Team:Calgary/PHB Fermentation

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PHB Fermentation

Overview

In this stage of the process, VFA-rich stream from the previous step is fermented by engineered E. coli to produce PHB. This continuous fermentation process occurs in a 5L stirred-tank bioreactor at 37°C and under anaerobic conditions. A continuous flow of the VFA-rich stream is generated by the pump. To achieve continuous fermentation, a mechanical self-cleaning filter with 0.2-micron filters is used to separate and recycle bacteria back to the bioreactor. The resulting bacteria-free harvest stream that contains PHB is then passed to PHB extraction and water recovery. The proposed process is shown in Figure 1.

PHB Fermentation

Figure 1: Diagram of the proposed PHB fermentation process.

Design options considered

Other considered design options include:

  • External membrane bioreactor (EMB)
  • Immersed membrane bioreactor (IMB): specifically the hollow fiber and the flat sheet designs
  • Stirred-tank bioreactor with self-cleaning filter separation

The major disadvantage of membrane bioreactors is fouling. Because of fouling, frequent filter cleaning and filter replacement might be required resulting in higher crew-time requirements and transportation costs to supply replacement membranes.

The stirred-tank bioreactor, on the other hand, provides continuous agitation and easy temperature control, while the implementation of the self-cleaning filter reduces fouling. An example of a stirred tank bioreactor can be found following this link, certain specifications - like power, mass and volume of the following model were used in the ESM parameters estimation. An Example of smaller-scale self-cleaning filter can be found on the Eaton