Max Planck Institute for Marine Microbiology, Bremen, Germany.
Biotechnol Bioeng. 2010 Feb 15;105(3):524-33. doi: 10.1002/bit.22553.
Novel high-pressure biotechnical systems that were developed and applied for the study of anaerobic oxidation of methane (AOM) are described. The systems, referred to as high-pressure continuous incubation system (HP-CI system) and high-pressure manifold-incubation system (HP-MI system), allow for batch, fed-batch, and continuous gas-phase free incubation at high concentrations of dissolved methane and were designed to meet specific demands for studying environmental regulation and kinetics as well as for enriching microbial biomass in long-term incubation. Anoxic medium is saturated with methane in the first technical stage, and the saturated medium is supplied for biomass incubation in the second stage. Methane can be provided in continuous operation up to 20 MPa and the incubation systems can be operated during constant supply of gas-enriched medium at a hydrostatic pressure up to 45 MPa. To validate the suitability of the high-pressure systems, we present data from continuous and fed-batch incubation of highly active samples prepared from microbial mats from the Black Sea collected at a water depth of 213 m. In continuous operation in the HP-CI system initial methane-dependent sulfide production was enhanced 10- to 15-fold after increasing the methane partial pressure from near ambient pressure of 0.2 to 10.0 MPa at a hydrostatic pressure of 16.0 MPa in the incubation stage. With a hydraulic retention time of 14 h a stable effluent sulfide concentration was reached within less than 3 days and a continuing increase of the volumetric AOM rate from 1.2 to 1.7 mmol L(-1) day(-1) was observed over 14 days. In fed-batch incubation the AOM rate increased from 1.5 to 2.7 and 3.6 mmol L(-1) day(-1) when the concentration of aqueous methane was stepwise increased from 5 to 15 mmol L(-1) and 45 mmol L(-1). A methane partial pressure of 6 MPa and a hydrostatic pressure of 12 MPa in manifold fed-batch incubation in the HP-MI system yielded a sixfold increase in the volumetric AOM rate. Over subsequent incubation periods AOM rates increased from 0.6 to 1.2 mmol L(-1) day(-1) within 26 days of incubation. No inhibition of biomass activity was observed in all continuous and fed-batch incubation experiments. The organisms were able to tolerate high sulfide concentrations and extended starvation periods.
描述了为研究甲烷厌氧氧化(AOM)而开发和应用的新型高压生物技术系统。这些系统被称为高压连续培养系统(HP-CI 系统)和高压歧管培养系统(HP-MI 系统),可在高浓度溶解甲烷下进行批量、补料分批和连续气相自由培养,旨在满足研究环境调控和动力学以及长期培养中富集微生物生物量的特定需求。在第一技术阶段,缺氧培养基用甲烷饱和,然后在第二阶段用饱和培养基为生物量培养提供营养。在 20 MPa 下,甲烷可以连续供应,在 45 MPa 的静压下,培养系统可以在富气培养基的恒定供应下运行。为了验证高压系统的适用性,我们展示了来自黑海微生物垫的高活性样品在连续和补料分批培养中的数据,这些样品是在水深 213 米处采集的。在 HP-CI 系统的连续运行中,在培养阶段将甲烷分压从接近环境压力的 0.2 MPa 增加到 10.0 MPa 后,初始依赖甲烷的硫化物生成增强了 10-15 倍。在水力停留时间为 14 h 的情况下,在不到 3 天的时间内达到了稳定的出水硫化物浓度,并在 14 天内观察到体积 AOM 速率从 1.2 增加到 1.7 mmol L(-1)天(-1)。在补料分批培养中,当水相甲烷浓度从 5 mmol L(-1)逐步增加到 15 mmol L(-1)和 45 mmol L(-1)时,AOM 速率分别从 1.5 增加到 2.7 和 3.6 mmol L(-1)天(-1)。在 HP-MI 系统的歧管补料分批培养中,当甲烷分压为 6 MPa,静压为 12 MPa 时,体积 AOM 速率增加了六倍。在随后的培养期间,在 26 天的培养期内,AOM 速率从 0.6 增加到 1.2 mmol L(-1)天(-1)。在所有连续和补料分批培养实验中均未观察到生物量活性受到抑制。这些生物能够耐受高浓度的硫化物和长时间的饥饿期。