CORK TREATMENT - A NEW INDUSTRIAL
APPLICATION OF SUPERCRITICAL FLUIDS
Dr. Eduard Lack1), H. Seidlitz1), Moaad Bakali2), Rudolf Zobel2)
1) NATEX Prozesstechnologie GesmbH, Werkstrasse 7, 2630 Ternitz, Austria, e-mail: office@natex.at, Fax:
+43-2630-38163
2) Diamant Techoenologie S.A., Corchos de Mérida, Carreterra de la Estación, km.1, 06500 San Vicente de
Alcántara, Spain
Microorganisms produce secondary metabolites like trichloroanisole (2,4,6-TCA), but also
other unpleasant substances, which cause the typical “cork taint” in wine. This has led to
serious problems for the cork industry in recent years and market share of cork stoppers
decreased continuously. Conventional processes to reduce TCA content were only partly
successful. Therefore a research program was started using supercritical CO2 in order to
reduce the TCA content below the detectable limit. The R&D project was successful in
achieving this target and consequently the results were patented. After pilot tests and scale-up
an industrial project was realized in San Vicente de Alcántara at the end of 2005. Soon it was
recognised that supercritical CO2 also eliminates other substances responsible for certain offtastes of wine.
1. INTRODUCTION
The cork oak (Quercus suber), an evergreen oak species reaching a height of 20 m, is the raw
material for the production of cork stoppers. It is mainly grown in the southwest of Europe
and northwest of Africa. Cork stoppers produced from the bark of the cork oak are resilient
and tight closures for wine and sparkling wine bottles. [1] [2] [3]
Nowadays mainly in Portugal, Spain, Tunisia, Morocco, Italy, France and Algeria cork oaks
are grown. The European cork industry produces about 340.000 tons of cork per year, which
represent a value of 1.5 billion EURO, and employs directly around 30.000 employees.
Portugal is number one of the cork producing countries with a share of 31 % of the cork oaks.
190.000 tons of cork or 51 % of the world production are produced in Portugal’s cork forests.
Spain is one of the main producers of cork products.
The stems of the cork oaks show a shining red colour after peeling. The year when the peeling
took place is marked on the stems (for example no. 2 for 2002). So the farmers can calculate
when they can peel the trees again. The first cork of young oak trees has a low quality and
cannot be used for cork stoppers. The bark should be removed very carefully from the stem in
order to avoid any damage of the underlying phloem. From the age of 20 years up to around
200 years the stem can be peeled every 10 - 12 years. In this way a good quality of cork
material can be obtained and thickness is sufficient to produce cork stoppers.
For centuries cork stoppers have been used to seal wine bottles, even in ancient times wine
amphoras were closed with cork. In western society people expect the typical sound “blob”
when opening a bottle of wine, which is part of the drinking culture. Worldwide around 20
billion cork stoppers are used every year. Cork is a natural polymer foam based on the
substance suberine. [5]
The average chemical composition of cork is:
- Suberine (45%) - the main component of the cell walls and responsible for the
resilience of cork
- Lignin (27%) – a cross-linked aromatic polymer
- Polysaccharides (12%) – the structural component of the cell walls
- Tannins (5%), terpenoids and steroides (5%)
Like most other natural raw materials cork can contain secondary metabolites produced by
microorganisms. The worst one is TriChloroAnisole (2,4,6-TCA) which is primarily
responsible for the typical “cork taint”. Good wine specialists can recognize a TCA content in
wine of about 2 ng/l already, while usual consumers notice concentrations between 5-10 ng/l.
The cork industry made a lot of efforts to solve this problem because it became very serious
during the recent years. Quite a number of different processes with steam or alcohol were
developed to reduce the TCA concentration in cork, but theses processes usually don’t
achieve more than 85 % efficiency at industrial scale.
In 1997 one of the leading cork producers, Sabaté, later Oeneo Bouchage, started the
development of a cork cleaning process with supercritical gases in cooperation with CEA.
The tests were very successful and consequently the process was patented. Supercritical CO2
allows a reduction of the TCA content below the detectable limit, which is at the moment 0.5
ng/l. Furthermore CO2 has special properties regarding reduction of pesticides and inhibition
of fungus growth.
In 2003 the Austrian based company NATEX Prozesstechnologie, a well recognized leading
specialist for scale-up and supply of supercritical processes was selected for the exploitation
of the patent and for scale-up purposes. Several test series were executed first on the 80 litres
pilot plant owned by NATEX and later on industrial size in order to proof and confirm the
theoretically calculated scale-up factors. Cork has a very low bulk density (around 60 kg/m³),
which makes special equipment necessary for loading and unloading of the extractors.
Cork in its natural form has a relatively precise bubble size distribution. The gas bubbles have
a diameter of around 25-35 µm as can be seen in Fig. 1.
Figure 1: Electron microscope picture of cork. The left picture shows a cork in good
condition and the right one a cork cell with fungi infection.
2. EXPERIMENTAL SECTION AND THEORY
Raw cork granules start to shrink above 15 bar during pressurization in the extraction vessel.
This shrinking continues up to about 90 bar. Above this pressure no further major
deformation could be recognized. During the depressurization step the original shape of the
raw material is slightly changed. It is difficult to extract whole cork stoppers and more
recommendable to extract cork granulate first and to produce the final cork stoppers by
compacting the treated cork granulate afterwards. For the tests extraction pressures between
100-300 bar and temperatures between 40-60°C were selected. The extraction conditions are
mainly influenced by the cork material itself. Young trees have larger bubbles, the cork
material is softer and consequently the diffusion is faster. Older trees (100 years and older)
have a more solid bark with small bubbles, which reduces mass transfer due to the higher
diffusion resistance. Further the climate in the area, where the trees are grown, influences the
cell structure of the cork bark. Very important is the moisture content of the raw material and
the degree of moisture during the extraction process.
3. ENGINEERING AND SCALE-UP OF THE PRODUCTION PLANT [6]
After obtaining enough information regarding the scale-up factors and the extraction
behaviour the engineering of the industrial plant started. A production capacity of 2500 tons
per year, which corresponds to 500 million cork stoppers, was the basis for the design. In
order to optimize energy consumption a careful comparison between the pump- and the
compressor process was executed. Larger industrial processes with supercritical CO2 were
only designed as pump processes until today. The evaluation showed economical advantages
for the compressor process and in consequence design engineering was adjusted accordingly.
Figure 2 shows the schematic CO2 process for cork cleaning
A circulation compressor increases the CO2 pressure from separation conditions to the
required extraction pressure. After the compressor a heat exchanger adjusts the CO2 to the
corresponding extraction temperature. As the discharge temperature of the compressor is
higher than the necessary extraction temperature, the heat exchanger must be able to operate
as cooler and heater. While flowing through the cork bed the CO2 is loaded with the soluble
substances, mainly TCA, but also resins and other organic components. After passing the
extractor the supercritical fluid is depressurized by means of a control valve and routed
through an evaporator, in which the liquid part of CO2 is evaporated. The gaseous CO2 with
the liquid extract reaches the separator, where the extracted substances are precipitated. The
extract, mainly an oil and wax emulsion with an unpleasant smell, must be treated as waste.
Big efforts were made for the design and manufacturing of the compressors. As a compressor
process was used for an industrial supercritical CO2 extraction plant for the first time, careful
analysis regarding safety and piping design was necessary. In spring 2005 the construction of
the plant was started and it was already commissioned at the end of the same year.
Figure 3: Cork cleaning plant in San Vicente de Alcántara, Oeneo Bouchage
Figure 4a: Extractors with cork filling system
Figure 4b: Compressor station
4. RESULTS
Very soon it was recognized that the DIAM closure gives excellent results regarding sensorial
neutrality with emphasis on fruit aromas in fresh wines. Starting with 2005 Oeneo Bouchage
led an extensive research program to verify whether the sensorial nature of wine closures with
DIAM is only related to the extraction of 2,4,6-trichloroanisole or if the extraction of other
aromatic substances is important for the quality of the cork stoppers.
Due to the fact that the Diamant Process was already in operation on industrial scale enough
treated cork flour and cork extract was available for the research program. The cork raw
material showed an average TCA content of 11-25 ng/l. The extracts obtained in the
separators of the production plants showed a TCA content of 70 - 200 ng/l.
Figure 5: Sensory differences between treated and non-treated cork flour
tested in the cork flour macerate [4]
As shown in Fig. 5 it is most important to eliminate mould flavour and reduce substantially
humus and mushroom, leather/synthetic phenol and alcohol/aggressive type notes. Quite
positive is the increase of floral notes. The results also showed an increase of the cocoa grill
and vanilla notes. The reason of this enhancement is not really clear and cannot be caused by
temperature in the CO2 process, which is around 50C°.
Further a series of tests was performed, in which white wine (chardonnay) was contaminated
with liquid or solid fractions of the CO2 extracts. Even after adding small quantities of
extracts to white wines, notes of humus, mushrooms synthetic, leather and mould were rising
immediately.
Chromatographic analysis [4]
The following chromatographic analysis carried out on treated and untreated cork
demonstrated the reduction of extracted substances besides TCA.
Figure 6: Chromatogram of 1-octen-3-ol substances in the cork
granulates before and after the Diamant Process ( These substances
are associated with the humus/mushroom descriptor )
Figure 7: Chromatogram of the content of the
sesquiterpenes in the cork granulates before and after
the Diamant Process. ( These substances are
associated
with
the
phenol/leather/synthetic
descriptor )
Figure 8: Chromatogram of the content of isomers
of anisole isopropyl methylen before and after the
Diamant Process
During the chromatographic analysis around 150 substances were detected by GC-MS and a
great number of substances could be identified. Most of the substances belong to different
chemical families, like alcohol, ketones, aldehydes, acids, esters, phenol compounds, anisoles,
furans, furanones, pyranones, alkylbenzenes, hydrocarbons, terpenes, sesquiterpenes, etc.
5. PRODUCTS
As mentioned above cork granules extracted with supercritical CO2 have an absolutely neutral
taste and are nearly free from microbiological contamination. Most of the wooden parts are
already removed during the grinding process and the final cork stoppers have a very
homogeneous structure. During the SFE process elasticity behaviour of the cork is not
changed and if the final stopper is deformed, 97% of the original shape is reached again
within 30 sec. Further gas diffusion through the stopper can be adjusted by the moulding
process of the cork stopper.
Figure 9: Efficiency of the Diamant Process
With the Diamant Process a secured and reproducible reduction of the TCA content can be
reached on industrial scale. After three years of industrial practice no reduction of the
efficiency of the process is recognizable.
6. CONCLUSIONS
“Cork taint” in wine is a serious problem and has led to increased use of alternatives to cork
stoppers. A research program was carried out to eliminate TCA by means of dense CO2.
Because of the very successful results of this research program an industrial scale SFE plant
was realized in Spain. This plant can process up to 2500 tons of cork granules per year.
During CO2 extraction also other substances besides TCA are removed. Cork flour treated
with supercritical CO2 can therefore be characterised by significantly improved sensorial
neutrality along with an expression of certain positive aromatic notes, such as floral, vanilla,
cacao (grilled), which are naturally present in cork but are normally masked by other less
positive notes. This was proved by comparative sensorial analyses and chromatographic
analyses. With this innovation the conservative cork industry stepped into a new era and gave
hope to the cork farmers. Furthermore it was a genuine European project, because most of the
cork is produced in Europe, mainly in Portugal and Spain, and also the final cork stoppers are
produced mainly in Europe.
7. REFERENCES
[1] TAYLOR M. K., YOUNG T. M., BUTZKE CH. E., EBELER S.E., Supercritical fluid
extraction of 2,4,6-trichloroanisole from cork stoppers. American Chemical Society,
2000, (48).
[2] LUMIA G., ARACIL J. M., BARTH F., SARRADE S., Cork material treatment by
supercritical CO2, AWITC Symposium, July 2004, (Australia)
[3] FELSVANG K., IVERSEN S., LARSEN T., LÜTHJE V., ARACIL J. M., SEIDLITZ H.,
LANG F., LACK E., The World’s First Supercritical Plant for Cork Cleaning, 7th
International Symposium on Supercritical Fluids, May 2005, Orlando (USA).
[4] BOBE A., LOISEL C., Impact du procédé Diamant® sur les caractéristiques
organoleptiques de la farine de liège, Juillet 2006, Revue des Œnologues No. 120
[5] LACK E., SEIDLITZ H., Industrial cleaning of cork with supercritical CO2, 3rd
International Meeting on High Pressure Chemical Engineering, May 10-12, 2006,
Erlangen (Germany)
[6] LACK E., SEIDLITZ H., Kork, Spezialöle, Mikrokomposite – Neue industrielle
Anwendungen überkritischer Fluide, High Pressure Meets Advanced Fluids, RWTH
Aachen, March 10-11, 2008, Aachen (Germany)