Method and arrangement for feeding heat-sensitive materials to fixed-bed reactors
The invention relates to an arrangement for feeding heat-sensitive feedstock to a fixed-bed reactor system comprising means for product recycle and a fixed-bed reactor system comprising a fixed-bed reactor comprising at least one reaction zone having at least one catalyst bed and said reaction zone comprising a cold feed distributor arranged on top of each catalyst bed and a conventional distributor arranged above each cold feed distributor. Also a method is provided for feeding heat-sensitive feedstock to a fixed-bed reactor system wherein said fixed-bed reactor system comprises means for product recycle and a fixed-bed reactor comprising at least one reaction zone having at least one catalyst bed and said reaction zone comprising a cold feed distributor arranged on top of each catalyst bed and a conventional distributor arranged above each cold feed distributor.
1. A method for feeding heat-sensitive feedstock to a fixed-bed reactor system,
wherein said fixed-bed reactor system comprises means for product recycle and a fixed bed reactor comprising more than one reaction zone,
wherein each of the more than one reaction zone comprises at least one catalyst bed, and
wherein a cold feed distributor is arranged on top of each catalyst bed and a conventional distributor is arranged above each cold feed distributor,
said process comprising introducing a liquid feed comprising the heat-sensitive feedstock into the fixed-bed reactor system to each reaction zone with the cold feed distributor, and
introducing a dilution stream comprising at least part of a product recycle into the fixed-bed reactor system at the top of the fixed-bed reactor and to each reaction zone with the conventional distributor,
wherein the heat-sensitive feedstock is at least one feedstock selected from the group consisting of a fatty acid, a derivative thereof, and a bio oil.
2. The method according to claim 1 , wherein a temperature of the liquid feed is from 20 to 250° C.
3. The method according to claim 1 , wherein the liquid feed is mixed with said dilution stream having a temperature of 50-340° C. higher than a temperature of the liquid feed, before introducing to each reaction zone.
4. The method according to claim 1 , wherein a temperature of said dilution stream is between 280 and 450° C.
5. The method according to claim 1 , wherein at least one gaseous component is introduced to said dilution stream and then to the top of the fixed-bed reactor, wherein the gaseous component is hydrogen or a gas containing hydrogen.
6. The method according to claim 1 , wherein at least one gaseous component is introduced to at least one reaction zone together with the liquid feed, wherein the gaseous component is hydrogen or a gas containing hydrogen.
7. The method according to claim 2 , wherein said temperature of the liquid feed is from 60 to 240° C.
8. A method for feeding heat-sensitive feedstock to a fixed-bed reactor system,
wherein said fixed-bed reactor system comprises means for product recycle and a fixed bed reactor comprising more than one reaction zone,
wherein each of the more than one reaction zone comprises at least two catalyst beds, and
wherein a cold feed distributor is arranged on top of each of said at least two catalyst beds and a conventional distributor is arranged above each cold feed distributor,
said process comprising introducing a liquid feed comprising the heat-sensitive feedstock into the fixed-bed reactor system to each reaction zone with the cold feed distributor, and
introducing a dilution stream comprising at least part of a product recycle into the fixed-bed reactor system at the top of the fixed-bed reactor and to each reaction zone with the conventional distributor,
wherein the heat-sensitive feedstock is at least one feedstock selected from the group consisting of a fatty acid, a derivative thereof, and a bio oil.
9. The method according to claim 8 , wherein a temperature of the liquid feed is from 20 to 250° C.
10. The method according to claim 9 , wherein a temperature of said dilution stream is between 280 and 450° C.
11. The method according to claim 10 , wherein at least one gaseous component is introduced to said dilution stream and then to the top of the fixed-bed reactor, wherein the gaseous component is hydrogen or a gas containing hydrogen.
12. The method according to claim 1 , wherein the heat-sensitive feedstock is at least one component selected from the group consisting of a C 12 -C 24 fatty acid and a derivative thereof.
13. The method according to claim 12 , wherein the derivative of the fatty acid is at least one component selected from the group consisting of an anhydride, an ester, and a triglyceride.
14. The method according to claim 1 , wherein the bio oil is at least one component selected from the group consisting of a plant oil, an animal oil, a fish oil, a compound derived therefrom, and mixtures thereof.
15. The method according to claim 8 , wherein the heat-sensitive feedstock is at least one component selected from the group consisting of a C 12 -C 24 fatty acid and a derivative thereof.
16. The method according to claim 15 , wherein the derivative of the fatty acid is at least one component selected from the group consisting of an anhydride, an ester, and a triglyceride.
17. The method according to claim 8 , wherein the bio oil is at least one component selected from the group consisting of a plant oil, an animal oil, a fish oil, a compound derived therefrom, and mixtures thereof.