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第 36 卷第 6 期                             精   细   化   工                                  Vol.36, No.6
             201 9 年 6 月                             FINE CHEMICALS                                 June    2019


              催化与分离提纯技术
                     MO /Y 催化剂常温催化臭氧氧化甲苯的性能
                            x


                                      黄金花      1,2,3 ,叶丽萍      1,2,3* ,罗   勇   1,2,3

                 (1.  上海化工研究院有限公司,上海    200062;2.  聚烯烃催化技术与高性能材料国家重点实验室,上海
                 200062;3.  上海市聚烯烃催化技术重点实验室,上海    200062)

                 摘要:以 Y 分子筛为载体,采用等体积浸渍法制备了 MO x /Y 催化剂,并用于常温催化臭氧氧化甲苯反应。采用
                 XRD、BET、H 2 -TPR、甲苯吸附对催化剂进行表征,以甲苯转化率维持 95%以上的时间(t 95 )为指标对催化性
                                                                                                    2
                 能进行评价。结果表明:10%  MnO 2 /Y 催化剂〔m(MnO 2 )/m(Y)=0.1〕具有较大的比表面积(538.6  m /g)
                                3
                 和孔容积(0.440 cm /g),较好的催化臭氧氧化甲苯活性(t 95 =210 min);CuO 的加入提高了催化活性,5% MnO 2 -5%
                 CuO/Y  〔m(MnO 2 )/m(Y)=0.05 且 m(CuO)/m(Y)=0.05〕催化剂上 t 95 =240  min,CO x 选择性为 80.6%,CO 2 与 CO
                 摩尔比为 4.970。由表征结果可知,较大的比表面积和孔容积有利于甲苯吸附,CuO 与 MnO 2 之间的相互作用促
                 进了氧化还原性能的提高,进而有利于催化活性的提高。GC-MS 结果表明:反应副产物堵塞催化剂孔道,占据
                 催化剂表面活性位,导致催化剂失活。5% MnO 2 -5% CuO/Y 催化剂失活-再生 4 次后 t 95 可达 220 min。
                 关键词:常温;臭氧;甲苯;MnO 2 ;CuO;Y 分子筛;再生;催化技术
                 中图分类号:O643.3      文献标识码:A      文章编号:1003-5214 (2019) 06-1132-07



                          Catalytic performance of MO x/Y Catalyst for the Toluene
                                  Oxidation with Ozone at Room Temperature


                                       Huang Jin-hua 1,2,3 , Ye Li-ping 1,2,3* , Luo Yong 1,2,3
                 (1. Shanghai Research Institute of Chemical Industry Co., Ltd, Shanghai 200062, China; 2. State Key Laboratory of
                 Polyolefin and Catalysts, Shanghai 200062, China; 3. Shanghai Key Laboratory of Catalyst Technology for Polyolefin,
                 Shanghai 200062, China)

                 Abstract: A series of MO x/Y catalysts were prepared by incipient-wetness impregnation method with Y
                 zeolite as support for the toluene oxidation with ozone at room temperature. The catalysts were characterized
                 by XRD, BET, H 2-TPR and toluene adsorption techniques. The catalytic performance was evaluated by the
                 time (t 95) of toluene conversion rate above 95%. The results revealed that 10% MnO 2/Y〔m(MnO 2)/m(Y)
                                                                     2
                                                                                                 3
                 =0.1〕catalyst  had  a  larger  specific  surface  area  of  538.6  m /g and pore  volume of  0.440  cm /g,  and
                 exhibited a better catalytic activity for toluene oxidation with ozone at room temperature. The addition of
                 CuO improved the catalytic activity of 5% MnO 2-5% CuO/Y〔m(MnO 2)/m(Y)=0.05 and m(CuO)/m(Y)=
                 0.05〕catalyst (t 95 of 240 min, CO x selectivity of 80.6%, and molar ratio of CO 2 to CO of 4.970). It was
                 found that larger surface area and pore volume promoted toluene adsorption, the interaction between CuO
                 and MnO 2 improved the reduction property of 10% MnO 2/Y catalyst. Thus, 5% MnO 2-5% CuO/Y catalyst
                 exhibited a high catalytic activity in the toluene oxidation with ozone at room temperature. GC-MS results
                 revealed that the by-products blocked the catalysts pores and occupied active sites on the surface of the
                 catalysts, resulting in the inactivation of the catalysts. The results of regeneration experiment indicated that
                 5%  MnO 2-5%  CuO/Y〔m(MnO 2)/m(Y)=0.05  and  m(CuO)/m(Y)=0.05〕catalyst  showed  good  catalytic
                 activity with t 95 of 220 min after regeneration for four times.
                 Key words: room temperature; ozone; toluene; MnO 2; CuO; Y zeolite; regeneration; catalysis technology




                 收稿日期:2018-09-19;  定用日期:2019-01-16; DOI: 10.13550/j.jxhg.20180698
                 作者简介:黄金花(1987—),女,工程师,硕士。联系人:叶丽萍(1981—),女,高工,博士,电话:021-52815377(1823),E-mail:
                 ylp_by@126.com。
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