Salkinoja-Salonen M, Apajalahti J, Silakoski L, Hakulinen R
University of Helsinki, Dept. of General Microbiology, Finland.
Biotechnol Adv. 1984;2(2):357-75. doi: 10.1016/0734-9750(84)90015-6.
Anaerobic treatment has seldom been used for wastewaters from the pulp and paper industry and other branches of the chemical industry. Escape of volatile pollutants to the atmosphere, which always occurs during aerobic treatment, is avoided, and much less sludge is being produced than in an aerobic process. The greatest obstacle for using anaerobic treatment in the pulp and paper industry is the large wastewater volume, which necessitates short hydraulic detention times, because the treatment is to occur in an enclosed space. We used solid carrier particles to prevent wash-out of biomass from the reactor at high hydraulic loading, and an up-flow system in order to be able to use very small carrier particles, maximizing the surface area for biomass attachment. In this paper we describe and discuss the results obtained with this type of anaerobic reactor (fluidised bed) at bench and semitechnical scale for wastewaters from pressurized ground wood pulping and paper manufacture, sulphite pulp evaporator condensate and bleach waste. Earlier work with Kraft pulp bleaching effluent and thermomechanical pulping wastewater and evaporator condensates using anaerobic reactors is also discussed. The results obtained thus far show that there are several wastewater streams from the pulping industry, where 60 to 90% of the dissolved organic pollutants (measured as COD(Cr) or TOC) was biodegraded within 4 to 24 h. The high strength waste streams (COD(Cr) >2000 mg O(2) 1(-1)) allowed organic space load of 4 to 10 kg COD(Cr) m(-3) reactor volume d(-1). With low strength wastes the hydraulic loading was the limiting factor.
厌氧处理很少用于制浆造纸工业及其他化工行业的废水处理。与好氧处理过程中挥发性污染物总会排放到大气中不同,厌氧处理避免了这种情况,且产生的污泥比好氧处理少得多。在制浆造纸工业中应用厌氧处理的最大障碍是废水流量大,这就需要较短的水力停留时间,因为处理过程要在封闭空间内进行。我们使用固体载体颗粒以防止在高水力负荷下生物量从反应器中被冲走,并采用上流式系统以便能够使用非常小的载体颗粒,从而使生物量附着的表面积最大化。在本文中,我们描述并讨论了这种类型的厌氧反应器(流化床)在实验室规模和半工业规模下处理加压磨木浆制浆及造纸废水、亚硫酸盐浆蒸发器冷凝水和漂白废水所获得的结果。同时也讨论了早期使用厌氧反应器处理硫酸盐浆漂白废水、热磨机械浆废水及蒸发器冷凝水的相关工作。目前所获得的结果表明,制浆工业中有几种废水流,其中60%至90%的溶解性有机污染物(以COD(Cr)或TOC计)在4至24小时内被生物降解。高浓度废水流(COD(Cr)>2000 mg O₂ l⁻¹)允许的有机容积负荷为4至10 kg COD(Cr) m⁻³反应器容积 d⁻¹。对于低浓度废水,水力负荷是限制因素。