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Biodiesel hydrodeoxygenation process

A technology of hydrodeoxygenation and biodiesel, which is applied in the fields of hydrotreating process, petroleum industry, and hydrocarbon oil treatment, etc. It can solve the problems of biodiesel molecular structure unchanged, deterioration, damage to the engine, etc.

Inactive Publication Date: 2016-12-14
锡山区绿春塑料制品厂
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, with the wide application of biodiesel, more and more defects are found: animal and vegetable oils and fats contain different types of fatty acids, and the production process will not change the degree of unsaturation, which is high, such as Biodiesel produced from cottonseed oil, rapeseed oil, etc., contains a large number of carbon-carbon unsaturated bonds in the molecular structure, which is easy to oxidize and cause deterioration during storage, transportation and use. If the unsaturation is low, such as industrial lard and tallow The freezing point of the biodiesel produced by biodiesel is much higher than that of petrochemical diesel. Even if it is mixed with petrochemical diesel in a lower proportion, it is easy to precipitate in low temperature seasons such as autumn and winter, resulting in pipeline blockage, and even damage to the engine in severe cases.
Despite a lot of research and improvements, the molecular structure of biodiesel has not changed, so its defects still exist

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0040] The catalyst was prepared by impregnation method, and the carrier was doped Co 2+ KIT-1, Co. 2+ The doping amount in KIT-1 is controlled at 0.65% of the carrier mass. The active component molybdenum nitride MO 2 N, tungsten nitride W 2 N, molybdenum carbide Mo 2 The total content of C and tungsten carbide WC is 10% of the mass of the carrier, and their molar ratio is 1:0.4:0.3:0.8.

[0041] The catalyst is loaded into a fixed bed reactor, the reaction tube of the reactor is made of stainless steel with an inner diameter of 50 mm, the catalyst bed temperature is measured with a UGU808 temperature control meter, and the raw material light oil is manufactured by Beijing Satellite Manufacturing Plant The double-plunger micropump continuously transports the hydrogen gas from a high-pressure cylinder and controls the flow rate with a Beijing Qixing Huachuang D07-11A / ZM gas mass flow meter. The catalyst loading is 2kg. The reacted product is cooled in a water bath for gas...

Embodiment 2

[0046] The catalyst was prepared by impregnation method, and the carrier was doped Co 2+ KIT-1, Co. 2+ The doping amount in KIT-1 is controlled at 0.7% of the carrier mass. The active component molybdenum nitride MO 2 N, tungsten nitride W 2 N, molybdenum carbide Mo 2 The total content of C and tungsten carbide WC is 10% of the mass of the carrier, and the molar ratio is 1:0.6:0.45):1.2.

[0047] All the other conditions are the same as in Example 1.

[0048] After testing the final product, its deoxidation rate reached 99.85%. After 500 hours of continuous operation of the device, the deoxidation rate still reached 99.5%.

Embodiment 3

[0073] The catalyst contains catalyst promoter TiO 2 , CeO 2 , V 2 o 5 and NbOPO 4 , its content is respectively 1%, 1.5%, 1% and 3%, all the other are identical with embodiment 1.

[0074] The final product was tested, and after 3 months of use, the pressure drop of the catalyst bed did not change, which was 16% lower than the pressure drop of the catalyst bed in Example 1 for the same use time.

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PUM

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Abstract

The invention discloses a biodiesel hydrodeoxygenation process which is characterized by comprising a fixed bed reactor filled with hydrodeoxygenation catalysts, the catalysts include carriers, active components and catalytic auxiliaries, the carriers are KIT-1 with synthetic skeleton structures doped with heteroatoms Co2+, the active components are molybdous nitride MO2N, tungsten nitride W2N, molybdenum carbide Mo2C and tungsten carbide WC mixture, and the catalytic auxiliaries are TiO2, CeO2, V2O5 and NbOPO4 mixture. The reaction condition of the fixed bed reactor includes reaction temperature of 300-450 DEG C, hydrogen pressure of 2.5-3.5MPa, hydrogen to oil volume ratio of 500-800, and volume space velocity of 1.0-2.5h<1>. By the process, the hydrodeoxygenation rate of biodiesel can be controlled to be high (99.8% or more), and catalytic activity cannot be obviously reduced in continuous running for 500 hours.

Description

technical field [0001] The invention relates to biodiesel hydrodeoxygenation process. Background technique [0002] In the 21st century, the demand and use of fuel oil have increased significantly, and the environmental pollution caused by sulfur compounds in it has attracted people's attention. Sulfur oxides (SO x ) into the air, producing acid rain and sulfuric acid smog pollution, etc., resulting in air pollution. [0003] In order to solve the increasingly serious environmental problems and reduce the environmental pollution caused by fossil fuels, it has recently become a hot spot to use vegetable oil as the basis and make full use of renewable resources as fuel. [0004] In the 1980s, American Graham Quick introduced linseed oil and cottonseed oleate methyl ester into diesel engines for the first time. After that, he defined fatty acid monoester compounds obtained through transesterification as biodiesel. This fatty acid monoester compound can be used alone or mixed...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G45/08C10G67/14B01J29/04
CPCC10G45/08B01J29/045B01J2229/18C10G67/14C10G2300/202C10G2300/305C10G2300/70
Inventor 朱忠良
Owner 锡山区绿春塑料制品厂
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