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PERP/PERP ABSTRACTS 2009
Nylon 6 and Nylon 6,6
Process Technology, Production
Costs, Regional Supply/Demand
Forecasts, and Economic Comparison
of Alternative Production Routes are
presented.
PERP07/08S6
Report Abstract
April 2009
Nylon 6 and Nylon 6,6
PERP07/08S6
Report Abstract
April 2009
www.chemsystems.com
The ChemSystems Process Evaluation/Research Planning (PERP) program is recognized globally as
the industry standard source for information relevant to the chemical process and refining industries.
PERP reports are available as a subscription program or on a report by report basis.
Nexant, Inc. (www.nexant.com) is a leading management consultancy to the global energy, chemical, and related industries. For over 38 years,
ChemSystems has helped clients increase business value through assistance in all aspects of business strategy, including business intelligence, project
feasibility and implementation, operational improvement, portfolio planning, and growth through M&A activities. Nexant has its main offices in
San Francisco (California), White Plains (New York), and London (UK), and satellite offices worldwide.
For further information about these reports, please contact the following:
New York, Dr. Jeffrey S. Plotkin, Vice President and Global Director, PERP Program, phone: + 1-914-609-0315, e-mail: jplotkin@nexant.com;
or Heidi Junker Coleman, Multi-client Programs Administrator, phone: + 1-914-609-0381, e-mail: hcoleman@nexant.com.
London, Dr. Alexander Coker, Senior Consultant, phone: + 44-(20)-709-1570, e-mail: acoker@nexant.com.
Bangkok, Maoliosa Denye, Marketing Manager, Energy & Chemicals Consulting: Asia, phone: + 66-2793-4612, e-mail: mdenye@nexant.com.
Website: www.chemsystems.com
Copyright © by Nexant Inc. 2009. All Rights Reserved.
www.chemsystems.com
CHEMSYSTEMS PERP PROGRAM
Report Abstract – Nylon 6 and Nylon 6,6 07/08S6
1
PERP ABSTRACTS 2009 00101.0008.4114
Nylon 6 and Nylon 6,6
INTRODUCTION
Polyamides or nylons are the first engineering plastics and still represent the biggest and most
important class of these types of material. The development of polyamide began with the first
publications describing polycondensation which is the basic principle of nylon synthesis in 1929.
The development of nylon production continued with the synthesis of poly (hexamethylene
adipamide), the original “nylon” which was conducted by Wallace H. Carothers in a DuPont
Laboratory in 1935. This invention resulted in the first patent for the production of synthetic
polyamides in 1937 and the subsequent commercial production of nylon 6,6 for toothbrush
filaments by DuPont in 1938. In 1941, DuPont introduced the first moldable nylon grades. The
other commercially important polyamide, nylon 6 based on caprolactam was first produced at
IG Farbenindustrie in Germany by P. Schlack in 1938 and the patent for nylon 6 was
subsequently issued in 1941. Although the large markets of polyamides were traditionally for
fiber applications, the use of polyamides as plastics grew gradually since the 1950s.
Polyamides comprise a wide range of materials, depending on the monomers employed.
Commonly used products are designated as nylon 6; 6,6; 6,12; 11 and 12 with the nomenclature
designating the number of carbon atoms that separate the repeating amide group. Nylon 6 and
nylon 6,6 continue to be the most popular types among polyamide commercial products, still
accounting for more than 90 percent of nylon used in the global market.
Two basic reactions are used to synthesize polyamide engineering polymers:
(1) polycondensation of a dibasic acid and a diamine or (2) polymerization of an amino acid or
lactam. The most widely used nylon polymers are semicrytalline products with molecular
weight of 10-40 thousand and chemical structures in which amide linkages connect aliphatic
chain segments.
Polyamides are a versatile family of thermoplastics that have a broad range of properties ranging
from relative flexibility to significant stiffness, strength, and toughness. Major properties such
as resistance to chemicals, toughness, thermal stability, good appearance, and good
processability are key considerations that make nylon suitable for engineering plastics
applications. Traditionally, the majority of nylon produced was used in the fiber application.
This consumption trend has changed substantially over the past decade with increasing
proportion of nylon going into the engineering thermoplastics market. This is due to the fact that
nylons have particular utility in performing mechanical duties that traditionally relied on metal
parts.
In terms of properties, nylon 6 and nylon 6,6 appear to be comparatively similar although
nylon 6 has better toughness and processability. On the other hand, nylon 6,6 has superior
mechanical properties and higher heat resistance. For engineering plastics, both nylon 6 and
nylon 6,6 can be used over an extensive range of applications including automotive, consumer,
industrial, electrical and electronics segments. Overall, automotive applications have been the
major driver for this positive growth in recent years in the trend towards replacing metal parts
with plastics, in order to reduce weight and costs as well as meet vehicle emission standards.
Nylon 6 and Nylon 6,6
www.chemsystems.com
CHEMSYSTEMS PERP PROGRAM
Report Abstract – Nylon 6 and Nylon 6,6 07/08S6
2
PERP ABSTRACTS 2009 00101.0008.4114
Market outlook for nylon 6 and nylon 6,6 varies extensively depending on domestic demand and
current market conditions in each country. Overall, developed markets of North America and
Europe will experience sluggish growth over the foreseeable future as a result of the global
economic downturn and movement of several manufacturing activities into lower-cost base
countries. One of Japan’s very mature markets (automotive industry) will likely suffer low
growth over the next coming years due to saturated market conditions and steady erosion of the
Japanese manufacturing base. China is expected to be one of the fastest growing countries for
ETP nylon, largely driven by phenomenal growth in the automotive and electrical/electronics
markets.
CHEMISTRY
Nylon 6 is the linear addition polymer of caprolactam (6-amino-caproic acid). The
polymerization process for nylon 6 can be batch or continuous, however, the state-of-the-art
process for its manufacture is continuous polymerization. Three reversible reactions, hydrolysis,
polycondensation, and polyaddition are the main steps in nylon 6 production. The overall
reaction is illustrated as follows:
The first step is a hydrolysis reaction to open the caprolactam ring, forming ε-aminocaproic acid:
This reaction proceeds in molten caprolactam in the presence of a small weight percent water.
Although the reaction will proceed with only caprolactam and water present, a material such as
phosphoric acid is added at low concentration to act as a chain stabilizer and help achieve the
desired final viscosity (molecular weight).
Polyaddition is the reaction which is mainly responsible for the growth of the linear polymer
chains. It is the most important reaction as soon as a certain amount of end groups has been
made available by the hydrolysis of caprolactam. Thus, final polymerization occurs by the
following caprolactam addition reaction:
Nylon 6 and Nylon 6,6
www.chemsystems.com
CHEMSYSTEMS PERP PROGRAM
Report Abstract – Nylon 6 and Nylon 6,6 07/08S6
3
PERP ABSTRACTS 2009 00101.0008.4114
The polymer dissolves in the unreacted caprolactam. The polymer end groups affect the stability
and final molecular weight of the polyamide. Organic acids (such as acetic acid) can be added as
chain stabilizers. Monofunctional organic amines can also be added.
The linear polymer chain formed in the polyaddition reaction can further increase its molecular
weight via a polycondensation reaction. The reactive end groups polycondensate forming linear
chain molecules and byproduct water. Thus, two linear chain molecules condense producing a
longer chain molecule with higher molecular weight. In other words, the polycondensation is
regarded as the most important reaction in the last phase of nylon 6 formation in which the
distribution of polymer chain lengths is adjusted. Caprolactam can also be polymerized in-situ in
a mold. A typical procedure uses the sodium salt of caprolactam as a catalyst. A brief
discussion of the raw materials – caprolactam, additives, initiators, catalysts, and chain
stabilizers and additional ingredients used during production of nylon 6 is given.
Nylon 6,6 chemistry and raw materials are also discussed.
PRODUCTION PROCESSES
Nylon 6 Batch & Continuous Processes
Commercially, the ring-opening polymerization of caprolactam to nylon 6 can be accomplished
by both hydrolytic and anionic mechanisms. However, nylon 6 is produced almost exclusively
by hydrolytic polymerization of caprolactam because it is easier to control and better adapted for
large-scale operation. The polymerization process for nylon via the hydrolytic mechanism can
be batch or continuous. The hydrolytic process for nylon 6 contains the following steps:
caprolactam and additives addition, hydrolysis, addition, condensation, pelletizing,
leaching/extraction of monomers, drying, and packaging.
Process flow diagrams and process descriptions for both the batch and continuous
process are given in the report.
Nylon 6,6 Batch Process
A batch nylon 6,6 process is described in this section and illustrated with a process flow
diagram.
Nylon 6,6 Continuous Process
To solve the limitations inherent in the batch process, the continuous polymerization process was
developed. The main steps of the continuous process include salt preparation, and
polymerization. Solid phase polymerization is an additional step used to increase molecular
weight of the polymer without damaging properties of the polymer.
Nylon 6 and Nylon 6,6
www.chemsystems.com
CHEMSYSTEMS PERP PROGRAM
Report Abstract – Nylon 6 and Nylon 6,6 07/08S6
4
PERP ABSTRACTS 2009 00101.0008.4114
A conceptual process design for the Salt Preparation process is schematically illustrated, coupled
with a brief description.
The concentrated nylon salt solution is pumped from storage into the first-stage polymerization
reactor, and this is schematically illustrated along with a brief description.
A brief description of solid-phase polymerization (SPP) is given.
CURRENT COMMERCIAL TECHNOLOGIES
This section reviews the technical features of modern commercial processes offered by the major
licensors of polyamide technology. In the polyamide market, most producers have developed
their own technology know-how and the advantage stay with the developers. DuPont, for
instance, has developed its own proprietary technology. The basic production steps in
manufacturing nylon have not changed significantly through the years and several technology
holders generally hold similar production features for most commercially produced nylon: nylon
6 and nylon 6,6. Manufacturing technology, however, has improved from year to year in terms
of production efficiency, reduction in utility requirement, special features in reactor design to
improve quality and to minimize raw material. Major commercial licensors for polymer
production process includes Zimmer AG and Uhde Inventa-Fischer.
Lurgi Zimmer Gmbh process flow diagram and process description are given.
Uhde Inventa-Fischer process is described along with schematic illustrations.
TECHNOLOGY DEVELOPMENTS
Nylon 6 and nylon 6,6 have been commercially produced for almost seventy years. The
technology for producing nylon today is considered to be mature. However, every one of the
many steps used in nylon production has been the subject of numerous improvements over the
years and important developments are constantly being made with respect to process and
equipment design and catalysts improvements.
The technology developments for nylon 6 continuous productions have been focused on further
process advancements and cost reduction if a way can be found to avoid the lactam wash
extraction step.
Other trends in technology can be characterized as evolutionary – there does not appear to be a
revolutionary advance on the horizon. Areas where design improvements are being sought with
the existing continuous processes are improvements in energy utilization, improvements in
quality, increases in scale, and further improvements in capital utilization. The advances in
technology and engineering of polyamide products will lead to the development of differentiated
new products, offering valuable solutions in existing and new markets.
Most commercial improvements and developments for nylon production are generally treated as
confidential information. This technology section reviews recent published patents on process
improvements, new production technologies, new methods of recycling raw materials, and many
more. However, it is not known if these patents will be effectively applied in a commercial scale
production or not.
Nylon 6 and Nylon 6,6
www.chemsystems.com
CHEMSYSTEMS PERP PROGRAM
Report Abstract – Nylon 6 and Nylon 6,6 07/08S6
5
PERP ABSTRACTS 2009 00101.0008.4114
PRODUCT AND END-USE
Resins and Compounds
The usefulness of nylons rests upon their combination of properties and their susceptibility to
modification. The key properties of nylon include resistance to oil and solvents, toughness,
fatigue and abrasion resistance, low friction and creep resistance, high tensile strength, thermal
stability, fire resistance, drawability, good appearance and good processability.
Resins properties and additives and fillers are discussed; recycling, storage, and
compounding are mentioned in brief.
Fabrication Methods
Processability is another advantage that nylon has over thermosets and other engineering
plastics. Nylon can be processed via a variety of techniques including injection molding,
extrusion, blow molding, monomer casting, solution coating, fluidized-bed or electrostatic
coating, or forming. The large proportion of nylon is processed by injection molding, extrusion
and blow molding.
Injection Molding and Extrusion are briefly discussed; Blow Molding, Rotomolding,
Reaction Injection Molding, Assembly Techniques are also mentioned in brief.
Nylon Major Markets
Polyamide 6 and 6,6 are highly versatile materials that are consumed in a host of applications
including fibers, films, and molded articles. This section in the report focuses only on the
technical, or engineering polymer applications of polyamide 6 and 6,6.
Automotive, electronics and electrical, consumer & other applications are briefly
discussed; new developments in Nylon 6 and 6,6 products are mentioned in brief.
ECONOMIC ANALYSIS
Costs of production estimates for the following have been developed:
Production of Nylon 6 via batch process
Production of Nylon 6,6 via batch process
Production of Nylon 6 via continuous process
Production of Nylon 6,6 via continuous process
In the petrochemical industry, feedstock integration is an important consideration in assessing
the competitive position of participants in a given value chain. This is true, even though there is
still a high-value added component to compounded nylon resin selling prices. With a number of
alternative routes to caprolactam and HMDA production under development, an understanding
of the potential impact of alternative pricing for these raw materials is important.
To test the effect of alternative caprolactam or HMDA prices on nylon 6 and nylon 6,6
production costs, sensitivities have been prepared that looked at these raw materials at alternative
prices. Also, a sensitivity analysis was performed to test the impact of larger sized lines on the
economics of continuous units.
Nylon 6 and Nylon 6,6
www.chemsystems.com
CHEMSYSTEMS PERP PROGRAM
Report Abstract – Nylon 6 and Nylon 6,6 07/08S6
6
PERP ABSTRACTS 2009 00101.0008.4114
MARKET ANALYSIS
Nylon was introduced to the market in the 1940s as the first synthetic fiber. From the 1950s
onwards, nylon demand for resin has steadily grown accounting for 38 percent of the global
demand for nylon nowadays (as shown in the Figure below). Among most types of polyamide,
approximately 85-90 percent of nylon in the global market are nylon 6 and nylon 6,6.
Global Nylon Consumption by End-Use
(6.7 million tons)
Fiber
62%
Extrusion Resin
8%
Injection Molding
Resin
30%
Q109_00101.0008.4114_chart s.xls F8.9
Supply and demand for North America, Europe Japan, and China are discussed.
Nylon 6 and Nylon 6,6 engineering thermoplastics demand by end use for 2005-2007,
estimate for 2008 and forecast to 2012 is given for each of the regions above.
Production capacity for individual plants are given for each region cited above (tables list
company, location, capacity and type of nylon produced).
www.chemsystems.com
Nexant, Inc.
San Francisco
London
Tokyo
Bangkok
New York
Washington
Houston
Phoenix
Madison
Boulder
Dusseldorf
Beijing
Shanghai
Paris

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Nylon 6 and 6,6 Report Abstract

  • 1. PERP/PERP ABSTRACTS 2009 Nylon 6 and Nylon 6,6 Process Technology, Production Costs, Regional Supply/Demand Forecasts, and Economic Comparison of Alternative Production Routes are presented. PERP07/08S6 Report Abstract April 2009
  • 2. Nylon 6 and Nylon 6,6 PERP07/08S6 Report Abstract April 2009 www.chemsystems.com The ChemSystems Process Evaluation/Research Planning (PERP) program is recognized globally as the industry standard source for information relevant to the chemical process and refining industries. PERP reports are available as a subscription program or on a report by report basis. Nexant, Inc. (www.nexant.com) is a leading management consultancy to the global energy, chemical, and related industries. For over 38 years, ChemSystems has helped clients increase business value through assistance in all aspects of business strategy, including business intelligence, project feasibility and implementation, operational improvement, portfolio planning, and growth through M&A activities. Nexant has its main offices in San Francisco (California), White Plains (New York), and London (UK), and satellite offices worldwide. For further information about these reports, please contact the following: New York, Dr. Jeffrey S. Plotkin, Vice President and Global Director, PERP Program, phone: + 1-914-609-0315, e-mail: jplotkin@nexant.com; or Heidi Junker Coleman, Multi-client Programs Administrator, phone: + 1-914-609-0381, e-mail: hcoleman@nexant.com. London, Dr. Alexander Coker, Senior Consultant, phone: + 44-(20)-709-1570, e-mail: acoker@nexant.com. Bangkok, Maoliosa Denye, Marketing Manager, Energy & Chemicals Consulting: Asia, phone: + 66-2793-4612, e-mail: mdenye@nexant.com. Website: www.chemsystems.com Copyright © by Nexant Inc. 2009. All Rights Reserved.
  • 3. www.chemsystems.com CHEMSYSTEMS PERP PROGRAM Report Abstract – Nylon 6 and Nylon 6,6 07/08S6 1 PERP ABSTRACTS 2009 00101.0008.4114 Nylon 6 and Nylon 6,6 INTRODUCTION Polyamides or nylons are the first engineering plastics and still represent the biggest and most important class of these types of material. The development of polyamide began with the first publications describing polycondensation which is the basic principle of nylon synthesis in 1929. The development of nylon production continued with the synthesis of poly (hexamethylene adipamide), the original “nylon” which was conducted by Wallace H. Carothers in a DuPont Laboratory in 1935. This invention resulted in the first patent for the production of synthetic polyamides in 1937 and the subsequent commercial production of nylon 6,6 for toothbrush filaments by DuPont in 1938. In 1941, DuPont introduced the first moldable nylon grades. The other commercially important polyamide, nylon 6 based on caprolactam was first produced at IG Farbenindustrie in Germany by P. Schlack in 1938 and the patent for nylon 6 was subsequently issued in 1941. Although the large markets of polyamides were traditionally for fiber applications, the use of polyamides as plastics grew gradually since the 1950s. Polyamides comprise a wide range of materials, depending on the monomers employed. Commonly used products are designated as nylon 6; 6,6; 6,12; 11 and 12 with the nomenclature designating the number of carbon atoms that separate the repeating amide group. Nylon 6 and nylon 6,6 continue to be the most popular types among polyamide commercial products, still accounting for more than 90 percent of nylon used in the global market. Two basic reactions are used to synthesize polyamide engineering polymers: (1) polycondensation of a dibasic acid and a diamine or (2) polymerization of an amino acid or lactam. The most widely used nylon polymers are semicrytalline products with molecular weight of 10-40 thousand and chemical structures in which amide linkages connect aliphatic chain segments. Polyamides are a versatile family of thermoplastics that have a broad range of properties ranging from relative flexibility to significant stiffness, strength, and toughness. Major properties such as resistance to chemicals, toughness, thermal stability, good appearance, and good processability are key considerations that make nylon suitable for engineering plastics applications. Traditionally, the majority of nylon produced was used in the fiber application. This consumption trend has changed substantially over the past decade with increasing proportion of nylon going into the engineering thermoplastics market. This is due to the fact that nylons have particular utility in performing mechanical duties that traditionally relied on metal parts. In terms of properties, nylon 6 and nylon 6,6 appear to be comparatively similar although nylon 6 has better toughness and processability. On the other hand, nylon 6,6 has superior mechanical properties and higher heat resistance. For engineering plastics, both nylon 6 and nylon 6,6 can be used over an extensive range of applications including automotive, consumer, industrial, electrical and electronics segments. Overall, automotive applications have been the major driver for this positive growth in recent years in the trend towards replacing metal parts with plastics, in order to reduce weight and costs as well as meet vehicle emission standards.
  • 4. Nylon 6 and Nylon 6,6 www.chemsystems.com CHEMSYSTEMS PERP PROGRAM Report Abstract – Nylon 6 and Nylon 6,6 07/08S6 2 PERP ABSTRACTS 2009 00101.0008.4114 Market outlook for nylon 6 and nylon 6,6 varies extensively depending on domestic demand and current market conditions in each country. Overall, developed markets of North America and Europe will experience sluggish growth over the foreseeable future as a result of the global economic downturn and movement of several manufacturing activities into lower-cost base countries. One of Japan’s very mature markets (automotive industry) will likely suffer low growth over the next coming years due to saturated market conditions and steady erosion of the Japanese manufacturing base. China is expected to be one of the fastest growing countries for ETP nylon, largely driven by phenomenal growth in the automotive and electrical/electronics markets. CHEMISTRY Nylon 6 is the linear addition polymer of caprolactam (6-amino-caproic acid). The polymerization process for nylon 6 can be batch or continuous, however, the state-of-the-art process for its manufacture is continuous polymerization. Three reversible reactions, hydrolysis, polycondensation, and polyaddition are the main steps in nylon 6 production. The overall reaction is illustrated as follows: The first step is a hydrolysis reaction to open the caprolactam ring, forming ε-aminocaproic acid: This reaction proceeds in molten caprolactam in the presence of a small weight percent water. Although the reaction will proceed with only caprolactam and water present, a material such as phosphoric acid is added at low concentration to act as a chain stabilizer and help achieve the desired final viscosity (molecular weight). Polyaddition is the reaction which is mainly responsible for the growth of the linear polymer chains. It is the most important reaction as soon as a certain amount of end groups has been made available by the hydrolysis of caprolactam. Thus, final polymerization occurs by the following caprolactam addition reaction:
  • 5. Nylon 6 and Nylon 6,6 www.chemsystems.com CHEMSYSTEMS PERP PROGRAM Report Abstract – Nylon 6 and Nylon 6,6 07/08S6 3 PERP ABSTRACTS 2009 00101.0008.4114 The polymer dissolves in the unreacted caprolactam. The polymer end groups affect the stability and final molecular weight of the polyamide. Organic acids (such as acetic acid) can be added as chain stabilizers. Monofunctional organic amines can also be added. The linear polymer chain formed in the polyaddition reaction can further increase its molecular weight via a polycondensation reaction. The reactive end groups polycondensate forming linear chain molecules and byproduct water. Thus, two linear chain molecules condense producing a longer chain molecule with higher molecular weight. In other words, the polycondensation is regarded as the most important reaction in the last phase of nylon 6 formation in which the distribution of polymer chain lengths is adjusted. Caprolactam can also be polymerized in-situ in a mold. A typical procedure uses the sodium salt of caprolactam as a catalyst. A brief discussion of the raw materials – caprolactam, additives, initiators, catalysts, and chain stabilizers and additional ingredients used during production of nylon 6 is given. Nylon 6,6 chemistry and raw materials are also discussed. PRODUCTION PROCESSES Nylon 6 Batch & Continuous Processes Commercially, the ring-opening polymerization of caprolactam to nylon 6 can be accomplished by both hydrolytic and anionic mechanisms. However, nylon 6 is produced almost exclusively by hydrolytic polymerization of caprolactam because it is easier to control and better adapted for large-scale operation. The polymerization process for nylon via the hydrolytic mechanism can be batch or continuous. The hydrolytic process for nylon 6 contains the following steps: caprolactam and additives addition, hydrolysis, addition, condensation, pelletizing, leaching/extraction of monomers, drying, and packaging. Process flow diagrams and process descriptions for both the batch and continuous process are given in the report. Nylon 6,6 Batch Process A batch nylon 6,6 process is described in this section and illustrated with a process flow diagram. Nylon 6,6 Continuous Process To solve the limitations inherent in the batch process, the continuous polymerization process was developed. The main steps of the continuous process include salt preparation, and polymerization. Solid phase polymerization is an additional step used to increase molecular weight of the polymer without damaging properties of the polymer.
  • 6. Nylon 6 and Nylon 6,6 www.chemsystems.com CHEMSYSTEMS PERP PROGRAM Report Abstract – Nylon 6 and Nylon 6,6 07/08S6 4 PERP ABSTRACTS 2009 00101.0008.4114 A conceptual process design for the Salt Preparation process is schematically illustrated, coupled with a brief description. The concentrated nylon salt solution is pumped from storage into the first-stage polymerization reactor, and this is schematically illustrated along with a brief description. A brief description of solid-phase polymerization (SPP) is given. CURRENT COMMERCIAL TECHNOLOGIES This section reviews the technical features of modern commercial processes offered by the major licensors of polyamide technology. In the polyamide market, most producers have developed their own technology know-how and the advantage stay with the developers. DuPont, for instance, has developed its own proprietary technology. The basic production steps in manufacturing nylon have not changed significantly through the years and several technology holders generally hold similar production features for most commercially produced nylon: nylon 6 and nylon 6,6. Manufacturing technology, however, has improved from year to year in terms of production efficiency, reduction in utility requirement, special features in reactor design to improve quality and to minimize raw material. Major commercial licensors for polymer production process includes Zimmer AG and Uhde Inventa-Fischer. Lurgi Zimmer Gmbh process flow diagram and process description are given. Uhde Inventa-Fischer process is described along with schematic illustrations. TECHNOLOGY DEVELOPMENTS Nylon 6 and nylon 6,6 have been commercially produced for almost seventy years. The technology for producing nylon today is considered to be mature. However, every one of the many steps used in nylon production has been the subject of numerous improvements over the years and important developments are constantly being made with respect to process and equipment design and catalysts improvements. The technology developments for nylon 6 continuous productions have been focused on further process advancements and cost reduction if a way can be found to avoid the lactam wash extraction step. Other trends in technology can be characterized as evolutionary – there does not appear to be a revolutionary advance on the horizon. Areas where design improvements are being sought with the existing continuous processes are improvements in energy utilization, improvements in quality, increases in scale, and further improvements in capital utilization. The advances in technology and engineering of polyamide products will lead to the development of differentiated new products, offering valuable solutions in existing and new markets. Most commercial improvements and developments for nylon production are generally treated as confidential information. This technology section reviews recent published patents on process improvements, new production technologies, new methods of recycling raw materials, and many more. However, it is not known if these patents will be effectively applied in a commercial scale production or not.
  • 7. Nylon 6 and Nylon 6,6 www.chemsystems.com CHEMSYSTEMS PERP PROGRAM Report Abstract – Nylon 6 and Nylon 6,6 07/08S6 5 PERP ABSTRACTS 2009 00101.0008.4114 PRODUCT AND END-USE Resins and Compounds The usefulness of nylons rests upon their combination of properties and their susceptibility to modification. The key properties of nylon include resistance to oil and solvents, toughness, fatigue and abrasion resistance, low friction and creep resistance, high tensile strength, thermal stability, fire resistance, drawability, good appearance and good processability. Resins properties and additives and fillers are discussed; recycling, storage, and compounding are mentioned in brief. Fabrication Methods Processability is another advantage that nylon has over thermosets and other engineering plastics. Nylon can be processed via a variety of techniques including injection molding, extrusion, blow molding, monomer casting, solution coating, fluidized-bed or electrostatic coating, or forming. The large proportion of nylon is processed by injection molding, extrusion and blow molding. Injection Molding and Extrusion are briefly discussed; Blow Molding, Rotomolding, Reaction Injection Molding, Assembly Techniques are also mentioned in brief. Nylon Major Markets Polyamide 6 and 6,6 are highly versatile materials that are consumed in a host of applications including fibers, films, and molded articles. This section in the report focuses only on the technical, or engineering polymer applications of polyamide 6 and 6,6. Automotive, electronics and electrical, consumer & other applications are briefly discussed; new developments in Nylon 6 and 6,6 products are mentioned in brief. ECONOMIC ANALYSIS Costs of production estimates for the following have been developed: Production of Nylon 6 via batch process Production of Nylon 6,6 via batch process Production of Nylon 6 via continuous process Production of Nylon 6,6 via continuous process In the petrochemical industry, feedstock integration is an important consideration in assessing the competitive position of participants in a given value chain. This is true, even though there is still a high-value added component to compounded nylon resin selling prices. With a number of alternative routes to caprolactam and HMDA production under development, an understanding of the potential impact of alternative pricing for these raw materials is important. To test the effect of alternative caprolactam or HMDA prices on nylon 6 and nylon 6,6 production costs, sensitivities have been prepared that looked at these raw materials at alternative prices. Also, a sensitivity analysis was performed to test the impact of larger sized lines on the economics of continuous units.
  • 8. Nylon 6 and Nylon 6,6 www.chemsystems.com CHEMSYSTEMS PERP PROGRAM Report Abstract – Nylon 6 and Nylon 6,6 07/08S6 6 PERP ABSTRACTS 2009 00101.0008.4114 MARKET ANALYSIS Nylon was introduced to the market in the 1940s as the first synthetic fiber. From the 1950s onwards, nylon demand for resin has steadily grown accounting for 38 percent of the global demand for nylon nowadays (as shown in the Figure below). Among most types of polyamide, approximately 85-90 percent of nylon in the global market are nylon 6 and nylon 6,6. Global Nylon Consumption by End-Use (6.7 million tons) Fiber 62% Extrusion Resin 8% Injection Molding Resin 30% Q109_00101.0008.4114_chart s.xls F8.9 Supply and demand for North America, Europe Japan, and China are discussed. Nylon 6 and Nylon 6,6 engineering thermoplastics demand by end use for 2005-2007, estimate for 2008 and forecast to 2012 is given for each of the regions above. Production capacity for individual plants are given for each region cited above (tables list company, location, capacity and type of nylon produced).
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