Catalystic reforming method for hydrocarbons
A technology for catalytic reforming and hydrocarbons, which is used in the catalytic reforming of naphtha, etc., and can solve the problems of lower octane number of reformed products, low yield of aromatics, and decreased catalyst acidity.
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example 1
[0026] A stainless steel reactor is loaded with a bimetallic reforming catalyst, and the catalyst carrier is alumina, which contains 0.26% by mass of platinum, 0.28% by mass of rhenium, and 1.0% by mass of chlorine (both based on alumina). The reaction apparatus was purged first with nitrogen and then with hydrogen. Then, using n-heptane as a raw material, n-heptane and hydrogen are fed into the reactor, and the water content of the n-heptane is 1.0 ppm. At 500°C, 0.35MPa, n-heptane feed liquid hourly space velocity 3.0 -1 , Hydrogen / hydrocarbon volume ratio of 1000:1 under the conditions of the reaction. After the start of the reaction, phosphorus trichloride was added to the n-heptane feed every 24 hours, with each addition taking 12 hours. The addition amount of phosphorus trichloride is shown in Table 1, and reaction result is shown in Fig. 1, Fig. 2.
example 2
[0031] Carry out reforming reaction with n-heptane as raw material by the method for example 1, difference is that phosphorus trichloride is added continuously when n-heptane feeds, and reaction result is shown in Fig. 3, Fig. 4.
example 3
[0038] Get the catalyst after the reaction of Example 2, Comparative Example 2 and Comparative Example 3, measure its carbon deposition amount, and take the catalyst carbon deposition amount without adding any substance in the raw material as a benchmark, calculate the reaction after adding different substances in the above three raw materials The amount of coke deposited on the catalyst is reduced, as shown in Figure 5. As can be seen from Figure 5, the reduction rate of the amount of carbon deposition of the catalyst D obtained by the method of the present invention is close to 30%, that is to say, the amount of carbon deposition of the catalyst has decreased by about 30%, indicating that the method of the present invention has a higher resistance to carbon deposition performance.
[0039] Table 1
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