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Method for producing ethane by catalyzing ethanol dehydration

A technology for catalytic dehydration and ethanol, which is applied in the production of bulk chemicals, chemical instruments and methods, molecular sieve catalysts, etc., and can solve problems such as poor catalyst stability

Active Publication Date: 2014-11-26
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0010] The technical problem to be solved by the present invention is that there is a problem of poor catalyst stability in the prior art, and a new method for producing ethylene by catalytic dehydration of ethanol is provided

Method used

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  • Method for producing ethane by catalyzing ethanol dehydration
  • Method for producing ethane by catalyzing ethanol dehydration
  • Method for producing ethane by catalyzing ethanol dehydration

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] By 1SiO 2 : 0.01Al2 o 3 : 0.41TEAOH: 0.31 acetylacetone: 31.76H 2 O Weigh each material, dissolve sodium aluminate in distilled water, add tetraethylammonium hydroxide dropwise, stir for 1 hour, then add ethyl orthosilicate dropwise, stir for 1 hour, then add acetylacetone, stir for 1 hour , adjusted to pH = 13.0 with 0.1N sodium hydroxide solution, and continued to stir for 5 hours. The resulting mixture was crystallized under hydrothermal conditions at 170°C for 4 days, washed, filtered and dried. The XRD spectrum of the obtained product is shown in figure 2 In curve 1, the relative intensity of (020), (040), (060) and (080) peaks in the diffraction spectrum is significantly increased, which shows that the synthesized product grows preferentially in the (010) direction (b-axis).

[0024] The synthesized raw ZSM-5 zeolite powder was treated with 0.8 mol / L acetic acid at 70°C for 5 hours for 4 consecutive times, wherein the weight ratio of the acid solution to the Z...

Embodiment 2

[0027] By 1SiO 2 : 0.01Al 2 o 3 : 0.25TPAOH : 0.05 sodium oxalate : 32.0H 2 O Weigh each material, dissolve sodium aluminate in distilled water, add tetrapropylammonium hydroxide dropwise, stir for 1 hour, then add silica sol dropwise, stir for 1 hour, then add sodium oxalate, stir for 1 hour, use 0.1 N sodium hydroxide solution was used to adjust the pH to 12.0, and stirring was continued for another 5 hours. The resulting mixture was crystallized under hydrothermal conditions at 200°C for 3 days, washed, filtered and dried. XRD spectrum see figure 2 In curve 2, the relative intensity of (020), (040), (060) and (080) peaks in the diffraction spectrum is significantly increased, which shows that the synthesized product grows preferentially in the (010) direction (b-axis). The synthesized raw ZSM-5 zeolite powder was treated with 0.8 mol / L acetic acid at 70°C for 5 hours for 4 consecutive times, wherein the weight ratio of the acid solution to the ZSM-5 zeolite was 9 to o...

Embodiment 3

[0030] By 1SiO 2 : 0.02Al 2 o 3 : 0.23TEAOH: 0.278-hydroxyquinoline: 44.64H 2 O Weigh each material, dissolve aluminum triethoxide in distilled water, add tetraethylammonium hydroxide dropwise, stir for 1 hour, then add silica sol dropwise, stir for 1 hour, then add 8-hydroxyquinoline, stir for 1 hour , adjust pH=11.0 with 0.1N sodium hydroxide solution, and continue stirring for 5 hours. The resulting mixture was crystallized under hydrothermal conditions at 150°C for 6 days, washed, filtered and dried. XRD spectrum see figure 2 In curve 3, the relative intensity of (020), (040), (060) and (080) peaks in the diffraction spectrum is significantly increased, which shows that the synthesized product grows preferentially in the (010) direction (b-axis). The synthesized raw ZSM-5 zeolite powder was treated with 0.8 mol / L acetic acid at 80°C for 5 hours for 3 consecutive times, wherein the weight ratio of the acid solution to the ZSM-5 zeolite was 8 to obtain HZSM-5.

[0031...

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Abstract

The invention relates to a method for producing ethane by catalyzing ethanol dehydration, and mainly solves the problems of poor stability of a catalyst in the prior art. The catalyst employed by the method is prepared by the following steps of mixing a silicon source, an aluminium source, a template R1, a template R2 and water; adjusting the pH value of a reaction mixture to be 8-14 with an inorganic base, wherein the molar ratio of the reaction mixture is as follows: Al2O3 / SiO2=0.003-0.05, R1 / SiO2=0.1-2, H2O / SiO2=10-100 and R2 / SiO2=0.05-2; and hydrothermally crystallizing the reaction mixture for 1-10 days in a condition with a temperature of 100-250 DEG C. The template R1 is at least one selected from tetramethyl ammonium hydroxide, tetraethyl ammonium hydroxide, tetrapropyl ammonium hydroxide or tetrabutyl ammonium hydroxide; and the template R2 is at least one selected from beta-diketone, beta-diketone salt, oxalic acid, oxalate, pyrocatechol or 8-hydroxyquinoline. The technical solution solves the problems well, and can be used in industrial production of preparing ethene from ethanol catalytic dehydration.

Description

technical field [0001] The invention relates to a method for producing ethylene by catalytic dehydration of ethanol. Background technique [0002] As a basic organic chemical raw material and a leading product in the petrochemical industry, ethylene is known as the "mother of petrochemical industry". It is mainly used in the production of polyethylene, ethylene oxide / ethylene glycol, dichloroethane, styrene, acetic acid Chemicals such as ethylene. With the rapid development of ethylene derivative industries such as chemical industry, energy and materials, the demand for ethylene is increasing. At present, ethylene mainly comes from naphtha cracking. As petroleum resources are non-renewable and are gradually becoming exhausted, the use of renewable biomass resources to develop bioenergy and biochemical industries has become an inevitable trend of current and future economic development. Ethanol can be obtained by fermentation of plant starch or wood fiber. The source of ra...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C11/04C07C1/24B01J29/40
CPCY02P20/52
Inventor 李亚男金照生徐菁金萍
Owner CHINA PETROLEUM & CHEM CORP