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Preparation method of desulphurization adsorbent and obtained product and application

An adsorbent and accelerator technology, which is used in the preparation of desulfurization adsorbents and the resulting products and application fields, can solve the problems of reduced adsorbent activity and small pore volume of adsorbents, and achieves improved activity and stability. The effect of abrasion resistance

Active Publication Date: 2014-05-28
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] In these adsorbent preparation methods, the strength of the adsorbent is improved by adding clay, but since the clay itself has no pores, it is easy to make the pore volume of the adsorbent smaller and reduce the activity of the adsorbent.

Method used

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  • Preparation method of desulphurization adsorbent and obtained product and application

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046] 1.03 kg of nano zinc oxide (Alfa Aesar company, analytically pure, 20-30nm) was slowly added to 1.8 kg of 15% nitric acid (chemically pure, produced by Beijing Chemical Plant) solution under stirring and stirred for 1 hour to form a white Sol.

[0047] With 4.0 kg of zinc oxide powder (produced by Beijing Chemical Plant, >99.7%), 1.46 kg of kaolin (Qilu catalyst branch, containing 1.20 kg on a dry basis, the kaolin contains 51wt% alumina and 48wt% silicon oxide) and 2.09 kg of expanded Perlite (Qilu Catalyst Branch, containing 2.01 kg on a dry basis, the expanded perlite contains 20 wt% alumina and 74 wt% silica) was added to 5.8 kg of deionized water, and stirred for 30 minutes. Then add the above-mentioned zinc oxide sol, mix and stir for 1 hour to obtain a carrier slurry.

[0048] The carrier slurry uses Niro Bowen Nozzle Tower TM The model spray dryer is used for spray drying, the spray drying pressure is 8.5 to 9.5MPa, the inlet temperature is below 500°C, and th...

Embodiment 2

[0051] With 2.18 kilograms of kaolin (Qilu Catalyst Branch, containing 1.81 kilograms on a dry basis), 1.75 kilograms of zinc hydroxide (Sinopharm Chemical Reagent Company, analytically pure) and 3.0 kilograms of neutral water (pH value is 6-8) are mixed under stirring Finally, add 75 grams of concentrated nitric acid (chemically pure, produced by Beijing Chemical Plant) and stir and heat up to above 60°C for acidification for 1 hour to form a zinc sol containing kaolin. When the temperature dropped below 40° C., 5.0 kg of zinc oxide (Headhorse Company, >99.7%) powder was added, mixed and stirred for 1 hour to obtain a carrier mixture slurry.

[0052] Referring to the method of Example 1, the carrier was spray-dried and molded and the active component nickel was introduced to obtain the adsorbent A2. The chemical composition of the adsorbent A2 is: the content of zinc oxide is 64.3wt%, the content of silicon dioxide is 8.7wt%, the content of aluminum oxide is 9.2wt%, and nicke...

Embodiment 3

[0054] Get 1.92 kilograms of zinc formate dihydrate (Sinopharm Chemical Reagent Company, >98.5%) and dissolve it in 5.7 kilograms of deionized water, and add 100 milliliters of concentrated ammonia water (chemically pure, produced by Beijing Chemical Factory) after the zinc acetate is completely dissolved. Then stir for 1 hour, and the zinc acetate peptizes to generate a transparent zinc sol.

[0055] Add 1.45 kg of kaolin (Qilu Catalyst Branch, containing 1.20 kg on a dry basis), 1.32 kg of expanded perlite (Qilu Catalyst Branch, containing 1.30 kg on a dry basis) and 5.0 kg of zinc oxide powder (Headhorse Company) to the above-mentioned zinc sol , >99.7%), mixed and then stirred for 1 hour to obtain carrier slurry.

[0056] Referring to the method of Example 1, the carrier was spray-dried and molded and the active component nickel was introduced to obtain the adsorbent A3. The chemical composition of the adsorbent A3 is as follows: the content of zinc oxide is 60.0wt%, the ...

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Abstract

The invention relates to a preparation method of a desulphurization adsorbent, which comprises: (1) hydrolyzing and aging a zinc oxide precursor to form zinc sol; (2) mixing the zinc sol, a silicon oxide source, and zinc oxide to form a carrier mixture; (3) molding the mixture, drying and roasting to form a carrier; (4) introducing a compound component containing promoter metal into the carrier, drying and roasting to obtain an adsorbent precursor; (5) reducing the adsorbent precursor in the hydrogen-containing atmosphere to allow the promoter metal to basically be in a reduction state so as to obtain the adsorbent. The invention adopts zinc sol as a binder to prepare the adsorbent, and the prepared adsorbent has good wear-resistant intensity and good activity and stability, and can be used for the adsorption desulphurization process of gasoline and diesel oil.

Description

technical field [0001] The present invention relates to an adsorbent for removing sulfur from liquid raw materials of cracked gasoline and diesel fuel, its preparation method and application method. Background technique [0002] As people pay more and more attention to environmental protection, environmental regulations are becoming stricter, and reducing the sulfur content of gasoline and diesel is considered to be one of the most important measures to improve air quality, because sulfur in fuel will affect the performance of automotive catalytic converters produce adverse effects. Sulfur oxides present in automobile engine exhaust can inhibit and irreversibly poison precious metal catalysts in converters. Exhaust gases from inefficient or poisoned converters contain unburned non-methane hydrocarbons and oxides of nitrogen and carbon monoxide, which are catalyzed by sunlight to form photochemical smog. [0003] Most of the sulfur in gasoline in my country comes from therm...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J20/10B01J20/30C10G25/00
Inventor 林伟田辉平朱玉霞陆友保王磊王振波郭晓峰
Owner CHINA PETROLEUM & CHEM CORP