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Catalyst filling material for selective hydrogenation

A hydrogenation catalyst, catalyst technology, applied in the direction of selective hydrorefining, physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, etc., can solve the problem of affecting reaction efficiency, manufacturing and installation difficulties, cost Advanced problems, to achieve the effect of improving reaction efficiency, avoiding workload, and avoiding the influence of mass transfer

Active Publication Date: 2006-11-29
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] The catalytic distillation element used in the method is complex in structure, difficult to manufacture and install, and high in cost, and because the catalyst is wrapped, the reactants and products must be diffused to contact or leave the catalyst, which also affects the reaction efficiency

Method used

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  • Catalyst filling material for selective hydrogenation

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] Pseudo-boehmite is dehydrated at 700°C for 0.5 seconds, and the powder after dehydration is mixed with 5.0% by weight of citric acid, 2.5% by weight of nitric acid and 1.0% by weight of kale powder, and is mixed with a molding machine (model is B3705, produced by American Bonnot Company, the same below) made of 4mm×4mm×1mm (diameter×height×thickness) Raschig ring random packing, then dried at 120°C, and then roasted in dry air at 450°C for 4 hours. filler carrier.

[0029] The calcined filler carrier was prepared with LiNO 3 The solution was immersed for 1 hour, dried at 120°C for 4 hours, and then baked at 900°C for 4 hours; then the prepared Ni(NO 3 ) 2 The solution was soaked for 4 hours, dried at 120° C. for 4 hours, and then calcined at 450° C. for 4 hours to prepare the selective hydrogenation catalyst packing. The composition and properties of the catalyst packing are listed in Table 1.

[0030] The catalyst packing is installed in the reaction section in the...

Embodiment 2

[0032] Dehydrate pseudo-boehmite at 700°C for 0.5 seconds, add 2.5% by weight of citric acid, 5.0% by weight of nitric acid and 1.5% by weight of kale powder to the dehydrated powder, mix evenly, and use a molding machine to make 4mm × 4mm×1mm (diameter×height×thickness) θ-ring bulk packing, then dried at 120°C, and then calcined in dry air at 450°C for 4 hours to obtain a filler carrier.

[0033] The calcined filler carrier was prepared with LiNO 3 The solution was immersed for 1 hour, dried at 120°C for 4 hours, and baked at 900°C for 4 hours; then the prepared Ni(NO 3 ) 2 The solution was soaked for 4 hours, dried at 120°C for 4 hours, and calcined at 450°C for 4 hours to prepare the selective hydrogenation catalyst packing. The composition and properties of the catalyst packing are listed in Table 1.

[0034] The catalyst packing is installed in the reaction section in the middle of the catalytic distillation tower with a diameter of 32 mm, and the loading amount is 100...

Embodiment 3

[0036] Dehydrate pseudo-boehmite at 700°C for 0.5 seconds, add 4.0% by weight of citric acid, 5.0% by weight of nitric acid and 1.0% by weight of kale powder to the dehydrated powder and mix evenly, and use a molding machine to make a corrugated board The structured packing was then dried at 120°C and then calcined in dry air at 450°C for 4 hours to obtain a filler carrier.

[0037] The calcined filler carrier was prepared with LiNO 3 The solution was immersed for 1 hour, dried at 120°C for 4 hours, and calcined at 900°C for 4 hours; then the prepared Ni(NO 3 ) 2 The solution was soaked for 4 hours, dried at 120° C. for 4 hours, and calcined at 450° C. for 4 hours to prepare the selective hydrogenation catalyst packing. The composition and properties of the catalyst packing are listed in Table 1.

[0038] The catalyst packing is installed in the reaction section in the middle of the catalytic distillation tower with a diameter of 32 mm, and the loading amount is 100 grams. ...

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Abstract

Disclosed is a selective hydrogenation catalyst filler, which comprises 5-25 wt% of nickel oxide, 0.1-2.0 wt% of lithium or alkali earth metal and balancing aluminum oxide, wherein the catalyst is in the form of bulk grid filler or corrugated plate type filler form. The reaction rate of the catalyst can be improved.

Description

technical field [0001] The invention relates to a selective hydrogenation catalyst packing. More specifically, it is a catalyst capable of both selective hydrogenation and as a filler. Background technique [0002] In the field of petrochemical industry, olefins produced during high temperature steam cracking, catalytic cracking or thermal cracking all contain certain dienes and alkynes, and these dienes and alkynes need to be reduced to a certain concentration in further processing and utilization It is also required to ensure that olefins are not lost and to improve the utilization of resources. At the same time, with the improvement of gasoline fuel standards in China, and because the use of MTBE is banned to a certain extent, the most promising process is alkylation and butylation to increase gasoline octane number and reduce gasoline Reid vapor pressure (RVP). ene dimerization. Both FCC and steam cracked butene can be used as raw materials for...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/755B01J19/30C10G45/36C10G45/00
Inventor 渠红亮姜蕾毛俊义王少兵张占柱孙连霞
Owner CHINA PETROLEUM & CHEM CORP