Method for preparing hydrogenation catalyst
A hydrogenation treatment and catalyst technology, applied in the direction of catalyst activation/preparation, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problems of atomic ratio mismatch, reduced catalyst activity, metal loss, etc., and achieve simple preparation process , Avoid metal loss, low production cost
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Embodiment 1
[0029] The method of the invention prepares the catalyst.
[0030] (1) According to Chinese patent 96109048, a high-concentration molybdenum-nickel solution is prepared, and the solution contains
[0031] MoO 3 70g / 100mL, NiO18g / 100mL, P2.55g / 100mL.
[0032] (2) Take 60mL of the solution obtained in step 1, add 32g of ammonium metatungstate (containing WO 3 85%), fully dissolved.
[0033] (3) 16.5g (dry basis) of SB-alumina powder (produced in Germany) was fully mixed with the solution obtained in step 2, and extruded into a catalyst precursor.
[0034] (4) Dry the catalyst precursor obtained in step 3 at 120° C. in air for 4 hours.
[0035] (5) Treat the catalyst dry strip obtained in step 4 under the catalyst at 350° C. for 1 hour.
[0036]The prepared catalyst is denoted as catA. The catalyst contains 10.8w% NiO, 42.0w% MoO 3 and 27.2w% WO 3 , 3.5w%P 2 o 5 .
Embodiment 2
[0038] The method of the invention prepares the catalyst.
[0039] (1) Prepare high-concentration molybdenum-nickel solution according to Chinese patent 96109048, which contains MoO 3 60g / 100mL, NiO12g / 100mL, P2g / 100mL.
[0040] (2) Fully mix 15g (dry basis) of SB-alumina powder (produced in Germany) with 110mL of the solution obtained in step 2.
[0041] (3) The mixture obtained in step 4 was dried at 80° C. to 40% on a dry basis, and extruded into a catalyst precursor.
[0042] (4) With embodiment 1 step 4.
[0043] (5) With embodiment 1 step 5.
[0044] The prepared catalyst is denoted as catB. The catalyst contains 13.2w% NiO, 66.0w% MoO 3 and 5.0w%P 2 o 5 .
Embodiment 3
[0046] The method of the invention prepares the catalyst.
[0047] (1) Take 100mL of clean water, add ammonium metatungstate (containing WO 3 85%) 44.7g, nickel nitrate 37.5g, fully dissolved, adding molybdenum oxide 30g. The volume of the final suspension was 120 mL.
[0048] (2) Fully mix 20g (dry basis) of SB-alumina powder (produced in Germany) with the suspension obtained in step 2.
[0049] (3) The mixture obtained in step 2 was dried at 80° C. to 40% on a dry basis, and extruded into a catalyst precursor.
[0050] (4) With embodiment 1 step 4.
[0051] (5) with embodiment 1 step 5.
[0052] The prepared catalyst is denoted as catC. The catalyst contains 12.0w% NiO, 30.0w% MoO 3 and 38.0w% WO 3 .
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