Stamicarbon CO2-Stripping Urea Process of Duplex Stainless Steels
(Ref. 2) The production of urea is based on the following reaction mechanism:
2 NH3 + CO2 <====> NH2COONH4
NH2COONH4 <===> CO(NH2)2 + H2O
The process flow diagram of the Stamicarbon stripping process is shown in figure 1. The synthesis section consists of a urea reactor (c), a stripper for unconverted reactants (d), a high-pressure carbamate condenser (e) and a high-pressure off-gas scrubber (f). In the carbamate condenser (e) CO2 and NH3 are converted into ammonium carbamate. In the reactor the ammonium carbamate is partly converted into urea and water.
The urea synthesis process takes place at a pressure of 140 bar and a temperature of 185°C. The bulk of the unconverted carbamate decomposes in the stripper, where ammonia and carbon dioxide are stripped off. This stripping is effected by counter current contact between the urea solution and oxygen-containing carbon dioxide at synthesis pressure. The oxygen is needed to maintain a passive (corrosion resistant) layer on the stainless steels in the synthesis section. On leaving the stripper, gaseous ammonia and carbon dioxide are condensed in the high-pressure carbamate condenser (e) at synthesis pressure. Before being purged from the synthesis section, the inert gases, mainly oxygen and nitrogen, are washed in the high-pressure scrubber (f) with carbamate solution from the low-pressure recirculation section.
The urea synthesis solution is highly corrosive, the most aggressive component being ammonium carbamate. onsequently, materials of construction to be used here must meet high standards in terms of composition and quality. Awareness of the important factors in materials selection, equipment design, manufacture and inspection, technological design and proper plant operations, together with periodic corrosion inspections, are the key factors for safe operation for many years.
Stamicarbon:We are the world’s leading urea licensor.
http://www.stamicarbon.com/Urea-2000Plus-TM-Pool-Reactor-concept.html
UAN – Stamicarbon
It’s possible to produce Urea Ammonium Nitrate (UAN) solutions with relative ease thanks to Stamicarbon’s partial-recycle CO2-stripping process.
http://www.stamicarbon.com/UAN.html
(WO/1999/029663) PROCESS FOR THE PREPARATION OF UREA
Of the urea processes mentioned above the urea stripping processes of Stamicarbon, Toyo-ACES and IDR have a urea stripping plant according to the Stamicarbon CO2-stripping
http://www.wipo.int/pctdb/en/wo.jsp?IA=NL1998000677&DISPLAY=DESC
Uhde GmbH – Technology Profile: Urea
We have access to the leading urea technologies, such as: CO2 stripping processes, Stamicarbon, licensing subsidiary of DSM, The Netherlands
http://www.uhde.eu/competence/technologies/ammonia/techprofile.en.epl?profile=6&pagetype=0
Fertiliser Society – Proceedings Number 495
Keywords: Urea production, Pool condenser, CO2 stripping, Revamp, sizes needed for a 3250 mtpd pool condenser-type CO2 stripping urea plant. The plant will be equipped with
http://www.fertiliser-society.org/Proceedings/UK/Prc495.HTM
Urea
The technologies of STAMICARBON apply in the most modern plants built around the world The process is converted into the CO2 Stripping Process with a new Synthesis section
http://www.ceamag.com/index.php?option=com_content&view=article&id=9&Itemid=18?=en
Urea :: Phase_79 :: Process Economics Program :: SRI Consulting
The fast growth in the use of urea as a fertilizer, and to a lesser extent as an Stamicarbon–CO2 Stripping Process. Snamprogetti–NH3 Self-Stripping
http://www.sriconsulting.com/PEP/Public/Reports/Phase_79/RP056A/
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tags: chemical process industry, duplex, duplex stainless steel, HTM, materials, pressure, process, selective attack, stress corrosion cracking, water