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Intensified phenols extraction and oil removal for industrial semi-coking wastewater: A novel economic pretreatment process design

机译:工业半焦化废水的强化酚提取和除油:一种新型的经济预处理工艺设计

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Current semi-coking wastewater treatment process has low performance of pollutants removal and consumes a large amount of high-grade steams. It far exceeds the semi-coke plants' utilities supply capacity and easily lead to the breakdown of whole treatment system. This paper identified the bottleneck of current process as followed: low removal efficiency of oil and dust; poor extraction conditions caused by the high pH value and the fouling and plugging of internals; high-grade steam requirement and investment cost. To improve the deficiencies of current process, a novel hybrid process is proposed based on the benchmark treatment capacity of 240 m(3)/d. The effects of acidification and extraction conditions on zeta potential and extraction efficiency have been analyzed following industrial semi-coking wastewater experiments. The results show that the concentrations of oil and dust are reduced less than 50 mg/L when pH value is lower than 4.8. The removal efficiencies of COD and total phenols after extracted are increasing as pH value decreases. The conceptual design is accomplished based on the experimental and simulative analysis. The concentrations of sour gas, total phenols, ammonia and COD decreases to 10 mg/L, 270 mg/L, 50 mg/L and 3050 mg/L, respectively. It also eliminates 2.5 MPag and 1.0 MPag steam demand at the expense of 24.1 kW more electricity uses and 70.84 kg/h reagents consumption, as suggested in simulation results. The estimated investment cost saving are 0.77 million US$, and the net cost reduction is 0.63 US$/t water. (c) 2019 Elsevier Ltd. All rights reserved.
机译:当前的半焦化废水处理工艺的污染物去除性能低,并且消耗大量的高等级蒸汽。它远远超过了半焦工厂的公用事业供应能力,很容易导致整个处理系统崩溃。本文确定了当前过程的瓶颈:油和灰尘的去除效率低;高pH值以及内部部件的结垢和堵塞导致萃取条件差;高等级的蒸汽需求和投资成本。为了改善当前工艺的缺陷,基于240 m(3)/ d的基准处理能力,提出了一种新型的混合工艺。通过工业半焦化废水实验,分析了酸化和萃取条件对zeta电位和萃取效率的影响。结果表明,当pH值低于4.8时,油尘浓度降低到50 mg / L以下。随着pH值的降低,萃取后COD和总酚的去除效率增加。基于实验和仿真分析,完成了概念设计。酸性气体,总酚,氨和COD的浓度分别降低至10 mg / L,270 mg / L,50 mg / L和3050 mg / L。如仿真结果所示,它还消除了2.5 MPag和1.0 MPag的蒸汽需求,但以24.1 kW以上的用电量和70.84 kg / h的试剂消耗为代价。估计节省的投资成本为77万美元,每吨水的净成本降低为0.63美元。 (c)2019爱思唯尔有限公司。保留所有权利。

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