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Previous year question hub

Bioreaction Engineering - Fundamentals of Biological Engineering - Biotechnology Previous Year Questions

Practice Bioreaction Engineering - Fundamentals of Biological Engineering - Biotechnology previous year questions organised from real papers, with year-wise coverage and clear topic navigation.

4Papers
4Years
22Questions
1Topics

Bioreaction Engineering question pattern

Every graph below is calculated only from this selection.

Questions by year

Year-wise coverage for Bioreaction Engineering. Each bar uses a separate theme-derived color.

Difficulty distribution

How the classified questions are distributed by difficulty.

Easy 13 59.1%
Medium 9 40.9%

Question type distribution

MCQ, numerical, multiple-select and other formats found in these papers.

MCQ 17 77.3%
Numerical Answer Type (NAT) 3 13.6%
Fill in the blanks 2 9.1%

Subject weightage

Top subjects by unique question coverage.

Biotechnology
22 Qs

Most asked topics

Top topics across the included previous year papers.

Fundamentals of Biological Engineering
22 Qs

Subtopic coverage

Top subtopics inside this exact selection.

Bioreaction Engineering
22 Qs

Paper coverage

Question coverage for the most populated papers. Every active PYP paper remains listed below.

Biotechnology (BT) 2025
1 Qs
Biotechnology (BT) 2019
1 Qs
Biotechnology (BT) 2013
10 Qs
Biotechnology (BT) 2012
10 Qs

Included previous year papers

Newest papers appear first. Sort by year, question coverage or name.

PaperYear / sessionQuestions in this viewOpen
Biotechnology (BT) 202520251View paper
Biotechnology (BT) 201920191View paper
Biotechnology (BT) 2013201310View paper
Biotechnology (BT) 2012201210View paper

All Bioreaction Engineering previous year questions

Practice every matching question in batches of 20, with every available option.

1
2013 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2013

The catalytic efficiency for an enzyme is defined as

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2
2013 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2013
A chemostat is operated at a dilution rate of \(0.6 h^{-1}\). At steady state, the biomass concentration in the exit stream was found to be \(30 g l^{-1}\). The biomass productivity (\(g l^{-1} h^{-1}\)) after 3h of steady state operation will be ________
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3
2013 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2013
In a batch culture, the specific rate of substrate utilization is \(0.25 g (g cell mass)^{-1} h^{-1}\) and specific rate of product formation is \(0.215 g (g cell mass)^{-1} h^{-1}\). Calculate the yield of product from the substrate(\(Y_{p/s}\)). ________
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4
2013 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2013

Determine the correctness or otherwise of the following Assertion (a) and Reason (r).

Assertion: Immobilization of plant cells can enhance secondary metabolite production during bioreactor cultivation.

Reason: Immobilization protects the plant cells from shear forces in the bioreactor.

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5
2013 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2013

The activity of an enzyme was measured by varying the concentration of the substrate (S) in the presence of three different concentrations of inhibitor (I) 0, 2 and 4 mM. The double reciprocal plot given below suggests that the inhibitor (I) exhibits

Question diagram

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6
2013 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2013
The maximum cell concentration (g l-1) expected in a bioreactor with initial cell concentration of 1.75 g l-1 and an initial glucose concentration of 125 g l-1 is (YX/S = 0.6 g cell/g substrate) ________
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7
2013 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2013
A fed batch culture was operated with intermittent addition of glucose solution at a flow rate of 200 ml h-1. The values of Ks, μm and D are 0.3 g l-1, 0.4 h-1 and 0.1 h-1, respectively. Determine the concentration of growth limiting substrate (gl-1) in the reactor at quasi-steady state. ________
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8
2013 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2013
The number of ligand binding sites present on receptors R1 and R3, respectively are

Question diagram

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9
2013 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2013

Which one of the receptors has the highest affinity for the ligand?

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10
2013 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2013
What is the holding period (min) at a k value of 3.36min-1?
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11
2019 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2019
Which one of the following can NOT be a limiting substrate if Monod's growth kinetics is applicable?
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12
2025 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2025
For the coupled reactions given below
Glucose 6-phosphate + H2O → Glucose + Pi (Reaction 1)
ATP + Glucose → ADP + Glucose 6-phosphate (Reaction 2)
the standard free energy change of ATP hydrolysis at 25 °C is __________ kJ/mol.
The equilibrium constants for Reaction 1 and Reaction 2 are 360 and 800, respectively; Gas constant R = 8.314 J mol-1 K-1. (Round off to two decimal places)
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13
2012 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2012

Choose the correct signal transduction pathway.

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14
2012 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2012
The activity of an enzyme is expressed in International Units (IU). However, the S.I. unit for enzyme activity is Katal. One Katal is
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15
2012 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2012

Identify the statement that is NOT applicable to an enzyme catalyzed reaction.

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16
2012 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2012
In an exponentially growing batch culture of Saccharomyces cerevisiae, the cell density is 20 g l-1 (DCW), the specific growth rate (μ) is 0.4 h-1 and substrate uptake rate (ν) is 16 g l-1 h-1. The cell yield coefficient YX/S will be
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17
2012 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2012
Determine the correctness or otherwise of the following Assertion (a) and Reason (r).
Assertion: Cell mass yield of a methylotrophic yeast is more on methanol compared to glucose.
Reason: Methanol has a greater degree of reductance compared to glucose.
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18
2012 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2012
An enzymatic reaction is described by the following rate expression.
\[ v = \frac{V_{max} s}{K_m + s + s^2/K_i} \]
Which one of the following curves represents this expression?

Question diagram

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19
2012 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2012
The free energy change for the transport of three Na⁺ out of the cell is
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20
2012 · Biotechnology · Fundamentals of Biological Engineering · Bioreaction Engineering
Biotechnology (BT) 2012
The free energy change for the transport of two K⁺ into the cell is
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Showing 20 of 22 questions