Catalyst Technology Update
Raise efficiency of ultra-low SHR production of styrene monomer with a novel catalyst formulation
The production of styrene monomer from ethylbenzene requires superheated steam as an energy source, as well as dehydrogenation catalysts to facilitate the reaction. As steam generation poses the highest influence on production costs, significant effort has been devoted to optimizing process design.
The optimal catalyst makeup in an FCC unit
Fluid catalytic cracking (FCC) is one of the key process technologies in the refining industry. The FCC unit increases refining margins by upgrading low-value streams, such as vacuum gasoils or atmospheric and vacuum residues, to more valuable products, such as propylene, butylenes and high-octane naphtha.
Improve FCC yields from contaminated feeds using boron-based nickel passivation
The drive to improve refinery margins leads to the processing of heavier, more contaminated crude and, consequently, an increasing amount of contaminants in fluid catalytic cracking (FCC) feedstock. Of these, nickel (Ni) deposits on the FCC catalyst and catalyzes dehydrogenation reactions, producing unwanted hydrogen (H2) and contaminant coke. These effects diminish the profitability and operability of the FCCU, creating strong demand for Ni passivation technology. Ni passivation is especially beneficial when the FCCU operates at the wet gas compressor (WGC), regenerator temperature limit, or air limit.
- WinGD delivers exceptional results in full-load X-DF-A ammonia engine test 3/14
- COAMO Agroindustrial Cooperativa selects ICM for design and engineering of new corn biorefinery in Brazil 3/14
- South Dakota (U.S.) bans use of eminent domain for CO2 pipelines 3/14
- ABB and Charbone Hydrogen sign agreement to advance North American green H2 production facilities 3/14
- U.S., Vietnam firms sign deals on energy and minerals 3/14
- Russian diesel continues to flow to Syria on U.S.-sanctioned tankers 3/14
