VERTICAL CYLINDRICAL REACTOR WITH THIN CATALYST BED
An axial thin-film reactor for carrying out catalytic reactions in the gas phase, comprising a cylindrical pressure casing, a device for letting in a gaseous reactant stream, a device for letting out a gaseous product stream, a device for receiving a catalyst bed arranged vertically in the reaction chamber and isolated from the reactor wall at the sides and at the ends so as to produce two separate chambers for the gaseous reactant stream and the gaseous product stream that are sealed with respect to one another and have two gas-permeable bounding walls arranged plane-parallel to one another. The device is designed in such a way that it has a height-to-thickness ratio greater than 1 and the catalyst bed has a height-to-thickness ratio greater than 1.
1 . Axial thin-layer reactor for the performance of catalytic reactions in the gas phase, comprising:
a cylindrical pressure shell,
a device for the inlet of a gaseous feed stream,
a device for the outlet of a gaseous product stream,
device vertically arranged in the reaction chamber for holding a catalyst bed, separated from the reactor wall on the sides and at the ends so that two separate compartments for the gaseous feed stream and the gaseous product stream are formed, which are sealed against each other,
characterised in that
the vertically arranged device for holding the catalyst bed is provided with two confining walls plane-parallel to each other and permeable to gas,
the device vertically arranged in the reaction chamber for holding the catalyst bed is of a height-to-thickness ratio larger than 1,
the catalyst bed is of a height-to-thickness ratio larger than 1, the catalyst bed extending over its full height along the vertical reactor axis,
the gas inlet and the gas outlet of the catalyst bed are arranged at an angle to the reactor axis, and
the gas inlet and the gas outlet of the reactor are provided at the same height of the cylindrical pressure shell.
2 . Axial thin-layer reactor according to claim 1 , characterised in that the device for holding the catalyst bed is composed of a plurality of vertically arranged devices for holding catalyst beds.
3 . Axial thin-layer reactor according to claim 1 , characterised in that a compensation volume is provided.
4 . Axial thin-layer reactor according to claim 1 , characterised in that the compensation volume is sealed towards all sides.
5 . Axial thin-layer reactor according to claim 1 , characterised in that the compensation volume is open towards the gas inlet side or the gas outlet side.
6 . Axial thin-layer reactor according to claim 1 , characterised in that a manhole and/or an emptying device are provided.
7 . Process for performing catalytic reactions in an axial thin-layer reactor according to claim 1 , characterised in that the passage of the gaseous feed stream through the catalyst bed is predominantly in horizontal direction.
8 .- 9 . (canceled)
10 . Process for performing catalytic reactions according to claim 7 in an axial thin-layer reactor characterised in that:
the compensation volume is sealed towards all sides, and
there is no passage of gaseous feed stream through the compensation volume in the upper part of the catalyst bed.
11 . Process for performing catalytic reactions according to claim 7 in an axial thin-layer reactor characterised in that:
the compensation volume is open towards the gas inlet side or the gas outlet side, and
there is a passage of gaseous feed stream through the compensation volume in the upper part of the catalyst bed.