| 抽余油加氢催化剂FHDA-10的工业应用 |
| |
| 引用本文： | 陈齐全,邹圣武.抽余油加氢催化剂FHDA-10的工业应用[J].石化技术与应用,2011,29(5):439-442,452. |
| |
| 作者姓名： | 陈齐全 邹圣武 |
| |
| 作者单位： | 中国石化九江分公司,江西九江,332004 |
| |
| 摘 要： | 介绍了抽余油加氢催化剂FHDA-10在10万t/a芳烃抽提装置上的工业应用情况。运行结果表明,在反应温度为100℃,反应压力为1.2 MPa,氢油体积比为168的操作条件下,可生产高等级的6#,120#溶剂油产品,并使装置能耗下降100～130 MJ/t。
|
| 关 键 词： | 重整抽余油 芳烃抽提 加氢催化剂 溶剂油 捕硅剂 溴指数 |
Industrial application of reformed raffinate oil hydrogenation catalyst FHDA-10 |
| |
| Chen Qiquan,Zou Shengwu.Industrial application of reformed raffinate oil hydrogenation catalyst FHDA-10[J].Petrochemical Technology & Application,2011,29(5):439-442,452. |
| |
| Authors: | Chen Qiquan Zou Shengwu |
| |
| Affiliation: | Chen Qiquan,Zou Shengwu(Jiujiang Company,SINOPEC,Jiujiang 332004,China) |
| |
| Abstract: | Industrial application of reformed raffinate oil hydrogenation catalyst FHDA -10 in 100 kt/a aromatics extraction unit was introduced. The results showed that under the operating condition of temperature 100 ℃ ,pressure 1.2 MPa and volume ratio of hydrogen to oil 168 ,the 6^# and 120^# high -grade solvent naphthas could be produced ,and the energy consumption of the unit could be reduced by 100 - 130 MJ/t. |
| |
| Keywords: | reformed raffinate oil aromatics extraction hydrogenation catalyst solvent naphtha silicon trapping agent bromine index |
| 本文献已被 CNKI 维普 万方数据 等数据库收录！ |
|
