English
Technology
Spheripol Process and Services Production of PP Homopolymer, random copolymer, heterophasic impact copolymer
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A True Polyolefin Perspective
1. An Introduction to Basell Basell is the world’s largest
• Advanced Polyolefins Business,
producer of polypropylene and
which consists of polypropylene
advanced polyolefins products, a
compounds and other specialty
leading supplier of polyethylene
products, and
and catalysts, and a global leader in the development and licensing
• Polyolefins Business, which
of polypropylene and polyethylene
comprises polypropylene and
processes.
polyethylene.
Basell, together with its joint ventures,
Basell has its corporate centre in The
has manufacturing facilities around
Netherlands and has regional offices
the world and sells products in
in Belgium, Germany, the United
more than than 120 countries. With
States, Brazil and Hong Kong, as well
research and development activities
as sales offices in the major markets
in Europe, North America and
around the globe.
the Asia-Pacific region, Basell is continuing a technological heritage
For further information on Basell,
that dates back to the beginning of
please see separate leaflets in the
the polyolefins industry. Basell is
pocket-page in the back of this
committed to innovation both through
brochure or visit the company’s
improvements of its processes
web site: www.basell.com.
and a continuous extension of the properties of its polyolefins portfolio. The company is organised in three businesses: • Technology Business, which includes licensing, catalysts development and sales, R&D and new projects;
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Your Partner in the World of Polyolefins Technology
2.1 Leading the Technology Race The history of Basell and its prede-
and cost-effective solutions that
cessors is one of continuing achieve-
meet the changing requirements of
ments and breakthroughs in cata-
our customers.
lysts, process and product developments in the field of polyolefins.
Thanks to the close integration between our marketing, R&D and man-
It began with the discoveries in poly-
ufacturing, new developments of cat-
olefins technology and catalysts by
alysts, processes and products are al-
Karl Ziegler and Giulio Natta, reward-
ways focused on meeting market de-
ed with the Nobel Prize in 1963, and
mands and commercialised quickly
has continued through five revolu-
in a responsible manner.
tionary generations of Ziegler Ziegler-Natta -Natta catalysts to the development of a new metallocene-based polypropylene catalyst family and products. From the first industrial polypropylene and polyethylene processes to our latest multi-zone circulating reactor developments, Basell and its predecessors have delivered stateof-the-art polyolefin catalysts, technologies, and products to customers world-wide. For us, creating innovative polyolefin products is a way of life, delivering both superior performances
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2.2 A Licensing Portfolio for Any Producer’s Needs Basell is the only licensor offering
❏
Spherilene, the dual reactors swing
process technologies for production
gasphase process technology for
of all PP and PE product families. Our
the production of LLDPE and HDPE
technologies are some of the most
❏
Lupotech G, the fluidised bed gas-
reliable, efficient and cost-effective in
phase technology for the produc-
the world, and can meet both the di-
tion of chromium type HDPE and
verse needs of performance plastics
MDPE or ZN based HDPE / LLDPE
manufacturers manufactur ers and those of com-
❏
Lupotech T, the high pressure tubu-
modity-oriented polyolefin produc-
lar reactor process technology for
ers.
the production of LDPE homopoly-
Basell’s licensing portfolio of process-
mers and EV EVA-copolymers A-copolymers
es and services includes the following technologies:
Some of the processes can be easily upgraded in capacity and capability
❏
Spheripol , the world’s leading tech-
to produce more sophisticated prod-
nology for the production of
ucts, if required.
polypropylene homopolymer plus
❏
❏
random and heterophasic copoly-
Basell’s Avant catalyst range covers
mers
titanium, chromium and zirconium-
Spherizone, this new manufactur-
based polymerisation and is the opti-
ing platform with a multi-zone cir-
mal solution for the process tech-
culating reactor system that cre-
nologies we offer. Avant catalysts
ates polypropylene and novel,
can also be used in most other types
propylene-based polyolefinic ma-
of polyethylene and polypropylene
terials with outstanding quality
process technologies.
Hostalen, the leading low-pressure
slurry process technology for the production of bimodal HDPE
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PP consumption trend 1975 - 2005 45,0 40,0 35,0 30,0 a / t k
25,0 20,0 15,0 10,0 5,0 0,0 5 7 9 1
7 7 9 1
9 7 9 1
1 8 9 1
3 8 9 1
5 8 9 1
7 8 9 1
9 8 9 1
1 9 9 1
3 9 9 1
5 9 9 1
7 9 9 1
9 9 9 1
1 0 0 2
3 Technology 3.1 Introduction to Spheripol Technology Global demand for polypropylene
This includes Exxon, Dow, Borealis,
(PP) has grown quickly over many
Showa Denko, Hyundai and Sinopec,
decades. There are three major rea-
to name but a few. Today, products
sons for this:
from the Spheripol process are routinely sold in over 100 countries, and
❏
As a well-established plastic resin
future licensees will certainly benefit
with a broad application range, PP
from this wide acceptance and prod-
usage has grown in line with the
uct standardisation standardisation..
overall economy. ❏
During their transition phase, developing countries experience rapid growth in their per capita PP consumption.
❏
There is huge untapped technical potential in PP resins, which continues to extend their usage into market segments of traditional materials like glass, wood, paper, metal, etc., other plastics and, in some cases, even engineering plastics.
Basell's Spheripol process is the most widely licensed technology ever developed for the production of polypropylene. Since 1982, proof of its enduring worldwide success is the number of leading polypropylene producers choosing this technology.
2 0 0 2
5 0 0 2
Source: TECNON, Basell
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3.1.1 3.1 .1 An ove overvi rview ew of Spheripol Technology development
Today’s Spheripol process is the re-
In the 1970s, the discovery of se-
morphology, isotacticity and molecu-
sult of forty years of continual im-
cond-generation high yield catalysts
lar weight, and continually challeng-
provement. However, to truly appre-
(6,000 kg PP/kg catalyst) eliminated
ing new frontiers in the development
ciate the unique capabilities of this
the need for catalyst residue re-
of propylene polymers.
technology, it is helpful to under-
moval, but atactic was still unaccept-
stand the evolution of the polypropy-
ably high. This simplified the wash-
Due to its low density, good physical
lene industry and the breakthroughs
ing but did not eliminate the atactic
properties and easy processability,
that led to the discovery of the
recovery steps.
polypropylene is the world’s fastest
Spheripol process.
growing thermoplastic. In the 1980s, third generation high
In the 1960s, polypropylene processes
yield, high selectivity (HY/HS) cata-
employed first generation low yield
lysts (30,000 kg PP/kg catalyst) elim-
catalysts (<1,000 kg PP/kg catalyst) in
inated the need for catalyst and atac-
mechanically stirred reactors filled with
tic removal. This further simplified
an inert hydrocarbon diluent. Polymer
the process and improved product
produced with these catalysts had un-
quality. Other breakthroughs oc-
acceptably high residual metals, and
curred in the process design,
contained 10 % atactic polypropylene,
through the refinement of gas-phase
which required separation. Removal of
and bulk polymerisation reactors
catalyst residues and atactic PP in-
that led to the development of
volved treatment of the polymer with
Spheripol technology in 1982.
alcohol, multiple organic and/or water washings, multistage drying and elabo-
Today, the capabilities of the
rate solvent, amorphous and catalyst
Spheripol process are further en-
separation systems. These processes
hanced by the current catalyst gene-
were costly and difficult to operate,
ration, which has the ability to pro-
and also required extensive water
duce new families of reactor reactor-based -based
treatment facilities, and catalyst residue
products with improved properties.
disposal systems.
They offer even greater control over
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3.2 Spheripol Key Characteristics
The Spheripol process offers li-
self), recovery and recycling of unre-
censees a simple and economical
acted monomers, and the absence of
method of producing a wide range of
undesired by-products from the reac-
PP products of the highest quality.
tion.
Today, more companies are using the Spheripol process than the technolo-
Reliability
gies of the three closest competitors
At the end of 2002, a year-on-year
combined.
analysis of operating records from
The unmatched success of Spheripol
over 80 Spheripol process plants
technology is a result of our focus on
worldwide, showed the average
polyolefins and a commitment to
overall operability rate is about 98 %.
continuous improvement.
Of an average 2 % downtime, less than 1 % is due to process features.
Safety & Loss prevention Basell has a safety record among the best in the industry. To date, Basell technologies have achieved nearly 7 million operating hours without any major incident. Reducing Resource Intensity Spheripol technology includes fea-
tures that reduce both resource consumption and emissions from the process. These include use of high yield, highly stereospecific catalysts, the absence of solvents in the process to suspend the polymer (the suspension agent is the monomer it-
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Versatility
Design flexibility
Dedicated support
In comparison with any gas-phase
A range of single line capacities
The experience of Basell's dedica-
technology, a Spheripol process
from 40 – 450 kt/a are available f or
ted technology team is made avail-
plant offers on a single polymeriza-
homopolymer,, random copolymer homopolymer
able to Spheripol process licensees
tion line the widest range of ho-
or heterophasic impact copolymer copolymer,,
to ensure the highest degree of suc-
mopolymers, random copolymers
either using polymer or chemical
cess during project implementation
and terpolymers, as well as het-
grade monomer.
and plant operation.
erophasic impact and specialty impact copolymers covering all PP ap-
Modular installation
plication fields. Intense efforts in
By a modular installation, Spheripol
product application development
process technology is easily adapt-
for all the major market areas in the
ed to meet changing market re-
world, ensures Basell's PP products
quirements when new business op-
keep a leading position in most
portunities arise for licensees. This
profitable market segments, with
flexible modular design has virtual-
excellent results in PP specialties
ly no impact on initial investment
and "high quality" demanding appli-
costs. On existing plants, expan-
cations development.
sions of up to 30 - 4 0 % of the initial capacity have been achieved
Quality
through minor adjustments.
Spheripol technology delivers un-
matched quality with minimum
Low capital and operating costs
property variation due to excellent
Capital costs for the Spheripol
process stability and the consisten-
process are competitive with cur-
cy of Basell's catalysts performance.
rently available PP processes. The technology also offers the lowest operating costs and excellent plant reliability and transition efficiency. efficiency.
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3.3 Process Description
The Spheripol process, using high
Bulk polymerisation employs tubular
yield/high selectivity (HY/HS) catalysts
loop reactors filled with liquid propy-
supplied by Basell, has the unique abil-
lene to produce homopolymer and
ity to produce polymer spheres direct-
random copolymer or terpolymer. terpolymer.
ly in the reactor. Spherical polypropy-
The catalyst, liquid propylene and
lene differs considerably from the
hydrogen for molecular weight con-
small, irregularly shaped, granular par-
trol are continuously fed into the
ticles produced with some other tech-
loop reactor. Residence time in the
nologies and provides significant ad-
reactor is lower than other technolo-
vantages in terms of process reliability.
gies because of the high monomer
The Spheripol process is a modular
density and increased catalyst activi-
technology. In its most widely adopted
ty. The loop reactor is used because
configuration the polymerisation sec-
it offers low cost, high heat transfer
tion involves the following main units:
and maintains uniform temperature, pressure and catalyst distribution.
❏
Catalyst feeding
The low residence time also results
❏
Polymerisation
in short transitions during grade
- Bulk polymerisation (homopoly-
changes, while the complete filling of
mer/random copolymer and ter-
the reactors eliminates any risk of
polymer)
contamination between different
- Gas-phase polymerisation (heterophasic impact and speciality
terface between the actual reaction
copolymer) - option (gas-phase
volume and disengagement.
copolymer unit can be added at a later stage without affecting initial plant configuration or involving significant implementation costs) ❏
grades due to the presence of an in-
Finishing
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Spheripol process
Propylene + Hydrogen Steam Catalyst
Ethylene Nitrogen
Propylene + Hydrogen Ethylene
To polymer handling and extrusion
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A homogeneous mixture of poly-
(ethylene/propylene rubber) formed
propylene spheres is circulated in-
by the introduction of ethylene is al-
side the reactor loop. If the produc-
lowed to polymerise within the ho-
tion of random copolymer or terpoly-
mopolymer matrix that resulted from
mer is desired, ethylene and/or
the first reaction stage. The carefully
butene-1 are introduced in small
developed pores inside the polymer
quantities into the loop reactor. This
particle allow the rubber phase to de-
process achieves very high solid con-
velop without the sticky nature of
centration (>50% by weight), excellent
the rubber to disrupt the operation
heat removal (by water circulation in
by forming agglomerates.
the reactor jacket) and temperature control (no hot spots). The resulting
Fluidisation is maintained by ade-
polymer is continuously discharged discharged
quate recirculation of reacting gas:
from the reactor through a flash
reaction heat is removed from the re-
heater into a first-stage de-gassing
cycled gas by a cooler, before the
cyclone. Unreacted propylene from
cooled gas is recycled back to the
the cyclone is recovered, condensed
bottom of the gas-phase reactor for
and pumped back into the loop reac-
fluidisation. This type of gas-phase
tor.
reactor is efficient because it maintains a high degree of turbulence in
For the production of impact and
order to enhance monomer diffusion
specialty impact copolymers, poly-
and reaction rates, and offers an effi-
mer from the first reactor is fed to a
cient heat removal system.
gas-phase fluidised bed reactor that
Some speciality products, incorpora-
operates in series with the loop reac-
ting two different ethylene content
tor (this gas-phase reactor is by-
copolymers, require a second gas-
passed when homopolymer or ran-
phase reactor in series.
dom copolymer is produced). In this
In impact copolymer production, at
reactor, an elastomer
least 60% of the final product is pro-
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duced in the first-stage loop reactor. reactor. In addition, since ethylene is more reactive than propylene, the gas-phase reactors are smaller than would be required if this design were to be used for homopolymer production. Spherical morphology ensures high reliability and elimination of fouling phenomena, which frequently disrupt other gas-phase systems. Polymer discharged from the reactors flows to a low-pressure separator and subsequently to a steam treatment vessel where catalyst residues are neutralised and the dissolved monomer is removed, recovered and recycled back to the reactor system. From the steamer, polymer is discharged into a small fluidised-bed dryer with a hot nitrogen closed loop system to remove the moisture. The final product is conveyed to an extrusion unit, where it is mixed with additives and extruded to pellets.
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3.4
Safety and Environment
Basell has a safety record among the best in the industry. To date, Basell technologies have achieved nearly 7 million operating hours without any major incident. Spheripol process plants are built ac-
cording to the Basell Safety Design Criteria and must undergo Safety Audits prior to commissioning and start-up. All licensed sites receive visits from a team of specialists experienced in diverse fields, including: ❏
Safety and Loss Prevention
❏
Health & Environmental
❏
Process Operations
❏
Instrument/Electrical/Mechanical design
This team verifies and ensures that the plant is built according to the Basell Safety Design Criteria, and assists the licensee with any safety, health or environmental concerns regarding the process and related facilities.
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3.4.1 Intrinsic safety of the process
3.4.2 Spheripol : Technology designed to lower environmental impacts
The design of each Spheripol process
Spheripol process units are config-
plant includes a number of safety
ured so that unreacted monomers
features, such as:
are recovered and recycled. If necessary, other discontinuous hydrocar-
❏
❏
Proprietary Catalyst Deactivation
bon purges can be sent to "off-gas
System, which immediately stops
recovery” for use as a fuel supply or
all reaction
to a flare system.
Computer controlled emergency shutdown systems
The Spheripol process does not use
Uninterruptible Uninterruptibl e Power Supply (UPS)
hydrocarbon diluents nor contami-
for computer control and critical
nant chemicals and the only waste-
instrumentation control
water is released from the steam-
❏
Instrument air emergency buffer
ing/drying section of the plant which
❏
Emergency Blowdown System to
contains steam condensate and a
empty the plant quickly, in the
small amount of inert polymer fines,
event of an emergency
which are recovered by a separator.
❏
❏
Gas detectors which instantly determine and highlight (on a graphic easy-to-read board) the source of any hydrocarbons in the event of leakage into the atmosphere
❏
Automatic fire protection systems
Depending upon the severity of the situation, the plant can be shut down manually in a step-by-step, controlled fashion, more rapidly by both manual and computer control, or by instant automatic shutdown.
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3.5 Process Capability 3.5.1 Design Flexibility Spheripol process plants are de-
a later date to produce heterophasic
signed to meet the particular require-
impact and speciality impact copoly-
ments of individual licensees, yet
mers. Impact copolymers are more
they are flexible enough to be easily
specialised products, which require
expanded to meet future needs as
additional capital investment and
the business develops. Two critical
technical support.
design elements that are easily ex-
The simple design of a Spheripol
panded include capacity and product
process plant does not require
range.
mandatory equipment or instrument/electrical vendor lists. There is
Spheripol process facilities have been
also a list of suitable suppliers and
designed with capacities ranging
designs for critical equipment, en-
from 40 - 450 kt/a. This wide capaci-
abling purchasers to benefit from the
ty range and the modular installation
most economic pricing available.
approach allows, within limits, easy debottlenecking. This minimises initial capital costs and allows new capacity to be added later when required. The product range can also be easily expanded. Often new entrants to the polypropylene business will build a plant to produce only homopolymer and random copolymer products as these are the least expensive, are easy to operate and their products account for 75% of all polypropylene sold in the world. A basic homopolymer plant can be easily expanded at
17
Spheripol Process Capability
MFR (g/10’)
0.3 to > 1600
Xylene Insolubles (%)
90 to 99 %
Particle size (mm)
0.3 to 5.0
Melting point (°C)
130 to 165
Flexural Modulus (MPa)
600 to > 2400
IZOD impact at 23°C (J/m)
30 to 1000
3.5.2 Versatility
3.5.3 Advanced Process Control
Spheripol technology's versatility is
Although the standard control sys-
demonstrated by its easy process op-
tems are highly capable of control-
eration and ability to deliver a pro-
ling the process reliably and effi-
duct range that includes all standard
ciently, Advanced Process Control
polypropylene grades, and many
software can be made available to
unique, special products.
Spheripol licensees in order to fur-
ther benefit from the process capaKey to this versatility is the applica-
bilities.
tion of Basell's high yield / high selectivity Avant catalysts: ❏
High polymerisation activity (mileage over 40,000 kg PP/kg cat-
3.5.4 Simulation / Operator Training program
alyst), resulting in extremely high ❏
❏
❏
❏
polymer purity
A special developed simulation pro-
Stereospecificity Stereospecificit y control of poly-
gram is used for training and deve-
mer
lopment purposes, and can be made
Morphology control of particle
available to Spheripol licensees. The
size, shape and distribution
program allows training for start-up,
Molecular weight distribution con-
steady state, grade-change and shut-
trol
down operations, and can assist in
Use of polymer or chemical grade
optimising your Spheripol plant.
monomer ❏
Homopolymer, random copolymers and terpolymers, heterophasic impact and speciality impact copolymer production
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3.5.5 Technol echnology ogy Summar Summary y
The Spheripol process is the most cost effective technology for whole PP family production Other Processes
Spheripol Process
Conventional gas-phase design suffers from equip-
Spheripol process operation is not affected by the
ment size scale up problems and constraints in
presence of critical machines. Complete monomers
plant operation economics due to monomer losses
recovery is possible even in case of chemical grade
and mechanical weakness.
monomer use. Catalyst yield is higher higher..
Plant configuration is modular in order to optimise investment costs to product slate requirements, loop reactors design allows for better scale up efficiency (single line over 400 kt/a does not imply any criticality in equipment sizing or reactors configuration) configuration)
Gas-phase operating window is limited in terms
Hydrogen response is higher. Loop reactors design
of hydrogen response and heat removal.
and liquid monomer operation grants extremely efficient heat removal and temperature control.
Spheripol technology ensures better product quality and reproducibility
Other Processes
Spheripol Process
Polymer morphology may affect process reliability
Controlled morphology of the polymerising particle
and represent a constraint to finishing efficiency
(independently from average particle size) improves
and complete monomer recovery. recovery.
finishing efficiency and eliminates risk of fouling when producing impact copolymers even at high ethylene content.
Catalyst system distribution and process parame-
Polymerisation conditions are completely homoge-
ters control is more critical.
neous and can be reproduced exactly any time by simple parameter selection.
Hydrogen response is limited and reactors cascade
Hydrogen response is very high, catalyst system ca-
operating mode (bimodal operation) is not available.
pabilities and bimodal operation mode allows for accurate control of product quality in a wide range of properties.
19
Spheripol technology provides the easiest and cheapest grade change
Other Processes
Spheripol Process
Cumbersome product transition from grade to
The switch from one grade to another is particularly
grade, especially when switching to or from copo-
easy, quick, and low cost because hydrogen composi-
lymers. Presence of an interface between polymer
tion can be adjusted immediately without reducing ca-
bed and disengagement section increases risk of
pacity and impact copolymer production can be star-
product contamination.
ted by just feeding homopolymer to copolymer reactor.
Off-grade material associated with each cam-
Very low residence time, allowed by extremely high
paign takes up a recognisable portion of the pro-
reactivity conditions, minimise transition material.
duction. Full reactors avoid product contamination .
Spheripol technology has reduced environmental impact to negligible levels
Other Processes
Spheripol Process
Conventional approach.
Extremely high attention to environment environmental al and safety considerations due to the "liquid phase hydrocarbons culture".
Lower efficiency associated with hydrocarbon hydrocarbons s
All monomer residues are recovered to the polymeri-
polluted nitrogen stream recovery and polymer
sation thanks to the unique "live steam” stripping
residual volatiles.
which ensures a complete polymer "finishing”.
20
3.6 Process Economics 3.6.1 Reliability and operability The Spheripol process has proven to
Products from the Spheripol process
be extremely reliable. In use since
are superior in quality. The Spheripol
1982, it has been continuously re-
process was designed around the
fined and optimised. Yearly world-
catalyst to minimise property varia-
wide surveys of operating Spheripol
tions and to ensure consistent results
process lines reveal an average on-
with regard to:
stream operability of around 98%. Key contributors to this remarkably
❏
Particle size and shape
high operability include:
❏
Crystallinity and stiffness
❏
Melt flow
A simple, straightforward process
❏
Molecular weight distribution
design with simple and reliable
❏
Comonomer distribution
equipment
❏
Physical and optical property per-
❏
❏
Easy on-line product change
❏
Rapid restart after shutdown
❏
No scheduled maintenance down-
High catalyst mileage results in ex-
time for cleaning or inspection
tremely low residual metal content.
purposes
3.6.2 Quality In addition to high operating rates, products produced with the Spheripol process maintain consis-
tently high quality from one run to the next. Products are identical from different plants, wherever located.
formance
21
3.6.3 Consumptions
Spheripol process plant capital and
operating costs are among the lowest in the industry as a result of: ❏
Smaller reactor volumes
❏
Minimum transition time
❏
Lowest monomer consumption
❏
Utilisation of low cost chemical grade or polymer grade monomer
❏
Low steam and electric power consumption
Typical specific consumption (per 1000 kg of PP produced)
Monomers (kg)
(1)
3 (2)
Hydrogen (Nm )
Catalysts & Chemicals ($) Electric power (kWh) Steam (kg)
(5)
Cooling water (m3) 3
Nitrogen (Nm ) (1) (2) (3)) (3 (4) (5) (6)
(4)
(6)
(3)
Homopolymer
Impact Copolymer
1002
1002
0.01-0.5
0.01-0.5
22-25
23-26
250-270
280-300
280
280
110
120
15
15
Net consumption of 100% monomers / co-monomers included Depending of reactor gas composition, according to polymer MFR Typ ypic ica al Gen ene era rall Pur urp pos ose e st sta abil ilis isa ati tio on Extrusion included, consumption depending on product MFR Low pressure steam, high pressure steam consumption for extruder die plate or barrels heating is excluded At T = 10°C
22
3.7 Products and Applications
Isotactic polypropylene is well suited
ties and sealing initiation tempera-
for a variety of end uses, ranging
tures in compliance with the U.S.
from flexible and rigid packaging to
Food and Drug Administration (FDA)
fibres and large moulded parts for
regulations for food contact.
automotive and consumer products.
Heterophasic copolymers with out-
Polypropylene is recyclable, an im-
standing low-temperature behaviour,
portant consideration in many pack-
high-impact strength and enhanced
aging and automotive applications,
stiffness can be obtained in the
and it can be incinerated without
widest range of melt viscosities.
toxic emissions. It can be processed
As a global average, homopolymer
using most methods including extru-
accounts for 65-70 % of all
sion, extrusion coating, blow mould-
polypropylene, random copolymer
ing and stretch blow moulding, injec-
and terpolymer for 10-15 % and het-
tion moulding, and thermoforming.
erophasic copolymer for 15-20 %.
Its physical properties can be easily enhanced through the addition of
Film and fibre are the two largest
fillers such as calcium carbonate or
segments in the global PP market,
talc. Polypropylene has excellent
but injection/blow moulding and ex-
chemical resistance and electrical in-
trusion account for significant quan-
sulating properties.
tities. Typical polypropylene fabrica-
Typical applications for polypropy-
tion processes and end uses include
lene products produced in the
the following major fields:
Spheripol process include fibres and
filaments, oriented and cast film, in jection-moulding items, blow-moulded bottles and parts, and thermoformed containers. Random copolymers can be produced with excellent optical proper-
23
By courtesy of SIMONA
Fabrication Process
Markets/End Uses
Film Extrusion
BOPP film / WQB film / cast film/ (flexible packaging for textiles, confectionery, bakery and cigarette wrap)
Multifilaments
woven sacs (raffia)/fibrillated tape for carpet backing, geotextiles, rope and twine, upholstery and cigarette tow
Nonwovens
geotextiles, medical application (meltblown and spunbonded)
Injection moulding
automotive, appliances, houseware, furniture, consumer products, packaging (crates, cases, caps and closures, thin walled and transparent containers)
Blow moulding
packaging
Profiles extrusion
pipes, conduits, corrugated sheet, wire and cable extrusion coating, lamination.
Basell Avant catalysts are capable of
range of PP products, including ho-
high quality levels, where excellent re-
manufacturing products with virtually
mopolymers, random copolymers and
sults have been achieved.
unlimited combinations of physical
terpolymers, as well as heterophasic
properties to meet the increasing de-
impact and specialty impact copoly-
For better evaluation of the capabili-
mands of customers in new and more
mers covering all PP application fields.
ties of the Spheripol process, and to
challenging applications.
Extensive product application develop-
demonstrate its superiority to any
ment has enabled products from the
competing technology, listed overleaf
In comparison with any competitor
Spheripol technology to keep a leading
are some of the Spheripol process
gas-phase technology, a Spheripol
position in most market segments
products which ensure Basell's leading
process plant is making available on a
worldwide, and particularly in PP spe-
position in specialties and high perfor-
single polymerization line the widest
cialties and applications demanding
mance PP market segments:
24
.. Copyright Citroen Communications
Homopolymers ❏
❏
❏
Very high processability BOPP, for
terpolymers
application on very fast tenter ma-
A new family of very high clarity ran-
chines (over 300 m/min).
dom copolymers of propylene and
Single and multi-layer cast film
butene-1 with less hexane extracta-
produced on high-speed lines
bles (very important for food con-
using new grades particularly suit-
tact) is under commercial develop-
able for thin gauges.
ment. Uses will include high perfor-
Fine denier continuous filament
mance cast film application with dif-
and non-woven fabrics products
ferent stabilization package as well
for disposable clothing, lining,
as for extrusion applications, such as
medical hygienic, feminine care,
thermoforming, blow molding, sheet
diapers, crop protection in agricul-
extrusion and blown film.
ture. ❏
Random copolymers and
High clarity gamma ray resistant for syringes injection grade.
In addition, a number of new commercial grades have been successfully introduced to the market for very high stiffness homopolymers (Flexural Modulus higher than 2300 MPa) for injection and thermoforming.
25
Heterophasic impact copolymers ❏
Improved impact/stiffness balance
with very high creep resistance are
copolymers for corrugated pipe,
now available for pipe applications.
injection and thin wall injection-
There are also a whole family of high
moulding applications. These
rigidity "ultra" grades for fast injec-
grades have been recently intro-
tion applications, and high clarity im-
duced on a commercial scale and
pact grades for cosmetic packaging
made available to the Spheripol
and houseware.
process licensees. ❏
Very high MFR impact copolymers for thin wall injection (MFR 70 and 100 g/10' pelletised commercial grades are regularly produced in Basell's Spheripol process plants).
❏
Specialty impact heterophasic copolymers for bumpers presenting extremely high impact resistance even at very low temperatures. These reactor grades were developed in the Spheripol process to the requirements of all major car manufacturers in Europe.
❏
In addition, heterophasic copolymers
High impact for special applications such as a low MFR grade free of fish eyes for film and tape or extrusion and blow moulding.
26
4 Licensing Customer Services
During the development of a project
also described. Payment conditions
and throughout the operation of the
vary from lump sums to running roy-
plant, experts from the Licensing De-
alties, or an appropriate combination
partment and the Technology Trans-
of both these elements.
fer Centre will be dedicated to the li-
Further sections of the License
censee’s needs in the following areas
Agreement stipulate the project as-
of activity:
sistance, particularly during commissioning and start-up of the plant and
Licensing process
the performance testruns, by Basell
Prior to the granting of a license,
experts in process design, polymeri-
Basell will actively participate in the
sation, extrusion and quality control.
definition of the project, based on
Other more formal chapters cover se-
the product and marketing expecta-
crecy, liability, patent issues, force
tions from the customer. This stage
majeure, applicable law, etc.
defines the optimal technology and particular design features - such as capacity, reactor configuration, catalyst system, etc. - under a confidentiality agreement. Once the scope of the plant has been jointly identified, a draft License Agreement will be prepared and negotiated; the agreement will contain articles that define the type and capacity of the plant, the product grade slate, etc. The supply of the Process Design Package, the extent of the granting of the license, the license fee and the payment conditions are
Business start-up support
27
Basell is open to discuss possible sup-
❏
Equipment list + data sheets
ply of resins from Basell production for
❏
Instrument list + data sheets
pre-marketing of resins by the li-
❏
Safety valve list + data sheets
censee, and use the Basell marketing
❏
Plot plans
and sales organisations to support the
❏
Safety design criteria
licensee in the development of the
❏
Emergency flaring load
polyolefins business, by agreement on
❏
Fluid list and piping classes
defined off-take volumes of resins
❏
Environmental Environment al information
until the licensee can market the entire
❏
Guidelines for the operating manu-
production volume itself.
al ❏
Etc.
Process Design Services Engineering
Ideally the Basic Engineering may be
The Process Design Package (PDP)
provided by a contractor with a
provided by Basell Process Design
proven record of the Basell technolo-
contains a comprehensive technical
gy. Alternatively this can be done by
description of the entire process, and
another contractor on the basis of
is adequate to allow for the prepara-
the PDP.
tion of the engineering of the plant,
The Detailed Engineering – at least in
application to authorities for environ-
part - is typically done by a local en-
mental licenses, and the preparation
gineering company in the region of
of the operating manual. Typical PDP
the license plant.
content is:
Experts from Basell Process Design can assist the engineering activities.
❏
Process description
❏
Process flow diagram (PFD) with heat and material balances
❏
Piping and instrument diagrams (PIDs)
28
Technology Transfer:
Start-up support and guarantee
Besides some initial support during
testruns
the licensing process, the main ser-
A start-up team, consisting of Basell
vices provided to the Licensees by
expert operators, will provide assis-
Technology Transfer are in agree-
tance during pre-commissioning and
ment with the Licensing Agreement,
commissioning of the plant.
and consist of the following:
After completion of the commissioning, Basell HSE experts will partici-
Training
pate in a Plant Safety Audit to verify
Prior to the start-up, highly experi-
the adherence to the Safety Design
enced trainers at Basell’s training
Criteria, with special attention to
centres (Ferrara, Italy / Bayport,
health and environmental concerns.
Texas, USA / Aubette, France) will
The start-up team will assist during
train licensees’ experts on Opera-
the start-up, in order to obtain a safe
tions, Quality Control, Maintenance,
and reliable start-up, and normally
Applications and Safety. Comput-
remain until the performance guaran-
erised dynamic process simulators
tee testruns have been finalised.
are available to enable licensees’ personnel to train for start-up, steady state, grade-change and shutdown operations. Courses are tailored to fit the specific needs of the customer, not only with regard to content, but also accommodation, interpretation, transportation, visas, etc.
29
Technical support after start-up
❏
While the full commercial operation
Advice on maintenance and quality control procedures
of the plant will soon become a rou-
❏
Marketing exchange
tine business of the licensee, devel-
❏
New product development or adjust-
opments in the world of polyolefins will continue.
ments to local markets ❏
Safety information about Basell, its
Meetings with focus on licensee’s
joint ventures and/or licensees will be directly shared unconditionally, in
Periodical Technical Exchange issues
❏
Periodical seminars / conferences
order to continue to improve the
with focus on safety, best practice
safety standard of our technologies.
and breakthrough in process and
In order to further benefit from
catalysts
Basell’s technical knowledge and developments, licensees can enter into
Engineering services
a Technical Support Agreement (TSA)
If market conditions change, and the
with Basell, typically comprising the
capacity of the plant needs to be in-
following elements:
creased, or a variation in the product grade slate needs to be made, Basell
❏
❏
Explanation and details of technical
can assist in the engineering activi-
improvements within the scope of
ties needed to upgrade the plant ac-
the original License Agreement
cordingly.
Non-confidential information on Basell’s R&D progress that goes beyond the current license
❏
Further training sessions
❏
Optimisation of plant efficiency: trouble shooting / trial for new products / new catalyst implementation, provided with technical assistance at the customer’s site
30
Source: Nasa
Basell Technology Licensing – Conclusion
Basell is unique in providing excellent process technologies for all polyolefin production for all fields of product applications. This, together with our drive for customer satisfaction, continuing R&D developments, and the support from the organisation of the world leader in polyolefins, will make Basell technology the optimum choice for your polyolefin production, now and in the future.
31
l n l i a r e l c a s e w a b y B e a l l h g d e t s n e t i z a a d i r B h u o l t l l h c a e n t r i u h u , a s s d t n e n n e i l a e y v o p b s m e l a i d o r e n d l o n n g i u s i o s s d h e g n s r p n a i , y x t e e i n h , r i o y w T n i . t n n e a i p s r t o u r p s a e ’ l d w c l e e d a x e s a n e l e t l B t e u s t n t a i i t a e e s B c h n f i t o o r r c f p o t l e f o a s e n h l e a b s b h c a e r t o n u i u d o p s t s e e s n i h i t t e i t m l c i f b u u a o d c i o l d o r d y n u p s n f i e h a e r h t T e r . m o t ) a u t m s c h t o s u c . a d n l o o l r i o r t e s s p a a e e n b i i . t h m n t r w a f e w r r o t e w a t d t w n a e t l m n l h e e e c d s u s c a n a e l B e p k p e e m a r d o s r m i n f i o e t s n l m i b d w a e a o l i z l c r a i r l i o l e v a h a h t t e r o e r u a f k a s s i y a t m e e d e e . d h n s l o m e e u S o r o a N g e a h t v m s a . i D e s a s r y s u d l e t o p s f e c y x r u a r a u e l r S p p e l r e h h a a t m t i l , e o r x e u c g e d t i n n a t r i t r a M i ( a r o , s . p r y l a w e e l v i n t i m a r i o g o e f d n t u s l s e e p u d s , c n e r l n g , a t a a t i i c l y f e t u e r i s n d f o e a y w u o r q r s t p t i e e i h s l c l l u b t e d o n a o s t s c a o n s , B r a l e l p h a a l i l c n g e r U c n s e . e p i a e s B m e s u e f y r o o o e f h r t y l o e t p l e f e s n m b B u a r e a
Corporate Centre
North America Regional Office
Australia Sales Office
Basell B.V. Hoeksteen 66 2132 MS Hoofddorp The Netherlands Tel. +31 20 4468 644 Fax +31 20 4468 649
Basell North America Regional Office and Research & Development Centre 912 Appleton Road Elkton, Maryland, USA 21921-3920 Tel. +1 410 996 1600 Fax +1 410 996 1660
Basell Australia Pty. Ltd. Level 2, 199 Toorak Road South Yarra VIC 3141 Melbourne Australia Tel. + 61 3 9829 9455 Fax + 61 3 9829 9431
Europe Regional Office
Basell North American Advanced Polyolefins Business and Technical Centre 2727 Alliance Drive Lansing, Michigan, USA 48910 Tel. +1 517 336 9600 Fax +1 517 336 9611
For more information on Basell licensing services, Spheripol technology, or engineering engineering,, technical and marketing services, please contact:
[email protected]
Basell Polyolefins Company B.V.B.A. Woluwe Garden Woluwedal 24 1932 Zaventem (Brussels) Belgium Tel. +32 2 715 80 00 Fax +32 2 715 80 50
Main European Sales Offices* Advanced Polyolefins
Basell Deutschland GmbH Industriepark Hoechst Building B 852 65926 Frankfurt am Main Germany Tel. +49 69 305 85800 Fax +49 69 305 85803 Polyolefins Europe
Basell Deutschland GmbH Bruehler Strasse 50389 Wesseling Germany Tel. +49 2236 726000 Fax +49 2236 726034 * For a complete list of Basell European sales offices, please visit www.basell.com
South and Central America Regional Office Basell Brasil Ltd. Estrada Samuel Aizemberg, 1707 Sao Bernardo do Campo 09851-550 Sao Paulo, Brazil Tel. + 55 11 4343 3461 Fax + 55 11 4343 3464
Asia-Pacific Regional Office Basell Asia Pacific Ltd. 22/F Hennessy Centre 500 Hennessy Road Causeway Bay Hong Kong China Tel. + 852 2577 3855 Fax + 852 2895 0905
You can find out more about Basell by visiting our website at: www.basell.com Avant, Catalloy, Hostalen, Lupolen, Lupotech G, Lupotech T, Spherilene, Spheripol and Spherizone are trademarks owned or used by Basell. Hostalen, Lupolen and Spherilene are registered in the U.S. Patent and Trademark Office. Copyright 2005 Basell Service Company BV. All rights reserved.
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