Isopropanol biosynthesis from crude glycerol using fatty acid precursors via engineered oleaginous yeast Yarrowia lipolytica.

BACKGROUND: Isopropanol is widely used as a biofuel and a disinfectant. Chemical preparation of isopropanol destroys the environment, which makes biological preparation of isopropanol necessary. Previous studies focused on the use of expensive glucose as raw material. Therefore, the microbial cell factory that ferments isopropanol with cheap raw materials will provide a greener way to produce isopropanol. RESULTS: This study converted crude glycerol into isopropanol using Y. lipolytica. As a microbial factory, the active natural lipid and fatty acid synthesis pathway endows Y. lipolytica with high malonyl-CoA production capacity. Acetoacetyl-CoA synthase (nphT7) and isopropanol synthesis genes are integrated into the Y. lipolytica genome. The nphT7 gene uses the accumulated malonyl-CoA to synthesize acetoacetyl-CoA, which increases isopropanol production. After medium optimization, the best glycerol medium was found and resulted in a 4.47-fold increase in isopropanol production. Fermenter cultivation with pure glycerol medium resulted in a maximum isopropanol production of 1.94 g/L. In a crude glycerol fermenter, 1.60 g/L isopropanol was obtained, 82.53% of that achieved with pure glycerol. The engineered Y. lipolytica in this study has the highest isopropanol titer reported. CONCLUSIONS: The engineered Y. lipolytica successfully produced isopropanol by using crude glycerol as a cheap carbon source. This is the first study demonstrating the use of Y. lipolytica as a cell factory to produce isopropanol. In addition, this is also a new attempt to accumulate lipid synthesis precursors to synthesize other useful chemicals by integrating exogenous genes in Y. lipolytica.

Enhanced biodegradation of waste poly(ethylene terephthalate) using a reinforced plastic degrading enzyme complex.

Poly(ethylene terephthalate) (PET) is synthesized via a rich ester bond between terephthalate (TPA) and ethylene glycol (EG). Because of this, PET degradation takes a long time and PET accumulates in the environment. Many studies have been conducted to improve PET degrading enzyme to increase the efficiency of PET depolymerization. However, enzymatic PET decomposition is still restricted, making upcycling and recycling difficult. Here, we report a novel PET degrading complex composed of Ideonella sakaiensis PETase and Candida antarctica lipase B (CALB) that improves degradability, binding ability and enzyme stability. The reaction mechanism of chimeric PETase (cPETase) and chimeric CALB (cCALB) was confirmed by PET and bis (2-hydroxyethyl terephthalate) (BHET). cPETase generated BHET and mono (2-hydroxyethyl terephthalate (MHET) and cCALB produced terephthalate (TPA). Carbohydrate binding module 3 (CBM3) in the scaffolding protein greatly improved PET film binding affinity. Finally, the final enzyme complex demonstrated a 6.5-fold and 8.0-fold increase in the efficiency of hydrolysis from PET with either high crystalline or waste to TPA than single enzymes, respectively. This complex could effectively break down waste PET while maintaining enzyme stability and would be applied for biological upcycling of TPA.

Bio-isopropanol production in Corynebacterium glutamicum: Metabolic redesign of synthetic bypasses and two-stage fermentation with gas stripping.

Isopropanol is a commodity chemical widely used as a biofuel, fuel additive, rubbing alcohol and intermediate in various fields. Here, an engineered Corynebacterium glutamicum overproducing isopropanol was developed. To our knowledge, despite a representative industrial host to produce valuable chemicals, the high-level production of isopropanol in C. glutamicum has never been reported. First, the problem of the inability to produce isopropanol was solved by finding a key factor in its metabolism. The consolidation and modular optimization of synthetic bypasses including succinate and mevalonate bypasses enhanced isopropanol production. Flux redistribution of central metabolism significantly directed the carbon flux toward isopropanol biosynthesis. The final engineered strain produced 10.25 ± 1.12 g/L isopropanol in two-stage fed-batch fermentation with an optimized gas stripping, which is the highest titer, yield and productivity in C. glutamicum. These strategies could be useful for the high-level production of isopropanol in C. glutamicum.