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Vapor horn

From Wikipedia, the free encyclopedia

A Vapor horn is a device used primarily for two-phase (liquid/vapor) feeds to petroleum refinery fractionators, which is designed to provide both bulk phase separation of the vapor and liquid, and to provide initial distribution of the feed vapor.[1][2][3]

Operation

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For vapor/liquid phase separation, vapor horns utilize an open bottom construction and induced centrifugal action to direct entrained liquid particles to the column wall, which will then flow down into the column sump or collector tray below. Some vapor horn designs employ baffles, to avoid excessive impingement and splashing which can result in the formation of small liquid particles that are at higher risk of being re-entrained. Additional baffles can be employed to eliminate cyclonic motion once the bulk phase separation is complete and the swirling motion is no longer desirable.[1] Some vapor horns have been designed to handle high inlet velocities.[2]

Applications

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Vapor horns often find application on the inlet to crude oil vacuum distillation towers, where liquid entrainment can be quite detrimental to tower performance.[4][5] It has been noted that in high vapor rate vacuum services, vapor horns have low levels of entrainment relative to similar technologies.[6] In some cases, refiners have removed vapor horns within vacuum towers to reduce coking. While this does work as intended, it also has the unintended consequence of increasing carryover into heavy vacuum gas oil, thereby lowering its quality.[7]

References

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  1. ^ a b Koch-Glitsch. "Model 758 Enhanced Vapor Horn" (PDF). Retrieved 13 December 2015.
  2. ^ a b Sulzer. "Sulzer Tangential Gas Inlet Device Vapour Horn". Retrieved 13 December 2015.
  3. ^ AMACS Process Tower Internals. "Feed Inlet Devices". Retrieved 13 December 2015.
  4. ^ Justia Patents. "Oil distillation vacuum column with thickened plate in the vapor horn section". Retrieved 13 December 2015.
  5. ^ Digital Refining. "Entrainment issues in vacuum column flash zones". Retrieved 13 December 2015.
  6. ^ Hanson, D.W. Lieberman, N. and Lieberman, E. "De-entrainment and washing of flash-zone vapors in heavy-oil fractionators" (PDF). Retrieved 13 December 2015.{{cite web}}: CS1 maint: multiple names: authors list (link)
  7. ^ Barletta, T. & Golden, S. "Refiners must optimize FCC feed hydrotreating when producing low-sulfur gasoline" (PDF). Retrieved 13 December 2015.{{cite web}}: CS1 maint: multiple names: authors list (link)