Method for producing catalyst carrier material applicable to high-temperature environment
A catalyst carrier and high-temperature environment technology, which is applied in the direction of catalyst carriers, chemical instruments and methods, physical/chemical process catalysts, etc., can solve problems such as poor high-temperature thermal stability, achieve high-temperature performance improvement, increase high-temperature specific surface area and high-temperature thermal stability performance, good catalytic effect
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Embodiment 1
[0032] 1) Preparation of feed liquid:
[0033] Aluminum hydroxide and the sodium hydroxide that mass percent concentration is 35% are added in the reaction kettle and stirred and heated to boiling, and keep boiling state for 40 minutes, until aluminum hydroxide dissolves completely, then add pure water to adjust the [Al 2 o 3 ]=200g / l, [OH-]=6.0mol / L, filter after being cooled to 20~25 ℃, finish the preparation of sodium metaaluminate feed liquid; The feed molar ratio of described aluminum hydroxide and sodium hydroxide is 1 : 1.5;
[0034] Add silica sol and nitric acid to the reaction kettle and stir, add pure water to adjust the [H + ]=3.0mol / L, [SiO 2 ]=45.0g / l, complete the preparation of acidic silica sol feed liquid; The weight ratio of described silica sol and nitric acid is 1: 4.5, and the concentration of described nitric acid is 8mol / l, the silica quality in described silica sol The percentage content is 22%.
[0035] 2) Continuous precipitation:
[0036] Firs...
Embodiment 2
[0046] 1) Preparation of feed liquid:
[0047] Aluminum hydroxide and the sodium hydroxide that mass percent concentration is 32% are added in the reaction kettle and stirred and heated to boiling, and keep boiling state for 35 minutes, until aluminum hydroxide dissolves completely, then add pure water to adjust the [Al 2 o 3 ]=180g / l, [OH - ]=5.0mol / L, after being cooled to 30~35 ℃, filter, and complete the preparation of sodium metaaluminate feed liquid; The molar ratio of described aluminum hydroxide and sodium hydroxide is 1: 1.5;
[0048] Add silica sol and nitric acid to the reaction kettle and stir, add pure water to adjust the [H + ]=2.0mol / L, [SiO 2 ]=30.0g / l, complete the preparation of acidic silica sol feed liquid; The weight ratio of described silica sol and nitric acid is 1: 4, and the concentration of described nitric acid is 9mol / l, the silica quality in described silica sol The percentage content is 23%.
[0049] 2) Continuous precipitation:
[0050] First...
Embodiment 3
[0060] 1) Preparation of feed liquid:
[0061] Aluminum hydroxide and the sodium hydroxide that mass percentage concentration is 37% are added in the reaction kettle and stirred and heated to boiling, and keep boiling state for 50 minutes, until aluminum hydroxide dissolves completely, then add pure water to adjust the [Al 2 o 3 ]=220g / l, [OH - ]=7.0mol / L, filter after cooling to 30~35 ℃, complete the preparation of sodium metaaluminate feed liquid; The molar ratio of described aluminum hydroxide and sodium hydroxide is 1: 1.5;
[0062] Add silica sol and nitric acid to the reaction kettle and stir, add pure water to adjust the [H + ]=4.0mol / L, [SiO 2 ]=60.0g / l, complete the preparation of acidic silica sol feed liquid; The weight ratio of described silica sol and nitric acid is 1: 5, and the concentration of described nitric acid is 7mol / l, the silica quality in described silica sol The percentage content is 22%.
[0063] 2) Continuous precipitation:
[0064] First add ...
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