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Snamprogetti urea process

The Snamprogetti (SNAM) process, the synthesis section of the Stamicarbon (STAC) process and the synthesis section of the Toyo-ACES (Advanced Process for Cost and Eneigy Saving) process are described in References 108 and 110. An updated version of the STAC process, Urea 2000plus, is offered by DSM (Stamicarbon s parent company).108110... [Pg.1049]

Snamprogetti granulation technology has been applied in a 1,650-tpd plant operating since 1990. The plant is completely free from pollution problems. All vents are efficiently treated so that they are discharged to atmosphere practically free of ammonia and urea. Process wastewater is hydrolized within the plant to achieve boiler feedwater specification and recover ammonia and carbon dioxide. [Pg.116]

Integrating the ammonia and urea process into a single train was proposed by Snamprogetti to reduce investment and operating costs [1099] (see also Chapter 7). [Pg.190]

Saipem S.p.A. Urea (Snamprogetti Urea Technology) Ammonia and carbon dioxide Process is pollution-free, and energy-efficient 116 2009... [Pg.303]

Figure 9.5. Snamprogetti Thermal Stripping Urea Process. [Pg.265]

At this time over 95% of all new urea plants are Hcensed by Snamprogetti, Stamicarbon, or Toyo Engineering. SNAM utilizes thermal stripping while STAC (Stamicarbon) and Toyo use CO2 stripping. Only these three processes are, therefore, covered in detail. Process flow sheets are included for others at the end of this section. [Pg.300]

The second reaction represents the decomposition of the carbamate. The reaction conditions are 200°C and 30 atmospheres. Decomposition in presence of excess ammonia limits corrosion problems and inhibits the decomposition of the carbamate to ammonia and carbon dioxide. The urea solution leaving the carbamate decomposer is expanded by heating at low pressures and ammonia recycled. The resultant solution is further concentrated to a melt, which is then prilled by passing it through special sprays in an air stream. Figure 5-3 shows the Snamprogetti process for urea production. ... [Pg.146]

Figure 5-3. The Snamprogetti process for producing urea (1) reactor, (2,3,4) carbonate decomposers, (5,6) crystallizing and prilling. Figure 5-3. The Snamprogetti process for producing urea (1) reactor, (2,3,4) carbonate decomposers, (5,6) crystallizing and prilling.
All processes still require use of oxygen for pasava-tion in the synthesis loop. Metallurgical advances have reduced the amount required. Snamprogetti now utilizes a bimetallic zirconium/25-22-2 (Ni, Cr, Mo) tube in its stripper. The corrosion rate for zirconium in urea service is nil. Toyo utilizes a duplex alloy (ferrite-austenite), which requires less ojqjgen. Stamicarbon working with the Swedish steel producer Sandvik, has patented a proprietary material called Saferex, which requires very little oxygen future plants wnll use this new material,... [Pg.264]

The Snamprogetti process is based on using ammonia to strip CO2 and NH3 out of the urea reactor effluent. One of the impurities that affects the performance of urea as a fertilizer is biuret. To avoid a yield loss and minimize product contamination, it is important to minimize biuret formation. The con-... [Pg.1103]

The first reaction is exothermic and goes almost to completion, while the second, endothermic, reaction converts less than 70% of feedstocks to urea. Consequently, the once-through process of urea synthesis had to be combined with production of other nitrogen compounds. Modern syntheses use a more expensive total recycle process in which all the unreacted CO2 and NH3 is separated from the effluent solution and returned to the reactor. Conversion rates range between 65 and 67% for each pass, and the overall reaction yield is on the order of 99%. Three commercial processes—Dutch Stamicarbon, Italian Snamprogetti, and Japanese Toyo—dominate today s world market for large (up to 2,000 t/day) urea plants using the total recycle process. ... [Pg.136]


See other pages where Snamprogetti urea process is mentioned: [Pg.269]    [Pg.101]    [Pg.116]    [Pg.207]    [Pg.261]    [Pg.68]    [Pg.72]    [Pg.302]    [Pg.302]   
See also in sourсe #XX -- [ Pg.253 ]




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