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 pipeline blockage, biodiesel molecular structure unchanged, engine damage, etc.

Inactive Publication Date: 2016-12-07
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 unsaturati

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0039] The catalyst was prepared by impregnation method, and the carrier was doped Co 2+ SAPO-5, Co 2+ The doping amount in SAPO-5 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.

[0040] 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 ga...

Embodiment 2

[0045] The catalyst was prepared by impregnation method, and the carrier was doped Co 2+ SAPO-5, Co 2+ The doping amount in SAPO-5 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.

[0046] All the other conditions are the same as in Example 1.

[0047] After testing the final product, its deoxidation rate reached 99.85%, and after 500 hours of continuous operation of the device, the deoxidation rate still reached 99.6%.

Embodiment 3

[0072] 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.

[0073] The final product was tested, and after 3 months of use, the pressure drop of the catalyst bed did not change, which was 13% 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. The biodiesel hydrodeoxygenation process is characterized in that a fixed bed reactor is adopted for the process and filled with a hydrodeoxygenation catalyst, and the catalyst comprises a carrier and an active component; the carrier is SAPO-5 with heteroatom Co2+ doped in a synthetic skeleton structure; the active component is a mixture of molybdenum nitride (MO2N), tungsten nitride (W2N), molybdenum carbide (Mo2C) and tungsten carbide (WC); the catalyst further contains a catalytic promoter, 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>. By means of the process, hydrodeoxygenation on biodiesel can be controlled at a high deoxidation rate (99.8% or above), and catalytic activity is not obviously reduced after continuous operation is carried out 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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IPC IPC(8): C10G45/12B01J29/85
CPCC10G45/12B01J29/85B01J2229/183B01J2229/186C10G2300/202C10G2400/04
Inventor 朱忠良
Owner 锡山区绿春塑料制品厂
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