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Catalyst used for isobutane dehydrogenation for preparing isobutylene, and preparation method thereof

A catalyst and isobutane technology, applied in chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, etc., can solve the problems of low efficiency of dehydrogenation catalysts and achieve production costs Inexpensive, easy to handle, and improved yield

Active Publication Date: 2017-06-27
PETROCHINA CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] For the catalytic dehydrogenation reaction of isobutane, the acidity of the catalyst surface plays a crucial role. In the catalyst provided by the invention, iron is added as the main active component, and vanadium, aluminum and other auxiliary elements are added at the same time. Form a synergistic effect between each other to change the surface morphology of the catalyst, thereby adjusting the surface acidity of the catalyst; it is because of the synergistic effect that the surface acidity of the catalyst can still form a good reaction to isobutane on the one hand. Adsorption to complete the activation of isobutane; on the other hand, the surface acidity of the catalyst is not so strong that it is difficult for the active intermediate to detach from the surface of the catalyst, resulting in a deep reaction; effectively solve the traditional dehydrogenation with iron as the main component Catalyst efficiency is too low

Method used

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  • Catalyst used for isobutane dehydrogenation for preparing isobutylene, and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0043] The present embodiment provides a catalyst for isobutane dehydrogenation, and the preparation method of the catalyst comprises the following steps:

[0044] 1. Dissolve 0.644g ammonium metavanadate in 30mL saturated solution of oxalic acid (density is 1.653g / mL), mix 20.0g ferric nitrate hexahydrate, 45g aluminum nitrate, 0.31g hexahydrate cerium nitrate, 0.429g potassium nitrate, Dissolve 0.302g of copper nitrate trihydrate and 0.176g of tin tetrachloride pentahydrate in 100mL of distilled water, and then mix the two to obtain a mixed system;

[0045] 2. Add ammoniacal liquor (mass concentration is 25%) dropwise to the above-mentioned mixing system under stirring, the dripping rate of ammoniacal liquor is controlled to be 1-20 drops / 10s, and its addition is advisable to make the mixing system form a sol;

[0046] 3. Transfer the sol to an autoclave, keep it at 150°C for 24 hours, then raise the temperature to a pressure of 4MPa, keep it for 30 minutes, release the pres...

Embodiment 2

[0050] The present embodiment provides a catalyst for isobutane dehydrogenation, and the preparation method of the catalyst comprises the following steps:

[0051] 1. Dissolve 0.846g ammonium metavanadate in 30mL saturated solution of oxalic acid, 20.0g ferric nitrate hexahydrate, 45g aluminum nitrate, 0.31g cerium nitrate hexahydrate, 0.429g potassium nitrate, 0.302g copper nitrate trihydrate, 0.176 g tin tetrachloride pentahydrate was dissolved in 100mL of distilled water, and then the two were mixed to obtain a mixed system;

[0052] 2. Add ammoniacal liquor (mass concentration is 30%) dropwise to the mixing system under stirring, the dripping rate of ammoniacal liquor is controlled to be 1-20 drops / 10s, and its addition is advisable to make the mixed system form a sol;

[0053] 3. Transfer the sol to an autoclave, keep it at 140°C for 26 hours, then raise the temperature to a pressure of 4.5MPa, keep it for 25 minutes, release the pressure, and cool to obtain a solid;

[...

Embodiment 3

[0057] The present embodiment provides a catalyst for isobutane dehydrogenation, and the preparation method of the catalyst comprises the following steps:

[0058] 1. Dissolve 1.287g ammonium metavanadate in 30mL saturated solution of oxalic acid, 15.0g ferric nitrate hexahydrate, 45g aluminum nitrate, 0.31g cerium nitrate hexahydrate, 0.429g potassium nitrate, 0.302g copper nitrate trihydrate, 0.176 g tin tetrachloride pentahydrate was dissolved in 100mL of distilled water, and then the two were mixed to form a mixed system;

[0059] 2. Add ammoniacal liquor (mass concentration 20%) dropwise to the mixing system under agitation, the dripping rate of ammoniacal liquor is controlled to be 1-20 drops / 10s, and the amount added is advisable to make the mixed system form a sol;

[0060] 3. Transfer the sol to an autoclave, keep it at 130°C for 28 hours, then raise the temperature to a pressure of 4MPa, keep it for 40 minutes, release the pressure, and cool to obtain a solid;

[00...

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Abstract

The invention provides a catalyst used for isobutane dehydrogenation for preparing isobutylene, and a preparation method thereof. The catalyst comprises, by mass, 8-35% of iron, 8-30% of vanadium, 25-71% of aluminum and 10-22% of assistant elements. The invention also provides a preparation method of the catalyst. The preparation method comprises the following steps: 1, dissolving a vanadium precursor in a saturated oxalic acid solution, dissolving precursors of iron, aluminum and the assistant elements in the same aqueous solution, and mixing the obtained vanadium precursor solution with the obtained aqueous solution; 2, adding ammonia water to a mixed solution obtained in step 1 to form sol; 3, transferring the sol into a reaction kettle, and processing the sol to obtain a solid; and calcining the solid to obtain the catalyst. The catalyst has the advantages of high catalysis efficiency, low cost, simplicity in preparation, and easiness in industrial production.

Description

technical field [0001] The invention relates to a catalyst, in particular to a catalyst for preparing isobutene by catalytic dehydrogenation of isobutane, which belongs to the field of petrochemical industry. Background technique [0002] my country is rich in C4 resources, and with the development of the petroleum industry, the demand for butene is increasing. Therefore, the research and development of new technologies for butane dehydrogenation to butene, and the addition of low-value-added butane to high-value-added butene not only solve the problem of surplus butane resources, but also solve the demand for related olefins in my country , which is conducive to the deep development and utilization of liquefied petroleum gas and the realization of circular economy. [0003] At present, there are two main types of catalysts used in the industrial production of isobutane dehydrogenation, one is chromium-based catalyst system, such as Cr 2 o 3 / Al 2 o 3 system, the catalys...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/847B01J35/10C07C11/09C07C5/333
CPCC07C5/3335B01J23/8472B01J35/60C07C11/09
Inventor 李博李秋颖李长明田亮董炳利程中克苟文甲马建泰
Owner PETROCHINA CO LTD
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