Filtering distributor plate for supplying a fixed bed reactor having a co-current downflow of gas and liquid for the treatment of heavy clogging feeds
US-9480957-B2 · Nov 1, 2016 · US
US10537866B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10537866-B2 |
| Application number | US-201816221071-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 14, 2018 |
| Priority date | Dec 21, 2017 |
| Publication date | Jan 21, 2020 |
| Grant date | Jan 21, 2020 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
The invention involves a scale collection device that is located within downflow reactor head for removing solids from feed streams to increase reactor operating cycle time without impact on effective reactor space for catalyst loading. More particularly, a filtering zone is located in an upper portion of a reactor vessel above a rough liquid distribution tray and a distribution tray.
Opening claim text (preview).
The invention claimed is: 1. A reactor comprising an upper portion and a lower portion wherein the upper portion comprises: a rough liquid distribution tray comprising a cylindrical wall spaced apart from a reactor wall and a perforated bottom plate; a scale collection device within the rough liquid distribution tray, the scale collection device comprising a plurality of media support/spacers, the plurality of media support/spacers located on the bottom plate of the rough liquid distribution tray, and the media support/spacers and the cylindrical wall of the rough liquid distribution tray defining a filtering zone; and a vapor-liquid distribution tray located below the rough liquid distribution tray and wherein the vapor-liquid distribution tray comprises a plurality of distributors. 2. The reactor of claim 1 , wherein the filtering zone comprises a first portion in an upper region comprising porous pellets having larger pores than a second portion in a lower region of the filtering zone. 3. The reactor of claim 1 , wherein the filtering zone comprises porous ceramic pellets. 4. The reactor of claim 1 , wherein the plurality of media support/spacers are coupled to the rough liquid distribution tray. 5. The reactor of claim 1 , wherein the plurality of media support/spacers comprise profile wire. 6. The reactor of claim 1 , wherein the plurality of media support/spacers comprise grating. 7. The reactor of claim 1 , wherein the plurality of media support/spacers comprise grating and wire mesh. 8. The reactor of claim 1 , wherein the plurality of media support/spacers comprises a perforated plate. 9. The reactor of claim 1 , further comprising a plurality of overflow chimneys, wherein the overflow chimneys contain slots, wherein the slots may be v-shaped. 10. The reactor of claim 1 , further comprising a plurality of overflow chimneys, wherein the overflow chimneys contain cuts. 11. The reactor of claim 1 , further comprising a plurality of overflow chimneys, wherein the overflow chimneys contain holes. 12. The reactor of claim 1 , further comprising a plurality of overflow chimneys, wherein the overflow chimneys may comprise bubble caps. 13. The reactor of claim 1 , wherein the perforated bottom plate of the rough liquid distribution tray contains holes sized to generate the desired liquid level on the rough liquid distribution tray. 14. An apparatus comprising an upper portion and a lower portion wherein the upper portion comprises: a rough liquid distribution tray comprising a cylindrical wall spaced apart from a reactor wall and a perforated bottom plate; a scale collection device within the rough liquid distribution tray, the scale collection device comprising a plurality of media support/spacers, the plurality of media support/spacers located on the bottom plate of the rough liquid distribution tray, and the media support/spacers and the cylindrical wall of the rough liquid distribution tray defining a filtering zone; a plurality of overflow chimneys attached to the media support/spacers and extending upward through the filtering zone; and a vapor-liquid distribution tray located below the rough liquid distribution tray and wherein the vapor-liquid distribution tray comprises a plurality of distributors. 15. The apparatus of claim 14 , wherein the filtering zone comprises a first portion in an upper region comprising porous pellets having larger pores than a second portion in a lower region of the filtering zone. 16. The apparatus of claim 14 , wherein the filtering zone comprises porous ceramic pellets. 17. The apparatus of claim 14 , wherein the perforated bottom plate of the rough liquid distribution tray contains holes sized to generate the desired liquid level on the rough liquid distribution tray.
the feeding side being of particular interest · CPC title
Membranes, e.g. feeding or removing reactants or products to or from the catalyst bed through a membrane · CPC title
Flow distribution elements · CPC title
Downward filtration, the filter material being supported by pervious surfaces · CPC title
Filters in combination with devices for the removal of gas, air purge systems · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.