Biochemical Reaction Engineering Mid - II, November - 2014
1.The overwhelming majority of industrial reactors are multiphase reactors. Most reactors contain
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Solid phase (biomass aggregates or biomass immobilized on carrier material)
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Liquid phase (water phase with pollutants / nutrient and products)
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Gas phase (air or gas feed, gaseous products CO2, N2, CH4)
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All of the above.
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Answer: D
2.Depending on the location of the cell aggregates / immobilized cells and the movement of carrier material three reactor categories can be distinguished:
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Mixed suspended particles (e.g. fluidized beds)
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Fixed particles or large surfaces (e.g. packed beds, trickling filters)
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Both a & b
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None of the above.
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Answer: C
3.Immobilization of biomass removes the washout limitation in continuous operation with
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Free cells
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Biological cells
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Suspended cells
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Electric cells
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Answer: A
4.Cell recycling is, however, an alternative to cell immobilization that might be considered for operation at high cell densities, both in fed-batch and …………. also for removing the washout limitation
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Continuous modes
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Fixed cell
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Suspended mode
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Moving surfaces
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Answer: A
5.Which flow in characteristic fashions, either dispersed in other phases or separately
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Gases
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Solids
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Liquids
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All of the above
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Answer: D
6.In an ideal plug-flow or batch reactor, all the elements of material leaving the reactors have been inside them for exactly the same amount of time. The time reaction elements has spent in a reactor is called
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Reaction time
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Product time
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Residence time
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Non residence time
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Answer: C
7.The model of CSTR with Bypassing and Dead Space can be used to describe this non-ideal flow existing inside a
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Real bioreactor
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Fluidised bed
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Non real bioreactor
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None of the above
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Answer: A
8.Based on the ways of substrate addition, we can divide the bioreactors into
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Batch
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Continuous categories
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Fed-batch
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All of the above
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Answer: D
9.Most fermentations outside of the food and beverage industry are carried out using
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Pure cultures
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Aseptic conditions
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Both a & b
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septic conditions
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Answer: C
10.To prevent contamination during this operation, all of the vessels are needed to maintain positive air pressure. The simplest method is to pressurize the inoculum vessels using
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Sterile air
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Autoclave
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Sterile water
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Hot air oven
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Answer: A
11.Design and operation of two-phase systems (liquid-solid) is considerably easier than_____________.
Answer: Three-phase reactors
12.Although for each type of immobilized cell system a variety of reactor types can be selected, optimal performance requires a careful matching of immobilization method and ___________________.
Answer: Reactor configuration
13.Cell recycling is, however, an alternative to cell immobilization that might be considered for operation at _________________.
Answer: High cell densities
14.The separation and recycling of cells can be achieved with the help of a ___________________.
Answer: Centrifugation/ settling or a membrane.
15.Flow patterns in these reactors are complex and phases rarely exhibit idealized _____________ or well-stirred flow behavior.
Answer: Plug-flow
16.__________model is mainly used to design medium continuous sterilization processes discussed previously or some enzyme catalytic reactions carriedout within tubular reactors.
Answer: The dispersion
17.Large bioreactors used for traditional fermentation industry, two parameter model ______________ and dead zone can be applied into these situations.
Answer: CSTR with bypassing
18.Bioreactors can also be classified according to the status of biomass within the reactors, that is, freely suspended or__________________
Answer: Or immobilized enzyme or cell bioreactors.
19.Typically, 3−5% of fermentations in an industrial plant are lost due to failure of_________________.
Answer: Sterilization procedures.
20.The gap between the rotating stirrer shaft and the fermenter bodies must be sealed properly. For small vessels_____________________ are preferential.
Answer: Magnetically driving stirrers