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Development and Field-Scale Optimization of a Honeycomb Zeolite Rotor Concentrator/Recuperative Oxidizer for the Abatement of Volatile Organic Carbons from Semiconductor Industry

机译:用于减少半导体工业中挥发性有机碳的蜂窝沸石转子浓缩器/蓄热式氧化剂的开发和现场规模优化

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摘要

The combined concentrator/oxidizer system has been proposed as an effective physical-chemical option and proven to be a viable solution that enables Volatile Organic Carbons (VOCs) emitters to comply with the regulations. In this work, a field scale honeycomb zeolite rotor concentrator combined with a recuperative oxidizer was developed and applied for the treatment of the VOC waste gas. The research shows the following: (1) for the adsorption rotor, zeolite is a more appropriate material than Granular Activated Carbon (GAC). The designing and operation parameters of the concentrator were discussed in detail including the size and the optimal rotation speed of rotor. Also the developed rotor performance's was evaluated in the field; (2) Direct Fired Thermal Oxidizer (DFTO), Recuperative Oxidizer (RO), Regenerative Thermal Oxidizer (RTO) and Regenerative Catalytic oxidizer (RCO) are the available incinerators and the RO was selected as the oxidizer in this work; (3) The overall performance of the developed rotor/oxidizer was explored in a field scale under varying conditions; (4) The energy saving strategy was fulfilled by reducing heat loss from the oxidizer and recovering heat from the exhaust gas. Data shows mat the developed rotor/oxidizer could remove over 95% VOCs with reasonable cost and this could be helpful for similar plants when considering VOC abatement
机译:组合式浓缩器/氧化剂系统已被提议作为有效的物理化学选择,并被证明是使挥发性有机碳(VOC)排放体符合法规的可行解决方案。在这项工作中,开发了一种现场规模的蜂窝式沸石转子浓缩器与回热式氧化剂结合,并用于处理VOC废气。研究表明:(1)对于吸附转子,沸石比颗粒活性炭(GAC)更合适。详细讨论了选矿厂的设计和运行参数,包括转子的尺寸和最佳转速。同时,还对开发的转子性能进行了现场评估。 (2)可以使用直接燃烧式热氧化器(DFTO),回热式氧化器(RO),蓄热式氧化器(RTO)和蓄热式催化氧化器(RCO),并且在本工作中选择了RO作为氧化剂; (3)在不同条件下以田间规模研究了研制的转子/氧化剂的整体性能; (4)通过减少氧化剂的热损失并从废气中回收热量来实现节能策略。数据显示,开发的转子/氧化剂可以合理的成本去除95%以上的VOC,这对于考虑减少VOC的类似工厂可能会有帮助

著录项

  • 来源
    《Environmental Science & Technology》 |2012年第1期|p.441-446|共6页
  • 作者单位

    State Environmental Protection Key Laboratory of Environmental Risk Assessment and Control on Chemical Process,School of Resources and Environmental Engineering, East China University of Science and Technology, Shanghai 200237,People's Republic of China;

    Semiconductor Manufacturing International Corporation (SMIC), 18 Zhangjiang Rd, Pudong New Area, Shanghai 201203, People'sRepublic of China,School of Environmental Science and Engineering, Shanghai Jiao Tong University, Shanghai 200240, People's Republic of China;

    State Environmental Protection Key Laboratory of Environmental Risk Assessment and Control on Chemical Process,School of Resources and Environmental Engineering, East China University of Science and Technology, Shanghai 200237,People's Republic of China;

    State Environmental Protection Key Laboratory of Environmental Risk Assessment and Control on Chemical Process,School of Resources and Environmental Engineering, East China University of Science and Technology, Shanghai 200237,People's Republic of China;

    School of Environmental Science and Engineering, Shanghai Jiao Tong University, Shanghai 200240, People's Republic of China;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);美国《化学文摘》(CA);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    c_c: the adsorbent heat capacity (J/kg • K); c_p: the air heat capacity (J/kg•K); t_1: the surface temperature of the oxidizer (℃); t_2: the room temperature (21.8 °C when tested); v: gas superficial velocity passing the wheel (m/s);

    机译:c_c:吸附剂的热容量(J / kg•K);c_p:空气热容(J / kg•K);t_1:氧化剂的表面温度(℃);t_2:室温(测试时为21.8°C);v:气体通过车轮的表面速度(m / s);
  • 入库时间 2022-08-17 14:02:35

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