A method for producing hydrocarbon phase-change heat storage material with natural acid
A phase change heat storage, natural acid technology, applied in heat exchange materials, chemical instruments and methods, chemical recovery and other directions, can solve problems such as high cost, high operational risk, and complex process conditions
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Embodiment 1
[0063] The preparation process of the hydrogenation catalyst used in the present invention is as follows:
[0064] 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 2.0h; then filtered, washed until neutral, and baked at 120°C dry; take the above 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).
[0065] Two catalysts were prepared according to the above method: catalyst 1 (4% palladium mass content) and catalyst 2 (7% palladium mass content).
Embodiment 2
[0067] This embodiment includes (A) hydrogenation, (B) sweating and (C) deployment three parts.
[0068] (A) Hydrogenation
[0069] This part includes hydrodeoxygenation of wax acid and hydrodeoxygenation of montanic acid.
[0070] (A1) Hydrodeoxygenation of cerotic acid
[0071] Add 1.5 parts of cerotic acid, 0.4 parts of Pd / MwCNTs catalyst 1 and 16 parts of n-hexane into the reaction kettle, and fill it with hydrogen (containing 10 μL / L of NH 3 ), the initial hydrogen pressure was 5.0MPa, stirring and heating were started, and the reaction was stopped after 7.0 hours at 240°C; the catalyst was separated by filtration.
[0072] The solvent n-hexane was distilled off at 80°C to obtain the hydrogenation product of cerotic acid.
[0073] Gas chromatography was used to quantitatively detect the hydrogenation products of cerotic acid. It can be seen that the conversion rate of cerotic acid was 80%, and the yield of the product n-hexacane was 97%.
[0074] (A2) Montan acid hydr...
Embodiment 3
[0115] This embodiment includes (A) hydrogenation, (B) sweating and (C) deployment three parts.
[0116] (A) Hydrogenation
[0117] With embodiment 2.
[0118] (B) sweating
[0119] This part includes (B1) sweating of cerotic acid hydrogenation products and (B2) sweating of montan acid hydrogenation products.
[0120] (B1) Hydrogenation product of cerotic acid sweats
[0121] This part includes: (1) preparation work, (2) crystallization, (3) sweating, (4) refining and other processes.
[0122] (1) Preparation
[0123] Prepare a number of stainless steel plates, each stainless steel plate has an external dimension of 0.98 m × 0.98 m × 0.02 m, and drill through holes of φ0.0015 m evenly distributed on the stainless steel plate (the hole is drilled at 0.01m from the edge, and the center of the hole Spacing 0.04m) (the pressure generated by each stainless steel plate is about 1.5kPa), spare.
[0124] Connect the sealing system of the sweating dish (same as Example 2) with the ...
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Abstract
Description
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