Volume 5 Supplement 8

22nd European Society for Animal Cell Technology (ESACT) Meeting on Cell Based Technologies

Open Access

DoE of fed-batchprocesses – model-based design and experimental evaluation

  • Onur Sercinoglu1,
  • Oscar Platas Barradas1,
  • Volker Sandig2,
  • An-Ping Zeng1 and
  • Ralf Pörtner1Email author
BMC Proceedings20115(Suppl 8):P46

DOI: 10.1186/1753-6561-5-S8-P46

Published: 22 November 2011


Experimental process-development and optimization is expensive and time-consuming. Real optimization by means of design of experiments involves data generation before optimization can be aimed for. This can make the way from process development to process establishment even harder, since academia or start-up research facilities might not have the possibility to generate these data. Furthermore, bioprocesses involving mammalian cells deal with many critical variables; processes are not only carried out batch wise, but increasingly in fed-batch mode with desired feeding profiles.

The use of DoE tools in combination with an appropriate growth model might allow the experimenter to develop and to test fed-batch strategies in silico, before experiments are carried out in the laboratory.

In our work, an unstructured model for mammalian cell culture was used for simulation. Kinetic parameters were derived from a small number of shake-flask experiments. The model was tested for data generation on common fed-batch strategies. By means of design of experiments strategies, relevant conditions were selected and experimentally tested. In this way, suitable fed-batch strategies for mammalian cell lines are evaluated in silico before bioreactor experiments are to be performed. This results in a significant reduction in the number of experiments during process development for mammalian cell culture.

Concept – fed-batchAnalyzer -

A tool was developed in Mathworks‘ Matlab for simulation of batch and fed-batch cultivations of mammalian cells. This program was created as a GUI (Guided User Interface), in which the user will be guided through the process of developing a fed-batch strategy. Growth models can be selected as well as different fed-batch modes. For a manageable comparison of fed-batch strategies, in silico experiments can be planned by design of experiments (DoE) and initial conditions as well as cell-line-specific kinetic parameters can be obtained from a reduced number of small-scale experiments e.g. shake flasks. The following steps will explain the procedure for in silico experimentation during the development of a fed-batch strategy for the human production cell line AGE1.hn (ProBioGen AG). Afterwards, one process condition will be chosen and tested in the laboratory.

Step 1: Define the process model

Growth models [1, 2] have been predefined for operation of the tool. However, the user can modify or include new models according to her/his expertise and knowledge of the cell line. For determination of model parameters, a reduced number of experiments in small scale (e.g. shake flasks), is to be performed.

Step 2: Load the model

Step 3: Choose a feeding strategy

Simple feeding strategies have been predefined in order to make the transfer of in silico results into laboratory experimentation easier. Constant feed, linear feed, exponential feed and step feed can be selected. New feeding profiles can be added to the program to improve its possibilities.

Step 4: Create design

The design (e.g. full factorial design) can be either planed within the program (MATLAB Statistics Toolbox) or loaded from other DoE tools (e.g. Design Expert). In order to define the central point for the design, data from batch experiments can be used.

Step 5: Run design

The tool conduct the in silico experiments and delivers a response. This is normally a variable the user is interested in (IVCD, VCD or product concentration).

Step 6: Obtain in silicoresults

For each set of conditions, the tool generates a sheet with virtual curves. For an overview of results and better comparison of the process conditions, a response curve can be generated (see Figure 1).
Figure 1

Surface response plan for a feeding strategy with constant feed rate.

Step 7: Implementation in the laboratory

Following experiment was planned and performed in a 1 L Bioreactor. (Table 1, Figure 2)
Table 1

Experimental conditions for validation of a contant feeding strategy.



Initial conditions ( batch )


10 mM


2 mM

fed-batch strategy



Glucose in Feed

60 mM

Glutamin in Feed

8 mM

Feed Rate

0.059 mL min-1

Feed Start

24 h

Figure 2

Experimental results after culture of AGE1.HN cells in bioreactor with a constant feed rate.



Funding by the BMBF, Grand Nr. 0315275A is gratefully acknowledged.

Authors’ Affiliations

Institute of Bioprocess and Biosystems Engineering, Hamburg University of Technology
ProBioGen AG


  1. Jang JD, Barford J.P: An Unstructured Kinetic Model of Macromolecular Metabolism in Batch and Fed-Batch Cultures of Hybridoma Cells Producing Monoclonal Antibody. Biochemical Engineering Journal. 4 (2): 153-168.
  2. Zeng A-P, Deckwer W-D: Mathematical modeling and analysis of glucose and glutamine utilization and regulation in cultures of continuous mammalian cells. Biotechnology and Bioengineering. 1995, 47: 3-View ArticleGoogle Scholar


© Sercinoglu et al; licensee BioMed Central Ltd. 2011

This article is published under license to BioMed Central Ltd. This is an open access article distributed under the terms of the Creative Commons Attribution License (http://creativecommons.org/licenses/by/2.0), which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.