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Macroporous iron carbide catalyst, and preparation method and application thereof

An iron carbide and catalyst technology, applied in physical/chemical process catalysts, chemical instruments and methods, preparation of liquid hydrocarbon mixtures, etc., can solve the problems of energy consumption, small preparation amount, single iron carbide, etc. Simple operation method and short cycle effect

Inactive Publication Date: 2014-01-01
CHINA UNIV OF PETROLEUM (BEIJING)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, these processes need to be carried out at high temperature, which is a process that consumes a lot of energy, and the appearance of iron carbide is a single particle, and the preparation amount is not large (less than 1 gram).
[0005] Carbide catalysts with a pore structure have not been reported so far, and experiments on carbide catalysts for biosynthesis of oil have not been reported in the literature.

Method used

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  • Macroporous iron carbide catalyst, and preparation method and application thereof
  • Macroporous iron carbide catalyst, and preparation method and application thereof
  • Macroporous iron carbide catalyst, and preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0075] Example 1 Preparation method of carboxyl modified colloidal crystal template

[0076] In this embodiment, the carboxyl modified colloidal crystal template was prepared according to the following method:

[0077] (1) Preparation of monodisperse carboxyl modified polymethyl methacrylate (c-PMMA) microspheres by an improved soap-free emulsion polymerization method

[0078] Add 50ml acetone and 150ml deionized water to a stirrer, reflux condenser, thermometer and N 2 In a 1000ml four-necked flask with trachea, pass N after vacuuming 2 , Add MMA and AA with a volume ratio of 25:1 (both monomers are refined by vacuum distillation), and heat to 80°C. At the same time, weigh 0.27g of the initiator KPS and 0.45g of AIBN, dissolve it in 150ml of water, heat it to 80°C and add it to a four-neck flask. N 2 After reacting for 1.5 hours under protection, it was naturally cooled to room temperature under stirring, ultrasonically treated for 1.5 hours, and suction filtered to obtain c-PMMA p...

Embodiment 2

[0083] Example 2 Preparation method of three-dimensional penetrating iron carbide

[0084] (1) Preparation of monodisperse carboxyl modified polymethyl methacrylate (c-PMMA) microspheres by an improved soap-free emulsion polymerization method

[0085] Add 50ml acetone and 150ml deionized water to a stirrer, reflux condenser, thermometer and N 2 In a 1000ml four-necked flask with trachea, pass N after vacuuming 2 , Add a certain volume ratio of MMA and AA (both monomers are refined by vacuum distillation), and heat to 80°C. At the same time, a certain amount of initiators KPS and AIBN were weighed and dissolved in 150ml of water, heated to 80°C and then added to a four-neck flask. N 2 After reacting for 1.5 hours under protection, it was naturally cooled to room temperature under stirring, ultrasonically treated for 1.5 hours, and suction filtered to obtain c-PMMA polymer microspheres. figure 1 The FT-IR infrared absorption spectrum of the composite is provided.

[0086] (2) Preparat...

Embodiment 3

[0091] Example 3 Results of catalytic performance of macroporous iron carbide catalyst for catalytic conversion of biosyngas to fuel oil

[0092] The gas composition of biosynthesis gas is 20%H 2 , 19%CO, 12%CO 2 , 2%CH 4 And 49% N 2 . The catalyst prepared in Example 2 was first activated by biosynthesis gas at 310°C for 2 hours. The reaction operating conditions are: temperature 310℃, space velocity 2000h -1 , The pressure is 6.5MPa. The experimental results are as Figure 7 Shown. The macroporous iron carbide catalyst shows high catalytic activity and stability, the conversion rate of CO is maintained above 90%, the selectivity of liquid fuel oil products exceeds 60%, and the activity of the catalyst remains basically stable for 500 hours. The results of its catalytic activity for the conversion of biosyngas to fuel oil are as follows Figure 7 Shown.

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Abstract

The invention provides a macroporous iron carbide catalyst, and a preparation method and application of the macroporous iron carbide catalyst. The iron carbide catalyst is prepared by using a carboxylic acid-modified polymethyl methacrylate microsphere as a template and ferric nitrate as a precursor; the pore diameter of the macroporous iron carbide catalyst is within the range of 50-1000 nm. According to the invention, the carboxylic acid-modified microsphere is used as the template, the ferric nitrate is used as the precursor, and direct roasting is carried out under the condition of a methanol and ethylene glycol mixed solution to prepare the three-dimensionally communicated iron carbide; the operation method is simple, the period is short and the cost is low.

Description

Technical field [0001] The invention relates to the preparation field of carbide catalysts, in particular to a macroporous iron carbide catalyst and its preparation method and application, and more specifically to a three-dimensional penetrating macroporous iron carbide with strong acid and alkali resistance and mechanical properties. Its preparation method and application. Background technique [0002] Carbide is an "interstitial alloy" (interstitial alloy) formed by carbon and metal, that is, smaller carbon atoms occupy the voids of the densely packed layer of metal atoms, and the formed often have a simple crystal structure. [0003] Carbide is a kind of material with high melting point and hardness, high thermal and mechanical stability, and almost resistance to various chemical corrosion at room temperature. In addition, it also has electrical and magnetic properties similar to its parent metal. It is these properties that make them widely used in mechanical cutting, mineral ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/22C10G2/00
CPCY02E50/32Y02E50/30
Inventor 刘坚赵震谭小玉徐春明韦岳长段爱军姜桂元
Owner CHINA UNIV OF PETROLEUM (BEIJING)