• 主题
高级搜索  >
历史搜索 清空历史
首页> 美国卫生研究院文献>Membranes >Performance Modeling and Cost Analysis of a Pilot-Scale Reverse Osmosis Process for the Final Purification of Olive Mill Wastewater
【2h】

Performance Modeling and Cost Analysis of a Pilot-Scale Reverse Osmosis Process for the Final Purification of Olive Mill Wastewater

机译：橄榄工厂废水最终净化中试反渗透过程的性能建模和成本分析

代理获取
本网站仅为用户提供外文OA文献查询和代理获取服务，本网站没有原文。下单后我们将采用程序或人工为您竭诚获取高质量的原文，但由于OA文献来源多样且变更频繁，仍可能出现获取不到、文献不完整或与标题不符等情况，如果获取不到我们将提供退款服务。请知悉。
页面导航
  • 摘要
  • 著录项
  • 相似文献
  • 相关主题

摘要

A secondary treatment for olive mill wastewater coming from factories working with the two-phase olive oil production process (OMW-2) has been set-up on an industrial scale in an olive oil mill in the premises of Jaén (Spain). The secondary treatment comprises Fenton-like oxidation followed by flocculation-sedimentation and filtration through olive stones. In this work, performance modelization and preliminary cost analysis of a final reverse osmosis (RO) process was examined on pilot scale for ulterior purification of OMW-2 with the goal of closing the loop of the industrial production process. Reduction of concentration polarization on the RO membrane equal to 26.3% was provided upon increment of the turbulence over the membrane to values of Reynolds number equal to 2.6 × 104. Medium operating pressure (25 bar) should be chosen to achieve significant steady state permeate flux (21.1 L h−1 m−2) and minimize membrane fouling, ensuring less than 14.7% flux drop and up to 90% feed recovery. Under these conditions, irreversible fouling below 0.08 L h−2 m−2 bar−1 helped increase the longevity of the membrane and reduce the costs of the treatment. For 10 m3 day−1 OMW-2 on average, 47.4 m2 required membrane area and 0.87 € m−3 total costs for the RO process were estimated.
机译：在哈恩（西班牙）的一家橄榄油厂中，已经进行了工业规模的二级处理，该二级处理来自采用两阶段橄榄油生产工艺（OMW-2）的工厂生产的橄榄油厂废水。二级处理包括类Fenton氧化，然后进行絮凝沉淀和橄榄石过滤。在这项工作中，对最终反渗透（RO）过程的性能建模和初步成本分析在中试规模上进行了检查，以期对OMW-2进行进一步纯化，目的是封闭工业生产过程的环路。当膜上的湍流增加到雷诺数等于2.6×10 4 时，RO膜上的浓度极化降低了26.3％。应选择中等工作压力（25 bar），以实现显着的稳态渗透通量（21.1 L h -1 m -2 ）并最大程度地减少膜污染，确保低于14.7 ％的助焊剂下降和高达90％的进料回收率。在这些条件下，低于0.08 L h - 2 m - 2 bar - 1 帮助提高膜的寿命并降低治疗费用。对于平均10 m 3 天 -1 OMW-2，需要47.4 m 2 所需的膜面积，而0.87€m −3 < / sup>估算了RO过程的总成本。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
代理获取

客服邮箱：kefu@zhangqiaokeyan.com

京公网安备：11010802029741号 ICP备案号：京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有

  • 客服微信

  • 服务号