galanthamine biosynthesis in plant in vitro systems
TRANSCRIPT
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Received: 17-May-2014; Revised: 18-Jul-2014; Accepted: 23-Sep-2014.
This article has been accepted for publication and undergone full peer review but has not been through the copyediting,
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Record. Please cite this article as doi: 10.1002/elsc.201300159.
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Review
Galanthamine biosynthesis in plant in vitro systems
Strahil Berkov
Institute of Biodiversity and Ecosystem Research, 23 Acad. G Bonchev Str, 1113 Sofia,
Bulgaria
Ivan Ivanov
Department of Organic Chemistry, University of Food Technology, 26 Maritza Boulevard,
Plovdiv 4002, Bulgaria
Vasil Georgiev
Laboratory of Applied Biotechnology, The Stefan Angeloff Institute of Microbiology,
Bulgarian Academy of Sciences, 139 Ruski Boulevard, Plovdiv4000, Bulgaria
Center for Viticulture and Small Fruit Research, Florida A&M University, 6505, Mahan
Drive, Tallahassee 32317, USA
Carles Codina
Departament de Productes Naturals, Biologia Vegetal i Edafologia, Facultat de Farmacia,
Universitat de Barcelona, Avda. Diagonal 643, 08028 Barcelona, Spain
Atanas Pavlov
Department of Analytical Chemistry, University of Food Technology, 26 Maritza Boulevard,
Plovdiv 4002, Bulgaria
Laboratory of Applied Biotechnology, The Stefan Angeloff Institute of Microbiology,
Bulgarian Academy of Sciences, 139 Ruski Boulevard, Plovdiv 4000, Bulgaria
Keywords: Acetylcholinesterase inhibitor, Biosynthesis, Bioreactors, Galanthamine, Plant in
vitro systems
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Abbreviations
AChE - acetylcholinesterase
DW – dry weight
FDA - U.S. Food and Drag Administration
Gal - galanthamine
GC-MS – gas chromatography–mass spectrometry
L-phe - L-phenylalanine
L-tyr - L-tyrosine
PAL - phenylalanine ammonia lyase
RITA -Récipient à Immersion Temporaire Automatique
TIS – temporarry immersion system
Abstract
The Amaryllidaceae alkaloid galanthamine is a long-acting, selective, reversible and
competitive acetylcholinesterase (AChE) inhibitor used for the treatment of early- to mid-
stage Alzheimer’s disease, poliomyelitis and other neurological diseases. Currently,
galanthamine is produced by extraction from plants such as daffodils (Narcissus cultivar
Carlthon), snowflake (Leucojum aestivum), ‘red-tubed lily’ (Lycoris radiata), and Ungernia
victoria, and alternatively by chemical synthesis. Due to the increased demand by the generic
pharmaceutical companies and the limited availability of plant sources, the biosynthesis of
galanthamine by plant in vitro systems has been considered as an alternative approach for its
sustainable production. The present article reviews the state-of-the-art of in vitro
galanthamine biosynthesis including growth regulators, medium components, culture
conditions, elicitation and bioreactor systems. It may be used as a starting point for further
studies in this area leading to a progress in biotechnological production of this valuable
alkaloid.
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1 Introduction
Galanthamine is an Amaryllidaceae alkaloid which is a long-acting, selective,
reversible and competitive acetylcholinesterase (AChE) inhibitor [1] crossing the blood-
brain, and marketed as a hydrobromide salt under the name of Razadine® (formerly
Reminyl®) and Nivalin® for the treatment of Alzheimer’s disease [2]. AChE is responsible
for the degradation of acetylcholine at the neuromuscular junction, in peripheral and central
cholinergic synapses and in parasympathetic target organs. AChE inhibitors compensate the
diminished cholinergic function and are widely used for symptomatic treatment of dementia.
Four AChE inhibitors have received approval for clinical use in early- to mid-stage
Alzheimer’s disease: tacrine, donepezil, rivastigmine and galanthamine. Tacrine, approved by
FDA in 1993, has been largely withdrawn due to adverse side effects, including possible liver
damage. Galanthamine hydrobromide have shown superior pharmacological profiles and
increased tolerance compared to the original AChE inhibitors, physostigmine or tacrine [3].
This natural compound stimulates pre- and postsynaptic nicotinic receptors and amplifies the
nerve-muscle transfer. Its pharmacological profile also includes causation of respiration and
reduction of the intraocular pressure. Besides this, it has shown a mild analeptic, analgesic,
hypotensive and a weak antimalarial activities [4].
Galanthamine was discovered in Galanthus woronowii by Proskurina and Yakovleva
in 1952 [5]. It has been first extracted by Sopharma (Bulgaria) in the early 1960s from G.
nivalis and later from considerably bigger plant Leucojum aestivum [6]. Galanthamine has
been found also in plants from the genera Amaryllis, Hippeastrum, Lycoris, Ungernia,
Narcissus, Zephyranthes, Hymenocallis, and Haemanthus [7] but it is currently being
extracted from daffodils (Narcissus cultivar Carlthon) in central and west Europe, snowflake
(Leucojum aestivum) in East Europe, ‘red-tubed lily’ (Lycoris radiata) in China, and
Ungernia victoria in Uzbekistan and Kazakhstan. Galanthamine content in plants used for
industrial extraction, reffered as percent from the dry weight, varies from traces to ca. 0.5%
(generally ca. 0.1-0.3%) in L. aestivum, from 0.10% to 0.15% in Narcissus cultivars, and up
to 0.52% in U. victoria [6].
The biosynthesis of galanthamine starts with enzymatic conversion of L-
phenylalanine (L-phe), including the enzyme phenylalanine ammonia lyase (PAL), and L-
tyrosine (L-tyr), including the enzyme tyrosine decarboxylase, to protocatechuic aldehyde
and tyramine, respectively. The junction of the tyramine and the protocatechuic aldehyde
results in a Schiff’s base, which is converted to norbelladine. Norbelladine or related
compounds could undergo oxidative coupling in Amaryllidaceae plants. 4’-O-
methylnorbelladine is considered as a key intermediate. Experiments with application of 13
C-
labelled O-methylnorbelladine to field grown Leucojum aestivum have indicated that the
biosynthesis of galanthamine involves the phenol oxidative coupling of O-
methylnorbelladine to a postulated dienone, which undergoes spontaneous conversion to N-
demethylnarwedine, giving norgalanthamine after stereoselective reduction. Norgalanthamine
is N-methylated to galanthamine in the final step of biosynthesis [8] (Figure 1). Later studies
indicated that deuterated-4'-O-methylnorbelladine is incorporated into three different groups
of Amaryllidaceae alkaloids that are biosynthesized by three modes of intramolecular
oxidative phenol coupling [9, 10].
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Plants remain the main source of galanthamine although its chemical synthesis has
been achieved [11]. Due to the increased demand by the generic pharmaceutical companies
and the limited availability of plant sources, the biosynthesis of galanthamine by plant in
vitro systems has been considered as an alternative approach for sustainable production of
this valuable natural product. The first articles on the biosynthesis of galanthamine by
Narcissus confusus and L. aestivum in vitro shoot cultures were published in the early 1990s
[12-18].
The undifferentiated cell cultures derived from N. confusus and L. aestivum produce
low levels of alkaloids – about 30 μg/g DW and 12 μg/g DW, respectively [17, 19, 20]. The
small amounts of alkaloids indicate that undifferentiated cell cultures are unsuitable for
development of a biotechnological process [17]. Differentiation results in an increased
amount of biosynthesized galanthamine and its related alkaloids [17, 20]. The biosynthesis of
galanthamine and the Amaryllidaceae alkaloids by shoot cultures derived from different
explants—bulbs [15, 16, 18, 20], young fruit, and seeds—has been investigated. They
accumulate 25 to 454 μg Gal/g DW [16]. There are also reports in scientific literature on the
successful transformation of L. aestivum with Agrobacterium rhizogenes, where the authors
obtained a transformed root culture with stable morphological characteristics, which,
however, did not produce galanthamine [21].
Callus re-differentiation in the shoot culture correlates with higher levels of alkaloids,
including galanthamine [19]. Cellular differentiation affects the biosynthetic pathway of
alkaloids, in particular it increases the para-ortho’ oxidative phenol coupling, yielding
galanthamine precursors [22]. The following studies demonstrate that shoot cultures are a
good experimental system for galanthamine and its accompanying alkaloids [15, 17].
2 Effect of growth regulators on galanthamine biosynthesis
Growth regulators significantly affect galanthamine biosynthesis because of their
specific connection with cellular differentiation. There are studies on the effect of auxins,
cytokinins, and ethylene on the yield of galanthamine. The maximum galanthamine yield of
1354 μg/g of fresh biomass in N. confusus shoot cultures was reported for 3 mg/L
benzyladenine, where the amount of biosynthesized galanthamine correlates with the
benzyladenine concentration [22]. Diop et al. [15] have discussed the variations in the
accumulation of galanthamine in L. aestivum in vitro cultures, grown in media with various
combinations of growth regulators. In the absence of growth regulators the amount of
galanthamine is 1.14x10-3
% of dry biomass. When cultivated in media with 10μM α-
naphthyl acetate and 0.5 μM benzyladenine, the highest yield was obtained – 6.79x10-3
% of
dry biomass. The influence of cytokinins (benzo adenine, zeatin, kinetin meta-topolin and
thidiazuron) on galanthamine biosynthesis by L. aestivum shoot cultures cultivated in RITA
systems with periodic agitation has been studied and it was found that the maximum yield of
galanthamine (0.05% DW) was achieved when the cytokinin thidiazuron was used [23].
The same authors have proved that ethylene exerts inhibitory action on the
biosynthesis of galanthamine and lycorine in various L. aestivum in vitro [24, 25]. The
ethylene precursor 1-aminocyclopropane-1-carboxylic acid on the other hand caused a six-
fold increase in the amount of accumulated galanthamine and it reached up to 2% of the dry
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biomass [25]. Tahchy et al. [26], studying the effect of growth regulators and sucrose
concentrations in tissue cultures of L. aestivum, Galanthus elwesii and N. pseudonarcissus
found a species specific response on AChE inhibitory activity and galanthamine content.
These results indicate that growth regulators affect secondary metabolism differently in
different in vitro cultures derived from the same plant. Their influence is specific and should
be studied separately for each individual culture. An overview of galanthamine content in
different in vitro systems is presented in Table 1.
3 Effect of medium components and cultivation conditions on galanthamine
biosynthesis
The optimization of the medium composition is an important step towards creating a
biotechnological process for biosynthesis of secondary metabolites [27]. Most often, the
composition of nutrient media is optimized with respect to the concentrations of the key
nutrient components (carbon, nitrogen and phosphorus sources) and/or the C/N ratio [28].
The links in the biological system “nutrient medium - in vitro culture - product(s)” are
examined by a multifactorial analysis. Then, depending on the results obtained, the nutrient
medium may be optimized to obtain maximum yields of the target product, biomass or both
[27].
The primary carbon source employed in in vitro systems biosynthesizing
galanthamine is sucrose [18, 27]. The study of the influence of sucrose amounts on
galanthamine biosynthesis in Narcissus confusus in vitro shoot cultures has found that the
highest amount of galanthamine (0.457 mg per culture) is accumulated at sucrose
concentration of 180 g/L in the nutrient medium [18]. At the same time, the best culture
growth was observed in a medium containing 90 g/L sucrose. The alkaloids haemanthamine,
tazetin and N-formilnorgalantamin accompanying galanthamine have maximum levels at low
sucrose concentrations. The sucrose concentration affects not only the biosynthesis of
alkaloids, but also the morphology of the test culture, and the activity of the photosynthetic
systems. For example, shoot cultures grown in sucrose concentration less than 9% are dark
green and consist of segments with foliage length of 5-6 cm. If grown in media with a higher
sucrose concentration, they are pale green with vitrification tendency, can form necrotic spots
and demonstrate late elongation. High sucrose levels are a stress factor affecting shoot
cultures also by changing the osmotic pressure [18]. On this basis, the optimization of the
nutrient media should be carried out not only with regard to the maximum yield of the target
product, but also should take into account the growth characteristics of the culture.
The combined influence has been studied of four independent variables in the culture
medium (sucrose, ammonium, nitrate and phosphate ions) on the production of biomass and
on galanthamine biosynthesis by a L. aestivum shoot culture by a multifactorial statistical
analysis [27]. The maximum values of the independent variables for a maximum
galanthamine yield were determined using a statistical analysis. Based on the results
obtained, Georgiev et al. [27] have proposed a modified variant of an MS growth medium for
maximum galanthamine biosynthesis by L. aestivum shoot cultures.
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The nitrogen source in the nutrient media, used for cultivation, is a combination of
ammonium and nitrate ions. It has been found that in the optimal medium at NO3-/NH4
+ ratio
of (8.6/1) the biosynthesized galanthamine has a maximum level, while in the standard
medium the ratio is 6.5/1. This phenomenon is accompanied by the fact that nitrate ions are
absorbed more slowly (compared to ammonia), and nitrogen is needed mainly in the form of
nitrate ions in the secondary metabolism of cells [27]. Another important factor in the
optimization of nutrient media is the C/N ratio. Maximum amounts of galanthamine are
biosynthesized at higher concentrations of the carbon source (C/N – 21/1) compared to the
standard medium (15/1) [29]. The elevated carbon and nitrogen concentrations expectedly
have a positive impact due to the relationship between the carbon source and the biosynthesis
of secondary metabolites, on the one hand, and the presence of a nitrogen atom in the
galanthamine molecule, on the other [27]. In the optimal medium the alkaloid profile in the
shoot culture also changes. GC-MS analyses revealed that by cultivating the in vitro culture
in the modified medium, an increase occurred in the relative concentrations of intracellular
galanthamine (1.14 times) compared to the total ion current [27].
4 Light as a factor influencing galanthamine biosynthesis
Light has a positive effect on the growth of in vitro cultures and on the production of
secondary metabolites, in particular galanthamine [13, 17]. Light affects the plant cell with
differentiated shoot cultures by changing its metabolism from heterotrophic to mixotrophic.
Light also enhances the biosynthesis of phenol-containing amino acids (phenylalanine and
tyrosine), which are alkaloid direct precursors, in particular galanthamine, by inducing the
shikimate pathway enzymes [30].
The N. confusus shoot cultures have a better growth index when cultivated under light
conditions compared to those grown in dark conditions [13]. In vitro systems cultivated under
light conditions have green leaves while those grown in the dark are with pale leaves. The
fresh to dry biomass ratio is higher when cultivation is conducted in the dark, due to
differences in metabolism. Cultures grown under light conditions have photomixotrophic
metabolism, and those grown in the dark have heterotrophic metabolism. Maximum
galanthamine production was achieved in cultures grown under light conditions [13].
The growth characteristics of the L. aestivum in vitro shoot culture cultivated under
light and dark conditions in flasks gave a clear picture of the relationship between
illumination, culture development and galanthamine biosynthesis [17].
The results of the comparative study of 10 L. aestivum shoot lines cultivated in dark
and light conditions show that there are no significant differences in the alkaloid profile of
the cultures, i.e. light synchronously activates the biosynthesis of all types of alkaloids
identified in the L. aestivum in vitro cultures [19]. Tyramine protoalkaloids decrease in the
light, which indicates that light activates the enzymes in the initial stages of the synthesis of
alkaloids as they are precursors in the biosynthetic pathway of the Amaryllidaceae alkaloids.
On the other hand, galanthamine in the cultures is more than twice as high as those cultivated
under light – 73.8 μg/g dry biomass, unlike those cultivated under dark conditions – 38.5 μg/
dry biomass [19].
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5 Elicitation
The main functions of secondary metabolites are associated with the protection of
plant organisms against various pathogens, as well as with their resistance to various biotic
and abiotic stress factors, whereas their biosynthesis is stress-induced by various elicitors and
signalling molecules [31]. On this basis a variety of strategies have been developed to
improve the yield of secondary metabolites by treating plant cells with elicitors or abiotic
stress [32]. Elicitors are chemical molecules or biofactors isolated from different sources that
can induce a physiological or morphological response by biosynthesizing phytoalexins [31].
Elicitation is a current commonly used method for optimization of the biosynthesis of various
secondary metabolites by plant in vitro systems.
Elicitation with biotic and abiotic elicitors is a method allowing a manifold increase in
the production of secondary metabolites by plant in vitro systems [33]. The effects of various
concentrations of four elicitors (methyl jasmonate, chitosan, arachidonic acid, and salicylic
acid) on galanthamine biosynthesis by Narcissus confusus shoot cultures have been studied
[34]. It has been found that the addition of methyl jasmonate at the start of the cultivation
process results in a twofold increase in the concentration of biosynthesized galanthamine.
Methyl jasmonate also increases the concentrations of the alkaloids accompanying
galanthamine: N-formyl-norgalanthamine, haemanthamine, homolycorine and pretazetine –
where the total amount of alkaloids is three times higher than the control. Schumann et al.
[29] studied the effect of copper sulphate, silver nitrate, salicylic acid and methyl jasmonate
on the growth and biosynthesis of galanthamine by L. aestivum shoot cultures. In that study
again it was found that methyl jasmonate increased galanthamine biosynthesis most strongly.
Recent studies in our laboratory [35] have indicated that methyl jasmonate increase mainly
the transcription of the enzyme phenylalanine ammonia lyase, and to a lesser degree that of
tyrosine decarboxylase. On the other hand, jasmonic acid advantageously increases the
transcription of tyrosine decarboxylase, and to a lesser extent the transcription of
phenylalanine ammonia lyase. Due to the different induction levels of both enzymes in the
initial stages of the biosynthetic pathway of Amaryllidaceae alkaloids by methyl jasmonate
and jasmonic acid, the biosynthesized galanthamine amounts are different. Galanthamine
biosynthesis was induced to the highest degree by jasmonic acid – 1.36 times more than the
control. This increase in galanthamine yield is due mainly to the enhanced expression of the
tyrosine decarboxylase gene, which in turn leads to an increase in the amounts of
biosynthesized tyramine – a direct precursor of the Amaryllidaceae alkaloids [35]. These
results indicate that the mechanisms of eliciting the biosynthesis of Amaryllidaceae alkaloids
are unclear and further in-depth studies are required on the interactions of jasmonic acid and
methyl jasmonate with the signal system that switches on in response to stress conditions in
the plant cell - calcium/calmodulin and protein phosphorylation/dephosphorylation, and the
induction and expression of the tyrosine decarboxylase and phenylalanine ammonia lyase
genes, as well as the other genes involved in the biosynthetic pathway of the Amaryllidaceae
alkaloids. The clarification of these relationships will have a significant impact on the
structuring of a cost-effective technology for the production of galanthamine from in vitro
systems of the Amaryllidaceae plants.
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6 Bioreactor systems for galanthamine biosynthesis
The cultivation of differentiated organ cultures in bioreactors is associated with a
number of difficulties, mainly due to their morphology. Culture growth requires bioreactors
of special design in terms of the mass transfer of nutrients and gas phase. Despite these
difficulties, various bioreactors have been developed for cultivation of shoot organ cultures
[36]. Bioreactors in plant biotechnology are used for micropropagation of various species of
decorative plants and industrial crops, as well as for the biosynthesis of various secondary
metabolites [36]. Cultivation in a bioreactor occurs in depth, which may result in limitation of
the gas exchange between the culture fluid and the in vitro culture, causing vitrification and
hyperhydration of the plant tissue [37]. To overcome the problems encountered in deep
cultivation in liquid media, different cultivation systems have been developed such as
bioreactors with liquid phase diffuser and culture systems with periodic agitation [38, 39].
Regardless of the ever-increasing interest in plant in vitro technologies for producing
biologically active substances (including galanthamine), up till now a large-scale technology
based on plant organ cultures has not been implemented. One of the main reasons for the
limited industrial application of plant shoot cultures are the difficulties associated with their
cultivation in large volumes. The various bioreactor systems used for the cultivation of plant
organ cultures all too often are with a complicated design and expensive. Another thing is
that the problem concerning the inoculation of the bioreactor systems with large workloads
has not been solved [1].
For the successful development and introduction of new biotechnology for
galanthamine production by plant organ cultures, it is essential to establish the optimal
conditions for the accumulation of the product and to choose the most productive culture
system (bioreactor system). The interest is primarily directed towards the systems with
periodic agitation, considering the biological matrix producer of galanthamine (organ
culture). These systems are characterized by a low level of mechanical stress and a low
degree of hyperhydration.
The main parameters (agitation period and cultivation temperature) affecting the
growth and synthetic characteristics of line L. aestivum G 80 in RITA culture system were
optimized by statistical analysis [40]. The maximum galanthamine yield, 265 μg/RITA (1.17
mg/L), was obtained under optimal conditions (15 min agitation period and 8 hours resting
period, cultivation temperature 26°C). The optimal conditions for galanthamine accumulation
coincide with the optimal growth conditions (GI – 2.98) and maximum absorption of the
nutrients [40]. Ivanov et al. [41] studied the effect of the agitation period and cultivation
temperature on the alkaloid profile of line L. aestivum G 80 cultivated in RITA® system. By
GC-MS analysis, it was found that the cultivation temperature had a significant influence on
the biosynthesis of alkaloids. The highest relative amount of galanthamine was synthesized at
22°C, twice as much as the amount synthesized at 26°C [41].
Schumann et al. [29] investigated the growth and biosynthetic characteristics of L.
aestivum shoot cultures cultivated in different bioreactor systems - TIS, bubble and air-lift
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column bioreactors. The agitation period and the amount of the culture were optimized. It
was found that the TIS system – 1L air-lift column bioreactor with agitation of 12 times daily
for 5 min was the most productive. In that cultivation system, productivity reached 214.7 μg
Gal/L per day, the in vitro culture biosynthesized 1.49 mg Gal/g DW. Good results were also
obtained in the cultivation of L. aestivum shoot cultures in the 1, 5 and 10 L bubble column
bioreactors (0.52, 0.72 and 0.68 mg Gal/g DW, respectively). It was found that maximum
galanthamine yield was obtained in deep cultivation conditions [29]. The authors did not
explore the influence of the cultivation conditions and type of cultivation system on the
alkaloid profile of the intracellular and extracellular alkaloid mixtures.
The course of bioreactor investigations has logically led to the further development of
a new type of cultivation system by Georgiev et al. [42]. The column bioreactor with internal
sections allows the distribution of the culture in separate sections in the whole reactor (Figure
2). This impedes the flotation of the culture and improves the mass transfer. That bioreactor
system entirely satisfies the requirements pointed out by Schumann et al. [29] for maximum
galanthamine yield. This system ensures good growth of the L. aestivum shoot cultures. A
maximum biomass yield of 20.8 g/L was achieved, which was about twice as high as the
yield obtained in the RITA cultivation system. The period of doubling the biomass was
shortened (from 282 h in the RITA system to 175 h in the modified column bioreactor); the
growth index increased. A statistical optimization method was used to obtain the optimal
values for the independent variables (cultivation temperature and air intake volume), that
influence galanthamine biosynthesis. A maximum galanthamine yield of line L. aestivum G
80 (1.7 mg/L) was reached at a cultivation temperature of 22°C and incoming air flow
velocity of 18 L/L.h. The yield achieved was 1.45 higher compared to the yield achieved in
the RITA cultivation system [42].
The authors investigated the effect of the growth conditions (intake airflow rate and
cultivation temperature) in a column bioreactor with inner sections on the alkaloid profile of
synthesized Amaryllidaceae alkaloids. Seventeen alkaloids of galanthamine, lycorine,
homolycorine and haemanthamine type were identified by a GC-MS analysis. Galanthamine
and lycorine were dominant, both in the intracellular and extracellular alkaloid mixtures (50-
70% of the total ion current for lycorine, and 19-60% of the total ion current for
galanthamine) [42]. The cultivation temperature had a significant influence on the alkaloid
profile in the cultivation of line L. aestivum G 80 in the column bioreactor with internal
sections. The relative concentration of the intracellular and extracellular galanthamine was
the highest at 22°C; similar results were also reported in the cultivation of line L. aestivum G
80 in the RITA® culture system [41, 42]. Under optimal conditions for galanthamine
biosynthesis of 22°C and intake airflow rate of 18 L/L.h, over 40% of the biosynthesized
galanthamine was extracellular with 45% purity of the total ion current. All these results
indicate that the column bioreactor with inner sections is a suitable cultivation system for
galanthamine production by shoot cultures of L. aestivum. The design of the bioreactor
allows a subsequent increase in the cultivation volume.
On this basis, a successful two-phase technology process can be developed for in situ
extraction of galanthamine biosynthesized in a column bioreactor with inner sections by
means of adsorption resins with low ion exchange capacity Amberlite XAD. This would
increase the yield of galanthamine, and would also increase its relative concentration, i.e.
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biosynthesis of galanthamine at the expense of the accompanying Amaryllidaceae alkaloids.
The reported galanthamine yields, though high, are not satisfactory for a large-scale in vitro
technology for galanthamine biosynthesis. It is necessary to breed new highly productive L.
aestivum shoot lines with new improved genetic characteristics that can ensure steady growth
on the one hand, and high yields of galanthamine, eliminating the accompanying alkaloids,
on the other.
7 Concluding remarks
Plant in vitro systems are an alternative for galanthamine bioproduction. However, the
obtained yields are still too low and not attractive for the pharmaceutical industry. To
overcome this disadvantage, an integrated approach for process optimization should be
applied. A critical point in such an approach is the development of a new suitable design of
bioreactors for shoot cultivation.
The authors have declared no conflicts of interest.
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Table 1. Galanthamine biosynthesis in different plant in vitro cultures
Plant In vitro culture Cultivation
system
Galanthamine
References
Narcissus
confussus
Callus
Shoot
Flask 30-60 μg/g DW
110-130 μg/g
DW
[11]
Leucojum
aestivum
Callus
Shoot
Flask 12 μg/g DW
100-200 μg/g
DW
[19, 41]
Shoot Flask 25-454 μg/g DW [26]
In vitro bulblets Flask 1.14-6.79x10-3
%
DW
[15, 21]
Shoot RITA 1.17 mg/L [16]
Shoot TIS systems 2.40 mg/g DW [25]
Shoot Bubble bioreactor 0.72 mg/g DW
Shoot Bubble column
bioreactor with
internal section
1.7 mg/L [9]
Shoot RITA 0.05% DW [35]
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Figure 1. Biosynthesis of galanthamine
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Figure 2. (A) Construction and (B) schematic diagram of modified bubble-column bioreactor
with internal sections: 1, bubble column with internal sections; 2, fluorescent lamps; 3, filters;
4, sampling. (C) Twenty-eight day of cultivation of L. aestivum line 80 shoot culture in
modified bubble-column bioreactor with internal sections at 22◦C and flow rate of inlet air of
18 L/(L·h) [18]