Microsoft word - cellimm.doc

Cell Immobilization

Cell immobilization is a technique to fix plant cells in a suitable matrix. Cell
immobilization is different from cell entrapment in that immobilized cells can be
entrapped cells but also the cells are absorbed onto support materials (Pras and
Woenderbag, 1999).
Immobilization is now a well-established technique with the history of enzyme
immobilization going back over 25 years and including many industrial
applications. The immobilization of microorganism is less well developed in terms
of large-scale application, but it is widely used in the laboratory. With this
background it was inevitable that immobilization techniques should be applied to
plant cell cultures and much work has been carried out to establish methods for
plant cell immobilization and suitable bioreactors for use with the immobilized
cultures (Williams and Mavituna, 1992).
Plant cells grow much more slowly, they produce targetted compounds more
slowly, they are more easily disrupted by physical stress and their behaviour
(growth and synthesis) is influenced by chemical signals by neigbouring. Then by
immobilization, the plant cells are protected from liquid shear forces. Moreover,
immobilization facilitates the importance of cellular cross talk, which can establish
inter-cellular communication by the action of signalling molecules. This should
enhance the biosynthetic of plant cells (Haigh and Linden, 1989; Pras and
Woenderbag, 1999).
Freely suspended plant cells mostly accumulate their secondary metabolistes in
the stationary phase of their growth cycle, at the point of time their growth stop.
Entrapment of plant cells is one the means to create non-growth condition under
which the production of secondary metabolites may be improved (Pras and
Woenderbag, 1999).
Immobilized plant cells have been employed to perform biotransformations and
reported to have higher production rates than freely suspended cells. For
example, immobilized Capsicum cultures treated with precursors accumulated
more quantities of biotrasnformed compounds than freely suspended cultures
(Johnson et al., 1996; Rao and Ravishankar, 2000).
Advantage and Disadvantage of Cell Immobilization

In an immobilized system growth and production phases can be decoupled and
control ed by chemical and physical stress conditions. This allows cells to be
retained in the bioreactor for extended periods, with alternating
rejuvanation/growth and secondary metabolite production cycles (Williams and
Mavituna, 1992).
Process engineering problems may develop from the tendency of plant cells to aggregate, which can lead to blockages in pipes and openings and to the culture rapidly sedimenting, if it is not continually agitated. However the shear sensitivity of the culture means that mechanical agitation may be detrimental to cells and that cultures can not be transported using conventional pumps without significant loss of viability. Again immobilization may be a solution to these problems and may offer a microenviroment protected from sustained shear (Williams and Mavituna, 1992). The physical separation of the cells and medium in the immobilized system also makes for easy exchange of medium for purposes of metabolic control or nutrient replenishment. The composition of the culture medium can be readily and continuously monitored via an external loop, and the concentrations of O2, sugar, etc. adjusted as required. Similarly, extracellular products can be harvested
continuously by adsorption on a suitable resin, or by other means (Tyler et al.,
In the horse radish immobilized cells, the acid invertase activities were lowered
therefore the availability of intracellular sucrose for glucosylation was high, thus
glucosinolates were produced earlier than that of suspended cell cultures (Mevy
et al., 1999)
The main disadvantage of immobilization is that it is only of use with cell lines,
which excrete the product of interest into the culture medium. Attempt to induce
the release of products which are normally retained within the cells by such
techniques as permeabilisation have generally decreased cell viability to an
undesirable extend, although reversible permeabilisation of Catharanthus roseus
using dimethyl sulfoxide (DMSO) was promising (Williams and Mavituna, 1992).
Function of Immobilization

Immobilized plant cells, just like that of freely suspended cells can be used for
the purposes of bioconversion, the novo synthesis and sysnthesis from
Methods of Immobilization

As mentioned earliear that entrapment is part of immobilization. Entrapment
methods that have been used with plant cell cultures can be categorised into:
1. Gel entrapment by ionic network formation.
Entrapment by ionic network formation, especial y in the form of alginate beads,
is the most widely used method. Alginate is a polysaccharide that forms a stable
gel in the presence of cations, with calcium the most frequently used. Beads of alginate-containing cells, are formed by dripping a cell suspension-sodium alginate solution mixture into a stirred calcium chloride solution. κ-Carragenan can also be used in similar manner instead of alginate, using either calcium or potassium. Advantage of this method is that the gel can be reversible by adding EDTA. Moreover, synerisis can happen in the presence of other Calcium chelating agent such as phosphates (Williams and Mavituna, 1992). Cultivation of Morinda citrifolia, Catharanthus roseus and Digitalis lanata were successfully done by this method of immobilization, with significant increase of metabolite and the stability of metabolic capacity was also extended for long periods of time (Brodelius et al., 1979). Moreover the immobilized cells release the metabolite to the medium as also the case with maize plant cells (Zayed, 1997). 2. Gel entrapment by precipitation. Preparations of agar and agarose can be used to trap plant cells by precipitation. The polysaccahrides form gel when a heated aquoues solution is cooled. The gel can be dispersed into particles in the warm liquid state by mixing in a hydrophobic phase, e. g. olive oil. When particels of the desired size are obtained the entire mixture is cooled and this results in solidification (Williams and Mavituna, 1992). In the case for Catharanthus roseus, 5 gram of wet weight cells was suspended in 5% agarose at 40 degree Celcius. As quickly as possible the suspension was poured over a teflon plate covered with holes (diameter 3 mm). Another plate was used as support, and the two plates were holded together by clamps. After the agarose had solidified, the two plates were taken apart to release the cylindrical beads (Brodelius and Nilsson, 1980). Felix et al. (1981) found out that enzyme isolation was obviated and the enzymes were more stable in immobilized Catharanthus roseus cells (Felix et al., 1981). 3. Gel entrapment by polymerisation. Gel entrapment by polimerisation is most commonly carried out using polyacrylamide. However, the toxicity of the initiator and cross-lingking agents used in the polymerisation has in some cases caused a loss of cell viability. Brodelius and Nilsson (1980) showed that Catharanthus roseus cells entraped by polyacrylamide gel did not grow at all and hence respiration and plasmolysis were not detected. On the other hand, by suspending plant cells in aqueous solution of prepolymerised linear polyacrylamide partially substituted with acrylhydrazide groups, Galun and co-workers (1984) were successful to maintain the vitality of entraped microbial cells.
4. Entrapment in the preformed structures.
Entrapment in preformed structures involves some form of open network through
which nutrient medium may pass, but which entraps plant cells or cell
aggregates. Such structures can be facilitated by using cotton fibre, fibreglass
mats, reticulate polyurethane foam, and in a cloth nonwoven polyester short
The polyurethane foam has some merit as a matrix; no reagent which might not
toxic to plant cells, and no complicated operation causing microbial
contamination are required. Cells were immobilized via their invasion into pre-
formed polyurethane foam cut into blocks. Lindsey et al. (1983) immobilized
Capsicum frutescence cells in reticulate polyurethane foam, and showed that the
immobilized cells produced more capsaicin than the free cells.
The glass fibre material were shown to be an ideal substratum for immobilising
cultured Catharanthus roseus cells because of its high surface free energy and
large surface area to give maximum adhesion. This type of inert support
eliminates undefined physiological perturbartion in gel systems caused by the
high calcium content, the low phosphate level necessary to reduce calcium ion
chelation and the polysaccharide gel (Facchini and DiCosmo, 1991)
Factors Affecting Immobilization

Cell-Matrix interaction
It is important to note when using reticulated polyurethane foam, in order for any
immobilized cells to grow well, the volumetric fraction of the foam has to be
sufficient enough for all the cells and the reticulated pores of the foam is large
enough to contain the cells. Moreover, Hu and Yuan (1995) emphasize the
importance of initial interaction of cells with the surface of the polyurethane
particles, intrusion of cells into the foam, simultaneous growth and coalescence
of cells in the foam and retention of cells in the foam.
Mass Transfer
The transfer of compounds through immobilized cell matrix is usually assumed to be by molecular diffusion as in gel entrapment. Nevertheless, the microstructure of the immobilization matrix may bring other types into action such as capilary and active transports. These types of transport mechanism are true for reticulated foam, membrane and fibre mats matrices (Williams and Mavituna, 1992). Natural y, the resistance towards mass transfer that results in a decrease in the transport of nutrients, can be an advantage in creating a stress factor for secondary metabolite synthesis. Further, Tyler et al. (1995) stated that mass transfer restriction within the biomass can be minimised by surface immobilization in a layer form where there is maximum contact between the surface of the immobilized cultures and the liquid phase. Relationship between metabolism and dissolved oxygen concentration is complex, a conclusion can not be reached about the effect of reduced availability of oxygen in immobilized plant cell system on secondary metabolite production and growth. Alginate entrapped cells of Thalictrum minus were found to turn black owing to the insufficient supply of oxygen and they failed to produce berberine (Kobayashi, et. al., 1987). On the contrary, Wilkinson et al. (1988) discovered that a reduction in the dissolved oxygen concentration of the medium resulted in the production of capsaicin by Capsicum frutescens entrapped in polyurethane foam particles. Metabolism of cultures can be affected by periodic exposure to light, and the
quality and intensity of the light are significant. Only the outer cell layers of the
cultures in the immobilized matrix may receive some light. This may be
advantageous in the case where some precursors are form in light and some in
dark condition, such as Catharanthus alkaloids. The supply of light to the interior
of the immobilized cell matrix may be possible by the use of optical fibres.
Harvesting in Immobilized System

Immobilized plant cell cultures notably allows ease of continuous harvesting in
the large scale, provided that metabolites are excreted into the medium.
Some plant cells are able to release their secondary metabolites spontaneously
such as indoles, pyridines, quinolines, benzyl isoquinolines, quinolizidines,
anthraquinones, capsaicins, opines, phenolics and terpenoids. In certain cases,
immobilisation appears to induce spontaneous release of the products that are
normally stored within the cells in suspension (Williams and Mavituna, 1992).
The release of metabolites into the medium can be improved by the methods of
permeabilization and in-situ extraction. Two most popular approaches in
permeabilization involve surface-active chemicals such DMSO, phenetyl alcohol,
chroloform, triton X-100 and hexadesyltrymethylamonium bromide and
electroporation. Other permeabilization methods include ultrasonication and
ionophoretic release eventhough the use of these methods is discouraged due
possibility of cell damage (Williams and Mavituna, 1992).
In-situ adsorption and extraction can be performed by adding inert hydrophobic
chemicals (liquid or solid) especial y having high adsorption capacity for the
hydrophobic plant products into the cultures (Kim and Chang, 1990).
Scaling-Up (Bioreactor)
It is worthied to note that the time necessary to establish a large-scale volume of
plant cells is time-consuming and expensive process. Moreover, any large
bioreactors that must be used to compesate for the low volumetric productivity of
slow growing plant cell cultures are sensitive to contamination.
Nevertheless, immobilised plant cell bioreactor has been chosen over the
conventional stirred or fed batch bioreactor due to protection of cells from liquid
shear forcess allowing for increased mixing speeds and more efficient mass
transfer. It is also possible to use smaller reactor volumes since the slow growing
immobilised biomass can be maintained in a productive state growth for an
extended period. Separation of growth and production phases using easily
exchangeable growth and production media is feasible in the immobilised plant
cell bioreactors (Facchini and DiCosmo, 1991).
Lambie (1990) stated other advantageous of immobilized cell reactors as follows:
1. It leads to high cell concentration within the reactor. 2. It prevents washouts in continuous reactors. 3. It allows batch reactors to be operated on a drain/refill basis. 4. It permits specific spacial arrangement within the reactors. Type of Bioreactors for Immobilized Plant Cells A. Packed Bed Reactors. This type of reactor have been used with immbolized cells of Pseudomonas spp. in alginate beads for production of L-Cysteine (Ryu et al., 1996), It appeared this system have poor mass transfer characteristics and the beads may suffer from compresion under their own static weights (Lambie, 1990) B. Mechanically agitated and Airlift Reactors Surfaced immobilized cells of C. roseus (Archambault et al., 1989; Tyler et al., 1995) and T. rugosum (Faccini and DiCosmo, 1990) were placed in an agitated and airlift reactors for production of alkaloids. Viability of immobilized cells of T. rugosum cultivated in Bioreactores was the same as the one in shake flask but the accumulation of the protoberberine was lower than the one in the shake flask. This, however, was due to low ratio of innoculum to fresh medium in order to maintain a constant ratio of biomas to the fibre substratum. Mechanically agitated reactores might damage the plant cells or the beads (if immobilized in alginate) in which the cells are entrapped. In contrast, airlift reactore minimise damage to cells, but they are unsuitable for particles eg. Gel beads used to immobilized cells. Immobilized cells of Coffea arabica in alginates were photocultured using a bubble column reactor. The cells were damaged so severely at a low aeration rate that they neither grow nor produce alkaloids because of physical stress from thin film of bursting bubbles (Kurata et al., 1994; Kurata and Furusaki, 1993). Cells of Glycine max, Daucus carota, Petunia hybrida, Coffea arabica and Nicotiana tabacum were once cultivated using this reactor where their concentrated suspension of cells were introduced into the shell side of the reactor and medium aerated in separate researvoir was circulated through the fibres (Williams and Mavituna, 1992). Such reactors have several advantageous including good control of fluid dynamic and flow distribution, and the inherent advantage of using a membrane, of improved protection againsts contamination. However, membrane reactors are also expensive, liable to fouling, having problems with gas transfer and difficult to innoculate (Lambie et al., 1990). In this design the sheet of foam were suspended as vertical baffles in a stirred reactor so that the plant cells were incorporated into the network by the stirring to give solid sheets of cells. Furthermore, the immobilised cells are in direct contact with the nutrient medium; there is no permebiality barrier to nutrients and metabolites that could be created by the gel. This system was applied for immobilised cells of Capsicum frutescens (Lindsey et al. 1983; Williams and Mavituna, 1992).

Immobilisation has been used for several cell lines for either production of
metabolites or their biocoversion. For Capsicum frutescens and Catharanthus
roseus, immobilisation significantly affects the production of capsain and
alkaloids, respectively.
Further research is needed to investigate the possibility of immobilised plant cell
cultures to produce compound of interest economically. One paramount
requirement for large-scale production is that the cell has to be able to excrete
the compound of interest into the medium and hence continuous feeding and
harvesting can be achieved.
At the same token, there is also a need to obtain an optimised method for cell

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matrices, FEBS Letters, 122: 312 - 316.
Facchini, P. J. and DiCosmo, F., 1991, Plant Cell Bioreactor for the production of
protoberberine alkaloids from Immobilized Thalictrum rugosum cultures,
biotechnolgy and Bioengineering, 37: 397 - 403.
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and secondary metabolism of simultanously permeabilized and immobilized plant
cells, Analytical Biochemistry, 116: 462 - 470.
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plant cells immobilized in cross-linked polyacrylamide-hydrazide, Planta Medica,
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Nicotiana tabacum cells, Plant Cel Reports, 8: 475 - 478.
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cells in polyurethane foams, Chemical Engineering Science, 50: 3297 - 3301.
Johnson, T. S., Ravishankar, G. A. and Venkataraman, L. V., 1996,
Biotransformation of ferulic acid and vanyllylamine to capsicin and vanillin in
immobilized cell culters of Capsicum frutescens, Plant Cel , Tissue and organ
Culture, 44: 117 - 121.
Kim, D. J. and Chang, H.N., 1990, Enhance shikonin production from
Lithospermum erythrorhizon by insitu extraction and calcium alginate
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a bubble column reactor with control ed light intensity, Biotechnology and
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Kurata, H., Seki, M. and Furusaki, S., 1994, Light Effect to Promote Secondary Metabolite Production of Plant Cel Culture in Advances in Plant Biotechnology, Ryu, D. D. Y. and Furusaki, S., Elsevier, Amsterdam. Lambie, A. J., 1990, Commercial Aspects Of The Production Of Secondary Compounds By Immobilised Plant Cells in Secondary Product from Plant Tissue Culture, Charlwood, B. V. and Rhodes, M. J. C., (Eds), Clarendon Press, Oxford. Mevy, J. P., Rabier, J., Quinsac, A., and Ribaillier, D., 1999, Sucrose metabolism and indoleglucosinolate production of immobilized horseradish cells, Plant Cell, Tissue and Organ Culture, 57: 163 - 171. Pras, N. and Woerdenbag, H. J., 1999, Production of Secondary Metabolites by Bioconversion, in Biotechnology: Secondary Metabolites, Ramawat, K. G. and Merillon, J. M., (Editors), Science Publisher, Inc., USA. Rao, S. R. and Ravishankar, G. A., 2000, Biotransformation of protocatechuic aldehyde and caffeic acid to vanillin and capsaicin in freely suspended and immobilized cell cultures of Capsicum frutescens, Journal of Biotechnology, 76: 137 - 146. Ryu, O. H., Ju, J. Y. and Shin, C. S., 1996, Continuous L-cysteine production using immobilized cells reactors and product extractors, Process Biochemistry, 32: 201 - 209. Tyler, R. T., Kurz, W. G. W., Paiva, N. L. and Chavadej, S., 1995, Bioreactors for surface immobilized cells, Plant Cell, Tissue and Organ Culture, 42: 81 - 90. Wilkinson, A., Williams, P. and Mavituna, F., 1988, The Effect Of Oxygen Stress On Secondary Metabolites Production By Immobilized Plant Cells In Bioreactors, in Plant Cel Biotechnology, Ed. Pais, M., Mavituna, F. and Novais, J., Springer, Berlin. Williams, P. D. and Mavituna, F., 1992, Immobilized Plant Cells, in Plant Biotechnology: Comprehensive Biotechnology, Second Supplement, Fowler, M. W., Warren, G. S. and Moo-Young, M., Pergamon Press, Oxford. Zayed, G., 1997, Can immobilazation of Bacillus megaterium cells in alginate beads protect them against bacteriophages? Plant and Soil, 197: 1 - 7.


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