Energy conversion apparatus
US-2020370446-A1 · Nov 26, 2020 · US
US9809759B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9809759-B2 |
| Application number | US-201615061560-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 4, 2016 |
| Priority date | Dec 8, 2011 |
| Publication date | Nov 7, 2017 |
| Grant date | Nov 7, 2017 |
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The present disclosure relates to reactor components and their use, e.g., in regenerative reactors. A process and apparatus for utilizing different wetted areas along the flow path of a fluid in a pyrolysis reactor, e.g., a thermally regenerating reactor, such as a regenerative, reverse-flow reactor, is described.
Opening claim text (preview).
What is claimed is: 1. A hydrocarbon pyrolysis reactor, the reactor comprising: a housing enclosing an interior region and having one or more insulation components disposed adjacent to the housing; a plurality of input means configured to manage the flow of one or more streams into the interior region from a location external to the interior region; one or more process flow components configured to manage the flow of fluids through the interior region, wherein the one or more process flow components comprise (i) a first bed packing having a first plurality of flow passages and a first wetted area a v1 ; (ii) a second bed packing having a second plurality of flow passages and a second wetted area a v2 , wherein the ratio of the second wetted area a v2 to the first wetted area a v1 is ≦0.75; and (iii) a third bed packing having a third plurality of flow passages and a third wetted area a v3 , wherein the ratio of the third wetted area a v3 to the second wetted area a v2 is ≦0.75. 2. The hydrocarbon pyrolysis reactor of claim 1 , further comprising a mixing means disposed between the first bed packing and the second bed packing and/or disposed adjacent to the second bed packing. 3. The hydrocarbon pyrolysis reactor of claim 2 , wherein the mixing means comprises one or more different plates. 4. The hydrocarbon pyrolysis reactor of claim 2 , wherein the mixing means consisting essentially of a gap. 5. The hydrocarbon pyrolysis reactor of claim 1 , wherein (i) the first bed packing is a first monolith and the first wetted area a v1 is in a range of 500 m −1 to 4000 m −1 and (ii) the second bed packing is a second monolith and the second wetted area a v2 is in the range of 100 m −1 to 1000 m −1 . 6. The hydrocarbon pyrolysis reactor of claim 1 , wherein the first bed packing is a first monolith and the first wetted area a v1 is in a range of 800 m −1 to 3000 m −1 and the second bed packing is a second monolith and the second wetted area a v2 is in the range of 100 m −1 to 800 m −1 .
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