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Biodiesel hydrodeoxygenation process

A hydrodeoxygenation and biodiesel technology, applied in the petroleum industry, processing hydrocarbon oil, refining hydrocarbon oil, etc., can solve problems such as deterioration, biodiesel molecular structure unchanged, and pipeline blockage

Inactive Publication Date: 2017-01-11
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 is prepared by impregnation method, and the carrier is doped Cu 2+ KIT-1, Cu 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 carrier mass, and the molar ratio is 1:0.4:0.3:0.8.

[0041] The catalyst was filled into a fixed-bed reactor. The reaction tube of the reactor was made of stainless steel with an inner diameter of 50mm. The temperature of the catalyst bed was measured with a UGU808 temperature control meter. The raw material light oil was manufactured by Beijing Satellite Manufacturing Factory. The double plunger micro-pump continuously delivers hydrogen. The hydrogen is supplied from a high-pressure cylinder and the flow rate is controlled by the Beijing Qixing Huachuang D07-11A / ZM gas mass flow meter. The catalyst loading is 2kg. The product after the reaction is cooled i...

Embodiment 2

[0046] The catalyst is prepared by impregnation method, and the carrier is doped Cu 2+ KIT-1, Cu 2+ The amount of doping 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 carrier mass, and the molar ratio is 1:0.6:0.45):1.2.

[0047] The remaining conditions are the same as in Example 1.

[0048] After testing the final product, its deoxygenation rate reached 99.85%, and after 500 hours of continuous operation of the device, the deoxygenation rate still reached 99.0%.

Embodiment 3

[0073] The catalyst contains catalytic promoter TiO 2 , CeO 2 , V 2 O 5 And NbOPO 4 , The contents are 1%, 1.5%, 1% and 3% respectively, and the rest are the same as in Example 1.

[0074] After testing the final product, after 3 months of use, there was no change in the pressure drop of the catalyst bed, which was reduced by 17% compared to the catalyst bed pressure drop of Example 1 for the same use time.

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PUM

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Abstract

The invention discloses a biodiesel hydrodeoxygenation process. The biodiesel hydrodeoxygenation process is characterized in that a fixed bed reactor is adopted in the process, the fixed bed reactor is filled with a hydrodeoxygenation catalyst, and the catalyst comprises a carrier and an active component; the carrier is KIT-1 formed by doping heteroatom Cu2+ in a synthetic framework structure. The active component is a mixture of molybdenum nitride (MO2N), tungsten nitride (W2N), molybdenum carbide (Mo2C) and tungsten carbide (WC). The catalyst further comprises a catalytic promoter, and the catalytic promoter is a mixture of TiO2, CeO2, V2O5 and NbOPO4. According to the reaction conditions of the fixed bed reactor, the reaction temperature ranges from 300 DEG C to 450 DEG C, the hydrogen pressure ranges from 2.5 MPa to 3.5 MPa, the hydrogen-oil volume ratio ranges from 500 to 800, and the volume air speed ranges from 1.0 h<-1> to 2.5 h<-1>. According to the process, hydrodeoxygenation of biodiesel can be controlled at a high deoxygenation rate (99.8% or above), and catalytic activity is not obviously reduced after the process continuously runs for 500 hours.

Description

Technical field [0001] The invention relates to a 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-containing compounds has attracted more attention. The sulfur oxides (SO x ) Discharge into the air, causing acid rain and sulfuric acid smog type pollution, causing air pollution. [0003] In order to solve the increasingly severe environmental problems and reduce the pollution of fossil fuels to the environment, in the recent period, it has become a hot spot to make full use of renewable resources based on vegetable oil as fuel. [0004] In the 1980s, American Graham Quick introduced linseed oil and cottonseed methyl oleate into diesel engines for the first time. Since then, the fatty acid monoester compounds obtained through the transesterification reaction have been defined as biodiesel. This fatty acid monoester compound can be used...

Claims

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Application Information

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IPC IPC(8): C10G45/12B01J29/04
CPCC10G45/12B01J29/045B01J2229/18B01J2229/20C10G2300/202C10G2400/04
Inventor 朱忠良
Owner 锡山区绿春塑料制品厂
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