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Regeneration and treatment of sulfidic spent caustic usingudanalytic hierarchy process

机译:硫化废碱的再生和处理层次分析法

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摘要

Background: Sulfur compounds must be removed from petroleum because they contribute to environmentaludpollution. A strong alkaline solution such as caustic soda is used to remove these compounds. This spentudcaustic has high values for chemical oxygen demand (COD) concentration, pH and total sulfur. In thisudstudy, the regeneration and treatment methodology of sulfidic spent caustic was investigated by applyingudthe analytic hierarchy process (AHP).udMethods: The evaluation index system developed was based on group decision-improved AHP. ExpertudChoice software was used to simplify decision-making when choosing a practical method and prioritizingudtreatment of spent caustic. Cost, environmental considerations, availability and scale-up were chosen asudcriteria and wet air oxidation and biological and catalytic methods were selected as alternative methods. Theudtreatment and regeneration of spent caustic was carried out in a batch bubble column reactor loaded withudIVKAZ catalyst and the effluent was treated in a precipitation-stirred tank reactor.udResults: Evaluation indicated that cost ranked first among criteria at 40.9%. The results showed that theudproposed process produced about 13% (wt) of caustic, 50 g/L of COD and 36 g/L of S2-.udConclusion: The results indicate that the catalytic method was more effective (0.45) than wet air oxidationudand the biological method. This process regenerated more than 85% of initial caustic and the economy ofudthe process improved by the recycling of the stream of caustic.udKeywords: Catalytic oxidation, Wastewater treatment, Recovery, Expert Choice
机译:背景:硫化合物必须从石油中去除,因为它们会造成环境污染。使用强碱溶液(如苛性钠)除去这些化合物。该废碱具有较高的化学需氧量(COD)浓度,pH和总硫值。本研究采用层次分析法(AHP),研究了硫化废碱液的再生和处理方法。方法:基于群体决策改进的层次分析法建立评价指标体系。在选择一种实用的方法并对废碱进行优先处理时,使用Expert udChoice软件简化了决策过程。选择成本,环境因素,可利用性和扩大规模作为标准,选择湿空气氧化以及生物和催化方法作为替代方法。废苛性碱的后处理和再生在装有udIVKAZ催化剂的间歇式鼓泡塔反应器中进行,废水在沉淀搅拌的槽式反应器中进行处理。结果结果:评估表明,成本为40.9%,位居第一。结果表明,不建议的工艺产生约13%(wt)的苛性碱,50 g / L的COD和36 g / L的S2-。 ud结论:结果表明,催化方法比(0.45)更有效。湿空气氧化生物方法。此过程再生了超过原始苛性碱的85%,并且通过苛性碱流的再循环提高了该过程的经济性。

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