Acetone production with metabolically engineered strains of Acetobacterium woodii

作者：Hoffmeister Sabrina^*; Gerdom Marzena; Bengelsdorf Frank R; Linder Sonja; Fluechter Sebastian; Oeztuerk Hatice; Bluemke Wilfried; May Antje; Fischer Ralf Joerg; Bahl Hubert; Duene Peter

来源：Metabolic Engineering, 2016, 36: 37-47.

DOI：10.1016/j.ymben.2016.03.001

• Acetobacterium woodii
• Acetone
• CoA transferase
• Replicon for Gram-positives
• Carbon dioxide
• Continuous gas fermentation
• Syngas

Expected depletion of oil and fossil resources urges the development of new alternative routes for the production of bulk chemicals and fuels beyond petroleum resources. In this study, the clostridia) acetone pathway was used for the formation of acetone in the acetogenic bacterium Acetobacterium woodii. The acetone production operon (APO) containing the genes thlA (encoding thiolase A), ctfA/ctfB (encoding CoA transferase), and adc (encoding acetoacetate decarboxylase) from Clostridium acetobutylicum were cloned under the control of the thlA promoter into four vectors having different replicons for Gram positives (pIP404, pBP1, pCB102, and pCD6). Stable replication was observed for all constructs. A. woodii [PJIR_act(tnlA)] achieved the maximal acetone concentration under autotrophic conditions (15.2 +/- 3.4 mM). Promoter sequences of the genes ackA from A. woodii and pta-ack from C. ljungdahlii were determined by primer extension (PEX) and cloned upstream of the APO. The highest acetone production in recombinant A. woodii cells was achieved using the promoters P-thlA and Ppta-ack. Batch fermentations using A. woodii [pMTL84151_act(thlA)] in a bioreactor revealed that acetate concentration had an effect on the acetone production, due to the high K-m value of the CoA transferase. In order to establish consistent acetate concentration within the bioreactor and to increase biomass, a continuous fermentation process for A. woodii was developed. Thus, acetone productivity of the strain A. woodii [pMTL84151_act(thlA)] was increased from 1.2 mg L-1 h(-1) in bottle fermentation to 26.4 mg L-1 h(-1) in continuous gas fermentation.

• 出版日期2016-7