Catalyst for coal-to-natural gas high-temperature methanation and preparation method thereof
A methanation catalyst and coal-to-natural gas technology, which is applied in catalyst activation/preparation, physical/chemical process catalyst, catalyst carrier, etc., can solve the problems of low thermal stability of methanation catalyst, low thermal stability of catalyst, etc. The effect of improving methanation activity and thermal stability, strong ability to store and release oxygen, and large heat resistance
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Embodiment 1
[0028] Embodiment 1 prepares high-temperature methanation catalyst I
[0029] (1) 2L containing 25.23g Ce(NO 3 ) 3 ·6H 2 O, 257.44g Al(NO 3 ) 3 9H 2 O and 28.51g Zr(NO 3 ) 4 The mixed aqueous solution was added to the constant temperature reaction kettle, the reaction temperature was controlled at 70°C, and 8% Na was added under the condition of electric stirring. 2 CO 3 Aqueous solution, adjust the pH value to 8.5, after constant temperature reaction for 2 hours, the slurry is washed and filtered, dried at 80°C for 8 hours, and calcined at 450°C for 6 hours to obtain CeO 2 -Al 2 o 3 -ZrO 2 Composite carrier.
[0030] (2) The above CeO 2 -Al 2 o 3 -ZrO 2 The composite carrier was dispersed in 0.5L containing 116.79g Ni(NO 3 ) 2 ·6H 2 O, 29.51g Ca(NO 3 ) 2 4H 2 O and 31.57g Cr(NO 3 ) 3 9H 2 In the nitrate solution of O, soak at 50°C for 6h, then raise the temperature to 80°C, and evaporate the slurry to dryness.
[0031] (3) The evaporated material was...
Embodiment 2
[0032] Example 2 Preparation of High Temperature Methanation Catalyst II
[0033] (1) 2L containing 30.28g Ce(NO 3 ) 3 ·6H 2 O, 183.88g Al(NO 3 ) 3 9H 2 O and 35.76g Zr(NO 3 ) 4 The mixed aqueous solution was added to the constant temperature reaction kettle, the reaction temperature was controlled at 75 ° C, and 10% Na was added under the condition of electric stirring. 2 CO 3 Aqueous solution, adjust the pH value to 8.0, after constant temperature reaction for 1.5h, the slurry is washed and filtered, dried at 80°C for 8h, and calcined at 500°C for 5h to obtain CeO 2 -Al 2 o 3 -ZrO 2 Composite carrier.
[0034] (2) The above CeO 2 -Al 2 o 3 -ZrO 2 The composite carrier was dispersed in 0.5L containing 136.25g Ni(NO 3 ) 2 ·6H 2 O, 44.87 Mg(NO 3 ) 2 ·6H 2 O and 31.57g Cr(NO 3 ) 3 9H 2 In the nitrate solution of O, soak at 60°C for 5h, then raise the temperature to 90°C, and evaporate the slurry to dryness.
[0035] (3) The evaporated material was dried...
Embodiment 3
[0036] Example 3 Preparation of High Temperature Methanation Catalyst III
[0037] (1) 2L containing 20.19g Ce(NO 3 ) 3 ·6H 2 O, 220.66g Al(NO 3 ) 3 9H 2 O and 33.01g Zr(NO 3 ) 4 The mixed aqueous solution was added to the constant temperature reactor, the reaction temperature was controlled at 75°C, and 12% Na was added under the condition of electric stirring. 2 CO 3 Aqueous solution, adjust the pH value to 8.5, after constant temperature reaction for 2 hours, the slurry is washed and filtered, dried at 80°C for 8 hours, and calcined at 500°C for 5 hours to obtain CeO 2 -Al 2 o 3 -ZrO 2 Composite carrier.
[0038] (2) The above CeO 2 -Al 2 o 3 -ZrO 2 The composite carrier was dispersed in 0.5L containing 97.32g Ni(NO 3 ) 2 ·6H 2 O, 51.28g Mg(NO 3 ) 2 ·6H 2 O and 17.68g Mn(NO 3 ) 2 4H 2 In the nitrate solution of O, soak at 40°C for 6h, then raise the temperature to 85°C, and evaporate the slurry to dryness.
[0039] (3) The evaporated material was d...
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