Residual oil hydrotreatment method for prolonging device operating cycle
A technology for residual oil hydrogenation and treatment method, which is applied in the fields of hydroprocessing process, hydrocarbon oil treatment, hydrocarbon oil cracking, etc. Problems such as pressure drop and reduction of the loading amount of the main catalyst can be achieved to increase the effect of backwashing, increase the porosity of the bed, and save the amount of consumption
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Embodiment 1-3
[0047] The test was carried out on the continuous high-pressure fixed-bed hydrogenation pilot plant imported from XYTEL Company of the United States. The device adopts three reactors connected in series, the raw material oil is from top to bottom, and a filtering device is added behind each reactor.
[0048] The catalyst used in the test is a full range of residual oil hydrotreating catalysts developed by Fushun Petrochemical Research Institute, including four types of catalysts with four different functions: desulfurization (HDS), demetallization (HDM), denitrogenation (HDN) and protective agent. The main physicochemical properties of the catalysts are listed in Table 1. The loading conditions of the catalysts in each reactor are as follows: one side fills CEN-2, CEN4, FZC-16, CEN-5, CEN6 from top to bottom, and the filling ratio (volume ratio) is: 1:1.5:2.2:2.4:13, The second reactor is filled with ZTS01 and ZTS02 from top to bottom, the filling ratio (volume ratio) is 7.5:...
Embodiment 4
[0069] Embodiment 4 adopts the same test device, catalyst loading scheme, standard operating conditions, and test feedstock oil as in Example 1 to carry out the test, and the device obtains the hydrogenation-generated oil value of 3000 hours of stable operation of the feedstock oil in Table 2 under standard operating conditions. For the impurity removal data and the pressure drop values of each reverse, under the same conditions as the standard operating conditions, the reaction pressure and the hydrogen-to-oil ratio, the temperature of each reverse was reduced to 320°C at 10°C / h (space velocity 0.2), and after stabilization, the temperature was reduced to 0.24h -1 The volume space velocity is reversely introduced into the device containing vulcanizing agent (CS 2 ) heavy diesel oil (Saudi Arabia's third line), and the diesel fraction generated by itself is recycled back to the reactor inlet as supplementary distillate oil, and the amount of circulating oil is 20% of the feed...
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