Methods for removing metallic and non-metallic impurities from hydrocarbon oils
a technology of hydrocarbon oil and impurities, which is applied in the field of reducing, can solve the problems of promoting serious corrosion of turbine blades, detrimental contaminants, and corrosion problems of turbine blades and other components, and achieves the effects of reducing the number of turbine blades
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example 1
Adsorption of Vanadium Porphyrin Compounds
[0043]Britesorb® C930 silica adsorbent was used in this example. The material had a surface area (BET) of 452 m2 / g; and a pore volume (Vp) of 1.27 cc / g. Approximately 0.11 g of the C930 material was weighed into a vial. 5.06 g of a petroleum ether solution of vanadium etioporpyrin (15 ppm V in the solvent) was added to the vial. The mixture was stirred for 2 minutes, at room temperature. (The approximate composition of this grade of petroleum ether, as determined by gas chromatograph (GC) analysis, was as follows: 50 wt % pentane; 5 wt % 2,2-dimethylbutane; 5 wt % 2,3-dimethylbutane; 25 wt % 2-methylpentane; and 15 wt % 3-methylpentane). After stirring, the mixture was centrifuged, and the clear liquid which resulted was decanted. All of the color which was characteristic of the vanadium compound had been completely absorbed by the silica adsorbent. The petroleum ether solution was thus free of vanadium.
example 2
Adsorption of Vanadium Porphyrin Compounds
[0044]Approximately 0.11 g Britesorb® R100 silica adsorbent was used in this example. The material had a surface area (BET) of 277 m2 / g; and a pore volume (Vp) of 0.55 cc / g. The R100 material was weighed into a vial, and 5.07 g of a petroleum ether solution of vanadium etioporpyrin (15 ppm V) was added. The mixture was stirred for 2 minutes at room temperature. It was centrifuged, and the slightly-pinkish liquid was decanted. In this instance, the R100 did not completely absorb the color which is characteristic of the vanadium compound. This observation provides an indication that the R100 grade of silica adsorbent may not have the optimal pore structure for some applications, and more of the adsorber may be required to treat a given volume of oil. (However, use of the R100 would be suitable in other situations).
example 3
Use of a Silica Xerogel for the Adsorption of Impurities in Crude Oil
[0045]The experiment outlined in Example 2 was repeated, using a different silica adsorbent material. In this instance, a silica xerogel was employed, designated as Britesorb® D350EL. The material had a surface area (BET) of 680 m2 / g; and a pore volume (Vp) of 1.4 cc / g. 3.5 g of the gel was weighed into the Waring blender. 10 g of crude oil was added, along with 40 g of petroleum ether. The resulting slurry was mixed for 2 minutes, and poured into centrifuge tubes. Each tube was centrifuged for 10 minutes, at 2100 rpm. The resulting liquid fractions were decanted into vials, and the vanadium and nickel contents were measured by the ICP-MS (Inductively Coupled Plasma Mass Spectrometry) technique. The results indicated that residual vanadium and nickel levels were below detection limits.
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