Culture media optimization for growth and phycoerythrin production from Porphyridium purpureum

Porphyridium spp. is a red micro alga and is gaining importance as a source of valuable products viz., phycobiliproteins (PB), sulfated exopolysaccharides, and polyunsaturated fatty acids with potential applications in the food and pharmaceutical industries. In the present study, the effects of the major media constituents of Porphyridium species were studied using response surface methodology (RSM) on biomass yield, total PB and the production of phycoerythrin (PE). A second order polynomial can be used to predict the PB and PE production in terms of the independent variables. The independent variables such as the concentrations of sodium chloride, magnesium sulfate, sodium nitrate, and dipotassium hydrogen phosphate influenced the total PB and PE production. The optimum conditions showed that total PB was 4.8% at the concentration of sodium chloride 26.1 g/L, magnesium sulfate 5.23 g/L, sodium nitrate 1.56 g/L, and dipotassium hydrogen phosphate 0.034 g/L. In case of optimum PE production (3.3%), the corresponding values are 29.62, 6.11, 1.59, and 0.076 g/L, respectively. PE production depends greatly on the concentrations of chloride, nitrate, and sulfate as well as phosphate of which the former possess the maximum effect.     

Role of intracellular carbonic anhydrase in inorganic-carbon assimilation by Porphyridium purpureum

Air-grown cells of Porphyridium purpurem contain appreciable carbonic-anhydrase activity, comparable to that in air-grown Chlamydomonas reinhardtii, but activity is repressed in CO₂-grown cells. Assay of carbonic-anhydrase activity in intact cells and cell extracts shows all activity to be intracellular in Porphyridium. Measurement of inorganic-carbon-dependent photosynthetic O₂ evolution shows that sodium ions increase the affinity of Porphyridium cells for HCO ₃ ^- . Acetazolamide and ethoxyzolamide were potent inhibitors of carbonic anhydrase in cell extracts but at pH 5.0 both acetazolamide and ethoxyzolamide had little effect upon the concentration of inorganic carbon required for the half-maximal rate of photosynthetic O₂ evolution (K_0.5[CO₂]). At pH 8.0, where HCO ₃ ^- is the predominant species of inorganic carbon, the K_0.5 (CO₂) was increased from 50 M to 950 M in the presence of ethoxyzolamide. It is concluded that in air-grown cells of Porphyridium. HCO ₃ ^- is transported across the plasmalemma and intracellular carbonic anhydrase increases the steady-state flux of CO₂ from inside the plasmalemma to ribulose-1,5-bisphosphate carboxylase-oxygenase by catalysing the interconversion of HCO ₃ ^- and CO₂ within the cell.Abbreviations AZ acetazolamide - EZ ethoxyzolamide - K_0.5[CO₂] half-maximal rate of photosynthetic O₂ evolution     

Effects of nitrogen on growth and carbohydrate formation in Porphyridium cruentum

The microalga Porphyridium cruentum (Rhodophyta) has several industrial and pharmaceutical uses, especially for its polysaccharide production. This study aimed to investigate the influence of nitrogen levels as reflected by altered N:P ratios on the production and content of biomass and carbohydrate. N:P molar ratios were altered in batch cultures to range from 1.6 to 50 using the Redfield ratio of 1:16 as reference. Algal growth (estimated as final cell number, biomass concentration and maximum specific growth rate) was negatively affected at low N:P ratios. The optimal N:P ratio for growth was identified at 35–50, with specific growth rates of 0.19 day^?1 and maximum cell concentrations of 59·10⁸ cells L^?1 and 1.2 g dry weight of biomass L^?1. In addition, variation in cell size was seen. Cells with larger diameters were at higher N:P ratios and smaller cells at lower ratios. The cellular carbohydrate content increased under reduced nitrogen availability. However, because accumulation was moderate at the lowest N:P ratio, 0.4 g per g dry weight biomass compared to 0.24 at the Redfield ratio of 16:1, conditions for increased total carbohydrate formation were identified at the N:P ratios optimal for growth. Additionally, carbohydrates were largely accumulated in late exponential to stationary phase.     

Scale-up cultivation enhanced arachidonic acid accumulation by red microalgae Porphyridium purpureum

Bioprocess and Biosystems Engineering - The present study attempts to cultivate Porphyridium purpureum under different scale-up conditions for further development and commercialization of...     

Induced cultivation pattern enhanced the phycoerythrin production in red alga Porphyridium purpureum

Bioprocess and Biosystems Engineering - Porphyridium purpureum is a rich source for producing phycoerythrin (PE); however, the PE content is greatly affected by culture conditions. Researchers have...     

Analysis of the complete plastid genome of the unicellular red alga Porphyridium purpureum

We determined the complete nucleotide sequence of the plastid genome of the unicellular marine red alga Porphyridium purpureum strain NIES 2140, belonging to the unsequenced class Porphyridiophyceae. The genome is a circular DNA composed of 217,694 bp with the GC content of 30.3 %. Twenty-nine of the 224 protein-coding genes contain one or multiple intron(s). A group I intron was found in the rpl28 gene, whereas the other introns were group II introns. The P. purpureum plastid genome has one non-coding RNA (ncRNA) gene, 29 tRNA genes and two nonidentical ribosomal RNA operons. One rRNA operon has a tRNA^Ala(UGC) gene between the rrs and the rrl genes, whereas another has a tRNA^Ile(GAU) gene. Phylogenetic analyses suggest that the plastids of Heterokontophyta, Cryptophyta and Haptophyta originated from the subphylum Rhodophytina. The order of the genes in the ribosomal protein cluster of the P. purpureum plastid genome differs from that of other Rhodophyta and Chromalveolata. These results suggest that a large-scale rearrangement occurred in the plastid genome of P. purpureum after its separation from other Rhodophyta.     

Efficient cultivation of Porphyridium purpureum integrated with swine wastewater treatment to produce phycoerythrin and polysaccharide

Journal of Applied Phycology - In the present study swine wastewater diluted at the different percentages (10%, 20%, 60%, and 100%) was used to cultivate the red alga Porphyridium purpureum to...     

Stable nuclear transformation of rhodophyte species Porphyridium purpureum: advanced molecular tools and an optimized method

Photosynthesis Research - A mutated phytoene desaturase (pds) gene, pds-L504R, conferring resistance to the herbicide norflurazon has been reported as a dominant selectable marker for the genetic...     

Growth of Porphyridium purpureum (Porphyridiales,Rhodophyta) and Production of B-Phycoerythrin under Varying Illumination

Russian Journal of Plant Physiology - The red pigment B-phycoerythrin (B-PE) belongs to the group of phycobiliproteins (PBPs). It is a part of the light-harvesting pigment complex of the red...     

Correction to: Induced cultivation pattern enhanced the phycoerythrin production in red alga Porphyridium purpureum

Bioprocess and Biosystems Engineering - The original version of the article unfortunately contained an error in Microalgae strain and culture medium section. Below is the corrected version.     

Kinetic models for growth and product formation on multiple substrates

Hydrolyzates from lignocellulosic biomass contain a mixture of simple sugars; the predominant ones being glucose, cellobiose and xylose. The fermentation of such mixtures to ethanol or other chemicals requires an understanding of how each of these substrates is utilized.Candida lusitaniae can efficiently produce ethanol from both glucose and cellobiose and is an attractive organism for ethanol production. Experiments were performed to obtain kinetic data for ethanol production from glucose, cellobiose and xylose. Various combinations were tested in order to determine kinetic behavior with multiple carbon sources. Glucose was shown to repress the utilization of cellobiose and xylose. However, cellobiose and xylose were simultaneously utilized after glucose depletion. Maximum volumetric ethanol production rates were 0.56, 0.33, and 0.003 g/L-h from glucose, cellobiose and xylose, respectively. A kinetic model based on cAMP mediated catabolite repression was developed. This model adequately described the growth and ethanol production from a mixture of sugars in a batch culture.     

Agitation effects on submerged growth and product formation of Aspergillus niger

Product formation of mycelial organisms, like Aspergillus niger, is intimately connected with their morphology. Pellet morphology is often requested for product formation. Therefore, it is important to reveal the influence of the hydrodynamic conditions on the morphological development. In the present study, pellet morphology and glucoamylase formation were studied under different agitation intensities of A. niger AB1.13. For pellet formation inside the bioreactor, without the use of precultures, it is necessary to work at low energy dissipation rates. Biomass growth and glucoamylase activity were correlated with energy dissipation. Furthermore, product yield was analysed in dependence of pellet size and concentration. The present work shows that simple equations based on Monod-kinetics can describe growth and product formation, in general, also in mycelian organisms. All measured morphological data, like pellet concentration, as well as glucoamylase formation, strongly depend on the hydrodynamic conditions.     

A metabolic network stoichiometry analysis of microbial growth and product formation

Using available biochemical information, metabolic networks have been constructed to describe the biochemistry of growth of Saccharomyces cerevisiae and Candida utilis on a wide variety of carbon substrates. All networks contained only two fitted parameters, the P/O ratio and a maintenance coefficient. It is shown that with a growth-associated maintenance coefficient, K, of 1.37 mol ATP/ C-mol protein for both yeasts and P/O ratios of 1.20 and 1.53 for S. cerevisiae and C. utilis, respectively, measured biomass yields could be described accurately. A metabolic flux analysis of aerobic growth of S. cerevisiae on glucose/ethanol mixtures predicted five different metabolic flux regimes upon transition from 100% glucose to 100% ethanol. The metabolic network constructed for growth of S. cerevisiae on glucose was applied to perform a theoretical exercise on the overproduction of amino acids. It is shown that theoretical operational product yield values can be substantially lower than calculated maximum product yields. A practical case of lysine production was analyzed with respect to theoretical bottlenecks limiting product formation. Predictions of network-derived irreversibility limits for Y(sp) (mu) functions were compared with literature data. The comparisons show that in real systems such irreversibility constraints may be of relevance. It is concluded that analysis of metabolic network stoichiometry is a useful tool to detect metabolic limits and to guide process intensification studies. (c) 1995 John Wiley & Sons, Inc.     

Analysis of microbial growth and product formation with Nitrate as Nitrogen source

Mass balance regularities are used to develop equations for the estimation of maintenance coefficients, true growth yields, and true product yields when nitrate is the nitrogen source. An available electron balance is presented that includes the uptake of nitrate. The application of the theory is illustrated using continuous-culture data of Stouthamer and Bettenhaussen in which Aerobacter aerogenes is grown aerobically with KNO₃ as the nitrogen source.     

Photoperiodic control of tetrasporangium formation in the red alga Rhodochorton purpureum

Six geographical isolates of Rhodochorton purpureum (Lightfoot) Rosenvinge (Rhodophyta, Nemalionales) formed tetrasporangia only in short days at 10°C. For most isolates, the critical day-length increased with latitude of origin from 9.5 h for an isolate from California to 14.5 h for one from Antarctica. Tetrasporangium production could be induced by 9–15 short-day cycles followed by a further 22–28 cycles in long days. A night-break consisting of 1 h of white light in the middle of a 16-h dark period inhibited the short-day response of isolates from low latitudes, but not those from higher latitudes. When a similar night-break was given in the middle of a 14-h dark period, however, the response of all isolates was at least partially inhibited. Night-breaks given at any time in the central 7 h of a 14-h dark period were equally inhibitory. Broad-band red light (0.3–0.4 mmol m^-2), given as a night-break, caused 50% inhibition of the short-day response. At a slightly higher photon exposure (0.6 mmol m^-2, given as 1 μmol m^-2 s^-1 for 10 min), narrow-band red (662 nm) and blue (448 nm) light caused similar inhibition, but green (547 nm) and far-red (731 nm) were ineffective as night-breaks. The inhibitory effect of a 10-min night-break with red light could not be reversed by subsequent exposure to an equal photon exposure of far-red light. These results add to the existing evidence that the pigments mediating photoperiodic responses among algae are more varied than those among flowering plants.     

Cultivation of hybridoma cells in continuous cultures: kinetics of growth and product formation

Mouse hybridoma cells were grown in suspension in continuous stirred bioreactors. Cell growth, substrate utilization, and monoclonal antibody (MAb) production were studied using serum-free medium. Steady-state data were obtained at different dilution rates, between 0.012 and 0.039 h(-1) Viability was profoundly affected by dilution rate, particularly near the lower end of the dilution-rate range investigated. MAb concentration and productivity went through a maximum with respect to dilution rate. Lactate yield on glucose declined with in creasing dilution rate. Experiments were carried out to study the effects of medium glucose concentration on cell growth, product formation, and lactate yield on glucose. Reduction of glucose concentration in the feed medium did not considerably affect cell density and MAb concentration in the culture, but lactate levels dropped sharply; lactate yield on glucose declined substantially, indicating alterations in cell metabolic path ways for energy metabolism. Optimization strategy for continuous cell culture is discussed.     

Factors affecting growth and product formation in plant cells grown in continuous culture

In the present work we examined the potential benefits of the continuous culture (chemostat) technique at improving biomass yields of Mentha and Dioscorea cells and product formation (diosgenin) by Dioscorea cells. In contrast to Mentha cells, Dioscorea cells were sensitive to mechanical agitation in the exponential growth phase and could only be grown in a bubble column type fermentor. Maximal biomass yield of 0.5 and 0.4 g cell dry weight g^?1sucrose were obtained for Mentha and Dioscorea cells, respectively. When the phosphate concentration during the growth phase of Dioscorea was increased, a maximal concentration of 7.8% diosgenin (of dry weight) was obtained. Productivity of diosgenin was 12 mg 1^?1 day^?1 in a two-stage continuous process as compared to 7.3 mg 1^?1 day^?1 in a batch culture.