脱碳方式对沼气发酵甲烷原位富集的影响

    Influence of techniques for desorption of carbon dioxide on in situ methane enrichment during biogas fermentation

    • 摘要: 甲烷原位富集是通过厌氧发酵直接制取生物天然气的一项技术,该技术通过将溶解在发酵液中的CO2持续脱除达到产出高甲烷含量沼气的目的,影响甲烷原位富集效果的关键是CO2的脱除方式。为了研究和探索适宜甲烷原位富集的脱碳方式,该文研究了空气吹脱、真空脱碳和超声波辅助空气吹脱3种脱碳方式对甲烷原位富集的影响。采用葡萄糖配制的人工废水为原料,在中温38℃条件下开展了厌氧发酵甲烷原位富集试验。结果表明,空气吹脱除碳方式下,发酵液日循环比率(daily recycle rates,DRR)为0.2和0.4 L/(L·d)时,所产沼气中甲烷平均体积分数分别达到了76.4%和78.3%,比对照组的65.4%分别提高了17%和20%;DRR为0.2 L/(L·d)空气吹脱组的累积甲烷产量与对照组相近,但DRR为0.4 L/(L·d)空气吹脱组累积甲烷产量比对照下降了15%,原因是吹脱提高了溶解氧含量并导致了抑制作用;在真空度0.1 MPa下真空脱碳组沼气甲烷体积分数比DRR为0.2 L/(L·d)的空气吹脱组下降了4.6%。超声波辅助空气吹脱试验结果表明,超声波可以加强CO2吹脱效果,在前3 min内其脱除CO2的速度比空气吹脱组提高了32%,同时经过21 min吹脱经其处理发酵液中游离态CO2的脱除量比单独空气吹脱组提高了29.8%。总之,控制空气吹脱携带溶解氧对厌氧发酵的抑制作用是甲烷原位富集工艺需重点考虑的因素,超声波对CO2空气吹脱能产生明显的促进作用,值得深入研究。

       

      Abstract: Abstract: In situ methane enrichment method can increase the methane content in biogas, which is a cost-effective technology used for producing bio-methane compared with conventional biogas upgrading technologies. During the in situ methane enrichment process, liquid stream from the anaerobic digester is circulated through a CO2-desorption unit and then returned back to the digester. The most important step in this process is CO2 desorption. In this study we evaluated the effects of different CO2 desorption techniques. Three CO2 desorption methods including air stripping, vacuum extraction and ultrasonic-auxiliary air stripping were studied through experiments. The experiments were conducted under mesophilic (38℃) anaerobic digestion by using synthetic wastewater with glucose and supplemental nutrients. The experimental apparatus included one anaerobic digester with volume of 1 500 mL and two CO2-desorption bottles with volume of 500 mL used for air stripping and vacuum extraction respectively. The results showed that the average volume fraction of methane in biogas reached 76.4% and 78.3% for the air stripping groups (aeration fluxes of 205 mL/min and daily stripping time of 30min), and increased by 17% and 20% compared to the control (65.4%) with the daily recycle rates of liquid stream (DRR) at 0.2 L/(L·d) and 0.4 L/(L·d), respectively. The cumulative methane production is similar to controlled one for the group with DRR of 0.2 L/(L·d). But the cumulative methane production decreased by 15% compared with control one for the group with DRR of 0.4 L/(L·d). In situ methane enrichment effect of the group of CO2 vacuum extraction with 0.1 MPa vacuum maintaining 5 min was slightly lower than that of the air stripping group with aeration flux at 205 mL/min, daily stripping time 20min and DDR 0.2 L/(L·d). The methane volume fraction of biogas in the first group was decreased by 4.6% compared to that of the second group . However, the difference is not significant (P>0.05). The results of experiment of ultrasonic-auxiliary air stripping, with aeration flux of 100 mL/min, daily stripping time of 21 min and ultrasonic frequency of 40 kHz, show that ultrasonic wave can accelerate CO2 air stripping, especially when the concentration of CO2 in the liquid was high. During the initial 3 min of stripping the CO2 removing rate of ultrasonic-auxiliary air stripping group was advanced by 32% compared to air stripping group. The total free CO2 removal amount from the liquid stream was increased by 29.8% compared to air stripping group during the whole stripping time of 21 min. Furthermore, ultrasonic wave has potential advantages on CO2 removing by lowering pH of liquid and increasing anaerobic digestion efficiency through decomposing many complex organic compounds. Therefore, the effect of air stripping and vacuum extraction on methane enrichment has no significance difference, but vacuum extraction has no problem of oxygen inhibition, the control of which is vital for successful running of in situ methane enrichment process of air stripping. Ultrasonic-auxiliary air stripping method has advantages for CO2 desorption due to its unique characteristics of lowering pH, degrading complex compounds and increasing CO2 removal.

       

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