Hydrogenation Catalyst for Preparation of Cyclohexylamine
A technology of hydrogenation catalyst and cyclohexylamine, which is applied in the direction of catalyst activation/preparation, physical/chemical process catalyst, amino compound preparation, etc., can solve the problems of low yield and selectivity of cyclohexylamine, and achieve outstanding technical effects Effect
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Embodiment 1
[0051] Modified carrier P / Al 2 o 3 Preparation of:
[0052] (1) Phosphoric acid (H 3 PO 4 ) aqueous solution 180ml impregnated in 1L diameter 6mm, pore volume is 0.92cm 3 / g, the specific surface area is 200cm 2 / g Al 2 o 3 , standing for 24 hours, and drying at 110° C. for 4 hours to obtain the carrier precursor I.
[0053] (2) Calcining the carrier precursor I at 630°C for 5h under a nitrogen gas atmosphere to obtain the modified carrier P / Al 2 o 3 .
[0054] The P content in the carrier was determined to be 1.48 g / L by ICP.
[0055] Preparation of hydrogenation catalyst:
[0056] (i) Cobalt ammonium sulfate containing 2.18g Co ((NH 4 ) 2 Co(SO 4 ) 2 ·6H 2 O) and 200ml of aqueous solution of lithium acetate (LiOAc) containing 1.88g Li is impregnated in P / Al 2 o 3 , to obtain catalyst precursor I;
[0057] (ii) drying at 110° C. for 4 hours to obtain the catalyst.
[0058] The Co content of the catalyst measured by ICP is 2.18g / L, and the Li content is 1.8...
Embodiment 2
[0063] Modified carrier P / Al 2 o 3 Preparation of:
[0064] (1) Phosphoric acid (H 3 PO 4 ) aqueous solution 180ml impregnated in 1L diameter 6mm, pore volume is 0.92cm 3 / g, the specific surface area is 200cm 2 / g Al 2 o 3 , standing for 24 hours, and drying at 110° C. for 4 hours to obtain the carrier precursor I.
[0065] (2) Calcining the carrier precursor I at 630°C for 5h under a nitrogen gas atmosphere to obtain the modified carrier P / Al 2 o 3 .
[0066] The P content in the carrier was determined to be 1.48 g / L by ICP.
[0067] Preparation of hydrogenation catalyst:
[0068] (i) Cobalt ammonium sulfate containing 2.18g Co ((NH 4 ) 2 Co(SO 4 ) 2 ·6H 2 O) and zinc citrate (Zn 3 (C 6 h 5 o 7 ) 2 2H 2 O) 200ml of aqueous solution impregnated in P / Al 2 o 3 , to obtain catalyst precursor I;
[0069] (ii) drying at 110° C. for 4 hours to obtain the catalyst.
[0070] The Co content of the catalyst was measured by ICP to be 2.18g / L, and the Zn content...
Embodiment 3
[0099] Modified carrier P / Al 2 o 3 Preparation of:
[0100] (1) Ammonium phosphate (NH 4 ) 3 PO 4 ) aqueous solution 180ml impregnated in 1L diameter 6mm, pore volume is 0.92cm 3 / g, the specific surface area is 200cm 2 / g Al 2 o 3 , standing for 24 hours, and drying at 110° C. for 4 hours to obtain the carrier precursor I.
[0101] (2) Calcining the carrier precursor I at 630°C for 5h under a nitrogen gas atmosphere to obtain the modified carrier P / Al 2 o 3 .
[0102] The P content in the carrier was determined by ICP to be 0.80 g / L.
[0103] Preparation of hydrogenation catalyst:
[0104] (i) Cobalt ammonium sulfate containing 2.18g Co ((NH 4 ) 2 Co(SO 4 ) 2 ·6H 2 O) and 200ml of aqueous solution of potassium acetate (KOAc) containing 1.88g K is impregnated in P / Al 2 o 3 , to obtain catalyst precursor I;
[0105] (ii) drying at 110° C. for 4 hours to obtain the catalyst.
[0106] The Co content of the catalyst was measured by ICP to be 2.18g / L, and the K...
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