Tuin B J W, Geerts R, Westerink J B, van Ginkel C G
Akzo Nobel Chemicals Research, Department of Process Technology, P.O. Box 9300, 6800 SB Arnhem, The Netherlands.
Water Sci Technol. 2006;53(3):17-25. doi: 10.2166/wst.2006.072.
Wastewater from an Akzo Nobel production site contains more than 50 g/l total dissolved salts, mainly chlorides and sulphates, and is currently being treated after 10-20 x dilution. Biological treatment of undiluted or less diluted wastewater is very desirable for environmental and economic reasons. Possibilities were investigated in laboratory scale reactors to treat this highly saline and high strength wastewater aerobically, either after long adaptation or after removing part of the salts by a pretreatment. Adaptation and selection from mixed activated sludge populations took approximately 40 days to finally achieve a COD removal in aerobic treatment of 55-65% at two times dilution (11-16 g/l chloride and 5-7 g/l sulphate). Undiluted wastewater was not treatable. A higher removal percentage (> 80%) was possible at the original high salt concentration only when the sludge load was limited to approximately 0.4-0.5 kg COD/kg sludge/day. A longer adaptation time was required. Nanofiltration (NF) and crystallization could be used as a pretreatment to remove and recover up to 80% of the sulphate in the form of crystallized Glauber salt. Recovery strongly depended on the sulphate and chloride concentration in the NF concentrate and on crystallization temperature. The salt (sulphate) reduction through the NF improved the removal efficiency of a consecutive biotreatment only at a relatively low chloride level, demonstrating that the combination of nanofiltration-crystallization-aerobic biodegradation is less feasible for very saline wastewaters. Anaerobic pretreatment of saline waters turned out to be rather sensitive to high salinities. Only wastewater diluted to 10 g/l chloride could be treated well: sulphate concentration decreased by 80% and COD by 40%. Removal efficiencies of the combined anaerobic-aerobic treatment were approximately 80-85%, proving that this was a feasible route for 2-3 x diluted wastewater. The study has shown that several alternatives are available for treatment of the very saline wastewaters at a much lower degree of dilution than currently practiced.
阿克苏诺贝尔生产基地的废水含有超过50克/升的总溶解盐,主要是氯化物和硫酸盐,目前在经过10至20倍稀释后进行处理。出于环境和经济原因,对未稀释或稀释程度较低的废水进行生物处理非常有必要。在实验室规模的反应器中研究了多种可能性,以便在经过长时间适应或通过预处理去除部分盐分后,对这种高盐度和高强度废水进行好氧处理。从混合活性污泥群体中进行适应和筛选大约需要40天,最终在两倍稀释(氯化物含量为11至16克/升,硫酸盐含量为5至7克/升)的情况下,好氧处理的化学需氧量(COD)去除率达到55%至65%。未稀释的废水无法进行处理。只有当污泥负荷限制在约0.4至0.5千克化学需氧量/千克污泥/天时,在原始高盐浓度下才有可能实现更高的去除率(>80%)。这需要更长的适应时间。纳滤(NF)和结晶可作为预处理方法,以结晶芒硝的形式去除并回收高达80%的硫酸盐。回收率强烈依赖于纳滤浓缩液中的硫酸盐和氯化物浓度以及结晶温度。通过纳滤减少盐分(硫酸盐)仅在相对较低的氯化物水平下提高了后续生物处理的去除效率,这表明纳滤 - 结晶 - 好氧生物降解的组合对于高盐废水不太可行。事实证明,盐水的厌氧预处理对高盐度相当敏感。只有稀释至氯化物含量为10克/升的废水才能得到良好处理:硫酸盐浓度降低80%,化学需氧量降低40%。厌氧 - 好氧联合处理的去除效率约为80%至85%,证明这是处理两倍至三倍稀释废水的可行途径。该研究表明,对于目前稀释程度远低于实际水平的高盐废水处理,有几种替代方案可供选择。