Klebsiella pneumoniae HR526, a new isolated 1,3-propanediol (1,3-PD) producer, exhibited great productivity. However, the accumulation of lactate in the late-exponential phase remained an obstacle of 1,3-PD industrial scale production. Hereby, mutants lacking D-lactate pathway were constructed by knocking out the ldhA gene encoding fermentative D-lactate dehydrogenase (LDH) of HR526. The mutant K. pneumoniae LDH526 with the lowest LDH activity was studied in aerobic fed-batch fermentation. In experiments using pure glycerol as feedstock, the 1,3-PD concentrations, conversion, and productivity increased from 95.39 g L(-1), 0.48 and 1.98 g L(-1) h(-1) to 102. 06 g L(-1), 0.52 mol mol(-1) and 2.13 g L(-1) h(-1), respectively. The diol (1,3-PD and 2,3-butanediol) conversion increased from 0.55 mol mol(-1) to a maximum of 0.65 mol mol(-1). Lactate would not accumulate until 1,3-PD exceeded 84 g L(-1), and the final lactate concentration decreased dramatically from more than 40 g L(-1) to <3 g L(-1). Enzymic measurements showed LDH activity decreased by 89-98% during fed-batch fermentation, and other related enzyme activities were not affected. NADH/NAD(+) enhanced more than 50% in the late-exponential phase as the D-lactate pathway was cut off, which might be the main reason for the change of final metabolites concentrations. The ability to utilize crude glycerol from biodiesel process and great genetic stability demonstrated that K. pnemoniae LDH526 was valuable for 1,3-PD industrial production.

1,3-Propanediol (PDO), is now taking the transition from a traditional "specialty chemical" to a "commodity chemical". The market for PDO is growing rapidly as the technology develops. With the advancing PDO production technology, polytrimethylene terephthalate (PTT) as a new type of polyester has been applied in carpet and textile fibers, monofilaments, films, and nonwoven fabrics, and in the engineering thermoplastics area, because PTT has unique properties compared to other polymers such as polyethylene terephthalate (PET) and polybutylene terephthalate (PBT). Responding to the environmental and sustainability factors, one- or two-step fermentation technology for PDO production has attracted people's attention. A novel flexible process for PDO production by using aerobic fermentation from glycerol or glucose has been developed and demonstrated with a facility capacity of 4000 t/year in a pilot plant. By using engineered Escherichia coli, 135 g/L PDO was obtained with glucose as feedstock. Since the bio-process of PDO production consumes 40% less energy and reduces greenhouse gas emissions by 20% versus petroleum-based propanediol, the bio-based PTT is more environmentally friendly and sustainable compared with the fossil fuel-based polymers, which made PTT more attractive with good prospects for the future.

Microbial fermentation under strictly anaerobic conditions has been conventionally used for the production of 1,3-propanediol, a key raw material required for the synthesis of polytrimethylene terephthalate (PTT) and other polyester fibers. In the current study, we have identified eight strains of microorganism which are able to produce 1,3-propanediol under aerobic condition. Those strains were isolated from garden soil, which were enriched by culturing in LB medium with glycerol added under aerobic condition. The identities of those strains were established based on their 16S rRNA sequences and physiological characteristics. Results indicated 6 strains are Citrobacter freundii and 2 strains are Klebsiella pneumoniae subsp Penumoniae. One of Klebsiella pneumoniae subsp Penumoniae strains, designated as TUAC01, demonstrated comparable levels of 1,3-propanediol oxidoreductase, glycerol dehydratase and glycerol dehydrogenase activity to the anaerobic microorganisms described in the literature. Accordingly, in larger scales (5 l) fed-batch culture the TUAC01 strain showed a remarkable 1,3-propanediol producing potency under aerobic conditions. 60.1 g/l of 1,3-propanediol was yield after 42 h incubation in an agitating bioreactor; and in air-lift bioreactor 66.3 g/l of 1,3-propanediol was yield after 58.5 h incubation. The aerobic ferment process, reduced the product cost and made the biological method of 1,3-propanediol production more attractive.

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