Annular catalyst carrier container for use in a tubular reactor
10252236 ยท 2019-04-09
Assignee
Inventors
Cpc classification
B01J2208/00814
PERFORMING OPERATIONS; TRANSPORTING
B01J8/067
PERFORMING OPERATIONS; TRANSPORTING
B01J8/06
PERFORMING OPERATIONS; TRANSPORTING
B01J8/0214
PERFORMING OPERATIONS; TRANSPORTING
B01J2208/06
PERFORMING OPERATIONS; TRANSPORTING
B01J8/0015
PERFORMING OPERATIONS; TRANSPORTING
International classification
B01J8/06
PERFORMING OPERATIONS; TRANSPORTING
B01J8/02
PERFORMING OPERATIONS; TRANSPORTING
B01J8/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
In a catalyst carrier for insertion in a reactor tube of a tubular reactor, the catalyst carrier includes a container for holding catalyst in use. The container has a bottom surface closing the container, and a top surface. A carrier outer wall extends from the bottom surface to the top surface. A seal extends from the container by a distance which extends beyond the carrier outer wall. The carrier outer wall has apertures located below the seal.
Claims
1. A catalyst carrier for insertion in a reactor tube of a tubular reactor, said catalyst carrier comprising: an annular container for holding catalyst in use, said container having a perforated inner container wall defining an inner channel, a perforated outer container wall, a bottom surface closing the annular container, and a top surface closing the annular container; a surface closing the bottom of the inner channel formed by the inner container wall of the annular container; a carrier outer wall extending from the bottom surface to the top surface; a seal extending from the container by a distance which extends beyond the carrier outer wall; said carrier outer wall having apertures located below the seal such that one or more reactants enter the annular container through the perforated inner container wall and flow radially towards the perforated outer container wall wherein the carrier outer wall directs reactants and product upwardly between the inner surface of the carrier wall and the perforated outer container wall of the annular container until they reach the apertures in the carrier outer wall.
2. The catalyst carrier according to claim 1, comprising a cap closing the inner channel formed by the perforated inner container wall, said cap including one or more apertures.
3. The catalyst carrier according to claim 1, wherein the carrier outer wall is smooth or shaped.
4. The catalyst carrier according to claim 1, wherein the apertures in the carrier outer wall are slots.
5. The catalyst carrier according to claim 1, wherein the carrier outer wall is comprised of a wall material and the wall material is left partially attached to the carrier outer wall when the apertures are formed.
6. The catalyst carrier according to claim 5, wherein the attached material is configured to induce direction for the fluid flow.
7. The catalyst carrier according to claim 1, additionally including catalyst.
8. A reactor tube comprising a plurality of catalyst carriers of claim 1.
9. A reactor including one or more reactor tubes of claim 8.
10. A process for carrying out a reaction wherein the reactants enter into a catalyst carrier of claim 1.
Description
(1) The present invention will now be described, by way of example, with reference to the accompanying drawings in which:
(2)
(3)
(4)
(5)
(6)
(7) One example of a catalyst carrier 1 of the present invention is illustrated in
(8) A seal 10 extends from the upper surface 6 and an upstanding collar 11 is provided coaxial with the inner channel 5.
(9) A cap 12 closes the top of inner channel 5. Apertures 13 in the cap allow for fluid ingress.
(10) A carrier outer wall 14 surrounds the container 2. Apertures 16 allow fluid egress from the catalyst carrier.
(11) A catalyst carrier 1 of the present invention is located in a reactor tube 15. The flow of gas is illustrated schematically in
(12) As illustrated in
(13) In the arrangement illustrated in
(14) In this arrangement, the reactants flow through the apertures 21 in the spacer 20 and into the space above the top surface 6. The flow is then the same as illustrated in