Preparation method for trans-1,4-cyclohexanedimethanol, and catalyst used therefor
A technology of cyclohexanedimethanol and its production method, which is applied in the field of trans-1,4-cyclohexanedimethanol production and its catalyst, and can solve the problem of low selectivity
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Embodiment 1
[0013] Pretreatment of the carrier: reflux the activated carbon in a solution containing 35wt% nitric acid at 65°C for 3h. After the end, fully wash with deionized water until neutral, and then dry it in a vacuum oven at a constant temperature of 80°C for 12h, ready to use.
[0014] Catalyst preparation: First, weigh the corresponding mass of SnCl according to the Sn loading in the Pd-Pt-Sn-Cu / C catalyst is 3wt% and the Sn / Cu molar ratio is 1 2 and CuCl 2 And dissolve it in hydrochloric acid aqueous solution to form an impregnating liquid, mix the obtained impregnating liquid with 50 g of the above-mentioned pretreated activated carbon, impregnate for 12 h, filter, and dry at 120 ° C for 3 h to obtain the catalyst precursor I, and then follow the Pd-Pt- The content of Pt in the Sn-Cu / C catalyst is 1wt%, and the Pd-Pt heterobinuclear complex [PdPtCl 2 (PPh 2 py)] and dissolved in chloroform solution to form an impregnating solution, the resulting impregnating solution was mix...
Embodiment 2-5
[0016] The loading of Pt in the catalyst was changed without changing the Pd-Pt heterobinuclear complex, and the rest of the operations were the same as in Example 1. The Pt content in the catalyst obtained in each example is shown in Table 1.
Embodiment 6-14
[0018] The loading of Pt in the catalyst was not changed, but the Pd-Pt heterobinuclear complex was changed, and the remaining operations were the same as in Example 3. The Pd-Pt heterobinuclear complexes used in each example and the Pt content in the obtained catalyst are shown in Table 1.
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