Mixing Reactor and Related Process
US-2015367318-A1 · Dec 24, 2015 · US
US11148112B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11148112-B2 |
| Application number | US-201816628791-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 27, 2018 |
| Priority date | Jul 6, 2017 |
| Publication date | Oct 19, 2021 |
| Grant date | Oct 19, 2021 |
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 present invention relates to different liquid distributors for monolith in multiphase applications. The present invention more particularly relates to distributor devices in the form of a single injection and multiple injection pipe distributors; shower head distributor comprising a plurality of holes for plunging liquid; a packing of spherical particles with a pre-distributor to split the liquid into manifold streams, before entry into the monolith bed. The present invention provides liquid distributors for monolith in multiphase applications providing improved liquid distribution into the monolith bed resulting in uniform fluid flow in each channel so as to make maximum use of the catalyst surface area.
Opening claim text (preview).
The invention claimed is: 1. A device for distributing a liquid flow stream downwardly into a monolith bed having a monolith surface, comprising: a. an enclosed vessel comprising inlet port to hold an inlet feed axial pipe through a connector at centre position in vessel to feed liquid; b. two side inlet ports at the top peripheral of the vessel for gas phase entry; c. an output of inlet feed pipe for recovering liquid either through single drip (single pipe distributor) or the said output transforming into multiple nozzles having nozzle exits downstream symmetrically spaced to distribute liquid in a uniform fashion across the cross section of monolith; and d. sufficient space of 0.1 to 0.6 times the bed diameter interposed in between the nozzle exits and the monolith surface wherein liquid and gas communicate before entering the monolith bed. 2. The device as claimed in claim 1 , wherein the ratio of the diameter of the pipe distributor with the diameter of bed (d dist /d bed ) is a variable within 0.04 to 0.4. 3. The device as claimed in claim 2 , wherein the value of d dist /d bed ≈0.17 offers an appropriate distribution without excessive pressure drop.
for the reactants · CPC title
vertical · CPC title
Catalysts coated on the surface of the monolith channels · CPC title
Packing elements in the form of grids or built-up elements for forming a unit or module inside the apparatus for mass or heat transfer · CPC title
Monolithic reactors · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.