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A catalytic cracking regenerated flue gas sulfur transfer additive and its preparation method

A technology of sulfur transfer aid and regenerating flue gas, applied in chemical instruments and methods, physical/chemical process catalysts, separation methods, etc., can solve the problems of complex preparation process, aggravate catalyst metals, poisoning, etc., and achieve high SOx removal. rate, improve wear resistance, improve the effect of specific surface area

Active Publication Date: 2017-01-18
天津市瑞萦德达环保科技有限公司
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  • Application Information

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Problems solved by technology

[0004] In the technology disclosed in the above-mentioned patents, although the liquid sulfur transfer aid is simple to prepare and easy to use, in recent years, the increasingly heavy and inferior quality of catalytic cracking raw materials has increased the amount of heavy metal deposition on the catalytic cracking balancer. Depositing a certain amount of liquid sulfur transfer additive active metal on the balancer will often aggravate the metal poisoning of the catalyst, resulting in a decrease in catalyst activity and poor selectivity, and 50-60% of the sulfur transfer activity is difficult to meet the increasingly stringent environmental protection requirements Require
In solid sulfur transfer aids, whether it is the early alumina carrier loaded active components, or the more popular aluminum-magnesium spinel or hydrotalcite-like carrier loaded active metals in recent years, there are complex preparation processes, MgO content and Low specific surface area of ​​additives, containing metals that are toxic to catalytic cracking catalysts, such as alkali metals and transition metal vanadium, etc.

Method used

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  • A catalytic cracking regenerated flue gas sulfur transfer additive and its preparation method
  • A catalytic cracking regenerated flue gas sulfur transfer additive and its preparation method
  • A catalytic cracking regenerated flue gas sulfur transfer additive and its preparation method

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preparation example Construction

[0018] The preparation method of the catalytic cracking regenerated flue gas sulfur transfer aid comprises the following specific steps:

[0019] (1) described co-precipitation method makes magnesium aluminum spinel (MgAl 2 o 4 ) is to add the mixed solution of magnesium salt and aluminum salt dropwise to the mixed solution of sodium hydroxide and sodium carbonate at 50-70°C, the dropping time is 0.2-0.5 hours, and the pH value of the solution is controlled at 8-10 After the dropwise addition, continue to stir for 4-15 hours to nucleate and crystallize, then cool, filter, and wash until neutral to obtain magnesium-aluminum spinel (MgAl 2 o 4 ). The molar ratio of the two metal oxides of magnesium and aluminum varies within the following range: 1.0-5.0:1.0. The concentration of sodium hydroxide and sodium carbonate is 2.5-5.5mol / L, 0.15-0.2 5mol / L. The two mixed solutions were reacted in equal volumes.

[0020](2) Manganese-magnesium-aluminum hydrotalcite (MnMgAl-LDH) is ...

Embodiment 1

[0024] The first step of preparation of Al-Mg spinel (MgAl 2 o 4 )

[0025] Add 2500gH in a 5-liter three-neck flask 2 O, 114g NaOH and 44.5g Na 2 CO 3 , Stir well at 65°C, add 1500gH 2 O, 108.5gMg(NO 3 ) 2 .6H 2 O, 93.5gAl(NO 3 ) 3 .9H 2 O, the dropwise addition time is 0.6h, after the dropwise addition, continue to stir to nucleate and crystallize for 15h, then cool, filter with suction, and wash until neutral to obtain magnesia-aluminum spinel A 1 .

[0026] The second step of preparation of manganese magnesium aluminum hydrotalcite (MnMgAl-LDH)

[0027] Add 2500gH in a 5-liter three-neck flask 2 O, 126gNaOH and 53.0gNa 2 CO 3 , Stir evenly at 75°C, add 1500gH 2 O, 7.5gMn(NO 3 ) 2 4H 2 O, 285.0gMg(NO 3 ) 2 .6H 2 O, 123.5gAl(NO 3 ) 3 .9H 2 O solution, the dropwise addition time is 0.7h, after the dropwise addition, continue to stir to nucleate and crystallize for 18h, then cool, suction filter, and wash until neutral to obtain hydrotalcite-like B 1 ...

Embodiment 2

[0031] The first step of preparation of Al-Mg spinel (MgAl 2 o 4 )

[0032] Add 2500gH in a 5-liter three-neck flask 2 O, 114g NaOH and 44.5g Na 2 CO 3 , Stir well at 65°C, add 1500gH 2 O, 120.5gMg(NO 3 ) 2 .6H 2 O, 93.5gAl(NO 3 ) 3 .9H 2 O, the dropwise addition time is 0.6h, after the dropwise addition, continue to stir to nucleate and crystallize for 15h, then cool, filter with suction, and wash until neutral to obtain magnesia-aluminum spinel A 2 .

[0033] The second step of preparation of manganese magnesium aluminum hydrotalcite (MnMgAl-LDH)

[0034] Add 2500gH in a 5-liter three-neck flask 2 O, 126gNaOH and 53.0gNa 2 CO 3 , Stir evenly at 75°C, add 1500gH 2 O, 9.5gMn(NO 3 ) 2 4H 2 O, 245.0gMg(NO 3 ) 2 .6H 2 O, 123.5gAl(NO 3 ) 3 .9H 2 O solution, the dropwise addition time is 0.7h, after the dropwise addition, continue to stir to nucleate and crystallize for 18h, then cool, suction filter, and wash until neutral to obtain hydrotalcite-like B 2 ...

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Abstract

The invention discloses a sulfur-transferring additive for regenerative flue gas in catalytic cracking and a preparation method thereof and particularly relates to a high-efficiency sulfur transferring agent adopting aluminium-magnesium spinels and hydrotalcite-like compounds as carriers. The preparation method comprises the following steps: with magnesium and aluminium as active components, adopting a coprecipitation method to prepare the aluminium-magnesium spinels (MgAl2O4); with manganese, magnesium and aluminium as the active components, adopting the coprecipitation method to prepare zinc-magnesium-aluminium hydrotalcites (MnMgAl-LDH); with rare-earth cerium as the active component and copper as a desorbing active component, adding aluminum sol to form uniform slurry, spraying, forming, drying and roasting to obtain the sulfur-transferring additive. The sulfur-transferring additive and the preparation method disclosed by the invention have the advantages that the content of MgO in the additive is high; pseudo-boehmites are acidified, and the aluminium sol is added, so that the wear resistance of the additive is improved; the additive contains the pseudo-boehmites and the manganese-magnesium-aluminium hydrotalcites, so that the specific surface area of the additive is enlarged; and the additive does not contain harmful components such as vanadium and iron for the catalytic cracking, so that the obtained sulfur transferring agent for FCC regenerative flue gas has higher SOx removing rate and better regenerative performance.

Description

technical field [0001] The invention relates to a catalytic cracking regenerated flue gas sulfur transfer additive and a preparation method thereof, in particular to a high-efficiency sulfur transfer agent with aluminum-magnesium spinel and a hydrotalcite-like compound as a carrier and a preparation method thereof. Background technique [0002] Fluid catalytic cracking (FCC) is the main secondary processing process of light oil products in refineries. While producing a large amount of high-quality light oil products, a certain amount of SOx will be emitted from the regeneration flue gas. It will pollute the environment and cause corrosion of the device. It is estimated that the SOx emission in the FCC regeneration flue gas accounts for about 6%-7% of the SOx emission in the air. The main methods to reduce SOx emissions in FCC regenerators are: 1. flue gas scrubbing; 2. raw oil hydrogenation; 3. using sulfur transfer agent. Since the use of sulfur transfer agent requires al...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/889B01D53/86B01D53/50
Inventor 张伟
Owner 天津市瑞萦德达环保科技有限公司