“…In general, solubility data in supercritical fluids can be used in diversified fields such as extraction, reaction, particle formation, and materials processing [6][7][8][9]. The methods used for measuring the solubility of organic solids in supercritical fluids may be classified into four different categories: (1) dynamic, (2) static, (3) chromatographic, and (4) spectroscopic methods [10].…”
“…In general, solubility data in supercritical fluids can be used in diversified fields such as extraction, reaction, particle formation, and materials processing [6][7][8][9]. The methods used for measuring the solubility of organic solids in supercritical fluids may be classified into four different categories: (1) dynamic, (2) static, (3) chromatographic, and (4) spectroscopic methods [10].…”
“…• The use of organo-transition metal complexes as homogeneous catalysts for reactions in SCF and biphasic systems [45][46][47][48] • Extraction of heavy metals from various matrices with SCF [49][50][51] • Synthesis of inorganic powders with controlled size distribution by decomposition of organometallic complexes in SCF [52][53][54][55][56] • Impregnation of polymers with different metal complexes and the subsequent transformation of the metal precursor within such matrices [57][58][59][60][61][62] • Incorporation of metallic nanoparticles in porous inorganic and carbonaceous substrates by deposition of SCF [63][64][65] This chapter focuses on the last point, in order to contribute to developing the incorporation of metallic active phases in porous substrates by dissolving organometallic complexes in sc-CO 2 .…”
Section: Synthesis Of Materials In Supercritical Fluidsmentioning
Metal and metal oxide nanoparticles have attracted increased attention due to their unusual physical and chemical properties. The nature, dispersion, and size of the nanoparticles are key factors in determining the activity and selectivity of the supported catalysts. Supercritical fluid deposition (SCFD) is a promising method to deposit metallic nanoparticles and films on inorganic porous supports. CO 2 is the most commonly used supercritical fluid (sc-CO 2) for material synthesis because it is nontoxic, nonreactive, nonflammable, and inexpensive. This work presents the synthesis of cobalt, nickel, and ruthenium nanoparticles on MCM-41, Al-MCM-41, MCM-48, and activated carbon supports in sc-CO 2. Batch and continuous deposition are studied, with two high-pressure reactor configurations: column or alternative (sandwich). To avoid the length of the bed being too long, the reagents were separated into smaller amounts and placed alternately, keeping the total mass of the precursor and support constant. The prepared samples were characterized by scanning electron (SEM/EDX) and transmission electron microscopy (TEM).
“…The solver needs to determine j SBR H 2 and j SBR CO to maximize selectivity towards the linear aldehyde while simultaneously minimizing the deviation from the desired terminal liquid hold-up of the flash buffer tank and ensuring Eq. (16)(17)(18)(19). As a consequence, convergence of the RSBR-process to an optimal cyclic steady-state not only requires accurate knowledge of the underlying reaction network but also precise control of the reaction conditions.…”
Section: Comparison Of the Steady-state And Dynamic Modelmentioning
confidence: 99%
“…The chosen solvent system must provide adequate solubility of the components, good separability, and easy recovery of the expensive catalyst complex to ensure an economically profitable process. Walter [11] provides a good overview of different solvents including thermomorphic multicomponent solvent systems [4], micellar solvent (MLS) systems [12,13], ionic liquids [14], gas-expanded liquids [15] and supercritical carbon dioxide [16].…”
Section: Introductionmentioning
confidence: 99%
“…As initial conditions for the first process cycle, are chosen analogous to the case studies of the steady-state model. For subsequent process cycles, the initial conditions are dependent on the Idle stage and the amount of fresh substrate which is calculated in the previous process cycle in accordance with Eq (16)(17)(18)(19)…”
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