Catalyst capable of directly loading reactive metals on metallic packing

A metal filler, active metal technology, applied in the direction of metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, organic chemistry, etc., can solve the problems of complex operation, structural limitation of metal components, etc. The effect of simplicity, high utilization rate and simple and easy preparation method

Active Publication Date: 2018-01-12
HEBEI UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the above method can directly support active metals on the surface of metal materials, this process needs to be completed with the help of supported catalysts. The treatment process requires filtration and separation of catalysts, which is not only complicated to operate, but also has great restrictions on the structure of the metal components to be processed. , only applicable to reactor metal walls, stirring paddles, thermocouple sleeves, cooling coils, and a small number of component types that can be attached to metal baffles, metal tubes, and wire mesh, and the load type used after treatment needs to be solved Recovery and Utilization of Catalyst Active Metals

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] In the first step, put 4L of stainless steel θ ring packing with a specification of 3×3mm into a tubular fixed-bed reactor with a diameter of 100mm and a height of 600mm, and the specific surface area of ​​the packing is 2800m 2 / m 3 , the bulk density is 460kg / m 3 ;

[0021] The second step is to replace the treatment device and pipeline system with nitrogen for 8 to 12 minutes;

[0022] In the third step, chloroplatinic acid and water are mixed and prepared into 150L platinum chloroplatinic acid solution with a platinum concentration of 0.8ppm and put into the solution storage tank as a treatment solution;

[0023] In the fourth step, pump the treatment liquid in the solution storage tank of the third step at a space velocity of 100h -1 Put it into the preheater, the temperature of the preheater is 80°C, and then the space velocity is 500h -1 , The nitrogen-hydrogen mixed gas with a nitrogen-hydrogen ratio of 10:1 is mixed and enters the first step reactor and act...

Embodiment 2

[0025] In the first step, put 4L of 2×2mm stainless steel θ-ring filler into a tubular fixed-bed reactor with a diameter of 100mm and a height of 600mm, and the specific surface area of ​​the filler is 3700m 2 / m 3 , the bulk density is 576kg / m 3 ;

[0026] The second step is to replace the treatment device with nitrogen for 8 to 12 minutes;

[0027] The 3rd step, chloroplatinic acid and water are mixed and prepared into 150L platinum concentration and are the chloroplatinic acid solution of 1.0ppm and put into the solution storage tank as treatment liquid;

[0028] In the fourth step, pump the treatment liquid in the solution storage tank of the third step at a space velocity of 100h -1 Put it into the preheater, the temperature of the preheater is 80°C, and then the space velocity is 500h -1 , The nitrogen-hydrogen mixed gas with a nitrogen-hydrogen ratio of 10:1 is mixed and then enters the reactor of the first step. The temperature of the reactor is 80°C and the pressu...

Embodiment 3

[0030] In the first step, put 4L zirconium orifice corrugated packing into a tubular fixed-bed reactor with a diameter of 100mm and a height of 600mm, and the specific surface area of ​​the packing is 501m 2 / m 3 , the bulk density is 325kg / m 3 ;

[0031] The second step is to replace the treatment device with nitrogen for 8 to 12 minutes;

[0032] In the third step, chloroplatinic acid and water are mixed and prepared into 150L platinum chloroplatinic acid solution with a platinum concentration of 0.5ppm and put into the solution storage tank as a treatment solution;

[0033] In the fourth step, pump the treatment liquid in the solution storage tank of the third step at a space velocity of 100h -1 Put it into the preheater, the temperature of the preheater is 150°C, and then the space velocity is 500h -1 1. The nitrogen-hydrogen mixed gas with a nitrogen-hydrogen ratio of 10:1 is mixed and then enters the reactor of the first step and acts on the surface of the filler. The ...

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Abstract

The invention discloses a catalyst capable of directly loading reactive metals on metallic packing. The catalyst is prepared by the following method, and the method comprises the following steps: 1, filling the metallic packing into a reactor, wherein the filling volume of the packing is 80-90% of the volume of the reactor, and replacing a treatment device and a pipeline system with nitrogen; 2, pumping a treatment solution in a solution storage tank into a preheater by a pump, enabling the solution to enter the reactor in the first step, condensing the gas exhausted from the reactor and emptying, collecting the discharged liquid into the solution storage tank to serve as the treatment solution to continuously participate in treatment; continuously treating for 1-2 hours in the reactor, thereby obtaining the reactive metal/metallic packing catalyst. The catalyst prepared by the method disclosed by the invention is high in reactive metal utilization rate, the heat and mass transfer superficial area is large, the resistance is low, and any inner-diffusion effect is avoided in the reaction process.

Description

technical field [0001] The invention belongs to the field of catalytic reactions, in particular to a catalyst directly supporting active metals on metal fillers. Background technique [0002] Supported metal catalysts are an important class of industrial catalysts, widely used in many important reaction processes in the chemical industry. It is usually supported by porous oxides with high specific surface area. Due to the internal diffusion process of porous oxide supports, the heterogeneous catalytic reaction rate will be reduced and the selectivity will be poor. Usually, reducing the particle size of the catalyst and increasing the pore volume and pore diameter of the catalyst are used to increase the effective factor of internal diffusion and reduce the influence of internal diffusion, but it will increase the pressure drop of the catalyst bed, reduce the mechanical strength, and reduce the specific surface, etc. Other issues affecting catalytic efficiency. On the othe...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/42B01J23/44B01J23/46B01J23/52B01J23/755B01J23/89C07C209/36C07C211/46
Inventor 王淑芳关聪聪任小亮王延吉张东升
Owner HEBEI UNIV OF TECH
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