《Table 3 Product distribution over HZSM-5, HZSM-5@Si O2 and HZSM-5@SBA-15 in MTA reaction》
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《Synthesis of Core-Shell HZSM-5@SBA-15 Composite and Its Performance in the Conversion of Methanol to Aromatics》
Notes:Product distribution was calculated by area normalization method with relative error not exceeding 0.5%.Reaction conditions:0.1 MPa,410oC,WHSV=2.7 h-1,time on stream=16 h.
The catalytic performance of the HZSM-5@SBA-15catalyst in MTA process was tested and compared with HZSM-5@Si O2 and HZSM-5.The methanol conversion,oil yield and BTX selectivity were correlated to the time on stream in Figure 7.Meanwhile,the detailed results of the product distribution achieved by MTA reaction after16 h on stream are listed in Table 3.
图表编号 | XD0011293500 严禁用于非法目的 |
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绘制时间 | 2018.03.30 |
作者 | Wang Lu、Li Jian、Wang Lijuan、Chu Shuang、Yang Lina |
绘制单位 | School of Petrochemical Engineering, Liaoning Shihua University、School of Petrochemical Engineering, Liaoning Shihua University、School of Petrochemical Engineering, Liaoning Shihua University、School of Petrochemical Engineering, Liaoning Shihua University |
更多格式 | 高清、无水印(增值服务) |