厌氧膜分离工艺处理低强度废水的初步研究

D. Stensel
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摘要

由于对生物质能减少技术进行了评价,发现厌氧处理在处理城市和工业废水中有可能产生最低水平的生物质能。在低温条件下,厌氧废水处理工艺对稀废水的限制是在反应器中维持显著水平的产甲烷生物以维持有效处理的能力。提出了厌氧折流板反应器+膜分离处理低温低强度废水的工艺方案。在西雅图的西点污水处理厂组装并安装了一个4gpm的中试装置,以测试厌氧/膜分离处理系统的可行性。在7个月的时间里,进行了3次不同的系统启动尝试,结果表明厌氧折流板反应器系统的产甲烷活性很小。启动期间的温度范围为10至15°C,这可能是无法在可用时间内产生大量产甲烷菌群的重要因素。这项持续研究的另一个方面是进行成本分析,以评估厌氧/膜工艺减少生物质的潜力。成本分析表明,增加膜反应器改造现有的二级处理系统所产生的大量资本支出,其年摊销成本高于减少污泥产量、降低曝气马力和过量甲烷气体产生所带来的显著运营成本节约。由于膜分离系统约占改造成本的90%,因此成本分析表明,在低强度废水厌氧处理后,应寻求一种更便宜的液固分离方法。本文归属于WERF研究报告丛书ISBN: 9781843397298(电子书)
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Preliminary Investigation of an Anaerobic Membrane Separation Process for Treatment of Low-Strength Wastewaters
As a result of an evaluation of biomass reduction technologies, anaerobic treatment was found to have potential for the lowest level of biomass production in the treatment of municipal and industrial wastewaters. A limitation of anaerobic wastewater treatment processes for dilute wastewaters and at cold temperatures is the ability to maintain a significant level of methanogenic organisms in the reactor to sustain efficient treatment. A process consisting of an anaerobic baffled reactor followed by membrane separation was proposed for the treatment of low strength wastewaters at colder temperatures. A 4 gpm pilot plant facility was assembled and installed at the West Point wastewater treatment plant in Seattle, to test the feasibility of the anaerobic/membrane separation treatment system. During a 7 month period, 3 different attempts were made for system start up with the result of little methanogenic activity in the anaerobic baffled reactor system. The temperatures during the start up ranged from 10 to 15°C and may have been a significant factor in the inability to generate a significant methanogenic population within the time available. Another aspect of this continuing study to investigate biomass reduction was a cost analysis to evaluate the potential for an anaerobic/membrane process for biomass reduction. The cost analysis showed that the significant capital expenditure for adding a membrane reactor to retrofit an existing secondary treatment system resulted in a greater annual amortization costs than the significant operational cost savings realized by less sludge production, less aeration hp, and excess methane gas production. Because the membrane separation system represented about 90% of the retrofit costs, the cost analysis suggests that a less expensive method be pursued for liquid solids separation after anaerobic treatment of low strength wastewaters. This title belongs to WERF Research Report Series ISBN: 9781843397298 (eBook)
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