Abstract

Temperature control is a very important factor on triterpene productivity in submerged liquid fermentation. Temperature effects from 23 to 32°C on triterpene production by Ganoderma lucidum G0119 were investigated in 6-L stirred fermentor. Logistic and Luedeking-Piret equations were used to estimate the mycelial growth and triterpene production kinetics by regression analysis. On that basis, a temperature-shifting fermentation control strategy was established. From 0 to 61h, culturing was performed at 32°C to get high specific mycelial growth rate. Between 62 and 127h, the temperature was decreased stepwise from 31 to 30°C to maintain high triterpene productivity. After 128h, temperature was maintained at 29°C to minimize triterpene production inhibition and sustain high productivity. Elevated triterpene level (0.269gL-1), yield (0.0101gg-1), and productivity (0.00207g (Lh)-1) were achieved representing 27.32, 13.94, and 37.11% higher than submerged liquid fermentation at constant temperature of 29°C, respectively, feasible for the industrial scale.

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