A catalytic gasoline hydrogenation dearsenic agent and its preparation method and application

A technology for catalyzing gasoline and arsenic removal agent, which is applied in chemical instruments and methods, refining hydrocarbon oil, treating hydrocarbon oil, etc., and can solve the problems of blocked pores, oxide content, arsenic removal activity and selectivity, and octane number loss, etc. question

Active Publication Date: 2021-05-28
PETROCHINA CO LTD +1
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0011] To sum up, the above-mentioned technology is mainly used in the dearsenic reaction of naphtha and constant top gasoline mainly composed of alkanes, as well as light diesel oil and gaseous hydrocarbons, and is not specifically aimed at gasoline, especially catalytic gasoline with high olefin content. , the existing literature only reflects its dearsenic activity, but does not reflect the changes of olefins and octane numbers during hydrodearsenication
At the same time, the existing technology is mainly based on single Ni and Mo-Ni-P systems, and the pore distribution characteristics and oxide content have a great influence on t...

Method used

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  • A catalytic gasoline hydrogenation dearsenic agent and its preparation method and application
  • A catalytic gasoline hydrogenation dearsenic agent and its preparation method and application
  • A catalytic gasoline hydrogenation dearsenic agent and its preparation method and application

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preparation example Construction

[0039] A preparation method of catalytic gasoline hydrogenation dearsenic agent, comprising the following steps:

[0040] Step 1: Mix alumina or a mixture of alumina and titanium oxide with scallop powder evenly, add organic polymer pore-forming agent, binder and deionized water, knead, extrude, and dry at 100-150°C for 3-6 hours , heat treatment at 650-1000°C for 3-6 hours at high temperature to prepare arsenic-removing agent carrier;

[0041] Step 2: The arsenic removal agent carrier is subjected to hydrothermal treatment to expand the pores, the treatment temperature is 400-700°C, and the mass space velocity is 0.5-1.5h -1 , treated for 1-10 hours to obtain arsenic-removing agent-modified carrier;

[0042] Step 3, dissolving the active component nickel salt in one or more of citric acid, ammonia water and deionized water to form a stable active metal complex solution, and then impregnating the arsenic removal agent with an equal volume of the active metal complex solution ...

Embodiment 1

[0049] Weigh 100g of pseudo-boehmite, add 3.0g of fenugreek powder, and then add 3% nitric acid aqueous solution, knead and extrude, dry at 120°C for 4h, and then roast at 750°C for 4h to obtain arsenic removal agent carrier A (see Table 1 for properties). Weigh 20.0g of the carrier and put it into a beaker, add excess deionized water and let it stand for 3 hours, then remove the excess water on the surface of the carrier, compare the weight w1 of the carrier before immersion and the weight w2 of the carrier after immersion to calculate its water absorption, and then follow the equal volume immersion method , according to the water absorption of the carrier, the preparation of the active component impregnation solution is carried out. First weigh 60ml of deionized water, then add 42g of nickel nitrate and stir until dissolved, and finally use deionized water to make up the volume. The carrier was impregnated by an equal volume impregnation method, so that the catalyst carrier...

Embodiment 2

[0051] Weigh out 5% TiO 2 Add 100g of pseudo-boehmite to 100g of pseudo-boehmite, add 3.0g of fenugreek powder, 5g of organic polymer pore-forming agent polyvinyl alcohol with a particle size of 200μm, and then add 3% aqueous nitric acid solution, knead, extrude, and dry at 120°C for 4h , and then roasted at 750°C for 4h, then hydrothermally treated, the treatment conditions are: reaction temperature 600°C, mass space velocity 0.5h -1 , 4h, prepared modified carrier B (properties are shown in Table 1). The impregnation method of the metal active component, the impregnation amount of the nickel salt, and the drying and roasting conditions were the same as in Example 1, and the arsenic removal agent sample T2 was obtained.

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Abstract

The invention relates to a catalytic gasoline hydrogenation arsenic removal agent and its preparation method and application. The arsenic removal agent is composed of 7-20wt% NiO and 0-15wt% TiO 2 , and the rest are Al 2 o 3 . The preparation method comprises the following steps: uniformly mixing aluminum oxide or a mixture of aluminum oxide and titanium oxide with squid powder, adding an organic polymer pore-forming agent, a binder and deionized water, kneading, extruding, drying, and heat treatment at high temperature. The arsenic removal agent carrier is obtained; the arsenic removal agent carrier is subjected to hydrothermal treatment to expand pores to obtain arsenic removal agent modified carrier; the active component nickel salt is dissolved in one or more of citric acid, ammonia water and deionized water, Prepare a stable active metal complex solution, and then impregnate the modified carrier of the arsenic removal agent with the active metal complex solution to obtain a finished product of the arsenic removal agent. The arsenic removal agent is used for the arsenic removal of catalytic gasoline with high olefin content, and has strong carbon capacity, high arsenic removal activity (arsenic removal rate above 90%), good arsenic removal selectivity (above 99%), and no loss of octane number .

Description

technical field [0001] The present invention relates to a gasoline dearsenic agent and a preparation method thereof, in particular to a dearsenic agent with abundant mesopores for catalytic gasoline dearsenic, more specifically a dearsenic agent for catalytic gasoline or heavy gasoline It is a hydrogen dearsenic agent with abundant mesopores for raw material dearsenization, which will not cause olefin saturation and octane number loss in gasoline during the dearsenic process. Background technique [0002] Hydrogenation technology is one of the main methods to clean gasoline in my country. Refining companies generally use hydrogenation technology to reduce the sulfur content in gasoline. However, arsenic compounds in raw oil are toxic substances in the hydrogenation process, and a very small amount of arsenic compounds will cause permanent poisoning and deactivation of the hydrogenation catalyst, shorten the long-term operation period of the device, and bring greater economic...

Claims

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Application Information

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IPC IPC(8): B01J20/08B01J20/30C10G25/00
CPCB01J20/0225B01J20/0248B01J20/08C10G25/003C10G2300/202C10G2400/02
Inventor 鞠雅娜刘坤红兰玲钟海军胡亚琼葛少辉吕忠武张学军李天舒冯琪赵秦峰李阳姜增坤康洪敏侯远东朴佳锐孙洪磊霍明辰
Owner PETROCHINA CO LTD
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