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.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Example Embodiment
[0022] Example 1
[0023] (1) Catalyst preparation
[0024] Use 6M HNO in 80 ℃ oil bath 3 Multi-walled carbon nanotubes (commercially available products, purity> 95%, diameter 40~60nm, length 5~15μm, provided by Shenzhen Nanoport Co., Ltd.) oxidize for 2h; then filter, wash until neutral, and dry at 120 ℃; take the oxidized carbon nanotube and add 70mL Water, ultrasonic dispersion; 2%~10% palladium as the active component by mass percentage, add H 2 PdC1 4 After stirring the solution, add the formaldehyde solution, adjust the pH value to 9 with 1M NaOH solution, stir for 25min, filter, wash with plenty of water, and dry to obtain Pd / multi-walled carbon nanotube catalyst (Pd / MwCNTs).
[0025] Two catalysts were prepared according to the above method: Catalyst 1 (Palladium content of 4%) and Catalyst 2 (Palladium content of 7%).
[0026] (2) Myristic acid hydrodeoxygenation
[0027] Add 2.0 parts (parts by volume, the same below) myristic acid, 0.5 parts of Pd / MwCNTs catalyst 2 and 1...
Example Embodiment
[0038] Example 2
[0039] (1) Preparation of catalyst (same as Example 1)
[0040] (2) Hydrogenation of myristic acid.
[0041] Add 2.5 parts (parts by volume, the same below) myristic acid, 0.3 parts of Pd / MwCNTs catalyst 1 and 20 parts of n-hexane into a 100mL reactor, fill it with hydrogen, and start stirring and heating at 280 ℃. The reaction was stopped after 6 hours. After cooling to room temperature, the catalyst was separated by filtration. Quantitative detection of the product by gas chromatography showed that the conversion rate of raw myristic acid was 82%, and the total yield of product tetradecane was 76% (molar yield, the product n-tetradecane accounts for the percentage of raw myristic acid, Same below).
[0042] (3) Palmitic acid hydrodeoxygenation.
[0043] Add 2.5 parts (parts by volume, the same below) n-hexadecanoic acid, 0.3 parts of Pd / MwCNTs catalyst 1 and 20 parts of n-octane into a 100mL reactor, fill it with hydrogen, and start the stirring and heating at an...
PUM
Property | Measurement | Unit |
---|---|---|
Phase transition temperature | aaaaa | aaaaa |
Heat of phase change | aaaaa | aaaaa |
Phase transition temperature | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap