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Bioprocessing, elements

Microbial processes can also detoxify mercury ions and organic compounds by reducing the mercury to the elemental form, which is volatile (86). This certainly reduces the environmental impact of compounds such as methylmercury, however, such a bioprocess would have to include a mercury capture system before it could be exploited on a large scale with pubHc support. [Pg.37]

Always based on the use of IR spectrophotometry, a novel attenuated total reflection-Fourier-transform infrared (ATR-FTIR) sensor [42] was proposed for the on-line monitoring of a dechlorination process. Organohalogenated compounds such as trichloroethylene (TCE), tetrachloroethylene (PCE) and carbon tetrachloride (CT) were detected with a limit of a few milligrams per litre, after extraction on the ATR internal-reflection element coated with a hydro-phobic polymer. As for all IR techniques, partial least squares (PLS) calibration models are needed. As previously, this system is promising for bioprocess control and optimization. [Pg.261]

Based on these chemosensors, biosensors can be set up such as glucose or H2O2 sensors. In this case the appropriate biological compound (glucose oxidase or catalase) must be immobilized on the chemosensor. Different optical sensors are also used as transducer elements for the production of biosensors, especially of immuno-sensors. Here the affinity component is immobilized on the tip of the fiber and all available immuno-sensing assays can be performed using this transducer element. Since these sensors cannot be sterilized and used for on-line monitoring in a bioprocess we refer to other publications [25-27]. [Pg.23]

Disparate elements, which affect economic decisions for bioprocesses, can be combined into a logical approach. An attempt must be made to combine fundamentals of bioreactor design, downstream processing, and properties of biomolecules in the context of process evaluation. The ability to set technical priorities based on economic assessment is essential, and requires communication betv/een researchers, process engineers, technical managers, and marketing managers. [Pg.232]

Thermal Mass Flowmeters The trend in the chemical process industries is toward increased usage of mass flowmeters that are independent of changes in pressure, temperature, viscosity, and density. Thermal mass meters are widely used in semiconductor manufacturing and in bioprocessing for control of low flow rates (called mass flow controllers, or MFCs). MFCs measure the heat loss from a heated element, which varies with flow rate, with an accuracy of 1 percent. Capacitance probes measure the dielectric constant of the fluid and are useful for flow measurements of slurries and other two-phase flows. [Pg.60]

In this section we will consider the energetics of exopolysaccharide production in some detail. We will see how chemostat (substrate limited) derived yield coefficients and elemental balances can be used to determine how the nature of the substrate influences rates of metabolite production, and to give an indication of the scc for improvement of the producing micro-organism. You should note that for most industrial bioprocesses, the unavailability of data in the primary literature would prevent such an andysis. Further aspects of exopolysaccharide production are covered in Chapter 7 of flus text. [Pg.52]

ELECTROWINNING OF LEAD BATTERY PASTE WITH THE PRODUCTION OF LEAD AND ELEMENTAL SULPHUR USING BIOPROCESS TECHNOLOGIES... [Pg.803]

Theoretically, any biological recognition element can be interfaced to any of these types of transducers, provided an appropriate reaction product or analyte probe can be devised and measured. There are, however, a number of technical and practical issues which must be considered in the development of biosensors for environmental and bioprocess monitoring applications. In addition to a sensitive and specific response to the target analyte, biosensors which are most likely to find commercial success for these application areas, will require simple and inexpensive configurations which lend themselves easily to miniaturization and manufacturing techniques. [Pg.3]

It should also be emphasized that the coupling of FIA/SIA with diamond-based ATR probes for online bioprocess monitoring was found to be an excellent alternative to in situ measurements aiming to overcome biofilm formation and gas bubble adherence to the surface of the ATR element. [Pg.1280]

To construct a simple unstructured model for bioprocesses, at least one of the reactions taking place in the culture must be specified in kinetic terms. Generally a complete set of constitutive equations for each of the N chemical reactions taking place in the culture can be written in the form of a sum or a matrix (Roels, 1980a Schubert and Hofmann, 1975). The net conversion rate of each of the components present follows with the aid of r — v -r. For a system in steady state, the net production rate is equal to minus the flow into the system, as is clear from Equ. 2.10. Furthermore, the elemental balance principle (according Equ. 2.11) specifies k relationships between the flows Fj... [Pg.53]

Figure 5.23 gives the complete time course of a discontinuous growth processes the growth curve as a function of time is reflected in Fig. 5.1. Whenever a bioprocess shows an exceptional lag phase, the simple growth kinetics n(s) should be augmented with a time-dependent element n — /t(s, t). Figure 5.23 gives the complete time course of a discontinuous growth processes the growth curve as a function of time is reflected in Fig. 5.1. Whenever a bioprocess shows an exceptional lag phase, the simple growth kinetics n(s) should be augmented with a time-dependent element n — /t(s, t).
Figure 6.51. Diagrammatic representation of a steady-state bioprocess in balance area (reactor) following the macroscopic principle by analyzing elemental composition of significant process variables (substrate, nitrogen source, biomass, product, O2, CO2, H2O). (Adapted from Roels, 1980a.)... Figure 6.51. Diagrammatic representation of a steady-state bioprocess in balance area (reactor) following the macroscopic principle by analyzing elemental composition of significant process variables (substrate, nitrogen source, biomass, product, O2, CO2, H2O). (Adapted from Roels, 1980a.)...
The essential elements of an integrated bioprocess are as shown in Figure 6.1 (a) feedstock processing capability for the conversion of a wide variety of feedstocks to fermentable carbon and coproduct streams, preferably using enzymes, (b) engineered biocatalysts (cell factories) for the conversion of a variety of carbon substrates... [Pg.135]

Every bioprocess starts with the best possible cell factory. A better performing cell will allow for less capital, lower variable cost for the fermentation, and a simpler recovery process as the product will be more concentrated. More than one property makes for a good cell factory and none of the commonly used cell factories have all the needed attributes. Case-by-case development of a biocatalyst is still the norm, even though a platform for a given organism would help accelerate process development. Described below are elements from a process point of view to consider in choosing a biocatalyst for a bioprocess. [Pg.137]


See other pages where Bioprocessing, elements is mentioned: [Pg.84]    [Pg.85]    [Pg.96]    [Pg.635]    [Pg.117]    [Pg.271]    [Pg.15]    [Pg.216]    [Pg.478]    [Pg.487]    [Pg.283]    [Pg.185]    [Pg.191]    [Pg.1]    [Pg.460]    [Pg.65]    [Pg.640]    [Pg.15]    [Pg.455]    [Pg.206]    [Pg.4]    [Pg.5]    [Pg.194]    [Pg.194]    [Pg.72]    [Pg.382]    [Pg.395]   
See also in sourсe #XX -- [ Pg.104 ]




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