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Method for preparation of n-docosane by natural acid-behenic acid

A technology of docosane and behenic acid, which is applied in the field of catalysis, can solve problems such as low yield, complex process conditions, high requirements for equipment and materials, and achieve the effects of lower reaction temperature, simple preparation process, and easy recycling

Active Publication Date: 2015-06-17
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the above methods can obtain the corresponding n-alkane monomers, there are certain problems in each method: as the first method, the process conditions are more complicated, and the requirements for some equipment and materials are very high; the second method is only applicable For symmetrical even-numbered alkanes, the resulting products need to be extracted repeatedly with ether solvent; the third and fourth methods are very dangerous to operate, and petroleum ether is very easy to erupt in the violent reaction between metal sodium and halogenated alkanes, with low safety factor and high cost
[0005] The corresponding alkanes can be prepared by hydrogenation of higher fatty acid esters, but during the hydrogenation reaction, a large number of decarboxylation and decarbonylation reactions will occur, making the composition of the reaction product complex and producing more alkanes with reduced carbon numbers. On the one hand, it is not conducive to improving the yield of the target product. On the other hand, the decarboxylation reaction and decarbonylation reaction will produce carbon monoxide or carbon dioxide, which will have an adverse effect on the hydrogenation reaction.
[0006] CN200910100260.5 discloses a method for preparing alkanes from higher fatty acid esters, using fatty acid methyl esters containing 8 to 22 carbon atoms or fatty acid ethyl esters containing 8 to 22 carbon atoms as raw materials for hydrogenation reaction to produce alkanes, However, it can be seen that in the obtained alkane products, most of the carbon in the fatty acid is still removed, such as using methyl stearate (stearic acid is octadecyl carboxylic acid) as raw material, the obtained heptadecane The total yield of octadecanes and octadecanes is only 75%, therefore, the yield of non-decarburized direct hydrogenation products (octadecanes) will be lower
At the same time, the difference between the boiling points of heptadecanes and octadecanes is very small, and it is very difficult to further obtain octadecanes through separation technology
However, the technology of producing n-docosane by hydrogenation method has not been reported yet.

Method used

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0018] Catalyst preparation

[0019] 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 Nanometer Port Co., Ltd.) were oxidized for 2h, 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 / multi-walled carbon nanotube catalyst (Pd / MwCNTs), and prepared two kinds of catalysts namely Catalyst 1 (the mass content of palladium is 4%) and catalyst 2 (the mass content of palladium is 7%).

Embodiment 2

[0021] Add 2.5 parts (parts by volume, the same below) of behenic 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 the stirring and heating at 280°C. After 6 hours, the reaction was stopped, and after cooling to room temperature, the catalyst was separated by filtration. Carry out quantitative detection to product with gas chromatography, it can be known that the transformation rate of raw material behenic acid is 86%, and the total yield of product n-docosane is 80% (molar yield, product n-docosane accounts for 80% of raw material behenic acid. percentage, the same below).

Embodiment 3

[0023] Add 1.5 parts of behenic acid, 0.4 parts of Pd / MwCNTs catalyst 2, and 16 parts of n-hexane into a 100 mL reaction kettle, and fill it with hydrogen gas (containing 5 μL / L of NH 3 ), with an initial hydrogen pressure of 5.0MPa, start stirring and heating, stop the reaction after reacting at 260°C for 7 hours, and separate the catalyst by filtration after cooling to room temperature. Quantitative detection of the product by gas chromatography shows that the conversion rate of raw material behenic acid is 90%, and the yield of product n-docosane is 85%.

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Abstract

The invention relates to a method for preparation of n-docosane by natural acid-behenic acid, a behenic acid raw material is mixed with a solvent for hydrogenation reaction in the presence of a catalyst and hydrogen, the catalyst is a palladium / carbon nanotube catalyst, the hydrogen contains 5-50 mu L / L of NH3, the hydrogenation reaction pressure is 1-10MPa, the reaction temperature 220-320 DEG C, and the reaction time is 3-10h. The catalyst uses multi-wall carbon nanotube as a carrier, and 2%-10% by mass of palladium as an active component; the solvent is one of n-hexane, n-heptane, n-octane or dodecane. Compared with the prior art, the method has the advantages of simple preparation process, low reaction temperature, less solvent consumption, high reaction activity and higher yield of an objective product.

Description

technical field [0001] The invention relates to a method for generating n-docosane through liquid-phase catalytic hydrodeoxygenation of behenic acid, which belongs to the field of catalytic technology. Background technique [0002] As one of the key components of low-temperature diesel oil improvers and environmentally friendly liquid fuel compositions, n-paraffins have been widely used. important role. [0003] The preparation method of existing n-alkane mainly contains the following several kinds: one, adopt molecular sieve or urea dewaxing to prepare the mixture of n-alkane, then carry out the method of subsection freezing, separation n-alkane monomer, wherein typical process There is an IVDW process developed by our country; 2. The Wurtz reaction is used to prepare symmetrical n-alkanes; 3. The iodoalkane reduction method is used; 4. Petroleum ether, n-hexane, and n-heptane are used as solvents to link halogenated alkanes. Although the above methods can obtain the corr...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C9/22C07C1/207B01J23/44
Inventor 张志银孙剑锋全辉姚春雷孙国权林振发赵威
Owner CHINA PETROLEUM & CHEM CORP