Enhanced vincamine production in selected tryptophan-overproducing shoots of Vinca minor

Vinca minor is the sole source of vincamine, an alkaloid known to be used in a variety of cerebral disorders. Three stable variant shoot lines (V10, V20 and V30) with tolerance thresholds of 10, 20 and 30?mg/l 5-methyltryptophan (5-MT; analogue of tryptophan), respectively, were selected. These lines showed twofold to threefold increase in tryptophan content and 1.5- to 2-fold increment in the total alkaloids in comparison to the wild line shoots. A maximum of 16-fold enhancement in vincamine production was recorded in V30 line followed by eightfold in V20 line. Inter simple sequence repeat (ISSR)-PCR amplification of all the three lines showed total of 65 bands; out of which 60 were monomorphic (92.3?%) and 5 were polymorphic (7.7?%). Tryptophan being a limiting factor in the indole alkaloid pathway plays a crucial role in modulating the flux towards vincamine production and its over-production positively resulted into enhanced vincamine production.     

Overexpression of a Catharanthus tryptophan decarboxylase (tdc) gene leads to enhanced terpenoid indole alkaloid (TIA) production in transgenic hairy root lines of Rauwolfia serpentina

To enhance the production of terpenoid indole alkaloids in Rauwolfia serpentina, Catharanthus tryptophan decarboxylase (Crtdc) gene was over-expressed in transgenic hairy root cultures using Agrobacterium rhizogenes-mediated transformation. Among six transgenic hairy root lines, line RT4 accumulated the highest alkaloid content, with 0.1202 % dry weight (DW) reserpine and 0.0064 % DW ajmalicine, after 10 weeks of culture. Whereas, wild-type roots accumulated 0.0596 ± 0.003 % DW reserpine and 0.0011 ± 0.001 % DW ajmalicine. Transgenic hairy root line RT7 produced the lowest alkaloid content (reserpine: 0.0896 ± 0.002 % DW; ajmalicine: 0.002 ± 0.0 % DW). On the basis of alkaloid content the six hairy root lines were grouped as RT4/RT2 > RT3/RT5 > RT7/RT8. Analysis of gene expression profile indicated that Crtdc was expressed at a higher level in transgenic lines, which could be correlated with enhanced metabolite accumulation in roots. This study confirms that over-expression of Crtdc is a superlative method to improve the biosynthetic potential of Rauwolfia hairy root cultures. Enhanced reserpine and ajmalicine production can serve as an alternative choice to provide resources for relative pharmaceutical industries.     

Nutrition and bioprocess development for efficient biosynthesis of an antitumor compound from marine-derived fungus

An integrated nutrition and bioprocess strategy was developed for improving the biosynthesis of an antitumor compound, 1403C, by a marine-derived fungus, Halorosellinia sp. (no. 1403). First, statistical design strategies were synthetically applied to optimize the nutritional composition. The resulting 1403C production reached 2.07 g/l, which was 143.5 % higher than the original production. However, it only produced 0.44 g/l of 1403C in 5-l bioreactor fermentation. Thus, the operating parameters including culture pH, dissolved oxygen, agitation speed, impeller type and inoculum level were considered to improve the fermentation process, and an effective control strategy for 1403C production by Halorosellinia sp. submerged in a 5-l bioreactor was established. When inoculating 0.22 g/l dry biomass, controlling dissolved oxygen not lower than 30 % during the growth phase but ranging between 30 and 40 % during the stationary phase, using a double-layer six-flat-blade Rushton disc turbine agitated at 400 rpm, keeping short-term low pH and rapid-rising pH with glucose starvation, the highest 1403C production was finally obtained at 1.32 g/l, which was promoted by 200 % compared to before optimization. Fermentation scale-up was finally performed in a 500-l bioreactor, and 1403C production of 1.09 g/l was obtained.     

Expression of the Arabidopsis feedback-insensitive anthranilate synthase holoenzyme and tryptophan decarboxylase genes in Catharanthus roseus hairy roots

In plants, the indole pathway provides precursors for a variety of secondary metabolites. In Catharanthus roseus, a decarboxylated derivative of tryptophan, tryptamine, is a building block for the biosynthesis of terpenoid indole alkaloids. Previously, we manipulated the indole pathway by introducing an Arabidopsis feedback-insensitive anthranilate synthase (AS) alpha subunit (trp5) cDNA and C. roseus tryptophan decarboxylase gene (TDC) under the control of a glucocorticoid-inducible promoter into C. roseus hairy roots [Hughes, E.H., Hong, S.-B., Gibson, S.I., Shanks, J.V., San, K.-Y. 2004a. Expression of a feedback-resistant anthranilate synthase in Catharanthus roseus hairy roots provides evidence for tight regulation of terpenoid indole alkaloid levels. Biotechnol. Bioeng. 86, 718-727; Hughes, E.H., Hong, S.-B., Gibson, S.I., Shanks, J.V., San, K.-Y. 2004b. Metabolic engineering of the indole pathway in Catharanthus roseus hairy roots and increased accumulation of tryptamine and serpentine. Metabol. Eng. 6, 268-276]. Inducible expression of either or both transgenes did not lead to significant increases in overall alkaloid levels despite the considerable accumulation of tryptophan and tryptamine. In an attempt to more successfully engineer the indole pathway, a wild type Arabidopsis ASbeta subunit (ASB1) cDNA was constitutively expressed along with the inducible expression of trp5 and TDC in C. roseus hairy roots. Transgenic hairy roots expressing both trp5 and ASB1 show a significantly greater resistance to feedback inhibition of AS activity by tryptophan than plants expressing only trp5. In fact, a 4.5-fold higher concentration of tryptophan is required to achieve 50% inhibition of AS activity in plants overexpressing both genes than in plants expressing only trp5. In addition, upon a 3 day induction during the exponential phase, a trp5:ASB1 hairy root line produced 1.8 times more tryptophan (specific yield ca. 3.0 mg g(-1) dry weight) than the trp5 hairy root line. Concurrently, tryptamine levels increase up to 9-fold in the induced trp5:ASB1 line (specific yield ca. 1.9 mg g(-1) dry weight) as compared with only a 4-fold tryptamine increase in the induced trp5 line (specific yield ca. 0.3 mg g(-1) dry weight). However, endogenous TDC activities of both trp5:ASB1 and trp5 lines remain unchanged irrespective of induction. When TDC is ectopically expressed together with trp5 and ASB1, the induced trp5:ASB1:TDC hairy root line accumulates tryptamine up to 14-fold higher than the uninduced line. In parallel with the remarkable accumulation of tryptamine upon induction, alkaloid accumulation levels were significantly changed depending on the duration and dosage of induction.     

Submerged cultivation of Stephania glabra (Roxb.) Miers cells in different systems: Specific features of growth and accumulation of alkaloid stepharine

Strains of a Stephania glabra suspension culture grown in flasks and two types of bioreactors (laboratory-scale bubble and pilot-scale stirred reactors) have been compared according to their growth characteristics and accumulation of the alkaloid stepharine. The best characteristics have been recorded for strains 113 and 261. In the case of batch cultivation in flasks, the maximal accumulation of dry biomass by these strains reaches 19–21 g/l; that of the alkaloid stepharine, 0.30–0.35% of dry biomass. The used strains differ in their response to cultivation scale-up from flasks to bioreactors, strain 254 displaying the lowest adaptation to such changes. A bubble reactor is the most beneficial system for submerged cultivation of S. glabra. The absence of detectable stepharine synthesis on the background of a considerable decrease in all growth characteristics of the cultures has been observed when using a pilot stirred bioreactor. The batch cultures of strains 113 and 261 in a bubble bioreactor accumulate 11–16 g/l of dry biomass containing 0.05–0.16% of the alkaloid. It has been shown that strains 113 and 261 retain satisfactory physiological characteristics in a semi-flow regime of a bubble bioreactor. This scale-up scheme can be used for further industrial cultivation.     

A promising approach on biomass accumulation and withanolides production in cell suspension culture of Withania somnifera (L.) Dunal

Withanolide is one of the most extensively exploited steroidal lactones, which are biosynthesized in Withania somnifera. Its production from cell suspension culture was analyzed to defeat limitations coupled with its regular supply from the plant organs. In order to optimize the different factors for sustainable production of withanolides and biomass accumulations, different concentrations of auxins or cytokinins and their combinations, carbon sources, agitation speed, organic additives and seaweed extracts was studied in cell suspension culture. Maximum biomass accumulation (16.72 g fresh weight [FW] and 4.18 g dry weight [DW]) and withanolides production (withanolide A 7.21 mg/g DW, withanolide B 4.23 mg/g DW, withaferin A 3.88 mg/g DW and withanone 6.72 mg/g DW) were achieved in the treatment of Gracilaria edulis extract at 40 % level. Organic additive l-glutamine at 200 mg/l in combination with picloram (1 mg/l) and KN (0.5 mg/l) promoted growth characteristics (11.87 g FW and 2.96 g DW) and withanolides synthesis (withanolide A 5.04 mg/g DW, withanolide B 2.59 mg/g DW, withaferin A 2.36 mg/g DW and withanone 4.32 mg/g DW). Sucrose at 5 % level revolved out to be a superior carbon source yielded highest withanolides production (withanolide A 2.88 mg/g DW, withanolide B 1.48 mg/g DW, withaferin A 1.35 mg/g DW and withanone 2.47 mg/g DW), whereas biomass (7.28 g FW and 1.82 g DW) was gratefully increased at 2 % level of sucrose in cell suspension culture. This optimized protocol can be utilized for large scale cultivation of W. somnifera cells in industrial bioreactors for mass synthesis of major withanolides.     

Polyunsaturated fatty acid production by marine bacteria

Polyunsaturated fatty acids are important in maintaining human health. Limitations associated with current sources of ω-3 fatty acids and ω-6 fatty acids, from animal and plant sources, have led to increased interest in microbial production. Marine bacteria may provide a suitable alternative, although the isolation of production strains and the identification of operating conditions must be addressed before manufacturing processes become economically viable. Marine isolate 560 was identified as an eicosapentaenoic acid (EPA) producer via GC/MS. The isolate was initially identified as Vibrio cyclitrophicus by 16S rRNA sequencing. Statistically based experimental designs were applied to the optimisation of medium components and environmental factors for the production of EPA. A Plackett–Burman design was used to screen for the effect of temperature, pH, and media components. Subsequently, the concentrations of NaCl, yeast extract, and peptone, identified as significant factors, were optimised using a central composite design. The predicted optimal combination of media components for maximum EPA production (4.8 mg/g dry weight) was determined as 7.9 g/l peptone, 16.2 g/l NaCl, and 6.2 g/l yeast extract. On transfer of this process to bioreactor cultivation, where a range of pH and DO values were tested, the maximum amount of EPA produced increased to 7.5 mg/g dry weight and 10 % of the total fatty acid.     

Mist trickling bioreactor for <Emphasis Type="Italic">Centaurium erythraea</Emphasis> Rafn growth of shoots and production of secoiridoids

Shoots of Centaurium erythraea Rafn were cultivated in 5 l mist trickling bioreactor for 21 and 28 days increasing their dry weight from 0.54 g to 13.7 g and 18.3 g, respectively. About 6880 shoots from 223 initial shoot-tips in 21-day bioreactor producing cycle were produced. The shoots could be successfully rooted and transferred to soil. Secoiridoid accumulation (expressed as a sum of gentiopicroside, sweroside and swertiamarin) in shoots after 21 days of culture reached about 303 mg l⁻¹.     

Phenylalanine and tyrosine accumulating cell lines of a dihaploid potato selected by resistance to 5-methyltryptophan

The selection and characterization of 5-methyltryptophan (5-MT) resistant cell lines is described in a dihaploid potato, clone H²578(007). The frequency of resistant calli was increased by treatment of a cell suspension with N-ethyl-N-nitroso-urea. Two lines, 5-MT-21 and 5-MT-26, accumulated tyrosine (160 nMol and 1546 nMol/g fresh callus), and the third, 5-MT-27, accumulated both tyrosine (841 nMol/g fresh callus) and phenylalanine (451 nMol/g fresh callus). In the wildtype tyrosine and phenylalanine content was 65 nMol and 42 nMol/g callus, respectively. The tryptophan content of line 5-MT-26 was significantly increased, from 20 nMol/g to 76 nMol/g fresh callus. The total free amino acid content of the three variant cell lines was higher than that of the wildtype. Variant cell lines 5-MT-21, -26 and -27 showed a low degree of resistance to 5-MT, when grown on a selective medium and were cross-resistant to parafluorophenylalanine and 3-fluorotyrosine, analogues of phenylalanine and tyrosine.Abbreviations ENU N-ethyl-N-nitroso-urea - 5-MT 5-methyltryptophan - 3-FT 3-fluorotyrosine - PFP parafluorophenylalanine - AEC S-(2-amino-ethyl) L-cysteine     

Alkaloid production by plant cell cultures of Holarrhena antidysenterica: II. Effect of precursor feeding and cultivation in stirred tank bioreactor

Precursor feeding strategy for increasing the yield of conessine, a steroidal alkaloid of Holarrhena antidysenterica, was established in cell suspension culture. A total of 50 mg/L added cholesterol was converted into 43 mg/L of alkaloid, 90% of which constituted the conessine. By applying the precursor feeding policy to the cell suspension culture in modified Murashige and Skoog (MS) medium, a total of 143 mg/L of alkaloid was produced in 8 days. In this way the alkaloid content of the cells was increased more than six times compared to that obtained in the standard MS medium. The steps leading to biotransformation of cholesterol into alkaloids were unaffected by phosphate. The shake flask data were successfully transferred to a bench scale 6-L stirred tank bioreactor in which the specific biosynthetic rate of alkaloid production was 110 mg/100 g dry cell weight per day, about 160 times higher than that of whole plant.     

Adventitious root culture of <Emphasis Type="Italic">Polygonum multiflorum</Emphasis> for phenolic compounds and its pilot-scale production in 500 L-tank

Polygonum multiflorum Thunb. is an important medicinal plant that synthesizes an array of phenolic compounds. Its roots are used in a variety of pharmacological and cosmetic formulations, notably as hair dye. In the present study, the inoculum density (3–15 g/L) and culture period (1–7 weeks) were optimized in a 3 L bioreactor. High root biomass (14.18 g/L dry weight (DW)) was recorded with an inoculum of 7 g/L (p?≤?0.05), which is consistent with the results for 5 and 10 g/L. However, significantly higher yield of bioactive compounds (53.87 mg/g DW total phenolics and 27.96 mg/g DW total flavonoids) with high free radical scavenging activity was obtained in root samples from 5 g/L inoculum density. A 4 week culture period was sufficient for optimum root growth and metabolite production. The optimized conditions were used for large-scale (5 and 20 L) and pilot-scale (500 L) studies. Considering that the continuous aeration of root cultures may lead to oxidative stress, antioxidant enzyme activity and lipid peroxidation also were studied. The results revealed high catalase (CAT) and guaiacol peroxidase (G-POD) activities, and low malondialdehyde (MDA) production, with increasing culture scale (20 and 500 L), which may indicate low-level oxidative damage to the cultures. An optimal yield of 4.01 kg dry root biomass with 287.12 mg/L of total phenolic productivity was achieved in a 500 L pilot-scale bioreactor. This work can pave the way for commercial production of biomass and secondary metabolites at the industrial level, and meet the rising demand for natural ingredients, especially in the pharmaceutical and cosmetic industries.     

Production of carotenoids and lipids by <Emphasis Type="Italic">Rhodococcus opacus</Emphasis> PD630 in batch and fed-batch culture

Production of carotenoids by Rhodococcus opacus PD630 is reported. A modified mineral salt medium formulated with glycerol as an inexpensive carbon source was used for the fermentation. Ammonium acetate was the nitrogen source. A dry cell mass concentration of nearly 5.4 g/L could be produced in shake flasks with a carotenoid concentration of 0.54 mg/L. In batch culture in a 5 L bioreactor, without pH control, the maximum dry biomass concentration was ~30 % lower than in shake flasks and the carotenoids concentration was 0.09 mg/L. Both the biomass concentration and the carotenoids concentration could be raised using a fed-batch operation with a feed mixture of ammonium acetate and acetic acid. With this strategy, the final biomass concentration was 8.2 g/L and the carotenoids concentration was 0.20 mg/L in a 10-day fermentation. A control of pH proved to be unnecessary for maximizing the production of carotenoids in this fermentation.     

Influence of medium salt strength and nitrogen source on biomass and metabolite accumulation in adventitious root cultures of Pseudostellaria heterophylla

We investigated the effects of medium salt strength and ammonia/nitrate ratio on biomass production and metabolites accumulation of adventitious root. The medium with full-strength Murashige and Skoog (MS) reached the highest growth rate (16.77), and the contents of saponin and polysaccharide reached the peak (i.e., 0.65 and 24.85 %) at 3/4 MS and 1 MS, respectively. In case of ammonia/nitrate ratio, a NH₄ ⁺/NO₃ ^? ratio of 20:40 was optimal for the production of biomass and polysaccharide (23.27 %). In contrast, the content of saponin achieved the optimum (0.74 %) at a NH₄ ⁺/NO₃ ^? ratio of 30:30. In 5-L balloon-type bubble bioreactor (BTBB) cultures, an approximately 23-fold increase in biomass was recorded. The fresh weight (FW) and dry weight (DW) were 72.78 and 6.79 g per bioreactor with the contents of saponin (0.62 %) and polysaccharide (17.32 %), respectively. It indicated potential application to produce adventitious roots of pseudostellaria heterophylla with bioreactors on large scale in commercial.     

Improved production of withanolides in shoot suspension culture of Withania somnifera (L.) Dunal by seaweed extracts

The influence of Gracilaria edulis and Sargassum wightii extracts was investigated for the production of biomass and withanolides in the multiple shoot suspension culture of Withania somnifera. Supplementation of 40 % G. edulis extract in MS liquid medium for 24 h exposure time in the culture recorded the highest biomass accumulation [62.4 g fresh weight and 17.82 g dry weight (DW)] and withanolides production (withanolide A 0.76 mg/g DW; withanolide B 1.66 mg/g DW; withaferin A 2.80 mg/g DW and withanone 2.42 mg/g DW) after 5 weeks of culture, which were 1.45–1.58-fold higher than control culture. This naturally available G. edulis extract-treated multiple shoot suspension culture protocol offers a potential alternative for the optimum production of biomass and withanolides utilizing shake-flasks.     

Expression of a feedback-resistant anthranilate synthase in Catharanthus roseus hairy roots provides evidence for tight regulation of terpenoid indole alkaloid levels

Different plant species produce a variety of terpenoid indole alkaloids, which are of interest as plant defensive secondary metabolites and as valuable pharmaceuticals. Although significant progress has been made, the mechanisms regulating the levels of this important class of compounds require continued elucidation. Previous precursor feeding studies have indicated that alkaloid accumulation can be improved during the exponential growth phase of hairy root cultures through enhanced tryptophan availability. To test this relationship, transgenic hairy root cultures of Catharanthus roseus were established with a glucocorticoid-inducible promoter controlling the expression of an Arabidopsis feedback-resistant anthranilate synthase alpha subunit. Enzyme assays demonstrated that the Arabidopsis alpha subunit is compatible with the native beta subunit and that anthranilate synthase activity is more resistant to tryptophan inhibition in induced than in uninduced extracts. The metabolic effects of expressing the feedback-resistant anthranilate synthase alpha subunit were also dramatic. Over a 6-day induction period during the late exponential growth phase, tryptophan and tryptamine specific yields increased from almost undetectable levels to 2.5 mg/g dry weight and from 25 microg/g to 267 microg/g dry weight, respectively. The greater than 300-fold increase in tryptophan levels observed in these studies under certain induction conditions compares favorably with the fold increases obtained in previous constitutive expression studies. Despite the large increases in tryptophan and tryptamine, the levels of most terpenoid indole alkaloids were not significantly altered, with the exception of lochnericine, which increased 81% after a 3-day induction period. These results suggest that terpenoid indole alkaloid levels are tightly controlled.     

Pilot-scale culture of somatic embryos of Eleutherococcus senticosus in airlift bioreactors for the production of eleutherosides

Purpose of work

To establish pilot scale bioreactor cultures of somatic embryos of Siberian ginseng for the production of biomass and eleutherosides. Somatic embryos of Eleutherococcus senticosus were cultured in airlift bioreactors using Murashige and Skoog medium with 30 g sucrose l^?1 for the production of biomass and eleutherosides. Various parameters including the type of bioreactor, aeration volume, and inoculum density were optimized for 3 l capacity bioreactors. Balloon-type airlift bioreactors, utilizing a variable aeration volume of 0.1–0.3 vvm and an inoculum of 5 g l^?1, were suitable for biomass and eleutheroside production. In 500 l balloon-type airlift bioreactors, 11.3 g dry biomass l^?1, 220 µg eleutheroside B l^?1, 413 µg eleutheroside E l^?1, and 262 µg eleutheroside E1 l^?1 were produced.     

Polymer production by two newly isolated extremely halophilic archaea: application of a novel corrosion-resistant bioreactor

A novel corrosion-resistant bioreactor composed of polyetherether ketone (PEEK), tech glass and silicium nitrite ceramics was constructed and applied for the cultivation of two newly isolated, extremely halophilic archaea producing poly(γ-glutamic acid) (PGA), or poly(β-hydroxy butyric acid) (PHB), respectively. These bacteria were isolated from hypersaline soil close to Aswan (Egypt). The isolate strain 40, which is related to the genus Natrialba, produced large amounts of PGA when cultivated on solid medium. Culture conditions were optimised applying the corrosion-resistant bioreactor. PGA production was dependent on NaCl concentration and occurred about at 20% (w/v) NaCl in the medium. A maximum cell density of about 1.6 g cell dry matter/l was obtained when the bioreactor was stirred and aerated in a batch fermentation process using proteose-peptone medium. The supernatant was monitored with respect to PGA formation, and after 90 h a maximum of 470 mg/l culture volume was detected by HPLC analysis. Culture conditions were optimized for the isolate 56, which accumulated PHB as intracellular granules. Batch fermentations in the stirred and aerated bioreactor applying acetate and n-butyric acid as carbon sources led to cell density of 2.28 g cell dry matter/l and a maximum PHB accumulation contributing to about 53% of cellular dry weight. About 4.6 g PHB were isolated from 10.6 g dried cells of strain 56, which exhibited a weight average molar mass of 2.3 × 10⁵ g mol⁻¹ and a polydispersity of about 1.4. Received: 3 December 1999 / Received revision: 22 February 2000 / Accepted: 25 February 2000     

Selection of fungal elicitors to increase indole alkaloid accumulation in catharanthus roseus suspension cell culture

Various fungal elicitors derived from 12 fungi were tested to improve indole alkaloid production in Catharanthus roseus cell suspension cultures. Results show that different fungal mycelium homogenates stimulate different kinds of indole alkaloid (ajmalicine, serpentine and catharanthine) accumulation, which ranged from 2- to 5-fold higher than the control. Some fungal culture filtrates also efficiently elicited the biosynthesis of different indole alkaloids. The optimal elicitor addition and exposure time for the maximal alkaloid production were on day 7 after subculture and for 3 days of treatment but different fungal elicitors showed the different optimal treatment dosages. Additions of elicitor at the doses ranging from 5 mg/l to 30 mg/l of carbon hydrate equivalent resulted in varieous amounts and kinds of indole alkaloid accumulation. Exposed to a same fungal elicitor, several different cell lines generated the different responses regarding as growth rate, culture color and alkaloid production.     

Development of a bioprocess to convert PET derived terephthalic acid and biodiesel derived glycerol to medium chain length polyhydroxyalkanoate

Sodium terephthalate (TA) produced from a PET pyrolysis product and waste glycerol (WG) from biodiesel manufacture were supplied to Pseudomonas putida GO16 in a fed-batch bioreactor. Six feeding strategies were employed by altering the sequence of TA and WG feeding. P. putida GO16 reached 8.70 g/l cell dry weight (CDW) and 2.61 g/l PHA in 48 h when grown on TA alone. When TA and WG were supplied in combination, biomass productivity (g/l/h) was increased between 1.3- and 1.7-fold and PHA productivity (g/l/h) was increased 1.8- to 2.2-fold compared to TA supplied alone. The monomer composition of the PHA accumulated from TA or WG was predominantly composed of 3-hydroxydecanoic acid. PHA monomers 3-hydroxytetradeeanoic acid and 3-hydroxytetradecenoic acid were not present in PHA accumulated from TA alone but were present when WG was supplied to the fermentation. When WG was either the sole carbon source or the predominant carbon source supplied to the fermentation the molecular weight of PHA accumulated was lower compared to PHA accumulated when TA was supplied as the sole substrate. Despite similarities in data for the properties of the polymers, PHAs produced with WG present in the PHA accumulation phase were tacky while PHA produced where TA was the sole carbon substrate in the polymer accumulation phase exhibited little or no tackiness at room temperature. The co-feeding of WG to fermentations allows for increased utilisation of TA. The order of feeding of WG and TA has an effect on TA utilisation and polymer properties.