Koppar Abhay, Pullammanappallil Pratap
Department of Agricultural and Biological Engineering, University of Florida, Gainesville, FL 32611, USA.
Bioresour Technol. 2008 May;99(8):2831-9. doi: 10.1016/j.biortech.2007.06.051. Epub 2007 Sep 12.
Spent sugar beet pulp as received was digested in a single-stage, batch, unmixed, leach-bed, laboratory scale thermophilic anaerobic digester. Biogasification of each 0.450 kg (wet weight) batch of spent pulp was initiated by inoculating with anaerobically digested liquor from previous run. The average methane yield was 0.336 m3 CH4 at STP (kgVS)(-1), the maximum methane production rate was 0.087 m3 CH4 at STP (kgVS)(-1)d(-1), average lag time to initiate methanogenesis was only 0.44 days and time required to achieve 95% methane yield was 8 days. The pH in the digesters ranged between 8.0 and 9.5. High rates of methane generation were sustained even at high pH values. The equivalent organic loading rate in the batch digesters was 4 kgCODm(-3)d(-1). The digestion process used here offers significant improvements over one-stage and two-stage systems reported in the literature with comparable performance as it is a single-stage system where the feedstock does not require size reduction, and mixing is not required in the digester.
将收到的废甜菜粕在实验室规模的单级、间歇、未混合、浸出床式嗜热厌氧消化器中进行消化。每批0.450千克(湿重)废粕的沼气发酵通过接种上一批次厌氧消化液启动。在标准温度和压力下,平均甲烷产量为0.336立方米CH₄/(千克挥发性固体),最大甲烷产生速率为0.087立方米CH₄/(千克挥发性固体)·天,开始产甲烷的平均延迟时间仅为0.44天,达到95%甲烷产量所需时间为8天。消化器中的pH值在8.0至9.5之间。即使在高pH值下,也能维持较高的甲烷生成速率。间歇式消化器中的等效有机负荷率为4千克化学需氧量/立方米·天。这里使用的消化工艺与文献中报道的单级和两级系统相比有显著改进,具有可比性能,因为它是单级系统,原料无需减小尺寸,消化器中也无需混合。