METHOD FOR PRODUCING SOLID UREA BY GRANULATION
20220072492 · 2022-03-10
Assignee
Inventors
Cpc classification
C07C273/14
CHEMISTRY; METALLURGY
International classification
B01J2/16
PERFORMING OPERATIONS; TRANSPORTING
C05C9/00
CHEMISTRY; METALLURGY
C07C273/14
CHEMISTRY; METALLURGY
Abstract
Method for producing solid urea by granulation, wherein the granulation is fed with liquid urea having a purity greater than 98% by weight and not containing formaldehyde.
Claims
1) Method for producing solid urea by granulation, characterized in that the granulation is fed with urea melt having a concentration of more than 98% by weight and in that no formaldehyde is added to said urea melt.
2) Method according to claim 1, characterized in that said urea melt has a concentration of at least 99.5% by weight and preferably at least 99.7% by weight.
3) Plant for producing solid urea in granule form, operating using a method according to claim 1 or 2.
4) Solid urea in granule form, free from formaldehyde, obtained with a method according to claim 1 or 2.
5) Method for revamping a plant for producing solid urea, wherein the plant comprised a prilling section for production of solid urea by means of prilling of a high-concentration urea melt, the method comprising the steps of: installing a granulation section and feeding at least part of said urea melt originally intended for the prilling section, and without the addition of formaldehyde, to said new granulation section.
6) Method according to claim 5, wherein a portion of said urea melt is used in the prilling section to produce seeds for said new granulation section.
Description
DESCRIPTION OF THE FIGURES
[0025]
[0026]
[0027]
DESCRIPTION OF PREFERRED EMBODIMENTS
[0028]
[0029] Said solution passes through evaporation section EV inside which the water is removed, obtaining a urea melt UM containing more than 98%, for example 99.7%, by weight of urea. Said urea melt UM, without the addition of formaldehyde, is fed to a granulation section GS, obtaining granules of urea U.
[0030]
[0031] In some embodiments, the UM stream is directed entirely towards the new granulation section GS, i.e. the production of prills P is discontinued.
[0032]