发明名称 |
Process for direct hydrogen injection in liquid full hydroprocessing reactors |
摘要 |
A process of hydroprocessing a hydrocarbon in a down flow reactor comprising one or more hydroprocessing-catalyst beds. The hydrocarbon feed is mixed with hydrogen and optionally diluent to form a liquid feed mixture wherein hydrogen is dissolved in the mixture, and the liquid feed mixture is introduced into the down flow reactor under hydroprocessing conditions. The hydroprocessing-catalyst bed(s) are liquid-full and the feed reacts by contact with the catalyst. Hydrogen gas is injected into at least one of the hydroprocessing-catalyst beds such that at least part of the hydrogen consumed in that bed is replenished and the liquid-full condition is maintained. In a multi-bed reactor, hydrogen gas may be injected into more than one or all of the hydroprocessing-catalyst beds. |
申请公布号 |
US9365781(B2) |
申请公布日期 |
2016.06.14 |
申请号 |
US201213480574 |
申请日期 |
2012.05.25 |
申请人 |
E I DU PONT DE NEMOURS AND COMPANY |
发明人 |
Dindi Hasan |
分类号 |
C10G65/02;C10G49/00 |
主分类号 |
C10G65/02 |
代理机构 |
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代理人 |
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主权项 |
1. A hydroprocessing process comprising:
(a) providing a down flow reactor comprising one or more hydroprocessing-catalyst beds and providing when two or more hydroprocessing-catalyst beds are present that said beds are disposed in sequence and in liquid communication; (b) contacting a hydrocarbon feed with hydrogen and optionally diluent to form a liquid feed mixture wherein hydrogen is dissolved in the mixture; (c) introducing said liquid feed mixture into the down flow reactor under hydroprocessing conditions; (d) reacting the liquid feed mixture by contact with the one or more hydroprocessing-catalyst beds, wherein each of said one or more hydroprocessing-catalyst beds is substantially liquid-full; (e) injecting hydrogen gas directly into at least one of the one or more hydroprocessing-catalyst beds at a controlled rate such that at least part of the hydrogen consumed in each bed by the hydroprocessing reaction is replenished and the substantially liquid-full condition in each hydroprocessing-catalyst bed is maintained; and (f) adjusting the controlled rate of hydrogen gas directly injected into at least one of the one or more hydroprocessing-catalyst beds based on the amount of hydrogen gas determined to be in a headspace above said at least one of the one or more hydroprocessing-catalyst beds. |
地址 |
Wilmington DE US |