甲烷氧化菌吸附膜反应器中环氧丙烷的连续生物转化

以流化床作为固定化体系 ,在硅藻土颗粒表面构建了混合培养的甲烷氧化细菌的吸附膜。研究发现延迟期后固定化细胞的甲烷单加氧酶活性明显增加。流化床中 90 %以上的甲烷氧化细菌以吸附形式存在。吸附膜浓度为 3.3～3.7 mgdryweightcell gDS。通过批式反应考察了丙烯 甲烷共氧化过程合成环氧丙烷的可能性。研究了甲烷对丙烯环氧化以及丙烯对甲烷氧化细菌生长的影响。通过最佳配比的混合反应气体 (methane :35 % ;propene :20% ;oxygen :45 % )连续循环通入流化床反应器中抽提产物环氧丙烷 ,克服了产物抑制。该生物反应器最初产生环氧丙烷的日产量为 110～ 150μmol d ,连续操作25d ,未观察到环氧丙烷生产能力的明显减小.

Continuous Biosynthesis of Epoxypropane in a Methanotrophic Attached-films Reactor

Using a fluidized bed as immobilization system, mixed culture methanotrophic attached-films were developed on diatomite particles. The Methane Monooxygenase (MMO) activity was found to increase obviously as soon as the lag phase ended. Greater than 90% of the MMO activity in the bed was attached. Biofilm concentration of 3.3-3.7 mg dry weight cell/g DS was observed. Batch experiments were performed to explore the possibility of producing epoxypropane by a cooxidation process. The effect of methane on the oxidation of propene to epoxypropane and the effect of propene on the growth of methanotroph were also studied. In continuous experiments, optimum mixed gaseous substrates (methane: 35%; propene: 20%; oxygen: 45%) were continuously circulated through the fluidized bed reactor to remove product. Initial epoxypropane productivity was 110-150 mumol/d. The bioreactor operated continuously for 25 d without obvious loss of epoxypropane productivity.