Method for revamping a self-stripping urea plant

US9770699B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9770699-B2
Application numberUS-201414778460-A
CountryUS
Kind codeB2
Filing dateMar 5, 2014
Priority dateMar 27, 2013
Publication dateSep 26, 2017
Grant dateSep 26, 2017

How to read this patent

A practical reading order for non-experts. Skip the full description unless you need deep technical detail.

  1. Title

    What the patent document calls the invention.

  2. Abstract

    A short plain-language summary of the technical disclosure.

  3. Assignees and inventors

    Who owns or filed the patent and who is credited as inventor.

  4. Key dates

    Filing, priority, publication, and grant dates set the timeline.

  5. First independent claim

    The legal scope of protection — read this for what is actually claimed.

  6. CPC / IPC classifications

    Technology tags used to group this patent with similar filings.

  7. Citations and related patents

    Prior art links and similar publications in this corpus.

Abstract

Official abstract text for this publication.

A method for revamping a self-stripping urea plant comprising the installation of a new CO2-stripping synthesis section ( 6 ), wherein at least part of the aqueous urea solution ( 10 ) leaving said new section ( 6 ) is directed to the existing low pressure recovery section ( 4 ) of the self-stripping plant, by-passing the existing self-stripping high-pressure section ( 2 ) and medium pressure treatment section ( 3 ).

First claim

Opening claim text (preview).

The invention claimed is: 1. A method for revamping a self-stripping urea plant, said plant comprising: a high pressure urea synthesis section including at least a reactor, a thermal stripper or an ammonia stripper and a condenser; a medium pressure treatment section; a low pressure recovery section, the method comprising the following steps: installation of a CO 2 -stripping synthesis section, where ammonia and carbon dioxide are converted to an aqueous urea solution according to CO 2 -stripping process, wherein said new CO 2 -stripping section comprises at least: a synthesis reactor, a stripper, and a condenser, which are part of a high-pressure loop, and wherein at least a portion of the aqueous urea solution leaving said new CO 2 -stripping section is directed to said existing low pressure recovery section, by-passing the existing self-stripping high-pressure section and medium pressure treatment section. 2. The method according to claim 1 , wherein said new CO 2 -stripping section further comprises a scrubber. 3. The method according to claim 1 , said high-pressure loop operating substantially at the same pressure as the existing self-stripping synthesis section. 4. The method according to claim 1 , wherein a first portion of the aqueous urea solution leaving said new CO 2 -stripping section is directed to said low pressure recovery section, while a second remaining portion of said solution is directed to said medium pressure treatment section. 5. The method according to claim 4 , said first portion of urea solution being greater than said second portion. 6. The method according to claim 1 , wherein a portion of liquid ammonia and/or a portion of carbamate solution, which are recovered from the existing medium-pressure section, is fed to the new CO 2 -stripping section. 7. The method according to claim 6 , wherein said portion of liquid ammonia and/or portion of carbamate is fed to said CO 2 -stripping section via existing pumps of the self-stripping plants. 8. The method according to claim 1 , wherein: the existing self-stripping urea plant comprises more than one urea production lines in parallel, the aqueous urea solution leaving said new CO 2 -stripping section and by-passing the medium-pressure sections is split into a plurality of streams, and each of said streams is directed to a respective low-pressure recovery section of the existing urea production lines. 9. The method according to claim 8 , wherein some of the urea solution from the new CO 2 stripping section is also directed to one or more of the medium-pressure sections. 10. The method according to claim 8 , wherein respective portions of liquid ammonia and/or carbamate solution, recovered from the medium-pressure sections of the urea production lines, are directed to the new CO 2 stripping section.

Assignees

Inventors

Classifications

  • Revamping, retrofitting or modernisation of existing plants · CPC title

  • C07C273/04Primary

    from carbon dioxide and ammonia · CPC title

  • B01J10/00Primary

    Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor (B01J19/08 takes precedence; separation, e.g. distillation, also combined with chemical reactions B01D, {e.g. B01D3/009}) · CPC title

Patent family

Related publications grouped by family.

External sources

Frequently asked questions

Answers are generated from the same data shown on this page.

What does patent US9770699B2 cover?
A method for revamping a self-stripping urea plant comprising the installation of a new CO2-stripping synthesis section ( 6 ), wherein at least part of the aqueous urea solution ( 10 ) leaving said new section ( 6 ) is directed to the existing low pressure recovery section ( 4 ) of the self-stripping plant, by-passing the existing self-stripping high-pressure section ( 2 ) and medium pressure t…
Who is the assignee on this patent?
Casale Sa
What technology area does this patent fall under?
Primary CPC classification C07C273/04. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Sep 26 2017 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).