as
agreed on by industry representatives and related trade and research
organizations with support from the U.S. Department of Energy (DOE). The six
topics on the research agenda are:
- Sustainable forest management.
Although trees are expected to dominate as a paper fiber source in the
United States, the growing and harvesting of substantially increased
yields from existing land resources without negative impacts on soil
stability, water quality, biodiversity, and indigenous wildlife habitats
will be necessary. The impacts of clear cutting and monocultures of
single-species, man-made plantations must also be recognized.
- Environmental performance.
Improved environmental compatibility of conventional and developing pulp
and papermaking processes is the focus of the research needs in this
category. Attention will be directed to the effects of those processes on
human health, energy/ environmental tradeoffs, and reduction of emissions
and effluent that have potentially harmful consequences. Complete closure
of the effluent system is a major goal for mills of the future.
- Energy performance.
Given the degree of energy intensity in the industry's fundamental
processes, research efforts will be directed to environmentally benign,
low-cost energy sources, including recovery and gasification of process
residues.
- Improved capital effectiveness.
The economically optimal size of a modern pulp and paper mill, combined
with the high cost of the favored kraft recovery process contribute to the
industry's standing as the most capital-intensive among manufacturing
industries.
- Recycling. Solid waste
reduction, improved fiber recovery systems, and enhanced development of
"urban forests" will continue to be priority environmental targets of the
U.S. industry.
- Sensors and controls. The
complexity of current processes and the need to comply with increasingly
stringent operating and environmental permits call for maximum efficiency
through the use of increasingly sophisticated, online measurement and
expert/control systems.
Other apparent trends within the U.S.
industry are the following:
- Implementation of the Cluster Rule will
act as a driver for technology implementation for ECF bleaching and for
extended delignification (using oxygen). ECF bleaching will likely emerge
as the preferred process over TCF bleaching or use of elemental chlorine.
- Research and progress will continue on
development of techniques to reduce or eliminate greatly water use and
process effluent from both bleach plant and whole-mill operations.
Historically, U.S. investments are driven by
cost-effectiveness, regulatory mandates, and consumer demand for
environmentally benign products. This trend is expected to continue as the
industry moves into the twenty-first century.
REFERENCES
American Forest & Paper Association. Agenda 2020: A Technology Vision and
Research Agenda for America's Forest, Paper, and Wood Industry (American
Forest & Paper Association, November 1994).
Atchison, Joseph E. "Twenty-five years of global progress in nonwood plant
fiber repulping," TAPPI Journal, 79, 10, pp. 87-95 (1996).
EPA. Handbook on Pollution Prevention Opportunities for Bleached Kraft
Pulp and Paper Mills, EPA/600/R-93/098 (Washington: EPA Office of
Research and Development, June 1993).
EPA. Profile of the Pulp and Paper Industry, EPA/310/R-95/015
(Washington: EPA Office of Compliance, September 1995).
Slinn, Ronald J. "The Potential Impacts on the U.S. Paper and Allied
Products Industry (SIC 26) of Increased Fuel Prices Resulting from Co-ordinated
Global Public Policy Commitments to Mitigate Green House Gas Emission"
(Washington, U.S. Department of Energy Argonne National Laboratory, 1996).
Smook, Gary A. Handbook for Pulp and Paper Technologists (Atlanta:
Technical Association of the Pulp and Paper Industry, 1992).
Springer, Allan M. Industrial Environmental Control: Pulp and Paper
Industry (Atlanta: Technical Association of the Pulp and Paper Industry,
1993).
Selected articles from:
- TAPPI Journal
- Pulp and Paper International
- Pulp & Paper
Selected publications of:
- Alliance for Environmental Technology (AET)
- American Forest & Paper Association
(AF&PA)
- American Paper Institute
- National Council of the Paper Industry
for Air and Stream Improvement (NCASI)
- Paper Industry Manufacturers
Association (PIMA)
- Technical Association of the Pulp and
Paper Industry (TAPPI).
|