Hydrocarbon phase change heat storage material and preparation method thereof with natural acid as raw material
A technology of phase change heat storage and hydrocarbons, applied in heat exchange materials, chemical instruments and methods, and producing hydrocarbons from oxygen-containing organic compounds, etc., can solve the problem of high equipment and material requirements, impossibility of practical application, and dangerous operation It has the advantages of easy recycling, high latent heat of product phase change, and flexible process operation.
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Embodiment 1
[0023] (1) Catalyst preparation
[0024] 6M HNO in an 80 °C oil bath 3 Multi-walled carbon nanotubes (commercially available, purity>95%, diameter 40-60nm, length 5-15μm, provided by Shenzhen Nanoport Co., Ltd.) were oxidized for 2h; then filtered, washed until neutral, and dried at 120°C ; Take the above-mentioned oxidized carbon nanotubes, add 70mL water, and ultrasonically disperse; add H 2 PdC1 4 solution, stirred evenly, added formaldehyde solution, adjusted the pH value to 9 with 1M NaOH solution, stirred for 25min, filtered, washed with a large amount of water, and dried to obtain Pd / MwCNTs catalyst (Pd / MwCNTs).
[0025] Two catalysts were prepared according to the above method: catalyst 1 (4% palladium mass content) and catalyst 2 (7% palladium mass content).
[0026] (2) Hydrodeoxygenation of myristic acid
[0027] Add 2.0 parts (parts by volume, the same below) of myristic acid, 0.5 parts of Pd / MwCNTs catalyst 2 and 18 parts of n-hexane into a 100mL reactor, an...
Embodiment 2
[0039] (1) Catalyst preparation (same as Example 1)
[0040] (2) Hydrogenation of myristic acid.
[0041] Add 2.5 parts (parts by volume, the same below) of myristic acid, 0.3 parts of Pd / MwCNTs catalyst 1 and 20 parts of n-hexane into a 100mL reactor, fill with hydrogen, the initial hydrogen pressure is 2.5MPa, start stirring and heating, and react at 280 °C After 6 hours, the reaction was stopped. After cooling to room temperature, the catalyst was separated by filtration. Quantitative detection is carried out to product with gas chromatography, as can be known that the conversion rate of raw material myristic acid is 82%, the total yield of product tetradecane is 76% (molar yield, the percentage of product n-tetradecane accounts for raw material myristic acid, the same below).
[0042] (3) Hydrodeoxygenation of palmitic acid.
[0043] Add 2.5 parts (parts by volume, the same below) of n-hexadecanoic acid, 0.3 parts of Pd / MwCNTs catalyst 1 and 20 parts of n-octane into a ...
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