Method for reducing water concentration in a multi-phase column reactor
View Patent ↗The present invention relates to a method and apparatus for water removal in multi-phase reactors operating at Fischer-Tropsch conditions. In a preferred embodiment of the present invention, a method of reducing the concentration of water in a multi-phase reactor for Fisher-Tropsch synthesis containing an expanded slurry bed and a water-rich slurry region includes removing a portion of water from the water-rich slurry from a predetermined region in the reactor, removing the water from the water-rich slurry to form a water-reduced slurry, and returning the water-reduced slurry back to the reactor. Preferably the water-rich slurry region is located between ½ H to H and ½ R to R, where H is the height of the expanded slurry bed and R is the radius of the expanded slurry bed.
1. A method of reducing the concentration of water in a multi-phase reactor for Fischer-Tropsch synthesis containing an expanded slurry bed, including a water-rich region, the method comprising:
a) removing a portion of slurry from the water-rich region in the reactor to form a water-rich slurry stream;
b) removing the water-rich slurry stream from the reactor;
c) removing water from the water-rich slurry stream in a water removal loop to form a water-reduced slurry stream; and
d) returning the water-reduced slurry stream back to the reactor.
2. The method according to claim 1 wherein the water-rich region is located between ½ H and H and between ½ R and R, where H is the height of the expanded slurry bed and R is the radius of the expanded slurry bed.
3. The method according to claim 2 wherein the water-rich region is located between ¾ H and H and between ¾ R and ⅞ R.
4. The method according to claim 1 wherein at least 60% of the water initially present in the water-rich slurry stream is removed in step b).
5. The method according to claim 4 wherein at least 80% of water initially present in the water-rich slurry stream is removed.
6. The method according to claim 1 , further including degassing the water-rich slurry stream prior to step (b).
7. The method according to claim 1 wherein step b) includes a technique selected from the group consisting of phase addition, phase creation, and stripping.
8. The method according to claim 1 wherein a difference in fluid densities causes slurry to flow through the water removal loop.
9. The method according to claim 1 wherein step b) is carried out using a semi-permeable barrier.
10. The method according to claim 1 wherein step b) is carried Out using a solid agent.
11. The method according to claim 1 wherein step b) is carried out using an external field or gradient.
12. The method according to claim 1 wherein step a) is carried out using a slurry removal device comprising a manifold having a plurality of intake ports.
13. The method according to claim 1 wherein the reactor has a wall and wherein step a) is carried out using a slurry removal device comprising a plurality of openings in said reactor wall.
14. The method according to claim 1 wherein step a) is carried out using a slurry removal device comprising an annular ring having at least one opening positioned in the water-rich slurry region.
15. A method for producing hydrocarbons comprising:
a) contacting a synthesis gas with a hydrocarbon synthesis catalyst in a multi-phase reactor having an expanded slurry bed, including a water-rich slurry region, under reaction conditions effective to form gaseous and/or liquid product streams comprising hydrocarbons, water and secondary products from the synthesis gas;
b) removing a portion of slurry from the water-rich slurry region in the reactor to form a water-rich slurry stream;
c) flowing the water-rich slurry stream out of the reactor into a water removal zone and removing water from the water-rich slurry stream so as to form a water-reduced slurry; and
d) returning the water-reduced slurry stream back into the reactor.
16. The method according to claim 15 wherein the water-rich slurry region is located between ½ H and H and between ½ R and R, where H is the height of the expanded slurry bed and R is the radius of the expanded slurry bed.
17. The method according to claim 15 wherein the water-rich slurry region is located between ¾ H and H and between ¾ R and ⅞ R.
18. The method according to claim 15 wherein at least 60% of water initially present in the water-rich slurry stream is removed.
19. The method according to claim 18 wherein at least 80% of water initially present in the water-rich slurry stream is removed.
20. The method according to claim 15 further including the step of degassing the water-rich slurry stream prior to step c).
21. The method according to claim 15 wherein step c) includes a technique selected from the group consisting of phase addition, phase creation, and stripping.
22. The method according to claim 15 wherein a difference in fluid densities causes slurry to flow through the water removal zone and back into the reactor.
23. The method according to claim 15 wherein the water removal zone includes a barrier separation system.
24. The method according to claim 15 wherein the water removal zone includes a solid agent separation system.
25. The method according to claim 15 wherein the water removal zone includes an external field or gradient separation system.
26. The method according to claim 15 wherein step b) is carried out using a slurry removal device comprising a manifold having a plurality of intake ports.
27. The method according to claim 15 wherein the reactor has a wall and wherein step b) is carried out using a slurry removal device comprising a plurality of openings in said reactor wall.
28. The method according to claim 15 wherein step b) is carried out using a slurry removal device comprising an annular ring having at least one opening positioned in the water-rich slurry region.