Tube isothermal catalytic reactor
Vertical reactor ( 1 ) for chemical reactions, comprising a tube heat exchanger ( 6 ) immersed in a catalytic bed ( 5 ), wherein said tube exchanger ( 6 ) comprises a plurality of straight tube bundles ( 6.1, 6.2 ) with respective tube plates for feeding ( 9.1, 9.2 ) and collecting ( 10.1, 10.2 ) the heat exchange fluid, and wherein the tube bundles and the respective tube plates are vertically staggered so as to allow access to the shell side.
1. A vertical chemical reactor comprising at least a catalytic bed and a tube heat exchanger immersed in said catalytic bed and fed with a heat exchange fluid, wherein:
said tube exchanger comprises a plurality of straight tube bundles, each tube bundle having a respective feed tube plate and a respective collection tube plate for the fluid,
wherein said plurality of tube bundles comprises at least a first set of tube bundles arranged at a first height inside the reactor and a second set of tube bundles arranged at a second height inside the reactor, the bundles of the first set and the second set being alternated so that each tube bundle is staggered vertically with respect to the adjacent bundles,
wherein said tube plates are shaped as circular sectors or ring sectors and each one of said sectors extend substantially along the full radial extension of said catalytic bed.
2. The reactor according to claim 1 , wherein said tube plates have a surface of interface with the tubes, which is flat.
3. The reactor according to claim 1 , wherein the free spaces between adjacent tube plates, due to the vertically staggered arrangement, define access points to the reactor zone containing the catalytic bed, which can be used for loading and unloading catalyst.
4. The reactor according to claim 1 , wherein the tube plates, viewed in cross-section, cover the entire cross-section of the catalytic bed.
5. The reactor according to claim 1 , wherein the tube bundles comprise straight tubes having the same length.
6. The reactor according to claim 1 , wherein the catalytic bed has an essentially annular geometry being situated between two vertical and coaxial cylindrical walls, and the bed is crossed by a radial or axial-radial flow, and the tube plates are formed as ring sectors.
7. The reactor according to claim 1 , for one of the following uses: methanol synthesis reactor, ammonia synthesis reactor, synthesis gas shift reactor.