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Engineering Life: Miracles in Biotechnology - Parts of fermenter-advanced

Grade 9CBSE

Review the key concepts, formulae, and examples before starting your quiz.

🔑Concepts

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The Fermenter (Bioreactor) is a specialized vessel designed to provide a controlled environment for the growth of microorganisms or animal/plant cells to produce specific metabolites or biomass.

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The Agitator/Impeller system is responsible for mixing the culture broth. It ensures a uniform distribution of nutrients and prevents the settling of cells. The mixing efficiency is often related to the Reynolds number (ReRe).

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The Sparger is a device (usually a ring with small holes) located at the bottom of the vessel that introduces sterile air or oxygen into the medium. It breaks the gas into small bubbles to increase the surface area for gas exchange.

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Baffles are metal strips attached to the inner wall of the fermenter. Their primary function is to break the circular flow (vortex) created by the impeller and convert it into turbulent flow for better mixing.

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The Cooling Jacket or internal coils are used to regulate the temperature. Since microbial growth is an exothermic process, the heat generated must be removed to maintain the optimal temperature (ToptT_{opt}).

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Probes and Sensors are critical for real-time monitoring. Common sensors include pHpH probes, Dissolved Oxygen (DODO) sensors, and temperature sensors (thermocouples) to maintain homeostasis.

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Headspace refers to the empty volume left at the top of the fermenter (usually 20%−30%20\% - 30\% of the total volume) to allow for foaming and gas exchange without clogging the exhaust filters.

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Sterilization is achieved using high-pressure steam. The vessel must be designed to withstand pressures typically around 1.1 kg/cm21.1 \text{ kg/cm}^2 at 121∘C121^\circ C.

📐Formulae

OTR=kLa(C∗−CL)OTR = k_L a (C^* - C_L) where OTROTR is the Oxygen Transfer Rate, kLak_L a is the volumetric mass transfer coefficient, C∗C^* is the saturated dissolved oxygen concentration, and CLC_L is the actual dissolved oxygen concentration.

D=FVD = \frac{F}{V} where DD is the Dilution Rate (h−1h^{-1}), FF is the flow rate of the medium (L/hL/h), and VV is the culture volume (LL).

Vcyl=πr2hV_{cyl} = \pi r^2 h to calculate the working volume of a cylindrical fermenter.

Pg=K(P2/ND3)0.45P_g = K (P^2 / N D^3)^{0.45} representing the Gassed Power (PgP_g) requirement in aerobic fermentation.

💡Examples

Problem 1:

A cylindrical fermenter has a radius of r=0.5 mr = 0.5 \text{ m} and a height of h=2 mh = 2 \text{ m}. If the vessel is filled to 75%75\% of its total height to allow for headspace, calculate the working volume VV of the medium. (Use π≈3.14\pi \approx 3.14)

Solution:

First, calculate the total volume of the fermenter: Vtotal=πr2hV_{total} = \pi r^2 h Vtotal=3.14×(0.5)2×2V_{total} = 3.14 \times (0.5)^2 \times 2 Vtotal=3.14×0.25×2=1.57 m3V_{total} = 3.14 \times 0.25 \times 2 = 1.57 \text{ m}^3 Now, calculate the working volume at 75%75\% capacity: Vworking=0.75×1.57V_{working} = 0.75 \times 1.57 Vworking=1.1775 m3V_{working} = 1.1775 \text{ m}^3 Since 1 m3=1000 L1 \text{ m}^3 = 1000 \text{ L}, the working volume is 1177.5 L1177.5 \text{ L}.

Explanation:

The working volume is the actual amount of liquid medium used, which is always less than the total volume to provide 'headspace' for gas expansion and foam formation.

Problem 2:

In a continuous culture fermenter, the medium is being fed at a flow rate of F=50 L/hF = 50 \text{ L/h} into a vessel with a fixed culture volume of V=250 LV = 250 \text{ L}. Calculate the dilution rate (DD).

Solution:

The formula for dilution rate is: D=FVD = \frac{F}{V} Substitute the given values: D=50250D = \frac{50}{250} D=0.2 h−1D = 0.2 \text{ h}^{-1}

Explanation:

The dilution rate represents the number of volumes of medium passing through the fermenter per unit time. It is the reciprocal of the residence time.