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Nickel-based catalyst for hydrodeoxygenation of oils and fats

A nickel-based catalyst, oil hydrogenation technology, applied in the direction of metal/metal oxide/metal hydroxide catalyst, heterogeneous catalyst chemical element, physical/chemical process catalyst, etc., can solve the problem of catalyst deactivation, poor stability, Short life and other problems, to achieve the effect of high catalytic activity, strong stability and long life

Inactive Publication Date: 2016-11-09
ANHUI HAIDE PETROCHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the above oil catalytic conversion technology, the stability of the metal sulfurized catalyst is good, but it is necessary to introduce sulfur-containing hydrogen sulfide to maintain the activity of the catalyst, so it is easy to introduce sulfur-contaminated products
At present, the newly developed non-sulfur metal catalysts are greener and cleaner, and the reaction conditions are milder, but they have poor stability, low activity and short life.
The pore diameter of catalysts based on traditional microporous molecular sieves is less than 2nm, and oil macromolecules can only react on the surface of the catalyst and the pore openings. The diffusion of reactants, intermediates and products is the first to cause carbon deposition and permanently deactivate the catalyst.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0014] (1) Carrier pretreatment: add 3 times the weight of nano alumina to 10% ammonium chloride aqueous solution with mass concentration, fully disperse and let stand for 35 minutes, and microwave frequency 2450MHz, power 700W for 10 minutes, filter, and filter residue Dry for 8 hours at 100-110°C, then roast at 450-500°C for 3 hours, and finally continue to heat up to 800-850°C for 3 hours;

[0015] (2) Preparation of the main active component solution: add nickel to 5 times the weight of 20% dilute nitric acid aqueous solution with mass concentration, heat to reflux with stirring to completely dissolve it, then cool naturally to 55-65℃ and keep it for 1h, and finally continue Naturally cool to room temperature to obtain the main active component solution;

[0016] (3) Preparation of auxiliary active component solution: add copper oxide and manganese dioxide to 5 times the weight of 20% dilute nitric acid aqueous solution, heat to reflux with stirring to completely dissolve, and ...

Embodiment 2

[0020] (1) Carrier pretreatment: Add nano-alumina to 3 times the weight of 10% ammonium chloride aqueous solution with a mass concentration of 10%, fully disperse it and let it stand for 60 minutes, and microwave it at a microwave frequency of 2450MHz and a power of 700W for 7 minutes, filter, and remove the filter residue. Dry it at 100-110℃ for 8h, then roast it at 450-500℃ for 5h, and finally continue to heat up to 800-850℃ for 2h;

[0021] (2) Preparation of the main active component solution: add nickel to 5 times the weight of 20% dilute nitric acid aqueous solution with mass concentration, heat to reflux with stirring to completely dissolve it, then cool naturally to 55-65℃ and keep it for 1h, and finally continue Naturally cool to room temperature to obtain the main active component solution;

[0022] (3) Preparation of auxiliary active component solution: add copper oxide and manganese dioxide to 5 times the weight of 20% dilute nitric acid aqueous solution, heat to reflux...

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PUM

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Abstract

The invention discloses a nickel-based catalyst for hydrodeoxygenation of oils and fats, and relates to the technical field of catalyst preparation. According to the invention, nickel is taken as a main active component, copper oxide and manganese dioxide are taken as auxiliary active components, and nano-alumina is taken as a carrier, wherein the loading amount of the nickel is 10 to 20%, the loading amount of copper is 5 to 8% and the loading amount of manganese is 2 to 3%. The catalyst disclosed by the invention has the characteristics of high catalytic activity, long service life and strong stability, and the carrier is pretreated to further expand the pore channel of the nano-alumina, so that the average pore diameter of the pore channel of nano-alumina is more than 20 nanometers to not only greatly increase the loading amounts of the active components but also avoid the problem of permanent deactivation of the catalyst caused by carbon deposition for small aperture of the catalyst.

Description

Technical field: [0001] The invention relates to the technical field of catalyst preparation, in particular to a nickel-based catalyst for the hydrodeoxygenation of fats and oils. Background technique: [0002] Oil-based biomass is considered to be a potential renewable resource. The main components are carbon, hydrogen and oxygen, and are composed of saturated or unsaturated fatty acid glycerides and a small amount of free fatty acids. The carbon number of these fatty acids is distributed in C 14 -C 18 Among them, it is consistent with the corresponding diesel components, so the catalytic conversion of grease into fuel oil is a new way to solve the energy crisis. At present, the technologies for deoxygenation and conversion of fats and oils into aliphatic hydrocarbons mainly include metal sulfided catalyst hydrodeoxygenation technology, sulfur-free reduced metal hydrodeoxygenation technology and catalytic cracking technology. In the above-mentioned catalytic conversion technolo...

Claims

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Application Information

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IPC IPC(8): B01J23/889B01J35/10C10G3/00
CPCC10G3/45C10G3/50B01J23/002B01J23/8892B01J2523/00C10G2300/1011B01J35/647B01J2523/847B01J2523/72B01J2523/17B01J2523/31Y02P30/20
Inventor 黄帮义
Owner ANHUI HAIDE PETROCHEM