Updated: April, 2004-
Raghavendra R. Hegde, Atul Dahiya, M. G. Kamath,
Olefin fiber is a manufactured fiber in which the fiber-forming substance is any long-chain synthetic polymer composed of at least 85% by weight of ethylene, propylene, or other olefin units. Olefin fiber is a generic description that covers thermoplastic fibers derived from olefins, predominately aliphatic hydrocarbons. Olefins are products of the polymerization of propylene and ethylene gases. Polypropylene (PP) and polyethylene (PE) are the two most common members of the family. Polypropylene is extremely versatile as a fiber-forming material, whereas polyethylene is not as good a fiber-forming high polymer material. Since its introduction into the textile industry in the 1950s, the list of successful products and markets for polypropylene fiber has increased exponentially [1]. Figure 1 shows the forecasted world consumption of nonwovens in millions of tons from 1998 to 2007[2].

Fig 1 Forecasted world consumption of Polypropylene in
Nonwovens in Millions of Tons till 1996-2007[2]
Of the polypropylene used in the
2.2 POLYMERIZATION PROCESS FOR LINEAR HDPE, MDPE,
LLDPE AND COPOLYMERS
2.3 POLYMERIZATION PROCESS FOR PP AND PROPYLENE
COPOLYMERS
All the above processes have been used in the
production of PP. The special process Technologies for PP and propylene
copolymers include two kinds of liquid pool slurry Process:
2.3 POLYMERIZATION PROCESS OF OTHER POLYOLEFINS
There are six important processing methods for
Polyolefins, these are:
A major virtue of polypropylene is its ability to be
used in a wide range of fibrous forms[3]. Fibrous forms of polypropylene
include staple, bicomponent staple, monofilament, multifilament, slit film
yarns, slit-fibrillated film yarns, spunbonds, melt blown nonwovens, synthetic
pulps, and extruded nettings. It can be made into ropes and cordage, primary
and secondary carpet backing, carpet face yarns, upholstery fabrics,
geotextiles, filtration materials, horticulture/agriculture materials,
automotive fabrics, spill-cleanup materials, disposable diapers,
hospital/medical care materials, and protective clothing. The melting point of
polypropylene (160-170°C) is an advantage in many nonwovens processing steps.
PP fiber can be softened sufficiently to bond to one another without destroying
fiber properties. Nonwoven fibers made from polypropylene can therefore be
fusion-bonded, eliminating the need for chemical binders. The benefits of this
technique include both energy saving and environmentally friendliness. Uses of
thermally bonded cover stock in baby diapers and similar products will result
in a markedly increased use of polypropylene. The fusion characteristics of
polypropylene are used not only to bond carded webs but also to improve the
dimensional stability of needle-bonded fabrics. A large amount of engineered
fabrics for road stabilization, dam and lake reinforcement, soil stabilization
and roofing are made from polypropylene fibers. Melt-blown fabrics are widely
used in filtration media, battery separators, etc. The relatively high melting
point allows PP nonwovens to be used up to the temperature of 120°C before
softening occurs. The soft hand and hydrophobic properties make PP nonwovens
particularly suitable for hygiene products, baby diapers and adult
incontinents. Spunbond and meltblown are the two main processes for
polypropylene nonwoven fabrication. Both techniques require PP resins with high
melting flow rate and relatively very narrow molecular weight distribution. The
fibers produced in spunbonded nonwovens are spun filaments, whose diameters are
in the range of 10-35 microns, whereas the fibers of meltblown nonwovens are
usually discontinuous and much finer, typically less than 10 microns. This
partially explains why meltblown webs are usually weaker than spunbonded webs.
Processability of a polymer is highly dependent on its rheological properties,
which have close relationship with its molecular weight, molecular weight
distribution, and temperature and shear rate. PP resins are generally
categorized according to their melt flow rates (MFR), which is the amount of
material that passes through a standard die hole for ten minutes. Polymers with
higher molecular weight have lower MFR and higher viscosity (under a given
temperature). Commercial polypropylene has a wide range of MFR from 0.25 to
1200. MFR is a very important parameter for both melt-blown and spunbond
processing. PP melts exhibit non-Newtonian viscosity, normal stress in shear
flow, excessive entrance and exit pressure drop, die swell, melt fracture and
draw resonance. PP melts are more viscoelastic than PET and nylon melts. The
flow pattern and stability of PP melts are highly dependent on the shear rate.
Above the critical shear rate, melt fracture may occur.
Processability of polypropylene fiber is also
influenced by the die geometry. The L/D ratio has to be optimized to reduce
instability and the effects of PP's high viscosity. Both melt fracture and draw
resonance represent instabilities in flow. Draw resonance is a periodic
variation in diameter of a spinning threadline above a critical draw-down
ratio. Slowing down the drawing operation or a suitable cooling procedure may
prevent this. In addition, processability of polypropylene fiber can also be
affected by other factors such as finishing. Finish oil is a mixture of several
chemicals that function as anti-static agent and lubricator to protect the
filament. The results of the effects of finishing on this area are not
available in this report yet. Since unmodified polypropylene is not dyeable,
pigmentation has become the preferred way of coloration in textile and
textile-related applications. Generally, the fastness properties of pigmented
fibers are superior to those of dyed fibers. Pigmented polypropylene fibers
have become established for contract carpets, indoor/outdoor carpeting,
synthetic turf, and other applications, in part because of their superior
fastness properties. Light stabilizers have helped to open new markets for
products intended for use outdoors, and improved heat stabilizers have boosted
extrusion efficiency and allowed use of more recycled material.
Polypropylene chips can be converted to fiber/filament
by traditional melt spinning, though the operating parameters need to be
adjusted depending on the final products. Spunbonded and melt blown processes
are also very important fiber producing techniques for nonwovens. As an
example, the staple fiber production is shown in Fig. 2.

Fig.2: Schematic diagram of staple fiber
production unit of PP.
Identifiers are shown with the figure. Additional comments and description are as
follows:
For more information about melt spinning processing,
reference 3 is recommended. The spunbonded and melt blown techniques will be
described in the following chapters.
6.1 FIBER STRUCTURE
Polypropylene fibers are composed of crystalline and
non-crystalline regions. The spherulites developed from a nucleus can range in
size from fractions of a micrometer to centimeters in diameter. The a-axis of
the crystal unit cell is aligned radially and the chain axis is homogeneously
distributed in planes perpendicular to this radial direction. Each crystal is
surrounded by non-crystalline material. Fiber spinning and drawing may cause
the orientation of both crystalline and amorphous regions. If the extension is
less than 0.5%, the spherulite deformation is elastic and no disruption of the
structure occurs, otherwise spherulites are highly oriented in the direction of
the force and finally are converted to microfibrils. These highly anisotropic
microfibrillar structures lead to anisotropic fiber properties.
6.2. CRYSTALLINITY OF PP FIBER
The degree of crystallinity of PP fiber is generally
between 50-65%, depending on processing conditions. Crystallization occurs
between glass transition temperature (Tg) and the equilibrium melting point
(Tm). The crystallization rate of PP is fast at low temperature. It is reported
[5] that the crystallization rate decreases with increasing crystallization
temperatures and also decreases with the increase of molecular weight as shown
in Fig 3. A paracrystalline structure with only 45% crystallinity resulting
from immediate quenching after extrusion was observed. A significantly higher
crystallinity of 62% was achieved when quenching further downstream of the die.
Although the drawing orients the crystallites, it also might decrease the
crystallinity as shown in Fig 4[5], which is different from that of PET and PAN
fibers.

Fig. 3: Relationship between rate of
crystallization and temperature for PP of various molecular weights [4].

Fig.4: Effect of draw ratio and draw
temperature on PP-fiber crystallinity: at draw temperature of 100°C; Ddraw ratio of 4:1[4]
The crystalline structure of PP has different forms, subject to its respective drawing condition, as shown in Fig 5. For example, the "alpha-form" is thermodynamically more stable and accordingly requires greater drawing force than the other two.

Heat setting removes the residual strains and
produces a defect-free and stable crystalline structure to make fiber/fabrics
dimensionally stable. It also improves the percentage of overall crystallinity.
The smectic structure changes to a more perfect monoclinic structure. During
the process of heat setting if the temperature is above 70°C. At 145°C the
conversion is almost complete. In comparison to the predominantly smectic form,
the monoclinic form does not experience any major change in crystalline
structure during the course of drawing and heat setting.
6.3. MECHANICAL PROPERTIES
The general physical properties of PP fibers are
shown in Table 1. Polypropylene fibers are produced in a variety of types with
different tenacities designed to suit varying market requirements. Fibers for
general textile uses have tenacities in the range of 4.5-6.0 g/den. High
tenacity yarns up to 9.0 g/den are produced for the use in ropes, nets and
other similar applications. High performance PP fibers have been made with high
strength and high modulus. The techniques include ultra-drawing[6], solid-state
extrusion[7] and crystal
surface growth[8]. The filaments with tenacities over 13.0 g/den can be made.
Table 1: Physical properties of Polypropylene
|
Moisture Regain |
< 0.1% |
|
Refractive Index |
1.49 |
|
Thermal Conductivity |
0.95Btu-in/ft |
|
Coefficient of linear
thermal expansion |
4.0x10 |
|
Heat of fusion |
21 cal/g |
|
Specific heat |
0.46 cal/g.c |
|
Density of Melt at 180°c |
0.769 g/cc |
|
Heat of Combustion |
19,400 Btu/lb |
|
Oxygen index |
17.4 |
|
Decomposition temperature
range |
328-410°C |
|
Dielectric constant (0.1
MHz) |
2.25 |
|
Dissipation factor (0.1
MHz) |
< 0.0002 |
|
Specific volume
resistively |
> 10 |
The degree of orientation
achieved by drawing influences the mechanical properties of PP filaments. The
greater the degree of stretch, the higher the tensile strength and the lower
the elongation as shown in Fig. 6. Commercial PP monofilaments have an
elongation-at-break in the range of 12-25%. Multifilaments and staple fibers
are in the range of 20-30% and 20-35%, respectively.

Fig.6: Relationship between mechanical property and stretching of PP fibers [11]
6.4. THERMAL PROPERTIES
Polypropylene fibers have a softening point in the
region of 150°C and a melting point at 160-170°C. At temperatures of -70°C or
lower, PP fibers retain their excellent flexibility. At higher temperature (but
below 120°C) PP fibers nearly remain their normal mechanical properties. PP
fibers have the lowest thermal conductivity of all commercial fibers. In this
respect, it is the warmest fiber of all. The thermal conductivity of common
textile fibers is shown in Table 2.
Table 2: Thermal Conductivity of textile
fibers
|
Material |
Thermal Conductivity |
|
Air |
1.0 |
|
PP |
6.0 |
|
Wool |
6.4 |
|
Acetate |
8.6 |
|
Viscose |
11 |
|
Cotton |
17.0 |
6.5. DYEABILITY
The dyeability of fibers is controlled by both
chemical and physical properties. Fibers that have polar functional groups in
their molecular repeat units can more easily be dyed. These polar groups may
serve as active sites for combination with dye molecules by chemical bonds.
Since PP molecular chains have no polar functional groups, the dye molecules
cannot be chemically attracted to the fibers. The dye molecules cannot even be
strongly adsorbed by the fiber surfaces because of their hydrophobic
properties. Therefore, these adsorbed molecules, which interact with the fiber
surface by weak van der Waal's force, are easily washed away. In addition, PP
fiber has relatively high crystallinity (50-65%), which partially attributes to
its very low dyeability.
Fiber modifications have been investigated to make
polypropylene dyeable this includes copolymerization to provide dyesites along
the macromolecular chain and blend with dyeable polymers. Baumann [9] has
reviewed the attempts by several researchers to improve polypropylene
dyeability. The method of grafting chloromethylstyrene has been introduced. In
addition, the method of blending a polyethyleneimine compound with
polypropylene was described briefly. Bromination of polypropylene fibers was
reported to give PP fibers an affinity for basic dyes [10]. These methods have,
owever, generally led to the significant decrease of the desirable physical
properties of polypropylene fibers.
In recent years, surface modification of hydrophobic
fibers by plasma treatment has opened up new possibilities in this field.
Functional groups can be introduced onto the surface of PP fibers by special
gas plasma treatment or plasma polymerization [11]. The polar layer on the
fiber surface improves the wettability and the affinity of the fiber surface
for water and water-soluble dye molecules. After reaction with the functional
groups, which are introduced by plasma treatment, dye molecules are fixed onto
the fiber surface. Because plasmas do not interact with the inner part of the
fiber, this technique may not greatly influence the mechanical properties of
the treated fiber [12]. Great progress in improving dyeability of PP nonwoven
webs had been made by the Textiles and Nonwovens development Center (TANDEC),
6.6. OTHER PROPERTIES OF PP
In general, PP fiber has excellent chemical
resistance to acids and alkalis, high abrasion resistance and resistance to
insects and pests. PP fiber is also easy to process and inexpensive compared to
other synthetic fibers. Its low moisture absorption helps aid the quick
transport of moisture.
6.7 DISADVANTAGES OF PP FIBERS
The main drawbacks of PP fibers are listed below:
Note: PP fiber has many useful textile properties;
however, one key disadvantage is that it is flammable. Topical FR treatments
have serious deficiencies, such as high add-on and limited durability. Dr.
David Buszard [13] (FMC) introduced Reoflam FG-372, a new phosphorus-bromine
based melt-processable flame retardant, stable at processing temperatures up to
230°C. It acts as a plasticier during fibre
spinning, because of a similar melting temperature. An add-on level of 3% to 8%
is required to meet the majority of textile flammability requirements. PP
fibers containing Reoflam FG-372 are already being used in automative
carpeting, where good light stability is also of importance.
Because of its superior
performance characteristics and comparatively low-cost, PP fiber finds
extensive use in the nonwovens industry. PP is a very important fiber in
nonwoven processing and dominates in many nonwoven markets. The main
application areas include: nonwoven fabrics (refer to Table 3), particularly
absorbent product coverstock markets, home furnishings and automotive markets.
Application
|
Fiber
Grade
|
Industry
|
Cigarette
Filter
|
Staple
fiber 3 denier
|
Cigarette
|
Technical
filters
|
Staple
fiber 5 dsenier, needle punched nonwoven
|
Wet
filteration, excellent, chemical resistance, used in water, milk, bear, paints,
coatings, petrochemicals,
Pharmaceuticals,
filtration
|
PP
woven socks
|
PP
film fiber, with 10-15% LDPE to reduce fibrillation and cost
|
Fertilizers,
flour, wheat, sugar, cement
|
Ropes
and Twines
|
PP
film and fiber
|
Agriculture
|
PP
bale warp
|
Spun
Bonded PP
|
Synthetic
fibers
|
PP
tapes
|
High
modulus PP obtained by increasing draw ratio
|
Construction
material like asphalt and concrete
|
PP
construction / industry fabrics
|
Filling
grade and staple fiber
|
Construction
materials like asphalt and concrete
|
Substrate
fabrics
|
Nonwoven
needle punched 3-4 denier staple fibers
|
Furniture
fabrics as backing material for visual furniture fabrics, it serves as
reinforcement. Also used for wall covering, luggage, table-clothes,
tarpaulins, and automobile
|
Outdoor
Applications
|
Heavy
deniers containing stabilizers, UV absorber, etc
|
Sports
|
Non-electric
fuses for initiating explosives
|
PP
slit film tapes
|
Mining
industry
|
Medical/Surgical
disposable fabric
|
PP staple fiber nonwovens, Face masks |
Hospital
|
Below are some major olefin fiber uses:
7.1 CARPET AND UPHOLSTERY
Since polypropylene became a commercially available
fiber more than 40 years ago, it has historically been a fiber for carpet and
upholstery. About 90% of all carpet backing and more than 25% of all carpet
face fiber is polypropylene [14]. In 1997 almost 3.8 billion pounds -
approximately 39 percent of all fibers shipped by domestic manufacturers - were
delivered to
Table 4: Polypropylene Staple Fiber Shipments
(millions of pounds)
|
|
1993 |
1994 |
1995 |
1996 |
1997 |
1998 |
|
Carpet-face yarns |
579.6 |
722.3 |
820.8 |
891.4 |
925.6 |
935 |
|
Carpet-backing yarns |
454 |
485.6 |
405.7 |
478.2 |
488.2 |
514 |
|
Broadwoven |
419.9 |
446.2 |
448 |
231.1 |
235.8 |
274 |
|
Narrow Wovens |
19.6 |
21.3 |
21.8 |
15.8 |
16.5 |
18 |
|
Rope/Cordage/Fishline |
113 |
114.1 |
121.6 |
118 |
111.4 |
130 |
|
Other |
45.4 |
48.7 |
61.8 |
197.8 |
239 |
240 |
|
Total |
1,631.5 |
1,838.2 |
1,879.7 |
1,932.3 |
2,016.5 |
2,111 |
Source: Fiber Economics Bureau and Author's
Estimates
Polypropylene BCF (bulked continuous filament) yarns
now account for almost 1 billion lbs/yr of the face fiber used in carpets and
rugs in the
7.2 ABSORBENT PRODUCTS (Diapers)
Absorbent products are very important in the
nonwovens business. Of the absorbent product applications, the baby diaper area
is the largest volume user, however, applications in adult incontinence currently
show the highest growth in recent years.
The major structural components of current diapers
are[16].
Secondary component materials are:
Current nonwoven materials used in topsheet
applications include spunbonded polypropylene (usually produced on a multibeam
system), SMS (spunbond/melt blown/spunbond) polypropylene composites and carded
polypropylene thermal bonds. In some applications, thermally bonded bicomponent
structures are being used.
Polypropylene spunbonded webs, treated to render
them hydrophilic (or partially treated to make them hydrophilic in zones) have
proved popular materials for coverstock applications, but they have not always
been rated as soft as other materials, i.e., staple fiber-based thermally
bonded polypropylene.
However, recent developments in polymer technology
with the availability of metallocene polypropylene would appear to provide a
route to improve the resultant web softness. Alternative web-forming
technologies, (such as those of Ason Engineering, Ft. Lauderdale, FL and Kobe,
Tokyo, Japan) with the capability to produce bicomponent and microdenier webs,
can now provide materials with better web formation, better softness and
improved strength, allowing a reduction in web weight and consequently the
possibility of a reduction in cost.
The nonwovens business in
Principal polypropylene applications for nonwovens
in automobiles are interior fabrics used in or on kick panel, package shelf,
seat construction, truck liners, load decks, cabin air filters etc [18].
REFERENCES
1. Richard G. Mansfield,
"Polypropylene in the Textile Industry", Plastics Engineering, June 1999, 30.
2. www.ifj.Com, "Man Made Fibers fuel for
Growth",P3.Issue Feb 2001.
3.
4. Gilmore, T.F. Danis, H.A.
and. Batra, S.K. " Thermal Bonding of Nonwoven Fabrics", Textile
Progress. 26(2), p24-32, (1995).
5.
6. Weeks, N.E. and Porter, P.S.
J. Polym. Sci, Phys Ed. 12, p635, (1974).
7. Jong G Lim,etal, " The
Potential for High Performance Fiber from Nylon 6", Prog. Polym. Sci. 14,
p 763-809, (1989).
8. Baumann,H.P., " The
Mechanism of dyeing polypropylene", American Dyestuff Reporter 79(1963)
527-529
9. Shah, C.D. & Jain, D.K.,
" Dyeing of modified polypropylene: cationic dyes on brominated
polypropylene" Textile Research Journal 54 (1984) 742-748
10. Shengmei Yuan and Roger E.
Marchant "Surface Modification of Polyethylene Film By Plasma
Polymerization and Subsequent Chemical Derivatization@ Plasma Deposition of
Polymeric Thin Films, John Wiley & Sons, 77-80 (1994)
11. Nam Sik Yoon and Yong Jin
Lim, Mitsuru Tahara, Toru Takashi, "Mechanical and Dyeing Properties of
Wool and Cotton Fabrics Treated with Low Temperature Plasma and Enzymes",
Textile Res. J. 66(5), 329 (1996).
12. Dr. Lado Benisek, "Burning
Issues", Textile Month", July 1999. 19-23
13. John W. Mc Curry,
"Polypropylene Propomemts See New Promise: Growth Markets for This Manmade
Fiber Include Geotextiles, Automotives, Homefurnishings and Apparel", Textile
World, June 1998, 30
14. John E. Luke, "Carpet's New
King",
15. Colin White, "Baby Diapers
and Training Pants", Nonwovens Industry, 30, Jan. 1999, 26-39.
16. Freddy Gustavo Rewald,
"Nonwovens in Automotive Uses", Nonwovens Industry, 30, March 1999.
17. "BBA Nonwovens" Nonwovens
Industry, 28, April 1997, 80.
Back to Table of contents
DEVELOPMENT OF METALLOCENE BASED POLYPROPYLENE
M. G. Kamath, Atul Dahiya, Raghavendra R. Hegde
In past decades, the use of polypropylene, has dominated in the production of melt blown and spunbonded nonwovens. The main reasons for the growing use of PP in polymer-laid nonwovens are that the raw materials are relatively inexpensive and available throughout the world, and PP resins can offer a relatively attractive cost combined with good value and ease of use when compared to conventional resins, such as polyester and polyamides. Continuing advances in PP fiber grade resins are strengthening the olefins price / properties ratio, which make them more suitable for polymer-laid nonwovens applications.
Polypropylene resins have been produced from Ziegler-Natta catalysts for over 30 years.
The drive for technology evolution has been the industry's desire to continuously improve control of the molecular architecture that leads to improved polymer performance.
In 1990's, the introduction of single site catalyst for making superior polyolefin resins set another technological trend, marked with Metallocene Catalysts having a precise control over molecular architecture for highly tailored polymers; improved processing; and properties for all polyolefins. This technology has been developed and designed for nonwoven applications [1]. The manufacturer may be able to take properties and very low extractables. Advantage of the higher barrier properties is to reduce basis weight or increase line speed. Because this material is so clean, the nonwoven manufacturer may be able to extend the intervals between die changes and process clean-ups. The absence of peroxide in this product leads to reduced viscosity variations and more consistent extrusion performance. Reduced process air rates are possible with this material, which can reduce energy costs. Due to these advantages, this innovative new melt blown material is expected to gain rapid acceptance in the nonwovens industry.
Metallocene catalysts offer unique advantages versus conventional catalysts. They allow producing consistent, controllable molecular structures that can be designed to:
2.1 Specialty of metallocene catalyst
In PP manufacturing, the monomers are reacted using a catalyst. All catalysts have reactive sites enabling them to perform their function, i.e. linking individual molecules of monomers to form a polymeric chain. Conventional catalysts have many reactive sites located randomly on the surface of the catalysts. This produces different and varying polymers (See fig-1 below). The new catalyst system, which is known as single site catalyst, also has many reactive sites, but all sites are identical. This in turn gives identical polymers and does away variability of polymers.

Fig. 1: Comparison of two types of catalysts [2]
3. Metallocene based PP NONWOVENS
Metallocene based PP resins for nonwovens and
fiber applications can help to produce polymers with very low catalyst residues
and very high purity. The polymer modification process, called controlled
rheology, enables us to tailor the resin for the specific need of nonwovens
applications. Advantages of the fiber grade metallocene based PP resin in
spunbonding and melt blowing over the conventional resin:
The primary feature that makes metallocene-catalyzed polymers preferable to conventional polymers is structural uniformity, which eliminates very low and high molecular weight polymer components present with conventional catalysts (Fig.2).


Fig. 2: Showing molecular weight distribution for various PP [3]
Table -1 Comparison of Metallocene
PP with Conventional PP
|
Product Attribute |
Metallocene |
Conventional PP |
|
Melting Point (°C) |
148 |
162 |
|
Flexural Modulus (MPa) |
1380 |
1360 |
|
MWD (Mw/Mn) |
2.0 |
3.5 / (2.8) * |
|
Recoverable Compliance |
0.4 |
3.5 / (0.9) * |

Fig. 3: Thermo mechanical analysis (TMA) of filaments from different PP [4]
'mPP' means
Metallocene PP,
'znPP' means Conventional PP

Fig. 4: Tensile strength comparison of filaments from different PP [4]
4. Applications
Presently, the metallocene based polyolefin polymers are produced by many companies in the world, but among those, BASF, Germany, and ExxonMobile Chemical Co., USA are the main producers of metallocene based PP. Exxon began development of Escorene Polypropylene grades used for nonwovens in 1960, and introduced AchieveTM propylene polymers based on Exxpol catalyst technology in 1995. This brought in overall property improvements versus conventional polypropylene yielding finer and stronger fibers at a lower production cost. Applications of Metallocene Polypropylene:
References
1. http://tancon.utk.edu/2003/Richeson.pdf
2.
Malkan,
'Advancements in Polyolefin Resins for Polymer-laid Nonwovens,' Hi-Per Fab'96
3.
D.
Permentier, C.Y. Cheng and G.A. Stahl, 'Metallocene Based Propylene Polymer for
Nonwoven Applications', Index 96 Congress Presentations, February 13-16, 1996.
4. Gajanan Bhat, "Structure Development in SBMB Process", PP Fiber Tech Conf. 2002