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You Are On Multi Choice Question Bank SET 416

20801. The region of an airlift bioreactor in which the liquid travels in a downward direction is called the





20802. Population doubling time, td can be expressed as (where μ is the specific growth rate.)





20803. A higher Ks value of Monod's equation means





20804. The increased air flow rate in bubble column fermenter can cause excessive foaming and high retention of air bubbles in the column which





20805. Which of the following is correct for the prediction of time requirement in a batch fermenter?





20806. In an airlift bioreactor, the spent gases released from the liquid are called





20807. The contents in jet loop reactor are mixed through





20808. The specific growth rate (μ) is defined as





20809. The number of baffles in a standard stirred tank bioreactor is





20810. In the stationary phase





20811. Which of the following is an example of a mathematical model?





20812. Biomass concentrations during fermentation is





20813. Chemostats work on the principle of





20814. During the exponential phase the maximum specific growth rate equals specific growth rate as





20815. An internal draft tube is preferrred to an external draft tube because





20816. A functional relationship between the specific growth rate and essential compounds concentration was proposed by Monod in





20817. The optical density sometimes drops during the lag phase because





20818. The application of just in time (JIT) manufacturing techniques in biotechnology is important because





20819. Residence time distribution (RTD) of a reactor is independent of





20820. The bubble column fermenter is usually limited to





20821. A culture in a closed vessel to which no additional medium is added and from which no waste products are removed is called a __________ culture.





20822. If the specific growth rate, μ. is constant with time during the exponential growth period, the equation correlating bacterial number density Cn), cell number concentration with respect to time can be expressed as





20823. The diameter of the baffles in a standard stirred tank bioreactor ranges from





20824. During the log phase cell numbers increase exponentially





20825. Lag phase occurs mainly due to





20826. In a batch reactor specific growth rate





20827. Turbidostat is recommended when continuous fermentation needs to be carried out at





20828. The advantage of airlift bioreactors over stirred tank bioreactors of a similar size is





20829. Stirred tank fermenter (STF) can be employed for





20830. The specific growth rate is affected by





20831. The main function(s) of a draft tube in an air lift fermenter is/are to





20832. Which of the following is incorrect?




20833. The contents in bubble column and air lift reactor are mixed through





20834. Which of the following statements would be appropriate while comparing bubble column and air lift fermenter of the same size?





20835. During the lag phase





20836. Concentration of the growth limiting substrate means





20837. Tower fermentors are used for





20838. In wastewater treatment, which bioreactor is generally used?





20839. The contents in stirred tank rector are mixed through





20840. The height to diameter ratio (H/D) for the tank fermenters is





20841. The relatively large volume (10 to 40% of total fermenter volume) of the seed culture is employed to





20842. In an airlift bioreactor, the air sparging region is called





20843. The air riser is located on the outside of the draft tube for the large-scale airlift bioreactors because of





20844. At the end of the lag phase, when growth begins, the division rate increases gradually and reaches a maximum value in the exponential growth period. This transitional period is commonly called the accelerated growth phase and is often included as a part of the





20845. Which of the following(s) is/are considered the limitations of the exponential growth model?





20846. To describe components of an airlift bioreactor which of the follow-ings are generally included?





20847. The function of the disengagement zone in an airlift fermenter is to





20848. Stationary phase is described as





20849. In the accelerated phase, cell starts to





20850. The monod model predicts that the specific growth rate





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