The co-production of 3-hydroxypropionic acid (3HP) and 1,3-propanediol (PDO) from glycerol was studied using the resting cells of a recombinant Klebsiella pneumoniae J2B strain that overexpresses an aldehyde dehydrogenase (KGSADH). Active biomass was produced in a mineral salt medium containing yeast extract and glycerol under a range of aeration conditions, and shifted to potassium phosphate buffer containing glycerol for bioconversion. The microaerobic or anaerobic conditions were favorable for both the production of active biomass and subsequent bioconversion. At the flask level, the recombinant strain (2.0 g CDW/L) grown under microaerobic conditions produced 43.2 mM 3HP and 59.0 mM PDO from glycerol (117 mM) in 30 min with a cumulative yield of 0.87 (mol/mol). The fed-batch bioconversion, which was performed in a 1.5-L bioreactor with 1.0 g CDW/L at a constant pH 7.0 under anaerobic conditions, resulted in 125.6 mM 3HP and 209.5 mM PDO in 12 h with a cumulative overall productivity, yield, and maximum specific production rate of 27.9 mmol/L/h, 0.71 (mol/mol), and 128.5 mmol/g CDW/h, respectively. Lactate, succinate and 2,3-butanediol were the major by-products, whereas the production of acetate and ethanol was marginal. This is the first report of the simultaneous production of 3HP and PDO from glycerol using a resting cell system.
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http://dx.doi.org/10.1007/s00253-012-4187-9 | DOI Listing |
Front Bioeng Biotechnol
November 2024
State Key Laboratory of Mycology, Institute of Microbiology, Chinese Academy of Sciences, Beijing, China.
1,3-Propanediol (1,3-PDO) is one of the important organic chemical materials and is widely used in polyester synthesis, and it also shows great potential in medicine, cosmetics, resins, and biodegradable plastics. So far, 1,3-PDO mainly comes from chemical synthesis. However, the by-products and the side effects during chemical synthesis of 1,3-PDO bring about serious damage to the environment.
View Article and Find Full Text PDFAngew Chem Int Ed Engl
December 2024
State Key Laboratory of Chemical Resource Engineering, College of Chemistry, Beijing University of Chemical Technology, Beijing, 100029, China.
Bioresour Technol
February 2025
School of Resources & Environment and Engineering Research Center of Watershed Carbon Neutrality of Ministry of Education, Nanchang University, 999 Xuefu Ave, Honggutan District, Nanchang 330047, PR China. Electronic address:
Glycerol hydrogenolysis to n-propanol (1-PO) represents an approach to realize synthesizing sustainable fuels from biodiesel byproduct. However, it suffers from harsh reaction conditions and noble catalysts. Herein, a simple Cu20/HZSM-5(Si/Al = 120) was fabricated, demonstrating high efficiency under mild conditions for non-noble metal catalysts, achieving a 71.
View Article and Find Full Text PDFBiotechnol Bioeng
February 2025
Faculty of Biotechnology, Federal University of Pará, Belém, Brazil.
Mathematical modeling and computer simulation are fundamental for optimizing biotechnological processes, enabling cost reduction and scalability, thereby driving advancements in the bioindustry. In this work, mathematical modeling and estimation of fermentative kinetic parameters were carried out to produce 1,3-propanediol (1,3-PDO) from residual glycerol and Klebsiella pneumoniae BLh-1. The Markov chain Monte Carlo method, using the Metropolis-Hastings algorithm, was applied to experimental data from a batch bioreactor under aerobic and anaerobic conditions.
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