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A modified molecular sieve catalyst for ethanol dehydration to ethylene and its application

An ethanol dehydration and molecular sieve technology, which is applied in molecular sieve catalysts, catalyst activation/preparation, physical/chemical process catalysts, etc., can solve the problems of high preparation cost, high energy consumption and complex modification process of modified catalysts, and avoid ethylene The effect of reducing selectivity, reducing the amount of medium and strong acids, and increasing the amount of weak acids

Active Publication Date: 2021-06-22
XIAN ORIGIN CHEM TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] At present, there are various shortcomings in the process of acid-base modification of HZSM-5 molecular sieve: the main reason is that the modification process is relatively complicated. Generally, the acid-base modification of molecular sieve powder is carried out first, because the raw material exists in powder form, so in order to To ensure the uniformity of modification, it is necessary to use mechanical stirring, which leads to high energy consumption in the modification process. After modification, drying, roasting and other processes are required to form modified molecular sieve powder, and then use the modified molecular sieve powder Molecular sieve powder as raw material and macroporous pseudo-boehmite powder are bonded, extruded, dried, and roasted to prepare the acid-base modified molecular sieve catalyst
However, the molecular sieve catalyst uses relatively expensive organic bases such as tetramethylammonium hydroxide, tetraethylammonium hydroxide, tetrapropylammonium hydroxide, etc. in the modification, resulting in higher preparation costs for the modified catalyst

Method used

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  • A modified molecular sieve catalyst for ethanol dehydration to ethylene and its application
  • A modified molecular sieve catalyst for ethanol dehydration to ethylene and its application
  • A modified molecular sieve catalyst for ethanol dehydration to ethylene and its application

Examples

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Effect test

Embodiment 1

[0031] The modified molecular sieve catalyst of the present embodiment is prepared by the following method:

[0032] Step 1. Mix 70.0g HZSM-5 molecular sieve powder, 43.0g macroporous pseudo-boehmite powder and 3.5g scallop powder for 20 minutes to obtain a mixture, and then add 40.2mL of carboxylate with a mass concentration of 0.5% to the mixture. The sodium methylcellulose aqueous solution was mixed uniformly and rolled for 40 minutes, and then extruded into a cylindrical catalyst with a diameter of 2.0 mm on an extruder, and the cylindrical catalyst was placed in an oven and dried at a temperature of 110 ° C for 2 hours. , obtained unmodified bar-shaped molecular sieve catalyst after natural cooling; the average particle size of the HZSM-5 molecular sieve powder is 0.5 μm, the molar ratio of silicon to aluminum is 60, and the specific surface area is 210m 2 / g, the pore volume is 0.18mL / g, Na 2 The mass percentage of O is 0.05%; the specific surface area of ​​the macropor...

Embodiment 2

[0040] The modified molecular sieve catalyst of the present embodiment is prepared by the following method:

[0041] Step 1. Mix 80.0g HZSM-5 molecular sieve powder, 28.6g macroporous pseudo-boehmite powder and 3.4g scallop powder for 20 minutes to obtain a mixture, and then add 39.8mL of carboxylate with a mass concentration of 0.5% to the mixture. The sodium methylcellulose aqueous solution was mixed uniformly and rolled for 40 minutes, and then extruded into a cylindrical catalyst with a diameter of 2.0 mm on an extruder, and the cylindrical catalyst was placed in an oven and dried at a temperature of 110 ° C for 2 hours , obtained unmodified bar-shaped molecular sieve catalyst after natural cooling; the average particle size of the HZSM-5 molecular sieve powder is 0.5 μm, the molar ratio of silicon to aluminum is 60, and the specific surface area is 210m 2 / g, the pore volume is 0.18mL / g, Na 2 The mass percentage of O is 0.05%; the specific surface area of ​​the macroporo...

Embodiment 3

[0049] The modified molecular sieve catalyst of the present embodiment is prepared by the following method:

[0050] Step 1. Mix 60.0g of HZSM-5 molecular sieve powder, 57.1g of macroporous pseudoboehmite powder and 3.7g of turnip powder for 20 minutes to obtain a mixture, and then add 44.1mL of carboxylate with a mass concentration of 0.5% to the mixture. The sodium methylcellulose aqueous solution was mixed uniformly and rolled for 40 minutes, and then extruded into a cylindrical catalyst with a diameter of 2.0 mm on an extruder, and the cylindrical catalyst was placed in an oven and dried for 3 hours at a temperature of 100 ° C. , obtained unmodified bar-shaped molecular sieve catalyst after natural cooling; the average particle size of the HZSM-5 molecular sieve powder is 0.5 μm, the molar ratio of silicon to aluminum is 50, and the specific surface area is 210m 2 / g, the pore volume is 0.18mL / g, Na 2 The mass percentage of O is 0.05%; the specific surface area of ​​the m...

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Abstract

The invention discloses a modified molecular sieve catalyst for ethanol dehydration to ethylene. The catalyst uses HZSM-5 molecular sieve powder and macroporous pseudo-boehmite powder as raw materials to prepare an unmodified strip-shaped molecular sieve catalyst, and then sequentially uses Na 2 CO 3 The aqueous solution and the citric acid aqueous solution are subjected to alkali modification and acid modification, and are prepared by drying and roasting; the invention also discloses the application of a modified molecular sieve catalyst for ethanol dehydration to ethylene. In the preparation and modification process of the catalyst of the present invention, no stirring process is required, the preparation process is simplified, and at the same time, the amount of weak acid on the surface of the catalyst is greatly increased, and the amount of medium-strong acid is reduced, thereby improving the catalytic performance of the modified molecular sieve catalyst for the reaction of ethanol dehydration to ethylene , and improve the conversion rate of raw material ethanol and the selectivity of product ethylene, and prolong the service life of the modified molecular sieve catalyst; the application of the modified molecular sieve catalyst of the present invention in ethanol dehydration to ethylene is simple and suitable for popularization.

Description

technical field [0001] The invention belongs to the technical field of catalyst preparation, and in particular relates to a modified molecular sieve catalyst for ethanol dehydration to ethylene and an application thereof. Background technique [0002] Ethylene is one of the most basic raw materials in the organic chemical industry. It is mainly used in synthetic resins, rubber, fibers, coatings, adhesives, surfactants and other polymer materials. At the same time, the modern ethylene industry produces ethylene and by-products such as propylene, butadiene, benzene, xylene, etc., which are also important raw materials for the manufacture of related synthetic materials. At present, the main raw materials for industrial production of ethylene come from two ways: one is light hydrocarbons from natural gas processing plants: such as ethane, propane, butane, etc.; the other is processed products from refineries: such as refinery gas, gasoline, diesel oil, etc.; The raw materials o...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/40B01J37/10B01J37/06C07C1/20C07C11/04
CPCB01J29/40B01J37/06B01J37/10C07C1/20C07C11/04Y02P20/52Y02P30/20Y02P30/40
Inventor 吕宏安何观伟袁岚张芳王新星崔楼伟卞雯
Owner XIAN ORIGIN CHEM TECH
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