Reactor for the catalytic treatment of a gas stream
View Patent ↗A reactor may have a catalyst bed for the catalytic treatment of a gas stream, with the catalyst bed extending substantially over a cross section of the reactor. Gas to be treated may axially fly through the catalyst bed. A carrier structure for the catalyst bed that is at least partly floatingly mounted in the reactor may include a sieve element and, radially outwardly, carrier elements fixedly joined to the reactor wall below the sieve element. The sieve element provides a resting surface for the catalyst bed. The sieve element terminates, radially outwardly, at a distance from the reactor wall. The carrier structure also includes support elements for the sieve element that are floatingly mounted in the reactor. An improved floating mounting is thus provided where not only the sieve element itself but also further parts of the carrier structure are mounted to prevent stresses due to thermal expansion.
1 . A reactor for catalytic treatment of residual gas for reducing a content of nitrogen oxides in processes for producing nitric acid by the Ostwald process, comprising:
a catalyst bed for catalytic treatment of a gas stream, wherein the catalyst bed extends substantially over a cross section of the reactor and the catalyst bed is axially flown through by gas to be treated; and
a carrier structure for the catalyst bed that is at least partly floatingly mounted in the reactor, wherein the carrier structure comprises:
a sieve element,
radially outwardly, carrier elements fixedly joined to a reactor wall below the sieve element, wherein the sieve element provides a resting surface for the catalyst bed, wherein the sieve element terminates, radially outwardly, at a distance from the reactor wall, and
support elements for the sieve element that are floatingly mounted in the reactor;
wherein the carrier elements fixedly joined to the reactor wall include brackets on which the support elements displaceably rest;
wherein the sieve element rests on the displaceable support elements.
2 . The reactor of claim 1 wherein two or more of the brackets are respectively spaced apart from one another in a longitudinal direction or in a circumferential direction of the reactor, wherein the support elements displaceably rest on the two or more of the brackets, wherein the sieve element rests on one or more of the support elements.
3 . The reactor of claim 1 wherein the support elements displaceably rest on the brackets with two degrees of freedom of motion in two directions approximately perpendicular to one another.
4 . The reactor of claim 3 wherein the support elements rest on the brackets such that the support elements are displaceable in a longitudinal direction of the brackets and in a transverse direction of the brackets.
5 . The reactor of claim 1 wherein the brackets are wider in a transverse direction of the brackets than the support elements.
6 . The reactor of claim 1 wherein the support elements terminate at a distance from the reactor wall.
7 . The reactor of claim 1 wherein cheeks are mounted to the brackets such that the cheeks limit displaceable motion of the support elements relative to the brackets in a transverse direction of the brackets.
8 . The reactor of claim 7 wherein in each case two parallel cheeks of the cheeks are spaced apart from one another and are mounted on both sides of the brackets, wherein the two parallel cheeks are joined to one another via a spacer element extending in a transverse direction.
9 . The reactor of claim 8 comprising a sleeve that is force-locked connected to the two parallel cheeks as the spacer element.
10 . The reactor of claim 8 wherein each support element comprises a slot and extends through a slot transverse to the support element.
11 . The reactor of claim 1 wherein the carrier structure comprises a carrier element circumferentially arranged at the reactor wall and jointed thereto, wherein the sieve element floatingly rests on the carrier element at a distance from the reactor wall such that an edge gap between the sieve element and the reactor wall remains.
12 . The reactor of claim 1 comprising a circumferential cover plate that covers an edge gap between the sieve element and the reactor wall.
13 . The reactor of claim 12 wherein an edge region of the sieve element that faces the reactor wall is enclosed by the circumferential cover plate and a carrier element of the carrier structure that is circumferentially arranged at the reactor wall and jointed thereto.
14 . The reactor of claim 1 configured as:
a horizontal reactor where the residual gas flows through the catalyst bed substantially perpendicularly or transversely to a vessel axis, or
a vertical reactor where the residual gas flows through the catalyst bed substantially in an axis direction or parallel to a vessel axis.
15 . The reactor of claim 1 comprising stiffening ribs that are approximately vertically oriented, extend along the sieve element, and are spaced apart from one another, with the stiffening ribs being disposed above or below the sieve element in the catalyst bed.
16 . The reactor of claim 1 wherein the catalyst bed is a first catalyst bed, the reactor comprising a second catalyst bed, wherein the catalyst beds are spaced apart from one another, wherein at least a portion of the gas stream flows via a first inlet to the first catalyst bed, wherein at least a portion of the gas stream flows via a second inlet to the second catalyst bed.
17 . The reactor of claim 16 wherein the first inlet and the second inlet are fluidically connected to one another via an inlet manifold.
18 . The reactor of claim 16 wherein at least a portion of the gas stream is dischargeable from the reactor via a first outlet in a region of the first catalyst bed, wherein at least a portion of the gas stream is dischargeable from the reactor via a second outlet in a region of the second catalyst bed.
19 . The reactor of claim 18 wherein the first outlet and the second outlet are fluidically connected to one another via an outlet manifold.
20 . The reactor of claim 16 wherein the first catalyst bed and the second catalyst bed are fluidically separated from one another by a separating element.