Reformed raw oil desulfurizing agent and preparation method thereof
A technology of desulfurizer and raw oil, applied in the field of desulfurization of oil products, can solve the problems of low radial crushing strength, complex production process, short service life, etc., and achieve non-brittleness or even pulverization, low bulk density, high strength Improved effect
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Embodiment 1
[0027] The reformed raw oil desulfurizer in this embodiment is made of the following raw materials in mass percentage: CuO25%, NiO25%, ZnO15%, carrier 35%, and the carrier is aluminate cement or / and ordinary Portland cement. Examples The carrier is preferably CA-60 aluminate cement, and the ternary active components CuO, NiO and ZnO are preferably respectively: CuO is obtained from basic copper carbonate after roasting for 1 hour at a temperature of 500 ° C and air circulation conditions. Decomposition products; NiO comes from the roasted product obtained after roasting nickel carbonate at a temperature of 500 °C and air circulation for 2 h, and ZnO comes from the roasted product obtained after roasting zinc carbonate at a temperature of 500 °C and air circulation for 1.5 h product
[0028] The preparation method of the reformed stock oil desulfurizer of the present embodiment comprises the following steps:
[0029] Step 1, taking CuO, NiO, ZnO and carrier by mass percentage ...
Embodiment 2
[0034] The reformed raw oil desulfurizer of this embodiment is made of the following raw materials in mass percentage: CuO 25%, NiO 25%, ZnO 15%, carrier 35%, and the carrier is aluminate cement or / and ordinary portland cement The carrier of this embodiment is preferably 42.5# ordinary Portland cement, and the ternary active components CuO, NiO and ZnO are preferably respectively: CuO comes from the roasted copper carbonate obtained after roasting for 2 hours under the condition of 500 ° C and air circulation. Decomposition products, NiO is obtained from the roasted product of basic nickel carbonate at a temperature of 500 °C and air circulation for 1.5 h, and ZnO is obtained from zinc carbonate after roasting at a temperature of 500 °C and air circulation for 1 h baked product.
[0035] The preparation method of the reformed stock oil desulfurizer of the present embodiment comprises the following steps:
[0036] Step 1, taking CuO, NiO, ZnO and carrier by mass percentage and...
Embodiment 3
[0041] The reformed raw oil desulfurizer of this embodiment is made of the following raw materials in mass percentage: CuO 10%, NiO 30%, ZnO 5%, carrier 55%, and the carrier is aluminate cement or / and ordinary Portland cement, The carrier in this example is preferably a mixture obtained by mixing CA-50 aluminate cement and 42.5# ordinary Portland cement at a mass ratio of 1:1, and the ternary active components CuO, NiO and ZnO are respectively preferably: CuO comes from basic Copper carbonate was roasted for 2 hours at a temperature of 450°C with air circulation. NiO was obtained from basic nickel carbonate roasted for 1.5 hours at a temperature of 520°C with air circulation. ZnO It comes from the roasted product obtained after roasting basic zinc carbonate at a temperature of 520°C and air circulation for 1 hour.
[0042] The preparation method of the reformed stock oil desulfurizer of the present embodiment comprises the following steps:
[0043] Step 1, taking CuO, NiO, Zn...
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