Matteau Yanick, Ramsay Bruce
a Department of Chemical Engineering , Ecole Polytechique de Montreal , Montreal , Canada.
J Air Waste Manag Assoc. 1999 Mar;49(3):350-354. doi: 10.1080/10473289.1999.10463808.
Thermophilic biodégradation of toluene with active compost biofilters was studied. Thermophilic conditions were maintained either by daily substrate addition (semicontinuous composting) or with a heating system (batch thermophilic composting). The semicontinuous system was designed for the treatment of cool (less than approximately 35 °C) gases under thermophilic conditions, while the extended batch approach was developed for the treatment of warmer gases. When the semicontinuous system was operated at 50 °C (after a one-day start-up period) at an average inlet concentration of 5.5 g m, toluene was degraded at a rate ranging from 73 to 110 g C m hr. Batch thermophilic treatment was somewhat less effective at the same inlet concentration. Semicontinuous toluene biofiltration at 60 °C was also investigated, but biodegradation rates were significantly lower than at 50 °C. In all systems, toluene biodegradation was proportional to the inlet concentration. Rates of up to 289 g C m hr (at an inlet concentration of 14.7 g m) were achieved for semicontinuous and batch operation and 251 g C m hr (at an inlet concentration of 18.4 g m) for batch thermophilic at 50 °C. Semicontinuous thermophilic operation at 60 °C showed a maximum rate of 119 g C m hr. Active compost ther-mophilic biofiltration was found to be very effective when concentrations are high. At lower concentrations, rates were similar to those obtained with mesophilic biofiltration. Mixing, humidity, and the presence of cosubstrate were important parameters in maintaining high degradation rates. Biofiltration in the batch thermophilic mode could be useful when conventional biofiltration is ineffective due to elevated gas temperatures. Biofiltration in the semicontinuous thermophilic could reduce the biofilter size necessary for treatment of cooler gases containing high concentrations of volatile organic compounds.
研究了利用活性堆肥生物滤池对甲苯进行嗜热生物降解。通过每日添加底物(半连续堆肥)或加热系统(间歇嗜热堆肥)来维持嗜热条件。半连续系统设计用于在嗜热条件下处理低温(低于约35°C)气体,而扩展间歇法是为处理较高温度气体而开发的。当半连续系统在50°C(经过一天的启动期)下以平均入口浓度5.5 g/m³运行时,甲苯的降解速率为73至110 g C/m³·h。在相同入口浓度下,间歇嗜热处理的效果稍差。还研究了在60°C下半连续甲苯生物过滤,但生物降解速率明显低于50°C时的速率。在所有系统中,甲苯生物降解与入口浓度成正比。半连续和间歇运行在50°C时,入口浓度为14.7 g/m³时,速率高达289 g C/m³·h;间歇嗜热在入口浓度为18.4 g/m³时,速率为251 g C/m³·h。60°C下半连续嗜热运行的最大速率为119 g C/m³·h。发现当浓度较高时,活性堆肥嗜热生物过滤非常有效。在较低浓度下,速率与中温生物过滤获得的速率相似。混合、湿度和共底物的存在是维持高降解速率的重要参数。当传统生物过滤因气体温度升高而无效时,间歇嗜热模式的生物过滤可能有用。半连续嗜热生物过滤可以减小处理含有高浓度挥发性有机化合物的低温气体所需的生物滤池尺寸。