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连续水热氧化苯酚生产小分子有机酸
引用本文:张光义,曾旭,张聚伟,余剑,汪印,许光文.连续水热氧化苯酚生产小分子有机酸[J].同济大学学报(自然科学版),2013,41(5):722-727.
作者姓名:张光义  曾旭  张聚伟  余剑  汪印  许光文
作者单位:1. 中国科学院过程工程研究所多相复杂系统国家重点实验室,北京100190;同济大学污染控制与资源化研究国家重点实验室,上海200092
2. 同济大学污染控制与资源化研究国家重点实验室,上海,200092
3. 中国科学院过程工程研究所多相复杂系统国家重点实验室,北京,100190
基金项目:国家"八六三"高技术研究发展计划,国家自然科学基金
摘    要:以甲酸和乙酸为目标产物,利用自行研发的连续水热反应装置开展了苯酚水热氧化资源化试验研究.结果表明,加入碱显著地促进了甲酸和乙酸的生成,但过量的碱降低了甲酸和乙酸的产率;甲酸和乙酸产率均随反应温度、供氧率、反应时间先增加后减少;在温度300℃、NaOH质量浓度1.0mol.L-1、供氧率70%、反应时间为60s时甲酸和乙酸产率分别达到最高值9.5%和11.2%.基于产物识别探讨了小分子有机酸特别是甲酸和乙酸的生成路径.

关 键 词:水热氧化  苯酚  连续水热反应装置  甲酸  乙酸
收稿时间:2012/4/24 0:00:00
修稿时间:2013/2/20 0:00:00

Continuous hydrothermal oxidation of phenol for small molecule organic acids production
Zhang Guangyi,Zeng Xu,Zhang Juwei,Yu Jian,Yu Jian and Xu Guangwen.Continuous hydrothermal oxidation of phenol for small molecule organic acids production[J].Journal of Tongji University(Natural Science),2013,41(5):722-727.
Authors:Zhang Guangyi  Zeng Xu  Zhang Juwei  Yu Jian  Yu Jian and Xu Guangwen
Institution:State Key Laboratory of Multiphase Complex System, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100091, China; State Key Laboratory of Pollution Control and Resources Reuse, Tongji University, Shanghai 200092, China;State Key Laboratory of Pollution Control and Resources Reuse, Tongji University, Shanghai 200092, China;State Key Laboratory of Multiphase Complex System, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100091, China;State Key Laboratory of Multiphase Complex System, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100091, China
Abstract:With formic and acetic acids as the main objective products, the experimental research hydrothermal oxidation of phenol for producing small molecule organic acids was conducted by using a self-developed continuous-flow hydrothermal reaction apparatus. The results show that the addition of alkali promotes formic and acetic production but excess alkali decreases formic and acetic acids yields. Formic and acetic acids yields increase first and then decrease with the increasing in the oxygen supply, reaction time and temperature. The highest yields of up to 9.5% and 11.2% for formic and acetic acids, respectively, are obtained at the temperature of 300 oC with the concentration of 1.0 mol•L-1 NaOH and oxygen supply of 70% for 60 s. Based on the products recognization, production pathways of the small molecule organic acids, especially formic and acetic acids, are discussed.
Keywords:hydrothermal oxidation  phenol  continuous flow hydrothermal reaction apparatus  formic acid  acetic acid
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