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Stami Specialties Controlled Release Fertilizer Design leaflet.

One of the main papers presented during the 11th Stamicarbon symposium of 2008 was titled “Stamicarbon‟s new urea plant concept“ and presented the new Low Elevation Technology Avancore®. Main characte

Stamicarbon introduced the granulation in 2002. The process, based on the film spraying nozzle, was well accepted in the market leading to a number of references. The main feature of the plant is the

Large urea plants require large high-pressure equipment that is difficult and costly to manufacture and transport. To reduce urea fabrication costs, Stamicarbon has developed a Mega Plant concept for

Stamicarbon is a reputed licensor for the urea process. Stamicarbon licenses the whole range of finishing technologies: prilling, granulation and pelletizing. The fluid bed granulation technique resul

In this presentation, we show the recent STAC developments in Urea FBG, our pioneership for the future market. - Product quality and low operating costs (energy&UF85) are critical factors in a pro

Slide presentation on Stamicarbon's UAN technology. Years of experience with AN/UANplants: - More than 150 years of operation in AN and UAN plants. - 15 years at our own DSM plant in Geleen, the Nethe

Review of literature date shows that 1st generation biofuels show a clear energy balance deficiency. 2nd generation biofuels have a clear positive energy balance. This is even true if the urea require

Slide presentation Finishing Technologies for Urea - Prilling - Pelletizing/pastillation - Granulation

The Medium-Pressure Add-on Debottlenecking Technology developed by Stamicarbon paves the way for single line large-scale urea plants up to 5000 metric tons per day. The urea plant at SKW Piesteritz is

  Slide presentation Stamicarbon’s view on large scale urea plants: - MEGA technology: - Feasible route to design urea plants up to 6000 MTPD. - Based on a combination of proven design and siz

The Stamicarbon urea process, like other processes, unfortunately emits gaseous (ammonia) emissions due to the fact that the urea reaction is an equilibrium reaction. In principle, emission problems c

Sources of urea dust in the air exhaust of a granulator: •Fine dust coming from the crushing-process of coarse granules •Evaporation/sublimation from urea melt (Isocyanicequilibrium) CO(NH2)2-> H

• Why a new finishing technology? • Principle of dry finishing technology • The process • Alternative applications • Current Status