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Preparation method of ruthenium-base ammonia synthetic catalyst

A kind of ammonia synthesis and catalyst technology, which is applied in the field of preparation of high-activity new ammonia synthesis catalyst, can solve the problems of low activity and poor stability, achieve high activity, improve dispersion, and improve metal surface utilization

Inactive Publication Date: 2007-05-02
XIAMEN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The object of the present invention is to provide a kind of preparation method of novel ruthenium-based ammonia synthesis catalyst for the problems of its low activity and poor stability of the existing loaded-type nail-based ammonia synthesis catalyst, which catalyst (with hydrogen and nitrogen as raw materials In the production process of synthetic ammonia) has a higher activity of nitrogen and hydrogen into ammonia and better stability

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] 2g nano magnesium oxide and 0.21g RuCl 3 ·nH 2 O was added to 50ml of hexanediol solution, heated to 180°C in an oil bath, stirred for 1.5h, then immediately placed in an ice-water bath and stirred for 3h; stirred and evaporated to dryness at 160-250°C, and the organic solution was removed. The obtained solid powder was passed through hydrogen at 425°C for 12 hours to remove chloride ions. 0.15g KNO 3 Dissolve in about 20ml of hexanediol solution, put 1g of Ru / MgO into KNO 3 After impregnating in the hexanediol solution with stirring for 6 hours, evaporate to dryness with stirring at 160-250°C, and pass hydrogen gas through the obtained catalyst at 425°C for 3 hours to remove the remaining hexanediol. Take about 0.2 g of catalyst and place it in a reaction tube to measure its catalyst activity at a pressure of 0.2 MPa and a flow rate of 2100 ml / h. Catalyst KNO prepared by traditional method 3 -Ru / MgO-con was also prepared and evaluated under the same conditions. T...

Embodiment 2

[0032] 2.0g nano-magnesia and 0.21gRuCl 3 ·nH 2 O was added to 50ml of hexanediol solution, heated to 80°C in an oil bath, stirred for 2.5 hours, then immediately placed in an ice-water bath and stirred for 5 hours; stirred and evaporated to dryness at 160-250°C, and the organic solution was removed. The obtained solid powder was passed through hydrogen at 425°C for 12 hours to remove chloride ions. 0.15g KNO 3 Dissolve in about 20ml of hexanediol solution, put 1g of Ru / MgO into KNO 3 After impregnating in the hexanediol solution with stirring for 6 hours, stir and evaporate to dryness at 160-250° C., pass hydrogen gas through the obtained catalyst at 425° C. for 3 hours to remove the remaining hexanediol. Take about 0.2 g of catalyst and place it in a reaction tube to measure its catalyst activity at a pressure of 0.2 MPa and a flow rate of 2100 ml / h.

Embodiment 3

[0034] 2g nano magnesium oxide and 0.21g RuCl 3 ·nH 2O was added to 50ml of hexanediol solution, heated to 140°C in an oil bath, stirred for 0.5h, then immediately placed in an ice-water bath and stirred for 3h; stirred and evaporated to dryness at 160-250°C, and the organic solution was removed. The obtained solid powder was passed through hydrogen at 425°C for 12 hours to remove chloride ions. 0.15g KNO 3 Dissolve in about 20ml of hexanediol solution, put 1g of Ru / MgO into KNO 3 After impregnating in the hexanediol solution with stirring for 6 hours, evaporate to dryness with stirring at 160-250°C, and pass hydrogen gas through the obtained catalyst at 425°C for 3 hours to remove the remaining hexanediol. Take about 0.2 g of catalyst and place it in a reaction tube to measure its catalyst activity at a pressure of 0.2 MPa and a flow rate of 2100 ml / h. The results are shown in Table 2. The results show that the catalytic activity is the highest when the reduction tempera...

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Abstract

An Ru-based catalyst for synchronizing ammonia from H2 and N2 is composed of Ru as active center and metal oxide (MgO) as carrier, and is prepared through adding the aqueous solution of ammonia to the aqueous solution of magnesium nitrate, filtering to obtain Mg(OH)2 deposit, washing, baking, calcining, adding it to the solution of reducer, stirring, cooling in ice water bath, stirring while evaporating, filling H2 to obtain Ru / MgO, adding it along with nitrate of alkali metal (MNO3) to solvent, laying aside, stirring while evaporating, and filling H2.

Description

technical field [0001] The present invention relates to an ammonia synthesis catalyst, in particular to a method for preparing a highly active novel ammonia synthesis catalyst with ruthenium (Ru) as the active center and metal oxides such as magnesium oxide (MgO) as the carrier, suitable for hydrogen and nitrogen Ammonia synthesis reaction. Background technique [0002] At present, the problem of energy depletion has become a global concern and an urgent problem to be solved. Before alternative energy sources are found, reducing energy consumption has become an important means to slow down energy depletion and ensure sustainable economic development. The ammonia industry consumes a lot of energy, consuming about 1% of the world's energy every year. At present, the industrial ammonia synthesis catalysts used at home and abroad mainly use multi-promoted iron-based catalysts, usually made of selected magnetite and a series of additives with different contents (such as Al2O3 3...

Claims

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Application Information

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IPC IPC(8): B01J23/46B01J23/58B01J37/00C01C1/04
CPCY02P20/52
Inventor 廖代伟许清池林敬东符显珠杨振威
Owner XIAMEN UNIV