National Key Laboratory of Biochemical Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing, People's Republic of China.
Bioprocess Biosyst Eng. 2013 Feb;36(2):223-30. doi: 10.1007/s00449-012-0778-1. Epub 2012 Jul 8.
A novel patented solid-state bioreactor (251 L) with honeycomb loading device was designed and its performance was tested. First, this apparatus gave a 66.87 % of calculated loading coefficient (volume ratio), which was almost twofold compared with conventional fermenters. Next, considering the crucial effect of heat transfer on bed loading and microbial growth, the performance was validated by temperature variance during fermentation and spore viability of Bacillus cereus DM423. Air pressure pulsation or external water jacket was used to control temperature; the maximal temperature variation was 7.7 versus 19.8 °C, respectively during fermentation. The difference was mainly due to the continuous gas phase characterized by solid-state fermentation (SSF). The average living spores of (1.50 ± 0.07) × 10(11) cfu/g at 40 h obtained from the device was higher than (0.70 ± 0.03) × 10(11) cfu/g from flask at 48 h. The results indicated that this new loading bioreactor with air pressure pulsation could be a good prospect for industrialization of SSF employing bacterial cultures.
设计了一种新型专利的固态生物反应器(251 L),带有蜂窝状装料装置,并对其性能进行了测试。首先,该设备的计算装料系数(体积比)达到了 66.87%,几乎是传统发酵罐的两倍。其次,考虑到传热对床层装料和微生物生长的关键影响,通过发酵过程中的温度变化和蜡状芽孢杆菌 DM423 的孢子活力验证了该设备的性能。采用气压脉冲或外部水套来控制温度;发酵过程中的最大温度变化分别为 7.7 和 19.8°C。差异主要归因于固态发酵(SSF)所具有的连续气相。从该设备中获得的 40 h 时的活菌孢子(1.50 ± 0.07)×10(11)cfu/g 高于 48 h 时从瓶中获得的活菌孢子(0.70 ± 0.03)×10(11)cfu/g。结果表明,这种带有气压脉冲的新型装料生物反应器有望在采用细菌培养的 SSF 工业化方面取得良好的前景。