发明名称 |
Process and Device for Treating Catalyst Discharged from Bubbling Bed Hydrogenation of Residual Oil |
摘要 |
The invention relates to a process and a device for treating a catalyst discharged from bubbling bed hydrogenation of residual oil. Provided is a process for treating a catalyst discharged from bubbling bed hydrogenation of residual oil, comprising the following steps: (1) adjustment and control to reduce viscosity; (2) desorption and separation by rotational flow; and (3) separation and resource utilization of an oil-water-catalyst three phase. Also provided is a device for treating a catalyst discharged from bubbling bed hydrogenation of residual oil. |
申请公布号 |
US2015218463(A1) |
申请公布日期 |
2015.08.06 |
申请号 |
US201214398059 |
申请日期 |
2012.07.25 |
申请人 |
Li Jianping;Wang Jiangang;Wang Hualin;Zhang Yanhong;Cui Xin;Shen Ling;Li Liquan;Chen Chonggang;Zeng Qian;Zhao Ying |
发明人 |
Li Jianping;Wang Jiangang;Wang Hualin;Zhang Yanhong;Cui Xin;Shen Ling;Li Liquan;Chen Chonggang;Zeng Qian;Zhao Ying |
分类号 |
C10G53/02;B01J38/48 |
主分类号 |
C10G53/02 |
代理机构 |
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代理人 |
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主权项 |
1. A process for treating a catalyst discharged from bubbling bed for hydrogenation of residual oil, comprising the following steps:
(1) adjustment and control to reduce viscosity, wherein a catalyst discharged intermittently from a bubbling bed reactor for hydrogenation of residual oil is adjusted for storage and then discharged continuously, and is subjected to temperature adjustment by adding water, such that a viscosity of an oil adsorbed on a surface and within pores of discharged catalyst particles is reduced, and a flowability of the adsorbed oil on the surface and within the pores of the discharged catalyst particles is improved; (2) desorption and separation by rotational flow, wherein the adsorbed oil is desorbed and separated from the surface and the pores of the discharged catalyst particles by a flowing shear force from a rotational flow field; and (3) separation and resource utilization of an oil-water-catalyst three phase, wherein an oil/water/catalyst mixture produced from the desorption and separation by rotational flow step is subjected to three-phase separation, achieving recovery of oil, recycling of water obtained by separation, and full recovery of solid particles obtained by separation. |
地址 |
Shanghai CN |