1988
DOI: 10.1016/0167-7012(88)90042-5
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The uses and future potential of microbial hollow-fibre bioreactors

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Cited by 32 publications
(7 citation statements)
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“…Ten milliliters of starter culture was inoculated into the shell side of the reactor through an inoculation port using a sterile 20-mL syringe fitted with a hypodermic needle. Cells were delivered into the outer spongy matrix layer of the hollow-fibers by pumping PBS into the reactor from the shell side, through the walls of the hollow fibers, and into the lumen of the latter (transverse or crossflow mode; Bunch, 1988) at a flow rate of 40 mL h −1 for 1 h. The shell side of the reactor was then rinsed with PBS at a flow rate of 60 mL h −1 for 30 min to remove residual cells in this compartment. The cells were grown in situ for 24 h using growth medium (Oxoid Nutrient Broth No.…”
Section: Hollow-fiber Bioreactormentioning
confidence: 99%
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“…Ten milliliters of starter culture was inoculated into the shell side of the reactor through an inoculation port using a sterile 20-mL syringe fitted with a hypodermic needle. Cells were delivered into the outer spongy matrix layer of the hollow-fibers by pumping PBS into the reactor from the shell side, through the walls of the hollow fibers, and into the lumen of the latter (transverse or crossflow mode; Bunch, 1988) at a flow rate of 40 mL h −1 for 1 h. The shell side of the reactor was then rinsed with PBS at a flow rate of 60 mL h −1 for 30 min to remove residual cells in this compartment. The cells were grown in situ for 24 h using growth medium (Oxoid Nutrient Broth No.…”
Section: Hollow-fiber Bioreactormentioning
confidence: 99%
“…Entrapment within hollow-fiber membranes was selected as the immobilization method of choice, offering one-step immobilization under gentle conditions, operational flexibility (gaseous and aqueous electron donors can be used), and complete containment of the cells, and therefore accumulated, reduced Tc (Bunch, 1988). A recent study compared the activities of resting cells of E. coli, pregrown anaerobically, and entrapped in membrane, foam, and gel matrices (Raihan et al, in press).…”
Section: Introductionmentioning
confidence: 99%
“…The solution must be free of particulate materials. 63 This reduces membranes fouling caused by unwanted materials thus increasing the membrane service life. Installation of filters before the reactor units and use of non-corrosive materials prevents particulate matter.…”
Section: Fluids Characteristicsmentioning
confidence: 99%
“…50,57,60 -62 They also have high volumetric productivity, simultaneous products separation, are easily reutilized, cheap enzyme fixation, little loss of the enzyme catalytic activity, high substrate concentration, and stable lipases activity. 62 -66 However, they have several drawbacks, for instance solutions must be free of particulate materials, use of specific type of fibre, 63 diffusion resistance 64,67 and enzyme conformational changes. 68,69 Other membrane configurations having only one connection to downstream/permeate-side such as the spiralwound are not suitable for the application.…”
Section: Tsp-emr: Basic Needsmentioning
confidence: 99%
“…In general, cells are cultivated in the outer shell space of the bioreactor with nutrients being supplied to the cells and (waste) products removed from the cells via the fibres. Many potential advantages of using hollow-fibre bioreactors over other systems have been identified (Bunch 1988). Several examples of their potential use with microbial cells have been mooted, including the production of lactic acid (VickRoy et al 1983) and ethanol (Inloes et al 1985).…”
Section: Introductionmentioning
confidence: 99%