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1.
J Biotechnol ; 93(1): 45-57, 2002 Jan 31.
Article in English | MEDLINE | ID: mdl-11690694

ABSTRACT

Physical microenvironmental parameters conducive to production of flavonoids in vitro from continuous Vaccinium pahalae suspension cultures were examined first in shake flask culture experiments, and results were used to guide adaptations of a bioreactor production environment. Anthocyanin pigments were primarily concentrated in smaller aggregates up to 519 microm diameter. Agitation at 150 rpm and routine use of a mechanical scraper to periodically retrieve cells thrown out of solution was sufficient to keep productive plant cell aggregates in bioreactor suspension. A set up for enhanced irradiance with mercury lamps providing an average of 240 micromol m(-2) s(-1) PPF at the inner surface of the bioreactor vessel was required to sustain anthocyanin productivity through a 10-day production cycle.


Subject(s)
Anthocyanins/biosynthesis , Vaccinium/metabolism , Anthocyanins/isolation & purification , Biomass , Bioreactors , Biotechnology , Light , Vaccinium/cytology , Vaccinium/radiation effects
2.
J Biotechnol ; 91(1): 63-74, 2001 Sep 13.
Article in English | MEDLINE | ID: mdl-11522363

ABSTRACT

The effects of different types of cell carriers, strategies for cell transfer on carriers, and of several fusion inhibitors on the growth kinetics of primary human myoblasts culture were studied in order to develop a bioprocess suitable for the treatment of Duchenne muscular dystrophy based on the transplantation of unfused cells. Our results indicate that myoblast production is larger on Cytodex 1 and 3 than on polypropylene or polyester fabrics and on a commercial porous macrocarrier. Myoblast growth conditions with Cytodex 1 were further investigated to establish the bioprocess operating conditions. It was found that microcarrier density of 3 g DW l(-1), inoculum density of 2x10(5) cells ml(-1), and continuous agitation speed of 30-rpm result in final myoblast production comparable to static cultures. However, for all the culture conditions used, myoblasts growth kinetics exhibited a lag phase that lasted a minimum of 1 week prior to growth, the end of the lag phase correlating with the appearance of microcarrier aggregates. Based on this observation, we propose that aggregation promotes cell growth by offering a network of very large inter-particular pores that protect cells from mechanical stress. We took advantage of the presence of these aggregates for the scale-up of the culture process. Indeed, using myoblast-loaded microcarrier-aggregates instead of myoblast suspension to inoculate a fresh suspension of microcarriers significantly reduced the duration of the lag phase and allowed the scale-up of the bioprocess at the 500-ml scale. In order to ensure the production of unfused myoblasts, the efficiency of five different fusion inhibitors was investigated. Only calpeptin (9.1 microg ml(-1)) significantly inhibited the fusion of the myoblasts, while TGFbeta (50 ng ml(-1)) and LPA (10 microg ml(-1)) increased myoblasts growth but did not affect fusion, sphingosine (30 microg ml(-1)) induced a 50% death and NMMA (25 microg ml(-1)) had no effect on either growth or fusion. Finally, transplantation trials on severe combined immunodeficient mice showed that microcarrier-cultured human myoblasts grown using the optimized bioprocess resulted in grafts as successful as myoblasts grown in static cultures. The bioprocess, therefore, prove to be suitable for the large-scale production of myoblasts required for muscular dystrophy treatment.


Subject(s)
Cell Culture Techniques/methods , Muscle, Skeletal/cytology , Animals , Cell Culture Techniques/instrumentation , Cell Division , Cell Fusion , Clone Cells , Humans , Infant , Mice , Mice, SCID , Muscle Development , Muscle, Skeletal/growth & development
3.
Biotechnol Bioeng ; 47(2): 131-8, 1995 Jul 20.
Article in English | MEDLINE | ID: mdl-18623385

ABSTRACT

Vitis vinifera cell suspension cultures carried out in shake flasks were closely examined for biomass growth and cell division in relation to carbohydrate, NH(4), NO(3)PO(4), and dissolved oxygen (DO)consumption. After inoculation, the oxygen uptake rate of the cultures measured on-tine was observed to increase continuously to a maximum value of 3.8 mmol O(2)L(-1)h(-1) at day 7 when cell division ceased and dissolved oxygen reached its lowest level of 17% air saturation. During this first phase of growth, the specific oxygen uptake rate remained constant at approximately 0.6 mmol 02 O(2) g(-1) dw h(-1)or approximately 2.2 mumol O(2), (10(6) cells)(-1) h(-1) whereas dry biomass concentration increased exponentially from 1.5 to 6.0 g dw L(-1). Thereafter, dry biomass concentration increased linearly to approximately 14 g dw L(-1) at day 14 following nitrate and carbohydrate uptake. During this second phase of growth, the biomass wet-to-dry weight ratio was found to increase in an inverse relationship with the estimated osmotic pressure of the culture medium. This corresponded to inflection points in the dry and wet biomass concentration and packed cell volume curves. Furthermore, growth and nutrient uptake results suggest that extracellular ammonium or phosphate ion availability may limit cell division. These findings indicate that cell division and biomass production of plant cell cultures may not always be completely associated, which suggests important new avenues to improve their productivity. (c) 1995 John Wiley & Sons, Inc.

4.
Biotechnol Bioeng ; 44(8): 930-43, 1994 Oct.
Article in English | MEDLINE | ID: mdl-18618911

ABSTRACT

Embryogenic cultures of a transformed Eschscholtzia californica cell line were carried out in a 11-L helical ribbon impeller bioreactor operated under various conditions to evaluate the performance of this equipment for somatic embryo (SE) production. All bioreactor cultures produced SE suspensions with maximum concentrations at least comparable to those obtained from flask control cultures ( approximately 8-13 SE . mL(-;1)). However, an increase of the mixingspeed, from 60 to 100 rpm, and low sparging rate ( approximately 0.05 VVM, k(L) a approximately 6.1 h(-;1)) for dissolved oxygen concentration (DO) control yielded poorer quality embryogenic cultures. The negative effects on SE production were attributed mainly to the low but excessive shear experienced by the embryogenic cells and/or embryoforming aggregates. High DO ( approximately 60% of air saturation) conditions favored undifferentrated biomass production and high nutrient uptake rates at the expense of the slower SE differentiation process in both flask and bioreactor cultures. Too low DO (-5-10%) inhibited biomass and SE production. The best production of SE ( approximately 44 SE . mL(-1) or approximately 757 SE . g dw(-1) . d(-1)) was achieved by operating the bioreactor at 60 rpm while controlling DO at approximately 20%by surface oxygenation only (0.05 VVM, k(L) a approximately 1.4 h(-;1)). This production was found to be a biomass production/growth-associated process and was mainly limited by the availability of extracellular phosphate, magnesium, nitrogen salts, and carbohydrates. (c) 1994 John Wiley & Sons, Inc.

5.
Biotechnol Bioeng ; 38(11): 1285-91, 1991 Dec 20.
Article in English | MEDLINE | ID: mdl-18600729

ABSTRACT

The plant Tripterygium wilfordii produces di- and triterpenes of interest for male contraception and treatment of arthritis and skin disorders. Cell line TRP4a obtained form this plant in 1981 was reported to produce these valuable compounds at yields ( approximately 0.04% of the biomass dry weight) higher than found in the plant (0.001%). In order to improve this production, studies were carried out to determine the feasibility of eliminating the troublesome component of coconut milk originally used to culture this cell line. A defined formulation suitable for growth ad maintenance has been developed. This medium consisted of Gamborg's PRL4 or B5 medium supplemented with 2 mg L(-1) 2,4-dichlorophenoxyacetic acid and 20 g L(-1) sucrose. Furthermore, monitoring of carbohydrate uptake revealed that T. wilfordii cells, contrary to many plant cell species, did not hydrolyze sucrose extra-cellularly before uptake. Replacement of this disaccharide by glucose or fructose increased specific growth rate from 0.15 to 0.25 day(-1). As tripdiolide is reported to be present in broth extract in significant amounts, plant cell immobilization technology offers a promising alternative to suspension cultures, especially in view to on line harvesting of the product. Surface immobilized T. wilfordii cell cultures were successfully carried out in 2-L bioreactors. Their biomass production and carbohydrate uptake were comparable to those observed for shake flask grown suspension cultures. Higher nitrate and ammonium uptake were found in immobilized cultures.

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