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Article

Simple Fed-Batch Strategy for Production of Capsular Polysaccharide by Haemophilus influenzae b at Pilot Scale

by
Mateus Ribeiro da Silva
1,2,
Silvia Maria Ferreira Albani
1,
Joaquin Cabrera-Crespo
1,†,
José Geraldo da Cruz Pradella
3 and
Mickie Takagi
1,*
1
Process Development Laboratory, Development and Innovation Center, Butantan Institute, São Paulo 05503-900, SP, Brazil
2
Bioprocess Laboratory, University of Campinas, UNICAMP, Campinas 13083-970, SP, Brazil
3
Bioprocess Laboratory—IP&D, University of the Paraiba Valley, UNIVAP, São José dos Campos 12000-000, SP, Brazil
*
Author to whom correspondence should be addressed.
In memoriam.
Bioengineering 2026, 13(2), 249; https://doi.org/10.3390/bioengineering13020249
Submission received: 30 November 2025 / Revised: 12 January 2026 / Accepted: 23 January 2026 / Published: 20 February 2026
(This article belongs to the Section Biochemical Engineering)

Abstract

Haemophilus influenzae b (Hib) is a pathogenic bacterium that causes meningitis worldwide, mainly in children less than two years old. The capsular polysaccharide b (PRP) is an essential antigen for vaccine formulation. This study aimed to develop a high-yield, technically accessible production strategy for PRP production to facilitate vaccine manufacturing in non-profit laboratories. Various fed-batch cultivation strategies were evaluated to address metabolic limitations and identify a robust, simplified process suitable for seamless scale-up to pilot scale. Glucose limitation strategies did not reduce inhibitory acetic acid accumulation due to deficiencies in Hib’s respiratory chain, whereas oxygen availability was identified as critical parameter. Increasing the specific air flow from 0.5 to 1.0 vvm in constant fed-batch (Cfb) resulted in a 33% yield increase, reaching 1706.40 mg PRP.L−1. However, the highest PRP concentration was achieved using exponential fed-batch with cell recycling (EfbCR), resulting in 1879.28 mg PRP.L−1. Although EfbCR offered high productivity, the Cfb strategy emerged to be the most technically feasible and robust solution and was successfully scaled up to an 80 L bioreactor, achieving 1885 mg PRP.L−1. These results advance understanding of PRP production by Hib and provides valuable insight into an efficient and simplified strategy for producing this key/vital vaccine antigen. The findings support the potential for cost-effective local production in public health initiatives.
Keywords: fed-batch cultivation; scale-up; capsular polysaccharide; Haemophilus influenzae; vaccine; pilot-scale fed-batch cultivation; scale-up; capsular polysaccharide; Haemophilus influenzae; vaccine; pilot-scale
Graphical Abstract

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MDPI and ACS Style

da Silva, M.R.; Albani, S.M.F.; Cabrera-Crespo, J.; da Cruz Pradella, J.G.; Takagi, M. Simple Fed-Batch Strategy for Production of Capsular Polysaccharide by Haemophilus influenzae b at Pilot Scale. Bioengineering 2026, 13, 249. https://doi.org/10.3390/bioengineering13020249

AMA Style

da Silva MR, Albani SMF, Cabrera-Crespo J, da Cruz Pradella JG, Takagi M. Simple Fed-Batch Strategy for Production of Capsular Polysaccharide by Haemophilus influenzae b at Pilot Scale. Bioengineering. 2026; 13(2):249. https://doi.org/10.3390/bioengineering13020249

Chicago/Turabian Style

da Silva, Mateus Ribeiro, Silvia Maria Ferreira Albani, Joaquin Cabrera-Crespo, José Geraldo da Cruz Pradella, and Mickie Takagi. 2026. "Simple Fed-Batch Strategy for Production of Capsular Polysaccharide by Haemophilus influenzae b at Pilot Scale" Bioengineering 13, no. 2: 249. https://doi.org/10.3390/bioengineering13020249

APA Style

da Silva, M. R., Albani, S. M. F., Cabrera-Crespo, J., da Cruz Pradella, J. G., & Takagi, M. (2026). Simple Fed-Batch Strategy for Production of Capsular Polysaccharide by Haemophilus influenzae b at Pilot Scale. Bioengineering, 13(2), 249. https://doi.org/10.3390/bioengineering13020249

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