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Catalyst for ultralow temperature high activty ammonia synthesis

A catalyst, high activity technology, used in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, preparation/separation of ammonia, etc. There are no commercial reports of ammonia synthesis catalysts, which achieve the effects of excellent anti-toxicity, delayed grain growth, enhanced anti-wear and pressure-resistant mechanical properties

Inactive Publication Date: 2005-03-23
ZHEJIANG UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There are no commercial reports of ammonia synthesis catalysts with ferric oxide as the main component
In the existing various iron-based ammonia synthesis catalyst technologies, the cocatalysts are all metal oxides, and the catalytic activity and thermal stability at lower temperatures cannot fully meet the needs of industrial practical applications, and the development direction of ammonia synthesis catalysts is It is required to have higher catalytic activity at low temperature and low pressure, and finally realize the synthesis of ammonia at normal temperature and pressure. To achieve this goal, low temperature catalyst is the core technology. It is necessary to reduce the temperature and pressure used in today's industries and develop high activity catalysts at lower temperatures. , step by step towards normal temperature and pressure synthetic ammonia

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0013] Embodiment 1: (following component content is percentage by weight)

[0014] According to the ratio of selected magnetite powder 73.4, pure iron powder 19.1, potassium oxide 0.7, aluminum oxide 2.2, calcium oxide 2.5, titanium powder 0.4, strontium oxide, tungsten oxide and magnesium oxide mixture 1.7 ratio. First put the selected magnetite powder and pure iron powder in a mixer and mix them, then put the co-catalyst into the mixer and mix them for a certain period of time, evenly put them into an electric melting furnace, and melt them directly in the atmospheric environment without adjustment during the melting process Iron ratio, with a certain current consumption as the control melting end point. After melting, the liquid high-temperature magma is quickly discharged into the rapid cooling tank with a water jacket. After cooling, the solid melt is quickly broken and sieved, and the angle grinding is used to obtain the irregular granular products required by industry....

Embodiment 2

[0015] Embodiment 2: (following component content is percentage by weight)

[0016] According to the ratio of selected magnetite powder 72.0, pure iron powder 21.9, potassium oxide 0.6, aluminum oxide 3.1, calcium oxide 1.0, molybdenum powder 0.3, ruthenium powder 0.3, chromium oxide and magnesium oxide mixture 0.8. First put the selected magnetite powder and pure iron powder into the mixer and mix them, then put the co-catalyst into the mixer and mix them for a certain period of time. After they are uniform, take them out and put them in the melting furnace. The melting process and control are the same as Example 1. After melting, the high-temperature molten slurry is quickly discharged into the quick-cooling tank with a water jacket, and after cooling, it is broken, screened, and angled to form 1.5-3.0mm, 2.2-3.3mm, 3.3-4.7mm commonly used in industry mm, 4.7-6.7mm particle size catalyst. The sample Fe 2+ / Fe 3+ The value is 6.7, the ferrous oxide is 80.5, the ferric oxid...

Embodiment 3

[0017] Embodiment 3: (following component content is percentage by weight)

[0018] According to the ratio of selected magnetite powder 70.3, pure iron powder 24.4, potassium oxide 0.4, aluminum oxide 2.5, calcium oxide 1.0, tungsten powder 0.6, and mixture of zirconia and magnesium oxide 0.8. First put the magnetite powder and pure iron powder in the mixer and mix them, then put the co-catalyst into the mixing machine and mix them for a certain period of time, and put them into the electric melting furnace after they are evenly mixed, and melt them directly in the atmospheric environment without adjusting the iron ratio during the melting process , to control the melting end point with a certain current consumption. After melting, the liquid high-temperature magma is quickly discharged into the rapid cooling tank with a water jacket. After cooling, the solid melt is quickly broken and sieved, and the angle grinding is used to obtain the irregular granular products required by...

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Abstract

A super low-temperature high activity ammonia synthetic catalyst using ferrous oxide as main component, and using potassium oxide, aluminum oxide, calcium oxide as basic catalyst promoter, and also contains metals and other metallic oxide mixture which is prepared by the conventional molten method. The catalyst shows very high catalytic activity under low-temperature, it is easy to be deacidized, and possesses excellent heat-proof, antitoxin and mechanical property.

Description

Technical field: [0001] The invention belongs to an ammonia synthesis catalyst in the chemical industry, in particular to an ultra-low temperature and high activity ammonia synthesis catalyst. It is suitable for the preparation of ammonia synthesis catalyst, and the technical product is used in the synthesis of ammonia and the industry of producing pure hydrogen and nitrogen by ammonia cracking. Background technique: [0002] Before the present invention was made, the industrial ammonia synthesis catalysts all used iron oxide as the main component, and the iron oxide mainly included three kinds of ferric oxide, ferric oxide and ferrous oxide. In the catalyst of the same iron oxide, the main difference is the composition and content of the co-catalyst, which changes the performance of the catalyst, so the essential difference lies in the co-catalyst. There are no commercial reports of ammonia synthesis catalysts with ferric oxide as the main component. However, the ammonia ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/76B01J23/89C01C1/04
CPCY02P20/52
Inventor 胡樟能刘化章傅冠平
Owner ZHEJIANG UNIV OF TECH
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