Preparation method for porous alumina dealcoholizing agent

A technology of porous alumina and dealcoholization agent, which is applied in the direction of chemical instruments and methods, separation methods, alkali metal oxides/hydroxides, etc., which can solve the problem of decreased catalyst utilization, uneven active components, and uncontrollable loading capacity and other problems, to achieve the effect of no obvious decline in regeneration cycle performance, rich active sites, and obvious synergistic effect

Active Publication Date: 2018-05-08
WUHAN TEXTILE UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Patent document: CN105289477 A discloses an adsorbent for removing impurities in olefin streams in coal chemical industry and its application. Zeolite molecular sieves, mesoporous materials, and metal components are mixed and formed according to a certain ratio, and then added to the metal or metal oxide solution Impregnated to obtain an adsorbent; and patent literature: CN101885656 A discloses a method for adsorbing and purifying hydrocarbon streams, patent literature: CN104148006A discloses an adsorbent for removing polar molecules in light hydrocarbon streams and its preparation, Regeneration method: the above four adsorbents all use the impregnation method to load the active components. The direct impregnation method can easily lead to the problem of pore blockage, which will greatly reduce the decarbonization activity and the utilization rate of the catalyst. And because the loading capacity cannot be controlled, This will lead to problems such as difficult regeneration and decreased reaction rate that cannot be ignored.
[0005] Patent document CN104383874A discloses a purification adsorbent based on mesoporous molecular sieve material and its preparation method and application. In this method, mesoporous molecular sieve and activated alumina are mixed mec

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  • Preparation method for porous alumina dealcoholizing agent
  • Preparation method for porous alumina dealcoholizing agent
  • Preparation method for porous alumina dealcoholizing agent

Examples

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Embodiment 1

[0034] 1. Weigh 0.5mol of AlCl 3 .6H 2 O, 0.02mol polyethylene glycol 400, configured as AlCl 3 .6H 2 O mass fraction is 10% solution A, pours in the 500mL there-necked flask, for subsequent use;

[0035] 2. Weigh 0.2 mol of diethylenetriamine (DETA) again, and configure it into lye B with a mass fraction of 10%, for subsequent use;

[0036] 3. Put the three-necked flask containing aluminum chloride hexahydrate solution A in a water bath at 80°C, start stirring at 800r / min, and add lye B to aluminum chloride hexahydrate solution A drop by drop with a constant pressure dropping funnel In the middle, the dropping time is controlled at about 1h, and the control is 7.5

[0037] 4. After the dropwise addition is completed, continue to insulate and stir for 1 hour, then stop the reaction to obtain alumina colloid, and age the obtained colloid at the reaction temperature for 18 hours;

[0038] 5. After the aging is completed, add 5% NaHCO 3 , stirring and reacting at 80...

Embodiment 2

[0043] 1. Weigh 0.5mol of AlCl 3 .6H 2 O, 0.02mol polyethylene glycol 400, configured as AlCl 3 .6H 2 O mass fraction is 10% solution A, pours in the 500mL there-necked flask, for subsequent use;

[0044] 2. Weigh again 0.2mol monoethanolamine (MEA), and configure it into lye B with a mass fraction of 10%, and set aside;

[0045] 3. Put the three-necked flask containing aluminum chloride hexahydrate solution A in a water bath at 80°C, start stirring at 800r / min, and add lye B to aluminum chloride hexahydrate solution A drop by drop with a constant pressure dropping funnel In the middle, the dropping time is controlled at about 1h, and the control is 7.5

[0046] 4. After the dropwise addition is completed, continue to insulate and stir for 1 hour, then stop the reaction to obtain alumina colloid, and age the obtained colloid at the reaction temperature for 18 hours;

[0047] 5. After the aging is completed, add 5% NaHCO 3 , stirring and reacting at 800r / min for 1...

Embodiment 3

[0052] 1. Weigh 0.5mol of AlCl 3 .6H 2 O, 0.02mol polyethylene glycol 400, configured as AlCl 3 .6H 2 O mass fraction is 10% solution A, pours in the 500mL there-necked flask, for subsequent use;

[0053] 2. Weigh 0.2mol triethanolamine (TEOA) again, and configure it into lye B with a mass fraction of 10%, for subsequent use;

[0054] 3. Put the three-necked flask containing aluminum chloride hexahydrate solution A in a water bath at 80°C, start stirring at 800r / min, and add lye B to aluminum chloride hexahydrate solution A drop by drop with a constant pressure dropping funnel In the middle, the dropping time is controlled at about 1h, and the control is 7.5

[0055] 4. After the dropwise addition is completed, continue to insulate and stir for 1 hour, then stop the reaction to obtain alumina colloid, and age the obtained colloid at the reaction temperature for 18 hours;

[0056] 5. After the aging is completed, add 5% NaHCO 3 , stirring and reacting at 800r / min ...

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Abstract

The invention discloses a preparation method for a porous alumina dealcoholizing agent. The porous alumina dealcoholizing agent prepared by using the preparation method provided by the invention can generally reach a specific surface area of 400 m2/g or above, has a pore volume of larger than 0.5 cm3/g, and has a pore channel which is a slit type mesopore with a length of 5 to 13 nm. According tothe invention, the porous alumina dealcoholizing agent can adapt to different process conditions through an adsorption reaction, especially has high penetrable adsorption capacity which is generally 8% or above at normal temperature and atmospheric pressure, can reach a saturated adsorption capacity of 25% or above, has high removal accuracy, can directly remove alcohol to a volume of 0.1 ppm or below, has a regeneration temperature of 100 to 300 DEG C, has rapid regeneration speed and rapid reaction rate, can bear large space velocity range, is free of toxicity, side reactions and byproducts,is not obviously decreased in use performance after a plurality times of adsorption-regeneration cycles, has good circulation stability, is free of corrosion to equipment, and is pollution-free to the environment.

Description

technical field [0001] The invention relates to the technical fields of environmental protection and chemical industry, in particular to a preparation method of a porous alumina dealcoholization agent. Background technique [0002] Ethylene and propylene are the most important basic organic chemical raw materials, and the ethylene industry is a symbol to measure the level of a country's industrial petrochemical industry. In recent years, my country's ethylene and propylene industries have developed rapidly. However, due to my country's special energy structure of "rich in coal, short of oil, and low in gas", the production capacity of ethylene and propylene cannot meet the demand for a long time. Space. The production steps of producing low-carbon hydrocarbons from coal through methanol mainly include four steps: coal-to-synthesis gas, synthesis gas purification, gas-to-methanol, and methanol-to-olefins. The produced low-carbon hydrocarbons are separated and purified to obt...

Claims

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Application Information

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IPC IPC(8): B01J20/08B01J20/28B01J20/30B01D53/02
CPCB01D53/02B01J20/08B01J20/28019
Inventor 夏明桂张腊梅王彩凤何秋瑾夏王哲夏广曲瑞娜王琦王伟明薛志勇吴剑虹陈飞飞彭雄义卢惠娟
Owner WUHAN TEXTILE UNIV
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