Process for direct hydrogen injection in liquid full hydroprocessing reactors
View Patent ↗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.
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.
2. The process of claim 1 further comprising venting excess gas from a headspace above at least one of the one or more hydroprocessing-catalyst beds.
3. The process of claim 2 wherein the total amount of hydrogen gas vented is not more than 10%, on a molar basis, of total hydrogen gas directly injected into the one or more hydroprocessing-catalyst bed(s).
4. The process of claim 2 wherein the total amount of hydrogen gas vented is not more than 5%, on a molar base, of total hydrogen gas directly injected into the one or more hydroprocessing-catalyst bed(s).
5. The process of claim 1 wherein the down flow reactor comprises two or more hydroprocessing-catalyst beds and hydrogen gas is directly injected into all of the two or more hydroprocessing-catalyst beds.
6. The process of claim 1 wherein the down flow reactor comprises two or more hvdroprocessing-catalyst beds, each catalyst bed has a catalyst volume, and the catalyst volume increases with each succeeding bed.
7. The process of claim 6 wherein the hydrogen consumption in each catalyst bed is about the same.
8. The process of claim 1 wherein no more than 10% of the hydrogen gas directly injected into the at least one of the one or more hydroprocessing-catalyst beds remains in the gas phase long enough to escape into a headspace above the at least one of the one or more hydroprocessing-catalyst beds.
9. The process of claim 1 wherein no more than 1% of the hydrogen gas directly injected into the at least one of the one or more hydroprocessina-catalyst beds remains in the gas phase long enough to escape into a headspace above the at least one of the one or more hydroprocessing-catalyst beds.
10. The process of claim 1 , wherein the liquid feed mixture comprises diluent and the volume ratio of diluent to liquid hydrocarbon feed is less than about 5.
11. The process of claim 1 , wherein the liquid feed mixture comprises diluent and the volume ratio of diluent to liquid hydrocarbon is less than 1.
12. The process of claim 1 wherein the liquid feed mixture comprises diluent and the volume ratio of diluent to liquid hydrocarbon is less than 0.5.
13. The process of claim 10 wherein the diluent is recycled effluent from one of the hydroprocessing-catalyst beds.
14. The process of claim 11 wherein the diluent is recycled effluent from one of the hydroprocessing-catalyst beds.
15. The process of claim 12 wherein the diluent is recycled effluent from one of the hydroprocessing-catalyst beds.
16. The process of claim 1 wherein no diluent is present.
17. The process of claim 1 wherein the hydrogen gas is injected directly into at least one of the one or more hydroprocessing-catalyst beds through a bubbler, a sparge tube, or a perforated annular ring.
18. The process of claim 1 wherein more than one catalyst bed is present, each catalyst bed has a catalyst volume, and the catalyst volume increases with each succeeding bed.
19. The process of claim 18 wherein the hydrogen consumption in each catalyst bed is about the same.