Axial-radial flow converter
US-10329159-B2 · Jun 25, 2019 · US
US9687801B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9687801-B2 |
| Application number | US-201314760829-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 19, 2013 |
| Priority date | Jan 29, 2013 |
| Publication date | Jun 27, 2017 |
| Grant date | Jun 27, 2017 |
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A multi-bed catalytic converter ( 1 ) with inter-bed heat exchangers, comprising a plurality of superimposed catalytic beds and a common heat exchanger ( 5 ) which is shared between two or more consecutive catalytic beds, said common heat exchanger including heat exchange bodies such as a tube bundle ( 6 ), and a wall system ( 9, 10 ) to define a tube side and a shell side respectively, and the shell side comprising at least a first space ( 12 ) and a second space ( 13 ), wherein the first space ( 12 ) receives the product gas leaving the first of said consecutive beds, and the inter-cooled gas leaving said first space ( 12 ) is admitted in the second bed ( 3 - 3 ) for further conversion, and a sealing means ( 14 ) preventing a direct gas passage from said first space to said second space.
Opening claim text (preview).
The invention claimed is: 1. A multi-bed catalytic converter comprising a pressure vessel, a plurality of superimposed catalytic beds, said beds being configured with a cylindrical annular container and an axial core passage, and means for the inter-bed cooling of a gas stream between at least two of said catalytic beds, wherein said means for inter-bed cooling include a heat exchanger which comprises: heat exchange bodies which extend axially and without a solution of continuity through the core passages of at least two consecutive catalytic beds, and a wall system which is also arranged in said core passages and surrounds said heat exchange bodies, to define a boundary of a shell side of said heat exchanger, wherein said wall system is structured in such a way that: the shell side of said heat exchanger comprises at least a first space and a second space, and said first space has a gas inlet and a gas outlet, the inlet being in communication with an outlet of a first of said consecutive catalytic beds, to receive a hot gas leaving said first bed, and the outlet being in communication with the inlet of a second of said consecutive catalytic beds, so that the inter-cooled gas leaving said first space can enter said second bed for further conversion, and said second space has a gas inlet in communication with the outlet of said second bed, and wherein the converter also comprises sealing means to prevent a direct gas passage from said first space to said second space. 2. The converter according to claim 1 , the outlet of the first space being in communication with the inlet of said second catalytic bed via a chamber located between said least two consecutive catalytic beds. 3. The multi-bed catalytic converter according to claim 1 , said wall system comprising a first cylindrical wall and a second cylindrical wall, the first wall surrounding an upper portion of said heat exchange bodies and the second wall surrounding a lower portion of said heat exchange bodies, and wherein the second wall is distanced from the first wall, so that said first wall and second wall form a shell with a gap. 4. The converter according to claim 3 , said first wall being located in the central passage of said first catalytic bed, and said second wall being located in the central passage of said second catalytic bed, and said gap being located between said first and second catalytic beds. 5. The converter according to claim 1 , said sealing means including a first elastic ring member and a second elastic ring member, and a seal between said elastic members. 6. The converter according to claim 5 , said seal being a labyrinth seal. 7. The converter according to claim 5 , said first member being fixed to the heat exchange bodies, and said second member being fixed to a wall of one of said consecutive catalytic beds. 8. The converter according to claim 1 , said heat exchange bodies being a bundle of tubes. 9. The converter according to claim 1 , comprising also a quench line arranged to feed a quench gas for mixing with the partially reacted gas stream leaving said first space of the shell side of said heat exchanger. 10. The converter according to claim 1 , said heat exchanger being extended through more than two consecutive catalytic beds. 11. The converter according to claim 1 , comprising a structurally independent catalytic cartridge, and said catalytic beds and means for inter-bed cooling being part of said catalytic cartridge. 12. The converter according to claim 1 , comprising: four superimposed catalytic beds, a top inter-bed exchanger, fitted in the central passage of the first annular bed and arranged to cool the hot flow leaving said first bed, and a bottom inter-bed exchanger, with heat exchange bodies in common between the second bed and third bed. 13. The converter according to claim 1 , the converter being for the synthesis of ammonia or for the synthesis of methanol. 14. A catalytic cartridge for use in a multi-bed catalytic converter, said cartridge comprising: a plurality of superimposed catalytic beds, said beds being configured with a cylindrical annular container and an axial core passage, and means for the inter-bed cooling of a gas stream between at least two of said catalytic beds, wherein said means for inter-bed cooling include a heat exchanger which comprises: heat exchange bodies which extend axially and without a solution of continuity through the core passages of at least two consecutive catalytic beds, and a wall system which is also arranged in said core passages and surrounds said heat exchange bodies, to define a boundary of a shell side of said heat exchanger, and wherein said wall system is structured in such a way that: the shell side of said heat exchanger comprises at least a first space and a second space, and said first space has a gas inlet and a gas outlet, the inlet being in communication with an outlet of a first of said consecutive catalytic beds, to receive a hot gas leaving said first bed, and the outlet being in communication with the inlet of a second of said consecutive catalytic beds, so that the inter-cooled gas leaving said first space can enter said second bed for further conversion, and said second space has a gas inlet in communication with the outlet of said second bed, and also comprising sealing means to prevent a direct gas passage from said first space to said second space. 15. A method for the revamping of a converter, said converter having a pressure vessel with a full opening and the method comprising the steps of: removing the existing internals including catalytic beds and heat exchange means, and introducing a pre-assembled cartridge according to claim 14 in the pressure vessel of said converter, via said full opening.
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