College of Engineering, Northeast Agricultural University, Harbin, 150030, China.
College of Engineering, Northeast Agricultural University, Harbin, 150030, China.
J Environ Manage. 2024 Aug;366:121864. doi: 10.1016/j.jenvman.2024.121864. Epub 2024 Jul 16.
This research aimed to design an integrated aerobic-anaerobic reactor with dynamic aeration that was automatically regulated based on real-time oxygen concentration and investigate the aerobic pretreatment and subsequent dry co-anaerobic digestion (co-AD) characteristics of highly solids-loaded corn stover and swine manure in terms of temperature rise, physiochemical characteristics, and methane production. The high-temperature feedstocks from the aerobic pretreatment phase rapidly entered the AD phase without transportation and effectively improved the start-up and methane production of the co-AD. Oxygen concentration range, aeration rate, and pretreatment time affected the cumulative aeration time, temperature rise, and organic matter removal interactively during aerobic pretreatment, and a low aeration rate was relatively preferable. Although the lignocellulose removal increased with the increase in pretreatment duration, the maximal lignin elimination efficiency only reached 1.30%. The inoculum injection in the transition phase from aerobic pretreatment to co-AD and the leachate reflux during co-AD were also critical for producing methane steadily apart from aerobic pretreatment. The cold air weakened the temperature rise of aerobic pretreatment, and the low-temperature leachate reduced the methane production in the co-AD process. An oxygen concentration range of 13%-17%, aeration rate of 0.10 m/(min·m), pretreatment time of 84 h, inoculum loading of 40%, leachate refluxing thrice per day, and double-layer inoculation were optimum for improving the integrated aerobic-anaerobic digestion system's ability to resist low temperatures and achieving high methane production. The maximal cumulative and volatile solids (VS) methane yields of corn stover and swine manure reached 444.58 L and 266.30 L/kg VS.
本研究旨在设计一种集成式好氧-厌氧反应器,采用动态曝气,根据实时氧浓度自动调节,并研究高固体负荷的玉米秸秆和猪粪在升温、理化特性和甲烷生成方面的好氧预处理及随后的干共厌氧消化(共 AD)特性。好氧预处理阶段的高温物料无需运输即可快速进入 AD 阶段,有效提高了共 AD 的启动和甲烷生成效率。氧气浓度范围、曝气率和好氧预处理时间在好氧预处理过程中相互影响,共同影响累积曝气时间、升温速率和有机质去除率,较低的曝气率相对更有利。虽然木质纤维素的去除率随着预处理时间的增加而增加,但最大木质素去除效率仅达到 1.30%。在从好氧预处理到共 AD 的过渡阶段注入接种物和在共 AD 期间进行渗滤液回流对于稳定产生甲烷也至关重要,除了好氧预处理。冷空气削弱了好氧预处理的升温,低温渗滤液降低了共 AD 过程中的甲烷生成。氧气浓度范围为 13%-17%、曝气率为 0.10 m/(min·m)、预处理时间为 84 h、接种物负荷为 40%、每天渗滤液回流三次以及双层接种是提高集成好氧-厌氧消化系统低温抵抗能力和实现高甲烷产量的最佳条件。玉米秸秆和猪粪的最大累积和挥发性固体(VS)甲烷产量分别达到 444.58 L 和 266.30 L/kg VS。