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Shafirah Samsuri Nurul Aini Amran Norshafika Yahya 《Chemical Engineering Communications》2016,203(3):345-363
Progressive freeze concentration (PFC) is a process where only a large single ice crystal is formed in the system and grown on the cooling surface so that the separation between the ice crystal and the mother solution is very easy. This makes the system very simple and leads to a lower cost. The conventional setup of PFC produces ice with high purity but lower productivity than suspension freeze concentration (SFC). The volume of ice produced is also usually low. Hence, continued areas of the development for PFC system include the quest for improved productivity and better efficiency. Different kinds of design have been investigated, which are easy to operate and cost-effective besides the ability to obtain high quality of product and better efficiency of the system. The PFC system is recognized as a good alternative if high-quality products can be produced with higher productivity. In this article, previous researches on PFC designs were reviewed for the purpose of providing an understanding on methods of designing a PFC system and also to provide references for future application of PFC. 相似文献
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A progressive freeze concentration process, unidirectional downward freezing (UDF), was investigated for removal of five commonly used pharmaceuticals (ibuprofen, gemfibrozil, acetylsalicylic acid, metoprolol and sulfamethoxazole) in water. The feed water with the pharmaceutically active compounds (PhACs) at concentrations from ng/L to mg/L range was frozen at −7 and −15 °C. The separation efficiency of PhACs in the single stage and two-stage UDF was examined. By freezing only 80% (volume) of the feed water and without washing of the ice, about 84-92% reduction of the drug content in ice was achieved in the single stage UDF and about 99% reduction in the two-stage UDF. The partitioning behavior of the PhACs in the ice and liquid phases seems different from the solutes in glucose solutions or liquid foods reported in the literature. A strong linear relationship between the PhACs concentration and their TOC concentration was established, suggesting that TOC, a parameter commonly used to measure WWTP effluent quality might be used to monitor the level of PhACs in WWTP effluent. 相似文献
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实验主要研究制革废水厌氧最佳条件、COD去除率和污泥减量,根据制革废水的特点以及实验目的要求,在不经絮凝剂处理的情况下,加入中性酶经过2~3h的处理后,在不同外界环境下进行多组厌氧处理,使废水能够迅速的处理到一定浓度,解决制革废水厌氧处理上的难题. 相似文献
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《分离科学与技术》2012,47(7):1433-1446
Abstract Several applications of ozonation were examined in this study for:
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the treatment of stabilized high strength municipal landfill leachates,
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the reclamation potential and toxicity reduction of municipal secondary effluents, and
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the removal potential of phytoplanktons from surface waters.
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根据离线镀膜生产线生产特点,介绍与之相适应的冷冻冷却水系统的设计和选型,及安装过程中的注意事项. 相似文献
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采用高浓缩倍数无磷水处理方案,使循环水在5倍以上高浓缩倍数下运行处理,运行指标和监测数据均达到并优于国标和中石化规定的要求。运行结果表明,该方案达到了很好的抗腐蚀、结垢和微生物控制效果,同时兼具环保、节水效果。 相似文献
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高浓度聚合物驱采出水水质特性及处理技术研究 总被引:1,自引:0,他引:1
以大庆油田采油六厂高浓度聚合物试验区中心井采出水为研究对象,室内进行了沉降分离和离心分离技术的研究。研究结果表明:采出水中聚合物浓度增加,使得采出水粘度增加,油珠上浮速度慢,油水分离难度加大,单纯地依靠油水密度差长时间沉降分离很难达到预期的目的;当采出水粘度较大时,采用离心法具有较好的处理效果。 相似文献
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染色废水的还原脱色及其回用 总被引:1,自引:1,他引:1
使用还原型双组分脱色剂对含有不同种类水溶性染料的染色废水进行脱色处理,重点研究了脱色剂用量、反应温度、pH值和时间对脱色反应的影响。并且将脱色后的染色废水回用于织物染色中,在染料的上染速率曲线和颜色特征方面进行了比较。结果表明,随着脱色刑用量的增加,染色废水的脱色率都逐渐升高:中性pH条件和温度的升高均可以促进染色废水的脱色;在60℃~700℃,脱色率可达到90%;在常温下3~5分钟内完成脱色,而直接染料不超过15分钟,脱色废水能够回用于织物染色中,染料的上染曲线几乎没有变化,染色深度和色差变化极小。 相似文献
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介绍了高氨氮煤化工废水的处理技术:物化法、生化联合法和新型生物脱氮法。目前实际应用中多采用生化联合法技术,在生物处理前,先对高浓度氨氮废水进行物化处理。短程硝化反硝化等一些新型生物脱氮法技术前景看好,值得关注。 相似文献
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通过采用专用比色皿进行多次实验,对高浓度有机废水中COD的进行了改进,该法检测速度快,误差小,能很好的运用于实际工作中的废水检测。 相似文献
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针对天然水体体积计算难题,从水侵量的定义公式出发,以S理想边水驱油藏为例,以廖运涛方法获得的精确解为约束条件,主要是对采用的综合压缩系数进行校正,获得了理想边水驱油藏天然水体体积的简便估算方法,在类似油藏上应用取得了好效果,为选择合适的开发方式提供了重要依据。对于井网完善、已全面投入开发、完全依靠边水补充能量、以自喷为主的高渗透、稀油油藏,在经历几年的开发后有明显的油层压降情况下,只要能够落实清楚总压降值和与之对应的水侵量,就可以估算出天然水体的体积。至于该方法能否拓宽应用范围,尚需进一步探讨。 相似文献
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介绍了采用一体化曝气生物滤池(BAF)工艺深度处理小型低浓度的工业废水和生活污水的混合水工程实例。运行结果表明:在进水CODCr浓度不高于60 mg/L的情况下,最终出水水质达到《地表水环境质量标准》(GB3838-2002)中的Ⅲ类排放标准。该工艺具有占地面积小、运行稳定、无风机噪声、成本低、出水水质好等优点。 相似文献