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Minimum effluent process for pulp mill.

机译:制浆厂的最小废水处理工艺。

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This work studied the possibility and effectiveness of concentrating pulp mill effluents through gas hydrates purification process. The pulp mill effluents were proven to be able to form gas hydrates under proper temperature and pressure conditions. The important parameters affecting the effectiveness of the gas hydrate concentration, such as the presence of fiber, operating temperature and pressure, mass transfer, and washing, were also studied in this research. This purification process was shown to be very effective in terms of the reduction of Total Dissolved Solids (TDS) and Total Suspended Solids (TSS) reductions. The Chemical Oxygen Demand (COD) reduction, however, only achieved 53% reduction in the batch reactor. With application of multistage recrystallization, the COD reduction improved to just over 80%, still lower than the industrial expected over 95% reduction. The unsatisfied COD reduction was mainly due to the inherent equipment limitation and possibly unknown chemical compositions of the pulp mill effluents. Layer crystallization model was used to predict the impurity concentration in the final recovered water. Over 95% COD reduction can be achieved with 2 crystallization stages. In addition, final product purity and process yield was found to strongly depend upon the yield of each gas hydrate concentration stage and growth rate of gas hydrates. Meanwhile, the relationship between final product purity and process yield implicated the necessary optimization between yield and purity.
机译:这项工作研究了通过天然气水合物净化工艺浓缩纸浆厂废水的可能性和有效性。事实证明,制浆厂的废水能够在适当的温度和压力条件下形成气体水合物。在这项研究中,还研究了影响气体水合物浓度有效性的重要参数,例如纤维的存在,工作温度和压力,传质和洗涤。在减少总溶解固体(TDS)和减少总悬浮固体(TSS)方面,该纯化工艺非常有效。但是,分批反应器中化学需氧量(COD)的减少仅实现了53%的减少。随着多阶段重结晶的应用,化学需氧量的减少提高到刚好超过80%,仍然低于工业界预期的减少95%以上。 COD降低率不令人满意的主要原因是设备固有的局限性以及制浆厂废水的化学成分可能未知。使用层结晶模型来预测最终回收水中的杂质浓度。通过两个结晶阶段可以实现超过95%的COD减少。另外,发现最终产物的纯度和工艺产率在很大程度上取决于每个气体水合物浓缩阶段的产率和气体水合物的生长速率。同时,最终产物纯度与工艺产率之间的关系暗示了产率与纯度之间的必要优化。

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