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US5096599A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for purifying the effluent from urea production plants

Assignee: SnamProgetti SpA
•
Filing: 1990-08-17
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Granted: 1992-03-17
•
Expires: 2010-08-17
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Abstract

Abstract A process for purifying the effluent originating from urea production plants, consisting of three successive treatment stages, namely stripping of the volatile components, thermal hydrolyis of the urea and biuret in a plurality of zones traversed with piston flow, and final stripping of the volatile components produced by the hydrolysis.

Inventors

  • 👤 Franco Granelli

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 00:26
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/58; C02F1/586; C02F1/02; C02F1/025; Y; Y10; Y10S; Y10S210/00; Y10S210/902; Y10S210/903

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 268 words
A process for the purification of the effluent originating from urea production plants and containing ammonia, carbon dioxide and urea as pollutants, said purification being conducted by hydrolysis and stripping to obtain treated effluent containing from 10 to 0.4 ppm of ammonia and urea, wherein said purification is conducted in three successive stages, comprising: a first stage in which said effluent to be treated is stripped with steam to release volatile pollutants, which are then recycled to the urea production plant in a liquid or vapor phase; a second stage in which the effluent obtained from the preceding stage is hydrolyzed to decompose non-volatile components urea and biuret, said decomposition being conducted at pressure of 20-40 bars gauge, at a temperature of 200°-240° C. and with a residence time of 20-40 minutes, in a horizontal cylindrical reactor the interior of which comprises a succession of vertical baffles which separate the reactor into a plurality of hydrolysis zones defining a tortuous path with a piston flow of said effluent, and from each of which the vapor phase produced is separated, said baffles consisting alternately of circular plates cut horizontally both at their top and at their bottom, so that their total height is 70-90% of the internal diameter of the reactor, said vapor phase being combined with the vapor phase obtained from the stripping stage to be then recycled to the urea production plant; a third stage in which the effluent which has undergone hydrolysis is further stripped with steam, the stripping stages being conducted at a pressure of 1.5-4 bars gauge and at a temperature of 128°-150° C.
Claim 2
Dependent Claim 268 words
A process for the purification of the effluent originating from urea production plants and containing ammonia, carbon dioxide and urea as pollutants, said purification being conducted by hydrolysis and stripping to obtain treated effluent containing from 10 to 0.4 ppm of ammonia and urea, wherein said purification is conducted in three successive stages, comprising: a first stage in which said effluent to be treated is stripped with steam to release volatile pollutants, which are then recycled to the urea production plant in a liquid or vapor phase; a second stage in which the effluent obtained from the preceding stage is hydrolyzed to decompose non-volatile components urea and biuret, said decomposition being conducted at pressure of 20-40 bars gauge, at a temperature of 200°-240° C. and with a residence time of 20-40 minutes, in a horizontal cylindrical reactor the interior of which comprises a succession of vertical baffles which separate the reactor into a plurality of hydrolysis zones defining a tortuous path with a piston flow of said effluent, and from each of which the vapor phase produced is separated, said baffles consisting alternately of circular plates cut horizontally both at their top and at their bottom, so that their total height is 70-90% of the internal diameter of the reactor, said vapor phase being combined with the vapor phase obtained from the stripping stage to be then recycled to the urea production plant; a third stage in which the effluent which has undergone hydrolysis is further stripped with steam, the stripping stages being conducted at a pressure of 1.5-4 bars gauge and at a temperature of 128°-150° C.
Claim 3
Dependent Claim 50 words
A process for treating the effluent originating from urea production plants as claimed in claim 1 wherein the first and third stage which strip the effluent before and after the hydrolysis are implemented in two sections of one and the same column which are connected together by a stack plate.
Claim 4
Dependent Claim 32 words
A process for treating effluent originating from urea production plants as defined in claim 2 wherein vapor produced by the hydrolysis stage is fed to the column of the first stripping stage.
Claim 5
Dependent Claim 60 words
A process for treating the effluent originating from urea production plants defined in claim 2, wherein the hydrolysis operating conditions for obtaining effluent with an ammonia and urea content of less than 1 ppm are the following: ______________________________________ pressure 33-37 bars gauge temperature 230-236° C. No. of baffles 8-12 baffle height 75-85% of the diameter residence time 30-40 minutes. ______________________________________
Claim 6
Dependent Claim 33 words
A process for treating the effluent originating from urea production plants as defined in claim 1 wherein vapor produced by the hydrolysis stage is fed to the column of the first stripping stage.
Claim 7
Dependent Claim 60 words
A process for treating the effluent originating from urea production plants defined in claim 5, wherein the hydrolysis operating conditions for obtaining effluent with an ammonia and urea content of less than 1 ppm are the following: ______________________________________ pressure 33-37 bars gauge temperature 230-236° C. No. of baffles 8-12 baffle height 75-85% of the diameter residence time 30-40 minutes ______________________________________
Claim 8
Dependent Claim 60 words
A process for treating the effluent originating from urea production plants defined in claim 1 wherein the hydrolysis operating conditions for obtaining effluent with an ammonia and urea content of less than 1 ppm are the following: ______________________________________ pressure 33-37 bars gauge temperature 230-236° C. No. of baffles 8-12 baffle height 75-85% of the diameter residence time 30-40 minutes. ______________________________________

References Cited (Backward Citations)

US3922222A Cited
US4098579A Cited
US4087513A Cited
US4220635A Cited
EP0019326A1 Cited
US4354040A Cited
US4354040B1 Cited
EP0053410A1 Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1995-03-17 1995-09-16 1996-03-17 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1999-03-17 1999-09-16 2000-03-17 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2003-03-17 2003-09-16 2004-03-17 $7700.00 Window Closed / Lapsed

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