Desulfurization and novel sorbents for same
An adsorbent and sulfur removal technology, applied in the field of desulfurization of cracked gasoline and diesel fuel fluid streams, can solve the problem of high cost of hydrogen consumption, and achieve the effects of avoiding octane number, avoiding significant drop, and reducing sulfur content
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Embodiment I
[0101] The reduced nickel metal solid adsorbent was produced as follows: 568 g of diatomaceous earth silica and 945 g of zinc oxide and 189 g of CaSO 4 Dry blending in the mill for 10 minutes produced the first mixture. With continued mixing, a solution containing 241 g of Dispersal alumina (Condea), 850 g of deionized water, and 26 g of glacial acetic acid was added to the mill to produce a second mixture. Mixing was continued for 25 minutes after addition of these components was complete. The second mixture was then dried at 300°F for 3 hours and fired at 1175°F for 1 hour to form a third mixture. The third mixture was then granulated using a Stokes Pennwalt granulator equipped with a 50 mesh screen. 50 g of the resulting granulated mixture was then impregnated with 37.1 g of the nickel nitrate hexahydrate composition dissolved in 11.7 g of hot deionized water to produce a first impregnated granule. The first impregnated particles were dried at 300°F for 1 hour and calcin...
Embodiment II
[0104] The desulfurization ability of the granular solid nickel adsorbent prepared in Example I was tested as follows.
[0105] A 1 in quartz tube reactor was charged with the sorbent of Example I in the amounts indicated below. The solid nickel sorbent was placed on a frit in the middle of the reactor and reduced with hydrogen at a total pressure of 15 psia and a partial hydrogen pressure of 15 psi for .03 hr. A gaseous cracked gasoline containing about 340 ppm sulfur (parts by weight of sulfur compounds based on the weight of the gaseous cracked gasoline) and about 95 ppm sulfur based on the weight of the gaseous cracked gasoline was pumped upward through the reactor. % by weight thiophenes (eg, alkylbenzothiophenes, alkylthiophenes, benzothiophenes, and thiophenes). The flow rate is 13.4ml / hr. Produces sulfurized solid sorbent and desulfurized gaseous cracked gasoline. In Test 1, hydrogen was added at a partial pressure of 13.2 psi to the cracked gasoline feed, resulting...
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