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Hydrocarbon oil desulphurization adsorbent, and preparation method and application thereof

A technology of adsorbent and hydrocarbon oil, which is applied in the field of hydrocarbon oil desulfurization adsorbent and its preparation and application, can solve the problem of lack of desulfurization activity of the adsorbent, and achieve high desulfurization activity and increase the effect of gasoline octane number

Active Publication Date: 2013-01-30
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] Although the addition of shape-selective molecular sieves in the above two methods is beneficial to isomerization to increase the octane number of gasoline, the adsorbent lacks sufficient desulfurization activity due to the lack of suitable content of accelerator metals and sulfur storage media.

Method used

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  • Hydrocarbon oil desulphurization adsorbent, and preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0045] 4.43 kilograms of zinc oxide powder (Headhorse company, purity 99.7wt.%), 0.84 kilograms of β molecular sieves (Nanjing Catalyst Branch, containing 0.70 kilograms on a dry basis) and 4.57 kilograms of deionized water were mixed, and after stirring for 30 minutes, zinc oxide and β Molecular sieve mixed slurry.

[0046] Take 1.37 kg of alumina (produced by Shandong Aluminum Factory, containing 1.00 kg on a dry basis) and 2.10 kg of expanded perlite (including 2.06 kg on a dry basis) and mix them under stirring, then add 4.6 kg of deionized water and mix well, then add 360 ml 30wt.% hydrochloric acid (chemically pure, produced by Beijing Chemical Plant) was stirred and acidified for 1 hour, then heated to 80° C. and aged for 2 hours, then added zinc oxide and Beta molecular sieve slurry, mixed and stirred for 1 hour to obtain carrier slurry.

[0047] The carrier slurry uses Niro Bowen Nozzle Tower TM The model spray dryer is used for spray drying, the spray drying pressur...

Embodiment 2

[0055] Get 1.61 kilograms of pseudo-boehmite (produced by Shandong Aluminum Plant, containing 1.17 kilograms on a dry basis) and 1.54 kilograms of diatomite (containing 1.50 kilograms on a dry basis) and mix under stirring, then add 8.2 kilograms of deionized water and mix well, Add 260 milliliters of 30% hydrochloric acid (chemically pure, produced by Beijing Chemical Factory) and stir for acidification for 1 hour, then raise the temperature to 80° C. and age for 2 hours. After the temperature dropped, 5.52 kg of zinc oxide powder (Headhorse Company, purity 99.7%) and 0.36 kg of β molecular sieve (Nanjing Catalyst Branch, containing 0.30 kg on a dry basis) were added and stirred for 1 hour to obtain a 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 A2. The chemical composition of the adsorbent A2 is: the content of zinc oxide is 55.2wt.%, the content of...

Embodiment 3

[0061] The adsorbent was prepared as follows: 4.93 kg of zinc oxide powder (Headhorse Company, purity 99.7%), 0.56 kg of USY (Qilu Catalyst Branch, containing 0.50 kg on a dry basis) and 5.57 kg of deionized water were mixed and stirred for 30 minutes to obtain Mixed slurry of zinc oxide and USY.

[0062] Take 1.85 kg of pseudo-boehmite (produced by Shandong Aluminum Plant, containing 1.35 kg on a dry basis) and 1.64 kg of diatomite (world mining company, containing 1.60 kg on a dry basis) and mix them under stirring, then add 4.6 kg of deionized water After mixing evenly, add 300 ml of 30% hydrochloric acid (chemically pure, produced by Beijing Chemical Factory) to make the pH value of the slurry 2.5, stir and acidify for 1 hour, then heat up to 80° C. and age for 2 hours. Zinc oxide slurry was added and stirred for 1 hour to obtain carrier slurry.

[0063] Referring to the method of Example 1, the spray drying of the carrier was carried out and the active components nickel ...

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Abstract

The invention provides a hydrocarbon oil desulphurization adsorbent, and a preparation method and an application thereof. With a total weight of the adsorbent as a standard, The adsorbent provided by the invention at least comprises the components of, by weight: (1) 1-20% of an aluminosilicate molecular sieve with a duodenary-ring pore-channel structure, (2) 3-35% of an alumina adhesive, (3) 5-40% of a silicon oxide source, (4) 10-80% of zinc oxide, and (5) 5-30% of at least one metal accelerating agent selected from cobalt, nickel, iron and manganese. The absorbent provided by the invention has high desulphurization activity, and has an advantage of a capacity for substantially increasing gasoline octane number.

Description

technical field [0001] The invention relates to an adsorbent for removing sulfur from hydrocarbon oil, a preparation method and application thereof. Background technique [0002] CN 1355727A provides a novel absorbent composition containing zinc oxide, silicon oxide, aluminum oxide and nickel or cobalt, and provides the preparation method of this adsorbent. In this method, a carrier containing zinc oxide, silicon oxide and aluminum oxide is prepared first, and then nickel is introduced by impregnation. The adsorbent can be used to remove sulfur from cracked gasoline or diesel fuel. [0003] In CN 1208124C, a promoter metal such as cobalt and nickel is used to impregnate an adsorbent carrier containing zinc oxide, expanded perlite and alumina, and then reduce the promoter at a suitable temperature to prepare an adsorbent for removing sulfide in cracked gasoline. [0004] When the above-mentioned adsorbent removes sulfur from gasoline under hydrogen-facing conditions, the oc...

Claims

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Application Information

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IPC IPC(8): B01J20/18B01J20/30C10G25/00
Inventor 林伟田辉平朱玉霞王磊
Owner CHINA PETROLEUM & CHEM CORP
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