Urea synthesis process and plant
US-9512069-B2 · Dec 6, 2016 · US
US2018071708A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018071708-A1 |
| Application number | US-201615563460-A |
| Country | US |
| Kind code | A1 |
| Filing date | Mar 11, 2016 |
| Priority date | Mar 30, 2015 |
| Publication date | Mar 15, 2018 |
| Grant date | — |
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.
Process and respective reactor for urea or melamine synthesis, comprising sonication treatment of at least part of a reaction liquid mass or two-phase mixture contained inside said reactor.
Opening claim text (preview).
1 . A process for the synthesis of urea from ammonia and carbon dioxide, or for the synthesis of melamine from urea, inside a chemical reactor, said process comprises comprising a sonication treatment of at least part of a reaction liquid mass or two-phase mixture contained inside said chemical reactor. 2 . The process according to claim 1 , wherein said sound waves have a frequency in the range 1 kHz to 1 MHz. 3 . The process according to claim 2 , wherein said sound waves have a frequency equal to or greater than 20 kHz. 4 . The process according to claim 1 , said sound waves being generated by one or more electrical or mechanical sources. 5 . The process according to claim 1 , wherein the sonication treatment is performed in a sonication zone inside said chemical reactor. 6 . The process according to claim 5 , comprising the circulation of a liquid phase or liquid/vapour phase through at least one reaction zone and a recirculation zone, which are arranged coaxial and concentric inside said reactor, wherein the sonication treatment is performed in at least one of said two reaction and recirculation zones. 7 . The process according to claim 6 , for melamine synthesis, wherein the reaction zone is a primary reaction zone fed with urea melt. 8 . A reactor for urea synthesis or melamine synthesis according to the process of claim 1 , wherein it comprises at least one sonication sound waves source. 9 . The reactor according to claim 8 , wherein said sound waves source is located inside a sonication chamber. 10 . The reactor according to claim 9 , said sonication chamber being delimited, inside the reactor, by a cylindrical wall or by a vertical-axis tube. 11 . The reactor according to claim 10 , said chamber being coaxial with the reactor. 12 . The reactor according to claim 8 , wherein said source is designed to produce sound waves with a frequency in the range of 1 kHz to 1 MHz. 13 . The reactor according to claim 8 , comprising a reaction chamber and a recirculation chamber which are concentric and coaxial, wherein said at least one sound waves source is located inside one of said chambers. 14 . The reactor according to claim 13 , the reactor being intended for melamine synthesis, wherein the reaction chamber is delimited by a central tube and is directly in communication with an inlet for urea melt, and the recirculation chamber is an annular chamber around said reaction chamber and comprises heating elements. 15 . The reactor according to claim 8 , wherein it comprises a mechanical stirrer arranged so as to direct a liquid phase, contained inside the reactor, towards said sonication source. 16 . Use of a sonication treatment inside a reactor for urea synthesis or inside a reactor for melamine synthesis, wherein said treatment provides transmission of sound waves to at least part of a liquid mass or two-phase mixture contained inside said reactor. 17 . The process according to claim 3 , wherein said sound waves have a frequency of 20 to 40 kHz. 18 . The reactor according to claim 12 , wherein said source is designed to produce sound waves with an ultrasound frequency of at least 20 kHz.
combined with the synthesis of melamine · CPC title
from carbon dioxide and ammonia · CPC title
internally, i.e. the mixture circulating inside the vessel such that the upward stream is separated physically from the downward stream(s) · CPC title
Recycling of unreacted starting or intermediate materials · CPC title
employing sonic or ultrasonic vibrations · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.