2 ethylhexanoic acid
2-ethylhexanoic acid is a carboxylic acid with a chemical formula of C8H16O2. It is a colorless, oily liquid with a characteristic odor. 2-ethylhexanoic acid is commonly used as an intermediate in the production of various chemical compounds and is a key ingredient in certain lubricants, plasticizers, and other industrial applications.
Lab products found in correlation
22 protocols using 2 ethylhexanoic acid
Synthesis of Colloidal Semiconductor Nanocrystals
Colloidal Synthesis of Inorganic Nanomaterials
Synthesis of Ag-SiO2 Nanoparticles
Flame Spray Pyrolysis Synthesis of Cu-Zn-Ce Oxide Catalysts
oxide catalysts were prepared by a single-step flame spray pyrolysis
(FSP) method using a Tethis NPS10 apparatus. The catalyst precursor
solution was prepared by dissolving appropriate amounts of Cu(NO3)2·3H2O (99%, Sigma-Aldrich), Zn(NO3)2·6H2O (99%, Sigma-Aldrich), and
Ce(NO3)3·6H2O (99%, Sigma-Aldrich)
in a 1:1 (vol %) solvent mixture of ethanol (HPLC, Sigma-Aldrich)
and 2-ethylhexanoic acid (99%, Sigma-Aldrich) at room temperature.
The total metal (Cu, Zn, and Ce) concentration was 0.15 M. The precursor
solution was then injected into the nozzle of the Tethis setup at
a flow rate of 5 mL/min. The flame was fed with a 1.5 L/min methane
flow and a 3.0 L/min oxygen flow with an additional 5.0 L/min oxygen
dispersion flow around it. The resulting catalyst powder was collected
from the quartz filter placed after the combustion zone. The as-prepared
Cu–Zn–Ce oxide catalysts are denoted as Cu(x)/CeO2, Cu(x)/ZnO, or Cu(x)/ZnO–CeO2(y) where x and y, respectively, stand for Cu loading (wt %)
and Zn atomic ratio in the supports (Zn/(Zn + Ce)). Additionally,
a commercial Cu–ZnO-based methanol synthesis catalyst (MSC)
was purchased from Alfa Aesar (no. 45776).
Synthesis of Bio-Based Thermoset Resins
Synthesis of Inorganic Nanoparticles and Dyes
Fecal Short-Chain Fatty Acid Analysis
Synthesis of Dye-Functionalized Nanoparticles
Characterization of PLA and PHB Polymers
Flame Spray Pyrolysis of Ferrite Nanoparticles
iron(III) nitrate nonahydrate (purity 98%; Sigma-Aldrich, Sweden)
and either zinc nitrate hexahydrate (purity 98%; Sigma-Aldrich) or
manganese(II) nitrate tetrahydrate (purity 97%; Sigma-Aldrich) in
a solvent mixture (1:1) of 2-ethylhexanoic acid (99%; Sigma-Aldrich)
and ethanol (>99.7%, HPLC grade; VWR, Belgium) to obtain a total
metal
concentration of 0.7 M. Reference pure iron oxide (γ-Fe2O3) was produced from a 0.7 M iron(III) nitrate
nonahydrate precursor solution.
The precursor solutions were
stirred for at least 1 h at room temperature. Subsequently, the precursor
was fed at 6 mL min–1 and dispersed using 3 L min–1 O2 (>99.5%, Linde AGA Gas AB, Sweden)
at a constant pressure (1.6 bar). The flame was ignited by a premixed
supporting flame of CH4 and O2 (>99.5%, Linde
AGA Gas AB) at flow rates of 1.5 and 3.2 L min–1, respectively. A 5 L min–1 O2 sheath
gas was fed through the outermost sinter metal plate of the FSP burner.
Gas flow rates were controlled with calibrated mass flow controllers
(Bronkhorst, the Netherlands). The particles were collected on a glass
fiber filter (Albert LabScience, Germany) with the aid of a Mink MM
1144 BV vacuum pump (Busch, Sweden).
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