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Composite catalyst for synthesizing benzene through methane anaerobic aromatization and preparation method and application thereof

A technology of catalyst and chemical synthesis, which is applied in the field of composite catalyst and its preparation, can solve the problems of low conversion rate of methane and other problems that are not involved in the report of composite catalyst, and achieve the improvement of conversion rate and benzene yield, conversion rate and product benzene The effect of increasing the yield and increasing the yield

Inactive Publication Date: 2019-08-09
SHAANXI COAL & CHEM TECH INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the reaction is limited by thermodynamics and the methane conversion rate is low. In order to solve this problem, researchers have tried to add various metal additives to improve the activity and stability of the catalyst. For example, Xu Yide et al. reported in the patent document CN1167653 that methane was The aromatization process is carried out under the action of the Mo-R / HZSM-5 catalyst with the second component R (R=La, Ce, Pr, Nd), but the thermodynamic limit cannot be broken, and the methane conversion rate is still low
[0006] At present, a lot of work has been done on the aromatization of pure methane at home and abroad, but there are no reports involving composite catalysts

Method used

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  • Composite catalyst for synthesizing benzene through methane anaerobic aromatization and preparation method and application thereof
  • Composite catalyst for synthesizing benzene through methane anaerobic aromatization and preparation method and application thereof

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0040] 1.1 Preparation method

[0041] 2%Mo1.5%Fe0.05%Mg / ZSM-5 catalyst was prepared by co-impregnation method. First, the ZSM-5 molecular sieve was calcined at 400°C for 24 hours; secondly, the calcined ZSM-5 molecular sieve was impregnated into (NH 4 ) 6 Mo 7 o 24 , Fe(NO 3 ) 3 and Mg(NO 3 ) 2 in the aqueous solution (the mass ratio of the three is 11.4:

[0042] 21.3: 1) Stir for 8 hours, evaporate to dryness at 110°C, and dry at 90°C for 16 hours; finally, put it in a muffle furnace and roast at 400°C for 8 hours, and the prepared catalyst powder is tabletted, crushed and screened to obtain 40-60 Objective Mo-based solid-phase catalyst.

[0043] The above-mentioned Mo-based solid-phase catalyst was loaded into a fixed-bed reactor, and the catalyst was pre-carbonized with methane for 20 min at 700 °C and a space velocity of 5 L / g h.

[0044] The above-mentioned pre-carbonized Mo-based solid-phase catalyst was unloaded, and then physically mixed with 40-60 mesh met...

Embodiment 2

[0048] 2.1 Preparation method

[0049] 6%Mo0.7%Co0.2%Mn / ZSM-11 catalyst was prepared by co-impregnation method. First, the ZSM-11 molecular sieve was calcined at 500 °C for 12 h; secondly, the calcined ZSM-11 molecular sieve was impregnated into (NH 4 ) 6 Mo 7 o 24 , Co(NO 3 ) 2 and Mn(NO 3 ) 2 (the mass ratio of the three is 16.0:3.3:1) and stirred for 18h, evaporated to dryness at 110°C, and dried at 110°C for 12h; finally, put it into a muffle furnace and roast at 500°C for 5h, and the prepared catalyst powder was After tableting, crushing and screening, a Mo-based solid-phase catalyst of 40-60 meshes is obtained.

[0050] The above-mentioned Mo-based solid-phase catalyst was loaded into a fixed-bed reactor, and the catalyst was pre-carbonized with methane for 30 min at 650 °C and a space velocity of 2 L / g h.

[0051] The above pre-carbonized Mo-based solid-phase catalyst was physically mixed with 40-60 mesh metal Ti particles at a mass ratio of 1:1.5 to obtain an ...

Embodiment 4

[0061] 4.1 Preparation method

[0062] 10%Mo0.1%Ru0.5%Rh / MCM-49 catalyst was prepared by co-impregnation method. First, the MCM-49 molecular sieve was calcined at 500°C for 18 hours; secondly, the calcined MCM-49 molecular sieve was impregnated into (NH 4 ) 6 Mo 7 o 24 , Ru(NO)(NO 3 ) 3 and Rh(NO 3 ) 3 The aqueous solution (the mass ratio of the three is 55.3:1:4.5) was stirred for 12h, evaporated to dryness at 110°C, and dried at 120°C for 8h; finally, it was put into a muffle furnace and calcined at 500°C for 1h, and the prepared catalyst powder was After tableting, crushing and screening, a Mo-based solid-phase catalyst of 40-60 meshes is obtained.

[0063] The above-mentioned Mo-based solid-phase catalyst was loaded into a fixed-bed reactor, and the catalyst was pre-carbonized with methane for 10 min at 750 °C and a space velocity of 5 L / g h.

[0064] The above pre-carbonized Mo-based solid-phase catalyst and 40-60 mesh 50%Zr50%Ti particles were physically mixed a...

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Abstract

The invention provides a composite catalyst for synthesizing benzene through methane anaerobic aromatization and a preparation method and application thereof. The catalyst comprises a Mo base solid phase catalyst and a hydrogen absorption material, the Mo base solid phase catalyst comprises a molecular sieve carrier and an active component Mo, an auxiliary M1 and an auxiliary M2 loaded on the molecular sieve carrier; the M1 is Fe or Co or Ni or Ru, and the M2 is Mg or Mn or Cu or Rh; the hydrogen absorption material is Zr or Ti or ZrTi alloy. By mass, the contents of Mo, M1 and M2 in the Mo base solid phase catalyst are 2-10%, 0.1-1.5% and 0.05-0.5% respectively, and the mass ratio of the Mo base solid phase catalyst to the hydrogen absorption material is 1:(1-3). The catalyst remarkably increases the methane conversion rate and the yield of the product benzene.

Description

technical field [0001] The invention belongs to the technical field of chemical catalysts, and in particular relates to a catalyst for methane aromatization, and more particularly to a composite catalyst for synthesizing benzene by anaerobic aromatization of methane and its preparation method and application. Background technique [0002] In recent years, shale gas and coalbed methane have been developing vigorously in the world. They have gone through the research of shale gas geological conditions, the selection of "sweet spots" and the drilling of evaluation wells and the preliminary preparations for exploration and development, to the industrial exploitation test of marine shale gas, and the transition between land and sea. There are two development stages of exploration and evaluation of shale gas, namely, marine shale gas and continental shale gas, and they are advancing in an orderly manner to the large-scale exploitation of marine shale gas, and the experimental stage...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/48B01J29/78C07C2/76C07C15/04
CPCB01J29/48B01J29/78B01J29/7876B01J2229/18B01J2229/186C07C2/76C07C2529/48C07C2529/78C07C15/04Y02P20/52
Inventor 孙建平王磊张国权张生军闵小建
Owner SHAANXI COAL & CHEM TECH INST
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